循环经济视角下的旅游产业生态化研究

旅游循环经济指导下的旅游产业生态化是实现旅游持续发展的战略途径。基于此,文章尝试将循环经济的理念应用到推进旅游产业生态化中,在循环经济“3R”原则指导下,提出了实现旅游产业生态化的策略,包括旅游企业内部的生态化、旅游企业间的生态化以及旅游产业与其他产业间的生态化。     

钢筋混凝土梁裂缝宽度的有限元分析

文章根据所做试验情况,对钢筋混凝土梁的裂缝宽度进行了有限元模拟.有限元分析结果与试验结果吻合良好.说明有限元分析在某种程度上可以代替试验对钢筋混凝土梁裂缝宽度进行研究分析.     

生物技术在挥发性有机化合物处理中的应用研究

介绍了生物技术在挥发性有机化合物处理方面的研究现状和进展,对生物技术的优缺点、分类、影响因素、动力学模型做了详细的说明,并结合近年来的研究状况和存在的问题做出展望。     

硫磺安全仓储关键技术

介绍了硫磺火灾爆炸机理,并对硫磺仓储系统的危险性进行了分析。结合相关实验数据,提出了仓库设计、工艺运行、事故预防中的安全措施,以保证硫磺散装系统能够安全、长周期平稳运行。     

川东北地区天然气勘探清洁生产技术措施分析

对川东北地区天然气勘探过程中的几项清洁生产技术措施进行了初步的分析,确定在取得良好的经济效益的同时,实现勘探过程中废弃物"减量化、无害化、资源化"的清洁生产目标,降低了勘探过程中的环境风险,同时也产生了良好的社会效益。     

浅谈环境监测实验室前期内部设计过程中应注意的问题

文章结合作者自己站环境监测实验室建设的实际,提出了环境监测实验室建设的原则和理念,明确了实验室建设内部设计过程,并对环境监测实验室初期内部设计应关注的地方进行了阐述,给以后的环境监测实验室建设内部设计提供必要的借鉴。     

射击场土壤重金属污染及其生物有效性

为了解射击场土壤重金属污染问题,采集某射击场土壤和植物样品,对重金属和P元素含量进行了检测分析,并对重金属的生物有效性进行了评价.研究发现,射击场表层土壤存在一定程度的Pb、Cu、Hg、Sb污染并呈不均匀的斑块状分布,Pb、Cu、Sb含量随土壤深度增加呈下降趋势,射击场土壤重金属存在一定程度的垂直迁移和侧向迁移.射击场...     

Characterization of the e ective cellulose degrading strain CTL-6

An e cient cellulose degrading bacteria exists in the thermophilic wheat straw-degrading community, WDC2. However, this strain cannot be isolated and cultured using conventional separation techniques under strict anaerobic conditions. We successfully isolated a strain of e ective cellulose degrading bacteria CTL-6 using a wash, heat shock, and solid-liquid alternating process. Analysis of its properties revealed that, although the community containing the strain CTL-6 grew under aerobic conditions, the purified strain CTL-6 only grew under anaerobic culture conditions. The strain CTL-6 had a striking capability of degrading cellulose (80.9% weight loss after 9 days of culture). The highest e ciency value of the endocellulase (CMCase activity) was 0.404 mol/(min mL), cellulose degradation e ciency by CTL-6 was remarkably high at 50–65°C with the highest degradation e ciency observed at 60°C. The 16S rRNA gene sequence analysis indicated that the closest relative to strain CTL-6 belonged to the genus Clostridium thermocellum. Strain CTL-6 was capable of utilizing cellulose, cellobiose, and glucose. Strain CTL-6 also grew with Sorbitol as the sole carbon source, whereas C. thermocellum is unable to do so.     

Macroscale and microscale analysis of Anammox in anaerobic rotating biological contactor

Inoculated with conventional anaerobic activated sludge, the Anammox process was successfully developed in an anaerobic rotating biological contactor (AnRBC) fed with a low ratio of C/N synthetic wastewater. Operated in a single point feed mode, the AnRBC removed 92.1% (n = 126) of the influent N at the highest surface load of 12 g/(m².day). The biomass increased by 25% and 17.1 g/(m².day) of maximum N removal surface load was achieved by elevating flow rate with another feed point. Fluorescence in situ hybridization and polymerase chain reaction analysis indicated that the Anammox genus Candidatus Kuenenia stuttgartiensis dominated the community. Both Anammox and denitrifying activity were detected in biofilm by the application of microelectrodes. In the outer layer of the biofilm (0-2500 μupm), nitrite and ammonium consumed simultaneously in a ratio of 1.12/1, revealing the occurrence of Anammox. In the inner layer (> 2500 μupm), a decrease of nitrate was caused by denitrification in the absence of nitrite and ammonium.     

Denitrification of coking wastewater with micro-electrolysis

The denitrification for the coking wastewater was conducted by means of original battery principle with Fe-C micro-electrolysis. Fe-C serves as positive and negative electrodes, by which N0₂^?-N and TN were reduced to nitrogen, and then the purpose of denitrifieation for coking wastewater was realized. The influences of pH value, carbon particle size, Fe/C ratio (mass ratio), reaction time and coagulation pH value on removal rate of N0₂^?-N and TN were investigated. Coking wastewater originated from Jiamusi Coal Chemistry Engineering Company. The optimum conditions of treatment were as follows: the initial pH was 3.0, the dosage of Fe 73.5 g/L, reaction time 70 min, mass ratio of Fe/C ratio 1.0:1.3, coagulation pH 9.0 and sedimentation time 40 min. Under those conditions, nitrogen removal efficiencies of N0₂^?-N and TN were beyond 50% and 45%, respectively.