CN103438606B - Adsorption-type waste heat recovery plate type refrigerator - Google Patents
Adsorption-type waste heat recovery plate type refrigerator Download PDFInfo
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- CN103438606B CN103438606B CN201310352459.3A CN201310352459A CN103438606B CN 103438606 B CN103438606 B CN 103438606B CN 201310352459 A CN201310352459 A CN 201310352459A CN 103438606 B CN103438606 B CN 103438606B
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- 239000002918 waste heat Substances 0.000 title claims abstract description 38
- 238000011084 recovery Methods 0.000 title claims abstract description 31
- 238000001704 evaporation Methods 0.000 claims abstract description 72
- 239000003507 refrigerant Substances 0.000 claims abstract description 65
- 238000001179 sorption measurement Methods 0.000 claims abstract description 43
- 230000008020 evaporation Effects 0.000 claims abstract description 42
- 238000005057 refrigeration Methods 0.000 claims abstract description 41
- 238000009833 condensation Methods 0.000 claims abstract description 40
- 230000005494 condensation Effects 0.000 claims abstract description 40
- 238000002336 sorption--desorption measurement Methods 0.000 claims abstract description 34
- 238000010438 heat treatment Methods 0.000 claims abstract description 29
- 239000007789 gas Substances 0.000 claims abstract description 28
- 239000003463 adsorbent Substances 0.000 claims abstract description 23
- 239000012774 insulation material Substances 0.000 claims abstract description 16
- 238000001816 cooling Methods 0.000 claims description 29
- 238000009413 insulation Methods 0.000 claims description 20
- 239000002912 waste gas Substances 0.000 claims description 12
- 238000007789 sealing Methods 0.000 claims description 5
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 3
- 229910052802 copper Inorganic materials 0.000 claims description 3
- 239000010949 copper Substances 0.000 claims description 3
- 229910001220 stainless steel Inorganic materials 0.000 claims description 3
- 239000010935 stainless steel Substances 0.000 claims description 3
- 239000003795 chemical substances by application Substances 0.000 claims 1
- 238000012423 maintenance Methods 0.000 abstract description 5
- 238000010521 absorption reaction Methods 0.000 abstract 1
- 238000000034 method Methods 0.000 description 8
- 238000003795 desorption Methods 0.000 description 4
- 238000010586 diagram Methods 0.000 description 4
- 238000004378 air conditioning Methods 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 239000010425 asbestos Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 229920002635 polyurethane Polymers 0.000 description 2
- 239000004814 polyurethane Substances 0.000 description 2
- 229910052895 riebeckite Inorganic materials 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 230000001143 conditioned effect Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003546 flue gas Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000004321 preservation Methods 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
Classifications
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A30/00—Adapting or protecting infrastructure or their operation
- Y02A30/27—Relating to heating, ventilation or air conditioning [HVAC] technologies
- Y02A30/274—Relating to heating, ventilation or air conditioning [HVAC] technologies using waste energy, e.g. from internal combustion engine
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
- Y02B30/62—Absorption based systems
- Y02B30/625—Absorption based systems combined with heat or power generation [CHP], e.g. trigeneration
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P80/00—Climate change mitigation technologies for sector-wide applications
- Y02P80/10—Efficient use of energy, e.g. using compressed air or pressurized fluid as energy carrier
- Y02P80/15—On-site combined power, heat or cool generation or distribution, e.g. combined heat and power [CHP] supply
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- Sorption Type Refrigeration Machines (AREA)
Abstract
本发明公开了一种吸附式废热回收板式制冷器,包括前盖板、后盖板、板式制冷片和螺杆,所述前盖板通过螺杆串接固定后盖板和板式制冷片,板式制冷片位于前盖板与后盖板两者之间;所述板式制冷片内部抽真空,由吸附/脱附区、绝热区和冷凝/蒸发区组成,板式制冷片顶端为吸附/脱附区,中间为绝热区,底端为冷凝/蒸发区;所述吸附/脱附区包括制冷剂通道管a、加热盘管、吸附剂、高温废气入口、高温废气出口;所述绝热区包括制冷剂通道管b和绝热材料;所述冷凝/蒸发区包括冷凝盘管、冷凝空气入口、冷凝空气出口、蒸发盘管、蒸发空气入口和蒸发空气出口;本发明提供一种结构简单、可靠性高且拆卸组装及检修方便的吸附式废热回收板式制冷器。
The invention discloses an adsorption waste heat recovery plate refrigerator, which comprises a front cover plate, a rear cover plate, a plate type refrigeration sheet and a screw rod, the front cover plate is connected in series with the screw rod to fix the rear cover plate and the plate type refrigeration sheet, and the plate type refrigeration sheet It is located between the front cover and the rear cover; the inside of the plate refrigeration sheet is evacuated and consists of an adsorption/desorption area, an adiabatic area, and a condensation/evaporation area. The top of the plate refrigeration sheet is the adsorption/desorption area, and the middle It is an adiabatic area, and the bottom end is a condensation/evaporation area; the adsorption/desorption area includes a refrigerant channel pipe a, a heating coil, an adsorbent, a high-temperature exhaust gas inlet, and a high-temperature exhaust gas outlet; the adiabatic area includes a refrigerant channel pipe b and thermal insulation material; the condensation/evaporation area includes a condensation coil, a condensation air inlet, a condensation air outlet, an evaporation coil, an evaporation air inlet and an evaporation air outlet; the present invention provides a simple structure, high reliability and disassembly assembly And the absorption type waste heat recovery plate refrigerator with convenient maintenance.
Description
技术领域technical field
本发明属于固体吸附制冷领域,特别是一种吸附式废热回收板式制冷器。The invention belongs to the field of solid adsorption refrigeration, in particular to an adsorption waste heat recovery plate refrigerator.
背景技术Background technique
固体吸附式制冷器是一种可有效将废热能、太阳能转化为冷量的制冷技术,且对环境无污染。Solid adsorption refrigerator is a refrigeration technology that can effectively convert waste heat energy and solar energy into cold energy, and has no pollution to the environment.
目前,国内外常用的固体式吸附制冷机的结构是:整体式吸附床、蒸发器、冷凝器,制冷系统中采用阀门控制各个循环过程。常见吸附床的结构形式有壳管式、管翅式、螺旋板式,各吸附床通过阀门的闭合进行床体切换,从而实现连续制冷。采用这样的结构问题和缺陷是:①吸附床和蒸发、冷凝器分开连接,稳定性差,主要突出问题是真空度难以保持;②需要根据所需负荷进行整套的定做,不能够很好的够拆卸组装。③系统复杂庞大,检修、维修困难,尤其是在制冷冷量不能满足用户需求时,需要将整套的系统进行拆卸维修。At present, the structure of solid adsorption refrigerators commonly used at home and abroad is: integral adsorption bed, evaporator, condenser, and valves are used to control each cycle process in the refrigeration system. Common adsorption bed structures include shell-and-tube type, tube-fin type, and spiral plate type. Each adsorption bed is switched by closing the valve to achieve continuous refrigeration. The problems and defects of adopting such a structure are: ①The adsorption bed is connected separately from the evaporator and condenser, and the stability is poor. The main outstanding problem is that the vacuum degree is difficult to maintain; ②The whole set needs to be customized according to the required load, and it cannot be disassembled well. Assemble. ③The system is complicated and huge, and it is difficult to overhaul and maintain it. Especially when the cooling capacity cannot meet the user's needs, the entire system needs to be disassembled and repaired.
发明内容Contents of the invention
本发明的目的是为了克服现有的吸附式制冷/空调系统在运行过程中真空度难以保持、适应能力差、系统复杂、检修维修困难等问题,从而提供了一种吸附式废热回收板式制冷器。The purpose of the present invention is to provide an adsorption waste heat recovery plate refrigerator to overcome the problems of the existing adsorption refrigeration/air conditioning system, such as difficulty in maintaining the vacuum degree, poor adaptability, complex system, and difficult maintenance during operation. .
实现本发明目的的技术解决方案为:The technical solution that realizes the object of the present invention is:
一种吸附式废热回收板式制冷器,包括前盖板、后盖板、板式制冷片和螺杆,所述前盖板通过螺杆串接固定后盖板和板式制冷片,板式制冷片位于前盖板与后盖板两者之间;所述板式制冷片内部抽真空,由吸附/脱附区、绝热区和冷凝/蒸发区组成,板式制冷片顶端为吸附/脱附区,中间为绝热区,底端为冷凝/蒸发区;An adsorption type waste heat recovery plate refrigerator, comprising a front cover, a rear cover, a plate refrigeration piece and a screw, the front cover is connected in series with the screw to fix the rear cover and the plate refrigeration piece, and the plate refrigeration piece is located on the front cover and the back cover plate; the inside of the plate refrigeration sheet is evacuated, which is composed of an adsorption/desorption area, an adiabatic area and a condensation/evaporation area. The top of the plate type refrigeration sheet is an adsorption/desorption area, and the middle is an adiabatic area. The bottom is the condensation/evaporation zone;
所述吸附/脱附区包括制冷剂通道管a、加热盘管、吸附剂、高温废气入口、高温废气出口;所述制冷剂通道管a贯穿在吸附/脱附区中,吸附/脱附区内部设置有加热盘管;加热盘管一端与高温废气入口相连接,加热盘管另一端与高温废气出口相连接;吸附剂填充在吸附/脱附区中;The adsorption/desorption area includes a refrigerant channel pipe a, a heating coil, an adsorbent, a high-temperature exhaust gas inlet, and a high-temperature exhaust gas outlet; the refrigerant channel pipe a runs through the adsorption/desorption area, and the adsorption/desorption area There is a heating coil inside; one end of the heating coil is connected to the high-temperature exhaust gas inlet, and the other end of the heating coil is connected to the high-temperature exhaust gas outlet; the adsorbent is filled in the adsorption/desorption area;
所述绝热区包括制冷剂通道管b和绝热材料;所述制冷剂通道管b贯穿在绝热区中,绝热材料填充在绝热区中;所述制冷剂通道管a与制冷剂通道管b相连接;The heat insulation area includes refrigerant channel pipe b and heat insulation material; the refrigerant channel pipe b runs through the heat insulation area, and the heat insulation material is filled in the heat insulation area; the refrigerant channel pipe a is connected to the refrigerant channel pipe b ;
所述冷凝/蒸发区包括冷凝盘管、冷凝空气入口、冷凝空气出口、蒸发盘管、蒸发空气入口和蒸发空气出口;所述冷凝/蒸发区上端设置有冷凝盘管,下端设置有蒸发盘管;冷凝盘管一端与冷凝空气入口相连接,另一端与冷凝空气出口相连接;蒸发盘管一端与蒸发空气入口相连接,另一端与蒸发空气出口相连接。The condensing/evaporating area includes a condensing coil, a condensing air inlet, a condensing air outlet, an evaporating coil, an evaporating air inlet, and an evaporating air outlet; ; One end of the condensing coil is connected to the condensing air inlet, and the other end is connected to the condensing air outlet; one end of the evaporating coil is connected to the evaporating air inlet, and the other end is connected to the evaporating air outlet.
本发明与现有技术相比,其显著优点:Compared with the prior art, the present invention has significant advantages:
(1)本发明吸附式废热回收板式制冷器可节约能源,直接利用废气、废热作为热源来制取冷量;且应用范围广,可根据所填充制冷工质对的不同,应用于废气或废热温度为70℃~400℃的场合。(1) The adsorption type waste heat recovery plate refrigerator of the present invention can save energy, directly use waste gas and waste heat as heat source to produce cooling capacity; and has a wide range of applications, and can be applied to waste gas or waste heat according to the different pairs of refrigerants to be filled. When the temperature is 70°C to 400°C.
(2)本发明吸附式废热回收板式制冷器可根据不同条件下,不同负荷的要求组成不同功率大小的空调器,适应能力强,拆卸组装及检修方便;一旦有个别制冷片损坏,可单独更换,而不影响其他制冷单元,安装和检修十分方便。(2) The adsorption type waste heat recovery plate refrigerator of the present invention can form air conditioners of different power sizes according to different conditions and different load requirements, with strong adaptability, convenient disassembly, assembly and maintenance; once individual refrigeration chips are damaged, they can be replaced separately , without affecting other refrigeration units, very convenient for installation and maintenance.
(3)本发明吸附式废热回收板式制冷器集吸附器、冷凝器、蒸发器于一体,无节流装置,无冷剂控制阀门及复杂的管路连接,系统结构简单,且密封性好、可靠性高、传热能力强、系统结构紧凑。(3) The adsorption type waste heat recovery plate refrigerator of the present invention integrates an adsorber, a condenser, and an evaporator, has no throttling device, no refrigerant control valve and complicated pipeline connections, and has a simple system structure and good sealing performance. High reliability, strong heat transfer capacity, and compact system structure.
下面结合附图对本发明作进一步详细描述。The present invention will be described in further detail below in conjunction with the accompanying drawings.
附图说明Description of drawings
图1为本发明吸附式废热回收板式制冷器中板式制冷片的结构示意图。Fig. 1 is a schematic structural view of the plate refrigeration plate in the adsorption waste heat recovery plate refrigerator of the present invention.
图2为本发明吸附式废热回收板式制冷器中板式制冷片的部分结构示意图。Fig. 2 is a partial structural schematic diagram of the plate refrigeration plate in the adsorption waste heat recovery plate refrigerator of the present invention.
图3为本发明吸附式废热回收板式制冷器中制冷剂通道管a的结构示意图。Fig. 3 is a schematic structural view of the refrigerant channel pipe a in the adsorption waste heat recovery plate refrigerator of the present invention.
图4为本发明吸附式废热回收板式制冷器中板式制冷片串接示意图。Fig. 4 is a schematic diagram of the serial connection of the plate refrigeration plates in the adsorption waste heat recovery plate refrigerator of the present invention.
图5为本发明吸附式废热回收板式制冷器中前、后盖板的结构示意图。Fig. 5 is a schematic structural view of the front and rear cover plates in the adsorption waste heat recovery plate refrigerator of the present invention.
图6为本发明吸附式废热回收板式制冷器的结构示意图。Fig. 6 is a schematic structural diagram of an adsorption waste heat recovery plate refrigerator of the present invention.
图7为本发明吸附式废热回收板式制冷器组成制冷系统的结构示意图。Fig. 7 is a schematic structural diagram of a refrigeration system composed of an adsorption waste heat recovery plate refrigerator of the present invention.
图中:1.前盖板、2.后盖板、3.板式制冷片、4.螺杆、5.制冷剂通道管a、6.加热盘管、7.吸附剂、8.高温废气入口、9.高温废气出口、10.制冷剂通道管b、11.绝热材料、12.冷凝盘管、13.冷凝空气入口、14.冷凝空气出口、15.蒸发盘管、16.蒸发空气入口、17.蒸发空气出口、18.高温废气流入连接口、19.冷凝空气流入连接口、20.蒸发空气流入连接口、21.高温废气排出连接口、22.冷凝空气排出连接口、23.蒸发空气排出连接口、24.翅片。In the figure: 1. Front cover plate, 2. Rear cover plate, 3. Plate cooling plate, 4. Screw, 5. Refrigerant channel pipe a, 6. Heating coil, 7. Adsorbent, 8. High temperature exhaust gas inlet, 9. High temperature exhaust gas outlet, 10. Refrigerant channel pipe b, 11. Insulation material, 12. Condensation coil, 13. Condensation air inlet, 14. Condensation air outlet, 15. Evaporation coil, 16. Evaporation air inlet, 17 .Evaporation air outlet, 18. High temperature exhaust gas inflow connection port, 19. Condensed air inflow connection port, 20. Evaporation air inflow connection port, 21. High temperature exhaust gas discharge connection port, 22. Condensed air discharge connection port, 23. Evaporation air discharge Connecting port, 24. Fins.
具体实施方式Detailed ways
如图1~6所示:As shown in Figures 1 to 6:
一种吸附式废热回收板式制冷器,包括前盖板1、后盖板2、板式制冷片3和螺杆4,所述前盖板1通过螺杆4串接固定后盖板2和板式制冷片3,板式制冷片3位于前盖板1与后盖板2两者之间;所述板式制冷片3内部抽真空,由吸附/脱附区、绝热区和冷凝/蒸发区组成,板式制冷片3顶端为吸附/脱附区,中间为绝热区,底端为冷凝/蒸发区;An adsorption waste heat recovery plate refrigerator, comprising a front cover 1, a rear cover 2, a plate cooling plate 3 and a screw 4, the front cover 1 is connected in series by the screw 4 to fix the rear cover 2 and the plate cooling plate 3 , the plate cooling plate 3 is located between the front cover plate 1 and the rear cover plate 2; the inside of the plate cooling plate 3 is evacuated, and is composed of an adsorption/desorption area, an adiabatic area and a condensation/evaporation area, and the plate type cooling plate 3 The top is the adsorption/desorption zone, the middle is the adiabatic zone, and the bottom is the condensation/evaporation zone;
所述吸附/脱附区包括制冷剂通道管a5、加热盘管6、吸附剂7、高温废气入口8、高温废气出口9;所述制冷剂通道管a5贯穿在吸附/脱附区中,吸附/脱附区内部设置有加热盘管6;加热盘管6一端与高温废气入口8相连接,加热盘管6另一端与高温废气出口9相连接;吸附剂7填充在吸附/脱附区中;The adsorption/desorption area includes a refrigerant channel pipe a5, a heating coil 6, an adsorbent 7, a high-temperature exhaust gas inlet 8, and a high-temperature exhaust gas outlet 9; the refrigerant channel pipe a5 runs through the adsorption/desorption area, and the adsorption / There is a heating coil 6 inside the desorption area; one end of the heating coil 6 is connected to the high-temperature exhaust gas inlet 8, and the other end of the heating coil 6 is connected to the high-temperature exhaust gas outlet 9; the adsorbent 7 is filled in the adsorption/desorption area ;
所述绝热区包括制冷剂通道管b10和绝热材料11;所述制冷剂通道管b10贯穿在绝热区中,绝热材料11填充在绝热区中;所述制冷剂通道管a5与制冷剂通道管b10相连接;The heat insulation area includes refrigerant channel pipe b10 and heat insulation material 11; the refrigerant channel pipe b10 runs through the heat insulation area, and the heat insulation material 11 is filled in the heat insulation area; the refrigerant channel pipe a5 and the refrigerant channel pipe b10 connected;
所述冷凝/蒸发区包括冷凝盘管12、冷凝空气入口13、冷凝空气出口14、蒸发盘管15、蒸发空气入口16和蒸发空气出口17;所述冷凝/蒸发区上端设置有冷凝盘管12,下端设置有蒸发盘管15;冷凝盘管12一端与冷凝空气入口13相连接,另一端与冷凝空气出口14相连接;蒸发盘管15一端与蒸发空气入口16相连接,另一端与蒸发空气出口17相连接。The condensation/evaporation area includes a condensation coil 12, a condensation air inlet 13, a condensation air outlet 14, an evaporation coil 15, an evaporation air inlet 16 and an evaporation air outlet 17; the upper end of the condensation/evaporation area is provided with a condensation coil 12 , the lower end is provided with an evaporating coil 15; one end of the condensing coil 12 is connected to the condensing air inlet 13, and the other end is connected to the condensing air outlet 14; one end of the evaporating coil 15 is connected to the evaporating air inlet 16, and the other end is connected to the evaporating air Outlet 17 is connected.
所述前盖板1上设置有高温废气流入连接口18、冷凝空气流入连接口19、蒸发空气流入连接口20;所述后盖板2上设置有高温废气排出连接口21,冷凝空气排出连接口22,蒸发空气排出连接口23;所述前盖板1和后盖板2上的各个连接口与板式制冷片3上相对应的出入口在同一条水平直线上。The front cover 1 is provided with a high-temperature exhaust gas inflow connection port 18, condensed air inflow connection port 19, and evaporated air inflow connection port 20; the rear cover 2 is provided with a high-temperature exhaust gas discharge connection port 21, and the condensed air discharge connection Port 22, evaporating air discharge connection port 23; each connection port on the front cover plate 1 and rear cover plate 2 is on the same horizontal line as the corresponding entrance and exit on the plate cooling plate 3.
所述加热盘管6、冷凝盘管12和蒸发盘管15外侧都装有翅片24。Fins 24 are installed on the outer sides of the heating coil 6 , the condensing coil 12 and the evaporating coil 15 .
所述吸附/脱附区设置有多个制冷剂通道管a5,每个制冷剂通道管a5填埋在吸附剂7内部,贯穿于吸附/脱附区,其管壁上均匀的钻有通孔。The adsorption/desorption area is provided with a plurality of refrigerant channel tubes a5, and each refrigerant channel tube a5 is buried inside the adsorbent 7 and runs through the adsorption/desorption area, and through holes are evenly drilled on the tube wall .
所述绝热区设置有多个制冷剂通道管b10,每个制冷剂通道管b10填埋在绝热材料11内部,贯穿于绝热区,其长度和绝热区的高度相同;所述制冷剂通道管b10的数量多于制冷剂通道管a5的数量。The heat insulation area is provided with a plurality of refrigerant channel pipes b10, and each refrigerant channel pipe b10 is embedded in the heat insulation material 11, runs through the heat insulation area, and its length is the same as the height of the heat insulation area; the refrigerant channel pipe b10 The number of is more than the number of refrigerant channel pipes a5.
所述前盖板1与后盖板2之间串接固定1个或1个以上板式制冷片3。One or more plate-type refrigeration fins 3 are fixed in series between the front cover plate 1 and the rear cover plate 2 .
所述相邻两个板式制冷片3连接处套有耐高温密封圈。A high-temperature-resistant sealing ring is sleeved at the junction of the two adjacent plate-type refrigerating fins 3 .
所述制冷剂通道管a5和制冷剂通道管b10均采用不锈钢或铜管材质。Both the refrigerant passage pipe a5 and the refrigerant passage pipe b10 are made of stainless steel or copper pipe.
所述吸附剂7可根据不同温度的废气、废热采用不同的吸附工质对。The adsorbent 7 can adopt different pairs of adsorption working fluids according to waste gas and waste heat at different temperatures.
所述绝热材料11采用耐高温石棉与保温性能良好的聚氨酯保温材料结合起来。The thermal insulation material 11 is made of high temperature resistant asbestos combined with polyurethane thermal insulation material with good thermal insulation performance.
下面结合实施例对本发明吸附式废热回收板式制冷器做进一步详细的描述:The following is a further detailed description of the adsorption waste heat recovery plate refrigerator of the present invention in conjunction with the examples:
本发明吸附式废热回收板式制冷器,包括前盖板1、后盖板2、板式制冷片3和螺杆4,前盖板1、后盖板2和板式制冷片3上都设有多个螺孔,所述前盖板1通过螺杆4串接固定后盖板2和板式制冷片3,板式制冷片3位于前盖板1与后盖板2两者之间;所述板式制冷片3内部抽真空,由吸附/脱附区、绝热区和冷凝/蒸发区组成(如图2所示),板式制冷片3顶端为吸附/脱附区,中间为绝热区,底端为冷凝/蒸发区;The adsorption type waste heat recovery plate refrigerator of the present invention comprises a front cover 1, a rear cover 2, a plate refrigeration plate 3 and a screw 4, and a plurality of screws are arranged on the front cover 1, the rear cover 2 and the plate refrigeration plate 3. hole, the front cover 1 is fixed in series with the rear cover 2 and the plate cooling plate 3 through the screw 4, and the plate cooling plate 3 is located between the front cover 1 and the rear cover 2; the inside of the plate cooling plate 3 Vacuumizing, consisting of an adsorption/desorption area, an adiabatic area, and a condensation/evaporation area (as shown in Figure 2), the top of the plate refrigeration plate 3 is an adsorption/desorption area, the middle is an adiabatic area, and the bottom is a condensation/evaporation area ;
所述吸附/脱附区包括制冷剂通道管a5、加热盘管6、吸附剂7、高温废气入口8、高温废气出口9;吸附/脱附区均匀分布3个制冷剂通道管a5,每个制冷剂通道管a5填埋在吸附剂7内部,贯穿于吸附/脱附区,其管壁上均匀的钻有通孔(如图3所示);在吸附/脱附区内部固定安装加热盘管6;加热盘管6一端与高温废气入口8相连接,加热盘管6另一端与高温废气出口9相连接;所述吸附剂7可根据不同温度的废气、废热采用沸石-水、活性炭-氨或硅胶-水等不同的吸附工质对,填充在吸附/脱附区中;其中,制冷剂通道管a5采用不锈钢或铜管材质制成,直径为10mm,其管壁上通孔的直径为1~3mm。The adsorption/desorption area includes refrigerant channel pipe a5, heating coil 6, adsorbent 7, high-temperature exhaust gas inlet 8, and high-temperature exhaust gas outlet 9; three refrigerant channel pipes a5 are evenly distributed in the adsorption/desorption area, each Refrigerant channel pipe a5 is buried inside the adsorbent 7 and runs through the adsorption/desorption area, and through holes are evenly drilled on the pipe wall (as shown in Figure 3); a heating plate is fixedly installed inside the adsorption/desorption area Tube 6; one end of the heating coil 6 is connected to the high-temperature exhaust gas inlet 8, and the other end of the heating coil 6 is connected to the high-temperature exhaust gas outlet 9; the adsorbent 7 can be zeolite-water, activated carbon- Different adsorption working medium pairs such as ammonia or silica gel-water are filled in the adsorption/desorption area; among them, the refrigerant channel pipe a5 is made of stainless steel or copper pipe with a diameter of 10mm, and the diameter of the through hole on the pipe wall is 1 to 3mm.
所述绝热区包括制冷剂通道管b10和绝热材料11;绝热区均匀分布6个制冷剂通道管b10,每个制冷剂通道管b10填埋在绝热材料11内部,贯穿于绝热区,其长度和绝热区的高度相同;所述绝热材料11采用耐高温石棉与保温性能良好的聚氨酯保温材料结合起来,填充在绝热区中;所述制冷剂通道管a5与制冷剂通道管b10相贯通;其中,制冷剂通道管b10直径为2~5mm。The heat insulation area includes refrigerant channel pipe b10 and heat insulation material 11; six refrigerant channel pipes b10 are evenly distributed in the heat insulation area, and each refrigerant channel pipe b10 is buried inside the heat insulation material 11 and runs through the heat insulation area. The height of the heat insulation area is the same; the heat insulation material 11 is filled in the heat insulation area by combining high temperature resistant asbestos and polyurethane insulation material with good heat preservation performance; the refrigerant channel pipe a5 is connected with the refrigerant channel pipe b10; wherein, The diameter of the refrigerant channel pipe b10 is 2-5 mm.
所述冷凝/蒸发区包括冷凝盘管12、冷凝空气入口13、冷凝空气出口14、蒸发盘管15、蒸发空气入口16和蒸发空气出口17;所述冷凝/蒸发区上端设置有冷凝盘管12,下端设置有蒸发盘管15;冷凝盘管12一端与冷凝空气入口13相连接,另一端与冷凝空气出口14相连接;蒸发盘管15一端与蒸发空气入口16相连接,另一端与蒸发空气出口17相连接;所述加热盘管6、冷凝盘管12和蒸发盘管15外侧都装有翅片24,以增强其传热。The condensation/evaporation area includes a condensation coil 12, a condensation air inlet 13, a condensation air outlet 14, an evaporation coil 15, an evaporation air inlet 16 and an evaporation air outlet 17; the upper end of the condensation/evaporation area is provided with a condensation coil 12 , the lower end is provided with an evaporating coil 15; one end of the condensing coil 12 is connected to the condensing air inlet 13, and the other end is connected to the condensing air outlet 14; one end of the evaporating coil 15 is connected to the evaporating air inlet 16, and the other end is connected to the evaporating air The outlets 17 are connected; fins 24 are installed on the outside of the heating coil 6 , condensing coil 12 and evaporation coil 15 to enhance heat transfer.
如图4所示,将一定数量的板式制冷片3通过螺杆串接在一起,再将图5中的板式制冷片的前盖板1和后盖板2串接在图4中板式制冷片的两边,相邻两个板式制冷片3连接处套有耐高温密封圈,然后再通过螺杆上的螺丝将板式制冷片3和前、后盖板夹紧固定就组成了如图6所示的板式制冷器;可以根据要求,将不同数量的板式制冷片组装成不同功率大小的板式制冷器,来满足不同负荷的要求。As shown in Figure 4, a certain number of plate cooling fins 3 are connected in series by screws, and then the front cover 1 and rear cover 2 of the plate cooling fins in Figure 5 are connected in series to the plate cooling fins in Figure 4 On both sides, the joints of two adjacent plate-type cooling plates 3 are covered with high-temperature resistant sealing rings, and then the plate-type cooling plates 3 and the front and rear cover plates are clamped and fixed by the screws on the screw to form a plate-type cooling plate as shown in Figure 6. Refrigerator: According to the requirements, different numbers of plate refrigeration plates can be assembled into plate refrigerators of different power sizes to meet the requirements of different loads.
如图5,所述前盖板1上设置有高温废气流入连接口18、冷凝空气流入连接口19、蒸发空气流入连接口20;所述后盖板2上设置有高温废气排出连接口21,冷凝空气排出连接口22,蒸发空气排出连接口23;所述前盖板1和后盖板2上的各个连接口与板式制冷片3上相对应的出入口在同一条水平直线上;其流程为:吸附剂7脱附时,高温废气流入高温废气进入连接口18,然后均匀的流进各个板式制冷片3的高温废气入口8,流过加热盘管6,然后再从板式制冷片3的高温废气出口9流出,各个板式制冷片流出的高温烟气汇聚在一起,最后从高温废气排出连接口21排出;冷凝空气流入冷凝空气进入连接口19,然后均匀的流进各个板式制冷片3的冷凝空气入口13,流过冷凝盘管12,然后再从板式制冷片3的冷凝空气出口14流出,汇聚在一起,最后从冷凝空气排出连接口22排出。制冷时,空调空气流入蒸发空气流入连接口20,均匀的流进各个板式制冷片3的蒸发空气入口16,流过蒸发盘管15,然后再从板式制冷片3的蒸发空气出口17流出,汇聚在一起,最后从蒸发空气排出连接口23排出。As shown in Figure 5, the front cover 1 is provided with a high-temperature waste gas inflow connection port 18, a condensed air flow-in connection port 19, and an evaporated air flow-in connection port 20; the rear cover 2 is provided with a high-temperature waste gas discharge connection port 21, The condensed air is discharged from the connection port 22, and the evaporated air is discharged from the connection port 23; each connection port on the front cover plate 1 and the rear cover plate 2 is on the same horizontal line as the corresponding entrance and exit on the plate cooling plate 3; the process is as follows: : When the adsorbent 7 is desorbed, the high-temperature exhaust gas flows into the high-temperature exhaust gas into the connection port 18, and then evenly flows into the high-temperature exhaust gas inlet 8 of each plate-type refrigeration piece 3, flows through the heating coil 6, and then from the high-temperature exhaust gas of the plate-type refrigeration piece 3 The exhaust gas outlet 9 flows out, and the high-temperature flue gas flowing out of each plate cooling plate is gathered together, and finally discharged from the high-temperature exhaust gas discharge connection port 21; the condensed air flows into the condensing air into the connecting port 19, and then evenly flows into the condensation of each plate cooling plate 3 The air inlet 13 flows through the condensing coil 12 , and then flows out from the condensed air outlet 14 of the plate cooling fin 3 , gathers together, and finally discharges from the condensed air discharge connection port 22 . During cooling, the conditioned air flows into the evaporating air inlet 20, flows evenly into the evaporating air inlet 16 of each plate cooling fin 3, flows through the evaporating coil 15, and then flows out from the evaporating air outlet 17 of the plate cooling fin 3, converging Together, they are finally discharged from the evaporative air discharge connection port 23.
其中,所述的板式制冷片3,内部抽真空,并向内灌充吸附剂7,将一定数量的板式制冷片3串接在前、后盖板的中间,再用螺杆紧密连接起来,就组成了板式制冷器;所述的吸附/脱附区内置有3个制冷剂通道管a5和加热盘管6,同时在制冷剂通道管a5和加热盘管6周围填充吸附剂7。制冷剂通道管a5保证吸附剂7脱附时,制冷剂蒸气能够有效的流进冷凝器;吸附剂7吸附时,制冷剂蒸气能够有效的从蒸发器流入吸附器被吸附剂充分吸附;在所有盘管外侧装有翅片,以增强其传热。所述的制冷剂通道管b10,能够保证制冷剂蒸气在吸附/脱附区和冷凝/蒸发区上下流动,并且保证吸附/脱附区内的吸附剂不散落到冷凝/蒸发区内。Wherein, the plate-type refrigerating fins 3 are vacuumized inside and filled with adsorbent 7, and a certain number of plate-type refrigerating fins 3 are connected in series between the front and rear cover plates, and then tightly connected with screws, thus A plate refrigerator is formed; the adsorption/desorption area is built with three refrigerant passage pipes a5 and heating coil 6, and the refrigerant passage pipe a5 and heating coil 6 are filled with adsorbent 7 at the same time. The refrigerant channel pipe a5 ensures that when the adsorbent 7 is desorbed, the refrigerant vapor can effectively flow into the condenser; when the adsorbent 7 is adsorbed, the refrigerant vapor can effectively flow from the evaporator into the adsorber and be fully absorbed by the adsorbent; The outside of the coil is finned to enhance its heat transfer. The refrigerant passage pipe b10 can ensure that the refrigerant vapor flows up and down in the adsorption/desorption area and the condensation/evaporation area, and ensure that the adsorbent in the adsorption/desorption area does not scatter into the condensation/evaporation area.
本发明吸附式废热回收板式制冷器中板式制冷片3的具体制冷过程:The specific refrigeration process of the plate refrigeration plate 3 in the adsorption waste heat recovery plate refrigerator of the present invention:
第一,脱附、冷凝过程:高温废气废热通过加热盘管6,从而加热吸附/脱附区内的吸附剂7,使制冷剂脱附出来,脱附出来的制冷剂蒸气,通过制冷剂通道管a5管壁上的通孔流入制冷剂通道管a5,流过制冷剂通道管b10,进入冷凝/蒸发区。与此同时,冷凝空气流过冷凝盘管12,使脱附出来的制冷剂蒸气,在冷凝盘管12周围冷凝液化,并存储在蒸发盘管15周围;First, the process of desorption and condensation: the waste heat of high-temperature exhaust gas passes through the heating coil 6, thereby heating the adsorbent 7 in the adsorption/desorption area, so that the refrigerant is desorbed, and the desorbed refrigerant vapor passes through the refrigerant channel The through hole on the tube wall of the tube a5 flows into the refrigerant channel tube a5, flows through the refrigerant channel tube b10, and enters the condensation/evaporation zone. At the same time, the condensed air flows through the condensing coil 12, so that the desorbed refrigerant vapor is condensed and liquefied around the condensing coil 12, and stored around the evaporating coil 15;
第二,蒸发、制冷过程:当脱附完毕,蒸发盘管15周围充满了液态制冷剂,停止向加热盘管6通入高温废气废热;让大气空气通过加热盘管6,使吸附床快速冷却下来;待吸附床冷却下来后,空调空气通入蒸发盘管15使蒸发盘管15周围的液态制冷剂汽化,带走大量的汽化潜热,使流过空调空气的温度降低,从而达到制冷的目的。Second, the process of evaporation and refrigeration: when the desorption is completed, the surroundings of the evaporation coil 15 are filled with liquid refrigerant, and the high-temperature waste gas and waste heat are stopped feeding into the heating coil 6; atmospheric air is allowed to pass through the heating coil 6 to rapidly cool the adsorption bed down; after the adsorption bed cools down, air-conditioning air flows into the evaporating coil 15 to vaporize the liquid refrigerant around the evaporating coil 15, taking away a large amount of latent heat of vaporization, reducing the temperature of the air flowing through the air-conditioning, so as to achieve the purpose of refrigeration .
结合图7,采用两个本发明吸附式废热回收板式制冷器,组成连续交替的循环制冷系统。整个过程只涉及外部热气流(包括加热/冷却气流和冷凝/蒸发气流)流向的切换,而不涉及内部工质流向的切换,系统的内部制冷工质的循环制冷全部在各自板式制冷片3独立同步完成。其工作过程是:一个板式制冷器进行脱附、冷凝,另一个板式制冷器进行蒸发、制冷,这样两个板式制冷器通过相应的阀切换而交替工作,可以连续的提供冷量。连续交替的循环制冷系统利用本发明吸附式废热回收板式制冷器,实现了系统结构简单,密封性好、可靠性高且拆卸组装及检修方便。Referring to Fig. 7, two adsorption waste heat recovery plate refrigerators of the present invention are used to form a continuous and alternating cycle refrigeration system. The whole process only involves the switching of the flow direction of the external hot air flow (including heating/cooling air flow and condensation/evaporation air flow), not the switching of the flow direction of the internal working medium. Synchronization complete. Its working process is: one plate cooler performs desorption and condensation, and the other plate cooler performs evaporation and refrigeration. In this way, the two plate coolers work alternately through corresponding valve switching, and can continuously provide cooling capacity. The continuous alternating cycle refrigeration system utilizes the adsorption waste heat recovery plate refrigerator of the present invention to realize a simple system structure, good sealing performance, high reliability, and convenient disassembly, assembly and maintenance.
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Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN2521556Y (en) * | 2001-12-26 | 2002-11-20 | 财团法人工业技术研究院 | Solid Adsorption Refrigeration Unit |
CN1656346A (en) * | 2002-04-18 | 2005-08-17 | 索尔泰克股份公司 | Solid substance sorption heat pump |
JP2006052889A (en) * | 2004-08-11 | 2006-02-23 | Toshiba Kyaria Kk | Adsorption tower for adsorption refrigeration system |
CN101135508A (en) * | 2007-08-16 | 2008-03-05 | 青岛大学 | Solid Adsorption Unit Tube and Its Composite Adsorption Refrigeration Device |
CN101512251A (en) * | 2006-09-08 | 2009-08-19 | 华威大学 | Plate heat exchanger |
CN101532751A (en) * | 2009-04-16 | 2009-09-16 | 郑州大学 | Built-in sorbent floating head type adsorbent bed refrigeration unit |
JP2013019664A (en) * | 2011-07-11 | 2013-01-31 | Palo Alto Research Center Inc | Plate-based adsorption chiller subassembly |
-
2013
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Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN2521556Y (en) * | 2001-12-26 | 2002-11-20 | 财团法人工业技术研究院 | Solid Adsorption Refrigeration Unit |
CN1656346A (en) * | 2002-04-18 | 2005-08-17 | 索尔泰克股份公司 | Solid substance sorption heat pump |
JP2006052889A (en) * | 2004-08-11 | 2006-02-23 | Toshiba Kyaria Kk | Adsorption tower for adsorption refrigeration system |
CN101512251A (en) * | 2006-09-08 | 2009-08-19 | 华威大学 | Plate heat exchanger |
CN101135508A (en) * | 2007-08-16 | 2008-03-05 | 青岛大学 | Solid Adsorption Unit Tube and Its Composite Adsorption Refrigeration Device |
CN101532751A (en) * | 2009-04-16 | 2009-09-16 | 郑州大学 | Built-in sorbent floating head type adsorbent bed refrigeration unit |
JP2013019664A (en) * | 2011-07-11 | 2013-01-31 | Palo Alto Research Center Inc | Plate-based adsorption chiller subassembly |
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