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1. 发明授权

US09657240B2 Method for improving the transportability of heavy crude oil 有权
公开(公告)号：US09657240B2
公开(公告)日：2017-05-23
申请号：US14425431
申请日：2013-08-22
申请人： Ulrich Wagner , Wolff Balthasar , Dierk Müller
发明人： Ulrich Wagner , Wolff Balthasar , Dierk Müller
IPC分类号： C10G71/00 , C10G3/00
CPC分类号： C10G71/00 , C07C29/1516 , C10G3/00 , F17D1/16 , F17D1/17 , F17D1/18 , F17D3/12 , Y02E60/34 , Y02P30/20
摘要： The invention relates to a method for improving the transportability of heavy crude oil.Proceeding from the disadvantages of the known prior art a method is to be provided, in which an additive can be used which is producible from a byproduct arising during mineral oil production. The method is to be performable with low expenditure and without any special safety precautions. Further the additive shall lead to an increased yield of conventional petroleum during subsequent refining.According to the invention, an aqueous hydrocarbon mixture having a chain length of predominantly C4 to C12 which does not contain any oxygen-containing hydrocarbon compounds is utilized. This is produced in the area of a mineral oil field from natural gas arising as by-product and/or mineral oil-associated gas. Thereby from the heavy crude oil a crude oil which is light in quality and transportable is obtained. During the subsequent refining of the light crude oil to give conventional petroleum, the amount of petroleum produced is increased by the amount of hydrocarbons present in the aqueous hydrocarbon mixture.

2. 发明申请

US20150232767A1 Method for improving the transportability of heavy crude oil 审中-公开
标题翻译：改善重质原油运输能力的方法
公开(公告)号：US20150232767A1
公开(公告)日：2015-08-20
申请号：US14425431
申请日：2013-08-22
申请人： Ulrich WAGNER , Wolff BALTHASAR , Dierk MÜLLER
发明人： Ulrich Wagner , Wolff Balthasar , Dierk Müller
IPC分类号： C10G71/00 , C10G3/00
CPC分类号： C10G71/00 , C07C29/1516 , C10G3/00 , F17D1/16 , F17D1/17 , F17D1/18 , F17D3/12 , Y02E60/34 , Y02P30/20
摘要： The invention relates to a method for improving the transportability of heavy crude oil.Proceeding from the disadvantages of the known prior art a method is to be provided, in which an additive can be used which is producible from a byproduct arising during mineral oil production. The method is to be performable with low expenditure and without any special safety precautions. Further the additive shall lead to an increased yield of conventional petroleum during subsequent refining.According to the invention, an aqueous hydrocarbon mixture having a chain length of predominantly C4 to C12 which does not contain any oxygen-containing hydrocarbon compounds is utilized. This is produced in the area of a mineral oil field from natural gas arising as by-product and/or mineral oil-associated gas. Thereby from the heavy crude oil a crude oil which is light in quality and transportable is obtained. During the subsequent refining of the light crude oil to give conventional petroleum, the amount of petroleum produced is increased by the amount of hydrocarbons present in the aqueous hydrocarbon mixture.
摘要翻译：本发明涉及一种改善重质原油运输性能的方法。从已知现有技术的缺点出发，提供一种方法，其中可以使用可在矿物油生产过程中产生的副产物产生的添加剂。该方法是以低开支执行，没有任何特别的安全预防措施。此外，添加剂将导致随后精炼期间常规石油的产量增加。根据本发明，使用具有不含任何含氧烃化合物的主链C4-C12链长的含水烃混合物。这是在作为副产物和/或矿物油相关气体产生的天然气的矿物油田地区生产的。因此，从重质原油获得质量轻且可运输的原油。在随后精炼轻质原油以提供常规石油的过程中，生产的石油的量增加了含水烃混合物中存在的烃的量。

3. 发明授权

US08388864B2 Process and plant for producing synthesis gas 有权
标题翻译：生产合成气的工艺和设备
公开(公告)号：US08388864B2
公开(公告)日：2013-03-05
申请号：US12300683
申请日：2007-05-10
申请人： Andreas Bormann , Dierk Müller
发明人： Andreas Bormann , Dierk Müller
IPC分类号： C01B3/24 , C01B3/38
CPC分类号： C01B3/382 , C01B2203/0233 , C01B2203/0244 , C01B2203/061 , C01B2203/068 , C01B2203/1241 , C01B2203/127 , C01B2203/141 , C01B2203/143
摘要： When producing synthesis gas from a starting material containing hydrocarbons, in particular natural gas, a feed stream of the starting material is divided into a first partial stream and a second partial stream. The first partial stream is supplied to a steam reformer (4), in which together with steam it is catalytically converted to a gas stream containing carbon oxides. Then, the first partial stream is again combined with the second partial stream and the combined gas stream is supplied to an autothermal reformer (7), in which together with gas rich in oxygen it is autothermally reformed to a synthesis gas in the presence of a cracking catalyst. Processing a starting material with a high content of higher hydrocarbons is made possible in that before the steam reformer (4) and before the autothermal reformer (7) the entire starting material is supplied to a pre-reformer (2) in which the starting material largely is liberated from higher hydrocarbons.
摘要翻译：当从含有烃，特别是天然气的原料生产合成气时，原料的进料流被分成第一部分流和第二部分流。将第一部分流供应到蒸汽重整器（4），其中蒸汽与蒸汽一起被催化转化成含有碳氧化物的气流。然后，将第一部分流再次与第二部分流合并，将合并的气流供应至自热重整器（7），其中与富含氧气的气体一起，在有气体的情况下自动重整成合成气裂化催化剂。加工具有高含量高烃的原料是可能的，因为在蒸汽重整器（4）之前和自热重整器（7）之前，将整个起始原料供应到预重整器（2），其中原料主要是从高级碳氢化合物中释放出来

4. 发明授权

US08471076B2 Process and plant for producing methanol 有权
标题翻译：生产甲醇的工艺和装置
公开(公告)号：US08471076B2
公开(公告)日：2013-06-25
申请号：US12674460
申请日：2008-08-18
申请人： Dierk Müller , Andreas Bormann
发明人： Dierk Müller , Andreas Bormann
IPC分类号： C07C29/151 , C07C29/152 , B01J8/04 , B01J8/06
CPC分类号： C07C29/1516 , B01J8/0488 , B01J8/0496 , B01J8/067 , B01J2208/00212 , B01J2208/0053 , C07C31/04
摘要： In the production of methanol from a synthesis gas containing hydrogen and carbon oxides, the synthesis gas is passed through a first, preferably water-cooled reactor, in which a part of the carbon oxides is catalytically converted to methanol. The obtained mixture containing synthesis gas and methanol vapor is supplied to a second, preferably gas-cooled reactor, in which a further part of the carbon oxides is converted to methanol. Subsequently, methanol is separated from the synthesis gas, and the synthesis gas is recirculated to the first reactor. To achieve a maximum methanol yield even with an aged catalyst, a partial stream of the synthesis gas is guided past the first reactor and introduced directly into the second reactor.
摘要翻译：在从含有氢和碳氧化物的合成气生产甲醇时，使合成气通过第一，优选水冷却的反应器，其中一部分碳氧化物被催化转化成甲醇。将得到的含有合成气和甲醇蒸气的混合物供给到第二气化冷却反应器，其中另外部分的碳氧化物转化为甲醇。随后，从合成气中分离出甲醇，合成气再循环到第一反应器。为了即使用老化的催化剂实现最大的甲醇产率，合成气的一部分流被引导通过第一反应器并直接引入到第二反应器中。

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