CN201028896Y - Spraying liquid storage type heat converter - Google Patents

Spraying liquid storage type heat converter Download PDF

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Publication number
CN201028896Y
CN201028896Y CNU2006200475162U CN200620047516U CN201028896Y CN 201028896 Y CN201028896 Y CN 201028896Y CN U2006200475162 U CNU2006200475162 U CN U2006200475162U CN 200620047516 U CN200620047516 U CN 200620047516U CN 201028896 Y CN201028896 Y CN 201028896Y
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CN
China
Prior art keywords
utility
fluid
model
cryogen
tube bank
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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
CNU2006200475162U
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Chinese (zh)
Inventor
特拉维斯
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ASIA TECHLINK ENERGY SAVING EQUIPMENT Co Ltd
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ASIA TECHLINK ENERGY SAVING EQUIPMENT Co Ltd
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Priority to CNU2006200475162U priority Critical patent/CN201028896Y/en
Application granted granted Critical
Publication of CN201028896Y publication Critical patent/CN201028896Y/en
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Expired - Fee Related legal-status Critical Current

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Abstract

The utility model discloses a spraying and liquid storing type heat exchanger structure for a hot pump system, which comprises a casing, a pipe bunch, a fluid A entrance, a fluid A exit, a cryogen entrance and a cryogen exit. The utility model is characterized in that the entrance and the exit of the fluid A are connected to the pipe bunch in the casing, thus forming a fluid channel in the pipe bunch; the entrance and the exit of the cryogen are positioned on the wall of the casing, thus forming a cryogen channel outside of the pipe bunch; the bottom of the casing has an oil returning mouth; and the upper part of the pipe bunch has a cryogen allotter. Thus the utility model has the beneficial effects that the utility model can be used as an evaporator when in refrigeration and as a condenser when produce heat; a liquid storing machine is removed from the hot pump system, thus realizing a machine with multi functions, so as to enhance performance, reduce the quantity of cryogen and lower cost.

Description

Spray water storage type heat exchanger
Technical field
The utility model belongs to the refrigeration and air-conditioning technical field, is specifically related to a kind of spray water storage type heat exchanger that can be used for handpiece Water Chilling Units and heat pump.
Background technology
Mainly contain four critical pieces in the heat pump, two heat exchangers (evaporimeter and condenser), a compressor and an expansion valve.Direct expansion formula evaporimeter is widely used in the heat pump, its reason is that the advantage of direct expansion formula evaporimeter is both to have can be used as evaporimeter, can be used as condenser again, but direct expansion formula evaporimeter heat transfer property is poor, also needs a reservoir to store cold-producing medium unnecessary when heating.Thereby flooded evaporator replaced direct expansion formula evaporimeter gradually in large-scale handpiece Water Chilling Units, thereby improved heat transfer property greatly.But the shortcoming of flooded evaporator is: can not be used as condenser and full-liquid type and also need a large amount of cold-producing mediums, cost height, Heavy Weight in the heating mode purposes.
The utility model content
The purpose of this utility model provides a kind of spray water storage type heat exchanger that is used for heat pump, both can as condenser, can omit the reservoir that adds again when heating as evaporimeter when refrigeration.
For achieving the above object, the technical solution adopted in the utility model is: spray water storage type heat exchanger, comprise housing, place the tube bank in the housing, the import of fluid and outlet, the import of cold-producing medium and outlet, it is characterized in that: the tube bank in the import of fluid and outlet and the described housing connects to form the tube bank fluid passage, place the import and the outlet of the cold-producing medium on the housing, in described housing, form coolant channel outside the tube bank, be equipped with liquid refrigerant outlet and oil return opening in the bottom of described housing.Be in the chamber of described housing that the top of described tube bank also can be equipped with refrigerant distributor.
The beneficial effects of the utility model are: the utility model is in heat pump applications, not only can when freezing, be used as evaporimeter but also can when heating, be used as condenser, the cold-producing medium consumption that the utility model needs is few, self can store cold-producing medium unnecessary when heating, therefore can cancel the reservoir that adds in the heat pump, realized one-object-many-purposes, improved performance and reduce cost.The utility model also can be made evaporimeter and use in handpiece Water Chilling Units.
Description of drawings
The utility model is described in further detail below in conjunction with drawings and Examples.
Fig. 1 is the utility model structural representation;
Fig. 2 is the A-A profile of Fig. 1;
Fig. 3 is that the utility model is made evaporimeter time spent fundamental diagram;
Fig. 4 is that the utility model is made condenser time spent fundamental diagram.
Among the figure: the 1-housing; The outlet of 2-gaseous refrigerant (evaporimeter) or import (condenser); The 3-fluid inlet; The 4-oil return opening; The 5-liquid refrigerant outlet; The 6-fluid issuing; The 7-refrigerant inlet; The 8-tube bank; The 9-refrigerant distributor.
The specific embodiment
Fig. 1, Fig. 2 is the utility model structural representation, diagram spray water storage type heat exchanger, comprise housing 1, place the tube bank 8 in the housing 1, fluid inlet 3 and outlet 6, the import 7 of liquid refrigerant and outlet (evaporimeter) 2 or the import (condenser) of gaseous refrigerant, it is characterized in that: the tube bank 8 in the import 3 of fluid and outlet 6 and the described housing 1 connects to form tube bank 8 fluid passage, the import 7 of cold-producing medium and the outlet 2 of gaseous refrigerant when making evaporimeter, make the import 2 of condenser time spent gaseous refrigerant and the shell wall that liquid refrigerant outlet 5 places housing 1, in described housing 1, form coolant channel outside the tube bank 8, be equipped with oil return opening 4 in the bottom of described housing 1.In the chamber of described housing 1, the top of described tube bank 8 also can be equipped with refrigerant distributor 9.During the work operation, the fluid of uniform temperature, in the tube bank 8 in fluid inlet 3 inflow heat exchanger housings 1, cold-producing medium enters in the heat exchanger shell 1 from refrigerant inlet 7, fluid and cold-producing medium are by the tube wall heat exchange of tube bank 8, fluid flows out from exporting 6 subsequently, and cold-producing medium is from exporting 2 or 5 outflow heat exchangers.
Fig. 3 is that the utility model is made evaporimeter time spent fundamental diagram (refrigeration), after the cold-producing medium that liquid state or gas-liquid two-phase mix enters heat exchanger inlets 7, be evenly distributed to above the tube bank 8 through distributor 9, liquid refrigerant is after tube bank 8 surfaces are by gasification, and upwards flowing arrives gas vent 2.The unevaporated refrigerant liquid of part flows to the bottom of housing 1, does pond attitude boiling after being heated, and upwards flows and arrive gas vent 2 in the gasification back.Parts of lubricating oil after the purification is got back to system from oil return opening 4.
Fig. 4 is that the utility model is made condenser time spent fundamental diagram (heating).After gaseous refrigerant entered heat exchanger inlets 2, gas was at tube bank 8 surface condensations.Condensed refrigerant liquid drops onto lower housing portion, flows out from liquid refrigerant outlet 5 then.Because the demand of filling quantity of refrigerant when heating is few when freezing, so unnecessary cold-producing medium can be stored at bottom in the water storage type heat exchanger shell 1 of the present invention when heating.
The utility model not only can be used as evaporimeter but also can be used as condenser when heating when freezing, spray water storage type heat exchanger has been realized one-object-many-purposes, has improved performance and has reduced cost.

Claims (2)

1. spray the water storage type heat exchanger, comprise housing (1), place the tube bank (8) in the housing (1), the import of fluid A (3) and outlet (6), the import of cold-producing medium (7) with advance, outlet (2), it is characterized in that: fluid inlet (3) connects to form the fluid passage with the tube bank (8) that exports in (6) and the described housing (1), the import of cold-producing medium (7) and advancing, outlet (2) is connected with described housing (1), form in the housing (1), tube bank (8) outer refrigerant circulation passage is equipped with liquid refrigerant outlet (5) and oil return opening (4) in the bottom of described housing (1).
2. spray water storage type heat exchanger according to claim 1 is characterized in that in the chamber of described housing (1), and the top of described tube bank (8) is equipped with refrigerant distributor (9).
CNU2006200475162U 2006-11-03 2006-11-03 Spraying liquid storage type heat converter Expired - Fee Related CN201028896Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNU2006200475162U CN201028896Y (en) 2006-11-03 2006-11-03 Spraying liquid storage type heat converter

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNU2006200475162U CN201028896Y (en) 2006-11-03 2006-11-03 Spraying liquid storage type heat converter

Publications (1)

Publication Number Publication Date
CN201028896Y true CN201028896Y (en) 2008-02-27

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Family Applications (1)

Application Number Title Priority Date Filing Date
CNU2006200475162U Expired - Fee Related CN201028896Y (en) 2006-11-03 2006-11-03 Spraying liquid storage type heat converter

Country Status (1)

Country Link
CN (1) CN201028896Y (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102878724A (en) * 2012-10-19 2013-01-16 哈尔滨工业大学 Water and refrigerant heat exchanger with evaporative heat exchange and condensing heat exchange functions
CN103322732A (en) * 2013-07-16 2013-09-25 方真健 Spray type heat exchanger for heat pump
CN105987542A (en) * 2016-01-29 2016-10-05 四川同达博尔置业有限公司 Heat exchanger unit
CN106766392A (en) * 2016-11-22 2017-05-31 罗众锋 One kind spray tank-type heat exchanger and its application method
CN109269132A (en) * 2018-07-16 2019-01-25 同济大学 A kind of mixed working fluid compression circulatory system of carrying liqs boost-up circuit
CN114459263A (en) * 2020-10-21 2022-05-10 中国石油化工股份有限公司 Heat exchanger, butylene oxidative dehydrogenation device and method for preparing butadiene through butylene oxidative dehydrogenation

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102878724A (en) * 2012-10-19 2013-01-16 哈尔滨工业大学 Water and refrigerant heat exchanger with evaporative heat exchange and condensing heat exchange functions
CN103322732A (en) * 2013-07-16 2013-09-25 方真健 Spray type heat exchanger for heat pump
CN103322732B (en) * 2013-07-16 2016-01-20 方真健 Spray type heat exchanger for heat pump
CN105987542A (en) * 2016-01-29 2016-10-05 四川同达博尔置业有限公司 Heat exchanger unit
CN106766392A (en) * 2016-11-22 2017-05-31 罗众锋 One kind spray tank-type heat exchanger and its application method
CN106766392B (en) * 2016-11-22 2023-11-07 营口庆营石油化工设备有限公司 Spray tank type heat exchanger and use method thereof
CN109269132A (en) * 2018-07-16 2019-01-25 同济大学 A kind of mixed working fluid compression circulatory system of carrying liqs boost-up circuit
CN114459263A (en) * 2020-10-21 2022-05-10 中国石油化工股份有限公司 Heat exchanger, butylene oxidative dehydrogenation device and method for preparing butadiene through butylene oxidative dehydrogenation
CN114459263B (en) * 2020-10-21 2023-08-29 中国石油化工股份有限公司 Heat exchanger, butene oxidative dehydrogenation device and method for preparing butadiene by butene oxidative dehydrogenation

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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: 20080227

Termination date: 20091203