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This report presents a feasibility analysis of Diesel production from carbon dioxide in the United States using a three-step process. Initially, algae are cultivated to produce lipids in a step similar to Simgae. These oils are then extracted from cells in a process similar to OriginOil Single Step Extraction. The triglycerides are catalytically hydrotreated to n-alkanes that meet diesel specifications.
This study provides a techno-economic analysis of Renewable Diesel production from algae in the United States. In this process, lipids extracted from the algal biomass are hydrotreated to Diesel.
The report analyzed is a techno-economic analysis of Renewable Diesel production from soybean oil in the United States using a typical hydroprocessing process. Hydrogen used for this reaction is not generated on-site, being purchased in the market. In this case, naphtha is generated as by-product.
This report presents a techno-economic analysis of Renewable Diesel production from soybean oil in the United States. The process employed is a hydroprocessing similar Neste Oil NExBTL. In this case, propane is generated as by-product.
This report presents a techno-economic analysis of Renewable Diesel production from soybean oil in the United States using a typical hydroprocessing process presenting an integrated hydrogen production plant from natural gas.
This report approaches an economic analysis of Renewable Diesel production from corn stover in the United States. In this process, corn stover is pretreated and its components are hydrolyzed, being then bioconverted to free fatty acids (FFA). The FFAs are then hydrotreated to paraffinic compounds forming the Diesel product.
This report provides a techno-economic analysis of Renewable Diesel production from corn stover in the United States using a catalytic conversion process. In this process, corn stover is pretreated and its components are hydrolyzed. The hydrolysate is hydrogenated, reformed in aqueous phase, condensed, oligomerized and finally hydrotreated, yielding diesel.
This report provides a techno-economic analysis of Diesel production from wood chips in the United States. This study evaluates a fast pyrolysis process followed by a hydroprocessing step using woody biomass as raw material.
This report approaches the economics of Fischer-Tropsch (FT) Diesel production from wood chips via syngas in the United States. This process consists of two steps: a gasification step similar to Linde Carbo-V Technology to produce syngas and a Fischer-Tropsch synthesis step similar to Shell GTL process.
This report provides a techno-economic analysis of Ultra-Low Sulfur Diesel (ULSD) production via a hydrotreating process in the United States. In this process, a high-sulfur diesel feed is passed through a fixed-bed catalytic reactor, where sulfur and nitrogen impurities are reacted with hydrogen and converted into hydrogen sulfide and ammonia. The reactor effluent is then subjected to a sequence of separation steps, so that Ultra-Low Sulfur Diesel (10 ppm sulfur) is obtained as the final product.
This report presents a techno-economic analysis of Ultra-Low Sulfur Diesel (ULSD) production via the sulfur removal of a low-sulfur diesel feed by means of a reactive adsorption process similar the S Zorb technology (originally developed by ConocoPhillips). The economic analysis performed assumes a plant located in the United States.
This report approaches an economic analysis for Very-Low Sulfur Diesel (VLSD) production via a hydrotreating process in the United States. In this process, a high-sulfur diesel feed is passed through a fixed-bed catalytic reactor, where sulfur and nitrogen impurities are reacted with hydrogen and converted into hydrogen sulfide and ammonia. The reactor effluent is then subjected to a sequence of separation steps, so that Very-Low Sulfur Diesel (50 ppm sulfur) is obtained as the final product.