| 序号 | 专利名 | 申请号 | 申请日 | 公开（公告）号 | 公开（公告）日 | 发明人 |
|---|---|---|---|---|---|---|
| 21 | 単環芳香族炭化水素の製造方法 | JP2011067690 | 2011-03-25 | JP5646381B2 | 2014-12-24 | 柳川 真一朗; 真一朗 柳川; 領二 伊田; 泰之 岩佐; 小林 正英; 正英 小林; 進 安井; 宜重 杉; 敦 福井; 篤郎 南雲 |
| 22 | Process for the production of diesel and aromatic compounds | JP2010514741 | 2007-07-06 | JP2010532753A | 2010-10-14 | タッカー，ヴァサント・ピー; フレイ，スタンレー・ジェイ |
| 低硫黄ディーゼルおよび芳香族化合物の生産のための方法であって、Ｃ
９ ＋炭化水素を水素化分解して低硫黄ディーゼルおよびナフサ沸騰範囲の流れを生成し、それを統合トランスアルキル化区画においてトランスアルキル化してキシレンを生成する方法。
【選択図】 無し |
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| 23 | Method for producing hydrocrackate, method for treating plastic and method for producing benzene | JP2006294307 | 2006-10-30 | JP2007332345A | 2007-12-27 | TAKENAKA JOICHI; NOBUSAWA TATSUYA; MIYAZAWA KUNIO; MATSUO KAZUYOSHI; YAMAKI TOSHIO |
| <P>PROBLEM TO BE SOLVED: To provide a method for producing a hydrocrackate which can produce the hydrocrackate containing benzenes but no chlorine from chlorine-containing plastics and, even when the plastics and a used solvent contain N, S and the like, the hydrocrackate containing none of them. <P>SOLUTION: The method for producing the hydrocrackate comprises a dissolution process for preparing a plastic solution by heating a mixture comprising chlorine, plastics and a solvent and dissolving the plastics, a first hydrocracking process for preparing a first hydrocrackate by carrying out a hydrocracking reaction by reacting the plastic solution with hydrogen in the presence of a first catalyst, a chlorine fixing/removing process for fixing and/or removing chlorine included in the first hydrocrackate by chlorine fixing means and/or chlorine removing means, and a second hydrocracking process for preparing a second hydrocrackate containing no chlorine by reacting the afore-described product with hydrogen in the presence of a second catalyst. <P>COPYRIGHT: (C)2008,JPO&INPIT | ||||||
| 24 | Catalytic oxygenolysis of polynuclear aromatic hydrocarbons | JP4032482 | 1982-03-16 | JPS57159727A | 1982-10-01 | DAAKU TEII EI FUIBAASU; ROBAATO BAAKUREI JIYUNIA; RAJIYUNI SHII SHIYAA |
| 25 | HYDROCRACKING CATALYST FOR PREPARING VALUABLE LIGHT AROMATIC HYDROCARBONS FROM POLYCYCLIC AROMATIC HYDROCARBONS | EP11834653.5 | 2011-10-21 | EP2629888A4 | 2015-02-25 | KIM, Do Woan; KOH, Jae Hyun; LEE, Sang Il; LEE, Seung Woo; OH, Seung Hoon; KOH, Jae Suk; KIM, Yong Seung; KIM, Gyung Rok; CHOI, Sun; KIM, Hong Chan; OH, Sang Hun |
| 26 | 다환식 방향족 화합물로부터 ＢＴＸ 함유 단일 고리 방향족 화합물의 전환 방법 | KR1020150033643 | 2015-03-11 | KR1020160110711A | 2016-09-22 | 이동근; 김지예; 최선; 장호식; 이진석; 이용걸; 조계성 |
| 본발명은 PFO(pyrolysis fuel oil) 및 LCO(light cycle oil)를포함하는다환방향족화합물이다량존재하는유분으로부터수소화분해촉매의존재하에서부분수소화및 수첨분해공정을통하여단일고리방향족탄화수소를정제하는방법에관한것이다. 본발명에따르면 PFO 및 LCO를원료로사용하여고부가가치의방향족화합물을제품으로생산할수 있는방향족제품의제조방법을제공할수 있다. 또한, 본발명에따르면다환방향족유분의성상(S, N, 방향족함량)에따라수첨탈황/탈질공정및 수첨분해반응공정의조건을달리하여높은수율의방향족제품의제조방법을제공할수 있다. 아울러, 본발명은수첨탈황/탈질및 분해반응효과가뛰어난저유황, 저질소, 저공해의고부가가치의방향족제품의제조방법을제공할수 있다. | ||||||
| 27 | 単環芳香族炭化水素製造用触媒および単環芳香族炭化水素の製造方法 | JP2016019280 | 2016-02-03 | JP6147376B2 | 2017-06-14 | 柳川 真一朗; 小林 正英; 早坂 和章 |
| 28 | 単環芳香族炭化水素製造用触媒および単環芳香族炭化水素の製造方法 | JP2014239361 | 2014-11-26 | JP5813853B2 | 2015-11-17 | 柳川 真一朗; 小林 正英; 岩佐 泰之; 伊田 領二 |
| 29 | Process for the recovery of xylenes | JP2010514741 | 2007-07-06 | JP5227402B2 | 2013-07-03 | フレイ，スタンレー・ジェイ; タッカー，ヴァサント・ピー |
| 30 | 単環芳香族炭化水素製造用触媒および単環芳香族炭化水素の製造方法 | JP2011505307 | 2011-01-20 | JPWO2011090121A1 | 2013-05-23 | 柳川 真一朗; 真一朗 柳川; 小林 正英; 正英 小林; 和章 早坂 |
| この単環芳香族炭化水素製造用触媒は、10容量%留出温度が140℃以上かつ90容量%留出温度が380℃以下である原料油から炭素数6〜8の単環芳香族炭化水素を製造するための単環芳香族炭化水素製造用触媒であって、12員環の骨格構造を有する大細孔ゼオライトと10員環の骨格構造を有する中細孔ゼオライトとを含む結晶性アルミノシリケートを含有する。 | ||||||
| 31 | Method for producing monocyclic aromatic hydrocarbon | JP2011067690 | 2011-03-25 | JP2012201795A | 2012-10-22 | YANAGAWA SHINICHIRO; IDA RYOJI; IWASA YASUYUKI; KOBAYASHI MASAHIDE; YASUI SUSUMU; SUGI YOSHISHIGE; FUKUI ATSUSHI; NAGUMO ATSUO |
| PROBLEM TO BE SOLVED: To provide a method for producing a monocyclic aromatic hydrocarbon capable of suppressing extreme heat generation upon hydrogenation reaction and avoiding increase of equipment cost of a hydrogenation reactor.SOLUTION: The method for producing the monocyclic aromatic hydrocarbon having 6-8 carbon atoms has a breakdown/modification reaction step of bringing a starting material oil into reactive contact with a catalyst to obtain a product containing the monocyclic aromatic hydrocarbon, a purification/collection step of purifying and collecting monocyclic aromatic hydrocarbon isolated from the product generated in the breakdown/modification step, a hydrogenation reaction step of hydrogenating a heavy fraction isolated from the product generated in the breakdown/modification step, a dilution step of returning a portion of a hydrogenated product of the heavy fraction obtained in the hydrogenation reaction step to the hydrogenation reaction step as a dilution oil, and a recycling step of returning the hydrogenated product of the heavy fraction obtained in the hydrogenation reaction step to the breakdown/modification reaction step. | ||||||
| 32 | Method for producing monocyclic aromatic hydrocarbon | JP2010294186 | 2010-12-28 | JP2012140371A | 2012-07-26 | YANAGAWA SHINICHIRO; KOBAYASHI MASAHIDE; IWASA YASUYUKI; IDA RYOJI |
| PROBLEM TO BE SOLVED: To provide a method for producing 6-8C monocyclic aromatic hydrocarbon from raw oil containing polycyclic aromatic hydrocarbon.SOLUTION: In this method for producing monocyclic aromatic hydrocarbon, the raw oil, 10% by volume of which has been distilled at 140°C or higher and 90% by volume of which has been distilled at 380°C or lower, is brought into contact with a catalyst for producing monocyclic aromatic hydrocarbon made of a mixture of a first catalyst containing crystalline aluminosilicate containing gallium and/or zinc and phosphorus, and a second catalyst containing crystalline aluminosilicate containing phosphorus. | ||||||
| 33 | Catalyst for producing monocyclic aromatic hydrocarbon and method of producing the monocyclic aromatic hydrocarbon | JP2010294185 | 2010-12-28 | JP2012139640A | 2012-07-26 | YANAGAWA SHINICHIRO; KOBAYASHI MASAHIDE; IWASA YASUYUKI; IDA RYOJI |
| PROBLEM TO BE SOLVED: To provide a catalyst for producing monocyclic aromatic hydrocarbon and a method of producing the monocyclic aromatic hydrocarbon, which can produce 6-8C monocyclic aromatic hydrocarbon at a high yield from raw oil including polycyclic aromatic hydrocarbon and can prevent temporal decline in a yield of the 6-8C monocyclic aromatic hydrocarbon.SOLUTION: The catalyst for producing monocyclic aromatic hydrocarbon is used for producing 6-8C monocyclic aromatic hydrocarbon from raw oil having 140°C or higher of 10 vol.% distillation temperature and 380°C or lower of 90 vol.% distillation temperature, and includes crystalline aluminosilicate and phosphorus. A molar ratio (P/Al ratio) between phosphorus included in the crystalline aluminosilicate and aluminum of the crystalline aluminosilicate is set to be 0.1 or more and 1.0 or less. In the method of producing the monocyclic aromatic hydrocarbon, the raw oil having 140°C or higher of 10 vol.% distillation temperature and 380°C or lower of 90 vol.% distillation temperature is brought into contact with the catalyst for producing monocyclic aromatic hydrocarbon. | ||||||
| 34 | Production of monocyclic aromatic-containing hydrocarbon | JP13480889 | 1989-05-30 | JPH032128A | 1991-01-08 | KANAI JUNICHI; MASUNAGA HIROJI |
| PURPOSE: To efficiently obtain the subject compound useful as a raw material for substrate for high-octane gasolines or pertrochemicals, such as benzene or toluene, in high yield by reacting a polycyclic aromatic-containing hydrocarbon using a specific catalyst. CONSTITUTION: A polycyclic aromatic-containing hydrocarbon is reacted in the presence or absence of hydrogen gas in the presence of a catalyst containing Ga or Zn and zeolite having 1-12 value of control index [CI=log 10 (residual content of n-hexane)/log 10 (residual content of 3-methylpentane)] or in the coexistence of an inert gas, such as nitrogen gas, at 350-700°C, preferably 450-600°C to afford the objective compound. Especially preferred reaction conditions are a temperature within the range of 450-600°C and the molar ratio of the H fed to the reaction system to the polycyclic aromatic-containing hydrocarbon within the range of ≥0 to ≤1. Furthermore, the aforementioned catalyst is prepared by a method for ion exchange, etc., using a Ca- or Zn-containing compound together with the zeolite. COPYRIGHT: (C)1991,JPO&Japio | ||||||
| 35 | JPS536140B2 - | JP6922173 | 1973-06-21 | JPS536140B2 | 1978-03-04 | |
| 36 | HYDROCRACKING CATALYST FOR PREPARING VALUABLE LIGHT AROMATIC HYDROCARBONS FROM POLYCYCLIC AROMATIC HYDROCARBONS | PCT/KR2011/007877 | 2011-10-21 | WO2012053853A3 | 2012-04-26 | KIM, Do Woan; KOH, Jae Hyun; LEE, Sang Il; LEE, Seung Woo; OH, Seung Hoon; KOH, Jae Suk; KIM, Yong Seung; KIM, Gyung Rok; CHOI, Sun; KIM, Hong Chan; OH, Sang Hun |
This invention relates to a hydrocracking catalyst for preparing valuable light aromatic hydrocarbons from polycyclic aromatic hydrocarbons derived from oil, which includes (i) beta-zeolite, (ii) pseudo-boehmite, and (iii) one or more metals selected from among metals of Groups VIII and VIB, and which further includes a cocatalyst component, thereby producing a maximum amount of BTX (Benzene, Toluene, Xylene) from LCO (Light Cycle Oil). |
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| 37 | MODIFIED PT/RU CATALYST FOR RING OPENING AND PROCESS USING THE CATALYST | PCT/US2006/038700 | 2006-10-02 | WO2007041605A1 | 2007-04-12 | XU, Feng; BAUER, Lorenz, J.; GILLESPIE, Ralph, D.; BRICKER, Maureen, L.; BRADLEY, Steven, A. |
A catalyst for opening naphthenic rings has been developed. The catalyst comprises ruthenium and platinum as the active catalytic metals and a modifier with cerium being a preferred modifier. At least 50% of the platinum and ruthenium components are present as particles wherein more ruthenium is present on the surface of the particles than in the center. All of these components are dispersed on a metal oxide support such as aluminas. A ring opening process using the catalyst is also described. |
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| 38 | INHIBITORS OF AMINO ACID TRANSPORT | PCT/US2021071989 | 2021-10-22 | WO2022087630A1 | 2022-04-28 | GREWER CHRISTOF; SCHLESSINGER AVNER; NDARU ELIAS; SHI YUEYUE; ZIELEWICZ LAURA JANE |
| Disclosed herein are compounds and compositions of formula (I) that are inhibitors of amino acid transport, specifically alanine serine cysteine transporter 2 (ASCT2): These compounds are useful as therapeutic agents for treating various cancers. Methods for inhibiting an ASCT2 transporter are also disclosed. Certain compounds are selective for an ASCT transporter. | ||||||
| 39 | LOW-SULFUR AROMATIC-RICH FUEL OIL BLENDING COMPONENT | PCT/US2020/048517 | 2020-08-28 | WO2021041890A1 | 2021-03-04 | HODGKINS, Robert Peter; KOSEOGLU, Omer Refa |
A method for making a fuel oil blend comprising the steps of: supplying an aromatic bottoms; supplying an aromatic blending component from the aromatic bottoms; blending the aromatic blending component with bulk fuel oil components to produce a fuel oil blend; wherein the bulk fuel oil components comprise a hydrocarbon component selected from the group consisting of: vacuum residue oil, light gas oil, kerosene, fluid catalytic cracking decant oil (FCC DCO), visbroken residues, delayed coking liquids, and combinations of the same. |
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| 40 | PROCESS FOR RECOVERY OF LIGHT ALKYL MONO-AROMATIC COMPOUNDS FROM HEAVY ALKYL AROMATIC AND ALKYL-BRIDGED NON-CONDENSED ALKYL AROMATIC COMPOUNDS | SG11201906825U | 2018-02-16 | SG11201906825UA | 2019-08-27 | BEADLE BRUCE; RAMASESHAN VINOD; BILAUS RAKAN; KOSEOGLU OMER; HODGKINS ROBERT |
| hi — Supplying. to the reactor a hydrogen stream , 114 110 Feeding, to the reactor, a recycled hydrocarbon stream containing unreacted alkyl bridged non-condensed alkyl aromatic compounds Feeding the hydrocarbon product to a separation zone to separate the hydrocarbon I r 112 product into a lighter hydrocarbon stream and a heavier hydrocarbon stream Feeding the heavier hydrocarbon stream to a fractionation zone for fractionating into two or more streams Supplying, to a reactor, a hydrocarbon feedstock including a plurality of alkyl Er 102 bridged non-condensed alkyl aromatic compounds. r Recovering, from the reactor, a hydrocarbon product including the alkyl E 108 mono-aromatic compounds Allowing, in the reactor using a catalyst and the hydrogen, cleavage of the alkyl — 106 bridges of the alkyl-bridged non-condensed alkyl aromatic compounds to produce alkyl mono-aromatic compounds 00 00 O O (12) INTERNATIONAL APPLICATION PUBLISHED UNDER THE PATENT COOPERATION TREATY (PCT) (19) World Intellectual Property Organization International Bureau (43) International Publication Date 23 August 2018 (23.08.2018) WIP0 I PCT mu °million °nolo moncill oil Eno iflo oimIE (10) International Publication Number WO 2018/152389 Al (51) International Patent Classification: C07C 4/26 (2006.01) C07C 15/08 (2006.01) CO7C 15/00 (2006.01) (21) International Application Number: PCT/US2018/018471 (22) International Filing Date: 16 February 2018 (16.02.2018) (25) Filing Language: English (26) Publication Language: English (30) Priority Data: 15/435,039 16 February 2017 (16.02.2017) US (71) Applicant: SAUDI ARABIAN OIL COMPANY [SA/SA]; 1 Eastern Avenue, Dhahran, 31311 (SA). (71) Applicant (for AG only): ARAMCO SERVICES COM- PANY [US/US]; 9009 West Loop South, Houston, TX 77096 (Us). (72) Inventors: BEADLE, Bruce, Richard; Saudi Aramco, P.O. Box 10822, Dhahran, 31311 (SA). RAMASESHAN, Vinod; Saudi Aramco Box 1256, Najmah, Ras Tanura, 31311 (SA). BILAUS, Rakan, Sulaiman; Saudi Aramco Box 19887, Dhahran, 31311 (SA). KOSEOGLU, Omer, R.; Saudi Arabian Oil Company, P.O. Box 8560, Dhahran, 31311 (SA). HODGKINS, Robert, P.; Saudi Arabian Oil Company, P.o. Box 10981, Dhahran, 31311 (SA). (74) Agent: RHEBERGEN, Constance, Gall; Bracewell LLP, P.O. Box 61389, Houston, TX 77208-1389 (US). (81) Designated States (unless otherwise indicated, for every kind of national protection available): AE, AG, AL, AM, AO, AT, AU, AZ, BA, BB, BG, BH, BN, BR, BW, BY, BZ, (54) Title: PROCESS FOR RECOVERY OF LIGHT ALKYL MONO-AROMATIC COMPOUNDS FROM HEAVY ALKYL ARO- MATIC AND ALKYL-BRIDGED NON-CONDENSED ALKYL AROMATIC COMPOUNDS 100 FIG. 1 (57) : Embodiments in the present disclosure describe a process for recovery of lighter mono-aromatic compounds from a stream containing alkyl bridged non-condensed alkyl multi-aromatic compounds by conversion to non-condensed alkyl mono-aromatic compounds. The process includes supplying, to a reactor, a hydrocarbon feedstock containing alkyl bridged non-condensed alkyl aro- matic compounds and a hydrogen stream. The process further includes allowing the alkyl-bridged non-condensed alkyl multi-aromatic compounds to react with hydrogen in the presence of a suitable catalyst to produce alkyl mono-aromatic compounds. The process may include processing the alkyl mono-aromatic compounds to produce valuable products, such as para-xylene. Various other embodiments are disclosed and claimed [Continued on next page] WO 2018/152389 Al MIDEDIMOMOIDEIREEMOMMIMMOMEHOMEEN CA, CH, CL, CN, CO, CR, CU, CZ, DE, DJ, DK, DM, DO, DZ, EC, EE, EG, ES, FI, GB, GD, GE, GH, GM, GT, HN, HR, HU, ID, IL, IN, IR, IS, JO, JP, KE, KG, KH, KN, KP, KR, KW, KZ, LA, LC, LK, LR, LS, LU, LY, MA, MD, ME, MG, MK, MN, MW, MX, MY, MZ, NA, NG, NI, NO, NZ, OM, PA, PE, PG, PH, PL, PT, QA, RO, RS, RU, RW, SA, SC, SD, SE, SG, SK, SL, SM, ST, SV, SY, TH, TJ, TM, TN, TR, TT, TZ, UA, UG, US, UZ, VC, VN, ZA, ZM, ZW. (84) Designated States (unless otherwise indicated, for every kind of regional protection available): ARIPO (BW, GH, GM, KE, LR, LS, MW, MZ, NA, RW, SD, SL, ST, SZ, TZ, UG, ZM, ZW), Eurasian (AM, AZ, BY, KG, KZ, RU, TJ, TM), European (AL, AT, BE, BG, CH, CY, CZ, DE, DK, EE, ES, FI, FR, GB, GR, HR, HU, IE, IS, IT, LT, LU, LV, MC, MK, MT, NL, NO, PL, PT, RO, RS, SE, SI, SK, SM, TR), OAPI (BF, BJ, CF, CG, CI, CM, GA, GN, GQ, GW, KM, ML, MR, NE, SN, TD, TG). Published: — with international search report (Art. 21(3)) | ||||||
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