生物法去除含甲硫醇恶臭气体的机理

对用生物法去除含甲硫恶臭气体的机理进行探讨和说明，得出甲硫系恶化恶臭气体的代谢过程中具有重要的地位。     

Surface characterization of metal oxides-supported activated carbon fiber catalysts for simultaneous catalytic hydrolysis of carbonyl sulfide and carbon disulfide

The sol–gel method was used to synthesize a series of metal oxides-supported activated carbon fiber (ACF) and the simultaneous catalytic hydrolysis activity of carbonyl sulfide (COS) and carbon disulfide (CS₂) at relatively low temperatures of 60°C was tested. The effects of preparation conditions on the catalyst properties were investigated, including the kinds and amount of metal oxides and calcination temperatures. The activity tests indicated that catalysts with 5 wt.% Ni after calcining at 400°C (Ni(5)/ACF(400)) had the best performance for the simultaneous catalytic hydrolysis of COS and CS₂. The surface and structure properties of prepared ACF were characterized by scanning electron microscope-energy disperse spectroscopy (SEM-EDS), Brunauer–Emmett–Teller (BET), X-ray diffraction (XRD), carbon dioxide-temperature programmed desorption (CO₂-TPD) and diffuse reflectance Fourier transform infrared reflection (DRFTIR). And the metal cation defects were researched by electron paramagnetic resonance (EPR) method. The characterization results showed that the supporting of Ni on the ACF made the ACF catalyst show alkaline and increased the specific surface area and the number of micropores, then improved catalytic hydrolysis activity. The DRFTIR results revealed that -OH species could facilitate the hydrolysis of COS and CS₂; -COO and -C–O species could facilitate the oxidation of catalytic hydrolysate H₂S. And the EPR results showed that high calcination temperature conditions provide more active reaction center for the COS and CS₂ adsorption.     

氨氮和硫酸盐对谷氨酸厌氧生物降解性能的抑制及机理

采用连续运行1119d的上流式厌氧污泥床（UASB）反应器,研究了最佳有机负荷条件下氨氮和硫酸盐对模拟废水中谷氨酸降解性能的抑制作用.结果表明,有机负荷为8.0g COD/（L·d）时,COD去除率达到最高值为（97.94±0.28）%.逐步提高进水氨氮浓度,起初对谷氨酸降解性能的影响不大;但升到2000mg/L时COD去除率和甲烷产率明显降低,继续升至4000mg/L时即达到半抑制状态.逐步提高进水硫酸盐浓度至4000mg/L,甲烷产率和溶液中游离硫化氢（FS）浓度分别呈现一直下降和升高趋势,但COD去除率均能维持在90%以上.进水中的氨氮和硫酸盐分别因离解平衡和生物还原作用形成游离氨（FAN）和FS,进而抑制了产甲烷菌的活性;前者因FAN扩散到细胞内部破坏质子平衡从而过多消耗ATP,后者还因硫酸盐还原菌的增殖存在底物竞争抑制作用.     

Town-scale microbial sewer community and H2S emissions response to common chemical and biological dosing treatments

Controlling hydrogen sulfide (H₂S) odors and emissions using a single, effective treatment across a town-scale sewer network is a challenge faced by many water utilities. Implementation of a sewer diversion provided the opportunity to compare the effectiveness of magnesium hydroxide (Mg(OH)₂) and two biological dosing compounds (Bioproducts A and B), with different modes of action (MOA), in a field-test across a large sewer network. Mg(OH)₂ increases sewer pH allowing suppression of H₂S release into the sewer environment while Bioproduct A acts to disrupt microbial communication through quorum sensing (QS), reducing biofilm integrity. Bioproduct B reduces H₂S odors by scouring the sewer of fats, oils and grease (FOGs), which provide adhesion points for the microbial biofilm. Results revealed that only Mg(OH)₂ altered the microbial community structure and reduced H₂S emissions in a live sewer system, whilst Bioproducts A and B did not reduce H₂S emissions or have an observable effect on the composition of the microbial community at the dosed site. Study results recommend in situ testing of dosing treatments before implementation across an operational system.     

氧化环境中FeS修复重金属的稳定性变化与机制

硫化亚铁(FeS)是良好的重金属修复剂,但它对氧化环境敏感.当环境氧气浓度升高时,FeS对重金属的固定效果可能发生改变.本研究考察了氧化环境中FeS与重铬酸根、铅和镉离子的反应规律和结合机制变化.结果表明,环境氧气浓度升高可促进Fe~(2+)的释放,且增加FeS表面S(-II)氧化态的比例(与Pb~(2+)反应:从24%增加到44%,与Cd~(2+)反应:从60%增加到78%).延长反应时间至30 d,虽然PbS和CdS结晶度提高,但两者表面出现Pb—O和Cd—O氧化形态,预示着重金属再释放的风险.有氧干燥条件下FeS表面矿物相转变为纤铁矿,对Cr(VI)的还原能力大幅下降.与未干燥FeS(FeS-Cr-3h)相比,当有氧干燥的FeS与Cr(VI)反应时,总铬的去除量下降约96%(由约100 mg·g~(-1)降至(3.74±1.12) mg·g~(-1)),Cr(VI)去除量下降约57%(由约100 mg·g~(-1)降至(43.28±0.46) mg·g~(-1)).FeS及重金属硫化物的氧化显然不利于重金属的长期稳定.如何延缓或抑制FeS与重金属硫化物的氧化因此成为未来研究需回答的问题.     

荧光灯管芯柱玻璃中金属铅的机械化学硫化

以硫化钠为硫化剂,机械化学硫化荧光灯管芯柱玻璃中金属铅,实现金属铅向硫化铅快速转化.通过单因素实验,考察了不同机械化学硫化条件,即球磨时间、球磨转速和球料比对硫化率的影响,并通过XRD、SEM和粒度对硫化产物进行表征.结果表明,硫化率随球磨时间和球磨转速的增大而增大,随球料比的增大先增大后减小,当球磨转速为750r/min、球磨时间为120min、球料比为50：1g/g时,荧光灯管芯柱玻璃中金属铅的硫化率可达96.18%.XRD结果表明,荧光灯管芯柱玻璃中金属铅的机械化学硫化产物为PbS、SEM和粒度结果表明,荧光灯管芯柱玻璃的粒径随球磨转速和球磨时间的增加而减小.     

Effect of ignition position on vented hydrogen–air deflagration in a 1 m3 vessel

This study investigates the effect of the ignition position on vented hydrogen-air deflagration in a 1 m³ vessel and evaluates the performance of the commercial computational fluid dynamics (CFD) code FLACS in simulating the vented explosion of hydrogen-air mixtures. First, the differences in the measured pressure-time histories for various ignition locations are presented, and the mechanisms responsible for the generation of different pressure peaks are explained, along with the flame behavior. Secondly, the CFD software FLACS is assessed against the experimental data. The characteristic phenomena of vented explosion are observed for hydrogen-air mixtures ignited at different ignition positions, such as Helmholtz oscillation for front ignition, the interaction between external explosion and combustion inside the vessel for central ignition, and the wall effect for back-wall ignition. Flame-acoustic interaction are observed in all cases, particularly in those of front ignition and very lean hydrogen-air mixtures. The predicted flame behavior agree well with the experimental data in general while the simulated maximum overpressures are larger than the experimental values by a factor of 1.5–2, which is conservative then would lead to a safe design of explosion panels for instance. Not only the flame development during the deflagration was well-simulated for the different ignition locations, but also the correspondence between the pressure transients and flame behavior was also accurately calculated. The comparison of the predicted results with the experimental data shows the performance of FLACS to model vented mixtures of hydrogen with air ignited in a lab scale vessel. However, the experimental scale is often smaller than that used in practical scenarios, such as hydrogen refueling installations. Thus, future large-scale experiments are necessary to assess the performance of FLACS in practical use.     

Heterogeneous uptake of gaseous hydrogen peroxide on mineral dust

The heterogeneous uptake processes of hydrogen peroxide on Arizona test dust and two types of authentic Chinese mineral dusts, i.e., Inner Mongolia desert dust and Xinjiang calciferous dust, were investigated using a Knudsen cell reactor coupled with a quadrupole mass spectrometer. The uptake coefficients were measured as a function of the initial concentration of H_2O_2 from 2.6 × 10~(11) to 1.2 × 10~(12)molecules/cm~3, and the temperature dependence of the uptake coefficients was investigated over a range from 253 to 313 K. The concentration of H_2O_2 showed little effect on the uptake coefficients of these heterogeneous processes. As a function of temperature, the initial uptake coefficients decrease with increasing temperature, whereas the steady state uptake coefficients of Arizona test dust and Inner Mongolia desert dust increase with increasing temperature. Implications for the understanding of the uptake processes onto mineral dust samples were also discussed.     

富硫沉积生境中微生物群落的垂直分布特征

为探讨富硫沉积环境中特定微生物类群对硫循环的贡献,人工建立富含硫酸盐的模型,对模型中各种环境化学参数进行监测,并采用不依赖于培养的微生物分子生态学技术对微生物群落垂向分布特征进行解析.结果表明,以沉积物-水界面为分界线,上层水相为好氧环境,硫化物浓度较底;而沉积物相中硫化物浓度较高,为厌氧生境.微生物群落分布与环境特征具有很好的吻合性,沉积物相中微生物群落相似性较高,多样性相对较低,而水相中微生物多样性较高,且与沉积物中微生物分离距离较大.在水-沉积物垂向剖面中,细菌域中的变形菌门(Protebacteria)(丰度为7.6%~32.8%)、绿弯菌门(Chloroflexi)(13.6%~22.3%)以及古菌域中的广古菌门(Euryarchaeota)(19.3%~29.2%)是微生物群落中的绝对优势类群.在该生境中,存在微生物主导的硫循环过程,在厌氧沉积物表层,δ变形菌纲(Deltaprotebacteria)中的硫酸盐还原细菌还原硫酸盐产生硫化物,同时降解有机质.硫化物向上层扩散时,被Thiobacillus、Acidithiobacillus和Halothiobacillus等属的硫氧化微生物氧化为单质硫,并进一步氧化为硫酸盐,在硫循环过程中有机质被逐渐降解.特定微生物种群的富集需要在不同的环境因素,多种微生物共同参与硫循环过程,完成有机质降解.     

Experimental investigation of the complex deflagration phenomena of hybrid mixtures of activated carbon dust/hydrogen/air

This paper aims to develop quantitative insights based on measured deflagration parameters of hybrid mixtures of activated carbon (AC) dust and hydrogen (H₂) gas in air. The generated experimental evidence is used to reject the claim of the null hypothesis (H₀) that severity of deflagrations of H₂/air mixtures always bound the severity of deflagrations of heterogenous combustible mixtures of AC dust/H₂/air containing the same H₂ concentrations as in the H₂/air binaries. The core insights of this investigation show that the maximum deflagration pressure rise (ΔP_MAX) and maximum rate of pressure rise ((dP/dt)_MAX) of this hybrid mixture are greater than those corresponding to deflagrations of H₂/air mixtures for all the dust and H₂ concentrations being examined. The deflagration severity indices (K_St and ES) of the hybrid mixture containing 29 mol% H₂ are found to be greater than those of the H₂/air mixture containing 29 mol% H₂. Also, the minimum explosible concentration (MEC) of the hybrid mixture is lower than that of the AC dust in air only. The insights gained should lead to better realization of the severity of a postulated safety-significant accident scenario associated with on-board cryoadsorption H₂ storage systems for fuel-cell (FC) powered light-duty vehicles. The identified insights could also be relevant to other industrial processes where combustible dusts are generated in the vicinity of solvent vapors. Moreover, these insights should be useful for supporting quantitative risk assessment (QRA) of on-board H₂ storage systems, designing improved safety measures for cryoadsorption H₂ storage tanks, and guiding H₂ safety standards and transportation regulations.