用改性活性碳纤维去除CO2原料气中的H2S

采用固定床动态吸附实验，用改性活性碳纤维（ACF）吸附去除CO2原料气中的H2S。通过改变改性剂种类、反应温度和原料气中CO2浓度，找出用改性ACF去除CO2原料气中H2S的规律。实验结果表明：常温下，可用NaON改性的ACF来消除CO2的酸性对去除H2S的不利影响；随着反应温度的升高，CO2与ACF形成的C（O＊）中间产物增多，CO2的存在有利于改性ACF去除H2S；而当反应温度过高时，CO2与ACF形成的C（O＊）中间产物发生分解，导致ACF碳化，不利于H2S的吸附去除。     

多因素耦合条件下硫化矿自燃神经网络动态预测模型研究

硫化矿石自燃是多种因素、多场耦合综合作用的结果,是一典型的非线性问题。笔者应用人工神经网络技术,以Matlab软件为平台,通过现场调查和理论分析,建立了矿石含硫量、通风强度、环境温度3因素与硫化矿石自燃之间的预测模型;通过数据样本学习与部分现场监测数据相结合进行模拟,研究表明预测数据与实测结果基本吻合,误差控制在10%以内,取得了较好的效果。该研究为预防硫化矿石自燃提供一个新的思路和方法,具有一定的理论意义和应用价值。     

Research of Toxic Mechanism on Anaerobic Digestion by Lead

The paper analyzes the influence of lead toxicity by anaerobic granule sludge inhibition and recovering experiments. The result shows that there are different inhibition types at different lead contents. Higher lead content leads to more inhibition granular sludge, and at the same time, the time of gas recovery is different. Lower lead content per microorganism results in sooner sludge recovery. Microorganisms have a good ability to resist lead toxicity.     

钠盐量影响下DD6单晶高温合金的高温热腐蚀规律研究

目的 开展镍基单晶高温合金DD6在950 ℃下的热盐腐蚀试验(95%Na2SO4+5%NaCl)，探明涂盐量和涂盐方式(周期涂盐和单次涂盐)对DD6高温热腐蚀的影响规律和机理。方法 结合扫描电子显微镜、X射线能量色散谱、X射线衍射等设备，对不同涂盐量及涂盐方式下DD6的表面及横截面形貌进行观察分析，分析不同涂盐量和涂盐方式下DD6的高温热腐蚀机理。结果 DD6在950 ℃下主要发生碱性熔融热腐蚀，同时伴随氧化、硫化和氯化等过程。高温热腐蚀使得DD6合金表面生成的保护性氧化膜被熔融态的腐蚀介质破坏，导致O、S、Cl等外部元素通过氧化膜的缺陷进入DD6基体中，在合金的亚表面发生内氧化、内硫化以及内氯化反应，横截面上出现明显的腐蚀层，其主要由氧化物以及硫化物组成。随着热腐蚀的进行，DD6表面物质发生了剥蚀，沉积盐量的增加导致剥蚀现象越加严重，合金内部致密的组织结构也被破坏，横截面上出现了大量孔洞、裂纹等缺陷。在相同涂盐量下，周期涂盐法使得DD6的腐蚀程度高于单次涂盐法。结论 DD6高温热腐蚀行为与涂盐量及涂盐方式密切相关，相同涂盐方式下，涂盐量越大，DD6热腐蚀更加严重。涂盐量一定时，周期涂盐法使得DD6的热腐蚀剧烈程度大于单次涂盐法，且DD6在上述热腐蚀条件下均发生剥蚀破坏。     

Effect of six kinds of scale inhibitors on calcium carbonate precipitation in high salinity wastewater at high temperatures

Precipitation of calcium carbonate(Ca CO3) scale on heat transfer surfaces is a serious and expensive problem widely occurring in numerous industrial processes. In this study, we compared the scale inhibition effect of six kinds of commercial scale inhibitors and screened out the best one(scale inhibitor SQ-1211) to investigate its scale inhibition performance in highly saline conditions at high temperature through static scale inhibition tests. The influences of scale inhibitor dosage, temperature, heating time and p H on the inhibition efficiency of the optimal scale inhibitor were investigated. The morphologies and crystal structures of the precipitates were characterized by Scanning Electron Microscopy and X-ray Diffraction analysis. Results showed that the scale inhibition efficiency of the optimal scale inhibitor decreased with the increase of the reaction temperature. When the concentration of Ca2+was 1600 mg/L, the scale inhibition rate could reach 90.7% at 80°C at p H 8. The optimal scale inhibitor could effectively retard scaling at high temperature. In the presence of the optimal scale inhibitor, the main crystal structure of Ca CO3 changed from calcite to aragonite.     

连续流动法测定沉积物中的酸挥发性硫化物

优化沉积物中酸挥发性硫化物(Acid Volatile Sulfide,AVS)的提取方法并采用连续流动分析法检测提取液中的硫化物.研究了吸收液的种类、氮气流量与吹气的时间和反应温度对AVS提取效果的影响以优化提取方法.结果表明,与传统的氢氧化钠或硫酸镉-氢氧化钠吸收液相比,以氯化锌-羧甲基纤维素钠溶液为吸收液吸附效率好,稳定性高且无毒.用连续流动分析法检测提取液中的AVS快速、准确、稳定性好.     

Experimental and theoretical research on the inhibition performance of ethanol gasoline/air explosion by C6F12O

The safety issue of ethanol gasoline and the methods to control or weaken its explosion have attracted attention. To clarify the effect of C₆F₁₂O (perfluoro(2-methyl-3-pentanone)) on the explosion of ethanol gasoline-air mixtures and intrinsic mechanism, the explosion overpressure and flame propagation behavior under different equivalence ratios (φ = 0.6–0.8) and C₆F₁₂O concentrations (χ_inh = 0–4.0%) were experimentally obtained. The detailed inhibitor reaction process was also obtained by CHEMKIN based on a new assembly kinetic mechanism. The results show that the effects of C₆F₁₂O on the explosion characteristics of ethanol gasoline varied with χ_inh and φ. For rich flames, C₆F₁₂O is more effective than and heptafluoropropane (C₃HF₇) and nitrogen (N₂) in suppressing explosions; for lean and equivalence ratio flames, the addition of C₆F₁₂O may result in more severe explosions. The decrease in chemical reactivity is mainly because the mole fractions of OH and H radicals and the proportion of paths H radicals involved decrease after adding C₆F₁₂O, and R1500: CF₃COF + H = CF₃CO + HF, R965: CF₂:O + H = CF:O + HF, R863: CF₃ + H = CF₂ + HF are main suppressing reactions.     

3种填料A.ferrooxidans挂膜效果及对模拟酸性矿山废水中Fe2+生物矿化能力比较

氧化亚铁硫杆菌（A.ferrooxidans）介导的生物矿化方法可促使酸性矿山废水（Acid Mine Drainage,AMD）中Fe离子向次生铁矿物转变. 采用固定化的方式来提高A.ferrooxidans密度有助于强化Fe²⁺的生物矿化能力.选取流化床19孔填料、弹性填料、悬浮球填料作为挂膜对象, 通过多批次的连续培养来考察3种填料的A.ferrooxidans挂膜能力及稳定挂膜所需周期,继而比较3种挂膜填料对模拟AMD中Fe²⁺的生物矿化能力,并估算A.ferrooxidans有效生物量.结果表明,3种填料（5.00 g）的A.ferrooxidans挂膜能力依次为弹性填料（1.76 g）＞流化床19孔填料（0.90 g）＞悬浮球填料（0.78 g）（干重）,且挂膜启动至稳定状态至少需要4批次.X射线衍射分析（X-ray diffraction,XRD）表明,3种填料表面 含矿生物膜均为施氏矿物和黄钾铁矾的混合物.以游离态A.ferrooxidans的Fe²⁺氧化速率作为参比,估算出流化床19孔填料、弹性填料、悬浮球填料生物膜中A.ferrooxidans有效生物量依次为1.67×10⁸、8.52×10⁸、1.92×10⁸ cells·g^-1 （干基）.研究还发现,等同Fe²⁺生物氧化速率下, A.ferrooxidans挂膜填料比游离态A.ferrooxidans具有更强的AMD矿化驱动能力.     

氧化硫硫杆菌固定化菌球制备及其耦合填料去除H2S

以海藻酸钠(SA)为包埋载体,对氧化硫硫杆菌(Acidithiobacillus thiooxidans)进行固定化制备菌球,优化菌球制备条件,在生物滤塔内验证其对H₂S的去除能力.以前期驯化获得的富含硫系恶臭降解微生物菌群的污泥为菌源进行生物滤塔填料筛选,耦合A.thiooxidans菌球和填料进行生物除臭.结果表明,优选的固定化条件为:SA浓度3.0%､吸附剂CNT､A.thiooxidans菌悬液与混合液比例20%､CaCl₂浓度4.0%､改性剂己二胺溶液,获得的菌球机械强度､传质性能､硫氧化能力最好.将A.thiooxidans菌球填装于生物滤塔,H₂S最大去除率和去除能力为70%和1.06g H₂S/m³·h.以混合挂膜方式进行填料挂膜后,在聚氨酯泡沫､活性碳布和陶粒中优选出最佳填料活性碳布,获得H₂S最大去除率和去除能力为88%和0.84g H₂S/m³·h.以混合填装方式将A.thiooxidans菌球与活性碳布填装于生物滤塔,获得H₂S最大去除率和去除能力为86%和1.00g H₂S/m³·h.     

南京秋冬季非难熔性亚微米颗粒物来源解析

利用Aerodyne高分辨率飞行时间气溶胶质谱仪（HR-ToF-AMS）对南京北郊秋冬季非难熔性亚微米气溶胶（NR-PM₁）的化学组分（包括有机物、硝酸盐、硫酸盐、铵盐和氯化物）和特征进行实时在线监测,并利用多元线性模型（ME-2）对其中复杂的有机物进行来源解析.观测期间,有机物、硝酸盐、硫酸盐、铵盐、氯化物对NR-PM₁的贡献分别为42%,28%,15%,13%和2%.有机物解析出6类有机气溶胶：烃类有机气溶胶（HOA）、烹饪类有机气溶胶（COA）、生物质燃烧有机气溶胶（BBOA）、高氧化有机气溶胶（MO-OOA）、低氧化有机气溶胶（LO-OOA）、液相反应生成氧化有机气溶胶（aq-OOA）,平均浓度分别占总有机气溶胶的18%,14%,19%,19%,11%和19%.通过不同污染事件的对比结果表明,本次观测期间二次气溶胶在污染时期占比会明显上升并且液相反应对二次组分的形成有显著的促进作用.