SU1214726A1 - Method of producing low-molecular olefins - Google Patents
Method of producing low-molecular olefins Download PDFInfo
- Publication number
- SU1214726A1 SU1214726A1 SU843810282A SU3810282A SU1214726A1 SU 1214726 A1 SU1214726 A1 SU 1214726A1 SU 843810282 A SU843810282 A SU 843810282A SU 3810282 A SU3810282 A SU 3810282A SU 1214726 A1 SU1214726 A1 SU 1214726A1
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- mordenite
- catalyst
- zirconium silicate
- producing low
- silicate carrier
- Prior art date
Links
- 238000000034 method Methods 0.000 title claims description 5
- 150000001336 alkenes Chemical class 0.000 title description 6
- 239000003054 catalyst Substances 0.000 claims description 17
- 229910052680 mordenite Inorganic materials 0.000 claims description 13
- GFQYVLUOOAAOGM-UHFFFAOYSA-N zirconium(iv) silicate Chemical compound [Zr+4].[O-][Si]([O-])([O-])[O-] GFQYVLUOOAAOGM-UHFFFAOYSA-N 0.000 claims description 11
- 238000000197 pyrolysis Methods 0.000 claims description 7
- 229930195733 hydrocarbon Natural products 0.000 claims description 3
- 150000002430 hydrocarbons Chemical class 0.000 claims description 3
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 claims description 2
- 239000002253 acid Substances 0.000 claims description 2
- 238000004519 manufacturing process Methods 0.000 claims description 2
- 229910052750 molybdenum Inorganic materials 0.000 claims description 2
- 239000011733 molybdenum Substances 0.000 claims description 2
- 229910052759 nickel Inorganic materials 0.000 claims description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims 2
- 239000004215 Carbon black (E152) Substances 0.000 claims 1
- 239000010941 cobalt Substances 0.000 claims 1
- 229910017052 cobalt Inorganic materials 0.000 claims 1
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 claims 1
- VLAPMBHFAWRUQP-UHFFFAOYSA-L molybdic acid Chemical compound O[Mo](O)(=O)=O VLAPMBHFAWRUQP-UHFFFAOYSA-L 0.000 description 8
- 229910021536 Zeolite Inorganic materials 0.000 description 6
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 6
- 239000010457 zeolite Substances 0.000 description 6
- 150000002500 ions Chemical class 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 229910020630 Co Ni Inorganic materials 0.000 description 2
- -1 C4Hb Chemical class 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical class OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000001354 calcination Methods 0.000 description 1
- 239000000017 hydrogel Substances 0.000 description 1
- 238000005342 ion exchange Methods 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 235000019353 potassium silicate Nutrition 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 229910001415 sodium ion Inorganic materials 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- ZXAUZSQITFJWPS-UHFFFAOYSA-J zirconium(4+);disulfate Chemical compound [Zr+4].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O ZXAUZSQITFJWPS-UHFFFAOYSA-J 0.000 description 1
Landscapes
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Description
Изобретение относитс к способу получени ниткомолекул рных олефино- вых углеводородов, вл ющихс ценньм сырьем дл органического и нефтехимического синтеза, путем пиролиза никокачественного нефт ного сырь .The invention relates to a method for producing nitric molecular olefinic hydrocarbons, which are valuable raw materials for organic and petrochemical synthesis, by pyrolysis of poor-quality petroleum feedstock.
Цель изобретени - повьшение выхода целевого продукта - низкомоле- кул рньгх олефинов при пиролизе углеводородного сырь .The purpose of the invention is to increase the yield of the target product - low molecular weight olefins during the pyrolysis of hydrocarbons.
Пример 1. Гидрогель носител получают методом совместного осаждени из растворов жидкого стекла и подкисленной серной кислотой соли сернокислого циркони при 20 и РН 8,5.Example 1. A carrier hydrogel is prepared by the method of co-precipitating from solutions of liquid glass and acidified with sulfuric acid salt of zirconium sulfate at 20 and PH 8.5.
Со ЬЧ и Со Ni - формы морденита получают методом ионного обмена. В последующем, дл получени цеолитсо- держащего катализатора 80 г цирко- нийсиликатного носител , 20 г цеолит Ni - морденит (степень обмена ионов Na на ионы зкв.%) и 7,9 г молибденовой кислоты тщательно перемешивают , сушат при комнатной температуре и подвергают ступенчатой прокалке при 110, 250, 350, 450, 550°С в течение 4 ч каждый раз. Полученный катализатор содержит цирконийсили- катного носител 74,2%, Ni-мордени- та 18,5%, дополнительно модифицированный 7,3% молибденовой кислотой на массу катализатора.Co LCH and Co Ni — mordenite forms are obtained by ion exchange. Subsequently, to obtain a zeolite-containing catalyst, 80 g of a zirconium silicate carrier, 20 g of a zeolite Ni — mordenite (the degree of exchange of Na ions for ions Sq.%) And 7.9 g of molybdic acid are thoroughly mixed, dried at room temperature and subjected to stepwise calcining at 110, 250, 350, 450, 550 ° C for 4 h each time. The resulting catalyst contains a zirconium silicate carrier 74.2%, Ni-mordenite 18.5%, additionally modified with 7.3% molybdic acid per catalyst weight.
Результаты гшролиза низкокачественного бензина в присутствии данного катализатора представлены в табл, 1.The results of low-grade gasoline grololiza in the presence of this catalyst are presented in Table 1.
Пример 2, Цирконийсиликат- ньй носитель получают как описано в примере 1. Дл получени катализатора используют Со-морденит (степень обмена Na на Со 65 экв.%) и 9,0 г молибденовой кислоты. Полученный катализатор содержит цирконийсиликат ного носител 73,5%, Со-морденита 18,3%, модифицированный С,2 мас.% молибденовой кислотой. Результать пиролиза бензина представлены в табл. 2.Example 2 A zirconium silicate carrier is prepared as described in Example 1. For the preparation of the catalyst, Co-mordenite (degree of exchange of Na for Co 65 eq.%) And 9.0 g of molybdic acid are used. The resulting catalyst contains a zirconium silicate carrier 73.5%, Co-mordenite 18.3%, modified C, 2 wt.% Molybdic acid. Take out the pyrolysis of gasoline are presented in table. 2
Пример 3. Катализатор получают как описаЕ1о в примере 1, толькоExample 3. The catalyst receive as opaE1O in example 1, only
о качестве цеолита используют Со Ni - -морденит (степень обмена Na на ионы и 35 экв.% соответствен47262about the quality of the zeolite, Co Ni - α-mordenite is used (the degree of exchange of Na for ions and 35 eq.%, respectively, 47262
но). Полученный катализатор имеет такой же состав, как катализатор при- мера 1.but). The catalyst obtained has the same composition as the catalyst of Example 1.
Результаты пи)олиза бензина пред- ставлены в табл, 3.The results of pi) gasoline olisa are presented in Table 3.
Пример 4. Цирконийсиликат- ный носитель получают, как в примере 1, Дл получени цеолитсодержаще- го катализатора используют Ni-морде- 0 нит (степень обмена Na на ионы 60 экв.%) и 8,4 г молибденовой кислоты . Полученный катализатор содержит цирконийсиликатного носител 73,9%, морденита 18,4%, модифициро- 5 ванный 7,7 мас.% молибденовой кислотой .Результаты пиролиза представлены в табл. 4.Example 4. A zirconium silicate carrier is prepared as in Example 1. To obtain a zeolite-containing catalyst, a Ni-mordetnite (degree of exchange of Na for ions of 60 eq.%) And 8.4 g of molybdic acid is used. The resulting catalyst contains a zirconium silicate carrier 73.9%, mordenite 18.4%, modified with 7.7 wt.% Molybdic acid. The results of pyrolysis are presented in Table. four.
Пример 5. Цирконийсиликат- ный носитель получают, как описано 0 в примере 1. Дл получени цеолитсо- держащего катализатора смешивают 85 г цирконийсиликатного носител , 15 г цеолита-морденита (степень обмена ионы Ni 60 зкв. %) и 5 7,9 г молибденовой кислоты. Полученный катализатор содержит цирконийсиликатного носител 78,8%, Ni-мордени- та 13,9%, модифицированный 7,3 мас.% молибденовой кислотой.Example 5. A zirconium silicate carrier is prepared as described in Example 1. In order to obtain a zeolite-containing catalyst, 85 g of a zirconium silicate carrier, 15 g of zeolite-mordenite (a degree of exchange of Ni ions of 60 Sv.%) And 5 7.9 g of molybdenum acid. The resulting catalyst contains a zirconium silicate carrier 78.8%, Ni-mordenite 13.9%, modified 7.3% by weight molybdic acid.
3 Результаты пиролиза бензина представлены в табл.-53 The results of the pyrolysis of gasoline are presented in Table-5
Таким образом, предлагаемый способ получени низкомолекул рных олефинов пиролизом низкокачественного бензина на цеолитсодержащих катализаторах , состо щих из цирконийсиликатного носител . Со, Ni, CoNi-форм морденита и дополнительно модифицированных молибденовой кислотой в ко- личестве 7,3 - 8,2 мас.%, превосходит известный способ по выходу целевого продукта. При 600 и 650 С, объемной скорости 1 и 3 ч сумма низкомолекул рных олефинов, включа , С4Нб, в составе газа составл ет 80,7- 90,0 мас,% или сумма низкомолекул рных олефинов ( С. ) в составе газа составл ет 78,6 - 89,0 мас.% при выходе газа 75-93,0%. По известному способу сумма низкомолекул рных олефинов в составе газа составл ет 73,7-87,6 мас.% при выходе газа 70-88 мас.%.Thus, the proposed method of producing low molecular weight olefins by the pyrolysis of low quality gasoline on zeolite-containing catalysts consisting of a zirconium silicate carrier. Co, Ni, CoNi-forms of mordenite and additionally modified by molybdic acid in the amount of 7.3–8.2 wt.% Exceed the known method in the yield of the target product. At 600 and 650 ° C, the space velocity of 1 and 3 hours is the sum of low molecular weight olefins, including C4Hb, in the gas composition is 80.7- 90.0 wt%, or the sum of low molecular weight olefins (C.) in the gas composition is 78.6 - 89.0 wt.% When the gas output 75-93,0%. In a known manner, the amount of low molecular weight olefins in the gas composition is 73.7-87.6% by weight with a gas output of 70-88% by weight.
00
60012,3 74,9 1,3 2,2 3,0 38,0 1,0 30,6 1,8 17,8 2,4 1,9 88,360012.3 74.9 1.3 2.2 3.0 38.0 1.0 30.6 1.8 17.8 2.4 1.9 88.3
65012,8 86,0 1,2 5,5 3,1 39,2 1,3 31,0 1,1 14,t 1,1 2,4 86,765012.8 86.0 1.2 5.5 3.1 39.2 1.3 31.0 1.1 14, t 1.1 2.4 86.7
Таблица 2table 2
60012,7 75,0 1,2 2,9 3,5 39,9 1,7 28,9 1,6 14,8 3,9 1,6 85,260012.7 75.0 1.2 2.9 3.5 39.9 1.7 28.9 1.6 14.8 3.9 1.6 85.2
i5013,0 85,0 1,3 4,5 5,3 37,0 1,6 25,8 1,7 15,8 4,9 2,1 80,7i5013.0 85.0 1.3 4.5 5.3 37.0 1.6 25.8 1.7 15.8 4.9 2.1 80.7
65013,2 93,0 1,0 1,6 4,0 38,1 1,5 32,2 1,3 12,0 5,4 2,9 85,265013.2 93.0 1.0 1.6 4.0 38.1 1.5 32.2 1.3 12.0 5.4 2.9 85.2
6503 3,7 82,0 1,0 1,7 4,8 39,6 1,1 34,0 1,0 13,4 2,4 1,0 88,06503 3.7 82.0 1.0 1.7 4.8 39.6 1.1 34.0 1.0 13.4 2.4 1.0 88.0
Таблица 1Table 1
Таблица 3Table 3
600 650600 650
2,5 79,0 1,2 4,2 4,2 38,2 1,2 31,7 1,6 13,6 2,6 1,5 85,0 2,8 85,0 1,3 5,0 4,7 37,9 2,0 35,0 1,4 9,5 1,9 1,3 83,72.5 79.0 1.2 4.2 4.2 38.2 1.2 31.7 1.6 13.6 2.6 1.5 85 85 2.8 85.0 1.3 5, 0 4.7 37.9 2.0 35.0 1.4 9.5 1.9 1.3 83.7
60012,5 78,0 1,2 3,3 3,4 37,2 1,0 31,5 4,1 17,3 1,0 1,0 87,060012.5 78.0 1.2 3.3 3.4 37.2 1.0 31.5 4.1 17.3 1.0 1.0 87.0 87
65012,9 90,0 1,0 1,6 3,5 38,1 1,5 32,2 1,3 14,0 4,2 2,6 86,965012.9 90.0 1.0 1.6 3.5 38.1 1.5 32.2 1.3 14.0 4.2 2.6 86.9
65033,2 84,0 1,0 2,0 2,0 39,7 1,4 33,0 1,6 16,3 2,0 1,0 90,065033.2 84.0 1.0 2.0 2.0 39.7 1.4 33.0 1.6 16.3 2.0 1.0 90.0
Редактор И. Сегл никEditor I. Segl nick
Составитель Р. АбудльмановCompiled by R. Abudlmanov
Техред Т.ТуликКорректорВ, Бут гаTehred T.TulikKorrektorV, But ha
Заказ 856/37Тираж 483 ПодписноеOrder 856 / 37Card 483 Subscription
ВНИИПИ Государственного комитета СССРVNIIPI USSR State Committee
по делам изобретений и открытий 113035, Москва, Ж-35, Раушска наб., д. 4/5for inventions and discoveries 113035, Moscow, Zh-35, Raushsk nab., 4/5
Филиал ППП Патент, г. Ужгород, ул. Проектна , 4Branch PPP Patent, Uzhgorod, st. Project, 4
Таблица 4Table 4
Таблица 5Table 5
Claims (1)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SU843810282A SU1214726A1 (en) | 1984-11-01 | 1984-11-01 | Method of producing low-molecular olefins |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SU843810282A SU1214726A1 (en) | 1984-11-01 | 1984-11-01 | Method of producing low-molecular olefins |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| SU1214726A1 true SU1214726A1 (en) | 1986-02-28 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| SU843810282A SU1214726A1 (en) | 1984-11-01 | 1984-11-01 | Method of producing low-molecular olefins |
Country Status (1)
| Country | Link |
|---|---|
| SU (1) | SU1214726A1 (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5380690A (en) * | 1993-03-29 | 1995-01-10 | China Petro-Chemical Corporation | Cracking catalyst for the production of light olefins |
| US5670037A (en) * | 1993-11-05 | 1997-09-23 | China Petro-Chemical Corporation | Process for producing light olefins by catalytic conversion of hydrocarbons |
| WO2008028343A1 (en) | 2006-08-31 | 2008-03-13 | China Petroleum & Chemical Corporation | A process for catalytic converting hydrocarbons |
| WO2008034299A1 (en) | 2006-08-31 | 2008-03-27 | China Petroleum & Chemical Corporation | A catalyst for converting hydrocarbons |
| US7923399B2 (en) | 2004-03-31 | 2011-04-12 | China Petroleum & Chemical Corporation | Zeolite-containing hydrocarbon-converting catalyst, the preparation process thereof, and a process for converting hydrocarbon oils with the catalyst |
| US9486795B2 (en) | 2007-06-27 | 2016-11-08 | China Petroleum & Chemical Corporation | Catalytic cracking catalyst, its preparation and use |
-
1984
- 1984-11-01 SU SU843810282A patent/SU1214726A1/en active
Non-Patent Citations (1)
| Title |
|---|
| Суханов В.П. Каталитические процессы в нефтепереработке. М.: Хими , 1979, с. 11. Авторское свидетельство СССР № 1057520, кл. С 10 G11/00, 1963. * |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5380690A (en) * | 1993-03-29 | 1995-01-10 | China Petro-Chemical Corporation | Cracking catalyst for the production of light olefins |
| US5670037A (en) * | 1993-11-05 | 1997-09-23 | China Petro-Chemical Corporation | Process for producing light olefins by catalytic conversion of hydrocarbons |
| US7923399B2 (en) | 2004-03-31 | 2011-04-12 | China Petroleum & Chemical Corporation | Zeolite-containing hydrocarbon-converting catalyst, the preparation process thereof, and a process for converting hydrocarbon oils with the catalyst |
| WO2008028343A1 (en) | 2006-08-31 | 2008-03-13 | China Petroleum & Chemical Corporation | A process for catalytic converting hydrocarbons |
| WO2008034299A1 (en) | 2006-08-31 | 2008-03-27 | China Petroleum & Chemical Corporation | A catalyst for converting hydrocarbons |
| US8716163B2 (en) | 2006-08-31 | 2014-05-06 | China Petroleum & Chemical Corporation | Hydrocarbon conversion catalyst |
| US8900445B2 (en) | 2006-08-31 | 2014-12-02 | China Petroleum & Chemical Corporation | Process for the catalytic conversion of hydrocarbons |
| US9486795B2 (en) | 2007-06-27 | 2016-11-08 | China Petroleum & Chemical Corporation | Catalytic cracking catalyst, its preparation and use |
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