CN203980934U - Carbonated drink plate-type heat-exchange unit - Google Patents
Carbonated drink plate-type heat-exchange unit Download PDFInfo
- Publication number
- CN203980934U CN203980934U CN201420429812.3U CN201420429812U CN203980934U CN 203980934 U CN203980934 U CN 203980934U CN 201420429812 U CN201420429812 U CN 201420429812U CN 203980934 U CN203980934 U CN 203980934U
- Authority
- CN
- China
- Prior art keywords
- type heat
- inlet tube
- desuperheating
- heat exchanger
- water
- 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.)
- Withdrawn - After Issue
Links
Landscapes
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The utility model discloses carbonated drink plate-type heat-exchange unit, belong to heat exchange unit, its structure comprises plate type heat exchanger, water tank, small pump, electrical control cubicles and underframe, also comprise filter and circulating pump, plate type heat exchanger is connected with Desuperheating device, and Desuperheating device comprises housing, steam inlet pipe, thermal source outlet, desuperheating water inlet tube, desuperheating water jet pipe and wire packing; On plate type heat exchanger, be respectively arranged with healed water outlet, healed water inlet tube, thermal source inlet tube and hydrophobic outlet; Hydrophobic outlet is connected with water tank by hydrophobic inlet tube, water tank is connected with the healed water inlet tube of plate type heat exchanger with feed pipe by filling pipe, backwater supervisor, circulating pump, feed pipe is connected with desuperheating water inlet tube, and backwater supervisor top is provided with healed water return pipe.The utlity model has solved plate type heat exchanger can not be for the shortcoming of high-temperature steam; Circulating backwater is as cooling water; Compact conformation, the feature such as heat exchange efficiency is high, low cost of manufacture.
Description
Technical field
The utility model relates to a kind of heat exchange unit, especially a kind of carbonated drink plate-type heat-exchange unit.
Background technology
Because gasket type plate type heat exchanger has, volume is little, floor space is few, energy-conservation capital expenditure, and effective heat exchange area is large, lightweight; Heat transfer efficiency is high, and the heat transfer coefficient of plate type heat exchanger, generally at 3000-7000W/m. ℃, is 3-5 times of other heat exchangers; Heat loss is little; Assembling flexibly, conveniently increases or reduces heat exchange plate; Dismantle, clean, overhaul the advantages such as convenient, in the multiple fields such as oil, chemical industry, metallurgy, medicine, papermaking, food, heat supply, all obtained application quite widely.But the seal gasket in plate type heat exchanger can not be high temperature resistant, should not under the condition of 150 ℃, work for a long time, more can not be not suitable for high-temperature steam media for heat exchange working at the temperature of 150 ℃, make like this use of plate type heat exchanger under higher temperature be restricted.
Because of plate type heat exchanger can not be for temperature the steam higher than 150 ℃, therefore heating on market, air-conditioning carbonated drink unit are generally used shell-and-tube heat exchanger now, but shell-and-tube heat exchanger heat exchange efficiency is low, area is large, manufactures and maintenance difficult.
At present, the solution also not had.
Utility model content
Technical assignment of the present utility model is to provide a kind of carbonated drink plate-type heat-exchange unit for above-mentioned deficiency of the prior art, this carbonated drink plate-type heat-exchange unit have solved plate type heat exchanger can not be for the shortcoming of high-temperature steam; Utilize circulating backwater as cooling water, realize the cooling to steam; Make full use of the advantage of plate type heat exchanger, compact conformation, heat exchange efficiency is high, low cost of manufacture; The feature that is applicable to various conventional steam operating modes.
The utility model solves the technical scheme that its technical problem adopts: it comprises plate type heat exchanger, water tank, small pump, electrical control cubicles and underframe, also comprise filter and circulating pump, described plate type heat exchanger, water tank, small pump, filter and circulating pump are separately positioned on underframe, described plate type heat exchanger is connected with Desuperheating device by connecting bend, described Desuperheating device comprises housing, steam inlet pipe, thermal source outlet, desuperheating water inlet tube, desuperheating water jet pipe and wire packing, described steam inlet pipe and thermal source outlet are separately positioned on top and the bottom of housing, described wire packing is arranged on the bottom of housing, the top of thermal source outlet, in the upper body of described wire packing, be provided with desuperheating water jet pipe, the bottom of described desuperheating water jet pipe is connected with desuperheating water inlet tube, described desuperheating water inlet tube is arranged on a side of housing, on described desuperheating water jet pipe, be provided with a plurality of spray orifices, described thermal source outlet is connected with plate type heat exchanger by connecting bend, on described plate type heat exchanger, be respectively arranged with healed water outlet, healed water inlet tube, thermal source inlet tube and hydrophobic outlet, described thermal source inlet tube is connected with connecting bend, described hydrophobic outlet is connected with water tank by hydrophobic inlet tube, on described hydrophobic inlet tube, be provided with drain valve, on described water tank, be provided with moisturizing import, in described moisturizing import, be provided with ball-cock assembly, described water tank passes through filling pipe, backwater supervisor, circulating pump is connected with the healed water inlet tube of plate type heat exchanger with feed pipe, described feed pipe top is connected with desuperheating water inlet tube, on described desuperheating water inlet tube, be provided with electric control valve, on described filling pipe, be provided with small pump, described backwater supervisor top is provided with healed water return pipe, described small pump, circulating pump and electric control valve are electrically connected to electrical control cubicles respectively.
Described a plurality of spray orifices evenly arrange along desuperheating water jet pipe sidewall.
Described connecting bend is connected with the thermal source outlet of Desuperheating device bottom and the thermal source inlet tube of plate type heat exchanger by adpting flange respectively.
On the water tank on described moisturizing import top, be provided with overfall, the bottom of described water tank is provided with sewage draining exit, on the water tank on sewage draining exit top, is provided with liquid level gauge.
Described small pump comprises two, and two small pumps are set up in parallel.
Described circulating pump comprises two, and two circulating pumps are set up in parallel.
On described healed water return pipe, be provided with filter, described filter is y-type filter.
Compared to the prior art carbonated drink plate-type heat-exchange unit of the present utility model, has following outstanding beneficial effect: having solved plate type heat exchanger can not be for the shortcoming of high-temperature steam; Utilize circulating backwater as cooling water, realize the cooling to steam; Make full use of the advantage of plate type heat exchanger, compact conformation, heat exchange efficiency is high, low cost of manufacture; Be applicable to various conventional steam operating modes, without with pressure-reducing valve to features such as steam reduce pressure.
Accompanying drawing explanation
Accompanying drawing 1 is the main TV structure schematic diagram of carbonated drink plate-type heat-exchange unit;
Accompanying drawing 2 is that carbonated drink plate-type heat-exchange unit is removed the plan structure schematic diagram after electrical control cubicles;
Accompanying drawing 3 is A-A amplification views of the Desuperheating device shown in Fig. 1;
Description of reference numerals: 1 plate type heat exchanger, 2 Desuperheating devices, 3 steam inlet pipes, 4 desuperheating water inlet tubes, 5 wire packings, 6 thermal source outlets, 7 desuperheating water jet pipes, 8 healed water outlets, 9 healed water inlet tubes, 10 hydrophobic outlets, 11 connecting bends, 12 thermal source inlet tubes, 13 housings, 14 spray orifices, 15 adpting flanges, 16 electric control valves, 17 filters, 18 healed water return pipes, 19 circulating pumps, 20 drain valves, 21 hydrophobic inlet tubes, 22 overfalls, 23 water tanks, 24 sewage draining exits, 25 underframe, 26 small pumps, 27 ball-cock assemblys, 28 moisturizing imports, 29 electrical control cubicles, 30 filling pipes, 31 backwater supervisors, 32 feed pipes, 33 liquid level gauges.
The specific embodiment
With reference to Figure of description 1 to 3 pairs of carbonated drink plate-type heat-exchange units of the present utility model of accompanying drawing, be described in detail below.
Carbonated drink plate-type heat-exchange unit of the present utility model, its structure comprises plate type heat exchanger 1, water tank 23, small pump 26, electrical control cubicles 29 and underframe 25, also comprise filter 17 and circulating pump 19, described plate type heat exchanger 1, water tank 23, small pump 26, filter 17 and circulating pump 19 are separately positioned on underframe 25, described plate type heat exchanger 1 is connected with Desuperheating device 2 by connecting bend 11, described Desuperheating device 2 comprises housing 13, steam inlet pipe 3, thermal source outlet 6, desuperheating water inlet tube 4, desuperheating water jet pipe 7 and wire packing 5, described steam inlet pipe 3 and thermal source outlet 6 are separately positioned on top and the bottom of housing 13, described wire packing 5 is arranged on the bottom of housing 13, the top of thermal source outlet 6, in the upper body 13 of described wire packing 5, be provided with desuperheating water jet pipe 7, the bottom of described desuperheating water jet pipe 7 is connected with desuperheating water inlet tube 4, described desuperheating water inlet tube 4 is arranged on a side of housing 13, on described desuperheating water jet pipe 7, be provided with a plurality of spray orifices 14, described thermal source outlet 6 is connected with plate type heat exchanger 1 by connecting bend 11, on described plate type heat exchanger 1, be respectively arranged with healed water outlet 8, healed water inlet tube 9, thermal source inlet tube 12 and hydrophobic outlet 10, described thermal source inlet tube 12 is connected with connecting bend 11, described hydrophobic outlet 10 is connected with water tank 23 by hydrophobic inlet tube 21, on described hydrophobic inlet tube 21, be provided with drain valve 20, on described water tank 23, be provided with moisturizing import 28, in described moisturizing import 28, be provided with ball-cock assembly 27, described water tank 23 is by filling pipe 30, backwater supervisor 31, circulating pump 19 is connected with the healed water inlet tube 9 of plate type heat exchanger 1 with feed pipe 32, described feed pipe 32 tops are connected with desuperheating water inlet tube 4, on described desuperheating water inlet tube 4, be provided with electric control valve 16, on described filling pipe 30, be provided with small pump 26, described backwater is responsible for 31 tops and is provided with healed water return pipe 18, described small pump 26, circulating pump 19 and electric control valve 16 are electrically connected to electrical control cubicles 29 respectively.
Described a plurality of spray orifices 14 evenly arrange along desuperheating water jet pipe 7 sidewalls.
Described connecting bend 11 is connected with the thermal source outlet 6 of Desuperheating device 2 bottoms and the thermal source inlet tube 12 of plate type heat exchanger 1 by adpting flange 15 respectively.
On the water tank 23 on described moisturizing import 28 tops, be provided with overfall 22, unnecessary water is discharged, the bottom of described water tank 23 is provided with sewage draining exit 24, by sewage draining exit 24, regularly the dirt in water tank 23 is got rid of, on the water tank 23 on sewage draining exit 24 tops, be provided with liquid level gauge 33, conveniently watch the liquid level in water tank 23.
Described small pump 26 comprises two, and two small pumps 26 are set up in parallel.During work, a use, another is standby.
Described circulating pump 19 comprises two, and two circulating pumps 19 are set up in parallel.During work, a use, another is standby.
On described healed water return pipe 18, be provided with filter 17, described filter 17 is y-type filter.Use the circulating backwater looping back to filter out impurity in water by filter 17 user.
Moisturizing enters water tank 23 by moisturizing import 28, and when water level arrives after certain water level, ball-cock assembly 27 is closed, and moisturizing finishes.By electrical control cubicles 29, control small pump 26 (the using and the reserved) system is carried out to moisturizing, when hydraulic pressure reaches after required pressure, by electrical control cubicles 29 controlled circulation pumps 19 (the using and the reserved), start, be heated and circulate.Steam enters Desuperheating device 2 by steam inlet pipe 3, by electrical control cubicles 29, control the opening degree of electric control valve 16, the recirculated water that control is transmitted by water tank 23, small pump 26, filling pipe 30, backwater supervisor 31, circulating pump 19, feed pipe 32 and desuperheating water inlet tube 4 successively enters 2 pairs of steam of Desuperheating device and lowers the temperature, vapor (steam) temperature remains on below 150 ℃, and the recirculated water that enters plate type heat exchanger 1 from healed water inlet tube 9 with feed pipe 32 carries out heat exchange.Condensed water after steam heat-exchanging enters water tank 23 by drain valve 20, hydrophobic inlet tube 21, as moisturizing, uses.Enter into circulating water heating in plate type heat exchanger 1 to after temperature required, for to user.The circulating backwater looping back from user enters plate type heat exchanger 1 by healed water return pipe 18, circulating pump 19, feed pipe 32 after filtering by filter 17, carries out circulating-heating, thereby reaches the object of continuous heat supply.All devices is assembled into a set of integral device by underframe 25.
Plate type heat exchanger 1 heat exchange operation principle: steam enters by steam inlet pipe 3 in the housing of Desuperheating device 2, recirculated water enters Desuperheating device 2 by desuperheating water inlet tube 4 simultaneously.Recirculated water, by a plurality of spray orifices 14 ejections on desuperheating water jet pipe 7, forms water smoke, contacts with high-temperature steam, mixes desuperheat, and steam is carried out to one-level desuperheat.Steam enters wire packing 5 gradually downwards, carries out the degree of depth mix in wire packing 5 with recirculated water, carries out secondary desuperheat.Flow by controlled circulation water remains at below 150 ℃ vapor (steam) temperature, then by the desuperheat recirculated water in the steam after secondary desuperheat and Desuperheating device 2, by thermal source outlet 6, connecting bend 11 and thermal source inlet tube 12, enter plate type heat exchanger 1, recirculated water enters plate type heat exchanger 1 by healed water inlet tube 9 and carries out exchange heat.After steam and the heat exchange of desuperheat recirculated water, become hydrophobic hydrophobic outlet 10 outflows of passing through, by the recirculated water after heat exchange, by healed water outlet 8, flowed out.Complete the heat exchange of steam and recirculated water.
Except the technical characterictic described in description, be the known technology of those skilled in the art.
Claims (7)
1. carbonated drink plate-type heat-exchange unit, comprise plate type heat exchanger, water tank, small pump, electrical control cubicles and underframe, it is characterized in that: also comprise filter and circulating pump, described plate type heat exchanger, water tank, small pump, filter and circulating pump are separately positioned on underframe, described plate type heat exchanger is connected with Desuperheating device by connecting bend, described Desuperheating device comprises housing, steam inlet pipe, thermal source outlet, desuperheating water inlet tube, desuperheating water jet pipe and wire packing, described steam inlet pipe and thermal source outlet are separately positioned on top and the bottom of housing, described wire packing is arranged on the bottom of housing, the top of thermal source outlet, in the upper body of described wire packing, be provided with desuperheating water jet pipe, the bottom of described desuperheating water jet pipe is connected with desuperheating water inlet tube, described desuperheating water inlet tube is arranged on a side of housing, on described desuperheating water jet pipe, be provided with a plurality of spray orifices, described thermal source outlet is connected with plate type heat exchanger by connecting bend, on described plate type heat exchanger, be respectively arranged with healed water outlet, healed water inlet tube, thermal source inlet tube and hydrophobic outlet, described thermal source inlet tube is connected with connecting bend, described hydrophobic outlet is connected with water tank by hydrophobic inlet tube, on described hydrophobic inlet tube, be provided with drain valve, on described water tank, be provided with moisturizing import, in described moisturizing import, be provided with ball-cock assembly, described water tank passes through filling pipe, backwater supervisor, circulating pump is connected with the healed water inlet tube of plate type heat exchanger with feed pipe, described feed pipe top is connected with desuperheating water inlet tube, on described desuperheating water inlet tube, be provided with electric control valve, on described filling pipe, be provided with small pump, described backwater supervisor top is provided with healed water return pipe, described small pump, circulating pump and electric control valve are electrically connected to electrical control cubicles respectively.
2. carbonated drink plate-type heat-exchange unit according to claim 1, is characterized in that: described a plurality of spray orifices evenly arrange along desuperheating water jet pipe sidewall.
3. carbonated drink plate-type heat-exchange unit according to claim 1, is characterized in that: described connecting bend is connected with the thermal source outlet of Desuperheating device bottom and the thermal source inlet tube of plate type heat exchanger by adpting flange respectively.
4. carbonated drink plate-type heat-exchange unit according to claim 1, is characterized in that: on the water tank on described moisturizing import top, be provided with overfall, the bottom of described water tank is provided with sewage draining exit, on the water tank on sewage draining exit top, is provided with liquid level gauge.
5. carbonated drink plate-type heat-exchange unit according to claim 1, is characterized in that: described small pump comprises two, and two small pumps are set up in parallel.
6. carbonated drink plate-type heat-exchange unit according to claim 1, is characterized in that: described circulating pump comprises two, and two circulating pumps are set up in parallel.
7. carbonated drink plate-type heat-exchange unit according to claim 1, is characterized in that: on described healed water return pipe, be provided with filter, described filter is y-type filter.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420429812.3U CN203980934U (en) | 2014-07-31 | 2014-07-31 | Carbonated drink plate-type heat-exchange unit |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420429812.3U CN203980934U (en) | 2014-07-31 | 2014-07-31 | Carbonated drink plate-type heat-exchange unit |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203980934U true CN203980934U (en) | 2014-12-03 |
Family
ID=51978365
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420429812.3U Withdrawn - After Issue CN203980934U (en) | 2014-07-31 | 2014-07-31 | Carbonated drink plate-type heat-exchange unit |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203980934U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104142073A (en) * | 2014-07-31 | 2014-11-12 | 山东国舜压力容器有限公司 | Steam and water plate-type heat exchange unit |
-
2014
- 2014-07-31 CN CN201420429812.3U patent/CN203980934U/en not_active Withdrawn - After Issue
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104142073A (en) * | 2014-07-31 | 2014-11-12 | 山东国舜压力容器有限公司 | Steam and water plate-type heat exchange unit |
| CN104142073B (en) * | 2014-07-31 | 2016-01-27 | 山东国舜压力容器有限公司 | Carbonated drink plate-type heat-exchange unit |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102721299A (en) | Stepped high-efficiency heat exchanger | |
| CN104142073B (en) | Carbonated drink plate-type heat-exchange unit | |
| CN203980934U (en) | Carbonated drink plate-type heat-exchange unit | |
| CN203964713U (en) | Double-shell side pipe heat exchanger | |
| CN203980969U (en) | Carbonated drink plate type heat exchanger | |
| CN205279819U (en) | Novel spiral plate type heat exchanger | |
| CN201476612U (en) | Shell heat exchanger | |
| CN205332873U (en) | High efficiency antiseep type heat exchanger | |
| CN205115337U (en) | Low power consuming is by device of methyl alcohol preparation aerosol dimethyl ether | |
| CN204447364U (en) | A kind of distillation still condenser system | |
| CN209166145U (en) | A kind of glass pipe bundle condenser | |
| CN205228237U (en) | Take soda plate heat exchanger of desuperrheater | |
| CN202814202U (en) | Forced circulation heat exchanger | |
| CN104089504A (en) | Vapor-water plate heat exchanger | |
| CN101694356A (en) | Coiled pipe type vapour-liquid heat exchanger | |
| CN104075594A (en) | Double shell pass tubular heat exchanger | |
| CN102580334B (en) | Flash evaporator | |
| CN201173725Y (en) | High-temperature vapour water heat exchanger | |
| CN205808184U (en) | Efficiently U-tube volumetric heat exchanger | |
| CN202008309U (en) | Condenser for heating | |
| CN108645251A (en) | A kind of chemical heat exchanger that heat-transfer effect is good | |
| CN103994672A (en) | Efficient double-cavity turbulent heat exchanger | |
| CN206113728U (en) | Ready -package condenser | |
| CN203190826U (en) | Welded sheet condenser | |
| CN204778907U (en) | Evaporation plant who handles coking desulfurization waste liquid is exclusively used in |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20141203 Effective date of abandoning: 20160127 |
|
| C25 | Abandonment of patent right or utility model to avoid double patenting |