气相色谱法测定氨气中的甲硫醇及甲硫醚

建立了测定氨气中甲硫醇及甲硫醚的气相色谱分析方法。样品充入高纯氮气后，通过磷酸吸收液脱除氨气，有机硫化物由氨气转移到高纯氮气中，收集这部分气体，取1．0～2．0mL采用火焰光度检测填充柱气相色谱法进行分析。方法的相对标准偏差小于7％，甲硫醇和甲硫醚的加标回收率分别为92．1％和87．6％，最低检出量分别为0．11ng和0．17ng，最低检出质量浓度分别为0．11μg／L和0．17μg/L。     

二甲基二硫醚废气的处理

研究了二甲基二硫醚（DMDS）废气的处理技术，先将废气冷凝成废液，废液经蒸馏回收二甲基二硫醚，利用双氧水将废残液中二甲基硫醚（DMS）氧化为二甲基亚砜（DMSO），考察了反应溶剂及其用量，反应温度、原料配比、双氧水滴加速度等反应的影响。确定的适宜工艺条件：以丙酮为溶剂，二甲基硫醚，双氧水，丙酮的体积配比为0．75：1：1，双氧水的流量为2．0mL/min，反应时间为3．0－3．5h，反应温度为20－30℃，在此工艺条件下二甲基亚砜的产率为90．7％。     

生物滴滤塔处理模拟甲硫醚废气

在常温条件下,采用生物滴滤塔处理模拟甲硫醚废气,考察了气体空床停留时间(EBRT)、容积负荷、喷淋密度及营养液pH对生物滴滤塔性能的影响。实验结果表明:当EBRT为90 s、进气甲硫醚质量浓度为150 mg/m~3、喷淋密度为0.65 m~3/(m~2·h),营养液pH为6.8时,甲硫醚去除率为90%;容积负荷高于15 g/(m~3·h)时,对生物滴滤塔的性能产生抑制作用;EBRT为90 s及60 s时,最佳喷淋密度分别为0.56~0.65 m~3/(m~2·h)及0.65~0.75 m~3/(m~2·h);降解甲硫醚的微生物对pH的变化较敏感,最适营养液pH为6~7。     

TiO2气溶胶快速去除空气中的芥子气模拟剂

在自制反应器内,通过喷射法将纳米TiO_2分散成气溶胶形式,用以降解空气中的芥子气模拟剂二乙基硫醚(DES)。利用自行设计的一套气溶胶沉降行为评价装置,对TiO_2气溶胶的释放条件进行了优化。系统研究了相对湿度、反应温度、光强、催化剂加入量、反应物浓度等因素对DES降解速率和彻底矿化速率的影响。结果表明:TiO_2气溶胶对2.80 mg/L(近似芥子气快速致死浓度)DES降解的半衰期由涂覆型TiO_2的34.5 min缩短至8.5 min;TiO_2气溶胶光催化降解DES的最佳相对湿度为35%,此时CO_2最快生成速率可达34.64μg/(L·min),150 min内彻底矿化比例达66.1%;对于1.5 L反应器,催化剂加入量为30 mg时降解DES的量效比达到最佳状态;TiO_2气溶胶光催化适用于含低浓度DES空气的快速净化。     

GC-MS分析好氧颗粒污泥降解黄连素的产物

采用GC-MS法分析好氧颗粒污泥降解黄连素的产物。实验结果表明，经过360min的反应黄连素被分解为6-甲氧苯并二氢呋喃-7-醇-3-酮、2，5-二甲氧基苯甲醛、4-烯丙基-5-氨基-藜芦醚、2，4-二羟基-6-甲基-1，3-间苯二甲醛、3，4-亚甲基二氧苯基丙酮酸、1，3-二噁唑并（4，5-g）异喹啉-5（6H）-酮，7，8-二氢。     

二甲基二硫醚生产废气的回收和处理

在二甲基二硫醚的生产过程中,产生含有机硫化物（二甲基二硫醚、甲硫醚、甲硫醇等）的恶臭废气,严重污染大气环境。笔者采用冷冻回收、氧化吸收、吸附净化等方法治理该废气,取得了较好的治理效果。（１）冷冻回收二甲基二硫醚和甲硫醚具有较高的回收价值,常压下前者液化点较高（为１０３℃）,易于冷凝;后者液化点较低（为３７℃）,不易冷凝回收,故采用冷冻机强制冷降温,将冷凝器循环介质出口温度控制在５℃以下。甲硫醚的回收率在８０％以上,二甲基二硫醚的回收率达到９８％。（２）氧化吸收甲硫醇具有较强的还原性,极易与次氯酸…     

利用磷霉素生产盐渣合成阻垢剂

将磷霉素生产盐渣经水解得到右旋磷霉素二钠,再通过亲核取代反应得到可用作循环冷却水阻垢剂的氨基二乙基(1-甲基-2-羟基)膦酸四钠(ADMHP·Na4),并用FTIR表征了产物结构.实验结果表明:在取代反应温度为25℃、取代反应时间为2h、n(氨水)∶n(右旋磷霉素二钠)=8的条件下,由右旋磷霉素二钠制备ADMHP·Na4,收率可达83.87％.处理1t盐渣可创造利润3 080元.当ADMHP·Na4质量浓度为30 mg/L,水样温度为60℃时,ADMHP·Na4对CaCO3的阻垢效果较好,阻垢率可达91.47％.     

气相置换合成Zn-Cu-BTC及其吸附脱硫性能

采用气相置换法制备了Zn-Cu-BTC双金属有机骨架化合物,运用XRD,SEM-EDS,BET等技术对材料进行了分析表征,并以二苯并噻吩-正辛烷为模拟油（硫含量450 μg/g）,通过吸附脱除二苯并噻吩评价了材料的吸附脱硫性能。表征结果显示,Zn的引入改变了Cu-BTC特有的八面体结构。实验结果表明：在模拟油与吸附剂的质量比100∶1、吸附温度30 ℃的条件下,吸附90 min后Zn-Cu-BTC对硫的吸附达到平衡,吸附量可达38.8 mg/g,脱硫率为94.20%,而Cu-BTC吸附120 min后达到平衡,吸附量仅为26.6 mg/g;Langmuir等温吸附模型可有效描述Zn-Cu-BTC对硫的吸附过程。     

化学氧化法脱除石油焦中的硫

分别采用硝酸、硝酸-冰醋酸混合液以及王水作氧化剂脱除石油焦中的硫。实验结果表明:石油焦粒径越小,脱硫率越高;随液固比(氧化剂体积与石油焦质量比,mL/g)增大、反应时间延长、反应温度升高,脱硫率先增大,达到极值后保持稳定。王水的脱硫率高于硝酸和硝酸-冰醋酸混合液。王水脱除石油焦中硫的最佳工艺条件为:石油焦粒径0.1mm,液固比20mL/g,反应时间20h,反应温度50℃。在此最佳条件下,脱硫率达42.3%。经王水在最佳脱硫工艺条件下处理后,可有效脱除石油焦中大部分的噻吩类和硫醇类有机硫以及全部的无机硫。     

生物法处理甲基硫化物恶臭气体的研究

采用活性污泥法富集培养去除甲硫醇、甲硫醚、二甲基二硫等甲基硫化物的优势菌种。结果表明，经过驯化后的活性污泥，对废水中的甲硫醇钠及COD去除率达90％，SV为18％。分析了在活性污泥驯化过程中原生动物的数量和种群的演替过程。将经驯化的活性污泥固定化后处理甲硫醚和二甲基二硫恶臭废气，在进气质量浓度分别为2～50，1～40mg／m。的范围内，甲硫醚和二甲基二硫去除率都能稳定在90％左右。     

Odor compounds from different sources of landfill: characterization and source identification

This study investigated the odor compounds from different areas in a landfill site, which included the municipal solid waste (MSW)-related area, the leachate-related area and the sludge-related area. Nine sampling points were placed and 35 types of odorous substances were measured and quantified from these grabbed samples. The results showed that the main odorous substances emitted from landfill site were styrene, toluene, xylene, acetone, methanol, n-butanone, n-butylaldehyde, acetic acid, dimethyl sulfide, dimethyl disulfide and ammonia. In the MSW-related area, the highest concentrations of oxygenated compounds were observed at the gas extraction wells (GW), while sulfur compounds were rare. Ammonia in the sludge-related area was very abundant. Sludge discharge area (SD1) and sludge disposal work place (SD2) were representative points of pre- and post-drying, in which the characterizations of the emitted odorous gas were different. After chemical drying, the concentration of ammonia increased, whereas those of volatile fatty acids and sulfur compounds decreased. In the leachate-related area, relatively low concentrations of all those odorants were detected in leachate storage pool (LS), which may be due to the enclosure operation of the leachate storage pool. Using principal components analysis and cluster analysis, GW, SD1 and SD2 were distinguished from the other sampling points. The typical odorants in GW were acetaldehyde, ethyl benzene, xylene, methylamine and dimethyl formamide. The typical odorants in SD1 were methyl mercaptan, valeric acid and isovaleric acid, while those in SD2 were carbon disulfide, acetone, 3-pentanone, methanol and trimethylamine. The typical odorants in other sampling points were hydrogen sulfide, n-butylaldehyde and acetic acid.     

Field scale evaluation of volatile organic compound production inside biosecure swine mortality composts

Emergency mortality composting associated with a disease outbreak has special requirements to reduce the risks of pathogen survival and disease transmission. The most important requirements are to cover mortalities with biosecure barriers and avoid turning compost piles until the pathogens are inactivated. Temperature is the most commonly used parameter for assessing success of a biosecure composting process, but a decline in compost core temperature does not necessarily signify completion of the degradation process. In this study, gas concentrations of volatile organic compounds (VOCs) produced inside biosecure swine mortality composting units filled with six different cover/plant materials were monitored to test the state and completion of the process. Among the 55 compounds identified, dimethyl disulfide, dimethyl trisulfide, and pyrimidine were found to be marker compounds of the process. Temperature at the end of eight weeks was not found as an indicator of swine carcass degradation. However, gas concentrations of the marker compounds at the end of eight weeks were found to be related to carcass degradation. The highest gas concentrations of the marker compounds were measured for the test units with the lowest degradation (highest respiration rates). Dimethyl disulfide was found to be the most robust marker compound as it was detected from all composting units in the eighth week of the trial. Concentration of dimethyl disulfide decreased from a range of 290–4340 ppmv to 6–160 ppbv. Dimethyl trisulfide concentrations decreased to a range of below detection limit to 430 ppbv while pyrimidine concentrations decreased to a range of below detection limit to 13 ppbv.     

液液萃取—GC-MS法同时测定石化废水中双酚A和邻苯二甲酸二乙酯

建立了液液萃取（LLE）—气相色谱-质谱（GC-MS）法同时测定石化废水中双酚A（BPA）和邻苯二甲酸二乙酯（DEP）的新方法,对液液萃取条件进行了优化。最佳的液液萃取条件为：萃取剂为乙酸乙酯,水样调成酸性（pH<2）,每次加入萃取剂0.1 mL/mL、盐析剂NaCl 0.1 g/mL,萃取次数为6次,每次萃取时间为2 min。实验结果表明：在质量浓度1~100 mg/L的范围内,BPA和DEP测定标准曲线的线性关系良好;BPA和DEP的检出限（LOD）分别为5.18 μg/L和0.89 μg/L,定量限（LOQ）分别为17.11 μg/L和2.96 μg/L,回收率为81.4 %~124.9 %,相对标准偏差（RSD）（n=7）小于5.5 %。     

活性炭对气体中二硫化碳吸附性能的研究

研究了４种不同活性炭的孔结构及对二硫化碳的平衡吸附性能,并对４种活性炭床层的穿透性进行了考察,为选择吸附净化废气中低浓度二硫化碳的吸附剂奠定了基础。     

Preparation of aluminium-magnesium alloys and some valuable salts from used beverage cans

The purpose of this work is to recover standard aluminium-magnesium alloy(s) and some valuable salts from used beverage cans (UBCs). The suggested method updated the current recycling technology by augmenting removal of the coating paint, decreasing magnesium loss during melting process and improving hydrochloric acid leaching of the formed slag. Iron impurity present in the leaching solution, was removed by oxidation using oxygen gas or hydrogen peroxide and filtered as goethite. Results obtained revealed that a mixture of methyl ethyl ketone/dimethyl formamide entirely removes the paint coating at room temperature. The process compares favorably to the current methods involving firing or swell peeling. The coating decomposes to titanium dioxide by heating at 750 degrees C for 30 min. Standard compositions of Al-Mg alloys are formulated using secondary magnesium. The extent of recovery (R) of these alloy(s) is a function of the melting time and temperature and type of the flux. The maximum (R) value amounts to 94.4%. Sodium borate/chloride mix decreases magnesium loss to a minimum. The extent of leaching valuable salts from the slag increases with increasing the molarity, stoichiometric ratio and leaching temperature of the acid used. Removal of iron is a function of the potential of the oxidation process. Stannous chloride has been recovered from the recovered and dried salts by distillation at 700-750 degrees C.     

吸附回收法处理甲硫醚废气

采用吸附回收法处理高浓度小排放量的甲硫醚废气，以活性炭不吸附剂，废气中甲硫醚的质量浓度可从处理前的151g/m^3降至0．06g/m^3，甲硫醚的去除率大于99％，处理后的废气可达标排放，将吸附饱和后的活性炭用水蒸气解吸再生，解吸得到的甲硫醚回用于生产。     

液体吸收法脱除烟气中二氧化硫的研究

对烟气中SO2有机吸收剂进行了筛选，研究出一种新型烟气脱硫吸收剂－二甲基亚砜加Mn^2 。与纯二甲基亚砜相比，添加Mn^2 对烟气脱硫效率有较大的影响。同时还进行了工艺条件试验，并对新型烟气脱硫吸收剂的吸收机理进行了探讨。     

Increase of the purification efficiency of biofilters by the use of a complementary ionisation step

The biofilter and the ionisation system are two oxidative treatment techniques for purification of waste gas streams with low concentrations of volatile organic compounds. In this paper, the authors present the investigations of an ionisation technique aimed at increasing the efficiency of the reduction of the odorant concentration in waste gas streams from biological waste treatment plants. The objective is to enable advanced odour emission reduction and to adjust the existing biofilters to stricter requirements. In a first step, the odorous substances which are major contributors to the overall odorant concentration are identified on basis of various emission data sets with the help of a method of life cycle impact assessment. Thereby limonene, alpha-pinene, ethyl butyrate and dimethyl disulphide were identified as crucial indicators. In a second step, experimental investigations using limonene as a model compound were conducted to gain an understanding of the ionisation process itself and at last for the evaluation of the system.     

二硫化碳萃取—气相色谱法同时测定含盐酸废水中的甲苯、邻氯甲苯、对氯甲苯和氯化苄

建立了二硫化碳萃取—气相色谱法同时测定含盐酸废水中甲苯、邻氯甲苯、对氯甲苯和氯化苄的方法，并应用于实际水样的测定。采用二硫化碳萃取含盐酸废水中的甲苯、邻氯甲苯、对氯甲苯、氯化苄，待测物质经30QC3/AC20（30 m×0.32 mm×0.50 μm）毛细管柱气相分离。采用保留时间定性，外标法定量。实验结果表明，甲苯、邻氯甲苯、对氯甲苯和氯化苄的质量浓度在0.2~100.0 mg/L范围内与对应的峰面积呈良好的线性关系，检出限分别为0.09，0.12，0.13，0.10 mg/L。该方法的精密度和准确度较高，相对标准偏差小于2%，加标回收率在96.4%~101.0%之间。     

自动进样气相色谱法测定气体中的非甲烷烃

用泰德拉气体采样袋采样，自动进样气相色谱法测定气体中的非甲烷烃含量。甲烷、总烃的线性范围分别为0～2439，0—2066mg／m^3。进样量为1mL时，检出限为0．02mg／m^3（信噪比为3）。对3种不同浓度甲烷与丙烷混合标准气进行测定，重复性相对标准偏差为0．4％-1．0％。对4种不同性质的试样进行加标回收实验，加标回收率为96．7％-102．0％。5名实验人员分别用自动进样法及手动进样法分析4种不同性质的试样，自动进样法的重现性相对标准偏差为1．2％～1．8％，优于手动进样法的6．5％～8．3％。该法可一次连续测定21个试样，精密度高、重现性好、分析效率高。