CN104235870A - Condenser dead steam waste heat recovery and energy saving device and energy saving method - Google Patents

Condenser dead steam waste heat recovery and energy saving device and energy saving method Download PDF

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CN104235870A
CN104235870A CN201410518220.3A CN201410518220A CN104235870A CN 104235870 A CN104235870 A CN 104235870A CN 201410518220 A CN201410518220 A CN 201410518220A CN 104235870 A CN104235870 A CN 104235870A
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冯留建
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Abstract

凝汽器乏汽余热回收节能装置,包括电厂汽轮机排气口通过电厂冷却系统进行冷却,其特征是携带乏汽余热的循环水经循环水泵送往冷却塔,在循环水泵出口母管上连接支路,将要送至冷却塔的循环水一部分经循环水支路引至锅炉中间的一次风机和送风机入口处,在该处建立与循环水相连的小型间冷塔;一次风机、送风机入口设置在小型间冷塔上部,风机运行在上部形成负压,空气从小型间冷塔底部进入,跟小型间冷塔换热后形成热空气,风机将热空气送入炉膛,部分回收乏汽余热;经小型间冷塔冷却后的循环水连接至凝汽器进水母管,继续送入凝汽器,吸收凝汽器内乏汽余热,从而完成整个乏汽余热回收过程。

Condenser waste steam waste heat recovery energy-saving device, including power plant steam turbine exhaust port is cooled by the power plant cooling system, it is characterized in that the circulating water carrying waste steam heat is sent to the cooling tower through the circulating water pump, and the outlet main pipe of the circulating water pump is connected to the branch A part of the circulating water that will be sent to the cooling tower is led to the inlet of the primary fan and the blower in the middle of the boiler through the circulating water branch, where a small intercooling tower connected with the circulating water is established; the inlet of the primary fan and the blower are set in a small On the upper part of the intercooling tower, the fan runs on the upper part to form a negative pressure. The air enters from the bottom of the small intercooling tower, and after heat exchange with the small intercooling tower, hot air is formed. The fan sends the hot air into the furnace, and part of the waste heat is recovered; The circulating water cooled by the intercooling tower is connected to the water inlet pipe of the condenser, and then sent to the condenser to absorb the waste heat of the exhaust steam in the condenser, thereby completing the entire recovery process of exhaust steam and waste heat.

Description

凝汽器乏汽余热回收节能装置及节能方法Energy-saving device and energy-saving method for recovering waste heat from exhausted steam in condenser

技术领域 technical field

本发明涉及一种利用凝汽器乏汽余热回收的节能装置及节能方法,具体涉及到火力发电厂凝汽器冷却循环水系统和锅炉风烟系统。 The invention relates to an energy-saving device and an energy-saving method for recovering waste heat from exhaust steam of a condenser, in particular to a condenser cooling circulating water system and a boiler air-smoke system in a thermal power plant.

背景技术 Background technique

火力发电厂在发电过程中,蒸汽经汽轮机做功后的乏汽,排入凝汽器中冷凝放热,这部分冷凝热被循环水带到冷却塔直接排向大气,排放热量一般占到输入总能量的15%以上,造成了巨大的能源浪费,如何将这些排向大气的余热利用起来是当今热力发电厂难题。 During the power generation process of a thermal power plant, the exhausted steam after the steam turbine has done work is discharged into the condenser to condense and release heat. This part of the condensation heat is brought to the cooling tower by the circulating water and directly discharged to the atmosphere. The discharged heat generally accounts for the total input. More than 15% of the energy has caused a huge waste of energy. How to utilize the waste heat discharged to the atmosphere is a difficult problem for thermal power plants today.

发明内容 Contents of the invention

本发明的主要解决的技术问题是提供一种从凝汽器冷却循环水回收凝汽器乏汽余热的节能装置和节能方法,该节能装置及节能方法是将凝汽器循环水系统及风烟系统进行相应的改造,将原本要排向大气的热量经风烟系统送入炉膛,回收部分乏汽余热,从而提高电厂的综合热效率,降低发电煤耗,且多台机组可公用一个小间冷塔,在成本不增加的前提下可使节能效果翻倍。 The main technical problem to be solved by the present invention is to provide an energy-saving device and an energy-saving method for recovering the exhaust heat of the condenser from the cooling circulating water of the condenser. The system is modified accordingly, and the heat originally to be exhausted to the atmosphere is sent into the furnace through the wind and smoke system, and part of the exhaust heat is recovered, so as to improve the comprehensive thermal efficiency of the power plant and reduce the coal consumption of power generation, and multiple units can share a small cooling tower , on the premise of no increase in cost, the energy-saving effect can be doubled.

为解决上述问题,本发明的技术方案如下:凝汽器乏汽余热回收节能装置,包括电厂汽轮机排气口通过电厂循环冷却水系统进行冷却,携带乏汽余热的循环水经循环水泵送往冷却塔,在循环水泵出口母管上连接支路,将要送至冷却塔的一部分循环水经该支路引至锅炉一次风机和送风机入口处,在该处建立与循环水相连的小型间冷塔(换热装置);锅炉的一次风、二次风入口设置在小型间冷塔上部,风机运行在上部形成负压,空气从小型间冷塔底部进入,跟小间冷塔内部翅片换热后形成热空气,风机将热空气送入炉膛,从而回收部分乏汽余热,经小型间冷塔冷却后的水连接至循环水回水母管,从而完成整个乏汽余热回收过程; In order to solve the above-mentioned problems, the technical solution of the present invention is as follows: the energy-saving device for recovering exhaust steam and waste heat of the condenser, including the steam turbine exhaust port of the power plant is cooled by the circulating cooling water system of the power plant, and the circulating water carrying the exhaust steam and waste heat is sent to the cooling system through the circulating water pump. A branch is connected to the outlet main pipe of the circulating water pump, and a part of the circulating water to be sent to the cooling tower is led to the boiler primary fan and the inlet of the blower through the branch, where a small intercooling tower connected to the circulating water is established ( Heat exchange device); the primary air and secondary air inlets of the boiler are set on the upper part of the small intercooling tower, and the fan runs on the upper part to form a negative pressure. The air enters from the bottom of the small intercooling tower and exchanges heat with the internal fins of the small intercooling tower. The hot air is formed, and the fan sends the hot air into the furnace to recover part of the waste heat of the exhaust steam. The water cooled by the small intercooling tower is connected to the circulating water return jellyfish pipe, thereby completing the entire exhaust steam waste heat recovery process;

利用上述节能装置实现节能的方法包括以下步骤: The method for realizing energy saving by using the above-mentioned energy-saving device comprises the following steps:

1)夏季运行时,直接将携带凝结热的部分循环水经支路自动液压流量调节装置送至小型间冷塔,一次风机、送风机运行吸取换热后的热空气,并将之送入炉膛,实现余热回收;一次风机和送风机冷却部分循环水使循环水温度下降,提高凝汽器真空,实现机组效率提高; 1) During summer operation, part of the circulating water carrying condensation heat is directly sent to the small intercooling tower through the branch automatic hydraulic flow adjustment device, and the primary fan and blower operate to absorb the hot air after heat exchange and send it into the furnace. Realize waste heat recovery; the primary fan and blower cool part of the circulating water to lower the temperature of the circulating water, increase the vacuum of the condenser, and improve the efficiency of the unit;

2)冬季运行时,电厂汽轮机在确保安全的前提下,适度提高电厂汽轮机运行背压的压力,从而提高电厂汽轮机的乏汽在凝汽器中的凝结温度,满足小型间冷塔回水温度在40℃以上,防止小型间冷塔冻裂,在保证机组的安全运行的前提下,一次风机、送风机风运行吸取换热后的热空气将其送入炉膛,实现余热回收; 2) During winter operation, under the premise of ensuring safety, the power plant steam turbine moderately increases the operating back pressure of the power plant steam turbine, thereby increasing the condensation temperature of the exhaust steam of the power plant steam turbine in the condenser to meet the return water temperature of the small intercooling tower. Above 40 ℃, to prevent the small intercooling tower from freezing and cracking. Under the premise of ensuring the safe operation of the unit, the primary fan and blower will absorb the hot air after heat exchange and send it into the furnace to realize waste heat recovery;

3)利用上述节能装置对火电厂凝汽器乏汽余热进行回收及相应的节能方法,夏季、冬季均可提高送风温度,回收余热,提高了锅炉的燃烧效率,达到节能降耗的目的,相对而言夏季可以适当降低循环水温度,提高凝汽器真空,提高汽轮机组热效率,冬季则大幅度提高送风温度,尤其是相对与北方寒冷地区,其乏汽余热回收效果更好,同时提高冬季锅炉内的燃烧效率。 3) Using the above-mentioned energy-saving device to recover the waste heat of exhaust steam in the condenser of the thermal power plant and the corresponding energy-saving method, the temperature of the air supply can be increased in summer and winter, and the waste heat can be recovered, which improves the combustion efficiency of the boiler and achieves the purpose of saving energy and reducing consumption. Relatively speaking, in summer, the circulating water temperature can be appropriately reduced, the vacuum of the condenser can be increased, and the thermal efficiency of the steam turbine unit can be improved. Combustion efficiency in winter boilers.

凝汽器乏汽余热回收节能装置的投入和使用,在提高机组效率的前提下,同时可以代替一次风暖风器、二次风暖风器等装置,节约投资成本。 The investment and use of the exhaust steam waste heat recovery energy-saving device of the condenser can replace the primary air heater, secondary air heater and other devices under the premise of improving the efficiency of the unit, saving investment costs.

对于两台机组来说,可以共用一个小型间冷塔,从而节约建造成本。  For two units, a small intercooling tower can be shared to save construction cost. the

乏汽余热回收节能装置可以独立设置,即在凝汽器中设置独立的换热装置,吸收凝汽器乏汽余热,循环水泵循将携带乏汽余热的水送至小间冷塔进行换热,换热后的水进入凝汽器吸收凝汽器乏汽余热,形成完整循环。 The energy-saving device for waste heat recovery of exhaust steam can be installed independently, that is, an independent heat exchange device is installed in the condenser to absorb the waste heat of exhaust steam in the condenser, and the circulating water pump will send the water carrying waste heat of exhaust steam to the small cooling tower for heat exchange , the water after heat exchange enters the condenser to absorb the exhaust heat of the condenser, forming a complete cycle.

附图说明 Description of drawings

图1为凝汽器乏汽余热回收装置系统实施示意图。 Figure 1 is a schematic diagram of the implementation of the exhaust steam waste heat recovery system of the condenser.

图2为凝汽器乏汽余热回收装置系统循环水系统单独布置示意图。 Figure 2 is a schematic diagram of the separate layout of the circulating water system of the exhaust steam waste heat recovery device system of the condenser.

图1中1为低压缸,2凝汽器,3为循环水泵,4为循环水泵出口母管,5为冷却塔,6为凝汽器进水母管,7为自动液压流量调节装置,8为小间冷塔,9为一次风机,10为送风机,11为锅炉。 In Figure 1, 1 is the low-pressure cylinder, 2 is the condenser, 3 is the circulating water pump, 4 is the outlet main pipe of the circulating water pump, 5 is the cooling tower, 6 is the water inlet pipe of the condenser, 7 is the automatic hydraulic flow adjustment device, 8 is Small cooling tower, 9 is a fan, 10 is a blower, and 11 is a boiler.

图2中1为低压缸,2凝汽器,3为循环水泵,4为循环水泵出口母管,5为冷却塔,6为凝汽器进水母管,7为自动液压流量调节装置,8为循环水泵,9为小间冷塔,10为送风机,11为一次风机,12为锅炉。 In Figure 2, 1 is the low-pressure cylinder, 2 is the condenser, 3 is the circulating water pump, 4 is the outlet main pipe of the circulating water pump, 5 is the cooling tower, 6 is the water inlet pipe of the condenser, 7 is the automatic hydraulic flow adjustment device, 8 is Circulating water pump, 9 is a small cooling tower, 10 is a blower fan, 11 is a primary fan, and 12 is a boiler.

具体实施方式 Detailed ways

小间冷塔循环水接自冷却塔循环水,如图1所示低压缸1排出的乏汽经循环水冷却后,凝结成液体,在凝汽器2内建立真空环境,循环水泵3将携带乏汽余热的水送至循环水出口母管4,在循环水出口母管4出一部分送至冷却塔5,一部分经自动液压流量调节装置7送至小间冷塔8;经冷却塔5冷却后的循环水送至凝汽器2,继续循环冷却,保持凝汽器真空;送至小间冷塔8的循环水经小间冷塔8冷却后送至凝汽器进水母管6,一次风机9风道及入口送风机10风道入口设置在小间冷塔8上部,一次风机9和送风机10运行在其入口风道出形成负压,将环境风从底部间冷管道吸入,从而实现冷却循环水,提高入口风温的目的,经风机的作用将其送入炉膛,实现热电厂运行效率的提高。 The circulating water of the small cooling tower is connected to the circulating water of the cooling tower. As shown in Figure 1, the exhausted steam discharged from the low-pressure cylinder 1 is cooled by the circulating water and condenses into a liquid. A vacuum environment is established in the condenser 2, and the circulating water pump 3 will carry The water with exhausted steam and waste heat is sent to the circulating water outlet main pipe 4, and a part of the circulating water outlet main pipe 4 is sent to the cooling tower 5, and a part is sent to the small cooling tower 8 through the automatic hydraulic flow adjustment device 7; it is cooled by the cooling tower 5 The final circulating water is sent to the condenser 2 to continue circulating cooling to keep the condenser vacuum; the circulating water sent to the small cooling tower 8 is cooled by the small cooling tower 8 and then sent to the condenser inlet pipe 6, once The air duct of the fan 9 and the inlet of the air supply fan 10 are set on the upper part of the small cooling tower 8, and the primary fan 9 and the air supply fan 10 run in the inlet air duct to form a negative pressure, and the ambient air is sucked in from the bottom intercooling pipe, thereby realizing cooling The purpose of circulating water to increase the inlet air temperature is to send it into the furnace through the action of the fan, so as to realize the improvement of the operation efficiency of the thermal power plant.

小间冷塔循环水单独布置,如图2所示将换热装置设置在凝汽器2上部,用以吸收低压缸1排出的乏汽余热,经自动液压流量调节装置7调节后,送至小间冷塔9,经循环水泵8加压后形成整个乏汽余热回收循环,其余的余热由原循环水冷却系统进行冷却。 The circulating water of the small cooling tower is arranged separately. As shown in Figure 2, the heat exchange device is arranged on the upper part of the condenser 2 to absorb the waste heat of exhausted steam discharged from the low-pressure cylinder 1. After being adjusted by the automatic hydraulic flow adjustment device 7, it is sent to The small cooling tower 9 is pressurized by the circulating water pump 8 to form the entire waste steam waste heat recovery cycle, and the rest of the waste heat is cooled by the original circulating water cooling system.

采用凝汽器乏汽余热回收节能装置的节能效果如下,以一台300MW抽凝机组为例,机组年利用小时数以5012小时(电监会2013年全国区域统调常规燃煤发电机组6000千瓦及以上电厂发电设备平均利用小时数)计算,一次风、二次风总风量以进风量1200 t/h计算: The energy-saving effect of adopting the exhaust steam waste heat recovery energy-saving device of the condenser is as follows. Taking a 300MW condensing unit as an example, the annual utilization hours of the unit are 5012 hours (the Electric Regulatory Commission in 2013 the national regional unified adjustment of conventional coal-fired generating units of 6000 kilowatts and the average utilization hours of power generation equipment in power plants above), and the total air volume of primary air and secondary air is calculated with an air intake of 1200 t/h:

1)采用本发明技术改造后,对于间接冷却系统(间接冷却塔)、直接空冷系统(空冷岛),夏季一般可提高一次风、二次风入口风温20℃,小间冷塔的冷却方式属于强制风冷,增加散热面积,在夏季运行时可降低循环水温度,提高凝汽器真空,其所带来的效益基本上可以和小间冷塔带来的延程阻力相抵,冬季一般可提高一次风、二次风入口风温可提高40℃,春秋季一般可提高一次风、二次风入口风温30℃;夏季,对于湿式冷却塔系统,循环水温度与环境温度差在8-15摄氏度,温差较小,可回收热量较少,可根据实际情况决定是否停运,秋冬季回收效果则与间接冷却系统和直接空冷系统相差不大; 1) After adopting the technical transformation of the present invention, for the indirect cooling system (indirect cooling tower) and the direct air cooling system (air cooling island), the primary air and secondary air inlet air temperature can generally be increased by 20°C in summer, and the cooling method of the small cooling tower It belongs to forced air cooling, which increases the heat dissipation area. It can reduce the circulating water temperature and increase the vacuum of the condenser during summer operation. The benefits brought by it can basically be offset by the extension resistance brought by the small cooling tower. Generally, it can be used in winter. The air temperature at the inlet of primary air and secondary air can be increased by 40°C. Generally, the air temperature at the inlet of primary air and secondary air can be increased by 30°C in spring and autumn; in summer, for the wet cooling tower system, the temperature difference between circulating water and ambient temperature is 8- 15 degrees Celsius, the temperature difference is small, and the recoverable heat is less. It can be decided whether to stop operation according to the actual situation. The recovery effect in autumn and winter is not much different from that of the indirect cooling system and the direct air cooling system;

2)经上述所述的节能装置,对于间接冷却系统(间接冷却塔)、直接空冷系统(空冷岛),夏季每小时经一次风、二次风可回收凝汽器乏汽余热约24000 MJ,夏季一季度(按年利用小时数平均分配到四季)可回收凝汽器乏汽余热约30072000 MJ,相当于节约1026吨标准煤;春秋季每小时经一次风、二次风可回收凝汽器乏汽余热约36000 MJ,春、秋两季度可回收凝汽器乏汽余热约90216000 MJ,相当于节约3079吨标准煤;冬季每小时可回收凝汽器乏汽余热约48000 MJ,冬季一季度可回收凝汽器乏汽余热约60144000 MJ,相当于节约2052吨标准煤,合计每台30万机组每年可节约6157吨标准煤;如果是湿式冷却塔系统,则夏季余热回收效果相对较差,而对于我国北部如新疆等地区冬天较长,且因缺水大多采用间接空冷和直接空冷系统的机组,其节能效果更好; 2) With the energy-saving device mentioned above, for the indirect cooling system (indirect cooling tower) and the direct air cooling system (air cooling island), about 24000 MJ of exhaust heat of the condenser can be recovered by the primary air and secondary air every hour in summer, In the first quarter of summer (evenly distributed to the four seasons according to the annual utilization hours), about 30,072,000 MJ of waste steam waste heat of the condenser can be recovered, which is equivalent to saving 1,026 tons of standard coal; the condenser can be recovered by primary air and secondary air every hour in spring and autumn The exhaust steam waste heat is about 36000 MJ, and the exhaust steam waste heat of the condenser can be recovered about 90216000 MJ in spring and autumn, which is equivalent to saving 3079 tons of standard coal; the exhaust steam waste heat of the condenser can be recovered every hour in winter. About 60,144,000 MJ of waste steam waste heat can be recovered from the condenser, which is equivalent to saving 2,052 tons of standard coal, and a total of 6,157 tons of standard coal can be saved per 300,000 units per year; if it is a wet cooling tower system, the waste heat recovery effect in summer is relatively poor. For the northern part of China, such as Xinjiang, where the winter is long, and most of the units that use indirect air-cooling and direct air-cooling systems due to lack of water, the energy-saving effect is better;

3)如上所述的节能装置,两台机组公用一个小间冷塔则在成本不增加的情况下,则节能效果及节能收益翻倍; 3) For the energy-saving device mentioned above, if the two units share a small cooling tower, the energy-saving effect and energy-saving benefits will be doubled without increasing the cost;

4)如上所述的节能装置,可以减少一次风暖风器、二次风暖风器设备的安装和使用。 4) The above-mentioned energy-saving device can reduce the installation and use of primary air heaters and secondary air heaters.

如上所述的小间冷塔,其布置方式只需有相应的间冷管束,其布置方式可以有多种形式,如直接将循环水管道引至风机入口,将循环水换热管束布置在相应风机入口,起到代替暖风器的作用,也可以是仅有底部换热翅片的小型间冷塔。 As mentioned above, the small intercooling tower only needs to have corresponding indirect cooling tube bundles in its layout, and its layout can be in various forms, such as directly leading the circulating water pipe to the fan inlet, and arranging the circulating water heat exchange tube bundle in the corresponding The inlet of the fan plays the role of replacing the heater, and it can also be a small intercooling tower with only bottom heat exchange fins.

综上所述,本发明可带来巨大的企业经济效益、环境效益。 In summary, the present invention can bring huge economic and environmental benefits to the enterprise.

Claims (5)

1.凝汽器乏汽余热回收节能装置,包括凝汽器乏汽余热回收装置与冷却循环水支路直接相连及凝汽器乏汽余热回收装置独立设置两个方案;对于凝汽器乏汽余热回收装置与冷却循环水支路直接相连,则包括电厂汽轮机排气口通过电厂冷却系统进行冷却,其特征是携带冷凝热的循环水经循环水泵送往冷却塔,在循环水泵出口母管上连接一支路,将要送至冷却塔的循环水经循环水支路,通过自动液压流量调节装置引至锅炉一次风机和送风机进风口处,在该处建立与循环水相连的小型间冷塔;一次风机、送风机入口设置在小型间冷塔上部,风机运行在上部形成负压,空气从小型间冷塔底部进入,跟间冷塔换热后形成热空气,风机将热空气送入炉膛,回收部分乏汽余热;经小型间冷塔冷却后的循环水连接至凝汽器进水母管,继续送入凝汽器,吸收凝汽器内乏汽凝结热,从而完成整个乏汽余热回收过程;对于凝汽器乏汽余热回收装置独立设置,包括将换热装置设置在凝汽器,用以吸收凝汽器内乏汽余热,吸收余热的循环水经自动液压流量调节装置送至小间冷塔,与空气换热后,返回至凝汽器继续换热,循环水泵为整个循环提供动力,经与小间冷塔换热后的热空气,经一次风机,二次风机送至锅炉,从而完成整个凝汽器乏汽余热回收过程。 1. Condenser exhaust heat recovery energy-saving device, including the direct connection between the condenser exhaust heat recovery device and the cooling cycle water branch and the independent setting of the condenser exhaust heat recovery device; for the condenser exhaust The waste heat recovery device is directly connected with the cooling circulating water branch, including the steam turbine exhaust port of the power plant for cooling through the cooling system of the power plant. Connect a branch, and the circulating water to be sent to the cooling tower will pass through the circulating water branch, through the automatic hydraulic flow adjustment device, to the boiler primary fan and the air inlet of the blower, where a small intercooling tower connected to the circulating water will be established; The primary fan and blower inlet are set on the upper part of the small intercooling tower. The fan runs on the upper part to form a negative pressure. The air enters from the bottom of the small intercooling tower. After exchanging heat with the intercooling tower, hot air is formed. Part of exhaust steam waste heat; the circulating water cooled by the small inter-cooling tower is connected to the condenser inlet pipe, and then sent to the condenser to absorb the condensation heat of exhaust steam in the condenser, thereby completing the entire exhaust steam waste heat recovery process; For the exhaust steam waste heat recovery device of the condenser, the independent setting includes setting the heat exchange device in the condenser to absorb the waste heat of the exhaust steam in the condenser, and the circulating water that absorbs the waste heat is sent to the small room cooler The tower, after exchanging heat with the air, returns to the condenser to continue the heat exchange. The circulating water pump provides power for the whole cycle. After exchanging heat with the small cooling tower, the hot air is sent to the boiler through the primary fan and the secondary fan, thereby Complete the exhaust steam waste heat recovery process of the entire condenser. 2.如权利要求1所述的凝汽器乏汽余热回收节能装置,其特征在于:小间冷塔支路上设有循环水流量调节液动蝶阀,用以调节小间冷塔流量。 2. The energy-saving device for recovering exhausted steam and waste heat of the condenser as claimed in claim 1, characterized in that: a circulating water flow regulating hydraulic butterfly valve is installed on the branch of the small cooling tower to adjust the flow of the small cooling tower. 3.如权利要求1所述的凝汽器乏汽余热回收节能装置,其特征在于:小间冷塔有两种形式,一种是直接循环水支路引至风机入口,直接在一次风机、送风机入口建立相应换热管束的换热器,用于同空气换热;一种是底部建立换热管束,即小型间接冷却塔,一次风、二次风入口设置在圆形管束上部,从上部引出换热后的热风。 3. The energy-saving device for recovering exhausted steam waste heat of the condenser as claimed in claim 1, characterized in that: the small cooling tower has two forms, one is that the direct circulating water branch leads to the fan inlet, and directly connects the primary fan, A heat exchanger with a corresponding heat exchange tube bundle is established at the inlet of the blower to exchange heat with the air; one is to establish a heat exchange tube bundle at the bottom, that is, a small indirect cooling tower, and the primary air and secondary air inlets are set on the upper part of the circular tube bundle. Draw out the hot air after heat exchange. 4.如权利要求1所述的凝汽器乏汽余热回收节能装置,其特征在于:两台及以上机组可以公用一个小型间冷塔。 4. The energy-saving device for recovering exhaust steam and waste heat of the condenser according to claim 1, wherein two or more units can share a small intercooling tower. 5.利用如权利要求1所述的凝汽器乏汽余热回收节能装置的节能方法,其特征在于包括以下步骤: 5. Utilize the energy-saving method of condenser exhaust steam waste heat recovery energy-saving device as claimed in claim 1, it is characterized in that comprising the following steps: 1)在春季、秋季、夏级运行时,通过调节液动蝶阀调节循环水流量,使经小间冷塔循环后的回水温度问接近于冷却塔循环水回水水温,夏季运行时如果环境温度和冷却塔循环水回水温度相近时可以停运该装置; 1) During spring, autumn and summer operation, adjust the flow of circulating water by adjusting the hydraulic butterfly valve, so that the temperature of the return water after circulating through the small cooling tower is close to the return water temperature of the circulating water of the cooling tower. The device can be shut down when the temperature is similar to the return water temperature of the circulating water of the cooling tower; 2)在冬季运行时,在确保机组安全运行的前提下,适当提高电厂汽轮机运行排气背压的压力,从而提高循环水温度,调节液动蝶阀调节循环水流量,防止间冷塔冻裂,此时也相对提高了风机入口风温。 2) During winter operation, on the premise of ensuring the safe operation of the unit, appropriately increase the pressure of the exhaust back pressure of the steam turbine in the power plant to increase the temperature of the circulating water, adjust the hydraulic butterfly valve to adjust the flow of circulating water, and prevent the intercooling tower from freezing. At this time, the air temperature at the inlet of the fan is relatively increased.
CN201410518220.3A 2014-10-01 2014-10-01 Condenser dead steam waste heat recovery and energy saving device and energy saving method Pending CN104235870A (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105626171A (en) * 2016-03-28 2016-06-01 西安热工研究院有限公司 Waste heat utilization system for indirect air-cooling unit
CN106016241A (en) * 2016-07-15 2016-10-12 大唐(北京)能源管理有限公司 Cold-end waste heat gradient-utilization energy-saving system and method
CN106186200A (en) * 2016-09-06 2016-12-07 大唐环境产业集团股份有限公司 A kind of indirect air cooling unit recuperation of heat and water treatment facilities and method
CN109237509A (en) * 2018-08-30 2019-01-18 华电电力科学研究院有限公司 A kind of method and device that indirect air cooling unit circulating water afterheat is recycled to boiler supply air system

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105626171A (en) * 2016-03-28 2016-06-01 西安热工研究院有限公司 Waste heat utilization system for indirect air-cooling unit
CN106016241A (en) * 2016-07-15 2016-10-12 大唐(北京)能源管理有限公司 Cold-end waste heat gradient-utilization energy-saving system and method
CN106016241B (en) * 2016-07-15 2024-06-11 大唐环境产业集团股份有限公司 Cold end waste heat cascade utilization energy-saving system and method
CN106186200A (en) * 2016-09-06 2016-12-07 大唐环境产业集团股份有限公司 A kind of indirect air cooling unit recuperation of heat and water treatment facilities and method
CN109237509A (en) * 2018-08-30 2019-01-18 华电电力科学研究院有限公司 A kind of method and device that indirect air cooling unit circulating water afterheat is recycled to boiler supply air system

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