厚壳玻璃钢艇体选材、铺层设计及工艺

本文涉及玻璃钢猎扫雷艇艇体材料的优选、铺层设计和工艺等内容。试验确定了以１６２９间苯聚酯树脂为基体、以９００ｇ／ｍ２无碱无捻粗纱短切毡（Ｍ）和８１０ｇ／ｍ２无碱无捻粗纱方格布（Ｒ）为增强体以及（Ｍ＋Ｒ）为基本铺层设计单元的方案。试验表明，按上述材料和铺层制作的层板，性能达到Ｌｅｒｉｃｉ和ＭＨＣ－５１艇壳层板的指标要求。     

泡沫铝的动态压缩性能和吸能性研究

通过测量泡沫铝在动态和准静态压缩条件下的应力 -应变曲线 ,研究了泡沫铝的准静态和动态压缩行为以及不同应变条件下的吸能性 ,并对其应变率效应进行了分析。结果表明 ,在高应变速率和准静态压缩下 ,泡沫铝的σ -ε曲线均表现出弹性变形段、平缓段和密实段三阶段特征 ;泡沫铝的压缩性能具有明显的应变速率敏感性 ,随应变速率的提高 ,流动应力上升 ,吸能性升高     

前景璀璨的新型生物降解塑料-聚乳酸

简要介绍了聚乳酸的一般合成方法、性质、应用，着重介绍聚乳酸在医药和医疗领域中的应用和世界范围内的市场发展概况。     

THE LAURENCE BISHOP SILVER MEDAL INAUGURAL LECTURE THE IMPACT OF SCIENTIFIC MEASUREMENT ON THE BREWING PROCESS

Laurence Bishop's contribution to the brewing industry over more than 50 years of research endeavour and committee activities is reviewed. Three research areas — prediction of extract, the effect of turbidity on yeast activity during fermentation and the development of a 3-vessel fermentation system — are used to highlight his achievements. Five topics with which the author was intimately involved, three of which were connected with Laurence Bishop's own researches, are used to describe the author's activities. These concerned the assessment of beer foam, the prediction of beer stability, the assessment of the bittering value of hops, time course changes in the analytical characteristic of an ale fermentation and the use of fractional factorial designs to facilitate experimental programmes.     

Rapid analysis of polymer homologues and additives with SFE/SFC-MS coupling

A rapid and easy analysis method for polymers is presented. The method involves sample preparation by SFE, separation of the extracted compounds by SFC and simultaneous quantitative detection by FID, as well as identification of unknowns by MS. The applications illustrate how structural research work and routine polymer analysis can be done with this time saving method.     

聚苯乙烯泡沫塑料板在三清干渠改建工程中的试验

高台县友联灌区三清干渠地处严寒地区，且渠道沿线地质条件较差，影响渠道衬砌改建质量的关键技术问题是防冻胀设计。由于三清干渠附近缺乏垫层料，采用垫层置换防冻胀投资高，且垫层质量难以控制。设计人员根据有关规范要求．结合渠线地质条件．采用聚苯乙烯泡沫塑料保温板进行防冻胀试验，较好地解决了冻胀问题。     

我国塑料机械工业概况与发展

介绍了我国2001年塑料机械工业的生产状况，通过大量翔实的数据对我国注射机、挤出机和吹塑机三大产品的生产技术、经济技术指标及进出口市场状况进行了分析。     

水工钢闸门聚酯玻璃钢复合防腐处理方法

水环境的恶化，使水工钢闸门腐蚀加重，传统的防腐工艺保护效果下降。聚酯玻璃钢复合防腐层的水工钢闸门防腐工艺具有使用设备少，工艺简单、防腐效果好、成本低等优点，适用于在各种水环境中作各种形式的水工钢闸门防腐，效果良好。该文结合江苏省淮海农场工程施工经验，提出了水工钢闸门聚酯玻璃钢复合防腐层结构设计、施工工艺及质量标难，为今后的推广应用提供了一定的参考依据。     

多层复合膜的成型技术

阐述了用AutoLisp程序模拟塑料熔体在2层复合膜机头内的流动情况，并介绍了复合膜机头的内部结构。     

Prediction of foam growth and its nucleation in free and limited expansion

The influence volume approach (IVA) is often utilized for modeling the mass transfer process dictating bubble growth dynamics in physical foaming. However, the assumed concentration profile in the IVA method is only valid when the changes in dissolved gas concentration are small (less than 5%). In addition, the validity of the IVA method is difficult to justify in chemical foaming applications because of the difficulties involved in defining the dissolved gas concentration profile.In the present work, we define two distinct stages of bubble growth for physical foaming. These two stages are termed as free and limited expansion and are controlled by the bubble nucleation rate. Bubble nucleation is assumed to occur only in the free expansion stage. In this stage, the bubble pressure drops substantially from an initially high pressure in the supersaturated state while the dissolved gas concentration changes very little. The second stage of our two-stage mass transfer model is termed the limited expansion stage and accounts for bubble growth in the late stages of foam evolution, when the pressure changes become small. However, in the limited stage of bubble growth the dissolved gas concentration drops significantly, as the available dissolved gas is depleted. To summarize our two-stage mass transfer model of foam expansion, the pressure difference between the bubble phase and the liquid phase is the primary mechanism for driving mass transfer in the early (free) stages of foam growth and the concentration difference is the driver for bubble growth in the late (limited) stages of growth. The first stage can be regarded as the nucleation stage and it is relatively short; while the second stage can be regarded as the bubble growth stage and is much longer. Most of the bubble volume expansion takes place in the second stage.The concentration gradient at the bubble edge, which is often ignored in other models, is analyzed in detail in this paper. The details of our novel mass transfer model are also presented.