CN206121194U - Two imitate formula level pipe falling liquid film vapor recompression evaporimeter - Google Patents
Two imitate formula level pipe falling liquid film vapor recompression evaporimeter Download PDFInfo
- Publication number
- CN206121194U CN206121194U CN201621024711.3U CN201621024711U CN206121194U CN 206121194 U CN206121194 U CN 206121194U CN 201621024711 U CN201621024711 U CN 201621024711U CN 206121194 U CN206121194 U CN 206121194U
- Authority
- CN
- China
- Prior art keywords
- effect
- evaporation tube
- effects
- evaporation
- xiao
- 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.)
- Withdrawn - After Issue
Links
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model relates to a two imitate formula level pipe falling liquid film vapor recompression evaporimeter. It is big that there is the energy consumption in the current vapor recompression evaporimeter of main solution, and the extravagant energy leads to the technical problem that manufacturing cost increases and production efficiency is low. Include vapor compressor and the vaporization system who is connected with vapor compressor, vaporization system includes that one imitates evaporation plant and two effect evaporation plant, an effect evaporation plant includes an effect jar body, an effect material conveying mechanism, an effect evaporating pipe and an effect cloth liquid mechanism, it is internal that an effect jar is located to an effect evaporating pipe, the two -effect evaporation device includes the two effects jar body, two effect material conveying mechanism, two -effect evaporation pipe and two effect cloth liquid mechanisms. The utility model discloses a two imitate the purpose that the mode that combines together realized the evaporation, and the energy saving reduces the energy consumption, can realize that it is 12 of level pipe falling liquid film vapor recompression evaporimeter that one ton of hydroenergy of every evaporation consumes. Realized reasonable use of energy effectively, reduction in production cost increases production efficiency.
Description
Technical field
This utility model is related to a kind of vaporizer, more particularly to a kind of two imitate the evaporation of formula horizontal tube falling film vapor recompression
Device.
Background technology
According to《12 " national strategy new industry development plan》In main task and developing direction, need to strengthen
The driving effect of policy and standard, fully uses modern technologies achievement, breaks through high efficiency of energy and echelon utilization, resource reclaim and follows
Ring such as utilizes at the key core technology, greatly develops the new equipment and product of energy-efficient, advanced environmental protection and resource circulation utilization.
It is in order to cater to national policy, a kind of in evaporation industry to connect a kind of vapor recompression vaporizer and be devised,
Horizontal tube falling film vapor recompression vaporizer as a kind of new vapor recompression vaporizer and original vertical tube falling and
Liter film vapor recompression vaporizer is compared and is had many good qualities.There are completely different theory, horizontal pipe falling film evaporation in design first
The steam of device is flowed in evaporation tube, and material is examined action of gravity and flowed downward in the outer film forming of evaporation tube, heating chamber and vaporization chamber
It is incorporated in a cylinder.It is this design have in performance the coefficient of heat transfer it is high, it is less scaling the characteristics of, have body in structure
The characteristics of product little, compact conformation, the energy can be greatlyd save and take up an area space.
Although horizontal tube falling film vapor recompression vaporizer has had breakthrough in the utilization to resource, with the energy
Increasingly depleted, it is necessary to find more energy saving evaporation equipment.And due to there was only 1 effect body, it is impossible to carry out multiple phase steaming
Process is evaporated, has limitation to the treatment types of material.
Utility model content
In order to overcome the shortcoming and weak point of background technology, this utility model to provide a kind of two and imitate the steaming of formula horizontal tube falling film
Vapour recompression evaporator, solving existing vapor recompression vaporizer, to there is energy consumption big, wastes the energy, cause production cost to increase with
And the technical problem of low production efficiency.
The technical solution of the utility model is：A kind of two imitate formula horizontal tube falling film vapor recompression vaporizer, including steam
Compressor and the vapo(u)rization system being connected with vapour compression machine, it is characterised in that：The vapo(u)rization system includes effect evaporation dress
Put and two effect vaporising devices, it is described one effect vaporising device include an effect tank body, one effect material conveying mechanism, one effect evaporation tube and
One Xiao Bu liquid mechanism, in an effect tank body, upper part of evaporating is imitated positioned at one to an effect evaporation tube in the Xiao Bu liquid mechanism,
The one effect material conveying mechanism is connected with a Xiao Bu liquid mechanism, is provided between an effect evaporation tube and an effect tank body upper end
One effect indirect steam runner, the effect tank body are provided with the indirect steam outlet communicated with described one effect indirect steam runner,
Indirect steam outlet is connected with the steam inlet of vapour compression machine, described two imitate vaporising device include two effect tank bodies, two
Effect material conveying mechanism, two effect evaporation tubes and two Xiao Bu liquid mechanisms, the two effect evaporation tube are imitated in tank bodies located at two, and described two
Xiao Bu liquid mechanism is connected with two Xiao Bu liquid mechanisms positioned at two effect upper part of evaporating, the two effects material conveying mechanism, and described two
Two effect indirect steam runners are provided between effect evaporation tube and two effect tank body upper ends, are set between an effect tank body and two effect tank bodies
There is adapter cavity, the two effect indirect steam runner is mutually circulated with described one effect evaporation tube by adapter cavity, on the two effects tank body
It is provided with the steam of the second-compressed steam inlet communicated with two effect evaporation tubes, the second-compressed steam inlet and vapour compression machine
Outlet is communicated, and an effect material conveying mechanism and two effect material conveying mechanisms are connected.
The one Xiao Bu liquid mechanism and two Xiao Bu liquid mechanisms are constituted by collecting tank and training wall, are provided with the collecting tank
Storing space, the training wall is located at the both sides of collecting tank and there is certain gap and the side wall of collecting tank between, and described
The upper end of training wall is connected with the outside of the collecting tank, and lower end is in unlimited and, the liquid collecting corresponding with the evaporation tube
The bottom side of the wall of groove is provided with the opening communicated with training wall.
If an effect evaporation tube and two effect evaporation tubes are dry doubling and are distributed in horizontal parallel, some evaporation tube phases of each effect
Mutually misplace and assume diamond in shape distribution.
The one effect material conveying mechanism includes an effect material pot, an effect discharging pump and an effect Matter Transfer pump, described
Two effect material conveying mechanisms include two effect material pots, two effect discharging pumps and two effect Matter Transfer pumps, the effect Matter Transfer
Pump one is imitated discharging pump and is connected with an effect material pot, and the effect Matter Transfer pump is connected with a Xiao Bu liquid mechanism, and described two imitate out
Material pump, two effect Matter Transfer pumps are connected with two effect material pots, and described two imitate Matter Transfer pump and two Xiao Bu liquid mechanisms, an effect
Feed supplement pump is connected with two effect material pots.
An effect cyclone hydraulic separators is provided between the one effect indirect steam runner and indirect steam outlet, two effect is secondary
Two effect cyclone hydraulic separators are provided between steam flow channel and adapter cavity.
The one effect evaporation tube and an effect evaporation tube include the first evaporation tube group and the second evaporation tube group, and described first steams
Pipe group and the second evaporation tube group are sent out in being distributed up and down, described one imitates one end of the first evaporation tube group of evaporation tube and adapter cavity phase
Logical, the other end is communicated with its second evaporation tube group, and one end of the first evaporation tube group of the two effects evaporation tube is steamed with second-compressed
Vapor inlet is communicated, and the other end is communicated with its second evaporation tube group.
The bottom of the collecting tank is V-arrangement, and its bottom is provided with through hole.
The one effect cyclone hydraulic separators and two effect cyclone hydraulic separators are by first support, second support and flow deflector, institute
State flow deflector to be located between first support and second support, the flow deflector is multiple and is " S " type, and each other in interval
Array distribution, one end of each flow deflector are connected by first support, and the other end of each flow deflector passes through second
Frame is connected, and the end between adjacent baffle forms steam demisting import, is formed and steam between the sidepiece of each adjacent baffle
Vapour demisting is exported.
This utility model has the advantages that：The mesh that this utility model is realized evaporating using the two effect modes of combining
, energy saving reduces energy consumption, can realize that often evaporating one ton of water consumption reduces by 1/2 relative to existing vaporizer.It is effectively real
Show reasonable energy utilization, reduced production cost, increase production efficiency.
Description of the drawings
Fig. 1 is structural representation of the present utility model.
Structural representations of the Fig. 2 for this utility model Zhong Bu liquid mechanism.
Fig. 3 is the structural representation of cyclone hydraulic separators in this utility model.
In figure, an effect tank body 1, an effect material conveying mechanism 2, an effect evaporation tube 3, a Xiao Bu liquid mechanism 4, the secondary steaming of an effect
Steam flow road 5, indirect steam outlet 6, two effect tank bodies 7, two effect material conveying mechanisms 8, two effect evaporation tubes 9, two Xiao Bu liquid mechanisms 10,
Two effect indirect steam runners 11, adapter cavity 12, second-compressed steam inlet 13, collecting tank 14, training wall 15, storing space 16,
Gap 17, opening 18, an effect material pot 19, an effect feed supplement pump 20, an effect Matter Transfer pump 21, two effect material pots 22, two effects
Discharging pump 23, two effect Matter Transfer pumps 24, an effect cyclone hydraulic separators 25, two effect cyclone hydraulic separators 26, the first evaporation tube group 27, the
Two evaporation tube groups 28, through hole 29, first support 30, second support 31, flow deflector 32, steam demisting import 33, steam demisting goes out
Mouth 34.
Specific embodiment
Embodiment of the present utility model is described further below for accompanying drawing：
As illustrated, a kind of two imitate formula horizontal tube falling film vapor recompression vaporizer, including vapour compression machine and with steaming
The vapo(u)rization system that vapour compressor is connected, the vapo(u)rization system include an effect vaporising device and two effect vaporising devices, an effect
Vaporising device includes effect material conveying mechanism 2, the effect evaporation tube 3 of an effect tank body 1, one and a Xiao Bu liquid mechanism 4, an effect
In an effect tank body 1, above an effect evaporation tube 3, described one imitates material conveying to evaporation tube 3 for the Xiao Bu liquid mechanism 4
Mechanism 2 is connected with a Xiao Bu liquid mechanism 4, is provided with an effect indirect steam between the effect evaporation tube 3 and 1 upper end of effect tank body
Runner 5, the effect tank body 1 are provided with the indirect steam outlet 6 communicated with described one effect indirect steam runner 5, described secondary
Steam (vapor) outlet 6 is connected with the steam inlet of vapour compression machine, and the two effects vaporising device includes the effect material of two effect tank body 7, two
Conveying mechanism 8, two imitates evaporation tube 9 and two Xiao Bu liquid mechanisms 10, and the two effect evaporation tube 9 is imitated in tank bodies 7 located at two, and described two
Above two effect evaporation tubes 9, the two effects material conveying mechanism 8 is connected with two Xiao Bu liquid mechanisms 10 for Xiao Bu liquid mechanism 10,
Two effect indirect steam runners 11, the effect tank body 1 and two effects are provided between the two effects evaporation tube 9 and two 7 upper ends of effect tank body
Adapter cavity 12 is provided between tank body 7, the two effect indirect steam runner is mutually circulated with described one effect evaporation tube by adapter cavity, institute
State two effect tank bodies and be provided with the second-compressed steam inlet 13 communicated with two effect evaporation tubes 9, the second-compressed steam inlet 13
Communicate with the steam (vapor) outlet of vapour compression machine, and an effect material conveying mechanism 4 is connected with two effect material conveying mechanisms 8.Work
When making, in the Xiao Bu liquid mechanism that the effect material conveying mechanism of material one is entered in an effect tank body, the indirect steam of generation passes through
Indirect steam outlet is entered in compressor, the material after an effect evaporation tube evaporation and concentration, then by an effect material conveying
Mechanism is delivered to material in two effect material conveying mechanisms, then is delivered to two Xiao Bu liquid mechanisms by two effect material conveying mechanisms,
By two effect evaporation tube evaporations, the indirect steam after compressor compresses enters into two effects by second-compressed steam inlet
In evaporation tube, and material is evaporated, the indirect steam after evaporation enters into transition intracavity by two effect indirect steam runners,
Then re-enter in an effect evaporation tube and use for evaporating material, so circulate, be just capable of achieving to recycle steam resource.It is whole
Individual vapo(u)rization system sets up 2 independent vacuum environment in an effect and two effects by vacuum pump, allows material in the evaporation of an effect and two effects
Temperature produces a difference, and the indirect steam of two effects can directly make an effect material reach the evaporating temperature of setting.Compressor is to one
The indirect steam acting of effect, changes into heat energy electric energy, and guides steam to enter two effects.According to such scheme, this utility model
The purpose for realizing evaporating using the two effect modes of combining, energy saving reduce energy consumption, can realize often evaporating one ton of water consumption phase
For existing vaporizer reduces by 1/2.Reasonable energy utilization is have effectively achieved, production cost is reduced, increases production efficiency.
Material is moved towards：Material is entered from an effect material pot, by an effect Matter Transfer pump in an effect vaporising device, thing
Material uniformly flows to lower end from heating evaporation pipe upper end by collecting tank, and realization exchanges heat and evaporates.Material is concentrated through vaporizer
Afterwards by feed supplement pump into two effect material pots, then 2nd effect evaporator is entered by two effect Matter Transfer pumps, material is again by collection
Liquid bath uniformly flows to lower end from heating evaporation pipe upper end, and realization exchanges heat and evaporates.Material reaches after vaporizer concentration and sets
Meter concentration simultaneously discharges.Steam moves towards explanation：The indirect steam that one effect is produced is taken away by compressor by cyclone hydraulic separators, through pressure
Contracting machine is squeezed into after doing manual work in two effect evaporation tubes and is heated for two effect materials, is condensed into liquid and collects after steam heat-exchanging.Two effects are produced
Secondary steaming by cyclone hydraulic separators into an effect evaporation tube, be effect material heating, steam is condensed into liquid and collects.Work
Principle：Whole vapo(u)rization system sets up 2 independent vacuum environment in an effect and two effects by vacuum pump, allows material in an effect and two effects
Evaporating temperature produce a difference, two effect indirect steams can directly make an effect material reach the evaporating temperature of setting.Compression
Machine is done manual work to the indirect steam of an effect, electric energy is changed into heat energy, and guides steam to enter two effects.
In this utility model, the Xiao Bu liquid mechanism 4 and two Xiao Bu liquid mechanisms 10 are by collecting tank 14 and training wall
15 compositions, are provided with storing space 16 in the collecting tank 14, the training wall 15 is located at the both sides of collecting tank 14 and collecting tank
There is certain gap 17 between 14 side wall, and the upper end of the collecting tank 14 be connected with the outside of the collecting tank 14,
Lower end is in open wide and corresponding with evaporation tube, and the bottom side of the wall of the collecting tank 14 is provided with the opening communicated with training wall 15
18.During cloth liquid, material enters collecting tank by material conveying mechanism, and collecting tank is in the form of slot, and material passes through after filling up storing space
Opening flows towards training wall and along training wall to dirty, and material flows downward by gravity traction, and material is guided into by training wall
Evaporation tube, changes training wall shape and can change thickness of liquid film.Material falls rather than spray form in drops, greatly reduces evaporation
Indoor material is atomized situation.
In this utility model, if the effect evaporation tube 3 and two effect evaporation tubes 9 are dry doubling and are distributed in horizontal parallel,
Some evaporation tube mutual dislocations of each effect the distribution that assumes diamond in shape.Evaporation tube assumes diamond in shape distribution, can allow material in each tubulation
Upper film forming.And horizontal tube falling film vapor recompression vaporizer is the characteristics of have heat transfer temperature difference little, structural cycle, and thing are extended
Material is in heat transfer outside a tube, fouling easy cleaning.Steam can be more effectively utilized, and also reduces the volume of heat exchanger.Device height
Only the 1/2 of vertical tube, compact conformation, greatly reduce Factory Building requirement, have saved occupation of land resource.
In this utility model, it is described one effect material conveying mechanism 2 include an effect material pot 19, an effect discharging pump 20 and
One effect Matter Transfer pump 21, the two effects material conveying mechanism 8 include the effect of two effect material pot 22, two discharging pump 23 and two effect things
Material circulating pump 24, the effect Matter Transfer pump 21 1 are imitated discharging pump 20 and are connected with an effect material pot 19, and the effect material is followed
Ring pump 21 is connected with a Xiao Bu liquid mechanism 4, and the two effects effect Matter Transfer of discharging pump 23, two pump 24 and two imitates 22 phases of material pot
Even, the two effect Matter Transfer pump 24 and two Xiao Bu liquid mechanisms 10, the effect feed supplement pump 20 are connected with two effect material pots 22.Thing
Material into after an effect material pot is delivered to Bu Ye mechanisms by an effect Matter Transfer pump and is evaporated, and the material after concentration is entered
One effect material pot, is delivered to two effect material pots by an effect Matter Transfer pump, is then delivered to two by two effect Matter Transfer pumps
Xiao Bu liquid mechanism, into two effect material pots after evaporation and concentration, and is discharged by two effect discharging pumps.Using said structure
Material conveying mechanism so that between an effect evaporation device and two effect evaporation devices can intercommunication, realize it is overall circulate, rationally utilize
The energy, save resources expend little.
In this utility model, between the effect indirect steam runner 5 and indirect steam outlet 6, an effect spinning liquid point is provided with
Two effect cyclone hydraulic separators 26 are provided between device 25, the two effect indirect steams runner 11 and adapter cavity 12.Imitated by arranging one
Cyclone hydraulic separators, two effect cyclone hydraulic separators so that the indirect steam that an effect is produced is taken away by compressor by cyclone hydraulic separators, Jing
Overcompression machine is squeezed into after doing manual work in two effect evaporation tubes and is heated for two effect materials, is condensed into liquid and collects after steam heat-exchanging.Two effects
The secondary steaming for producing is by cyclone hydraulic separators into an effect evaporation tube.The demisting formula horizontal tube falling film vapor recompression vaporizer leads to
Cross and cyclone hydraulic separators is set in horizontal tube vapor recompression vaporizer, using the cyclone hydraulic separators deflector type gas-liquid separation device
Gas-liquid separation is carried out, with the cleaning protected compressor and ensure distilled water.
In this utility model, the effect evaporation tube 3 and two effect evaporation tubes 9 include the first evaporation tube group 27 and second
, in being distributed up and down, described one imitates the first of evaporation tube 3 for evaporation tube group 28, the first evaporation tube group 27 and the second evaporation tube group 28
One end of evaporation tube group 27 is communicated with adapter cavity 12, and the other end is communicated with its second evaporation tube group 28, the two effects evaporation tube 9
One end of first evaporation tube group 27 is communicated with second-compressed steam inlet 13, and the other end is communicated with its second evaporation tube group 28.One
Effect evaporation tube 3 and two effect evaporation tubes 9 include the first evaporation tube group 27 and the second evaporation tube group 28, so as to realize overall evaporation tube
Distribution.Rational in infrastructure, evaporation effect is good, and stability is strong.
In this utility model, the bottom of the collecting tank 14 is V-arrangement, and its bottom is provided with through hole 29.Collecting tank 14
Bottom is v-shaped structure, and contributing to material using v-shaped structure quickly can flow down, and improves blanking velocity, strengthens the blanking effect of material
Rate.
In this utility model, an effect cyclone hydraulic separators 25 and two effect cyclone hydraulic separators 26 by first support 30,
Second support 31 and flow deflector 32, the flow deflector 32 are located between first support 30 and second support 31, the flow deflector
32 is multiple and be " S " type, and is distributed in spaced array each other, and one end of each flow deflector 32 is by first support 30
It is connected, the other end of each flow deflector 32 is connected by second support 31, and the end shape between adjacent baffle 32
Into steam demisting import 33, steam demisting outlet 34 between the sidepiece of each adjacent baffle 32, is formed.As cyclone hydraulic separators is adopted
Constituted with first support 30, second support 31 and flow deflector 32, and flow deflector is " S " type, demisting formula horizontal tube falling film steaming
Vapour recompression evaporator is rolled over using the cyclone hydraulic separators by arranging cyclone hydraulic separators in horizontal tube vapor recompression vaporizer
Streaming gas-liquid separation device carries out gas-liquid separation, good separating effect, with the cleaning protected compressor and ensure distilled water.
Claims (8)
1. a kind of two imitate formula horizontal tube falling film vapor recompression vaporizer, including vapour compression machine and be connected with vapour compression machine
The vapo(u)rization system for connecing, it is characterised in that：The vapo(u)rization system includes an effect vaporising device and two effect vaporising devices, and an effect is steamed
Transmitting apparatus include effect effect evaporation tube of material conveying mechanism (2) of an effect tank body (1) (3) and a Xiao Bu liquid mechanism (4), described
, in effect tank body (1), the Xiao Bu liquid mechanism (4) is above effect evaporation tube (3), described for one effect evaporation tube (3)
One effect material conveying mechanism (2) is connected with a Xiao Bu liquid mechanism (4), and effect evaporation tube (3) imitates tank body (1) upper end with one
Between be provided with effect indirect steam runner (5), effect tank body (1) is provided with and described one effect indirect steam runner (5) phase
Logical indirect steam outlet (6), indirect steam outlet (6) are connected with the steam inlet of vapour compression machine, two effect
Vaporising device includes two effect tank bodies (7), two effects material conveying mechanism (8), two effects evaporation tube (9) and two Xiao Bu liquid mechanisms
(10), in two effects tank body (7), the two Xiao Bu liquid mechanism (10) is positioned at two effects evaporation tube (9) for two effect evaporation tube (9)
Top, two effect material conveying mechanism (8) are connected with two Xiao Bu liquid mechanisms (10), and two effect evaporation tube (9) is imitated with two
Two effects indirect steam runner (11) are provided between tank body (7) upper end, are provided between effect tank body (1) and two effects tank body (7)
Adapter cavity (12), the two effect indirect steam runner are mutually circulated with described one effect evaporation tube by adapter cavity, the two effects tank body
It is provided with the second-compressed steam inlet (13) communicated with two effects evaporation tube (9), the second-compressed steam inlet (13) and steaming
The steam (vapor) outlet of vapour compressor is communicated, and effect material conveying mechanism (2) is connected with two effects material conveying mechanism (8).
2. a kind of two formula horizontal tube falling film vapor recompression vaporizer is imitated according to claim 1, it is characterised in that：Described one
Xiao Bu liquid mechanism (4) and two Xiao Bu liquid mechanisms (10) are constituted by collecting tank (14) and training wall (15), the collecting tank (14)
Storing space (16) is provided with inside, the training wall (15) is located at the both sides of collecting tank (14) and and the side wall of collecting tank (14) between
There is certain gap (17), and the upper end of the training wall (15) is connected with the outside of the collecting tank (14), lower end is in
Open wide and corresponding with evaporation tube, the bottom side of the wall of the collecting tank (14) is provided with the opening communicated with training wall (15)
(18)。
3. a kind of two formula horizontal tube falling film vapor recompression vaporizer is imitated according to claim 1, it is characterised in that：Described one
Effect evaporation tube (3) and two effects evaporation tube (9) are distributed in horizontal parallel if being dry doubling, and some evaporation tube mutual dislocations of each effect are simultaneously
Assume diamond in shape distribution.
4. according to claim 1 a kind of two formula horizontal tube falling film vapor recompression vaporizer is imitated, it is characterised in that：It is described
One effect material conveying mechanism (2) includes effect material pot (19), effect discharging pump (20) and effect Matter Transfer pump (21), institute
Two effect material conveying mechanisms (8) are stated including two effects material pot (22), two effects discharging pump (23) and two effects Matter Transfer pump (24),
The one effect Matter Transfer pump (21) one is imitated discharging pump (20) and is connected with effect material pot (19), the effect Matter Transfer pump
(21) it is connected with a Xiao Bu liquid mechanism (4), two effect discharging pump (23), two effects Matter Transfer pump (24) imitate material pots with two
(22) it is connected, described two imitate Matter Transfer pump (24) and two Xiao Bu liquid mechanisms (10), effect feed supplement pump (20) and two effect things
Batch can (22) is connected.
5. a kind of two formula horizontal tube falling film vapor recompression vaporizer is imitated according to claim 1, it is characterised in that：Described one
An effect cyclone hydraulic separators (25), the two effects indirect steam are provided between effect indirect steam runner (5) and indirect steam outlet (6)
Two effect cyclone hydraulic separators (26) are provided between runner (11) and adapter cavity (12).
6. according to claim 1 a kind of two formula horizontal tube falling film vapor recompression vaporizer is imitated, it is characterised in that：It is described
One effect evaporation tube (3) and two effects evaporation tube (9) including the first evaporation tube group (27) and the second evaporation tube group (28), described first
, in being distributed up and down, described one imitates the first evaporation tube group (27) of evaporation tube (3) for evaporation tube group (27) and the second evaporation tube group (28)
One end communicate with adapter cavity (12), the other end is communicated with its second evaporation tube group (28), it is described two effect evaporation tube (9) first
One end of evaporation tube group (27) is communicated with second-compressed steam inlet (13), and the other end is communicated with its second evaporation tube group (28).
7. according to claim 2 a kind of two formula horizontal tube falling film vapor recompression vaporizer is imitated, it is characterised in that：It is described
The bottom of collecting tank (14) is V-arrangement, and its bottom is provided with through hole (29).
8. according to claim 1 a kind of two formula horizontal tube falling film vapor recompression vaporizer is imitated, it is characterised in that：It is described
One effect cyclone hydraulic separators (25) and two effects cyclone hydraulic separators (26) are by first support (30), second support (31) and flow deflector
(32), the flow deflector (32) is between first support (30) and second support (31), the flow deflector (32) for it is multiple simultaneously
For " S " type, and it is distributed in spaced array each other, one end of each flow deflector (32) is connected by first support (30)
Connect, the other end of each flow deflector (32) is connected by second support (31), and the end between adjacent baffle (32)
Steam demisting import (33) is formed, steam demisting outlet (34) between the sidepiece of each adjacent baffle (32), is formed.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621024711.3U CN206121194U (en) | 2016-08-31 | 2016-08-31 | Two imitate formula level pipe falling liquid film vapor recompression evaporimeter |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621024711.3U CN206121194U (en) | 2016-08-31 | 2016-08-31 | Two imitate formula level pipe falling liquid film vapor recompression evaporimeter |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206121194U true CN206121194U (en) | 2017-04-26 |
Family
ID=58567470
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621024711.3U Withdrawn - After Issue CN206121194U (en) | 2016-08-31 | 2016-08-31 | Two imitate formula level pipe falling liquid film vapor recompression evaporimeter |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206121194U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106178566A (en) * | 2016-08-31 | 2016-12-07 | 浙江中机环保科技股份有限公司 | A kind of two effect formula horizontal tube falling film vapor recompression vaporizers |
-
2016
- 2016-08-31 CN CN201621024711.3U patent/CN206121194U/en not_active Withdrawn - After Issue
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106178566A (en) * | 2016-08-31 | 2016-12-07 | 浙江中机环保科技股份有限公司 | A kind of two effect formula horizontal tube falling film vapor recompression vaporizers |
| CN106178566B (en) * | 2016-08-31 | 2019-03-01 | 浙江中机环保科技股份有限公司 | One kind two imitates formula horizontal tube falling film vapor recompression evaporator |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103951005B (en) | The more technology coupling seawater desalination plants of zero-emission and its method | |
| CN203852856U (en) | Seven-effect and three-section evaporation indirect-condensation evaporator set for concentrated sodium aluminate solution | |
| CN105858768A (en) | Two-effect plate type distillation and desalination device | |
| CN206121194U (en) | Two imitate formula level pipe falling liquid film vapor recompression evaporimeter | |
| CN206315497U (en) | A kind of cooling driers air cleaner | |
| CN208711077U (en) | Multi-way multiple-effect MVR vapo(u)rization system | |
| CN203852855U (en) | Six-efficiency three-segment evaporation indirect condensation evaporator group for concentrated sodium aluminate solution | |
| CN106178566B (en) | One kind two imitates formula horizontal tube falling film vapor recompression evaporator | |
| CN209422985U (en) | A kind of multieffect evaporator | |
| CN208959348U (en) | A kind of evaporation concentration device of feed liquid | |
| CN205784014U (en) | A kind of flooded evaporator | |
| CN202080906U (en) | Four-effect evaporator applied to sodium bichromate evaporation technology | |
| CN201510766U (en) | Plate-type falling-film evaporator | |
| CN208493265U (en) | High-efficiency falling film concentrate evaporator system | |
| CN208454536U (en) | A kind of industrial wastewater vaporising device | |
| CN102020327A (en) | Ammonia nitrogen waste water treatment equipment | |
| CN211752568U (en) | Horizontal falling film evaporation concentration device of MVR | |
| CN101804262B (en) | Triple effect seven-stroke falling film evaporator | |
| CN205627127U (en) | MVR triple -effect evaporator | |
| CN204173941U (en) | Horizontal tube falling film thermocompression distiller | |
| CN209221520U (en) | A kind of evaporation equipment for Calcium Chloride Production | |
| CN207507038U (en) | A kind of falling film evaporator with cleaning device | |
| CN207175900U (en) | A kind of yellow rice wine vinasse water cooling plant | |
| CN202440400U (en) | Film-rising type multi-effect distilled water machine | |
| CN205398149U (en) | High salt waste water degree of depth enrichment facility of horizontal tubular falling film evaporation |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20170426 Effective date of abandoning: 20190301 |