Air sampling of volatile sex pheromone components in a closed jar

A cotton wool plug, used as the source for pheromone release, was placed in closed 1-quart Mason jars, either at the mouth or at the rear of the jar. Air sampling of the two components of the sex pheromone (total 2.2 mg at the source) of the almond moth (Ephestia cautella) female showed that the saturation period near the source in still air was 20–22 hr and that far from the source was 40–50 hr, reaching a level of less than 1 ng/ml air. The ratio between the components (Z,E)-9,12-tetradecadienyl acetate, designated D, and (Z)-9-tetradecenyl acetate designated M, in the air was close to the original ratio for both sampling sites, albeit somewhat richer in the more volatile (Z)-9-tetradecenyl acetate (source 77.023.0 DM, air 73.0– 74.327.0–25.7; source 80.119.9, air 77.622.4; source 25.174.9, air 23.976. 1 DM). The total amount of pheromone per milliliter of air was two to three times larger near the source than far from it at the early stages of the evaporation and saturation process. When the amount of pheromone applied to the source was tripled (7 mg), the amount far from the source was almost tripled, or the saturation time was cut by factor of two to three.     

Treatment of methanol wastewater with two-stage and two-phase anaerobic process

The two-stage and two-phase anaerobic process (TSTP) composed of hydrolytic acidification reactor,first-order and second-order external circulation anaerobic reactors (EC) was taken to treat methanol wastewater. Test results show that TSTP process is quick start-up in 51 d, and the maximum VFA of hydrolytic acidification reactor effluent reaches 876 mg/L. Under the condition of volume loading of 6.56 kgCOD/m3·d, COD removal rate of the first-order EC reactor is about 85%, and under the condition of volume loading of 1.02 kgCOD/m3·d, COD removal rate of the second-order EC reactor is about 50%. When the inflow COD of TSTP process is between 7000-11000 mg/L, its effluent COD is lower than 600 mg/L. In the biological conversion process of methanol into methane,the production of acetic acids as an intermediate product can be ignored and the direct production of methane from methanol is predominant.     

气液两相流中气泡形态及运动特征参数提取

对气泡发生装置中竖直向上气泡的形态及运动特征提取方法进行了研究。采集原始气泡图像,进行图像灰度化、差影和中值滤波等图像预处理,针对气泡图像的特点,提出动态阈值压缩大津法进行阈值分割,并结合扫描线种子填充算法与图像形态学运算进行孔洞填充,同时基于边缘面积属性对气泡特征区域进行自动识别。实验结果表明,该方法简单有效,鲁棒性强,可以很好地将目标气泡从背景中分离出来,有效提取气泡周长、面积、圆形度和质心坐标等形态特征参数,并实现气泡运动速度的测量。     

一类效应代数中的理想

证明了若I是效应代数（E（Ω）,,⊥,0,1）的一个闭理想,则存在Ω的一个闭的子集S,使得I是所有在S上为零的函数的集合.反之,若S是一个Ω的闭子集,则所有在S上为零的函数之集是效应代数（E（Ω）,,⊥,0,1）的一个闭理想.     

气体释放速率对浅层气藏中气水运移的影响

为了论证在防治浅层气地质工程灾害中预先采取的有控制性排气措施的合理性和必要性,借助非饱和水气两相渗流原理,研究浅层气藏在气体释放路径下的气水运移规律.采用数值方法描述排气井不同释放速率对地下浅层气藏中气水运移的影响.结果表明:气体释放速率对气藏中的气水运移和分布形态有显著影响,释放速率越快,"水锥"效应越明显;实际工程中需结合详勘数据,选取适宜的排气速率,实施控制性放气措施,避免过早发生淹井,导致气井快速失效;在气藏中的浅层气体释放完毕后,砂土中会残留部分以气泡形式存在的气体,施工过程中需引起重视.     

IDC机房用热管换热器节能特性试验研究

机房空调能耗约占机房总能耗的40%。在IDC机房节能方案中,使用热管换热器利用自然冷源散热,能够减少空调工作时间,同时可避免室内外空气接触,满足湿度、洁净度的要求。参考北京某IDC机房,搭建试验模型,分析IDC机房内热管换热器和空调各自的散热负荷和能耗特性,研究围护结构的散热特性,比较设定温度和室外温度对空调能耗的影响。结果表明,北京冬季工况下,仅依靠围护结构的散热,无法满足IDC机房的散热需求;围护结构散热量约占IDC机房总散热量的19.5%;空调平均每天耗能3.5~4 kWh;使用热管换热器室内外温差不超过20℃,能耗仅为空调能耗的41%,全年节能约40%;与室内设定温度相比,室外气温对空调能耗的影响较大;室外温度提高1℃,空调能耗平均增加5%~6%。     

沸腾两相流动压力波动信号的特性

研究了竖直管内沸腾两相流动时压力波动信号的特性,对压力波动时间序列进行了标准偏差分析、功率谱密度函数分析、分维数分析、相关维分析及Kolmogorov熵分析,考察了热流密度对压力波动的影响规律.结果表明沸腾两相流动具有非线性混沌特性,且热流密度对各特征参数有不同影响.     

Computational fluid dynamics (CFD) modeling of spouted bed: Influence of frictional stress, maximum packing limit and coefficient of restitution of particles

Following the previous article [Du, W., Bao, X., Xu, J., Wei, W., 2006. Computational fluid dynamics (CFD) modeling of spouted bed: assessment of drag coefficient correlations. Chemical Engineering Science 61 (5), 1401-1420], this contribution describes the influences of the frictional stress, maximum packing limit and coefficient of restitution of particles on CFD simulation of spouted beds. Using the two-fluid method embedded in the commercial CFD simulation package Fluent 6.1, the spouting hydrodynamics of a cylindrical-conical spouted bed was simulated and verified with the experimental data of He et al. [He, Y.L., Lim, C.J., Grace, J.R., Zhu, J.X., Qin, S.Z., 1994a. Measurements of voidage profiles in spouted beds. Canadian Journal of Chemical Engineering 72 (4), 229-234; He, Y.L., Qin, S.Z., Lim, C.J., Grace, J.R., 1994b. Particle velocity profiles and solid flow patterns in spouted beds. Canadian Journal of Chemical Engineering 72(8), 561-568]. The results showed that, for coarse particles, the frictional stress is important only for the annulus computation and has no obvious effects on the hydrodynamics of the solids flow in the spout region. The specification of the maximum packing limit could significantly affect the properties of the pseudo-fluid phase of the particles by changing the radial distribution function. The strong dependence of the pseudo-fluid properties of the particle phase, such as pressure, bulk viscosity and shear viscosity, on the granular temperature accounts for the influence of the coefficient of restitution of particles on CFD modeling. The solids volume fraction at loose packing state is suitable for spouted bed simulations, and a pretest of the coefficient of restitution of particles must be conducted when no experimental datum is available.     

湿法磷酸固-液体系混沌混合与浸出强化行为

湿法磷酸浸出过程中，传统刚性搅拌桨的作用方式主要是剪切作用，容易形成对称性流场结构，降低搅拌效率。实验考察了桨叶类型、离底高度、搅拌速度、柔性钢丝绳长度、柔性钢丝直径对磷矿浸出率及最大Lyapunov指数(LLE)的影响。实验结果表明：刚柔组合桨通过刚-柔-流的耦合作用，改善流场的结构，提高了流体混沌混合效果。当搅拌转速225 r/min，浸出时间120 min，离底高度h=T/4，柔性钢丝绳直径d= 0.42r，柔性钢丝绳长度L=1.3T时，刚柔组合桨的最大Lyapunov指数达到0.09071，磷矿浸出率提高了10.8%。另外，在相同的功耗(P _v=9890 W/m³)条件下，刚柔组合桨使反应器内的悬浮均匀度和渣中磷含量分别降低了40.8%和17.67%，有效地改善了晶体的形貌，提高了磷石膏的过滤性能，强化了颗粒的混合与浸出。     

双水相分离纯化R-藻红蛋白

为了获得优于食品级的R-藻红蛋白(R-PE),采用双水相体系从坛紫菜中分离纯化R-PE.结果表明,聚乙二醇(PEG)/酒石酸钾钠双水相体系,当PEG相对分子质量为1 500且p H为8.06、系线长22.30%、体积比0.12时纯化效果最佳,R-PE纯度由细胞破碎液的0.43提高到1.47,回收率为84.42%.经过二次双水相纯度达1.55,纯化因子为3.60.得到的R-PE具有较高的生物活性.PEG相对分子质量1500/酒石酸钾钠双水相体系成功分离纯化R-PE,操作简单,成本低,适于工业化.