Production Cost Report
ICC - Is Bespoken: 0
ICC - Main References: ?
ICC - Issue: D
ICC - Volume: 208
ICC - Report ID: 208-D
ICC - Report Location: United States
ICC - Is Popular: 0
ICC - Is Developed: 1
ICC - Title: LLDPE from Ethylene and 1-Octene (Similar to DOWLEX)
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-E,208-F,208-G,208-H
ICC - Related Reports List: 277-C,277-B,172-B,172-A
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-D.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-Octene</b>. Octene is any alkene having eight carbons. Among octene isomers, 1-octene is considered and important liner alpha olefin (LAO), produced commercially from ethylene oligomerization, Fischer-Tropsch synthesis and dehydration of alcohols. Main uses of octene are in organic sysnthesis, primarily as comonomer in the production of linear low-density polyethylene (LLDPE) and high-density polyethylene (HDPE). To a lesser extent, this chemical is used in plasticizers, surfactants, pulp and paper industry and lubricants, among others.</p>
ICC - Process Schematic Image: //cdn.intratec.us/images/icc/process-schematics/208-D.jpg
ICC - Process Schematic Text: <p>The process under analysis comprises four major sections: (1) Polymerization; (2) Devolatilization; (3) Distillation; and (4) Finishing.</p><p>Polymerization. Ethylene and 1-octene are sent to fixed-bed adsorption systems to remove water, oxygen and other polar impurities (potential catalyst poisons). The purified monomers are then mixed with the polymerization solvent (C8-C9 parrafins mixture) and fed to the first of two continuous stirred tank reactors (CSTR) operating in series, where the polymerization itself takes place. The polymerization is carried out adiabatically in the liquid phase, and hydrogen act as molecular weight regulator. </p><p>Devolatilization & Pelletizing. The polymer solution exiting the second reactor is fed into an adiabatic flash vessel, where the reduction in pressure allows volatile components, mainly unreacted ethylene, to vaporize. The concentrated polymer solution from the flash vessel is heated and subsequently passed through a devolatilization vessel, in such a way that residual monomers are removed from the polymer. Volatile components separated from the polymer are cooled and directed to distillation section., while the polymer is directed to finishing section. The devolatilized polymer stream 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><p>Raw Materials Recovery. The gaseous streams from the devolatilization, containing unreacted monomers and solvent, are passed through a couple of distillation columns for the recovery of such components and removal of heavy impurities.</p>
ICC - Short Description: This report presents the economics of Linear Low Density Polyethylene (LLDPE) production from polymer grade (PG) ethylene and 1-octene in the United States. The process examined in this report is similar to Dow DOWLEX. In this technology, the polymerization is carried out in two CSTR reactors operating in series.
ICC - Main Product: LLDPE
ICC - Plant Capacity: 300.00
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LLDPE from Ethylene and 1-Octene (Similar to DOWLEX)

LLDPE Production Costs Report | Issue D | Q2 2024

Production Cost Report

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

This report presents a cost analysis of a 300 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

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

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

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