Commodity Production Costs Report
Ammonia Production from Coal
Ammonia Operating Costs & Plant Construction Costs
This report examines the costs related to Ammonia production from coal in China. In this process, coal undergoes pyrolysis, producing coke. It is then subjected to a gasification process. Coke reacts with steam and oxygen yielding mainly carbon monoxide (CO), hydrogen and carbon dioxide (CO2). CO and water are shifted to CO2 and hydrogen. Finally, nitrogen and hydrogen react to produce ammonia.
The report provides a comprehensive study of Ammonia production and related Ammonia production cost, covering three key aspects: a complete description of the Ammonia production process examined; an in-depth analysis of the related Ammonia plant capital cost (Capex); and an evaluation of the respective Ammonia plant operating costs (Opex).
The Ammonia production process description includes a block flow diagram (BFD), an overview of the industrial site installations, detailing both the process unit and the necessary infrastructure, process consumption figures and comprehensive process flow diagrams (PFD). The Ammonia plant capital cost analysis breaks down the Capex by plant cost (i.e., ISBL, OSBL and Contingency); owner's cost; working capital; and costs incurred during industrial plant commissioning and start-up. The Ammonia plant operating costs analysis covers operating expenses, including variable costs like raw materials and utilities, and fixed costs such as maintenance, labor, and depreciation.
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The process under analysis comprises three major sections: (1) Coal Gasification; (2) Raw Syngas Purification; and (3) Ammonia Synthesis.
Coal Gasification. Initially, coal and limestone are received from the storage area, prepared, metered, mixed and conveyed to the gasifier. As coal is fed to the gasifier, it dries due to the vaporization of water and undergoes pyrolysis, producing coke. Steam and oxygen are fed to the gasifier and react with the char, producing mainly carbon monoxide and carbon dioxide. The gasification reactions are carried out at high temperatures (700°C) and medium pressures (3 – 4 MPa), with gaseous reaction products ascending countercurrent to the coal introduced in the gasifier.
Raw Syngas Purification. The outlet from the gasification is fed to a two-stage high and low temperature reactors, where the bulk of the carbon monoxide is converted into carbon dioxide and hydrogen. The shifted gas is then cooled through a series of heat exchangers, in such a way that water present in the gas condenses and is removed. Mercury and other contaminants still present in the gas stream are removed by means of a carbon bed adsorption system. The gas stream is sent to the CO2 Absorption for the removal of CO2 and H2S. A Claus plant is used for recovering Sulfur from the stream rich in H2S. The gas stream free from CO2 is heated and fed to the Methanator, where residual carbon oxides are converted to methane in the presence of catalysts.
Ammonia Synthesis. After a nitrogen wash that removes remaining carbon monoxide and methane, the resulting gas is compressed and directed to the Ammonia Reactor, an intercooled horizontal converter, where hydrogen and nitrogen reacts at the correct stoichiometric ratio yielding Ammonia.
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Professional report based on Q3 2024 economic data, ensuring timely evaluations.
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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 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 | Q3 2024 | 107 pages | Issue B | From $1,199 USD

Ammonia Production from Natural Gas (Chemical Looping Process)
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.
Details: 800 kta United States-based plant | Q3 2024 | 107 pages | Issue C | From $1,199 USD

Ammonia Production from Fuel Oil
This report examines the costs related to Ammonia production from heavy fuel oil. The process under analysis integrates a heavy fuel oil partial oxidation process for synthesis gas production with a unit that produces ammonia from hydrogen and nitrogen. The economic analysis provided assumes a plant located in the United States.
Details: 800 kta United States-based plant | Q3 2024 | 107 pages | Issue E | From $1,199 USD
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