洛阳石化环境质量管理系统的开发及应用

洛阳石化开发的环境质量管理系统，实现了对环保监测站化验分析数据的自动采集、污染源分析数据的汇总统计分析。统计报表的自动生成和打印。系统建立了以废水、废气重点污染源排放点的污染源自动监测系统，对污染源进行实时监控与分析；系统具备方便直观的数据发布功能和人员、设备、库房等事务管理功能。     

循环悬浮式半干法烟气脱硫技术在煤粉锅炉中的应用

半千法烟气脱硫技术目前在国内正在快速推广应用中，但成功的实例还较少，还存在系统不可靠，技术指标达不到，故障率高等问题。介绍了循环悬浮式半千法烟气脱硫技术及首次在煤粉锅炉中应用的烟气净化新工艺：静电预除尘＋循环悬浮式半干法烟气脱硫＋布袋除尘，论述了净化原理及在我厂的实际应用情况。     

磷肥厂烘干磨高压静电除尘技术及应用

本文根据高压静电除尘的原理,磷肥厂烘干磨粉尘的特性分析,以及作者本人的工作实践,探讨了高压静电除尘技术在磷肥厂烘干磨粉尘治理中应用的可行性。     

Comparative analysis of anaerobically digested wastes flow properties

The flow curve of anaerobically digested wastes from different origins was determined through rheological measurements. Regardless of their origin, samples can be divided into two families: simple non-Newtonian liquids well modelled by basic power law below 10%DC and viscoelastic liquids with a yield stress, well modelled by a Herschel–Bulkley model above. In all the cases, the rheological behaviour is driven by both the organic content and the volatile fraction (organic content/solid content), indicating that anaerobic digestion tends to smooth the rheological characteristics of organic wastes, whichever their origins.     

规划环境影响评价中生境评价的应用

本文即围绕规划环境影响评价工作当中,有关生境评价的几点问题展开详细分析与探讨,望能够促进生境评价在实际工作的应用质量与水平。     

环境统计在环境保护中的应用

环境统计是用数字反映并计量人类活动引起的环境变化和环境变化对人类影响的工作。从统计工作实践出发,通过能源环境统计数据、环境质量统计数据和污染源排放统计数据在日常环境管理中的应用实例,总结出环境统计在环境保护中的应用价值,以期引起对环境统计工作的重视。     

搅拌-序批式活性污泥反应器(WSBR)中好氧颗粒污泥的特性研究

为研究搅拌-序批式活性污泥反应器(WSBR)中好氧颗粒污泥的特性,利用WSBR反应器与传统SBR反应器对好氧活性污泥颗粒化的过程进行了比较.结果表明,在添加同量的聚炳烯酰胺(PAM)条件下,具有合理二次流场的WSBR反应器在4d就可见好氧颗粒污泥,而SBR反应器则在第10d才出现好氧颗粒污泥,且WSBR反应器中好氧颗粒...     

Prediction of vortex height from mechanical mixing in metal matrix nanocomposite processing by means of dimensional analysis and scaling

Mechanical mixing can be used for initial dispersion and distribution of nanoparticle agglomerates in metal matrix nanocomposite (MMNC) fabrication. As vortex height increases, flow is enhanced as well as the risk of oxidate melt contamination. The goal of this study was to examine and predict vortex height using dimensional analysis while varying fluid and the angular speed of a pitched square-blade impeller. An equation proposed by Markopoulos et al. was verified for the present experimental conditions. The relevant dimensionless numbers were the Reynolds (Re), Froude (Fr) and Galilei (Ga) numbers. A modified Fr was defined (Fr*) including the shaft and blade angles of the impeller. Experiments allowed calculation of the dimensionless numbers. Two fluids, water and 50 vol% aqueous glycerine, were used. Angular clockwise speed varied from 200 to 900 rpm in 100 rpm increments. Vortex height was measured in lateral view digital images. Correlations of the dimensionless numbers yielded, first, a linear relationship of the product of dimensionless vortex height (H) and specific gravity (ρ*) with respect to Fr*. A polynomial relationship was found between H and ReFr* for each fluid. The polynomial coefficients, in turn, follow a power law behavior with respect to Ga. This allows a prediction of vortex height in other Newtonian fluids that satisfy the single-phase isothermal flow condition. Perhaps, molten aluminum used in MMNC fabrication, can be analyzed based on a simple, room temperature, low cost transparent fluid system. For the experimental conditions in this study, the equation proposed by Markopoulos et al. was valid. The predicting methodology was verified with experimental results using 25 vol% aqueous glycerine, resulting in an absolute percent error of 5.29%, comparable and lower than an error of 9.12% obtained by predicting vortex height with Markopoulos’ equation.     

Experimental research of LNG accidental underwater release and combustion behavior

Evaluating potential hazards caused by accidental LNG release from underwater pipelines or vessels is a significant consideration in marine transportation safety. The aim of this study was to capture the dynamic behavior of LNG jet released under water and to analyze its vapor dispersion characteristics and combustion characteristics on the water surface during different release scenarios. Controlled experiments were conducted where LNG was jet released from a cryogenic storage tank. The dynamic process of LNG being jet released from orifices of different sizes and shapes, as well as the rising plume structure, were captured by a high-speed camera. The leakage flow rate and pipeline pressure were recorded by a flow meter and pressure gauge, respectively. The concentration distribution that emanated from the water surface was measured utilizing methane sensors in different positions with various wind speeds. The flame combustion characteristics of LNG vapor clouds, which immediately ignited upon the enclosed water tank, were also recorded. Additionally, the mass burning rate of the flame on the water surface was evaluated, and a new correlation between the ratio of flame length and width was established. The results indicated a large dimensionless heat release rate (Q*) and a continuous release flow rate in a limited burning area. This study could provide greater understanding of the mechanisms of LNG release and combustion behavior under water.     

Numerical study on premixing characteristics and explosion process of starch in a vertical pipe under turbulent flow

Fire and explosion accidents are frequently caused by combustible dust, which has led to increased interest in this area of research. Although scholars have performed some research in this field, they often ignored interesting phenomena in their experiments. In this paper, we established a 2D numerical method to thoroughly investigate the particle motion and distribution before ignition. The optimal time for the corn starch dust cloud to ignite was determined in a semi-closed tube, and the characteristics of the flame propagation and temperature field were investigated after ignition inside and outside the tube. From the simulation, certain unexpected phenomena that occurred in the experiment were explained, and some suggestions were proposed for future experiments. The results from the simulation showed that 60–70 ms was the best time for the dust cloud to ignite. The local high-temperature flame clusters were caused by the agglomeration of high-temperature particles, and there were no flames near the wall of the tube due to particles gathering and attaching to the wall. Vortices formed around the nozzle, where the particle concentration was low and the flame spread slowly. During the explosion venting, particles flew out of the tube before the flame. The venting flame exhibited a “mushroom cloud” shape due to interactions with the vortex, and the flame maintained this shape as it was driven upward by the vortex.