Featured Report: Calcium Hypochlorite from Slaked Lime and Cl2 (Sodium Method)

This report presents an up-to-date, detailed cost analysis of Calcium Hypochlorite production from slaked lime, sodium hydroxide and chlorine. The process examined is a typical sodium process. This process consists mainly in passing chlorine into a slurry of slaked lime and sodium hydroxide, generating Calcium Hypochlorite and sodium chloride. After separation steps, Calcium Hypochlorite (about 70 wt%) and an aqueous solution of sodium chloride are obtained as products.

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Featured Report: Carbon Monoxide Production

This report presents an up-to-date, detailed cost analysis of Carbon Monoxide (CO) production from synthesis gas. The process examined is a typical cryogenic partial condensation process. In this analysis, CO and hydrogen from syngas are separated in heat exchangers at cryogenic temperatures.

You can check now more information about this report and also search in the library available at Intratec website (www.intratec.us) for reports focused on other industrial products.  Our Production Cost Reports provide up-to-date analysis of capital and operating costs.

Featured Report: Propylene Production from Ethylene

This report presents an up-to-date, detailed cost analysis of Polymer Grade (PG) Propylene production from ethylene using two integrated processes: dimerization and metathesis. The processes examined are similar to Lummus technologies: Ethylene Dimerization Technology and Olefins Conversion Technology (OCT). In these processes, ethylene is first dimerized into butenes, and then, Propylene is produced through a metathesis reaction of 2-butene and ethylene.

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Featured Report: Acetaldehyde Production from Acetic Acid

This report presents an up-to-date, detailed cost analysis of Acetaldehyde production from acetic acid. The process examined is a hydrogenation process similar to the one proposed by Eastman. In this process, acetic acid is hydrogenated in a fixed-bed reactor, in the presence of an iron oxide/palladium catalyst. The reaction product is passed through an absorber for the separation of hydrogenation products and subsequently distilled for the separation of high-purity Acetaldehyde from reaction by-products. Ethyl acetate is generated as by-product.

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Featured Report: Impact PP from Propylene and Ethylene (UNIPOL)

This report presents an up-to-date, detailed cost analysis of Polypropylene impact copolymer production from propylene and ethylene using a gas phase polymerization process. The process examined is similar to Grace UNIPOL process. This process is based on the polymerization of gaseous polymer grade propylene and ethylene in two fluidized-bed reactors connected in series.

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Featured Report: Acetaldehyde Production from Ethylene (Two-Step Process)

This report presents an up-to-date, detailed cost analysis of Acetaldehyde production from ethylene. The process examined is a typical two-step oxidation process. In this process, ethylene is oxidized by air to Acetaldehyde in tubular reactors, using a palladium/copper catalyst system. Acetaldehyde produced in a first reactor is flashed, so that an Acetaldehyde-water vapor mixture is separated and then distilled, yielding high-purity Acetaldehyde. The catalyst solution from the flash is oxidized in a second reactor and returned to the first reactor. Exhaust gases from both reaction steps are scrubbed for the recovery of residual Acetaldehyde.

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Featured Report: Phosgene Production

This report presents an up-to-date, detailed cost analysis of Phosgene production from chlorine and carbon monoxide. The process examined is a typical industrial process. In this plant, chlorine and carbon dioxide react over activated carbon catalyst, yielding Phosgene product.

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Featured Report: Acetaldehyde Production from Acetic Acid

This report presents an up-to-date, detailed cost analysis of Acetaldehyde production from acetic acid. The process examined is a hydrogenation process similar to the one proposed by Eastman. In this process, acetic acid is hydrogenated in a fixed-bed reactor, in the presence of an iron oxide/palladium catalyst. The reaction product is passed through an absorber for the separation of hydrogenation products and subsequently distilled for the separation of high-purity Acetaldehyde from reaction by-products. Ethyl acetate is generated as by-product.

You can check now more information about this report and also search in the library available at Intratec website (www.intratec.us) for reports focused on other industrial products.  Our Production Cost Reports provide up-to-date analysis of capital and operating costs.

Featured Report: Acetaldehyde Production from Acetylene (Vapor-Phase Hydration)

This report presents an up-to-date, detailed cost analysis of Acetaldehyde production from acetylene. The process examined is a typical vapor phase acetylene hydration over solid catalyst. In this process, steam is generated and mixed with acetylene. The gaseous stream is fed to fixed bed reactors in parallel, where acetylene is hydrated to form acetaldehyde. The excess of water in the reactor product is partially condensed and returned to the reactor. The gaseous stream is transferred to distillation units that recover unreacted acetylene for reuse and generate the purified acetaldehyde product.

You can check now more information about this report and also search in the library available at Intratec website (www.intratec.us) for reports focused on other industrial products.  Our Production Cost Reports provide up-to-date analysis of capital and operating costs.

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