大蒜油不同加工工艺的比较

通过对大蒜油加工工艺中的几种提取方法的比较，确定大蒜油加工的最佳提取方法为超临界CO2萃取法，其提取压力为20MPa，温度为50℃，萃取时间4h，所得大蒜油质量好、得率高。     

降低异氰酸酯单体含量的技术进展

介绍聚氨酯预聚体中游离异氰酸酯单体的产生及其检测方法,制品施工现场空气中异氰酸酯浓度与产品中游离单体含量的关系,重点介绍分子筛吸收法、薄膜蒸发法、共沸蒸馏法、分子蒸馏法、溶剂萃取法及化学转化法等降低游离异氰酸酯单体的技术途径。     

稀土元素的分离技术

对目前稀土元素分离过程中几种常用的分离技术进行了综述，使用得较多的仍然是溶剂萃取法和离子交换法，而且新方法也在不断地出现。     

Enantioselective extraction of mandelic acid enantiomers based on chiral ligand exchange

Based on the chiral ligand exchange, the distribution behavior of mandelic acid enantiomers, and the partition of Cu^2 at different pH values were studied in a water/alcohol two-phase system containing Cu^2 and N-ndodecyl-L-proline(A). The influences of the solvent sort, the pH value, the concentrations of Cu^2 and chiral ligand on the partition coefficient(K) and separation factor(α) were discussed. The experimental results show that the A formed has more stable ternary complex with D-mandelic acid enantiomer than with L-mandelic acid enantiomer. There is an important influence of the pH value on K and a. When the pH values are less than 3.5, the formation of binary complexes is thermodynamically unfavourable. K and a become maximum when pH values are above 3.5 and the molar ratio of the chiral ligand to Cu^2 is 2:1.     

萃取法制备干酪素

干酪素是一种用途极为广泛的精细化工产品，用萃取法生产工业干酪素，其产品质量优于机械分离法，对生产特级品工业干酪素有一定推动作用。     

富集纯化三七皂甙Rb_3方法的研究

研究了丙酮直接结晶法,正丁醇萃取法,HPD-100型药用大孔吸附树脂对三七皂甙Rb3的精制作用,并对它们的效果及可行性进行比较,主要从上样量,纯化效果进行优化,确定了用大孔吸附树脂是工业上的最佳条件。     

溶剂萃取法回收与处理含DMAc废水的研究

本文研究了用低沸点萃取剂处理和回收含二甲基乙酰胺（DMAc)废水的可行性及工艺条件，经研究表明，在常温20－35℃时，用氯仿萃取二甲基乙酰胺，当溶剂与水相体积比为2：1时，经六级逆流萃取，可将废水中20％（w/w)的二甲基乙酰胺含量降至300mg/L以下。废水的pH值对萃取效率有明显的影响，当废水的pH值较大，即偏碱性对萃取有利。     

从钛白的副产品生产硫酸钾肥的新工艺研究

通过对钛白生产中的副产品硫酸亚铁的综合利用进行深入研究，提出了萃取法生产硫酸钾的新工艺，分别对萃取铁离子和萃取氯离子的体系进行了系统研究。优化了工艺流程，通过对工业副产品硫酸亚铁的综合利用，可获得较大的经济效益和社会效益。     

手性化合物合成与拆分技术进展

目前，手性物质的生产除了直接进行不对称合成与发酵之外，主要是通过化学合成DL-型外消旋体物质，然后通过各种拆分方法得到所需要的具有光学活性的对映体。当前用于手性化合物拆分的方法主要有结晶法、外消旋拆分法、萃取法等，电合成作为合成手性化合物的方法则一支独秀。     

水性氯化物介质中对甲基苯烷基硫醚萃取钯的研究

p-Methylphenylalkylsulfide of various alkyl chain length as extractant were synthesized and the extraction of palladium was examined in terms of equilibrium and kinetics. Distribution ratio of Pd was independent of alkyl chain length. For aqueous chloride media, there was a significant difference in distribution ratios for the solution of NaC1 and HC1. The results of loading test and the slope analysis suggest that the extractant and Pd (Ⅱ) form 2:1 complex. Furthermore, the extraction rate based on the volume of aqueous phase was obtained in a stirred vessel, and the rate equation was presented. Unfortunately, it was difficult to construct surfactant liquid membrane system by use of the present extractant.