Refining process and apparatus
    1.
    发明授权
    Refining process and apparatus 失效
    精炼工艺和设备

    公开(公告)号:US5679118A

    公开(公告)日:1997-10-21

    申请号:US735931

    申请日:1996-10-23

    CPC classification number: C10G35/04 C10L1/023

    Abstract: A process of producing high octane alcohols includes the steps of preparing a first mixture of substantially ethanol and butane or natural gasoline, the mixture having a certain temperature and a certain pressure, adjusting the certain pressure of the mixture to a magnitude within the range of 10 to 50 pounds per square inch, adjusting the temperature of the mixture to a magnitude within the range of 100 to 350 degrees Fahrenheit, adjusting the pressure of the mixture to a pressure within the range of 500 to 1000 pounds per square inch, catalyzing the mixture with a platinum catalyst, lowering the temperature of the mixture to a magnitude within a range of 90 to 190 degrees Fahrenheit, and separating out liquid product and gas from the mixture. Then a second mixture of said liquid product and methanol is prepared and the process steps are repeated on this second mixture to produce a second product plus gas.

    Abstract translation: 一种制备高辛烷醇的方法包括以下步骤:制备基本上乙醇和丁烷或天然汽油的第一混合物,该混合物具有一定的温度和一定的压力,将混合物的一定压力调节到10的范围内 至50磅/平方英寸,将混合物的温度调节到100至350华氏度的范围内,将混合物的压力调节至500至1000磅/平方英寸范围内的压力,催化该混合物 使用铂催化剂,将混合物的温度降低到90至190华氏度的范围内,并从混合物中分离出液体产物和气体。 然后制备所述液体产物和甲醇的第二混合物,并在该第二混合物上重复该工艺步骤以产生第二产物加气体。

    Refining process and apparatus
    2.
    发明授权
    Refining process and apparatus 失效
    精炼工艺和设备

    公开(公告)号:US5679117A

    公开(公告)日:1997-10-21

    申请号:US734091

    申请日:1996-10-21

    CPC classification number: C10G35/04 C10G35/085 C10L1/023

    Abstract: A process of producing high octane hydrocarbons includes the steps of preparing a mixture of substantially ethanol and butane or natural gasoline, or low octane gasoline, the mixture having room temperature and atmospheric pressure, adjusting the pressure of the mixture to a magnitude within the range of 10 to 50 pounds per square inch, adjusting the temperature of the mixture to a magnitude within the range of 100 to 460 degrees Fahrenheit, adjusting the pressure of the mixture to a pressure within the range of 500 to 1000 hydrocarbons pounds per square inch, catalyzing the mixture with a platinum catalyst, lowering the temperature of the mixture to a magnitude within a range of 90 to 190 degrees Fahrenheit, and separating out liquid product and gas from the mixture. An apparatus for producing high octane alcohols includes a starting tank for retaining a mixture of substantially ethanol and butane or natural gasoline, or low octane gasoline, a heat exchanger for raising the temperature of the mixture, a first high pressure conduit extending from the starting tank to the heat exchanger, a catalyzing chamber, second and third high pressure conduits extending from the heat exchanger to the catalyzing chamber, a nozzle interconnecting the second and third high pressure conduits, high pressure pumps for extracting the heated mixture from the heat exchanger and delivering the mixture to the catalyzing chamber through the second and third high pressure conduits, and a separator for precipitating liquid product out of the mixture.

    Abstract translation: 一种生产高辛烷值烃的方法包括以下步骤:制备基本上乙醇和丁烷或天然汽油或低辛烷值汽油的混合物,该混合物具有室温和大气压力,将混合物的压力调节至在 10至50磅/平方英寸,将混合物的温度调节至100至460华氏度的范围内,将混合物的压力调节至500至1000碳氢化合物磅/平方英寸范围内的压力,催化 与铂催化剂的混合物,将混合物的温度降低到90至190华氏度的范围内,并从混合物中分离出液体产物和气体。 用于生产高辛烷值醇的装置包括用于保持基本上乙醇和丁烷或天然汽油或低辛烷值汽油的混合物的起始罐,用于提高混合物温度的热交换器,从起始罐延伸的第一高压管道 到热交换器,从热交换器延伸到催化室的催化室,第二和第三高压管道,连接第二和第三高压管道的喷嘴,用于从热交换器提取加热的混合物并输送 通过第二和第三高压管道到催化室的混合物,以及用于将液体产物从混合物中沉淀出来的分离器。

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