CN101781056B - Treatment method of waste papermaking water - Google Patents
Treatment method of waste papermaking water Download PDFInfo
- Publication number
- CN101781056B CN101781056B CN2009100012703A CN200910001270A CN101781056B CN 101781056 B CN101781056 B CN 101781056B CN 2009100012703 A CN2009100012703 A CN 2009100012703A CN 200910001270 A CN200910001270 A CN 200910001270A CN 101781056 B CN101781056 B CN 101781056B
- Authority
- CN
- China
- Prior art keywords
- section
- water
- treatment
- sludge
- mud
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
- 238000000034 method Methods 0.000 title claims abstract description 107
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 81
- 229910001868 water Inorganic materials 0.000 title claims abstract description 81
- 239000002699 waste material Substances 0.000 title abstract 3
- 230000008569 process Effects 0.000 claims abstract description 62
- 238000005189 flocculation Methods 0.000 claims abstract description 27
- 230000016615 flocculation Effects 0.000 claims abstract description 25
- 239000010802 sludge Substances 0.000 claims description 68
- 238000005516 engineering process Methods 0.000 claims description 35
- 238000005273 aeration Methods 0.000 claims description 28
- 238000006243 chemical reaction Methods 0.000 claims description 25
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 22
- 239000001301 oxygen Substances 0.000 claims description 22
- 229910052760 oxygen Inorganic materials 0.000 claims description 22
- 241000894006 Bacteria Species 0.000 claims description 21
- 238000009826 distribution Methods 0.000 claims description 15
- 239000013049 sediment Substances 0.000 claims description 12
- 238000010992 reflux Methods 0.000 claims description 9
- 230000001580 bacterial effect Effects 0.000 claims description 7
- 239000011259 mixed solution Substances 0.000 claims description 6
- 238000005276 aerator Methods 0.000 claims description 4
- 241001148470 aerobic bacillus Species 0.000 claims description 4
- 238000001471 micro-filtration Methods 0.000 claims description 4
- 150000001875 compounds Chemical class 0.000 claims description 3
- 241001148471 unidentified anaerobic bacterium Species 0.000 claims description 3
- 239000002351 wastewater Substances 0.000 abstract description 44
- 230000000694 effects Effects 0.000 abstract description 29
- 238000001914 filtration Methods 0.000 abstract description 10
- 238000004062 sedimentation Methods 0.000 abstract description 5
- 239000000126 substance Substances 0.000 description 23
- 238000012545 processing Methods 0.000 description 18
- 239000010893 paper waste Substances 0.000 description 13
- 238000011068 loading method Methods 0.000 description 12
- 230000015556 catabolic process Effects 0.000 description 11
- 239000003795 chemical substances by application Substances 0.000 description 11
- 238000006731 degradation reaction Methods 0.000 description 11
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 8
- 230000007062 hydrolysis Effects 0.000 description 8
- 238000006460 hydrolysis reaction Methods 0.000 description 8
- 239000012528 membrane Substances 0.000 description 8
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 8
- 239000010865 sewage Substances 0.000 description 7
- 238000004065 wastewater treatment Methods 0.000 description 7
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 6
- 238000004537 pulping Methods 0.000 description 6
- 238000000108 ultra-filtration Methods 0.000 description 6
- 238000010521 absorption reaction Methods 0.000 description 5
- 235000011089 carbon dioxide Nutrition 0.000 description 5
- 239000007789 gas Substances 0.000 description 5
- 230000001965 increasing effect Effects 0.000 description 5
- 238000006396 nitration reaction Methods 0.000 description 5
- 230000000050 nutritive effect Effects 0.000 description 5
- 238000001223 reverse osmosis Methods 0.000 description 5
- 238000001179 sorption measurement Methods 0.000 description 5
- QTBSBXVTEAMEQO-UHFFFAOYSA-M Acetate Chemical compound CC([O-])=O QTBSBXVTEAMEQO-UHFFFAOYSA-M 0.000 description 4
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- 239000000701 coagulant Substances 0.000 description 4
- -1 compound aluminum chloride Chemical class 0.000 description 4
- 150000002823 nitrates Chemical class 0.000 description 4
- 229910052757 nitrogen Inorganic materials 0.000 description 4
- 238000007254 oxidation reaction Methods 0.000 description 4
- 150000003839 salts Chemical class 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- IOVCWXUNBOPUCH-UHFFFAOYSA-M Nitrite anion Chemical compound [O-]N=O IOVCWXUNBOPUCH-UHFFFAOYSA-M 0.000 description 3
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 3
- 239000002253 acid Substances 0.000 description 3
- 230000009471 action Effects 0.000 description 3
- 230000000274 adsorptive effect Effects 0.000 description 3
- 229910021529 ammonia Inorganic materials 0.000 description 3
- 239000000920 calcium hydroxide Substances 0.000 description 3
- 235000011116 calcium hydroxide Nutrition 0.000 description 3
- 229910052799 carbon Inorganic materials 0.000 description 3
- 230000008859 change Effects 0.000 description 3
- 239000002131 composite material Substances 0.000 description 3
- 238000013461 design Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 238000007599 discharging Methods 0.000 description 3
- 230000007613 environmental effect Effects 0.000 description 3
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 230000003647 oxidation Effects 0.000 description 3
- 239000001814 pectin Substances 0.000 description 3
- 229920001277 pectin Polymers 0.000 description 3
- 235000010987 pectin Nutrition 0.000 description 3
- 229910052698 phosphorus Inorganic materials 0.000 description 3
- 239000011574 phosphorus Substances 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- 239000010902 straw Substances 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
- 241000108664 Nitrobacteria Species 0.000 description 2
- 238000005842 biochemical reaction Methods 0.000 description 2
- 230000033228 biological regulation Effects 0.000 description 2
- BVKZGUZCCUSVTD-UHFFFAOYSA-N carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 description 2
- 239000001913 cellulose Substances 0.000 description 2
- 229920002678 cellulose Polymers 0.000 description 2
- 235000013339 cereals Nutrition 0.000 description 2
- 238000005345 coagulation Methods 0.000 description 2
- 230000015271 coagulation Effects 0.000 description 2
- 239000003245 coal Substances 0.000 description 2
- 230000001276 controlling effect Effects 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 239000003344 environmental pollutant Substances 0.000 description 2
- 239000000835 fiber Substances 0.000 description 2
- 239000008103 glucose Substances 0.000 description 2
- 239000008187 granular material Substances 0.000 description 2
- 239000010842 industrial wastewater Substances 0.000 description 2
- 229920005610 lignin Polymers 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- BDAGIHXWWSANSR-UHFFFAOYSA-N methanoic acid Natural products OC=O BDAGIHXWWSANSR-UHFFFAOYSA-N 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 239000005416 organic matter Substances 0.000 description 2
- 230000020477 pH reduction Effects 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 150000002978 peroxides Chemical class 0.000 description 2
- 231100000719 pollutant Toxicity 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 230000035484 reaction time Effects 0.000 description 2
- 230000001105 regulatory effect Effects 0.000 description 2
- 230000000630 rising effect Effects 0.000 description 2
- 239000002002 slurry Substances 0.000 description 2
- 150000003384 small molecules Chemical class 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 230000004083 survival effect Effects 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- 238000012546 transfer Methods 0.000 description 2
- OSWFIVFLDKOXQC-UHFFFAOYSA-N 4-(3-methoxyphenyl)aniline Chemical compound COC1=CC=CC(C=2C=CC(N)=CC=2)=C1 OSWFIVFLDKOXQC-UHFFFAOYSA-N 0.000 description 1
- 108010059892 Cellulase Proteins 0.000 description 1
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- 108090000790 Enzymes Proteins 0.000 description 1
- 102000004190 Enzymes Human genes 0.000 description 1
- 241001465754 Metazoa Species 0.000 description 1
- 241001495402 Nitrococcus Species 0.000 description 1
- 239000004677 Nylon Substances 0.000 description 1
- 240000007594 Oryza sativa Species 0.000 description 1
- 235000007164 Oryza sativa Nutrition 0.000 description 1
- 206010033799 Paralysis Diseases 0.000 description 1
- 229920001131 Pulp (paper) Polymers 0.000 description 1
- 229920002472 Starch Polymers 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 241000209140 Triticum Species 0.000 description 1
- 235000021307 Triticum Nutrition 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- 159000000013 aluminium salts Chemical class 0.000 description 1
- 229910000329 aluminium sulfate Inorganic materials 0.000 description 1
- VSCWAEJMTAWNJL-UHFFFAOYSA-K aluminum chloride Substances Cl[Al](Cl)Cl VSCWAEJMTAWNJL-UHFFFAOYSA-K 0.000 description 1
- 230000008953 bacterial degradation Effects 0.000 description 1
- 239000002585 base Substances 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- WQZGKKKJIJFFOK-VFUOTHLCSA-N beta-D-glucose Chemical compound OC[C@H]1O[C@@H](O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-VFUOTHLCSA-N 0.000 description 1
- 230000003851 biochemical process Effects 0.000 description 1
- 238000010170 biological method Methods 0.000 description 1
- 150000007516 brønsted-lowry acids Chemical class 0.000 description 1
- 150000007528 brønsted-lowry bases Chemical class 0.000 description 1
- 150000001720 carbohydrates Chemical class 0.000 description 1
- 235000014633 carbohydrates Nutrition 0.000 description 1
- 125000001547 cellobiose group Chemical group 0.000 description 1
- 229940106157 cellulase Drugs 0.000 description 1
- 239000013043 chemical agent Substances 0.000 description 1
- 238000009388 chemical precipitation Methods 0.000 description 1
- 239000004927 clay Substances 0.000 description 1
- 230000001112 coagulating effect Effects 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000005261 decarburization Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000005202 decontamination Methods 0.000 description 1
- 230000003588 decontaminative effect Effects 0.000 description 1
- 239000007857 degradation product Substances 0.000 description 1
- 238000011033 desalting Methods 0.000 description 1
- 235000014113 dietary fatty acids Nutrition 0.000 description 1
- 230000029087 digestion Effects 0.000 description 1
- 229910001882 dioxygen Inorganic materials 0.000 description 1
- 150000002016 disaccharides Chemical class 0.000 description 1
- 239000005446 dissolved organic matter Substances 0.000 description 1
- 238000000909 electrodialysis Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 229940088598 enzyme Drugs 0.000 description 1
- 235000019441 ethanol Nutrition 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000009293 extended aeration Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000000194 fatty acid Substances 0.000 description 1
- 229930195729 fatty acid Natural products 0.000 description 1
- 150000004665 fatty acids Chemical class 0.000 description 1
- 238000000855 fermentation Methods 0.000 description 1
- 230000004151 fermentation Effects 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 235000019253 formic acid Nutrition 0.000 description 1
- 150000004676 glycans Chemical class 0.000 description 1
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 125000004435 hydrogen atom Chemical class [H]* 0.000 description 1
- 239000000413 hydrolysate Substances 0.000 description 1
- 230000003301 hydrolyzing effect Effects 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000008235 industrial water Substances 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 238000005342 ion exchange Methods 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- RBTARNINKXHZNM-UHFFFAOYSA-K iron trichloride Chemical compound Cl[Fe](Cl)Cl RBTARNINKXHZNM-UHFFFAOYSA-K 0.000 description 1
- 238000005304 joining Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 230000002503 metabolic effect Effects 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 235000010755 mineral Nutrition 0.000 description 1
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 description 1
- 229920001778 nylon Polymers 0.000 description 1
- 238000005457 optimization Methods 0.000 description 1
- 230000008520 organization Effects 0.000 description 1
- 239000002957 persistent organic pollutant Substances 0.000 description 1
- 239000000049 pigment Substances 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 229920001282 polysaccharide Polymers 0.000 description 1
- 239000005017 polysaccharide Substances 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 239000012716 precipitator Substances 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 235000009566 rice Nutrition 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 238000012216 screening Methods 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 241000894007 species Species 0.000 description 1
- 235000019698 starch Nutrition 0.000 description 1
- 239000008107 starch Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 238000005728 strengthening Methods 0.000 description 1
- 239000006228 supernatant Substances 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
Images
Landscapes
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
The invention relates to a treatment method of waste papermaking water, which comprises the steps of filtration, flocculation and sedimentation, QA2O treatment and deep treatment. Because the QA2O treatment process is adopted in the treatment method of the invention for replacing the conventional biochemical treatment method, the treatment cost is greatly reduced, in addition, the treatment effect is perfect, and the technical process is simple and can be implemented easily. The method of the invention can be used for treating various kinds of waste papermaking water, particularly the middle section waste water with high load. The waste water treated by the method of the invention can reach the national specified discharge standard, or can be reused in the papermaking process.
Description
Technical field
The present invention relates to a kind of technological process of treating papermaking method, particularly relate to a kind of purifying treatment method of papermaking midcourse wastewater.
Background technology
The whole process of production of pulp and paper industry needs a large amount of water; These water have compiled a large amount of industrial objectionable impuritiess in process of production, both can't directly utilize, and directly discharging pollutes the environment again; Therefore; The waste water that each stage of pulping and papermaking processes is produced carries out recycling, and remarkable economical and social value are arranged, and is determining the survival and development of papermaking enterprise.
In paper industry, adopt treatment process centering water such as chemical precipitation, air supporting processing and bio-oxidation to handle usually.
Papermaking environmental protection one-level processing traditional technology is just heavy or materialization flocculation sediment at present; The flocculation process clearance is higher; Especially can remove the organic pollutant of a large amount of polymer difficult degradations; This lays a good foundation for next step carries out biochemical treatment, yet such processing is only applicable to the lower waste water of loading.European countries are the most advanced on materialization is handled, and eliminated horizontal sedimentation tank basically, adopt the advanced precipitation technology of plusator, sludge blanket clarifier and highly dense settling pond or the like.
Microbial film ultra-filtration technique, r-o-, electrodialysis, ion exchange treatment means constantly occur in recent years.In paper industry, because processing cost is too high, owing to the paper waste complicated component, the treatment technology difficulty is very big, therefore, does not still have industrialized ripe treatment technology to use so far on the other hand on the one hand.
For example, CN101186418A has disclosed a kind of recoverying and utilizing method of paper-making industrial waste water, and this method combines membrane technique and Treatment of Industrial Water technology, and concrete grammar comprises: micro-filtration process section, ultrafiltration technology section and reverse osmosis membrane process section.Because before the micro-filtration process section, need at first carry out biochemical treatment, the ultrafiltration technology section need adopt ultra-filtration membrane, the reverse osmosis process section need adopt reverse osmosis membrane.Therefore, cost of water treatment is too high, and in addition, the requirement to water in the implementation process of this method is quite strict, therefore, for the paper waste complicated component is changeable, is difficult to industriallization.
CN1255340C has disclosed the decoloring method of water in a kind of papermaking, adopts oxygen, dioxide peroxide, and flocculation agent handles the middle water through biochemical treatment respectively, with obtain can reuse purify waste water.Yet this method need be used dioxide peroxide, itself is exactly a kind of chemical agent of forbidding gradually at present.This method needs long sedimentation, long processing period in addition.
CN101050044A has disclosed and a kind of papermaking wastewater has been carried out the method for advanced treatment, comprises chemical coagulation, gravitational settling, and composite filtering material filters, and the biological adsorption agent absorption degradation purifies or the oxygenant oxidation, etc. step.Wherein chemical coagulation has adopted traditional flocculation agent such as aluminium salt and/or molysite, and SEPIGEL 305 (PAM).Owing to do not carry out desalting treatment, therefore, increased the composite filtering material filtration in this method; And purification of biological adsorption agent absorption degradation or oxygenant oxidation, not only increased processing cost, but also made complex disposal processization; Operability variation in implementation process, treatment effect is undesirable.
CN1203231C has disclosed a kind of method of papermaking straw pulp WWT, comprises that interpolation flocculation agent (compound aluminum chloride) and coagulant aids (SEPIGEL 305) carry out flocculation sediment and handle, and carries out air supporting then and handles, and clear water directly discharges or reuse.Because soluble salt content is very high in the waste water, adopts simple flocculation sediment not remove, therefore, certainly, the middle water of handling through this method does not reach the direct discharging of present national regulation or the standard of reuse.
CN100357191C has disclosed the decoloring method of water in a kind of papermaking, comprises adding white clay and flocculation agent among the Xiang Zhongshui, adsorbs to reach through slag then and reduces the COD and the purpose of decolouring.This method is not still handled water-soluble salts a large amount of in the waste water, therefore, is difficult to reach the emission standards of present national regulation.
CN1057512C has disclosed a kind of improvement method of paper waste, comprises adding acidifying to isolate xylogen; Utilize coal grain and iron dust filtration organism and solid particulate; Add milk of lime and carry out flocculation sediment; Adding flocculation agent again carries out flocculation sediment with milk of lime and separates.Because black liquor and middle water are mixed, therefore, this method needs a large amount of acid to carry out the acidifying separating lignin, has lost a large amount of bronsted lowry acids and bases bronsted lowries artificially.In addition, used a large amount of coal grain and iron filings, and milk of lime, with producing a large amount of secondary pollutions.Moreover, owing to water-soluble salt is not wherein handled, make final process result undesirable, be difficult to reach national specified discharge standard.
In the above-mentioned prior art, quite a few adopts simple flocculation sediment to handle, and isolates throw out then; Clear water directly discharges or reuse; Still can use for the lower waste water of load, higher for load, for example; By the middle-stage wastewater that pulping process of straw pulp produces, above-mentioned treatment process is difficult to reach national specified discharge standard.Also have some treatment processs to adopt flocculation sediments, (biology) adsorption filtration, or the like step, will produce a large amount of secondary pollutions in the treating processes, in addition, treating processes is too complicated, therefore, cost will improve greatly.The prior art that has has adopted ultrafiltration membrane technique and reverse osmosis membrane to combine with conventional method of wastewater treatment, in theory should thoroughly decontamination problem.But owing to the cost reason; And technical reason; Be that the papermaking midcourse wastewater complicated component is changeable, on Processing Paper Wastewater, not only brought the high problem of cost for ultrafiltration membrane technique and reverse osmosis membrane technology, technical meeting runs into beyond thought trouble when handling but also make.Therefore, it is high to solve the cost that exists in the prior art, and the processing means are complicated, cause serious secondary pollution problem again, is the cardinal task that current paper waste is handled, and can paper waste be handled and accomplished smoothly, determined the survival and development of papermaking enterprise.
Summary of the invention
To the problems referred to above of prior art, the inventor has accomplished the present invention through concentrating on studies.Promptly the present invention proposes and a kind ofly can reduce processing cost effectively, simplify technological process greatly, and can handle various paper wastes, the particularly treatment process of high loading middle-stage wastewater.
Specifically, the invention provides a kind of technological process of treating papermaking method, comprising: filter, flocculation sediment, biochemical treatment and advanced treatment step is characterized in that, QA is adopted in biochemical treatment
2The O treatment process.
Wherein, described QA
2The O treatment process comprises complex reaction aeration, the multistage AO aeration of time-delay and pulse water distribution upwelling anaerobic reaction.
In addition, treatment process of the present invention also comprises handling the advanced treatment step of waste water.
In addition, the said micro-filtration that is filtered into, the order number of filter screen is from the 80-120 order.
Also comprise in addition QA
2The mud that O produces carries out sludge dewatering treatment.
QA
2O mainly comprises three sections of A1, A2, O; But bigger with traditional A2O process distinction, because of its A1, A2, three sections independent settings of O, and every section is respectively A1 (complex reaction aeration tank), A2 (pulse water distribution upwelling anaerobic reactor), O (the multistage AO aeration tank of delaying time); This technology has the removal ability of pollutents such as extremely strong SS, COD, BOD; The circulation of traditional A2O mud all runs through whole technology, and the Aerobic Pond mixed solution circulates in A2 section and O section in a large number, and main purpose is the realization denitrogenation dephosphorizing.
1, technical process contrast
QA2O technology: see Fig. 2 for details
Tradition A2O technology: see Fig. 3 for details
Can find out that by above-mentioned two artworks QA2O technology and traditional A2O process distinction are bigger; Mud is circulation in three sections of A1, A2, O in traditional A2O technology; Settling tank is not established in the centre, and the mixed solution circulation is arranged in that A2, O two are intersegmental, and A1 is that anaerobism A2 is that the oxygen O that holds concurrently is aerobic in these three sections.The A1 section is main with the oxygen bacterium of holding concurrently in QA2O technology, met physical reaction again simultaneously, and this section is provided with settling tank separately; The independently mud recycle system is arranged, and the A2 section is main with obligatory anaerobic bacteria, is anaerobic technique completely; The independently mixed solution recycle system is arranged, do not rely on A1 and O section mud and reflux, the O section is main with aerobic bacteria then; Alternately oxygen supply through aerator realizes that the series connection of a plurality of oxygen enrichment anoxic sections is multistage AO, and the biological pond of selecting is set before the O section, to reach the purpose of optimizing bacterial classification.
This technology mainly contains five effects greatly: remove SS, denitrogenation, dephosphorization, raising biodegradability, degraded COD and BOD.
(1) is main in the A1 section to remove SS, the nitration denitrification reaction takes place simultaneously, realize denitrification dephosphorization function (seeing complex reaction aeration tank part for details)
(2) be main mainly in the A2 section, play the effect that certain larger molecular organics chain rupture is decomposed into small organic molecule again simultaneously, improved the clearance of follow-up O section, and realize the release of phosphorus with anaerobic digestion.(seeing acoustic streaming anaerobic reactor part on the pulse water distribution for details).
(3) then bring into play the advantage of aerobic bacteria fully in the O section, and realize that simultaneously multistage AO alternately, makes mikrobe have more activity, to reach higher removal efficient.Under the time-delay underload, move for a long time in addition and generated a large amount of aerobic particle muds.
The complex reaction aeration tank
The complex reaction aeration tank is the A1 section in this technology.
The selection of waste water treatment process is directly connected to effect, running cost and the total investment of engineering of wastewater treatment, so the suitable waste water treatment process of careful selection is the key of this engineering.The selection of waste water treatment process should be taken all factors into consideration according to multiple factors such as design Inlet and outlet water water quality, degree of treatment requirement, floor space, project scales, and various technologies all have its applicable elements, should fit actual conditions and decides.
China's pulp and paper industry output has occupied the third place in the world, and paper technology upgrades day by day.The paper-making industrial waste water quantity discharged is big, and is seriously polluted, and ecological damage property is big, is puzzlement countries in the world paper industry and the hot issue of environmental protection organization and the emphasis of research for many years always.My company furthers investigate paper waste from putting into practice the angle of practical applications, has developed the feasible suitable process program of a cover.
The waste water of papermaking enterprise discharging mainly contains middle-stage wastewater and paper machine white water.Plain boiled water can be handled all or part of slurrying workshop section that is back in back; Middle section water is mainly from the waste water that produces in pulping, screening, the floatation process; Its staple is tiny suspension fiber, papermaking filler, waste paper impurity and a small amount of pectin, wax, carbohydrate, and all kinds of organic and mineral compound that adds in the paper process.The characteristics of waste water are that SS and COD are all higher; And non-solubility COD is higher, accounts for more than 60%; When SS is removed, but non-dissolubility COD simultaneously also major part be lowered.The ratio of B/C in the paper waste is generally not high, but most BOD and solubility COD also want the applying biological method to remove, and is more hard to manage.
And confirm to adopt combined chemistry reaction aeration tank-precipitator method (QA at last through test in place repeatedly
2The A of O technology
1Section) as pre-treating technology, can obtain good ss, cod treatment effect.
One, this technology is the novel technique that biological absorption-degrading activity mud method combines with the materialization flocculation reaction; Be in the conventional activated sludge method, (the AB method is the absorption biological degradation method for two sections activated sludge processes, materialization flocculence, AB methods; Form by A section B section two portions; The A section is main with bacterium absorption propagation, belongs to the high loading biochemical processing process, and the B section can be traditional aerobic biological treatment process) the basis on the sewage treatment process that grows up.This technology belongs to the high loading activated sludge process, and sewage is introduced into the A1 section of high loading, and then gets into the A2 section of low anaerobism load, is getting into the series operation of ultra-low load O section.A1 section mud has very strong adsorptive power and good sedimentation function.The A1 section is that flocculation adsorption with bacterium is main to organic removal, with materialization flocculation adsorption as strengthening and replenishing.A1 segment process sludge loading height, mud age and hydraulic detention time are short, so the investment of A segment process and working cost are low, the enhanced primary that belongs to the high loading Sludge System is handled.This technology has following characteristics in paper waste is handled:
(1) capacity of resisting impact load is strong, and water quality, the water yield of intaking had huge self-regulated ability, can not make the treatment system paralysis because of the rapid variation of water quality and quantity, stop transport, and loses processing power; When coming water water-quality COD, SS by normal variation water quality to 2 times, water outlet still can keep higher clearance even higher clearance, if in time adjust operating parameter even can keep effluent quality constant, or slightly raises.Strong like this anti impulsion load is for the steady running of whole integrated technique provides assurance.
(2) mud has very strong adsorptive power and good sedimentation function, and process sludge load height reaches as high as 7kg/kgmlss.d, mud age and the water conservancy residence time short (30min-60min), and investment and working cost are low, clearance high (40%-65%).
(3) used technology has bigger biochemical reaction impellent, has stronger adsorption-flocculation and decomposing oxidation to improve the biodegradability ability to the pollution substance of difficult for biological degradation in the paper waste; Because this pond is to be main with the oxygen bacterium of holding concurrently with aerobic bacteria, especially double oxygen effect makes waste water B:C behind this pond can improve 2%-5%.
(4) transfer efficiency of oxygen is higher, saves aeration energy consumption; Move owing to adopt under the LDO condition, this has just improved gas-liquid mass transfer efficient greatly, uses coefficient of oxygen utilization to improve greatly, can use dissolved oxygen efficiency to reach more than 40%, and dynamicefficiency reaches more than 4.
(5) technical process is simple, and structures are few, simple and convenient operation and maintenance;
(6) treatment effect is stable;
(7) biochemistry is combined with materialization, obtain higher removal efficient and more stable effect of settling.
Commercially available aerator commonly used can be adopted in the complex reaction aeration tank, is conspicuous to those skilled in the art for equipments choice, need not to make creative work.
A large amount of mikrobe (bacterium) is generally all surviving in the waste water; These bacterial growth reproduction speeds are very fast, can realize a generation cycle in general 20 minutes, that is to say one day and can breed for 72 generations; And the general vitality of these bacteriums is more intense, and is not high to environmental requirement.Can utilize the excess sludge of aerobic activated sludge to improve concentration and the population density of mikrobe such as bacterium and primary metazoan in the aeration tank in addition, to reach high efficiency operation.
Three, processing parameter
After waste water entered into the complex reaction aeration tank, this pond main control parameters was following:
Flow Q=MAX120000M
3/ d
Temperature T=20-35 ℃
Hydraulic detention time HTR=30min-60min
Sludge concentration MLSS=3000-10000mg/L
Dissolved oxygen DO=0.1-1.0
Ph＝6-8
30 fens SV of settling ratio
30=30-90
Sludge index SVI=150-350
Sludge age SRT=20-40min
Reflux ratio R=40%-200%
Through behind the aeration, get into the settling tank precipitate and separate, for example between aeration tank and settling tank, adding in right amount according to separating effect, PAM regulates.Before getting into the complex reaction aeration tank, for example can add PAC commonly used.In the operational process of settling tank, must control sludge interface, surface load and reflux ratio.Belong to the scope of conventional design for these parameter control, those of ordinary skills can carry out suitable adjusting according to the particular case of waste water.Usually, sludge interface is suitable to be controlled at more than 3 meters, and surface load should be lower than 1.2m
3/ m
2.h, reflux ratio is controlled according to sludge interface and excess sludge output.Can improve the service efficiency of settling tank like this, improve sludge loading and also increased removal efficient simultaneously.
This technology is compound physical-chemical reaction and biochemical reaction makes the flco density, adsorptive power etc. of physical reaction obtain great enhancing, and the settleability that has promoted biochemical action is arranged simultaneously, makes it be easier to mud-water separation, is that water outlet is more clear.
Pulse water distribution upwelling anaerobic reactor
This reactor drum is the A2 section in the QA2O technology, is main with anaerobic reaction mainly, and sewage is in this section, and main hydrolytic reactions, fermentative acidification react, produce acetic acidreaction and methanation reaction.
One, this reactor drum principal feature has:
1, without triphase separator.This is one of maximum difference of this anaerobic reactor and conventional reactors, through bigger diameter/height ratio (5: 1), has reduced the flow velocity of waste water, thereby has reached the purpose of solid-liquid separation.
2, adopt the pulse water distribution system; Through syphonic effect with having stored in the water distributor 3～5 minutes A1 section water outlet rushes at the pond with very fast flow velocity in the short period of time (several seconds to tens seconds) at the bottom of; Upwards dash the sludge blanket at the bottom of the pond and to be suspended state; Thereby make the muddy water uniform mixing in the pond, guaranteed the efficient of anaerobic reaction.
3, be particularly useful for (but being not limited only to) wheat straw chemical pulp middle-stage wastewater.Mierocrystalline cellulose in this waste water, semicellulose, polysaccharide, reducing sugar, treated starch, part lignin and the verivate thereof etc. of joining in the coating waste-water there is good specific aim; Well brought into play acidication these macromole size degradations have been become small molecules, for follow-up aerobic treatment creates conditions.
4, anerobes is granule sludge and floc sludge.Because diameter is too small, flow velocity is high mostly for the tradition anaerobism, and it is serious to make floc sludge run off; And be main to cultivate the prilling anaerobic sludge, this reactor drum then can make the coexistence of granule sludge and floc sludge, acts on simultaneously; To reach higher removal effect, also improved the removal ability of ss simultaneously.
5, single pond processing power is big, owing to adopt big blade diameter length ratio, makes single pond processing power improve greatly.
This reactor drum mainly be with the organism in the waste water under the acting in conjunction of a large amount of mikrobes; Be converted into methane, carbonic acid gas, water, hydrogen sulfide and ammonia; Different anerobess, the oxygen bacterium of holding concurrently interact, condition each other in this process, are very complicated coenosiss.The process of its degradation of organic substances can be divided into four sections:
1, the macromolecular organism of hydrolysis stage is decomposed into small molecules in this stage by the bacterium extracellular enzyme, is chain rupture, and micromolecular hydrolysate is easy to dissolving.For example: the Mierocrystalline cellulose in this stage paper waste is cellobiose, glucose etc. by cellulase hydrolysis; Pectin and degradation product thereof be by the pectin enzymic hydrolysis, and then better degraded by bacterium.
2, souring stage is converted into voltaile fatty acid, alcohols, carbonic acid gas, hydrogen, ammonia, hydrogen sulfide etc. by dissolved organic matter such as disaccharides, the glucose etc. that hydrolysis section generates under the effect of fermenting bacterial.
3, produce the acetate stage under the effect of acetogen, the product of souring stage is converted into acetate, hydrogen, carbonic acid gas and other new cell etc.
4, produce methane phase under the effect of methanogen, acetate, hydrogen, carbonic acid, formic acid, methyl alcohol etc. are converted into methane, carbonic acid gas, new cell etc.Thereby reach the purpose of degradation of organic substances.
After waste water was handled through the A1 section, the proportioning through adjustment C: N: P for example was adjusted to 200: 5: 1, flows automatically to the A2 section, gets into the for example about 300m of volume
3The pulse water distribution jar, the pulse water distribution device water distribution cycle is 8 minutes, the pulse water distribution device was accomplished a water-filling water distribution process in promptly per 8 minutes; Waste water is sent into the anaerobic sludge layer uniformly through the water distributor of cloth at the bottom of the pond, under the effect of obligatory anaerobic bacteria, DeRs such as organic hydrolysis, fermentation, product acetate, methanation takes place; The general stop 16 hours all accomplished these reactions, and sewage progressively rises in reactor drum; For example accomplish mud-water separation in 2.5-1.0 rice apart from rising pipe at last, sludge settling continues to fall after rise to sludge blanket, and continues to rise through the gas of sewage behind the anaerobic reaction and anaerobism generation; At the rising pipe place; Sewage overflow goes out reactor drum, and aerogenesis (methane, hydrogen sulfide, carbonic acid gas etc.) gathers gas collection district, top, pond, and is collected into the biogas cabinet at this top gas collection tube place, district.
The main technical details of this system is following:
1, the water yield: single pond maximum amount of water Q
MAX60000M
3/ d.
2, influent load: COD
CR1000-4000mg/L.
3, water distribution: effect and water distribution that acid is produced in hydrolysis have much relations; This section adopts the high-efficiency pulse water distribution system; It is with having stored in the water distributor 3～7 minutes A1 section water outlet rushes at the pond with very fast flow velocity in the short period of time (several seconds to tens seconds) at the bottom of through syphonic effect; Upwards dashed the sludge blanket at the bottom of the pond and to be suspended state, thereby made the muddy water uniform mixing in the pond.
4, temperature: this parameter directly affects growth velocity and activity, the physico-chemical property etc. of bacterium, tackles this and carries out strictness control.Have a liking for the warm type mikrobe because the mikrobe in this system belongs to, the temperature of system is controlled at 20～39 ℃.
5, pH: because hydrolysis bacterium and acid-producing bacteria have flexibility in a big way to pH, methanogen then requires relatively harsher to pH, and the pH of system of therefore controlling well influence system for anaerobic treatment to move one of fine or not important factor.Through test of many times, this value is controlled between the 6.5-7.5.
6, sludge concentration: require to have very high sludge concentration in the normal postrun hydrolysis acidification pool, the general controlled 6000-25000mg/L that is made as, the best is 18000mg/L
7, hydraulic detention time: 16h.
8, the sludge retention time in the reactor drum: 15-60d, preferred 45d.
9, sludge volume index: 50-150, preferred 70
10, system sludge internal recycle amount: confirm according to the water yield and water distribution situation, can be controlled between the 0-40%.
11, O section return sludge ratio: need a large amount of O section mud to tame during debugging, need add certain anaerobic species simultaneously.Can add on a small quantity during normal the operation,, increase sludge concentration, improve the anerobes rate of growth to improve clearance.
12, nutritive substance:, therefore must maintain good bacterial growth state because the anaerobic treatment process of waste water is accomplished by bacterium fully.Except the carbon source of necessity, nitrogenous source, also need replenish necessary nutritive element in the paper waste.The characteristics of actual waste water are arranged and determine it to add ratio, the COD in operational process of assurance system: N: P is 150～500: 5: 1.Preferred 200: 5: 1.Those of ordinary skills can suitably adjust above-mentioned parameter according to the particular case of waste water, and these adjustment are conspicuous to those skilled in the art, need not to make creative work.
The multistage AO aeration tank explanation of delaying time
The multistage AO aeration tank of delaying time is the O section in the QA2O technology, waste water in this section, mainly be with aerobic be main, realize the series connection of a plurality of oxygen enrichment anoxic sections the nitrification and denitrification reaction taking place through the alternately oxygen supply of aerator.
One, principal feature:
1, more reasonable to the utilization of oxygen
Multistage A/O process using is interrupted aeration, and active sludge is in " aerobic-anoxic " alternative environment.That active sludge is in is this " hungry full " alternative state can be brought into play self potential, under good oxygen condition, accelerates the degradation speed to pollutent, and the raising processing efficiency especially improves the utilization ratio to oxygen.
2, more effective to the removal of NH4-N
Repeatedly nitrated-anti-nitration reaction stack, to the removal effect of NH4-N be superior to tradition single nitrated-anti-nitration reaction.-denitrification technology (clearance of NH4-N generally 60%～70%) nitrated with tradition compared, and multistage A/O technology has shortened nitrated-anti-nitration reaction time, has increased progression; Through experiment proof: after the controlling reaction time, each cycle can obtain 20%～30% NH4-N clearance, can obtain the clearance greater than 85% through for example 8 cycles.
3, effectively avoided the generation of sludge bulking phenomenon
Sludge bulking the most directly shows as sludge index SVI and raises.Cause the reason of sludge bulking a lot (like the variation of water temperature and quality etc.), with regard to the high sludge loading in aeration tank itself, high sludge concentration, single operation scheme all when water quality worsens suddenly sludge bulking takes place easily.Because multistage A/O process using is interrupted aeration, mixed solution is through the alternating action of aerobic zone and oxygen-starved area repeatedly, and whole process using hangs down sludge loading, can effectively avoid the generation of sludge bulking phenomenon.
4, surplus sludge volume is few
This process sludge quantity of reflux is big, sludge concentration high (sludge concentration of design aeration tank is 3000-4000mg/L), and living weight is big.The residence time of mud in the aeration tank is long, and pollutants in waste water can be by fully degraded.
Waste water from the A2 section in the QA2O technology at first gets into biological selector, through preaeration, carries out the domestication of dominant bacteria.Get into the aeration zone then; Under the aeration zone was in aerobic condition, aerobic cenobium (nitrobacteria, nitrite bacteria etc.) was preponderated, and making itrogenous organic substance is ammonia by bacterial degradation; Under the effect of nitrite bacteria, further be converted into nitrite then, be converted into nitrate salt through the nitrobacteria effect again; Nitrate salt enters into the district that stops the supple of gas or steam, and facultative cenobium is preponderated gradually, under the effect of facultative different oxygen bacterium; Utilize or part utilizes that original organism carbon source is electron donor in the waste water; Substitute molecular oxygen with nitrate salt and make electron acceptor(EA), decompose organic matter, simultaneously; Nitrogen in the nitrate salt is reduced to gaseous nitrogen (N, NO2 etc.); When entering into the aeration zone again, aerobic cenobium is preponderated again and ability strengthens; In like manner enter into when stopping the supple of gas or steam the district, facultative cenobium is preponderated again and ability strengthens; The carrying out of going round and beginning again, nutritive substance reduce and the cenobium quality and quantity is all increasing, and reach " balance between supply and demand " state very soon; Be " supply-less-than-demand " state afterwards, nutritive substance is by thoroughly clean decomposition, and the material of some difficult degradations is also decomposed by the mud cenobium of excellent performance at this moment.
Sewage is through biological selector, carry out the optimization of bacterial classification after, get into the multistage AO of time-delay aeration tank, under the effect of nitrifier, nitrococcus, facultative heterotrophic bacteria, the nitrification and denitrification reaction is taking place, thereby degradation of organic substances.The main technical details of this system has:
1, mud organic loading: the mud organic loading in the native system is about 0.05-0.1kgBOD5/kg (MLSS); Preferred 0.05; This has also demonstrated fully characteristics---the underload activated sludge process of multistage A/O; It has made full use of mikrobe and the metabolic whole process of mikrobe that mud provides, and pollutants in waste water is fully degraded.
2, mixed solution sludge concentration: in real work, adopt this index to measure the quantity of active sludge microorganism indirectly, the operation of system.Usually be controlled between the 3000-4000mg/L preferred 3500mg/L.
3, hydraulic detention time: native system belongs to extended aeration, and general hydraulic detention time is between 50-65 hour, and is best between the 52-57.The so long residence time is that good treatment effect provides the prerequisite assurance, makes pollutent obtain the more purifying treatment of the degree of depth.Make the excess sludge very stable corruption that is difficult for that becomes because nitration reaction has taken place, excess sludge has obvious minimizing simultaneously.
4, sludge index (SVI): this parameter has reflected the loosening degree of mud, is to judge that sludge settling concentrates a parameter commonly used of performance, in daily administration, can judge whether to take place sludge bulking through this parameter, and the control sludge volume.According to service experience, this parameter generally is controlled between the 150-200, and sludge settling property is bad when too high, the sludge dewatering weak effect, though it is good to cross low settling property, but absorption property is poor.
5, reflux ratio: this system sludge quantity of reflux is big, adopts 100% to reflux.Surplus sludge volume is little, because action of microorganisms makes that mud can be not smelly, the processing of mud is also than being easier to simultaneously.
6, dissolved oxygen: the demand of the DO of different bacterial classifications is different, and to this system of multistage A/O, we control DO between 0.2-2.0, preferred 0.5-1.0, thus realize the decarburization denitrogenation better.
7, sludge age: the sludge age of system is long more, and the nitrogen and phosphorus content in the mud is just low more, organic matter removal thorough more.Generally be controlled at 15-25 days, 18-22 days best.
8, nutritive element: carbon, nitrogen, phosphorus are the important elements that constitutes the sludge microbe body, and they provide the energy for the existence of bacterium, and native system is regulated three's ratio at any time according to the variation of water quality, and generally with COD: N: P was controlled at 100: 5: 1.
Waste water through after this system handles can be by reducing in the 100mg/L about former water COD5000mg/L.
In filtration step of the present invention, can adopt filtering technique conventional in the prior art, so that remove silt particle, fiber, part xylogen, pigment or the like, when removing a large amount of solid substances (SS), can also reclaim slurry.
Preferably, adopt rotary Microfilter to filter, select 80-120 purpose steel mesh or nylon wire for use, the slurry that recovery obtains preferably is concentrated into 2% (weight) and returns pulping system, and waste water is after filtering controlled its SS less than 800mg/L.
Waste water after filtering still contains silt, for reducing the reuse cost, improves quality of reused water, guarantees the normal operation of follow-up equipment, preferably waste water is carried out desanding and handles.Can adopt desanding means commonly used in the prior art, this is conspicuous for those of ordinary skills.
Usually adopt settling pit to carry out sand setting and handle, the sediment outflow at intermittence is carried out in the bottom, and supernatant carries out step of flocculation precipitation.
It in the present invention, has no particular limits, can adopt flocculation agent commonly used in the prior art, as long as can reach the purpose of flocculation sediment for the flocculation agent that is adopted.For example, can adopt ferro-aluminum composite salt salt flocculation agent well known in the prior art.
In the present invention,, can also add coagulant aids in order to reach better flocculation sediment effect, same, have no particular limits for the use of coagulant aids, as long as can reaching, it helps the purpose of coagulating.For example can adopt SEPIGEL 305 coagulant aids commonly used or the like.Its consumption is had no particular limits, and those of ordinary skills can carry out appropriate selection as required.
Through method of wastewater treatment of the present invention, the reclamation rate of waste water reaches more than 60%.
Description of drawings
Below in conjunction with accompanying drawing technical process of the present invention is described:
Fig. 1 is the synoptic diagram of method of wastewater treatment of the present invention.
Fig. 2 is Q
2The synoptic diagram of AO.
Fig. 3 is the synoptic diagram of traditional A2O technology.
Embodiment
Embodiment 1
15-22 day in July, 08 is because pulping process is changed the former water COD5300mg/L of middle section water, the water 2530mg/L that after this system handles, just settles out, A
1Water outlet 1550mg/L, A
2Water outlet 900 second pond water outlet 80-105mg/L, SS＜50mg/L.
Embodiment 2
3-10 day in October, 08, the former water COD3500mg/L of middle section water, the water 1800mg/L that after this system handles, just settles out, A
1Water outlet 1150mg/L, A
2Water outlet 705 second pond water outlet 70-55mg/L, SS＜50mg/L.
Embodiment 3
The 10-11 month 10 in July, 08, the equal COD3800mg/L of the former level of middle section water, the equal 1900mg/L of level that after this system handles, just settles out, A
1Water outlet 1280mg/L, A
2Water outlet 730 second pond water outlet 85mg/L, SS＜50mg/L.
Comparative Examples:
Certain pulping and paper-making factory adopts traditional materialization+aerobic biochemical process to handle, the about COD2500mg/L of former water, and materialization adds flocculation agent PAC800ppm, PAM5ppm, about water outlet COD1850,96 hours water outlet COD350mg/L of aerobic biochemical hydraulic detention time.Processing cost is higher than this technology, and go out water unstable can not be up to standard.
More than combine embodiment and accompanying drawing that the present invention has been carried out more detailed explanation.For simplicity, only water in the papermaking is carried out among the embodiment.Yet those of ordinary skills should be understood that, so long as the waste water salt content is higher, in the time of should not passing through simply to handle reuse, all can adopt method of the present invention to handle.Therefore, the processing of water during treatment process of the present invention is not limited only to.Under spirit of the present invention, those of ordinary skills can carry out suitable change or change to method of the present invention as required, and these changes and change all fall within the scope of the present invention.Protection scope of the present invention is as the criterion with appending claims.
Claims (3)
1. technological process of treating papermaking method comprises: filters, and flocculation sediment, biochemical treatment and advanced treatment step is characterized in that, QA is adopted in biochemical treatment
2The O treatment process, QA
2O comprises three sections of A1, A2, O, and every section is respectively A1 complex reaction aeration tank, A2 pulse water distribution upwelling anaerobic reactor, the O multistage AO aeration tank of delaying time; At QA
2The A1 section is main with the oxygen bacterium of holding concurrently in the O technology, simultaneously compound again physical reaction, and this section is provided with settling tank separately; The independently mud recycle system is arranged, and the A2 section is main with obligatory anaerobic bacteria, is anaerobic technique completely; The independently mixed solution recycle system is arranged, do not rely on A1 and O section mud and reflux, the O section is main with aerobic bacteria then; Alternately oxygen supply through aerator realizes that the series connection of a plurality of oxygen enrichment anoxic sections is multistage AO, and the biological pond of selecting is set before the O section, to reach the purpose of optimizing bacterial classification.
2. method according to claim 1, the said micro-filtration that is filtered into, the order number of filter screen is from the 80-120 order.
3. method according to claim 2 also comprises QA in addition
2The mud that O produces carries out sludge dewatering treatment.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009100012703A CN101781056B (en) | 2009-01-16 | 2009-01-16 | Treatment method of waste papermaking water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009100012703A CN101781056B (en) | 2009-01-16 | 2009-01-16 | Treatment method of waste papermaking water |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN101781056A CN101781056A (en) | 2010-07-21 |
| CN101781056B true CN101781056B (en) | 2012-01-04 |
Family
ID=42521226
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2009100012703A Active CN101781056B (en) | 2009-01-16 | 2009-01-16 | Treatment method of waste papermaking water |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN101781056B (en) |
Families Citing this family (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102225827B (en) * | 2011-05-24 | 2012-09-05 | 青岛理工大学 | Treatment method of straw pulp papermaking middle-stage wastewater |
| CN102515427A (en) * | 2011-12-07 | 2012-06-27 | 浙江省环境保护科学设计研究院 | Printing and dyeing waste water treatment system and process with low yield of sludge |
| CN102515425A (en) * | 2011-12-07 | 2012-06-27 | 浙江省环境保护科学设计研究院 | High efficiency town sewage treatment system and process with low yield of sludge |
| CN103224309B (en) * | 2013-04-25 | 2014-06-25 | 西华大学 | Leather waste water treatment system and treatment process |
| CN104445802B (en) * | 2014-10-24 | 2017-03-15 | 浙江百斯特化工有限公司 | Multi-stage sedimentation treatment system for papermaking wastewater |
| CN105239438B (en) * | 2015-10-13 | 2017-07-07 | 新疆国力源投资有限公司 | A kind of paper machine plain boiled water circulation reusing technology |
| CN107746159A (en) * | 2017-11-27 | 2018-03-02 | 青岛城投娄山河水务有限公司 | A kind of New Type of Sewage Treatment System and technique |
-
2009
- 2009-01-16 CN CN2009100012703A patent/CN101781056B/en active Active
Also Published As
| Publication number | Publication date |
|---|---|
| CN101781056A (en) | 2010-07-21 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US5342522A (en) | Method for the treatment of sewage | |
| JP6563333B2 (en) | Hybrid sewage treatment | |
| US5853589A (en) | Advanced biological phosphorus removal using a series of sequencing batch reactors | |
| CN100402448C (en) | Purification and treatment method of pulping and papermaking wastewater | |
| US20040206699A1 (en) | Combined activated sludge-biofilm sequencing batch reactor and process | |
| CN101781056B (en) | Treatment method of waste papermaking water | |
| CN107021597A (en) | Improve the system and method for biochemical and deeply treating wastewater using Powdered Activated Carbon | |
| CN102826710B (en) | Treatment process and treatment device of high-salinity high-ammonia nitrogen pharmaceutical sewage | |
| CN102603128A (en) | Method for advanced treatment and recycling of landfill leachate | |
| CN110902962A (en) | A waste water system for treating melamine adhesive film paper | |
| CN108328871A (en) | Landfill leachate efficient denitrification system and its denitrification process | |
| CN101781055B (en) | Treatment method of waste papermaking water | |
| CN110054361A (en) | A kind of electric field-enhanced MBR sewage treatment process | |
| CN102336483A (en) | Method and device for treating landfill leachate thick water | |
| CN103073156A (en) | Method for treating poly butylene succinate production waste water by biochemical method | |
| CN111252994A (en) | Domestic fungus wastewater treatment method | |
| CN105110556A (en) | Integrated denitrification decarbonization biological aerated filter and processing system thereof | |
| CN117088579B (en) | Non-membrane method full-quantization treatment method for landfill leachate | |
| CN206985970U (en) | It is a kind of to improve biochemical and deeply treating wastewater system using Powdered Activated Carbon | |
| CN111153551A (en) | Municipal sewage treatment device and treatment process | |
| CN112188996A (en) | Combination of dissolved air flotation and fixed film bioreactor solutions | |
| CN112624500B (en) | Kitchen waste sewage treatment system and method | |
| CN211445406U (en) | Landfill leachate treatment device | |
| CN211226832U (en) | Pharmacy effluent disposal system | |
| CN116605988A (en) | A rapid start-up method for an integrated aerobic granular sludge-membrane bioreactor |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| ASS | Succession or assignment of patent right |
Owner name: SHANDONG HERUN PULP + PAPER CO., LTD. Free format text: FORMER OWNER: SHANDONG QUALIN PAPER INDUSTRY CO., LTD. Effective date: 20101221 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| COR | Change of bibliographic data |
Free format text: CORRECT: ADDRESS; FROM: 252800 NO. 26, GUANDAO STREET, GAOTANG COUNTY, SHANDONG PROVINCE TO: 252800NO. 15, GUANGMING EAST ROAD, GAOTANG COUNTY, SHANDONG PROVINCE |
|
| TA01 | Transfer of patent application right |
Effective date of registration: 20101221 Address after: 252800 No. 15 Guangming East Road, Gaotang County, Shandong Province Applicant after: Shandong Tralin Paper Co., Ltd. Address before: Shandong province Gaotang County Road 252800 Street No. 26 Applicant before: Shandong Qualin Paper Industry Co., Ltd. |
|
| ASS | Succession or assignment of patent right |
Owner name: SHANDONG FUYIN PAPER MAKING ENVIRONMENTAL PROTECTI Free format text: FORMER OWNER: SHANDONG HERUN PULP AND PAPER CO., LTD. Effective date: 20110124 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| COR | Change of bibliographic data |
Free format text: CORRECT: ADDRESS; FROM: 252800 NO. 15, GUANGMING EAST ROAD, GAOTANG COUNTY, SHANDONG PROVINCE TO: 252800 NO. 26, GUANDAO STREET, GAOTANG COUNTY, SHANDONG PROVINCE |
|
| TA01 | Transfer of patent application right |
Effective date of registration: 20110124 Address after: Shandong province Gaotang County Road 252800 Street No. 26 Applicant after: Shandong Fuyin Paper Making Environmental Protection Technology Co., Ltd. Address before: 252800 No. 15 Guangming East Road, Gaotang County, Shandong Province Applicant before: Shandong Tralin Paper Co., Ltd. |
|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of invention: Method of treating waste water from pulping and papermaking by lime process Effective date of registration: 20140211 Granted publication date: 20120104 Pledgee: China Development Bank Co Pledgor: Shandong Quanlin Paper Industry Co. Ltd.|Shandong Fuyin Paper Environmental Technology Co. Ltd. Registration number: 2014990000101 |
|
| PLDC | Enforcement, change and cancellation of contracts on pledge of patent right or utility model |