Dimethyl Carbonate Production Process - Cost Analysis - DMC E11A

Dimethyl Carbonate Production Process - Cost Analysis - DMC E11A
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Publisher : Intratec Solutions
Total Pages : 101
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Synopsis Dimethyl Carbonate Production Process - Cost Analysis - DMC E11A by : Intratec

This report presents a cost analysis of Dimethyl Carbonate (DMC) production from methanol. The process examined is a typical oxidative carbonylation process. This process is a non-phosgene alternative for DMC production, in which CO, O2 and methanol react in the presence of copper chloride (CuCI) catalyst. Although reaction occurs in the liquid phase, a heterogeneous-phase mixture forms and the product stream is withdrawn from the reactor in vapor phase. The vapor is partially condensed, treated for recovery of catalyst and then subjected to distillation operations. Unreacted methanol is recovered and recycled to the reactor. Purified Dimethyl Carbonate is obtained after separation of side-product water. This report was developed based essentially on the following reference(s): (1) US Patent 20030236428, issued to General Electric Company (2) US Patent 5685957, issued to Enichem Synthesis in 1997 Keywords: Non-Phosgene Process, Phosgene-Free, Oxidative Carbonylation, Enichem, Eni

Dimethyl Carbonate Production Process - Cost Analysis - DMC E11A

Dimethyl Carbonate Production Process - Cost Analysis - DMC E11A
Author :
Publisher : Intratec
Total Pages : 101
Release :
ISBN-10 : 9781641480925
ISBN-13 : 1641480920
Rating : 4/5 (25 Downloads)

Synopsis Dimethyl Carbonate Production Process - Cost Analysis - DMC E11A by : Intratec

This report presents a cost analysis of Dimethyl Carbonate (DMC) production from methanol The process examined is a typical oxidative carbonylation process. This process is a non-phosgene alternative for DMC production, in which CO, O2 and methanol react in the presence of copper chloride (CuCI) catalyst. Although reaction occurs in the liquid phase, a heterogeneous-phase mixture forms and the product stream is withdrawn from the reactor in vapor phase. The vapor is partially condensed, treated for recovery of catalyst and then subjected to distillation operations. Unreacted methanol is recovered and recycled to the reactor. Purified Dimethyl Carbonate is obtained after separation of side-product water. This report was developed based essentially on the following reference(s): (1) US Patent 20030236428, issued to General Electric Company (2) US Patent 5685957, issued to Enichem Synthesis in 1997 Keywords: Non-Phosgene Process, Phosgene-Free, Oxidative Carbonylation, Enichem, Eni

Ziram Production Process - Cost Analysis - Ziram E11A

Ziram Production Process - Cost Analysis - Ziram E11A
Author :
Publisher : Intratec
Total Pages : 102
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ISBN-10 :
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Rating : 4/5 ( Downloads)

Synopsis Ziram Production Process - Cost Analysis - Ziram E11A by : Intratec

This report presents a cost analysis of Ziram production from dimethylamine, carbon disulfide, sodium hydroxide, and zinc sulfate. In the process, dimethyl amine reacts with carbon disulfide. The product is mixed with sodium hydroxide, producing a sodium salt which is oxidized by the addition of zinc sulfate, producing Thiram. This report was developed based essentially on the following reference(s): Keywords: Zinc Dimethyldithiocarbamate, Dimethyldithiocarbamic Acid Zinc Salt

Polyoxymethylene Production Process - Cost Analysis - POM E11A

Polyoxymethylene Production Process - Cost Analysis - POM E11A
Author :
Publisher : Intratec
Total Pages : 102
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ISBN-10 :
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Rating : 4/5 ( Downloads)

Synopsis Polyoxymethylene Production Process - Cost Analysis - POM E11A by : Intratec

This report presents a cost analysis of Polyacetal Resins (also known as Polyoxymethylene, POM) production from acetic anhydride and formaldehyde. The process examined is similar to the one owned by DuPont. In this process, starting formaldehyde (37wt% solution) is concentrated to a purity higher than 99.9wt% by means of two distillation steps and a treatment step. High purity formaldehyde is then polymerized in an inert cyclohexane medium. This report was developed based essentially on the following reference(s): (1) "Acetal Resins", Kirk-Othmer Encyclopedia of Chemical Technology, 5th edition (2) US Patent 2768994, issued to Du Pont in 1956 Keywords: Acetyl resin, polyoxymethylene (POM) resins, polymer of formaldehyde, DuPont, polyformaldehyde

Ethylene Vinyl Acetate Production Process - Cost Analysis - EVA E11A

Ethylene Vinyl Acetate Production Process - Cost Analysis - EVA E11A
Author :
Publisher : Intratec Solutions
Total Pages : 101
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ISBN-10 :
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Rating : 4/5 ( Downloads)

Synopsis Ethylene Vinyl Acetate Production Process - Cost Analysis - EVA E11A by : Intratec

This report presents a cost analysis of Ethylene Vinyl Acetate (EVA) production from ethylene and vinyl acetate. The process examined is a typical high-pressure tubular polymerization processes. The final product obtained is Ethylene Vinyl Acetate (EVA) copolymer with a vinyl acetate content of 20 wt%. This report was developed based essentially on the following reference(s): (1) US Patent 6899852, issued to ExxonMobil in 2005 (2) US Patent 20130333832, issued to LyondellBasell in 2013 Keywords: Ethene, EVA, BASF, Tubular Reactor, ExxonMobil, LyondellBasell, Lupotech

Barium Chloride Production Process - Cost Analysis - Barium Chloride E11A

Barium Chloride Production Process - Cost Analysis - Barium Chloride E11A
Author :
Publisher : Intratec
Total Pages : 102
Release :
ISBN-10 :
ISBN-13 :
Rating : 4/5 ( Downloads)

Synopsis Barium Chloride Production Process - Cost Analysis - Barium Chloride E11A by : Intratec

This report presents a cost analysis of a typical Barium Chloride production process from baryte, calcium chloride, and coke. In the process, calcium chloride is heated with barytes and coke. The Barium Chloride formed is leached out from the mixture with water. This report was developed based essentially on the following reference(s): Keywords: Barium Muriate, Barium Dichloride

Methyl Ester Sulfonate Production Process - Cost Analysis - MES E11A

Methyl Ester Sulfonate Production Process - Cost Analysis - MES E11A
Author :
Publisher : Intratec Solutions
Total Pages : 102
Release :
ISBN-10 :
ISBN-13 :
Rating : 4/5 ( Downloads)

Synopsis Methyl Ester Sulfonate Production Process - Cost Analysis - MES E11A by : Intratec

This report presents a cost analysis of Methyl Ester Sulfonate (MES) production from palm oil. The process examined consists of two steps: a transesterification step similar to Lurgi Transesterification process and a sulfonation step similar to Chemithon process. In this process, palm oil and methanol are reacted forming methyl ester, which is then sulfonated to Methyl Ester Sulfonate. This report was developed based essentially on the following reference(s): (1) US Patent 8288574, issued to Lurgi in 2012 (2) Handbook of Detergents, Part F: Production Keywords: Methyl Alcohol, Sulfur Burning, Air/SO3 Sulfonation

Technical Grade Glycerol Production Process - Cost Analysis - Glycerol E11A

Technical Grade Glycerol Production Process - Cost Analysis - Glycerol E11A
Author :
Publisher : Intratec
Total Pages : 102
Release :
ISBN-10 :
ISBN-13 :
Rating : 4/5 ( Downloads)

Synopsis Technical Grade Glycerol Production Process - Cost Analysis - Glycerol E11A by : Intratec

This report presents a cost analysis of Technical Grade Glycerol production via fuel grade glycerol treatment. The process examined is a typical pre-treatment process. This report was developed based essentially on the following reference(s): Keywords: Glycerin, Industrial Grade Glycerol, Lurgi

Methyl Chloride Production Process - Cost Analysis - Methyl Chloride E11A

Methyl Chloride Production Process - Cost Analysis - Methyl Chloride E11A
Author :
Publisher : Intratec
Total Pages : 103
Release :
ISBN-10 : 9781641481182
ISBN-13 : 1641481188
Rating : 4/5 (82 Downloads)

Synopsis Methyl Chloride Production Process - Cost Analysis - Methyl Chloride E11A by : Intratec

This report presents a cost analysis of Methyl Chloride production from methanol and hydrogen chloride The process examined is a typical catalytic vapor phase process. In this process, 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. This report was developed based essentially on the following reference(s): (1) "Chloromethanes", Ullmann's Encyclopedia of Industrial Chemistry, 2012; (2) Handbook of Industrial Chemistry and Biotechnology, 2012 Keywords: Chloromethane, R-40, HCC-40, chlorosilanes production

CO2 Sequestration and Valorization

CO2 Sequestration and Valorization
Author :
Publisher : BoD – Books on Demand
Total Pages : 474
Release :
ISBN-10 : 9789535112259
ISBN-13 : 9535112252
Rating : 4/5 (59 Downloads)

Synopsis CO2 Sequestration and Valorization by : Claudia R. V. Morgado

The reconciliation of economic development, social justice and reduction of greenhouse gas emissions is one of the biggest political challenges of the moment. Strategies for mitigating CO2 emissions on a large scale using sequestration, storage and carbon technologies are priorities on the agendas of research centres and governments. Research on carbon sequestration is the path to solving major sustainability problems of this century a complex issue that requires a scientific approach and multidisciplinary and interdisciplinary technology, plus a collaborative policy among nations. Thus, this challenge makes this book an important source of information for researchers, policymakers and anyone with an inquiring mind on this subject.