CN205119914U - Liquid system is divided to low pressure - Google Patents
Liquid system is divided to low pressure Download PDFInfo
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- CN205119914U CN205119914U CN201520939236.1U CN201520939236U CN205119914U CN 205119914 U CN205119914 U CN 205119914U CN 201520939236 U CN201520939236 U CN 201520939236U CN 205119914 U CN205119914 U CN 205119914U
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- pipeline
- pipe
- heat collector
- low pressure
- liquid
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Abstract
The utility model relates to a liquid system is divided to low pressure relates to the technical field of medium pipe overall arrangement, has solved present heat utilization equipment middle and low voltage liquid medium and has divided liquid even for making, causes the pipeline too fat to move, technical problem that the equipment thermal efficiency is low. The utility model discloses a feed liquor pipe and outlet duct, characterized by the feed liquor pipe be divided into two the intercommunication two isometric branch liquid pipes, branch liquid pipe respectively through a plurality of hot plates that gather of equidistance pipeline intercommunication, the junction symmetry setting of gathering the relative feed liquor guan yufen liquid of hot plate connector pipe on the bipartition liquid pipe, respectively gather the hot plate respectively through equidistance pipeline intercommunication outlet duct and connector equidistance on the outlet duct arrange. The utility model discloses a tee bend point that uses feed liquor pipe and divide the liquid pipe is basic point, pipeline symmetrical arrangement for each work efficiency who gathers the hot plate is close, and the medium energy storage is even, and save the pipeline, and simple to operate, and the pipeline overall arrangement is beautifully spent quantity high and that gather the hot plate and can be adjusted in a flexible way.
Description
Technical field
The utility model relates to the technical field of medium pipeline layout, particularly one and is applicable to heat utilization equipment medium pipeline low pressure liquid separation system.
Background technology
Existing high-power heat utilization equipment often has multiple heat collector panel, in order to allow medium pipeline equilibrium shunting, promote the operating efficiency of each heat collector panel, most employing is in parallel by pipeline by heat collector panel, and each heat collector panel is consistent to the length of pipe that general export is used from medium general import, the method can cause near always entering, the heat collector panel of outlet needs with a lot pipeline of white many layouts, especially when the single installation of polylith heat collector panel, this separatory mode can make engineering seem too too fat to move, very unsightly, cause the energy dissipation of medium in pipeline simultaneously, heat collector panel operating efficiency height is irregular, Whole Equipment inefficiency, and traditional separatory mode require the number of heat collector panel must be 2 power can divide even, greatly limit applicable situation and the using method of heat collector panel.
Utility model content
Technical problem to be solved in the utility model is, provides a kind of low pressure liquid separation system, and each heat collector panel heat absorption average variance is little, and evenly, line arrangement is simple, and the pipeline put with calico is few in heat absorption, and the high and quantity of heat collector panel of pipe-line layout aesthetics can adjust flexibly.
For solving the problems of the technologies described above, a kind of low pressure liquid separation system that the utility model provides, comprise feed tube and escape pipe, it is characterized in that described feed tube is divided into two the isometric separating tube of connection two, described separating tube is respectively by the some heat collector panels of equidistant pipeline communication, the relative feed tube of heat collector panel connector on two separating tubes and the junction of separating tube are symmetrical arranged, and described each heat collector panel is respectively by the escape pipe described in equidistant pipeline communication and connector equidistant arrangement on escape pipe.
In feed tube, medium is the liquid state of low pressure, be symmetrical arranged medium diverting flow to each heat collector panel by two separating tubes, the gaseous state that after medium flows through heat collector panel, medium becomes high pressure is back to escape pipe again and discharges, and the entrance of feed tube is general import, and the outlet of escape pipe is general export, even by this system pipeline separatory, heat collector panel operating efficiency is close, and medium energy storage is even, and saves pipeline, easy for installation, the high and quantity of heat collector panel of pipe-line layout aesthetics can adjust flexibly.
As preferably:
Described feed tube to be divided into two connection two separating tube by Y-type three way type, and two separating tube length are consistent, guarantee that separatory is even by Y-type three way type.
Pipeline for being communicated with heat collector panel is all connected by T-shaped threeway with escape pipe, and T-shaped threeway is applicable to the mode of communicating that this kind derives many pipelines from the straight tube of a band outlet, and medium stream is smooth and easy.
Described separating tube is communicated with the heat collector panel connecting pipe of caudal end by T-shaped threeway, and all the other heat collector panel connecting pipes are Y-type three way type, are communicated with by which, and separatory is more even, and medium stream is smooth and easy.
Described heat collector panel is equidistantly arranged at the connector of separating tube, rationally distributed, guarantees that separatory is even.
Described separating tube and the end of escape pipe all leave surplus section, and the described surplus section end mouth of pipe is closed, and surplus section is used for the bounce-back backflow that medium flows to the end, eliminates the pipeline impact being connected to the heat collector panel of end, the operating efficiency of each heat collector panel balanced.
Described surplus segment length is greater than 150mm, ensures the effect of buffering reflux.
The surplus segment length of described separating tube and escape pipe is all equal, reaches equivalent reflux effect.
A kind of low pressure liquid separation system of the present utility model, break through original each heat collector panel from medium general import to the consistent arrangement of the length of pipe that general export is used, adopt with the Tee Joint Point of feed tube and separating tube as basic point, pipeline is arranged symmetrically with, make the operating efficiency of each heat collector panel close, medium energy storage is even, and saves pipeline, easy for installation, and the high and quantity of heat collector panel of pipe-line layout aesthetics can adjust flexibly.
Accompanying drawing explanation
Fig. 1 is the utility model structural representation.
Wherein: 1, feed tube, 2, escape pipe, 3, separating tube, 4, heat collector panel, 5, pipeline, 6, Y-type three way type, 7, T-shaped threeway, 8, surplus section.
Detailed description of the invention
Below by embodiment, the utility model will be further described by reference to the accompanying drawings.
As shown in Figure 1, a kind of low pressure liquid separation system that the present embodiment provides, comprise feed tube 1 and escape pipe 2, described feed tube 1 is divided into two the isometric separating tube 3 of connection two, described separating tube 3 is communicated with four heat collector panels 4 respectively by equidistant pipeline 5, two separating tubes 3 totals are communicated with eight heat collector panels 4, the relative feed tube of heat collector panel connector on two separating tubes and the junction of separating tube are symmetrical arranged, and described each heat collector panel 4 is communicated with described escape pipe 2 respectively by equidistant pipeline 5 and connector equidistant arrangement on escape pipe 2.
Described feed tube 1 to be divided into two connection two separating tube 3 by Y-type three way type 6, pipeline for being communicated with heat collector panel 4 is all connected by T-shaped threeway 7 with escape pipe 2, described separating tube 3 is communicated with heat collector panel 4 connecting pipe of caudal end by T-shaped threeway 7, all the other heat collector panel 4 connecting pipes are Y-type three way type 6, this threeway connected mode, be specially adapted to the layout of this pipeline, the medium stream being passed to heat collector panel be evenly distributed, reach the effect that each heat collector panel operating efficiency is close.Described heat collector panel 4 is equidistantly arranged at the connector of separating tube, rationally distributed, guarantees that separatory is even.
Described separating tube 3 and the end of escape pipe 2 all leave the surplus section 8 that length is greater than 150mm, and the described surplus section 8 end mouth of pipe is closed, surplus section 8 identical length etc. of described separating tube 3 and escape pipe 2.Surplus section is used for the bounce-back backflow that medium flows to the end, eliminates the pipeline impact being connected to the heat collector panel of end, the operating efficiency of each heat collector panel balanced.
The medium stream of the technical program flows into from feed tube, and now medium is the liquid state of low pressure, by two separating tubes by medium diverting flow to each heat collector panel, after medium flows through heat collector panel, medium becomes the gaseous state of high pressure, then be back to escape pipe discharge.Pipe-line layout and threeway are suitable for rationally, and heat is not suitable for the separatory layout of low-pressure medium, makes the homogeneous media that each heat collector panel obtains, operating efficiency is close, and medium energy storage is even, and saves pipeline, easy for installation, and the high and quantity of heat collector panel of pipe-line layout aesthetics can adjust flexibly.
Claims (8)
1. a low pressure liquid separation system, comprise feed tube (1) and escape pipe (2), it is characterized in that described feed tube (1) is divided into two the isometric separating tube (3) of connection two, described separating tube (3) is communicated with some heat collector panels (4) respectively by equidistant pipeline (5), the relative feed tube of heat collector panel connector on two separating tubes and the junction of separating tube are symmetrical arranged, and described each heat collector panel (4) is respectively by the escape pipe (2) described in equidistant pipeline (5) connection and connector goes up equidistant arrangement at escape pipe (2).
2. a kind of low pressure liquid separation system according to claim 1, is characterized in that described feed tube (1) to be divided into two connection two separating tube (3) by Y-type three way type (6).
3. a kind of low pressure liquid separation system according to claim 1, is characterized in that the pipeline for being communicated with heat collector panel (4) is all connected by T-shaped threeway (7) with escape pipe (2).
4. a kind of low pressure liquid separation system according to claim 1, it is characterized in that described separating tube (3) is communicated with heat collector panel (4) connecting pipe of caudal end by T-shaped threeway (7), all the other heat collector panels (4) connecting pipe is Y-type three way type (6).
5. a kind of low pressure liquid separation system according to claim 1, is characterized in that described heat collector panel (4) is equidistantly arranged at the connector of separating tube.
6. a kind of low pressure liquid separation system according to claim 1, is characterized in that the end of described separating tube (3) and escape pipe (2) all leaves surplus section (8), and described surplus section (8) the end mouth of pipe is closed.
7. a kind of low pressure liquid separation system according to claim 6, is characterized in that described surplus section (8) length is greater than 150mm.
8. a kind of low pressure liquid separation system according to claim 6 or 7, is characterized in that described separating tube (3) and surplus section (8) identical length etc. of escape pipe (2).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520939236.1U CN205119914U (en) | 2015-11-23 | 2015-11-23 | Liquid system is divided to low pressure |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520939236.1U CN205119914U (en) | 2015-11-23 | 2015-11-23 | Liquid system is divided to low pressure |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205119914U true CN205119914U (en) | 2016-03-30 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520939236.1U Active CN205119914U (en) | 2015-11-23 | 2015-11-23 | Liquid system is divided to low pressure |
Country Status (1)
| Country | Link |
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| CN (1) | CN205119914U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105241295A (en) * | 2015-11-23 | 2016-01-13 | 唐玉敏 | Low-pressure liquid separation system |
-
2015
- 2015-11-23 CN CN201520939236.1U patent/CN205119914U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105241295A (en) * | 2015-11-23 | 2016-01-13 | 唐玉敏 | Low-pressure liquid separation system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20230105 Address after: 313000 Factory Building 20 #, Changxing National University Science Park, No. 669 High speed Railway, Changxing County, Huzhou City, Zhejiang Province Patentee after: ZHEJIANG SHIZI NEW ENERGY TECHNOLOGY CO.,LTD. Address before: 315400 room 104, building 9, new city garden, Yangming street, Yuyao City, Ningbo City, Zhejiang Province Patentee before: Tang Yumin Patentee before: Yu Hongwei |