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Methylene Chloride DCM Degreaser
- Product Name: Methylene Chloride DCM Degreaser
- Factroy Site: Binhai New Area, Tianjin, China
- Price Inquiry: sales4@ascent-chem.com
- Manufacturer: Ascent Petrochem Holdings Co., Limited
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- In terms of specification, Methylene Chloride DCM Degreaser is supplied with 99.9% minimum purity and 0.01% maximum moisture content, making it suitable for precision vapor degreasing of metal components.
| HS Code | 485945 |
| Chemical Name | Methylene Chloride |
| Cas Number | 75-09-2 |
| Molecular Formula | CH2Cl2 |
| Appearance | Clear, colorless liquid |
| Odor | Ether-like, sweet odor |
| Boiling Point | 39.6 °C (103.3 °F) |
| Melting Point | -96.7 °C (-142.1 °F) |
| Density | 1.322 g/cm³ at 25 °C |
| Vapor Pressure | 47.4 kPa at 20 °C |
| Solubility In Water | Slightly soluble (20 g/L at 20 °C) |
| Flash Point | No flash point (non-flammable in liquid form) |
| Autoignition Temperature | 556 °C (1,033 °F) |
| Vapor Density | 2.93 (air = 1) |
| Evaporation Rate | High (11.2 vs butyl acetate = 1) |
| Dielectric Constant | 9.08 at 20 °C |
As an accredited Methylene Chloride DCM Degreaser factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Methylene Chloride DCM Degreaser packaged in a 1-gallon (3.78 L) metal can with secure lid and prominent hazard warning labels. |
| Container Loading (20′ FCL) | 20′ FCL: Load UN1593 Methylene Chloride DCM degreaser in sealed drums, upright, secured, labeled, ventilated, segregated from foodstuffs. |
| Shipping | Methylene Chloride DCM degreaser ships as a regulated hazardous material (UN1593, Class 6.1). It must be packaged in UN-approved containers, properly labeled and documented, and transported by ground freight only. Air shipment is prohibited. Ensure compliance with all DOT/IATA/IMDG regulations and segregation from incompatible materials. |
| Storage | Store methylene chloride (DCM) degreaser in a cool, dry, well-ventilated area away from sunlight, heat, and ignition sources. Keep containers tightly closed and upright, protected from moisture and incompatible substances like strong oxidizers and certain metals. Use corrosion-resistant secondary containment, ensure clear labeling, and maintain access to safety showers and eyewash stations. |
| Shelf Life | Shelf life is approximately 2–5 years when stored properly in sealed containers away from moisture and sunlight. |
In AS9100D-certified aerospace machine shops operating closed-loop vapor degreasing cells, methylene chloride DCM degreaser is charged into the boil sump at 100 wt% as vapor-degreasing grade; the formulation addition ratio is undiluted product with a stabilizer package not exceeding 0.05 wt% cyclohexane oxide equivalent, and no hydrocarbon co-solvent is introduced. The controlling raw-material purchase specification is ASTM D4701-00(2020), with batch certificates for water-soluble halides by ASTM D2988-96(2021) and acid acceptance by ASTM D2942-02(2017). Equipment operation follows ASTM D3698-04(2015); AS9100D clause 8.5.1 requires the cleaning process parameters to be defined, monitored, and revalidated before release of flight-critical hardware. The production line is a three-stage open-top vapor degreaser with type 304L stainless steel sumps, magnetically coupled distillate return pumps, a plate-type water separator rated for 0.3 L/min continuous water rejection, and a two-stage condenser using a 10–15°C primary coil and a -20°C secondary coil to suppress vapor diffusion. Ultrasonic transducers operate simultaneously at 25 kHz and 40 kHz with a power density of 6–10 W/cm², and boil sump temperature is held at 39–42°C. Freeboard ratio is set at 1.0 for new equipment under 40 CFR Part 63 Subpart T; lip-vent extraction velocity is maintained above 0.75 m/s across the loading face. Rack speed for aerospace parts with blind tapped holes is limited to 0.8–1.2 m/min to avoid condensed solvent pooling in recesses. The DCM degreaser removes chlorinated sulfurized cutting fluids, fluorocarbon-based tapping compounds, and boron nitride anti-seize residues from Ti-6Al-4V landing gear actuator housings, 17-4 PH fuel system fasteners, and Inconel 718 turbine casing segments. Operational boundaries include exclusion of polycarbonate sight windows, fluorosilicone gaskets, and EPDM seals from wetted paths; titanium parts are processed at room temperature only because hot chloride contact above 130°C in dry-down zones may induce stress-corrosion risk.
How Does DCM Degreaser Manage the Production Bottleneck in Automotive Remanufacturing Lines?
Remanufacturing cells for cast iron and aluminium brake calipers and transmission valve bodies use a two-stage cleaning sequence in which the first tank is formulated at 75–85 wt% DCM degreaser with 15–25 wt% low-aromatic aliphatic hydrocarbon co-solvent to soften oxidised gear oil, burnt brake fluid, and carbonised diesel soot, and the second tank is charged at 100 wt% DCM degreaser for vacuum vapor rinse and drying. The vacuum vapor stage runs at 35–40°C under 20–25 kPa absolute chamber pressure in a rotary basket machine, with a total cycle of 6–9 min; the reduced pressure lowers the boiling point and shortens the drying segment for high-mass valve bodies. Compliance is anchored to ISO 16232-10:2007 for fluid circuit component cleanliness expression and IATF 16949:2016 for production part release control; halogenated solvent machine emissions are managed under 40 CFR 63 Subpart T. After solvent cleaning, the load is transferred within 4 h to a 1.5 t shot-blast line that generates a 25–50 µm anchor profile for phosphate conversion coating or zinc thermal spray on remanufactured caliper bodies. Process-scale failure modes observed in such lines include solvent phase separation when cold immersion moisture exceeds 0.2 vol%, vapor carry-over caused by overloaded baskets above 350 kg, and elastomer swelling in unapproved seal materials exposed to the solvent blend. Terminal products are remanufactured brake calipers, automatic transmission valve bodies, and diesel injector cores. Published data for exact bath life under these production conditions is limited; operators control acid acceptance and non-volatile residue per batch.
Injection Mold Release-Agent Depolymerisation and PVD Pre-Coating Solvent Wash
Tool maintenance departments use DCM degreaser at 100 wt% in closed-loop ultrasonic immersion lines to remove methyl-phenyl RTV release agent, oxidized polyol ester hydraulic oil, and carbonized gate residue from hardened H13 mold inserts, ejector sleeves, and hot-runner tips. The addition ratio is not diluted with co-solvent because a lower solubility parameter match reduces removal of crosslinked silicone domains. Compliance is set by IEST-STD-CC1246D surface cleanliness level L/10 or better, and PVD coating vendors require non-volatile residue below 25 mg/ft² before TiAlN or CrN deposition. The cleaning process uses 30 kHz ultrasonic agitation at 6–8 W/cm² and bath temperature 25–30°C, followed by a distillate rinse trough, nitrogen blow-off at 0.3–0.5 MPa, and vacuum baking at 80°C for 2 h inside the coating machine load lock. Terminal products include automotive connector mold halves, gas-assist mold inserts, and PVD-coated ejector pins and forming dies. Operational limitation: the solvent must not contact polycarbonate mold covers, polyurethane wiper rings, or ABS inspection covers because DCM degreaser causes rapid surface dulling and cracking.
Before brazing evaporator copper coils and hermetic compressor shell subassemblies, DCM degreaser is applied at 100 wt% in a vacuum degreasing line to remove mineral-oil drawing lubricants, copper fines, and press-forming esters from U-bend tubes and steel shells. The formulation addition ratio for HVAC/R tube-cleaning is undiluted product, with water content held below 50 ppm by the inline azeotrope water separator; no aqueous detergent is introduced because residual moisture would create brazing porosity and copper pitting under refrigerant exposure. Compliance is set by ASTM B280-18 for seamless copper tube dimensions and surface quality, UL 207 for hermetic refrigerant motor-compressors, and ISO 9001:2015 clause 8.5.1 for validated cleaning process control. The cleaning sequence consists of a 3-min vapor hold to condense solvent on the copper surfaces, ultrasonic agitation at 28 kHz, a distillate spray rinse, and vacuum drying below 2 kPa absolute. After cleaning, components are transferred within 4 h to conveyor furnaces for silver-phosphorus brazing at 650–750°C under nitrogen-hydrogen atmosphere to prevent recontamination. Terminal downstream products are brazed evaporator coils, reversing valve bodies, and hermetic compressor housings. Process boundary: water-soluble halides in the degreaser are verified by ASTM D2988, acid acceptance by ASTM D2942, and surface residue is checked by ion chromatography; DCM degreaser must not contact EPDM O-rings, polycarbonate sight glasses, or nylon valve components used in final assembly. Production-scale experience shows that loading copper tube bundles above the basket freeboard line creates uneven solvent condensation and water entrapment, so bundle heights are limited to 70% of the vapor zone height. Published data for this specific configuration is limited; operating limits are therefore established by the cleaning equipment manufacturer’s thermal balance calculation.
When DCM Degreaser Replaces n-Propyl Bromide in Precision Optics Metal Mask and Solder Stencil Cleaning
Electroformed and laser-cut 304 stainless steel solder stencils with aperture widths from 0.075 mm downward are cleaned in reciprocating spray equipment where DCM degreaser is used as a replacement for n-propyl bromide after regulatory restrictions on nPB. The formulation addition ratio in this process is 100 wt% DCM degreaser in the spray sump, with the vapor rinse stage charged from the same product; acid acceptor content is monitored at 0.02–0.05 wt% sodium hydroxide equivalent to counteract any chloride generation from solder flux residues. Compliance includes IPC J-STD-001F cleanliness requirements for soldered electrical assemblies, IEST-STD-CC1246D for particulate levels on optical aperture masks, and ASTM D3698-04(2015) for vapor degreasing operation. The downstream process passes the metal stencil through spray impingement at 0.4–0.6 MPa nozzle pressure and 25°C solvent temperature, then vapor rinse at 39–42°C and HEPA-filtered hot-air drying at 60°C for 10 min. After cleaning, aperture edge acuity is verified by optical comparator at 20×, and residual flux ion content is tested by omegameter against an acceptance limit below 1.56 µg/cm² sodium chloride equivalent. Terminal products include fine-pitch solder stencils for 0201 and micro-BGA placement, electroformed nickel encoder discs, and stainless steel optical slit masks used in laser alignment systems. Operational boundary: DCM degreaser is not applied to polyimide or acrylic optical films; it attacks acrylic and polycarbonate polarizer films, so metal masks are cleaned only after delamination from bonded polymer substrates.
Medical Device Pre-Passivation Cleaning Requires Chloride-Controlled DCM Degreaser
Stainless steel surgical instruments and dental scaler blanks are processed through a solvent degreasing step immediately before acid passivation to remove sulfurized cutting oil, lapping compound, and vacuum grease residues that would otherwise shield the surface from citric or nitric acid treatment. The DCM degreaser is charged at 100 wt% in a closed-loop vapor degreasing system; the formulation addition ratio is not reduced with water because aqueous dilution would introduce chloride ion carryover and compromise the passivation step. Compliance is established under ISO 13485:2016 clause 8.5.1 for controlled production, FDA 21 CFR 820.70(c) for cleaning and sanitation of manufacturing equipment, and ASTM A967-17 for chemical passivation of stainless steel parts. The degreasing process uses 39–42°C vapor hold, 30 kHz ultrasonic immersion, distillate spray rinse, and vacuum drying below 1 kPa absolute for 8–12 min to eliminate solvent retention in box locks and serrated jaw teeth. Acid acceptance is verified per ASTM D2942, water content held below 50 ppm, and water-soluble halides checked by ASTM D2988 to avoid chloride-induced pitting on 17-4 PH and 420 martensitic stainless steel. Downstream, the instruments are passivated in 20–25 vol% nitric acid at 50–60°C for 30 min, then neutralized and dried. Terminal products include reusable stainless steel forceps, rongeurs, osteotomes, dental scaler tips, and orthopedic trial instruments. Process limitation: DCM degreaser is not used on titanium implantable components in this line because chloride ion control above 10 µg/cm² may conflict with osseointegration requirements; such components are routed to alternative aqueous cleaning.
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- Methylene Chloride DCM Degreaser is manufactured under an ISO 9001 quality system and complies with relevant regulatory requirements.
- COA, SDS/MSDS, and related certificates are available upon request. For certificate requests or inquiries, contact: sales4@ascent-chem.com.
Designated Model MCD-DG 99.9, the Methylene Chloride DCM Degreaser is a stabilized chlorinated solvent based on dichloromethane, CAS 75-09-2 and EINECS 200-838-9, supplied for industrial low-temperature degreasing of metallic and ceramic substrates. The base solvent has a molecular weight of 84.93 g/mol, a boiling point of 39.6 °C at 101.325 kPa, a vapor pressure of 47.3 kPa at 20 °C, and a liquid density of 1.326 g/cm³ at 20 °C. The as-supplied material is specified to a minimum dichloromethane assay of 99.90 area% by gas chromatography with flame ionization detection; the remaining fraction consists of an acid-acceptor stabilizer package intended to neutralize hydrogen chloride generated by slow solvent decomposition. The product is a clear and colorless liquid with a maximum Pt-Co color of 10 under ASTM D2108.
Standard supply configurations include 200 L epoxy-phenolic lined steel drums and 1000 L stainless steel intermediate bulk containers equipped with closed-transfer adapters. Because the vapor pressure reaches 47.3 kPa at 20 °C, storage must remain below 30 °C with pressure-relief venting. The solvent is regulated under 29 CFR 1910.1052, with an 8-hour time-weighted average permissible exposure limit of 25 ppm and a short-term exposure limit of 125 ppm. This product is not supplied for consumer paint stripping or aerosol uses.
| Property | Limit | Test method |
|---|---|---|
| Dichloromethane assay | 99.90 area% minimum | Gas chromatography with FID |
| Color | 10 Pt-Co maximum | ASTM D2108 |
| Density at 20 °C | 1.320–1.330 g/cm³ | ASTM D2111 |
| Water content | 0.020 wt% maximum | ASTM D1364 |
| Acidity as HCl | 0.0010 wt% maximum | ASTM D1613 |
| Distillation range at 101.3 kPa | 39.0 °C to 40.5 °C, 95 vol% recovered | ASTM D1078 |
| Total acid acceptance | 0.10–0.20 wt% as NaOH | ASTM D2942 |
| Kauri-butanol value | 136 typical | ASTM D1133 |
The narrow distillation range is not merely a compositional marker; it controls reboiler behavior in solvent recovery stills. If high-boiling contaminants accumulate above 40.5 °C, the vapor zone becomes enriched in less volatile oils and the degreasing rate declines. In continuous recovery stills, the residue is drawn off when the still-bottom temperature exceeds 45 °C. Water separators must be fabricated from materials resistant to acidic hydrolysis; stainless steel 316L is acceptable only when acid acceptance is maintained within specification.
What Stabilizer Acid Acceptance Level Prevents Solvent Decomposition in Closed-Loop Degreasers?
Total acid acceptance is maintained between 0.10 wt% and 0.20 wt% as NaOH when measured according to ASTM D2942. The acid acceptor scavenges hydrogen chloride as it forms, preventing free acidity from rising above 0.0010 wt% as HCl under ASTM D1613. In closed-loop vapor degreasers with immersion-heated sumps, local heater-surface temperatures above 120 °C accelerate the hydrolysis of dichloromethane, especially when water separates poorly. Water must be removed continuously by a decanter or separated sump because the saturation solubility of water in the solvent is approximately 0.2 g/100 g at 20 °C, and excess water drives hydrochloric acid formation and lowers stabilizer life. When acid acceptance falls below 0.10 wt%, free acidity attacks 300-series stainless steel and can initiate pitting at liquid-vapor interfaces. Open-top degreasers therefore require a freeboard ratio of at least 0.75 times the tank width, with freeboard chillers operated between −10 °C and −20 °C to suppress vapor escape. Heaters should be fabricated from 316L stainless steel, nickel, or PTFE-coated elements; titanium is generally resistant but not preferred where water contamination is likely.
Application in vapor degreasing relies on a two-phase equilibrium: the boiling sump generates a saturated vapor zone at 39.6 °C, and condensation on cooler workpieces transfers solvent to the surface. The solvent dissolves heavy machining oils, chlorinated paraffins, waxes, drawing compounds, buffing residues, and rosin flux; the Kauri-butanol value of 136 under ASTM D1133 indicates stronger solvency than perchloroethylene or n-propyl bromide. Parts with blind holes and tight tolerances are cleaned in ultrasonic tanks operating at 25 kHz or 40 kHz transducer frequency, with power densities of 10 W/L to 30 W/L. After cleaning, a separate vapor rinse or clean-solvent flush prevents redeposition of oil. Because the solvent evaporates without leaving an ionic residue, no deionized water rinse is required, but the work zone must be ventilated to maintain airborne concentrations below 25 ppm.
Vapor degreasing cells should include a water separator and a desiccant breather on storage tanks. Condensed water forms a separate upper phase above the denser solvent because the solvent density is 1.326 g/cm³; gravity separation is therefore effective. The water layer must be removed before acid extraction depletes the stabilizer. Cartridge filters rated at 10 µm to 25 µm remove particulate and extend solvent life in continuous recovery systems.
Ultrasonic Immersion, Cold Swab, and Flushing Operations
Ultrasonic immersion is used for metallic parts with chips, polishing residues, or baked-on oils. The cavitation field in small tanks is typically generated with 40 kHz transducers, while larger lines may use 25 kHz for coarser particulate removal. Stainless steel 316L and 304L, copper alloys, brass, glass, and most ceramics are accepted when the stabilizer acidity is within specification. Seals and gaskets should be limited to PTFE, PFA, or PVDF; nitrile, neoprene, EPDM, silicone, and natural rubber exhibit unacceptable swell and hardening after repeated exposure. For cold cleaning, the solvent is applied by saturated lint-free swab or brush to localized areas on electrical contacts, sensor housings, and tool surfaces. The high evaporation rate creates a visible condensation boundary and rapid cooling of the substrate; this effect can condense atmospheric moisture in humid environments unless the part is dried with filtered compressed air or placed in a low-temperature drying cabinet.
Maintenance cleaning of adhesive residues from steel and glass tooling is performed by immersion or flow-over application. The solvent penetrates cyanoacrylate, pressure-sensitive adhesive, and partially cured epoxy films by diffusion rather than by bulk dissolution alone, so soak time is governed by film thickness and crosslink density. Published data for this specific configuration is limited; performance should be qualified on production coupons with the actual adhesive lot and substrate roughness before full-scale replacement. Unlike low-aromatic hydrocarbon degreasers, this solvent has no closed-cup flash point under ASTM D56; however, lower operator exposure limits of 25 ppm require powered local exhaust ventilation and continuous air monitoring.
When Perchloroethylene or n-Propyl Bromide Is Evaluated as a Replacement
Perchloroethylene has a higher boiling point of 121.1 °C and a lower Kauri-butanol value of 90 under ASTM D1133. It is less aggressive toward some polymers but requires higher sump temperatures and longer dwell on oxidized mineral oils. n-Propyl bromide has a boiling point of 71 °C and a Kauri-butanol value of 125, placing it closer to dichloromethane in solvency, but its acid-acceptance demand in vapor degreasing is more sensitive to water and light-metal contact. DCM remains suitable when the workpiece must remain below 40 °C to avoid thermal distortion of thin-walled assemblies or when fast evaporation is required after cleaning. The choice is application-specific and is governed by substrate compatibility, vapor pressure, toxicity thresholds, and waste classification rather than by a single property.
| Solvent | Boiling point at 101.325 kPa | Density at 20 °C | KB value, ASTM D1133 | Flash point, ASTM D56 | Primary industrial limitation |
|---|---|---|---|---|---|
| Methylene chloride degreaser | 39.6 °C | 1.326 g/cm³ | 136 | None | Exposure limit, polymer stress cracking |
| n-Propyl bromide | 71 °C | 1.343 g/cm³ | 125 | None | Stabilizer acid control and metal reactivity |
| Trichloroethylene | 87.2 °C | 1.464 g/cm³ | 130 | None | Carcinogenicity and regulatory pressure |
| Perchloroethylene | 121.1 °C | 1.623 g/cm³ | 90 | None | Higher operating temperature, lower solvency |
Material compatibility boundaries are defined by stress cracking and swell data. DCM aggressively attacks polycarbonate, acrylic, ABS, polystyrene, and rigid PVC; elastomers should be limited to PTFE, PFA, or PVDF. Aluminum, zinc, magnesium, and titanium require strict control of water content below 0.020 wt% and free acidity below 0.0010 wt% because acid generation can cause surface attack. The solvent is incompatible with strong oxidizers, alkali metals, and concentrated caustic solutions; exposure to hot surfaces above 120 °C can generate hydrogen chloride and trace decomposition products. Spent solvent from degreasing operations is classified as F002 under 40 CFR 261.31 and must be managed as hazardous waste.
Industrial use only. The product is within the scope of REACH Annex XVII Entry 59 for paint stripper restrictions, and workplace exposure in the United States is governed by 29 CFR 1910.1052. Facilities without closed-transfer liquid handling, refrigerated freeboard, local exhaust ventilation, and exposure monitoring should not operate this solvent in open-top degreasing cells.
