CN207899001U - The film condensing device of calm and peaceful Gallus domesticlus brisson Gly-His-Lys - Google Patents
The film condensing device of calm and peaceful Gallus domesticlus brisson Gly-His-Lys Download PDFInfo
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- CN207899001U CN207899001U CN201721418110.5U CN201721418110U CN207899001U CN 207899001 U CN207899001 U CN 207899001U CN 201721418110 U CN201721418110 U CN 201721418110U CN 207899001 U CN207899001 U CN 207899001U
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- separation chamber
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Abstract
The utility model discloses a kind of film condensing devices of calm and peaceful Gallus domesticlus brisson Gly-His-Lys, it is characterised in that：Including loading assemblies, inspissator, evaporate separation chamber and material collecting box, upper and lower ends are respectively arranged with upper sealing panel and lower sealing plate in inspissator, array has multiple hollow and inclined concentration tube between upper sealing panel and lower sealing plate, the top of evaporation separation chamber, which is provided with, to be tangential on evaporation separation chamber and exports the separate inlet opening being connected with the gas-liquid mixed of inspissator, the bottom of evaporation separation chamber is provided with concentrate outlet, evaporation is provided with steam (vapor) outlet at the top of separation chamber, the condensation-water drain connects having heaters, heater is connected to the high-temperature steam entrance, the steam (vapor) outlet is connected with an auxiliary heater, auxiliary heater is connect with compressor, compressor is connected to high-temperature steam entrance.
Description
Technical field
The utility model is related to a kind of enrichment facility more particularly to a kind of film condensing devices of calm and peaceful Gallus domesticlus brisson Gly-His-Lys.
Background technology
Calm and peaceful Gallus domesticlus brisson Gly-His-Lys not only good absorbing, it is in good taste, it can more reach the ideal purpose of the five internal organs equilibrium six internal organs, alleviate conditioning
Female menstrual period perplexs, and is a pervasive nutriment.Calm and peaceful Gallus domesticlus brisson Gly-His-Lys improve women skin aging, and conditioning menstrual period puzzlement increases
Strong skin elasticity improves metabolism, meanwhile, there is immunoloregulation function.
Existing method for concentration includes evaporation and concentration, vacuum concentration and film concentration.
Evaporation and concentration is that material is heated, and makes the volatile partial moisture of material in its boiling temperature constantly by liquid
Generated indirect steam constantly excludes when becoming gaseous state, and will gasify, to make the concentration of product be continuously improved, until reaching
Concentration requirement.
Vacuum concentration is using being evaporated in vacuo or the methods of mechanically decoupled concentrated to reach material.Currently, dense in order to improve
The quality of contracting product, widely used vacuum concentration are right with steam indirect heating manner generally under 18~8kPa low-pressure states
Feed liquid heats, and makes its explosive evaporation at low temperature, and such temperature of charge is low, and the temperature difference for heating steam used and boiling liquid material increases
Greatly, under identical heat transfer condition, evaporation rate when than atmospheric evaporation is high, can reduce the loss of liquid material nutrition, and using low
Pressure steam does evaporation heat source.Under Preheated steam pressure same case, when vacuum evaporation, solution low boiling point, heat transfer temperature difference increases
The heat transfer area of evaporator can be reduced accordingly greatly；The solution that non-refractory can be evaporated, especially suitable in food production
The evaporation of thermal sensitivity feed liquid；Low-pressure steam or exhaust steam can be utilized to make heating agent；Operation temperature is low, and heat loss is less；To material
Liquid plays heating bactericidal effect, is conducive to the preservation of food, drug.But due to being concentrated in vacuo, there must be pumped vacuum systems, to increase
Mill auxiliaries device and power；Increase since evaporation latent heat is reduced with boiling point, so heat consumption is big.
Membrane type enrichment facility is the form flowing for making feed liquid be dispersed into liquid film on tube wall or wall, to make disengagement area
It greatly increases, improves and be concentrated by evaporation efficiency.It eliminates traditional vacuum concentration and needs the technological requirement vacuumized.In concentration technology mistake
Cheng Zhong is conducive to improve the effects of energy conservation and environmental protection that calm and peaceful Gallus domesticlus brisson Gly-His-Lys are manufactured.
Utility model content
The technical problems to be solved in the utility model is the present situation for the prior art, provides a kind of calm and peaceful Gallus domesticlus brisson Gly-His-Lys
Film condensing device realizes calm and peaceful Gallus domesticlus brisson Gly-His-Lys concentration technology, has the characteristics that energy conservation and environmental protection.
Technical solution is used by the utility model solves above-mentioned technical problem：Including loading assemblies, inspissator, evaporation
Separation chamber, material collecting box；
Upper and lower ends are respectively arranged with upper sealing panel and lower sealing plate in inspissator, between upper sealing panel and lower sealing plate
Array has multiple hollow concentration tubes, and top to the upper sealing panel of inspissator forms mixed zone, upper sealing panel in inspissator and
Enrichment region is formed between lower sealing plate, bottom to the lower sealing plate of inspissator forms feed(raw material)inlet area, the top setting of enrichment region
There are high-temperature steam entrance, the lower part of enrichment region to be provided with condensation-water drain, the top of mixed zone is provided with gas-liquid mixed outlet, former
The bottom of material inlet region is provided with feed(raw material)inlet；
The agitator tank that loading assemblies include feed liquid storage box, are connected with the feed liquid storage box, the bottom of agitator tank passes through one
Delivery pump is connect with the feed(raw material)inlet, and a stirring motor is provided at the top of agitator tank, is arranged on the output shaft of stirring motor
There is a paddle being placed in agitator tank；
The top of evaporation separation chamber, which is provided with, to be tangential on evaporation separation chamber outer wall and exports phase with the gas-liquid mixed of inspissator
Separate inlet opening even, the bottom for evaporating separation chamber are provided with the connected concentrate outlet of a material collecting box, evaporate separation chamber
Top is provided with steam (vapor) outlet；
The condensation-water drain connects having heaters, and heater is connected to the high-temperature steam entrance, the steam (vapor) outlet
It is connected with an auxiliary heater, auxiliary heater is connect with compressor, and compressor is connected to high-temperature steam entrance.
As an improvement, the concentration tube, in the tilted arrangement of enrichment region, the concentration tube of inclined design increases concentration pipe range
Degree reduces the resistance of feed liquid rising, increases feed liquid evaporation effect.
It improves again, the evaporation separation chamber includes a separation ontology, is provided with a hollow tube in separation ontology, is detaching
It is provided with hang plate on the inner wall of ontology, which separates separate inlet opening and steam (vapor) outlet, the company of offering in the middle part of hang plate
Hole is connected, is connected at the top of hollow tube on the hole wall of connection through-hole.Indirect steam and concentrate solution are outside separation ontology
Wall tangentially enters within separation ontology, and declines around hollow pipe outer wall spiral, and heavier concentrate solution is gathered in evaporation separation
The bottom of room, and export and be discharged from concentrate, lighter indirect steam moves upwards from the lower port of hollow tube again, finally from point
Steam (vapor) outlet discharge from body upper part.
It improves again, helical blade is provided on the concentrate outlet inside wall of the evaporation separation chamber, by the way that helical-blade is arranged
Piece, it is therefore prevented that extraneous air enters in evaporation separation chamber, influences gas-liquid separation effect.
Compared with prior art, the utility model has the advantage of：The utility model recycles the condensation from inspissator
The cooling water that water out comes out carries out heating and gasifying using heater, generates high-temperature steam as heat source, while recycling cold
Condenser steam (vapor) outlet come out indirect steam, it is heated using auxiliary heater, and using compressor compressed into
One step improves vapor (steam) temperature, and the high-temperature steam of generation enters the high-temperature steam entrance of inspissator, and high-temperature steam is full of enrichment region
Concentrate pipe outer wall, at the same time, feed liquid enters from feed liquid storage box in agitator tank, stirring motor work, paddle to feed liquid into
It is sufficiently stirred before entering inspissator, the feed(raw material)inlet of feed liquid inspissator bottom enters later, in concentration tube bottommost section
It is completely filled with feed liquid, heat relies primarily on convection current, in the centre portion of concentration tube, starts to generate steam bubble, feed liquid is made to produce
Raw climbing power generates strong climbing power due to the double evaporation-cooling of expansion in the top section of concentration tube, and feed liquid exists in film-form
Uplink in pipe is in spray form in tube top portion, realizes that feed liquid enters from the bottom of inspissator in concentration tube, heated steam heating boiling
Rise rear rapid vaporization, indirect steam and feed liquid caused by feed liquid rise along its inner wall in membranaceous high speed, carry out continuous heat transfer and steam
Hair, such feed liquid are gradually concentrated from from the bottom of inspissator to pipe top export, and the feed liquid after concentration is entered with high speed steams
Separation chamber is sent out, by evaporating the centrifugation of separation chamber, the concentrate for reaching concentration requirement is discharged from separation chamber bottom, separately
Outside, indirect steam is recycled from discharge at the top of evaporation separation chamber into auxiliary heater temperature raising, in addition, the cooling that concentration generates
Water is discharged from the condensation-water drain of inspissator, is utilized again by gasification into heater, realizes recycling for water, have section
The feature of energy environmental protection.
Description of the drawings
Fig. 1 is the structural schematic diagram of the film condensing device of calm and peaceful Gallus domesticlus brisson Gly-His-Lys in the utility model embodiment；
Fig. 2 is the structural schematic diagram of upper evaporation separation chamber in the utility model embodiment.
Specific implementation mode
The utility model is described in further detail below in conjunction with attached drawing embodiment.
As shown in Figure 1, 2, the film condensing device of the calm and peaceful Gallus domesticlus brisson Gly-His-Lys in this implementation, including loading assemblies, inspissator 1,
Evaporate separation chamber 3, material collecting box 4.
Wherein, upper and lower ends are respectively arranged with upper sealing panel 111 and lower sealing plate 112 in inspissator 1, in upper sealing panel
Array has multiple hollow concentration tubes 15, top to the upper sealing panel 111 of inspissator 1 to be formed between 111 and lower sealing plate 112
Mixed zone 12 forms enrichment region 13 between the upper sealing panel 111 and lower sealing plate 112 in inspissator 1, and the bottom of inspissator 1 is extremely
Lower sealing plate 112 forms feed(raw material)inlet area 14, and the top of enrichment region 13 is provided with high-temperature steam entrance 131, under enrichment region 13
Portion is provided with condensation-water drain 132, and the top of mixed zone 12 is provided with gas-liquid mixed outlet 121, the bottom in 14th area of feed(raw material)inlet
It is provided with feed(raw material)inlet 141；
The agitator tank 23 that loading assemblies include feed liquid storage box 21, are connected with the feed liquid storage box 21, the bottom of agitator tank 23
Portion is connect by a delivery pump 24 with the feed(raw material)inlet 141, and the top of agitator tank 23 is provided with a stirring motor 22, stirring electricity
A paddle 221 being placed in agitator tank 21 is provided on the output shaft of machine 22；
The top of evaporation separation chamber 3, which is provided with, to be tangential on evaporation 3 outer wall of separation chamber and is exported with the gas-liquid mixed of inspissator 1
The bottom of 121 connected separate inlet openings 31, evaporation separation chamber 3 is provided with the connected concentrate outlet 33 of a material collecting box 4,
The top of evaporation separation chamber 3 is provided with steam (vapor) outlet 32；
The condensation-water drain 132 connects having heaters 5, and heater 5 is connected to the high-temperature steam entrance 131, described
Steam (vapor) outlet 32 is connected with an auxiliary heater 51, and auxiliary heater 51 is connect with compressor, compressor 6 and high-temperature steam entrance
131 connections.
Further, concentration tube 15 increases concentration tube in 13 tilted arrangement of enrichment region, the concentration tube 15 of inclined design
15 length reduce the resistance of feed liquid rising, increase feed liquid evaporation effect.
In addition, evaporation separation chamber 3 includes a separation ontology 301, it is provided with a hollow tube 34 in separation ontology 301,
It detaches and is provided with hang plate 35 on the inner wall of ontology 301, which separates separate inlet opening 31 and steam (vapor) outlet 32, is inclining
35 middle part of inclined plate offers connection through-hole 351, and the top of hollow tube 34 is connected on the hole wall of connection through-hole 351.Secondary steaming
Vapour and concentrate solution tangentially enter from the outer wall of separation ontology 301 within separation ontology 301, and around 34 outer wall spiral of hollow tube
Decline, heavier concentrate solution is gathered in the bottom of evaporation separation chamber 31, and is discharged from concentrate outlet 33, lighter secondary steaming
Vapour is moved upwards from the lower port of hollow tube 34 again, is finally discharged from the steam (vapor) outlet 32 on 301 top of separation ontology.
In addition, the concentrate of evaporation separation chamber 31 exports is provided with helical blade 331 on 33 inner walls, by the way that helical-blade is arranged
Piece 331, it is therefore prevented that extraneous air enters in evaporation separation chamber 31, influences gas-liquid separation effect.
The utility model recycle from the condensation-water drain 132 of inspissator 1 come out cooling water, using heater 5 into
Row heating and gasifying generates high-temperature steam as heat source, while recycling the indirect steam that 3 steam (vapor) outlet 32 of condenser comes out,
It is heated using auxiliary heater 51, and carries out compression using compressor 6 and further increases vapor (steam) temperature, the height of generation
Warm steam enters the high-temperature steam entrance 131 of inspissator 1, and high-temperature steam is full of 15 outer wall of concentration tube of enrichment region 13, same with this
When, feed liquid enters from feed liquid storage box 21 in agitator tank 23, and stirring motor 22 works, and paddle 221 enters inspissator 1 to feed liquid
Before be sufficiently stirred, later 1 bottom of feed liquid inspissator feed(raw material)inlet 141 enter, it is complete in 15 bottommost section of concentration tube
It is full of feed liquid entirely, heat relies primarily on convection current, in the centre portion of concentration tube 15, starts to generate steam bubble, feed liquid is made to produce
Raw climbing power generates strong climbing power due to the double evaporation-cooling of expansion in the top section of concentration tube 15, and feed liquid is in film-form
The uplink in pipe is in spray form in tube top portion, realizes that feed liquid enters from the bottom of inspissator 1 in concentration tube 15, heated steam
Rapid vaporization after ebuillition of heated, indirect steam and feed liquid caused by feed liquid rise along its inner wall in membranaceous high speed, carry out continuous
Heat transfer evaporation, such feed liquid are gradually concentrated from from the bottom of inspissator 1 to pipe top export, and the feed liquid after concentration is with height
Speed enters evaporation separation chamber 3, by evaporating the centrifugation of separation chamber 3, reaches the concentrate of concentration requirement from separation chamber
Bottom is discharged, in addition, indirect steam is recycled from the 3 top discharge of evaporation separation chamber into 51 temperature raising of auxiliary heater, in addition,
It concentrates the cooling water generated to be discharged from the condensation-water drain 132 of inspissator 1, is utilized, realize by gasification again into heater 5
Recycling for water, has the characteristics that energy conservation and environmental protection.
Claims (4)
1. a kind of film condensing device of calm and peaceful Gallus domesticlus brisson Gly-His-Lys, it is characterised in that：Including loading assemblies, inspissator (1), evaporation separation
Room (3), material collecting box (4)；
Inspissator (1) interior upper and lower ends are respectively arranged with upper sealing panel (111) and lower sealing plate (112), in upper sealing panel (111)
Array has multiple hollow concentration tubes (15), top to upper sealing panel (111) of inspissator (1) between lower sealing plate (112)
It is formed mixed zone (12), forms enrichment region (13) between the upper sealing panel (111) and lower sealing plate (112) in inspissator (1), it is dense
The bottom of contracting device (1) to lower sealing plate (112) forms feed(raw material)inlet area (14), and the top of enrichment region (13) is provided with high-temperature steam
The lower part of entrance (131), enrichment region (13) is provided with condensation-water drain (132), and the top of mixed zone (12) is provided with gas-liquid and mixes
Outlet (121) is closed, the bottom of feed(raw material)inlet area (14) is provided with feed(raw material)inlet (141)；
The agitator tank (23) that loading assemblies include feed liquid storage box (21), are connected with the feed liquid storage box (21), agitator tank (23)
Bottom connect with the feed(raw material)inlet (141) by a delivery pump (24), be provided at the top of agitator tank (23) stirring electricity
Machine (22) is provided with a paddle (221) being placed in agitator tank (23) on the output shaft of stirring motor (22)；
The top of evaporation separation chamber (3), which is provided with, to be tangential on evaporation separation chamber's (3) outer wall and goes out with the gas-liquid mixed of inspissator (1)
The bottom of the connected separate inlet opening (31) of mouth (121), evaporation separation chamber (3) is provided with the connected concentration of a material collecting box (4)
Object exports (33), and steam (vapor) outlet (32) is provided at the top of evaporation separation chamber (3)；
Condensation-water drain (132) the connection having heaters (5), heater (5) are connected to the high-temperature steam entrance (131),
The steam (vapor) outlet (32) is connected with an auxiliary heater (51), and auxiliary heater (51) is connect with compressor (6), compressor
(6) it is connected to high-temperature steam entrance (131).
2. the film condensing device of calm and peaceful Gallus domesticlus brisson Gly-His-Lys according to claim 1, it is characterised in that：The concentration tube (15) exists
Enrichment region (13) tilted arrangement.
3. the film condensing device of calm and peaceful Gallus domesticlus brisson Gly-His-Lys according to claim 1, it is characterised in that：The evaporation separation chamber
(3) include a separation ontology (301), a hollow tube (34) is provided in separation ontology (301), in separation ontology (301)
Hang plate (35) is provided on inner wall, which separates separate inlet opening (31) and steam (vapor) outlet (32), in hang plate
(35) middle part offers connection through-hole (351), is connected at the top of hollow tube (34) on the hole wall of connection through-hole (351).
4. the film condensing device of calm and peaceful Gallus domesticlus brisson Gly-His-Lys according to claim 1, it is characterised in that：The evaporation separation chamber
(3) helical blade (331) is provided on concentrate outlet (33) inner wall.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721418110.5U CN207899001U (en) | 2017-10-30 | 2017-10-30 | The film condensing device of calm and peaceful Gallus domesticlus brisson Gly-His-Lys |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721418110.5U CN207899001U (en) | 2017-10-30 | 2017-10-30 | The film condensing device of calm and peaceful Gallus domesticlus brisson Gly-His-Lys |
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| Publication Number | Publication Date |
|---|---|
| CN207899001U true CN207899001U (en) | 2018-09-25 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201721418110.5U Expired - Fee Related CN207899001U (en) | 2017-10-30 | 2017-10-30 | The film condensing device of calm and peaceful Gallus domesticlus brisson Gly-His-Lys |
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| CN (1) | CN207899001U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2020155840A1 (en) * | 2019-02-01 | 2020-08-06 | 武汉美味源生物工程有限公司 | Hollow helical blade heated thin-film evaporator and evaporation method |
| CN114014394A (en) * | 2021-11-05 | 2022-02-08 | 中国船舶重工集团公司第七一八研究所 | Waste liquid heat pump evaporation system and control method, control equipment and medium thereof |
-
2017
- 2017-10-30 CN CN201721418110.5U patent/CN207899001U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2020155840A1 (en) * | 2019-02-01 | 2020-08-06 | 武汉美味源生物工程有限公司 | Hollow helical blade heated thin-film evaporator and evaporation method |
| CN114014394A (en) * | 2021-11-05 | 2022-02-08 | 中国船舶重工集团公司第七一八研究所 | Waste liquid heat pump evaporation system and control method, control equipment and medium thereof |
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| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180925 Termination date: 20191030 |
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| CF01 | Termination of patent right due to non-payment of annual fee |