CN217004429U - System for recovering wet water of boiler for industrial steam supply - Google Patents

System for recovering wet water of boiler for industrial steam supply Download PDF

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CN217004429U
CN217004429U CN202121409846.2U CN202121409846U CN217004429U CN 217004429 U CN217004429 U CN 217004429U CN 202121409846 U CN202121409846 U CN 202121409846U CN 217004429 U CN217004429 U CN 217004429U
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water
steam
saturated
steam supply
boiler
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石慧
吕凯
许朋江
薛朝囡
张建元
邓佳
王妍
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Xian Thermal Power Research Institute Co Ltd
Xian Xire Energy Saving Technology Co Ltd
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Xian Thermal Power Research Institute Co Ltd
Xian Xire Energy Saving Technology Co Ltd
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Abstract

The utility model discloses a system for recovering boiler wet water for industrial steam supply, which is provided with a flash tank and an electric heater, wherein high-energy saturated water generated in the wet operation of a boiler is flashed into saturated steam under the pressure of industrial steam supply, the temperature is raised to the temperature of the industrial steam supply, and the saturated steam is finally supplied to the outside, so that the recovery of working media and energy of the wet water is realized, and the operation economy of a unit is greatly improved. Meanwhile, the utility model has the advantages of small transformation range, low cost, short investment recovery period and feasibility in finance.

Description

一种回收锅炉湿态水用于工业供汽的系统A system for recovering boiler wet water for industrial steam supply

技术领域technical field

本实用新型属于燃煤发电机组热电联产供热领域,具体涉及一种回收锅炉湿态水用于工业供汽的系统。The utility model belongs to the field of cogeneration of heat and power for coal-fired generating sets, in particular to a system for recycling boiler wet water for industrial steam supply.

背景技术Background technique

随着太阳能、风能、水能等清洁、低碳、可再生能源的迅速发展,传统火电由发电主体型能源向保障型能源快速转变,大型火电机组亟需承担电网深度调峰任务。而随着工业转型升级以及人民生活水平提高,工业蒸汽、集中供暖等用热需求在快速增长。其中,在工业供汽领域,为满足用汽企业的正常运转,要求工业供汽参数持续、稳定、可靠,而机组在低负荷下运行时,主、辅机设备严重偏离设计工况,很难确保热电联供系统的可靠性。因此,火电机组深度调峰需求和供汽能力保障的矛盾日益突出。With the rapid development of clean, low-carbon, and renewable energy such as solar energy, wind energy, and water energy, traditional thermal power has rapidly transformed from the main energy source of power generation to the guaranteed energy source. Large thermal power units urgently need to undertake the task of deep power grid peak regulation. With the transformation and upgrading of industries and the improvement of people's living standards, the demand for heat such as industrial steam and central heating is growing rapidly. Among them, in the field of industrial steam supply, in order to meet the normal operation of steam users, the parameters of industrial steam supply are required to be continuous, stable and reliable. However, when the unit operates under low load, the main and auxiliary equipment seriously deviate from the design conditions, which is difficult to achieve. Ensure the reliability of the combined heat and power system. Therefore, the contradiction between the deep peak shaving demand of thermal power units and the guarantee of steam supply capacity has become increasingly prominent.

大型火电机组深度调峰至锅炉负荷小于约30%BMCR时,炉膛内的热量无法将进入水冷壁的给水全部加热成饱和蒸汽,锅炉转为湿态运行。来自水冷壁系统的汽水混合物进入分离器后,旋转产生的离心力将汽水分离,分离后的蒸汽从分离器顶部引出至低温过热器,水从分离器底部进入储水箱。当水质合格时,储水箱内的近饱和水排入凝汽器,造成了大量的能量损失;当水质不合格时,储水箱内的近饱和水通过排污系统排出厂外,造成了大量的工质损失和能量损失。When the large thermal power unit is deeply peaked to the extent that the boiler load is less than about 30% BMCR, the heat in the furnace cannot heat all the feed water entering the water wall into saturated steam, and the boiler turns to wet operation. After the steam-water mixture from the water-cooled wall system enters the separator, the centrifugal force generated by the rotation separates the steam-water, the separated steam is led out from the top of the separator to the low-temperature superheater, and the water enters the water storage tank from the bottom of the separator. When the water quality is qualified, the nearly saturated water in the water storage tank is discharged into the condenser, causing a lot of energy loss; when the water quality is unqualified, the nearly saturated water in the water storage tank is discharged out of the plant through the sewage system, causing a large amount of work. mass loss and energy loss.

由于锅炉湿态运行时储水箱内收集的水为给水压力下的近饱和水,能量品质较高,十分有必要将其回收再利用。因此,在火电机组长期低负荷运行和供汽品质难以维持的形势下,提出将锅炉湿态水回收用于高压工业供汽的改造方法。Since the water collected in the water storage tank is near-saturated water under the feed water pressure when the boiler is operating in wet state, the energy quality is high, and it is necessary to recycle it for reuse. Therefore, under the situation of long-term low-load operation of thermal power units and the difficulty of maintaining the quality of steam supply, a retrofit method of recycling boiler wet water for high-pressure industrial steam supply is proposed.

发明内容SUMMARY OF THE INVENTION

本实用新型的目的在于解决现有火电机组深度调峰至低负荷,锅炉湿态运行时,汽水分离器分离出的湿态水无法有效利用,导致机组低负荷运行经济性差的问题,同时缓解机组长期低负荷运行和工业供汽品质难以保障的矛盾,将高能湿态水回收用于高压工业供汽,提供一种回收锅炉湿态水用于工业供汽的系统。The purpose of the utility model is to solve the problem that the existing thermal power unit is in deep peak regulation to low load, and the wet water separated by the steam-water separator cannot be effectively used when the boiler is running in a wet state, which leads to the problem of poor economy in the low-load operation of the unit, and alleviates the problem of the unit at the same time. Due to the contradiction between long-term low-load operation and the difficulty of guaranteeing the quality of industrial steam supply, high-energy wet water is recycled for high-pressure industrial steam supply, and a system for recovering boiler wet water for industrial steam supply is provided.

为了达到上述目的,本实用新型包括汽水分离器、储水箱、闪蒸罐和电加热器;In order to achieve the above purpose, the utility model includes a steam-water separator, a water storage tank, a flash tank and an electric heater;

汽水分离器的入口连接水冷壁系统的汽水混合物,汽水分离器的饱和水出口连接储水箱,储水箱连接闪蒸罐,闪蒸罐的饱和蒸汽出口连接电加热器。The inlet of the steam-water separator is connected to the steam-water mixture of the water wall system, the saturated water outlet of the steam-water separator is connected to the water storage tank, the water storage tank is connected to the flash tank, and the saturated steam outlet of the flash tank is connected to the electric heater.

汽水分离器的饱和蒸汽出口连接低温过热器。The saturated steam outlet of the steam-water separator is connected to the low-temperature superheater.

闪蒸罐的饱和水出口连接凝汽器。The saturated water outlet of the flash tank is connected to the condenser.

储水箱与闪蒸罐的连接管路上设置有截止阀。A stop valve is arranged on the connection pipeline between the water storage tank and the flash tank.

储水箱与闪蒸罐的连接管路上设置有电动调阀。An electric regulating valve is arranged on the connecting pipeline between the water storage tank and the flash tank.

电加热器用于将闪蒸罐产生的饱和蒸汽加热至工业供汽温度,对外供出。The electric heater is used to heat the saturated steam produced by the flash tank to the industrial steam supply temperature and supply it to the outside.

与现有技术相比,本实用新型设置闪蒸罐和电加热器,首先将锅炉湿态运行时产生的高能饱和水闪蒸为工业供汽压力下的饱和蒸汽,提温至工业供汽温度,最终对外供出,实现了对湿态水的工质和能量的回收,大大提高了机组运行经济性。同时,本实用新型改造范围小,成本较低,投资回收期短,财务上可行。Compared with the prior art, the utility model is provided with a flash tank and an electric heater. First, the high-energy saturated water generated during the wet operation of the boiler is flashed into saturated steam under the industrial steam supply pressure, and the temperature is raised to the industrial steam supply temperature. , and finally supplied to the outside world, realizing the recovery of the working fluid and energy of the wet water, and greatly improving the operating economy of the unit. At the same time, the utility model has the advantages of small transformation scope, low cost, short investment recovery period and financial feasibility.

附图说明Description of drawings

图1为本实用新型的系统结构图;Fig. 1 is the system structure diagram of the present utility model;

其中,1、汽水分离器,2、储水箱,3、截止阀,4、电动调阀,5、闪蒸罐,6、电加热器,7、凝汽器。Among them, 1. Steam-water separator, 2. Water storage tank, 3. Globe valve, 4. Electric regulating valve, 5. Flash tank, 6. Electric heater, 7. Condenser.

具体实施方式Detailed ways

下面结合附图对本实用新型做进一步说明。The present utility model will be further described below in conjunction with the accompanying drawings.

参见图1,本实用新型包括汽水分离器1、储水箱2、闪蒸罐5和电加热器6;Referring to Figure 1, the present utility model includes a steam-water separator 1, a water storage tank 2, a flash tank 5 and an electric heater 6;

汽水分离器1的入口连接水冷壁系统的汽水混合物,汽水分离器1的饱和水出口连接储水箱2,汽水分离器1的饱和蒸汽出口连接低温过热器。储水箱2连接闪蒸罐5,储水箱2与闪蒸罐5的连接管路上设置有截止阀3和电动调阀4。闪蒸罐5的饱和蒸汽出口连接电加热器6。闪蒸罐5的饱和水出口连接凝汽器7。电加热器6用于将闪蒸罐产生的饱和蒸汽加热至工业供汽温度,对外供出。The inlet of the steam-water separator 1 is connected to the steam-water mixture of the water wall system, the saturated water outlet of the steam-water separator 1 is connected to the water storage tank 2, and the saturated steam outlet of the steam-water separator 1 is connected to the low temperature superheater. The water storage tank 2 is connected to the flash tank 5 , and the connection pipeline between the water storage tank 2 and the flash tank 5 is provided with a stop valve 3 and an electric regulating valve 4 . The saturated steam outlet of the flash tank 5 is connected to the electric heater 6 . The saturated water outlet of the flash tank 5 is connected to the condenser 7 . The electric heater 6 is used to heat the saturated steam generated by the flash tank to the industrial steam supply temperature and supply it to the outside.

本实用新型的工作方法,包括以下步骤:The working method of the present utility model comprises the following steps:

机组湿态运行时,来自水冷壁系统的汽水混合物进入汽水分离器1,产生一定量给水压力下的饱和湿态水,饱和湿态水在储水箱2中汇集;汽水分离器1分离出的饱和蒸汽进入低温过热器。When the unit is running in a wet state, the steam-water mixture from the water-cooled wall system enters the steam-water separator 1, producing saturated wet-state water under a certain amount of feed water pressure, and the saturated wet-state water is collected in the water storage tank 2; the saturated wet-state water separated by the steam-water separator 1 The steam enters the low temperature superheater.

储水箱2中的饱和湿态水经出口管道进入闪蒸罐5;The saturated wet water in the water storage tank 2 enters the flash tank 5 through the outlet pipe;

闪蒸罐5闪蒸后产生所需工业供汽压力下的饱和水和饱和蒸汽,饱和蒸汽进入电加热器6。闪蒸罐5闪蒸后产生的饱和水排入凝汽器7。After flashing in the flash tank 5, saturated water and saturated steam under the required industrial steam supply pressure are generated, and the saturated steam enters the electric heater 6. The saturated water produced after flashing in the flash tank 5 is discharged into the condenser 7 .

饱和蒸汽在电加热器6中加热至工业供汽温度,对外供出。The saturated steam is heated to the industrial steam supply temperature in the electric heater 6 and supplied to the outside.

实施例:Example:

某电厂1000MW机组汽轮机为东方汽轮机有限公司制造的N1000-25/600/600型、超超临界、单轴、四缸、四排汽、一次中间再热、凝汽式汽轮机,需承担工业供汽参数为2.5MPa、320℃。The steam turbine of a 1000MW unit in a power plant is an N1000-25/600/600 type, ultra-supercritical, single-shaft, four-cylinder, four-exhaust, one-time intermediate reheat, condensing steam turbine manufactured by Dongfang Steam Turbine Co., Ltd., and it needs to undertake industrial steam supply. The parameters are 2.5MPa, 320℃.

锅炉20%THA负荷湿态运行时,机组发电功率为205.2MW,产生约120t/h的高能饱和水(压力为13.6MPa,温度为334.4℃)。利用该实用新型改造后,设置闪蒸罐和电加热器,闪蒸罐设计压力为2.5MPa,闪蒸后的饱和蒸汽压力为2.5MPa,温度为224℃,流量为39.1t/h。经电加热器加热进一步升温至320℃后对外供出。When the boiler is running in wet state with 20% THA load, the generating power of the unit is 205.2MW, producing about 120t/h of high-energy saturated water (pressure is 13.6MPa, temperature is 334.4℃). After the utility model is transformed, a flash tank and an electric heater are installed. The design pressure of the flash tank is 2.5MPa, the saturated steam pressure after flashing is 2.5MPa, the temperature is 224°C, and the flow rate is 39.1t/h. After heating by an electric heater, it is further heated up to 320°C and then supplied to the outside.

利用本实用新型改造回收后,机组在25%THA工况湿态运行时热耗率约为8817.6kJ/kWh(折合煤耗率约为330.3g/kWh),比改造前机组热耗率9330.8kJ/kWh(折合煤耗率约为349.6g/kWh)下降约513.2kJ/kWh(折合煤耗率约为19.3g/kWh),下降幅度为5.5%,大大提高了机组运行经济性。After the utility model is transformed and recovered, the heat consumption rate of the unit is about 8817.6kJ/kWh (the equivalent coal consumption rate is about 330.3g/kWh) when the unit is running in a wet state under 25% THA condition, which is 9330.8kJ/kWh compared to the unit before the reconstruction. kWh (equivalent coal consumption rate is about 349.6g/kWh) decreased by about 513.2kJ/kWh (equivalent coal consumption rate is about 19.3g/kWh), a decrease of 5.5%, which greatly improves the operating economy of the unit.

Claims (6)

1. A system for recovering wet water of a boiler for industrial steam supply is characterized by comprising a steam-water separator (1), a water storage tank (2), a flash tank (5) and an electric heater (6);
the inlet of the steam-water separator (1) is connected with a steam-water mixture of a water wall system, the saturated water outlet of the steam-water separator (1) is connected with the water storage tank (2), the water storage tank (2) is connected with the flash tank (5), and the saturated steam outlet of the flash tank (5) is connected with the electric heater (6).
2. A system for recovering wet water of a boiler for industrial steam supply according to claim 1, characterized in that the saturated steam outlet of the steam-water separator (1) is connected with a low-temperature superheater.
3. A system for recovering boiler wet water for industrial steam supply according to claim 1, characterized in that the saturated water outlet of the flash tank (5) is connected to a condenser (7).
4. A system for recovering boiler wet water for industrial steam supply according to claim 1, characterized in that a stop valve (3) is arranged on the connection pipeline between the water storage tank (2) and the flash tank (5).
5. A system for recovering boiler wet water for industrial steam supply according to claim 1, characterized in that an electric regulating valve (4) is arranged on the connection pipeline between the water storage tank (2) and the flash tank (5).
6. A system for recovering wet water of a boiler for industrial steam supply according to claim 1, characterized in that the electric heater (6) is used for heating the saturated steam generated by the flash tank (5) to the industrial steam supply temperature and supplying the saturated steam to the outside.
CN202121409846.2U 2021-06-23 2021-06-23 System for recovering wet water of boiler for industrial steam supply Active CN217004429U (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113251402A (en) * 2021-06-23 2021-08-13 西安热工研究院有限公司 System for recycling wet water of boiler for industrial steam supply and working method

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113251402A (en) * 2021-06-23 2021-08-13 西安热工研究院有限公司 System for recycling wet water of boiler for industrial steam supply and working method

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