
Udeesha Tomar
AVP - Strategy and Solutions
Leading procurement research solutions across chemicals, materials, and food & beverages, with expertise in price forecasting and market analytics.
The report provides detailed analysis essential for establishing a perchloroethylene production plant. It encompasses all critical aspects necessary for perchloroethylene production, including the cost of perchloroethylene production, perchloroethylene plant cost, perchloroethylene production costs, and the overall perchloroethylene production plant cost. Additionally, the study covers specific expenditures associated with setting up and operating a perchloroethylene 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.
Perchloroethylene, also known as tetrachloroethylene or PCE, is a fully chlorinated two-carbon solvent. It is a dense, colorless, nonflammable liquid with an ether-like odor. Chlorine accounts for about 85 percent of its weight, making access to chlorine and hydrogen chloride important for production. As a result, most perchloroethylene is produced by chlor-alkali and vinyl chloride manufacturers with these materials available on site. It was once widely used in dry cleaning but is now mainly used to produce fluorocarbon refrigerants and as an industrial cleaning solvent.
Perchloroethylene demand has changed significantly over the past three decades. Around 1990, dry cleaning accounted for about 53 percent of global demand, while chemical intermediates represented about 23 percent, mainly for CFC-113 production. A later US producer estimate placed chemical intermediates at 60 percent, dry cleaning and textile processing at 18 percent, and surface cleaning at 18 percent. Refinery catalyst regeneration accounted for the remaining 2 percent. Chemical intermediate demand now comes mainly from HFC-125 production, which is used in common refrigerant blends. Meanwhile, dry-cleaning demand continues to decline as the United States, Europe, and Canada tighten restrictions on the solvent.
A perchloroethylene demand and supply analysis must consider chlorine availability, refrigerant production, and regulatory changes. US output reported under federal chemical data reporting fell from about 420 million pounds in 2012 to about 324 million pounds in 2015, including imports. Chinese demand increased with the growth of its refrigerant industry, and China imported a large share of its requirements in the early 2020s. In August 2026, delivered prices ranged from USD 1.64 to 1.81 per kg in North America, USD 1.22 to 1.35 per kg in Europe, and USD 0.57 to 0.63 per kg in Northeast Asia. Upon delivery, buyers check purity using gas chromatography and test for water, acidity expressed as HCl, nonvolatile residue, color, and stabilizer content.
Perchloroethylene (C2Cl4), CAS number 127-18-4, is a chlorinated organic compound with a molar mass of 165.83 g/mol. It has a density of approximately 1.623 g/cm³ at 20 degree Celsius, a boiling point of 121 degree Celsius, and a freezing point of about minus 19 degree Celsius. Its vapor pressure is approximately 14 mmHg at room temperature. It has very low solubility in water, at about 0.15 g/L at 25 degree Celsius, but mixes readily with ethanol, diethyl ether, and benzene. Moreover, the compound is nonflammable under normal conditions.
Perchloroethylene is stable under suitable storage conditions but can decompose when exposed to heat, light, or moisture. Exposure to sunlight and air can produce hazardous compounds, including phosgene and trichloroacetyl chloride. Thermal decomposition during a fire can release hydrogen chloride and phosgene. The compound can react with strong oxidizers, certain reactive metals, and strong alkalis. Stabilizers such as amines, phenols, or epoxides are added at concentrations of 0.01% to 0.35% to limit acid formation. Commercial grades typically contain no more than 50 ppm water, 0.0005% acidity as HCl, and 0.001% nonvolatile residue.
Perchloroethylene is available in technical, dry-cleaning, vapor-degreasing, and high-purity grades, with specifications depending on the intended application. Fluorocarbon feedstock and isomerization grades can reach 99.995% purity. Dry-cleaning and general technical grades differ mainly in their stabilizer content, while vapor-degreasing grades contain stabilizer systems designed for heated operations and metal contact. Laboratory applications use specialized grades, including USP, spectrophotometric, and reagent grades, which require tighter control of impurities.
Perchloroethylene is primarily used as a chemical intermediate in fluorocarbon production and as an industrial solvent and cleaning agent. It is widely used for vapor degreasing metal components, cleaning electrical equipment, and preparing maskants for chemical milling. Refineries also use it in catalyst regeneration processes. Additional applications include dry cleaning, textile scouring & adhesive formulations, and paint removers. Its strong solvent properties and nonflammability make it suitable for several industrial cleaning and chemical processing operations.
Fluorocarbon production is the main end-use for perchloroethylene. In the usual process, perchloroethylene reacts with hydrogen fluoride in the vapor phase at about 200 to 400 degree Celsius over a chromia-based catalyst. HCFC-123 and HCFC-124 form as intermediates and are recycled until most of the feed is converted into HFC-125, also known as pentafluoroethane. HFC-125 is a key component of R-410A and other refrigerant blends used in air conditioners and commercial refrigeration systems. Fluorochemical manufacturers are the largest buyers of perchloroethylene and require high purity, low water content, and reliable supply.
Industrial cleaning & processing form the second end-use group. Vapor degreasing is the main solvent application, particularly for aerospace, automotive, and precision metal parts. Perchloroethylene has a boiling point of 121 degree Celsius, compared with 87 degree Celsius for trichloroethylene, allowing it to operate at a higher vapor temperature during cleaning. Refineries also use it as a chlorine source during catalyst regeneration. Other applications include maskants, adhesives, and energized electrical cleaning products. These buyers typically purchase stabilized grades in drums and isotanks.
Dry cleaning and textile processing form the third and declining end-use segment. Perchloroethylene replaced trichloroethylene in dry cleaning in the mid-1950s because it is gentler on fabrics. By the 2000s, about 70 percent of US dry cleaners still used it, but this share is now falling rapidly. The EPA's final TSCA rule prohibits the use of perchloroethylene in newly acquired dry-cleaning machines and phases out existing machines over ten years. France has prohibited it in new dry-cleaning installations near homes, while Canada has regulated its use in dry cleaning since 2003.
Perchloroethylene faces significant regulatory risks in major markets due to concerns about human health and environmental safety. In the United States, regulatory measures require the phaseout of all consumer uses and many industrial applications, with most affected uses scheduled to end within three years. Remaining applications, including refrigerant chemical production, must comply with workplace exposure controls. Key compliance deadlines range from June 21, 2027, for initial monitoring to December 20, 2027, for exposure control plans. The regulatory framework remains subject to reconsideration. In the European Union, perchloroethylene is classified as a Category 2 carcinogen, while international assessments also identify concerns about its potential carcinogenicity.
Perchloroethylene also faces demand risks from the gradual phase-down of hydrofluorocarbon (HFC) refrigerants. Measures under the Kigali Amendment and the US AIM Act limit HFC production, potentially reducing long-term demand for HFC-125 and the perchloroethylene used in its manufacture. Greater adoption of hydrofluoroolefin (HFO) and natural refrigerants could further affect consumption. Supply disruptions caused by Gulf Coast hurricanes, chlor-alkali plant outages, and scheduled maintenance can also reduce availability and increase prices. Chinese market prices may fluctuate sharply during import shortages and local plant shutdowns. In addition, carbon tetrachloride, a major co-product, is subject to strict controls due to its ozone-depleting properties, limiting producers' flexibility in managing output.
Perchloroethylene is made by high-temperature chlorination or oxychlorination of C1 to C3 hydrocarbons or their chlorinated derivatives, then separated from carbon tetrachloride, trichloroethylene, and hydrogen chloride by distillation.
Chlorinolysis is the most common route. Chlorine and the carbon feed enter a thermal reactor at about 500 to 700 degree Celsius and close to atmospheric pressure, with residence times of a few seconds. The reaction strips hydrogen and breaks carbon chains until fully chlorinated products remain. Perchloroethylene and carbon tetrachloride form together. Producers adjust the ratio by recycling carbon tetrachloride to the reactor. When ethylene is the carbon source, each molecule of perchloroethylene uses four molecules of chlorine and releases four molecules of hydrogen chloride. Recycle rates, feed mix, and reactor temperature decide yield. The hot reactor gas is quenched with cold hydrochloric acid and then cold water. That step condenses the chlorinated organics and absorbs hydrogen chloride. The hydrogen chloride is sold as hydrochloric acid or sent to an oxychlorination unit to make ethylene dichloride. Unreacted chlorine is dried & recycled. A distillation train then separates carbon tetrachloride, perchloroethylene, and a heavy fraction. The heavy fraction contains hexachloroethane, hexachlorobutadiene, and hexachlorobenzene. It is chlorinated again under pressure over iron chloride and recycled. The final residue is destroyed by high-temperature incineration.
Two other routes run at integrated vinyl sites. Oxychlorination of ethylene dichloride or other C2 chlorinated hydrocarbons with hydrogen chloride and oxygen makes trichloroethylene and perchloroethylene together, with no net hydrogen chloride. Noncatalytic chlorination of ethylene dichloride gives the same pair. An older perchloroethylene route built the product from acetylene through tetrachloroethane and pentachloroethane, but high acetylene cost ended it in the US by the 1970s. Finished perchloroethylene is dried, stabilized for its grade, and checked for purity, water, acidity, and residue. The main cost factors are chlorine value, hydrogen chloride outlet, co-product balance, and residue destruction.
Chlorine is the main factor driving perchloroethylene production cost. Chlorine makes up 85.5 percent of the product by mass, so its transfer value sets most of the variable cost. The route sets how much more chlorine is needed. Chlorinolysis of ethylene-based feed sends half of the chlorine out as hydrogen chloride. That hydrogen chloride has to be sold or used in oxychlorination, or it becomes a cost. Plants with an ethylene dichloride unit beside them turn it into value. Carbon feed is a smaller cost, and chlorinated residues from vinyl chloride plants are often a low-cost feed.
Co-product balance is the second major cost factor. Carbon tetrachloride forms alongside perchloroethylene and must be recycled, used as feedstock, or sold into tightly regulated markets. Trichloroethylene from oxychlorination faces its own TSCA restrictions. Energy goes to heating feed to reaction temperature, distillation, chlorine drying, and refrigeration. The incinerator for heavy ends, vent scrubbers, and wastewater treatment carry fixed costs that do not shrink at low rates. Regulatory compliance, exposure monitoring, and stewardship programs add further overhead in the US and Europe.
Regional chlorine economics show up directly in perchloroethylene prices. The global average delivered price was about USD 1.27 per kg in the first quarter of 2026. North America sat near USD 1.73 per kg, Europe near USD 1.28, and Northeast Asia near USD 0.60. North American prices rose about 10 percent from the previous quarter on high chlorine input costs. Northeast Asian prices fell about 12 percent as Chinese supply outpaced demand. A producer's margin depends on where its chlorine cost sits against these regional price levels.
Perchloroethylene production mainly requires chlorine and a carbon source. Chlorine is generally obtained through the electrolysis of brine in chlor-alkali plants, which also produce caustic soda. Most manufacturers produce chlorine on-site to reduce transportation costs and handling risks. Carbon sources include ethylene dichloride, propylene dichloride, methane, ethane, propane, and chlorinated heavy ends from vinyl chloride production. Feedstock selection depends on process requirements, availability, cost, and the purity specifications of the final product.
Feedstock quality directly affects production yield, operating costs, and purification requirements. Variations in the composition of chlorinated heavy ends can change chlorine consumption and processing efficiency. Aromatic and oxygenated impurities may increase the formation of hexachlorobenzene and other heavy by-products, requiring additional treatment. Moisture in chlorine and recycle streams can cause severe corrosion at high reaction temperatures. Stabilizers are procured from specialty chemical suppliers, while drums, isotanks, and rail tank cars are used for transportation and storage where required.
Procurement strategies focus on maintaining consistent feedstock quality, reliable supply, and efficient material handling. On-site chlorine supply is generally managed through internal pipelines, with contingency arrangements for plant outages. External feedstocks are assessed for composition, chlorine content, and moisture before use, while stabilizers are checked for purity and batch consistency. Locating the plant within an integrated chlor-alkali and vinyl chloride complex provides access to chlorine, hydrogen chloride handling facilities, and chlorinated by-product streams, helping reduce logistics costs and improve production efficiency.
A perchloroethylene plant handles chlorine, hydrogen chloride, carbon tetrachloride, and persistent chlorinated heavies. Vents pass through caustic scrubbers to remove chlorine and hydrogen chloride. Heavy ends rich in hexachlorobenzene, a persistent organic pollutant, go to high-temperature incineration with acid gas scrubbing. Wastewater from quenching and scrubbing carries dissolved chlorinated organics and needs stripping before treatment. Groundwater protection matters because spilled perchloroethylene sinks and persists. Many old dry-cleaning and degreasing sites still require cleanup decades later.
The regulatory requirements for perchloroethylene are among the strictest for any solvent. In the US, the TSCA rule sets an exposure limit and requires monitoring, regulated areas, respiratory protection, and exposure control plans. Perchloroethylene is a hazardous air pollutant under the Clean Air Act and an RCRA hazardous waste under codes U210, F001, and F002. Its CERCLA reportable quantity is 100 pounds, and the US drinking water limit is 0.005 mg/L. Japan sets an environmental water standard of 0.01 mg/L, and the WHO guideline value is 0.04 mg/L. OSHA sets a 100 ppm time-weighted limit. In the EU, it is registered under REACH and classified H351 and H411. Carbon tetrachloride co-product falls under Montreal Protocol feedstock rules.
A perchloroethylene plant is a high-temperature chlorination unit integrated with a chlor-alkali and vinyl production complex. The main equipment includes chlorine vaporizers and preheaters, a corrosion-resistant thermal reactor, and a quench and hydrogen chloride absorption system. Downstream equipment includes chlorine drying and recycling systems, distillation columns for separating carbon tetrachloride, perchloroethylene, and heavy residues, and a pressure chlorinator for treating the heavy fraction. Supporting facilities include a high-temperature incinerator, caustic scrubbers, wastewater stripping, and storage tanks for chlorine-containing liquids. Oxychlorination plants also require an oxygen supply and a catalytic reactor. The quality control laboratory performs gas chromatography, Karl Fischer titration, acidity, and residue tests.
Perchloroethylene operating costs are mainly driven by chlorine prices. Variable costs include chlorine, carbon feed, heating and distillation energy, refrigeration, stabilizers, caustic for scrubbing, and incineration fuel. Revenue or credits from hydrochloric acid or ethylene dichloride production can offset some costs. Fixed costs include labor, maintenance, exposure monitoring, environmental permits, and insurance. Perchloroethylene plant setup costs vary according to the production route, reactor capacity, co-product handling requirements, and incinerator size. Chlorine accounts for the largest share of operating costs, followed by energy, residue disposal, and labor. Corrosion also increases maintenance costs.
The first decision for a perchloroethylene project is whether the site has a captive chlorine supply and a market for hydrogen chloride. Without both, the project is rarely economical. The US Gulf Coast, particularly Texas and Louisiana, offers established chlor-alkali, ethylene, and vinyl chloride capacity. Lower Saxony in Germany has chlorine and chlorinated chemical production centered around Stade. Zhejiang and Shandong in China combine large chlor-alkali operations with major refrigerant producers. India has expanding chlor-alkali capacity in Gujarat and a growing fluorochemical industry. Each location also needs access to a licensed hazardous-waste incinerator, either on site or nearby, because heavy residues cannot be sent to landfills. Permits for chlorine storage and chlorinated solvent emissions can take time to obtain in all these regions.
The second decision is the target market. A plant supplying refrigerant manufacturers requires high-purity perchloroethylene and a long-term supply contract with a fluorochemical producer. A plant targeting solvent applications needs stabilizer blending, packaging, and distribution facilities but faces declining regulated demand in the United States and Europe. Co-product management is equally important. Carbon tetrachloride has few permitted uses, so most new plant designs aim to recycle it until it is fully converted. Plant capacity should therefore match chlorine availability and demand from fluorochemical customers rather than solvent demand alone.
The United States, China, and Germany hold most perchloroethylene capacity. Olin runs chlorinated organics at Freeport in Texas, Plaquemine in Louisiana, and Stade in Germany. Occidental Chemical makes perchloroethylene at Geismar in Louisiana and chlorinated solvents at Wichita in Kansas. Westlake supplies the product from its US chlorovinyls system. In China, Ningbo Juhua Chemical and Binhua each have about 80,000 metric tons per year of capacity. Europe also relies on distributors for solvent grades. Northeast Asia has the lowest prices because Chinese capacity serves a large domestic refrigerant market. A new perchloroethylene plant would most likely sit inside a Chinese or Indian chlor-alkali complex beside a fluorochemical customer.
Olin Corporation
Occidental Chemical Corporation
Westlake Corporation
Ningbo Juhua Chemical Co. Ltd.
Shandong Binhua Group
KH Chemicals B.V.
Perchloroethylene Production Cost Report

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| Particulars | Details |
|---|---|
| Product Name | Perchloroethylene |
| 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) |
Perchloroethylene Production Cost Processes with Cost Analysis

This study analyzes Perchloroethylene Production by Huels Method, covering manufacturing, process flow, operating expenses, and financial considerations.
At Procurement Resource, we focus on improving the should-cost of production for perchloroethylene and map every stage of the route. That runs from chlorine drying and vaporizing and carbon feed preparation, through thermal chlorinolysis or oxychlorination, quenching and hydrogen chloride absorption, chlorine recycle, and distillation of carbon tetrachloride, perchloroethylene, and heavies, to heavy-end chlorination, residue incineration, and stabilization. The cost model resolves each input separately, including chlorine, ethylene dichloride, propylene dichloride, methane or other carbon feed, oxygen, iron chloride catalyst, stabilizers, caustic for scrubbing, fuel, steam, power, refrigeration, labor, GC and Karl Fischer testing, incineration, and drum, isotank, and rail packaging. We evaluate CAPEX and OPEX as cost per kilogram of perchloroethylene, with hydrochloric acid credits and carbon tetrachloride handling shown separately.
Alongside the cost build-up, the report identifies technology options for chlorinolysis, oxychlorination, heavy-end recycle, and residue destruction. It offers a supplier database for chlorine, chlorinated feeds, stabilizers, corrosion-resistant equipment, and incineration services. It sets out a feasible plant layout covering chlorine handling, the reactor and quench section, hydrogen chloride absorption, the distillation train, the incinerator and scrubbers, the tank farm and loading area, and the QC laboratory. By modeling chlorine value, hydrogen chloride outlet, co-product ratio, and plant utilization, the analysis shows where cash production cost can be reduced. It supports decisions on route choice, feedstock versus solvent grade focus, and siting inside a chlor-alkali and vinyl complex.

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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