Solution-Processed Organic Solar Cells with High Open-Circuit Voltage of 1.3 V and Low Non-Radiative Voltage Loss of 0.16 V

Compared with inorganic or perovskite solar cells, the relatively large non-radiative recombination voltage losses (ΔV_non-rad) in organic solar cells (OSCs) limit the improvement of the open-circuit voltage (V_oc). Herein, OSCs are fabricated by adopting two pairs of D–π–A polymers (PBT1-C/PBT1-C-2Cl and PBDB-T/PBDB-T-2Cl) as electron donors and a wide-bandgap molecule BTA3 as the electron acceptor. In these blends, a charge-transfer state energy (E_CT) as high as 1.70–1.76 eV is achieved, leading to small energetic differences between the singlet excited states and charge-transfer states (ΔE_CT ≈ 0.1 eV). In addition, after introducing chlorine atoms into the π-bridge or the side chain of benzodithiophene (BDT) unit, electroluminescence external quantum efficiencies as high as 1.9 × 10⁻³ and 1.0 × 10⁻³ are realized in OSCs based on PBTI-C-2Cl and PBDB-T-2Cl, respectively. Their corresponding ΔV_non-rad are 0.16 and 0.17 V, which are lower than those of OSCs based on the analog polymers without a chlorine atom (0.21 and 0.24 V for PBT1-C and PBDB-T, respectively), resulting in high V_oc of 1.3 V. The ΔV_non-rad of 0.16 V and V_oc of 1.3 V achieved in PBT1-C-2Cl:BTA3 OSCs are thought to represent the best values for solution-processed OSCs reported in the literature so far.     

粗金粉中金的氯浸-控制电位还原精炼

某冶炼厂氰化金泥还原得到的粗金产品纯度较低，采用氯浸-还原工艺对粗金进行了精炼提纯。在生产工艺中采用盐酸+氯酸钠对粗金进行氯浸溶解，用焦亚硫酸钠控制电位选择性还原浸出液中的金。采用补水-冷却使银和铅从氯浸液充分沉淀析出，通过调整pH值、改变焦亚硫酸钠添加方式、精确控制还原电位等方法，产品金锭达到IC-Au99.99标准。两年的生产实践创造了明显的经济效益。     

Simultaneous extraction of gold and zinc from refractory carbonaceous gold ore by chlorination roasting process

A novel process based on chlorination roasting was proposed to simultaneously recover gold and zinc from refractory carbonaceous gold ore by using NaCl as chlorination agent. The effects of roasting temperature, roasting time and NaCl content on the volatilization rates of gold and zinc were investigated. The reaction mechanism and the phase transition process were also analyzed by means of SEM, EDS and XRD. The results demonstrated that under the optimal conditions of NaCl content of 10%, roasting temperature of 800 °C, roasting time of 4 h and gas flow rate of 1 L/min, the rates of gold and zinc were 92% and 92.56%, respectively. During low-temperature chlorination roasting stage, a certain content of sulfur was beneficial to the chlorination reactions of gold and zinc; and during high-temperature chlorination roasting stage, the crystal structure of vanadium-bearing mica was destroyed, and the vanadium-containing oxides were beneficial to the chlorinating volatilization of gold and zinc. Eventually, the chlorinated volatiles of gold and zinc could be recovered by alkaline solution.     

质子酸催化合成α-氯代十二酸工艺研究

采用廉价的浓硫酸为催化剂,氧气为自由基捕集剂,以十二酸为原料,经氯化合成α-氯代十二酸。系统考察了反应温度、催化剂用量、氯气流量、氧氯比、反应时间等因素的影响,得到最佳工艺条件:十二酸20 g,在反应温度135℃、催化剂10%、氯气流量50 mL·min-1、vO2/vCl2=1∶2、反应时间3 h,可实现十二酸基本完全转化,目标产物α-氯代十二酸选择性达到94.5%。     

石蜡氯化反应异常停止的原因

氯化石蜡生产中因液氯质量问题引起反应终止,分析了影响液氯质量的因素（主要是液氯中硫酸、二氧化硫、铁的化合物、水分、光气及二氧化氯等含量超标）,提出了解决措施.     

硫代硫酸钠脱氯特性及其动力学分析

考察了二级生物处理出水经氯消毒后采用硫代硫酸钠脱氯的效果。结果表明，在氯消毒后初始余氯为10mgCl2／L的条件下，当反应时间为60min、硫代硫酸钠投量由理论投加量的100％增加至500％时，余氯去除率由41．2％增加到95．5％。硫代硫酸钠脱氯过程为分步反应：在最初的1min内，余氯脱除速率最快；反应1min后，自由氯脱除呈现零级反应，一氯胺、有机氯胺为一级反应；自由氯脱除速度快于一氯胺和有机氯胺，无机氯胺和有机氯胺是硫代硫酸钠脱氯反应速率的限制因素。当以硫代硫酸钠作为脱氯剂时，采用普通活性污泥法的污水处理厂需通过提高硫代硫酸钠投加量来实现快速脱氯，而采用生物脱氮工艺且硝化效果良好的污水处理厂只要保证足够的脱氯反应时间即可实现很好的脱氯效果。     

Reaction processes effecting the analysis of chloroform by direct aqueous injection gas chromatography

Several important reaction processes which influence the analysis of chloroform by direct aqueous injection (DAI) gas chromatography have been identified through an investigation of the chlorination reactions of humic acid and a series of simple polyhydroxyaromatic and diketone model compounds in dilute solution. The reaction of chlorine with each substrate system was studied over the pH range 2–12. Gas chromatographic analysis by the DAI and organic solvent liquid-liquid extraction (LLE) procedures gave different measurements for the yield of CHCl₃ depending on the pH of the reaction solution and the chemical structure of the substrate. Under acidic and neutral conditions, a variety of trichloromethyl-substituted intermediates were identified at high concentrations in addition to chloroform by GC/MS. Chloral hydrate, trichloroacetic acid, pentachloroacetone and hexachloroacetone undergo hydrolysis and/or decarboxylation to form CHCl₃ at the high injection port temperatures employed in aqueous injection GC analysis. The results obtained in the current study indicate that the decomposition of these and structurally-related species accounts for differences previously observed upon application of the DAI and either the LLE or purge-and-trap techniques for the determination of CHCl₃ in chlorinated natural waters.     

Breakpoint chlorination and free-chlorine contact time: implications for drinking water N-nitrosodimethylamine concentrations

North American drinking water utilities are increasingly incorporating alternative disinfectants, such as chloramines, in order to comply with disinfection by-product (DBP) regulations. N-Nitrosodimethylamine (NDMA) is a non-halogenated DBP, associated with chloramination, having a drinking water unit risk two to three orders of magnitude greater than currently regulated halogenated DBPs. We quantified NDMA from two full-scale chloraminating water treatment plants in Alberta between 2003 and 2005 as well as conducted bench-scale chloramination/breakpoint experiments to assess NDMA formation. Distribution system NDMA concentrations varied and tended to increase with increasing distribution residence time. Bench-scale disinfection experiments resulted in peak NDMA production near the theoretical monochloramine maximum in the sub-breakpoint region of the disinfection curve. Breakpoints for the raw and partially treated waters tested ranged from 1.9:1 to 2.4:1 (Cl(2):total NH(3)-N, M:M). Bench-scale experiments with free-chlorine contact (2h) before chloramination resulted in significant reductions in NDMA formation (up to 93%) compared to no free-chlorine contact time. Risk-tradeoff issues involving alternative disinfection methods and unregulated DBPs, such as NDMA, are emerging as a major water quality and public health information gap.     

钛白粉的制备方法现状及展望

综述了钛白粉的制备方法现状及研究进展,分析了各种方法的技术特点,指出金红石型钛白粉生产应以氯化法为主,但在中国发展氯化法钛白需加强适合国内高钙镁钛资源制备沸腾氯化炉料方法的研究,进一步掌握沸腾氯化法生产的核心技术,同时开展熔盐氯化废渣的循环利用研究,开发清洁的熔盐氯化法新技术。锐钛型钛白粉产品在功能材料方面有着不可替代的市场地位,硫酸法、盐酸法、亚熔盐法、氟化法均可生产出锐钛型钛白产品,这些方法还需解决生产过程中试剂的循环利用以及三废的综合利用问题,才能实现钛白粉产业的绿色转型。     

典型含氮有机物的氯消毒副产物生成潜能研究

污水再生利用是解决我国城市水资源短缺的有效途径，消毒是保证再生水水质安全的必要措施。氯消毒可以有效杀灭病原微生物，但同时也会生成各种具有毒性和“三致”效应的消毒副产物。由于含氮有机物是污水氯消毒副产物的一类重要前体物，故选取20种基本氨基酸为研究对象，考察了它们经氯消毒后生成三氯甲烷、卤乙酸、卤乙腈、三氯硝基甲烷、1，1-二氯-2-丙酮和1，1，1-三氯-2-丙酮的潜能。结果表明，各种氨基酸的消毒副产物生成潜能与它们的R基结构密切相关，其中R基上带有活性苯环的色氨酸和酪氨酸均表现出了较高的三氯甲烷、卤乙酸和卤乙腈生成潜能。