CN203518661U - Air tower spray condenser with non-filler cooling tower system - Google Patents
Air tower spray condenser with non-filler cooling tower system Download PDFInfo
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- CN203518661U CN203518661U CN201320383747.0U CN201320383747U CN203518661U CN 203518661 U CN203518661 U CN 203518661U CN 201320383747 U CN201320383747 U CN 201320383747U CN 203518661 U CN203518661 U CN 203518661U
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- spray condenser
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- tower spray
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Abstract
The utility model discloses an air tower spray condenser with a non-filler cooling tower system. The air tower spray condenser with the non-filler cooling tower system comprises a non-filler cooling tower, an air tower spray condenser body and a transfer pool, wherein the non-filler cooling tower comprises a tower body, a water receiving device is arranged at the upper portion inside the tower body, an atomization device is arranged at the lower portion inside the tower body and is connected with a main water inlet pipe A; the main water inlet pipe is connected with the transfer pool; the air tower spray condenser body comprises a barrel, a main water inlet pipe B arranged outside the barrel, a water outlet formed in the bottom of the barrel, and a condensation component arranged inside the barrel; the water outlet of the air tower spray condenser body is connected with a water outlet pipeline; the water outlet pipeline is connected with the transfer pool; the other end of the main water inlet pipe B is also connected with the transfer pool. Due to the fact that the non-filler cooling tower and the air tower spray condenser body are combined to be used, cooling water of the air tower spray condenser body is water cooled by the non-filler cooling tower in advance, the vacuum degree of the air tower spray condenser body can be improved greatly, the efficiency is improved, and energy consumption is reduced.
Description
Technical field
The utility model relates to a kind of high-vacuum apparatus, particularly a kind of empty tower spray condenser.
Background technology
The condensation element of at present general empty tower spray condenser is generally comprised of drip water plate and cooling tubulation, having pipeline easily stops up, the shortcoming that cooling water is inhomogeneous, making to be condensed gas can not be fully and cooling water heat exchange, thereby abundant condensation condensable gas, therefore weak effect, system energy consumption is high, yield poorly, production cost is high.And in general, the cooling effect of empty tower spray condenser is better, the temperature in condenser is lower, and its vacuum is lower, better once the lower evaporation effect of effect two effect vacuum.
Summary of the invention
Goal of the invention of the present utility model is: for the problem of above-mentioned existence, provide a kind of and can significantly improve vacuum, empty tower spray condenser.
The technical solution adopted in the utility model is such: a kind of empty tower spray condenser with cooling tower without filling material system, comprise cooling tower without filling material, empty tower spray condenser and transfer pond, describedly without the cold tower of filler, comprise tower body, described tower body internal upper part is provided with water collection device, bottom is provided with atomising device, described atomising device is connected with water inlet manifold A, and described water inlet manifold is connected with transfer pond; Described empty tower spray condenser comprises cylindrical shell, be located at water inlet manifold B outside cylindrical shell, be provided with delivery port and be located at the condensation element in cylindrical shell with cylinder body bottom, the delivery port of described empty tower spray condenser is connected with outlet conduit, described outlet conduit is connected with transfer pond, the other end of described water inlet manifold B is also connected with transfer pond, described condensation element comprises atomizer and drip water plate, the staggered cylinder inboard wall that is fixed on of drip water plate, atomizer is stratified and set in cylindrical shell, and setting alternate with drip water plate.
As preferably: described cooling tower without filling material top at least, lower than 2 meters of empty tower spray condenser bottoms, is provided with water pump on described water inlet manifold B.
The water of the water inlet manifold B of empty tower spray condenser is from transfer pond, through the condensed water of empty tower spray condenser, by delivery port and outlet conduit, enters again transfer pond, and the water in transfer pond can enter without filler cooling carry out cooling.And for empty tower spray condenser, by the indirect steam in vapo(u)rization system, from air inlet pipe, enter in cylindrical shell, from the cooling water in transfer pond, by water inlet manifold B, enter belt water tank, by taking over from atomizer, be vaporific evenly sprinkling downwards again, condensable gas is carried out in a large number, fully condensation, and condensed water to have passed through cooling tower without filling material cooling, make native system better form high vacuum state, reach consumption reduction, energy-conservation, the object of volume increase, can be widely used in chemical industry, medicine, the multiple-effect evaporation production technology of the industries such as metallurgy, enter low 1 degree of temperature of empty tower spray condenser cooling water, empty tower spray condenser vacuum just can improve 1%, thereby energy-conservation 10%.
Empty tower spray condenser is set to higher than cooling tower without filling material, and the cooling water in transfer pond need to be with being pumped into empty tower spray condenser, and the water outlet of empty tower spray condenser can flow directly into transfer pond by pressure reduction, has also saved energy consumption.
In sum, owing to having adopted technique scheme, the beneficial effects of the utility model are: due to by cooling tower without filling material and empty tower spray condenser coupling, the cooling water of empty tower spray condenser is to carry out cooling in advance water through cooling tower without filling material, thereby can greatly improve the vacuum of empty tower spray condenser, thereby raise the efficiency, save energy consumption.
Accompanying drawing explanation
Fig. 1 is the structural representation of empty tower spray condenser in the utility model embodiment;
Fig. 2 is the structural representation of cooling tower without filling material in the utility model embodiment.
Mark in figure: 1 is delivery port, 2 is hypocentrum, and 3 is feet, and 4 is water inlet pipe reinforcement, 5 is indirect steam water inlet pipe, and 6 is drip water plate A, and 7 is the water tank that goes in ring, and 8 is water inlet pipe pipe nipple, 9 is water inlet manifold B, and 10 is drip water plate B, and 11 for taking over, and 12 is upper cover, 13 is on-condensible gas escape pipe, and 14 is cylindrical shell, and 15 is manhole, and 16 is atomizer, 17 is tower body, and 18 is water collection device, and 19 is atomising device, and 20 is water inlet manifold A, 21 for being motor, and 22 is blower fan, and 23 is transfer pond.
The specific embodiment
Below in conjunction with accompanying drawing, the utility model is described in detail.
In order to make the purpose of this utility model, technical scheme and advantage clearer, below in conjunction with drawings and Examples, the utility model is further elaborated.Should be appreciated that specific embodiment described herein is only in order to explain the utility model, and be not used in restriction the utility model.
As illustrated in fig. 1 and 2, a kind of empty tower spray condenser with cooling tower without filling material system, comprise cooling tower without filling material, empty tower spray condenser and transfer pond 23, wherein, described empty tower spray condenser comprises cylindrical shell 14, hypocentrum 2, upper cover 12, feet 3, be located at the delivery port 1 of hypocentrum 2 lower ends, the indirect steam water inlet pipe 5 being communicated with cylindrical shell 14 bottoms, water inlet pipe reinforcement 4, be located at the water inlet manifold B9 outside cylindrical shell, be located at the on-condensible gas escape pipe 13 at upper cover 12 tops, be located at the condensation element that atomizer 16 in cylindrical shell 14 and drip water plate form, be located at the belt water tank 7 of cylindrical shell 14 outer walls, and be located at the manhole 15 on cylindrical shell 14, cylindrical shell 14 welds respectively upper cover 12 and hypocentrum 2 up and down, feet 3 arranges four, be welded on respectively on hypocentrum 2, water inlet manifold B9 and cylindrical shell 14 be arranged in parallel, 7 minutes upper and lower two-layer cylindrical shell 14 outer walls that are welded on of water tank that go in ring, and be communicated with water inlet manifold B9 by water inlet pipe pipe nipple 8, atomizer 16 arranges two groups corresponding to annular water tank 7, the two-layer setting of every component, two-layer staggered, atomizer 16 is communicated with belt water tank 7 by taking over 11, at cylindrical shell 14 inwalls and two groups of alternate drip water plate A6 and drip water plate B10 of being welded with of atomizer 16, drip water plate A6 and drip water plate B10 are symmetrical arranged, be first quarter moon shape, and be connected to zigzag baffle plate in string side weld, on drip water plate A6 and drip water plate B10, be evenly drilled with aperture, delivery port 1 is connected with outlet conduit, and described outlet conduit is communicated with transfer pond 23,
Describedly without the cold tower of filler, comprise tower body 17, described tower body 17 internal upper parts are provided with water collection device 18, and bottom is provided with atomising device 19, and described atomising device 19 is connected with water inlet manifold A20, tower body 17 tops are also disposed with blower fan 22 and motor 21, and described water inlet manifold A20 is communicated with transfer pond 23;
Described cooling tower without filling material top, lower than 3 meters of empty tower spray condenser bottoms, is provided with water pump on described water inlet manifold B9, by water pump, will in transfer pond 23, through in cooling tower without filling material, through overcooled water, pump into empty tower spray condenser.
The foregoing is only preferred embodiment of the present utility model; not in order to limit the utility model; all any modifications of doing within spirit of the present utility model and principle, be equal to and replace and improvement etc., within all should being included in protection domain of the present utility model.
Claims (2)
1. the empty tower spray condenser with cooling tower without filling material system, it is characterized in that: comprise cooling tower without filling material, empty tower spray condenser and transfer pond, describedly without the cold tower of filler, comprise tower body, described tower body internal upper part is provided with water collection device, bottom is provided with atomising device, described atomising device is connected with water inlet manifold A, and described water inlet manifold is connected with transfer pond; Described empty tower spray condenser comprises cylindrical shell, be located at water inlet manifold B outside cylindrical shell, be provided with delivery port and be located at the condensation element in cylindrical shell with cylinder body bottom, the delivery port of described empty tower spray condenser is connected with outlet conduit, described outlet conduit is connected with transfer pond, the other end of described water inlet manifold B is also connected with transfer pond, described condensation element comprises atomizer and drip water plate, the staggered cylinder inboard wall that is fixed on of drip water plate, atomizer is stratified and set in cylindrical shell, and setting alternate with drip water plate.
2. the empty tower spray condenser with cooling tower without filling material system according to claim 1, is characterized in that: described cooling tower without filling material top at least, lower than 2 meters of empty tower spray condenser bottoms, is provided with water pump on described water inlet manifold B.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201320383747.0U CN203518661U (en) | 2013-07-01 | 2013-07-01 | Air tower spray condenser with non-filler cooling tower system |
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CN201320383747.0U CN203518661U (en) | 2013-07-01 | 2013-07-01 | Air tower spray condenser with non-filler cooling tower system |
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CN201320383747.0U Expired - Fee Related CN203518661U (en) | 2013-07-01 | 2013-07-01 | Air tower spray condenser with non-filler cooling tower system |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106512881A (en) * | 2016-12-28 | 2017-03-22 | 浙江华源颜料股份有限公司 | Steam recycling tower for oxidation barrel |
CN107490304A (en) * | 2017-09-13 | 2017-12-19 | 浙江天能电池(江苏)有限公司 | Spinning cooling tower |
-
2013
- 2013-07-01 CN CN201320383747.0U patent/CN203518661U/en not_active Expired - Fee Related
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106512881A (en) * | 2016-12-28 | 2017-03-22 | 浙江华源颜料股份有限公司 | Steam recycling tower for oxidation barrel |
CN106512881B (en) * | 2016-12-28 | 2018-04-20 | 浙江华源颜料股份有限公司 | One kind is used for oxidation barrel steam recovery tower |
CN107490304A (en) * | 2017-09-13 | 2017-12-19 | 浙江天能电池(江苏)有限公司 | Spinning cooling tower |
CN107490304B (en) * | 2017-09-13 | 2023-07-21 | 浙江天能电池(江苏)有限公司 | Self-rotating cooling tower |
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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: 20140402 Termination date: 20140701 |
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EXPY | Termination of patent right or utility model |