CN106951010A - It is a kind of can continuous alternating temperature constant temperature system and constant temperature method - Google Patents

It is a kind of can continuous alternating temperature constant temperature system and constant temperature method Download PDF

Info

Publication number
CN106951010A
CN106951010A CN201710290495.XA CN201710290495A CN106951010A CN 106951010 A CN106951010 A CN 106951010A CN 201710290495 A CN201710290495 A CN 201710290495A CN 106951010 A CN106951010 A CN 106951010A
Authority
CN
China
Prior art keywords
temperature
module
value
heat
temp
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.)
Pending
Application number
CN201710290495.XA
Other languages
Chinese (zh)
Inventor
栾玉国
于春和
徐世峰
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.)
Shenyang Aerospace University
Original Assignee
Shenyang Aerospace University
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 Shenyang Aerospace University filed Critical Shenyang Aerospace University
Priority to CN201710290495.XA priority Critical patent/CN106951010A/en
Publication of CN106951010A publication Critical patent/CN106951010A/en
Pending legal-status Critical Current

Links

Classifications

    • GPHYSICS
    • G05CONTROLLING; REGULATING
    • G05DSYSTEMS FOR CONTROLLING OR REGULATING NON-ELECTRIC VARIABLES
    • G05D23/00Control of temperature
    • G05D23/19Control of temperature characterised by the use of electric means

Landscapes

  • Physics & Mathematics (AREA)
  • General Physics & Mathematics (AREA)
  • Engineering & Computer Science (AREA)
  • Automation & Control Theory (AREA)
  • Control Of Temperature (AREA)

Abstract

The invention belongs to constant temperature technology field, specifically related to it is a kind of can continuous alternating temperature constant temperature system, including heating module, Water Tank with Temp.-controlled, refrigeration module, monitoring module, control module and host module, described heating module, refrigeration module, monitoring module are connected with the control module respectively, and described monitoring module, heating module are also connected with the Water Tank with Temp.-controlled respectively with the refrigeration module;Described host module is connected with the control module;Simultaneously present invention also offers a kind of method of constant temperature, during isoperibol, the system changes traditional passive actively, to carry out actively mending temperature preferably to keep isoperibol to constant temperature system;In heat temperature raising, by algorithm make system rapidly and efficiently reach design temperature;Refrigerating plant is added, similar heating algorithm is used when needing cooling so that system drops to assigned temperature well, makes system more perfect;To meet experiment demand, it may be set in constant under different temperatures in specified range.

Description

It is a kind of can continuous alternating temperature constant temperature system and constant temperature method
Technical field
The invention belongs to constant temperature technology field, and in particular to it is a kind of can continuous alternating temperature constant temperature system and constant temperature method.
Background technology
At present, contact constant temperature system is (for example:Water Tank with Temp.-controlled), this system one more and more applied to experiment and scientific research As associative operation is carried out using the constant temperature under liquid (be generally distilled water) environment.In the constant temperature system applied at present, need When wanting heat temperature raising, often occur that temperature after heating is higher than design temperature, the process of design temperature, experiment are then rolled back again In, it is often necessary to it is constant for a long time at a certain temperature, so that the physical quantity of correlation is measured, and during steady temperature, by Gradually scattering and disappearing for heat is caused in system internal-external temperature difference, so that temperature drop, will again after being limited at a temperature of reaching setting Heating is heated up, so that temperature keeps constant, and this working method not environmentally and easily causes the wasting of resources.At present, constant temperature The constant temperature working method of system, is to start to heat again when certain limit is reached after temperature drop, when reaching or slightly higher Stop heating when design temperature, circulate to reach the purpose of constant temperature with this.The present invention, will change this passive heating and mend temperature Mode, change into actively carry out mend temperature, that is, temperature do not occur decline change in the case of, according to heat balance relation The mode of taking the initiative carries out mending temperature, while, it is necessary to which during refrigeration cool-down, similar heating often occurs in the constant temperature system applied The situation of heating, exactly after cooling to below design temperature, then rises the process for returning to design temperature, for such process again In shortcoming, design a kind of relatively reasonable and energy-conservation mode.
The content of the invention
For not enough in the prior art and shortcoming, the problem of a kind of new method of the present invention is to solve such, root The temperature reached according to needs, closes heater by thermal relationship, temperature stabilization is increased to assigned temperature, in order to keep automatically In assigned temperature constant a period of time, by the way of temperature is mended in active, we will be certainly by the way of control heater power The heat so lost is supplemented, so as to preferably make systems constant in assigned temperature etc., specific technical scheme is as follows:
It is a kind of can continuous alternating temperature constant temperature system,:Including heating module, Water Tank with Temp.-controlled, refrigeration module, monitoring module, control Molding block and host module, Water Tank with Temp.-controlled built with liquid, described heating module, refrigeration module, monitoring module respectively with institute Control module connection is stated, described monitoring module, heating module are also connected with the Water Tank with Temp.-controlled respectively with the refrigeration module; Described host module is connected with the control module;Described monitoring module is used for the temperature of monitor and detection Water Tank with Temp.-controlled, together When data detection signal is transferred to control module, control module controls the heating module pair according to the data detection signal The Water Tank with Temp.-controlled is heated, or control module controls the refrigeration module to the perseverance according to the data detection signal Warm water tank carries out refrigeration cool-down;Set the temperature value of the constant temperature system on the host module, the host module is by temperature Angle value information transfer gives the control module,
Initialization system constant temperature corresponding time at regular intervals in certain temperature range, in order to carry out the survey of constant temperature Try and use.
Further, the heating module is provided with heater, and the power P of the heater is continuously adjustabe and energy On-line Control, can select suitable heating power to be heated as needed.
Further, refrigeration module is provided with refrigerating plant, and the power P of the refrigerating plant simultaneously can be online for continuously adjustabe Control, similarly the power P of refrigerating plant is alterable value, can be adjusted as needed.
According to another aspect of the present invention, additionally provide it is a kind of can continuous alternating temperature constant temperature method, it is characterised in that:Including Following steps,
Step 1:The assigned temperature value Ta that liquid in the Water Tank with Temp.-controlled needs to reach is set on the host module, this In in described Water Tank with Temp.-controlled the temperature of liquid be this constant temperature system temperature;
Step 2:Monitoring module is detected to the real time temperature of liquid in the Water Tank with Temp.-controlled, obtains temperature value information, Temperature value information is transferred to control module by the monitoring module, the assigned temperature value Ta that control module sets host module with Real-time temperature values are contrasted, so that it is determined that system needs to heat or freezed;
Step 3:When the real time temperature is less than assigned temperature value Ta, the heating dress on control module control heating module Put to Water Tank with Temp.-controlled heat time t;Before heating reaches assigned temperature value Ta, heating module releases heat and reaches system During required heat, heater is closed;According to system thermal relation QInhale=k1·QPut, the QPutHeat is released for heater Amount, the QInhaleFor the heat of liquid absorption in Water Tank with Temp.-controlled, fluid temperature stabilization in Water Tank with Temp.-controlled is set to be increased to assigned temperature value Ta;Reach after assigned temperature value Ta, automatically adjusting heater power P is heated systems stay, so that balance system institute Natural dispersed heat, carries out actively mending temperature to liquid in Water Tank with Temp.-controlled, is allowed to constant in assigned temperature value Ta;
Step 4:When the real time temperature is higher than assigned temperature value Ta, control module controls the refrigeration of the refrigeration module Device cooling time t1, refrigerating plant is similarly closed according to the thermal relationship of heat release-heat absorption in advance, temperature stabilization is reduced to institute Need assigned temperature value Ta;Drop to after assigned temperature value Ta, the power P of regulation heating or refrigerating plant is heated or made again It is cold, Water Tank with Temp.-controlled is carried out actively to mend temperature, makes in Water Tank with Temp.-controlled liquid constant in assigned temperature value Ta;
Further, in the step 3 heat time t by adding a coefficient k in the thermal relationship1Value come true It is vertical, i.e.,
QInhale=k1·QPut
Wherein, QInhale=Cm Δs T, QPut=Pt, and then Cm Δs T=k1·P·t
Wherein C is specific heat of liquid, and m is Water Tank with Temp.-controlled liquid quality, and Δ T is constant temperature system temperature variation, wherein P For the heating power of heater, t is the heat time;Determined by experiment and temperature-rise period temperature survey algorithm under the different temperature difference K1Value, so as to set up on k1Mathematical Modeling:
When needing heating, by measuring the different temperature difference so as to choose corresponding k1Value, just can determine that taking for heat time t Value, and then reach the constant of temperature.
Further, actively mend in temperature operation to heater power P in the step 3 with the step 4, being heated The specific selection of value, can be by adding a coefficient k2To determine, setting up model formation is specially:QLose=k2·t′
Wherein, QLoseThe heat lost for this constant temperature system under natural environment, k2For coefficient of heat transfer under the different temperature difference, t ' is Constant temperature system radiates the time, and constant temperature system absorbs heat will be equal with the heat of constant temperature system natural loss, i.e. QInhale=QLoseNamely k1Pt=k2T ', due to being same constant temperature system, then constant temperature system internal-external temperature difference is identical, and constant temperature system is scattering and disappearing naturally Actively heating is carried out while heat and mends temperature, therefore heat time t is also identical with radiating time t ', so:
k1P=k2, i.e.,:
By formulaAs long as determining k2Value, it is possible to obtain power P value;
K under the different temperature difference2Value, can be determined by experiment and temperature constant state temperature survey algorithm.
Further, the cooling time t of refrigerating plant is started in the step 41With starting adding for heater in step 3 Hot time t validation testings are identical.
Advantage of the invention is that:In isoperibol, the system changes traditional passive actively, to enter to constant temperature system Row actively mends temperature preferably to keep constant temperature;In heat temperature raising, by algorithm make system rapidly and efficiently reach setting Temperature;Refrigeration module is added, similar heating algorithm is used when needing cooling so that system drops to assigned temperature well, makes System is more perfect;To meet experiment demand, it may be set in constant under different temperatures in specified range.
Brief description of the drawings
Fig. 1 is the structural representation of this constant temperature system;
Embodiment
In order to make the purpose , technical scheme and advantage of the present invention be clearer, it is right below in conjunction with drawings and Examples The present invention is further elaborated.It should be appreciated that the specific embodiments described herein are merely illustrative of the present invention, and It is not used in the restriction present invention.
As shown in figure 1, it is a kind of can continuous alternating temperature constant temperature system,:Including heating module, Water Tank with Temp.-controlled, refrigeration module, prison Control module and control module, Water Tank with Temp.-controlled built with liquid, described heating module, refrigeration module, monitoring module respectively with institute Control module connection is stated, described monitoring module, heating module are also connected with the Water Tank with Temp.-controlled respectively with the refrigeration module; Described host module is connected with the control module;Described monitoring module is used for the temperature of monitor and detection Water Tank with Temp.-controlled, together When data detection signal is transferred to control module, control module controls the heating module pair according to the data detection signal The Water Tank with Temp.-controlled is heated, or control module controls the refrigeration module to the perseverance according to the data detection signal Warm water tank carries out refrigeration cool-down;Initialization system constant temperature corresponding time at regular intervals in certain temperature range, in order to carry out The test of constant temperature and use.
Further, the heating module is provided with heater, and the power P of the heater is continuously adjustabe and energy On-line Control, can select suitable heating power to be heated as needed.
Further, refrigeration module is provided with refrigerating plant, and the power P of the refrigerating plant simultaneously can be online for continuously adjustabe Control, similarly the power P of refrigerating plant is alterable value, can be adjusted as needed.
According to another aspect of the present invention, additionally provide it is a kind of can continuous alternating temperature constant temperature method, it is characterised in that:Including Following steps,
Step 1:The assigned temperature value Ta that liquid in the Water Tank with Temp.-controlled needs to reach is set on the host module, this In in described Water Tank with Temp.-controlled the temperature of liquid be this constant temperature system temperature;
Step 2:Monitoring module is detected to the real time temperature of liquid in the Water Tank with Temp.-controlled, obtains temperature value information, Temperature value information is transferred to control module by the monitoring module;
Step 3:When the real time temperature is less than assigned temperature value Ta, the heating dress on control module control heating module Put to Water Tank with Temp.-controlled heat time t;Before heating reaches assigned temperature value Ta, heating module releases heat and reaches system During required heat, heater is closed;According to system thermal relation QInhale=k1·QPut, the QPutHeat is released for heater Amount, the QInhaleFor the heat of liquid absorption in Water Tank with Temp.-controlled, fluid temperature stabilization in Water Tank with Temp.-controlled is set to be increased to assigned temperature value Ta;Reach after assigned temperature value Ta, automatically adjusting heater power P is heated systems stay, to select suitable here Heating power P so that the natural dispersed heat of balance system institute, carries out actively mending temperature to liquid in Water Tank with Temp.-controlled, is allowed to permanent It is scheduled on assigned temperature value Ta;
Step 4:When the real time temperature is higher than assigned temperature value Ta, control module controls the refrigeration of the refrigeration module Device cooling time t1, similarly closes refrigerating plant in advance according to the thermal relationship of heat release-heat absorption, temperature stabilization is reduced to institute Need assigned temperature value Ta;Drop to after assigned temperature value Ta, the power P of regulation heating or refrigerating plant is heated or made again It is cold, Water Tank with Temp.-controlled is carried out actively to mend temperature, makes in Water Tank with Temp.-controlled liquid constant in assigned temperature value Ta;
Further, in the step 3 heat time t by adding a coefficient k in the thermal relationship1Value come true It is vertical, i.e.,
QInhale=k1·QPut
Wherein, QInhale=Cm Δs T, QPut=Pt, and then Cm Δs T=k1·P·t
Wherein C is specific heat of liquid, and m is Water Tank with Temp.-controlled liquid quality, and Δ T is constant temperature system temperature variation, and wherein P is The heating power of heater, t is the heat time, and it is right under the different temperature difference to be determined by experiment and temperature-rise period temperature survey algorithm The k answered1Value, so as to set up on k1Mathematical Modeling:
When needing heating, by measuring the different temperature difference so as to choose corresponding k1Value, just can determine that taking for heat time t Value, and then reach the constant of temperature.
Further, actively mend in temperature operation to heater power P in the step 3 with the step 4, being heated The specific selection of value, can be by adding a coefficient k2To determine, setting up model formation is specially:QLose=k2T ',
Wherein, QLoseThe heat lost for this constant temperature system under natural environment, k2For coefficient of heat transfer under the different temperature difference, t ' is Constant temperature system radiates the time, and constant temperature system absorbs heat will be equal with the heat of constant temperature system natural loss, i.e. QInhale=QLoseNamely k1Pt=k2T ', due to being same constant temperature system, then constant temperature system internal-external temperature difference is identical, and constant temperature system is scattering and disappearing naturally Actively heating is carried out while heat and mends temperature, therefore heat time t is also identical with radiating time t ', so:k1P=k2, i.e.,:By formulaAs long as determining k2Value, it is possible to obtain power P value;K under the different temperature difference2Value, can lead to Cross experiment and related temperature constant state temperature survey algorithm is determined.
Further, the cooling time t of refrigerating plant is started in the step 4 with starting adding for heater in step 3 Hot time t1Validation testing is identical.
Associated temperature Measurement Algorithm is used in the present invention, and thereby determines that heating, mend temperature model and parameter k1And k2Take Value, it is specific as follows:
1st, temperature-rise period temperature survey algorithm:
Due in constant temperature system temperature-rise period, due to factors such as natural loss, heating module is caused to release heat QPutAnd It can not be fully absorbed completely by liquid in system, it is assumed that liquid absorbs heat for QInhale, according to heat conservation relation, set up mould Type formula then has, QInhale=k1·QPut, wherein, QInhale=Cm Δs T, QPut=Pt, and then Cm Δs T=k1Pt, wherein C is specific heat of liquid, and m is Water Tank with Temp.-controlled liquid quality, and Δ T is constant temperature system temperature variation, the i.e. temperature difference, and wherein P is heating The heating power of device, t is the heat time.
It can be obtained by above-mentioned formula:
In formula, C, m, Δ T, P are definite value, due to parameter k1Can be by external environment, system heat-insulating property, internal-external temperature difference etc. The influence of factor, so parameter k1It is not a fixed parameter, it will be a variable being continually changing, is sent out by testing Existing k1Value relation in line approximate with time t, using least square method to experimental data carry out fitting a straight line, can be very Good obtains k1Value and time t corresponding relation, so as to obtain parameter k1Value model.
2nd, temperature constant state temperature survey algorithm:
System is in temperature constant state, because system can be by factors such as external environment, system heat-insulating property, internal-external temperature differences Influence, causes constant temperature system meeting natural loss heat, so as to cause the change of system temperature, thus sets up model formation as follows:
QLose=k2·t′
Wherein, QLoseThe heat lost for this constant temperature system under natural environment, k2For coefficient of heat transfer under the different temperature difference, t ' is Constant temperature system radiates the time.Because thermal loss causes the change of temperature, so as to have:
QLose=Cm Δs T
It can be obtained by above-mentioned formula:
K is found through experiments that2Value and the time also approximate relation in line, using least square method to experimental data Fitting a straight line is carried out, can be very good to obtain k2Value and the corresponding relation of time, so as to obtain parameter k2Value model.
3rd, temperature-fall period temperature survey algorithm:
Temperature-fall period parameter value model is similar with temperature-rise period, is not repeated.
Presently preferred embodiments of the present invention is the foregoing is only, is not intended to limit the invention, all essences in the present invention Any modification, equivalent and improvement made within refreshing and principle etc., should be included within the scope of the present invention.

Claims (7)

1. it is a kind of can continuous alternating temperature constant temperature system, it is characterised in that:Including heating module, Water Tank with Temp.-controlled, refrigeration module, monitoring Module, control module and host module, described heating module, refrigeration module, monitoring module connect with the control module respectively Connect, described monitoring module, heating module are also connected with the Water Tank with Temp.-controlled respectively with the refrigeration module;Described main frame mould Block is connected with the control module;Described monitoring module is used for the temperature of monitor and detection Water Tank with Temp.-controlled, while detection data Signal transmission controls the heating module to the Water Tank with Temp.-controlled to control module, control module according to the data detection signal Heated, or control module controls the refrigeration module to the Water Tank with Temp.-controlled system according to the data detection signal Cold cooling;The temperature value of the constant temperature system is set on the host module, the host module transmits temperature value information To the control module.
2. it is as claimed in claim 1 it is a kind of can continuous alternating temperature constant temperature system, it is characterised in that:The heating module is provided with Heater, the power P of the heater is continuously adjustabe and energy On-line Control.
3. it is as claimed in claim 1 it is a kind of can continuous alternating temperature constant temperature system, it is characterised in that:Refrigeration module is stated provided with system Device for cooling, the power P of the refrigerating plant is continuously adjustabe and energy On-line Control.
4. it is a kind of based on described in claim 1-3 can the continuous constant temperature system of alternating temperature constant temperature method, it is characterised in that:Including such as Lower step,
Step 1:The assigned temperature value Ta that liquid in the Water Tank with Temp.-controlled needs to reach is set on the host module;
Step 2:Monitoring module is detected to the real time temperature of liquid in the Water Tank with Temp.-controlled, obtains temperature value information, described Temperature value information is transferred to control module by monitoring module, the assigned temperature value Ta that control module sets host module with real time Temperature value is contrasted, so that it is determined that system needs to heat or freezed;
Step 3:When the real time temperature is less than assigned temperature value Ta, the heater pair on control module control heating module Water Tank with Temp.-controlled heat time t;According to thermal relationship, the QPutHeat, the Q are released for heaterInhaleFor Water Tank with Temp.-controlled The heat of interior liquid absorption, heating reaches before assigned temperature value Ta that heating module releases heat and reaches heat required for system When, heater is closed, fluid temperature stabilization in Water Tank with Temp.-controlled is increased to assigned temperature value Ta;Reach assigned temperature value Ta Afterwards, the power P of regulation heater is heated, and liquid in Water Tank with Temp.-controlled is carried out actively to mend temperature, is allowed to constant and is being specified temperature Angle value Ta;
Step 4:When the real time temperature is higher than assigned temperature value Ta, control module controls the refrigerating plant of the refrigeration module Cooling time t1, refrigerating plant is similarly closed according to the thermal relationship of heat release-heat absorption in advance, temperature stabilization is reduced to required finger Constant temperature angle value Ta;Drop to after assigned temperature value Ta, the power P that heater is adjusted again is heated, Water Tank with Temp.-controlled is carried out Temperature is actively mended, makes fluid temperature in Water Tank with Temp.-controlled constant in assigned temperature value Ta.
5. it is as claimed in claim 4 it is a kind of can continuous alternating temperature constant temperature method, it is characterised in that:When being heated in the step 3 Between t by adding a coefficient k in thermal relationship1Value establish, i.e.,
QInhale=k1·QPut
Wherein, QInhale=Cm Δs T, QPut=Pt, and then Cm Δs T=k1Pt, wherein C are specific heat of liquid, and m is Water Tank with Temp.-controlled liquid quality, Δ T is temperature variation, and wherein P is the heating power of heater, and t is the heat time;Pass through reality Test and temperature-rise period temperature survey algorithm determines k under different temperature difference T1Value, so as to set up on k1Mathematical Modeling:
k 1 = C · m · Δ T P · t
When needing heating, by measuring different temperature difference T so as to choose corresponding k1Value, just can determine that taking for heat time t Value, and then reach the constant of temperature.
6. it is as claimed in claim 4 it is a kind of can continuous alternating temperature constant temperature method, it is characterised in that:With institute in the step 3 State in step 4, the specific selection to heater power P value in temperature operation is actively mended in heating, can be by adding a coefficient k2Come It is determined that, setting up model formation is specially:QLose=k2T ' wherein, QLoseThe heat lost for this constant temperature system under natural environment, k2 For coefficient of heat transfer under the different system temperature difference, t ' is that constant temperature system radiates the time, and constant temperature system absorbs heat will be with constant temperature system certainly The heat so lost is equal, i.e. QInhale=QLoseThat is k1Pt=k2T ', due to being same constant temperature system, then inside and outside constant temperature system The temperature difference is identical, and constant temperature system carries out actively heating while natural dissipated heat and mends temperature, therefore heat time t is with the radiating time T ' is also identical, so:
k1P=k2, i.e.,:
By formulaK is determined again2Value, it is possible to obtain power P value;K under the different temperature difference herein2Value, passes through experiment And temperature constant state temperature survey algorithm is determined.
7. it is as claimed in claim 4 it is a kind of can continuous alternating temperature constant temperature method, it is characterised in that:Start system in the step 4 The cooling time t of device for cooling1It is identical with the heat time t validation testing for starting heater in step 3.
CN201710290495.XA 2017-04-28 2017-04-28 It is a kind of can continuous alternating temperature constant temperature system and constant temperature method Pending CN106951010A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201710290495.XA CN106951010A (en) 2017-04-28 2017-04-28 It is a kind of can continuous alternating temperature constant temperature system and constant temperature method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201710290495.XA CN106951010A (en) 2017-04-28 2017-04-28 It is a kind of can continuous alternating temperature constant temperature system and constant temperature method

Publications (1)

Publication Number Publication Date
CN106951010A true CN106951010A (en) 2017-07-14

Family

ID=59477020

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201710290495.XA Pending CN106951010A (en) 2017-04-28 2017-04-28 It is a kind of can continuous alternating temperature constant temperature system and constant temperature method

Country Status (1)

Country Link
CN (1) CN106951010A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108628358A (en) * 2018-04-23 2018-10-09 中国科学院理化技术研究所 A kind of constant temperature system
CN110825133A (en) * 2019-10-29 2020-02-21 深圳市裕展精密科技有限公司 Temperature control method, device and computer readable storage medium
CN111227962A (en) * 2020-02-26 2020-06-05 浙江隐齿丽医学技术有限公司 Film pressing control system and method for preparing shell-shaped tooth appliance
CN113640335A (en) * 2021-08-12 2021-11-12 醴陵华鑫电瓷科技股份有限公司 Temperature cycle test system for ceramic products

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN2435771Y (en) * 2000-07-17 2001-06-20 张剑文 Automatic power-adjusting thermostat for liquid heating equipment
CN2785007Y (en) * 2005-02-04 2006-05-31 彭永军 Constant temperature box
CN1928761A (en) * 2006-08-25 2007-03-14 中国海洋大学 Multiple temperature control system for aquatic organisms
CN202621198U (en) * 2012-04-28 2012-12-26 河南省建筑科学研究院有限公司 High-accuracy thermostatic waterbath control box
CN104132580A (en) * 2014-08-18 2014-11-05 广东汇嵘节能服务有限公司 Intelligent heat conduction steam-water heat exchange dynamic temperature control method and dynamic temperature control system
CN104166414A (en) * 2014-06-03 2014-11-26 武汉昌宝环保工程有限公司 Small-sized water temperature control system

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN2435771Y (en) * 2000-07-17 2001-06-20 张剑文 Automatic power-adjusting thermostat for liquid heating equipment
CN2785007Y (en) * 2005-02-04 2006-05-31 彭永军 Constant temperature box
CN1928761A (en) * 2006-08-25 2007-03-14 中国海洋大学 Multiple temperature control system for aquatic organisms
CN202621198U (en) * 2012-04-28 2012-12-26 河南省建筑科学研究院有限公司 High-accuracy thermostatic waterbath control box
CN104166414A (en) * 2014-06-03 2014-11-26 武汉昌宝环保工程有限公司 Small-sized water temperature control system
CN104132580A (en) * 2014-08-18 2014-11-05 广东汇嵘节能服务有限公司 Intelligent heat conduction steam-water heat exchange dynamic temperature control method and dynamic temperature control system

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108628358A (en) * 2018-04-23 2018-10-09 中国科学院理化技术研究所 A kind of constant temperature system
CN110825133A (en) * 2019-10-29 2020-02-21 深圳市裕展精密科技有限公司 Temperature control method, device and computer readable storage medium
CN111227962A (en) * 2020-02-26 2020-06-05 浙江隐齿丽医学技术有限公司 Film pressing control system and method for preparing shell-shaped tooth appliance
CN111227962B (en) * 2020-02-26 2021-11-16 浙江隐齿丽医学技术有限公司 Film pressing control system and method for preparing shell-shaped tooth appliance
CN113640335A (en) * 2021-08-12 2021-11-12 醴陵华鑫电瓷科技股份有限公司 Temperature cycle test system for ceramic products

Similar Documents

Publication Publication Date Title
CN106951010A (en) It is a kind of can continuous alternating temperature constant temperature system and constant temperature method
Koseoglu et al. The role of jet inlet geometry in impinging jet heat transfer, modeling and experiments
Wang et al. The novel use of phase change materials in refrigeration plant. Part 1: Experimental investigation
Ezan et al. Energy and exergy analyses of an ice-on-coil thermal energy storage system
CN105326386B (en) Water temperature boiling point determination methods and device and electric kettle
CN107562155A (en) A kind of liquid-cooled suit business device and its flow-measuring method
Cho et al. Experimental and numerical study on the application of low-temperature radiant floor heating system with capillary tube: Thermal performance analysis
CN106052141A (en) Water heater, water temperature setting method of water heater and water temperature setting device of water heater
Cimmino et al. Experimental determination of the g-functions of a small-scale geothermal borehole
CN104112065A (en) Water heater and method for calculating left bath time of water heater
CN107388589A (en) The display control method and device of Hot water units
Zhou et al. Determination and analysis of parameters for an in-situ thermal response test
CN105445319B (en) A kind of method and device for determining the surface of steel plate water cooling coefficient of heat transfer
JP2017501416A (en) Method and apparatus for determining the heat loss coefficient of a building
Wang et al. Heat transfer characteristics of a novel sleeping bed with an integrated hot water heating system
Jiang et al. Experimental investigation on an energy-efficient floor heating system with intelligent control: A case study in Chengdu, China
US9891180B2 (en) Thermal needle probe
Uttam Objective measurement of heat transport through clothing
CN104866694A (en) Optimal start time prediction model of floor-radiating heating system
Atayılmaz Transient and steady-state natural convection heat transfer from a heated horizontal concrete cylinder
Sutjahja et al. Thermophysical Parameters and Enthalpy Temperature Curve of Phase Change Material with Supercooling from T-History Data
Cheng et al. Analysis of heat transfer mechanism for shelf vacuum freeze‐drying equipment
CN104594879A (en) Temperature control device and method for oil and gas field physical simulation experiments
Mandrykin et al. Turbulent convection of liquid sodium in an inclined cylinder of unit aspect ratio
EP3015803A1 (en) A method for estimating thermal capacity of foodstuff

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
RJ01 Rejection of invention patent application after publication
RJ01 Rejection of invention patent application after publication

Application publication date: 20170714