CN206308177U - A kind of water treatment facilities for starch sugar - Google Patents
A kind of water treatment facilities for starch sugar Download PDFInfo
- Publication number
- CN206308177U CN206308177U CN201621479962.0U CN201621479962U CN206308177U CN 206308177 U CN206308177 U CN 206308177U CN 201621479962 U CN201621479962 U CN 201621479962U CN 206308177 U CN206308177 U CN 206308177U
- Authority
- CN
- China
- Prior art keywords
- filter
- water
- pump
- starch sugar
- treatment facilities
- 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 113
- 229920002472 Starch Polymers 0.000 title claims abstract description 36
- 235000019698 starch Nutrition 0.000 title claims abstract description 36
- 239000008107 starch Substances 0.000 title claims abstract description 36
- 238000001223 reverse osmosis Methods 0.000 claims abstract description 22
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 20
- 238000010612 desalination reaction Methods 0.000 claims abstract description 18
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 16
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 7
- 239000010453 quartz Substances 0.000 claims description 6
- 239000000126 substance Substances 0.000 claims description 6
- 239000003795 chemical substances by application Substances 0.000 claims description 5
- 238000004140 cleaning Methods 0.000 claims description 4
- 239000003638 chemical reducing agent Substances 0.000 claims description 3
- 238000005374 membrane filtration Methods 0.000 claims description 3
- 238000000034 method Methods 0.000 description 5
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 230000008569 process Effects 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
- 239000008103 glucose Substances 0.000 description 2
- 235000019534 high fructose corn syrup Nutrition 0.000 description 2
- 238000001764 infiltration Methods 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
- 239000006004 Quartz sand Substances 0.000 description 1
- 230000003321 amplification Effects 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 230000008859 change Effects 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
- 238000001914 filtration Methods 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000008235 industrial water Substances 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
- 230000035699 permeability Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 150000003839 salts Chemical class 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 raw water box；One raw water pump, the water inlet of raw water pump is connected with raw water box；One more medium filter, an active carbon filter and a cartridge filter, more medium filter, active carbon filter and cartridge filter are sequentially connected, and the delivery port of raw water pump is connected with the entrance of more medium filter；One high-pressure pump, the water inlet of high-pressure pump is connected with the outlet of cartridge filter；One reverse osmosis unit, the delivery port of high-pressure hydraulic pump is connected with the entrance of reverse osmosis unit；One desalination water tank, the outlet of reverse osmosis unit is connected with desalination water tank.The utility model enables to starch sugar water to reach standard by more medium filter, active carbon filter, cartridge filter and reverse osmosis unit.
Description
Technical field
The utility model is related to the technical field of water treatment facilities, more particularly to a kind of water process dress for starch sugar
Put.
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 water process dress for starch sugar
Put.
To achieve these goals, the technical scheme that the utility model is taken is：
A kind of water treatment facilities for starch sugar, wherein, including：One raw water box；One raw water pump, the raw water pump enters
The mouth of a river is connected with the raw water box；One more medium filter, an active carbon filter and a cartridge filter, the multimedium
Filter, the active carbon filter and the cartridge filter are sequentially connected, and the delivery port of the raw water pump and described are situated between more
The entrance of mass filter is connected；One high-pressure pump, the water inlet of the high-pressure pump is connected with the outlet of the cartridge filter；
One reverse osmosis unit, the delivery port of the high-pressure hydraulic pump is connected with the entrance of the reverse osmosis unit；One desalination water tank, it is described
The outlet of reverse osmosis unit is connected with the desalination water tank.
The above-mentioned water treatment facilities for starch sugar, wherein, also including a pure water pump, the water inlet of the pure water pump with
The desalination water tank is connected, delivery port accessing user's water spot of the pure water pump.
The above-mentioned water treatment facilities for starch sugar, wherein, the delivery port of the pure water pump can be external clear by one
Wash pump and connect the desalination water tank, the pure water pump, the high-pressure pump or the cartridge filter.
The above-mentioned water treatment facilities for starch sugar, wherein, the more medium filter uses quartz filter.
The above-mentioned water treatment facilities for starch sugar, wherein, the active carbon filter and the cartridge filter it
Between be provided with chemicals dosing plant.
The above-mentioned water treatment facilities for starch sugar, wherein, antisludging agent and reducing agent are provided with the chemicals dosing plant.
The above-mentioned water treatment facilities for starch sugar, wherein, the reverse osmosis unit uses membrane filtration pattern.
The above-mentioned water treatment facilities for starch sugar, wherein, the outlet of the more medium filter, the activated carbon mistake
The outlet of 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.
Brief description of the drawings
Fig. 1 is the schematic diagram of the water treatment facilities 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.
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 water treatment facilities for starch sugar of the present utility model, shown in Figure 1, is shown
A kind of water treatment facilities for starch sugar of preferred embodiment, includes：Raw water box 1 and raw water pump 2, the water inlet of raw water pump 2
Mouth is connected with raw water box 1.
Additionally, in as preferred embodiment, the water treatment facilities for starch sugar also includes：More medium filter 3, work
Property carbon filter 4 and cartridge filter 5, more medium filter 3, active carbon filter 4 and cartridge filter 5 are sequentially connected, former
The delivery port of water pump 2 is connected with the entrance of more medium filter 3.
In addition, in as preferred embodiment, the water treatment facilities for starch sugar also includes：High-pressure pump 6, counter-infiltration is filled
Put 7 and desalination water tank 8, the water inlet of high-pressure pump 6 is connected with the outlet of cartridge filter 5, the delivery port of high-pressure hydraulic pump 6 with it is anti-
The entrance of permeability apparatus 7 is connected, and the outlet of reverse osmosis unit 7 is connected with desalination water tank 8.
Further, in as preferred embodiment, the water treatment facilities for starch sugar also includes：Pure water pump 9, pure water pump
9 water inlet is connected with desalination water tank 8, and delivery port accessing user's water spot of pure water pump 9, the water outlet of pure water pump 9 can reach
Corresponding standard, is 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.
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 (8)
1. a kind of water treatment facilities for starch sugar, it is characterised in that including：
One raw water box；
One raw water pump, the water inlet of the raw water pump is connected with the raw water box；
One more medium filter, an active carbon filter and a cartridge filter, the more medium filter, the activated carbon mistake
Filter and the cartridge filter are sequentially connected, and the delivery port of the raw water pump is connected with the entrance of the more medium filter
Connect；
One high-pressure pump, the water inlet of the high-pressure pump is connected with the outlet of the cartridge filter；
One reverse osmosis unit, the delivery port of the high-pressure hydraulic pump is connected with the entrance of the reverse osmosis unit；
One desalination water tank, the outlet of the reverse osmosis unit is connected with the desalination water tank.
2. the water treatment facilities for starch sugar according to claim 1, it is characterised in that also including a pure water pump, institute
The water inlet for stating pure water pump is connected with the desalination water tank, delivery port accessing user's water spot of the pure water pump.
3. the water treatment facilities for starch sugar according to claim 2, it is characterised in that the delivery port of the pure water pump
The desalination water tank, the pure water pump, the high-pressure pump or the cartridge filter can be connected by an external cleaning pump.
4. the water treatment facilities for starch sugar according to claim 1, it is characterised in that the more medium filter is adopted
Use quartz filter.
5. the water treatment facilities for starch sugar according to claim 1, it is characterised in that the active carbon filter with
Chemicals dosing plant is provided between the cartridge filter.
6. the water treatment facilities for starch sugar according to claim 5, it is characterised in that set in the chemicals dosing plant
There are antisludging agent and reducing agent.
7. the water treatment facilities for starch sugar according to claim 1, it is characterised in that the reverse osmosis unit is used
Membrane filtration pattern.
8. the water treatment facilities for starch sugar according to claim 1, it is characterised in that the more medium filter
Outlet, the outlet of the active carbon filter, the outlet of the cartridge filter and the outlet of the reverse osmosis unit are respectively provided with
There is non-return valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621479962.0U CN206308177U (en) | 2016-12-30 | 2016-12-30 | A kind of water treatment facilities for starch sugar |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621479962.0U CN206308177U (en) | 2016-12-30 | 2016-12-30 | A kind of water treatment facilities for starch sugar |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206308177U true CN206308177U (en) | 2017-07-07 |
Family
ID=59247940
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621479962.0U Expired - Fee Related CN206308177U (en) | 2016-12-30 | 2016-12-30 | A kind of water treatment facilities for starch sugar |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206308177U (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 CN201621479962.0U patent/CN206308177U/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 |
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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: Hou Jie Inventor after: Wu Lanying Inventor before: Lv Dapeng Inventor before: Zhang Dexin Inventor before: Wu Lanying |
|
| 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 |