CN104722160A - Wet dust removal system and method - Google Patents
Wet dust removal system and method Download PDFInfo
- Publication number
- CN104722160A CN104722160A CN201510158485.1A CN201510158485A CN104722160A CN 104722160 A CN104722160 A CN 104722160A CN 201510158485 A CN201510158485 A CN 201510158485A CN 104722160 A CN104722160 A CN 104722160A
- Authority
- CN
- China
- Prior art keywords
- deduster
- air outlet
- spray equipment
- communicated
- circulating line
- 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.)
- Pending
Links
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
-
- 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
- B01D47/12—Washers with plural different washing sections
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/26—Drying gases or vapours
Abstract
The invention discloses a wet dust removal system and method. The system comprises a first deduster and a second deduster, wherein the first deduster is communicated with a nanometer foam machine, nanoscale foam groups are generated to be subjected to convection with smoke, so that physical and chemical reaction in the smoke are accelerated, an ideal dust removal effect is achieved, meanwhile, through the arrangement of the second deduster, acidic or alkaline impurities and other impurities in the smoke are further removed, and the pollution to the environment and the harm to human bodies caused by the smoke are reduced.
Description
Technical field
The present invention relates to airhandling equipment and method, particularly relate to a kind of wet dedusting system and method.
Background technology
The general principle of wet scrubber is the larger particles allowing liquid or drop and relatively little grit contact, combine the easy trapping of generation.In this process, grit grows up to large particle by several method.These methods comprise larger drop and grit are combined, and grit absorbs moisture thus quality (or density) to be increased, or the formation of condensable particle and increase under lower temperature in deduster.
Wet scrubber manufacturing cost is relatively low, but for chemical industry, spray paint, the dust with moisture content, viscosity and penetrating odor that glaze spraying, the industry such as pigment produce is optimal dedusting method.Diameter can be that the liquid state of 0.1-20 microns or solid particles remove from air-flow by wet scrubber effectively, meanwhile, also can remove part gaseous contaminant.It has that structure is simple, floor space is little, operation and easy to maintenance and purification efficiency advantages of higher, the air-flow of high temperature, high humidity can be processed, water also can be utilized to remove a part of peculiar smell may minimizing of catching fire, explode, if harmful gas (as a small amount of sulfur dioxide, salt acid mist etc.), absorbent can be prepared absorb in cleaning solution.
The common at present wet scrubber of existing wet scrubber is the suction utilizing centrifugal high pressure fan, dusty gas is pressed onto in the tank that certain altitude water is housed, and water-bath can a part of dust adsorption in water.After uniform shunting, gas flows from the bottom up, and high-pressure nozzle then sprays water smoke from top to bottom, the grit of trapping remainder.Existing deduster dust removing effects is undesirable.
The people such as rain fruit (Hugo) propose solid liquid interface and there is nano bubble in the process of research surface hydrophobicity long-range mechanism of action, due to the difference of experiment condition, the pattern of various countries scientist to nano bubble has different views, and the bubble be present in liquid usually size being less than hundreds of nanometer is called nano bubble.The manufacture of nano bubble has multiple method, as directly method, external source method, alcohol water Shift Method, chemical reaction method etc. are put in leaching.The advantages such as nano bubble has substantial amounts, and surface area is huge, and translational speed is slow, dissolved oxygen content is large, in environmental protection industry (epi), Metallurgy Industry, aquatic products industry and agricultural, sewage disposal.Health fields etc. have huge applications prospect.
Summary of the invention
The present invention provides a kind of wet dedusting system to solve deficiency of the prior art, efficiency of dust collection is high, water loss is few, except dust quantity large.
For achieving the above object, the technical solution used in the present invention is:
A kind of wet dedusting system, comprise the first deduster and the second deduster that are communicated with successively, nanometer foam machine is provided with bottom the first described deduster, to be communicated with the spray equipment on the first deduster top by the first circulating line and to form peripheral passage, first deduster lower end is provided with the first air inlet, upper end is provided with the first air outlet, first air outlet is communicated with by second air inlet of ventilation shaft with the second deduster lower end, collecting tank is provided with bottom second deduster, collecting tank is communicated with the spray equipment in the second deduster by the second circulating line, collecting tank is connected with medicine system, second dust remover roof is provided with the second air outlet.
As a kind of preferred version of wet dedusting system of the present invention, the second described air outlet is provided with drying device, preferred drying device is macromolecule desciccator diaphragm, can certainly be other drying devices, water vapor filtering in gas after scrubbing is got off continue to use, steam can be reduced on the one hand to enter in a large number in air, also can reduce the consumption of recirculated water in the second deduster on the other hand.
As a kind of preferred version of wet dedusting system of the present invention, the first described circulating line and the second circulating line are equipped with water circulating pump.
The present invention discloses a kind of dust collection method utilizing described wet dedusting system, flue gas enters the first deduster bottom by the first described air inlet and upwards flows, start nanometer foam machine and produce nano bubble, nano bubble enters spray equipment by water circulating pump along the first circulating line, spray through spray equipment explosion type, obtain highly dispersed nano bubble group, convection current is formed with flue gas stream upwards, in decline process, nano bubble group surrounds suspended particulate in flue gas and captures and swim on nanometer foam machine liquid level, wind through a scrubbing enters the second deduster through ventilation shaft, and flow from down to up in the second deduster, liquid in collecting tank is sprayed downwards by spray equipment after water circulating pump pressurization, convection current is formed with wind upwards, wind after secondary scrubbing reaches discharge standard and discharges along the second air outlet.
Accompanying drawing explanation
Fig. 1 is wet dedusting system schematic diagram provided by the invention.
Wherein: 1, the first deduster 2, second deduster 3, nanometer foam machine 4, first circulating line 5, second circulating line 6,7, spray equipment 8, collecting tank 9, medicine system 10, drying device 11,12, water circulating pump 13, ventilation shaft
Detailed description of the invention
Below in conjunction with the drawings and specific embodiments, the present invention is described in further detail.
Embodiment 1
As shown in Figure 1, a kind of wet dedusting system, comprise the first deduster 1 and the second deduster 2 be communicated with successively, nanometer foam machine 3 is provided with bottom the first described deduster 1, by the first circulating line 4 nanometer foam machine 3 is communicated with the spray equipment 6 on the first deduster top and forms peripheral passage, first circulating line 4 is provided with water circulating pump 11, the nanometer foam that nanometer foam machine produces is pressurized to spray equipment 6 and explosion type ejection by water circulating pump 11, forming nano bubble group spreads in the cavity of the first deduster 1, nano bubble group forms nanoscale bubble by breaing up after water oxygenation, these bubbles are assembled, wrapped up by larger bubble, form the bubble group that dissolved oxygen content is huge, accelerate the physics in flue gas, chemical reaction, obtain desirable dust removing effects.
First deduster lower end is provided with the first air inlet, upper end is provided with the first air outlet, first air outlet is communicated with the second air inlet of the second deduster lower end by ventilation shaft 13, collecting tank 8 is provided with bottom second deduster, collecting tank 8 is communicated with the spray equipment 7 in the second deduster by the second circulating line 5, second circulating line 5 is provided with water circulating pump, spray equipment is pressed into by after the liquid pressing in collecting tank, and sprayed by spray equipment 7, further dedusting is carried out to the air-flow by the second deduster.Collecting tank 8 is connected with medicine system (not shown in FIG.), the flue gas of dedusting as required or the character of dirty air, adds corresponding effective liquid, and regulated the concentration of chemical feeding quantity by medicine system in medicine system.Second dust remover roof is provided with the second air outlet, and the second air outlet is provided with drying device 10, and preferred drying device is macromolecule desciccator diaphragm, can certainly be other drying devices.
Embodiment 2
A kind of dust collection method utilizing described wet dedusting system, flue gas enters the first deduster bottom by the first described air inlet and upwards flows, start nanometer foam machine and produce nano bubble, nano bubble enters spray equipment by water circulating pump along the first circulating line, spray through spray equipment explosion type, obtain highly dispersed nano bubble group, convection current is formed with flue gas stream upwards, in decline process, nano bubble group surrounds suspended particulate in flue gas and captures and swim on nanometer foam machine liquid level, wind through a scrubbing enters the second deduster through ventilation shaft, and flow from down to up in the second deduster, liquid in collecting tank is sprayed downwards by spray equipment after water circulating pump pressurization, convection current is formed with wind upwards, wind after secondary scrubbing reaches discharge standard after drying device drying, finally discharge along the second air outlet.
Although be illustrated embodiments of the present invention in description, these embodiments just as prompting, should not limit protection scope of the present invention.Carry out various omission, displacement and change without departing from the spirit and scope of the present invention all should be included in protection scope of the present invention.
Claims (6)
1. a wet dedusting system, it is characterized in that: comprise the first deduster and the second deduster that are communicated with successively, nanometer foam machine is provided with bottom the first described deduster, to be communicated with the spray equipment on the first deduster top by the first circulating line and to form peripheral passage, first deduster lower end is provided with the first air inlet, upper end is provided with the first air outlet, first air outlet is communicated with by second air inlet of ventilation shaft with the second deduster lower end, collecting tank is provided with bottom second deduster, collecting tank is communicated with the spray equipment in the second deduster by the second circulating line, collecting tank is connected with medicine system, second dust remover roof is provided with the second air outlet.
2. wet dedusting system according to claim 1, is characterized in that: the second described air outlet is provided with drying device.
3. wet dedusting system according to claim 2, is characterized in that: described drying device is macromolecule desciccator diaphragm.
4. wet dedusting system according to claim 1, is characterized in that: the first described circulating line and the second circulating line are equipped with water circulating pump.
5. one kind utilizes the dust collection method of the wet dedusting system described in claim 1, it is characterized in that: flue gas enters the first deduster bottom by the first described air inlet and upwards flows, start nanometer foam machine and produce nano bubble, nano bubble enters spray equipment by water circulating pump along the first circulating line, spray through spray equipment explosion type, obtain highly dispersed nano bubble group, convection current is formed with flue gas stream upwards, in decline process, nano bubble group surrounds suspended particulate in flue gas and captures and swim on nanometer foam machine liquid level, wind through a scrubbing enters the second deduster through ventilation shaft, and flow from down to up in the second deduster, liquid in collecting tank is sprayed downwards by spray equipment after water circulating pump pressurization, convection current is formed with wind upwards, wind after secondary scrubbing reaches discharge standard and discharges along the second air outlet.
6. wet dust removal method according to claim 5, is characterized in that: the wind after secondary scrubbing is just discharged by the second air outlet after drying device drying.
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201510158485.1A CN104722160A (en) | 2015-04-03 | 2015-04-03 | Wet dust removal system and method |
PCT/CN2015/087032 WO2016155196A1 (en) | 2015-04-03 | 2015-08-14 | Wet dust removing system and dust removing method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201510158485.1A CN104722160A (en) | 2015-04-03 | 2015-04-03 | Wet dust removal system and method |
Publications (1)
Publication Number | Publication Date |
---|---|
CN104722160A true CN104722160A (en) | 2015-06-24 |
Family
ID=53446941
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201510158485.1A Pending CN104722160A (en) | 2015-04-03 | 2015-04-03 | Wet dust removal system and method |
Country Status (2)
Country | Link |
---|---|
CN (1) | CN104722160A (en) |
WO (1) | WO2016155196A1 (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2016155188A1 (en) * | 2015-04-03 | 2016-10-06 | 永固工程技术(江苏)有限公司 | Outdoor fresh air purifying system |
WO2016155196A1 (en) * | 2015-04-03 | 2016-10-06 | 永固工程技术(江苏)有限公司 | Wet dust removing system and dust removing method |
CN108392940A (en) * | 2017-02-08 | 2018-08-14 | 江苏绿陵百农可生物科技有限公司 | The dust treatment system of deodorization and dedusting for poultry house |
CN111957186A (en) * | 2020-06-29 | 2020-11-20 | 福建省气柜设备安装有限公司 | Wet-process corona desulfurization denitration dedusting flue gas purification device and use method thereof |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1040930A (en) * | 1988-09-06 | 1990-04-04 | 巴布考克日立株式会社 | Apparatus for desulfurization of waste pases by wet process |
US20100089133A1 (en) * | 2008-10-10 | 2010-04-15 | Sharp Kabushiki Kaisha | Nanobubble-containing liquid producing apparatus and nanobubble-containing liquid producing method |
CN203905994U (en) * | 2014-05-15 | 2014-10-29 | 上海世骞节能科技有限公司 | Foam and dry fog dust suppression all-in-one machine equipment |
CN104359175A (en) * | 2014-11-12 | 2015-02-18 | 长江水利委员会长江科学院 | Water-base air purifying device for haze and dust environments |
CN204182256U (en) * | 2014-10-13 | 2015-03-04 | 北京国电龙源环保工程有限公司 | A kind of washing degree of depth dust arrester |
CN204522614U (en) * | 2015-04-03 | 2015-08-05 | 永固工程技术(江苏)有限公司 | A kind of wet dedusting system |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007245118A (en) * | 2006-03-20 | 2007-09-27 | Sharp Corp | Exhaust gas treating method and exhaust gas treating system |
JP2010089054A (en) * | 2008-10-10 | 2010-04-22 | Sharp Corp | Treating device and treating method |
CN201735293U (en) * | 2010-07-13 | 2011-02-09 | 蚌埠丰原明胶有限公司 | Wet-type dust removal device |
CN104722160A (en) * | 2015-04-03 | 2015-06-24 | 永固工程技术(江苏)有限公司 | Wet dust removal system and method |
-
2015
- 2015-04-03 CN CN201510158485.1A patent/CN104722160A/en active Pending
- 2015-08-14 WO PCT/CN2015/087032 patent/WO2016155196A1/en active Application Filing
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1040930A (en) * | 1988-09-06 | 1990-04-04 | 巴布考克日立株式会社 | Apparatus for desulfurization of waste pases by wet process |
US20100089133A1 (en) * | 2008-10-10 | 2010-04-15 | Sharp Kabushiki Kaisha | Nanobubble-containing liquid producing apparatus and nanobubble-containing liquid producing method |
CN101721929A (en) * | 2008-10-10 | 2010-06-09 | 夏普株式会社 | Nanobubble-containing liquid producing apparatus and nanobubble-containing liquid producing method |
CN203905994U (en) * | 2014-05-15 | 2014-10-29 | 上海世骞节能科技有限公司 | Foam and dry fog dust suppression all-in-one machine equipment |
CN204182256U (en) * | 2014-10-13 | 2015-03-04 | 北京国电龙源环保工程有限公司 | A kind of washing degree of depth dust arrester |
CN104359175A (en) * | 2014-11-12 | 2015-02-18 | 长江水利委员会长江科学院 | Water-base air purifying device for haze and dust environments |
CN204522614U (en) * | 2015-04-03 | 2015-08-05 | 永固工程技术(江苏)有限公司 | A kind of wet dedusting system |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2016155188A1 (en) * | 2015-04-03 | 2016-10-06 | 永固工程技术(江苏)有限公司 | Outdoor fresh air purifying system |
WO2016155196A1 (en) * | 2015-04-03 | 2016-10-06 | 永固工程技术(江苏)有限公司 | Wet dust removing system and dust removing method |
CN108392940A (en) * | 2017-02-08 | 2018-08-14 | 江苏绿陵百农可生物科技有限公司 | The dust treatment system of deodorization and dedusting for poultry house |
CN111957186A (en) * | 2020-06-29 | 2020-11-20 | 福建省气柜设备安装有限公司 | Wet-process corona desulfurization denitration dedusting flue gas purification device and use method thereof |
Also Published As
Publication number | Publication date |
---|---|
WO2016155196A1 (en) | 2016-10-06 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN205832807U (en) | Efficiently industrial waste gas processing system | |
CN206676187U (en) | A kind of organic exhaust gas adsorption spray cleaning equipment | |
CN105020782B (en) | Air purification method and air purifier | |
CN204522619U (en) | A kind of waste gas, PM2.5 particle, haze absorption cleaning car | |
CN104722160A (en) | Wet dust removal system and method | |
CN204522614U (en) | A kind of wet dedusting system | |
CN110314503A (en) | A kind of environment-protecting industrial waste gas purification apparatus | |
CN203577607U (en) | Multilevel high-efficiency waste gas purifying box | |
CN105536523B (en) | The purification method of container spray painting organic exhaust gas | |
CN205700007U (en) | A kind of cleaner unit for pelletizing discharging | |
CN203777867U (en) | Waste gas purification device | |
CN204768032U (en) | Water film dust collector | |
CN204447556U (en) | With the dedusting fan of multiple impacts formula gas-liquid separation | |
CN102824801B (en) | Rotary wet dust collector | |
CN207951092U (en) | A kind of super oxygen nanometer microbubble organic waste gas treatment system | |
CN203379766U (en) | Gas purification device | |
CN203842448U (en) | Wet type dust remover | |
CN104548918B (en) | The technique and system of particle content after a kind of reduction flue gas desulfurization | |
CN107096340A (en) | Hoisting type Wet smoke clarifier | |
CN211159071U (en) | Mining air pipe with dustproof function | |
CN203764054U (en) | Micro-pore type water-mist dust extraction device | |
CN204411978U (en) | A kind of fine particulates wet method capture system | |
CN203764117U (en) | Washing agent spraying adsorption type dust removal and deodorization device | |
CN203108413U (en) | Oxynitride absorption device | |
CN201899975U (en) | SO2 recovery device matched with coal burning boiler for use |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
RJ01 | Rejection of invention patent application after publication |
Application publication date: 20150624 |
|
RJ01 | Rejection of invention patent application after publication |