IC反应器处理高浓度硫酸盐废水的启动研究

采用木糖生产废水,进行了(IC)反应器处理高浓度硫酸盐有机废水的启动研究.结果表明,接种厌氧颗粒污泥,当进水COD/SO2-4值约为3.5时,控制COD负荷提高幅度为每次20%左右,经过26 d的驯化培养,COD和SO2-4负荷分别可达20 kg/(m3·d)和5.5 kg/(m3·d),COD去除率达到80%以上,硫...     

Validation of the UN test method N.5

Many substances react with water in such a way that flammable gases are formed. For transport issues this reaction may possess a considerable hazard especially if the cargo is wetted by rain or by water from other sources. In the UN Recommendations on the Transport of Dangerous Goods these kinds of problems are addressed. The UN test N.5 “Test method for substances which in contact with water emit flammable gases” corresponds to this hazard. Classification according to the test method is done by measurement of the gas evolution rate of the flammable gas by any suitable procedure. At BAM a gravimetric approach is used to measure the gas evolution rate. In this paper we present the evaluation of the apparatus by means of an absolute calibration routine utilizing a reaction where a known amount of gas is produced as well as the evaluation of important parameters influencing the gas evolution rate using different substances. It can be shown that the apparatus is capable of measuring absolute gas volumes as low as 6 mL with an acceptable error of about 17% as determined from the reaction of Mg with demineralized water.     

Preparation of PFS coagulant by sectionalized reactor

The oxidation rate of ferrous sulfate is investigated for the preparation of polyferric sulfate(PFS)coagulant.In is proved that this reaction is zero order with respect to Fe^2 ,first order with respect to NO2(g),and first order with respect to the interface area between gas phase and liquid phase.According to this mechanism,sectionalized reactor(SR) is used in place of traditional reactor(TR),and the liquid of reaction mixture is recycled by pump.As a result,not only the flow path of reaction liquid is prolonged,but also gas-liquid contact area enlarged,and the reaction distinctly accelerated,compared with traditional reactor.The effects of parameters including temperature,acidity and others on the reaction rate are also discussed.     

离子强度和SO2-4对土壤吸附Al的影响

研究了离子强度和SO4^2-对土壤吸附Al的影响，结果表明：在所研究的pH范围内，随着NaCl支持电解质浓度的提高，土壤对Al的吸附量基本保持不变，并且当pH＜3．9时，即土壤表面净电荷为正时，土壤对Al的吸附量仍然很大，超过最大吸附量的50％，而用CaCl2作支持电解质时，当pH＜4．5时，在溶液中CaCl2浓度最高的情况下，Al的吸附量最小，在其余两种浓度条件下则基本相等；当pH＞4．5时，Al的吸附量几乎不受CaCl2浓度变化的影响。SO4^2-的加入对土壤吸附Al没有影响。这些都说明土壤吸附Al的作用机制主要为专性吸附。     

钛对聚合硫酸铁制备与性能的影响

研究了由FeSO4制备聚合硫酸铁过程中,钛对聚铁聚合态分布和稳定性的影响,并进一步考察了含钛聚合硫酸铁的絮凝性能.应用络合比色法对聚铁中不同水解形态聚铁的含量进行了分析测定,并通过沉淀实验考察了不同钛含量对聚铁稳定性的影响;随后,通过出水浊度、TOC、金属离子残余量和出水pH等指标测试,研究了钛对聚合硫酸铁混凝性能的影响.结果表明,较低的钛含量(<0.025)在一定程度上有利于中聚态聚铁的形成,提高了聚铁絮凝剂的混凝效率;反之,钛含量超过0.025时不仅聚铁的稳定性显著下降,而且处理后出水的钛残留增加,pH降低.     

Microbial cycling of iron and sulfur in acidic coal mining lake sediments

Lakes caused by coal mining processes are characterized by low pH, low nutrient status, and high concentrations of Fe(II) and sulfate due to the oxidation of pyrite in the surrounding mine tailings. Fe(III) produced during Fe(II) oxidation precipitates to the anoxic acidic sediment, where the microbial reduction of Fe(III) is the dominant electron-accepting process for the oxidation of organic matter, apparently mediated by acidophilic Acidiphilium species. Those bacteria can reduce a great variety of Fe(III)-(hydr)oxides and reduce Fe(III) and oxygen simultaneously which might be due to the small differences in the redox potentials under low pH conditions. Due to the absence of sulfide, Fe(II) formed in the upper 6 cm of the sediment diffuses to oxic zones in the water layer where itcan be reoxidized by Acidithiobacillus species. Thus, acidic conditions are stabilized by the cycling of iron which inhibits fermentative and sulfate-reducing activities. With increasing sediment depth, the amount of reactive iron decrease, the pH increases above 5, and fermentative and as yet unknown Fe(III)-reducing bacteria are also involved in the reduction of Fe(III). Sulfate is reduced apparently by the activity of spore-forming sulfate reducers including new species of Desulfosporosinus that have their pH optimum similar to in situconditions and are not capable of growth at pH 7. However, generation of alkalinity via sulfate reduction is reduced by the anaerobic reoxidation of sulfide back to sulfate. Thus, the microbial cycling of iron at the oxic-anoxic interface and the anaerobic cycling of sulfur maintains environmental conditions appropriate for acidophilic Fe(III)-reducing and acid-tolerant sulfate-reducing microbial communities.     

Hydrogen Sulfide Gas Treatment by a Chemical‐Biological Process: Chemical Absorption and Biological Oxidation Steps

In order to remove high concentrations of hydrogen sulfide (H₂S) gas from anaerobic wastewater treatments in livestock farming, a novel process was evaluated for H₂S gas abatement involving the combination of chemical absorption and biological oxidation processes. In this study, the extensive experiments evaluating the removal efficiency, capacity, and removal characteristics of H₂S gas by the chemical absorption reactor were conducted in a continuous operation. In addition, the effects of initial Fe^2 + concentrations, pH, and glucose concentrations on Fe^2 + oxidation by Thiobacillus ferrooxidans CP9 were also examined. The results showed that the chemical process exhibited high removal efficiencies with H₂S concentrations up to 300 ppm, and nearly no acclimation time was required. The limitation of mass‐transfer was verified as the rate‐determining step in the chemical reaction through model validation. The Fe^2 + production rate was clearly affected by the inlet gas concentration as well as flow rate and a prediction equation of ferrous production was established. The optimal operating conditions for the biological oxidation process were below pH 2.3 and 35°C in which more than 90% Fe^3 + formation ratio was achieved. Interestingly, the optimal glucose concentration in the medium was 0.1%, which favored Fe^2 + oxidation and the growth of T. ferrooxidans CP9.     

砷华生产废渣中硫的回收利用研究

高温下氧化焙烧细磨后的砷华生产废渣，利用软锰矿浆吸收产生的SO2气体，吸收液经净化除杂、浓缩结晶等工序可制备工业产品硫酸锰。适宜的焙烧条件如下：焙烧温度为650℃，焙烧时间为60min，废渣粒度为-97μm。选择合适的吸收工艺，Mn的浸出率可达96．20％，此时SO2脱除率为87．20％。     

粗MnSO4溶液中MnS2O6的去除条件研究

用软锰矿吸收SO2生成MnSO4时会伴随有副产物MnS2O6生成。产品中MnS2O6的存在会降低硫酸锰产品质量,同时会缓慢释放出SO2气体污染环境。本文用单因素实验方法研究了粗MnSO4溶液中MnS2O6的最优去除条件。研究结果显示,软锰矿用量为12.2 g,硫酸加入量为20 mL、反应温度100℃、反应时间3 h、搅拌速度500 r/min,MnS2O6的去除率可达91%以上。其最终产品能达到GB1622-1986一级品标准。     

区域大气环境模式RegAEMS中二次气溶胶的改进模拟研究

为了提升二次气溶胶的模拟精度,在区域大气环境模式RegAEMS中加入了硫酸盐气溶胶的两种新生成机制（NO₂+SO₂化学过程和过渡金属催化氧化（TMI））以及二次有机气溶胶（SOA）生成的挥发性有机物基集（VBS）方法.模拟了2020年1月上海市两次中度污染过程,并与观测数据进行对比验证.研究发现,两次污染过程硫氧转化率（SOR）均大于0.4,PM_2.5主要组分为SO₄^2-、NO₃^-、NH₄⁺等水溶性离子,占比为61.25%~63.85%.SOA占比为2.92%~3.0%.加入NO₂+SO₂化学过程和过渡金属催化氧化（TMI）后,硫酸盐模拟精度明显提升（相关系数（R）从0.49~0.63提升至0.58~0.67,相对标准偏差（NMB）从-35.0%~-36.5%提升至-17.3%~-14.2%）.两种化学过程在污染发展阶段平均贡献占比为23.3%~27.9%,这可能是造成污染条件下SO₄^2-浓度迅速增加的主要原因.VBS机制能够较好地模拟出SOA的变化趋势（相关系数为0.53~0.56）,由于硫酸盐和SOA生成机理的改进,RegAEMS在PM_2.5的模拟精度上有所提升（相对标准偏差（NMB）从-13.5%~-6.0%提升至-9.0%~-3.3%）.