An assessment of how distance and diesel oxidation catalyst will impact thermal decomposition behaviors of particles

Decomposition mass loss and pyrolysis products analyses of particles sampled at various locations along the tailpipe of a Euro-IV diesel engine were performed using a thermogravimetry in conjunction with Fourier transformation infrared spectrometry-mass spectrum. Diesel particles were collected at the same location with and without diesel oxidation catalyst (DOC) mounted on the test engine separately. The three poles in thermal gravity-differential thermal gravity images suggested that the decomposition process of diesel particles could be divided into three stages which correspond to the decompositions of lower boiling substances, higher boiling substances and soot respectively. It is noticed that no matter whether DOC was mounted or not, the further the particles were sampled away from the engine block, the lower the peak temperatures and the heavier the mass losses within the first two stages, which indicated that the soluble organic fraction in the particle samples increased and therefore lowering the activation energy of thermal decomposition. Hydroxyl, ammonia, C_xH_y fragments, benzene, toluene, and phenol were found to be the primary products of particle decomposition, which didn't change with the location of particle sample point. The employment of DOC increased the activation energy for particle oxidation and resulted in a higher peak temperature and lower mass loss within the first-stage. Moreover, the CO stretching bands of aldehyde and ketone at 1771 cm^?1 was only detected without a DOC, while the NO₂ peak at 1634 cm^?1 was solely noticed with the presence of DOC. Compared to the first-stage pyrolysis products, more polycyclic aromatic hydrocarbons and less C_xH_y fragments were seen in the second-stage.     

脱水污泥薄层干燥特性及动力学模型分析

采用薄层干燥方式进行脱水污泥热干燥的研究,考察了污泥的干燥特性,并引入薄层干燥模型进行数值分析.结果表明, Logarithmic模型比其他模型更适合薄层污泥干燥分析.应用Fick扩散模型,得到80~150℃条件下薄层污泥干燥的有效扩散系数的变化范围为8.486′10-10~4.386′10-9m2/s,并根据Arrhenius经验公式建立温度与扩散系数的关系,得到污泥干燥时水分扩散的活化能为29.56kJ/mol.     

基于生物膜法磷回收工艺厌氧释磷研究

城市污水经过碳回收后的低碳源进水水质将对活性污泥法强化除磷（EBPR）工艺的运行带来困难.本研究基于生物膜法磷回收的序批式反应器（Biofilm-SBR）对低碳、低磷进水进行磷回收,在BSBR反应器好氧无碳源、厌氧低碳源投加的运行基础上,研究了该工艺在低碳模式下厌氧磷释放的关键影响因素.同时,研究了不同的碳源浓度和碳源投加方式对BSBR工艺释磷的影响.最后,分析了系统中生物膜蓄磷量的变化,并探究其与碳源消耗、释磷效果的量化关系.结果表明,该系统在好氧无碳源、厌氧仅200 mg·L^-1的碳源投加下,即可取得115 mg·L^-1（可溶性磷）的富磷回收液.系统的C_upt/P_rel（释放单位质量磷的COD消耗量）平均为（11.12±1.03）mg·mg^-1,最大蓄磷量为124 mg·g^-1.     

基于时空尺度的中国省级区域能源消费碳排放公平性分析

为深入了解各省级区域能源消费碳排放的差异性和公平性,论文通过对基尼系数内涵的扩展,构建碳排放公平性评价模型,计算1996-2008年能源消费碳排放的生态基尼系数和经济基尼系数,结果表明:从生态角度,能源消费碳排放的不公平程度逐渐减小,但仍然处于"高度不平均"状态;从经济角度,能源消费碳排放的不公平程度先上升后下降,位于"相对平均"区间。同时,提出经济贡献系数和生态承载系数以评价2008年各个省级区域能源消费碳排放的公平性和差异性,利用贡献系数矩阵对各个区域进行类型划分,阐述各个类别的特点,以期为国家制定区域差别化的节能减排政策提供依据,提升应对气候变化的整体能力。     

近海沉积物组份对有机物的吸附与吸附机理探讨

以大连近海沉积物主要组份碳酸钙、金属氧化物、腐殖酸和粘土矿物为沉积物模拟样品,测定该4种组份对硝基苯等4种毒性有机的吸附等温线,在此基础上建立了多组份吸附剂吸附等温模式。通过吸附热的测定,探付了4种沉积物组份吸附毒性有机物的机理,并比较了相对吸附能力大小     

裂纹梁损伤识别的一种新型方法

在能量有限元法研究基础上,提出了基于能量密度的结构损伤识别方法。以工程结构基本构件梁为研究对象,以能量密度突变作为损伤识别指标,对损伤结构进行了仿真;在此基础上,对结构损伤中最常见的形式——裂纹进行损伤识别试验。结果表明基于能量密度的损伤识别方法适用于中高频场合,具有对结构微小缺陷敏感、操作简便、精确度高、无需复杂数据处理等优点,有较高的工程应用价值。     

秸秆生物炭吸附对乙酰氨基酚的机制及其位能分布特征

作为药品和个人护理产品（PPCPs）中用量最大的一类,对乙酰氨基酚广泛存在于水环境中,具有潜在的环境风险;因此,有必要对其去除机制开展研究.基于我国农业秸秆资源高值转化的需求,通过热解制备秸秆生物炭吸附净化水中对乙酰氨基酚具有良好的应用前景.然而秸秆生物炭对对乙酰氨基酚的吸附过程和机制尚不清楚.选用4种秸秆（稻秆、麦秆、玉米秆和大豆秆）作为原料,通过热裂解在400℃和500℃制备生物炭,进行序批吸附实验,同时研究腐殖酸和pH对吸附过程的影响.结果表明,基于Freundlich模型和位置能量分布模型可知,500℃生物炭对对乙酰氨基酚的吸附量显著高于400℃生物炭（吸附系数K_F高出1.16~2.53倍）,且具有较多的高能吸附位点.高温热解生物炭的主要吸附机制为孔道吸附和π-π作用;低温热解生物炭的主要吸附机制为表面氢键作用.腐殖酸对对乙酰氨基酚在生物炭上的去除具有协同效应,这归因于所选腐殖酸具有一定芳香性,可促进与对乙酰氨基酚的相互作用.pH升高抑制生物炭吸附主要归因于对乙酰氨基酚团聚.吸附机制研究表明,可通过提高热解温度促进对乙酰氨基酚在秸秆生物炭上的孔道吸附和π-π作用;腐殖酸和pH影响研究表明,秸秆生物炭与对乙酰氨基酚的相互作用不受腐殖酸影响,在低pH环境下也具有良好吸附性能.     

能量耗损相关底物消耗对微生物产率的影响

根据底物反应平衡,提出在底物充分的条件下,微生物消耗的底物总量等于微生物生长所利用的量,微生物维持代谢所利用的量及由于能量代谢分离而消耗的量之和,由此,建立了描述在底物充分的条件下,微生物产率与剩余底物浓度相应关系的动力学模型,证明了观测到的产率随剩余底物２的增加而减少的现象,此模型能很好实验数据相符,结果表明随剩余的底物２的增加,微生物的产率可下降７０％左右。     

Oxidation inhibition of sulfite in dual alkali FGD system

A laboratory-scale well-mixed thermostatic reactor with continuously blasting air was used to investigate the oxidation inhibition of sulfite in dual alkali flue gas desulfurization （FGD） system. The effects of operating parameters such as pH value and catalyst concentration on the oxidation were studied. Sodium thiosulfate was used in the system, and was found that it significantly inhabited the sulfite oxidation. In the absence of catalyst, sodium thiosulfate at 12.67 mmol/L had an inhibition efficiency of approximately 98%. While in the presence of catalyst, sodium thiosulfate at 26.72 mmol/L had an inhibition efficiency less than 85.0%. The oxidation reaction order of sulfite in the sodium thiosulfate was determined to be -1.90 and 4）.55 in the absence and presence of the catalyst, respectively. Apparent activation energy of oxidation inhibition was calculated to be 53.9 kJ/mol. Pilot tests showed that the consumption rate of thiosulfate agreed well with the laboratory-scale experimental results.     

长期施肥对红壤稻田耕层土壤碳储量的影响

以红壤性稻田土壤为对象,研究了长期施肥（1990～2006年）对稻田表层土壤碳储量及固碳潜力的影响,讨论了耕层厚度变化对碳储量估算及处理间差异的影响.研究发现,与长期施用化肥相比,有机物的循环利用能显著提高红壤性稻田土壤碳储量,其碳储量为57.7～66.2 t/hm²,比试验前高出18.7～27.2 t/hm²,而长期施用化肥碳储量提高幅度平均为5.4 t/hm².红壤性稻田土壤饱和固碳量为84.0 t/hm²,与目前碳储量相比还有17.8～43.7 t/hm²的固碳潜力.研究证实,土壤碳储量与土壤容重和表层土壤厚度的变化密切相关,以20 cm或23 cm作为统计厚度估算表层土壤的碳储量将分别低估20.6％和11.3％,其中有机物施用处理碳储量低估幅度最大（分别为26.8％和18.9％）;另外,用相同统计厚度进行碳储量估算减小了不同施肥处理间的差异.从稻田土壤碳储量及固碳潜力来考虑,有机物配合化肥施用是红壤稻田较优的施肥方式.