Featured Report: Vinyl Chloride Production from Ethylene and EDC

This report presents an up-to-date, detailed cost analysis of Vinyl Chloride production from ethylene and ethylene dichloride (EDC). The process examined combines: (1) EDC production from ethylene via oxychlorination, and (2) Vinyl Chloride production via thermal cracking of EDC. In this process, initially EDC is submitted to a thermal cracking, producing VCM and hydrogen chloride (HCl). This HCl is reacted with ethylene via an oxychlorination reaction to generate EDC, that is cracked to additional VCM. The HCl requirement is balanced by purchasing additional EDC from the market.

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Featured Report: Nitrile Rubber Production

This report presents an up-to-date, detailed cost analysis of Nitrile Rubber (solid NBR) production from acrylonitrile and butadiene. The process examined is a typical continuous cold emulsion process for producing NBR. In this process, an emulsion comprising water, acrylonitrile and butadiene monomers is polymerized into a latex, which is then coagulated to form the Nitrile Butadiene Rubber, containing 33 wt% of acrylonitrile.

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Featured Report: 2-Ethylhexyl Acrylate Production

This report presents an up-to-date, detailed cost analysis of 2-Ethylhexyl Acrylate (2-EHA) production from acrylic acid and 2-ethylhexanol. The process examined is similar to the Synthomer process. In this process, acrylic acid and 2-ethylhexanol are directly converted to 2-ethylhexyl acrylate via an esterification reaction catalyzed by p-Toluene Sulfonic Acid.

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Featured Report: Butyraldehyde from Propylene and Syngas (N/Iso Ratio of 30:1)

This report presents an up-to-date, detailed cost analysis of n-Butyraldehyde production from propylene and syngas. The process examined is similar to the LP OXO technology jointly licensed by JM Davy and Dow, employing Selector 30 catalyst. In this process, the production ratio of n- to iso-butyraldehyde in the oxo reaction is about 30. The n-Butyraldehyde is separated as the final product and the isobutyraldehyde is obtained as a by-product.

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Featured Report: Methyl Chloride Production

This report presents an up-to-date, detailed cost analysis of Methyl Chloride production from methanol and hydrogen chloride. The process examined is a typical catalytic vapor phase process. In this plant, methanol and anhydrous HCl are combined in vapor phase and passed through a catalyst bed. Reactor vapor outlet is quenched, dried by sulfuric acid scrubbing and then purified to generate high-purity Methyl Chloride.

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Featured Report: Sodium Chlorate Production

This report presents an up-to-date, detailed cost analysis of Sodium Chlorate production from sodium chloride. The process examined is a typical electrolysis process. In this process, sodium chloride is dissolved in water forming a brine solution, which is purified and subjected to electrolysis. The sodium chlorate product is recovered from the cells liquor through crystallization, centrifugation and drying. The electrolysis also generates hydrogen gas as by-product.

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Featured Report: Polyvinyl Chloride Production from VCM (Suspension Polymerization)

This report presents an up-to-date, detailed cost analysis of Polyvinyl Chloride (PVC) production from vinyl chloride monomer (VCM). The process examined is a typical suspension polymerization process. In this process, VCM droplets dispersed in water are polymerized to PVC.

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Featured Report: Precipitated Silica Production

This report presents an up-to-date, detailed cost analysis of Precipitated Silica production from a sodium silicate solution and sulfuric acid. The process examined is a typical industrial process. In the process, the sodium silicate solution is treated with sulfuric acid. The solution is precipitated, filtered, washed, and dried, producing Precipitated Silica.

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Featured Report: Hydrogen Peroxide Production

This report presents an up-to-date, detailed cost analysis of Hydrogen Peroxide production from hydrogen. The process examined is a conventional anthraquinone auto-oxidation (AO) process. In this process, 2-ethyl anthraquinone is sequentially hydrogenated and oxidized, generating Hydrogen Peroxide.

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Featured Report: Dimethyl Ether Production from Synthesis Gas (Direct Method)

This report presents an up-to-date, detailed cost analysis of Dimethyl Ether (DME) production from synthesis gas through the one-step process. In this process, syngas is contacted with a bifunctional catalyst that supports its conversion to methanol and the subsequent dehydration of methanol to DME - making it possible to obtain DME from syngas in a single reaction step. The presence of water due to the dehydration reaction causes a side reaction that generates carbon dioxide and hydrogen. These side products must also be separated from the crude reaction product.

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