中国区域能源、经济与环境耦合的动态演化

文章全面解析了系统耦合机制,以此为基础构建了能源、经济与环境三系统耦合模型,测算了1995—2014年中国四大区域三大系统间的耦合协调水平,并从时空两个维度对区域三系统交互关系的变化特征以及差异做出了全面讨论。结果表明,1各省区经济和环境综合指数呈持续上升的良好态势,而能源综合指数在小幅波动中保持了较为稳定的发展状态,同时三者关系极为密切,具体表现为三类指数的变动具有显著的相关性。2三系统交互作用的耦合度均保持不断递增的演化趋势,但绝对水平较低,且区域间差异较为明显,整体上呈现由东到西递减态势。3三系统的耦合变化与能源-经济、能源-环境和经济-环境三类二元系统的协调发展具有密切的相关性。4在探索三系统耦合协调的持续发展路径时,需重点引导三系统打破固有束缚,通过有秩序的相互配合产生单个系统所不具备的发展能力。而从现实状态看,在当前面临经济下行、资源环境不可持续以及区域发展差异扩大等问题的严峻挑战,各省区需结合本区域实际发展状况和比较优势制定发展规划。东部需以雄厚的经济实力为基础强化技术创新,以带动能源高效利用和环境保护;中部和东北需调整能源消费结构并提高能源利用效率;西部则应将重点放在绿色发展和防范环境风险两方面。     

东北地区农业现代化与新型城镇化协调发展研究

新型城镇化与农业现代化作为"三化"、"四化"乃至"五化"战略的重要核心内容,研究新型城镇化与农业现代化的协调发展对于开创中国未来城乡经济社会发展一体化的新格局至关重要。以东北三省34个地级城市为研究对象,构建农业现代化与新型城镇化的评价指标体系,结合熵值赋权、变异系数赋权的综合确权法测算城市农业现代化与新型城镇化的发展水平,基于耦合协调度模型探讨二者的耦合度与协调发展度,并划分其阶段类型,研究表明:(1)东北三省新型城镇化的发展水平排序:辽宁省吉林省黑龙江省,农业现代化的发展优势排序:黑龙江省辽宁省吉林省;辽宁与吉林省的新型城镇化发展速度超前于农业现代化,仅黑龙江省的新型城镇化发展滞后于农业现代化;(2)东北三省新型城镇化的高值区分布在以哈尔滨为核心的黑龙江省西南、以长春为核心的吉林省中部、以沈阳和大连为核心的辽宁省中部及南端,农业现代化的高值区分布在哈—大—齐—绥沿线的松嫩平原;沈阳、大连、哈尔滨、长春新型城镇化水平居于东北三省前列,哈尔滨、沈阳、齐齐哈尔、绥化农业现代化水平位于首位;(3)辽宁省新型城镇化与农业现代化的耦合协调发展度均强于黑龙江省,吉林省略低;耦合度高值区位于黑龙江省东北部的三江平原、辽宁省的沿海经济带,协调发展度高值区位于黑龙江省西南部的松嫩平原及以长春、沈阳、大连为核心的小范围圈层区域;仅哈尔滨与沈阳市处于勉强协调阶段,多数城市处于高强度、中高强度拮抗耦合与轻度、中度失调阶段。     

中部地区资源型城市城市化与生态环境动态耦合关系

通过构建城市化与生态环境耦合模型,利用中部地区37个资源型城市2005—2014年城市化系统和生态环境系统的30个指标数据,对城市化与生态环境耦合关系动态变化进行测度,并比较分析不同类型资源型城市城市化水平、生态环境水平及其二者耦合协调度的变化。结果表明:(1)2005以来人口城市化对资源型地区城市化综合水平的影响力减弱,社会城市化的影响力逐渐加大并趋于比较重要的地位。尽管资源条件对资源型城市的生态环境综合水平影响最大,但生态环境治理水平对资源型地区生态环境综合水平的影响力正变得日益重要。(2)各城市间城市化综合水平差异较大,而生态环境综合水平差异较小。自2005年以来城市化发展综合水平的城际差异无较大改变,但生态环境发展水平的城际差异正变得日趋缩小。位于山西省的资源型城市城市化综合水平和生态环境综合水平的变动较之其他省份更为显著。(3)中部地区资源型城市的协调类型处于勉强协调、初级协调和中级协调,并以初级协调型为主。2005以来中部地区多数资源型城市城市化与生态环境关系保持不变,关系恶化的资源型城市主要分布在安徽、江西和湖南,关系更为协调的资源型城市主要位于山西。(4)不同类型资源型城市的城市化综合水平差异显著,而生态环境综合水平差异并不明显。再生型和衰退型城市的耦合协调度水平较高,成熟型城市的耦合协调度较低。(5)城市化滞后仍是资源型城市城市化与生态环境关系不协调发展的主要原因。     

长江中游城市群经济-城市-社会-环境耦合度空间差异分析

以长江中游城市群的36个城市为例,构建了经济发展、城市化、社会保障、生态环境综合评价指标体系,运用耦合度模型评估了36个城市2011~2013年的耦合度,并利用GIS技术分析系统的得分与耦合度的空间分布特征。结果表明:长江中游城市群的36个城市的经济发展、城市化和社会保障水平的空间分布比较相似,三者间存在显著的正相关关系。但是,存在显著性的地区差异。36个城市生态环境得分均值很高,城市之间差异很小。从耦合度的空间分布来看,长江中游城市群明显存在3个高耦合度的聚集区域,即长株潭城市圈,武汉-南昌(含鄂州、黄石和九江)城市带和鄂北4市,即十堰、襄阳、宜昌和荆门。最后,36个城市之间耦合度的差异呈现逐年缩小的趋势。     

A full-scale sequencing batch reactor system for swine wastewater treatment

A full-scale sequencing batch reactor (SBR) system was evaluated for its ability to remove carbon and nitrogen from swine wastewater. The SBR was operated on four, six-hour cycles each day, with each cycle consisting of 4.5 hours of “React,” 0.75 hours of “Settling”, 0.75 hours for “Draw” and “Fill.” Within each cycle, an amount of wastewater equivalent to about 5% of the reactor volume (5,500 litres) was removed and added. The SBR system was able to remove 82% of biochemical oxygen demand (BOD) and more than 75% of nitrogen. Even though the SBR effluent, with an average effluent BOD₅ of about 588 mg L^{? 1}, did not meet the discharge criteria, it enabled a reduction of the land base required for land application of swine wastewater by about 75%. Results indicated that the SBR system was a viable method for the treatment of swine wastewater.     

Treatment of wastewater from red and tropical fruit wine production by zeolite anaerobic fluidized bed reactor

A study of the anaerobic treatment of wastewaters derived from red (RWWW) and tropical fruit wine (TFWWW) production was carried out in four laboratory-scale fluidized bed reactors with natural zeolite as bacterial support. These reactors operated at mesophilic temperature (35°C). Reactors R1 and R2 contained Chilean natural zeolite, while reactors R3 and R4 used Cuban natural zeolite as microorganism support. In addition, reactors R1 and R3 processed RWWW, while reactors R2 and R4 used TFWWW as substrate. The biomass concentration attached to zeolites in the four reactors studied was found to be in the range of 44–46 g volatile solids (VS)/L after 90 days of operation time. Both types of zeolites can be used indistinctly in the fluidized bed reactors achieving more than 80%–86% chemical oxygen demand (COD) removals for organic loading rates (OLR) of up to at least 20 g COD/L d. pH values remained within the optimal range for anaerobic microorganisms for OLR values of up to 20 and 22 g COD/L d for RWWW and TFWWW, respectively. Toxicity and inhibition levels were observed at an OLR of 20 g COD/L d in reactors R1 and R3 while processing RWWW, whereas the aforementioned inhibitory phenomena were not observed at an OLR of 24 g COD/L d in R2 and R4, treating TFWWW as a consequence of the lower phenolic compound content present in this substrate. The volatile fatty acid (VFA) levels were always lower in reactors processing TFWWW (R2 and R4) and these values (< 400 mg/L, as acetic acid) were lower than the suggested limits for digester failure. The specific methanogenic activity (SMA) was twice as high in reactors R2 and R4 than in R1 and R3 after 120 days of operation when all reactors operated at an OLR of 20 g COD/L d.     

城市污水条件下ASBR厌氧氨氧化的启动与脱氮性能

采用ASBR在城市污水条件下进行厌氧氨氧化的启动与脱氮性能研究。实验接种好氧硝化污泥,在温度为(35±1)℃、HRT为24 h、pH为7.3～8.5的条件下经过130 d的培养,成功启动了厌氧氨氧化反应。实验结果表明,厌氧氨氧化反应稳定运行时,TN容积负荷平均为0.179 kg/(m3.d),NH4+-N、NO2--N和TN去除率分别达到了95.30%、91.30%和76.28%。启动期和稳定运行期NH4+-N、NO2--N去除量和NO3--N生成量的比值分别达到1∶1.54∶0.25和1∶1.27∶0.27;稳定运行期进出水pH差值由启动时的0.85下降到0.24。启动期反硝化和厌氧氨氧化反应同时存在而在稳定运行期厌氧氨氧化发展成为主导反应。MLSS和MLVSS/MLSS先减少后增加,反映了启动过程中硝化细菌、反硝化细菌的衰亡和厌氧氨氧化菌逐渐富集的过程,这与反应器的宏观运行效果相一致。     

Removal of tetrabromobisphenol A by conventional activated sludge, submerged membrane and membrane aerated biofilm reactors

The goal of this study was to compare removal efficiencies of tetrabromobisphenol A (TBBPA) using typical wastewater treatment technologies, and to identify the most significant mechanisms of removal. Two types of municipal wastewater reactors were studied: a full-scale conventional activated sludge (CAS) reactor with tertiary treatment; and three pilot-scale membrane bioreactors (MBRs) having different sludge retention times (SRTs). All four reactors were fed the same influent. A third reactor type, a membrane aerated biofilm reactor (MABR) was fed tap water, ammonia, and TBBPA. TBBPA in municipal influent ranged from 1 to 41 ng L⁻¹ (n = 10). The CAS effluent had an average TBBPA concentration of 0.7 ± 1.3 ng L⁻¹ (n = 3). Effluent concentrations from the MBRs were an average of 6 ± 6 ng L⁻¹ TBBPA (n = 26). Significant TBBPA removal was observed in the MABR throughout the 5 week of study (p ? 0.05). Removal of TBBPA from wastewater treatment was found to be due to a combination of adsorption and biological degradation. Based on experimental results, nitrification is likely a key process therein. No significant relationship between removal of TBBPA and SRT was identified (p ? 0.05).     

厌氧滤池处理纺织印染废水的中试研究

对厌氧滤池反应器处理难降解印染废水进行中试研究。结果表明,厌氧滤池反应器水力停留时间(HRT)在8.1～14.6 h之间,进水COD浓度波动较大(500～1 000 mg/L)时,对COD平均去除率为20%。印染废水的BOD5/COD由0.23提高到0.35,废水可生化性明显改善。印染废水中硫酸根浓度略有下降,去除浓度为70 mg/L左右。厌氧滤池进出水颜色明显变化,由紫红色变为蓝黑色,紫外可见光谱分析表明废水中的有机物结构发生变化。     

常温条件下2种厌氧折流板反应器处理淀粉废水的启动实验

为了研究厌氧折流板反应器在常温下的启动情况,在22.5～30.2℃条件下,对不加填料的5隔室厌氧折流板反应器和加填料的4隔室复合式厌氧折流板反应器同步进行了启动实验。实验用水为高浓度淀粉废水,两反应器采用相同的启动策略,即梯度增加进水COD浓度与降低水力停留时间相结合的方式。两反应器有效容积均为47.8 L,启动初始负荷为0.6 kg COD/(m3.d),逐渐增加到10 kg COD/(m3.d)。实验表明,经过6个阶段87 d的运行,反应器启动完成,并成功培养出颗粒污泥,两反应器对COD的去除率都能达到85%以上。在启动过程中两反应器对COD的去除效率相近。