DK2744876T3 - Proces og apparat til at genvinde hydroprocesserede kulbrinter med to strippere - Google Patents
Proces og apparat til at genvinde hydroprocesserede kulbrinter med to strippere Download PDFInfo
- Publication number
- DK2744876T3 DK2744876T3 DK12825585.8T DK12825585T DK2744876T3 DK 2744876 T3 DK2744876 T3 DK 2744876T3 DK 12825585 T DK12825585 T DK 12825585T DK 2744876 T3 DK2744876 T3 DK 2744876T3
- Authority
- DK
- Denmark
- Prior art keywords
- cold
- hot
- stream
- hydroprocessing
- stripper
- Prior art date
Links
- 238000000034 method Methods 0.000 title claims description 38
- 238000005194 fractionation Methods 0.000 claims description 49
- 229930195733 hydrocarbon Natural products 0.000 claims description 25
- 150000002430 hydrocarbons Chemical class 0.000 claims description 25
- 239000000463 material Substances 0.000 claims description 21
- 230000004888 barrier function Effects 0.000 claims description 18
- 239000004215 Carbon black (E152) Substances 0.000 claims description 16
- 238000010438 heat treatment Methods 0.000 claims description 9
- 239000003990 capacitor Substances 0.000 claims 1
- 239000007788 liquid Substances 0.000 description 42
- 238000004891 communication Methods 0.000 description 41
- 239000003054 catalyst Substances 0.000 description 40
- 238000004517 catalytic hydrocracking Methods 0.000 description 38
- 239000001257 hydrogen Substances 0.000 description 30
- 229910052739 hydrogen Inorganic materials 0.000 description 30
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 26
- 229910052751 metal Inorganic materials 0.000 description 25
- 239000002184 metal Substances 0.000 description 25
- 238000010992 reflux Methods 0.000 description 24
- 208000033830 Hot Flashes Diseases 0.000 description 18
- 206010060800 Hot flush Diseases 0.000 description 18
- 239000003921 oil Substances 0.000 description 18
- 238000009835 boiling Methods 0.000 description 17
- 239000007789 gas Substances 0.000 description 14
- 239000010457 zeolite Substances 0.000 description 14
- 238000006243 chemical reaction Methods 0.000 description 11
- 238000012545 processing Methods 0.000 description 10
- 239000002585 base Substances 0.000 description 9
- 238000011027 product recovery Methods 0.000 description 9
- 238000011084 recovery Methods 0.000 description 9
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 8
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 8
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 8
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 8
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 8
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 8
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 7
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 7
- 239000002002 slurry Substances 0.000 description 7
- 239000011593 sulfur Substances 0.000 description 7
- 229910052717 sulfur Inorganic materials 0.000 description 7
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 6
- 229910021536 Zeolite Inorganic materials 0.000 description 6
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 6
- 239000000446 fuel Substances 0.000 description 6
- 150000002739 metals Chemical class 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- 150000001875 compounds Chemical class 0.000 description 5
- -1 dachiardite Inorganic materials 0.000 description 5
- 239000000203 mixture Substances 0.000 description 5
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 description 4
- 229910021529 ammonia Inorganic materials 0.000 description 4
- 229910017052 cobalt Inorganic materials 0.000 description 4
- 239000010941 cobalt Substances 0.000 description 4
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 4
- 238000005336 cracking Methods 0.000 description 4
- 238000010586 diagram Methods 0.000 description 4
- 229910052759 nickel Inorganic materials 0.000 description 4
- 229910052757 nitrogen Inorganic materials 0.000 description 4
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 4
- 238000005201 scrubbing Methods 0.000 description 4
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonia chloride Chemical compound [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 description 3
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 3
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 description 3
- 239000013078 crystal Substances 0.000 description 3
- 238000013461 design Methods 0.000 description 3
- 238000004821 distillation Methods 0.000 description 3
- 239000003502 gasoline Substances 0.000 description 3
- 238000005342 ion exchange Methods 0.000 description 3
- 229910052742 iron Inorganic materials 0.000 description 3
- 239000003350 kerosene Substances 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- 239000002808 molecular sieve Substances 0.000 description 3
- 229910052750 molybdenum Inorganic materials 0.000 description 3
- 239000011733 molybdenum Substances 0.000 description 3
- 229910052680 mordenite Inorganic materials 0.000 description 3
- 229910000510 noble metal Inorganic materials 0.000 description 3
- 238000012856 packing Methods 0.000 description 3
- 239000000377 silicon dioxide Substances 0.000 description 3
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 description 3
- 150000003464 sulfur compounds Chemical class 0.000 description 3
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 description 3
- 229910052721 tungsten Inorganic materials 0.000 description 3
- 239000010937 tungsten Substances 0.000 description 3
- 238000011144 upstream manufacturing Methods 0.000 description 3
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 2
- KJTLSVCANCCWHF-UHFFFAOYSA-N Ruthenium Chemical compound [Ru] KJTLSVCANCCWHF-UHFFFAOYSA-N 0.000 description 2
- HIVLDXAAFGCOFU-UHFFFAOYSA-N ammonium hydrosulfide Chemical compound [NH4+].[SH-] HIVLDXAAFGCOFU-UHFFFAOYSA-N 0.000 description 2
- 150000003863 ammonium salts Chemical class 0.000 description 2
- 239000001284 azanium sulfanide Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 239000011230 binding agent Substances 0.000 description 2
- 230000033228 biological regulation Effects 0.000 description 2
- 238000001354 calcination Methods 0.000 description 2
- 230000003197 catalytic effect Effects 0.000 description 2
- 239000000460 chlorine Substances 0.000 description 2
- 229910052801 chlorine Inorganic materials 0.000 description 2
- 239000000571 coke Substances 0.000 description 2
- 230000003247 decreasing effect Effects 0.000 description 2
- 239000003085 diluting agent Substances 0.000 description 2
- 239000012013 faujasite Substances 0.000 description 2
- 125000005842 heteroatom Chemical group 0.000 description 2
- 150000002431 hydrogen Chemical class 0.000 description 2
- 239000011261 inert gas Substances 0.000 description 2
- 239000007791 liquid phase Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 229910052763 palladium Inorganic materials 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 229910052697 platinum Inorganic materials 0.000 description 2
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- 230000001105 regulatory effect Effects 0.000 description 2
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- 229920006395 saturated elastomer Polymers 0.000 description 2
- 238000009738 saturating Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 238000000859 sublimation Methods 0.000 description 2
- 230000008022 sublimation Effects 0.000 description 2
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- 238000010306 acid treatment Methods 0.000 description 1
- 230000004913 activation Effects 0.000 description 1
- 229910052783 alkali metal Inorganic materials 0.000 description 1
- 150000001340 alkali metals Chemical class 0.000 description 1
- 150000001342 alkaline earth metals Chemical group 0.000 description 1
- 150000001412 amines Chemical class 0.000 description 1
- 235000019270 ammonium chloride Nutrition 0.000 description 1
- 239000011959 amorphous silica alumina Substances 0.000 description 1
- 239000002518 antifoaming agent Substances 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 239000008346 aqueous phase Substances 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 229910001570 bauxite Inorganic materials 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- UNYSKUBLZGJSLV-UHFFFAOYSA-L calcium;1,3,5,2,4,6$l^{2}-trioxadisilaluminane 2,4-dioxide;dihydroxide;hexahydrate Chemical compound O.O.O.O.O.O.[OH-].[OH-].[Ca+2].O=[Si]1O[Al]O[Si](=O)O1.O=[Si]1O[Al]O[Si](=O)O1 UNYSKUBLZGJSLV-UHFFFAOYSA-L 0.000 description 1
- 125000002091 cationic group Chemical group 0.000 description 1
- 150000001768 cations Chemical class 0.000 description 1
- 229910052676 chabazite Inorganic materials 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 230000003009 desulfurizing effect Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 229910052675 erionite Inorganic materials 0.000 description 1
- 229910001657 ferrierite group Inorganic materials 0.000 description 1
- 235000003891 ferrous sulphate Nutrition 0.000 description 1
- 239000011790 ferrous sulphate Substances 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 229910052677 heulandite Inorganic materials 0.000 description 1
- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 1
- 238000005984 hydrogenation reaction Methods 0.000 description 1
- 238000010348 incorporation Methods 0.000 description 1
- 229910052741 iridium Inorganic materials 0.000 description 1
- GKOZUEZYRPOHIO-UHFFFAOYSA-N iridium atom Chemical compound [Ir] GKOZUEZYRPOHIO-UHFFFAOYSA-N 0.000 description 1
- BAUYGSIQEAFULO-UHFFFAOYSA-L iron(2+) sulfate (anhydrous) Chemical compound [Fe+2].[O-]S([O-])(=O)=O BAUYGSIQEAFULO-UHFFFAOYSA-L 0.000 description 1
- XBDUTCVQJHJTQZ-UHFFFAOYSA-L iron(2+) sulfate monohydrate Chemical compound O.[Fe+2].[O-]S([O-])(=O)=O XBDUTCVQJHJTQZ-UHFFFAOYSA-L 0.000 description 1
- 229910000359 iron(II) sulfate Inorganic materials 0.000 description 1
- 239000011344 liquid material Substances 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- 239000010687 lubricating oil Substances 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 125000005609 naphthenate group Chemical group 0.000 description 1
- WWZKQHOCKIZLMA-UHFFFAOYSA-M octanoate Chemical compound CCCCCCCC([O-])=O WWZKQHOCKIZLMA-UHFFFAOYSA-M 0.000 description 1
- 229910052762 osmium Inorganic materials 0.000 description 1
- SYQBFIAQOQZEGI-UHFFFAOYSA-N osmium atom Chemical compound [Os] SYQBFIAQOQZEGI-UHFFFAOYSA-N 0.000 description 1
- 239000003209 petroleum derivative Substances 0.000 description 1
- 239000012071 phase Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 239000002243 precursor Substances 0.000 description 1
- 238000000197 pyrolysis Methods 0.000 description 1
- 229910052761 rare earth metal Inorganic materials 0.000 description 1
- 150000002910 rare earth metals Chemical class 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 229910052703 rhodium Inorganic materials 0.000 description 1
- 239000010948 rhodium Substances 0.000 description 1
- MHOVAHRLVXNVSD-UHFFFAOYSA-N rhodium atom Chemical compound [Rh] MHOVAHRLVXNVSD-UHFFFAOYSA-N 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000000741 silica gel Substances 0.000 description 1
- 229910002027 silica gel Inorganic materials 0.000 description 1
- 150000004760 silicates Chemical class 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 229910052678 stilbite Inorganic materials 0.000 description 1
- 238000010998 test method Methods 0.000 description 1
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
- C10G67/00—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only
- C10G67/02—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only plural serial stages only
- C10G67/14—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only plural serial stages only including at least two different refining steps in the absence of hydrogen
-
- 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
-
- 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
- B01D3/34—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping with one or more auxiliary substances
- B01D3/38—Steam distillation
-
- 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
-
- 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
- C10G7/00—Distillation of hydrocarbon oils
-
- 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
- C10G2300/20—Characteristics of the feedstock or the products
- C10G2300/201—Impurities
- C10G2300/207—Acid gases, e.g. H2S, COS, SO2, HCN
-
- 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
- C10G2300/40—Characteristics of the process deviating from typical ways of processing
- C10G2300/4006—Temperature
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Claims (5)
1. Hydroprocesseringsproces (10), der omfatter: at hydroprocessere et kulbrintefødemateriale (16) i en hydroprocesseringsreaktor (24) for at tilvejebringe en udgangsstrøm (26) fra hydroprocessering; at adskille udgangsstrømmen (26) fra hydroprocessering til en kold udgangsstrøm (56) fra hydroprocessering og en varm udgangsstrøm (48) fra hydroprocessering; at strippe den kolde udgangsstrøm (56) fra hydroprocessering i en kold stripper (60) med stripping medium (78) for at tilvejebringe en kold strippet strøm (92); at strippe den varme udgangsstrøm (48) fra hydroprocessering i en varm stripper (50) med stripping medium (94) for at tilvejebringe en varm strippet strøm (106); at opvarme den varme strippede strøm i en opfyret varmeanordning (108) og at omlede den kolde strippede strøm uden om den opfyrede varmeanordning; at opvarme den kolde strippede strøm i en procesvarmeanordning eller en procesvarmeveksler; at tilføre den kolde strippede strøm og den varme strippede strøm til en produktfraktioneringskolonne (90); og at fraktionere den kolde strippede strøm og den varme strippede strøm i produktfraktioneringskolonnen for at tilvejebringe produktstrømme.
2. Hydroprocesseringsproces ifølge krav 1, hvorved strippingen af den kolde udgangsstrøm (56) fra hydroprocessering med stripping medium (78) i en kold stripper (60) også tilvejebringer en kold strøm (80) af dampe, og stripping af den varme udgangsstrøm (48) fra hydroprocessering med stripping medium (94) i den varme stripper (50) tilvejebringer en varm strøm (96) af dampe; og som yderligere omfatter: at kondensere den kolde strøm af dampe og den varme strøm af dampe i en kondensator for at tilvejebringe en kondenseret strøm fra en overliggende del.
3. Apparat (10) til hydroprocessering, der omfatter: en reaktor (24) til hydroprocessering; en kold stripper (60) i forbindelse med reaktoren (24) til hydroprocessering til at strippe en kold udgangsstrøm (56) fra hydroprocessering; en første ledning (78) til stripping medium i forbindelse med den kolde stripper (60) til at strippe den kolde udgangsstrøm (56) fra hydroprocessering; en varm stripper (50) i forbindelse med reaktoren (24) til hydroprocessering til at strippe en varm udgangsstrøm (48) fra hydroprocessering; en anden ledning (94) til stripping medium i forbindelse med den varme stripper (50) til at strippe den varme udgangsstrøm (48) fra hydroprocessering; og én eller flere separatorer i forbindelse med reaktoren (24) til hydroprocessering til at separere en udgangsstrøm (26) fra hydroprocessering fra reaktoren (24) til hydroprocessering i den kolde udgangsstrøm (56) fra hydroprocessering og den varme udgangsstrøm (48) fra hydroprocessering; en produktfraktioneringskolonne (90) i forbindelse med den kolde stripper (60) og den varme stripper (50) til at separere de strippede strømme (92, 106) til produktstrømme; en opfyret varmeanordning (108) på en ledning, som bærer den varme strippede strøm til produktfraktioneringskolonnen (90), og en ledning (92), som bærer den kolde strippede strøm til produktfraktioneringskolonnen (90), idet den omledes uden om den opfyrede varmeanordning (108); og en procesvarmeanordning eller en procesvarmeveksler, som er konfigureret til at opvarme den kolde strippede strøm på ledningen, som bærer den kolde strippede strøm til produktfraktioneringskolonnen (90) .
4. Apparat til hydroprocessering ifølge krav 3, der yderligere omfatter: et strippingkar (330), som indeholder den kolde stripper og den varme stripper; og en barriere (340) til at forhindre materiale i at komme ind i den kolde stripper fra den varme stripper.
5. Apparat til hydroprocessering ifølge krav 3, der yderligere omfatter en kondensator i forbindelse med både en overliggende del af den kolde stripper og en overliggende del af den varme stripper.
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US13/213,319 US8940254B2 (en) | 2011-08-19 | 2011-08-19 | Apparatus for recovering hydroprocessed hydrocarbons with two strippers |
| US13/213,310 US9518230B2 (en) | 2011-08-19 | 2011-08-19 | Process for recovering hydroprocessed hydrocarbons with two strippers |
| PCT/US2012/050513 WO2013028379A2 (en) | 2011-08-19 | 2012-08-13 | Process and apparatus for recovering hydroprocessed hydrocarbons with two strippers |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| DK2744876T3 true DK2744876T3 (da) | 2018-10-22 |
Family
ID=47747030
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| DK12825585.8T DK2744876T3 (da) | 2011-08-19 | 2012-08-13 | Proces og apparat til at genvinde hydroprocesserede kulbrinter med to strippere |
Country Status (6)
| Country | Link |
|---|---|
| EP (1) | EP2744876B1 (da) |
| KR (1) | KR101603396B1 (da) |
| CN (1) | CN103608432B (da) |
| DK (1) | DK2744876T3 (da) |
| RU (1) | RU2556218C1 (da) |
| WO (1) | WO2013028379A2 (da) |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US9809763B2 (en) * | 2015-06-01 | 2017-11-07 | Uop Llc | Process and apparatus for recovering hydrotreated hydrocarbons with two strippers |
| RU2719459C2 (ru) * | 2016-07-14 | 2020-04-17 | Ифп Энержи Нувелль | Способ обработки углеводородного сырья |
| FR3069173B1 (fr) * | 2017-07-21 | 2021-04-16 | France Evaporation | Procede et installation de traitement d'un liquide |
| US10899977B2 (en) * | 2018-06-26 | 2021-01-26 | Uop Llc | Process and apparatus for hydrocracking with light fractionation column with three products |
| US10829704B2 (en) * | 2018-06-26 | 2020-11-10 | Uop Llc | Process and apparatus for hydrocracking with prefractionator for stripped streams |
Family Cites Families (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3090747A (en) * | 1959-06-08 | 1963-05-21 | Kellogg M W Co | Process for desulfurization of dissimilar hydrocarbons |
| US3483119A (en) * | 1966-03-02 | 1969-12-09 | Exxon Research Engineering Co | Hydrofining processing technique for improving the color properties of middle distillates |
| US3733260A (en) * | 1972-02-04 | 1973-05-15 | Texaco Inc | Hydrodesulfurization process |
| EP0288627A1 (en) * | 1987-04-30 | 1988-11-02 | Mobil Oil Corporation | Method and apparatus for fractionating heavy hydrocarbons |
| US4822480A (en) * | 1987-12-22 | 1989-04-18 | Mobil Oil Corporation | Hydrocarbon product stripping |
| GB8807807D0 (en) * | 1988-03-31 | 1988-05-05 | Shell Int Research | Process for separating hydroprocessed effluent streams |
| US5110444A (en) * | 1990-08-03 | 1992-05-05 | Uop | Multi-stage hydrodesulfurization and hydrogenation process for distillate hydrocarbons |
| US5453177A (en) * | 1994-01-27 | 1995-09-26 | The M. W. Kellogg Company | Integrated distillate recovery process |
| US5705052A (en) * | 1996-12-31 | 1998-01-06 | Exxon Research And Engineering Company | Multi-stage hydroprocessing in a single reaction vessel |
| US5720872A (en) * | 1996-12-31 | 1998-02-24 | Exxon Research And Engineering Company | Multi-stage hydroprocessing with multi-stage stripping in a single stripper vessel |
| US6261441B1 (en) * | 1998-09-24 | 2001-07-17 | Mobil Oil Corporation | Integrated hydroprocessing scheme with segregated recycle |
| US6303020B1 (en) * | 2000-01-07 | 2001-10-16 | Catalytic Distillation Technologies | Process for the desulfurization of petroleum feeds |
| US6517705B1 (en) * | 2001-03-21 | 2003-02-11 | Uop Llc | Hydrocracking process for lube base oil production |
| RU2386669C2 (ru) * | 2005-09-02 | 2010-04-20 | Юоп Ллк | Способ каталитического гидрокрекинга углеводородного сырья для получения сверхмалосернистого дизельного топлива |
| US7927480B2 (en) * | 2008-01-29 | 2011-04-19 | Catalytic Distillation Technologies | Process for desulfurization of cracked naphtha |
| US8618344B2 (en) * | 2009-07-02 | 2013-12-31 | Reliance Industries Limited | Process for recovery of propylene and LPG from FCC fuel gas using stripped main column overhead distillate as absorber oil |
-
2012
- 2012-08-13 DK DK12825585.8T patent/DK2744876T3/da active
- 2012-08-13 KR KR1020137033196A patent/KR101603396B1/ko not_active Expired - Fee Related
- 2012-08-13 CN CN201280030112.0A patent/CN103608432B/zh active Active
- 2012-08-13 WO PCT/US2012/050513 patent/WO2013028379A2/en not_active Ceased
- 2012-08-13 RU RU2013154776/04A patent/RU2556218C1/ru active
- 2012-08-13 EP EP12825585.8A patent/EP2744876B1/en active Active
Also Published As
| Publication number | Publication date |
|---|---|
| KR20140025516A (ko) | 2014-03-04 |
| EP2744876A2 (en) | 2014-06-25 |
| RU2013154776A (ru) | 2015-06-20 |
| WO2013028379A3 (en) | 2013-04-18 |
| CN103608432A (zh) | 2014-02-26 |
| CN103608432B (zh) | 2016-01-06 |
| WO2013028379A2 (en) | 2013-02-28 |
| KR101603396B1 (ko) | 2016-03-14 |
| EP2744876B1 (en) | 2018-07-04 |
| EP2744876A4 (en) | 2015-04-08 |
| RU2556218C1 (ru) | 2015-07-10 |
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