上海市居民生活用能消费碳排放测算与分析研究

根据上海市居民生活能源消费相关的能源消费数据,采用统计分析方法,从最终需求角度评估了2001年-2010年居民生活能源消费及其碳排放。研究发现2001年-2010年上海市居民生活用能碳排放量从173．47万t增长到391．87万t,居民生活用能碳排放量呈较快上升趋势,但总体处于较低水平。居民生活用能消费结构从以原煤和电力为主转变为以油品电力消费为主,原煤天然气综合利用的消费模式。未来一段时期内上海市需要合理拓展居民生活用能排放空间。     

乡镇垃圾综合利用途径分析研究

社会主义新农村建设推动了乡镇经济的发展,但乡镇的环境问题并没有随之解决,而固体废弃物的综合利用成为解决当前乡镇环境问题的有效手段之一。乡镇垃圾现状分析表明,其组分以有机易腐成分为主．不适用于城市垃圾的处理方式。乡镇垃圾经合理分类,其综合利用的主要途径有三条,包括可回收垃圾一回收一循环再利用,有机垃圾制肥-肥料-回田,餐厨垃圾、人畜粪便、秸秆等有机垃圾厌氧发酵-沼气-热能或电能。该途径可最终实现乡镇垃圾的资源化和能源化。     

能源承载力预测分析方法的研究与应用研究

能源需求和人口、经济密切相关。能源需求分析是在一定的人口和经济增长假设下进行的。从投入产出角度看,能源需求的高低取决于终端需求与满足终端需求的中间过程。经济结构的变化,经济增长模式的选择,技术进步,优质能源的可获得性,环境保护要求等因素会对终端需求和中间过程产生影响。由于资源对国家和地区的重要性,资源承载力的研究显得尤为重要。因此有必要对一个区域的能源需求量作出预测和分析,提高区域发展和管理的科学性,从而实现区域的可持续发展。     

基于提升能源化工基地清洁生产水平的节能减排潜力分析

文章以榆林能源化工基地代表性的支柱产业为例,开展依靠科技进步提升清洁生产水平的节能减排潜力分析。分析结果表明,至"十二五"末期榆林能源化工基地的支柱产业分别将清洁生产水平提高至一级或二级,可减少的二氧化硫排放量是3 451.8吨/年和1 094.3吨/年,氮氧化物排放量是5 333.5吨/年和1 962.5吨/年。     

铁阳极电解脱色直接黄11染料模拟废水

研究采用铁为阳极电化学法处理直接黄11染料模拟废水脱色性能的影响进行研究。影响因素包括:电流密度、pH值、染料浓度和电解质浓度。研究结果表明,电流密度大有利于染料废水脱色,但能耗消耗大;初始溶液在中性条件下不仅取得很好的处理效果,而且脱色能耗较低;随着染料初始浓度增加脱色率和脱色能耗降低的趋势;随着电解质浓度升高染料脱色率下降的趋势,脱色能耗先减少,然后缓慢增大。在染料初始浓度50 mg/L、pH值为7.11、电流密度2.083 mA/cm2、电解质Na2SO4浓度0.01 mol/L、温度20℃、搅拌速度600 r/min、电解时间60min条件下,脱色率达到92.2%,脱色能耗1.709 kW.h/kg染料。     

城镇生活污水厂实行清洁生产途径分析

结合企业清洁生产理论,根据污水处理厂实际情况,从“节能、降耗、减排、增效”出发,详细阐述了污水厂实行清洁生产的途径。指出节约电能、新鲜水、药剂,减少污染物排放是污水处理厂清洁生产的主要出发点。并进行实例分析。     

沼液复合型杀虫剂的田间应用试验研究

通过沼液复合型杀虫剂的田间应用试验,对各种沼液复合型杀虫剂的抗病防虫性能进行了深入研究.在大田应用条件下测试了沼液复合型杀虫剂的杀虫效果.结果表明,该沼液复合型杀虫剂对蚜虫的毒杀作用均比较明显.为了推进沼液复合型杀虫剂的商业化进程,提出便于其田间应用的各种最佳配比浓度,即BP01号、BP02号、BP03号、BP04号、BP05号沼液复合型杀虫剂抗病防虫性能最佳的配比分别为9 500倍液、26000倍液、11 667倍液、22 000倍液和13 333倍液.     

Oxidation inhibition of sulfite in dual alkali FGD system

A laboratory-scale well-mixed thermostatic reactor with continuously blasting air was used to investigate the oxidation inhibition of sulfite in dual alkali flue gas desulfurization （FGD） system. The effects of operating parameters such as pH value and catalyst concentration on the oxidation were studied. Sodium thiosulfate was used in the system, and was found that it significantly inhabited the sulfite oxidation. In the absence of catalyst, sodium thiosulfate at 12.67 mmol/L had an inhibition efficiency of approximately 98%. While in the presence of catalyst, sodium thiosulfate at 26.72 mmol/L had an inhibition efficiency less than 85.0%. The oxidation reaction order of sulfite in the sodium thiosulfate was determined to be -1.90 and 4）.55 in the absence and presence of the catalyst, respectively. Apparent activation energy of oxidation inhibition was calculated to be 53.9 kJ/mol. Pilot tests showed that the consumption rate of thiosulfate agreed well with the laboratory-scale experimental results.     

Inorganic nitrogen removal of toilet wastewater with an airlift external circulation membrane bioreactor

Removal of inorganic nitrogen (inorganic-N) from toilet wastewater, using a pilot-scale airlift external circulation membrane bioreactor (AEC-MBR) was studied. The results showed that the use of AEC-MBR with limited addition of alkaline reagents and volumetric loading rates of inorganic-N of 0.19-0.40 kg inorganic-N/(m3·d) helped achieve the desired nitrification and denitrification. Furthermore, the effects of pH and dissolved oxygen (DO) on inorganic-N removal were examined. Under the condition of MLSS at 1.56-2.35 g/L, BOD5/ammonia nitrogen (NH/-N) at 1.0, pH at 7.0-7.5, and DO at 1.0-2.0 mg/L, the removal efficiencies of NH4 -N and inorganic-N were 91.5% and 70.0%, respectively, in the AEC-MBR. The cost of addition of alkaline reagent was approximately 0.5-1.5 RMB yuan/m3, and the energy consumption was approximately 0.72 kWh/m3 at the flux of 8 L/(m2·h).     

Kinetics of selective catalytic reduction of NO by NH3 on Fe-Mo/ZSM-5 catalyst

The catalyst of Fe-Mo/ZSM-5 has been found to be more active than Fe-ZSM-5 and Mo/ZSM-5 separately for selective catalytic reduction (SCR) of nitric oxide (NO) with NH3. The kinetics of the SCR reaction in the presence of O2 was studied in this work. The results show that the observed reaction orders were 0.74-0.99, 0.01-0.13, and 0 for NO, O2 and NH3, respectively, at 350-450℃. And the apparent activation energy of the SCR was 65 kJ/mol on the Fe-Mo/ZSM-5 catalyst. The SCR mechanism was also deduced. Adsorbed NO species can react directly with adsorbed ammonia species on the active sites to form N2 and H2O. Gaseous O2 might serve as a reoxidizing agent for the active sites that have undergone reduction in the SCR process. It is also important to note that a certain amount of NO was decomposed directly over the Fe-Mo/ZSM-5 catalyst in the absence of NH3.