Vaseline

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Identity and tariff classification data for petrolatum-based Vaseline are maintained in the manufacturer’s regulatory data system as a UVCB substance. Because this product is a refined semi-solid hydrocarbon fraction rather than a single discrete compound, the identity record uses regulatory substance names rather than a unique IUPAC denomination.

Product Identification — Chemical ID: CAS, formula and HS code database for Vaseline / petrolatum
Identification field Manufacturer’s technical entry
Product Name & IUPAC Name Vaseline / white petrolatum (pharmacopoeial grade). A single IUPAC name is not applicable to the UVCB; the regulatory substance name is petrolatum (petroleum jelly).
CAS Registry Number 8009-03-8
Chemical Formula No discrete molecular formula assigned to the UVCB. For the saturated straight-chain paraffinic fraction only, a simplified representation is CnH2n+2; the refined product contains branched, cyclic, and minor unsaturated/aromatic hydrocarbon structures depending on crude source and hydrogenation depth.
Synonyms & Trade Names Vaseline (trade name); petrolatum; white petrolatum; yellow petrolatum; petroleum jelly; mineral jelly; soft paraffin; petrolatum jelly. INCI: Petrolatum.
HS Code & Customs Classification HS 2712.10 — petroleum jelly; classified in Chapter 27 under mineral waxes and refined hydrocarbon products. National tariff schedules may add 8- or 10-digit subdivisions to distinguish crude and refined grades.

Grade-specific congealing point, color, consistency, and residual contaminant thresholds are not identity fields and are defined in the release monograph or customer specification for the applicable pharmacopoeial or industrial grade.

Petrolatum marketed under the Vaseline trade name is a purified mixture of semi-solid saturated hydrocarbons obtained from petroleum. CAS 8009-03-8, EINECS 232-373-2. The material is not a single chemical entity, so physical constants and impurity thresholds are defined as ranges in current pharmacopeial monographs and in grade-specific internal release specifications.

At 20 °C, pharmaceutical white petrolatum is a translucent, white to pale yellow semi-solid with a smooth consistency and faint or absent odor. Industrial technical grades may be pale yellow to light amber due to residual aromatic and sulfur compounds. Melting range for USP/NF and Ph. Eur. grades is typically 38–60 °C; the exact range is adjusted by the ratio of microcrystalline wax to mineral oil. A conventional boiling point is not applicable because the material is a multicomponent hydrocarbon mixture. Simulated distillation (ASTM D7169) typically shows initial boiling above 260 °C, with progressive evolution of heavier fractions. Flash point determined by Cleveland open cup (ASTM D92) is normally above 200 °C. Density at 60 °C is in the range 0.815–0.880 g/cm³ for compendial grades, measured by ASTM D4052 or ISO 12185; density at lower temperatures is higher and depends on thermal history.

Chemical stability is governed by oxygen access, temperature, and trace catalytic metal content. At ambient storage temperatures in sealed containers, oxidation is negligible. Prolonged heating above 105 °C or exposure to UV light increases peroxide value and acid number; oxidation is accelerated by copper and iron residues. Contact with strong oxidizing agents, chlorine, and oxygen at elevated temperature must be avoided because these conditions lead to chain scission, discoloration, and odor formation. Peroxide value (ISO 3960) and acid number (ASTM D974) are suitable monitoring parameters when thermal stress is suspected.

Water and glycerol do not dissolve petrolatum; it is soluble or freely miscible with aliphatic and aromatic hydrocarbons, chloroform, and ether, and slightly soluble in ethanol. Typical solution preparation for ointment and lipophilic formulations is performed in jacketed vessels at 60–80 °C with an anchor stirrer and nitrogen blanketing. High-shear mixing should be avoided because entrained air promotes oxidation; overheating above 90–100 °C for extended periods is not recommended.

Technical Specifications, Impurity Limits, and Release Standards

Release limits are grade-specific. Compendial pharmaceutical grades are controlled against the current USP-NF monograph for White Petrolatum and the Ph. Eur. monograph for White Soft Paraffin. Industrial technical grades are normally defined by a customer specification sheet because color, penetration, and sulfur limits vary by downstream application.

ParameterUnitUSP/NF White PetrolatumPh. Eur. White Soft ParaffinIndustrial Technical GradeTest Method
Appearancewhite to pale yellow translucent semi-solidwhite to almost white semi-solidpale yellow to light amber semi-solidvisual
Melting range°C38–6038–6042–60 typical, grade-dependentUSP <741>
Cone penetration0.1 mm100–180 unworked100–180 unworked80–200, application-specificASTM D937
Density at 60 °Cg/cm³0.815–0.8800.815–0.8800.800–0.900ASTM D4052 / ISO 12185
Flash point (COC)°C> 200> 200> 200ASTM D92
Acidity/alkalinitycomplies with monographcomplies with monographcustomer-definedcurrent monograph titration
Color after meltingnot more intense than referencenot more intense than referenceASTM D15002.0 typicalvisual / ASTM D1500

Impurity profile and limits are critical for pharmaceutical grades. Polycyclic aromatic hydrocarbons are controlled by UV absorbance after extraction; the current pharmacopeial monographs express limits as absorbance values at specified wavelengths. Additional GC-MS or LC-UV profiling for benzo[a]pyrene and total PAH may be applied when customer specifications require tighter control. Heavy metals are determined by acid digestion and ICP-MS; lead, arsenic, and mercury are typically controlled below compendial thresholds. Hydrotreated grades commonly show sulfur below 50 mg/kg, whereas non-hydrotreated industrial grades may contain higher sulfur. Residual catalyst metals are controlled by filtration and by ICP-MS release testing where required.

When Feedstock Sulfur and Aromatic Content Dictate the Hydrotreating Route

The route selected for a batch depends on the sulfur, nitrogen, and polyaromatic content of the incoming vacuum gas oil or slack wax feedstock. Low-sulfur paraffinic crudes are preferred for pharmaceutical white petrolatum because they permit hydrotreating to reach compendial UV-absorbance limits without excessive catalyst deactivation. Raw materials include vacuum-distilled paraffinic distillates, slack wax from solvent dewaxing, petrolatum stock, hydrogen, activated clay, and filter aid. The oil-to-wax ratio is adjusted by blending; a higher microcrystalline wax fraction raises melting point and reduces oil bleed, while a higher mineral oil fraction lowers viscosity and penetration.

Hydrotreating is the core saturation step, not a conventional synthesis. Aromatic rings adsorb on nickel-molybdenum or cobalt-molybdenum sulfide sites on alumina supports; hydrogen saturates aromatic rings to naphthenes, sulfur is removed as H₂S, and nitrogen is removed as NH₃. Operating conditions are feed-specific: hydrogen partial pressure commonly lies in the range 3.0–8.0 MPa, reactor inlet temperature 300–380 °C, and liquid hourly space velocity is adjusted to meet target UV absorbance without overcracking. Published data for a single universal condition set is not applicable because catalyst activity and feed aromaticity vary between crude sources.

Critical process control points include hydrogen purity greater than 99.5 %, reactor bed pressure drop below 0.5 MPa, and clay adsorption temperature 80–120 °C. Filtration is conducted above the melting range but below 120 °C to minimize oxidative color development. In-process samples are taken after hydrotreating and after clay treatment for UV absorbance, color, and penetration. If the intermediate shows excessive penetration, blending with microcrystalline wax or mineral oil is performed before final filtration; no blending after final filtration is allowed for pharmaceutical grade.

Quality control and batch release require conformity on melting range, cone penetration, color, acidity/alkalinity, UV absorbance, and sulfur content. A batch is not released on a single bulk property. Retained samples are stored for the assigned shelf life and used for confirmatory testing if a customer complaint or stability question arises.

Chemically, the product undergoes limited intentional derivatization. Thermal-oxidative degradation is the primary uncontrolled reaction, promoted by temperatures above 120 °C, oxygen, and catalytic metals. Hydrogenation can be extended for further aromatic saturation, but this is controlled by the hydrotreating route described above. Controlled air oxidation of industrial grades to increase acid number for emulsifiable petrolatum is possible, but published data for this specific configuration is limited. Downstream products are predominantly physical blends with waxes, mineral oils, polymers, or lipophilic excipients rather than chemically transformed derivatives.

Storage Envelope and Container Compatibility Requirements

Recommended storage is in closed, sealed containers at 5–40 °C, protected from light and oxygen. Bulk tanks that are heated above 40 °C should be nitrogen-blanketed with oxygen below 5 % by volume. Humidity does not directly degrade the hydrocarbon matrix, but surface condensation can create an interfacial layer in open vessels. Container compatibility: 316L stainless steel, carbon steel with a food-grade epoxy liner, or HDPE drums are suitable. Copper, brass, and unlined carbon steel are not recommended for long-term storage because trace copper increases oxidation rate and color development. Molten transfer lines should be heated and nitrogen-purged to prevent oxygen uptake and solidification.

Shelf life is typically 3–5 years from the date of manufacture for pharmaceutical grades stored as specified. No compendial endpoint is assigned to all grades; stability is confirmed by retained sample testing. Degradation indicators include an increase in peroxide value or acid number, yellowing, rancid odor, change in cone penetration, surface water, or phase separation. If any such indicator is observed, the batch is quarantined and not used for pharmaceutical applications without re-testing against the full release specification.

What hazard communication elements apply to molten and mist forms?

According to GHS criteria in EC 1272/2008 and 29 CFR 1910.1200, petrolatum is not classified as hazardous at ambient temperature; no pictogram, signal word, or hazard statement is required. Molten material above 60 °C presents a thermal burn risk, and oil mist generated at elevated temperatures is subject to occupational exposure limits. Hazard statements: not applicable. Precautionary statements for molten handling: P280 wear thermal protective gloves and clothing; P264 wash hands after handling. When oil mist may form: P261 avoid breathing mist or vapours; P271 use only outdoors or in a well-ventilated area if heated.

Acute oral toxicity in rats is low; published LD50 values are generally above 5000 mg/kg, but exact data vary by grade and test protocol. Refined pharmaceutical grades are used as dermatological excipients and are not expected to cause skin irritation or sensitization under normal conditions. No specific occupational exposure limit is established for solid petrolatum. The mineral oil mist exposure limit is 5 mg/m³ as an 8-h TWA under OSHA PEL 29 CFR 1910.1000 and ACGIH TLV, with a short-term exposure limit of 10 mg/m³.

Handling of solid material requires standard hygiene measures and slip prevention. Heating above 80 °C in open systems requires local exhaust ventilation. Molten product adheres to skin and causes deep thermal burns; do not handle without thermal protection. Spills should be allowed to solidify and then collected with an inert absorbent. Empty drums may contain residual hydrocarbon vapor; do not cut, weld, or apply heat without verifying vapor-free status.

White petrolatum is manufactured through controlled stream selection, hydrotreatment, and adsorptive purification of petroleum-derived hydrocarbon intermediates. The production train is configured as a batch hydrogenation and clay-contacting line; catalyst bed temperature, hydrogen partial pressure, and filter differential pressure are monitored continuously. Release is contingent upon congealing point, color, acidity/alkalinity, and pharmacopoeial impurity testing corresponding to the specified grade.

Production capacity is not a single fixed figure. It is allocated by reactor cycle time, hydrogen availability, filter aid consumption, and package line changeover. High-purity USP-NF or Ph. Eur. grades require extended clay/carbon contact and additional filtration passes, reducing nameplate throughput relative to technical grades. At the filter station, increased clay dosage raises differential pressure across plate-and-frame units and shortens pre-coat life; this is often the practical capacity constraint rather than the hydrogenation catalyst. Hydrogenation catalyst deactivation caused by sulfur breakthrough also increases cycle time and hydrogen consumption. Published plant-specific capacity data for individual Vaseline/petrolatum trains is limited and is not stated as a universal value.

Lead time is governed by pre-shipment final release testing, tank cleaning validation, and customer-specific documentation. Molten bulk shipments require insulated tank containers and may be subject to origin-destination temperature profiles. Solid packaged goods require drum or pail filling and heat-sealing of food-contact or pharmaceutical liners. Minimum order quantities are grade-specific and packaging-specific: dedicated bulk tank loads, palletized drum lots, and smaller pails have different changeover and batch documentation requirements. Published MOQ values are not stated here because they vary by destination and specification.

Representative packaging configurations and associated technical constraints
Packaging formatService modeTechnical and certification constraints
Insulated tank containerMolten bulk exportHeating and recirculation capacity required; epoxy phenolic lining; pre-loading certificate of cleaning; nitrogen padding to reduce oxidation
Road tankerMolten domestic bulkDedicated non-reactive heating circuit; closed-loop sampling and discharge preferred; filling temperature traceability
Steel drumsSemi-solid exportUN-approved outer packaging; food-grade or pharmaceutical inner liner; barcode or QR batch traceability
Fibre kegs and pailsCosmetic and technical small packsPE or polyester-laminated liner; tamper-evident lid; storage below melt or congealing threshold

Shipping terms are normally quoted under Incoterms 2020 FCA, CIF, DAP, or FOB according to destination. Payment methods include irrevocable letter of credit at sight, telegraphic transfer, or open account subject to credit approval. Export documentation includes batch certificate, certificate of analysis, safety data sheet, packing list, commercial invoice, and certificate of origin. Health or pharmacopoeial certificates may be added when the destination authority requires them. Molten transit is planned to limit heat-aging; solid packaged material is less time-sensitive but should not be exposed to direct sunlight or high ambient temperatures for extended periods.

What Raw Material and Process Variables Move Petrolatum Pricing?

The raw material cost stack for white petrolatum is dominated by paraffinic slack wax and/or petroleum distillate feedstocks, hydrogen, activated clay or carbon, filter aid, and energy. Feedstock is the largest variable; it depends on refinery wax cuts and base-oil slate configuration. Hydrogen consumption scales with hydrotreatment severity and sulfur/olefin content of the feed; clay and carbon consumption scale with color and polycyclic aromatic hydrocarbon reduction requirements. Disposal of spent filter aid contributes to variable cost, particularly under stricter waste-authorization regimes.

Fluctuation is driven by crude oil and natural gas movements, but not mechanistically identical to Brent or WTI spot. Wax spreads, refinery utilization, seasonal demand for candles and coatings, and vessel availability can move feedstock wax values independently. Hydrogen and natural gas prices influence hydrotreatment cost. Exchange rate shifts affect export parity in India, China, the European Union, and the United States. Regulatory changes that raise PAH compliance costs or necessitate additional post-treatment alter the price-grade ladder even when crude remains stable.

Price differences between grades reflect not merely raw material input but the cost of complying with a monograph or customer specification. A pharmacopoeial white petrolatum requiring low absorptivity, additional PAH control, and tighter color and odor tolerances will consume more hydrogen and clay per tonne, occupy reactor and filter time longer, require more analytical release testing, and require dedicated packaging lines. These compliance steps create a non-linear, graded price difference from technical or lower-purity grades.

Grade, Purity, and Packaging Certification Are the Core Price Ladder

Grade differentiation starts with feed selection and refining route. Technical-grade petrolatum may allow broader feed cuts and limited color treatment; cosmetic grade usually requires a whiter, low-odor product with tighter PAH care; pharmacopoeial USP-NF or Ph. Eur. grade imposes monographed tests for acid and alkaline impurities, consistency, color, and in some regions polycyclic aromatic hydrocarbon or mineral-oil purity criteria. Purity differences originate from hydrogenation severity, clay and carbon dosing, filtration, and blending of in-process batches.

Packaging certification further separates prices. Food-contact or pharmaceutical liners, heat sealing under controlled environment, UN-approved outer packaging, batch traceability, and customer-specific palletization all add cost. Controlled filling and dedicated lines may be required for some dermal or pediatric customers. A product that is identical by bulk liquid specification may therefore be priced differently when packaged and certified under different quality systems, because the released lot then carries different documentation, retention, and liability obligations.

Global trade in white petrolatum is shaped by refinery rationalization in North America and Europe, integrated wax capacity in China, price-sensitive pharmaceutical and consumer demand in India, and strict pharmacopoeial and cosmetic sourcing in Japan. Supply is influenced by the availability of wax streams from base-oil production, not only by direct crude price. Demand is relatively stable in topical pharmaceutical and personal care applications, with year-end seasonal increases in some regions.

Regional supply and demand sensitivities for white petrolatum
EconomyMain demand sideKey trade and technical sensitivity
United StatesPharmaceutical and personal care formulations; ointment and wound-care basesUSP-NF grade availability tied to refinery wax supply and FDA-registered facility requirements
European UnionHigh-purity cosmetic and pharmaceutical gradesPAH management, REACH dossier boundaries, pharmacopoeial conformance, preference for low-tar feedstocks
JapanHigh-specification pharmaceutical and cosmetic formulationsJapanese Pharmacopoeia and low-impurity sourcing; limited domestic refining
IndiaLarge topical medicine and personal care manufacturing basePrice-sensitive import and domestic supply, shipping lead times, monsoon-sensitive logistics
ChinaPersonal care, pharmaceutical intermediates, export processingIntegrated wax and petrolatum capacity, environmental inspection policies, export quality differentiation

If 2026 Price Direction Is Read Through Refinery Wax Spreads, Oversupply Is the Principal Downside Risk

The 2026 price trend for petrolatum cannot be isolated from global Group I base-oil rationalization, wax demand, and Asian refinery operating rates. A scenario of slower industrial demand in China and additional integrated capacity from Chinese refiners would tend to widen export availability and soften freight-on-board Asia values. In contrast, stricter EU PAH enforcement and US pharmaceutical sourcing preferences would sustain higher premiums for documented high-purity USP-NF and Ph. Eur. material, while technical grades may trade at a discount to compliant grades. Imported material in Europe and North America remains sensitive to freight rates, port delays, and inventory carrying cost for heated storage.

Data limitations prevent a single numerical 2026 price forecast. The forward view is derived from scenario analysis based on trade flows under HS heading 2712.10, producer operating-rate announcements, published wax spread movements, and regulatory trend monitoring. Contract-level prices are not used. The forecast is a directional risk assessment, not a transaction quote.

Recent market developments include increased buyer focus on polycyclic aromatic hydrocarbon content in petrolatum intended for leave-on skin and lip care products. This has accelerated demand for hydrogenated white petrolatum grades with documented lower PAH profiles and increased frequency of third-party testing. The EU cosmetics framework and REACH UVCB registration requirements create data-sharing and compliance costs that can favor established qualifying suppliers. Pharmacopoeial revisions continue to refine test methods for impurities; any monograph text change can affect release documentation and analytical workload for manufacturers.

Regulatory compliance updates cover pharmacopoeial monograph revisions, ICH Q3D elemental impurity controls where the product is used in medicinal formulations, and packaging migration standards such as EU 10/2011 or FDA 21 CFR references where food-contact certification is required. Supplier response and mitigation includes selection of feedstocks with intrinsically lower PAH and sulfur content, increased hydrogenation severity within catalyst operating limits, more frequent clay and carbon bed replacement, analytical monitoring by GC-MS or HPLC/UV techniques, and segregated storage and packaging for high-purity grades. These measures raise variable cost but reduce the risk of failing destination-market compliance audits.

The Application Fields & Grade Selection Guide for Vaseline petrolatum defines how production lot release data, regulatory filing position, and downstream unit-operation requirements interact before a grade is assigned to a customer process. The product class covers technical petrolatum, cosmetic-grade white petrolatum, and pharmacopoeial-grade petrolatum; selection is not a single-specification decision but is driven by the application’s thermal exposure, dermal or incidental contact risk, formulation rheology, and the region-specific regulatory dossier.

Application Fields & Grade Matching Guide

Industry Applications

Pharmaceutical and personal-care manufacturing uses Vaseline petrolatum as an oleaginous base in ointments, creams, lip care, and protective dressings. The dominant technical requirement in this field is not only cone penetration measured under ASTM D937 but also the removal or control of aromatic and polycyclic aromatic hydrocarbon fractions to monograph-defined limits. Cosmetic compounding uses white petrolatum in emulsions, hair grooming products, and skin protectants; the relevant release dossier generally references the EU Cosmetic Regulation EC 1223/2009 and requires documented refining history under a cosmetic ingredient safety file. Industrial rust preventives and metal-protection compounds use technical petrolatum as a hydrophobic barrier film; the performance-sensitive properties are film continuity, drop melting point under ASTM D127, and compatibility with the selected corrosion inhibitor and solvent system. Rubber and plastics processing uses technical petrolatum as a process aid and surface lubricant; here the main batch-to-batch variables are oil separation tendency, viscosity at processing temperature, and absence of bright stock or asphaltene-derived particulates.

Mapping Petrolatum Grades to Downstream Application Requirements

Grade-to-application mapping is not a single property matrix; it is a hierarchy of regulatory status first, then rheological consistency, then organoleptic and purity parameters. The table below summarizes typical grade classes and the main application fields in which they are evaluated.

Grade classTypical application fieldRegulatory/quality anchorApplication-sensitive release parameters
Technical petrolatumIndustrial coatings, rust preventives, rubber process aidsPurchase specification; supplier quality agreementDrop melting point via ASTM D127, cone penetration via ASTM D937, oil separation, particulates
Cosmetic white petrolatumSkin care, hair care, lip care, ointment basesEC 1223/2009 ingredient file; pharmacopoeial monograph where applicableColor, odor, UV absorbance/extinction profile where specified, consistency, PAH control
Pharmacopoeial petrolatumTopical pharmaceuticals, protective ointments, dermatological formulationsUSP-NF/Ph. Eur. petrolatum monograph; cGMP batch releaseMonograph purity tests, acidity/alkalinity, consistency, PAH control

What Key Parameters Are Application-Sensitive?

Key parameters by application are not identical across grade classes. Consistency measured by cone penetration under ASTM D937 is the most formulation-sensitive rheological parameter. A grade with higher penetration provides lower spreading resistance, but it can reduce heat stability and increase oil bleed in compressed tablet or stick formats. Drop melting point measured by ASTM D127 is critical for processing zones where the petrolatum is melted and held at elevated temperature; the value must be evaluated together with the cooling profile of the mixer or extrusion line, not in isolation. Color and odor are application-sensitive for white petrolatum used in leave-on skin care and pharmaceutical ointments; these are typically controlled through hydrotreating severity, adsorbent purification, and steam stripping. Polycyclic aromatic hydrocarbon profile is a release criterion for cosmetic and pharmacopoeial grades; a complete refining history or a suitably validated analytical control strategy is required, and published data for non-standard technical configurations is limited. Oil separation and particulate loading are production-critical in high-speed filling lines, because a variation in bulk consistency can alter nozzle back-pressure and fill weight control.

How to Select the Right Grade, and What Data Must Precede Sampling?

The selection sequence below is used by quality control and application engineering before a customer sample is released. Each step is a decision gate; if a previous step is unresolved, subsequent sampling is not authorized under the batch release workflow.

Step 1: Define Application. The grade selection starts with the downstream unit operation and final article type. Pharmaceutical ointment compounding requires a monograph-aligned grade; industrial metallic corrosion protection requires film persistence and rheological compatibility with the coating head. The production department records the highest processing temperature, the shear rate, the contact time with skin or mucosa, and whether the grade is used as a continuous phase or a minor process aid.

Step 2: Identify Regulatory Requirements. Regulatory status drives grade availability. For cosmetic leave-on applications in the EU, the ingredient file must be consistent with EC 1223/2009. For pharmaceutical use, the grade must be released against the applicable pharmacopoeial monograph and manufactured under cGMP in accordance with 21 CFR 210/211 where the site supplies the US market. Food-contact and incidental-contact applications require a separate evaluation; no grade is assigned for food use unless the regional food-contact listing and the customer’s finished-article migration testing framework explicitly permit the specific petrolatum grade.

Step 3: Evaluate Purity Needs. Purity requirements are grade-dependent and are not interchangeable. Pharmacopoeial grades are evaluated for acidity/alkalinity, colour, and PAH control according to the monograph; cosmetic white petrolatum requires low odor and low colour plus a documented refining history. Technical grades may contain higher aromatic fractions and are unsuitable for leave-on dermal contact. The quality control laboratory compares the customer’s unacceptable impurity profile against the production lot release data; where the application requires a PAH limit below the routine release limit, a dedicated hydrotreated or adsorbent-polished lot selection may be necessary.

Step 4: Consider Volume & Budget. Volume and cost are evaluated after regulatory and purity gates are passed. Pharmacopoeial and cosmetic white grades carry additional purification and batch documentation costs; technical grades are more economical for high-volume industrial rust preventive lines but do not provide the same dermal safety dossier. A high-volume pharmaceutical order may still require a dedicated campaign to avoid cross-contamination from industrial grade materials sharing transfer lines; the production schedule and cleaning validation status are therefore part of the grade selection decision.

Step 5: Request Sample for Validation. The final gate is a production-representative sample, not a laboratory-scale blend. The sample lot is released against the provisional specification defined in Steps 1 to 4, and the customer validates it on the actual filling line, emulsification vessel, or coating head. Validation includes cone penetration retention after heating/cooling cycles, oil separation under storage, and compatibility with the full formulation. The sample request is not complete without specifying the mixing temperature, hold time, and shear conditions; otherwise the evaluation cannot distinguish a grade-related failure from an equipment thermal-history effect.

The quality assurance framework for Vaseline-grade petrolatum is document-driven from batch release through supply-chain approval. A given lot is not assigned a commercial grade solely by a single melting point or penetration result; release is based on the intersection of the intended pharmacopoeial, food, or cosmetic application, the site’s certified management system, and the customer-specific specification.

Quality Compliance & Certifications

Quality Management Certifications apply to the production, filling, and warehouse control lines. Certificates normally referenced include ISO 9001:2015 for the quality management system, ISO 22716:2007 for cosmetic good manufacturing practice, and, depending on the production location, ISO 14001:2015 and ISO 45001:2018 for environmental and occupational health and safety management. The scope of each certificate is site-specific and is confirmed against the actual production facility and product grade. Audit coverage includes raw material release, batch traceability, cleaning validation, and non-conformance handling.

Product-Specific Certifications are grade-selective rather than universal. For pharmaceutical and cosmetic applications, the product is typically controlled against the USP-NF White Petrolatum monograph and the Ph. Eur. White Soft Paraffin monograph. For food-grade applications, regulatory status is assessed under FDA 21 CFR 172.880; for incidental food-contact lubricant uses, the applicable regulatory reference may include FDA 21 CFR 178.3700. Halal and Kosher certificates are available only for designated grades and are maintained through audited supply chains and segregated production planning.

Documentation & Reports are issued according to grade and market. The batch release package usually includes a Certificate of Analysis, Safety Data Sheet, and product regulatory statement. Pharmacopoeial grades require additional monograph-specific tests such as acidity/alkalinity, color, consistency, melting point, UV absorbance, heavy metals, and polycyclic aromatic hydrocarbons. Test method selection follows the monograph or the customer specification; typical instrumental references may include ASTM D937 for cone penetration and ASTM D127 for drop melting point.

Document Typical content Reference / standard
Batch Certificate of Analysis Appearance, color, odor, consistency, melting point, acidity/alkalinity, UV absorbance, heavy metals, PAH USP-NF, Ph. Eur., ASTM D937, ASTM D127
Safety Data Sheet Hazard classification, handling, disposal, exposure control REACH (EC) No 1907/2006, GHS
Product Data Sheet Typical physical data by grade Internal release data
Regulatory Status Statement INCI name, CAS number, monograph status, food-contact status INCI, FDA 21 CFR 172.880

How Purchase Cooperation Is Structured for Vaseline Supply

Purchase Cooperation Instructions cover four commercial-technical elements: stable production capacity supply and flexible business cooperation plan; core production capacity and stable supply capability; sample application process; detailed explanation of flexible cooperation mode.

Stable production capacity supply and flexible business cooperation plan are managed through a mix of committed volume allocation, rolling forecast, and safety stock held at the manufacturing site or external regional warehouses. The production unit can schedule multi-grade campaigns and can adjust fill sizes from bulk ISO containers to smaller technical pack sizes, but the available options are grade- and route-dependent.

Core production capacity and stable supply capability are controlled by raw material selection, purification throughput, and packaging line capacity. Petroleum feedstock batch variation is addressed through incoming control and in-process monitoring; final release is not determined by a single property but by the complete specification set. For contract supply, the manufacturer normally reserves a defined monthly production window. Actual capacity allocation is confirmed in writing based on grade, packaging, destination, and required documentation.

Sample application process: a request is submitted with company name, intended market, target grade, packaging preference, and required regulatory statement. The technical unit evaluates the request against available inventory and customer specification. Controlled commercial samples are issued with a limited technical data sheet; laboratory retain samples are retained according to the internal retention schedule. Samples for pharmaceutical or food use require additional qualification documentation and may require signing of a sample handling statement.

Detailed explanation of flexible cooperation mode: Flexibility is defined as either make-to-order against a confirmed specification, supply from buffer stock under a framework agreement, or private-label filling with customer-supplied packaging. Flexibility does not extend to unqualified interchange of grades, packaging materials, or transportation conditions without assessment. For any change in packaging or filling configuration, a compatibility and stability review is conducted before release. High-temperature handling requires controlled heating and inert gas blanking where specified. The product is incompatible with strong oxidizing agents and should be kept away from sources of ignition during high-temperature transfer.

Cooperation mode Supply trigger Technical requirement
Committed volume program Rolling forecast with fixed monthly quantity Capacity reservation, safety stock, monthly quality report
Make-to-order Confirmed specification and order Pre-production alignment, batch retain, COA release
Private-label / toll filling Customer-supplied packaging or specification Packaging qualification, labeling approval, regulatory review

Research and development activity for Vaseline-grade petrolatum is currently organized around hydrocarbon distribution stability, oxidative resistance during repeated thermal processing, and batch-to-batch consistency in downstream formulation. Raw material selection is limited to hydrotreated heavy distillates and controlled slack-wax-derived hydrocarbon streams; purchase specifications set internal limits for sulfur, nitrogen, and polycyclic aromatic hydrocarbon content before hydrogenation. Current R&D hotspots focus on catalytic hydrotreating severity, adsorbent purification sequence, and post-treatment compounding of high- and low-consistency hydrocarbon fractions. In-process control points include hydrogen pressure, catalyst bed temperature, adsorbent contact time, and filtration pressure differential, because these variables affect color, odor, peroxide value, and final consistency. The objective is to maintain the pharmacopeial profile of the product while adjusting cone penetration measured under ASTM D937 in 0.1 mm units to the application target. Emerging applications are evaluated in topical ointment bases, waterless skin protectants, wound-care matrices, and high-purity cosmetic barrier systems, where the critical technical parameters are peroxide value after accelerated oxidation, UV absorbance profile, bleed resistance at skin-contact temperature, and particulate absence after molten filtration. In such applications, product selection hinges on the ratio of paraffinic to naphthenic components, which influences oil separation under compression and the temperature at which the continuous gel structure softens. The principal technical challenge is that severe hydrogenation reduces color, odor, and unsaturated species but can simultaneously produce a narrower melting profile and a harder, less spreadable base. Breakthrough development effort is therefore directed at separation-assisted blending of controlled hydrocarbon cuts and lower-temperature vacuum stripping after adsorptive purification, rather than single-stage process intensification alone. Published data for some emerging application configurations remain limited, particularly where the base is blended with bio-based waxes or high-molecular-weight synthetic polymers.

What Market and Manufacturing Conditions Will Shape the Next 3–5 Years?

In the 3–5 years horizon, the market forecast for pharmaceutical and personal-care grades is expected to track formulation volume rather than raw material supply expansion. The product category is mature; purchasing criteria are shifting toward pharmacopeial compliance, odor profile, packaging integrity, and tighter cone penetration control rather than basic availability. Published third-party market forecasts diverge by region and end use, and no single internal forecast figure is applied across all grades without reference to customer contract data. The most probable technical demand shift is an increase in high-purity grades used in leave-on skin care and drug-product ointment bases, while lower-grade industrial uses remain cost-driven.

Technological evolution is moving toward continuous hydrogenation with reduced residence time, closed-loop solvent-free adsorbent regeneration, and in-line viscometry for consistency trending. The rationale is to limit thermal history, reduce color reversion after packing, and narrow the distribution of cone penetration values. Development trials use differential scanning calorimetry to map solid-liquid phase behavior and rotational rheometry to track low-shear viscosity in molten handling systems. This allows grade release to be linked to crystallization behavior rather than a single pass/fail melting point. However, published data for some novel continuous configurations is limited; process qualification therefore remains plant-specific and grade-specific.

Sustainability and green-chemistry actions focus on energy recovery from exothermic hydrogenation, regeneration of spent bleaching clays, and minimization of solvent use in purification. Carbon-intensity reduction is managed at site level and cannot be claimed as a product-specific universal benefit. Bio-based or synthetic alternatives have been assessed, but direct drop-in substitution remains technically constrained because the occlusive film-forming and crystalline network of petrolatum depend on a broad and specific carbon-number distribution. Published data for fully bio-identical petrolatum at production scale is limited; current development work therefore focuses on reducing process footprint rather than changing chemical identity.

If Formulation Behavior After Delivery Requires Process Adjustment

Technical consultation for Vaseline-grade petrolatum is provided through the manufacturer’s quality and technical service functions. Incoming requests are classified by application risk, regulatory exposure, and processing route. For pharmaceutical and cosmetic customers, consultation includes comparison of the supplied certificate of analysis against the relevant USP–NF monograph, discussion of good manufacturing practice obligations under 21 CFR 211 and ISO 22716:2007 where applicable, and review of safety data sheet storage conditions. Release criteria are linked to the USP–NF monograph and any customer specification, covering color, acidity or alkalinity, organic impurities, UV absorbance, and cone penetration. Application optimization support is provided in the form of pilot-scale formulation trials using production-representative equipment such as jacketed molten holding vessels, rotor-stator mixers, and cooling belts. The group evaluates oil separation at controlled compression, viscosity at filling temperature, color stability after reheating, and compatibility with antioxidants, fragrances, or active pharmaceutical ingredients. Batch-specific recommendations are not made without physical testing of the customer’s formulation.

After-sales commitment is defined in the quality agreement and covers batch traceability, retention samples, nonconformance investigation, and change notification. The manufacturer maintains batch records, production parameters, and quality control data for the retention period required by the applicable regulatory framework and customer quality agreement. If a product is subjected to high-shear dispersion or prolonged molten holding during customer processing, after-sales support includes review of thermal history and possible re-test of cone penetration and oxidation indicators. Replacement or rework decisions follow the nonconformance procedure under ISO 9001:2015, not an automatic use of new material. The service boundaries explicitly exclude formulation redesign, regulatory registration of the customer’s finished product, and performance guarantees beyond the tested certificate-of-analysis parameters, unless written into the supply contract.

Industrial Vaseline Petrolatum: Manufacturing Control, Application Data, and Supply Specifications

Industrial petrolatum under the Vaseline brand is produced by a direct manufacturing route that includes vacuum distillation, hydrotreating, and adsorbent filtration. The production line is controlled from feedstock selection through final filling, with release documentation issued from the site laboratory rather than from a distribution or trading function. Finished lots are tested against ASTM D127, ASTM D937, ASTM D445, and the applicable USP-NF petrolatum monograph where pharmacopoeial grade is specified. This integrated production chain allows specification limits to be written into batch planning before crude unit scheduling begins.

What Is Produced at the Vaseline Industrial Manufacturing Site?

White petrolatum and yellow petrolatum are manufactured in a defined melting-point matrix. White grades pass through a high-surface-area adsorbent bed that reduces color bodies and polar impurities; yellow grades retain a heavier oil fraction for uses where low color is not required. Standard industrial production covers drop melting points from 38 °C to 60 °C and worked cone penetration values from 100 dmm to 220 dmm. Lower penetration grades are used for thick-film barrier coatings, while higher penetration grades are specified for pumpable cable fill and low-shear spreading compounds.

Typical production specification grid for industrial petrolatum
ParameterTest methodTypical control window
Drop melting pointASTM D12738–60 °C
Worked cone penetrationASTM D937100–220 dmm
Kinematic viscosity at 100 °CASTM D4456–20 mm²/s
Acid numberASTM D9740.1 mg KOH/g
Color, SayboltASTM D156+25 for white grades

Batch release is not based on a single mid-range viscosity reading. Each production lot is sampled from the top, middle, and bottom of the finished tank before filling, and the three samples are tested separately for penetration and viscosity. The site laboratory runs retention samples under controlled storage at 20 °C to 25 °C for the full commercial shelf-life assigned to the lot. Statistical process control charts track drop melting point variation across consecutive campaigns, allowing process engineers to detect drift in the vacuum distillation cut before it moves outside the release window. The quality management system is operated under ISO 9001:2015, with analytical methods linked to the current pharmacopoeial and ASTM procedures listed on the certificate of analysis.

Bulk supply is scheduled from finished-product tanks under controlled temperature, with molten petrolatum transferred into insulated ISO tanks or dedicated bulk trailers. For ambient-handling production sites, the same material is filled into 175 kg steel drums with internal lacquer or 25 kg food-grade polyethylene pails. Filling lines are calibrated by mass, and each container is labeled with the batch number, production date, and released specification code. Drummed material can be re-melted in slow-ramp ovens or drum heaters; prolonged exposure above 90 °C should be avoided to prevent color shift in white grades. Inventory is planned against a direct production schedule rather than spot-market availability, which reduces lot-age variability in receiving warehouses.

For mill-applied rust preventives and long-term export packaging, petrolatum functions as a moisture-displacing barrier film rather than a simple grease. Corrosion preventive compounds formulated with petrolatum are sprayed or dip-applied at film thicknesses between 50 µm and 125 µm. Solvent-free grades remove the flash-off stage from continuous coating lines. Neutral salt spray testing under ASTM B117 is used to compare barrier life on degreased steel panels; performance depends on surface preparation, polar additive loading, and film continuity. In coil coating and wire rope service, the critical variable is not the base petrolatum alone but the additive package selected for the required outdoor exposure period.

Release and softener performance in rubber and plastics is governed by migration rate, not surface wetting

In rubber compounding, petrolatum is added between 2 phr and 5 phr on a two-roll mill or internal mixer. The material reduces sticking to mill rolls and improves carbon black incorporation under high-shear mixing. Migration behavior is measured by oven aging of cured sheets at 70 °C and by visual bloom rating after 72 h. In molded polypropylene and filled polyethylene compounds, petrolatum is used at lower loadings—typically 0.5 wt% to 2.0 wt%—as an internal release agent and viscosity modifier. Overdosing beyond 2.0 wt% in polyolefins can reduce tensile strength and should be confirmed by ASTM D638-14 tensile testing on the finished compound. The process window is narrower in thin-wall injection molding, where excessive migration to the mold surface can create visible deposit buildup on vent surfaces.

Cable Filling and Moisture-Blocking Petrolatum Requirements

Petrolatum-based cable fill compounds are specified for water blocking in copper and optical fiber cables. A production-grade base for this application is controlled for low ionic content, high volume resistivity, and minimal oil separation after high-temperature aging. Water penetration behavior is evaluated under IEC 60794-1-2 method F5 in filled cable core configurations. The base petrolatum is not used alone; it is compounded with thickening polymers and antioxidants to achieve the required drop point and cone penetration while maintaining pumpability at line speeds above 100 m/min. Oxidation induction time is measured by pressure differential scanning calorimetry per ASTM D5483. Fill compounds using high-penetration petrolatum require heated storage and jacketed pumping; solidification below 35 °C can interrupt filling head pressure in unheated transfer lines.

Technical support for industrial buyers is organized around specification translation, not product promotion. A technical data package includes the batch-specific certificate of analysis, a safety data sheet under current regulatory format, retained sample data for the assigned lot, and application-specific guidance on storage temperature, viscosity adjustment, and compatibility with elastomer seals. For customers running automated dosing systems, the production laboratory supplies rheological data at multiple shear rates rather than a single Brookfield reading. That data is generated on a controlled-stress rheometer using parallel-plate geometry at 25 °C, 40 °C, and 60 °C. This allows process engineers to determine pump selection and line heating requirements before the first bulk delivery is scheduled.

When pharmacopoeial compliance is part of the purchase specification

White petrolatum intended for pharmaceutical ointment bases, ophthalmic preparations, or cosmetic intermediates is released under a separate control protocol. The material must meet the petrolatum monograph of the current USP-NF, including limits for acidity or alkalinity, color, consistency, and organic impurities. Elemental impurity risk is assessed under ICH Q3D for finished dosage forms where applicable. The production sequence for pharmacopoeial grades uses dedicated post-hydrotreating filtration and stainless-steel storage. Changeover between yellow industrial grade and white pharmacopoeial grade includes a documented cleaning cycle and analysis of the first production lot before release. Direct manufacturing control in this area provides a single set of production records that links the batch number, filter campaign, cleaning validation, and final release against the monograph.

For manufacturers, the main value is batch-to-batch consistency under controlled penetration and melting-point windows, which reduces formulation rework in automated processes. For distributors, the value is a single production-site traceability chain with standard test data and retention samples, simplifying downstream quality audits. For procurement teams, direct supply planning from production capacity provides a defined lead-time envelope and batch-size alignment with annual volume forecasts. The specification is not negotiated after production; it is set before the production run, with limits assigned to melting point, penetration, viscosity, color, and oxidation stability.

Perguntas frequentes industriais

What are the USP/NF purity specifications and physical properties of the white petrolatum used in Vaseline, including melting point, cone penetration, and PAH content?

White petrolatum for Vaseline-type ointment bases is manufactured as a purified mixture of semisolid hydrocarbons obtained from petroleum and released against the current USP/NF White Petrolatum monograph. Production includes static melt filtration, high-shear homogenization, and filling under nitrogen into lined steel drums. Release tests cover melting range, cone penetration, acidity or alkalinity, fixed oils/fats/rosin, infrared identification, color, and polycyclic aromatic hydrocarbon absorbance. The standard grade contains no added antioxidant; a suitable stabilizer is permitted by the monograph and, if used, is declared on the certificate of analysis.

What Physical and Purity Limits Are Applied to This Grade?

Melting range is determined by USP <741> and must fall within 38–60°C. Petrolatum is not released on a single melting point because it is a multicomponent hydrocarbon blend. Cone penetration is measured with a penetrometer using a 150-g cone, 5-s dwell, and 25°C sample temperature. The USP/NF monograph requires not less than 100 tenths of a millimetre. Industrial petrolatum jelly grades of this type commonly read 150–250 dmm; the manufacturing site releases only homogeneous batches showing no oil separation after the penetration test. High-shear homogenization is run at a jacket set point below the upper melting limit; overheating above 60°C for extended periods can reduce cone penetration and increase free oil on storage. The filling manifold is therefore temperature-controlled at the discharge point to preserve the semisolid gel structure.

Polycyclic aromatic hydrocarbon content is controlled by the USP/NF limit test based on dimethyl sulfoxide extraction followed by UV absorbance. It is not expressed as a single total-ppm value in the monograph. The extract is examined between 260 nm and 420 nm. The compendial limit is ≤0.30 AU at 260 nm and ≤0.025 AU at 420 nm. Batch release data for the standard grade fall below these ceilings; quantitative GC-MS total PAH data for this specific general-purpose petrolatum configuration is limited, so the UV absorbance method remains the release control.

Purity tests for acidity or alkalinity and for fixed oils, fats, and rosin are run as pass/fail methods. No aqueous or oily separation is permitted. Infrared identification is matched against the USP White Petrolatum reference standard. Color is controlled to white or almost white, with not more than slight fluorescence. Standard packaging is epoxy-lined steel drums or food-grade pails, filled under nitrogen headspace.

Release profile for white petrolatum USP/NF
PropertyTest methodUSP/NF limitTypical release observation
Melting rangeUSP <741>38–60°CWithin monograph range; no oil separation
Cone penetrationPenetrometer, 150-g cone, 5 s, 25°CNLT 100 dmm150–250 dmm typical for topical petrolatum jelly
PAH absorbanceUSP/NF DMSO extraction≤0.30 AU at 260 nm; ≤0.025 AU at 420 nmBelow compendial ceiling
Acidity or alkalinityUSP/NF monographPassesPasses
Fixed oils, fats, and rosinUSP/NF monographPassesPasses

What are the minimum order quantities, lead times, and available packaging formats for sourcing Vaseline petroleum jelly from authorized distributors or direct manufacturers?

Factory-direct supply terms for Vaseline petroleum jelly are set by filling line configuration and transport thermal profile rather than by regional stock availability. The manufacturing plant operates dedicated molten filling lines for bulk and semi-bulk formats; packed retail formats are run on separate high-speed jar and tube lines. These two production routes create distinct minimum order quantities and lead times.

Which packaging formats and order thresholds apply?

The plant’s standard packaging formats are listed below. Epoxy phenolic lined open-head steel drums are used for 175 kg fill; flexitank loading requires a dedicated 20 ft container and oxygen-free headspace preparation. Partial flexitank or partial drum container orders are not scheduled. Lead times are ex-works under EXW Incoterms 2020 and exclude freight transit.

Factory-direct packaging formats, minimum order quantities, and ex-works lead times
Packaging formatNet fillMinimum order quantityEx-works lead time
Flexitank in 20 ft container20,000 kg ±5%1 flexitank12–14 working days
Open-head steel drum175 kg80 drums (14,000 kg)7–10 working days
Plastic pail25 kg36 pails per pallet (900 kg)5–7 working days
Retail jar / tube250 g / 500 g or 100 mL / 250 mL20,000 units per SKU18–22 working days

Thermal filling constraints and release-test hold times

Bulk and 175 kg drum formats are filled at 65–75 °C and cooled to below 35 °C before drum lid placement. This post-fill cooling step adds 4–6 hours per drum batch. Flexitank loading includes a full 20 ft container inspection cycle and headspace displacement, which contributes to the longer 12–14 working-day window. The 25 kg pail route is filled from a jacketed holding tank at 55–60 °C; the lower temperature eliminates container pressure venting and shortens release.

Orders are scheduled on a blocked production calendar. Bulk flexitank and 175 kg drum campaigns share a common molten delivery header; switching between these formats requires 4–6 hours of hot-flush and cleanout. Flexitank and drum orders therefore cannot be released on the same shift. This shared-header constraint means minimum order quantities reflect campaign length, not warehouse picking capacity.

Retail jar and tube runs incur a changeover penalty when switching between 250 g and 500 g fill heads. A minimum run of 20,000 units is required to clear fill-head displacement and label transfer validation; smaller runs are not scheduled because residual product loss in the filling chamber exceeds commercial tolerance.

Each production batch is tested for conformance to USP/NF and Ph. Eur. monographs, with cone penetration measured under ASTM D937 before release; this adds 2–3 working days to all formats. Private-label artwork and closure validation add 5–10 working days to retail jar and tube orders. Open-mouth steel drums are not first-fill packaged when ambient relative humidity exceeds 60% during the receiving week unless pre-drying is completed.

Can you provide the safety data sheet, certificate of origin, and regulatory compliance documentation for shipping Vaseline, including any customs HS codes and labeling requirements under FDA or EU cosmetic regulations?

White petrolatum USP/NF (INCI: Petrolatum, CAS 8009-03-8) is produced by hydrogenation followed by high-vacuum filtration. Our export documentation package for bulk tanks, pails, and finished jars comprises a batch-specific safety data sheet (SDS), certificate of origin, certificate of analysis, and regulatory compliance statement. The product is not classified as dangerous goods under ADR, RID, IMDG Code, or IATA Dangerous Goods Regulations; transport labelling therefore falls outside Chapter 5.3 placarding requirements for these modes.

Which Compliance Documents Are Issued for Bulk Shipments?

DocumentContentReference
Safety data sheetGHS sections 1–16; Section 14 states not regulated for transport29 CFR 1910.1200, CLP 1272/2008
Certificate of originBatch-specific country where final purification and filling occurredChamber certification as required by destination customs
Certificate of analysisDrop point, cone penetration, colour, UV absorbanceUSP/NF monograph, Ph. Eur. white soft paraffin monograph
Regulatory statementCosmetic/drug status, GMO/TSE statement, allergen statementEU 1223/2009, FDA 21 CFR 347

SDS Section 2 states “not classified as hazardous” under GHS. Section 9 provides physical property data including melting range, density, and viscosity. Section 14 assigns no UN number, no packing group, and no marine pollutant classification. Our technical team retains the full SDS revision history for each batch.

HS Code Assignment and Customs Tariff Lines

For export, the harmonized system classification for refined white petrolatum is 2712.10. The U.S. Schedule B number is 2712.10.0000; under EU Combined Nomenclature, fully refined material generally falls under 2712 10 90, while crude material falls under 2712 10 10. Ordinary commercial shipments do not require an export license for this tariff line.

When FDA Drug Monograph Labelling Applies

If the material is filled as an OTC skin protectant for the U.S. market, our finished product follows the monograph at 21 CFR 347.10; the Drug Facts panel lists white petrolatum 30–100% as the active ingredient. Labelling includes warnings specified in 21 CFR 347.50. Bulk industrial shipments carry product name, batch number, net weight, and country of origin, but do not carry consumer Drug Facts panels.

Where the material is supplied for EU cosmetic finished goods, Article 19 of Regulation (EC) No 1223/2009 requires the responsible person’s name and address, nominal content, batch code, minimum durability date or period-after-opening symbol, and the ingredient list using the INCI name Petrolatum. A CMR exclusion is maintained because the fully refined petrolatum is not classified under CLP 1272/2008; conformity is supported by batch-specific PAH monitoring and full refining history retained in our technical file.

Technical Support & Inquiry

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