Production Cost Report
ICC - Is Bespoken: 0
ICC - Main References: ?
ICC - Issue: G
ICC - Volume: 208
ICC - Report ID: 208-G
ICC - Report Location: United States
ICC - Is Popular: 0
ICC - Is Developed: 1
ICC - Title: LLDPE from Ethylene and 1-Butene (Similar to Spherilene)
ICC - Show Overview: 1
ICC - Report Location ID: 1
ICC - Plant Capacity Unit ID: 14
ICC - Volume Reports List: 208-A,208-B,208-C,208-D,208-E,208-F,208-H
ICC - Related Reports List: 172-A,175-C,175-B,172-B
ICC - Report Location Code: USA
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ICC - Prices: {"versions":{"1":{"1":"799","2":"799","3":"799"},"2":{"1":"1599","2":"1599","3":"1599"},"3":{"1":"2699","2":"2699","3":"2699"}},"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/208-G.jpg
ICC - Process Overview Text: <h6>Product</h6> <p><b>LLDPE</b>. LLDPE (a.k.a. Linear Low Density Polyethylene) is one of the three main types of polyethylene. It is a copolymer of ethylene and alpha-olefins. The most common comonomers (also referred to as short-chain branches) used commercially are 1-butene, 1-hexene, and 1-octene. The physical and mechanical properties of LLDPE are functions of density, type, and amount of comonomer, molecular weight (MW), and molecular weight distribution (MWD). Conventional LLDPE differs from Low Density Polyethylene (LDPE) primarily by having a narrower molecular weight distribution and by not containing long-chain branching. </p> <h6>Raw Materials</h6> <p><b>Ethylene</b>. Ethylene is known as a key building block for the petrochemical industry, being one of the largest-volume petrochemical produced worldwide. It is widely used as chemical intermediate in the production of several end products, including plastics, resins and fibers. Ethylene is largely produced by thermal cracking of petroleum-based feedstocks, in the presence of steam. It is stored in a liquid state under high pressure or at low temperatures. However, ethylene is, most of times, directly supplied to its consumers.</p> <b>Chemicals</b>. </p> <b>1-Butene</b>. 1-butene, cis-2-butene, trans-2-butene, isobutylene and butadiene are usually coproduced as a mixture - referred to as C4 fraction - from petroleum refinery/petrochemical process. Typically, for obtaining pure 1-butene, C4 fraction is sent a selective extraction of isobutylene with sulfuric acid, butadiene selective hydrogenation and distillation for 2-butenes separation. An alternative means of producing 1-butene is the ethylene dimerization. Butenes are mainly used as alkylate and polymer gasoline, in fuel applications, and as co-monomers in the production of some polymers. 1-butene, particularly, is mostly used as a comonomer for LLDPE production, and as a comonomer for modifying high density polyethylene (HDPE).</p>
ICC - Process Schematic Image: //cdn.intratec.us/images/icc/process-schematics/208-G.jpg
ICC - Process Schematic Text: <p>The process under analysis comprises three major sections: (1) Polymerization; (2) Polymer Degassing and (3) Finishing. </p><p>Polymerization. Initially, ethylene and 1-butene are passed through fixed-bed adsorption systems, in which potential catalyst poisons are removed before polymerization. After purification, the ethylene is polymerized in combination with 1-butene in a reaction loop consisting of a fluidized-bed reactor, a compressor and a heat exchanger. The polymerization occurs in the gas phase at mild conditions of temperature and pressure. Propane is used as inert diluent, and hydrogen is used as molecular weight regulator. </p><p>Polymer Degassing. The spherical product particles are fed to a degassing vessel, in which unreacted monomers and hydrogen are removed by a counter-current propane stream. The degassed polymer particles are transferred to a vessel where residual hydrocarbons are removed and the catalyst is deactivated by stripping with steam. The wet polymer is then dried by nitrogen before being transferred to finishing section. The gaseous stream from degassing, containing unreacted monomers and diluent, is passed through a couple of distillation columns for the recovery of such components before being recycled to the polymerization.</p><p>Finishing. The resulting polymer is further fed into an extruder, which is used to incorporate the required additives, as well as to pelletize the polymer. The product is then sent to product blending and storage.</p>
ICC - Short Description: This report presents the economics of Linear Low Density Polyethylene (LLDPE) production from polymer grade (PG) ethylene and 1-butene in the United States. The process examined in this report is similar to LyondellBasell Spherilene S. It comprises a small loop reactor for catalyst activation before the main reaction loop with fluid-bed reactor. Residual hydrocarbons are stripped from the product by nitrogen.
ICC - Main Product: LLDPE
ICC - Plant Capacity: 400.00
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LLDPE from Ethylene and 1-Butene (Similar to Spherilene)

LLDPE Production Costs Report | Issue G | Q2 2024

Production Cost Report

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400 kta United States-based plant   |   Q2 2024   |   107 pages   |   Delivered in PDF

This report presents a cost analysis of a 400 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

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Production Process Information

Process Consumptions

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Plant Capital Cost Summary

Operating Cost Summary

Production Costs Datasheet

Plant Capital Cost Details

Operating Cost Details

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Plant Capacity Assessment

Process Flow Diagrams

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Content Highlights

Plant Capital Cost Summary

Summary outlining the capital cost required for building the LLDPE 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 LLDPE 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 LLDPE 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 LLDPE 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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The cost analyses presented in this report target a 450 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.

LLDPE from Ethylene and 1-Butene (Similar to SCLAIRTECH)

This report examines the costs related to Linear Low Density Polyethylene (LLDPE) production from polymer grade (PG) ethylene and 1-butene in the United States. The process examined in this report is a solution process similar to NOVA Chemicals SCLAIRTECH. The polymerization is carried out in a tubular reactor and a CSTR reactor.

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