CN2506964Y - Adjustable pressure increasing heat-exchanging energy saving device - Google Patents
Adjustable pressure increasing heat-exchanging energy saving device Download PDFInfo
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- CN2506964Y CN2506964Y CN 01267048 CN01267048U CN2506964Y CN 2506964 Y CN2506964 Y CN 2506964Y CN 01267048 CN01267048 CN 01267048 CN 01267048 U CN01267048 U CN 01267048U CN 2506964 Y CN2506964 Y CN 2506964Y
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Abstract
An adjustable supercharging heat transfer energy-saving device comprises an adjustable steam accelerating chamber, a two-phase mixed chamber and a pressure boosting chamber, wherein, water inlets are arranged respectively between the adjustable steam accelerating chamber and the two-phase mixed chamber and between the two-phase mixed chamber and the pressure boosting chamber. The utility model is applicable to heat supply, drainage, domestic water consumption and so on, and has the advantages of low operation cost, safety, reliability, energy saving, low consumption, good adoptability, and so on, and can adjust steam accelerating chamber so as to realize duel functions of heat transfer and pressure boosting under different working conditions, and is an ideal dedicated device that replaces a heat exchanger and a circulating water pump in the thermodynamic field.
Description
The utility model relates to a kind of heat power engineering isolated plant, is specifically to be used for the alternative heat exchanger of heating system and the adjustable supercharging heat exchange energy saver that water circulating pump equipment carries out exchange heat.
The heat exchange station of traditional heating system, most heat exchangers that adopt add the circulation of water circulating pump heat supply water, and its equipment is huge, system complex, investment is high, operation energy consumption is big, and there is poor reliability in the system failure rate height, service life of equipment is short, maintenance cost height, shortcoming such as noise is big; Also select carbonated drink mixing arrangement such as patent No. 98221409.X, carbonated drink counterflow pump for use, content according to this patent disclosure is difficult to realize its goal of the invention, it requires steam pressure higher, can only adapt to fixedly area of heat-supply service, promptly decide single operating modes such as steam parameter, the operating mode that can not adapt to various variations flexibly, the narrow range of application; And have that steam jet is non-adjustable, the variable working condition ability, be difficult to phenomenons such as control, design parameter is inaccurate, system noise is big, heat exchange efficiency is low, so As-Is is difficult to satisfy the instructions for use of heating system.
The utility model purpose is to provide a kind of can eliminate above-mentioned shortcoming, improvement at ZL98221409.X, it is less demanding to steam pressure, the size of steam regulation accelerating chamber, position easily, adapt to various operating modes, can be according to the needs of different user, regulate arbitrarily and control, satisfy user demand, realize the steam-water heat exchanging and the dual-use function that boosts with machine, have adjustable supercharging heat exchange energy savers reasonable in design, easy to use, characteristics such as heat exchange efficiency is high, production cost is low, applied range.
The utility model purpose is realized by following technical scheme:
Adjustable supercharging heat exchange energy saver comprises compositions such as adjustable steam accelerating chamber, two-phase mixing chamber, booster chamber and first, second water inlet, wherein adjustable steam accelerating chamber, two-phase mixing chamber and booster chamber, be linked in sequence successively, end at the two-phase mixing chamber is equipped with the adjustable steam accelerating chamber, first water inlet is arranged, in the junction of two-phase mixing chamber and booster chamber second water inlet is arranged in the junction of adjustable steam accelerating chamber and two-phase mixing chamber.It can be with diffluence room in the outer end that the adjustable steam accelerating chamber is connected with two-phase mixing chamber, booster chamber successively, constitute the device that has diffluence room, total water inlet is arranged in diffluence room, in diffluence room, filter course can be housed, wherein can select diffluence room's diameter and booster chamber outlet diameter than being 2-3, on the end face of the one the second water inlets, leave through hole, usually preferably select 1-20 through hole, the first water inlet via area and with adjustable steam accelerating chamber import sectional area ratio be 1-1.7, the filter course in diffluence room preferably selects for use metal or macromolecular material to make.
Described adjustable steam accelerating chamber is that profile is the circular cone stage body, its inner chamber is the stack of circular cone stage body, place or be movably connected in the sleeve of mixing chamber, by size or the adjusting accelerating chamber position of changing accelerating chamber, to reach the purpose that adapts to various operating modes, wherein: the diameter of the minimum place of frustum of a cone diameter and import department is than being 0.3-0.6, and minimum place diameter and outlet diameter are than being 0.17-1; Wherein the first water inlet diameter is 1-1.7 with adjustable steam accelerating chamber inlet diameter ratio; Adjustable steam accelerating chamber outlet diameter and two-phase mixing-chamber inlet diameter ratio are 0.2-0.5; Adjustable steam accelerating chamber inlet diameter is 1-1.7 with the ratio of booster chamber's outlet diameter; The distance that the adjustable steam accelerating chamber is exported to the two-phase mixing chamber inlet is the 0-100 millimeter, is preferably the 0-40 millimeter.
The end of going into of described two-phase mixing chamber is connected with first water inlet, accelerating chamber, it goes out end and is connected with second water inlet, booster chamber, its inner chamber is the stack of cylinder and circular cone stage body, its inlet is 1-2 with the diameter ratio of outlet, the length of its conical section is 0-14 with import straight length diameter ratio, its inlet flow development length and conical section length sum are 6-9 with adjustable steam accelerating chamber outlet diameter ratio, its outlet flow development length is 1-3 with the outlet diameter ratio, and the distance that two-phase mixing chamber outlet to booster chamber enters the mouth is 5-14 with the ratio of both diameter differences.
The end of going into of described booster chamber is connected with second water inlet, mixing chamber, and it goes out end and is connected with heat supply pipeline, and its inner chamber is the stack of circular cone stage body, booster chamber's inlet and outlet diameter ratio be 0.4-0.7, with conical section length ratio be 0.15-0.5; The second water inlet diameter with booster chamber outlet diameter ratio is: 1-1.7.
The course of work of this device is steam to be entered by the import of adjustable steam accelerating chamber arrive slot, arriving outlet after the acceleration again slows down, pressurizes, water inlet with first water inlet mixes mutually again, form a kind of the have steam of certain computed volume ratio and the mixture of water, this mixture directly enters the two-phase mixing chamber; Because the velocity of sound of this mixture is lower than its flowing velocity, so can in the cross section of contraction section, overcome sound barrier, then in cylindrical tube chamber, finish flowing velocity to subsonic transformation, produced pressure " shock wave " this moment, pressure acutely increases, be heated, the water of supercharging enters booster chamber, promptly is admitted in the heat supply pipeline after slowing down in booster chamber, boosting, and finishes heat exchange and the function of boosting.
Advantage of the present utility model is: equipment takes up an area of little, simple in structure, energy-saving and cost-reducing, reliable, especially used the adjustable steam accelerating chamber, realized steam, working conditions change is controlled, the scope of application is big, and design parameter is accurate, noiselessness, and heat exchange efficiency is high, can satisfy the different requirement of different user, be desirable heat-exchange energy-saving device.
Description of drawings:
Fig. 1: adjustable supercharging heat exchange energy saver structure chart
Fig. 2: 4-the first water inlet, 5-the second water inlet, 6-water inlet manifold, 7-diffluence room of adjustable supercharging heat exchange energy saver structure chart 1-accelerating chamber 2-mixing chamber 3-booster chamber, the 8-filter course of band diffluence room further specifies embodiment of the present utility model in conjunction with the accompanying drawings:
This device mainly contains adjustable steam accelerating chamber (1), and there are first water inlet (4) in two-phase mixing chamber (2) and booster chamber (3) at adjustable steam accelerating chamber and two-phase mixing chamber junction, at two-phase mixing chamber and booster chamber junction second water inlet (5) are arranged.It can be with diffluence room (7) in the outer end that adjustable steam accelerating chamber (1) is connected with two-phase mixing chamber (2), booster chamber (3) successively, constitute the device that has diffluence room, total water inlet (6) is arranged in diffluence room (7), filter course (8) can be housed in diffluence room (7), flange that is used to install etc. can be housed on this device main body.
Can to select adjustable steam accelerating chamber (1) for use be to be movably connected in the two-phase mixing chamber to this device as shown in Figure 1, its inlet diameter is 40 millimeters, minimum place diameter is 7.0 millimeters, outlet is 8.1 millimeters, two-phase mixing chamber (2) inlet diameter is 13 millimeters, outlet is 9 millimeters, middle tapering segment length is 22 millimeters, booster chamber (3) inlet diameter is 9.5 millimeters, outlet is 40 millimeters, tapered section length is 120 millimeters, and two-phase mixing chamber outlet and booster chamber's inlet distance are 5 millimeters, and the outlet of steam accelerating chamber is 10 millimeters with two-phase mixing chamber inlet distance.40 millimeters of first water inlet (4) Circularhole diameters, second water inlet (5) Circularhole diameter are 32 millimeters etc., also can select other related datas for use usually.
Can to select adjustable steam accelerating chamber (1) for use be to be positioned in the two-phase mixing chamber to this device as shown in Figure 2, its inlet diameter is 40 millimeters, minimum place diameter is 6.5 millimeters, outlet is 7.7 millimeters, two-phase mixing chamber (2) inlet diameter is 12 millimeters, outlet is 8.1 millimeters, middle circular cone segment length is 18.1 millimeters, booster chamber (3) inlet diameter is 9.3 millimeters, outlet is 40 millimeters, tapered section length is 58 millimeters, two-phase mixing chamber (2) outlet and booster chamber (3) inlet distance are 4 millimeters, steam accelerating chamber (1) outlet is 6 millimeters with two-phase mixing chamber (2) inlet distance, first water inlet (4)) be the circular hole of 10 millimeters of 8 diameters, second water inlet (5) is the circular hole of 7 millimeters of 8 diameters, diffluence room (7) diameter is 100 millimeters, total water inlet (6) diameter is 50 millimeters, and the filter course in the diffluence room (8) is 32 order stainless (steel) wires etc., also can select other related datas for use usually.
Claims (13)
1, a kind of adjustable supercharging heat exchange energy saver, be connected with booster chamber by the two-phase mixing chamber, it is characterized in that the adjustable steam accelerating chamber being housed, first water inlet is arranged, second water inlet is arranged in the junction of mixing chamber and booster chamber in the junction of accelerating chamber and mixing chamber at an end of two-phase mixing chamber.
2, adjustable supercharging heat exchange energy saver as claimed in claim 1, it is characterized in that the adjustable steam accelerating chamber being housed at an end of two-phase mixing chamber, the other end is connected with booster chamber, in the junction of accelerating chamber and mixing chamber first water inlet is arranged, in the junction of mixing chamber and booster chamber second water inlet is arranged, the adjustable steam accelerating chamber is connected with two-phase mixing chamber, booster chamber successively, be with diffluence room in its outer end, total water inlet is arranged in diffluence room, in diffluence room, filter course can be housed, on first, second water inlet, leave through hole.
3, as claim 1,2 described adjustable supercharging heat exchange energy savers, it is characterized in that described adjustable steam accelerating chamber is that profile is the circular cone stage body, its inner chamber is the stack of circular cone stage body, place or movable being attached in the sleeve of mixing chamber, wherein: the diameter of the minimum place of frustum of a cone diameter and import department is than being 0.3-0.6, and minimum place diameter and outlet diameter are than being 0.17-1.
4, as claim 1,2 described adjustable supercharging heat exchange energy savers, the end of going into that it is characterized in that described two-phase mixing chamber is connected with first water inlet, accelerating chamber, it goes out end and is connected with second water inlet, booster chamber, its inner chamber is the stack of cylinder and circular cone stage body, its inlet is 1-2 with the diameter ratio of outlet, the length of its conical section is 0-14 with import straight length diameter ratio, its inlet flow development length and conical section length sum are 6-9 with adjustable steam accelerating chamber outlet diameter ratio, and its outlet flow development length is 1-3 with the outlet diameter ratio.
5, as claim 1,2 described adjustable supercharging heat exchange energy savers, the end of going into that it is characterized in that described booster chamber is connected with second water inlet, mixing chamber, it goes out end and is connected with heat supply pipeline, its inner chamber is the stack of circular cone stage body, and booster chamber's inlet is 0.4-0.7, is 0.15-0.5 with conical section length ratio with the outlet diameter ratio.
6,, it is characterized in that two-phase mixing chamber outlet to the ratio of the distance of booster chamber inlet and both diameter differences is 5-14 as claim 1,2 described adjustable supercharging heat exchange energy savers.
7,, it is characterized in that the first water inlet diameter and adjustable steam accelerating chamber inlet diameter ratio are 1-1.7 as claim 1,2 described mode supercharging heat exchange energy savers.
8,, it is characterized in that the second water inlet diameter and booster chamber outlet diameter ratio are: 1-1.7 as claim 1,2 described mode supercharging heat exchange energy savers.
9, as claim 1,2 described adjustable supercharging heat exchange energy savers, it is characterized in that adjustable steam accelerating chamber outlet diameter and two-phase mixing-chamber inlet diameter ratio are 0.2-0.5.
10,, it is characterized in that the adjustable steam accelerating chamber inlet diameter and the ratio of booster chamber outlet diameter are 1-1.7 as claim 1,2 described adjustable supercharging heat exchange energy savers.
11,, it is characterized in that the distance that the adjustable steam accelerating chamber is exported to the two-phase mixing chamber inlet is the 0-40 millimeter as claim 1,2 described adjustable supercharging heat exchange energy savers.
12, adjustable supercharging heat exchange energy saver as claimed in claim 2 is characterized in that diffluence room's diameter and booster chamber outlet diameter are than being 2-3.
13, adjustable supercharging heat exchange energy saver as claimed in claim 2 is characterized in that being equipped with filter course in diffluence room, and this filter course metal or macromolecular material are made.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 01267048 CN2506964Y (en) | 2001-11-03 | 2001-11-03 | Adjustable pressure increasing heat-exchanging energy saving device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 01267048 CN2506964Y (en) | 2001-11-03 | 2001-11-03 | Adjustable pressure increasing heat-exchanging energy saving device |
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| Publication Number | Publication Date |
|---|---|
| CN2506964Y true CN2506964Y (en) | 2002-08-21 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN 01267048 Expired - Fee Related CN2506964Y (en) | 2001-11-03 | 2001-11-03 | Adjustable pressure increasing heat-exchanging energy saving device |
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| CN (1) | CN2506964Y (en) |
Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100400999C (en) * | 2002-10-17 | 2008-07-09 | 洛阳蓝海实业有限公司 | Variable acoustic pressurizing dual blast heat exchanger |
| CN102410747A (en) * | 2010-09-20 | 2012-04-11 | 崔学勤 | Multi-level boost energy-saving heat exchanger |
| CN103743262A (en) * | 2013-12-04 | 2014-04-23 | 无锡伊诺永利文化创意有限公司 | Circulating cooling-type high-pressure fluid heat exchanger |
| CN103743260A (en) * | 2013-12-04 | 2014-04-23 | 无锡伊诺永利文化创意有限公司 | Multi-flow circulating-type high-pressure fluid heat exchanger |
| CN103837000A (en) * | 2013-12-04 | 2014-06-04 | 无锡伊诺永利文化创意有限公司 | Double-flow cooling-type high-pressure fluid heat exchanger |
| CN103836999A (en) * | 2013-12-04 | 2014-06-04 | 无锡伊诺永利文化创意有限公司 | Inner flow-type high-pressure fluid heat exchanger |
| CN103837001A (en) * | 2013-12-04 | 2014-06-04 | 无锡伊诺永利文化创意有限公司 | Air-cooling-type high-pressure fluid heat exchanger |
| CN103837009A (en) * | 2013-12-04 | 2014-06-04 | 无锡伊诺永利文化创意有限公司 | Cooling circulating-type high-pressure fluid heat exchanger |
| CN103837010A (en) * | 2013-12-04 | 2014-06-04 | 无锡伊诺永利文化创意有限公司 | Circulating-type high-pressure fluid heat exchanger |
| CN103837004A (en) * | 2013-12-04 | 2014-06-04 | 无锡伊诺永利文化创意有限公司 | Multi-flow cooling-type high-pressure fluid heat exchanger |
| CN103837008A (en) * | 2013-12-04 | 2014-06-04 | 无锡伊诺永利文化创意有限公司 | Fine-diameter fluid pipe-type high-pressure fluid heat exchanger |
| CN103837002A (en) * | 2013-12-04 | 2014-06-04 | 无锡伊诺永利文化创意有限公司 | Integrated high-pressure fluid heat exchanger |
-
2001
- 2001-11-03 CN CN 01267048 patent/CN2506964Y/en not_active Expired - Fee Related
Cited By (15)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100400999C (en) * | 2002-10-17 | 2008-07-09 | 洛阳蓝海实业有限公司 | Variable acoustic pressurizing dual blast heat exchanger |
| CN102410747A (en) * | 2010-09-20 | 2012-04-11 | 崔学勤 | Multi-level boost energy-saving heat exchanger |
| CN102410747B (en) * | 2010-09-20 | 2013-07-03 | 崔学勤 | Multi-level boost energy-saving heat exchanger |
| CN103743262A (en) * | 2013-12-04 | 2014-04-23 | 无锡伊诺永利文化创意有限公司 | Circulating cooling-type high-pressure fluid heat exchanger |
| CN103743260A (en) * | 2013-12-04 | 2014-04-23 | 无锡伊诺永利文化创意有限公司 | Multi-flow circulating-type high-pressure fluid heat exchanger |
| CN103837000A (en) * | 2013-12-04 | 2014-06-04 | 无锡伊诺永利文化创意有限公司 | Double-flow cooling-type high-pressure fluid heat exchanger |
| CN103836999A (en) * | 2013-12-04 | 2014-06-04 | 无锡伊诺永利文化创意有限公司 | Inner flow-type high-pressure fluid heat exchanger |
| CN103837001A (en) * | 2013-12-04 | 2014-06-04 | 无锡伊诺永利文化创意有限公司 | Air-cooling-type high-pressure fluid heat exchanger |
| CN103837009A (en) * | 2013-12-04 | 2014-06-04 | 无锡伊诺永利文化创意有限公司 | Cooling circulating-type high-pressure fluid heat exchanger |
| CN103837010A (en) * | 2013-12-04 | 2014-06-04 | 无锡伊诺永利文化创意有限公司 | Circulating-type high-pressure fluid heat exchanger |
| CN103837004A (en) * | 2013-12-04 | 2014-06-04 | 无锡伊诺永利文化创意有限公司 | Multi-flow cooling-type high-pressure fluid heat exchanger |
| CN103837008A (en) * | 2013-12-04 | 2014-06-04 | 无锡伊诺永利文化创意有限公司 | Fine-diameter fluid pipe-type high-pressure fluid heat exchanger |
| CN103837002A (en) * | 2013-12-04 | 2014-06-04 | 无锡伊诺永利文化创意有限公司 | Integrated high-pressure fluid heat exchanger |
| CN103837010B (en) * | 2013-12-04 | 2016-01-20 | 江苏高博智融科技有限公司 | Circulating high pressure fluid heat exchanger |
| CN103837001B (en) * | 2013-12-04 | 2016-03-09 | 江苏高博智融科技有限公司 | Air-cooled exchanger for high pressure fluid |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |