CN110631318A - Power plant circulating water cooling system - Google Patents
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- CN110631318A CN110631318A CN201911055370.4A CN201911055370A CN110631318A CN 110631318 A CN110631318 A CN 110631318A CN 201911055370 A CN201911055370 A CN 201911055370A CN 110631318 A CN110631318 A CN 110631318A
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 202
- 238000001816 cooling Methods 0.000 title claims abstract description 132
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims abstract description 122
- 229910021529 ammonia Inorganic materials 0.000 claims abstract description 53
- 239000000498 cooling water Substances 0.000 claims abstract description 28
- 239000007788 liquid Substances 0.000 claims abstract description 13
- 238000012544 monitoring process Methods 0.000 claims description 19
- 239000000945 filler Substances 0.000 claims description 4
- 230000001105 regulatory effect Effects 0.000 claims description 4
- 238000005507 spraying Methods 0.000 claims 2
- 238000005057 refrigeration Methods 0.000 abstract description 25
- 238000005260 corrosion Methods 0.000 description 6
- 230000007797 corrosion Effects 0.000 description 6
- 238000000034 method Methods 0.000 description 6
- 238000010586 diagram Methods 0.000 description 5
- 230000008569 process Effects 0.000 description 5
- 239000002455 scale inhibitor Substances 0.000 description 5
- 239000007921 spray Substances 0.000 description 5
- 239000013043 chemical agent Substances 0.000 description 4
- 230000005611 electricity Effects 0.000 description 4
- 238000001704 evaporation Methods 0.000 description 4
- 230000008020 evaporation Effects 0.000 description 4
- 239000012535 impurity Substances 0.000 description 4
- 239000003112 inhibitor Substances 0.000 description 4
- 239000013505 freshwater Substances 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 230000009471 action Effects 0.000 description 2
- 230000001276 controlling effect Effects 0.000 description 2
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 1
- 239000000701 coagulant Substances 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000006073 displacement reaction Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B15/00—Sorption machines, plants or systems, operating continuously, e.g. absorption type
- F25B15/02—Sorption machines, plants or systems, operating continuously, e.g. absorption type without inert gas
- F25B15/04—Sorption machines, plants or systems, operating continuously, e.g. absorption type without inert gas the refrigerant being ammonia evaporated from aqueous solution
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25D—REFRIGERATORS; COLD ROOMS; ICE-BOXES; COOLING OR FREEZING APPARATUS NOT OTHERWISE PROVIDED FOR
- F25D17/00—Arrangements for circulating cooling fluids; Arrangements for circulating gas, e.g. air, within refrigerated spaces
- F25D17/02—Arrangements for circulating cooling fluids; Arrangements for circulating gas, e.g. air, within refrigerated spaces for circulating liquids, e.g. brine
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25D—REFRIGERATORS; COLD ROOMS; ICE-BOXES; COOLING OR FREEZING APPARATUS NOT OTHERWISE PROVIDED FOR
- F25D29/00—Arrangement or mounting of control or safety devices
- F25D29/001—Arrangement or mounting of control or safety devices for cryogenic fluid systems
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28C—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA COME INTO DIRECT CONTACT WITHOUT CHEMICAL INTERACTION
- F28C1/00—Direct-contact trickle coolers, e.g. cooling towers
- F28C1/14—Direct-contact trickle coolers, e.g. cooling towers comprising also a non-direct contact heat exchange
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28C—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA COME INTO DIRECT CONTACT WITHOUT CHEMICAL INTERACTION
- F28C1/00—Direct-contact trickle coolers, e.g. cooling towers
- F28C2001/006—Systems comprising cooling towers, e.g. for recooling a cooling medium
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
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- Combustion & Propulsion (AREA)
- Engine Equipment That Uses Special Cycles (AREA)
Abstract
本发明公开了一种电厂循环水冷却系统,包括:循环水系统和氨制冷系统,前者包括凝汽器、汇水箱、循环水泵、冷却塔、分水箱和连接它们的管道,后者包括蒸发器、压缩机、冷凝器、储液罐、膨胀阀和连接它们的管道(管道中填充有液氨),其中,蒸发器设置在冷却塔出水管上,压缩机的出口与蒸发器的进氨口连接,蒸发器的出氨口与压缩机的进口连接,冷凝器、储液罐和膨胀阀沿液氨流动方向依次设置在蒸发器进氨管上。本发明的有益之处在于:在循环水系统的基础上增设氨制冷系统,由氨制冷系统对从冷却塔流出的冷却循环水进一步进行冷却,从而使得冷却水的出塔温度降到更低,进而可以提高中、高压机组的效率。
The invention discloses a circulating water cooling system of a power plant, comprising: a circulating water system and an ammonia refrigeration system, the former includes a condenser, a water collection tank, a circulating water pump, a cooling tower, a water distribution tank and pipes connecting them, and the latter includes an evaporator , compressor, condenser, liquid storage tank, expansion valve and pipes connecting them (the pipes are filled with liquid ammonia), wherein the evaporator is set on the outlet pipe of the cooling tower, and the outlet of the compressor and the ammonia inlet of the evaporator The ammonia outlet of the evaporator is connected to the inlet of the compressor, and the condenser, liquid storage tank and expansion valve are sequentially arranged on the ammonia inlet pipe of the evaporator along the flow direction of liquid ammonia. The benefit of the present invention is that an ammonia refrigeration system is added on the basis of the circulating water system, and the cooling circulating water flowing out of the cooling tower is further cooled by the ammonia refrigeration system, so that the temperature of the cooling water coming out of the tower is lowered, In turn, the efficiency of medium and high pressure units can be improved.
Description
技术领域technical field
本发明涉及一种冷却系统,具体涉及电厂循环水冷却系统,属于电厂冷却技术领域。The invention relates to a cooling system, in particular to a power plant circulating water cooling system, and belongs to the technical field of power plant cooling.
背景技术Background technique
在火电厂的建设中,循环水冷却系统是必不可少的。电厂现有的循环水冷却系统主要由凝汽器、汇水箱、循环水泵、冷却塔、分水箱以及连接它们的管道组成,结构如图1所示。其中,冷却塔是组成循环水冷却系统的关键结构。In the construction of thermal power plants, circulating water cooling system is essential. The existing circulating water cooling system of the power plant is mainly composed of a condenser, a water header tank, a circulating water pump, a cooling tower, a water distribution tank and the pipes connecting them. The structure is shown in Figure 1. Among them, the cooling tower is the key structure of the circulating water cooling system.
冷却塔的冷却性能直接影响火电厂运行的经济性,电厂热效率的提高与冷却水的出塔温度的降低成正比,冷却水的出塔温度每下降1℃,中、高压机组的效率能分别提高0.47%、0.35%。The cooling performance of the cooling tower directly affects the economy of thermal power plant operation. The improvement of the thermal efficiency of the power plant is proportional to the decrease of the temperature of the cooling water exiting the tower. When the temperature of the cooling water exiting the tower drops by 1°C, the efficiency of the medium and high pressure units can be increased respectively. 0.47%, 0.35%.
因此,如何使冷却水的出塔温度降到更低对于火电厂而言至关重要。Therefore, how to lower the outlet temperature of cooling water is very important for thermal power plants.
而现有冷却塔采用自然通风降温,在炎热的夏天,空气温度高,降温效果难以保证。And existing cooling tower adopts natural ventilation to cool down, and in hot summer, air temperature is high, and cooling effect is difficult to guarantee.
此外,目前电厂循环冷却塔采用开式结构,一方面造成新鲜冷却水的蒸发损失,另一方面开式冷却塔的冷却水直接与大气接触,很容易将空气中大量的杂质带入循环系统,致使管道腐蚀和结垢严重,不得不投加大量阻垢剂、缓蚀剂等化学药剂,既不经济又会产生二次污染。In addition, the current power plant circulation cooling tower adopts an open structure. On the one hand, it causes evaporation loss of fresh cooling water. On the other hand, the cooling water of the open cooling tower is directly in contact with the atmosphere, which easily brings a large amount of impurities in the air into the circulation system. As a result, pipeline corrosion and scaling are serious, and a large amount of scale inhibitors, corrosion inhibitors and other chemical agents have to be added, which is not economical and will cause secondary pollution.
发明内容Contents of the invention
本发明的第一个目的在于:提供一种能够使冷却水的出塔温度降到更低的电厂循环水冷却系统。The first object of the present invention is to provide a power plant circulating water cooling system capable of lowering the tower temperature of the cooling water.
本发明的第二个目的在于:提供一种全封闭式循环水冷却系统,既能保证循环水的高效运行,又能减少水资源的消耗。The second object of the present invention is to provide a fully enclosed circulating water cooling system, which can not only ensure the efficient operation of circulating water, but also reduce the consumption of water resources.
为了实现上述目标,本发明采用如下的技术方案:In order to achieve the above object, the present invention adopts the following technical solutions:
一种电厂循环水冷却系统,包括:循环水系统,前述循环水系统包括:凝汽器、汇水箱、循环水泵、冷却塔、分水箱和连接它们的管道,其中,凝汽器用于冷却汽轮机做功后的乏汽,凝汽器的循环水出口与冷却塔的循环水进口连接,冷却塔的循环水出口与凝汽器的循环水进口连接,汇水箱和循环水泵沿水流方向依次设置在冷却塔进水管上,分水箱设置在冷却塔出水管上,其特征在于,前述电厂循环水冷却系统还包括氨制冷系统,前述氨制冷系统包括:蒸发器、压缩机、冷凝器、储液罐、膨胀阀和连接它们的管道,管道中填充有液氨,其中:A circulating water cooling system for a power plant, comprising: a circulating water system, the aforementioned circulating water system comprising: a condenser, a water header tank, a circulating water pump, a cooling tower, a water distribution tank and pipes connecting them, wherein the condenser is used to cool the steam turbine to perform work After exhaust steam, the circulating water outlet of the condenser is connected to the circulating water inlet of the cooling tower, and the circulating water outlet of the cooling tower is connected to the circulating water inlet of the condenser. On the water inlet pipe, the water distribution tank is arranged on the outlet pipe of the cooling tower. It is characterized in that the circulating water cooling system of the power plant also includes an ammonia refrigeration system. The ammonia refrigeration system includes: an evaporator, a compressor, a condenser, a liquid storage tank, an expansion Valves and pipes connecting them filled with liquid ammonia, wherein:
前述蒸发器设置在冷却塔出水管上;The aforementioned evaporator is arranged on the outlet pipe of the cooling tower;
前述压缩机的出口与蒸发器的进氨口连接,蒸发器的出氨口与压缩机的进口连接;The outlet of the aforementioned compressor is connected with the ammonia inlet of the evaporator, and the ammonia outlet of the evaporator is connected with the inlet of the compressor;
前述冷凝器、储液罐和膨胀阀沿液氨流动方向依次设置在蒸发器进氨管上。The aforementioned condenser, liquid storage tank and expansion valve are sequentially arranged on the ammonia inlet pipe of the evaporator along the flow direction of liquid ammonia.
前述的电厂循环水冷却系统,其特征在于,前述电厂循环水冷却系统还包括温度监测与控制系统,前述温度监测与控制系统设置在冷却塔出水管上,位于蒸发器与冷却塔之间,并与压缩机和膨胀阀信号连接。The aforementioned power plant circulating water cooling system is characterized in that the aforementioned power plant circulating water cooling system also includes a temperature monitoring and control system, and the aforementioned temperature monitoring and control system is arranged on the outlet pipe of the cooling tower, between the evaporator and the cooling tower, and Signal connection to compressor and expansion valve.
前述的电厂循环水冷却系统,其特征在于,前述冷却塔内从上到下依次设置有收水器、喷淋装置、填料和集水池,其中,前述喷淋装置的进水口与冷却塔进水管的末端连接,集水池的出水口与冷却塔出水管的首端连接;或者,前述冷却塔内设置有多个盘管和多个槽带板式翅片,其中,每个槽带板式翅片均竖直设置,全部槽带板式翅片沿水平方向均匀排开,每个盘管均由多个S形弯管首尾相接而成且这些S形弯管位于同一个竖直平面内,全部盘管沿水平方向均匀排开并通过分支管道连通,盘管所在的竖直平面与槽带板式翅片所在的竖直平面垂直,槽带板式翅片上留有供盘管穿过的孔,盘管嵌在槽带板式翅片内,盘管的进水口和出水口分别与冷却塔进水管的末端、冷却塔出水管的首端连接。The aforementioned circulating water cooling system of the power plant is characterized in that, the aforementioned cooling tower is provided with a water eliminator, a spray device, a filler and a sump sequentially from top to bottom, wherein the water inlet of the aforementioned spray device and the water inlet pipe of the cooling tower The end of the pool is connected, and the water outlet of the sump is connected to the head end of the outlet pipe of the cooling tower; or, the aforementioned cooling tower is provided with multiple coils and multiple grooves with plate fins, wherein each groove with plate fins Set vertically, all slotted plate fins are arranged evenly along the horizontal direction, each coil is formed by connecting multiple S-shaped bends end to end, and these S-shaped bends are located in the same vertical plane, all coils The tubes are evenly arranged in the horizontal direction and connected through branch pipes. The vertical plane where the coil is located is perpendicular to the vertical plane where the slotted plate fins are located. There are holes for the coil to pass through the slotted plate fins. Embedded in the slotted plate fins, the water inlet and outlet of the coil are respectively connected to the end of the cooling tower water inlet pipe and the head end of the cooling tower water outlet pipe.
前述的电厂循环水冷却系统,其特征在于,前述蒸发器选用的是半焊式板式蒸发器。The aforementioned circulating water cooling system of the power plant is characterized in that the aforementioned evaporator is a semi-welded plate evaporator.
前述的电厂循环水冷却系统,其特征在于,前述压缩机的冷却水出口与汇水箱连接。The aforementioned power plant circulating water cooling system is characterized in that the cooling water outlet of the aforementioned compressor is connected to the water header tank.
前述的电厂循环水冷却系统,其特征在于,前述冷凝器的冷却水进口与分水箱连接,冷却水出口与汇水箱连接。The aforementioned power plant circulating water cooling system is characterized in that the cooling water inlet of the aforementioned condenser is connected to the water distribution tank, and the cooling water outlet is connected to the water collection tank.
前述的电厂循环水冷却系统,其特征在于,前述汇水箱上设置有其他水入口。The aforementioned power plant circulating water cooling system is characterized in that the aforementioned water collection tank is provided with other water inlets.
前述的电厂循环水冷却系统,其特征在于,前述凝汽器与汇水箱之间、前述凝汽器与分水箱之间均设有调节阀。The aforementioned power plant circulating water cooling system is characterized in that regulating valves are provided between the aforementioned condenser and the header tank, and between the aforementioned condenser and the water distribution tank.
本发明的有益之处在于:The benefits of the present invention are:
(1)在循环水系统的基础上增设氨制冷系统,由氨制冷系统对从冷却塔流出的冷却循环水进一步进行冷却,从而使得冷却水的出塔温度降到更低,进而可以提高中、高压机组的效率;(1) An ammonia refrigeration system is added on the basis of the circulating water system, and the ammonia refrigeration system further cools the cooling circulating water flowing out of the cooling tower, so that the temperature of the cooling water coming out of the tower can be lowered, thereby improving the medium and high temperature. Efficiency of the high pressure unit;
(2)在冷却塔出水管上设置温度监测与控制系统,温度监测与控制系统可监测冷却塔出水温度,并根据监测结果对氨制冷系统进行调控,可以有效的节约成本,使效益最大化;(2) A temperature monitoring and control system is installed on the outlet pipe of the cooling tower. The temperature monitoring and control system can monitor the outlet water temperature of the cooling tower and regulate the ammonia refrigeration system according to the monitoring results, which can effectively save costs and maximize benefits;
(3)采用闭式冷却塔,使得循环水系统构成了一个完全封闭的循环回路,既避免了新鲜水的蒸发损失,减少了循环水的损耗,又避免了大气中的杂质被带入循环水系统中,进而减少了阻垢剂、缓蚀剂等化学药剂的投放,从而节省了成本,也减少了二次污染,具有广泛的经济价值和实用价值。(3) The closed cooling tower is adopted, so that the circulating water system forms a completely closed circulating loop, which not only avoids the evaporation loss of fresh water, reduces the loss of circulating water, but also prevents impurities in the atmosphere from being brought into the circulating water In the system, the input of chemical agents such as scale inhibitors and corrosion inhibitors is further reduced, thereby saving costs and reducing secondary pollution, which has extensive economic and practical values.
附图说明Description of drawings
图1是电厂现有的循环水冷却系统的组成结构示意图;Figure 1 is a schematic diagram of the composition and structure of the existing circulating water cooling system of the power plant;
图2是本发明提供的电厂循环水冷却系统的第一个具体实施例的组成结构示意图;Fig. 2 is the composition structure schematic diagram of the first specific embodiment of the power plant circulating water cooling system provided by the present invention;
图3是本发明提供的电厂循环水冷却系统的第二个具体实施例的组成结构示意图;Fig. 3 is the composition structure schematic diagram of the second specific embodiment of the power plant circulating water cooling system provided by the present invention;
图4是图3中的槽带板式翅片和盘管的局部放大示意图;Fig. 4 is a partially enlarged schematic diagram of the slotted plate fin and the coiled pipe in Fig. 3;
图5是图4中的槽带板式翅片和盘管的右视图。FIG. 5 is a right side view of the slotted plate fin and coil in FIG. 4 .
图中附图标记的含义:Meanings of reference signs in the figure:
1-汽轮机、2-凝汽器、3-汇水箱、4-循环水泵、5-冷却塔、6-分水箱、7-蒸发器、8-压缩机、9-冷凝器、10-储液罐、11-膨胀阀、12-温度监测与控制系统;1-steam turbine, 2-condenser, 3-collection tank, 4-circulating water pump, 5-cooling tower, 6-water distribution tank, 7-evaporator, 8-compressor, 9-condenser, 10-liquid storage tank , 11-expansion valve, 12-temperature monitoring and control system;
501-收水器、502-喷淋装置、503-填料、504-集水池;501-water eliminator, 502-spray device, 503-filler, 504-collection tank;
511-盘管、512-槽带板式翅片。511-coil, 512-slot with plate fins.
具体实施方式Detailed ways
以下结合附图和具体实施例对本发明作具体的介绍。The present invention will be specifically introduced below in conjunction with the accompanying drawings and specific embodiments.
实施例1Example 1
本发明提供的电厂循环水冷却系统包括:循环水系统、氨制冷系统和温度监测与控制系统。The power plant circulating water cooling system provided by the invention includes: a circulating water system, an ammonia refrigeration system and a temperature monitoring and control system.
参照图2,循环水系统包括:凝汽器2、汇水箱3、循环水泵4、冷却塔5、分水箱6和连接它们的管道。其中,凝汽器2用于冷却汽轮机1做功后的乏汽,凝汽器2的循环水出口与冷却塔5的循环水进口连接,冷却塔5的循环水出口与凝汽器2的循环水进口连接,汇水箱3和循环水泵4沿水流方向依次设置在冷却塔进水管上,分水箱6设置在冷却塔出水管上。Referring to Fig. 2, the circulating water system includes: a
冷却塔5采用开式冷却塔,冷却塔5内从上到下依次设置有收水器501、喷淋装置502、填料503和集水池504,其中,喷淋装置502的进水口与冷却塔进水管的末端连接,集水池504的出水口与冷却塔出水管的首端连接。The
作为一种优选的方案,凝汽器2与汇水箱3之间、凝汽器2与分水箱6之间均设有调节阀。As a preferred solution, regulating valves are provided between the
参照图2,氨制冷系统包括:蒸发器7、压缩机8、冷凝器9、储液罐10、膨胀阀11和连接它们的管道,管道中填充有液氨。其中,蒸发器7设置在冷却塔出水管上,压缩机8的出口与蒸发器7的进氨口连接,蒸发器7的出氨口与压缩机8的进口连接,冷凝器9、储液罐10和膨胀阀11沿液氨流动方向依次设置在蒸发器进氨管上。蒸发器7为循环水和液氨的冷热交换提供了场所。Referring to Fig. 2, the ammonia refrigeration system includes: an evaporator 7, a
作为一种优选的方案,蒸发器7选用的是半焊式板式蒸发器,半焊式板式蒸发器能够有效的利用液氨将循环水中的热量吸收到氨制冷系统中。As a preferred solution, the evaporator 7 is a semi-welded plate evaporator, which can effectively use liquid ammonia to absorb the heat in the circulating water into the ammonia refrigeration system.
作为一种优选的方案,压缩机8的冷却水出口与汇水箱3连接。As a preferred solution, the cooling water outlet of the
冷凝器9中的压缩后过热的气氨的冷却采用水冷方式,作为一种优选的方案,冷凝器9的冷却水进口与分水箱6连接,冷却水出口与汇水箱3连接,即冷凝器9的冷却水来源为分水箱6,冷却水在冷凝器9中与过热气氨换热后又流入汇水箱3中等待冷却。The cooling of the overheated gas ammonia after compression in the
作为一种优选的方案,汇水箱3上还设置有其他水入口。汇水箱3中待冷却的热水来自于汽轮机1的冷却水、压缩机8的冷却水、冷凝器9的冷却水以及通过其他水入口流进来的其他冷却水。As a preferred solution, other water inlets are also arranged on the
参照图2,温度监测与控制系统12设置在冷却塔出水管上,位于蒸发器7与冷却塔5之间,并与压缩机8和膨胀阀11信号连接。温度监测与控制系统12监测冷却塔出水温度,根据监测结果对氨制冷系统进行调控,具体的:Referring to FIG. 2 , the temperature monitoring and
(1)当冷却塔出水温度高于凝汽器2的进水温度要求时,温度监测与控制系统12通过控制氨制冷系统的压缩机8(开启)和膨胀阀11(开启)自动开启氨制冷过程,由氨制冷系统对冷却塔出水管中的循环水进行进一步冷却,以使冷却塔出水温度达到凝汽器2的进水温度要求;(1) When the outlet water temperature of the cooling tower is higher than the inlet water temperature requirement of the
(2)当冷却塔出水温度达到凝汽器2的进水温度要求时,温度监测与控制系统12通过控制氨制冷系统的压缩机8(关闭)和膨胀阀11(关闭)自动关闭氨制冷过程,以降低损耗。(2) When the outlet water temperature of the cooling tower reaches the water inlet temperature requirement of the
可见,增设温度监测与控制系统12可以有效的节约成本,使效益最大化。It can be seen that adding the temperature monitoring and
在使用时,冷却水在凝汽器2中与推动汽轮机1做功后的乏汽进行换热,换热后水温升高流入汇水箱3中,经循环水泵4加压后进入冷却塔5内,利用空气自然对流进行第一次冷却,冷却水在重力作用下进入集水池504,经冷却塔5冷却后的循环水在蒸发器7中与液氨进行热交换,实现第二次冷却,被冷却后的水进入分水箱6,进而进入凝汽器2与乏汽换热,之后流入汇水箱3中,如此循环保证凝汽器2的正常运转;液氨在蒸发器7中与循环水换热后,因温度升高、压力降低而蒸发为气氨,气氨经压缩机8压缩为过热气氨,过热气氨在冷凝器9中经过冷却、冷凝后变为饱和液氨,冷却后的液氨进入储液罐10中储存备用,储液罐10中的液氨经膨胀阀11绝热节流膨胀后压力和温度都降低,压力和温度都降的液氨再次进入蒸发器7中与需要被冷却的水进行换热,换热蒸发的氨再次进入压缩机8中往复循环,从而实现了利用氨制冷循环冷却冷却水的目的;同时,设置在冷却塔出水管上的温度监测与控制系统12对冷却塔出水温度进行监测,根据监测结果对氨制冷系统进行调控,若冷却塔出水温度达到凝汽器2的进水温度要求,则自动关闭氨制冷过程以降低损耗,否则自动调控氨制冷过程的制冷量以使冷却塔出水温度达到凝汽器2的进水温度要求。When in use, the cooling water exchanges heat with the exhaust steam that drives the steam turbine 1 to perform work in the
实施例2Example 2
本发明提供的电厂循环水冷却系统包括:循环水系统、氨制冷系统和温度监测与控制系统。The power plant circulating water cooling system provided by the invention includes: a circulating water system, an ammonia refrigeration system and a temperature monitoring and control system.
参照图3,循环水系统包括:凝汽器2、汇水箱3、循环水泵4、冷却塔5、分水箱6和连接它们的管道。其中,凝汽器2用于冷却汽轮机1做功后的乏汽,凝汽器2的循环水出口与冷却塔5的循环水进口连接,冷却塔5的循环水出口与凝汽器2的循环水进口连接,汇水箱3和循环水泵4沿水流方向依次设置在冷却塔进水管上,分水箱6设置在冷却塔出水管上。Referring to Fig. 3, the circulating water system includes: a
冷却塔5采用闭式冷却塔,冷却塔5内设置有多个盘管511和多个槽带板式翅片512,其中,每个槽带板式翅片512均竖直设置,全部槽带板式翅片512沿水平方向均匀排开,每个盘管511均由多个S形弯管首尾相接而成且这些S形弯管位于同一个竖直平面内,全部盘管511沿水平方向均匀排开并通过分支管道连通,盘管511所在的竖直平面与槽带板式翅片512所在的竖直平面垂直,槽带板式翅片512上留有供盘管511穿过的孔,盘管511嵌在槽带板式翅片512内,盘管511的进水口和出水口分别与冷却塔进水管的末端、冷却塔出水管的首端连接。槽带板式翅片512和盘管511的局部放大示意图见图4和图5。来自凝汽器2的热循环水进入汇水箱3中,需要冷却的循环水在循环水泵4的作用下进入冷却塔5内,循环水流经冷却塔5内的盘管511时,通过槽带板式翅片512加速传热,利用塔底进入的空气带走部分热量。The
现有电厂的循环水冷却系统大多采用图2所示的开式冷却塔,开式冷却塔一方面会造成新鲜水的蒸发损失,另一方面冷却水直接与大气接触,大量大气中的杂质容易被带入循环水系统,致使管道腐蚀和结垢严重,不得不投加大量阻垢剂、缓蚀剂等化学药剂,既不经济又会产生二次污染。在本具体实施例中,我们对开式冷却塔的结构进行了改进,设计出了一种闭式冷却塔,使得循环水系统构成了一个完全封闭的循环回路,既避免了新鲜水的蒸发损失,减少了循环水的损耗,又避免了大气中的杂质被带入循环水系统中,进而减少了阻垢剂、缓蚀剂等化学药剂的投放,从而节省了成本,也减少了二次污染,具有广泛的经济价值和实用价值。以某电厂为例,循环水系统保有水量10000m3,循环水量5000m3/h,补水量150m3/h,排水量运行成本为:药剂费(混凝剂、阻垢剂)0.029元/t水、水费2.8元/t;本发明的氨制冷过程以JZLG系列螺杆氨制冷压缩机组为例,电动机机组在标准工况下以最大功率450kW计算,工业电费为0.9元/千瓦时,压缩氨所用的电是电厂内部的电,价格要比市场至少低30%以上;因此,电厂的循环水系统每年可节省费用如下:(1)水费:150×24×365×2.8=367.9万元;(2)药剂费:5000×0.029×24×365=127万元;而循环水系统产生的电费为:450×24×365×0.9×0.7=248.4万元;可见,采用闭式冷却塔后,每年可节省246.5万元,对于严重缺水地区来说,潜在的经济价值远远大于以上计算的数值。The circulating water cooling system of existing power plants mostly adopts the open cooling tower shown in Figure 2. On the one hand, the open cooling tower will cause evaporation loss of fresh water, and on the other hand, the cooling water is directly in contact with the atmosphere, and a large number of impurities in the atmosphere are easily It is brought into the circulating water system, resulting in serious corrosion and scaling of the pipeline, and a large amount of chemical agents such as scale inhibitors and corrosion inhibitors have to be added, which is not economical and will cause secondary pollution. In this specific example, we improved the structure of the open cooling tower and designed a closed cooling tower, so that the circulating water system forms a completely closed circulation loop, which avoids the evaporation loss of fresh water , reducing the loss of circulating water, and avoiding the impurities in the atmosphere from being brought into the circulating water system, thereby reducing the input of chemical agents such as scale inhibitors and corrosion inhibitors, thereby saving costs and reducing secondary pollution , has extensive economic value and practical value. Taking a power plant as an example, the circulating water system retains 10,000m 3 of water, 5,000m 3 /h of circulating water, and 150m 3 /h of supplementary water. The operating cost of the displacement is: chemical fee (coagulant, scale inhibitor) 0.029 yuan/t of water, The water fee is 2.8 yuan/t; the ammonia refrigeration process of the present invention takes the JZLG series screw ammonia refrigeration compressor unit as an example, the motor unit is calculated with a maximum power of 450kW under standard working conditions, and the industrial electricity fee is 0.9 yuan/kWh. Electricity is the electricity inside the power plant, and the price is at least 30% lower than the market; therefore, the annual cost savings of the circulating water system of the power plant are as follows: (1) Water fee: 150×24×365×2.8=3.679 million yuan; (2 ) Pharmacy fee: 5000×0.029×24×365=1.27 million yuan; and the electricity cost generated by the circulating water system is: 450×24×365×0.9×0.7=2.484 million yuan; Saving 2.465 million yuan, for areas with severe water shortage, the potential economic value is far greater than the value calculated above.
参照图3,氨制冷系统包括:蒸发器7、压缩机8、冷凝器9、储液罐10、膨胀阀11和连接它们的管道,管道中填充有液氨。其中,蒸发器7设置在冷却塔出水管上,压缩机8的出口与蒸发器7的进氨口连接,蒸发器7的出氨口与压缩机8的进口连接,冷凝器9、储液罐10和膨胀阀11沿液氨流动方向依次设置在蒸发器进氨管上。流出盘管511的循环水在蒸发器7中与液氨进行二次换热,之后流入分水箱6用于与凝汽器2中的乏汽换热,如此构成循环。Referring to FIG. 3 , the ammonia refrigeration system includes: an evaporator 7 , a
作为一种优选的方案,蒸发器7选用的是半焊式板式蒸发器。As a preferred solution, the evaporator 7 is a semi-welded plate evaporator.
作为一种优选的方案,压缩机8的冷却水出口与汇水箱3连接。As a preferred solution, the cooling water outlet of the
作为一种优选的方案,冷凝器9的冷却水进口与分水箱6连接,冷却水出口与汇水箱3连接。As a preferred solution, the cooling water inlet of the
作为一种优选的方案,汇水箱3上设置有其他水入口。As a preferred solution, other water inlets are arranged on the
参照图3,温度监测与控制系统12设置在冷却塔出水管上,位于蒸发器7与冷却塔5之间,并与压缩机8和膨胀阀11信号连接。Referring to FIG. 3 , the temperature monitoring and
需要说明的是,上述实施例不以任何形式限制本发明,凡采用等同替换或等效变换的方式所获得的技术方案,均落在本发明的保护范围内。It should be noted that the above embodiments do not limit the present invention in any form, and all technical solutions obtained by means of equivalent replacement or equivalent transformation fall within the protection scope of the present invention.
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Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113375384A (en) * | 2021-07-17 | 2021-09-10 | 南京拓展科技有限公司 | Ultrahigh-precision process cooling water system and constant temperature control method thereof |
| CN113812838A (en) * | 2021-11-05 | 2021-12-21 | 广东美芝制冷设备有限公司 | Cooking utensil |
| CN114234668A (en) * | 2021-12-24 | 2022-03-25 | 重庆大学 | Cooling water-saving device for cooling tower and wet cooling tower |
| CN115900191A (en) * | 2022-10-25 | 2023-04-04 | 珠海格力电器股份有限公司 | Water chilling unit |
| CN116782598A (en) * | 2023-06-25 | 2023-09-19 | 安徽正飞机电设备有限公司 | A heat dissipation circulation system and heat dissipation control method for electromechanical equipment |
| CN116961570A (en) * | 2023-07-21 | 2023-10-27 | 大唐环境产业集团股份有限公司 | Photovoltaic efficiency improving system utilizing liquid ammonia evaporation residual cooling |
| CN117168185A (en) * | 2022-04-12 | 2023-12-05 | 常州中冷环保技术有限公司 | Secondary cooling tower utilizing low-temperature waste heat |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20070000275A1 (en) * | 2005-06-30 | 2007-01-04 | Zhiming Li | Water cooling system with full heat recovery |
| RU87247U1 (en) * | 2009-04-28 | 2009-09-27 | Закрытое акционерное общество "Совасатом-М" | AIR COOLING UNIT FOR COOLING RETAIL WATER |
| CN102809306A (en) * | 2012-08-16 | 2012-12-05 | 上海廷亚冷却系统有限公司 | Water-saving isenthalpic humidifying and temperature reducing closed cooling tower |
| CN202734361U (en) * | 2012-07-16 | 2013-02-13 | 泰州雪旺制冷设备有限公司 | Ice-cream machine condenser with water-cooled device |
| CN206803843U (en) * | 2017-04-07 | 2017-12-26 | 石福军 | A kind of generating plant circulation-water secondary cooling system |
| CN210801754U (en) * | 2019-10-31 | 2020-06-19 | 西安石油大学 | Power plant circulating water cooling system |
-
2019
- 2019-10-31 CN CN201911055370.4A patent/CN110631318A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20070000275A1 (en) * | 2005-06-30 | 2007-01-04 | Zhiming Li | Water cooling system with full heat recovery |
| RU87247U1 (en) * | 2009-04-28 | 2009-09-27 | Закрытое акционерное общество "Совасатом-М" | AIR COOLING UNIT FOR COOLING RETAIL WATER |
| CN202734361U (en) * | 2012-07-16 | 2013-02-13 | 泰州雪旺制冷设备有限公司 | Ice-cream machine condenser with water-cooled device |
| CN102809306A (en) * | 2012-08-16 | 2012-12-05 | 上海廷亚冷却系统有限公司 | Water-saving isenthalpic humidifying and temperature reducing closed cooling tower |
| CN206803843U (en) * | 2017-04-07 | 2017-12-26 | 石福军 | A kind of generating plant circulation-water secondary cooling system |
| CN210801754U (en) * | 2019-10-31 | 2020-06-19 | 西安石油大学 | Power plant circulating water cooling system |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113375384A (en) * | 2021-07-17 | 2021-09-10 | 南京拓展科技有限公司 | Ultrahigh-precision process cooling water system and constant temperature control method thereof |
| CN113375384B (en) * | 2021-07-17 | 2022-08-30 | 南京拓展科技有限公司 | Ultrahigh-precision process cooling water system and constant temperature control method thereof |
| CN113812838A (en) * | 2021-11-05 | 2021-12-21 | 广东美芝制冷设备有限公司 | Cooking utensil |
| CN114234668A (en) * | 2021-12-24 | 2022-03-25 | 重庆大学 | Cooling water-saving device for cooling tower and wet cooling tower |
| CN114234668B (en) * | 2021-12-24 | 2023-12-12 | 重庆大学 | A cooling and water-saving device for cooling towers and wet cooling towers |
| CN117168185A (en) * | 2022-04-12 | 2023-12-05 | 常州中冷环保技术有限公司 | Secondary cooling tower utilizing low-temperature waste heat |
| CN115900191A (en) * | 2022-10-25 | 2023-04-04 | 珠海格力电器股份有限公司 | Water chilling unit |
| CN116782598A (en) * | 2023-06-25 | 2023-09-19 | 安徽正飞机电设备有限公司 | A heat dissipation circulation system and heat dissipation control method for electromechanical equipment |
| CN116961570A (en) * | 2023-07-21 | 2023-10-27 | 大唐环境产业集团股份有限公司 | Photovoltaic efficiency improving system utilizing liquid ammonia evaporation residual cooling |
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