活性炭辅助微波活化煤矸石的“枣糕”模型

采用活性炭辅助微波活化煤矸石,将煤矸石的活化时间由传统高温焙烧方法的2 h缩短到了24 min以内。将70目活性炭与200目煤矸粉以2.0∶1的质量配比充分混合后在800 W微波功率下活化24 min,铝铁浸出率可达750℃焙烧2 h的1.71倍。将微波看做实体物质,将活化过程看做是由活性炭向煤矸粉的单向微波能量传递,引入化学反应工程学方法,"枣糕"模型计算表明,在680 W功率下,活性炭的微波附着速率常数ka=0.334 min-1,微波脱附速率常数k’a=0.050 min-1,煤矸粉的微波附着速率常数kb=0.262 min-1,相关系数R=0.99997。在528、680、800 W 3个功率水平下,"枣糕"模型的计算值均与实验值拟合良好,相关系数均高于0.999,在以上3功率下,发现极限铝铁相对浸出率a与极限温升ΔTmax近似成正比。     

AOAB工艺处理难降解混合化工污水的挂膜启动

采用AOAB(水解酸化A1+生物接触氧化O+深度水解酸化A2+曝气生物滤池BAF)工艺处理难降解混合化工污水,重点研究工艺挂膜方式和生物膜的驯化。结果表明,采用分段连续式挂膜法进行反应器挂膜,20 d即可完成快速挂膜启动;采用分阶段同步培养驯化法驯化生物膜,30 d内可完成高浓度多组分混合化工污水进水的驯化,最终进水COD 1 456 mg/L,出水COD 324 mg/L,总去除率76.85%,驯化效果显著;整个工艺对COD的降解主要集中在生物接触氧化池和曝气生物滤池,驯化期间生物接触氧化池去除率稳定在40%左右,曝气生物滤池去除率稳定在50%以上。同时,通过对比一段水解酸化和深度水解酸化的VFA(挥发性脂肪酸)产出,表明在高有机负荷进水时,一段水解酸化降解大分子有机物的能力有限,但这些有机物可通过二段水解酸化再次降解,由此体现了AOAB工艺在处理多组分混合型的难降解化工污水的优势。     

回灌型准好氧填埋场脱氮特性及加速稳定化研究

采用2个模拟填埋生物反应器,1号柱渗滤液简单回灌,2号柱为渗滤液回灌准好氧联合运行方式,研究了渗滤液回灌准好氧生物反应器填埋场的脱氮特性及加速垃圾稳定化特性.研究结果表明:渗滤液回灌准好氧填埋场具有很强的脱氮能力,2号柱由厌氧运行方式改为准好氧条件下,渗滤液中的氨氮和凯式氮浓度分别由最大值的3 198 mg/L和3 345 mg/L降低到第160 d的73 mg/L和81 mg/L,去除率分别为97.7%和97.6%,pH快速升高到8.0左右,COD浓度快速降低.渗滤液中溶解性有机物(DOM)分级结果表明,2号柱HA和FA含量的增加明显快于1号柱.2号柱DOM的三维荧光光谱特性发生了较大变化,荧光基团从60 d结构简单的类蛋白物质转变为95 d结构复杂的类胡敏酸和富里酸物质,而l号柱渗滤液DOM荧光基团一直是结构简单的类蛋白物质.结果表明回灌准好氧生物反应器填埋场的稳定化速度远快于简单回灌的生物反应器填埋场.     

垃圾填埋场填埋气产生与迁移计算机模拟

准确预测填埋场内填埋气随时间和空间的变化规律,对填埋场的管理和填埋气的合理应用具有重要作用.以多孔介质流体动力学理论为基础,构建了填埋场中气体迁移转化过程三维模型.应用有限单元法和迭代法对模型的非线性方程组进行了求解,计算了填埋场中气体的压力分布情况.结果表明,填埋初期气压随深度和时间的增加而增加;而后气压随时间增加逐渐减小.     

处理日本遗弃在华化学武器专用透气防毒服的研究

本文针对日本遗弃在华化学武器的性质和特点,根据销毁工程对个人防护装备的需求．通过对目前国内外主要透气防毒材料的比较分析,提出了专用透气防毒服内外层纺织材料的技术性能指标和要求．为专用透气防毒服的研制做了前期技术准备。     

整装沙漠油田废水零排放的研究探索

文章介绍了陆梁油田通过对采出水处理工艺进行优化,并将其应用于油田水处理厂罐内喷淋除气技术等工艺;污水回收工艺作业废液处理采用二段式自然除油沉降原理进行预处理;利用反应吸附技术进行废液二次处理,生活污水一元化处理等工艺,对油田废水进行处理回注。年节约费用671.8万元,实现废水零排放,达到了环境保护和经济效益双赢的目的,为沙漠油田污水处理提供借鉴。     

河北省高校社会体育专业培养目标及学生满意度调查分析

运用文献资料法、问卷调查法、数理统计法和对比分析法,对我省社会体育专业本专科院校的培养目标情况、学生收获和满意度情况进行调查分析。研究结果表明,中环院社会体育专业学生对课程体系设置的满意度最高,就业信心指数最大。进一步分析可知,以社会体育产业为目标定位、以能力本位为教育模式对社会体育专业学生的培养具有一定的优越性     

Spatial distribution,potential risk assessment,and source apportionment of polycyclic aromatic hydrocarbons (PAHs) in sediments of Lake Chaohu,China

Twenty-nine sediment samples were collected from Lake Chaohu, a shallow eutrophic lake in Eastern China, and were analyzed for 15 priority polycyclic aromatic hydrocarbons (PAHs) to determine the spatial distribution and exposure risks of PAHs. Three receptor models, the principal component analysis-multiple linear regression (PCA-MLR) model, the positive matrix factorization (PMF) model, and the Unmix model, were used in combination with the PAHs diagnostic ratios to investigate the potential source apportionment of PAHs. A clear gradient in the spatial distribution and the potential toxicity of PAHs was observed from west to east in the sediments of Lake Chaohu. ∑₁₅PAH concentrations and the TEQ were in the range of 80.82-30 365.01 ng g^?1 d.w. and 40.77-614.03, respectively. The highest values of the aforementioned variables were attributed to urban–industrial pollution sources in the west lake region, and the levels decreased away from the river inlets. The three different models yielded excellent correlation coefficients between the predicted and measured levels of the 15 PAH compounds. Similarly, source apportionment results were derived from the three receptor models and the PAH diagnostic ratios, suggesting that the highest contribution to the PAHs was from coal combustion and wood combustion, followed by vehicular emissions. The PMF model yielded the following contributions to the PAHs from gasoline combustion, diesel combustion, unburned petroleum emissions, and wood combustion: 34.49, 24.61, 16.11, 13.01, and 11.78 %, respectively. The PMF model produced more detailed source apportionment results for the PAHs than the PCA-MLR and Unmix models.     

An efficient resin for solid-phase extraction and determination by UPLCMS/MS of 44 pharmaceutical personal care products in environmental waters

• A hydrophilic resin (GCHM) was facile synthesis and characterized. • Average absolute recovery of GCHM (75.6%) performs better than Oasis^® HLB. • Detection limits of method (SPE-UPLC-MS/MS) ranged between 0.03 and 0.6 ng/L. • 22 PPCPs were determined in environmental waters ranging from 0.5 to 1590 ng/L. In this study, a hydrophilic resin named GCHM was fabricated based on poly(N-vinyl pyrrolidone-co-divinylbenzene), characterized, and applied as a solid-phase extraction (SPE) material. Up to 44 pharmaceuticals and personal care products (PPCPs) belonging to 10 classes were recovered in environmental water samples. Different variables affecting extraction, such as adsorbent amount, sample pH, and loading speed, were optimized. Under optimal conditions, the average absolute recovery of 44 PPCPs was 75.6% using GCHM, indicating a better performance than the commercial Oasis^® HLB. SPE with home-made hydrophilic polymeric sorbent followed by ultra-performance liquid chromatography and tandem mass spectrometry was validated, and the method achieved good linearity (r²>0.991, for all analytes). In addition, the method detection limits of target compounds ranged from 0.03 to 0.6 ng/L. The developed method was applied to determine PPCPs in 10 environmental water samples taken from the Yangtze River, Huaihe River, and Taihu Lake, 1 groundwater sample from Changzhou in Jiangsu Province, 1 wastewater sample from Xiamen and 2 seawater samples from the Jiulong River in Fujian Province, China. In these samples, 22 compounds were determined at levels ranging from 0.5 to 1590 ng/L.     

Effects of Pd doping on N<Subscript>2</Subscript>O formation over Pt/BaO/Al<Subscript>2</Subscript>O<Subscript>3</Subscript> during NO<Subscript><Emphasis Type="Italic">x</Emphasis></Subscript> storage and reduction process

N₂O is a powerful greenhouse gas and plays an important role in destructing the ozone layer. This present work investigated the effects of Pd doping on N₂O formation over Pt/BaO/Al₂O₃ catalyst. Three types of catalysts, Pt/BaO/Al₂O₃, Pt/Pd mechanical mixing catalyst (Pt/BaO/Al₂O₃ + Pd/Al₂O₃) and Pt-Pd co-impregnation catalyst (Pt-Pd/BaO/Al₂O₃) were prepared by incipient wetness impregnation method. These catalysts were first evaluated in NSR activity tests using H₂/CO as reductants and then carefully characterized by BET, CO chemisorption, CO-DRIFTs and H2-TPR techniques. In addition, temperature programmed reactions of NO with H2/CO were conducted to obtain further information about N₂O formation mechanism. Compared with Pt/BaO/Al₂O₃, (Pt/BaO/ Al₂O₃ + Pd/Al₂O₃) produced less N₂O and more NH3 during NO _x storage and reduction process, while an opposite trend was found over (Pt-Pd/BaO/Al₂O₃ + Al₂O₃). Temperature programmed reactions of NO with H₂/CO results showed that Pd/Al₂O₃ component in (Pt/BaO/Al₂O₃ + Pd/Al₂O₃) played an important role in NO reduction to NH₃, and the formed NH3 could reduce NO _x to N₂ leading to a decrease in N₂O formation. Most of N₂O formed over (Pt-Pd/BaO/Al₂O₃ + Al₂O₃) was originated from Pd/BaO/Al₂O₃ component. H₂-TPR results indicated Pd-Ba interaction resulted in more difficultto- reduce PdOx species over Pd/BaO/Al₂O₃, which inhibits the NO dissociation and thus drives the selectivity to N₂O in NO reduction.

Open image in new window