CN206308179U - A kind of concentrated phase water filtering device for starch sugar - Google Patents
A kind of concentrated phase water filtering device for starch sugar Download PDFInfo
- Publication number
- CN206308179U CN206308179U CN201621492136.XU CN201621492136U CN206308179U CN 206308179 U CN206308179 U CN 206308179U CN 201621492136 U CN201621492136 U CN 201621492136U CN 206308179 U CN206308179 U CN 206308179U
- Authority
- CN
- China
- Prior art keywords
- water
- filter
- concentrated
- outlet
- starch sugar
- 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.)
- Expired - Fee Related
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 181
- 229920002472 Starch Polymers 0.000 title claims abstract description 41
- 235000019698 starch Nutrition 0.000 title claims abstract description 41
- 239000008107 starch Substances 0.000 title claims abstract description 41
- 238000001914 filtration Methods 0.000 title claims description 36
- 238000001223 reverse osmosis Methods 0.000 claims abstract description 33
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 29
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 25
- 238000010612 desalination reaction Methods 0.000 claims abstract description 15
- 230000008676 import Effects 0.000 claims abstract description 5
- 230000000694 effects Effects 0.000 claims description 7
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 7
- 239000003795 chemical substances by application Substances 0.000 claims description 6
- 239000000126 substance Substances 0.000 claims description 6
- 238000004140 cleaning Methods 0.000 claims description 5
- 239000010453 quartz Substances 0.000 claims description 5
- 238000005374 membrane filtration Methods 0.000 claims description 3
- 239000003638 chemical reducing agent Substances 0.000 claims description 2
- 238000009298 carbon filtering Methods 0.000 claims 1
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 description 2
- 239000006004 Quartz sand Substances 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000008103 glucose Substances 0.000 description 2
- 235000019534 high fructose corn syrup Nutrition 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 230000003204 osmotic effect Effects 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- 230000003321 amplification Effects 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 239000000084 colloidal system Substances 0.000 description 1
- 235000009508 confectionery Nutrition 0.000 description 1
- 238000000855 fermentation Methods 0.000 description 1
- 230000004151 fermentation Effects 0.000 description 1
- 238000011010 flushing procedure Methods 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000008235 industrial water Substances 0.000 description 1
- 238000001764 infiltration Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 235000020429 malt syrup Nutrition 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 238000003199 nucleic acid amplification method Methods 0.000 description 1
- 229920001542 oligosaccharide Polymers 0.000 description 1
- 150000002482 oligosaccharides Chemical class 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000009287 sand filtration Methods 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/124—Water desalination
- Y02A20/131—Reverse-osmosis
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
- Water Treatment By Sorption (AREA)
Abstract
The utility model discloses a kind of water treatment facilities for starch sugar, including：One water treatment facilities, water treatment facilities includes the raw water box, raw water pump, more medium filter, active carbon filter, cartridge filter, high-pressure pump and the desalination water tank that are sequentially connected；One reverse osmosis concentrated water tank, reverse osmosis concentrated water tank is connected with the concentrated water outlet of reverse osmosis unit；One backwash water pump, the entrance of backwash water pump is connected with the outlet of reverse osmosis concentrated water tank, and the outlet of backwash water pump is connected with more medium filter and active carbon filter respectively；One concentrated water filter, the import of the backwash mouth of more medium filter and the backwash mouth of active carbon filter respectively with concentrated water filter is connected；One concentrated water case, the outlet of concentrated water filter is connected with concentrated water case.The utility model enables to starch sugar water to reach standard by more medium filter, active carbon filter, cartridge filter and reverse osmosis unit, and with the function of being backwashed using concentrated water.
Description
Technical field
The utility model is related to the technical field of water treatment facilities, more particularly to a kind of concentrated phase water filtration for starch sugar
Device.
Background technology
Glucose industry is branch's industry of fermentation industry, and it is with starchiness as raw material, by different degrees of hydrolysis
Deep processing derivative, mainly including glucose (slurry), malt syrup, HFCS and starch sugar kind etc. various oligosaccharide.
Current China's starch sugar annual production is 10,000,000 tons or so, adds starch multi-sugar alcohol, reaches 12,000,000 tons or so, it is estimated that
By the end of the end of the year 2012, only HFCS yield is estimated will be up to 5,000,000 tons or so, and starch candy output will appear from amplification higher.
Starch sugar manufacturing industry water resources consumption amount is larger, and production starch sugar is producing starch sugar for also having certain requirement with water
Before need to process industrial water.
Utility model content
For the problem of above-mentioned generation, the purpose of this utility model is to provide a kind of concentrated phase water filtration for starch sugar
Device.
To achieve these goals, the technical scheme that the utility model is taken is：
A kind of concentrated phase water filtering device for starch sugar, wherein, including：One water treatment facilities, the water treatment facilities
Including the raw water box, raw water pump, more medium filter, active carbon filter, cartridge filter, high-pressure pump and the desalination that are sequentially connected
Water tank；One reverse osmosis concentrated water tank, the reverse osmosis concentrated water tank is connected with the concentrated water outlet of the reverse osmosis unit；One backwash water
Pump, the entrance of the backwash water pump is connected with the outlet of the reverse osmosis concentrated water tank, the outlet of the backwash water pump respectively with
The more medium filter is connected with the active carbon filter；One concentrated water filter, the recoil of the more medium filter
Import of the backwash mouth of mouth and the active carbon filter respectively with the concentrated water filter is washed to be connected；One concentrated water case, institute
The outlet for stating concentrated water filter is connected with the concentrated water case.
The above-mentioned concentrated phase water filtering device for starch sugar, wherein, the backwash pipe outlet of the more medium filter
It is connected with a backwash water tank with the backwash pipe outlet of the active carbon filter.
The above-mentioned concentrated phase water filtering device for starch sugar, wherein, also including a pure water pump, the water inlet of the pure water pump
Mouth is connected with the desalination water tank, delivery port accessing user's water spot of the pure water pump.
The above-mentioned concentrated phase water filtering device for starch sugar, wherein, the delivery port of the pure water pump can be external by one
Cleaning pump connect the desalination water tank, the pure water pump, the high-pressure pump or the cartridge filter.
The above-mentioned concentrated phase water filtering device for starch sugar, wherein, the more medium filter uses quartz sand filtration
Device.
The above-mentioned concentrated phase water filtering device for starch sugar, wherein, the active carbon filter and the security personnel filter
Chemicals dosing plant is provided between device.
The above-mentioned concentrated phase water filtering device for starch sugar, wherein, antisludging agent is provided with the chemicals dosing plant and is gone back
Former agent.
The above-mentioned concentrated phase water filtering device for starch sugar, wherein, the reverse osmosis unit uses membrane filtration pattern.
The above-mentioned concentrated phase water filtering device for starch sugar, wherein, the outlet of the more medium filter, the activity
The outlet of carbon filter, the outlet of the cartridge filter and the outlet of the reverse osmosis unit are provided with non-return valve.
The utility model is as a result of above-mentioned technology, the good effect for being allowed to have compared with prior art：
(1) the utility model passes through more medium filter, active carbon filter, cartridge filter and reverse osmosis unit energy
Enough so that starch sugar water reaches standard, and with the function of being backwashed using concentrated water.
Brief description of the drawings
Fig. 1 is the schematic diagram of the concentrated phase water filtering device for starch sugar of the present utility model.
In accompanying drawing：1st, raw water box；2nd, raw water pump；3rd, more medium filter；4th, active carbon filter；5th, cartridge filter；
6th, high-pressure pump；7th, reverse osmosis unit；8th, desalination water tank；9th, pure water pump；10th, reverse osmosis concentrated water tank；11st, backwash water pump；12nd, concentrated water
Filter；13rd, concentrated water case.
Specific embodiment
The utility model is described in further detail with specific embodiment below in conjunction with the accompanying drawings, but not as of the present utility model
Limit.
Fig. 1 is the schematic diagram of the concentrated phase water filtering device for starch sugar of the present utility model, shown in Figure 1, is shown
A kind of concentrated phase water filtering device for starch sugar of preferred embodiment is gone out, has included：Water treatment facilities, water treatment facilities bag
Raw water box 1 and raw water pump 2 are included, the water inlet of raw water pump 2 is connected with raw water box 1.
Additionally, in as preferred embodiment, the concentrated phase water filtering device sewerage disposing device for starch sugar also includes：
More medium filter 3, active carbon filter 4 and cartridge filter 5, more medium filter 3, active carbon filter 4 and ensured public security
Filter 5 is sequentially connected, and the delivery port of raw water pump 2 is connected with the entrance of more medium filter 3.
In addition, in as preferred embodiment, the concentrated phase water filtering device water treatment facilities for starch sugar also includes：It is high
Press pump 6, reverse osmosis unit 7 and desalination water tank 8, the water inlet of high-pressure pump 6 are connected with the outlet of cartridge filter 5, water under high pressure
The delivery port of pump 6 is connected with the entrance of reverse osmosis unit 7, and the outlet of reverse osmosis unit 7 is connected with desalination water tank 8.
Further, in as preferred embodiment, the concentrated phase water filtering device water treatment facilities for starch sugar also includes：
Pure water pump 9, the water inlet of pure water pump 9 is connected with desalination water tank 8, delivery port accessing user's water spot of pure water pump 9, pure water pump
9 water outlets can reach corresponding standard, be available for user directly to use.
Further, as in preferred embodiment, the delivery port of pure water pump 9 can be by an external cleaning pump (in figure
It is not shown) connection desalination water tank 8, pure water pump 9, high-pressure pump 6 or cartridge filter 5, are drawn the pure water after filtering by pure water pump 9
Entering desalination water tank 8, pure water pump 9, high-pressure pump 6 or cartridge filter 5 carries out cleaning, prevents desalination water tank 8, pure water pump 9, height
The possibility that press pump 6 or cartridge filter 5 are blocked.
Further, as in preferred embodiment, desalination water tank 8, pure water pump 9, high-pressure pump 6 or cartridge filter 5 enter
Water after row cleaning introduces the import of reverse osmosis unit 7 by pipeline, is filtered use again.
Further, in as preferred embodiment, the concentrated phase water filtering device for starch sugar also includes：Reverse osmosis concentrated water tank
10, reverse osmosis concentrated water tank 10 is connected with the concentrated water outlet of reverse osmosis unit 7.
Further, in as preferred embodiment, the concentrated phase water filtering device for starch sugar also includes：Backwash water pump 11,
The entrance of backwash water pump 11 is connected with the outlet of reverse osmosis concentrated water tank 10, the outlet of backwash water pump 11 respectively with multi-medium filtering
Device 3 is connected with active carbon filter 4.Using the concentrated water processed by reverse osmosis unit 7 to more medium filter 3 and activated carbon
Filter 4 carries out backwash water, reaches the effect of concentrated water recycling.
Further, in as preferred embodiment, the concentrated phase water filtering device for starch sugar also includes：Concentrated water filter
12, more medium filter 3 backwash mouth and active carbon filter 4 backwash mouth respectively with the import phase of concentrated water filter 12
Connection, the backwash mouthful for carrying out backwash mouth and active carbon filter 4 that the concentrated water after backwash water passes through more medium filter 3 is entered
Enter concentrated water filter 12 to be filtered.
Further, as in preferred embodiment, concentrated water case 13, the outlet of concentrated water filter 12 is connected with concentrated water case 13
Connect, concentrated water case 13 is used for the recovery of concentrated water, the concentrated water after being filtered through concentrated water filter 12, concentrated water case 13 are collected by concentrated water case 13
The concentrated water of collection can be used as the flushing of other equipment.
The foregoing is only the utility model preferred embodiment, not thereby limit implementation method of the present utility model and
Protection domain.
The utility model on the basis of the above also have mode is implemented as follows：
In further embodiment of the present utility model, continuing with shown in Figure 1, more medium filter 3 uses quartz sand
Filter.Anthracite-quartz sand-magnetic iron ore filter, activated carbon-quartz sand-magnetic iron ore filter, activity can also be used
Charcoal-quartz filter, quartz sand-ceramic filter etc..
In further embodiment of the present utility model, dosing dress is provided between active carbon filter 4 and cartridge filter 5
Put (not shown).
In further embodiment of the present utility model, antisludging agent and reduction are provided with chemicals dosing plant (not shown)
Agent.Antisludging agent and reducing agent are added to the water that will enter cartridge filter 5 by chemicals dosing plant, the stifled of cartridge filter 5 is prevented
Plug.
In further embodiment of the present utility model, reverse osmosis unit 7 uses membrane filtration pattern.Counter-infiltration is higher than molten
Under the pressure effect of liquid osmotic pressure, by means of the selective retention for only allowing water to pass through without allowing the pellicle of other material permeances
Effect separates the solute in solution with solvent.Using the stalling characteristic of reverse osmosis membrane, the dissolving that can effectively go in water removal
The impurity such as salt, colloid, organic matter, bacterium, microorganism, the pressure higher than solution osmotic pressure is reached by high-pressure pump 6.
In further embodiment of the present utility model, the outlet of more medium filter 3, the outlet of active carbon filter 4, guarantor
The outlet of the outlet and reverse osmosis unit 7 of pacifying filter 5 is provided with non-return valve, and non-return valve is used to prevent more medium filter 3
Outlet, the outlet of active carbon filter 4, the exit of the outlet of cartridge filter 5 and reverse osmosis unit 7 completed treatment
Water is countercurrently.
The foregoing is only the utility model preferred embodiment, not thereby limit implementation method of the present utility model and
Protection domain, to those skilled in the art, should can appreciate that in all utilization the utility model specifications and diagram
Hold the scheme obtained by done equivalent and obvious change, should be included in protection model of the present utility model
In enclosing.
Claims (9)
1. a kind of concentrated phase water filtering device for starch sugar, it is characterised in that including：
One water treatment facilities, the water treatment facilities includes the raw water box, raw water pump, more medium filter, the activity that are sequentially connected
Carbon filter, cartridge filter, high-pressure pump and desalination water tank；
One reverse osmosis concentrated water tank, the reverse osmosis concentrated water tank is connected with the concentrated water outlet of the reverse osmosis unit；
One backwash water pump, the entrance of the backwash water pump is connected with the outlet of the reverse osmosis concentrated water tank, the backwash water pump
Outlet be connected with the more medium filter and the active carbon filter respectively；
One concentrated water filter, the more medium filter backwash mouth and the active carbon filter backwash mouth respectively with
The import of the concentrated water filter is connected；
One concentrated water case, the outlet of the concentrated water filter is connected with the concentrated water case.
2. the concentrated phase water filtering device for starch sugar according to claim 1, it is characterised in that the multi-medium filtering
The backwash pipe outlet of device and the backwash pipe outlet of the active carbon filter are connected with a backwash water tank.
3. the concentrated phase water filtering device for starch sugar according to claim 1, it is characterised in that also including a pure water
Pump, the water inlet of the pure water pump is connected with the desalination water tank, delivery port accessing user's water spot of the pure water pump.
4. the concentrated phase water filtering device for starch sugar according to claim 3, it is characterised in that the pure water pump goes out
The mouth of a river can connect the desalination water tank, the pure water pump, the high-pressure pump or the security personnel and filter by an external cleaning pump
Device.
5. the concentrated phase water filtering device for starch sugar according to claim 1, it is characterised in that the multi-medium filtering
Device uses quartz filter.
6. the concentrated phase water filtering device for starch sugar according to claim 1, it is characterised in that the activated carbon filtering
Chemicals dosing plant is provided between device and the cartridge filter.
7. the concentrated phase water filtering device for starch sugar according to claim 6, it is characterised in that in the chemicals dosing plant
It is provided with antisludging agent and reducing agent.
8. the concentrated phase water filtering device for starch sugar according to claim 1, it is characterised in that the reverse osmosis unit
Using membrane filtration pattern.
9. the concentrated phase water filtering device for starch sugar according to claim 1, it is characterised in that the multi-medium filtering
The outlet of device, the outlet of the active carbon filter, the outlet of the cartridge filter and the outlet of the reverse osmosis unit are equal
It is provided with non-return valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621492136.XU CN206308179U (en) | 2016-12-30 | 2016-12-30 | A kind of concentrated phase water filtering device for starch sugar |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621492136.XU CN206308179U (en) | 2016-12-30 | 2016-12-30 | A kind of concentrated phase water filtering device for starch sugar |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206308179U true CN206308179U (en) | 2017-07-07 |
Family
ID=59247740
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621492136.XU Expired - Fee Related CN206308179U (en) | 2016-12-30 | 2016-12-30 | A kind of concentrated phase water filtering device for starch sugar |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206308179U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108191120A (en) * | 2018-03-08 | 2018-06-22 | 湖南水口山有色金属集团有限公司 | A kind of Water Treatment equipment |
-
2016
- 2016-12-30 CN CN201621492136.XU patent/CN206308179U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108191120A (en) * | 2018-03-08 | 2018-06-22 | 湖南水口山有色金属集团有限公司 | A kind of Water Treatment equipment |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN206266345U (en) | A kind of 10 tons of twin-stage pure water systems per hour | |
| CN202358976U (en) | Glass wastewater treatment equipment | |
| CN217119589U (en) | Filter equipment of sugar palm polysaccharide iron production | |
| CN206308179U (en) | A kind of concentrated phase water filtering device for starch sugar | |
| CN102382203A (en) | High-efficiency extraction process for polysaccharide of lotus seeds | |
| CN206308177U (en) | A kind of water treatment facilities for starch sugar | |
| CN205892902U (en) | Efficient water conservation intelligence purifier | |
| CN205042366U (en) | Changeable segmentation reverse osmosis membrane of direction of intaking piles structure | |
| CN201512490U (en) | Integrated device for extracting, separating and concentrating anthocyanin of vaccinium vitis-idaea | |
| CN104803516A (en) | Integrated container type sea water desalting equipment and desalting process thereof | |
| CN104529003B (en) | A kind of acid regeneration equipment | |
| CN204198447U (en) | A kind of device of separated powder gac from waste water | |
| CN205216328U (en) | A filtration equipment for biological enzyme retrieval and utilization | |
| CN202717637U (en) | Primary water storage circulating system of purified water preparation workshop | |
| CN202705273U (en) | D-ribose extraction and purification production line | |
| CN203360184U (en) | Strong brine treating and recovering system | |
| CN206033429U (en) | Concentrated processing system of membrane of mud filtrating | |
| CN206463617U (en) | A kind of L alanine microporous filter pipeline surplus material recovery device | |
| CN204952381U (en) | Water filter device | |
| CN204981230U (en) | Industrial water active carbon filter equipment | |
| CN205145993U (en) | A equipment for traditional chinese medicine purification | |
| CN206502706U (en) | A kind of water filtering system produced for concrete waterproofer | |
| CN204981423U (en) | Hydrologic cycle processing apparatus for swimming pool | |
| CN112779426B (en) | CO (carbon monoxide) 2 +O 2 Method for recycling uranium in wastewater of in-situ leaching uranium mining evaporation pool | |
| CN204625338U (en) | A kind of pig-breeding wastewater treatment equipment |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CB03 | Change of inventor or designer information | ||
| CB03 | Change of inventor or designer information |
Inventor after: Lv Dapeng Inventor after: Song Guangbin Inventor after: Zhang Dexin Inventor before: Lv Dapeng Inventor before: Song Guangbin Inventor before: Zhang Dexin |
|
| CB03 | Change of inventor or designer information | ||
| CB03 | Change of inventor or designer information |
Inventor after: Lv Dapeng Inventor after: Song Guangbin Inventor after: Zhu Xiaofeng Inventor before: Lv Dapeng Inventor before: Song Guangbin Inventor before: Zhang Dexin |
|
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170707 |