水力停留时间对阴离子交换膜生物反应器去除硝酸盐的影响

考察了水力停留时间(HRT)对阴离子交换膜生物反应器去除硝酸盐的影响。实验结果表明,当进水NO3-浓度在113.96~116.01 mg/L范围内,HRT从11.12 h降低到4.82 h,硝酸盐去除率降低,但出水中NO3--N浓度符合我国饮用水水质标准中10 mg/L的要求(NO3-浓度≤44.29 mg/L)。厌氧生物反应器具有良好的反硝化性能,出水NO3-浓度低于20 mg/L。硝酸盐膜通量随着HRT的增加而增加,出水pH值稳定在7左右。     

强力霉素在凹凸棒土上的吸附行为

通过等温吸附平衡法研究了强力霉素在凹凸棒土上的吸附行为,考察了pH、反应时间、离子强度和离子类型等因素对吸附的影响,探讨了吸附机理.结果表明,pH=8.5时,饱和吸附容量最大,为293.35μmol.g-1;强力霉素在凹凸棒土上的吸附可用Langmuir型等温方程和准二级动力学方程很好地拟合;离子强度对强力霉素的吸附影响不是很明显;0.05 mol.L-1NaOH能显著地将强力霉素从凹凸棒土上解吸下来.红外表征结果说明凹凸棒土对强力霉素的吸附可能是化学吸附,酸性条件下,强力霉素主要通过阳离子交换、静电作用、氢键作用等吸附在凹凸棒土上,部分H+可能通过强力霉素质子化吸附到凹凸棒土上.弱碱性条件下主要通过水桥接,与凹凸棒土层间阳离子配位以及结合于凹凸棒土边缘吸附位点达到吸附.     

Model of stomatal ammonia compensation point (STAMP) in relation to the plant nitrogen and carbon metabolisms and environmental conditions

Agricultural crops can be either a source or a sink of ammonia (NH₃). Most NH₃ exchange models developed so far do not account for the plants nitrogen (N) metabolism and use prescribed compensation points. We present here a leaf-scale simplified NH₃ stomatal compensation point model related to the plants N and carbon (C) metabolisms, for C₃ plants. Five compartments are considered: xylem, cytoplasm, apoplasm, vacuole and sub-stomatal cavity. The main processes accounted for are the transport of ammonium (NH₄⁺), NH₃ and nitrate (NO₃⁻) between the different compartments, NH₄⁺ production through photorespiration and NO₃⁻ reduction, NH₄⁺ assimilation, chemical and thermodynamic equilibriums in all the compartments, and stomatal transfer of NH₃.The simulated compensation point is sensitive to paramaters related to the apoplastic compartment: pH, volume and active transport rate. Determining factors are leaf temperature, stomatal conductance and NH₄⁺ flux to the leaf. Atmospheric NH₃ concentration seem to have very little effect on the compensation point in conditions of high N fertilization. Comparison of model outputs to experimental results show that the model underestimates the NH₃ compensation point for high N fertilization and that a better parametrisation of sensitive parameters especially active trasport rate of NH₄⁺ may be required.     

酸雨胁迫对木荷叶片气体交换和叶绿素荧光参数的影响

通过盆栽试验,研究了3种不同pH值（2.5、4.0、5.6）的模拟酸雨溶液对2年生木荷（Schima superba）幼苗叶片气体交换和荧光参数的影响。结果表明：在不同酸雨处理下,净光合速率和气孔导度日变化均呈＂双峰＂型,最大净光合速率和最高表观量子效率（AQE）变化趋势依次是pH4.0〉pH5.6〉pH2.5,说明pH4.0处理对木荷光合作用有促进作用;在不同酸雨处理下,PSⅡ原初光能转换效率（Fv/Fm）、PSⅡ潜在活性（Fv/Fo）和相对叶绿素含量均呈现出pH4.0〉pH5.6〉pH2.5的变化趋势,pH4.0酸雨处理下表现出最高值,说明适度降低酸雨pH值（pH4.0）并不会对木荷的光合系统活性造成损伤,反而有促进作用,表明木荷对酸雨有较强的适应能力。     

Optimization of phosphorus removal in uniFed SBR system for domestic wastewater treatment

The characteristic of phosphorus removal and appropriate change of the traditional operation modes were investigated in UniFed sequencing batch reactor (SBR) laboratory-scale apparatus (40 L), treating actual domestic wastewater with low ratios of C/N (2.57) and C/P (30.18), providing theoretical basis for actual application of wastewater treatment plant. UniFed SBR system with its unique operation mode had the distinct superiority of phosphorus removal. On this occasion, the effect of volumetric exchange ratio (VER) and the method of influent introduction for phosphorus removal were studied. When the carbon source became the limiting factor to phosphorus release, the higher the VER, the lower the phosphorus concentration in the effluent. Three different influent patterns, including one-time filling, four-time filling, and continuous filling with the same quantity of wastewater could increase the release rate of anaerobic phosphorus from 0.082 to 0.143 mg·P·(L·min)^-1. Appropriate change of the traditional operation modes could optimize the efficiency of phosphorus removal. When the feed/ decant time was extended from 2 h to 4 h, the phosphorous removal efficiency increased from 59.93% to 88.45% without any external carbon source. In the mode of alternation of anoxic-aerobic (A/O) condition, phosphorous removal efficiency increased from 55.07% to 72.27% clearly. The carbon source in the influent can be used adequately, and denitrifying phosphorus removal was carried out in anoxic stage 2 (A2). This mode was optimal for the treatment of actual domestic wastewater with low C/N and C/P ratios.     

A HYBRID COMPUTER PROGRAM FOR PREDICTING THE CHEMICAL QUALITY OF IRRIGATION RETURN FLOWS1

ABSTRACT. A hybrid computer program was developed to predict the water and salt outflow from a river basin in which irrigation is the major user of water. The model combines a chemical model which predicts the quality of water percolated through a soil profile with a general hydrologic model. The chemical model considers the reactions that occur in the soil, including the exchange of calcium, magnesium, and sodium cations on the soil complex, and the dissolution and precipitation of gypsum and lime. The chemical composition of the outflow is a function of these chemical processes within the soil, plus the blending of undiverted inflows, evaporation, transpiration, and the mixing of sub surface return flows with groundwater. The six common ions of western waters, namely calcium (Ca⁺⁺), magnesium (Mg⁺⁺), sodium (Na⁺), sulfate (SO₄⁼), chloride (Cl^?), and bicarbonate (HCO₃^?) were considered in the study. Total dissolved solids (TDS) outflow was obtained by adding the individual ions. The overall model operates on a monthly time unit. The model was tested on a portion of the Little Bear River basin in northern Utah. The model successfully simulated measured outflows of water and each of the six ions for a 24-month period. The usefulness of the model was demonstrated by a management study of the prototype system. For example, preliminary results indicated that the available water supply could be used to irrigate additional land without unduly increasing the salt outflow from the basin. With minor adjustments the model can be applied to other hydrologic areas.     

Quaternized agricultural by-products as anion exchange resins

The objectives of this study were the chemical modification of readily available, low-cost agricultural by-products to anion exchange resins and the selection of the best modified by-product for further use in anion removal. Resins were prepared through the quaternization of a series of 12 agricultural by-products with N-(3-chloro-2-hydroxypropyl) trimethylammonium chloride (CHMAC). Phosphate ion adsorption assays were conducted at pH 7 in order to compare adsorption properties among the by-products. Quaternized corn stover showed the highest phosphorus adsorption at 0.66 mmole/g. Since corn stover exhibited the best uptake of phosphate ion, it was compared to a commercially available, cellulose-based anion exchange resin. Additionally, adsorption capacities of quaternized corn stover for arsenate, chromate, and selenate were evaluated and adsorption efficiencies were determined in simulated wastewater samples. Our results indicate that modified corn stover demonstrates good adsorption uptake for arsenate and selenate and especially for chromate.     

中国与欧盟的航空安全信息分类法比较

为探讨中国和欧盟政府间进行航空安全信息交换的可行性,从中国和欧盟各自航空安全信息系统的信息结构和报告内容出发,对中国和欧盟的航空安全信息分类法进行比较。结果表明,两个分类法的信息结构是相同的,不同之处在于主题差异、部分差异和属性差异。笔者认为,虽然存在3种差异,但两个分类法都是基于国际民航组织航空安全信息分类法设计的,信息报告内容具有很大的相似性,因此,从信息内容上看,中欧进行航空安全信息交换是可行的。同时,对如何改进我国航空安全信息分类法提出了建议。     

阳离子交换树脂生产中废酸的回收利用及树脂质量控制

采用 酸套洗工艺代替传统的加水稀释洗涤工艺，成功地解决了阳离子交换树脂生产中废酸的回收利用问题，研究了采用新洗涤工艺后树脂变红的机理和防止对策，结果表明，树脂发红帅微生物的参与而引起的。采以完善洗涤 灭菌措施可防止树脂 ，从而确保了稀酸套洗工艺的顺利实施。     

Australian junior exploration floats, 2001–06, and their implications for IPOs

An analysis of 179 junior exploration floats, listed on the Australian Securities Exchange (ASX) between July 2001 and June 2006, helped to build a basic understanding of the strategy and business structure of these companies. The “typical” junior explorer raised A$4 million at initial public offering (IPO) to finance a 2-year, mainly greenfields exploration program. The capital raised at IPO entitled its investors to approximately half of the company, with the balance in the hands of the promoters, vendors and/or seed capital investors. Of the A$4 million raised at IPO, it intended to spend approximately two-thirds on exploration, while the remainder was absorbed in corporate overheads and the costs of the IPO. Once these were paid, ongoing corporate overheads averaged approximately 28% of its total operational expenditure. However, given an average total annual expenditure of approximately A$2.6 million, most juniors held insufficient capital reserves to meet operational costs beyond a time frame of 2 years. As at October 2006, 9% of the companies were in the process of mine construction, whereas 6% had made it to producer status. The lead time from listing to production ranged from 1.5 to 53 months, giving a median of 28 months.