SU571292A1 - Apparatus for heat-mass exchange and chemical processes - Google Patents
Apparatus for heat-mass exchange and chemical processesInfo
- Publication number
- SU571292A1 SU571292A1 SU7502130585A SU2130585A SU571292A1 SU 571292 A1 SU571292 A1 SU 571292A1 SU 7502130585 A SU7502130585 A SU 7502130585A SU 2130585 A SU2130585 A SU 2130585A SU 571292 A1 SU571292 A1 SU 571292A1
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- heat
- equidistant
- heavy
- chemical processes
- mass exchange
- Prior art date
Links
- 238000001311 chemical methods and process Methods 0.000 title claims 2
- 238000005192 partition Methods 0.000 claims description 7
- 239000000203 mixture Substances 0.000 claims description 3
- 239000000463 material Substances 0.000 claims description 2
- 230000002730 additional effect Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- VJOVAKSZILJDBB-UHFFFAOYSA-N iodol Chemical compound IC=1NC(I)=C(I)C=1I VJOVAKSZILJDBB-UHFFFAOYSA-N 0.000 description 1
- 229950000077 iodol Drugs 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
Landscapes
- Cyclones (AREA)
Description
(54) АППАРАТ ДЛЯ ТЕПЛОМАССООВМЕННЫХ И ХИМИЧЕСКИХ ГГРОЦЕССОВ(54) APPARATUS FOR HEAT AND MASSIFICABLE AND CHEMICAL GROCESS
ми, а патрубки дл ввода транспортирующего агента и вывода т желой фракции установлены , соответственно, в начале первой и в конце последней секций эквидистантной перегородки .5The pipes for entering the transporting agent and for withdrawing the heavy fraction are installed, respectively, at the beginning of the first and at the end of the last sections of the equidistant partition .5
На фиг. 1 показано устройство предлагаемого аппарата, иродольный разрез; -la фиг. 2 - разрез А-А фиг. 1,FIG. 1 shows the device of the proposed apparatus, and an iodol section; -la FIG. 2 - section A-A of FIG. one,
В корпусе 1 аппарата установлена спи .ральна перегородка 2, патрубок 3 дл вво-ijo да транспортирукшего агента, эквидистант на секционированна перегородка 4, патрубок 5 дл вывода крупнодисперсной или т желой фракции, шарнирные заслонки 6, патрубок 7 дл ввода исходных попид сперс- ных материалов в смесей с неодинаковой плотностью, циклон 8 с патрубком 9 дл ,вывода легкой фракции..In the housing 1 of the apparatus, an oral partition 2 is installed, a pipe 3 for inlet and transport agent, an equidistant to a partitioned wall 4, a pipe 5 for the coarse or heavy fraction, articulated dampers 6, a pipe 7 for introducing the initial spacing materials in mixtures with unequal density, cyclone 8 with pipe 9 dl, the output of the light fraction ..
Аппарат работает следук цим образом. Исходные компоненты через патрубок 7 20 даютс в спиральнь1й канал. В последнем под действием центробежной сил|з1 и благодар зазорам между спиральной 2 и эквиднстачрой 4 перегородками щэоисходит перераспределение и переход исходных компонен- 5 тов пропорционально дентробе{5кному фактору разаелени крутшодасперскых т желых фракций во внешнюю часть спирального канала, ,отделенную перегородкой 4. Перешедшие фракции подхватываютс транспортирующим ;30 йгентом, который подаетс через патрубок 3, Остатки парогазовой взвеси или смеси фракций аз спирального канала поступают в цйкнон 8, где происходит разделение ва легкие в средние фракции, выводимые, соот ветственно, через патрубок 9 и коническую часть циклона. Т желые фракции через патрубок 5 выход т из аппарата.The device works in the following way. Source components through pipe 7-20 are fed into the spiral duct. In the latter, under the action of centrifugal forces | 3 and due to gaps between spiral 2 and equidistant 4 partitions, there is a redistribution and transition of the initial components in proportion to the detrobe {5knuyu factor of separation of the hard-hip and heavy fractions into the outer part of the spiral channel, separated by a partition 4. Recycled 4 picked up by the transporting; 30 agent, which is fed through the pipe 3, the residues of vapor-gas suspension or a mixture of fractions az of the spiral channel enter the pycnon 8, where the split occurs It’s easy to bring in light into the middle fractions, respectively, through pipe 9 and the conical part of the cyclone. Heavy fractions through the pipe 5 out of the apparatus.
На ичие эквидистантной секционированной перегородка повышает равномерность обработки, так как траектори движени I перешедших фракций во внешнюю часть спирального какала длиннее, чем траектори The presence of an equidistant partitioned partition increases the uniformity of processing, since the trajectory of movement of the I transferred fractions to the outer part of the spiral crock is longer than the trajectory of
движени мелкодисперсных или легких фракций , поэтому врем обработки их неодинаково .movements of fine or light fractions, therefore, their processing time is unequal.
Дополнителыюе регулирование времени пребывани в аппарате обрабатываемых компонентов осуществл етс соответствующей установкой шарнирных заслонок 6.Additional adjustment of the residence time in the apparatus of the components to be processed is carried out by appropriate installation of the hinged dampers 6.
Ввод через патрубок 3 транспортирующего агента ускор ет процессы обмена между крупнодисперсной (т желой) фракцией и транспортирующим агентом. Конструкци аппарата также позвол ет получить дополнительный эффект классификации готового продукта высокого качества по фракции.Entering through the nozzle 3 a transporting agent accelerates the exchange processes between the coarse (heavy) fraction and the transporting agent. The design of the apparatus also provides an additional effect of classifying the finished product of high quality by fraction.
Claims (2)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SU7502130585A SU571292A1 (en) | 1975-04-08 | 1975-04-08 | Apparatus for heat-mass exchange and chemical processes |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SU7502130585A SU571292A1 (en) | 1975-04-08 | 1975-04-08 | Apparatus for heat-mass exchange and chemical processes |
Publications (1)
Publication Number | Publication Date |
---|---|
SU571292A1 true SU571292A1 (en) | 1977-09-05 |
Family
ID=20618275
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
SU7502130585A SU571292A1 (en) | 1975-04-08 | 1975-04-08 | Apparatus for heat-mass exchange and chemical processes |
Country Status (1)
Country | Link |
---|---|
SU (1) | SU571292A1 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4623470A (en) * | 1981-11-09 | 1986-11-18 | Helipump, Inc. | Process and apparatus for separating or fractionating fluid mixtures |
US5405497A (en) * | 1990-08-28 | 1995-04-11 | Kamyr, Inc. | Method of chemically reacting a liquid with a gas in a vortex |
-
1975
- 1975-04-08 SU SU7502130585A patent/SU571292A1/en active
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4623470A (en) * | 1981-11-09 | 1986-11-18 | Helipump, Inc. | Process and apparatus for separating or fractionating fluid mixtures |
US5405497A (en) * | 1990-08-28 | 1995-04-11 | Kamyr, Inc. | Method of chemically reacting a liquid with a gas in a vortex |
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