陶瓷废水处理原理及常用固液分离方法比较

本文就陶瓷废水的产生来源及废水处理原理进行了分析，对佛山市该行业废水处理常用的固液分离方式进行了处理效果及技术经济比较，指出将常用于给水处理工艺的水力循环澄清池应用在陶瓷废水处理工艺中，与其它分离方法相比，不仅占地面积小，效率高，而且易于操作和控制，可实现废水的全部回用，并建议对这种高悬浮物、高浊度水的混凝反应过程进行自动控制以提高水处理的稳定性。     

大气自动监测系统在炼油厂的应用

运用日本引进的大气自动测定仪组成炼油厂的大气环境自动监测系统。运行结果表明，该系统自动化程度高，故障率低，操作简便，数据齐全，它的建立使我厂的大气环境监测上了一个新台阶．     

上海港散装液态危险品运输和监管现状

简要介绍了上海港散装液态危险货物运输开展的历史及迄今有关方面的现状，进而对上海港监为确保危险品散化运输在安全、防污、环保、贸易等之间的相互协调发展所采取的一系列相关措施加以概括、归纳，使之条理化。     

一种新型复合式生物流化反应器混合特性的研究

对新型蜂窝状断面复合生物流化反应器进行了液体循环速率和水力停留时间分布曲线的测定，实验表明新型反应器具有抗冲击负荷强，接近CSTR反应器的特点，反应器随气量增大、载体投加量减少和进水量减少而更近似于CSTR反应器，通过理论分析，证明了影响液体循环速率的参数主要有气体流量(气含率)、反应器沿程和局部阻力系数以及Ad/Ar，并且得出液体循环速率与反应器高度的0．5次方成正比。     

新型绿色化学反应介质的研究进展

综述了绿色化学在反应介质方面的研究进展。新型的有机合成反应介质主要包括离子液体、超临界流体、水溶剂及微波无溶剂技术。这些新型反应介质不仅可以取代传统的挥发性有毒有害有机溶剂,同时还可提高反应的活性和选择性,加速反应的进行,且有利于催化剂的回收利用及产品的分离。新型绿色化学反应介质是实现有机合成绿色化的重要途径。     

液体浮选法回收废旧电脑线路板中铜的研究

本文用物理及化学方法研究了废旧电脑线路板的处理回收工艺.首先通过粉碎机将线路板破碎,在不同破碎时间和转速下,对筛分后各粒级的产物作累积产率曲线,得到理想的破碎时间和转速,然后利用液体对破碎的物料进行浮选,量化分析铜与非金属的解高程度,最后通过碘量法检测浮选后铜的回收情况.实验结果表明:在R＞2000 rpm的条件下线路板粉碎120s,采用三溴甲烷作浮选液,进行液体浮选,在dp＜0.074 mm的细粒级中,主要是玻璃纤维和碳化硅等非金属物质,线路板中的铜主要富集在0.84～0.125 mm粒级中,在0.84～0.42 mm粒级中,铜的回收率可达到97.89%.     

五日生化需氧量(BOD5)测定方法探讨

本文针对GB／T7488-1987《水质五日生化需氧量(BOD5)稀释与接种法》中BOD5的测定和计算时接种稀释水的空白扣除方法，提出了直接测接种液的BOD5值，按接种液的比例在水样中进行扣除的方法，提高了BOD5值的准确性。更能反应BOD5的真实性。     

Assessment of the maximum possible liquid superheat during flashing leak flow

During the discharge of flashing liquids through leaks due to abrupt depressurization a transient thermodynamic non-equilibrium in the form of a boiling delay in the superheated liquid flow can occur. As a consequence the actual mass flow quality is smaller than calculated under the assumption of an immediate adjustment of the thermodynamic equilibrium between the phases. For the prediction of the leak mass flow for a given pressure difference the magnitude of this self-adjusting mass flow quality is needed.

Most of the models cited in the literature include only the equilibrium mass quality as limiting quantity and ignore further effects as that of the depressurization velocity or the mean nucleus distance. For the assessment of the maximum possible liquid superheat during flashing only the conduction heat transfer from a stagnant liquid to the bubble surface is used to describe the bubble growth.

The sub-model for the bubble growth due to expansion and mass transfer necessary for the global prediction of the transient thermodynamic non-equilibrium in flashing liquids was validated using bubble radii measured by Hooper et al. [Bubble growth and pressure relationship in the flashing of superheated water. Technical publication 6904, Mechanical Engineering Department, University of Toronto, 1969] for the case of a sudden depressurization of initially saturated water. On this basis the calculated time-dependent temperature field, the actual mass quality, the mean liquid temperature and, in comparison to the corresponding values based on the assumption of immediate thermodynamic equilibrium, the maximum possible liquid superheat are predicted.     

On the response of 500 gal propane tanks to a 25% engulfing fire

This paper presents detailed data on the thermal response of two 500 gal ASME code propane tanks that were 25% engulfed in a hydrocarbon fire. These tests were done as part of an overall test programme to study thermal protection systems for propane-filled railway tank-cars.

The fire was generated using an array of 25 liquid propane-fuelled burners. This provided a luminous fire that engulfed 25% of the tank surface on one side. The intent of these tests was to model a severe partially engulfing fire situation.

The paper presents data on the tank wall and lading temperatures and tank internal pressure. In the first test the wind reduced the fire heating and resulted in a late failure of the tank at 46 min. This tank failed catastrophically with a powerful boiling liquid expanding vapour explosion (BLEVE). In the other test, the fire heating was very severe and steady and this tank failed very quickly in 8 min as a finite rupture with massive two-phase jet release. The reasons for these different outcomes are discussed. The different failures provide a range of realistic outcomes for the subject tank and fire condition.     

液化气运输过程中的危险分析

应用各种爆炸后果估计模型对液化气运输过程中的爆炸后果进行了评估，并用ETA分析方法对存在的危险进行了分析，指出了控制措施。