医疗废物中有机质的热解动力学研究

在空气气氛下,对医疗废物中几种有代表性的有机质进行非等温热解实验。分析实验结果发现,热解失重曲线与N2气氛下不同,出现多个DTG峰。利用Freeman Carroll法求出了各有机质的表观动力学参数,并建立了能较好反映各物料失重过程的表观多步反应动力学模型。针对混合物料无法直接求出表观动力学参数,建立了多组分反应动力学模型。     

不干胶废弃物热解与燃烧动力学特性

采用热重分析方法对不干胶废弃物(PSAs)进行了热解和燃烧失重分析,并采用Doyle法拟合计算了PSAs热解和燃烧动力学参数。结果表明:当温度低于200℃或高于600℃,PSAs的热解和燃烧失重过程具有性;300~600℃时,PSAs热解过程具有3个失重峰,而其燃烧过程具有2个失重峰。动力学分析结果表明:PSAs的热解是由多阶段复杂的热裂解反应组成,其热解过程可用4个一级反应来描述,随着升温速率的提高热解阶段第1峰区表观活化能降低;而第2、3峰区以及半焦深度裂解阶段的第4峰区活化能逐渐升高;PSAs燃烧过程可用3个一级反应来描述,随着升温速率的提高,PSAs燃烧过程的表观活化能均逐渐降低,并且燃烧表观活化能均低于热解表观活化能。     

船舶塑料垃圾热解特性及动力学分析

利用热重分析(TGA)研究船舶塑料垃圾在不同升温速率和不同气氛下的热解特性,并得到了热解动力学参数。结果表明,船舶塑料垃圾的热解过程主要有3个阶段,比一般塑料热解复杂;随着升温速率增大,最大热解速率和最大热解速率温度等热解特性参数也增大,反应变得更剧烈;N2/CO2比为4∶1时,热解反应进行得最完全,固体残留率最少。动力学分析表明,采用3个连续一级反应模型能很好地拟合实验数据;不同的升温速率和气氛比对反应各阶段活化能均有不同程度的影响。     

不同升温速率下城市污水污泥热解特性及动力学研究

利用差热-热重分析法和Coats-Redfern积分法,对杭州某污水处理厂污泥在不同升温速率下的热解特性及反应动力学特征进行研究。实验结果表明,热解温度从室温升至900℃时,污泥热解过程可分为4个失重阶段;升温速率对污泥热解转化率、挥发分析出温度以及最大失重率等热解特性参数都有显著影响。升温速率越高污泥最大失重率越大;而较低的升温速率延迟了污泥热解反应时间,导致污泥失重量相对较大。根据Coats-Redfern积分法计算结果,污泥在氮气氛围下的热解反应为二级反应模式。提高升温速率可显著增加污泥热解的表观活化能和频率因子。     

污水污泥在富氧环境下燃烧特性的实验研究

采用综合热分析仪研究了空气气氛和富氧气氛下污水污泥和煤的燃烧曲线,分析比较氧浓度对污泥燃烧特性参数的影响,并计算得到各工况下的动力学参数。结果表明：随着氧浓度增加,污泥燃烧DTG曲线向低温区移动,着火温度和燃尽温度均降低,综合燃烧指数大大提高,污泥燃烧特性得到改善。可用两段一级反应动力学模型来较好的描述污泥的主要燃烧过...     

零价铁修复受三氯乙烯污染地下水的实验研究

通过批实验和柱实验研究了三氯乙烯（TCE）初始浓度、四氯乙烯(PCE)等对零价铁去除三氯乙烯的影响，并建立了三氯乙烯降解的反应动力学方程。结果表明：（1）零价铁对TCE具有较好的降解效果，反应符合准一级反应动力学方程，表观反应速率常数随TCE浓度的增加而减小；（2）在铁粉充足的条件下，TCE初始浓度对降解效果影响不显著，且TCE去除率皆可达到90%以上；（3）PCE的存在抑制了TCE的脱氯反应。PCE和TCE共存时，TCE的最大去除率仅为64.2%；TCE脱氯反应的表观反应速率明显降低，反应半衰期由TCE单独存在时的6.8～9.7 h增大到66 h～346.5 h。     

ACF脱除SO2/NOx反应器数学模型的建立

在大量试验研究获得数据基础上,结合机理分析,考虑ACF同时脱除多种污染物的主要影响因素,运用气固催化反应动力学方法进行分析,采用"混合模型法"建立ACF反应器数学模型,并用MATLAB软件与实验数据相结合迭代求取了模型参数,求出了宏观反应速率方程,并将计算模拟值与实验值进行比对,发现模拟结果与实验结果基本吻合,证实了模型的可靠性.为ACF反应器从试验研究的成果放大到工业规模的应用奠定了基础.     

热红联用研究废聚氨酯硬泡的燃烧特性

在热重分析仪上对废聚氨酯硬泡在空气中不同升温速率下加热的热失重行为进行了研究,并就升温速率对其热失重行为的影响进行了探讨.结果表明,随着升温速率的提高,废聚氨酯硬泡在空气气氛下热失重时挥发分析出温度(Ts)向高温区偏移,失重速率峰值(DTGmx)显著增大；空气气氛下,废聚氨酯硬泡热失重时有3个失重峰,后2个峰失重率分别约为41.51％和51.96％.同时,结合傅里叶变换红外光谱仪对各条件下的气体产物进行了定性分析,并对主要气体产物的释放规律做了探讨分析.实验发现,废聚氨酯硬泡热解燃烧失重主要阶段的产物种类相似,都检测到了CO、CO2、H2O、三氯一氟甲烷(CFC-11)、烯烃类、烷烃类、醇类、含氯化合物和带有苯环类化合物的特征吸收峰；主要气体产物有相似的析出规律,说明升温速率的变化并未影响到样品在空气气氛下的反应机制.     

臭氧水中传质模型的研究

在传统鼓泡塔中对臭氧在水中的传质过程进行实验研究。利用实验改变进水流量、臭氧进气流量以及臭氧进气浓度等，得到臭氧传质系数、臭氧传质效率和臭氧消耗等有关参数。建立一个臭氧传质模型，可以预测不同操作条件下臭氧传质效率，从而优化控制臭氧化反应动力学。     

城市生活垃圾典型组分的热解动力学分析

利用热分析仪对城市生活垃圾中典型组分的热解过程进行了热重分析实验，采用不同形式的反应机理函数对实验结果进行了线性拟合计算，得到了针对不同组分的最合理的反应机理函数形式，并求出了相应的反应活化能E及频率因子A，由此构建了能更准确地反映垃圾各组分的热解反应过程的动力学模型。计算结果表明，垃圾中多数组分的热解过程用扩散模型来表示最为合理。     

石灰预处理和干发酵对稻草热解特性影响

深入研究生物质热解有助于热解机理的理解,利用热重分析来探讨石灰预处理和干发酵对稻草热解特性的影响。结果表明:预处理使木质素和半纤维素含量增加,而干发酵使VS、半纤维素和纤维素含量降低;预处理和干发酵改变稻草热解特性,但未改变稻草的热反应机理;热解一级动力学方程很好模拟稻草热解的主失重阶段,稻草热解活化能数值为42.3～47.8 kJ/mol,属于正常范围;预处理降低反应活化能,而干发酵增加反应活化能。这为秸秆及其干发酵残渣的气化提供了重要的设计依据。     

罐底含油泥热解动力学参数计算方法的优选

在化学反应设计中反应动力学是较重要的因素。为得到更合理的污泥热解动力学参数计算方法,利用热重分析仪,在氮气气氛下对罐底含油污泥的热解特性进行研究。根据热重实验数据,分别采用Coats-Redfern法、Kissinger法、FWO法和Popescu法计算污泥热解动力学参数,并获取罐底泥热解制油的主要阶段(第2阶段)的反应活化能E、频率因子A并分析各种方法反应机理。通过对比不同计算方法得到动力学参数及拟合曲线与实验曲线的相关性,确定了最佳罐底含油污泥热解动力学参数计算方法。研究表明,Popescu法得到罐底泥的热解过程符合Jander方程,活化能E为101.43 kJ/mol,与FWO法得到的91.20 kJ/mol相近,且预测曲线与实验曲线有较好的相关性(0.9816),说明Popescu法计算罐底泥热解动力学参数更合适。     

Sorption-desorption behaviour of 2,4-dichlorophenol by marine sediments

Batch kinetic and isotherm experiments were conducted to determine the sorption-desorption behavior of 2,4-dichlorophenol from seawater solutions by marine sediments containing various amounts of organic carbon (from 1.02% to 12.72% dry weight). The results indicated linear type isotherms for sorption and desorption in all marine sediments studied. The observed difference in linear sorption coefficients between sorption and desorption was indicative of sorption hysteresis. The kinetic experiments showed that equilibrium was established in less than 20 h. The study is significant with respect to sediment remediation in contaminated harbors and coastal areas.     

吸附-电化学氧化耦合处理对氯苯酚废水及动力学

以毡状活性炭纤维为阳极,不锈钢为阴极,吸附-电化学氧化耦合降解对氯苯酚废水进行了研究。考察了吸附或耦合电化学氧化过程、电流密度、支持电解质硫酸钠浓度和活性炭纤维重复使用对废水COD去除率的影响,结果表明,采用吸附-电化学氧化耦合方法,当电流密度7.6 mA/cm2支持电解质（硫酸钠）浓度为1 g/L,处理时间为180 min,4-CP废水COD去除率可达97.09%。毡状活性炭纤维对4-CP的静态吸附过程符合Langmiu吸附等温方程。建立了吸附-电化学氧化COD去除动力学模型,动力学模型参数表明,对于COD的去除,电化学氧化作用比吸附作用大。     

Kinetics of phenol degradation in an anaerobic fixed-biofilm process.

A mathematical model was developed to describe phenol degradation in an anaerobic fixed-biofilm process. The model incorporates the mechanisms of diffusive mass transport and Monod kinetics. The model was solved using a combination of the orthogonal collocation method and Gear's method. A pilot-scale column reactor was used to verify the model. Batch kinetic tests were conducted independently to determine the biokinetic parameters used in the model, while shear loss and initial thickness of biofilm were assumed so that the model simulated the substrate concentration results well. The removal efficiency for phenol was approximately 98.5% at a steady-state condition. The model accurately described the effluent substrate concentrations and the sequence of biodegradation in the reactor. The model simulations are in agreement with the experimental results. The approaches presented in this paper could be used to design fullscale anaerobic fixed-biofilm reactor systems for the biodegradation of phenolic substrates.     

Characterization of metal adsorption kinetic properties in batch and fixed-bed reactors

Copper adsorption kinetic properties in batch and fixed-bed reactors were studied in this paper. The isothermal adsorption experiments showed that the copper adsorption capacity of a granular activated carbon (Filtrasorb 200) increased when ionic strength was higher. The presence of EDTA diminished the adsorption. An intraparticle diffusion model and a fixed-bed model were successfully used to describe the batch kinetic and fixed-bed operation behaviors. The kinetics became faster when the solution pH was not controlled, implying that the surface precipitation caused some metal uptake. The external mass transfer coefficient, the diffusivity and the dispersion coefficient were obtained from the modeling. It was found that both external mass transfer and dispersion coefficients increased when the flow rate was higher. Finally effects of kinetic parameters on simulation of fixed-bed operation were conducted.     

Kinetic studies of adsorption of lead(ll) from aqueous solution by wine-processing waste sludge.

A waste sludge produced from a wine-processing wastewater treatment process was used as an adsorbent to removal of heavy metal-lead(II) from aqueous solution. Results of kinetic experiments demonstrated that the adsorption was effective and rapid. Four different kinds of adsorption kinetic models (i.e., pseudo-first-order, pseudo-second-order, and two intra-particular mass diffusion models) were used to investigate the adsorption mechanisms. A normalized standard deviation was used to find the best adsorption kinetic model for the removal of lead(ll) by the sludge. The comparison shows that the kinetic adsorption data can be well-described by the pseudo-second-order adsorption model and that sorption might be a rate-limiting control. The adsorption-rate constant and adsorption capacity of pseudo-second-order adsorption equation were calculated. The parameters (initial lead(II) concentration, sludge-particle size, and sludge dosages), which affect the adsorption capacity of sludge, were discussed by using the pseudo-second-order adsorption equation.     

可旋转径向式微粒捕集器消声特性影响因素灰色关联分析

为降低可旋转径向式微粒捕集器中的排气噪声,采用有限元法建立可旋转径向式微粒捕集器声学特性模型,分析得到了其消声特性和传递损失曲线,并采用灰色关联分析方法研究可旋转径向式微粒捕集器结构参数对消声特性的影响程度。结果表明,可旋转径向式微粒捕集器具有降噪能力,且对高频噪声消声效果明显好于低频噪声,平均消声量为20 dB左右;直径比和扩张管锥角是影响可旋转径向式微粒捕集器消声特性的2个主要因素,适当选用小的直径比和扩张管锥角,有利于提高可旋转径向式微粒捕集器的消声性能。