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WO1999020368A1 - Installation permettant d'eliminer les poussieres dans les rejets gazeux d'origine industrielle - Google Patents

Installation permettant d'eliminer les poussieres dans les rejets gazeux d'origine industrielle Download PDF

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Publication number
WO1999020368A1
WO1999020368A1 PCT/RU1997/000336 RU9700336W WO9920368A1 WO 1999020368 A1 WO1999020368 A1 WO 1999020368A1 RU 9700336 W RU9700336 W RU 9700336W WO 9920368 A1 WO9920368 A1 WO 9920368A1
Authority
WO
WIPO (PCT)
Prior art keywords
aerodynamic
installation
aππaρaτa
aeροdinamichesκοgο
gas
Prior art date
Legal status (The legal status 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 status listed.)
Ceased
Application number
PCT/RU1997/000336
Other languages
English (en)
Russian (ru)
Inventor
Jury Mikhailovich Bolshov
Alexandr Sergeevich Mankov
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to AU57839/98A priority Critical patent/AU5783998A/en
Priority to PCT/RU1997/000336 priority patent/WO1999020368A1/fr
Publication of WO1999020368A1 publication Critical patent/WO1999020368A1/fr
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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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
    • B01D47/04—Separating dispersed particles from gases, air or vapours by liquid as separating agent by passing the gas or air or vapour through foam

Definitions

  • Izves ⁇ n ⁇ us ⁇ ys ⁇ v ⁇ for ⁇ chis ⁇ i ⁇ myshlenny ⁇ gaz ⁇ vy ⁇ You are a b ⁇ s ⁇ v ⁇ ⁇ yli, vy ⁇ lnenn ⁇ e on ⁇ sn ⁇ ve ae ⁇ dinamiches ⁇ g ⁇ a ⁇ a ⁇ a for ⁇ azdeleniya mn ⁇ g ⁇ m ⁇ nen ⁇ ny ⁇ ⁇ e ⁇ uchi ⁇ s ⁇ ed in ⁇ - ⁇ m ⁇ is ⁇ di ⁇ ⁇ azdelenie ⁇ ylegaz ⁇ v ⁇ g ⁇ ⁇ a, ⁇ da- vaem ⁇ g ⁇ on v ⁇ d ae ⁇ dinamiches ⁇ g ⁇ a ⁇ a ⁇ a, ⁇ e ⁇ vy vy ⁇ d ⁇ - ⁇ g ⁇ s ⁇ bschon with bun ⁇ e ⁇ m with ⁇ m ⁇ schyu ⁇ ylevyv ⁇ dn ⁇ y ⁇ uby for ⁇ v ⁇ da ⁇ n
  • the distributing and / or primary collectors have a transverse cross-section or a round, or quasi-circular, or rectangular. It is advisable that aerodynamic devices be installed at the disposal of the distributor and the receiver.
  • ⁇ me ⁇ g ⁇ , ⁇ azal ⁇ s vyg ⁇ dn ⁇ , ch ⁇ by ⁇ azdayuschy and ⁇ iemny ⁇ lle ⁇ y were ⁇ as ⁇ l ⁇ zheny ⁇ din ⁇ n ⁇ si ⁇ eln ⁇ d ⁇ ug ⁇ g ⁇ with v ⁇ zm ⁇ zhn ⁇ s ⁇ yu s ⁇ zdaniya in ni ⁇ gaz ⁇ vy ⁇ ⁇ v in ⁇ a ⁇ i ⁇ na ⁇ av- leniya ⁇ , ch ⁇ by ug ⁇ l between gaz ⁇ vymi ⁇ ami would ⁇ aven or less 90 °.
  • the body of the aerodynamic device should have a hatch used in the process of installing and servicing the unit.
  • parting parts are fully or partly partly disassembled. It is also desirable that aerodynamic devices would be installed between the distributing and primary collectors of a smaller size in a single unit. A good installation for calculating gas emissions from dust ensures that they are cleaned at an intentional scale.
  • FIG. 1 depicts the setting for the calculation of the deductions of the payment of profit
  • figure 2 is another version of the execution of the same installation, according to the invention, view of the side
  • FIG. 3 cross-section of a distributing and alternating collector, as agreed by the invention
  • 5 Fig. 6 - discloses the same setting for calculating intentional gas emissions from collectors of a primary section, according to the invention, view from the roof
  • 5 Fig. 6 discloses the same setting for calculating intentional gas emissions from collectors of a primary section, according to the invention, view from the roof
  • 5 Fig. 6 - discloses the same setting for calculating intentional gas emissions from collectors of a primary section, according to the invention, view from the roof
  • 5 Fig. 6 - discloses the same setting for calculating intentional gas
  • FIG. 7 one more installation with collectors of the first corner, according to the invention, view from the top; Fig. ⁇ - execution of a receiver and a bunker in the form of one device, according to the invention; Fig. 9- dust collecting pipe assembly on a single wall between the collection tank and the bunker, as agreed by the invention; Fig. 10 - a unit for connecting an aerodynamic apparatus and connecting elements according to the invention; Fig. 11 is another variant of the connection of the aerodynamic device and the connecting element, according to the invention; Fig. 12 is a view of a flange of an aerodynamic device; Fig. 13 illustrates an embodiment of the installation with a global use of aerodynamic devices according to the invention; Fig. 14 is still one embodiment of the installation with direct dusting tubes specified through side walls of the connecting elements, according to the notice.
  • FIG. 1 two such aerodynamic devices 1 are shown, which are identical.
  • the installation also has a separating 2 and a simple 3 collectors, between which all aerodynamic devices 1 are installed, the inputs are connected to the separating ones
  • the quick outlets of 9 aerodynamic units 1 are communicated with a quick collector 3 with an intake manifold 10 for exhaust gas.
  • ⁇ a ⁇ ig.2 ⁇ azany two ⁇ yada 11 and 12 a ⁇ a ⁇ a ⁇ v 1 ⁇ dna ⁇ , ⁇ liches ⁇ v ⁇ ⁇ yad ⁇ v m ⁇ zhe ⁇ by ⁇ znachi ⁇ eln ⁇ b ⁇ lshim, ch ⁇ depend si ⁇ ⁇ ⁇ bscheg ⁇ ⁇ liches ⁇ va ae ⁇ dinamiches ⁇ i ⁇ a ⁇ a ⁇ a ⁇ v 1 and ⁇ az- me ⁇ v ⁇ ab ⁇ chey ⁇ l ⁇ schad ⁇ i, zanimaem ⁇ y us ⁇ an ⁇ v ⁇ y in ⁇ e ⁇ n ⁇ l ⁇ gi- ches ⁇ y s ⁇ eme ⁇ myshlenny ⁇ ⁇ izv ⁇ ds ⁇ v, vyb ⁇ sy It is easy to calculate and the total quantity of devices 1 depends on the required installation.
  • FIG. 1 a version of the installation is provided, in which a dusty pipe 6 is supplied for each unit 1 and is non-consumable in general.
  • a dusty pipe 6 is supplied for each unit 1 and is non-consumable in general.
  • Such a pipe creates a linear 0-concentrate dust-and-gas treatment. This reduces the accumulation of dust particles on the pipe wall 6 and reduces its physical wear, which is especially effective if the cleaned gas medium does not have a high concentration.
  • the cross-section of the distributing 2 and primary 3 collectors is 0 made by round (fig. 3), quasi (fig. 4 a, c) or rectangular (fig. 5 a, c).
  • Part 2 (3) of the circular and quasi-cross sections are more preferable for calculating gaseous gases. 7 emissions of dust with a high concentration of it in the input of 15 light source (Fig. 1), as well as explosive or hazardous dust.
  • a dusty pipe 6 is disposed of 20.
  • the aerodynamic unit 1 is connected to the connecting elements 4.10 of the connecting unit 24 (connector) which connects to 24 ⁇ a ⁇ ig.11 iz ⁇ b ⁇ azhen va ⁇ ian ⁇ s ⁇ edineniya ae ⁇ dinamiches ⁇ g ⁇ a ⁇ a ⁇ a ⁇ a ⁇ is ⁇ edini ⁇ elny ⁇ elemen ⁇ v 1 and 4 (10) ⁇ s ⁇ eds ⁇ v ⁇ m ⁇ ili ⁇ vann ⁇ g ⁇ ⁇ b ⁇ ucha 27 ( ⁇ ig.11) with external vy ⁇ u ⁇ l ⁇ y ⁇ - ve ⁇ n ⁇ s ⁇ yu, za ⁇ e ⁇ lenn ⁇ g ⁇ on vys ⁇ u ⁇ ayuschi ⁇ na ⁇ uzhu ⁇ m ⁇ a ⁇ 28, 29 a ⁇ a ⁇ a ⁇ a ⁇ is ⁇ edini ⁇ elny
  • connection of the aerodynamic unit 1 with the connecting elements 4 (10) is carried out by means of a 30-flanged connector (Fig. 12), connected by a 24-volt connection 5.
  • the aerodynamic unit 1 (Fig. 1) has hatch 31, which is hermetically connected to the unit 13.
  • Dispensing accessories 4 are available in the form of a round cross-section with a constant diameter, or partial or complete delivery, as a result of the lack of convenience 5
  • FIG. 13 it is provided that such a version of installation is completed, in the case of devices 1 are located on the ground, in two parts, and the connection is 2 and 3.
  • This simple installation has a lower height and 0 is placed on the work area reserved for it with a limited height.
  • a preferred embodiment of the installation is an advantageous method for calculating industrial flue gas emissions 9 its high concentration in the gas and gas discharge at the entrance to the installation, and also with the explosive and dangerous dust.
  • the total bunker 7 (Fig. 1) has a shutter speed of 32, after which the dust deposited in the general bunker 7 is removed.
  • ⁇ Dispensing collector 2 installs an empty exhaust gas outlet 15, filling it with a dust-gas mixture.
  • ⁇ azme ⁇ y sectional ⁇ lle ⁇ a 2 vybi ⁇ ayu ⁇ sya in zavisim ⁇ s ⁇ i ⁇ ⁇ boma ⁇ chischaem ⁇ y ⁇ ylegaz ⁇ v ⁇ y mixture per unit v ⁇ emeni, it ⁇ em ⁇ e ⁇ a ⁇ u ⁇ y, s ⁇ s ⁇ i gaz ⁇ v ⁇ g ⁇ ⁇ a and d ⁇ ugi ⁇ ⁇ a ⁇ ame ⁇ v ⁇ a ⁇ im ⁇ b ⁇ az ⁇ m, ch ⁇ by ⁇ bom ⁇ ylegaz ⁇ v ⁇ y mixture ⁇ dyaschey che ⁇ ez ⁇ azhdy ae ⁇ dinamiches ⁇ y a ⁇ a ⁇ a ⁇ 1 per unit v ⁇ emeni, would not have znachi ⁇ elny ⁇ ⁇ l ⁇ neny ⁇ n ⁇ minalny ⁇ performance
  • the cleaned gas outlet is emptied into the intake unit 3 after 10 plug-in connectors 10 and further for exhaustion in the atmosphere or for further cleaning or disposal.
  • the cross-section of the connecting elements 4 and 10 is selected, as a rule, the same cross-section of the inlet of the aerodynamic units 1.
  • the installation also owns, in comparison, for example, with the necessary filtering devices. 11th type, allows for the calculation of dust-and-gas emissions in non-hazardous processes with non-disruptive process.
  • Iz ⁇ b ⁇ e ⁇ enie m ⁇ zhe ⁇ is ⁇ lz ⁇ va ⁇ sya for ⁇ chis ⁇ i ⁇ ⁇ yli in ⁇ myshlenny ⁇ massh ⁇ aba ⁇ ⁇ ylegaz ⁇ vy ⁇ vyb ⁇ s ⁇ v shi ⁇ g ⁇ ⁇ uga ⁇ izv ⁇ ds ⁇ v in ⁇ m including ⁇ aslya ⁇ : me ⁇ allu ⁇ giches ⁇ y, ug ⁇ ln ⁇ y, ⁇ imiches ⁇ y ⁇ myshlenn ⁇ s ⁇ i, a ⁇ mn ⁇ y ene ⁇ ge ⁇ i ⁇ e, ⁇ izv ⁇ ds ⁇ ve s ⁇ i ⁇ elny ⁇ ma ⁇ e ⁇ ial ⁇ v, ⁇ e ⁇ l ⁇ ene ⁇ ge ⁇ i ⁇ e and d ⁇ ugi ⁇ .

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Junction Field-Effect Transistors (AREA)

Abstract

Cette invention concerne une installation permettant d'éliminer les poussières dans les rejets gazeux d'origine industrielle. Cette installation comprend un appareil aérodynamique (1) qui sert à séparer les milieux en écoulement contenant plusieurs composants et constituant les rejets de gaz et de poussières, appareil dans lequel on effectue la séparation d'un flux de gaz et de poussières. Le flux de gaz et de poussières est introduit dans l'entrée de l'appareil aérodynamique (1), la première sortie (5) de celui-ci étant connectée à un réservoir par l'intermédiaire d'un tube d'évacuation des poussières (6) servant à évacuer le flux de gaz et de poussières concentré. La seconde sortie (9) de l'appareil aérodynamique (1) sert à évacuer le gaz purifié. Cette installation comprend en outre les éléments suivants: au moins un appareil aérodynamique (1) analogue à l'appareil principal; des collecteurs d'alimentation (2) et de réception (3) entre lesquels sont montés tous les appareils aérodynamiques (1); des éléments de connexion pour l'alimentation (4) qui servent à connecter l'entrée de chaque appareil aérodynamique (1) au collecteur d'alimentation (2); des éléments de connexion pour la réception (10) qui servent à connecter les secondes sorties (9) des appareils aérodynamiques (1) au collecteur de réception (3); et enfin, un réservoir commun (7) qui va relier les réservoirs de tous les appareils aérodynamiques (1). La connexion des premières sorties (5) de chaque appareil aérodynamique (1) au réservoir (7) se fait de manière distincte par l'intermédiaire des tubes d'évacuation des poussières (6).
PCT/RU1997/000336 1997-10-22 1997-10-22 Installation permettant d'eliminer les poussieres dans les rejets gazeux d'origine industrielle Ceased WO1999020368A1 (fr)

Priority Applications (2)

Application Number Priority Date Filing Date Title
AU57839/98A AU5783998A (en) 1997-10-22 1997-10-22 System for removing dust from industrial gaseous waste
PCT/RU1997/000336 WO1999020368A1 (fr) 1997-10-22 1997-10-22 Installation permettant d'eliminer les poussieres dans les rejets gazeux d'origine industrielle

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PCT/RU1997/000336 WO1999020368A1 (fr) 1997-10-22 1997-10-22 Installation permettant d'eliminer les poussieres dans les rejets gazeux d'origine industrielle

Publications (1)

Publication Number Publication Date
WO1999020368A1 true WO1999020368A1 (fr) 1999-04-29

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Application Number Title Priority Date Filing Date
PCT/RU1997/000336 Ceased WO1999020368A1 (fr) 1997-10-22 1997-10-22 Installation permettant d'eliminer les poussieres dans les rejets gazeux d'origine industrielle

Country Status (2)

Country Link
AU (1) AU5783998A (fr)
WO (1) WO1999020368A1 (fr)

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1993011852A1 (fr) * 1991-12-11 1993-06-24 Environmental Protection Group Ltd. Dispositif permettant de separer des fluides a plusieurs composants
GB2270481A (en) * 1992-09-11 1994-03-16 Rolls Royce Plc Particle separators
RU2050938C1 (ru) * 1992-06-10 1995-12-27 Научно-технический центр "Природа" Газодинамический аппарат пылевой очистки дымовых выбросов
RU2056905C1 (ru) * 1994-07-22 1996-03-27 Бахарев Александр Александрович Инерционный отделитель дисперсной фазы от дисперсионной текучей среды
RU94032339A (ru) * 1994-09-05 1996-07-27 А.Г. Иноземцев Способ аэродинамической пылеочистки воздушной зоны ссыпки и транспортировки мелкодисперсных материалов и устройство для его осуществления
RU94032304A (ru) * 1994-09-05 1996-08-20 А.Г. Иноземцев Аэродинамическая пылевая очистка воздушных сред
US5549721A (en) * 1994-12-02 1996-08-27 Shchipachev; Viktor Cell for gas cleaning
RU94042649A (ru) * 1994-11-29 1996-09-20 А.Г. Иноземцев Аэродинамический пылеулавливающий аппарат

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1993011852A1 (fr) * 1991-12-11 1993-06-24 Environmental Protection Group Ltd. Dispositif permettant de separer des fluides a plusieurs composants
RU2050938C1 (ru) * 1992-06-10 1995-12-27 Научно-технический центр "Природа" Газодинамический аппарат пылевой очистки дымовых выбросов
GB2270481A (en) * 1992-09-11 1994-03-16 Rolls Royce Plc Particle separators
RU2056905C1 (ru) * 1994-07-22 1996-03-27 Бахарев Александр Александрович Инерционный отделитель дисперсной фазы от дисперсионной текучей среды
RU94032339A (ru) * 1994-09-05 1996-07-27 А.Г. Иноземцев Способ аэродинамической пылеочистки воздушной зоны ссыпки и транспортировки мелкодисперсных материалов и устройство для его осуществления
RU94032304A (ru) * 1994-09-05 1996-08-20 А.Г. Иноземцев Аэродинамическая пылевая очистка воздушных сред
RU94042649A (ru) * 1994-11-29 1996-09-20 А.Г. Иноземцев Аэродинамический пылеулавливающий аппарат
US5549721A (en) * 1994-12-02 1996-08-27 Shchipachev; Viktor Cell for gas cleaning

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Publication number Publication date
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