袋式除尘器进气均布板结构参数对气流分布的影响分析

针对袋式除尘器的进气均布板主要结构参数对气流分布影响的问题,采用正交试验方法进行CFD模拟试验设计,并以气流速度相对均方根σ值作为气流均匀性的评价指标。研究结果给出了σ与板数n、板长L、挡板上端距灰斗顶部截面高度ΔH、挡板前后偏角θ及过滤风速v之间的函数关系式。表明适当增加n、增大ΔH和θ、减小L、降低v,可以提高进气流分布均匀程度,影响进气均匀分布程度的排序为L>θ>n>ΔH>ΔL。     

厌氧生物滴滤法脱除冷煤气中硫化氢的研究

水煤气中硫化氢在燃烧时会转变成二氧化硫,对环境产生污染。文章采用厌氧生物滴滤塔法对冷煤气进行脱硫处理。因煤气对氧的严格限制,通过设计生物滴滤塔,经挂膜驯化后在厌氧条件下对浓度在1~5 g/m3左右的硫化氢进行脱除处理,考察滴滤塔运行条件对脱除效果的影响。结果表明,生物挂膜25 d后,生物滴滤塔达到稳定,喷淋液pH值为2.23,ORP值为283 mV,溶解氧为0.4 mg/L,对溶液中硫离子氧化效率达到94%。滴滤塔在液气比0.15,空塔气速0.088 m/s,pH值5.0~7.0,填料高度为82 cm,塔温为25~30℃左右时,达到较优的运行条件,此时该滴滤塔对以CO、CO2、H2和1 940 mg/m3H2S组成的模拟水煤气的脱硫效率达91.2%。     

某海洋平台上海水篮式过滤器事故分析

目的研究分析东海某一海上平台海水用篮式过滤器发生的腐蚀和堵塞事故原因。方法从海洋平台海水系统用篮式过滤器的原理、工艺流程、材料选择、滤网精度,滤芯设计、人工操作等多方面进行分析。结果受内压滤芯结构要优于受外压滤芯结构,如果过滤精度选择过高,会增加压差,造成滤芯堵塞。结论篮式过滤器滤芯单元应采用多滤芯的受内压结构,过滤精度应根据下游用户要求来确定。     

一种适用于深水压试验的传压隔热装置设计

目的真实高效地进行深水压环境的温度模拟。方法提出一种深水压试验压力加载过程中的恒温实现方法,通过开展基于皮囊的结构设计、密封性设计、导热性研究等工作,设计一种适用于深水压试验的传压隔热装置,对其进行理论分析和仿真计算。结果该装置可以实现液体温度在较长时间内基本恒定,具有良好的传压隔热性能。结论在建立的实验系统上进行了试验研究,实现了深水压环境模拟试验中压力载荷同步条件下液体温度小范围恒定功能,该技术为深水压环境试验的相关技术研究提供了技术储备。     

油田用钨合金镀层腐蚀性能评价研究

目的评价钨合金镀层油管的腐蚀性能。方法利用高压釜模拟高压气井和高含硫气井的腐蚀环境,进行高压高温腐蚀试验,以及标准的氢致开裂(HIC)和硫化氢应力腐蚀试验。采用电子扫描显微镜(SEM)及其能谱仪(EDS)和X射线衍射分析仪(XRD),分析或检测钨合金镀层和基管的腐蚀形貌、腐蚀产物的组成。结果油管表面的钨合金镀层平整而致密,其主要组成元素为W和Ni。高温高压腐蚀试验后,镀层仍然致密平整,腐蚀程度轻微。在60、90、120、140℃试验7天时,镀层和基材的H_2S/CO_2腐蚀速率分别为0.0179、0.0093、0.0102、0.0369 mm/a和1.030、1.272、1.183、0.991 mm/a。试验30天,在120℃时,其H_2S/CO_2腐蚀速率分别为-0.0085、0.1789 mm/a;在160℃时,其CO_2腐蚀速率分别为0.0091、0.8976 mm/a。该钨合金镀层均通过了标准的氢致开裂和硫化氢应力腐蚀试验。结论该钨合金镀层具有很好的耐腐蚀性能。     

动态膜压法测定江、污混合水体中有机物含量的探讨

用双驱动动态膜压仪测定江、污混合水中有机物含量。通过测定白龙港污水和长江水混合后的膜压和滞回环面积，用它们与相应的经典法CODCr作图，获得了滞回环面积和CODCr之间良好地线性关系，表明用动态膜压法可快速测定混合水中的有机物含量，不须加任何试剂，不会产生二次污染。同时，对实验结果进行了初步的机理探讨。     

Optimization of the high-pressure, near-critical liquid-based microsortation of recyclable post-consumer plastics

High-pressure, near-critical liquids were used as float-sink separation media for the microsortation of polyolefin mixtures and PET/PVC mixtures. Near-critical carbon dioxide was used for the refinement of the polyolefins, and sulfur hexafluoride was used to separate post-consumer PVC from PET. Preliminary experiments indicated that there was no overlap in the density ranges of post-consumer HDPE, LDPE and PP containers. There was no overlap in the PET and PVC densities, with the exception of a single PVC packaging material with a density in the PET range. These initial results indicated that a float-sink separation was a viable means of microsortation. Separations of 91% LDPE (1/8′ beads)/9% PP (1/8′ chopped strands) resin mixtures and mixed post-consumer polyolefin flakes were then conducted in a laboratory-scale, 1-I batch apparatus. This apparatus not only permitted the observation of the separation, but also enabled the separated fractions to be removed from the high-pressure environment. The results indicated that LDPE purity of greater than 98.9% was obtained in 3 min or less if (a) the fluid density was 0.018 g/cm³ greater than the PP density and only 0.002 g/cm³ less than the LDPE density, thereby providing the greatest buoyancy force for the removal of the PP, (b) the fluid was recirculated upward through the bed of mixed plastics, facilitating the upward movement of the PP, and (c) the loading was kept at levels below 40% by volume. HDPE purity of 99% was also attained with clean, dry, post-consumer mixed plastic flakes. The loadings for these separations were very low, however, due to the difficulty in agitating the mixed bed of plastics using fluid recirculation. An economic analysis of these microsortation processes indicated that the value of the sorted plastics relative to the mixed feed must increase by approx. $0.08/lb for the CO₂-based separation and approx. $0.27/lb for the SF₆-based separation to justify the implementation of these high-pressure processes.     

Concentrations of inorganic elements in 20 municipal waters in Sweden before and after treatment – links to human health

The water chemistry of 20 municipal water treatment plants in southern Sweden, representing various bedrock situations, and water qualities, were investigated. Four water samples, raw and treated, were collected from each plant and analyzed by predominantly ICP-OES and ICP-MS at four occasions from June to December, 2001. The concentrations of Ca, Mg, K, Na, HCO₃ and a number of micronutrients, varied considerably in treated waters from the studied plants (ranges; Ca: 9.1–53.7 mg L⁻¹, Mg: 1.4–10.9 mg L⁻¹, K: 1.1–4.8 mg L⁻¹, Na; 5.4–75.6 mg L⁻¹, HCO₃: 27–217 mg L⁻¹). The elimination of Fe and Mn from raw water was efficient in all treatments investigated, giving concentrations in treated waters below the detection limits at some plants. Softening filters gave waters with Ca-concentrations comparable to the softest waters in this study. Adjustment of pH by use of chemicals like lye, soda or lime, modified the consumer water composition significantly, besides raising the pH. It was estimated that drinking water contributed to approximately 2.2–13% of the daily Ca uptake, if the gastrointestinal uptake efficiency from food and water was estimated to be around 50%. The corresponding figures for Mg was 1.0–7% and for F 0–59%. None of the studied elements showed any significant time trends in raw or treated waters during the follow-up period. The concentrations of potentially toxic metals such as Al, Pb and U were low and did not indicate risks for adverse health effects (ranges; Al: 0.5–2.3 μg L⁻¹, Pb: 0–0.3 μg L⁻¹, U: 0.2.5 μg L⁻¹).     

新型聚乙烯填料生物滴滤床净化硫化氢气体的启动研究

研究了新型高密度聚乙烯改良型拉西环填料生物滴滤床净化硫化氢气体的启动过程,重点比较了启动过程中不同的挂膜方式对启动时间及效能的影响.结果表明,采用液相连续流强化挂膜法成膜时间短,在环境温度20～28℃时7 d可以挂膜成功.在启动过程中,随着工艺参数的突然改变(GRT缩短)和入口浓度波动,液相连续流强化挂膜后反应器的硫化氢去除率更稳定.在进气浓度最高为343 mg/m³时硫化氢去除率稳定在95%以上.试验过程中还发现,将SO₄^2-浓度作为活性污泥驯化完成的监测指标、液相S^2-去除率作为挂膜完成的监测指标更合理.启动结束后,通过2种途径减去喷淋液中的碳源并未影响硫化氢的去除率,这进一步表明生物滴滤床中硫化氢的净化主要由自养菌完成.     

Vapour pressures, aqueous solubility, Henry's law constants and air/water partition coefficients of 1,8-dichlorooctane and 1,8-dibromooctane

New data on the vapour pressures and aqueous solubility of 1,8-dichlorooctane and 1,8-dibromooctane are reported as a function of temperature between 20 °C and 80 °C and 1 °C and 40 °C, respectively. For the vapour pressures, a static method was used during the measurements which have an estimated uncertainty between 3% and 5%. The aqueous solubilities were determined using a dynamic saturation column method and the values are accurate to within ±10%. 1,8-Dichlorooctane is more volatile than 1,8-dibromooctane in the temperature range covered (p_sat varies from 3 to 250 Pa and from 0.53 to 62 Pa, respectively) and is also approximately three times more soluble in water (mole fraction solubilities at 25 °C of 5.95 × 10⁻⁷ and 1.92 × 10⁻⁷, respectively). A combination of the two sets of data allowed the calculation of the Henry’s law constants and the air water partition coefficients. A simple group contribution concept was used to rationalize the data obtained.