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1. 发明申请

US20170152449A1 Method and Apparatus for Recovering Synthetic Oils from Composite Oil Streams 审中-公开
公开(公告)号：US20170152449A1
公开(公告)日：2017-06-01
申请号：US15428195
申请日：2017-02-09
申请人： PNG Gold Corporation
发明人： Martin R. MacDonald
IPC分类号： C10G53/04 , C11B3/00
CPC分类号： C10G53/04 , C07C5/02 , C07C7/005 , C10G7/00 , C10G7/003 , C10G7/006 , C10G21/006 , C10G21/02 , C10G21/16 , C10G21/18 , C10G21/20 , C10G21/24 , C10G45/04 , C10G53/06 , C10G53/08 , C10G67/04 , C10G67/14 , C10G2300/1007 , C10G2300/44 , C10G2400/22 , C10G2400/30 , C11B3/006
摘要： A method for recovering synthetic oils from a feed stream, the method comprising separating at least a portion of the non-synthetic oil constituents from a commingled stream to produce a partially purified synthetic oil stream and one or more contaminant streams. Extracting at least a portion of the synthetic oil from the partially purified synthetic oil stream to produce a synthetic oil stream and a second contaminant stream.

2. 发明申请

US20160045841A1 NEW AND IMPROVED SYSTEM FOR PROCESSING VARIOUS CHEMICALS AND MATERIALS 审中-公开
标题翻译：用于加工各种化学品和材料的新型改进系统
公开(公告)号：US20160045841A1
公开(公告)日：2016-02-18
申请号：US14776732
申请日：2014-05-15
申请人： Allen KAPLAN , Randall BRADLEY , TRANSTAR GROUP, LTD.
发明人： Allen KAPLAN , Randall BRADLEY
IPC分类号： B01D3/06 , C10G57/00 , C10G45/00 , C10G33/00 , C10G7/06 , C10G11/18 , C10L9/10 , C10J3/72 , C10G1/00 , C01B17/027 , C01B17/74 , B01J6/00 , B01J2/00 , B01J19/24 , B01D53/48 , B01D53/62 , C22B9/00 , F27B17/00 , C02F1/00 , C22B7/00 , B29B17/00 , B22F3/10 , B22F9/00 , C22B21/00 , C22B15/00 , C22B13/00 , H01M8/00 , H01M10/54 , H02K55/02 , H02K7/09 , B02C23/00 , B03C1/00 , C10G7/00
CPC分类号： B01D3/06 , B01D53/48 , B01D53/62 , B01J2/00 , B01J6/008 , B01J19/0093 , B01J19/24 , B01J2219/00864 , B01J2219/00867 , B01J2219/00871 , B02C23/00 , B03C1/00 , B09B5/00 , B22F3/10 , B22F9/00 , B22F2009/001 , B29B17/00 , C01B3/32 , C01B13/02 , C01B17/02 , C01B17/027 , C01B17/48 , C01B17/74 , C01B32/05 , C01B32/20 , C01B32/50 , C01B2203/0205 , C01B2203/0283 , C01B2203/043 , C01B2203/0445 , C01B2203/0475 , C01G21/02 , C02F1/00 , C10G1/00 , C10G1/02 , C10G1/10 , C10G7/00 , C10G7/003 , C10G7/06 , C10G11/18 , C10G31/08 , C10G33/00 , C10G45/00 , C10G57/00 , C10G75/04 , C10J3/72 , C10J2300/093 , C10J2300/0946 , C10L9/10 , C10L2290/544 , C22B7/00 , C22B9/00 , C22B13/00 , C22B15/00 , C22B21/00 , F27B17/00 , H01M8/00 , H01M10/54 , H02K7/09 , H02K55/02 , Y02E20/16 , Y02E20/18 , Y02P10/143 , Y02P20/129 , Y02P30/446 , Y02W10/33 , Y02W10/37 , Y02W30/84
摘要： Eco-friendly systems, methods and processes/processing (EFSMP) or an integrated Matrix encompasses stand-alone and/or interconnected modules for completely self-sustained, closed-loop, emission-free processing of multiple source feedstock that can include pretreatment, with poisoning materials isolated during pretreatment being further recycled to provide useful materials such as, for example, separated metals, carbon and fullerenes for production of nano materials, sulfur, water, sulfuric acid, gas, heat and carbon dioxide for energy production, and production of refined petroleum, at a highly-reduced cost over the best state-of-the-art refining methods/systems that meets new emissions standards as well as optimizes production output with new ultra-speed cycle times. By-products from the petroleum refining process which were previously discarded also now are recycled as renewable sources of energy (water, waste oil and rubber/coal derived pyrolyic (pyrolysis) oil, carbon gases and process gases), or recyclable resources, such as metals and precious metals, oxides, minerals, etc., can be obtained.
摘要翻译：环保系统，方法和过程/处理（EFSMP）或集成Matrix包含独立和/或互连的模块，用于完全自我维持，闭环，无排放地处理多种原料，包括预处理，在预处理期间分离的中毒材料被进一步再循环以提供有用的材料，例如分离的金属，用于生产纳米材料的碳和富勒烯，用于能量生产的硫，水，硫酸，气体，热和二氧化碳，以及生产精炼的石油，以最优化的最先进的精炼方法/系统降低成本，满足新的排放标准，并以新的超速循环时间优化生产产量。以前废弃的石油炼制过程的副产物现在也被再循环为可再生能源（水，废油和橡胶/煤衍生的热解（热解）油，碳氢气和工艺气体）或可循环利用的资源，例如金属和贵金属，氧化物，矿物等。

3. 发明申请

US20140257008A1 METHOD AND APPARATUS FOR RECOVERING SYNTHETIC OILS FROM COMPOSITE OIL STREAMS 审中-公开
标题翻译：从复合油流回收合成油的方法和装置
公开(公告)号：US20140257008A1
公开(公告)日：2014-09-11
申请号：US14169113
申请日：2014-01-30
申请人： VeroLube, Inc.
发明人： Martin R. MacDonald
IPC分类号： C10G53/04
CPC分类号： C10G53/04 , C07C5/02 , C07C7/005 , C10G7/00 , C10G7/003 , C10G7/006 , C10G21/006 , C10G21/02 , C10G21/16 , C10G21/18 , C10G21/20 , C10G21/24 , C10G45/04 , C10G53/06 , C10G53/08 , C10G67/04 , C10G67/14 , C10G2300/1007 , C10G2300/44 , C10G2400/22 , C10G2400/30 , C11B3/006
摘要： A method for recovering synthetic oils from a feed stream, the method comprising separating at least a portion of the non-synthetic oil constituents from a commingled stream to produce a partially purified synthetic oil stream and one or more contaminant streams. Extracting at least a portion of the synthetic oil from the partially purified synthetic oil stream to produce a synthetic oil stream and a second contaminant stream.
摘要翻译：一种从进料流中回收合成油的方法，该方法包括从混合物流中分离出至少一部分非合成油成分以产生部分纯化的合成油料流和一种或多种污染物流。从部分纯化的合成油料流中提取合成油的至少一部分以产生合成油料流和第二污染物流。

4. 发明申请

US20140197075A1 FIELD ENHANCED SEPARATION OF HYDROCARBON FRACTIONS 审中-公开
标题翻译：油气分离场的现场加强分离
公开(公告)号：US20140197075A1
公开(公告)日：2014-07-17
申请号：US14132228
申请日：2013-12-18
申请人： ExxonMobil Research and Engineering Company
发明人： Krista Marie Prentice , Michel Daage , Jason M. McMullan , Gregory J. DeMartin , John Stephen Szobota , Ronald M. Gould , Anastasios Ioannis Skoulidas , Hyungsik Lee , Pawel K. Peczak , Charles Lambert Baker, JR. , Thomas Francis Degan, JR. , Lei Zhang , X B III , Philip J. Lenart
IPC分类号： C10G7/00
CPC分类号： C10G7/003 , B01D17/005 , B03C11/00 , B03C2201/02 , C10G31/06 , C10G32/02 , C10G53/02 , C10G71/00
摘要： Systems and methods are provided for using field enhanced separations to produce multiple fractions from a petroleum input. A liquid thermal diffusion and/or electric field separation is used to produce the fractions. The fractions can then be used to form multiple outputs that share a first feature while being different with regard to a second feature. For example, a first fraction from the plurality of fractions can have a desired value for a first property such as viscosity index. Two or more additional fractions from the plurality of fractions can then be blended together to make a blended fraction or output. The blended fraction can have a value for the first property that is substantially similar to the value for the first fraction. However, for a second property, the first fraction and the blended fraction can have distinct values. As a result, multiple output fractions can be formed that share a first feature but differ in a second feature.
摘要翻译：提供了系统和方法，用于使用场增强分离从石油输入产生多个馏分。使用液体热扩散和/或电场分离来生产级分。然后可以使用分数来形成共享第一特征的多个输出，同时关于第二特征不同。例如，来自多个级分的第一级分可以具有用于第一性质（例如粘度指数）的期望值。然后将来自多个馏分的两个或更多个附加馏分混合在一起以制备混合部分或输出。混合分数可以具有基本上类似于第一级分的值的第一性质的值。然而，对于第二特性，第一级分和混合级分可以具有不同的值。结果，可以形成共享第一特征但在第二特征中不同的多个输出分数。

5. 发明授权

US07976699B2 Distillation apparatus and method of use 有权
标题翻译：蒸馏装置及其使用方法
公开(公告)号：US07976699B2
公开(公告)日：2011-07-12
申请号：US11762741
申请日：2007-06-13
申请人： Michael L. Kesler
发明人： Michael L. Kesler
IPC分类号： C10M175/00
CPC分类号： C10G7/003 , C10G7/06 , C10G2300/1007
摘要： A method and apparatus is provided for distilling and processing chemicals. The apparatus is particularly suited for processing and distilling difficult to distill compounds, and is capable of producing diesel fuel and other products from used oil at a quality level similar to that of products produced from virgin crude oil.
摘要翻译：提供一种用于蒸馏和处理化学品的方法和装置。该设备特别适用于加工和蒸馏难以蒸馏的化合物，并且能够以与从原始原油生产的产品相似的质量水平从废油生产柴油燃料和其他产品。

6. 发明授权

US06413414B1 Process for separation of dewaxed lube oil into light and heavy products 有权
标题翻译：将脱蜡润滑油分离成轻质和重质产品的方法
公开(公告)号：US06413414B1
公开(公告)日：2002-07-02
申请号：US09565676
申请日：2000-05-04
申请人： Victor E. Arnold , Richard T. Cleveland
发明人： Victor E. Arnold , Richard T. Cleveland
IPC分类号： C10G7302
CPC分类号： C10G31/06 , C10G7/003 , C10G2400/10
摘要： Methods and apparatus to separate a light lube stock product and a heavy lube stock product from heavy dewaxed lube oils are described which maintain product specifications while utilizing conventional refinery equipment. The heavy dewaxed lube oil stream is first heated, such as in a spiral heat exchanger in the top of a vacuum stripper, with the heavy lube stock fraction, and/or with hot oil. Next, the heated heavy dewaxed lube oil stream is injected into the vacuum stripper, and fuel gas is injected at the bottom of the stripper as the stripping medium. A light lube stock fraction is removed from the upper portion of the stripper, and a heavy lube stock fraction is removed from the lower portion thereof. Optionally, the gas stripping medium is removed from the top of the stripper by a vacuum pump and used to fuel a hot oil exchanger to heat the oil which in turn is employed to heat the heavy dewaxed lube oil stream.
摘要翻译：描述了从重型脱蜡润滑油分离轻润滑油原料和重润滑油原料的方法和设备，其在使用常规炼油设备的同时保持产品规格。首先将沉重的脱蜡润滑油料流加热，例如在真空汽提器顶部的螺旋式热交换器中，重润滑油原料馏分和/或热油。接下来，将加热的高浓度脱蜡润滑油料流注入真空汽提器中，并将燃料气体作为汽提介质注入汽提塔底部。从汽提器的上部除去轻质润滑油原料馏分，从其下部除去重质润滑油原料馏分。任选地，通过真空泵将气体剥离介质从汽提器的顶部除去，并用于燃料热油交换器以加热油，其又被用于加热重的脱蜡润滑油流。

7. 发明申请

US20170283734A1 Method for Producing Base Lubricating Oil from Waste Oil 审中-公开
公开(公告)号：US20170283734A1
公开(公告)日：2017-10-05
申请号：US15628955
申请日：2017-06-21
申请人： Gen III Oil Corporation
发明人： Martin R. MacDonald
IPC分类号： C10M175/00 , C10G21/06 , B01D3/06 , B01D3/10 , B01D3/40 , C10G21/16 , C10G21/18 , C10G21/20 , C10G21/24 , C10G45/04 , C10G53/04 , C10G67/04 , C10G67/14 , C10G7/00 , C10G21/00 , C10G21/02 , C10G71/00 , C10G7/12
CPC分类号： C10M175/005 , B01D3/065 , B01D3/10 , B01D3/40 , C10G7/003 , C10G7/006 , C10G7/12 , C10G21/006 , C10G21/02 , C10G21/06 , C10G21/16 , C10G21/18 , C10G21/20 , C10G21/24 , C10G45/04 , C10G53/04 , C10G67/04 , C10G67/14 , C10G71/00 , C10G2300/1003 , C10G2300/1007 , C10G2300/301 , C10G2300/308 , C10G2300/4081 , C10G2300/44 , C10G2400/10
摘要： A method for recovering base oil from waste lubricating oil by separating base oil range constituents from a waste lubricating oil mixture, thereafter separating higher quality base oil constituents and lower quality base oil constituents from the base oil recovered from the waste lubricating oil mixture and thereafter treating the lower quality base oil constituents to produce marketable base oil. The total base oil produced from a waste lubricating oil mixture by this process is greater than the quantity producible by previous processes using only base oil separation from the waste lubricating oil mixture or processes which use only treatment of the base oil recovered from the waste lubricating oil mixture to produce the product base oil.

8. 发明申请

US20170275538A1 Method for Producing Base Lubricating Oil from Oils Recovered from Combustion Engine Service 审中-公开
公开(公告)号：US20170275538A1
公开(公告)日：2017-09-28
申请号：US15618603
申请日：2017-06-09
申请人： Gen III Oil Corporation
发明人： Martin R. MacDonald
IPC分类号： C10G53/04 , C07C7/00 , C10G21/02 , C10G67/14 , C10G67/04 , C10G45/04 , C10G21/20 , C10G21/18 , C10G21/16 , C10G7/00 , C10G21/00 , C07C5/02 , C10G21/24
CPC分类号： C10G53/04 , C07C5/02 , C07C7/005 , C10G7/00 , C10G7/003 , C10G7/006 , C10G21/006 , C10G21/02 , C10G21/16 , C10G21/18 , C10G21/20 , C10G21/24 , C10G45/04 , C10G53/06 , C10G53/08 , C10G67/04 , C10G67/14 , C10G2300/1007 , C10G2300/44 , C10G2400/22 , C10G2400/30 , C11B3/006
摘要： A method for producing ILSAC GF5 or higher compatible oils from used oil, comprising separating material having a boiling point less than about 350° F. from recovered oil to produce de-volatized fraction and light oil fraction. Separating material with a boiling point greater than about 350° F. and less than about 650° F. from the de-volatized oil fraction to produce fuel oil fraction and heavy oil fraction. Separating material with a boiling point greater than about 1200° F. from the heavy oil fraction to produce partially purified oil fraction and residual fraction. Treating the partially purified oil fraction to separate it into purified oil fraction and contaminant fraction. Hydrogenating the contaminant fraction to remove predetermined compounds, further saturating the fraction and thereby creating a saturated oil fraction. Fractionating the saturated oil stream to produce one or more of naphtha fraction, diesel oil fraction and base oil fraction.

9. 发明申请

US20150361356A1 REFINING USED MOTOR OIL THROUGH SUCCESSIVE HYDROTREATING PROCESSES 有权
标题翻译：通过成功的加氢过程精制使用的电机油
公开(公告)号：US20150361356A1
公开(公告)日：2015-12-17
申请号：US14306893
申请日：2014-06-17
申请人： AIR PRODUCTS AND CHEMICALS, INC.
发明人： Diwakar Garg , Timothy D. Lebrecht
IPC分类号： C10G45/22
CPC分类号： C10G65/04 , C10G7/003 , C10G7/06 , C10G67/02 , C10G2300/1007 , C10G2300/1059 , C10G2300/1074
摘要： A method for refining used motor oil using two or more hydrotreating reactors arranged in series. The used motor oil may be vacuum distilled to produce an unrefined gasoil. The unrefined gasoil may then be hydrotreated in a first hydrotreating reactor with hydrogen operated at a temperature ranging from approximately 245° C. to approximately 260° C. to produce a hydrotreated gasoil. The hydrogen may comprise a mixture of fresh hydrogen and recycled hydrogen recovered from the last of the two or more hydrotreating reactors. The hydrotreated gasoil may then be hydrotreated in one or more additional hydrotreating reactors operated at temperatures ranging from approximately 260° C. to approximately 330° C. to produce a refined gasoil. The first hydrotreating reactor may remove a substantial portion of metallic impurities from the unrefined impurities, while the one or more additional hydrotreating reactors remove a substantial portion of heteroatom impurities from the unrefined gasoil.
摘要翻译：一种使用两个或更多个串联排列的加氢处理反应器来精炼二次发动机油的方法。所用的机油可以被真空蒸馏以产生未精制的气油。然后可以在第一加氢处理反应器中加氢处理未精制的气油，氢气在约245℃至约260℃的温度下操作，以产生加氢处理的气油。氢气可以包括从两个或更多个加氢处理反应器中的最后一个回收的新鲜氢气和再循环的氢气的混合物。然后可以在一个或多个额外的加氢处理反应器中加氢处理加氢处理的气油，所述加氢处理反应器在约260℃至约330℃的温度下操作，以产生精制气油。第一加氢处理反应器可以从粗精制杂质中去除大部分金属杂质，而一个或多个另外的加氢处理反应器从未精制的气油中除去大部分的杂原子杂质。

10. 发明申请

US20150129412A1 METHOD FOR PRODUCING BASE LUBRICATING OIL FROM WASTE OIL 审中-公开
公开(公告)号：US20150129412A1
公开(公告)日：2015-05-14
申请号：US14601146
申请日：2015-01-20
申请人： VEROLUBE, INC.
发明人： Martin R. MacDonald
IPC分类号： C10M175/00 , B01D3/40 , B01D3/06 , B01D3/10
CPC分类号： C10M175/005 , B01D3/065 , B01D3/10 , B01D3/40 , C10G7/003 , C10G7/006 , C10G7/12 , C10G21/006 , C10G21/02 , C10G21/06 , C10G21/16 , C10G21/18 , C10G21/20 , C10G21/24 , C10G45/04 , C10G53/04 , C10G67/04 , C10G67/14 , C10G71/00 , C10G2300/1003 , C10G2300/1007 , C10G2300/301 , C10G2300/308 , C10G2300/4081 , C10G2300/44 , C10G2400/10
摘要： A method for recovering base oil from waste lubricating oil by separating base oil range constituents from a waste lubricating oil mixture, thereafter separating higher quality base oil constituents and lower quality base oil constituents from the base oil recovered from the waste lubricating oil mixture and thereafter treating the lower quality base oil constituents to produce marketable base oil. The total base oil produced from a waste lubricating oil mixture by this process is greater than the quantity producible by previous processes using only base oil separation from the waste lubricating oil mixture or processes which use only treatment of the base oil recovered from the waste lubricating oil mixture to produce the product base oil.

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