CN115111931A - A kind of absorber and endothermic control method for alumina waste heat - Google Patents
A kind of absorber and endothermic control method for alumina waste heat Download PDFInfo
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- CN115111931A CN115111931A CN202210544873.3A CN202210544873A CN115111931A CN 115111931 A CN115111931 A CN 115111931A CN 202210544873 A CN202210544873 A CN 202210544873A CN 115111931 A CN115111931 A CN 115111931A
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- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 title claims abstract description 44
- 239000006096 absorbing agent Substances 0.000 title claims abstract description 20
- 238000000034 method Methods 0.000 title claims abstract description 18
- 239000002918 waste heat Substances 0.000 title claims abstract description 11
- 238000005338 heat storage Methods 0.000 claims abstract description 75
- 238000010521 absorption reaction Methods 0.000 claims abstract description 17
- 239000011232 storage material Substances 0.000 claims abstract description 13
- 239000004020 conductor Substances 0.000 claims abstract description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 18
- 238000001514 detection method Methods 0.000 claims description 15
- 238000009413 insulation Methods 0.000 claims description 3
- 238000004519 manufacturing process Methods 0.000 abstract description 4
- 239000002699 waste material Substances 0.000 abstract description 3
- 238000004146 energy storage Methods 0.000 description 6
- 230000007704 transition Effects 0.000 description 4
- 238000001816 cooling Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 238000003723 Smelting Methods 0.000 description 1
- 238000009529 body temperature measurement Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
- F27D17/00—Arrangements for using waste heat; Arrangements for using, or disposing of, waste gases
- F27D17/10—Arrangements for using waste heat
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
- F27D17/00—Arrangements for using waste heat; Arrangements for using, or disposing of, waste gases
- F27D17/10—Arrangements for using waste heat
- F27D17/12—Arrangements for using waste heat using heat storage
- F27D17/13—Arrangements for using waste heat using heat storage using regenerative heat exchangers
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D20/00—Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00
- F28D20/02—Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00 using latent heat
- F28D20/028—Control arrangements therefor
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- Control Of Temperature (AREA)
Abstract
Description
技术领域technical field
本发明涉及吸收器,具体涉及一种用于氧化铝余热的吸收器,本发明还涉及该吸收器的吸放热控制方法。The present invention relates to an absorber, in particular to an absorber for alumina waste heat, and also to a method for controlling the heat absorption and release of the absorber.
背景技术Background technique
在氧化铝冶炼过程中,氧化铝锭出炉后需要冷却才能进行下一步工作。出炉后的氧化铝锭自然冷却散热慢,冷却过程极大地影响企业生产效率,氧化铝锭冷却同时造成能量极大程度的浪费,并且高温氧化铝锭对操作员工的生产安全也造成严重影响。In the alumina smelting process, the alumina ingot needs to be cooled before proceeding to the next step. The natural cooling of alumina ingots after being released from the furnace is slow to dissipate heat. The cooling process greatly affects the production efficiency of the enterprise. The cooling of alumina ingots also causes a great waste of energy, and the high-temperature alumina ingots also have a serious impact on the production safety of operators.
发明内容SUMMARY OF THE INVENTION
针对现有氧化铝锭出炉后热量损失的情况,本发明所要解决的技术问题是提供一种能够吸收出炉后氧化铝锭所释放热的吸收器。Aiming at the situation of heat loss after the existing alumina ingots are released, the technical problem to be solved by the present invention is to provide an absorber capable of absorbing the heat released by the alumina ingots after being released.
为解决上述技术问题,本发明所采取的技术方案是:一种用于氧化铝余热的吸收器,包括固定架,在所述固定架上设阶梯型储热主体,阶梯型储热主体的一端连设由多根伸入到阶梯型储热主体内由管状导热体组成的接触性集热端,接触性集热端另一端与目标热源接触;在阶梯型储热主体的另一端通过管道连设调频引风机;阶梯型储热主体内沿接触性集热端到调频引风机方向设多根内部填充有储热材料的储热管,储热材料由五段相变温度不同的储热材料组成,储热材料相变温度按从高到低的顺序由接触性集热端向调频引风机端依次在储热管内填充;在接触性集热端上连设第一温度探测器,在从接触性集热端向调频引风机端上的阶梯型储热主体上依次设与五段相变温度不同的储热材料相连的第二温度探测器、第三温度探测器、第四温度探测器、第五温度探测器、第六温度探测器,在阶梯型储热主体与调频引风机间的管道上设第七温度探测器;固定架上的电控装置与每个温度探测器、调频引风机控制连接。In order to solve the above-mentioned technical problems, the technical solution adopted in the present invention is: an absorber for alumina waste heat, comprising a fixing frame, a stepped heat storage body is arranged on the fixing frame, and one end of the stepped heat storage body is arranged on the fixing frame. A plurality of contact heat collecting ends consisting of tubular heat conductors extending into the stepped heat storage body are connected, and the other end of the contact heat collecting end is in contact with the target heat source; the other end of the stepped heat storage body is connected by pipes. A frequency-modulated induced draft fan is installed; a plurality of heat storage pipes filled with heat-storage materials are arranged in the stepped heat storage body along the direction from the contact heat collecting end to the frequency-modulated induced draft fan. , the phase transition temperature of the heat storage material is filled in the heat storage pipe from the contact heat collecting end to the frequency modulation induced draft fan end in the order from high to low; a first temperature detector is connected on the contact heat collecting end, and the first temperature detector is connected to the contact heat collecting end. A second temperature detector, a third temperature detector, a fourth temperature detector, a second temperature detector, a third temperature detector, a fourth temperature detector, The fifth temperature detector and the sixth temperature detector, the seventh temperature detector is arranged on the pipeline between the stepped heat storage main body and the frequency modulation induced draft fan; the electronic control device on the fixed frame is connected with each temperature detector and the frequency modulation induced draft fan. Control connection.
所述阶梯型储热主体为一罐体,多根储热管在罐体内沿接触性集热端到调频引风机方向设置,在罐体的外层设置有保温层。The stepped heat storage body is a tank body, a plurality of heat storage pipes are arranged in the tank body along the direction from the contact heat collecting end to the frequency modulation induced draft fan, and an insulating layer is arranged on the outer layer of the tank body.
在所述阶梯型储热主体与接触性集热端的连接端、阶梯型储热主体与调频引风机之间的管道上分别设防火阀,电控装置与控制阀控制连接。Fire dampers are respectively provided on the connecting end of the stepped heat storage body and the contact heat collecting end, and on the pipeline between the stepped heat storage body and the frequency modulation induced draft fan, and the electric control device is controlled and connected to the control valve.
本发明吸收器的吸放热控制方法是:The heat absorption and heat release control method of the absorber of the present invention is:
A.吸热流程A. Endothermic process
步骤1.将一体化装置安装到位后使接触性集热端与氧化铝接触,打开阶梯型储热主体两端的防火阀,同时开启调频引风机,调频引风机以最低频率运行;Step 1. After the integrated device is installed in place, the contact heat collecting end is in contact with the alumina, the fire dampers at both ends of the stepped heat storage body are opened, and the frequency modulation induced draft fan is turned on at the same time, and the frequency modulation induced draft fan runs at the lowest frequency;
步骤2.当第一温度探测器的数值在600℃以上时,调频引风机的风机频率依照每分钟5HZ的频率进行增加,直至第七温度探测器的温度为80—100℃为止;
步骤3.当第一温度探测器的数值达到500—600℃时,考察第二温度探测器的温度是否达到500℃以上,当该温度达到500℃以上时,再探第三测温度探测器、第四测温度探测器、第五测温度探测器、第六测温度探测器是否达到相应的400℃、300℃、200℃、100℃以上,如达到后则判定该次储热完成;如其中有未达到的情况,则利用30%频率运行调频引风机至所有工段满足要求;
步骤4.当第一温度探测器的数值达到400—500℃时,考察第三温度探测器的温度是否达到400℃以上,当该温度达到400℃以上时,再探测第四温度探测器、第五温度探测器、第六温度探测器是否达到相应的300℃、200℃、100℃以上,如达到后则判定该次储热完成一半;如其中有未达到的情况,则利用30%频率运行调频引风机至第四温度探测器、第五温度探测器、第六温度探测器探测工段满足要求;当第三温度探测器、第四温度探测器、第五温度探测器、第六温度探测器探测工段全都达到要求后,考察第二温度探测器的温度是否达到500℃以上,如未达到,提示换新氧化铝块进行吸收,直至储能达标;
步骤5.当第一温度探测器的数值达到300—400℃时,考察第四温度探测器的温度是否达到300℃以上,当该温度达到300℃以上时,再探测第五温度探测器、第六温度探测器是否达到相应的200℃、100℃以上,如达到后则判定该次储热完成一半;如其中有未达到的情况,则利用30%频率运行调频引风机至第五温度探测器、第六温度探测器探测工段满足要求;当第四温度探测器、第五温度探测器、第六温度探测器探测工段全都达到要求后,考察第二温度探测器、第三温度探测器的温度是否达到500℃、400℃以上,如未达到,提示换新氧化铝块进行吸收,直至储能达标;
步骤6.当第一温度探测器的数值达到200—300℃时,考察第五温度探测器的温度是否达到200℃以上,当该温度达到200℃以上时,再探测第六温度探测器是否达到相应的100℃以上,如达到后则判定该次储热完成一半;如其中有未达到的情况,则利用30%频率运行调频引风机至第六温度探测器探测工段满足要求;当第五温度探测器、第六温度探测器探测工段全都达到要求后,考察第二温度探测器、第三温度探测器、第四温度探测器的温度是否达到500℃、400℃、300℃以上,如未达到,提示换新氧化铝块进行吸收,直至储能达标;Step 6. When the value of the first temperature detector reaches 200-300 ℃, check whether the temperature of the fifth temperature detector reaches 200 ℃ or more, when the temperature reaches 200 ℃ or more, then check whether the sixth temperature detector reaches 200 ℃. The corresponding 100°C or higher, if it is reached, it will be judged that half of the heat storage is completed; if there is a situation that is not reached, use 30% frequency to run the frequency-modulated induced draft fan to the sixth temperature detector detection section to meet the requirements; when the fifth temperature After the detection section of the detector and the sixth temperature detector all meet the requirements, check whether the temperature of the second temperature detector, the third temperature detector and the fourth temperature detector has reached 500°C, 400°C and 300°C. , prompting to replace the new alumina block for absorption until the energy storage reaches the standard;
步骤7.当第一温度探测器的数值达到100—200℃时,提示请更换氧化铝块;
B.放热流程B. Exothermic Process
步骤1. 阶梯型储热主体应垂直安装并倒置,调频引风机出口与热交换器连接,控制接触性集热端的防火阀阀门开启30%;开启调频引风机引导热风进入热交换器与热交换器内的水进行热交换;Step 1. The stepped heat storage body should be installed vertically and upside down, the outlet of the FM induced draft fan should be connected to the heat exchanger, and the fire damper valve at the contact heat collecting end should be controlled to open 30%; The water in the container exchanges heat;
步骤2.检测热交换器内的水是否达到所需水温度或蒸汽温度,当达到时保持阀门开启度;当超过时将调频引风机的频率调小以达到所需水温度或蒸汽温度;当不到时将调频引风机的频率调大以达到所需水温度或蒸汽温度。
本发明采用上述技术方案所设计的一种用于氧化铝余热的吸收器与吸放热控制方法,能够吸收出炉后的氧化铝锭所释放的热,并将吸收的热用作他用,使氧化铝锭释放的热得到利用,减少了能量的浪费,节约了能源。通过对出炉后氧化铝锭所释放热的吸收,避免了高温氧化铝锭对操作员工的生产安全所造成的严重影响,确保操作员工能够安全生产,减少事故的发生。本发明结构简单,吸热、放热方法简单,实现了出炉后氧化铝锭释放热的较好利用。The present invention adopts an absorber and an endothermic control method for alumina waste heat designed by the above technical scheme, which can absorb the heat released by the alumina ingot after being released from the furnace, and use the absorbed heat for other purposes, so that the The heat released by the alumina ingot is utilized, which reduces the waste of energy and saves energy. By absorbing the heat released by the alumina ingots after being released, the serious impact of the high-temperature alumina ingots on the production safety of the operators is avoided, and the operators can produce safely and reduce the occurrence of accidents. The invention has simple structure, simple heat absorption and heat release methods, and realizes better utilization of the heat released by the alumina ingot after being released from the furnace.
附图说明Description of drawings
图1表示本发明吸收器的结构示意图;Fig. 1 shows the structure schematic diagram of the absorber of the present invention;
图2表示本发明阶梯型储热主体的内部结构示意图;FIG. 2 is a schematic diagram showing the internal structure of the stepped heat storage body of the present invention;
图3表示本发明阶梯型储热主体上所设的温度探测器分布图。FIG. 3 shows the distribution diagram of the temperature detectors provided on the stepped heat storage main body of the present invention.
具体实施方式Detailed ways
下面结合附图对本发明一种用于氧化铝余热的吸收器与吸放热控制方法作具体说明。Below in conjunction with the accompanying drawings, an absorber for alumina waste heat and a method for controlling endothermic and exothermic heat of the present invention will be described in detail.
本发明一种用于氧化铝余热的吸收器,参见图1至图3,包括固定架,在固定架上设阶梯型储热主体3,阶梯型储热主体3的一端连设接触性集热端1,接触性集热端1是由多根伸入到阶梯型储热主体3内的管状导热体组成,接触性集热端1的另一端与目标热源(出炉后的高温氧化铝锭)接触。在阶梯型储热主体3的另一端通过管道连设调频引风机5。在阶梯型储热主体3与接触性集热端1的连接端设防火阀2,在阶梯型储热主体3与调频引风机5之间的管道上也设防火阀4,防火阀2和防火阀4均由设置在固定架上的电控装置控制。An absorber for alumina waste heat according to the present invention, referring to Fig. 1 to Fig. 3, includes a fixing frame on which a stepped
本发明阶梯型储热主体3为一罐体,在罐体内设多根储热管7,储热管7沿接触性集热端1到调频引风机5的方向设置,在储热管7内填充有储热材料,储热材料由五段相变温度不同的储热材料组成,储热材料相变温度按从高到低的顺序由接触性集热端1向调频引风机5端依次在储热管7内填充。氧化铝锭降温时保守估计其温度在800℃以上,所以阶梯型储热主体3的阶梯段设计为5段,这样可以更好的交换以及储存热量。在接触性集热端1上连设第一温度探测器8,第一温度探测器8用于探测接触性集热端1内的温度,也即检测氧化铝锭的温度。在从接触性集热端1向调频引风机5端上的储热管7上依次设第二温度探测器9、第三温度探测器10、第四温度探测器11、第五温度探测器12、第六温度探测器13,第二温度探测器9、第三温度探测器10、第四温度探测器11、第五温度探测器12、第六温度探测器13分别探测储热管7内的五段相变温度不同的储热材料所具有的温度。在阶梯型储热主体3与调频引风机5间的管道上设第七温度探测器14,第七温度探测器14用于探测调频引风机5入口端的温度,以确保调频引风机5在其工作温度范围内工作。第一温度探测器8、第二温度探测器9、第三温度探测器10、第四温度探测器11、第五温度探测器12、第六温度探测器13、第七温度探测器14以及调频引风机5由电控装置控制。本发明还在罐体的外层设置有保温层6用于对罐体的保温。The stepped
本发明吸收器的吸热流程是:The heat-absorbing process of the absorber of the present invention is:
步骤1.将一体化装置安装到位后使接触性集热端1与氧化铝锭接触,打开阶梯型储热主体3两端的防火阀2和防火阀4,同时开启调频引风机5,调频引风机5以最低频率运行;Step 1. After the integrated device is installed in place, the contact heat collecting end 1 is in contact with the alumina ingot, the
步骤2.当第一温度探测器8的数值在600℃以上时,调频引风机5的风机频率依照每分钟5HZ的频率进行增加,直至第七温度探测器14的温度为80—100℃为止;
步骤3.当第一温度探测器8的数值达到500—600℃时,考察第二温度探测器9的温度是否达到500℃以上,当该温度达到500℃以上时,再探第三测温度探测器10、第四测温度探测器11、第五测温度探测器12、第六测温度探测器13是否达到相应的400℃、300℃、200℃、100℃以上,如达到后则判定该次储热完成。如其中有未达到的情况,则利用30%频率运行调频引风机5至所有工段满足要求;
步骤4.当第一温度探测器8的数值达到400—500℃时,考察第三温度探测器10的温度是否达到400℃以上,当该温度达到400℃以上时,再探测第四温度探测器11、第五温度探测器12、第六温度探测器13是否达到相应的300℃、200℃、100℃以上,如达到后则判定该次储热完成一半。如其中有未达到的情况,则利用30%频率运行调频引风机5至第四温度探测器11、第五温度探测器12、第六温度探测器13探测工段满足要求;当第三测温度探测器10、第四测温度探测器11、第五测温度探测器12、第六测温度探测器13探测工段全都达到要求后,考察第二温度探测器的温度是否达到500℃以上,如未达到,提示换新氧化铝块进行吸收,直至储能达标;
步骤5.当第一温度探测器8的数值达到300—400℃时,考察第四温度探测器11的温度是否达到300℃以上,当该温度达到300℃以上时,再探测第五温度探测器12、第六温度探测器13是否达到相应的200℃、100℃以上,如达到后则判定该次储热完成一半。如其中有未达到的情况,则利用30%频率运行调频引风机5至第五温度探测器12、第六温度探测器13探测工段满足要求。当第四温度探测器11、第五温度探测器12、第六温度探测器13探测工段全都达到要求后,考察第二温度探测器9、第三温度探测器10的温度是否达到500℃、400℃以上,如未达到,提示换新氧化铝块进行吸收,直至储能达标;
步骤6.当第一温度探测器8的数值达到200—300℃时,考察第五温度探测器12的温度是否达到200℃以上,当该温度达到200℃以上时,再探测第六温度探测器13是否达到相应的100℃以上,如达到后则判定该次储热完成一半。如其中有未达到的情况,则利用30%频率运行调频引风机5至第六温度探测器13探测工段满足要求。当第五温度探测器12、第六温度探测器13探测工段全都达到要求后,考察第二温度探测器9、第三温度探测器10、第四温度探测器11的温度是否达到500℃、400℃、300℃以上,如未达到,提示换新氧化铝块进行吸收,直至储能达标;Step 6. When the value of the first temperature detector 8 reaches 200-300°C, check whether the temperature of the
步骤7.当第一温度探测器8的数值达到100—200℃时,提示请更换氧化铝块。
本发明吸收器的放热流程是:The heat release process of the absorber of the present invention is:
步骤1. 阶梯型储热主体3应垂直安装并倒置,调频引风机出口与热交换器连接,控制防火阀2阀门(高温端阀门)开启30%。开启调频引风机5引导热风通过管道进入热交换器(图中未示)与热交换器内的水进行热交换;Step 1. The stepped
步骤2.检测热交换器内的水是否达到所需水温度或蒸汽温度,当达到时保持阀门开启度。当超过时将调频引风机5的频率调小以达到所需水温度或蒸汽温度。当不到时将调频引风机5的频率调大以达到所需水温度或蒸汽温度。
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