中小企业安全生产“供求”与政府管制

从安全生产作为一种"公共产品"的视角,分析中小企业供给与需求状况,得出目前中小企业安全生产处于"供给低、需求低"的非正常状态,说明劳动力市场对安全供求的调节已经失灵;通过对安全管制下中小企业日常安全管理行动的调研,结合相关研究成果,说明中小企业安全生产管制存在"管制失灵";对安全生产管制存在的问题进行分析,并提出以完善安全生产法律法规体系为前提,以加强中小企业安全生产监管信息库建设为基础,以建立和完善中小企业安全生产三大机制为手段将中小企业安全生产引入良性发展轨道。     

针对供热系统的安全节能自控系统设计与开发

针对供热系统存在的水力失衡、能耗高、故障多、事故风险大等问题,分析了系统中的主要能耗环节和危险性,提出了安全节能自控系统的结构,详细研究和分析了主系统和子系统的工作原理及节能机制,设计开发了集实时智能自动监控、预警报警、故障诊断、数据管理、安全分析等功能于一体的安全节能自控系统。所开发系统的工程示范应用表明达到了一定程度的节能降耗、安全稳定和经济运行的良好效果。     

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。     

Evaluation of the technoeconomic feasibility of electrochemical hydrogen peroxide production for decentralized water treatment

• Gas diffusion electrode (GDE) is a suitable setup for practical water treatment. • Electrochemical H₂O₂ production is an economically competitive technology. • High current efficiency of H₂O₂ production was obtained with GDE at 5–400 mA/cm². • GDE maintained high stability for H₂O₂ production for ~1000 h. • Electro-generation of H₂O₂ enhances ibuprofen removal in an E-peroxone process. This study evaluated the feasibility of electrochemical hydrogen peroxide (H₂O₂) production with gas diffusion electrode (GDE) for decentralized water treatment. Carbon black-polytetrafluoroethylene GDEs were prepared and tested in a continuous flow electrochemical cell for H₂O₂ production from oxygen reduction. Results showed that because of the effective oxygen transfer in GDEs, the electrode maintained high apparent current efficiencies (ACEs,>80%) for H₂O₂ production over a wide current density range of 5–400 mA/cm², and H₂O₂ production rates as high as ~202 mg/h/cm² could be obtained. Long-term stability test showed that the GDE maintained high ACEs (>85%) and low energy consumption (<10 kWh/kg H₂O₂) for H₂O₂ production for 42 d (~1000 h). However, the ACEs then decreased to ~70% in the following 4 days because water flooding of GDE pores considerably impeded oxygen transport at the late stage of the trial. Based on an electrode lifetime of 46 days, the overall cost for H₂O₂ production was estimated to be ~0.88 $/kg H₂O₂, including an electricity cost of 0.61 $/kg and an electrode capital cost of 0.27 $/kg. With a 9 cm² GDE and 40 mA/cm² current density, ~2–4 mg/L of H₂O₂ could be produced on site for the electro-peroxone treatment of a 1.2 m³/d groundwater flow, which considerably enhanced ibuprofen abatement compared with ozonation alone (~43%–59% vs. 7%). These findings suggest that electrochemical H₂O₂ production with GDEs holds great promise for the development of compact treatment technologies for decentralized water treatment at a household and community level.     

价值共创视角下非遗研学旅行产品开发研究--基于需求侧的调研

以非遗研学旅行产品为例,需求侧在产品开发中的缺位是造成产品问题的重要原因,可运用价值共创理论指导产品开发。根据调查问卷结果及分析,基于对实际决策人--学生家长的产品选择偏好、考虑因素、价值感知、购买意向与满意度4个维度的分析,提出优化非遗研学产品开发的4个方面建议:政府营造研学氛围,加强制度保障;学校开展非遗教育,发挥桥梁作用;供方考虑市场需求,强化产品内涵;供需两侧共建价值共创平台。     

环渤海河流COD入海通量及其对渤海海域COD总量的贡献

于2013年8月~2014年10月,分季节对环渤海36条入海河流进行了4次调查采样,核算其COD入海通量,并评估其对渤海水质的影响.结果表明,大部分河流都受到了严重污染(COD为地表IV类),但污染最重的河流并不是COD入海通量最大的河流,COD的最大值和COD入海通量的最大值不具有一致性;环渤海河流排入渤海的COD_Cr的年入海通量最大(606万t),其次是酸性COD_Mn的入海通量(62万t),碱性COD_Mn最小,为53万t;环渤海河流在丰水期COD的入海通量约占全年的68%,其次是平水期(28%),枯水期最小(4%);整个渤海海域的碱性COD_Mn总量为239万t,其中环渤海河流输入约占25%.     

洋河-戴河河口海域COD时空分布特征研究

首先应用MIKE 21软件建立了洋河-戴河河口海岸水域水动力与污染物输运数学模型,然后采用实测潮流和化学需氧量(COD)浓度对数学模型进行了验证,最后模拟分析了河口海岸水域COD的输运过程.结果表明,洋河-戴河近岸海域潮波为驻波;潮流为顺岸往复流,涨潮流方向为NE向SW,落潮流方向为SW向NE.涨、落急时刻,河口至外海水域潮流流速递增.COD输运方向与涨落潮潮流方向一致.涨憩时刻,COD高浓度区向河道推进,其面积最小;落憩时刻,COD高浓度区向外海推进,其面积最大;葡萄岛周围潮流流速低,在潮周期内小于0.14m/s,对COD的稀释作用较弱.     

Electrochemical degradation of Acid Red I dye and its treatment by UV light

Degradation of Acid Red I (ARI) dye by electrochemical treatment and UV light irradiation was studied in this work. The effect of the current density and the concentration of NaCl and dye on the decoloration and degradation efficiency were studied and optimized. The UV irradiation was monitored by UV-Vis spectrophotometry and chemical oxygen demand. The kinetic constants for decoloration and degradation were calculated. Degradation of 86% was achieved in 160?min and the first-order kinetic constant was 0.013?min^?1. Degradation products were identified by gas chromatography/mass spectrometry. The mechanism for the degradation of ARI was proposed.     

Optimal locations of monitoring stations in water distribution systems under multiple demand patterns: a flaw of demand coverage method and modification

A flaw of demand coverage method in solving optimal monitoring stations problem under multiple demand patterns was identified in this paper. In the demand coverage method, the demand coverage of each set of monitoring stations is calculated by accumulating their demand coverage under each demand pattern, and the impact of temporal distribution between different time periods or demand patterns is ignored. This could lead to miscalculation of the optimal locations of the monitoring stations. To overcome this flaw, this paper presents a Demand Coverage Index (DCI) based method. The optimization considers extended period unsteady hydraulics due to the change of nodal demands with time. The method is cast in a genetic algorithm framework for integration with Environmental Protection Agency Net (EPANET) and is demonstrated through example applications. Results show that the set of optimal locations of monitoring stations obtained using the DCI method can represent the water quality of water distribution systems under multiple demand patterns better than the one obtained using previous methods.