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1. 发明授权

US09193653B1 Ether lubricants from fatty acids 有权
标题翻译：来自脂肪酸的醚润滑剂
公开(公告)号：US09193653B1
公开(公告)日：2015-11-24
申请号：US14540459
申请日：2014-11-13
申请人： Sven Ivar Hommeltoft
发明人： Sven Ivar Hommeltoft
IPC分类号： C07C43/00 , C07C41/01 , C07C41/09 , C07C41/06 , C07C45/48 , C07C29/145
CPC分类号： C07C29/145 , C07C41/01 , C07C41/06 , C07C41/09 , C07C45/48 , Y02P20/582 , C07C49/04 , C07C31/02 , C07C43/04
摘要： Processes for producing long chain ethers from long chain secondary alcohols using fatty acid containing feedstocks. In an embodiment, a long chain secondary alcohol may be reacted with a primary alcohol, a secondary alcohol, or an olefin to form a long chain ether. In another embodiment, a long chain secondary alcohol or the corresponding alkoxide may be reacted with an alkyl halide to form a long chain ether. In yet a further embodiment, a long chain secondary alcohol may be converted to a halide, and the halide may be reacted with a second alcohol or the corresponding alkoxide to form a long chain ether. Long chain ether compositions of matter are also disclosed.
摘要翻译：使用含脂肪酸的原料从长链仲醇生产长链醚的方法。在一个实施方案中，长链仲醇可以与伯醇，仲醇或烯烃反应形成长链醚。在另一个实施方案中，长链仲醇或相应的醇盐可与烷基卤反应形成长链醚。在又一个实施方案中，长链仲醇可以转化为卤化物，并且卤化物可以与第二醇或相应的醇盐反应形成长链醚。还公开了物质的长链醚组合物。

2. 发明授权

US08871154B2 Oligomerization reactor and control system 有权
标题翻译：低聚反应堆和控制系统
公开(公告)号：US08871154B2
公开(公告)日：2014-10-28
申请号：US13586760
申请日：2012-08-15
申请人： Sven Ivar Hommeltoft
发明人： Sven Ivar Hommeltoft
IPC分类号： B01J8/02 , C07C2/22
CPC分类号： C07C2/22 , B01J31/0284 , B01J31/0295 , B01J31/0298 , C07C2527/125 , C07C2527/24 , C07C11/02
摘要： A process unit, having: a) an oligomerization reactor; and b) a control system that enables the reactor to be operated in a distillate mode and in a lubricant mode; and wherein the reactor can switch between modes.
摘要翻译：一种处理单元，具有：a）低聚反应器; 以及b）控制系统，其使反应器能够以馏出模式和润滑剂模式运行; 并且其中所述反应器可以在模式之间切换。

3. 发明申请

US20140171710A1 METHOD FOR REDUCING ORGANIC HALIDE CONTAMINATION IN HYDROCARBON PRODUCTS 有权
标题翻译：减少碳氢化合物产品有机卤化物污染的方法
公开(公告)号：US20140171710A1
公开(公告)日：2014-06-19
申请号：US13715845
申请日：2012-12-14
申请人： Cedrick Mahieux , Sven Ivar Hommeltoft
发明人： Cedrick Mahieux , Sven Ivar Hommeltoft
IPC分类号： C07C7/148
CPC分类号： C07C7/14883 , C07C7/14858 , C07C7/173 , C10G29/00 , C10G29/205 , C10G53/00 , C10G53/04 , C10G53/16 , C10G2300/1096 , C10G2300/201 , C10G2400/02 , C10G2400/04 , C10G2400/08 , C10G2400/10 , C07C9/14 , C07C9/00
摘要： We provide a method for making hydrocarbon products with reduced organic halide contamination, comprising: a. separating an effluent from an ionic liquid catalyzed hydrocarbon conversion reaction into: i. a hydrocarbon fraction comprising an organic halide contaminant and from greater than zero to less than 5000 wppm olefins; and ii. a used ionic liquid catalyst fraction comprising a used ionic liquid catalyst; and b. contacting the hydrocarbon fraction with an aromatic hydrocarbon reagent and an ionic liquid catalyst to reduce a level of the organic halide contaminant to from greater than zero to 20 wppm in a finished hydrocarbon product.
摘要翻译：我们提供一种制备具有降低的有机卤化物污染物的烃产品的方法，包括：a。将来自离子液体催化的烃转化反应的流出物分离成：i。包含有机卤化物污染物和大于0至小于5000wppm烯烃的烃馏分; 和ii。使用的离子液体催化剂级分包含使用的离子液体催化剂; 和b。使烃馏分与芳族烃试剂和离子液体催化剂接触，以将成品烃产物中的有机卤化物污染物的含量降至大于0至20wppm。

4. 发明授权

US08685880B2 On-site drying of aqueous salt for ionic liquid make-up 有权
标题翻译：用于离子液体组合的含水盐的现场干燥
公开(公告)号：US08685880B2
公开(公告)日：2014-04-01
申请号：US13167446
申请日：2011-06-23
申请人： Sven Ivar Hommeltoft
发明人： Sven Ivar Hommeltoft
IPC分类号： B01J31/02 , B01J27/125
CPC分类号： B01J31/0284 , B01J31/0279
摘要： Methods for amending the composition of catalyst inventory of ionic liquid catalyzed processes, whereby the catalytic activity of the catalyst inventory may be adjusted and maintained for the steady state operation of such processes by contacting the catalyst inventory with a liquid phase, catalyst make-up material comprising an anhydrous salt and/or a mixture of the ionic liquid with the salt, wherein the salt comprises a precursor of the ionic liquid.
摘要翻译：用于修改离子液体催化过程的催化剂库存的组成的方法，由此可以通过使催化剂库存与液相，催化剂补充材料接触来调节和维持催化剂库存的稳定状态操作包括无水盐和/或离子液体与盐的混合物，其中盐包含离子液体的前体。

5. 发明申请

US20140073826A1 BASE OIL UPGRADING BY CO-FEEDING A KETONE OR BETA-KETO-ESTER FEEDSTOCK 有权
标题翻译：通过加入一个酮或BETA-KETO-ESTER FEEDSTOCK进行基础油升级
公开(公告)号：US20140073826A1
公开(公告)日：2014-03-13
申请号：US13615054
申请日：2012-09-13
申请人： Stephen Joseph Miller , Sven Ivar Hommeltoft , Saleh Ali Elomari
发明人： Stephen Joseph Miller , Sven Ivar Hommeltoft , Saleh Ali Elomari
IPC分类号： C10M105/04
CPC分类号： C10M111/02 , C10G3/50 , C10G45/58 , C10G47/00 , C10G65/12 , C10G2400/10 , C10L1/04 , C10L2200/043 , C10L2200/0438 , C10L2200/0446 , C10L2200/0469 , C10L2270/023 , C10L2270/026 , C10L2270/04 , C10L2290/08 , C10L2290/543 , C10M101/00 , C10M105/04 , C10M109/02 , C10M2203/1025 , C10N2230/02 , Y02P30/20 , C10N2220/022
摘要： This invention discloses a process for making high viscosity index lubricating base oils having a viscosity index of at least 110 by co-feeding a ketone or a beta-keto-ester feedstock with a lubricant oil feedstock directly to a hydrocracking unit to produce a hydrocracked stream. Then at least a portion of the hydrocracked stream is treated under hydroisomerization conditions to produce a high viscosity index lubricating base oil. The process may involve bypassing a hydrotreating or hydrofinishing step, which may result in improved efficiency and economics in producing high viscosity index lubricating base oils.
摘要翻译：本发明公开了一种制备粘度指数至少为110的高粘度指数润滑基础油的方法，该方法通过将酮或β-酮酯原料与润滑油原料直接加到加氢裂化装置中以产生加氢裂化的流。然后在加氢异构化条件下处理至少一部分加氢裂化物流以产生高粘度指数的润滑油基础油。该方法可能涉及绕过加氢处理或加氢精制步骤，这可以提高生产高粘度指数润滑基础油的效率和经济性。

6. 发明授权

US08524968B2 Process to make base oil by oligomerizing low boiling olefins 有权
标题翻译：通过低沸点烯烃低聚制备基础油的方法
公开(公告)号：US08524968B2
公开(公告)日：2013-09-03
申请号：US12966638
申请日：2010-12-13
申请人： Saleh A. Elomari , Stephen J. Miller , Sven Ivar Hommeltoft
发明人： Saleh A. Elomari , Stephen J. Miller , Sven Ivar Hommeltoft
IPC分类号： C07C2/04 , C07C2/08 , C10M143/00
CPC分类号： C10M107/02 , C10G50/02 , C10G2400/10 , C10M107/06 , C10M2205/024 , C10M2205/0245 , C10N2220/021 , C10N2220/022 , C10N2230/02 , C10N2240/04 , C10M2205/028 , C10M2205/0285
摘要： A process for making base oil, comprising: oligomerizing one or more olefins having a boiling point less than 82° C. in the presence of an ionic liquid catalyst to produce the base oil having a kinematic viscosity at 40° C. of 1100 mm2/s or higher. Also, a process, comprising: oligomerizing the olefins in the presence of an ionic liquid catalyst to produce the base oil having a kinematic viscosity at 40° C. of 300 mm2/s or higher and a low cloud point, wherein a wt % yield of products boiling at 482° C.+ (900° F.+) is at least 65 wt % of a total yield of products from the oligomerizing. Additionally, a process, comprising: oligomerizing the olefins in the presence of an ionic liquid catalyst to produce the base oil having a kinematic viscosity at 40° C. greater than 1100 mm2/s and a low cloud point.
摘要翻译：一种制备基础油的方法，包括：在离子液体催化剂存在下，使沸点小于82℃的一种或多种烯烃低聚，生成在40℃下的运动粘度为1100mm 2 / s以上。而且，一种方法包括：在离子液体催化剂的存在下使烯烃低聚以产生在40℃下的运动粘度为300mm 2 / s或更高和低浊点的基础油，其中wt％产率的沸点为482℃的产物+（900°F +）是来自低聚产物的总产率的至少65重量％。另外，一种方法包括：在离子液体催化剂的存在下使烯烃低聚以产生具有大于1100mm 2 / s和低浊点的40℃下的运动粘度的基础油。

7. 发明申请

US20130190167A1 METHOD TO MAKE AN ACIDIC IONIC LIQUID CATALYST HAVING GREATER THAN 20 WT% CONJUNCT POLYMER 审中-公开
标题翻译：制备具有超过20 WT％CONJUNCT聚合物的酸性离子液体催化剂的方法
公开(公告)号：US20130190167A1
公开(公告)日：2013-07-25
申请号：US13790866
申请日：2013-03-08
申请人： Sven Ivar Hommeltoft , Howard Steven Lacheen , Saleh Ali Elomari
发明人： Sven Ivar Hommeltoft , Howard Steven Lacheen , Saleh Ali Elomari
IPC分类号： B01J31/06
CPC分类号： B01J31/06 , B01J31/0284 , B01J31/0298 , B01J2231/32 , C07C2/58 , C07C2527/126 , C07C2531/02 , C07C2531/06
摘要： A method to make an acidic ionic liquid catalyst comprising: a. mixing aluminum chloride in the presence of a hydrocarbon solvent, and an organic chloride, to make an acid catalyst phase comprising a conjunct polymer; b. adding hydrogen chloride to the acid catalyst phase.
摘要翻译：一种制备酸性离子液体催化剂的方法，包括：a。在烃溶剂和有机氯化物的存在下混合氯化铝，以制备包含结合聚合物的酸催化剂相; b。在酸催化剂相中加入氯化氢。

8. 发明授权

US08487154B2 Market driven alkylation or oligomerization process 有权
标题翻译：市场驱动的烷基化或低聚过程
公开(公告)号：US08487154B2
公开(公告)日：2013-07-16
申请号：US12726009
申请日：2010-03-17
申请人： Hye-Kyung Timken , Shawn Winter , Howard S. Lacheen , Sven Ivar Hommeltoft
发明人： Hye-Kyung Timken , Shawn Winter , Howard S. Lacheen , Sven Ivar Hommeltoft
IPC分类号： C10G57/00
CPC分类号： C10G29/205 , B01J31/0277 , B01J31/0284 , B01J31/26 , B01J31/40 , B01J2219/00006 , B01J2219/00047 , B01J2231/20 , C10L1/06
摘要： A process comprising adjusting a level of conjunct polymers in an ionic liquid catalyst between a low level that favors production of C5+ products boiling at 137.8° C. or below and a higher level that favors production of both C5+ products boiling at 137.8° C. or below and C5+ products boiling above 137.8° C.; wherein the adjusting is done in response to market demand. A process unit, comprising a reactor that operates with an ionic liquid catalyst comprising a low level or a higher level of conjunct polymers, and the alkylation reactor is switched between operating with the low and the higher levels in response to market demand. A process unit, comprising a reactor that operates in an alkylate mode and a distillate mode, and a catalyst regenerator that operates with varying severity to adjust the level of conjunct polymers in response to demand for gasoline or distillate.
摘要翻译：一种方法包括调节离子液体催化剂中的结合聚合物的水平，其水平低于沸点为137.8℃或更低的C5 +产物的生成，以及有利于沸点为137.8℃的两种C5 +产物的生产的较高水平，或 C5 +产物沸点高于137.8℃。其中所述调整是根据市场需求进行的。一种处理单元，其包括用包含低水平或更高水平的结合聚合物的离子液体催化剂操作的反应器，并且烷基化反应器响应于市场需求在低和高水平操作之间切换。一种处理单元，包括以烷基化模式和馏出物模式操作的反应器，以及催化剂再生器，其以不同的严重程度操作，以响应于对汽油或馏出物的需求来调节结合聚合物的水平。

9. 发明授权

US08436221B2 Processes for upgrading fischer-tropsch condensate olefins by alkylation of hydrocrackate 有权
标题翻译：通过加氢裂化烷基化来提高费 - 托缩合烯烃的方法
公开(公告)号：US08436221B2
公开(公告)日：2013-05-07
申请号：US12975752
申请日：2010-12-22
申请人： Sven Ivar Hommeltoft , Bi-Zeng Zhan
发明人： Sven Ivar Hommeltoft , Bi-Zeng Zhan
IPC分类号： C07C2/62 , C07C2/60
CPC分类号： C10G57/00 , C10G29/205 , C10G50/00 , C10G65/14 , C10G2300/1022 , C10G2300/1088
摘要： Processes for upgrading Fischer-Tropsch condensate olefins by alkylation of hydrocrackate may involve providing an olefin enriched condensate stream and further providing a Fischer-Tropsch derived hydrocarbon stream comprising wax, hydrocracking the latter Fischer-Tropsch hydrocarbon stream to provide a distillate enriched hydrocracked product comprising isoparaffins, and alkylating the olefins with the isoparaffins in an alkylation zone to provide an alkylate product. The alkylate product may be fed to a distillation unit together with the hydrocracked product, while a naphtha containing fraction from the distillation unit may be fed to the alkylation zone together with the olefin enriched hydrocarbon stream.
摘要翻译：通过加氢裂化烷基化来提高费 - 托冷凝物烯烃的方法可包括提供富含烯烃的冷凝物流，并进一步提供包含蜡的费 - 托衍生烃流，加氢裂化后者费 - 托烃流，以提供富含馏出物的加氢裂化产物，其包含异链烷烃，并在烷基化区中用异链烷烃烷基化烯烃以提供烷基化产物。烷基化产物可以与加氢裂化产物一起进料到蒸馏单元，而含有来自蒸馏单元的含石脑油馏分可与富含烯烃的烃流一起进料至烷基化区。

10. 发明授权

US08323478B2 Process for measuring and adjusting halide in an alkylation reactor 有权
标题翻译：在烷基化反应器中测量和调节卤化物的方法
公开(公告)号：US08323478B2
公开(公告)日：2012-12-04
申请号：US13187656
申请日：2011-07-21
申请人： Sven Ivar Hommeltoft , Howard S. Lacheen
发明人： Sven Ivar Hommeltoft , Howard S. Lacheen
IPC分类号： C07C2/58
CPC分类号： C10G29/205 , C10G45/32 , C10G2300/1081 , C10G2300/1088 , C10G2300/1096 , C10G2300/201 , C10G2300/305 , C10G2300/4025 , C10G2300/80 , C10G2400/02 , C10G2400/04 , C10G2400/08 , C10G2400/10
摘要： A process, comprising: a. taking a sample from a continuous alkylation reactor process; b. measuring a content of a halide in the sample; and c. within 45 minutes from the taking a sample, adjusting a flow of a halide containing additive comprising the halide to control a ratio of a yield of an alkylate gasoline and a yield of a middle distillate. Also a process, comprising: a. taking a sample from an effluent of an alkylation reactor in an alkylation reactor process; b. measuring a content of a halide in the sample; and c. in response to the measured content of the halide, adjusting a flow of a halide containing additive to a predetermined range that has been selected to obtain a ratio of a yield of an alkylate gasoline and a yield of a middle distillate from 0.31 to 4.0 in a product from the alkylation reactor.
摘要翻译：一个过程，包括：a。从连续烷基化反应器工艺中取样; b。测量样品中卤化物的含量; 和c。在取样后45分钟内，调节包含卤化物的含卤化物添加剂的流动，以控制烷基化汽油的产率和中间馏分的产率。还有一个过程，包括：a。在烷基化反应器工艺中从烷基化反应器的流出物中取出样品; b。测量样品中卤化物的含量; 和c。响应于测量的卤化物含量，将含卤化物的添加剂的流量调节到预定范围内，以获得烷基化汽油的产率与中间馏分的产率之比为0.31至4.0，在产物从烷基化反应器。

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