CN111589230A - High-temperature dust removal and heat exchange integrated equipment - Google Patents
High-temperature dust removal and heat exchange integrated equipment Download PDFInfo
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- CN111589230A CN111589230A CN202010537597.9A CN202010537597A CN111589230A CN 111589230 A CN111589230 A CN 111589230A CN 202010537597 A CN202010537597 A CN 202010537597A CN 111589230 A CN111589230 A CN 111589230A
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- chamber shell
- heat exchange
- gas chamber
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- 239000000428 dust Substances 0.000 title claims abstract description 77
- 239000000779 smoke Substances 0.000 claims abstract description 16
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 8
- 229910001018 Cast iron Inorganic materials 0.000 claims description 4
- 241000237942 Conidae Species 0.000 claims description 3
- 238000007599 discharging Methods 0.000 claims 3
- 238000005299 abrasion Methods 0.000 claims 1
- 238000004519 manufacturing process Methods 0.000 abstract description 4
- 238000012423 maintenance Methods 0.000 abstract description 3
- 238000004140 cleaning Methods 0.000 abstract description 2
- 238000009434 installation Methods 0.000 abstract description 2
- 238000004134 energy conservation Methods 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 16
- 239000003546 flue gas Substances 0.000 description 13
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 12
- 238000000034 method Methods 0.000 description 4
- 239000002918 waste heat Substances 0.000 description 3
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 2
- XLOMVQKBTHCTTD-UHFFFAOYSA-N Zinc monoxide Chemical compound [Zn]=O XLOMVQKBTHCTTD-UHFFFAOYSA-N 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 239000011701 zinc Substances 0.000 description 2
- 229910052725 zinc Inorganic materials 0.000 description 2
- 238000003723 Smelting Methods 0.000 description 1
- 238000005266 casting Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000012774 insulation material Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000011787 zinc oxide Substances 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D45/00—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
- B01D45/04—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by utilising inertia
- B01D45/08—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by utilising inertia by impingement against baffle separators
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
- F28F9/22—Arrangements for directing heat-exchange media into successive compartments, e.g. arrangements of guide plates
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- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Chimneys And Flues (AREA)
- Separating Particles In Gases By Inertia (AREA)
Abstract
Description
技术领域technical field
本发明涉及一种高温除尘换热一体化设备,属于除尘换热设备技术领域。The invention relates to a high-temperature dedusting and heat-exchanging integrated equipment, belonging to the technical field of dedusting and heat-exchanging equipment.
背景技术Background technique
在冶炼氧化锌的过程中,因矿石的比例占多数,而矿石的温度要在1100℃时才能达到工艺要求,此时的锌已经溶解和气化,并且会与烟气粉尘等往后经过800mm的N形式的管道自然冷却然后去烟囱排放,在经过N形式的管道冷却时的余热是无法回收的,主要原因还是冷却后的锌与粉尘会堆积在换热管上,因此直到现在此烟气中的余热都不进行回收。In the process of smelting zinc oxide, the proportion of ore is the majority, and the temperature of the ore can only meet the process requirements when the temperature is 1100 ° C. At this time, the zinc has been dissolved and gasified, and will pass through 800mm of smoke and dust. The N-type pipe is naturally cooled and then discharged to the chimney. The waste heat cannot be recovered when the N-type pipe is cooled. The main reason is that the cooled zinc and dust will accumulate on the heat exchange pipe. The waste heat is not recovered.
发明内容SUMMARY OF THE INVENTION
本发明的目的在于克服现有技术中存在的不足,提供一种高温除尘换热一体化设备,可以降低烟气流动的阻力,提高换热和除尘效率。The purpose of the present invention is to overcome the deficiencies in the prior art, and to provide a high temperature dust removal and heat exchange integrated equipment, which can reduce the resistance of flue gas flow and improve the heat exchange and dust removal efficiency.
按照本发明提供的技术方案:一种高温除尘换热一体化设备,包括气室外壳,气室外壳的一侧侧部倾斜设置烟气进口,与所述烟气进口同一侧的气室外壳内壁上横向连接冲撞式平板集尘器,冲撞式平板集尘器的内端延伸至气室外壳中部,所述冲撞式平板集尘器位于烟气进口下方;气室外壳的内壁上环设冲撞式集尘板;According to the technical solution provided by the present invention: a high-temperature dust-removal and heat-exchange integrated equipment, comprising a gas chamber shell, one side of the gas chamber shell is obliquely provided with a flue gas inlet, and the inner wall of the gas chamber shell on the same side as the flue gas inlet The upper side is horizontally connected to the impact type flat dust collector, the inner end of the impact type flat dust collector extends to the middle of the air chamber shell, and the impact type flat dust collector is located below the flue gas inlet; the inner wall of the air chamber shell is surrounded by impact type dust collector;
所述气室外壳的底部与集尘换热器的上端联通,所述集成换热器包括直筒外壳,直筒外壳内固定设置内筒体,所述内筒体的上下两端分别设有封头,内筒体的筒壁上设置冲撞式换热除尘管,上端的封头连接出水管、下端的封头连接进水管;所述直筒外壳的下端联通盲状集尘管,所述盲状集尘管包括锥形外壳和下灰外壳,下灰外壳的底部设置放灰口;The bottom of the air chamber shell is communicated with the upper end of the dust collector heat exchanger, the integrated heat exchanger includes a straight-tube shell, an inner cylinder is fixed in the straight-tube shell, and the upper and lower ends of the inner cylinder are respectively provided with heads , the wall of the inner cylinder is provided with an impact heat exchange and dust removal pipe, the upper end head is connected to the water outlet pipe, and the lower end head is connected to the water inlet pipe; The dust pipe includes a conical shell and a lower ash shell, and the bottom of the lower ash shell is provided with an ash outlet;
所述直筒外壳的下端侧部设置烟气出口,烟气出口上端设置一弧形挡气板,弧形挡气板一头连接于位于烟气进口上端的筒体内壁上,弧形挡气板另一头穿过锥体外壳所在的筒体内部后延伸到下灰外壳所在的筒体段内部。The lower end side of the straight casing is provided with a smoke outlet, the upper end of the smoke outlet is provided with an arc-shaped air baffle, one end of the arc-shaped air baffle is connected to the inner wall of the cylinder at the upper end of the smoke inlet, and the other is the arc-shaped air baffle. One end passes through the interior of the cylinder where the cone shell is located and then extends to the interior of the cylinder section where the lower ash shell is located.
进一步地,所述气室外壳上固定设置气体分配器,气体分配器的截面为倒置的Y型,气体分配器位于气室外壳与直筒外壳相连处。Further, a gas distributor is fixed on the air chamber shell, the cross section of the gas distributor is an inverted Y shape, and the gas distributor is located at the connection between the air chamber shell and the straight cylinder shell.
进一步地,所述冲撞式平板集尘器、冲撞式集尘板和弧形平板集尘器均采用耐高温铸铁。Further, the impact type flat dust collector, the impact type dust collector plate and the arc-shaped flat dust collector are all made of high temperature resistant cast iron.
进一步地,所述冲撞式换热除尘管上设置防磨板。Further, a wear-resistant plate is arranged on the impact-type heat-exchange dust-removing pipe.
进一步地,所述内筒体内设置导流管。Further, a guide tube is arranged in the inner cylinder.
进一步地,所述内筒体的上端设有防磨罩。Further, the upper end of the inner cylinder is provided with a wear-resistant cover.
进一步地,所述内筒体通过设置在上部的定位撑和设置在下部的支撑架固定在直筒外壳内。Further, the inner cylinder body is fixed in the straight cylinder casing by a positioning brace provided on the upper part and a support frame provided on the lower part.
进一步地,所述气室外壳上设置人孔。Further, a manhole is provided on the air chamber shell.
进一步地,所述气室外壳、直筒外壳和锥形外壳和下灰外壳的壳体内外壁之间填充有浇注料。Further, castables are filled between the inner and outer walls of the shell of the air chamber shell, the straight shell, the conical shell and the lower ash shell.
本发明与现有技术相比,具有如下优点:Compared with the prior art, the present invention has the following advantages:
1.可以降低烟气流动的阻力。1. It can reduce the resistance of flue gas flow.
2.具有换热效率高,节省能源,除尘效果好,制造工艺简单,生产成本低,安装、维修、清洗方便的优点。2. It has the advantages of high heat exchange efficiency, energy saving, good dust removal effect, simple manufacturing process, low production cost and convenient installation, maintenance and cleaning.
3.采用了超出余热回收器体积的集尘罩,在罩内有多个集尘板可回收熔状型的颗粒。当罩内的集尘板收集堆积到一定量时,可以将集尘板更换掉。3. A dust collecting hood that exceeds the volume of the waste heat recovery device is adopted, and there are multiple dust collecting plates in the hood to recover molten particles. When the dust collecting plate in the hood collects and accumulates to a certain amount, the dust collecting plate can be replaced.
4.当换热管上的集尘保护板堆满后,可以从上部吊出更换。吊出时只需将下部的支撑松开,方便快捷。4. When the dust collecting protection plate on the heat exchange tube is full, it can be lifted from the top for replacement. When hanging out, just loosen the lower support, which is convenient and quick.
5.投资省回报快。5. Save investment and return quickly.
6.设备体积小,占地只有原来的1/20。6. The equipment is small in size, occupying only 1/20 of the original area.
7.维护保养简单方便,不需要停车检查,只需看阻力和温度等变化及可以知道内部运行情况。7. Maintenance is simple and convenient, no need to stop and check, just look at the changes in resistance and temperature and know the internal operation.
8.运行时间长,一般5年以上无需更换新设备。8. Long running time, generally no need to replace new equipment for more than 5 years.
附图说明Description of drawings
图1为本发明结构示意图。Figure 1 is a schematic structural diagram of the present invention.
附图标记说明:1-烟气进口、2-气室外壳、3-冲撞式平板集尘器、4-冲撞式集尘板、5-气体分配器、6-防磨罩、7-封头、8-出水管、9-定位撑、10-防磨板、11-换热除尘管、12-内筒体、13-导流管、14-支撑架、15-进水管、16-直筒外壳、17-弧形挡气板、18-锥形外壳、19-下灰外壳、20-浇注料、21-人孔、22-烟气出口、23-放灰口。Description of reference numerals: 1- flue gas inlet, 2- air chamber shell, 3- impact type flat dust collector, 4- impact type dust collector plate, 5- gas distributor, 6- anti-wear cover, 7- head , 8-water outlet pipe, 9-positioning support, 10-wear-proof plate, 11-heat exchange and dust removal pipe, 12-inner cylinder, 13-guide pipe, 14-support frame, 15-water inlet pipe, 16-straight cylinder shell , 17-curved baffle, 18-conical shell, 19-lower ash shell, 20-casting material, 21-manhole, 22-smoke outlet, 23-ash outlet.
具体实施方式Detailed ways
下面结合具体附图对本发明作进一步说明。The present invention will be further described below in conjunction with the specific drawings.
如图1所示,一种高温除尘换热一体化设备,包括气室外壳2,气室外壳2的一侧侧部倾斜设置烟气进口1,与所述烟气进口1同一侧的气室外壳2内壁上横向连接冲撞式平板集尘器3,冲撞式平板集尘器3的内端延伸至气室外壳2中部,所述冲撞式平板集尘器3位于烟气进口1下方;气室外壳2的内壁上环设冲撞式集尘板4;所述冲撞式平板集尘器3和冲撞式集尘板4都可以采用耐高温铸铁制作,烟气从侧部的烟气进口1进入后,冲撞到冲撞式平板集尘器3上后反弹到侧壁上的冲撞式集尘板4,再进入集尘换热器内。As shown in FIG. 1 , a high-temperature dust removal and heat exchange integrated equipment includes a gas chamber shell 2 , and a flue gas inlet 1 is inclined on one side of the gas chamber shell 2 , and a gas chamber on the same side as the flue gas inlet 1 is provided. The impact type
所述气室外壳2的底部与集尘换热器的上端联通,所述集成换热器包括直筒外壳16,直筒外壳16内固定设置内筒体12,所述内筒体12的上下两端分别设有封头7,内筒体12的筒壁上设置冲撞式换热除尘管11,上端的封头7连接出水管8、下端的封头7连接进水管15;所述直筒外壳16的下端联通盲状集尘管,所述盲状集尘管包括锥形外壳18和下灰外壳19,下灰外壳19的底部设置放灰口23;工作时放灰口23关闭,当灰尘积多了以后可以打开将灰排出。The bottom of the air chamber shell 2 communicates with the upper end of the dust collector heat exchanger. The integrated heat exchanger includes a
所述直筒外壳16的下端侧部设置烟气出口22,烟气出口22上端设置一弧形挡气板17,弧形挡气板17一头连接于位于烟气进口上端的筒体内壁上,弧形挡气板17另一头穿过锥体外壳18所在的筒体内部后延伸到下灰外壳19所在的筒体段内部。A
所述气室外壳2上固定设置气体分配器5,气体分配器5的截面为倒置的Y型,气体分配器5位于气室外壳2与直筒外壳16相连处。A
所述冲撞式平板集尘器3、冲撞式集尘板4和弧形平板集尘器17均采用耐高温铸铁。The impact type
所述冲撞式换热除尘管11上设置防磨板10。A wear-resistant plate 10 is provided on the impact heat exchange and dust removal pipe 11 .
所述内筒体12内设置导流管13。所述内筒体12的上端设有防磨罩6。所述气室外壳2上设置人孔21。A
所述内筒体12通过设置在上部的定位撑9和设置在下部的支撑架14固定在直筒外壳16内。The inner cylinder 12 is fixed in the
所述气室外壳2、直筒外壳16和锥形外壳18和下灰外壳19的壳体内外壁之间填充有浇注料20,浇注料20为保温材料。A castable 20 is filled between the inner and outer walls of the air chamber shell 2 , the
工作过程:高温废气从烟气进口1进入设备,经过冲撞式平板集尘器3除尘后再经过气室外壳四周的冲撞式集尘板4集尘进入下部一体集尘换热器,然后从下部盲状集尘管底部往上从烟气出口20排出设备。Working process: The high temperature exhaust gas enters the equipment from the flue gas inlet 1, is dedusted by the impact type
800℃左右的熔状式粉尘经过熔状粉尘收集盘收集,和四周的冲撞式集尘板集尘后,然后进入高温除尘换热一体设备再次除尘和温度回收,温度从800℃降至500℃左右,此时的熔状式颗粒经过温度下降后强度有所加强。然后经过中温除尘换热一体化设备再次进行除尘和换热。The molten dust at about 800 °C is collected by the molten dust collection tray, and after being collected by the surrounding impact dust collecting plates, it enters the high temperature dust removal and heat exchange integrated equipment for dust removal and temperature recovery again, and the temperature drops from 800 °C to 500 °C At this time, the strength of the molten particles is strengthened after the temperature is lowered. Then, the dust removal and heat exchange are carried out again through the integrated equipment of medium temperature dust removal and heat exchange.
可以理解的是,以上实施方式仅仅是为了说明本发明的原理而采用的示例性实施方式,然而本发明并不局限于此。对于本领域内的普通技术人员而言,在不脱离本发明的精神和实质的情况下,可以做出各种变型和改进,这些变型和改进也视为本发明的保护范围。It can be understood that the above embodiments are only exemplary embodiments adopted to illustrate the principle of the present invention, but the present invention is not limited thereto. For those skilled in the art, without departing from the spirit and essence of the present invention, various modifications and improvements can be made, and these modifications and improvements are also regarded as the protection scope of the present invention.
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CN206508767U (en) * | 2017-02-27 | 2017-09-22 | 天津普惠节能换热设备有限公司 | Flue gas disappears white equipment |
CN109357557A (en) * | 2017-09-22 | 2019-02-19 | 萍乡市华星环保工程技术有限公司 | A kind of flue gas ash removal and waste heat recycle integrated device |
CN109395882A (en) * | 2018-12-28 | 2019-03-01 | 福建龙净环保股份有限公司 | A kind of dust-collecting and heat exchanging disappears white equipment and system |
CN110102113A (en) * | 2019-04-30 | 2019-08-09 | 上海化工研究院有限公司 | A kind of containment type heat-exchange dedusting integrated apparatus |
CN213101180U (en) * | 2020-06-12 | 2021-05-04 | 江苏世能化工设备有限公司 | High-temperature dust removal and heat exchange integrated equipment |
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2020
- 2020-06-12 CN CN202010537597.9A patent/CN111589230B/en active Active
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
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CN206508767U (en) * | 2017-02-27 | 2017-09-22 | 天津普惠节能换热设备有限公司 | Flue gas disappears white equipment |
CN109357557A (en) * | 2017-09-22 | 2019-02-19 | 萍乡市华星环保工程技术有限公司 | A kind of flue gas ash removal and waste heat recycle integrated device |
CN109395882A (en) * | 2018-12-28 | 2019-03-01 | 福建龙净环保股份有限公司 | A kind of dust-collecting and heat exchanging disappears white equipment and system |
CN110102113A (en) * | 2019-04-30 | 2019-08-09 | 上海化工研究院有限公司 | A kind of containment type heat-exchange dedusting integrated apparatus |
CN213101180U (en) * | 2020-06-12 | 2021-05-04 | 江苏世能化工设备有限公司 | High-temperature dust removal and heat exchange integrated equipment |
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