CN106277565A - The processing means of a kind of sucralose waste water and using method - Google Patents
The processing means of a kind of sucralose waste water and using method Download PDFInfo
- Publication number
- CN106277565A CN106277565A CN201610639900.XA CN201610639900A CN106277565A CN 106277565 A CN106277565 A CN 106277565A CN 201610639900 A CN201610639900 A CN 201610639900A CN 106277565 A CN106277565 A CN 106277565A
- Authority
- CN
- China
- Prior art keywords
- reactor
- waste water
- processing means
- baf
- anaerobic
- 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.)
- Granted
Links
- 239000002351 wastewater Substances 0.000 title claims abstract description 36
- 239000004376 Sucralose Substances 0.000 title claims abstract description 26
- BAQAVOSOZGMPRM-QBMZZYIRSA-N sucralose Chemical compound O[C@@H]1[C@@H](O)[C@@H](Cl)[C@@H](CO)O[C@@H]1O[C@@]1(CCl)[C@@H](O)[C@H](O)[C@@H](CCl)O1 BAQAVOSOZGMPRM-QBMZZYIRSA-N 0.000 title claims abstract description 26
- 235000019408 sucralose Nutrition 0.000 title claims abstract description 26
- 238000000034 method Methods 0.000 title claims abstract description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 26
- 230000003647 oxidation Effects 0.000 claims abstract description 16
- 238000007254 oxidation reaction Methods 0.000 claims abstract description 16
- 230000000694 effects Effects 0.000 claims abstract description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 16
- 229920002635 polyurethane Polymers 0.000 claims description 8
- 239000004814 polyurethane Substances 0.000 claims description 8
- 229910021536 Zeolite Inorganic materials 0.000 claims description 6
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 claims description 6
- 239000010457 zeolite Substances 0.000 claims description 6
- 239000011435 rock Substances 0.000 claims description 5
- 238000005273 aeration Methods 0.000 claims description 4
- 238000007599 discharging Methods 0.000 claims description 4
- 239000000945 filler Substances 0.000 claims description 4
- 230000002572 peristaltic effect Effects 0.000 claims description 4
- 239000011148 porous material Substances 0.000 claims description 4
- ZCYVEMRRCGMTRW-UHFFFAOYSA-N 7553-56-2 Chemical compound [I] ZCYVEMRRCGMTRW-UHFFFAOYSA-N 0.000 claims description 3
- 238000006243 chemical reaction Methods 0.000 claims description 3
- 229910052740 iodine Inorganic materials 0.000 claims description 3
- 239000011630 iodine Substances 0.000 claims description 3
- 239000003610 charcoal Substances 0.000 claims 1
- 239000007788 liquid Substances 0.000 abstract description 3
- 239000002028 Biomass Substances 0.000 abstract description 2
- 230000000813 microbial effect Effects 0.000 abstract description 2
- 239000010865 sewage Substances 0.000 abstract description 2
- 239000007787 solid Substances 0.000 abstract description 2
- 239000000758 substrate Substances 0.000 abstract description 2
- 239000000126 substance Substances 0.000 description 3
- 239000000470 constituent Substances 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- UOCLXMDMGBRAIB-UHFFFAOYSA-N 1,1,1-trichloroethane Chemical compound CC(Cl)(Cl)Cl UOCLXMDMGBRAIB-UHFFFAOYSA-N 0.000 description 1
- 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 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000008103 glucose Substances 0.000 description 1
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 1
- 125000004836 hexamethylene group Chemical group [H]C([H])([*:2])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])[*:1] 0.000 description 1
- 230000002401 inhibitory effect Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/02—Aerobic processes
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/28—Anaerobic digestion processes
Abstract
The invention discloses the processing means of a kind of sucralose waste water, including water leg, anaerobic reactor, aerobic reactor, BAF reactor and deep oxidation pond, described water leg, anaerobic reactor, aerobic reactor, BAF reactor and deep oxidation pond are sequentially connected.Meanwhile, the invention also discloses the using method of the processing means of above-mentioned sucralose waste water.The each reactor of the present invention cultivates the substrate component with this space and the suitable microbial population of envirment factor in the space of each fire resisting division, the mud formed in each independent space is prevented to be mutually mixed, the gas that different piece produces individually discharges, do not mix with other parts, between use power water distribution, make waste water in flow process with substantial amounts of active biomass generation multiple-contact, substantially increase the capacity utilization of reactor, effectively reduce effluent COD concentration, improve sewage treating efficiency, good effect of separating solid from liquid, anti impulsion load, the feature that biosolids interception capacity is high.
Description
Technical field
The invention belongs to chemical industry environmental protection field, be specifically related to processing means and the processing method of a kind of sucralose waste water.
Background technology
Sucralose technique waste water is the one of high-concentration organic chemical wastewater, is that a kind of typical " three-hypers one is difficult " is fine
Wastewater from chemical industry, its water-quality constituents is complicated, concentration is high, biodegradability is poor, and intractability is bigger.The water-quality constituents of waste water is complicated, special
Levy the material micro-lifes to biochemical treatment such as the DMF in the stable performance of pollution factor, especially waste water, trichloroethane and hexamethylene
Thing has the strongest inhibitory action；If sucralose waste water is not set up perfect waste water disposal facility, effluent quality is caused not reach
Mark, have impact on the ecological environment of water body.Therefore, sucralose wastewater processing technology economic, efficient is explored, it appears the most urgent
Cut.
Summary of the invention
Goal of the invention: present invention aims to the deficiencies in the prior art, it is provided that the place of a kind of sucralose waste water
Reason device.
Another object of the present invention is to provide the using method of the processing means of sucralose waste water.
Technical scheme: in order to reach foregoing invention purpose, the present invention is specifically achieved like this: a kind of sucralose gives up
The processing means of water, including water leg, anaerobic reactor, aerobic reactor, BAF reactor and deep oxidation pond, described in catchment
Groove, anaerobic reactor, aerobic reactor, BAF reactor and deep oxidation pond are sequentially connected by pipeline, anaerobic reactor, good
Oxygen reactor, BAF reactor are connected by outlet pipe respectively collecting-tank, and it is anti-that collecting-tank is connected to next anaerobism by peristaltic pump
Answer and connect mud discharging mouth, anaerobism by blow-off line bottom device, aerobic reactor or BAF reactor, water leg and each collecting-tank
It is provided with active filler in reactor, bottom aerobic reactor, BAF reactor and deep oxidation pond, is provided with some micro-pore aeration holes.
Wherein, the number of described anaerobic reactor is 4, is provided with activated carbon bottom front 3 anaerobic reactors, and iodine number is
650 ~ 1100, the 4th anaerobic reactor lower floor be volcanic rock, upper strata be polyurethane sponge.
Wherein, be filled with zeolite bottom described aerobic reaction pond, activated carbon is filled on upper strata.
Wherein, described BAF reactor bottom fills volcanic rock, and top is polyurethane sponge.
Wherein, the thickness of described zeolite or activated carbon is 1 ~ 40mm.
Wherein, the thickness of described polyurethane sponge is 2cm.
The using method of the processing means of a kind of sucralose waste water, comprises the following steps: waste water is passed through sucralose
The processing means of waste water processes, and controls the anaerobic reactor time of staying 36 ~ 96h, the aerobic reactor time of staying 12 ~ 48h, BAF
Reactor residence time 8 ~ 24h, the deep oxidation pond time of staying 2 ~ 6h, controlling pH is 5.5 ~ 8.5, and temperature 25 ~ 45 DEG C, anaerobism is anti-
Control DO ＜ 0.5mg/l, aerobic reactor and BAF reactor in device is answered to control DO ＞ 8 mg/l.
Beneficial effect: the present invention is compared with conventional art, and each reactor is cultivated and this space in the space of each fire resisting division
Substrate component and the suitable microbial population of envirment factor, prevent in each independent space formed mud be mutually mixed,
Different piece produce gas individually discharge, do not mix with other parts, between use power water distribution so that waste water is flowing over
With substantial amounts of active biomass generation multiple-contact in journey, substantially increase the capacity utilization of reactor, effectively reduce out
Water COD concentration, improves sewage treating efficiency, good effect of separating solid from liquid, anti impulsion load, the spy that biosolids interception capacity is high
Point.
Accompanying drawing explanation
Fig. 1 is the structural representation of the processing means of the present invention a kind of sucralose waste water.
Wherein, 1-water leg, 2-anaerobic reactor, 3-aerobic reactor, 4-BAF reactor, 5-deep oxidation pond, 6-water outlet
Pipe, 7-collecting-tank, 8-peristaltic pump, 9-blow-off line connects mud discharging mouth, 10-active filler, 11-micro-pore aeration hole 11.
Detailed description of the invention
Embodiment 1:
The processing means of a kind of sucralose waste water, including water leg 1, anaerobic reactor 2, aerobic reactor 3, BAF reactor 4
With deep oxidation pond 5, described water leg 1, anaerobic reactor 2, aerobic reactor 3, BAF reactor 4 and deep oxidation pond 5 are passed through
Pipeline is sequentially connected, and anaerobic reactor 2, aerobic reactor 3, BAF reactor 4 are connected by outlet pipe 6 respectively collecting-tank 7,
Collecting-tank 7 is connected to next anaerobic reactor 2, aerobic reactor 3 or BAF reactor 4 by peristaltic pump 8, water leg 1 and each
Connect mud discharging mouth 9 by blow-off line bottom collecting-tank 7, in anaerobic reactor 2, be provided with active filler 10, aerobic reactor 3,
Some micro-pore aeration holes 11 it are provided with bottom BAF reactor 4 and deep oxidation pond 5；The number of described anaerobic reactor 2 is 4, front
Being provided with activated carbon bottom 3 anaerobic reactors, iodine number is 650 ~ 1100, and the 4th anaerobic reactor lower floor is that volcanic rock, upper strata are
Polyurethane sponge, is filled with zeolite, activated carbon is filled on upper strata bottom aerobic reaction pond 3, and the thickness of described zeolite or activated carbon is 1 ~
40mm, the thickness of polyurethane sponge is 2cm.
Embodiment 2:
The using method of the processing means of a kind of sucralose waste water, comprises the following steps: by waste water by sucralose waste water
Processing means process, control the anaerobic reactor time of staying 36 ~ 96h, the aerobic reactor time of staying 12 ~ 48h, BAF react
The device time of staying 8 ~ 24h, the deep oxidation pond time of staying 2 ~ 6h, controlling pH is 5.5 ~ 8.5, temperature 25 ~ 45 DEG C, anaerobic reactor
Middle control DO ＜ 0.5mg/l, aerobic reactor and BAF reactor control DO ＞ 8 mg/l.
Embodiment 3:
Whole anaerobic reactor anaerobic species+glucose simulated wastewater is tamed, altogether 7 cycles of domestication, each cycle 5d,
COD is increase gradually to 10000 mg/l from 3000 mg/l, after domestication terminates, starts to test, every time with sucralose waste water
Water inlet is for 5L, and the water outlet that the water inlet of a rear reactor is previous reactor, final outflow water is clear liquid on which after static 30min
Monitoring Data (as shown in Table 1), show anaerobism section influent COD at about 10000 mg/l, water outlet is in 1000mg/l, anaerobism section
COD clearance maintains 90%, and anaerobic effluent is maintained by peristaltic pump to aerobic reactor, water outlet 150 mg/l, COD clearance
About 85%, outputted aerobic water is to BAF reactor, and COD drops to about 100 mg/l, clearance more than 30%, BAF water outlet warp
Crossing deep oxidation, water outlet COD is at 100 below mg/l, qualified discharge.
Inlet and outlet water COD value when table 1 flow is 5L/d
Claims (7)
1. a processing means for sucralose waste water, including water leg (1), anaerobic reactor (2), aerobic reactor (3),
BAF reactor (4) and deep oxidation pond (5), it is characterised in that described water leg (1), anaerobic reactor (2), aerobic reactor
(3), BAF reactor (4) and deep oxidation pond (5) be sequentially connected by pipeline, anaerobic reactor (2), aerobic reactor (3),
BAF reactor (4) is connected by outlet pipe (6) respectively collecting-tank (7), and collecting-tank (7) is connected to next by peristaltic pump (8)
Anaerobic reactor (2), aerobic reactor (3) or BAF reactor (4), water leg (1) and each collecting-tank (7) bottom are by row
Dirty pipeline connects mud discharging mouth (9), is provided with active filler (10), aerobic reactor (3), BAF reactor in anaerobic reactor (2)
(4) and it is provided with some micro-pore aeration holes (11) bottom deep oxidation pond (5).
The processing means of sucralose waste water the most according to claim 1, it is characterised in that described anaerobic reactor (2)
Number be 4, be provided with activated carbon bottom front 3 anaerobic reactors, iodine number is 650 ~ 1100, the 4th anaerobic reactor lower floor
It is polyurethane sponge for volcanic rock, upper strata.
The processing means of sucralose waste water the most according to claim 1, it is characterised in that bottom described aerobic reaction pond
Be filled with zeolite, activated carbon is filled on upper strata.
The processing means of sucralose waste water the most according to claim 1, it is characterised in that described BAF reactor bottom
Filling volcanic rock, top is polyurethane sponge.
5. according to the processing means of the sucralose waste water described in Claims 2 or 3, it is characterised in that described zeolite or activity
The thickness of charcoal is 1 ~ 40mm.
6. according to the processing means of the sucralose waste water described in claim 2 or 4, it is characterised in that described polyurethane sponge
Thickness be 2cm.
7. the using method of the processing means of a sucralose waste water, it is characterised in that comprise the following steps: waste water is passed through
The processing means of sucralose waste water processes, and controls the anaerobic reactor time of staying 36 ~ 96h, and aerobic reactor time of staying 12 ~
48h, BAF reactor residence time 8 ~ 24h, the deep oxidation pond time of staying 2 ~ 6h, controlling pH is 5.5 ~ 8.5, temperature 25 ~ 45
DEG C, anaerobic reactor controls DO ＜ 0.5mg/l, aerobic reactor and BAF reactor and controls DO ＞ 8 mg/l.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610639900.XA CN106277565B (en) | 2016-08-08 | 2016-08-08 | Sucralose wastewater treatment device and use method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610639900.XA CN106277565B (en) | 2016-08-08 | 2016-08-08 | Sucralose wastewater treatment device and use method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN106277565A true CN106277565A (en) | 2017-01-04 |
| CN106277565B CN106277565B (en) | 2020-02-14 |
Family
ID=57665950
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610639900.XA Active CN106277565B (en) | 2016-08-08 | 2016-08-08 | Sucralose wastewater treatment device and use method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106277565B (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114988652A (en) * | 2022-07-13 | 2022-09-02 | 福建科宏生物工程股份有限公司 | Method for treating sucralose wastewater by using lipoic acid wastewater |
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-
2016
- 2016-08-08 CN CN201610639900.XA patent/CN106277565B/en active Active
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101492222A (en) * | 2008-12-30 | 2009-07-29 | 广西贵糖（集团）股份有限公司 | Method for comprehensive treatment of wastewater and sludge gas utilization of cane sugar factory |
| CN101549908A (en) * | 2009-05-11 | 2009-10-07 | 江苏金山环保工程集团有限公司 | High-efficiency beet sugar-manufacturing wastewater treatment system |
| CN102211807A (en) * | 2011-05-04 | 2011-10-12 | 南京工业大学 | High-density porous support for treating wastewater of biological fluidized bed and preparation method thereof |
| CN102225827A (en) * | 2011-05-24 | 2011-10-26 | 青岛理工大学 | Treatment method for wastewater from straw pulp papermaking intermediate section |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114988652A (en) * | 2022-07-13 | 2022-09-02 | 福建科宏生物工程股份有限公司 | Method for treating sucralose wastewater by using lipoic acid wastewater |
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| CN106277565B (en) | 2020-02-14 |
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Address after: 214221 Jiangsu city of Yixing Province, Lin Dingshu Town Industrial Park Applicant after: JIANGSU LASON CHEMICAL ENVIRONMENTAL PROTECTION CO.,LTD. Address before: 214221 Jiangsu city of Wuxi province Yixing City, Lin Dingshu Town Industrial Park Applicant before: JIANGSU LASON CHEMICAL ENVIRONMENTAL PROTECTION CO.,LTD. |
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| CB03 | Change of inventor or designer information |
Inventor after: Jiang Weiqun Inventor after: Jiang Haodong Inventor after: Wei Limin Inventor after: Zhou Zhengsheng Inventor before: Jiang Weiqun Inventor before: Wei Limin Inventor before: Zhou Zhengsheng Inventor before: Cui Bing Inventor before: Bi Shengyao |
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Denomination of invention: A treatment device for sucralose wastewater and its application method Effective date of registration: 20210817 Granted publication date: 20200214 Pledgee: Wuxi rural commercial bank Limited by Share Ltd. Yixing branch Pledgor: JIANGSU LASON CHEMICAL ENVIRONMENTAL PROTECTION Co.,Ltd. Registration number: Y2021320010315 |
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Date of cancellation: 20221217 Granted publication date: 20200214 Pledgee: Wuxi rural commercial bank Limited by Share Ltd. Yixing branch Pledgor: JIANGSU LASON CHEMICAL ENVIRONMENTAL PROTECTION CO.,LTD. Registration number: Y2021320010315 |
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| PC01 | Cancellation of the registration of the contract for pledge of patent right |