Production Cost Report
ICC - Is Bespoken: 0
ICC - Main References: ?
ICC - Issue: B
ICC - Volume: 69
ICC - Report ID: 069-B
ICC - Report Location: United States
ICC - Is Popular: 0
ICC - Is Developed: 1
ICC - Title: Diammonium Phosphate from Phosphate Rock, Sulfuric Acid and Ammonia
ICC - Show Overview: 1
ICC - Report Location ID: 1
ICC - Plant Capacity Unit ID: 14
ICC - Volume Reports List: 069-A,069-B,069-C
ICC - Related Reports List: 070-A,070-B
ICC - Report Location Code: USA
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ICC - Prices: {"versions":{"1":{"1":"1399","2":"1399","3":"1399"},"2":{"1":"2199","2":"2199","3":"2199"},"3":{"1":"3599","2":"3599","3":"3599"}},"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/069-B.jpg
ICC - Process Overview Text: <h6>Product</h6> <b>Diammonium Phosphate</b></p></b></p> <h6>Raw Materials</h6> <p><b>Chemicals</b></p>, <p><b>Ammonia</b></p>, <p><b>Sulfuric Acid</b></p>, <p><b>Rock Phosphate</b></p>
ICC - Process Schematic Image: //cdn.intratec.us/images/icc/process-schematics/069-B.jpg
ICC - Process Schematic Text: <p>The process under analysis comprises four major sections: (1) Phosphoric acid production; (2) Ammoniation-granulation; (3) Drying, cooling and sizing; and (4) Scrubbers. </p><p>Phosphoric acid production. Phosphate rock is first ground before being fed to the digestion reactor, which has two compartments. The first compartment receives the ground rocks and recycled phosphoric acid; sulfuric acid is added in the second compartment. The slurry formed in the reactor is filtered to remove dihydrate calcium sulfate (gypsum). The filtered acid proceeds to clarification, then concentration via two evaporators. The first one concentrates it to 40% P2O5 and the second one to 54% P2O5. A bypass stream of 40% P2O5 acid is used in the ammonia scrubbers downstream. The 54% P2O5 acid is clarified a second time, then fed to the pre-neutralizer. </p><p>Ammoniation-granulation. Phosphoric acid, gaseous ammonia, and scrubber liquor are fed to the pre-neutralizer reactor. An ammonium phosphate slurry is formed and sent to the pipe reactor, along with additional phosphoric acid and gaseous ammonia. The reaction mixture from the pipe-reactor is sprayed onto the rolling bed of the rotary ammoniator-granulator, where the slurry then reacts with additional liquid ammonia and recycled solids from the sizing and crushing area. </p><p>Drying, cooling and sizing. The Diammonium Phosphate granules formed in the granulator are dried, then distributed over screens to separate onsize material from the oversize and undersize material. The oversize material is sent to chain mills, then recycled along with the undersize material to the granulator. Finally, DAP granules are cooled and packed in bags to be stored in warehouses. </p><p>Scrubbers. A scrubbing system is used to capture fluorine compounds from the off-gases produced during phosphoric acid production. Another system is used to recover the unabsorbed ammonia gases from pre-neutralizer, granulator, dryer, and cooler. The aforementioned 40% P2O5 phosphoric acid is used in the second system. The scrubber liquor with recovered ammonia is recycled to the pre-neutralizer. </p>
ICC - Short Description: This study presents the economics of a plant located in the United States producing Diammonium Phosphate (DAP formulation 18-46-0) from phosphoric acid and ammonia integrated the production of phosphoric acid from phosphate rock and sulfuric acid.
ICC - Main Product: Diammonium Phosphate
ICC - Plant Capacity: 800.00
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Diammonium Phosphate from Phosphate Rock, Sulfuric Acid and Ammonia

Diammonium Phosphate Production Costs Report | Issue B | Q2 2024

Production Cost Report

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

This report presents a cost analysis of a 800 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

Plant Capital Cost Summary

Operating Cost Summary

Production Costs Datasheet

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Production Process Information

Process Consumptions

Labor Requirements

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Operating Cost Summary

Production Costs Datasheet

Plant Capital Cost Details

Operating Cost Details

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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 Diammonium Phosphate 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 Diammonium Phosphate 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 Diammonium Phosphate 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 Diammonium Phosphate 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 Diammonium Phosphate Production Cost Reports

Diammonium Phosphate from Phosphoric Acid and Ammonia

This feasibility study shows the economics of Diammonium Phosphate (DAP formulation 18-46-0) production from phosphoric acid and ammonia via an ammoniation-granulation process. The reaction occurs in a sequence of pre-neutralizer, pipe-reactor and granulator. The economic analysis presented is based on a plant constructed in the United States.

Details: 850 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue A   From $799 USD

The cost analyses presented in this report target a 850 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.

Diammonium Phosphate from Phosphate Rock, Sulfuric Acid and Ammonia

This study presents the economics of a plant located in the United States producing Diammonium Phosphate (DAP formulation 18-46-0) from phosphoric acid and ammonia integrated the production of phosphoric acid from phosphate rock and sulfuric acid.

Details: 800 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue B   From $1,399 USD

The cost analyses presented in this report target a 800 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.

Diammonium Phosphate from Phosphate Rock, Sulfur and Ammonia

This report concerns the production of Diammonium Phosphate (DAP formulation 18-46-0) via an integrated plant comprising: (1) sulfuric acid production from sulfur; (2) phosphoric acid production from phosphate rock; and (3) Diammonium Phosphate (DAP formulation 18-46-0) production from phosphoric acid and ammonia. The economic analysis performed is based on a plant constructed in the United States.

Details: 750 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue C   From $1,699 USD

The cost analyses presented in this report target a 750 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

Ammonia Production from Syngas

This report presents the economics of Ammonia production from synthesis gas (syngas). In this process, hydrogen, recovered from syngas feedstock, and nitrogen, recovered from air, react producing Ammonia. The economic analysis performed assumes a plant located in the United States.

Details: 800 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue A   From $799 USD

The cost analyses presented in this report target a 800 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.

Ammonia Production from Natural Gas (Combined Reforming)

This report presents the economics of Ammonia production from natural gas in the United States using a process similar to KBR Purifier process. In the process examined, syngas is initially produced from natural gas via a combined reforming. The syngas is purified through several steps into nitrogen and hydrogen which are synthesized to ammonia.

Details: 800 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue B   From $1,199 USD

The cost analyses presented in this report target a 800 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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