CN87204649U - Low-resistance whirlwind type boiler duster with heat-exchange function - Google Patents
Low-resistance whirlwind type boiler duster with heat-exchange function Download PDFInfo
- Publication number
- CN87204649U CN87204649U CN 87204649 CN87204649U CN87204649U CN 87204649 U CN87204649 U CN 87204649U CN 87204649 CN87204649 CN 87204649 CN 87204649 U CN87204649 U CN 87204649U CN 87204649 U CN87204649 U CN 87204649U
- Authority
- CN
- China
- Prior art keywords
- whirlwind
- heat exchange
- dust
- heat
- cylindrical shell
- 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.)
- Withdrawn
Links
Images
Landscapes
- Cyclones (AREA)
Abstract
The utility model discloses a low-resistance whirlwind type boiler duster with heat-exchange function, comprising a dust-contained airflow inlet [1], a whirlwind cylindrical shell [7], a whirlwind ash hopper [10], a net gas outlet [4], a dust exhausting valve [9], etc. The utility model is characterized in that the whirlwind cylindrical shell [7] is a log spiral whirlwind cylindrical shell, a heat exchange spiral water pipe [6] is arranged in the whirlwind cylindrical shell [7], and simultaneously, a bottom plate [11] of the boiler duster is arranged between the whirlwind cylindrical shell [7] and the whirlwind ash hopper [10]. The utility model has the advantages of simple structure, low cost, convenient maintenance, good dust removing effect, dust removing and heat exchange, and can be used to replace the precious boiler economizer.
Description
The utility model relates to a kind of heat exchange low resistance cyclone deduster.
At present, the cyclone dust collectors that use all only as gathering dust and usefulness, generally all comprise dust-contained airflow inlet (1) both at home and abroad, cyclone cylinder (7), whirlwind ash bucket (10), pure qi (oxygen) outlet (4), flange (5), dust discharge valve (9) etc.The dust constaining air-flow enters cyclone cylinder (7) by dust-contained airflow inlet (1), in cylindrical shell (7), the air-flow rotation, produce centrifugal force, soot dust granule is separated, the grit of collecting gathers in the whirlwind ash bucket (10), regularly removes through the dust discharge valve, and the air-flow after the purification is through pure qi (oxygen) outlet (4) discharging.Such deduster all adopts steel to make, and is high temperature resistant, can be used for the clarifying smoke of industrial furnace, still, but still has been discharged into atmosphere for heat contained in the high-temperature flue gas, caused the thermal pollution of atmosphere and the waste of heat energy.And the gas-flow resistance loss is bigger, serious wear, the coating that has wearing layer, also can only use about 1 year.
The purpose of this utility model be to provide a kind of can dedusting, can reclaim the heat exchange low-resistance deduster of contained heat energy in the flue gas again, to reduce to the thermal pollution of atmosphere and the waste of heat energy.
Solution of the present utility model is the log spiral principle that forms according to sand-flood, make the log spiral Whirlwind barrel, the heat exchange pipe with spiral pipe is installed in the log spiral Whirlwind barrel, make cold water and high-temperature flue gas in the water pipe carry out heat exchange, reclaim a large amount of heat energy in the high-temperature flue gas, reduce the thermal pollution of atmosphere and the waste of heat energy.Simultaneously, between log spiral Whirlwind barrel and whirlwind ash bucket, be provided with the deduster base plate,, reduce the whirlpool loss of energy to cut off forced vortex rotation air-flow.
The utility model comprises the dust-contained airflow inlet, Whirlwind barrel, the whirlwind ash bucket, the pure qi (oxygen) outlet, flange, dust discharge valve, it is characterized in that Whirlwind barrel is the log spiral Whirlwind barrel, the heat exchange pipe with spiral pipe is installed in Whirlwind barrel, simultaneously, between log spiral Whirlwind barrel and whirlwind ash bucket, is provided with the deduster base plate.Its feature also is to be equipped with in the log spiral Whirlwind barrel two groups, three groups or organize the heat exchange pipe with spiral pipe more, to improve heat exchange efficiency.Flow through dust-contained airflow inlet of the ash-laden gas of high temperature, enter in the log spiral Whirlwind barrel, in Whirlwind barrel, the air-flow rotation, produce centrifugal force, soot dust granule is separated, the grit of collection gathers in the whirlwind ash bucket, open the dust discharge valve and regularly remove, the air-flow after the purification is through pure qi (oxygen) outlet discharging.In the dust constaining air-flow rotation separating process of high temperature, because the rotation of air-flow, produce eddy current, make air-flow along the pipe with spiral pipe horizontal stroke, vertically wash away, produce strong heat exchange effect, heat is passed to the cold water that is flowed into pipe with spiral pipe by cooling water inlet, and the water behind the absorption heat is sent into boiler or is made other purposes by hot water outlet.Between log spiral Whirlwind barrel and whirlwind ash bucket, be provided with the deduster base plate, can cut off forced vortex rotation air-flow, reduce the whirlpool loss of energy.
Fig. 1 is a structure principle chart of the present utility model.
Fig. 2 is a vertical view of the present utility model.
The utility model is described in further detail below in conjunction with accompanying drawing.
The utility model as shown in Figure 1, it comprises dust-contained airflow entrance (1), Whirlwind barrel (7), whirlwind ash bucket (10), pure qi (oxygen) outlet (4), flange (5), dust discharge valve (9), the Whirlwind barrel (7) that is characterised in that of the present utility model is the log spiral Whirlwind barrel, is provided with deduster base plate (11) between log spiral Whirlwind barrel (7) and whirlwind ash bucket (10). Be further characterized in that in the log spiral Whirlwind barrel (7). Be equipped with two groups, three groups or organize heat exchange pipe with spiral pipe (6), to improve heat exchange efficiency, as shown in Figure 1, be the situation that the heat exchange pipe with spiral pipe (6) of three groups of various outer diameters is installed more. The ash-laden gas of the high temperature dust-contained airflow entrance (1) of flowing through, enter in the log spiral Whirlwind barrel (7), in Whirlwind barrel (7), flow rotation produces centrifugal force, and soot dust granule is separated, the grit of collecting gathers in the whirlwind ash bucket (10), open dust discharge valve (9), regularly remove, the air-flow after the purification is through pure qi (oxygen) outlet (4) discharging. In the process of the dust constaining air-flow rotating separation of high temperature, because the rotation of air-flow, produce eddy current, make air-flow horizontal along heat exchange pipe with spiral pipe (6), vertically wash away, produce strong heat exchange effect, heat is passed to the cold water that is flowed into heat exchange pipe with spiral pipe (6) by cooling water inlet (8), and the water behind the absorbing heat is sent into boiler or is made other purposes by hot water outlet. Between log spiral Whirlwind barrel (7) and whirlwind ash bucket (10), be provided with deduster base plate (11), can play partition, forced vortex rotation air-flow, reduce the whirlpool loss of energy.
The utility model is simple in structure, and cost is low, and dust-collecting efficiency reaches more than 80%, and resistance loss is below 300 handkerchiefs, and the coefficient of heat transfer is more than 40. This deduster can play the effect of gathering dust of cyclone dust collectors, can play again the effect of boiler economizer; Particularly can directly replace present boiling boiler, the economizer of coal-powder boiler, and the heat exchanging water pipe need not artificial deashing. If be installed on the lower grate furnace of dust exhausting concentration, can reach the secondary row mark requirement of China.
Embodiment:
Log spiral Whirlwind barrel of the present utility model (7) can be rolled with veneer reeling machine by cold bundle or heat bundle thin plate and form, top board (3), whirlwind ash bucket (10), deduster base plate (11) all are connected with flange with log spiral Whirlwind barrel (7), its airflow inlet (1), outlet (4) all are connected with flange with flue, dust-exhausting port is provided with dust discharge valve (9), so that lock gas and ash discharge.Heat exchange pipe with spiral pipe (6) bends with the pachydermia seamless pipe and forms, and is screwed with deduster, so that the dismounting when changing.
Description of reference numerals:
High temperature dust air flow inlet---(1); Hot water outlet---(2);
Deduster top board---(3); Pure qi (oxygen) outlet---(4);
Flange---(5); Heat exchange pipe with spiral pipe---(6);
Log spiral Whirlwind barrel---(7); Cooling water inlet---(8);
Dust discharge valve---(9); Whirlwind ash bucket---(10);
Deduster base plate---(11).
Claims (2)
1, a kind of heat exchange low resistance cyclone deduster, comprise dust-contained airflow inlet [1], Whirlwind barrel [7], whirlwind ash bucket [10], pure qi (oxygen) outlet [4], flange [5], dust discharge valve [9], the Whirlwind barrel [7] that is characterised in that of the present utility model is the log spiral Whirlwind barrel, heat exchange pipe with spiral pipe [6] is installed in Whirlwind barrel [7], simultaneously, between Whirlwind barrel [7] and whirlwind ash bucket [10], be provided with deduster base plate [11].
2, heat exchange low-resistance deduster according to claim 1 is characterized in that being equipped with in the Whirlwind barrel (7) two groups, three groups or organize heat exchange pipe with spiral pipe (6) more.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 87204649 CN87204649U (en) | 1987-09-30 | 1987-09-30 | Low-resistance whirlwind type boiler duster with heat-exchange function |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 87204649 CN87204649U (en) | 1987-09-30 | 1987-09-30 | Low-resistance whirlwind type boiler duster with heat-exchange function |
Publications (1)
Publication Number | Publication Date |
---|---|
CN87204649U true CN87204649U (en) | 1988-04-20 |
Family
ID=4820503
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN 87204649 Withdrawn CN87204649U (en) | 1987-09-30 | 1987-09-30 | Low-resistance whirlwind type boiler duster with heat-exchange function |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN87204649U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110438289A (en) * | 2019-07-31 | 2019-11-12 | 中国科学院力学研究所 | A kind of coal gas of converter cyclone dust collectors |
-
1987
- 1987-09-30 CN CN 87204649 patent/CN87204649U/en not_active Withdrawn
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110438289A (en) * | 2019-07-31 | 2019-11-12 | 中国科学院力学研究所 | A kind of coal gas of converter cyclone dust collectors |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN104534491A (en) | Ultralow-dust rear smoke channel system of boiler | |
CN208952142U (en) | A kind of smoke comprehensive processing unit | |
CN87204649U (en) | Low-resistance whirlwind type boiler duster with heat-exchange function | |
CN101629725A (en) | Method for reducing ash fouling of air preheater of coal burning boiler and cyclone separator therefor | |
CN204404203U (en) | A kind of boiler ultra low-ash back-end ductwork system | |
CN108421637A (en) | Industrial waste gas fine particle coalescence removes and the total system of UTILIZATION OF VESIDUAL HEAT IN | |
CN203170448U (en) | High-efficiency heat pipe heat-exchange type cyclone dust collector | |
CN2148597Y (en) | Wet-type, efficient dust collector | |
CN209828585U (en) | Calcium carbide furnace gas purifying and dust removing device | |
CN209917461U (en) | Axial flow combined type dust removal system for high-temperature high-dust-content flue gas | |
CN207294699U (en) | Cold process system between a kind of novel powdered coal temperature gasification and high dedusting | |
CN2148888Y (en) | Streamlined coal-saving device | |
CN207159151U (en) | A kind of pyrolkigneous liquid collecting device | |
CN87214854U (en) | D.c. cyclone slit-type dust remover | |
CN2405644Y (en) | Electric stone-ash collecting device | |
CN2165331Y (en) | Dusting coal-saver | |
CN2222891Y (en) | Flue gas purifying energy saver | |
CN87214901U (en) | Dual-inserter cyclone dust collector and heat exchanger | |
CN2073082U (en) | Heat exchanger with dust-collection | |
CN214209943U (en) | Cyclone type gypsum rain removing device | |
CN2428698Y (en) | Small-boiler energy-saving desulfurizing dust-collecting integrated apparatus | |
CN215413218U (en) | Be provided with ferrosilicon pouring flue gas waste heat recovery and recycle device of heat absorption cover | |
CN217315033U (en) | Biomass boiler flue gas dust collector | |
CN214536390U (en) | Coal gas condensate water heat exchanger | |
CN210219694U (en) | Flue type waste heat boiler with self-ash-cleaning function |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
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 |