CN202938560U - Two-phase flow liquid storage current stabilizer - Google Patents

Two-phase flow liquid storage current stabilizer Download PDF

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Publication number
CN202938560U
CN202938560U CN 201220694759 CN201220694759U CN202938560U CN 202938560 U CN202938560 U CN 202938560U CN 201220694759 CN201220694759 CN 201220694759 CN 201220694759 U CN201220694759 U CN 201220694759U CN 202938560 U CN202938560 U CN 202938560U
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CN
China
Prior art keywords
liquid
phase flow
gas
liquid storage
port
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Expired - Lifetime
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CN 201220694759
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Chinese (zh)
Inventor
祝长宇
丁式平
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Beijing Fulllink Oreith Technology Co ltd
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Beijing Deneng Hengxin Technology Co Ltd
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Priority to CN 201220694759 priority Critical patent/CN202938560U/en
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Abstract

The utility model provides a two-phase flow liquid storage current stabilizer which comprises a solution storage tank, an inflow end opening of refrigerating fluid, an outflow end opening of the refrigerating liquid, and a gas-liquid two-phase flow matching pipe which is arranged inside the solution storage tank. The solution storage tank is a high-pressure resistance sealing container, and a thermal insulating layer is arranged on the outer surface of the high-pressure resistance sealing container. Two externally-connected joints of the two-phase flow solution storage current stabilizer respectively are the inflow end opening of refrigerating fluid and an outflow end opening of the refrigerating liquid. The gas-liquid two-phase flow matching pipe is a straight pipe, and mainly comprises two end openings and a reflowing hole which is formed in the gas-liquid two-phase flow matching pipe. The two-phase flow solution storage current stabilizer has the functions of storing working medium, achieve gas-liquid separation of the working medium, reasonably allocate flow proportion of liquid working medium and gas working medium in a circulation loop, and form stable working medium in the circulation loop.

Description

A kind of two-phase flow liquid storage flow straightener
Technical field
The utility model relates to a kind of device for storing liquid, is specifically related to a kind of two-phase flow liquid storage flow straightener.
Background technology
Compress in mechanism cold circulation and heat pipe heat exchanging circulation in freezing and refrigeration, cryogenic refrigeration etc., fluid reservoir is one of refrigeration heat exchange annex of commonly using.Traditional liquid storage tank structure is simple, and performance is single, only has the liquid storage function.in actual refrigeration and heat exchange, whole system is in cyclic process, cold-producing medium can not be stable supply with adjusting according to the evaporimeter of system and the demand of condenser, reach refrigeration and heat exchange efficiency maximum, if can the circulation of cold-producing medium be a gas-liquid phase transition circulation in refrigeration or heat exchange circulation, refrigeration and heat exchange efficiency can improve a lot, therefore can seek a kind of mode or equipment, its liquid-working-medium in can the reasonable distribution closed circuit and the flow proportional of gas working dielectric, necessary to form stable working media two-phase flow in closed circuit.
Summary of the invention
The purpose of this utility model is to provide a kind of two-phase flow liquid storage flow straightener, solve the problems referred to above, not only can store working media, realize the gas-liquid separation of working media, liquid-working-medium in all right reasonable distribution closed circuit and the flow proportional of gas working dielectric are to form stable working media two-phase flow in closed circuit.
The utility model technical solution problem adopts following technical scheme:
A kind of two-phase flow liquid storage flow straightener, comprise fluid reservoir, cold-producing medium inflow port, cold-producing medium outflow port and be positioned at the gas-liquid two-phase flow pipe of fluid reservoir inside; Described fluid reservoir is the high-pressure-resistant sealed container that an outer surface is provided with thermal insulation layer; Two external interfaces of described two-phase flow liquid storage flow straightener are respectively the inflow port of cold-producing medium and the outflow port of cold-producing medium; Described gas-liquid two-phase flow pipe is a straight tube, and it mainly is made of two ports and the return port that is positioned on gas-liquid two-phase flow pipe; A port of described gas-liquid two-phase flow pipe is connected in the cold-producing medium outflow port of described two-phase flow liquid storage flow straightener, and its another port is in the liquid level bottom of liquid refrigeration working medium in two-phase flow liquid storage flow straightener; The return port of described gas-liquid two-phase flow pipe is in the liquid level top of liquid refrigeration working medium in two-phase flow liquid storage flow straightener.
The quantity of the return port mesopore of the above gas-liquid two-phase flow pipe is a hole, or highly different a plurality of holes.
The return port of the above gas-liquid two-phase flow pipe be one along the backflow of duct orientation seam, it substitutes the effect of a plurality of return ports that distribute along the pipeline throughput direction.
The a small amount of gaseous state that flows in the above return port or the seam that refluxes or the flow of liquid refrigerant have its pore size and number or gap width and length to control, and namely the liquid refrigerant liquid level is just controlled the length of the number in the hole in return port or the seam that refluxes in two-phase flow liquid storage flow straightener.
the utility model compared with prior art, simple for general liquid storage tank structure, performance is single, only has the liquid storage function, and the design by two-phase flow liquid storage flow straightener, two-phase flow liquid storage flow straightener not only can store working media, realize the gas-liquid separation of working media, liquid-working-medium in simultaneously can the reasonable distribution closed circuit and the flow proportional of gas working dielectric, to form stable working media two-phase flow in closed circuit, operating efficiency and the practicality of refrigeration or heat-exchange system have been improved, and realized the stability of whole system circulation.
Description of drawings
Fig. 1 is the structural representation of two-phase flow liquid storage flow straightener.
Fig. 2 is the planar structure schematic diagram of the return port of two-phase flow pipe and the seam that refluxes.
Fig. 3 is the use principle figure of two-phase flow liquid storage flow straightener.
In figure: (1) fluid reservoir; (2) the inflow port of the cold-producing medium of two-phase flow liquid storage flow straightener; (3) outflow port of the cold-producing medium of two-phase flow liquid storage flow straightener; (4) gas-liquid two-phase flow pipe; (41) return port on gas-liquid two-phase flow pipe; (42) ~ (43) two ports of gas-liquid two-phase flow pipe; (44) backflow seam; (5) circulating pump; (6) evaporimeter; (7) condenser.
The specific embodiment:
Also be described further by reference to the accompanying drawings below by embodiment:
the system and device agent structure that relates to when the present embodiment is realized comprises fluid reservoir (1), the inflow port (2) of the cold-producing medium of two-phase flow liquid storage flow straightener, the outflow port (3) of the cold-producing medium of two-phase flow liquid storage flow straightener, gas-liquid two-phase flow pipe (4), return port (41) on gas-liquid two-phase flow pipe, two ports (42) ~ (43) of gas-liquid two-phase flow pipe, seam (44) refluxes, circulating pump (5), evaporimeter (6), condenser (7) and the gas-liquid delivery pipe that is communicated with demand.
A kind of two-phase flow liquid storage flow straightener as shown in Figure 1, comprise the cold-producing medium of fluid reservoir (1), two-phase flow liquid storage flow straightener inflow port (2), two-phase flow liquid storage flow straightener cold-producing medium outflow port (3) and be positioned at the gas-liquid two-phase flow pipe system (4) of fluid reservoir inside; Described fluid reservoir (1) is the high-pressure-resistant sealed container that an outer surface is provided with thermal insulation layer; Two external ports (2 that connect of described two-phase flow liquid storage flow straightener; 3), be respectively the outflow port (3) of inflow port (2) and the cold-producing medium of cold-producing medium; Described gas-liquid two-phase flow pipe (4) is a straight tube, and it is mainly by two ports (42; 43) and the return port (41) that is positioned on gas-liquid two-phase flow pipe consist of; A port (43) of described gas-liquid two-phase flow pipe (4) is connected in the cold-producing medium outflow port (3) of described two-phase flow liquid storage flow straightener, and its another port (42) is in the liquid level bottom of liquid refrigeration working medium in two-phase flow liquid storage flow straightener; The return port (41) of described gas-liquid two-phase flow pipe (4) is in the liquid level top of liquid refrigeration working medium in two-phase flow liquid storage flow straightener; Cold-producing medium enters in fluid reservoir (4) from the inflow port (2) of the cold-producing medium of two-phase flow liquid storage flow straightener like this, gas-liquid refrigeration intermediate medium basis physical property is separately separated in fluid reservoir (4), then gas-liquid refrigeration intermediate medium is through the effect of gas-liquid two-phase flow pipe (4), liquid-working-medium in the reasonable distribution closed circuit and the flow proportional of gas working dielectric, outflow port (3) through the cold-producing medium of two-phase flow liquid storage flow straightener is transported in systemic circulation, like this to form stable working media two-phase flow in closed circuit.
Embodiment one:
the use principle figure of two-phase flow liquid storage flow straightener as shown in Figure 3, comprise circulating pump (5), evaporimeter (6), condenser (7), two-phase flow liquid storage flow straightener and link pipeline, described circulating pump (5), evaporimeter (6), condenser (7) and two-phase flow liquid storage flow straightener link by mutual connecting pipe according to said sequence and have just formed a two-phase flow power heat pipe circulatory system, during described two-phase flow power heat pipe circulatory system work, circulating pump (5) is from the interior a small amount of gaseous state refrigeration working medium that extracts a large amount of liquid refrigeration working medium and replenish whole stable circulation by the part of return port (41) of the fluid reservoir (1) of two-phase flow liquid storage flow straightener, enter evaporimeter (6) through the evaporimeter catheter, evaporimeter (6) contacts with high temperature heat source, liquid working media is subjected to the heating of high temperature heat source and is evaporated to gas in evaporimeter (6), and absorption heat, the gas that evaporation forms does not have the liquid intermediate medium of evaporation mutually to mix formation gas-liquid two-phase flow body in flow at high speed with part, they are delivered to condenser (7) through the two-phase flow pipe, condenser (7) contacts with low-temperature heat source, gaseous working medium is subjected to the cooling of low-temperature heat source and is condensed into liquid in condenser (7), and emit heat, the liquid-working-medium that condensation forms enters in the fluid reservoir (1) of two-phase flow liquid storage flow straightener through the condenser catheter, it carries out gas-liquid separation, then gas-liquid refrigeration intermediate medium is through the effect of gas-liquid two-phase flow pipe (4), liquid-working-medium in the reasonable distribution closed circuit and the flow proportional of gas working dielectric, so just can form stable working media two-phase flow in the closed circuit of the described two-phase flow power heat pipe circulatory system, improved the operating efficiency of whole system.

Claims (4)

1. a two-phase flow liquid storage flow straightener, comprise a fluid reservoir (1) and two external-connected ports (2; 3), it is characterized in that, also comprise the gas-liquid two-phase flow pipe (4) that is positioned at fluid reservoir inside; Described fluid reservoir (1) is the high-pressure-resistant sealed container that an outer surface is provided with thermal insulation layer; Two external ports (2 that connect of described two-phase flow liquid storage flow straightener; 3), be respectively the outflow port (3) of inflow port (2) and the cold-producing medium of cold-producing medium; Described gas-liquid two-phase flow pipe (4) is a straight tube, and it is mainly by two ports (42; 43) and the return port (41) that is positioned on gas-liquid two-phase flow pipe consist of; A port (43) of described gas-liquid two-phase flow pipe (4) is connected in the cold-producing medium outflow port (3) of described two-phase flow liquid storage flow straightener, and its another port (42) is in the liquid level bottom of liquid refrigeration working medium in two-phase flow liquid storage flow straightener; The return port (41) of described gas-liquid two-phase flow pipe (4) is in the liquid level top of liquid refrigeration working medium in two-phase flow liquid storage flow straightener.
2. a kind of two-phase flow liquid storage flow straightener according to claim 1, is characterized in that, the quantity of return port (41) mesopore of described gas-liquid two-phase flow pipe (4) is a hole, or highly different a plurality of holes.
3. a kind of two-phase flow liquid storage flow straightener according to claim 1, it is characterized in that, the return port (41) of described gas-liquid two-phase flow pipe (4) be one along the backflow of duct orientation seam (44), it substitutes the effect of a plurality of return ports that distribute along the pipeline throughput direction.
4. according to claim 2 or 3 described a kind of two-phase flow liquid storage flow straighteners, it is characterized in that, the a small amount of gaseous state that flows in described return port (41) or the seam (44) that refluxes or the flow of liquid refrigerant have its pore size and number or gap width and length to control, and namely the liquid refrigerant liquid level is just controlled the length of the number in the hole in return port or the seam that refluxes in two-phase flow liquid storage flow straightener.
CN 201220694759 2012-12-17 2012-12-17 Two-phase flow liquid storage current stabilizer Expired - Lifetime CN202938560U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 201220694759 CN202938560U (en) 2012-12-17 2012-12-17 Two-phase flow liquid storage current stabilizer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 201220694759 CN202938560U (en) 2012-12-17 2012-12-17 Two-phase flow liquid storage current stabilizer

Publications (1)

Publication Number Publication Date
CN202938560U true CN202938560U (en) 2013-05-15

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN 201220694759 Expired - Lifetime CN202938560U (en) 2012-12-17 2012-12-17 Two-phase flow liquid storage current stabilizer

Country Status (1)

Country Link
CN (1) CN202938560U (en)

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C14 Grant of patent or utility model
GR01 Patent grant
C56 Change in the name or address of the patentee
CP03 Change of name, title or address

Address after: 100020 Chaoyang District City, Chaoyang Street, No. 15, floor 1518, unit 18,

Patentee after: BEIJING FULLLINK OREITH TECHNOLOGY Co.,Ltd.

Address before: 100041 Beijing, Badachu hi tech park, West Wells Road, building 9415, room 3, No., room 3

Patentee before: BEIJING DENENG HENGXIN SCIENCE AND TECHNOLOGY Co.,Ltd.

CX01 Expiry of patent term
CX01 Expiry of patent term

Granted publication date: 20130515