This guide provides drug development researchers and scientists with a comprehensive framework for selecting solvents to minimize Process Mass Intensity (PMI), a key green chemistry metric.
This guide provides drug development researchers and scientists with a comprehensive framework for selecting solvents to minimize Process Mass Intensity (PMI), a key green chemistry metric. It covers the foundational principles of green chemistry and PMI, explores practical methodologies and industry-standard tools for solvent evaluation, offers strategies for troubleshooting and optimizing processes, and outlines validation and comparative analysis techniques. By integrating these strategies, professionals can design more efficient, cost-effective, and environmentally sustainable pharmaceutical manufacturing processes.
Process Mass Intensity (PMI) is a key green chemistry metric used to benchmark the efficiency and environmental performance of chemical processes, particularly in the pharmaceutical industry. It provides a comprehensive measure of the total mass of materials used to produce a unit mass of a final product. Unlike simple yield calculations, PMI accounts for all inputs, including solvents, reagents, catalysts, and process chemicals, offering a more holistic view of resource efficiency and environmental impact. The adoption of PMI has helped the pharmaceutical industry focus attention on the main drivers of process inefficiency, cost, and environment, safety, and health impact [1].
PMI represents a significant advancement over traditional efficiency metrics because it captures the full environmental footprint of a chemical process. The pharmaceutical sector has embraced PMI as a tool to drive more sustainable processes, with the first PMI benchmarking exercise conducted in 2008 and regularly continued since then [1]. This metric is especially valuable in active pharmaceutical ingredient (API) synthesis, where complex multi-step processes often generate substantial waste relative to the final product.
The standard PMI calculation is defined as the total mass of all materials input into a process divided by the mass of the final product, typically expressed in kilograms of input per kilogram of product. The formula is:
PMI = Total Mass of Inputs (kg) / Mass of Product (kg)
This calculation encompasses all substances introduced during the synthesis, including reactants, solvents, catalysts, acids, bases, and work-up chemicals. Water may be included in the total mass, though accounting practices may vary between organizations. The resulting dimensionless number represents the efficiency of the process â a lower PMI indicates a more efficient and environmentally favorable process.
For a typical chemical reaction, the PMI calculation would account for:
The following table illustrates a sample PMI calculation for a hypothetical API synthesis:
Table 1: Example PMI Calculation for a Representative API Synthesis Step
| Input Material | Quantity Used (kg) | Function in Process |
|---|---|---|
| Starting Material A | 1.5 | Reactant |
| Reagent B | 0.8 | Reagent |
| Solvent C | 12.0 | Reaction solvent |
| Catalyst D | 0.1 | Catalyst |
| Aqueous HCl | 5.0 | Acid work-up |
| Total Input Mass | 19.4 kg | |
| API Product Mass | 1.7 kg | |
| PMI | 11.4 |
For complex multi-step syntheses, especially convergent routes where multiple branches synthesize different fragments later combined into the final API, the original PMI calculator was enhanced to create the Convergent PMI Calculator [1]. This tool uses the same fundamental calculations but allows for multiple branches in single-step or convergent synthesis, providing accurate PMI values for complex synthetic routes that reflect modern pharmaceutical manufacturing.
PMI serves as a crucial strategic tool for process chemists and engineers in pharmaceutical companies who are tasked with identifying efficient routes and processes to new chemical entities [1]. The efficiency of any molecular synthesis combines both the synthetic strategy and process design optimization. PMI benchmarking has enabled significant advances in green chemistry and engineering by providing a standardized metric to compare processes and track improvements over time.
The continuing development of PMI tools represents a substantial contribution to green chemistry and engineering. The ability to benchmark and predict process mass intensity for complex organic molecules enables scientists and engineers in both academia and industry to develop better, more cost-effective, and more sustainable processes [1].
Solvents typically constitute the largest portion of mass in pharmaceutical API synthesis, accounting for an average of 54% of chemicals and materials used in technological processes [2]. Consequently, solvent selection is paramount to PMI reduction efforts. The relationship between solvent choice and PMI is multifaceted:
Table 2: Solvent Impact on PMI and Environmental Performance
| Factor | Impact on PMI | Green Chemistry Considerations |
|---|---|---|
| Solvent Mass | Direct contribution to total input mass | Reduction directly lowers PMI |
| Recyclability | Affects net material consumption | Closed-loop systems minimize waste |
| Green Solvent Alternatives | May enable mass reduction | Bio-based, water-based, supercritical fluids, and deep eutectic solvents offer environmentally friendly options [3] |
| Process Design | Influences overall material efficiency | Integration of reaction and separation steps |
The pharmaceutical sector is increasingly using green solvents as environmentally friendly substitutes for conventional solvents [3]. These include bio-based solvents (dimethyl carbonate, limonene, ethyl lactate), water-based solvents, supercritical fluids (like COâ), and deep eutectic solvents (DES). These alternatives typically offer lower toxicity, biodegradable properties, and reduced release of volatile organic compounds, contributing to improved PMI profiles.
Recent advances have integrated predictive analytics with historical data from large-scale syntheses to enable better decision-making during ideation and route design. The PMI prediction app developed by Bristol Myers Squibb in collaboration with academic partners utilizes predictive analytics and historical data to help scientists select the most efficient synthetic options prior to laboratory development [4]. This approach enables a quantitative method for predicting potential efficiencies centered around PMI of proposed synthetic routes before experimental evaluation.
When combined with machine learning Bayesian optimization (EDBO/EDBO+) to explore chemical space and identify more sustainable reaction conditions with fewer experiments, these tools significantly accelerate the advancement of "greener-by-design" outcomes [4]. For example, in one real clinical candidate example, a process that yielded 70% yield and 91% enantiomeric excess through traditional one-factor-at-a-time optimization requiring 500 experiments was surpassed by the EDBO+ platform, which achieved 80% yield and 91% enantiomeric excess in only 24 experiments [4].
Advanced solvent screening protocols complement PMI optimization by identifying environmentally friendly and cost-effective solvent options. These protocols often combine computational methods like COSMO-RS (Conductor-like Screening Model for Real Solvents) with machine learning to explore extended solvent spaces efficiently [5]. The integration of these approaches enables researchers to:
This methodology is particularly valuable given that extensive experimental screening, while most reliable, is limited by the time, effort, and costs required [5]. Machine learning approaches offer a viable alternative for exploring solvent space when supported by reliable predictive models.
Objective: To determine the Process Mass Intensity for a chemical reaction at laboratory scale.
Materials and Equipment:
Procedure:
Notes:
Objective: To identify solvent systems that minimize PMI while maintaining reaction performance.
Materials:
Procedure:
Analysis:
Diagram 1: PMI-Driven Process Development Workflow
Diagram 2: PMI Calculation Methodology
Table 3: Essential Research Tools for PMI-Driven Process Development
| Tool/Reagent | Function in PMI Optimization | Application Notes |
|---|---|---|
| ACS GCI PMI Calculator | Standardized PMI calculation for linear and convergent syntheses | Web-based tool available through ACS Green Chemistry Institute Pharmaceutical Roundtable [1] |
| Convergent PMI Calculator | PMI calculation for complex multi-branch syntheses | Handles convergent routes common in API manufacturing [1] |
| Bio-based Solvents (e.g., ethyl lactate, limonene) | Lower environmental impact solvent options | Low toxicity, biodegradable properties, reduced VOC release [3] |
| Deep Eutectic Solvents (DES) | Tunable, environmentally benign solvent systems | Created by combining hydrogen bond donors and acceptors; used in synthesis and extraction [3] |
| Supercritical Fluids (e.g., COâ) | Alternative solvent for extraction and reactions | Selective and efficient bioactive compound extraction with minimal environmental damage [3] |
| COSMO-RS Computational Screening | Prediction of solubility and solvent performance | Enables rational solvent selection prior to experimental work [5] |
| Bayesian Optimization Platforms (e.g., EDBO/EDBO+) | Efficient experimental optimization with fewer experiments | Machine learning approach to identify optimal conditions rapidly [4] |
| Water-based Solvent Systems | Non-flammable, non-toxic alternatives | Aqueous solutions of acids, bases, or alcohols as reaction media [3] |
Within pharmaceutical research and development, solvent use constitutes the largest mass input in synthetic processes, directly influencing process mass intensity (PMI) and environmental impact [6]. The 12 Principles of Green Chemistry provide a foundational framework for redesigning chemical processes to minimize their environmental footprint [7] [8]. This article delineates specific protocols and application notes for applying these principles systematically to solvent selection, supporting the broader objective of developing comprehensive solvent guides for lower PMI in active pharmaceutical ingredient (API) synthesis. By integrating quantitative green chemistry metrics with practical experimental methodologies, researchers can make informed decisions that significantly reduce waste, hazard, and resource consumption throughout the drug development lifecycle.
Evaluating solvent greenness requires robust, quantitative metrics that enable objective comparison between alternatives. Key mass-based and environmental metrics provide critical data for informed decision-making.
Table 1: Core Green Chemistry Metrics for Solvent Evaluation
| Metric | Calculation | Interpretation | Application Context |
|---|---|---|---|
| Process Mass Intensity (PMI) | Total mass of inputs (kg) / Mass of product (kg) [6] | Lower values indicate higher efficiency; Ideal PMI = 1 | Primary metric for overall process efficiency; industry benchmarking |
| E-Factor | Total waste (kg) / Product (kg) [9] | Lower values preferable; Pharmaceutical industry often 25-100+ [9] | Waste production assessment; PMI = E-Factor + 1 [9] |
| Carbon Footprint | kg COâ produced per kg product [10] | Quantifies climate change impact | Lifecycle assessment from raw material to disposal [10] |
| Cumulative Energy Demand (CED) | Energy for production + Use - Recycling/Incineration credits [11] | Lower values preferable; Identifies optimal end-of-life strategy | Energy impact assessment; Informs recycling vs. incineration decisions [11] |
Several structured approaches facilitate solvent evaluation and substitution based on environmental, health, and safety (EHS) profiles:
Purpose: To systematically identify and evaluate greener solvent alternatives for a specific chemical reaction or unit operation.
Materials:
Methodology:
Data Analysis: Compile results into a comparative assessment matrix scoring each solvent across technical performance, EHS criteria, and lifecycle impacts to identify the optimal balance of properties.
Purpose: To minimize PMI through solvent reduction strategies and recycling implementation.
Materials:
Methodology:
Data Analysis: Track PMI improvement throughout optimization stages and calculate net environmental benefit using the ETH Zurich CED methodology to confirm the optimal end-of-life strategy [11].
The following diagram illustrates the systematic decision pathway for applying green chemistry principles to solvent selection:
Table 2: Essential Materials for Green Solvent Implementation
| Category | Specific Examples | Function | Green Chemistry Principle Addressed |
|---|---|---|---|
| Green Solvent Candidates | 2-MeTHF, Cyrene, dimethyl isosorbide [11] | Bio-based solvent alternatives | Principle 5 (Safer Solvents), Principle 7 (Renewable Feedstocks) |
| Assessment Tools | ACS GCI Solvent Selection Tool, Rowan University Solvent Index [12] [11] | Quantitative solvent evaluation | Principle 2 (Atom Economy), Principle 12 (Accident Prevention) |
| Analytical Instrumentation | GC-MS, HPLC, in-line PAT tools [9] | Solvent purity analysis, reaction monitoring | Principle 11 (Real-Time Analysis) |
| Catalytic Systems | Immobilized enzymes, heterogeneous catalysts [10] [6] | Enable alternative solvent use, improve selectivity | Principle 9 (Catalysis) |
The 12 Principles of Green Chemistry provide a robust, actionable framework for transforming solvent selection practices in pharmaceutical research and development. By integrating quantitative metrics like PMI and E-Factor with systematic assessment protocols and advanced solvent selection tools, researchers can significantly reduce the environmental impact of synthetic processes while maintaining efficiency and efficacy. The experimental protocols and decision frameworks presented herein offer practical pathways for implementing these principles, supporting the broader objective of developing sustainable solvent selection guides for lower PMI in API synthesis. As green chemistry continues to evolve, the integration of innovative solvent systems, biocatalysis in non-conventional media [10], and predictive analytics for greener-by-design synthesis [4] will further advance the sustainability of pharmaceutical manufacturing.
In the pursuit of more sustainable pharmaceutical manufacturing, solvent use presents a critical challenge. Solvents typically constitute the largest mass input in synthetic processes, making them the primary contributor to process mass intensity (PMI) and a significant source of manufacturing waste [6]. The pharmaceutical industry is notably resource-intensive, accounting for approximately 5% of global greenhouse gas (GHG) emissions annually, with Active Pharmaceutical Ingredient (API) manufacturing alone responsible for about 25% of emissions from pharmaceutical companies [14]. This environmental burden is compounded by economic factors; the pharmaceutical solvent market is projected to reach $5.61 billion by 2032, escalating both production costs and waste disposal challenges [14]. Within this context, addressing solvent waste through recovery, recycling, and informed selection becomes not merely an operational consideration but a fundamental requirement for sustainable drug development.
The following table summarizes key quantitative data highlighting the dominant role of solvents in pharmaceutical manufacturing waste:
Table 1: Environmental and Economic Impact of Pharmaceutical Solvents
| Metric | Impact Value | Context & Reference |
|---|---|---|
| Global Pharma GHG Emissions | 5% of total global emissions | Annual contribution [14] |
| API Manufacturing Share | 25% of pharma company emissions | From overall pharma carbon footprint [14] |
| Current Solvent Recycling Rate | ~35% | Majority of spent solvents still incinerated [14] |
| COâe from Solvent Incineration | 2-4 kg COâe/kg solvent | End-of-life emissions [14] |
| COâe from Solvent Recycling | 0.1-0.5 kg COâe/kg solvent | Through distillation; significantly lower than incineration [14] |
| Potential Cost Savings | Up to 90% | Reduction in new solvent purchase and disposal costs [14] |
Pharmaceutical processes utilize various solvents, many classified as hazardous waste under regulatory frameworks like the Resource Conservation and Recovery Act (RCRA). The table below lists common solvents encountered in pharmaceutical manufacturing, particularly those listed as "F-listed" wastes from solvent procedures [14]:
Table 2: Common Solvents in Pharmaceutical Processes and Hazardous Waste Categories
| Solvent Name | Typical Applications | Hazardous Waste Category |
|---|---|---|
| Acetone | Extraction, cleaning | F-listed spent solvent [14] |
| Methanol | Synthesis, crystallization | F-listed spent solvent [14] |
| Ethyl Acetate | Extraction, chromatography | F-listed spent solvent [14] |
| Toluene | Reaction medium, azeotropic drying | F-listed spent solvent [14] |
| Xylene | Histology, synthesis | F-listed spent solvent [14] |
| n-Butyl Alcohol | Synthesis, extraction | F-listed spent solvent [14] |
| Cyclohexanone | Solvent for polymers, resins | F-listed spent solvent [14] |
Crystallization is a critical purification step in API manufacturing. Selecting an appropriate solvent is paramount for yield and purity. The following protocol provides a systematic method for testing single solvents for crystallization [15].
Application Note: This method is ideal for small-scale R&D during process development to identify viable crystallization solvents before scaling up.
Step 1: Initial Solubility Screening
Step 2: Heating and Dissolution
Step 3: Cooling and Crystallization
Distillation is the most common method for industrial-scale solvent recovery, enabling the reuse of spent solvents, which reduces PMI and waste disposal costs [16] [17].
Application Note: This protocol outlines the general stages for implementing an on-site distillation recovery system for single-solvent or multi-component solvent waste streams.
Step 1: Collection and Segregation
Step 2: Separation via Distillation
Step 3: Purification
Step 4: Reuse/Recycling
The following workflow diagram visualizes the decision path for solvent recovery and recycling:
The following table details key tools and resources essential for scientists aiming to optimize solvent use and reduce PMI.
Table 3: Essential Tools for Green Solvent Selection and Process Analysis
| Tool / Resource | Function & Application |
|---|---|
| ACS GCIPR Solvent Selection Guide | An interactive tool based on Principal Component Analysis (PCA) of 70+ physical properties of 272 solvents. It aids in selecting or replacing solvents based on polarity, H-bonding, EHS, and LCA profiles [6] [12]. |
| Process Mass Intensity (PMI) Calculator | A key green metric, PMI is calculated as the total mass of inputs (kg) per mass of product (kg). This calculator helps track and benchmark the resource efficiency of synthetic routes [6]. |
| PMI Prediction Tool | Predicts the mass efficiency of proposed synthetic routes using a dataset of nearly 2,000 reactions, allowing virtual screening of different routes for efficiency during R&D [6]. |
| On-Site Solvent Recycler (Distillation Unit) | A system designed to recover and purify spent solvents directly at the facility, drastically reducing new solvent purchases and hazardous waste generation [16] [14]. |
| Continuous Distillation Laboratory | Provides small-scale testing (e.g., using modular glass equipment) to de-risk and optimize solvent recovery processes before costly full-scale implementation [17]. |
| Brevianamide M | Brevianamide M, MF:C18H15N3O3, MW:321.3 g/mol |
| RdRP-IN-7 | RdRP-IN-7, MF:C26H45N7O3Si2, MW:559.9 g/mol |
The dominance of solvents in pharmaceutical manufacturing waste is an inescapable reality, but it also presents a significant opportunity. By understanding the quantitative impact detailed in these application notes, research scientists and drug development professionals can take decisive action. Integrating robust experimental protocols for solvent selection, implementing on-site recovery technologies like distillation, and leveraging modern tools for solvent substitution and PMI analysis form a comprehensive strategy. This multi-faceted approach directly addresses the core thesis that a strategic solvent selection guide is fundamental to lower PMI research, ultimately leading to more sustainable, cost-effective, and environmentally responsible pharmaceutical manufacturing.
Within pharmaceutical development and broader chemical research, solvents often constitute the largest mass input in a synthetic process. Their selection is therefore critical for developing sustainable processes with lower Process Mass Intensity (PMI). A rigorous assessment based on Environmental, Health, and Safety (EHS) criteria provides a foundational strategy for reducing the environmental footprint of chemical manufacturing [18] [11]. This document outlines the core EHS principles, standardized assessment protocols, and available tools to guide researchers in selecting greener solvents, directly contributing to the goals of lower PMI research.
The push for greener solvents is further driven by evolving regulatory landscapes. For instance, the U.S. Environmental Protection Agency (EPA) has implemented new rules restricting many uses of methylene chloride due to health risks such as neurotoxicity and cancer [19]. Similarly, the European REACH regulation places restrictions on solvents like toluene, chloroform, and DCM [11]. These regulatory actions underscore the necessity of proactively integrating EHS criteria into solvent selection to ensure both worker safety and long-term process viability.
A comprehensive EHS assessment evaluates a solvent's impact across three interconnected domains. The guiding principle is that a truly green solvent must perform favorably in all three areas, not just one or two [11].
This category assesses the solvent's impact on ecosystems and the environment throughout its life cycle.
This category focuses on the direct effects of solvent exposure on human health.
This category addresses the physical hazards associated with handling and storing the solvent.
Table 1: Key EHS Criteria and Their Assessment Parameters
| EHS Domain | Criteria | Key Assessment Parameters / Standards |
|---|---|---|
| Environmental | Biodegradability | Inherent/readily biodegradable; OECD test guidelines |
| Aquatic Toxicity | LC50 (fish), EC50 (daphnia), GHS categories (H400, H410, H412) [21] | |
| Ozone Depletion | Ozone Depletion Potential (ODP); regulated under Montreal Protocol [11] | |
| Volatility | Boiling point, VOC status | |
| Health | Acute Toxicity | LD50 (oral, dermal), GHS classification [18] [21] |
| Carcinogenicity | IARC classification; GHS H350, H351 | |
| Reproductive Toxicity | GHS H360, H361 | |
| Organ Toxicity | Specific target organ toxicity (STOT) | |
| Safety | Flammability | Flash point, auto-ignition temperature; GHS flammability categories [21] |
| Reactivity/Stability | Peroxide formation, energy of decomposition |
Several organizations have developed solvent selection guides that synthesize EHS data into user-friendly formats. These tools are invaluable for making rapid, informed comparisons.
The CHEM21 guide is a widely recognized tool developed by a European public-private partnership, including pharmaceutical companies and academic institutions. It scores solvents based on Safety, Health, and Environmental impacts, aligning with the Globally Harmonized System (GHS) of Classification and Labelling [21]. It categorizes solvents as "Recommended," "Problematic," or "Hazardous," providing a clear, actionable ranking for chemists.
This interactive web-based tool allows for solvent selection based on a Principal Component Analysis (PCA) of 70 physical properties. It includes 272 solvents and provides data on health impacts, air/water impacts, life-cycle assessment, and ICH solvent classes [12]. It helps identify solvents with similar properties but potentially greener EHS profiles.
The GSK guide uses a comprehensive numerical ranking system across multiple EHS and life-cycle categories. While highly detailed, its complexity can make it challenging to trace how individual data points contribute to the final score [18]. It has, however, served as a valuable dataset for training machine learning models to predict solvent greenness [22].
Table 2: Comparison of Major Solvent Selection Guides
| Guide / Tool | Primary Scoring/Categorization Method | Key Strengths | Context in Lower PMI Research |
|---|---|---|---|
| CHEM21 | Recommended, Problematic, Hazardous | Aligns with GHS; user-friendly, clear categories | Promotes inherently safer solvents, reducing waste from controls and incidents |
| ACS GCIPR Tool | PCA mapping of physical properties | Interactive; large database (272 solvents); links properties to EHS | Identifies drop-in replacements with lower EHS impact, minimizing re-optimization |
| GSK Solvent Guide | Comprehensive numerical ranking | Very detailed assessment; incorporates LCA | Holistic view of solvent impact from production to disposal, informing total PMI |
| GEARS Metric | Quantitative scoring (e.g., 0-3 pts per parameter) [18] | Includes 10 parameters (EHS, functional, economic); transparent | Directly links solvent properties to process efficiency and waste generation |
This protocol provides a step-by-step methodology for evaluating and comparing solvents for a specific chemical process using established EHS criteria and selection guides.
1. Define Process Requirements
2. Compile EHS Data
3. Apply Solvent Selection Guides
4. Perform a Comparative Analysis and Selection
5. Life-Cycle and Waste Considerations
Diagram 1: EHS Solvent Selection Workflow. This diagram outlines the iterative process for selecting a green solvent based on EHS criteria and functional requirements.
Table 3: Essential Research Reagents and Tools for EHS-Driven Solvent Selection
| Tool / Resource Name | Function / Purpose | Relevance to EHS & Lower PMI |
|---|---|---|
| CHEM21 Selection Guide | Provides a quick, GHS-aligned classification of solvents as Recommended, Problematic, or Hazardous [21]. | Enables rapid identification of inherently safer solvents, reducing hazardous waste streams. |
| ACS GCIPR Solvent Tool | Interactive tool for mapping solvents by physical properties and viewing EHS impact categories [12]. | Identifies functionally similar, greener solvent alternatives to minimize re-optimization efforts and PMI. |
| GSK Solvent Sustainability Guide | A comprehensive numerical ranking system for solvent greenness [18] [6]. | Offers a detailed, holistic assessment of solvent sustainability, informing long-term process design. |
| REACH Dossiers / eChemPortal | Official databases for regulatory chemical data, including hazard and risk assessments [18]. | Provides authoritative, validated data for conducting rigorous EHS assessments. |
| PMI Calculator (ACS GCIPR) | Calculates the Process Mass Intensity of a synthetic route, accounting for all material inputs [6]. | Quantifies the mass efficiency of a process, directly measuring the success of green solvent selection in reducing waste. |
| GreenSolventDB | A large public database of green solvent metrics generated via machine learning predictions [22]. | Expands the universe of assessable solvents beyond traditional guides, enabling discovery of novel green options. |
Integrating a rigorous, multi-parameter EHS assessment into solvent selection is a non-negotiable practice for modern, sustainable drug development. By leveraging established frameworks like the CHEM21 guide, interactive tools from the ACS GCIPR, and emerging metrics like %Greenness [23], researchers can make informed decisions that significantly reduce Process Mass Intensity. This methodology aligns with regulatory trends, mitigates workplace hazards, and minimizes environmental impact, thereby advancing the core objectives of green chemistry and lower PMI research. The future of solvent selection will be further enhanced by data-driven approaches, including machine learning models that can predict the greenness of a vast array of solvents, accelerating the discovery and adoption of truly sustainable alternatives [22].
Cumulative Energy Demand represents the total amount of primary energy consumed throughout the complete lifecycle of a product, process, or service, accounting for all direct and indirect energy inputs from raw material extraction to end-of-life disposal [24]. In pharmaceutical research and development, CED provides a comprehensive metric to quantify the true energy burden of manufacturing processes, enabling scientists to identify hotspots for improvement in resource efficiency.
CED calculations are typically performed within the standardized framework of Life Cycle Assessment (LCA) and are expressed in megajoules (MJ) of primary energy, categorized by energy source types [25]. This methodology helps researchers move beyond simple operational energy efficiency to understand the complete energy footprint embedded in synthetic routes, which is particularly important when aiming to reduce Process Mass Intensity (PMI) in active pharmaceutical ingredient (API) manufacturing.
The Solvent Footprint encompasses the aggregated environmental, health, and safety impacts of solvents throughout their life cycle, including raw material acquisition, manufacturing, use, recycling, and treatment [26]. solvents represent the largest mass input in most synthetic pharmaceutical processes, making their footprint a critical concern for sustainable process design. Key impact categories for solvent footprint assessment include global warming potential, photochemical ozone creation, human toxicity, aquatic ecotoxicity, and resource depletion [26] [12].
Integrating CED and solvent footprint analysis provides a holistic sustainability assessment framework for pharmaceutical development teams, enabling informed solvent selection decisions that align with green chemistry principles and corporate sustainability goals while maintaining process efficiency and product quality.
Table 1: CED Impact Categories and Units [25]
| Category Name | Unit |
|---|---|
| Non-renewable, biomass | MJ |
| Non-renewable, fossil | MJ |
| Non-renewable, nuclear | MJ |
| Renewable, biomass | MJ |
| Renewable, water | MJ |
| Renewable, wind, solar, geothermal | MJ |
| Total | MJ |
| Total, non-renewable | MJ |
| Total, renewable | MJ |
Table 2: LCIA Methods for Comprehensive Solvent Footprint Assessment [27]
| Method | Developer | Key Features | Applicable Impact Categories |
|---|---|---|---|
| IPCC | Intergovernmental Panel on Climate Change | Global warming potential factors (GWP100, GWP20) | Carbon footprint, Climate change |
| ReCiPe | RIVM, Radboud University, Leiden University, Pré Consultants | Midpoint and endpoint assessment; multiple cultural perspectives | Human health, Ecosystem quality, Natural resources |
| EF v3.1 | European Commission | Standardized for Environmental Footprint studies | Multiple impact categories including toxicity, resource use |
| USEtox | UNEP/SETAC | Consensus model for toxicity assessment | Human toxicity, Freshwater ecotoxicity |
| Cumulative Energy Demand | ecoinvent | Primary energy demand assessment | Total energy resource consumption |
| Ecological Scarcity | Swiss Federal Office for the Environment | Distance-to-target method; eco-points (UBP) | Multiple aggregated impact categories |
Objective: To determine the cumulative energy demand of API synthesis routes to identify energy hotspots and guide PMI reduction strategies.
Materials and Equipment:
Procedure:
Goal and Scope Definition:
Life Cycle Inventory Compilation:
CED Calculation:
Interpretation and Hotspot Analysis:
Data Analysis: Calculate PMI (Process Mass Intensity) using the formula:
Integrate CED and PMI results to identify both mass and energy efficiency improvement opportunities.
Objective: To evaluate and compare the environmental footprint of different solvent options for specific chemical transformations to guide sustainable solvent selection.
Materials and Equipment:
Procedure:
Solvent Function Requirement Analysis:
Life Cycle Impact Assessment:
EHS Profiling:
Green Solvent Alternative Assessment:
Multi-Criteria Decision Analysis:
Validation: Confirm laboratory performance of selected green solvents through reaction optimization and process efficiency measurements. Monitor PMI reduction and document sustainability improvements.
Table 3: Essential Tools for CED and Solvent Footprint Assessment
| Tool/Resource | Function | Application Context |
|---|---|---|
| ACS GCI Solvent Selection Tool [12] | Interactive solvent selection based on PCA of physical properties and environmental data | Replacement of hazardous solvents with greener alternatives |
| Ecoinvent Database [27] | Provides life cycle inventory data for energy and materials | CED calculation and environmental footprint assessment |
| ReCiPe 2016 LCIA Method [27] | Midpoint and endpoint impact assessment with multiple cultural perspectives | Comprehensive environmental impact evaluation |
| USEtox Model [27] | Characterization of human and ecotoxicity impacts | Toxicity footprint assessment for solvent selection |
| Process Mass Intensity Calculator [6] | Determination of PMI from raw material inputs | Resource efficiency benchmarking and monitoring |
| Green Solvent Guides [6] [3] | Reference for bio-based and less hazardous solvent options | Initial screening of potential green solvent alternatives |
| Brequinar-d3 | Brequinar-d3, MF:C23H15F2NO2, MW:378.4 g/mol | Chemical Reagent |
| Flaviviruses-IN-2 | Flaviviruses-IN-2, MF:C21H20N2O3S, MW:380.5 g/mol | Chemical Reagent |
Successful integration of CED and solvent footprint analysis into pharmaceutical development requires a systematic approach that aligns with existing workflow. Development teams should establish baseline CED and PMI metrics for current processes, then set reduction targets aligned with corporate sustainability goals. The ACS GCI Pharmaceutical Roundtable solvent selection guide provides a validated starting point for identifying preferred solvents and those to be avoided or replaced [6].
For synthetic route design, researchers should prioritize chemical transformations that minimize energy-intensive processes and enable the use of green solvents. Early-stage incorporation of life cycle thinking allows for significant reduction of environmental impacts before process lock-in occurs. Regular monitoring of PMI and CED metrics throughout development provides quantitative data to track improvement and demonstrate the business case for sustainable chemistry practices.
The transition to green solvents, including bio-based alternatives like ethyl lactate and dimethyl carbonate, deep eutectic solvents, and supercritical fluids, represents a significant opportunity for reducing both CED and solvent footprint in pharmaceutical manufacturing [3]. However, technical performance, scalability, and economic viability must be carefully evaluated alongside environmental benefits to ensure practical implementation.
The American Chemical Society Green Chemistry Instituteâs Pharmaceutical Roundtable (ACS GCIPR) provides a comprehensive framework for solvent selection to advance sustainability in pharmaceutical research and development. Solvents constitute approximately 50% of the total mass of materials used to manufacture active pharmaceutical ingredients (APIs), making their judicious selection critical for reducing Process Mass Intensity (PMI) [28]. The ACS GCIPR specifically endorses the CHEM21 Solvent Selection Guide as a key resource, which classifies solvents based on safety, health, and environmental (SHE) criteria to help researchers identify problematic solvents and select preferable alternatives [29] [30] [28]. This guide is instrumental in systematically reducing the environmental footprint of chemical processes, directly contributing to lower PMI in pharmaceutical synthesis.
The CHEM21 guide employs a standardized methodology to evaluate and rank solvents, providing a clear, color-coded classification system [30]. It categorizes solvents as "recommended," "problematic," or "hazardous" based on combined safety, health, and environmental scores, enabling rapid assessment and substitution decisions [30].
The ACS GCIPR Solvent Selection Tool is an interactive platform based on Principal Component Analysis (PCA) of 70 physical properties from 272 research, process, and next-generation green solvents [12]. This tool visualizes solvents in a property space where proximity indicates similarity, facilitating the identification of alternatives with comparable chemical functionality but improved SHE profiles [12] [6]. The tool incorporates additional data on functional groups, environmental impact categories, ICH solvent classes, and plant accommodation parameters, supporting holistic solvent choices [12].
The CHEM21 guide employs a precise scoring system where SHE criteria are rated from 1-10, with higher scores indicating greater hazard [30]. The overall classification derives from the most stringent combination of these scores according to the following table:
Table 1: CHEM21 Solvent Ranking Criteria [30]
| Score Combination | Ranking by Default |
|---|---|
| One score ⥠8 | Hazardous |
| Two "red" scores (7-10) | Hazardous |
| One score = 7 | Problematic |
| Two "yellow" scores (4-6) | Problematic |
| Other combinations | Recommended |
Safety scores primarily derive from flash point (FP), with contributions from auto-ignition temperature (AIT), resistivity, and peroxide formation potential [30]:
Table 2: Safety Scoring Criteria [30]
| Basic Safety Score | Flash Point (°C) | GHS Statements |
|---|---|---|
| 1 | > 60 | -- |
| 3 | 23 to 60 | H226 |
| 4 | 22 to 0 | -- |
| 5 | -1 to -20 | -- |
| 7 | < -20 | H225 or H224 |
Health scores incorporate the most stringent GHS H3xx statements with adjustments for boiling point, while environment scores consider both volatility (boiling point) and GHS H4xx statements [30].
Table 3: CHEM21 Solvent Classifications and Properties (Selected Examples) [30]
| Family | Solvent | BP (°C) | FP (°C) | Safety Score | Health Score | Env. Score | Recommended |
|---|---|---|---|---|---|---|---|
| Alcohols | MeOH | 65 | 11 | 4 | 7 | 5 | Yes* |
| Alcohols | EtOH | 78 | 13 | 4 | 3 | 3 | Yes |
| Alcohols | n-BuOH | 118 | 29 | 3 | 4 | 3 | Yes |
| Ketones | Acetone | 56 | -18 | 5 | 3 | 5 | Yes* |
| Ketones | MEK | 80 | -6 | 5 | 3 | 3 | Yes |
| Esters | EtOAc | 77 | -4 | 5 | 3 | 3 | Yes |
| Esters | n-PrOAc | 102 | 14 | 4 | 2 | 3 | Yes |
| Water | Water | 100 | N/A | 1 | 1 | 1 | Yes |
*After discussion, despite "problematic" default ranking
Purpose: To systematically identify and evaluate solvents for a specific chemical reaction to maximize efficiency while minimizing environmental impact and PMI.
Materials and Equipment:
Procedure:
Initial Solvent Identification: Using the ACS GCIPR Interactive Solvent Tool, identify a preliminary set of solvents with physical properties similar to traditional options but improved SHE profiles [12] [6].
Hazard Assessment: Screen identified solvents against the CHEM21 guide, prioritizing those classified as "recommended" [30]. Calculate SHE scores for any solvents not in the guide using the published methodology [30].
Experimental Validation:
PMI Calculation: For promising solvents, calculate Process Mass Intensity using the formula:
PMI = Total mass in process (kg) / Mass of product (kg) [6]
Include all solvent masses used in reaction, workup, and purification.
Final Selection: Choose the solvent that balances reaction performance with SHE considerations and lowest PMI.
Purpose: To replace a hazardous or problematic solvent with a safer alternative between process steps while maintaining API stability and purity.
Materials and Equipment:
Procedure:
Phase Equilibrium Analysis: Confirm favorable vapor-liquid equilibrium (VLE) behavior between original and swap solvents [32].
Solubility Verification: Determine API solubility in pure swap solvent and mixtures with original solvent to prevent precipitation during exchange [32].
Swap Process Execution:
Option A: Put-Take Procedure:
Option B: Constant Volume Procedure:
Process Verification: Monitor original solvent concentration throughout process. Confirm API stability and final product quality meets specifications.
Table 4: Key Resources for Solvent Selection and PMI Reduction
| Resource | Function | Application in PMI Reduction |
|---|---|---|
| ACS GCIPR Solvent Selection Tool | Interactive PCA-based solvent mapping | Identifies alternatives with similar properties but lower environmental impact [12] [6] |
| CHEM21 Selection Guide | Safety, Health, Environment solvent ranking | Systematically avoids hazardous solvents, reducing waste handling [30] [28] |
| PMI Prediction Calculator | Predicts mass efficiency of synthetic routes | Benchmarks and forecasts PMI during route scouting [6] [28] |
| Process Mass Intensity Calculator | Quantifies total mass input per product mass | Measures actual PMI for process optimization [28] |
| ICH Q3C Guidelines | Regulatory framework for residual solvents | Ensures compliance and patient safety [31] |
| Solvent Recovery Systems | Distillation and purification equipment | Enables solvent reuse, significantly reducing PMI [31] |
| Tanshinone Iib | Tanshinone Iib, MF:C19H18O4, MW:310.3 g/mol | Chemical Reagent |
| SelSA | SelSA, MF:C13H16N2OSe, MW:295.25 g/mol | Chemical Reagent |
The ACS GCI Pharmaceutical Roundtable's solvent selection tools provide a science-based framework for making informed solvent choices that directly contribute to reduced Process Mass Intensity in pharmaceutical research and manufacturing. By systematically applying the CHEM21 Selection Guide and Interactive Solvent Tool, researchers can identify safer, more sustainable solvent alternatives while maintaining or improving reaction performance. The experimental protocols outlined enable practical implementation of these principles, supporting the pharmaceutical industry's transition toward greener manufacturing processes with lower environmental impact and improved sustainability metrics.
The selection of solvents is a pivotal component in the design of sustainable chemical processes, directly influencing the Process Mass Intensity (PMI), a key metric endorsed by the ACS Green Chemistry Institute Pharmaceutical Roundtable (ACS GCI PR) for benchmarking process efficiency and environmental impact [33]. PMI, defined as the total mass of materials used in a process divided by the mass of the product, provides a comprehensive measure of resource efficiency, with lower values indicating greener processes [33]. Within the pharmaceutical industry, solvents can constitute up to 50% of the materials used in the manufacturing of active pharmaceutical ingredients (APIs), making their rational selection a primary lever for improving sustainability [28].
This guide provides researchers and drug development professionals with practical application notes and protocols for integrating bio-based and green solvents, such as ethyl lactate and dimethyl carbonate, into their workflows. By transitioning from hazardous conventional solvents to safer, renewable alternatives, scientists can significantly reduce the environmental footprint of their syntheses and extractions while maintaining, and often enhancing, performance. The subsequent sections detail the properties of prominent green solvents, outline a practical framework for solvent selection, and provide experimentally validated protocols to facilitate immediate adoption.
A new generation of solvents derived from renewable resources or possessing superior environmental, health, and safety (EHS) profiles is now available. The table below summarizes the key properties and applications of several well-established and emerging green solvents.
Table 1: Properties and Applications of Select Green Solvents
| Solvent Name | Source/Basis of 'Greenness' | Key Properties | Example Applications | PMI & Sustainability Considerations |
|---|---|---|---|---|
| Ethyl Lactate [34] [35] | Bio-based, derived from lactic acid. | Biodegradable, low toxicity, high boiling point. | Reaction medium, extraction solvent for natural products. | Reduces waste (lower E-factor); renewable feedstock. |
| Dimethyl Carbonate (DMC) [36] [37] | Eco-friendly synthetic production. | Low toxicity, biodegradable, versatile reactivity (methylating agent). | Polycarbonate synthesis, battery electrolytes, solvent for pesticide residue analysis. | Non-halogenated, safer alternative to phosgene and methyl halides. |
| Natural Deep Eutectic Solvents (NaDES) [38] | Composed of natural primary metabolites (e.g., choline chloride, sugars). | Tunable properties, low volatility, high solubilizing power for a wide range of compounds. | Pharmaceutical synthesis, extraction, formulation, and as active ingredients (TheDES). | Biocompatible, can be prepared from abundant, renewable materials with low energy input. |
Integrating green solvents into research and development requires a systematic approach that balances sustainability with technical performance. The following workflow provides a step-by-step guide for this selection process, specifically aligned with the goal of reducing PMI.
Figure 1: A workflow for selecting green solvents to reduce Process Mass Intensity (PMI).
Consult Established Selection Guides: Begin with industry-standard tools like the ACS GCI Solvent Selection Tool and the CHEM21 Solvent Selection Guide [28]. These guides rate solvents based on comprehensive health, safety, and environmental (HSE) criteria, providing a validated starting point for identifying greener alternatives.
Assess EHS and PMI Impact: Evaluate the full lifecycle impact of candidate solvents. Use simple green metrics like Process Mass Intensity (PMI) to quantify material efficiency. The ACS GCI PR provides a PMI calculator to facilitate this evaluation [28] [33]. Lower PMI directly correlates with reduced waste and lower environmental impact.
Evaluate Technical Performance: Screen solvents for technical suitability. Use tools like the Hansen Solubility Parameters to predict solvation behavior [22]. For reaction media, confirm the solvent's inertness or desired reactivity (e.g., DMC as a methylating agent) [36].
Lab-Scale Experimental Screening: Conduct small-scale experiments to validate the performance of the top candidate solvents. Key performance indicators (KPIs) include reaction yield, product purity, extraction efficiency, and ease of product isolation.
Process Optimization: Once a promising solvent is identified, optimize the entire process (e.g., catalyst loading, temperature, work-up procedure) to minimize the total mass of all inputs, thereby achieving the lowest possible PMI [33].
Scale-Up Validation: Validate the optimized process at pilot or manufacturing scale, confirming that the environmental and economic benefits are realized at the operational level.
This protocol outlines a method for extracting pesticide residues from apple samples, using dimethyl carbonate (DMC) as a sustainable alternative to traditional solvents like acetonitrile [37].
Table 2: Research Reagent Solutions for SFE with DMC
| Item | Function/Description | Green Rationale |
|---|---|---|
| Dimethyl Carbonate (DMC) | Organic co-solvent to modify polarity of supercritical COâ. | Low toxicity, biodegradable; replaces hazardous acetonitrile [37]. |
| Supercritical COâ | Primary extraction fluid. | Non-toxic, non-flammable, and readily recyclable. |
| Apple Sample | Matrix for pesticide residue analysis. | N/A |
Experimental Workflow:
Figure 2: Workflow for supercritical fluid extraction using DMC.
Key Findings: This method achieved an average extraction yield of 85% for a panel of 64 pesticides, demonstrating performance comparable to or better than acetonitrile. A significant additional benefit was the production of cleaner extracts, reducing co-extraction of matrix components and simplifying subsequent analysis [37].
NaDES, composed of natural compounds like choline chloride and sugars, are versatile solvents for synthesis, extraction, and formulation [38].
Experimental Workflow for a General NaDES-Mediated Synthesis:
Figure 3: General workflow for running a chemical reaction in a NaDES.
Table 3: Key Research Tools for Green Solvent Implementation
| Tool Name | Developer | Function | Access |
|---|---|---|---|
| Solvent Selection Guide [28] | ACS GCI Pharmaceutical Roundtable (CHEM21) | Rates solvents based on health, safety, and environmental (HSE) criteria. | Publicly available online. |
| PMI Calculator [28] | ACS GCI Pharmaceutical Roundtable | Calculates Process Mass Intensity to benchmark and quantify process efficiency. | Publicly available online. |
| Machine Learning for Green Solvents [22] | Academic Research | Predicts solvent "greenness" and identifies substitutes from a large database (>10,000 solvents). | Emerging technology; some databases like GreenSolventDB are becoming public. |
| GreenSolventDB [22] | Academic Research (via ML) | Large database of green solvent metrics, aiding in the discovery of novel alternatives. | Publicly available database. |
The strategic adoption of bio-based and green solvents is a critical and achievable step toward more sustainable research and development in the chemical and pharmaceutical industries. By leveraging the practical frameworks, detailed protocols, and innovative tools outlined in this guideâfrom established solvents like ethyl lactate and dimethyl carbonate to emerging platforms like NaDESâscientists can make informed decisions that significantly reduce the Process Mass Intensity of their work. This transition not only aligns with the principles of green chemistry but also drives economic efficiency and fosters scientific innovation, ultimately contributing to a more sustainable future for chemical manufacturing.
Current environmental and health concerns are compelling a reassessment of the pharmaceutical industry, with the objective of minimising the environmental impact of drug production processes [38]. Identifying strategies that address multiple aspects of the production chain is therefore of significant interest. Within the context of developing a solvent selection guide for lower Process Mass Intensity (PMI), Natural Deep Eutectic Solvents (NaDES) present a promising solution. Composed of various biosourced metabolites, NaDES offer significant economic, health, and environmental benefits [39]. Their remarkable ability to interact with target compounds through non-covalent bonds enhances their versatility, allowing them to function as solvents, excipients, cofactors, catalysts, solubilisation promoters, stabilisers, and absorption agents [39] [38]. This application note explores the theory, preparation, and applications of NaDES, providing detailed protocols and data to facilitate their adoption in pharmaceutical research and development, ultimately contributing to more sustainable processes with reduced PMI.
In the context of phase behaviour, the term âeutecticâ, derived from the Greek eutektos meaning âeasy meltingâ, refers to a mixture with a melting point lower than that of any other composition of the same constituents [40] [38]. A Natural Deep Eutectic Solvent (NaDES) is a mixture of two or more natural, often biosourced, compounds (e.g., sugars, organic acids, amino acids, choline derivatives) that forms a eutectic liquid with a melting point significantly lower than that of an ideal liquid mixture [40] [41] [38]. The liquidus curve of a mixture can be derived using the Schröderâvan Laar equation, and if the experimental eutectic point is at a lower temperature than the theoretical curve, the mixture is termed a Deep Eutectic Solvent (DES) [40] [38].
Key Definition: Martins et al. provide a rigorous description, defining a DES as âa mixture of two or more pure compounds where the eutectic point temperature is significantly lower than that of an ideal liquid mixture, exhibiting notable negative deviations from ideal (ÎT > 0)â [40] [38]. When a DES consists of natural compounds, it is termed a NaDES. A familiar example of a NaDES is honey, comprising glucose and fructose, which are individually solid at room temperature but form a viscous liquid when combined [40].
The fundamental principle behind NaDES formation is the interaction through hydrogen bonding between a Hydrogen Bond Acceptor (HBA), such as choline chloride or betaine, and a Hydrogen Bond Donor (HBD), such as urea, glycerol, or organic acids [41] [42]. This interaction leads to charge delocalization between the HBA and HBD, which is responsible for the marked depression in the freezing point of the mixture, inhibiting crystallization and resulting in a stable liquid at room temperature [41]. The strength and number of these hydrogen bonds directly influence the solvent's properties, including its phase-transition temperature, stability, and solvating power [41].
The following phase diagram illustrates the typical behavior of a eutectic system, showing how the mixture's melting point drops to a minimum at the specific eutectic composition.
NaDES can be prepared using several simple and green methods [41] [42]. The following protocols detail the most common and reliable techniques.
This is the most frequently used and straightforward method for NaDES preparation [41].
This method is suitable for components that can form a liquid eutectic without external heating and is advantageous for its low energy consumption [41] [42].
This is a rapid and efficient green technique that significantly reduces reaction time and energy consumption [41] [42].
Ultrasound waves create a cavitation effect that promotes interactions between HBD and HBA components, accelerating the formation of the eutectic [41] [42].
The following workflow diagram summarizes the primary preparation paths for creating a NaDES.
Owing to their versatile physicochemical properties, NaDES hold considerable promise across multiple pharmaceutical applications [40] [38].
NaDES serve as efficient, sustainable solvents for extracting active phytocompounds like saponins, flavonoids, and alkaloids from plant materials, often outperforming conventional organic solvents [42].
NaDES can enhance the solubility, stability, and bioavailability of poorly soluble Active Pharmaceutical Ingredients (APIs). They can function as solubilizing agents, co-solvents, or even form Therapeutic Deep Eutectic Solvents (TheDES) where the API itself is a component of the eutectic mixture [40] [41].
In pharmaceutical synthesis, NaDES can replace traditional organic solvents as reaction media, often leading to improved reaction rates, selectivity, and yields. They can also act as catalysts or reagents [38].
Table 1: Key Components and Reagents for NaDES Research
| Item | Function / Role | Common Examples |
|---|---|---|
| Hydrogen Bond Acceptors (HBA) | Forms the cationic part of the eutectic, interacts with HBD. | Choline Chloride, Betaine [41] [42] |
| Hydrogen Bond Donors (HBD) | Interacts with HBA via H-bonding, dictates solvent properties. | Urea, Glycerol, Lactic Acid, Citric Acid, Glucose, Fructose, Proline [41] [42] |
| Active Pharmaceutical Ingredient (API) | Component for creating Therapeutic DES (TheDES). | Ibuprofen, Lidocaine, Prilocaine [40] |
| Heating & Stirring Equipment | For synthesis via heating/stirring method. | Hot Plate with Magnetic Stirrer, Thermostated Water Bath [41] |
| Grinding Equipment | For synthesis via grinding method at room temperature. | Mortar and Pestle [41] [42] |
| Microwave Reactor | For rapid, microwave-assisted synthesis. | Controlled Microwave Synthesizer [41] [42] |
| Ultrasonic Bath | For ultrasound-assisted synthesis. | Laboratory Ultrasonic Bath [42] |
| Analytical Instruments | For characterization of NaDES and analysis of extracts/reactions. | HPLC-MS/MS [43], NMR [41], FT-IR [41], Differential Scanning Calorimetry (DSC) [40] |
| GSK3735967 | GSK3735967, MF:C25H31N7OS, MW:477.6 g/mol | Chemical Reagent |
| PSB-1114 tetrasodium | PSB-1114 tetrasodium, MF:C10H15F2N2Na4O13P3S, MW:626.18 g/mol | Chemical Reagent |
The adoption of NaDES aligns with the principles of green chemistry and can significantly contribute to reducing the Process Mass Intensity (PMI) in pharmaceutical development. PMI is defined as the total mass of materials input per mass of product output ( \text{PMI} = \frac{\text{Mass of Raw Materials Input}}{\text{Mass of Product}} ) and is a key metric endorsed by the ACS Green Chemistry Institute Pharmaceutical Roundtable for assessing process efficiency and environmental impact [6] [38].
Table 2: Green Metrics Comparison for Solvent Systems
| Metric | Definition | NaDES Advantage |
|---|---|---|
| Process Mass Intensity (PMI) | ( \frac{\text{Total Mass of Input}}{\text{Mass of Product}} ) | Lower PMI is achievable due to high solvation power, potential for solvent recycling, and integration of multiple steps (e.g., extraction and stabilization in one pot) [6] [38]. |
| Atom Economy (AE) | ( \frac{\text{Molar Mass of Product}}{\text{Molar Mass of all Reactants}} \times 100\% ) | High for NaDES synthesis itself, as components are simply mixed without byproducts [38]. |
| Reaction Mass Efficiency (RME) | AE adjusted for yield and excess reagents. | Can be improved when NaDES act as both solvent and catalyst, reducing reagent needs [38]. |
| Environmental Impact | Toxicity, biodegradability, sourcing. | NaDES are composed of natural, often low-toxicity metabolites, are biodegradable, and can be prepared from renewable resources, offering a superior profile compared to many volatile organic solvents (VOCs) [39] [41] [38]. |
Evaluating processes that utilize NaDES with these green metrics, particularly PMI, allows for a direct comparison with conventional solvent-based processes, demonstrating their potential to create more sustainable and economically viable pharmaceutical manufacturing pathways.
Process Mass Intensity (PMI) is a key metric used to benchmark the sustainability, or "greenness," of a chemical process. It is defined as the total mass of materials used to produce a unit mass of the final product [44]. This encompasses all inputs, including reactants, reagents, solvents (for reaction and purification), and catalysts. Within the pharmaceutical industry, PMI has been instrumental in driving efficiency by focusing attention on the main drivers of process inefficiency, cost, and environmental, safety, and health (ESH) impact [1] [44].
The ACS Green Chemistry Institute Pharmaceutical Roundtable (ACS GCI PR) has been a pioneer in developing and promoting PMI. The Roundtable conducted its first industry-wide PMI benchmarking exercise in 2008 and has since developed a suite of calculators to aid scientists and engineers [1] [44]. A lower PMI value indicates a more efficient and environmentally favorable process, as it signifies less waste generation and resource consumption. Given that solvents often constitute more than 80% of the materials used in pharmaceutical manufacturing, solvent selection is a critical lever for achieving a lower PMI [45].
The PMI calculation is straightforward and provides a clear, quantitative measure of process efficiency. The formula is [44]:
PMI = Total Mass of Materials Used (kg) / Mass of Product (kg)
Where the "Total Mass of Materials Used" includes the mass of all reactants, reagents, solvents, and catalysts introduced throughout the synthesis.
The significant contribution of solvents to the overall PMI makes their careful selection paramount. Reducing solvent usage directly improves PMI, leading to cost savings and a reduced environmental footprint [1]. The ACS GCI PR's Solvent Selection Tool and Solvent Selection Guide are essential resources for identifying solvents with better ESH profiles and properties that can lead to more efficient separations and work-ups, thereby lowering PMI [45].
The ACS GCI PR provides several freely available calculators to support different stages of process development.
Table: Overview of ACS GCI PR PMI Calculators
| Calculator Name | Primary Function | Best Used For |
|---|---|---|
| PMI Calculator [1] [45] | Determines the PMI value for a linear synthesis by accounting for all raw material inputs against the API output. | Simple, linear synthetic routes. |
| Convergent PMI Calculator [1] [45] | Uses the same core calculation as the standard PMI calculator but allows for multiple branches in a synthesis. | Convergent syntheses where two or more pathways are combined. |
| PMI Prediction Calculator [44] [45] | Estimates probable PMI ranges for a proposed synthetic route using historical data and predictive analytics (Monte Carlo simulations). | Early development stages, prior to laboratory work, for route scouting and comparison. |
| PMI-LCA Tool [45] | Provides a high-level estimation of both PMI and environmental life cycle impacts based on the materials used. | Understanding the broader environmental footprint of a process beyond mass efficiency. |
The following workflow diagram illustrates the strategic process of using PMI calculators for route benchmarking and solvent selection.
This protocol provides a detailed methodology for benchmarking a convergent synthetic route.
A recent example from Merck demonstrates the profound impact of PMI-driven process redesign. The team was developing a manufacturing process for a complex Antibody-Drug Conjugate (ADC) drug-linker [46].
Achieving a lower PMI requires more than just a calculator; it requires a suite of tools to inform decision-making.
Table: Key Research Reagent Solutions and Tools for PMI Reduction
| Tool/Resource | Function in PMI Reduction | Relevance to Solvent Selection |
|---|---|---|
| ACS GCI PR Solvent Selection Guide [45] | Provides EHS and environmental scores for classical and bio-derived solvents. | Critical for choosing safer, greener solvents to minimize environmental and safety impact. |
| ACS GCI PR Reagent Guides [45] | Offers comparisons of the scalability, utility, and greenness of reagents for over 25 transformations. | Enables selection of efficient reagents that may simplify work-up and purification, reducing solvent waste. |
| ACS GCI PR Biocatalysis Guide [45] | A simple guide to commonly used enzyme classes for synthetic chemists. | Biocatalytic reactions often proceed in aqueous media, reducing the need for organic solvents. |
| Acid-Base Selection Tool [45] | An interactive tool to filter and select more sustainable acids and bases based on pKa, EHS, and other parameters. | Facilitates the choice of acids/bases that are easier to remove or recycle, streamlining purification and reducing solvent use. |
| Analytical Method Greenness Score (AMGS) Calculator [45] | Provides a metric to compare the greenness of analytical separation methods (e.g., HPLC). | Helps reduce the significant environmental impact of analytical-scale solvent use in quality control. |
The ACS GCI PR's PMI calculators are indispensable tools for benchmarking and driving innovation in pharmaceutical process development. By providing a clear, quantitative metric, they allow researchers and scientists to objectively compare synthetic routes, identify inefficiencies, and focus optimization efforts where they matter most. When integrated with complementary tools for solvent, reagent, and biocatalyst selection, PMI calculation moves from a simple benchmarking exercise to a powerful framework for designing inherently sustainable, cost-effective, and greener manufacturing processes. This integrated approach is fundamental to advancing the principles of green chemistry and engineering within the pharmaceutical industry and its allied partners.
The selection of optimal solvents is a critical factor in the pharmaceutical industry, influencing process mass intensity (PMI), product yield, and environmental impact. Conventional experimental screening methods are often time-consuming, resource-intensive, and combinatorially complex. In-silico solvent optimization using computational tools has emerged as a powerful strategy to address these challenges, enabling rapid prediction of thermodynamic properties and systematic exploration of chemical space. This approach aligns with the pharmaceutical industry's goals of developing greener, more sustainable manufacturing processes by reducing material consumption and waste generation.
The Conductor-like Screening Model for Real Solvents (COSMO-RS) has established itself as a particularly valuable methodology for these applications. This quantum chemistry-based model calculates molecular interactions in liquids, allowing for the prediction of solubilities, activity coefficients, and partition coefficients without extensive experimental data. By integrating COSMO-RS with modern optimization algorithms, researchers can efficiently identify optimal pure solvents or solvent mixtures for specific applications, significantly accelerating process development while supporting green chemistry objectives through reduced PMI.
COSMO-RS combines quantum chemical calculations with statistical thermodynamics to predict the thermodynamic properties of fluids and liquid mixtures. The methodology operates through two sequential phases:
Quantum Chemical COSMO Calculations: Each molecule undergoes a quantum chemical calculation in a virtual conductor environment, where its electrons are perfectly screened. This calculation produces a polarization charge density (Ï) on the molecular surface, which is encoded in a Ï-profile â a histogram representing the polarity distribution of the molecule [47].
Statistical Thermodynamics of Surface Segments: The Ï-profiles of all components in a mixture are used to compute the pairwise interactions (electrostatic, hydrogen-bonding, and van der Waals) between surface segments. COSMO-RS treats the liquid as an ensemble of these interacting segments, applying statistical thermodynamics to derive macroscopic properties such as activity coefficients, chemical potentials, and solubilities [47] [48].
This first-principles approach allows COSMO-RS to model complex, multi-component systems with high accuracy and minimal experimental input. Its capability to handle any solvent or solute combination, including solvents from a database of over 2500 pre-computed compounds [49], makes it exceptionally well-suited for comprehensive solvent screening and optimization.
Several specialized computational tools implement the COSMO-RS theory for practical solvent optimization:
COSMO-RS/Solvent Optimization Program: This implementation, featured in the Amsterdam Modeling Suite, directly addresses the combinatorial complexity of solvent selection. It formulates the search for an optimal solvent system as a Mixed Integer Nonlinear Programming (MINLP) problem. The program includes dedicated templates for common tasks like SOLUBILITY (maximizing/minimizing solute solubility) and LLEXTRACTION (optimizing distribution ratios in liquid-liquid extraction) [50]. It can be operated via command line with flags to specify solutes, solvents, property methods (COSMO-RS or COSMO-SAC2016), and optimization objectives (-max or -min).
BESSICC (Biocatalytic Equilibrium Shift by Solvent Engineering in In-silico Cocrystals): This algorithm leverages COSMO-RS to predict the effect of solvent composition on the equilibrium position of biocatalyzed reactions. By calculating activity coefficients for all reaction species and minimizing the Gibbs free energy, BESSICC can predict reaction yields in different solvents starting from a single experimental measurement, with reported errors below 25% for specific esterification reactions [51].
In-silico Cocrystal Screening: Beyond conventional solvents, COSMO-RS is effectively applied in pharmaceutical cocrystal screening to enhance API solubility. The method evaluates the miscibility of an API and coformer in a supercooled melt phase, which correlates with their affinity in the solid-state cocrystal, allowing for rapid prioritization of coformers likely to form stable cocrystals with improved bioavailability [47] [48].
ACS GCI Pharmaceutical Roundtable Solvent Selection Tool: This interactive tool uses Principal Component Analysis (PCA) of 70 physical properties to map 272 solvents. Solvents close to each other on the PCA map possess similar properties, aiding in the rational selection or substitution of solvents based on polarity, functional group compatibility, and environmental impact categories [28] [12].
AstraZeneca's Digital LLE Tool: A recent innovation is a Python-based digital tool for designing aqueous liquid-liquid extraction processes. It calculates pH-dependent extraction efficiency using a general partitioning equation that accounts for multiple ionic species, providing interactive visualizations to guide experimental work and reduce development lead times [52].
Objective: Identify an optimal solvent mixture from a candidate set to maximize the mole fraction solubility of Paracetamol at 298.15 K.
Workflow:
Input Preparation:
CC(=O)NC1=CC=C(C=C1)O or a .coskf file.-meltingpoint flag. The enthalpy of fusion will be automatically estimated if unavailable [50]..coskf files from a database (e.g., Acetic Acid, Hexane, Toluene, Butanoic Acid, Ethanol).Command Line Execution:
-t SOLUBILITY sets the problem template.-max directs the optimization towards maximizing solubility.-solute flag follows the SMILES string to identify it as the solute.Output and Analysis:
Objective: Find an optimal two-phase solvent system and composition to maximize the distribution ratio (D) for separating two solutes.
Workflow:
Input Preparation:
.mol, or .coskf files, marking them with the -solute flag..coskf files. Ensure the candidate set includes solvents of differing polarity to facilitate phase immiscibility.Command Line Execution:
-t LLEXTRACTION selects the liquid-liquid extraction template.-multistart N is recommended for LLE problems to start the optimization from N random points, helping to locate a global optimum.-warmstart can be beneficial for problems involving highly immiscible solvents.Output and Analysis:
D = max( (γâá´µ/γâᴵᴵ) * (γâᴵᴵ/γâá´µ), (γâá´µ/γâᴵᴵ) * (γâᴵᴵ/γâá´µ) ), where I and II denote the two liquid phases [50].Objective: Determine the optimal aqueous phase pH and organic solvent to maximize the extraction efficiency of a desired product while rejecting impurities [52].
Workflow:
Input and Data Retrieval:
V_org, V_aq), and the isolation phase (organic or aqueous).Calculation and Visualization:
Application Example:
The table below summarizes the characteristics of the two main COSMO-RS optimization templates [50]:
Table 1: Performance Characteristics of COSMO-RS Solvent Optimization Templates
| Problem Template | Minimum Number of Solvents | Preferred Number of Solvents | Typical Solution Time | Recommended Multistarts |
|---|---|---|---|---|
| SOLUBILITY | 1 | >1 | < 2 s | < 5 |
| LLEXTRACTION | 2 | >4 | 1 - 30 s | 5 - 10 |
Best Practices for Reliable Optimization:
-multistart flag (5-10 starts) to increase the probability of finding the global optimum rather than a local one [50].-warmstart flag for problems with a small number of solvents or known highly immiscible solvent pairs to generate a high-quality initial guess [50]..coskf files for common solvents and in-house molecules to streamline the setup of screening studies [49].Table 2: Key Computational and Experimental Resources for In-silico Solvent Optimization
| Tool / Resource Name | Type | Primary Function | Application Context |
|---|---|---|---|
| COSMO-RS Database [49] | Chemical Database | Provides pre-computed Ï-profiles for ~2500 compounds (solvents, ions, small molecules). | Instantaneous property prediction without quantum calculations. |
| ADFCRS-2018 Database | Chemical Database | A specific, curated database of common solvents and compounds included with the Amsterdam Modeling Suite. | Used in example protocols for solvent optimization [50]. |
| BIOVIA COSMOtherm [53] | Software GUI | A commercial implementation of COSMO-RS providing a user-friendly interface for property prediction and screening. | Virtual solvent screening for solubility, log P, and reaction media. |
| ACS GCI Solvent Selection Guide [28] | Guidance Document | Rates solvents based on health, safety, and environmental (HSE) criteria. | Selecting green and sustainable solvents post-screening. |
| CHEM21 Solvent Selection Guide | Guidance Document | A widely adopted guide for rating solvents based on HSE criteria, suggested by the ACS GCI PR [28]. | Integrating green chemistry principles into solvent choice. |
| Process Mass Intensity (PMI) Calculator [28] | Calculation Tool | Quantifies the total mass of materials used per mass of product in a process. | Benchmarking the environmental and efficiency performance of a optimized solvent process. |
| Balomenib | Balomenib, CAS:2939850-17-4, MF:C33H34F3N7O2, MW:617.7 g/mol | Chemical Reagent | Bench Chemicals |
| hA2AAR antagonist 1 | hA2AAR antagonist 1, MF:C15H15N5O, MW:281.31 g/mol | Chemical Reagent | Bench Chemicals |
The following diagram illustrates the integrated computational and experimental workflow for rational solvent optimization aimed at reducing PMI.
Integrated Workflow for Solvent Optimization and PMI Reduction
The integration of COSMO-RS and complementary digital tools into solvent selection workflows represents a paradigm shift in chemical process development. These in-silico methods enable researchers to rapidly navigate vast solvent spaces, predict key thermodynamic properties with remarkable accuracy, and rationally design solvent systems for solubility, extraction, and reaction applications. By prioritizing experiments and reducing the traditional trial-and-error approach, these computational strategies significantly accelerate development timelines.
Framed within the broader objective of creating a solvent selection guide for lower PMI, these protocols provide a scientifically rigorous pathway to greener processes. The ability to optimize for performance while simultaneously considering environmental and safety criteria through tools like the ACS GCI Solvent Selection Guide ensures that sustainability is embedded at the design stage. As these computational techniques continue to evolve and become more accessible, their adoption is poised to play an indispensable role in advancing sustainable drug development and minimizing the ecological footprint of the pharmaceutical industry.
The use of hazardous dipolar aprotic solvents accounts for over 40% of total solvents used in synthetic, medicine-related, and process chemistry [54]. However, growing regulatory pressure is fundamentally reshaping the solvent landscape. The European Chemicals Agency (ECHA) now restricts or prohibits the use of many hazardous solvents, particularly those with reproductive toxicity, carcinogenicity, or mutagenicity profiles [55] [54]. Specifically, N,N-dimethylformamide (DMF) is now restricted in Europe due to its classification as a reproduction-toxic solvent and CMR agent (carcinogenic, mutagenic, or toxic for reproduction) [56]. Similarly, the U.S. Environmental Protection Agency (EPA) has issued a final rule in 2024 significantly restricting most uses of dichloromethane (DCM) under the Toxic Substances Control Act (TSCA), requiring stringent workplace chemical protection programs for any remaining laboratory uses [57]. These regulatory developments, coupled with the pharmaceutical industry's focus on reducing Process Mass Intensity (PMI), have accelerated the search for safer, more sustainable solvent alternatives that maintain performance while reducing environmental and health impacts [58] [56].
Several comprehensive solvent selection guides have been developed by pharmaceutical industries and consortia to facilitate the transition from hazardous solvents to safer alternatives. The GlaxoSmithKline (GSK) solvent guide analyzes 154 small molecules commonly used in pharmaceutical industries across four primary categories: waste, environment, human health, and safety, ranking solvents on a scale from 1 (major issues) to 10 (few known issues) [54]. The CHEM21 guide, produced by a European consortium and Innovative Medicines Initiative (IMI), ranks solvents in environmental, health, and safety categories on a scale from 1 (recommended) to 10 (hazardous) [54]. These frameworks provide invaluable tools for researchers seeking to identify regrettable substitutions and select truly greener alternatives based on comprehensive hazard assessments rather than single-issue evaluations.
Table 1: Hazardous Solvents and Their Primary Replacements
| Hazardous Solvent | Key Health/Environmental Concerns | Recommended Replacements | Replacement Applications |
|---|---|---|---|
| DMF (N,N-Dimethylformamide) | Reproductive toxicity, CMR agent [56] | DMSO/EtOAc mixtures [55] [56], N-butyl pyrrolidinone (NBP) [56] | Solid-phase peptide synthesis [55] [56] |
| DCM (Dichloromethane) | Carcinogenic, neurotoxic, metabolized to carbon monoxide [57] | Ethyl acetate/ethanol mixtures (e.g., 3:1 ratio) [57] [59], cyclopentyl methyl ether [54] | Chromatography, extraction, reaction solvent [57] [59] |
| NMP (N-Methyl-2-pyrrolidone) | Reproductive toxicity, skin irritation [60] | Sulfolane [60], 2,5,7,10-Tetraoxaundecane (TOU) [61], 1,3-dioxolane [61] | Polymer processing, synthesis, cleaning applications [60] [61] |
Significant advances have been made in replacing DMF in solid-phase peptide synthesis (SPPS) with green binary solvent mixtures that can be tailored to specific synthetic steps. Research demonstrates that mixtures such as DMSO/ethyl acetate (EtOAc), DMSO/1,3-dioxolane (DOL), and DMSO/2-methyl tetrahydrofuran (2-Me-THF) display similar polarity and viscosity profiles to DMF, making them viable alternatives [55]. The key innovation lies in dynamically adjusting the solvent composition during synthesis: using less polar mixtures for coupling reactions and more polar mixtures for Fmoc-removal reactions [55]. This approach not only maintains synthetic efficiency but can actually suppress common side-reactions like Arg-lactamisation and aspartimide formation through precise polarity control [55].
Table 2: Binary Solvent Mixtures for SPPS with Optimized Polarity Ratios
| Binary Solvent System | Ratio for Coupling (Less Polar) | Polarity [ET(30)] (kcal molâ»Â¹) | Ratio for Fmoc-Removal (More Polar) | Polarity [ET(30)] (kcal molâ»Â¹) |
|---|---|---|---|---|
| DMSO/DOL [55] | 2:8 | 42.21 | 4:6 | 43.38 |
| DMSO/2-Me-THF [55] | 2:8 | 41.94 | 4:6 | 43.16 |
| NFM/DOL [55] | 2:8 | 40.89 | 4:6 | 41.83 |
| NBP/DOL [55] | 2:8 | 40.84 | 4:6 | 41.11 |
Application Note: This protocol describes the implementation of a DMSO/EtOAc binary solvent system for solid-phase peptide synthesis as a direct replacement for DMF, suitable for both manual and automated synthesizers [56].
Materials and Equipment:
Procedure:
Validation: This method has been successfully applied to the synthesis of the peptide therapeutic Bivalirudin on a 7.5 mmol scale, significantly suppressing problematic Arg-lactamisation side-reactions through simple adjustment of the solvent ratio in critical synthesis steps [55].
DCM replacement requires careful consideration of the specific application, as no single solvent matches all of DCM's properties. For chromatography, a 3:1 mixture of ethyl acetate and ethanol can effectively replace DCM in many normal-phase purification systems [57] [59]. For extraction processes, ethyl acetate, methyl tert-butyl ether (MTBE), and 2-methyltetrahydrofuran have shown promise as alternatives, though each requires application-specific validation [59] [54]. Supercritical COâ has also emerged as a powerful alternative to DCM for extraction of natural products, particularly when combined with vegetable, drupe, legume, or seed oils as co-extractants [54].
Application Note: This protocol provides a method for substituting DCM-containing mobile phases with greener solvent systems for flash chromatography purification [57] [59].
Materials and Equipment:
Procedure:
Validation: This approach has been validated using a library of "drug-like" compounds, demonstrating that the eluting properties of these greener solvent systems can effectively replace DCM for purification while reducing toxicity concerns [59].
NMP replacement strategies have focused on identifying solvents with similar dipolar aprotic characteristics but improved toxicity profiles. Sulfolane has emerged as a particularly promising alternative, offering strikingly similar solvency performance to NMP with lower toxicity and minimal skin penetration characteristics [60]. For applications requiring closer physical similarity to NMP, 2,5,7,10-tetraoxaundecane (TOU) exhibits very close boiling point, flash point, and viscosity properties while avoiding reproductive toxicity concerns [61]. 1,3-Dioxolane provides another alternative with comparable solvent power to NMP and full water miscibility, though its higher volatility may require additional engineering controls [61].
Table 3: Physical and Safety Properties of NMP Alternatives
| Solvent | Boiling Point (°C) | Flash Point (°C) | Viscosity (cP at 25°C) | Toxicity Profile | Key Advantages |
|---|---|---|---|---|---|
| NMP [60] | 202 | 86 | 1.65 | Moderate (reproductive toxicity) | Benchmark properties |
| Sulfolane [60] | 285 | 176 | 1.2 | Low | High thermal stability, not flammable |
| TOU [61] | ~200 | ~90 | Similar to NMP | Low | Direct physical replacement |
| 1,3-Dioxolane [61] | 75 | -5 | Lower than NMP | Low | Excellent wetting properties |
Successful implementation of solvent replacement strategies requires access to appropriate materials and assessment tools. The following toolkit components are essential for researchers transitioning from hazardous solvents to greener alternatives:
Solvent Selection Guides: Printed or digital copies of the GSK Solvent Guide and CHEM21 Selection Guide for rapid assessment of solvent sustainability profiles [54].
Polarity Assessment Tools: Access to Reichardt's dye for empirical polarity measurements (ET(30) values) or reference tables of solvent polarity parameters to guide binary mixture optimization [55] [54].
Binary Solvent Components: Laboratory stocks of DMSO, ethyl acetate, 1,3-dioxolane, 2-methyltetrahydrofuran, and cyclopentyl methyl ether for preparing customized solvent mixtures [55] [54] [61].
Chromatography Alternatives: 3:1 ethyl acetate/ethanol mixtures pre-mixed in appropriate volumes for direct substitution in purification protocols [57].
Safety Equipment: Chemical-resistant gloves (nitrile alone is insufficient for many solvents), appropriate respiratory protection, and engineering controls to ensure safe handling of both conventional and alternative solvents [57].
The following workflow provides a systematic approach for implementing solvent replacement strategies within the context of overall Process Mass Intensity reduction:
Systematic Solvent Replacement Workflow
This structured approach ensures that solvent replacements not only reduce hazards but also contribute meaningfully to overall process mass intensity reduction goals. Companies like WuXi TIDES have demonstrated the effectiveness of this strategy, reporting significant reductions in PMI through solvent optimization, substitution, and recycling initiatives [58].
The transition from hazardous solvents to greener alternatives is both a regulatory necessity and a sustainability opportunity. By implementing the structured protocols and selection frameworks presented in this document, researchers and drug development professionals can effectively replace DMF, DCM, and NMP while maintaining synthetic efficiency and reducing environmental impact. The ability to dynamically adjust binary solvent mixtures provides particular promise for peptide synthesis applications where DMF has historically been dominant. Through systematic solvent replacement integrated with PMI reduction goals, the pharmaceutical industry can achieve more sustainable manufacturing processes without compromising product quality or synthetic efficiency.
Within pharmaceutical development and chemical manufacturing, solvent selection is a critical determinant of process efficiency, cost, and environmental impact. The drive toward sustainable practices necessitates a strategic approach to solvent selection, directly aligning with the goal of reducing Process Mass Intensity (PMI)âthe total mass of materials used per mass of product. Solvents can constitute up to 50-80% of the total mass in a typical pharmaceutical process, making their optimization a primary lever for PMI reduction [45] [28]. Liquid-liquid extraction (LLE), a ubiquitous unit operation for purification and impurity removal, is a key area where solvent choice profoundly influences yield, purity, and waste generation. This document provides a structured framework and detailed protocols for optimizing solvent mixtures, integrating physicochemical principles, data-driven tools, and empirical validation to guide researchers toward more efficient and sustainable processes [52].
The following workflow outlines the strategic approach to solvent system optimization:
The partitioning of a solute between two immiscible liquid phases is governed by its physicochemical properties and the properties of the solvents. For ionizable compounds, the partition coefficient (D) is highly dependent on pH and the pKa of the solute. The fraction of a compound in its neutral form (fN) can be calculated as a function of pH and pKa, and the distribution ratio (D) or fraction extracted (forg) can be predicted using established mathematical models [52]:
Fraction of Neutral Species (fN) and Organic Phase Extraction (forg):
Where KP is the partition coefficient of the neutral species, and VR is the volume ratio of the organic to aqueous phase (Vorg/Vaq) [52].
For the separation of multiple components, such as a product from impurities, the extraction efficiency (E) can be defined as the product of the fraction of the desired compound extracted into the target phase multiplied by the mean of the sum of the fractions of all impurities rejected [52]. This quantitative framework allows for the in-silico screening of optimal conditions, such as pH and solvent volume ratio, before laboratory experimentation.
The table below summarizes key parameters and their influence on extraction efficiency:
Table 1: Key Physicochemical Parameters for LLE Optimization
| Parameter | Symbol | Definition | Influence on Extraction |
|---|---|---|---|
| Partition Coefficient (Neutral) | KP | Ratio of neutral solute concentration in organic vs. aqueous phases at equilibrium. | Determines inherent affinity for organic phase; higher KP favors extraction. |
| Distribution Ratio | D | Ratio of total solute concentration (all forms) in organic vs. aqueous phases at equilibrium. | The operational measure of partitioning; depends on KP, pH, and pKa. |
| Dissociation Constant | pKa | pH at which 50% of the solute is ionized. | Determines the pH range for effective manipulation of solute charge and D. |
| Selectivity | S | Ratio of distribution ratios of two solutes (S = D1/D2). | Defines the ability to separate two compounds; S > 1 is required for separation. |
| Polarity Index | - | Empirical scale of solvent polarity. | Matching solvent polarity to solute hydrophobicity (LogP/D) improves recovery [62]. |
Modern solvent optimization leverages digital tools and publicly available resources to guide empirical work. The ACS Green Chemistry Institute Pharmaceutical Roundtable (ACS GCI PR) provides several vetted tools to aid in this process [45] [28].
These tools can be integrated with predictive models. For instance, a digital tool described by Karageorgis et al. uses Python to automate the retrieval of compound properties (LogP, pKa), calculate extraction efficiencies across the pH scale, and generate visualizations to identify optimal extraction "sweet spots" [52]. The convergence of predictive modeling, green chemistry principles, and high-throughput experimentation (HTE) is paving the way for more efficient solvent selection. Emerging machine learning approaches are being applied to rich datasets that screen solvent mixtures and continuous process conditions to directly predict reaction yields and separation efficiencies [63].
This protocol is designed for the rapid identification of promising extraction conditions using 96-well plate technology [62].
Research Reagent Solutions:
Procedure:
This detailed protocol, adapted from Shekarsaraee et al., is used for in-depth study of a ternary (water-solute-solvent) system [64].
Materials and Apparatus:
Procedure:
The following diagram illustrates the experimental workflow for LLE data determination:
A study on the extraction of 2-methoxyphenol from aqueous solutions provides quantitative data on solvent performance, demonstrating the relationship between solvent type and key efficiency metrics [64].
Table 2: Distribution Coefficients (D) and Selectivities (S) for 2-Methoxyphenol in Various Solvents at 298.2 K
| Solvent | Polarity Index | Distribution Coefficient (D) | Selectivity (S) |
|---|---|---|---|
| Dichloromethane | 3.1 | 28.7 | 1874 |
| Chloroform | 4.1 | 24.9 | 1328 |
| Toluene | 2.4 | 11.7 | 1160 |
| m-Xylene | - | 9.7 | 1075 |
| Cyclohexane | 0.0 | 1.4 | 273 |
Data adapted from Shekarsaraee et al. [64]
Key Findings: Halogenated solvents like dichloromethane and chloroform showed the highest distribution coefficients, indicating strong extraction power for 2-methoxyphenol. This can be attributed to their hydrogen-bond donor capability, which interacts effectively with the solute. While toluene and xylene have lower D values, they still exhibit high selectivity, which is crucial for purification. The nonpolar cyclohexane was the least effective, underscoring the "like-dissolves-like" principle [64].
A digital tool was applied to optimize the workup of a BuchwaldâHartwig coupling reaction [52]. The challenge was to separate the product 3 from excess amine starting material 2.
Scenario 1: Separating Product from Excess Amine
Scenario 2: Incomplete Reaction with Multiple Impurities
The following table catalogues critical tools and reagents for executing the described optimization strategies.
Table 3: Essential Research Reagent Solutions for Solvent Optimization
| Tool / Reagent | Function / Description | Example Use Case |
|---|---|---|
| ACS GCI Solvent Selection Guide | A guide ranking solvents based on health, safety, and environmental (HSE) criteria. | First-pass selection of sustainable solvents before experimental screening [45] [28]. |
| PCA-Based Solvent Tool | Interactive map showing solvents with similar/dissimilar properties based on Principal Component Analysis. | Finding greener substitutes with properties similar to a known high-performing but problematic solvent [28]. |
| LogP/D & pKa Databases | Online databases (e.g., ChemSpider, Chemicalize) providing key solute physicochemical parameters. | Input for predictive modeling of extraction efficiency and pH scoping [52] [62]. |
| Buffer Solutions (pH 2-12) | Aqueous solutions to control the ionization state of ionizable solutes. | Systematic investigation of pH impact on distribution ratio during LLE screening [62]. |
| Solvent Polarity Index Set | A library of organic solvents with a wide range of polarity indexes (e.g., Heptane 0.0 to MEK 4.7). | Experimental mapping of solvent polarity to solute recovery and selectivity [62]. |
| Salt Additives | Salts like sodium sulfate or ion-pairing reagents (e.g., tetraalkylammonium salts). | Salting-out hydrophilic analytes or forming extractable ion pairs to improve recovery [62]. |
| PMI Calculator | Spreadsheet-based tool to calculate Process Mass Intensity. | Quantifying the environmental and mass efficiency impact of a chosen solvent system [45]. |
This document details practical methodologies for implementing continuous processing and complementary technologies to significantly reduce Process Mass Intensity (PMI) in pharmaceutical manufacturing. High PMI, indicative of resource-intensive processes, is a critical challenge, especially in peptide synthesis and other complex molecule production [58]. By integrating continuous bioprocessing, membrane-based separations, and sustainable solvent selection, manufacturers can achieve substantial improvements in efficiency, cost, and environmental sustainability. The strategies outlined herein are supported by quantitative data and provide a clear roadmap for researchers and development professionals.
The following tables summarize key performance data from various studies on PMI reduction technologies.
Table 1: Performance Metrics of Continuous Processing Technologies
| Technology | Application | Key Performance Improvement | Reference |
|---|---|---|---|
| 3-Column Periodic Counter-Current Chromatography (3C-PCC) | mAb Capture | Productivity of ~100 mg/mL resin/h; Increased resin capacity utilization [65]. | |
| Hybrid Continuous Bioprocessing | Biologics Production | >10-fold productivity gains (up to 8 g/L-day); Reduced Cost of Goods (COGs) [66]. | |
| Fully End-to-End Continuous Production (E. coli) | Recombinant Proteins | Reduced operational footprint, CAPEX, and OPEX compared to fed-batch [66]. | |
| Multi-Column Countercurrent Solvent Gradient Purification (MCSGP) | Peptide Purification | Reduced solvent demand while maintaining throughput scalability [58]. |
Table 2: Solvent Reduction and Sustainability Metrics
| Technology / Strategy | Application | Solvent Reduction / Sustainability Outcome | Reference |
|---|---|---|---|
| Organic Solvent Nanofiltration (OSN) with PAT | API Purification | 50% reduction in solvent usage compared to traditional diafiltration [67]. | |
| Solvent Optimization & Recycling (WuXi TIDES) | Peptide Synthesis | 25% cut in overall solvent use; 50% of DMF replaced with sustainable solvents [58]. | |
| Continuous Capture Chromatography | mAb Purification | Lower buffer consumption per gram of product [65]. | |
| Novel OSN Process Design | API Purification | Improved recovery efficiency by 103% [67]. |
This protocol is adapted for the capture of monoclonal antibodies (mAbs) from a high-titer harvest (â¥5 g/L) and is supported by in-silico modeling [65].
This protocol describes a stepwise methodology for using OSN to remove trace oligomeric impurities from an Active Pharmaceutical Ingredient (API), reducing solvent consumption by 50% versus traditional methods [67].
Table 3: Essential Materials for Implementing Low-PMI Continuous Processes
| Item | Function & Application | Example(s) |
|---|---|---|
| Protein A Resins | Affinity capture of monoclonal antibodies (mAbs) in continuous chromatography; high dynamic binding capacity is critical. | MabSelect SuRe [65], Purolite AP+ resin portfolio [66]. |
| Ion Exchange Resins | Polishing step in continuous processing to remove impurities like host cell proteins after capture. | CaptoS ImpAct [65]. |
| OSN Membranes | Membrane-based purification for APIs, peptides, and oligonucleotides; reduces solid waste and solvent use versus chromatography. | Commercial flat-sheet membranes from Borsig or Evonik [67]. |
| PAT (Process Analytical Technology) Tools | Inline, real-time monitoring of critical process parameters (e.g., concentration) to enable precise control and solvent reduction. | UV/Vis flow cell, FTIR [67]. |
| Specialized Solvents | Sustainable solvents with improved SHE (Safety, Health, Environment) profiles for synthesis and purification, as guided by solvent selection guides. | Bio-derived or less classical solvents from the CHEM21 guide [30]; alternatives to DMF and acetonitrile [58]. |
| Continuous Bioprocessing Platforms | Integrated systems for end-to-end continuous production of biologics, improving productivity and reducing footprint. | enGenes-eXpress (E. coli system) [66], Benchtop pilot platforms with cGMP flow paths [66]. |
Within the framework of developing a comprehensive solvent selection guide for lower Process Mass Intensity (PMI), this case study examines a successful industrial application of green chemistry principles. PMI, a key metric of environmental efficiency in active pharmaceutical ingredient (API) manufacturing, measures the total mass of materials used per unit mass of final API produced [68]. High PMI values, often ranging from 70 to 433 kg materials per kg of API, correlate directly with significant environmental footprints, including substantial waste generation and carbon emissions [68]. The pharmaceutical industry faces mounting pressure to reduce its environmental impact, with a particular focus on solvents which constitute a major portion of manufacturing waste. This analysis details a specific implementation of solvent and process redesign that successfully reduced PMI while maintaining product quality and efficacy, providing a reproducible protocol for industry researchers and drug development professionals.
The case focuses on the manufacturing process for a small-molecule API where the existing synthetic route exhibited a PMI of 210. A comprehensive analysis revealed that conventional solvents accounted for over 60% of the total mass input and contributed significantly to the process's carbon footprint through both production and end-of-life incineration emissions [68]. The primary objective was to reduce PMI by at least 40% through a systematic solvent and process redesign initiative while maintaining or improving process safety, yield, and regulatory compliance. Secondary objectives included reducing greenhouse gas emissions by approximately 30% and decreasing solvent-related waste incineration by implementing advanced recovery systems [68].
The redesign employed a systematic solvent selection methodology based on the Gani et al. framework, augmented with specific criteria for pharmaceutical processes [69]. This approach integrated computational predictions with empirical validation to identify optimal green solvent alternatives.
Key Selection Criteria:
For the liquid-liquid extraction steps, researchers implemented a Bayesian Experimental Design (BED) framework to optimize solvent systems efficiently [70]. This iterative approach combined computational predictions with high-throughput experimentation:
This approach demonstrated significantly lower mean absolute error values than computational predictions alone, with continuous improvement through each iterative cycle [70].
For solvent recovery operations, the team implemented physics-enforced multi-task machine learning models to identify optimal polymer membranes for pervaporation-based solvent separation [71]. The methodology integrated experimental and simulated diffusivity data while enforcing physical relationships such as:
The model screened over 13,000 known polymers and millions of virtually generated candidates to identify sustainable, high-performance membrane materials for solvent recovery operations [71].
The implementation focused on replacing three high-PMI solvents in the original process with environmentally preferable alternatives. The following table summarizes the key substitutions and their impacts:
Table 1: Green Solvent Substitutions and Quantitative Impacts
| Original Solvent | Green Alternative | PMI Reduction | Carbon Footprint Reduction | Key Properties |
|---|---|---|---|---|
| Dichloromethane | Dimethyl carbonate | 28% | 45% | Bio-based, low toxicity, biodegradable [3] |
| N,N-Dimethylformamide | Ethyl lactate | 32% | 52% | Bio-based, renewable feedstocks [3] |
| Hexane | Limonene | 25% | 38% | Bio-based, low VOC emission [3] |
| Acetonitrile | Deep Eutectic Solvent (DES) | 41% | 60% | Tunable properties, low volatility [3] |
Beyond direct solvent substitution, the project implemented significant process modifications that contributed to PMI reduction:
Table 2: Process Modifications and Efficiency Improvements
| Process Modification | Implementation Details | PMI Reduction | Additional Benefits |
|---|---|---|---|
| Solvent recovery system | Pervaporation membranes with ML-optimized polymers [71] | 22% | 75% reduction in solvent waste incineration |
| Process step elimination | Telescoping of three steps into one | 31% | Reduced processing time by 45% |
| Continuous manufacturing | Implementation of flow chemistry | 18% | Improved yield and reproducibility |
| Heat integration | High-temperature heat pump system | 8% | 90% plant emissions reduction at one facility [68] |
The combined solvent and process redesign initiatives yielded substantial improvements across multiple environmental and economic indicators:
Purpose: To efficiently identify optimal green solvent mixtures for liquid-liquid extraction processes [70]
Materials:
Procedure:
Iterative Optimization Cycle:
Validation:
Purpose: To implement membrane-based solvent recovery for PMI reduction [71]
Materials:
Procedure:
System Operation:
Performance Evaluation:
Purpose: To efficiently replace high-PMI solvents with greener alternatives in existing processes [69]
Materials:
Procedure:
Swap Execution:
Crystallization Optimization (if applicable):
Bayesian Solvent Optimization
Integrated PMI Reduction Framework
Table 3: Essential Materials for Green Solvent Implementation
| Reagent/Material | Function/Application | Key Characteristics | Sustainability Profile |
|---|---|---|---|
| Dimethyl Carbonate | Replacement for chlorinated solvents | Low toxicity, biodegradable | Bio-based synthesis [3] |
| Ethyl Lactate | Polar aprotic solvent substitute | Renewable feedstock, low VOC | Readily biodegradable [3] |
| Limonene | Hydrocarbon solvent alternative | Bio-based, pleasant odor | From citrus waste streams [3] |
| Deep Eutectic Solvents (DES) | Tunable solvent systems | Designable properties | Low volatility, low toxicity [3] |
| Supercritical CO2 | Extraction and reaction medium | Non-flammable, tunable density | Zero ODP, non-toxic [3] |
| Polymer Membranes (ML-optimized) | Solvent recovery via pervaporation | High permselectivity | Halogen-free alternatives [71] |
| Bayesian Optimization Software | Solvent system design | Efficient experimental design | Reduces experimental waste [70] |
| COSMO-RS Computational Tool | Solvent property prediction | Thermodynamic predictions | Guides green solvent selection [70] |
This case study demonstrates that systematic solvent and process redesign can achieve substantial PMI reductions exceeding 60% while maintaining process viability and economic feasibility. The successful implementation combined multiple strategies: substitution with bio-based solvents, process intensification through step reduction, implementation of advanced solvent recovery systems, and energy integration through heat recovery. The methodologies describedâincluding Bayesian experimental design, physics-enforced machine learning for membrane selection, and systematic solvent swap protocolsâprovide reproducible frameworks for similar initiatives across API manufacturing.
Future directions in PMI reduction will likely involve increased integration of computational prediction tools with high-throughput experimentation, development of novel bio-based solvent systems with improved technical profiles, and advanced hybrid separation technologies that minimize energy consumption. Furthermore, the growing emphasis on circular economy principles will drive innovation in solvent recycling and recovery technologies, potentially incorporating chemically recyclable polymer membranes [71] and industrial ecology approaches that repurpose waste solvents from pharmaceutical manufacturing into valuable inputs for other industries. As regulatory frameworks continue to evolve toward stricter environmental standards, the systematic approaches outlined in this case study will become increasingly essential for sustainable pharmaceutical manufacturing.
The Analytical Method Greenness Score (AMGS) Calculator is a metric tool developed by the ACS Green Chemistry Institute Pharmaceutical Roundtable (ACS GCIPR) to encourage analysts to develop more sustainable separation methods during drug development [72] [73]. It provides a standardized approach for comparing the environmental impact of high-pressure liquid chromatography (HPLC), UHPLC, and supercritical fluid chromatography (SFC) methods [45]. The AMGS metric is particularly valuable within research focused on solvent selection for lower Process Mass Intensity (PMI), as it quantifies the environmental footprint of analytical methods that are frequently used throughout chemical development and quality control [6] [58].
The primary output is a single numerical score where a lower AMGS value indicates a greener method [73]. This score raises environmental awareness and provides a straightforward means to benchmark one method against another, helping scientists make informed decisions that align with green chemistry principles [73] [74].
The AMGS calculation integrates several environmental and energy factors into a comprehensive score. The core components are summarized in the table below.
Table 1: Key Metrics Integrated into the AMGS Calculation
| Metric Category | Description | Data Sources |
|---|---|---|
| Solvent Impact | Health, safety, and environmental impact of solvents used [73] [45]. | Solvent Selection Guide, EHS criteria [6] [28]. |
| Cumulative Energy Demand | Total energy consumed from raw material extraction to production [72] [73]. | Life cycle inventory data. |
| Instrument Energy Usage | Direct electrical energy consumption of the chromatographic instrument [73]. | Method run time and instrument power characteristics. |
| Method Solvent Waste | Total volume of solvent waste generated [72] [73]. | Flow rate, run time, and post-analysis handling. |
The calculator uses a color-coding system (yellow and red) to highlight which of the three main categories (Solvent Impact, Cumulative Energy Demand, and a combined Instrument Energy/Solvent Waste score) contributes most significantly to the total AMGS. This immediately directs the scientist to the area with the greatest potential for improvement [73]. The logical relationship between these components and the final score is outlined below.
Before using the calculator, gather all necessary method parameters.
Table 2: Essential Data Requirements for the AMGS Calculator
| Data Field | Description | Example |
|---|---|---|
| Solvent(s) Used | Identity and volume of each solvent in the mobile phase. | Methanol, Acetonitrile. |
| Method Duration | Total run time per injection, including equilibration. | 10 minutes. |
| Flow Rate | Mobile phase flow rate. | 1.0 mL/min. |
| System Suitability Test (SST) Volume | Total volume of solvent used for all dilutions to prepare the SST solution. If both resolution and sensitivity solutions are used, include the total volume for both [73]. | 50 mL. |
| Instrument Type | Specification of HPLC, UHPLC, or SFC system. | UHPLC. |
Follow this detailed protocol to determine the AMGS for your analytical method.
Procedure:
Successful application of the AMGS calculator and the development of greener methods often rely on a suite of complementary tools and guides.
Table 3: Essential Research Tools for Green Analytical Chemistry
| Tool Name | Function | Relevance to AMGS & Lower PMI |
|---|---|---|
| ACS GCI Solvent Selection Guide | Provides safety, health, and environmental scores for classical and bio-derived solvents [28]. | Informs choice of greener solvents, directly reducing the solvent impact component of the AMGS [6]. |
| Interactive Solvent Selection Tool | Allows interactive selection based on Principal Component Analysis (PCA) of solvent properties [6] [28]. | Helps identify solvents with similar properties but lower environmental impact, aiding in method development. |
| Process Mass Intensity (PMI) Calculator | Measures the total mass of raw materials per mass of product [45] [28]. | The primary research metric for process efficiency; AMGS is the analytical counterpart. Reducing solvent use improves both. |
| Reagent Guides | Venn diagrams evaluating reagents on scalability, utility, and greenness for over 25 transformations [45]. | While focused on synthesis, the principles inform a holistic green chemistry approach in the lab. |
Consider a scenario where a scientist is developing a new analytical method and must choose between a traditional HPLC and a modern UHPLC configuration.
Table 4: Hypothetical AMGS Comparison for HPLC vs. UHPLC Methods
| Parameter | Method A: HPLC | Method B: UHPLC |
|---|---|---|
| Solvent | Acetonitrile (ACN) | Acetonitrile (ACN) |
| Run Time | 20 min | 5 min |
| Flow Rate | 1.5 mL/min | 0.5 mL/min |
| Total Solvent Waste | 30 mL | 2.5 mL |
| Calculated Solvent Impact | High (e.g., 45%) | High (e.g., 45%) |
| Calculated Instrument Energy | High (e.g., Red) | Medium (e.g., Yellow) |
| Calculated Waste/Energy Score | High (e.g., Red) | Low (e.g., No Highlight) |
| Overall AMGS | Higher (Less Green) | Lower (Greener) |
Interpretation: Although both methods use the same solvent, Method B (UHPLC) achieves a lower (greener) AMGS due to a significantly shorter run time and lower flow rate. This reduces both instrument energy consumption and the volume of solvent waste generated. The color-coding would clearly show that improving instrument energy and solvent waste is the key advantage of Method B. This example demonstrates how the AMGS calculator incentivizes the adoption of faster, more efficient separation technologies, which directly aligns with PMI reduction goals by minimizing material use [72] [58].
gcipr@acs.org with suggestions or reports on how they are using the calculator [73].Process Mass Intensity (PMI) is a key mass-based metric used to evaluate the resource efficiency and environmental impact of chemical processes, particularly in the pharmaceutical industry. It is defined as the total mass of materials used to produce a unit mass of the desired product, calculated using the formula: PMI = Total Mass of Materials Input (kg) / Mass of Product (kg) [6]. A lower PMI value indicates a more efficient and environmentally friendly process, as it signifies less waste generation and reduced resource consumption. PMI has emerged as a fundamental green chemistry metric for benchmarking and quantifying improvements in manufacturing processes, enabling researchers to objectively compare traditional methodologies with optimized green alternatives [28] [75]. Within the pharmaceutical industry, where solvents can constitute approximately 50% of materials used in active pharmaceutical ingredient (API) manufacturing, PMI analysis provides crucial insights for sustainability assessments and process optimization [28].
This application note provides detailed methodologies for conducting comparative PMI analyses between traditional and green processes, with emphasis on solvent selection strategies that significantly influence PMI outcomes. The protocols outlined herein are designed for researchers, scientists, and drug development professionals seeking to implement green chemistry principles while maintaining process efficiency and product quality.
While PMI serves as a comprehensive metric encompassing all input materials, several complementary mass-based metrics are essential for thorough process analysis:
The relationship between these metrics provides a multi-faceted view of process efficiency, with PMI offering the most comprehensive assessment of overall material usage [75].
The ACS Green Chemistry Institute Pharmaceutical Roundtable (ACS GCIPR) has developed standardized tools for PMI calculation, including a basic PMI calculator and a convergent PMI calculator for complex syntheses [28]. For discovery-level assessments, the PMI Prediction Calculator uses historical data and predictive analytics to estimate efficiencies of proposed synthetic routes before laboratory evaluation [28].
Table 1: PMI Benchmarking Data for Different Therapeutic Modalities
| Therapeutic Modality | Typical PMI Range | Key Influencing Factors |
|---|---|---|
| Small Molecule APIs | 50-200 | Reaction steps, solvent intensity, catalyst usage |
| Monoclonal Antibodies | Comparable between batch and continuous processes | Bioreactor scale, productivity per unit time [76] |
| Oligonucleotides | Varies by process optimization | Protecting group strategy, isolation methods [6] |
| Peptides | Dependent on synthesis method | Solid-phase vs. solution-phase, coupling reagents |
Recent studies indicate that continuous processes for biologics manufacture may have PMIs similar to batch processes, but their higher productivity per unit time can result in lower overall energy consumption per unit of drug substance produced [76].
Objective: To quantitatively compare the material efficiency of traditional and optimized green processes through PMI calculation.
Materials and Equipment:
Procedure:
Data Interpretation:
Objective: To systematically evaluate and select greener solvent alternatives that reduce PMI without compromising reaction efficiency.
Materials and Equipment:
Procedure:
Data Interpretation:
Table 2: Essential Research Tools for PMI Analysis and Solvent Selection
| Tool Name | Function | Application in PMI Analysis |
|---|---|---|
| ACS GCI PMI Calculator | Calculates PMI from material inputs | Standardized PMI determination for single and convergent syntheses [28] |
| PMI Prediction Calculator | Predicts PMI of proposed synthetic routes | Virtual screening of route efficiency during process design [28] [6] |
| ACS GCI Solvent Selection Tool | Interactive solvent selection based on PCA of properties | Identifying greener alternatives with similar chemical functionality [12] |
| CHEM21 Solvent Selection Guide | Rates solvents based on health, safety, and environmental criteria | Classifying solvents as recommended, problematic, or hazardous [21] |
| Green Chemistry Innovation Scorecard | Quantifies impact of innovation on waste reduction | Benchmarking process improvements against industry data [28] |
The following diagram illustrates the systematic workflow for conducting a comparative PMI analysis between traditional and optimized green processes:
A comparative analysis between batch and continuous manufacturing processes for monoclonal antibodies (mAbs) reveals that while PMI values may be similar, continuous processes achieve multifold higher productivity per unit time, resulting in lower overall energy consumption per unit of drug substance produced [76]. This highlights the importance of considering additional sustainability metrics beyond PMI alone.
Table 3: PMI Comparison Between Process Types for mAb Production
| Process Parameter | Batch Process | Continuous Process |
|---|---|---|
| Bioreactor Scale | Baseline | Comparable scale |
| Productivity (g DS/time) | Baseline | Multifold higher [76] |
| PMI Value | Comparable between processes [76] | Comparable to batch [76] |
| Energy Consumption per unit DS | Baseline | Potentially lower |
| Environmental Sustainability | Lower when considering full lifecycle | Potentially higher due to productivity gains [76] |
Sensitivity analysis of continuous biologics processes demonstrates that specific process parameters, particularly cell culture density and purification efficiency, significantly impact material usage efficiency [76]. This case study underscores that while PMI provides valuable benchmarking data, comprehensive sustainability assessment requires additional metrics that account for energy consumption, productivity, and environmental impacts.
Systematic comparative PMI analysis provides researchers with a robust framework for evaluating and improving the sustainability of chemical processes. By integrating standardized PMI calculation methods with sophisticated solvent selection tools, scientists can quantitatively demonstrate improvements achieved through green chemistry optimization. The experimental protocols outlined in this application note enable comprehensive assessment of both material efficiency and environmental, health, and safety impacts of process modifications. As green chemistry continues to evolve, PMI remains a foundational metric for driving innovation in sustainable pharmaceutical development and manufacturing, though it should be complemented with additional sustainability indicators for holistic environmental assessment [76] [75].
Process Mass Intensity (PMI) is a pivotal green chemistry metric, defined as the total mass of materials used to produce a specified mass of an active pharmaceutical ingredient (API). A lower PMI signifies a more efficient and environmentally sustainable process, reducing waste, energy consumption, and cost [77]. Solvent use is a major contributor to PMI in pharmaceutical manufacturing, often accounting for the largest mass input. This application note details a successful case study where a strategic solvent selection and process optimization led to a significant reduction in PMI for the production of a co-precipitated amorphous dispersion (cPAD) of posaconazole, providing a reproducible protocol for researchers and process chemists [78].
Posaconazole, a model BCS Class II compound, was used to form an amorphous solid dispersion (ASD) with the polymer HPMCAS-M to enhance bioavailability. The initial manufacturing process faced a critical challenge: using an n-heptane anti-solvent system during co-precipitation resulted in residual crystallinity in the final product. While switching to an acidified water anti-solvent system solved the crystallinity issue, it created a new problem of unacceptably low bulk powder density, compromising downstream processability. The objective was to develop a process that achieved both a fully amorphous solid-state and favorable bulk powder properties while minimizing the overall PMI [78].
The following optimized protocol outlines the steps for producing a high-quality, fully amorphous cPAD with high bulk density.
Materials:
Procedure:
The strategic solvent and process selection successfully mitigated crystallization and improved bulk density. The use of a high-shear mixer was critical to achieving the necessary mixing intensity on a millisecond scale, preventing crystal nucleation and growth before the formation of the amorphous phase [78].
Table 1: PMI and Property Comparison of Posaconazole cPAD Processes
| Process Parameter | Initial Process (n-Heptane Anti-solvent) | Sub-Optimal Process (Aqueous Anti-solvent) | Optimized Process (n-Heptane with High-Shear) |
|---|---|---|---|
| Residual Crystallinity | Present | Absent | Absent [78] |
| Bulk Powder Density | High | Low | High [78] |
| Primary PMI Driver | Solvent/anti-solvent mass | Solvent/anti-solvent mass | Solvent/anti-solvent mass |
| Key Improvement | -- | Solved crystallinity | Solved crystallinity & maintained high density [78] |
This case study highlights that PMI reduction is not solely about switching solvents but involves a holistic approach integrating solvent properties with equipment and process parameters.
Table 2: Key Research Reagents and Solutions for cPAD Development
| Item | Function/Application | Key Considerations |
|---|---|---|
| HPMCAS-M Polymer | Matrix former in ASD to inhibit API crystallization and stabilize the amorphous form [78]. | Polymer grade and drug-polymer miscibility are critical for physical stability. |
| Green Solvents (e.g., Acetone, Ethyl Acetate) | To dissolve API and polymer for the co-precipitation process [78] [54]. | Select based on GSK/CHEM21 guide rankings, solubility, boiling point, and EHS criteria [54] [31]. |
| Anti-solvent (e.g., n-Heptane, Water) | To induce supersaturation and precipitation of the API-polymer mixture [78]. | Miscibility with solvent, environmental, health, and safety (EHS) profile, and impact on solid-state properties. |
| High-Shear Mixer | Provides rapid, homogeneous mixing to generate a uniform supersaturation field [78]. | Mixing intensity (tip speed) and time scales are critical to prevent crystallization. |
The following diagram illustrates a systematic workflow for solvent selection and process development aimed at reducing PMI, integrating the principles from the posaconazole case study.
Workflow for PMI Reduction
This workflow emphasizes an iterative development cycle where solvent selection is continuously refined based on performance data against the TPP and PMI targets.
This application note demonstrates that a science-led approach to solvent and process selection is fundamental to reducing PMI in pharmaceutical manufacturing. The posaconazole case study proves that challenges like residual crystallinity and poor powder properties can be overcome without sacrificing process efficiency, by leveraging mechanistic understanding and advanced engineering solutions. Adopting the detailed protocols, reagent guides, and workflows provided herein will equip scientists and engineers to design more sustainable, cost-effective, and robust pharmaceutical processes.
The strategic selection of green solvents and the implementation of solvent-free technologies are pivotal for advancing sustainable practices in pharmaceutical development and specialty manufacturing. Moving beyond traditional metrics, this assessment demonstrates that such choices yield significant competitive advantages across economic, regulatory, and supply chain dimensions. Quantitative analyses reveal that green chemistry principles can reduce process mass intensity (PMI) by factors of tenfold or more, directly translating to lower waste disposal costs and raw material consumption [79]. Furthermore, adopting safer, bio-based solvents and solvent-free processes mitigates regulatory risks associated with hazardous substances and creates more resilient, sustainable supply chains. This document provides a structured framework, complete with validated protocols and analytical tools, to guide researchers and drug development professionals in quantifying these broader impacts and making informed, strategic solvent selections.
The transition to green solvents and solvent-free processes offers measurable benefits across multiple business and operational domains. The following tables summarize key quantitative and strategic impacts.
Table 1: Economic and Operational Impact Analysis
| Impact Category | Traditional Process Benchmark | Green Alternative Outcome | Quantitative Benefit |
|---|---|---|---|
| Process Efficiency | High E-Factor (25-100+ kg waste/kg API) [79] | Reduced E-Factor/PMI [79] | Up to 10-fold reduction in Process Mass Intensity (PMI) [79] |
| Waste Management | High-cost hazardous waste disposal [79] | Reduced hazardous waste generation [3] [79] | Lower waste disposal costs; reduced environmental liability |
| Resource Consumption | Reliance on petrochemical feedstocks [79] | Use of renewable, bio-based feedstocks [3] [80] | Insulation from fossil fuel price volatility; long-term supply security [79] |
| Operational Safety | Costs for specialized handling, PPE, and containment [79] | Use of non-toxic, biodegradable solvents (e.g., ethyl lactate, limonene) [3] | Reduced insurance premiums; lower risk of workplace accidents [79] |
| Energy Efficiency | High-energy curing/drying (e.g., ovens, ventilation) [81] | Lower temperature curing; reduced energy needs [81] | Lower utility bills; reduced carbon footprint [79] [81] |
Table 2: Regulatory and Supply Chain Advantage Assessment
| Impact Category | Traditional Process Risk | Green Alternative Advantage | Strategic Benefit |
|---|---|---|---|
| Regulatory Compliance | Scrutiny and bans on PFOS, PFOA, VOCs [82] | Elimination of regulated substances (PFAS-free) [82] | Simplified approvals; alignment with FDA QbD/PAT initiatives [79] |
| Supply Chain Resilience | Price volatility of petroleum-derived solvents [79] | Bio-based solvents (e.g., dimethyl carbonate) [3] | Diversified sourcing; reduced geopolitical risk [79] |
| Market Access & Brand Value | Increasing restrictions on VOC emissions and hazardous chemicals [82] [81] | Solvent-free fusion technology [82] | Certified safety (CPSIA, FDA); enhanced brand loyalty [82] |
| Product Performance & Lifetime | Adhesive degradation in laminated fabrics [82] | Molecular thermal fusion bonding [82] | Performance longevity (>300 wash cycles) [82] |
This protocol provides a methodology for quantifying the total cost of ownership and broader impacts of solvent choices in a pharmaceutical process.
I. Research Reagent Solutions
II. Procedure
This protocol outlines testing procedures to validate that solvent-free materials meet or exceed the performance of traditional solvent-based systems, focusing on durability and functional integrity.
I. Research Reagent Solutions
II. Procedure
The following diagrams map the critical pathways for integrating broader impact assessments into R&D and manufacturing decision-making.
Solvent Selection Decision Pathway
This workflow visualizes the multi-faceted decision-making process for selecting new solvents or processes, emphasizing that technical and economic feasibility must be evaluated alongside regulatory and supply chain factors.
Impact of Green Chemistry Adoption
This causal loop diagram illustrates how initial environmental and cost drivers lead to the adoption of green chemistry, which in turn generates a cascade of benefits that reinforce economic viability and create a sustainable competitive edge.
Within the context of developing a solvent selection guide for lower Process Mass Intensity (PMI), establishing robust internal benchmarks is not merely an operational improvement tacticâit is a fundamental requirement for sustainable drug development. The pharmaceutical sector is increasingly adopting green solvents as environmentally friendly substitutes for conventional solvents in response to rising ecological concerns and regulatory restrictions [3]. These alternatives, including bio-based solvents, water-based solvents, supercritical fluids, and deep eutectic solvents, offer significant potential to reduce the environmental footprint of Active Pharmaceutical Ingredient (API) synthesis. A solvent selection guide provides a critical framework for this transition, enabling researchers to quickly identify problematic solvents and select preferred alternatives without spending significant time analyzing each individual substance [29].
The core objective of these application notes is to provide researchers, scientists, and drug development professionals with a structured methodology for implementing internal benchmarking practices specifically tailored to green solvent evaluation and adoption. This process enables organizations to quantitatively measure and improve their chemical processes against the best internal practices before comparing them against external competitors [83]. For synthetic chemists and process engineers, this translates to a systematic approach for identifying the 'best of the best' within an organization and leveraging those insights to elevate overall sustainability performance across all development activities [83]. When properly executed, internal benchmarking serves as a powerful catalyst for continuous improvement, transforming solvent selection from an arbitrary choice into a data-driven decision that directly contributes to reduced PMI and more sustainable API synthesis [4].
Internal benchmarking involves comparing internal processes and performance metrics within the same organization [83]. Unlike external benchmarking, which looks outward to compare with other companies, internal benchmarking offers a more introspective view that is particularly valuable during the early stages of green chemistry implementation. This approach is fundamentally an ongoing process of measuring and improving business practices against the companies that can be identified as the best worldwide [84].
For pharmaceutical development teams, internal benchmarking provides several distinct advantages. First, it is resource-efficient, requiring less time and financial investment compared to external benchmarking, which demands access to often elusive or expensive competitor data [83]. Second, it facilitates the identification of best practices, highlights inefficiencies, and uncovers areas ripe for enhancement using existing internal data [83]. Most importantly, internal benchmarking allows organizations to refine their approach to green solvent adoption without divulging sensitive internal data or seeking confidential information about competitors, thus sidestepping potential ethical or legal pitfalls [83].
The application of benchmarking to solvent selection represents a strategic evolution in green chemistry implementation. As Richard Schonberger defines in Operations Management, core competencies are "key business output or process through which an organization distinguishes itself positively" [84]. For process chemists, developing expertise in green solvent selection constitutes precisely such a core competency, potentially lowering operating costs, reducing environmental impact, and improving regulatory compliance [84].
A gap analysis is a key component of any benchmarking project and helps that project achieve the business objectives [84]. This methodology is divided into three main phases:
In the context of solvent selection for lower PMI, this framework enables research teams to quantify their current solvent utilization, identify the maximum potential improvement possible with existing technologies, and establish targets based on optimized processes. To utilize gap analysis effectively, the benchmarking project must be able to produce quantifiable results [84]. All measures must be expressed clearly and concisely so that the improvement program can be quantified, making this approach particularly suitable for PMI reduction where mass-based metrics provide natural quantification.
Figure 1: The three-phase gap analysis framework for solvent benchmarking
The initial phase of establishing an effective internal benchmarking program for solvent selection requires clear, measurable goals aligned with organizational green chemistry objectives [83]. For pharmaceutical development teams focusing on PMI reduction, this typically involves:
Once objectives are established, the next critical step is selecting key performance metrics that directly align with these goals [83]. For solvent selection guides, the American Productivity and Quality Center's The Benchmarking Management Guide suggests core competencies should impact business measures including quality, asset utilization, and capacity [84]. The following table summarizes essential metrics for solvent benchmarking:
Table 1: Key Performance Metrics for Solvent Benchmarking
| Metric Category | Specific Metric | Measurement Method | Target Value |
|---|---|---|---|
| Process Efficiency | Process Mass Intensity (PMI) | Total mass in process/mass of API | <40 kg/kg |
| Solvent Intensity | Total solvent mass/mass of API | <30 kg/kg | |
| Environmental | Wastewater Generation | Volume per kg API | Minimize |
| Volatile Organic Compound Emissions | Mass per kg API | <0.5 kg/kg | |
| Economic | Solvent Cost Index | Cost relative to benchmark solvent | <1.2 |
| Recovery Efficiency | % solvent recovered and reused | >80% | |
| HSE Performance | Carcinogenic/Mutagenic/Reprotoxic (CMR) Usage | Binary (Y/N) | Eliminate |
| Flammability Score | NFPA rating | <3 |
Data serves as the cornerstone of any benchmarking process [83]. For solvent selection benchmarking, collecting comprehensive data on chosen subjects requires both standardized experimental protocols and systematic data management practices.
Purpose: To quantitatively evaluate alternative green solvents against established benchmarks for specific synthetic transformations.
Materials and Equipment:
Procedure:
Alternative Solvent Screening:
Performance Analysis:
Data Recording:
Data Analysis:
This systematic approach to data collection ensures that comparisons between solvent systems are based on reproducible, quantitative metrics rather than subjective assessments. The emphasis on mass-based accounting directly supports PMI reduction goals while providing a foundation for continuous improvement.
The transition from data collection to implemented best practices represents the most critical phase of internal benchmarking. This process involves investigating top-performing teams or processes to understand what they are doing differently and how these practices can be adapted throughout the organization [83].
For solvent selection, this typically follows a structured workflow:
Figure 2: Implementation workflow for solvent best practices
The implementation plan should be approached systematically, with clear plans and timelines, and most importantly action owners for each improvement [83]. This phase often includes:
Establishing metrics to track the impact of these changes is equally important, with continuous monitoring allowing for adjustments and ensuring long-term success [83]. This monitoring should include regular reviews of solvent selection metrics, periodic reassessment of best practices, and mechanism for incorporating new green solvent technologies as they emerge.
The integration of predictive analytics represents the frontier of solvent benchmarking for lower PMI. Advanced tools now enable quantitative prediction of potential efficiencies centered around Process Mass Intensity of proposed synthetic routes prior to their evaluation in a laboratory [4]. This allows scientists to select the most efficient option prior to development and arrive at a holistically more sustainable chemical synthesis.
The Bristol Myers Squibb team, recipients of the 2024 Data Science & Modeling for Green Chemistry award, demonstrated this approach by combining a PMI prediction app that utilizes predictive analytics and historical data with Experimental Design via Bayesian optimization (EDBO/EDBO+) to accelerate the optimization of individual chemical transformations [4]. This powerful combination enables process scientists to incorporate state-of-the-art open-access data science tools and algorithms into both defining their overall project strategies and conducting their daily laboratory experimentation [4].
For the specific example included in their work, a process that yielded 70% yield and 91% ee through traditional one factor at a time (OFAT) using 500 experiments, was surpassed by the EDBO+ platform, providing 80% yield and 91% ee in only 24 experiments [4]. This dramatic improvement in experimental efficiency directly translates to reduced solvent consumption and lower PMI while accelerating process optimization.
Table 2: Key Research Reagent Solutions for Solvent Benchmarking
| Reagent/Solution | Function | Application Notes |
|---|---|---|
| Bio-based Solvents (e.g., dimethyl carbonate, limonene, ethyl lactate) | Low toxicity, biodegradable alternatives to conventional solvents [3] | Use for halogenated solvent replacement; ethyl lactate particularly effective for extraction processes |
| Deep Eutectic Solvents (DES) | Formed by hydrogen bond donors and acceptors; unique properties for chemical synthesis and extraction [3] | Customizable for specific applications; show promise for biotransformations and metal-catalyzed reactions |
| Supercritical COâ | Selective and efficient extraction of bioactive compounds with minimal ecosystem harm [3] | Requires specialized equipment; excellent for thermolabile compounds; leaves no solvent residues |
| Aqueous Solutions (acids, bases, alcohols) | Non-flammable, non-toxic substitutes for organic solvents [3] | Ideal for chromatography and recrystallization; may require additives for hydrophobic compounds |
| PMI Prediction Software | Predictive analytics for route selection prior to laboratory evaluation [4] | Utilizes historical data; enables greener-by-design synthesis planning |
| Bayesian Optimization Platforms (EDBO/EDBO+) | Machine learning approach to rapidly identify optimized reaction conditions [4] | Dramatically reduces experimental burden; open-source platforms available |
Establishing internal benchmarks and best practices for solvent selection represents a critical strategy for reducing PMI in pharmaceutical development. The systematic approach outlined in these application notesâfrom defining clear objectives and metrics to implementing data-driven best practicesâprovides a roadmap for continuous improvement in green chemistry performance. By leveraging internal benchmarking as a foundational practice, research organizations can not only accelerate their adoption of sustainable solvents but also build the core competencies necessary for long-term leadership in environmentally responsible pharmaceutical manufacturing. The integration of predictive tools like PMI applications and Bayesian optimization further enhances this capability, transforming solvent selection from a routine decision into a strategic advantage for sustainable drug development.
Strategic solvent selection is no longer a peripheral concern but a central pillar for achieving sustainable and economically viable drug development. By mastering the principles of green chemistry, leveraging powerful tools like the ACS GCI guides and PMI calculators, and adopting advanced optimization strategies, scientists can dramatically lower Process Mass Intensity. This not only reduces environmental impact and waste disposal costs but also streamlines manufacturing, mitigates regulatory risks, and builds a more resilient supply chain. The future of pharmaceutical manufacturing lies in the widespread adoption of these practices, further accelerated by emerging technologies like AI-powered process optimization and the development of next-generation, sustainable solvent platforms.