CN206196877U - A kind of fruit-juice concentration systems - Google Patents
A kind of fruit-juice concentration systems Download PDFInfo
- Publication number
- CN206196877U CN206196877U CN201621064761.4U CN201621064761U CN206196877U CN 206196877 U CN206196877 U CN 206196877U CN 201621064761 U CN201621064761 U CN 201621064761U CN 206196877 U CN206196877 U CN 206196877U
- Authority
- CN
- China
- Prior art keywords
- film
- concentration
- main frame
- pump
- liquid
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model discloses a kind of fruit-juice concentration systems, including original fluid container, pretreatment charging pump, preprocessor, intermediate storage tank, film concentration booster pump, film concentration cycles pump, film concentration main frame, cleaning pump, purge tank, filtrate tanks, dope storage tank, pressure gauge, thermometer, pressure sensor, temperature sensor, turbine flowmeter, electric control valve and switch board after pressure gauge, film before film, the subsystem such as each part correspondence connection forms pretreatment, concentration, cleans, automatically controls.The utility model is concentrated using film concentration main frame to pretreated fruit juice, and good stability, efficiency high is not easily blocked；Film concentration process is carried out only using pressure as driving force at normal temperatures, is not required to heating, does not consume steam, and operating cost is only hot concentration technique 20% 30%, while avoiding fruit juice from being gelatinized；Using on-line cleaning technique, the concentration membrane component that equipment is included is not required to dismounting, can direct-on-line cleaning and sterilizing.
Description
Technical field
The utility model is related to a kind of juice production equipment, more particularly to that a kind of fruit juice loss of aroma is small, energy consumption is low is new
Type concentration of juices system.
Background technology
Fruit juice is such as to be squeezed by physical method as raw material with fruit, be centrifuged, extracting the juice product for obtaining, usually
Refer to pure juice or 100% fruit juice.In order to improve taste of juice, it is the production necessary program of fruit juice that concentration is carried out to fruit juice.
At present, concentration of juices technique mainly has vacuum concentration, evaporation and concentration etc..Vacuum concentration due to entering under vacuum conditions
Row concentration, the fragrance matter loss in fruit is very big；It is concentrated by evaporation temperature in use high, paste easily occurs in fruit juice long-time heating
The scenes such as change, color burn, product quality is poor.In addition, being either concentrated in vacuo or being concentrated by evaporation, all needed in concentration process
To be heated by steam, high energy consumption.
Utility model content
The purpose of this utility model be that provide that a kind of fruit juice loss of aroma is small in order to solve the above problems, fruit juice not
Can be gelatinized, the fruit-juice concentration systems that energy consumption is low.
The utility model is achieved through the following technical solutions above-mentioned purpose：
A kind of fruit-juice concentration systems, including original fluid container, pretreatment charging pump, preprocessor, intermediate storage tank, film concentration
Pressure gauge, film before booster pump, film concentration cycles pump, film concentration main frame, cleaning pump, purge tank, filtrate tanks, dope storage tank, film
Pressure gauge, thermometer, pressure sensor, temperature sensor, turbine flowmeter, electric control valve and switch board, the stoste afterwards
The liquid outlet of filling is connected by the pretreatment charging pump with the liquid inlet of the preprocessor, the recovered liquid of the preprocessor
Export the liquid inlet filled with the stoste to be connected, the material liquid outlet of the preprocessor connects with the liquid inlet of the intermediate storage tank
Connect, the liquid outlet of the intermediate storage tank passes sequentially through the film concentration booster pump, the film concentration cycles pump and concentrated with the film
The liquid inlet connection of main frame, the filtrate (liquid of the film concentration main frame is connected with the liquid inlet of the filtrate tanks, and the film is dense
The material liquid outlet of contracting main frame is connected with the liquid inlet of the dope storage tank and the liquid inlet of the purge tank respectively, the purge tank
Liquid outlet be connected by the liquid inlet that the cleaning pump and the film concentrate main frame, pressure gauge is installed on the film before the film
On the pipeline of the liquid inlet side for concentrating main frame, pressure gauge, the thermometer, the pressure sensor, the temperature after the film
Sensor, the turbine flowmeter and the electric control valve be respectively arranged in the film concentration main frame and the dope storage tank it
Between pipeline on, the signal output part of the pressure sensor, the signal output part of the temperature sensor and the turbine flow
Signal input part of the signal output part of gauge respectively with the switch board is connected, the control input of the pretreatment charging pump
End, the film concentrate control signal, the control signal of the film concentration cycles pump, the control of the cleaning pump of booster pump
Control output end of the control signal of input and the electric control valve respectively with the switch board is connected.
For the ease of controlling the on off state between each part manually, between the original fluid container and the pretreatment charging pump
Pipeline on pretreatment liquid feed valve is installed, be provided with the pipeline between the preprocessor and the original fluid container and pre-processed back
Stream valve, is provided with pretreatment and considers liquid valve, the film concentration cycles on the pipeline between the preprocessor and the intermediate storage tank
Concentration liquid feed valve is installed, between the cleaning pump and film concentration main frame on the pipeline between pump and film concentration main frame
Pipeline on cleaning liquid feed valve is installed, cleaning backflow is installed on the pipeline between the film concentration main frame and the purge tank
Valve, filtrate liquid feed valve is provided with the pipeline between the film concentration main frame and the filtrate tanks.
Preferably, the preprocessor is membrane filtration main frame, the material liquid outlet of the preprocessor is filled with the stoste
Liquid inlet connection and the connecting pipe on be provided with preprocessor cleaning return valve；The filtrate (liquid of the film concentration main frame is also
It is connected with blow-off line and the pipeline and blowoff valve is installed.
Preferably, respectively by the connection of 304 stainless steel pipes between the liquid in-out mouthful of each part, each part with it is described
The connection of fast-assembling chuck is respectively adopted between 304 stainless steel pipes, the wire between the switch board and other parts is respectively adopted
Shielding line.
Preferably, the concentration film that the film concentration main frame is used is high temperature resistant rolled cylindrical multilayer complex films, its diameter
It is 203 millimeters, length is 1016 millimeters, and below the dalton of molecular cut off 150, operating pressure is 1.0-3.5MPa, concentration temperature
It is 15-35 DEG C to spend, and cleaning temperature is 35 DEG C -45 DEG C, and the concentration film of crossing is the concentration film comprising polyacrylonitrile-radical.
The beneficial effects of the utility model are：
The utility model is concentrated using film concentration main frame to pretreated fruit juice, and good stability, efficiency high is difficult
Block；Film concentration process is carried out only using pressure as driving force at normal temperatures, is not required to heating, does not consume steam, and operating cost is only
It is hot concentration technique 20%-30%, while avoiding fruit juice from being gelatinized；Using on-line cleaning technique, the concentration membrane element that equipment is included
Part is not required to dismounting, can direct-on-line cleaning and sterilizing；Using membrane filtration main frame as preprocessor, its retention precision is higher, can have
Effect trapped particles impurity；Whole equipment is easy to clean, can Reusability, with low cost, auto-manual overall-in-one control schema, system is steady
Qualitative high, fault rate is low；Use concentration retaining molecular weight for 150 dalton below, energy effectively catching fruit juice in it is effective
Composition, can directly discharge through water；Directly it is divided into inspissated juice (i.e. feed liquid or dope) after film concentration main frame and passes through water (i.e.
Filtrate), cocnentration factor can control, and can arbitrarily be controlled according to user's specific requirement.
Brief description of the drawings
Fig. 1 is the structural representation of fruit-juice concentration systems described in the utility model.
Specific embodiment
The utility model is described in further detail below in conjunction with the accompanying drawings：
As shown in figure 1, fruit-juice concentration systems described in the utility model include original fluid container 1, pretreatment charging pump 2, pre-
Processor 3, intermediate storage tank 4, film concentration booster pump 6, film concentration cycles pump 7, film concentration main frame 10, cleaning pump 8, purge tank 9, filter
Pressure gauge 27, thermometer 25, pressure sensor 28, temperature sensor after pressure gauge 28, film before liquid storage tank 11, dope storage tank 5, film
26th, turbine flowmeter 24, electric control valve 19 and switch board (not shown), the liquid outlet of stoste filling 1 is by pre-processing feed
Pump 2 is connected with the liquid inlet of preprocessor 3, and the liquid inlet that the recovered liquid outlet of preprocessor 3 fills 1 with stoste is connected, and pre-processes
The material liquid outlet of device 3 fills 1 liquid inlet with stoste respectively and the liquid inlet of intermediate storage tank 4 is connected, the liquid outlet of intermediate storage tank 4 according to
The secondary liquid inlet for concentrating main frame 10 with film by film concentration booster pump 6, film concentration cycles pump 7 is connected, and film concentrates the filter of main frame 10
Liquid outlet be connected with the liquid inlet of filtrate tanks 11, film concentrate main frame 10 material liquid outlet respectively with the liquid inlet of dope storage tank 5
Liquid inlet with purge tank 9 is connected, and the liquid outlet of purge tank 9 is connected by the liquid inlet that cleaning pump 8 concentrates main frame 10 with film, film
Preceding pressure gauge 28 is installed on the pipeline of the liquid inlet side of film concentration main frame 10, pressure gauge 27, thermometer 25, pressure sensing after film
Device 28, temperature sensor 26, turbine flowmeter 24 and electric control valve 19 are respectively arranged in film concentration main frame 10 and dope storage tank 5
Between pipeline on, the signal output part of pressure sensor 28, the signal output part of temperature sensor 26 and turbine flowmeter 24
Signal input part of the signal output part respectively with the switch board be connected, pre-process control signal, the film concentration of charging pump 2
The control signal of booster pump 6, the control signal of film concentration cycles pump 7, the control signal of cleaning pump 8 and electric control valve
Control output end of 19 control signal respectively with the switch board is connected；Pipe between original fluid container 1 and pretreatment charging pump 2
Pretreatment liquid feed valve 13 is installed on road, pretreatment return valve 14 is installed on the pipeline between preprocessor 3 and original fluid container 1,
Pretreatment is installed on the pipeline between preprocessor 3 and intermediate storage tank 4 and considers liquid valve 16, film concentration cycles pump 7 concentrates master with film
Concentration liquid feed valve 17 is installed on the pipeline between machine 10, is provided with the pipeline between cleaning pump 8 and film concentration main frame 10 clear
Wash liquid feed valve 18, cleaning return valve 20 be installed on the pipeline between film concentration main frame 10 and purge tank 9, film concentration main frame 10 with
Filtrate liquid feed valve 22 is installed, preprocessor 3 and stoste fill the pipeline between 1 liquid inlet on the pipeline between filtrate tanks 11
On be provided with preprocessor cleaning return valve 15, film concentration main frame 10 filtrate (liquid be also associated with blow-off line and the pipeline
Blowoff valve 23 is installed.
Preferably, being connected by 304 stainless steel pipes 12 respectively between the liquid in-out mouthful of each part, each part and 304
The connection of fast-assembling chuck (not shown), the wire between the switch board and other parts are respectively adopted between stainless steel pipes 12
Shielding line (not shown) is respectively adopted；The concentration film that film concentration main frame 10 is used is high temperature resistant rolled cylindrical multilayer complex films,
Its a diameter of 203 millimeters, length is 1016 millimeters, and below the dalton of molecular cut off 150, operating pressure is 1.0-3.5MPa,
Thickening temperature is 15-35 DEG C, and cleaning temperature is 35 DEG C -45 DEG C, and the concentration film of crossing is the concentration film comprising polyacrylonitrile-radical.
In said structure, 304 stainless steel pipes 12 between the liquid in-out mouthful of each part, some pipelines are to partly overlap,
So employing the structure that supervisor is further divided into branch pipe；Above-mentioned each part is conventional components of the prior art, the utility model
Innovation be by various parts carry out organic combination, optimization connection, formed a new system；Intermediate storage tank 4 and dope are stored up
Tank 5 can be independent tank body, or same tank body, and two kinds of work(are realized using two kinds of different operating times of tank body
Energy.
With reference to Fig. 1, when the system is run, the flow direction of raw juice is：The raw juice that stoste is filled in 1 is supplied by pretreatment
Material pump 2 is pre-processed after being pressurized into preprocessor 3, and the present embodiment is filtration treatment, during the qualified feed liquid after filtering enters
Between storage tank 4, unqualified liquid is back to stoste and fills 1, and feed liquid in intermediate storage tank 4 is through film concentration booster pump 6, film concentration cycles pump
Enter film concentration main frame 10 after 7 superchargings to be concentrated, the dope (i.e. feed liquid) after concentration enters dope storage tank 5, and filtrate (passes through
Water) enter filtrate tanks 11, or be used to clean film concentration main frame 10 into purge tank 9.
Above-described embodiment is preferred embodiment of the present utility model, is not the limit to technical solutions of the utility model
System, as long as the technical scheme that can be realized on the basis of above-described embodiment without creative work, is regarded as falling into
In the rights protection scope of the utility model patent.
Claims (5)
1. a kind of fruit-juice concentration systems, it is characterised in that：Including original fluid container, pretreatment charging pump, preprocessor, middle storage
Before tank, film concentration booster pump, film concentration cycles pump, film concentration main frame, cleaning pump, purge tank, filtrate tanks, dope storage tank, film
Pressure gauge, thermometer, pressure sensor, temperature sensor, turbine flowmeter, electric control valve and switch board after pressure gauge, film,
The liquid outlet that the stoste is filled is connected by the pretreatment charging pump with the liquid inlet of the preprocessor, the preprocessor
Recovered liquid outlet with the stoste fill liquid inlet be connected, the material liquid outlet of the preprocessor enters with the intermediate storage tank
Liquid mouthful connection, the liquid outlet of the intermediate storage tank pass sequentially through the film concentration booster pump, the film concentration cycles pump with it is described
The liquid inlet connection of film concentration main frame, the filtrate (liquid of the film concentration main frame is connected with the liquid inlet of the filtrate tanks, institute
The material liquid outlet for stating film concentration main frame is connected with the liquid inlet of the dope storage tank and the liquid inlet of the purge tank respectively, described
The liquid outlet of purge tank is connected by the liquid inlet that the cleaning pump concentrates main frame with the film, and pressure gauge is installed on before the film
On the pipeline of the liquid inlet side of the film concentration main frame, pressure gauge, the thermometer, the pressure sensor, institute after the film
State temperature sensor, the turbine flowmeter and the electric control valve and be respectively arranged in film concentration main frame and the dope
On pipeline between storage tank, the signal output part of the pressure sensor, the signal output part of the temperature sensor and described
Signal input part of the signal output part of turbine flowmeter respectively with the switch board is connected, the control of the pretreatment charging pump
Input, the film concentration control signal of booster pump, the control signal of the film concentration cycles pump, the cleaning pump
Control output end of the control signal of control signal and the electric control valve respectively with the switch board is connected.
2. fruit-juice concentration systems according to claim 1, it is characterised in that：The original fluid container is supplied with the pretreatment
Pretreatment liquid feed valve is installed on pipeline between material pump, is provided with the pipeline between the preprocessor and the original fluid container
Pretreatment return valve, is provided with pretreatment and considers liquid valve, the film on the pipeline between the preprocessor and the intermediate storage tank
Concentration liquid feed valve is installed on pipeline between concentration cycles pump and film concentration main frame, the cleaning pump is concentrated with the film
Cleaning liquid feed valve is installed on the pipeline between main frame, is provided with the pipeline between the film concentration main frame and the purge tank
Cleaning return valve, filtrate liquid feed valve is provided with the pipeline between the film concentration main frame and the filtrate tanks.
3. fruit-juice concentration systems according to claim 2, it is characterised in that：The preprocessor is membrane filtration master
Machine, the liquid inlet that the material liquid outlet of the preprocessor is filled with the stoste is connected and is provided with preprocessor on the connecting pipe
Cleaning return valve；The filtrate (liquid of the film concentration main frame is also associated with being provided with blowoff valve on blow-off line and the pipeline.
4. fruit-juice concentration systems according to claim 1,2 or 3, it is characterised in that：The liquid in-out mouth of each part
Between respectively by 304 stainless steel pipes connect, be respectively adopted between each part and 304 stainless steel pipes fast-assembling chuck company
Connect, the wire between the switch board and other parts is respectively adopted shielding line.
5. fruit-juice concentration systems according to claim 1,2 or 3, it is characterised in that：The film concentration main frame is used
Concentration film be high temperature resistant rolled cylindrical multilayer complex films, its a diameter of 203 millimeters, length be 1016 millimeters, molecular cut off
Below 150 dalton, operating pressure is 1.0-3.5MPa, and thickening temperature is 15-35 DEG C, and cleaning temperature is 35 DEG C -45 DEG C, described
Concentration film is the concentration film comprising polyacrylonitrile-radical.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621064761.4U CN206196877U (en) | 2016-09-20 | 2016-09-20 | A kind of fruit-juice concentration systems |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621064761.4U CN206196877U (en) | 2016-09-20 | 2016-09-20 | A kind of fruit-juice concentration systems |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206196877U true CN206196877U (en) | 2017-05-31 |
Family
ID=58761815
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621064761.4U Active CN206196877U (en) | 2016-09-20 | 2016-09-20 | A kind of fruit-juice concentration systems |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206196877U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107223826A (en) * | 2017-06-27 | 2017-10-03 | 杭州瑞纳膜工程有限公司 | A kind of Rosa roxburghi Juice film concentration technology and concentration systems |
| CN110506816A (en) * | 2018-05-22 | 2019-11-29 | 湖南佛子岭茶业发展有限公司 | A kind of preparation method of the instant dark tea based on low temperature concentration technique containing cream |
| CN113975968A (en) * | 2021-11-29 | 2022-01-28 | 四川和诚过滤科技集团有限公司 | Membrane concentration ethanol recovery equipment for industrial hemp alcohol extract |
-
2016
- 2016-09-20 CN CN201621064761.4U patent/CN206196877U/en active Active
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107223826A (en) * | 2017-06-27 | 2017-10-03 | 杭州瑞纳膜工程有限公司 | A kind of Rosa roxburghi Juice film concentration technology and concentration systems |
| CN110506816A (en) * | 2018-05-22 | 2019-11-29 | 湖南佛子岭茶业发展有限公司 | A kind of preparation method of the instant dark tea based on low temperature concentration technique containing cream |
| CN113975968A (en) * | 2021-11-29 | 2022-01-28 | 四川和诚过滤科技集团有限公司 | Membrane concentration ethanol recovery equipment for industrial hemp alcohol extract |
| CN113975968B (en) * | 2021-11-29 | 2024-02-06 | 四川和诚过滤科技集团有限公司 | Membrane concentration ethanol recovery equipment for industrial cannabis ethanol extract |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN206196877U (en) | A kind of fruit-juice concentration systems | |
| CN201163993Y (en) | Double-loop perfuming, charging and feeding system | |
| CN212640033U (en) | Membrane system for cleaning fluid regeneration of dairy | |
| CN103651049A (en) | Simple drop irrigation device with two-stage filtration | |
| CN202762319U (en) | Ultrafiltration membrane cleaning system | |
| CN204752277U (en) | Hydrogen is led duolite and is concentrated regenerating unit | |
| CN206109366U (en) | Novel fruit wine clarification filtration system | |
| CN206188458U (en) | Impulse -type reverse osmosis membrane off -line cleaning device | |
| CN206020232U (en) | A kind of purifier test system | |
| EP0735916B1 (en) | Process and device for concentrating solid/liquid mixtures by means of diaphragm technology | |
| CN210303550U (en) | Intelligent blending system for ethanol for cannabinoid extraction | |
| CN212236751U (en) | Novel vitamin B12 midbody processing device | |
| CN207435103U (en) | A kind of animal protein wastewater membrane filtration system apparatus | |
| CN207126188U (en) | A kind of air-source water heater filter | |
| CN203803392U (en) | Integrated device for off-line cleaning and detecting of 8-inch reverse osmosis membrane elements | |
| CN207266828U (en) | The membrane equipment of the reinforced ultrafiltration membrane of high throughput | |
| CN207429839U (en) | A kind of ferment clarification filtration equipment | |
| CN102626569B (en) | Filtering process and filtering system for use in preparation of injection liquid medicament | |
| CN202297430U (en) | Plasma protein ultrafiltration membrane device | |
| CN206940847U (en) | A kind of clarification filtration equipment of mature vinegar | |
| CN206173124U (en) | Drinking water treatment equipment with cavity ultrafiltration device | |
| CN208740030U (en) | A kind of room temperature concentration systems equipment of dark green tea extracting solution | |
| CN205095660U (en) | Receive strain, reverse osmosis membrane's cleaning system | |
| CN206275098U (en) | A kind of concentration of juices system | |
| CN204502814U (en) | A kind of tubular ultra-filtration membrane off-line cleaning equipment |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |