墩头超长实用堰泄洪安全分析及模型试验验证——以缅甸DAPEIN(Ⅰ)水电站工程为例

以缅甸DAPEIN(Ⅰ)水电站工程为例,论述了将WES实用堰的闸墩墩头向上游超长延伸之后,对泄洪安全所造成的影响。针对WES实用堰流量系数、堰面动水压力容易受边界因子影响的特点,对设计断面的堰顶布置和墩头形状进行了优化。根据堰面空化数计算公式及水流特性推导出计算的关键部位,对空化数进行计算。采用几何比尺为1∶60的物理模型对溢流堰的泄流能力和堰面动水压力进行了试验测试。试验结果表明:溢流堰的模型试验泄流能力和设计泄流能力非常相近。堰面动水压力除工况2的B4测点出现了-1.2 k Pa的微小负压值外,其余堰面时均压强值均大于0。从而,在泄流能力和堰面动水压力两方面都验证了这种设计方案的合理性。该工程所遇到的结构布置问题在中低溢流坝工程中属常见问题,解决思路可为今后类似工程建设借鉴参考。     

高黏度头孢菌素C发酵液的超滤研究

利用新型的板式超滤系统对高黏度头孢菌素C发酵液进行了澄清实验研究,通过实验数据与现有系统的运行数据对比,该系统基本解决了目前国内头孢菌素C发酵液超滤提纯中存在的主要过滤问题.     

国内外苯酚的供需现状及发展前景

目前,全球苯酚的总生产能力约为926万ta/,2004年总消费量为774.5万t,预计到2009年总消费量将达到约945.2万t。2005年我国苯酚的总生产能力约为54.0万ta/,产量为44.3万t,消费量约为73.3万t。预计到2007年和2010年我国苯酚的总生产能力将分别达到约85万ta/和110万ta/,消费量将分别达到约85.0万t和96.0万t。针对目前存在的问题,提出了我国苯酚今后的发展建议。     

大容量矿热炉用电极糊的研制

大容量矿热炉用电极糊，采用电煅无烟煤为主要原料，加入一部分石墨碎，选用合适的配方，其理化指标高，使用效果好．     

我国化肥催化剂工业现状

全国48家化肥催化剂制造厂总能力为57Kt/a,产量近30kt/a,设备利用率不到50%。平均万吨氨耗催化剂10.36t,高于国外5.60t水平。现生产31个品种203个型号的催化剂中有103种经部级鉴定,但经常使用的约50种。目前化肥催化剂工业水平与国外相比还存在四方面差距。     

我国合成树脂的展望

综述了我国“八五”期间合成树脂LDPE、LLDPE、HDPE、PP、PS、ABS以及工程塑料PA、POM、PC、PET、PBT、PTFE、PSF、PPO、MPPO、PPS的发展情况,并介绍了新建合成树脂装置及其生产能力。     

Ethanol production from raw starch by a recombinant yeast having saccharification and fermentation activities

In order to develop a method for converting raw starch into ethanol efficiently, direct fermentation of ozonized raw starch using a recombinant yeast was investigated. Ozonolysis was carried out as a pretreatment to convert raw starch into ethanol rapidly and efficiently, and then the effect of the ozone degradation conditions on the degree of polymerization and the amount of amylose in a raw starch was determined. Since the degree of polymerization was low and the amount of amylose was high, raw starch treated with an ozone concentration of 40 gm^?3 and an ozonation time of 30 min was the material chosen for alcohol fermentation. Though the recombinant yeast could not convert the untreated raw starch, it converted the soluble starch and the ozonized raw starch at a comparatively high yield into ethanol. About 56% of the ozonized raw starch decomposed, and the ethanol concentration obtained from the ozonized raw starch was markedly greater than that obtained from untreated raw starch. The dynamic behavior of cell growth, substrate degradation, and ethanol production was examined in a continuous culture under various dilution rates, and the optimal dilution rate, ie 0.15 h^?1, was determined for maximizing the ethanol productivity (amount of ethanol produced per unit time). © 2002 Society of Chemical Industry     

航空胶片显影液调整的计算机处理方法

为解决航空胶片显影液调整问题，采用了Visual Basic6.0开发了“显影液化学分析调整软件，该系统具有一定的应用价值。     

静压桩终压力及单桩竖向承载力的相关性

以苏南软土地区的静压桩施工实测资料为依据,着重分析了静压桩的终压力与单桩竖向承载力之间的相互关系,并按照静压桩的入土深度,提出两者之间的相关性估算方法,为静压桩的安全、合理施工提供参考。     

Simultaneous hydrolysis and fermentation of pulp mill primary clarifier sludge

Bioconversion of sludge from the primary clarifier of a sulphite pulping operation to ethanol offers a number of advantages over conventional disposal options. The amount of material which must be disposed of is reduced while, at the same time, salable and environmentally friendly fuel-ethanol is produced. In this study, primary clarifier sludge (PCS) was shown to be hydrolysed to produce fermentable sugars at a rate proportional to enzyme loading. Initial (1 hour) hydrolysis rates as high as 12.6 g reducing sugar/L · h were observed at an initial enzyme loading of 10 filter paper units (FPU)/g. Hydrolysis was inhibited by spent sulphite liquor (SSL), an inhibition which could be completely overcome by fermenting the SSL to remove sugars. Surfactants were found to only marginally improve the production of sugars. To reduce the deleterious effects of end product inhibition, single stage simultaneous hydrolysis and fermentation (SHF) was carried out using cellulase enzymes and Saccharomyces cerevisiae.