CN104009588A - Evaporative cooling system for vertical shaft motor - Google Patents
Evaporative cooling system for vertical shaft motor Download PDFInfo
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- CN104009588A CN104009588A CN201410271259.XA CN201410271259A CN104009588A CN 104009588 A CN104009588 A CN 104009588A CN 201410271259 A CN201410271259 A CN 201410271259A CN 104009588 A CN104009588 A CN 104009588A
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- H—ELECTRICITY
- H02—GENERATION; CONVERSION OR DISTRIBUTION OF ELECTRIC POWER
- H02K—DYNAMO-ELECTRIC MACHINES
- H02K9/00—Arrangements for cooling or ventilating
- H02K9/19—Arrangements for cooling or ventilating for machines with closed casing and closed-circuit cooling using a liquid cooling medium, e.g. oil
- H02K9/193—Arrangements for cooling or ventilating for machines with closed casing and closed-circuit cooling using a liquid cooling medium, e.g. oil with provision for replenishing the cooling medium; with means for preventing leakage of the cooling medium
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- H—ELECTRICITY
- H02—GENERATION; CONVERSION OR DISTRIBUTION OF ELECTRIC POWER
- H02K—DYNAMO-ELECTRIC MACHINES
- H02K9/00—Arrangements for cooling or ventilating
- H02K9/19—Arrangements for cooling or ventilating for machines with closed casing and closed-circuit cooling using a liquid cooling medium, e.g. oil
- H02K9/20—Arrangements for cooling or ventilating for machines with closed casing and closed-circuit cooling using a liquid cooling medium, e.g. oil wherein the cooling medium vaporises within the machine casing
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- H—ELECTRICITY
- H02—GENERATION; CONVERSION OR DISTRIBUTION OF ELECTRIC POWER
- H02K—DYNAMO-ELECTRIC MACHINES
- H02K9/00—Arrangements for cooling or ventilating
- H02K9/24—Protection against failure of cooling arrangements, e.g. due to loss of cooling medium or due to interruption of the circulation of cooling medium
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- H—ELECTRICITY
- H02—GENERATION; CONVERSION OR DISTRIBUTION OF ELECTRIC POWER
- H02K—DYNAMO-ELECTRIC MACHINES
- H02K9/00—Arrangements for cooling or ventilating
- H02K9/28—Cooling of commutators, slip-rings or brushes e.g. by ventilating
Abstract
An evaporative cooling system for a vertical shaft motor comprises a vacuum pump, an exhaust pipe, an evaporative cooling device and a liquid supplying and draining device. The liquid supplying and draining device comprises a liquid storage main tank, a transition liquid storage tank, a connection pipe and a liquid supplying and draining main pipe. The lower portion of the transition liquid storage tank is connected with a first liquid supplying and draining pipeline and a second liquid supplying and draining pipeline. The first liquid supplying and draining pipeline and the second liquid supplying and draining pipeline are communicated through the connection pipe, and the second liquid supplying and draining pipeline is provided with a main liquid return pipe for communicating a liquid supplying and draining pump and the liquid supplying and draining main pipe. The evaporative cooling device comprises a pressure balancing pipe, a first condenser, a stator bar cooling branch line and a collector ring cooling branch line. The stator bar cooling branch line is connected with the first liquid supplying and draining pipeline, the collector ring cooling branch line is connected with the second liquid supplying and draining pipeline, the pressure balancing pipe is connected to the first condenser and is connected with a steam recycling device through the exhaust pipe, and the vacuum pump is connected with the exhaust pipe. The evaporative cooling system for the vertical shaft motor provides two liquid supplying modes for primary liquid supplying of the evaporative cooling device and can reduce loss of cooling media in the evaporative cooling system.
Description
Technical field
The present invention relates to motor device, relate in particular to a kind of vertical shaft motor evaporative cooling system that comprises evaporation-cooled device, liquid supplying and draining device and exhaust recovery device.
Background technology
Along with improving constantly of motor single-machine capacity, the heat load of motor also significantly increases, and causes that therefrom the temperature rise of winding, collector ring and each position temperature difference increase.Therefore, reducing motor winding, collector ring temperature rise and improve the uniformity of Temperature Distribution, is vital to the reliability service of large-size machine.
At present, the cooling technology of large-size machine generally comprises the technology such as gas cooled, water-cooled, evaporative cooling, adopt transpiration-cooled effect better, can adapt to better the needs of different load operation, can meet the capacity requirement that gas cooled reaches, can overcome water-cooling system cost high and cause hollow conductor stop up problem.Evaporation cooling technique is to realize the cooling of motor by cooperations such as evaporation-cooled device, supervisory control system, liquid supplying and draining device, exhaust recovery devices, and wherein evaporation-cooled device and liquid supplying and draining device have respectively following prior art:
As Chinese patent " 200520036095.9 " discloses a kind of evaporation cooling combined cycle device of hydraulic generator stator, its open day is on December 27th, 2006, its technical scheme comprises the condenser system that is soaked with the stator winding heater of evaporative medium and carries out heat exchange with coolant steam, also comprise the stator collector ring heater that is soaked with evaporative medium, one end of described stator winding heater is by the first collector tube, the first liquid back pipe is connected with condenser bottom, its other end is communicated with first total steam collector, first total steam collector is communicated with the top of condenser by the first steam collector again, one end of described stator collector ring heater is communicated with condenser bottom by the second collector tube, the second liquid back pipe, and its other end is communicated with second total steam collector, and second total steam collector is communicated with the top of condenser by the second steam collector again.
As China Patent No. " 200910091705.8 " discloses a kind of liquid supplying and draining device of evaporating and cooling system of water wheel generator stator, its open day is on 02 03rd, 2010, and its technical scheme comprises feed flow branch road and discharge opeing branch road.Feed flow branch road comprises fluid reservoir, supplying valve, solution feed pump, transition tank, confession/draining solenoid valve; The collector tube of fluid reservoir, supplying valve, solution feed pump, transition tank, confession/draining solenoid valve and generator unit stator evaporative cooling system is linked in sequence successively according to media flow direction, and solution feed pump is in the lowest part of described liquid supplying and draining device.In discharge opeing branch road, the collector tube of generator unit stator evaporative cooling system, confession/draining solenoid valve, transition tank, positive displacement pump, check-valves, tapping valve, fluid reservoir are linked in sequence successively according to media flow direction, and positive displacement pump is in the lowest part of whole device; The power supply of whole device and control are provided by supply and discharge hydraulic power/control cubicle.
In conjunction with above-mentioned two prior aries that patent document is representative, in actual use, still exist following defect: one, above-mentioned liquid supplying and draining device only has a liquid feeding pipeline, and feed liquid way is single, in the time that solution feed pump breaks down, will cause can not feed flow; And, because stator winding heater is different with the position of collector ring heater, need the amount of coolant also different, single feed liquid way can extend the feed flow time to stator winding heater and collector ring heater, causes production efficiency low.Two, because the pressure in liquid feeding pipeline is consistent with ambient pressure, therefore after first feed flow completes, in evaporation-cooled device, also there is air, cause evaporative cooling system to set up the self-loopa time longer, and in running, need repeatedly to start for a long time exhaust recovery device, just can make the pressure of evaporative cooling system reach service requirement.
In addition, condenser in above-mentioned patent is in the time of work, steam contacts with cooling water pipe, in the outer surface generation heat exchange of cooling water pipe and be aggregated into liquid film, but due to the capillary effect of liquid medium, the liquid film that condensation forms can not separate with cooling water pipe outer surface immediately, causes the heat exchange efficiency of steam and cooling water pipe low poor with condensation effect.In order to solve the above-mentioned technical problem of condenser, a kind of efficient pair of cooling pipe double tube sheet condenser disclosed in prior art, its patent No. is " 201220731998.9 ", its open day is on 08 21st, 2013, this patent can be accelerated breaking of condensate film by the sheet shape helical tooth with sawtooth on outer tube outer wall, but under the capillary effect of liquid medium, the speed of separating out of condensate liquid is still slower, still cause condensation effect poor low with condensation efficiency; And, be proven, in condensation process, the condensing rate of steam is very high, and this just causes condenser bottom can accumulate a large amount of condensate liquids, easily floods the cooling water pipe near condenser bottom, thereby reduces the utilance of condenser.And steam directly enters the structure of cylindrical shell one end by air inlet pipe, make the pressure in the each region of inner barrel have difference.
Summary of the invention
The object of the invention is to overcome the above-mentioned problems in the prior art and risk, make up the deficiencies in the prior art, vertical shaft motor evaporative cooling system is provided, the present invention can solve following technical problem: 1, can provide two kinds of feed liquid ways for the first feed flow of evaporation-cooled device, in the time that wherein a kind of feed liquid way breaks down, can use standby mode to continue feed flow, ensure to stablize feed flow; 2, can provide feed flow branch road to stator bar heater and collector ring heater respectively, and two feed flow branch roads can be to stator winding heater and collector ring heater feed flow simultaneously; 3, after first feed flow, the pressure in evaporation-cooled device just can reach operating pressure requirement, and in running, the number of starts of exhaust recovery device is few, can reduce the loss of coolant in evaporative cooling system, and then reduces operating fluid infusion number of times.
For achieving the above object, the technical solution used in the present invention is as follows:
Vertical shaft motor evaporative cooling system, it is characterized in that: comprise vacuum pump, gland steam exhauster, evaporation-cooled device, liquid supplying and draining device and vapour-recovery unit, described liquid supplying and draining device comprises the total tank of liquid storage, transition fluid reservoir, tube connector and confession liquid header, described transition fluid reservoir bottom is connected with for evaporation-cooled device and supplies drain line for drain line with for evaporation-cooled device for second of discharge opeing for first of discharge opeing, described first is communicated with by tube connector for drain line for drain line and second, in described the second confession drain line, be provided with the total liquid back pipe being communicated with for positive displacement pump with confession liquid header, described one end for liquid header is communicated with for drain line with first, the other end is communicated with the total tank of liquid storage, described evaporation-cooled device comprises balance pipe, the first condenser, the cooling branch road of stator bar being connected with the first condenser and the cooling branch road of collector ring being connected with the first condenser, the cooling branch road of described stator bar is connected for drain line with first, the cooling branch road of described collector ring is connected for drain line with second, described balance pipe is connected on the first condenser, and be connected with vapour-recovery unit by gland steam exhauster, described vacuum pump is connected with gland steam exhauster, described tube connector and first is arranged on between liquid header and the cooling branch road of stator bar for drain line tie point, described tube connector and second is arranged on between positive displacement pump and the cooling branch road of collector ring for drain line tie point.
The cooling branch road of described stator bar comprises the first liquid collecting endless tube, stator bar heater, the first collecting ring pipe, the first liquid back pipe and steam collector, one end of stator bar heater is connected with the first condenser with steam collector by the first collecting ring pipe successively, the other end is connected for drain line with first by the first liquid collecting endless tube, and the first liquid back pipe is arranged between the first condenser and the first liquid collecting endless tube; The cooling branch road of described collector ring comprises the second liquid collecting endless tube, collector ring heater, the second collecting ring pipe, the second liquid back pipe and steam collector, one end of collector ring heater is connected with the first condenser with steam collector by the second collecting ring pipe successively, the other end is connected for drain line with second by the second liquid collecting endless tube, and the second liquid back pipe is arranged between the first condenser and the second liquid collecting endless tube.
On described the first liquid collecting endless tube, be connected with the first liquid level gauge, on described the second liquid collecting endless tube, be connected with the second liquid level gauge, the top of described the first liquid level gauge and the second liquid level gauge is all connected with balance pipe, on balance pipe, be at least provided with one with the valve one of air communication.
Described vapour-recovery unit comprises aspiration pump, the second condenser, filter, catch box and water tank, the inlet end of described aspiration pump is connected with gland steam exhauster, outlet side is connected with the second condenser, described the second condenser is connected with water tank by filter, and described catch box is connected with the second condenser and filter respectively.
The top of the total tank of described liquid storage is provided with valve 16, is provided with the 4th liquid level gauge on sidewall, and bottom is provided with scroll wheel and the discharging tube one being connected with confession liquid header, is provided with valve 17 on discharging tube one; Described one end for liquid header is provided with valve 18, and the other end is provided with valve 14; On described transition fluid reservoir, be connected with discharging tube two, valve seven and the 3rd liquid level gauge, on discharging tube two, be provided with valve six.
One end of described gland steam exhauster is provided with valve five, and the other end is provided with valve two, on the gland steam exhauster between valve five and valve two, is provided with valve three and electromagnetically operated valve, and electromagnetically operated valve is in parallel with valve three; Described vacuum pump is connected with blast pipe by valve four.
Described first arranges valve 13 and valve 15 in drain line, and described valve 13 and valve 15 are separately positioned on for liquid header and the first both sides for drain line junction; Described second is respectively arranged with valve eight and valve ten for the two ends of drain line, and the described positive displacement pump that supplies is arranged between valve eight and valve ten; Described total liquid back pipe is arranged on for positive displacement pump and between liquid header, and is provided with valve nine on total liquid back pipe; Between described the first liquid collecting endless tube and tube connector, be provided with valve 11, between described the second liquid collecting endless tube and tube connector, be provided with valve 12.
Described transition fluid reservoir be arranged on the total tank of liquid storage above or below.
Described the first condenser comprises cylindrical shell, is provided with many cooling water pipes in described cylindrical shell, is provided with the coating for condensate liquid is separated with cooling water pipe on the outer surface of described cooling water pipe.
Described coating is made up of polytetrafluoroethylene, Kynoar, silane organic substance or ceramic material, and its thickness is 1 μ m-0.5mm.
Described cooling water pipe is individual layer cooling water pipe or double-deck cooling water pipe, and during for double-deck cooling water pipe, described coating is arranged on the outer tube-surface of double-deck cooling water pipe.
Described cooling water pipe is pipe or finned pipe, during for finned pipe, on described fin, is provided with coating.
Described cylindrical shell top is provided with steam inlet and gas bag, and described steam inlet communicates with gas bag, and described gas bag communicates with cylinder lumen.
Described cylindrical shell bottom is provided with hole for back flow, is provided with the liquid bag for collecting condensate liquid in described cylindrical shell, and described hole for back flow communicates with liquid bag.
Employing the invention has the advantages that:
One, in the present invention, when to the first feed flow of evaporation-cooled device, both can be by the direct feed flow of confession positive displacement pump of transition fluid reservoir below, also can extract in advance the air in evaporation-cooled device pipeline out by vacuum pump, make the pressure in pipeline be less than ambient pressure, utilize pressure differential that the coolant in total liquid storage tank is pressed in evaporation-cooled device.And, while adopting vacuum-pump liquid-supplying, in feed flow front evaporator cooling device, form certain vacuum degree, after coolant supply puts in place, because the air in liquid feeding pipeline is little, not only be conducive to accelerate first liquid supply speed, also help the Rapid Establishment of whole evaporation-cooled device self-loopa, make the pressure in evaporation-cooled device meet from the beginning the requirement that runs on low pressure conditions, thereby can start less or not start vapour-recovery unit, thereby can avoid the loss of coolant in running, and then can greatly reduce feed flow number of times and the liquid supply rate to evaporation-cooled device in running.On the other hand, even break down for positive displacement pump, can also adopt vacuum pump to carry out first feed flow, these two kinds of feed liquid ways coordinate, and have ensured the stability of first feed flow, are conducive to enhance productivity.In addition, by coordinating of respective valves and pipeline, first can be separately to the cooling branch road feed flow of stator bar for drain line, second can be separately to the cooling branch road feed flow of collector ring for drain line, two-way coordinates and can, simultaneously to evaporation-cooled device feed flow, significantly reduce the feed flow time for discharge opeing branch road.Compared with the prior art that is representative with China Patent No. " 200910091705.8 ", the present invention is reducing one under the prerequisite of positive displacement pump, not only can realize first feed flow, can also provide feed liquid way for subsequent use for first feed flow, effectively ensure the stable operation of whole evaporative cooling system.
Two, in the present invention, tube connector one end is connected to second in drain line, the other end is connected to the first liquid collecting endless tube and supplies the structure between liquid header, both made first for drain line and second for drain line can be respectively to the cooling branch road of stator bar and the cooling branch road feed flow of collector ring and fluid infusion, also make first for drain line or second for drain line can be respectively to the cooling branch road of stator bar and the cooling branch road feed flow of collector ring and fluid infusion, feed flow fluid infusion mode is varied, has effectively ensured the reliability of evaporative cooling system.
Three, in the present invention, can monitor in real time the amount of coolant in evaporation-cooled device heater respectively by the first liquid level gauge and the second liquid level gauge, ensure that liquid supplying and draining device is to the real-time fluid infusion of evaporation-cooled device heater.In addition, break down all can not be to the first feed flow of evaporation-cooled device time when vacuum pump or for positive displacement pump, can pass through the manual feed flow of a pair of evaporation-cooled device of valve, avoid affecting production efficiency.
Four, in the present invention, described vapour-recovery unit comprises aspiration pump, the second condenser, filter, catch box and water tank, the inlet end of described aspiration pump is connected with gland steam exhauster, outlet side is connected with the second condenser, described the second condenser is connected with water tank by filter, and described catch box is connected with the second condenser and filter respectively.This structure can reclaim the steam medium of discharging in evaporation-cooled device effectively, compared with prior art, by increasing filter, can avoid to greatest extent medium steam to enter atmosphere.
Five, in the present invention, the total tank of liquid storage is connected with liquid header by the discharging tube one with valve 17, and the total tank of liquid storage bottom is provided with the structure of scroll wheel, make the total tank of liquid storage can continue, to other evaporative cooling system feed flow, to have improved the utilance of the total tank of liquid storage after to one of them evaporative cooling system feed flow.Because the price of the total tank of liquid storage is very expensive, therefore, multiple evaporative cooling systems share a total tank of liquid storage and can also reduce production costs again.
Six, in the present invention, one end of described gland steam exhauster is provided with valve five, the other end is provided with valve two, on gland steam exhauster between valve five and valve two, be provided with valve three and electromagnetically operated valve, electromagnetically operated valve is in parallel with valve three, when this structure can ensure that electromagnetically operated valve breaks down, can realize steam discharge by manual control valve three.
Seven, in the present invention, described transition fluid reservoir be arranged on the total tank of liquid storage above or below, this structure makes transition fluid reservoir can be arranged on different terrain, is conducive to the mounting arrangement of whole evaporative cooling system.
Eight, in the present invention, in whole evaporative cooling system, be proven, mutual combination by valve one to valve 18, can produce multiple specific for draining mode, in the time that a certain confession draining mode breaks down, can adopt other standby mode feed flow, ensure the stable operation of whole evaporative cooling system.In addition, because fluid infusion or discharge opeing etc. in first feed flow, running to evaporation-cooled device have the multiple draining mode that supplies, this just makes people multiple best for draining mode for choosing in draining mode, to ensure to supply discharge opeing efficiency higher.
Nine, in the present invention, in the first condenser, can accelerate the separating rate of condensate liquid and cooling water pipe by coating, the condensate film that steam and cooling water pipe generation heat exchange generate can depart from from the outer surface of cooling water pipe rapidly, is conducive to improve condensation effect and condensation efficiency; Compared with the prior art that is representative with China Patent No. " 201220731998.9 ", the present invention arranges one deck coating on the outer surface of outer tube just can accelerate the speed that condensate film departs from cooling water pipe, obtains better cooling effect.
11, in the present invention, the coating of being made by polytetrafluoroethylene, Kynoar, silane organic substance or ceramic material, can with cooling water pipe outer surface strong bonded, again not can with cooling fluid generation chemical reaction, also there is the characteristic of low surface tension simultaneously, be conducive to further accelerate the speed that condensate film departs from cooling water pipe.In addition, if the thickness of described coating is less than 1 μ m, the speed on condensate film disengaging cooling water pipe surface will be reduced, thereby weaken the heat transfer effect of cooling water pipe, if and the thickness of described coating is greater than 0.5mm, again the thermal resistance that causes cooling water pipe outer surface is significantly increased, not only can significantly weaken the heat exchange of steam and cooling water pipe, also can cause the manufacture difficulty of condenser and cost to raise.Therefore, the thickness of described coating is set to 1 μ m-0.5mm, can ensure that cooling water pipe outer surface thermal resistance does not significantly increase, and can significantly improve the speed that condensate film departs from cooling water pipe, can, can adapt to the needs of different occasions by manufacture difficulty and cost control in the reasonable scope.
12, in the present invention, described cooling water pipe can be individual layer cooling water pipe, can be also double-deck cooling water pipe, can be used in the condenser of different size, and the scope of application is wider.While adopting double-deck cooling water pipe, can also between two-layer pipe, gap be set, if the coolant of inner layer pipe leaks, can detect by the checkout gear being arranged in gap, can avoid to greatest extent the coolant leakage pollution evaporative cooling medium of inner layer pipe.
13, in the present invention, described cooling water pipe is pipe or finned pipe, during for finned pipe, on described fin, is provided with coating, can increase the contact area of steam and outer tube by fin, thereby improves cooling rate.
14, in the present invention, the gas bag arranging on cylindrical shell top, the steam that makes to enter condenser can be dispersed to rapidly the regional of condenser inner chamber, has the effect of balanced condenser internal pressure, is conducive to improve the utilance of condensation effect and condenser.
15, in the present invention, arrange one in cylindrical shell bottom and be specifically designed to the liquid bag that stores the condensate liquid that obtains after condensation, be conducive to prevent that lower floor's cooling water pipe liquid that is condensed from flooding and condenser utilance is reduced.
Brief description of the drawings
Fig. 1 is structural representation of the present invention;
Fig. 2 is the structural representation of condenser in the present invention;
Fig. 3 is that the A of Fig. 2 is to view;
Fig. 4 is A-A cutaway view of Fig. 2;
Being labeled as in figure: 1, balance pipe, 2, stator bar heater, 3, collector ring heater, 4, the first collecting ring pipe, 5, the second collecting ring pipe, 6, steam collector, 7, the first liquid collecting endless tube, 8, the second liquid collecting endless tube, 9, the first liquid back pipe, 10, the second liquid back pipe, 11, insulation drainage tube, 12, the first condenser, 13, the first liquid level gauge, 14, the second liquid level gauge, 15, gland steam exhauster, 16, vacuum pump, 17, aspiration pump, 18, the second condenser, 19, filter, 20, catch box, 21, water tank, 22, machine hole, 23, valve one, 24, valve two, 25, valve three, 26, electromagnetically operated valve, 27, valve four, 28, valve five, 29, the total tank of liquid storage, 30, transition fluid reservoir, 31, for positive displacement pump, 32, valve six, 33, valve seven, 34, the 3rd liquid level gauge, 35, valve eight, 36, total liquid back pipe, 37, valve nine, 38, for liquid header, 39, second for drain line, 40, valve ten, 41, tube connector, 42, discharging tube one, 43, discharging tube two, 44, valve 11,45, valve 12,46, first for drain line, 47, valve 13,48, valve 14,49, valve 15,50, scroll wheel, 51, valve 16,52, valve 17,53, valve 18,54, the 4th liquid level gauge, 55, gas bag, 56, liquid bag, 57, cylindrical shell, 58, end cap, 59, cooling water pipe, 60, cooling water inlet and outlet connectors, 61, steam inlet, 62, hole for back flow, 63, interface.
Embodiment
Embodiment 1
Vertical shaft motor evaporative cooling system, comprise vacuum pump 16, gland steam exhauster 15, evaporation-cooled device, liquid supplying and draining device and vapour-recovery unit, described liquid supplying and draining device comprises the total tank 29 of liquid storage, transition fluid reservoir 30, tube connector 41 and confession liquid header 38, described transition fluid reservoir 30 bottoms are connected with for evaporation-cooled device and supply drain line 39 for drain line 46 with for evaporation-cooled device for second of discharge opeing for first of discharge opeing, described first is communicated with by tube connector 41 for drain line 39 for drain line 46 and second, in described the second confession drain line 39, be provided with the total liquid back pipe 36 being communicated with for positive displacement pump 31 with confession liquid header 38, described one end for liquid header 38 is communicated with for drain line 46 with first, the other end is communicated with the total tank 29 of liquid storage, described evaporation-cooled device comprises balance pipe 1, the first condenser 12, the cooling branch road of stator bar being connected with the first condenser 12 and the cooling branch road of collector ring being connected with the first condenser 12, the cooling branch road of described stator bar is connected for drain line 46 with first, the cooling branch road of described collector ring is connected for drain line 39 with second, described balance pipe 1 is connected on the first condenser 12, and be connected with vapour-recovery unit by gland steam exhauster 15, described vacuum pump 16 is connected with gland steam exhauster 15, described tube connector 41 and first is arranged on between liquid header 38 and the cooling branch road of stator bar for drain line 46 tie points, described tube connector 41 and second is arranged on between positive displacement pump 31 and the cooling branch road of collector ring for drain line 39 tie points.
The preferred implementation of the present embodiment is, the cooling branch road of described stator bar comprises the first liquid collecting endless tube 7, stator bar heater, the first collecting ring pipe 4, the first liquid back pipe 9 and steam collector 6, one end of stator bar heater is connected with the first condenser 12 with steam collector 6 by the first collecting ring pipe 4 successively, the other end is connected for drain line 46 with first by the first liquid collecting endless tube 7, and the first liquid back pipe 9 is arranged between the first condenser 12 and the first liquid collecting endless tube 7; The cooling branch road of described collector ring comprises the second liquid collecting endless tube 8, collector ring heater 3, the second collecting ring pipe 5, the second liquid back pipe 10 and steam collector 6, one end of collector ring heater 3 is connected with the first condenser 12 with steam collector 6 by the second collecting ring pipe 5 successively, the other end is connected for drain line 39 with second by the second liquid collecting endless tube 8, and the second liquid back pipe 10 is arranged between the first condenser 12 and the second liquid collecting endless tube 8.Wherein, stator bar heater is connected with the first collecting ring pipe 4 and the first liquid collecting endless tube 7 by insulation drainage tube 11 respectively, and described collector ring heater 3 is connected with the second collecting ring pipe 5 and the second liquid collecting endless tube 8 by insulation drainage tube 11 respectively.
Further, on described the first liquid collecting endless tube 7, be connected with the first liquid level gauge 13, on described the second liquid collecting endless tube 8, be connected with the second liquid level gauge 14, and the top of the first liquid level gauge 13 and the second liquid level gauge 14 is all connected with balance pipe 1, on balance pipe 1, be at least provided with one with the valve 1 of air communication.In actual use, the first liquid level gauge 13 is to be indirectly connected with the first condenser 12 with the top of the second liquid level gauge 14, break down all can not carry out first feed flow to evaporation-cooled device time when vacuum pump 16 with for positive displacement pump 31, can pass through one 23 pairs of manual feed flows of evaporation-cooled device of valve.
The another preferred implementation of the present embodiment is, described vapour-recovery unit comprises aspiration pump 17, the second condenser 18, filter 19, catch box 20 and water tank 21, the inlet end of described aspiration pump 17 is connected with gland steam exhauster 15, outlet side is connected with the second condenser 18, described the second condenser 18 is connected with water tank 21 by filter 19, and described catch box 20 is connected with the second condenser 18 and filter 19 respectively.When recovered steam, open aspiration pump 17, take out institute's pump by steam pump to the second condenser 18, gas after the second condenser 18 enters filter 19 and filters, tail gas after filtering enters in water tank 21, after the water in water tank 21 purifies, discharge, the condensate liquid that steam produces after the second condenser 18 and filter 19 enters in catch box 20 again.Further, preferably between water tank 21 and filter 19, valve is set, prevents that the water in water tank 21 from entering filter 19.The filter 19 that the porous materials such as its middle filtrator 19 is active carbon are filter core, aspiration pump 17 is compressor or air blast.
The another preferred implementation of the present embodiment is, the top of the total tank 29 of described liquid storage is provided with valve 16, on sidewall, be provided with the 4th liquid level gauge 54, bottom is provided with and the discharging tube 1 being connected for liquid header 38, is provided with valve 17 on discharging tube 1; Described one end for liquid header 38 is provided with valve 18, and the other end is provided with valve 14; On described transition fluid reservoir 30, be connected with discharging tube 2 43, valve 7 33 and the 3rd liquid level gauge 34, on discharging tube 2 43, be provided with valve 6 32; One end of described gland steam exhauster 15 is provided with valve 5 28, and the other end is provided with valve 2 24, is provided with valve 3 25 and electromagnetically operated valve 26 on the gland steam exhauster 15 between valve 5 28 and valve 2 24, and electromagnetically operated valve 26 is in parallel with valve 3 25; Described vacuum pump 16 is connected with blast pipe by valve 4 27; Described first arranges valve 13 and valve 15 in drain line 46, and described valve 13 and valve 15 are separately positioned on for liquid header 38 and the first both sides for drain line 46 junctions; Described second is respectively arranged with valve 8 35 and valve 10 for the two ends of drain line 39, and the described positive displacement pump 31 that supplies is arranged between valve 8 35 and valve 10; Described total liquid back pipe 36 is arranged on for positive displacement pump 31 and between liquid header 38, and is provided with valve 9 37 on total liquid back pipe 36; Between described the first liquid collecting endless tube 7 and tube connector 41, be provided with valve 11, between described the second liquid collecting endless tube 8 and tube connector 41, be provided with valve 12.Be proven, by valve 1 to the cooperatively interacting and combining of valve 18, can produce multiple specific for draining mode, in the time that a certain confession draining mode breaks down, can adopt other standby mode to continue feed flow, ensure the stable operation of whole evaporative cooling system.In addition, because fluid infusion or discharge opeing etc. in first feed flow, running to evaporation-cooled device have the multiple draining mode that supplies, this just makes people multiple best for draining mode for choosing in draining mode, to ensure to supply discharge opeing efficiency higher.
In the present embodiment, the total tank of described liquid storage 29 bottoms are provided with scroll wheel 50, and the total tank 29 of liquid storage is connected with liquid header by the discharging tube 1 with valve 17, therefore the total tank 29 of liquid storage is dismantled and assembled and mobile, make the total tank 29 of same liquid storage respectively to multiple evaporative cooling system feed flows, to have improved the utilance of the total tank 29 of liquid storage.Further, after first feed flow completes, vacuum pump 16 also can be removed, and detachable vacuum pump 16 coordinates with the total tank 29 of liquid storage movably, makes many units can share a total tank 29 of liquid storage and vacuum pump 16, the purchase cost of significantly having saved equipment.Wherein, because the two ends for liquid header 38 are provided with valve, therefore, after the feed flow of evaporation-cooled device completes, removing the total tank 29 of liquid storage can not affect the normal operation of evaporation-cooled device.
In the present embodiment, preferably transition fluid reservoir 30 is arranged on the below of the total tank 29 of liquid storage, and the lowest point of preferred discharging tube 1 is higher than the highest liquid level of transition fluid reservoir 30, to ensure that the coolant in the total tank 29 of liquid storage can enter transition fluid reservoir 30 fast.But at some extreme terrain, transition fluid reservoir 30 also can be arranged on the top of the total tank 29 of liquid storage.
In the present embodiment, described vapour-recovery unit, evaporation-cooled device and liquid supplying and draining device are all fixedly installed in machine hole 22.
In the present embodiment, described aspiration pump 17 is connected with supervisory control system of the prior art.
In the present embodiment, in order further to ensure the stable operation of evaporative cooling system, also can be for subsequent use for positive displacement pump 31 for increasing in drain line 39 second.In addition, because the present invention only has one for positive displacement pump 31, therefore only need one for subsequent use and supply positive displacement pump 31, and the patent No. is for having two in " 200910091705.8 " patent for positive displacement pump 31, just need to increase by two if this patent increases stand-by pump.Therefore, compared with prior art, do not increasing or increasing for subsequent use confession under the situation of positive displacement pump 31, production cost of the present invention is all well below prior art.
In the present invention, the confession discharge opeing process of described liquid supplying and draining device comprises the feed flow first after installing or having overhauled, automatic liquid supply and the discharge opeing in running, feed flow first after wherein installing or having overhauled comprises three kinds of feed liquid methods, for clear, respectively said process is elaborated below.
(1), install or overhauled after feed flow first.
Method 1: use for positive displacement pump 31 feed flows, first valve-off 9 37, valve 15, valve 6 32, valve 3 25 and valve 4 27, open all the other valves, coolant in the total tank 29 of liquid storage is by naturally flowing into transition fluid reservoir 30 for liquid header 38 and first for drain line 46, the 3rd liquid level gauge 34 on transition fluid reservoir 30 reaches while starting liquid level for positive displacement pump 31, start for positive displacement pump 31, coolant in transition fluid reservoir 30 is pumped into evaporation-cooled device by second for drain line 39, owing to being greater than the flow of the first coolant for drain line 46 for the pump output to coolant of positive displacement pump 31, so, the registration of the 3rd liquid level gauge 34 will decline, when being down to while stopping liquid level, quit work for positive displacement pump 31, prevent from dallying for positive displacement pump 31, in the time that the registration of the 3rd liquid level gauge 34 reaches startup liquid level again, again start for positive displacement pump 31 feed flows, so repeat, in the time that the first liquid level gauge 13 readings reach predetermined fluid level, valve-off 11, in the time that the second liquid level gauge 14 readings reach predetermined fluid level, valve-off 12, valve 1, valve 8 35, valve 7 33 and confession positive displacement pump 31, the total tank 29 of liquid storage continues to fill with liquid in transition fluid reservoir 30, in the time that the reading of the 3rd liquid level gauge 34 approaches the highest liquid level, valve-off 16, valve 17 and valve 18, after the 3rd liquid level gauge 34 registrations are stable, valve-off 7 33 and valve 14.
Method 2: when cannot normally working for positive displacement pump 31, and can not change in time time, use vacuum pump 16 feed flows, first valve-off 1, valve 5 28, valve 6 32, valve 9 37, valve 10, valve 13 and valve 17, open all the other valves, air in evaporation-cooled device pipeline is pumped with vacuum pump 16, then valve-off 4 27 and vacuum pump 16, open valve 17.Because the air pressure in evaporation-cooled device pipeline is far below atmospheric pressure, therefore the coolant in the total tank 29 of liquid storage will be inhaled into evaporation-cooled device for drain line 46 by first.In the time that the first liquid level gauge 13 readings reach predetermined fluid level, valve-off 11, valve-off 12 and valve 15 in the time that the second liquid level gauge 14 readings reach predetermined fluid level.Then open valve 13, coolant flows into transition fluid reservoir 30 naturally.In the time that the 3rd liquid level gauge 34 registrations approach predetermined value, valve-off 16, valve 17 and valve 18, after the 3rd liquid level gauge 34 registrations are stable, valve-off 7 33 and valve 14.In normal course of operation, valve 2 24, valve 5 28 and valve 8 35 are in normally open, valve 1, valve 3 25, valve 4 27, valve 6 32, valve 9 37, valve 15 and valve 18 are in normally off, and valve 7 33, valve 10, valve 11 and valve 12 are opened in the time of fluid infusion.
Method 3: in the time supplying positive displacement pump 31 and vacuum pump 16 all cannot normally work and can not change in time, from valve 1, evaporation-cooled device is carried out to first feed flow.
(2) automatic liquid supply in running
In running, exhaust action can be discharged the part evaporative cooling medium steam in evaporation-cooled device, can reduce the amount of coolant in cooling circuit, so need the liquid level of coolant in Real-Time Monitoring cooling circuit in running.If the output valve of the first liquid level gauge 13 is during lower than fluid infusion liquid level, start for positive displacement pump 31, and open valve 7 33, valve 10 and valve 11, coolant in transition fluid reservoir 30 is pumped to the first liquid collecting endless tube 7 and stator bar heater 2 etc., in the time that the first liquid level gauge 13 readings reach predetermined fluid level, close for positive displacement pump 31, valve 7 33, valve 10 and valve 11, system completes automatic liquid supply one time.If the output valve of the second liquid level gauge 14 is during lower than fluid infusion liquid level, start for positive displacement pump 31, valve 7 33, valve 10 and valve 12 are opened, coolant in transition fluid reservoir 30 is pumped to, the second liquid collecting endless tube 8 and collector ring heater 3 etc., in the time that the second liquid level gauge 14 readings reach predetermined fluid level, valve 7 33, valve 10 and valve 12 are closed, and close for positive displacement pump 31, and system completes automatic liquid supply one time.If the 3rd liquid level gauge 34 during lower than fluid infusion liquid level, utilizes the total tank 29 of liquid storage and for liquid header 38 to 30 fluid infusion of transition fluid reservoir.
(3) discharge opeing
In the time that evaporation-cooled device needs discharge opeing, valve-off 2 24, valve 6 32, valve 10 and valve 14, open all the other valves, coolant in evaporation-cooled device pipeline is back to transition fluid reservoir 30 by first for drain line 46, in the time that the 3rd liquid level gauge 34 registrations reach discharge opeing liquid level, start for positive displacement pump 31, coolant is pumped into the total tank 29 of liquid storage by total liquid back pipe 36, owing to for positive displacement pump 31, the flow that pumps of coolant being greater than to the first flow for coolant in drain line 46, so, the 3rd liquid level gauge 34 registrations will decline, when being down to while stopping discharge opeing liquid level, quit work for positive displacement pump 31, to prevent that supply and discharge liquid pump 31 from dallying, in the time that the 3rd liquid level gauge 34 registrations reach discharge opeing liquid level again, again start for positive displacement pump 31 discharge opeings, so repeat, until medium is discharged totally.
In the present invention, the course of work of described vapour-recovery unit is: when the steam pressure in balance pipe 1 is during higher than 0.06MPa, electromagnetically operated valve 26 and aspiration pump 17 leave, and in cooling circuit, unnecessary steam is drawn into the second condenser 18, and steam is aggregated into liquid, tail gas enters filter 19, entrained steam is aggregated into liquid, and filter 19 tail gas enter water tank 21, finally enter air, when pressure in balance pipe 1 is during lower than the opening pressure of electromagnetically operated valve 26, electromagnetically operated valve 26 and aspiration pump 17 are closed.Valve 3 25 is hand by-pass valve, in the time that electromagnetically operated valve 26 cannot normally be opened, carries out exhaust by manual unlocking valve 3 25.
Embodiment 2
The present embodiment and above-described embodiment are basic identical, and the main distinction is: described the first condenser 12 comprises cylindrical shell 57, and the two ends of described cylindrical shell 57 are respectively arranged with end cap 58, on one of them end cap 58, is provided with cooling water inlet and outlet connectors 60; In described cylindrical shell 57, be provided with many cooling water pipes 59, on the outer surface of described cooling water pipe 59, be provided with the coating for condensate liquid is separated with cooling water pipe 59; Described cylindrical shell 57 tops are provided with steam inlet 61 and gas bag 55, and described gas bag 55 communicates with cylindrical shell 57 inner chambers, are provided with the interface 63 for connecting balance pipe 1 on described gas bag 55, and described steam inlet 61 is communicated with gas bag 55 and steam collector 6 respectively; Described cylindrical shell 57 bottoms are provided with hole for back flow 62, are provided with the liquid bag 56 for collecting condensate liquid in described cylindrical shell 57, and the top of described hole for back flow 62 communicates with liquid bag 56, bottom by joint respectively with the first liquid back pipe 9 and second time liquid be communicated with.Wherein, the second condenser 18 is different from the structure of the first condenser 12, and the second condenser 18 is conventional condenser of the prior art.
In the present embodiment, described coating is made up of polytetrafluoroethylene, Kynoar, silane organic substance or ceramic material, and coating layer thickness can be 1 μ m, can be also 0.5mm, and the thickness of preferred coatings is 0.1mm.Adopt above-mentioned material to make the coating that thickness is 0.1mm, there is the characteristic of low surface tension, can either with cooling water pipe 59 strong bonded, there is not again obvious physical property with coolant generation chemical reaction and in coolant and change, be conducive to accelerate the separating rate of condensate liquid and cooling water pipe 59.
The preferred implementation of the present embodiment is, described cooling water pipe 59 is individual layer cooling water pipe 59 or double-deck cooling water pipe 59, and during for double-deck cooling water pipe 59, described coating is arranged on the outer tube-surface of double-deck cooling water pipe 59.
Further, described cooling water pipe 59 is pipe or finned pipe, during for finned pipe, is provided with equally coating on described fin.
Claims (10)
1. vertical shaft motor evaporative cooling system, it is characterized in that: comprise vacuum pump (16), gland steam exhauster (15), evaporation-cooled device, liquid supplying and draining device and vapour-recovery unit, described liquid supplying and draining device comprises the total tank of liquid storage (29), transition fluid reservoir (30), tube connector (41) and confession liquid header (38), described transition fluid reservoir (30) bottom is connected with for evaporation-cooled device and supplies drain line (39) for drain line (46) with for evaporation-cooled device for second of discharge opeing for first of discharge opeing, described first is communicated with by tube connector (41) for drain line (39) for drain line (46) and second, in described the second confession drain line (39), be provided with the total liquid back pipe (36) being communicated with for positive displacement pump (31) with confession liquid header (38), described one end for liquid header (38) is communicated with for drain line (46) with first, the other end is communicated with the total tank of liquid storage (29), described evaporation-cooled device comprises balance pipe (1), the first condenser (12), the cooling branch road of stator bar being connected with the first condenser (12) and the cooling branch road of collector ring being connected with the first condenser (12), the cooling branch road of described stator bar is connected for drain line (46) with first, the cooling branch road of described collector ring is connected for drain line (39) with second, described balance pipe (1) is connected on the first condenser (12), and be connected with vapour-recovery unit by gland steam exhauster (15), described vacuum pump (16) is connected with gland steam exhauster (15), described tube connector (41) and first is arranged on between liquid header (38) and the cooling branch road of stator bar for drain line (46) tie point, described tube connector (41) and second is arranged on between positive displacement pump (31) and the cooling branch road of collector ring for drain line (39) tie point.
2. vertical shaft motor evaporative cooling system as claimed in claim 1, it is characterized in that: on described the first liquid collecting endless tube (7), be connected with the first liquid level gauge (13), on described the second liquid collecting endless tube (8), be connected with the second liquid level gauge (14), the top of described the first liquid level gauge (13) and the second liquid level gauge (14) is all connected with balance pipe (1), on balance pipe (1), be at least provided with one with the valve one (23) of air communication.
3. vertical shaft motor evaporative cooling system as claimed in claim 1, it is characterized in that: the top of the total tank of described liquid storage (29) is provided with valve ten six (51), on sidewall, be provided with the 4th liquid level gauge (54), bottom is provided with scroll wheel (50) and the discharging tube one (42) being connected with confession liquid header (38), is provided with valve ten seven (52) on discharging tube one (42); Described one end for liquid header (38) is provided with valve ten eight (53), and the other end is provided with valve ten four (48); On described transition fluid reservoir (30), be connected with discharging tube two (43), valve the seven (33) and the 3rd liquid level gauge (34), on discharging tube two (43), be provided with valve six (32).
4. the vertical shaft motor evaporative cooling system as described in claim 1,2 or 3, it is characterized in that: one end of described gland steam exhauster (15) is provided with valve five (28), the other end is provided with valve two (24), on gland steam exhauster (15) between valve five (28) and valve two (24), be provided with valve three (25) and electromagnetically operated valve (26), electromagnetically operated valve (26) is in parallel with valve three (25); Described vacuum pump (16) is connected with blast pipe by valve four (27).
5. vertical shaft motor evaporative cooling system as claimed in claim 1, it is characterized in that: described first in drain line (46), valve ten three (47) and valve ten five (49) being set, described valve ten three (47) and valve ten five (49) are separately positioned on for liquid header (38) and the first both sides for drain line (46) junction; Described second is respectively arranged with valve eight (35) and valve ten (40) for the two ends of drain line (39), and the described positive displacement pump (31) that supplies is arranged between valve eight (35) and valve ten (40); Described total liquid back pipe (36) is arranged on for positive displacement pump (31) and between liquid header (38), and is provided with valve nine (37) on total liquid back pipe (36); Between described the first liquid collecting endless tube (7) and tube connector (41), be provided with valve ten one (44), between described the second liquid collecting endless tube (8) and tube connector (41), be provided with valve ten two (45).
6. vertical shaft motor evaporative cooling system as claimed in claim 1, it is characterized in that: described the first condenser (12) comprises cylindrical shell (57), in described cylindrical shell (57), be provided with many cooling water pipes (59), on the outer surface of described cooling water pipe (59), be provided with the coating for condensate liquid is separated with cooling water pipe (59).
7. vertical shaft motor evaporative cooling system as claimed in claim 6, is characterized in that: described coating is made up of polytetrafluoroethylene, Kynoar, silane organic substance or ceramic material, its thickness is 1 μ m-0.5mm.
8. vertical shaft motor evaporative cooling system as claimed in claim 6, is characterized in that: described cooling water pipe (59) is pipe or finned pipe, during for finned pipe, on described fin, is provided with coating.
9. vertical shaft motor evaporative cooling system as claimed in claim 6, it is characterized in that: described cylindrical shell (57) top is provided with steam inlet (61) and gas bag (55), described steam inlet (61) communicates with gas bag (55), and described gas bag (55) communicates with cylindrical shell (57) inner chamber.
10. vertical shaft motor evaporative cooling system as claimed in claim 6, it is characterized in that: described cylindrical shell (57) bottom is provided with hole for back flow (62), in described cylindrical shell (57), be provided with the liquid bag (56) for collecting condensate liquid, described hole for back flow (62) communicates with liquid bag (56).
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410271259.XA CN104009588B (en) | 2014-06-18 | 2014-06-18 | Vertical shaft motor evaporative cooling system |
| PCT/CN2015/080009 WO2015192710A1 (en) | 2014-06-18 | 2015-05-28 | Evaporative cooling system of vertical-shaft motor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410271259.XA CN104009588B (en) | 2014-06-18 | 2014-06-18 | Vertical shaft motor evaporative cooling system |
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| Publication Number | Publication Date |
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| CN104009588A true CN104009588A (en) | 2014-08-27 |
| CN104009588B CN104009588B (en) | 2016-07-13 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201410271259.XA Active CN104009588B (en) | 2014-06-18 | 2014-06-18 | Vertical shaft motor evaporative cooling system |
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| Country | Link |
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| CN (1) | CN104009588B (en) |
| WO (1) | WO2015192710A1 (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2015192710A1 (en) * | 2014-06-18 | 2015-12-23 | 东方电气集团东方电机有限公司 | Evaporative cooling system of vertical-shaft motor |
| CN106253582A (en) * | 2016-08-19 | 2016-12-21 | 中国人民解放军海军工程大学 | A kind of multifunctional safety device of evaporative cooling motor |
| CN111864994A (en) * | 2019-04-30 | 2020-10-30 | 新疆金风科技股份有限公司 | Heat exchange system and motor |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20060125332A1 (en) * | 2002-09-20 | 2006-06-15 | Hans-Jurgen Tolle | Redundant cooling system with two cooling circuits for an electric motor |
| CN2852509Y (en) * | 2005-11-15 | 2006-12-27 | 东方电机股份有限公司 | Combined circulating device for hydro-turbo generator stator evaporating and cooling |
| JP2008045784A (en) * | 2006-08-11 | 2008-02-28 | Tlv Co Ltd | Condensate collecting device |
| CN101640452A (en) * | 2009-08-24 | 2010-02-03 | 中国科学院电工研究所 | Liquid supplying and draining device of evaporating and cooling system of water wheel generator stator |
| CN203151314U (en) * | 2012-10-31 | 2013-08-21 | 中国科学院电工研究所 | Compulsory circulating evaporation cooling device for water turbine generator stator busbar |
| CN204030863U (en) * | 2014-06-18 | 2014-12-17 | 东方电气集团东方电机有限公司 | A kind of vertical shaft motor evaporative cooling system |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102035307B (en) * | 2010-12-29 | 2012-07-04 | 哈尔滨电机厂有限责任公司 | Evaporative cooling system for water-wheel generator with master-slave condenser |
| CN102969838B (en) * | 2012-10-31 | 2014-08-27 | 中国科学院电工研究所 | Forced circulation evaporation cooling device of hydro-generator stator busbar |
| DE102012220559A1 (en) * | 2012-11-12 | 2014-05-15 | Siemens Aktiengesellschaft | Cooling for electric generators |
| CN104009588B (en) * | 2014-06-18 | 2016-07-13 | 东方电气集团东方电机有限公司 | Vertical shaft motor evaporative cooling system |
-
2014
- 2014-06-18 CN CN201410271259.XA patent/CN104009588B/en active Active
-
2015
- 2015-05-28 WO PCT/CN2015/080009 patent/WO2015192710A1/en active Application Filing
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20060125332A1 (en) * | 2002-09-20 | 2006-06-15 | Hans-Jurgen Tolle | Redundant cooling system with two cooling circuits for an electric motor |
| CN2852509Y (en) * | 2005-11-15 | 2006-12-27 | 东方电机股份有限公司 | Combined circulating device for hydro-turbo generator stator evaporating and cooling |
| JP2008045784A (en) * | 2006-08-11 | 2008-02-28 | Tlv Co Ltd | Condensate collecting device |
| CN101640452A (en) * | 2009-08-24 | 2010-02-03 | 中国科学院电工研究所 | Liquid supplying and draining device of evaporating and cooling system of water wheel generator stator |
| CN203151314U (en) * | 2012-10-31 | 2013-08-21 | 中国科学院电工研究所 | Compulsory circulating evaporation cooling device for water turbine generator stator busbar |
| CN204030863U (en) * | 2014-06-18 | 2014-12-17 | 东方电气集团东方电机有限公司 | A kind of vertical shaft motor evaporative cooling system |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2015192710A1 (en) * | 2014-06-18 | 2015-12-23 | 东方电气集团东方电机有限公司 | Evaporative cooling system of vertical-shaft motor |
| CN106253582A (en) * | 2016-08-19 | 2016-12-21 | 中国人民解放军海军工程大学 | A kind of multifunctional safety device of evaporative cooling motor |
| CN111864994A (en) * | 2019-04-30 | 2020-10-30 | 新疆金风科技股份有限公司 | Heat exchange system and motor |
| CN111864994B (en) * | 2019-04-30 | 2023-01-24 | 新疆金风科技股份有限公司 | Heat exchange system and motor |
| US11770050B2 (en) | 2019-04-30 | 2023-09-26 | Xinjiang Goldwind Science & Technology Co., Ltd. | Heat exchange system and motor |
Also Published As
| Publication number | Publication date |
|---|---|
| CN104009588B (en) | 2016-07-13 |
| WO2015192710A1 (en) | 2015-12-23 |
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