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公开(公告)号:CN112638850A
公开(公告)日:2021-04-09
申请号:CN201980057003.X
申请日:2019-09-05
Applicant: 巴斯夫欧洲公司
IPC: C07C29/38 , C07C33/025 , B01J3/008 , B01J4/002 , B01J19/26
Abstract: 一种生产异戊烯醇的方法,包括通过多个平行操作的喷嘴将甲醛源和异丁烯混合并注入反应器中并使甲醛源和异丁烯在超临界条件下反应;其中该反应器包括垂直放置的容器、侧壁、上部和下部;并且其中将甲醛源和异丁烯注入设置在上部的反应器混合室中并将包含甲醛和/或异丁烯和/或异戊烯醇的流体从该混合室送入设置在下部的后反应室中;以及在该混合室中提供在各喷嘴之下基本同心排列的通流管,其中通流管提供在通流管之内的降液管和在通流管之外的升气管,从而使通过喷嘴注入的甲醛源和异丁烯在降液管中通常向下移动,包含甲醛和/或异丁烯和/或异戊烯醇的流体则在升气管中在通常向上的方向上转向,并且使该流体与注入的甲醛源和异丁烯返混。该方法允许以高选择性和高产率得到异戊烯醇。本发明还涉及一种反应器,包括:垂直放置的容器,侧壁,上部和下部,将设置在上部的反应器混合室和设置在下部的后反应室分隔的多孔板;多个将流体以基本向下的方向注入该混合室中的喷嘴;在该混合室中的各喷嘴之下基本同心排列的通流管,其中通流管提供在通流管之内的降液管和在通流管之外的升气管,从而使通过喷嘴注入的流体在降液管中通常向下移动,已反应流体则在升气管中在通常向上的方向上转向,并且使该流体与注入的流体返混;和在后反应室中的流体出口。
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公开(公告)号:WO2021133975A1
公开(公告)日:2021-07-01
申请号:PCT/US2020/066945
申请日:2020-12-23
Applicant: SAUDI ARABIAN OIL COMPANY , ARAMCO SERVICES COMPANY
Inventor: CHOI, Ki-Hyouk , ALNASIR, Ali S. , SHAFEI, Emad N.
IPC: C10G9/36 , C10G11/20 , C10G11/05 , C10G21/00 , C10G31/08 , C10G51/06 , C10G55/06 , B01D3/06 , B01D3/10 , B01J19/245 , B01J3/008 , C10G21/003 , C10G2300/107 , C10G2300/1074 , C10G2300/1077 , C10G2300/202 , C10G2300/206 , C10G2300/308 , C10G2300/4006 , C10G2300/4012 , C10G2300/805 , C10G2400/02 , C10G2400/20 , C10G2400/22 , C10G55/00 , C10L1/06 , C10L2200/0423 , C10L2270/023 , C10L2290/543
Abstract: Embodiments of the disclosure provide a system and method for producing light olefins from a crude oil. A crude oil feed is introduced to a crude distillation unit to produce a distillate fraction and a residue fraction. The distillate fraction is introduced to a non-catalytic steam cracker to produce a light olefin fraction and a pyrolysis oil fraction. The residue fraction is introduced to a supercritical water reactor to produce an effluent stream. The effluent stream is introduced to a flash separator to produce a gas phase fraction and a liquid phase fraction. The gas phase fraction is introduced to a catalytic steam cracker to produce a light olefin fraction and a pyrolysis oil fraction. Optionally, the residue fraction is introduced to a vacuum distillation unit to produce a light vacuum gasoil fraction, a heavy vacuum gasoil fraction, and a vacuum residue fraction. The vacuum residue fraction is introduced to a solvent deasphalting unit to produce a deasphalted oil and a pitch fraction. The deasphalted oil fraction, optionally combined with the heavy vacuum gasoil fraction, can be introduced to the supercritical water reactor in lieu of the residue fraction.
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公开(公告)号:WO2021262657A1
公开(公告)日:2021-12-30
申请号:PCT/US2021/038383
申请日:2021-06-22
Applicant: SAUDI ARABIAN OIL COMPANY , ARAMCO SERVICES COMPANY
Inventor: CHOI, Ki-Hyouk , ALABDULHADI, Abdullah , LEE, Joo-Hyeong , ALSOMALI, Ali
IPC: C10G31/06 , C10G31/08 , C10G9/36 , B01J3/008 , C10G1/02 , C10G1/08 , C10G2300/1085 , C10G2300/1092 , C10G2300/4012 , C10G2300/805 , C10G2400/20 , C10G2400/30
Abstract: A process for producing olefins comprising the steps of separating the liquid oil in the fractionator to produce a light oil product; separating the light oil product in the extractor to produce a paraffin fraction stream; increasing a pressure of the paraffin fraction stream in a paraffin pump to produce a pressurized paraffin stream; mixing the pressurized paraffin stream with a pressurized water feed in the water mixer to produce a paraffin-containing water stream; heating the paraffin-containing water stream in the water heater to produce a hot paraffin-water stream, wherein a temperature of the hot paraffin-water stream is greater than 450 deg C, wherein the short chain paraffins are operable to crack at the temperature of the hot paraffin- water stream; mixing the hot paraffin-water stream and the hot feedstock in the feed mixer to produce a mixed feed stream; and introducing the mixed feed stream to the supercritical unit.
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公开(公告)号:WO2020127957A2
公开(公告)日:2020-06-25
申请号:PCT/EP2019/086659
申请日:2019-12-20
Applicant: UHDE HIGH PRESSURE TECHNOLOGIES GMBH , THYSSENKRUPP AG
Inventor: STEINHAGEN, Volkmar , HERBER, Ansgar
IPC: B01D11/02 , B01J3/00 , B01J13/00 , C08J11/08 , A23F5/24 , B01D11/0203 , B01D11/0207 , B01D11/0219 , B01D11/0226 , B01D11/0234 , B01D11/0238 , B01D11/0242 , B01D11/0246 , B01D11/0253 , B01D11/0257 , B01D11/028 , B01D11/0284 , B01D11/0288 , B01J13/0091 , B01J19/20 , B01J3/008 , B01J8/10 , C12C3/10
Abstract: Die Erfindung betrifft ein Verfahren zum Hochdruckbehandeln von Schüttgut (1) durch Extrahieren und/oder Imprägnieren, welches Schüttgut im Hochdruckbehandlungsvolumen (Vi) einer Druckbehältervorrichtung (20) angeordnet wird und auf einem Hochdruckniveau behandelt wird, insbesondere Hochdruck im Bereich von 40 bis 1000bar, wobei das Verfahren wenigstens die drei folgenden jeweils individuell regelbaren Schrittfolgen umfasst: Druckbeaufschlagung (V1), Hochdruckbehandlung (V2), Entspannung (V3); wobei die Hochdruckbehandlung (V2) auf kontinuierliche Weise im Hochdruckbehandlungsvolumen (Vi) durchgeführt wird, wobei das Hochdruckbehandlungsvolumen (Vi) oder die gesamte Druckbehältervorrichtung (20) während der Hochdruckbehandlung (V2) ortsfest angeordnet ist, und wobei die Kontinuität der Hochdruckbehandlung (V2) allein mittels des einen Hochdruckbehandlungsvolumens (Vi) sichergestellt wird, und wobei das Schüttgut mittels einer rotatorischen Stellbewegung oder in Abhängigkeit von wenigstens einer translatorischen Stellbewegung während der Hochdruckbehandlung durch das Hochdruckbehandlungsvolumen gefördert wird. Dies ermöglicht insbesondere eine prozesstechnische Optimierung von Hochdruckbehandlungsvorgängen wie z.B. der Extraktion. Ferner betrifft die Erfindung eine entsprechende Vorrichtung zum Hochdruckbehandeln von Schüttgut.
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公开(公告)号:WO2021262584A1
公开(公告)日:2021-12-30
申请号:PCT/US2021/038212
申请日:2021-06-21
Applicant: SAUDI ARABIAN OIL COMPANY , ARAMCO SERVICES COMPANY
Inventor: CHOI, Ki-Hyouk , ALNASIR, Ali , SHAFEI, Emad
IPC: C10G31/08 , B01D17/02 , B01D3/06 , B01D5/006 , B01J19/0013 , B01J2219/00159 , B01J2219/00162 , B01J3/008 , C07C2/06 , C07C2/42 , C10G2400/30 , C10G49/08 , C10G49/18
Abstract: A process to produce aromatic compounds in a heavy oil product stream comprising the steps of separating the depressurized effluent to produce a vapor product stream and a liquid product stream, reducing a temperature of the vapor product stream to produce a cooled vapor product, separating the cooled vapor product to produce a light oil stream, wherein the light oil stream comprises olefins, separating the light oil stream to produce a light oil slip stream and a light stream, mixing the light stream with a water feed stream to produce an olefin-containing water stream, increasing a pressure of the olefin-containing water stream to produce a pressurized water feed, increasing a temperature of the pressurized water feed to produce a hot water feed, wherein a temperature of the hot water feed is greater than 450 °C, converting olefins to aromatic compounds in the hot water feed.
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公开(公告)号:WO2020049111A1
公开(公告)日:2020-03-12
申请号:PCT/EP2019/073723
申请日:2019-09-05
Applicant: BASF SE
Inventor: LOEFFLER, Ralf Dirk , HEIDEBRECHT, Peter , WOELFERT, Andreas , HOFINGER, Julia , KUNKELMANN, Christian , SEEBER, Georg
IPC: C07C29/38 , C07C33/025 , B01J3/008 , B01J4/002 , B01J19/26
Abstract: A process for producing isoprenol, comprising: mixing and injecting a formaldehyde source and isobutylene into a reactor through a plurality of nozzles operated in parallel and reacting the formaldehyde source and isobutylene under supercritical conditions; wherein the reactor comprises a vertically disposed vessel, a sidewall, an upper portion and a lower portion; and wherein the formaldehyde source and isobutylene are injected into a mixing chamber of the reactor disposed in the upper portion and a fluid comprising formaldehyde and/or isobutylene and/or isoprenol is passed from the mixing chamber into a post-reaction chamber disposed in the lower portion; and providing draft tubes arranged essentially concentrically underneath each of the nozzles in the mixing chamber, the draft tubes providing downcomer conduits within the draft tubes and a riser conduit outside of the draft tubes, so that the formaldehyde source and isobutylene injected through the nozzles travel generally downward in the downcomer conduits, a fluid comprising formaldehyde and/or isobutylene and/or isoprenol is then diverted in a generally upward direction in the riser conduit, and the fluid is back-mixed with the injected formaldehyde source and isobutylene. The process allows for isoprenol to be obtained with high selectivity and in high yields. The invention also relates to a reactor comprising: a vertically disposed vessel, a sidewall, an upper portion and a lower portion, a perforated plate separating a mixing chamber of the reactor disposed in the upper portion and a post-reaction chamber disposed in the lower portion; a plurality of nozzles for injecting a fluid into the mixing chamber in an essentially downward direction; draft tubes arranged essentially concentrically underneath each of the nozzles in the mixing chamber, the draft tubes providing downcomer conduits within the draft tubes and a riser conduit outside of the draft tubes, so that the fluid injected through the nozzles travels generally downward in the downcomer conduits, a reacted fluid is then diverted in a generally upward direction in the riser conduit, and the fluid is back-mixed with the injected fluid; and a fluid outlet in the post-reaction chamber.
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公开(公告)号:WO2021150687A1
公开(公告)日:2021-07-29
申请号:PCT/US2021/014323
申请日:2021-01-21
Applicant: SAUDI ARABIAN OIL COMPANY , ARAMCO SERVICES COMPANY
Inventor: YOUNES, Mourad , JAMAL, Aqil
IPC: C10G27/12 , C10G19/02 , C10G31/10 , C10G31/08 , C10G31/06 , C10G27/14 , B01D9/00 , B01D11/0403 , B01D11/0488 , B01D17/0208 , B01D9/0059 , B01J19/0006 , B01J19/0013 , B01J19/2445 , B01J19/245 , B01J2219/00038 , B01J2219/0004 , B01J2219/00103 , B01J2219/00159 , B01J2219/00162 , B01J3/008 , C10G2300/202 , C10G2300/207 , C10G2300/4006 , C10G2300/4012 , C10G2300/405 , C10G2300/70 , C10G2300/805 , C10G53/02 , C10G53/14
Abstract: The present application provides systems and methods for upgrading an oil stream. The system includes a reactor, a phase separator, an expansion device, a cooling unit, and two separation units. The reactor receives the oil stream, ammonia, and supercritical water, The supercritical water upgrades the oil stream, and the ammonia reacts with sulfur initially present in the oil stream to produce ammonia-sultur compounds. The phase separator receives a mixture stream comprising the upgraded oil stream, supercritical water, and the ammonia-sulfur compounds, and separates out non-dissolved components. The expansion device reduces the pressure of the mixture stream below a water critical pressure. The cooling unit reduces the temperature of the mixture stream. A first separation unit separates the mixture stream it into a hydrocarbon-rich gaseous phase, a water stream containing ammonia-sulfur compounds, and a treated oil stream. A second separation unit separates the ammonia-sulfur compounds from the water stream.
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公开(公告)号:WO2021123695A1
公开(公告)日:2021-06-24
申请号:PCT/FR2020/052574
申请日:2020-12-18
Applicant: SYCTOM L'AGENCE METROPOLITAINE DES DECHETS MENAGERS , SYNDICAT INTERDEPARTEMENTAL POUR L'ASSAINISSEMENT DE L'AGGLOMERATION PARISIENNE
Inventor: CHATAING, Thierry , MINVIELLE, Zoé , CIGNA, Julien
IPC: B01J3/00 , B09B3/00 , C02F11/08 , B08B9/027 , C01B3/36 , B01J2219/00252 , B01J3/008 , B09B3/0083 , B09B5/00 , C02F11/04 , C02F11/086
Abstract: L'invention concerne un réacteur (1) échangeur thermique qui comprend : - une chambre réactive (10) qui loge des tubes chauds (14C) d'un conduit de circulation (14), les tubes chauds (14C) comprenant au niveau de leur extrémité haute (14H) une ouverture haute (15H) en regard d'un passage traversant (IIP) ménagé dans une section supérieure (11) de la chambre réactive (10); - une chambre haute (16) maintenue à une pression Ps supérieure à la pression Pi, disposée contre la section supérieure (11), et à partir de laquelle des écouvillons (18) maintenus solidairement les uns aux autres traversent chacun un des passages traversant (IIP), chaque écouvillon (18) étant associé à un des tubes chauds (14C) et est agencé pour effectuer un mouvement entre une position haute et une position basse dans le tube chaud auquel il est associé afin d'en racler la paroi interne.
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