CN2564543Y - Vertical condenser - Google Patents
Vertical condenser Download PDFInfo
- Publication number
- CN2564543Y CN2564543Y CN 02268411 CN02268411U CN2564543Y CN 2564543 Y CN2564543 Y CN 2564543Y CN 02268411 CN02268411 CN 02268411 CN 02268411 U CN02268411 U CN 02268411U CN 2564543 Y CN2564543 Y CN 2564543Y
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- pipe
- water
- steam
- cooling
- cylindrical shell
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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
Disclosed is a vertical condensator belonging to the water distillation equipment field. The device includes a steam inlet pipe, a cooling water inlet pipe, a condensate water inlet pipe, a cooling water outlet pipe and a drum. The drum is communicated with a distillation water outlet pipe. The device is characterized in that the cooling water inlet pipe is arranged on the lower part of the drum, and the steam inlet pipe and the condensate water inlet pipe are arranged on the upper part of the drum, the steam condensation pipe and the condensate water cooling pipe are arranged in the drum, one end of the steam condensation pipe and one end of the condensate water cooling pipe are communicate with the steam condensation pipe and the condensate water cooling pipe, and the other end of the steam condensation pipe and the other end of the condensate water cooling pipe are communicated with the distillation water outlet pipe. For the adoption of the structure that the steam flows in the pipe and the cooling water flows in the drum, the utility model not only reduces the loss of steam and heat energy, but lowers the temperature of the environment around the condensator, thus being conducive to the physical health of the workers; on the other hand, the adoption of the negative heat exchange structure in which the steam flows from the top to bottom and the cooling water from bottom to top is not only good for raising the efficiency of heat exchange, but for the sufficiently utilizing of the steam energy.
Description
Technical field
The utility model belongs to water distillation plant field, particularly a kind of condenser.
Background technology
The equipment of producing medical distilled water generally adopts multi-effect water distillator, and this distillation machine is made up of condenser and a plurality of vaporizer.At present, steam is carried out condenser condensing generally adopt horizontal condenser, promptly condenser is horizontal on methods, rack on the multi-effect water distillator.The cylindrical shell two ends of condenser are provided with flange and blind flange respectively, and steam inlet pipe, distilled water outlet Guan Junyu cylindrical shell are connected.The steam that comes out in the vaporizer enters inner barrel by the steam inlet pipe, at the inner stream of consubstantiality; Water coolant enters in the intravital refrigeration cycle pipe of tube by the entrance of cooling water pipe, flows in pipe; Water coolant in the pipe becomes distilled water to managing outer high-temperature steam cooling condensation behind the intravital vapor condensation of tube, and distilled water is derived from the distilled water outlet pipe.There is following deficiency in process of production in this kind horizontal condenser:
(1) because high-temperature steam is mobile in cylindrical shell, and cylindrical shell is not done the insulation processing, and it is bigger to distribute heat energy.Like this, the envrionment temperature in the work-yard will raise, and is unfavorable for that the operator's is healthy; Simultaneously, the Controlling System and the electric installation of surrounding devices caused damage, and also wasted the energy.
(2) heat exchanger effectiveness of horizontal condenser is low.The cooling range that the refrigeration cycle pipe is upper and lower section is low, caused water coolant from the intravital steam of tube, not draw heat energy effectively, so both caused steam effectively fully not cooled off, also make come out in the condenser to enter the water temperature that condiments water is used in the vaporizer not high, strengthened the steam consumption that enters in the 1st effective evaporator.
Summary of the invention
For the practical problems that the horizontal condenser that overcomes prior art exists, the utility model provides a kind of vertical (type) condenser, and this condenser can reduce the heat radiation of steam, the envrionment temperature around the reduction condenser, and the heat exchanger effectiveness height.
The technical scheme that its technical problem that solves the utility model adopts is: design a kind of vertical (type) condenser, comprise the steam inlet pipe, the entrance of cooling water pipe, coagulate the water inlet pipe, cooling water outlet pipe and cylindrical shell, the two ends of cylindrical shell are provided with flange and blind flange respectively, the distilled water outlet pipe is connected with cylindrical shell, it is characterized in that the entrance of cooling water pipe is arranged on the bottom of cylindrical shell, the steam inlet pipe, the water inlet pipe is arranged on the top of cylindrical shell with fixed attention, steam condenser pipe is set in the cylindrical shell and coagulates water composite cooling pipe, steam condenser pipe, an end that coagulates water composite cooling pipe respectively with the steam inlet pipe, coagulate the water inlet pipe and be connected steam condenser pipe, the other end that coagulates water composite cooling pipe communicates with the distilled water outlet pipe.
Steam condenser pipe of the present utility model, coagulate water composite cooling pipe and can adopt tubulation, the upper and lower part of cylindrical shell is provided with upper and lower tube sheet, constitute vapor chamber between upper tubesheet and the upper flange and coagulate water cavity, vapor chamber and coagulate between the water cavity and isolate by dividing plate, the top of vapor chamber is connected with the steam inlet pipe, the bottom communicates with steam condenser pipe, the top of coagulating water cavity with coagulate that the water inlet pipe is connected, the bottom is connected with water composite cooling pipe with fixed attention, constitute the distillation water cavity between lower tubesheet and the lower flange, the distillation water cavity is connected with the distilled water outlet pipe.Steam condenser pipe, coagulate water composite cooling pipe and can also adopt straight tube, steam condenser pipe, coagulate water composite cooling pipe an end respectively with the steam inlet pipe, coagulate the water inlet pipe and be connected, the bottom of cylindrical shell is provided with tube sheet, constitute the distillation water cavity between tube sheet and the lower flange, steam condenser pipe, coagulate water composite cooling pipe and be connected with the distillation water cavity, distill water cavity and be connected with the distilled water outlet pipe by tube sheet.
For improving heat exchanger effectiveness, more than one traverse baffle is set in the cylindrical shell, each traverse baffle is staggered and constitutes snakelike chamber, and an end in snakelike chamber is connected with the entrance of cooling water pipe, the other end is connected with cooling water outlet pipe.Entrance of cooling water is offered in lower end at barrel wall, and entrance of cooling water is connected with the entrance of cooling water pipe.The outer setting thermal insulation layer of cylindrical shell.
The beneficial effects of the utility model are: owing to adopted steam to flow and water coolant mobile structure formation in cylindrical shell in pipe, reduced and reduced the steam heat loss of energy, also reduce simultaneously condenser envrionment temperature on every side, be of value to the healthy of workman; Moreover, adopt steam from top to bottom, the reverse heat exchange structure form that constitutes from bottom to top of water coolant, also improved heat exchanger effectiveness, made full use of steam energy.
Description of drawings
Below in conjunction with accompanying drawing the utility model is further elaborated.
Fig. 1 is the structural representation of an embodiment of the utility model;
Fig. 2 is the structural representation of another embodiment of the utility model;
Fig. 3 is the snakelike cavity configuration synoptic diagram that is made of traverse baffle.
Embodiment
Embodiment one
As shown in Figure 1: entrance of cooling water pipe 11 is arranged on the bottom of cylindrical shell 16, steam inlet pipe 2, coagulates the top that water inlet pipe 5 is arranged on cylindrical shell 16, steam condenser pipe 17 is set in the cylindrical shell 16 and coagulates water composite cooling pipe 9, steam condenser pipe, coagulates water composite cooling pipe and all adopts tubulation; Upper tubesheet 7, lower tubesheet 14 are set in the upper and lower part of cylindrical shell 16, constitute vapor chamber 1 between upper tubesheet 7 and the flange 8 and coagulate water cavity 6, vapor chamber 1 and coagulate between the water cavity 6 and isolate by dividing plate 3, the top of vapor chamber 1 is connected with steam inlet pipe 2, the bottom communicates with steam condenser pipe 17, the top of coagulating water cavity 6 with coagulate that water inlet pipe 5 is connected, the bottom is connected with water composite cooling pipe 9 with fixed attention, constitute distillation water cavity 12 between lower tubesheet 14 and the flange 15, distillation water cavity 12 is connected with distilled water outlet pipe 13.A plurality of traverse baffles 10 are set in the cylindrical shell 16, and each traverse baffle is staggered and constitutes snakelike chamber, and an end in snakelike chamber is connected with entrance of cooling water pipe 11, the other end is connected with cooling water outlet pipe 18.Entrance of cooling water is offered in the lower end of barrel wall, and entrance of cooling water is connected with entrance of cooling water pipe 11.For insulation, at the outer setting thermal insulation layer of cylindrical shell.
The high-temperature steam that comes out from vaporizer enters vapor chamber 1 in steam inlet pipe 2, the logical steam vent (not drawing among the figure) on upper tubesheet 7 enters in the steam condenser pipe 17 then; The hyperthermal distilled water that comes out from vaporizer enters water cavity 6 with fixed attention from coagulating water inlet pipe 5, then in water distributing tray 4 and upper tubesheet enter into fixed attention water composite cooling pipe 9.Water coolant rises from entrance of cooling water pipe 11 interior inflow cylindrical shells and along cylindrical shell.Be subjected to the effect of traverse baffle, water coolant is made the serpentine curve along the snakelike chamber (shown in Figure 3) that traverse baffle is formed and is risen, and this kind rising mode has increased the rise time of water coolant, has also just increased the time that water coolant and steam carry out heat exchange.The intravital water coolant of tube is drawn steam thermal energy respectively, draws distilled water heat energy from is coagulated water composite cooling pipe from steam condenser pipe in uphill process.Therefore, steam enters in the distilled water chamber 12 after being condensed into distilled water by cooling, discharges by distilled water outlet pipe 13 then; Also enter in the distillation water cavity 12 after hyperthermal distilled water in the water composite cooling pipe 9 is lowered the temperature with fixed attention, discharge by distilled water outlet pipe 13 at last.In this heat exchanging process, the intravital water coolant of tube has been realized gradient increased temperature in uphill process, after cooling water outlet pipe 18 discharges; High-temperature vapour in the steam condenser pipe 17 and coagulate in the process that the hyperthermal distilled water in the water composite cooling pipe 9 descends in pipe and realized gradient cooling.The mode of this kind gradient increased temperature and gradient cooling has improved heat exchanger effectiveness, has made full use of heat energy.Simultaneously, steam flows in pipe, and pipe is located at the heat-energy losses that frame mode in the water coolant has also effectively been avoided steam, has improved energy utilization rate, has reduced the envrionment temperature around the condenser.Embodiment two
Steam condenser pipe of the present utility model, coagulate water composite cooling pipe and can also adopt straight tube (also can adopt spiral tube), the bottom of cylindrical shell is provided with tube sheet, constitutes the distillation water cavity between tube sheet and the flange.Steam condenser pipe 19, coagulate water composite cooling pipe 20 top respectively with steam inlet pipe 24, coagulate water inlet pipe 25 and be connected, steam condenser pipe 19, the bottom of coagulating water composite cooling pipe 20 are connected with distillation water cavity 22 by tube sheet 21, distill water cavity 22 and are connected with distilled water outlet pipe 23.Other frame modes are identical with embodiment one with principle of work.
Claims (6)
1. vertical (type) condenser, comprise the steam inlet pipe, the entrance of cooling water pipe, coagulate the water inlet pipe, cooling water outlet pipe and cylindrical shell, the two ends of cylindrical shell are provided with upper flange respectively, lower flange, cylindrical shell is communicated with the distilled water outlet pipe, it is characterized in that the entrance of cooling water pipe is arranged on the bottom of cylindrical shell, the steam inlet pipe, the water inlet pipe is arranged on the top of cylindrical shell with fixed attention, steam condenser pipe is set in the cylindrical shell and coagulates water composite cooling pipe, steam condenser pipe, an end that coagulates water composite cooling pipe respectively with the steam inlet pipe, coagulate the water inlet pipe and be connected steam condenser pipe, the other end that coagulates water composite cooling pipe communicates with the distilled water outlet pipe.
2. vertical (type) condenser according to claim 1, it is characterized in that steam condenser pipe, coagulate water composite cooling pipe and all adopt tubulation, the upper and lower part of cylindrical shell is provided with upper and lower tube sheet, constitute vapor chamber between upper tubesheet and the upper flange and coagulate water cavity, vapor chamber and coagulate between the water cavity and isolate by dividing plate, the top of vapor chamber is connected with the steam inlet pipe, the bottom communicates with steam condenser pipe, the top of coagulating water cavity with coagulate that the water inlet pipe is connected, the bottom is connected with water composite cooling pipe with fixed attention, constitute the distillation water cavity between lower tubesheet and the lower flange, the distillation water cavity is connected with the distilled water outlet pipe.
3. vertical (type) condenser according to claim 1, it is characterized in that steam condenser pipe, coagulate water composite cooling pipe and all adopt straight tube, steam condenser pipe, coagulate water composite cooling pipe an end respectively with the steam inlet pipe, coagulate the water inlet pipe and be connected, the bottom of cylindrical shell is provided with tube sheet, constitute the distillation water cavity between tube sheet and the lower flange, steam condenser pipe, coagulate water composite cooling pipe and be connected with the distillation water cavity, distill water cavity and be connected with the distilled water outlet pipe by tube sheet.
4. according to claim 1 or 2 or 3 described vertical (type) condensers, it is characterized in that being provided with in the cylindrical shell more than one traverse baffle, each traverse baffle is staggered and constitutes snakelike chamber, and an end in snakelike chamber is connected with the entrance of cooling water pipe, the other end is connected with cooling water outlet pipe.
5. according to claim 1 or 2 or 3 or 4 described vertical (type) condensers, it is characterized in that entrance of cooling water is offered in the lower end of barrel wall, entrance of cooling water is connected with the entrance of cooling water pipe.
6. vertical (type) condenser according to claim 1 is characterized in that the outer setting thermal insulation layer of cylindrical shell.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 02268411 CN2564543Y (en) | 2002-07-15 | 2002-07-15 | Vertical condenser |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 02268411 CN2564543Y (en) | 2002-07-15 | 2002-07-15 | Vertical condenser |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2564543Y true CN2564543Y (en) | 2003-08-06 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 02268411 Expired - Fee Related CN2564543Y (en) | 2002-07-15 | 2002-07-15 | Vertical condenser |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2564543Y (en) |
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102350062A (en) * | 2011-07-22 | 2012-02-15 | 浙江一火科技有限公司 | Separation device for degreased mixed liquid |
| CN102849810A (en) * | 2012-09-03 | 2013-01-02 | 北京航空航天大学 | Novel combination type evaporation condenser |
| CN103834476A (en) * | 2012-11-26 | 2014-06-04 | 北京中天金谷粮油工程技术有限公司 | Fatty acid condenser for edible oil |
| CN104075489A (en) * | 2014-07-19 | 2014-10-01 | 烟台明辉热泵节能科技有限公司 | High-temperature steam heat pump unit |
| CN105188879A (en) * | 2013-03-15 | 2015-12-23 | 住友化学株式会社 | Mist separation apparatus, reactive system, epsilon-caprolactam production method, and use in production of epsilon-caprolactam |
| CN105384150A (en) * | 2015-12-04 | 2016-03-09 | 广西农垦糖业集团柳兴制糖有限公司 | Vertical water jacket for cooling of sulfur dioxide gas |
| CN106931682A (en) * | 2017-04-18 | 2017-07-07 | 美的集团武汉制冷设备有限公司 | Air-conditioning system |
| CN107062695A (en) * | 2017-04-18 | 2017-08-18 | 广东美的制冷设备有限公司 | Air-conditioning system |
| CN107906641A (en) * | 2017-10-24 | 2018-04-13 | 广西柳工机械股份有限公司 | LNG air-conditioner of engineering machinery systems |
| CN108441397A (en) * | 2018-06-12 | 2018-08-24 | 泸州市润达机械设备有限公司 | Cooling device and distillation cooling device |
| CN111544918A (en) * | 2020-05-19 | 2020-08-18 | 常州海克莱化学有限公司 | Condensing equipment for distillation plant |
| CN113624046A (en) * | 2021-08-11 | 2021-11-09 | 广东工业大学 | Array fin type condensing device and loop heat pipe |
| CN113624047A (en) * | 2021-08-11 | 2021-11-09 | 广东工业大学 | Condenser with embedded radial micro-channel and loop heat pipe |
-
2002
- 2002-07-15 CN CN 02268411 patent/CN2564543Y/en not_active Expired - Fee Related
Cited By (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102350062A (en) * | 2011-07-22 | 2012-02-15 | 浙江一火科技有限公司 | Separation device for degreased mixed liquid |
| CN102849810A (en) * | 2012-09-03 | 2013-01-02 | 北京航空航天大学 | Novel combination type evaporation condenser |
| CN103834476A (en) * | 2012-11-26 | 2014-06-04 | 北京中天金谷粮油工程技术有限公司 | Fatty acid condenser for edible oil |
| CN105188879A (en) * | 2013-03-15 | 2015-12-23 | 住友化学株式会社 | Mist separation apparatus, reactive system, epsilon-caprolactam production method, and use in production of epsilon-caprolactam |
| CN104075489A (en) * | 2014-07-19 | 2014-10-01 | 烟台明辉热泵节能科技有限公司 | High-temperature steam heat pump unit |
| CN105384150A (en) * | 2015-12-04 | 2016-03-09 | 广西农垦糖业集团柳兴制糖有限公司 | Vertical water jacket for cooling of sulfur dioxide gas |
| CN106931682A (en) * | 2017-04-18 | 2017-07-07 | 美的集团武汉制冷设备有限公司 | Air-conditioning system |
| CN107062695A (en) * | 2017-04-18 | 2017-08-18 | 广东美的制冷设备有限公司 | Air-conditioning system |
| CN107906641A (en) * | 2017-10-24 | 2018-04-13 | 广西柳工机械股份有限公司 | LNG air-conditioner of engineering machinery systems |
| CN108441397A (en) * | 2018-06-12 | 2018-08-24 | 泸州市润达机械设备有限公司 | Cooling device and distillation cooling device |
| CN111544918A (en) * | 2020-05-19 | 2020-08-18 | 常州海克莱化学有限公司 | Condensing equipment for distillation plant |
| CN113624046A (en) * | 2021-08-11 | 2021-11-09 | 广东工业大学 | Array fin type condensing device and loop heat pipe |
| CN113624047A (en) * | 2021-08-11 | 2021-11-09 | 广东工业大学 | Condenser with embedded radial micro-channel and loop heat pipe |
| CN113624046B (en) * | 2021-08-11 | 2022-11-18 | 广东工业大学 | Array fin type condensing device and loop heat pipe |
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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 |