关于模糊数学在环境质量综合评判中“最大隶属度”原则不适用性的讨论

通过对模糊数学在环境质量综合评判中的分析，指出“最大隶属度”原则的不适用性，并根据环境质量分级所存在的固有关系提出改进的方法。     

生物炭降解苯和甲苯混合废气性能研究

该研究以生物炭为过滤介质 ,探讨过滤塔降解气流中苯、甲苯的生物降解性能 .实验表明 ,在总有机负荷低于 3 5 0 g/ (h·m3)、停留时间 1 5～ 90s的实验条件下 ,滤塔对苯和甲苯混合气体有较好的降解性能 ,苯、甲苯的最大削减能力分别为 1 2 0 g/ (h·m3)和 1 5 0 g/ (h·m3) ,甲苯比苯更易被微生物降解 .滤塔中CO2 生成量随苯、甲苯降解量的增加而增加 ,但实验增长速率小于理论增长速率 .菌落分析表明 ,滤塔中微生物主要有真菌、杆菌、芽孢杆菌 ,其中芽孢杆菌为优势菌种 .根据吸附 生物降解机理 ,建立了VOCs去除模型 ,并予以验证 .     

降低气流粉碎过程中噪声强度的研究

主要报导了超音速气流超细粉碎过程中噪声产生的原因、影响因素及降低噪声强度所采取的技术原理途径与措施。研究结果表明 :采用CSQ消声装置完全可以将超音速气流粉碎过程中产生的噪声 130dB(A)降低到国家规定的标准 85dB(A)之下。该装置结构简单 ,既能消除噪声 ,又便于产品卸料 ,拆卸清理方便 ,综合性能良好。     

O3/UV降解喹啉过程中不同氧化剂的相对重要性

研究O3 /UV降解自配喹啉水溶液时水体中存在的不同氧化剂对喹啉降解的相对重要性的结果表明 ,O3 和·OH是喹啉降解过程的主要氧化剂 .通过靛蓝二磺酸钠法和·OH探针化合物 (对氯苯甲酸 )法分别测定了水体中的O3 浓度和·OH浓度 ,定量地计算了O3 和·OH在降解喹啉时的相对重要性 ,得到喹啉与·OH的二级反应速率常数为 6 65× 1 0 9mol·(L·s) - 1.在本试验条件下 ,由·OH引起的喹啉去除率占总去除率的 88% ,而由O3 引起的喹啉去除率占总去除率的 1 2 % .提高水体中·OH的浓度有利于提高喹啉的总降解速率 .     

Histopathological changes in zebrafish embryos exposed to DLPCBs extract from Zhanjiang coastal sediment

Dioxin-like polychlorinated biphenyls (DLPCBs) are ubiquitous persistent pollutants that cause adverse effects in many environmental organisms. DLPCBs in marine sediments can be absorbed by benthic organisms, bioaccumulate, and biomagnify through the food chain and threaten animal and human health. There are no reports of DLPCBs concentrations in the Zhanjiang Gulf seabed. This study was designed to investigate the concentration of DLPCBs in the Zhanjiang coastal sediment and histopathological changes in zebrafish (Diano rerio) embryos exposed to environmentally relevant concentrations of DLPCBs. Of the five sites selected, two sites TS and JSW contained DLPCBs at concentrations of 0.08 and 22.54 ng/g dry sediment, respectively. Two groups of zebrafish embryos were used. One group was exposed to 3.75, 7.5, 15, 30, and 60 mg/ml of DLPCBs extracted from the sediments sampled from the TS site and the second group to 4.375, 8.75, 17.5, 35, and 70 mg/ml of DLPCBs from JSW site from 0.75 h post-fertilization (hpf) to 96 hpf. The zebrafish exposed to 60 and 70 mg/ml of DLPCBs at 96 hpf displayed gross histopathological changes with cardiac lesions including pericardial edema being the most deleterious. Other changes observed were hydropic degeneration of gill filaments and hepatocytes, loss of intestinal folds, and uninflated swim bladder. It appears that only a few sites of the Zhanjiang gulf are contaminated with DLPCBs. This is the first report of histopathological changes in the gills, hepatocytes, intestines, heart, and the swim bladder in zebrafish embryos exposed to DLPCBs from a coastal sediment. Further studies with sampling at different stages of development are required to identify which organ/tissue is most sensitive to DLPCBs.     

碳氮比对低温投加介体生物反硝化脱氮的影响

污水的生物脱氮效果受低温抑制,投加氧化还原介体有利于反硝化过程。采用规格相同的序批式反应器,使用人工配制硝酸盐废水和经过驯化的活性污泥,考察了不同碳源浓度(碳氮比)对低温(10℃)投加氧化还原介体1, 2-萘醌-4-磺酸(NQS)污水生物反硝化脱氮过程的影响。结果表明:当碳源浓度(以COD计)为150～400mg·L~(-1) (碳氮比为1.8～4.7)时,脱氮效率随碳氮比的升高而升高;当碳源浓度为400～550 mg·L~(-1) (碳氮比为4.7～6.5)时,脱氮效率随着碳氮比的升高而降低;当碳源浓度为400 mg·L~(-1) (碳氮比为4.7)左右时效果最好,总氮去除率最高为64.7%。对于脱氮速率,介体强化脱氮速率随着碳氮比的升高而升高。同时,探讨了投加介体污水生物反硝化脱氮的机理,发现投加介体降低了体系的氧化还原电位(ORP),有利于反硝化脱氮反应的进行。     

浓盐水处理技术研究进展

海水淡化技术是解决中国水资源危机的一种具有根本性的举措之一.然而随着海水淡化产业规模的增大,其产生的浓盐水的排放成了本身面临解决的问题之一.本文阐述了浓盐水的特性及其对环境的各种危害性,并对浓盐水直接排放问题进行了详细分析.介绍了国内外近年来主要处理浓盐水的方法-真空膜蒸馏浓缩技术、正渗透技术、喷雾蒸发技术、冷冻法浓缩技术.对各种处理技术的原理和特点进行了详细综述,并对其研究进展进行了归纳总结.最后对各项处理技术的应用前景提出了展望.     

论民初我国救灾之主要特征

民国初年我国救灾的主要特征有三:一是救灾主体多元化,这可从阶层、国籍、职业、身份等方面看出,总体上又可划分为政府和社会力量两个方面。至于救灾效能,无论是政府还是社会救济力量均存在着或多或少的局限性。二是短效机制占主导,这可从救灾因素之临设性、救灾甚于防灾两点看出。三是社会过渡性彰显,无论是思想,还是机构、制度,都呈现出明显的新旧交错性,即社会过渡性。     

Enhancement of thermophilic anaerobic digestion of thickened waste activated sludge by combined microwave and alkaline pretreatment

Pretreatment of thickened waste activated sludge (TWAS) by combined microwave and alkaline pretreatment (MAP) was studied to improve thermophilic anaerobic digestion efficiency. Uniform design was applied to determine the combination of target temperature (110–210°C), microwave holding time (1–51 min), and NaOH dose (0–2.5 g NaOH/g suspended solids (SS)) in terms of their effect on volatile suspended solids (VSS) solubilization. Maximum solubilization ratio (85.1%) of VSS was observed at 210°C with 0.2 g-NaOH/g-SS and 35 min holding time. The effects of 12 different pretreatment methods were investigated in 28 thermophilic batch reactors by monitoring cumulative methane production (CMP). Improvements in methane production in the TWAS were directly related to the microwave and alkaline pretreatment of the sludge. The highest CMP was a 27% improvement over the control. In spite of the increase in soluble chemical oxygen demand concentration and the decrease in dewaterability of digested sludge, a semi-continuous thermophilic reactor fed with pretreated TWAS without neutralization (at 170°C with 1 min holding time and 0.05 g NaOH/g SS) was stable and functioned well, with volatile solid (VS) and total chemical oxygen demand (TCOD) reductions of 28% and 18%, respectively, which were higher than those of the control system. Additionally, methane yields (L@STP/g-CODadded, at standard temperature and pressure (STP) conditions of 0°C and 101.325 kPa) and (L@STP/g VSadded) increased by 17% and 13%, respectively, compared to the control reactor.     

Identification of odorous compounds in reclaimed water using FPA combined with sensory GC-MS

Odorous compounds in the influent of a reclaimed water treatment plant (RWTP), consisting of coagulation, sedimentation, continuous micro-filtration (CMF), and chlorination in succession, in a north China city, were identified by combining flavor profile analysis (FPA) with sensory gas chromatograph-mass spectrometry (GC-MS). The sewery/swampy/septic odor with an odor intensity of 6.4 was found to be the major odor group in the RWTP influent, and the existence of well-known odorant including dimethyl disulfide, dimethyl trisulfide, indole and skatole were confirmed using GC-MS. The result of a spiking test showed that the intensity (3.6) of the sewery/swampy/septic odor caused by these four chemicals contributed to over 50% of the odor intensity of the influent. The FPA intensity for sewery/swampy/septic odor in the RWTP effluent was 3.8, showing that the treatment process was not efficient for the removal of odorants, particularly indole and skatole.