| HS Code | 703937 |
| Chemical Formula | C3H8O |
| Cas Number | 67-63-0 |
| Molecular Weight | 60.10 g/mol |
| Purity | 99% anhydrous |
| Grade | technical/industrial grade |
| Appearance | clear colorless liquid |
| Odor | strong alcohol odor, isopropyl-like |
| Boiling Point | 82.5°C (180.5°F) |
| Melting Point | -89.5°C (-129.1°F) |
| Flash Point | 11.7°C (53°F) closed cup |
| Autoignition Temperature | 399°C (750°F) |
| Specific Gravity | 0.786 at 20°C |
| Vapor Density | 2.1 (air=1) |
| Vapor Pressure | 33 mmHg at 20°C |
| Solubility | miscible in water |
| Container Size | 55 gallon drum |
As an accredited Isopropyl Alcohol 99% Anhydrous – 55 Gallon Drum factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | One 55-gallon drum of 99% anhydrous isopropyl alcohol, sealed in an industrial-grade container for safe handling and storage. |
| Container Loading (20′ FCL) | 20′ FCL: 55-gallon drums of anhydrous isopropyl alcohol securely loaded, blocked, and ventilated for safe transport. |
| Shipping | Shipping restricted to ground transport only due to flammability hazard (UN1219, Isopropanol). This 55-gallon drum is packaged as regulated dangerous goods, requiring hazard labels, proper placarding, and a certified hazmat shipper. No air, rail, or international shipments; domestic ground delivery only. Signature required upon receipt. |
| Storage | Store the 55-gallon drum upright in a cool, dry, well-ventilated area away from heat, sparks, and open flames. Keep the container tightly sealed to prevent moisture absorption and vapor release. Use proper grounding and bonding. Ensure secondary containment and segregation from oxidizers and incompatible materials. Inspect regularly and follow local fire codes. |
| Shelf Life | Shelf life is typically 3 years when stored sealed, away from moisture and heat. |
On high-density printed circuit board assembly and semiconductor packaging lines, 99% anhydrous isopropyl alcohol is deployed as a final rinse and stencil cleaning solvent where water entrapment under low-standoff components causes electrochemical migration. The 55 gallon drum supply is received under UN 1219, Class 3, Packing Group II, and its chemical purity is normally specified to ASTM D770 with point-of-use water content controlled below 0.1% by Karl Fischer titration. Residue removal is governed by IPC J-STD-001 and IPC-A-610, with ionic contamination thresholds referenced to IPC-CH-65B and chloride quantification per ASTM D512-23. The solvent is applied neat or at 70–90 vol% with deionized water for ultrasonic immersion, but the final rinse is maintained at 99% anhydrous to keep water content below 0.3% before drying. In production-scale inline cleaning, a closed-loop stainless steel 316L sump with 40 kHz ultrasonic transducers and a 0.2 µm PTFE filtration loop removes flux soils from stencils and reflowed assemblies at 30–35 °C for 3–5 min; prolonged contact beyond 10 min on ink-marked components can soften some legend inks. Because the solvent has a flash point of 12 °C, the cleaning module must be Class I Division 1 explosion-proof, and 55 gallon drum transfer should use a conductive PTFE diaphragm AODD pump with a nitrogen-blanketed drum headspace to limit atmospheric moisture ingress. Terminal articles include printed circuit board assemblies, semiconductor lead frames, wire-bonded MEMS sensors, and stencils used for 0201 and 01005 component paste printing. Published data for specific low-standoff batch configurations is limited; the above operating window is drawn from standard process bulletins for ultrasonic flux removal and should be validated by ion chromatography per IPC-TM-650 Method 2.3.25.
Oral solid dose manufacturing uses 99% anhydrous isopropyl alcohol as a wet granulation vehicle for water-sensitive APIs because it evaporates below 82.5 °C and is classified as a Class 3 solvent under ICH Q3C, with a permitted daily exposure of 50 mg/day and a residual solvent limit of 5,000 ppm in drug product. Compliance with USP <467> requires headspace gas chromatographic detection of isopropyl alcohol in each lot, while equipment cleaning must satisfy 21 CFR 211.67 with swab recovery studies and residue limits of not more than 10 ppm in most programs. Published formulation work for immediate-release matrices typically uses addition levels of 8–25 wt% of dry blend mass when the diluent is a lactose/microcrystalline cellulose system; the actual endpoint is controlled by granulator torque and current draw rather than a fixed ratio. In a high-shear mixer granulator, the solvent is sprayed through a 2.0–3.5 mm nozzle at 0.5–2.0 bar atomizing pressure with main impeller speed 200–400 rpm and chopper speed 500–1,500 rpm, typically over 3–8 min. The wet mass is then discharged through a 1.5–3.0 mm screen and dried in a vacuum tray dryer at 40–55 °C with ±5 °C bed uniformity until loss on drying is below 2.0%. Terminal product types include immediate-release tablets and hard gelatin capsule formulations containing acid-labile or moisture-sensitive active pharmaceutical ingredients. The main process boundary is that anhydrous IPA cannot be used with strong oxidizers or acetaldehyde-prone actives; residual water must remain below 0.5% in the wet granulation solvent to avoid hydration of anhydrous salts and premature disintegration failures.
Solvent-based flexographic printing of polyethylene and oriented polypropylene films relies on 99% anhydrous isopropyl alcohol to lower ink viscosity to the transfer window required by anilox roll metering without disturbing resin solubility. Press-side dilution is normally controlled by ASTM D4212 viscosity measurement or a Zahn #2 cup reading of 22–28 s at 25 °C, with addition levels of 3–8 wt% of ink mass for process prints. US EPA Method 24 governs volatile organic compound content for the diluted ink, and the printer must maintain permitted VOC emission limits for the pressroom; solvent dryer exhaust is routed through a regenerative thermal oxidizer at 760–820 °C. The downstream production sequence involves blending 99% anhydrous IPA into the return line of a closed ink sump using a solenoid-metered dispense system, passing through a 10 µm filter, and re-entering the doctor blade chamber so that photopolymer plate swell remains below 0.5%. Terminal finished product types include surface-printed and reverse-printed flexible packaging, self-adhesive labels, and barrier laminates for snack and confectionary pouches. In water-based high-acid acrylic resin systems, addition above 10 wt% can shock the resin colloid and reduce ink transfer; solvent-based formulations are therefore the standard application route for this solvent.
Machined stainless steel fittings, aluminum pneumatic manifolds, and titanium implant subcomponents requiring pre-passivation cleaning are immersed in 99% anhydrous isopropyl alcohol when water-based alkaline parts washers cannot meet surface tension requirements. Applicable compliance is 29 CFR 1910.106 for Class IB flammable liquids, NFPA 30, and flash point verification per ASTM D93-20; aerospace-facing sites may impose ASTM D770 solvent specification limits for water and nonvolatile residue. The solvent is applied neat or at 70–90 vol% in a two-stage rinse, with final immersion at 99% anhydrous for 5–10 min at 20–28 °C in an explosion-proof ultrasonic tank. Because this is a cleaning bath rather than a formulated product, addition ratios are operational use concentrations rather than formulation levels; bath life is controlled by nonvolatile residue and visual clarity, and published data for specific fitting counts per 55 gallon drum is limited. Downstream processing includes oil-free nitrogen blow-off at 2–4 bar, followed by vacuum bake at 60–80 °C. Terminal articles include passivated 316L compression fittings, aluminum pneumatic manifolds, and titanium implant subcomponents. The primary boundary is moisture pickup: if water content of the bath exceeds 0.8%, white spotting can appear on polished aluminum; if applied to zinc-plated surfaces, rapid flash drying may leave a visually dull film that must be validated by comparative light reflectance measurement.
Cold-process alcohol-based hair fixative and scalp tonic manufacturing uses 99% anhydrous isopropyl alcohol as a low-temperature solvent that reduces water activity below 0.5, limiting microbial growth risk without heating. Compliance is assessed under EU Cosmetic Regulation 1223/2009 and the CIR Expert Panel monograph for isopropyl alcohol, with final product batch release including ISO 18415 or equivalent challenge testing. Addition levels in published concentrate formulations range from 10–30 wt% of the finished bulk when combined with SD Alcohol 40-B and film-forming polymers; the solvent is metered into a closed 304 stainless steel mixing vessel at 20–25 °C before polymer addition to avoid lump formation. Downstream processing consists of low-shear mixing at 100–300 rpm, chilled aerosol concentrate filling at −5 to 5 °C, and final crimp torque verification. Terminal article types include pump hairsprays, aerosol hairsprays, scalp tonics, and cooling skin mists. Published data for water activity limits in lower-alcohol pouches is limited; the specified water activity threshold is a process control derived from USP <1112> microbial growth guidelines rather than a direct anhydrous IPA specification.
When aqueous emulsifiable concentrate systems contain ester or carbamate active ingredients, 99% anhydrous isopropyl alcohol is introduced as a polar co-solvent to maintain a single-phase solution between technical-grade actives, aromatic solvents, and nonionic emulsifier packages. Under US 40 CFR 180.920, isopropyl alcohol is cleared as an inert ingredient for nonfood and food use, while international registration data are assessed through FAO/WHO JMPR pesticide specifications. Formulation addition ratios for emulsifiable concentrates generally fall between 5–30 wt% of total liquid mass, with the upper boundary limited by flash point reduction and the lower boundary controlled by cold-storage clarity after 72 h at 0 °C. Downstream processing includes charging the anhydrous solvent and technical active into a jacketed 316L reactor at 25–35 °C, then adding calcium dodecylbenzenesulfonate/nonylphenol ethoxylate emulsifier packages under 150–600 rpm agitation, followed by 5 µm filtration. Terminal product types include emulsifiable concentrate insecticides, herbicides, and plant growth regulators. The operational boundary is that anhydrous IPA must be excluded from formulations containing alkaline breakdown agents because ester and carbamate actives can undergo solvent-enhanced hydrolysis; batch stability is confirmed by CIPAC MT36.1 emulsion stability testing.
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Isopropyl Alcohol 99% Anhydrous – 55 Gallon Drum is a high-assay, low-water isopropanol package supplied for industrial solvent applications in which residual water, non-volatile residue, and package integrity are controlled. The product is identified as propan-2-ol, CAS 67-63-0, UN 1219, Class 3, Packing Group II, with a molecular formula C3H8O and molecular weight 60.10 g/mol. At 20°C, density by ASTM D4052 is reported in the range 0.785–0.787 g/cm³, the boiling point is approximately 82.5°C, and the Tag closed-cup flash point is approximately 11.7°C. Vapor pressure at 20°C is approximately 4.4 kPa, and vapor density is 2.07 relative to air, so released vapor tends to accumulate in low areas. The anhydrous designation is generally supported by a water content ≤ 0.1 wt% by Karl Fischer titration, unlike 70% isopropanol, which contains roughly 30 wt% water, and 91% isopropanol, which contains roughly 9 wt% water. The 55 gallon drum format is intended for process lines with sufficient solvent consumption to justify bulk handling, but it requires secondary containment, bonding and grounding, and flammable-liquid storage controls.
Because the product contains no added water, it may be described as anhydrous in contrast to some 99% technical-grade isopropanol that carries a looser water limit. A nominal 55 US gallon drum corresponds to approximately 208 L and a net mass near 163 kg at the specified density, although actual fill weight varies with filling tolerance and temperature. Distributor documentation should identify the lot number, drum material, grade, and retest date. Where drums are returned or refilled, contamination by water, dissolved metals, or non-volatile residues must be controlled, and the original drum should not be refilled without documented cleaning and inspection.
Selection among 70%, 91%, and 99% anhydrous isopropanol is governed by water concentration and downstream process sensitivity. 70% isopropanol remains the standard for surface disinfection because water slows evaporation and supports penetration through microbial cell walls; 99% anhydrous IPA may coagulate surface proteins rapidly, which can reduce penetration and change antimicrobial efficacy. Published log-reduction data for 99% anhydrous IPA across all relevant organisms, surface finishes, and exposure times is limited; therefore, validation under the intended contact time, temperature, and surface condition is required before replacing 70% IPA in a biocidal step. In moisture-sensitive polymer and coating operations, the anhydrous grade is preferred because water can interfere with cure, promote corrosion, or shift analytical response. In isocyanate-containing systems, water reacts with free isocyanate groups to generate carbon dioxide and amine intermediates, altering the NCO index and potentially creating bubbles or hardness variation. Even a water content of 0.1 wt% may be process-significant in these systems, so the drum should be sampled and titrated after opening and after prolonged storage.
Isopropanol 99% anhydrous should not be confused with anhydrous ethanol, methanol, or denatured alcohol. It is a secondary alcohol, not ethanol, and is not suitable for consumption. Denaturant status should be confirmed when the solvent is used in analytical, biomedical, or regulatory-controlled processes. Compared with 91% IPA, the anhydrous grade is selected where water is the critical impurity; compared with 70% IPA, the fire hazard is also larger because the flash point is below ambient process temperatures in many plants. The 55 gallon drum is therefore normally moved into a fixed solvent-dispensing station rather than used as a portable container.
For a 55 gallon drum of 99% anhydrous isopropanol, the term “anhydrous” is a water-content designation, not a compendial or electronic-grade claim. The purchase specification should state whether the required grade is technical, USP, ACS reagent, or low-ion/electronic. Table 1 lists representative specification parameters for standard industrial technical-grade isopropanol. These limits are supplier-specific and must be confirmed against the actual lot certificate and the process specification.
| Parameter | Method or Reference | Representative Limit |
|---|---|---|
| Assay | GC; ASTM D770 may be cited as the general specification | ≥ 99.0 wt% |
| Water content | Karl Fischer titration, ASTM D1364 | ≤ 0.1 wt% |
| Acidity as acetic acid | ASTM D1613 | ≤ 0.002 wt% |
| Non-volatile residue | ASTM D1353 | ≤ 10 ppm |
| Density at 20°C | ASTM D4052 | 0.785–0.787 g/cm³ |
| Distillation range at 760 mmHg | ASTM D1078 | 81.0–83.0°C |
| Color, Pt-Co/APHA | ASTM D1209 | ≤ 10 |
Electronic-grade 99.5%+ isopropanol may add specifications for chloride, sulfate, nitrate, sodium, iron, and particle count; these values are product and supplier specific. ACS reagent and USP monographs add separate impurity, assay, and residue requirements that may not be met by an industrial technical-grade 99% anhydrous product. For pharmaceutical or food-contact use, compendial or 21 CFR batch documentation is required; the standard technical grade is not automatically suitable for those applications.
Because isopropanol is hygroscopic, opened drums can absorb atmospheric moisture over time. In areas where relative humidity exceeds 60%, a dry-air or nitrogen blanket on the drum vent may be required to maintain the anhydrous specification. Karl Fischer titration should be repeated at defined intervals when the drum supplies a moisture-critical process. For analytical applications, low water is not the only variable; non-volatile residue and stabilizer or denaturant content may also affect results.
On printed circuit board assembly lines, the 55 gallon drum can supply automated under-stencil wipe rolls or manual cleaning benches. The drum reduces package changeover on high-throughput lines but requires fill-level sensing and leak detection because a single drum contains a large flammable load. Ultrasonic cleaning baths operating at 40 kHz with IPA require covers, vapor extraction, and cooling where extended sonication raises bath temperature. For fiber optic end-face cleaning, wipes and swabs saturated from this grade must be checked for non-volatile residue and particulate shedding, because solvent purity alone does not control contamination from the wipe substrate.
Transfer from a 55 gallon drum is commonly performed with a sealless polypropylene or PVDF drum pump driven by an air motor or an explosion-proof electric motor. Wetted seals, hoses, and diaphragms are typically PTFE, polypropylene, high-density polyethylene, or 316L stainless steel. Metal receivers, dispensing containers, and the drum itself must be bonded and grounded; free-fall dispensing into an open container should be avoided, and fill lines should be submerged below the liquid surface to reduce splash and static charge. Electrical equipment in the dispensing area is selected for the hazardous location class and group. Isopropanol is generally Class I, Group D under NFPA 70, and installations are commonly governed by Article 501 for Class I, Division 1 locations or Article 504 for intrinsically safe circuits. Drums should remain closed when not in use, and dispensing equipment should be cleaned or flushed before changing solvent lots to avoid cross-contamination.
Before transfer, the drum should be inspected for dents, damaged gaskets, and pressure build-up. The bung area should be cleaned before pump insertion to avoid introducing debris. A pressure/vacuum relief valve is used where atmospheric pressure changes may collapse or pressurize the drum. When transferring to smaller containers, the receiving container must be grounded and should be an approved safety can or a container constructed of non-sparking material with a flame arrestor. Table 2 summarizes selected safety and exposure parameters for 99% anhydrous isopropanol.
| Parameter | Value | Reference |
|---|---|---|
| Flash point closed cup | 11.7°C | ASTM D56 |
| Lower explosive limit | 2.0 vol% | NFPA 325 / SDS |
| Upper explosive limit | 12.7 vol% | NFPA 325 / SDS |
| Vapor pressure at 20°C | 4.4 kPa | Supplier SDS |
| Vapor density relative to air | 2.07 | Supplier SDS |
| Autoignition temperature | 399°C | Supplier SDS |
| OSHA PEL 8-hr TWA | 400 ppm (980 mg/m³) | 29 CFR 1910.1000 Table Z-1 |
| ACGIH TLV TWA / STEL | 200 ppm / 400 ppm | ACGIH |
| UN / DOT classification | UN 1219, Class 3, Packing Group II | 49 CFR 172.101 |
Polymer and elastomer compatibility should be verified with seal supplier data at the maximum process temperature, not only at ambient laboratory temperature. PTFE and polypropylene are generally accepted for long-term wetted service. High-density polyethylene is commonly used for drum bodies but has permeation limits at elevated temperature. EPDM and nitrile may be acceptable in specific formulations; natural rubber and some polyurethane elastomers are generally unsuitable where swell or extractables are unacceptable. Some epoxy-lined steel drums may release trace iron if the lining is scratched; HDPE drums may permit gradual moisture and oxygen transport over long storage. For low-ion electronic use, stainless steel or fluoropolymer-lined containers are generally preferred.
Keep 99% IPA away from strong oxidizing agents, strong acids, acid chlorides, and alkali metals. At storage temperatures above 35°C, vapor pressure increases, and standard drum closures should be evaluated for venting and gasket performance. Work areas are typically designed to maintain airborne concentrations below the ACGIH TLV-TWA of 200 ppm; if the exposure limit is exceeded, local exhaust ventilation or an appropriate organic vapor respirator is required under 29 CFR 1910.134. Spent solvent and saturated wipes may be ignitable hazardous waste under 40 CFR 261.21 and must be collected and disposed through a permitted waste handler.
In analytical laboratories, 99% anhydrous IPA is used for sample preparation, LC mobile-phase adjustment, and glassware cleaning. When used with reversed-phase UHPLC columns having 0.2 µm inlet frits, the solvent should be filtered and checked for non-volatile residue to avoid column fouling. Karl Fischer verification is required before use in reagent systems where the solvent blank must be below the method limit. For printing and coating lines, IPA may be used to reduce ink viscosity or clean anilox rolls; open drums should be capped immediately after withdrawal, and dry-air blanketing is required where water uptake from humid air would shift the process outside the anhydrous specification.