高活性反硝化颗粒污泥的研究

以上流式厌氧污泥床（ＵＡＳＢ）反应器中的反硝化颗粒污泥为样品,研究了颗粒污泥的基本特性。测定出颗粒污泥中的优势无机元素为Ｃａ、Ｐ．颗粒表面以球菌和短杆菌为主。反硝化菌是颗拉中的优势菌群,数量可达６．５ｘ１０^８－１．５ｘ１０^１０个／ｍｌ颗粒污泥。初步鉴定了两株脱氮菌Ｍｉｃｒｏｃｏｃｃｕｓｓｐ．ｓｔｒａｉｎＮ_１和ＰｓｅｕｄｏｍｏｎａｓａｅｒｕｇｉｎｏｓａｓｔｒａｉｎＮ_２．     

气提式内循环硝化反应器运行性能的研究

气提式内循环反应器具有很好的生物硝化性能,能承受高进水氨浓度（78.49mmol/L）,具有高容积转化效率（163.18 mmol/L·d）,运行性能稳定（氨去除率保持在94.42%以上）。在气提式内循环反应器的运行过程中,可产生硝化颗粒污泥。颗粒污泥开始出现的时间约为45d,颗粒污泥的粒径平均值0.83 mm,沉降速度55.53m/h,氨氧化活性0.95mmol (NH⁺₄-N)/g(VS)·d。硝化颗粒污泥也具有厌氧氨氧化活性,氨氧化速率0.23mmol (NH⁺₄-N)/g(VS)·d,亚硝酸还原速率0.24mmol (NO^-₂-N)/g(VS)·d。     

内循环颗粒污泥床硝化反应器流动模型研究

采用脉冲刺激响应技术,对稳态内循环颗粒污泥床硝化反应器进行了示踪试验。根据试验结果,分别运用轴向扩散模型和多釜全混流反应器串联模型,对反应器沉淀区和循环区的流态进行了分析和判断。结果表明,反应器沉淀区的分散数D/uL为0.00148,该区域的流态接近于平推流反应器（PFR）;反应器循环区的串联级数为1.021,该区域的流态接近于全混流反应器（CSTR）。稳态时,反应器的理论水力停留时间为360min,实际水力停留时间为341.2min,反应器中死区所占的体积百分比为5.22％,其中生物体死区为0.75%,水力死区为4.47%,表明反应器结构性能良好。根据试验和分析结果,建立了内循环颗粒污泥床硝化反应器的流动模型,即全混流和平推流的串联组合模型。由流动模型所得的理论停留时间分布曲线与由试验所得的实际停留时间分布曲线吻合良好,两者的平均相对误差为8.56%,表明所建模型具有较高的准确性。     

膜-生物硝化反应器处理含氨废水效能的研究

研究了膜 生物硝化反应器对含氨废水的处理效能以及分离膜的截留和渗透效能。膜_生物反应器启动迅速 ,在水力停留时间为 1d的情况下 ,反应器最高进水浓度达 80mmol(NH₄⁺-N)·L^-1 ,最高容积负荷达 1 12kg(NH₄⁺ -N)·m^-3·d^-1 ,氨氮去除率保持在 95%以上。试验证明 ,分离膜对微生物有良好的截留作用 ,50天内反应器的污泥浓度从 5g·L^-1 增长到 10g·L^-1 ,分离膜表面附着的生物层则对废水氨氮和亚硝氮有进一步的转化作用。在液位差低于 80cm时 ,提高液位差可增大膜渗透通量 ;液位差超过 80cm后 ,增大液位差的膜渗透通量效应很小 ;其中 ,当液位差为 2 0cm左右时 ,膜通量达 2 . 5 1L·m^-2 ·h^-1 ,阻力最小 [(2 . 6 3× 10^-5)m^-1]。该膜_生物硝化反应器可依靠液位差压力驱动出水 ,无需外加动力。     

喷射自吸管式生化反应器研究

本文研究了喷射自吸管式生化反应器的吸气及所液传质特性,提出了吸气量(Qs)和容积氧传递系数(kLa)的数学表达式：Qg=5.2×10^-2W^0.144_cLR^0.079_cD(L-D)^0.328D²_nPoπ——P^o_gTo[(D-Dn)²-1](Pn-Pl)-1)(Kla)₁=0.999(W-V)^0.38V^0.90_sg(L-D)^-0.16(Kla)2=1.003(W-V)^0.71V^0.28_sg(L-D)^-0.32(加C圈)反应器的具优工况为：L/D=320-400,D/D=2.7—3。8,Pn=5—13×10⁴N/m²。Kla最高达4280h^-1,比能耗为0.72—2.16×10³kJ/kgO₂用于培养饲料酵母,酵母浓度达40.04kg/m³.最大生长速率为6.24kg/m³·h,比能耗为1.66—2.52×10³KJ/kg DBM.空气利用率为10—20%.是一般生化反应器的2—4倍。     

自絮凝酵母SPSC01在组合反应器系统中酒精连续发酵的研究

建立了一套由四级磁力搅拌发酵罐串联组成、总有效容积4000mL的小型组合生物反应器系统 ,其中一级罐作为种子培养罐。以脱胚脱皮玉米粉双酶法制备的糖化液为种子培养基和发酵底物 ,进行了自絮凝颗粒酵母酒精连续发酵的研究。种子罐培养基还原糖浓度为100g L ,添加 (NH₄)₂HPO₄ 和KH₂PO₄ 各 20g L ,以0.017h^-1 的恒定稀释速率流加 ,并溢流至后续酒精发酵系统。发酵底物初始还原糖浓度 220g/L ,添加 (NH₄)₂HPO₄ 15g/L和KH₂PO₄2 5g/L ,流加至第一级发酵罐 ,稀释速率分别为 0.017、0.025、0.033、0.040和0.05 0h^-1。实验数据表明 ,自絮凝颗粒酵母在各发酵罐中呈部分固定化状态 ,在稀释速率0.040h^-1 条件下 ,发酵系统呈一定的振荡行为 ,其他四个稀释速率实验组均能够达拟稳态。当稀释速率不超过 0 0 33h^-1 ,流出末级发酵罐的发酵液中酒精浓度可以达到 12 % (V/V)以上 ,残还原糖和残总糖分别在 0 11%和 0 35 % h^-1,流出末级发酵罐的发酵液中酒精浓度可以达到12%（V/V）以上,残还原糖和残总糖分别在0.11%和0.35%（W/V）以下。在稀释速率为0.033h^-1时,计算发酵系统酒精的设备生产强度指标为3.32（g·L^-1·h^-1）,与游离酵母细胞传统酒精发酵工艺相比,增加约1倍。     

纤维载体固定化红螺菌反应器处理发酵废液及其动力学模型

在充填软性纤维材料的玻璃柱式反应器中,利用Rhodopseudomonas palustris Y6光合细菌(PSB)连续处理发酵废液。建立了该处理系统动力学模型。计算出模型参数t K_s=45．56mg／m1,μm=0．224h^-1。模型理论曲线与实验值较吻合。研究得出较适合的稀释率Dopt为o．129^-1’,此时COD去除能力最大为1686．Oppm COD／h。本文为纤维载体固定化PSB处理有机废水提供了一些放大操作依据。     

温度和水分变化对冻土区泥炭地土壤氮循环功能基因丰度的影响

以大兴安岭多年冻土区泥炭地为研究对象,通过室内模拟增温实验,研究温度升高对不同深度（0-150 cm）土壤氮循环功能基因丰度的影响。同时针对0-20 cm和20-40 cm土壤设置两个水分处理,分别为土壤原始含水量和淹水状态,研究水分变化对表层土壤氮循环功能基因丰度的影响。结果表明温度升高显著提高了活动层（0-60 cm）、过渡层（60-80 cm）、永冻层（80-100 cm）中nifH、nirK基因丰度,温度升高显著提高了活动层（0-40 cm）和过渡层（60-80 cm）中nirS基因丰度。温度升高显著提高了过渡层（60-80 cm）NH₄⁺-N和较深永冻层（140-150 cm）NO₃^--N的含量,但降低了过渡层（60-80 cm）NO₃^--N和较深永冻层（120-150 cm）NH₄⁺-N的含量,相关性分析表明,NH₄⁺-N含量与nifH和nirS基因丰度呈显著正相关,NO₃^--N含量与nirK基因丰度呈显著正相关,说明温度升高能够通过改变微生物丰度促进过渡层固氮作用和反硝化作用。在增温条件下,淹水处理使表层土壤nirS和nirK基因丰度及NH₄⁺-N含量降低,但提高了NO₃^--N含量,说明淹水造成了过度还原的条件使反硝化底物浓度降低,降低反硝化微生物活性进而抑制了土壤反硝化作用。该结果对于明确未来气候变化影响下冻土区泥炭地土壤氮循环过程具有重要意义。     

CellCul－20A反应器的丝网间液体交换速率及氧传递模型

针对笼式通气搅拌生物反应器的特点,本文提出了一种简单可信的测量丝网内外液体交换速率的实验方法,根据此方法,在CellCul-20 A生物反应器中得出了通过丝网的液体交换速率关联式: 单层丝网：Qs=1．93×1O^-5N^1.81+1．13×10^-4UG^0.61(Ⅰ) 双层丝网：Qs=3．42×10^-5N^1.49+1．46×10^-4UG ^0.68 (Ⅱ)并在此基础上,建立了台适的深层通气的氧传递模型,得到： 1- 1- 1- (K_La)d.Vc Qs + Vb.[(K_La)b-(K_La)d](Ⅲ)理论分析和实验结果表明,增大丝网内的液体体积和提高丝网内的氧传递速率,可以有效地提高反应器的体积氧传递系数。     

抗IBDV独特型抗体杂交瘤细胞株的建立及其产物生物学特性测定

用纯化的抗IBDV IgG免疫Balb/c小鼠,取其脾细胞与SP2/0细胞在聚乙二醇（PEG）作用下融合,ELISA法检测筛选,经有限稀释法克隆3次,获得2株（5F₄株,2B₆株）分泌抗IBDV独特型抗体的杂交瘤细胞株,其能诱生Balb/c小鼠产生ELISA抗体效价分别为1∶12 800和1∶25 600的含抗IBDV独特型抗体的腹水。用此独特型抗体与福氏完全佐剂和福氏不完全佐剂乳化制备成抗IBDV独特型抗体疫苗,免疫接种SPF鸡和普通京白公鸡,然后用IBDV强毒株(SD株)2000 ELD50攻毒,SPF鸡免疫组50只,有5只发病、2只死亡;对照组10只全部发病,8只死亡。普通京白鸡免疫组30只,有7只发病, 1只死亡;对照组10只全部发病,6只死亡。经X²检验,SPF鸡X²＝34.15,普通鸡X²＝16.68,查X²值表得X²_(1)0.01＝6.63, SPF鸡X²和普通鸡X2均大于X²_{(1) 0.01}（P＜0.01）,由此表明抗IBDV独特型抗体疫苗具有很好的免疫原性,对易感日龄的SPF鸡和普通鸡均具有极其明显的保护作用。从而证实了抗IBDV独特型抗体疫苗有潜在的研究和应用价值。     

Bioaugmentation as a tool for improving the start-up and stability of a pilot-scale partial nitrification biofilm airlift reactor

The effectiveness of bioaugmentation in the improvement of the start-up of a biofilm airlift reactor to perform partial nitrification was investigated. Two identical biofilm airlift reactors were inoculated. The non-bioaugmented reactor (NB-reactor) was inoculated with conventional activated sludge, whereas the bioaugmented reactor (B-reactor) was seeded with the same conventional activated sludge but bioaugmented with nitrifying activated sludge from a pilot plant performing full nitritation under stable conditions (100% oxidation of influent ammonium to nitrite). The fraction of specialized nitrifying activated sludge in the inoculum of the B-reactor was only 6% (measured as dry matter). To simplify comparison of the results, operational parameters were equivalent for both reactors. Partial nitrification was achieved significantly faster in the B-reactor, showing a very stable operation. The results obtained by fluorescence in situ hybridization assays showed that the specialized nitrifying biomass added to the B-reactor remained in the biofilm throughout the start-up period.     

一种新型颗粒污泥——无机核颗粒污泥的形成和机理探讨

在人工配水以葡萄糖为主要基质长期运行的EGSB反应器中,发现了一种具有特殊结构的新型厌氧颗粒污泥———无机核颗粒污泥。扫描电镜观察,其内部形成较大直径、带有清晰微生物自溶痕迹、均匀分布的无机质核心,外层则为紧密的微生物所包裹。通过能谱、X射线衍射分析,确定内核无机质为Ca5(PO4·CO3)3(OH)(碳磷灰石)。根据结构特征,提出了无机核颗粒污泥的生长过程模型。进一步分析认为EGSB反应器的宏观pH值环境和颗粒污泥微观pH值环境是形成颗粒污泥无机核的原因。     

Liquid circulation velocity in the inverse fluidized bed airlift reactor

Results of the investigations of the liquid circulation velocity in the external loop airlift reactor with the fluidized bed in the downcomer are reported. Densities of solid particles are much lower than the liquid density. It is found that the curve of the liquid circulation velocity dependence on the gas flow rate consists of two different parts. A slow linear increase of the liquid circulation velocity is observed if the gas velocity is lower than the minimum fluidization velocity. An exponential course of the liquid circulation velocity curve is observed if the gas flow rate exceeds the minimum fluidization velocity. A theoretical equation for the prediction of liquid circulation velocity for gas velocities higher than the minimum fluidization velocity is presented.     

Development of thermophilic methanogenic sludge in compartmentalized upflow reactors

The characteristics and development of thermophilic anaerobic sludge in upflow staged sludge bed (USSB) reactors were studied. The compartmentalized reactors were inoculated with partially crushed mesophilic granular sludge and then fed with either a mixture of volatile fatty acids (VFA) or a mixture of sucrose and VFA. The staged degradation of the soluble substrate in the various compartments led to a clear segregation of specific types of biomass along the height of the reactor, particularly in reactors fed with the sucrose-VFA mixture. Both the biological as well as the physical properties of the cultivated sludge were affected by the fraction of nonacidified substrate. The sludge in the first compartment of the reactor treating the sucrose-VFA mixture was whitish and fluffy, most likely resulting from the development of acidifying bacteria. Sludge granules which developed in the top part of this reactor possessed the highest acetogenic and methanogenic activity and the highest granule strength as well. The experiments also revealed that the conversion of the sucrose-VFA mixture into methane gradually deteriorated at prolonged operation at high organic loading rates (50 to 100 g COD . L(-1) . day(-1)). Stable long-term performance of a reactor can only be achieved by preserving the sludge segregation along the height of the reactor. In the reactor fed solely with the VFA mixture little formation of granular sludge occurred. In this reactor, large differences in sludge characteristics were also observed along the reactor height. Li(+)-tracer experiments indicated that the hydraulic regime in the USSB reactor is best characterized by a series of at least five completely mixed reactors. The formation of granular sludge was found to influence the liquid flow pattern. (c) 1996 John Wiley & Sons, Inc.     

Feasibility of expanded granular sludge bed reactors for the anaerobic treatment of low-strength soluble wastewaters

The application of the expanded granular sludge bed (EGSB) reactor for the anaerobic treatment of low-strength soluble wastewaters using ethanol as a model substrate was investigated in laboratory-scale reactors at 30oC. Chemical oxygen demand (COD) removal efficiency was above 80% at organic loading rates up to12 g COD/L . d with influent concentrations as low as 100 to 200 mg COD/L. These results demonstrate the suitability of the EGBS reactor for the anaerobic treatment of low-strength wastewaters. The high treatment performance can be attributed to the intense mixing regime obtained by high hydraulic and organic loads. Good mixing of the bulk liquid phase for the substrate-biomass contact and adequate expansion of the substrate-biomass contact and adequate expansion of the sludge bed for the degassing were obtained when the liquid upflow velocity (V(up)) was greater than 2.5 m/h. Under such conditions, an extremely low apparent K(s) value for acetoclastic methanogenesis of 9.8 mg COD/L was observed. The presence of dissolved oxygen in the wastewater had no detrimental effect on the treatment performance. Sludge piston flotation from pockets of biogas accumulating under the sludge bed occurred at V(up) lower than 2.5 m/h due to poor bed expansion. This problem is expected only in small diameter laboratory-scale reactors. A. more important restriction of the EGSB reactor was the sludge washout occurring at V(up) higher than 5.5 m/h and which was intensified at organic loads higher than 7 g COD/L. d due to buoyancy forces from the gas production. To achieve an equilibrium between the mixing intensity and the sludge hold-up, the operation should be limited to an organic loading rate of 7 g COD/L d. and to a liquid up-flow velocity between 2.5 and 5.5 m/h (c) 1994 John Wiley & Sons, Inc.     

Assessment of the addition of Thiobacillus denitrificans and Thiomicrospira denitrificans to chemolithoautotrophic denitrifying bioreactors

The aim of the present study was to assess the impact of adding cultures of Thiobacillus denitrificans and Thiomicrospira denitrificans to two upflow anaerobic sludge bed (UASB) reactors: one inoculated with granular sludge and the other filled only with activated carbon (AC). The performances of the bioreactors and the changes in biomass were compared with a non-bioaugmented control UASB reactor inoculated with granular sludge. The reactors inoculated with granular sludge achieved efficiencies close to 90% in nitrate and thiosulfate removal for loading rates as high as 107 mmol-NO3 -/l per day and 68 mmol-S2O3 2-/l per day. Bioaugmentation with Tb. denitrificans and Tm. denitrificans did not enhance the efficiency compared to that achieved with non-bioaugmented granular sludge. The loading rates and efficiencies were 30-40% lower in the AC reactor. In all the reactors tested, Tb. denitrificans became the predominant species. The results strongly suggest that this bacterium was responsible for denitrification and sulfoxidation within the reactors. We additionally observed that granules partially lost their integrity during operation under chemolithoautotrophic conditions, suggesting limitations for long-term operation if bioaugmentation is applied in practice.