CN209060579U - A kind of internal heat type molecular distillation equipment - Google Patents
A kind of internal heat type molecular distillation equipment Download PDFInfo
- Publication number
- CN209060579U CN209060579U CN201821354944.9U CN201821354944U CN209060579U CN 209060579 U CN209060579 U CN 209060579U CN 201821354944 U CN201821354944 U CN 201821354944U CN 209060579 U CN209060579 U CN 209060579U
- Authority
- CN
- China
- Prior art keywords
- heater
- molecular distillation
- distillation equipment
- heating
- seal body
- 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
Links
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model relates to a kind of internal heat type molecular distillation equipments, including external molecular distillation equipment ontology and the heater of molecular distillation equipment body interior is set, molecular distillation equipment ontology is hollow cylindrical or barrel-shaped structure with bottom, molecular distillation equipment ontology is equipped with top end socket, top end socket is equipped with material inlet pipe, has multiple material distributors on heater outer wall and inner wall heating surface；The top of molecular distillation equipment ontology connects vacuum tube, and the space between molecular distillation equipment body interior and heater is connected to vacuum tube.The utility model internal structure is compact, the two-sided evaporation of heater Double-side Heating, maximum heating surface (area) (HS (disengagement area) is realized with the smallest volume, the manufacturing cost for several distillation equipments that the applicant can be designed originally further decreases, it is especially suitable for the manufacture processing of large-scale super-huge molecular distillation equipment, is suitble to large-scale production.
Description
Technical field
The utility model belongs to mechanical equipment technical field, is related to that a kind of edible oil, oil-fat chemical products, other are each
The equipment of class chemical products, the distilation of plant extracts and separation heterogeneity, specifically a kind of internal heat type molecule
Distillation equipment.
Background technique
Molecular distillation is also known as short-path distillation, it is newer liquid-liquid for being not yet widely used in industrialized production point
From technology, application can solve the problem of wide variety of conventional distillation technique cann't be solved.It than conventional distil-lation technology compared to have with
Lower advance: 1. common distillations are to carry out lock out operation at boiling temperature, as long as and reaching between cold and hot two faces of molecular distillation
To enough temperature difference can be carried out at any temperature separation thus molecular distillation operation temperature be far below material boiling
Point.2. common distillation has bubbling, boiling phenomenon, and molecular distillation is freely evaporating for liquid film surface, and the very low of operating pressure is general
For the 0.1-1Pa order of magnitude, heated time is very short, is typically only ten seconds to a few minutes.3. the evaporation and condensation commonly distilled are can
Inverse process is in dynamic phase balance between liquid and gas, and in molecular clock process, the molecule escaped from heating surface is direct
A possibility that flying on cryosurface, being theoretically not returned to heating surface, so the substance that molecular distillation is not not readily separated；
But its shortcomings that thering is one can not amplify, the maximum molecular distillation equipment to be stirred is Germany's manufacture in the world at present,
Now maximum only 60 square metres of heating surface (area) (HS.And the two-sided evaporation of heater Double-side Heating of the utility model, with the smallest
Volume realizes maximum heating surface (area) (HS (disengagement area), in the case where same volume, that is to say, that in identical installation space
In, the molecular distillation equipment of the utility model is 2-4 times of the disengagement area of original all molecular distillation equipments, can be light
The molecular distillation of ground manufacture 100 square metres of heating surface (area) (HS, 200 square metres of heating surface (area) (HS, 300 square metres of heating surface (area) (HS
Equipment, and the associated patent of the applicant applied for a utility model patent on August 7th, 2012, and utility model is special
Benefit number is ZL201210277674.7, and molecular distillation equipment includes molecular distillation equipment ontology and vacuum tube, molecular distillation equipment
Ontology is the inversion ontology ring-type rotary table that upper annulus is greater than lower annulus.Have accumulated design abundant, manufacturing experience.
The applicant have been devoted to molecular distillation equipment innovation work, also applied at 2 months 2017 one specially
Sharp CN201710082649.6, the molecular distillation equipment ontology are semicircle or half elliptic hollow cylinder, open tubular column
The rectangle side plane of body is material heating panel.Material automatically forms film along inclined-plane from top to bottom, produces serialization, object
Material is short by the time of heating surface, superior product quality.But in constantly experiment process of innovation, the applicant is to existing skill
Art carries out drive to the basket.
Utility model content
Purpose of the utility model is to solve defect of the existing technology, a kind of internal heat type molecular distillation is provided and is set
It is standby.
To achieve the goals above, the technical solution adopted in the utility model is:
A kind of internal heat type molecular distillation equipment is set including external molecular distillation equipment ontology and setting in molecular distillation
The heater of standby body interior, molecular distillation equipment ontology are hollow cylindrical or barrel-shaped structure with bottom, and molecule steams
Apparatus body is evaporated equipped with top end socket, and top end socket is equipped with material inlet pipe, has on heater outer wall and inner wall heating surface more
A material distributor；The top of molecular distillation equipment ontology connects vacuum tube, molecular distillation equipment body interior and heater it
Between space be connected to vacuum tube；
The heater of the molecular distillation equipment body interior is ring heater, and ring heater is in rotary table annular, circle
Conical ring or cylindrical annular structure, heater are mounted on the inner bottom of molecular distillation equipment ontology or become molecular distillation equipment
A part of ontology bottom end, the top surface of heater, lateral surface and medial surface are heating surface, substantially increase heater and object
The contact area of material.
A kind of above-mentioned internal heat type molecular distillation equipment, material distributor quantity are multiple, first material distributor installation
On the heating surface on heater top, the medial surface of heater and the heating surface of lateral surface is arranged in other material distributors
On.
A kind of above-mentioned internal heat type molecular distillation equipment, the material distributor are annulus tubular structure, material distributor
Annulus bottom of the tube reserve several apertures.
A kind of above-mentioned internal heat type molecular distillation equipment, the material distributor are annulus plate structure, material distributor
Circular Plate medial surface and heater heating surface between have certain gap.
A kind of above-mentioned internal heat type molecular distillation equipment, the heater are heat-conducting medium heating system, the bottom of heater
Portion is equipped with heat medium import (outlet), and top is equipped with Crude product input (import), and heat medium import and heat medium go out
Mouth forms a heating circulation system relative to heater.Heat medium preferably uses the heat medium of solar energy heating, in reality
In production, for more energy efficient consumption reduction environmental protection, heat medium preferably uses solar energy heating, reduces the consumption of the fuel such as coal, natural gas,
It is more conducive to environment, reduces the discharge of the exhaust gas such as carbon dioxide in atmosphere.
A kind of above-mentioned internal heat type molecular distillation equipment, the heater are electric heating system, and the inside of heater is equipped with
The heating wire that disk is set.
A kind of above-mentioned internal heat type molecular distillation equipment, molecular distillation equipment body interior are equipped with more than one heating
Device, multiple heaters radial diffusion type in molecular distillation equipment ontology arrange, annulus are equipped between adjacent heater and is condensed
Device, the quantity and heater of annulus condenser correspond, and annulus condenser has cooling water inlet and cooling water outlet.
A kind of above-mentioned internal heat type molecular distillation equipment, the body wall (inner wall) of the seal body are that heating surface or water cooling are pressed from both sides
Cover cooling surface.
A kind of above-mentioned internal heat type molecular distillation equipment, be connected at the top of the molecular distillation equipment ontology filling body or
Column plate, vacuum tube are connect with filling body or column plate.
The utility model has the following beneficial effects: the equipment sealing effect is good, device fabrication and operation expense are lower, no
Agitating device is needed, material automatically forms film along the heating surface of heater from top to bottom, produces serialization, material is by adding
The time in hot face is short, superior product quality, while saving electric power resource, and heat utilization rate is high, and production cost is low；If can be
It is widely applied in relevant industries, will be relevant industries lifting means, lifting process technology sound assurance.
The utility model internal structure is compact, the two-sided evaporation of heater Double-side Heating, is realized with the smallest volume maximum
Heating surface (area) (HS (disengagement area), in the case where same volume, that is to say, that in identical installation space, the utility model
Molecular distillation equipment is 2-4 times of the disengagement area of original all molecular distillation equipments, the applicant can be designed originally
The manufacturing costs of several distillation equipments further decrease, be especially suitable for the manufacture processing of large-scale super-huge molecular distillation equipment,
It is suitble to large-scale production.
Detailed description of the invention
Fig. 1 is that 1 circular ring shape molecular distillation equipment center line of the utility model embodiment erects schematic cross-sectional view；
Fig. 2 is 1 circular ring shape molecular distillation equipment ring heater horizontal cross-sectional schematic of the utility model embodiment；
Fig. 2 a is the area the A enlarged drawing in Fig. 1；
Fig. 3 is that 2 rotary table circular ring shape molecular distillation equipment center line of the utility model embodiment erects schematic cross-sectional view；
Fig. 4 is that molecular distillation equipment center line of the utility model embodiment 2 with condenser erects schematic cross-sectional view；
Fig. 5 is that more than the 3 circular ring shape molecular distillation equipment center lines of the utility model embodiment erect schematic cross-sectional view；
Fig. 6 is more than the 3 circular ring shape molecular distillation equipment ring heater horizontal cross-sectional schematics of the utility model embodiment；
Fig. 7 is that the molecular distillation equipment center line of 1 outer wall belt of the utility model embodiment heating erects schematic cross-sectional view；
Fig. 8 is that the molecular distillation equipment center line of 1 outer wall belt of the utility model embodiment condensation erects schematic cross-sectional view；
Fig. 9 is that the utility model has the molecular distillation equipment of filling body to erect schematic cross-sectional view；
Figure 10 is the molecular distillation equipment horizontal cross-sectional schematic that the utility model has filling body.
In figure, material inlet pipe 1, low boiling material outlet 2, high boiler material outlet 3, vacuum tube 4, heat medium import
5, Crude product input 6, first material distributor 7-1, second material distributor 7-2, third material distributor 7-3, cooling water
Import 8, cooling water outlet 9, molecular distillation equipment ontology 10, filling body 11, heater 12, annulus condenser 13, heating device
14。
Specific embodiment
The technical solution of the utility model is explained in conjunction with specific attached drawing and embodiment, specific as follows:
Embodiment 1
As shown in Figure 1, Figure 2, shown in Fig. 2 a, a kind of internal heat type molecular distillation equipment includes molecular distillation equipment ontology 10 and vacuum
Pipe 4, molecular distillation equipment ontology 10 are equipped with top end socket, and top end socket is equipped with material inlet pipe 1, and vacuum tube 4 is located at molecule
On distillation equipment ontology, the space between molecular distillation equipment body interior and heater 12 is connected to vacuum tube 4；Molecular distillation
The bottom of apparatus body 1 is equipped with low boiling material outlet 2 and high boiler material outlet 3, inside molecular distillation equipment ontology 10
Heater 12 is cylindrical annular, and cylindrical annular heater is mounted on the interior bottom end of molecular distillation equipment ontology 1；Cylindrical annular heating
There are multiple material distributors on device outer wall and inner wall heating surface；Material distributor is preferably three, the top surface 121 of heater 12,
Lateral surface 122 and medial surface 123 are heating surface, substantially increase the contact area of heater and material, wherein the first object
Material distributor 7-1 is located at the upper end top surface 121 of heater 12, and other material distributors are located at 123 He of medial surface of heater
On the heating surface of lateral surface 122；
Material distributor is annulus plate structure；There is certain gap between material distributor Circular Plate bottom and heating surface
124, which forms material flow passage, and first material distributor 7-1 is located at the lower section of material inlet pipe 1.
Heater has heat medium import 5 and Crude product input 6, and heat medium is entered from heat medium import 5
Guarantee that the temperature of each heating surface of heater 12 is stablized in heater 12 to increase, material enters the first object from material inlet pipe 1
Material distributor 7-1 is simultaneously past dirty along the heating surface of heater from the gap 124 of the bottom first material distributor 7-1, flows naturally
Film-form is dropped down into, when flowing to second material distributor 7-2, material makes material more under the action of second material distributor 7-2
Uniformly, in being heated device 12 when the heating of heat medium, low-boiling substance is initially evaporated, and a part is taken out by vacuum tube 4
It being recycled after arriving the condensation of distillation equipment external condenser out, a part of air cooling wall by molecular distillation equipment body interior is air-cooled to get off,
By 2 recycling of low boiling material outlet；When unevaporated substance continues trickling to third material distributor 7-3, material is in third
Make material further uniform under the action of material distributor 7-3, material originally has one in third material distributor 7-3
A buffer function is the process that a material is reallocated into film again simultaneously, then is flowed downward from third material distributor 7-3.Object
Material low-boiling substance on heating surface initially evaporates, after a part is retracted to the condensation of distillation equipment external condenser by vacuum tube 4
Recycling, a part are gone out by recycling after the molecular distillation equipment ontology cooling wall condensation of outer seal device by low boiling material
Mouth 2 collects, and remaining high boiling substance is finally pooled to bottom, goes out by high boiler material all after heating surface
Mouth 3 enters next process.
Embodiment 2
The embodiment is that heater 12 is rotary table annular, the installation of rotary table ring heater relative to the difference of embodiment 1
In the interior bottom end of molecular distillation equipment ontology, become a part of molecular distillation equipment ontology bottom end；Ring heater outer wall and
There are multiple material distributors on inner wall heating surface；First material distributor 7-1 is located at the upper end of heater, other material distributions
Device is located on the heating surface of heater；In addition, the material distributor in the present embodiment is ring tube structure；The material of annulus tubulose
There is certain gap between distributor and heating surface；Vacuum tube 4 is located on molecular distillation equipment ontology, molecular distillation equipment ontology
Space between internal and heater is connected to vacuum tube 4.
As shown in figure 3, material enters first material distributor 7-1 from material inlet pipe 1, it is past dirty along heating inclined-plane,
Naturally trickling is at film-form, and when flowing to second material distributor 7-2, material makes under the action of second material distributor 7-2
More evenly, in being heated device when the heating of heat medium, low-boiling substance initially evaporates material, through vacuum a part by
Vacuum tube 4 recycles after being retracted to the condensation of distillation equipment external condenser, a part of air cooling wall by molecular distillation equipment body interior
It is air-cooled to get off, by 2 recycling of low boiling material outlet；When unevaporated substance continues trickling to third material distributor 7-3, object
Material makes material further uniform under the action of third material distributor 7-3, and material originally is in third material distributor
Have a buffer function in 7-3 simultaneously and be again a process that material is reallocated into film, then from third material distributor 7-3 to
Lower flowing.Material low-boiling substance on heating surface initially evaporates, and a part is retracted to distillation equipment condensed exterior by vacuum tube 4
It is recycled after device condensation, a part after the molecular distillation equipment ontology cooling wall condensation of outer seal device by recycling, by low boiling
Point material outlet 2 collects, and remaining high boiling substance is finally pooled to bottom all after heating surface, and process is high boiling
Point material outlet 3 enters next process.
Embodiment 3
The present embodiment is relative to the difference of embodiment 1: the heater 12 corresponding one inside molecular distillation equipment
A annulus condenser 13, annulus condenser 13 have cooling water inlet 8, cooling water outlet 9.
As shown in figure 4, in order to be adequately cooled the steam of some low-boiling point materials, while reducing the pumping of vacuum pump
Tolerance reduces the energy consumption of vacuum pump, and it is therefore necessary to design an annulus condenser 13；Material enters first from material inlet pipe 1
Material distributor 7-1, along heating inclined-plane toward flowing down, trickling is at film-form, when flowing to second material distributor 7-2, object naturally
Material makes material more evenly under the action of second material distributor 7-2, and heat medium adds in being heated medium collet
When hot, low-boiling substance is initially evaporated, and is returned after vacuum fraction is retracted to the condensation of distillation equipment external condenser by vacuum tube 4
It receives, it is most of to be condensed out by annulus condenser, by 2 recycling of low boiling material outlet；Unevaporated substance continues trickling and arrives
When third material distributor 7-3, material makes material further uniform under the action of third material distributor 7-3, originally
Material have a buffer function in third material distributor 7-3 simultaneously and be again the process that material is reallocated into film,
It flows downward again from third material distributor 7-3.Material low-boiling substance on heating surface initially evaporates, by annulus condenser
13 and outer seal device the condensation of molecular distillation equipment ontology cooling wall after recycle, 2 gathered up by low boiling material outlet
Come, remaining high boiling substance is finally pooled to bottom all after heating surface, under entering by high boiler material outlet 3
One procedure.
Embodiment 4
The present embodiment is further improved on the basis of embodiment 3, inside molecular distillation equipment there are two heater 12 with
And corresponding two annulus condensers 13.
As shown in Fig. 5 Fig. 6, in order to be adequately cooled the steam of some low-boiling point materials, while vacuum pump is reduced
Sucking rate reduce the energy consumption of vacuum pump, it is therefore necessary to design the corresponding two annulus condensers of two heaters；Material is from object
Expect that inlet tube 1 enters first material distributor 7-1, along heating inclined-plane toward flowing down, trickling flows to the second object at film-form naturally
When expecting distributor 7-2, material makes material more evenly under the action of second material distributor 7-2, is being heated medium folder
In set when the heating of heat medium, low-boiling substance is initially evaporated, and is retracted to distillation equipment by vacuum tube 4 through vacuum fraction
It is recycled after external condenser condensation, it is most of to be condensed out by annulus condenser, by 2 recycling of low boiling material outlet；It does not evaporate
Substance when continuing trickling to third material distributor 7-3, material makes material again under the action of third material distributor 7-3
Further uniformly, it is again that a material divides again that material originally has a buffer function simultaneously in third material distributor 7-3
It is made into the process of film, then is flowed downward from third material distributor 7-3.Material low-boiling substance on heating surface steams first
Hair, by being recycled after the condensation of the molecular distillation equipment ontology cooling wall of annulus condenser and outer seal device, by low boilers
Material outlet 2 collects, and remaining high boiling substance is finally pooled to bottom, by high boiling product all after heating surface
Material outlet 3 enters next process.
Embodiment 5
The present embodiment the difference from example 2 is that, the body wall of molecular distillation equipment ontology 10 can also be a heating
Device 14 a, specifically, ring-shaped sealing sleeve, ring-shaped sealing sleeve and molecule are arranged on the inner wall of molecular distillation equipment ontology 10
Heat medium is filled between the inner wall of distillation equipment ontology 10, and material distributor 15, material are installed on the inner wall of ring-shaped sealing sleeve
Branch pipe 16 on inlet tube 1 is connected to the top of material distributor 15.
As shown in fig. 7, material enters first material distributor 7-1 from material inlet pipe 1, it is past dirty along heating inclined-plane,
Naturally trickling is at film-form, and when flowing to second material distributor 7-2, material makes under the action of second material distributor 7-2
More evenly, in being heated medium collet when the heating of heat medium, low-boiling substance initially evaporates material, through vacuum by
Vacuum tube 4 recycles after being retracted to the condensation of distillation equipment external condenser；Unevaporated substance continues trickling to third material distributor
When 7-3, material makes material further uniform under the action of third material distributor 7-3, and material originally is in third object
Having a buffer function in material distributor 7-3 simultaneously is process of the material reallocation at film again, then is divided from third material
Cloth device 7-3 flows downward.Material low-boiling substance on heating surface initially evaporates, and remaining high boiling substance is all by adding
Behind hot face, it is finally pooled to bottom, enters next process by high boiler material outlet 3.Meanwhile the material in branch pipe 16 is led
Entering can also successively be evaporated into the material distributor 15 on heating device 14.
Embodiment 6
The present embodiment and the difference of embodiment 3 are that the body wall of molecular distillation equipment ontology 10 is water-cooled jacket set 17.
As shown in figure 8, in order to be adequately cooled the steam of some low-boiling point materials, while reducing the pumping of vacuum pump
Tolerance reduces the energy consumption of vacuum pump, is 17 He of water-cooled jacket set it is therefore necessary to design the body wall of molecular distillation equipment ontology 10
One annulus condenser 13；Material enters first material distributor 7-1 from material inlet pipe 1, along heating inclined-plane toward flowing down, certainly
So trickling is at film-form, and when flowing to second material distributor 7-2, material makes object under the action of second material distributor 7-2
More evenly, in being heated medium collet when the heating of heat medium, low-boiling substance initially evaporates material, through the small portion of vacuum
Divide after being retracted to the condensation of distillation equipment external condenser by vacuum tube 4 and recycles, it is most of to be condensed out by annulus condenser 13, pass through
2 recycling of low boiling material outlet；When unevaporated substance continues trickling to third material distributor 7-3, material is in third material
Make material further uniform under the action of distributor 7-3, material originally has one to delay in third material distributor 7-3
Punching effect is the process that a material is reallocated into film again simultaneously, then is flowed downward from third material distributor 7-3.Material exists
Low-boiling substance initially evaporates on heating surface, is water-cooling jacket dress by the body wall of annulus condenser and molecular distillation equipment ontology
It recycles, is collected by low boiling material outlet 2, remaining high boiling substance is all after heating surface, most after setting condensation
After be pooled to bottom, by high boiler material outlet 3 enter next process.
Embodiment 7
The present embodiment the difference from embodiment 1 is that: the top bonding pad body 11 or tower of molecular distillation equipment ontology 10
Plate, vacuum tube are connect with filling body or column plate.
By taking ethanol distillation purifies as an example, as shown in Fig. 9 Figure 10, ethyl alcohol enters first material distributor from material inlet pipe 1
7-1, along heating inclined-plane toward flowing down, trickling is at film-form naturally, and when flowing to second material distributor 7-2, material is in the second object
Make material more evenly under the action of material distributor 7-2, in being heated device when the heating of heat medium, low-boiling substance
It initially evaporates, the steam of vaporized ethyl alcohol encounters filler, is influenced by filler resistance and temperature, and the height for reaching filler is got over
The purity of high substance is also higher, this, which suits the requirements, produces content (purity) and reach 95%, 98%, 99% or even 99.5%, 99.9%
The needs of enterprise and requirement are recycled, a part after vacuum a part is retracted to the condensation of distillation equipment external condenser by vacuum tube 4
Got off by the air cooling wall of molecular distillation equipment body interior is air-cooled, by 2 recycling of low boiling material outlet；Unevaporated substance after
When third material distributor 7-3 is dropped down in afterflow, material makes material further equal under the action of third material distributor 7-3
Even, it is that a material is reallocated into film again that material originally has a buffer function simultaneously in third material distributor 7-3
Process, then flow downward from third material distributor 7-3.Material low-boiling substance on heating surface initially evaporates, and one
Divide after being retracted to the condensation of distillation equipment external condenser by vacuum tube 4 and recycle, a part is set by the molecular distillation of outer seal device
It recycles, is collected by low boiling material outlet 2, remaining high boiling substance is all by adding after standby ontology cooling wall condensation
Behind hot face, it is finally pooled to bottom, enters next process by high boiler material outlet 3.
The equipment sealing effect is good, and device fabrication and operation expense are lower, does not need agitating device, material from upper and
Under along the heating surface of heater automatically form film, produce serialization, material is short by the time of heating surface, product quality
It is good, while electric power resource is saved, heat utilization rate is high, and production cost is low；It is answered if can obtain promoting in relevant industries
With will be relevant industries lifting means, lifting process technology sound assurance.
The utility model internal structure is compact, the two-sided evaporation of heater Double-side Heating, is realized with the smallest volume maximum
The manufacturing cost of heating surface (area) (HS (disengagement area), several distillation equipments that the applicant can be designed originally further decreases,
It is especially suitable for the manufacture processing of large-scale super-huge molecular distillation equipment, is suitble to large-scale production.
Because the utility model molecular distillation equipment manufacturing process is more simple, manufacturing cost is steamed relative to existing molecule
It is extremely cheap to evaporate equipment, in order to protect the utility model molecular distillation equipment, is required in the production process of any product hereby
Conceive using the utility model molecular distillation equipment and using the utility model, belongs to equivalent replacement, it is all practical new at this
Within the protection scope of type patent.
Utility model device is not limited by examples detailed above, and other any examples applied using the present apparatus are belonged to
Equivalent replacement, all within the protection scope of the utility model patent.
Claims (8)
1. a kind of internal heat type molecular distillation equipment, including external seal body and the heating being arranged in inside seal body
Device, which is characterized in that seal body is hollow cylindrical or barrel-shaped structure with bottom, and seal body is sealed equipped with top
Head, top end socket are equipped with material inlet pipe, have multiple material distributors on heater outer wall and inner wall heating surface；Seal body
Top connects vacuum tube, and the space between seal body inside and heater is connected to vacuum tube；
Heater inside the seal body is ring heater, and ring heater is in rotary table annular, circular cone annular or cylinder
Ring structure, heater are mounted on the inner bottom of seal body or a part as seal body bottom end, the top of heater
Face, lateral surface and medial surface are heating surface；
More than one heater, multiple heaters radial diffusion type arrangement, phase in seal body are equipped with inside seal body
Annulus condenser is equipped between adjacent heater, the quantity and heater of annulus condenser correspond, and annulus condenser has
Cooling water inlet and cooling water outlet.
2. a kind of internal heat type molecular distillation equipment according to claim 1, which is characterized in that material distributor quantity is more
A, first material distributor is mounted on the heating surface on heater top, and other material distributors are arranged in heater
On the heating surface of side and lateral surface.
3. a kind of internal heat type molecular distillation equipment according to claim 2, which is characterized in that the material distributor is circle
The annulus bottom of the tube of tubular ring structure, material distributor reserves several apertures.
4. a kind of internal heat type molecular distillation equipment according to claim 2, which is characterized in that the material distributor is circle
Ring plate structure has certain gap between the Circular Plate medial surface of material distributor and the heating surface of heater.
5. a kind of internal heat type molecular distillation equipment according to claim 2, which is characterized in that the heater is thermally conductive Jie
Matter heating system, the bottom of heater are equipped with heat medium import, and top is equipped with Crude product input, heat medium import and plus
Thermal medium outlet forms a heating circulation system relative to heater, and heat medium selects the heat medium of solar energy heating.
6. a kind of internal heat type molecular distillation equipment according to claim 2, which is characterized in that the heater is electric heating
System, the inside of heater are equipped with the heating wire that disk is set.
7. a kind of internal heat type molecular distillation equipment according to claim 6, which is characterized in that the body wall of the seal body
For heating surface or water-cooling jacket cooling surface.
8. a kind of internal heat type molecular distillation equipment according to claim 6, which is characterized in that the top of the seal body
It is connected with filling body or column plate, vacuum tube is connect with filling body or column plate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821354944.9U CN209060579U (en) | 2018-08-22 | 2018-08-22 | A kind of internal heat type molecular distillation equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821354944.9U CN209060579U (en) | 2018-08-22 | 2018-08-22 | A kind of internal heat type molecular distillation equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209060579U true CN209060579U (en) | 2019-07-05 |
Family
ID=67090918
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201821354944.9U Active CN209060579U (en) | 2018-08-22 | 2018-08-22 | A kind of internal heat type molecular distillation equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209060579U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108854132A (en) * | 2018-08-22 | 2018-11-23 | 金溪遥遥领先高科有限公司 | A kind of internal heat type molecular distillation equipment |
-
2018
- 2018-08-22 CN CN201821354944.9U patent/CN209060579U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108854132A (en) * | 2018-08-22 | 2018-11-23 | 金溪遥遥领先高科有限公司 | A kind of internal heat type molecular distillation equipment |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN111437619B (en) | Multi-tower differential pressure energy-saving absolute alcohol distillation system and absolute alcohol energy-saving production method | |
| CN205925048U (en) | Retrieve batch distillation device of ethanol in china cypress paper production process | |
| CN107789854A (en) | A kind of internal heat type molecular distillation equipment | |
| CN111803986B (en) | Improved tower plate filler type rectifying tower for molecular distillation | |
| CN106591887B (en) | A kind of aluminium cell side wall device for generating power by waste heat based on organic flash distillation cycle | |
| CN101991968B (en) | Internal heat integration energy-saving rectification device and assembly method thereof | |
| CN201658857U (en) | Rectifying tower for continuous rectification | |
| CN209060579U (en) | A kind of internal heat type molecular distillation equipment | |
| CN104524800B (en) | A kind of thermal coupling with heat exchange column plate is sprayed and flows tower | |
| CN108992958A (en) | A kind of hypergravity rectifying is used for reaction process solvent recovering system | |
| CN110105216B (en) | Self-backheating rectification method and device | |
| CN208809499U (en) | A kind of device improving Butyl Glycolate rectification yield | |
| CN108854132A (en) | A kind of internal heat type molecular distillation equipment | |
| CN207605386U (en) | A kind of rectifying column | |
| CN112403012A (en) | Circulation accuse temperature formula molecular distillation equipment | |
| CN205461092U (en) | Rectification system | |
| CN214861267U (en) | Rectifying tower | |
| CN208049426U (en) | A kind of internal heat type molecular distillation equipment | |
| CN203494188U (en) | Double-effect concentrator | |
| CN104606910A (en) | Heat pump rectifying device based on heat storage technology and starting method of heat pump rectifying device | |
| CN213667981U (en) | Differential pressure thermal coupling rectification separation device | |
| CN205759794U (en) | A kind of Nitrobenzol topping still | |
| CN203989923U (en) | A kind of distiller | |
| CN106693427A (en) | Molecule distillation equipment | |
| CN207126157U (en) | A kind of wire mesh packing rectifying tower |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |