专利快速检索-快速检索全球专利，免费商用专利数据库-IPRDB

1. 发明授权

US4810359A Gas-liquid separation in an ebullated bed process 失效
标题翻译：沸腾床工艺中的气液分离
公开(公告)号：US4810359A
公开(公告)日：1989-03-07
申请号：US897233
申请日：1986-08-18
申请人： Scott M. Sayles
发明人： Scott M. Sayles
IPC分类号： B01D19/00 , B01J8/22 , C10G1/08 , C10G49/12 , C10G23/00
CPC分类号： B01D19/0015 , B01D19/0042 , B01J8/22 , C10G1/083 , C10G49/12
摘要： In an ebullated bed process it has been found that a hydroclone effectively removes gas from recycled liquid used to ebullate the catalyst bed. When a 5 psi or greater inlet head and 5 psi pressure drop from the hydrocyclone inlet to the liquid outlet is maintained, essentially all gas is removed form the recycled liquid. Stabilized recycle pump operation is experienced and steady state achieved thereby.
摘要翻译：在沸腾床方法中，已经发现水力旋流器有效地从用于沸腾催化剂床的再循环液体中除去气体。当保持从水力旋流器入口到液体出口的5psi或更大的入口头和5psi的压力下降时，基本上所有的气体都从再循环的液体中移出。经历了稳定的循环泵操作，从而实现了稳定的状态。

2. 发明授权

US4163708A Process for the removal of thiols from hydrocarbon oils 失效
标题翻译：从烃油中除去硫醇的方法
公开(公告)号：US4163708A
公开(公告)日：1979-08-07
申请号：US892544
申请日：1978-04-03
申请人： Robert L. Jacobson , K. R. Gibson
发明人： Robert L. Jacobson , K. R. Gibson
IPC分类号： C10G25/00 , C10G29/04 , C10G29/06 , C10G61/06 , C10G69/10 , C10G23/00
CPC分类号： C10G29/06 , C10G25/003 , C10G29/04 , C10G61/06 , C10G69/10
摘要： Thiol impurities are removed from hydrocarbon oils by contacting the oil with a scavenger at a temperature in the range of about 120.degree. to 400.degree. C. The scavenger is a composite having a copper component and an inorganic porous carrier component and having a surface area in the range 20 to 1000 square meters per gram. The contacting must be with the scavenger below its thiol-sulfur end point.
摘要翻译：通过使油与清除剂在约120-400℃的温度下接触，从烃油中除去硫醇杂质。清除剂是具有铜组分和无机多孔载体组分的复合物，其表面积范围为20至1000平方米每克。接触必须与清除剂低于其硫醇 - 硫终点。

3. 发明授权

US4141816A Preventing ammonium chloride deposition in hydrogen recycle stream 失效
标题翻译：防止氯化氢沉积在氢循环流中
公开(公告)号：US4141816A
公开(公告)日：1979-02-27
申请号：US811356
申请日：1977-06-29
申请人： Ralph P. Crowley , Max G. Staples
发明人： Ralph P. Crowley , Max G. Staples
IPC分类号： C10G35/00 , C10G45/00 , C10G47/00 , C10G23/00
CPC分类号： C10G35/00 , C10G45/00 , C10G47/00
摘要： Deposition of ammonium chloride from gaseous streams is prevented by maintaining the temperature of the gaseous stream above the deposition temperature for ammonium chloride at operating pressure. The invention is particularly useful in hydrocarbon hydrogen treating processes in which hydrogen recycle streams containing ammonium chloride or ammonium chloride-forming constituents must be recompressed before recycle to the hydrogen treating process.
摘要翻译：通过将气态流的温度保持在操作压力下氯化铵的沉积温度以上，可以防止氯化铵从气流中的沉积。本发明在烃氢处理方法中特别有用，其中含有氯化铵或形成氯化铵的组分的氢循环物流必须在再循环到氢气处理过程之前再压缩。

4. 发明授权

US4135013A Method for the prevention of stress corrosion cracking 失效
标题翻译：防止应力腐蚀破裂的方法
公开(公告)号：US4135013A
公开(公告)日：1979-01-16
申请号：US764142
申请日：1977-01-31
申请人： Kineo Yamaguchi , Katsuhiko Kawakami
发明人： Kineo Yamaguchi , Katsuhiko Kawakami
IPC分类号： C10G49/00 , C23F13/02 , C10G23/00 , C23C7/00
CPC分类号： C23F13/02 , C10G49/005 , Y10T29/49888 , Y10T428/12757
摘要： Equipment used in a substantially water free, but corrosive environment is protected from corrosion by coating only certain welded parts thereof with a metal more base than the metal part coated.

5. 发明授权

US4082648A Process for separating solid asphaltic fraction from hydrocracked petroleum feedstock 失效
$Process for separating solid asphaltic fraction from hydrocracked petroleum feedstock$
标题翻译：从石油沥青混合料分离固体沥青混合料的工艺
公开(公告)号：US4082648A
公开(公告)日：1978-04-04
申请号：US765141
申请日：1977-02-03
申请人： James R. Murphy
发明人： James R. Murphy
IPC分类号： C10G45/04 , C10G45/18 , C10G47/04 , C10G49/00 , C10G65/04 , C10G67/02 , C10G31/06 , C10G13/00 , C10G23/00 , C10G31/10
CPC分类号： C10G49/007 , C10G45/04 , C10G45/18 , C10G47/04 , C10G65/04 , C10G67/02
摘要： A pretreating process for upgrading heavy petroleum feedstocks is disclosed. In a pretreating zone, the feedstock is contacted, in the presence of hydrogen, with a cracking catalyst. In this pretreating zone, the heavy metals content of the feedstock is reduced, and a significant quantity of the feedstock coke precursors are converted directly to oils which are readily recoverable from the pretreating zone effluent. Further, some unconverted coke precursors and the heavy metals complexed therewith are separated from the pretreating zone effluent in a solid asphaltic fraction. The pretreating zone effluent remaining after separation of this solid asphaltic fraction is an upgraded feedstock having significantly reduced heavy metal, sulfur, and Conradson carbon residue contents.

6. 发明授权

US4062762A Process for desulfurizing and blending naphtha 失效
标题翻译：石脑油脱硫和混合工艺
公开(公告)号：US4062762A
公开(公告)日：1977-12-13
申请号：US723152
申请日：1976-09-14
申请人： Kent A. Howard , William E. Winter, Jr. , Karsten H. Moritz , John D. Paynter
发明人： Kent A. Howard , William E. Winter, Jr. , Karsten H. Moritz , John D. Paynter
IPC分类号： C10G67/16 , C10G34/00 , C10G23/00 , C10G29/04
CPC分类号： C10G67/16 , C10G2400/02
摘要： A sulfur-containing naphtha is separated into at least three fractions. Each fraction is desulfurized separately by a different desulfurization method. Subsequently, the desulfurized fractions are recombined. The intermediate boiling point naphtha fraction is desulfurized by an alkali metal desulfurization process, preferably in the presence of added hydrogen.
摘要翻译：含硫石脑油被分成至少三个馏分。每个馏分通过不同的脱硫方法分开脱硫。随后，将脱硫馏分重组。中间沸点石脑油馏分通过碱金属脱硫方法脱硫，优选在加入氢气的情况下进行脱硫。

7. 发明授权

US4053388A Process for preparing aromatics from naphtha 失效
标题翻译：从NAPHTHA制备AROMATICS的方法
公开(公告)号：US4053388A
公开(公告)日：1977-10-11
申请号：US747863
申请日：1976-12-06
申请人： Angus B. Bailey
发明人： Angus B. Bailey
IPC分类号： C10G69/08 , C07C1/00 , C07C5/373 , C07C15/02 , C07C15/08 , C07C67/00 , C10G50/00 , C10G59/02 , C10G23/00 , C10G34/00
CPC分类号： C10G59/02 , C07C15/08 , Y02P20/52
摘要： This invention is directed to producing a high yield of aromatics from naphtha by integrating a catalytic reformer and a thermal hydrocracking unit followed by fractionating the product stream to obtain the desired aromatic. In this process, after sulfur is removed, the naphtha is catalytically reformed under conditions adapted to provide the maximum aromatic content. The reformed stream is then thermally hydrocracked, preferably in a system containing multiple reactors. The process does not require an external source of hydrogen since the reforming and hydrocracking units are operated to maintain a hydrogen balance. The hydrocracked stream is fractionated in a series of columns to produce the desired mix of aromatics. In one example, the fractionation separates out (1) benzene, which is further purified, if necessary (2) a toluene stream and a C.sub.9 + aromatic stream which are charged to a transalkylation reactor to produce a composition containing mixed xylenes sent to recycle and (3) a mixed xylene stream from which paraxylene is separated by a liquid-solid adsorption technique and from which the remaining xylenes are isomerized to produce further paraxylene. A by-product stream of light hydrocarbons is also produced. This procedure can be readily modified to produce greater amounts of benzene and/or toluene and less xylene.

8. 发明授权

US4017381A Process for desulfurization of residua with sodamide-hydrogen and regeneration of sodamide 失效
标题翻译：残余物脱硫与苏氨酰胺氢的再生方法
公开(公告)号：US4017381A
公开(公告)日：1977-04-12
申请号：US571955
申请日：1975-04-28
申请人： William Chalmers Baird, Jr. , Roby Bearden, Jr. , Ralph Louis Bollinger, Jr.
发明人： William Chalmers Baird, Jr. , Roby Bearden, Jr. , Ralph Louis Bollinger, Jr.
IPC分类号： C10G19/00 , C10G19/08 , C10G45/00 , C10G23/00
CPC分类号： C10G19/00 , C10G19/08 , C10G45/00 , Y10S423/12
摘要： Sulfur-containing petroleum oil feedstocks which include heavy hydrocarbon constituents undergo simultaneous desulfurization and hydroconversion by contacting and reacting such feedstocks with sodamide in the presence of hydrogen and at elevated temperatures. The mixture of reaction products resulting from the above procedure is separated to give a sodium sulfur salt by-product, and a petroleum oil product which has been substantially desulfurized and demetallized, as well as being significantly improved as indicated by a reduced Conradson carbon content and an increased API gravity relative to the feedstock. Sodamide is regenerated from the sodium sulfur salt by-product and can be recycled for reaction with additional feedstock.
摘要翻译：包括重质烃成分的含硫石油原料通过在氢气存在下和高温下使这些原料与sodamide接触和反应而同时进行脱硫和加氢转化。分离由上述方法得到的反应产物的混合物，得到硫化钠盐副产物，以及基本脱硫和去金属化的石油产品，并且显着改善，如Conradson碳含量和相对于原料的API重力增加。钠盐从钠硫酸钠副产物中再生，可再循环用于与额外原料反应。

9. 发明授权

US3843512A Hydrogen manufacture using centrifugal compressors 失效
标题翻译：使用离心压缩机的氢气制造
公开(公告)号：US3843512A
公开(公告)日：1974-10-22
申请号：US5986570
申请日：1970-06-26
申请人： CHEVRON RES
发明人： SMITH C , MCLEOD W
IPC分类号： C01B3/36 , C10G49/00 , C10K1/16 , C10G23/00
CPC分类号： C10G49/007 , C01B3/36 , C01B2203/0233 , C01B2203/0283 , C01B2203/0288 , C01B2203/0415 , C01B2203/0445 , C01B2203/0475 , C01B2203/0495 , C01B2203/0811 , C01B2203/0816 , C01B2203/0822 , C01B2203/0827 , C01B2203/0866 , C01B2203/0877 , C01B2203/0883 , C01B2203/0894 , C01B2203/1047 , C01B2203/1052 , C01B2203/1076 , C01B2203/1241 , C01B2203/146 , C01B2203/147 , C10K1/165 , Y02P20/128
摘要： 1. IN A PROCESS FOR MANUFACTURING HIGH PURITY BY A TRAIN OF STEPS COMPRISING REACTING HYDROCARBON WITH OXYGEN-AFFORDING GAS AT CONDITIONS INCLUDING A PRESSURE BELOW 900 P.S.I.G. AND ELEVATED TEMPERATURE TO FORM A GAS MIXTURE COMPRISING H2, CO AND CO2, REACTING CO IN THE MIXTURE WITH H2O TO FORM ADDITIONAL H2 AND CO2, AND REMOVING THE CO2 TO PROVIDE HIGH PURITY HYDROGEN, THE IMPROVEMENT FOR PROVIDING THE HIGH PURITY HYDROGEN AT ELEVATED PRESSURE WHICH COMPRISES: (A) CENTRIFUGALLY COMPRESSING WITH A CENTRIFUGAL COMPRESSOR THE GAS MIXTURE COMPRISING H2 AND C02 FROM THE PRESSURE BELOW ABOUT 900 P.S.I.G. TO A SUBSTANTIALLY HIGHER PRESSURE ABOVE 900 P.S.I.G., SAID MIXTURE CONTAINING SUFFICIENT CO2 SO THAT THE MOLECULAR WEIGHT OF THE MIXTURE IS AT LEAST 4; THEN (B) REMOVING CO2 FROM SAID COMPRESSED GAS BY ABSORBING CO2 IN A PHYSICAL ABSORBENT AT A PRESSURE ABOVE 900 P.S.I.G. TO THUS OBTAIN SAID HIGH PURITY HYDROGEN; (C) PASSING THE HIGH PURITY HYDROGEN TO A HYDROCONVERSION ZONE, AND REACTING SAID PURIFIED HYDROGEN WITH HYDROCARBONS IN SAID HYDROCONVERSION ZONE; (D) WITHDRAWING A HOT EFFLUENT FROM THE HYDROCONVERSION ZONE AND PASSING SAID HOT EFFLUENT THROUGH A STREAM BOILER TO GENERATE STEAM; AND (E) USING SAID STEAM TO DRIVE THE CENTRIFUGAL COMPRESSOR THROUGH A STREAM TUBINE LINKAGE FOR SAID CENTRIFUGAL COMPRESSING.

10. 发明授权

US3842122A Treating tar sands bitumen 失效
标题翻译：处理三文治
公开(公告)号：US3842122A
公开(公告)日：1974-10-15
申请号：US31931572
申请日：1972-12-29
申请人： HYDROCARBON RESEARCH INC
发明人： WOLK R , CHERVENAK M
IPC分类号： C10G1/06 , C10G1/00 , C10G9/16 , C10G23/00
CPC分类号： C10G1/065
摘要： (B) MAINTAINTAING THE SUPERFICIAL LINEAR VELOCITY OF THE DOOWNFLOWING LIQUID IN SEPARATION ZONE IN THE RANGE OF 0.006 TO 1.0 FOOT PER SECOND THE LOWER TEMPERATURE REQUIRING THE LOWER VELOCITY, (C) THE RANGE OF TEMPERATURE VERSOUS LIQUID VELOCITY BEING A SUBSTANTIALLY LINEAR RELATION OF TEMPERATURE VERSOUS A LOG-LOG SCALE OF DOWNFLOW LIQUID VELOCITY, (D) THE SPACE VELOCITY OF THE FEED THROUGH THE REACTION ZONE AND THE TEMPERATURE BEING SUCH THAT AT LAST 50 PERCENT OF THE FEED BOILING ABOVE 975*F. IS CONVERTED TO MATERIAL BOILING BELOW 975*F, (E) AND THEREBY AVOIDING COKING OF THE SEPARATOR.

1. IN A PROCESS FOR REFINING A TAR SAND DERIVED MATERIAL SELTED FROM THE GROUP CONSISTING OF NATURAL TAR AND BITUMEN, WHICH REFINING PROCESS INCLUDES THE STEPS OF PASSING THE FEED SUBSTANITALLY IN THE LIQUID PHASE THROUGH A REACTION ZONE IN THE PESENCE OF A HYDROGEN-CONTAINING GAS UNDER TEMPERATURE IN THE RANGE OF 700 TO 950*F. AND HYDROGEN PARTIAL PRESSURE IN THE RANGE OF 200 TO 1500 P.S.I. WHEREIN THE EFFLUENT IS REMOVED FROM THE REACTTION ZOZONE AND PASSED TO A SEPARATION ZONE AND WHEREIN THE EFFLUENT IS SEPARATED INTO AT LEAST A VAPOR FRACTION AND A LIQUID FRACTION, THE IMPROVEMENT WHICH COMPRISES: (A) MAINTAINING A TEMPERATURE IN THE SEPARATION ZONE IN THE RANGE OF 500*F. TO 800*F,

你已经成功收藏专利！

检索式保存成功!

IPRDB

热门服务

关于我们

友情链接

联系方式