高浓度洗毛废水生物降解的研究

根据高浓度洗毛废水的水质特性,选择、驯化出高效污泥和菌株,并对生物降解该废水时的工艺、污泥量、时间三要素进行了深入的研究．结果表明,对于物化处理彻底的废水, Ｈ／ Ｏ 工艺（ 水解／ 好氧工艺） 与好氧工艺处理差异不大;７０ ％ 左右物化效果时, Ｈ／ Ｏ 工艺处理时, Ｃ Ｏ Ｄｃｒ 去除率增加;废水在处理过程中成分变化大,后段水可用筛选优势菌的方法处理．实验室流动模型运行结果为：在原水ρ（ Ｃ Ｏ Ｄｃｒ） １８５４４ ｍｇ／ Ｌ 和设定ｔ Ｈ Ｒ（ 延滞期） 下,混凝后出水ρ（ Ｃ Ｏ Ｄｃｒ） ５３２２ ｍｇ／ Ｌ,水解池出水ρ（ Ｃ Ｏ Ｄｃｒ） ４７６３ ｍｇ／ Ｌ,好氧池出水 Ｃ Ｏ Ｄｃｒ１９９ ．９ ｍｇ／ Ｌ,总 Ｃ Ｏ Ｄｃｒ去除率为９８ ．９ ％     

湘江铜霞段镉环境容量模型研究

镉是一种毒性很强的累积性重金属污染物,在<污水综合排放标准>中是第一类污染物.为了控制湘江铜霞段的镉污染,根据该段水环境功能要求及水力学特征,在分析多年水文参数和相应环境监测资料的基础上,根据质量守恒定律,应用稳态二维模型建立了该江段镉环境容量模型.经用该段2002年的3月、6月、9月和12月份的有关监测数据检验,结果表明,模型预测值与实测值相对误差为1.38%～21.4%,具有较好的相关性.该模型可用于该江段镉环境容量及水体中镉浓度时空分布的预测预报,对强化该江段环境管理、实施区域含镉废水污染源总量控制具有指导意义.     

企业节能量计算方法浅析

阐述了企业在实施节能降耗过程中普遍采用的节能量计算方法,对产品单耗节能量和技术措施节能量进行了分析,并对比了采用单耗法和技术措施法计算节能量的适用范围和局限性,指出两种方法对企业的意义,提出了在节能量计算过程中的注意事项和几点认识。     

运用经验公式分析BOD5

运用经验公式分析BOD5,节省时间、人力、财力,对污染源企业用此方法是可行的。     

城镇燃气埋地含缺陷聚乙烯管道应力分析

建立了埋地含缺陷聚乙烯管道模型,应用有限元方法计算管道的应力和变形量,分别考虑管道内压、地面载荷和管道缺陷深度变化对管道应力和变形的影响。研究结果表明,管道最大应力随管道内压的增大而增大;随地面载荷的增加呈先减小后增大趋势;随管道缺陷深度增大而增大。管道变形量随内压增大而增大,但增长较小;随地面载荷增大而增大,增长较大;管道缺陷深度只对管道缺陷处变形量有影响。研究结果为确定城镇燃气聚乙烯管道工作能力提供了理论依据。     

Phast validation of discharge and atmospheric dispersion for pressurised carbon dioxide releases

The consequence modelling package Phast examines the progress of a potential incident from the initial release to the far-field dispersion including the modelling of rainout and subsequent vaporisation. The original Phast discharge and dispersion models allow the released substance to occur only in the vapour and liquid phases. The latest versions of Phast include extended models which also allow for the occurrence of fluid to solid transition for carbon dioxide (CO₂) releases.As part of two projects funded by BP and Shell (made publicly available via CO2PIPETRANS JIP), experimental work on CO₂ releases was carried out at the Spadeadam site (UK) by GL Noble Denton. These experiments included both high-pressure steady-state and time-varying cold releases (liquid storage) and high-pressure time-varying supercritical hot releases (vapour storage). The CO₂ was stored in a vessel with attached pipework. At the end of the pipework a nozzle was attached, where the nozzle diameter was varied.This paper discusses the validation of Phast against the above experiments. The flow rate was predicted accurately by the Phast discharge models (within 10%; considered within the accuracy at which the BP experimental data were measured), and the concentrations were found to be predicted accurately (well within a factor of two) by the Phast dispersion model (UDM). This validation was carried out with no fitting whatsoever of the Phast extended discharge and dispersion models.     

Validation of discharge and atmospheric dispersion for unpressurised and pressurised carbon dioxide releases

This paper discusses the validation of discharge and subsequent atmospheric dispersion for both unpressurised and pressurised carbon dioxide releases using the consequence modelling package Phast.The paper first summarises the validation of the Phast dispersion model (UDM) for unpressurised releases. This includes heavy gas dispersion from either a ground-level line source (McQuaid wind-tunnel experiments) or an area source (Kit-Fox field experiments). For the McQuaid experiments minor modifications of the UDM were made to support line sources. For the Kit Fox experiments steady-state and 20-s finite-duration releases were simulated for both neutral and stable conditions. Most accurate predictions of the concentrations for finite duration releases were obtained using the UDM Finite Duration Correction method.Using experiments funded by BP and Shell and made available via DNV's CO2PIPETRANS JIP, the paper secondly summarises the validation of the Phast discharge and dispersion models for pressurised CO₂ releases. This modelling accounted for the possible presence of the solid CO₂ phase following expansion to atmospheric pressure. These experiments included both high-pressure steady-state and time-varying cold releases (liquid storage) and high-pressure time-varying supercritical hot releases. Both the flow rate and the concentrations were found to be predicted accurately.The above validation was carried out with no fitting whatsoever of the Phast extended discharge and dispersion models.     

2015年我国废钢铁总资源及可获量的推定

概述了国内资深专家对我国废钢铁资源现状和发展前景的看法,并对我国2015年废钢铁总资源及可获量进行推定。     

乙酰丙酮荧光法在线监测环境空气中的甲醛

我国现行环境空气中甲醛的标准测定方法普遍难以满足当前大气监测中对痕量浓度水平甲醛的监测需要。在乙酰丙酮分光光度法的基础上改进得到的乙酰丙酮荧光法具有更低的检出限和更高的灵敏度,适用于大气中痕量浓度水平甲醛的监测。基于乙酰丙酮荧光法设计了甲醛在线监测系统,并对其主要性能指标进行了评估测试。测试结果显示,该系统的吸收效率为98.9%~100.1%,检出限为0.045 4×10^-9,精密度为0.44%,线性误差为-0.55%,线性范围为0.0~80.0×10^-9,响应时间为282 s,单日零点漂移为-0.04×10^-9~1.33×10^-9,单日跨度漂移为-0.90×10^-9~3.45×10^-9。测试结果表明,其各项性能指标均能满足当前对大气环境中痕量浓度水平甲醛的监测需求。     

两性磁化炭添加比例对河流沿岸土吸附Cu2+的影响

将两性(十二烷基二甲基甜菜碱)修饰磁化炭分别以质量分数0、1%和2%加入嘉陵江流域(川渝段)内苍溪(CX)、南部(NB)、嘉陵(JL)和合川(HC)沿岸土中,考察各混合土样对Cu^2+的等温吸附和热力学特征。结果表明:混合土样对Cu^2+的最大吸附量为58.36 mmol/kg~366.85 mmol/kg,添加等量两性磁化炭时各混合土样对Cu^2+吸附量表现为JL>NB>CX>HC的趋势,且添加比越高吸附能力越强。各混合土样对Cu^2+的吸附为自发、吸热和熵增的反应过程,对Cu^2+的吸附量与温度和pH值均呈正相关关系。当离子强度为0.1 mol/L时,各混合土样(除HC外)对Cu^2+的吸附量最大。