两种类型活套的张力控制模型

介绍了带钢热连轧过程中电动活套和液压活套各自的张力控制模型，前者以电机电流作为控制对象，后者以液压缸压力作为控制对象。     

有滞后环节的系统的闭环鲁棒辨识方法

提出一种新的针对带滞后环节的任意阶系统的闭环辨识方法。通过“三步法”，实现在闭环条件下的被控制对象的传递函数参数的辨识，所提出方法具有很强的鲁棒性。仿真例子表明该方法的有效性。     

薄板坯连铸浸入式水口结构数值模拟

使用有限元计算方法开展薄板坯连铸浸入式水口流场的研究 ,分别对水口不同浸入深度的流场分布、水口出口不同角度的流场分布进行计算。结果发现 :水口的浸入深度在 30 0mm时较为合理 ;水口的出口角度以R1 5、60°、45°为宜     

连续电镀锌镍合金的研究

提出了一种高氯化铵弱酸型镀液体系连续电镀锌镍合金工艺，研究了m(Ni^2 )/[m(Ni^2 ) m(Zn^2 )]、氯化铵浓度，电流密度、温度、PH值对镀层镍含量的影响，推导出连续镀的镀速计算公式，采用此工艺可获得外观良好、镍含量在13％－15％的锌镍合金镀层。     

DQ型高效催化剂在环管PP装置上的应用

介绍了使用DQ型球形高效催化剂在上海石油化工股份有限公司塑料事业部70kt/a环管连续法工业聚丙烯生产装置上应用研究的结果，并对结果进行了讨论。     

连续聚合法生产高粘度PA6

介绍连续聚合法生产高粘度ＰＡ６的聚合工艺，特点及产品性能指标，并介绍了关键生产设备的特点及作用。     

工业化连续生产对(艹孟)烷的影响因素探讨

主要对工业化连续生产对烷的影响因素进行了研究,探讨了原料中重组分含量、反应温度、反应压力等不同条件对对烷的生成所产生的影响。通过试验确定了主要生产工艺参数为:原料中重组分含量不超过1.2%,反应温度185-200℃,反应压力9-11 MPa。     

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     

SIMULATION AND ESTIMATION OF LONG MEMORY CONTINUOUS TIME MODELS

Abstract. Some general properties of long memory continuous time processes are recalled or proved. Methods of simulation are studied. A comparison with the usual discrete time autoregressive fractionally integrated moving-average filter is made and illustrations are provided. Then, two methods of estimation of the parameters of such a model from a discrete sample are studied, both theoretically and empirically, with Monte Carlo experiments.     

Modeling of solid—liquid adsorption: Effects of adsorbent loads on model parameters

The adsorption of cobalt phthalocyanine dye onto activated carbon in a continuous stirred tank adsorber was studied. The variables investigated were: adsorbent mass, adsorbent particle size and fluid flowrate. Several models based on film, pore and surface diffusion were constructed and fitted to the experimental data. Experimental results showed: (i) the increasing importance of the film mass transfer resistance for increasing adsorbent loads; (ii) the increasing importance of the surface diffusion mechanism for increasing adsorbent loads; and (iii) the better discrimination among different models for higher adsorbent loads and lower flowrate.