CN204854428U - A MGGH heat exchange system - Google Patents
A MGGH heat exchange system Download PDFInfo
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- CN204854428U CN204854428U CN201520479906.6U CN201520479906U CN204854428U CN 204854428 U CN204854428 U CN 204854428U CN 201520479906 U CN201520479906 U CN 201520479906U CN 204854428 U CN204854428 U CN 204854428U
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Abstract
本实用新型公开一种MGGH换热系统,包括依次设置的升温换热器、脱硫除尘设备和降温换热器,管道连接升温换热器和降温换热器形成封闭循环回路,封闭循环回路上设有媒介补偿罐、循环泵以及媒介加热器,升、降温换热器均包括壳体、汇流箱及板式热交换模组,壳体上、下端设有进烟通道和排烟通道,进烟通道和排烟通道均由法兰和导向筒构成;板式热交换模组包括数个换热板,换热板两侧设有烟道支撑凸起和媒介道支撑凸起,相邻换热板的媒介道支撑凸起之间形成传热媒介折程流道,其烟道支撑凸起之间形成排烟一次流过通道。该换热系统低耗能烟气处理,结构简单,投入和运行成本低,运行可靠,换热效率高,易于清理和维护,其换热器强度高,寿命长。
The utility model discloses an MGGH heat exchange system, which comprises a heating heat exchanger, desulfurization and dust removal equipment, and a cooling heat exchanger arranged in sequence. Pipelines are connected to the heating heat exchanger and the cooling heat exchanger to form a closed loop. There are medium compensation tanks, circulation pumps and medium heaters. Both the heating and cooling heat exchangers include shells, combiner boxes and plate heat exchange modules. The upper and lower ends of the shell are provided with smoke inlet channels and smoke exhaust channels. Both the exhaust channel and the smoke exhaust channel are composed of flanges and guide cylinders; the plate heat exchange module includes several heat exchange plates, and there are flue support protrusions and medium channel support protrusions on both sides of the heat exchange plates. The heat transfer medium folding flow channel is formed between the medium channel support protrusions, and the exhaust smoke primary flow channel is formed between the flue support protrusions. The heat exchange system has low energy consumption for flue gas treatment, simple structure, low input and operating costs, reliable operation, high heat exchange efficiency, easy cleaning and maintenance, and the heat exchanger has high strength and long service life.
Description
技术领域technical field
本实用新型涉及电力行业排烟处理设备技术领域,尤其涉及一种MGGH换热系统。The utility model relates to the technical field of smoke exhaust treatment equipment in the electric power industry, in particular to an MGGH heat exchange system.
背景技术Background technique
为了适应GB13553-2011《火电厂大气污染物排放标准》的规定,燃煤发电企业在排烟前需要进行相应的脱硫处理,目前,国内外的烟气脱硫处理技术主要采取的换热器有回转式烟气换热器(RGGH)和中间热媒体烟气换热器(MGGH)2种,其中,MGGH以其节能、运行经济性和可靠性的优势,具有较大的市场前景。In order to meet the requirements of GB13553-2011 "Emission Standards of Air Pollutants for Thermal Power Plants", coal-fired power generation enterprises need to carry out corresponding desulfurization treatment before exhausting smoke. There are two types of flue gas heat exchangers (RGGH) and intermediate heat medium flue gas heat exchangers (MGGH). Among them, MGGH has great market prospects due to its advantages in energy saving, operating economy and reliability.
MGGH是利用原烟的高温加热媒介,降低烟气温度,减少烟气流量,提高烟气处理性能,再使用媒介加热低温净烟气,使其排放温度升高,易于消散;现有技术的MGGH大多以管式、翅片式为主,烟气与冷却水管道表面接触实现换热,接触面积小,换热行程过长,排烟压降大,且换热管束的设计和布置无法充分利用换热箱体内的有效换热面积,同时,由于烟气与换热管是垂直接触,排烟阻力大,冷却水管道的背风面和滞留区易积灰,不易进行清理,导致其换热性能降低。MGGH uses the high-temperature heating medium of the original smoke to reduce the temperature of the flue gas, reduce the flow rate of the flue gas, improve the performance of the flue gas treatment, and then use the medium to heat the low-temperature clean flue gas to increase the discharge temperature and make it easy to dissipate; the existing MGGH Most of them are tube type and fin type. The flue gas is in contact with the surface of the cooling water pipe to exchange heat. The contact area is small, the heat exchange stroke is too long, the pressure drop of the exhaust gas is large, and the design and arrangement of the heat exchange tube bundle cannot be fully utilized. At the same time, due to the vertical contact between the flue gas and the heat exchange tube, the smoke exhaust resistance is large, and the leeward side of the cooling water pipe and the stagnation area are easy to accumulate dust, which is difficult to clean, resulting in poor heat transfer performance. reduce.
实用新型内容Utility model content
本实用新型所要解决的技术问题是,克服现有技术中存在的不足,提供一种结构紧凑、排烟阻力小、清理方便及换热效率高的MGGH换热系统。The technical problem to be solved by the utility model is to overcome the deficiencies in the prior art and provide an MGGH heat exchange system with compact structure, low smoke exhaust resistance, convenient cleaning and high heat exchange efficiency.
本实用新型的一种MGGH换热系统是通过以下技术方案予以实现,其包括依次设置于烟气排放管上的升温换热器、脱硫除尘设备和降温换热器,管道连接升温换热器的媒介进口和降温换热器的媒介出口、以及管道连接升温换热器的媒介出口和降温换热器的媒介进口,形成传热媒介的封闭循环回路,封闭循环回路上设有媒介补偿罐、循环泵以及媒介加热器;A MGGH heat exchange system of the utility model is realized through the following technical scheme, which includes a heating heat exchanger, a desulfurization and dust removal equipment, and a cooling heat exchanger arranged sequentially on the flue gas discharge pipe, and the piping connecting the heating heat exchanger The medium inlet and the medium outlet of the cooling heat exchanger, as well as the pipeline connecting the medium outlet of the heating heat exchanger and the medium inlet of the cooling heat exchanger, form a closed circulation loop of the heat transfer medium, and the closed circulation loop is equipped with a medium compensation tank and circulation pumps and medium heaters;
其中,升温换热器和降温换热器均包括:Among them, both the heating heat exchanger and the cooling heat exchanger include:
壳体,其上、下端设有进烟通道和排烟通道,进烟通道由进口法兰和进烟导向筒构成,排烟通道由出口法兰和排烟导向筒构成,进烟导向筒和排烟导向筒的内壁设有导烟斜度;The shell has a smoke inlet channel and a smoke exhaust channel at its upper and lower ends. The smoke inlet channel is composed of an inlet flange and a smoke guide tube. The smoke exhaust channel is composed of an outlet flange and a smoke guide tube. The smoke guide tube and The inner wall of the smoke guide cylinder is provided with a smoke guide slope;
与壳体连通的汇流箱,媒介进口和媒介出口分别设于其两端;A combiner box connected to the shell, with medium inlet and medium outlet respectively located at its two ends;
以及位于壳体内部的板式热交换模组,其一端与汇流箱连接,板式热交换模组包括数个平行于排烟方向均匀排列的换热板,换热板的两侧分别设有烟道支撑凸起和媒介道支撑凸起,相邻换热板的媒介道支撑凸起相抵靠或媒介道支撑凸起与换热板的板平面相抵靠并连接,形成连通媒介进口和媒介出口的密封的传热媒介折程流道,传热媒介折程流道包括数个具有独立介质进出口的周向通道及设置在周向通道内使传热媒介沿周向通道往复折程流动的分程隔板,相邻换热板的烟道支撑凸起之间形成排烟一次流过通道。And the plate heat exchange module located inside the shell, one end of which is connected to the combiner box, the plate heat exchange module includes several heat exchange plates evenly arranged parallel to the smoke exhaust direction, and the two sides of the heat exchange plates are respectively equipped with flue channels Support protrusions and medium channel support protrusions, the medium channel support protrusions of adjacent heat exchange plates abut or the medium channel support protrusions abut and connect with the plate plane of the heat exchange plate, forming a seal connecting the medium inlet and the medium outlet The heat transfer medium folded flow channel, the heat transfer medium folded flow channel includes several circumferential channels with independent medium inlets and outlets and the split partitions arranged in the circumferential channels to allow the heat transfer medium to reciprocate along the circumferential channel. A smoke exhaust primary flow channel is formed between the flue support protrusions adjacent to the heat exchange plate.
进一步地,升温换热器和降温换热器的排烟通道内均设有温度变送器,媒介加热器还连接有加热电磁阀,封闭循环回路还设有连通降温换热器的媒介进口和媒介出口的一旁通支路,旁通支路上设有旁通电磁阀,升温换热器上的温度变送器与加热电磁阀电性连接,降温换热器上的温度变送器与旁通电磁阀电性连接。Further, temperature transmitters are installed in the smoke exhaust passages of the heating heat exchanger and the cooling heat exchanger, the medium heater is also connected with a heating solenoid valve, and the closed circulation loop is also provided with a medium inlet and a medium connected to the cooling heat exchanger. The bypass branch of the medium outlet is equipped with a bypass solenoid valve, the temperature transmitter on the heating heat exchanger is electrically connected to the heating solenoid valve, and the temperature transmitter on the cooling heat exchanger is connected to the bypass The solenoid valve is electrically connected.
进一步地,分程隔板至少为一个,传热媒介折程流道的折程数为偶数,汇流箱位于壳体一侧,且其内部设有隔板,隔板将汇流箱内隔绝成与媒介进口连通的入口分流区和与媒介出口连通的出口汇流区。Further, there is at least one dividing plate, the number of folded paths of the heat transfer medium is an even number, the combiner box is located on one side of the shell, and a divider is arranged inside it, and the divider isolates the inside of the combiner box from the medium inlet. A connected inlet diversion area and an outlet confluence area connected with the medium outlet.
进一步地,分程隔板至少为一个,传热媒介折程流道的折程数为奇数,汇流箱由位于壳体两侧的两个分壳体组成。Furthermore, there is at least one dividing plate, the number of folding paths of the heat transfer medium is an odd number, and the combiner box is composed of two sub-housings located on both sides of the casing.
进一步地,媒介道支撑凸起和烟道支撑凸起为冲压波纹凸起、焊筋或板筋。Further, the media channel support protrusion and the flue support protrusion are stamped corrugated protrusions, welding ribs or plate ribs.
进一步地,板式热交换模组的另一端与壳体之间设有弹性体,弹性体为弹簧或橡胶。Further, an elastic body is provided between the other end of the plate heat exchange module and the casing, and the elastic body is a spring or rubber.
进一步地,板式热交换模组的另一端与壳体之间设有柔性板,柔性板包括一体成型形成卡靠于板式热交换模组端角上的L形靠板、与壳体侧面贴紧定位的固定板以及连接L形靠板和固定板的弯折曲板。Further, a flexible plate is provided between the other end of the plate heat exchange module and the housing, and the flexible plate includes an L-shaped backing plate that is integrally formed and clamped against the end corner of the plate heat exchange module, and is in close contact with the side of the housing. The positioning fixing plate and the bent bending plate connecting the L-shaped backing plate and the fixing plate.
本实用新型的有益效果是:The beneficial effects of the utility model are:
1.在封闭循环回路内的传热媒介的循环换热下,利用原烟的热量加热净烟气,可实现低耗能烟气处理,烟气处理效果显著,同时,结构简单,投入和运行成本低,运行可靠;1. Under the cyclical heat exchange of the heat transfer medium in the closed loop, the heat of the original smoke is used to heat the clean flue gas, which can realize low energy consumption flue gas treatment, and the flue gas treatment effect is remarkable. At the same time, the structure is simple, and it is easy to put into operation. Low cost and reliable operation;
2.排烟经过降温换热器和升温换热器时,在进烟导向筒的导烟斜度的导向作用下,排烟在板式热交换模组内流场分布均匀,壁面出现冷热不均衡现象,提高换热效率;2. When the exhaust smoke passes through the cooling heat exchanger and the heating heat exchanger, under the guidance of the smoke guide slope of the smoke inlet guide cylinder, the flow field of the exhaust smoke is evenly distributed in the plate heat exchange module, and the wall surface appears cold and hot. Equilibrium phenomenon, improve heat transfer efficiency;
3.排烟在热交换模组内和传热媒介进行多程交错逆流换热,相互接触面积大,因此,换热行程可较大程度缩短,换热器的结构更加紧凑,更易于安装在排烟管道或烟囱上,且升温换热器和降温换热器的距离不受限制;3. The exhaust smoke performs multi-pass cross-current heat exchange with the heat transfer medium in the heat exchange module, and the mutual contact area is large. Therefore, the heat exchange stroke can be shortened to a large extent, and the structure of the heat exchanger is more compact, which is easier to install in On the exhaust pipe or chimney, and the distance between the heating heat exchanger and the cooling heat exchanger is not limited;
4.换热板两侧分别设有支撑凸起,不仅可形成传热媒介和排烟通道,同时也可提高换热板承受两侧压力差的能力,防止换热板变形导致的密封失效的问题,且板式热交换模组本身为一个可独立实现密封热交换的模块,不需与壳体侧面形成密封,因此,长期运行可靠,且易于进行模块化组装。4. There are supporting protrusions on both sides of the heat exchange plate, which can not only form the heat transfer medium and smoke exhaust channel, but also improve the ability of the heat exchange plate to withstand the pressure difference on both sides, and prevent the seal failure caused by the deformation of the heat exchange plate problem, and the plate heat exchange module itself is a module that can independently realize sealed heat exchange, and does not need to be sealed with the side of the shell. Therefore, it is reliable for long-term operation and easy to carry out modular assembly.
附图说明Description of drawings
图1是本实用新型的结构示意图;Fig. 1 is the structural representation of the utility model;
图2是图1中升温换热器的结构示意图;Fig. 2 is a schematic structural view of the heating heat exchanger in Fig. 1;
图3是图2中柔性板的结构示意图;Fig. 3 is a schematic structural diagram of the flexible board in Fig. 2;
图4是本实用新型的换热板对的逆向流动模式原理图;Fig. 4 is a schematic diagram of the reverse flow mode of the heat exchange plate pair of the present invention;
图5是本实用新型的换热板对的顺向流动模式原理图。Fig. 5 is a schematic diagram of the forward flow mode of the heat exchange plate pair of the present invention.
图中:1.升温换热器,10.壳体,11.柔性板,111.固定板,112.弯折曲板,113.L形靠板,12.板式热交换模组,121.换热板对,1211.分程隔板,1212.周向通道,1213.烟道支撑凸起,1214.媒介道支撑凸起,13.排烟通道,131.出口法兰,132.排烟导向筒,14.进烟通道,141.进口法兰,142.进烟导向筒,15.汇流箱,16.媒介出口,17.媒介进口,18.汇流箱盖板,19.隔板,2.降温换热器,3.旁通电磁阀,4.媒介补偿罐,5.循环泵,6.媒介加热器,7.加热电磁阀,8.脱硫除尘设备;In the figure: 1. Heating heat exchanger, 10. Shell, 11. Flexible plate, 111. Fixed plate, 112. Bending plate, 113. L-shaped backing plate, 12. Plate heat exchange module, 121. Exchanger Hot plate pair, 1211. Partition partition, 1212. Circumferential channel, 1213. Flue support protrusion, 1214. Medium channel support protrusion, 13. Smoke exhaust channel, 131. Outlet flange, 132. Smoke exhaust guide Tube, 14. Smoke inlet channel, 141. Inlet flange, 142. Smoke inlet guide tube, 15. Combiner box, 16. Medium outlet, 17. Medium inlet, 18. Combiner box cover plate, 19. Partition plate, 2. Cooling heat exchanger, 3. Bypass solenoid valve, 4. Medium compensation tank, 5. Circulation pump, 6. Medium heater, 7. Heating solenoid valve, 8. Desulfurization and dust removal equipment;
A:排烟,B:传热媒介(可为水、冷却液或油等换热系数高的液体)。A: smoke exhaust, B: heat transfer medium (it can be liquid with high heat transfer coefficient such as water, coolant or oil).
具体实施方式Detailed ways
为了使本技术领域的技术人员更好地理解本实用新型的技术方案,下面结合附图和最佳实施例对本实用新型作进一步的详细说明。In order to enable those skilled in the art to better understand the technical solution of the utility model, the utility model will be further described in detail below in conjunction with the accompanying drawings and preferred embodiments.
如图1-5所示,本实用新型的一种板式低温省煤器,其包括依次设置于烟气排放管上的升温换热器1、脱硫除尘设备8和降温换热器2,管道连接升温换热器1的媒介进口17和降温换热器2的媒介出口16、以及管道连接升温换热器1的媒介出口16和降温换热器2的媒介进口17,形成传热媒介的封闭循环回路,封闭循环回路上设有媒介补偿罐4、循环泵5以及媒介加热器6,媒介补偿罐4可补充封闭循环回路中的传热媒介,稳定回路内的媒介压力,循环泵5提供传热媒介循环动力,媒介加热器6设于升温换热器1的媒介进口17后端,对进入升温换热器1的传热媒介进行加热,保证排烟温度;As shown in Figure 1-5, a plate-type low-temperature economizer of the present invention includes a heating heat exchanger 1, a desulfurization and dust removal equipment 8, and a cooling heat exchanger 2 arranged on the flue gas discharge pipe in sequence, and the pipes are connected The medium inlet 17 of the heating heat exchanger 1 and the medium outlet 16 of the cooling heat exchanger 2, and the pipeline connecting the medium outlet 16 of the heating heat exchanger 1 and the medium inlet 17 of the cooling heat exchanger 2 form a closed cycle of heat transfer medium loop, the closed circulation loop is provided with a medium compensation tank 4, a circulation pump 5 and a medium heater 6, the medium compensation tank 4 can supplement the heat transfer medium in the closed circulation loop, stabilize the medium pressure in the loop, and the circulation pump 5 provides heat transfer Medium circulation power, the medium heater 6 is set at the rear end of the medium inlet 17 of the heating heat exchanger 1, and heats the heat transfer medium entering the heating heat exchanger 1 to ensure the exhaust gas temperature;
其中,升温换热器1和降温换热器2的结构一致,其均包括:Wherein, the structure of the heating heat exchanger 1 and the cooling heat exchanger 2 is consistent, and they both include:
壳体10,其上、下端设有进烟通道14和排烟通道13,进烟通道14由进口法兰141和进烟导向筒142构成,排烟通道13由出口法兰131和排烟导向筒132构成,进烟导向筒142和排烟导向筒132的内壁设有导烟斜度,即进烟导向筒142和排烟导向筒132具有锥形内腔,或进烟导向筒142和排烟导向筒132的内腔四壁均为与排烟方向形成大于0°夹角的斜壁,可根据需要和壳体10的形状选择;同时壳体10的上下端端口上还设有拉杆或拉筋(图中未示),用于固定和限位板式热交换模组12;The casing 10 has a smoke inlet channel 14 and a smoke exhaust channel 13 at its upper and lower ends. The smoke inlet channel 14 is composed of an inlet flange 141 and a smoke inlet guide tube 142. The smoke exhaust channel 13 is formed by an outlet flange 131 and a smoke exhaust guide. The inner wall of the smoke inlet guide cylinder 142 and the smoke exhaust guide cylinder 132 is provided with a smoke guide slope, that is, the smoke inlet guide cylinder 142 and the smoke exhaust guide cylinder 132 have a tapered inner cavity, or the smoke inlet guide cylinder 142 and the exhaust gas guide cylinder 142 have a conical inner cavity. The four walls of the inner cavity of the smoke guiding cylinder 132 are inclined walls forming an angle greater than 0° with the smoke exhaust direction, which can be selected according to the needs and the shape of the housing 10; meanwhile, the upper and lower ports of the housing 10 are also provided with pull rods or Tension bars (not shown in the figure) are used to fix and limit the plate heat exchange module 12;
与壳体10连通的汇流箱15,媒介进口17和媒介出口16分别设于其两端;A combiner box 15 communicating with the housing 10, a medium inlet 17 and a medium outlet 16 are respectively arranged at its two ends;
以及位于壳体10内部的板式热交换模组12,其一端与汇流箱15连接,板式热交换模组12包括数个平行于排烟方向均匀排列的换热板,换热板的两侧分别设有烟道支撑凸起1213和媒介道支撑凸起1214,相邻换热板的媒介道支撑凸起1214相抵靠,或者一换热板上的媒介道支撑凸起1214与另一换热板上板平面相抵靠,并连接形成连通媒介进口17和媒介出口16的密封的传热媒介折程流道,传热媒介折程流道包括数个具有独立介质进出口的周向通道1212及设置在周向通道1212内使传热媒介沿周向通道1212往复折程流动的分程隔板1211,相邻换热板的烟道支撑凸起1213之间形成排烟一次流过通道,相邻换热板的烟道支撑凸起1213之间形成排烟一次流过通道,烟道支撑凸起1213可相对抵靠接触连接,也可烟道支撑凸起1213与换热板的板平面相抵靠接触连接,防止热胀变形,排烟与传热媒介流向相互垂直,并在流过板式热交换模组12内呈交错逆流进行换热;And the plate heat exchange module 12 located inside the housing 10, one end of which is connected to the combiner box 15, the plate heat exchange module 12 includes several heat exchange plates evenly arranged parallel to the smoke exhaust direction, the two sides of the heat exchange plates are respectively There are flue support protrusions 1213 and medium channel support protrusions 1214, the medium channel support protrusions 1214 of adjacent heat exchange plates abut against each other, or the medium channel support protrusions 1214 on one heat exchange plate and the other heat exchange plate The planes of the upper plate are abutted against each other and connected to form a sealed heat transfer medium folded flow channel connecting the medium inlet 17 and the medium outlet 16. The heat transfer medium folded flow channel includes several circumferential channels 1212 with independent medium inlets and outlets and arranged in the circumferential channel. In 1212, the partition plate 1211 that makes the heat transfer medium flow back and forth along the circumferential channel 1212, and the smoke exhaust primary flow channel is formed between the flue support protrusions 1213 of adjacent heat exchange plates, and the adjacent heat exchange plates The flue support protrusions 1213 form a channel for the primary flow of smoke. The flue support protrusions 1213 can be connected against each other, or the flue support protrusions 1213 can be connected with the plate plane of the heat exchange plate to prevent Thermal expansion and deformation, the flow direction of the exhaust gas and the heat transfer medium are perpendicular to each other, and they flow through the plate heat exchange module 12 in a staggered countercurrent for heat exchange;
如图4所示,分程隔板1211将周向通道1212分为进出口通道及折程通道,进出口通道宽度与折程通道宽度可相同,也可以不同;各程通道宽度可相同,也可以不同;折程数以及每程通道宽度可根据需要进行调整;As shown in Figure 4, the dividing partition 1211 divides the circumferential channel 1212 into an inlet and outlet channel and a folding channel. The width of the inlet and outlet channels and the width of the folding channel can be the same or different; It can be different; the number of folds and the width of each channel can be adjusted according to needs;
两个换热板叠合后在形成周向通道1212的两侧媒介道支撑凸起1214和作为分程隔板1211的媒介道支撑凸起1214进行电阻焊或者粘结连接,周向通道1212两侧连续焊形成密封的媒介折程流道,分程隔板1211可以压紧接触连接、连续焊、间断焊或多点焊,形成内部具有密封的多程折程流道的换热板对121;换热板对121内的传热媒介压力大于换热板对121之间的排烟压力;换热板对121之间的烟道支撑凸起1213相互抵靠或者烟道支撑凸起1213与板平面抵靠,形成与排烟流向平行的排烟一次流过通道;媒介道支撑凸起1214和烟道支撑凸起1213可为冲压波纹凸起、焊筋或板筋,媒介道支撑凸起1214和烟道支撑凸起1213为对称或非对称,即换热板两侧的凸起深度可相等,也可不等;凸起可为各种波纹形式,媒介道支撑凸起1214和烟道支撑凸起12133不仅可形成传热媒介和排烟的通道,同时可相互支撑,提高换热板承受两侧压力差的能力,防止换热板变形导致的密封失效的问题,且板式热交换模组12本身为一个可独立实现密封热交换的模块,不需与壳体10侧面形成密封,因此,长期运行可靠,易于进行模块化组装和大规模生产;After the two heat exchange plates are superimposed, resistance welding or adhesive connection is carried out on the media channel support protrusions 1214 on both sides of the circumferential channel 1212 and the media channel support protrusions 1214 as the partition plate 1211. The two sides of the circumferential channel 1212 Side continuous welding forms a sealed medium-folding flow channel, and the split-pass separator 1211 can be pressed into contact connection, continuous welding, intermittent welding or multi-spot welding to form a heat exchange plate pair 121 with a sealed multi-pass folding flow channel inside; The pressure of the heat transfer medium in the pair 121 is greater than the exhaust pressure between the heat exchange plate pairs 121; the flue support protrusions 1213 between the heat exchange plate pairs 121 abut against each other or the flue support protrusions 1213 abut against the plate plane , to form a smoke exhaust primary flow channel parallel to the exhaust gas flow direction; the medium channel support protrusion 1214 and the flue support protrusion 1213 can be stamped corrugated protrusions, welding ribs or plate ribs, the medium channel support protrusion 1214 and the flue channel The support protrusions 1213 are symmetrical or asymmetrical, that is, the depths of the protrusions on both sides of the heat exchange plate can be equal or unequal; It can form channels for heat transfer medium and smoke exhaust, and at the same time support each other, improve the ability of the heat exchange plate to withstand the pressure difference on both sides, and prevent the problem of seal failure caused by the deformation of the heat exchange plate, and the plate heat exchange module 12 itself is a The module that can independently realize sealed heat exchange does not need to be sealed with the side of the housing 10, so it is reliable in long-term operation and easy to carry out modular assembly and mass production;
换热板可采用碳钢、不锈钢、钛及其合金、镍及其镍基合金或其它钢种或有色金属,其耐温范围在-196~1200℃。The heat exchange plate can be made of carbon steel, stainless steel, titanium and its alloys, nickel and its nickel-based alloys, or other steel types or non-ferrous metals, and its temperature resistance range is -196 to 1200 °C.
因此,该实用新型的MGGH与现有技术相比,原烟首先进入降温换热器2与传热介质发生热交换,实现降温,降温后的原烟温度降低,同时流量减小,能够充分地在位于降温换热器2前端的脱硫除尘设备8中进行充分地脱硫和除尘,有效降低排烟的含硫量;传热媒介在降温换热器2中吸热后,由循环泵5驱动在封闭循环回路内流动,于升温换热器1中放热,对处理后的净烟气加热,提高净烟气的排放温度,防止净烟气被凝结的水汽吸附腐蚀烟道或烟囱,使净烟气更易、更快速升至高空消散;因此,该换热系统可实现低耗能烟气处理,烟气处理效果显著,同时,结构简单,投入和运行成本低,使用可靠;Therefore, compared with the prior art, the MGGH of this utility model first enters the cooling heat exchanger 2 to exchange heat with the heat transfer medium to realize cooling. Sufficient desulfurization and dust removal are carried out in the desulfurization and dust removal equipment 8 located at the front end of the cooling heat exchanger 2 to effectively reduce the sulfur content of the exhaust gas; It flows in the closed circulation loop, releases heat in the heating heat exchanger 1, heats the treated clean flue gas, increases the discharge temperature of the clean flue gas, and prevents the clean flue gas from being adsorbed by condensed water vapor to corrode the flue or chimney, making the clean flue gas The flue gas rises to the high altitude more easily and quickly to dissipate; therefore, the heat exchange system can realize low energy consumption flue gas treatment, and the flue gas treatment effect is remarkable. At the same time, the structure is simple, the input and operation costs are low, and the use is reliable;
如图2所示,排烟经过降温换热器2和升温换热器1时,在其锥形进烟导向筒142的导向作用下,排烟在板式热交换模组12内流场分布均匀,壁面出现冷热不均衡现象,提高换热效率;排烟在热交换模组内和传热媒介进行多程交错逆流换热,相互接触面积大,因此,换热行程可较大程度缩短,换热器的结构更加紧凑,更易于安装在排烟管道或烟囱上;换热板平行于排烟流向设置,排烟阻力小,同时,换热器内部易于进行清理和维护;换热板两侧分别设有支撑凸起,不仅可形成传热媒介和排烟通道13,同时也可提高换热板承受两侧压力差的能力。As shown in Figure 2, when the exhaust smoke passes through the cooling heat exchanger 2 and the heating heat exchanger 1, under the guidance of the conical smoke inlet guide cylinder 142, the exhaust smoke is evenly distributed in the flow field in the plate heat exchange module 12 , there is an imbalance of cold and heat on the wall surface, which improves the heat exchange efficiency; the exhaust smoke performs multi-pass cross-current heat exchange with the heat transfer medium in the heat exchange module, and the mutual contact area is large. Therefore, the heat exchange stroke can be shortened to a large extent. The structure of the heat exchanger is more compact, and it is easier to install on the exhaust pipe or chimney; the heat exchange plate is arranged parallel to the flow direction of the exhaust gas, and the resistance of the exhaust smoke is small. At the same time, the inside of the heat exchanger is easy to clean and maintain; the two heat exchange plates The sides are respectively provided with supporting protrusions, which can not only form the heat transfer medium and the smoke exhaust channel 13, but also improve the ability of the heat exchange plate to withstand the pressure difference on both sides.
如图1所示,升温换热器1和降温换热器2的排烟通道13内均设有温度变送器,媒介加热器6还连接有加热电磁阀7,封闭循环回路还设有连通降温换热器2的媒介进口17和媒介出口16的一旁通支路,旁通支路上设有旁通电磁阀3,升温换热器1上的温度变送器与加热电磁阀7电性连接,降温换热器2上的温度变送器与旁通电磁阀3电性连接,加热电磁阀7和旁通电磁阀3分别根据排烟通道13内的排烟温度启动媒介加热器6或旁通支路,在满足烟气处理要求的基础上,进一步节省不必要的能源消耗。As shown in Figure 1, temperature transmitters are installed in the smoke exhaust passages 13 of the heating heat exchanger 1 and the cooling heat exchanger 2, the medium heater 6 is also connected with a heating solenoid valve 7, and the closed circulation loop is also provided with a communication A bypass branch of the medium inlet 17 and the medium outlet 16 of the cooling heat exchanger 2, the bypass solenoid valve 3 is provided on the bypass branch, and the temperature transmitter on the heating heat exchanger 1 is electrically connected with the heating solenoid valve 7 , the temperature transmitter on the cooling heat exchanger 2 is electrically connected to the bypass solenoid valve 3, and the heating solenoid valve 7 and the bypass solenoid valve 3 respectively activate the medium heater 6 or the bypass solenoid valve according to the exhaust gas temperature in the exhaust gas passage 13. On the basis of meeting the flue gas treatment requirements, unnecessary energy consumption can be further saved.
本例中分程隔板1211至少为一个,传热媒介折程流道的折程数为偶数,传热媒介进出口在同一边,汇流箱15位于壳体10一侧,结构紧凑,在汇流箱15的一侧还可设有可拆卸的汇流箱盖板18,便于清理和检修板式热交换模组12内的流道,汇流箱15内部设有隔板19,隔板19将汇流箱15内隔绝成与媒介进口17连通的入口分流区和与媒介出口16连通的出口汇流区;当分程隔板1211为偶数时,介质便在周向通道1212内完成奇数次折程,介质进出口在不同边,进出流动方向相同,汇流箱15由位于壳体10两侧的两个分壳体10组成。In this example, there is at least one dividing plate 1211, the number of folded paths of the heat transfer medium is an even number, the inlet and outlet of the heat transfer medium are on the same side, the combiner box 15 is located on the side of the shell 10, and the structure is compact. One side of the side can also be provided with detachable combiner box cover plate 18, is convenient to clean up and the flow path in the plate heat exchange module 12 of maintenance, combiner box 15 interior is provided with divider 19, divider 19 isolates the inside combiner box 15 It forms an inlet diverging area connected with the medium inlet 17 and an outlet converging area connected with the medium outlet 16; when the division partition 1211 is an even number, the medium completes an odd number of folds in the circumferential channel 1212, and the medium inlet and outlet are on different sides. , the direction of flow in and out is the same, and the combiner box 15 is composed of two sub-shells 10 located on both sides of the shell 10 .
如图4所示,当传热媒介为逆向流动时,换热板组叠后,竖直方向作为排烟的进出口通道,即排烟由进烟导向筒142导向从下方进入,一次流过板片,从上方流出,传热媒介横向往复折程流动,从侧边下方第一程通道口进入,通过多次折程后,从侧边上方第一程通道口流出,即冷源进出为逆向流动;当然两者流动方向也可以倒置,以前者所述的流动方向为最优选。As shown in Figure 4, when the heat transfer medium flows in the reverse direction, after the heat exchange plates are stacked, the vertical direction is used as the inlet and outlet channels for the smoke exhaust, that is, the exhaust smoke is guided by the smoke inlet guide tube 142 and enters from below, and flows through once. The plate flows out from the top, and the heat transfer medium flows in the horizontal reciprocating folding process, enters from the first channel opening below the side, and flows out from the first channel opening above the side after passing through multiple folding processes, that is, the cold source enters and exits as Reverse flow; Of course, the two flow directions can also be reversed, and the flow direction described above is the most preferred.
如图5所示,当传热媒介为顺向流动时,换热板组叠后,竖直方向作为排烟的进出口通道,即排烟由进烟导向筒142导向从上边进入,一次流过板片,从下边流出,传热媒介横向往复折程流动,从侧边一端下方第一程通道口进入,通过多次折程后,从侧边另一端上方第一程通道口流出,即传热媒介进出为顺向流动;当然两者流动方向也可以倒置。As shown in Figure 5, when the heat transfer medium flows in the forward direction, after the heat exchange plates are stacked, the vertical direction is used as the inlet and outlet channels for the smoke exhaust, that is, the exhaust smoke is guided by the smoke inlet guide tube 142 and enters from the top, and the primary flow Pass through the plate and flow out from the bottom, the heat transfer medium flows in the horizontal reciprocating folding process, enters from the first channel opening below one end of the side, and flows out from the first channel opening above the other end of the side after passing through multiple folding processes, that is The flow in and out of the heat transfer medium is forward flow; of course, the flow direction of the two can also be reversed.
本例中,板式热交换模组12的另一端与壳体10为柔性连接,受热时,板式热交换模组12内的各传热板发生膨胀变形,相互挤压易发生密封失效和介质泄漏混杂,换热器作用失效,板式热交换模组12的另一端与壳体10之间预设柔性变形空间,吸收热胀变形,提高凝汽器寿命,柔性连接可通过板式热交换模组12的另一端与壳体10之间设有弹性体实现,弹性体为弹簧或橡胶,也可通过板式热交换模组12的另一端与壳体10之间设置柔性板11实现,如图3所示,柔性板11包括折弯形成卡靠于板式热交换模组12端角上的L形靠板113、与壳体10侧面贴紧定位的固定板111以及连接L形靠板113和固定板111的弯折曲板112。In this example, the other end of the plate heat exchange module 12 is flexibly connected to the shell 10. When heated, the heat transfer plates in the plate heat exchange module 12 expand and deform, and mutual extrusion is prone to seal failure and medium leakage. Mixed, the function of the heat exchanger is invalid, and the flexible deformation space is preset between the other end of the plate heat exchange module 12 and the shell 10 to absorb thermal expansion deformation and improve the life of the condenser. The flexible connection can pass through the plate heat exchange module 12 The other end of the plate heat exchange module 12 is provided with an elastic body between the housing 10, and the elastic body is a spring or rubber. It can also be realized by installing a flexible plate 11 between the other end of the plate heat exchange module 12 and the housing 10, as shown in Figure 3 As shown, the flexible plate 11 includes an L-shaped backing plate 113 that is bent to form a card against the end corner of the plate heat exchange module 12, a fixing plate 111 that is positioned close to the side of the housing 10, and connects the L-shaped backing plate 113 and the fixing plate. 111 of the bent plate 112 .
以上所述仅是本实用新型的优选实施方式,应当指出,对于本技术领域的普通技术人员来说,在不脱离本实用新型原理的前提下,还可以做出若干改进和润饰,这些改进和润饰也应视为本实用新型的保护范围。The above is only a preferred embodiment of the utility model, it should be pointed out that for those of ordinary skill in the art, without departing from the principle of the utility model, some improvements and modifications can also be made, these improvements and Retouching should also be regarded as the scope of protection of the present utility model.
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106323058A (en) * | 2015-07-06 | 2017-01-11 | 天津华赛尔传热设备有限公司 | Heat exchange system of MGGH |
CN106594778A (en) * | 2016-12-12 | 2017-04-26 | 墨宝股份有限公司 | Thermal power plant ultralow emission MGGH energy saving and environmental protecting equipment and method |
CN107504511A (en) * | 2016-06-14 | 2017-12-22 | 天津华赛尔传热设备有限公司 | A kind of smoke heat exchanging system |
CN110042340A (en) * | 2019-05-15 | 2019-07-23 | 江苏金色工业炉股份有限公司 | A kind of nitriding furnace air guide structure |
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2015
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106323058A (en) * | 2015-07-06 | 2017-01-11 | 天津华赛尔传热设备有限公司 | Heat exchange system of MGGH |
CN107504511A (en) * | 2016-06-14 | 2017-12-22 | 天津华赛尔传热设备有限公司 | A kind of smoke heat exchanging system |
CN106594778A (en) * | 2016-12-12 | 2017-04-26 | 墨宝股份有限公司 | Thermal power plant ultralow emission MGGH energy saving and environmental protecting equipment and method |
CN110042340A (en) * | 2019-05-15 | 2019-07-23 | 江苏金色工业炉股份有限公司 | A kind of nitriding furnace air guide structure |
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