CN203531984U - Direct air-cooling unit system with plate-type evaporative condenser set - Google Patents
Direct air-cooling unit system with plate-type evaporative condenser set Download PDFInfo
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- CN203531984U CN203531984U CN201320632653.2U CN201320632653U CN203531984U CN 203531984 U CN203531984 U CN 203531984U CN 201320632653 U CN201320632653 U CN 201320632653U CN 203531984 U CN203531984 U CN 203531984U
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Abstract
The utility model discloses a direct air-cooling unit system with a plate-type evaporative condenser set. The direct air-cooling unit system comprises a low-pressure cylinder, an air cooled condenser and the plate-type evaporative condenser set. A steam outlet of the low-pressure cylinder is communicated with a waste-steam outlet of a steam turbine, the low-pressure cylinder delivers waste steam through a steam outlet pipe to a waste-steam inlet of the air cooled condenser, and the steam outlet pipe is further communicated with a waste-steam inlet of the plate-type evaporative condenser set through a pipe and used for feeding part of waste steam discharged by the steam turbine to the plate-type evaporative condenser set to carry out condensation. According to the direct air-cooling unit system, the steam discharged by the steam turbine is led into the air cooled condenser through the steam outlet pipe connected with the low-pressure cylinder to be condensed, meanwhile, the pipe communicated with the waste steam inlet of the plate-type evaporative condenser set is arranged on the steam outlet pipe, part of the waste steam of the steam turbine is led into the plate-type evaporative condenser set to be condensed, heat loads entering the air cooled condenser are reduced, and therefore the steam outlet pressure of the steam turbine is lowered.
Description
Technical field
Belong to the utility model thermal power engineering, thermal power plant, direct air cooling generator set improve exerts oneself and energy-saving and cost-reducing field, is specifically related to a kind of Direct Air-cooled Unit system that adopts plate evaporating condensator group.
Background technique
The Direct Air-cooled Unit having put into operation at present, ubiquity summer high temperature period operation vacuum is low, unit output declines; The problems such as performance driving economy is low, gross coal consumption rate height.The measure that present stage takes is mainly on Air-Cooling Island, to adopt peak cooling device.
Peak cooling device has two kinds:
Be an evaporative cooling, the demineralized water of atomization is sprayed directly on to heat exchanger surface, utilize water vapor heat absorption to reduce heat exchanger surface temperature, thereby reduce condensing water temperature, reduction unit back pressure.This method is utilized air cooling condenser washing unit conventionally, in the summer high temperature period, air side outlet surface, air cooling unit is one by one sprayed to demineralized water.Because air cooling element number is many, and during spraying cooling, can only successively carry out each unit, so spraying cooling is little to the performance raising effect of whole air cooling condenser.
Another kind is that spraying is cooling, the demineralized water of atomization is sprayed on to the outlet of air cooling blower fan, utilizes water vapor heat absorption to reduce radiator intake temperature; Do not have in addition the water droplet of vaporization to rely on Air Flow to carry and enter spreader surface heat absorption; Thereby improve radiator heat-exchange performance, reduce unit operation back pressure.
All there is following shortcoming in above two kinds of technology:
Demineralized water waste is large, and cool water shower, in atmosphere, can not reclaim; Rate of water consumed in electric generator is increased, increase operating cost;
After water spray, the increasing of cooling-air humidity, heat radiator fin tube-surface humidity increase, and airborne dust is more easily sticked on heat radiator fin pipe, cause the dirty degree of fin tube stolen goods to strengthen, and heat exchange efficiency declines;
Demineralized water and Air Temperature Difference are less, weak effect.Under lower ambient temperature, (spring, autumn), does not almost have effect.
Model utility content
The purpose of this utility model is to address the above problem, and a kind of Direct Air-cooled Unit system that adopts plate evaporating condensator group is provided, and the raising air cooling condenser performance that this system can be larger reduces unit operation back pressure, reaches energy-saving and cost-reducing object; Reduce unit generation water consumption simultaneously, eliminate the energy-conservation cooling technology of direct air cooling system of the defects such as the large and Maintenance Difficulty of operating cost that prior art produces.
For achieving the above object, the technical solution adopted in the utility model is: comprise low pressure (LP) cylinder, air setting vapour device and plate evaporating condensator group; The steam-expelling port of low pressure (LP) cylinder is connected with the exhaust steam of steam turbine outlet, and low pressure (LP) cylinder is delivered to exhaust steam by blow-off line the exhaust steam entrance of air cooling condenser; Blow-off line is also connected with the exhaust steam entrance of plate evaporating condensator group by pipeline, sends into plate evaporating condensator group carry out condensation for a part of exhaust steam that steam turbine is discharged.
Described plate evaporating condensator comprises housing and is arranged on the plate heat exchanger package in housing; Enclosure interior is divided into two chambers in left and right by dehydrater, and the top of one of them chamber is provided with axial-flow blower; Plate heat exchanger package is arranged on the top of another chamber; The top of plate heat exchanger package is provided with spray header, and below is provided with packing tower; The below of packing tower is provided with cooling pond, and cooling pond is connected with spray header by circulating water pump.
Described circulating water pump is arranged at the outside of intake grill.
On described cooling pond, offer recirculated cooling water moisturizing entrance, and moisturizing ingress is provided with float valve.
Described air setting vapour device is all connected with the condensate water tank that is arranged on low pressure (LP) cylinder below by pipeline with the water of condensation outlet separately of plate evaporating condensator group; On the outlet conduit of condensate water tank, be disposed with condensate pump and gland heater.
The some single plate evaporating condensator of described plate heat exchanger package for assembling or dismantle, these single plate evaporating condensators distribute successively by steam main.
The heat exchanging plate runner of described plate evaporating condensator is corrugated, and arranges with regular net-point shape.
Also comprise for extract the vacuum pump of the inner build-up of air of the incondensable gas assembled in plate heat exchanger package and air cooling condenser simultaneously; Vacuum pump extracts the inner air of assembling of air cooling condenser by the vacuum lead being arranged in air cooling condenser.
On the pipeline that described plate evaporating condensator exhaust steam entrance is connected with blow-off line, be also provided with expansion joint, manual modulation valve and the electric control valve for controlling the exhaust steam that enters plate evaporating condensator group.
On described blow-off line, be also provided with the drain water piping that the steam drainage of blow-off line is delivered to condensate water tank.
Compared with prior art, the utlity model has following beneficial effect:
The utility model is introduced air cooling condenser by turbine discharge by the blow-off line being connected with low pressure (LP) cylinder and is carried out condensation, a pipeline being connected with plate evaporating condensator group exhaust steam entrance is set simultaneously on blow-off line, a part of exhaust steam in steam turbine is introduced to plate evaporating condensator group and carry out condensation, reduce and enter air cooling condenser heat load, thereby reduce steam turbine exhaust pressure.
Further, the heat exchanging part of the utility model plate evaporating condensator is the plate heat exchanger package being comprised of some single plate evaporating condensators, above plate heat exchanger package, spray header is set simultaneously, cooling water is evenly sprayed to the outer surface at heat-exchange plate, and make it to form the uniform water film that one deck is very thin, improved the heat exchange efficiency of plate heat exchanger package; In addition, above plate heat exchanger package, be provided with packing tower, the cooling water after heat absorption flows out from plate heat exchanger package bottom, enter packing tower, packing tower plays the effect that is similar to spraying to high-temperature cooling water, make high-temperature cooling water further cooling, flows into the cooling pond of below.
Further, the utility model exhaust steam in steam turbine enters in the corrugated heat-exchange plate runner of plate heat exchanger package, and the net-point shape of heat exchanging plate runner journey rule layout, can make fluid flow state even in whole flow process, improves heat transfer effect.
Further, the utility model arranges axial-flow blower on plate evaporating condensator, under the powerful air inducing of axial-flow blower, has strengthened Air Flow, promotes the evaporation of plate surface moisture film, has strengthened the heat release of exhaust steam; The air that axial-flow blower air inducing forms forms adverse current or cross flow with spraying water from bottom to top, thereby formation cross flow one, make liquid film and exhaust steam be able to abundant heat exchange, constantly be evaporated to water vapor, air stream by rapid flow is taken away, again cooling by the new wind in side when unevaporated high-temperature cooling water flows through filler, be dropped in the water-collecting tray of bottom, raw water service pump recycles.
Further, the utility model arranges cooling pond below plate evaporating condensator, by circulating water pump, the cooling water in cooling pond is introduced to spray header and recycles, and has realized recycling of water resources, has reached the object of the environmental protection that economizes on resources.
Further, in the middle of two Room, left and right of the utility model plate evaporating condensator housing, dehydrater is housed, during work, can effectively realizes the separated of gas-liquid two-phase and control the water rate of wafing.
Further, in the utility model water pond, float valve is set, when moisture constantly evaporates consumption, float valve is just opened automatically, supplements cooling water to normal water level.
Accompanying drawing explanation
Fig. 1 is total system schematic diagram of the present utility model.
Wherein, 1 is low pressure (LP) cylinder; 2 is air setting vapour device; 3 is blow-off line; 4 is condensate water tank; 5 is housing; 6 is plate heat exchanger package; 7 is dehydrater; 8 is axial-flow blower; 9 is spray header; 10 is packing tower; 11 is cooling pond; 12 is circulating water pump; 13 is expansion joint; 14 is manual modulation valve; 15 is electric control valve; 16 is vacuum pump; 17 is condensate pump; 18 is gland heater; 19 is vacuum lead.
Embodiment
Below in conjunction with accompanying drawing, the utility model is described in further detail:
Referring to Fig. 1, the utility model comprises low pressure (LP) cylinder 1, air setting vapour device 2 and plate evaporating condensator group; The steam-expelling port of low pressure (LP) cylinder 1 is connected with the exhaust steam of steam turbine outlet, and low pressure (LP) cylinder 1 is delivered to exhaust steam by blow-off line 3 the exhaust steam entrance of air cooling condenser 2; Blow-off line 3 is also connected with the exhaust steam entrance of plate evaporating condensator by pipeline, for a part of exhaust steam that steam turbine is discharged, sending into plate evaporating condensator group carries out cooling, on the pipeline that plate evaporating condensator group exhaust steam entrance is connected with blow-off line 3, be also provided with expansion joint 13, manual modulation valve 14 and the electric control valve 15 for controlling the exhaust steam that enters plate evaporating condensator, on blow-off line 3, be also provided with the hydrophobic drain water piping that is delivered to condensate water tank 4 of the exhaust steam of blow-off line 3; Plate evaporating condensator comprises housing 5 and is arranged on the plate heat exchanger package 6 in housing 5, the some single plate evaporating condensator of plate heat exchanger package 6 for assembling or dismantle, these single plate evaporating condensators distribute successively by steam main.The heat exchanging plate runner of plate evaporating condensator is corrugated, and arranges with regular net-point shape; Housing 5 inside are divided into two chambers in left and right by dehydrater 7, and the top of one of them chamber is provided with axial-flow blower 8; Plate heat exchanger package 6 is arranged on the top of another chamber; The top of plate heat exchanger package 6 is provided with spray header 9, and below is provided with packing tower 10; The below of packing tower 10 is provided with cooling pond 11, offer recirculated cooling water moisturizing entrance, and moisturizing ingress is provided with float valve on cooling pond 11; Cooling pond 11 is connected with spray header 9 by circulating water pump 12, and circulating water pump 12 is arranged at the outside of intake grill.Air setting vapour device 2 is all connected with the condensate water tank 4 that is arranged on low pressure (LP) cylinder 1 below by pipeline with plate evaporating condensator water of condensation outlet separately, is disposed with condensate pump 17 and gland heater 18 on the outlet conduit of condensate water tank 4.In whole system, be also provided with for extract the incondensable gas of gathering in plate heat exchanger package 6 and the vacuum pump 16 of air cooling condenser 2 inner build-up of air simultaneously; Vacuum pump 16 extracts the inner air of assembling of air cooling condenser 2 by the vacuum lead 19 being arranged in air cooling condenser 2.
Principle of the present utility model:
The utility model is introduced plate evaporating condensator group by part turbine discharge and is carried out condensation, reduces and enters air cooling condenser heat load, thereby reduce steam turbine exhaust pressure.
The plate evaporating condensator of the features such as plate evaporating condensator group is that unit-modularized degree is high, water quality requirement is low, the coefficient of heat transfer is high by having, is convenient to cleaning and maintenance, water consumption is low and environmental suitability is strong carries out organic assembling according to concrete condensation task, its working medium cooling water is through spray header, spray equably the outer surface at heat-exchange plate, and make it to form the uniform water film that one deck is very thin.Exhaust steam in steam turbine enters in corrugated heat-exchange plate runner from upper header, and the net-point shape of rule is arranged, can be made fluid flow state even in whole flow process.Exhaust steam passes to moisture film by heat by heat transferring plate, and by under the powerful air inducing of axial-flow blower, has strengthened Air Flow, promotes the evaporation of plate surface moisture film, has strengthened the heat release of exhaust steam.Water of condensation flows out from plate bottom collector.Part cooling water is entered atmosphere because heat absorption vaporization becomes water vapour by propeller fan carrying-off, again cooling by the new wind in side when the high-temperature cooling water not being evaporated flows through filler, is dropped in the water-collecting tray of bottom, and raw water service pump recycles.
Working procedure of the present utility model is such:
As shown in dotted line frame in Fig. 1, plate evaporating condensator group is mainly comprised of plate heat exchanger, axial-flow blower, circulating water pump, packing tower etc.The axial-flow blower of top right upside is in negative pressure state work; Lower-left side is cross-ventilation chamber, and high-efficiency packing tower is arranged in cross-ventilation chamber; Upper left side is plate heat exchanger, and Qi Ding is equipped with on top spraying water distribution system, and circulating water pump is placed in intake grill outside, and device bottom is circulating water pool.Dehydrater is equipped with in the middle of two Room in left and right, can effectively realize the separated of gas-liquid two-phase and control the water rate of wafing during work.
When summer high temperature period unit high back pressure moves, enable plate evaporating condensator group, part turbine discharge imports each plate evaporating condensator admission collector through extraction line, at corrugated heat-exchange plate runner, is evenly distributed; Cooling water is squeezed into spray header by circulating water pump and is sprayed cloth liquid, at heat-exchange plate outer surface, forms the very thin uniform water film of one deck; The air that axial-flow blower air inducing forms forms adverse current or cross flow with spraying water from bottom to top, thereby formation cross flow one, make liquid film and exhaust steam be able to abundant heat exchange, constantly be evaporated to water vapor, air stream by rapid flow is taken away, again cooling by the new wind in side when unevaporated high-temperature cooling water flows through filler, be dropped in the water-collecting tray of bottom, raw water service pump recycles.Water of condensation is confluxed and be back to steam exhaust device to the jellyfish pipe that condenses, and the incondensable gas that plate evaporating condensator is assembled is pumped to and is vacuumized female pipe by vacuum pump; Float valve is set in water pond, and when moisture constantly evaporates consumption, float valve is just opened automatically, supplements cooling water to normal water level.
The utility model, with respect to peak cooling device, can improve unit in summer operation vacuum by a larger margin.Evaporative type vapour condenser adopts modular design, improve unit vacuum, can increase evaporative type vapour condenser unit.In addition, also can use other industrial water, without demineralized water, reduce operating cost.The utility model heat-transfer coefficient is large, and good effect of heat exchange is convenient to clean and safeguard, environmental suitability is high, and water consumption is lower.
Effect: take 300MW direct air cooling as example, install plate-type evaporative condenser group additional, through calculating, when 30 ℃ of summer environment temperature, under unit rated load, vacuum improves 3kPa, and water consumes about 40t/h.
Claims (10)
1. a Direct Air-cooled Unit system that adopts plate evaporating condensator group, is characterized in that: comprise low pressure (LP) cylinder (1), air setting vapour device (2) and plate evaporating condensator group; Low pressure (LP) cylinder (1) is delivered to exhaust steam by blow-off line (3) the exhaust steam entrance of air cooling condenser (2); Blow-off line (3) is also connected with the exhaust steam entrance of plate evaporating condensator group by pipeline, sends into plate evaporating condensator group carry out condensation for a part of exhaust steam that steam turbine is discharged.
2. the Direct Air-cooled Unit system of employing plate evaporating condensator group according to claim 1, is characterized in that: described plate evaporating condensator comprises housing (5) and is arranged on the plate heat exchanger package (6) in housing (5); Housing (5) is inner is divided into two chambers in left and right by dehydrater (7), and the top of one of them chamber is provided with axial-flow blower (8); Plate heat exchanger package (6) is arranged on the top of another chamber; The top of plate heat exchanger package (6) is provided with spray header (9), and below is provided with packing tower (10); The below of packing tower (10) is provided with cooling pond (11), and cooling pond (11) are connected with spray header (9) by circulating water pump (12).
3. the Direct Air-cooled Unit system of employing plate evaporating condensator group according to claim 2, is characterized in that: described circulating water pump (12) is arranged at the outside of intake grill.
4. the Direct Air-cooled Unit system of employing plate evaporating condensator group according to claim 2, is characterized in that: on described cooling pond (11), offer recirculated cooling water moisturizing entrance, and moisturizing ingress is provided with float valve.
5. the Direct Air-cooled Unit system of employing plate evaporating condensator group according to claim 2, is characterized in that: described air setting vapour device (2) is all connected with the condensate water tank (4) that is arranged on low pressure (LP) cylinder (1) below by pipeline with the water of condensation outlet separately of plate evaporating condensator group; On the outlet conduit of condensate water tank (4), be disposed with condensate pump (17) and gland heater (18).
6. the Direct Air-cooled Unit system of employing plate evaporating condensator group according to claim 2, it is characterized in that: the some single plate evaporating condensator of described plate heat exchanger package (6) for assembling or dismantle, these single plate evaporating condensators distribute successively by steam main.
7. the Direct Air-cooled Unit system of employing plate evaporating condensator group according to claim 6, is characterized in that: the heat exchanging plate runner of described plate evaporating condensator is corrugated, and arranges with regular net-point shape.
8. the Direct Air-cooled Unit system of employing plate evaporating condensator group according to claim 1 and 2, is characterized in that: also comprise for extract the upper incondensable gas of assembling of plate heat exchanger package (6) and the vacuum pump (16) of the inner build-up of air of air cooling condenser (2) simultaneously; Vacuum pump (16) extracts the inner air of assembling of air cooling condenser (2) by the vacuum lead (19) being arranged in air cooling condenser (2).
9. the Direct Air-cooled Unit system of employing plate evaporating condensator group according to claim 8, is characterized in that: on the pipeline that described plate evaporating condensator exhaust steam entrance is connected with blow-off line (3), be also provided with expansion joint (13), manual modulation valve (14) and electric control valve (15) for controlling the exhaust steam that enters plate evaporating condensator group.
10. the Direct Air-cooled Unit system of employing plate evaporating condensator group according to claim 8, is characterized in that: on described blow-off line (3), be also provided with the drain water piping that the steam drainage of blow-off line (3) is delivered to condensate water tank (4).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320632653.2U CN203531984U (en) | 2013-10-14 | 2013-10-14 | Direct air-cooling unit system with plate-type evaporative condenser set |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320632653.2U CN203531984U (en) | 2013-10-14 | 2013-10-14 | Direct air-cooling unit system with plate-type evaporative condenser set |
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| CN203531984U true CN203531984U (en) | 2014-04-09 |
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| CN201320632653.2U Expired - Fee Related CN203531984U (en) | 2013-10-14 | 2013-10-14 | Direct air-cooling unit system with plate-type evaporative condenser set |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103527267A (en) * | 2013-10-14 | 2014-01-22 | 西安热工研究院有限公司 | Direct air-cooling unit system with plate-type evaporative condenser unit adopted |
| CN104632304A (en) * | 2014-12-31 | 2015-05-20 | 温高 | Cooling system and method for recovering vapor of cooling water |
| CN104806309A (en) * | 2015-04-13 | 2015-07-29 | 西安热工研究院有限公司 | Air cooling island condensed water potential energy utilizing system |
| CN104864732A (en) * | 2015-05-15 | 2015-08-26 | 西安热工研究院有限公司 | Evaporation type condenser system used for thermal power plant small steam turbine steam exhaust condensing |
| CN109736905A (en) * | 2019-03-21 | 2019-05-10 | 上海电气电站设备有限公司 | Combine cooling system between steam turbine multistage cylinder |
-
2013
- 2013-10-14 CN CN201320632653.2U patent/CN203531984U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103527267A (en) * | 2013-10-14 | 2014-01-22 | 西安热工研究院有限公司 | Direct air-cooling unit system with plate-type evaporative condenser unit adopted |
| CN103527267B (en) * | 2013-10-14 | 2015-05-27 | 西安热工研究院有限公司 | Direct air-cooling unit system with plate-type evaporative condenser unit adopted |
| CN104632304A (en) * | 2014-12-31 | 2015-05-20 | 温高 | Cooling system and method for recovering vapor of cooling water |
| CN104806309A (en) * | 2015-04-13 | 2015-07-29 | 西安热工研究院有限公司 | Air cooling island condensed water potential energy utilizing system |
| CN104864732A (en) * | 2015-05-15 | 2015-08-26 | 西安热工研究院有限公司 | Evaporation type condenser system used for thermal power plant small steam turbine steam exhaust condensing |
| CN109736905A (en) * | 2019-03-21 | 2019-05-10 | 上海电气电站设备有限公司 | Combine cooling system between steam turbine multistage cylinder |
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