Production Cost Report
ICC - Is Bespoken: 0
ICC - Main References: ?
ICC - Issue: A
ICC - Volume: 300
ICC - Report ID: 300-A
ICC - Report Location: United States
ICC - Is Popular: 0
ICC - Is Developed: 1
ICC - Title: Calcium Hypochlorite from Slaked Lime and Cl2 (Sodium Method)
ICC - Show Overview: 1
ICC - Report Location ID: 1
ICC - Plant Capacity Unit ID: 14
ICC - Volume Reports List: 300-B
ICC - Related Reports List: 110-B,110-A,111-B,111-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/300-A.jpg
ICC - Process Overview Text: <h6>Products</h6> <p><b>Calcium Hypochlorite</b></p>, <p><b>Sodium Chloride Solution</b></p> <h6>Raw Materials</h6> <p><b>Caustic Soda</b></p>, <p><b>Chlorine</b></p>, <p><b>Slaked Lime</b></p>
ICC - Process Schematic Image: //cdn.intratec.us/images/icc/process-schematics/300-A.jpg
ICC - Process Schematic Text: <p>The process under analysis comprises three major sections: (1) Reaction; (2) Separation; and (3) Finishing.</p><p>Reaction. Initially, caustic soda solution is mixed with recycled bleach mother liquor, composed of calcium hypochlorite and sodium chloride dissolved in water, in the caustic mixing vessel. The resulting solution is sent to the lime mixing vessel, where slaked lime is fed to form a milk of lime slurry. Such milk is forwarded to the salt nucleator vessel, where it is mixed with chlorinator liquor recycle and recycled bleach mother liquor. The resulting solution is supersatured with sodium chloride and calcium hypochlorite, what initiates the precipitation of the crystals. The mixture from salt nucleator vessel is fed to the chlorinator along with gaseous chlorine, which reacts with calcium hydroxide and sodium hydroxide to form calcium hypochlorite and sodium chloride. In this way, further crystals of calcium hypochlorite and sodium chloride are formed and growth of preexisting crystals occurs.</p><p>Separation. The chlorinator outlet slurry is fed at the midpoint of a two-stage upward flow cylindrical elutriator-classifier. Bleach mother liquor is fed at the bottom portion of the lower stage of the elutriator as the elutriating fluid. The upper stream of the elutriator, an aqueous slurry containing most of calcium hypochlorite, is sent to calcium hypochlorite centrifuge. The bottom product of the elutriator, an aqueous slurry containing the denser sodium chloride crystals, is centrifuged; the sodium chloride wet cake is then conveyed to an intermediate tank. The salt centrifuge mother liquor is sent to the calcium hypochlorite centrifuge.</p><p>Finishing. The wet cake from calcium hypochlorite centrifuge is dried in a turbo dryer; gases from the dryer are scrubbed and released. The dry calcium hypochlorite is squeezed, prilled and then classified; the oversize and undersize solids are returned for further processing, while the calcium hypochlorite product is directed to packing.</p><p></p>
ICC - Short Description: This report presents the economics of Calcium Hypochlorite (70 wt%) production from slaked lime, sodium hydroxide and chlorine via a typical sodium process. In this process, chlorine is passed into a slurry of slaked lime and sodium hydroxide, generating calcium hypochlorite and sodium chloride. The economic analysis is based on a plant located in the United States.
ICC - Main Product: Calcium Hypochlorite
ICC - Plant Capacity: 25.00
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Calcium Hypochlorite from Slaked Lime and Cl2 (Sodium Method)

Calcium Hypochlorite Production Costs Report | Issue A | Q3 2024

Production Cost Report

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

This report presents a cost analysis of a 25 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 Calcium Hypochlorite 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 Calcium Hypochlorite 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 Calcium Hypochlorite 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 Calcium Hypochlorite 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 Calcium Hypochlorite Production Cost Reports

Calcium Hypochlorite from Slaked Lime and Cl2 (Calcium Method)

This report presents the economics of Calcium Hypochlorite production from slaked lime and chlorine via a typical calcium process. In this process, slaked lime is hydrated and chlorinated. A mixture of Calcium Hypochlorite, calcium chloride, and calcium hydroxide (also known as bleaching powder) is obtained as the final product. The economic analysis is based on a plant located in the United States.

Details: 25 kta United States-based plant   |   Q3 2024   |   107 pages   |   Issue B   From $1,199 USD

The cost analyses presented in this report target a 25 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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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.

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