CN106362538A - Wet flue gas dehumidification and emission reduction device - Google Patents
Wet flue gas dehumidification and emission reduction device Download PDFInfo
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- CN106362538A CN106362538A CN201610879420.0A CN201610879420A CN106362538A CN 106362538 A CN106362538 A CN 106362538A CN 201610879420 A CN201610879420 A CN 201610879420A CN 106362538 A CN106362538 A CN 106362538A
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- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 title claims description 50
- 239000003546 flue gas Substances 0.000 title claims description 50
- 230000009467 reduction Effects 0.000 title claims description 23
- 238000007791 dehumidification Methods 0.000 title description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 89
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims description 15
- 239000000498 cooling water Substances 0.000 claims description 15
- 239000010936 titanium Substances 0.000 claims description 15
- 229910052719 titanium Inorganic materials 0.000 claims description 14
- 229910001220 stainless steel Inorganic materials 0.000 claims description 8
- 239000010935 stainless steel Substances 0.000 claims description 8
- 229910001069 Ti alloy Inorganic materials 0.000 claims description 7
- 239000002360 explosive Substances 0.000 claims description 6
- 239000000463 material Substances 0.000 claims description 5
- 229910000831 Steel Inorganic materials 0.000 claims 2
- 239000010959 steel Substances 0.000 claims 2
- 238000001816 cooling Methods 0.000 claims 1
- 239000007789 gas Substances 0.000 claims 1
- 230000008676 import Effects 0.000 claims 1
- 229920006395 saturated elastomer Polymers 0.000 description 12
- 229910052602 gypsum Inorganic materials 0.000 description 9
- 239000010440 gypsum Substances 0.000 description 9
- 238000006477 desulfuration reaction Methods 0.000 description 7
- 230000023556 desulfurization Effects 0.000 description 7
- 238000005260 corrosion Methods 0.000 description 6
- 230000007797 corrosion Effects 0.000 description 6
- 239000003344 environmental pollutant Substances 0.000 description 6
- 231100000719 pollutant Toxicity 0.000 description 6
- 230000007613 environmental effect Effects 0.000 description 5
- 239000002131 composite material Substances 0.000 description 4
- 239000000428 dust Substances 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 239000007788 liquid Substances 0.000 description 4
- 239000002245 particle Substances 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 150000003839 salts Chemical class 0.000 description 3
- 238000010521 absorption reaction Methods 0.000 description 2
- 229910001039 duplex stainless steel Inorganic materials 0.000 description 2
- 238000003912 environmental pollution Methods 0.000 description 2
- 229920002313 fluoropolymer Polymers 0.000 description 2
- 238000011044 inertial separation Methods 0.000 description 2
- 239000007769 metal material Substances 0.000 description 2
- 239000000779 smoke Substances 0.000 description 2
- AKEJUJNQAAGONA-UHFFFAOYSA-N sulfur trioxide Chemical compound O=S(=O)=O AKEJUJNQAAGONA-UHFFFAOYSA-N 0.000 description 2
- 230000002378 acidificating effect Effects 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000013618 particulate matter Substances 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
Classifications
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- 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
- B01D53/002—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 by condensation
-
- 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
- B01D47/05—Separating dispersed particles from gases, air or vapours by liquid as separating agent by condensation of the separating agent
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2258/00—Sources of waste gases
- B01D2258/02—Other waste gases
- B01D2258/0283—Flue gases
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Treating Waste Gases (AREA)
Abstract
本发明提供了一种湿烟气除湿减排装置,其特征在于,包括壳体,壳体的侧面设有湿烟气进口和湿烟气出口,壳体内设有换热管。本发明具有很好的耐腐蚀性能和传热性能,能够对脱硫塔后的饱和湿烟气进行冷却,将其中的水蒸气冷凝。烟气中的粉尘、石膏、可溶性盐等污染物在水蒸气冷凝过程中会附着在换热管管壁并随冷凝水一起流下,冷凝水及污染物在装置底部进行收集,从而达到节能、环保、节水的目的。
The invention provides a wet flue gas dehumidification and emission reduction device, which is characterized in that it comprises a casing, a wet flue gas inlet and a wet flue gas outlet are arranged on the side of the casing, and a heat exchange tube is arranged inside the casing. The invention has good corrosion resistance and heat transfer performance, and can cool the saturated wet flue gas behind the desulfurization tower and condense the water vapor therein. Dust, gypsum, soluble salt and other pollutants in the flue gas will adhere to the wall of the heat exchange tube during the condensation of water vapor and flow down with the condensed water. The condensed water and pollutants will be collected at the bottom of the device to achieve energy saving and environmental protection , The purpose of water saving.
Description
技术领域technical field
本发明属于电力节能、环保领域,特别涉及一种湿烟气除湿、减排装置。The invention belongs to the fields of electric power energy saving and environmental protection, and in particular relates to a wet flue gas dehumidification and emission reduction device.
背景技术Background technique
目前我国环境污染非常严重,火力发电厂的烟气排放对环境污染有不可推卸的责任。由于从脱硫吸收塔排出的烟气为饱和湿烟气,在经过下游烟道和烟囱时,会遇冷凝结出水并溶解多种酸性物质,对下游烟道和烟囱造成低温腐蚀。另外,在烟囱出口的湿烟气,由于排出烟囱时温度骤降,会迅速在烟囱出口附近凝结出大量液滴,并在烟囱周围沉降,由于这种液滴中含有湿法脱硫的产物石膏,俗称“石膏雨”,这种湿烟气通过烟囱直接排放产生的“石膏雨”会造成周围环境的污染。目前常用的方法是加热湿烟气来解决“石膏雨”问题,这样会消耗大量的热能,我国火力发电厂在环保的同时,还有巨大的节约能源的责任。如果能将饱和湿烟气在排放到大气前进行冷却,将饱和湿烟气中的水蒸气冷凝回收,将大大减少加热湿烟气的热量,起到节能的效果;同时将冷凝水和冷凝水中的粉尘、石膏、可溶性盐等污染物收集起来,能够产生巨大的节能环保效益。At present, my country's environmental pollution is very serious, and the smoke emission of thermal power plants has an inescapable responsibility for environmental pollution. Since the flue gas discharged from the desulfurization absorption tower is saturated wet flue gas, when it passes through the downstream flue and chimney, it will condense to condense water and dissolve various acidic substances, causing low-temperature corrosion to the downstream flue and chimney. In addition, due to the sudden drop in temperature of the wet flue gas at the chimney exit, it will quickly condense a large number of liquid droplets near the chimney exit and settle around the chimney. Since the liquid droplets contain gypsum, the product of wet desulfurization, Commonly known as "gypsum rain", the "gypsum rain" produced by the direct discharge of this wet flue gas through the chimney will cause pollution to the surrounding environment. At present, the commonly used method is to heat the wet flue gas to solve the problem of "gypsum rain", which will consume a lot of heat energy. my country's thermal power plants have a huge responsibility to save energy while protecting the environment. If the saturated wet flue gas can be cooled before being discharged into the atmosphere, and the water vapor in the saturated wet flue gas can be condensed and recovered, the heat of heating the wet flue gas will be greatly reduced, and the effect of energy saving will be achieved; at the same time, the condensed water and condensed water The collection of dust, gypsum, soluble salt and other pollutants can produce huge energy saving and environmental protection benefits.
脱硫吸收塔排出的饱和湿烟气具有很强的腐蚀性,无法使用普通金属材料制造这类除湿、减排装置。因此需要开发一种具有很强耐腐蚀性、传热性能好的湿烟气除湿、减排装置。The saturated wet flue gas discharged from the desulfurization absorption tower is highly corrosive, and ordinary metal materials cannot be used to manufacture such dehumidification and emission reduction devices. Therefore, it is necessary to develop a wet flue gas dehumidification and emission reduction device with strong corrosion resistance and good heat transfer performance.
发明内容Contents of the invention
本发明的目的在于有效提高电厂节能、环保水平,开发一种耐腐蚀性强、传热性能好的湿烟气除湿、减排装置。The purpose of the invention is to effectively improve the energy saving and environmental protection level of the power plant, and develop a wet flue gas dehumidification and emission reduction device with strong corrosion resistance and good heat transfer performance.
为了达到上述目的,本发明提供了一种湿烟气除湿减排装置,其特征在于,包括壳体,壳体的侧面设有湿烟气进口和湿烟气出口,壳体内设有换热管。In order to achieve the above object, the present invention provides a wet flue gas dehumidification and emission reduction device, which is characterized in that it includes a shell, the side of the shell is provided with a wet flue gas inlet and a wet flue gas outlet, and a heat exchange tube is arranged inside the shell .
优选地,所述的换热管的材质为钛或钛合金。Preferably, the heat exchange tube is made of titanium or titanium alloy.
更优选地,所述的壳体采用双相不锈钢材质。More preferably, the housing is made of duplex stainless steel.
优选地,所述的壳体的上侧设有上部封头箱,壳体的下侧设有下部封头箱,换热管的顶端设于上部封头箱中,换热管的底端设于下部封头箱中,换热管连接进水集箱和出水集箱,进水集箱和出水集箱设于上部封头箱中,进水集箱和出水集箱分别连接冷却水进口管和冷却水出口管。Preferably, the upper side of the housing is provided with an upper header box, the lower side of the housing is provided with a lower header box, the top of the heat exchange tube is arranged in the upper header box, and the bottom end of the heat exchange tube is arranged in the upper header box. In the lower head box, the heat exchange tubes are connected to the water inlet header and the water outlet header, and the water inlet header and the water outlet header are arranged in the upper head box, and the water inlet header and the water outlet header are respectively connected to the cooling water inlet pipe and cooling water outlet pipe.
更优选地,所述的进水集箱、出水集箱、冷却水出口管和冷却水进口管的材质为钛或钛合金。More preferably, the material of the water inlet header, water outlet header, cooling water outlet pipe and cooling water inlet pipe is titanium or titanium alloy.
更优选地,所述的壳体内设有至少一个用于收集冷凝水的中间集水管板,换热管穿过中间集水管板,中间集水管板连接分层集水管,分层集水管连接底部冷凝水收集水管,底部冷凝水收集水管位于下部封头箱下侧并与下部封头箱连接。More preferably, the shell is provided with at least one intermediate water collecting tube plate for collecting condensed water, the heat exchange tube passes through the intermediate water collecting tube plate, the intermediate water collecting tube plate is connected to the layered water collecting pipe, and the layered water collecting pipe is connected to the bottom The condensed water collecting pipe, the bottom condensed water collecting pipe is located at the lower side of the lower head box and connected with the lower head box.
更优选地,所述的壳体包括上部端板、下部端板和壳体侧板,壳体侧板的上端连接上部端板,下端连接下部端板,壳体内设有壳体支撑管,壳体支撑管设于上部端板和下部端板之间,壳体支撑管同上部端板、中间集水管板和下部端板进行焊接。More preferably, the housing includes an upper end plate, a lower end plate and a housing side plate, the upper end of the housing side plate is connected to the upper end plate, the lower end is connected to the lower end plate, a housing support tube is arranged inside the housing, and the housing The body support tube is arranged between the upper end plate and the lower end plate, and the shell support tube is welded with the upper end plate, the middle water collecting tube plate and the lower end plate.
更优选地,所述的上部封头箱包括上部封头箱顶板以及设于上部封头箱顶板下侧并与上部封头箱顶板连接的上部封头箱侧板。More preferably, the upper header box includes an upper header box top plate and an upper header box side plate arranged on the lower side of the upper header box top plate and connected with the upper header box top plate.
更优选地,所述的上部封头箱顶板为钛不锈钢爆炸复合板,钛不锈钢爆炸复合板的不锈钢层同上部封头箱侧板进行焊接,钛层同进水集箱和出水集箱进行焊接。More preferably, the top plate of the upper head box is a titanium stainless steel explosive composite plate, the stainless steel layer of the titanium stainless steel explosive composite plate is welded with the side plate of the upper head box, and the titanium layer is welded with the water inlet header and the water outlet header .
更优选地,所述的上部封头箱内设有集箱支撑固定板,进水集箱和出水集箱设于集箱支撑固定板之上并由集箱支撑固定板支撑。More preferably, the upper header box is provided with a header supporting and fixing plate, and the water inlet header and the water outlet header are arranged on the header supporting and fixing plate and supported by the header supporting and fixing plate.
优选地,所述的换热管立式、错列布置。Preferably, the heat exchange tubes are arranged vertically and staggeredly.
与现有技术相比,本发明的有益效果是:Compared with prior art, the beneficial effect of the present invention is:
1、本发明在火电厂脱硫塔的饱和湿烟气排放到大气前,将饱和湿烟气冷却,将其中的水蒸气冷凝并回收,同时减少为了解决“石膏雨”问题而使用的加热热量。1. The present invention cools the saturated wet flue gas, condenses and recovers the water vapor therein, and reduces the heating heat used to solve the problem of "gypsum rain" before the saturated wet flue gas of the desulfurization tower of the thermal power plant is discharged into the atmosphere.
2、本发明能够将冷凝水和冷凝水中的粉尘、石膏、可溶性盐等污染物收集起来,烟气中的粉尘、石膏、可溶性盐等污染物在水蒸气冷凝过程中会附着在换热管管壁并随冷凝水一起流下,冷凝水及污染物在装置底部进行收集,从而达到节能、环保、节水的目的。2. The present invention can collect the condensed water and the dust, gypsum, soluble salt and other pollutants in the condensed water, and the dust, gypsum, soluble salt and other pollutants in the flue gas will adhere to the heat exchange tube during the water vapor condensation process The condensed water and pollutants are collected at the bottom of the device, so as to achieve the purpose of energy saving, environmental protection and water saving.
3、本发明采用钛及钛合金换热管同普通金属材料换热管相比,耐腐蚀性能强,使用寿命长;同氟塑料换热管相比,传热性能更好。3. Compared with ordinary metal heat exchange tubes, titanium and titanium alloy heat exchange tubes used in the present invention have stronger corrosion resistance and longer service life; compared with fluoroplastic heat exchange tubes, they have better heat transfer performance.
4、本发明采用分层集水结构,利用惯性分离原理,冷凝水及污染物回收效率高。4. The present invention adopts a layered water collection structure and utilizes the principle of inertial separation, so that the recovery efficiency of condensed water and pollutants is high.
附图说明Description of drawings
图1为湿烟气除湿减排装置结构示意图。Figure 1 is a schematic structural diagram of a wet flue gas dehumidification and emission reduction device.
图2为湿烟气除湿减排装置侧视图;Fig. 2 is a side view of the wet flue gas dehumidification and emission reduction device;
图3为上部封头箱俯视图;Figure 3 is a top view of the upper header box;
图4为集箱支撑固定板示意图。Fig. 4 is a schematic diagram of the support and fixing plate of the header.
具体实施方式detailed description
下面结合具体实施例,进一步阐述本发明。应理解,这些实施例仅用于说明本发明而不用于限制本发明的范围。此外应理解,在阅读了本发明讲授的内容之后,本领域技术人员可以对本发明作各种改动或修改,这些等价形式同样落于本申请所附权利要求书所限定的范围。Below in conjunction with specific embodiment, further illustrate the present invention. It should be understood that these examples are only used to illustrate the present invention and are not intended to limit the scope of the present invention. In addition, it should be understood that after reading the teachings of the present invention, those skilled in the art can make various changes or modifications to the present invention, and these equivalent forms also fall within the scope defined by the appended claims of the present application.
实施例Example
如图1所示,为湿烟气除湿减排装置结构示意图,所述的湿烟气除湿减排装置包括壳体,壳体的侧面设有湿烟气进口和湿烟气出口,壳体内设有换热管9,换热管9立式、错列布置,换热管9内为冷却水,换热管9外为饱和湿烟气。As shown in Figure 1, it is a schematic structural diagram of a wet flue gas dehumidification and emission reduction device. The wet flue gas dehumidification and emission reduction device includes a housing, and the side of the housing is provided with a wet flue gas inlet and a wet flue gas outlet. There are heat exchange tubes 9 arranged vertically and staggeredly. The inside of the heat exchange tubes 9 is cooling water, and the outside of the heat exchange tubes 9 is saturated wet flue gas.
所述的壳体的上侧设有上部封头箱6,壳体的下侧设有下部封头箱13,换热管9的顶端设于上部封头箱6中,换热管9的底端设于下部封头箱13中,换热管9连接进水集箱1和出水集箱2,如图3所示,进水集箱1和出水集箱2设于上部封头箱6中,进水集箱1和出水集箱2分别连接冷却水进口管4和冷却水出口管3。The upper side of the housing is provided with an upper header box 6, the lower side of the housing is provided with a lower header box 13, the top of the heat exchange tube 9 is arranged in the upper header box 6, and the bottom of the heat exchange tube 9 The end is arranged in the lower header box 13, and the heat exchange tube 9 is connected to the water inlet header 1 and the water outlet header box 2, as shown in Figure 3, the water inlet header 1 and the water outlet header box 2 are arranged in the upper header box 6 , the water inlet header 1 and the water outlet header 2 are connected to the cooling water inlet pipe 4 and the cooling water outlet pipe 3 respectively.
所述壳体内设有至少一个用于收集冷凝水的中间集水管板8,换热管9穿过中间集水管板8,中间集水管板8连接设于壳体一侧的分层集水管11,分层集水管11连接底部冷凝水收集水管14,底部冷凝水收集水管14位于下部封头箱13下侧并与下部封头箱13连接。所述的壳体包括上部端板7、下部端板12和壳体侧板17,壳体侧板17的上端连接上部端板7,下端连接下部端板12,壳体内设有壳体支撑管10,壳体支撑管10设于上部端板7和下部端板12之间,壳体支撑管10同上部端板7、中间集水管板8和下部端板12进行焊接,将壳体部分固定为一个整体。The shell is provided with at least one intermediate water collecting tube plate 8 for collecting condensed water, the heat exchange tube 9 passes through the intermediate water collecting tube plate 8, and the intermediate water collecting tube plate 8 is connected to the layered water collecting tube 11 arranged on one side of the shell , the layered water collection pipe 11 is connected to the bottom condensed water collection pipe 14 , and the bottom condensed water collection pipe 14 is located at the lower side of the lower header box 13 and connected with the lower header box 13 . The housing includes an upper end plate 7, a lower end plate 12 and a housing side plate 17, the upper end of the housing side plate 17 is connected to the upper end plate 7, the lower end is connected to the lower end plate 12, and the housing is provided with a housing support tube 10. The shell support tube 10 is arranged between the upper end plate 7 and the lower end plate 12, and the shell support tube 10 is welded with the upper end plate 7, the middle water collecting tube plate 8 and the lower end plate 12 to fix the shell part as a whole.
所述的上部封头箱6包括上部封头箱顶板5以及设于上部封头箱顶板5下侧并与上部封头箱顶板5连接的上部封头箱侧板。所述的上部封头箱顶板5为钛不锈钢爆炸复合板,钛不锈钢爆炸复合板的不锈钢层同上部封头箱侧板进行焊接,钛层同进水集箱1和出水集箱2进行焊接,具有很好的密封效果,能够防止烟气泄漏。上部封头箱侧板的下端与壳体的上部端板7焊接。如图2所示,所述的上部封头箱6内设有集箱支撑固定板15,进水集箱1和出水集箱2设于集箱支撑固定板15之上并由集箱支撑固定板15支撑。集箱支撑固定板15的结构如图4所示,其上部设有与进水集箱1和出水集箱2匹配的凹槽。The upper header box 6 includes an upper header box top plate 5 and an upper header box side plate arranged on the lower side of the upper header box top plate 5 and connected with the upper header box top plate 5 . The top plate 5 of the upper head box is a titanium stainless steel explosive composite plate, the stainless steel layer of the titanium stainless steel explosive composite plate is welded with the side plate of the upper head box, and the titanium layer is welded with the water inlet header 1 and the water outlet header 2, It has a good sealing effect and can prevent smoke leakage. The lower end of the side plate of the upper header box is welded to the upper end plate 7 of the shell. As shown in Figure 2, the upper header box 6 is provided with a header supporting and fixing plate 15, and the inlet header 1 and the outlet header 2 are arranged on the header supporting and fixing plate 15 and are supported and fixed by the headers Plate 15 supports. The structure of the header support fixing plate 15 is shown in FIG. 4 , and its upper part is provided with grooves matching the water inlet header 1 and the water outlet header 2 .
所述的换热管9、进水集箱1、出水集箱2、冷却水出口管3和冷却水进口管4的材质为钛或钛合金,同普通金属材料相比,耐腐蚀性能强,使用寿命长;同氟塑料相比,传热性能更好。所述的壳体的上部端板7、中间集水管板8、壳体支撑管10、下部端板12、下部封头箱13、集箱支撑固定板15、上部封头箱侧板和壳体侧板17使用双相不锈钢材料,具有很好的耐腐蚀性能,使用寿命长。The material of the heat exchange tube 9, the water inlet header 1, the water outlet header 2, the cooling water outlet pipe 3 and the cooling water inlet pipe 4 is titanium or titanium alloy, which is stronger in corrosion resistance than ordinary metal materials. Long service life; better heat transfer performance than fluoroplastics. The upper end plate 7 of the shell, the middle water collection tube plate 8, the shell support pipe 10, the lower end plate 12, the lower header box 13, the header support fixing plate 15, the upper header box side plate and the shell The side plate 17 is made of duplex stainless steel, which has good corrosion resistance and long service life.
本发明的湿烟气除湿减排装置采用模块化设计,可以实际根据需求,多个装置组合使用。The wet flue gas dehumidification and emission reduction device of the present invention adopts a modular design, and multiple devices can be used in combination according to actual needs.
使用时,火电厂脱硫塔的饱和湿烟气进入该壳体后,饱和湿烟气中水蒸气碰到换热管9的管壁后会被冷凝,烟气中的颗粒物也会同烟气中液体发生凝聚,形成以颗粒物为核心的液滴,液滴相互碰撞,粒径逐渐增大。换热管9采用立式、错列布置,利用惯性分离原理,烟气中的液滴随气流冲击在换热管9上,气流方向发生急剧转变,借助颗粒物本身的惯性力作用,使其与气流分离,被换热管9管壁捕捉,由于重力作用,管壁上的颗粒物会和冷凝水一起沿管壁流入底部冷凝水收集水管14。When in use, after the saturated wet flue gas from the desulfurization tower of the thermal power plant enters the shell, the water vapor in the saturated wet flue gas will be condensed when it hits the tube wall of the heat exchange tube 9, and the particulate matter in the flue gas will also be condensed with the liquid in the flue gas. Agglomeration occurs to form droplets with particles as the core, the droplets collide with each other, and the particle size gradually increases. The heat exchange tubes 9 are arranged vertically and staggered. Using the principle of inertial separation, the liquid droplets in the flue gas impact on the heat exchange tubes 9 with the airflow, and the direction of the airflow changes sharply. With the help of the inertial force of the particles themselves, they are separated from the The air flow is separated and captured by the tube wall of the heat exchange tube 9. Due to the effect of gravity, the particles on the tube wall will flow into the bottom condensed water collection pipe 14 along the tube wall together with the condensed water.
本实施例的湿烟气除湿减排装置的冷却水由冷却水进口管4进入换热管9,将换热管9外部的饱和湿烟气冷却,将其中的水蒸气冷凝,吸收这些的热量,最后将吸收热量后的冷却水由出口管3流出。The cooling water of the wet flue gas dehumidification and emission reduction device of this embodiment enters the heat exchange tube 9 from the cooling water inlet pipe 4, cools the saturated wet flue gas outside the heat exchange tube 9, condenses the water vapor therein, and absorbs the heat , and finally the cooling water after absorbing the heat flows out from the outlet pipe 3.
本实施例的湿烟气除湿减排装置采用分层集水结构,中间集水管板8不仅作为固定板,同时具有分层收集冷凝水的功能,中间集水管板8收集的冷凝水流入分层集水管11中,最后汇入底部冷凝水收集水管14;装置底部的冷凝水经过下部端板12流入下部封头箱13,最后汇入冷凝水收集水管14。The wet flue gas dehumidification and emission reduction device of this embodiment adopts a layered water collection structure. The middle water collection tube plate 8 not only serves as a fixed plate, but also has the function of collecting condensed water in layers. The condensed water collected by the middle water collection tube plate 8 flows into the layered The water collecting pipe 11 finally flows into the condensed water collecting pipe 14 at the bottom;
经测定,本实施方式能够将脱硫塔后饱和湿烟气冷却5~20℃,冷却后的烟气几乎不需要加热就可以有效消除“石膏雨”;能够有效回收饱和湿烟气中的大量水分,减少甚至完全补充电厂脱硫运行补水;能够有效降低电厂排放烟气中的粉尘、三氧化硫等污染物。本实施方式具有很好的节能、环保、节水效果。It has been measured that this embodiment can cool the saturated wet flue gas after the desulfurization tower by 5-20°C, and the cooled flue gas can effectively eliminate "gypsum rain" almost without heating; it can effectively recover a large amount of moisture in the saturated wet flue gas , to reduce or even completely supplement the desulfurization operation of the power plant; it can effectively reduce the dust, sulfur trioxide and other pollutants in the flue gas emitted by the power plant. This embodiment has very good effects of energy saving, environmental protection and water saving.
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