SU557812A1 - Reactor - Google Patents
ReactorInfo
- Publication number
- SU557812A1 SU557812A1 SU1998318A SU1998318A SU557812A1 SU 557812 A1 SU557812 A1 SU 557812A1 SU 1998318 A SU1998318 A SU 1998318A SU 1998318 A SU1998318 A SU 1998318A SU 557812 A1 SU557812 A1 SU 557812A1
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- zone
- reaction
- reactor
- cone
- japanese patent
- Prior art date
Links
Landscapes
- Physical Or Chemical Processes And Apparatus (AREA)
Description
с насосом в газлифт 7 и транспортирует теплоноситель из зоны 4 подогрева в буферную емкость 5 и реакционную зону 3, откуда переливаетс в конус 9, далее - в зону И и возвращаетс в зону 4 подогрева. Сырье, испар емое в теплообменнике 12, через сырьевой патрубок 8 вводитс в конус 9 реакционной зоны 3, в котором протекает процесс изомеризации а-пинена. За счет высокой скорости сырь на выходе из патрубка 8 происходит инжекци теплоносител в конус 9 и его интенсивное перемешивание с исходным сырьем . Благодар большой разности удельных весов в зоне 11 сепарации протекает быстрое и эффективное разделение газол идкостной смеси . На выходе из зоны И продукты реакции охлаждаютс вводимым через патрубок 13 хладагентом (азот, вод ной пар, метан, а-пинен и т. п.) с последующим отводом смеси продуктов через холодильник 14. Дл выравнивани темПературного пол в реакционной зоне 3 предусмотрена дополнительна подпитка ее расплавом через патрубок 15. Благодар усеченному конусу 9 и эффекту инжекции интенсифицируетс циркул ци теплоносител в системе. При этом одновременно вследствие пр моточного движени сырь и теплоносител предотвращаетс унос последнего из аппарата.with the pump into the gas lift 7 and transports the coolant from the heating zone 4 to the buffer tank 5 and the reaction zone 3, from where it is poured into the cone 9, then to the zone And and returns to the heating zone 4. The raw material evaporated in the heat exchanger 12 through the raw pipe 8 is introduced into the cone 9 of the reaction zone 3, in which the process of isomerization of α-pinene takes place. Due to the high speed of the raw material at the outlet of the nozzle 8, the coolant is injected into the cone 9 and is intensively mixed with the feedstock. Due to the large difference in specific weights in the separation zone 11, a quick and efficient separation of the gas-liquid mixture proceeds. At the exit from the zone I, the reaction products are cooled by a coolant introduced through the pipe 13 (nitrogen, water vapor, methane, a-pinene, etc.) followed by drainage of the product mixture through the cooler 14. Additional leveling is provided in the reaction zone 3 to level the temperature. it is fed by melt through the nozzle 15. Due to the truncated cone 9 and the injection effect, the circulation of the coolant in the system is intensified. At the same time, due to the direct movement of the raw material and the coolant, the latter is prevented from being carried away from the apparatus.
Claims (3)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SU1998318A SU557812A1 (en) | 1974-02-11 | 1974-02-11 | Reactor |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SU1998318A SU557812A1 (en) | 1974-02-11 | 1974-02-11 | Reactor |
Publications (1)
Publication Number | Publication Date |
---|---|
SU557812A1 true SU557812A1 (en) | 1977-05-15 |
Family
ID=20576458
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
SU1998318A SU557812A1 (en) | 1974-02-11 | 1974-02-11 | Reactor |
Country Status (1)
Country | Link |
---|---|
SU (1) | SU557812A1 (en) |
-
1974
- 1974-02-11 SU SU1998318A patent/SU557812A1/en active
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