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Methylene Chloride TCI

    • Product Name: Methylene Chloride TCI
    • Factroy Site: Binhai New Area, Tianjin, China
    • Price Inquiry: sales4@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 474464
    Product Name Methylene Chloride (Dichloromethane)
    Chemical Name Dichloromethane
    Cas Number 75-09-2
    Molecular Formula CH2Cl2
    Molecular Weight 84.93 g/mol
    Purity ≥99.5%
    Appearance Colorless clear liquid
    Melting Point -97.6 °C
    Boiling Point 39.8 °C
    Density 1.325 g/cm3 at 20 °C
    Refractive Index 1.424 (nD20)
    Flash Point None
    Solubility Slightly soluble in water; miscible with alcohol, ether, acetone

    As an accredited Methylene Chloride TCI factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Methylene Chloride TCI is supplied in a 500 mL amber glass bottle with secure screw cap, labeled with hazard warnings.
    Container Loading (20′ FCL) 20′ FCL: Drums of Methylene Chloride TCI are loaded, secured, labeled, and ventilated properly for safe transport.
    Shipping Methylene Chloride (TCI) requires careful shipping as UN1593, Class 6.1 (toxic) Packing Group III. Transport in tightly sealed, corrosion-resistant containers, upright and well-ventilated. Ensure hazard labels, documentation, and segregation from oxidizers. Follow IATA/IMDG/ADR regulations; use authorized carriers trained for hazardous chemical transport. Avoid spills, heat, and direct sunlight.
    Storage Store Methylene Chloride (TCI) in its original, tightly closed container in a cool, dry, well-ventilated area away from direct sunlight, heat, and ignition sources. Keep it separate from strong oxidizers, acids, bases, and reactive metals. Protect from moisture, and ensure proper ventilation to avoid vapor accumulation.
    Shelf Life Store tightly closed in a cool, dry, ventilated area. Shelf life is typically three years from manufacture date.
    Application of Methylene Chloride TCI

    In continuous interfacial polycarbonate polymerization, methylene chloride functions as the lower organic phase that dissolves oligomeric polycarbonate while bisphenol A sodium salt partitions into the aqueous upper phase. Reactor feed disclosed for this configuration typically maintains the methylene chloride organic phase at 60–80 wt% of total liquid mass, with the balance aqueous sodium hydroxide at 5–10 wt% caustic and a chain stopper charge of para-tert-butylphenol at 0.5–2.0 mol% relative to bisphenol A. Phosgene is introduced under pH control between 9.5 and 11.5, and the condensation proceeds in a continuous reactor train equipped with turbine impellers and external heat exchange; temperature is held below 35°C to suppress emulsified fines. Crude organic phase is separated in a decanter, then subjected to dilute acid wash, water wash, and hot-water precipitation or steam stripping to remove the solvent. Production-scale continuous polymerizers handling this system require careful control of agitation intensity; excessive impeller shear at the emulsion boundary produces rag layers that carry water into devolatilization, while low shear reduces phosgene mass transfer and broadens molecular weight distribution. Residual dichloromethane in purified resin is quantified by headspace gas chromatography; where pharmacopoeial residual solvent criteria are invoked, the limit is the ICH Q3C Class 2 concentration of 600 ppm and PDE of 6.0 mg/day. After purification, pelletizing on twin-screw extruders with L/D of at least 40:1 strips residual solvent before melt filtration. Melt volume-flow rate is verified per ISO 1133-1:2022, tensile yield stress is characterized per ASTM D638-14, and food-contact resin conversion is evaluated under FDA 21 CFR 177.1580. Terminal product types include optical media substrates, automotive lighting lenses, electronic equipment housings, and injection-molded medical device components.

    What Limits Auxiliary Blowing Agent Concentration in Slabstock Foam Without Collapsing Green Buns?

    Flexible slabstock polyurethane foam production uses methylene chloride as a physical auxiliary blowing agent to lower foam density and modify hardness distribution. The addition ratio in low-pressure slabstock formulations is generally constrained between 3.0 php and 8.0 php; higher levels accelerate skin formation but increase the risk of center scorch and uncontrolled exotherm because the water–toluene diisocyanate reaction raises the bun core above 160°C at thick cross-sections. The process is run on continuous slabstock lines with high-shear pin mixheads, traversing pour conveyors, and forced-air exhaust tunnels; methylene chloride, with a boiling point of 39.6°C, volatilizes immediately after the mixhead pour and participates in bubble nucleation before the rising foam gels. Published plant-level correlation data for this specific DCM/water/TDI index is limited, and the formulation window must be revalidated for each mixhead and tin catalyst level. Emission control and workplace exposure are governed by US EPA 40 CFR Part 63 Subpart III and OSHA 29 CFR 1910.1052, with the OSHA 8-hour TWA at 25 ppm and the STEL at 125 ppm. Terminal products include upholstered furniture cushions, mattress cores, carpet underlay, and automotive interior padding, where density, hardness, and resilience are specified by end-user ASTM testing rather than by residual DCM content alone.

    Closed-Top Vapour Degreaser Chemistry and Freeboard Control

    Aqueous alkaline cleaning baths are not always acceptable for precision ferrous and nonferrous components because of flash rusting, entrained liquid in blind holes, and drying energy. Methylene chloride is charged to vapor degreasers as a neat solvent, not as a dilute additive; the working sump is maintained with a stabilizer package concentration between 50 ppm and 300 ppm to suppress acid hydrolysis, and the oil contamination is held below <30 wt% before reclamation. The operation follows ASTM D3698 and US EPA 40 CFR Part 63 Subpart T; workplace air monitoring is required by OSHA 29 CFR 1910.1052 with an 8-hour TWA of 25 ppm and a 15-minute STEL of 125 ppm. Process equipment is an open-top vapor degreaser with condensing coils at the freeboard, usually a freeboard ratio of 0.75 to 1.0 relative to the vapor zone depth, immersion sump, vapor rinse, and drying station. Because methylene chloride has no flash point under standard closed-cup methods, the process does not require the same electrical classification as hydrocarbons, but thermal decomposition above 120°C requires careful heater watt density. Terminal product types include cleaned machined stainless steel valve bodies, aerospace fasteners, aluminum heat exchangers, and electric motor laminations.

    ApplicationReference StandardLimit or Control Parameter
    Interfacial polycarbonate polymerizationICH Q3C(R8), ISO 1133-1:2022, ASTM D638-14Residual DCM ≤ 600 ppm where invoked; MFR per ISO 1133-1:2022
    Flexible slabstock polyurethane foamUS EPA 40 CFR Part 63 Subpart III, OSHA 29 CFR 1910.1052OSHA TWA 25 ppm, STEL 125 ppm; DCM 3.0–8.0 php
    Vapor degreasingASTM D3698, US EPA 40 CFR Part 63 Subpart T, OSHA 29 CFR 1910.1052Stabilizer 50–300 ppm, oil <30 wt%
    Coating removalEU REACH Annex XVII Entry 59, US EPA 40 CFR Part 751Formulation DCM 60–85 wt%
    Chloroprene contact adhesiveASTM D1876-08, FDA 21 CFR 175.105Solvent DCM 65–80 wt%, viscosity 2,000–5,000 cP
    Pharmaceutical extractionICH Q3C(R8), USP <467>PDE 6.0 mg/day, residual 600 ppm

    Where industrial coating removal requires non-flammable solvent activity without alkaline attack on aluminum substrates, methylene chloride-based remover formulations are applied by brush or airless spray and left to dwell for 5–30 min. The solvent blend in such products commonly contains 60–85 wt% methylene chloride, 5–20 wt% co-solvent such as methanol or isopropanol, 1–3 wt% cellulosic thickener, and 0.5–1.5 wt% paraffin wax to retard evaporation; an acid inhibitor may be added at 0.1–0.5 wt% to protect steel surfaces from hydrogen-induced degradation. Regulatory status is defined by EU REACH Annex XVII Entry 59 and US EPA 40 CFR Part 751, which restrict distribution and require engineering controls, respiratory protection, and worker exposure monitoring in permitted industrial settings. The downstream process proceeds from application to coating blistering, mechanical scraping, and subsequent solvent wipe-down, with spent solids disposed as hazardous waste under local waste codes; ambient-temperature immersion is not specified for heat-sensitive assemblies. Terminal products include stripped steel railcar body panels, aluminum aircraft structural components in authorized maintenance programs, industrial machinery housings, and bridge coating preparation surfaces.

    When a Chloroprene Contact Adhesive Requires Rapid Evaporation Without Ketone Solvent Residue

    Chloroprene-based contact adhesive manufacturing uses methylene chloride as a fast-evaporating carrier solvent in solvent blends that dissolve polychloroprene, alkyl phenolic tackifier resins, magnesium oxide, and zinc oxide at ambient temperatures. The solvent portion generally contains 65–80 wt% methylene chloride, with the balance toluene or aliphatic hydrocarbons; solids content ranges from 20–25 wt%, and the formulated adhesive viscosity is adjusted to 2,000–5,000 cP for roller or spray application. Processing occurs in enclosed high-shear dispersers with water-jacketed bowls, pre-masticated rubber lumps, and slow addition of magnesium oxide to avoid premature heat build-up; batch temperature is kept below 30°C because the solvent boils at 39.6°C. Adhesive performance is evaluated by ASTM D1876-08 peel testing, and where food-packaging lamination is performed, the finished adhesive must meet FDA 21 CFR 175.105. Terminal products include footwear sole bonding, automotive headliner lamination, office furniture edge banding, and mattress foam lamination.

    In pharmaceutical downstream processing, methylene chloride remains employed where extraction selectivity for alkaloids, steroids, or semisynthetic antibiotic intermediates requires a low-boiling halogenated solvent that can be removed under mild vacuum. Batch and continuous countercurrent extraction operations typically charge 5–10 L of methylene chloride per kilogram of dry solid process intermediate, with multi-stage mixer-settler trains operating at 15–25°C to reduce degradation of thermally labile actives. Residual solvent content in the isolated active pharmaceutical ingredient is controlled under ICH Q3C(R8), where methylene chloride is a Class 2 solvent with a PDE of 6.0 mg/day and a concentration limit of 600 ppm; final API powder is tested per USP <467> using headspace gas chromatography. Downstream solvent recovery uses falling-film evaporators and vacuum distillation at 300–500 mbar to maintain reboiler temperatures below 40°C, followed by brine washing and crystallization from anti-solvent. Terminal product types include purified alkaloid salts, semi-synthetic penicillin intermediates, steroid APIs for anti-inflammatory dosage forms, and lyophilized injectable powders.

    Supplied in bulk, 25 kg drums and 200 L steel drums. We provide import‑export service for global customers. Please contact us for latest price.

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    Certification & Compliance
    More Introduction

    Methylene Chloride TCI (dichloromethane, CAS 75-09-2) is supplied as a high-purity reagent for organic synthesis, liquid-liquid extraction, surface preparation, and laboratory cleaning. The product identity is defined by the linear formula CH₂Cl₂, a molar mass of 84.93 g mol⁻¹, a boiling range of 39.8–40.0 °C at 101.3 kPa, a density of 1.325 g mL⁻¹ at 25 °C, and a refractive index n20/D of 1.4242. TCI packaging uses amber glass bottles with fluoropolymer-lined caps in 500 mL and 1 L formats. The TCI catalogue item is the high-purity reagent, not a formulated degreasing solvent; stock-keeping units vary by bottle size and stabilizer option, and the lot-specific certificate of analysis should be checked before use because preservative-free and stabilizer-containing packaging configurations are not interchangeable in downstream catalytic reactions.

    What Controls the Purity Profile of TCI Methylene Chloride?

    Purity is assessed by gas chromatography with flame ionisation detection, Karl Fischer titration, and gravimetric residue analysis. The critical failure modes are hydrolytic release of free acid, accumulation of higher-boiling stabilizer residues, and water ingress during repeated bottle opening. A representative release profile is presented in Table 1. Gas chromatographic assay typically uses a 30 m × 0.32 mm fused-silica column coated with 5% phenyl methylpolysiloxane; the stationary phase separates chloroform, carbon tetrachloride and 1,2-dichloroethane from dichloromethane. These halocarbon impurities, if present, can quench organometallic catalysts or co-elute with target analytes in GC-MS extract scans. Water is determined by coulometric Karl Fischer titration under ASTM E203-16; water above 0.05% promotes slow hydrolysis and raises the free-acid value. Nonvolatile residue is measured by evaporation of a 100 mL aliquot in a platinum or borosilicate dish under ASTM D1353-13. The ≤0.005% limit is operational because less volatile impurities concentrate in rotary evaporator residues and distort total dissolved solids measurements.

    ParameterTest method / equipmentRepresentative limit
    AssayGC-FID, fused-silica column≥99.5%
    WaterCoulometric Karl Fischer, ASTM E203-16≤0.05%
    Nonvolatile residueEvaporation, ASTM D1353-13≤0.005%
    Free halogens / free acidArgentometric titration or ion chromatography≤0.001 meq g⁻¹
    ColorASTM D1209-05(2019)≤10 APHA
    StabilizerGC-MS, certificate of analysislot-specific; none, amylene, or ethanol

    The tabulated values are release criteria, not a guarantee of performance in any specific reaction. For catalytic hydrogenation, olefin metathesis, and radical polymerisation, the stabilizer identity and concentration must be checked on the certificate of analysis because amylene at even low residual levels can poison palladium and platinum surfaces. If a stabilizer-free item is not in stock, the solvent can be washed with sulfuric acid and distilled over calcium hydride under dry nitrogen using Schlenk-type glassware, but this laboratory preparation introduces a distillation step and a separate acid-handling operation.

    Liquid-liquid extraction with dichloromethane places the organic phase below the aqueous phase where the density of 1.325 g mL⁻¹ creates a stable lower layer. Continuous extractors for chlorinated solvents require fluoropolymer stopcocks and PTFE sleeves because chlorinated solvents swell and embrittle polyolefin fittings. The low boiling point of 39.8–40.0 °C permits concentration in a rotary evaporator at bath temperatures of 35–40 °C and pressure ramps from 500 mbar to 200 mbar. This reduces thermal damage to thermolabile analytes relative to higher-boiling chloroform or toluene. Compared with technical-grade dichloromethane, TCI product is differentiated by low nonvolatile residue and controlled free halogens; technical solvent grades often carry unspecified stabilizer packages that appear in GC-MS as unresolved complex matter in the C9–C14 range. Recoveries of semivolatile analytes should be verified by matrix spikes under US EPA 3510C or an equivalent validated liquid-liquid extraction protocol. Published data for TCI-specific extraction recoveries in environmental matrices are limited, so matrix-matched validation remains the operative control.

    Because dichloromethane is classified as a suspected human carcinogen under GHS H351, the TCI product should be handled only in fume hoods with demonstrated containment. Storage at 15–25 °C in the original amber bottle, with the cap closed under dry air or nitrogen, limits water uptake and photochemical oxidation. Repeated opening of the bottle is a common source of batch-to-batch variance in trace water; after 6 months of intermittent use, coulometric Karl Fischer re-testing is recommended before use in water-sensitive reactions. The product is not classified as flammable, but the vapour is heavier than air and can accumulate in low-lying areas; work areas without ramped ventilation should be avoided. The stabilizer, when present, may be consumed over time because it reacts with acidic species generated by slow degradation; this is another reason to check the certificate of analysis before catalytic work.

    When Drying and Stabilizer Selection Determine Suitability in Organometallic Work

    Organometallic transformations impose more stringent drying requirements than bulk release tests. Dichloromethane intended for Grignard reagents, alkyllithium compounds, Friedel–Crafts catalysts, or low-valent transition-metal complexes is dried by passage through an anhydrous solvent purification system with activated alumina and copper catalyst columns under dry nitrogen, or by reflux over calcium hydride followed by distillation in Schlenk-type glassware. The target water content after drying is <10 ppm by coulometric Karl Fischer; this is a process threshold rather than a purchase specification. Amylene-stabilized dichloromethane is a problematic feed for this drying sequence because 2-methyl-2-butene boils at 38.6 °C, too close to dichloromethane for complete separation by simple distillation. The olefinic stabilizer can form π-allyl complexes or compete for open coordination sites on palladium, platinum, and ruthenium centres. If amylene-free material is not available, the stabilizer is removed by stirring with concentrated sulfuric acid, separating the acid layer, washing with water and sodium bicarbonate, drying over activated 4A molecular sieves, and distilling under inert gas. This procedure is exothermic and must be performed in a fume hood with continuous ice-bath cooling of the wash vessel. Residual olefin is confirmed by headspace GC-MS before catalyst loading; an absence of the amylene molecular ion in extracted-ion chromatograms is the operational endpoint.

    Vapour Degreaser Chemistry, Thermal Stability, and Equipment Compatibility

    Vapour degreasing is not an intended use of TCI high-purity methylene chloride. Industrial vapour degreasing grades are formulated with acid-scavenging stabilizers and high-temperature inhibitors that suppress decomposition on hot vapour-generating surfaces. Reagent-grade dichloromethane without such additives may generate hydrogen chloride and traces of phosgene at metal surfaces above 120 °C; the risk is highest on overheated immersion heaters or in unvented vapour baths. Equipment compatibility is limited to stainless steel, glass, PTFE, and PVDF. Aluminium, zinc, magnesium, sodium, potassium, and strong alkalis are incompatible and can induce dehalogenation. The OSHA standard 29 CFR 1910.1052 establishes an 8-hour time-weighted average permissible exposure limit of 25 ppm, a 15-minute short-term exposure limit of 125 ppm, and an action level of 12.5 ppm. Fume hood containment should be verified under ASHRAE 110-2016; exposure monitoring is performed with pump-and-sorbent tubes analyzed by thermal desorption GC-MS or with calibrated photoionization detectors.

    DesignatorValue / classification
    CAS registry75-09-2
    EC number200-838-9
    UN transportUN 1593, Class 6.1, Packing Group III
    GHS classificationCarc. 2 (H351); Skin Irrit. 2 (H315); Eye Irrit. 2 (H319); STOT SE 3 (H336)
    OSHA PEL25 ppm TWA, 125 ppm STEL, action level 12.5 ppm under 29 CFR 1910.1052
    REACH restrictionAnnex XVII entry 59 restricts paint-stripper formulations containing dichloromethane; laboratory reagent use requires downstream exposure controls.

    On solvent recovery units using wiped-film evaporators, the wall temperature must be held below 120 °C to avoid chloride release from dichloromethane decomposition; operators monitor the recovered distillate for free chloride by Argentometric titration or ion chromatography. This field observation is not unique to TCI material and applies to all high-purity chlorinated methanes. In laboratory rotary evaporators, the condenser should be vented to the fume hood, and the water bath should not exceed 40 °C during prolonged concentration of dichloromethane extracts.

    Chloroform replacement is not a direct density-for-density substitution

    Dichloromethane has a density of 1.325 g mL⁻¹ at 25 °C and a dielectric constant of 8.93; chloroform has a density of 1.492 g mL⁻¹ at 25 °C and a dielectric constant of 4.81. These values are not trivial interchangeables: chloroform’s higher density and lower dielectric constant alter phase separation, emulsion behaviour, and partition of moderately acidic or basic analytes. The boiling point difference of 21.4 °C means that dichloromethane concentrates faster and at lower bath temperature, but the lower boiling point also increases losses during prolonged extraction. The TCI high-purity product reduces the stabilizer-derived background that can otherwise interfere with trace-level quantification, but it does not reproduce chloroform’s selectivity for certain alkaloid or polar lipid fractionations. Method transfer from chloroform to dichloromethane therefore requires revalidation of extraction recovery, chromatographic retention, and detector background. Published data for this specific replacement in preparative natural-product isolation is limited; a matrix-spike recovery study remains the appropriate verification for each sample type.

    Trace aromatic impurities and stabilizer residues in dichloromethane absorb in the low-ultraviolet region. The UV transmittance cutoff of high-purity dichloromethane is near 233 nm; for HPLC methods with UV detection below 235 nm, a spectrophotometric or HPLC-grade dichloromethane should be specified because the TCI reagent item intended for synthesis may not carry the additional absorbance guarantees of chromatography solvents. This distinction is operational, not a purity defect: the nonvolatile residue and water limits remain valuable for extraction and reaction use, while low-wavelength UV background must be measured lot-by-lot if no chromatographic grade is available.

    Cleaning of sintered-glass frits and laboratory glassware with dichloromethane is limited to nonpolar residues. The solvent should not be combined with hot-air drying guns or heated nitrogen above 60 °C because residual liquid in confined glass frits can thermally decompose and release hydrogen chloride. If highly fluorinated or silicone greases are present, dichloromethane may leave a low-level residue that is better removed by a two-step rinse with hexane or acetone. This operational boundary arises from the solvent’s swelling behaviour and chlorinated-methane degradation chemistry, not from a specific TCI product deficiency.