CN101070204A - Method and apparatus for treating waste water containing low-concentration perfluoro ammonium caprylate - Google Patents
Method and apparatus for treating waste water containing low-concentration perfluoro ammonium caprylate Download PDFInfo
- Publication number
- CN101070204A CN101070204A CN 200710069327 CN200710069327A CN101070204A CN 101070204 A CN101070204 A CN 101070204A CN 200710069327 CN200710069327 CN 200710069327 CN 200710069327 A CN200710069327 A CN 200710069327A CN 101070204 A CN101070204 A CN 101070204A
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- CN
- China
- Prior art keywords
- waste water
- nanofiltration membrane
- foam
- valve
- perfluoro ammonium
- 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 54
- YDDULLXUFDTAKJ-UHFFFAOYSA-M octanoate tetrafluoroazanium Chemical compound F[N+](F)(F)F.CCCCCCCC([O-])=O YDDULLXUFDTAKJ-UHFFFAOYSA-M 0.000 title claims abstract description 28
- 238000000034 method Methods 0.000 title claims abstract description 19
- 238000001728 nano-filtration Methods 0.000 claims abstract description 57
- 239000006260 foam Substances 0.000 claims abstract description 47
- 239000012528 membrane Substances 0.000 claims abstract description 47
- 239000007788 liquid Substances 0.000 claims abstract description 18
- 238000000926 separation method Methods 0.000 claims abstract description 17
- 239000012530 fluid Substances 0.000 claims abstract description 14
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 8
- 238000004064 recycling Methods 0.000 claims abstract description 4
- 238000003860 storage Methods 0.000 claims description 25
- SNGREZUHAYWORS-UHFFFAOYSA-N perfluorooctanoic acid Chemical compound OC(=O)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)F SNGREZUHAYWORS-UHFFFAOYSA-N 0.000 claims description 13
- 239000007864 aqueous solution Substances 0.000 claims description 12
- 239000000243 solution Substances 0.000 claims description 12
- 238000004065 wastewater treatment Methods 0.000 claims description 9
- 230000003139 buffering effect Effects 0.000 claims description 7
- 239000013078 crystal Substances 0.000 claims description 6
- 238000009826 distribution Methods 0.000 claims description 5
- 239000007787 solid Substances 0.000 claims description 5
- 239000012141 concentrate Substances 0.000 claims description 4
- 238000001914 filtration Methods 0.000 claims description 3
- 238000004519 manufacturing process Methods 0.000 claims description 3
- 241000282326 Felis catus Species 0.000 claims description 2
- 238000007599 discharging Methods 0.000 claims description 2
- 238000004140 cleaning Methods 0.000 abstract 1
- LDOAUKNENSIPAZ-UHFFFAOYSA-N tetrafluoroammonium Chemical compound F[N+](F)(F)F LDOAUKNENSIPAZ-UHFFFAOYSA-N 0.000 abstract 1
- 238000005265 energy consumption Methods 0.000 description 2
- 239000004809 Teflon Substances 0.000 description 1
- 229920006362 Teflon® Polymers 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000013543 active substance Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000002270 dispersing agent Substances 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 229910052731 fluorine Inorganic materials 0.000 description 1
- 239000011737 fluorine Substances 0.000 description 1
- 125000001153 fluoro group Chemical group F* 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 239000012716 precipitator Substances 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 230000000192 social effect Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
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- Separation Using Semi-Permeable Membranes (AREA)
Abstract
This invention relates to a treatment methods and device of low concentration perfluoro ammonium caprylate waste water. Pump clear perfluoro ammonium caprylate waste water into foam separation tower to carry out foam separation, defoam the wastewater tower top spume to gain high concentration perfluoro ammonium caprylate water solution which can be reutilized; gain lower concentration perfluoro ammonium caprulate water solution at tower bottom; use first order nano filter membrane to filter perfluoro ammonium caprylate water solution ejected by tower bottom, condense nano filtration trapped fluid, return it to foam separation tower to carry out foam separation; the permeation liquid of first order nano filter membrane enter secondary nano filter membrane; permeance liquid of secondary nano filter membrane can reach state waste water effluent standard; concentrated solution of secondary nano filter membrane return to first order nano filter membrane; then complete recycling and cleaning of waste water.
Description
Technical field
The present invention relates to contain surface active agent wastewater and handle, especially relate to a kind of low-concentration perfluoro ammonium caprylate method of wastewater treatment and device of containing.
Background technology
Dispersion method will add certain amount of dispersant ammonium perfluorocaprylate (PFOA) when producing teflon resin, outside the last ammonium perfluorocaprylate waste water discharge system with lower concentration.Ammonium perfluorocaprylate is a kind of tensio-active agent efficiently that costs an arm and a leg, and difficult for biological degradation has great harm to environment.Therefore waste water is handled to reclaim ammonium perfluorocaprylate, existing economic implications has social effect again.Existing treatment process has: the distillation absorption method, and its shortcoming is the energy consumption height, and is uneconomical; The precipitator method, as patent fluorine bonded treatment process and treated substance (application number 01802169.7), its shortcoming is to add precipitation agent, produces new useless solids.
Summary of the invention
In order to handle waste water cost-effectively, reclaim useful matter simultaneously, do not produce new refuse, the object of the present invention is to provide and adopt a kind of low-concentration perfluoro ammonium caprylate method of wastewater treatment and device of containing.The method that nanofiltration and foam separation combine is handled the ammonium perfluorocaprylate waste water that contains lower concentration.
The technical solution adopted for the present invention to solve the technical problems is:
One, contain the low-concentration perfluoro ammonium caprylate method of wastewater treatment:
(1) at first waste water is filtered with ultracentrifuge,, obtain the as clear as crystal ammonium perfluorocaprylate waste water that contains solid particulate filtering wherein;
(2) waste water is pumped into foam separating tower and carry out foam separation, obtain the high density perfluoro ammonium caprylate aqueous solution behind the cat head foam froth breaking, can turn back in the production and utilize again; Obtain the lower perfluoro ammonium caprylate aqueous solution of concentration at the bottom of the tower;
(3) perfluoro ammonium caprylate aqueous solution of discharging at the bottom of the foam separation Tata is filtered with first step nanofiltration membrane, the nanofiltration trapped fluid, promptly concentrated solution turns back to foam separating tower and carries out foam separation again; The liquid that sees through of first step nanofiltration membrane enters second stage nanofiltration membrane;
(4) liquid that sees through of second stage nanofiltration membrane has reached national wastewater discharge standard and the discharge system; The concentrated solution of second stage nanofiltration membrane turns back to first step nanofiltration membrane again; So far the recycling of the useful thing that contains low-concentration perfluoro ammonium caprylate waste water and the clean of waste water have been finished.
Two, contain the low-concentration perfluoro ammonium caprylate wastewater treatment equipment:
The waste water storage tank is connected to from as clear as crystal the containing ammonium perfluorocaprylate waste water input tube, concentrate nanofiltration trapped fluid input tube and waste water output tube of centrifugal, output waste water is through water pump, first valve, liquid spinner-type flowmeter, insert from the foam separation top of tower, and liquid distributor is equipped with in the access tube end; The pressurized air of air compressor inserts buffering humidification jar through second valve, buffering humidification jar is divided into two the tunnel, one the tunnel through the 3rd valve, gas rotameter, insert from the foam separation tower bottom, the foam separation tower bottom is equipped with gas distribution grid, another road connects blow-off valve, be connected to froth breaker from foam separation top of tower fairlead, the 4th valve inserts the foam solution storage tank, the raffinate storage tank is connected to through the input tube of the 5th valve from the lower perfluoro ammonium caprylate aqueous solution of foam separating tower bottom concentration, raffinate output tube and concentrated nanofiltration trapped fluid input tube, output raffinate pipe connects the one-level nanofiltration membrane component through one-level nanofiltration membrane feedstock pump; The one-level nanofiltration membrane component is divided into two the tunnel, one tunnel the 6th valve through concentrated nanofiltration trapped fluid output tube connects the waste water storage tank, another Lu Jingdi seven valves, secondary nanofiltration membrane feedstock pump connect the secondary nanofiltration membrane component, the secondary nanofiltration membrane component is divided into two the tunnel, one the tunnel connects the raffinate storage tank through the 8th valve, and another Lu Jingdi nine valves connect waste water discharge opening.
The beneficial effect that the present invention has is: the method that nanofiltration and foam separation combine is handled the ammonium perfluorocaprylate waste water that contains lower concentration.Do not add any medicament in the wastewater treatment process, can not produce new pollution, reach zero release after the processing, and reclaim useful matter, all be in normal temperature in the treating processes, energy consumption is low.
Description of drawings
Accompanying drawing is to contain low-concentration perfluoro ammonium caprylate wastewater treatment process synoptic diagram.
Among the figure: 1. air compressor, 2. buffering humidification jar, 3. blow-off valve, 4. gas rotameter, 5. waste water storage tank, 6. water pump, 7. liquid spinner-type flowmeter, 8. gas distribution grid, 9. foam separating tower, 10. liquid distributor, 11. froth breakers, 12. foam solution storage tanks, 13. the raffinate storage tank, 14. one-level nanofiltration membrane feedstock pumps, 15. one-level nanofiltration membrane components, 16. secondary nanofiltration membrane feedstock pump, 17. secondary nanofiltration membrane components, 18. waste water discharge openings.
Embodiment
As shown in drawings, waste water storage tank 5 of the present invention is connected to from as clear as crystal the containing ammonium perfluorocaprylate waste water input tube, concentrate nanofiltration trapped fluid input tube and waste water output tube of centrifugal, output waste water is through water pump 6, first valve, liquid spinner-type flowmeter 7, insert from foam separating tower 9 tops, and liquid distributor 10 is equipped with in the access tube end; The pressurized air of air compressor 1 inserts buffering humidification jar 2 through second valve, buffering humidification jar 2 is divided into two the tunnel, one the tunnel through the 3rd valve, gas rotameter 4, insert from foam separating tower 9 bottoms, gas distribution grid 8 is equipped with in foam separating tower 9 bottoms, another road connects blow-off valve 3, be connected to froth breaker 11 from foam separating tower 9 top fairleads, the 4th valve inserts foam solution storage tank 12, raffinate storage tank 13 is connected to through the input tube of the 5th valve from the lower perfluoro ammonium caprylate aqueous solution of foam separating tower 9 bottom concentration, raffinate output tube and concentrated nanofiltration trapped fluid input tube, output raffinate pipe connects one-level nanofiltration membrane component 15 through one-level nanofiltration membrane feedstock pump 14; One-level nanofiltration membrane component 15 is divided into two the tunnel, one tunnel the 6th valve through concentrated nanofiltration trapped fluid output tube connects waste water storage tank 5, another Lu Jingdi seven valves, secondary nanofiltration membrane feedstock pump 16 connect secondary nanofiltration membrane component 17, secondary nanofiltration membrane component 17 is divided into two the tunnel, one the tunnel connects raffinate storage tank 13 through the 8th valve, and another Lu Jingdi nine valves connect waste water discharge opening 18.
As shown in drawings, technical process of the present invention and principle of work are as follows:
(1) at first waste water is filtered with ultracentrifuge, with solid particulate filtering wherein, obtain the as clear as crystal ammonium perfluorocaprylate waste water that contains, and waste water is transported in the waste water storage tank 5;
(2) use water pump 6 through liquid spinner-type flowmeters 7 waste water in the waste water storage tank 5, by liquid distributor 10 (aperture 0.1～5mm) ejection that is contained in the foam separating tower 9, after with compressor 1 air being compressed simultaneously, through buffering humidification jar 2, enter foam separating tower 9 bottoms after gas rotameter 4 meterings, (foam separation is carried out in aperture 0.05～2mm) ejection in foam separating tower 9 by gas distribution grid 8;
(3) foam overflows from foam separating tower 9 tops and enters froth breaker 11, obtains the high density perfluoro ammonium caprylate aqueous solution behind the foam froth breaking and enters foam solution storage tank 12, can turn back to utilize in the production again or further concentrate to obtain the solid ammonium perfluorocaprylate;
(4) flow out the lower perfluoro ammonium caprylate aqueous solution of concentration from foam separating tower 9 bottoms, enter raffinate storage tank 13;
(5) the low concentration perfluoro ammonium caprylate aqueous solution in the raffinate storage tank 13 is sent into one-level nanofiltration membrane component 15 with one-level nanofiltration membrane feedstock pump 14 and filter, nanofiltration trapped fluid (being concentrated solution) turns back in the waste water storage tank 5;
(6) liquid that sees through of one-level nanofiltration membrane component 15 is sent into secondary nanofiltration membrane component 17 with secondary nanofiltration membrane feedstock pump 16;
(7) the nanofiltration trapped fluid of secondary nanofiltration membrane component 17 (being concentrated solution) turns back in the raffinate storage tank 13;
(8) liquid that sees through of secondary nanofiltration membrane component 17 has reached national wastewater discharge standard and the discharge system.
The recycling of the useful thing that contains low-concentration perfluoro ammonium caprylate waste water and the clean of waste water have been finished by above-mentioned 8 steps.
Claims (2)
1, contain the low-concentration perfluoro ammonium caprylate method of wastewater treatment, it is characterized in that the step of this method is as follows:
(1) at first waste water is filtered with ultracentrifuge,, obtain the as clear as crystal ammonium perfluorocaprylate waste water that contains solid particulate filtering wherein;
(2) waste water is pumped into foam separating tower and carry out foam separation, obtain the high density perfluoro ammonium caprylate aqueous solution behind the cat head foam froth breaking, can turn back in the production and utilize again; Obtain the lower perfluoro ammonium caprylate aqueous solution of concentration at the bottom of the tower;
(3) perfluoro ammonium caprylate aqueous solution of discharging at the bottom of the foam separation Tata is filtered with first step nanofiltration membrane, the nanofiltration trapped fluid, promptly concentrated solution turns back to foam separating tower and carries out foam separation again; The liquid that sees through of first step nanofiltration membrane enters second stage nanofiltration membrane;
(4) liquid that sees through of second stage nanofiltration membrane has reached national wastewater discharge standard and the discharge system; The concentrated solution of second stage nanofiltration membrane turns back to first step nanofiltration membrane again; So far the recycling of the useful thing that contains low-concentration perfluoro ammonium caprylate waste water and the clean of waste water have been finished.
2, contain the low-concentration perfluoro ammonium caprylate wastewater treatment equipment, it is characterized in that: waste water storage tank (5) is connected to from as clear as crystal the containing ammonium perfluorocaprylate waste water input tube, concentrate nanofiltration trapped fluid input tube and waste water output tube of centrifugal, output waste water is through water pump (6), first valve, liquid spinner-type flowmeter (7), insert from foam separating tower (9) top, and liquid distributor (10) is equipped with in the access tube end.The pressurized air of air compressor (1) inserts through second valve and cushions humidification jar (2), buffering humidification jar (2) is divided into two the tunnel, one the tunnel through the 3rd valve, gas rotameter (4), insert from foam separating tower (9) bottom, gas distribution grid (8) is equipped with in foam separating tower (9) bottom, and another road connects blow-off valve (3).Be connected to froth breaker (11), the 4th valve access foam solution storage tank (12) from foam separating tower (9) top fairlead, raffinate storage tank (13) is connected to through input tube, raffinate output tube and the concentrated nanofiltration trapped fluid input tube of the 5th valve from the lower perfluoro ammonium caprylate aqueous solution of foam separating tower (9) bottom concentration, and output raffinate pipe connects one-level nanofiltration membrane component (15) through one-level nanofiltration membrane feedstock pump (14); One-level nanofiltration membrane component (15) is divided into two the tunnel, one tunnel the 6th valve through concentrated nanofiltration trapped fluid output tube connects waste water storage tank (5), another Lu Jingdi seven valves, secondary nanofiltration membrane feedstock pump (16) connect secondary nanofiltration membrane component (17), secondary nanofiltration membrane component (17) is divided into two the tunnel, one the tunnel connects raffinate storage tank (13) through the 8th valve, and another Lu Jingdi nine valves connect waste water discharge opening (18).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2007100693274A CN100522835C (en) | 2007-06-15 | 2007-06-15 | Method and apparatus for treating waste water containing low-concentration perfluoro ammonium caprylate |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2007100693274A CN100522835C (en) | 2007-06-15 | 2007-06-15 | Method and apparatus for treating waste water containing low-concentration perfluoro ammonium caprylate |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN101070204A true CN101070204A (en) | 2007-11-14 |
| CN100522835C CN100522835C (en) | 2009-08-05 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB2007100693274A Expired - Fee Related CN100522835C (en) | 2007-06-15 | 2007-06-15 | Method and apparatus for treating waste water containing low-concentration perfluoro ammonium caprylate |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN100522835C (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101716464B (en) * | 2009-11-09 | 2011-11-09 | 浙江大学 | Method and device for separating surfactant from dilute solution |
| CN104583135A (en) * | 2012-08-17 | 2015-04-29 | 纳幕尔杜邦公司 | Treating wastewater by ultrafiltration in fluoropolymer resin manufacture |
| CN110026087A (en) * | 2019-05-30 | 2019-07-19 | 岭东核电有限公司 | Remaining waste processing system and its control method in membrane module |
| CN110342728A (en) * | 2019-05-10 | 2019-10-18 | 江苏智诚达环保科技有限公司 | A kind of method that micro-nano air bearing coupling electroxidation device removes perfluorochemical in waste water |
| EP3738674A1 (en) * | 2019-05-17 | 2020-11-18 | Björks Rostfria Aktiebolag | Apparatus, system and methods for water processing |
| CN113087062A (en) * | 2021-05-25 | 2021-07-09 | 中国人民解放军海军勤务学院 | Process for treating surfactant wastewater by adopting foam separation tower |
| US11447401B1 (en) | 2019-05-06 | 2022-09-20 | Arrowhead Center, Inc. | Separation columns for per- and polyfluoroalkyl substances (PFAS) remediation |
-
2007
- 2007-06-15 CN CNB2007100693274A patent/CN100522835C/en not_active Expired - Fee Related
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101716464B (en) * | 2009-11-09 | 2011-11-09 | 浙江大学 | Method and device for separating surfactant from dilute solution |
| CN104583135A (en) * | 2012-08-17 | 2015-04-29 | 纳幕尔杜邦公司 | Treating wastewater by ultrafiltration in fluoropolymer resin manufacture |
| US11447401B1 (en) | 2019-05-06 | 2022-09-20 | Arrowhead Center, Inc. | Separation columns for per- and polyfluoroalkyl substances (PFAS) remediation |
| CN110342728A (en) * | 2019-05-10 | 2019-10-18 | 江苏智诚达环保科技有限公司 | A kind of method that micro-nano air bearing coupling electroxidation device removes perfluorochemical in waste water |
| EP3738674A1 (en) * | 2019-05-17 | 2020-11-18 | Björks Rostfria Aktiebolag | Apparatus, system and methods for water processing |
| SE543716C2 (en) * | 2019-05-17 | 2021-06-29 | Bjoerks Rostfria Ab | Apparatus, system and methods for water processing |
| CN110026087A (en) * | 2019-05-30 | 2019-07-19 | 岭东核电有限公司 | Remaining waste processing system and its control method in membrane module |
| CN113087062A (en) * | 2021-05-25 | 2021-07-09 | 中国人民解放军海军勤务学院 | Process for treating surfactant wastewater by adopting foam separation tower |
Also Published As
| Publication number | Publication date |
|---|---|
| CN100522835C (en) | 2009-08-05 |
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Granted publication date: 20090805 Termination date: 20120615 |