SU505375A3 - Способ получени котельного топлива - Google Patents
Способ получени котельного топливаInfo
- Publication number
- SU505375A3 SU505375A3 SU1856224A SU1856224A SU505375A3 SU 505375 A3 SU505375 A3 SU 505375A3 SU 1856224 A SU1856224 A SU 1856224A SU 1856224 A SU1856224 A SU 1856224A SU 505375 A3 SU505375 A3 SU 505375A3
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- hydrogen
- sulfur
- line
- stage
- aromatic
- Prior art date
Links
- 238000000034 method Methods 0.000 title claims description 37
- 239000000446 fuel Substances 0.000 title claims description 19
- 239000011593 sulfur Substances 0.000 claims description 95
- 229910052717 sulfur Inorganic materials 0.000 claims description 95
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 claims description 93
- 239000001257 hydrogen Substances 0.000 claims description 73
- 229910052739 hydrogen Inorganic materials 0.000 claims description 73
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 63
- 238000006477 desulfuration reaction Methods 0.000 claims description 59
- 230000023556 desulfurization Effects 0.000 claims description 59
- 238000009835 boiling Methods 0.000 claims description 48
- 239000002994 raw material Substances 0.000 claims description 46
- 239000003054 catalyst Substances 0.000 claims description 43
- 238000006243 chemical reaction Methods 0.000 claims description 42
- 230000008569 process Effects 0.000 claims description 29
- 239000007789 gas Substances 0.000 claims description 26
- 229930195733 hydrocarbon Natural products 0.000 claims description 18
- 150000002430 hydrocarbons Chemical class 0.000 claims description 18
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 claims description 15
- 229910000037 hydrogen sulfide Inorganic materials 0.000 claims description 13
- 239000004215 Carbon black (E152) Substances 0.000 claims description 8
- 238000004519 manufacturing process Methods 0.000 claims description 2
- 125000003118 aryl group Chemical group 0.000 description 63
- 239000010426 asphalt Substances 0.000 description 58
- 239000003921 oil Substances 0.000 description 55
- 239000011347 resin Substances 0.000 description 37
- 229920005989 resin Polymers 0.000 description 37
- 239000000047 product Substances 0.000 description 36
- 229920006395 saturated elastomer Polymers 0.000 description 30
- 238000001704 evaporation Methods 0.000 description 29
- 230000008020 evaporation Effects 0.000 description 27
- 239000007788 liquid Substances 0.000 description 27
- 238000004821 distillation Methods 0.000 description 19
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 17
- 239000010779 crude oil Substances 0.000 description 17
- 230000007423 decrease Effects 0.000 description 12
- 239000000126 substance Substances 0.000 description 12
- 230000000694 effects Effects 0.000 description 11
- 229910052751 metal Inorganic materials 0.000 description 11
- 239000002184 metal Substances 0.000 description 11
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 10
- 150000002431 hydrogen Chemical class 0.000 description 10
- 229930195734 saturated hydrocarbon Natural products 0.000 description 9
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 8
- 238000004517 catalytic hydrocracking Methods 0.000 description 8
- 150000002739 metals Chemical class 0.000 description 8
- OFBQJSOFQDEBGM-UHFFFAOYSA-N Pentane Chemical compound CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 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
- 238000005336 cracking Methods 0.000 description 6
- 239000003085 diluting agent Substances 0.000 description 6
- 239000000295 fuel oil Substances 0.000 description 6
- 230000008901 benefit Effects 0.000 description 5
- 230000015572 biosynthetic process Effects 0.000 description 5
- 229910052759 nickel Inorganic materials 0.000 description 5
- 238000000926 separation method Methods 0.000 description 5
- 238000007614 solvation Methods 0.000 description 5
- QZYDAIMOJUSSFT-UHFFFAOYSA-N [Co].[Ni].[Mo] Chemical compound [Co].[Ni].[Mo] QZYDAIMOJUSSFT-UHFFFAOYSA-N 0.000 description 4
- 239000003849 aromatic solvent Substances 0.000 description 4
- 239000012634 fragment Substances 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 230000004048 modification Effects 0.000 description 4
- 238000012986 modification Methods 0.000 description 4
- 239000001294 propane Substances 0.000 description 4
- 229910052720 vanadium Inorganic materials 0.000 description 4
- LEONUFNNVUYDNQ-UHFFFAOYSA-N vanadium atom Chemical compound [V] LEONUFNNVUYDNQ-UHFFFAOYSA-N 0.000 description 4
- 230000008859 change Effects 0.000 description 3
- 150000001875 compounds Chemical class 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- 238000002474 experimental method Methods 0.000 description 3
- 239000012530 fluid Substances 0.000 description 3
- 150000002605 large molecules Chemical class 0.000 description 3
- 229920002521 macromolecule Polymers 0.000 description 3
- 238000012545 processing Methods 0.000 description 3
- 238000005292 vacuum distillation Methods 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 241000234435 Lilium Species 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 150000001491 aromatic compounds Chemical class 0.000 description 2
- 239000007795 chemical reaction product Substances 0.000 description 2
- 230000003247 decreasing effect Effects 0.000 description 2
- 238000010790 dilution Methods 0.000 description 2
- 239000012895 dilution Substances 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 238000000605 extraction Methods 0.000 description 2
- 239000012467 final product Substances 0.000 description 2
- -1 for example Substances 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 210000005036 nerve Anatomy 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000003209 petroleum derivative Substances 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- FCEHBMOGCRZNNI-UHFFFAOYSA-N 1-benzothiophene Chemical class C1=CC=C2SC=CC2=C1 FCEHBMOGCRZNNI-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- 125000001931 aliphatic group Chemical group 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000011203 carbon fibre reinforced carbon Substances 0.000 description 1
- 238000005266 casting Methods 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- WHDPTDWLEKQKKX-UHFFFAOYSA-N cobalt molybdenum Chemical compound [Co].[Co].[Mo] WHDPTDWLEKQKKX-UHFFFAOYSA-N 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 230000006378 damage Effects 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 230000003009 desulfurizing effect Effects 0.000 description 1
- 230000001627 detrimental effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- IYYZUPMFVPLQIF-UHFFFAOYSA-N dibenzothiophene Chemical class C1=CC=C2C3=CC=CC=C3SC2=C1 IYYZUPMFVPLQIF-UHFFFAOYSA-N 0.000 description 1
- 239000002270 dispersing agent Substances 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 230000004907 flux Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000010763 heavy fuel oil Substances 0.000 description 1
- 125000000623 heterocyclic group Chemical group 0.000 description 1
- 238000007327 hydrogenolysis reaction Methods 0.000 description 1
- 150000002632 lipids Chemical class 0.000 description 1
- 239000000395 magnesium oxide Substances 0.000 description 1
- CPLXHLVBOLITMK-UHFFFAOYSA-N magnesium oxide Inorganic materials [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 1
- AXZKOIWUVFPNLO-UHFFFAOYSA-N magnesium;oxygen(2-) Chemical compound [O-2].[Mg+2] AXZKOIWUVFPNLO-UHFFFAOYSA-N 0.000 description 1
- 239000013521 mastic Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 150000002790 naphthalenes Chemical class 0.000 description 1
- 230000003533 narcotic effect Effects 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 230000002688 persistence Effects 0.000 description 1
- 230000002085 persistent effect Effects 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 238000004525 petroleum distillation Methods 0.000 description 1
- 125000001997 phenyl group Chemical class [H]C1=C([H])C([H])=C(*)C([H])=C1[H] 0.000 description 1
- 239000012264 purified product Substances 0.000 description 1
- 239000011541 reaction mixture Substances 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000012453 solvate Substances 0.000 description 1
- 238000000638 solvent extraction Methods 0.000 description 1
- 239000006188 syrup Substances 0.000 description 1
- 150000003568 thioethers Chemical group 0.000 description 1
- 229930192474 thiophene Natural products 0.000 description 1
- 150000003577 thiophenes Chemical class 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
- 210000003462 vein Anatomy 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 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
- C10G65/00—Treatment of hydrocarbon oils by two or more hydrotreatment processes only
- C10G65/02—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only
- C10G65/04—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including only refining steps
-
- 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
- C10G2300/107—Atmospheric residues having a boiling point of at least about 538 °C
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Liquid Carbonaceous Fuels (AREA)
- Catalysts (AREA)
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US20608371A | 1971-12-08 | 1971-12-08 |
Publications (1)
Publication Number | Publication Date |
---|---|
SU505375A3 true SU505375A3 (ru) | 1976-02-28 |
Family
ID=22764905
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
SU1856224A SU505375A3 (ru) | 1971-12-08 | 1972-12-07 | Способ получени котельного топлива |
Country Status (11)
Country | Link |
---|---|
US (1) | US3775305A (de) |
JP (1) | JPS5549117B2 (de) |
CA (1) | CA970313A (de) |
DD (1) | DD103259A5 (de) |
DE (1) | DE2259593A1 (de) |
FR (1) | FR2162523B1 (de) |
GB (1) | GB1414493A (de) |
IT (1) | IT973938B (de) |
NL (1) | NL7216546A (de) |
PL (1) | PL89064B1 (de) |
SU (1) | SU505375A3 (de) |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3775304A (en) * | 1971-12-08 | 1973-11-27 | Gulf Research Development Co | Increasing the ratio of aromatics to saturates in hydrodesulfurization of heavy asphaltic feed oil |
US3893909A (en) * | 1971-12-27 | 1975-07-08 | Universal Oil Prod Co | Fuel oil production by blending hydrodesulfurized vacuum gas oil and hydrodesulfurized deasphalted residuum |
US4565620A (en) * | 1984-05-25 | 1986-01-21 | Phillips Petroleum Company | Crude oil refining |
US4713221A (en) * | 1984-05-25 | 1987-12-15 | Phillips Petroleum Company | Crude oil refining apparatus |
WO1996017903A1 (en) * | 1994-11-25 | 1996-06-13 | Kvaerner Process Technology Ltd | Multi-step hydrodesulfurization process |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3429801A (en) * | 1965-12-06 | 1969-02-25 | Universal Oil Prod Co | Two-stage hydrorefining of asphaltene-containing oils |
US3409538A (en) * | 1967-04-24 | 1968-11-05 | Universal Oil Prod Co | Multiple-stage cascade conversion of black oil |
US4165064A (en) * | 1978-03-13 | 1979-08-21 | Fip, S.A. De C.V. | Gate valve |
JPS5547077A (en) * | 1978-09-01 | 1980-04-02 | Ippei Tamai | Water feeding apparatus in use of float formed with aperture |
-
1971
- 1971-12-08 US US00206083A patent/US3775305A/en not_active Expired - Lifetime
-
1972
- 1972-08-03 CA CA148,614A patent/CA970313A/en not_active Expired
- 1972-12-06 IT IT54531/72A patent/IT973938B/it active
- 1972-12-06 DE DE2259593A patent/DE2259593A1/de active Pending
- 1972-12-06 PL PL1972159938A patent/PL89064B1/pl unknown
- 1972-12-06 NL NL7216546A patent/NL7216546A/xx unknown
- 1972-12-07 FR FR7243517A patent/FR2162523B1/fr not_active Expired
- 1972-12-07 SU SU1856224A patent/SU505375A3/ru active
- 1972-12-07 DD DD167448A patent/DD103259A5/xx unknown
- 1972-12-08 JP JP12263672A patent/JPS5549117B2/ja not_active Expired
- 1972-12-08 GB GB5678472A patent/GB1414493A/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
US3775305A (en) | 1973-11-27 |
DD103259A5 (de) | 1974-01-12 |
JPS4866109A (de) | 1973-09-11 |
GB1414493A (en) | 1975-11-19 |
JPS5549117B2 (de) | 1980-12-10 |
IT973938B (it) | 1974-06-10 |
NL7216546A (de) | 1973-06-13 |
FR2162523B1 (de) | 1978-12-01 |
DE2259593A1 (de) | 1973-06-14 |
PL89064B1 (de) | 1976-10-30 |
FR2162523A1 (de) | 1973-07-20 |
CA970313A (en) | 1975-07-01 |
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