催化氧化处理高浓度有机化工废水

本文提出了一种处理高浓度有机化工废水中COD、色度的有效新技术,该技术是用二氧化氯为催化剂,在自制催化剂存在的条件下将废水中的有机物氧化分解,COD去除率≥70％,色度去除率≥95％,一般高浓度有机化工废水经本法处理接后续生化可以达标。     

氧化塘底泥对作物生长影响的研究

本文通过农田试验 ,得出氧化塘底泥可以改良土壤结构、增加有机质含量、微生物数量、提高作物产量的结论。因此 ,底泥可以作为一种有机肥应用于农业。     

巷道放顶煤人-机-环境系统可靠性研究

应用系统可靠性和人 -机工程学理论 ,建立了急倾斜煤层巷道放顶煤人 -机 -环境系统可靠性模型 ,给出了系统可用度和生产能力的计算公式。结合开滦马家沟矿 972 3工作面人 -机-环境系统分析 ,探讨了提高系统可靠性和生产能力的有效途径。理论分析及实例计算结果表明 ,所建立的模型能简便地找出系统的薄弱环节 ,准确预测系统可用度和生产能力 ,从而为指导矿井设计和生产提供科学依据     

改性土壤对模拟含油废水中油的吸附

研究季铵盐阳离子表面活性剂四甲基铵离子 ( TMA)和十六烷基三甲基铵离子 ( HDTMA)改性的土壤 (黑土、黄棕壤、红壤 )对水中油的吸附作用 .结果表明 :改性土壤和未改性土壤均可吸附水中的油 ,但改性土壤对水中油的吸附能力明显高于未改性土壤 .改性土壤吸附油能力的顺序依次为 :1 CEC- HDTMA黑土 >1 CEC-HDTMA黄棕壤 >1 CEC- HDTMA红壤 >1 CEC-TMA黑土 >1 CEC-TMA黄棕壤 >1 CEC- TMA红壤 .未改性土壤和 HDTMA改性土壤对油的吸附通过分配来进行 ,吸附等温线可由 Henry方程表示 ,得出 logK_SOM为 2.69,logK_HDTMA为 3.35;TMA改性土壤对油的吸附符合 Langmuir方程 ,其对油的饱和吸附量分别为 1150 mg/kg( TMA黑土 ) ,751 mg/kg( TMA黄棕壤 ) ,172 mg/kg( TMA红壤 )     

对影响三槽氧化沟工艺除磷效果因素的分析

通过对唐山市北郊污水处理厂三槽氧化沟工艺分析,发现污泥浓缩池上清液的回流和无法形成严格厌氧环境是该工艺除磷效果不佳的主要原因。文中提出了一些改进途径。     

天然色素生产废水的生物处理研究

天然色素生产废水是一种色度大、难处理的高浓度有机废水,为了寻找该废水的有效处理方法,本文作者采用由升流式厌氧污泥床(UASB)、生物接触氧化、混凝吸附组成的废水处理工艺,对该废水进行了处理试验,结果表明,对稀释4倍的原水,当进水COD为14900mg/L左右时,UASB经过36h的水力停留时间,COD的去除率为58.2%～60.2%、出水色度为180～270倍,SS为119～126mg/L,pH值为6.5～6.8;UASB出水经过24h好氧生物接触氧化反应,COD的去除率超过90%,SS<70mg/L;最终经过Ca(ClO)2氧化和煤渣吸附深度处理,脱色可至无色,出水COD为200mg/L以下。UASB生物接触氧化氧化吸附组合处理工艺处理该类天然色素生产废水是可行的。     

应用臭氧氧化技术深度处理油船含油压载水的实验研究

油船含油压载水大量排放入海会对海洋生态环境产生较大的危害。在研究中,通过强电离放电技术制取高浓度臭氧,应用臭氧氧化方法来深度处理含油压载水,模拟实验表明在臭氧投加浓度达到120mg/L,在较短的接触时间(2min)内,臭氧对不同浓度的含油压载水中的油去除率可达到50%以上,同时使芳香族类物质显著减少,降低含油污水的生物毒性,处理方法具有可观的应用前景。     

鲁西北地区现状农业土地资源劳动力承载力模拟

传统农区农业劳动力的出路问题是中国目前面临的一个重要经济和社会问题,论文从农业土地资源劳动力承载力评价角度,对这一问题进行了探讨。提出了最小劳均耕地面积、农业土地资源劳动力承载力、规模种植压力指数和农业土地资源劳动力承载力指数的概念及模型,在建立模型分析农业土地资源劳动力承载能力的基础上估算劳动力的剩余。结果如下:在现实收入水平下,鲁西北地区最小劳均耕地面积为0.39hm₂,而实际劳均耕地面积为0.34hm₂;在现实收入水平下,鲁西北地区约有53.3×104个劳动力需要转移,剩余劳动力约占农林牧渔业总劳动力的14.9％;规模种植压力指数K=1.18>1,表明耕地处于正压力状态(承受压力)。说明目前鲁西北地区单位农林牧渔业劳动力所拥有的耕地规模较小,致使劳动生产率难以提高,农民收入增加缓慢,要大力提高农业劳动生产率,必须缩减从事农业的劳动力规模,寻求剩余劳动力转移的有效途径。     

Effects of a diesel oxidation catalyst on gaseous pollutants and fine particles from an engine operating on diesel and biodiesel

The effects of a diesel oxidation catalytic (DOC) converter on diesel engine emissions were investigated on a diesel bench at various loads for two steady-state speeds using diesel fuel and B20. The DOC was very effective in hydrocarbon (HC) and CO oxidation. Approximately 90%–95% reduction in CO and 36%–70% reduction in HC were realized using the DOC. Special attention was focused on the effects of the DOC on elemental carbon (EC) and organic carbon (OC) fractions in fine particles (PM_2.5) emitted from the diesel engine. The carbonaceous compositions of PM_2.5 were analyzed by the method of thermal/optical reflectance (TOR). The results showed that total carbon (TC), OC and EC emissions for PM_2.5 from diesel fuel were generally reduced by the DOC. For diesel fuel, TC emissions decreased 22%–32% after the DOC depending on operating modes. The decrease in TC was attributed to 35%–97% decrease in OC and 3%–65% decrease in EC emissions. At low load, a significant increase in the OC/EC ratio of PM_2.5 was observed after the DOC. The effect of the DOC on the carbonaceous compositions in PM_2.5 from B20 showed different trends compared to diesel fuel. At low load, a slight increase in EC emissions and a significant decrease in OC/EC ratio of PM_2.5 after DOC were observed for B20.     

Reduction of hexavalent chromium with scrap iron in a fixed bed reactor

The reduction of hexavalent chromium by scrap iron was investigated in continuous long-term fixed bed system. The effects of pH, empty bed contact time (EBCT), and initial Cr(VI) concentration on Cr(VI) reduction were studied. The results showed that the pH, EBCT, and initial Cr(VI) concentration significantly affected the reduction capacity of scrap iron. The reduction capacity of scrap iron were 4.56, 1.51, and 0.57 mg Cr(VI)·g^-1 Fe⁰ at pH 3, 5, and 7 (initial Cr(VI) concentration 4 mg·L^-1, EBCT 2 min, and temperature 25°C), 0.51, 1.51, and 2.85 mg Cr(VI)·g^-1 Fe⁰ at EBCTs of 0.5, 2.0, and 6.0 min (initial Cr(VI) concentration 4 mg·L^-1, pH 5, and temperature 25°C), and 2.99, 1.51, and 1.01 mg Cr(VI)·g^-1 Fe⁰ at influent concentrations of 1, 4, and 8 mg·L^-1 (EBCT 2 min, pH 5, and temperature 25°C), respectively. Fe(total) concentration in the column effluent continuously decreased in time, due to a decrease in time of the iron corrosion rate. The fixed bed reactor can be readily used for the treatment of drinking water containing low amounts of Cr(VI) ions, although the hardness and humic acid in water may shorten the lifetime of the reactor, the reduction capacity of scrap iron still achieved 1.98 mg Cr⁶⁺·g^-1 Fe. Scanning electron microscope equipped with energy dispersion spectrometer and X-ray diffraction were conducted to examine the surface species of the scrap iron before and after its use. In addition to iron oxides and hydroxide species, iron-chromium complex was also observed on the reacted scrap iron.