Sodium Lauryl Ether Sulfate Production
Sodium Lauryl Ether Sulfate Production Costs Report | Issue A | Q2 2024
Report Details |
15 kta United States-based plant | Q2 2024 | 107 pages | Delivered in PDF |
This report presents a cost analysis of a 15 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 Sodium Lauryl Ether Sulfate (SLES) production from chlorosulfonic acid, lauryl ethoxylate, and sodium hydroxide in the United States. In the process examined, lauryl ethoxylate reacts with chlorosulfonic acid (sulfation). The product is neutralized with sodium hydroxide, producing the surfactant.
The report provides a comprehensive study of Sodium Lauryl Ether Sulfate production and related Sodium Lauryl Ether Sulfate production cost, covering three key aspects: a complete description of the Sodium Lauryl Ether Sulfate production process examined; an in-depth analysis of the related Sodium Lauryl Ether Sulfate plant capital cost (Capex); and an evaluation of the respective Sodium Lauryl Ether Sulfate plant operating costs (Opex).
The Sodium Lauryl Ether Sulfate 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 Lauryl Ether Sulfate 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 Lauryl Ether Sulfate 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 four major sections: (1) Sulfation; (2) Neutralization; (3) Scrubbing; and (4) Packing.
Sulfation. Initially, the lauryl ethoxylate is batch sulfated by cholorosulfonic acid. Both reagents are fed to a glass-lined stirred, jacketed reactor, with the acid being gradually added to the reaction. The sulfation is carried out at 25 - 30°C under vacuum, over about a period of 2.5 hours. The gaseous HCl by-product is led off the sulfation product, and directed to a scrubber downstream. The sulfation product is fed to the neutralization.
Neutralization. The sulfation product is fed to a neutralization vessel, where it is contacted with a 50 wt% caustic soda solution along with process water for adjusting its active component. The neutralization reaction is carried out at a temperature below 45 °C, generating a 70 wt% sodium lauryl ether sulfate further routed to packaging.
Scrubbing. The HCl evolved during the sulfation is fed to a scrubber, where it is absorbed in process water generating a 33 wt% hydrochloric acid solution by-product.
Packing. SLES is packed in drums and then sent to warehouses at the facility’s outside battery limits (OSBL) to be stored.
Up-to-date PDF Report
Professional report based on Q2 2024 economic data, ensuring timely evaluations.
Multiple Use Cases
Ideal for investment screening, feasibility studies, cost estimates, and research planning.
Proven Methodology
Developed using a consistent methodology honed over a decade, ensuring reliable cost analyses.
Compact
$799 USD
Production Process Information
Process Consumptions
Labor Requirements
Plant Capital Cost Summary
Operating Cost Summary
Production Costs Datasheet
Pages | Tables | Images
Read-only Online PDF Format
Updated with Q2 2024 Data
DETAILED
$1,599 USD
Production Process Information
Process Consumptions
Labor Requirements
Plant Capital Cost Summary
Operating Cost Summary
Production Costs Datasheet
Plant Capital Cost Details
Operating Cost Details
Pages | Tables | Images
Downloadable PDF Format
Updated with Q2 2024 Data
PREMIUM
MOST POPULAR
$2,699 USD
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
Pages | Tables | Images
Print-enabled PDF Format Add-on
Updated with Q2 2024 Data
Share with Co-workers
Technical Support via Email
Content Highlights
Plant Capital Cost Summary
Summary outlining the capital cost required for building the Sodium Lauryl Ether Sulfate 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 Lauryl Ether Sulfate 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 Lauryl Ether Sulfate 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 Lauryl Ether Sulfate 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
Could Not Find the Report You Need?
Obtain a Bespoke Report
Get a report targeting the process in which you are interested
See Offer Details
Understand Bespoke Reports and how you can easily order them
Check Editions & Pricing
Complete a brief form and see a quotation for your Bespoke Report
Other Related Production Cost Reports
Sodium Hydroxide Production from Sodium Chloride (Membrane Process)
This report presents the economics of Sodium Hydroxide production from sodium chloride in the United States, via a typical membrane process. In this process, sodium chloride is decomposed electrolytically, producing sodium hydroxide. Chlorine and hydrogen are generated as by-products in the process.
Details: 550 kta United States-based plant | Q2 2024 | 107 pages | Issue A From $799 USD
The cost analyses presented in this report target a 550 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.
Sodium Hydroxide Production from Sodium Chloride (Diaphragm Process)
It presents the economics of Sodium Hydroxide production from brine in the United States. The process examined in this report is a typical diaphragm process. Chlorine and hydrogen are also generated as by-products in the process.
Details: 600 kta United States-based plant | Q2 2024 | 107 pages | Issue B From $799 USD
The cost analyses presented in this report target a 600 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.
+800 Reports Developed, Targeting +250 Commodities
Best-in-Class Reports
Analysis of capital and operating costs of commodity production processes. Prices starting at $799 USD
Vast Report Library
858 independent and up-to-date reports examining embryonic and established production processes
Free Sample Reports
Quickly understand the structure and depth of content of our professional reports