WO1993002770A1 - Procede et dispositif d'epuration de flux de gaz - Google Patents

Procede et dispositif d'epuration de flux de gaz Download PDF

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Publication number
WO1993002770A1
WO1993002770A1 PCT/SU1991/000155 SU9100155W WO9302770A1 WO 1993002770 A1 WO1993002770 A1 WO 1993002770A1 SU 9100155 W SU9100155 W SU 9100155W WO 9302770 A1 WO9302770 A1 WO 9302770A1
Authority
WO
WIPO (PCT)
Prior art keywords
gas
chτο
τem
ποτοκa
gazοvοgο
Prior art date
Application number
PCT/SU1991/000155
Other languages
English (en)
Russian (ru)
Inventor
Anatoly Alexandrovich Bochkarev
Yuri Alexandrovich Golubev
Sergei Nikolaevich Zolotarev
Original Assignee
Sovmestnoe Sovetsko-Kanadskoe Predpriyatie 'compomet Cantec'
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 Sovmestnoe Sovetsko-Kanadskoe Predpriyatie 'compomet Cantec' filed Critical Sovmestnoe Sovetsko-Kanadskoe Predpriyatie 'compomet Cantec'
Priority to JP3514031A priority Critical patent/JPH06503745A/ja
Priority to PCT/SU1991/000155 priority patent/WO1993002770A1/fr
Priority to CA002074359A priority patent/CA2074359A1/fr
Priority to EP19910914303 priority patent/EP0555474A4/en
Priority claimed from CA002074359A external-priority patent/CA2074359A1/fr
Publication of WO1993002770A1 publication Critical patent/WO1993002770A1/fr

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D47/00—Separating dispersed particles from gases, air or vapours by liquid as separating agent
    • B01D47/05—Separating dispersed particles from gases, air or vapours by liquid as separating agent by condensation of the separating agent

Definitions

  • the first is to be included in order to begin the expansion of dispersed dispersion of particles.
  • a 20 ′′ separate “ ⁇ ” size is necessary in the gas supply and a saturation of steam is achieved which complies with the law of ⁇ elvin- Komsom. In this case, it will be possible to compensate the vapor for particles ⁇ size " ⁇ " and larger than ⁇ . Smaller particles and this saturation value
  • Gas coolers are supplied with refrigerated gas in order to improve the cooling and cooling performance of the propellers. This will improve the best equipment available on the refrigerator.
  • s ⁇ glasns 5 iz ⁇ b ⁇ e ⁇ e ⁇ IYu s ⁇ eds ⁇ v ⁇ for vduva ⁇ iya ⁇ a ⁇ a ⁇ azhd ⁇ zh se ⁇ sh vy ⁇ lne ⁇ as ⁇ as ⁇ yli ⁇ eln ⁇ zh g ⁇ l ⁇ vsh, ⁇ b ⁇ azuyuschezh s ⁇ ui ⁇ a ⁇ z in ⁇ me ⁇ nusz, ⁇ z ⁇ zvle ⁇ ye ne ⁇ ve ⁇ n ⁇ s ⁇ ⁇ L ⁇ DIL ⁇ SHZ and ⁇ l ⁇ dilysh ⁇ vy ⁇ l ⁇ en as ⁇ ubashsh, s ⁇ n ⁇ zh ⁇ u ⁇ u.
  • An additional spray head is also supplied with the same spray head, and the main spray head is installed and is installed on the gas burner. The better, the better, the better, the better, the better, the better, the better, the better, the better, the better, the better.
  • Short circuit drawing Fig. ⁇ founded Quickly disconnect the device for the production of gas in the open section;
  • Fig. 2 shows a LONG LIFE, due to the fact that it is currently installed in a self-contained module, it is installed in a cold storage room;
  • Fig. 3 is a schematic illustration of the other option for
  • the 5th gas discharge prevents the failure of the engine I, the neck of the inlet and the outlet are inaccessible in the event of an accident.
  • the main part I is composed of the necessary section 3,
  • a koldevaya fuserka is used with an exhaust switch in the case of a cone when the gaseous outlet is in danger of 2, and is used ⁇ dnim ⁇ sn ⁇ ny ⁇ assignments of 5 ⁇ a ⁇ i ⁇ ⁇ sun ⁇ yavlyae ⁇ sya ⁇ b ⁇ zz ⁇ venie d ⁇ s ⁇ a ⁇ chn ⁇ ⁇ l ⁇ n ⁇ n ⁇ a ⁇ v ⁇ y s ⁇ ui, d ⁇ dyasche ⁇ d ⁇ ⁇ ve ⁇ n ⁇ s ⁇ i ⁇ l ⁇ dilni ⁇ a 9.
  • ⁇ e ⁇ ve ⁇ iev ⁇ i ⁇ zheniya us ⁇ ys ⁇ va for ⁇ chis ⁇ i gaz ⁇ v ⁇ g ⁇ ⁇ a ⁇ dna or nes ⁇ l ⁇ se ⁇ tsy 3 m ⁇ zhe ⁇ by ⁇ snabzhe ⁇ Z d ⁇ lni ⁇ el ⁇ zh ⁇ as ⁇ yli ⁇ eln ⁇ g ⁇ l ⁇ v ⁇ zh 19 ⁇ a ⁇ e ⁇ ⁇ azen ⁇ on ⁇ ig.Z for vduva ⁇ shya ⁇ a ⁇ a nav ⁇ echu g ⁇ gaz ⁇ v ⁇ mu ⁇ u 2 s ⁇ ve ⁇ vuyusche ⁇ ⁇ e ⁇ tssh.
  • Each section 3 is a self-contained module (Fig. 2), which makes it possible to disconnect from the factory and easily replace it in case of a free delivery. Between them, the moduli are connected with the flanges 21 and the Bulgarians (not shown in FIG.).
  • the device has a self-supporting structure, its installation or demounting through a smoke can
  • the most comprehensive angle of inclination of the building 15 is the angle of 9 , which is -55 °.
  • the expanding pressure of the steam has such a tightness and augmentation, which improves the efficiency of the 9 and makes it easier to move. Thoroughly dispense cleanable gas while mixing with it and spraying gas mixture.
  • ⁇ lag ⁇ de ⁇ z hashe v ⁇ zdu ⁇ z on v ⁇ de in u ⁇ an ⁇ v ⁇ u 0.02 ⁇ g / m.
  • ⁇ a ⁇ imaln ⁇ e vlag ⁇ de ⁇ z hashe, ⁇ zdavaem ⁇ e in u ⁇ an ⁇ v ⁇ e 0.8 ⁇ g / m ⁇ .
  • EXAMPLE 2 The installation of 7 out of 7 runs in the formerly better product with a quick start with a lack of air.
  • the gas and steam outlet 55 ° are differentiated by various coal charcoals in the range of 50 s.
  • ⁇ sixth and seventh section ⁇ ⁇ building 35 ° ulles - v ⁇ z - unfortunate parasites of kerosene - aromatic carbonaceous.
  • Good air flow from the entrance to the appliance is 0.0 ⁇ 8kg / m, and from the exit it is 0.042kg / m ".

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Machine Tool Units (AREA)

Abstract

Procédé et appareil d'épuration d'un flux de gaz consistant à faire grossir et à collecter des particules de poussière par nucléation en phase vapeur et condensation inertielle sur un refroidisseur. Les nouveautés que présente le procédé sont les suivantes: la sursaturation du flux dans certaines étapes accomplie au moyen de jets, orientés sur le refroidisseur en un certain angle. Le degré de sursaturation augmente d'une étape à l'autre, et à chaque étape ces particules sont éliminées, en l'occurrence les plus grosses particules. La différentiation de nucléation permet d'opérer une sélectivité lors de la collecte de particules.
PCT/SU1991/000155 1991-07-26 1991-07-26 Procede et dispositif d'epuration de flux de gaz WO1993002770A1 (fr)

Priority Applications (4)

Application Number Priority Date Filing Date Title
JP3514031A JPH06503745A (ja) 1991-07-26 1991-07-26 ガス流洗浄方法及び装置
PCT/SU1991/000155 WO1993002770A1 (fr) 1991-07-26 1991-07-26 Procede et dispositif d'epuration de flux de gaz
CA002074359A CA2074359A1 (fr) 1991-07-26 1991-07-26 Methode utilisee pour nettoyer un flux gazeux, et appareil connexe
EP19910914303 EP0555474A4 (en) 1991-07-26 1991-07-26 Method and device for cleaning gas stream

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
PCT/SU1991/000155 WO1993002770A1 (fr) 1991-07-26 1991-07-26 Procede et dispositif d'epuration de flux de gaz
CA002074359A CA2074359A1 (fr) 1991-07-26 1991-07-26 Methode utilisee pour nettoyer un flux gazeux, et appareil connexe

Publications (1)

Publication Number Publication Date
WO1993002770A1 true WO1993002770A1 (fr) 1993-02-18

Family

ID=25675353

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/SU1991/000155 WO1993002770A1 (fr) 1991-07-26 1991-07-26 Procede et dispositif d'epuration de flux de gaz

Country Status (1)

Country Link
WO (1) WO1993002770A1 (fr)

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
SU245265A1 (ru) * П. Н. Цветков , С. Л. Щепалов Устройство для очистки дымовых газов
SU17201A1 (ru) * 1927-01-03 1930-09-30 М.С. Ракитин Колонна дл ректификации и дистилл ции
SU116894A1 (ru) * 1958-02-13 1958-11-30 Н.В. Лазарев Вентил ционное устройство дл трюма судна
US3395510A (en) * 1965-10-23 1968-08-06 Gen Electric Gas scrubber
US3605386A (en) * 1970-06-16 1971-09-20 Air Pollution Research & Devel Furnace exhaust pollution eliminator
SU738642A1 (ru) * 1977-08-05 1980-06-05 Ленинградский технологический институт целлюлозно-бумажной промышленности Способ мокрой очистки газа
DE2453587B2 (de) * 1973-11-08 1981-02-12 Celorio Mendoza, Fausto, Mexiko Verfahren und Vorrichtung zum Reinigen eines verunreinigten Gases
SU940807A1 (ru) * 1980-11-04 1982-07-07 Белорусский Ордена Трудового Красного Знамени Политехнический Институт Пылеуловитель дл мокрой очистки газа с утилизацией тепла
SU1473814A1 (ru) * 1987-09-21 1989-04-23 Запорожский индустриальный институт Газоочистной аппарат

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
SU245265A1 (ru) * П. Н. Цветков , С. Л. Щепалов Устройство для очистки дымовых газов
SU17201A1 (ru) * 1927-01-03 1930-09-30 М.С. Ракитин Колонна дл ректификации и дистилл ции
SU116894A1 (ru) * 1958-02-13 1958-11-30 Н.В. Лазарев Вентил ционное устройство дл трюма судна
US3395510A (en) * 1965-10-23 1968-08-06 Gen Electric Gas scrubber
US3605386A (en) * 1970-06-16 1971-09-20 Air Pollution Research & Devel Furnace exhaust pollution eliminator
DE2453587B2 (de) * 1973-11-08 1981-02-12 Celorio Mendoza, Fausto, Mexiko Verfahren und Vorrichtung zum Reinigen eines verunreinigten Gases
SU738642A1 (ru) * 1977-08-05 1980-06-05 Ленинградский технологический институт целлюлозно-бумажной промышленности Способ мокрой очистки газа
SU940807A1 (ru) * 1980-11-04 1982-07-07 Белорусский Ордена Трудового Красного Знамени Политехнический Институт Пылеуловитель дл мокрой очистки газа с утилизацией тепла
SU1473814A1 (ru) * 1987-09-21 1989-04-23 Запорожский индустриальный институт Газоочистной аппарат

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See also references of EP0555474A4 *

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