Polychloroprene Production from Butadiene and Chlorine
Neoprene Production Costs Report | Issue B | Q3 2024
| Report Details |
| 50 kta United States-based plant | Q3 2024 | 107 pages |
This report presents a cost analysis of a 50 kta (kilo metric ton per annum) United States-based plant. You can add a customized cost analysis, assuming another location (country), when ordering a premium edition of this report.
Report Abstract
This study provides an economic analysis of Polychloroprene production starting from butadiene and chlorine, based on a plant located in the United States. In the first step, butadiene is chlorinated, generating dichlorobutenes, which are subjected to an isomerization to convert them to 3,4-dichloro-1-butene. It is then dehydrochlorinated, forming chloroprene. Finally, chloroprene is polymerized to the respective rubber.
The report provides a comprehensive study of Neoprene production and related Neoprene production cost, covering three key aspects: a complete description of the Neoprene production process examined; an in-depth analysis of the related Neoprene plant capital cost (Capex); and an evaluation of the respective Neoprene plant operating costs (Opex).
The Neoprene production process description includes a block flow diagram (BFD), an overview of the industrial site installations, detailing both the process unit and the necessary infrastructure, process consumption figures and comprehensive process flow diagrams (PFD). The Neoprene plant capital cost analysis breaks down the Capex by plant cost (i.e., ISBL, OSBL and Contingency); owner's cost; working capital; and costs incurred during industrial plant commissioning and start-up. The Neoprene plant operating costs analysis covers operating expenses, including variable costs like raw materials and utilities, and fixed costs such as maintenance, labor, and depreciation.
Process Schematic
The process under analysis comprises two major sections: (1) Butadiene Chlorination; and (2) Chloroprene Polymerization.
Butadiene Chlorination. In the first step, butadiene, chlorine and recycled butadiene and hydrochloric acid are mixed and fed to the chlorination reactor, where butadiene is chlorinated in the vapor phase. A large excess of butadiene is used to prevent the formation of super chlorinated species during this reaction. The two main products of the chlorination are 1,4-dichloro-2-butene and 3,4-dichloro-1-butene. An isomerization step is used to convert 1,4-dichloro-2-butene into 3,4-dichloro-1-butene (precursor to chloroprene), conducted in the reboiler of a distillation column. Caustic soda is diluted in process water, mixed with the 3,4-dichloro-1-butene stream and fed to a series of continuously stirred vessels. The gaseous chloroprene-rich stream is separated from heavy ends by means of stripping, evaporation and distillation steps.
Chloroprene Polymerization. The Polymerization is comprised of continuously stirred jacketed tank reactors connected in series, cooled by a brine solution. Chloroprene is first mixed with emulsifier, demineralized water and initiators (hydroperoxides/ferrous sulfates). The polymer molecular weight is controlled by means of a chain-transfer agent (tertiary dodecyl mercaptan). The reaction termination is accomplished with the addition of shortstop agents.The latex produced is steam-stripped for the removal of residual chloroprene, recycled. The hot latex is mixed with antioxidant and fed to a freeze roll to be coagulated into a polymer sheet, which is fed to a wash belt for removing polymerization reaction medium. The washed Polychloroprene film is dried in squeeze rolls and continuous-belt dryers. After drying, the film is formed into a rope and cut into polychloroprene chips, packed in bags.
Up-to-date PDF Report
Professional report based on Q3 2024 economic data, ensuring timely evaluations.
Multiple Use Cases
Ideal for investment screening, feasibility studies, cost estimates, and research planning.
Proven Methodology
Developed using a consistent methodology honed over a decade, ensuring reliable cost analyses.
Compact
$1,199 USD
Production Process Information
Process Consumptions
Labor Requirements
Plant Capital Cost Summary
Operating Cost Summary
Production Costs Datasheet
Pages | Tables | Images
Read-only Online PDF Format
Updated with Q3 2024 Data
DETAILED
$1,999 USD
Production Process Information
Process Consumptions
Labor Requirements
Plant Capital Cost Summary
Operating Cost Summary
Production Costs Datasheet
Plant Capital Cost Details
Operating Cost Details
Pages | Tables | Images
Downloadable PDF Format
Updated with Q3 2024 Data
PREMIUM
MOST POPULAR
$3,399 USD
Production Process Information
Process Consumptions
Labor Requirements
Plant Capital Cost Summary
Operating Cost Summary
Production Costs Datasheet
Plant Capital Cost Details
Operating Cost Details
Plant Cost Breakdowns
Plant Capacity Assessment
Process Flow Diagrams
Costs in Different Countries Add-on
Pages | Tables | Images
Print-enabled PDF Format Add-on
Updated with Q3 2024 Data
Share with Co-workers
Technical Support via Email
Content Highlights
Plant Capital Cost Summary
Summary outlining the capital cost required for building the Neoprene production plant examined
Plant Capital Cost Details
Detailing of fixed capital (ISBL, OSBL & Owner’s Cost), working capital and additional capital requirements
Plant Cost Breakdowns
Breakdown of Neoprene process unit (ISBL) costs and infrastructure (OSBL) costs; plant cost breakdown per discipline
Operating Costs Summary
Summary presenting the operating variable costs and the total operating cost of the Neoprene production plant studied
Operating Cost Details
Detailing of utilities costs, operating fixed costs and depreciation
Plant Capacity Assessment
Comparative analysis of capital investment and operating costs for different Neoprene plant capacities
Production Process Information
Block Flow Diagram, descriptions of process unit (ISBL) and site infrastructure (OSBL)
Process Consumptions
Raw materials and utilities consumption figures, by-products credits, labor requirements
Process Diagrams
Process flow diagrams (PFD), equipment list and industrial site configuration
Other Neoprene Production Cost Reports
Polychloroprene Production from Chloroprene
This report presents the economics of Chloroprene Rubber (or Polychloroprene) production from chloroprene using a typical emulsion process. The economic analysis is based on a plant constructed in the United States.
Details: 50 kta United States-based plant | Q3 2024 | 107 pages | Issue A From $999 USD
The cost analyses presented in this report target a 50 kta (kilo metric ton per annum per annum) United States-based plant. For those interested in cost analyses considering other plant capacities and/or locations, Intratec offers a customized analysis as an optional feature.
Could Not Find the Report You Need?
Obtain a Bespoke Report
Get a report targeting the process in which you are interested
See Offer Details
Understand Bespoke Reports and how you can easily order them
Check Editions & Pricing
Complete a brief form and see a quotation for your Bespoke Report
Other Related Production Cost Reports
Sodium Hydroxide Production from Sodium Chloride (Membrane Process)
This report presents the economics of Sodium Hydroxide production from sodium chloride in the United States, via a typical membrane process. In this process, sodium chloride is decomposed electrolytically, producing sodium hydroxide. Chlorine and hydrogen are generated as by-products in the process.
Details: 550 kta United States-based plant | Q3 2024 | 107 pages | Issue A From $799 USD
The cost analyses presented in this report target a 550 kta (kilo metric ton per annum per annum) United States-based plant. For those interested in cost analyses considering other plant capacities and/or locations, Intratec offers a customized analysis as an optional feature.
Sodium Hydroxide Production from Sodium Chloride (Diaphragm Process)
It presents the economics of Sodium Hydroxide production from brine in the United States. The process examined in this report is a typical diaphragm process. Chlorine and hydrogen are also generated as by-products in the process.
Details: 600 kta United States-based plant | Q3 2024 | 107 pages | Issue B From $799 USD
The cost analyses presented in this report target a 600 kta (kilo metric ton per annum per annum) United States-based plant. For those interested in cost analyses considering other plant capacities and/or locations, Intratec offers a customized analysis as an optional feature.
Chlorine Production from Sodium Chloride (Membrane Process)
This study presents the economics of Chlorine production from sodium chloride via a membrane process plant located in the United States. In the process under analysis, an aqueous solution of sodium chloride (brine) is decomposed electrolytically in a membrane cell, producing Chlorine, sodium hydroxide and hydrogen.
Details: 500 kta United States-based plant | Q3 2024 | 107 pages | Issue A From $799 USD
The cost analyses presented in this report target a 500 kta (kilo metric ton per annum per annum) United States-based plant. For those interested in cost analyses considering other plant capacities and/or locations, Intratec offers a customized analysis as an optional feature.
Chlorine Production from Sodium Chloride (Diaphragm Process)
This study presents the economics of Chlorine production from sodium chloride via a diaphragm plant located in the United States. In the process under analysis, an aqueous solution of sodium chloride (brine) is decomposed electrolytically in a diaphragm cell, producing Chlorine, sodium hydroxide and hydrogen.
Details: 550 kta United States-based plant | Q3 2024 | 107 pages | Issue B From $799 USD
The cost analyses presented in this report target a 550 kta (kilo metric ton per annum per annum) United States-based plant. For those interested in cost analyses considering other plant capacities and/or locations, Intratec offers a customized analysis as an optional feature.
Butadiene Production from n-Butane
This report presents the economics of 1,3-Butadiene (BD) production from n-butane. In the process, n-butane undergoes a dehydrogenation reaction process similar to Lummus Catadiene, generating a C4s stream which is purified to obtain 1,3-Butadiene. The economic analysis is based on a plant located in the United States.
Details: 100 kta United States-based plant | Q3 2024 | 107 pages | Issue A From $799 USD
The cost analyses presented in this report target a 100 kta (kilo metric ton per annum per annum) United States-based plant. For those interested in cost analyses considering other plant capacities and/or locations, Intratec offers a customized analysis as an optional feature.
Butadiene Production from Butenes
This study presents the economics of 1,3-Butadiene (BD) production from mixed butenes in a plant assumed to be erected in the United States. In this process, which is similar to TPC/UOP Oxo-D, butenes are catalytically dehydrogenated to produce the Butadiene product. Raffinate is obtained as by-product.
Details: 240 kta United States-based plant | Q3 2024 | 107 pages | Issue B From $799 USD
The cost analyses presented in this report target a 240 kta (kilo metric ton per annum per annum) United States-based plant. For those interested in cost analyses considering other plant capacities and/or locations, Intratec offers a customized analysis as an optional feature.
+800 Reports Developed, Targeting +250 Commodities
Best-in-Class Reports
Analysis of capital and operating costs of commodity production processes. Prices starting at $799 USD
Vast Report Library
858 independent and up-to-date reports examining embryonic and established production processes
Free Sample Reports
Quickly understand the structure and depth of content of our professional reports