黄土丘陵区坡面水蚀对降雨和下垫面微观格局的响应

黄土高原严重的土壤侵蚀是降雨和复杂脆弱的下垫面共同作用的结果.以微型小区尺度上(1.2 m×1.2 m;2 m×1.2m)模拟降雨技术为基本研究手段,定量刻画了降雨量和降雨强度等基本降雨特征值对定西安家沟自然坡面上荒草、沙棘中位、沙棘下位、沙棘上位、结皮裸地和裸地等不同植株微观格局及其处理下的水蚀过程的影响.主要取得以下结果:①雨强和雨量对水蚀的发生均能产生显著影响,但以雨强的影响力更大;②前期土壤含水量与产流时间显著负相关,而与径流量和侵蚀量显著正相关.前期含水量相同时,不同植株微景观格局对产流时间发挥了关键作用;③不同植株及其微观格局遏制地表径流的能力迥异.在50～60 mm.h-1的大雨强作用下,有沙棘覆盖的小区径流系数仅为5%～8%,荒草地为25%,结皮裸地为45%,而裸地则高达63%;④有沙棘覆盖的小区中,沙棘在小区中所处的具体位置对于水土流失效应又极为重要,以沙棘下位的水土保持效果最好.     

鲁西平原微咸水资源的开发意义

鲁西平原处于黄泛平原的尾闾地段,常受旱涝盐咸多种危害。本文分析了浅层微咸水的形成、水质及动态特征,对水质、水量进行了评价,探讨了开发利用微咸水的可能性及灌溉效益。农业上开采浅层微咸水,无疑对扩大地下水资源及促进鲁西平原水、土环境的良性循环有重大意义。     

酸化油水解废水脱酸处理工艺研究

酸化油是生产生物柴油的原料,其生产过程中产生的水解废水有机物含量高且具有强酸性,直接排放会严重污染环境。因此,对酸化油水解废水处理工艺进行研究有重要意义。通过对酸化油水解废水脱酸处理的条件及影响因素进行研究,并通过L9(34)正交实验确定了脱酸的最佳工艺条件。pH值为10,搅拌时间为15 min,温度为30℃是脱酸处理的最佳条件。     

高浓度钻井废泥浆处理工艺的试验研究

为实现钻井泥浆无害化处理,提出了酸化破胶-固液分离-催化氧化-微生物降解的处理方法,并采用钻井现场废泥浆进行了系列试验研究。结果表明:泥浆密度调节为1.15 kg/dm3,酸化pH≤3,固液分离效果最佳;过滤分离后固相浸毒液达到国家排放标准;液相经Fenton氧化、微生物降解后,COD将降低到110 mg/L以下。该方法运行成本低,处理彻底无隐患,为进一步工业化试验奠定了基础。     

热电厂再生水回用工艺分析

介绍一套日处理量14 400 t的再生水回用工艺,该工艺应用预处理+反渗透工艺深度处理二级城市污水并将产水回用于热电厂的循环冷却水及锅炉补给水的源水,分析了该工艺关键单元的特点。运行结果表明:该工艺可行,产水各项指标满足该热电厂对回用水的要求。最后,对工艺运行过程中出现的问题提出解决办法和改进建议。     

攀钢炼钢厂提钒转炉浊环水水质稳定研究

在对转炉提钒浊环水质状况进行分析化验的基础上提出了水质调整措施,实施后有效地稳定了提钒浊环水质,改善了因提钒浊环酸性水质导致的缺陷,较好地满足了生产需要。     

Partitioning of water soluble organic carbon in three sediment size fractions： Effect of the humic substances

Water soluble organic carbon (WSOC) in sediments plays an important role in transference and transformation of aquatic pollutants. This article investigated the inherent mechanisms of how sediemnt grain size affect the partitioning coeffcient (k) of WSOC. Influences of NaOH extracted humic substances were particularly focused on. Sediments were sampled from two cross-sections of the middle Yellow River and sieved into three size fractions (< 63 μm, 63-100 μm, and 100--300 μm). The total concentration of WSOC in sediments (CWSOC) and k were estimated using multiple water-sediment ratio experiments. Results show that CWSOC ranges from 0.012 to 0.022 mg/g, while k ranges from 0.8 to 3.9 L/kg. Correlations between the spectrum characteristics of NaOH extracted humic substances and k were analyzed. Strong positive correlations are determined between k and the aromaticity indicators of NaOH extracted humic substances in different sediment size fractions. Comparing with finer fractions (< 63 μm), k is higher in larger size fractions (63--100 and 100--300 μm) related to higher aromaticity degree of NaOH extracted humic substances mostly. While negative relationship between k and the area ratio of fourier transform infrared spectroscopy (FT-IR) at 3400 and 1430 cm-1 implied that the lowest k was related to the highest concentration of the acidic humic groups in particles < 63 μm. WSOC in finer fractions (< 63 μm) is likely to enter into pore water, which may further accelerate the transportation of aquatic contaminants from sediment to water.     

Combined alkaline and ultrasonic pretreatment of sludge beforeaerobic digestion

Alkaline and ultrasonic sludge disintegration can both be used as pretreatments of waste activated sludge (WAS) for improving the subsequent anaerobic or aerobic digestion. The pretreatment has been carried out using different combination of these two methods in this study. The effect was evaluated based on the quantity of soluble chemical oxygen demand (SCOD) in the pretreated sludge as well as the degradation of organic matter in the following aerobic digestion. For WAS samples with combined pretreatment, the released COD was in high level than those with ultrasonic or alkaline treatment. When combined with the same ultrasonic treatment, NaOH treatment resulted in more solubilization of WAS than Ca(OH)2. For combined NaOH and ultrasonic treatments with different sequences, the released COD were in the order: simultaneous treatment > ultrasonic treatment following NaOH treatment > NaOH treatment following ultrasonic treatment. For simultaneous treatment, low NaOH dosage (100 g/kg dry solid), short duration (30 min) of NaOH treatment, and low ultrasonic specific energy (7 500 kJ/kg dry solid) were beneficial for sludge disintegration. Using combined NaOH and ultrasonic pretreatment with the optimium parameters, the degradation efficiency of organic matter was increased from 38.0% to 50.7%, which is much higher than with ultrasonic (42.5%) or with NaOH pretreatment (43.5%) in the subsequent aerobic digestion at the same retention time.     

A bioaugmentation failure caused by phage infection and weak biofilmformation ability

Two biological aerated filters (BAF) were setup for ammonia removal treatment of the circulation water in a marine aquaculture. Oneof the BAFs was bioaugmented with a heterotrophic nitrifying bacterium, Lutimonas sp. H10, where the ammonia removal was notimproved and the massive inoculation was even followed by a nitrification breakdown from day 9 to 18. The nitrification was remainedstable in control BAF operated under the same conditions. Fluorescent in situ hybridization (FISH) with rRNA-targeted probes andcultivable method revealed that Lutimonas sp. H10 almost disappeared from the bioaugomented BAF within 3 d, and this was mainlydue to the infection of a specific phage as revealed by flask experiment, plaque assay and transmission electron observation. Analysesof 16S rRNA gene libraries showed that bacterial groups from two reactors evolved di erently and an overgrowth of protozoa wasobserved in the bioaugmented BAF. Therefore, phage infection and poor biofilm forming ability of the inoculated strain are the mainreasons for bioaugmentation failure. In addition, grazing by protozoa of the bacteria might be the reason for the nitrification breakdownin bioaugmented BAF during day 9–18.     

Development and application of a two-dimensional water quality model for theDaqinghe River Mouth of the Dianchi Lake

Water quality models are important tools to support the optimization of aquatic ecosystem rehabilitation programs and assess their efficiency. Basing on the flow conditions of the Daqinghe River Mouth of the Dianchi Lake, China, two-dimensional water quality model was developed in the research. The hydrodynamics module was numerically solved by the alternating direction iteration (ADI) method. The parameters of the water quality module were obtained through the in situ experiments and the lab analyses that were conducted from 2006 to 2007. The model was calibrated and verified by the observation data in 2007. Among the four modelled key variables that were water level, CODcr, NH3-N and PO4-P, the minimum value of the coefficient of determination (CoD) was 0.69, which mean the model performed reasonably well. The developed model was then applied to simulate the water quality changes at the downstream cross-section assuming that the designed restoration programs were implemented. According to the simulated results, the restoration programs could cut down the loads of CODcr and PO4-P about 15%, however, they would have very little effect on the NH3-N removal. Besides, the water quality at the outlet cross-section would be still in class V (3838-02), indicating more measures should be taken to further reduce the loads. The study demonstrated the capability of water quality models to support aquatic ecosystem restorations.