IT960366B - PROCEDURE AND APPARATUS FOR ELIMINATING SUBSTANCES IN PARTICLES FROM A GAS CURRENT - Google Patents

PROCEDURE AND APPARATUS FOR ELIMINATING SUBSTANCES IN PARTICLES FROM A GAS CURRENT

Info

Publication number
IT960366B
IT960366B IT67855/72A IT6785572A IT960366B IT 960366 B IT960366 B IT 960366B IT 67855/72 A IT67855/72 A IT 67855/72A IT 6785572 A IT6785572 A IT 6785572A IT 960366 B IT960366 B IT 960366B
Authority
IT
Italy
Prior art keywords
receptacle
hood
walls
liquid
manifold
Prior art date
Application number
IT67855/72A
Other languages
Italian (it)
Original Assignee
Oxy Dry Int Ltd
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 Oxy Dry Int Ltd filed Critical Oxy Dry Int Ltd
Application granted granted Critical
Publication of IT960366B publication Critical patent/IT960366B/en

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D47/00Separating dispersed particles from gases, air or vapours by liquid as separating agent
    • B01D47/02Separating dispersed particles from gases, air or vapours by liquid as separating agent by passing the gas or air or vapour over or through a liquid bath
    • B01D47/021Separating dispersed particles from gases, air or vapours by liquid as separating agent by passing the gas or air or vapour over or through a liquid bath by bubbling the gas through a liquid bath
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D47/00Separating dispersed particles from gases, air or vapours by liquid as separating agent
    • B01D47/02Separating dispersed particles from gases, air or vapours by liquid as separating agent by passing the gas or air or vapour over or through a liquid bath
    • B01D47/024Separating dispersed particles from gases, air or vapours by liquid as separating agent by passing the gas or air or vapour over or through a liquid bath by impinging the gas to be cleaned essentially in a perpendicular direction onto the liquid surface
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B41PRINTING; LINING MACHINES; TYPEWRITERS; STAMPS
    • B41FPRINTING MACHINES OR PRESSES
    • B41F23/00Devices for treating the surfaces of sheets, webs, or other articles in connection with printing
    • B41F23/002Devices for treating the surfaces of sheets, webs, or other articles in connection with printing cleaning devices for sheets or webs

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Separation Of Particles Using Liquids (AREA)
  • Separating Particles In Gases By Inertia (AREA)
  • Filtering Of Dispersed Particles In Gases (AREA)

Abstract

1377752 Gas cleaner OXY-DRY INTERNATIONAL Ltd 17 March 1972 [18 March 1971] 7216/71 Heading B1R Particulate matter is separated from a gaseous stream, e.g. air, moving at a given flow rate by passing the stream via an inlet 12 into a hood 10 which comprises an open hood base and hood walls defining a chamber, the hood being positioned relative to a receptacle 16 containing liquid 18, e.g. water, such that the open base is above the level of the liquid but the hood walls are partially within the receptacle with the chamber walls being spaced from the walls of the receptacle, the liquid level being adjusted at static conditions to be at a distance not exceeding about 3/8 inch from the open hood base and presenting a path for the gaseous stream to exit to the atmosphere from the open base, the chamber being sized to assist in adjusting the velocity of the gaseous stream at the open base to between about 1300 and 3000 ft./min. the adjustment of the distance of the open base from the liquid level and the selection of the size of the chamber being such that, as a combined effect, relatively high particle separation efficiency is obtained without substantially reducing the throughput of the gaseous stream. As shown in Fig. 3, the hood 30 may be rectangular in shape and may be flared from its inlet to the open base 32. The receptacle 34 may rest on a floor support 42 which may have levelling means 44, and is separable therefrom. Baffle means may be at least partially submerged in the particulate matter entrapping liquid and positioned between the walls of the hood and the receptacle walls to define a zone, the liquid levelling means being operatively positioned in the zone. The receptacle may be sized to provide a distance between its walls and the walls of the hood such that the turbulence of the liquid caused by the escaping gaseous stream is at a minimum at the receptacle walls. Fig. 10 (not shown) shows apparatus for carrying out the separation comprising a dust-collecting apparatus which includes a manifold 126 positioned adjacent a moving surface 120 and a powder applicator 122 to entrap powder which has become airborne, air distribution means 134 located in the manifold supplied with air by means 130, 132 to cause the powder to move towards the ends of the manifold, a respective plenum 138 adjacent each end of the manifold, the powder being exhausted from the ends of the manifold through the plenums through lines 140, 142 to blower 144 into the dustseparating apparatus 146 which includes a receptacle for containing a particulate matter entrapping liquid, a hood having an inlet to receive the air stream exhausted from the manifold, an open base and walls defining a chamber sized to assist, in use, in adjusting the velocity of the air stream to that quoted above as it exits the open base, the blood being partially wtihin but spaced from the receptacle and means for adjusting, in use, the liquid level in the receptacle to a distance of less than about 3/8 inch from the open base and a means for maintaining the liquid level at such distance.
IT67855/72A 1971-03-18 1972-03-17 PROCEDURE AND APPARATUS FOR ELIMINATING SUBSTANCES IN PARTICLES FROM A GAS CURRENT IT960366B (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB721671A GB1377752A (en) 1971-03-18 1971-03-18 Method and device for removing particles from a gaseous stream

Publications (1)

Publication Number Publication Date
IT960366B true IT960366B (en) 1973-11-20

Family

ID=9828857

Family Applications (1)

Application Number Title Priority Date Filing Date
IT67855/72A IT960366B (en) 1971-03-18 1972-03-17 PROCEDURE AND APPARATUS FOR ELIMINATING SUBSTANCES IN PARTICLES FROM A GAS CURRENT

Country Status (14)

Country Link
AR (1) AR195166A1 (en)
AT (1) AT345260B (en)
AU (1) AU464548B2 (en)
BE (1) BE780908A (en)
BR (1) BR7201610D0 (en)
CA (1) CA982931A (en)
CH (1) CH560064A5 (en)
DE (1) DE2213276C3 (en)
ES (1) ES400922A1 (en)
FR (1) FR2130458B1 (en)
GB (1) GB1377752A (en)
IT (1) IT960366B (en)
NL (1) NL7203631A (en)
ZA (1) ZA721751B (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4330510A (en) * 1978-03-28 1982-05-18 Schauer John M Method for cleansing noxious constituents from gas streams
DE4230124A1 (en) * 1992-09-09 1994-03-10 Babcock Energie Umwelt Device for cooling hot gases
EP1722180A4 (en) * 2004-03-05 2008-01-23 Yasakawa Sangyo Co Ltd INSTALLATION OF A COOLING AND CLEANING DEVICE FOR BURNED GAS DISENGAGED BY A REFILLING STOVE
CN113521939A (en) * 2020-04-16 2021-10-22 南阳市固德威机械装备有限公司 Dry tail powder collecting device of starch
CN115302080B (en) * 2022-10-11 2023-01-17 四川智龙激光科技有限公司 Convection type metal dust particle recovery device for material reducing machine tool

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2816621A (en) * 1956-11-13 1957-12-17 Fred W Weaver Humidifier and dust collector for industrial purposes
US3527026A (en) * 1968-06-03 1970-09-08 Mitsugi Miura Apparatus for treating a gas to remove impurities therefrom
FR2088778A5 (en) * 1970-04-24 1972-01-07 Tunzini

Also Published As

Publication number Publication date
AU4004272A (en) 1973-09-20
ATA235472A (en) 1978-01-15
DE2213276B2 (en) 1977-07-14
AT345260B (en) 1978-09-11
BR7201610D0 (en) 1973-09-20
NL7203631A (en) 1972-09-20
DE2213276A1 (en) 1972-09-21
FR2130458B1 (en) 1974-10-18
FR2130458A1 (en) 1972-11-03
CH560064A5 (en) 1975-03-27
CA982931A (en) 1976-02-03
BE780908A (en) 1972-07-17
ZA721751B (en) 1972-12-27
AR195166A1 (en) 1973-09-19
ES400922A1 (en) 1975-09-01
AU464548B2 (en) 1975-08-15
GB1377752A (en) 1974-12-18
DE2213276C3 (en) 1978-04-06

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