垃圾填埋场填埋气竖井收集系统设计优化

目前实际工程中通常采用现场抽气试验的方法确定垃圾填埋气收集系统的相关技术参数 ,这种方法不能对影响抽气效果的因素综合分析并加以优化。本文利用竖井抽气条件下填埋气压力分布模型 ,分析讨论了抽气系统各参数对对抽气效果的影响 ,提出了垃圾填埋场填埋气竖井收集系统的抽气量、抽气井影响半径、抽气井埋深的优化设计方法 ,可为填埋气污染控制与回收利用系统的规划设计及运行管理提供技术支持     

Heavy metals removal in fixed-bed column by the macro fungus Pycnoporus sanguineus

The ability of Pycnoporus sanguineus to adsorb heavy metals from aqueous solution was investigated in fixed-bed column studies. The experiments were conducted to study the effect of important design parameters such as column bed height, flow rate and initial concentration of solution. The breakthrough profiles were obtained in these studies. A mathematical model based on external mass transfer and pore diffusion was used for the prediction of mass transfer coefficient and effective diffusivity of metals in macro-fungi bed. Experimental breakthrough profiles were compared with the simulated breakthrough profiles obtained from the mathematical model. Bed Depth Service Time (BDST) model was used to analyse the experimental data and evaluated the performance of biosorption column. The BDST model parameters needed for the design of biosorption columns were evaluated for lead, copper and cadmium removal in the column. The columns were regenerated by eluting the metal ions using 0.1 M hydrochloric acid solution after the adsorption studies. The columns were subjected to repeated cycles of adsorption of same metal ions and desorption to evaluate the removal efficiency after adsorption-desorption.     

响应面法优化袋式除尘器脉冲清灰性能

基于计算流体动力学的方法采用三维、可压缩、非稳态流动数学模型对袋式除尘器脉冲清灰过程进行了数值模拟,得到了滤袋内外压差,并与文献实验值进行了比较,验证了仿真模型的可靠性。基于响应面法研究了喷吹压力、喷吹高度、滤袋直径和滤袋长度对脉冲清灰性能的影响,得到这4个影响因子的二次多项式预测模型,并进行优化。结果表明,喷吹压力为0.3 MPa,喷吹高度为0.2 m,滤袋直径为0.16 m,滤袋长度为6 m时,内外压差峰值最优,优化结果与仿真模拟结果相差小于3%。研究结果为袋式除尘器脉冲清灰系统的设计与优化提供了重要参考。     

Removal of arsenic from drinking water by chemical precipitation--a modeling and simulation study of the physical-chemical processes.

A dynamic mathematical model was developed for removal of arsenic from drinking water by chemical coagulation-precipitation and was validated experimentally in a bench-scale set-up. While examining arsenic removal efficiency of the scheme under different operating conditions, coagulant dose, pH and degree of oxidation were found to have pronounced impact. Removal efficiency of 91-92% was achieved for synthetic feed water spiked with 1 mg/L arsenic and pre-oxidized by potassium permanganate at optimum pH and coagulant dose. Model predictions corroborated well with the experimental findings (the overall correlation coefficient being 0.9895) indicating the capability of the model in predicting performance of such a treatment plant under different operating conditions. Menu-driven, user-friendly Visual Basic software developed in the study will be very handy in quick performance analysis. The simulation is expected to be very useful in full-scale design and operation of the treatment plants for removal of arsenic from drinking water.     

喷雾增湿设备的数学模拟设计

系统论述了喷雾增湿塔内水滴的运动状态与含尘气体的流动特性,建立了一个能反映喷雾增湿操作过程的数学模型,有助于确定该设备生产操作中的最佳控制参数.     

A2O氧化沟缺氧区三维流场模拟及结构形式优化

以FLUENT软件为工具,选用三维RNG k-ε紊流数学模型对重庆井口污水厂A2O氧化沟缺氧区内的流场进行模拟,分析了缺氧区内流场分布不均匀及沉泥的原因,提出了水下推进器的合理设置位置与导流墙的合理设置方式,并对优化后的缺氧区进行了模拟计算。通过优化后模拟的结果可见,在相同的功率密度下,缺氧区内的流场得到了较均匀的分布,流速从原来的0.131 m/s提升到0.204 m/s,减少了能量的损失。底部的流速也从原来的0.140 m/s提升到0.226 m/s,有效的防止或减少了沟中的污泥沉积。优化的结果对实际工程的设计也有一定的指导意义。     

A2O氧化沟缺氧区三维流场模拟及结构形式优化

以FLUENT软件为工具,选用三维RNG k-ε紊流数学模型对重庆井口污水厂A²O氧化沟缺氧区内的流场进行模拟,分析了缺氧区内流场分布不均匀及沉泥的原因,提出了水下推进器的合理设置位置与导流墙的合理设置方式,并对优化后的缺氧区进行了模拟计算。通过优化后模拟的结果可见,在相同的功率密度下,缺氧区内的流场得到了较均匀的分布,流速从原来的0.131 m/s提升到0.204 m/s,减少了能量的损失。底部的流速也从原来的0.140 m/s提升到0.226 m/s,有效的防止或减少了沟中的污泥沉积。优化的结果对实际工程的设计也有一定的指导意义。     

内循环厌氧反应器多相流流场的三维数值分析

利用数值模拟的方法,引入欧拉双流体多相流模型及标准k-s紊流模型,模拟计算内循环厌氧反应器的三相流三维流场,并通过改变污泥颗粒密度及进水流量,针对固相流速及固含率的变化情况,分析条件的改变对流场的影响。研究结果表明,应用数值模拟方法可以获得内循环厌氧反应器内的流场特征;污泥颗粒密度及进水流量的改变对于反应器内污泥颗粒的流速及分布的均匀性有较为明显的影响。模拟结果对反应器的应用及优化设计具有一定的参考价值。     

Removal of carbon disulfide via coupled reactions on a bi-functional catalyst: experimental and modeling results

A mathematical model describing the rate of carbon disulfide (CS₂) removal due to coupled reactions has been developed. Kinetic studies were carried out in a fixed bed reactor under atmospheric pressure and a range of temperatures (85–125 °C). The effects of flow rate, CS₂ inlet concentration, temperature and relative humidity were analyzed. A kinetic model based on axial dispersion, external and internal mass-transfer resistances, as well as effects of S deposition on the inner-face of the catalyst was in agreement with the CS₂ experimental breakthrough curves. The mathematical model can be used for process design and scale up of similar systems.     

Experimental design strategy for the Weibull dose response model

The objective of this research was to determine optimum design point allocation for estimation of relative yield losses from ozone pollution when the true and fitted yield-ozone dose response relationship follows the Weibull. The optimum design is dependent on the values of the Weibull model parameters. A transformation was developed which allowed the optimum design (by the determinant criterion) for one parametric situation to be translated to any other, and permitted the search for optimum designs to be restricted to one set of Weibull parameters. Optimum designs were determined for the case where the Weibull parameters are assumed known, and effects of deviating from the optimum designs were investigated. Several alternative design strategies were considered for protecting against incorrectly guessing the Weibull model parameters when their true values are not known.     

响应面法优化电渗析处理褐藻酸钠废水工艺

采用电渗析器处理过滤的褐藻酸钠废水,褐藻酸钠废水初始水质如下:Ca2+(56 mg/L)、Cl-(1 808 mg/L)、电导率(7.24 mS/cm)。处理目标值如下:Ca2+(60 mg/L)、Cl-(300 mg/L)、电导率(2.50 mS/cm)。运用Design-Expert分析软件,采用Box-Behnken的中心组合设计方法,研究了流量、电压及淡水浓水体积比及其交互作用对直流电耗的影响。建立了电渗析处理褐藻酸钠废水的二次多项数学模型,并以电渗析的直流电耗为响应值做响应面,确定电渗析处理褐藻酸钠废水的最佳工艺条件为:流量200 L/h、电压40 V、淡水浓水体积比1∶1。在此条件下电渗析的直流电耗最小为0.45 kWh/kg,电渗析器处理后的水质如下:Ca2+(56 mg/L)、Cl-(259 mg/L)、电导率(2.00 mS/cm),达到处理目标。     

The tidal hydrodynamics modeling of the Topolobampo coastal lagoon system and the implications for pollutant dispersion

The tidal hydrodynamics of the Topolobampo coastal lagoon system (Mexico) has been investigated through a modified two dimensional non-linear hydrodynamic finite difference model. The advective and diffusive process acting over a hypothetical pollutant released into the coastal lagoon have also been simulated. Maxima tidal currents (0.85 m/s) were predicted within the main channel, in agree with direct measurements. The direction of the observed fastest currents (SW), also agree quite well with the direction of the strongest tidal current predicted in this investigation, which occur during the ebb when the water of the coastal lagoon is discharged into the Gulf of California. Residual currents (0.01-0.05 m/s) were also predicted. The hypothetical pollutant released within the Topolobampo Harbor would spread to both Ohuira and Topolobampo sections, reaching the inlet after approximately 12 days.     

卡鲁塞尔氧化沟反应器两相流PIV图像处理研究及实验分析

在单相数字粒子图像测速度(PIV)技术的基础上,研究了PIV两相流动的测试及图像处理方法.利用数学形态学的原理以及互相关法,对两相粒子图像进行标定、识别、区分和流场分析,编辑了相应的软件.并采用此技术对卡鲁塞尔氧化沟模型直道及弯道段二维液固两相流速进行测量,克服了传统点测量方法无法获取全场流动同步信息的缺陷,较好地反映了不同位置处固液流动分布的基本特性.结果表明,沟内径向流速远小于轴向,流速大小相差约一个数量级;同一断面上轴向流动分布是决定水力特性的主要因素;径向流速和水体动能是决定污泥沉积位置的主要因数,固相总体流速小于液相.     

Removal of carbon disulfide via coupled reactions on a bi-functional catalyst: Experimental and modeling results

A mathematical model describing the rate of carbon disulfide (CS₂) removal due to coupled reactions has been developed. Kinetic studies were carried out in a fixed bed reactor under atmospheric pressure and a range of temperatures (85–125 °C). The effects of flow rate, CS₂ inlet concentration, temperature and relative humidity were analyzed. A kinetic model based on axial dispersion, external and internal mass-transfer resistances, as well as effects of S deposition on the inner-face of the catalyst was in agreement with the CS₂ experimental breakthrough curves. The mathematical model can be used for process design and scale up of similar systems.     

汽车尾气催化转化器模型研究进展

本文主要介绍汽车尾气催化转化器模型的研究进展 ,包括反应器内气体流动特性、单通道反应器内的传递现象和反应动力学、通道间的热传递和反应行为的模拟 ;并指出认识反应器内的各种特性和规律对设计汽车尾气催化转化器的必要性和意义     

太湖湖滨带的缓冲效果

在以农田．防护林．鱼塘为主的农业缓冲带一宜兴周铁太湖湖滨带内,比较和分析了不同降水时期和不同鱼塘排水时期湖滨带的缓冲效果。结果显示湖滨带的主要污染物是有机污染物、TN和Chla,尤其是有机污染物;TP污染相对较轻,NH4＋-N和BOD5污染很少。太湖湖滨带对N、P、COD等指标均有一定的缓冲效果,但对不同指标的缓冲能力不同,其中对N的缓冲效果更为明显。除COD外,湖滨带出水口基本可以达到IV类水水平。同时,强降雨导致大量污染物进入水体,导致水体污染物输出浓度显著增高,最为突出的是TN、TP和有机污染物。在垂直于太湖段,除NO3--N和NO2--N浓度略微下降外,其他水质指标均呈上升趋势。因此,该湖滨带的缓冲能力不足以净化来自地表和鱼塘的污染物质。在平行于太湖段。除NO3--N和NO2--N浓度逐步增高外,其他水质指标均呈下降趋势,说明包括河流在内的整个湖滨带的缓冲能力较高,净化作用大于湖滨带纳入的污染物质,缓冲效果好。鱼塘排水对水体的影响非常明显,这种影响大概可以持续2周左右。通过对不同时期的采样结果进行显著性分析,发现COD差异性不显著,且含量高,即有机污染物在各时期都是主要污染物。在鱼塘放水时期（已进入冬季）,各指标下的采样点之间均不显著,湖滨带的缓冲作用较低。     

Carrousel氧化沟的三维流场模拟与分析

利用CFD的Fluent软件，采用标准的三维K—ε紊流模型，对桂林市七里店污水处理厂1#氧化沟的流场进行了数值模拟，对导流墙和推进器附近的流速进行了计算分析。结果表明，氧化沟下层流速较低，局部区域流速低于0．2m／s。为了防止污泥沉降，应进一步降低推进器位置。能量损失分析表明，卡罗塞氧化沟能量损失主要来源于沿程摩擦损失和局部损失。可通过增加墙体光滑度、降低入口高度以及增加导流墙的曲率半径等措施减少能量损失，改善现有氧化沟的水力特征。     

响应面法优化聚磷硫酸铁的制备及其应用

采用单因素实验方法,针对制备聚磷硫酸铁(PPFS)的主要影响因素加以分析,包括酸度(nH2SO4/nFe2+、碱化度和nPO34-/nFe2+等。以生活污水中总磷(TP)的去除率为考察对象,采用Box-Behnken中心组合实验和响应面分析方法对主要影响因素加以优化,得到了二次响应曲面模型以及优化的水平值。结果表明,当把PPFS用于生活污水中TP的去除时,其最佳制备参数如下所列:酸度为0.1017,碱化度为12.21%,nPO34-/nFe2+为0.0560。通过回归分析,模型拟合性良好,在优化制备条件下得到的TP去除率预测值与实验值接近,误差为1.26%。     

Production and optimization of biodiesel using mixed immobilized biocatalysts in packed bed reactor

Vegetable oils are used as raw materials for biodiesel production using transesterification reaction. Several methods for the production of biodiesel were developed using chemical (alkali and acidic compounds) and biological catalysts (lipases). Biodiesel production catalyzed by lipases is energy and cost-saving processes and is carried out at normal temperature and pressure. The need for an efficient method for screening larger number of variables has led to the adoption of statistical experimental design. In the present study, packed bed reactor was designed to study with mixed immobilized biocatalysts to have higher productivity under optimum conditions. Contrary to the single-step acyl migration mechanism, a two-step stepwise reaction mechanism involving immobilized Candida rugosa lipase and immobilized Rhizopus oryzae cells was employed for the present work. This method was chosen because enzymatic hydrolysis followed by esterification can tolerate high free fatty acid containing oils. The effects of flow rate and bed height on biodiesel yield were studied using two factors five-level central composite design (CCD) and response surface methodology (RSM). Maximum biodiesel yield of 85 and 81 % was obtained for jatropha oil and karanja oil with the optimum bed height and optimum flow rate of 32.6 cm and 1.35 L/h, and 32.6 cm and 1.36 L/h, respectively.