JP5351766B2 - キシレン化合物のマルチゾーン製造方法 - Google Patents
キシレン化合物のマルチゾーン製造方法 Download PDFInfo
- Publication number
- JP5351766B2 JP5351766B2 JP2009544145A JP2009544145A JP5351766B2 JP 5351766 B2 JP5351766 B2 JP 5351766B2 JP 2009544145 A JP2009544145 A JP 2009544145A JP 2009544145 A JP2009544145 A JP 2009544145A JP 5351766 B2 JP5351766 B2 JP 5351766B2
- Authority
- JP
- Japan
- Prior art keywords
- stream
- zone
- xylene
- transalkylation
- reforming
- 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.)
- Expired - Fee Related
Links
Images
Classifications
-
- 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
- C10G69/00—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process
- C10G69/02—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process plural serial stages only
- C10G69/12—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process plural serial stages only including at least one polymerisation or alkylation step
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C6/00—Preparation of hydrocarbons from hydrocarbons containing a different number of carbon atoms by redistribution reactions
- C07C6/08—Preparation of hydrocarbons from hydrocarbons containing a different number of carbon atoms by redistribution reactions by conversion at a saturated carbon-to-carbon bond
- C07C6/12—Preparation of hydrocarbons from hydrocarbons containing a different number of carbon atoms by redistribution reactions by conversion at a saturated carbon-to-carbon bond of exclusively hydrocarbons containing a six-membered aromatic ring
- C07C6/126—Preparation of hydrocarbons from hydrocarbons containing a different number of carbon atoms by redistribution reactions by conversion at a saturated carbon-to-carbon bond of exclusively hydrocarbons containing a six-membered aromatic ring of more than one hydrocarbon
-
- 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
- C10G35/00—Reforming naphtha
- C10G35/04—Catalytic reforming
-
- 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
- C10G69/00—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process
- C10G69/02—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process plural serial stages only
- C10G69/08—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process plural serial stages only including at least one step of reforming naphtha
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Description
1.(a)キシレン含有量が3%を超え、71℃(160°F)〜216℃(420°F)の範囲で沸騰するナフサ流(16)を得る工程と、
(b)該ナフサ流の少なくとも一部を、トランスアルキル化ゾーン(18)内でトランスアルキル化条件下で少なくともトランスアルキル化触媒と接触させて液体炭化水素系トランスアルキル化流出物(19)及び水素を含んでなるガス流を生成する工程であって、該トランスアルキル化条件は、該トランスアルキル化流出物が実質的に非芳香族化合物共沸物を含有しないキシレンを含みかつ該トランスアルキル化触媒と接触させる前の該ナフサ流(16)のキシレン含有量よりも高いキシレン含有量を有するように選択される工程と、
(c)該トランスアルキル化ゾーン(18)後に、キシレンを回収して少なくとも90重量%のキシレン含有量を有するキシレン製品を得る工程と
を含んでなるキシレンの製造方法;
2.少なくとも80%の環状成分含有量を有するナフサ流(16)を得、該ナフサ流(16)が10%〜40%のナフテン含有量をさらに有すると共に15%未満のパラフィン含有量を有し、かつ、該ナフサ流(16)がC7、C8及びC9芳香族成分を含む中間留分ナフサを主に含み、該中間留分流が該ナフサ流の該C8芳香族成分を実質的にすべて含む、前記1に記載の方法;
3.キシレン製品(36)が98%を超える全キシレン含有量を有する、前記1に記載の方法;
4.トランスアルキル化ゾーン(18)からの製品流(22)をベンゼンストリッパー(23)及びトルエンストリッパー(26)に誘導してストリップされたベンゼン製品流(24)及びストリップされたトルエン製品流(27)を得る工程をさらに含み、ストリップされた製品流の一方又は両方の一部を該トランスアルキル化ゾーン(18)に再循環させる、前記1に記載の方法;
5.炭化水素系供給流(13)を主分留ゾーン(14)に送る工程をさらに含んでなり、該主分留ゾーン(14)からの該供給流(13)を少なくともナフサ流(16)に分離した後、トランスアルキル化触媒と接触させる、前記1に記載の方法;
6.主分留ゾーン(14)内の供給流(13)を、91℃(195°F)未満で沸騰する軽質炭化水素流を主に含んでなる第1の留分(15)と、193℃(380°F)を超える温度で沸騰する超低硫黄ディーゼル流を主に含んでなる第3の留分(17)とに分離する工程をさらに含み、ナフサ流(16)が第2の留分である、前記5に記載の方法;
7.ナフサ流(16)の少なくとも一部を改質ゾーン(18)内で改質条件下で改質触媒と接触させて水素及び芳香族化合物を含んでなる改質ゾーン流出物を生成した後、トランスアルキル化ゾーン(18)に送る工程をさらに含んでなる、前記1に記載の方法;
8.改質条件が700kPa(100psig)〜3.5MPa(500psig)の圧力、300℃(572°F)〜565℃(1049°F)の温度、及び0.2〜20hr−lの液空間速度を含む、前記7に記載の方法;
9.トランスアルキル化条件が、200℃(392°F)〜540℃(1004°F)の温度、700kPa(100psig)〜6MPa(870psig)の圧力、及び0.1〜20hr−1の液空間速度を含む、前記1に記載の方法;
10.主分留ゾーン(14)の上流においてC9+炭化水素(1)を含んでなる炭化水素系流を水素化分解ゾーン(4)内で水素化分解条件下で水素化分解触媒と接触させてキシレンを含んでなる水素化分解ゾーン流出物(5)を生成し、該流出物(5)の一部を該主分留ゾーン(14)に送る工程をさらに含んでなる、前記1に記載の方法。
Claims (3)
- (a)炭化水素系供給流(13)を主分留ゾーン(14)に送り、キシレン含有量が3%を超え、71℃(160°F)〜216℃(420°F)の範囲で沸騰するナフサ流(16)を得る工程、
(b)該ナフサ流(16)の少なくとも一部を改質ゾーン(18)内で改質条件下で改質触媒と接触させて水素及び芳香族化合物を含んでなる改質ゾーン流出物を生成する工程、
(c)該改質ゾーン流出物の少なくとも一部を、トランスアルキル化ゾーン(18)内でトランスアルキル化条件下で少なくともトランスアルキル化触媒と接触させて液体炭化水素系トランスアルキル化流出物(19)及び水素を含んでなるガス流を生成する工程であって、該トランスアルキル化条件は、該トランスアルキル化流出物が実質的に非芳香族化合物共沸物を含有しないキシレンを含みかつ該トランスアルキル化触媒と接触させる前の該ナフサ流(16)のキシレン含有量よりも高いキシレン含有量を有するように選択される工程、及び
(d)該トランスアルキル化ゾーン(18)後に、キシレンを回収して少なくとも90重量%のキシレン含有量を有するキシレン製品を得る工程、
を含んでなるキシレンの製造方法。 - 少なくとも80%の環状成分含有量を有するナフサ流(16)を得、該ナフサ流(16)が10%〜40%のナフテン含有量をさらに有すると共に15%未満のパラフィン含有量を有し、かつ、該ナフサ流(16)がC7、C8及びC9芳香族成分を含む中間留分ナフサを主に含み、該中間留分流が該ナフサ流の該C8芳香族成分を実質的にすべて含む、請求項1に記載の方法。
- キシレン製品(36)が98%を超える全キシレン含有量を有する、請求項1に記載の方法。
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US88282306P | 2006-12-29 | 2006-12-29 | |
US60/882,823 | 2006-12-29 | ||
PCT/US2007/086554 WO2008082842A1 (en) | 2006-12-29 | 2007-12-05 | Multi-zone process for the production of xylene compounds |
Publications (2)
Publication Number | Publication Date |
---|---|
JP2010514776A JP2010514776A (ja) | 2010-05-06 |
JP5351766B2 true JP5351766B2 (ja) | 2013-11-27 |
Family
ID=39584952
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2009544145A Expired - Fee Related JP5351766B2 (ja) | 2006-12-29 | 2007-12-05 | キシレン化合物のマルチゾーン製造方法 |
Country Status (6)
Country | Link |
---|---|
US (1) | US7692052B2 (ja) |
JP (1) | JP5351766B2 (ja) |
KR (1) | KR101439574B1 (ja) |
CN (1) | CN101573431B (ja) |
TW (1) | TWI412584B (ja) |
WO (1) | WO2008082842A1 (ja) |
Families Citing this family (22)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20040218547A1 (en) | 2003-04-30 | 2004-11-04 | Rhodey William George | Process modification to maximize benzene production |
CA2674212C (en) * | 2007-02-02 | 2015-04-14 | William George Rhodey | Process and system for extraction of a feedstock |
WO2009008878A1 (en) * | 2007-07-06 | 2009-01-15 | Uop Llc | Process for the production of diesel and aromatic compounds |
US20120012504A1 (en) * | 2009-03-27 | 2012-01-19 | Hideki Minami | Method for producing aromatic hydrocarbons |
KR101443476B1 (ko) | 2010-02-03 | 2014-09-22 | 엑손모빌 케미칼 패턴츠 인코포레이티드 | 중질 방향족 탄화수소 공급원료의 트랜스알킬화 |
ES2441371T3 (es) * | 2010-02-17 | 2014-02-04 | Klaus Dahleke Kg | Procedimiento para la preparación de aceites de proceso nafténicos mediante hidrogenación |
US8586809B2 (en) * | 2010-07-30 | 2013-11-19 | Exxonmobil Chemical Patents Inc. | Purification of transalkylation feedstock |
US8481797B2 (en) | 2010-10-01 | 2013-07-09 | Uop Llc | Processes for maximizing high-value aromatics production utilizing stabilized crude benzene withdrawal |
KR20130124545A (ko) * | 2011-03-31 | 2013-11-14 | 유오피 엘엘씨 | 2개의 스트림을 수소화처리하기 위한 방법 및 장치 |
US8617384B2 (en) * | 2011-10-07 | 2013-12-31 | Uop Llc | Integrated catalytic cracking gasoline and light cycle oil hydroprocessing to maximize p-xylene production |
US8524961B2 (en) * | 2011-10-07 | 2013-09-03 | Uop Llc | Integrated catalytic cracking and reforming processes to improve p-xylene production |
US9187384B2 (en) * | 2011-12-13 | 2015-11-17 | Exxonmobil Chemical Patents Inc. | Production of alkylaromatic compounds |
CN104230619B (zh) * | 2013-06-17 | 2016-12-28 | 中国石油化工股份有限公司 | 芳烃深度净化的方法 |
CN104557429B (zh) * | 2013-10-28 | 2016-09-07 | 中国石油化工股份有限公司 | 原料多样化生产对二甲苯的方法 |
CN105992751B (zh) * | 2014-02-13 | 2019-03-22 | Bp北美公司 | 用于分离来自tol/a9+转烷基化工艺的反应器流出物的能量高效的分馏工艺 |
US9199893B2 (en) | 2014-02-24 | 2015-12-01 | Uop Llc | Process for xylenes production |
CN104927915B (zh) * | 2014-03-18 | 2017-01-25 | 中国石油化工股份有限公司 | 以石脑油为原料生产烯烃和芳烃的方法 |
JP6254881B2 (ja) * | 2014-03-26 | 2017-12-27 | コスモ石油株式会社 | キシレンの製造方法 |
US10450243B2 (en) * | 2014-12-19 | 2019-10-22 | Exxonmobil Chemical Patents Inc. | Sulfiding process for aromatic transalkylations |
US20190359542A1 (en) * | 2016-10-04 | 2019-11-28 | Exxonmobil Chemical Patents Inc. | Transalkylation of Heavy Aromatic Hydrocarbons |
US10035742B1 (en) * | 2017-05-26 | 2018-07-31 | Saudi Arabian Oil Company | Process for maximizing xylenes production from heavy aromatics for use therein |
US10632414B2 (en) | 2018-01-25 | 2020-04-28 | Uop Llc | Integration of pressure swing adsorption and hydroprocessing for improved hydrogen utilization |
Family Cites Families (50)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2892858A (en) | 1959-06-30 | Certificate of correction | ||
NL76445C (ja) | 1950-03-08 | |||
IT642040A (ja) | 1959-12-30 | 1900-01-01 | ||
US3308069A (en) | 1964-05-01 | 1967-03-07 | Mobil Oil Corp | Catalytic composition of a crystalline zeolite |
USRE28341E (en) | 1964-05-01 | 1975-02-18 | Marshall dann | |
US3702886A (en) | 1969-10-10 | 1972-11-14 | Mobil Oil Corp | Crystalline zeolite zsm-5 and method of preparing the same |
US3702292A (en) | 1970-03-10 | 1972-11-07 | Du Pont | Composite hydrocarbon refinery apparatus and process arrangement |
US3709979A (en) | 1970-04-23 | 1973-01-09 | Mobil Oil Corp | Crystalline zeolite zsm-11 |
US3832449A (en) | 1971-03-18 | 1974-08-27 | Mobil Oil Corp | Crystalline zeolite zsm{14 12 |
US4012313A (en) | 1972-04-30 | 1977-03-15 | Chevron Research Company | Catalytic reforming process and catalyst |
US3852190A (en) | 1972-10-27 | 1974-12-03 | Chevron Res | Reforming with platinum on alumina derived from a byproduct of a ziegler process |
CA1064890A (en) | 1975-06-10 | 1979-10-23 | Mae K. Rubin | Crystalline zeolite, synthesis and use thereof |
US4241036A (en) | 1975-10-23 | 1980-12-23 | Union Carbide Corporation | Synthetic crystalline zeolite and process for preparing same |
US4058454A (en) * | 1976-04-22 | 1977-11-15 | Uop Inc. | Aromatic hydrocarbon separation via solvent extraction |
US4070272A (en) | 1976-06-14 | 1978-01-24 | Uop Inc. | Hydrodesulfurization of hydrocarbon distillate with a catalyst composite of carrier, Pt/Pd, Rh and Sn |
JPS5926632B2 (ja) | 1976-12-18 | 1984-06-29 | 堺化学工業株式会社 | 有機りん化合物の製造法 |
JPS5439024A (en) * | 1977-09-01 | 1979-03-24 | Nosonobuichi Masuriyans Gudaru | Process for preparing benzene and xylene |
BR7807374A (pt) * | 1977-11-08 | 1979-07-24 | Standard Oil Co | Processo para desproporcionamento de um hidrocarboneto de petroleo,e composicao catalitica |
US4150061A (en) | 1977-11-08 | 1979-04-17 | Standard Oil Company (Indiana) | Process for converting pyrolysis gasoline to benzene and ethylbenzene-lean xylenes |
US4158026A (en) | 1978-03-13 | 1979-06-12 | Uop Inc. | Combination process for selected aromatic hydrocarbon production |
US4157355A (en) | 1978-03-13 | 1979-06-05 | Uop Inc. | Combination process for selected aromatic hydrocarbon production |
US4158025A (en) | 1978-03-13 | 1979-06-12 | Uop Inc. | Selected aromatic hydrocarbon production |
US4159282A (en) | 1978-06-09 | 1979-06-26 | Mobil Oil Corporation | Xylene isomerization |
US4329259A (en) | 1978-08-07 | 1982-05-11 | Uop Inc. | Acidic multimetallic catalytic composite |
US4278565A (en) | 1979-03-14 | 1981-07-14 | Mobil Oil Corporation | Hydrocarbon manufacture from alcohols |
DE3165380D1 (en) | 1980-06-12 | 1984-09-13 | Ici Plc | Zeolite eu-1 |
US4440871A (en) | 1982-07-26 | 1984-04-03 | Union Carbide Corporation | Crystalline silicoaluminophosphates |
US4567029A (en) | 1983-07-15 | 1986-01-28 | Union Carbide Corporation | Crystalline metal aluminophosphates |
US4556477A (en) | 1984-03-07 | 1985-12-03 | Mobil Oil Corporation | Highly siliceous porous crystalline material ZSM-22 and its use in catalytic dewaxing of petroleum stocks |
AU3346689A (en) | 1988-02-19 | 1989-09-06 | Mobil Oil Corporation | Process for the production of gasoline from fuel gas and catalytic reformate |
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 |
US4950828A (en) | 1989-06-30 | 1990-08-21 | Amoco Corporation | Process for upgrading light paraffins |
US5053573A (en) | 1990-09-14 | 1991-10-01 | Mobil Oil Corporation | Reduction of benzene content of reformate by reaction with cycle oils |
US5296208A (en) | 1992-08-07 | 1994-03-22 | Uop | Molecular sieve synthesis |
USH1723H (en) | 1992-09-11 | 1998-04-07 | Leuenberger; Ernest L. | Process for producing gasoline blending components from jet range and heavier aromatics |
US5347061A (en) | 1993-03-08 | 1994-09-13 | Mobil Oil Corporation | Process for producing gasoline having lower benzene content and distillation end point |
ES2144049T3 (es) | 1993-03-08 | 2000-06-01 | Mobil Oil Corp | Reduccion de benceno en gasolina mediante alquilacion con olefinas superiores. |
US5599439A (en) | 1993-03-13 | 1997-02-04 | Mobil Oil Corporation | Gasoline and reformate upgrading process |
US5406016A (en) | 1993-06-07 | 1995-04-11 | Exxon Research And Engineering Company | Transalkylation of benzene with heavy catalytic naphtha |
US5396010A (en) | 1993-08-16 | 1995-03-07 | Mobil Oil Corporation | Heavy naphtha upgrading |
JP4240339B2 (ja) * | 1994-10-03 | 2009-03-18 | 山陽石油化学株式会社 | 芳香族炭化水素の製造方法 |
JPH08119882A (ja) * | 1994-10-07 | 1996-05-14 | Chevron Usa Inc | 不純トルエンの芳香族化及び選択的不均化の併用による高純度ベンゼン及びパラに富むキシレンの製造法 |
TW504501B (en) | 1995-02-10 | 2002-10-01 | Mobil Oil Corp | Process for converting feedstock comprising C9+ aromatic hydrocarbons to lighter aromatic products |
US5658453A (en) | 1995-05-30 | 1997-08-19 | Uop | Integrated aromatization/trace-olefin-reduction scheme |
US5723710A (en) | 1996-07-12 | 1998-03-03 | Uop | Zeolite beta and its use in aromatic alkylation |
US5968343A (en) * | 1997-05-05 | 1999-10-19 | Phillips Petroleum Company | Hydrocarbon conversion catalyst composition and processes therefor and therewith |
US6004452A (en) | 1997-11-14 | 1999-12-21 | Chevron Chemical Company Llc | Process for converting hydrocarbon feed to high purity benzene and high purity paraxylene |
KR100557558B1 (ko) * | 2000-11-30 | 2006-03-03 | 에스케이 주식회사 | 탄화수소 혼합물로부터 방향족 탄화수소 및 액화석유가스를 제조하는 방법 |
US6740788B1 (en) | 2002-12-19 | 2004-05-25 | Uop Llc | Integrated process for aromatics production |
US20050197518A1 (en) | 2004-03-04 | 2005-09-08 | Miller Jeffrey T. | Method of converting C9 aromatics-comprising mixtures to xylene isomers |
-
2007
- 2007-06-14 US US11/763,235 patent/US7692052B2/en active Active
- 2007-12-05 CN CN200780048816XA patent/CN101573431B/zh not_active Expired - Fee Related
- 2007-12-05 WO PCT/US2007/086554 patent/WO2008082842A1/en active Application Filing
- 2007-12-05 KR KR1020097015880A patent/KR101439574B1/ko active IP Right Grant
- 2007-12-05 JP JP2009544145A patent/JP5351766B2/ja not_active Expired - Fee Related
- 2007-12-28 TW TW096150910A patent/TWI412584B/zh not_active IP Right Cessation
Also Published As
Publication number | Publication date |
---|---|
CN101573431A (zh) | 2009-11-04 |
US20080161622A1 (en) | 2008-07-03 |
TW200842186A (en) | 2008-11-01 |
TWI412584B (zh) | 2013-10-21 |
JP2010514776A (ja) | 2010-05-06 |
KR20090107516A (ko) | 2009-10-13 |
CN101573431B (zh) | 2013-02-27 |
WO2008082842A1 (en) | 2008-07-10 |
US7692052B2 (en) | 2010-04-06 |
KR101439574B1 (ko) | 2014-09-11 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JP5351766B2 (ja) | キシレン化合物のマルチゾーン製造方法 | |
JP5462789B2 (ja) | ディーゼル燃料および芳香族化合物の製造のためのマルチゾーンプロセス | |
US7271303B1 (en) | Multi-zone process for the production of diesel and aromatic compounds | |
JP5592396B2 (ja) | 重質芳香族油からの芳香族物質の製造において水素を効率的に用いる方法 | |
CN101570698B (zh) | 一种石脑油的催化转化方法 | |
CN101175838B (zh) | 一种综合流体催化裂化方法 | |
JP2969062B2 (ja) | プレミアム異性化ガソリン生成用水素化処理方法 | |
CA2620078C (en) | Methods of making xylene isomers | |
US8617384B2 (en) | Integrated catalytic cracking gasoline and light cycle oil hydroprocessing to maximize p-xylene production | |
US8524961B2 (en) | Integrated catalytic cracking and reforming processes to improve p-xylene production | |
JP7362368B2 (ja) | キシレンの製造方法 | |
JP2004105963A (ja) | 芳香族炭化水素化合物の転化用触媒および転化方法 |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
A621 | Written request for application examination |
Free format text: JAPANESE INTERMEDIATE CODE: A621 Effective date: 20100728 |
|
A977 | Report on retrieval |
Free format text: JAPANESE INTERMEDIATE CODE: A971007 Effective date: 20121029 |
|
A131 | Notification of reasons for refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A131 Effective date: 20121120 |
|
A521 | Request for written amendment filed |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20130220 |
|
TRDD | Decision of grant or rejection written | ||
A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 Effective date: 20130726 |
|
A61 | First payment of annual fees (during grant procedure) |
Free format text: JAPANESE INTERMEDIATE CODE: A61 Effective date: 20130823 |
|
R150 | Certificate of patent or registration of utility model |
Ref document number: 5351766 Country of ref document: JP Free format text: JAPANESE INTERMEDIATE CODE: R150 Free format text: JAPANESE INTERMEDIATE CODE: R150 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
LAPS | Cancellation because of no payment of annual fees |