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The report provides detailed analysis essential for establishing an allyl chloride production plant. It encompasses all critical aspects necessary for allyl chloride production, including the cost of allyl chloride production, allyl chloride plant cost, allyl chloride production costs, and the overall allyl chloride production plant cost. Additionally, the study covers specific expenditures associated with setting up and operating an allyl 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.
Allyl chloride is an industrial chemical intermediate used mainly in the production of epichlorohydrin. It is a colorless, volatile, and highly flammable liquid produced by the chlorination of propylene. Most of the allyl chloride produced is converted into epichlorohydrin, which is further used to manufacture epoxy resins and glycerol. The remaining volume is used to produce other allyl compounds and as an alkylating agent in chemical synthesis. Its demand is closely linked to the epichlorohydrin and epoxy resin markets, making it dependent on construction, coatings, and the wider chemical industry.
The main buyers of allyl chloride are chemical manufacturers, particularly epichlorohydrin producers. Most epichlorohydrin manufacturers consume allyl chloride in their own integrated production facilities. Other chemical manufacturers use it to produce allyl alcohol, allylamine, and related compounds. Pharmaceutical and agrochemical manufacturers also use it as an alkylating agent in chemical synthesis. An allyl chloride demand and supply analysis therefore considers the strong demand from epichlorohydrin production alongside the cost of propylene and chlorine, the main feedstocks, as well as the energy and separation requirements of the manufacturing process.
Allyl chloride supply is mainly controlled by large chemical manufacturers with access to chlorine, propylene, and established chlorination technology. A significant portion of production is captive, as manufacturers convert allyl chloride into epichlorohydrin within their own facilities, leaving a relatively small merchant market. Major production bases are located in North America and Europe, with expanding capacity in Asia. The main feedstocks, propylene and chlorine, are supplied by the petrochemical and chlor-alkali industries. Buyers are primarily epichlorohydrin and other chemical manufacturers worldwide. Allyl chloride prices are mainly influenced by propylene and chlorine costs, along with processing expenses. On receipt, buyers check the product's purity and chlorinated impurity levels.
Allyl chloride, also known as 3-chloropropene, has the molecular formula C3H5Cl, a molar mass of approximately 76.52 g/mol, and CAS number 107-05-1. It is a reactive chlorinated organic compound containing a carbon-carbon double bond and a chlorine atom attached to the adjacent carbon. It is a colorless, volatile liquid with a pungent odor and a boiling point of approximately 45 degree Celsius. It has low solubility in water, dissolves readily in organic solvents, and is highly flammable.
Allyl chloride is classified as a highly flammable and toxic chemical that requires strict storage and handling controls. It is stored in tightly sealed containers under controlled temperatures and an inert atmosphere, away from heat, sparks, and other ignition sources. Its volatile vapors require effective ventilation and containment to minimize worker exposure. Appropriate protective equipment and safety systems are necessary because the compound is harmful through inhalation, ingestion, and skin contact. Controlling vapor emissions, fire hazards, and occupational exposure are the main considerations during storage and handling.
Allyl chloride is mainly supplied as a high-purity industrial-grade chemical for use in downstream chemical manufacturing. The grade specifications focus on purity, color, and the levels of chlorinated impurities and other by-products. Since a significant portion of production is consumed captively, the required purity is often determined by the specifications of the downstream process. The product is supplied as a liquid in suitable sealed containers or bulk storage systems designed for flammable and volatile chemicals. Consistent quality is essential for its use in producing epichlorohydrin & other chemical derivatives.
Allyl chloride is primarily used as a feedstock for producing epichlorohydrin, which is further processed into epoxy resins for coatings, adhesives, and composite materials, as well as synthetic glycerol. It is also used in the manufacture of allyl alcohol, allylamines, allyl isothiocyanate, and other specialty chemicals. Additionally, it serves as an alkylating agent and chemical intermediate in the production of certain pharmaceuticals and agrochemicals. Its reactive chlorine group and carbon-carbon double bond make it an important building block for several industrial chemical processes.
Epichlorohydrin production is the major end-use of allyl chloride, accounting for the largest share of its consumption. Allyl chloride is converted into epichlorohydrin, which is further used to manufacture epoxy resins for coatings, adhesives, electronics, and composite materials, as well as synthetic glycerol. This application requires high-purity allyl chloride and is often carried out in integrated chemical manufacturing facilities. Demand from epichlorohydrin production is closely linked to the epoxy resin and chlor-alkali industries, making it the primary driver of allyl chloride consumption.
The production of allyl compounds and other chemical derivatives forms another important end-use segment. Allyl chloride is used as a chemical intermediate to manufacture allyl alcohol, allylamines, allyl isothiocyanate, allyl ethers, esters, and other allyl-based compounds. These derivatives are further used in the production of resins and specialty chemicals. This segment supports demand from specialty chemical manufacturers that use allyl chloride as a starting material for producing various chemical intermediates and derivatives.
Pharmaceutical, agrochemical, and other specialty applications account for the remaining consumption of allyl chloride. It is used as an alkylating agent to introduce the allyl group into specific pharmaceutical and agrochemical compounds. It also serves as an intermediate in other specialty chemical synthesis processes. These applications depend on its chemical reactivity and ability to form different allyl derivatives, supporting demand from pharmaceutical, agrochemical, and specialty chemical manufacturers beyond its major use in epichlorohydrin production.
Allyl chloride production depends heavily on propylene and chlorine, making their prices and availability the main cost risks. Propylene prices are influenced by petrochemical market conditions, including crude oil and propane prices, while chlorine costs depend on electricity prices and operating conditions in the chlor-alkali industry. Since these feedstocks account for a major share of production costs, fluctuations in their prices directly affect the manufacturing cost of allyl chloride. In addition, high-temperature chlorination requires significant energy, further increasing production costs.
The market also faces demand, safety, and supply-related challenges. Demand for allyl chloride is closely linked to epichlorohydrin production and the downstream epoxy resin industry, making it sensitive to changes in construction, coatings, and related industrial activities. Its high flammability, toxicity, and suspected carcinogenicity require strict handling, storage, transportation, and worker-protection measures, increasing operating costs. Furthermore, the market is concentrated among a limited number of integrated producers, creating potential supply constraints and intensifying competition.
The allyl chloride production process runs from propylene and chlorine, through a high-temperature chlorination that substitutes chlorine onto the propylene, to the recovery of the by-product hydrogen chloride and the distillation of the allyl chloride from the chlorinated by-products.
The process begins with the high-temperature chlorination. Propylene and chlorine are reacted at a high temperature, around 500 degree, where the chlorine substitutes for a hydrogen on the carbon next to the double bond of the propylene, giving allyl chloride and hydrogen chloride, in a free-radical reaction. The high temperature favors this substitution to allyl chloride, while a lower temperature would favor the addition of chlorine to give a dichloropropane by-product. Controlling the temperature and the reaction is the foundation of the process, since it determines the yield of allyl chloride against the by-products. The key stage is the separation and recovery. The reaction mixture is cooled, and the by-product hydrogen chloride is separated and recovered, usually as hydrochloric acid, which is a useful by-product. The allyl chloride is then separated from the chlorinated by-products, such as the dichloropropanes and dichloropropenes, by fractional distillation, which is a careful, multi-step separation because several chlorinated compounds are present. This separation and recovery is the heart of making a pure product, and controlling it sets the purity and the recovery of the allyl chloride.
Purification, finishing, and quality control complete the process. The allyl chloride is purified to a high purity by distillation, with the chlorinated impurities and the color controlled, and it is stored cool and under an inert atmosphere due to its flammability. The hydrogen chloride and the chlorinated by-products are recovered and sold or used, and the chlorine and flammable hazards are contained throughout, with scrubbing. The product is tested for purity and chlorinated impurities. The main cost factors are the propylene and the chlorine, with energy, separation, and by-product credits next.
Propylene and chlorine are the main factors affecting allyl chloride production cost. Propylene is a petrochemical feedstock whose price depends on crude oil and broader petrochemical market conditions. Chlorine is obtained from the chlor-alkali industry, where its cost is influenced by electricity prices and the value of caustic soda as a co-product. Together, these feedstocks account for most of the raw material cost. By-product hydrogen chloride and other chlorinated compounds can provide partial cost recovery, reducing the overall manufacturing expenses.
Other important cost factors include energy consumption, product separation, reaction selectivity, and plant capacity. High-temperature chlorination requires energy, although some of the heat generated by the exothermic reaction can be recovered and reused. Fractional distillation to separate allyl chloride from chlorinated by-products also requires energy and careful process control. Reaction selectivity affects product yield, as higher by-product formation increases raw material consumption per unit of finished product. Integration with chlor-alkali and epichlorohydrin production can improve operating efficiency, while larger plants help reduce unit costs by spreading fixed expenses over higher production volumes.
Allyl chloride raw material sourcing centers on propylene and chlorine. Propylene is the carbon feedstock, a petrochemical bought from crackers and refineries, and chlorine is the chlorinating agent, made by the chlor-alkali industry, often on the same site. These two feedstocks are the main cost. The central sourcing concern is securing propylene and chlorine at a competitive cost, usually by being integrated with a chlor-alkali operation for the chlorine and having a reliable propylene supply. The feedstocks are most of the cost, and chlorine is best handled on site.
The quality of the feedstocks affects both the product and the cost. The propylene must be of good purity, since impurities affect the reaction and the product, and the chlorine must be dry and of good quality, since moisture and impurities cause corrosion and by-products. The purity of the feedstocks is checked, and the chlorine is handled with the care that a toxic, reactive gas requires. Each of these factors shows up as the product's purity, the yield, or the cost, and the quality and the safe handling of the feedstocks, especially the chlorine, are central.
These factors shape how allyl chloride producers manage their inputs. Producers are usually integrated chemical companies that make or have chlorine from a chlor-alkali plant on site and secure propylene from the petrochemical industry, and that often use the allyl chloride captive to make epichlorohydrin. Because the feedstocks are most of the cost and chlorine must be handled on site, the integration and the feedstock supply are central. The feedstocks are checked before use. A manufacturer integrated with chlor-alkali and epichlorohydrin, with a competitive propylene supply, holds a clear advantage.
An allyl chloride plant handles chlorine and a toxic, flammable product, so its central concerns are the containment of the hazardous materials and the use of the by-products. The by-product hydrogen chloride is recovered as hydrochloric acid, and the chlorinated by-products are recovered and used or sold, so little is wasted, and the chlorine is used efficiently. The chlorine and the hydrogen chloride are contained and scrubbed to prevent any release, and the toxic, flammable allyl chloride is contained. The heat from the exothermic chlorination is recovered, which improves the energy efficiency. Containing the hazardous materials, recovering the by-products, and recovering the heat are the main ways the plant manages its impact.
The regulatory requirements for allyl chloride are strict, centered on its hazards. The compound is highly flammable, highly toxic, and a suspected carcinogen, with a very low workplace exposure limit. As a result, the plant operates under strict occupational-health, environmental, fire, and chemical-safety rules, including containment, monitoring, worker protection, and controlled flammable storage and transport. The handling of chlorine and hydrogen chloride is tightly regulated. The chlorinated by-products and the effluent are controlled under environmental rules. Producers hold quality, safety, and environmental certifications such as ISO 9001 and ISO 14001, along with specific hazardous-material compliance.
An allyl chloride plant is a large chemical manufacturing facility, often integrated with chlor-alkali and epichlorohydrin production. The main equipment includes high-temperature chlorination reactors made from corrosion-resistant alloys to withstand chlorine and hydrogen chloride at around 500 degree. The plant also requires propylene and chlorine feeding systems, along with heat recovery equipment. Quenching systems and hydrogen chloride recovery units capture the by-product acid, while fractional distillation columns separate allyl chloride from other chlorinated compounds and purify the final product. Additional facilities include inert and flammable product storage, chlorine and hydrogen chloride scrubbers, and containment systems to prevent accidental releases. Utility requirements cover energy, heat recovery, cooling, and power. Civil works include propylene and chlorine storage, the chlorination area, hydrogen chloride recovery, distillation, product storage, scrubbing, effluent treatment, and a quality control laboratory for purity, chlorinated impurities, and color testing.
The operating costs of allyl chloride production are mainly influenced by propylene and chlorine consumption, which account for the largest share of variable costs. Energy required for chlorination and distillation is another major expense, although heat recovery helps reduce overall consumption. By-product hydrogen chloride and other chlorinated compounds can provide additional value and offset some production costs. Labor, maintenance, quality control, and safety and containment requirements further contribute to operating expenses. The production cost per tonne depends largely on feedstock prices, by-product credits, energy consumption, and separation requirements. The allyl chloride plant setup costs are high because of the investment required in high-temperature chlorination reactors, hydrogen chloride recovery systems, and distillation equipment. Overall, feedstocks represent the largest cost component, followed by energy and product separation expenses.
A commercially viable allyl chloride site sits where propylene, chlorine, and the epichlorohydrin chain meet. Producers are usually integrated chemical sites with a chlor-alkali plant for the chlorine, a propylene supply, and often an epichlorohydrin plant that uses the allyl chloride, in the chemical regions of North America, Europe, and Asia. A site needs propylene and chlorine supply, high-temperature chlorination and distillation technology, chlorine and hydrogen chloride handling, and strong safety and containment for the flammable, toxic product. Access to the epichlorohydrin and derivative markets, usually on site, is important. The key factor is integration with chlorine and the epichlorohydrin chain, with a competitive propylene supply.
Investment in an allyl chloride plant mainly depends on its integration with chlor-alkali and epichlorohydrin production. Since feedstocks account for most of the production cost and allyl chloride is largely used captively to produce epichlorohydrin, on-site chlorine production and integration with the epichlorohydrin plant are important considerations. Other key decisions include securing a reliable feedstock supply, selecting suitable chlorination and separation technologies, and investing in safety systems and containment for hazardous materials. Plant capacity and investment should align with the requirements of the integrated epichlorohydrin production chain.
Allyl chloride production is closely linked to chlorine chemistry and the epichlorohydrin industry. North America and Europe host the established major producers, integrated with chlor-alkali and epichlorohydrin. Asia, led by China, is a large and growing producing region, with its large chlor-alkali and epichlorohydrin industry, and Japan and other countries also produce it. The feedstocks, propylene and chlorine, come from the petrochemical and chlor-alkali industries in these regions. The demand, dominated by epichlorohydrin, is worldwide, tied to the epoxy resin and construction markets. A new allyl chloride plant would most likely be built as part of an integrated chlorine and epichlorohydrin complex where propylene and chlorine are available.
Dow
Olin Corporation
Solvay
Formosa Plastics
Sumitomo Chemical
Chinese chlor-alkali and epichlorohydrin producers
Allyl Chloride Production Cost Report
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| Particulars | Details |
|---|---|
| Product Name | Allyl 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) |
Allyl Chloride Production Cost Processes with Cost Analysis
The report involves the cost analysis of production of allyl chloride by the chlorination of propylene via a free radical mechanism at high temperatures.
At Procurement Resource, we focus on improving the should-cost of production for allyl chloride, where the propylene and the chlorine set the cost. The route runs from propylene and chlorine, through the high-temperature chlorination that substitutes chlorine onto the propylene to form allyl chloride and hydrogen chloride, to the recovery of the hydrogen chloride and the fractional distillation that separates the allyl chloride from the chlorinated by-products and purifies it. The cost model resolves each input separately, including propylene, chlorine, energy net of recovered heat, labor, purity and chlorinated-impurity testing, hydrogen chloride recovery, chlorine and hydrogen chloride scrubbing, containment and worker protection, effluent treatment, and packaging, with the feedstocks and the by-product credits shown as key factors. We evaluate CAPEX and OPEX as cost per tonne, with the integrated and the merchant positions distinguished.
Alongside the cost build-up, the report identifies the high-temperature chlorination and the separation steps, the by-product recovery, and the integration with chlor-alkali and epichlorohydrin. It offers a supplier database for propylene, chlorine, and process equipment. It sets out a feasible plant layout covering the propylene and chlorine storage, the chlorination hall, the hydrogen chloride recovery, the distillation area, the flammable product storage, the scrubbing and effluent treatment, and the QC laboratory. By modeling the propylene and chlorine cost, the energy, the separation, the by-product credits, and the integration against scale, the analysis shows where cost can be managed, above all through the feedstocks and the integration. It supports decisions on integration, feedstock sourcing, and plant scale.
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Delivering price trend analysis and procurement market insights at Procurement Resource, with expertise in identifying commodity patterns, supporting purchasing strategies, and improving cost efficiency through actionable market intelligence.
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