沙尘天气对沈阳市空气质量的影响分析

针对沙尘天气的成因、来源及危害进行综述 ,对沈阳市 2 0 0 2年出现的沙尘天气特点及对空气质量影响进行了分析 ,提出几点防治对策     

轻烧镁窑烟尘污染治理技术的筛选与应用

利用煤气发生炉生产煤气，烧结轻烧镁，具有产品质量高，大幅度削减烟尘排放量，节约能源等优点，该项技术具有广泛的推广价值，本文较详细地介绍了辽宁省轻烧镁窑烟尘污染治理技术的典型，具有同类技术的国内先进水平．     

冲击水浴除尘器密闭式水位控制箱的研制

通过对的冲击水浴除尘器存在运行工况不稳定等问题的分析，介绍了一种能提高除尘器净化效率，稳定设备运行阻力的新型水位控制箱。     

GW型加热炉烟气净化系统研究设计

为适应日益严格的环保要求,根据GW型燃油加热炉烟气排放特征和排放规律,设计采用循环流化床工艺进行除尘脱硫。中试结果表明:在最佳工况条件下,系统除尘效率可达97%～98%,脱硫效率达80%～90%,达到国家燃油锅炉一类区域排放标准要求。     

高炉出铁场除尘设计新思路

论述了高炉出铁场烟尘治理的现状，对二次除尘设计提出了新的设想。     

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。     

Differences and similarities of gas and dust explosions: A critical evaluation of the European ‘ATEX’ directives in relation to dusts

Explosive gas mixtures and explosive dust clouds, once existing, exhibit similar ignition and combustion features. However, there are two basic differences between dusts and gases which are of substantially greater significance in design of safety standards than these similarities. Firstly, the physics of generation and up-keeping of dust clouds and premixed gas/vapour clouds are substantially different. This means that in most situations where accidental explosive gas clouds may be produced quite readily, generation of explosive dust clouds would be highly unlikely. Secondly, contrary to premixed gas flame propagation, the propagation of flames in dust/air mixtures is not limited only to the flammable dust concentration range of dynamic clouds. The state of stagnant layers/deposits offers an additional discrete possibility of flame propagation.

The two European Directives 94/9/EC (1994) and 1999/92/EC (1999) primarily address gases/vapours, whereas the particular properties of dusts are not addressed adequately. Some recent IEC and European dust standards resulting from this deficiency are discussed, and the need for revising the two directives accordingly is emphasized.     

吴泾工业区扬尘污染治理中降尘监测的影响因素研究

降尘监测可以较客观地反映与评价城市区域扬尘污染水平。及时掌握降尘污染状况,对区域扬尘污染治理措施成效和评价城市区域环境空气质量具有实际意义。降尘监测具有采样设备简单、操作简便易行、成本相对较低等特点。但是监测周期长、环节多等都会影响降尘监测的准确性。本文通过对吴泾工业区扬尘污染治理中降尘数据分析发现,降尘监测中存在降尘数据波动大、受周边环境影响大、人为损坏多等诸多因素的影响,就这些影响因素进行分析探讨,并提出了若干建议和解决方法。     

Ash deposition impact on the energy performance of photovoltaic generators

A little known side effect of the atmospheric air pollution is the degradation of photovoltaic (PV) cells’ performance due to the deposition of solid particles varying in composition, size and origin. In this context, an experimental-based investigation is conducted in order to compare the energy performance of two identical pairs of PV-panels; the first being clean and the second being artificially polluted with ash, i.e. a by-product of incomplete hydrocarbons’ combustion mainly originating from thermal power stations and vehicular exhausts. A series of systematic measurements of current intensity, voltage output and solar radiation are executed simultaneously for the clean and the polluted PV-panel, so that the effect of several mass depositions on the PVs’ power output, energy yield and conversion efficiency may be determined. According to the results, a considerable deterioration of the PV-panels’ performance is obtained, i.e. almost 30% energy reduction per hour or 1.5% efficiency decrease (in absolute terms) for ash accumulation on the panels’ surface reaching up to 0.4 mg/cm².     

Effect of pyrolysis and oxidation characteristics on lauric acid and stearic acid dust explosion hazards

The effect of pyrolysis and oxidation characteristics on the explosion sensitivity and severity parameters, including the minimum ignition energy MIE, minimum ignition temperature MIT, minimum explosion concentration MEC, maximum explosion pressure P_max, maximum rate of pressure rise (dP/dt)_max and deflagration index K_st, of lauric acid and stearic acid dust clouds was experimentally investigated. A synchronous thermal analyser was used to test the particle thermal characteristics. The functional test apparatuses including the 1.2 L Hartmann-tube apparatus, modified Godbert-Greenwald furnace, and 20 L explosion apparatus were used to test the explosion parameters. The results indicated that the rapid and slow weight loss processes of lauric acid dust followed a one-dimensional diffusion model (D1 model) and a 1.5 order chemical reaction model (F1.5 model), respectively. In addition, the rapid and slow weight loss processes of stearic acid followed a 1.5 order chemical reaction model (F1.5 model) and a three-dimensional diffusion model (D3 model), respectively, and the corresponding average apparent activation energy E and pre-exponential factor A were larger than those of lauric acid. The stearic acid dust explosion had higher values of MIE and MIT, which were mainly dependent on the higher pyrolysis and oxidation temperatures and the larger apparent activation energy E determining the slower rate of chemical bond breakage during pyrolysis and oxidation. In contrast, the lauric acid dust explosion had a higher MEC related to a smaller pre-exponential factor A with a lower amount of released reaction heat and a lower heat release rate during pyrolysis and oxidation. Additionally, due to the competition regime of the higher oxidation reaction heat release and greater consumption of oxygen during explosion, the explosion pressure P_m of the stearic acid dust was larger in low concentration ranges and decayed to an even smaller pressure than with lauric acid when the concentration exceeded 500 g/m³. The rate of explosion pressure rise (dP/dt)_m of the stearic acid dust was always larger in the experimental concentration range. The stearic acid dust explosion possessed a higher P_max, (dP/dt)_max and K_st mainly because of a larger pre-exponential factor A related to more active sites participating in the pyrolysis and oxidation reaction. Consequently, the active chemical reaction occurred more violently, and the temperature and overpressure rose faster, indicating a higher explosion hazard class for stearic acid dust.