CN208302238U - A kind of recyclable device of chondroitin sulfate extract liquor - Google Patents
A kind of recyclable device of chondroitin sulfate extract liquor Download PDFInfo
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- CN208302238U CN208302238U CN201820457221.5U CN201820457221U CN208302238U CN 208302238 U CN208302238 U CN 208302238U CN 201820457221 U CN201820457221 U CN 201820457221U CN 208302238 U CN208302238 U CN 208302238U
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- heat exchanger
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Abstract
The utility model discloses a kind of recyclable devices of chondroitin sulfate extract liquor, belong to biomaterial production equipment technology, including destilling tower and condensing tower, it is characterized in that being provided with heat exchanger between the destilling tower and condensing tower, the heat exchange structure includes stripping section, changeover portion and rectifying section, the side of stripping section, changeover portion and rectifying section is provided with liquid-inlet, the beneficial effects of the utility model are: heat exchanger realizes the recycling of energy；The side of stripping section, changeover portion and rectifying section is provided with liquid-inlet, on the basis of this has been based on heat exchanger to initial material preheating, bubble point temperature is approached, and it can be according to the difference of temperature of charge and the difference of column plate temperature, switch the feed inlet of initial material, the initial material of preheating and the temperature difference of column plate are reduced as much as possible, improve the efficiency of gasification.
Description
Technical field
The utility model belongs to biomaterial production equipment technology, relates more specifically to a kind of chondroitin sulfate extraction
The recyclable device of liquid.
Background technique
Destilling tower is a kind of tower vapor-liquid contacting apparatus for carrying out rectifying.There is different wave using each component in mixture
Hair degree, i.e. this different property of the vapour pressure of each component at the same temperature, are transferred to the light component (low-boiling-point substance) in liquid phase
In gas phase, and the heavy constituent (high-boiling components) in gas phase is transferred in liquid phase, to realize the purpose of separation.
General rectifier unit is made of equipment such as rectifying column tower body, condenser, return tank and reboilers.Charging from
The enterprising people Ta Nei of certain section of column plate in rectifying column, this block column plate are known as feedboard.Rectifying column is divided into two sections by feedboard, charging
Plate above section is known as rectifying section, is partially known as stripping section below feedboard.
Charging Board position be it is fixed, in this way with the progress of distillation, the temperature of heating plate of rectifying column is increased, and is passed through at this time
The temperature difference of the feeding temperature of the increase material of heat exchange simply, material and column plate is larger, is not easy to material gasification reaction, causes to exchange heat
Efficiency is lower, the raising of energy consumption.
Summary of the invention
To solve the above problems, overcome the deficiencies in the prior art, it is lower and can that the utility model provides a kind of energy consumption
Conducive to the recyclable device of the chondroitin sulfate extract liquor of material gasification reaction, it is higher and be not easy to object to can be effectively solved energy consumption
The problem of expecting gasification reaction.
The utility model solve above-mentioned technical problem the specific technical proposal is: the chondroitin sulfate extract liquor returns
Receiving apparatus, including destilling tower and condensing tower, it is characterised in that heat exchanger, the steaming are provided between the destilling tower and condensing tower
Evaporating tower includes heating structure and heat exchange structure, and the heat exchange structure includes stripping section, changeover portion and rectifying section, stripping section, transition
The side of section and rectifying section is provided with liquid-inlet, and the heat exchanger includes the import of heat exchanger condensate liquid and heat exchanger condensate liquid
Outlet, the heat exchanger condensate liquid import is connected with material pipe, heat exchanger condensate outlet pass through pipeline respectively with stripping section,
Changeover portion is connected with the liquid-inlet of rectifying section side, and thermometer, the distillation tower top are provided at heat exchanger condensate outlet
Portion is successively connected with heat exchanger and condensing tower by pipeline.
Further, the condensing tower is provided with the import of condensing tower condensate liquid and condensing tower condensate outlet, condensing tower
Condensate liquid be arranged to water.
Further, it is provided with tubulation in the heat exchanger and condensing tower, the material of tubulation is arranged to two-phase stainless
Steel.
Further, the destilling tower heat exchange structure is arranged to heat exchanger plates, the liquid of the stripping section, changeover portion and rectifying section
Body import is provided with inlet valve.
The beneficial effects of the utility model are: the heat exchanger realizes the recycling of energy；The heat exchange structure packet
Stripping section, changeover portion and rectifying section are included, the side of stripping section, changeover portion and rectifying section is provided with liquid-inlet, this is based on
On the basis of heat exchanger preheats initial material, bubble point temperature is approached, and can be according to the difference and column plate temperature of temperature of charge
The difference of degree switches the feed inlet of initial material, reduces the initial material of preheating and the temperature difference of column plate as much as possible, improve
The efficiency of gasification；Tubulation is provided in heat exchanger and condensing tower, the material of tubulation is arranged to two phase stainless steel, is effectively prevented
Corrosion because of chloride ion to steel, thus the problem of polluting alcohol.
Detailed description of the invention:
Attached drawing 1 is the utility model structure diagram；In attached drawing:
1. condensing tower, 2. heat exchanger condensate liquid imports, 3. heat exchangers, 4. heat exchanger condensate outlets, 5. temperature
Meter, 6. liquid-inlets, 7. rectifying sections, 8. changeover portions, 9. inlet valves, 10. stripping sections, 11. heating structures.
Specific embodiment:
To keep the purposes, technical schemes and advantages of the utility model implementation clearer, 1 more comprehensively with reference to the drawings
Ground description.In the description to the utility model, it is to be understood that term " center ", "upper", "lower", "left", "right",
The orientation or positional relationship of the instructions such as " rear ", " lower-left ", " upper right ", "outside" is to be based on the orientation or positional relationship shown in the drawings,
It is merely for convenience of describing the present invention and simplifying the description, rather than the device or element of indication or suggestion meaning must have
Specific orientation is constructed and operated in a specific orientation, therefore should not be understood as the limitation to scope of protection of the utility model.This
Outside, term " first ", " second ", " third " are used for descriptive purposes only and cannot be understood as indicating or suggesting relative importance.
Specific embodiment of the present utility model: the recyclable device of the chondroitin sulfate extract liquor, including destilling tower
With condensing tower 1, it is characterised in that be provided with heat exchanger 3 between the destilling tower and condensing tower 1, the destilling tower includes heating knot
Structure 11 and heat exchange structure, the heat exchange structure include stripping section 10, changeover portion 8 and rectifying section 7, stripping section 10, changeover portion 8 and essence
The side for evaporating section 7 is provided with liquid-inlet 6, and the heat exchanger 3 includes that heat exchanger condensate liquid import 2 and heat exchanger condensate liquid go out
Mouthfuls 4, the heat exchanger condensate liquid import 2 is connected with material pipe, heat exchanger condensate outlet 4 pass through pipeline respectively with stripping section
10, changeover portion 8 is connected with the liquid-inlet 6 of 7 side of rectifying section, and thermometer 5 is provided at heat exchanger condensate outlet 4, described
Successively it is connected with heat exchanger 3 and condensing tower 1 at the top of destilling tower by pipeline.
Further, the condensing tower 1 is provided with the import of condensing tower condensate liquid and condensing tower condensate outlet, condensing tower
1 condensate liquid is arranged to water.
Further, it is provided with tubulation in the heat exchanger 3 and condensing tower 1, the material of tubulation is arranged to two-phase not
Become rusty steel.
Further, the destilling tower heat exchange structure is arranged to heat exchanger plates, the stripping section 10, changeover portion 8 and rectifying section 7
Liquid-inlet 6 be provided with inlet valve 9.
It should be noted that the utility model is a kind of recyclable device of chondroitin sulfate extract liquor, when specific works,
1. the material containing alcohol and sodium chloride is passed through heat exchanger 3 by heat exchanger condensate liquid import 2, at this time material temperature
Spend lower, thermometer 5 shows actual temperature, adjusts inlet valve 9 at this time, opens and send material to stripping section 10, and by heat exchange
Plate is down to heating structure 11, opens heating structure 11 and heats to material, and the material after heating is carried out due to the difference of boiling point
Separation, the gas liquid mixture containing alcohol and water carry out further gas-liquid separation according to the difference of allocation proportion in heat exchanger plates,
Water flow returns heating structure 11, and alcohol steam enters heat exchanger 3；
2. the tubulation of 3 high temperature of heat exchanger preheats material, thermometer 5 shows actual temperature, adjusts inlet valve at this time
9, unlatching send material to changeover portion 8；
3. the tubulation of 3 high temperature of heat exchanger preheats material, thermometer 5 shows actual temperature, adjusts inlet valve at this time
9, it opens and send material the temperature difference of the material and heat exchanger plates that make heating to rectifying section 7 to reduce, to improve separative efficiency；
4. alcohol steam flows into condensing tower 1 by heat exchanger 3, it is collected after condensation, the material of tubulation is arranged to
Two phase stainless steel effectively avoids corrosion of the chondroitin sulfate extract liquor to tubulation containing sodium chloride, extends making for device
Use the service life；Finally the concentrate in heating structure 11 is discharged by discharge gate.
The basic principles and main features of the present invention and the advantages of the present invention have been shown and described above.Current row
The technical staff of industry is described in above embodiments and description it should be appreciated that the present utility model is not limited to the above embodiments
Only illustrate the principles of the present invention, on the premise of not departing from the spirit and scope of the utility model, the utility model is also
It will have various changes and improvements, these various changes and improvements fall within the scope of the claimed invention.The utility model
Claimed range is defined by the appending claims and its equivalent thereof.
Claims (4)
1. a kind of recyclable device of chondroitin sulfate extract liquor, including destilling tower and condensing tower (1), it is characterised in that the distillation
It is provided between tower and condensing tower (1) heat exchanger (3), the destilling tower includes heating structure (11) and heat exchange structure, described to change
Heat structure includes stripping section (10), changeover portion (8) and rectifying section (7), and the one of stripping section (10), changeover portion (8) and rectifying section (7)
Side is provided with liquid-inlet (6), and the heat exchanger (3) includes heat exchanger condensate liquid import (2) and heat exchanger condensate outlet
(4), the heat exchanger condensate liquid import (2) is connected with material pipe, heat exchanger condensate outlet (4) by pipeline respectively with mention
Evaporate section (10), changeover portion (8) is connected with the liquid-inlet (6) of rectifying section (7) side, setting at heat exchanger condensate outlet (4)
Have thermometer (5), is successively connected with heat exchanger (3) and condensing tower (1) at the top of the destilling tower by pipeline.
2. the recyclable device of chondroitin sulfate extract liquor according to claim 1, it is characterised in that the condensing tower (1)
It is provided with the import of condensing tower condensate liquid and condensing tower condensate outlet, the condensate liquid of condensing tower (1) is arranged to water.
3. the recyclable device of chondroitin sulfate extract liquor according to claim 1, it is characterised in that the heat exchanger (3)
With condensing tower (1) in be provided with tubulation, the material of tubulation is arranged to two phase stainless steel.
4. the recyclable device of chondroitin sulfate extract liquor according to claim 1, it is characterised in that the destilling tower heat exchange
Structure setting is provided with charging at heat exchanger plates, the liquid-inlet (6) of the stripping section (10), changeover portion (8) and rectifying section (7)
Valve (9).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820457221.5U CN208302238U (en) | 2018-04-03 | 2018-04-03 | A kind of recyclable device of chondroitin sulfate extract liquor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820457221.5U CN208302238U (en) | 2018-04-03 | 2018-04-03 | A kind of recyclable device of chondroitin sulfate extract liquor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208302238U true CN208302238U (en) | 2019-01-01 |
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ID=64718185
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820457221.5U Active CN208302238U (en) | 2018-04-03 | 2018-04-03 | A kind of recyclable device of chondroitin sulfate extract liquor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208302238U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110496490A (en) * | 2019-09-19 | 2019-11-26 | 上海富钟节能环保科技有限公司 | A kind of device and method for collecting escaping gas |
-
2018
- 2018-04-03 CN CN201820457221.5U patent/CN208302238U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110496490A (en) * | 2019-09-19 | 2019-11-26 | 上海富钟节能环保科技有限公司 | A kind of device and method for collecting escaping gas |
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| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: A recovery device for chondroitin sulfate extract Effective date of registration: 20210726 Granted publication date: 20190101 Pledgee: Bank of China Limited Sishui sub branch Pledgor: SHANDONG XINSHENG BIO-TECH Co.,Ltd. Registration number: Y2021980006770 |