CN2889463Y - Solid and liquid two-phase purifier for odor gas - Google Patents
Solid and liquid two-phase purifier for odor gas Download PDFInfo
- Publication number
- CN2889463Y CN2889463Y CN 200620096010 CN200620096010U CN2889463Y CN 2889463 Y CN2889463 Y CN 2889463Y CN 200620096010 CN200620096010 CN 200620096010 CN 200620096010 U CN200620096010 U CN 200620096010U CN 2889463 Y CN2889463 Y CN 2889463Y
- Authority
- CN
- China
- Prior art keywords
- phase adsorption
- liquid
- adsorption chamber
- solid phase
- solid
- 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
Links
Landscapes
- Treating Waste Gases (AREA)
Abstract
The utility model discloses a solid-liquid phase off-flavor cleaner. The cleaner tank is divided into a solid phase adsorption chamber and a liquid phase adsorption chamber by a gas distribution plate arranged with a large amount of micropores; an off-flavor discharge pipe is arranged at the top of the tank, a solid phase adsorption stuffing inlet hole is arranged at the upper part of the solid phase adsorption chamber, a solid phase adsorption stuffing outlet hole is positioned at the lower part of the solid phase adsorption chamber, a liquid adsorption inlet hole is positioned at the upper part of the liquid phase adsorption chamber, a liquid adsorption outlet hole is positioned at the lower part of the liquid phase adsorption chamber, and an off-flavor inlet pipe is inserted in the liquid phase adsorption chamber and communicated with a gas distribution pipe locating at the bottom of the liquid phase adsorption chamber. The micropore gas distribution plate is used for uniformly distributing gas and supporting the stuffing in the solid phase adsorption chamber. The off-flavor discharge pipe is inserted into the pipe. The two adsorption chambers both should reserve a space with certain height; otherwise, it will affect the deodorizing effect. The utility model has the advantages of no clogging, small volume, uniform gas distribution, corrosion resistance, and high deodorizing efficiency.
Description
Technical field
The utility model belongs to sewage disposal device, and specifically, it relates to a kind of clarifier, especially solid liquid two-phase odour purifier.
Background technology
Sewage disposal has become a major issue of environmental protection, produces a large amount of foul smell in the collection of Sewage Biological Treatment and sewage and storage process.Existing this type of odor treatment device is more, and the clarifier that is used for the foul smell processing also has much.A kind of clarifier commonly used is made up of tank body, air inlet, gas outlet, simple solid phase adsorption chamber (or liquid phase adsorption chamber), and there are problems such as easily obstruction, volume are big, gas distribution is inhomogeneous, perishable, odor removal efficient is not high in this clarifier.
Summary of the invention
The purpose of this utility model is to provide a kind of clarifier that overcomes above-mentioned defective, i.e. solid liquid two-phase odour purifier, this clarifier are difficult for stopping up, volume is little, gas distribution is even, corrosion-resistant, and the odor removal efficient height.
A kind of solid liquid two-phase odour purifier provided by the invention comprises the liquid phase adsorption chamber, it is characterized in that: the clarifier tank body is divided into the upper and lower two parts in solid phase adsorption chamber and liquid phase adsorption chamber by the air distribution plate that is distributed with a large amount of micropores; The foul smell discharge pipe is positioned at the tank body top, the solid phase adsorption filler enters the top that the hole is positioned at the solid phase adsorption chamber, the solid phase adsorption filler portals and is positioned at the bottom of solid phase adsorption chamber, adsorption liquid enters the top that the hole is positioned at the liquid phase adsorption chamber, adsorption liquid portals and is positioned at the bottom of liquid phase adsorption chamber, and the foul smell air inlet pipe is inserted in the liquid phase adsorption chamber and with the gas distribution pipe that is positioned at bottom, liquid phase adsorption chamber and is connected.
When using this solid liquid two-phase odour purifier, foul smell with certain pressure enters from the foul smell air inlet pipe, because the result of pressure effect, the place evenly discharges at gas distribution pipe, foul smell indoorly fully contacts with adsorption liquid in liquid phase adsorption, hybrid reaction and make, enter the solid phase adsorption chamber by the micropore air distribution plate then, the indoor solid phase adsorption filler of foul smell and solid phase adsorption contacts, after the foul smell discharge pipe is discharged solid liquid two-phase odour purifier.
Foul smell is under the effect of air-introduced machine or air blast, had behind certain pressure foul smell air inlet pipe by solid liquid two-phase odour purifier, form the bubble ejection that diameter is little, the gas-liquid contact area is big at the gas distribution pipe place, the micro-bubble that produces constantly breaks in the process of the indoor rising of liquid phase adsorption, and the moisture that is adsorbed in the liquid dissolves, chemical composition haptoreaction in the composition of generation stink and the adsorption liquid in the part foul smell, produce the new chemical substance of no stink, thereby remove the composition of most generation stink in the foul smell.Unnecessary foul smell upwards evenly enters the solid phase adsorption chamber by the micropore air distribution plate, the indoor layered arrangement adsorption stuffing of solid phase adsorption, difference according to ingredient in the foul smell is arranged each layer filler according to different ratios, foul smell is when flowing through each layer filler, contained different foul smell composition in the foul smell is adsorbed respectively, and the gas after the deodorizing enters atmosphere through the foul smell discharge pipe.
In a word, the utlity model has be difficult for to stop up, volume is little, gas distribution is even, corrosion-resistant and odor removal efficient advantages of higher.
Description of drawings
Fig. 1 is the structural representation of solid liquid two-phase odour purifier.
The specific embodiment
As shown in Figure 1, the utility model solid liquid two-phase odour purifier, by foul smell air inlet pipe 1, gas distribution pipe 2, liquid phase adsorption chamber 3, air distribution plate 4, solid phase adsorption chamber 5, foul smell discharge pipe 6 and clarifier tank body 7 are formed, be respectively equipped with in the upper and lower of liquid phase adsorption chamber 3 that adsorption liquid enters hole 8, adsorption liquid portals 9, be respectively equipped with in the upper and lower of solid phase adsorption chamber 5 that the solid phase adsorption filler enters hole 10, the solid phase adsorption filler portals 11.This clarifier tank body 7 adopts the integral type design, and is cylindric, and air distribution plate 4 is divided into two parts up and down to this clarifier, is solid phase adsorption chamber 5 above, is liquid phase adsorption chamber 3 below; Be distributed with a large amount of micropores on the air distribution plate 4, liquid phase adsorption chamber 3 communicates by the micropore on the air distribution plate 4 with solid phase adsorption chamber 5.The effect of micropore air distribution plate 4 has two: one, even gas distribution, the 2nd, the filler in the support solid phase adsorption chamber 5.Foul smell air inlet pipe 1 is inserted from the middle and upper part of liquid phase adsorption chamber 3, and links to each other with gas distribution pipe 2 downwards.Gas distribution pipe 2 can be perforation gas distribution pipe, microporous diaphragm air distribution head or tube-type micropore gas distribution pipe.Foul smell discharge pipe 6 inserts in the pipe from the top of tank body 7.It is after adsorption liquid absorption is saturated that adsorption liquid advances 9 the effect of portalling of hole 8 and adsorption liquid, portals from adsorption liquid and 9 discharges, and new adsorption liquid enters hole 8 from adsorption liquid and adds; It is after adsorption stuffing absorption is saturated that the solid phase adsorption filler advances 11 the effect of portalling of hole 10 and solid phase adsorption filler, portals from adsorption stuffing and 11 discharges, and new adsorption stuffing advances hole 10 layerings from filler and adds.The problem that should note is, the space of certain altitude all should be reserved in the top of two adsorption chambers, this part space preferably accounts for about 1/5 to 1/4 of each adsorption chamber space respectively, otherwise the bubble that produces in the liquid phase adsorption chamber easily enters the solid phase adsorption chamber, influences the solid phase adsorption effect; The space that top, solid phase adsorption chamber is reserved is to allow some leeway for packing layer in the foul smell uphill process expands, and this part space can not be excessive, if excessive, after filler expands, space between the filler is excessive, and foul smell may directly flow through packing layer without absorption, thereby causes adsorption effect to descend.
Claims (2)
1. a solid liquid two-phase odour purifier comprises the liquid phase adsorption chamber, it is characterized in that: clarifier tank body (7) is divided into the upper and lower two parts in solid phase adsorption chamber (5) and liquid phase adsorption chamber (3) by the air distribution plate that is distributed with a large amount of micropores (4); Foul smell discharge pipe (6) is positioned at tank body (7) top, the solid phase adsorption filler enters the top that hole (10) is positioned at solid phase adsorption chamber (5), the solid phase adsorption filler portal (11) be positioned at the bottom of solid phase adsorption chamber (5), adsorption liquid enters the top that hole (8) is positioned at liquid phase adsorption chamber (3), adsorption liquid portal (9) be positioned at the bottom of liquid phase adsorption chamber (3), foul smell air inlet pipe (1) is inserted in the liquid phase adsorption chamber (3) and with the gas distribution pipe (2) that is positioned at bottom, liquid phase adsorption chamber (3) and is connected.
2. solid liquid two-phase odour purifier according to claim 1 is characterized in that: the solid phase adsorption filler enters hole (10) apart from about 1/5 to 1/4 place, top, solid phase adsorption chamber (5), and adsorption liquid enters hole (8) apart from about 1/5 to 1/4 place, top, liquid phase adsorption chamber (3).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200620096010 CN2889463Y (en) | 2006-04-05 | 2006-04-05 | Solid and liquid two-phase purifier for odor gas |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200620096010 CN2889463Y (en) | 2006-04-05 | 2006-04-05 | Solid and liquid two-phase purifier for odor gas |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2889463Y true CN2889463Y (en) | 2007-04-18 |
Family
ID=38020115
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200620096010 Expired - Fee Related CN2889463Y (en) | 2006-04-05 | 2006-04-05 | Solid and liquid two-phase purifier for odor gas |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2889463Y (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101592587B (en) * | 2009-07-10 | 2012-10-10 | 中国科学院等离子体物理研究所 | Device and method for static corrosion experiment of liquid medium |
| CN103157124A (en) * | 2011-12-12 | 2013-06-19 | 美利环境技术（香港）有限公司 | Deodorizing gas-distribution plate |
| CN109603477A (en) * | 2018-12-28 | 2019-04-12 | 武汉紫光能控科技有限公司 | A kind of sewage disposal system eliminating malodours from gases device |
| CN110215788A (en) * | 2019-06-12 | 2019-09-10 | 深圳市昊源新辉电子有限公司 | A kind of printed circuit station-service dust collect plant |
-
2006
- 2006-04-05 CN CN 200620096010 patent/CN2889463Y/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101592587B (en) * | 2009-07-10 | 2012-10-10 | 中国科学院等离子体物理研究所 | Device and method for static corrosion experiment of liquid medium |
| CN103157124A (en) * | 2011-12-12 | 2013-06-19 | 美利环境技术（香港）有限公司 | Deodorizing gas-distribution plate |
| CN109603477A (en) * | 2018-12-28 | 2019-04-12 | 武汉紫光能控科技有限公司 | A kind of sewage disposal system eliminating malodours from gases device |
| CN109603477B (en) * | 2018-12-28 | 2024-04-09 | 中煤紫光湖北环保科技有限公司 | Gaseous deodorizing device of sewage treatment system |
| CN110215788A (en) * | 2019-06-12 | 2019-09-10 | 深圳市昊源新辉电子有限公司 | A kind of printed circuit station-service dust collect plant |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN202844876U (en) | Novel high-efficiency biological deodorization purifier | |
| CN2889463Y (en) | Solid and liquid two-phase purifier for odor gas | |
| CN105642083A (en) | Combined treatment technology for biochemical odors | |
| CN107021558A (en) | A kind of method and apparatus using drop filter processing sewage and foul smell | |
| CN100502952C (en) | Solid liquid two-phase odor purifier | |
| CN200974008Y (en) | Alkalescence solid and liquid washing and deodorizing tower | |
| CN203737105U (en) | Deodorizing device for sewage treatment | |
| CN106853331A (en) | A kind of device of large-wind-volume low-concentration foul gas purification | |
| CN201147648Y (en) | Sulfuric acid degassing tower | |
| CN200939376Y (en) | Mini plant for preparation of gas | |
| CN212348329U (en) | Kitchen waste biological deodorization device | |
| CN203355608U (en) | Bio-trickling filter tower | |
| CN204637922U (en) | A kind of cold analysis still device for recovering tail gas | |
| CN208356509U (en) | Two-part is layered postposition air inducing ring energy type deodoration system | |
| CN209406062U (en) | A kind of small towns sewage emission-control equipment | |
| CN202398284U (en) | High-efficiency biotrickling filter deodorizing device | |
| CN201036628Y (en) | Deodorizing device for vacuum dung-suction vehicle | |
| CN201144177Y (en) | Sewage purifier with biological carbon dynamic membrane | |
| CN220737057U (en) | Deodorization structure mounted on dissolved air flotation machine | |
| CN204380497U (en) | A kind of purification of air deodorizing tower | |
| CN218281262U (en) | Pharmacy workshop exhaust treatment device | |
| CN213032207U (en) | High-efficient environmental protection deodorizing device | |
| CN201565246U (en) | Odour treatment device | |
| CN205995230U (en) | A kind of amino acid fermentation tank tail-gas deep cleaning device | |
| CN110559828A (en) | Small tail gas absorption and deodorization device for sludge composting tail gas treatment |
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 |