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This report presents a cost analysis of 1,3-Propanediol (PDO) production from raw sugar using a fermentation process. The process examined is similar to DuPont process. In this process, raw sugar (sucrose) is diluted and sucrose is hydrolyzed into glucose and fructose (invert sugars). The invert sugars are then fermented to produce Propanediol. This report was developed based essentially on the following reference(s): (1) US Patent 7745184, issued to DuPont and Genencor in 2010 (2) US Patent 6479716, issued to Archer-Daniels-Midland in 2002 Keywords: Bio-PDO, Trimethylene Glycol, Polytrimethylene Terephthalate, PTT, Aerobic Fermentation, Tate and Lyle
This report presents a cost analysis of 1,3-Propanediol (PDO) production from glucose syrup using a fermentation process. The process examined is similar to DuPont process. In this process, a 70 wt% glucose-water syrup is used as raw material. This report was developed based essentially on the following reference(s): (1) US Patent 7745184, issued to DuPont and Genencor in 2010 (2) US Patent 6479716, issued to Archer-Daniels-Midland in 2002 Keywords: Bio-PDO, Trimethylene Glycol, Polytrimethylene Terephthalate, PTT, Aerobic Fermentation, Tate and Lyle
This report presents a cost analysis of 1,3-Propanediol (PDO) production from crude glycerol using a fermentation process. In this process, crude glycerol obtained as by-product of biodiesel plants, is used as the main raw material. This report was developed based essentially on the following reference(s): Keywords: Bio-PDO, Trimethylene Glycol, Polytrimethylene Terephthalate, PTT, Aerobic Fermentation, Tate and Lyle
The incessantly interest in aqueous polymer dispersions (APD) since more than 90 years can be related to the almost unlimited possibilities to tailor APD to specific needs. These proceedings from an international symposium on "Polymer Colloids: Preparation & Properties of Aqueous Polymer Dispersions" held at the Swabian Conference Center (Kloster Irsee, Germany) witness this statement. The 33 contributions cover important aspects of APD such as control of particle size and stabilization, different polymerization technologies, applications as binders, paints, or as supports for proteins and hence, span the whole range from academic to practical.
This report presents a cost analysis of bio-based Isobutanol production from raw sugar using a typical fermentation process. In this process, raw sugar (sucrose) is diluted and sucrose is hydrolyzed into glucose and fructose (invert sugars). The invert sugars are then fermented to produce Isobutanol. Ethanol is generated as by-product. This report was developed based essentially on the following reference(s): US Patent 8975049, issued to The Regents Of The University Of California in 2015 Keywords: Butyl Alcohol, Biomass, Biofuel
This report presents a cost analysis of Lactic Acid production from raw sugar using a fermentation process. The process examined is similar to Corbion process. In this process, the fermentation broth is acidified in order to recover Lactic Acid and the product purification is realized by the use of a solvent. The process generates an 88 wt% Lactic Acid solution in water as final product. This report was developed based essentially on the following reference(s): (1) EP Patent 1220827, issued to Purac (now Corbion) in 2006 (2) US Patent 6747173, issued to Purac (now Corbion) in 2004 Keywords: Dextrose, 2-Hydroxypropanoic Acid, Anaerobic Fermentation, Calcium Carbonate, Sulfuric Acid
This report presents a cost analysis of bio-based 1,3-Butadiene (BD) production from raw sugar using a fermentation process. The process examined is similar to Global Bioenergies process. In this process, raw sugar (sucrose) is diluted and hydrolyzed into glucose and fructose (invert sugars). The invert sugars are then fed to an anaerobic fermentation step to produce 1,3-Butadiene. This report was developed based essentially on the following reference(s): Keywords: BD, Hydrolysis, Sugar Inversion, Dextrose, Glucose Fermentation, Anaerobic Fermentation, Green Butadiene, Renewable Feedstock
This report presents a cost analysis of 2,5-Furandicarboxylic Acid (FDCA) production from raw sugar (sucrose). The process examined is a non-commercial route based concepts presented on recently published patents and articles. In this process, sucrose is hydrolyzed into glucose and fructose and the glucose obtained is isomerized into fructose. The resulting fructose is dehydrated to hydroxymethylfurfural (HMF) in ionic liquid medium, which is then oxidized to FDCA. This report was developed based essentially on the following reference(s): (1) DE Patent 102008009933, issued to Friedrich-Schiller-Universitat Jena, in 2009 (2) US Patent 20140256964 issued to Eastman in 2014 Keywords: Green FDCA, Hydroxyl Methyl Furan, HMF, ionic liquid
This report presents a cost analysis of bio-based 1,4-Butanediol (BDO) production from raw sugar. The process examined consists of two steps: a fermentation step similar to Korea Advanced Institute of Science & Technology (KAIST) process and a succinic acid hydrogenation step similar to Invista. In this process, raw sugar (sucrose) is hydrolyzed into glucose and fructose (invert sugars). The invert sugars are fermented to produce succinic acid, which is then hydrogenated to produce BDO. This report was developed based essentially on the following reference(s): (1) WO Patent 2009082050, issued to Korea Advanced Institute of Science & Technology (KAIST) in 2009 (2) US Patent 6008384, issued to DuPont in 1999 (assigned to Invista in 2007) Keywords: BDO, Glucose Fermentation, Butanedioic Acid, DuPont
This report presents a cost analysis of bio-based 1,4-Butanediol (BDO) production from raw sugar. The two-step process examined is similar to Myriant/JM Davy process. Raw sugar (sucrose) is diluted and sucrose is hydrolyzed into glucose and fructose (invert sugars). The invert sugars are then fermented to produce succinic acid, the intermediate for BDO production. The process generates ammonium sulfate and tetrahydrofuran (THF) as by-products. This report was developed based essentially on the following reference(s): (1) US Patent 8778656, issued to Myriant in 2014 (2) US Patent 20140350308, issued to Johnson Matthey Davy Technologies in 2014 Keywords: Dextrose, Esterification, Methanol, Hydrogenation, Butanedioic Acid