Commodity Production Costs Report
Sodium Polyacrylate Production
Sodium Polyacrylate Operating Costs & Plant Construction Costs
It presents the economics of Sodium Polyacrylate production from glacial acrylic acid and sodium hydroxide in the United States. In this process, acrylic acid is partially neutralized by sodium hydroxide, yielding a solution of sodium acrylate monomers, which is subsequently polymerized to Sodium Polyacrylate via copolymerization of acrylic acid and its salts.
The report provides a comprehensive study of Sodium Polyacrylate production and related Sodium Polyacrylate production cost, covering three key aspects: a complete description of the Sodium Polyacrylate production process examined; an in-depth analysis of the related Sodium Polyacrylate plant capital cost (Capex); and an evaluation of the respective Sodium Polyacrylate plant operating costs (Opex).
The Sodium Polyacrylate 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 Sodium Polyacrylate 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 Sodium Polyacrylate 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) Polymerization; (2) Particles size Reduction; and (3) Surface Cross-Linking and Packaging.
Polymerization. Acrylic acid is neutralized by a sodium hydroxide solution, resulting in a solution of sodium acrylate monomer. This solution is sent to another area, where it is continuously mixed with additional acrylic acid, a mix of chemicals that serves as polymerization initiator, and trimethylolpropane triacrylate, used as cross-linking agent. Such feed stream is then pumped onto a continuous, moving belt reactor, where the polymerization occurs, yielding a Sodium Polyacrylate gel.
Particles size reduction. The gel is passed through an extrusion unit, where the gel particles diameter is reduced to a range of 0.5–3 cm, in a way to increase the surface area and speed the drying step carried out in a circulating belt dryer, in which the gel water content is reduced to 5 – 10 wt.%. Residual acrylic acid and unreacted monomer also evaporate together with the water. The dried product is ground and classified. The particles are passed through an attrition mill and through roll crushers, yielding particles with grain size between 0.15 and 0.8 mm, which are then sieved with vibrating screens: overflow particles are returned to milling, while fines are partly recycled to the monomer solution, with the remainder sent to surface cross-linking.
Surface Cross-Linking and Packaging. Initially, a surface-crosslinking agent solution composed of 1,4-butanediol / propylene glycol / water / isopropanol is sprayed onto the dried polymer particles, in a vertical mixer. The coated polymer particles are then routed to a disk dryer, where they are dried thermally at 150 to 200° C for the surface cross-linking reaction occur. Afterwards, the Sodium Polyacrylate particles are packed and stored.
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Content Highlights
Plant Capital Cost Summary
Summary outlining the capital cost required for building the Sodium Polyacrylate 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 Sodium Polyacrylate 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 Sodium Polyacrylate 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 Sodium Polyacrylate 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 Sodium Polyacrylate Production Cost Reports

Starch-Graft Sodium Polyacrylate Production
This report analyses the economics of Starch-Graft Sodium Polyacrylate production from corn and glacial acrylic acid in the United States. In this process, acrylic acid is grafted into corn starch forming a polyacrylate, which is then saponificated with sodium hydroxide.
Details: 70 kta United States-based plant | Q3 2024 | 107 pages | Issue A | From $799 USD
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