SU48206A1 - Catalyst Preparation Method - Google Patents
Catalyst Preparation MethodInfo
- Publication number
- SU48206A1 SU48206A1 SU171393A SU171393A SU48206A1 SU 48206 A1 SU48206 A1 SU 48206A1 SU 171393 A SU171393 A SU 171393A SU 171393 A SU171393 A SU 171393A SU 48206 A1 SU48206 A1 SU 48206A1
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- artists
- catalyst preparation
- compounds
- catalyst
- catalysts
- Prior art date
Links
- 239000003054 catalyst Substances 0.000 title description 10
- 238000002360 preparation method Methods 0.000 title 1
- 150000001875 compounds Chemical class 0.000 description 6
- 238000000034 method Methods 0.000 description 4
- 239000003502 gasoline Substances 0.000 description 3
- 229910052739 hydrogen Inorganic materials 0.000 description 3
- 239000001257 hydrogen Substances 0.000 description 3
- 238000005984 hydrogenation reaction Methods 0.000 description 3
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- PHFQLYPOURZARY-UHFFFAOYSA-N chromium trinitrate Chemical compound [Cr+3].[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O PHFQLYPOURZARY-UHFFFAOYSA-N 0.000 description 2
- VQWFNAGFNGABOH-UHFFFAOYSA-K chromium(iii) hydroxide Chemical compound [OH-].[OH-].[OH-].[Cr+3] VQWFNAGFNGABOH-UHFFFAOYSA-K 0.000 description 2
- 238000006477 desulfuration reaction Methods 0.000 description 2
- 230000023556 desulfurization Effects 0.000 description 2
- 239000007791 liquid phase Substances 0.000 description 2
- 239000002574 poison Substances 0.000 description 2
- 231100000614 poison Toxicity 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 1
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 1
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 1
- 239000005977 Ethylene Substances 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- ZCDOYSPFYFSLEW-UHFFFAOYSA-N chromate(2-) Chemical class [O-][Cr]([O-])(=O)=O ZCDOYSPFYFSLEW-UHFFFAOYSA-N 0.000 description 1
- 229910052804 chromium Inorganic materials 0.000 description 1
- 239000011651 chromium Substances 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 1
- 239000003350 kerosene Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 150000003464 sulfur compounds Chemical group 0.000 description 1
- 230000009897 systematic effect Effects 0.000 description 1
- 239000012808 vapor phase Substances 0.000 description 1
Landscapes
- Catalysts (AREA)
- Lubricants (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Description
Описываемые в научной и патентной литературе методы гидрогенизационной очистки углеводородных смесей основаны на том, что в присутствии специальных катализаторов и - водорода происходит распад сернистых соединений с образованием сероводорода и насыщение водородом непредельных соединений. Получаемые при этом, в определенных услови х, продукты содержат незначительное количество серы и оказываютс стойкими в отношении смолообразовани как при хранении, так и в процессе сжигани топлива в двигател х.The methods of hydrogenation purification of hydrocarbon mixtures described in the scientific and patent literature are based on the fact that in the presence of special catalysts and - hydrogen decomposition of sulfur compounds occurs with the formation of hydrogen sulfide and saturation of unsaturated compounds with hydrogen. The resulting, under certain conditions, products contain an insignificant amount of sulfur and are resistant to resin formation both during storage and in the process of burning fuel in engines.
Катализаторами дл осуществлени подобного рода процесса служат обычно соединени элементов б-й группы, но могут также примен тьс и соединени элементов других групп. Так, например, в патенте № 17448 от 18 декабр 1928 года имеетс указание на применение в качестве катализаторов COS, FeS, ZnS, NiS, MnS как непосредственно, так и с добавками к ним окисных соединений Wo, Сг и др.; англ, патент № 363711 указывает катализаторы 4-7 групп (окислы и их соединени ); в амер. пат. № 1989388 .Юниверсал Ойль Продукте К° указываетс , что обессеривание производитс над хроматами металлов; в амер. пат. № 1905353 указываетс , что катализатором служит актквнмй гель СГ|О, полученный из раствора нитрата хрома ос«ждением NHt ОН.Compounds of elements of the 6th group usually serve as catalysts for carrying out this kind of process, but compounds of elements of other groups can also be used. Thus, for example, in patent No. 17448 of December 18, 1928, there is an indication of the use of catalysts COS, FeS, ZnS, NiS, MnS both directly and with additives to them oxide compounds Wo, Cr, etc .; Patent No. 363711 indicates catalysts of 4-7 groups (oxides and their compounds); in Amer. pat No. 1989388. Universal Oil Product K ° indicates that desulfurization is carried out on metal chromates; in Amer. pat No. 1905353 indicates that the SG / O gel obtained from chromium nitrate solution is used as a catalyst by waiting for NHt OH.
Wielbur, Lazier and Vaughen (Pan, Chem. Soc. 54, 3080, 1932) упбтребл ли дл гидрировани этилена в качестве катализатора СгзОз, предварительно пропуска через него водород при 400. Несмотр на наличие в литературе данных по применению в качестве катализатора гидрата окиси хрома дл гидрогенизационной очистки, нигде в литературе нет указаний на необходимость предварительной обработки гидрата окиси хрома в особых услови х с целью получени высокоактивного и отравостойкого катализатора.Wielbur, Lazier and Vaughen (Pan, Chem. Soc. 54, 3080, 1932) used to hydrogenate ethylene as a Cg3O3 catalyst, pre-passing hydrogen through it at 400. Despite the availability of literature data on the use of chromium hydroxide as a catalyst for hydrogenation purification, there is no indication anywhere in the literature that it is necessary to pretreat chromium hydroxide under special conditions in order to obtain a highly active and poison-resistant catalyst.
Авторы насто щего изобретени установили , что не вс кий гель вл етс высокоактивным и отравостойким катализатором .The inventors have found that a non-all gel is a highly active and poison-resistant catalyst.
В результате систематической работы по обессериванию и стабилизации методом гидрогенизации дестиллатов, богатых сернистыми и непредельными соединени ми (бензины Веймарнских и Гдовских сланцев, бензины Черемховских углей, бензины и керосины Ишимбаевской нефти, бензины парофазного и жидкофазного крэкинга), авторам удалось добитьс применением специально обработанного гидрата окиси хрома, что указйнн| 1е pfejwe дестиллат уже приAs a result of systematic work on the desulfurization and stabilization by the method of hydrogenation of distillates rich in sulfurous and unsaturated compounds (Weimarn and Gdov shale gasolines, Cheremkhovsky gasolines, Ishimbayevo gasoline and kerosene, vapor-phase and liquid-phase gasoline, gasoline craters, by the artists, as a theme, the author, and the masters), by the artists, as a theme, the artist, the artists, and the masters of the artwork groups, the author of the artwork of the artists, and the vapor-liquid and liquid-phase cracking patterns by the artists, as the theme by the artists, the author, and the masters. chromium that ukazinn | 1e pfejwe destillat already at
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SU171393A SU48206A1 (en) | 1935-06-18 | 1935-06-18 | Catalyst Preparation Method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SU171393A SU48206A1 (en) | 1935-06-18 | 1935-06-18 | Catalyst Preparation Method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| SU48206A1 true SU48206A1 (en) | 1936-08-31 |
Family
ID=48361179
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| SU171393A SU48206A1 (en) | 1935-06-18 | 1935-06-18 | Catalyst Preparation Method |
Country Status (1)
| Country | Link |
|---|---|
| SU (1) | SU48206A1 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4919211A (en) * | 1987-07-30 | 1990-04-24 | National Research Development Corporation | Clod crumbler |
-
1935
- 1935-06-18 SU SU171393A patent/SU48206A1/en active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4919211A (en) * | 1987-07-30 | 1990-04-24 | National Research Development Corporation | Clod crumbler |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US4062762A (en) | Process for desulfurizing and blending naphtha | |
| GB1577821A (en) | Process for the selective desulphurization of cracked naphthas | |
| US2433603A (en) | Catalytic treatment of petroleum hydrocarbons | |
| SU48206A1 (en) | Catalyst Preparation Method | |
| US2298347A (en) | Treatment of hydrocarbon oils | |
| DE971558C (en) | Process for the hydrocatalytic desulphurization of crude petroleum containing vanadium and sodium | |
| US2091239A (en) | Treating hydrocarbon oils | |
| US2037789A (en) | Treatment of hydrocarbon oils | |
| Pimerzin et al. | Catalysts based on molybdenum and tungsten heteropoly compounds for the hydrotreatment of oil fractions | |
| US3507784A (en) | Hydrorefining catalyst preparation and the use thereof | |
| EP0002819A1 (en) | Method for improving combustion processes | |
| US2298346A (en) | Treatment of hydrocarbon oils | |
| US1889388A (en) | Treatment of hydrocarbon oils | |
| US2574449A (en) | Process of catalytic desulfurization of naphthenic petroleum hydrocarbons followed by catalytic cracking | |
| US2905624A (en) | Manufacture of lubricating oil | |
| US2037781A (en) | Treatment of hydrocarbon oils | |
| US2339717A (en) | Process for reclaiming used and partially oxidized lubricating oil | |
| US2759873A (en) | Sweetening of hydrocarbon oils with raw clay followed by copper sweetening | |
| MX172339B (en) | PROCEDURE FOR THE MANUFACTURE OF CHEROSENE AND / OR PETROL | |
| GB686701A (en) | Improvements in or relating to the forming of urea or thiourea complexes | |
| US2877172A (en) | Combined thermal reforming, catalytic cracking and hydrofining process to improve engine cleanliness | |
| GB652760A (en) | Hydrocarbon fuel suitable for jet combustion purposes | |
| US3264211A (en) | Pour point reduction process | |
| RU2773141C1 (en) | Method for processing heavy oil in the presence of an in situ catalyst | |
| RU2716165C1 (en) | Method of producing low-sulfur diesel fuel and low-sulfur gasoline |