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11.发明授权Preparation of 1-methyl-3,5-diisopropyl benzene from charge streams containing diisopropyl toluene 失效从含有二异丙基甲苯的电荷流中制备1-甲基-3,5-二异丙基苯
公开(公告)号：US4314091A
公开(公告)日：1982-02-02
申请号：US135609
申请日：1980-03-31
Applicant: John M. Crone, Jr. , Robert M. Suggitt
Inventor： John M. Crone, Jr. , Robert M. Suggitt
CPC classification number: C07C4/18 , C07C2521/12
Abstract: Charge hydrocarbon stream containing diisopropyl toluene isomers is catalytically treated to recover product stream containing increased proportions of 1-methyl-3,5-diisopropyl benzene.
Abstract translation: 对含有二异丙基甲苯异构体的加料烃流进行催化处理以回收含有较高比例的1-甲基-3,5-二异丙基苯的产物流。
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12.发明授权Biosynthesis of protein by fermentation of methanol obtained from the gasification of coal or residual oil 失效通过从煤或残油的气化获得的甲醇发酵生物合成蛋白质
公开(公告)号：US4242458A
公开(公告)日：1980-12-30
申请号：US954712
申请日：1978-10-25
Applicant: Edward T. Child , Robert M. Suggitt
Inventor： Edward T. Child , Robert M. Suggitt
IPC: C07C29/151 , C12N1/32 , C12N1/36 , C12R1/78
CPC classification number: C07C29/1518 , C12N1/32 , Y02P20/132 , Y10S435/804 , Y10S435/93
Abstract: This invention relates to a method of synthesizing single cell protein from residual oils and/or coal by a mutually advantageous combination of a synthesis gas generation process or a coal gasification process in the production of methanol and ammonia, and their use by the protein producing bacteria.
Abstract translation: 本发明涉及通过在甲醇和氨的生产中合成气生成过程或煤气化方法的相互有利的组合以及由蛋白质生产细菌的使用而从残油和/或煤合成单细胞蛋白的方法 。
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公开(公告)号：US4160011A
公开(公告)日：1979-07-03
申请号：US865452
申请日：1977-12-29
Applicant: John H. Estes , Stanley Kravitz , Robert M. Suggitt
Inventor： John H. Estes , Stanley Kravitz , Robert M. Suggitt
CPC classification number: C01B33/2823 , C01B39/20 , Y10S423/21 , Y10S423/24
Abstract: An amorphous powder useful as a precursor for the preparation of crystalline aluminosilicates is prepared by forming a sodium aluminum silicate water mixture whose composition falls within specified ranges for forming sodium zeolite A. By dehydrating the mixture with a water miscible solvent prior to aging and crystal formation, an amorphous powder is recovered for future use. Upon subsequent treatment the amorphous powder can be converted to crystalline aluminosilicates including type 3A, 4A, 5A, X and Y.
Abstract translation: 可用作制备结晶铝硅酸盐的前体的无定形粉末通过形成其组成落入用于形成钠沸石A的特定范围内的硅酸钠水混合物来制备。通过在老化和晶体形成之前用水混溶性溶剂脱水混合物 回收无定形粉末以供将来使用。 随后的处理可以将无定形粉末转化为包括3A，4A，5A，X和Y型晶体的硅铝酸盐。
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公开(公告)号：US4042490A
公开(公告)日：1977-08-16
申请号：US428638
申请日：1973-12-26
Applicant: Robert M. Suggitt , Walter C. Gates, Jr.
Inventor： Robert M. Suggitt , Walter C. Gates, Jr.
IPC: B01J23/58 , B01J23/78 , B01J23/84 , C07C1/00 , C07C7/163 , C07C9/15 , C07C67/00 , C10G45/04 , C10G23/02 , C10G23/04
Abstract: A process for converting mixtures of C.sub.6 to C.sub.30 n-paraffin and n-paraffin by-products to substantially pure n-paraffin which comprises catalytically hydrogenating the mixture at a temperature of from about 600.degree. to 750.degree. F. in the presence of a Group VIII metal on alumina catalyst where the catalyst contains from about 0.05 to 2.0 weight percent of an alkali metal oxide or alkaline earth metal oxide or thallous oxide. The catalyst can additionally contain a Group VIB or VIIB metal.
Abstract translation: 将C6至C30正链烷烃和正链烷烃副产物的混合物转化为基本上纯的正链烷烃的方法，该方法包括在组合存在下在约600至750°F的温度下催化氢化混合物 Ⅷ金属在氧化铝催化剂上，其中催化剂含有约0.05至2.0重量％的碱金属氧化物或碱土金属氧化物或氧化铊。 催化剂还可以含有VIB族或VIIB族金属。
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公开(公告)号：US3966828A
公开(公告)日：1976-06-29
申请号：US532352
申请日：1974-12-13
Applicant: Robert M. Suggitt , Walter C. Gates, Jr. , Ralph B. Hudson, Jr.
Inventor： Robert M. Suggitt , Walter C. Gates, Jr. , Ralph B. Hudson, Jr.
CPC classification number: C07C9/00
Abstract: A process for converting mixtures of C.sub.6 to C.sub.30 n-paraffin and n-paraffin by-products to substantially pure n-paraffin which comprises catalytically hydrogenating the mixture at a temperature of from about 600.degree. to 750.degree.F. in the presence of a Group VIII metal on alumina catalyst, and from about 10 to 5,000 parts per million of nitrogen present as ammonia or an organonitrogen compound. The catalyst can additionally contain a Group VIB or VIIB metal.
Abstract translation: 将C6至C30正链烷烃和正链烷烃副产物的混合物转化为基本上纯的正链烷烃的方法，该方法包括在组合存在下在约600至750°F的温度下催化氢化混合物 VIII金属，氧化铝催化剂上的金属，以及作为氨或有机氮化合物存在的约10至5,000ppm的氮。 催化剂还可以含有VIB族或VIIB族金属。
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Patent Agency Ranking
公开(公告)号：US3962362A
公开(公告)日：1976-06-08
申请号：US563754
申请日：1975-03-31
Applicant: Robert M. Suggitt
Inventor： Robert M. Suggitt
Abstract: Polyphenyls including biphenyl and terphenyl, are prepared by hydroalkylation of a charge benzene, dehydrogenation of hydroalkylate, and separation of desired product polyphenyls.
Abstract translation: 包括联苯和三联苯在内的多苯基通过加料苯的加氢烷基化，加氢烷基化的脱氢和所需的产物聚苯的分离来制备。
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公开(公告)号：US5152975A
公开(公告)日：1992-10-06
申请号：US669796
申请日：1991-03-15
Applicant: Wing-Chiu F. Fong , Henry C. Chan , Robert M. Suggitt , Manuel E. Quintana
Inventor： Wing-Chiu F. Fong , Henry C. Chan , Robert M. Suggitt , Manuel E. Quintana
IPC: C01B3/48
CPC classification number: C01B3/48 , C01B2203/025 , C01B2203/0288 , C01B2203/043 , C01B2203/045 , C01B2203/0465 , C01B2203/0485 , C01B2203/0495 , C01B2203/0816 , C01B2203/0822 , C01B2203/0833 , C01B2203/0844 , C01B2203/0877 , C01B2203/0883 , C01B2203/0894 , C01B2203/1011 , C01B2203/1041 , C01B2203/1047 , C01B2203/1205 , C01B2203/1241 , C01B2203/146 , C01B2203/148 , Y02P20/128
Abstract: A process for producing high purity hyrogen is disclosed. Specifically, the process includes (1) partially oxidizing a gaseous hydrocarbonaceous feedstock to produce a synthesis gas mixture of carbon monoxide and hydrogen, (2) reacting the synthesis gas mixture with steam to convert the carbon monoxide into a raw gas mixture which primarily includes carbon dioxide and hydrogen, and (3) subjecting the raw gas mixture to pressure swing adsorption to purify the raw gas mixture, thereby producing high purity hydrogen and a reject gas mixture of impurities.The gaseous hydrocarbonaceous feed is specific, inasmuch as it is characterized by containing a major component which includes at least one C.sub.1 -C.sub.3 hydrocarbon and which has an average molecular weight of up to about 30.
Abstract translation: 公开了一种生产高纯度氢的方法。 具体来说，该方法包括（1）部分氧化气态烃类原料以产生一氧化碳和氢气的合成气混合物，（2）使合成气体混合物与蒸汽反应，将一氧化碳转化成主要包括碳的原料气体混合物 二氧化碳和氢气，（3）对原料气体混合物进行变压吸附以净化原料气体混合物，从而产生高纯度氢气和杂质的废气混合物。 气态烃类进料是特异性的，因为其特征在于含有包含至少一个C 1 -C 3烃并且平均分子量高达约30的主要组分。
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公开(公告)号：US4532227A
公开(公告)日：1985-07-30
申请号：US218610
申请日：1980-12-22
Applicant: Robert M. Suggitt
Inventor： Robert M. Suggitt
CPC classification number: C01B31/083 , B01J21/18 , B01J23/42
Abstract: Low ash pelleted carbon is prepared by contacting pelleted carbon first with hydrochloric acid followed by leaching with hydrofluoric acid.
Abstract translation: 通过先将沉淀碳与盐酸接触，然后用氢氟酸浸出来制备低灰分颗粒碳。
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公开(公告)号：US4199328A
公开(公告)日：1980-04-22
申请号：US974191
申请日：1978-12-28
Applicant: Edward L. Cole , John H. Estes , Robert M. Suggitt
Inventor： Edward L. Cole , John H. Estes , Robert M. Suggitt
CPC classification number: B01J29/146 , C10G2400/26
Abstract: A method of and a catalyst for the conversion of petroleum distillate fractions to high heating value fuel gases suitable for use as town gas or pipeline gas by reacting a petroleum derived feedstock containing paraffins with hydrogen in the presence of a lanthanum-cobalt/Y zeolite catalyst at elevated temperature and pressure.
Abstract translation: 一种用于将石油馏出物馏分转化成适用于城镇煤气或管道气体的高热值燃料气体的方法和催化剂，其通过在镧 - 钴/ Y沸石催化剂存在下使包含链烷烃的石油衍生原料与氢反应 在高温和高压下。
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20.发明授权Hydrocracking alkylaromatic-containing hydrocarbons at mild cracking conditions and then subjecting the alkylaromatic hydrocarbon to alkyl transfer 失效在轻度裂解条件下加氢裂化含烷基芳烃的烃，然后使烷基芳族烃进行烷基转移
公开(公告)号：US4127471A
公开(公告)日：1978-11-28
申请号：US819901
申请日：1977-07-28
Applicant: Robert M. Suggitt , Sheldon Herbstman
Inventor： Robert M. Suggitt , Sheldon Herbstman
CPC classification number: C07C6/126 , C07C15/00 , C07C4/12 , C07C6/123 , C10G65/043 , C07C2521/04 , C07C2521/12 , C07C2523/40 , C07C2523/74
Abstract: Hydrocarbon conversion is effected by hydrocracking a charge stock at mild cracking conditions followed by alkyl transfer typically transalkylation or disproportionation or isomerization under conditions conducive to extended catalyst life.
Abstract translation: 烃转化通过在轻度裂解条件下加氢裂化电荷原料进行，然后在有利于延长催化剂寿命的条件下通常进行烷基转移或歧化或异构化。
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