[go: up one dir, main page]

CN1178036C - Generator structure for absorption-diffusion type refrigerating device - Google Patents

Generator structure for absorption-diffusion type refrigerating device Download PDF

Info

Publication number
CN1178036C
CN1178036C CNB011184892A CN01118489A CN1178036C CN 1178036 C CN1178036 C CN 1178036C CN B011184892 A CNB011184892 A CN B011184892A CN 01118489 A CN01118489 A CN 01118489A CN 1178036 C CN1178036 C CN 1178036C
Authority
CN
China
Prior art keywords
pipe
ammonia solution
generator
double
absorption
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 - Fee Related
Application number
CNB011184892A
Other languages
Chinese (zh)
Other versions
CN1389690A (en
Inventor
豪 白
白豪
詹儒和
郭晋宏
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.)
Thermal Energy Sci Tech Development Co ltd
Original Assignee
Thermal Energy Sci Tech Development 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 Thermal Energy Sci Tech Development Co ltd filed Critical Thermal Energy Sci Tech Development Co ltd
Priority to CNB011184892A priority Critical patent/CN1178036C/en
Publication of CN1389690A publication Critical patent/CN1389690A/en
Application granted granted Critical
Publication of CN1178036C publication Critical patent/CN1178036C/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A30/00Adapting or protecting infrastructure or their operation
    • Y02A30/27Relating to heating, ventilation or air conditioning [HVAC] technologies
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02BCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00Energy efficient heating, ventilation or air conditioning [HVAC]
    • Y02B30/62Absorption based systems

Landscapes

  • Sorption Type Refrigeration Machines (AREA)

Abstract

A generator structure used for absorbing the diffusion type refrigerating plant, it includes heating device, double-pipe and heat conduction bush locating between inside and outside pipe of the double-pipe located in heating device, the inside pipe of the double-pipe is a concentrated aqueous ammonia solution pipe, and the outside pipe is a dilute aqueous ammonia solution pipe; the heating device heats the double sleeves so that the concentrated ammonia water solution in the inner pipe releases ammonia gas to form bubble flow due to heating, and the heat conduction sleeve is used for reducing the heat resistance between the inner pipe and the outer pipe so as to reduce the temperature for activating the bubbles of the generator.

Description

Be used in the generator architecture of absorption-diffusion type refrigerator
The present invention relates to a kind of generator architecture that is used in absorption-diffusion type refrigerator, particularly relate to a kind of utilization heat conduction sleeve,, and then reduce the innovation structure of steam bubble activationary temperature so that reduce the thermal resistance between inner and outer pipe.
General ammonia absorption type freeze cycle and the difference of compression freeze cycle are the different of mode that it finishes compression, promptly in absorption freezing circulation, after its low pressure ammonia steam is absorbed by water, and with hydraulic pump with this liquid solution pump to high pressure.As shown in Figure 1, it is the action flow chart of ammonia absorption type freeze cycle, and at first low pressure ammonia steam leaves behind the evaporimeter and enters absorber, and is absorbed by dilute ammonia solution in it, this process is a little more than carrying out under the ambient temperature, so wherein must there be heat to reach the external world in temperature; Moreover, with the concentrated ammonia solution of gained with pump through a heat exchanger, and pump is to the generator that remains under the high pressure-temperature, thus, the high temperature heat source in this generator import heat into, and make ammonia steam be evaporated out by concentrated ammonia solution, and flow to the formation liquid ammonia that condenses in the condenser, and enter evaporimeter, then return in the absorber by the dilute ammonia solution that this generator produced in addition, to finish an absorption freezing circulation through over-heat-exchanger.
In addition, in refrigerating circulation system, for the waste that prevents that energy loss from causing, there is the design of various pipeline in regular meeting, and as design of two sleeve pipes (or double pipe) etc., and this pair sleeve pipe is the thermal treatment zone that can be applicable to generator, so that have more complete heat exchange; But the interior pipe of this pair sleeve pipe is to be concentrated ammonia liquor liquation pipe, promptly because of heat pass to need by managing in the outer tube indirect, therefore, if the concentrated ammonia solution generation vapour of pipe in wanting to make, when liquid separates certainly will be heated to suitable high temperature so that activate the generation of steam bubble; Therefore, this generator need provide sizable external energy so as to producing high temperature, it not only increases whole power consumption, and also be restricted (for example can't adopt in generally can producing, the fuel cell and the general used heat of low temperature, so also can't be implemented on small-sized refrigerator etc.) in the design application facet; As seen, on reality is used, obviously have inconvenience and have defective, and demand urgently being improved.
The object of the present invention is to provide a kind of generator architecture that is used in absorption-diffusion type refrigerator, to overcome the existing in prior technology defective.
The object of the present invention is achieved like this: a kind of generator architecture that is used in absorption-diffusion type refrigerator, its key is, includes two sleeve pipes and that a heater, is positioned at this heater and is located at heat conduction sleeve between the inner and outer pipe of this pair sleeve pipe; It has complete heat exchange, and can reduce the thermal resistance between inner and outer pipe, and then reduces the steam bubble activationary temperature of generator.
The described generator architecture that is used in absorption-diffusion type refrigerator, wherein the interior pipe of this pair sleeve pipe is to be the concentrated ammonia solution pipe, outer tube then is the dilute ammonia solution pipe.
The described generator architecture that is used in absorption-diffusion type refrigerator wherein should heat conduction sleeve surface can offer plural groove.
This shows, the invention provides a kind of generator architecture that is used in absorption-diffusion type refrigerator, it includes two sleeve pipes and that a heater, is positioned at this heater and is located at heat conduction sleeve between the inner and outer pipe of this pair sleeve pipe, wherein, the interior pipe of this pair sleeve pipe is to spill pipe for concentrated ammonia liquor is molten, outer tube then is the dilute ammonia solution pipe, and should heat conduction sleeve surface be to offer plural groove, and the dilute ammonia solution that is beneficial to outer tube passes through; In view of the above,, can have more complete heat exchange, and utilize this heat conduction sleeve to be reduced thermal resistance between inner and outer pipe, and then reduce the steam bubble activationary temperature of generator by heating this pair sleeve pipe.
Below in conjunction with embodiment and accompanying drawing thereof, feature of the present invention and technology contents are described in further detail, yet shown in accompanying drawing only provide with reference to and the explanation usefulness, be not to be used for the present invention is limited.
Fig. 1 is the action flow chart of general ammonia absorption type freeze cycle;
Fig. 2 is the enforcement state diagram of generator architecture of the present invention;
Fig. 3 is the side cut away view of generator architecture of the present invention;
Fig. 4 is the cross-section cutaway view of the B-B part of Fig. 3;
Fig. 5 is the cross-section cutaway view of the C-C part of Fig. 3.
The present invention provides a kind of generator architecture that is used in absorption-diffusion type refrigerator, wherein, this absorption-diffusion type refrigerator (as shown in Figure 2) is to comprise a dense ammonia water trough 1, a generator 2, a vapor-liquid separating device 3, a condenser 4, an evaporimeter (figure slightly), an absorber 5, and necessary pipeline 6 is formed with control device members such as (figure slightly).
This refrigerating plant is as refrigerant agent with ammonia, and the concentration by ammoniacal liquor can be divided into concentrated ammonia solution and dilute ammonia solution, the cooling action specification of this refrigerating plant is as follows: at first, the concentrated ammonia solution 70 that flows out from this dense ammonia water trough 1 is heated by this generator 2, and rising along with temperature, produce steam bubble so that make this concentrated ammonia solution 70 begin vaporization, and isolate dilute ammonia solution 71 and ammonia steam 72; Wherein, 72 of this ammonia steam enter this condenser 4 and give condensation, so that make this ammonia steam 72 ammonia liquid 73 of freeze-outing, then this ammonia liquid 73 promptly enters this evaporimeter (figure slightly), and make this ammonia liquid 73 be evaporated into ammonia (figure slightly), and the hydrogen (figure slightly) that this ammonia (figure slightly) is with this absorber 5 certainly flows out mixes, flows back into this dense ammonia water trough 1 so that form mixing ammonia and hydrogen 74.
In addition, the dilute ammonia solution 71 that above-mentioned generator 2 is separated is to enter this absorber 5, the dilute ammonia solution 71 of this absorber 5 be can with mix ammonia and hydrogen 74 mutual absorptions by this absorber 5, so that this dilute ammonia solution 71 is absorbed gradually become concentrated ammonia solution 70 and flows back to this dense ammonia water trough 1, in addition the mixing ammonia by this absorber 5 also is absorbed with hydrogen 74 and gradually becomes hydrogen (figure slightly) to enter this evaporimeter (figure omits), so as to finishing the motion flow of a freeze cycle.
In view of the above, the present invention's generator of being primarily aimed at above-mentioned absorption-diffusion type refrigerator is designed; Please consult Fig. 2 and shown in Figure 3 simultaneously, the concentrated ammonia solution 70 that flows out from this dense ammonia water trough 1 promptly flows into a concentrated ammonia solution pipe 20, this concentrated ammonia solution pipe 20 is to be socketed on a dilute ammonia solution pipe 21 interior (as shown in Figure 4) and to form two sleeve pipes with coaxial manner, and this concentrated ammonia solution pipe 20 is to be connected in these vapor-liquid separating device 3 places with this dilute ammonia solution pipe 21, also be, 70 of concentrated ammonia solutions by this generator 2 are separated into dilute ammonia solution 71 and ammonia steam 72, and when both flow to these vapor-liquid separating device 3 places, this ammonia steam 72 can up flow to this condenser 4, and this dilute ammonia solution 71 then down refluxes and enters in this dilute ammonia solution pipe 21.
In addition, this generator 2 is to utilize a heater 22 to be heated by this is dense, dilute ammonia solution pipe 20, concentrated ammonia solution 70 and dilute ammonia solution 71 in 21, and make this concentrated ammonia solution 70 be separated into dilute ammonia solution 71 and ammonia steam 72, and dense in heating place, dilute ammonia solution pipe 20,21 are equipped with a heat conduction sleeve 23, the surface of this heat conduction sleeve 23 is to offer plural groove 230, pass through in order to the dilute ammonia solution 71 in this dilute ammonia solution pipe 21, and should heat conduction sleeve 23 be to reduce that this is dense, dilute ammonia solution pipe 20,21 thermal resistance, and then the bubble activationary temperature of reduction generator.
In sum, the generator architecture that is to use in absorption-diffusion type refrigerator disclosed in this invention, it mainly utilizes a heat conduction sleeve, can make generator in, low temperature just can reach the effect that vapour, liquid separate.
But; the above only is a preferable possible embodiments of the present invention, is not so limits protection scope of the present invention, so the equivalent structure that every utilization specification of the present invention and accompanying drawing content are carried out changes; all be contained in the determined protection domain of claim of the present invention, close and give Chen Ming.

Claims (1)

1、一种使用于吸收扩散式冷冻装置的发生器结构,其特征在于,包括有一加热装置、一位于该加热装置旁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液管,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,据此,通过加热该双套管,即可具有完整的热交换,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。1. A generator structure used in an absorption-diffusion refrigeration device, characterized in that it includes a heating device, a double casing positioned next to the heating device, and an inner and outer tube of the double casing. The heat conduction sleeve, wherein, the inner tube of the double sleeve is a concentrated ammonia solution tube, and the outer tube is a dilute ammonia solution tube, and the surface of the heat conduction sleeve is provided with multiple grooves. Accordingly, by heating the double The casing can have complete heat exchange, and can reduce the thermal resistance between the inner and outer tubes, thereby reducing the bubble activation temperature of the generator.
CNB011184892A 2001-06-01 2001-06-01 Generator structure for absorption-diffusion type refrigerating device Expired - Fee Related CN1178036C (en)

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

Publications (2)

Publication Number Publication Date
CN1389690A CN1389690A (en) 2003-01-08
CN1178036C true CN1178036C (en) 2004-12-01

Family

ID=4663227

Family Applications (1)

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

Country Status (1)

Country Link
CN (1) CN1178036C (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
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

Also Published As

Publication number Publication date
CN1389690A (en) 2003-01-08

Similar Documents

Publication Publication Date Title
CN101344345B (en) Compression-absorption-diffusion combined refrigerating plant and its refrigeration cycle method
CN102052799A (en) Device for producing low-temperature water by using waste heat
CN105674616B (en) A kind of absorption type refrigeration circulating system of membrane distillation concentration lithium-bromide solution
CN101876496B (en) Double-evaporator direct-fired absorption refrigerating and heating unit
EP0588943A1 (en) Regenerative absorption cycles with multiple stage absorber
CN101413739A (en) Double-effect heat pump circulation three-effect heat exchanger
KR101225843B1 (en) Absorption Type Cooler and Heater
CN1260536C (en) Absorbing refrigerator
CN103807946B (en) The rectification regenerating unit of heat source tower anti-freezing solution
CN101603745A (en) A pressurized absorption self-cascading absorption refrigeration cycle system
CN1178036C (en) Generator structure for absorption-diffusion type refrigerating device
CN101000180A (en) Two-stage and multistage absorption refrigeration machine
CN108507219A (en) A kind of compound two-stage type lithium bromide absorption type heat pump and working method
CN207741379U (en) A kind of absorption deep refrigerating system of industrial waste heat driving
JPS5886357A (en) Air-conditioning method utilizing solar heat and its device
CN201161936Y (en) Desalination system
CN204630143U (en) Two-period form dual effect type lithium bromide absorbing type refrigeration/heating machine set
CN204630144U (en) Dual circulation absorbs dual effect type lithium bromide absorbing type refrigeration/heating machine set
CN203375765U (en) Absorption heat pump unit
CN101886855A (en) Pressure-and-suction type refrigerating system
JPH05332633A (en) Composite freezer device
CN204923556U (en) Steam - direct combustion dual intensity source integration central cooling system
CN217715521U (en) Generator with U-shaped pipe
CN2814262Y (en) Lithium bromide suction type cooling water and warming water machine set
KR200288609Y1 (en) Ammonia absorbtion- type refrigerator

Legal Events

Date Code Title Description
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20041201

Termination date: 20110601