医疗废物处置厂污水处理技术

从污水处理工艺、处理方式、水量平衡和自动控制方面论述了医疗废物处置厂污水处理系统,并申请了发明专利。根据医疗废物处置厂水质复杂、水量小、需中水回用等特点,采用物化、生化和微滤膜处理工艺,达到中水回用标准。消毒废水单独处理,循环使用。     

手提式蒸汽消毒器同时消解总磷总氮实验分析

水体中总磷、总氮的增多,会造成藻类的滋生,使水环境质量降低。因此,对总磷、总氮的监测十分必要。国标方法测定水中总磷总氮,都要用手提式蒸汽消毒器进行消解,且消解温度和时间相同。为建立一种快速的测定方法,将总磷、总氮同时放入蒸汽消毒器中进行消解,将此方法与标准消解法进行了对比分析。结果表明:同时消解法的精密度、准确度、回收率、工作曲线等均符合总磷总氮的测定要求,标准物质的测定结果和相对误差均在规范范围内,说明此方法可靠。在总磷、总氮都需检测时,大大缩短了实验时间,减少了蒸汽消毒器的使用频率,是一种快速、简便测定水中总磷总氮的方法。     

FeⅡ(EDTA)络合协同RDB去除NO废气效能及过程分析

为进一步提高一氧化氮(NO)的去除效率,在新型生物转鼓反应器(rotating drum biofilter,RDB)中,以FeⅡ(EDTA)络合协同RDB生物转鼓的耦合技术强化难水溶性NO的气液传质速率,提高生物还原效能为目标进行了研究.结果表明,适量FeⅡ(EDTA)被添加到RDB底部营养液后,能迅速吸收气相中的NO并生成FeⅡ(EDTA)-NO络合物,进而可通过反硝化实现同步脱氮和络合剂再生.在转速0.5 r.min-1、空床停留时间(EBRT)57.7 s、温度30℃、pH 7～8的实验条件下,RDB的净化效能随络合剂的投加而显著改善;FeⅡ(EDTA)质量浓度从0增至500 mg.L-1后,NO去除率从61.1%提高到97.6%,去除负荷从16.2 g.(m3.h)-1上升到26.7 g.(m3.h)-1.分析了FeⅡ(EDTA)络合协同净化NO的反应过程,建立了NO净化效率与FeⅡ(EDTA)添加浓度的关联方程,可较好地拟合实验数据.     

蒸汽锅炉爆炸危险性分析及预防措施

简要叙述了锅炉爆炸机理及爆炸冲击波的破坏、伤害作用,采用TNT当量法对中国石化胜利油田石化总厂动力蒸汽锅炉爆炸事故后果进行了预测计算,分析了导致锅炉爆炸事故发生的原因,并给出了应对措施。     

微波消解-紫外分光光度法测定水中总氮

在分析比较前人实验方法的基础上,采用微波消解一紫外分光光度法测定水中总氮含量.对几种常见态氮溶液进行消解,如硝态氮、亚硝态氮和铵态氮,在确定消解时间后,作出校准曲线,并进行精密度检验.结果表明,该方法与国家标准方法相比具有操作简单、省时、消解完全、精密度较高等优点.     

焦炭塔现场操作的危险原因分析和解决措施

根据具体的事故案例,对焦炭塔现场操作过程存在的各种危险进行了原因分析,提出要从完善仪表控制、加强操作工培训、改善操作条件、进行技术动改及不断完善操作规程和各类制度等方面入手,切实做好各类基础工作,才能消除危险,保障安全。     

污水污泥间壁热干燥实验研究

研究了污泥间壁热干燥的工艺过程,分析了其工艺参数、冷凝水水质和产生的污染气体,探讨了有机物水解机理.结果表明,污泥含水率与停留时间呈负指数函数相关.收集到的干燥冷凝水属高浓度有机废水,其总有机碳（TOC）、挥发性有机酸（VFA）和氨氮（NH₃-N）浓度均很高,pH值保持在9～9.5.干燥冷凝水中挥发性有机酸和氨氮来源于2部分：低温110 ～130℃时,主要发生蛋白质的水解,生成有机酸和氨氮;高温140～150℃时,主要发生脂肪类的水解,生成有机酸.干燥温度低于150 ℃时,污泥间壁热干燥过程无污染气体产生.     

Steam reforming of glycerol for syngas generation under cold plasma conditions: A DFT study

Density functional theory (DFT) has been used to investigate the reaction pathways with steam reforming of glycerol under cold plasma conditions. Total energies, energy barriers, and reaction enthalpies at 298.15 K have been calculated at the GGA/PW91/DNP level. The calculation shows that, with the presence of steam, the energy barrier of glycerol conversion is reduced and the conversion from glycerol to H₂ and CO is promoted under cold plasma conditions. The formation of syngas was through a multi-step pathway via the conversion of OHCH₂CHOH, CH₂OH, CH₂O, HCO,·and CH₃, while the recombination of H generated extra H₂. The synthesis of hydrocarbons are from the recombination of·CH₃,·CH₂, and·CH, which could be primarily generated through glycerol dissociation. The structure of glycerol anion was also studied in this work, and it was less stable than the neutral molecule. The route for the formation of OHCH₂CHOH·and CH₂OH·from glycerol anion is thermodynamically favorable.     

The effect of moisture content within multilayer protective clothing on protection from radiation and steam

The moisture from skin sweat and atmospheric water affects the thermal protective performance provided by multilayer protective clothing. Four levels of moisture content were selected to evaluate the impact of moisture on thermal protection under dry (thermal radiation) and wet (thermal radiation and low-pressure steam) heat exposure. Also, the role of moisture and its relationship with exposure time were analyzed based on skin heat flux and Henriques integral value. The addition of moisture to a fabric system was found to result in differences in second-degree and third-degree skin burn times. When moisture is added to a fabric system, it both acts as a thermal conductor to present a negative effect and provides a positive effect owing to thermal storage of water and evaporative heat loss. The positive or negative effects of moisture are mainly dependent on the thermal exposure time, the moisture content and the presence of hot steam.     

A comparison of pretreatments on release of sugars from sweet sorghum bagasse for bioethanol production

Dilute acid pretreatment and steam pretreatment were evaluated for maximum sugars release and ethanol production from sweet sorghum bagasse (SSB). The fermentation potential of the condensate and hydrolysate obtained from steam pretreatment (10 kg/cm², 10 minutes) and dilute acid hydrolysis (1% (w/w) sulphuric acid, 25% substrate loading) respectively, was checked with Pichia stipitis NCIM 3497 and Debaryomyces hansenii sp. Ethanol production and yield using acid hydrolysate was higher with Debaryomyces hansenii sp. (28.4 g/L and 0.37 g/g respectively) as compared with Pichia stipitis NCIM 3497 (21.9 g/L and 0.29 g/g respectively).