CN2416953Y - Full boiling type apparatus for removing sulphur and dust - Google Patents
Full boiling type apparatus for removing sulphur and dust Download PDFInfo
- Publication number
- CN2416953Y CN2416953Y CN 00207667 CN00207667U CN2416953Y CN 2416953 Y CN2416953 Y CN 2416953Y CN 00207667 CN00207667 CN 00207667 CN 00207667 U CN00207667 U CN 00207667U CN 2416953 Y CN2416953 Y CN 2416953Y
- Authority
- CN
- China
- Prior art keywords
- housing
- shell body
- perforated plate
- dust
- plate
- 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.)
- Expired - Fee Related
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Abstract
The utility model relates to a full boiling type device for removing sulphur and dust, which comprises a blower, an exhaust pipe, a vortex plate, a shell body and a smoke inlet. The top part of the shell body is connected with the exhaust pipe. The blower is arranged on the exhaust pipe. The vortex plate, a perforated plate and an ash hopper are arranged in the shell body. The smoke inlet is arranged on the shell body and between the perforated plate and the ash hopper. The bottom part of the shell body is connected with a filtering pool and a circulation chamber. The circulation chamber is connected into the shell body through a pump and a water pipe. The utility model has the advantage of high dust removing effect. The utility model can completely avoid the problems of blockage of the perforated plate, water which is driven by the blower, corrosion and large quantity of waste water.
Description
The utility model relates to dust arrester, especially a kind of full boiling type desulfation dust-extraction device.
At first release and be put to produce the blank of full boiling desulfation dust-extraction device--bubble dust collector as far back as the fifties Soviet Union scholar, afterwards, Japan and some countries of west also carried out research and extension to this, and obtained certain progress.But because resource and social development situation different separately, each state all successively attention diversion to as having gone on electric cleaner, the sack cleaner.Wet scrubber approximately is the sixties also to be introduced into China, and once obtained using more widely, but because they have occurred in running such as sieve plate obstruction, fan belt water, corrosion, big, the not high many disadvantages of efficient of wastewater flow rate, this class deduster has slowly disappeared.
The purpose of this utility model just provides a kind of efficiency of dust collection height, can avoid orifice plate obstruction, fan belt water, corrosion, full boiling type desulfation dust-extraction device that wastewater flow rate is big.
The utility model purpose is realized by following technical scheme:
Full boiling type desulfation dust-extraction device comprises blower fan, blast pipe, eddy flow plate, housing, advances mouth, pump, water pipe, case top and blast pipe join, blast pipe is provided with blower fan, the housing internal upper part is provided with the eddy flow plate, and the bottom is an ash bucket, is provided with two-layer perforated plate between eddy flow plate and the ash bucket, housing side between ash bucket and perforated plate has into mouth, housing bottom communicates with filtering ponds, and filtering ponds link to each other with circular chamber, and circular chamber links to each other with housing by pump, water pipe.
Full boiling type desulfation dust-extraction device operation principle:
Full boiling type desulfation dust-extraction device reasonably cloth wind makes air-flow from bottom to top evenly by the water layer on the perforated plate, when air velocity is controlled within the specific limits, can form boiling bed on perforated plate, the bubble foam constantly breaks, merges again and generates in boiling bed.When ash-laden gas at boiling bed by high temperature, dirt gas is divided into two immediately, air-flow is output, and dust is captured, and sulfur dioxide obtains neutralization, gas is purified, Purge gas is discharged from blast pipe, and dust collection is in ash bucket, and water flow into filtering ponds through ash bucket, enter circular chamber again, be input in the housing once more from water pipe through pumping action.
Full boiling type desulfation dust-extraction device of the present utility model has the following advantages:
1, adopts the sandwich tape orifice plate, guaranteed to seethe with excitement and carried out smoothly, and prevented the clogging generation;
2, adopt the spiral-flow type dehydration, thereby obtained under the little situation of drag losses, to be close to 100% dehydrating effect, solved fan belt water or water fender blockage problem in the past;
3, solve the slag ash and handle problems, and handle old water well, guaranteed that water recycles in some cycles.
Below in conjunction with accompanying drawing the utility model is elaborated.
Full boiling type desulfation dust-extraction device comprises blower fan 1, blast pipe 2, eddy flow plate 3, housing 4, advance mouth 8, pump 12, water pipe 13, housing 4 tops and blast pipe 2 join, blast pipe 2 is provided with blower fan 1, housing 4 internal upper parts are provided with eddy flow plate 3, the bottom is an ash bucket 9, be provided with two-layer perforated plate 5 between eddy flow plate 3 and the ash bucket 9,6, housing 4 sides that ash bucket 9 and perforated plate are 6 have into mouth 8, enter mouth 8 places sprinkler head 7 is set, housing 4 bottoms communicate with filtering ponds 10, filtering ponds 10 link to each other with circular chamber 11, and circular chamber 11 is by pump 12, water pipe 13 and housing 4 interior eddy flow plates 3, cavity between the perforated plate 5 links to each other.
Claims (2)
1, a kind of full boiling type desulfation dust-extraction device comprises blower fan (1), blast pipe (2), eddy flow plate (3), housing (4), advance mouth (8), pump (12), water pipe (13), housing (14) top and blast pipe (2) join, blast pipe (2) is provided with blower fan (1), it is characterized in that: housing (4) internal upper part is provided with eddy flow plate (3), the bottom is ash bucket (9), be provided with two-layer perforated plate (5) between eddy flow plate (3) and the ash bucket (9), (6), housing (4) side between ash bucket (9) and perforated plate (6) has into mouth (8), housing (4) bottom communicates with filtering ponds (10), filtering ponds (10) link to each other with circular chamber (11), and circular chamber (11) is by pump (12), water pipe (13) and the interior eddy flow plate of housing (4) (3), cavity links to each other between the perforated plate (5).
2, full boiling type desulfation dust-extraction device according to claim 1 is characterized in that: advance mouth (8) and locate to be provided with sprinkler head (7).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 00207667 CN2416953Y (en) | 2000-04-11 | 2000-04-11 | Full boiling type apparatus for removing sulphur and dust |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 00207667 CN2416953Y (en) | 2000-04-11 | 2000-04-11 | Full boiling type apparatus for removing sulphur and dust |
Publications (1)
Publication Number | Publication Date |
---|---|
CN2416953Y true CN2416953Y (en) | 2001-01-31 |
Family
ID=33575262
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN 00207667 Expired - Fee Related CN2416953Y (en) | 2000-04-11 | 2000-04-11 | Full boiling type apparatus for removing sulphur and dust |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN2416953Y (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103127793A (en) * | 2013-03-11 | 2013-06-05 | 张家凡 | Exhaust gas cleaner |
CN104028072A (en) * | 2014-06-23 | 2014-09-10 | 中能佳程环保能源科技(北京)有限公司 | Method for performing flue gas purification by turning-back cyclone type multistage flue gas purification equipment |
-
2000
- 2000-04-11 CN CN 00207667 patent/CN2416953Y/en not_active Expired - Fee Related
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103127793A (en) * | 2013-03-11 | 2013-06-05 | 张家凡 | Exhaust gas cleaner |
CN104028072A (en) * | 2014-06-23 | 2014-09-10 | 中能佳程环保能源科技(北京)有限公司 | Method for performing flue gas purification by turning-back cyclone type multistage flue gas purification equipment |
CN104028072B (en) * | 2014-06-23 | 2016-02-10 | 中能佳程环保能源科技(北京)有限公司 | Cyclonic multi-stage flue gas cleaning equipment of turning back is utilized to carry out the method for gas cleaning |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C19 | Lapse of patent right due to non-payment of the annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |