甲烷氧化菌在填埋场覆盖层中的工程应用(Ⅱ):基质选择性及长效性

针对已筛选获得的甲烷氧化混合菌,选取填埋场覆盖土(LCS)、矿化垃圾(AR)和塘渣(TZ)3种填埋场周边易得的材料为供试生存基质,从基质选择性及长效性角度进行了甲烷减排应用条件的探究及使用效能评估.结果表明,在TZ、LCS、AR、TZ-AR和LCS-AR这5种生存基质中,TZ-AR最适合甲烷氧化混合菌的生长,且TZ与AR的复配比例以5∶5为最佳.甲烷氧化混合菌在TZ-AR的粒径≤4 mm和含水率为20%时具有最高甲烷氧化能力.一次性接种甲烷氧化混合菌在静态体系中的最佳使用有效期为31 d.其在接种量为0.08、0.16、0.20 m L·g-1和0.25m L·g-1时甲烷氧化速率无明显差异,从工程应用角度而言,8%的接种量为最佳.     

初始pH对厌氧环境下污泥中抗生素抗性基因行为特征的影响

污水处理厂产生大量的剩余污泥中含有丰富的抗性基因,给环境带来了潜在风险。以城市污水处理厂的剩余污泥为研究对象,在不同初始p H(对照组、初始p H=3、5、7、9、11)下观察厌氧条件下,8种抗生素浓度以及四环素类抗性基因(tet A、tet G、tet L、tet M、tet O、tet Q、tet W、tet X)、磺胺类抗性基因(sul I、sul II)和Ⅰ类整合子(int I 1)的行为特征。研究结果显示,初始p H对抗生素的降解影响较小,污泥中总抗生素的平均去除率为42%。对照组及初始p H为3、5、7、9、11下的总四环素类抗性基因分别削减0.65 log、0.96 log、0.75 log、0.62 log、0.86 log和0.98 log。不同四环素类抗性基因表现相似,在初始p H=3和初始p H=11下部分抗性基因削减较多,特别是tet A、tet G、tet L、tet O和tet X。2种磺胺类抗性基因均无削减,浓度平均上升0.18log。相关性分析显示,总抗性基因与TN、NH3-N、TP、SCOD(溶解性COD)均存在显著相关性(P0.05)。上述研究结果为污泥厌氧消化中抗生素抗性基因减量条件提供参考依据。     

四环素类抗生素和铜复合污染对猪粪厌氧消化的影响

兽用抗生素和矿物元素添加剂可起到预防动物疾病、促进动物生长、提高饲料转化率等作用,因此被广泛应用于畜禽养殖业。本研究以猪粪中温厌氧消化为研究目标,采用全自动甲烷潜势测试系统,考察了一定浓度的四环素(TC:30 mg·kg~(-1)dry weight,DW)、土霉素(OTC:50 mg·kg~(-1)DW)和金霉素(CTC:15 mg·kg~(-1)DW)对厌氧累积产甲烷量和日产甲烷速率的影响。结果表明,TC、OTC和CTC对猪粪中温厌氧消化累积产甲烷量和日产甲烷速率均有促进作用(累积产甲烷总量提高比例分别为7.9%、0.4%和5.4%)。另外,采用超高效液相色谱-四极杆串联质谱对猪粪厌氧消化前后样品中四环素类抗生素及其代谢产物进行了分析。结果表明,液相中的四环素类抗生素在猪粪厌氧消化过程中得到了明显的去除,去除率达到90%~100%;而固相中只有金霉素和差向异构金霉素有明显的去除效果,去除率分别为41.69%和41.58%。采用Tessier连续提取法对猪粪厌氧消化前后样品中5种形态的铜包括可交换态、碳酸盐结合态、铁锰氧化结合态、有机物结合态、残渣态进行了分析,结果表明,猪粪厌氧消化后,可交换态、碳酸盐结合态和铁锰结合态的铜浓度比厌氧消化前分别降低了1%~9%、0.1%~3%、12%~19%,而有机态和残渣态的铜浓度却在厌氧消化后分别增加了15%~35%、1%~2%。厌氧消化后,70%~80%的铜都是以有机铜的形态存在。铜逐渐从不稳定态转化为相对稳定的有机态和残渣态铜,因此,厌氧消化过程使铜从可生物利用态转变为不可生物利用态,趋于稳定化。     

内循环厌氧反应器流动模型及反应过程模拟

为揭示内循环厌氧反应器放大过程中所出现的规律,本文对反应器中流动模型和反应过程进行了模拟研究,通过对主反应区的停留时间分布的实验研究,确定了主反应区流型可用一平推流与两个并联的全混流进行串联的三参数组合模型进行模拟.在实验范围内,平推流区所占的体积分数约为36%,两个全混流区所占的体积分数分别为53%和11%.结合厌氧反应动力学方程,应用组合模型模拟了实际反应器的状态,并和实验值进行了对比,发现反应器出口处CH_4体积流量最大误差为9.67%,在可允许的范围内.同时,模拟了基质初始COD和温度变化对反应器出口状态的影响.研究表明,与其它模型相比,组合模型计算简洁,同时又有较好的精度,能够满足反应器的设计需要.     

不同有机废水厌氧产酸过程的研究

主要研究了不同类废弃有机物厌氧产酸过程中产生的挥发性脂肪酸的产量和组成比例。研究发现,废糖蜜溶液、蛋白废液和淀粉废液在达到最高产酸量时,超过50%的VFAs是乙酸,其次是丙酸,还含有少量的丁酸和戊酸。废甘油溶液在达到最高产酸量时,产生的VFAs的主要成分是丙酸。4种有机废液中,相同初始COD浓度条件下,淀粉废液产生的VFAs产量最多,初始COD为5000mg/L时最高产量为2.321g/L,其次是废甘油溶液,最高产量是2.244g/L。     

不同养殖模式池塘沉降颗粒营养物质组成特征

2012年4~10月采用自制沉降颗粒收集装置收集主养草鱼和黄颡鱼池塘生态系统中沉降颗粒物,开展了颗粒物质的垂直沉降量以及沉降颗粒中碳氮磷等营养物质的组成及沉降通量的季节变化特征的研究。结果表明:养殖可以显著提高池塘颗粒物质的垂直沉降量,主养草鱼池塘中颗粒物质垂直沉降量显著高于主养黄颡鱼池塘(p0.01),且两种养殖模式池塘颗粒物质沉降量随着养殖时间推进有显著增加的趋势。主养草鱼的池塘中颗粒物质垂直沉降量在100.39~414.66g/(m2·d)之间变化,平均为224.46g/(m2·d),主养黄颡鱼池塘中沉降颗粒物质垂直沉降量在34.14~272.91g/(m2·d)之间变化,平均为155.18g/(m2·d)。两种养殖模式沉降颗粒的碳氮磷成分在养殖周期内的变化规律不明显但具有相似的变化趋势,主养黄颡鱼池塘沉降颗粒中TN、TC、TOC和TON的含量均比同时期主养草鱼高,且均随着养殖时间的推进,沉降颗粒中碳氮磷的总量呈增加趋势。两种养殖模式池塘沉降颗粒中的C/N比值与沉积物中的C/N比值较为接近,表明沉降颗粒与沉积物营养物质来源具有一定的相似性,同时养殖系统内养殖对象与其所处环境的相互依存和相互影响对颗粒物质的产生以及沉降具有重要作用。     

秸秆厌氧发酵产沼气技术现状进展

秸秆是世界上数量最大的可再生资源,但是秸秆内木质纤维素的复杂结构和难降解性限制了秸秆的应用,因此秸秆预处理成为秸秆发酵产气的重要一环。本文介绍了木质纤维素预处理物理技术、化学技术、生物技术、联合处理技术和秸秆厌氧发酵研究进展,并对秸秆预处理技术前景进行展望。     

Aerobic treatment of palm oil mill effluent

In this study treatment of palm oil mill effluent (POME) was investigated using aerobic oxidation based on an activated sludge process. The effects of sludge volume index, scum index and mixed liquor suspended solids during the acclimatizing phase and biomass build-up phase were investigated in order to ascertain the reactor stability. The efficiency of the activated sludge process was evaluated by treating anaerobically digested and diluted raw POME obtained from Golden Hope Plantations, Malaysia. The treatment of POME was carried out at a fixed biomass concentration of 3900+/-200mg/L, whereas the corresponding sludge volume index was found to be around 105+/-5mL/g. The initial studies on the efficiency of the activated sludge reactor were carried out using diluted raw POME for varying the hydraulic retention time, viz: 18, 24, 30 and 36h and influent COD concentration, viz: 1000, 2000, 3000, 4000 and 5000mg/L, respectively. The results showed that at the end of 36h of hydraulic retention time for the above said influent COD, the COD removal efficiencies were found to be 83%, 72%, 64%, 54% and 42% whereas at 24h hydraulic retention time they were 57%, 45%, 38%, 30% and 27%, respectively. The effectiveness of aerobic oxidation was also compared between anaerobically digested and diluted raw POME having corresponding CODs of 3908 and 3925mg/L, for varying hydraulic retention time, viz: 18, 24, 30, 36, 42, 48, 54 and 60h. The dissolved oxygen concentration and pH in the activated sludge reactor were found to be 1.8-2.2mg/L and 7-8.5, respectively. The scum index was found to rise from 0.5% to 1.9% during the acclimatizing phase and biomass build-up phase.     

A study on recovery of oil from sludge containing oil using froth flotation

Induced air flotation was used to recover oil from synthetically prepared sludge containing oil. A commercial surfactant was used as the collector and frother. The effects of various parameters, namely flotation time, initial amount of oil in the feed and the amount of surfactant used on the recovery of oil were investigated. Within the range of operating conditions studied herein, the maximum oil recovery obtained was about 55%. A detailed study of flotation kinetics based on oil recovery was carried out. It showed that the process followed first-order kinetics.     

Some properties of a sequencing batch reactor for treatment of wastewater containing thiocyanate compounds

Thiocyanate (SCN) compounds in photo-processing wastewater (PPWW) could be treated by an SBR system without any release of thiocyanate to the atmosphere during the aeration step. An SCN loading greater than 84 g m(-3)d(-1) showed negative effects on the growth of bio-sludge and removal efficiencies of the system. The acclimatization period of the system was increased with an increase in SCN concentration or loading. The COD, BOD(5), TKN, and SCN removal efficiencies were 96.0 +/- 1.6%, 72 +/- 2%, 49 +/- 5%, and 82 +/- 3%, respectively, under an SCN loading of up to 84 g m(-3)d(-1). The removal efficiency of the system was repressed by SCN due to the repressed growth rate of nitrification bacteria. However, the removal efficiency could be increased with an increase in HRT or a decrease in SCN loading. Also, increases in HRT or decreases in SCN loading led to increased sludge age or solid retention time (SRT) and decreased the sludge volume index (SVI) value. The SRT and SVI of the system with synthetic wastewater containing 840 mg l(-1) SCN under an HRT of 3 days (SCN loading of 280 g m(-3)d(-1)) were 3.9 +/- 0.7 days and 65 +/- 4 ml g(-1), respectively, while they were 11.2+/-0.8 days and 55 +/- 6 ml g(-1), respectively under an HRT of 10 days (SCN loading of 84 g m(-3)d(-1)).