CN205138246U - Multistage condensing system - Google Patents
Multistage condensing system Download PDFInfo
- Publication number
- CN205138246U CN205138246U CN201520902939.7U CN201520902939U CN205138246U CN 205138246 U CN205138246 U CN 205138246U CN 201520902939 U CN201520902939 U CN 201520902939U CN 205138246 U CN205138246 U CN 205138246U
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- China
- Prior art keywords
- drainer
- coiled
- condenser
- cooling tower
- cooling
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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses a multistage condensing system, package rubbing board formula condenser, the cooling tower, the liquid storage pot, the coiled drainer, plate type condenser's steam inlet and steam pipe or hot water pipe connected, plate type condenser's liquid outlet and liquid storage pot inlet are connected, the liquid outlet and the coiled drainer inlet of liquid storage pot are connected, the delivery port of cooling tower and the coolant liquid entry linkage of condenser and coiled drainer, the cooling liquid exit of condenser and coiled drainer is connected with the water inlet of cooling tower, plate type condenser is one or more, all plate type condenser are parallelly connected mode, wherein the coiled drainer is one or more, wherein the coiled drainer is for establishing ties or establish ties and the parallelly connected mode that combines, the coolant liquid entry of coiled drainer is all direct continuous with the cooling tower delivery port, the export of coolant liquid links to each other with the water inlet of cooling tower. Can increase through connecting plate type condenser in parallel steam or hydrothermal condensation rate, improve production efficiency.
Description
Technical field
The utility model relates to a kind of multi-stage condensing system, especially relates to a kind of chemical industry, medicine, food, the multi-stage condensing system of brewing industry.
Background technology
Due to usually steam or heatable substance can be used in the industry such as chemical industry, medicine, needs cooling, and under normal circumstances, many companies adopt the series connection of condensing plant to achieve the goal, but ignore production efficiency, and energy ezpenditure is excessive.
Summary of the invention
The purpose of this utility model is to provide a kind of energy efficiently and condensation effect is good, and energy consumption is low simultaneously, saves the multi-stage condensing equipment of water.
A kind of multi-stage condensing system, comprise plate-type condenser, cooling tower, fluid reservoir, coiled drainer, the air intake of described plate-type condenser is connected with steam pipe or hot-water line, the liquid outlet of plate-type condenser is connected with fluid reservoir inlet, the liquid outlet of fluid reservoir is connected with coiled drainer inlet, and the delivery port of cooling tower is connected with the cooling fluid entrance of condenser and coiled drainer, and condenser is connected with the water inlet of cooling tower with the cooling liquid outlet of coiled drainer.
Further improvement of the utility model, because the flow of plate-type condenser is little, in time can not meeting plant produced demand, can by plate-type condenser be at least set to one, when for time multiple, all plate-type condensers are paralleling model, and liquid outlet is all connected with fluid reservoir.
Further improve, described coiled tube condenser is one or more, when for more than one, wherein coiled drainer is the pattern that series connection or series and parallel connections combine, and the cooling fluid entrance of described coiled drainer is all direct is connected with cooling tower delivery port, the outlet of cooling fluid is connected with the water inlet of cooling tower.
The beneficial effects of the utility model are: by the condensation rate that can increase steam or hot water that is together in parallel by plate-type condenser, enhance productivity, when needing the liquid of required condensation to be more suitable for producing with a lower temperature in production process, collected through plate-type condenser cooling fluid by fluid reservoir, the unified coiled drainer combined through series connection or connection in series-parallel further cools again, and the cooling flow of coiled drainer is slightly large, series connection or series-parallel pattern can be selected as required to produce, both the demand of flow had been met, also the needs producing required chilling temperature can be met, carry out the combination of condensing plant.
Accompanying drawing explanation
The simple view of Fig. 1 multi-stage condensing system.
In figure: 1 is reactor; 2 plate-type condensers; 3 fluid reservoirs; 4 coiled drainers; 5 fluid reservoirs; 6 condensate return pipes; 7 cooling towers; 8 materail tubes; 9 cooling water pipes.
Detailed description of the invention
A kind of multi-stage condensing system, comprise plate-type condenser, cooling tower, fluid reservoir, coiled drainer, the air intake of described plate-type condenser is connected with steam pipe or hot-water line, the liquid outlet of plate-type condenser is connected with fluid reservoir inlet, the liquid outlet of fluid reservoir is connected with coiled drainer inlet, and the delivery port of cooling tower is connected with the cooling fluid entrance of condenser and coiled drainer, and condenser is connected with the water inlet of cooling tower with the cooling liquid outlet of coiled drainer.
This programme further improves, and described plate-type condenser is multiple, and all plate-type condensers are paralleling model, and liquid outlet is all connected with fluid reservoir.
This programme further improves, and described coiled drainer is multiple, and wherein coiled drainer is the pattern that series connection or series and parallel connections combine.
In above-mentioned all technical schemes, the cooling fluid entrance of described coiled drainer is all direct to be connected with cooling tower delivery port, and the outlet of cooling fluid is connected with the water inlet of cooling tower.
Embodiment 1.
As shown in Figure 1, in reactor 1 produce vapours or hot liquid enters into two plate-type condensers 2 through materail tube 8, the condensed water that cooling tower 7 produces flows through plate-type condenser 2 through condensate pipe 9, heat exchange is carried out to the material in plate-type condenser 2, now the temperature of material declines to some extent, and the water temperature of condensed water heats up, now material continues to enter into fluid reservoir 3 through materail tube 8, condensed water continuation backflow after intensification enters into cooling tower and cools, arrive after certain position until fluid reservoir 3 liquid level, continuation cooling can be carried out by boot disk tubular type drainer to material, because the material flow of coiled drainer is very fast, single or multiple coiled drainer can be taked to connect or according to the pattern that need of production adopts multiple coiled drainer to carry out series and parallel connections combination, continuation cooling is carried out to material, material after cooling continues through materail tube and flow into fluid reservoir 5, all plate-type condensers are all connected with materail tube 8 with material outlet with the material inlet of coiled drainer, all plate-type condensers are all connected with condensate pipe 9 with the cooling fluid entrance of coiled drainer, outlet is all connected with condensate return pipe.
By adopting multi-stage condensing system, accelerate about 60% to the cooling velocity of honeysuckle distillation in the production process of the distilled liquid of honeysuckle, the temperature of temperature and traditional single stage condenser system is low about 10 ~ 20 DEG C, enhances productivity preferably, within the unit interval, more multiple batches of product can be produced.
The foregoing is only embodiment of the present utility model; not thereby scope of patent protection of the present utility model is limited; every utilize the utility model description and accompanying drawing content thereof to do equivalent structure or equivalence transformation; or direct or indirect other association areas used beyond the utility model, all can be considered in scope of patent protection of the present utility model.
Claims (5)
1. a multi-stage condensing system, it is characterized in that: comprise plate-type condenser, cooling tower, fluid reservoir, coiled drainer, the air intake of described plate-type condenser is connected with steam pipe or hot-water line, the liquid outlet of plate-type condenser is connected with fluid reservoir inlet, the liquid outlet of fluid reservoir is connected with coiled drainer inlet, the delivery port of cooling tower is connected with the cooling fluid entrance of condenser and coiled drainer, and condenser is connected with the water inlet of cooling tower with the cooling liquid outlet of coiled drainer.
2. multi-stage condensing system according to claim 1, is characterized in that, described plate-type condenser is multiple, and all plate-type condensers are paralleling model, and liquid outlet is all connected with fluid reservoir.
3. multi-stage condensing system according to claim 2, is characterized in that, described coiled drainer is multiple, and wherein coiled drainer is series connection.
4. multi-stage condensing system according to claim 2, is characterized in that, described coiled drainer is multiple, and wherein coiled drainer is the pattern that series and parallel connections combines.
5. the multi-stage condensing system according to claim 3 or 4, is characterized in that, the cooling fluid entrance of described coiled drainer is all direct to be connected with cooling tower delivery port, and the outlet of cooling fluid is connected with the water inlet of cooling tower.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520902939.7U CN205138246U (en) | 2015-11-13 | 2015-11-13 | Multistage condensing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520902939.7U CN205138246U (en) | 2015-11-13 | 2015-11-13 | Multistage condensing system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205138246U true CN205138246U (en) | 2016-04-06 |
Family
ID=55624032
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520902939.7U Expired - Fee Related CN205138246U (en) | 2015-11-13 | 2015-11-13 | Multistage condensing system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205138246U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108434923A (en) * | 2018-06-01 | 2018-08-24 | 洛阳丰瑞氟业有限公司 | A kind of hydrogen fluoride gas condenser system and method |
-
2015
- 2015-11-13 CN CN201520902939.7U patent/CN205138246U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108434923A (en) * | 2018-06-01 | 2018-08-24 | 洛阳丰瑞氟业有限公司 | A kind of hydrogen fluoride gas condenser system and method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160406 Termination date: 20191113 |