CN211101488U - System for stabilizing convection heat exchange coefficient of crystallizer copper plate cooling water - Google Patents

System for stabilizing convection heat exchange coefficient of crystallizer copper plate cooling water Download PDF

Info

Publication number
CN211101488U
CN211101488U CN201921684609.XU CN201921684609U CN211101488U CN 211101488 U CN211101488 U CN 211101488U CN 201921684609 U CN201921684609 U CN 201921684609U CN 211101488 U CN211101488 U CN 211101488U
Authority
CN
China
Prior art keywords
water
cooling water
copper plate
crystallizer
crystallizer copper
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
CN201921684609.XU
Other languages
Chinese (zh)
Inventor
曾晶
王文学
王蓉
刘赵卫
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.)
China National Heavy Machinery Research Institute Co Ltd
Original Assignee
China National Heavy Machinery Research Institute Co Ltd
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 China National Heavy Machinery Research Institute Co Ltd filed Critical China National Heavy Machinery Research Institute Co Ltd
Priority to CN201921684609.XU priority Critical patent/CN211101488U/en
Application granted granted Critical
Publication of CN211101488U publication Critical patent/CN211101488U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Abstract

The utility model provides a system for stabilize crystallizer copper cooling water convection heat transfer coefficient, calculate module, T including crystallizer copper cooling water yieldmeanThe system comprises a processing module, a water quantity control module, a water inlet temperature sensor, a water outlet temperature sensor, an electromagnetic flowmeter and a pneumatic regulating valve. The utility model discloses in slab caster's production, according to the steel grade of production, the change of pulling rate, the water yield through dynamic adjustment crystallizer copper cooling water makes the coefficient of convection heat transfer of cooling water in crystallizer copper water seam reach and keep at predetermined target value, and real-time balance and the influence that the temperature change of eliminating the cooling water brought have avoided leading to crystallization because of the change of crystallizer copper cooling water supply temperatureA phenomenon that the cooling intensity of the cooler deviates from a predetermined value occurs; the probability of surface cracks of the steel grade sensitive to the hot cracks is reduced, and the surface quality of the casting blank is further improved.

Description

System for stabilizing convection heat exchange coefficient of crystallizer copper plate cooling water
Technical Field
The utility model belongs to the technical field of metallurgical continuous casting equipment, concretely relates to system for stabilizing crystallizer copper cooling water convection heat transfer coefficient.
Background
In the production of the slab caster, the cooling water flow of the copper plate of the crystallizer needs to be reasonably adjusted according to the change of the produced steel grade and the pulling speed, and the heat convection coefficient of the copper plate in a water gap of the copper plate is changed, so that the aim of adjusting the cooling strength of the crystallizer is fulfilled. The rationality and scientificity of the convective heat transfer coefficient of cooling water in the water gap of the copper plate of the crystallizer are the key points for ensuring good surface quality of the casting blank.
Generally, when the flow rate variation rule of the cooling water of the copper plate of the crystallizer is determined, the temperature of the cooling water is regarded as a constant value (generally 35 ℃), and the influence caused by the variation of the water supply temperature of the cooling water of the copper plate of the crystallizer is not considered; in fact, the water supply temperature of the crystallizer copper plate cooling water can be greatly changed due to the influence of various factors such as weather, environment, different stages of production and the like; in the process, as the physical property of water changes along with the change of temperature, even under the condition of the same cooling water flow, the heat convection coefficient of the cooling water in the water gap of the copper plate of the crystallizer is different due to the difference of water supply temperature, so that the cooling intensity of the crystallizer deviates from a preset value; particularly, when steel grade sensitive to hot cracks is produced, if the water supply temperature of the cooling water of the copper plate of the crystallizer is changed greatly, the probability of cracks on the surface of a casting blank is obviously increased, and more hidden troubles are buried in the subsequent process.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to provide a system for stabilizing crystallizer copper cooling water convection heat transfer coefficient has avoided the change of crystallizer copper cooling water supply temperature and has leaded to the phenomenon emergence of the skew predetermined value of cooling strength of crystallizer, has reduced the probability that the sensitive steel grade surface crack of thermal crack produced, has improved the surface quality of casting blank.
Therefore, the utility model provides a technical scheme as follows:
a system for stabilizing the convection heat exchange coefficient of cooling water of a crystallizer copper plate comprises a crystallizer copper plate cooling water quantity calculation module and a TmeanThe system comprises a processing module, a water quantity control module, a water inlet temperature sensor, a water outlet temperature sensor, an electromagnetic flowmeter and a pneumatic regulating valve;
the inlet water temperature sensor and the outlet water temperature sensor are both connected with TmeanProcess module electrical connection, said TmeanThe processing module is used for receiving signals of the water inlet temperature sensor and the water outlet temperature sensor in real time and calculating the average temperature T of the water inlet and the water outlet of the cooling water of the copper plate of the crystallizermeanThe electromagnetic flow meter, the crystallizer copper plate cooling water volume calculation module and the pneumatic regulating valve are all electrically connected with the water volume control module, the water volume control module is used for receiving water volume information sent by the crystallizer copper plate cooling water volume calculation module and water volume information actually measured by the electromagnetic flow meter in real time and sending an adjusting control signal to the pneumatic regulating valve according to the difference between the two, TmeanThe processing module is electrically connected with the crystallizer copper plate cooling water amount calculating module.
Pneumatic governing valve, electromagnetic flowmeter, the temperature sensor of intaking locate in proper order on the pipeline between crystallizer copper cooling water tank's the delivery port and crystallizer copper water inlet, go out on water temperature sensor locates the pipeline between crystallizer copper delivery port and the water inlet of crystallizer copper cooling water tank.
The crystallizer copper plate cooling water amount calculation module is used for acquiring T in real timemeanAccording to the cross section area A of a single water seam of the copper plate of the crystallizerwsThe perimeter P of the cross section of a single water seam of the copper plate of the crystallizerwsThe number n of the water gaps of the crystallizer copper plate and the target value h of the convective heat transfer coefficient of the cooling water of the crystallizer copper plateaimAnd calculating the water quantity of the cooling water which is required to be supplied to the copper plate of the crystallizer currently, and sending the water quantity information to a water quantity control module.
And a pump is arranged between the pneumatic regulating valve and the crystallizer copper plate cooling water tank.
And a water outlet temperature sensor and a crystallizer copper plate cooling water radiator are sequentially arranged on a pipeline between the water outlet of the crystallizer copper plate and the water inlet of the crystallizer copper plate cooling water tank.
The utility model has the advantages that:
the utility model dynamically adjusts the water quantity of the crystallizer copper plate cooling water to balance and eliminate the influence caused by the change of the cooling water temperature in real time, thereby avoiding the phenomenon that the cooling intensity of the crystallizer deviates from a preset value due to the change of the water supply temperature of the crystallizer copper plate cooling water; the probability of surface cracks of the steel grade sensitive to the hot cracks is reduced, and the surface quality of the casting blank is further improved.
In order to make the above and other objects of the present invention more comprehensible, preferred embodiments accompanied with figures are described in detail below.
Drawings
FIG. 1 is a schematic diagram of the system of the present invention;
FIG. 2 is a graph of thermal conductivity of water versus temperature;
FIG. 3 is a graph of water density versus temperature;
FIG. 4 is a relationship of specific heat of water to temperature;
FIG. 5 is the kinematic viscosity of water versus temperature;
FIG. 6 is a plot of the prandtl number of water versus temperature;
FIG. 7 shows the convection heat transfer coefficient and T of the cooling water of the copper plate of the crystallizermeanThe relationship of (1);
FIG. 8 is a schematic cross-sectional view of the relationship between the inner and outer copper plates of the mold and the cast slab.
Description of reference numerals:
1. a cooling water tank of the crystallizer copper plate; 2. a pump; 3. a pneumatic regulating valve; 4. an electromagnetic flow meter; 5. a water quantity control module; 6. a water quantity calculating module for crystallizer copper plate cooling water; 7. t ismeanA processing module; 8. an inlet water temperature sensor; 9. an effluent temperature sensor; 10. a crystallizer copper plate; 11. a crystallizer copper plate cooling water radiator; 12. casting blanks; 13. an outer arc copper plate of the crystallizer; 14. an inner arc copper plate of the crystallizer; 15. and (5) water gaps of a crystallizer copper plate.
Detailed Description
The following description is provided for illustrative embodiments of the present invention, and other advantages and effects of the present invention will be readily apparent to those skilled in the art from the disclosure herein.
The exemplary embodiments of the present invention will now be described with reference to the accompanying drawings, which, however, may be embodied in many different forms and are not limited to the embodiments described herein, which are provided for complete and complete disclosure of the present invention and to fully convey the scope of the invention to those skilled in the art. The terminology used in the exemplary embodiments presented in the accompanying drawings is not intended to be limiting of the invention. In the drawings, the same units/elements are denoted by the same reference numerals.
Unless otherwise defined, terms (including technical and scientific terms) used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this invention belongs. Further, it will be understood that terms, such as those defined in commonly used dictionaries, should be interpreted as having a meaning that is consistent with their meaning in the context of the relevant art and will not be interpreted in an idealized or overly formal sense.
Example 1:
the embodiment provides a system for stabilizing convection heat exchange coefficient of cooling water of a crystallizer copper plate, which comprises a pneumatic regulating valve 3, an electromagnetic flowmeter 4, a water quantity control module 5, a water quantity calculation module 6 of the cooling water of the crystallizer copper plate, and a TmeanThe system comprises a processing module 7, a water inlet temperature sensor 8 and a water outlet temperature sensor 9;
the inlet water temperature sensor 8 and the outlet water temperature sensor 9 are both connected with TmeanThe processing module 7 is electrically connected, TmeanThe processing module 7 is used for receiving signals of the inlet water temperature sensor 8 and the outlet water temperature sensor 9 in real time and calculating the average temperature T of inlet water and outlet water of cooling water of the copper plate of the crystallizermeanElectromagnetic flowmeter 4, crystallizer copper plate cooling water volume calculation module 6 and pneumatic control valve 3 all are connected with water volume control module 5 electricity, water volume control module 5 is used for receiving water volume information and the water volume information of 4 actual measurements of electromagnetic flowmeter that crystallizer copper plate cooling water volume calculation module 6 sent in real time to send the regulation control signal to pneumatic control valve 3 according to the difference between the two, TmeanProcessing module 7 and junctionAnd the crystal device copper plate cooling water amount calculation module 6 is electrically connected.
Example 2:
on the basis of embodiment 1, this embodiment provides a system for stabilizing crystallizer copper plate cooling water convection heat transfer coefficient, pneumatic control valve 3, electromagnetic flowmeter 4, temperature sensor 8 of intaking locate in proper order on the pipeline between the delivery port of crystallizer copper plate cooling water tank 1 and the crystallizer copper plate water inlet, go out on temperature sensor 9 locates the pipeline between the water outlet of crystallizer copper plate 10 and the water inlet of crystallizer copper plate cooling water tank 1.
As shown in fig. 1, a pump 2 is arranged between the pneumatic control valve 3 and the crystallizer copper plate cooling water tank 1.
And a water outlet temperature sensor 9 and a crystallizer copper plate cooling water radiator 11 are sequentially arranged on a pipeline between the water outlet of the crystallizer copper plate 10 and the water inlet of the crystallizer copper plate cooling water tank 1.
Wherein, the crystallizer copper plate cooling water quantity calculation module 6 is used for acquiring T in real timemeanAccording to the cross section area A of a single water seam of the copper plate of the crystallizerwsThe perimeter P of the cross section of a single water seam of the copper plate of the crystallizerwsThe number n of the water gaps 15 of the crystallizer copper plate and the target value h of the convective heat transfer coefficient of the cooling water of the crystallizer copper plateaimThe amount of cooling water to be supplied to the copper plate of the mold at present is calculated, and the information of the amount of cooling water is sent to the water amount control module 5.
Example 3:
the embodiment provides a method for stabilizing the convection heat exchange coefficient of cooling water of a copper plate of a crystallizer, and a system for stabilizing the convection heat exchange coefficient of the cooling water of the copper plate of the crystallizer, which is provided by the embodiment 1, comprises the following steps:
step 1) TmeanThe processing module 7 respectively obtains the water inlet temperature T of the current cooling water for the crystal copper plate through the water inlet temperature sensor 8 and the water outlet temperature sensor 9inAnd the temperature T of the outlet wateroutAnd calculating the average temperature T of the cooling water inlet and outlet of the copper plate of the crystallizermean
Step 2) a module for calculating the cooling water quantity of the copper plate of the crystallizer passes through TmeanProcessing module 7 obtains T in real timemeanAccording to the cross section area A of a single water seam of the copper plate of the crystallizerwsThe perimeter P of the cross section of a single water seam of the copper plate of the crystallizerwsThe number n of the water gaps 15 of the crystallizer copper plate and the target value h of the convective heat transfer coefficient of the cooling water of the crystallizer copper plateaimCalculating the water quantity Q of cooling water which is required to be supplied to the copper plate of the crystallizer currently, and sending the water quantity information to a water quantity control module 5;
step 3) the water quantity control module 5 receives the water quantity information Q sent by the crystallizer copper plate cooling water quantity calculation module 6 and the water quantity information actually measured by the electromagnetic flow meter 4 in real time, sends an adjusting control signal to the pneumatic adjusting valve 3 according to the difference between the water quantity information Q and the water quantity information, and controls the convective heat exchange coefficient of the crystallizer copper plate cooling water to be stable to a target value h by adjusting the cooling water quantity supplied to the crystallizer copper plateaim
The utility model dynamically adjusts the water quantity of the crystallizer copper plate cooling water to balance and eliminate the influence caused by the change of the cooling water temperature in real time, thereby avoiding the phenomenon that the cooling intensity of the crystallizer deviates from a preset value due to the change of the water supply temperature of the crystallizer copper plate cooling water; the probability of surface cracks of the steel grade sensitive to the hot cracks is reduced, and the surface quality of the casting blank is further improved.
Example 4:
on the basis of embodiment 3, this embodiment provides a method for stabilizing the convective heat transfer coefficient of the cooling water of the copper plate of the crystallizer, and the procedure of calculating the cooling water amount Q that should be currently supplied to the copper plate 10 of the crystallizer by the cooling water amount calculation module 6 in step 2) is as follows:
step (1) obtaining the average temperature T of inlet water and outlet water of cooling water of a crystallizer copper plate in real timemean
Step (2) according to the number n of the water gaps 15 of the crystallizer copper plate and the cross section area A of a single water gap of the crystallizer copper platewsThe perimeter P of the cross section of a single water seam of the copper plate of the crystallizerwsCalculating the hydraulic diameter D of the water gap of the copper plate of the single crystallizerh
Setting three variables Qup、QdownAnd QcurLet Qup=Qmax、Qdown=0、Qcur=0.5(Qup+Qdown) (ii) a Wherein Q ismaxSetting the maximum water quantity m for the cooling water of the copper plate of the crystallizer3/s;
Step (4) according to the average temperature T of the cooling water inlet and outlet of the crystallizer copper platemeanBy QcurCalculating the flow velocity V of cooling water in a water gap of the copper plate of the crystallizer and the corresponding Reynolds number Re of the cooling water of the copper plate of the crystallizerD(TmeanV) Nu corresponding to cooling water of copper plate of crystallizerD(TmeanV) and the convection heat transfer coefficient h of cooling water of the copper plate of the crystallizercur(Tmean,V);
Step (5) carrying out convection heat exchange coefficient h on cooling water of the copper plate of the crystallizercur(TmeanV) coefficient of heat transfer by convection with cooling water of copper plate of crystallizeraimMaking a comparison if hcur(Tmean,V)<haimThen, set Qdown=Qcur,Qcur=0.5(Qup+Qdown) If h iscur(Tmean,V)>haimThen, set Qup=Qcur,Qcur=0.5(Qup+Qdown) Repeating the step (4) until haim-Δhdown≤h(Tmean,V)≤haim+ΔhupOr (Q)up-Qdown) < Δ Q, then let Q ═ Qcur
Wherein,. DELTA.hdownThe deviation of the convection heat transfer coefficient target of the cooling water of the copper plate of the crystallizer is W.m-2·K-1;ΔhupThe target deviation of the convection heat transfer coefficient of the cooling water of the copper plate of the crystallizer is W.m-2·K-1
Step (6) obtaining the average temperature T of the inlet water and the outlet water of the cooling water of the copper plate of the current crystallizermeanIf T this timemeanRelative to last time TmeanThe change exceeds the allowable deviation delta T of the average temperature of the cooling water inlet and outlet of the copper plate of the crystallizermeanAnd (4) repeating the step (3), the step (4) and the step (5), otherwise, not adjusting the water quantity.
Example 5:
on the basis of embodiment 4, this embodiment provides a method for stabilizing the convective heat transfer coefficient of the cooling water of the copper plate of the crystallizer, and the hydraulic diameter D of the water gap of the copper platehThe calculation formula is as follows:
Figure BDA0002226088920000061
the calculation formula of the flow velocity V of the cooling water in the water gap of the copper plate of the crystallizer is as follows:
Figure BDA0002226088920000062
reynolds number Re corresponding to cooling water of crystallizer copper plateD(TmeanV) the calculation formula is as follows:
Figure BDA0002226088920000063
in the formula, v (T)mean) M is a function of the kinematic viscosity of water with respect to temperature2·s-1(ii) a As shown in fig. 5;
nu of Nu corresponding to cooling water of crystallizer copper plateD(TmeanV) the calculation formula is as follows:
Figure BDA0002226088920000064
in the formula, f is a friction factor of a crystallizer copper plate water seam and is dimensionless; pr (Pr) ofD(Tmean) Is a function of the prandtl number of water with respect to temperature, dimensionless.
The calculation formula of the friction factor f of the crystallizer copper plate water seam is as follows:
f(Tmean,V)=(0.790lnReD(Tmean,V)-1.64)-2
function Pr of the Plantt number of water with respect to the temperatureD(Tmean) The following formula:
Figure BDA0002226088920000071
in the formula, ρ (T)mean) Kg/m as a function of the density of the water with respect to the temperature-3;cp(Tmean) J.kg as a function of the specific heat capacity of water with respect to temperature-1·K-1;v(Tmean) As a function m of the kinematic viscosity of water with respect to temperature2And s. As shown in fig. 3, 4 and 5, respectively. The prandtl number of water as a function of temperature is shown in fig. 6.
Example 6:
on the basis of embodiment 4, this embodiment provides a method for stabilizing the convective heat transfer coefficient of the cooling water of the copper plate of the crystallizer, i.e., the convective heat transfer coefficient h of the cooling water of the copper plate of the crystallizercur(TmeanV) the calculation formula is as follows:
Figure BDA0002226088920000072
in the formula, k (T)mean) W.m as a function of the thermal conductivity of water with respect to temperature-1·K-1. As shown in fig. 2.
Example 7:
this embodiment is according to on-spot concrete operating mode, adopts the utility model discloses the method is stabilized at the target value h with crystallizer copper cooling water convection heat transfer coefficientaim
As shown in FIG. 7, h in this embodimentaim(15000W·m-2·K-1) The horizontal lines show that the convective heat transfer coefficients corresponding to different crystallizer copper plate cooling water flow rates (2500L/min, 2750L/min and 3000L/min respectively) at different temperatures are a series of curves, and the convective heat transfer coefficients corresponding to the various crystallizer copper plate cooling water flow rates are increased along with the increase of the temperatures.
As shown in FIG. 7, the average temperature T of the inlet water and the outlet water of the cooling water of the copper plate of the crystallizer at present is assumedmeanAt the temperature of 41.5 ℃, when the cooling water flow of the crystallizer copper plate is 2750L/min, the corresponding convective heat transfer coefficient is a target value, namely haim=15000W·m-2·K-1(ii) a If the average temperature T of the cooling water inlet and outlet of the crystallizer copper platemeanWhen the temperature is reduced to 33.5 ℃, if the cooling water flow rate is maintained at 2750L/min, the corresponding convective heat transfer coefficient is lower than the target value haimAt this time, the flow rate of the cooling water can be increased to 3000L/min, so that the corresponding convective heat transfer coefficient is stabilized at the target value haim(ii) a If the average temperature T of the cooling water inlet and outlet of the crystallizer copper platemeanWhen the temperature is raised to 52.5 ℃, if the cooling water flow rate is maintained at 2750L/min, the corresponding convective heat transfer coefficient is higher than the target value haimAt this time, the flow rate of the cooling water is reduced to 2500L/min, so that the corresponding convective heat transfer coefficient is stabilized at the target value haim
The utility model aims at the problem that the water supply temperature of the cooling water of the crystallizer copper plate of the slab caster is greatly changed under the influence of various factors such as weather, environment, different stages of production and the like, because the physical properties (heat conductivity coefficient, dynamic viscosity, specific heat, density and the like) of the water are different at different temperatures, even under the condition of the same cooling water flow, the heat convection coefficient of the cooling water in the water gap of the crystallizer copper plate is different due to different water supply temperatures, thereby leading the cooling intensity of the crystallizer to deviate from a preset value; particularly, when steel grade sensitive to hot cracks is produced, the probability of cracks appearing on the surface of a casting blank is obviously increased, and more hidden troubles are buried in the subsequent process.
As shown in fig. 8, the mold copper plate 10 provides support for the casting slab and cools the casting slab, and includes a mold outer arc copper plate 13 and a mold inner arc copper plate 14, and a plurality of mold copper plate water gaps 15 are formed on each of the mold outer arc copper plate 13 and the mold inner arc copper plate 14.
It will be understood by those skilled in the art that the foregoing embodiments are specific examples of the invention, and that various changes in form and details may be made therein without departing from the spirit and scope of the invention in its practical application. The components and structures of the present embodiments that are not described in detail are well known in the art and do not constitute essential structural elements or elements.

Claims (5)

1. Stabilizing knotThe system for the convection heat transfer coefficient of the cooling water of the crystallizer copper plate is characterized in that: comprises a pneumatic regulating valve (3), an electromagnetic flowmeter (4), a water quantity control module (5), a crystallizer copper plate cooling water quantity calculation module (6) and a TmeanThe device comprises a processing module (7), an inlet water temperature sensor (8) and an outlet water temperature sensor (9);
the inlet water temperature sensor (8) and the outlet water temperature sensor (9) are both connected with TmeanThe processing module (7) is electrically connected, TmeanThe processing module (7) is used for receiving signals of the inlet water temperature sensor (8) and the outlet water temperature sensor (9) in real time and calculating the average temperature T of inlet water and outlet water of cooling water of the copper plate of the crystallizermeanElectromagnetic flowmeter (4), crystallizer copper plate cooling water volume calculation module (6) and pneumatic control valve (3) all are connected with water volume control module (5) electricity, water volume control module (5) are used for receiving water volume information and electromagnetic flowmeter (4) actual measurement's water volume information that crystallizer copper plate cooling water volume calculation module (6) sent in real time to send regulation control signal to pneumatic control valve (3) according to the difference between the two, TmeanThe processing module (7) is electrically connected with the crystallizer copper plate cooling water amount calculating module (6).
2. The system for stabilizing the convection heat exchange coefficient of the cooling water of the copper plate of the crystallizer as claimed in claim 1, wherein: pneumatic governing valve (3), electromagnetic flow meter (4), temperature sensor (8) of intaking locate in proper order on the pipeline between the delivery port of crystallizer copper cooling water tank (1) and crystallizer copper water inlet, go out on water temperature sensor (9) locate the pipeline between the water inlet of crystallizer copper (10) delivery port and crystallizer copper cooling water tank (1).
3. The system for stabilizing the convection heat exchange coefficient of the cooling water of the copper plate of the crystallizer as claimed in claim 1, wherein: the crystallizer copper plate cooling water amount calculation module (6) is used for acquiring T in real timemeanAccording to the cross section area A of a single water seam of the copper plate of the crystallizerwsThe perimeter P of the cross section of a single water seam of the copper plate of the crystallizerwsThe number of the crystallizer copper plate water gaps (15)n, target value h of convection heat exchange coefficient of cooling water of copper plate of crystallizeraimThe amount Q of the cooling water to be supplied to the mold copper plate (10) at present is calculated, and the information of the amount of the cooling water is sent to a water amount control module (5).
4. The system for stabilizing the convection heat exchange coefficient of the cooling water of the copper plate of the crystallizer as claimed in claim 2, wherein: and a pump (2) is arranged between the pneumatic regulating valve (3) and the crystallizer copper plate cooling water tank (1).
5. The system for stabilizing the convection heat exchange coefficient of the cooling water of the copper plate of the crystallizer as claimed in claim 2, wherein: and an outlet water temperature sensor (9) and a crystallizer copper plate cooling water radiator (11) are sequentially arranged on a pipeline between a water outlet of the crystallizer copper plate (10) and a water inlet of the crystallizer copper plate cooling water tank (1).
CN201921684609.XU 2019-10-09 2019-10-09 System for stabilizing convection heat exchange coefficient of crystallizer copper plate cooling water Active CN211101488U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201921684609.XU CN211101488U (en) 2019-10-09 2019-10-09 System for stabilizing convection heat exchange coefficient of crystallizer copper plate cooling water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201921684609.XU CN211101488U (en) 2019-10-09 2019-10-09 System for stabilizing convection heat exchange coefficient of crystallizer copper plate cooling water

Publications (1)

Publication Number Publication Date
CN211101488U true CN211101488U (en) 2020-07-28

Family

ID=71723971

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201921684609.XU Active CN211101488U (en) 2019-10-09 2019-10-09 System for stabilizing convection heat exchange coefficient of crystallizer copper plate cooling water

Country Status (1)

Country Link
CN (1) CN211101488U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110666126A (en) * 2019-10-09 2020-01-10 中国重型机械研究院股份公司 System and method for stabilizing convection heat exchange coefficient of crystallizer copper plate cooling water
CN115383072A (en) * 2022-08-25 2022-11-25 太原晋西春雷铜业有限公司 Control method of cooling water in crystallizer

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110666126A (en) * 2019-10-09 2020-01-10 中国重型机械研究院股份公司 System and method for stabilizing convection heat exchange coefficient of crystallizer copper plate cooling water
CN110666126B (en) * 2019-10-09 2024-02-06 中国重型机械研究院股份公司 Method for stabilizing convection heat exchange coefficient of crystallizer copper plate cooling water
CN115383072A (en) * 2022-08-25 2022-11-25 太原晋西春雷铜业有限公司 Control method of cooling water in crystallizer

Similar Documents

Publication Publication Date Title
CN110666126B (en) Method for stabilizing convection heat exchange coefficient of crystallizer copper plate cooling water
CN211101488U (en) System for stabilizing convection heat exchange coefficient of crystallizer copper plate cooling water
CN108788032B (en) Crystallizer with adjustable cooling strength for continuous casting of magnesium alloy and method for controlling cooling
CN104162638B (en) A kind of crystallizer cooling water control device and method
CN103071774B (en) Method for controlling surface temperature of casting blank at straightening point of continuous casting machine
US8418748B2 (en) Casting composite ingot with metal temperature compensation
CN104959606A (en) Partial temperature control system for metal material 3D printing
CN113070461B (en) Active die-casting mold temperature control equipment and method
CN106825479B (en) A kind of determination method of hot delivering technology of CC billets process quenching technology for surfaces cooling water flow
CN106125790A (en) Die face and the drop stamping temperature control system of plate Multi-Point Closed-Loop observing and controlling
CN115509266A (en) Control device and control method for adjusting melt flow through rapid reaction and application of control device and control method
CN101396725B (en) Pouring method and device capable of stabilizing the crystallizer molten steel surface temperature
CN108755840A (en) A kind of equal balance system of industrial flow and its matching process
CN204122708U (en) A kind of crystallizer cooling water control device
JP2010508151A (en) Method and control device for controlling the amount of heat removed from the side plate of the mold
CN105215312B (en) A kind of double-roll thin-belt continuous casting roller cooling water flow control method
CN106282533B (en) A kind of temprature control method to be rolled of heating furnace
CN102228970A (en) System for simulating molten steel solidification heat-transfer process inside continuous casting crystallizer
JPH06504954A (en) Adjustment of flow rate of molten product
KR20110073788A (en) Monitoring method and device for continuous casting
CN109960835A (en) The method for establishing continuous cast mold heat flux distribution model
CN110802208B (en) Method for adjusting water yield of continuous casting production in high-latitude area
CN102228971B (en) Method for online simulation of molten steel solidification heat-transfer process inside continuous casting crystallizer
CN113128030A (en) Crystallizer slag rolling fault determination method and device
CN102218515B (en) Method for calculating molten steel solidification and heat transfer process in continuous casting crystallizer

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant