喷雾干燥的节能分析

喷雾干燥是能耗较大的单元操作,节能工作十分重要。对喷雾干燥过程中的热量分配作了计算分析,并根据作者对喷雾干燥过程的研究及编制的程序对各种操作因素对干燥过程能耗的影响进行了分析评价,给出了干燥过程的节能措施。     

超长、超大基坑开挖对邻近地铁结构安全影响的数值模拟分析

为了研究超长、超大基坑开挖对邻近地铁结构安全影响,以西安地铁2号线周边某基坑为工程实例,通过运用数值分析软件,结合场地的水文地质和工程地质条件,建立数值模型,进行施工过程的动态模拟,同时进行现场监测,经对比数值模拟结果及监测数据,表明运用PLAXIS软件能有效的模拟基坑开挖过程中的土体变形。同时工程采用的分段、分块开挖,中心岛顺做,周边预留土台反压、使用旋喷锚索的支护方案,对复杂条件下基坑开挖对邻近地铁结构的变形影响能起到有效的控制作用,可对类似工程的设计优化提供有益的参考及借鉴。     

环氧酯底漆的研制

介绍了用环氧树脂、脂肪酸、干性油、季戊四醇、邻苯二甲酸酐制成的气干型环氧酯底漆。讨论了各种因素对树脂、涂料性能的影响。     

大冶硫酸四系列干吸塔结构特点

以干燥塔为例，介绍大冶公司硫酸四系列干吸塔的结构特点。除捕沫层简体及出气管为316L不锈钢外，其余塔体均为碳钢内衬瓷砖结构。塔底为球形底，中心排酸。采用槽管式分酸器，分酸点密度为43个/m^2，设可调闸板以保证各槽酸量均匀；闸板外设置带孔板的分布板，以消除进口酸的冲击，保证槽内酸液面平稳。比较了该塔与常规塔的不同之处，强调了设备节点的优化设计。     

Ultrasonic Spray Pyrolysis for Synthesis of Spherical Zirconia Particles

This paper presents new findings on ultrasonic spray pyrolysis of zirconium hydroxyl acetate precursor drops whose sizes were precisely measured using laser light diffraction technique. Precursor concentration plays a predominant role in determination of product particle size. At 0.01 wt% precursor concentration, conventional spray pyrolysis at 750°C using precursor drops 5–8 μm in diameter, generated by an ultrasonic nebulizer at 2.66 MHz, yielded uniform spherical yttria-stabilized zirconia (YSZ) particles 73 nm in diameter measured by scanning electron microscopy. The YSZ particle diameters were much smaller than those predicted by the one-particle-per-drop mechanism. Under similar reaction conditions, the high-throughput ultrasound-modulated two-fluid (UMTF) spray pyrolysis of larger precursor drops (28-μm peak diameter) also yielded spherical dense particles; they were significantly smaller in size than those produced by the low-throughput conventional ultrasonic spray pyrolysis of smaller drops (6.8-μm peak diameter).     

工业喷漆的环境污染研究

化工企业对环境的影响较大,其制造的化工产品严重威胁着人们的健康。近年来,随着化工企业的规模越来越大,其带来的环境污染问题也越来越严峻。就工业喷漆对环境污染的状况和治理措施进行了分析、探究。     

An Experimental Investigation of Lime Juice Drying in a Pilot Plant Spray Dryer

One of the major problems in spray drying of fruit juices such as lime juice is stickiness and thermoplasticity of their compositions. Lime juice consists of invert sugars and citric acid, which have low glass transition temperatures. Due to this characteristic, the particles stick on the dryer wall upon their collision with it. As a result, drying of these materials is very difficult. In order to solve this problem, various percent of silicon dioxide and maltodextrin (DE5), based on total soluble solid content of lime juice, have been used to reach a suitable drying condition. A cool chamber wall spray dryer was used in this investigation in order to decrease the probability of particles stickiness on the wall. Our investigation revealed that an addition of 10% silicon dioxide and 20% maltodextrin (DE5) to lime juice is the optimum amount for a complete and successful drying of lime juice. Sampling of particles from different longitudinal distances in the dryer tower is carried out to find the particle moisture contents as they fly downward in the dryer. The results show a very fast decrease in entrance moisture contents. Based on our experimental data, the variation of moisture contents are presented as a function of radial distance from central line and longitudinal distance from the entrance region.     

提高氯气干燥效果的措施

阐述了在隔膜法烧碱生产过程中，因氯气含水多、干燥塔板积液和塔板上无泡沫层等造成氯气干燥效果不好导致酸流量调节困难，并影响设备使用寿命的问题。提出了具体有效的整改措施。     

Drying-induced stresses in elastic and viscoelastic saturated materials

The paper presents a theoretical analysis of stresses generated during convective drying of kaolin, based on elastic and viscoelastic models. The equations of these models were solved analytically for a cylindrically shaped sample; the distribution and evolution of the radial and circumferential stresses are illustrated in diagrams. The acoustic emission method was used in experimental tests for identification on line of the time period during which the stresses reach their maximal values. A better correlation has been found between the experimental tests and the theoretical predictions obtained on the basis of the viscoelastic model.     

Fluidized Bed Air Drying: Experimental Study and Model Development

The presented study describes the processes and mechanisms of batch fluidized bed drying. The influencing factors of hot air drying are theoretically and experimentally examined, in order to present the relations between temperature and humidity profiles and all other drying parameters. A physical model is presented to facilitate the calculation of the drying processes under defined conditions. Three succeeding drying stages are therefore modeled. Mass and energy balances including all components taking part in the process are formulated. The model clarities the drying process under the assumption of pure heat transfer mechanisms. It does not contain adaptive parameters and takes into account an inactive bypass fraction of the fluidization and drying medium. The evaluation of the model was successful for two fluidized bed plants with nominal widths of 100 mm and 400 mm. The experiments showed sufficient accuracy and transferability of the model to equipment of application‐oriented dimensions.