CN208465201U - A kind of low-temperature vacuum thickener group - Google Patents
A kind of low-temperature vacuum thickener group Download PDFInfo
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- CN208465201U CN208465201U CN201820938697.0U CN201820938697U CN208465201U CN 208465201 U CN208465201 U CN 208465201U CN 201820938697 U CN201820938697 U CN 201820938697U CN 208465201 U CN208465201 U CN 208465201U
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Abstract
The utility model relates to a kind of low-temperature vacuum thickener groups, belong to technical field of food machinery.The vacuum concentration unit is provided with feeding device, material-heat-exchanging device is connected on the feeding device, evaporation concentration device is connected on the material-heat-exchanging device, it is connected on the evaporation concentration device and aromatic cools back receiving apparatus, box chilled water unit is connected on the cooling recyclable device of the fragrance, vacuum generating device is also connected on the cooling recyclable device of the fragrance, hot water circulating device is additionally provided on the material-heat-exchanging device, the bottom of the evaporation concentration device is provided with concentrate recyclable device.The benificial effect of the utility model is to passing through the various pieces of low-temperature vacuum thickener group, effectively the moisture content in fruit juice is evaporated, and cooling recycling is carried out to the fragrance in evaporation moisture content by the cooling recyclable device of fragrance, to effectively raise the utilization rate of material, the utility model structure novel, it is easy to operate.
Description
Technical field
The utility model relates to a kind of low-temperature vacuum thickener groups, belong to technical field of food machinery.
Background technique
Fruit juice is such as to squeeze, be centrifuged by physical method using fruit or vegetables as raw material, extracting the production of obtained juice
Product generally refer to pure juice or 100% fruit juice, and fruit juice is divided into clear juice and suspended pulp by form, and clear juice clarification is saturating
Bright, such as cider, and suspended pulp is uniformly muddy, such as orange juice；It is divided into original fruit juice, fruit syrup, fruit drink, fruit by juice content
Grain fruit drink, juice carbonated drink, fruit-flavor type beverage, and refer to will be in fruit juice by certain technique or equipment for inspissated juice
The fruit juice that moisture is evaporated and obtained after being concentrated, this inspissated juice mainly be more convenient for storage, production and transportation because without
The fruit juice of concentration, if directly carry out it is filling, can to enterprise increase 3-14 times packing material cost and increase 3-14 times transport
Cost, to virtually increase the cost of enterprise.
The method of existing fruit concentration is relatively more, and common method has centrifugal thin-film concentration, freeze concentration, membrane separation concentrated
Contracting, reverse osmosis concentration and heating concentration, but above method is complex, and fruit juice can be destroyed in concentration process
Nutritional ingredient, especially heating concentration destroy the nutritional ingredient of fruit juice even more serious.
Fruit juice is in concentration process, and as the evaporation of moisture can volatilize a large amount of aroma substance, this aroma substance is just
It is the natural essence contained in fruit juice, this natural essence is the essence in fruit juice and very expensive, existing concentration of juices
In production, there are no equipment to be recycled to this aroma substance, to bring certain waste to user.
With advances in technology, traditional vacuum has been concentrated to get certain development, and traditional vacuum concentration refers to will be to be concentrated
Fruit juice be placed in vacuum centrifuge, fruit juice is concentrated by vacuum centrifuge, this method can be realized in room temperature
The purpose that fruit juice is concentrated under state, thickening efficiency is higher, and more can completely keep the nutrition in fruit juice at
Point, however existing vacuum centrifuge structure is complex, material heating temperature height, extreme loss product nutrient substances, loss
The color of product, and the amount handled is smaller, is not able to satisfy the production requirement that user is growing, and whole market is existing at present
Some enrichment facilities are not provided with fragrance recyclable device, cause the byproduct of high added value to be largely lost, cause great resource
Waste.
Simply illustrate that the principle being evaporated in vacuo, vacuum concentration are also referred to as evaporated in vacuo, refer in vacuum below
The evaporation operation of lower progress.Liquid (or solid) is evaporated in vacuo (or distillation) and becomes to need to absorb heat when steam, referred to as
Heat of vaporization.The heat of vaporization of substance is slightly reduced with the raising of vapourizing temperature.Such as lmol water, it is vaporized in 50oC, heat of vaporization
For 42780J, and vaporized in 100oC, heat of vaporization 40680J.The vacuum freshness retaining of vegetable and fruit allows the part moisture content of vegetables true
Evaporative air, whens these water evaporations, will draw heat of vaporization out of vegetables body, so that vegetables is being dehydrated while is being cooled down, water evaporation is utilized
The principle of heat absorption.
In view of the above-mentioned problems, needed in industry a kind of structure novel, ultralow evaporating temperature, superelevation working efficiency ultralow temperature
It is concentrated in vacuo unit, is particularly suitable for fruit juice, drug, health care product, health food, biological agent, the moisture evaporation in enzyme preparation
It extracts, has saved the 50%-70% energy for the subsequent drying process of Related product while having improved 2-3 times of working efficiency, and can
The different cycles of concentration of different end products is adjusted at any time, and general is 3-14 times of cycles of concentration, to solve to face in industry
Series of problems.
Summary of the invention
The technical problem to be solved by the utility model is to provide a kind of low-temperature vacuum thickener group of structure novel,
In order to solve the above-mentioned technical problem, the utility model is realized by following technical method:
A kind of low-temperature vacuum thickener group, is provided with low-temperature vacuum thickener group, the vacuum concentration unit be provided with into
Expect device, be connected with material-heat-exchanging device on the feeding device, be connected with evaporation concentration device on the material-heat-exchanging device,
The material-heat-exchanging device is connected together with the evaporation concentration device by horizontal positioned lateral material connecting tube, described
Connected on evaporation concentration device it is aromatic cool back receiving apparatus, the evaporation concentration device and the cooling recyclable device of fragrance pass through the
One cooling tubulation connects together, and is connected with box chilled water unit on the cooling recyclable device of the fragrance, the fragrance is cooling
It is also connected with vacuum generating device on recyclable device, passes through between the cooling recyclable device of the fragrance and the vacuum generating device
Vacuum connection tube connects together, and hot water circulating device, the evaporation concentration device are additionally provided on the material-heat-exchanging device
Bottom be provided with concentrate recyclable device.
Preferably, the material-heat-exchanging device is provided with the heat exchange shell of inner hollow and structure cylindrical, institute
The upper and lower ends for stating heat exchange shell are respectively arranged with upper conical connecting plate and inferior pyramidal connecting plate, the upper conical connecting plate and
It is provided between the tube sheet flange multiple by tube sheet flanged joint to together between inferior pyramidal connecting plate and heat exchange shell
Material-heat-exchanging pipe, the side of the heat exchange shell are additionally provided with inlet and outlet, are arranged on the upper conical connecting plate
There is lateral material connecting tube.
Preferably, the evaporation concentration device is provided with the evaporation and concentration tank body of inner hollow, the evaporation and concentration tank
It is provided with multiple stiffener plates on the outside of body, is additionally provided with multiple CIP Butterworth Hatch, the steaming on the outside of the evaporation and concentration tank body
The outer upper of hair concentration tank body is additionally provided with material feed inlet, and the transverse direction material connecting tube is connected to the material feed inlet
On, the evaporation and concentration tank body is internally provided with oblique materail tube, and the oblique materail tube is connected to the material feed inlet
On, the lower inside for being concentrated by evaporation tank body is additionally provided with distributing device, and the inside for being concentrated by evaporation tank body is also evenly equipped with more
A foam-blocker.
Preferably, the stepped structure of distributing device, the distributing device is by multiple drapery panels in conical structure
It is welded to each other, the foam-blocker semicircular in shape structure, is provided on the foam-blocker and multiple flutters foam hole.
Preferably, the cooling recyclable device of the fragrance is provided with essence recycling can and is installed on the essence recycling can
The first cooling device, the second cooling device, first cooling device and the second cooling device place and be parallel to each other vertically,
First cooling device and the second cooling device are internally provided with multiple cooling tubulations, and the bottom of the cooling tubulation passes through
Bottom coohng tubulation connects together, and the outer upper of first cooling device is provided with ultralow temperature cooling water apopore, institute
The outer upper for stating the second cooling device is provided with cooling water inlet opening, the cooling water apopore and cooling water inlet opening difference
It is connected on the box chilled water unit.
Preferably, floating ball type liquid level sensor is provided in the essence recycling can, the bottom of the essence recycling can
It is provided with essence recycling discharge port, essence discharging butterfly valve is provided on the essence discharge port, is gone back on the essence discharging butterfly valve
It is connected with discharging centrifugal pump.
Preferably, the concentrate recyclable device is provided with concentrate draw-off pump, the charging of the concentrate draw-off pump
Mouth is connected to the bottom of the evaporation concentration device by concentrate pipeline, and the discharge port of the concentrate draw-off pump is provided with
Line pol detector is additionally provided with threeway pneumatic operated valve on the online pol detector, and the threeway pneumatic operated valve also passes through pipeline
It is connected respectively on concentrate storage tank and material-heat-exchanging device.
Preferably, being also connected with cleaning tapping equipment on the concentrate pipeline, the cleaning tapping equipment is provided with
Delivery pipe is cleaned, cleaning manual ball valve and drain valve are provided on the cleaning delivery pipe.
Preferably, the vacuum generating device is provided with multiple vacuum pump sets and controls the vacuum pump set of vacuum pump set
Control cabinet.
Preferably, the hot water circulating device is provided with water tank, electric heater is provided in the water tank, it is described
Intake pump is additionally provided on water tank, the feeding device is provided with head tank, and liquid feeding pump is provided on the head tank, described
Liquid feeding pump is connected on the material-heat-exchanging device by pipeline.
Compared with prior art, the benificial effect of the utility model is to by the various pieces of low-temperature vacuum thickener group,
Effectively the moisture content in fruit juice is evaporated, enlivens moisture by evaporating corresponding sports contained in material under high vacuum state
Son generates vaporized state under the action of high vacuum and continues to be taken away by vacuum, and passes through fragrance recyclable device outer shell layer
The effect of the ultralow temperature cooling water of the inside cools down the gas that vacuum strength band comes, the cooling when gas by extreme cold
When water, liquid can be converted by gas rapidly, thus principle rapidly converts " fragrance " to the principle of fragrance liquid.It is fragrant
Smart recycling can carries out cooling recycling to xiang semen, to effectively raise the utilization rate of material, improves agricultural product added value, keeps away
Exempt from byproduct to be largely lost, cause the great wasting of resources and environmental pollution.The utility model structure novel, intelligence degree
High, reliable for operation, energy saving, operation and maintenance and its conveniently.
Detailed description of the invention:
The present invention will be further described with reference to the accompanying drawing.
Fig. 1 is the general assembly drawing of the utility model.
Fig. 2 is the structural schematic diagram of material-heat-exchanging device.
Fig. 3 is the A-A cross-sectional view of Fig. 2.
Fig. 4 is the main view of evaporation concentration device.
Fig. 5 is the left view of evaporation concentration device.
Fig. 6 is the structural schematic diagram of distributing device.
Fig. 7 is the structural schematic diagram of foam-blocker.
Fig. 8 is the structural schematic diagram of the cooling recyclable device of fragrance.
Fig. 9 is the structural schematic diagram of concentrate recyclable device.
Figure 10 is the structural schematic diagram of vacuum generating device.
Figure 11 is the structural schematic diagram of hot water circulating device.
Figure 12 is the structural schematic diagram of feeding device.
Specific embodiment:
The present invention will be described in detail below with reference to the accompanying drawings and specific embodiments:
As shown in Figure 1, unit is concentrated in a kind of ultra low temperature vacuum, it is provided with low-temperature vacuum thickener group, the vacuum concentration
Unit is provided with feeding device 1, and material-heat-exchanging device 2 is connected on the feeding device 1, is connected on the material-heat-exchanging device 2
It is connected to evaporation concentration device 3, the material-heat-exchanging device 2 passes through horizontal positioned lateral material with the evaporation concentration device 3
Connecting tube 4 connects together, and connects on the evaporation concentration device 3 and aromatic cools back receiving apparatus 5, the evaporation concentration device
3 are connected together with the cooling recyclable device 5 of fragrance by the first cooling tubulation 6, second on the cooling recyclable device 5 of the fragrance
Group is connected with box chilled water unit 7, is also connected with vacuum generating device 8, the fragrance on the cooling recyclable device 5 of the fragrance
It is connected together between cooling recyclable device 5 and the vacuum generating device 8 by vacuum connection tube 11, the material-heat-exchanging dress
It sets and is additionally provided with hot water circulating device 9 on 2, the bottom of the evaporation concentration device 3 is provided with concentrate recyclable device 10.
As shown in Figures 2 and 3, the material-heat-exchanging device 2 is provided with the heat exchange of inner hollow and structure cylindrical
Shell 201, the upper and lower ends of the heat exchange shell 201 are respectively arranged with upper conical connecting plate 202 and inferior pyramidal connecting plate
203, connected between the upper conical connecting plate 202 and inferior pyramidal connecting plate 203 and heat exchange shell 201 by tube sheet flange 204
It is connected to together, multiple material-heat-exchanging pipes 205 is provided between the tube sheet flange 204, the side of the heat exchange shell 201 is also
It is provided with water inlet 206 and water outlet 207, is provided with lateral material connecting tube 4 on the upper conical connecting plate 202.
As shown in Figure 4 and Figure 5, the evaporation concentration device 3 is provided with the evaporation and concentration tank body 301 of inner hollow, described
The outside for being concentrated by evaporation tank body 301 is provided with multiple stiffener plates 302, and the outside for being concentrated by evaporation tank body 301 is additionally provided with
Multiple CIP Butterworth Hatch 303, the outer upper for being concentrated by evaporation tank body 301 are additionally provided with material feed inlet 304, the transverse direction
Material connecting tube 4 is connected on the material feed inlet 304, and the evaporation and concentration tank body 301 is internally provided with oblique material
Pipe 305, the oblique materail tube 305 are connected on the material feed inlet 304, the interior subordinate for being concentrated by evaporation tank body 301
Side is additionally provided with distributing device 306, and the inside for being concentrated by evaporation tank body 301 is also evenly equipped with multiple foam-blockers 307.
As shown in Figure 6 and Figure 7, the stepped structure of the distributing device 306, the distributing device 306 is by multiple in cone
The drapery panel of structure is welded to each other, the 307 semicircular in shape structure of foam-blocker, is provided on the foam-blocker 307 multiple
Flutter foam hole 308.
It is returned as shown in figure 8, the cooling recyclable device 5 of the fragrance is provided with essence recycling can 501 and is installed on the essence
The first cooling device 502, the second cooling device 503 in closed cans 501, first cooling device 502 and the second cooling device
503 place and are parallel to each other vertically, in first cooling device 502 and the second cooling device 503 be internally provided with it is multiple
Cooling tubulation 504, the bottom of the cooling tubulation 504 are connected together by bottom coohng tubulation, first cooling device
502 outer upper is provided with cooling water apopore 505, and the outer upper of second cooling device 503 is provided with cooling water
Inlet opening 506, the cooling water apopore 505 and cooling water inlet opening 506 are connected respectively to the box chilled water unit 7
On.
Floating ball type liquid level sensor 507, the bottom of the essence recycling can 501 are provided in the essence recycling can 501
It is provided with essence discharge port 508, essence discharging butterfly valve 509, the essence discharging butterfly valve are provided on the essence discharge port 508
Discharging centrifugal pump 510 is also connected on 509.
As shown in figure 9, the concentrate recyclable device 10 is provided with concentrate draw-off pump 1001, the concentrate draw-off pump
1001 feed inlet is connected to the bottom of the evaporation concentration device 3, the concentrate draw-off pump by concentrate pipeline 1002
1001 discharge port is provided with online pol detector 1003, and it is pneumatic to be additionally provided with threeway on the online pol detector 1003
Valve 1004, the threeway pneumatic operated valve 1004 are also connected respectively to concentrate storage tank 1005 and material-heat-exchanging device 2 by pipeline
On.
Cleaning tapping equipment is also connected on the concentrate pipeline 1002, the cleaning tapping equipment is provided with cleaning row
Pipe 1006 is put, cleaning manual ball valve 1007 and drain valve 1008 are provided on the cleaning delivery pipe 1006.
As shown in Figure 10, the vacuum generating device 8 is provided with multiple vacuum pump sets 801 and control vacuum pump set 801
Vacuum pump set control cabinet 802.
As is illustrated by figs. 11 and 12, the hot water circulating device 9 is provided with water tank 901, the inner setting of the water tank 901
There is electric heater 902, intake pump 903 is additionally provided on the water tank 901, the feeding device 1 is provided with head tank 101,
Liquid feeding pump 102 is provided on the head tank 101, the liquid feeding pump 102 is connected to the material-heat-exchanging device 2 by pipeline
On.
Before use, starting vacuum generating device 8 first, multiple vacuum pump sets are started by vacuum pump set control cabinet 802
801, since vacuum generating device 8 is connected on the cooling recyclable device 5 of fragrance by vacuum connection tube 11, and fragrance cools back
Receiving apparatus 5 is connected on evaporation concentration device 3 by the first cooling tubulation 6, cooling to fragrance by vacuum generating device 8 in this way
Recyclable device 5 and evaporation concentration device 3 carry out vacuum pumping, at the cooling recyclable device 5 of the fragrance made and evaporation concentration device 3
In high vacuum state.
In use, raw material to be concentrated is placed into head tank 101 first, then starts liquid feeding pump 102, pass through feed liquor
Pump 102 extracts the raw material in head tank 101, and the material-heat-exchanging pipe 205 of material-heat-exchanging device 2 is sent to by pipeline
In, and raw material is sent to by material-heat-exchanging pipe 205 and material connecting tube 4 and is concentrated by evaporation in tank body 301, while starting hot water and following
Intake pump 903 on loop device 9, by intake pump 903 by the hot water in water tank 901 from water inlet on heat exchange shell 201
206 throw into, and flow out from water outlet 207, while flowing into water tank 901, due to being provided in heat exchange shell 201
Material-heat-exchanging pipe 205, such material are up moved from the bottom of material-heat-exchanging pipe 205, and hot water is from the upper of material-heat-exchanging pipe 205
Portion moves down, and such material can be fully warmed-up, and improves the effect of evaporation, is ready for the production of next step.
When material is after being fully warmed-up of material-heat-exchanging device 2, and transported material to by lateral material connecting tube 4
In oblique materail tube 305, tank body 301 is concentrated by evaporation since oblique materail tube 305 is connected to from the top for being concentrated by evaporation tank body 301
Lower part, such material will flow to the bottom of oblique materail tube 305 along oblique materail tube 305, and oblique materail tube 305
Lower exit is provided with distributing device 306, and such material will splash distributing device 306, due to the stepped structure of distributing device 306,
Material will be in high vacuum state due to being concentrated by evaporation tank body 301 on uniform cloth to distributing device 306 in this way, uniform in this way
The material of distribution just will receive sufficient rapid concentration evaporation, be constantly in high vacuum state due to being concentrated by evaporation in tank body 301,
Partial material can be splashed in being concentrated by evaporation tank body 301 due to pressure, be at this moment arranged in being concentrated by evaporation tank body 301 and multiple flutterred foam
Device 307 is blocked the material of splashing by foam-blocker 307, is prevented the material to splash to be extracted and is concentrated by evaporation tank body 301, in order to
Multiple foam-blockers 307 are intersected and are placed by the service efficiency for improving foam-blocker 307, to improve the use effect of foam-blocker 307
Rate.
When material be concentrated by evaporation tank body 301 be sufficiently concentrated by evaporation when, be concentrated by evaporation the concentrate meeting of formation
It trickles to the bottom for being concentrated by evaporation tank body 301, at this moment concentrate draw-off pump 1001 can extract concentrate, and what is extracted is dense
Contracting liquid first passes around the detection of online pol detector 1003, and online pol detector 1003 is in a kind of detection concentrate containing sugar
The detecting instrument of amount, solid content, by sugar content, the setting value of solid content in detection concentrate, so that it is determined that
Whether concentrate reaches the requirement of setting, if the sugar content of concentrate, the setting value of solid content meet the standard of setting
It is worth, illustrates that concentrate is qualified, at this moment system automatic switching three-way pneumatic operated valve 1004, will be concentrated by threeway pneumatic operated valve 1004
Liquid is transported to concentrate storage tank 1005, if the sugar content of concentrate does not meet the requirement of setting value, illustrates the water in material
Divide evaporation capacity not enough, then threeway pneumatic operated valve 1004 does not execute any movement at this time, the former movement of execution conveys material to heat exchange
In device 2 and evaporation and concentration tank body 301, normally it is concentrated by evaporation, until the standard value that concentrate reaches setting can be automatic
Discharging, simultaneity factor start the realization of feeding device 1 automatic feeding automatically and act and (repeat original charging movement), so certainly
It moves, is continuous, reruning.
The material in tank body 301 is concentrated by evaporation in evaporating concentration process, as the evaporation of moisture can volatilize largely
Aroma substance, this aroma substance are exactly the natural essence contained in fruit juice, and aroma substance is cooling as moisture enters fragrance
In recyclable device 5, and automatically into 501 essence recycling cans, box chilled water unit 7 starts work automatically before this
Make, the cooling recyclable device 5 of fragrance has been provided with the fragrance (secondary steam being namely evaporated) by gaseous state by gaseous state at this time
Change the process of liquefied of being converted to, by the cooling water pump on box chilled water unit 7 by cooling water from the second cooling device 503
Cooling water inlet opening 506 throw into, and typed it out from cooling water apopore 505, cooling water will in cooling tubulation 504 into
The quick continuous coo1ing of row, and the temperature that fragrance (gaseous state) substance will be cooled water on the inside of cooling 504 tubulation of tubulation is anti-
Difference effect and the function of leading to be converted into liquid by gaseous state is realized, aroma substance will be cooled water condensation, to form fragrance
Condensate liquid, and fall in essence recycling can 501, since the bottom of the essence recycling can 501 is provided with essence discharge port 508,
And it is provided with floating ball type liquid level sensor 507 in essence recycling can 501, is provided with essence on the essence discharge port 508
Discharge butterfly valve 509, is also connected with discharging centrifugal pump 510 on the essence discharging butterfly valve 509, is sensed in this way by floating ball type liquid level
After device 507 detects the numerical value that the liquid level of fragrance condensate liquid reaches setting, essence discharging butterfly valve 509 is opened, and start discharging
Centrifugal pump 510, by discharging in the storage container set that centrifugal pump 510 conveys fragrance condensate liquid.
When equipment needs to process various materials, it just may require that and evaporation concentration device 3 cleaned, it at this moment will be clear
Washing lotion conveys from CIP Butterworth Hatch 303, and is arranged by the remaining ejected wash water that cleaning manual ball valve 1007 generates cleaning
It goes out, in food and medicine trade, CIP is meant that the meaning of on-line cleaning.
It is emphasized that: the above is only the preferred embodiment of the present utility model, not appoints to the utility model
What formal limitation, any simple modification made by the above technical examples according to the technical essence of the present invention, etc.
With variation and modification, it is still within the scope of the technical solutions of the present invention.
Claims (10)
1. a kind of low-temperature vacuum thickener group, is provided with low-temperature vacuum thickener group, it is characterised in that: the vacuum concentration unit
It is provided with feeding device (1), is connected with material-heat-exchanging device (2) on the feeding device (1), the material-heat-exchanging device (2)
On be connected with evaporation concentration device (3), the material-heat-exchanging device (2) and the evaporation concentration device (3) pass through horizontal positioned
Lateral material connecting tube (4) connect together, connected on the evaporation concentration device (3) it is aromatic cool back receiving apparatus (5),
The evaporation concentration device (3) is connected together with fragrance cooling recyclable device (5) by first cooling tubulation (6), the perfume (or spice)
It is connected on air cooling recyclable device (5) box chilled water unit (7), the fragrance is also connected on cooling recyclable device (5)
Vacuum generating device (8) passes through bonding in vacuum between the fragrance cooling recyclable device (5) and the vacuum generating device (8)
Pipe (11) connects together, and is additionally provided with hot water circulating device (9) on the material-heat-exchanging device (2), the evaporation and concentration dress
The bottom for setting (3) is provided with concentrate recyclable device (10).
2. low-temperature vacuum thickener group according to claim 1, it is characterised in that: material-heat-exchanging device (2) setting
There is the heat exchange shell (201) of inner hollow and structure cylindrical, the upper and lower ends of the heat exchange shell (201) are set respectively
It is equipped with upper conical connecting plate (202) and inferior pyramidal connecting plate (203), the upper conical connecting plate (202) and inferior pyramidal connecting plate
(203) it is connected together between heat exchange shell (201) by tube sheet flange (204), is set between the tube sheet flange (204)
Multiple material-heat-exchanging pipes (205) are equipped with, the side of the heat exchange shell (201) is additionally provided with water inlet (206) and water outlet
(207), lateral material connecting tube (4) is provided on the upper conical connecting plate (202).
3. low-temperature vacuum thickener group according to claim 1, it is characterised in that: evaporation concentration device (3) setting
There is the evaporation and concentration tank body (301) of inner hollow, is provided with multiple stiffener plates on the outside of the evaporation and concentration tank body (301)
(302), multiple CIP Butterworth Hatch (303), the evaporation and concentration tank body are additionally provided on the outside of the evaporation and concentration tank body (301)
(301) outer upper is additionally provided with material feed inlet (304), it is described transverse direction material connecting tube (4) be connected to the material into
It is described to be concentrated by evaporation being internally provided with oblique materail tube (305) for tank body (301), the oblique materail tube in material mouth (304)
(305) it is connected on the material feed inlet (304), the lower inside for being concentrated by evaporation tank body (301) is additionally provided with cloth
Device (306), the inside for being concentrated by evaporation tank body (301) are also evenly equipped with multiple foam-blockers (307).
4. low-temperature vacuum thickener group according to claim 3, it is characterised in that: the distributing device (306) is stepped
Structure, the distributing device (306) are welded to each other by multiple drapery panels in conical structure, and the foam-blocker (307) is in
Semicircular structure is provided on the foam-blocker (307) and multiple flutters foam hole (308).
5. low-temperature vacuum thickener group according to claim 1, it is characterised in that: the fragrance is cooling recyclable device (5)
It is provided with essence recycling can (501) and the first cooling device (502) being installed on the essence recycling can (501), second cold
But device (503), first cooling device (502) and the second cooling device (503) are placed and are parallel to each other vertically, and described
(503) is internally provided with multiple cooling tubulations (504), the cooling column in one cooling device (502) and the second cooling device
The bottom of pipe (504) is connected together by bottom coohng tubulation, and the outer upper of first cooling device (502) is provided with
The outer upper of cooling water apopore (505), second cooling device (503) is provided with cooling water inlet opening (506), described
Cooling water apopore (505) and cooling water inlet opening (506) are connected respectively on the box chilled water unit (7).
6. low-temperature vacuum thickener group according to claim 5, it is characterised in that: the essence recycling can (501) is inner to be set
It is equipped with floating ball type liquid level sensor (507), the bottom of the essence recycling can (501) is provided with essence discharge port (508), described
It is provided with essence discharging butterfly valve (509) on essence discharge port (508), is also connected with discharging on essence discharging butterfly valve (509)
Centrifugal pump (510).
7. low-temperature vacuum thickener group according to claim 1, it is characterised in that: the concentrate recyclable device (10) sets
It is equipped with concentrate draw-off pump (1001), the feed inlet of the concentrate draw-off pump (1001) is connected by concentrate pipeline (1002)
To the bottom of the evaporation concentration device (3), the discharge port of the concentrate draw-off pump (1001) is provided with online pol detection
Instrument (1003) is additionally provided with threeway pneumatic operated valve (1004) on the online pol detector (1003), the threeway pneumatic operated valve
(1004) it is also connected respectively on concentrate storage tank (1005) and material-heat-exchanging device (2) by pipeline.
8. low-temperature vacuum thickener group according to claim 7, it is characterised in that: on the concentrate pipeline (1002) also
It is connected with cleaning tapping equipment, the cleaning tapping equipment is provided with cleaning delivery pipe (1006), the cleaning delivery pipe
(1006) cleaning manual ball valve (1007) and drain valve (1008) are provided on.
9. low-temperature vacuum thickener group according to claim 1, it is characterised in that: vacuum generating device (8) setting
There are multiple vacuum pump sets (801) and controls the vacuum pump set control cabinet (802) of vacuum pump set (801).
10. low-temperature vacuum thickener group according to claim 1, it is characterised in that: hot water circulating device (9) setting
Have water tank (901), the water tank (901) is inner to be provided with electric heater (902), is additionally provided on the water tank (901)
Intake pump (903), the feeding device (1) are provided with head tank (101), are provided with liquid feeding pump on the head tank (101)
(102), the liquid feeding pump (102) is connected on the material-heat-exchanging device (2) by pipeline.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820938697.0U CN208465201U (en) | 2018-06-19 | 2018-06-19 | A kind of low-temperature vacuum thickener group |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201820938697.0U CN208465201U (en) | 2018-06-19 | 2018-06-19 | A kind of low-temperature vacuum thickener group |
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| CN208465201U true CN208465201U (en) | 2019-02-05 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108525332A (en) * | 2018-06-19 | 2018-09-14 | 艾得客实业（湖北）有限公司 | A kind of low-temperature vacuum thickener group |
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2018
- 2018-06-19 CN CN201820938697.0U patent/CN208465201U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108525332A (en) * | 2018-06-19 | 2018-09-14 | 艾得客实业（湖北）有限公司 | A kind of low-temperature vacuum thickener group |
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