CN206089626U - A distillation plant for separation of lanolin remains of pesticide - Google Patents
A distillation plant for separation of lanolin remains of pesticide Download PDFInfo
- Publication number
- CN206089626U CN206089626U CN201620905794.0U CN201620905794U CN206089626U CN 206089626 U CN206089626 U CN 206089626U CN 201620905794 U CN201620905794 U CN 201620905794U CN 206089626 U CN206089626 U CN 206089626U
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- CN
- China
- Prior art keywords
- lanolin
- auxiliary
- pesticide
- remains
- short
- 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.)
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Classifications
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/74—Recovery of fats, fatty oils, fatty acids or other fatty substances, e.g. lanolin or waxes
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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses a distillation plant for separation of lanolin remains of pesticide, it is connected with the vacuum adsorption device including short distance distiller, short distance distiller, be provided with a plurality of supplementary adsorption pipeline among the short distance distiller, each supplementary adsorption pipeline all is connected with vacuum adsorption pump, being provided with among the supplementary adsorption pipeline along its inner wall and carrying out the supplementary condensation flue that extends, the inside packing of supplementary condensation flue has the comdenstion water, adopt above -mentioned technical scheme's a distillation plant for separation of lanolin remains of pesticide, its accessible short distance distillation is handled in order to distill lanolin to realize the separation processing of its and pesticide. Among the above -mentioned distillation process, distillation plant accessible vacuum adsorption device in this application and vacuum adsorption pump are in order to realize the high vacuum degree in the distiller, and the vaporization processing can be realized to lanolin under lower temperature under high vacuum environment, cause among the whole process separation precision of lanolin and pesticide to improve.
Description
Technical field
The utility model is related to biology and new medicine field, especially a kind of to be used for the detached distillation of lanolin remains of pesticide
Equipment.
Background technology
Lanolin is inevitably retained in preparation process, among its raw materials for production certain agricultural chemicals, above-mentioned residual
Agricultural chemicals not only cause the production precision and product purity of lanolin Related product to be affected, or even user can be caused
Certain potential safety hazard.In existing lanolin preparation technology, for above-mentioned agricultural chemicals is separated often through the mode of distillation
Process, however, the vapo(u)rizing temperature in the Collator Mode of routine due to agricultural chemicals and lanolin is close to, it cannot form good separation
Effect.
Utility model content
The technical problems to be solved in the utility model is to provide one kind for the detached distillation equipment of lanolin remains of pesticide,
It can efficiently separate the remains of pesticide among lanolin.
To solve above-mentioned technical problem, the utility model is related to one kind and sets for the detached distillation of lanolin remains of pesticide
Standby, it includes short-distance distiller, and short-distance distiller is connected with vacuum absorption device；It is provided among the short-distance distiller many
Individual auxiliary absorption pipeline,, via extending to inside short-distance distiller outside it, each auxiliary absorption pipeline is respectively connected with very for it
Empty adsorption pump；The auxiliary condensation pipe extended along its inwall is provided among the auxiliary absorption pipeline, condenser pipe is aided in
Road inside is filled with condensed water.
As a kind of improvement of the present utility model, at least 3 auxiliary absorption pipelines are provided with the short-distance distiller,
Each auxiliary absorption pipeline includes the first end being arranged inside short-distance distiller, and is arranged at short-distance distiller
Outside the second end, the auxiliary condensation pipe is extended in auxiliary absorption pipeline via the first end of auxiliary absorption pipeline
Portion.Using above-mentioned technical proposal, it is efficient true inside for short-distance distiller to realize that it can pass through multiple auxiliary absorption pipelines
Suction is attached；At the same time, the set location for aiding in condensation pipe then can ensure that the material after distillation is entered in auxiliary absorption pipeline
Condensation recycling can be carried out, cause its organic efficiency further to be improved.
Used as a kind of improvement of the present utility model, the length of the auxiliary condensation pipe at least aids in absorption duct length
1/2.Using above-mentioned technical proposal, it can guarantee distilling material in auxiliary absorption pipeline by aiding in the length of condensation pipe
Reclaimed with forming it into liquid with enough condensation distances.
As a kind of improvement of the present utility model, recovery room is provided with the second end of the auxiliary absorption pipeline,
Condensation chuck is provided between the outer wall and inwall of recovery room, it is internal filled with condensed water；The vacsorb pump is connected to
On recovery room.Using above-mentioned technical proposal, it can be excessive in the distilling material in auxiliary absorption pipeline, and cause is passed to auxiliary
In the case of absorption pipeline, condensation recycling is carried out to it by the setting of recovery room and condensation chuck, so as to further
Material is avoided to enter among vacsorb pump.
Using above-mentioned technical proposal for the detached distillation equipment of lanolin remains of pesticide, it can be by short-path distillation
Manage to distill to lanolin, to realize its separating treatment with agricultural chemicals.In above-mentioned still-process, the distillation in the application sets
It is standby can be by vacuum absorption device and vacsorb pump to realize the condition of high vacuum degree in distiller, the wool under high vacuum environment
Fat can at a lower temperature realize vaporization process, cause lanolin in whole technological process to be changed with the separation accuracy of agricultural chemicals
It is kind.At the same time, multiple auxiliary absorption pipelines are while auxiliary vacuum suction is realized in above-mentioned distillation equipment, and it is internal auxiliary
That helps condenser pipe can carry out condensation recycling for the material in auxiliary absorption pipeline is entered, and inhale so as to avoid it from entering vacuum
Inside attached pump, to cause the loss of material or the damage of equipment.
Description of the drawings
Fig. 1 is the utility model schematic diagram；
Reference numerals list：
1-short-distance distiller, 2-vacuum absorption device, 3-auxiliary absorption pipeline, 301-first end, 302-the second
End, 4-vacsorb pump, 5-auxiliary condensation pipe, 6-recovery room, 7-condensation chuck.
Specific embodiment
With reference to specific embodiment and accompanying drawing, the utility model is further elucidated, it should be understood that following specific embodiment parties
Formula is merely to illustrate the utility model rather than limits scope of the present utility model.It should be noted that making in description below
Word "front", "rear", "left", "right", "up" and "down" refer to the direction in accompanying drawing, and word " interior " and " outward " refer to respectively
Be directed towards or away from the direction of particular elements geometric center.
Embodiment 1
One kind as shown in Figure 1 is used for the detached distillation equipment of lanolin remains of pesticide, and it includes short-distance distiller 1,
Short-distance distiller 1 is connected with vacuum absorption device 2；Multiple auxiliary absorption pipelines 3 are provided among the short-distance distiller 1, its
Via extending to outside it inside short-distance distiller 1, each auxiliary absorption pipeline 3 is respectively connected with vacsorb pump 4；It is described auxiliary
Help and the auxiliary condensation pipe 5 extended along its inwall is provided among absorption pipeline 3, the inside of auxiliary condensation pipe 5 is filled with
Condensed water.
As a kind of improvement of the present utility model, at least 3 auxiliary absorption pipelines are provided with the short-distance distiller 1
3, each auxiliary absorption pipeline 3 includes the first end 301 being arranged inside short-distance distiller 1, and is arranged at short
The second end 302 outside journey distiller 1, the auxiliary condensation pipe 5 prolongs via the first end 301 of auxiliary absorption pipeline 3
Extend inside auxiliary absorption pipeline 3.Using above-mentioned technical proposal, it can adsorb pipeline to realize for short distance by multiple auxiliary
High-efficiency vacuum absorption inside distiller；At the same time, the set location for aiding in condensation pipe then can ensure that the material after distillation
Condensation recycling can be carried out in auxiliary absorption pipeline, cause its organic efficiency further to be improved.
Used as a kind of improvement of the present utility model, the length of the auxiliary condensation pipe 5 at least aids in absorption pipeline 3 to grow
The 1/2 of degree.Using above-mentioned technical proposal, it can guarantee distilling material in auxiliary absorption pipeline by aiding in the length of condensation pipe
It is interior to be reclaimed with forming it into liquid with enough condensation distances.
Using above-mentioned technical proposal for the detached distillation equipment of lanolin remains of pesticide, it can be by short-path distillation
Manage to distill to lanolin, to realize its separating treatment with agricultural chemicals.In above-mentioned still-process, the distillation in the application sets
It is standby can be by vacuum absorption device and vacsorb pump to realize the condition of high vacuum degree in distiller, the wool under high vacuum environment
Fat can at a lower temperature realize vaporization process, cause lanolin in whole technological process to be changed with the separation accuracy of agricultural chemicals
It is kind.At the same time, multiple auxiliary absorption pipelines are while auxiliary vacuum suction is realized in above-mentioned distillation equipment, and it is internal auxiliary
That helps condenser pipe can carry out condensation recycling for the material in auxiliary absorption pipeline is entered, and inhale so as to avoid it from entering vacuum
Inside attached pump, to cause the loss of material or the damage of equipment.
Embodiment 2
As a kind of improvement of the present utility model, on the second end 302 of the auxiliary absorption pipeline 3 recovery is provided with
Room 6, is provided with condensation chuck 7 between the outer wall and inwall of recovery room 6, it is internal filled with condensed water；The vacsorb pump 4
It is connected on recovery room 6.Using above-mentioned technical proposal, it can be excessive in the distilling material in auxiliary absorption pipeline, causes it
In the case of by auxiliary absorption pipeline, condensation recycling is carried out to it by the setting of recovery room and condensation chuck, from
And further avoid material from entering among vacsorb pump.
Remaining feature of the present embodiment is same as Example 1 with advantage.
Claims (4)
1. it is a kind of to be used for the detached distillation equipment of lanolin remains of pesticide, it is characterised in that described for lanolin remains of pesticide
Detached distillation equipment includes short-distance distiller, and short-distance distiller is connected with vacuum absorption device；The short-distance distiller it
In be provided with multiple auxiliary absorption pipelines, its via extending to inside short-distance distiller outside it, each auxiliary absorption pipeline
It is respectively connected with vacsorb pump；The auxiliary condensation pipe extended along its inwall is provided among the auxiliary absorption pipeline,
Auxiliary condensation pipe inside is filled with condensed water.
2. according to described in claim 1 for the detached distillation equipment of lanolin remains of pesticide, it is characterised in that the short distance
At least 3 auxiliary absorption pipelines are provided with distiller, each auxiliary absorption pipeline is included and is arranged at short-path distillation
First end inside device, and the second end being arranged at outside short-distance distiller, the auxiliary condensation pipe is via auxiliary
The first end of absorption pipeline is extended to inside auxiliary absorption pipeline.
3. according to described in claim 2 for the detached distillation equipment of lanolin remains of pesticide, it is characterised in that the auxiliary
The length of condensation pipe at least aids in the 1/2 of absorption duct length.
4. according to described in Claims 2 or 3 for the detached distillation equipment of lanolin remains of pesticide, it is characterised in that it is described
Recovery room is provided with the second end of auxiliary absorption pipeline, between the outer wall and inwall of recovery room condensation chuck is provided with,
It is internal filled with condensed water；The vacsorb pump is connected on recovery room.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620905794.0U CN206089626U (en) | 2016-08-20 | 2016-08-20 | A distillation plant for separation of lanolin remains of pesticide |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620905794.0U CN206089626U (en) | 2016-08-20 | 2016-08-20 | A distillation plant for separation of lanolin remains of pesticide |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206089626U true CN206089626U (en) | 2017-04-12 |
Family
ID=58469688
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620905794.0U Expired - Fee Related CN206089626U (en) | 2016-08-20 | 2016-08-20 | A distillation plant for separation of lanolin remains of pesticide |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206089626U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112961731A (en) * | 2021-03-04 | 2021-06-15 | 浙江花园营养科技有限公司 | Method for preparing lanolin, wool oil and wool wax without pesticide residues |
| CN112980589A (en) * | 2021-03-04 | 2021-06-18 | 浙江花园营养科技有限公司 | Preparation method of ultra-low chroma lanolin |
-
2016
- 2016-08-20 CN CN201620905794.0U patent/CN206089626U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112961731A (en) * | 2021-03-04 | 2021-06-15 | 浙江花园营养科技有限公司 | Method for preparing lanolin, wool oil and wool wax without pesticide residues |
| CN112980589A (en) * | 2021-03-04 | 2021-06-18 | 浙江花园营养科技有限公司 | Preparation method of ultra-low chroma lanolin |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170412 Termination date: 20200820 |