Product Overview

The report provides detailed analysis essential for establishing a vinylidene chloride production plant. It encompasses all critical aspects necessary for vinylidene chloride production, including the cost of vinylidene chloride production, vinylidene chloride plant cost, vinylidene chloride production costs, and the overall vinylidene chloride production plant cost. Additionally, the study covers specific expenditures associated with setting up and operating a vinylidene chloride production plant. These encompass production processes, raw material requirements, utility requirements, infrastructure needs, machinery and technology requirements, manpower requirements, packaging requirements, transportation requirements, and more.

Vinylidene Chloride Market Analysis: Demand and Supply Analysis, and Sourcing

Vinylidene chloride, also called 1,1-dichloroethylene or VDC, is a chlorinated two-carbon monomer. It is a clear, colorless, very volatile liquid with a sweet, chloroform-like odor. It boils near room temperature and polymerizes easily, so it is always shipped with an inhibitor. Vinylidene chloride is made from 1,1,2-trichloroethane, a by-product of the vinyl chloride and ethylene dichloride chain. Most of it is used captive by the same companies that make PVDC barrier resins.

Vinylidene chloride is mainly bought by PVDC resin manufacturers, barrier coating producers, fluorochemical companies, and specialty chemical manufacturers. PVDC is combined with vinyl chloride, methyl acrylate, or acrylonitrile to make films, coatings, and latexes that prevent oxygen and water vapor from passing through easily. These materials are used in food packaging, pharmaceutical blister packs, packaging films, cling wraps, and barrier coatings. Vinylidene chloride is also used to make chlorinated and fluorinated chemical intermediates. Other buyers include latex manufacturers, film converters, and electronics material suppliers. A vinylidene chloride demand and supply analysis must weigh barrier packaging demand, fluorochemical quotas, chlor-alkali economics, and environmental rules on chlorinated solvents. Supply sits with integrated PVDC makers in Japan, Korea, the US, and Europe, plus several Chinese chlorine chemical groups. Buyers check purity, inhibitor level, acidity, water, color, and trace chlorinated impurities on every lot. Merchant prices depend on purity, lot size, delivery mode, inhibitor, and hazard freight.

Summary of the Product, Grades, and Uses

Vinylidene chloride has the formula C2H2Cl2 and a molar mass of about 96.94 g/mol under CAS 75-35-4. Its density is about 1.21 g/cm³ at 20 degree Celsius, and it boils near 31.6 degree Celsius and melts near -122.5 degree Celsius. Its flash point is well below 0 degree Celsius, and its vapor pressure at room temperature is about 600 mm Hg. It is nearly insoluble in water but mixes with ethanol, acetone, benzene, ether, and chloroform. Vinylidene chloride can polymerize violently during storage if the inhibitor is lost or contaminated. It is also toxic and reactive, so it needs careful handling at every stage.

Vinylidene chloride grades are split by purity and by inhibitor system. Commercial monomer grades run at 99% or higher purity. Polymer grades limit acetylenic compounds, other dichloroethylenes, and trichloroethane. Inhibitors such as MEHQ hold the monomer stable in storage and transport. High-purity grades serve semiconductor fabrication, where the compound helps grow high-purity silicon dioxide films. Most monomers move by pipeline or in insulated, nitrogen-padded containers. Main specification points are purity, inhibitor level, acidity, water, color, and trace chlorinated impurities.

Vinylidene chloride is mainly used to make polymers that provide strong barriers against oxygen and water vapor. PVDC copolymers also resist oil and grease and help retain the flavor of packaged products. The monomer is also used in chemical synthesis because of its reactivity. In packaging, PVDC helps keep food fresh for longer, reduce waste, use thinner films, and retain aroma.

Main End-Uses of Vinylidene Chloride

PVDC resins are the largest demand segment for vinylidene chloride, taking about 58% of volume in one industry review. Extrusion resins go into multilayer films and casings for meat, fish, poultry, and cheese. Latex grades coat films, paper, and pharmaceutical base webs. Typical water vapor transmission for these polymers runs from 0.05 to 10 g/m²/day, and oxygen transmission can fall below 1 cc/m²/day/bar. Cling wraps in Japan still use PVDC, while the US Saran Wrap brand moved to polyethylene in 2004. Each of these buyers sets limits on purity, color, inhibitor, and residual impurities. Pharmaceutical packaging buyers also ask for food contact approvals, change control, audits, and long-term supply.

Organic synthesis intermediates form the next major end-use segment for vinylidene chloride. It can be converted to 1,1,1-trichloroethane and to fluorinated intermediates such as HCFC-141b and HCFC-142b. HCFC-142b in turn feeds vinylidene fluoride, the monomer for PVDF binders used in lithium-ion batteries. Production quotas under the Montreal Protocol cap HCFC output for emissive use. China also sets separate quotas for HCFC-142b used inside its own fluoropolymer chains.

Smaller volumes go to coatings, flame-resistant binders, lacquer resins, and semiconductor processing. Carpet backing binders use vinylidene chloride copolymers for flame resistance. Water-based PVDC latexes protect metal and building surfaces against corrosion. Demand in these niches is steady but small. For coating users, key factors are film formation, adhesion, barrier, corrosion resistance, and drying speed.

Vinylidene Chloride Market Risks

Vinylidene chloride carries feedstock and chlor-alkali risk above all else. Its main feedstock, 1,1,2-trichloroethane, comes from the vinyl chloride and ethylene dichloride chain, so supply follows PVC and chlorine operating rates. Caustic soda, the main reagent, moves with chlor-alkali balances. Chlorine and ethylene prices also feed into feedstock cost. Changes in PVC demand, chlorine output, power prices, and ethylene supply all shift trichloroethane availability.

Vinylidene chloride faces significant product price risks due to differences in prices across suppliers and grades. Weak demand from PVDC manufacturers, fluorochemical plants, and traders can lead to lower selling prices and reduced margins. When several major buyers cut purchases at the same time, merchant sellers may struggle to maintain sales volumes and profitability.

Vinylidene chloride production carries its own risks because the monomer is toxic, flammable, and reactive. It can polymerize explosively if the inhibitor fails, and it forms explosive peroxides with air. Very low flash point and high volatility require closed, cold, nitrogen-padded systems. Brine and organic waste from dehydrochlorination need careful treatment. Most rejected lots trace back to high impurities, low inhibitor, color, water, and acidity. Polymer buildup in condensers, columns, pumps, and tanks also forces costly shutdowns.

Vinylidene Chloride Production Process and Main Cost Drivers

The vinylidene chloride production process runs from 1,1,2-trichloroethane and caustic soda or lime through reactive dehydrochlorination, overhead recovery, washing, drying, distillation, inhibitor addition, and cold storage.

  1. By Dehydrochlorination of 1,1,2-Trichloroethane with Caustic Soda or Lime: The main inputs are 1,1,2-trichloroethane from the vinyl chloride and ethylene dichloride chain, caustic soda or hydrated lime, process water, inhibitor, and nitrogen for blanketing.

Vinylidene chloride production opens with 1,1,2-trichloroethane fed to a stirred reactor or reactive distillation column with aqueous caustic soda or lime slurry. The base removes one molecule of hydrogen chloride and forms vinylidene chloride, salt, and water. The reaction runs at about 100 degree Celsius. Because vinylidene chloride boils near 32 degree Celsius, it flashes off as it forms and is taken overhead. Operators track temperature, caustic strength, feed ratio, pressure, and overhead purity through each run. Reactors, columns, and condenser materials must resist hot caustic, brine, and chlorinated organics. Unreacted trichloroethane returns to the reactor. Keeping the overhead cold and the residence time short limits side reactions and polymer buildup.

The crude monomer is condensed, washed with water, and dried. It then passes through distillation columns that remove light ends, water, and heavier chlorinated compounds. Inhibitor is added to the purified monomer, which is cooled and stored under nitrogen. Brines from the reactor are stripped of organics before treatment or reuse. A gas-phase cracking route without base is possible but less selective. QC covers purity by GC, inhibitor content, acidity, water, color, and trace chlorinated impurities.

Main Factors Affecting Vinylidene Chloride Production Cost

According to a vinylidene chloride production plant report, vinylidene chloride production cost is set mainly by 1,1,2-trichloroethane and caustic soda. At full yield, a kilogram of vinylidene chloride needs about 1.38 kg of trichloroethane and 0.41 kg of caustic soda on a 100% basis. It also yields about 0.60 kg of sodium chloride in brine. At about 1,813 yuan per ton of caustic on a 100% basis, caustic alone costs about 750 yuan per ton of monomer. With lime instead, about 0.38 kg of hydrated lime is needed per kilogram. Lime costs less per unit of base but leaves a calcium chloride slurry that is harder to handle.

The value of trichloroethane depends on whether it is bought or made in-house. Integrated plants recover it as a by-product, so its value ties to the cost of the vinyl chloride chain. Merchant buyers pay a market price that follows chlorine and ethylene. That gap gives integrated producers a clear cost edge over standalone plants, especially when monomer prices are low. Energy goes to heating, refrigeration for condensing, and distillation. Refrigeration runs around the clock, since the monomer must stay cold in every tank and line. Brine treatment, waste incineration, labor, testing, and insurance fall under fixed and semi-fixed costs. Typical cost lines include trichloroethane, caustic, inhibitor, nitrogen, steam, refrigeration, power, labor, and waste handling.

Raw Materials for Vinylidene Chloride Production Plant and its Procurement

Raw material sourcing for vinylidene chloride centers on 1,1,2-trichloroethane and caustic soda. Trichloroethane is produced as a by-product when making ethylene dichloride and vinyl chloride. It can also be made by reacting vinyl chloride or ethylene dichloride with chlorine. Caustic soda usually comes from nearby chlor-alkali plants, often within the same industrial complex. The process also requires lime, water, inhibitors, nitrogen, and refrigeration.

The quality of raw materials affects both production costs and the final product. Trichloroethane containing tetrachloroethane, dichloroethylenes, or other chlorinated impurities can reduce the reaction yield and increase the amount of distillation needed. Caustic soda containing high levels of chloride or iron can also cause deposits and other problems in equipment. Membrane-grade caustic costs more but generally has fewer impurities. For this reason, supply contracts specify the required purity, impurity levels, and concentration of each raw material. Plants located within a chlorine complex can also work with upstream units to reduce unwanted impurities before the materials reach production.

Raw material supply needs careful planning at a vinylidene chloride plant. Trichloroethane availability depends on production levels at vinyl chloride and ethylene dichloride plants. Caustic soda prices are affected by chlor-alkali production, demand from the alumina industry, and exports. Each incoming batch is tested for purity, water content, and impurities before use. Long-term supply agreements within a chlorine complex can help prevent shortages. Manufacturers also need backup suppliers for inhibitors and nitrogen, as any interruption in their supply can create safety risks.

Sustainability and Regulatory Requirements

According to a vinylidene chloride production plant project report, vinylidene chloride production raises environmental and occupational concerns that center on toxic vapor, flammability, chlorinated waste, and brine. The monomer affects the central nervous system, and high exposures cause sedation and unconsciousness. Closed handling, vapor recovery, gas detection, and fire protection are standard. Chlorinated heavy ends go to licensed incineration with acid gas scrubbing. Brine is stripped of organics before reuse or discharge. Staff need respirators, chemical gloves, eye protection, and fire-resistant clothing in monomer handling areas.

Regulatory obligations for vinylidene chloride are strict. IARC classifies it as possibly carcinogenic to humans, and NIOSH treats it as a potential occupational carcinogen. ACGIH sets a workplace limit of 5 ppm, and Germany sets 2 ppm. Transport falls under UN 1303 for stabilized vinylidene chloride, with a warning for explosive polymerization. HCFC uses fall under Montreal Protocol quotas. Labels and safety data sheets follow CLP in the EU and the OSHA Hazard Communication Standard in the US. Plants also follow major hazard rules, emissions permits, and wastewater limits for chlorinated organics.

CAPEX and OPEX for a Vinylidene Chloride Production Plant

A vinylidene chloride plant is a reactive distillation and purification unit built for a volatile, toxic monomer. Plant investment starts with trichloroethane and caustic storage, a dehydrochlorination reactor or reactive column, and refrigerated overhead condensers. Wash and drying systems follow. Distillation columns, reboilers, and chilled condensers purify the monomer. Inhibitor dosing, refrigerated nitrogen-padded tanks, and loading systems handle the product. Brine strippers, a thermal oxidizer with scrubbing, and vapor recovery handle waste. Utilities include steam, chilled water, cooling water, nitrogen, compressed air, and power. On the QC side, a laboratory holds gas chromatographs, titration for acidity and inhibitor, Karl Fischer water testing, and colorimeters. Civil works cover a tank farm, a process structure, a waste treatment area, and a control room.

Vinylidene chloride operating cost comes from the same inputs and control points that shape the process. The variable side is led by trichloroethane, followed by caustic soda, steam, refrigeration, and inhibitor. Labor, testing, waste treatment, maintenance, and insurance complete the running cost. Cost per kilogram then depends on feedstock value, selectivity, energy, and plant utilization. The vinylidene chloride plant setup cost depends on capacity, integration with a chlorine complex, refrigeration and storage design, and waste treatment scale. Working capital is moderate, since most products move to captive PVDC lines. Main fixed costs include staff, maintenance, insurance, safety systems, and depreciation on columns and tanks.

Plant Location and Investment Factors

A vinylidene chloride plant is best located within an existing chlorine or vinyl chloride complex. This gives the plant access to trichloroethane by-product, caustic soda, steam, incineration facilities, and existing safety systems. Having a PVDC or fluorochemical plant nearby also helps, as the monomer can be supplied through pipelines instead of being transported as a hazardous liquid. China, Japan, South Korea, the US, and Europe have several such integrated chemical complexes. The site must also have proper safety systems, emergency response facilities, and permits for handling chlorinated waste. Other factors to consider include raw material supply, caustic soda availability, refrigeration, incineration facilities, and nearby PVDC or fluorochemical manufacturers.

Integration is the main investment decision for a vinylidene chloride plant. Standalone plants that purchase trichloroethane and sell the monomer separately may face low profit margins and higher transport risks. Integrated plants can use trichloroethane generated as a by-product and supply vinylidene chloride directly to their own PVDC or fluorochemical units. Manufacturers must also decide how much production to allocate to PVDC and fluorochemical intermediates. Safety is another major concern because vinylidene chloride is toxic and highly reactive. A serious leak or uncontrolled polymerization can force a plant to shut down for months and affect customer relationships. For a new entrant, a steady supply of raw materials and proper inhibitor control are essential.

Major Vinylidene Chloride Producing Regions

China has several chemical manufacturers producing vinylidene chloride for PVDC and fluorochemical applications. Japan has PVDC manufacturers that supply materials for cling films and barrier packaging. South Korea and the US also produce PVDC resins used in food and pharmaceutical packaging. France produces PVDC barrier polymers for packaging and coating applications across Europe. Major demand comes from the food packaging, pharmaceutical, coatings, and electronics industries in Asia, Europe, and North America. Any new vinylidene chloride plant is likely to be set up within an existing chlorine and vinyl chloride complex in China, where trichloroethane, caustic soda, energy, and waste treatment facilities are readily available.

Key Vinylidene Chloride Producers

Asahi Kasei

  • Ranks among the key vinylidene chloride suppliers named in industry reviews.
  • Makes PVDC for the Saran Wrap cling film sold in Japan.
  • Also makes PVDC barrier films for food and other packaging.

Kureha

  • Ranks among the key vinylidene chloride suppliers named in industry reviews.
  • Makes PVDC at its Iwaki Factory in Fukushima, Japan.
  • Uses that resin for NEW Krewrap cling film and Krehalon packaging film.
  • Also makes PVDF and other specialty polymers.

SK geo centric

  • Bought the Saran PVDC resin business from Dow.
  • Led global PVDC sales in a recent industry review.
  • Serves food and pharmaceutical packaging makers with PVDC resins.

Syensqo

  • Makes Diofan and Ixan PVDC polymers at Tavaux, France.
  • Offers latexes and extrusion resins with both oxygen and water vapor barrier.
  • Serves food packaging, healthcare packaging & corrosion-resistant coatings.
  • Ranks among the vinylidene chloride and PVDC producers named in industry reviews.

Juhua Group

  • Ranks among the Chinese vinylidene chloride and PVDC producers named in industry reviews.
  • Runs a large fluorine and chlorine chemical complex in Zhejiang, China.
  • Serves PVDC, fluorochemical, and specialty chemical markets.
  • Also makes refrigerants and fluoropolymers.

Shandong Xinglu Chemical

  • Ranks among the Chinese vinylidene chloride and PVDC producers named in industry reviews.
  • Makes the monomer in Shandong, China.
  • Serves PVDC and chemical intermediate buyers.
  • Serves buyers in the Shandong market.

Vinylidene Chloride Production Cost Report

Vinylidene Chloride Production Cost Reports

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Product Details

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Product Details

Particulars Details
Product Name Vinylidene Chloride
Scope Production Process: Process Flow, Material Flow, Material Balance

Raw Material and Product Specifications: Raw Material Consumption, Product and Co-product Generation

Land and Site Cost: Offsites/Civil Works, Equipment Cost, Auxiliary Equipment Costs, Contingency, Engineering and Consulting Charges, Working Capital

Variable Cost: Raw Material, Utilities, Other Variable Costs

Fixed Cost: Labor Requirements and Wages, Overhead Expenses, Maintenance Charges, Other Fixed Costs

Financing Costs: Interest on Working Capital, Interest on Loans

Other Costs: Depreciation Charges, General Sales and Admin Cost
Currency US$ (Data can also be provided in the local currency)
Customization Scope The report can be customized as per the requirement of the customer
Post-Sale Analysts Report 10-12 weeks of post-purchase analyst support after report delivery for any queries from the deliverable
Delivery Format PDF and Excel format through email (editable version in PPT/Word format of the report can be also provided on special request)

Frequently Asked Questions

Trichloroethane and caustic storage, a dehydrochlorination reactor or reactive column, refrigerated condensers, wash and drying units, distillation columns, inhibitor dosing, refrigerated nitrogen-padded tanks, brine strippers, thermal oxidizer & a QC laboratory able to run GC, acidity, inhibitor and water tests.

1,1,2-Trichloroethane reacts with caustic soda or lime at about 100 degree Celsius, losing hydrogen chloride to form vinylidene chloride. The monomer flashes overhead, is washed, dried and distilled, then stabilized with inhibitor and stored cold under nitrogen.

A kilogram of vinylidene chloride needs about 1.38 kg of trichloroethane and 0.41 kg of caustic soda at full yield.

Reactors, reactive and distillation columns, refrigerated condensers, decanters, dryers, pumps, refrigerated tanks, strippers and a thermal oxidizer, supported by steam, chilled water, cooling water, nitrogen, compressed air and power.

Trichloroethane value, caustic or lime price, selectivity, steam and refrigeration energy, brine and waste treatment, inhibitor use, safety and insurance, and plant utilization.

Vinylidene chloride is an industrial monomer with no pharmacopoeia monograph. IARC classes it as possibly carcinogenic, ACGIH sets a 5 ppm limit, and it ships under UN 1303 as a stabilized monomer, while PVDC made from it must meet food and drug packaging rules.

China, Japan, Korea, the US and France host the main producers. Asahi Kasei, Kureha, SK geo centric, Syensqo, Juhua Group and Shandong Xinglu Chemical are among the producers named across the chain.

Vinylidene chloride is not a China or India API. Its feedstock comes from the vinyl chloride and ethylene dichloride chain and its reagent from chlor-alkali plants, so PVC and chlorine operating rates feed straight into supply and cost.

Monomer grades at 99% or higher with MEHQ or similar inhibitors, polymer grades with low impurities, and high-purity grades for semiconductor processing.

Hydrated lime can replace caustic soda, which is cheaper but produces calcium chloride brine and slurry handling. Gas-phase thermal cracking of trichloroethane avoids alkali but is less selective, so liquid-phase dehydrochlorination remains the main route.

1,1,2-Trichloroethane is the most important cost driver, since it supplies all the carbon and chlorine in the monomer. Caustic soda and energy follow.

Vinylidene Chloride Reports

Vinylidene Chloride Production Cost Processes with Cost Analysis

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Vinylidene Chloride Production by the Dehydrochlorination of 1,1,2-Trichloroethane with Caustic Soda

The study offers a detailed cost analysis of Vinylidene Chloride Production by the Dehydrochlorination of 1,1,2-Trichloroethane with Caustic Soda. In addition, the report incorporates the manufacturing process with detailed process and material flow, operating costs along with financial expenses and depreciation charges.

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How does our Vinylidene Chloride Production Cost Report Provide Exhaustive Data and Extensive Insights?

At Procurement Resource, we focus on improving the should-cost of production for vinylidene chloride and map every stage of the route, from 1,1,2-trichloroethane and caustic soda or lime through reactive dehydrochlorination, overhead recovery, washing, drying, distillation, inhibitor addition & refrigerated storage. The cost model resolves each input separately, including trichloroethane, caustic soda or lime, inhibitor, nitrogen, steam, refrigeration, power, labor, GC testing, brine and waste treatment, maintenance & insurance. We evaluate CAPEX and OPEX as cost per kilogram of saleable monomer, isolating the feedstock share, the reagent share & the energy and waste share, since these three items set most of the delivered cost for a chlorinated monomer.

Alongside the cost build-up, the report identifies providers of reactive distillation columns, refrigerated condensers, distillation trains, nitrogen-padded tanks, brine strippers & thermal oxidizers, and offers a supplier database for trichloroethane, caustic soda, lime, inhibitors & nitrogen. It sets out a feasible plant layout covering the feedstock tanks, the reaction and recovery area, the purification train, refrigerated storage, waste treatment & the QC laboratory. By modeling feedstock value, caustic price, selectivity, energy use & plant utilization, the analysis shows where the cash production cost can be reduced. It supports decisions on caustic versus lime, liquid-phase versus gas-phase routes, captive versus merchant sales & integration with a chlorine complex.

About the Author

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Udeesha Tomar

AVP - Strategy and Solutions

Leading procurement research solutions across chemicals, materials, and food & beverages, with expertise in price forecasting and market analytics.

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