公开(公告)号：US20140350132A1

公开(公告)日：2014-11-27

申请号：US14173905

申请日：2014-02-06

Applicant: Expander Energy Inc.

Inventor： KRESNYAK Steve

IPC: C10G2/00

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 vapour 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：US20140350131A1

公开(公告)日：2014-11-27

申请号：US14173876

申请日：2014-02-06

Applicant: EXPANDER ENERGY INC.

Inventor： KRESNYAK Steve

IPC: C10G2/00

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 vapour 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。