CN209386690U - A kind of vacuum refrigeration coupling waste heat circulation energy-saving dryer - Google Patents
A kind of vacuum refrigeration coupling waste heat circulation energy-saving dryer Download PDFInfo
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- CN209386690U CN209386690U CN201822140370.1U CN201822140370U CN209386690U CN 209386690 U CN209386690 U CN 209386690U CN 201822140370 U CN201822140370 U CN 201822140370U CN 209386690 U CN209386690 U CN 209386690U
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- 230000004087 circulation Effects 0.000 title claims abstract description 47
- 238000005057 refrigeration Methods 0.000 title claims abstract description 39
- 239000002918 waste heat Substances 0.000 title claims abstract description 14
- 230000008878 coupling Effects 0.000 title claims description 5
- 238000010168 coupling process Methods 0.000 title claims description 5
- 238000005859 coupling reaction Methods 0.000 title claims description 5
- 238000004108 freeze drying Methods 0.000 claims abstract description 44
- 230000008676 import Effects 0.000 claims description 74
- 239000012530 fluid Substances 0.000 claims description 37
- 239000003507 refrigerant Substances 0.000 claims description 21
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 claims description 15
- 238000001704 evaporation Methods 0.000 claims description 15
- 230000008020 evaporation Effects 0.000 claims description 13
- 239000007788 liquid Substances 0.000 claims description 12
- 230000005611 electricity Effects 0.000 claims description 11
- 239000002828 fuel tank Substances 0.000 claims description 8
- 239000000463 material Substances 0.000 abstract description 20
- 238000001816 cooling Methods 0.000 abstract description 7
- 238000005265 energy consumption Methods 0.000 abstract description 5
- 238000009777 vacuum freeze-drying Methods 0.000 abstract description 3
- 230000000694 effects Effects 0.000 abstract description 2
- 238000004134 energy conservation Methods 0.000 abstract description 2
- 238000010438 heat treatment Methods 0.000 description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 8
- 238000010521 absorption reaction Methods 0.000 description 4
- 238000004821 distillation Methods 0.000 description 4
- 238000001035 drying Methods 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 4
- 238000009938 salting Methods 0.000 description 4
- 239000007789 gas Substances 0.000 description 3
- 230000017525 heat dissipation Effects 0.000 description 3
- 238000004064 recycling Methods 0.000 description 3
- 238000000859 sublimation Methods 0.000 description 3
- 230000008022 sublimation Effects 0.000 description 3
- 230000009471 action Effects 0.000 description 2
- 230000005496 eutectics Effects 0.000 description 2
- 238000007710 freezing Methods 0.000 description 2
- 230000008014 freezing Effects 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 235000013324 preserved food Nutrition 0.000 description 2
- LVGUZGTVOIAKKC-UHFFFAOYSA-N 1,1,1,2-tetrafluoroethane Chemical compound FCC(F)(F)F LVGUZGTVOIAKKC-UHFFFAOYSA-N 0.000 description 1
- 241000251511 Holothuroidea Species 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000002637 fluid replacement therapy Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 235000016709 nutrition Nutrition 0.000 description 1
- 230000035764 nutrition Effects 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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Abstract
The utility model relates to a kind of vacuum refrigerations to couple waste heat circulation energy-saving dryer, using refrigeration compressor as main power machines, while double evaporators provide cooling capacity for freeze-drying system, it recycles condenser heat rejection and distils and parse step-up temperature for material, the main components such as freeze drying box, vacuum pump, cold-trap, electric heater, compressor, condenser, throttle valve, evaporator are combined together, flow is controlled and adjusted by all kinds of valves, completes the vacuum freeze drying of material.Unit has compact-sized, coefficient of performance height, the obvious feature of energy conservation and consumption reduction effects.
Description
Technical field
The present invention relates to a kind of vacuum refrigerations to couple waste heat circulation energy-saving dryer, belongs to refrigeration technology field.
Background technique
Vacuum freeze drying is that wet stock is first frozen into eutectic temperature or less, so that moisture is become solid ice, then
In vacuum and lower than under eutectic temperature, making ice distillation be water vapour, under vacuum pump swabbing action, water vapour enters cold-trap simultaneously
It is captured, to obtain the technology of dried product.Freeze Drying Technique is able to maintain the structure, property, shape of dried material
And bioactivity, and be able to maintain substantially after frozen dried food rehydration its it is fresh when color, shape, mouthfeel and nutrition, receive people
Popular welcome.But since freeze-drying is longer than the time required to other drying means, energy consumption is high, cause frozen dried food cost
Height, selling price is expensive, limits its widespread development.
Problems of the prior art are: vacuum freeze drying decilitre China and two stages of parsing, in order to take off moisture
It removes, needs to heat material in the two stages, remove its internal moisture, and condense in cold-trap.A side in the process
Face needs cold-trap and evaporator to absorb heat, and heat is discharged in environment by condenser, on the other hand needs electricity auxiliary again
Heating or boiler heat supplying make material that distillation and parsing-desiccation occur.For entire vacuum freezing drying device, in discharge heat
While again to its input heat, cause the waste of energy and repeatedly input, eventually lead to freeze-drying energy consumption it is higher.Cause
This, the energy input by rationally planning as a whole complete machine exports, and proposes novel freezing drying device, can reduce the freeze-drying energy and disappear
Consumption, and then the cost of freeze-drying prods is reduced, push the popularization and application of freeze drying technology.
Summary of the invention
It is an object of the invention to overcome above-mentioned the deficiencies in the prior art, a kind of vacuum refrigeration coupling waste heat circulation section is provided
Energy drying machine is used for heated material in distillation and the heat of parsing-desiccation stage recycling condenser, greatly reduces even without electricity
Heating, to reduce the energy consumption of freeze-drying.
Technical principle and technology path of the invention is as follows:
A kind of vacuum refrigeration proposed by the present invention couples waste heat circulation energy-saving dryer, and condenser uses water-cooled condenser,
Fluid media (medium) is that oil or ethylene glycol salting liquid, the fluid media (medium) of condenser are connected to freeze drying box, and refrigerant is in evaporator and cold-trap
After interior recycling heat, after compressor compresses, become the gas of high temperature and pressure, fluid Jie is transferred heat in condenser
Matter.Distillation with the parsing-desiccation stage, fluid media (medium) under pumping action enter freeze drying box, heated material, provide water sublimed with
Heat needed for parsing, insufficient section are provided by electricity auxiliary heating.
For achieving the above object, technical solution is described in detail below:
A kind of vacuum refrigeration couples waste heat circulation energy-saving dryer, including refrigeration compressor 1, condenser 2, fluid reservoir 3, the
One throttle valve 4, the 5th solenoid valve 24, evaporator 5, the first solenoid valve 6, second throttle 7, cold-trap 8, check-valves 9, freeze drying box
10, radiator 11, second solenoid valve 12, the 6th solenoid valve 13, first circulation pump 14, electric heater 15, third solenoid valve 16, electricity
Dynamic valve 17, case trap valve 18, fuel tank 19, the 4th solenoid valve 20, second circulation pump 21, vacuum pump 22, shut-off valve 23；
Also, condenser coil 2-1 built in condenser 2, evaporation coil 5-1 built in evaporator 5, cold-trap coil pipe built in cold-trap 8
8-1；
The vacuum freeze drier includes refrigerant circuit and fluid media (medium) circuit；
The import of condenser coil 2-1, condenser coil 2-1 in the outlet of the refrigeration compressor 1 connection condenser 2 of refrigerant circuit
Outlet connection 3 import of fluid reservoir, the outlet of fluid reservoir 3 are separately connected 6 import of the 5th solenoid valve 24 and the first solenoid valve, the 5th electromagnetism
The outlet of valve 24 connection 4 import of first throttle valve, the evaporation coil 5-1 import of the outlet of first throttle valve 4 connection evaporator 5, evaporation
The outlet coil pipe 5-1 connection 1 import of refrigeration compressor；
First solenoid valve 6 outlet connection 7 import of second throttle, the cold-trap coil pipe of the outlet of second throttle 7 connection cold-trap 8
8-1 import, the outlet cold-trap coil pipe 8-1 connection 9 import of check-valves, connects after the outlet of check-valves 9 is in parallel with the outlet evaporation coil 5-1
1 import of refrigeration compressor, wherein circulatory mediator is refrigerant；
8 lower exit port of cold-trap in fluid media (medium) circuit connects 23 import of shut-off valve, 23 outfall drain of shut-off valve；Under freeze drying box 10
Side is exported into 18 import of case trap valve, the outlet of case trap valve 18 connection 8 upper inlet of cold-trap is connect, and 8 left side outlet of cold-trap connects vacuum pump 22
Import,
The outlet of 10 lower right-hand side of freeze drying box is separately connected 5 import of evaporator, 13 import of the 6th solenoid valve and fuel tank 19, evaporates
5 left side outlet of device connects second circulation and pumps 21 imports, 21 outlet connection 20 import of the 4th solenoid valve of second circulation pump, the 4th electromagnetism
The outlet of valve 20 connection 10 right side upper inlet of freeze drying box,
First circulation pump 14 exports connection 2 import of condenser, and the outlet of condenser 2 is separately connected 11 import of radiator and electricity adds
Hot 15 import of device, the outlet of radiator 11 connection 12 import of second solenoid valve, the outlet of second solenoid valve 12 goes out with the 6th solenoid valve 13
Connection first circulation pumps 14 imports after mouth is in parallel, and the outlet of electric heater 15 connects 16 import of third solenoid valve, third solenoid valve 16
Outlet connection 17 import of motor-driven valve, the outlet of motor-driven valve 17 and the 4th solenoid valve 20 export it is in parallel after above connection freeze drying box 10 right side
Import, wherein circulatory mediator is oil or ethylene glycol salting liquid.
It is preferred that the condenser 2 is liquid condenser.
A kind of vacuum refrigeration couples waste heat circulation energy-saving dryer, the device on the basis for guaranteeing energy balance, with
Refrigeration compressor is as main power machines, while double evaporators provide cooling capacity for freeze-drying system, utilizes the heat of condenser releasing
Amount provides Elevated Temperature Conditions in material sublimation stage, by freeze drying box, vacuum pump, cold-trap, electric heater, compressor, condenser, throttling
The main components such as valve, evaporator are combined together, and control and adjust flow by all kinds of valves, complete the freeze-drying of material.
The present invention has following innovation compared with prior art: the present invention is changed existing freeze-drier and is added completely using electricity
Hot device or boiler provide the status of material moisture removing institute's calorific requirement, absorb heat by evaporator in refrigeration cycle and cold-trap,
Condenser is sent to by refrigerant, then condenser heat is recycled by oil or ethylene glycol salting liquid, freeze drying box heated material is sent to, realizes
Fully and rationally using for heat, directly recycling condenser heat are used for dry materials, so that freeze-drying energy consumption will be greatly reduced, together
When due to condenser it is cooling using liquid, condensation temperature is greatly reduced, and unit performance coefficient is improved, and further brings energy conservation
Lower consumption effect.
Detailed description of the invention
Fig. 1 is that a kind of vacuum refrigeration of the embodiment of the present invention 1 couples waste heat circulation energy-saving dryer structural schematic diagram.
Wherein, 1-refrigeration compressor, 2-condensers, 2-1-condenser coil, 3-fluid reservoirs, 4-first throttle valves,
5-evaporators, 5-1-evaporation coil, the 6-the first solenoid valve, 7-second throttle, 8-cold-traps, 8-1-cold-trap coil pipe, 9-
Check-valves, 10-freeze drying box, 11-radiators, 12-second solenoid valves, the 13-the six solenoid valve, 14-first circulations pump,
15-electric heaters, 16-third solenoid valves, 17-motor-driven valves, 18-casees trap valves, 19-fuel tanks, the 20-the four solenoid valve,
21-second circulations pump, 22-vacuum pumps, 23-shut-off valves, the 24-the five solenoid valve.
Specific embodiment
To make the purpose of the present invention, characteristics and advantages definitely, with reference to the accompanying drawing with regard to best embodiment party of the invention
Formula elaborates, wherein all around all refers to up and down described in attached drawing from bearing sense described in figure.
Embodiment 1
A kind of vacuum refrigeration couples waste heat circulation energy-saving dryer, including refrigeration compressor 1, condenser 2, fluid reservoir 3, the
One throttle valve 4, the 5th solenoid valve 24, evaporator 5, the first solenoid valve 6, second throttle 7, cold-trap 8, check-valves 9, freeze drying box
10, radiator 11, second solenoid valve 12, the 6th solenoid valve 13, first circulation pump 14, electric heater 15, third solenoid valve 16, electricity
Dynamic valve 17, case trap valve 18, fuel tank 19, the 4th solenoid valve 20, second circulation pump 21, vacuum pump 22, shut-off valve 23；
Also, condenser coil 2-1 built in condenser 2, evaporation coil 5-1 built in evaporator 5, cold-trap coil pipe built in cold-trap 8
8-1；
The vacuum freeze drier includes refrigerant circuit and fluid media (medium) circuit；
The import of condenser coil 2-1, condenser coil 2-1 in the outlet of the refrigeration compressor 1 connection condenser 2 of refrigerant circuit
Outlet connection 3 import of fluid reservoir, the outlet of fluid reservoir 3 are separately connected 6 import of the 5th solenoid valve 24 and the first solenoid valve, the 5th electromagnetism
The outlet of valve 24 connection 4 import of first throttle valve, the evaporation coil 5-1 import of the outlet of first throttle valve 4 connection evaporator 5, evaporation
The outlet coil pipe 5-1 connection 1 import of refrigeration compressor；
First solenoid valve 6 outlet connection 7 import of second throttle, the cold-trap coil pipe of the outlet of second throttle 7 connection cold-trap 8
8-1 import, the outlet cold-trap coil pipe 8-1 connection 9 import of check-valves, connects after the outlet of check-valves 9 is in parallel with the outlet evaporation coil 5-1
1 import of refrigeration compressor, wherein circulatory mediator is refrigerant；
8 lower exit port of cold-trap in fluid media (medium) circuit connects 23 import of shut-off valve, 23 outfall drain of shut-off valve；Under freeze drying box 10
Side is exported into 18 import of case trap valve, the outlet of case trap valve 18 connection 8 upper inlet of cold-trap is connect, and 8 left side outlet of cold-trap connects vacuum pump 22
Import,
The outlet of 10 lower right-hand side of freeze drying box is separately connected 5 import of evaporator, 13 import of the 6th solenoid valve and fuel tank 19, evaporates
5 left side outlet of device connects second circulation and pumps 21 imports, 21 outlet connection 20 import of the 4th solenoid valve of second circulation pump, the 4th electromagnetism
The outlet of valve 20 connection 10 right side upper inlet of freeze drying box,
First circulation pump 14 exports connection 2 import of condenser, and the outlet of condenser 2 is separately connected 11 import of radiator and electricity adds
Hot 15 import of device, the outlet of radiator 11 connection 12 import of second solenoid valve, the outlet of second solenoid valve 12 goes out with the 6th solenoid valve 13
Connection first circulation pumps 14 imports after mouth is in parallel, and the outlet of electric heater 15 connects 16 import of third solenoid valve, third solenoid valve 16
Outlet connection 17 import of motor-driven valve, the outlet of motor-driven valve 17 and the 4th solenoid valve 20 export it is in parallel after above connection freeze drying box 10 right side
Import, wherein circulatory mediator is oil or ethylene glycol salting liquid.
In use, a kind of work operation of vacuum refrigeration coupling waste heat circulation energy-saving dryer be divided into pre-freeze, lyophilization,
Parse 3 stages.
1) the pre-freeze stage is to provide cooling capacity for cabinet, so that it is frozen into solid-state the moisture cooling in material.At this time the 5th
Solenoid valve 24, second solenoid valve 12, first circulation pump the 14, the 4th solenoid valve 20, second circulation pump 21 is opened, and the first solenoid valve
6, electric heater 15, third solenoid valve 16, motor-driven valve 17, case trap valve 18, vacuum pump 22, shut-off valve 23, the 6th solenoid valve 13 close
It closes.
The refrigerant vapour that refrigeration compressor 1 exports enters the condenser coil 2-1 in condenser 2, releases a large amount of heat
The liquid for becoming high temperature and pressure afterwards enters first throttle valve 4 by the 5th solenoid valve 24 after fluid reservoir 3, freezes after throttling
Agent becomes the liquid of low-temp low-pressure, into the evaporation coil 5-1 of evaporator 5, becomes the refrigerant gas of low-temp low-pressure after heat absorption,
Flow back to refrigeration compressor 1, refrigerant R134a.
Fluid media (medium), by the under the driving of second circulation pump 21 after fluid media (medium) is absorbed heat in evaporator 5 all the way
Four solenoid valves 20 enter freeze drying box 10, and heat absorption flow back into evaporator 5 in cabinet.Another way fluid media (medium) flows through 2 quilt of condenser
Enter radiator 11 after heating, by second solenoid valve 12 after heat dissipation, flows back to condenser 2 under 14 driving of first circulation pump.
2) the lyophilization stage needs to vacuumize, and appropriate heating at low ambient temperatures, temperature are increased to set temperature (altogether
Crystal point is 5 DEG C low) after, switched by fluid media (medium) with refrigerant circuit on-off and keep its temperature constant, so sublimation stage decilitre
Temperature heating and holding temperature constant two stages.Most of water in sublimation stage material directly becomes gaseous state from solid-state and is taken out
It walks.
Lyophilization stage, the first solenoid valve 6, case trap valve 18, vacuum pump 22 are opened.
In the heating heating period, first circulation pump 14, third solenoid valve 16, motor-driven valve 17, the 6th solenoid valve 13 are opened, the
Five solenoid valves 24, second solenoid valve 12, the 4th solenoid valve 20, second circulation pump 21, electric heater 15, shut-off valve 23 are closed.
The refrigerant vapour that refrigeration compressor 1 exports at this time enters the condenser coil 2-1 in condenser 2, releases a large amount of
The liquid for becoming high temperature and pressure after heat enters second throttle 7 by the first solenoid valve 6 after fluid reservoir 3, makes after throttling
Cryogen successively cold-trap coil pipe 8-1, check-valves 9 through cold-trap 8, flow back to refrigeration compressor 1.Refrigerant will be flowed in condenser coil 2-1
Enter freeze drying box 10 through electric heater 15, third solenoid valve 16, motor-driven valve 17 after the heating of body medium, through the 6th solenoid valve after outflow
13, first circulation pump 14 returns to condenser coil 2-1.Meanwhile vacuum pump 22 is run, air pressure decline in freeze drying box 10, in material
Moisture starts to distil, and enters cold-trap 8 through case trap valve 18, condenses on the cold-trap surface coil pipe 8-1.
After temperature reaches setting value (5 DEG C), into keep temperature constant periods:
When temperature is higher than setting value, second solenoid valve 12, first circulation pump the 14, the 4th solenoid valve 20, second circulation pump
21, the 5th solenoid valve 24 is opened, and third solenoid valve 16, motor-driven valve 17, the 6th solenoid valve 13, electric heater 15, shut-off valve 23 close
It closes.The refrigerant vapour that refrigeration compressor 1 exports enters the condenser coil 2-1 in condenser 2, becomes high temperature and pressure after heat release
Liquid is divided into two-way after fluid reservoir 3, enters the evaporating pan of evaporator 5 after the 5th solenoid valve 24, first throttle valve 4 all the way
Pipe 5-1 becomes the refrigerant gas of low-temp low-pressure after heat absorption, flow back to refrigeration compressor 1；Another way refrigerant is through the first solenoid valve
6, second throttle 7, the cold-trap coil pipe 8-1 into cold-trap 8 provide the cooling capacity of capture vapor, then flow back to system through check-valves 9
Cold compressor 1.
Fluid media (medium), by the under the driving of second circulation pump 21 after fluid media (medium) is absorbed heat in evaporator 5 all the way
Four solenoid valves 20 enter freeze drying box 10, and heat absorption flow back into evaporator 5 in cabinet；Another way fluid media (medium) flows through 2 quilt of condenser
Enter radiator 11 after heating, by second solenoid valve 12 after heat dissipation capacity, flows back to condenser 2 under 14 driving of first circulation pump.
When temperature is lower than setting value, the 5th solenoid valve 24, the 4th solenoid valve 20, second circulation pump 21 are closed, the second electricity
Magnet valve 12, third solenoid valve 16, motor-driven valve 17, the 6th solenoid valve 13 are opened.The refrigerant vapour that refrigeration compressor 1 exports enters
Condenser coil 2-1 in condenser 2, becomes the liquid of high temperature and pressure after heat release, again through the first solenoid valve 6, after fluid reservoir 3
Two throttle valves 7 enter the cold-trap coil pipe 8-1 of cold-trap 8, capture the cooling capacity of vapor, then flow back to refrigeration compressor through check-valves 9
1；
Fluid media (medium), first the condenser coil 2-1 through condenser 2 is heated, and two-way is divided into after outflow, enters radiator all the way
11, by second solenoid valve 12 after heat dissipation capacity, flowed back to condenser coil 2-1 under 14 driving of first circulation pump, another way through electricity plus
Hot device 15, third solenoid valve 16, motor-driven valve 17 enter freeze drying box 10, pass through after the 6th solenoid valve 13 converges with another way after outflow
Condenser coil 2-1 is flowed back under 14 driving of first circulation pump.
Meanwhile temperature sensor is arranged in the fluid media (medium) entrance of freeze drying box 10, to the aperture of motor-driven valve 17 according to freeze-drying
The fluid media (medium) inlet temperature increase rate of case 10 is adjusted, and when fluid media (medium) inlet temperature increase rate is lower, is increased electronic
17 aperture of valve opens the auxiliary heating of electric heater 15 when 17 aperture maximum of motor-driven valve；When fluid media (medium) inlet temperature increases speed
When rate is higher, reduce 17 aperture of motor-driven valve.
3) it needs to further heat up material under vacuum conditions when resolution phase, and keeps certain temperature (parsing temperature
It is generally 25 DEG C -40 DEG C of degree, related to practical material variety), it is precipitated the combination water in material, the material in this example is
Sea cucumber, resolution temperature are 35 DEG C.The heating of resolution phase decilitre temperature and holding temperature constant two stages.In resolution phase material
Most of water be pumped with gaseous state.
First solenoid valve 6, case trap valve 18, vacuum pump 22 are opened.
In the heating heating period and temperature constant periods are kept, the switch state and lyophilization stage phase of valve and pump
Together.
In temperature-rise period, when 17 standard-sized sheet of motor-driven valve, heating temperature cannot still reach setting value, then electric heater 15 is opened
It opens, otherwise closes.
It is identical as the lyophilization stage in this two stage refrigerant circuits, the flowing of fluid media (medium) circuit.
Shut-off valve 23 is water discharging valve, is opened after the completion of dry, allows the remaining water in the inside to flow out, tightens valve after draining again
Door.Fuel tank 19 plays the role of level pressure and is the vacuum freeze drier fluid replacement medium.
The above are of the invention to illustrate, and only of the invention most preferably applies example, is not intended to limit the invention, all at this
The spirit of invention and modification, equivalent replacement within principle etc., should all be within protection scope of the present invention.
Claims (2)
1. a kind of vacuum refrigeration couples waste heat circulation energy-saving dryer, it is characterised in that including refrigeration compressor (1), condenser
(2), fluid reservoir (3), first throttle valve (4), evaporator (5), the first solenoid valve (6), second throttle (7), cold-trap (8), only
Return valve (9), freeze drying box (10), radiator (11), second solenoid valve (12), the 6th solenoid valve (13), first circulation pump (14), electricity
Heater (15), third solenoid valve (16), motor-driven valve (17), case trap valve (18), fuel tank (19), the 4th solenoid valve (20), second
Circulating pump (21), vacuum pump (22), shut-off valve (23), the 5th solenoid valve (24), also, condenser coil (2- built in condenser (2)
1), evaporation coil (5-1) built in evaporator (5), cold-trap coil pipe (8-1) built in cold-trap (8)；
The vacuum refrigeration coupling waste heat circulation energy-saving dryer includes refrigerant circuit and fluid media (medium) circuit；
Refrigerant circuit: the import of condenser coil (2-1), condenser coil in refrigeration compressor (1) outlet connection condenser (2)
The outlet (2-1) connection fluid reservoir (3) import, fluid reservoir (3) outlet are separately connected the 5th solenoid valve (24) and the first solenoid valve (6)
Import, the 5th solenoid valve (24) outlet connection first throttle valve (4) import, first throttle valve (4) outlet connection evaporator (5)
Evaporation coil (5-1) import, evaporation coil (5-1) outlet connection refrigeration compressor (1) import,
First solenoid valve (6) outlet connection second throttle (7) import, second throttle (7) outlet connect cold in cold-trap (8)
Trap coil pipe (8-1) import, cold-trap coil pipe (8-1) outlet connection check-valves (9) import, check-valves (9) outlet and evaporation coil (5-
1) refrigeration compressor (1) import is connected after outlet is in parallel, wherein circulatory mediator is refrigerant；
Fluid media (medium) circuit: cold-trap (8) lower exit port connects shut-off valve (23) import, shut-off valve (23) outfall drain, freeze drying box
(10) lower exit port connects cold-trap (8) upper inlet, cold-trap (8) left side into case trap valve (18) import, case trap valve (18) outlet is connect
Outlet connects vacuum pump (22) import,
The outlet of freeze drying box (10) lower right-hand side is separately connected evaporator (5) import, the 6th solenoid valve (13) import and fuel tank (19),
Evaporator (5) left side outlet connects second circulation and pumps (21) import, and second circulation pumps the 4th solenoid valve (20) of (21) outlet connection
Import, the 4th solenoid valve (20) outlet connection freeze drying box (10) right side upper inlet,
First circulation pump (14) outlet connection condenser (2) import, condenser (2) outlet be separately connected radiator (11) import and
Electric heater (15) import, radiator (11) outlet connection second solenoid valve (12) import, second solenoid valve (12) outlet and the
Connection first circulation pumps (14) import, electric heater (15) outlet connection third solenoid valve after six solenoid valves (13) outlet is in parallel
(16) import, third solenoid valve (16) outlet connection motor-driven valve (17) import, motor-driven valve (17) outlet and the 4th solenoid valve (20)
Upper inlet on the right side of connection freeze drying box (10) after outlet is in parallel, wherein circulatory mediator is oil or ethylene glycol solution.
2. a kind of vacuum refrigeration according to claim 1 couples waste heat circulation energy-saving dryer, it is characterised in that described cold
Condenser (2) is liquid condenser.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201822140370.1U CN209386690U (en) | 2018-12-19 | 2018-12-19 | A kind of vacuum refrigeration coupling waste heat circulation energy-saving dryer |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201822140370.1U CN209386690U (en) | 2018-12-19 | 2018-12-19 | A kind of vacuum refrigeration coupling waste heat circulation energy-saving dryer |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109458793A (en) * | 2018-12-19 | 2019-03-12 | 烟台大学 | A kind of vacuum refrigeration coupling waste heat circulation energy-saving dryer |
| CN111457683A (en) * | 2020-05-19 | 2020-07-28 | 烟台大学 | Novel waste heat and condensed water recovery freeze dryer and operation method thereof |
| CN111457682A (en) * | 2020-05-19 | 2020-07-28 | 烟台大学 | Novel freeze dryer capable of recycling condensed water and operation method thereof |
| CN111536762A (en) * | 2020-05-19 | 2020-08-14 | 烟台大学 | Novel freeze dryer for recycling defrosting water by using residual heat and operation method thereof |
-
2018
- 2018-12-19 CN CN201822140370.1U patent/CN209386690U/en not_active Withdrawn - After Issue
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109458793A (en) * | 2018-12-19 | 2019-03-12 | 烟台大学 | A kind of vacuum refrigeration coupling waste heat circulation energy-saving dryer |
| CN109458793B (en) * | 2018-12-19 | 2024-04-09 | 烟台大学 | Vacuum freezing coupling waste heat circulation energy-saving dryer |
| CN111457683A (en) * | 2020-05-19 | 2020-07-28 | 烟台大学 | Novel waste heat and condensed water recovery freeze dryer and operation method thereof |
| CN111457682A (en) * | 2020-05-19 | 2020-07-28 | 烟台大学 | Novel freeze dryer capable of recycling condensed water and operation method thereof |
| CN111536762A (en) * | 2020-05-19 | 2020-08-14 | 烟台大学 | Novel freeze dryer for recycling defrosting water by using residual heat and operation method thereof |
| CN111457683B (en) * | 2020-05-19 | 2023-06-02 | 烟台大学 | Novel waste heat and condensate recovery freeze dryer and operation method thereof |
| CN111536762B (en) * | 2020-05-19 | 2023-06-23 | 烟台大学 | Novel freeze dryer for recycling defrosting water by utilizing residual heat and operation method thereof |
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