Electrochemical pre-treatment of effluents containing chlorinated compounds using an adsorbent

Electrochemical pre-treatment of industrial wastewater to remove refractory and/or toxic organic components, making them more amenable to biological treatment, is likely to be more cost-effective than using a physical or chemical process for complete organic removal. This paper demonstrates the use of a carbon-based adsorbent material that preferentially removes chlorinated organic compounds. Electrochemical regeneration of the adsorbent is shown to be a quick, easy and cheap process, because the adsorbent is both highly electrically conducting and non-porous. High regeneration rates over a number of cycles were obtained by passing a charge of 25 C g⁻¹ through a bed of adsorbent particles, at a current density of 20 mA cm⁻² for 10 min. The energy required to remove a kg of COD from an industrial wastewater was calculated to be 27 kWh.     

磁性活性炭的一种制备方法

将磁化剂吸附于活性炭上 ,于室温下干燥即可得到磁性活性炭。这种活性炭用于黄金生产 ,可使提金得率提高 4 %。     

活性炭对含铬废水的吸附处理研究

研究了活性炭吸附处理实验室模拟含铬废水。实验结果表明,当活性炭用量为1 g,废水pH=4~5,吸附接触时间大于1 h,活性炭与铬含量比值大于5 mg Cr6+/g活性炭时,处理效果可达99%以上;吸附符合Freund lich等温模式,吸附等温方程式为logq=0.7780+0.9716 logc,以物理吸附为主;吸附穿透体积为25 mL,活性炭吸附Cr6+的工作吸附容量为14.59 mg Cr6+/g活性炭,工作饱和吸附容量为803.41 mg Cr6+/g活性炭。     

杂多酸化学吸收从天然气中脱除H_2S回收硫磺的研究

研究开发了利用杂多酸脱除天然气中H2S并回收硫磺的新工艺实验结果表明，H2S的脱除效率与溶液酸度、杂多酸浓度、H2S浓度以及吸收温度、停留时间均有关系．吸收的最佳酸度为0.1kmol／m3H2SO4，此时H2S的去除率可达99％以上．通过对比纯硫磺和H2S转化物的热重分析和微分差热分析图谱，确证了在吸收过程中H2S被氧化为硫磺，杂多酸被还原为单电子杂多兰．杂多兰可被Cl2、Fe3+和NO2氧化而再生．     

Langmuir吸附方程的应用

本文总结了Langmuir方程在吸附分离过程中的应用。利用Langmuir方程得到直观表达混合气组分气体间吸附强弱关系及分离的难易程度的x-y图，推导了Lewis关系式。     

交联球形壳聚糖树脂制备方法研究

介绍了壳聚糖－乙酸溶液制备交联球形壳聚糖树脂的方法，考察了各种制备因素对产品性能的影响，得到了较为合适的反应条件。产品溶酸性能、吸附性能有较大提高，并且容易再生。     

变压吸附富氧工艺用于合成氨制气过程的技术经济分析

本文介绍了变压吸附法制备富氧空气用于合成氨造气系统的新工艺，并对５００００ｔ／ａ合成氨厂进行了技术经济评估。结果表明，同间歇法气化相比，该技术工艺先进且具有显著的经济效益。     

烯（醚）醛一步法合成异戊二烯技术开发—基础理论研究进展

本文介绍了烯(醚)醛一步法合成异戊二烯技术开发中,基础理论研究工作的进展,其中包括化学热力学、化学动力学、再生烧炭本征动力学和扩散动力学等理论研究。并针对该反应特征进行了化学反应规律和流动传递规律的研究。建立了流化床反应器数模和流化床再生器数模,为工程技术开发提供理论依据。     

PEN/PTT共混聚酯的熔融行为

利用差示扫描量热仪对不同配比的聚萘二甲酸乙二醇酯/聚对苯二甲酸丙二醇酯(PEN/PTT)共混体系的熔融行为进行了分析,发现在共混体系中两组分形成各自的晶体,PEN和PTT的熔点均随另一组分含量的增加而下降。根据Nishi-Wang方程,按300℃计算,由PEN/PTT共混体系中PEN熔点下降计算所得到的相互作用能密度为-0．214 2 J/cm~3,相互作用参数为-0．006 8,表明PEN/PTY共混体系在熔融态是热力学性质稳定的相容体系。     

(CO2 + 2‐propanol) mixture as a foaming agent for polystyrene: A simple thermodynamic model for the high pressure VLE‐phase diagrams taking into account the foam vitrification

The equation of state model developed by Lacombe and Sanchez (J Phys Chem 1976, 80, 2352) is used in the form proposed later by Sanchez and Stone (Polymer Blends, Vol. 1: Formulation, 2000; Chapter 2) to correlate experimental vapor‐liquid equilibrium (VLE) data for the three binaries and the ternary systems. Experimental data from the binary systems carbon dioxide‐isopropyl alcohol (CO₂‐IPrOH), isopropyl alcohol‐polystyrene (IPrOH‐PS), and carbon dioxide‐polystyrene (CO₂‐PS) are used to calculate VLE properties for the ternary system CO₂‐IPrOH‐PS. Two‐dimensional VLE‐phase diagrams were calculated and used to describe from a thermodynamic point of view the pressure, volume, and temperature values that characterize a thermoplastic foam evolution process, from the extruder to the foaming die. For different initial mixture CO₂ + IPrOH concentrations, pressure reduction produces liquid foaming until the vitrification curve arrests the final foam volume expansion. The dependence of the vitreous transition with the system CO₂ + IPrOH concentration while foaming is represented by the Chow (Macromolecules 1980, 13, 362) equation. The calculation procedure is proposed as a design tool to reduce the amount of experimental data usually needed as a requirement previous to the design stage. © 2007 Wiley Periodicals, Inc. J Appl Polym Sci 104: 2663–2671, 2007