Products
| HS Code | 321696 |
| Chemical Name | Isopropyl Alcohol (2-Propanol) |
| Cas Number | 67-63-0 |
| Molecular Formula | C3H8O |
| Molecular Weight | 60.10 g/mol |
| Purity | ≥99.8% (typical) |
| Grade | ACS / HPLC / Laboratory Grade |
| Appearance | Clear, colorless liquid |
| Odor | Characteristic alcohol-like, sharp odor |
| Solubility | Miscible with water, ethanol, ether and most organic solvents |
| Boiling Point | 82.5 °C (at 760 mmHg) |
| Melting Point | -89 °C |
| Flash Point | 11.7 °C (closed cup) |
| Density | 0.786 g/cm³ (at 20 °C) |
| Refractive Index | 1.377 (at 20 °C) |
| Vapor Pressure | 33 mmHg (at 20 °C) |
As an accredited Merck Isopropyl Alcohol IPA, 2-Propanol at Affordable Prices factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Secure packaging includes a 1 L bottle of high-purity Merck Isopropyl Alcohol (IPA, 2-Propanol), ensuring safe handling and affordable value. |
| Container Loading (20′ FCL) | 20′ FCL loading of Merck Isopropyl Alcohol IPA (2-Propanol) — safely packed for transport, delivered in bulk at affordable prices. |
| Shipping | We offer reliable, affordable shipping for Merck Isopropyl Alcohol (IPA). Your order is securely packaged in compliant containers, ensuring safe transit. Standard delivery typically takes 3-5 business days, with expedited options available. Proper handling and documentation guarantee your high-quality solvent arrives safely and on time. |
| Storage | Store Merck Isopropyl Alcohol (IPA, 2-Propanol) in a cool, dry, well-ventilated area away from heat, sparks, and open flames. Keep containers tightly sealed to prevent evaporation and contamination. Avoid direct sunlight and incompatible oxidizers. Ensure proper grounding for dispensing. Despite its affordable price, maintain strict safety protocols for this flammable solvent. |
| Shelf Life | Shelf life is typically 3–5 years if stored tightly sealed, away from heat, flames, and sunlight. |
The use of a 70% v/v isopropanol dilution in a Grade C or Grade D pharmaceutical controlled environment is not determined by solvency alone. It is determined by water activity and the residence time of a continuous liquid film on the target surface. At 70% v/v, the mixture contains enough water to swell the peptidoglycan matrix of vegetative bacteria and allow alcohol penetration into the cell membrane. At 99% w/w, the solvent film evaporates before critical protein denaturation and membrane disruption are complete. A stainless-steel AISI 316L worktable is therefore wiped with a sterile polyester nonwoven impregnated with 70% v/v IPA and allowed to remain visibly wet for a defined contact period.
Wet-contact times are not carried over from supplier literature. They are generated through a surface test based on EN 13697 using a panel of vegetative organisms that normally includes Staphylococcus aureus ATCC 6538, Pseudomonas aeruginosa ATCC 15442, Enterococcus hirae ATCC 10541, Escherichia coli K12 NCTC 10538, and Candida albicans ATCC 10231. For a claimed contact time of 30 s, the test organism must show a logarithmic reduction of at least 4 log10 under a defined interfering-soil load. If the site claim is extended to 60 s or 2 min, the same reduction must be demonstrated at the longest allowable interval under the cleanroom’s surface-conditioning protocol.
The diluent used to prepare 70% v/v IPA is USP Purified Water, not municipal tap water. Calcium, magnesium, chloride, and sulfate ions present in hard water generate white drying films on stainless steel and can block the trigger sprayer of a gamma-irradiated IPA bottle. After drying, the surface is usually checked visually under defined lighting and by conductivity swab sampling. For an aseptic transfer isolator surface, the wipe is moved in a linear overlapping pattern from cleanest to dirtiest zone, and the number of wipes per square metre is fixed in the batch record. A single wipe is not used to clean more than one isolator panel to avoid cross-transfer of residual spores.
The operational boundary is sharp. Isopropanol is not sporicidal. It does not meet the performance requirements of EN 17126 for Clostridioides difficile or Bacillus subtilis spores. Disinfectant rotation with a sporicidal agent such as 6% hydrogen peroxide/peracetic acid is mandatory where spore control is required. The bottle label must state the final concentration, the date of dilution, the diluent type, and the expiry date because repeated opening of a flip-top cap changes water content by preferential evaporation and can reduce the mixture below the validated concentration.
No uniform header follows for the next application. The technical context is introduced directly from the production line.
On a mixed-surface SMT line, solder paste residues from SAC305 no-clean flux are removed manually with 99.5% w/w isopropanol applied through an ESD-safe LDPE wash bottle. The board is angled at 30° to 60° to allow gravity drainage away from connectors. A short-bristle brush or polyester-tipped swab is used beneath low-standoff QFN packages with a 0.4 mm pitch. The surface tension of isopropanol is approximately 21.7 mN/m at 20°C, compared with 72.8 mN/m for water. This difference permits penetration into capillary gaps below 0402 resistor bodies where aqueous cleaners would remain trapped and later cause electrochemical migration.
For manual cleaning, the non-volatile residue limit of the solvent is usually specified by the solder paste supplier and is commonly controlled below 50 µg/cm² of exposed board area after evaporation. The cleaned board is tested for residual ion contamination by resistivity of solvent extract according to IPC TM-650 2.3.25. Halide contamination is measured by ion chromatography according to IPC TM-650 2.3.28 because residual chloride or bromide ions are directly associated with leakage-current failure modes on biased assemblies. High-purity IPA used for this work normally contains chloride below 1 mg/kg and sulfate below 1 mg/kg. The solvent is filtered through a 0.2 µm membrane before it is loaded into the dispenser bottle. Automatic under-stencil wiping on the printer uses a two-cycle spray-and-wipe sequence with 99% w/w IPA and a solvent-refreshed woven wipe roll.
Compatibility must be checked before production. Isopropanol softens some screen-printed solder mask legends and can stain cellulose-based label stock. Natural rubber, butyl rubber, and neoprene are unsuitable for prolonged glove contact. Nitrile gloves used for IPA wiping should have a permeation breakthrough time of at least 30 min under EN 16523-1 testing. The area is ventilated to keep vapour concentration below 25% of the lower explosion limit, because the closed-cup flash point of pure isopropanol is 12°C and the LEL is 2.0% v/v.
Shellac is dissolved in 99% w/w isopropanol at a concentration of 20% w/w for a barrier coat applied by reverse-gravure coater to nitrocellulose-treated paper. The dissolving vessel is a closed stainless-steel stirred tank fitted with a reflux condenser because the vapour pressure of IPA at 20°C is 4.4 kPa and the closed-cup flash point is 12°C. The batch is mixed for 45 min at 300 rpm, filtered through a 10 µm bag filter, and then transferred to the coating pan. The dry coating weight is set at 5–8 g/m². The terminal article is a food-contact printed tissue in which the shellac layer functions as an oxygen and grease barrier.
The Hansen solubility parameters of isopropanol are δD = 15.8 MPa¹/², δP = 6.1 MPa¹/², and δH = 16.4 MPa¹/². These values explain its compatibility with nitrocellulose, polyamide, and acrylic resin systems at low addition levels. Viscosity adjustment on a gravure line is performed by adding 0.5–2.0% by mass of IPA to the press-ready ink. Flow time is verified with a 4 mm ISO 2431 cup at 25°C. The target efflux time is ink-specific and is typically fixed in the converter’s incoming-material specification, not the solvent supplier’s certificate. As the doctor blade removes solvent from the cylinder, solids build in the sump within 10 min; the refresh rate is therefore set at 1–2% of sump volume per hour.
When relative humidity exceeds 70%, the latent heat of vaporization of approximately 664 kJ/kg cools the film below the dew point. The result is blushing, pinholing, and loss of adhesion on the printed substrate. The press-room dew-point separation should be maintained at not less than 5°C from the surface temperature. If the room dew point cannot be controlled, a slower solvent such as n-propyl acetate or ethanol is blended with IPA to reduce the evaporation rate. The printed article is tested for residual solvent by headspace gas chromatography and for overall migration under EU Regulation 10/2011 where food-contact status is claimed. IPA is not the limiting solvent in most converted films, but its odour threshold may require a sensory panel evaluation before the reel is released.
In a cGMP wet granulation train, isopropanol is selected as a binder solvent for a moisture-sensitive active pharmaceutical ingredient because water would initiate hydrolysis of the ester side chain. The binder solution is prepared by dissolving povidone K30 in IPA at a concentration of 5% w/w in a jacketed stainless-steel vessel at 35°C. The solution is sprayed onto a fluid-bed granulator with an inlet air temperature of 45°C and a product temperature of 23–27°C. The exhaust air is kept above the lower explosion limit by maintaining 25% of LEL as the alarm setpoint. The granulation is dried at 50°C under 30–40 mbar until loss on drying is below 1.5%.
Residual solvent control follows ICH Q3C. Isopropanol is classified as a Class 3 residual solvent with a permitted daily exposure of 50 mg/day and a concentration limit in the finished drug product of 5000 ppm (0.5%). The release method is headspace gas chromatography according to USP <467> Procedure A. If the daily dose exceeds 10 g or the product is intended for paediatric use, ICH Q3C Options 2 or 3 are applied to sum all Class 3 solvents. The analytical laboratory calibrates the headspace method with IPA-spiked placebo at three levels, and the method is validated for specificity, linearity, and recovery before batch release.
Recrystallization is another downstream operation in which IPA functions as both solvent and anti-solvent. A crude API is dissolved in 5 volumes of hot IPA at 70–75°C, clarified through a 0.45 µm PTFE membrane, and cooled to 0°C over 4 h at a ramp rate of 0.3°C/min. The product is collected on a Büchner filter and washed with 1 volume of chilled IPA. The crystals are dried in a vacuum tray dryer at 40°C and 20 mbar for 12 h. The final product is tested by XRPD to confirm that the polymorphic form is unchanged and that no hydrate has formed during solvent contact.
Isopropanol must not be mixed with strong oxidizers. Concentrated nitric acid above 55% and hydrogen peroxide above 50% can generate exothermic decomposition and organic peroxide detonation. Storage in glass or HDPE containers at 15–25°C under nitrogen is required to limit peroxide accumulation. A peroxide test strip is used when the solvent is stored beyond its opening date or when it is exposed to air and UV light.
Botanical actives intended for leave-on emulsions are extracted with a binary solvent containing 40% v/v isopropanol and 60% v/v deionized water at 60°C for 3 h. The solvent-to-plant ratio is maintained at 10:1 v/w in a pneumatically stirred glass-lined extractor. Isopropanol is selected over ethanol when the target actives are medium-polar flavonoids and triterpenoids and when the extractor is not equipped for the higher vapour flow of an ethanol recovery system. The extract is cooled, filtered through a 5 µm depth filter, and concentrated on a rising-film evaporator at 200 mbar and 55°C.
The resulting native extract is dispensed into a glycerin/water matrix or into a preservative-free emulsion base. The residual IPA is controlled by process validation because the finished cosmetic product must meet the safety requirements of EU Regulation 1223/2009 and the product-specific Cosmetic Product Safety Report. IPA is permitted as a solvent and denaturant in cosmetic formulae, but the safety assessor must justify the residual level in the final leave-on product. Published data for a specific botanical matrix and extraction configuration may be limited if the plant source is not covered by a published safety dossier; in that case the manufacturer must generate a matrix-specific recovery study.
The equipment boundary for this application is important. IPA is not suitable for heat-sensitive anthocyanins because the 60°C maceration temperature accelerates glycoside hydrolysis. Ethanol at 40°C or supercritical carbon dioxide is preferred for that class of pigments. The extractor must be blanketed with nitrogen when the plant material contains naturally occurring metal ions or when the solvent is recovered and reused for multiple batches. The recovered solvent is dried over molecular sieve 3A and reanalyzed for density, refractive index, and water content before reuse.
High-purity isopropanol is used as a water-displacing agent in fibre-optic tube cleaning and connector end-face preparation. The water-displacement action is based on the low-boiling heterogeneous azeotrope with water: 87.7% w/w isopropanol and 12.3% w/w water distill at 80.37°C at 101.3 kPa. This property allows a small volume of IPA to remove adsorbed water from a ceramic ferrule tip without leaving an aqueous residue. The connector end-face is cleaned with 99.9% w/w IPA on a foam-tipped swab, followed by dry compressed air filtered to 0.3 µm. The cleaned assembly is inspected with a 200× or 400× optical microscope, and reflection and insertion loss are measured according to IEC 61300-3-35.
Compatibility is not assumed. Polycarbonate optical housings and acrylic light guides can stress-craze when exposed to liquid IPA for more than a few minutes. The cleaning protocol must restrict liquid contact to the ceramic ferrule and glass fibre. Plastic components are wiped with dry polyester or cleaned with a 50% v/v aqueous IPA solution only after a witness-coupon test. For antireflection-coated lenses, IPA can attack the edges of some magnesium fluoride overcoat layers. A solvent compatibility test is performed on a witness coupon according to ISO 9211-1 before the cleaning procedure is released to production.
Static discharge is a separate hazard. The closed-cup flash point of pure isopropanol is 12°C when measured by ASTM D56. Fibre-optic cleaning stations therefore use local exhaust ventilation with a capture velocity of at least 0.5 m/s. The solvent is stored in 1 L LDPE squeeze bottles with pressure-relief caps. The optical bench must meet IEC 61340-5-1 grounding requirements because a static discharge from a synthetic swab can ignite IPA vapour at room temperature. The worksurface-to-ground resistance is maintained in the ESD range of 10⁶ Ω to 10⁹ Ω, and the operator wears a grounded wrist strap.
The vapour-phase drying method is terminated when the inspection microscope shows no residual film or water staining on the fibre stub. The final cleaned connector is inserted into a dry mating sleeve and covered with a dust cap before the next assembly step.
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Merck Isopropyl Alcohol IPA, 2-Propanol is supplied as a clear, colourless, hygroscopic secondary alcohol with CAS 67-63-0, molecular formula C₃H₈O, and molecular weight 60.10 g/mol. The affordable-price positioning is implemented through grade-tiered release testing and packaging formats rather than by dilution or alteration of the base solvent. The product line comprises the EMPLURA® general-use grade, the EMSURE® ACS,ISO,Reag. Ph Eur grade, and the LiChrosolv® liquid-chromatography grade. For high-volume wiping, rinsing, and bulk-transfer operations, the certificate of analysis is limited to assay by gas chromatography, water content, evaporation residue, and acidity or alkalinity. Pharmacopoeial-grade material carries additional release tests for aldehydes and ketones, reducing substances, and UV transmittance. This stratification does not change the secondary alcohol backbone; the unit-cost difference is controlled by analytical release burden, packaging cleanliness, and documentary support.
Packaging is supplied in glass and high-density polyethylene containers from 1 L to 200 L. The material is classified under UN 1219 for transport and is stored in grounded flammable-liquid storage with local exhaust. The lower explosion limit is 2.0 vol% and the upper explosion limit is 12.7 vol%. Occupational exposure is controlled to the OSHA 29 CFR 1910.1000 Table Z-1 8-hour time-weighted average of 400 ppm for general industry. Process ventilation is designed to maintain measured vapour concentration below 20% of the lower explosion limit, with continuous monitoring in areas containing open solvent reservoirs.
The EMPLURA grade is positioned for production-scale washing, rinsing, and solvent-transfer operations where trace-metal certification and full pharmacopoeial documentary support are not required. Published grade-comparison certificates list assay by gas chromatography at ≥99.5 area% for EMPLURA and ≥99.9 area% for EMSURE ACS,ISO,Reag. Ph Eur. Water content is controlled to ≤0.1% for EMPLURA and ≤0.05% for the high-purity grade. Evaporation residue is specified at ≤0.005 wt% for EMPLURA and ≤0.002 wt% for EMSURE. These residue values translate directly to the maximum non-volatile film mass remaining after solvent removal and therefore distinguish suitability for residue-sensitive optical, analytical, and microelectronic cleaning.
Acidity and alkalinity are controlled as pass-for-purpose limits. The EMSURE grade is released against the current ACS reagent monograph, ISO 6353-2:1983 R87, and the European Pharmacopoeia 2-propanol monograph. The LiChrosolv grade is controlled for UV transmittance and baseline noise in liquid chromatography, with specified transmittance minima at 210 nm, 220 nm, and 245 nm. The cost difference between EMPLURA and EMSURE is therefore not derived from a different solvent structure but from the number of release tests, the documentary format, and the packaging cleanliness level.
| Grade | Release basis | Typical assay | Water | Evaporation residue |
|---|---|---|---|---|
| EMPLURA | Internal release; no pharmacopoeial claim | ≥99.5 area% | ≤0.1% | ≤0.005 wt% |
| EMSURE | ACS reagent, ISO 6353-2:1983 R87, Ph Eur 2-propanol | ≥99.9 area% | ≤0.05% | ≤0.002 wt% |
| LiChrosolv | HPLC UV transmittance, gradient elution, low residue | ≥99.9 area% | ≤0.05% | ≤0.002 wt% |
EMPLURA grade is not specified for UV-transmittance-sensitive liquid chromatography below 245 nm. Trace UV-absorbing impurities in general-use IPA can produce baseline drift and quantitation error in reversed-phase methods when UV detection is used at short wavelengths. The LiChrosolv grade is specified for gradient elution with UV detection; its release sheet includes transmittance minima at 210 nm, 220 nm, and 245 nm and a fluorescence suitability test. For isocratic methods using refractive-index or evaporative-light-scattering detection, EMPLURA may be used after filtration through a 0.2 µm PTFE membrane. This distinction is the principal operational boundary between general-use and chromatography-grade 2-propanol in analytical laboratories.
The following physical-property set applies to the ≥99.5 area% material and defines operational limits for transfer, drying, and explosion protection.
| Property | Value | Condition / Reference Method |
|---|---|---|
| Density | 0.785–0.789 g/cm³ | 20°C; ASTM D4052 |
| Boiling point | 82.4°C | 101.3 kPa |
| Flash point | 12°C | closed cup; ASTM D56 |
| Autoignition temperature | 399°C | ASTM E659 |
| Vapour pressure | 4.4 kPa | 20°C |
| Dynamic viscosity | 2.04 mPa·s | 25°C |
| Surface tension | 21.7 mN/m | 25°C |
| Refractive index | 1.376–1.378 | 20°C |
| Water azeotrope | 87.7 wt% IPA; bp 80.4°C | 101.3 kPa |
Residual film formation after IPA evaporation is governed primarily by the non-volatile residue specification. For EMPLURA grade at ≤0.005 wt%, a 100 g solvent load contains a maximum of 0.005 g of non-volatile material; for EMSURE grade the corresponding maximum is 0.002 g. Surface haze after evaporation is also influenced by extraction of wiper binders, packaging additives, and container closure systems. Low surface tension of 21.7 mN/m at 25°C supports wetting of low-energy substrates, while the viscosity of 2.04 mPa·s permits capillary penetration into narrow apertures. Drying time is not a universal cleanroom parameter because evaporative flux depends on air velocity, temperature, solvent loading, and ambient dew point. Published drying-time data for production cleanroom wiper substrates is limited; gravimetric drying curves should be generated on the target wiper material under the specified airflow regime, and surface cleanliness should be confirmed by dark-field inspection or ion-chromatographic extraction of ionic residues.
In diluted 70 vol% IPA/water mixtures, the solvent is used for removal of polar process soils and for controlled-environment surface sanitisation. The 87.7 wt% isopropanol–water azeotrope boils at 80.4°C at 101.3 kPa, which constrains distillation-based recovery: continuous solvent recycling units must be designed for azeotropic overhead composition rather than anhydrous distillate. In ultrasonic baths operating at 40 kHz, cavitation intensity is influenced by the vapour pressure of 4.4 kPa at 20°C and the surface tension of 21.7 mN/m; elevated bath temperature reduces viscosity but increases flammable vapour release. Cleaning-cycle qualification should use controlled rosin-flux coupons and post-wash ionic analysis by IPC-TM-650 method 2.3.28 rather than visual inspection alone.
Ethanol exhibits a vapour pressure of 5.8 kPa at 20°C and a boiling point of 78.4°C; 2-propanol exhibits 4.4 kPa and 82.4°C. Under identical airflow, IPA-wetted surfaces therefore retain liquid slightly longer, which can improve contact time for rosin-based flux residues but extends drying time. IPA has a lower polarity index than ethanol, which reduces dissolution rate for some ionic soils while improving wetting on hydrophobic substrates. Compared with n-propanol, which boils at 97.2°C and has a closed-cup flash point of 23°C, 2-propanol requires lower reboiler duty for evaporative drying and distills at a lower kettle temperature, but its flash point of 12°C imposes stricter ventilation and static-discharge controls.
Unlike methanol, which carries an 8-hour occupational exposure limit of 200 ppm and acute toxicity constraints, 2-propanol is used in general solvent substitution workflows at an 8-hour limit of 400 ppm. Process substitution nevertheless requires validation of elastomer compatibility, residue behaviour, and flammability classification because the closed-cup flash point of 12°C remains below typical ambient room temperatures. Published data for specific printed-circuit-board cleanliness outcomes in ethanol-to-IPA replacement is limited; a controlled substitution study should compare ionic residues by IPC-TM-650 method 2.3.28 and surface insulation resistance per IPC-TM-650 method 2.6.3.7.
Because 2-propanol is fully miscible with water and most aprotic solvents, it is used as a precipitation medium for nucleic-acid isolation and as a co-solvent in aqueous polymer dispersions. In extraction workflows, its partial water miscibility reduces the partition coefficient for lipophilic analytes relative to dichloromethane or hexane; salting-out with sodium chloride or sodium sulfate is used to promote phase separation and increase organic-phase recovery. These workflows use the EMPLURA grade only when downstream analysis is not UV-transmittance-limited; for HPLC quantification, the LiChrosolv grade is substituted to avoid co-extracted trace impurities.
2-Propanol is supplied without added radical inhibitors because the secondary alcohol does not form peroxides under ambient storage as readily as ethers; however, oxidative dehydrogenation to acetone proceeds in the presence of dissolved oxygen and heat. The rate of acetone formation is elevated in drum storage exposed to cyclic temperatures above 35°C and in partially filled containers with a large vapour headspace. Acetone has a closed-cup flash point of −20°C and higher vapour pressure than 2-propanol, so measurable acetone formation depresses the flash point of the stored liquid and may alter evaporative drying performance. Distillation for recovery at temperatures above 80°C should therefore be conducted under reduced pressure or inert atmosphere to limit oxidative degradation. Published data for long-term acetone formation in this specific packaging configuration is limited; storage stability should be verified by periodic gas-chromatographic assay for acetone in the retained liquid phase.
Compatibility with elastomer and polymer seals is not universal. Perfluoroelastomer and PTFE generally withstand continuous immersion; nitrile and EPDM should be evaluated under ASTM D471 immersion testing at the intended service temperature because seal swell is formulation-specific and cannot be generalised. Polycarbonate and acrylic components may stress-crack upon prolonged vapour exposure. Stainless steel, glass, and high-density polyethylene are preferred for storage and transfer. Direct handling in open containers is constrained by the 12°C closed-cup flash point and the 2.0 vol% lower explosion limit. Inert-gas blanketing is applied for high-rate transfer to control static charge accumulation, and transfer lines are bonded and grounded in accordance with NFPA 77 recommended practice for static electricity. The solvent should not be stored near strong oxidisers such as concentrated nitric acid or peroxides because oxidative conversion to acetone is exothermic. Long-term storage in partially emptied containers is limited by hygroscopic water uptake; at relative humidity above 60%, water content rises measurably, shifting the azeotropic composition and reducing residue-free drying for critical surfaces. Empty containers retain flammable vapour and should be grounded before disposal.