锅水碱度和pH值的相关性研究

研究了工业锅炉锅水碱度和pH值对锅炉的影响，对锅水碱度和pH值的相关性做了定量计算，提出了碱度和PH值同时达标的控制方法，经过实践证明效果良好。     

鲤鱼鱼鳃微环境酸碱条件与铜形态分布模拟

用鱼鳃微环境测定装置和化学平衡计算方法,研究了在人工河水中暴露于铜的鲤鱼鳃部微环境的pH、碱度、粘液含量和铜形态分布.结果发现,鱼鳃pH平衡点为6.92,人工河水pH高于或低于此值时,鱼鳃微环境pH偏低或偏高.变化幅度约达-0.6至0.4 个pH单位.根据实测结果分别建立了计算人工河水和鱼鳃微环境碱度以及鱼鳃粘液分泌量随暴露铜含量和pH变化的定量模型.化学平衡计算结果说明,在pH6至9范围内,人工河水中优势态铜从游离态铜过渡到羟基络合态铜.由于粘液和pH差异的影响,鱼鳃微环境中生物有效态铜含量显著低于人工河水.这样的差别在酸性条件下尤为显著.     

Effect of alkalinity on nitrite accumulation in treatment of coal chemical industry wastewater using moving bed biofilm reactor

Nitrogen removal via nitrite （the nitrite pathway） is more suitable for carbon-limited industrial wastewater. Partial nitrification to nitrite is the primary step to achieve nitrogen removal via nitrite. The effect of alkalinity on nitrite accumulation in a continuous process was investigated by progressively increasing the alkalinity dosage ratio （amount of alkalinity to ammonia ratio, mol/mol）. There is a close relationship among alkalinity, pH and the state of matter present in aqueous solution. When alkalinity was insufficient （compared to the theoretical alkalinity amount）, ammonia removal efficiency increased first and then decreased at each alkalinity dosage ratio, with an abrupt removal efficiency peak. Generally, ammonia removal efficiency rose with increasing alkalinity dosage ratio. Ammonia removal efficiency reached to 88% from 23% when alkalinity addition was sufficient. Nitrite accumulation could be achieved by inhibiting nitrite oxidizing bacteria （NOB） by free ammonia （FA） in the early period and free nitrous acid in the later period of nitrification when alkalinity was not adequate. Only FA worked to inhibit the activity of NOB when alkalinity addition was sufficient.     

重碳酸盐碱度对电吸附设备除盐性能影响的研究

为了系统地考察重碳酸盐碱度对电吸附设备除盐性能的影响,利用小型电吸附模块对含有不同重碳酸盐碱度的原水水质进行处理.实验结果表明,随着其含量从170 mg/L增加到400 mg/L,电吸附设备的除盐率明显下降.通过对起始工作电流降低这一变化作理论分析,认为重碳酸盐碱度在电吸附模块内部积存结垢是影响电吸附设备除盐性能的重要原因,并通过实验证实其与钙离子共同作用导致了结垢.     

碱度对UASB处理淀粉废水影响的研究

通过UASB中试装置对淀粉废水处理工艺中不同碱度对UASB反应器中的碱度和酸化的影响的研究,论述了减少碱度投加的途径和酸化的预防与系统恢复.补充碱度可以防止酸化,使反应器处于良好运行状况.通过控制运行条件可以有效降低厌氧处理中碱度需求,在最大程度上降低厌氧处理运行费用.阐述了日常监测的方法,以及预防酸化的产生的途径.     

浅析低压锅炉锅水pH值和碱度的关系及锅水碱度偏低的应对措施

通过对在用锅炉的水质监测，分析了为何锅水pH值合格而锅水碱度偏低的原因，并对锅水碱度偏低提出应对措施。     

厌氧颗粒污泥膨胀床原理特征分析

从污泥床层流态、生化反应动力学、体系物相平衡角度分析了以循环为特征的厌氧颗粒污泥膨胀床反应器的结构特点,基质代谢和酸碱平衡特征,进而得出:高面积(H /A)和回流比(R)是实现反应器较高上升流速的结构和运行指标;回流引起反应器基质代谢特征的变化,同时使反应器处理增强;厌氧颗粒污泥膨胀床的运行方式对调解、平衡系统的碱度、pH值起着积极的作用。     

Effects on nano zero-valent iron reactivity of interactions between hardness, alkalinity, and natural organic matter in reverse osmosis concentrate

Nanoscale zero-valent iron （NZVI） is considered to have potential to reduce nitrate in the concentrate generated by high pressure membrane processes aimed at water reuse. However, it is necessary to verify the effect of the matrix components in the concentrates on NZVI reactivity. In this study, the influence of hardness, alkalinity, and organic matter on NZVI reactivity was evaluated by the response surface method （RSM）. Hardness （Ca/＋） had a positive effect on NZVI reactivity by accelerating iron corrosion. In contrast, alkalinity （bicarbonate; HCO3） and organic matter （humic acid; HA） had negative effects on NZVI reactivity due to morphological change to carbonate green rust, and to competitive adsorption of HA, respectively. The validity of the statistical prediction model derived from RSM was confirmed by an additional confirmation experiment, and the experimental result was within the 95% confidential interval. Therefore, it can be indicated that the RSM model produced results that were statistically significant.     

碱度对低氨氮部分亚硝化的影响与机理分析

为了探讨进水碱度对低氨氮废水部分亚硝化过程的影响与机理,在控制碱度的条件下启动并运行SBR部分亚硝化反应器。结果表明,控制碱度/NH_4~+-N为3.67～4.05可成功实现低氨氮废水部分亚硝化反应器的启动和稳定运行,亚硝酸盐累积率90%。将稳定运行的SBR部分亚硝化反应器与厌氧氨氧化反应器串联运行,系统TN去除率为37.3%～84.3%。周期试验显示,当碱度值70 mg/L时,SBR部分亚硝化反应器NH_4~+-N转化速率介于2.81～5.67 mg/(L·h),当碱度减小至70 mg/L,NH_4~+-N转化速率明显下降,当碱度60 mg/L时,亚硝化反应停止。机理分析表明,以HCO_3~-盐为碱度物质时,碱度值70 mg/L可导致系统无机碳源匮乏,这是影响NH_4~+-N转化速率和控制亚硝化反应进程的主要原因。     

硫自养反硝化耦合厌氧氨氧化脱氮条件控制研究

采用全混式厌氧搅拌罐,研究自养条件下,厌氧氨氧化与硫自养反硝化共同存在时,前者对系统中硫酸盐的产生和碱度消耗的影响.投加单质硫颗粒50 g·L~(-1),接种厌氧氨氧化颗粒污泥100 g·L~(-1)(湿重),控制温度35℃±0.5℃,搅拌强度120r·min-1,p H为8.0~8.4.启动硫自养反硝化阶段,进水硝酸盐浓度为200 mg·L~(-1),水力停留时间为5.3 h,反应器硝态氮负荷达0.56~0.71 kg·(m~3·d)~(-1).硫自养反硝化耦合厌氧氨氧化反应过程中,添加60 mg·L~(-1)氨氮后,硝态氮负荷仍维持在0.66~0.88kg·(m~3·d)~(-1),氨氮负荷为0.27 kg·(m~3·d)~(-1).反应体系内单位硝酸盐转化产生的硫酸盐Δn(SO~(2-)_4)∶Δn(NO~-_3)由1.21±0.06降低至1.01±0.10,Δ(IC)∶Δ(NO~-_3-N)由0.72±0.1降低至0.51±0.11,出水p H值由6.5上升至7.2.序批试实验优化反应条件:在搅拌强度G_T值为22~64 s~(-1),p H值为8.08时,耦合反应Δn(NH~+_4)∶Δn(NO~-_3)最高达到0.43,硝酸盐转化速率提升60%,过高搅拌强度(搅拌速度G_T值64 s~(-1))、不适宜的p H值(最适p H值为8.02)环境都会起同步转化效率的降低.