CN209679520U - Vaporising device is used in a kind of concentration of chemical industry - Google Patents

Vaporising device is used in a kind of concentration of chemical industry Download PDF

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Publication number
CN209679520U
CN209679520U CN201920195825.1U CN201920195825U CN209679520U CN 209679520 U CN209679520 U CN 209679520U CN 201920195825 U CN201920195825 U CN 201920195825U CN 209679520 U CN209679520 U CN 209679520U
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China
Prior art keywords
evaporator shell
revolving part
channel
plate
steam
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CN201920195825.1U
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Chinese (zh)
Inventor
张忠勇
李明
李慧杰
张可擎
范景峰
史雨静
门倩
张笑
杨雅岚
邵菲菲
李珂
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Henan Vocational College of Applied Technology
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Henan Vocational College of Applied Technology
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Abstract

The utility model discloses a kind of chemical industry concentration vaporising devices, including evaporator shell, heating tube and revolving part, it is provided with chassis on the outside of the evaporator shell, for being supported to evaporator shell, the evaporator shell bottom is provided with outlet tube, and top is provided with gland steam exhauster;The evaporator shell is internally provided with newel, the newel upper end is fixed on the evaporator shell by suspending plate in midair, the suspention plate is that strip board ends are welded on the evaporator shell, the newel is internally provided with into vapour channel and apocenosis passage, the upper and lower ends that the newel is located at into vapour channel and the apocenosis passage.Beneficial effect is: heating tube can simultaneously be stirred solution, when heating to solution to improve the evaporation efficiency of solution;Wiper can also be carried out to evaporator shell inner wall and improve the discharge rate of concentrate solution to avoid being easy to stick on inner wall.

Description

Vaporising device is used in a kind of concentration of chemical industry
Technical field
The utility model belongs to chemical equipment technical field, and in particular to vaporising device is used in a kind of concentration of chemical industry.
Background technique
The concentration and evaporation of chemical reagent is mainly used for obtaining the solution of concentration or fixed solute, mainly by solution It is heated, by part solvent evaporation in the weak solution containing fixedness solute, the process of removing.It is generally necessary to pass through concentration Evaporator is vaporized.Applicants have discovered that at least there is following technical problem in the prior art: existing concentration evaporator is right When solution carries out heating evaporation, since heating tube is fixedly disposed in evaporator shell body, solution needs long-time and heating Pipe contact just can make temperature obtain whole promotion, therefore evaporation time is long, low efficiency, and be easy after increasing for some concentration The solution become viscous, solution is easy to stick on the inner wall of evaporator shell after concentration, is not easy to be discharged.
Utility model content
The purpose of this utility model is that solve the above-mentioned problems and provides a kind of chemical industry concentration vaporising device, energy The evaporation time of evaporator is enough greatly shortened, evaporation efficiency is improved.
To achieve the above object, the utility model provides following technical scheme:
Design a kind of chemical industry concentration vaporising device, including evaporator shell, heating tube and revolving part, the evaporator shell External side is provided with chassis, and for being supported to evaporator shell, the evaporator shell bottom is provided with outlet tube, top It is provided with gland steam exhauster;
The evaporator shell is internally provided with newel, and the newel upper end is fixed on the evaporation by suspending plate in midair On device shell, the suspention plate be strip board ends be welded on the evaporator shell, the newel be internally provided with into Vapour channel and apocenosis passage, the upper and lower ends that the newel is located at into vapour channel and the apocenosis passage, and two A channel is not connected, is connected with steam steam inlet pipe at the air intake into vapour channel, and the steam steam inlet pipe into vapour End is led on the outside of the evaporator shell, and revolving part, and revolving part rotation peace are provided with below the steam steam inlet pipe On the newel, the revolving part side is provided with drive disk, for driving the revolving part to rotate, the drive disk It is driven by motor, the motor is mounted on the outside of the evaporator shell;
It is provided with lower connecting plate below the revolving part, if being fixedly connected between the lower connecting plate and the revolving part The heating tube is done, and the heating tube is vertically arranged, and the steam into vapour channel can be conveyed downwards, and make cold Lime set is discharged out of described apocenosis passage, and the bottom of the apocenosis passage is connected with condensed water discharge pipe, and the condensed water is arranged Outlet pipe leads to the outside of the evaporator shell, and the two sides of the lower connecting plate are fixedly connected with scraper plate, and on the outside of the scraper plate It fits with the evaporator shell inner wall;
Liquid-feeding tube is installed on the side wall of the evaporator shell.
Using a kind of above-mentioned chemical industry concentration vaporising device, the evaporation is added by the liquid-feeding tube in solution to be concentrated In device shell, hot steam enters the newel through the steam steam inlet pipe, and flows into the heating tube along the revolving part, from And heat the heating tube to solution, make its evaporation, meanwhile, the motor described in the driving dish driving by rotating Part rotation, makes the heating tube while heating to solution, revolves inside the evaporator shell along the newel Turn, solution is stirred, to improve the evaporation efficiency of solution, while the lower connecting plate is when rotated, scrapes described in drive Plate carries out shovel to the inner sidewall of the evaporator shell and scrapes, so that the solution sticked on side wall be struck off, can be discharged into out Liquid pipe.
Preferably, being arch at the top of the evaporator shell, the gland steam exhauster is located at the top of arch, the evaporator The bottom of shell is infundibulate, and the scraper plate lower end edge infundibulate bottom wall is bent downward.
Preferably, being equipped with shut-off valve on the outlet tube.
Preferably, the bottom end into vapour channel extends at the revolving part center, the top of the apocenosis passage It extends at the lower connecting plate center, and described is provided with into the bottom end in vapour channel and the apical lateral of the apocenosis passage The tap hole of several circle distributions, the tap hole of upper end are connected with described into vapour channel, the tap hole of lower end It is connected with the apocenosis passage.
Preferably, the revolving part includes outer gear ring and upper junction plate, the upper junction plate is located at the outer gear ring On diameter line, and both ends are fixedly connected with the outer gear ring, and the upper junction plate is internally provided with lateral flow-guiding channel, and The flow-guiding channel shares two, and the axial centre of the flow-guiding channel and the tap hole axial centre of upper end are located at together In one plane, be provided with several split channels perforative straight down on the flow-guiding channel, the heating tube upper end with it is described Split channel is fixedly connected, and the lower connecting plate is identical as the upper junction plate structure, and two connecting plates are with the heating tube Horizontal central plane it is symmetrical, so that so that condensed water in the heating tube is passed through the lower connecting plate enters the row In liquid channel.
Preferably, the drive disk is the gear being meshed with the outer gear ring, and is provided on the outside of the drive disk Protective cover, the motor are fixedly mounted on the protective cover.
The utility model has the advantages that the heating tube of 1, the utility model when heating to solution, can simultaneously stir solution It mixes, to improve the evaporation efficiency of solution.
2, the setting of scraper plate is able to drive scraper plate in evaporator shell body when i.e. lower connecting plate rotates during the work time Wall carries out wiper and improves the discharge rate of concentrate solution to avoid being easy to stick on inner wall.
Detailed description of the invention
In order to illustrate the embodiment of the utility model or the technical proposal in the existing technology more clearly, below will be to embodiment Or attached drawing needed to be used in the description of the prior art is briefly described, it should be apparent that, the accompanying drawings in the following description is only It is some embodiments of the utility model, for those of ordinary skill in the art, in the premise not made the creative labor Under, it is also possible to obtain other drawings based on these drawings.
Fig. 1 is the schematic view of the front view of the utility model;
Fig. 2 is the schematic perspective view of revolving part;
Fig. 3 is longitudinal schematic cross-sectional view of Fig. 2;
Fig. 4 is the A-A of Fig. 3 to schematic cross-sectional view.
The reference numerals are as follows:
1, chassis;2, evaporator shell;
201, liquid-feeding tube;202, outlet tube;
3, heating tube;4, scraper plate;5, condensed water discharge pipe;6, steam steam inlet pipe;7, plate is suspended in midair;8, gland steam exhauster;9, center Column;
901, into vapour channel;902, tap hole;903, apocenosis passage;
10, revolving part;
1001, outer gear ring;1002, upper junction plate;1003, flow-guiding channel;1004, split channel;
11, motor;12, drive disk;13, protective cover;14, lower connecting plate.
Specific embodiment
To keep the purpose of this utility model, technical solution and advantage clearer, below by the technology to the utility model Scheme is described in detail.Obviously, the described embodiments are only a part of the embodiments of the utility model, rather than all Embodiment.Based on the embodiments of the present invention, those of ordinary skill in the art are not before making creative work Obtained all other embodiment is put, the range that the utility model is protected is belonged to.
Referring to shown in Fig. 1-4, the utility model provides a kind of chemical industry concentration vaporising device, including evaporator shell 2, Heating tube 3 and revolving part 10 are provided with chassis 1 on the outside of evaporator shell 2, for being supported to evaporator shell 2, evaporator 2 bottom of shell is provided with outlet tube 202, and top is provided with gland steam exhauster 8.
Evaporator shell 2 is internally provided with newel 9, and 9 upper end of newel is fixed on evaporator shell 2 by suspending plate 7 in midair On, suspention plate 7 is that strip board ends are welded on evaporator shell 2, and newel 9 is internally provided with into vapour channel 901 and drain Channel 903 is located at the upper and lower ends of newel 9 into vapour channel 901 and apocenosis passage 903, and two channels are not connected, It is connected with steam steam inlet pipe 6 at into the air intake in vapour channel 901, and the admission end of steam steam inlet pipe 6 leads to outside evaporator shell 2 Side, the lower section of steam steam inlet pipe 6 is provided with revolving part 10, and revolving part 10 is rotatably installed on newel 9, about 10 revolving part Both ends are fixed on newel 9 by bearing block, and 10 side of revolving part is provided with drive disk 12, for driving revolving part 10 to revolve Turn, drive disk 12 is driven by motor 11, and motor 11 is mounted on 2 outside of evaporator shell.
It is provided with lower connecting plate 14 below revolving part 10, several add is fixedly connected between lower connecting plate 14 and revolving part 10 Heat pipe 3, and heating tube 3 is vertically arranged, and will can be conveyed downwards into the steam in vapour channel 901, and make condensate liquid from drain Discharge in channel 903, the bottom of apocenosis passage 903 is connected with condensed water discharge pipe 5, and condensed water discharge pipe 5 leads to evaporator The outside of shell 2, the two sides of lower connecting plate 14 are fixedly connected with scraper plate 4, and 4 outside of scraper plate is affixed with 2 inner wall of evaporator shell It closes.Liquid-feeding tube 201 is installed on the side wall of evaporator shell 2.
Preferably, being arch at the top of evaporator shell 2, gland steam exhauster 8 is located at the top of arch, convenient for making steam along arch Inner top flows to gland steam exhauster 8, and the bottom of evaporator shell 2 is infundibulate, convenient for making to be easy to be discharged into outlet tube 202,4 lower end of scraper plate It is bent downward along infundibulate bottom wall, so set, convenient for improving the height dimension of 4 wiper of scraper plate.
Shut-off valve is installed on outlet tube 202, so set, convenient for controlling the discharge of concentrate solution by shut-off valve and cutting Only.
It is extended at 10 center of revolving part into the bottom end in vapour channel 901, the top of apocenosis passage 903 extends to lower connecting plate At 14 centers, and the apical lateral into the bottom end in vapour channel 901 and apocenosis passage 903 is provided with the shunting of several circle distributions The tap hole 902 in hole 902, upper end is connected with into vapour channel 901, and the tap hole 902 of lower end is connected with apocenosis passage 903 It is logical, so set, making lower connection convenient for enabling to flow outwardly into the hot steam in vapour channel 901 through the tap hole 902 of upper end Condensate liquid on plate 14 can flow into apocenosis passage 903 through the tap hole 902 of lower end.
Revolving part 10 includes outer gear ring 1001 and upper junction plate 1002, and upper junction plate 1002 is located at the diameter of outer gear ring 1001 On line, and both ends are fixedly connected with outer gear ring 1001, and upper junction plate 1002 is internally provided with lateral flow-guiding channel 1003, and Flow-guiding channel 1003 shares two, and the axial centre of flow-guiding channel 1003 and 902 axial centre of tap hole of upper end are located at together In one plane, convenient for making upper junction plate 1002 when rotated, flow-guiding channel 1003 can tap hole 902 dock, to make hot steaming Vapour flows into flow-guiding channel 1003 through the tap hole 902 of upper end, is provided on flow-guiding channel 1003 several perforative straight down Split channel 1004,3 upper end of heating tube are fixedly connected with split channel 1004, so set, convenient for heat in flow-guiding channel 1003 Steam flows into each heating tube 3 through split channel 1004, to heat to solution, lower connecting plate 14 and upper junction plate 1002 Structure is identical, and two connecting plates are symmetrical with the horizontal central plane of heating tube 3, to make the condensation water energy in heating tube 3 It is enough to enter in apocenosis passage 903 across lower connecting plate 14, so set, being generated after being convenient for making the hot steam in heating tube 3 to exchange heat Condensed water imported in flow-guiding channel 1003 through the split channel 1004 on lower connecting plate 14, and tap hole 902 through lower end flows Enter in apocenosis passage 903, is finally discharged through condensed water discharge pipe 5.
Drive disk 12 is the gear being meshed with outer gear ring 1001, and protective cover 13, motor are provided on the outside of drive disk 12 11 are fixedly mounted on protective cover 13, convenient for keeping the leakproofness of evaporator shell 2, while can block to drive disk 12 Protection.
Using the above structure, when specifically used, solution to be concentrated is added in evaporator shell 2 by liquid-feeding tube 201, heat Steam enters newel 9 through steam steam inlet pipe 6, and flows into heating tube 3 along revolving part 10, so that heating tube 3 be made to carry out solution Heating, makes its evaporation, meanwhile, motor 11 drives revolving part 10 to rotate by drive disk 12, adds heating tube 3 to solution While hot, along newel 9 in 2 internal rotating of evaporator shell, solution is stirred, to improve the evaporation effect of solution Rate, while lower connecting plate 14 is when rotated, drives scraper plate 4 to carry out shovel to the inner sidewall of evaporator shell 2 and scrapes, to will stick in side Solution on wall strikes off, and can be discharged into outlet tube 202.
Above description is only a specific implementation of the present invention, but the protection scope of the utility model is not limited to In this, anyone skilled in the art within the technical scope disclosed by the utility model, can readily occur in variation Or replacement, it should be covered within the scope of the utility model.Therefore, the protection scope of the utility model should be with the power Subject to the protection scope that benefit requires.

Claims (6)

1. a kind of chemical industry concentration vaporising device, it is characterised in that: including evaporator shell (2), heating tube (3) and revolving part (10), it is provided with chassis (1) on the outside of the evaporator shell (2), for being supported to evaporator shell (2), the evaporation Device shell (2) bottom is provided with outlet tube (202), and top is provided with gland steam exhauster (8);
The evaporator shell (2) is internally provided with newel (9), and newel (9) upper end is fixed on by suspending plate (7) in midair On the evaporator shell (2), the suspention plate (7) be strip board ends be welded on the evaporator shell (2), it is described in Stem (9) is internally provided with into vapour channel (901) and apocenosis passage (903), described into vapour channel (901) and the apocenosis passage (903) upper and lower ends of the newel (9) are located at, and two channels are not connected, it is described into vapour channel (901) into It is connected at steam ports steam steam inlet pipe (6), and the admission end of the steam steam inlet pipe (6) leads to the evaporator shell (2) outside Side is provided with revolving part (10) below the steam steam inlet pipe (6), and the revolving part (10) is rotatably installed in the center On column (9), revolving part (10) side is provided with drive disk (12), for driving the revolving part (10) to rotate, the drive Moving plate (12) is driven by motor (11), and the motor (11) is mounted on the outside of the evaporator shell (2);
It is provided with lower connecting plate (14) below the revolving part (10), between the lower connecting plate (14) and the revolving part (10) Several heating tubes (3) are fixedly connected with, and the heating tube (3) is vertically arranged, and can be by described into vapour channel (901) Interior steam conveys downwards, and makes condensate liquid discharge, bottom of the apocenosis passage (903) out of the apocenosis passage (903) It is connected with condensed water discharge pipe (5), and the condensed water discharge pipe (5) leads to the outside of the evaporator shell (2), under described The two sides of connecting plate (14) are fixedly connected with scraper plate (4), and the scraper plate (4) outside and the evaporator shell (2) inner wall phase Fitting;
Liquid-feeding tube (201) are installed on the side wall of the evaporator shell (2).
2. a kind of chemical industry concentration vaporising device according to claim 1, it is characterised in that: evaporator shell (2) top Portion is arch, and the gland steam exhauster (8) is located at the top of arch, and the bottom of the evaporator shell (2) is infundibulate, the scraper plate (4) lower end edge infundibulate bottom wall is bent downward.
3. a kind of chemical industry concentration vaporising device according to claim 2, it is characterised in that: pacify on the outlet tube (202) Equipped with shut-off valve.
4. a kind of chemical industry concentration vaporising device according to claim 3, it is characterised in that: described into vapour channel (901) Bottom end extends at the revolving part (10) center, and the top of the apocenosis passage (903) extends to the lower connecting plate (14) At center, and described several circumference are provided with into the bottom end of vapour channel (901) and the apical lateral of the apocenosis passage (903) The tap hole (902) of distribution, the tap hole (902) of upper end are connected with described into vapour channel (901), lower end it is described Tap hole (902) is connected with the apocenosis passage (903).
5. a kind of chemical industry concentration vaporising device according to claim 4, it is characterised in that: the revolving part (10) includes outer Gear ring (1001) and upper junction plate (1002), the upper junction plate (1002) are located on the diameter line of the outer gear ring (1001), And both ends are fixedly connected with the outer gear ring (1001), the upper junction plate (1002) is internally provided with lateral flow-guiding channel (1003), and the flow-guiding channel (1003) shares two, and the institute of the axial centre of the flow-guiding channel (1003) and upper end It is in the same plane to state tap hole (902) axial centre, is provided with and several passes through on the flow-guiding channel (1003) straight down The split channel (1004) worn, heating tube (3) upper end are fixedly connected with the split channel (1004), the lower connecting plate (14) identical as the upper junction plate (1002) structure, and two connecting plates are symmetrical with the horizontal central plane of the heating tube (3) Distribution, so that enabling the condensed water in the heating tube (3) to pass through the lower connecting plate (14) enters the apocenosis passage (903) in.
6. a kind of chemical industry concentration vaporising device according to claim 5, it is characterised in that: the drive disk (12) for institute The gear that outer gear ring (1001) is meshed is stated, and is provided with protective cover (13) on the outside of the drive disk (12), the motor (11) It is fixedly mounted on the protective cover (13).
CN201920195825.1U 2019-02-14 2019-02-14 Vaporising device is used in a kind of concentration of chemical industry Active CN209679520U (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113262510A (en) * 2021-06-01 2021-08-17 浙江翔隆厨房设备有限公司 Steam diversion heat energy recycling integrated system and control method thereof
CN115518398A (en) * 2022-10-03 2022-12-27 湖南力泓新材料科技股份有限公司 Novel zinc sulfate solution is concentrated device with even heating effect

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113262510A (en) * 2021-06-01 2021-08-17 浙江翔隆厨房设备有限公司 Steam diversion heat energy recycling integrated system and control method thereof
CN115518398A (en) * 2022-10-03 2022-12-27 湖南力泓新材料科技股份有限公司 Novel zinc sulfate solution is concentrated device with even heating effect

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