JPH10509730A - Mcm−49を用いる富ベンゼン改質油のアルキル化方法 - Google Patents
Mcm−49を用いる富ベンゼン改質油のアルキル化方法Info
- Publication number
- JPH10509730A JPH10509730A JP8517611A JP51761196A JPH10509730A JP H10509730 A JPH10509730 A JP H10509730A JP 8517611 A JP8517611 A JP 8517611A JP 51761196 A JP51761196 A JP 51761196A JP H10509730 A JPH10509730 A JP H10509730A
- Authority
- JP
- Japan
- Prior art keywords
- benzene
- stream
- catalyst
- olefin
- reformate
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J29/00—Catalysts comprising molecular sieves
- B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
- B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
- B01J29/70—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of types characterised by their specific structure not provided for in groups B01J29/08 - B01J29/65
- B01J29/7049—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of types characterised by their specific structure not provided for in groups B01J29/08 - B01J29/65 containing rare earth elements, titanium, zirconium, hafnium, zinc, cadmium, mercury, gallium, indium, thallium, tin or lead
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J29/00—Catalysts comprising molecular sieves
- B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
- B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
- B01J29/70—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of types characterised by their specific structure not provided for in groups B01J29/08 - B01J29/65
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B39/00—Compounds having molecular sieve and base-exchange properties, e.g. crystalline zeolites; Their preparation; After-treatment, e.g. ion-exchange or dealumination
- C01B39/02—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof; Direct preparation thereof; Preparation thereof starting from a reaction mixture containing a crystalline zeolite of another type, or from preformed reactants; After-treatment thereof
- C01B39/06—Preparation of isomorphous zeolites characterised by measures to replace the aluminium or silicon atoms in the lattice framework by atoms of other elements, i.e. by direct or secondary synthesis
- C01B39/065—Galloaluminosilicates; Group IVB- metalloaluminosilicates; Ferroaluminosilicates
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B39/00—Compounds having molecular sieve and base-exchange properties, e.g. crystalline zeolites; Their preparation; After-treatment, e.g. ion-exchange or dealumination
- C01B39/02—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof; Direct preparation thereof; Preparation thereof starting from a reaction mixture containing a crystalline zeolite of another type, or from preformed reactants; After-treatment thereof
- C01B39/46—Other types characterised by their X-ray diffraction pattern and their defined composition
- C01B39/48—Other types characterised by their X-ray diffraction pattern and their defined composition using at least one organic template directing agent
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G29/00—Refining of hydrocarbon oils, in the absence of hydrogen, with other chemicals
- C10G29/20—Organic compounds not containing metal atoms
- C10G29/205—Organic compounds not containing metal atoms by reaction with hydrocarbons added to the hydrocarbon oil
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G50/00—Production of liquid hydrocarbon mixtures from lower carbon number hydrocarbons, e.g. by oligomerisation
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G59/00—Treatment of naphtha by two or more reforming processes only or by at least one reforming process and at least one process which does not substantially change the boiling range of the naphtha
- C10G59/02—Treatment of naphtha by two or more reforming processes only or by at least one reforming process and at least one process which does not substantially change the boiling range of the naphtha plural serial stages only
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2229/00—Aspects of molecular sieve catalysts not covered by B01J29/00
- B01J2229/10—After treatment, characterised by the effect to be obtained
- B01J2229/26—After treatment, characterised by the effect to be obtained to stabilize the total catalyst structure
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2229/00—Aspects of molecular sieve catalysts not covered by B01J29/00
- B01J2229/30—After treatment, characterised by the means used
- B01J2229/36—Steaming
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2229/00—Aspects of molecular sieve catalysts not covered by B01J29/00
- B01J2229/30—After treatment, characterised by the means used
- B01J2229/42—Addition of matrix or binder particles
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geology (AREA)
- Life Sciences & Earth Sciences (AREA)
- Materials Engineering (AREA)
- General Chemical & Material Sciences (AREA)
- Crystallography & Structural Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
Description
Claims (1)
- 【特許請求の範囲】 1.ベンゼン含有フィードストリームをアルキル化する方法であって、活性型 の合成多孔質結晶性MCM−49を含んでなる触媒の存在下、十分な反応条件に て、フィードストリームを、C2-C5オレフィンを含む炭化水素ストリームに接 触させることによって、アルキル化ベンゼン生成物を含む流出ストリームを生成 させることを含んでなる方法。 2.C2-C5オレフィンを含む炭化水素ストリームが改質FCCプロパン/プ ロピレンストリームであり、ベンゼン含有フィードストリームがベンゼン、トル エン及びキシレンを含有する改質油であり、アルキル化ベンゼン生成物がクメン を含んでなる請求の範囲1記載の方法。 3.ベンゼン、トルエン、キシレン及びエチルベンゼンを含有する改質油フィ ードストリームをアルキル化する方法であって、 1)活性型の合成多孔質結晶性MCM−49を含んでなる触媒の存在下、ベン ゼンアルキル化条件にて、改質油フィードストリームを、C2-C5オレフィンを 含んでなる炭化水素ストリームに接触させることによって、ベンゼン含量がフィ ードストリームにおける値の少なくとも50重量%を下回り、オクタン価がフィ ードストリームにおける値を下回らず、全液体物質がフィードストリームよりも 多い流出ストリームを生成させること、並びに 2)流出ストリームのガソリン沸点範囲フラクションを回収すること を含んでなる方法。 4.アルキル化条件が、150℃〜350℃の温度、450〜7000kPa(5 0〜1000psig)の圧力、0.1〜0.9のベンゼン対オレフィンモル比、0.1 〜10の芳香族炭化水素化合物対オレフィンモル比及び0.1hr-1〜500hr-1 のフィードWHSVを含んでなり、改質油が全範囲改質油である請求の範囲3記 載の方法。 5.C2-C5オレフィンを含有する炭化水素ストリームが少なくとも30重量 %のプロピレンを含んでおり、ベンゼンアルキル化条件が200℃〜300℃の 温度、790〜3550kPa(100〜500psig)の圧力、及び0.5hr-1〜約 100hr-1の範囲の重量時間空間速度を含んでなる請求の範囲3記載の方法。 6.C2-C5オレフィンを含有する炭化水素ストリームが少なくとも40重量 %のプロピレンを含み、改質油フィードストリームが全範囲改質油(C5〜23 2℃(450°F))である請求の範囲5記載の方法。 7.触媒床が固定床を含んでなる請求の範囲3記載の方法。 8.合成多孔質結晶性MCM−49が、水素、水素前駆体、希土類金属、並び に周期表の第IIA族、第IIIA族、第IVA族、第IB族、第IIB族、第IIIB族、 第IVB族、第VIB及び第VIII族の金属からなる群から選ばれるカチオン又はカチ オン混合物によって、元々のカチオンを、少なくとも部分的に置換する処理が施 されたものである請求の範囲3記載の方法。 9.更に、 3)ガソリン沸点範囲フラクションを、非改質油ガソリン沸点範囲でないフラ クションと配合して、1容量%を越えないベンゼンを含有するガソリン沸点範囲 生成物を生成させること を含んでなる請求の範囲3記載の方法。 10.ベンゼン含有全範囲改質油フィード中のベンゼン含量を低減させる一方 で、オクタン価(RON)を少なくとも0.5上昇させる方法であって、 1)活性型の合成多孔質結晶性MCM−49を含んでなる触媒の存在下、21 5℃〜300℃の範囲の温度を含むベンゼンアルキル化条件にて、フィードを、 C2-C5オレフィンを含む炭化水素ストリームに接触させること、並びに 2)流出ストリームのガソリン沸点範囲フラクションを回収すること を含んでなる方法。
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US08/350,308 US5545788A (en) | 1991-06-19 | 1994-12-06 | Process for the alkylation of benzene-rich reformate using MCM-49 |
US350,308 | 1994-12-06 | ||
PCT/US1995/015137 WO1996017810A1 (en) | 1994-12-06 | 1995-11-21 | Process for the alkylation of benzene-rich reformate using mcm-49 |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH10509730A true JPH10509730A (ja) | 1998-09-22 |
JP3938934B2 JP3938934B2 (ja) | 2007-06-27 |
Family
ID=23376147
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP51761196A Expired - Lifetime JP3938934B2 (ja) | 1994-12-06 | 1995-11-21 | Mcm−49を用いる富ベンゼン改質油のアルキル化方法 |
Country Status (8)
Country | Link |
---|---|
US (1) | US5545788A (ja) |
EP (1) | EP0796234B1 (ja) |
JP (1) | JP3938934B2 (ja) |
KR (1) | KR100378141B1 (ja) |
AU (1) | AU687291B2 (ja) |
DE (1) | DE69519873T2 (ja) |
ES (1) | ES2156219T3 (ja) |
WO (1) | WO1996017810A1 (ja) |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2008535941A (ja) * | 2005-02-28 | 2008-09-04 | エクソンモービル リサーチ アンド エンジニアリング カンパニー | 気相芳香族アルキル化方法 |
JP2010515572A (ja) * | 2007-01-16 | 2010-05-13 | エクソンモービル・ケミカル・パテンツ・インク | 触媒組成物及び芳香族のアルキル化における該触媒組成物の使用 |
KR101116523B1 (ko) * | 2004-08-13 | 2012-02-28 | 엑손모빌 케미칼 패턴츠 인코포레이티드 | 페놀 및 메틸에틸케톤의 제조 방법 |
JP2012520376A (ja) * | 2009-03-13 | 2012-09-06 | エクソンモービル リサーチ アンド エンジニアリング カンパニー | 高いベンゼン転化率でのベンゼンアルキル化によるベンゼン含有率が低下したハイオクタン・ガソリンの製造方法 |
JP2013049695A (ja) * | 2012-10-26 | 2013-03-14 | Exxonmobile Chemical Patents Inc | 有機化合物変換方法 |
JP2014513152A (ja) * | 2011-02-07 | 2014-05-29 | バジャー・ライセンシング・エルエルシー | ガソリンのベンゼン含有量を低減する方法 |
JP2019534880A (ja) * | 2016-10-06 | 2019-12-05 | エクソンモービル・ケミカル・パテンツ・インク | ベンゼンおよび/またはトルエンのメチル化によるパラキシレン製造プロセス |
JP2019537563A (ja) * | 2016-10-06 | 2019-12-26 | エクソンモービル・ケミカル・パテンツ・インク | 芳香族炭化水素をメチル化するプロセス |
JP2020515605A (ja) * | 2017-03-29 | 2020-05-28 | エクソンモービル ケミカル パテンツ インコーポレイテッド | 炭化水素ストリームから不純物を除去する方法及び芳香族アルキル化プロセスにおけるそれらの使用 |
Families Citing this family (18)
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CA2355679A1 (en) * | 1998-12-29 | 2000-07-06 | Nick Allen Collins | Cetane upgrading via aromatic alkylation |
US6500996B1 (en) * | 1999-10-28 | 2002-12-31 | Exxonmobil Oil Corporation | Process for BTX purification |
US20020042548A1 (en) | 2001-07-11 | 2002-04-11 | Dandekar Ajit B. | Process for producing cumene |
AU2002353872B2 (en) | 2001-10-25 | 2007-05-17 | IFP Energies Nouvelles | Components for blending of transportation fuels |
ES2200702B1 (es) * | 2002-07-16 | 2005-05-01 | Univesidad Politecnica De Valencia | Catalizador conteniendo un material solido cristalino microporoso y proceso para mejorar la calidad de fracciones diesel utilizando dicho catalizador. |
US7517824B2 (en) * | 2005-12-06 | 2009-04-14 | Exxonmobil Chemical Company | Process for steam stripping hydrocarbons from a bromine index reduction catalyst |
MXPA06015023A (es) * | 2006-12-19 | 2008-10-09 | Mexicano Inst Petrol | Aplicacion de material adsorbente microporoso de carbon, para reducir el contenido de benceno de corrientes de hidrocarburos. |
IT1397886B1 (it) * | 2009-12-23 | 2013-02-04 | Eni Spa | Procedimento per la produzione di componenti di carburanti per autotrazione. |
CN106995713A (zh) | 2011-02-07 | 2017-08-01 | 巴杰许可有限责任公司 | 用于降低汽油的苯含量的方法 |
US9200215B2 (en) | 2011-02-07 | 2015-12-01 | Badger Licensing Llc | Process for reducing the benzene content of gasoline |
US9199891B2 (en) | 2011-02-07 | 2015-12-01 | Badger Licensing Llc | Process for reducing the benzene content of gasoline |
WO2012108926A1 (en) | 2011-02-07 | 2012-08-16 | Badger Licensing Llc | Process for reducing the benzene content of gasoline |
US9598330B2 (en) | 2011-08-19 | 2017-03-21 | Badger Licensing | Process for reducing the benzene content of gasoline |
CN103797091B (zh) | 2011-08-19 | 2016-07-06 | 巴杰许可有限责任公司 | 降低汽油的苯含量的方法 |
CN107001946B (zh) | 2014-11-25 | 2019-07-05 | 巴杰许可有限责任公司 | 降低汽油中苯含量的方法 |
WO2017188934A1 (en) | 2016-04-26 | 2017-11-02 | Badger Licensing Llc | Process for reducing the benzene content of gasoline |
US10246387B2 (en) | 2016-10-06 | 2019-04-02 | Exxonmobil Chemical Patents Inc. | Process for selectivating catalyst for producing paraxylene by methylation of benzene and/or toluene |
US11673849B2 (en) | 2016-12-21 | 2023-06-13 | Exxonmobil Chemical Patents Inc. | Process for selectivating catalyst for producing paraxylene by methylation of benzene and/or toluene |
Family Cites Families (18)
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US3649520A (en) * | 1970-03-13 | 1972-03-14 | Mobil Oil Corp | Production of lead free gasoline |
US3770614A (en) * | 1971-01-15 | 1973-11-06 | Mobil Oil Corp | Split feed reforming and n-paraffin elimination from low boiling reformate |
US3767568A (en) * | 1971-03-19 | 1973-10-23 | Mobil Oil Corp | Hydrocarbon conversion |
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US4746762A (en) * | 1985-01-17 | 1988-05-24 | Mobil Oil Corporation | Upgrading light olefins in a turbulent fluidized catalyst bed reactor |
US5149894A (en) * | 1986-01-29 | 1992-09-22 | Chevron Research And Technology Company | Alkylation using zeolite SSZ-25 |
US4954325A (en) * | 1986-07-29 | 1990-09-04 | Mobil Oil Corp. | Composition of synthetic porous crystalline material, its synthesis and use |
US4827069A (en) * | 1988-02-19 | 1989-05-02 | Mobil Oil Corporation | Upgrading light olefin fuel gas and catalytic reformate in a turbulent fluidized bed catalyst reactor |
US4992606A (en) * | 1988-10-06 | 1991-02-12 | Mobil Oil Corp. | Process for preparing short chain alkyl aromatic compounds |
US4950387A (en) * | 1988-10-21 | 1990-08-21 | Mobil Oil Corp. | Upgrading of cracking gasoline |
US4992607A (en) * | 1989-03-20 | 1991-02-12 | Mobil Oil Corporation | Petroleum refinery process and apparatus for the production of alkyl aromatic hydrocarbons from fuel gas and catalytic reformate |
US5334795A (en) * | 1990-06-28 | 1994-08-02 | Mobil Oil Corp. | Production of ethylbenzene |
US5236575A (en) * | 1991-06-19 | 1993-08-17 | Mobil Oil Corp. | Synthetic porous crystalline mcm-49, its synthesis and use |
US5347061A (en) * | 1993-03-08 | 1994-09-13 | Mobil Oil Corporation | Process for producing gasoline having lower benzene content and distillation end point |
US5362697A (en) * | 1993-04-26 | 1994-11-08 | Mobil Oil Corp. | Synthetic layered MCM-56, its synthesis and use |
US5329059A (en) * | 1993-07-06 | 1994-07-12 | Mobil Oil Corp. | Alkylaromatic disproportionation |
US5336820A (en) * | 1993-08-11 | 1994-08-09 | Mobil Oil Corporation | Process for the alkylation of benzene-rich gasoline |
US5457254A (en) * | 1993-12-27 | 1995-10-10 | Mobil Oil Corporation | Naphthalene alkylation process using mixed H/NH3 form catalyst |
-
1994
- 1994-12-06 US US08/350,308 patent/US5545788A/en not_active Expired - Lifetime
-
1995
- 1995-11-21 JP JP51761196A patent/JP3938934B2/ja not_active Expired - Lifetime
- 1995-11-21 EP EP95940777A patent/EP0796234B1/en not_active Expired - Lifetime
- 1995-11-21 DE DE69519873T patent/DE69519873T2/de not_active Expired - Lifetime
- 1995-11-21 AU AU42416/96A patent/AU687291B2/en not_active Expired
- 1995-11-21 ES ES95940777T patent/ES2156219T3/es not_active Expired - Lifetime
- 1995-11-21 KR KR1019970703744A patent/KR100378141B1/ko not_active IP Right Cessation
- 1995-11-21 WO PCT/US1995/015137 patent/WO1996017810A1/en active IP Right Grant
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR101116523B1 (ko) * | 2004-08-13 | 2012-02-28 | 엑손모빌 케미칼 패턴츠 인코포레이티드 | 페놀 및 메틸에틸케톤의 제조 방법 |
JP2008535941A (ja) * | 2005-02-28 | 2008-09-04 | エクソンモービル リサーチ アンド エンジニアリング カンパニー | 気相芳香族アルキル化方法 |
JP2010515572A (ja) * | 2007-01-16 | 2010-05-13 | エクソンモービル・ケミカル・パテンツ・インク | 触媒組成物及び芳香族のアルキル化における該触媒組成物の使用 |
JP2012520376A (ja) * | 2009-03-13 | 2012-09-06 | エクソンモービル リサーチ アンド エンジニアリング カンパニー | 高いベンゼン転化率でのベンゼンアルキル化によるベンゼン含有率が低下したハイオクタン・ガソリンの製造方法 |
JP2014513152A (ja) * | 2011-02-07 | 2014-05-29 | バジャー・ライセンシング・エルエルシー | ガソリンのベンゼン含有量を低減する方法 |
JP2013049695A (ja) * | 2012-10-26 | 2013-03-14 | Exxonmobile Chemical Patents Inc | 有機化合物変換方法 |
JP2019534880A (ja) * | 2016-10-06 | 2019-12-05 | エクソンモービル・ケミカル・パテンツ・インク | ベンゼンおよび/またはトルエンのメチル化によるパラキシレン製造プロセス |
JP2019537563A (ja) * | 2016-10-06 | 2019-12-26 | エクソンモービル・ケミカル・パテンツ・インク | 芳香族炭化水素をメチル化するプロセス |
JP2020515605A (ja) * | 2017-03-29 | 2020-05-28 | エクソンモービル ケミカル パテンツ インコーポレイテッド | 炭化水素ストリームから不純物を除去する方法及び芳香族アルキル化プロセスにおけるそれらの使用 |
Also Published As
Publication number | Publication date |
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KR100378141B1 (ko) | 2003-06-09 |
EP0796234B1 (en) | 2001-01-10 |
EP0796234A1 (en) | 1997-09-24 |
AU687291B2 (en) | 1998-02-19 |
WO1996017810A1 (en) | 1996-06-13 |
ES2156219T3 (es) | 2001-06-16 |
DE69519873T2 (de) | 2001-08-16 |
AU4241696A (en) | 1996-06-26 |
DE69519873D1 (de) | 2001-02-15 |
JP3938934B2 (ja) | 2007-06-27 |
US5545788A (en) | 1996-08-13 |
EP0796234A4 (en) | 1998-12-16 |
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