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公开(公告)号：US20170066972A1
公开(公告)日：2017-03-09
申请号：US15269736
申请日：2016-09-19
CPC分类号： C10G3/42 , C07C2/862 , C07C6/04 , C07C51/09 , C07C67/03 , C07C67/54 , C07C2531/14 , C07C2531/24 , C10G45/00 , C10G45/58 , C10G50/00 , C10G65/043 , C10G69/02 , C10G2300/1011 , C10G2300/1014 , C10G2300/1018 , C10G2300/1092 , C10G2300/1096 , C10G2300/202 , C10G2300/30 , C10G2300/301 , C10G2300/307 , C10G2300/308 , C10G2300/44 , C10G2400/00 , C10G2400/02 , C10G2400/04 , C10G2400/08 , C10G2400/20 , C10G2400/22 , C10L1/026 , C10L1/04 , C10L1/08 , C10L2200/0469 , C11B3/00 , C11C1/08 , C11C3/003 , Y02E50/13 , Y02P30/20 , Y02T50/678 , C07C69/533 , C07C57/03 , C07C57/12 , C07C11/02
摘要： Methods are provided for refining natural oil feedstocks. The methods comprise reacting the feedstock in the presence of a metathesis catalyst under conditions sufficient to form a metathesized product comprising olefins and esters. In certain embodiments, the methods further comprise separating the olefins from the esters in the metathesized product. In certain embodiments, the methods further comprise hydrogenating the olefins under conditions sufficient to form a fuel composition. In certain embodiments, the methods further comprise transesterifying the esters in the presence of an alcohol to form a transesterified product.
摘要翻译： 提供了用于精炼天然油原料的方法。 所述方法包括在复分解催化剂存在下，在足以形成包含烯烃和酯的复分解产物的条件下使原料反应。 在某些实施方案中，所述方法还包括将烯烃与复分解产物中的酯分离。 在某些实施方案中，所述方法还包括在足以形成燃料组合物的条件下氢化所述烯烃。 在某些实施方案中，所述方法还包括在醇存在下酯交酯化以形成酯交换产物。
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公开(公告)号：US20170002273A1
公开(公告)日：2017-01-05
申请号：US15197999
申请日：2016-06-30
发明人： Sheryl B. RUBIN-PITEL , Kenneth C.H. KAR , Stephen H. BROWN , Federico BARRAI , Brian A. CUNNINGHAM
CPC分类号： C10G11/18 , C10G47/02 , C10G69/04 , C10G2300/206 , C10G2400/00 , C10L1/06 , C10L1/08
摘要： Systems and methods are provided for upgrading catalytic slurry oil to form naphtha boiling range and/or distillate boiling range fuel products. It has been unexpectedly discovered that catalytic slurry oil can be separately hydroprocessed under fixed bed conditions to achieve substantial conversion of asphaltenes within the slurry oil (such as substantially complete conversion) while reducing or minimizing the amount of coke formation on the hydroprocessing catalyst. After hydroprocessing, the hydroprocessed effluent can be processed under fluid catalytic cracking conditions to form various products, including distillate boiling range fuels and/or naphtha boiling range fuels. Another portion of the effluent can be suitable for use as a low sulfur fuel oil, such as a fuel oil having a sulfur content of 0.1 wt % or less.
摘要翻译： 提供了用于升级催化浆料油以形成石脑油沸程和/或馏出物沸点燃料产品的系统和方法。 已经意外地发现，催化浆料油可以在固定床条件下分别进行加氢处理，以实现浆料油中沥青质的显着转化（例如基本上完全转化），同时减少或最小化加氢催化剂上的焦炭形成量。 在加氢处理之后，加氢处理的流出物可以在流体催化裂化条件下进行加工以形成各种产物，包括馏出物沸点范围的燃料和/或石脑油沸程燃料。 流出物的另一部分可适合用作低硫燃料油，例如硫含量为0.1重量％以下的燃料油。
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公开(公告)号：US08957268B2
公开(公告)日：2015-02-17
申请号：US12901829
申请日：2010-10-11
IPC分类号： C11C1/00 , C07C1/00 , C07C5/03 , C07C1/24 , C11B3/00 , C10G45/00 , C10G45/58 , C10G50/00 , C10G65/04 , C10L1/02 , C10L1/08 , C11C3/00 , C10G3/00 , C07C67/03 , C07C67/54 , C07C6/04 , C07C51/09 , C07C2/86
CPC分类号： C10G3/42 , C07C2/862 , C07C6/04 , C07C51/09 , C07C67/03 , C07C67/54 , C07C2531/14 , C07C2531/24 , C10G45/00 , C10G45/58 , C10G50/00 , C10G65/043 , C10G69/02 , C10G2300/1011 , C10G2300/1014 , C10G2300/1018 , C10G2300/1092 , C10G2300/1096 , C10G2300/202 , C10G2300/30 , C10G2300/301 , C10G2300/307 , C10G2300/308 , C10G2300/44 , C10G2400/00 , C10G2400/02 , C10G2400/04 , C10G2400/08 , C10G2400/20 , C10G2400/22 , C10L1/026 , C10L1/04 , C10L1/08 , C10L2200/0469 , C11B3/00 , C11C1/08 , C11C3/003 , Y02E50/13 , Y02P30/20 , Y02T50/678 , C07C69/533 , C07C57/03 , C07C57/12 , C07C11/02
摘要： Methods are provided for refining natural oil feedstocks. The methods comprise reacting the feedstock in the presence of a metathesis catalyst under conditions sufficient to form a metathesized product comprising olefins and esters. In certain embodiments, the methods further comprise separating the olefins from the esters in the metathesized product. In certain embodiments, the methods further comprise hydrogenating the olefins under conditions sufficient to form a fuel composition. In certain embodiments, the methods further comprise transesterifying the esters in the presence of an alcohol to form a transesterified product.
摘要翻译： 提供了用于精炼天然油原料的方法。 所述方法包括在复分解催化剂存在下，在足以形成包含烯烃和酯的复分解产物的条件下使原料反应。 在某些实施方案中，所述方法还包括将烯烃与复分解产物中的酯分离。 在某些实施方案中，所述方法还包括在足以形成燃料组合物的条件下氢化所述烯烃。 在某些实施方案中，所述方法还包括在醇存在下酯交酯化以形成酯交换产物。
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4.发明申请公开(公告)号：US20190241838A1
公开(公告)日：2019-08-08
申请号：US16385040
申请日：2019-04-16
IPC分类号： C11D1/22 , C11D17/04 , C07C303/02 , C07B41/04 , C07B41/02 , C07C5/32 , C07B45/04 , C11D1/37 , C07C2/66 , C10G3/00 , C10G1/10 , C10G1/00 , C10G65/04 , C10G45/02 , C10G45/00
CPC分类号： C11D1/22 , C07B41/02 , C07B41/04 , C07B45/04 , C07C2/66 , C07C5/32 , C07C303/02 , C10G1/002 , C10G1/10 , C10G3/42 , C10G3/50 , C10G45/00 , C10G45/02 , C10G65/04 , C10G2300/1003 , C10G2400/00 , C11D1/146 , C11D1/29 , C11D1/37 , C11D17/042 , C11D17/045 , Y02P30/20 , C07C11/02 , C07C15/107
摘要： The present invention relates generally to methods for producing detergent compounds from waste plastic feedstocks. More specifically, the invention relates to methods for producing detergent intermediates, including alkylbenzenes, paraffins, olefins, oxo alcohols, and surfactant derivatives thereof from waste plastic feedstock.
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公开(公告)号：US20160145511A1
公开(公告)日：2016-05-26
申请号：US14932232
申请日：2015-11-04
申请人： Xiaochun Xu , Bradley R. Fingland , Keith Wilson , Doron Levin , Stuart L. Soled , Sabato Miseo , Joseph E. Baumgartner , Ajit B. Dandekar
发明人： Xiaochun Xu , Bradley R. Fingland , Keith Wilson , Doron Levin , Stuart L. Soled , Sabato Miseo , Joseph E. Baumgartner , Ajit B. Dandekar
IPC分类号： C10G69/02 , C10M101/02 , C10G67/04
CPC分类号： C10G45/50 , B01J23/882 , B01J23/883 , B01J23/888 , B01J23/8885 , B01J37/20 , C10G35/06 , C10G45/08 , C10G47/06 , C10G65/02 , C10G65/04 , C10G65/08 , C10G65/12 , C10G67/04 , C10G69/02 , C10G69/08 , C10G2300/1048 , C10G2300/202 , C10G2300/301 , C10G2400/00 , C10M101/02
摘要： Methods are provided for hydroprocessing a feed (such as hydrotreating, hydrocracking, or hydrofining a feed) to generate a product with a reduced or minimized aromatics content relative to the severity of the hydroprocessing conditions. In some types of hydroprocessing applications, it can be desirable to select the severity of hydroprocessing conditions to achieve a desired level of removal for sulfur, a desired level for removal of nitrogen, and/or a desired level for increasing the viscosity index of a feed. The severity for heteroatom removal and/or viscosity index uplift can also correspond to an amount of conversion of a feed to lower boiling point products, so the lowest severity conditions suitable for achieving a product quality can be desirable. By improving the aromatics saturation during hydroprocessing, the severity of subsequent aromatics saturation processes can be reduced.
摘要翻译： 提供用于加氢处理饲料（例如加氢处理，加氢裂化或加氢精制饲料）以产生相对于加氢处理条件的严重性降低或最小化芳烃含量的产物。 在一些类型的加氢处理应用中，可以期望选择加氢处理条件的严重性以达到期望的硫去除水平，除去氮的所需水平和/或用于提高进料粘度指数的期望水平 。 杂原子除去和/或粘度指数升高的严重程度也可以对应于进料到低沸点产物的转化量，因此适合于获得产品质量的最低苛刻度条件是可取的。 通过改善加氢处理过程中的芳族化合物饱和度，可以降低随后的芳烃饱和过程的严重性。
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6.发明申请Composition Comprising Paraffin Fractions Obtained From Biological Raw Materials and Method of Producing Same 有权包含从生物原料获得的石蜡馏分的组合物及其生产方法公开(公告)号：US20150191404A1
公开(公告)日：2015-07-09
申请号：US14147243
申请日：2014-01-03
申请人： Neste Oil Oyj
发明人： Pekka AALTO , Kati SANDBERG , Tomi NYMAN , Maija HAKOLA
CPC分类号： C10G3/50 , C07C1/22 , C07C9/14 , C09D7/20 , C10G3/42 , C10G45/58 , C10G65/043 , C10G2300/1011 , C10G2400/00 , C10L1/04 , C10L2200/0469 , C10L2270/08 , C10M105/00 , C10M105/04 , C10M177/00 , C10M2203/003 , C10M2203/022 , C10N2220/021 , C10N2220/025 , C10N2220/028 , C10N2220/031 , C10N2240/201 , C10N2240/40 , Y02P20/582 , Y02P30/20
摘要： A composition, including 40-50 wt-% C14 paraffins, based on the total weight of the composition, and 35-45 wt-% C15 paraffins, based on the total weight of the composition, wherein the C14 and C15 paraffins are produced from a biological raw material.
摘要翻译： 基于组合物的总重量，包含40-50重量％C14链烷烃和基于组合物总重量的35-45重量％C 15链烷烃的组合物，其中C 14和C 15链烷烃由 生物原料。
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公开(公告)号：US10066172B2
公开(公告)日：2018-09-04
申请号：US15374289
申请日：2016-12-09
CPC分类号： C10G51/023 , C10G9/36 , C10G47/32 , C10G49/007 , C10G65/10 , C10G75/00 , C10G2300/107 , C10G2300/1074 , C10G2300/1077 , C10G2400/00 , C10G2400/10
摘要： Embodiments of a process for producing paraffins from a petroleum-based composition comprising long chain aromatics comprise mixing a supercritical water stream with a pressurized, heated petroleum-based composition to create a combined feed stream, introducing the combined feed stream to a first reactor through an inlet port of the first reactor, where the first reactor operates at supercritical pressure and temperature, cracking at least a portion of the long chain aromatics in the first reactor to form a first reactor product, and then introducing the first reactor product to a second reactor through an upper inlet port of the second reactor operating at supercritical pressure and temperature, where the second reactor is a downflow reactor comprising an upper inlet port, a lower outlet port, and a middle outlet port are provided. The middle outlet product passing out of the middle outlet port comprises paraffins and short chain aromatics.
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8.发明申请METHODS FOR PRODUCING ALKYLBENZENES, PARAFFINS, OLEFINS AND OXO ALCOHOLS FROM WASTE PLASTIC FEEDSTOCKS 审中-公开从废物塑料原料生产烷基苯甲酸，对苯二甲酸，烯烃和氧化物的方法公开(公告)号：US20170044465A1
公开(公告)日：2017-02-16
申请号：US15225865
申请日：2016-08-02
IPC分类号： C11D1/22 , C10G1/00 , C07C303/02 , C11D1/29 , C07B41/04 , C07B45/04 , C11D1/14 , C10G1/10 , C07B41/02
CPC分类号： C11D1/22 , C07B41/02 , C07B41/04 , C07B45/04 , C07C2/66 , C07C5/32 , C07C303/02 , C10G1/002 , C10G1/10 , C10G3/42 , C10G3/50 , C10G45/00 , C10G45/02 , C10G65/04 , C10G2300/1003 , C10G2400/00 , C11D1/146 , C11D1/29 , C11D1/37 , C11D17/042 , C11D17/045 , Y02P30/20 , C07C11/02 , C07C15/107
摘要： The present invention relates generally to methods for producing detergent compounds from waste plastic feedstocks. More specifically, the invention relates to methods for producing detergent intermediates, including alkylbenzenes, paraffins, olefins, oxo alcohols, and surfactant derivatives thereof from waste plastic feedstock.
摘要翻译： 本发明一般涉及从废塑料原料生产洗涤剂化合物的方法。 更具体地，本发明涉及用废塑料原料生产洗涤剂中间体的方法，包括烷基苯，链烷烃，烯烃，羰基合成醇及其表面活性剂衍生物。
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公开(公告)号：US20150240186A1
公开(公告)日：2015-08-27
申请号：US14590737
申请日：2015-01-06
IPC分类号： C11C1/08
CPC分类号： C10G3/42 , C07C2/862 , C07C6/04 , C07C51/09 , C07C67/03 , C07C67/54 , C07C2531/14 , C07C2531/24 , C10G45/00 , C10G45/58 , C10G50/00 , C10G65/043 , C10G69/02 , C10G2300/1011 , C10G2300/1014 , C10G2300/1018 , C10G2300/1092 , C10G2300/1096 , C10G2300/202 , C10G2300/30 , C10G2300/301 , C10G2300/307 , C10G2300/308 , C10G2300/44 , C10G2400/00 , C10G2400/02 , C10G2400/04 , C10G2400/08 , C10G2400/20 , C10G2400/22 , C10L1/026 , C10L1/04 , C10L1/08 , C10L2200/0469 , C11B3/00 , C11C1/08 , C11C3/003 , Y02E50/13 , Y02P30/20 , Y02T50/678 , C07C69/533 , C07C57/03 , C07C57/12 , C07C11/02
摘要： Methods are provided for refining natural oil feedstocks. The methods comprise reacting the feedstock in the presence of a metathesis catalyst under conditions sufficient to form a metathesized product comprising olefins and esters. In certain embodiments, the methods further comprise separating the olefins from the esters in the metathesized product. In certain embodiments, the methods further comprise hydrogenating the olefins under conditions sufficient to form a fuel composition. In certain embodiments, the methods further comprise transesterifying the esters in the presence of an alcohol to form a transesterified product.
摘要翻译： 提供了用于精炼天然油原料的方法。 所述方法包括在复分解催化剂存在下，在足以形成包含烯烃和酯的复分解产物的条件下使原料反应。 在某些实施方案中，所述方法还包括将烯烃与复分解产物中的酯分离。 在某些实施方案中，所述方法还包括在足以形成燃料组合物的条件下氢化所述烯烃。 在某些实施方案中，所述方法还包括在醇存在下酯交酯化以形成酯交换产物。
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公开(公告)号：US20180002615A1
公开(公告)日：2018-01-04
申请号：US15608070
申请日：2017-05-30
发明人： Stuart S. SHIH , Timothy L. HILBERT , Anastasios I. SKOULIDAS , Bryan A. PATEL , Michael R. CHUBA , Sean C. SMYTH , Mohan KALYANARAMAN
CPC分类号： C10G65/02 , B01J8/001 , B01J8/008 , B01J8/1872 , B01J8/24 , B01J23/40 , B01J29/7261 , B01J29/7292 , B01J29/7461 , B01J29/7492 , C10G45/02 , C10G45/62 , C10G45/64 , C10G65/04 , C10G2300/10 , C10G2300/1048 , C10G2300/202 , C10G2300/301 , C10G2300/304 , C10G2400/00
摘要： Systems and methods are provided for catalytically dewaxing a diesel boiling range feed. In some aspects, catalytic dewaxing can be performed at low hydrogen treat gas rates and/or low hydrogen purity conditions. In other aspects, the systems and methods can allow for distillate dewaxing while reducing or minimizing the amount of equipment required.
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