城市污水处理厂剩余污泥中温厌氧消化处理研究

应用污水处理厂剩余污泥开展污泥中温厌氧消化实验，对一系列影响污泥厌氧消化反应的因素进行了考察。实验结果表明：由于污泥C／N值较低，单独消化非常困难，有机物分解率比较低，分解速度慢，气体发生量少。在35℃时，污泥投配率为7．5％～10％，基质的去除率可达到35．54％。37．62％，去除单位基质的产甲烷量为O．265～O.274m^3／kgCOD。     

多元回归和BP人工神经网络模型对混合厌氧消化产气量的预测研究

在中温且控制pH值条件下,对脂肪类单基质和城市污水厂剩余污泥进行混合厌氧消化试验。基于多元回归原理和BP人工神经网络原理,对其建立产气量预测模型。由实验数据计算得出:两个阶段多元回归模型的预测平均准确率分别为75.69%和79.29%;BP神经网络模型的预测平均准确率为79.05%。通过对比两种模型的预测结果可知,两种模型都有较高的预测准确率,但BP模型的预测准确率更高,更适用于混合厌氧消化产气量预测。     

厌氧氨氧化工艺处理猪场废水沼液的试验研究

本文以实际猪场沼气废水为研究对象，以ASBR为反应器，接种厌氧消化污泥培养厌氧氨氧化细菌，厌氧氨氧化阶段成功启动后，研究了厌氧氨氧化脱氮最佳运行工艺。试验研究表明，厌氧氨氧化反应适宜的温度在35（±1）℃之间，适宜的pH在7．5—8．0之间，HRT选用24h。当达到最佳运行参数时，NH4＋-N的去除率达到87．6％，NO2- -N的去除率达到99．96％。     

石墨相氮化碳降解水中氨氮

利用石墨相氮化碳降解水中氨氮,并对该材料降解氨氮的效果进行考察。探究了在氙灯照射下,不同初始pH以及不同初始氨氮含量条件下对氨氮降解的影响。结果表明：在氙灯照射下,当初始pH=12,初始氨氮含量为7.5μg时,石墨相氮化碳对氨氮具有良好的降解效果;当初始pH=13时,控制初始氨氮含量为7.5μg,光催化2 h后,氨氮去除率为95.68%。采用伪一级动力学模型进行研究,石墨相氮化碳在碱性条件下对氨氮有良好的降解速率,可能归因于随着初始pH的增大,溶液中存在更多的OH-和·OH,从而增强光催化效果。     

一株纤维素分解茵利用枳实废渣产酶条件的研究

以枳实废渣为碳源，对产纤维素酶G2茵进行固体发酵，通过测定FPA、CMC、C1酶活的大小，对其产酶条件进行优化研究。结果表明产酶最适条件为：枳实在发酵前需进行酸处理；氮源为硫酸铵；含水率为70％；初始pH为5～6；发酵周期为6天。在以上最适条件下，G2菌酶活力为FPA：31．8IU／ml，CMC：11．86IU／ml，C1：15．79IU／ml。     

市政污泥与高浓度废弃物的厌氧共消化：一种生物质能源净产生的途径

厌氧共消化是一种绿色、实用的回收废弃物中能源的技术。本文介绍了厌氧共消化技术的原理，并介绍了美国佐治亚州F. Wayne Hil水资源处理中心采用油脂废弃物（FOG）和含糖工业废水与市政污泥进行连续流厌氧共消化的实际应用案例。结果表明，厌氧共消化可显著提高甲烷产量达2倍以上，甲烷产量随着高浓度有机废弃物负荷率及厌氧消化反应器停留时间的延长而增加，且COD和VS降解率可保持在合理范围内，经济效益显著。     

间接电化学降解亚甲基蓝废水的可行性研究

研究以ClO^-／Cl^-作媒介，间接电化学降解亚甲基蓝模拟废水的可行性。结果表明，亚甲基蓝的电化学降解与电极材料、电流密度以及添加剂种类等因素有关。以石墨为阳极，不锈钢为阴极，在无隔膜的烧杯中放置50ml浓度为1000mg/L的亚甲基蓝模拟废水，在室温25℃，pH6．0－8．0，槽电压10V，电流密度30．0mA/cm^2，Cl^-加入量2g/L的条件下，电解60min后，亚甲基蓝溶液的平均消色率达到98．0％，CODcr降解率为97．0％，BOD5降解率为99．0％；用浸涂过MnO2薄膜的石墨棒作阳极可显著加快其消解速率，而用浸涂过CeO2薄膜的石墨棒作阳极对其消解速率无明显的影响。并初步讨论了其降解机理。     

垃圾渗滤液COD降解菌株的筛选及其降解特性初探

采用不断增大垃圾渗滤液浓度的方法，筛选出3株能有效降解渗滤液的微生物DL01、DL02、DL03。以COD的去除率作为评价指标，研究常压。不同时间、温度以厦pH下优势菌株对渗滤液COD的降解特性。初步结果表明，优势菌株的接种量以7．5％（体积分数）最佳；各优势菌株对温度的适应范围较广，在20℃-40℃内具有较好的降解效果，COD的去除率均高于15．7％；3株优势茼株最适pH均为7，不同菌株耐受pH的范围不同，其中DL01对pH的适应范围最广，为6—9；在35℃，pH为7时，DL01对渗滤液COD的去除能力最强为35．5％，DL02和DL03分别为25．0％和21．5％；在此相同条件下，混合菌株比单一菌株的降解效果好，为39．3％；加入碳源有利于渗滤液COD的降解。无机氮源的加入使COD的去除率降低。     

餐厨垃圾厌氧消化系统酸化调控研究进展

介绍了餐厨垃圾的特点，针对餐厨垃圾在厌氧消化过程中容易出现的酸化抑制，梳理了目前常用的缓冲溶液添加、多元物料混合厌氧消化和两相厌氧消化等酸化调控技术，以及处于研发阶段的生物预处理、添加生物炭、驯化培养耐酸型产甲烷菌等酸化调控技术。比较了各种技术的优势与不足，提出未来的技术路径和研究方向，以期为餐厨垃圾厌氧消化工程的稳定运行提供技术支撑。     

中温厌氧消化垃圾焚烧发电厂渗滤液的试验研究

采用逐渐提高有机负荷的半连续进料方式,研究中温(35℃左右)条件下,猪粪为接种物,厌氧消化焚烧发电厂垃圾渗滤液的消化规律。试验以5%为单位,由5%体积负荷渗滤液起开始填料,逐步提高至35%的体积负荷。试验进行的7个负荷,消化系统pH值稳定在7.2~7.8之间,碱度、氨氮浓度较高,分别在7803~17948 mg/L、673~1630 mg/L之间,为系统提供了良好的酸碱缓冲环境。低负荷时,VFA值较低,生物气中甲烷含量稳定在60%左右;高负荷时,随着渗滤液的加入,VFA值波动较大,甲烷含量也随VFA值的变化起伏波动(25%负荷时,甲烷含量出现峰值,高达75.5%)。消化系统共进料2800 mL渗滤液(即197.3 gCODCr),累计产气量83086 mL,平均每gCODCr产沼气约421.1 mL(平均gCODcr产甲烷约273.7 mL)。进水渗滤液CODCr浓度为70472 mg/L,实验结束时,消化液CODCr浓度降至3373 mg/L,CODCr去除率高达95.2%。     

Thermophilic adaptation of a mesophilic anaerobic sludge for food waste treatment

As opposed to mesophilic, thermophilic anaerobic digestion of food waste can increase the biogas output of reactors. To facilitate the transition of anaerobic digesters, this paper investigated the impact of adapting mesophilic sludge to thermophilic conditions. A 5L bench scale reactor was seeded with mesophilic granular sludge obtained from an up-flow anaerobic sludge blanket digester. After 13 days of operation at 35 degrees C, the reactor temperature was instantaneously increased to 55 degrees C and operated at this temperature until day 21. The biomass was then fed food waste on days 21, 42 and 63, each time with an F/M (Food/Microorganism) ratio increasing from 0.12 to 4.43 gVS/gVSS. Sludge samples were collected on days 0, 21, 42 and 63 to conduct substrate activity tests, and reactor biogas production was monitored during the full experimental period. The sludge collected on day 21 demonstrated that the abrupt temperature change had no pasteurization effect, but rather lead to a biomass with a fermentative activity of 3.58 g Glucose/gVSS/d and a methanogenic activity of 0.47 and 0.26 g Substrate/gVSS/d, related respectively, to acetoclastic and hydrogenophilic microorganisms. At 55 degrees C, an ultimate gas production (Go) and a biodegradation potential (Bo) of 0.2-1.4 L(STP)/gVS(fed) and of 0.1-0.84 L(STP) CH(4)/gVS(fed) were obtained, respectively. For the treatment of food waste, a fully adapted inoculum was developed by eliminating the initial time-consuming acclimatization stage from mesophilic to thermophilic conditions. The feeding stage was initiated within 20 days, but to increase the population of thermophilic methanogenic microorganisms, a substrate supply program must be carefully observed.     

气田压裂返排液回用影响因素研究

针对气田压裂返排液回用配制压裂液的水质要求,研究了pH值、金属离子、细菌和泡沫对处理后液体配制压裂液的影响。结果表明,通过调节pH值、控制金属离子浓度、加入杀菌剂和消泡剂可以达到回用配制压裂液的要求。其中,pH值应控制在6.5左右;当Na2CO3和NaOH的复配比为800/600、NaOH投加量为300mg/L时,能有效去除Ca2+、Mg2+、Fe3+等离子的影响;杀菌剂采用气田压裂专用杀菌剂;消泡剂采用二甲基硅油。实验在气井井场采用撬装微涡流混凝装置处理气田压裂返排液,并对上清液回用配液,回用率达到98.4%。     

The Effects of Gas Flow Rate and the Interval Time of Water Supplement on Ethanol Production of Rice Straw by Simultaneous Saccharification and Fermentation

In the present work, characteristics of ethanol production from a single particle composing of pretreated rice straw, cellulase, and β-glucosidase were invesitgated by simultaneous saccharification and fermentation (SSF). The experiment experienced a start-up stage for S. cerevisiae biofilm formation, which was operated at an initial pH value of 4.8 for yeast solution, culture temperature of 30°C, flow rate of 0.8 mL/min for yeast solution, and stably operating stage for ethanol production at a culture temperature of 30°C. Investigations found that the maximal ethanol yield of 9.7 mg/g and the biofilm thickness of 0.37 mm were obtained at 30 mL/min of carrier gas flow rate. Also, the optimal interval time of water supplement was 4 h for SSF. The results show that the appropriate gas flow rate and the interval time of water supplement can keep the high activities of biofilm and enzymes during SSF and result in a high ethanol yield.     

Carbon turnover and ammonia emissions during composting of biowaste at different temperatures

The effects of different process temperatures (40, 55, and 67 degrees C) during composting of source-separated household waste were studied in a 200 L compost reactor at an oxygen concentration of 16%. The overall decomposition measured as carbon mineralization, decomposition of different carbon constituents, and the dynamics of nitrogen mineralization and the microbial community, are reported. Ammonia emissions at 67 degrees C were more than double those at lower temperatures, and they were lowest at 40 degrees C. The decomposition rate, measured as CO2 emission, was highest at 55 degrees C. Decomposition of crude fat was slower at 40 degrees C than at 55 and 67 degrees C. The peak in microbial biomass was largest in the run at 40 degrees C, where substantial differences were seen in the microbial community structure and succession compared to thermophilic temperatures. Biowaste composting can be optimized to obtain both a high decomposition rate and low ammonia emissions by controlling the process at about 55 degrees C in the initial, high-rate stage. To reduce ammonia emissions it seems worthwhile to reduce the temperature after an initial high-temperature stage.     

Effects of cattle slurry acidification on ammonia and methane evolution during storage

Slurry acidification before storage is known to reduce NH(3) emissions, but recent observations have indicated that CH(4) emissions are also reduced. We investigated the evolution of CH(4) from fresh and aged cattle slurry during 3 mo of storage as influenced by pH adjustment to 5.5 with sulfuric acid. In a third storage experiment, cattle slurry acidified with commercial equipment on two farms was incubated. In the manipulation experiments, effects of acid and sulfate were distinguished by adding hydrochloric acid and potassium sulfate separately or in combination, rather than sulfuric acid. In one experiment sulfur was also added to slurry as the amino acid methionine in separate treatments. In each treatment 20-kg portions of slurry (n = 4) were stored for 95 d. All samples were subsampled nine to 10 times for determination of NH(3) and CH(4) evolution rates using a 2-L flow-through system. In all experiments, the pH of acidified cattle slurry increased gradually to between 6.5 and 7. Acidification of slurry reduced the evolution of CH(4) by 67 to 87%. The greatest reduction was observed with aged cattle slurry, which had a much higher potential for CH(4) production than fresh slurry. Sulfate and methionine amendment to cattle slurry without pH adjustment also significantly inhibited methanogenesis, probably as a result of sulfide production. The study suggests that complex microbial interactions involving sulfur transformations and pH determine the potential for CH(4) emission during storage of cattle slurry, and that slurry acidification may be a cost-effective greenhouse gas mitigation option.     

Biological recycling of used baby diapers in a small-scale composting system

In Mexico used disposable diapers account for 6.5% of the urban waste that is sent to landfills, as no alternative treatment or valorization options is available. Due to their mixed organic–inorganic composition, they are usually perceived as a problematic non-biodegradable waste; nevertheless, due to their high cellulose content they could be recycled biologically in order to recover the nutrients present in them. This research assessed the feasibility of composting them along with yard waste, in 200 L bioreactors. An initial mixture of fresh trims of grass (55%), dry leaves (10%), fresh leaves (15%) and mulch (20%) was prepared and characterized to achieve an adequate C/N relationship. In the selected reactors 30% (mass basis) of previously shredded used baby diapers containing urine was added. The composting process lasted three months. Temperature, moisture, pH, nitrogen, CO₂ production, organic matter, C/N ratio, volume and mass reduction were measured and recorded periodically. The composting process was not affected by the presence of diapers. Temperature rose to 60–70 °C in the initial thermophilic phase, and reached a final plateau of 20–30 °C. The initial high temperatures allowed to eliminate the pathogens, as shown in the microbiological tests. Volume and mass of the substrates decreased more than 50% by the end of the process. Mass reduction for diapers was 87%, and only the plastic films were recovered. The final compost had good quality and accomplished with the limits set in the local regulation, except by pH, which has slightly above the set limit. It can be used as a soil amendment, as shown in the phytotoxicity tests performed using tomato. The results show that this is a feasible, affordable option for the valorization of used disposable diapers, which could be applied in small communities or daycare centers.     

The effects of leachate recirculation with supplemental water addition on methane production and waste decomposition in a simulated tropical landfill

In order to increase methane production efficiency, leachate recirculation is applied in landfills to increase moisture content and circulate organic matter back into the landfill cell. In the case of tropical landfills, where high temperature and evaporation occurs, leachate recirculation may not be enough to maintain the moisture content, therefore supplemental water addition into the cell is an option that could help stabilize moisture levels as well as stimulate biological activity. The objectives of this study were to determine the effects of leachate recirculation and supplemental water addition on municipal solid waste decomposition and methane production in three anaerobic digestion reactors. Anaerobic digestion with leachate recirculation and supplemental water addition showed the highest performance in terms of cumulative methane production and the stabilization period time required. It produced an accumulated methane production of 54.87 l/kg dry weight of MSW at an average rate of 0.58 l/kg dry weight/d and reached the stabilization phase on day 180. The leachate recirculation reactor provided 17.04 l/kg dry weight at a rate of 0.14l/kg dry weight/d and reached the stabilization phase on day 290. The control reactor provided 9.02 l/kg dry weight at a rate of 0.10 l/kg dry weight/d, and reached the stabilization phase on day 270. Increasing the organic loading rate (OLR) after the waste had reached the stabilization phase made it possible to increase the methane content of the gas, the methane production rate, and the COD removal. Comparison of the reactors' efficiencies at maximum OLR (5 kgCOD/m(3)/d) in terms of the methane production rate showed that the reactor using leachate recirculation with supplemental water addition still gave the highest performance (1.56 l/kg dry weight/d), whereas the leachate recirculation reactor and the control reactor provided 0.69 l/kg dry weight/d and 0.43 l/kg dry weight/d, respectively. However, when considering methane composition (average 63.09%) and COD removal (average 90.60%), slight differences were found among these three reactors.     

通风条件对城市污水厂污泥好氧堆肥过程的影响

本文选择堆肥熟料作为添加剂与城市污水厂污泥混合进行好氧堆肥。通过对温度、耗氧速率、有机物、含水率、pH值和氨氮等指标的分析,重点研究了不同通风条件对堆肥过程的影响。实验结果表明,污泥与熟料混合后,有机物含量较低,堆肥速率较快,对通风条件的改变比较敏感。当通风量低于0.025m3/(m3.min)时,堆肥前期系统供氧不足,堆肥速率较慢,耗时长,同时堆体内变为厌氧环境,pH值变低,臭气产生量高;当通风量高于0.05m3/(m3.min)以及采用变风量通风时,在保证供氧量充足的同时,具有较长的高温期,具有臭气产生量小、堆肥速率快的优点,但采用变风量通风更加节能。     

Formaldehyde degradation in the presence of methanol by photo-Fenton process

In this study, the photo-Fenton process for the degradation of formaldehyde was investigated in lab-scale experiments. Results showed that methanol, the additive chemical in a commercial product of formaldehyde, was also decomposed during the formaldehyde oxidation reaction. The oxidation reaction was in three-stages. The first stage was the Fe(2+)/H(2)O(2) reaction in which both formaldehyde and methanol were swiftly decomposed. The second and the third stages exerted a somewhat less rapid degradation of both chemicals. The first stage of the oxidation reaction can be discussed by means of the initial average rate and the third stage or Fe(3+)/H(2)O(2) stage was found to follow the first order reaction rate. The reaction was influenced by the initial pH, the concentration of hydrogen peroxide, the amount of ferrous ions. The initial pH at 2.6 provided the highest removal efficiencies in this system. In addition, the competition between formaldehyde and methanol was investigated and described as r(m)/r(f), where r(m) and r(f) were the initial rates of methanol and formaldehyde, respectively. The addition of methanol exhibited a competitive effect on formaldehyde degradation. The removal of formaldehyde decreased with increasing methanol concentration. At the high concentrations of methanol, the oxidation reaction of formaldehyde was repressed. It appears that all values of r(m)/r(f) obtained from the experiments are lower than the theoretical values.