糖尿病小型猪心肌、肝脏组织结构变化和心肌VEGF表达

以探讨高糖高脂高胆固醇饲料诱发的糖尿病广西巴马小型猪心肌和肝脏组织结构变化、肝糖原分解和心肌血管内皮生长因子(VEGF)表达情况为目的.通过3月龄雄性广西巴马小型猪10只,随机分2组,5只饲以基础饲料为CD组;5只饲以高糖高脂饲料为HFSCD组,饲养时间5个月.每月末从禁食过夜的小型猪眶静脉窦抽取血样,葡萄糖氧化酶法检测空腹血糖(Glucose);GPO-PAP酶法测定血浆甘油三脂(triglyceride,TG);放射免疫法测血浆胰岛素.第5个月末股动脉放血处死小型猪,取1小块心肌和肝脏组织,固定于10%中性甲醛固定液,常规石蜡包埋、切片、制片后用光学显微镜进行观察的方法.结果HFSCD组血糖、甘油三酯和胰岛素水平升高.与CD组比较,差异具有显著性意义(P<0.05).从肝脏病理切片观察所见,HFSCD组肝脏肝细胞索排列紊乱,肝细胞肿胀呈气球样变,亦可见肝细胞萎缩、坏死,脂肪变性明显,肝小叶间有单个核细胞浸润,肝糖原极少或消失.心肌组织中VEGF的蛋白表达显著增加,且表达范围广泛.得出高糖高脂高胆固醇饲料诱发的糖尿病广西巴马小型猪肝脏和心肌组织结构改变,肝糖原减少,心肌VEGF蛋白表达增加的结论.图5,参13.     

福建梅花山国家级自然保护区拟赤杨种群分布格局的分形分析

分形理论中的计盒维数、信息维数和关联维数能分别从空间占据程度、格局强度和个体空间关联的尺度变化角度,揭示种群分布格局的尺度变化特征.本文应用以上3个分形维数探讨了福建梅花山国家级自然保护区拟赤杨种群分布格局的多尺度分布规律,计算结果表明,拟赤杨种群的分布格局具有分形特征,其计盒维数为1.0298～1.2982,信息维数为0.9728～1.2464,关联维数为0.5089～0.8047.拟赤杨种群的计盒维数、信息维数较高,而关联维数较小,表明该种群的分布格局强度相对较高,结构相对复杂,具有集聚分布的趋势.     

佛坪三官庙地区大熊猫种群数量的DNA指纹分析

应用同位素标记大熊猫基因指纹探针Ｆ２ＺＧＰ９６０６０８０１，以秦岭南坡中段佛坪国家级大熊猫自然保护区三官庙范围内采集的大熊猫粪便样品作材料，进行了ＤＮＡ指纹检测．（１）在相同或不同时间、领域采得的粪便样品，显现出相同或不同的ＤＮＡ指纹图谱，达到个体认定的目的，进一步表明了大熊猫的尽量新鲜的粪便，可以作为ＤＮＡ指纹分析材料，进行野生种群数量调查．（２）根据检测２１个粪便样品的结果，无误地认定了三官庙地区有１３只大熊猫个体．其中有３个家系．（３）大熊猫粪便样品的ＤＮＡ指纹图，通过微机识别的个体数，准确可靠，能获得大熊猫在野外的真实个体数量．     

农林复合经营研究──桉树间种山毛豆对林木和土壤的影响

本文研究了桉树人工林间种山毛豆的适应性及其对林木和土壤的影响．结果表明，在一年生桉树人工林下，山毛豆生长正常，以后，随着林地的逐浓荫蔽，生长有逐渐衰退现象；间种山毛豆当年，可能对林木生长有一定影响，但可通过改善间种方式而消除．第二年以后对桉树生长的促进作用逐渐显著；间种山毛豆对提高土壤肥力也有一定作用，对促进林业生产的持续发展有重要意义．     

喷雾增湿塔用离心式雾化器的设计

在分析各种运行参数对雾化效果影响的基础上 ,介绍了喷雾增湿塔用离心式雾化器的选型与放大设计的方法。     

Total life cycle emissions of post-Panamax containerships powered by conventional fuel or natural gas

This study proposes an easy-to-apply method, the Total Life Cycle Emission Model (TLCEM), to calculate the total emissions from shipping and help ship management groups assess the impact on emissions caused by their capital investment or operation decisions. Using TLCEM, we present the total emissions of air pollutants and greenhouse gases (GHGs) during the 25-yr life cycle of 10 post-Panamax containerships under slow steaming conditions. The life cycle consists of steel production, shipbuilding, crude oil extraction and transportation, fuel refining, bunkering, and ship operation. We calculate total emissions from containerships and compare the effect of emission reduction by using various fuels. The results can be used to differentiate the emissions from various processes and to assess the effectiveness of various reduction approaches. Critical pollutants and GHGs emitted from each process are calculated. If the containerships use heavy fuel oil (HFO), emissions of CO₂ total 2.79 million tonnes (Mt), accounting for 95.37% of total emissions, followed by NO_x and SO_x emissions,which account for 2.25% and 1.30%, respectively.The most significant emissions are from the operation of the ship and originate from the main engine (ME).When fuel is switched to 100% natural gas (NG), SO_x, PM₁₀, and CO₂ emissions show remarkable reductions of 98.60%, 99.06%, and 21.70%, respectively. Determining the emission factor of each process is critical for estimating the total emissions. The estimated emission factors were compared with the values adopted by the International Maritime Organization (IMO).The proposed TLCEM may contribute to more accurate estimates of total life cycle emissions from global shipping.

Implications: We propose a total life cycle emissions model for 10 post-Panamax container ships. Using heavy fuel oil, emissions of CO₂ total 2.79 Mt, accounting for approximately 95% of emissions, followed by NO_x and SO_x emissions. Using 100% natural gas, SO_x, PM₁₀, and CO₂ emissions reduce by 98.6%, 99.1%, and 21.7%, respectively. NO_x emissions increase by 1.14% when running a dual fuel engine at low load in natural gas mode.     

富营养化供水中的藻类控制与去除

综述了富营养化的供水原水中，藻类控制与去除方法的国内外研究进展。首先扼要介绍藻类过度繁殖对原水处理工艺的诸多影响。然后叙述富营养化湖泊中，藻类生物量的控制方法和给水原水处理的藻类去除工艺，并就此技术现状提出若干结论和建议。     

处理啤酒废水的厌氧流化床操作特性的研究

试验表明,自制厌氧流化床(AFB)反应器对温度的变化、上升流速等环境的变化都具备良好的稳定性.它的处理温度控制在30±2℃范围,上升表观流速控制为19.1 m/h左右,回流比控制为8:1,水力停留时间在6.9 h左右,废水COD去除率可达80%以上.该AFB反应器能够承受高达30.65 kg COD/m3·d的有机容积负荷,其COD去除率也达到了73%～81%,产气速率系数为0.55～0.612 m2/kg COD.同时,也对实验中出现的偏析现象进行了分析.     

Lead contamination in tea garden soils and factors affecting its bioavailability

The consumption of heavy metals is detrimental to human health and most countries restrict the concentration of metals such as lead (Pb) in food and beverages. Recent tests have detected high Pb concentrations in certain commercial brands of tea leaves and this finding has raised concerns for both producers and consumers. To investigate what factors may be contributing to the increase in Pb accumulation in the tea leaves we collected tea leaves and soils from tea producing areas and analyzed them for Pb concentration, pH and organic matter content. The result showed the Pb concentration of 47% investigated tea leaves samples was beyond 2 mg kg(-1), the permissible levels given by China. The total Pb concentration in the surface and subsurface soil layers averaged 36.4 and 32.2 mg kg(-1), respectively which fall below of the 60 mg kg(-1) limit provided for organic tea gardens in China. The pH of the tea garden soils was severely acidic with the lowest pH of 3.37. Soils under older tea gardens tended to have a lower pH and a higher Pb bioavailability which was defined as the amount of lead extracted by CaCl2 solution than those under younger tea gardens. We found that the concentration of bioavailable Pb and the percentage of bioavailable Pb (bioavailable Pb relative to total Pb concentration) were positively correlated with soil H+ activity and soil organic matter content, and the organic matter accumulation contribute more effects on Pb bioavailability in these two factors. We conclude that soil acidification and organic matter accumulation could contribute to increasing Pb bioavailability in soil and that these could increase Pb uptake and accumulation in the tea leaves.     

Treatment of landfill leachate by electrochemical oxidation and anaerobic process.

The removal performance of typical refractory organic compounds in landfill leachate was investigated during the electrochemical (EC) oxidation and anaerobic process combined treatment system in this paper. The results indicated that the treatment of landfill leachate by the combined system was highly effective. The toxicity of leachate was notably decreased after the electrochemical oxidation process and the biodegradability was improved. The concentration of the organic acid with low molecular weight in the leachate increased from 28% to 90% based on the biodegradability assays after the EC oxidation process. The anaerobic digestion could further remove the residual organic compounds. At a hydraulic retention time (HRT) of 16 hours and an organic loading rate (OLR) of 8 kg COD/m3 d, the concentration of COD, SS, ALK, VA, N-TKN, N-NH4+ and P-PO4(3)- [corrected] in UASB effluent were 532, 12, 6744, 400, 540, 455 and 11.6 mg/L, respectively, with approximately 90% removal efficiency of COD. The organic compounds in the landfill leachate revealed different degradation characteristics in the combined system. p-chloroaniline, bisphenol A, 6-methyl-2-phenyl-quinoline, dimethylnaphthaline and N'-(2-methyl-4-chlorophenyl)-N-cyclohexyformamidine, classified into the first group in this paper, were completely removed by the EC oxidation and did not reappear in the effluent of the UASB reactor. Phenylacetic acid, 3-methyl-indole and N-cyclohexyl-acetamide, called the second group, were completely removed, but reappeared in the UASB reactor. 4-methyl-phenol, 3,4-dihydroisoquinoline, 2(3H)-benzothiazolone, exo-2-hydroxycineole and benzothiazole, the third group, were degraded little in the EC oxidation process, but extensively removed by the anaerobic process. Benzoic acid, benzenepropanoic acid and 2-cyano-3,5-dimethyl-1-hydroxypyrrole, the fourth group, concentration obviously increased in the EC process, but was completely removed in the UASB reactor. The content of volatile fatty acids (VFAs) markedly increased from 0.68% in the leachate to 16.18% in the effluent from the electrochemical oxidation process (EC(effl)). In addition, the degradation rate of organic compounds from the landfill leachate was different in the EC oxidation and anaerobic process.