发明名称 Method Of Making Oxygenates From A Non-Catalytic Chemical Reaction
摘要 A system and a method for forming oxygenates from a non-catalytic reaction. A hydrocarbon gas and an oxygen-containing gas are fed into a mixer and then heated to form a reactant gas stream. The reactant gas stream is fed into a fluidized bed reactor where the reaction of the gases occurs by oxidization to produce oxygenates. The oxygenate products are then removed from the reactor.
申请公布号 US2015133703(A1) 申请公布日期 2015.05.14
申请号 US201314399547 申请日期 2013.05.09
申请人 STRANDED SOLUTIONS, LLC 发明人 Pawlak Nathan
分类号 C07C29/50;B01J8/18 主分类号 C07C29/50
代理机构 代理人
主权项 1. A method for making oxygenates using a non-catalytic reaction, said method comprising the steps of: mixing a first stream of hydrocarbon gas with a second stream of gas including oxygen in a mixer; outputting a reactant stream from the mixer including the hydrocarbon gas of the first stream and the second stream of gas including oxygen; heating the reactant stream to a predetermined temperature of at least 300° C. and a pressure of from 40 to 85 atm; inputting the heated reactant stream into a fluidized bed reactor and wherein the fluidized bed reactor includes a reaction chamber with a plurality of inert reactor particles in the reaction chamber; distributing the heated reactant stream into the reaction chamber of the fluidized bed reactor by sending the heated reactant stream through a distributor plate, fluidizing the inert reactor particles in the reaction chamber by feeding the heated reactant stream vertically through the reaction chamber and suspending the inert reactor particles in the reaction chamber of the fluidized bed reactor; oxidizing in the reaction chamber of the fluidized bed reactor the hydrocarbon gas in the heated reactant stream with the gas including oxygen in the heated reactant stream to produce oxygenates comprising at least one of methanol, ethanol and propanol; maintaining the fluidized bed reactor at an isothermal condition of ±10% of a desired operating temperature range of from 300 to 900° C. and a desired operating pressure of 40 to 85 atm to facilitate the production of the oxygenates; and outputting a product stream including the oxygenates, byproducts, and unreacted hydrocarbon gas from the fluidized bed reactor.
地址 Charlevoix MI US