AAS与ICP—AES间接测定天然水中硫酸盐

本文以ＳＯ４＾２－与过量Ｂａ＾２＋形成ＢａＳＯ４沉淀反应为基础，较详细地讨论了反应条件，从而拟定了用ＡＡＳ和ＩＣＰ－ＡＥＳ间接测定天然水中ＳＯ４＾２－的方法、确定了方法的精密度，ＡＡＳ法的ＲＳＤ％为１．５，ＩＣＰ－ＡＥＳ法为３．２， 两种方法对比分析的结果接近，误差为１．０％（相对）。用于天然水中ＳＯ４＾２－的测定，获得满意的结果。     

中药川附子痕量砷的测定

本文报道了以ＨＮＯ３ － ＨＣｌＯ４ 混酸消化、Ｈ２ＳＯ４ － ＫＩ－ Ｔｅ（ Ⅳ） 体系极谱法测定中药川附子中的砷。该方法使样品消化过程的砷损失大为减少并简化了分析过程。样品中砷含量在０－２ ～０－６μｇ·ｇ－ １ ,回收率８４ ％ ～１０８ ％ 。     

自动电位滴定法测定气田废水中的C1~-

利用电位滴定法在７１６ＤＭＳ型自动电位滴定仪上实现对气田废水中Ｃ１－的快速、灵敏、准确测定,避免了色度、浊度的干扰。对方法的检出限、标样和实际水样精密度、准确度,进行了全面的测定分析,并与硝酸银滴定法进行了对比。氯化物的检出限为０．３２ｍｇ／Ｌ;相对标准偏差小于等于２．１％,加标回收率在９８．９％１０１％范围内,对同一标样和实际样品的测定两种方法的结果吻合较好。     

COD_(Cr)测定中排除氯离子干扰的进一步探讨

废水中化学需氧量的测定采用重铬酸钾法［１］,大多数情况下都存在Ｃｌ－干扰,其排除方法用ＨｇＳＯ４掩蔽,通过实验探讨不用剧毒药品ＨｇＳＯ４掩蔽Ｃｌ－的干扰,而用ＣＯＤＣｒ总量减去Ｃｌ－的量。实验结果表明：当测定化学需氧量较低而Ｃｌ－含量高的水样时,即使采用掩蔽Ｃｌ－也会产生较大的误差,而用测定值减去０．２２６［Ｃｌ－］之值更接近真值。     

分光光度法测定COD_(Cr)的试验条件选择

用分光光度法测定水中化学需氧量ＣＯＤＣｒ,通过正交试验选择氧化的最佳选择。试验结果表明对ＣＯＤＣｒ值为５０～１０００ｍｇ／Ｌ的水样：氧化剂Ｋ２Ｃｒ２Ｏ７用量为０．２０～０．４０ｍｏｌ／Ｌ,催化剂Ａｇ２ＳＯ４用量为１０ｇ／ＬＨ２ＳＯ４,消解时间１０ｍｉｎ,加热温度１８０℃。用ＣＯＤＣｒ为１３８ｍｇ／Ｌ的质控标样进行验证试验,其绝对误差为０．５～３．０ｍｇ／Ｌ。与标准方法相比用分光光度法测定ＣＯＤＣｒ具有分析误差小,省时、省力,节约药剂的特点。     

AAS与ICP－AES间接测定天然水中硫酸盐

本文以与过量形成ＢａＳＯ＿４沉淀反应为基础，较详细地讨论了反应条件、从而拟定了用ＡＡＳ和ＩＣＰ－ＡＥＳ间接测定天然水中的方法、确定了方法的精密度，ＡＡＳ法的ＲＳＤ％为１．５，ＩＣＰ－ＡＥＳ法为３．２．两种方法对比分析的结果接近，误差为１．０％（相对）。用于天然水中的测定，获得满意的结果。     

示差脉冲阳极溶出伏安法测定中药川附子痕量铅镉

本文报道了以ＨＮＯ３－ＨＣｌＯ４湿法消化、醋酸盐介质法差脉冲阳极溶出伏安法测定中药川附子中的铅镉。样品中铅镉含量分别在０．２－０．４μｇ．ｇ＾－１、０．０３－０．１６μｇ．ｇ＾－１,回收率９０－１１０％。     

简易流动注射仪化学发光法测定水环境中的铵态氮

在０．１Ｍ的碱性条件下，ＮＢＳ（Ｎ—溴代丁二酰亚　胺）在荧光素的增敏作用下氧化氯化铵，产生强的化学发光。基于此本文详细研究了其反应　的特性和影响因素，在优化的实验条件下体系对氯化铵的测定范围为１．０×１０－７～１　．５×１０－５ｇ／ｍＬ，检出限为３．６×１０－８ｇ／ｍＬ，对５．０×１０－６ｇ／ｍＬ氯化铵　进行１１次平行测定，其ＲＳＤ为２．８％。将本法用于环境水样中ＮＨ＋４的分析，并与常规的　方法进行对照，获得了满意的结果。     

UASB—Fe反应器处理城市污水中试研究

本文对ＵＡＳＢ－Ｆｅ装置处理城市污水进行了中试研究，结果表明，当厌氧ＨＲＴ３－４小时，进水浓度总ＣＯＤｃｒ为２４１．２－４０２．３ｍｇ／ｌ，溶ＢＯＤ５为８０．６－１３６．８ｍｇ／ｌ，ＳＳ为１７０．８－１８９．８ｍｇ／ｌ时，其平均去除率依次为４２．１－５６．６％，６４．０－３９．８％和７２．９－６５．４％。讨论了厌氧ＨＲＴ，进水浓度，温度等因子对厌氧处理效果的影响情况。浅析了铁填料层在城市污水处理中     

纳氏试剂光度法测定废水中氨氮的问题讨论

应用纳氏试剂比色法测定废水中的氨氮时,水样显色后稳定时间短,影响测定结果的准确性,针对这一问题进行了实验研究。实验中对主要影响因素Ｉ－和ＯＨ－的浓度变化进行了条件实验,结果表明选用所配的Ⅲ型纳氏试剂（ＫＩ含量为７．５ｇ）,可获得稳定的有色胶体,也可采用Ⅰ型纳氏试剂（ＫＩ含量为７．０ｇ）、在中和硼酸后再多加２ｍＬＮａＯＨ（１ｍｏｌ／Ｌ）,也可获得稳定的有色胶体。     

废钻井液脱稳与ξ电位关系的研究

为了寻求钻井液脱稳剂H2SO4的最佳用量,采用JS94B型微电泳仪对钻井液体系的ξ电位进行了研究。实验中测定了钻井液在不同稀释倍数下ξ电位的变化情况,研究了脱稳剂H2SO4加量与钻井液临界ξ电位的关系,从而得出H2SO4加入量以045mL/100g废钻井液为宜,其临界ξ电位为-752997mV。     

城市污水Al盐化学除磷的试验研究

针对新疆地区污水厂总磷去除效率有限,出水总磷存在超标排放风险的问题。试验中采用自配不同总磷含量的生活污水,通过小试试验,投加AlCl3进行试验室模拟化学除磷试验。研究结果表明:进水总磷浓度为2～4mg/L时,投加AlCl3/TP质量比为8.6;进水总磷浓度为6mg/L时,投加AlCl3/TP质量比上升到13.1,出水总磷浓度均<0.5mg/L,AlCl3投加不会改变污水的pH值,化学沉淀最佳时间为30min。建议设计除磷沉淀池的停留时间为25min～30min。     

高氯低COD废水中COD的测定

以某污水厂的高氯低COD生化出水为研究对象,探讨了硫酸汞加入量、K2Cr2O7溶液浓度、反应酸度、取水样量等参数对COD测定的影响,探讨消除该厂Cl-干扰最简单有效方法,结果表明:控制硫酸汞与氯离子比为15∶1(质量比)、K2Cr2O7浓度为0.18 mol/L、水样稀释0.75倍、Ag2SO4-H2SO4加入量为28mL,皆可有效减少氯离子的干扰。该方法相对氯气校正法,操作简单、准确可靠。     

废弃钻井液生物絮凝剂筛选实验研究＊

针对川渝地区废弃钻井液成分复杂,高COD,高色度的特点及现有的化学法、固化处理等技术存在的缺陷,提出微生物法处理废弃钻井液的思路。通过实验筛选出最佳C源为蔗糖、最佳N源为N2的菌株,并通过正交实验确定CaCl2用量0.1%,pH7.0,絮凝剂用量1.0%的最佳絮凝条件。经现场配合筛选出的菌株对废弃钻井液进行处理,COD去除率可达到72.4%。     

Release dynamic process identification for a cement based material in various leaching conditions. Part I. Influence of leaching conditions on the release amount

In this paper we investigate at laboratory scale the influence of the liquid/solid leaching conditions on the release of different chemical species from a reference porous material obtained by solidification of PbO and CdO with Portland cement. The pH influence on the dissolution of pollutants and the initial pore solution composition (target elements: Na(+), K(+), Ca(2+), Pb(2+), Cd(2+), SO(4)(2-)) were assessed by applying a methodology consisting of two equilibrium leaching tests, the Acid Neutralization Capacity (ANC) and the Pore Water (PW) tests and geochemical modelling. Samples of the same material were submitted in parallel to four different dynamic leaching tests in order to determine the influence of the sample shape (monolithic or granular) and eluate hydrodynamics (instantaneous L/S ratio, eluate renewal) on the leaching of the target elements. The comparison criteria were the eluate saturation state, the cumulative release and the released flux. Generally, the eluates obtained in the tests applied on granular material were more concentrated, even saturated for the eluate pH value with respect to Ca(2+), Pb(2+) and SO(4)(2-). The consequence of the eluate saturation is the slowing down effect on the dynamic release. The highest released flux was observed for the Monolith Leaching Test (MLT) involving the highest instantaneous L/S ratio and the lowest solid/liquid exchange surface and for which no saturation was observed, except Pb(2+) and SO(4)(2-) in some eluates. The maximum cumulative released-mass was obtained for the Column Leaching Test (CLT) applied on granular material having the highest exchange surface, the lowest instantaneous L/S and a continuous input flow of the leachant. The experimental results demonstrate the significance of the liquid/solid contact type which is also a scenario specific parameter.     

Anaerobic treatment of sulfate-rich wastewater in an anaerobic sequential batch reactor (AnSBR) using butanol as the carbon source

Biological sulfate reduction was studied in a laboratory-scale anaerobic sequential batch reactor (14 L) containing mineral coal for biomass attachment. The reactor was fed industrial wastewater with increasingly high sulfate concentrations to establish its application limits. Special attention was paid to the use of butanol in the sulfate reduction that originated from melamine resin production. This product was used as the main organic amendment to support the biological process. The reactor was operated for 65 cycles (48 h each) at sulfate loading rates ranging from 2.2 to 23.8 g SO(4)(2-)/cycle, which corresponds to sulfate concentrations of 0.25, 0.5, 1.0, 2.0 and 3.0 g SO(4)(2-) L(-1). The sulfate removal efficiency reached 99% at concentrations of 0.25, 0.5 and 1.0 g SO(4)(2-) L(-1). At higher sulfate concentrations (2.0 and 3.0 g SO(4)(2-) L(-1)), the sulfate conversion remained in the range of 71-95%. The results demonstrate the potential applicability of butanol as the carbon source for the biological treatment of sulfate in an anaerobic batch reactor.     

Gas dynamics in eutrophic lake sediments affected by oxygen, nitrate, and sulfate

In many freshwater ecosystems, the contents of NO3- and SO4(2-) have increased, whereas O2 has been depleted due to the increased acid and nutrient loads. These changes may affect carbon turnover and the dynamics of the major greenhouse gases CO2, CH4, and N2O. We studied the effects of O2, NO3-, and SO4(2-) availability on carbon mineralization, and fluxes of CO2, CH4, and N2O in the sediments of hyper-eutrophic Lake Kev?t?n, Finland. Undisturbed sediment cores from the deep (9 m) and shallow (4 m) profundal were incubated in a laboratory microcosm with oxic and anoxic water flows with NO3- or SO4(2-) concentrations of 0, 30, 100, 300, and 2000 microM. The carbon mineralization rate (i.e., the sum of released CO2-C and CH4-C) was not affected by the oxidants. However, the oxidants did change the pathways of carbon degradation and the release of CH4. All of the oxidants depressed CH4 fluxes in the shallow profundal sediments, which had low organic matter content. In the deep profundal sediments rich in organic matter, the CH4 release was reduced by O2 but was not affected by SO4(2-) (the effect of NO3- was not studied). There was an increase in N2O release as the overlying water NO3- concentration increased. Anoxia and highly elevated NO3- concentrations, associated with eutrophication, increased drastically the global warming potential (GWP) of the sedimentary gases in contrast to the SO4(2-) load, which had only minor effects on the GWP.     

常用钻井液填加剂对钻井污水化学需氧量的影响

针对石油工业钻井污水化学需氧量（ＣＯＤ）严重超标的状况,从分析测定目前油田常用的８种钻井液添加剂的ＣＯＤ入手,探讨了钻井液添加剂对钻井污水的影响。实验结果表明：８种钻井液添加剂按油田现场配比复配后,对钻井污水ＣＯＤ的影响程度各不相同,其大小依次为：柴油、ＨＰＡＮ、磺化沥青、ＰＡＮ、ＰＡＭ－１、ＦＡ－３６７、ＸＹ－２７、ＣＭＣ;钻井污水中ＣＯＤ值严重超标的主要因素是钻井液添加剂;并且钻井液添加剂浓度与其对应的ＣＯＤ之间存在良好的一元线性关系。根据一元线性回归方程可较好地预测油田现场各钻井液添加剂对ＣＯＤ的影响,为解决钻井污水处理这一难题提供科学依据。