SU109684A2 - Method for catalytic hydrocracking of natural and artificial hydrocarbons and their derivatives - Google Patents
Method for catalytic hydrocracking of natural and artificial hydrocarbons and their derivativesInfo
- Publication number
- SU109684A2 SU109684A2 SU429202A SU429206A SU109684A2 SU 109684 A2 SU109684 A2 SU 109684A2 SU 429202 A SU429202 A SU 429202A SU 429206 A SU429206 A SU 429206A SU 109684 A2 SU109684 A2 SU 109684A2
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- hydrocarbons
- derivatives
- natural
- artificial
- catalytic hydrocracking
- Prior art date
Links
Landscapes
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Description
Изобретение относитс к области каталитического гидрокрекинга т желы .х у|М1еводородов и их производных и ката.титической конверсии иолучаюиихс при этом углеводородных газов. При переработке углеводородов и их производных известными сиособамн не примен етс комбинаци процесса гидрогенизации с процессом каталитической конверсии получа1ОП1,ихс уг.леводородных газов, что делает эт1 способы дорогими н гро.моздкими.This invention relates to the field of catalytic hydrocracking of heavy hydrogen and hydrogen derivatives and their derivatives and the conversion of hydrocarbons to hydrocarbons. In the processing of hydrocarbons and their derivatives by the known methods, the combination of the hydrogenation process with the catalytic conversion process and the production of hydrocarbon gases are not used, which makes these methods expensive and cumbersome.
Предложенный способ свободен от указанных недостатков благодар ко.мбинации процесса гидрогенизации с процессом каталитической конверсии в единой технологической схеме с применением одного и того же катализатора дл обоих процессов и использованием тепла выжига кокса, образуюпгегос к процессе идрОКреки1Па, дл конверсии углеводородов .The proposed method is free from these drawbacks due to the combination of the hydrogenation process with the catalytic conversion process in a single technological scheme using the same catalyst for both processes and using the heat of coke burning, which forms the process for conversion of hydrocarbons.
Согласно предложенному способу, процесс гидрокрекинга, описанный в авт. св. ЛЬ 109423, и процесс каталитической конверсии осугцествл ютс 15 ОДНОМ тех;:о.10Г1 ческ 1 комплексе с единой схемой потоков катализатора и с замкнутым тепловым балансом.According to the proposed method, the hydrocracking process described in ed. St. LI 109423, and the process of catalytic conversion were made suspiciously 15 ONE of those;: about 10G1 and 1 complex with a single scheme of catalyst flows and with a closed thermal balance.
Конверси проводитс в движущемс или кип щем слое катализатора под тем же давлепием, которое примен етс при процессе гидрокрекинга , и не требует сероочистки газов , ввиду сероустойчнвости примен емого катализатора.Conversion is carried out in a moving or fluidized bed of catalyst under the same pressure that is used in the hydrocracking process, and does not require gas desulfurization, due to the sulfur resistance of the used catalyst.
Процесс конверсии по предложенной технологической схеме может быть ,ествле1 с малыми избытками пара. Папример, при конверсии метана достаточно иметь 3 мол воды на 1 моль газа.The process of conversion according to the proposed technological scheme can be, with small excesses of steam. For example, in methane conversion, it is sufficient to have 3 moles of water per 1 mole of gas.
Предложенный способ исключает необходимость сооружени отдельного водородного завода, цеха или установки дл производства специального катализатора дл конверсии утлеводородных газов крекинга .The proposed method eliminates the need to construct a separate hydrogen plant, plant or plant for the production of a special catalyst for the conversion of hydrocarbon cracking gases.
Предмет изобретени Subject invention
Способ осуществлени каталитического гидрокрекинга естественныхA method for effecting catalytic hydrocracking of natural
и 1;скусствс1 11ых углеводородов и ихand 1; st 11th hydrocarbons and their
.№ 109684- 2 -.№ 109684- 2 -
производных по авт. св. № 109423,необходимого при гидрокрекинге воотличающийс тем, что тепло,дорода путем осуществлени конверполучаемое при выжиге кокса с по-сии углеводородных газов с вод верхности регенерируемого катали-ным паром. затора, используют дл получени derivatives on auth. St. No. 109423, which is necessary for hydrocracking, is distinguished by the fact that heat is reduced by performing the convertible from the burning of coke from the surface of hydrocarbon gases from the water recovered by catalytic steam. mash is used to obtain
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SU429202A SU109684A2 (en) | 1953-03-11 | 1953-03-11 | Method for catalytic hydrocracking of natural and artificial hydrocarbons and their derivatives |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SU429202A SU109684A2 (en) | 1953-03-11 | 1953-03-11 | Method for catalytic hydrocracking of natural and artificial hydrocarbons and their derivatives |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| SU109684A2 true SU109684A2 (en) | 1956-11-30 |
Family
ID=50193656
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| SU429202A SU109684A2 (en) | 1953-03-11 | 1953-03-11 | Method for catalytic hydrocracking of natural and artificial hydrocarbons and their derivatives |
Country Status (1)
| Country | Link |
|---|---|
| SU (1) | SU109684A2 (en) |
-
1953
- 1953-03-11 SU SU429202A patent/SU109684A2/en active
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