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    • 3. 发明授权
    • Process for the preparation of hydrocarbons
    • 烃类制备方法
    • US5286455A
    • 1994-02-15
    • US995120
    • 1992-12-22
    • Jacobus EilersSytze A. PosthumaPieter J. Hoek
    • Jacobus EilersSytze A. PosthumaPieter J. Hoek
    • B01J8/06C10G2/00G05D7/00B01S8/06
    • C10G2/34B01J8/06
    • Hydrocarbons are prepared from a feed gas of hydrogen and carbon monoxide by feeding the feed gas into a reaction zone at an elevated temperature and pressure and allowing the hydrogen and carbon monoxide to react in the presence of a catalyst retained in the reaction zone to yield hydrocarbons. A reservoir of a hydrogen-rich gas is maintained at a pressure above the pressure of the feed gas, the reservoir and the reaction zone being connected in such a way that a continuous flow of hydrogen-rich gas is maintained from the reservoir into the reaction zone. A reactor in use in the preparation is shutdown by interrupting the feeding of the feed gas, thereby allowing hydrogen-rich gas to flow from the reservoir at increased rate and quench the reactions occurring in the reaction zone.
    • 通过将氢气和一氧化碳的进料气体通过将进料气体在升高的温度和压力下进料到反应区中并使氢气和一氧化碳在保留在反应区中的催化剂存在下反应以产生烃,从而制备碳氢化合物 。 富氢气体的储存器保持在高于进料气体压力的压力下,储存器和反应区域以这样的方式连接,使得从储存器保持连续的富氢气体流进入反应 区。 在制备中使用的反应器通过中断进料气体的进料来关闭,从而使富氢气体以增加的速率从储存器流出并淬灭在反应区域中发生的反应。
    • 4. 发明申请
    • PROCESS TO PREPARE A FISCHER-TROPSCH SYNTHESIS PRODUCT
    • 制备FISCHER-TROPSCH SYNTHESIS产品的方法
    • US20070213414A1
    • 2007-09-13
    • US11682351
    • 2007-03-06
    • Jacobus EilersRobert Schouwenaar
    • Jacobus EilersRobert Schouwenaar
    • C07C27/06
    • C10G2/00C01B3/36C01B3/382C01B3/52C01B2203/0216C01B2203/0255C01B2203/0415C01B2203/0485C01B2203/062C01B2203/0827C01B2203/1241C01B2203/142C01B2203/148C01B2203/1614C01B2203/169C10G2300/1022C10G2300/4081C10G2400/06
    • The invention provides a process to prepare a Fischer-Tropsch synthesis product from a gaseous mixture of hydrocarbons comprising methane, ethane and optional higher carbon number hydrocarbons comprising the steps of: (a) pre-reforming the hydrocarbon mixture adiabatically, (b) heating the gaseous mixture obtained in step (a) to a temperature greater than 650° C., (c) performing a non-catalyzed partial oxidation by contacting the heated mixture of step (b) yielding a reactor effluent having a temperature of between 1100 and 1500 ° C., (d) performing a Fischer-Tropsch synthesis using the hydrogen- and carbon monoxide-containing gas as obtained in step (c) as feedstock and (e) wherein from the synthesis product obtained in step (d) a relatively light stream is separated and wherein a first part of the light stream is recycled to step (a) to be subjected to pre-reforming and wherein a second part of the light stream is recycled to the burner of step (c) to be subjected to partial oxidation and wherein the temperature in step (a) is controlled by the adjusting the amount of light stream that is recycled to step (a).
    • 本发明提供了一种从包含甲烷,乙烷和任选的较高碳数烃​​的烃的气体混合物制备费 - 托合成产物的方法,包括以下步骤:(a)绝热地预先重整烃混合物,(b) 步骤(a)中获得的气态混合物至大于650℃的温度,(c)通过使加热的步骤(b)的混合物接触而进行非催化部分氧化,产生温度为1100至1500℃的反应器流出物 ℃,(d)使用步骤(c)中获得的含氢和一氧化碳的气体作为原料进行费 - 托合成,(e)其中从步骤(d)中获得的合成产物相对较轻 流分离,并且其中轻流的第一部分被再循环到步骤(a)以进行预重整,并且其中轻流的第二部分被再循环到步骤(c)的燃烧器以进行部分 氧化物 离子,并且其中步骤(a)中的温度通过调节再循环到步骤(a)的轻质流量来控制。
    • 10. 发明授权
    • Process to prepare a Fischer-Tropsch synthesis product
    • 制备费 - 托合成产物的方法
    • US07795317B2
    • 2010-09-14
    • US11682351
    • 2007-03-06
    • Jacobus EilersRobert Schouwenaar
    • Jacobus EilersRobert Schouwenaar
    • C07C27/00
    • C10G2/00C01B3/36C01B3/382C01B3/52C01B2203/0216C01B2203/0255C01B2203/0415C01B2203/0485C01B2203/062C01B2203/0827C01B2203/1241C01B2203/142C01B2203/148C01B2203/1614C01B2203/169C10G2300/1022C10G2300/4081C10G2400/06
    • The invention provides a process to prepare a Fischer-Tropsch synthesis product from a gaseous mixture of hydrocarbons comprising methane, ethane and optional higher carbon number hydrocarbons comprising the steps of: (a) pre-reforming the hydrocarbon mixture adiabatically, (b) heating the gaseous mixture obtained in step (a) to a temperature greater than 650° C., (c) performing a non-catalyzed partial oxidation by contacting the heated mixture of step (b) yielding a reactor effluent having a temperature of between 1100 and 1500° C., (d) performing a Fischer-Tropsch synthesis using the hydrogen- and carbon monoxide-containing gas as obtained in step (c) as feedstock and (e) wherein from the synthesis product obtained in step (d) a relatively light stream is separated and wherein a first part of the light stream is recycled to step (a) to be subjected to pre-reforming and wherein a second part of the light stream is recycled to the burner of step (c) to be subjected to partial oxidation and wherein the temperature in step (a) is controlled by the adjusting the amount of light stream that is recycled to step (a).
    • 本发明提供了一种从包含甲烷,乙烷和任选的较高碳数烃​​的烃的气体混合物制备费 - 托合成产物的方法,包括以下步骤:(a)绝热地预重整烃混合物,(b) 步骤(a)中获得的气态混合物至大于650℃的温度,(c)通过使加热的步骤(b)的混合物接触而进行非催化部分氧化,产生温度为1100至1500℃的反应器流出物 ℃,(d)使用步骤(c)中获得的含氢和一氧化碳的气体作为原料进行费 - 托合成,(e)其中从步骤(d)中获得的合成产物相对较轻 流分离,并且其中轻流的第一部分被再循环到步骤(a)以进行预重整,并且其中轻流的第二部分被再循环到步骤(c)的燃烧器以进行部分 氧化物 并且其中步骤(a)中的温度通过调节再循环到步骤(a)的轻流量来控制。