废旧油泵的改进与利用

将废旧油泵改装，制成循环水泵，并用于几种不同沸点化合物的减压蒸馏，对所获实验数据进行分析，结果表明该改制泵真空度高，抽气量大，简便，经济和耐用。     

Combined steam pretreatment and enzymatic hydrolysis of starch-free wheat fibers

Steam treatment of an industrial process stream, denoted starch-free wheat fiber, was investigated to improve the formation of monomeric sugars in subsequent enzymatic hydrolysis for further bioconversion into ethanol. The solid fraction in the process stream, derived from a combined starch and ethanol factory, was rich in arabinose (21.1%), xylose (30.1%), and glucose (18.6%), in the form of polysaccharides. Various conditions of steam pretreatment (170–220°C for 5–30 min) were evaluated, and their effect was assessed by enzymatic hydrolysis with 2 g of Celluclast + Ultraflo mixture/ 100 g of starch-free fiber (SFF) slurry at 5% dry matter (DM). The highest overall sugar yield for the combined steam pretreatment and enzymatic hydrolysis, 52g/100 g of DM of SFF, corresponding to 74% of the theoretical, was achieved with pretreatment at 190°C for 10 min followed by enzymatic hydrolysis.     

高丰度硼-10制备过程中的液相络合剂

高丰度硼-10主要是通过精馏与化学交换法进行制备，在交换反应过程中，液相络合剂的研究非常重要．为此以苯甲醚、硝基甲烷、丙酮、甲基异丁基酮作为络合刑进行了系统的实验研究．设计了合成络合物体系的实验反应器，并用这些络合荆分别与三氟化硼合成了4种络合物体系．对这4种络合物体系的密度、凝固点、BF3／络舍剂比率以及蒸气压等性能进行了实验研究，并拟合了蒸气压随温度变化的曲线，通过分析认为苯甲醚更适宜于应用在硼同位素的分离过程中，能减少能耗，降低成本．     

UHG-311-G型双冲量连续式水位控制器工作原理及应用

在工业锅炉生产工艺流程的基础上,介绍了UHG-311-G型双冲量连续式水位控制器在工业蒸汽锅炉控制系统中的工作原理,并对命名用时应注意的问题进行了提示.     

蒸馏中两组分溶液的气液相平衡分析

借助数学方法,结合相律中自由度数的分析,用拉乌尔(Raoult)定律、安托尼(Antoine)方程表述两组分均相混合溶液的温度与气相组成、温度与液相组成以及气相组成与液相组成的相平衡关系.综合相图、相律及相平衡关系,分析精溜操作中的状态参数,使抽象的相平衡内容具体、直观.     

精馏、吸收严格计算中焓的计算方法

总结了适合于精馏、吸收严格计算的焓的计算方法，并对各种条件下的精馏、吸收计算，推荐了焓的计算方法。     

白苏毒性的初步研究

进行白苏挥发油提取及该提取物对大白鼠的中毒试验,研究白苏的毒性机理。结果表明:白苏的主要药理成分—挥发油,在一定的浓度下可以致毒,主要是使动物神经系统致毒,严重中毒者可致死亡。同时初步讨论了白苏的致毒机理。     

Improved catalytic performance of Ni catalysts for steam methane reforming in a micro-channel reactor

Milliseconds process to produce hydrogen by steam methane reforming （SMR） reaction, based on Ni catalyst rather than noble catalyst such as Pd, Rh or Ru, in micro-channel reactors has been paid more and more attentions in recent years. This work aimed to further improve the catalytic performance of nickel-based catalyst by the introduction of additives, i.e., MgO and FeO, prepared by impregnation method on the micro-channels made of metal-ceramic complex substrate. The prepared catalysts were tested in the same micro-channel reactor by switching the catalyst plates. The results showed that among the tested catalysts Ni-Mg catalyst had the highest activity, especially under harsh conditions, i.e., at high space velocity and/or low reaction temperature. Moreover, the catalyst activity and selectivity were stable during the 12 h on stream test even when the ratio of steam to carbon （SIC） was as low as 1.0. The addition of MgO promoted the active Ni species to have a good dispersion on the substrate, leading to a better catalytic performance for SMR reaction.     

Kinetic behaviour of commercial catalysts for methane reforming in ethanol steam reforming process

Ethanol steam reforming has been studied in a fluidized bed （in order to ensure bed isothermicity） on commercial catalysts for methane reforming. The results allow analyzing the effect of temperature （in 300-700℃ range）, and both metal and support nature on the reaction indices （ethanol conversion, yields and selectivities to H2 and byproducts （CO2, CO, CH4 and C2H4O））. Special attention has been paid to catalysts＇ stability by comparing the evolution of the reaction indices with time on stream at 500°C （minimum CO formation） and 700℃ （minimum deactivation by coke deposition）. Although they provide a slightly lower H2 yield, the results evidence a good behaviour of Ni based catalysts, indicating that they are an interesting alternative of more expensive Rh based ones.     

Practical Methylation Procedure for (1H)‐1,2,4‐Triazole

Conversion of (1H)‐1,2,4‐triazole to its sodium salt with methanolic sodium methoxide is followed by reaction with iodomethane. A scalable approach that overcomes problems associated with water‐soluble starting material and water‐soluble product combined continuous extraction (chloroform/water) with a final short‐path distillation under a controlled vacuum to obtain spectroscopically pure 1‐methyl‐1,2,4‐triazole in 63% yield. Adaptation to microwave synthesis conditions, while providing a faster reaction time, offers no product yield or purification advantages over the conventional approach described. Conversions of this product to related derivatives such as 1,4‐dimethyl‐1,2,4‐triazolium iodide and 1‐methyl‐1,2,4‐triazolium hydrochloride are readily achieved.