CN204186438U - A kind of accumulating type residual neat recovering system - Google Patents
A kind of accumulating type residual neat recovering system Download PDFInfo
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- CN204186438U CN204186438U CN201420575902.3U CN201420575902U CN204186438U CN 204186438 U CN204186438 U CN 204186438U CN 201420575902 U CN201420575902 U CN 201420575902U CN 204186438 U CN204186438 U CN 204186438U
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- vaporizer
- superheater
- working medium
- tube side
- shell side
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
- Y02T10/00—Road transport of goods or passengers
- Y02T10/10—Internal combustion engine [ICE] based vehicles
- Y02T10/12—Improving ICE efficiencies
Abstract
The utility model discloses a kind of accumulating type residual neat recovering system, comprise flooded evaporator, superheater, decompressor, regenerator, condenser, working medium pump and generator; Waste heat tube outlet is divided into three tunnels by the first pipeline diverter, the first via is connected to the tube side of superheater, second road is connected to the tube side of vaporizer, and the 3rd road is connected to the bypass that the second shunt forms superheater tube side, and the second shunt connects exhaust pipe and the outlet of vaporizer tube side; From evaporator drier shell side forms working medium circulation loop through superheater shell side, decompressor, regenerator tube side, condenser tube side, working medium pump, regenerator shell side to vaporizer shell side successively; Condenser shell side passes into low-temperature receiver; Vaporizer shell-side outlet is connected to the import of superheater shell side by a back pressure valve; Decompressor is connected with generator coaxle.During the fluctuation of thermal source heat flow, by regulating vaporizer back pressure and working medium accumulation of energy, reach the object weakening this fluctuation and heat recovery system is impacted, extends the heat recovery time, improve heat recovery total amount.
Description
Technical field
The utility model belongs to residual-heat utilization technology, is specifically related to a kind of system and the energy storage evaporator that waste heat are converted into electric energy.
Background technique
Existing residual neat recovering system, if publication number is CN103983036A, its publication date is the CO reclaimed for afterheat of IC engine a kind of disclosed in the Chinese utility model patent application on August 13rd, 2014
2circulation polygenerations systeme is with CO
2for working medium, take afterheat of IC engine as energy source, by integrated Trans-critical cycle CO
2refrigeration cycle and supercritical CO
2power cycle realizes hot and cold, Electricity Federation product.Through in press cooler lower the temperature after supercritical CO
2gas is divided into two-way, and a road enters refrigerating circuit, first undergoes phase transition through decompressor or throttle valve step-down, the low temperature CO of generation
2liquid is for reducing ambient temperature; Another road enters power loop, first absorbs afterheat of IC engine by high pressure compressor supercharging, then enters power turbine expansion work, the compressor of drive system self, and unnecessary merit is used for generating.
Publication number is CN103994667A, publication date is that the Chinese utility model patent on August 20th, 2014 application discloses that a kind of steel rolling heating furnace residual neat recovering system, comprise main flue channel, in main flue channel, set gradually secondary evaporimeter, secondary air heat exchanger, one-level vaporizer, main air heat exchanger along flue gas flow direction; Main air heat exchanger is provided with cool air inlet, and is connected with the secondary air heat exchanger being provided with hot air outlet by pipeline; One-level vaporizer is provided with water source entrance, and by pipeline be provided with the secondary evaporimeter that steam water interface exports and connect; Outside main flue channel, place arranged side by side is provided with the auxiliary flue for regulating by secondary air heat exchanger exhaust gas volumn with secondary evaporimeter, is disposed with auxiliary flue vaporizer, auxiliary flue shutter in auxiliary flue along flue gas flow direction.The utility model, by arranging double effect evaporator in main flue channel, effectively increases steam hot area; By interlaced arrangement air heat exchanger and vaporizer, and main air heat exchanger is placed in main flue channel caudal end, such arrangement mode ensure that temperature difference during heat exchange, effectively improves heat exchange efficiency.Mainly be to improve system heat transfer performance and cascaded utilization of energy, although the object improving the thermal efficiency can be reached, do not consider the problem of the stability aspect of residual neat recovering system own.
Publication number is CN103994683A, its publication date is disclose a kind of high-temperature flue gas heat recovery and storage device and method in the Chinese utility model patent application on August 20th, 2014, heat accumulation chamber body internal voids is wherein filled with phase-change heat-storage material, high-temperature flue gas enters in heat accumulation chamber body, carry out heat exchange with thermal fluid, meanwhile, phase-change heat-storage material is with the mode storing heat of latent heat of phase change, and with thermal fluid heat exchange, cooling post crystallization is solid-state and releases latent heat of phase change.Be utilize phase-change thermal storage technology to weaken heat source fluctuations, but it has, and volume is large, cost is high, baroque defect, is difficult to the residual neat recovering system producing compact structure.
Model utility content
Vaporizer is the significant components of Rankine cycle recovery waste heat, because actual waste heat thermal source heat flow presents sudden transformation more, therefore, for problems of the prior art, the utility model provides a kind of accumulating type residual neat recovering system, adopts the organic rankine cycle system driven by waste heat, adopts the vaporizer of variable outlet pressure as heat exchange and accumulation of heat assembly, regulate evaporator exit pressure according to waste heat heat flow, improve heat recovery quality.Wherein, the working medium stored in flooded evaporator is used for accumulation of energy, the system fluctuation caused during to make up exhaust gas heat underfed and shutdown, thus the stable operation that can ensure system.The heat recovery time can be extended simultaneously, heat recovery total amount is increased.In addition, vaporizer instead of liquid container, simplifies system.
For solving the problems of the technologies described above, the technological scheme that a kind of accumulating type residual neat recovering system of the utility model adopts is: this system comprises vaporizer, superheater, decompressor, regenerator, condenser, working medium pump and generator, and described vaporizer is flooded evaporator; The tube side outlet port of described superheater is connected with the first pipeline diverter, and the tube side outlet of described vaporizer is connected to described first pipeline diverter, and described first pipeline diverter is connected with exhaust pipe; The import of waste heat pipeline is connected to thermal source, the outlet of waste heat pipeline is divided into three tunnels by the first pipeline diverter, the first via is connected to the tube side of described superheater, and the second road is connected to the tube side of described vaporizer, and the 3rd road is connected to the bypass that the second shunt forms a superheater tube side; A working medium circulation loop is formed through the shell side of the tube side of the tube side of the shell side of superheater, decompressor, regenerator, condenser, working medium pump regenerator to the shell side of described vaporizer successively from the shell side of described vaporizer; The facility that low-temperature receiver is provided is connected with between the shell side import and export of described condenser; The shell-side outlet of described vaporizer is connected to the shell side import of superheater by a back pressure valve; Described decompressor is connected with described generator coaxle.
Further, when the utility model being used for residual heat of tail gas of automobile recovery, described thermal source is the using waste heat from tail gas of vehicle internal combustion engine, and described exhaust pipe is provided with tail gas ternary catalyzing unit, and described low-temperature receiver is provided by fan coil unit.
When the utility model being used for residual heat from boiler fume recovery, described thermal source is residual heat from boiler fume, and described low-temperature receiver is provided by cooling tower.
In a kind of accumulating type residual neat recovering system of the utility model, the working medium in working medium circulation loop is ethanol.
Compared with prior art, the beneficial effects of the utility model are:
When waste heat thermal source heat flow fluctuates, the utility model residual neat recovering system, by regulating vaporizer back pressure and working medium accumulation of energy, reaches and weakens this fluctuation to the impact of residual neat recovering system, extends the heat recovery time simultaneously, improves the object of heat recovery total amount.
Accompanying drawing explanation
Fig. 1 is a kind of accumulating type residual neat recovering system of the utility model schematic diagram;
Fig. 2 is the system schematic of the utility model when reclaiming for residual heat of tail gas of automobile;
Fig. 3 is the system schematic of the utility model when reclaiming for residual heat from boiler fume;
Fig. 4 is the utility model residual neat recovering system state of cyclic operation tephigram.
In figure: 1-first pipeline diverter, 2-back pressure valve, 3-vaporizer, 4-superheater, 5-first pipeline diverter, 6-condenser, 7-working medium pump, 8-regenerator, 9-decompressor, 10-generator, 11-vehicle internal combustion engine, 12-fan coil unit, 13-tail gas ternary catalyzing unit, 14-cooling tower, 15-boiler.
Embodiment
Below in conjunction with the drawings and specific embodiments, technical solutions of the utility model are described in further detail.
As shown in Figure 1, a kind of accumulating type residual neat recovering system of the utility model, comprise vaporizer 3, superheater 4, decompressor 9, regenerator 8, condenser 6, working medium pump 7 and generator 10, described vaporizer is flooded evaporator; The tube side outlet port of described superheater 4 is connected with the first pipeline diverter 5, the tube side outlet of described vaporizer 3 is connected to described first pipeline diverter 5, described first pipeline diverter 5 is connected with exhaust pipe, and described decompressor 9 is coaxially connected with described generator 10.
The import of waste heat pipeline is connected to thermal source, the outlet of waste heat pipeline is divided into three tunnels by the first pipeline diverter 1: wherein, the first via is connected to the tube side of described superheater 4, second road is connected to the tube side of described vaporizer 3,3rd road is connected to the bypass that the second shunt 5 forms superheater 4 tube side, this bypass can realize: when flowing through without working medium in superheater 4, and the waste heat fluid of waste heat pipeline can not be branched to superheater 4 by the second pipeline diverter 1.
As shown in Figure 1, the annexation of relative assembly is: from the shell side of described vaporizer 3 successively through the tube side of the shell side of superheater 4, decompressor 9, regenerator 8, the tube side of condenser 6, the shell side of working medium pump 7 regenerator 8 to the shell side of described vaporizer 3, thus forming a working medium circulation loop, the working medium in the utility model is ethanol or ammoniacal liquor; The facility that low-temperature receiver is provided is connected with between the shell side import and export of described condenser.
The shell-side outlet of described vaporizer 3 is connected to the shell side import of superheater 4 by a back pressure valve 2, when the heat flow of waste heat fluid is not enough, turn down the pressure of back pressure valve 2, makes the working medium in vaporizer 3 continue vaporization.
When the utility model being used for residual heat of tail gas of automobile recovery, described thermal source is the using waste heat from tail gas of vehicle internal combustion engine 11, and described exhaust pipe is provided with tail gas ternary catalyzing unit 13, and described low-temperature receiver is provided by a fan coil unit 12.
When the utility model being used for residual heat from boiler fume recovery, described thermal source is boiler 15 fume afterheat, and described low-temperature receiver is provided by a cooling tower 14.
The working principle of a kind of accumulating type residual neat recovering system of the utility model is:
Waste heat fluid flows out after flowing into vaporizer 3 and superheater 4 and working medium heat exchange respectively.Working medium absorbs waste heat vaporization (as Fig. 4 state 7) in vaporizer 3, when vaporizer 3 internal pressure is higher than back pressure valve 2 setting pressure, working substance steam flows out vaporizer 3, enter superheater 4 to continue to absorb waste heat (as Fig. 4 state 1), rear outflow superheater 4 enters decompressor 8 and does work, and drives the generator 9 coaxial with decompressor 8 to generate electricity.Working medium exhaust steam (as Fig. 4 state 2) enters the working medium (as Fig. 4 state 3, state 6) after the pressurization of regenerator 7 preheating working medium pump 6 after flowing out decompressor 8, finally enter condenser 5 heat release (as Fig. 4 state 4), after working medium pump 6 pressurizes, (as Fig. 4 state 5) enters vaporizer 3 after entering regenerator 7 and decompressor 8 and exhaust steam heat exchange again, completes a thermodynamic cycle.When thermal source heat flow drop to be not enough to vaporizer 3 outlet pressure to rise to back pressure valve 2 setting pressure time, turn down back pressure valve pressure 2.Make working medium vaporization in vaporizer 3, flow into superheater 4 (as Fig. 4 state 1 ') and start above-mentioned thermodynamic cycle, continue acting generating.
The utility model principle and system are described further by example example below in conjunction with accompanying drawing.It should be noted that the present embodiment is narrative, but not determinate, this does not limit protection domain of the present utility model.
When the utility model accumulating type residual neat recovering system is used for residual heat of tail gas of automobile recovery, as shown in Figure 2, the tail gas of being discharged by vehicle internal combustion engine 11 forms a respective path through the tube side of the tube side of vaporizer 3 and superheater 4 respectively for its formation and annexation; The shell side being back to vaporizer 3 by the shell side of the tube side of the tube side of the shell side of the shell side of vaporizer 3, superheater 4, decompressor 9, regenerator 8, condenser 6, working medium pump 7, regenerator 8 forms a working medium circulation loop, and working medium is wherein ethanol.Generator 10 is coaxial with decompressor 9.When the utility model residual neat recovering system runs, after fuel burns in internal-combustion engine 11, tail gas enters the tube side of vaporizer 3 and the tube side of superheater 4 respectively through the second pipeline diverter 1, heat exchange is carried out with the working medium in both shell sides, after superheater 4, converge inflow tail gas ternary catalyzing unit 13 carry out catalytic treatment, discharge finally by exhaust pipe.Internal-combustion engine 11 is vented, first vaporizer 3 is flowed into through the second pipeline diverter 1, back pressure valve 2 pressure setting is 0.43MPa, working medium vaporization in vaporizer 3 shell side, when current pressure is higher than 0.43MPa, working medium flows out vaporizer 3, flow into superheater 4, now controlling the first pipeline diverter 5 makes tail gas flow into superheater 4, working medium flows into decompressor 9 be heated to superheat state further in superheater 4 after, flow into condenser 6 heat release after working medium heat exchange after exhaust steam inflow regenerator 8 after acting boosts with working medium pump 7, so far complete a circulation.When automobile because the reasons such as road conditions are slowed down or stopped, cause I. C. engine exhaust heat flow to decline, when vaporizer 3 outlet pressure cannot reach 0.43MPa, reduce back pressure valve setting pressure to 0.22MPa.Working medium in vaporizer 3 is then vaporized, and continues above-mentioned circulation, maintains residual neat recovering system and runs.Condenser tube side connecting fan coil pipe 12, cooling fluid adopt antifreeze liquid, as residual neat recovering system low-temperature receiver.
When the utility model accumulating type heat recovery system is used for residual heat from boiler fume recovery, as shown in Figure 3, the flue gas of being discharged by boiler 15 forms a respective path through the tube side of the tube side of vaporizer 3, superheater 4 respectively for its formation and annexation; Form a working medium circulation loop by the shell side of the tube side of the shell side of the shell side of vaporizer 3, superheater 4, decompressor 9, regenerator 8 tube side, condenser 6, working medium pump 7, regenerator 8, working medium is wherein ethanol.Generator 10 is coaxial with decompressor 9.When the utility model moon, reclaiming system was run, after fuel burns in boiler 15, flue gas enters the tube side of vaporizer 3 and the tube side of superheater 4 respectively through the second pipeline diverter 1, carries out heat exchange, after superheater 4, converge discharge with the working medium in both shell sides.First the flue gas that boiler 15 is discharged flows into vaporizer 3 through the second pipeline diverter 1, back pressure valve 2 pressure setting is 0.43MPa, working medium vaporization in the shell side of vaporizer 3, current pressure flows out vaporizer 3 higher than working medium during 0.43MPa, flow into superheater 4, now, controlling the first extension stove shunt 5 makes flue gas flow into superheater 4, working medium flows into decompressor 9 be heated to superheat state further in superheater 4 after, flow into condenser 6 heat release after working medium heat exchange after exhaust steam inflow regenerator 8 after acting boosts with working medium pump 7, so far complete a circulation.Need to change operating mode because run when boiler 15, cause flue gas heat flow to decline, when vaporizer 3 outlet pressure cannot reach 0.43MPa, reduce back pressure valve setting pressure to 0.22MPa.In vaporizer 3, working medium is then vaporized, and continues above-mentioned circulation, maintains residual neat recovering system and runs.Condenser tube side connect cooling tower 14, cooling fluid is water, as residual neat recovering system low-temperature receiver.
Although be described the utility model by reference to the accompanying drawings above; but the utility model is not limited to above-mentioned embodiment; above-mentioned embodiment is only schematic; instead of it is restrictive; those of ordinary skill in the art is under enlightenment of the present utility model; when not departing from the utility model aim, can also make a lot of distortion, these all belong within protection of the present utility model.
Claims (4)
1. an accumulating type residual neat recovering system, comprise vaporizer (3), superheater (4), decompressor (9), regenerator (8), condenser (6), working medium pump (7) and generator (10), it is characterized in that:
Described vaporizer is flooded evaporator;
The tube side outlet port of described superheater (4) is connected with the first pipeline diverter (5), the tube side outlet of described vaporizer (3) is connected to described first pipeline diverter (5), and described first pipeline diverter (5) is connected with exhaust pipe;
The import of waste heat pipeline is connected to thermal source, the outlet of waste heat pipeline is divided into three tunnels by the first pipeline diverter (1), the first via is connected to the tube side of described superheater (4), second road is connected to the tube side of described vaporizer (3), and the 3rd road is connected to the bypass that the second shunt (5) forms a superheater (4) tube side;
A working medium circulation loop is formed through the shell side of the tube side of the tube side of the shell side of superheater (4), decompressor (9), regenerator (8), condenser (6), working medium pump (7) regenerator (8) to the shell side of described vaporizer (3) successively from the shell side of described vaporizer (3); The facility that low-temperature receiver is provided is connected with between the shell side import and export of described condenser;
The shell-side outlet of described vaporizer (3) is connected to the shell side import of superheater (4) by a back pressure valve (2);
Described decompressor (9) is coaxially connected with described generator (10).
2. a kind of accumulating type residual neat recovering system according to claim 1, it is characterized in that, described thermal source is the using waste heat from tail gas of vehicle internal combustion engine (11), described exhaust pipe is provided with tail gas ternary catalyzing unit (13), and described low-temperature receiver is provided by a fan coil unit (12).
3. a kind of accumulating type residual neat recovering system according to claim 1, is characterized in that, described thermal source is boiler (15) fume afterheat, and described low-temperature receiver is provided by a cooling tower (14).
4. a kind of accumulating type residual neat recovering system according to claim 1, is characterized in that, the working medium in working medium circulation loop is ethanol.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
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| CN201420575902.3U CN204186438U (en) | 2014-09-30 | 2014-09-30 | A kind of accumulating type residual neat recovering system |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201420575902.3U CN204186438U (en) | 2014-09-30 | 2014-09-30 | A kind of accumulating type residual neat recovering system |
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| CN204186438U true CN204186438U (en) | 2015-03-04 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104265388A (en) * | 2014-09-30 | 2015-01-07 | 天津大学 | Energy storage type waste heat recycling system |
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2014
- 2014-09-30 CN CN201420575902.3U patent/CN204186438U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104265388A (en) * | 2014-09-30 | 2015-01-07 | 天津大学 | Energy storage type waste heat recycling system |
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| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150304 Termination date: 20150930 |
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| EXPY | Termination of patent right or utility model |