横向风对浮力扩散火焰的振荡影响研究

火焰振荡频率是火灾科学研究领域的一个重要基本参数,对横向风下火焰振荡频率的研究可以为火灾图像探测的参数设置提供理论依据。针对浮力扩散火焰(0.6×10~(-5)弗洛德数Fr2×10~(-2),10~2理查德森数Ri10~5),本研究将横向风条件下火焰结构假设为倾斜的柱状,通过对燃烧产生的浮力和横向风产生的拖曳力进行动力学分析,得出横向风条件下火焰振荡频率表达公式。结合实验结果得出,火焰振荡频率的理论值和实验值均随拖曳系数的增大(即外界风速的增加)而增大,但实验值的上升趋势较理论值平缓.这是因为公式忽略了风速对火焰温度和系数K的影响。     

Evaluation of the technoeconomic feasibility of electrochemical hydrogen peroxide production for decentralized water treatment

• Gas diffusion electrode (GDE) is a suitable setup for practical water treatment. • Electrochemical H₂O₂ production is an economically competitive technology. • High current efficiency of H₂O₂ production was obtained with GDE at 5–400 mA/cm². • GDE maintained high stability for H₂O₂ production for ~1000 h. • Electro-generation of H₂O₂ enhances ibuprofen removal in an E-peroxone process. This study evaluated the feasibility of electrochemical hydrogen peroxide (H₂O₂) production with gas diffusion electrode (GDE) for decentralized water treatment. Carbon black-polytetrafluoroethylene GDEs were prepared and tested in a continuous flow electrochemical cell for H₂O₂ production from oxygen reduction. Results showed that because of the effective oxygen transfer in GDEs, the electrode maintained high apparent current efficiencies (ACEs,>80%) for H₂O₂ production over a wide current density range of 5–400 mA/cm², and H₂O₂ production rates as high as ~202 mg/h/cm² could be obtained. Long-term stability test showed that the GDE maintained high ACEs (>85%) and low energy consumption (<10 kWh/kg H₂O₂) for H₂O₂ production for 42 d (~1000 h). However, the ACEs then decreased to ~70% in the following 4 days because water flooding of GDE pores considerably impeded oxygen transport at the late stage of the trial. Based on an electrode lifetime of 46 days, the overall cost for H₂O₂ production was estimated to be ~0.88 $/kg H₂O₂, including an electricity cost of 0.61 $/kg and an electrode capital cost of 0.27 $/kg. With a 9 cm² GDE and 40 mA/cm² current density, ~2–4 mg/L of H₂O₂ could be produced on site for the electro-peroxone treatment of a 1.2 m³/d groundwater flow, which considerably enhanced ibuprofen abatement compared with ozonation alone (~43%–59% vs. 7%). These findings suggest that electrochemical H₂O₂ production with GDEs holds great promise for the development of compact treatment technologies for decentralized water treatment at a household and community level.     

基于FBM法追踪秦皇岛海域赤潮迁移扩散

在Delft3D-FLOW模型模拟水动力的基础上,基于FBM粒子追踪法建立和验证赤潮迁移扩散模型.模拟了秦皇岛海域潮流和风生流,分析了风生流对赤潮迁移扩散的作用,对比分析了FBM法、拉格朗日法和常规布朗运动法在赤潮迁移扩散模拟中的特性,测试了模型Hurst指数的敏感性并得出其在赤潮模拟中的合理取值范围.主要结论为：①秦皇岛海域的赤潮主要随潮流的涨落而往复移动,一个涨落潮周期内赤潮的净迁移距离较小;②秦皇岛海域夏季潮流较弱,但风对赤潮迁移具有一定影响,易产生东北向风生流,导致赤潮更易往东北方向迁移;③Hurst指数较明显地影响粒子云的扩散范围,Hurst指数取0.80±0.03能比较真实地模拟秦皇岛海域赤潮的迁移扩散;④FBM法可模拟赤潮的non-Fickian扩散现象,使其模拟的粒子云扩散范围和分布形状明显优于拉格朗日法和常规布朗运动法.     

泄漏孔形状对液化石油气泄漏扩散的影响

基于液化石油气的特点,建立了有限空间内部发生泄漏扩散的物理模型,模拟了液化石油气泄漏扩散的过程,通过模拟结果分析其扩散规律,并对比当泄漏孔形状分别为正方形、圆形、三角形时液化石油气扩散过程的变化以及对所形成的的爆炸危险区域的影响。监测点1（0.8,0.3,0）,点2（2.4,0.3,2.5）,点3（0,0.3,1.5）,点4（2,0.3,3）的浓度变化,找出报警器的最佳安放位置。结果表明:泄漏时间相同,丙烷的扩散范围从大到小依次为三角形孔口、圆形孔口、正方形孔口,爆炸危险区域也与泄漏孔形状有关,三角形孔口的危险区域范围最广,其次是圆形泄漏孔,正方形泄漏孔的范围最小,点1处的丙烷浓度增长幅度较大,浓度较高,可以更早达到报警浓度。     

受限空间内湍流模型对气体扩散仿真结果的影响

针对受限空间内气体扩散问题,为研究不同湍流模型对气体扩散仿真结果的影响 ,选取FLUENT软件中工程应用较为广泛的湍流模型为研究对象,以相关气体扩散实验为 参考,构建数值仿真模型,在初始和边界条件相同的情况下采用不同的湍流模型对实验 过程进行数值模拟。在对模拟结果定量化分析方面,采用了Hanna等人提出的广泛应用 于重气扩散模型评价的误差分析方法,并结合了chang等人提出的有关模拟效果的统计 误差评判标准,通过计算模拟值与实验值之间的统计误差对比分析了各模型模拟效果。 结果表明,所选的5种Reynolds平均湍流模型模拟结果的统计误差指标均符合有效性评 判标准,模拟值总体上要高于实验值,并且Realizable k-ε模型的模拟效果要优于其 他模型。湍流模型的选用会对受限空间内气体扩散仿真结果产生影响,选择合适的湍流 模型有助于提高数值仿真的精度。     

氯气泄漏后毒害区的估算及泄漏的处置

运用毒害区计算方法对本部贮存的氯气泄漏后扩散的半径进行估算,同时以扩散的半径作参考,提出氯气泄漏的处置方法.     

辛置煤矿水力压裂卸压增透影响半径数值模拟研究

随着开采深度的增加,辛置煤矿瓦斯涌出量显著增大。为了提高瓦斯抽采效率,拟采用水力压裂卸压增透技术。理论分析了水力压裂对煤层的卸压增透作用,基于此利用RFPA模拟软件对辛置煤矿2-559回采工作面水力压裂卸压增透进行了数值模拟。研究表明,水力压裂主要在以下3个方面对煤体起到增透作用:使煤体卸压、提高煤层透气性;湿润煤体,增加塑性;改善瓦斯抽放环境。辛置煤矿2-559回采工作面水力压裂所需压力约为15MPa,压裂半径为5-6m,以此可以初步确定现场施工过程中水力压裂钻孔间距以不大于10m为宜。     

基于熵信息扩散理论的中国农业水旱灾害风险评估

农业水旱灾害是制约中国农业生产的重要因素。针对信息扩散理论模型存在的不足,论文构建了评估中国农业水旱灾害风险的熵信息扩散理论模型,依据1985-2013年数据资料,运用熵信息扩散理论模型对中国大陆30个省、市、自治区（重庆包含在四川中计算）的农业水旱灾害进行了风险评估,根据农业水旱灾害风险评估结果对中国农业水旱灾害风险进行了综合对比分析。评估和分析结果表明：中国面临着较大的农业水旱灾害风险压力;中国农业旱灾风险明显大于农业水灾风险;农业水旱灾害空间风险特征明显;农业水灾高中风险区域主要集中在长江中下游地区和东北地区,农业旱灾高风险区域主要集中在中国北部地区和东北地区,总体上看,中国农业水旱灾害的空间分布格局是南方地区易出现水灾,而北部地区易出现旱灾,东北地区面临水旱灾害重叠的双重压力。     

白洋淀夏季入淀区沉积物间隙水-上覆水水质特征及交换通量分析

为揭示白洋淀夏季入淀区上覆水-间隙水氮磷营养盐相互作用,本研究于2019年7月对白洋淀主要6条入淀河流取样,通过分析上覆水、间隙水水质特征以及营养盐在沉积物-水界面的扩散通量,评估了营养盐扩散对沉积物与上覆水的影响.结果表明白洋淀水质呈弱碱性;溶解氧（DO）含量较低,为沉积物内源污染物的释放提供了厌氧环境;氨氮（NH₄⁺-N）浓度在0.35~1.76mg·L^-1,作为主要给水来源的潴龙河淀区最高;硝氮（NO₃^--N）浓度在0.75~1.97mg·L^-1;溶解性总氮（TDN）浓度在0.99~2.70mg·L^-1,位于自然区的S2瀑河含量最高;溶解性总磷（TDP）浓度在0.03~0.15mg·L^-1,靠近居民区的白沟引河含量最高.间隙水氨氮浓度在5.24~10.64mg·L^-1,是上覆水体的10倍,内源污染严重;硝氮浓度在0.36~0.79mg·L^-1;溶解性总氮浓度在5.36~12.02mg·L^-1,是上覆水体的5倍;溶解性总磷浓度在0.03~0.3mg·L^-1.应用综合污染指数法对水质进行评价发现间隙水污染程度远高于上覆水,各采样点呈现出严重污染状态.对NH₄⁺-N、TDN和TDP进行交换通量分析显示,NH₄⁺-N的扩散通量在1.71~7.43mg·（m²·d）^-1,作为保定市纳污河流的府河采样点内源氨氮向上覆水扩散速率最快;TDN的扩散通量除白沟引河较低,其余5个采样点均值达到9.11mg·（m²·d）^-1,夏季水体中溶解氧含量较低且沉积物-水界面TDN浓度差较大,导致沉积物中含氮营养盐在厌氧条件下大量释放到上覆水中,对水质造成严重污染;萍河采样点TDP的扩散通量是负值表示上覆水体的磷污染物向沉积物聚集的状态,剩余5个采样点的扩散通量范围在0.03~0.16mg·（m²·d）^-1,表现出磷营养盐向上覆水释放的状态.扩散通量显示内源污染物是上覆水污染物的重要来源,为有效治理入淀区水质,沉积物氮磷营养盐的清淤处理迫在眉睫.     

Biosorption of Cr(III) from aqueous solution by freeze-dried activated sludge: Equilibrium,kinetic and thermodynamic studies

Batch biosorption experiments were conducted to remove Cr(III) from aqueous solutions using activated sludge from a sewage treatment plant. An investigation was conducted on the effects of the initial pH, contact time, temperature, and initial Cr(III) concentration in the biosorption process. The results revealed that the activated sludge exhibited the highest Cr(III) uptake capacity (120 mg·g⁻¹) at 45°C, initial pH of 4, and initial Cr(III) concentration of 100 mg·L⁻¹. The biosorption results obtained at various temperatures showed that the biosorption pattern accurately followed the Langmuir model. The calculated thermodynamic parameters, ΔG^o (−0.8– −4.58 kJ·mol⁻¹), ΔH^o (15.6–44.4 kJ·mol⁻¹), and ΔS^o (0.06–0.15 kJ·mol⁻¹·K⁻¹) clearly indicated that the biosorption process was feasible, spontaneous, endothermic, and physical. The pseudo first-order and second-order kinetic models were adopted to describe the experimental data, which revealed that the Cr(III) biosorption process conformed to the second-order rate expression and the biosorption rate constants decreased with increasing Cr(III) concentration. The analysis of the values of biosorption activation energy (E_a = −7 kJ·mol⁻¹) and the intra-particle diffusion model demonstrated that Cr(III) biosorption was film-diffusion-controlled.