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公开(公告)号：US20170335173A1
公开(公告)日：2017-11-23
申请号：US15668864
申请日：2017-08-04
Applicant: Axel R. Johnson
Inventor： Axel R. Johnson
Abstract: The present invention relates to processes employing industrial streams, including glycerol-containing by-products of triglyceride processing as well as waste glycol streams recovered from several sources, to produce oil well drilling, completion and hydrofracturing fluids.
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公开(公告)号：US09725641B2
公开(公告)日：2017-08-08
申请号：US13434049
申请日：2012-03-29
Applicant: Axel R. Johnson
Inventor： Axel R. Johnson
Abstract: The present invention relates to processes employing industrial streams, including glycerol-containing by-products of triglyceride processing as well as waste glycol streams recovered from several sources, to produce oil well drilling, completion and hydrofracturing fluids.
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3.发明申请METHODS FOR PRODUCING AND EMPLOYING OIL AND GAS WELL DRILLING AND COMPLETION FLUIDS AS WELL AS HYDRAULIC FRACTURING FLUIDS EMPLOYING TRIGLYCERIDE PROCESSING BY PRODUCTS AND PROPYLENE GLYCOL RECOVERED FROM AIRCRAFT DEICING OPERATIONS 审中-公开用于生产和使用石油和天然气钻井和完井液的方法，如用于使用产品的TRIGLYCERIDE处理的液压破碎流体和从飞机检测操作中回收的丙烯甘油公开(公告)号：US20130261031A1
公开(公告)日：2013-10-03
申请号：US13434049
申请日：2012-03-29
Applicant: Axel R. Johnson
Inventor： Axel R. Johnson
Abstract: The present invention relates to processes employing industrial streams, including glycerol-containing by-products of triglyceride processing as well as waste glycol streams recovered from several sources, to produce oil well drilling, completion and hydrofracturing fluids.
Abstract translation: 本发明涉及使用工业流的方法，包括甘油三酯处理的含甘油副产物以及从多个来源回收的废二醇流，以生产油井钻井，完井和水力压裂流体。
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公开(公告)号：US5976355A
公开(公告)日：1999-11-02
申请号：US574585
申请日：1995-12-14
Applicant: Axel R. Johnson , Robert J. Gartside , Joseph L. Ross , Dennis A. Duncan
Inventor： Axel R. Johnson , Robert J. Gartside , Joseph L. Ross , Dennis A. Duncan
CPC classification number: C10G11/18
Abstract: A process for producing liquid fuels from heavy hydrocarbons such as residual oil in which the cracking temperatures are in the range of 800.degree. F. to 1200.degree. F., and the residence times are between 0.05 seconds and 0.50 seconds.
Abstract translation: 一种重质烃类如裂解温度在800〜1200°F范围内的残油的液体燃料的制造方法，停留时间为0.05秒〜0.50秒。
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5.发明授权Process for catalytically cracking paraffin rich feedstocks comprising high and low concarbon components 失效包含高碳和低碳组分的含石蜡原料的催化裂化方法
公开(公告)号：US5730859A
公开(公告)日：1998-03-24
申请号：US680675
申请日：1996-07-16
Applicant: Axel R. Johnson , Joseph L. Ross , Atulya V. Saraf
Inventor： Axel R. Johnson , Joseph L. Ross , Atulya V. Saraf
CPC classification number: C10G11/18 , C10G11/182 , C10G51/06
Abstract: A process for contemporaneously catalytically cracking a paraffin rich feedstock and a heavy feedstock wherein the feedstocks are segregated prior to catalytic cracking in separate reactors with regenerated particulate catalyst solids. The process provides for the separate optimal cracking of paraffinic constituents and heavy naphthenic constituents while maintaining an overall heat balance.
Abstract translation: 同时催化裂化含石蜡原料和重质原料的方法，其中原料在具有再生颗粒催化剂固体的分离的反应器中在催化裂化之前被分离。 该方法提供链烷烃组分和重质环烷烃组分的单独的最佳裂化，同时保持总体热平衡。
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Patent Agency Ranking6.发明授权Catalytically cracking paraffin rich feedstocks comprising high and low concarbon components 失效催化裂解包含高碳和低碳组分的富含石蜡的原料
公开(公告)号：US5565176A
公开(公告)日：1996-10-15
申请号：US409182
申请日：1995-03-23
Applicant: Axel R. Johnson , Joseph L. Ross , Atulya V. Saraf
Inventor： Axel R. Johnson , Joseph L. Ross , Atulya V. Saraf
CPC classification number: C10G11/18 , C10G11/182 , C10G51/06
Abstract: An apparatus for contemporaneously catalytically cracking a paraffin rich feedstock and a heavy feedstock wherein the feedstocks are segregated prior to catalytic cracking in separate reactors with regenerated particulate catalyst solids. The apparatus provides for the separate optimal cracking of paraffinic constituents and heavy naphthenic constituents while maintaining an overall heat balance.
Abstract translation: 一种用于同时催化裂化石蜡富集原料和重质原料的装置，其中原料在具有再生的颗粒催化剂固体的分离的反应器中在催化裂化之前被分离。 该装置提供链烷烃组分和重质环烷烃组分的单独的最佳裂化，同时保持总的热平衡。
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7.发明授权Process for the production of aromatics benzene, toluene, xylene (BTX) from heavy hydrocarbons 失效从重质烃生产芳烃苯，甲苯，二甲苯（BTX）的方法
公开(公告)号：US4765883A
公开(公告)日：1988-08-23
申请号：US435608
申请日：1982-10-20
Applicant: Axel R. Johnson , S. Narayanan , Herman H. Woebcke
Inventor： Axel R. Johnson , S. Narayanan , Herman H. Woebcke
CPC classification number: C10G51/00 , C10G2400/30
Abstract: A process for producing improved yields of aromatics (benzene, toluene, xylene) by initially partially thermally cracking heavy hydrocarbon and thermally cracking ethane to high conversion and then completely cracking the partially cracked heavy hydrocarbon with the completely cracked ethane.
Abstract translation: 通过首先部分热裂解重质烃并将乙烷热裂解成高转化率，然后用完全裂化的乙烷完全裂解部分裂解的重质烃，从而提高芳族化合物（苯，甲苯，二甲苯）的产率。
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公开(公告)号：US4615795A
公开(公告)日：1986-10-07
申请号：US684009
申请日：1984-12-20
Applicant: Herman N. Woebcke , Swami Narayanan , Axel R. Johnson
Inventor： Herman N. Woebcke , Swami Narayanan , Axel R. Johnson
CPC classification number: C10G51/023 , C10G51/00
Abstract: A process and system for the production of olefins from heavy hydrocarbon feedstocks. A heavy hydrocarbon feed is first pretreated at high pressure and moderate temperatures to preferentially remove coke precursors in a liquid product. The pretreated hydrocarbon is then separated into lighter and heavier fractions; the lighter fraction being further thermally cracked to produce olefins.
Abstract translation: 用于从重质烃原料生产烯烃的方法和系统。 首先将重质烃进料在高压和中等温度下进行预处理，以优先除去液体产物中的焦炭前体。 然后将预处理的烃分离成较轻和较重的馏分; 更轻的部分被进一步热裂化以产生烯烃。
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9.发明授权Process for cracking heavy hydrocarbon to produce olefins and liquid hydrocarbon fuels 失效裂解重质烃以生产烯烃和液体烃燃料的方法
公开(公告)号：US4552645A
公开(公告)日：1985-11-12
申请号：US587952
申请日：1984-03-09
Applicant: Robert J. Gartside , Axel R. Johnson , Joseph L. Ross
Inventor： Robert J. Gartside , Axel R. Johnson , Joseph L. Ross
Abstract: A process for cracking heavy hydrocarbon feedstocks by separation into light and heavy fractions and concommitantly thermally cracking the light fraction and coking the heavy fraction.
Abstract translation: 一种通过分离成轻质和重质馏分来裂解重质烃原料，同时热裂解轻馏分并焦化重馏分的方法。
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公开(公告)号：US4497638A
公开(公告)日：1985-02-05
申请号：US178491
申请日：1980-08-15
Applicant: Axel R. Johnson , Herman N. Woebcke
Inventor： Axel R. Johnson , Herman N. Woebcke
CPC classification number: C10G9/32 , B01J8/003 , C10G9/00 , C10G2400/20
Abstract: An improved process and apparatus for generating fuel gas and decoking particulate solids used as the source of heat to effect chemical reactions in a TRC system.
Abstract translation: 一种改进的用于产生燃料气体的方法和装置，并且将用作热源的颗粒固体除焦以在TRC系统中实现化学反应。
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