Production Cost Report
ICC - Is Bespoken: 0
ICC - Main References: ?
ICC - Issue: K
ICC - Volume: 230
ICC - Report ID: 230-K
ICC - Report Location: United States
ICC - Is Popular: 0
ICC - Is Developed: 0
ICC - Title: Propylene Production from Butenes
ICC - Show Overview: 1
ICC - Report Location ID: 1
ICC - Plant Capacity Unit ID: 14
ICC - Volume Reports List: 230-A,230-B,230-C,230-D,230-E,230-G,230-H,230-I,230-J,230-L,230-M,230-F,230-N
ICC - Related Reports List: 199-C,199-A
ICC - Report Location Code: USA
ICC - Delivery Times: {"versions":{"1":{"1":{"time":"10","price":0},"2":{"time":"5","price":"599"}},"2":{"1":{"time":"10","price":0},"2":{"time":"5","price":"599"}},"3":{"1":{"time":"12","price":0},"2":{"time":"7","price":"599"}}},"unit":"d"}
ICC - Prices: {"versions":{"1":{"1":"1199","2":"1199","3":"1199"},"2":{"1":"1999","2":"1999","3":"1999"},"3":{"1":"3399","2":"3399","3":"3399"}},"currency":"USD"}
ICC - Plant Capacity Unit Name: kilo metric ton per annum
ICC - Plant Capacity Unit Short Name: kta
ICC - Process Overview Image: //cdn.intratec.us/images/icc/process-overview/230-K.jpg
ICC - Process Overview Text: <h6>Products</h6> <p><b>Propylene</b>. Propylene, the main raw material consumed, is a colorless gas at room temperature. It is a low-boiling, flammable, and highly volatile gas, with molecular formula C3H6. Propylene reacts vigorously with oxidizing materials. It may be mildly irritating to the nose, throat, and respiratory tract; propylene has low acute toxicity from inhalation. PG Propylene has been mainly produced as ethylene manufacturing co-product (via steam cracking of paraffinic hydrocarbons) and by-product of petroleum refining (separation from refinery gas). Most recently, amid a tight propylene market, new and novel lower-cost chemical processes for on-purpose propylene production have emerged.</p> <p><b>Crude C5s</b>. Crude C5s are a byproduct of naphtha cracking, consisting of a mixture of C5 hydrocarbons. They serve as feedstocks for the production of synthetic rubbers, resins, and adhesives. Crude C5s are separated through distillation and refining processes and are stored as liquids. They play a significant role in the chemical industry, especially in the production of high-performance elastomers.</p> <h6>Raw Material</h6> <p><b>Raffinate-1</b>. Raffinate-1 is a C4 residual stream primarily consisting of isobutylene, 1-butylene, 2-butylenes, and butanes, obtained from the extraction of 1,3-butadiene from crude C4s stream, which is one of the products of the naphtha steam cracking processes.</p>
ICC - Process Schematic Image: //cdn.intratec.us/images/icc/process-schematics/230-K.jpg
ICC - Short Description: This report analyses the economics of Polymer Grade (PG) Propylene production from raffinate-1 in the United States, using two typical integrated processes: isomerization and metathesis. In these processes, 1-butene present in raffinate-1 is isomerized into 2-butenes. The 2-butenes are submitted with ethylene to a metathesis reaction, producing propylene. A C5s stream is generated as by-product.
ICC - Main Product: Propylene
ICC - Plant Capacity: 480.00
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ICC - Table Count: {"versions":{"1":"22","2":"28","3":"34"}}

Propylene Production from Butenes

Propylene Production Costs Report | Issue K | Q3 2024

Production Cost Report

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480 kta United States-based plant   |   Q3 2024   |   107 pages

This report presents a cost analysis of a 480 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.

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Production Process Information

Process Consumptions

Labor Requirements

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Production Costs Datasheet

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Production Process Information

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Production Costs Datasheet

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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

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Content Highlights

Plant Capital Cost Summary

Summary outlining the capital cost required for building the Propylene 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 Propylene 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 Propylene 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 Propylene 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

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This report presents the economics of Polymer Grade (PG) Propylene production from vacuum gas oil (VGO) in China. The portrayed process is similar to Sinopec Deep Catalytic Cracking (DCC) technology, in which VGO is converted to Propylene, generating propane, C4 fraction, C5+ naphtha and fuel oil as by-products.

Details: 400 kta China-based plant   |   Q3 2024   |   107 pages   |   Issue I   From $799 USD

The cost analyses presented in this report target a 400 kta (kilo metric ton per annum per annum) China-based plant. For those interested in cost analyses considering other plant capacities and/or locations, Intratec offers a customized analysis as an optional feature.

PG Propylene Production from RG Propylene

This report examines the costs related to Polymer Grade (PG) Propylene production from refinery grade (RG) propylene, via a typical purification process. Propane stream is generated as by-product. The economic analysis performed assumes a plant located in the United States.

Details: 400 kta United States-based plant   |   Q3 2024   |   107 pages   |   Issue J   From $799 USD

The cost analyses presented in this report target a 400 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.

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Other Related Production Cost Reports

PP Homopolymer from Propylene (Spheripol)

This report presents the economics of Polypropylene (PP) Homopolymer production from polymer grade (PG) propylene. The process under analysis uses a bulk phase polymerization process similar to LyondellBasell Spheripol and Mitsui Hypol II. The economic analysis performed assumes a plant located in the United States.

Details: 350 kta United States-based plant   |   Q3 2024   |   107 pages   |   Issue A   From $799 USD

The cost analyses presented in this report target a 350 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.

PP Homopolymer from Propylene (Spherizone)

This report examines the costs related to Polypropylene (PP) Homopolymer production from polymer grade (PG) propylene, using a gas phase polymerization process similar to LyondellBasell Spherizone. The reaction occurs in a multi-zone circulating reactor (MZCR). The economic analysis performed assumes a plant located in the United States.

Details: 350 kta United States-based plant   |   Q3 2024   |   107 pages   |   Issue C   From $799 USD

The cost analyses presented in this report target a 350 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.

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