TWI622572B - 用於自媒裂烴類獲得芳香烴的方法及系統 - Google Patents
用於自媒裂烴類獲得芳香烴的方法及系統 Download PDFInfo
- Publication number
- TWI622572B TWI622572B TW102134542A TW102134542A TWI622572B TW I622572 B TWI622572 B TW I622572B TW 102134542 A TW102134542 A TW 102134542A TW 102134542 A TW102134542 A TW 102134542A TW I622572 B TWI622572 B TW I622572B
- Authority
- TW
- Taiwan
- Prior art keywords
- stream
- xylene
- aromatic hydrocarbon
- para
- toluene
- Prior art date
Links
- 238000000034 method Methods 0.000 title claims abstract description 64
- 229930195733 hydrocarbon Natural products 0.000 title abstract description 11
- 150000002430 hydrocarbons Chemical class 0.000 title abstract description 11
- 238000004523 catalytic cracking Methods 0.000 title 1
- URLKBWYHVLBVBO-UHFFFAOYSA-N Para-Xylene Chemical group CC1=CC=C(C)C=C1 URLKBWYHVLBVBO-UHFFFAOYSA-N 0.000 claims abstract description 80
- 239000008096 xylene Substances 0.000 claims abstract description 38
- 238000004519 manufacturing process Methods 0.000 claims abstract description 24
- 238000005336 cracking Methods 0.000 claims abstract description 17
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 claims description 108
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 claims description 71
- 150000004945 aromatic hydrocarbons Chemical class 0.000 claims description 52
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 claims description 41
- 150000001336 alkenes Chemical class 0.000 claims description 22
- 238000000926 separation method Methods 0.000 claims description 21
- 238000000605 extraction Methods 0.000 claims description 18
- 239000012535 impurity Substances 0.000 claims description 16
- 238000004821 distillation Methods 0.000 claims description 14
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 claims description 14
- 238000006317 isomerization reaction Methods 0.000 claims description 13
- 238000011084 recovery Methods 0.000 claims description 12
- 238000010555 transalkylation reaction Methods 0.000 claims description 11
- YNQLUTRBYVCPMQ-UHFFFAOYSA-N Ethylbenzene Chemical compound CCC1=CC=CC=C1 YNQLUTRBYVCPMQ-UHFFFAOYSA-N 0.000 claims description 10
- 239000003208 petroleum Substances 0.000 claims description 10
- 239000003054 catalyst Substances 0.000 claims description 9
- 238000000638 solvent extraction Methods 0.000 claims description 9
- 210000004556 brain Anatomy 0.000 claims description 8
- 230000011987 methylation Effects 0.000 claims description 8
- 238000007069 methylation reaction Methods 0.000 claims description 8
- 238000006243 chemical reaction Methods 0.000 claims description 7
- 238000010521 absorption reaction Methods 0.000 claims description 6
- 238000000895 extractive distillation Methods 0.000 claims description 6
- 238000000622 liquid--liquid extraction Methods 0.000 claims description 6
- 238000002425 crystallisation Methods 0.000 claims description 5
- 238000001179 sorption measurement Methods 0.000 claims description 5
- 230000008025 crystallization Effects 0.000 claims description 4
- 238000005984 hydrogenation reaction Methods 0.000 claims description 4
- 238000005574 benzylation reaction Methods 0.000 claims description 3
- 230000008929 regeneration Effects 0.000 claims description 3
- 238000011069 regeneration method Methods 0.000 claims description 3
- 239000000203 mixture Substances 0.000 claims description 2
- 238000007323 disproportionation reaction Methods 0.000 claims 2
- 230000029936 alkylation Effects 0.000 claims 1
- 238000005804 alkylation reaction Methods 0.000 claims 1
- 150000001555 benzenes Chemical class 0.000 claims 1
- 150000003738 xylenes Chemical class 0.000 abstract description 2
- 239000003502 gasoline Substances 0.000 description 11
- 238000005899 aromatization reaction Methods 0.000 description 7
- 239000000047 product Substances 0.000 description 7
- 230000008901 benefit Effects 0.000 description 5
- 238000000197 pyrolysis Methods 0.000 description 5
- 239000002994 raw material Substances 0.000 description 5
- 239000004215 Carbon black (E152) Substances 0.000 description 4
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 4
- KKEYFWRCBNTPAC-UHFFFAOYSA-N Terephthalic acid Chemical compound OC(=O)C1=CC=C(C(O)=O)C=C1 KKEYFWRCBNTPAC-UHFFFAOYSA-N 0.000 description 4
- IVSZLXZYQVIEFR-UHFFFAOYSA-N m-xylene Chemical group CC1=CC=CC(C)=C1 IVSZLXZYQVIEFR-UHFFFAOYSA-N 0.000 description 4
- 229910052717 sulfur Inorganic materials 0.000 description 4
- 239000011593 sulfur Substances 0.000 description 4
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 150000001335 aliphatic alkanes Chemical class 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 239000003915 liquefied petroleum gas Substances 0.000 description 3
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 3
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 3
- 125000002029 aromatic hydrocarbon group Chemical group 0.000 description 2
- 125000003118 aryl group Chemical group 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- 239000006227 byproduct Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 229940078552 o-xylene Drugs 0.000 description 2
- -1 polyethylene terephthalate Polymers 0.000 description 2
- 229920000139 polyethylene terephthalate Polymers 0.000 description 2
- 239000005020 polyethylene terephthalate Substances 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- VXNZUUAINFGPBY-UHFFFAOYSA-N 1-Butene Chemical compound CCC=C VXNZUUAINFGPBY-UHFFFAOYSA-N 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- ZQRGREQWCRSUCI-UHFFFAOYSA-N [S].C=1C=CSC=1 Chemical compound [S].C=1C=CSC=1 ZQRGREQWCRSUCI-UHFFFAOYSA-N 0.000 description 1
- 125000000217 alkyl group Chemical group 0.000 description 1
- IAQRGUVFOMOMEM-UHFFFAOYSA-N butene Natural products CC=CC IAQRGUVFOMOMEM-UHFFFAOYSA-N 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 239000003518 caustics Substances 0.000 description 1
- 238000003776 cleavage reaction Methods 0.000 description 1
- 239000010779 crude oil Substances 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- ONIHPYYWNBVMID-UHFFFAOYSA-N diethyl benzene-1,4-dicarboxylate Chemical compound CCOC(=O)C1=CC=C(C(=O)OCC)C=C1 ONIHPYYWNBVMID-UHFFFAOYSA-N 0.000 description 1
- 238000011143 downstream manufacturing Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 239000013462 industrial intermediate Substances 0.000 description 1
- 239000004434 industrial solvent Substances 0.000 description 1
- 239000000543 intermediate Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- TVMXDCGIABBOFY-UHFFFAOYSA-N octane Chemical compound CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 description 1
- 238000005504 petroleum refining Methods 0.000 description 1
- 125000001997 phenyl group Chemical group [H]C1=C([H])C([H])=C(*)C([H])=C1[H] 0.000 description 1
- 230000006798 recombination Effects 0.000 description 1
- 238000005215 recombination Methods 0.000 description 1
- 230000007017 scission Effects 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C5/00—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
- C07C5/22—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by isomerisation
- C07C5/27—Rearrangement of carbon atoms in the hydrocarbon skeleton
- C07C5/2729—Changing the branching point of an open chain or the point of substitution on a ring
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2/00—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms
- C07C2/76—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by condensation of hydrocarbons with partial elimination of hydrogen
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C5/00—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
- C07C5/22—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by isomerisation
- C07C5/27—Rearrangement of carbon atoms in the hydrocarbon skeleton
- C07C5/2729—Changing the branching point of an open chain or the point of substitution on a ring
- C07C5/2732—Catalytic processes
-
- 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
- C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
- C10G11/14—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts
- C10G11/18—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts according to the "fluidised-bed" technique
-
- 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
- C10G55/00—Treatment of hydrocarbon oils, in the absence of hydrogen, by at least one refining process and at least one cracking process
- C10G55/02—Treatment of hydrocarbon oils, in the absence of hydrogen, by at least one refining process and at least one cracking process plural serial stages only
- C10G55/06—Treatment of hydrocarbon oils, in the absence of hydrogen, by at least one refining process and at least one cracking process plural serial stages only including at least one catalytic cracking step
-
- 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
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/10—Feedstock materials
- C10G2300/1074—Vacuum distillates
-
- 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
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/10—Feedstock materials
- C10G2300/1077—Vacuum residues
-
- 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)
- 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)
- Physics & Mathematics (AREA)
- Electromagnetism (AREA)
- Mechanical Engineering (AREA)
Applications Claiming Priority (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US201261711934P | 2012-10-10 | 2012-10-10 | |
| US61/711,934 | 2012-10-10 | ||
| US13/830,189 | 2013-03-14 | ||
| US13/830,189 US10308567B2 (en) | 2012-10-10 | 2013-03-14 | Processes and systems for obtaining aromatics from catalytic cracking hydrocarbons |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| TW201414698A TW201414698A (zh) | 2014-04-16 |
| TWI622572B true TWI622572B (zh) | 2018-05-01 |
Family
ID=50433205
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| TW102134542A TWI622572B (zh) | 2012-10-10 | 2013-09-25 | 用於自媒裂烴類獲得芳香烴的方法及系統 |
Country Status (18)
| Country | Link |
|---|---|
| US (1) | US10308567B2 (enExample) |
| EP (1) | EP2906663B1 (enExample) |
| JP (1) | JP6119062B2 (enExample) |
| KR (1) | KR101995233B1 (enExample) |
| CN (1) | CN104919026B (enExample) |
| AR (1) | AR092980A1 (enExample) |
| AU (1) | AU2013330434A1 (enExample) |
| BR (1) | BR112015008035A2 (enExample) |
| CA (1) | CA2888111A1 (enExample) |
| IL (1) | IL238173A0 (enExample) |
| IN (1) | IN2015DN03742A (enExample) |
| MX (1) | MX2015004456A (enExample) |
| MY (1) | MY183432A (enExample) |
| PL (1) | PL2906663T3 (enExample) |
| RU (1) | RU2664543C2 (enExample) |
| SG (1) | SG11201502727YA (enExample) |
| TW (1) | TWI622572B (enExample) |
| WO (1) | WO2014058465A1 (enExample) |
Families Citing this family (26)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106488897B (zh) * | 2014-06-30 | 2020-04-24 | 埃克森美孚化学专利公司 | 制备二甲苯的方法 |
| CN106458794B (zh) * | 2014-06-30 | 2020-02-14 | 埃克森美孚化学专利公司 | 制备二甲苯的方法 |
| WO2016003611A1 (en) * | 2014-06-30 | 2016-01-07 | Exxonmobil Chemical Patents Inc. | Process for the production of para-xyxlene |
| US9708233B2 (en) | 2014-08-15 | 2017-07-18 | Exxonmobil Chemical Patents Inc. | Aromatics production process |
| WO2016025077A1 (en) * | 2014-08-15 | 2016-02-18 | Exxonmobil Chemical Patents Inc. | Aromatics production process |
| US20170073285A1 (en) * | 2015-09-10 | 2017-03-16 | Uop Llc | Processes and apparatuses for toluene methylation in an aromatics complex |
| WO2017052858A1 (en) * | 2015-09-25 | 2017-03-30 | Exxonmobile Chemical Patents Inc. | Conversion of non-aromatic hydrocarbon |
| WO2017105787A1 (en) | 2015-12-16 | 2017-06-22 | Uop Llc | Processes and apparatuses for olefin saturation in an aromatics complex |
| CN108430958B (zh) * | 2015-12-16 | 2021-01-01 | 环球油品公司 | 用于芳族化合物复合设备中的甲苯甲基化的方法及装置 |
| JP6574059B2 (ja) * | 2016-04-28 | 2019-09-11 | 旭化成株式会社 | 芳香族炭化水素含有化合物の製造方法 |
| CN108250014A (zh) * | 2016-12-28 | 2018-07-06 | 中国石油天然气股份有限公司 | 一种异构化制备对二甲苯的方法 |
| WO2019036291A1 (en) | 2017-08-15 | 2019-02-21 | Sabic Global Technologies B.V. | SHALE GAS AND CONDENSATE GIVING CHEMICALS |
| US10427993B2 (en) | 2017-08-31 | 2019-10-01 | Uop Llc | Process for recovering benzene and fuel gas in an aromatics complex |
| US10793493B2 (en) | 2017-08-31 | 2020-10-06 | Uop Llc | Process for recovering benzene and fuel gas in an aromatics complex |
| US10392316B2 (en) * | 2017-10-11 | 2019-08-27 | Uop Llc | Process for minimizing benzene, toluene, and a recycle loop in a zero benzene aromatics complex |
| US10308571B2 (en) * | 2017-10-11 | 2019-06-04 | Uop Llc | Process for minimizing benzene, toluene, and a recycle loop in a zero benzene aromatics complex |
| CN112313193B (zh) | 2018-06-25 | 2023-10-31 | 沙特基础工业全球技术有限公司 | 用于生产对二甲苯的方法和系统 |
| KR102800623B1 (ko) | 2018-09-03 | 2025-04-28 | 에네오스 가부시키가이샤 | 크실렌의 제조 방법 |
| EP3921296A1 (en) | 2019-02-04 | 2021-12-15 | China Petroleum & Chemical Corporation | Process for making phenol and xylenes |
| US20200354293A1 (en) * | 2019-05-10 | 2020-11-12 | Uop Llc | Process and apparatus for dual feed para-xylene separation |
| CN113527026A (zh) * | 2020-04-21 | 2021-10-22 | 国家能源投资集团有限责任公司 | 用于将轻质烷烃转化成芳香族化合物的系统和方法 |
| KR102819375B1 (ko) * | 2020-06-16 | 2025-06-11 | 주식회사 엘지화학 | 방향족 탄화수소의 제조방법 |
| KR102464478B1 (ko) * | 2020-06-16 | 2022-11-07 | 주식회사 엘지화학 | 방향족 탄화수소 제조장치 |
| KR102464480B1 (ko) * | 2020-06-16 | 2022-11-07 | 주식회사 엘지화학 | 방향족 탄화수소의 제조방법 |
| CN114426879B (zh) | 2020-10-15 | 2023-08-08 | 中国石油化工股份有限公司 | 含烃混合物的利用系统和方法 |
| US11548842B1 (en) | 2022-06-01 | 2023-01-10 | Saudi Arabian Oil Company | Conversion of light naphtha to enhanced value aromatics in an integrated reactor process |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| 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 |
Family Cites Families (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4206035A (en) * | 1978-08-15 | 1980-06-03 | Phillips Petroleum Company | Process for producing high octane hydrocarbons |
| US5609751A (en) * | 1994-07-26 | 1997-03-11 | Chevron Chemical Company | Para-xylene selective reforming/aromatization |
| JPH08301796A (ja) * | 1995-05-12 | 1996-11-19 | Koa Oil Co Ltd | 炭素数８の芳香族炭化水素の製造方法 |
| US5685972A (en) * | 1995-07-14 | 1997-11-11 | Timken; Hye Kyung C. | Production of benzene, toluene, and xylene (BTX) from FCC naphtha |
| US6376733B1 (en) * | 1996-01-25 | 2002-04-23 | Exxonmobil Chemical Patents Inc. | Process for production of paraxylene |
| US6565742B1 (en) * | 1997-09-03 | 2003-05-20 | Gtc Technology Inc. | Aromatics separation process and method of retrofitting existing equipment for same |
| US20080287719A1 (en) * | 2004-12-30 | 2008-11-20 | Deng-Yang Jan | Process for para-xylene production from light aliphatics |
| JP5463281B2 (ja) * | 2007-04-04 | 2014-04-09 | エクソンモービル・ケミカル・パテンツ・インク | パラキシレン製造プロセス及び装置 |
| WO2009043753A1 (de) * | 2007-09-28 | 2009-04-09 | Basf Se | Verfahren zur gewinnung von aromatischen kohlenwasserstoffen aus einem kohlenwasserstoffgemisch |
| JP2009242555A (ja) * | 2008-03-31 | 2009-10-22 | Mitsui Eng & Shipbuild Co Ltd | 廃プラスチックの処理方法及び処理装置 |
| PL215253B1 (pl) * | 2008-06-26 | 2013-11-29 | Uop Llc | Sposób do wydzielania para-ksylenu z mieszaniny weglowodorów aromatycznych C8 i C9 i aparatura do wydzielania para-ksylenu z mieszaniny weglowodorów aromatycznych C8 i C9 |
| JP4837114B2 (ja) * | 2010-03-26 | 2011-12-14 | 千代田化工建設株式会社 | 芳香族炭化水素の製造方法および芳香族炭化水素の製造プラント |
| US8569559B2 (en) * | 2010-06-25 | 2013-10-29 | Exxonmobil Chemical Patents Inc. | Paraxylene production process and apparatus |
| WO2012078373A2 (en) * | 2010-12-10 | 2012-06-14 | Exxonmobil Chemical Patents Inc. | Method and apparatus for obtaining aromatics from diverse feedstock |
| US8679321B2 (en) * | 2011-04-29 | 2014-03-25 | Uop Llc | Process for increasing benzene and toluene production |
| JP5759262B2 (ja) * | 2011-05-24 | 2015-08-05 | Ｊｘ日鉱日石エネルギー株式会社 | キシレンの製造方法 |
-
2013
- 2013-03-14 SG SG11201502727YA patent/SG11201502727YA/en unknown
- 2013-03-14 EP EP13845138.0A patent/EP2906663B1/en active Active
- 2013-03-14 WO PCT/US2013/031146 patent/WO2014058465A1/en not_active Ceased
- 2013-03-14 MX MX2015004456A patent/MX2015004456A/es unknown
- 2013-03-14 IN IN3742DEN2015 patent/IN2015DN03742A/en unknown
- 2013-03-14 AU AU2013330434A patent/AU2013330434A1/en not_active Abandoned
- 2013-03-14 PL PL13845138T patent/PL2906663T3/pl unknown
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- 2013-03-14 US US13/830,189 patent/US10308567B2/en not_active Expired - Fee Related
- 2013-03-14 MY MYPI2015701117A patent/MY183432A/en unknown
- 2013-03-14 CN CN201380053326.4A patent/CN104919026B/zh active Active
- 2013-03-14 CA CA2888111A patent/CA2888111A1/en not_active Abandoned
- 2013-03-14 RU RU2015116113A patent/RU2664543C2/ru active
- 2013-03-14 JP JP2015536758A patent/JP6119062B2/ja active Active
- 2013-03-14 BR BR112015008035A patent/BR112015008035A2/pt not_active IP Right Cessation
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-
2015
- 2015-04-12 IL IL238173A patent/IL238173A0/en unknown
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| 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 |
Also Published As
| Publication number | Publication date |
|---|---|
| JP6119062B2 (ja) | 2017-04-26 |
| EP2906663A4 (en) | 2016-06-08 |
| EP2906663A1 (en) | 2015-08-19 |
| RU2015116113A (ru) | 2016-11-27 |
| AU2013330434A1 (en) | 2015-05-14 |
| RU2664543C2 (ru) | 2018-08-20 |
| EP2906663B1 (en) | 2017-09-27 |
| US10308567B2 (en) | 2019-06-04 |
| MX2015004456A (es) | 2015-07-14 |
| KR20150066586A (ko) | 2015-06-16 |
| JP2015531405A (ja) | 2015-11-02 |
| US20140100398A1 (en) | 2014-04-10 |
| IL238173A0 (en) | 2015-05-31 |
| CN104919026B (zh) | 2018-01-02 |
| WO2014058465A1 (en) | 2014-04-17 |
| TW201414698A (zh) | 2014-04-16 |
| CA2888111A1 (en) | 2014-04-17 |
| IN2015DN03742A (enExample) | 2015-09-18 |
| PL2906663T3 (pl) | 2018-03-30 |
| SG11201502727YA (en) | 2015-05-28 |
| KR101995233B1 (ko) | 2019-07-02 |
| BR112015008035A2 (pt) | 2017-07-04 |
| AR092980A1 (es) | 2015-05-13 |
| MY183432A (en) | 2021-02-18 |
| CN104919026A (zh) | 2015-09-16 |
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