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 ％ 。     

纳氏试剂光度法测定氨氮存在问题探讨

文章就纳氏试剂光度法测定氨氮时试剂性状、试剂的配制方法、实验用水、过滤滤纸以及反应条件对纳氏试剂光度法测定氨氮的影响进行了分析,并就存在的问题进行了初步的探讨。     

纳氏比色法测定NH3—N的改进

减少显色剂中ＨｇＣＬ２、ＫＩ的含量，以聚乙烯醇作胶体稳定剂，显著提高了显色剂的稳定度和显色的稳定度。以ＫＯＨ和酒石酸作缓冲液，保持恒定的显色碱度，同时也隐蔽了金属离子的干扰，从而大大降低了空白吸光度和检出限。废水预处理，通过条件实验，确定稀释比．稀释水样用絮凝沉淀法或蒸馏法处理，蒸馏时用磷酸盐缓冲液，并降低硼酸吸收液的浓度，提高了回收率。     

纳氏试剂显色原理与反应机制探讨

文章分析了在纳氏试剂显色法测定水中氨氮时,常出现影响测定结果的原因,提出使［Ｈｇｌ４］＾２－络离子达到一定的浓度,保证纳氏试剂的性能。     

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％。     

采用新型载体的好氧流化床的动力学研究

本文以稀释的味精废水为基质,对采用新型载体ＬＳＡＲ的好氧生物流化床进行动力学研究,求得动力学参数分别为γｍａｘ＝８．８１（ｇＣＯＤ／ｇｖｓ．ｄ）,Ｋｓ＝０２８９（ｇＣＯＤ／Ｌ）,Ｋｄ＝０．０４６ｄ＾－１,Ｙ＝０．１６（ｇｖｓ／ｇＣＯＤ）。其值基本处于文献的报导之内,说明以ＬＳＡＲ为载体的好氧微生物膜具有较好的活性,ＬＳＡＲ作为好氧流化床载体是可行的。     

乌鲁木齐河跃进桥蒸发观测实验

Ｅ６０１ｋ型玻璃钢蒸发器与Ｅ６０１型水面蒸发器比测实验取得成功，两套Ｅ６０１Ｋ型蒸发量相近，比铁制Ｅ６０１型水面蒸发器蒸发偏大８．５％，系数偏大０．０６。用Ｅ８３型土壤蒸渗仪测定草地、裸地和云杉蒸发量，５月－１０月份分别为４９１．９ｍｍ，４３３．６ｍｍ和３７９．７ｍｍ（云杉为６月－１０月份）。     

纳氏试剂分光光度法测定水中氨氮的影响因素浅析

纳氏试剂分光光度法测定水质氨氮受多种因素干扰,直接影响分析结果。针对此情况,结合环境监测工作实际,通过纳氏试剂配制、水样存放时间、稀释方式、显色条件4个方面对实验结果产生的影响进行了研究,并对这些干扰因素的消除进行了讨论,为确保纳氏试剂分光光度法测定水中氨氮结果的准确性提供了参考。     

间歇曝气系统中硝酸盐氮负荷对脱氮效率的影响

本试验主要考察间歇反应器缺氧阶段硝酸盐氮负荷ＮＮＯ－ｘ－Ｎ（ＫｇＮＯ－ｘ－Ｎ／ＫｇＭＬＳＳｄ）对脱氮效率的影响。试验结果表明：在一定水温和ＢＯＤ５／ＮＯｘ－Ｎ下,ＮＮＯｘ－Ｎ负荷对脱氮效率有显著影响。在反应器中采用高浓度污泥是降低ＮＮＯｘ－Ｎ的有效途径,有利于反应器脱氮速率ＶＤＮ（ｍｇ／ｌ·ｍｉｎ）的提高。此外,通过正交试验得出了在ＢＯＤ５／ＮＯ－ｘ一定时,ＮＮＯ－ｘ－Ｎ、Ｔ℃与脱氮效率ηＮＯ－ｘ－Ｎ之间的数量关系式     

纳氏试剂和校准曲线对水中氨氮测定影响分析

纳氏试剂分光光度法是油田废水中氨氮测定的经典方法,纳氏试剂的配置和校准曲线绘制是主要影响因素。文章比较了两种纳氏试剂的配置方法,得出HgCl2法纳氏试剂虽然配制麻烦,但含汞量、空白吸光度均较低,灵敏度、精密度和加标回收率较高,是氨氮测定的首选纳氏试剂。分别以氨氮的质量和质量浓度为横坐标,吸光度为纵坐标绘制两组校准曲线,得出以质量浓度为横坐标绘制的校准曲线测定结果的相对误差较小,准确度高。     

Mechanical performance of woodfibre–waste plastic composite materials

Plastic products used for packaging are often discarded after a single use resulting in an inexhaustible supply of waste polymeric materials. The stiffness and strength of polymeric materials have been known to improve with the addition of lignocellulosic fibres available in abundance in nature. Hence, composite materials containing natural fibres and waste plastics would result in the reduction of solid wastes and the use of cheap, renewable resources. Composite specimens, consisting of waste plastics obtained from a Kerbside collection (high density polyethylene (HDPE) waste, Janitorial waste, Kerbside waste I and Kerbside waste II) and Pinus radiata woodfibres (medium density fibres (MDF)), have been produced through melt blending and injection moulding. The effects of fibre content, matrix type and interfacial bonding on the tensile and flexural properties of these composite materials have been determined through extensive testing at various conditions. The mechanical properties of these composites at room temperature and humidity depend on the amount of woodfibres, the mechanical properties of the waste plastics used and the presence of a suitable coupling agent. The tensile strengths of MDF/waste plastic composites do not generally change with fibre content except for 40% MDF/HDPE waste and 40% MDF/Kerbside waste II (plus 1% Epolene™) composites, where the tensile strengths increase by about 25% compared to those of the corresponding waste plastics. Flexural strengths of MDF/waste plastic composites increase with the addition of medium density fibres with the exception of MDF/Kerbside waste I composites. The tensile and flexural moduli of MDF/waste plastic composites mostly increase with increasing fibre content.     

应用QC方法降低废水处理站出水的COD波动值

通过QC小组活动,对造成某废水处理站出水COD波动值较大的因素进行了分析,最终确定是因为药剂投加量调控次数不够,造成药剂供需不平衡影响COD的波动。通过制定对策控制主要因素,可以将COD波动值由原有35.88 mg/L控制至25 mg/L以下,吨水处理药剂费用减少了5.7%,为外排水水质稳定达标提供了有力保障,大幅降低了实验人员、操作人员的劳动强度。     

聚合物驱注入液黏度稳定剂研究进展

油田采出水中影响聚合物溶液黏度的主要因素有金属离子、还原性物质、细菌等,次要影响因素有pH值、溶解氧、含油量、悬浮固体、残余聚合物、残余化学剂等。针对以上影响因素,可通过投加适宜的化学剂来消除影响,从而控制聚合物溶液的黏度损失。根据作用机理,目前常用的黏度稳定剂可分为水质改性型和黏度稳定型两种,对造成黏度损失的主要因素可投加水质改性型药剂、对溶解氧等问题可投加黏度稳定型药剂来降低黏度损失。此外,不同单剂组合的复配可通过协同作用有效地提高药剂效果,复合型药剂的应用前景将更为广阔。     

流动注射—光度法联用测定海水中PO4-P

本法针对海水分析时严重的盐度和基体干扰,以监测的海水试样为载流,并在流动注射进样阀前流路上首次引入自制全容量阴离子交换柱,去除载流中的磷酸盐,使进入系统的载流盐度与试样一致,消除了基体干扰,并通过阴柱在线再生条件试验和工作曲线优化试验,建立了流动注射磷锑钼蓝(还原剂为抗坏血酸)光度法直接测定PO4-P浓度为Ⅰ类～Ⅳ类海水的新方法,能分辨海水类别。结果表明,在最适合条件下,该方法在PO4-P浓度5～80μg/L范围内峰高与浓度成线性关系,方法检出限为0.73μg/L,空白海水加10μg/L、30μg/L和60μg/L PO4-P标准物质连续进样,RSD分别为4.57%(n=5)、4.72%(n=4)和5.76%(n=4)。进行实际样品分析时,加标回收率为101%～102%,具有很好的准确性,与国家标准方法———磷钼蓝分光光度法比对,结果吻合,令人满意。     

孤岛油区外排采油污水生化处理技术的研究

针对孤岛污水矿化度高,Cl-含量高,油含量和COD含量严重超标的现象,采取微生物接触氧化工艺进行外排采油污水治理的工艺研究。在处理过程中首先对菌种进行了严格的筛选和培养,然后在室内进行了模拟试验,最后在现场进行了中试。目前已根据中试结果,对孤岛污水原有的污水池进行了改造,设置了隔油池、气浮池、接触氧化池和沉淀池四个部分,经过一年的运行,成功地实现了污水的达标排放。     

利用化学混凝法处理钻井污水实验研究

采用化学混凝法对江汉油田钻井污水进行了室内处理实验。实验结果表明,污水处理时所选絮凝剂的种类、加入量、加入顺序、温度和加入后的沉降时间等都会影响处理效果。采用单一无机化学药剂,沉降速度较慢,故考虑将无机和有机药剂复配使用,即利用先加无机药剂后再加入有机药剂的顺序处理该油田钻井废水。该实验结果为油田钻井污水无害化处理提供了基础资料。     

预膜过滤技术在采油污水处理中的应用

详细介绍了新开发的FDF300型过滤工艺,并通过试验验证了自行研制的新型GM助剂在FDF型过滤器中应用的工艺条件,考察了助剂用量、型号、预膜时间以及空气反吹脱渣时间、反吹压力等因素对过滤效果的影响。结果表明,选用150gGM3助剂,预膜时间约20 min,空气反吹脱渣时间5 min,反吹压力0.35 MPa等工艺条件,可以获得理想的过滤效果,解决了长期困扰油田采油污水含油量和机械杂质不达标的难题。     

Use of magnesia for boron removal from irrigation water

The risk of B phytotoxicity due to high levels of B in irrigation water can be avoided by removing B from the water, before its use, through adsorption on certain adsorbents, such as magnesia (industrial MgO), if the latter can be proven to be an effective and easy to handle means for B removal. In addition, if such a material is applied as a fertilizer after its use and the adsorbed B is easily released into the soil solution, B phytotoxicity could constitute a potential hazard. The objectives of this work were to: (a) establish the optimum working conditions (equilibration time, solution to adsorbent ratio, and particle size of the adsorbent) for B adsorption, (b) assess the magnitude of B adsorption by magnesia, both in capacity and intensity terms, as well as the influence of temperature, (c) study B desorbability from magnesia, spiked with B at two rates, 5 and 0.5 mg g(-1), and (d) compare the results from b and c to those obtained using reagent grade MgO. The results showed that the time to achieve equilibrium depended on the B concentration of the external solution and ranged from 6 h (for B /= 50 mg L(-1)). The percentage of B adsorbed decreased as the volume of external solution to adsorbent increased and a working ratio of 50:1 was selected. For magnesia, B adsorption was particle size dependent with the smallest fraction (<0.1 mm) sorbing more B than the other three fractions studied (0.1-1.0, 1.1-2.0, 2.1-4.0 mm). Boron adsorption was conducted under strongly alkaline pH (10.3 +/- 0.2 and 10.4 +/- 0.1 for the reagent and magnesia, respectively) and increased with temperature. Both adsorbents exhibited a high B adsorption capacity (Langmuir maximum values were 5.85 +/- 0.39 and 4.45 +/- 1.31 mg B g(-1) for the reagent and magnesia, respectively) comparable to other metal oxides. However, the reagent grade MgO seemed to be superior to magnesia in terms of capacity and strength of B retention. This superiority of the reagent was attributed to its greater surface area (34.7 compared with 5.8 m(2) g(-1) for magnesia) and to its conversion to Mg(OH)(2) during the adsorption process, whereas magnesia remained unaltered, as was evident from X-ray diffractograms. Based on this data, magnesia seems to be an effective means for removing excess B from irrigation water, particularly if a material of fine particle size is used. Boron desorbability after 240 h of desorption time was more pronounced for magnesia reaching up to 55 and 60% of the amount of B added, at the spiked rates of 5 and 0.5 mg g(-1), respectively. Although these figures indicate that approximately half of the amount of B added remained adsorbed, they cannot be easily extrapolated to field conditions, and if B-laden magnesia is applied to soils, the possibility of B phytotoxicity cannot be excluded.     

Enzyme catalyzed biodiesel production from rubber seed oil containing high free fatty acid

Unrefined rubber seed oil contains high levels of free fatty acids and moisture, which make the conventional chemical catalyzed transesterification unsuitable. The method of enzyme catalyzed transesterification is well suited for biodiesel production from rubber seed oil as the enzymes are insensitive to the free fatty acids. In the present work, rubber seed oil was extracted from preserved rubber seed cake by mechanical means. The extraction process was designed and optimized through 2⁴ full factorial design. Extracted oil was subjected to enzymatic transesterification using four different lipases to identify the best one for the purpose. Transesterification process was optimized by considering three influencing variables for biodiesel production viz. methanol/oil molar ratio, catalyst concentration (% w/v) and solvent content (% v/v). A 2³ full factorial design was applied to design the experiments and optimize the biodiesel production. The interactive effects of the independent variables on biodiesel yield were analyzed and regression models were developed for each set of enzyme reactions. Among the four lipases, Thermomysis Lanugonosus Lipase was found to be the most suitable for the transesterification of rubber seed oil with a biodiesel conversion of 92.83% at a molar ratio of 4% and 5% (w/v) enzyme concentration in solvent free reaction medium.     

化学药剂对吸入式气浮净化机除油浮选动力学的影响

本研究在实验室装置上着重考察了化学药剂对吸入式气浮净化机除油浮选动力学的影响。研究结果表明化学药剂对浮选速率常数有明显影响,不同化学药剂及用量其影响效果不同。