Production Cost Report
ICC - Is Bespoken: 0
ICC - Main References: ?
ICC - Issue: C
ICC - Volume: 70
ICC - Report ID: 070-C
ICC - Report Location: United States
ICC - Is Popular: 0
ICC - Is Developed: 1
ICC - Title: Ammonia Production from Natural Gas (Chemical Looping Process)
ICC - Show Overview: 1
ICC - Report Location ID: 1
ICC - Plant Capacity Unit ID: 14
ICC - Volume Reports List: 070-A,070-B,070-D,070-E,070-F
ICC - Related Reports List: 247-D,069-A
ICC - Report Location Code: USA
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ICC - Prices: {"versions":{"1":{"1":"1199","2":"1199","3":"1199"},"2":{"1":"1999","2":"1999","3":"1999"},"3":{"1":"3399","2":"3399","3":"3399"}},"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/070-C.jpg
ICC - Process Overview Text: <h6>Product</h6> <p><b>Ammonia</b>. Ammonia (NH3) is one of the most produced synthetic chemicals worldwide. The main application of this world class commodity is in nitrogen fertilizers, followed by the synthesis of nitric acid. It is also used, to a lesser extent, in several other applications such as pulping of wood and as ingredient in household cleaners and drugs. Ammonia is produced basically by the reaction between nitrogen and hydrogen, in a 1:3 stoichiometric ratio. Its production routes are related to the source of the hydrogen used, being steam reforming the main one.</p> <h6>Raw Material</h6> <p><b>Natural Gas</b>. Natural gas is a naturally occurring mixture of hydrocarbon found in porous subsurface geologic formations. It is composed mainly of methane, but also contains varying amounts of higher hydrocarbons such as ethane, propane, and butane. Additionally, natural gas may also include non-hydrocarbon components considered impurities such as nitrogen, carbon dioxide, and hydrogen sulfide. Natural gas is primarily used as a source of heat energy for residential, commercial, and industrial applications. It may also be used in the production of important chemicals such as ammonia, methanol, and hydrogen. </p>
ICC - Process Schematic Image: //cdn.intratec.us/images/icc/process-schematics/070-C.jpg
ICC - Process Schematic Text: <p>The process under analysis comprises two major sections: (1) Chemical-looping and (2) Ammonia Synthesis.</p><p>Chemical-looping. After being compressed and desulfurized, the natural gas is fed into the first of three chemical-looping reactors. Via an oxidation reaction, the natural gas is converted into CO2 and water, that are discarded in further steps. Along with the oxidation reaction, there is the regeneration (reduction) of the iron catalyst, which goes to the next reactor. In this second reactor, steam is converted into hydrogen, by the partial oxidation of the catalyst. Hydrogen produced is sent to a Purification system to remove water (by compression and condensation). The catalyst is transferred to the third reactor, where ambient air is fed into. The catalyst is fully oxidized by all the oxygen present in air, remaining almost-pure nitrogen, which is sent to Ammonia Synthesis area, where it is mixed with purified hydrogen. Excess nitrogen is purged to prevent its accumulation.</p><p>Ammonia Synthesis. Hydrogen and nitrogen are compressed, heated, and fed into the Ammonia Reactor, an intercooled horizontal converter. The cooled down reactor outlet is then directed to a multistream heat exchanger that causes the condensation of the Ammonia (recovery). Residual gases are recycled to the compressor, before being fed into the Ammonia synthesis reactor.</p>
ICC - Short Description: This study approaches the economics of Ammonia manufacturing from natural gas in the United States. This report assumes a novel plant configuration reported in the literature, in which three chemical looping reactors, respectively fed by natural gas, steam and air are used. The outlet from the looping reactors is passed through compression and water separation steps to generate pure streams of nitrogen, hydrogen and carbon dioxide. Nitrogen and hydrogen react to generate Ammonia.
ICC - Main Product: Ammonia
ICC - Plant Capacity: 800.00
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Ammonia Production from Natural Gas (Chemical Looping Process)

Ammonia Production Costs Report | Issue C | Q4 2024

Production Cost Report

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800 kta United States-based plant   |   Q4 2024   |   107 pages

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

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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 Ammonia 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 Ammonia 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 Ammonia 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 Ammonia 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 Ammonia 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   |   Q4 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   |   Q4 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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Other Related 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   |   Q4 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.

DL-Methionine Production from Acrolein, Methyl Mercaptan and HCN

This report presents the economics of DL-Methionine production from acrolein, methyl mercaptan, and hydrogen cyanide (HCN) in the United States. In this process, refined acrolein and methyl mercaptan are reacted to form MMP (also called methional), which is further reacted with HCN to generate DL-Methionine via a typical carbonate process.

Details: 150 kta United States-based plant   |   Q4 2024   |   107 pages   |   Issue D   From $1,199 USD

The cost analyses presented in this report target a 150 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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