CN207280010U - Ice maker heat recovery equipment - Google Patents
Ice maker heat recovery equipment Download PDFInfo
- Publication number
- CN207280010U CN207280010U CN201721296983.3U CN201721296983U CN207280010U CN 207280010 U CN207280010 U CN 207280010U CN 201721296983 U CN201721296983 U CN 201721296983U CN 207280010 U CN207280010 U CN 207280010U
- Authority
- CN
- China
- Prior art keywords
- hot water
- heat
- evaporator
- ice maker
- compressor
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 238000011084 recovery Methods 0.000 title claims abstract description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 81
- 239000003507 refrigerant Substances 0.000 claims abstract description 14
- 238000001816 cooling Methods 0.000 claims abstract description 13
- 238000009434 installation Methods 0.000 claims abstract description 6
- 230000008676 import Effects 0.000 claims description 3
- 239000002826 coolant Substances 0.000 claims 1
- 238000009833 condensation Methods 0.000 abstract description 11
- 230000005494 condensation Effects 0.000 abstract description 11
- 239000002918 waste heat Substances 0.000 abstract description 5
- 238000004134 energy conservation Methods 0.000 abstract description 2
- 230000007613 environmental effect Effects 0.000 abstract description 2
- 239000003344 environmental pollutant Substances 0.000 abstract description 2
- 231100000719 pollutant Toxicity 0.000 abstract description 2
- 238000010977 unit operation Methods 0.000 abstract description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 36
- 229910021529 ammonia Inorganic materials 0.000 description 18
- 239000007789 gas Substances 0.000 description 12
- 239000000498 cooling water Substances 0.000 description 6
- 238000000034 method Methods 0.000 description 5
- 238000001704 evaporation Methods 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 230000008020 evaporation Effects 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 230000008901 benefit Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 235000008708 Morus alba Nutrition 0.000 description 1
- 240000000249 Morus alba Species 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 238000004176 ammonification Methods 0.000 description 1
- 238000003287 bathing Methods 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 239000002283 diesel fuel Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000005057 refrigeration Methods 0.000 description 1
- 238000010025 steaming Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Abstract
Ice maker heat recovery equipment, on body (1) installation condenser (3), heat regenerator (6), compressor (8), evaporator (11) and expansion valve (9) are sequentially connected into circuit by refrigerant circulation pipeline (4);Wherein, cooling media outlet (2) is picked out on condenser (3), hot water inlet (5) and hot water outlet (7) are connected on heat regenerator (6), cooled medium entrance (10) is connected on evaporator (11).By unit freeze caused by waste heat hot water preparing, improve unit efficiency, improve working conditions, power consumption is less, and heat exchanger effectiveness higher, operating cost is low, cost-effective expense, save unit operation expense.It can not only realize Waste Heat Reuse, reduce the thermal pollution that condensation heat produces environment, and the operating cost and noise of cooling tower can be reduced.Energy conservation and environmental protection, without any disposal of pollutants, securely and reliably.
Description
Technical field
It the utility model is related to the energy-saving structure improved technology of ice maker equipment, especially ice maker heat recovery equipment.
Background technology
Ice maker is the property that is easily compressed and liquefied using gas ammonia come the equipment freezed, and is commonly used in chemical industry, pharmaceutical field.Gas
The process that body is changed into liquid is known as liquefying.The liquefaction of gas ammonia includes the compression and condensation of gas ammonia, gas ammonia condensation temperature under normal pressure
For -33.35 DEG C.Therefore, under normal pressure and temperature, gas ammonia cannot make it be condensed into liquefied ammonia with normal-temperature water.The condensation temperature of ammonia is with pressure
Strong raising and raise, when pressure improves 1.6MPa, condensation temperature is 40 DEG C, higher than general cooling water temperature, therefore can be with
With 25~35 DEG C of room temperature water cooling, it is allowed to liquefy.Gas ammonia is condensed into liquefied ammonia, is completed by freeze cycle, freeze cycle
Mainly by compressing, cooling condensation, throttling expansion, evaporation Four processes composition.Gas ammonia is after ice maker compresses pressure-raising, into condensation
Gas ammonia, liquefied ammonia is condensed into by cooling water by device, is taken away gas ammonia liberated heat by cooling water, condensed liquefied ammonia passes through throttling
Valve (ammonification valve) is down to evaporating pressure by condensing pressure.Ammonia after throttling expansion, the cooled water of evaporation absorption in evaporator
Heat, at this time liquefied ammonia be changed into again gas ammonia be sent into ice maker import.A circulation is so formed, this progress of circulation in cycles,
The temperature of cooled material reaches technological requirement easy to reduction.Ammonia is because latent heat is big, and price is low, and raw material is easy to get and is followed in freezing
Intermediate medium is used as in ring, by ice maker to its work done, has achieveed the purpose that absorbing heat from cryogenic substance passes to high temperature material.
Present recuperation of heat unit covers many fields of refrigeration, for example heat recovery water source heat pump unit, recuperation of heat screw rod are cold
Water dispenser group, recuperation of heat condensation unit etc., meets needed for various fields.Recovery cold water heat machine is widely used in hotel, hospital, mulberry
By fields such as bathing, factory, dormitories.Recovery cold water heat unit is a kind of new handpiece Water Chilling Units, is in common cooling-water machine
On the basis of the new generation product developed, meet the energy saving trend of low-carbon environment-friendly, benefit the nation and the people.Since cooling-water machine process of refrigerastion is one
A heat exchanging process, in process of refrigerastion, necessarily leads to substantial amounts of waste heat, it is necessary to by there is air-cooled two kinds of form condensers of water cooling
Distribute, reduce compressor temperature.Common cooling-water machine is exactly that this partial heat is passed through cooling tower, fan or other forms
It is dispersed into air, wastes thermal energy and electric energy is more, in need then to want additional heat when using hot water and in practical application, wave
Take the energy, take a lot of work laborious.
Utility model content
The purpose of this utility model is to provide ice maker heat recovery equipment, solves above prior art problem, effectively recycling profit
With the circulated heat of ice maker.
The purpose of this utility model will be realized by following technical measures:Including body, cooling media outlet, condensation
Device, refrigerant circulation pipeline, hot water inlet, heat regenerator, hot water outlet, compressor, expansion valve, cooled medium entrance and steaming
Send out device;Installation is sequentially connected condenser, heat regenerator, compressor, evaporator and expansion by refrigerant circulation pipeline on body
Valve is into circuit;Wherein, cooling media outlet is picked out on condenser, hot water inlet and hot water outlet, evaporation are connected on heat regenerator
Cooled medium entrance is connected on device.
Especially, economizer is installed on evaporator.
Especially, connection box for motor is installed on compressor 8, meanwhile, installation touch screen control panel by compressor on body.
Especially, heat regenerator connects clack valve by hot water outlet, subsequently into hot water reservoir;Pacify in hot water reservoir
Fill water replanishing device;Hot water reservoir passes sequentially through filter, pressure gauge and hot water inlet and takes back heat regenerator;Meanwhile hot water stores up
Deposit and hot water valve is picked out by water pump, connecting hose and pressure controller on case.
The advantages of the utility model and effect:By unit freeze caused by waste heat hot water preparing, improve unit efficiency,
Improve working conditions, power consumption is less, and heat exchanger effectiveness higher, operating cost is low, cost-effective expense, saves unit operation and takes
With.It can not only realize Waste Heat Reuse, reduce the thermal pollution that condensation heat produces environment, and the operating cost of cooling tower can be reduced
And noise.Energy conservation and environmental protection, without any disposal of pollutants, securely and reliably.
Brief description of the drawings
Fig. 1 is attachment structure schematic diagram in the utility model embodiment 1.
Fig. 2 is the middle part of the utility model embodiment 1 exceptionally type structure diagram.
Fig. 3 is the external hot water reservoir structure diagram of heat regenerator in the utility model embodiment 1.
Reference numeral includes:Body 1, cooling media outlet 2, condenser 3, refrigerant circulation pipeline 4, hot water inlet 5, heat
Recover 6, hot water outlet 7, compressor 8, expansion valve 9, cooled medium entrance 10, evaporator 11, pressure gauge 12, filter
13rd, clack valve 14, water replanishing device 15, hot water reservoir 16, water pump 17, pressure controller 18, hot water valve 19, connecting hose 20, section heat
Device 21, connection box for motor 22, touch screen control panel 23.
Embodiment
The utility model principle is that handpiece Water Chilling Units are applied to the heating of high-temperature-hot-water, the increased power consumption of meeting, but total power consumption
Relative to boiler heat it is obvious save it is very much, so, either preheated using recuperation of heat or heat hot water, can
Save substantial amounts of system operation expense.
The utility model includes:Body 1, cooling media outlet 2, condenser 3, refrigerant circulation pipeline 4, hot water inlet 5,
Heat regenerator 6, hot water outlet 7, compressor 8, expansion valve 9, cooled medium entrance 10 and evaporator 11.
The utility model is described in further detail with reference to the accompanying drawings and examples.
Embodiment 1:As shown in figure 1 and 2, on body 1 installation by refrigerant circulation pipeline 4 be sequentially connected condenser 3,
Heat regenerator 6, compressor 8, evaporator 11 and expansion valve 9 are into circuit;Wherein, cooling media outlet 2, heat are picked out on condenser 3
Hot water inlet 5 and hot water outlet 7 are connected on recover 6, cooled medium entrance 10 is connected on evaporator 11.
In foregoing, economizer 21 is installed on evaporator 11.
In foregoing, connection box for motor 22 is installed on compressor 8, meanwhile, installation touch-screen control in the side of compressor 8 on body 1
Panel 23.
In foregoing, as shown in Figure 3, heat regenerator 6 connects clack valve 14 by hot water outlet 7, subsequently into hot water storage
Case 16;Water replanishing device 15 is installed in hot water reservoir 16;Hot water reservoir 16 passes sequentially through filter 13, pressure gauge 12 and hot water
Import 5 takes back heat regenerator 6;Meanwhile heat is picked out by water pump 17, connecting hose 20 and pressure controller 18 in hot water reservoir 16
Water valve 19.
In the present embodiment, as shown in Figure 1, the high temperature and high pressure gaseous refrigerant that compressor 8 is discharged is introduced into heat regenerator
6, heat domestic water or other liquid state materials are released, then return to evaporator 11 by condenser 3 and expansion valve 9 and absorb
After the heat of cooled medium, become the gaseous refrigerant of low-temp low-pressure, return to compressor 8.
In the present embodiment, as shown in Figure 3, what is passed through in heat regenerator 6 is the gaseous refrigerant of high temperature and pressure, and temperature is about
70 DEG C -85 DEG C, while high-temperature high-pressure refrigerant is by heat regenerator 6, the water of room temperature is passed through into heat using water circulating pump 17
Water inlet 5 is sent into heat regenerator 6, and water carries out heat exchange with high pressure refrigerant vapor in heat regenerator 6, what refrigerant was condensed
Water temperature is raised at the same time, hot water reservoir 16 is then returned to by hot water outlet 7, water pump 17 again will from hot water reservoir 16
Water is sent into heat regenerator 6 and carries out circulating-heating, hot water temperature is further raised.Water in hot water reservoir 16 is through heat regenerator
More than 6 heat exchange, is finally reached 55 DEG C -60 DEG C or so of water temperature.When hot water temperature reaches setting value, water circulating pump 17 stops
Work.
The utility model is in addition to refrigerating capacity is provided, the condensation heat extraction of recyclable unit, generates 35~40 DEG C of warm water, substitutes
The loss of boiler diesel oil or gas fuel.
Claims (4)
1. ice maker heat recovery equipment, including body (1), cooling media outlet (2), condenser (3), refrigerant circulation pipeline (4),
Hot water inlet (5), heat regenerator (6), hot water outlet (7), compressor (8), expansion valve (9), cooled medium entrance (10) and
Evaporator (11);It is characterized in that, installation is sequentially connected condenser (3), heat by refrigerant circulation pipeline (4) on body (1)
Recover (6), compressor (8), evaporator (11) and expansion valve (9) are into circuit;Wherein, cooling medium is picked out on condenser (3)
Export (2), hot water inlet (5) and hot water outlet (7) are connected on heat regenerator (6), cooled medium is connected on evaporator (11)
Import (10).
2. ice maker heat recovery equipment as claimed in claim 1, it is characterised in that economizer (21) is installed on evaporator (11).
3. ice maker heat recovery equipment as claimed in claim 1, it is characterised in that compressor installs connection box for motor on (8)
(22), meanwhile, touch screen control panel (23) is installed on body (1) by compressor (8).
4. ice maker heat recovery equipment as claimed in claim 1, it is characterised in that heat regenerator (6) is connected by hot water outlet (7)
Clack valve (14) is connect, subsequently into hot water reservoir (16);Water replanishing device (15) is installed in hot water reservoir (16);Hot water reservoir
(16) filter (13), pressure gauge (12) and hot water inlet (5) are passed sequentially through and takes back heat regenerator (6);Meanwhile hot water reservoir
(16) hot water valve (19) is picked out by water pump (17), connecting hose (20) and pressure controller (18) on.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201721296983.3U CN207280010U (en) | 2017-10-10 | 2017-10-10 | Ice maker heat recovery equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201721296983.3U CN207280010U (en) | 2017-10-10 | 2017-10-10 | Ice maker heat recovery equipment |
Publications (1)
Publication Number | Publication Date |
---|---|
CN207280010U true CN207280010U (en) | 2018-04-27 |
Family
ID=61988938
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201721296983.3U Expired - Fee Related CN207280010U (en) | 2017-10-10 | 2017-10-10 | Ice maker heat recovery equipment |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN207280010U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112797607A (en) * | 2021-01-04 | 2021-05-14 | 珠海格力电器股份有限公司 | Heat recovery system, control method and air conditioning unit |
-
2017
- 2017-10-10 CN CN201721296983.3U patent/CN207280010U/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112797607A (en) * | 2021-01-04 | 2021-05-14 | 珠海格力电器股份有限公司 | Heat recovery system, control method and air conditioning unit |
CN112797607B (en) * | 2021-01-04 | 2023-02-24 | 珠海格力电器股份有限公司 | Heat recovery system, control method and air conditioning unit |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN103629854B (en) | The ammonia that a kind of heat medium water drives and the integrated absorption type refrigerating unit of lithium bromide and method | |
CN101000180B (en) | Two-stage and three-stage absorption refrigeration machine | |
CN201666686U (en) | Throttling air supply system with ejectors | |
CN104034083A (en) | Self-driven thermocompression heat pump cooling method and device | |
CN103398485A (en) | Steam compression refrigerating system device and supercooling method | |
CN101482321A (en) | Ultra-low temperature heat pump water heater | |
CN103615824B (en) | A kind of many warm areas cold acquisition methods and device reclaiming driving based on expansion work | |
CN207280010U (en) | Ice maker heat recovery equipment | |
CN201945082U (en) | Integrative industrial water chiller unit | |
CN102778078A (en) | Comprehensive heating and refrigerating energy-saving device and system | |
CN108834386A (en) | A kind of heat recovery module data center | |
CN105352213A (en) | Steam and air cascade refrigerating system | |
CN205718040U (en) | Solar energy, geothermal energy auxiliary CO2trans-critical cycle refrigerating and heat-supplying system | |
CN210512081U (en) | Air conditioner waste heat recovery utilizes system | |
CN208567187U (en) | A kind of ability of swimming water cooling unit | |
CN207112767U (en) | Energy-saving cold-hot economic benefits and social benefits steam generator | |
CN202598947U (en) | Comprehensive heating and refrigeration energy-saving apparatus and system | |
CN209267917U (en) | A kind of heat recovery module data center | |
CN209415835U (en) | A kind of plus supercooling recyclable device moderate and high temperature heat system | |
CN202511521U (en) | Refrigerator | |
CN208431975U (en) | A kind of energy recycling system in cryogenic rectification process | |
CN207299605U (en) | A kind of heated type refrigerating circulatory device | |
CN105865075A (en) | Low-temperature hot water large-temperature-difference lithium bromide absorbing type refrigerating unit | |
CN102022825A (en) | A heat pump hot-water unit for recovering food grade residual heat recovery | |
CN205957531U (en) | Refrigerating system of supplementary water -cooling unit in area |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180427 |
|
CF01 | Termination of patent right due to non-payment of annual fee |