Sulphate, Nitrogen and Base Cation Budgets at 21 Forested Catchments in Canada, the United States and Europe

To assess the concern over declining base cation levels in forest soils caused by acid deposition, input-output budgets (1990s average) for sulphate (SO₄), inorganic nitrogen (NO₃-N; NH₄-N), calcium (Ca), magnesium (Mg) and potassium (K) were synthesised for 21 forested catchments from 17 regions in Canada, the United States and Europe. Trend analysis was conducted on monthly ion concentrations in deposition and runoff when more than 9 years of data were available (14 regions, 17 sites). Annual average SO₄ deposition during the 1990s ranged between 7.3 and 28.4 kg ha⁻¹ per year, and inorganic nitrogen (N) deposition was between 2.8 and 13.8 kg ha⁻¹ per year, of which 41–67% was nitrate (NO₃-N). Over the period of record, SO₄ concentration in deposition decreased in 13/14 (13 out of 14 total) regions and SO₄ in runoff decreased at 14/17 catchments. In contrast, NO₃-N concentrations in deposition decreased in only 1/14 regions, while NH₄-N concentration patterns varied; increasing at 3/14 regions and decreasing at 2/14 regions. Nitrate concentrations in runoff decreased at 4/17 catchments and increased at only 1 site, whereas runoff levels of NH₄-N increased at 5/17 catchments. Decreasing trends in deposition were also recorded for Ca, Mg, and K at many of the catchments and on an equivalent basis, accounted for up to 131% (median 22%) of the decrease in acid anion deposition. Base cation concentrations in streams generally declined over time, with significant decreases in Ca, Mg and K occurring at 8, 9 and 7 of 17 sites respectively, which accounted for up to 133% (median 48%) of the decrease in acid anion concentration. Sulphate export exceeded input at 18/21 catchments, likely due to dry deposition and/or internal sources. The majority of N in deposition (31–100%; median 94%) was retained in the catchments, although there was a tendency for greater NO₃-N leaching at sites receiving higher (<7 kg ha^-1 per year) bulk inorganic N deposition. Mass balance calculations show that export of Ca and Mg in runoff exceeds input at all 21 catchments, but K export only exceeds input at 16/21 sites. Estimates of base cation weathering were available for 18 sites. When included in the mass balance calculation, Ca, Mg and K exports exceeded inputs at 14, 10 and 2 sites respectively. Annual Ca and Mg losses represent appreciable proportions of the current exchangeable soil Ca and Mg pools, although losses at some of the sites likely occur from weathering reactions beneath the rooting zone and there is considerable uncertainty associated with mineral weathering estimates. Critical loads for sulphur (S) and N, using a critical base cation to aluminium ratio of 10 in soil solution, are currently exceeded at 7 of the 18 sites with base cation weathering estimates. Despite reductions in SO₄ and H⁺ deposition, mass balance estimates indicate that acid deposition continues to acidify soils in many regions with losses of Ca and Mg of primary concern. The U.S. Government's right to retain a non-exclusive, royalty free licence in and to any copyright is acknowledged. The Canadian Crown reserves the right to retain a non-exclusive, royalty free licence in and to any copyright.     

微电解-水解酸化/接触氧化工艺处理染化废水的研究

采用微电 解 Ｈ／ Ｏ 工艺对染 料化 工 废水 进行 了 处理 研究 ，结 果表 明 以微 电解 和 水解 酸 化作预处理 ，可使废 水的 Ｂ Ｏ Ｄ５／ Ｃ Ｏ Ｄ Ｃｒ 的比由 ０２５ 提高 到０５ ０ 左 右，平 均 增加 ５０ ％ 。通 过加 酸， 可提高微电 解的去除 效果，在 进水 Ｃ Ｏ Ｄ Ｃｒ 为４ １００ ～４ ３００ ｍ ｇ／ Ｌ，色度 为３ ４００ ～３ ６００（ 倍） 范围内 ，系统对 Ｃ Ｏ Ｄ Ｃｒ 和色度 的去除效 果分别 可达到９７ ５ ％ 和９８３ ％     

感光胶片废水的水解酸化—好氧处理工艺试验

对感光胶片有机生产废水处理工艺进行了方法采用水解酸化－好氧串联工艺和传统活性污泥法两种方法并进行对照。结果经水解酸化处理，废水的ＢＯＤ５／ＣＯＤｃｒ可提高至０．５４－０．５６，平均增加了１７％左右，证实了水解酸化菌在该工艺条件下具有搞高效片废水可生化性的功能。     

物化-生化组合工艺处理化纤厂浆粕综合废水

根据化纤厂浆粕综合废水的水质特点 ,选择采用中和曝气 水解酸化 生物接触氧化 絮凝沉降处理工艺。实验结果表明 :当浆粕综合废水进水CODCr浓度 310 0～ 34 6 0mg/L ,BOD5浓度 10 2 0～ 142 0mg/L范围内时 ,处理后水质可达到《污水综合排放标准》GB8978 96中化纤浆粕工业二级排放标准。     

可发性聚苯乙烯废水处理工程的设计与运行

介绍了采用中和混凝 水解酸化 生物接触氧化 化学除磷工艺对可发性聚苯乙烯 (EPS)废水的处理工艺。在废水中的CODCr、TP、SS、NH3 N分别为 194 0mg L、112mg L、5 92mg L、2 3 6mg L的条件下 ,废水经过处理后 ,出水CODCr、TP、SS、NH3 N分别为 70mg L、0 38mg L、2 6mg L、0 32mg L ,均可达到《污水综合排放标准》中的一级标准 ,废水中CODCr、TP、SS、NH3 N的平均去除率分别为 96 4 %、99 3%、95 6 %、98 6 %。     

生化-砂滤-光催化氧化处理苎麻脱胶废水

根据苎麻脱胶废水的水质特点 ,选择了水解酸化 -接触氧化 -砂滤 -光催化氧化处理工艺 ,结果表明 ,出水水质达到了GB8978 1996二级排放标准 ,大部分指标达到了一级排放标准。该工艺具有针对性强、占地面积少、运行稳定、处理费用低、操作管理方便、无二次污染等优点 ,值得推广应用     

印染废水的治理及相关问题

文中讨论了水解酸化-好氧-生物炭及水解酸化-好氧-气浮工艺处理印染废水时的优缺点，采用上述工艺印染污水，可使CODcr：1000mg／L、BOD5：300mg／L、ss：300mg／L、色度：〉300倍的印染废水达标排放.     

水解酸化-好氧工艺处理感光材料有机废水研究

感光材料有机生产废水含有多种合成有机物，其BOD5／CODer比值为0．46～0．48，可生化性良好，经水解酸化处理后该废水的BOD5／CODcr的比值可提高至0．54～056，平均增加了17％左右。水解酸化－好氧串联工艺对该废水总的处理效果表明：在废水CODer进水浓度2000～2500mg／L范围内，CODer总去除率可达95％左右，BOD5总去除率可达97％左右；水解酸化后好氧生化系统的动力学半速度常数Ks＝103mg／L，最大比降解速度K＝5．0／日。     

水解酸化—厌氧工艺处理高浓度抗生素废水研究

研究了水解酸化与厌氧消化组合工艺处理高浓度抗生素废水,结果表明,水解酸化反应器最大CODcr容积负荷达到 16.84kg/m3·d,复合厌氧反应器CODcr容积负荷达到8.57kg/m3·d;系统进水SO42-浓度为1325mg/L,CODcr/SO42-值最低达到 3;CODCr与SO42-总去除率分别为75.5％和95.2％,对各种抑制物质和冲击负荷表现出很好的适应性。     

HA-SBR法在制药废水中的应用

介绍SBR法在制药废水中的应用及工艺流程.通过处理COD从3600mg/l降到130mg/l.COD总去除率达到96%,出水可以达标排放.