CN2310936Y - Multipipe cyclone dust-collecting and heat-saving device - Google Patents
Multipipe cyclone dust-collecting and heat-saving device Download PDFInfo
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- CN2310936Y CN2310936Y CN 97220235 CN97220235U CN2310936Y CN 2310936 Y CN2310936 Y CN 2310936Y CN 97220235 CN97220235 CN 97220235 CN 97220235 U CN97220235 U CN 97220235U CN 2310936 Y CN2310936 Y CN 2310936Y
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- cyclone
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Abstract
The utility model relates to a dust collecting and heat saving device which is formed by utilizing multi-tube cyclone dust collectors, wherein, the goal of dust collecting on high temperature dust waste gases can be achieved by the cyclone dust collectors. Independent space is formed between an inlet pipe fixed plate arranged above a plurality of single distributed cyclone collectors and a sealing fixed plate arranged under the cyclone dust collectors. The distributed plurality of single cyclone dust collectors are divided into a Z-shaped air flow passage through partition boards in the independent space in which a heat exchanger is arranged. Both ends of the Z-shaped air flow passage are of a room temperature air inlet and a room temperature air outlet. The outside air flows through the Z-shaped air flow passage and does the heat exchange with a cylinder cone body of each single cyclone dust collector with the high temperature waste gases.
Description
The utility model is the device of a kind of control of dust and Jie Re.The control of dust and the economizer that particularly utilize the particular arrangement of multi-tube dust collector to carry out recuperation of heat.
Multi-tube dust collector is a kind of of existing dry type cyclone, is dust-contained airflow is entered in the cylinder cone via top vortex guide vane, the centrifugal force that utilizes its high speed rotary to produce, and reach the control of dust purpose.The cyclone that quantity is a lot, arrange and (square or rectangular is arranged) is set in the casing of same import and export, dust-contained airflow is evenly distributed in each cylinder cone allows unordered air-flow and crushing be reduced to minimum, the then separated funnel bottom that is deposited in of dust.Can be according to the processing air quantity, the droop loss size, dust catching efficiency, how many particle size selects caliber size and quantity.
Aspect energy technology utilizes, utilize heat recovery system from the exhaust device of gas turbine, diesel motor, boiler, kiln, incinerator and other discharging heat, to reclaim heat cost-effectively.In the application of recuperation of heat, the type of heat exchanger has: air is to gas, gas to water, gas to organic fluid, gas to water or steam etc., and air to gas application on, air preheater is to be used for reclaiming the contained heat energy of chimney exhaust gas, and improve a kind of heat-exchange apparatus of combustion-supporting chamber's temperature, have and can significantly reduce fuel consumption and improve the boiler combustion efficiency double benefit.
Therefore, the Waste Heat Recovery of air preheater is used, and is commonly industrial quarters and adopts, yet when any type of air preheat interchanger use Waste Heat Recovery, all may face the dust obstruction, the problem of crushing increase or cold end corrosion.Avoid extended surface tube to be had by the method that dust stops up: install soot blower (Soot Blower), filter screen (Filter) additional, adopt box (Cassette) the heat pipe heat exchanger, add wet method (Wet Air) and vibration dust method (Vibration) etc., wherein first three methods is fit to a spot of dust of control and stops up.The heat exchanger of box, the heat pipe of each row of tool can independently be extracted out and change or clean, but cost is higher.Add wet method and be fit to adopt when the moisture deal of waste gas is the highest, before waste gas enters heat pipe exchanger, hot water or steam are sprayed among the waste gas, make it, condense to quicken its dew point on tube wall near saturation state.
Adhere to solids and have the effectiveness that reduces pollution on the device of only a few, recuperation of heat program itself does not reduce air or water pollutes.Dust stops up incrustation to the utility model in the heat exchanger in order to overcome, and alleviates its wearing and tearing, improves heat recovery efficiency, can solve air pollution problems inherent (shot-like particle, cold end corrosion) simultaneously; With multi-tube dust collector modification the becoming air preheat interchanger of an air, will solve air pollution problems inherent from the waste gas control of dust of chimney or waste heat source on the one hand to gas; On the one hand will single cyclone be used as heat pipe and transmit heat by heat pipe and make and enter the air preheat that boiler combustion uses and reduce the heat of waste gas mistake that body is arranged, thereby can reduce the fuel consumption of boiler, the efficiency of combustion of raising boiler.
Known dust arrester, as No. the 200021st, Taiwan patent announcement, name is called " tower cyclone ", or announce No. 165597 " the special-purpose dust arrester of chimney " though etc. all have the function of control of dust, can't reclaim used heat effectively simultaneously.
The purpose of this utility model is to overcome the deficiencies in the prior art, provide a kind of have concurrently control of dust and joint hot merit can multi-cyclone control of dust and economizer, this device can prevent that air pollution again can energy savings, and improves efficiency of combustion.
The purpose of this utility model is achieved in that
A kind of multi-cyclone control of dust and economizer, it is to utilize the multi-tube dust collector configuration to form, several single cyclone of arranging are fixed with the inlet tube fixed head, become a separate space between the sealing fixed head of inlet tube fixed head and below, place as heat exchanger, this separate space and with dividing plate perpendicular to the sealing fixed head of top inlet tube fixed head and below, link these both, and several single the cyclone that will arrange are separated into the zigzag air flow channel, one end of this zigzag air flow channel is the air intake of a normal temperature, the other end then is the air outlet slit of high temperature, suck and send for outside air, outside air this zigzag air flow channel of flowing through, and carry out heat exchange with the cylinder cone of each single the cyclone that contains high-temp waste gas.
Multi-tube dust collector can be the multi-tube dust collector of wing shaft type multi-tube dust collector or other patterns; Also add an air-introduced machine that motor is housed up near the outlet.
The utility model utilizes a plurality of cyclones to constitute a heat exchanger, makes it to have control of dust and recuperation of heat double effects, can prevent that air pollution again can energy savings.This device can be arranged between waste heat source and the general heat exchanger, improves rate of heat exchange on the one hand, reduces the flue outlet temperature.Avoid general heat exchanger cigarette ash to stop up on the one hand, the air pollution that selective sootblowing caused also has the effect that prolongs life of heat-exchanger.
The utility model as air preheater, has increased the contact area of heat exchange because a plurality of single the dust arresters that will arrange are separated into the air flow channel of zigzag, improves rate of heat exchange, and reduces the high-temperature exhaust air amount, reduces contamination preventing equipment and running cost.The intake air that improves temperature via heat exchange can also be made for the heating source of other purposes.
The utility model is that a kind of combination is simple, can make the control of dust and the economizer of different configurations according to different environmental condition permissions, utilize intrinsic pressure fan of combustion apparatus and chimney that running can be installed, need not increase auxiliary power in addition, but also can additionally install air-introduced machine again additional to improve the efficient of ventilating.
Below in conjunction with accompanying drawing the specific embodiment of the present utility model is further described:
Fig. 1 is the stereogram of the utility model multi-cyclone control of dust and economizer outward appearance;
Fig. 2 is the utility model structural representation;
The cutaway view of Fig. 3 for being done along A-A line among Fig. 2;
The cutaway view of Fig. 4 for being done along M-M line among Fig. 2;
Fig. 5 is the schematic diagram that is provided with of the utility model one embodiment.
Be illustrated in figure 1 as the outward appearance of the utility model multi-cyclone control of dust and economizer (1), its body is a waterproofing and airtight corner post shape, and material is a steel plate, and outside lining rock wool and zinc coated sheet are in order to heat-insulation and heat-preservation; The below is PYR funnel (2), connects rotary valve (3) down.As shown in Figure 2, the utility model multi-cyclone control of dust and economizer contain a plurality of lists cyclone (4) only, and high temperature dust waste gas system enters via high temperature dust exhaust gas entrance (15).Inlet tube fixed head (5) in whole, be in order to carry each single cyclone (4), intercept high temperature simultaneously and contain waste gas, make it must be in vortex guide vane (6) enter cyclone cylinder cone (7), discharge via rotary valve (3) and dust separation is deposited in pyramid funnel (2) bottom, peace and quiet gas is then sent through top outlet (8) again.The working procedure of this cyclone (4) is known to the technology operating personnel in this field, and non-main points of the present invention, so do not add detailed description.
As shown in Figures 2 and 3,,, sealed and fixed, only stayed dust outlet (9) as inlet tube fixed head (5) with each single cyclone (4) below side by side; Simultaneously as shown in Figure 4 to be same as the dividing plate (10) of inlet tube fixed head (5) material, connect the inlet tube fixed head (5) of top and the sealing fixed head (11) of below, and each single the cyclone (4) that will arrange is separated into zigzag air flow channel (12) as shown in Figure 3, and the air intake (13) of a normal temperature and the air outlet slit (14) of high temperature (Fig. 2 and Fig. 3 arrow are depicted as the flow direction of air) are respectively opened in front and back, this zigzag air flow channel supplies the usefulness of carrying out heat exchange from normal temperature air inlet (13) outside air that enters and the cyclone cylinder cone (7) that contains high-temp waste gas promptly as the place of heat exchanger.As shown in Figure 3, dividing plate (10) is separated into zigzag air flow channel (12) with whole separate space, outside air enters the mouth after (13) enter from an end normal temperature air, flow through whole zigzag air flow channel (12) and contact with the cylinder cone of the cyclone that contains high-temp waste gas and carry out heat exchange, come out from the high temperature air outlet (14) of the other end then, and continue to improve the usefulness of the heating of heating installation as preheated burning air, air-conditioning, heavy oil, medicine etc. and dry sandstone aggregate, mud, adobe etc., or other purposes are as the usefulness of heating source.
Fig. 5 is the configuration schematic diagram of a control of dust and recuperation of heat specific embodiment, (arrow is represented the direction of transporting among the figure) wherein, fuel (20) is delivered to burner (22) via fuel channel (21), confuse the preheated burning air that comes by the preheated burning air duct and produce burning, the high-temp waste gas that comes from waste heat source (23) owing to the burning generation is transported to the utility model multi-cyclone control of dust and economizer (1) via high-temp waste gas pipeline (24), after control of dust and recuperation of heat, peace and quiet air is then discharged from chimney (26) via the discharge tube (25) of top.The outside air that sucks enters zigzag passage (12) from normal temperature air inlet (13), through sending by high temperature air outlet (14) after the heat exchange, sending pipeline (27) via air is transported to preheated burning air duct (28) or is made for heating or sludge-dryings such as heavy oil, medicine, the usefulness of adobe (29), also can be used as the heating source (30) of other purposes, then discharge through chimney (26) again.
It should be noted that the utility model multi-cyclone control of dust shown in Fig. 5 and economizer additionally add one and the air-introduced machine (16) of motor (17) be housed to improve its drafting efficiency near top outlet (8).
Claims (3)
1. multi-cyclone control of dust and economizer, it is to utilize the multi-tube dust collector configuration to form, it is characterized in that: single cyclone of several of arrangement is fixed with the inlet tube fixed head, become a separate space between the sealing fixed head of inlet tube fixed head and below, place as heat exchanger, this separate space and with dividing plate perpendicular to the sealing fixed head of top inlet tube fixed head and below, link these both, and several single the cyclone that will arrange are separated into the zigzag air flow channel, one end of this zigzag air flow channel is the air intake of a normal temperature, the other end then is the air outlet slit of high temperature, suck and send for outside air, outside air this zigzag air flow channel of flowing through carries out heat exchange with the cylinder cone of each single the cyclone that contains high-temp waste gas.
2. multi-cyclone control of dust as claimed in claim 1 and economizer is characterized in that: described multi-tube dust collector can be the multi-tube dust collector of wing shaft type multi-tube dust collector or other patterns.
3. multi-cyclone control of dust as claimed in claim 1 and economizer is characterized in that: add an air-introduced machine that motor is housed up near the outlet.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 97220235 CN2310936Y (en) | 1997-09-23 | 1997-09-23 | Multipipe cyclone dust-collecting and heat-saving device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 97220235 CN2310936Y (en) | 1997-09-23 | 1997-09-23 | Multipipe cyclone dust-collecting and heat-saving device |
Publications (1)
Publication Number | Publication Date |
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CN2310936Y true CN2310936Y (en) | 1999-03-17 |
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN 97220235 Expired - Fee Related CN2310936Y (en) | 1997-09-23 | 1997-09-23 | Multipipe cyclone dust-collecting and heat-saving device |
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CN (1) | CN2310936Y (en) |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102141244A (en) * | 2010-11-26 | 2011-08-03 | 张家港华汇特种玻璃有限公司 | Powder tube of spray gun |
CN104383754A (en) * | 2014-11-21 | 2015-03-04 | 信阳凯米特环保工程有限公司 | Combined heat-exchange dust remover for production of expanded perlite |
CN104402281A (en) * | 2014-11-21 | 2015-03-11 | 信阳凯米特环保工程有限公司 | Opening expanded perlite complete production equipment |
CN105854491A (en) * | 2016-05-31 | 2016-08-17 | 浙江惠尔涂装环保设备有限公司 | Spray powder recycling device |
CN106064011A (en) * | 2016-07-06 | 2016-11-02 | 浙江惠尔涂装环保设备有限公司 | A kind of dusty spray retracting device |
CN106110805A (en) * | 2016-05-31 | 2016-11-16 | 浙江惠尔涂装环保设备有限公司 | The filter mechanism of dusty spray retracting device |
CN108151047A (en) * | 2017-12-23 | 2018-06-12 | 云南乾程科技开发有限公司 | A kind of biomass combustion thermal energy complete utilization gas cleaning hot air apparatus |
CN110545706A (en) * | 2017-04-13 | 2019-12-06 | 泰通株式会社 | Dust suction device suitable for beads |
-
1997
- 1997-09-23 CN CN 97220235 patent/CN2310936Y/en not_active Expired - Fee Related
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102141244A (en) * | 2010-11-26 | 2011-08-03 | 张家港华汇特种玻璃有限公司 | Powder tube of spray gun |
CN104383754A (en) * | 2014-11-21 | 2015-03-04 | 信阳凯米特环保工程有限公司 | Combined heat-exchange dust remover for production of expanded perlite |
CN104402281A (en) * | 2014-11-21 | 2015-03-11 | 信阳凯米特环保工程有限公司 | Opening expanded perlite complete production equipment |
CN104402281B (en) * | 2014-11-21 | 2016-09-14 | 信阳凯米特环保工程有限公司 | Perforate expanded perlite complete production unit |
CN105854491A (en) * | 2016-05-31 | 2016-08-17 | 浙江惠尔涂装环保设备有限公司 | Spray powder recycling device |
CN106110805A (en) * | 2016-05-31 | 2016-11-16 | 浙江惠尔涂装环保设备有限公司 | The filter mechanism of dusty spray retracting device |
CN106064011A (en) * | 2016-07-06 | 2016-11-02 | 浙江惠尔涂装环保设备有限公司 | A kind of dusty spray retracting device |
CN110545706A (en) * | 2017-04-13 | 2019-12-06 | 泰通株式会社 | Dust suction device suitable for beads |
CN108151047A (en) * | 2017-12-23 | 2018-06-12 | 云南乾程科技开发有限公司 | A kind of biomass combustion thermal energy complete utilization gas cleaning hot air apparatus |
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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 |