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CN102557252B - Treating method of typical PPCPs (Pharmaceutical and Personal Care Products) - Google Patents

Treating method of typical PPCPs (Pharmaceutical and Personal Care Products) Download PDF

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Publication number
CN102557252B
CN102557252B CN201010608033.6A CN201010608033A CN102557252B CN 102557252 B CN102557252 B CN 102557252B CN 201010608033 A CN201010608033 A CN 201010608033A CN 102557252 B CN102557252 B CN 102557252B
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ppcps
water
electric field
typical
biofilm
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CN102557252A (en
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胡翔
凌绘
孙治荣
王家德
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Beijing University of Chemical Technology
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Beijing University of Chemical Technology
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Abstract

本发明涉及一体化电场强化生物降解典型PPCPs的新方法。一体化电场强化生物法是将电化学处理工艺与生物膜处理工艺组合在一个反应器中,典型PPCPs物质经电化学氧化还原作用发生降解,生成易降解的有机中间产物,新生成的有机中间产物则被反应系统中的微生物进一步降解,最终产物为二氧化碳和水。一体化电场强化生物法在降解典型PPCPs的过程中,不需要投加化学药剂,因而不会产生二次污染,而且由于外加电场电压、电流密度低,不存在安全隐患,使该方法易于实际应用。通过工艺条件的优化,确定适宜的外加电场工艺条件及生物处理的工艺条件,一体化电场强化生物法对典型难降解PPCPs的去除率最高可达95%以上。

The invention relates to a novel method for integrated electric field enhanced biodegradation of typical PPCPs. The integrated electric field enhanced biological method is to combine the electrochemical treatment process and the biofilm treatment process in one reactor. Typical PPCPs substances are degraded by electrochemical redox, and easily degradable organic intermediates are generated. The newly generated organic intermediates It is further degraded by microorganisms in the reaction system, and the final products are carbon dioxide and water. The integrated electric field enhanced biological method does not need to add chemical agents in the process of degrading typical PPCPs, so it will not cause secondary pollution, and because of the low voltage and current density of the applied electric field, there is no potential safety hazard, making this method easy to practical application . Through the optimization of process conditions, the appropriate applied electric field process conditions and biological treatment process conditions are determined, and the removal rate of typical refractory PPCPs by the integrated electric field enhanced biological method can reach up to 95%.

Description

The treatment process of a kind of typical PPCPs
Technical field
The present invention relates to a kind of water technology of novelty, it combines biological process and electrochemical process, has without the need for machine carbon source, the feature such as between redox ability high and microbial film and electrode mass transfer is efficient.It is a kind of method of efficient processing organic micro-pollution material.
Technical background
Medicine and personal-care supplies PPCPs comprise number of chemical material, are present in multiple prescribed and non prescribed medicine (as microbiotic, steroid, anodyne, depressor, soporific, diet pill etc.), soap, shampoo, toothpaste, perfume, skin care product, sunscreen, hair jelly, hair dye etc.
PPCPs in modern society consumption is very large, and the PPCPs not utilized completely by human body enters municipal effluent by excretion or bathing, and municipal effluent is one of the main source of PPCPs in ecotope.Nearly ten years, started to pay close attention to the pollution of PPCPs to environment abroad, research shows, synthetic musk material, photographic developer, microbiotic, oestrogenic hormon, anti-inflammation analgesic, disinfection sanitizer etc. and the closely-related PPCPs of human lives ubiquity in environment.More than 70 kind of PPCPs and meta-bolites thereof in municipal effluent, surface water, underground water and drinking water source, have been detected abroad.The scientist of the U.S. and Britain further studies discovery, and near sewage work and factory's sewage draining exit, the wild fish of water body has produced sex entanglement, a large amount of Malformed frogs.Scientist thinks, environmental hormone is main assailant, and PPCPs is one of important sources of environmental hormone.Research both at home and abroad finds that PPCPs may produce adverse influence to the shellfish immunity system in water surrounding, as the PPCPs such as triclosan may have a negative impact to the hemocyte function of bivalve and the activity of digestive gland enzyme in the structure and function generation of algae in fresh water environment and seawater, in addition, PPCPs also may have chronic toxic action to biologies such as the water fleas in water surrounding, as can be seen here, PPCPs may have toxicity to a lot of biologies in water surrounding, and may pass through tap water or food chain harm humans health, thereby the Transport And Transformation of this pollutant in environment and biological impact has been become to a new environmental problem that causes extensive concern.
The discharge of cutting down PPCPs is to solve one of main method of this environmental problem, but more it is disturbing, about the research of PPCPs control techniques just just starts, because its concentration is low and have special metabolisming property, traditional waste water treatment plant does not have obvious removal effect to quite a few PPCPs, up to now, people also do not find the technological method of effective control, elimination PPCPs material.
Electrochemical treatment technology, owing to not adding chemical reagent thereby can not produce secondary pollution, has broad application prospects in water and field of waste water treatment, be considerable technology it.Since CNT (carbon nano-tube) self-discovery, it has been the center that people pay close attention to always.Carbon nanotube has electroconductibility and complete surface tissue, thereby it is a kind of good electrode materials, and carbon nanotube electrode can promote biomolecules Electron Transfer, can obtain good treatment effect, and has higher current efficiency.Biomembrance process can be used to process the waste water of lower concentration.Integrated electric field-enhanced biotechnology is in conjunction with biomembrance process and electrochemical process and the new technology of getting up, can fully combine active sludge or biomembranous microorganism fixed growth and the higher redox ability of electrolytic process, and the advantage such as efficient mass transfer relation between the two, at aspects such as processing lower concentration Persistent organic pollutants, there is obvious advantage.
Summary of the invention
The present invention seeks to by integrated electric field-enhanced biological process, utilize its biology and electrochemistry acting in conjunction, adopt but be not limited to SBR and process typical difficult degradation PPCPs material
The method that integrated electric field-enhanced biological process of the present invention is processed typical difficult degradation PPCPs comprises the following steps:
(1) Biofilm Colonization.This test temperature is room temperature.The mass concentration of dissolved oxygen is that 2-3mg/L. adopts quick spoil disposal biofilm method to carry out biofilm.The active sludge biological that inoculation has been tamed is abundant mutually, and the mass concentration of mud is 3.2g/L, and SV is about 25%.The waste water of above-mentioned kind of mud and artificial preparation mixes and adds each reactor as the ratio of 2: 3 take muddy water volume ratio, after submergence filler Static Contact 24h. get rid of mud. start the biofilm of intaking.Influent COD is 500mg/L, and ammonia-nitrogen content is 10mg/L, pH furnishing 7.5 left and right, the cycle of operation is 12h, aeration 10h, standing 1h, water outlet, water inlet, filler starts biofilm, is algae green, but biofilm insecure, easily come off; After 2 weeks, biofilm is mature on the whole, and difficult drop-off, after launching in water, is fine hair shape, overworks the whole inwall of filler.
(2) electrode biomembrane domestication.After microbial film is stable, in reactor, adds electrode and pass into direct current.Starting stage voltage is 1V, electric current is 2mA, add small portion microbial death after electric field, discharge, in reactor, on battery lead plate, have the thick microbial film of one deck 2mm, on filler, also have certain thickness microbial film, by the above results can determine in reactor, growth has nitrifier and denitrifying bacteria on battery lead plate and soft-filler, domestication cultivation stage completes, and system run all right, formally enters experimental stage.
(3) after system run all right, in rising pipe, take out experiment water outlet, measure.The leading indicator of measuring has the COD value, ammonia nitrogen of concentration, the water outlet of PPCPs (Ibuprofen BP/EP, diclofenac) etc.
(4) by changing influent load, select best influent load value, experimental result shows that the less PPCPS of influent load (Ibuprofen BP/EP, diclofenac) removal effect is better.
(5) change strength of current, strength of current increases successively, is up to 50mA.Along with the increase of strength of current, removal effect increases gradually.The clearance of Ibuprofen BP/EP reaches as high as more than 74%, and the clearance of diclofenac reaches as high as more than 95%.
In reaction process, COD removal effect all can reach more than 95%, and ammonia nitrogen removal effect can reach more than 90%, meets national standard effluent quality.
Present method utilizes the electrochemistry of integrated electric field-enhanced biological process and biodegradable acting in conjunction to process as Ibuprofen BP/EP and diclofenac typical difficult degradation PPCPs.Characteristic and the advantage of present method are, do not need to add chemical agent, thereby can not produce secondary pollution, and because extra electric field voltage, current density are low, do not have potential safety hazard, make the method be easy to practical application; This method has very high removal effect to COD, ammonia nitrogen, and its cost is lower, economic and practical, is a method of effectively removing lower concentration PPCPs.
Be that drawings and Examples further describe the present invention below, but the invention is not restricted to following embodiment
Accompanying drawing explanation
Fig. 1 .. electrode biomembrane of the present invention is processed the artwork of PPCPS
Reference numeral
1, mixing section 2, penstock 3, peristaltic pump 4, reactor
5, graphite electrode plate 6, microbial film 7, power supply 8, wire
9, water output duct 10, second pond
Specific implementation method
In experiment, in the nutritive medium of 1L, adding Ibuprofen BP/EP and diclofenac to make its concentration is 1mg/L, and microbial film is tamed and cultivated 7-15 days, after microorganism is stable, then adds electric field.Voltage is 1V, and electric current is 5mA, tames and cultivates 7-15 days, makes microorganism adapt to, after electric field and specific waste water thereof, carry out experimental debugging completely.Reaction has adopted SBR intermittent loading, every day to carry out 3 cycles, aeration 5h, precipitation 2h, and water inlet water outlet is respectively 0.5h.Taking out experiment water outlet measures.

Claims (1)

1.一种电化学与生物作用协同处理典型PPCPs的方法,其特征是在同一反应器中实现电化学处理工艺与生物膜处理工艺的耦合,综合发挥电化学、吸附和微生物降解多种作用机理,实现对PPCPs的高效处理,且不产生二次污染,它包括以下步骤:1. A method for the co-processing of typical PPCPs by electrochemical and biological action, which is characterized in that the coupling of electrochemical treatment process and biofilm treatment process is realized in the same reactor, and multiple action mechanisms of electrochemical, adsorption and microbial degradation are comprehensively played , to achieve efficient treatment of PPCPs without secondary pollution, it includes the following steps: (1)生物膜挂膜:溶解氧的质量浓度为2-3mg/L,采用快速排泥挂膜法进行挂膜,接种已经驯化好的活性污泥,污泥的质量浓度为3.2g/L,SV为25%,接种的污泥和人工配制的含一定浓度典型PPCPs的水样以泥水体积比为2∶3的比例混合加入反应器,浸没填料并静态接触24h后,排除污泥,开始进水挂膜,进水COD为500mg/L,氨氮含量为10mg/L,pH调成7.5,运行周期为12h,曝气10h,静置1h,出水、进水,填料开始挂膜,呈藻绿色,但挂膜不牢固、易脱落;2周后,挂膜成熟,不易脱落,在水中展开后,呈茸毛状,挂满填料的整个内壁;(1) Biofilm hanging film: the mass concentration of dissolved oxygen is 2-3mg/L, adopt the rapid sludge discharge film hanging method to carry out film hanging, inoculate the activated sludge that has been domesticated, and the mass concentration of sludge is 3.2g/L , the SV is 25%, the inoculated sludge and the artificially prepared water sample containing a certain concentration of typical PPCPs are mixed into the reactor at a ratio of 2:3 by volume ratio of sludge to water, and the filler is submerged and statically contacted for 24 hours. After the sludge is removed, start The film is formed in the water, the COD of the water is 500 mg/L, the ammonia nitrogen content is 10 mg/L, the pH is adjusted to 7.5, the operation cycle is 12 hours, the aeration is 10 hours, and the water is left for 1 hour. Green, but the hanging film is not firm and easy to fall off; after 2 weeks, the hanging film is mature and not easy to fall off. After being unfolded in water, it is fluffy and covers the entire inner wall of the filler; (2)电极生物膜驯化:待生物膜运行稳定后,在反应器中加入电极并通入直流电,初始阶段电压为1V,电流为2mA,加入电场后小部分微生物死亡,排出,反应器内电极板上附有一层2mm厚的生物膜,填料上也有生物膜,确定反应器内、电极板以及填料上生长有硝化菌和反硝化菌,驯化培养阶段完成,系统运行稳定,正式进入试验阶段;(2) Electrode biofilm acclimatization: After the biofilm is running stably, add electrodes to the reactor and supply direct current. The initial voltage is 1V and the current is 2mA. After adding the electric field, a small part of microorganisms die and are discharged. There is a layer of 2mm thick biofilm on the plate, and there is also biofilm on the packing. It is confirmed that there are nitrifying bacteria and denitrifying bacteria growing in the reactor, on the electrode plate and packing. (3)采用连续流或SBR工艺,在适宜的外加电场、电极间距及溶解氧浓度条件下,根据进水水质情况选定适宜的水力停留时间或运行周期、污泥停留时间,含一定浓度典型PPCPs的水样进入反应器得到降解,处理后出水进入二沉池;(3) Using continuous flow or SBR process, under the appropriate external electric field, electrode spacing and dissolved oxygen concentration conditions, select the appropriate hydraulic retention time or operation cycle, sludge retention time according to the influent water quality, with a certain concentration of typical The water sample of PPCPs enters the reactor to be degraded, and the treated effluent enters the secondary sedimentation tank; (4)进入二沉池的水样经泥水分离后排水;(4) The water sample entering the secondary sedimentation tank is drained after separation of mud and water; 所述的典型PPCPs为布洛芬、双氯芬酸;Described typical PPCPs are ibuprofen, diclofenac; 所处理的含典型PPCPs的水样中PPCPs的浓度为0.2-20mg/L;The concentration of PPCPs in the treated water samples containing typical PPCPs is 0.2-20mg/L; 反应在室温下进行;The reaction is carried out at room temperature; 电极材料为石墨、碳纳米管;Electrode materials are graphite and carbon nanotubes; 外加电场为直流电,电极上电流密度为不超过5mA/cm2The applied electric field is direct current, and the current density on the electrode is not more than 5mA/cm 2 ; 阴阳电极间距控制在1-10cm;The distance between cathode and anode electrodes is controlled at 1-10cm; 步骤(3)中,曝气时,反应器中溶解氧浓度控制在1-4mg/L。In step (3), during aeration, the dissolved oxygen concentration in the reactor is controlled at 1-4 mg/L.
CN201010608033.6A 2010-12-28 2010-12-28 Treating method of typical PPCPs (Pharmaceutical and Personal Care Products) Expired - Fee Related CN102557252B (en)

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