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 CURRENTInfo
- 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
Links
- 239000002245 particle Substances 0.000 title abstract 2
- 239000000126 substance Substances 0.000 title 1
- 239000007788 liquid Substances 0.000 abstract 10
- 239000000843 powder Substances 0.000 abstract 4
- 239000013618 particulate matter Substances 0.000 abstract 3
- 238000000926 separation method Methods 0.000 abstract 2
- 239000008280 blood Substances 0.000 abstract 1
- 210000004369 blood Anatomy 0.000 abstract 1
- 230000002301 combined effect Effects 0.000 abstract 1
- 230000003068 static effect Effects 0.000 abstract 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract 1
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
- B01D47/02—Separating 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
- B01D47/021—Separating 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
-
- 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
- B01D47/02—Separating 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
- B01D47/024—Separating 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B41—PRINTING; LINING MACHINES; TYPEWRITERS; STAMPS
- B41F—PRINTING MACHINES OR PRESSES
- B41F23/00—Devices for treating the surfaces of sheets, webs, or other articles in connection with printing
- B41F23/002—Devices 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.
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)
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)
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 |
-
1971
- 1971-03-18 GB GB721671A patent/GB1377752A/en not_active Expired
-
1972
- 1972-03-14 ZA ZA721751A patent/ZA721751B/en unknown
- 1972-03-15 CA CA137,154A patent/CA982931A/en not_active Expired
- 1972-03-16 AU AU40042/72A patent/AU464548B2/en not_active Expired
- 1972-03-17 NL NL7203631A patent/NL7203631A/ unknown
- 1972-03-17 BE BE780908A patent/BE780908A/en unknown
- 1972-03-17 AR AR241003A patent/AR195166A1/en active
- 1972-03-17 CH CH398372A patent/CH560064A5/xx not_active IP Right Cessation
- 1972-03-17 IT IT67855/72A patent/IT960366B/en active
- 1972-03-18 DE DE2213276A patent/DE2213276C3/en not_active Expired
- 1972-03-18 ES ES400922A patent/ES400922A1/en not_active Expired
- 1972-03-20 BR BR721610A patent/BR7201610D0/en unknown
- 1972-03-20 FR FR7209635A patent/FR2130458B1/fr not_active Expired
- 1972-03-20 AT AT235472A patent/AT345260B/en not_active IP Right Cessation
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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