CN208302233U - A kind of novel thin film concentration evaporator - Google Patents

A kind of novel thin film concentration evaporator Download PDF

Info

Publication number
CN208302233U
CN208302233U CN201820442577.1U CN201820442577U CN208302233U CN 208302233 U CN208302233 U CN 208302233U CN 201820442577 U CN201820442577 U CN 201820442577U CN 208302233 U CN208302233 U CN 208302233U
Authority
CN
China
Prior art keywords
exchanger tube
heat exchanger
heat exchange
solution
cavity
Prior art date
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.)
Active
Application number
CN201820442577.1U
Other languages
Chinese (zh)
Inventor
徐巧玲
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Changzhou Wankang Electron Co., Ltd.
Original Assignee
Shenzhen Way Technology Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Shenzhen Way Technology Co Ltd filed Critical Shenzhen Way Technology Co Ltd
Priority to CN201820442577.1U priority Critical patent/CN208302233U/en
Application granted granted Critical
Publication of CN208302233U publication Critical patent/CN208302233U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Abstract

The utility model relates to a kind of novel thin film concentration evaporators, including solution inlet, the buffer in portion acts on descending to enter the heat exchange pipe in heat exchanger tube the solution being pumped by pressure pump under the vaporizers, high temperature steam pipe is communicated at the upper side of the heat exchanger tube, the heat exchange pipe that high-temperature steam enters in rear heat exchanging cylinder is heated, solution in the heat exchange pipe is expelled to concentrated solution outlet by the cavity above heat exchanger tube, solution vapor enters secondary separation chamber by the ventilative film that blocks water above cavity, has separator above the secondary separation chamber.It is two layers inside and outside by the way that evaporator to be divided into, internal layer lays heat exchange pipe, outer layer is passed through high-temperature steam, larger heat exchange area can be realized in smaller space, concentration ratio, while the time condensation cavity being arranged are improved, the solvent being mingled in vapor can be separated, impurity content in discharge gas is reduced, is reduced to air pollution.

Description

A kind of novel thin film concentration evaporator
Technical field
The utility model relates to material handling apparatus field, specifically a kind of novel thin film concentration evaporator.
Background technique
Thin film evaporator (Thin film evaporator) is a kind of type of evaporator, and feature is that feed liquid edge adds Heat pipe wall is conducted heat and is evaporated in membranaceous flowing, and advantage is heat transfer efficiency height, and evaporation rate is fast, and residence time of material is short, Therefore it is particularly suitable for the evaporation of heat-sensitive substance.In use, evaporator can generate material deposition, need periodically to evaporation It is rinsed inside device, in the prior art to the flusher of evaporator using relatively broad, such as Chinese patent CN206621811U discloses a kind of clean-up line structure of thin film evaporator outlet, and the kettle liquid outlet port of thin film evaporator is through becoming Frequency gear pump group suction line connects the entrance of frequency conversion gear pump group, and the outlet of frequency conversion gear pump group is through frequency conversion gear pump group outlet Line connects tar tank entrance, is equipped with first-hand valve on frequency conversion gear pump group suction line, in frequency conversion gear pump group outlet line On second-hand's valve is installed, wherein the C9 tower reactor oil export of Cutting Tap is formed with three branches after the first regulating valve, can distinguish Thin film evaporator bottom, frequency conversion gear pump group suction line and frequency conversion gear pump group outlet clean-up line are rinsed.This reality The frequency for reducing pipeline blocking with New Energy, so that the dredging of pipeline is more quick and convenient;It, can be quickly and in pipeline blocking Dredge pipeline, thus realize shorten the pipeline block clearing time, but its there are still following disadvantages in use: need to existing Evaporator shell increases pipeline and valve, higher to existing equipment improvement cost, and structure is complicated for entire flusher, takes up an area face Product is big, limits it and expands application range.
Utility model content
The technical problem to be solved by the utility model is to provide a kind of novel thin film concentration evaporators, to solve existing skill Defect present in art.
The technical solution that the utility model solves above-mentioned technical problem is as follows:
A kind of novel thin film concentration evaporator, including solution inlet, the solution being pumped by pressure pump portion under the vaporizers The lower heat exchange pipe into heat exchanger tube of buffer effect, be communicated with high temperature steam pipe at the upper side of the heat exchanger tube, high temperature The heat exchange pipe that steam enters in rear heat exchanging cylinder is heated, and the side of relatively-high temperature steam pipe is on-condensible gas on heat exchanger tube Outlet, high-temperature steam are discharged after exchanging heat by the non-condensable gas export;Solution in the heat exchange pipe passes through heat exchanger tube The cavity of top is expelled to concentrated solution outlet, and solution vapor enters secondary separation chamber by the ventilative film that blocks water above cavity, There is separator, having heaters, temperature sensor, the heating is arranged in the secondary separation chamber above the secondary separation chamber Device, temperature sensor and peripheral control unit connect, the controller control secondary separation cavity temperature be maintained at 100-110 DEG C it Between, vapor is exported by secondary steam after separator and is discharged, and solvent of the fusing point higher than 110 DEG C liquefies after separator, is stored up There are the bottoms of secondary separation chamber;Side is provided with condensation-water drain below the heat exchanger tube.
Further, the buffer is the cavity of both-side opening, and the cavity is connected to heat exchange pipe;
Further, the side of the heat exchanger tube relatively-high temperature steam also has pressure sensor, steams for detecting high temperature Whether steam pipe enters the steam pressure in heat exchanger tube up to standard.
Further, the top of the intracavitary separator of the secondary separation has pressure gauge, connect with peripheral control unit, when When the intracavitary pressure of secondary separation is more than setting value, the electromagnetic valve of pressure gauge side, which is opened, carries out pressure release, prevents danger.
The beneficial effects of the utility model are: two layers inside and outside by the way that evaporator to be divided into, internal layer lays heat exchange pipe, outer layer It is passed through high-temperature steam, larger heat exchange area can be realized in smaller space, improves concentration ratio, while the secondary separation being arranged Chamber can separate the solvent being mingled in vapor, reduce impurity content in discharge gas, reduce to air pollution.
Detailed description of the invention
FIG. 1 is a schematic structural view of the utility model;
Specific embodiment
The principles of the present invention and feature are described below in conjunction with attached drawing, example is served only for explaining that this is practical It is novel, it is not intended to limit the scope of the utility model.
As shown in Figure 1, a kind of novel thin film concentration evaporator, including solution inlet 1, existed by the solution that pressure pump is pumped into Enter the heat exchange pipe 5 in heat exchanger tube 4 under the effect of buffer 2 of evaporator lower part, is communicated with height at the upper side of the heat exchanger tube 4 Warm steam pipe 8, the heat exchange pipe 5 that high-temperature steam enters in rear heat exchanging cylinder 4 are heated, relatively-high temperature steam on heat exchanger tube 4 The side of pipe 8 is non-condensable gas export 10, and high-temperature steam is discharged after exchanging heat by the non-condensable gas export 10;The heat exchange Solution in comb 5 is expelled to concentrated solution outlet 9 by the cavity of 4 top of heat exchanger tube, and solution vapor passes through saturating above cavity Vapour lock water film enters secondary separation chamber 15, has separator 16, the secondary separation chamber 15 above the secondary separation chamber 15 Having heaters 11, temperature sensor 13 are set, and the heater 11, temperature sensor 13 are connect with peripheral control unit, the control Temperature is maintained between 100-110 DEG C in device control secondary separation chamber 15 processed, and vapor passes through secondary steam after separator 16 17 discharge of outlet, solvent of the fusing point higher than 110 DEG C liquefy after separator, are stored in the bottom of secondary separation chamber 15.
In order to buffer to the solution for entering heat exchange pipe, the buffer 2 is the cavity of both-side opening, the cavity It is connected to heat exchange pipe 5.
Further, side is provided with condensation-water drain 3 below the heat exchanger tube.
The side of the 4 relatively-high temperature steam of heat exchanger tube also has pressure sensor 7, for detect high temperature steam pipe 8 into Whether the steam pressure entered in heat exchanger tube 5 is up to standard.
The top of 15 inner separator of secondary separation chamber has pressure gauge 14, connect with peripheral control unit, when secondary When pressure is more than setting value in disengagement chamber 15, the electromagnetic valve 12 of pressure gauge side, which is opened, carries out pressure release, prevents danger.
The above is only the preferred embodiment of the present invention, is not intended to limit the utility model, all practical at this Within novel spirit and principle, any modification, equivalent replacement, improvement and so on should be included in the guarantor of the utility model Within the scope of shield.

Claims (4)

1. a kind of novel thin film concentration evaporator, it is characterised in that: including solution inlet, the solution being pumped by pressure pump is steaming The lower heat exchange pipe into heat exchanger tube of buffer effect of device lower part is sent out, the heat exchanger tube upper side is communicated with high-temperature steam Pipe, the heat exchange pipe that high-temperature steam enters in rear heat exchanging cylinder are heated, and the side of relatively-high temperature steam pipe is on heat exchanger tube Non-condensable gas export, high-temperature steam are discharged after exchanging heat by the non-condensable gas export;Solution in the heat exchange pipe is logical The cavity crossed above heat exchanger tube is expelled to concentrated solution outlet, and solution vapor is entered secondary by the ventilative film that blocks water above cavity Disengagement chamber, the secondary separation chamber top have separator, and having heaters, temperature sensor, institute is arranged in the secondary separation chamber It states heater, temperature sensor and peripheral control unit to connect, the controller control secondary separation cavity temperature is maintained at 100- Between 110 DEG C, vapor is exported by secondary steam after separator and is discharged, and solvent of the fusing point higher than 110 DEG C is after separator Liquefaction is stored in the bottom of secondary separation chamber, and side is provided with condensation-water drain below the heat exchanger tube.
2. a kind of novel thin film concentration evaporator according to claim 1, it is characterised in that: the buffer is opened for two sides The cavity of mouth, the cavity are connected to heat exchange pipe.
3. a kind of novel thin film concentration evaporator according to claim 1, it is characterised in that: the heat exchanger tube relatively-high temperature The side of steam also has pressure sensor.
4. a kind of novel thin film concentration evaporator according to claim 2 or 3, it is characterised in that: the secondary separation chamber The top of inner separator has pressure gauge, connect with peripheral control unit, when the intracavitary pressure of secondary separation is more than setting value, pressure The electromagnetic valve of power meter side, which is opened, carries out pressure release.
CN201820442577.1U 2018-03-30 2018-03-30 A kind of novel thin film concentration evaporator Active CN208302233U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201820442577.1U CN208302233U (en) 2018-03-30 2018-03-30 A kind of novel thin film concentration evaporator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201820442577.1U CN208302233U (en) 2018-03-30 2018-03-30 A kind of novel thin film concentration evaporator

Publications (1)

Publication Number Publication Date
CN208302233U true CN208302233U (en) 2019-01-01

Family

ID=64721874

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201820442577.1U Active CN208302233U (en) 2018-03-30 2018-03-30 A kind of novel thin film concentration evaporator

Country Status (1)

Country Link
CN (1) CN208302233U (en)

Similar Documents

Publication Publication Date Title
CN104759108B (en) Three grades of continuous falling liquid film circulating and evaporating concentration systems with function of mechanical steam recompression
CN107032429A (en) A kind of reverse osmosis thick water treatment system and handling process
CN101874938A (en) Forced circulation continuous crystallization system with mechanical vapor recompression function
CN101966396B (en) Evaporation device
CN106196718B (en) Absorption type heat pump system and its round-robin method
CN208302233U (en) A kind of novel thin film concentration evaporator
CN108525338A (en) Alcohol recycle rectifying device and alcohol recycle rectificating method
CN204943429U (en) A kind of pure steam generator
CN206837530U (en) A kind of vacuum evaporation device for being used to reclaim full heat and latent heat
CN106582050B (en) A kind of downward film evaporator liquid feeding control system
CN205627127U (en) MVR triple -effect evaporator
CN206121209U (en) Steam distillation equipment
CN209123373U (en) The continuous ethanol distillation system of outer circulation
CN211289994U (en) Waste heat recovery system
CN103182194A (en) Integrated-type liquid vaporization-separation tank device
CN207850110U (en) A kind of steam condensate recovering device
CN109731361A (en) Integral type climbing film evaporator
CN206142860U (en) Device is used multipurposely to used heat
CN207418323U (en) A kind of split type condensing unit
CN106091719B (en) For the steam condensed water waste heat reclamation set in cryogenic distillation apparatus
CN205627164U (en) Sodium nitrate solution evaporation crystallization equipment
CN109248461A (en) Continuous forced circulation flashes energy-saving concentrator
CN217612942U (en) Reaction solvent recovery unit is used in bromine nitryl alcohol production
CN205164164U (en) Tape unit tool vapor recompression's tertiary concentrated system of falling liquid film circulation evaporating in succession
CN208287516U (en) A kind of chondroitin sulfate extracting solution double-effect evaporation device

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant
TR01 Transfer of patent right

Effective date of registration: 20190522

Address after: 213000 Weicun Industrial Zone, Chunjiang Town, Xinbei District, Changzhou City, Jiangsu Province

Patentee after: Changzhou Wankang Electron Co., Ltd.

Address before: 518000 Dongxiao Road, Dongxiao Street, Luohu District, Shenzhen City, Guangdong Province, No. 3001 Buxinteli Industrial Park, 9 Blocks 118

Patentee before: Shenzhen way Technology Co., Ltd.

TR01 Transfer of patent right