CN211199116U - Dry quenching double-super power generation circulating water cooling device - Google Patents
Dry quenching double-super power generation circulating water cooling device Download PDFInfo
- Publication number
- CN211199116U CN211199116U CN201921378606.3U CN201921378606U CN211199116U CN 211199116 U CN211199116 U CN 211199116U CN 201921378606 U CN201921378606 U CN 201921378606U CN 211199116 U CN211199116 U CN 211199116U
- Authority
- CN
- China
- Prior art keywords
- circulating water
- water
- inert gas
- unit
- pressure stabilizing
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Images
Landscapes
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The utility model discloses a dry quenching double-super power generation circulating water cooling device. Belongs to the technical field of dry coke quenching energy-saving and environment-friendly treatment, and is characterized in that: the system comprises a turbine condenser circulating water unit, an inert gas pressure stabilizing unit, an air cooling unit and an auxiliary spraying circulating water unit; the steam turbine condenser circulating water unit is connected with the air cooling unit and the auxiliary spraying circulating water unit through low-temperature water pipes by pipelines, and is connected with the inert gas pressure stabilizing unit through high-temperature water pipes by pipelines; the inert gas pressure stabilizing unit is connected with the air cooling unit through a plate type heat exchanger pipeline, so that the steam turbine condenser circulating water unit, the inert gas pressure stabilizing unit, the air cooling unit and the auxiliary spraying circulating water unit form closed-loop pipeline connection. It reduces sewage treatment scale and sewage treatment cost, reduces water quality stabilization treatment cost and reduces environmental pollution.
Description
Technical Field
The utility model discloses a dry quenching double-super power generation circulating water cooling device. Belonging to the technical field of dry coke quenching energy-saving and environment-friendly treatment.
Background
The common wet quenching is a quenching mode commonly adopted in the coking industry, and has the advantages of small investment, simple and convenient operation and capability of consuming a large amount of coking wastewater. But has the disadvantages of serious air pollution and waste of a large amount of heat. With the stricter requirements of national energy conservation and environmental protection, the common wet quenching method is gradually replaced by the dry quenching process, and becomes a standby process. For example, since 2012 in the environment-friendly hall of Shandong province, independent coking enterprises approved by the province hall require a dry quenching process to belong to a circular economic project in a park for standby wet quenching. At present, dry quenching units are built in independent coking plants such as Shandong iron and male, Tongling Xinyaxing and the like; the Tangshan City of Hebei province starts to require all coking enterprises to build a dry quenching process in 2015. In early 2016, leaders in air pollution control of the province gave out a special action scheme for pollution control in the coking industry in Hebei province, and all coking enterprises before 2017 are required to be built into a dry quenching and sewage deep treatment process in view of air pollution control and compression capacity. Although dry quenching can fully utilize sensible heat of red coke to generate electricity, has considerable economic benefit and can basically eliminate the pollution of quenching to the environment, the one-time energy input is larger, the reconstruction of coking enterprises with short sites is difficult, and a condenser of a dry quenching waste heat power generation system needs a large amount of circulating water, the loss of the circulating water due to evaporation, wind blowing and leakage accounts for 2-3% of the total amount of the circulating water, and the pollution discharge loss is 0.25 times of the loss of the circulating water according to the concentration ratio of 5, so the larger the circulating water is, the larger the consumed new production water is, the larger the pollution discharge is, the larger the supply amount and the discharge amount of the new water are increased, the new water cost and the sewage treatment cost are increased, and meanwhile, the increase of the supply water amount also increases the water quality stabilization treatment cost and the enterprise burden. Therefore, a proper method is required to be found to modify the existing circulating water treatment mode, so that the purposes of saving new water, reducing sewage and reducing the treatment cost of stable water quality are achieved, and meanwhile, the requirements of energy conservation and environmental protection are met.
Disclosure of Invention
The utility model aims at providing a two super power generation circulating water cooling plant of dry process quenching to reduce sewage treatment scale and sewage treatment expense, reduce the stable treatment cost of water quality, reduce environmental pollution.
The utility model aims at realizing the above, a dry quenching double-super power generation circulating water cooling device, which is characterized in that: the system comprises a turbine condenser circulating water unit, an inert gas pressure stabilizing unit, an air cooling unit and an auxiliary spraying circulating water unit; the steam turbine condenser circulating water unit is connected with the air cooling unit and the auxiliary spraying circulating water unit through low-temperature water pipes by pipelines, and is connected with the inert gas pressure stabilizing unit through high-temperature water pipes by pipelines; the inert gas pressure stabilizing unit is connected with the air cooling unit through a plate type heat exchanger pipeline, so that the steam turbine condenser circulating water unit, the inert gas pressure stabilizing unit, the air cooling unit and the auxiliary spraying circulating water unit form closed-loop pipeline connection; the low-temperature water pipe is a water outlet pipeline of the second circulating water pump, and the high-temperature water pipe is a water outlet pipeline of the first circulating water pump.
The steam turbine condenser circulating water unit comprises an auxiliary circulating water pump, a steam turbine generator condenser, a circulating water pump water inlet pipeline, a first circulating water pump water outlet pipeline and a second circulating water pump water outlet pipeline; when the steam turbine generator condenser works, the circulating water pump conveys low-temperature water to the steam turbine generator condenser through the second circulating water pump water outlet pipe, indirect heat exchange is carried out in the steam turbine generator condenser, and circulating water after heat exchange is conveyed to the water inlet of the inert gas pressure stabilizing tank through the first circulating water pump water outlet pipeline.
The inert gas pressure stabilizing unit comprises: an inert gas pressure stabilizing tank, a safety valve, a blow-down valve, a water outlet and a soft water replenishing pipe; in order to prevent oxygen in the air from entering the auxiliary spraying circulating water unit, an inert gas pressure stabilizing tank in the inert gas pressure stabilizing unit is filled with nitrogen through an inert gas inlet of the pressure stabilizing tank; the inert gas pressure stabilizing tank is kept to operate under constant pressure, in order to ensure the operation safety of the inert gas pressure stabilizing unit, a safety valve is arranged on the inert gas pressure stabilizing tank, and when the system pressure exceeds the standard, the safety valve is opened to ensure the operation safety of the inert gas pressure stabilizing tank; when the quality of the circulating water exceeds the standard, discharging sewage through a drain valve at the bottom of the inert gas pressure stabilizing tank; when the water level of the inert gas pressure stabilizing tank is ultralow, water is supplemented into the system through a soft water supplementing pipe; circulating water flows to the plate heat exchanger through a water outlet of the inert gas pressure stabilizing tank after pressure stabilization.
The air cooling unit comprises a glass fiber reinforced plastic enclosure wall, a glass fiber reinforced plastic kinetic energy recovery type air duct, a coupler and an axial flow fan, wherein the coupler and the axial flow fan are used for providing air circulation, the air quantity and the air temperature during air-water heat exchange are adjusted according to the circulating water temperature of circulating water of the steam turbine condenser, the air cooling unit is used for adjusting the requirement of the steam turbine generator condenser on the circulating water temperature, and the coupler and the axial flow fan work to enable the glass fiber reinforced plastic kinetic energy recovery type air duct in the glass fiber reinforced plastic enclosure wall to form air circulation in the glass fiber reinforced plastic kinetic energy recovery type air duct.
The supplementary circulating water unit that sprays include: the auxiliary spraying water unit comprises a spraying water accumulation pool, an auxiliary spraying circulating water pump water outlet pipe and a spraying head, wherein when the auxiliary spraying water unit works, the auxiliary spraying circulating water pump absorbs water through an auxiliary spraying circulating water pump inlet pipe, and sprays water to the plate heat exchanger through an auxiliary spraying circulating water pump outlet pipe and the spraying head, and the spraying water falls into the spraying water accumulation pool below.
The steam turbine condenser circulating water unit comprises an auxiliary circulating water pump, a circulating water pump water inlet pipeline, a first circulating water pump water outlet pipeline and a second circulating water pump water outlet pipeline; one port of a steam turbine generator condenser is connected with a steam turbine generator, the other port of the steam turbine generator condenser is connected with a condensate pump, the interior of the steam turbine generator condenser is outwards connected with a first circulating water pump water outlet pipeline and a second circulating water pump water outlet pipeline through a coil pipe, and the second circulating water pump water outlet pipeline is connected with an auxiliary spraying circulating water pump outlet pipe of an auxiliary spraying circulating water unit through a circulating water pump and a circulating water pump water inlet pipeline; and the water outlet pipeline of the first circulating water pump is connected with the water inlet pipeline of the inert gas pressure stabilizing tank.
The inert gas pressure stabilizing unit comprises: the device comprises an inert gas pressure stabilizing tank, a pressure stabilizing tank inert gas inlet, a safety valve, a blow-down valve, a water inlet, a water outlet and a soft water replenishing pipe; the inert gas pressure stabilizing tank is connected with the auxiliary spray water unit through a water outlet, and an air cooling unit is arranged outside the water outlet pipe; the inert gas pressure stabilizing tank is connected with an inert gas inlet of the pressure stabilizing tank, a safety valve, a blow-down valve, a water outlet and a soft water replenishing pipe through a connector, the blow-down valve is arranged at the bottom of the inert gas pressure stabilizing tank, the water outlet is arranged at the lower bottom of the inert gas pressure stabilizing tank, the water inlet is arranged at the upper part of the inert gas pressure stabilizing tank, and the safety valve is arranged at the top of the inert gas pressure stabilizing tank; the water outlet is connected with the plate heat exchanger through a pipeline.
The supplementary circulating water unit that sprays include: the spray head is arranged at the upper end of the plate heat exchanger, the spray water accumulation pool is arranged at the bottom of the plate heat exchanger, the plate heat exchanger is of 4 levels, the water inlet pipeline of the circulating water pump of the 4-level plate heat exchanger is communicated with each other, the water inlet pipeline of the circulating water pump is connected with an auxiliary spray circulating water pump inlet pipe, an auxiliary spray circulating water pump and an auxiliary spray water supplementing pipe, and the auxiliary spray circulating water pump is connected with the spray head through an auxiliary spray circulating water pump outlet pipe.
The utility model discloses carry out soda, air water heat transfer under airtight pressure's condition, turbine condenser circulation system inner circulating water adopts soft water or demineralized water, can stop basically because of evaporation loss, the loss of blowing and the seepage loss of air water heat transfer cooling production circulating water, because of adopting soft water or demineralized water as thermal carrier, improvement circulation multiplying power that can be very big to greatly reduced blowdown loss.
The inert gas nitrogen is used as the pressure-stabilizing gas, so that oxygen entering a circulating water system is reduced, and the corrosion of oxygen entering to metal in the circulating water system is greatly reduced.
For guarantee circulating water system's efficiency under the most unfavorable condition in summer to carry out the shower water to the heat exchanger and improve plate heat exchanger's heat transfer effect, reach the effect of temperature steady operation, increase the supplementary circulating water unit that sprays.
The water loss can be reduced to the maximum extent by carrying out air-water cooling through a soft water or demineralized water closed-loop circulating water system, so that the water supplement amount and the sewage discharge amount are reduced; the closed cycle is carried out by utilizing the specific gravity difference between high temperature and low temperature of the circulating water, and the circulating water pump only plays an auxiliary role, so that the power of the circulating water pump can be greatly reduced, and the power consumption of the circulating water is reduced.
The utility model has the advantages that: the heat exchange of steam water and gas water is carried out under the condition of closed pressure, the circulating water in the circulating system of the steam turbine condenser adopts soft water or desalted water, so that the evaporation loss, the blowing loss and the leakage loss of the circulating water caused by the heat exchange and cooling of the gas water can be basically avoided, and the circulating multiplying power can be greatly improved by adopting the soft water or the desalted water as a heat carrier, so that the pollution discharge loss is greatly reduced; the inert gas nitrogen is used as the pressure-stabilizing gas, so that the oxygen entering into a circulating water system is reduced, and the corrosion of the oxygen entering into the metal in the circulating water system is greatly reduced; for the efficiency of guaranteeing the circulating water system under the most unfavorable condition in summer to carry out the shower water to the heat exchanger and improve plate heat exchanger's heat transfer effect, reach the effect that the temperature steady operation. The water loss can be reduced to the maximum extent by carrying out air-water cooling through a soft water or demineralized water closed-loop circulating water system, so that the water supplement amount and the sewage discharge amount are reduced; the closed cycle is carried out by utilizing the specific gravity difference between high temperature and low temperature of the circulating water, and the circulating water pump only plays an auxiliary role, so that the power of the circulating water pump can be greatly reduced, and the power consumption of the circulating water is reduced.
Drawings
The invention is further described below with reference to the accompanying drawings of the embodiments:
fig. 1 is a schematic view of a system according to an embodiment of the present invention.
In the figure: 1. a water circulating pump; 2. a turbine generator condenser; 3. a water inlet pipeline of the circulating water pump; 4. a water outlet pipeline of the first circulating water pump; 4', a water outlet pipeline of a second circulating water pump; 5. an inert gas surge tank; 6. an inert gas inlet of the surge tank; 7. a safety valve; 8. a blowoff valve; 9. a water inlet; 10. a water outlet; 11. a glass fiber reinforced plastic enclosure wall; 12. a kinetic energy recovery type wind cylinder; 13. a coupling and an axial flow fan; 14. a plate heat exchanger; 15. spraying a water accumulation pool; 16. an auxiliary spraying circulating water pump inlet pipe; 17. an auxiliary spray circulating water pump; 18. an outlet pipe of the auxiliary spraying circulating water pump; 19. a shower head; 20. a soft water replenishing pipe; 21. an auxiliary spray water replenishing pipe; 22. a steam turbine generator; 23. a condensate pump; 24. and (4) coiling the pipe.
Detailed Description
As shown in fig. 1, a dry quenching double super power generation circulating water cooling device comprises a turbine condenser circulating water unit, an inert gas pressure stabilizing unit, an air cooling unit and an auxiliary spraying circulating water unit;
the steam turbine condenser circulating water unit is used for carrying out air-water cooling on a closed circulating water system through soft water or demineralized water to reduce the water supplement amount and the sewage discharge amount; the high and low temperature specific gravity difference of the circulating water is utilized to carry out closed cycle, so that the power consumption of the circulating water is reduced;
the inert gas pressure stabilizing unit is used for reducing oxygen entering the circulating water system and reducing corrosion of oxygen entering to metal in the circulating water system;
the air cooling unit is used for adjusting the air quantity and the air temperature during air-water heat exchange according to the circulating water temperature of the circulating water of the steam condenser, and forming air circulation in the glass fiber reinforced plastic kinetic energy recovery type air cylinder 12;
the auxiliary spraying circulating water unit is used for ensuring the efficiency of a circulating water system under the condition of high temperature in summer.
In fig. 1, a turbine condenser circulating water unit is connected with an air cooling unit and an auxiliary spraying circulating water unit through low-temperature water pipes, and the turbine condenser circulating water unit is connected with an inert gas pressure stabilizing unit through high-temperature water pipes; the inert gas pressure stabilizing unit is connected with the air cooling unit through a plate type heat exchanger pipeline, so that the steam turbine condenser circulating water unit, the inert gas pressure stabilizing unit, the air cooling unit and the auxiliary spraying circulating water unit form closed-loop pipeline connection; the low-temperature water pipe is a water outlet pipeline of the second circulating water pump, and the high-temperature water pipe is a water outlet pipeline of the first circulating water pump.
The specific structure is illustrated by the following description:
the steam turbine condenser circulating water unit comprises an auxiliary circulating water pump 1, a steam turbine generator condenser 2, a circulating water pump water inlet pipeline 3, a first circulating water pump water outlet pipeline 4 and a second circulating water pump water outlet pipeline 4'; when the turbonator condenser 2 works, the circulating water pump 1 conveys low-temperature water to the turbonator condenser 2 through the second circulating water pump water outlet pipeline 4', indirect heat exchange is carried out in the turbonator condenser 2, and circulating water after heat exchange is conveyed to the water inlet 9 of the inert gas pressure stabilizing tank 5 through the first circulating water pump water outlet pipeline 4. The utility model provides a low temperature water or normal atmospheric temperature water, or secondary treatment's circulating water
The inert gas pressure stabilizing unit comprises: an inert gas pressure stabilizing tank 5, a safety valve 7, a blow-off valve 8, a water outlet 10 and a soft water replenishing pipe 20; in order to prevent oxygen in the air from entering the auxiliary spraying circulating water unit, an inert gas pressure stabilizing tank 5 in the inert gas pressure stabilizing unit is filled with nitrogen through an inert gas inlet 6 of the pressure stabilizing tank; the operation of the inert gas pressure stabilizing tank 5 is kept under constant pressure, in order to ensure the operation safety of the inert gas pressure stabilizing unit, a safety valve 7 is arranged on the inert gas pressure stabilizing tank 5, and when the system pressure exceeds the standard, the safety valve 7 is opened to ensure the operation safety of the inert gas pressure stabilizing tank 5; when the quality of the circulating water exceeds the standard, discharging sewage through a drain valve 8 at the bottom of the inert gas pressure stabilizing tank 5; when the water level of the inert gas pressure stabilizing tank 5 is ultralow, water is supplemented into the system through a soft water supplementing pipe 20; the circulating water after pressure stabilization flows to the plate heat exchanger 14 through the water outlet 10 of the inert gas pressure stabilization tank 5.
The air cooling unit comprises a glass fiber reinforced plastic enclosure wall 11, a glass fiber reinforced plastic kinetic energy recovery type air duct 12, a coupler and an axial flow fan 13, wherein the coupler and the axial flow fan 13 are used for providing air circulation, the air quantity and the air temperature during air-water heat exchange are adjusted according to the circulating water temperature of circulating water of the steam turbine condenser, the air cooling unit is used for adjusting the requirement of the steam turbine generator condenser 2 on the circulating water temperature, and the coupler and the axial flow fan 13 work to enable the glass fiber reinforced plastic kinetic energy recovery type air duct 12 in the glass fiber reinforced plastic enclosure wall 11 to form air circulation in the glass fiber reinforced plastic kinetic energy recovery type air duct 12.
Example 2
On the basis of embodiment 1, in order that air cooling can not satisfy the requirement of the steam turbine on the circulating water temperature in summer, an auxiliary spraying circulating water unit is added, and the auxiliary spraying circulating water unit comprises: the spray water accumulation pool 15, the auxiliary spray circulating water pump 17, the auxiliary spray circulating water pump outlet pipe 18 and the spray header 19, when the auxiliary spray circulating water unit works, the auxiliary spray circulating water pump 17 sucks water through the auxiliary spray circulating water pump inlet pipe 16, and sprays water to the plate heat exchanger 14 through the auxiliary spray circulating water pump outlet pipe 18 to the spray header 19, and the spray water falls into the spray water accumulation pool 15 below.
The utility model discloses carry out soda, air water heat transfer under airtight pressure's condition, turbine condenser circulation system inner circulating water adopts soft water or demineralized water, can stop basically because of evaporation loss, the loss of blowing and the seepage loss of air water heat transfer cooling production circulating water, because of adopting soft water or demineralized water as thermal carrier, improvement circulation multiplying power that can be very big to greatly reduced blowdown loss.
The inert gas nitrogen is used as the pressure-stabilizing gas, so that oxygen entering a circulating water system is reduced, and the corrosion of oxygen entering to metal in the circulating water system is greatly reduced.
For guarantee circulating water system's efficiency under the most unfavorable condition in summer to carry out the shower water to the heat exchanger and improve plate heat exchanger's heat transfer effect, reach the effect of temperature steady operation, increase the supplementary circulating water unit that sprays.
The water loss can be reduced to the maximum extent by carrying out air-water cooling through a soft water or demineralized water closed-loop circulating water system, so that the water supplement amount and the sewage discharge amount are reduced; the closed cycle is carried out by utilizing the specific gravity difference between high temperature and low temperature of the circulating water, and the circulating water pump only plays an auxiliary role, so that the power of the circulating water pump can be greatly reduced, and the power consumption of the circulating water is reduced.
The above description is only for the purpose of illustrating the preferred embodiments of the present invention and is not intended to limit the present invention, and all modifications, equivalents, improvements and the like that are made within the spirit and principles of the present invention are intended to be included within the scope of the present invention.
The circulating water unit of the steam turbine condenser comprises an auxiliary circulating water pump 1, a circulating water pump water inlet pipeline 3, a first circulating water pump water outlet pipeline 4 and a second circulating water pump water outlet pipeline 4'; one port of the steam turbine generator condenser 2 is connected with a steam turbine generator 22, the other port of the steam turbine generator condenser 2 is connected with a condensate pump 23, the interior of the steam turbine generator condenser 2 is outwards connected with a first circulating water pump water outlet pipeline 4 and a second circulating water pump water outlet pipeline 4 'through a coil pipe 24, and the second circulating water pump water outlet pipeline 4' is connected with an auxiliary spraying circulating water pump outlet pipe 18 of an auxiliary spraying circulating water unit through the circulating water pump 1 and a circulating water pump water inlet pipeline 3; the water outlet pipeline 4 of the first circulating water pump is connected with the water inlet 9 of the inert gas pressure stabilizing tank 5 through a pipeline.
The inert gas pressure stabilizing unit comprises: an inert gas surge tank 5, a surge tank inert gas inlet 6, a safety valve 7, a blow-off valve 8, a water inlet 9, a water outlet 10 and a soft water replenishing pipe 20; the inert gas pressure stabilizing tank 5 is connected with the auxiliary spray water unit through a water outlet 10, and an air cooling unit is arranged outside the water outlet pipe; the inert gas pressure stabilizing tank 5 is connected with an inert gas inlet 6 of the pressure stabilizing tank, a safety valve 7, a blow-down valve 8, a water outlet 10 and a soft water replenishing pipe 20 through interfaces, the blow-down valve 8 is arranged at the bottom of the inert gas pressure stabilizing tank 5, the water outlet 10 is arranged at the lower bottom of the inert gas pressure stabilizing tank 5, a water inlet 9 is arranged at the upper part of the inert gas pressure stabilizing tank 5, and the safety valve 7 is arranged at the top of the inert gas pressure stabilizing tank 5; the water outlet 10 is connected with a plate heat exchanger 14 through a pipeline.
The supplementary circulating water unit that sprays include: the spray header 19 is arranged at the upper end of the plate heat exchanger 14, the spray water accumulation pool 15 is arranged at the bottom of the plate heat exchanger 14, the plate heat exchanger 14 has 4 levels, the water inlet pipeline 3 of the circulating water pump of the 4-level plate heat exchanger 14 is communicated, the water inlet pipeline 3 of the circulating water pump is connected with an auxiliary spray circulating water pump inlet pipe 16, an auxiliary spray circulating water pump 17 and an auxiliary spray water replenishing pipe 21, and the auxiliary spray circulating water pump 17 is connected with the spray header 19 through an auxiliary spray circulating water pump outlet pipe 18.
Components and structures not described in detail in the embodiments are those well-known in the art and commonly used structures or commonly used means, which are not all specifically described herein.
Claims (8)
1. A dry quenching double-super power generation circulating water cooling device is characterized in that: the system comprises a turbine condenser circulating water unit, an inert gas pressure stabilizing unit, an air cooling unit and an auxiliary spraying circulating water unit; the steam turbine condenser circulating water unit is connected with the air cooling unit and the auxiliary spraying circulating water unit through low-temperature water pipes by pipelines, and is connected with the inert gas pressure stabilizing unit through high-temperature water pipes by pipelines; the inert gas pressure stabilizing unit is connected with the air cooling unit through a plate type heat exchanger pipeline, so that the steam turbine condenser circulating water unit, the inert gas pressure stabilizing unit, the air cooling unit and the auxiliary spraying circulating water unit form closed-loop pipeline connection; the low-temperature water pipe is a water outlet pipeline (4') of the second circulating water pump, and the high-temperature water pipe is a water outlet pipeline (4) of the first circulating water pump.
2. The dry quenching double super power generation circulating water cooling device as claimed in claim 1, wherein: the steam turbine condenser circulating water unit comprises an auxiliary circulating water pump (1), a steam turbine generator condenser (2), a circulating water pump water inlet pipeline (3), a first circulating water pump water outlet pipeline (4) and a second circulating water pump water outlet pipeline (4'); when the steam turbine generator condenser (2) works, the circulating water pump (1) conveys low-temperature water to the steam turbine generator condenser (2) through the second circulating water pump water outlet pipeline (4'), indirect heat exchange is carried out in the steam turbine generator condenser (2), and circulating water after heat exchange is conveyed to the water inlet (9) of the inert gas pressure stabilizing tank (5) through the first circulating water pump water outlet pipeline (4).
3. The dry quenching double super power generation circulating water cooling device as claimed in claim 1, wherein: the inert gas pressure stabilizing unit comprises: an inert gas pressure stabilizing tank (5), a safety valve (7), a blow-down valve (8), a water outlet (10) and a soft water replenishing pipe (20); in order to prevent oxygen in the air from entering the auxiliary spraying circulating water unit, an inert gas pressure stabilizing tank (5) in the inert gas pressure stabilizing unit is filled with nitrogen through an inert gas inlet (6) of the pressure stabilizing tank; the operation of the inert gas pressure stabilizing tank (5) is kept under constant pressure, in order to ensure the operation safety of the inert gas pressure stabilizing unit, a safety valve (7) is arranged on the inert gas pressure stabilizing tank (5), and when the system pressure exceeds the standard, the safety valve (7) is opened to ensure the operation safety of the inert gas pressure stabilizing tank (5); when the quality of the circulating water exceeds the standard, discharging sewage through a drain valve (8) at the bottom of the inert gas pressure stabilizing tank (5); when the water level of the inert gas pressure stabilizing tank (5) is ultralow, water is supplemented into the system through a soft water supplementing pipe (20); circulating water flows to the plate heat exchanger (14) through a water outlet (10) of the inert gas pressure stabilizing tank (5) after pressure stabilization.
4. The dry quenching double super power generation circulating water cooling device as claimed in claim 1, wherein: the air cooling unit comprises a glass fiber reinforced plastic enclosure wall (11), a glass fiber reinforced plastic kinetic energy recovery type air cylinder (12), a coupler and an axial flow fan (13) for providing air circulation, air quantity and air temperature during air-water heat exchange are adjusted according to the circulating water temperature of circulating water of the steam turbine condenser, the air cooling unit is used for adjusting the requirement of the steam turbine generator condenser (2) on the circulating water temperature, and the coupler and the axial flow fan (13) work to enable the glass fiber reinforced plastic kinetic energy recovery type air cylinder (12) in the glass fiber reinforced plastic enclosure wall (11) to form air circulation in the glass fiber reinforced plastic kinetic energy recovery type air cylinder (12).
5. The dry quenching double super power generation circulating water cooling device as claimed in claim 1, wherein: the supplementary circulating water unit that sprays include: the auxiliary spraying water unit comprises a spraying water accumulation pool (15), an auxiliary spraying circulating water pump (17), an auxiliary spraying circulating water pump outlet pipe (18) and a spraying head (19), wherein when the auxiliary spraying water unit works, the auxiliary spraying circulating water pump (17) absorbs water through an auxiliary spraying circulating water pump inlet pipe (16), the water is sprayed to the plate heat exchanger (14) through the auxiliary spraying circulating water pump outlet pipe (18) and the spraying water falls into the spraying water accumulation pool (15) below.
6. The dry quenching double super power generation circulating water cooling device as claimed in claim 1, wherein: the circulating water unit of the steam turbine condenser comprises an auxiliary circulating water pump (1), a circulating water pump water inlet pipeline (3), a first circulating water pump water outlet pipeline (4) and a second circulating water pump water outlet pipeline (4'); one port of the steam turbine generator condenser (2) is connected with a steam turbine generator (22), the other port of the steam turbine generator condenser is connected with a condensate pump (23), the interior of the steam turbine generator condenser (2) is outwards connected with a first circulating water pump water outlet pipeline (4) and a second circulating water pump water outlet pipeline (4') through a coil pipe (24), and the second circulating water pump water outlet pipeline (4') is connected with an auxiliary spraying circulating water pump outlet pipe (18) of an auxiliary spraying circulating water unit through a circulating water pump (1) and a circulating water pump water inlet pipeline (3); the water outlet pipeline (4) of the first circulating water pump is connected with the water inlet (9) of the inert gas pressure stabilizing tank (5) through a pipeline.
7. The dry quenching double super power generation circulating water cooling device as claimed in claim 1, wherein: the inert gas pressure stabilizing unit comprises: an inert gas pressure stabilizing tank (5), an inert gas inlet (6) of the pressure stabilizing tank, a safety valve (7), a blow-down valve (8), a water inlet (9), a water outlet (10) and a soft water replenishing pipe (20); the inert gas pressure stabilizing tank (5) is connected with the auxiliary spray water unit through a water outlet (10), and an air cooling unit is arranged outside the water outlet; the inert gas pressure stabilizing tank (5) is connected with an inert gas inlet (6) of the pressure stabilizing tank, a safety valve (7), a blow-down valve (8), a water outlet (10) and a soft water replenishing pipe (20) through interfaces, the blow-down valve (8) is arranged at the bottom of the inert gas pressure stabilizing tank (5), the water outlet (10) is arranged at the lower bottom of the inert gas pressure stabilizing tank (5), a water inlet (9) is arranged at the upper part of the inert gas pressure stabilizing tank (5), and the safety valve (7) is arranged at the top of the inert gas pressure stabilizing tank (5); the water outlet (10) is connected with the plate heat exchanger (14) through a pipeline.
8. The dry quenching double super power generation circulating water cooling device as claimed in claim 1, wherein: the supplementary circulating water unit that sprays include: spray water ponding pond (15), supplementary spray circulating water pump (17), supplementary spray circulating water pump outlet pipe (18) and shower head (19), shower head (19) are arranged in the upper end of plate heat exchanger (14), spray water ponding pond (15) are in the bottom of plate heat exchanger (14), plate heat exchanger (14) have 4 grades, 4 grades of plate heat exchanger (14) circulating water pump inlet pipe (3) communicate with each other, circulating water pump inlet pipe (3) are connected with supplementary spray circulating water pump inlet pipe (16), supplementary spray circulating water pump (17), supplementary spray water moisturizing pipe (21), supplementary spray circulating water pump (17) are connected with shower head (19) through supplementary spray circulating water pump outlet pipe (18).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201921378606.3U CN211199116U (en) | 2019-08-23 | 2019-08-23 | Dry quenching double-super power generation circulating water cooling device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201921378606.3U CN211199116U (en) | 2019-08-23 | 2019-08-23 | Dry quenching double-super power generation circulating water cooling device |
Publications (1)
Publication Number | Publication Date |
---|---|
CN211199116U true CN211199116U (en) | 2020-08-07 |
Family
ID=71863626
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201921378606.3U Active CN211199116U (en) | 2019-08-23 | 2019-08-23 | Dry quenching double-super power generation circulating water cooling device |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN211199116U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110437850A (en) * | 2019-08-23 | 2019-11-12 | 西安华江环保科技股份有限公司 | A kind of double super generating electricity circulating water cooling systems of Dry Quenching |
-
2019
- 2019-08-23 CN CN201921378606.3U patent/CN211199116U/en active Active
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110437850A (en) * | 2019-08-23 | 2019-11-12 | 西安华江环保科技股份有限公司 | A kind of double super generating electricity circulating water cooling systems of Dry Quenching |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN106801886B (en) | Cooling and heat exchanging system for eliminating white smoke plume of coal-fired power plant and operation method thereof | |
CN204693561U (en) | A kind of UTILIZATION OF VESIDUAL HEAT IN heating installation with peak regulating function | |
CN110455006B (en) | Waste heat recovery and energy cascade utilization coupling system of metallurgical oxygen plant | |
CN203656903U (en) | Boiler blow-down drainage waste heat cascade utilization device | |
CN104296554A (en) | Steam condensing type power station steam condenser chamber vacuumizing system | |
CN211199116U (en) | Dry quenching double-super power generation circulating water cooling device | |
CN201843651U (en) | Afterheat utilizing system of cold circulating water in steam turbine | |
CN204420978U (en) | A kind of energy saving drainage system of boiler hydrophobic development unit | |
CN215924849U (en) | Natural circulating water cooling system for dry quenching double super power generation | |
CN201280954Y (en) | Rear gland sealing steam supply device for condensing steam turbine | |
CN210638530U (en) | Waste heat heating device of dry quenching ultrahigh-temperature ultrahigh-pressure gas condensation type generator set | |
CN204611733U (en) | The recycling system of boiler afterheat | |
CN202532433U (en) | Periodic emission heat recovery system of boiler | |
CN206590926U (en) | Deoxygenation condensate vacuum system | |
CN201934152U (en) | Indirect air cooling system for supercritical unit or ultra-supercritical unit | |
CN204388643U (en) | Condensing-type condenser of power station steam chest pumped vacuum systems | |
CN201421066Y (en) | Secondary steam generator of closed circulating phase change heat supply system of industrial boiler | |
CN201697254U (en) | Jet loom workshop air compressor and air conditioning energy saving system | |
CN202054818U (en) | Softened water circulating system of air compressors in beer production technology | |
CN207850109U (en) | A kind of condensing plant reducing condensed water dissolved oxygen | |
CN207701210U (en) | A kind of jet dynamic control tail gas waste heat utilizing device | |
CN218349273U (en) | Air compressor waste heat recovery system for gasifying liquid carbon dioxide | |
CN214990388U (en) | High salt waste water flue drying solidification equipment | |
CN203949522U (en) | A kind of interior circulated water-cooled vapour condensation device | |
CN216521770U (en) | Air preheating device utilizing low-temperature flue gas waste heat |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant |