Exploring the Versatility and Sustainability of Hydroxypropyl Methylcellulose (HPMC) in Modern Chemical Industry
Abstract
1. Introduction
- HPMC characterization by reported analytical protocols and its classification.
- Raw materials and manufacturing.
- HPMC primarily in food, construction, and pharmaceuticals.
- Environmental impacts.
- Life cycle assessments considerations.
- Concluding thoughts and future directions.
2. Physicochemical Properties and Analytical Techniques for Hydroxypropyl Methylcellulose Characterization
2.1. Physicochemical Properties

2.1.1. Substitution and Viscosity Types
2.1.2. Thermal Gelation
2.1.3. Molecular Weight
2.1.4. Water Solubility
2.2. Analytical Techniques and Methodologies for Hydroxypropyl Methylcellulose Characterization
2.2.1. Scanning Electron Microscopy (SEM)
2.2.2. Transmission Electron Microscopy (TEM)
2.2.3. Fourier Transform Infrared Spectroscopy (FTIR)
2.2.4. Raman Spectroscopy
2.2.5. X-Ray Diffraction (XRD)
2.2.6. Nuclear Magnetic Resonance (NMR)
2.2.7. Differential Scanning Calorimetry (DSC)
2.2.8. Thermogravimetric Analysis (TGA)
2.2.9. Rheological Techniques
3. Classification of Hydroxypropyl Methylcellulose
3.1. Classification Based on the Substitution Degree
3.2. Classification Based on Viscosity
4. Raw Materials and Manufacturing Process
4.1. Raw Material Selection
4.2. Etherification Reaction
4.3. Purification and Washing
4.4. Particle Size Control
4.5. Blending and Formulation
4.6. Quality Control
4.6.1. Analytical Quantifications and Testing
4.6.2. Determination of the Substitution Pattern
4.6.3. Impurities Monitoring
4.7. Packaging and Storage
4.7.1. Packaging Materials
4.7.2. Storage Conditions
4.7.3. Shelf Life
5. Applications of Hydroxypropyl Methylcellulose
5.1. Construction Applications
5.2. Food Industry Applications
5.3. Pharmaceutical Application
5.4. Other Applications
6. Environmental Impact of Hydroxypropyl Methylcellulose and Life Cycle
6.1. Main Environmental Impacts
6.2. Life Cycle Assessment (LCA) and Environmental Product Declarations (EPD)
7. Conclusions
- Deeper understanding of the relationships between substitution patterns, molecular architecture, and end-use performances.
- More standardized comparisons among commercial HPMC grades to ensure predictability in formulations.
- Improved knowledge of processing–structure–property relationships across different industrial contexts.
- Sustainability metrics, greener production routes, and comprehensive life cycle assessments.
- Advanced applications of HPMC in functional materials, active packaging, controlled release systems, and sustainable formulations.
Supplementary Materials
Author Contributions
Funding
Institutional Review Board Statement
Data Availability Statement
Conflicts of Interest
References
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| USP | Grade | Viscosity (cP) | Methoxy (%) | Hydroxypropyl (%) | Properties | Construction | Food | Pharma |
|---|---|---|---|---|---|---|---|---|
| 2910 | E 3 Premium LV | 3 | 28–30 | 7–12 | Low viscosity, fast hydration, clear solution | Tile adhesives, wall putty, cement renders | Food emulsifier, stabilizer | Tablet film coating, binder |
| 2910 | E 5 Premium LV | 5 | 28–30 | 7–12 | Low viscosity, easily dispersible | Paints, plasters, joint fillers | Bakery product texture, sauce thickener | Tablet film coating, binder |
| 2910 | E 6 Premium LV | 6 | 28–30 | 7–12 | Low–medium viscosity, stabilizer | Gypsum and cement plasters, renders | Dairy dessert stabilizer, ice cream | Sustained-release agent, granulation binder |
| 2910 | E 15 Premium LV | 15 | 28–30 | 7–12 | Moderate viscosity, good film-former | Wall skim coat, repair mortars, putty | Dairy thickener, cream stabilizer | Film coating, capsule production |
| 2910 | E 50 Premium LV | 50 | 28–30 | 7–12 | Moderate viscosity, thickening and binding | Cement renders, mortars, adhesives | Food sauce and soup thickener | Sustained-release matrix, film coating |
| 2910 | E 4M Premium | 4000 | 28–30 | 7–12 | High viscosity, gel forming, water retention | Tile adhesives, EIFS, self-leveling compounds | Bread improver, texture modifier | Controlled-release agent, matrix design |
| 2910 | E 4M Premium CR | 4000 | 28–30 | 7–12 | High viscosity, controlled rheology | Tile adhesives, repair mortars | Meat binder, emulsifier | Modified release coatings, hydrophilic matrix |
| 2910 | E 10M Premium CR | 10,000 | 28–30 | 7–12 | Very high viscosity, gel structure | Self-leveling compounds, tile adhesives | Gel desserts, food thickeners | Extended-release matrices |
| 2906 | F 4M Premium | 4000 | 27–30 | 4–7.5 | High viscosity, lower hydroxypropyl | Plaster and putty improvement | Frozen dough stabilizer, emulsifier | Binder in direct compression, film coating |
| 2208 | K 3 Premium LV | 3 | 19–24 | 4–12 | Low viscosity, good solubility | Self-level flooring, sprayable mortars | Fat replacer, beverage clouding agent | Artificial tears, ophthalmic lubricants |
| 2208 | K 100 Premium LV | 100 | 19–24 | 4–12 | Medium viscosity, effective thickener | Cement tile adhesives, grout, putty | Ice cream stabilizer and thickener | Tablet binder, controlled release |
| 2208 | K 100 Premium LV CR | 100 | 19–24 | 4–12 | Medium viscosity, controlled rheology | Skim coat mortar, brick mortars | Food suspending agent, beverage stabilizer | Controlled-release matrix, film formation |
| 2208 | K 100 Premium LV LH | 100 | 19–24 | 4–12 | Medium viscosity, low hydroxypropyl | Smoothing compounds, repair mortars | Milk and cream foaming agent | Sustained-release matrix, capsule coating |
| 2208 | K 100 Premium LV LH CR | 100 | 19–24 | 4–12 | Medium viscosity, slow-release properties | Leveling compounds, masonry mortars | Emulsifier and extender in foods | Extended-release agent, oral suspensions |
| 2208 | K 4M Premium | 4000 | 19–24 | 4–12 | High viscosity, excellent water retention | Mortars, grouts, tile adhesives | Frozen dessert stabilizer, bread dough enhancer | Hydrophilic matrix, binder in tablets |
| 2208 | K 4M Premium CR | 4000 | 19–24 | 4–12 | High viscosity, controlled rheology | Repair mortars, high thixotropy adhesives | Meat product binder, processed food thickener | Controlled-release, matrix for osmotic tablets |
| 2208 | K 15M Premium | 15,000 | 19–24 | 4–12 | Very high viscosity, strong thickener | Joint compounds, thick render pastes | Dough improver for bakery applications | Modified-release tablet cores, binder |
| 2208 | K 15M Premium CR | 15,000 | 19–24 | 4–12 | Very high viscosity, controlled release | Tile adhesives, grouting | Emulsifier and texturizer in processed foods | Matrix agent for extended-release tablets |
| 2208 | K 100M Premium | 100,000 | 19–24 | 4–12 | Ultra-high viscosity, highly water-retentive | Highly thixotropic plasters, adhesives | Food gelling agent, dessert gels | Hydrophilic matrix, texturizer for pharmaceuticals |
| 2208 | K 100M Premium CR | 100,000 | 19–24 | 4–12 | Ultra-high viscosity, modified rheology | Grout and mortar additives, repair mortars | Food texture modifier, stabilizer in gels | Controlled-release matrix, capsule gelling agent |
| Stage | Purpose | Inputs | Key Process Controls | Output | Main Quality Risks |
|---|---|---|---|---|---|
Raw Material Selection![]() | Selection of cellulose source and confirmation of purity for consistent reactivity and final performance | Cotton linters or wood pulp; incoming specs/CoA | Source qualification; impurity limits (lignin/hemicellulose/ash); incoming QC | Qualified cellulose feedstock | Variability in starting cellulose affects DS/MW and downstream reproducibility |
Etherification Reaction![]() | Chemical modification of cellulose to introduce methoxy and hydroxypropyl substituents (HPMC formation) | NaOH/KOH (alkalization); methyl chloride; propylene oxide | Temperature, pressure, pH (alkaline), time; in-process sampling (DSMe, MSHP, MW) | Etherified HPMC reaction mass | Under-/over-substitution; degradation/crosslinking; residual reagents/by-products |
Removal of Impurities (Purification and Washing)![]() | Removal of soluble residues, salts, catalysts, residual reagents, and low-MW by-products; conditioning | Water; possible alcohols (ethanol/isopropanol); pH adjustment agents (as needed) | Washing cycles; solid–liquid separation efficiency; pH/conductivity; residuals tracking | Purified wet HPMC cake | Insufficient washing → residual solvents/salts; product losses; inconsistent purity |
Filtration and Drying![]() | Separation from wash liquor and controlled drying to stable powder/granules | Filtration aids (if used); drying air/energy | Filtration mode (vacuum/pressure/centrifuge); drying temperature/time; residual moisture/solvent | Dried HPMC | Over-drying/thermal stress; residual moisture → clumping/instability |
Particle Size Control![]() | Milling and classification to meet target PSD and handling/performance | Dried HPMC; milling/sieving equipment | Milling parameters (speed/feed/time/heat); sieve cuts; PSD testing (laser diffraction/microscopy) | HPMC with specified particle size distribution | Too fine → dusting; too coarse → slow hydration; PSD variability affects performance |
Blending and Formulation![]() | Homogenization and tailoring (when applicable) to meet application specs | HPMC + excipients/additives/actives (as relevant) | Mixing time/speed/order; blend uniformity; DoE-based optimization (as needed) | Homogeneous blend/formulated product | Segregation; inconsistent functionality; interaction effects (e.g., viscosity/release) |
Quality Control![]() | Analytical verification of identity, substitution pattern, impurities, and performance attributes | QC methods (IR, NMR, GC/HPLC, rheology, DSC, XRD, PSD, microbiology, ICP-MS) | Release specs: DSMe/MSHP, viscosity, MW, residual solvents, metals, microbes, moisture, etc. | Released batch (compliant) | Non-compliance with pharmacopeias/food regs; batch-to-batch drift |
| Packaging and Storage | Protection from moisture/contamination; stability through shelf life | Moisture barrier packs (bags/drums/liners); labels | RH/temperature control; sealing integrity; FIFO; stability checks | Packaged HPMC with defined shelf life | Moisture uptake → caking/property changes; contamination; label/traceability issues |
| Key Observations | Sector | Research Gaps and Challenges |
|---|---|---|
| General |
|
| Construction |
|
| Food |
|
| Pharma |
|
| Other |
|
| Parameter/Degree of Substitution | Low DSMe/Low MSHP | High DSMe/Low MSHP | Low DSMe/High MSHP | High DSMe/High MSHP | General Remarks |
|---|---|---|---|---|---|
| Substituent Groups | Few methoxy, few hydroxypropyl | Many methoxy, few hydroxypropyl | Few methoxy, many hydroxypropyl | Many methoxy, many hydroxypropyl | DSMe—methoxy degree of substitution (typical 1.3–2.1); MSHP—hydroxypropyl molar (typical 0.1–1.0) |
| Viscosity | Low | Medium | Medium | High | Increases with MW and substitution; commercial grades of 3–100,000 cP |
| Thermal Gelation | High gelation temperature | Low gelation temperature. | Medium gelation temperature. | Low gelation temperature. | Higher DSMe and lower MSHP = lower gelation temperature |
| Water Solubility | High | Medium | Very high | Medium | Higher MSHP/DSMe favors solubility; low viscosity = higher solubility |
| Organic Solubility | Very low | Very low | Very low | Very low | Insoluble in acetone, chloroform, etc. |
| Applications | Fast drug release, coatings | Controlled-release matrices, ophthalmic gels | Hydrophilic matrices, food, cosmetics | Sustained-release systems, adhesives | Viscosity and gelation determine use in pharma, food, cosmetics |
| Environmental Impact | Biodegradable, low impact | Biodegradable, low impact | Biodegradable, low impact | Biodegradable, low impact | Cellulose-derived, non-toxic, low environmental risk |
| Life-Cycle Stage | Description | Environmental Impact/Remarks |
|---|---|---|
| Raw Material Extraction | Cellulose source: the main raw material for HPMC is cellulose, typically derived from cotton or wood. | Impacts: deforestation, energy consumption, and emissions from harvesting and processing cellulose. |
| Production | Chemical processing: HPMC production involves chemical reactions, including etherification. | Impacts: use of chemicals and energy, with significant emissions. |
| Energy use: the manufacturing process is energy intensive. | Impacts: contribution to greenhouse gas emissions. | |
| Transport | Logistics: the transport of raw materials to the production plant and the distribution of the final product to consumers. | Impacts: fuel consumption and emissions associated with transportation. |
| Use | Application: in its various applications, HPMC generally has a low environmental impact. | Note: specific use may influence the overall environmental footprint. |
| End of Life | Disposal: the biodegradability of HPMC is a positive factor, but disposal methods (landfill, incineration) can generate impacts. | Impacts: depending on the disposal method, environmental effects may occur. |
| Sustainability efforts: companies aim to reduce environmental impact by improving energy efficiency, using sustainable raw materials, and optimizing processes. | Note: growing trend towards sustainability in HPMC production. | |
| Regulatory compliance: complying with environmental regulations and standards is essential to minimize the ecological footprint. | Note: regulatory compliance helps to reduce the environmental impact of HPMC production. |
| Indicator | Unit | Upstream | Core | Downstream | Total |
|---|---|---|---|---|---|
| Global Warming Potential (total) | kg CO2 | 3.75 | 4.81 | 2.35 | 10.9 |
| GWP—Fossil | kg CO2 | 6.06 | 4.78 | 0.349 | 11.2 |
| GWP—Biogenic | kg CO2 | −2.31 | 0.0287 | 2.00 | −0.286 |
| GWP—LULUC | kg CO2 | 0.00493 | 0.00135 | 0.000181 | 0.00647 |
| Ozone Depletion Potential (ODP) | kg CFC11 | 3.77 × 10−5 | 3.39 × 10−8 | 4.75 × 10−9 | 3.77 × 10−5 |
| Acidification Potential (AP) | mol H+ | 0.0591 | 0.0211 | 0.00148 | 0.0816 |
| Eutrophication (freshwater, EP) | kg P | 0.0105 | 0.000755 | 0.0000297 | 0.0113 |
| Eutrophication (marine, EP) | kg N | 0.0697 | 0.00438 | 0.00229 | 0.0764 |
| Eutrophication (terrestrial, EP) | mol N | 0.182 | 0.0434 | 0.00529 | 0.231 |
| Photochemical Ozone Creation (POCP) | kg NMVOC | 0.0258 | 0.0136 | 0.00235 | 0.0417 |
| Abiotic Depletion—Minerals/Metals (ADP-M&M) | kg Sb | 2.39 × 10−5 | 2.30 × 10−6 | 1.04 × 10−6 | 2.72 × 10−5 |
| Abiotic Depletion—Fossil (ADP-fossil) | MJ | 75.5 | 51.3 | 4.32 | 131 |
| Water Deprivation Potential (WDP) | m3 | 2.63 | −1.24 | 0.0297 | 1.42 |
| Renewable Primary Energy (PERE) | MJ | 0 | 1.04 | 0.0345 | 1.07 |
| Renewable Mat. Energy (PERM) | MJ | 28.8 | 0 | 0 | 28.8 |
| Non-Renewable Primary Energy (PENRT) | MJ | 75.5 | 51.3 | 4.32 | 131 |
| Net Freshwater Use (FW) | m3 | 0 | 0.011 | 0 | 0.011 |
| Hazardous Waste Disposed (HWD) | kg | 0 | 0.00395 | 0 | 0.00395 |
| Non-Hazardous Waste Disposed (NHWD) | kg | 0 | 0.417 | 1.00 | 1.42 |
| Radioactive Waste Disposed (RWD) | kg | 0 | 0 | 0 | 0 |
| Particulate Matter (PM) | disease inc. | 7.00 × 10−7 | 2.87 × 10−7 | 2.42 × 10−8 | 1.01 × 10−6 |
| Ionizing Radiation (IRP) | kBq U235 | 0.264 | 0.0965 | 0.00511 | 0.366 |
| Ecotoxicity—Freshwater (ETP-fw) | CTUe | 179 | 29.5 | 6.68 | 216 |
| Human Toxicity—Cancer (ETP-c) | CTUh | 2.79 × 10−10 | 1.01 × 10−10 | 1.51 × 10−10 | 1.44 × 10−9 |
| Human Toxicity—Non-Cancer (HTP-nc) | CTUh | −9.31 × 10−8 | 3.36 × 10−8 | 6.21 × 10−9 | −5.33 × 10−8 |
| Land Use/Soil Quality (SQP) | dimensionless | 548 | 7.55 | 2.80 | 558 |
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Matilla, S.; Mudhoo, A.; Díez, C.; Otero, M. Exploring the Versatility and Sustainability of Hydroxypropyl Methylcellulose (HPMC) in Modern Chemical Industry. Polymers 2026, 18, 1105. https://doi.org/10.3390/polym18091105
Matilla S, Mudhoo A, Díez C, Otero M. Exploring the Versatility and Sustainability of Hydroxypropyl Methylcellulose (HPMC) in Modern Chemical Industry. Polymers. 2026; 18(9):1105. https://doi.org/10.3390/polym18091105
Chicago/Turabian StyleMatilla, Sonia, Ackmez Mudhoo, Carlos Díez, and Marta Otero. 2026. "Exploring the Versatility and Sustainability of Hydroxypropyl Methylcellulose (HPMC) in Modern Chemical Industry" Polymers 18, no. 9: 1105. https://doi.org/10.3390/polym18091105
APA StyleMatilla, S., Mudhoo, A., Díez, C., & Otero, M. (2026). Exploring the Versatility and Sustainability of Hydroxypropyl Methylcellulose (HPMC) in Modern Chemical Industry. Polymers, 18(9), 1105. https://doi.org/10.3390/polym18091105


