污泥与不同pH值渗滤液联合厌氧发酵产氢分析

以污泥与垃圾焚烧厂渗滤液为原料,通过小瓶批式试验,考察了垃圾渗滤液的添加量以及渗滤液初始pH对联合厌氧消化产氢的影响。结果表明:未添加污泥的渗滤液本身也可以在厌氧发酵过程中产氢。而污泥与垃圾渗滤液联合厌氧发酵,当渗滤液初始pH为5.20时,添加90%的渗滤液体系产氢量最大,为201.58 mL,最大产氢速率也最高,为9.56 mL/h;当初始渗滤液pH为4.47时,最大产氢量出现在渗滤液添加剂量为60%的样品,为57.73 mL,随后减小,但最大产氢速率在添加40%的渗滤液达到峰值,为5.11 mL/h。     

短期干旱胁迫对马尾松排放挥发性有机物的影响

为探究干旱环境对BVOCs排放的影响,应用动态封闭式采样系统和热脱附-气相色谱-飞行质谱仪,对短期干旱胁迫作用下马尾松的BVOCs排放进行了实验室测量,定量分析BVOCs排放速率和排放组成的变化.结果表明,干旱胁迫时异戊二烯的排放受到抑制,排放速率降低约50%;单萜烯和倍半萜烯的排放水平增强,排放速率分别为137.85和0.98μg/（m²·h）,是未受胁迫时的2.9和2.0倍.除反式-α-香柠檬烯外,干旱胁迫促进各单萜烯和倍半萜烯化合物的排放,是未受胁迫时的1.3~42.4倍,其中3-蒈烯排放的响应最敏感,α-葑烯、α-水芹烯和石竹烯的响应最弱.干旱胁迫时单萜烯和倍半萜烯的排放组成有所变化,但主导的化合物种类不变,单萜烯以α-蒎烯、香桧烯和β-蒎烯为主,占比分别为48%、17%和17%;倍半萜烯以石竹烯和长叶烯为主,占比分别为57%和34%.     

长治市沙尘天气污染特征及传输路径解析

以2018年3次沙尘天气为研究对象,分析了PM_2.5和PM₁₀浓度、水溶性离子组分、气象条件和气溶胶光学特征,研究了长治市沙尘天气的典型污染特征和传输路径.结果表明：长治市2018年共8d为受沙尘天气影响日,其中4月份最多（5d）,这与春季大气环流调整,冷暖空气活动频繁有关.沙尘污染发生前一般受西方或西北方冷空气影响,大气层结不稳定,大气环流转为经向环流,平均风速达4m/s以上;沙尘污染过程中PM_2.5/PM₁₀均低于0.3,环境空气中粗颗粒物占比较大,水溶性离子总浓度在PM_2.5中占比下降,Ca²⁺浓度为沙尘污染发生前的4倍以上.冬季沙尘为近地面扩散传输,春夏季沙尘为高空沉降传输,影响范围大,区域传输贡献明显.长治市沙尘重要潜在源区为蒙古国、哈萨克斯坦中部和新疆中北部的荒漠地区,传输路径主要为西北路径和正北路径,其中西北路径为哈萨克斯坦—新疆中北部—内蒙古西部—长治以及新疆中北部—内蒙古西部—长治两条路径,正北路径为蒙古国—内蒙古中部—山西北部—长治.     

矿山排水污染稻田土壤胶体对砷的吸附研究

为研究矿山排水污染土壤胶体对砷的吸附影响,文章以高砷污染区和背景区土壤的胶体在不同的pH、离子强度以及好氧/厌氧淹水条件下对As(Ⅴ)的吸附进行对比试验。结果表明:土壤胶体对As(Ⅴ)的吸附量随pH的增大而减少,且污染区胶体比背景区胶体对As(Ⅴ)的吸附量大;离子强度越大,胶体对As(Ⅴ)的吸附量越大,Ca(NO_3)_2浓度从0.001 mol/L增至0.1 mol/L时,污染区与背景区胶体对As(Ⅴ)的吸附量分别增加了30.57%、50.25%;厌氧淹水后的胶体对As(Ⅴ)的吸附量低于好氧条件下的胶体,解吸量较高,且厌氧淹水后污染区胶体与背景区胶体相比无明显吸附优势,而好氧条件下污染区胶体的解吸率低于背景区胶体,说明厌氧淹水后的胶体不易吸附且易释放As(Ⅴ)。因此,低p H和高离子强度以及好氧的条件有利于土壤胶体对砷的吸附。     

海水入侵指标对比分析与评价—以珠江口地下水含水层为例

合理评价海水入侵对于地下水含水层管理和居民生活健康有着重要的意义。当前海水入侵评价应用较广泛的为包含单一因子和基于统计分析的多种水化学方法。本文综合阐述了海水入侵评价中所用的水化学指标、原理与方法,包括在国内评价体系中少见的一些方法,并以珠江口地下水含水层为例,对比了各种指标的有效性,评价了各类方法的优缺点以及在实际应用中可能产生的问题。结果显示,以Cl-和TDS作为简单直接的单因子可以快速评价海水入侵,尤其对于大范围的海水入侵评价十分有效。而和Ca2+,HCO₃-,SO₄2-等变化有关的指标具有地域性,在研究区对海水入侵的指示并不是十分敏感。在复杂评价因子中,与离子交换有关SAR,BEX以及GQI_SWI与Cl-相关性较高,可以较好的指示海水入侵及水岩相互作用。经过分析,受到地下含水层和地表水道双重介质入侵的影响,研究区海水入侵范围在过去几个年代有向北推进的趋势。本研究对于高速经济发展下的沿海地下水含水层管理和评价有重要的指导意义。     

Direct capture of carbon dioxide from air via lime-based sorbents

Mitigation and Adaptation Strategies for Global Change - Direct air capture (DAC) is a developing technology for removing carbon dioxide (CO2) from the atmosphere or from low-CO2-containing...     

Simulation of a 100-MW solar-powered thermo-chemical air separation system combined with an oxy-fuel power plant for bio-energy with carbon capture and storage (BECCS)

The combination of concentrated solar power–chemical looping air separation (CSP-CLAS) with an oxy-fuel combustion process for carbon dioxide (CO₂) capture is a novel system to generate electricity from solar power and biomass while being able to store solar power efficiently. In this study, the computer program Advanced System for Process Engineering Plus (ASPEN Plus) was used to develop models to assess the process performance of such a process with manganese (Mn)-based oxygen carriers on alumina (Al₂O₃) support for a location in the region of Seville in Spain, using real solar beam irradiance and electricity demand data. It was shown that the utilisation of olive tree prunings (Olea europaea) as the fuel—an agricultural residue produced locally—results in negative CO₂ emissions (a net removal of CO₂ from the atmosphere). Furthermore, it was found that the process with an annual average electricity output of 18 MW would utilise 2.43% of Andalusia’s olive tree prunings, thereby capturing 260.5 k-tonnes of CO₂, annually. Drawbacks of the system are its relatively high complexity, a significant energy penalty in the CLAS process associated with the steam requirements for the loop-seal fluidisation, and the gas storage requirements. Nevertheless, the utilisation of agricultural residues is highly promising, and given the large quantities produced globally (~?4 billion tonnes/year), it is suggested that other novel processes tailored to these fuels should be investigated, under consideration of a future price on CO₂ emissions, integration potential with a likely electricity grid system, and based on the local conditions and real data.

     

Evaluating national hydrogen refueling infrastructure requirement and economic competitiveness of fuel cell electric long-haul trucks

This study explored the national hydrogen refueling infrastructure requirement along major United States (US) interstate highway corridors to support the deployment of fuel cell electric trucks (FCETs) for the national long-haul trucking fleet. Given the long-haul trucking shipment demand in 2025 projected by the Freight Analysis Framework, locations and capacities of hydrogen stations were identified for inter-zone freight flows, and the total daily refueling demand was estimated for intra-zone flows for each FAF zone. Based on the infrastructure deployment results, we conducted an economic feasibility analysis of FCETs by evaluating the total ownership cost. We found that when the FCET penetration is relatively high (e.g., 10% penetration), FCETs become more competitive in terms of fuel cost and idling cost and could be economic viable if the incremental vehicle cost is reduced to meet the near-term FCET technology cost targets and the liquefaction cost is reduced to an optimal case. We also observed that the station cost depends on regional factors, particularly regional demand, which is used to determine station capacity. Thus, one possible strategy for station roll-out is to have early investment in target regions where station costs are expected to be relatively low such as the Pacific and West South Central regions.