CN207614369U - A kind of film condensing device of calm and peaceful Gallus domesticlus brisson Gly-His-Lys - Google Patents
A kind of film condensing device of calm and peaceful Gallus domesticlus brisson Gly-His-Lys Download PDFInfo
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- CN207614369U CN207614369U CN201721417097.1U CN201721417097U CN207614369U CN 207614369 U CN207614369 U CN 207614369U CN 201721417097 U CN201721417097 U CN 201721417097U CN 207614369 U CN207614369 U CN 207614369U
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- inspissator
- condenser
- separation chamber
- steam
- outlet
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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 inspissator,High temperature shift component,Evaporate separation chamber and condenser,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,High temperature shift component includes the steam collection pipe being connected with boiler exhaust gas,The heat pump being connected with steam collection pipe,The diffuser being connected is exported with heat pump,Connect the connecting tube of diffuser and high-temperature steam entrance,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,Steam (vapor) outlet is connected with the top of condenser,The top of condenser is provided with cold water inlet,The bottom of condenser is provided with condensate outlet,Air outlet slit is provided at the top of condenser.
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, recycles the heat of boiler exhaust gas, has energy-saving and environment-friendly spy
Point.
Technical solution is used by the utility model solves above-mentioned technical problem：A kind of film concentration of calm and peaceful Gallus domesticlus brisson Gly-His-Lys
Device, it is characterised in that：Including inspissator, high temperature shift component, evaporation separation chamber, condenser and condensation water tank, in inspissator
Upper and lower ends are respectively arranged with upper sealing panel and lower sealing plate, between upper sealing panel and lower sealing plate array have it is multiple hollow and
Mixed zone is formed on inclined concentration tube, the top of inspissator to upper sealing panel, the upper sealing panel and lower sealing plate in inspissator it
Between form enrichment region, bottom to the lower sealing plate of inspissator forms feed(raw material)inlet area, and the top of enrichment region is provided with high-temperature steam
The lower part of entrance, enrichment region is provided with condensation-water drain, and the top of mixed zone is provided with gas-liquid mixed outlet, feed(raw material)inlet area
Bottom is provided with feed(raw material)inlet, and high temperature shift component includes the steam collection pipe being connected with boiler exhaust gas and steam collection pipe phase
Heat pump even, the diffuser connected with heat pump outlet, the connecting tube for connecting diffuser and high-temperature steam entrance, evaporate separation chamber
Top, 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, and separation chamber is evaporated
Bottom is provided with concentrate outlet, evaporates and is provided with steam (vapor) outlet at the top of separation chamber, the top of steam (vapor) outlet and condenser
It is connected, the top of condenser is provided with cold water inlet, and the bottom of condenser is provided with condensate outlet, the top setting of condenser
There are air outlet slit, the condensation-water drain connection of the condensation water tank and inspissator, the condensate outlet of condensation water tank and condenser
Connection, condensation water tank are connected by the cold water inlet of a water pump and condenser.
As an improvement, being provided with circulation pipe between evaporation separation chamber bottom and the feed(raw material)inlet area of inspissator, pass through
Circulation pipe is set, and the concentrate that evaporation can be detached to indoor low concentration is recirculated in the area of feed(raw material)inlet, is carried out again
Primary concentration cycles.
It improves again, a silk screen is provided in the evaporation separation chamber, by the way that silk screen is arranged, enter in gas-liquid mixture high speed
When evaporating separation chamber, prevents concentrate from entering in condenser with steam, cause the waste of concentrate.
It improves again, mounting hole is offered on the upper sealing panel and/or lower sealing plate, plastic hoop is provided in mounting hole,
The nozzle of the concentration tube is plugged in plastic hoop, by the way that plastic hoop is arranged, on the one hand, is convenient for the installation of concentration tube, another party
Face improves the sealing performance of concentration tube installation.
It improves again, a vacuum pump is provided at the top of the inspissator, by the way that a vacuum pump is arranged so that enter in feed liquid
When concentration tube, negative pressure is formed in the mixed zone of inspissator, can be risen in concentration tube convenient for feed liquid, to increase concentration tube
Design.
It improves again, the film condensing device further includes a feed liquid storage box, the agitator tank that is connected with the feed liquid storage box, is stirred
The bottom for mixing case is connect with first liquor inlet, and a stirring motor, the output of stirring motor are provided at the top of agitator tank
Be provided with a paddle being placed in agitator tank on axis, pass through and agitator tank, stirring motor and paddle are set so that feed liquid into
It has obtained fully stirring before entering the first liquor inlet of the first evaporator, it is therefore prevented that the precipitation of feed liquid.
Compared with prior art, the utility model has the advantage of：The utility model recycles the heat that boiler generates and steams
Vapour, however the temperature of the hot steam of boiler generation does not reach the requirement that design needs, and cannot directly use, the utility model profit
With heat pump and diffuser, initial steam is first passed through to the nozzle of heat pump, since flow velocity is very high, the pressure reduction of mixing chamber sucks pot
Stove steam is simultaneously mixed, and subsequently into diffuser, flow velocity reduces at this time, and kinetic energy is converted into pressure energy so that the pressure of steam and
Temperature reaches the state of heating steam, and heating steam enters from the high-temperature steam entrance of inspissator, and heating steam is in enrichment region
It is moved from top to bottom along concentration tube, at the same time, feed liquid enters from the feed(raw material)inlet of inspissator bottom, in concentration tube bottommost
Feed liquid is completely filled in section, heat relies primarily on convection current, in the centre portion of concentration tube, starts to generate steam bubble, make
Feed liquid generates climbing power, in the top section of concentration tube, strong climbing power is generated due to the double evaporation-cooling of expansion, feed liquid is in thin
The membranaceous 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
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 to pipe top export, and the feed liquid after concentration is with high speed
Reach the concentrate of concentration requirement from separation chamber bottom by evaporating the centrifugation of separation chamber into evaporation separation chamber
Discharge does not reach the concentrate of concentration by circulation pipe, returns inspissator bottom, secondary concentration is carried out, in addition, secondary steaming
Vapour is from discharge at the top of evaporation separation chamber, into condenser, after the condensed water mixing in indirect steam and condenser, and cooling gas
It is discharged from the top of condenser, avoids the discharge of high-temperature steam, in addition, the utility model is recycled using a condensation water tank
The condensed water that inspissator and condenser generate later is re-used in condenser using water pump, has saved water source.
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 mounting structure schematic diagram of upper sealing panel and concentration tube 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 inspissator 1, high temperature shift group
Part, evaporation separation chamber 3, condenser 4 and condensation water tank 5.
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 a multiple hollow and inclined concentration tube 15 between 111 and lower sealing plate 112, the top of inspissator 1 to upper sealing panel 111
Mixed zone 12 is formed, enrichment region 13, the bottom of inspissator 1 are formed between the upper sealing panel 111 and lower sealing plate 112 in inspissator 1
Portion 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 entrance 131, enrichment region 13
Lower part be provided with condensation-water drain 132, the top of mixed zone 12 is provided with gas-liquid mixed outlet 121, feed(raw material)inlet area 14
Bottom is provided with feed(raw material)inlet 141, and high temperature shift component includes the steam collection pipe 21 being connected with 20 tail gas of boiler, received with steam
The connected heat pump 22 of collector 21, connect diffuser 23 and high-temperature steam entrance 131 at the diffuser 23 being connected with the outlet of heat pump 22
Connecting tube 24, the top of evaporation separation chamber 3, which is provided with, to be tangential on evaporation separation chamber 3 and exports 121 with the gas-liquid mixed of inspissator 1
The bottom of connected separate inlet opening 31, evaporation separation chamber 3 is provided with concentrate outlet 33, the top setting of evaporation separation chamber 3
There are steam (vapor) outlet 32, steam (vapor) outlet 32 to be connected with the top of condenser 4, the top of condenser 4 is provided with cold water inlet 41, cold
The bottom of condenser 4 is provided with condensate outlet 42, and the top of condenser 4 is provided with air outlet slit 43, condensation water tank 5 and inspissator
1 condensation-water drain 132 connects, and condensation water tank 5 is connect with the condensate outlet 42 of condenser 4, and condensation water tank 5 passes through a water pump
41 connect with the cold water inlet 41 of condenser 4.
Further, the top of inspissator 1 is provided with a vacuum pump 6, pass through be arranged a vacuum pump 6 so that feed liquid into
When entering concentration tube 15, negative pressure is formed in the mixed zone of inspissator 1 12, can be risen in concentration tube 15 convenient for feed liquid, to increase
The design of concentration tube 15 is grown.
In addition, circulation pipe 35 is provided between evaporation 3 bottom of separation chamber and the feed(raw material)inlet area 14 of inspissator 1, by setting
Circulation pipe 35 is set, the concentrate of the low concentration evaporated in separation chamber 3 can be recirculated in feed(raw material)inlet area 14, into
The concentration cycles of row again.
In addition, being provided with a silk screen 34 in evaporation separation chamber 3, by the way that silk screen 34 is arranged, enter in gas-liquid mixture high speed
When evaporating separation chamber 3, prevents concentrate from entering in condenser 4 with steam, cause the waste of concentrate.
In addition, mounting hole is offered on upper sealing panel 111 and/or lower sealing plate 112, plastic hoop is provided in mounting hole
16, the nozzle of the concentration tube 1 is plugged in plastic hoop 16, by the way that plastic hoop 16 is arranged, on the one hand, is convenient for the peace of concentration tube 15
On the other hand dress improves the sealing performance of the installation of concentration tube 15.
Finally, film condensing device further include a feed liquid storage box 7, the agitator tank 81 that is connected with the feed liquid storage box 7, stirring
The bottom of case 81 is connect with first liquor inlet 16, and the top of agitator tank 81 is provided with a stirring motor 82, stirring motor
A paddle 83 being placed in agitator tank 81 is provided on 82 output shaft, by the way that agitator tank 81, stirring motor 82 is arranged and stirs
Mix leaf 83 so that feed liquid has obtained fully stirring before the first liquor inlet 16 for entering the first evaporator 1, it is therefore prevented that feed liquid
Precipitation.
The utility model recycles the hot steam that boiler 20 generates, however the temperature of the hot steam of the generation of boiler 20 does not have
Reach the requirement that design needs, cannot directly use, the utility model utilizes heat pump 22 and diffuser 23, is first passed through initial steam
The nozzle of heat pump 22, since flow velocity is very high, the pressure reduction of mixing chamber sucks Boiler Steam and is mixed, subsequently into expansion
Separate tube 23, flow velocity reduction, kinetic energy are converted into pressure energy at this time so that the pressure and temperature of steam reaches the state of heating steam, adds
Hot steam enters from the high-temperature steam entrance 131 of inspissator 1, heating steam in the enrichment region 13 along concentration tube 15 from up to
Lower movement, at the same time, feed liquid enter from the feed(raw material)inlet 141 of 1 bottom of inspissator, in 15 bottommost section of concentration tube completely
Full of feed liquid, heat relies primarily on convection current, in the centre portion of concentration tube 15, starts to generate steam bubble, feed liquid is made to generate
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 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 1 in concentration tube 15, heated steam adds
Rapid vaporization after heat boiling, indirect steam and feed liquid caused by feed liquid, in the rising of membranaceous high speed, are continuously passed along its inner wall
Thermal evaporation, such feed liquid are gradually concentrated from from the bottom of inspissator 1 to pipe top export, the feed liquid after concentration with high speed into
Enter to evaporate separation chamber 3, by evaporating the centrifugation of separation chamber 3, reaches the concentrate of concentration requirement from separation chamber bottom
Discharge does not reach the concentrate of concentration by circulation pipe 35, returns 1 bottom of inspissator, secondary concentration is carried out, in addition, two
Secondary steam is from the 3 top discharge of evaporation separation chamber, into condenser 4, after the condensed water mixing in indirect steam and condenser 4,
Cooling gas is discharged from the top of condenser 4, avoids the discharge of high-temperature steam, in addition, the utility model utilizes a condensed water
Case 5 has been recycled the condensed water that inspissator 1 and condenser 4 generate and has been re-used later in condenser using water pump 51
4, save water source.
Claims (5)
1. a kind of film condensing device of calm and peaceful Gallus domesticlus brisson Gly-His-Lys, it is characterised in that：Including inspissator (1), high temperature shift component, evaporation
Separation chamber (3), condenser (4) and condensation water tank (5), inspissator (1) interior upper and lower ends be respectively arranged with upper sealing panel (111) and
Lower sealing plate (112), array has multiple hollow and inclined concentration tube between upper sealing panel (111) and lower sealing plate (112)
(15), the top of inspissator (1) to upper sealing panel (111) forms mixed zone (12), the upper sealing panel (111) in inspissator (1)
Enrichment region (13) is formed between lower sealing plate (112), bottom to the lower sealing plate (112) of inspissator (1) forms feed(raw material)inlet
The top in area (14), enrichment region (13) is provided with high-temperature steam entrance (131), and the lower part of enrichment region (13) is provided with condensed water and goes out
The top of mouth (132), mixed zone (12) is provided with gas-liquid mixed outlet (121), and the bottom of feed(raw material)inlet area (14) is provided with original
Expect entrance (141), high temperature shift component includes the steam collection pipe (21) and steam collection pipe being connected with boiler (20) tail gas
(21) connected heat pump (22), be connected with heat pump (22) outlet diffuser (23), connect diffuser (23) and high-temperature steam enters
The connecting tube (24) of mouthful (131), the top of evaporation separation chamber (3) be provided be tangential on evaporation separation chamber's (3) outer wall and with concentration
The separate inlet opening (31) that the gas-liquid mixed outlet (121) of device (1) is connected, the bottom of evaporation separation chamber (3) are provided with a concentrate
It exports (33), steam (vapor) outlet (32), the top of steam (vapor) outlet (32) and condenser (4) is provided at the top of evaporation separation chamber (3)
It is connected, the top of condenser (4) is provided with cold water inlet (41), and the bottom of condenser (4) is provided with condensate outlet (42), cold
Air outlet slit (43) is provided at the top of condenser (4), the condensation water tank (5) and the condensation-water drain (132) of inspissator (1) connect
It connects, condensation water tank (5) is connect with the condensate outlet (42) of condenser (4), and condensation water tank (5) passes through a water pump (51) and condensation
The cold water inlet (41) of device (4) connects.
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 evaporation separation chamber
(3) it is provided with circulation pipe (35) between bottom and the feed(raw material)inlet area (14) of inspissator (1).
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) silk screen (34) is provided in.
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 upper sealing panel
(111) and/or on lower sealing plate (112) mounting hole is offered, plastic hoop (16), the concentration tube (15) is provided in mounting hole
Nozzle be plugged in plastic hoop (16).
5. the film condensing device of calm and peaceful Gallus domesticlus brisson Gly-His-Lys according to claim 1, it is characterised in that：The inspissator (1)
Top is provided with a vacuum pump (6).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721417097.1U CN207614369U (en) | 2017-10-30 | 2017-10-30 | A kind of film condensing device of calm and peaceful Gallus domesticlus brisson Gly-His-Lys |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721417097.1U CN207614369U (en) | 2017-10-30 | 2017-10-30 | A kind of film condensing device of calm and peaceful Gallus domesticlus brisson Gly-His-Lys |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207614369U true CN207614369U (en) | 2018-07-17 |
Family
ID=62826949
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721417097.1U Expired - Fee Related CN207614369U (en) | 2017-10-30 | 2017-10-30 | A kind of film condensing device of calm and peaceful Gallus domesticlus brisson Gly-His-Lys |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207614369U (en) |
-
2017
- 2017-10-30 CN CN201721417097.1U patent/CN207614369U/en not_active Expired - Fee Related
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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 |
Granted publication date: 20180717 Termination date: 20191030 |
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| CF01 | Termination of patent right due to non-payment of annual fee |