CN202032783U - Single-stage ammonia water absorption refrigerator - Google Patents
Single-stage ammonia water absorption refrigerator Download PDFInfo
- Publication number
- CN202032783U CN202032783U CN2011201361530U CN201120136153U CN202032783U CN 202032783 U CN202032783 U CN 202032783U CN 2011201361530 U CN2011201361530 U CN 2011201361530U CN 201120136153 U CN201120136153 U CN 201120136153U CN 202032783 U CN202032783 U CN 202032783U
- Authority
- CN
- China
- Prior art keywords
- pipeline
- gas
- generator
- liquid separator
- solution
- 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.)
- Expired - Lifetime
Links
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 title claims abstract description 16
- 235000011114 ammonium hydroxide Nutrition 0.000 title claims abstract description 16
- 238000010521 absorption reaction Methods 0.000 title abstract 2
- 239000007788 liquid Substances 0.000 claims abstract description 26
- 239000006096 absorbing agent Substances 0.000 claims description 15
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 abstract description 38
- 229910021529 ammonia Inorganic materials 0.000 abstract description 18
- 239000000498 cooling water Substances 0.000 abstract description 14
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonium chloride Substances [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 abstract description 4
- 230000000630 rising effect Effects 0.000 abstract description 2
- 238000000926 separation method Methods 0.000 abstract 1
- 238000005057 refrigeration Methods 0.000 description 4
- 230000008859 change Effects 0.000 description 3
- 238000004134 energy conservation Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 230000008901 benefit Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 239000011555 saturated liquid Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
Classifications
-
- 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
本实用新型公开的一种单级氨水吸收式制冷机，系统中不设置分凝器，发生器-精馏塔顶端通过管路连接冷凝器顶端，冷凝器下端出口管路依次流经气液分离器、过冷器和蒸发器连到气液分离器上部，气液分离器底端通过管路连接到发生器-精馏塔上部，该段管路上安装有溶液泵，蒸发器出口处气液分离器中的氨水溶液与来自冷凝器的液氨进行热交换后，经溶液泵加压直接从精馏塔顶部喷淋，与发生器-精馏塔中上升的蒸汽进行热质交换，既保证了精馏塔出口氨蒸汽的浓度，又回收了精馏热，且避免了外界温度变化对精馏塔内部温度的影响，系统运行的稳定性大大提高。本实用新型装置简化了冷却水系统，减少了冷却水用量，便于节能。
The utility model discloses a single-stage ammonia water absorption refrigerator. There is no decondenser in the system. The top of the generator-rectification tower is connected to the top of the condenser through a pipeline, and the outlet pipeline at the lower end of the condenser flows through the gas-liquid separation in sequence. The gas-liquid separator, subcooler and evaporator are connected to the upper part of the gas-liquid separator, and the bottom end of the gas-liquid separator is connected to the upper part of the generator-rectification column through a pipeline. A solution pump is installed on this section of the pipeline, and the gas-liquid After the ammonia solution in the separator exchanges heat with the liquid ammonia from the condenser, it is pressurized by the solution pump and sprayed directly from the top of the rectification tower, and exchanges heat and mass with the rising steam in the generator-rectification tower, which ensures The concentration of ammonia vapor at the outlet of the rectification tower is reduced, the rectification heat is recovered, and the influence of external temperature changes on the internal temperature of the rectification tower is avoided, so the stability of the system operation is greatly improved. The device of the utility model simplifies the cooling water system, reduces the consumption of cooling water, and is convenient for energy saving.
Description
Technical field
The utility model relates to the refrigeration machine field of industrial use, particularly relates to a kind of single-stage ammonia water absorbing refrigerator.
Background technology
At present, the single-stage ammonia water absorbing refrigerator of industrial use adopts segregator purification ammonia steam more, and in addition, absorber is directly delivered in the evaporimeter discharge opeing.Such system, consumption of cooling-water is big, the cooling water system complexity; Because cooling water temperature is subject to ectocine, and then influences vapor (steam) temperature in the rectifying column, be not easy to system's control, the less stable of system's operation; In addition, rectified heat can not get recycling, and the cooling water system power consumption is serious, causes system effectiveness lower.
The utility model content
Technical problem to be solved in the utility model is at the consumption of cooling-water that exists in the above-mentioned prior art big, the cooling water system complexity, cooling water temperature is subject to ectocine, and then influences vapor (steam) temperature in the rectifying column, be not easy to system's control, the less stable of system's operation; In addition, rectified heat can not get recycling, and the cooling water system power consumption is serious, causes problems such as system effectiveness is lower and a kind of single-stage ammonia water absorbing refrigerator of proposing, and this kind refrigeration machine has been simplified cooling water system, has reduced cooling water amount, is convenient to energy-conservation; Avoided outside air temperature to change simultaneously, be convenient to system's control Temperature Influence in the rectifying column; Refrigeration machine efficient improves.
The technical problem that the utility model requires to solve can be achieved through the following technical solutions:
A kind of single-stage ammonia water absorbing refrigerator, comprise generator-rectifying column, condenser, gas-liquid separator, subcooler, evaporimeter, absorber, solution pump, solution heat exchanger, described generator-rectifying column top connects the condenser top by pipeline, the described condenser lower end export pipeline gas-liquid separator of flowing through successively, subcooler and evaporimeter are linked gas-liquid separator top, described gas-liquid separator bottom is connected to generator-rectifier by pipeline, on described this section pipeline solution pump is installed, described gas-liquid separator top is connected to absorber top by pipeline through subcooler, described absorber top is connected by pipeline with generator-rectifying column bottom, described this section pipeline solution heat exchanger of flowing through, described absorber bottom is connected to generator-rectifying column middle part by pipeline, on described this section pipeline solution pump is installed, and the solution heat exchanger of flowing through.
Described gas-liquid separator bottom is provided with heat exchange coil.Realize that by the ammonia spirit heat exchange in heat exchange coil and the gas-liquid separator first time is cold excessively by the liquid ammonia that condenser flows out, and the ammonia spirit temperature is raise.
On the pipeline between described generator-rectifying column bottom and absorber top the solution choke valve is installed.
Described condenser lower end export pipeline is equipped with the solution choke valve in subcooler to this section of evaporimeter.
Segregator is not set in the system, adds solution pump between gas-liquid separator and the generator-rectifying column, the ammonia spirit in the gas-liquid separator with carry out heat exchange from the liquefied ammonia of condenser after, directly spray through the solution pump pressurization from the rectifying column top.
Owing to adopted as above technical scheme, the utility model compared with prior art has following characteristics: simplified cooling water system, reduced cooling water amount, be convenient to energy-conservation; Utilize solution spraying can reclaim rectified heat, and avoided outside air temperature to change Temperature Influence in the rectifying column, be convenient to system's control, the stability of system's operation improves greatly; Make from the liquefied ammonia of condenser realized twice cold excessively, effectively increased refrigerating capacity, be convenient to improve refrigeration machine efficient.
Description of drawings
Fig. 1 is the utility model structural representation.
Among the figure: 1, generator-rectifying column, 2, condenser, 3, gas-liquid separator, 4, subcooler, 5, choke valve, 6, evaporimeter, 7, absorber, 8,11, solution pump, 9, solution heat exchanger, 10, the solution choke valve.
The specific embodiment
For technological means, creation characteristic that the utility model is realized, reach purpose and effect is easy to understand, below in conjunction with concrete diagram, further set forth the utility model.
As shown in Figure 1, a kind of single-stage ammonia water absorbing refrigerator is made up of generator-rectifying column 1, condenser 2, gas-liquid separator 3, subcooler 4, choke valve 5, evaporimeter 6, absorber 7, solution pump 8,11, solution heat exchanger 9, solution choke valve 10.
Operation principle and flow process: the concentrated ammonia solution that is flowed out by absorber 7 pressurizes through solution pump 8, flow through after solution heat exchanger 9 and the dilute ammonia solution heat exchange from generator, the ammonia spirit that flows down with rectifying section flows into generator, in this process, contact with the steam that is evaporated of solution in the generator, carry out the caloic exchange, make in the solution ammonia concentration step-down gradually, and the ammonia concentration in the rising steam uprises gradually.Through carrying out the caloic exchange with low temperature ammonia spirit from gas-liquid separator, temperature reduces, because pressure is constant, by regulating flow from the ammonia spirit of gas-liquid separator, can change the temperature of rectifying column top ammonia steam, the concentration of control rectifying column outlet ammonia steam remains on more than 99.8% it indirectly, like this, both guaranteed the concentration of rectifying column outlet ammonia steam, reclaimed rectified heat again, and avoided the influence of ambient temperature variation to the rectifying column internal temperature, the stability of system's operation improves greatly.The ammonia steam that is flowed out by generator-rectifying column 1 is condensed into saturated liquid in condenser 2, after successively by gas-liquid separator 3 and subcooler 4 realize twice cold excessively, increased refrigerating capacity; The choke valve 5 of flowing through again enters evaporimeter 6.The two-phase mixture of the ammonia spirit that is flowed out by evaporimeter 6 separates in gas-liquid separator 3, solution with from after the liquefied ammonia heat exchange of condenser 2 by solution pump 11 pressurized delivered to generator-rectifying column 1, the vapour mixture subcooler 4 of flowing through, in absorber 7, absorbed, finish circulation with this by dilute ammonia solution from generator-rectifying column 1.
More than show and described basic principle of the present utility model, principal character and advantage of the present utility model.The technical staff of the industry should understand; the utility model is not restricted to the described embodiments; that describes in the foregoing description and the specification just illustrates principle of the present utility model; the utility model also has various changes and modifications under the prerequisite that does not break away from the utility model spirit and scope, and these changes and improvements all fall in claimed the utility model scope.The claimed scope of the utility model is defined by appending claims and equivalent thereof.
Claims (4)
1. single-stage ammonia water absorbing refrigerator, comprise generator-rectifying column, condenser, gas-liquid separator, subcooler, evaporimeter, absorber, solution pump, solution heat exchanger, it is characterized in that, described generator-rectifying column top connects the condenser top by pipeline, the described condenser lower end export pipeline gas-liquid separator of flowing through successively, subcooler and evaporimeter are linked gas-liquid separator top, described gas-liquid separator bottom is connected to generator-rectifier by pipeline, on described this section pipeline solution pump is installed, described gas-liquid separator top is connected to absorber top by pipeline through subcooler, described absorber top is connected by pipeline with generator-rectifying column bottom, described this section pipeline solution heat exchanger of flowing through, described absorber bottom is connected to generator-rectifying column middle part by pipeline, on described this section pipeline solution pump is installed, and the solution heat exchanger of flowing through.
2. a kind of single-stage ammonia water absorbing refrigerator as claimed in claim 1 is characterized in that described gas-liquid separator bottom is provided with heat exchange coil.
3. a kind of single-stage ammonia water absorbing refrigerator as claimed in claim 1 is characterized in that, on the pipeline between described generator-rectifying column bottom and absorber top the solution choke valve is installed.
4. a kind of single-stage ammonia water absorbing refrigerator as claimed in claim 2 is characterized in that, described condenser lower end export pipeline is equipped with the solution choke valve in subcooler to this section of evaporimeter.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011201361530U CN202032783U (en) | 2011-05-03 | 2011-05-03 | Single-stage ammonia water absorption refrigerator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011201361530U CN202032783U (en) | 2011-05-03 | 2011-05-03 | Single-stage ammonia water absorption refrigerator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202032783U true CN202032783U (en) | 2011-11-09 |
Family
ID=44895077
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011201361530U Expired - Lifetime CN202032783U (en) | 2011-05-03 | 2011-05-03 | Single-stage ammonia water absorption refrigerator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202032783U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102135342A (en) * | 2011-05-03 | 2011-07-27 | 上海海事大学 | Single-stage ammonia absorbing refrigerating machine |
| CN104725238A (en) * | 2015-04-21 | 2015-06-24 | 江苏金凯树脂化工有限公司 | Device and process for recycling trimethylamine |
| CN114322354A (en) * | 2021-12-20 | 2022-04-12 | 安徽普泛能源技术有限公司 | Absorption type circulating refrigeration system and process thereof |
-
2011
- 2011-05-03 CN CN2011201361530U patent/CN202032783U/en not_active Expired - Lifetime
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102135342A (en) * | 2011-05-03 | 2011-07-27 | 上海海事大学 | Single-stage ammonia absorbing refrigerating machine |
| CN102135342B (en) * | 2011-05-03 | 2012-11-28 | 上海海事大学 | Single-stage ammonia absorbing refrigerating machine |
| CN104725238A (en) * | 2015-04-21 | 2015-06-24 | 江苏金凯树脂化工有限公司 | Device and process for recycling trimethylamine |
| CN114322354A (en) * | 2021-12-20 | 2022-04-12 | 安徽普泛能源技术有限公司 | Absorption type circulating refrigeration system and process thereof |
| CN114322354B (en) * | 2021-12-20 | 2023-07-28 | 安徽普泛能源技术有限公司 | Absorption type circulating refrigeration system and process thereof |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101603746B (en) | An adiabatic absorption refrigeration cycle device | |
| CN106766342A (en) | Ammonia still process column overhead ammonia vapour residual heat system is reclaimed using lithium bromide absorption type heat pump | |
| CN202032783U (en) | Single-stage ammonia water absorption refrigerator | |
| CN102135342B (en) | Single-stage ammonia absorbing refrigerating machine | |
| CN102679614B (en) | Solution self-cooled rectified ammonia water absorption refrigerating system | |
| CN101029783A (en) | Sodium sulfocyanate-ammonia diffusion absorbing refrigerator | |
| CN101915478B (en) | Ammonia water absorption refrigerating machine driven by marine exhaust | |
| CN203922754U (en) | A kind of ammonia synthesis and lithium bromide absorption chiller system | |
| CN103206806B (en) | The ammoniacal liquor thermal release system that waste heat drives | |
| CN207035587U (en) | A kind of freon dry evaporator distributor | |
| CN201724465U (en) | Lithium bromide absorbing refrigeration unit | |
| CN214141658U (en) | Waste water decrement treatment equipment | |
| CN106679243B (en) | Refrigerating system capable of reducing liquid ammonia consumption | |
| CN206546048U (en) | It is a kind of to reduce the refrigeration system of liquefied ammonia consumption | |
| CN202947376U (en) | High-efficient heat exchanger for low-temperature dichlorodifluoromethane unit | |
| CN105805978B (en) | Utilize the ammonia absorption type refrigeration circulatory system of internal thermally coupled distillation column | |
| CN201163118Y (en) | Novel refrigeration unit | |
| CN202403442U (en) | Small absorption refrigeration device | |
| CN202403445U (en) | Ejector refrigeration unit with evaporative condenser | |
| CN206320954U (en) | Ammonia still process column overhead ammonia vapour residual heat system is reclaimed using lithium bromide absorption type heat pump | |
| CN109297255A (en) | A kind of energy-saving gas ammonia compression process | |
| CN202229520U (en) | Device for cooling circulating system of ice maker | |
| CN217367848U (en) | Desorption system for regenerable amine process desulfurization | |
| CN202403443U (en) | Low-temperature thermally driven refrigerating device | |
| CN217383359U (en) | Absorption type refrigerating device for improving absorption effect by utilizing gas-liquid convection |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20111109 Effective date of abandoning: 20130227 |
|
| RGAV | Abandon patent right to avoid regrant |