WO2018218573A1 - 一种电厂疏水回收至除氧器的系统 - Google Patents

一种电厂疏水回收至除氧器的系统 Download PDF

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Publication number
WO2018218573A1
WO2018218573A1 PCT/CN2017/086775 CN2017086775W WO2018218573A1 WO 2018218573 A1 WO2018218573 A1 WO 2018218573A1 CN 2017086775 W CN2017086775 W CN 2017086775W WO 2018218573 A1 WO2018218573 A1 WO 2018218573A1
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Prior art keywords
valve
deaerator
pump
water
regulating valve
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PCT/CN2017/086775
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English (en)
French (fr)
Inventor
邓军
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深圳市能源环保有限公司
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Priority to PCT/CN2017/086775 priority Critical patent/WO2018218573A1/zh
Publication of WO2018218573A1 publication Critical patent/WO2018218573A1/zh

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    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22—STEAM GENERATION
    • F22D—PREHEATING, OR ACCUMULATING PREHEATED, FEED-WATER FOR STEAM GENERATION; FEED-WATER SUPPLY FOR STEAM GENERATION; CONTROLLING WATER LEVEL FOR STEAM GENERATION; AUXILIARY DEVICES FOR PROMOTING WATER CIRCULATION WITHIN STEAM BOILERS
    • F22D1/00—Feed-water heaters, i.e. economisers or like preheaters
    • F22D1/50—Feed-water heaters, i.e. economisers or like preheaters incorporating thermal de-aeration of feed-water

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  • the invention relates to a power plant hydrophobic recovery system, in particular to a system for hydrophobic recovery of a power plant to a deaerator.
  • the power plant is hydrophobically recovered to the deaerator system, including the deaerator and the demineralizer pipeline access system, the condensate pipeline route system and the hydrophobic pipeline approach system, and includes deaeration. Go to the water supply system of the pump.
  • the drain pump is started to replenish the water to the deaerator deaerator through the hydrophobic pipeline.
  • the water level of the drain tank drops to the set
  • the low position stops the drain pump operation, suspend the hydrophobic hydration.
  • the pump recovery is continued, and the cycle is repeated, and the deaerator is intermittently replenished.
  • the deaerator pressure drops sharply and the temperature also drops rapidly, which easily causes the inlet of the feed water pump to vaporize, which seriously threatens the operation of the feed water pump.
  • the deaerator pressure temperature rises to the normal operation value, which causes the pressure and temperature of the deaerator to repeatedly fluctuate, which is not conducive to stable operation.
  • the main hydration of the deaerator is through the demineralized water pipeline system, and also uses intermittent operation.
  • the demineralization pump is started to replenish water, when the deaerator water level rises to Stop the desalination pump to replenish water when setting the high position.
  • the deaerator pressure temperature also drops.
  • the hydrophobic hydration and the demineralized water are intermittent, the pressure and temperature fluctuate repeatedly during the operation of the deaerator, which is not conducive to the stable operation of the deaerator.
  • the present invention provides a system for hydrophobic recovery of a power plant to a deaerator, including a deaerator and a demineralized water supply system, a condensate pipeline, and a drain pipe connected to the deaerator.
  • the road-to-road system further includes an outward route system for the feed water pump by the deaerator;
  • the demineralized water supply system includes a de-salting valve, a pneumatic check valve front stop valve, a pneumatic control valve, which are sequentially arranged according to the water flow direction.
  • Pneumatic control valve rear stop valve, deaerator inlet check valve also includes a pneumatic regulating valve bypass manual shut-off valve connected with the pneumatic regulating valve, the pneumatic regulating valve bypasses the manual stop valve inlet and is connected before the pneumatic regulating valve Before the valve, the pneumatic regulating valve bypasses the manual shut-off valve outlet and is connected to the pneumatic regulating valve and the shut-off valve.
  • the road system includes condensed water sequentially arranged according to the direction of the water flow to manually shut off the valve and the condensed water to the deaerator inlet check valve; the drain pipe approach system includes the direction according to the water flow Hydrophobic manually set the time to the shut-off valve and check valve hydrophobic.
  • the technical solution proposed by the present invention is to provide a system for hydrophobic recovery of a power plant to a deaerator, including a deaerator and a demineralized water pipeline system and a condensate pipeline connected to the deaerator.
  • the road system and the hydrophobic pipeline approach system also include an outward route system for the feed pump by the deaerator;
  • the demineralized water supply system includes a de-salting valve sequentially arranged according to a water flow direction, a pneumatic check valve front shut-off valve, a pneumatic regulating valve, a pneumatic regulating valve rear shut-off valve, a deaerator inlet check valve, and a
  • the pneumatic regulating valve is connected to the pneumatic regulating valve to bypass the manual shut-off valve.
  • the pneumatic regulating valve bypasses the manual shut-off valve inlet and is connected to the front of the pneumatic regulating valve.
  • the pneumatic regulating valve bypasses the manual shut-off valve outlet and is connected to the pneumatic regulating valve.
  • the condensed water pipeline approach system includes condensed water sequentially arranged according to the direction of the water flow to manually shut off the valve and the condensed water to the deaerator inlet check valve;
  • the hydrophobic pipeline approach system includes a hydrophobic shut-off valve and a hydrophobic check valve according to the water flow direction;
  • the utility model is characterized in that the hydrophobic pipeline incoming circuit system is arranged before the pneumatic regulating valve, and the outlet of the hydrophobic pipeline incoming road system is connected after the demineralized water is used to check the valve, before the pneumatic regulating valve front shut-off valve is
  • the flow rate of the drain pump and the desalinated pump to the deaerator must be automatically controlled by the pneumatic regulating valve and maintain the water level of the deaerator within the set range, and the drain pump and the desalinated pump are interlocked, that is, When the drain pump starts, the desalinated pump automatically stops and the drain pump automatically starts when the drain pump stops.
  • One of the two pumps of the drain pump and the desalinated pump keeps running, and the water supply to the deaerator is continuously performed.
  • the preferred solution of the present invention is that when the water level of the water tank is qualified, when the water level reaches the set high level, the drain pump is started, and the drain system is sent to the deaerator deaerator head through the hydrophobic pipeline to be drained under the control of the pneumatic regulating valve. Maintain the deaerator water level within the set range and stop the drain pump operation when the drain tank water level drops to the set low level.
  • the desalted water is sent to the deaerator through the demineralized water pipeline under the control of the pneumatic regulating valve, and the deaerator water level is maintained within a set range.
  • the present invention provides a system for hydrophobic recovery of a power plant to a deaerator, the drain pipe system is connected to the pneumatic regulator valve, and the drain pump and the desalinated pump are hydrated to the deaerator
  • the flow rate is automatically controlled by the pneumatic regulating valve and the water level of the deaerator is maintained within the set range, and the drain pump and the desalinated pump are operated in a chain, that is, the drain pump automatically stops when the drain pump starts, and the drain pump stops.
  • the brine pump is automatically started, one of the two pumps of the drain pump and the desalinated pump keeps running. Since the water supply to the deaerator is continuously performed, the pressure and temperature of the deaerator can be effectively ensured. Make sure the system is working properly.
  • FIG. 1 is a schematic structural view of an embodiment of the prior art.
  • Figure 2 is a schematic view showing the structure of the first embodiment of the present invention.
  • FIG. 1 is a schematic structural view of an embodiment of the prior art.
  • the power plant is hydrophobically recovered to the deaerator system, including the deaerator 11 and the desalinated pipeline access system, the condensate pipeline system and the hydrophobic pipeline connected to the deaerator.
  • the road system also includes an outward system for the feed pump by the deaerator.
  • the demineralizer pipeline system, the condensate pipeline system and the hydrophobic pipeline route system are connected to the deaerator to make the water source flow into the deaerator, and the dewatering system to the feed pump is to let the water source flow out.
  • the deaerator is placed one by one to ensure that the deaerator water level is maintained within the set range.
  • the demineralized water supply system includes demineralized water arranged in sequence according to the direction of water flow to check valve 3, pneumatic regulating valve front shutoff valve 5, pneumatic regulating valve 6, pneumatic regulating valve rear shutoff valve 7, deaerator inlet
  • the check valve 8 further includes a pneumatic regulating valve bypassing the manual shut-off valve 4 connected to the pneumatic regulating valve, and the pneumatic regulating valve bypasses the manual shut-off valve 4 inlet and is connected before the pneumatic regulating valve front shut-off valve 5, next to the pneumatic regulating valve
  • the outlet of the manual shut-off valve 4 is connected to the shut-off valve 7 after the pneumatic regulating valve, when the desalination pump is started, the flow rate of the desalinated pump is automatically controlled by the pneumatic regulating valve 6.
  • the condensate line introduction system includes condensed water sequentially disposed in accordance with the direction of the water flow to manually shut off the valve 9 and the condensed water to the deaerator inlet check valve 10.
  • the hydrophobic pipe approach system includes a hydraulic shut-off valve 1 and a hydrophobic check valve 2 in accordance with the water flow direction.
  • the problem of the prior art is that, in the normal operation process, when the water level of the water tank is qualified, when the water level reaches the set high position, the water pump is started to replenish the water to the deaerator deaerator through the hydrophobic pipeline. When the water level of the water tank drops to the set low level, stop the operation of the drain pump and suspend the water supply. When the water level of the trap tank rises again to the set high level, the pump recovery is continued, so that the cycle is repeated and the water is immersed intermittently to the deaerator.
  • FIG. 2 is a schematic view showing the structure of the first embodiment of the present invention.
  • the power plant is hydrophobically recovered to the deaerator system, including the deaerator 11 and the desalinated pipeline access system and the condensate pipeline access system connected to the deaerator.
  • the drain pipe system, and the de-route system for the feed pump by the deaerator are connected to the deaerator to make the water source flow into the deaerator, and the dewatering system to the feed pump is to let the water source flow out.
  • the deaerator is placed one by one to ensure that the deaerator water level is within the set range.
  • the demineralized water supply system includes de-salting water arranged in sequence according to the direction of water flow to check valve 3, pneumatic regulating valve front shut-off valve 5, pneumatic regulating valve 6, pneumatic regulating valve rear shut-off valve 7, deaerator inlet
  • the check valve 8 further includes a pneumatic regulating valve bypassing the manual shut-off valve 4 connected to the pneumatic regulating valve, and the pneumatic regulating valve bypasses the manual shut-off valve 4 inlet and is connected before the pneumatic regulating valve front shut-off valve 5, next to the pneumatic regulating valve After the outlet of the manual shut-off valve 4 is connected to the shut-off valve 7 after the pneumatic regulating valve, when the desalination pump is started, the flow rate of the desalinated pump is automatically controlled by the pneumatic regulating valve 6.
  • the condensate line introduction system includes condensed water sequentially disposed in accordance with the direction of the water flow to manually shut off the valve 9 and the condensed water to the deaerator inlet check valve 10.
  • the hydrophobic pipeline approach system includes a hydraulic shut-off valve 1 and a hydrophobic check valve 2 in accordance with the water flow direction.
  • the drain line approach system is placed before the pneumatic regulator valve 6, and the outlet of the drain line approach system is connected to the demineralized water to check valve 3.
  • the flow rate of the drain pump and the desalinated pump to the deaerator is automatically controlled by the pneumatic regulating valve 6 and the water level of the deaerator 11 is maintained within the set range, and the drain pump,
  • the demineralized water pump is interlocked, that is, when the drain pump is automatically stopped when the drain pump is started, the desalination pump is automatically started when the drain pump is stopped, and one of the two pumps of the drain pump and the desalinated pump is kept running.
  • the hydration of the deaerator is continuous. Since the hydration to the deaerator is continuously performed, the deaerator pressure and temperature are effectively ensured to ensure the normal operation of the system.
  • the drain pump starts, and the drain system delivers water to the deaerator deaerator through the hydrophobic pipeline, and maintains the control under the control of the pneumatic regulating valve.
  • the oxygen level is in the set range, and the drain pump stops when the water level of the tank drops to the set low level.
  • the desalted water is sent to the deaerator through the demineralized water pipeline under the control of the pneumatic regulating valve, and the deaerator water level is maintained within the set range.

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
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Abstract

一种电厂疏水回收至除氧器的系统，包括除氧器 (11)以及接入除氧器 (11)的除盐水管路来路系统、凝结水管路来路系统和疏水管路来路系统，还包括由除氧器 (11)去给水泵的去路系统，其特征是，所述疏水管路来路系统设置在所述气动调节阀 (6)之前，所述疏水管路来路系统的出口接入在除盐水来逆止阀 (3)之后、气动调节阀前截止阀 (5)之前，疏水泵和除盐水泵向除氧器 (11)补水时的流量都必须经过气动调节阀 (6)自动控制并维持除氧器 (11)的水位在设定范围内，并且疏水泵、除盐水泵两者是连锁运行的，即疏水泵启动时除盐水泵自动停止、疏水泵停止时除盐水泵自动启动，由于向除氧器 (11)的补水是连续进行的，因此可以有效确保除氧器 (11)压力和温度的稳定，确保系统正常运行。

Description

一种电厂疏水回收至除氧器的系统 技术领域
本发明涉及电厂疏水回收系统，尤其涉及一种电厂疏水回收至除氧器的系统。
背景技术
现今，随着环保要求的进一步提高和节能减排的需要，电厂需要对疏水进行回收。目前，电厂疏水回收至除氧器的系统，包括除氧器以及接入除氧器的除盐水管路来路系统、凝结水管路来路系统和疏水管路来路系统，还包括由除氧器去给水泵的去路系统。
在正常运行过程中，当疏水箱水质化验合格后，水位达到设定的高位时，启动疏水泵通过疏水管路来路系统向除氧器除氧头补水回收，当疏水箱水位下降到设定的低位时停止疏水泵运行，暂停疏水补水。等疏水箱水位再度上升到设定高位时继续启泵回收，如此循环反复，间断性地向除氧器进行补水。由于当疏水回收时，因回收流量大且疏水温度低，造成除氧器压力急剧下降，温度也下降较快，容易造成给水泵进口气化，严重威胁到给水泵的运行。而当停止疏水补水时，除氧器压力温度上升到正常运行值，这样造成除氧器运行中压力、温度反复波动，不利于稳定运行。
另一方面，除氧器主要补水是通过除盐水管路来路系统，也采用间断性运行，当除氧器水位下降到设定低位时，启动除盐水泵补水，当除氧器水位上升到设定高位时停止除盐水泵补水。用除盐水补水时，也造成除氧器压力温度下降。
因此，由于疏水补水和除盐水补水都是间断性的，导致除氧器运行中压力、温度反复波动，不利于除氧器稳定运行。
发明内容
为了解决现有技术问题，本发明提出一种电厂疏水回收至除氧器的系统，包括除氧器以及接入除氧器的除盐水管路来路系统、凝结水管路来路系统和疏水管路来路系统，还包括由除氧器去给水泵的去路系统；所述除盐水来路系统包括依据水流方向依次设置的除盐水来逆止阀、气动调节阀前截止阀、气动调节阀、气动调节阀后截止阀、除氧器入口逆止阀，还包括与气动调节阀并接的气动调节阀旁路手动截止阀，气动调节阀旁路手动截止阀入口并接在气动调节阀前截止阀之前，气动调节阀旁路手动截止阀出口并接在气动调节阀后截止阀之后，当启动除盐水泵时，除盐水泵的流量由所述气动调节阀自动控制；所述凝结水管路来路系统包括依据水流方向依次设置的凝结水来手动截止阀和凝结水至除氧器入口逆止阀；所述疏水管路来路系统包括依据水流方向依次设置的疏水来手动截止阀和疏水来逆止阀。
本发明解决技术问题所提出的技术方案是，本发明提出一种电厂疏水回收至除氧器的系统，包括除氧器以及接入除氧器的除盐水管路来路系统、凝结水管路来路系统和疏水管路来路系统，还包括由除氧器去给水泵的去路系统；
所述除盐水来路系统包括依据水流方向依次设置的除盐水来逆止阀、气动调节阀前截止阀、气动调节阀、气动调节阀后截止阀、除氧器入口逆止阀，还包括与气动调节阀并接的气动调节阀旁路手动截止阀，气动调节阀旁路手动截止阀入口并接在气动调节阀前截止阀之前，气动调节阀旁路手动截止阀出口并接在气动调节阀后截止阀之后，当启动除盐水泵时，除盐水泵的流量由所述气动调节阀自动控制；
所述凝结水管路来路系统包括依据水流方向依次设置的凝结水来手动截止阀和凝结水至除氧器入口逆止阀；
所述疏水管路来路系统包括依据水流方向依次设置的疏水来手动截止阀和疏水来逆止阀；
其特征是，所述疏水管路来路系统设置在所述气动调节阀之前，所述疏水管路来路系统的出口接入在除盐水来逆止阀之后、气动调节阀前截止阀之前，疏水泵和除盐水泵向除氧器补水时的流量都必须经过气动调节阀自动控制并维持除氧器的水位在设定范围内，并且疏水泵、除盐水泵两者是连锁运行的，即疏水泵启动时除盐水泵自动停止、疏水泵停止时除盐水泵自动启动，疏水泵、除盐水泵两台泵之中总有一台泵保持运行，向除氧器的补水是连续进行的。
本发明优选方案是，当疏水箱水质化验合格后，水位达到设定的高位时，疏水泵启动，通过疏水管路来路系统向除氧器除氧头输送疏水，在气动调节阀的控制下维持除氧器水位在设定范围，当疏水箱水位下降到设定的低位时停止疏水泵运行。
本发明优选方案是，当除盐水泵运行时，在气动调节阀的控制下通过除盐水管路来路系统向除氧器输送除盐水，并维持除氧器水位在设定范围。
本发明的有益效果：本发明提出一种电厂疏水回收至除氧器的系统，所述疏水管路来路系统接在所述气动调节阀之前，疏水泵和除盐水泵向除氧器补水时的流量都经过气动调节阀自动控制并维持除氧器的水位在设定范围内，并且疏水泵、除盐水泵两者是连锁运行的，即疏水泵启动时除盐水泵自动停止、疏水泵停止时除盐水泵自动启动，疏水泵、除盐水泵两台泵之中总有一台泵保持运行，由于向除氧器的补水是连续进行的，因此可以有效确保除氧器压力和温度的稳定，确保系统正常运行。
附图说明：
图1为现有技术一个实施例的结构示意图。
图2为本发明提出的第一个实施例的结构示意图。
图中，
1.疏水来手动截止阀；
2.疏水来逆止阀；
3.除盐水来逆止阀；
4.气动调节阀旁路手动截止阀；
5.气动调节阀前截止阀
6.气动调节阀；
7.气动调节阀后截止阀；
8.除氧器入口逆止阀；
9.凝结水来手动截止阀；
10.凝结水至除氧器入口逆止阀；
11.除氧器；
11.1排气阀。
具体实施方式
图1为现有技术一个实施例的结构示意图。图中显示，现有技术中，电厂疏水回收至除氧器的系统，包括除氧器11以及接入除氧器的除盐水管路来路系统、凝结水管路来路系统和疏水管路来路系统，还包括由除氧器去给水泵的去路系统。接入除氧器的除盐水管路来路系统、凝结水管路来路系统和疏水管路来路系统等管路系统使水源流入除氧器，而去给水泵的去路系统则是使水源流出除氧器，一入一出确保除氧器水位维持在设定的范围内。
图1中显示，除盐水来路系统包括依据水流方向依次设置的除盐水来逆止阀3、气动调节阀前截止阀5、气动调节阀6、气动调节阀后截止阀7、除氧器入口逆止阀8，还包括与气动调节阀并接的气动调节阀旁路手动截止阀4，气动调节阀旁路手动截止阀4入口并接在气动调节阀前截止阀5之前，气动调节阀旁路手动截止阀4出口并接在气动调节阀后截止阀7之后，当启动除盐水泵时，除盐水泵的流量由气动调节阀6自动控制。
图1中显示，凝结水管路来路系统包括依据水流方向依次设置的凝结水来手动截止阀9和凝结水至除氧器入口逆止阀10。
图1中显示，疏水管路来路系统包括依据水流方向依次设置的疏水来手动截止阀1和疏水来逆止阀2。
关键问题在于：现有技术中，疏水管路来路系统是直接接入到除氧器11中，疏水泵运行时直接向除氧器11补水而没有经过气动调节阀的流量控制。因此，现有技术的问题是，在正常运行过程中，当疏水箱水质化验合格后，水位达到设定的高位时，启动疏水泵通过疏水管路来路系统向除氧器除氧头补水回收，当疏水箱水位下降到设定的低位时停止疏水泵运行，暂停补水。等疏水箱水位再度上升到设定高位时继续启泵回收，如此循环反复，间断性向除氧器补水方式。由于当疏水回收时，因回收流量大且疏水温度低，造成除氧器压力急剧下降，温度也下降较快，容易造成给水泵进口气化，严重威胁到给水泵的运行。而当停止疏水补水时，除氧器压力温度上升到正常运行值，这样造成除氧器运行中压力、温度反 复波动，不利于稳定运行。
图2为本发明提出的第一个实施例的结构示意图。图中显示，与现有技术一样，本例中，电厂疏水回收至除氧器的系统，包括除氧器11以及接入除氧器的除盐水管路来路系统、凝结水管路来路系统和疏水管路来路系统，还包括由除氧器去给水泵的去路系统。接入除氧器的除盐水管路来路系统、凝结水管路来路系统和疏水管路来路系统等管路系统使水源流入除氧器，而去给水泵的去路系统则是使水源流出除氧器，一入一出确保除氧器水位在设定的范围内。
图2中显示，除盐水来路系统包括依据水流方向依次设置的除盐水来逆止阀3、气动调节阀前截止阀5、气动调节阀6、气动调节阀后截止阀7、除氧器入口逆止阀8，还包括与气动调节阀并接的气动调节阀旁路手动截止阀4，气动调节阀旁路手动截止阀4入口并接在气动调节阀前截止阀5之前，气动调节阀旁路手动截止阀4出口并接在气动调节阀后截止阀7之后，当启动除盐水泵时，除盐水泵的流量由气动调节阀6自动控制。
图2中显示，凝结水管路来路系统包括依据水流方向依次设置的凝结水来手动截止阀9和凝结水至除氧器入口逆止阀10。
图2中显示，疏水管路来路系统包括依据水流方向依次设置的疏水来手动截止阀1和疏水来逆止阀2。
图2中显示，与现有技术不同的是，本例中，疏水管路来路系统设置在气动调节阀6之前，疏水管路来路系统的出口接入在除盐水来逆止阀3之后、气动调节阀前截止阀5之前，疏水泵和除盐水泵向除氧器补水时的流量都经过气动调节阀6自动控制并维持除氧器11的水位在设定范围内，并且疏水泵、除盐水泵两者是连锁运行的，即疏水泵启动时除盐水泵自动停止、疏水泵停止时除盐水泵自动启动，疏水泵、除盐水泵两台泵之中总有一台泵保持运行，向除氧器的补水是连续进行的。由于向除氧器的补水是连续进行的，有效地确保除氧器压力和温度的稳定，确保系统正常运行。
本例中，当疏水箱水质化验合格后，水位达到设定的高位时，疏水泵启动，通过疏水管路来路系统向除氧器除氧头输送疏水，在气动调节阀的控制下维持除氧器水位在设定范围，当疏水箱水位下降到设定的低位时停止疏水泵运行。
本例中，当除盐水泵运行时，在气动调节阀的控制下通过除盐水管路来路系统向除氧器输送除盐水，并维持除氧器水位在设定范围。

Claims (3)

  1. 一种电厂疏水回收至除氧器的系统，包括除氧器以及接入除氧器的除盐水管路来路系统、凝结水管路来路系统和疏水管路来路系统，还包括由除氧器去给水泵的去路系统；
    所述除盐水来路系统包括依据水流方向依次设置的除盐水来逆止阀、气动调节阀前截止阀、气动调节阀、气动调节阀后截止阀、除氧器入口逆止阀，还包括与气动调节阀并接的气动调节阀旁路手动截止阀，气动调节阀旁路手动截止阀入口并接在气动调节阀前截止阀之前，气动调节阀旁路手动截止阀出口并接在气动调节阀后截止阀之后，当启动除盐水泵时，除盐水泵的流量由所述气动调节阀自动控制；
    所述凝结水管路来路系统包括依据水流方向依次设置的凝结水来手动截止阀和凝结水至除氧器入口逆止阀；
    所述疏水管路来路系统包括依据水流方向依次设置的疏水来手动截止阀和疏水来逆止阀；
    其特征是，所述疏水管路来路系统设置在所述气动调节阀之前，所述疏水管路来路系统的出口接入在除盐水来逆止阀之后、气动调节阀前截止阀之前，疏水泵和除盐水泵向除氧器补水时的流量都必须经过气动调节阀自动控制并维持除氧器的水位在设定范围内，并且疏水泵、除盐水泵两者是连锁运行的，即疏水泵启动时除盐水泵自动停止、疏水泵停止时除盐水泵自动启动，疏水泵、除盐水泵两台泵之中总有一台泵保持运行，向除氧器的补水是连续进行的。
  2. 根据权利要求1所述的一种电厂疏水回收至除氧器的系统，其特征是，当疏水箱水质化验合格后，水位达到设定的高位时，疏水泵启动，通过疏水管路来路系统向除氧器除氧头输送疏水，在气动调节阀的控制下维持除氧器水位在设定范围，当疏水箱水位下降到设定的低位时停止疏水泵运行。
  3. 根据权利要求1所述的一种电厂疏水回收至除氧器的系统，其特征是，当除盐水泵运行时，在气动调节阀的控制下通过除盐水管路来路系统向除氧器输送除盐水，并维持除氧器水位在设定范围。
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Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004170027A (ja) * 2002-11-21 2004-06-17 Mitsubishi Heavy Ind Ltd 脱気システム
CN203478197U (zh) * 2013-09-25 2014-03-12 济南澳海炭素有限公司 余热发电除氧器排汽回收加热装置
CN205655278U (zh) * 2016-05-16 2016-10-19 中国华电科工集团有限公司 一种应用于电站的锅炉启动上水系统
CN205918455U (zh) * 2016-07-11 2017-02-01 合肥天源热电有限公司 一种热电厂疏水回收系统装置
CN106996557A (zh) * 2017-06-01 2017-08-01 深圳市能源环保有限公司 一种电厂疏水回收至除氧器的系统

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004170027A (ja) * 2002-11-21 2004-06-17 Mitsubishi Heavy Ind Ltd 脱気システム
CN203478197U (zh) * 2013-09-25 2014-03-12 济南澳海炭素有限公司 余热发电除氧器排汽回收加热装置
CN205655278U (zh) * 2016-05-16 2016-10-19 中国华电科工集团有限公司 一种应用于电站的锅炉启动上水系统
CN205918455U (zh) * 2016-07-11 2017-02-01 合肥天源热电有限公司 一种热电厂疏水回收系统装置
CN106996557A (zh) * 2017-06-01 2017-08-01 深圳市能源环保有限公司 一种电厂疏水回收至除氧器的系统

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