Production Cost Report
ICC - Is Bespoken: 0
ICC - Main References: ?
ICC - Issue: E
ICC - Volume: 241
ICC - Report ID: 241-E
ICC - Report Location: Brazil
ICC - Is Popular: 0
ICC - Is Developed: 1
ICC - Title: Ethanol and Sugar Production from Sugarcane
ICC - Show Overview: 1
ICC - Report Location ID: 6
ICC - Plant Capacity Unit ID: 14
ICC - Volume Reports List: 241-C,241-F,241-H,241-J,241-M,241-Q,241-S,241-A,241-B,241-D,241-G,241-I,241-K,241-L,241-N,241-O,241-P,241-R,241-T
ICC - Related Reports List: 172-I,172-J
ICC - Report Location Code: BRA
ICC - Delivery Times: {"versions":{"1":{"1":{"time":"9","price":0},"2":{"time":"4","price":"599"}},"2":{"1":{"time":"9","price":0},"2":{"time":"4","price":"599"}},"3":{"1":{"time":"11","price":0},"2":{"time":"6","price":"599"}}},"unit":"d"}
ICC - Prices: {"versions":{"1":{"1":"799","2":"799","3":"799"},"2":{"1":"1599","2":"1599","3":"1599"},"3":{"1":"2699","2":"2699","3":"2699"}},"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/241-E.jpg
ICC - Process Overview Text: <h6>Products</h6> <p><b>Ethanol</b></p>, <p><b>Electricity</b></p>, <p><b>Raw Sugar</b></p> <h6>Raw Materials</h6> <p><b>Chemicals</b></p>, <p><b>Sugarcane</b></p>
ICC - Process Schematic Image: //cdn.intratec.us/images/icc/process-schematics/241-E.jpg
ICC - Process Schematic Text: <p>The process under analysis comprises four major sections: (1) Pretreatment; (2) Sugar Production; (3) Fermentation; and (4) Distillation.</p><p>Pretreatment. The sugarcane is milled to extract its juice. The sugarcane bagasse – solid residue from the milling – is directed to a cogeneration unit, where it is burned for steam and electricity generation. The juice is neutralized with lime in an agitated vessel and sent for clarification in a flocculator and decanter. The resulting clarified juice has a part sent to the evaporation process for raw sugar production, while the other part undergoes the fermentation process for Ethanol production. </p><p>Sugar Production. Treated cane juice is sent to multiple-effect evaporators to adjust the sugar concentration before crystallization. The concentrated cane juice goes through vacuum calandrias, cooling crystallizers, and centrifuges, producing two final streams: raw sugar and molasses. The raw sugar is dried and then stored in a warehouse, while molasses is filtered and sent as a substrate for fermentation process aimed at Ethanol production. </p><p>Fermentation. The molasses and treated cane juice are directed to the parallel batch fermenters, where the sugar will be fermented to produce Ethanol by adding yeast in a controlled temperature. The gases obtained in fermenters, mainly containing carbon dioxide, are sent to a scrubber to recover Ethanol. To separate the yeast biomass from the broth, centrifuges are used, and the recovered yeast returns to the fermenters after an acid treatment.</p><p>Distillation. At the end of fermentation, the concentration of Ethanol in the wine is about 10 vol%. To achieve the desired 93 wt% Ethanol, the wine passes through a concentration column, where most of water is separated by the bottom. An Ethanol/water mixture is withdrawn as a side stream. The Ethanol stream is then conducted to a rectifying column where Hydrous Ethanol (93 wt%) is obtained as distillate.</p>
ICC - Short Description: This report presents a techno-economic study of hydrous Ethanol and raw sugar production from sugarcane using a typical process in Brazil. In this process, part of the sugarcane juice is used in the production of raw sugar and part is fermented to produce hydrous Ethanol. The sugarcane bagasse is burned for electricity generation.
ICC - Main Product: Ethanol
ICC - Plant Capacity: 150.00
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Ethanol and Sugar Production from Sugarcane

Ethanol Production Costs Report | Issue E | Q4 2024

Production Cost Report

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150 kta Brazil-based plant   |   Q4 2024   |   107 pages

This report presents a cost analysis of a 150 kta (kilo metric ton per annum) Brazil-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

Process Consumptions

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Plant Capital Cost Summary

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Production Costs Datasheet

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Production Process Information

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Production Costs Datasheet

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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

Costs in Different Countries Add-on

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Content Highlights

Plant Capital Cost Summary

Summary outlining the capital cost required for building the Ethanol 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 Ethanol 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 Ethanol 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 Ethanol 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 Ethanol Production Cost Reports

Ethanol from Sugarcane Bagasse (Hemicelluloses Extraction)

This feasibility study provides the economic analysis of second generation Ethanol production from sugarcane bagasse in Brazil. The process examined is similar to GreenPower, also developed by American Process. In this process, only hemicelluloses are extracted from biomass and are used to produce hydrous Ethanol via fermentation of monomer sugars.

Details: 80 kta Brazil-based plant   |   Q4 2024   |   107 pages   |   Issue M   From $799 USD

The cost analyses presented in this report target a 80 kta (kilo metric ton per annum per annum) Brazil-based plant. For those interested in cost analyses considering other plant capacities and/or locations, Intratec offers a customized analysis as an optional feature.

Ethanol from Switchgrass (Digestion with SO2-Ethanol-Water Solution)

This feasibility study provides an economic analysis of Ethanol production from switchgrass in the United States using a biochemical conversion process similar to AVAP technology, developed by American Process. In this process, biomass is fractionated into cellulose, hemicelluloses and lignin by using a sulfur dioxide-ethanol-water solution. The cellulose and hemicelluloses obtained from biomass are converted to monomeric sugars, which are then used to produce Ethanol via fermentation.

Details: 200 kta United States-based plant   |   Q4 2024   |   107 pages   |   Issue O   From $799 USD

The cost analyses presented in this report target a 200 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

Ethylene from Ethanol (Similar to Hummingbird Process)

This study presents a techno-economic analysis of Green PG Ethylene production from hydrous ethanol in the United States using a dehydration process similar to the TechnipFMC’s Hummingbird process (former BP Chemicals). The reaction is carried out in multiple stage reactors with inter stage heaters in vapor phase.

Details: 210 kta United States-based plant   |   Q4 2024   |   107 pages   |   Issue I   From $799 USD

The cost analyses presented in this report target a 210 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.

Ethylene from Ethanol (Similar to Chematur Process)

This report provides the economics of Green Polymer Grade (PG) Ethylene production from hydrous ethanol in the United States using a dehydration process examined in this report is similar to the processes developed by Chematur and Petron. In this process, the reaction is carried out multiple reactors in series and a single furnace.

Details: 300 kta United States-based plant   |   Q4 2024   |   107 pages   |   Issue J   From $799 USD

The cost analyses presented in this report target a 300 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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