CN201593930U - Tower-type efficient liquid condensing collector - Google Patents
Tower-type efficient liquid condensing collector Download PDFInfo
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- CN201593930U CN201593930U CN2009202189239U CN200920218923U CN201593930U CN 201593930 U CN201593930 U CN 201593930U CN 2009202189239 U CN2009202189239 U CN 2009202189239U CN 200920218923 U CN200920218923 U CN 200920218923U CN 201593930 U CN201593930 U CN 201593930U
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- tower
- efficient liquid
- tower body
- liquid condensation
- storage tank
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Abstract
The utility model relates to a tower-type efficient liquid condensing collector, which mainly solves the problems of lower heat exchange efficiency and poor gas-liquid separation effect of the present condenser, and is characterized in that two annular cooling coil tubes (6) are connected between a cooling liquid inlet tube (3) and a cooling liquid outlet tube (4); a plurality of rows of tower plates (7) inclined downwards are uniformly distributed on the inner wall of a tower body (5); a temporary storage tank (8) wrapped by a thermal insulation layer (10) is arranged at the lower part of the tower body (5); and a syphon tube (9) protruding outside is arranged at the bottom of the temporary storage tank (8). The tower-type efficient liquid condensing collector has the advantages of compact structure, large heat transfer area, high heat exchange efficiency, no gas condensed in the condensed liquid, good separation effect and lower power consumption.
Description
Technical field:
The utility model relates to a kind of condensing plant, tower specifically efficient liquid condensation gatherer.
Background technology:
In the production process of modern chemistry industry; produce a large amount of fluid products through regular meeting; these fluid products need distillation refining in actual production process; perhaps fluid product and byproduct evaporate from reactor with gas form; all need us that its condensation is got off to become liquid and stored or handle, these operations all need to use condensing plant.
At present, condenses equipment in the Chemical Manufacture, the general next direct withdrawal liquid of vertical or horizontal shell and tube condenser that adopts, and these vertical or horizontal shell and tube condensers that often use generally have the following disadvantages: 1.. the vertical tube-type condenser is in certain height, the heat exchange area of cooling fluid and hot gas is little, make heat exchanger effectiveness low, reaching certain heat exchange efficiency can only increase the length or the number of tubulation, accelerate the circulation rate of cooling fluid, and the gas-liquid separation of condensate liquid and on-condensible gas is bad, cause the vapour lock of condensate flow pipeline easily, directly increased the circulation power consumption of cooling fluid.2.. horizontal shell and tube condenser heat exchange efficiency is low.The cooling fluid temperature difference that the cool cycles tubulation is upper and lower section is low, cause cooling fluid can not from hot gas, draw heat energy effectively, hot gas can not effectively fully be cooled, in order to reach the cooling purpose, also must increase tubulation length or number, accelerate the circulation rate of cooling fluid, so equally also increased the circulation power consumption of cooling fluid.
The utility model content:
In order to solve the above-mentioned problem of existing condenser, the utility model provides a kind of tower efficient liquid condensation gatherer, and this tower efficient liquid condensation gatherer has compact conformation, heat transfer area is big, heat exchange efficiency is high, on-condensible gas good separating effect, the little characteristics of power consumption in the condensate liquid.
The technical solution of the utility model is: a kind of tower efficient liquid condensation gatherer, the coolant outlet that comprises cooling fluid inlet tube, hot gas inlet tube and the tower body top of tower body, tower body bottom, the cooling worm that connects two annulars between cooling fluid inlet, the outlet, the column plate that tower body inner wall even distribution plurality of rows is downward-sloping, temporary storage tank by the heat-insulation layer parcel is arranged at the tower body bottom, and the siphon pipe that leads to the outside is arranged at the temporary storage tank bottom.
Two pipes of described cooling worm be respectively clockwise and counterclockwise around.
Described column plate is 4 rows, and circumferencial direction is disjunct three sections, and respectively arranges column plate and rotate a certain angle successively from the bottom to top.
The described column plate of respectively arranging rotates 30 ° of angles from the bottom to top successively.
The gap is 1/3rd of every segment length between three sections of the described column plates.
Described hot gas inlet tube stretches into tower body inside, and most advanced and sophisticated position is tiltedly below outlet.
Described temporary storage tank and tower body junction are funnel-form.
The utlity model has following beneficial effect: owing to take such scheme, adopt the cooling worm of Crossed Circle, under the situation that does not increase tower body height and diameter, increased the heat exchange area of cooling fluid and hot gas, improved heat exchanger effectiveness; The acting in conjunction of column plate and Crossed Circle cooling worm, steam are risen between cooling worm and are flowed, and form turbulent flow easily, so heat transfer coefficient is higher, have further improved heat exchanger effectiveness; And respectively arrange column plate 7 and rotate a certain angle successively from the bottom to top, it is very little so just to make it the vapour lock that produces, and needing hardly increases extra power consumption, makes that this condenser power consumption is little; Temporary storage tank is arranged at the bottom of tower body, so that the on-condensible gas that contains in the condensate liquid carries out gas-liquid separation once more, makes and carries on-condensible gas in the condensate liquid that obtains hardly secretly; The siphon pipe that is provided with on the temporary storage tank can be with the convenient storage tank of introducing condensate liquid automatically of condensate liquid.
Description of drawings:
Accompanying drawing 1 is a structural representation of the present utility model;
Accompanying drawing 2 is cross sectional representation of 4 row's column plates.
1-hot gas inlet tube among the figure, 2-on-condensible gas inlet tube, 3-cooling fluid inlet tube, 4-coolant outlet, 5-tower body, 6-cooling worm, 7-column plate, 8-temporary storage tank, 9-siphon pipe, 10-heat-insulation layer.
The specific embodiment:
The utility model is described in further detail below in conjunction with accompanying drawing:
By shown in Figure 1, a kind of tower efficient liquid condensation gatherer, comprise tower body 5, the cooling fluid inlet tube 3 of tower body 5 bottoms, the coolant outlet 4 on hot gas inlet tube 1 and top, the cooling fluid inlet, outlet (3,4) cooling worm 6 that connects two annulars between, two pipes of described cooling worm 6 be respectively clockwise and counterclockwise around, cooling worm 6 is under the situation that does not increase tower body 5 height and diameter, increased the heat exchange area of cooling fluid and hot gas, improved heat exchanger effectiveness, dicyclo cooling worm 6 guide functions of having held concurrently, guiding hot gas are gone in ring and are flowed and cause turbulence, increase the time of contact of hot gas and cooling fluid; This cooling worm 6 is easy to install in tower body 5, and gas-flow resistance is little, is difficult for forming the liquid resistance, and adopts the seamless pipe manufacturing can reduce stress influence.
The column plate 7 that tower body 5 inner wall even distribution plurality of rows are downward-sloping, as preferably, column plate 7 is made as 4 rows, the sectional view of each column plate 7 is respectively by shown in a among Fig. 2, b, c, the d, described column plate 7 circumferencial directions are disjunct three sections, the gap is 1/3rd of every segment length between three sections, and respectively arranging column plate 7 rotates a certain angle from the bottom to top successively, as preferably, take to rotate 30 ° of angles, promptly go up row's column plate 7 clockwise or be rotated counterclockwise 30 ° of angles with respect to next row's column plate 7, shown in Fig. 2 for turning clockwise; Column plate 7 and 6 actings in conjunction of Crossed Circle cooling worm, steam rise 6 of cooling worms and flow, and the interference effect owing to inertia force, centrifugal force cause forms turbulent flow easily, so heat transfer coefficient is higher, has further improved heat exchanger effectiveness; And respectively arrange column plate 7 and rotate a certain angle successively from the bottom to top, it is very little so just to make it the vapour lock that produces, needs to increase extra power consumption hardly.
Described hot gas inlet tube 1 stretches into tower body 5 inside, and most advanced and sophisticated position is tiltedly below outlet, prevent to pour in down a chimney and enter hot gas inlet tube 1 along the cooling liquid that drops down under the tower wall, in hot gases tube, form the liquid resistance and influence the operation of front reaction device, moreover hot gas middle part at the bottom of tower evenly disperses to rise mobile, also help effectively increasing the heat exchange area between hot gas and the cooling liquid, promptly improved heat exchanger effectiveness, made full use of the energy of hot gas.
Described temporary storage tank 8 is funnel-form with tower body 5 junctions, and the closing in of certain wide-angle is arranged, can reduce influencing each other between hot gas and the condensate liquid like this, has reduced hot gas the heating once more of condensate liquid is caused boiling.
Eventually the above, this tower efficient liquid condensation collector structure compactness, heat transfer area is big, heat exchange efficiency is high, on-condensible gas good separating effect in the condensate liquid, power consumption are little.In addition, the utility model can adopt the cooling fluid of different temperatures for the steam of different boiling ranges.
Claims (8)
1. tower efficient liquid condensation gatherer, the coolant outlet (4) that comprises cooling fluid inlet tube (3), hot gas inlet tube (1) and tower body (5) top of tower body (5), tower body (5) bottom, it is characterized in that: the cooling worm (6) that connects two annulars between cooling fluid inlet tube (3), the coolant outlet (4), the column plate (7) that tower body (5) inner wall even distribution plurality of rows is downward-sloping, temporary storage tank (8) by heat-insulation layer (10) parcel is arranged at tower body (5) bottom, and the siphon pipe (9) that leads to the outside is arranged at temporary storage tank (8) bottom.
2. tower efficient liquid condensation gatherer according to claim 1 is characterized in that: two pipes of described cooling worm (6) be respectively clockwise and counterclockwise around.
3. tower efficient liquid condensation gatherer according to claim 1 is characterized in that: described column plate (7) is 4 rows.
4. tower efficient liquid condensation gatherer according to claim 3 is characterized in that: described column plate (7) circumferencial direction is disjunct three sections, and respectively arranges column plate (7) and rotate a certain angle successively from the bottom to top.
5. tower efficient liquid condensation gatherer according to claim 4 is characterized in that: the described column plate (7) of respectively arranging rotates 30 ° of angles from the bottom to top successively.
6. tower efficient liquid condensation gatherer according to claim 4 is characterized in that: the gap is 1/3rd of every segment length between (7) three sections of the described column plates.
7. tower efficient liquid condensation gatherer according to claim 1 is characterized in that: described hot gas inlet tube (1) stretches into tower body (5) inside, and most advanced and sophisticated position is tiltedly below outlet.
8. tower efficient liquid condensation gatherer according to claim 1 is characterized in that: described temporary storage tank (8) is funnel-form with tower body (5) junction.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009202189239U CN201593930U (en) | 2009-12-10 | 2009-12-10 | Tower-type efficient liquid condensing collector |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009202189239U CN201593930U (en) | 2009-12-10 | 2009-12-10 | Tower-type efficient liquid condensing collector |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201593930U true CN201593930U (en) | 2010-09-29 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2009202189239U Expired - Fee Related CN201593930U (en) | 2009-12-10 | 2009-12-10 | Tower-type efficient liquid condensing collector |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201593930U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108443860A (en) * | 2018-03-14 | 2018-08-24 | 广州市盛吉成智能科技有限公司 | A kind of condensate water recovery device |
| CN114931991A (en) * | 2022-04-19 | 2022-08-23 | 中核核电运行管理有限公司 | Multifunctional condensation collecting device |
| CN114931990A (en) * | 2022-04-19 | 2022-08-23 | 中核核电运行管理有限公司 | Multifunctional condensation collecting device |
| CN117308631A (en) * | 2023-11-29 | 2023-12-29 | 方诺传热***(江苏)有限公司 | Cooling tower device special for steam and operation method thereof |
-
2009
- 2009-12-10 CN CN2009202189239U patent/CN201593930U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108443860A (en) * | 2018-03-14 | 2018-08-24 | 广州市盛吉成智能科技有限公司 | A kind of condensate water recovery device |
| CN114931991A (en) * | 2022-04-19 | 2022-08-23 | 中核核电运行管理有限公司 | Multifunctional condensation collecting device |
| CN114931990A (en) * | 2022-04-19 | 2022-08-23 | 中核核电运行管理有限公司 | Multifunctional condensation collecting device |
| CN114931991B (en) * | 2022-04-19 | 2024-05-10 | 中核核电运行管理有限公司 | Multifunctional condensation collection device |
| CN117308631A (en) * | 2023-11-29 | 2023-12-29 | 方诺传热***(江苏)有限公司 | Cooling tower device special for steam and operation method thereof |
| CN117308631B (en) * | 2023-11-29 | 2024-02-06 | 方诺传热***(江苏)有限公司 | Cooling tower device special for steam and operation method thereof |
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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 |
Granted publication date: 20100929 Termination date: 20171210 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |