废塑料再生过程废水中微塑料去除模拟试验

微塑料是一种存在于不同环境介质中的新兴污染物,主要来源于废弃塑料制品,其存在污染范围广、潜在环境污染大的问题.废塑料再生企业生产废水中微塑料浓度远高于其他类型废水,对其生产废水中的微塑料进行处理具有重要的环境意义.模拟废塑料再生过程的生产废水并进行微塑料去除的絮凝沉淀试验,研究絮凝剂投加量、pH、水力快速搅拌条件的单因素和正交试验对废水中微塑料去除率及其各因素作用的影响.结果表明:①当PAC (聚合氯化铝)投加量为10 mL,PAM (聚丙烯酰胺)投加量为7 mL,pH为9,水力快速搅拌条件为100 r/min下维持40 s再200 r/min下维持40 s时,微塑料的总去除率最高,达91%.②PAC投加量是影响微塑料去除效果的主要因素,其次是pH.③微塑料的去除率与其本身的密度有关,密度大的ABS (acrylonitrile butadiene styrene,丙烯腈-丁二烯-苯乙烯)去除率最高,密度小的PE (polyethylene,聚乙烯)去除率最低.④不同粒径区间的微塑料去除率区别较大,粒径小(0.1~0.25 mm)的微塑料去除效果最好.研究显示,通过控制PAC和PAM的投加量、pH和水力搅拌速率等条件,能够有效将废水中的微塑料通过絮凝沉淀的方法去除,从而达到净化含微塑料生产废水的目的.      

中国乘用车塑料的动态物质流分析

结合行业信息并基于动态物质流模型,本文对1950~2050年间中国乘用车塑料流量与存量进行了历史测算与情景分析.历史测算表明：1950~2018年国内乘用车行业累计消耗了以聚丙烯（PP）、聚氨酯（PU）等为主的塑料3278万t,产生了337万t塑料废弃物;报废汽车拆解后的车用废塑料仅28%得到回收利用.针对未来情况,本文设计了乘用车保有量、单车塑料使用量两大关键因素下的不同情景组合.结果显示车用塑料存量及废塑料产生量将大幅增长,到2050年存量将达到0.7~2.7亿t,废塑料产生量将达到500~1600万t,汽车拆解和塑料再生等相关行业对此应充分关注.到2050年车用废塑料回收率若能提升至80%,将减少376万t/a的车用废塑料填埋或焚烧,显著减少环境风险.     

Modelling of Materials Policies

This paper discusses the REAP1 model and its application for the analysis of CO₂ reduction and waste management policies for Japanese petrochemicals. The pros and cons of this modelling approach in comparison to other tools is elaborated. This is followed by a discussion of the model code and the modelling results. The results show that CO₂ policies can have significant impacts on waste flows and waste policies can have significant CO₂ benefits. As a consequence both effects must be considered in policy assessment. Pricing instruments are recommended instead of regulations because of the complex physical relations in the materials life cycle that extend beyond sector boundaries. A taxation approach is superior to a subsidy approach because rebound effects can be avoided.     

废塑料与炼焦配煤共焦化产物的分析

利用2kg模拟焦炉，进行了首钢炼焦配煤与北京市石景山区生活垃圾中的废塑料的共焦化实验。研究结果表明，添加废塑料有提高焦油收率和减少水的收率的趋势；但添加废塑料对成焦率、焦油产率及水产率的影响随废塑料处理方法和废塑料添加比例的不同而有差异；采用废塑料型煤或废塑料型煤破碎物与配煤共焦化在提高废塑料添加比例方面具有较大优势。     

废旧塑料的回收利用

废旧塑料是重要的再生资源，合理利用不仅环境保护，也将增加经济效益，阐述了废旧塑料回收利用情况及发展前景。     

生活垃圾中废塑料分选回收技术概述

近年来,废塑料在城市生活垃圾中占有相当大的比例,其含量正呈逐年上涨的趋势,因此对塑料进行分选和资源化利用势在必行。塑料分选技术是摆在我们中间的一项难题,目前生活垃圾废塑料的分选技术五花八门．由于在全国各地废塑料在垃圾中的还水量等因素的影响,现实中能实现废塑料的分选还不成熟。因此,研究一套适合废塑料的分选技术迫在眉睫。     

废弃阻燃塑料热失重行为与分解规律的研究

文章主要是研究废弃电子产品阻燃材料的热解回收方法;主要研究废弃阻燃塑料的热失重规律和热分解产物,以印刷线路板为原料利用差热热重分析仪和热裂解色谱和质谱进行了实验室规模热解实验.结果表明:热失重反应的平均活化能为182.294 kJ/mol,指前因子为3.07×1011s-1,反应的温度区间为580K～600K;随着升温...     

A research on dioxin generation from the industrial waste incineration

By using fluidized-bed furnace and rotary-kiln+stoker furnace and four different kinds of industrial wastes such as waste wood, coffee mill, waste oils and waste plastics, we have drawn the following conclusions:

(1) A relationship between H6CBz and DXN is acquired, which is DXN=0.34×H6CBz^1.1.

(2) The following means of emission reduction can be considered. (a) Reduction of DXN and Cl accumulation within the furnace, (b) control by the incinerated object, (c) control through the precursors of H6CBz, (d) improvement through operational control, (e) ammonia injection into the high-temperature zone of the furnace seems to be effective in reducing DXN and (f) DXN concentration is high with CO above 1800 ppm, though it decreases with CO below ≈10 ppm.     

Studies on enhanced degradable plastics: 1. The geographic variability in outdoor lifetimes of enhanced photodegradable polyethylenes

Studies on three types of enhanced photodegradable polyethylenes showed tensile elongation at break to be a suitable parameter for assessing disintegration due to outdoor weathering. Disintegration rates varied greatly with exposure location, with Arizona the harshest environment and Washington and New Jersey the mildest. The rate of breakdown of the enhanced degradable polyethylenes relative to unmodified plastic was termed an enhancement factor. For the materials studied, average enhancement factors generally ranged from five to fifteen. The location-dependent variability in rate parameters can be mostly explained in terms of different average radiation levels and temperatures at these locations. A duplicate exposure protocol was developed to determine if the test data were complicated by short-term fluctuations in sunlight or temperature during exposure.     

Utilization of red mud as catalyst in conversion of waste oil and waste plastics to fuel

The aim of this study was to investigate the possibilities of using a by-product (red mud) from alumina production as a catalyst for recovery of waste. The conversion of waste mineral oil (WMO) and waste mineral oil/municipal waste plastic (WMO/MWP) blends over red mud (RM), a commercial hydrocracking catalyst (silica–alumina), and a commercial hydrotreating catalyst (Ni–Mo/alumina) to fuel has been studied. The effect of the catalyst and the temperature on the product distribution (gas, liquid, and wax) and the properties of liquid products were investigated. In the case of hydrotreatment of WMO, the liquids obtained over RM at both 400° and 425°C had larger amounts of low-boiling hydrocarbons than that of thermal or catalytic treatment with hydrotreating catalyst. Gas chromatography and nuclear magnetic resonance analysis of the liquid products showed that RM had hydrogenation and cracking activity in hydrotreatment of WMO. In coprocessing of WMO with municipal waste plastics, temperature had an important effect as well as the amount of MWP in the blend and the catalyst type. The hydrocracking at 400°C produced no liquid product. In hydrocracking at 425°C, the product distribution varied with catalyst type and MWP amount. The commercial hydrocracking catalyst had more cracking ability in the conversion of WMO/MWP to liquid and gas fuel than RM. In the case of hydrocracking over RM, the largest amount of liquid having satisfactory quality was obtained only from the blend containing 20% MWP.