CN106766359B - A kind of refrigerating plant based on heat of solution and industrial waste heat - Google Patents

A kind of refrigerating plant based on heat of solution and industrial waste heat Download PDF

Info

Publication number
CN106766359B
CN106766359B CN201611041003.5A CN201611041003A CN106766359B CN 106766359 B CN106766359 B CN 106766359B CN 201611041003 A CN201611041003 A CN 201611041003A CN 106766359 B CN106766359 B CN 106766359B
Authority
CN
China
Prior art keywords
execution unit
solution
temperature
heat
heat exchanger
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.)
Active
Application number
CN201611041003.5A
Other languages
Chinese (zh)
Other versions
CN106766359A (en
Inventor
林鹏
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Hohai University HHU
Original Assignee
Hohai University HHU
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Hohai University HHU filed Critical Hohai University HHU
Priority to CN201611041003.5A priority Critical patent/CN106766359B/en
Publication of CN106766359A publication Critical patent/CN106766359A/en
Application granted granted Critical
Publication of CN106766359B publication Critical patent/CN106766359B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A30/00Adapting or protecting infrastructure or their operation
    • Y02A30/27Relating to heating, ventilation or air conditioning [HVAC] technologies
    • Y02A30/274Relating to heating, ventilation or air conditioning [HVAC] technologies using waste energy, e.g. from internal combustion engine
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02BCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00Energy efficient heating, ventilation or air conditioning [HVAC]
    • Y02B30/62Absorption based systems
    • Y02B30/625Absorption based systems combined with heat or power generation [CHP], e.g. trigeneration

Abstract

The invention discloses a kind of, and the refrigerating plant based on heat of solution and industrial waste heat is absorbed heat during its dissolution or concentrated solution are diluted to reach the refrigerating method of refrigeration effect using the solute of dissolving and heat absorbing.Execution unit of the present invention is made of valve and water pump etc., with the mixed i.e. controllable cryogenic temperature of speed of execution unit control mixer water inlet, can be controlled the preset value that is concentrated into of the concentration of refrigerant weak solution simply by the effect of execution unit.Subzero can be reduced the temperature to when the concentrated solution dilution of some refrigerants, refrigerating efficiency is higher.The Nitrates substance such as potassium nitrate, sodium nitrate, no pollution to the environment not strong to equipment corrosion can be used in refrigerant.

Description

A kind of refrigerating plant based on heat of solution and industrial waste heat
Technical field
The present invention relates to a kind of refrigerating methods, concretely relate to a kind of solute using dissolving and heat absorbing, in its dissolution Or the diluted heat absorption in the process of concentrated solution is to reach the refrigerating method of refrigeration effect.
Background technique
Under energy background increasingly in short supply, the technology freezed using low grade heat energies such as solar energy, industrial waste heats is more next More it is taken seriously.Absorption type refrigerating, absorption refrigeration can be freezed using low grade heat energy, but there are system control complexity, system Cryogen corrodes the problems such as equipment and inefficiency.Therefore, need a kind of control simpler, more using low grade heat energy refrigeration Increase the refrigerating method of effect, environmental protection.
Summary of the invention
The purpose of the present invention is overcoming deficiency in the prior art, a kind of refrigeration based on solute dissolving and heat absorbing is provided Method, using the solute of a kind of dissolving and heat absorbing as refrigerant, and using low grade heat energy as energy recovery refrigerant.
In order to solve the above-mentioned technical problem, the present invention is achieved through the following technical solutions:
A kind of refrigerating plant based on heat of solution and industrial waste heat, including mixer are provided with heat exchanger in mixer And temperature sensor, mixer are connect by refrigerant concentrated solution input channel with fluid reservoir one, and condensed water input channel is passed through It is connect with fluid reservoir two, control execution unit one is provided on refrigerant concentrated solution input channel, is set on condensed water input channel It is equipped with control execution unit two;
The liquid outlet of mixer connects refrigerant weak solution conveyance conduit, and refrigerant weak solution conveyance conduit is connected to hot friendship The output end of parallel operation one, heat exchanger one is connected to vacuum flask;Condensate output transistor road, condensed water are connected on heat exchanger one Output channel is connected to cooling chamber one;
The liquid outlet of vacuum flask is connected to evaporating separation device by pipeline, and execution unit three is provided on the pipeline, steams It is provided with heat exchanger two and concentration sensor in hair separator, heat exchanger two is connect with industrial waste heat;Evaporation separation dress The liquid outlet connection refrigerant concentrated solution output channel set, refrigerant concentrated solution output channel are connected to cooling chamber two, refrigerant Execution unit four is provided on concentrated solution output channel;
Execution unit one, execution unit two, execution unit three, execution unit four, concentration sensor, temperature sensor with Single-chip computer control system electrical connection.
A kind of refrigerating method based on heat of solution and industrial waste heat, user in single-chip computer control system set temperature value, Concentration value assigns instruction and opens refrigerating plant;
Single-chip computer control system control execution unit one and execution unit two, respectively will be in fluid reservoir one and fluid reservoir two Refrigerant concentrated solution and condensed water input mixer freeze, the low temperature generated in mixer is transferred to by heat exchanger Outside mixer;
Temperature signal is simultaneously transmitted back to single-chip computer control system by temperature in temperature sensor detection mixer, and single-chip microcontroller will Temperature signal and user's setting value compare, and the excessively high then control execution unit one of temperature and execution unit two accelerate potassium nitrate concentrated solution With condensed water input speed fast cooling, to reduce temperature;Temperature is too low, and control execution unit one and execution unit two subtract Slow potassium nitrate concentrated solution and condensed water input speed slow down cooling, so that temperature value be made to reach equal with preset value, mix at this time Solution in device is potassium nitrate weak solution;
Potassium nitrate weak solution in mixer is entered in heat exchanger one by refrigerant weak solution conveyance conduit, heat exchange Device one is connect with evaporating separation device, and the vapor in evaporating separation device, which is attached on heat exchanger one, discharges the latent heat of condensation, It is condensed into condensed water simultaneously, one natural cooling of cooling chamber is entered by the condensate output transistor road being connected on heat exchanger one To room temperature;Potassium nitrate weak solution is then tentatively heated by vapor, into vacuum flask;
Potassium nitrate weak solution in vacuum flask is sent into evaporating separation device by single-chip computer control system control execution unit three In, by the potassium nitrate weak solution in two heating evaporation separator of heat exchanger, concentration passes the heat of thermal power station's hot waste water The concentration of sensor real-time detection potassium nitrate weak solution simultaneously passes concentration signal back to single-chip computer control system, single-chip computer control system pair Specific concentration signal and user preset concentration value, after concentration signal reaches preset value, control execution unit four separates evaporation Potassium nitrate concentrated solution afterwards is delivered to two cooled to room temperature of cooling chamber by refrigerant concentrated solution output channel, is then shut off Control execution unit four opens execution unit three for the potassium nitrate weak solution in vacuum flask and is input to evaporating separation device progress newly The evaporation separation of one wheel;
Liquid is transported in fluid reservoir two and fluid reservoir one by cooling chamber one, cooling chamber two respectively after the completion of cooling.
The working principle of the invention:
(1) refrigeration principle: heat can be absorbed when potassium nitrate is dissolved in water to cool down, concentrated solution is in dilution It can absorb heat, can use this characteristic of potassium nitrate and freeze as refrigerant.Weak solution is obtained after dissolution or dilution, it is dilute molten Liquid can use low grade heat energy evaporation and concentration, thus circularly cooling agent.In addition to potassium nitrate, the chemical substances such as sodium nitrate, urea Also have the characteristics that similar, different refrigerants can be selected according to actual needs in actual application.
(2) process of refrigerastion: user sets the concentration of cryogenic temperature Yu potassium nitrate concentrated solution, single-chip microcontroller control according to actual needs System processed controls the execution unit being made of water pump and valve, makes concentrated nitric acid potassium solution and condensed water hybrid refrigeration, and temperature reduces; Temperature signal is simultaneously returned to single-chip computer control system, single-chip computer control system root by temperature sensor measurement temperature in mixer It is compared according to the signal passed back and user's setting value, then adjusts water pump and valve again, so that the temperature in mixer reaches Setting value.According to user's needs, the low temperature that mixer generates can be passed by circulatory systems such as hot channels.
(3) refrigerant circulating process: the potassium nitrate weak solution temperature that mixer generates is lower than room temperature, uses into heat exchanger In the vapor that condensation evaporation separator concentrate solution generates, and own temperature is increased, to tentatively heat up, efficiently uses Latent heat of moisture.Weak solution after heating enter vacuum flask heat preservation it is spare, wait the control signal of single-chip computer control system.It steams It sends out separator and evaporates weak solution using low grade heat energy, generate vapor and concentrate;Vapor enters heat exchanger, utilizes Above-mentioned dust technology potassium solution condensation, subsequently into condensation water cooling chamber's natural cooling;Concentration sensing in evaporating separation device The concentration signal of potassium nitrate solution is returned to single-chip computer control system by device, and single-chip computer control system is pre- by this signal and user If value compares, so as to adjust execution unit, so that the potassium nitrate solution concentration in evaporating separation device reaches preset value, so Concentrated solution is discharged to potassium nitrate solution cooling chamber natural cooling afterwards, sucking weak solution carries out the concentration of next step.In cooling chamber After the abundant natural cooling of liquid, it is spare to respectively enter two holding vessels.
Compared with prior art, the beneficial effects of the present invention are:
Execution unit of the present invention is made of valve and water pump etc., is with the mixed speed of execution unit control mixer water inlet Controllable cryogenic temperature can be controlled the preset value that is concentrated into of the concentration of refrigerant weak solution by the effect of execution unit Simply.Subzero can be reduced the temperature to when the concentrated solution dilution of some refrigerants, refrigerating efficiency is higher.Nitre can be used in refrigerant The Nitrates substance such as sour potassium, sodium nitrate, no pollution to the environment not strong to equipment corrosion.
Detailed description of the invention
Fig. 1 is structural schematic diagram of the invention.
Specific embodiment
Present invention is further described in detail with specific implementation method with reference to the accompanying drawing:
Assuming that fluid reservoir contains suitable potassium nitrate concentrated solution and condensed water respectively in the middle using potassium nitrate as refrigerant, Using thermal power station's hot waste water as heat source.By taking a refrigeration cycle as an example, the refrigeration based on heat of solution and industrial waste heat is filled It sets and is illustrated.
In conjunction with Fig. 1, user set temperature value, concentration value in single-chip computer control system 13 assign instruction and open refrigeration Device.13 control execution unit 1 of single-chip computer control system and execution unit 2 15, respectively by fluid reservoir 1 and fluid reservoir Potassium nitrate concentrated solution and condensed water input mixer 1 in 29 are freezed, and potassium nitrate concentrated solution passes through refrigerant concentrated solution Input channel 21 enters in mixer 1, and condensed water is entered in mixer 1 by condensed water input channel 20;It is generated in mixer Low temperature be transferred to outside mixer by heat exchanger 2;
Temperature signal is simultaneously transmitted back to single-chip computer control system 13 by temperature in 11 detection mixer 1 of temperature sensor, single Piece machine compares temperature signal and user's setting value, and the excessively high then control execution unit 1 of temperature and execution unit 2 15 accelerate nitre Sour potassium concentrated solution and condensed water input speed fast cooling, to reduce temperature;Too low one 14 He of then control execution unit of temperature Execution unit 2 15 slows down potassium nitrate concentrated solution and condensed water input speed slows down cooling, so that temperature value be made to reach and preset value Equal, the solution in mixer is potassium nitrate weak solution at this time;
Potassium nitrate weak solution in mixer 1 is entered in heat exchanger 1 by refrigerant weak solution conveyance conduit 22, heat Exchanger one is connect with evaporating separation device, and the vapor in evaporating separation device 5, which is attached on heat exchanger 1, discharges condensation Latent heat, while it being condensed into condensed water, cooling chamber 1 is entered by the condensate output transistor road 18 being connected on heat exchanger one Cooled to room temperature;Potassium nitrate weak solution is then tentatively heated by vapor, into vacuum flask 6;
Potassium nitrate weak solution in vacuum flask is sent into evaporation separation by 13 control execution unit 3 16 of single-chip computer control system In device 5, the heat of thermal power station's hot waste water passes through heat exchanger 24, and the potassium nitrate in heating evaporation separator 5 is dilute molten Liquid, the concentration of 12 real-time detection potassium nitrate weak solution of concentration sensor simultaneously pass concentration signal back to single-chip computer control system 13, list 13 reduced concentration signal of piece machine control system and user preset concentration value, after concentration signal reaches preset value, control is executed Potassium nitrate concentrated solution after evaporation separation is delivered to cooling chamber 28 certainly by refrigerant concentrated solution output channel 19 by unit 4 17 It is so cooled to room temperature, is then shut off control execution unit 4 17, open execution unit 3 16 potassium nitrate in vacuum flask 6 is dilute molten Liquid is input to the evaporation separation that evaporating separation device 5 carries out a new round.
Liquid is transported to fluid reservoir 29 and fluid reservoir 1 respectively after the completion of cooling by cooling chamber 1, cooling chamber 28 In.So far, a refrigeration cycle is completed.

Claims (2)

1. a kind of refrigerating plant based on heat of solution and industrial waste heat, which is characterized in that including mixer, be provided in mixer Heat exchanger and temperature sensor, mixer are connect by refrigerant concentrated solution input channel with fluid reservoir one, and condensed water is passed through Input channel is connect with fluid reservoir two, and control execution unit one, condensed water input are provided on refrigerant concentrated solution input channel Control execution unit two is provided on pipeline;
The liquid outlet of mixer connects refrigerant weak solution conveyance conduit, and refrigerant weak solution conveyance conduit is connected to heat exchanger One, the output end of heat exchanger one is connected to vacuum flask;Condensate output transistor road, condensed water output are connected on heat exchanger one Pipeline is connected to cooling chamber one;
The liquid outlet of vacuum flask is connected to evaporating separation device by pipeline, and execution unit three, evaporation point are provided on the pipeline From heat exchanger two and concentration sensor is provided in device, heat exchanger two is connect with industrial waste heat;Evaporating separation device Liquid outlet connects refrigerant concentrated solution output channel, and refrigerant concentrated solution output channel is connected to cooling chamber two, and refrigerant is dense molten Execution unit four is provided on liquid output channel;
Execution unit one, execution unit two, execution unit three, execution unit four, concentration sensor, temperature sensor are and monolithic Machine control system electrical connection.
2. a kind of refrigerating method based on heat of solution and industrial waste heat, which is characterized in that user sets in single-chip computer control system Determine temperature value, concentration value, assigns instruction and open refrigerating plant;
Single-chip computer control system control execution unit one and execution unit two, respectively by the system in fluid reservoir one and fluid reservoir two Cryogen concentrated solution and condensed water input mixer freeze, and the low temperature generated in mixer is transferred to mixing by heat exchanger Outside device;
Temperature signal is simultaneously transmitted back to single-chip computer control system by temperature in temperature sensor detection mixer, and single-chip microcontroller is by temperature Signal and user's setting value compare, and the excessively high then control execution unit one of temperature and execution unit two accelerate potassium nitrate concentrated solution and cold Condensate input speed fast cooling, to reduce temperature;Temperature is too low, and control execution unit one and execution unit two slow down nitre Sour potassium concentrated solution and condensed water input speed slow down cooling, to make temperature value reach equal with preset value, at this time in mixer Solution be potassium nitrate weak solution;
Potassium nitrate weak solution in mixer is entered in heat exchanger one by refrigerant weak solution conveyance conduit, heat exchanger one It is connect with evaporating separation device, the vapor in evaporating separation device, which is attached on heat exchanger one, discharges the latent heat of condensation, simultaneously It is condensed into condensed water, cooling chamber one is entered by the condensate output transistor road being connected on heat exchanger one and naturally cools to room Temperature;Potassium nitrate weak solution is then tentatively heated by vapor, into vacuum flask;
Potassium nitrate weak solution in vacuum flask is sent into evaporating separation device by single-chip computer control system control execution unit three, fire For the heat of power station hot waste water by the potassium nitrate weak solution in two heating evaporation separator of heat exchanger, concentration sensor is real When detection potassium nitrate weak solution concentration and pass concentration signal back to single-chip computer control system, single-chip computer control system reduced concentration Signal and user preset concentration value, after concentration signal reaches preset value, control execution unit four will evaporate the nitre after separating Sour potassium concentrated solution is delivered to two cooled to room temperature of cooling chamber by refrigerant concentrated solution output channel, is then shut off control and holds Row unit four opens execution unit three for the potassium nitrate weak solution in vacuum flask and is input to an evaporating separation device progress new round Evaporation separation;
Liquid is transported in fluid reservoir two and fluid reservoir one by cooling chamber one, cooling chamber two respectively after the completion of cooling.
CN201611041003.5A 2016-11-22 2016-11-22 A kind of refrigerating plant based on heat of solution and industrial waste heat Active CN106766359B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201611041003.5A CN106766359B (en) 2016-11-22 2016-11-22 A kind of refrigerating plant based on heat of solution and industrial waste heat

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201611041003.5A CN106766359B (en) 2016-11-22 2016-11-22 A kind of refrigerating plant based on heat of solution and industrial waste heat

Publications (2)

Publication Number Publication Date
CN106766359A CN106766359A (en) 2017-05-31
CN106766359B true CN106766359B (en) 2019-03-19

Family

ID=58974998

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201611041003.5A Active CN106766359B (en) 2016-11-22 2016-11-22 A kind of refrigerating plant based on heat of solution and industrial waste heat

Country Status (1)

Country Link
CN (1) CN106766359B (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110303654A (en) * 2019-05-28 2019-10-08 泸州市胜科模具制造有限公司 A kind of Bottle Coating Box pedestal injection mold
CN115229214B (en) * 2022-07-15 2024-01-09 深圳大学 Additive manufacturing and remanufacturing environment temperature adjusting device and method

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN2126595Y (en) * 1992-07-02 1993-01-20 阎守华 Household cold wind device
CN1453529A (en) * 2002-04-22 2003-11-05 童成双 Dissolving and heat absorbing chemical heat pump
CN201497249U (en) * 2009-09-23 2010-06-02 刘永强 Dissolving enthalpy change refrigerating and heating machine
CN102287952A (en) * 2011-06-23 2011-12-21 江苏河海新能源有限公司 Dissolving heat absorption type chemical heat pump and heating or refrigerating method thereof
CN102455082A (en) * 2010-10-26 2012-05-16 谢鹏飞 Refrigerator for refrigerating with low-grade heat energy and chemical substance dissolving heat
US9360242B2 (en) * 2013-05-17 2016-06-07 Rebound Technologies, Inc. Methods, systems, and devices for producing a heat pump

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN2126595Y (en) * 1992-07-02 1993-01-20 阎守华 Household cold wind device
CN1453529A (en) * 2002-04-22 2003-11-05 童成双 Dissolving and heat absorbing chemical heat pump
CN201497249U (en) * 2009-09-23 2010-06-02 刘永强 Dissolving enthalpy change refrigerating and heating machine
CN102455082A (en) * 2010-10-26 2012-05-16 谢鹏飞 Refrigerator for refrigerating with low-grade heat energy and chemical substance dissolving heat
CN102287952A (en) * 2011-06-23 2011-12-21 江苏河海新能源有限公司 Dissolving heat absorption type chemical heat pump and heating or refrigerating method thereof
US9360242B2 (en) * 2013-05-17 2016-06-07 Rebound Technologies, Inc. Methods, systems, and devices for producing a heat pump

Also Published As

Publication number Publication date
CN106766359A (en) 2017-05-31

Similar Documents

Publication Publication Date Title
KR101851230B1 (en) High efficiency absorption type heat pump system with increasing function for utilization rate from waste heat
KR101851231B1 (en) Absorption type heat pump system for gaining high temperature
CN104848581B (en) Two stage evaporation and absorption double effect type lithium bromide absorption refrigeration/heating machine unit
CN106766359B (en) A kind of refrigerating plant based on heat of solution and industrial waste heat
CN107144042A (en) A kind of second-kind absorption-type heat pump
CN106440476A (en) Two-stage independent cascade double-effect lithium bromide absorption type refrigerating heat pump unit
CN106247683A (en) A kind of CO2seizure system and technique
CN206695430U (en) First class lithium bromide absorptive heat pump unit with condensate recuperation of heat
CN204630144U (en) Dual circulation absorbs dual effect type lithium bromide absorbing type refrigeration/heating machine set
CN103657120B (en) Ultra high efficiency energy-saving type vacuum enrichment facility and method
CN103940146A (en) Cold and heat continuously-supplying system and method based on server waste heat and solar energy
CN103542592A (en) Direct combustion type lithium bromide absorption cold and hot water unit with heat recycling function
CN206944475U (en) A kind of two-period form Hot water units system
CN203731736U (en) Double-effect lithium bromide absorption heat transformer with function of coolant water heat recovery
CN202237295U (en) Device for drying and concentrating solution in vacuum
CN202521939U (en) Heat pump system and drying system
CN106642795B (en) Superposition type solution parallel connection mono-potency lithium bromide absorption type refrigeration heat pump unit
US10359217B2 (en) Continuous adsorption cooling system with air-cooled heat rejection unit
CN106403354B (en) Superposition type solution parallel double-effect lithium bromide absorption type refrigeration heat pump unit
CN101832678B (en) Absorbent solution circulating system and method
CN104807237A (en) Energy-saving device applying lithium bromide
CN203880999U (en) Cooling and heating combined system based on server waste heat and solar energy
CN219045821U (en) Absorption heat pump for driving steam to melt crystal
CN103542593A (en) Smoke heat recycling type lithium bromide absorption cold-hot water unit
CN103807947A (en) Forward osmosis regeneration device of heat source tower antifreeze solution

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant