Examining municipal response to a provincial climate action planning mandate in British Columbia,Canada

The engagement of UK local authorities is vital if national government is to meet its climate change commitments. However, with no mandatory targets at local government level, other drivers must explain engagement. Using a Geographic Information System, this study compares the spatial distribution of action on climate change based on past actions and stated intentions to a suite of relevant independent variables. The Action Index created is among the first to quantify climate change engagement beyond a simple binary measure and provides a useful comparative study to recent work in the USA. The Index enables investigation of both mitigation and adaptation, which show different trends in relation to some variables. The study shows that action is strongest where the voting habits of the local population suggest environmental concern and where neighbouring local authorities are also engaging in action on climate change. Physical vulnerability to the effects of climate change is a motivator for action only where the dangers are obvious. Action is less likely where other resource-intensive issues such as crime and housing exist within a local authority area.     

浅析低碳技术的评价方法

低碳技术可分为3类:减碳技术、无碳技术、去碳技术,选择最优低碳技术是一个项目能否成功的关键。低碳技术评价的内容通常从能源使用率、经济效益、生命周期方面进行评价,对技术的综合性评价的基本方法大致有层次分析法、综合评分法、德尔菲法、熵值法、模糊综合评判法等,这些方法渗透于指标权重分析、模型建立评价当中。通过研究对这些技术的评价方法,确定最优的技术项目,以促进循环经济及可持续发展战略的实施和进行。     

Energy balances,greenhouse gas emissions and economics of biochar production from palm oil empty fruit bunches

This paper presents results from a gate-to-gate analysis of the energy balance, greenhouse gas (GHG) emissions and economic efficiency of biochar production from palm oil empty fruit bunches (EFB). The analysis is based on data obtained from EFB combustion in a slow pyrolysis plant in Selangor, Malaysia. The outputs of the slow pyrolysis plant are biochar, syngas, bio-oil and water vapor. The net energy yield of the biochar produced in the Selangor plant is 11.47 MJ kg⁻¹ EFB. The energy content of the biochar produced is higher than the energy required for producing the biochar, i.e. the energy balance of biochar production is positive. The combustion of EFB using diesel fuel has the largest energy demand of 2.31 MJ kg⁻¹ EFB in the pyrolysis process. Comparatively smaller amounts of energy are required as electricity (0.39 MJ kg⁻¹ EFB) and for transportation of biochar to the warehouse and the field (0.13 MJ kg⁻¹ EFB). The net greenhouse gas emissions of the studied biochar production account for 0.046 kg CO₂-equiv. kg⁻¹ EFB yr⁻¹ without considering fertilizer substitution effects and carbon accumulation from biochar in the soil. The studied biochar production is profitable where biochar can be sold for at least 533 US-$ t⁻¹. Potential measures for improvement are discussed, including higher productivity of biochar production, reduced energy consumption and efficient use of the byproducts from the slow pyrolysis.     

活性炭纤维在油田采出废水处理中的应用

针对油田采出废水的特点,以粘胶基活性炭纤维为原料,经二次炭化和二次活化方式处理制得ACF样品。以ACF为过滤材料,对延长某采油厂经过沉降、分离处理后的采油废水进行动态吸附实验,实验结果表明:经水蒸汽二次活化得到的ACF样品对选用的油田废水处理效果最佳,其悬浮物颗粒粒径中值0.496μm(<1.0μm)、悬浮物含量为0.77mg/L(<1.0mg/L)。     

中国工业园区低碳发展路径研究

中国政府承诺CO₂排放力争于2030年前达到峰值,努力争取2060年前实现碳中和。在工业部门深化应对气候变化和全面推进绿色转型的背景下,数量庞大的工业园区已然成为"十四五"乃至今后一个时期工业领域实现科学、精准碳减排的关键靶点。本研究首先剖析了中国工业园区低碳发展面临的挑战与机遇;进而以2015年为基准年,面向2035和2050年美丽中国建设两阶段战略目标,研究提出了工业园区碳减排的目标、路径和潜力,以期为园区深化低碳发展提供决策参考。研究显示,2015年中国工业园区CO₂排放总量约为28亿吨,占全国总排放量的31%。通过产业结构调整、能效提升、能源结构优化、碳捕集等低碳路径,2015-2050年全国园区预期可减排CO₂ 18亿吨,在2015年基础上减排60%以上;其中,2015-2035年减排8亿吨,2035-2050年减排10亿吨。     

高吸附性能芦苇活性炭的制备方法研究

为实现白洋淀芦苇的有效利用,以白洋淀淀区芦苇(白苇)为原料,以KOH、K2CO3为活化剂,综合考虑制备过程中的剂料比、浸渍时间、活化温度、活化时间等因素的影响,通过正交试验,以碘吸附值和亚甲蓝吸附值综合作为吸附性能高低的评价标准,进行活性炭制备方法研究。结果表明:在以KOH为活化剂、剂料比为4∶1、浸渍时间36 h、850℃下活化1 h的条件下,制备的芦苇基生物质活性炭碘吸附值最高,亚甲基蓝吸附值较高;以K2CO3为活化剂、剂料比为3∶1、浸渍时间12 h、900℃下活化2 h的条件下,制备的芦苇基生物质活性炭有最高的碘吸附值和对亚甲蓝具有良好的吸附性。制备的生物质活性炭碘吸附值均高于国家活性炭一级品标准(1 000 mg/g),具备一定的实用性。     

沼泽湿地植物光合特性及固“碳”潜势对外源氮输入的响应

以沼泽湿地典型草甸植被小叶章(Calamagrostis angustifolia)为研究对象,在三江平原进行了野外培养实验,探讨了4个不同氮素输入水平(0(NO)、6(N6),12(N12)、24(N24)g·m-2· a-1)下沼泽湿地植物生长与光合特性的响应特征,并从光合固"碳"的角度分析了小叶章沼泽湿地的固"碳"潜势.结果表明,外源氮输入明显促进了小叶章的株高、叶面积及植株数,显著增加了碳的生物量积累,到植物生长季结束,N6、N12和N24三个施氮水平下,小叶章地上部分生物量分别比对照增加了58.79%、133.11%和190.55%.同时,小叶章叶片全氮含量、叶绿素、可溶性蛋白和游离氨基酸含量也显著增加,净光合速率明显提高,分别比对照增加了20.70%、26.69%和53.54%.从光合固"碳"的角度来看,外源氮输入能够促使沼泽湿地植物通过光合作用固定更多CO2.     

源分类家庭有机垃圾及其堆肥产品中的PAHs

将源分类家庭生物有机垃圾同秸秆按质量比10:1混合后进行堆肥处理,应用气相色谱-质谱联用仪(GC-MS)按照U.S.EPA 8270方法对生物有机垃圾及其堆肥产品中16种PAHs进行分析测试,比较生物有机垃圾及其堆肥产品中16种PAHs含量、分布及生物降解率,评估堆肥产品PAHs农田风险,综合论述影响家庭有机垃圾堆肥过程中PAHs降解因素,为生物有机垃圾堆肥农田利用提供依据.结果表明,源分类家庭生物有机垃圾及其堆肥产品中∑PAH16化合物含量分别为2.19和1.96mg/ks(以干重计,下同),其中萘、芴、菲、荧蒽含量相对较高,占总量的79.76%和81.76%,这4种有机物的苯环在2-3之间,属于易降解非致癌物质,在农田施用中易被降解;在生物垃圾堆肥过程中∑PAH16的生物降解率为25.88%,堆肥后产品PAHs含量符合农田使用标准.     

Characteristic and mercury adsorption of activated carbon produced by CO2 of chicken waste

Preparation of activated carbon from chicken waste is a promising way to produce a useful adsorbent for Hg removal. A three-stage activation process （drying at 200℃, pyrolysis in N2 atmosphere, followed by CO2 activation） was used for the production of activated samples. The effects of carbonization temperature （409-4500℃）, activation temperature （700-900℃）, and activation time （1-2.5 h） on the physicochemical properties （weight-loss and BET surface） of the prepared carbon wereinvestigated. Adsorptive removal of mercury from real flue gas onto activated carbon has been studied. The activated carbon from chicken waste has the same mercury capacity as commercial activated carbon （Darco LH） （Hg^v： 38.7% vs. 53.5%, Hg^0： 50.5% vs. 68.8%）, although its surface area is around 10 times smaller, 89.5 m^2/g vs. 862 m^2/g. The low cost activated carbon can be produced from chicken waste, and the procedure is suitable.     

Coupling catalytic hydrolysis and oxidation for CS2 removal

CS2 removal was Obtained by coupling catalytic hyidation on bi-functional catalyst.On the hydrolysis active sites,CS2 is hydrolyzed to H2S,while on the oxidation active sites,H2S is oxidized to elemental S or sulfuric acid deposited on the porous support.The above process can be expressed as followsCS2→H2O COS →H2O H2S→O2 S/SO2- 4.H2S oxidation eliminates its prohibition on CS2 hydrolysis so that the rate of coupling removal CS2 is 5 times higher than that of CS2 hydrolysis.The same active energy of hydrolysis and coupling reaction also indicates that H2S oxidation does not change the reaction mechanism of CS2 hydrolysis.Temperature has obvious effect on the process while the mole ratio of O2 concentration to CS2 concentration (O/S) does not,especially in excess of 2.5.The formation of sulfuric acid on the catalyst surface poisons hydrolysis active sites and causes the decrease of left OH-1 concentration on the catalysts surface.Lower temperature is suggested for this bi-functional catalyst owing to the low yield ratio of S/SO4 2-.