Production Cost Report
ICC - Is Bespoken: 0
ICC - Main References: ?
ICC - Issue: A
ICC - Volume: 111
ICC - Report ID: 111-A
ICC - Report Location: United States
ICC - Is Popular: 0
ICC - Is Developed: 1
ICC - Title: Chlorine Production from Sodium Chloride (Membrane Process)
ICC - Show Overview: 1
ICC - Report Location ID: 1
ICC - Plant Capacity Unit ID: 14
ICC - Volume Reports List: 111-B,111-C,111-E,111-D,111-F
ICC - Related Reports List: 089-B,852-D,326-A,176-D,089-F,852-C
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/111-A.jpg
ICC - Process Overview Text: <h6>Products</h6> <p><b>Chlorine</b></p>, <p><b>Hydrogen</b></p>, <p><b>Caustic Soda</b></p> <h6>Raw Materials</h6> <p><b>Electricity</b></p>, <p><b>Chemicals</b></p>, <p><b>Sodium Chloride</b></p>, <p><b>HCl</b></p>, <p><b>Sulfuric Acid</b></p>
ICC - Process Schematic Image: //cdn.intratec.us/images/icc/process-schematics/111-A.jpg
ICC - Process Schematic Text: <p>The process under analysis comprises three major sections: (1) Brine purification; (2) Electrolysis; and (3) Products Recovery.</p><p>Brine purification. Initially, recycled depleted brine is mixed with water and resaturated with fresh NaCl salt (sodium chloride). Heavy metal ions (e.g. Ca2+ and Mg2+) ions present in the brine would be harmful to the membranes. So the brine is treated with precipitants, in such a way the heavy metals precipitate forming a sludge, which is removed by settling in a clarifier. Subsequently, the clarified solution is filtered and then purified by ion exchange resins to remove residual hardness and achieve acceptable levels. </p><p>Electrolysis. The ultrapure brine and electricity are the main inputs to the electrolysis area. The brine is fed into the anolyte compartments of the cells, separated from the catholyte by cation-exchange membranes. Chlorine gas is generated at the anodes and sodium ions migrate through the membranes into the catholytes. The depleted brine from the anode compartments is dechlorinated downstream and then returned to brine saturation. On the catholyte side, water is electrolyzed generating hydrogen gas and hydroxyl ions. The membranes prevent the migration of such hydroxyl ions into the anolytes, in such a way that hydroxyl ions combine with the sodium ions forming caustic soda. The addition of demineralized water keeps the catholytes concentration at the desired level.</p><p>Products recovery. Hydrogen from electrolysis is compressed and directed to consumers. The caustic soda solution is concentrated to a saturated 50% NaOH solution – the commercialized form. The chlorine gas produced is sent to a drying system, consisting of drying towers where concentrated sulfuric acid circulates as dehydrating agent. The dry chlorine gas is compressed and then liquefied before being sent to storage.</p>
ICC - Short Description: 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.
ICC - Main Product: Chlorine
ICC - Plant Capacity: 500.00
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Chlorine Production from Sodium Chloride (Membrane Process)

Chlorine Production Costs Report | Issue A | Q2 2024

Production Cost Report

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500 kta United States-based plant   |   Q2 2024   |   107 pages

This report presents a cost analysis of a 500 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 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 Chlorine 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 Chlorine 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 Chlorine 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 Chlorine 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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Details: 550 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue B   From $799 USD

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Chlorine Production from Sodium Chloride (Mercury Cell Process)

This study presents the economics of Chlorine production from sodium chloride via a mercury cell process. The plant is assumed to be located in the United States. In the process under analysis, an aqueous solution of sodium chloride (brine) is decomposed electrolytically in a mercury cell, producing Chlorine, sodium hydroxide and hydrogen.

Details: 250 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue C   From $799 USD

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Sulfuric Acid from Sulfur (Single-Contact Process)

This report presents the economics of Sulfuric Acid production from sulfur in the United States. In this process, sulfur is burned to form sulfur dioxide, which is then converted to sulfur trioxide. This sulfur trioxide is converted to sulfuric acid by absorption with recirculating sulfuric acid solution in water in only one column.

Details: 1,480 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue B   From $999 USD

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This report presents the economics of spent sulfuric acid regeneration via wet sulfuric acid (WSA) process in the United States. In this process, spent acid is decomposed to form sulfur dioxide and water. The sulfur dioxide is oxidized to sulfur trioxide, which is then regenerated to sulfuric acid by vapor-phase reaction with water.

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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.

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This report presents the economics of Aluminum Chloride production from aluminum metal and chlorine in the United States. In the process, chlorine gas is passed through molten aluminum, producing Anhydrous Aluminum Chloride.

Details: 10 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue A   From $799 USD

The cost analyses presented in this report target a 10 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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