智能楼宇的指纹门禁系统

介绍一套基于TMS320VC5509A的指纹识别系统的硬件设计方案,并重点对指纹采集模块、指纹处理模块、CPLD接口模块进行了详细讨论.     

A~2/O工艺重新启动试验的污泥活性恢复研究

以处理实际城市污水的小试规模A2/O工艺为研究对象,在处理工艺稳定运行的基础上关停装置60 d,进行了"饥饿"期内不同关停模式下系统重新启动后污泥活性恢复的研究.结果表明,循环模式、厌氧模式和微曝模式3种不同关停模式下,系统重启第4天,污泥硝化性能及反硝化性能基本恢复甚至超过关停前水平,而脱碳性能和除磷性能的恢复速度则较缓慢,重新启动后系统呈现较好的反硝化除磷能力;重启第12天后3种关停模式出水水质良好,基本满足<城镇污水处理厂污染物排放标准>(GB 18918-2002)一级B标准.不同关停模式下,系统污泥活性恢复速率及出水水质对比显示,污水处理厂故障检修期间将搅拌、曝气等动力设备完全关闭的厌氧模式下系统污泥活性恢复较快,而且能耗最低.     

厌氧—交替O/A的序批式膜生物反应器脱氮除磷性能比较

提出一种高效脱氮除磷的新工艺,即厌氧-交替O/A的序批式膜生物反应器.在HRT为8.4 h、交替O/A时间为10min/10 min时,系统氨氮、总氮、总磷的平均去除率分别达到99.57%、89.92%、93.26%.典型周期试验证明.频繁的O/A环境更利于系统高效脱氮除磷,且O/A交替越频繁,系统中反硝化聚磷菌(DPAO)占聚磷菌(PAO)的比例(即缺氧吸磷速率与好氧吸磷速率的比值)越大.当交替O/A时间为10 min/10 min时.系统中DPAO占PAO的比例为70.87%,比交替O/A时间为30 min/30 min时提高了66%.     

白洋淀水中白腐真菌对双酚A的降解规律及途径研究

研究白洋淀表层水(白洋淀原水)、无机盐培养基、无机盐培养基强化的白洋淀原水中双酚A在白腐真菌作用下的生物降解规律,同时考察了细菌及pH等因素对降解率的影响.实验结果表明,白洋淀原水中双酚A在白腐真菌作用下的降解率很高.甚至高于最适营养条件(无机盐培养基)下双酚A的降解率.在6 d达到完全降解.但是无机盐培养基强化的白洋淀原水抑制了白腐真菌对双酚A的降解;当细菌存在时.白腐真菌与细菌对碳源和能源等形成了竞争关系,抑制了白腐真菌的生长.不利于白腐真菌对双酚A的降解;无机盐培养基强化的白洋淀原水在初始pH-6.00时双酚A的降解率高于初始pH=7.00时双酚A的降解率.通过气相色谱/质谱(GC/MS)分析.白腐真菌降解双酚A的中间产物包括2-对羟苯基-2-酮基-1-乙醇、2-羟基苯乙酸和丙二酸等小分子酸.     

UV-TiO_2光催化氧化降解双酚A的动力学研究

采用自制光催化氧化反应器,研究了双酚A(BPA)在纳米TiO_2悬浆体系中的光催化氧化特性.结果表明:(1)UV-TiO_2对水中BPA有较强光催化氧化降解作用.在10 W低压汞灯照射下,当纳米TiO_2用量为1.0 g/L、pH为5.5、BPA初始质量浓度为10 mg/L、曝气量为4.0 mL/min、温度为室温、反应时间为120 min时,BPA去除率可达97.1%.当pH≥9.5时,120 min后BPA已经基本光催化氧化降解完全.(2)BPA的光催化氧化降解曲线均很好地符合一级反应动力学方程.其速率常数与纳米TiO_2用量、pH、BPA初始浓度、曝气量有关;促进·OH和电子-空穴对的生成是提高光催化氧化反应速率的重要途径.     

Viable chemical recycling of poly(carbonate) as a phosgene equivalent illustrated by the coproduction of bisphenol A and carbohydrate carbonates

Chemical recycling of waste poly(carbonate) (PC) to coproduce bisphenol A (BPA) and carbohydrate carbonates was studied by selecting glycerol (Gly) and glucose (Glu) as model carbohydrates (CHs). In advance of the reaction of PC with CHs, reactions with diphenyl carbonate were examined as a model PC. In dioxane at 100°C using NaOH as catalyst, Gly was converted to cyclic carbonate hydroxymethyldioxolane (HMDO) at 98% and Glu was converted to the dicarbonate (Glu-DC) at 46%, in pyridine, in addition to the production of phenol. Similar treatment of PC with Gly using KOH as a catalyst produced HMDO and BPA at very high yields and treatment with Glu produced Glu-DC and BPA in 38%–42% yields. Chemical Feedstock Recycling & Other Innovative Recycling Techniques 6     

High nitrite accumulation and strengthening denitrification for old-age landfill leachate treatment using an autocontrol two-stage hybrid process

An autocontrol two-stage hybrid process was developed to treat landfill leachate. Biological nitrogen removal with nitrification and denitrification via nitrite pathway was split into two stages. The first stage was designed for the high nitrite accumulation and was composed of two hybrid bed reactors (Hybrid I and Hybrid II) and a coagulation–flocculation reactor having effective volumes of 120 L and 80 L, respectively. The second stage was designed for strengthening denitrification and included a single 80 L reactor. The carriers of the hybrid bed reactors were composed of fixed multiple flexible carriers and suspended particle carriers. Dissolved oxygen (DO), pH value, oxidation–reduction potential (ORP) and temperature were used as online fuzzy control parameters of the automatic control system. The concentration of nitrite in Hybrid I and Hybrid II could reach 411 mg L⁻¹ and 604 mg L⁻¹, respectively. Ammonia removal has reached maximal rates of 0.061 kgNH₄⁺-N (m³ h)⁻¹ and 0.041 kgNH₄⁺-N (m³ h)⁻¹, respectively. A maximum nitrite removal rate of 0.211 kgNO₂⁻-N (m³ h)⁻¹ was observed during the strengthening denitrification. The running time of one cycle was not fixed and was actually controlled by the system. The results indicated that the running period was more closely related to influent ammonia concentration than influent COD concentration. The aeration times could be shortened and the energy could be saved. The autocontrol two-stage hybrid process is therefore an economical and effective way for landfill leachate treatment.     

Occurrence and temporal variations of the xenoestrogens bisphenol A, 4-<Emphasis Type="Italic">tert</Emphasis>-octylphenol,and tech. 4-nonylphenol in two German wastewater treatment plants

GOAL, SCOPE, AND BACKGROUND: The xenoestrogens bisphenol A, 4-tert-octylphenol, and the technical isomer mixture of 4-nonylphenol (tech. 4-nonylphenol) belong to the group of chemicals which are called endocrine disrupters due to their property of causing hormonal dysfunctions in the endocrine system of organisms at very low concentrations. Bisphenol A, 4-tert-octylphenol, and the tech. 4-nonylphenol (mixture of isomers) were determined in water samples collected from the influent and effluent of two German wastewater treatment plants (WWTP) during a long-time sampling period from February 2003 till August 2005 to assess their occurrence and temporal variations in WWTPs. METHODS: The compounds were extracted and concentrated from water by solid-phase extraction (SPE) using Bond Elut PPL cartridges and quantified by use of gas chromatography-mass spectrometry (GC-MS). RESULTS: The influent concentrations were as follows: Bisphenol A < limit of detection of the method (< ldm)--12,205 ng L(-1), tech. 4-nonylphenol < ldm--10,186 ng L(-1), and 4-tert-octylphenol 39-1,495 ng L(-1). The measured effluent concentrations were lower with values in the range of < ldm--7,625 ng L(-1) for bisphenol A, < ldm--14,444 ng L(-1) for tech. 4-nonylphenol, and < ldm--392 ng L(-1) for 4-tert-octylphenol. All target compounds were largely eliminated during the wastewater treatment process. The elimination efficiency varied between 73% and 93%. DISCUSSION: All analytes show highly fluctuating influent concentrations with very high peak concentrations at particular sampling times. The variation of effluent concentrations is by far lower than the variation of influent concentrations. For tech. 4-nonylphenol, a significant temporal concentration variation has been detected with very high concentrations up to the microgram-per-liter level in the time from February 2003 till July 2003 and clearly decreasing concentrations in the time from June 2004 till August 2005. This corresponds well with the implementation of Directive 2003/53/EC (nonylphenol and nonylphenol ethoxylates in the European Union "may not be placed on the marked or used as a substance or constituent of preparations in concentrations equal or higher than 0.1% by mass") from January 2005 on. Bisphenol A is present in the effluent samples in a wide range of concentrations from below the detection limit to high concentrations up to the microgram-per-liter level. For 4-tert-octylphenol, no particular trend of concentration development has been observed. CONCLUSIONS: Combined SPE and GC-MS proved to be an efficient method to identify and quantify polar organic compounds in environmental samples. With respect to the concentrations measured in the present study, bisphenol A sometimes is the prominent compound in influent samples. Neither bisphenol A nor 4-tert-octylphenol or tech. 4-nonylphenol show seasonal variations. However, there was a significant general trend of decreasing concentrations of tech. 4-nonylphenol in influent and effluent samples from both WWTPs which probably reflects the implementing Directive 2003/53/EC. RECOMMENDATIONS AND PERSPECTIVES: Further research is needed to investigate whether the observed decrease of tech. 4-nonylphenol concentrations in German WWTPs since June 2004 will continue further on. The reason for the high effluent concentrations of bisphenol A in only a few samples has to be clarified in further research. The results from this study provide insight into the concentration development of the xenoestrogens bisphenol A, tech. 4-nonylphenol, and 4-tert-octylphenol in WWTPs in the time span between 2003 and 2005.     

新时代美丽中国的建设思路与战略任务研究

党的二十大提出要建设人与自然和谐共生的现代化,美丽中国建设是社会主义现代化强国的重要目标之一,是中国式现代化的基本内涵和重要表征。面对新时代美丽中国建设整体部署还需进一步明确的现实需求,本文在总结美丽中国建设进展成效的基础上,分析识别推进美丽中国建设面临的主要问题与挑战,提出推进美丽中国建设的总体思路和目标路径,围绕绿色低碳发展、环境治理、生态保护、应对气候变化、生态环境治理体系和治理能力现代化等美丽中国建设重点领域,提出推进加快发展方式绿色转型、推进国家重大战略绿色发展、推动环境污染防治、打造美丽宜居城乡、提升生态系统多样性、稳定性和持续性、推进碳达峰碳中和、构建生态环境风险防控体系、共建清洁美丽世界等8个方面美丽中国建设重点任务。