CN205747584U - Generator drive water source compression heat pump water vapour preparer - Google Patents
Generator drive water source compression heat pump water vapour preparer Download PDFInfo
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- CN205747584U CN205747584U CN201620582963.1U CN201620582963U CN205747584U CN 205747584 U CN205747584 U CN 205747584U CN 201620582963 U CN201620582963 U CN 201620582963U CN 205747584 U CN205747584 U CN 205747584U
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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
A kind of generator drive water source compression heat pump water vapour preparer: system integration electromotor, water source compression heat pump, drum, vapour vapour injector；Utilize generator drive water source compression heat pump, shorten the investment payback time 50%；Utilize heat pump to heat, overlap cylinder backheat, flue gas backheat step heat cycles moisturizing, to provide evaporation heat to distill out low-pressure steam；Utilize steam pipe system overbottom pressure hot compression low-pressure steam, save investment and the compression electricity charge of water vapour compressor；Realize 1 part of high steam and modulate the steam multiplication function of n+1 part middle pressure steam；Realize 3 parts of boiler heat supplyings of 1 part of the highest generation of fuel value.
Description
(1) technical field
The present invention relates to a kind of generator drive water source compression heat pump water vapour preparer.
(2) background technology
Distributed energy resource system is the area that should not build centralized power station, and the terminal temperature difference of transmission and distribution network provides energy
Source, effectively reduces electricity, heat, cold conveyance loss and induction system investment, provides the user high-quality, highly reliable clean energy resource
Service.
In addition consideration conveyance loss and vapor pressure demand, steam pipe system generally maintains 10bar pressure above.So
And much the actual steam pressure demand of heating equipment only has 3-4bar, therefore desuperheat, air relief valve will be set at device port,
To realize the actual pressure demand of equipment, thus generally waste steam pipe system overbottom pressure.
Existing water resource heat pump heating flash evaporation and water vapour compressor compresses, producing the technological process of water vapour be: thermal source
Water flows through vaporizer water side, so that the biphase heat pump fluid of low pressure flowing into vaporizer working medium side absorbs heat and evaporates and become low pressure
Cross hot gaseous heat pump fluid, and make discharge after heat source water heat release, cooling；Heat pump fluid is sucked compressor by air entry, and compresses
Become high pressure superheater gaseous state heat pump fluid, and send into the condensation of condenser working medium side and become high pressure supercooled liquid heat pump fluid, finally
Expanded valve throttling and again become the biphase heat pump fluid of low pressure, flow into vaporizer working medium side to complete heat pump cycle, handle simultaneously
Condenser heat is released to circular water replenishing side.When the recirculated water of drum outlet at bottom is after moisturizing threeway mixes with moisturizing, stream passes through
Filter, circulating pump, check-valves, Water in Condenser side, and after the heat that is condensed heats up, through choke valve decompression in flash tank
Adiabatic flash goes out indirect steam, and last indirect steam is flashed the water vapour compressor of tank top setting and sucks and be collapsed into institute
Need the water vapour of pressure.
But the reason that this technology is difficult to promote is:
(1) 10 times of refrigeration compressors of the investment of water vapour compressor unit inspiration capacity；
(2) when pressure reduction is more than 3-8bar, the isentropic efficiency of water vapour compressor is greatly reduced, and causes power consumption to increase；
(3) if reducing the pressure reduction of water vapour compressor, just need to improve the circulation pressure ratio of water resource heat pump, thus causing again water
Source heat pump power consumption increases；
(4) increase due to system investments and power consumption so that it is project investment payoff period more than more than 7 years, therefore, it is difficult to push away
Wide application.
(3) summary of the invention
The present invention seeks to: the fuel thermal energy step making full use of electromotor drives water source compression heat pump, set cylinder backheat
Device, flue gas regenerator heat cycles water, to distill out low-pressure steam, recycling steam pipe system overbottom pressure realizes the hot pressing of low-pressure steam
Contracting, so that steam flow multiplication.
According to the generator drive water source compression heat pump water vapour preparer shown in accompanying drawing 1, it is by 1-electromotor；1-1-
Air inlet；1-2-driving shaft；1-3-air vent；1-4-overlaps cylinder cooling water inlet；1-5-overlaps cylinder coolant outlet；2-fuel；3-
Electromotor；4-power transmission and distribution；5-motor；6-compressor；7-condenser；8-device for drying and filtering；9-expansion valve；10-water source evaporates
Device；11-overlaps cylinder regenerator；12-flue gas regenerator；13-filter；14-circulating pump；15-check-valves；16-refill flow regulates
Valve；17-liquid level controller；18-drum；19-vapour vapour injector；20-electric T-shaped valve；21-water vapour compressor bank becomes, and it is special
Levy and be:
The air inlet 1-1 of electromotor 1 inputs fuel 2 by pipeline, forms engine charge loop；
The driving shaft 1-2 of electromotor 1 is rotated by electromotor 3 and power transmission and distribution 4 driving electric machine 5, composition generating electromechanics
Power output loop；
The set cylinder cooling water inlet 1-4 of electromotor 1 and set cylinder coolant outlet 1-5 is by pipe connecting sleeve cylinder regenerator 11
Cooling water side, composition set cylinder cooling back-heating loop；
The air vent 1-3 of electromotor 1 connects flue gas regenerator 12 gas side by flue, forms flue gas backheat loop；
Motor 5 drives compressor 6 to rotate, and forms compressor electric power input circuit；
Compressor 6 connects condenser 7 working medium side, device for drying and filtering 8, expansion valve 9, water source vaporizer 10 working medium by pipeline
Side, forms water resource heat pump closed circuit；
Filter 13, circulating pump 14, check-valves 15, condenser 7 water side, set cylinder regenerator 11 water side, flue gas regenerator 12
Water side, forms circulating-heating loop.
Drum 18 outlet at bottom connects moisturizing threeway, filter 13, circulating pump 14, check-valves 15, condenser 7 by pipeline
Water side, set cylinder regenerator 11 water side, flue gas regenerator 12 water side, form moisturizing circulating-heating loop；Drum 18 top exit leads to
Piping connects vapour vapour injector 19, forms water vapour hot compression loop.
Drum 18 outlet at bottom connects moisturizing threeway, filter 13, circulating pump 14, check-valves 15, condenser 7 by pipeline
Water side, set cylinder regenerator 11 water side, flue gas regenerator 12 water side, form moisturizing circulating-heating loop；Drum 18 top exit leads to
Piping connects water vapour compressor 21, forms water vapour mechanical compress loop.
Electric T-shaped valve 20 is returned by pipeline connection filter 13, circulating pump 14, check-valves 15, condenser 7 water side, set cylinder
Hot device 11 water side, flue gas regenerator 12 water side, electric T-shaped valve 20, form hot water circulation heated loop.
Electromotor 1 be gas driven explosive motor 1, gasoline driven explosive motor 1, diesel driven explosive motor 1,
Kerosene drives explosive motor 1, Stirling external-burning engine 1, gas driven gas-turbine engine 1, coal gas to drive combustion gas wheel to send out
Motivation 1.
The operation principle of the present invention combines accompanying drawing 1 and is described as follows:
1, fuel driven electromotor drives water source compression type heat heat pump heating: fuel 2 is through air inlet 1-1 input electromotor 1 also
After lighting, drive driving shaft 1-2 to drive electromotor 3 low speed rotation, then rotated by power transmission and distribution 4 driving electric machine 5, motor 5
Compressor 6 is driven to rotate；Heat source water flows through water source vaporizer 10 water side, so that flowing into the low pressure two of water source vaporizer 10 working medium side
Phase heat pump fluid absorbs heat and evaporates and become low pressure superheated gaseous heat pump fluid, and makes discharge after heat source water heat release, cooling；Heat
Pump work substance is sucked compressor 6 by air entry, and is collapsed into high pressure superheater gaseous state heat pump fluid, sends into condenser 7 working medium side cold
Congeal into for high pressure supercooled liquid heat pump fluid, flow through device for drying and filtering 8 and expanded valve 9 throttles and becomes low pressure biphase heat pump work
Matter, back flows back into water source vaporizer 10 working medium side to complete heat pump cycle, condenser heat is released to recirculated water simultaneously.Recirculated water
Flow through condenser 7 water side, absorb another side condenser heat and heat up for the first time.
2, set cylinder cooling water-driven set cylinder regenerator 11 heats: the high temperature set cylinder cooling water of electromotor 1 is by overlapping cylinder cooling water
Outlet 1-5 flows through pipeline, set cylinder regenerator 11 cooling water side, the set cylinder cooling back-heating loop of set cylinder cooling water inlet 1-4 composition,
After the circulating water heating flowing through set cylinder regenerator 11 water side is heated up, then discharge of lowering the temperature.
3, flue gas drive flue gas regenerator 12 heat: the high-temperature flue gas of electromotor 1 by air vent 1-3 flow through flue,
The flue gas backheat loop of flue gas regenerator 12 gas side composition, to heat up the circulating water heating flowing through flue gas regenerator 12 water side
After, then discharge of lowering the temperature.
4, hot water heating circulation: as shown in Figure 2, heat source water flows through water source vaporizer 10 water side, steams so that flowing into water source
The biphase heat pump fluid of low pressure sending out device 10 working medium side absorbs heat and evaporates and become low pressure superheated gaseous heat pump fluid, and makes thermal source
Discharge after water heat release, cooling；Heat pump fluid is sucked compressor 6 by air entry, and is collapsed into high pressure superheater gaseous state heat pump fluid,
Send into the condensation of condenser 7 working medium side and become high pressure supercooled liquid heat pump fluid, flow through device for drying and filtering 8 and throttled by expansion valve 9
And become the biphase heat pump fluid of low pressure, back flow back into water source vaporizer 10 working medium side to complete heat pump cycle, simultaneously condensation heat
Amount is released to circulating backwater.Circulating backwater flows through filter 13, circulating pump 14, check-valves 15, condenser 7 water side, another to absorb
Side condenser heat and heat up for the first time, pass through set cylinder regenerator 11 water side, flue gas regenerator 12 water side absorbs another side set cylinder and returns
Heat, flue gas backheat amount and respectively second time heats up, third time heats up, to become high temperature circulation water outlet.
5, hot compression water vapour brew cycle: as shown in Figure 1, heat source water flows through water source vaporizer 10 water side, so that stream
The biphase heat pump fluid of low pressure entering water source vaporizer 10 working medium side absorbs heat and evaporates and become low pressure superheated gaseous heat pump fluid,
And discharge after making heat source water heat release, cooling；Heat pump fluid is sucked compressor 6 by air entry, and is collapsed into high pressure superheater gaseous state
Heat pump fluid, sending into the condensation of condenser 7 working medium side becomes high pressure supercooled liquid heat pump fluid, flows through device for drying and filtering 8 and by swollen
Swollen valve 9 throttles and becomes the biphase heat pump fluid of low pressure, back flows back into water source vaporizer 10 working medium side to complete heat pump cycle, simultaneously
Condenser heat is released to circular water replenishing.The recirculated water of drum 18 outlet at bottom is after moisturizing threeway mixes with moisturizing, and circulation is mended
Water flows through filter 13, circulating pump 14, check-valves 15, condenser 7 water side, heats up for the first time to absorb another side condenser heat,
Pass through set cylinder regenerator 11 water side, flue gas regenerator 12 water side absorbs another side set cylinder backheat amount, flue gas backheat amount and respectively the
Secondary temperature elevation, third time heat up, and to become high temperature circulation moisturizing, and distill out low-pressure steam in drum 18, last n part low pressure
Steam is in the vapour vapour injector 19 that drum 18 top is arranged, by flowing through diffusion after 1 part of high steam injection therein, to adjust
It is made for n+1 part middle pressure steam.
6, mechanical compress water vapour brew cycle: as shown in Figure 3, heat source water flows through water source vaporizer 10 water side, so that
The biphase heat pump fluid of low pressure flowing into water source vaporizer 10 working medium side absorbs heat and evaporates and become low pressure superheated gaseous heat pump work
Matter, and make discharge after heat source water heat release, cooling；Heat pump fluid is sucked compressor 6 by air entry, and is collapsed into high pressure superheater gas
State heat pump fluid, send into condenser 7 working medium side condensation become high pressure supercooled liquid heat pump fluid, flow through device for drying and filtering 8 and by
Expansion valve 9 throttles and becomes the biphase heat pump fluid of low pressure, back flows back into water source vaporizer 10 working medium side to complete heat pump cycle, with
Time condenser heat is released to circular water replenishing.The recirculated water of drum 18 outlet at bottom, after moisturizing threeway mixes with moisturizing, circulates
Moisturizing flows through filter 13, circulating pump 14, check-valves 15, condenser 7 water side, rises for the first time to absorb another side condenser heat
Temperature, passes through set cylinder regenerator 11 water side, flue gas regenerator 12 water side absorbs another side set cylinder backheat amount, flue gas backheat amount and difference
Second time heats up, third time heats up, and to become high temperature circulation moisturizing, and distills out low-pressure steam in drum 18, last low pressure
Steam, in the water vapour compressor 21 that drum 18 top is arranged, is mechanically compressed and becomes middle pressure steam.
Therefore, compared with existing application technology, feature of the present invention is as follows:
(1) system integration electromotor, water source compression heat pump, circulating pump, drum, vapour vapour injector；
(2) utilize electromotor output high-grade electrical energy drive water source compression heat pump, shorten the investment payback time 50%；
(3) utilize heat pump to heat, overlap cylinder backheat, flue gas backheat step heat cycles moisturizing, to provide evaporation heat, distillation
Go out low-pressure steam；
(4) utilize steam pipe system overbottom pressure to realize low-pressure steam hot compression, save investment and the compression electricity of water vapour compressor
Take；
(5) realize 1 part of high steam and modulate the steam multiplication function of n+1 part middle pressure steam；
(6) switching realizes water vapour brew cycle and hot water heating circulation；
(7) comprehensive energy utilization rate improves half, up to 120%, it is achieved 2.3 parts of boilers of 1 part of the highest generation of fuel value
Heat supply.
The most compared with prior art, the technology of the present invention advantage is as follows: system integration electromotor, water source compression type heat
Pump, circulating pump, drum, vapour vapour injector；Utilize electromotor output high-grade electrical energy drive water source compression heat pump, shorten investment
Payoff period 50%；Utilize heat pump to heat, overlap cylinder backheat, flue gas backheat step heat cycles moisturizing, to provide evaporation heat, distillation
Go out low-pressure steam；Utilize steam pipe system overbottom pressure hot compression low-pressure steam, save investment and the compression electricity charge of water vapour compressor；Real
Existing 1 part of high steam modulates the steam multiplication function of n+1 part middle pressure steam；Switching realizes water vapour brew cycle and adds with hot water
Thermal cycle；Comprehensive energy utilization rate improves half, up to 120%, it is achieved 3 parts of boiler heat supplyings of 1 part of the highest generation of fuel value.
(4) accompanying drawing explanation
Accompanying drawing 1 is the system flow chart of hot compression water vapour brew cycle of the present invention.
The system flow chart that accompanying drawing 2 circulates for hot water heating of the present invention.
Accompanying drawing 3 is the system flow chart of mechanical compress water vapour brew cycle of the present invention.
As shown in Figure 1, wherein: 1-electromotor；1-1-air inlet；1-2-driving shaft；1-3-air vent；1-4-set cylinder is cold
But water inlet；1-5-overlaps cylinder coolant outlet；2-fuel；3-electromotor；4-power transmission and distribution；5-motor；6-compressor；7-condenses
Device；8-device for drying and filtering；9-expansion valve；10-water source vaporizer；11-overlaps cylinder regenerator；12-flue gas regenerator；13-filter；
14-circulating pump；15-check-valves；16-refill flow regulation valve；17-liquid level controller；18-drum；19-vapour vapour injector；20-
Electric T-shaped valve；21-water vapour compressor.
(5) detailed description of the invention
The generator drive water source compression heat pump water vapour preparer embodiment that the present invention proposes is as shown in Figure 1, existing
It is described as follows:
The electromotor 1 of output shaft power 1.20MW；
The rustless steel air inlet 1-1 of diameter 32mm；
Length 400mm, the rustless steel driving shaft 1-2 of diameter 42mm；
The rustless steel air vent 1-3 of diameter 32mm；
The stainless steel sleeve cylinder cooling water inlet 1-4 of diameter 15mm；
The stainless steel sleeve cylinder coolant outlet 1-5 of diameter 15mm；
The gas fuel 2 of calorific value 8500kcal/Nm3；
Diameter 400mm, length 800mm, the electromotor 3 of generated energy 1.10MW；
The power transmission and distribution 4 of 380V, 50Hz；
Diameter 300mm, length 600mm, the motor 5 of power 1.00MW；
The compressor 6 of inspiration capacity 4860m3/h；
The shell-and-tube cooler 7 of condensation heating amount 5253kW；
The red copper device for drying and filtering 8 of interface diameter 100mm/ wall thickness 1mm；
Interface diameter 200mm, the rustless steel orifice plate expansion valve 9 of thickness 2mm；
The water source vaporizer 10 of evaporation endothermic amount 4105kW；
The set cylinder regenerator 11 of backheat amount 420kW；
The flue gas regenerator 12 of backheat amount 780kW；
The stainless steel filter 13 of interface diameter 200mm/ wall thickness 2.5mm；
The circulating pump 14 of interface diameter 200mm/ lift 7mH20/ flow 1131m3/h；
The rustless steel check-valves 15 of interface diameter 200mm/ wall thickness 2.5mm；
Interface diameter 25mm, the rustless steel refill flow regulation valve 16 of thickness 1mm；
The molten stainless steel level controller 17 of interface diameter 15mm/ wall thickness 1mm；
The rustless steel drum 18 of diameter 600mm/ length 2m/ wall thickness 6mm；
Injection low-pressure steam flow 9.2t/h, the vapour vapour injector 19 of middle pressure mixed vapour flow 11.2t/h；
The rustless steel electric T-shaped valve 20 of interface diameter 200mm/ wall thickness 2.5mm forms.
The air inlet 1-1 of electromotor 1 inputs fuel 2 by pipeline, forms engine charge loop；
The driving shaft 1-2 of electromotor 1 is rotated by electromotor 3 and power transmission and distribution 4 driving electric machine 5, composition generating electromechanics
Power output loop；
The set cylinder cooling water inlet 1-4 of electromotor 1 and set cylinder coolant outlet 1-5 is by pipe connecting sleeve cylinder regenerator 11
Cooling water side, composition set cylinder cooling back-heating loop；
The air vent 1-3 of electromotor 1 connects flue gas regenerator 12 gas side by flue, forms flue gas backheat loop；
Motor 5 drives compressor 6 to rotate, and forms compressor electric power input circuit；
Compressor 6 connects condenser 7 working medium side, device for drying and filtering 8, swollen by the copper tube of diameter 100mm/ wall thickness 1mm
Swollen valve 9, water source vaporizer 10 working medium side, form water resource heat pump closed circuit；
Filter 13, circulating pump 14, check-valves 15, condenser 7 water side, set cylinder regenerator 11 water side, flue gas regenerator 12
Water side, forms circulating-heating loop.
Drum 18 outlet at bottom connects moisturizing threeway, filter 13, circulating pump 14, check-valves 15, condenser 7 by pipeline
Water side, set cylinder regenerator 11 water side, flue gas regenerator 12 water side, form moisturizing circulating-heating loop；
Drum 18 top exit connects vapour vapour injector 19, composition by the stainless steel tube of diameter 200mm/ wall thickness 2.5mm
Water vapour hot compression loop.
Electric T-shaped valve 20 is returned by pipeline connection filter 13, circulating pump 14, check-valves 15, condenser 7 water side, set cylinder
Hot device 11 water side, flue gas regenerator 12 water side, electric T-shaped valve 20, form hot water circulation heated loop.
Electromotor 1 is gas driven explosive motor 1.
1, fuel driven electromotor drives water source compression type heat heat pump heating: gas fuel 2 starts through air inlet 1-1 input
Machine 1 after lighting, is driven driving shaft 1-2 to drive electromotor 3 low speed rotation, then is rotated by power transmission and distribution 4 driving electric machine 5, electricity
Motivation 5 drives compressor 6 to rotate；54 DEG C of heat source waters are the rinse water on beverage production line, and rinse water flows through water source vaporizer 10
Water side, so that the biphase heat pump fluid of low pressure flowing into water source vaporizer 10 working medium side absorbs 4105kW heat and evaporates and become low pressure
Cross hot gaseous heat pump fluid, and make rinse water heat release, be cooled to 44 DEG C after discharge；Heat pump fluid is sucked compressor 6 by air entry,
And it is collapsed into high pressure superheater gaseous state heat pump fluid, sending into the condensation of condenser 7 working medium side becomes high pressure supercooled liquid heat pump fluid,
Flow through device for drying and filtering 8 and expanded valve 9 throttles and becomes the biphase heat pump fluid of low pressure, back flow back into water source vaporizer 10 working medium
Side, to complete heat pump cycle, is released to recirculated water 5253kW condenser heat simultaneously.80 DEG C of circulating water flow condensed device 7 water sides,
Absorb another side condenser heat and be warming up to 84 DEG C for the first time.
2, set cylinder cooling water-driven set cylinder regenerator 11 heats: 95 DEG C of high temperature set cylinder cooling water of electromotor 1 are cold by overlapping cylinder
But water out 1-5 flows through pipeline, set cylinder regenerator 11 cooling water side, the set cylinder cooling back-heating of set cylinder cooling water inlet 1-4 composition
Loop, after the 84 DEG C of circulating water heatings flowing through set cylinder regenerator 11 water side are warming up to 84.33 DEG C, then is cooled to 87 DEG C of rows
Go out.
3, flue gas drives flue gas regenerator 12 to heat: 420 DEG C of high-temperature flue gas of electromotor 1 are flowed through flue gas by air vent 1-3
Pipeline, the flue gas backheat loop of flue gas regenerator 12 gas side composition, with the 84.33 DEG C of circulations flowing through flue gas regenerator 12 water side
After water is heated to 85 DEG C, then it is cooled to 120 DEG C of discharges.
4, hot water heating circulation: flow 354t/h, 54 DEG C of heat source waters flow through water source vaporizer 10 water side, so that flowing into water source
The biphase heat pump fluid of low pressure of vaporizer 10 working medium side absorbs heat and evaporates and become low pressure superheated gaseous heat pump fluid, and makes heat
Source water heat release, be cooled to 44 DEG C after discharge；Heat pump fluid is sucked compressor 6 by air entry, and is collapsed into high pressure superheater gaseous state
Heat pump fluid, sending into the condensation of condenser 7 working medium side becomes high pressure supercooled liquid heat pump fluid, flows through device for drying and filtering 8 and by swollen
Swollen valve 9 throttles and becomes the biphase heat pump fluid of low pressure, back flows back into water source vaporizer 10 working medium side to complete heat pump cycle, simultaneously
Condenser heat is released to circulating backwater.80 DEG C of circulating backwaters of heating network flow through electric T-shaped valve 20, filter 13, circulation
Pump 14, check-valves 15, condenser 7 water side, be warming up to 84 DEG C for the first time to absorb another side 5253kW condenser heat, pass through set
Cylinder regenerator 11 water side, flue gas regenerator 12 water side absorb another side set cylinder backheat amount, flue gas backheat amount and respectively second time heat up
To 84.33 DEG C, third time be warming up to 85 DEG C, to become high temperature circulation water outlet, and flow through electric T-shaped valve 20 with to heating network
Heat supply.
5, hot compression water vapour brew cycle: flow 354t/h, 54 DEG C of heat source waters flow through water source vaporizer 10 water side, so that
The biphase heat pump fluid of low pressure flowing into water source vaporizer 10 working medium side absorbs heat and evaporates and become low pressure superheated gaseous heat pump work
Matter, and make heat source water heat release, be cooled to 44 DEG C after discharge；Heat pump fluid is sucked compressor 6 by air entry, and is collapsed into high pressure
Crossing hot gaseous heat pump fluid, sending into the condensation of condenser 7 working medium side becomes high pressure supercooled liquid heat pump fluid, flows through device for drying and filtering
8 and throttled by expansion valve 9 and become the biphase heat pump fluid of low pressure, back flow back into water source vaporizer 10 working medium side and follow to complete heat pump
Ring, is released to circular water replenishing condenser heat simultaneously.The flow 1122t/h of drum 18 outlet at bottom, 80 DEG C of recirculated water warps of temperature
After moisturizing threeway mixes with the moisturizing of flow 9.2t/h, temperature 20 DEG C, circular water replenishing flow through electric T-shaped valve 20, filter 13,
Circulating pump 14, check-valves 15, condenser 7 water side, be warming up to 84 DEG C for the first time to absorb another side 5253kW condenser heat, then flow
Another side set cylinder backheat amount, flue gas backheat amount and second time is absorbed respectively through set cylinder regenerator 11 water side, flue gas regenerator 12 water side
It is warming up to 84.33 DEG C, is warming up to 85 DEG C, to become high temperature circulation moisturizing, after flowing through electric T-shaped valve 20, and at vapour for the third time
Distilling out the low-pressure steam of saturation temperature 80 DEG C in bag 18, the low-pressure steam of last flow 9.2t/h is arranged at drum 18 top
In vapour vapour injector 19, by flowing through diffusion after flow 20t/h therein, absolute pressure 10bar high steam injection, become with modulation
Flow 29.2t/h, the middle pressure steam of absolute pressure 4bar.
Claims (5)
1. a generator drive water source compression heat pump water vapour preparer, it is by electromotor (1)；Air inlet (1-1)；Actively
Axle (1-2)；Air vent (1-3)；Set cylinder cooling water inlet (1-4)；Set cylinder coolant outlet (1-5)；Fuel (2)；Electromotor
(3)；Power transmission and distribution (4)；Motor (5)；Compressor (6)；Condenser (7)；Device for drying and filtering (8)；Expansion valve (9)；Water source evaporates
Device (10)；Set cylinder regenerator (11)；Flue gas regenerator (12)；Filter (13)；Circulating pump (14)；Check-valves (15)；Moisturizing stream
Adjustable valve (16)；Liquid level controller (17)；Drum (18)；Vapour vapour injector (19)；Electric T-shaped valve (20)；Water vapour compresses
Machine (21) forms, it is characterised in that: the air inlet (1-1) of electromotor (1) is entered by pipeline input fuel (2), composition electromotor
Air circuit；The driving shaft (1-2) of electromotor (1) is rotated by electromotor (3) and power transmission and distribution (4) driving electric machine (5), composition
Generator electrical output loop；Set cylinder cooling water inlet (1-4) of electromotor (1) and set cylinder coolant outlet (1-5) are by pipe
Road adapter sleeve cylinder regenerator (11) cooling water side, composition set cylinder cooling back-heating loop；The air vent (1-3) of electromotor (1) passes through
Flue connects flue gas regenerator (12) gas side, forms flue gas backheat loop；Motor (5) drives compressor (6) to rotate, group
Become compressor electric power input circuit；Compressor (6) is connected condenser (7) working medium side, device for drying and filtering (8) by pipeline, is expanded
Valve (9), water source vaporizer (10) working medium side, form water resource heat pump closed circuit；Filter (13), circulating pump (14), check-valves
(15), condenser (7) water side, set cylinder regenerator (11) water side, flue gas regenerator (12) water side, form circulating-heating loop.
2. according to the generator drive water source compression heat pump water vapour preparer described in claim 1, it is characterised in that: drum
(18) outlet at bottom connects moisturizing threeway, filter (13), circulating pump (14), check-valves (15), condenser (7) water by pipeline
Side, set cylinder regenerator (11) water side, flue gas regenerator (12) water side, form moisturizing circulating-heating loop；Drum (18) top goes out
Mouth connects vapour vapour injector (19) by pipeline, forms water vapour hot compression loop.
3. according to the generator drive water source compression heat pump water vapour preparer described in claim 1, it is characterised in that: drum
(18) outlet at bottom connects moisturizing threeway, filter (13), circulating pump (14), check-valves (15), condenser (7) water by pipeline
Side, set cylinder regenerator (11) water side, flue gas regenerator (12) water side, form moisturizing circulating-heating loop；Drum (18) top goes out
Mouth connects water vapour compressor (21) by pipeline, forms water vapour mechanical compress loop.
4. according to the generator drive water source compression heat pump water vapour preparer described in claim 1, it is characterised in that: electronic
Three-way valve (20) connects filter (13), circulating pump (14), check-valves (15), condenser (7) water side, set cylinder backheat by pipeline
Device (11) water side, flue gas regenerator (12) water side, electric T-shaped valve (20), form hot water circulation heated loop.
5. according to the generator drive water source compression heat pump water vapour preparer described in claim 1, it is characterised in that: start
Machine (1) is gas driven explosive motor (1), gasoline driven explosive motor (1), diesel driven explosive motor (1), kerosene
Explosive motor (1), Stirling external-burning engine (1), gas driven gas-turbine engine (1), coal gas is driven to drive combustion gas wheel
Electromotor (1).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
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| CN105972863A (en) * | 2016-06-06 | 2016-09-28 | 侴乔力 | Water vapor modulation machine with water source compression type heat pump driven by generator |
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Effective date of registration: 20191008 Address after: 201501 Shanghai city Jinshan District Fengjing town pavilion Maple Road No. 8289 Patentee after: Shanghai Comer Machinery Co.,Ltd. Address before: 230051 Anhui province Baohe District of Hefei city Yangjiang Road water Ling Water Garden South Building 7 Room 301 Co-patentee before: Chen Jiang Patentee before: Qiaoli |
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Effective date of registration: 20210819 Address after: 314211 building 4, No. 588, Hongqiao North Road, Xindai Town, Pinghu City, Jiaxing City, Zhejiang Province Patentee after: Zhejiang Kemao energy saving and environmental protection engineering equipment Co.,Ltd. Address before: 201501 Shanghai city Jinshan District Fengjing town pavilion Maple Road No. 8289 Patentee before: SHANGHAI COMER MACHINERY Co.,Ltd. |
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Effective date of registration: 20230908 Address after: No. 108 Jiangong Road, Fengjing Town, Jinshan District, Shanghai, January 2015 Patentee after: SHANGHAI COMER MACHINERY Co.,Ltd. Address before: 314211 building 4, No. 588, Hongqiao North Road, Xindai Town, Pinghu City, Jiaxing City, Zhejiang Province Patentee before: Zhejiang Kemao energy saving and environmental protection engineering equipment Co.,Ltd. |