L6-M Al的超塑性工艺的实验研究

依拟定之正交实验方案，主要探讨工艺因素成形温度(T)，气体速度(V)，模具圆角半径(R)对铝板(L6-M)超塑性工艺性能的影响。经研究发现铝材(L6-M)在超塑性成形时，三个主要工艺因素对其影响的强弱顺序为成形温度(T)；气体速度(V)；模具圆角(R)，且都影响显著。     

新疆核试验场周围地区主要食品中~(90)Sr(锶)、~(137)Cs(铯)水平及其所致居民剂量

本文报道了新疆核试验场周围地区9个调查区17种主要食品中~(90)Sr、~(137)Cs含量分别为1.1～72.3,0.3～40.7×10~(-2)B_q·Kg~(-1);3个对照区分别为1.6～68.4,0.6～27.4×10~(-2)B_q·K_g~(-1)。两地区同类食品中~(90)Sr、~(137)Cs平均含量基本一致。调查区~(90)Sr、~(137)Cs所致成年居民有效剂量当量值分别为2μSV(集体剂量当量为30.0人· SV);0.3μSV(4.5人· SV)。对照区分别为2.2μSV(集体剂量当量为20.9人·SV);0.4μSV(3.0人·SV)。可见我国核试验产生的~(90)Sr、~(137)Cs对核试验场周围地区食品没有造成明显的局部污染,所致居民剂量当量负担仅为我国天然外照射所致年有效剂量当量(952μSV)的0.2％和0.03％。对该地区的广大居民健康不会产生有害的影响。     

创建绿色社区构建和谐社会--环境保护公众参与的有效途径

本文运用社会学和政策学原理，结合内蒙古自治区创建绿色社区的实践，从创建绿色社区的背景、绿色社区的有关概念、创建绿色社区的必要性和可行性分析、绿色社区的指标体系框架和创建绿色社区的主要方法等5个方面，对如何开展创建绿色社区工作进行了讨论。文章对即将在我区全面开展的创建绿色社区工作有一定的借鉴意义。     

一个液相化学反应机理的建立和应用

利用比较积分反应速率的方法，建立了一个简化液相化学反应机理ＡＲＣＭＬ，并在各种大气状况下以及各种物理参数下对ＡＲＣＭＬ作了验证，然后利用ＡＲＣＭＬ模拟光化学烟雾形成初期的云水酸化过程，结果表明，自由基氧化Ｓ（Ⅳ）在污染或高ＮＯｘ的大气中非常重要。     

青岛市区土壤天然放射性核素的外照射水平估算研究

城市的辐射环境质量对于人居和发展规划有重要意义。利用伽玛能谱仪对青岛市区内的天然放射性核素进行了大规模高密度的现场测量,采用Beck公式计算了离地面1m高处的空气吸收剂量率,进而计算了外照射年有效剂量、外照射指数和等效镭浓度,对研究区的外照射水平进行了系统的评价。与和其他国家全国比较,虽然该区的空气吸收剂量率较高,但是其他衡量天然放射性核素外照射水平的指标均在容许范围之内。因此该区属于外照射水平的安全区域,人居环境不受影响。     

Measuring biological diversity

The diversity of a set of species refers to the joint dissimilarity of the species in the set. This paper discusses the measurement of diversity from the set of pairwise distances between the species in the set. A measure called the effective number of species is developed from a non-parametric probability inequality and is shown to have a simple interpretation in terms of comparing linear experiments.     

时空效应下不同孔径超前钻孔有效排放半径研究*

为解决煤矿在施工过程中局部防突问题,进行现场实测并结合数值模拟计算,研究瓦斯排放钻孔影响半径在不同排放时间和不同超前钻孔直径影响下的变化规律。研究结果表明:对于同一孔径的钻孔,在一定时间内影响半径随着时间的增加而增加,不同直径的钻孔呈不同的函数关系;对于不同的孔径,影响半径随着钻孔直径的增加而增加,研究结果可为矿井作业中治理煤与瓦斯局部突出提供重要参考。     

Experimental study on unconfined methane explosion: Explosion characteristics and overpressure prediction method

Explosion accidents have become the main threat for the high-efficiency use of cleaner gas energy sources, such as natural gas. During an explosion, obstacle causing flame acceleration is the main reason for the increase of the explosion overpressure, which still remains to be fully understood. In this research, field experiments were conducted in a 1 m³ cubic frame apparatus to investigate the effect of built-in obstacles on unconfined methane explosion. Cage-like obstacles were constructed using square steel rods with different cross section size. The results demonstrated that the flame could get accelerated due to the hydrodynamic instability and obstacle-induced turbulence, which enhanced the explosion overpressure. In the near field, the overpressure wave travelled slower and the maximum overpressure could almost keep constant. Reducing the cross section size, or increasing the obstacle height or the obstacle number per layer could determine the rise of the maximum overpressure, the maximum pressure rising rate and the overpressure impulse. For uniformly constructed obstacles, self-similar theory was chosen to measure the influence of the hydrodynamic instability, and a parameter β was adopted to measure the flame acceleration caused by obstacle-induced turbulence, the value of which was 2 in this research. Based on the acoustic theory, an overpressure prediction model was proposed and the predicted results agreed with the measured values better than previous models, such as TNT equivalency model and TNO multi-energy model.     

Risk-based quantitative method for determining blast-resistant and defense loads of petrochemical buildings

Petrochemical buildings are usually distributed near chemical installations and have a high risk of explosion because of the concentration of people. In order to effectively design and protect buildings against explosion, it is needed to determine the blast-resistant and defense loads reasonably. Based on the theory of risk, a triangular pyramid explosion risk model was established in this study, which combined the overpressure p, duration t, and frequency f of the explosion scene at the same time. The first principle of “acceptable cumulative frequency” and the key principle of “maximum explosion risk” were formulated. According to this method, the explosion risk of eight leakage units with 10 groups of leakage hole size and three dangerous wind directions were obtained. According to the cumulative explosion frequency curve and the explosion risk curve, blast-resistant and defense loads of the four walls were determined quantitatively. Among the four walls, the explosion overpressure were 44.0–74.5 kPa, and the corresponding duration were 34.1–39.1 ms. The cumulative explosion frequency were 2.11E−5 to 8.58E−5 times annually. The explosion risk value were 3.64E−3 to 5.35E−3 kPa·ms annually. The results indicated that it was of great importance for the calculation of the explosion risk to reasonably divide the leakage unit and determine the leakage frequency. The explosion scene and its frequency, the volume of the obstructed region, and the distance of the explosion source were the key variables that affected the explosive load. The final blast-resistant and defense load values were found in the case of the middle hole size leakage. Blast-resistant and defense loads not only met the risk acceptance standard but also considered the overpressure and the duration of explosion. At present, they have been extensively applied in the blast-resistant design and engineering transformation of buildings in SINOPEC.     

聚合氯化铁-腐殖酸(PFC-HA)絮体的不同拓扑空间下分形维数的研究

通过对PFC混凝去除水中HA过程中所形成的PFC-HA絮体的研究结果表明,原水pH分另4为9.0、7.0和5.0时,最佳投药量下形成的絮体的平均沉降速度之间的比值为1.17:1.00:0.49,而且所有絮体的水平投影方向的平均直径与垂直投影方向的平均直径的比值均接近0.85.结合Logan公式和有效密度-长轴的双对数关系计算出的絮体三维空间的分形维数Df较为可靠,在本试验中3种pH的原水下形成的PFC-HA絮体的Df均小于2.0.絮体沉降速度的变化是质量分形维数Df、有效密度和粒径等因素的变化综合影响结果,因此,絮体的Df、有效密度各自的变化趋势有可能与沉降速度的不一致.原水pH=7.0时絮体的Df稍大于原水pH=9.0时絮体的Df,但比原水pH=5.0时絮体的Df大11.73%.可见,与原水pH=9.0时形成的絮体相比,原水pH=7.0时形成了稍微密实的小絮体,但原水pH=5.0时却形成了较为疏松的、很小的絮体.在本试验的图像分辨率下,PFC-HA絮体在一维拓扑空间下的分形维数D1比较低,一般都低于1.10.基于投影面积-长轴关系计算的二维拓扑空间的分形维数D2变化趋势为样品3稍大于样品2,样品1最小;然而基于投影面积一周长计算的二维拓扑空间的分形维数D2却呈现不同的变化趋势.另外,尽管PFC-HA絮体的Df小于2,但其与基于投影面积-长轴关系计算的二维拓扑空间的分形维数D2不相等,不符合Meakin的结论,这与本试验中CCD相机的分辨率和絮体样本数量有关.