胜利煤液化油煤浆表观黏度的影响因素研究

采用高温黏度计测定了胜利褐煤液化油煤浆在常压加热条件下的表观黏度,考察了煤浆质量分数、煤粉粒径、溶剂性质以及温度、剪切时间、剪切速率、溶胀等因素对煤浆体系表观黏度的影响。在常压室温至350℃的范围内,比较了胜利煤在起始溶剂和循环溶剂两种煤浆体系中的表观黏度。研究结果表明,胜利液化油煤浆体系是一种非牛顿流体,随着温度的升高,煤浆体系的黏度呈现先快速下降,然后基本保持不变,最后又逐渐上升的趋势。煤浆黏度保持不变的温度区间和黏度开始出现增加的温度随着煤浆的质量分数、煤粉的粒径以及配制煤浆所用溶剂的不同而不同。     

污泥干燥预处理后与神府煤共成浆性的研究

以萘系阴离子表面活性剂为分散剂,考查了污泥干燥条件和粒径对神府煤成浆性的影响。结果表明,将污泥干燥后再制浆,明显提高了污泥煤浆的成浆浓度;升高干燥温度,有利于提高污泥煤浆的成浆浓度。干燥温度对污泥的可磨性影响较大。干燥温度越高,干燥污泥可磨性越好,球磨的污泥平均粒径越小,制得的污泥煤浆表观黏度越低;温度高于105℃,污泥的可磨性无明显差别,污泥煤浆的表观黏度亦无明显变化。污泥粒径越小,颗粒越细,一定程度上提高了煤粉的堆积效率,使污泥煤浆的表观黏度降低。     

煤沥青水浆的制备及影响规律的研究

以中温煤沥青为原料,经冷冻粉碎后制得具有一定粒径级配的煤沥青粉,加入适量分散剂和水在高速搅拌下制备煤沥青水浆.结果表明,JL-C01中裂乳化剂是制备煤沥青水浆的优良分散剂,在此基础上进一步考察了分散剂用量及浆体浓度对煤沥青成浆性、煤沥青水浆流变性及稳定性的影响.结果表明,最大成浆浓度为70％;在分散剂用量相同的条件下,...     

褐煤水热提质改善水煤浆的成浆性、流变性和稳定性的实验研究

采用水热法对小龙潭褐煤进行提质处理,从煤质特性、含氧基团、表面亲水性和粒度分布等因素,探究了水热提质对褐煤水煤浆成浆浓度、流变特性以及稳定性的影响。结果表明,水热提质脱除了褐煤中的水分,氧含量降低,煤阶升高。水热提质脱除了褐煤中含氧基团,煤水表面接触角增大,褐煤表面亲水性得到改善。小龙潭褐煤颗粒粒度呈现双峰分布,水热提质后褐煤颗粒粒径减小且趋于规则。水热提质改善了水煤浆的成浆性能,成浆浓度由提质前的44.09%,最高可提升到61.94%。在相近的表观黏度下,水热提质后水煤浆的稠度系数K减小,流变指数n增大,水热提质在降低浆体黏度的同时,仍保持假塑性流体特征。水热提质降低水煤浆的析水率,延缓了浆体出现硬沉淀的时间,改善浆体的稳定性。水热提质从理化特性对褐煤进行深度改性,从而获得高浓度,假塑性以及稳定性良好的符合工业应用的水煤浆。     

蓝藻与神府煤共成浆性的研究

考察了预处理方法对含水蓝藻表观黏度的影响,以及蓝藻对神府煤浆成浆浓度、流变性和静态稳定性的影响。结果表明,采用添加化学药剂、高速搅拌、加热等方法对含水蓝藻进行预处理,可以使表观黏度从72mPa·s降低到21.8mPa·s(剪切速率100s^-1)。蓝藻结构受到破坏是表观黏度降低的主要原因。含水蓝藻表观黏度的降低有利于蓝藻煤浆成浆浓度的提高。当添加水质量与含水蓝藻质量比为1∶1时,蓝藻煤浆的成浆浓度达到60%。蓝藻的加入提高了神府煤浆的稳定性,使稳定性从4h提高到72h以上。蓝藻煤浆为假塑性流体,剪切变稀。     

基于钾基修饰铁矿石载氧体的煤化学链燃烧循环实验

对天然的铁矿石加以钾基修饰,在流化床上进行了煤化学链燃烧循环实验。研究了改性后的铁矿石对气体产物浓度及含碳气体体积分数影响的持续力。钾基铁矿石缩短了反应时间并明显提高了CO₂浓度;在20次循环中,钾基铁矿石能明显提高CO₂体积分数并降低CO体积分数,11次循环后,CO₂体积分数稍有减少,CO体积分数略有增加。借助于扫描电镜与电子能谱(SEM-EDX)和X射线衍射(XRD),对不同循环后的载氧体进行表征。与纯铁矿石相比,前10次循环钾基铁矿石载氧体表面严重烧结,20次循环之后烧结减轻,恢复多孔结构。结果表明,钾基铁矿石载氧体中KFe₁₁O₁₇或其衍生物对煤气化有催化作用;在20次循环中存在钾流失现象;20次循环后钾基铁矿石载氧体能完全氧化为Fe₂O₃。     

褐煤中水分对油煤浆流变性质的影响

针对云南褐煤,用真空干燥脱水和恒温恒湿箱处理获得了不同含水率的褐煤,在常温常压(t=19.3℃,p=1.01×105Pa)条件下研究了褐煤含水率对油煤浆流变特性的影响。研究表明,原料煤含水率对油煤浆黏度和流变特性有一定的影响。随褐煤含水率增加,油煤浆黏度先减小后增加。油煤浆浓度不同,剪切速率不同,黏度出现最低值的含水率值wmin也不同。浓度为45.45%的油煤浆,剪切速率小于4.4 s-1时,wmin为9.20%;剪切速率大于4.4 s-1时,wmin为7.80%。浓度为55.56%的油煤浆,剪切速率小于1.32 s-1时,wmin为7.40%;剪切速率大于1.32 s-1时,wmin为10.00%。随剪切速率变化,油煤浆黏度上下行曲线之间形成滞后环,表明油煤浆体系有触变性,并且不同含水率煤浆体系触变性不同,含水率越大,触变性越明显。实验中不同含水率褐煤油煤浆都属于假塑性流体,且含水率对模型参数有一定的影响。     

煤直接液化残渣制备水渣浆成浆性的研究

以煤直接液化残渣制备了水渣浆，考察了粒径分布、搅拌时间、分散剂的用量及种类对水渣浆性质的影响。根据实验确定了制备水渣浆的最佳工艺参数：Alfred粒径分布模型（d_280~154μm、d_154~74μm、d_<74μm 质量分数分别为14%、16%、70%），搅拌时间20 min，分散剂加入量为干渣基1.0%。实验结果表明，液化残渣制备水渣浆的定黏质量分数分别为73.5%（NSF）和71.0%（SL）。分散剂萘磺酸盐甲醛缩合物（NSF）的分散降黏效果优于改性碱木质素磺酸钠（SL），而水渣浆的流变性，分散剂SL要优于分散剂NSF。     

分散剂表面吸附特性和相关电化学性质对煤浆分散体系流变特性的影响

采用１７种不同变质程度的中国煤，详细研究了一种阴离子型分散剂在煤表面的吸附特性及其相关的表面电化学性质对煤成浆性及浆体流变特性的影响。结果表明，煤成浆性及浆体流变性并不单独取决于煤对分散剂的吸附量和煤表面动电位的大小。反映煤成浆性的浆体最高煤浆浓度取决于分散剂在煤表面的Ｌａｎｇｍｕｉｒ饱和吸附量Γｓ和相应动电位ξｓ的乘积Γｓ×ξｓ，而浆体流变指数则依赖于两者比值的大小Γｓ／ξｓ。表明水煤浆分散体系中煤颗粒的分散一方面是靠静电分散作用来实现，另一方面，分散剂在煤表面的吸附所产生的非静电分散作用也起了重要作用。同时，分散剂的表面吸附使煤表面产生的吸附荷电效应不能过高，否则，会对流体流变性不利。     

煤浆电解制氢的动力学研究

研究了煤浆电解过程中电压、温度、H₂SO₄浓度、Fe³⁺浓度等因素的影响,并进行了电解前后煤粉样品的热重测试和电解后溶液的成分分析。结果表明,电压、温度、添加的Fe³⁺浓度、H₂SO₄浓度等参数对电解过程的电流密度有较大影响。其中,温度对电流密度的影响符合阿伦尼乌斯方程,在电解电压1 V条件下煤浆电解活化能为31.87 kJ/mol。TGA和ICP分析表明,电解后煤中的部分金属离子溶入溶液,导致结构和灰分成分发生了较显著的变化。     

Modelling of The Rheological Properties of Bimodal Emulsions

The model of Ouchiyama and Tanaka 1 - 3 was successfully adapted to calculate the maximum packing fraction (ϕ_m) of polymer latexes with varying bimodal particle size distributions based upon rheological measurements performed on its constituent parts. The values of ϕ_m calculated from the model can be used to predict the rheological properties of the latices. The model was experimentally validated and used for the prediction the viscosity of studied bimodal latices of known concentration using the master curve of viscosity-reduced volume fraction (η vs. ϕ/ϕ_m).     

超声波强化水煤浆制备方法的研究

本文研究用超声波技术强化高浓度水煤浆的制备方法，选择适当的处理条件和设备，经超声波处理的水煤浆，煤粉级配明显向细的方向转化，不仅表观粘度大幅度降低，而且浆体静态稳定性和流变特性也得以显著改善。     

Flow properties of freshly prepared ettringite suspensions in water at 25 degrees C

The rheology of a complex, heterogeneous mineral colloid was rationalised using models devised for model rod systems. Mixing a calcium hydroxide slurry with an aluminium sulphate solution produces a suspension of rod-shaped ettringite particles. Ettringite rod suspensions exhibit non-Newtonian flow behaviour, which depends on the shape of the particles, their size distribution, concentration and surface properties as well as the suspension medium characteristics. We have measured the shear viscosity of suspensions of ettringite rods with a median aspect ratio, r(i) approximately 8, at 25 degrees C as a function of particle volume fraction, phi, in the range 0.0001-0.08. It was found that the viscosity of the suspensions increased with phi, and showed a marked change of slope at phi approximately 0.01, which we identified as the minimum overlap concentration phi(*). Above phi(*), the system is in the semi-dilute regime. At phi>phi(*), when Pe(rot)>1, hydrodynamic interactions between rods become increasingly significant, and we observe shear-thinning behaviour. The high effective hydrodynamic volume of rotating rods, resulting in much lower values of the maximum packing fraction, phi(c), than for spheres, dominates the rheological behaviour of ettringite suspensions.     

Rheology of concentrated multi-sized poly(St/BA/MMA) latices

 Four monodisperse latices with particle size of 75, 135, 340 and 477 nm were synthesized. The rheo-logical properties of mixture of the monodisperse latices were inves-tigated as a function of blending ratio, and compared with those of multi-modal latices, in a range of shear rate from 0.2 to 100 s^-1. The maximum packing (highest solid contents) was observed at a weight fraction 80% of large particles with respect to total solids contents for both bimodal and trimodal latices, and the lowest viscosity was obtained when the ratio of large to medium to small particles was approximately 80/10/10 (by wt.). It was also demonstrated that this minimum in the viscosity is not strongly dependent on the actual size of each kind of particles present in the multimodal latices. Received: 22 November 1996 Accepted: 26 November 1997     

Role of Electrostatic Repulsion on the Viscosity of Bidisperse Silica Suspensions

The flow behavior of bidisperse aqueous silica suspensions has been studied at different electrolyte concentrations as a function of shear rate, total volume fraction of the particles, and volume ratio of small to large particles. It is shown that the range of the electrostatic repulsion plays an important role in determining the viscosity of the suspension. Binary mixtures of particles of longer range repulsive forces showed higher viscosities than the suspensions of shorter range electrostatic interactions. Bimodal suspensions of long-range interactions showed non-Newtonian behavior over wider ranges of shear due to the deformation of the ionic cloud around the particles, which is larger in these systems. The viscosity of bimodal suspensions used in this study was scaled with respect to the viscosity of the related monosized systems and the viscosity of one bimodal suspension at a fixed total volume fraction of the particles, employing our earlier scaling method. The model normalizes the effect of colloidal forces by introducing a scaling factor that collapses the data into a single curve for bimodal suspensions of a particular size ratio, and it is shown that the model is valid for systems with both short-range and long-range repulsive forces. Copyright 1999 Academic Press.