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双语推荐:水解酸化

对生物制药废水水解酸化反应器采用接种污泥的方式进行启动,在不断增加进水污染负荷的条件下,40 d内完成水解酸化反应器的启动。试验研究表明:当水解酸化反应器的水力停留时间为8h时,COD去除率可达到34.2%。而且,水中有机氮在水解酸化过程中转化为氨氮,为后续二级生物处理提供了高效去除氨氮的基础。
The biological pharmaceutical wastewater is pretreated in a hydrolysis acidification and it is started by the sludge inoculation method .Under condition of increasing water pollution load ,hydrolysis acidification reactor has completed in 40 days .Experimental study shows that :when the HRT of hydrolysis acidification reactor hydraulic is 8 h ,removal rate of COD can reach 34 .2% ;organic nitrogen in the water is converted to ammonia nitrogen in the hydrolysis acidification process and it will provide foundation of the efficient removal of ammonia nitrogen for the secondary biological treatment .

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阐述了水解酸化工艺的机理,介绍了其以独立的工艺或与其他工艺相结合在印染废水处理中的应用,并分析了水解酸化过程中微生物及其产生的胞外酶的作用。另外,本文还总结了水解酸化阶段的优化调控方法,包括直接投加菌剂或共代谢基质类物质和投加激活剂,并概括了水解酸化调控效果的评价指标,包括pH值、色度、挥发性脂肪酸 VFA、BOD5/COD、有机物组成的变化、酶活、微生物种群结构变化。目前,虽然水解酸化工艺在印染废水处理中应用广泛且有所成效,但是对其中微生物的作用机制尚不十分了解,无法有针对性地对功能菌群进行优化调控。本文提出在深入探讨微生物作用机理的基础上,针对功能菌群进行优化调控,是提高水解酸化速率的一个有效途径,从而最大限度地发挥水解酸化工艺在印染废水处理中的作用。
The paper sketched the mechanisms of hydrolytic acidification process,introduced the applications of the independent process or combined with other technologies in dyeing wastewater treatment,and analyzed the roles of microbes and extracellular enzymes in hydrolytic acidification process. This paper also summarized the optimization regulation methods of hydrolytic acidification stages,including adding microbial agents or co-metabolism matrixes and activators. The evaluation indexes of hydrolytic acidification regulation effect were generalized , including pH value , chromaticity,volatile fatty acids (VFA),BOD5/COD,variation of organic matters,enzyme activity and changes of microbial population. Currently,although hydrolytic acidification process is widely used and made some achievements in dyeing wastewater treatment,the mechanisms of microbes in it are still not clear making the specifically regulations of functional microbes difficult. This paper proposed an effective way t

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1,4-丁二醇(BDO)生产废水含甲醛,难降解、毒性大、水质水量变化大,处理难度高。试验构建了预曝气水解酸化-高效厌氧反应器-接触氧化-膜生物反应器组合系统处理BDO废水。预曝气水解酸化可有效降低甲醛浓度,降低废水毒性。同时预曝气水解酸化和高效厌氧反应器均可提高废水的可生化性。系统对废水COD的去除率达到90%以上,出水COD满足国家《污水综合排放标准》(GB 8978—1996)一级标准。
1,4-butanediol(BDO) wastewater contains formaldehyde which is so refractory and toxic with great water quality and quantity changes,that it is difficult to be treated. The combined system,pre-aerated hydrolytic acidifica-tion reactor-anaerobic reactor-contact oxidation-membrane bioreactor ,has been constructed for treating the BDO wastewater. Pre-aerated hydrolytic acidification reactor can effectively reduce the formaldehyde concentration so that the toxicity of wastewater can be reduced. At the same time ,the biodegradability of wastewater can be improved by both of the pre-aerated hydrolytic acidification reactor and the anaerobic reactor. COD removing efficiency of the system reaches 90%above,and effluent COD can meet the requirements for the first grade of Integrated Wastewater Discharge Standard(GB 8978—1996).

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研究蔬菜类废物两相厌氧消化过程中水解酸化液物化性质随水解时间的变化情况,结合总有机碳(TOC)、溶解性有机碳(DOC)、颗粒粒径和溶解性有机物(DOM)分子量的分析,探讨了蔬菜类废物水解酸化过程中TOC溶出和颗粒降解之间的关系,分析了水解酸化相颗粒物降解规律.实验结果表明,蔬菜类废物水解过程可以分成两个阶段:易水解的颗粒物在前5d迅速水解,TOC浓度迅速升高,在第5d达到最大值4920mg/L,水解产生颗粒态物质的二次平均直径从第1d的58.38μm降至第5d的4.64μm,有机物快速溶出,DOC/TOC比值在第4d达到最大值85%,该水解过程可用Contois模型模拟;第5d后,难水解颗粒物质的缓慢水解起主导作用,颗粒态物质的二次平均直径从4.64μm开始逐渐增大,并稳定在8.97~10.68μm范围内,TOC和DOC溶出率逐渐降低,且DOC溶出率小于TOC溶出率.大分子溶解性有机物的降解也主要集中在水解过程的前5d,水解第1d 产生的大分子 DOM(1.6×109~1.9×109Da)到第5d 已经全部降解成分子量在5×104~4×106Da 的DOM;第5d过后,DOM的分子量分布情况并未发生较大变化.表明蔬菜类废物两相厌氧消化工艺过程中水解时间可缩短为5d.
During the two-phase anaerobic digestion process of vegetable waste, changes of hydrolytic acidification liquid’s physical-chemical properties were investigated. The relationship among dissolution of total organic carbon (TOC), dissolved organic carbon (DOC) and particulate degradation was discussed. The mechanism of particle hydrolysis acidification was assessed by combining the trend of TOC, DOC, particle size distribution and molecular weight evolution. The experiment results showed that, the hydrolysis process of vegetable waste could be divided into two stages. In the first five days, particulates with high degree of hydrolysis began to hydrolyze quickly. The TOC value rose rapidly, reaching the maximum of 4920mg/L in the fifth day. The quadratic mean diameter of particulates generated from hydrolysis dropped from 58.38 μm in the first day to 4.64 μm in the fifth day. Furthermore, organic matter dissolved rapidly, with a maximum of 85%DOC/TOC ratio. This process could

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本文介绍了一种处理有机硅废水的新的工艺组合,即铁炭微电解——水解酸化——UASB——MBR联合处理法,第一步铁炭微电解很明显的改善了有机硅原水的可生化性,BOD/COD值可达0.52;进入水解酸化池后,部分大分子降解成小分子物质,可生化性进一步提高;随后进入UASB,在颗粒污泥的作用下,COD去除率达到81%;在曝气池中,设置MBR,进一步去除了COD,去除率为96%;最终出水能达标排放。
This paper introduces a new combination of processes in the treatment of organic silicon waste water, which is the united method of the iron-carbon microelectrolysis proces-hydrolytic acidification-UASB-MBR. In the first step, the iron-carbon microelectrolysis process significantly improved the biodegradability of the organic silion raw water, BOD/COD value can reach 0.52; In the hydrolytic acidification tank, parts of the large molecules are degraded into small molecular substances, the biodegradability was further improved. In the third step, the removal rate of COD reached 81%at the effect of the granular sludge. In the final step, the organic pollutants got futher removal in the addition of MBR, and the removal rate of COD can reach 96%. The final effluent was appropriate to the standard.

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采用微电解—水解酸化-硝化反硝化工艺处理假发生产废水,微电解去除废水中的色度和其他污染物,并提高废水的可生化性,以利于后续生化处理;水解酸化提高后续处理的容积负荷,提高去除效率,对进水中有机氮的氨化作用明显,硝化反硝化可将水解产生的NH3-N全部转化。运行结果表明,进水COD为1 100 mg/L、氨氮为120 mg/L的情况下,该工艺降解COD及脱氮效果良好;处理工艺保证系统出水COD〈40 mg/L,氨氮〈5 mg/L,达到了《污水综合排放标准》一级标准。
With the process of micro electrolysis -hydrolysis acidification -nitrification and denitrification in the treatment of hairwork wastewater, that micro electrolysis removed chromaticity and other pollutants in wastewater, improved the biodegradability in wastewater, to facilitate the subsequent biochemical treatment, and hydrolysis acidification of subsequent processing volumetric loading, improved the efficiency of removing, which had an obvious effect of organic nitrogen in the water ammoniation, nitrification and denitrification can transform all the NH3 -N that produced by the hydrolysis. Running results showed that when the flooding water COD was 1 100 mg/L, ammonia nitrogen was 120 mg/L, the degradation process of COD and nitrogen removal effect was good. The process assuranced system effluent COD<40 mg/L, ammonia nitrogen <5 mg/L, and achieved the primary standard of sewage comprehensive discharge standard.

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为解决农村生活污水的高效除碳脱氮问题,以厌氧水解-同时硝化反硝化厌氧氨氧化(SNAD)工艺处理低C/N比农村生活污水。实验结果表明:水解酸化单元进水C/N比为2∶1时,COD的去除率达到69%;产物VFA主要成分为乙酸、丙酸和正丁酸,平均含量分别为88.4%、6.5%与5.1%,VFAs/COD比为0.74;出水C/N比为3∶5。水解酸化单元出水进入SNAD脱氮单元,通过亚硝化、反硝化与厌氧氨氧化的耦合作用,该单元COD与总氮的去除率分别可达到76.7%和84.1%。厌氧水解-SNAD组合工艺COD与总氮总去除率分别达到92.8%和84.1%。
In order to solve the problem of removal of carbon and nitrogen of rural sewage , the paper used an anaerobic hydrolysis -SNAD process to treat this kind of wastewater with low C/N ratio.The results show that , when the C/N ratio of influent in hydrolysis acidification unit is 2 to 1 , the removal efficiency of COD reaches 69%.The main components of VFAs are acetic acid , propionic acid and ethacetic acid . The average contents are 88.4%, 6.5%and 5.1%respectively.Meanwhile the ratio of VFAs and COD reaches 0.74 and the ratio of C/N in effluent is 3 to 5.The hydrolysis acidification unit come into SNAD nitrogen removal unit , through the action of the coupling of partial nitrification , denitrification and anam-mox, the removal efficiencies of COD and total nitrogen reach 76.7%and 84.1%respectively.The re-moval ratio of COD and total nitrogen by using anaerobic hydrolysis -SNAD combined process reach 92 . 8%and 84 .1%respectively .

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某污水厂在提升出水标准的工艺调控中,对磷的生物法去除进行了理论分析和实践研究,通过强化水解酸化效果,并对活性污泥在整个生化系统中的分布和循环进行调控后,试验取得了显著的生物除磷效果,当进水TP为4~5 mg/L时,出水TP1 mg/L。实践表明污泥龄并不一定对磷的去除效果有较大影响。在发挥水解酸化作用的基础上,创造条件使活性污泥在整个厌氧和好氧生化系统中充分循环是发挥生物除磷作用的关键环节。
The theory and practice on phosphorus removal were analyzed during the upgrading of effluent standard in a wastewater treatment plant. The results show by strengthening hydrolytic acidification and adjusting distribution and cyclic of activated sludge in the biochemical system,there is a remarkable effect on phosphorus removal. Practice also indicates that sludge age has not necessarily effect on phosphorus removal. Based on the action of hydrolysis acidification effect,to create conditions for the activated sludge to practice full circulation in the biochemical system is the key link on biological phosphorus removal.

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采用铁炭微电解-水解酸化-固定化高效菌-混凝技术对蒸氨后的焦化废水进行了研究,结果表明,通过微电解,B/C值由0.20提高到0.39,经水解酸化进一步提高到0.44,之后采用折流板生化反应池进行生化处理,当HRT=48 h时,CODCr由3717 mg/L降到393 mg/L,去除率达到90%左右,出水在混凝剂投加量为6 mL,pH =7,T=35℃,PAM=3 mL的最佳条件下,CODCr最终降到65 mg/L,达到污水综合排放标准一级标准.
The iron-carbon micro-electrolysis-hydrolytic acidification and immobilized highly efficient bacteria and coagulation technology were used to treat coking wastewater after steaming ammonia. Results showed that after iron-carbon micro-electrolysis, the B/C of wastewater increased from 0.20 to 0.39, after hydrolytic acidification, the B/C of wastewater increased to 0.44. Then using baffle biochemical reactor, when HRT=48 h, CODCr reduced from 3717 mg/L to 393 mg/L, the removal rate reached about 90%. Biochemical effluent under the best conditions of the coagulant dose was 6 mL, pH=7, the temperature of 35 ℃, coagulant aids dose was 3 mL, CODCr finally reduced to 65 mg/L, attained the First Grade discharge standard of integrated wastewater.

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介绍了采用“水解酸化-接触氧化”工艺处理印染废水的实例,当进水COD≤1800mg/L,色度≤900倍时,处理出水可达到国家《纺织染整工业水污染物排放标准》(GB4287-1992)一级标准。
The article introduces the example of treating printing and dyeing wastewater processed by hydrolytic acidification and bio-contact oxidation.While the influent water is COD≤1800 mg/L, chromaticity≤900,the effluent water reaches the first-order criterion of “Discharge Standard of Water Pollutant for Dyeing and Finishing of Textile Industry”(GB4287-1992).

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