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SU551037A1 - Granular filter - Google Patents

Granular filter

Info

Publication number
SU551037A1
SU551037A1 SU1952525A SU1952525A SU551037A1 SU 551037 A1 SU551037 A1 SU 551037A1 SU 1952525 A SU1952525 A SU 1952525A SU 1952525 A SU1952525 A SU 1952525A SU 551037 A1 SU551037 A1 SU 551037A1
Authority
SU
USSR - Soviet Union
Prior art keywords
granular
filter
granular filter
cleaning
gas
Prior art date
Application number
SU1952525A
Other languages
Russian (ru)
Inventor
Виктор Дмитриевич Михайлик
Георгий Степанович Кабалдин
Павел Степанович Куц
Виктор Сергеевич Никитин
Александр Тихонович Бахилов
Original Assignee
Ордена Трудового Красного Знамени Институт Массообмена Ан Белорусской Сср
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Ордена Трудового Красного Знамени Институт Массообмена Ан Белорусской Сср filed Critical Ордена Трудового Красного Знамени Институт Массообмена Ан Белорусской Сср
Priority to SU1952525A priority Critical patent/SU551037A1/en
Application granted granted Critical
Publication of SU551037A1 publication Critical patent/SU551037A1/en

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  • Filtering Of Dispersed Particles In Gases (AREA)

Description

Насто щее изобретение относитс  к области техники очистных устройств, например , дл  обеспыливани  потоков газа (воздуха , азота и т. д.) и может быть применено в теплоэнергетике, горнорудной, металлургической и других отрасл х промышленности , где требуетс  очистка промышленных выбросов в атмосферу. Известны зернистые фильтры с движу- ш,имс  зернистым слоем дл  очистки газа от пыли, регенераци  зернистого материала которых осуществл етс  вне фильтра }. Также известен 3epmiv. у и фильтр с движущимс  слоем дл  очистки газа от пыли, вклю- чающий корпус с патрубками дл  входа и выход газа, зернистый слой, расположенный внутри корпуса между входными и выходным патрубками , наклонное вибросито дл  регенерации , установленное на сходе зернистого сло  над бункером уловленной пыли и трубопровод дл  рециркул ции зернистого материала , соединенный одним кондом с нижней частью вибросита, а другим концом с бункером дл  ввода зернистого материала 2J, Однако регенераци  зернистого матераала осуществл етс  в известном фильтре не полно, что понижает эффективность очистки. Повышение эффективности очистки газа достигаетс  в предложенном фильтре тем, что над виброситом, перед рециркул ционным трубопроводом, установлены форсунки дл  орошени  водой, а под ним - бункер дл  сбора промывочной воды. Наклонное вибросито может быть выполнено не только в виде простого перфорированного листа, но и с подвижными жалюз ми , раскрывающимис  при вибрации, при этом размер образовавшихс  зазоров не превышает размера зернистой насадки, что можно обеспечить подбором длины жалюзей. их формы , креплени  и т.д. На чертеже схематически изображен зернистый фильтр, общий вид. Фильтр состоит из корпуса 1, решеток 2, зернистого сло  3, бункера уловленной пыли 4, вибросита 5, подъемника регенерированного сло  6, оросительных форсунок 7,The present invention relates to the field of cleaning devices, for example, to dedust gas streams (air, nitrogen, etc.) and can be applied in heat and power, mining, metallurgical and other industries that require purification of industrial emissions into the atmosphere. Granular filters are known with a slide, a granular layer for cleaning the gas from dust, the regeneration of the granular material of which is carried out outside the filter}. Also known 3epmiv. y and a filter with a moving layer for cleaning gas from dust, including a housing with nozzles for inlet and outlet of gas, a granular layer located inside the housing between the inlet and outlet nozzles, an inclined vibrating screen for regeneration, mounted on the gathering of the granular layer above the dust collector bin and a pipeline for recirculating the granular material, connected by one condom to the bottom of the vibrating screen, and the other end to the hopper for introducing the granular material 2J. However, the regeneration of the granular material is carried out in a known filter re not complete, which lowers the efficiency of cleaning. Improving the efficiency of gas cleaning is achieved in the proposed filter by the fact that above the shaker, in front of the recirculation pipeline, nozzles are installed for irrigation with water, and under it is a hopper for collecting the wash water. The inclined vibrating screen can be made not only in the form of a simple perforated sheet, but also with movable louvers that open during vibration, while the size of the gaps formed does not exceed the size of the granular nozzle, which can be ensured by choosing the length of the louver. their shapes, fastenings, etc. The drawing shows schematically a granular filter, a general view. The filter consists of body 1, grates 2, granular layer 3, collected dust bunker 4, vibrosieve 5, elevator of regenerated layer 6, irrigation nozzles 7,

SU1952525A 1973-07-24 1973-07-24 Granular filter SU551037A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
SU1952525A SU551037A1 (en) 1973-07-24 1973-07-24 Granular filter

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
SU1952525A SU551037A1 (en) 1973-07-24 1973-07-24 Granular filter

Publications (1)

Publication Number Publication Date
SU551037A1 true SU551037A1 (en) 1977-03-25

Family

ID=20562512

Family Applications (1)

Application Number Title Priority Date Filing Date
SU1952525A SU551037A1 (en) 1973-07-24 1973-07-24 Granular filter

Country Status (1)

Country Link
SU (1) SU551037A1 (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4254616A (en) 1979-07-31 1981-03-10 Exxon Research And Engineering Co. Process for flue gas desulfurization or nitrogen oxide removal using a magnetically stabilized fluid cross-flow contactor
US4254557A (en) 1979-07-31 1981-03-10 Exxon Research And Engineering Co. Magnetically stabilized fluid cross-flow contactor and process for using the same
US4254558A (en) 1979-07-31 1981-03-10 Exxon Research & Engineering Co. Louvered magnetically stabilized fluid cross-flow contactor and processes for using the same
US4255403A (en) 1979-07-31 1981-03-10 Exxon Research And Engineering Co. Magnetically stabilized fluid cross-flow contactor having support means and process for using the same
US4255166A (en) 1979-07-31 1981-03-10 Exxon Research And Engineering Company Process for the removal of particulates entrained in a fluid using a magnetically stabilized fluid cross-flow contactor

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4254616A (en) 1979-07-31 1981-03-10 Exxon Research And Engineering Co. Process for flue gas desulfurization or nitrogen oxide removal using a magnetically stabilized fluid cross-flow contactor
US4254557A (en) 1979-07-31 1981-03-10 Exxon Research And Engineering Co. Magnetically stabilized fluid cross-flow contactor and process for using the same
US4254558A (en) 1979-07-31 1981-03-10 Exxon Research & Engineering Co. Louvered magnetically stabilized fluid cross-flow contactor and processes for using the same
US4255403A (en) 1979-07-31 1981-03-10 Exxon Research And Engineering Co. Magnetically stabilized fluid cross-flow contactor having support means and process for using the same
US4255166A (en) 1979-07-31 1981-03-10 Exxon Research And Engineering Company Process for the removal of particulates entrained in a fluid using a magnetically stabilized fluid cross-flow contactor

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