CN205288109U - High fructose syrup production is with organic high temperature membrane filter equipment - Google Patents
High fructose syrup production is with organic high temperature membrane filter equipment Download PDFInfo
- Publication number
- CN205288109U CN205288109U CN201620062829.9U CN201620062829U CN205288109U CN 205288109 U CN205288109 U CN 205288109U CN 201620062829 U CN201620062829 U CN 201620062829U CN 205288109 U CN205288109 U CN 205288109U
- Authority
- CN
- China
- Prior art keywords
- filtration unit
- high temperature
- fructose syrup
- organic
- high fructose
- 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 relates to a high fructose syrup production is with organic high temperature membrane filter equipment. Including filter equipment and spray set, wherein, filter equipment is by installing the filter in turn and cross the filter frame between thrust plate and the pressure strip, be provided with high temperature resistant organic micro -filtration membrane on every filter, constituting the straining chamber between the filter, spray set forms for the more than one water pipe directly over lieing in filter equipment, is provided with the mouth that sprays more than two under the water pipe. The device can overcome the filtration membrane cannot resist high temperature who leads to because the high fructose syrup temperature is higher among the prior art, see through the big problem of volume, the utility model discloses the device washes the convenience, can used repeatedly, and it is with low costs.
Description
Technical field
The utility model relates to a kind of high fructose syrup and produces filtration unit, is specially a kind of high fructose syrup and produces with organic high temperature membrane filtration unit.
Background technology
In high fructose syrup production process, after Mashing process, sugar liquid is cooled to 60 DEG C, enter strainer again protein and other insoluble impuritiess of retrogradation in sugar liquid to be filtered away, thus obtain the saccharified liquid of clarification, in filtration procedure, owing to high fructose syrup temperature is higher, conventional strainer filtering membrane non-refractory is big through amount. Scatterer set up usually before filtration by existing filtration unit, is lowered the temperature further by sugar liquid, but one, to set up scatterer and can make sugar liquid production process produces loss, two, after setting up scatterer, add process flow steps, cost is also higher.
Summary of the invention
The purpose of this utility model is exactly the defect for above-mentioned existence and provides a kind of high fructose syrup to produce with organic high temperature membrane filtration unit. This device can overcome in prior art the filtering membrane non-refractory caused because high fructose syrup temperature is higher, through the problem that amount is big, sugar liquid can be lowered the temperature further in filtration procedure, do not need to increase scatterer again, the use of high temperature resistant organic microfiltration membrane also can adapt to certain temperature, and the utility model device rinses conveniently, it is possible to reusing, cost is low.
A kind of high fructose syrup of the present utility model is produced and by organic high temperature membrane filtration unit technical scheme is, comprise filtration unit and spray equipment, wherein, filtration unit is by alternately installing screen plate and filter frame between thrust plate and pressure strip, every block screen plate is provided with high temperature resistant organic microfiltration membrane, between screen plate, forms filter chamber; Spray equipment is positioned at directly over filtration unit, for more than one water pipe forms, is provided with the spray nozzle of two or more immediately below water pipe. 30-40 DEG C of water it is connected with in water pipe.
Sugar liquid entrance is connected with each filter chamber top by pump, and sugar liquid outlet is positioned at thrust plate bottom.
Sugar liquid entrance is connected with pump.
Ball valve and hose nipple are equipped with in sugar liquid exit.
Spray equipment is positioned at 0.5-1m place above filtration unit.
Described high temperature resistant organic microfiltration membrane is polypropylene-base or the organic microfiltration membrane of polysulfones.
It is provided with drip tray immediately below filtration unit, drip tray slant setting, below low one end, it is provided with waste water reclamation interface. Can the waste liquid in remanufacture process and spray equipment produce in time waste water.
A kind of high fructose syrup of the present utility model is produced and by organic useful effect of high temperature membrane filtration unit is: this device can overcome in prior art because of the higher filtering membrane non-refractory caused of high fructose syrup temperature, through the problem that amount is big, sugar liquid can be lowered the temperature further in filtration procedure, do not need to increase scatterer again, the use of high temperature resistant organic microfiltration membrane also can adapt to certain temperature, and the utility model device rinses conveniently, it is possible to reusing, cost is low.
Accompanying drawing illustrates:
Fig. 1 show basic structure schematic diagram of the present utility model.
In figure, 1. sugar liquid entrance, 2. venting port, 3. water pipe, 4. spray nozzle, 5. screen plate, 6. drip tray, 7. waste water reclamation interface, the 8. outlet of sugar liquid, 9. pressure strip, 10. thrust plate, 11. filter frames.
Embodiment:
In order to understand the utility model better, with specific examples, the technical solution of the utility model is described in detail below, but the utility model is not limited thereto.
Embodiment 1
A kind of high fructose syrup is produced with organic high temperature membrane filtration unit, comprise filtration unit and spray equipment, wherein, filtration unit is by alternately installing screen plate 5 and filter frame 11 between thrust plate 10 and pressure strip 9, every block screen plate 5 is provided with high temperature resistant organic microfiltration membrane, between screen plate 5, forms filter chamber; Spray equipment is positioned at directly over filtration unit, for more than one water pipe 3 forms, is provided with the spray nozzle 4 of two or more immediately below water pipe 3. 30-40 DEG C of water it is connected with in water pipe 3. Described high temperature resistant organic microfiltration membrane is polypropylene-base or the organic microfiltration membrane of polysulfones.
Sugar liquid entrance 1 is connected with each filter chamber top by pump, and sugar liquid outlet 8 is positioned at thrust plate 10 bottom.
Sugar liquid entrance 1 is connected with pump.
Sugar liquid exports 8 places and ball valve and hose nipple is housed.
Spray equipment is positioned at 0.5-1m place above filtration unit.
Being provided with drip tray 6 immediately below filtration unit, drip tray 6 slant setting, is provided with waste water reclamation interface 7 below low one end. Can the waste liquid in remanufacture process and spray equipment produce in time waste water.
Claims (6)
1. a high fructose syrup is produced with organic high temperature membrane filtration unit, it is characterized in that, comprise filtration unit and spray equipment, wherein, filtration unit is by alternately installing screen plate and filter frame between thrust plate and pressure strip, every block screen plate is provided with high temperature resistant organic microfiltration membrane, between screen plate, forms filter chamber; Spray equipment is positioned at directly over filtration unit, for more than one water pipe forms, is provided with the spray nozzle of two or more immediately below water pipe.
2. a kind of high fructose syrup according to claim 1 is produced with organic high temperature membrane filtration unit, it is characterised in that, sugar liquid entrance is connected with each filter chamber top by pump, and sugar liquid outlet is positioned at thrust plate bottom.
3. a kind of high fructose syrup according to claim 2 is produced with organic high temperature membrane filtration unit, it is characterised in that, sugar liquid entrance is connected with pump.
4. a kind of high fructose syrup according to claim 2 is produced with organic high temperature membrane filtration unit, it is characterised in that, ball valve and hose nipple are equipped with in sugar liquid exit.
5. a kind of high fructose syrup according to claim 1 is produced with organic high temperature membrane filtration unit, it is characterised in that, spray equipment is positioned at 0.5-1m place above filtration unit.
6. a kind of high fructose syrup according to claim 1 is produced with organic high temperature membrane filtration unit, it is characterised in that, it is provided with drip tray immediately below filtration unit, drip tray slant setting, below low one end, it is provided with waste water reclamation interface.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620062829.9U CN205288109U (en) | 2016-01-22 | 2016-01-22 | High fructose syrup production is with organic high temperature membrane filter equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620062829.9U CN205288109U (en) | 2016-01-22 | 2016-01-22 | High fructose syrup production is with organic high temperature membrane filter equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205288109U true CN205288109U (en) | 2016-06-08 |
Family
ID=56426606
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620062829.9U Active CN205288109U (en) | 2016-01-22 | 2016-01-22 | High fructose syrup production is with organic high temperature membrane filter equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205288109U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106092894A (en) * | 2016-08-23 | 2016-11-09 | 兆光生物工程(邹平)有限公司 | A kind of membrane filtration separation detecting device |
| CN111214956A (en) * | 2020-01-15 | 2020-06-02 | 山东润德生物科技有限公司 | Rotary membrane solid-liquid separation equipment |
-
2016
- 2016-01-22 CN CN201620062829.9U patent/CN205288109U/en active Active
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106092894A (en) * | 2016-08-23 | 2016-11-09 | 兆光生物工程(邹平)有限公司 | A kind of membrane filtration separation detecting device |
| CN106092894B (en) * | 2016-08-23 | 2018-07-13 | 兆光生物工程(邹平)有限公司 | A kind of membrane filtration separation detecting device |
| CN111214956A (en) * | 2020-01-15 | 2020-06-02 | 山东润德生物科技有限公司 | Rotary membrane solid-liquid separation equipment |
| CN111214956B (en) * | 2020-01-15 | 2021-10-08 | 山东润德生物科技有限公司 | Rotary membrane solid-liquid separation equipment |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN205288109U (en) | High fructose syrup production is with organic high temperature membrane filter equipment | |
| CN104147842A (en) | Combined multifunctional filtering device | |
| CN105327621A (en) | End component, hollow fiber membrane module and membrane filter unit | |
| CN204017527U (en) | A kind of composite multi-functional filter | |
| CN208493431U (en) | Mixing wastewater with air backwash automatic cleaning lamination filter | |
| CN207980878U (en) | A kind of external pressure tube-type micropore filter membrane device | |
| CN211920976U (en) | High-precision multilayer ultrafiltration device | |
| CN205127760U (en) | End part, hollow fiber membrane subassembly and membrane filter unit | |
| CN205288117U (en) | Air supporting membrane equipment | |
| CN208990577U (en) | A kind of natural pigment ultrafiltration apparatus | |
| CN208115290U (en) | Tantalum liquid produces dedicated microporous filter | |
| CN206793419U (en) | A kind of general valve group of ultrafiltration apparatus | |
| CN220715027U (en) | Palm oil filter equipment | |
| CN203373333U (en) | Filter device of rhodomyrtus tomentosa wine | |
| CN205603559U (en) | High -efficient deoxygenated water top wine device | |
| CN205295526U (en) | Electroplating production line filter exhaust apparatus | |
| CN209333290U (en) | A kind of core type filter of split type detachable for cleaning | |
| CN208426751U (en) | A kind of nanofiltration accessory device of filtration protein | |
| CN209092797U (en) | Chemical industry filter device | |
| CN214261406U (en) | Automatic cleaning system of ultrafiltration device | |
| CN2892255Y (en) | Static membrance filtering apparatus | |
| CN202170343U (en) | Automatic defecation and ultrafiltration device for virus harvest liquid | |
| CN216572463U (en) | Reverse osmosis membrane element and assembly | |
| CN220907221U (en) | Box type oil remover | |
| CN219399661U (en) | Reverse osmosis membrane |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |