Search for a Commodity and Check Solutions Offered
Refine Results
Results 881 - 920 of 1810
This report presents an economic analysis of Polyhydroxybutyrate (PHB) production from sugarcane bagasse. In this process, sugarcane bagasse is gasified to synthesis gas (syngas), which is fermented to PHB. The economic analysis presented is based on a plant constructed in Brazil.
This report presents the Economic analysis of Polyhydroxybutyrate (PHB) production from switchgrass. In this process, switchgrass is gasified to synthesis gas (syngas), which is fermented to PHB. The economic analysis presented is based on a plant constructed in the United States.
This report presents the economics of Polyisoprene production starting from glucose, based on a plant located in the United States. The process comprehends the fermentation of 70 wt% glucose-water syrup into isoprene, followed by solution polymerization step for converting isoprene to Polyisoprene.
This report presents the economics of Polyisoprene production from isoprene in the United States, via a typical solution polymerization process. The Ziegler/Natta catalyst system used in the process yields predominantly cis-1,4 units.
This report presents the economics of Polyisoprene production from starting from raw sugar, based on a plant located in Germany. The process comprehends the hydrolysis of sucrose, the fermentation of the obtained invert sugars into isoprene and a typical solution polymerization process for converting isoprene to Polyisoprene.
This study approaches the economics of Polylactic Acid production from corn in the United States. Initially, shelled corn is passed through a wet milling process to form corn starch, which is hydrolyzed to dextrose. Then, dextrose is fermented into lactic acid in a process similar to Cargill process. Finally, lactic acid is polymerized using a melt-phase polymerization process similar to the one proposed by NatureWorks.
This study approaches the economics of Polylactic Acid production from glucose syrup in the United States. First, lactic acid is produced from glucose syrup using a fermentation process similar to Cargill process. Then, lactic acid is polymerized into poly(lactic acid) using a melt-phase polymerization process similar to the one proposed by NatureWorks.
This report presents the economics of Polylactic Acid (PLA) production from lactic acid using a melt process similar to the one proposed by NatureWorks. In this process, lactic acid is first oligomerized and then depolymerized into lactide, a cyclic dimer of lactic acid, which is then polymerized to yield PLA by ring opening polymerization. The economic analysis presented is based on a plant constructed in the USA.
This report approaches the economics of producing Polylactic Acid (PLA) from lactide in a plant located in the United States. In the process examined, lactide, a cyclic dimer of lactic acid, undergoes a ring opening polymerization in the presence of a stannous octoate catalyst to be converted into Polylactic Acid.
This study approaches the economics of Polylactic Acid production from raw sugar in Germany. Initially, raw sugar is hydrolyzed into invert sugars. The invert sugars are then fermented to produce lactic acid, in a process similar to Cargill process. The lactic acid is oligomerized and then depolymerized into lactide, which is finally polymerized to yield PLA by ring opening polymerization, similar to the one proposed by NatureWorks.
In this report, it is assessed the production of Polyoxymethylene (POM), also called Polyacetal Resin. The economic analysis concerns Polyoxymethylene production from acetic anhydride and formaldehyde in the United States, assuming a process similar to the one owned by Dupont. Formaldehyde is initially concentrated and then polymerized in an inert cyclohexane medium. To enhance thermal stability, hydroxyl end groups are reacted with acetic anhydride.
This report approaches the production of Polyoxymethylene (POM) from methanol and acetic anhydride in the United States. Initially, methanol undergoes partial oxidation yielding formaldehyde over a silver catalyst. Formaldehyde is then polymerized to POM in an inert cyclohexane medium. To enhance thermal stability, hydroxyl end groups are reacted with acetic anhydride.
This report provides the economics of Polypropylene Carbonate (PPC) production from propylene oxide and carbon dioxide in the United States using a process based on patents issued to SK Energy. In this process, the polymerization occurs in full-liquid phase and under pressure.
This report presents the economics of Nonwoven production from polypropylene via spunbond technology. The economic analysis performed assumes a plant located in the United States.
This report presents the economics of Polytrimethylene Terephthalate (PTT) production from terephthalic acid (TPA) and glucose in the United States. The process portrayed in the report combines a process similar to DuPont process for generating propanediol from glucose and a process similar to Degussa (now Evonik) process for producing PTT from propanediol and terephthalic acid.
This report presents the economics of Polytrimethylene Terephthalate (PTT) production from terephthalic acid (TPA) and propanediol via a process similar to Degussa (now Evonik) technology. This process employs a direct esterification of terephthalic acid and 1,3-propanediol to make PTT. The economic assessment assumes a plant located in the United States.
This report presents the economics of Polytrimethylene Terephthalate (PTT) production from terephthalic acid and raw sugar in the United States. The process portrayed in the report combines a process similar to DuPont process for generating propanediol from raw sugar and a process similar to Degussa (now Evonik) process for producing PTT from propanediol and terephthalic acid.
This study presents the economics of Polyvinyl Chloride (PVC) production from vinyl chloride monomer (VCM) in the United States. The process examined is a typical bulk polymerization process.
It presents the economics of Polyvinyl Chloride (PVC) production from vinyl chloride monomer (VCM) in the United States. The process examined is a typical emulsion polymerization process in aqueous medium with emulsifiers.
This report presents the economics of Polyvinyl Chloride (PVC) production from vinyl chloride monomer (VCM) in the United States, via a typical suspension polymerization process. In this process, VCM droplets dispersed in water are polymerized to PVC.
This report presents the economics of Potassium Chlorate production from potassium chloride in the United States. In this process, potassium chloride is electrolyzed for the direct production of potassium chlorate.
This report presents the economics of Potassium Iodide production from potassium hydroxide, iodine, and coke in the United States. In this process, iodine is absorbed in potassium hydroxide, yielding Potassium Iodide. Potassium iodate is also generated as by-product.
It presents the economics of Electricity generation from wood in the USA via a gasification process. In the process examined, wood feedstock is converted to syngas via a gasification step, and the syngas is used as fuel to Electricity generation via a traditional combined-cycle.
In this study Electricity generation from wood is reviewed employing a biomass bubbling fluidized bed (BFB) boiler to burn wood and produce steam to drive a steam turbine. The economic analysis performed assumes a plant located in the USA.
This report approaches Electricity generation from natural gas, using advanced F-class combustion turbine in a simple-cycle mode. The economic analysis is also based on a plant constructed in the USA.
This report presents the economics of Electricity generation from coal in the USA using an advanced pulverization coal (APC) process. In the process under analysis, coal is burned to produce steam in a supercritical pulverized coal (SCPC) boiler.
The process examined in this study is an advanced pulverization coal (APC) process, including a carbon capture and sequestration (CCS) system. The economic assessment also assumes a plant located in the USA.
This report also provides a feasibility study about Electricity generation from natural gas in the USA. The process under analysis employs a conventional E-class combustion turbine (CT).
This report examines the costs related to Polymer Grade (PG) Propylene production from propane in the United States. In this process, polymer grade (PG) propylene is first produced via dehydrogenation of propane using fixed-bed reactors, in a process similar to Lummus CATOFIN. Then propylene is subjected to a gas phase polymerization in vertical stirred-bed reactors to produce polypropylene, in a process similar to Lummus Technology's Novolen.
In this process, propane is first dehydrogenated in fixed-bed reactors, using a process that is similar to Lummus CATOFIN, yielding polymer grade propylene. PG propylene is then polymerized using a bulk phase polymerization process similar to LyondellBasell Spheripol and Mitsui Hypol II. The economic analysis performed assumes a plant located in the United States.
This study presents the economics of Polypropylene production from propane. In this two-step process, first polymer grade (PG) propylene is produced via dehydrogenation of propane, carried out in a moving-bed reactor, similarly to UOP Oleflex. PG propylene is then polymerized using a bulk phase polymerization process similar to LyondellBasell Spheripol. The economic analysis performed assumes a plant located in the United States.
This study presents the economics of Polypropylene (PP) Homopolymer production from propane. In this two-step process, first polymer grade (PG) propylene is produced via dehydrogenation of propane, carried out in a moving-bed reactor, similarly to UOP Oleflex. Gaseous PG propylene is then polymerized to PP in fluidized-bed reactors (FBRs), similarly to the Grace UNIPOL process. The economic analysis performed assumes a plant located in the United States.
This study presents the economics of Polypropylene (PP) Homopolymer production from propane. Polymer grade (PG) propylene is first produced via a two-step propane dehydrogenation process (steam reforming/oxyreaction), similarly to the Uhde STAR process. PG propylene is then polymerized using a bulk phase polymerization process similar to LyondellBasell Spheripol. The economic analysis performed assumes a plant located in the United States.
This study presents the economics of Polypropylene (PP) Homopolymer production from PG propylene. The process under analysis uses a hybrid (slurry/gas) polymerization process similar to the Borealis BORSTAR process. The economic analysis assumes a plant constructed in the United States.
This report analyses the economics of Polypropylene (PP) Homopolymer production from polymer grade (PG) propylene in a plant assumed to be located in the United States. In this process, gaseous PG propylene is polymerized in horizontal agitated reactors connected in series. The process examined in this report is similar to INEOS INNOVENE and JPP HORIZONE.
This study presents the economics of Polypropylene (PP) Homopolymer production from polymer grade (PG) propylene in the United States. In this process, gaseous PG propylene is polymerized in vertical stirred-bed reactors. The process examined in this report is similar to Lummus Technology's Novolen.
This report presents the economics of Polypropylene (PP) Homopolymer production from polymer grade (PG) propylene. The process under analysis uses a bulk phase polymerization process similar to LyondellBasell Spheripol and Mitsui Hypol II. The economic analysis performed assumes a plant located in the United States.
This report examines the costs related to Polypropylene (PP) Homopolymer production from polymer grade (PG) propylene, using a gas phase polymerization process similar to LyondellBasell Spherizone. The reaction occurs in a multi-zone circulating reactor (MZCR). The economic analysis performed assumes a plant located in the United States.
This study presents the economics of Polypropylene (PP) Homopolymer production from polymer grade (PG) propylene. The process examined in this report is similar to Grace UNIPOL process. In this process, gaseous propylene is polymerized to PP in fluidized-bed reactors (FBRs). The economic analysis performed assumes a plant located in the United States.
This study presents the economics of Polypropylene (PP) Random Copolymer production from PG propylene and ethylene. The analysis concerns a plant constructed in the United States, using an hybrid (slurry/gas) polymerization process similar to Borealis BORSTAR.