CN1389690A - Generator Structure Used in Absorption Diffusion Refrigerator - Google Patents
Generator Structure Used in Absorption Diffusion Refrigerator Download PDFInfo
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- CN1389690A CN1389690A CN01118489A CN01118489A CN1389690A CN 1389690 A CN1389690 A CN 1389690A CN 01118489 A CN01118489 A CN 01118489A CN 01118489 A CN01118489 A CN 01118489A CN 1389690 A CN1389690 A CN 1389690A
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- ammonia solution
- absorption
- generator
- pipe
- tube
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- 238000009792 diffusion process Methods 0.000 title claims abstract description 15
- 238000010521 absorption reaction Methods 0.000 title description 7
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 claims abstract description 45
- 235000011114 ammonium hydroxide Nutrition 0.000 claims abstract description 45
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonium chloride Substances [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 claims abstract description 44
- QGZKDVFQNNGYKY-UHFFFAOYSA-N ammonia Natural products N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 abstract description 43
- 238000010438 heat treatment Methods 0.000 abstract description 10
- 229910021529 ammonia Inorganic materials 0.000 description 17
- 238000005057 refrigeration Methods 0.000 description 17
- 239000006096 absorbing agent Substances 0.000 description 8
- 239000007788 liquid Substances 0.000 description 8
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 4
- 230000004913 activation Effects 0.000 description 4
- 230000006835 compression Effects 0.000 description 2
- 238000007906 compression Methods 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 239000006193 liquid solution Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000003507 refrigerant Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
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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
-
- 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
Landscapes
- Sorption Type Refrigeration Machines (AREA)
Abstract
Description
本发明涉及一种使用于吸收扩散式冷冻装置的发生器结构,特别是涉及一种利用热传导套筒,以便减小内、外管间的热阻,进而降低汽泡激活温度的创新结构。The invention relates to a generator structure used in an absorption-diffusion refrigeration device, in particular to an innovative structure which utilizes a heat conduction sleeve to reduce the thermal resistance between inner and outer tubes, thereby lowering the activation temperature of bubbles.
一般氨吸收式冷冻循环与压缩式冷冻循环的不同点在于其完成压缩的方式的不同,即于吸收式冷冻循环中,其低压氨蒸汽被水所吸收后,而以液压泵将此液体溶液泵至高压。如图1所示,其为氨吸收式冷冻循环的动作流程图,首先低压氨蒸汽离开蒸发器后而进入吸收器,且于其内被稀氨水溶液吸收,此过程是在温度略高于外界温度下进行,故其中必定有热传至外界;再者,将所得的浓氨水溶液用泵经过一热交换器,而泵至保持于高压高温下的发生器中,由此,于该发生器内的高温热源的传入热量,而使氨蒸汽由浓氨水溶液被蒸发出来,且流至凝结器中凝结形成液态氨,并进入蒸发器,另外由该发生器所产生的稀氨水溶液则经过热交换器再回到吸收器中,以完成一吸收式冷冻循环。The difference between the general ammonia absorption refrigeration cycle and the compression refrigeration cycle lies in the way it completes the compression. In the absorption refrigeration cycle, the low-pressure ammonia vapor is absorbed by water, and the liquid solution is pumped by a hydraulic pump. to high pressure. As shown in Figure 1, it is the action flow chart of the ammonia absorption refrigeration cycle. First, the low-pressure ammonia vapor leaves the evaporator and enters the absorber, where it is absorbed by dilute ammonia solution. This process is carried out at a temperature slightly higher than that of the outside world. temperature, so there must be heat transfer to the outside; moreover, the obtained concentrated ammonia solution is pumped through a heat exchanger, and pumped into the generator maintained at high pressure and high temperature, thus, in the generator The incoming heat from the high-temperature heat source inside makes the ammonia vapor evaporate from the concentrated ammonia solution, flows to the condenser to condense to form liquid ammonia, and enters the evaporator, and the dilute ammonia solution produced by the generator passes through The heat exchanger returns to the absorber to complete an absorption refrigeration cycle.
另外,在冷冻循环系统中,为了防止能量损失所造成的浪费,常会有各式管路的设计,如双套管(或二重管)的设计等,且该双套管是可应用于发生器的加热区,以便具有较完整的热交换;但是,该双套管的内管是为浓氨水熔液管,即因热传需通过外管而间接加热内管,因此,如果想使内管的浓氨水溶液发生汽、液分离时,势必需加热至相当高温以致激活汽泡的发生;因此,该发生器需提供相当大的外来能量借以产生高温,其不仅增加整体的耗电量,且于设计应用方面也受到限制(例如无法采用一般可产生中、低温度的燃料电池及一般废热,所以也无法实施于小型的冰箱等);可见,在实际使用上,显然具有不便与存在缺陷,而亟待加以改善。In addition, in the refrigeration cycle system, in order to prevent waste caused by energy loss, there are often various pipeline designs, such as the design of double sleeves (or double tubes), and the double sleeves can be applied to In order to have a relatively complete heat exchange; however, the inner tube of the double sleeve is a concentrated ammonia solution tube, that is, the inner tube is heated indirectly through the outer tube due to heat transfer, so if you want to make the inner tube When the concentrated ammonia solution in the tube is separated into vapor and liquid, it must be heated to a relatively high temperature to activate the generation of bubbles; therefore, the generator needs to provide a considerable external energy to generate high temperature, which not only increases the overall power consumption, but also And it is also limited in design and application (for example, fuel cells and general waste heat that can generally generate medium and low temperatures cannot be used, so it cannot be implemented in small refrigerators, etc.); it can be seen that in actual use, it is obviously inconvenient and defective. , and urgently need to be improved.
本发明的目的在于提供一种使用于吸收扩散式冷冻装置的发生器结构,以克服现有技术所存在的缺陷。The object of the present invention is to provide a generator structure used in an absorption-diffusion refrigeration device, so as to overcome the defects in the prior art.
本发明的目的是这样实现的:一种使用于吸收扩散式冷冻装置的发生器结构,其关键在于,包括有一加热装置、一位于该加热装置的双套管及一设于该双套管的内、外管间的热传导套筒;其具有完整的热交换,且可减少内、外管间的热阻,进而降低发生器的汽泡激活温度。The object of the present invention is achieved like this: a kind of generator structure that is used in the absorption diffusion type freezing device, its key lies in, comprises a heating device, a double casing that is positioned at this heating device and is located at this double casing The heat conduction sleeve between the inner and outer tubes; it has complete heat exchange and can reduce the thermal resistance between the inner and outer tubes, thereby reducing the bubble activation temperature of the generator.
所述的使用于吸收扩散式冷冻装置的发生器结构,其中该双套管的内管是为浓氨水溶液管,而外管则为稀氨水溶液管。In the generator structure used in the absorption-diffusion refrigeration device, the inner tube of the double casing is a concentrated ammonia solution tube, and the outer tube is a dilute ammonia solution tube.
所述的使用于吸收扩散式冷冻装置的发生器结构,其中该热传导套筒表面可开设有复数沟槽。In the generator structure used in the absorption-diffusion refrigeration device, a plurality of grooves can be opened on the surface of the heat conduction sleeve.
由此可见,本发明提供了一种使用于吸收扩散式冷冻装置的发生器结构,其包括有一加热装置、一位于该加热装置的双套管及一设于该双套管的内、外管间的热传导套筒,其中,该双套管的内管是为浓氨水溶洒管,而外管则为稀氨水溶液管,且该热传导套筒表面是开设有复数沟槽,以利于外管的稀氨水溶液通过;据此,通过加热该双套管,即可具有较完整的热交换,且利用该热传导套筒予以减少内、外管间的热阻,进而降低发生器的汽泡激活温度。It can thus be seen that the present invention provides a generator structure used in an absorption-diffusion refrigeration device, which includes a heating device, a double casing positioned at the heating device, and an inner and outer tube located at the double casing The heat conduction sleeve between them, wherein, the inner tube of the double sleeve is a concentrated ammonia solution spray pipe, while the outer tube is a dilute ammonia solution pipe, and the surface of the heat conduction sleeve is provided with a plurality of grooves to facilitate the outer pipe The dilute ammonia solution passes through; accordingly, by heating the double sleeves, a relatively complete heat exchange can be achieved, and the heat conduction sleeve is used to reduce the thermal resistance between the inner and outer tubes, thereby reducing the bubble activation of the generator temperature.
下面结合实施例及其附图,对本发明的特征及技术内容作进一步详细说明,然而所示附图仅提供参考与说明用,并非用来对本发明加以限制。The features and technical content of the present invention will be described in further detail below in conjunction with the embodiments and accompanying drawings. However, the accompanying drawings are provided for reference and illustration only, and are not intended to limit the present invention.
图1为一般氨吸收式冷冻循环的动作流程图;Fig. 1 is the action flowchart of general ammonia absorption type refrigeration cycle;
图2为本发明发生器结构的实施状态图;Fig. 2 is the implementation status figure of generator structure of the present invention;
图3为本发明发生器结构的侧面剖面图;Fig. 3 is the side sectional view of generator structure of the present invention;
图4为图3的B-B部分的断面剖视图;Fig. 4 is the sectional view of the B-B part of Fig. 3;
图5为图3的C-C部分的断面剖视图。Fig. 5 is a sectional view of part C-C of Fig. 3 .
本发明是提供一种使用于吸收扩散式冷冻装置的发生器结构,其中,该吸收扩散式冷冻装置(如图2所示)是包括一浓氨水溶液槽1、一发生器2、一汽液分离装置3、一凝结器4、一蒸发器(图略)、一吸收器5,以及必要的管路6与控制装置(图略)等构件所组成。The present invention provides a generator structure used in an absorption-diffusion refrigeration device, wherein the absorption-diffusion refrigeration device (as shown in Figure 2) comprises a concentrated
该冷冻装置是以氨作为冷媒剂,且按氨水的浓度可区分为浓氨水溶液及稀氨水溶液,该冷冻装置的冷却动作说明如下:首先,自该浓氨水溶液槽1流出的浓氨水溶液70通过该发生器2而予以加热,且随着温度的升高,以便使该浓氨水溶液70开始汽化而产生汽泡,并分离出稀氨水溶液71及氨蒸汽72;其中,该氨蒸汽72则进入该凝结器4而予以冷凝,以便使该氨蒸汽72凝结出氨液体73,而后该氨液体73即进入该蒸发器(图略),而使该氨液体73被蒸发成氨气(图略),且该氨气(图略)是与自该吸收器5流出的氢气(图略)混合,以便形成混合氨气与氢气74而流回至该浓氨水溶液槽1。This refrigerating device uses ammonia as a refrigerant agent, and can be divided into a strong ammonia solution and a dilute ammonia solution according to the concentration of ammonia water. It is heated by the
另外,上述发生器2所分离的稀氨水溶液71是进入该吸收器5,该吸收器5的稀氨水溶液71是可与通过该吸收器5的混合氨气与氢气74相互吸收作用,以便使该稀氨水溶液71被吸收渐成浓氨水溶液70而流回该浓氨水溶液槽1,另通过该吸收器5的混合氨气与氢气74也被吸收渐成氢气(图略)而进入该蒸发器(图略),借以完成一冷冻循环的动作流程。In addition, the
据此,本发明主要针对上述吸收扩散式冷冻装置的发生器加以设计;请同时参阅图2及图3所示,自该浓氨水溶液槽1流出的浓氨水溶液70即流入一浓氨水溶液管20,该浓氨水溶液管20是以同轴方式套接于一稀氨水溶液管21内(如图4所示)而形成双套管,且该浓氨水溶液管20与该稀氨水溶液管21是于该汽液分离装置3处相连通,也即,通过该发生器2的浓氨水溶液70则分离成稀氨水溶液71及氨蒸汽72,且两者流至该汽液分离装置3处时,该氨蒸汽72会往上流至该凝结器4,而该稀氨水溶液71则往下回流进入该稀氨水溶液管21内。Accordingly, the present invention is mainly designed for the generator of the above-mentioned absorption-diffusion refrigeration device; please refer to Fig. 2 and shown in Fig. 3 simultaneously, the
另外,该发生器2是利用一加热装置22予以加热通过该浓、稀氨水溶液管20、21内的浓氨水溶液70及稀氨水溶液71,而使该浓氨水溶液70分离成稀氨水溶液71及氨蒸汽72,且在加热处的浓、稀氨水溶液管20、21间套置有一热传导套筒23,该热传导套筒23的表面是开设有复数沟槽230,以利该稀氨水溶液管21内的稀氨水溶液71通过,且该热传导套筒23是可减少该浓、稀氨水溶液管20、21间的热阻,进而降低发生器的气泡激活温度。In addition, the
综上所述,本发明所公开的是使用于吸收扩散式冷冻装置的发生器结构,其主要利用一热传导套筒,即可使发生器在中、低温便可达到汽、液分离的功效。To sum up, the present invention discloses a generator structure used in an absorption-diffusion refrigeration device, which mainly utilizes a heat conduction sleeve, so that the generator can achieve the effect of separating vapor and liquid at medium and low temperatures.
但是,以上所述仅为本发明的较佳可行实施例,并非因此来限定本发明的保护范围,所以凡是运用本发明说明书及附图内容所进行的等效结构变化,均包含于本发明的权利要求所确定的保护范围内,合予陈明。However, the above descriptions are only preferred feasible embodiments of the present invention, and are not intended to limit the protection scope of the present invention. Therefore, all equivalent structural changes made by using the description of the present invention and the contents of the accompanying drawings are included in the scope of the present invention. Within the scope of protection determined by the claims, it is agreed to state.
Claims (3)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB011184892A CN1178036C (en) | 2001-06-01 | 2001-06-01 | Generator structure for absorption-diffusion type refrigerating device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB011184892A CN1178036C (en) | 2001-06-01 | 2001-06-01 | Generator structure for absorption-diffusion type refrigerating device |
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| Publication Number | Publication Date |
|---|---|
| CN1389690A true CN1389690A (en) | 2003-01-08 |
| CN1178036C CN1178036C (en) | 2004-12-01 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB011184892A Expired - Fee Related CN1178036C (en) | 2001-06-01 | 2001-06-01 | Generator structure for absorption-diffusion type refrigerating device |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107677014A (en) * | 2017-11-13 | 2018-02-09 | 苏州市泰美达电器有限公司 | A kind of steam generator riser and absorption type refrigerating unit |
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2001
- 2001-06-01 CN CNB011184892A patent/CN1178036C/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107677014A (en) * | 2017-11-13 | 2018-02-09 | 苏州市泰美达电器有限公司 | A kind of steam generator riser and absorption type refrigerating unit |
| WO2019090792A1 (en) * | 2017-11-13 | 2019-05-16 | 苏州市泰美达电器有限公司 | Riser for vapor generator and absorption refrigeration device |
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| Publication number | Publication date |
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| CN1178036C (en) | 2004-12-01 |
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