脉冲等离子法烟气脱硫的放大实验

锅炉烟气进行脉冲等离子法脱硫的扩大实验，得到与模拟烟气实验相近的结果。研究表明，脉冲等离子法对锅炉烟气中的ＳＯ２去除率可达９５％以上，烟气在反应器内的停留时间（ｔｓ）、脉冲电源的放电功率（Ｐ）和添加ＮＨ３等条件，对脱硫效率９η）有较大影响。ｔｓ、Ｐ越大、η越高。处理烟气量（Ｑ）、能耗（Ｐ）与η存在函数关系：η＝１１８．０（Ｐ／Ｑ）＾０．１１１１。烟气中加入适量ＮＨ３，对脱硫效率有显著提高，以ＮＨ３     

高镁铝合金在喷射成形过程中显微组织的变化

研究了高镁铝合金在喷射成形过程中显微组织的变化。沉积态高镁铝合金基体呈全部等轴晶组织并存在少量显微孔洞是沉积态组织的主要特征。分析了等轴晶组织和显微孔洞在喷射成形中生成的机制。     

从废水中回收磷的主要方法和常见工艺

磷污染是引起水体富营养化的重要原因,磷资源紧缺是我们即将面对的事实,同时解决这两方面问题的办法就是必须从含磷废水中回收磷。文章叙述从废水中回收磷的主要方法和原理,并介绍常见工艺流程。     

聚合硫酸铁和聚合硫酸铝的配伍和性能研究

将聚合硫酸铁 (PFS)与聚合硫酸铝 (PAS)按一定比例混合 ,即可制得一类具有不同铝铁含量的新型净水剂——聚合硫酸铁铝 (PFAS)混合液 ,分析、检测了几种 PFAS的性质及其净水性能。结果表明 ,PFAS的综合性能优于 PFS和PAS,更能适应原水水质的变化 ,其中尤以铝铁分子摩尔比为 0 .64的 PFAS性能最优。     

COD/SO_4~(2-)值对硫酸盐还原率的影响

研究利用 UASB反应器考察了 COD和硫酸盐浓度的比值对硫酸盐还原的影响 ,同时分析了硫酸盐还原菌和产甲烷菌对COD的竞争情况 .发现在 HRT为 3.8h,SO2 -4 负荷为 6～ 7kg· ( m3· d) - 1 ,SO2 -4 浓度为 1 0 0 0 mg· L- 1 条件下 :1在 COD不足时 ,SRB与 MPB在竞争中占微弱优势 ;对于产甲烷活性比较好的厌氧污泥要经过较长的时间 ,SRB才能确立优势菌种的地位 .2 COD/ SO2 -4 比值决定了 SO2 -4 的去除率 .比值等于 2时 ,SO2 -4 的还原率在 95%以上 ;当比值为 1 .5时 ,SO2 -4 还原率为 75% ;当比值为 1时 ,SO2 -4 的还原率为 60 % .     

Catalytic oxidation effect of MnSO4 on As(III) by air in alkaline solution

The catalytic oxidation effect of MnSO₄ on As(III) by air in an alkaline solution was investigated. According to the X-ray diffraction (XRD), scanning electron microscope-energy dispersive spectrometer (SEM-EDS) and X-ray photoelectron spectroscopy (XPS) analysis results of the product, it was shown that the introduction of MnSO₄ in the form of solution would generate Na_0.55Mn₂O₄·1.5H₂O with strong catalytic oxidation ability in the aerobic alkaline solution, whereas the catalytic effect of the other product MnOOH is not satisfactory. Under the optimal reaction conditions of temperature 90°C, As/Mn molar ratio 12.74:1, air flow rate 1.0 L/min, and stirring speed 300 r/min, As(III) can be completely oxidized after 2 hr reaction. The excellent catalytic oxidation ability of MnSO₄ on As(III) was mainly attributed to the indirect oxidation of As(III) by the product Na_0.55Mn₂O₄·1.5H₂O. This study shows a convenient and efficient process for the oxidation of As(III) in alkali solutions, which has potential application value for the pre-oxidation of arsenic-containing solution or the detoxification of As(III).     

溶济萃取法处理含硫酸及硫酸盐的废水

采用溶剂萃取法处理含硫酸及硫酸盐的工业废水，主产优质农用硫酸钾，副产氯化铵和氮钾复合肥，整个工艺过程基本无三废排放，实现了对该废水的综合有效治理。     

Microbial cycling of iron and sulfur in acidic coal mining lake sediments

Lakes caused by coal mining processes are characterized by low pH, low nutrient status, and high concentrations of Fe(II) and sulfate due to the oxidation of pyrite in the surrounding mine tailings. Fe(III) produced during Fe(II) oxidation precipitates to the anoxic acidic sediment, where the microbial reduction of Fe(III) is the dominant electron-accepting process for the oxidation of organic matter, apparently mediated by acidophilic Acidiphilium species. Those bacteria can reduce a great variety of Fe(III)-(hydr)oxides and reduce Fe(III) and oxygen simultaneously which might be due to the small differences in the redox potentials under low pH conditions. Due to the absence of sulfide, Fe(II) formed in the upper 6 cm of the sediment diffuses to oxic zones in the water layer where itcan be reoxidized by Acidithiobacillus species. Thus, acidic conditions are stabilized by the cycling of iron which inhibits fermentative and sulfate-reducing activities. With increasing sediment depth, the amount of reactive iron decrease, the pH increases above 5, and fermentative and as yet unknown Fe(III)-reducing bacteria are also involved in the reduction of Fe(III). Sulfate is reduced apparently by the activity of spore-forming sulfate reducers including new species of Desulfosporosinus that have their pH optimum similar to in situconditions and are not capable of growth at pH 7. However, generation of alkalinity via sulfate reduction is reduced by the anaerobic reoxidation of sulfide back to sulfate. Thus, the microbial cycling of iron at the oxic-anoxic interface and the anaerobic cycling of sulfur maintains environmental conditions appropriate for acidophilic Fe(III)-reducing and acid-tolerant sulfate-reducing microbial communities.     

两相UASB反应器处理含高浓度硫酸盐黑液

两相UASB反应器处理含高浓度硫酸盐黑液,酸化相为8.87L的普通升流式反应器,甲烷相为28.75L的UASB反应器,系统温度(35±1)℃。当酸化相进水COD为(6.771～11.057)g/L,SO42-为(5.648～8.669)g/L,pH值为5.5时,整个系统COD去除率平均值为74.42%;系统对负荷的冲击有较强的耐受能力。     

玉米芯为碳源实现酸性矿山废水生物处理

引入了一种新的碳源——玉米芯，对SRB法处理酸性矿山废水进行了更加深入的探索，分析了各种参数条件对s暖一还原效果的影响，确定了常温下这种碳源所需要的最适宜工况条件，探讨了硫酸盐矿山废水的水质资源化问题，并对山西矿山废水的生物治理进行了可行性实验验证。实验证明，玉米芯为碳源时，矿山废水中SO^2-4的出水值可达221．1mg／L，金属离子的浓度也都达到了生活饮用水的质量标准，所以玉米芯可作为酸性矿山废水资源化生物处理的合适有效碳源。