CN1251386C - Device for recycling exhaust air and cooling fluid of condensator for evaporative cooling electric motor - Google Patents
Device for recycling exhaust air and cooling fluid of condensator for evaporative cooling electric motor Download PDFInfo
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- CN1251386C CN1251386C CN 02122111 CN02122111A CN1251386C CN 1251386 C CN1251386 C CN 1251386C CN 02122111 CN02122111 CN 02122111 CN 02122111 A CN02122111 A CN 02122111A CN 1251386 C CN1251386 C CN 1251386C
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- 238000001816 cooling Methods 0.000 title claims abstract description 51
- 239000012809 cooling fluid Substances 0.000 title 1
- 238000004064 recycling Methods 0.000 title 1
- 239000002826 coolant Substances 0.000 claims abstract description 32
- 239000007788 liquid Substances 0.000 claims abstract description 28
- 238000000926 separation method Methods 0.000 claims abstract description 20
- 238000011084 recovery Methods 0.000 claims abstract description 12
- 238000009833 condensation Methods 0.000 claims description 10
- 230000005494 condensation Effects 0.000 claims description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 10
- 239000000498 cooling water Substances 0.000 claims description 7
- 239000000203 mixture Substances 0.000 claims description 4
- 238000002955 isolation Methods 0.000 claims 1
- 239000000110 cooling liquid Substances 0.000 abstract description 9
- 238000005086 pumping Methods 0.000 abstract 1
- 238000009835 boiling Methods 0.000 description 9
- 230000000694 effects Effects 0.000 description 2
- 238000000605 extraction Methods 0.000 description 2
- CBEFDCMSEZEGCX-UHFFFAOYSA-N 1,1,2,2,2-pentafluoro-n,n-bis(1,1,2,2,2-pentafluoroethyl)ethanamine Chemical group FC(F)(F)C(F)(F)N(C(F)(F)C(F)(F)F)C(F)(F)C(F)(F)F CBEFDCMSEZEGCX-UHFFFAOYSA-N 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- ZZUFCTLCJUWOSV-UHFFFAOYSA-N furosemide Chemical compound C1=C(Cl)C(S(=O)(=O)N)=CC(C(O)=O)=C1NCC1=CC=CO1 ZZUFCTLCJUWOSV-UHFFFAOYSA-N 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 238000005057 refrigeration Methods 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
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Abstract
本发明蒸发冷却电机的冷凝器排气和冷却液回收装置是为改进和完善电机定子蒸发冷却系统而设计的。装置的两端分别与主冷凝器和浸泡电机定子的蒸发冷却室连接,第一压力控制器装在主冷凝器的顶部连接其冷凝空间,由第一压力控制器顺序连接第一电磁阀、抽气泵、副冷凝器和气液分离箱;分离出的空气经第一单向阀进入空气过滤器,经过滤后排出;气液分离箱中经冷凝的液体冷却介质(冷却液)通过下端装有第二压力控制器和第二电磁阀的管道流回电机定子蒸发冷却室。本发明装置在主冷凝器冷凝空间压力超过设定值时排出空气,使其工作在设定的压力下,同时回收冷却液,实现电机蒸发冷却系统高效安全经济运行的要求。
The condenser exhaust and coolant recovery device of the evaporative cooling motor of the present invention is designed for improving and perfecting the evaporative cooling system of the motor stator. The two ends of the device are respectively connected with the main condenser and the evaporative cooling chamber where the motor stator is soaked. The first pressure controller is installed on the top of the main condenser to connect with its condensing space. The first pressure controller is connected to the first solenoid valve, pumping Air pump, auxiliary condenser and gas-liquid separation box; the separated air enters the air filter through the first one-way valve, and is discharged after being filtered; the condensed liquid cooling medium (coolant) in the gas-liquid separation box passes through the first The pipes of the second pressure controller and the second solenoid valve flow back to the motor stator evaporative cooling chamber. The device of the invention discharges air when the pressure in the condensing space of the main condenser exceeds the set value, makes it work under the set pressure, and recovers the cooling liquid at the same time, so as to realize the requirement of efficient, safe and economical operation of the evaporative cooling system of the motor.
Description
技术领域technical field
本发明属于电机冷却装置,涉及蒸发冷却电机的改进和完善,提供冷凝器排气和冷却液回收装置。The invention belongs to a motor cooling device, relates to the improvement and completion of an evaporative cooling motor, and provides a condenser exhaust and cooling liquid recovery device.
背景技术Background technique
大型发电机包括汽轮发电机及水轮发电机,采用蒸发冷却技术比常用的空冷、水冷、氢冷的机组具有冷却效果好、运行安全可靠等优点。这里把定子发热体采用蒸发冷却的发电机称为蒸发冷却电机,它的蒸发冷却装置是一个密闭的冷却介质循环系统,在电机蒸发冷却室中,液态的冷却介质(又称冷却液)吸收电机定子发热后,发生沸腾蒸发相变,由液体变成气体,进入冷凝器中与二次冷却水进行热交换,冷凝成液体后重新返回冷却回路(蒸发冷却室)。冷却介质的沸点决定了电机的运行温度,而冷却介质的沸点又与冷凝空间的压力密切相关。蒸发冷却发电机在运行中由于空气泄入,往往使冷凝空间压力升高,造成冷却介质的沸点升高,随之也降低了蒸发冷却电机的冷却效果。这时为了保持合理的运行温度,必须打开阀门排出空气降低冷凝空间的压力。然而,排出空气的同时部分冷却介质的蒸气也被排出,这在某些应用场合是不允许的,例如在舰船上安装蒸发冷却电机的空间比较狭小,位置受到限制。Large-scale generators include turbo generators and hydro generators. Compared with commonly used air-cooled, water-cooled and hydrogen-cooled units, the evaporative cooling technology has the advantages of better cooling effect and safe and reliable operation. Here, the generator whose stator heating element adopts evaporative cooling is called an evaporative cooling motor. Its evaporative cooling device is a closed cooling medium circulation system. In the motor evaporative cooling chamber, the liquid cooling medium (also called coolant) absorbs the motor After the stator heats up, a boiling evaporation phase transition occurs, from liquid to gas, and enters the condenser for heat exchange with secondary cooling water, condenses into liquid and returns to the cooling circuit (evaporative cooling chamber). The boiling point of the cooling medium determines the operating temperature of the motor, and the boiling point of the cooling medium is closely related to the pressure of the condensation space. During the operation of the evaporative cooling generator, due to air leakage, the pressure of the condensation space often increases, causing the boiling point of the cooling medium to increase, and the cooling effect of the evaporative cooling motor is also reduced. At this time, in order to maintain a reasonable operating temperature, the valve must be opened to discharge air to reduce the pressure of the condensation space. However, part of the vapor of the cooling medium is also discharged while the air is discharged, which is not allowed in some applications, such as the space for installing evaporative cooling motors on ships is relatively narrow and the location is limited.
中国发明专利申请01131399.4和01131397.8提供了两种大型电机的蒸发冷却装置,在它们的蒸发冷却回路中,没有设冷凝器排气和冷却液回收装置。因此,有必要改进和完善蒸发冷却电机的蒸发冷却循环回路,通过控制冷凝空间压力使之可以选用不同沸点的冷却介质,以满足多种应用的要求,同时实现冷却液的回收。Chinese invention patent applications 01131399.4 and 01131397.8 provide two kinds of evaporative cooling devices for large-scale motors. In their evaporative cooling circuits, there are no condenser exhaust and cooling liquid recovery devices. Therefore, it is necessary to improve and perfect the evaporative cooling cycle of the evaporative cooling motor. By controlling the pressure of the condensing space, cooling media with different boiling points can be selected to meet the requirements of various applications, and at the same time realize the recovery of cooling liquid.
发明内容Contents of the invention
本发明的目的是提供蒸发冷却电机的冷凝器排气和冷却液回收装置,该装置在主冷凝器冷凝空间压力超过设定值时排出空气,使其压力保持在设定压力状态,同时回收因排气而外泄的冷却液(又称冷却介质),实现蒸发冷却电机的高效经济运行。The object of the present invention is to provide a condenser exhaust and coolant recovery device for evaporative cooling motors, the device discharges air when the pressure in the condensing space of the main condenser exceeds the set value, keeps its pressure at the set pressure state, and simultaneously recovers the The cooling liquid (also known as cooling medium) leaked from the exhaust gas realizes the efficient and economical operation of the evaporative cooling motor.
本发明蒸发冷却电机的冷凝器排气和冷却液回收装置的两端分别与主冷凝器和浸泡电机定子发热部件的蒸发冷却室连接。主冷凝器位于蒸发冷却室的上方。一台第一压力控制器装在主冷凝器的顶部连通其冷凝空间,由该第一压力控制器顺序连接第一电磁阀、抽气泵、副冷凝器和气液分离箱;气液分离箱上部装有带第一单向阀的排气管,该排气管与空气过滤器相连;气液分离箱的下端通过装有第二压力控制器、第二电磁阀和第二单向阀的管道与蒸发冷却室相连。The two ends of the exhaust gas of the condenser and the cooling liquid recovery device of the evaporative cooling motor of the present invention are respectively connected with the main condenser and the evaporative cooling chamber soaked in the heat-generating parts of the motor stator. The main condenser is located above the evaporative cooling chamber. A first pressure controller is installed on the top of the main condenser to communicate with its condensing space, and the first pressure controller is sequentially connected to the first solenoid valve, suction pump, auxiliary condenser and gas-liquid separation box; the upper part of the gas-liquid separation box is installed There is an exhaust pipe with a first one-way valve, which is connected to the air filter; the lower end of the gas-liquid separation box is connected with the second pressure controller, the second solenoid valve and the second one-way valve through a pipeline equipped with The evaporative cooling chamber is connected.
本发明装置中,副冷凝器包括流通冷却水的水箱和流通冷却介质蒸气和空气混合物的冷凝管。气液分离箱中有隔离板将入口和排气口隔开。空气过滤器为一下部盛水的容器,其顶部设排气口,近底部与气液分离箱用装有第一单向阀的管道相连,底部还设有排液管和阀门。主冷凝器上还装有漏水检测仪。In the device of the present invention, the secondary condenser includes a water tank through which cooling water flows and a condensation pipe through which the mixture of cooling medium steam and air flows. There is a separation plate in the gas-liquid separation box to separate the inlet and the exhaust port. The air filter is a container for holding water in the lower part, the top is provided with an air outlet, and the near bottom is connected with the gas-liquid separation box with a pipeline equipped with a first check valve, and the bottom is also provided with a drain pipe and a valve. A leak detector is also installed on the main condenser.
本发明装置是这样工作的,当主冷凝器顶部的冷凝空间因蒸发冷却循环系统泄漏,混入空气时引起工作压力升高,当压力达到第一压力控制器设定的压力上限时,第一电磁阀打开、同时抽气泵启动。主冷凝器内空气和冷却介质气体混合物被抽气泵压送入副冷凝器,在副冷凝器中与冷却水进行热交换。冷却介质被冷凝成液体和空气一道进入气液分离箱中,空气通过第一单向阀进入空气过滤器经过滤后排入大气。流入气液分离箱的冷却液达到一定高度后被这里的第二压力控制器检测到并发出信号命令,开启第二电磁阀使冷却液流入蒸发冷却室的储液部分。由于抽气泵的运行使主冷凝器的压力降低,当达到第一压力控制器设定的压力下限时,第一电磁阀和抽气泵同时关闭,完成一次排气循环。The device of the present invention works in this way, when the condensing space on the top of the main condenser leaks due to the evaporative cooling circulation system and air is mixed in, the working pressure will rise, and when the pressure reaches the pressure upper limit set by the first pressure controller, the first electromagnetic valve will Open and the suction pump starts at the same time. The mixture of air and cooling medium gas in the main condenser is pumped into the secondary condenser by the suction pump, where it exchanges heat with the cooling water. The cooling medium is condensed into liquid and enters the gas-liquid separation box together with the air, and the air enters the air filter through the first one-way valve and is discharged into the atmosphere after being filtered. After the coolant flowing into the gas-liquid separation box reaches a certain height, it is detected by the second pressure controller here and sends a signal command to open the second solenoid valve to make the coolant flow into the liquid storage part of the evaporative cooling chamber. Since the operation of the air extraction pump reduces the pressure of the main condenser, when the pressure lower limit set by the first pressure controller is reached, the first electromagnetic valve and the air extraction pump are simultaneously closed to complete an exhaust cycle.
本发明装置在主冷凝器冷凝空间压力过高时排出气体,使其工作在设定压力状态,同时回收冷却液。这样蒸发冷却装置就真正有可能在长期运行条件下,实现冷却介质的零泄漏,达到高效经济安全的运行要求。由于通过抽气泵的运行可以控制冷凝空间压力,进而可以调节冷却介质的沸腾温度,从而为选用不同沸点、符合环保要求的冷却介质创造了条件。即通过抽气泵的运行保持冷凝器冷凝空间为负压状态,使冷却介质在摄氏50度左右沸腾,这时最适合电机冷却要求。同时,由于系统运行在负压状态下也避免了冷却液的外泄。The device of the invention discharges gas when the pressure in the condensing space of the main condenser is too high, makes it work at a set pressure state, and recovers cooling liquid at the same time. In this way, it is really possible for the evaporative cooling device to achieve zero leakage of the cooling medium under long-term operating conditions and meet the requirements of efficient, economical and safe operation. Since the pressure of the condensing space can be controlled through the operation of the air pump, the boiling temperature of the cooling medium can be adjusted, thereby creating conditions for selecting cooling mediums with different boiling points and meeting environmental protection requirements. That is, through the operation of the air pump, the condensing space of the condenser is kept in a negative pressure state, so that the cooling medium boils at about 50 degrees Celsius, which is most suitable for the cooling requirements of the motor. At the same time, since the system operates in a negative pressure state, the leakage of coolant is also avoided.
附图说明Description of drawings
图1是本发明蒸发冷却电机的冷凝器排气和冷却液回收装置的示意图。Fig. 1 is a schematic diagram of the condenser exhaust and cooling liquid recovery device of the evaporative cooling motor of the present invention.
具体实施方式Detailed ways
图1是本发明的一个实施例。蒸发冷却电机定子发热部件浸泡在蒸发冷却室70中,主冷凝器10位于蒸发冷却室70的上方。本发明装置的两端分别与主冷凝器10和蒸发冷却室70连接。Figure 1 is an embodiment of the present invention. The heat-generating parts of the stator of the evaporative cooling motor are immersed in the
主冷凝器10是一箱体,通二次冷却水的管道16贯穿箱体,箱体内部空间上部是冷凝空间12,箱体之外冷凝空间12上方连接第一压力控制器11和漏水检测仪15。本实施例中第一压力控制器11选用型号为XZY-150电接点压力真空表,它具有压力显示、压力上限和压力下限设定,所述的压力显示,压力上限、压力下限设定都有对应的接通、断开电接点。漏水检测仪15可选用中国发明专利申请01131399.4提供的。当冷却水管16有漏水时发出警报。由第一压力控制器11顺序连接第一电磁阀13、抽气泵20、副冷凝器30和气液分离箱40。气液分离箱40上部装有第一单向阀45,第一单向阀45再与空气过滤器50相连。气液分离箱40下端的管道47通过装有第二压力控制器61、第二电磁阀63、第二单向阀65的管道与蒸发冷却发室70相连,供气液分离箱40中的液体冷却介质44流回蒸发冷却室70的冷凝空间。The
在实施例中,抽气泵20选用制冷机械常用的压缩机。副冷凝器30的主体包括箱体32和装在箱体中的螺旋形冷凝管34,冷凝管34中流通空气和冷却介质蒸气的混合物,箱体32中流通冷却水,两端装有入水和出水接头。In an embodiment, the
气液分离箱40的入口管与副冷凝器30的冷凝管34的出口管相连。箱中上部空间有一弯曲的隔离板41将入口管43与排出空气连接第一单向阀45的管道隔开,下部储存经冷却液化的冷却介质44,底部有排液管47。当气液分离箱40中存储的冷却液达到一定高度时,第二压力控制器61(选用与第一压力控制器11相同的电接点压力真空表)发出信号,第二电磁阀63开启,储存的冷却液44经排液管47和第二单向阀65流进蒸发冷却室70。The inlet pipe of the gas-
空气过滤器50中盛水54,与第一单向阀45相连的进气管53装在箱体近底部位置淹没在水中,顶部有排气口51。进入空气过滤器50中的空气经水54过滤后由排气口51排出。近底部还设有排液管和阀门55,用于排出液体。
在实施例中,冷却介质选用全氟三乙胺,其分子式为(C2F5)2N,在一个标准大气压下,沸点为摄氏69度;或者用拾氟戊烷,其分子式为C5H2F10。,在一个标准大气压下,沸点为摄氏55度。In the embodiment, the cooling medium is perfluorotriethylamine, whose molecular formula is (C 2 F 5 ) 2 N, and its boiling point is 69 degrees Celsius under a standard atmospheric pressure; or sefluoropentane, whose molecular formula is C 5 H 2 F 10 . , at a standard atmospheric pressure, the boiling point is 55 degrees Celsius.
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Cited By (1)
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| CN102035307A (en) * | 2010-12-29 | 2011-04-27 | 哈尔滨电机厂有限责任公司 | Evaporative cooling system for water-wheel generator with master-slave condenser |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102035307A (en) * | 2010-12-29 | 2011-04-27 | 哈尔滨电机厂有限责任公司 | Evaporative cooling system for water-wheel generator with master-slave condenser |
| CN102035307B (en) * | 2010-12-29 | 2012-07-04 | 哈尔滨电机厂有限责任公司 | Evaporative cooling system for water-wheel generator with master-slave condenser |
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