宁安市城区集中供热工程环境效益探讨

实施集中供热是城市环境污染的根本途径,不仅可以大幅度地提高城镇供热质量,改善居民生活环境,满足城区集中供热突出问题,还可以推动城镇环境建设和经济发展,有利于旅游事业的拓凰     

采油井口储罐加温装置的改进

针对采油井口储罐明火直接加温法安全系数较低、易发生事故、不符合国家标准要求的问题进行了改进,介绍了撬装式加温预热装置的流程及设备,经试用热效率提高,未发生生产事故。     

湿污泥热解制取富氢燃气影响因素研究

采用管式炉热解装置,在700～1000℃温度范围内对不同含水率的生物污泥进行中高温常压热解实验,研究了加热模式、热解终温、物料含水率及升温速率对热解产物产率及气相产物组成的影响规律.结果表明:待温度达到设定温度后,迅速将物料送入反应区的加热模式有利于得到高品质燃气;高温能减少固体碳和焦油的生成,促进富氢气体产生;同时,随着物料含水率的增加,氢气体积分数从17%提高到36%,当含水率为84%时,H2+CO的含量(体积分数)达到最大值;提高热解升温速率能使气相产物产率得到相应增加.湿污泥在高温条件下进行的快速热解过程,一次性完成了污泥干燥、热解和气化,更有利于氢气组分和其他可燃气体的生成,所得气体热值高达12MJ.m-3以上.     

微波间断加载作用下煤中瓦斯解吸响应特征实验研究

为揭示煤中瓦斯解吸过程中加载微波作用对解吸特性的影响,分析探讨了微波辐射促进煤层瓦斯解吸的基本原理,研制了微波作用下煤中瓦斯解吸实验装置,对微波间断加载作用及无微波作用条件下煤中瓦斯解吸特性进行了对比实验研究。实验表明:微波作用对煤中瓦斯解吸具有明显的促进作用,微波作用时间越长,解吸量越大,解吸率越高。在微波作用40 s条件下,微波间断加载作用使得煤样瓦斯解吸量增加290%,解吸率达到87%,解吸速度最大提高率为1 020%。     

气候变暖对中国夏热冬冷地区居住建筑采暖降温年耗电量的影响

20世纪80年代中期以来的气候变暖,尤其是90年代中期以来的气候显著变暖带给社会经济发展的利与弊,一直以来受到广泛关注。气候变暖对于建筑耗能,尤其是对采暖和降温总耗能的影响很值得研究。论文以主要使用电能进行空间调节的中国夏热冬冷地区为对象,以《夏热冬冷地区居住建筑节能设计标准JCJ134-2001》中所规定的采暖、降温耗电量限值为依据,研究了气候变暖对该区居住建筑单位面积采暖年耗电量、降温年耗电量及采暖降温年耗电总量的影响。结果表明,1986年以来的气候变暖,尤其是1996年以来的气候显著变暖,理论上使夏热冬冷地区居住建筑单位面积采暖年耗电量降低;同时增加了相当一部分地区居住建筑单位面积降温年耗电量;除个别地区外,气候变暖理论上使中国夏热冬冷地区居住建筑单位面积采暖降温耗电总量普遍下降。     

液化石油气储运容器不同受热条件下的温度压力的估算

提出了液化石油气储运容器在不同受热条件下,容器内的温度和压力的简化的计算方法,可用于此类火灾原因的分析认定、安全分析等,对火灾的扑救也具有十分重要的意义。     

微波焙烧法与马弗炉焙烧法处理废脱硝催化剂的效果比较

用Na_2CO_3作为助溶剂、Na_2O_2作为消解剂,采用微波焙烧法和马弗炉焙烧法消解处理废钒钨钛脱硝催化剂。通过XRF、BET、XRD和NH_3-TPD技术对两种消解方法制得的钛钨粉样品进行了表征。表征结果显示,与马弗炉焙烧法相比,微波焙烧法得到的钛钨粉纯度更高,TiO_2与WO_3含量之和大于96.7%(w),且该钛钨粉还具有更高的比表面积和酸性,可以作为钒钨钛脱硝催化剂的生产原料再利用。     

腐朽坑木与煤混合物升温氧化特性研究

为研究煤层及腐朽坑木着火特性,采集巷道内腐朽坑木与煤样并进行混合,对其混合物进行燃点测定和程序升温实验;通过对不同煤木混合物在升温过程中产生气体的规律性进行分析,优选出混合物产生的单一气体指标及复合指标.研究结果表明:随朽木在混合物中的比例上升,混合物燃点呈下降趋势,且CO,C2 H4等指标气体出现更早,CO产生量更大...     

Aspects on the analysis of 210Po

There has been little development regarding analysis of polonium (Po) in environmental samples since the 1960ies. This is due to the straightforward spontaneous deposition of this element on silver (Ag), nickel (Ni) or copper (Cu) without any radiochemical separation. For many years, no radiochemical yield determinant was used and it was generally supposed that the yield was 100% after two depositions. Counting was often done using ZnS scintillation counter coupled to a photomultiplier tube. However, the use of the yield determinants ²⁰⁸Po and ²⁰⁹Po and the development of alpha spectrometry showed that the yield was lower. Furthermore, the tendency of Po to volatilize at low temperatures constrains the sample preparation techniques; dry-ashing cannot be used. But during the wet-ashing procedure, there are still some losses.The aim of this study was to evaluate the Po losses during wet-ashing by the use of a double-tracer technique. We have found that the losses were about 30% when open glass beakers were used and about 17% when the samples were digested in microwave oven. When long-necked bottles (Kjeldahl flasks) were used, a loss of about 20% was registered.It has also been observed that ²¹⁰Pb to some extent is plating out together with its daughter nuclide Po during the electrochemical deposition. This will result in a systematic error since an unknown amount of supported ²¹⁰Po will be produced from the ²¹⁰Pb decay depending on the fraction of ²¹⁰Pb being deposited on the disc and the waiting time between deposition and measurement of the sample. A further consequence of this is that in the assessment of the ²¹⁰Pb content in the sample, very often the remaining liquid is stored after deposition for build-up of ²¹⁰Po. Since some ²¹⁰Pb is lost on the disc, the result for ²¹⁰Pb will be too low. Both these systematic errors give rise to a too high ²¹⁰Po/²¹⁰Pb ratio. The fraction of ²¹⁰Pb which is plating out has been assessed in this study for different matrices and is about 50-90%. During the measurement by solid state Si-detectors, some Po is evaporated in the vacuum conditions contaminating the detectors. Experiments have here been done by heating the discs after deposition which indicate that less Po is evaporated from Ag than from Ni. The losses from Ag are less than that from the other metals probably due to a deeper penetration into the surface of Po. We conclude that in most aspects, Ag is better to use than the other plating metals.     

加热酸化-Fenton氧化处理乳化液废水

采用加热酸化-Fenton氧化处理乳化液废水,在加酸量为1．0mL98％H2SO4／100mL乳化液、加热温度95℃、加热时间1h条件下,初始COD〉20万mg／L,浊度〉8000NTU的乳化液COD降低到46592mg／L,浊度降低到20NTU,加热和酸化的联合过程达到了良好的破乳效果;破乳后的出水在ρ（Fe2＋）／ρ（H2O2）=1：30、ρ（H2O2）和（COD）=1．4、pH=4的条件下进行Fenton氧化,处理后的出水COD可降到18600mg／L,去除率达61．4％,其B／C可由破乳后的0．11提高到0．43,废水的可生化性大大提高,为后续处理创造了可能。