GB1584090A - Temperature control of integrated fractionation and claytreating of hydrocarbons - Google Patents
Temperature control of integrated fractionation and claytreating of hydrocarbons Download PDFInfo
- Publication number
- GB1584090A GB1584090A GB35666/77A GB3566677A GB1584090A GB 1584090 A GB1584090 A GB 1584090A GB 35666/77 A GB35666/77 A GB 35666/77A GB 3566677 A GB3566677 A GB 3566677A GB 1584090 A GB1584090 A GB 1584090A
- Authority
- GB
- United Kingdom
- Prior art keywords
- stream
- temperature
- clay
- fractionation
- effluent stream
- 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
Links
- 238000005194 fractionation Methods 0.000 title claims description 44
- 229930195733 hydrocarbon Natural products 0.000 title claims description 37
- 150000002430 hydrocarbons Chemical class 0.000 title claims description 37
- 239000004927 clay Substances 0.000 claims description 102
- 239000004215 Carbon black (E152) Substances 0.000 claims description 23
- 238000000034 method Methods 0.000 claims description 22
- 238000006243 chemical reaction Methods 0.000 claims description 13
- 238000001816 cooling Methods 0.000 claims description 9
- 239000007788 liquid Substances 0.000 claims description 8
- 230000000694 effects Effects 0.000 claims description 5
- URLKBWYHVLBVBO-UHFFFAOYSA-N Para-Xylene Chemical group CC1=CC=C(C)C=C1 URLKBWYHVLBVBO-UHFFFAOYSA-N 0.000 claims description 4
- 150000004945 aromatic hydrocarbons Chemical class 0.000 claims description 4
- 239000012808 vapor phase Substances 0.000 claims description 3
- 238000010438 heat treatment Methods 0.000 claims description 2
- 238000006317 isomerization reaction Methods 0.000 claims description 2
- 239000003795 chemical substances by application Substances 0.000 claims 2
- 238000009833 condensation Methods 0.000 claims 1
- 230000005494 condensation Effects 0.000 claims 1
- 238000000926 separation method Methods 0.000 claims 1
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 57
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 30
- 239000000463 material Substances 0.000 description 16
- 238000012360 testing method Methods 0.000 description 8
- 238000011144 upstream manufacturing Methods 0.000 description 6
- 150000001875 compounds Chemical class 0.000 description 5
- 239000007791 liquid phase Substances 0.000 description 5
- 230000001105 regulatory effect Effects 0.000 description 5
- 238000012546 transfer Methods 0.000 description 5
- WKBOTKDWSSQWDR-UHFFFAOYSA-N Bromine atom Chemical compound [Br] WKBOTKDWSSQWDR-UHFFFAOYSA-N 0.000 description 4
- YNQLUTRBYVCPMQ-UHFFFAOYSA-N Ethylbenzene Chemical compound CCC1=CC=CC=C1 YNQLUTRBYVCPMQ-UHFFFAOYSA-N 0.000 description 4
- GDTBXPJZTBHREO-UHFFFAOYSA-N bromine Substances BrBr GDTBXPJZTBHREO-UHFFFAOYSA-N 0.000 description 4
- 229910052794 bromium Inorganic materials 0.000 description 4
- 150000001336 alkenes Chemical class 0.000 description 3
- 125000003118 aryl group Chemical group 0.000 description 3
- 230000001419 dependent effect Effects 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 229910052739 hydrogen Inorganic materials 0.000 description 3
- 239000001257 hydrogen Substances 0.000 description 3
- 229920000642 polymer Polymers 0.000 description 3
- 238000010555 transalkylation reaction Methods 0.000 description 3
- VIDOPANCAUPXNH-UHFFFAOYSA-N 1,2,3-triethylbenzene Chemical compound CCC1=CC=CC(CC)=C1CC VIDOPANCAUPXNH-UHFFFAOYSA-N 0.000 description 2
- KVNYFPKFSJIPBJ-UHFFFAOYSA-N 1,2-diethylbenzene Chemical compound CCC1=CC=CC=C1CC KVNYFPKFSJIPBJ-UHFFFAOYSA-N 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
- CPLXHLVBOLITMK-UHFFFAOYSA-N Magnesium oxide Chemical compound [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- MCMNRKCIXSYSNV-UHFFFAOYSA-N Zirconium dioxide Chemical compound O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 description 2
- 230000003197 catalytic effect Effects 0.000 description 2
- 230000001276 controlling effect Effects 0.000 description 2
- 238000006900 dealkylation reaction Methods 0.000 description 2
- 150000001993 dienes Chemical class 0.000 description 2
- 238000004821 distillation Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical group C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 238000006396 nitration reaction Methods 0.000 description 2
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 description 2
- 210000002741 palatine tonsil Anatomy 0.000 description 2
- 239000003208 petroleum Substances 0.000 description 2
- OTMSDBZUPAUEDD-UHFFFAOYSA-N Ethane Chemical group CC OTMSDBZUPAUEDD-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 150000004996 alkyl benzenes Chemical class 0.000 description 1
- 230000029936 alkylation Effects 0.000 description 1
- 238000005804 alkylation reaction Methods 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 229910000323 aluminium silicate Inorganic materials 0.000 description 1
- IXWIAFSBWGYQOE-UHFFFAOYSA-M aluminum;magnesium;oxygen(2-);silicon(4+);hydroxide;tetrahydrate Chemical compound O.O.O.O.[OH-].[O-2].[O-2].[O-2].[O-2].[O-2].[O-2].[O-2].[O-2].[O-2].[O-2].[Mg+2].[Al+3].[Si+4].[Si+4].[Si+4].[Si+4] IXWIAFSBWGYQOE-UHFFFAOYSA-M 0.000 description 1
- 238000000429 assembly Methods 0.000 description 1
- 230000000712 assembly Effects 0.000 description 1
- 229910001570 bauxite Inorganic materials 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 238000009529 body temperature measurement Methods 0.000 description 1
- 239000004295 calcium sulphite Substances 0.000 description 1
- 125000004432 carbon atom Chemical group C* 0.000 description 1
- 238000001833 catalytic reforming Methods 0.000 description 1
- 230000020335 dealkylation Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000004508 fractional distillation Methods 0.000 description 1
- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000000622 liquid--liquid extraction Methods 0.000 description 1
- 239000010687 lubricating oil Substances 0.000 description 1
- 239000000395 magnesium oxide Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 150000005673 monoalkenes Chemical class 0.000 description 1
- 229910052680 mordenite Inorganic materials 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 230000003606 oligomerizing effect Effects 0.000 description 1
- 239000000825 pharmaceutical preparation Substances 0.000 description 1
- 229940127557 pharmaceutical product Drugs 0.000 description 1
- 239000012071 phase Substances 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000002407 reforming Methods 0.000 description 1
- 238000005204 segregation Methods 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 238000000638 solvent extraction Methods 0.000 description 1
- 229920002994 synthetic fiber Polymers 0.000 description 1
- 239000008096 xylene Substances 0.000 description 1
- 150000003738 xylenes Chemical class 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C7/00—Purification; Separation; Use of additives
- C07C7/005—Processes comprising at least two steps in series
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/42—Regulation; Control
- B01D3/4211—Regulation; Control of columns
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C7/00—Purification; Separation; Use of additives
- C07C7/04—Purification; Separation; Use of additives by distillation
-
- 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
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/10—Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working
-
- 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
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S203/00—Distillation: processes, separatory
- Y10S203/19—Sidestream
-
- 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
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S208/00—Mineral oils: processes and products
- Y10S208/01—Automatic control
-
- 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
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S585/00—Chemistry of hydrocarbon compounds
- Y10S585/949—Miscellaneous considerations
- Y10S585/956—Condition-responsive control and related procedures in alicyclic synthesis and purification
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Water Supply & Treatment (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US05/717,978 US4024026A (en) | 1976-08-26 | 1976-08-26 | Temperature control of integrated fractionation and claytreating of hydrocarbons |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| GB1584090A true GB1584090A (en) | 1981-02-04 |
Family
ID=24884306
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| GB35666/77A Expired GB1584090A (en) | 1976-08-26 | 1977-08-25 | Temperature control of integrated fractionation and claytreating of hydrocarbons |
Country Status (6)
| Country | Link |
|---|---|
| US (1) | US4024026A (enExample) |
| CA (1) | CA1083067A (enExample) |
| ES (1) | ES459175A1 (enExample) |
| FR (1) | FR2363146A1 (enExample) |
| GB (1) | GB1584090A (enExample) |
| IT (1) | IT1079650B (enExample) |
Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4053367A (en) * | 1976-08-26 | 1977-10-11 | Uop Inc. | Temperature control of integrated fractionation and claytreating of hydrocarbons |
| US4129606A (en) * | 1977-01-24 | 1978-12-12 | Uop Inc. | Temperature control of integrated fractionation column and reaction zone |
| JPS54135726A (en) * | 1978-04-10 | 1979-10-22 | Mitsubishi Petrochem Co Ltd | Preparation of high-purity benzene |
| US5207894A (en) * | 1990-10-12 | 1993-05-04 | Lyondell Petrochemical Company | Removal of aromatic color bodies from aromatic hydrocarbon streams |
| US5057642A (en) * | 1991-04-18 | 1991-10-15 | Phillips Petroleum Company | Removal of basic impurities from olefin streams |
| US5997732A (en) * | 1997-12-22 | 1999-12-07 | Chevron U.S.A. Inc. | Clay treatment process for white mineral oil |
Family Cites Families (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2733286A (en) * | 1956-01-31 | Purification of a benzene fraction by mild liquid | ||
| US2775632A (en) * | 1953-05-13 | 1956-12-25 | Sun Oil Co | Treatment of aromatic hydrocarbons |
| US3139391A (en) * | 1960-10-31 | 1964-06-30 | Phillips Petroleum Co | Control process and system for fractional distillation systems |
| US3291850A (en) * | 1965-09-20 | 1966-12-13 | Universal Oil Prod Co | Hydrodealkylation of alkyl aromatic hydrocarbons |
| US3446709A (en) * | 1967-11-22 | 1969-05-27 | Lummus Co | Automatic control of gas absorption unit |
| US3434934A (en) * | 1967-12-22 | 1969-03-25 | Phillips Petroleum Co | Control system for fractional distillation columns |
| US3555837A (en) * | 1968-02-01 | 1971-01-19 | Phillips Petroleum Co | Temperature control of fluid separation systems |
| US3763022A (en) * | 1971-07-09 | 1973-10-02 | Phillips Petroleum Co | Condensing fractionator sidestream vapor as reboiler heat source |
| US3754045A (en) * | 1971-07-26 | 1973-08-21 | Hydrocarbon Research Inc | Hydrodealkylation |
| US3835037A (en) * | 1971-07-27 | 1974-09-10 | Ici Ltd | Purification of aromatic hydrocarbons |
-
1976
- 1976-08-26 US US05/717,978 patent/US4024026A/en not_active Expired - Lifetime
-
1977
- 1977-04-25 CA CA276,863A patent/CA1083067A/en not_active Expired
- 1977-05-05 IT IT49291/77A patent/IT1079650B/it active
- 1977-05-26 ES ES459175A patent/ES459175A1/es not_active Expired
- 1977-08-17 FR FR7725126A patent/FR2363146A1/fr active Granted
- 1977-08-25 GB GB35666/77A patent/GB1584090A/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| ES459175A1 (es) | 1978-04-16 |
| CA1083067A (en) | 1980-08-05 |
| FR2363146B1 (enExample) | 1982-03-19 |
| US4024026A (en) | 1977-05-17 |
| FR2363146A1 (fr) | 1978-03-24 |
| IT1079650B (it) | 1985-05-13 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PS | Patent sealed [section 19, patents act 1949] | ||
| PCNP | Patent ceased through non-payment of renewal fee |