公开(公告)号：US20150315481A1

公开(公告)日：2015-11-05

申请号：US14799901

申请日：2015-07-15

Applicant: Expander Energy Inc.

Inventor： Kresnyak Steve ,  Timothy William Giles

IPC: C10G2/00 ,  C10J3/20 ,  C01B3/38 ,  C10K3/06 ,  C10L1/08 ,  C10L1/04 ,  C10J3/02 ,  C10J3/82

CPC classification number: C10G2/32 ,  C01B3/38 ,  C01B2203/0233 ,  C01B2203/062 ,  C01B2203/1052 ,  C01B2203/1064 ,  C01B2203/1082 ,  C01B2203/1235 ,  C10G2/30 ,  C10G2/34 ,  C10G2300/1003 ,  C10G2300/1011 ,  C10G2300/4081 ,  C10G2400/02 ,  C10G2400/26 ,  C10J3/02 ,  C10J3/20 ,  C10J3/82 ,  C10J2300/1618 ,  C10J2300/1659 ,  C10J2300/1846 ,  C10K3/06 ,  C10L1/04 ,  C10L1/08 ,  C10L2200/0492 ,  C10L2270/026 ,  C10L2270/04 ,  C10L2290/04 ,  C10L2290/24 ,  C10L2290/42 ,  Y02E50/32 ,  Y02E60/324 ,  Y02P30/20 ,  Y02T50/678

Abstract: An enhanced Fischer-Tropsch process for the synthesis of sulfur free, clean burning, green hydrocarbon fuels, examples of which include syndiesel and aviation fuel. Naphtha is destroyed in a hydrogen generator and recycled as feedstock to a syngas (FT) reactor in order to enhance the production of syndiesel from the reactor. A further variation integrates a second hydrogen generator capturing light hydrocarbon gas for conversion to hydrogen and carbon monoxide which supplements the Fischer-Tropsch reactor, The result is a considerable increase in the volume of syndiesel formulated. A system for effecting the process is also characterized in the specification.

Abstract translation: 用于合成无硫，清洁燃烧，绿色碳氢化合物燃料的增强的费 - 托方法，其实例包括聚合物和航空燃料。 石脑油在氢发生器中被破坏，并作为原料再循环到合成气（FT）反应器中，以便增强反应器中的混合物的产生。 进一步的变化集成了第二个氢发生器捕获轻质烃气体转化为氢和补充费 - 托反应器的一氧化碳。结果是配制的混合物的体积显着增加。 实施该方法的系统也在说明书中表征。

公开(公告)号：US09340732B2

公开(公告)日：2016-05-17

申请号：US14173876

申请日：2014-02-06

Applicant: Expander Energy Inc.

Inventor： Kresnyak Steve

IPC: C10G2/00 ,  C01B3/36 ,  C01B3/38

CPC classification number: C10G2/40 ,  C01B3/36 ,  C01B3/386 ,  C01B2203/0233 ,  C01B2203/0244 ,  C01B2203/025 ,  C01B2203/0283 ,  C01B2203/0405 ,  C01B2203/0415 ,  C01B2203/043 ,  C01B2203/062 ,  C01B2203/1247 ,  C01B2203/1258 ,  C10G2/30 ,  C10G2/32 ,  C10G2300/1077 ,  C10G2400/02 ,  C10G2400/04 ,  C10G2400/06 ,  C10G2400/08

Abstract: A bitumen and heavy oil upgrading process and system is disclosed for the synthesis of hydrocarbons, an example of which is synthetic crude oil (SCO). The process advantageously avoids the waste attributed to residuum and/or petcoke formation which has a dramatic effect on the yield of hydrocarbon material generated. The process integrates Fischer-Tropsch technology with gasification and hydrogen rich gas stream generation. The hydrogen rich gas generation is conveniently effected using singly or in combination a hydrogen source, a hydrogen rich vapor from hydroprocessing and the Fischer-Tropsch process, a steam methane reformer (SMR) and autothermal reformer (ATR) or a combination of SMR/ATR. The feedstock for upgrading is distilled and the bottoms fraction is gasified and converted in a Fischer-Tropsch reactor. A resultant hydrogen lean syngas is then exposed to the hydrogen rich gas stream to optimize the formation of, for example, the synthetic crude oil.

公开(公告)号：US09328291B2

公开(公告)日：2016-05-03

申请号：US14173905

申请日：2014-02-06

Applicant: Expander Energy Inc.

Inventor： Kresnyak Steve

IPC: C10G2/00 ,  C01B3/36 ,  C01B3/38

CPC classification number: C10G2/40 ,  C01B3/36 ,  C01B3/386 ,  C01B2203/0233 ,  C01B2203/0244 ,  C01B2203/025 ,  C01B2203/0283 ,  C01B2203/0405 ,  C01B2203/0415 ,  C01B2203/043 ,  C01B2203/062 ,  C01B2203/1247 ,  C01B2203/1258 ,  C10G2/30 ,  C10G2/32 ,  C10G2300/1077 ,  C10G2400/02 ,  C10G2400/04 ,  C10G2400/06 ,  C10G2400/08

Abstract: A bitumen and heavy oil upgrading process and system is disclosed for the synthesis of hydrocarbons, an example of which is synthetic crude oil (SCO). The process advantageously avoids the waste attributed to residuum and/or petcoke formation which has a dramatic effect on the yield of hydrocarbon material generated. The process integrates Fischer-Tropsch technology with gasification and hydrogen rich gas stream generation. The hydrogen rich gas generation is conveniently effected using singly or in combination a hydrogen source, a hydrogen rich vapor from hydroprocessing and the Fischer-Tropsch process, a steam methane reformer (SMR) and autothermal reformer (ATR) or a combination of SMR/ATR. The feedstock for upgrading is distilled and the bottoms fraction is gasified and converted in a Fischer-Tropsch reactor. A resultant hydrogen lean syngas is then exposed to the hydrogen rich gas stream to optimize the formation of, for example, the synthetic crude oil.

Abstract translation: 公开了一种用于合成烃的沥青和重油改质方法和体系，其中一个实例是合成原油（SCO）。 该方法有利地避免了归因于残余物和/或石油焦炭形成的废物，其对产生的烃材料的产率具有显着影响。 该工艺将费 - 托技术与气化和富氢气流生成相结合。 富氢气体的生成可以单独或组合使用氢源，来自加氢处理的富氢蒸气和费 - 托法，蒸汽甲烷重整器（SMR）和自热重整器（ATR）或SMR / ATR的组合 。 将升级的原料蒸馏并将底部馏分气化并在费 - 托反应器中转化。 然后将所得的贫氢合成气暴露于富氢气流中以优化例如合成原油的形成。