Sulfuric Acid from Spent Acid (Double-Contact Process)
Sulfuric Acid Production Costs Report | Issue E | Q4 2024
Report Details |
150 kta United States-based plant | Q4 2024 | 107 pages |
This report presents a cost analysis of a 150 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.
Report Abstract
This report presents the economics of spent sulfuric acid regeneration via double-contact double absorption process. The spent acid is first decomposed in a furnace to sulfur dioxide, which is oxidized to sulfur trioxide. Finally, it is fed to the absorption process for producing sulfuric acid. The economic analysis performed is based on a plant constructed in the United States.
The report provides a comprehensive study of Sulfuric Acid production and related Sulfuric Acid production cost, covering three key aspects: a complete description of the Sulfuric Acid production process examined; an in-depth analysis of the related Sulfuric Acid plant capital cost (Capex); and an evaluation of the respective Sulfuric Acid plant operating costs (Opex).
The Sulfuric Acid 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 Sulfuric Acid 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 Sulfuric Acid plant operating costs analysis covers operating expenses, including variable costs like raw materials and utilities, and fixed costs such as maintenance, labor, and depreciation.
Process Schematic

The process under analysis comprises two major sections: (1) Spent Acid Decomposition; and (2) Sulfur Trioxide Formation and Absorption.
Spent Acid Decomposition. Spent acid is fed into a furnace. Fuel and hot air are also fed to it to provide heat. The temperature is controlled near 1,000 °C, causing the acid to evaporate and decompose into sulfur dioxide (SO2), water and hydrogen. The product gas is cooled in a waste heat boiler, and by using the gas to preheat the air fed to the furnace. The cooled gas, at about 300 °C, is then routed to the Scrubber downstream. The steam formed in the boiler is fed to a turbine generator set for power generation.
Sulfur Trioxide Formation and Absorption. The gas stream is treated to remove impurities particles and water, and is passed through a wet gas scrubber, an acid cooling tower, and electrostatic precipitators. It is then directed to a drying column to remove remaining water and avoid sulfuric acid mists formation, which is highly corrosive. Finally, the gas is fed to SO2 converter, comprised of five vanadium pentoxide catalyst beds. The sulfur trioxide (SO3) formed in the first three beds of the SO2 converter is absorbed in the intermediate absorber with concentrated sulfuric acid, where it reacts with water forming more sulfuric acid. The remaining SO2 is sent to the last two beds, and the outlet stream of the fifth bed is sent to a final absorption step, generating more sulfuric acid.
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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 Sulfuric Acid 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 Sulfuric Acid 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 Sulfuric Acid 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 Sulfuric Acid 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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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.
Details: 150 kta United States-based plant | Q4 2024 | 107 pages | Issue F From $999 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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The cost analyses presented in this report target a 100 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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