CN203777684U - Falling film evaporation device - Google Patents
Falling film evaporation device Download PDFInfo
- Publication number
- CN203777684U CN203777684U CN201320879767.7U CN201320879767U CN203777684U CN 203777684 U CN203777684 U CN 203777684U CN 201320879767 U CN201320879767 U CN 201320879767U CN 203777684 U CN203777684 U CN 203777684U
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- China
- Prior art keywords
- cover
- distributing
- falling film
- cylinder
- evaporation device
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- 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.)
- Expired - Fee Related
Links
- 239000011552 falling film Substances 0.000 title claims abstract description 19
- 230000008020 evaporation Effects 0.000 title claims abstract description 18
- 238000001704 evaporation Methods 0.000 title claims abstract description 18
- 238000007600 charging Methods 0.000 claims description 17
- 230000000740 bleeding effect Effects 0.000 claims description 3
- 238000007599 discharging Methods 0.000 claims description 3
- 239000007788 liquid Substances 0.000 abstract description 8
- 238000004519 manufacturing process Methods 0.000 abstract description 5
- 239000000126 substance Substances 0.000 abstract description 3
- 238000010438 heat treatment Methods 0.000 abstract description 2
- 239000011344 liquid material Substances 0.000 abstract description 2
- 239000012528 membrane Substances 0.000 abstract 1
- 239000010408 film Substances 0.000 description 15
- 239000004744 fabric Substances 0.000 description 6
- 238000000034 method Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 229940127554 medical product Drugs 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses chemical equipment and particularly relates to a falling film evaporation device of a liquid material. The device comprises an upper cover, a lower cover and a pipe body connected by flanges to form a barrel, wherein a feed inlet is formed in the upper end of the upper cover and a distributing disc is connected to the lower part of the upper cover; a steam chamber is arranged on one side of the pipe body located below the distributing disc, the steam chamber is connected with a steam inlet, an exhaust opening is formed in one side on the upper part of the lower cover while a suction opening is formed in the other side on the upper part of the lower cover, and a discharge opening is formed in the lower part of the lower cover. A plurality of orifices are formed in the distributing disc, the lower end of each orifice is connected with a distributing head and the outer wall of the distributing head is sleeved with a hollow tube. The distributing head consists of the upper cover, an S-shaped guide slot, a second-level distributing plate and a third-level distributing plate, so that the to-be-concentrated liquid entering the distributing head is subjected to three-level guiding through the S-shaped guide slot, the second-level distributing plate and the third-level distributing plate to form a uniform membrane which moves downward along the inner wall of the tube to the maximum extent, so that the heat efficiency and the production efficiency are greatly improved. Heating steam entering the falling film evaporation device is split to move downward through a flow split baffle in the barrel to carry out full heat exchange, so that the heat utilization ratio is increased.
Description
Technical field
The utility model relates to a kind of chemical industry equipment, is specifically related to a kind of falling film evaporation device of liquid material.
Background technology
The concentration process that often relates to reactant liquor or extract in chemical industry, medical product research, production, this concentration process normally carries out in a kind of evaporimeter, and falling film evaporation device is considered to an efficient evaporation concentration device.The efficiency of utilization of this type of falling film evaporator and production efficiency depend on the film forming situation of solution to be concentrated on falling film evaporator tubulation inwall.Film forming is more even, and the thermal efficiency is just higher.The uniformity of film forming depends mainly on again the structure of filming device, has reported various types of falling film evaporation devices, all in the structure of filming device, improves.But existing filming device all adopts a substandard cloth film or two substandard cloth films, actual conditions are the effects due to liquid cohesive force, the liquid of film forming can reassemble into drop and drip along tubulation middle part in descending process, thereby affects the efficiency of film forming, thereby has reduced the thermal efficiency and production efficiency.
Summary of the invention
Not enough based on prior art, the utility model object is to provide a kind of can further improve into film uniformity, thereby further improves a kind of falling film evaporation device of the thermal efficiency and production efficiency.
For realizing the utility model object, falling film evaporation device described in the utility model comprises by the connected upper cover of flange, lower cover, body, forms cylindrical shell.Upper cover upper end is provided with charging aperture, and bottom connects distributing disc; Body one side being positioned under distributing disc is provided with vaporium, and vaporium is connected with steam inlet, and lower cover top one side is provided with exhaust outlet, lower cover top opposite side is provided with bleeding point, and lower cover bottom is provided with discharging opening.Distributing disc is provided with a plurality of chargings aperture, and each lower end, charging aperture connects a distribution head, and this is also key component of the present invention.This distribution head is cylindrical, by top cover, upper cylinder, lower prop three parts, be socketed to form, the diameter of top cover slightly larger in diameter each charging aperture on distributing disc wherein, the diameter of upper cylinder is slightly less than the internal diameter of tubulation, the diameter of lower prop is slightly less than again cylinder, the real cylinder of upper cylinder, lower prop is hollow cylinder.Hollow tubulation is placed on outside distribution head, isometric with distribution head.
The external wall of upper prop has equally distributed three S type guiding gutters, and lower prop middle part and lower end are respectively connected with a distribution grid.On each distribution grid, be uniformly distributed four flow-guiding mouths.Flow-guiding mouth on upper and lower distribution grid becomes 45 degree to intersect, and in the middle of distribution head upper cover, opens charging aperture, and charging aperture bottom outwards has three flow-guiding mouths that are mutually 120 degree, and flow-guiding mouth is corresponding with three S type guiding gutters on upper cylinder.
In body, be longitudinally evenly distributed with nozzle for flow dismounting plate, nozzle for flow dismounting plate the right and left is alternately distributed.The area of each nozzle for flow dismounting plate is 1/2 to 2/3 of the interior sectional area of tubulation.
Body lower end is connected with centrum, and centrum is positioned at lower cover.
When liquid to be concentrated enters after the charging aperture on distribution head top cover, descending along the S type guiding gutter of upper cylinder.Because upper cylinder is real cylinder, outer wall is close to tubulation inwall, and lower flowing liquid can only be descending along tubulation inwall film forming, thereby reaches the first substandard cloth film.If have a small amount of liquid along inner tubal wall with interior lower, can drip on first distribution grid.Complete herein the second substandard cloth film.Same liquid that could not film forming at first distribution grid place completes cloth film for the third time on the 3rd distribution grid.By three substandard cloth films, just greatly having improved descending liquid becomes film uniformity.Nozzle for flow dismounting plate is alternately distributed along tubulation the right and left, and the heating steam that makes to enter falling film evaporation device is descending by the descending S of the becoming type of straight line split flow, has extended the arrhea time of steam between vaporising device tubulation and the time of contact of tubulation outer wall, has improved efficiency of utilization.
Research shows, adopts this falling film evaporation device, can improve the thermal efficiency more than 10%, enhances productivity more than 15%.
Accompanying drawing explanation
Fig. 1 is the utility model falling film evaporation device structural representation;
Fig. 2 is the utility model distributing disc top view;
Fig. 3 is the utility model falling film evaporation device distribution head structural representation;
Fig. 4 is the utility model distribution head upper cover top view;
Fig. 5 is the utility model distribution grid upward view;
Fig. 6 is the utility model distribution head A-A profile;
The specific embodiment
For the utility model is better illustrated, act is implemented as follows:
Embodiment:
Falling film evaporation device described in the utility model comprises by the connected upper cover 1 of flange, lower cover 2, body 3, forms cylindrical shell.Upper cover 1 upper end is provided with charging aperture 4, and bottom connects distributing disc 5; Body 3 one sides that are positioned under distributing disc 5 are provided with vaporium 6, and vaporium 6 is connected with steam inlet 7, and lower cover 2 top one sides are provided with exhaust outlet 8, lower cover 2 top opposite sides are provided with bleeding point 9, and lower cover 2 bottoms are provided with discharging opening 10.Distributing disc 5 is provided with a plurality of apertures, and each lower end, aperture connects a distribution head 11, and this is also key component of the present invention.This distribution head 11 is cylindrical, by top cover 12, upper cylinder 13, lower prop 14 3 parts, be socketed to form, the diameter of top cover 12 slightly larger in diameter each charging aperture on distributing disc 5 wherein, the diameter of upper cylinder 13 is slightly less than the internal diameter of tubulation 18, and the diameter of lower prop 14 is slightly less than again cylinder 13.Hollow tubulation 18 is tightly placed in distribution head 11 outer walls, isometric with distribution head 11.Upper cylinder 13 is real cylinder, and lower prop 14 is hollow cylinder.Upper cylinder 13 outer walls are carved with equally distributed three S type guiding gutters, and lower prop 14 middle parts and lower end are respectively connected with a distribution grid 15.On each distribution grid 15, be uniformly distributed four flow-guiding mouths.Flow-guiding mouth on upper and lower distribution grid 15 becomes 45 degree to intersect, and in the middle of the upper cover 12 of distribution head 11, opens charging aperture 16, and charging aperture 16 bottoms outwards have three flow-guiding mouths that are mutually 120 degree, and flow-guiding mouth is corresponding with three S type guiding gutters on upper cylinder 13.
The interior nozzle for flow dismounting plate 17 that is longitudinally evenly distributed with of body 3, nozzle for flow dismounting plate 17 the right and lefts are alternately distributed.The area of each nozzle for flow dismounting plate 17 is 1/2 to 2/3 of tubulation 18 interior sectional areas.
Body 3 lower ends are connected with centrum 19, and centrum 19 is positioned at lower cover 2, and body 3 is long to be supported by bearing 20.
Claims (3)
1. a falling film evaporation device, is characterized in that, it comprises by the connected upper cover of flange, lower cover, body, forms cylindrical shell; Upper cover upper end is provided with charging aperture, and bottom connects distributing disc; Body one side being positioned under distributing disc is provided with vaporium, and vaporium is connected with steam inlet, and lower cover top one side is provided with exhaust outlet, lower cover top opposite side is provided with bleeding point, and lower cover bottom is provided with discharging opening;
Distributing disc is provided with a plurality of chargings aperture, and each lower end, charging aperture connects a distribution head; This distribution head is cylindrical, by top cover, upper cylinder, lower prop three parts, be socketed to form, wherein top cover diameter is greater than the diameter of each charging aperture on distributing disc, the diameter of upper cylinder is less than the internal diameter of tubulation, the diameter of lower prop is less than again cylinder, upper cylinder is real cylinder, and lower prop is hollow cylinder; Hollow tubulation is placed on outside distribution head, isometric with distribution head; The external wall of upper prop has equally distributed three S type guiding gutters, and lower prop middle part and lower end are respectively connected with a distribution grid; On each distribution grid, be uniformly distributed four flow-guiding mouths; Flow-guiding mouth on upper and lower distribution grid becomes 45 degree to intersect, and in the middle of distribution head upper cover, opens charging aperture, and charging aperture bottom outwards has three flow-guiding mouths that are mutually 120 degree, and flow-guiding mouth is corresponding with three S type guiding gutters on upper cylinder.
2. falling film evaporation device as claimed in claim 1, is characterized in that, the area of each nozzle for flow dismounting plate is 1/2 to 2/3 of the interior sectional area of hollow tubulation.
3. falling film evaporation device as claimed in claim 1 or 2, is characterized in that, body lower end is connected with centrum, and centrum is positioned at lower cover.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201320879767.7U CN203777684U (en) | 2013-12-30 | 2013-12-30 | Falling film evaporation device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201320879767.7U CN203777684U (en) | 2013-12-30 | 2013-12-30 | Falling film evaporation device |
Publications (1)
Publication Number | Publication Date |
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CN203777684U true CN203777684U (en) | 2014-08-20 |
Family
ID=51313915
Family Applications (1)
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CN201320879767.7U Expired - Fee Related CN203777684U (en) | 2013-12-30 | 2013-12-30 | Falling film evaporation device |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105806101A (en) * | 2014-12-31 | 2016-07-27 | 北京首创股份有限公司 | Material heat exchanger for sludge treatment |
CN107261535A (en) * | 2017-07-16 | 2017-10-20 | 苏州卓群钛镍设备有限公司 | A kind of falling film evaporator |
CN113975836A (en) * | 2021-10-29 | 2022-01-28 | 阜阳安固锅炉压力容器制造有限公司 | Falling film evaporator |
CN114191843A (en) * | 2022-01-14 | 2022-03-18 | 上海东庚化工技术有限公司 | Efficient continuous falling film melting crystallizer |
-
2013
- 2013-12-30 CN CN201320879767.7U patent/CN203777684U/en not_active Expired - Fee Related
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105806101A (en) * | 2014-12-31 | 2016-07-27 | 北京首创股份有限公司 | Material heat exchanger for sludge treatment |
CN107261535A (en) * | 2017-07-16 | 2017-10-20 | 苏州卓群钛镍设备有限公司 | A kind of falling film evaporator |
CN107261535B (en) * | 2017-07-16 | 2023-08-15 | 苏州卓群钛镍设备有限公司 | Falling film evaporator |
CN113975836A (en) * | 2021-10-29 | 2022-01-28 | 阜阳安固锅炉压力容器制造有限公司 | Falling film evaporator |
CN114191843A (en) * | 2022-01-14 | 2022-03-18 | 上海东庚化工技术有限公司 | Efficient continuous falling film melting crystallizer |
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Effective date of registration: 20191126 Granted publication date: 20140820 |
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PD01 | Discharge of preservation of patent |
Date of cancellation: 20231230 Granted publication date: 20140820 |
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