CN2436803Y - Oil-combustion fume purifier - Google Patents
Oil-combustion fume purifier Download PDFInfo
- Publication number
- CN2436803Y CN2436803Y CN 00237891 CN00237891U CN2436803Y CN 2436803 Y CN2436803 Y CN 2436803Y CN 00237891 CN00237891 CN 00237891 CN 00237891 U CN00237891 U CN 00237891U CN 2436803 Y CN2436803 Y CN 2436803Y
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- gas
- tower body
- oil burning
- nozzle
- cyclone
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Abstract
The utility model relates to an oil-combustion fume purifier. A plurality of vortex mixers and cyclone separators are arranged in a tower, and row of atomizing nozzles are arranged among the vortex mixer or on the upper surfaces of the vortex mixers. The spraying nozzles are connected with a circulation water pump on the outside of the tower body. The utility model uses the combination of wet dust removing and the chemical processing, the vortex mixing technology and the atomizing nozzles with large through diameters and no plugs, the fume can be purified in a same device, and the chrominance is below the Ringelman first level. The utility model can be widely used for the purification of the oil-combustion fume.
Description
The utility model belongs to environmental protection equipment, is specifically related to a kind of gas from oil burning purifier.
At present, fuel oils such as industrial furnace, boiler, smelting furnace, generating set, oxidation reaction can generate grit and pernicious gas under complete or imperfect combustion state, as CO
x, NO
x, SO
2Deng, general designation flue gas, serious environment pollution and influence health of people and quality of life.
Improvement technology to above-mentioned pernicious gas still is in development, improves the stage, and these technology are concluded, and great majority belong to the conventional art of dry type and wet dust removal to be used, and some is aided with chemical method and removes pernicious gas on physical method.In this type of The Application of Technology, electrostatic technique was once voguish, but proved through application practice for many years: static can only dedusting and can not be removed pernicious gas, and power consumption is big, cost is high, volume is big, the life-span is short, makes it be difficult to apply.Other wet type technology is used, and as spray absorption, auto-excitation type, water dissolving type etc., the basic agent input that accompanies by at some pernicious gas absorbs, and all has certain effect, but still has many deficiencies at aspects such as processing method, device structure and effects.Gas cleaning degree after handling does not generally speaking reach the Lin Geman one-level and maybe can not remove most pernicious gas.
The purpose of this utility model is the deficiency at existing gas from oil burning purifier, provide a kind of simple in structure, easy to operate, cost is low, operating cost is little, the better gas from oil burning purifier of clean-up effect.
The purpose of this utility model is to realize by following technical solution:
This gas from oil burning purifier is to be provided with several cyclone mixers and several cyclone separators in tower body, one group of spraynozzle is equipped with in the cyclone mixer top, nozzle links to each other by the outer water circulating pump of pipeline and tower body, and the pipeline other end links to each other with the cyclic water tank of bottom in the tower body.
The number needs of nozzle, cyclone mixer is decided according to exhaust gas volumn in described tower body diameter and the tower body, and exhaust gas volumn is big, and the tower body diameter is big, and the tower body planted agent is provided with more nozzle and cyclone mixer; Nozzle should arrange evenly that this nozzle has dismountable cap and sphere eddy flow chamber, taper eddy flow chamber and cap port spreading of spray.When pressure liquid medicine entered sphere eddy flow chamber, taper eddy flow chamber by nozzle eccentric orfice tangent line, it was vaporific to produce conical hollow, promptly was atomized into small water smoke form (being atomized steam) ejection, jeting area ringwise, spray angle is 40 ° to 90 °.This spraynozzle can produce the atomized steam that is evenly distributed under flow and the pressure on a large scale.
The structure of described cyclone mixer is identical with the structure of cyclone separator, described cyclone separator belongs to prior art, the utility model is according to the size of required smoke treatment amount, designing and calculating is determined the size of the diameter and the corresponding component thereof of required cyclone mixer, cyclone separator, thereby select the cyclone separator of current version specification for use, the garden tubular cyclone separator of ring type blade in preferably selecting for use.
Be added with chemical agent in the described cyclic water tank.Added chemical agent is a block polyether.
The utility model is owing to having adopted wet dust removal and chemical treatment efficiently and eddy flow hybrid technology, major path not to have the nozzle of obstruction atomization technique, flue gas can efficiently purify in same device, good purification, below the gas cleaning Du Dalingeman one-level after the processing, other index also is better than national standard, water consumption, electric weight are little, simple in structure, cost is low, and operating cost is little, be applicable to contain the less gas cleaning of particulate, be particularly useful for gas from oil burning and purify.
Below in conjunction with accompanying drawing the utility model gas from oil burning purifier is described further:
Fig. 1 is the structural representation of the utility model gas from oil burning purifier.
Fig. 2 is the nozzle structural representation of the utility model gas from oil burning purifier atomizing.
Fig. 3 is the cyclone mixer of the utility model gas from oil burning purifier and the swirl vane scheme of installation of cyclone separator.
As shown in Figure 1, the utility model has the tower body 1 of a tubular to be made by steel plate, and its underpart is provided with air inlet 11, and guide plate 12 is housed in the air inlet, and its top is provided with gas outlet 13.In tower body, be provided with three cyclone mixers 2 above the air inlet, the interior ring type swirl vane 20 that this blender adopts steel plate to make, its external diameter is fixed on the tower body inwall, and it is that gas-liquid two-phase quickens to rotate, fully mixes and the grit separating and treating apparatus.Above cyclone mixer, be provided with three cyclone separators 8, the interior ring type swirl vane 20 that this cyclone separator adopts steel plate to make, its external diameter is fixed on the tower body inwall, and it is that gas-liquid two-phase quickens rotation, separating and treating apparatus.One group of spraynozzle 3 is housed above cyclone mixer, is used to provide atomizing liquid medicine.Its structure as shown in Figure 2, it is made up of housing 14 and dismountable cap 15 that is contained in the housing water outlet end, housing 14 is square, make with stainless steel material, has screw thread on its water inlet, the delivery port inwall, have eccentric orfice 16 and sphere eddy flow chamber 17 in it, cap 15 is threadedly connected to housing 14 water outlet ends, has taper eddy flow chamber 18 in it, it is 40 ° to 90 ° that water outlet end has spreading of spray, make the soup tangent line enter inner chamber, quicken, produce the ejection of conical hollow spray form through ball, conical internal cavity rotation.Nozzle 3 links to each other with placing tower body 1 water pump 10 outward by pipeline 9.Pipeline 9 other ends link to each other with cyclic water tank 28 in tower body 1 bottom.Be added with the chemical agent block polyether in the water tank.This chemical agent is alkalescence, and the lipophile smokeshade is had extremely strong wetting power, and pernicious gas is had very strong solvability, it and CO
x, NO
x, SO
2Deng all chemical reaction takes place, the compound of generation is a kind of nuisanceless inorganic matter.During use, water tank changed water in one time every month, added medicine weekly one time, and by the dosing of water yield size, concentration is about 1%.
During work, flue gas is under blower fan air-supply (malleation) or exhausting (negative pressure) state, air inlet 11 through linking to each other with fume pipe, and behind guide plate 12 water conservancy diversion, enter in the tower body 1, entering cyclone mixer acceleration rotation then fully mixes, contacts with the atomizing soup that sprays through nozzle 3, flue gas is atomized soup and fully absorbs, and with medicament generation chemical reaction wherein, grit volume and weight in the flue gas is increased rapidly, under action of centrifugal force, got rid of to smooth tower body 1 inwall and assembled, fall to tower body 1 bottom naturally and regularly remove.Through three grades quicken the rotation mixing, absorption is with chemical reaction and separate, and makes grit and pernicious gas in the flue gas reduce step by step, purify.Flue gas after being purified enters in the cyclone separator 8 through quickening rotation for three times carries out the aqueous vapor two-phase and effectively separates, at last by outlet 13 dischargings; Separated drop is assembled on tower body 1 inwall, falls to tower body 1 bottom cyclic water tank 28 naturally, links to each other with water pump 10 by pipeline 9, recycles.
Claims (5)
1. gas from oil burning purifier, it is characterized in that being provided with in the tower body (1) several cyclone mixers (2) and several cyclone separators (8), one group of spraynozzle (3) is equipped with in the cyclone mixer top, nozzle (3) links to each other by pipeline (9) water circulating pump (10) outer with placing tower body (1), and pipeline (9) other end links to each other with the cyclic water tank (28) of the interior bottom of tower body (1).
2. gas from oil burning purifier according to claim 1 is characterized in that described eddy flow mixes (2) and cyclone separator (8) is a kind of garden tubular cyclone separator of interior ring type blade (20).
3. gas from oil burning purifier according to claim 1, it is characterized in that described nozzle does not have the plug of seeing spraynozzle for the big latus rectum of evenly arranging, this nozzle is made up of housing (14) and dismountable cap (15) that is contained in the housing port of export, housing (14) is square, have eccentric orfice (16) and sphere eddy flow chamber (17) and taper eddy flow chamber (18) in this nozzle, cap (15) is threadedly connected to housing (14) water outlet end, and its port has spreading of spray (19).
4. gas from oil burning purifier according to claim 1 is characterized in that being added with chemical agent in the described cyclic water tank (28).
5. gas from oil burning purifier according to claim 1 is characterized in that described chemical agent is a block polyether.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 00237891 CN2436803Y (en) | 2000-08-11 | 2000-08-11 | Oil-combustion fume purifier |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 00237891 CN2436803Y (en) | 2000-08-11 | 2000-08-11 | Oil-combustion fume purifier |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2436803Y true CN2436803Y (en) | 2001-06-27 |
Family
ID=33599054
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 00237891 Expired - Fee Related CN2436803Y (en) | 2000-08-11 | 2000-08-11 | Oil-combustion fume purifier |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2436803Y (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105536391A (en) * | 2015-12-31 | 2016-05-04 | 河北唯沃环境工程科技有限公司 | High-pressure self-rotation centrifugal air washer |
| CN105921495A (en) * | 2016-06-12 | 2016-09-07 | 常熟市畅晟环保科技发展有限公司 | Household garbage incineration fly ash stabilizing treatment system |
| CN108434966A (en) * | 2018-06-11 | 2018-08-24 | 深圳市山水乐环保科技有限公司 | A kind of incinerator smoke processing unit and its method |
| CN110465171A (en) * | 2019-08-19 | 2019-11-19 | 石家庄天鲲化工设备有限公司 | Low temperature liquid phase cyclone desulfuration denitration dust-removing integrated technique |
| CN111871086A (en) * | 2020-07-06 | 2020-11-03 | 龙井和 | Imitative dandelion formula printing and dyeing waste gas's floccule adsorption equipment |
| CN112337616A (en) * | 2019-08-06 | 2021-02-09 | 吴万益 | Movable livestock carcass crushing and drying treatment equipment |
| CN113736520A (en) * | 2021-08-18 | 2021-12-03 | 中国神华煤制油化工有限公司 | Equipment for rapidly reducing temperature of furnace blowing out in low-temperature zone and process treatment method |
-
2000
- 2000-08-11 CN CN 00237891 patent/CN2436803Y/en not_active Expired - Fee Related
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105536391A (en) * | 2015-12-31 | 2016-05-04 | 河北唯沃环境工程科技有限公司 | High-pressure self-rotation centrifugal air washer |
| CN105921495A (en) * | 2016-06-12 | 2016-09-07 | 常熟市畅晟环保科技发展有限公司 | Household garbage incineration fly ash stabilizing treatment system |
| CN108434966A (en) * | 2018-06-11 | 2018-08-24 | 深圳市山水乐环保科技有限公司 | A kind of incinerator smoke processing unit and its method |
| CN112337616A (en) * | 2019-08-06 | 2021-02-09 | 吴万益 | Movable livestock carcass crushing and drying treatment equipment |
| CN110465171A (en) * | 2019-08-19 | 2019-11-19 | 石家庄天鲲化工设备有限公司 | Low temperature liquid phase cyclone desulfuration denitration dust-removing integrated technique |
| CN111871086A (en) * | 2020-07-06 | 2020-11-03 | 龙井和 | Imitative dandelion formula printing and dyeing waste gas's floccule adsorption equipment |
| CN111871086B (en) * | 2020-07-06 | 2022-01-18 | 江苏原木环境科技有限公司 | Imitative dandelion formula printing and dyeing waste gas's floccule adsorption equipment |
| CN113736520A (en) * | 2021-08-18 | 2021-12-03 | 中国神华煤制油化工有限公司 | Equipment for rapidly reducing temperature of furnace blowing out in low-temperature zone and process treatment method |
| CN113736520B (en) * | 2021-08-18 | 2022-04-29 | 中国神华煤制油化工有限公司 | Equipment for rapidly reducing temperature of furnace blowing out in low-temperature zone and process treatment method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20010627 Termination date: 20090911 |