辽宁省生态系统评价与生态功能分区研究

生态系统评价是为了向决策者提供生态系统管理信，息而对生态系统结构、功能进行分析，并根据其变化趋势及驱动力提出相应措施的综合研究过程。生态功能分区是依据生态系统胁迫过程与效应、生态环境质量、敏感性和生态系统服务功能重要性等特征空间分异规律而进行的地理空间分区，目的是辨析区域生态环境问题与生态环境脆弱区和良好区，明确优先保护的生态系统和地区，为生态保护与建设、产业结构调整与优化及区域生态系统分区管理提供科学依据。本研究以辽宁省域生态系统为对象，在生态环境调查的基础上，分析了生态环境状况及变化趋势，进行了生态环境质量、敏感性和生态系统服务功能重要性评价，辨析了存在的生态环境问题及驱动力，明确了生态环境质量、敏感性和生态系统服务功能重要性空间分布格局，然后对辽宁省进行了生态功能区划分，并指出了各功能区生态保护与建设的重点和措施以及产业结构调整与优化的对策和方向研究结果表明，在经济和人口增长的长期胁迫作用下，辽宁省生态环境问题依然严峻，主要表现为：土地退化，地表水污染严重，森林质量下降和功能减弱，草地减少与退化并存，天然湿地萎缩，滩涂和海岸带生境恶化，生物多样性面临威胁，农业面源污染凸显，生态系统抗干扰能力下降，生态灾害加剧。全省生态环境质量超过2／3属于一般以下水平，其中优级面积仅占12.56％，良好级面积占18.71％，主要分布在东部及东南部；一般级面积占34.25％，主要分布在中部、北部和南部；较差级面积占34.48％，主要分布在西部及西北部。全省县级市及县有44个，其中生态环境质量为优的仅有4个市县，占总县数的9.09％；生态环境质量为良的有7个市县，占总县数的15.91％；生态环境质量一般的有19个市县，占总县数的43.18％，生态环境质量较差的有14个市县，占总县数的31.82％。全省处于轻度至高度敏感区域。高度敏感区占34.00％，主要分布在辽东山地丘陵、辽东半岛、辽西低山丘陵、辽西北、柳绕地区和大洼县。辽东山地丘陵、辽东半岛和辽西低山丘陵主要是土壤侵蚀高度敏感。辽西北和柳绕地区主要是土地沙漠化高度敏感。大洼县是土壤盐渍化高度敏感。中度敏感区占能．66％，与高度敏感区相间分布。轻度敏感区占3.34％，零星分布在辽东，在辽西和辽河平原也有少量分布。全省生态服务功能均处于比较重要以上。极重要地区占60.66％，基本分布在辽东、辽西和辽河平原的北部与盘锦滨海地区，辽东主要为水源涵养、生物多样性保护、土壤保持、营养物质保持，辽西主要为土壤保持、生物多样性保护、水源涵养、营养物质保持，辽北主要为土壤保持，盘锦滨海地区主要为生物多样性保护。中等重要地区占37.01%，基本分布在辽河平原，在辽东、辽西也有分布，辽河平原主要为土壤保持、水源涵养，沙漠化控制，辽东和辽西主要为土壤保持，辽西北为沙漠化控制。其它地区为比较重要地区，仅占2.33％，主要分布在辽东和辽河平原，在辽西也有少量分布，主要为土壤保持。在生态系统评价的基础上，首先根据地貌和气候划分出4个生态区，即辽东山地丘陵温带湿润半湿润生态区、辽河平原温带半湿润生态区、辽西低山丘陵温带半湿润生态区、辽南环黄渤海海岸带生态区。在明确生态区的基础上，依据生态系统类型与过程的完整性，以及生态服务功能类型的一致性，划分出21个生态亚区。依据生态环境质量、敏感性及生态服务功能重要性等的一致性，进一步划分出52个生态功能区。

红松针阔混交林林木死亡量和主要树种倒木分解规律的研究

红松针阔混交林，是我国东北东部山地稳定的地带性天然森林植被。开展其林木死亡量和倒木分解规律的研究，不仅能有效地监测红松针阔混交林的动态。而且能加深倒木生态功能的认识，为合理管理倒木资源提出对策。同时也有助于填补我国倒木研究的空白。根据研究，长白山红松阔叶林和阔叶红松林林木年死亡量分别为0.15 ～ 0.66T/年·ha和1.23 T /年·ha。倒木年输入量分别为0.03 ～ 0.19 T/年·ha和0.22 T /年·ha。林木年死亡量和倒木年输入量随着林分时空的变化差异很大。风害是其林木致死的主要原因。红松阔叶林有倒木82株/ha，站杆8析/ha。倒木的生物量为7.90T/ha，倒木的复盖度为1.31%。阔叶红松林倒木和站杆分别为94株/ha和24株/ha，倒木生物量为16.23T/ha。倒木的复盖度为2.02%。红松紫椴倒木分别占上述这两个类型倒木总生物量的59.17%与46.77%。红松阔叶林和阔叶红松林倒木株数、复盖面积、体积和生物量按腐烂级分配基本呈正态分布。红松阔叶林倒木的径级结构与活立木径级结构并非完全一致林地倒木的方向与主风向关系不大。研究表明，红松（y_1）和紫椴（y_2）的分解模型分别为y_1 = 0.3747e - 0.0162t. y_2 = 0.4454 e~(-0.0275t)，单项指数衰减模型是红松紫椴倒木分解较为理想的数学模型。它们的分解常数为0.0162 ～ 0.0230/年与0.0275 ～ 0.0390/年，其中粉碎常各为0.0068/年与0.0115/年。红松紫椴倒木重量损失掉50%，大约需43年与25年，重量损失掉95%，大致需185年与106年。红松倒木胸径大小对分解常数无显著影响。倒木下方一般比倒木上方和侧方分解要快一些。但差异并不十分显著。倒木边材到心材的不同层次。其分解常数逐渐下降。红松和紫椴倒木分解中。倒木C含量比较稳定。N、Ca和Na都呈不同程度的递增。k呈下降趋势。而P和Mg变化没有明显的规律。红松阔叶林和阔叶红松林倒木中分别含有C3361.12 kg/ha、7184.11kg/ha; N 26.83kg/ha、33.44 kg/ha; P 3.68kg/ha、6.29kg/ha; ca33.33kg/ha 38.04kg/ha; mg 2.67kg/ha、 3.87 kg/ha; K 4.73 kg/ha. 8.15 kg/ha; Na 1.42 kg/ha、2.76 kg/ha. 倒木是重要的养分库，尤其是N素库。红松阔叶林倒木影响天然更新的主要方式是通过林木风倒或枯死。形成林窗。为天然更新创造有利条件。这和云冷杉林大部分是直接在腐烂的倒木上完成天然更新的机制不同。研究结果表明，倒木是红松针阔混交林生态系统中重要的组成部分。为此建议在长白山自然保护区，应严禁人为清理倒木，并进一步开展倒木的研究。同时针对以生产木材为主的红松阔叶林内侧木，提出了一些相应的管理措施。

有机碳对混合菌群亚硝酸盐氮氧化的影响

自养硝化过程在自然界氮素循环和污水处理系统脱氮过程中起着关键作用。因此，了解有机碳对硝化的影响和硝化菌与异养菌之间的竞争对微生物生态学和污水处理系统设计都很重要。目前对氨氧化到硝酸盐氮过程的研究文献很多，但对亚硝酸盐氧化过程在异养菌的存在下如何受到有机碳影响的研究甚少。本文从生理生化指标、基因组学、蛋白组学三方面考察了在实验室条件下有机碳（乙酸钠）对硝化细菌和异养菌组成的混合菌群的硝化性能、菌群结构及代谢功能的变化的影响。 全文分为两大部分： 第一部分为乙酸钠对游离态硝化混合菌群的硝化性能和菌群结构的短期影响。混合菌株先在自养条件下进行连续培养，两个月后硝化速率达到20 mg N/(L·d)；而后离心收集菌体进行批式实验。在批式反应器中，初始亚硝氮均为126mg N/ L，乙酸钠-C 与亚硝酸盐-N 的比分别为0，0.44，0.88，4.41，8.82。结果表明：在低C/N 比（0.44 和0.88）时，亚硝酸盐去除速率比C/N=0 下高，细菌呈现一次生长；而在高C/N 比（4.41 和8.82）时，出现连续的硝化反硝化，亚硝酸盐去除率仍比对照下高，细菌呈现二次生长。不同C/N 比下微生物群落明显不同，优势菌群从自养和寡营养细菌体系（包括亚硝酸盐氧化菌，拟杆菌门,α-变形菌纲,浮霉菌门和绿色非硫细菌下的一些菌株）过渡到异养和反硝化菌体系 （γ-变形菌纲的菌株尤其是反硝化菌Pseudomonas stutzeri 和P. nitroreducens 占主导）。 第二部分为乙酸钠对硝化混合菌群生物膜的硝化性能和菌群结构的长期影响。接种富集的硝化混合菌群于装有组合式填料的三角瓶中，于摇床中自养培养；两个月后填料上形成生物膜的硝化速率达到20 mg N/ (L·d)；而后进行长期实验，每12 小时更换混合营养培养基（亚硝氮约200 mg N/ L，C/N 比同上）。结果显示：相较于C/N 比=0 时的亚硝酸盐氧化反应来说，低C/N 比出现了部分的反硝化，而高C/N 比则是几乎完全的反硝化。与对照比，C/N=0.44 时亚硝酸盐氧化速率并未受乙酸钠的影响，反而上升了，但C/N=0.88 时亚硝酸盐氧化速率有所下降。菌群结构分析表明自养对照与混合营养下微生物群落的不同；PCR-DGGE未检测出混合营养下硝化杆菌的存在，而显示异养菌尤其是反硝化菌的大量存 在。荧光定量PCR 结果表明随C/N 比上升，硝化杆菌数量从2.42 × 104 下降到1.34× 103 16S rRNA gene copies/ ng DNA，反硝化菌由0 增加至2.51 × 104 nosZgene copies/ ng DNA。SDS-PAGE 的结果表明不同C/N 比下的蛋白组较为复杂且呈现一定的差异性。 有机碳对亚硝氮氧化及微生物群落的影响很复杂，本文分别讨论了对游离态和生物膜固定态两种状态的混合菌群相应的短期和长期影响研究。研究发现，有机碳并非一定带来硝化的负影响，如果控制在适当的C/N 比范围，有机碳是有利于亚硝氮氧化的。这些发现阐明了有机碳和硝化反硝化的关系，填补了硝化微生物生态学上的空白，对污水处理系统中减少异养菌的影响并提高氮去除率有一定理论指导意义。 Nitrification plays a key role in the biological removal of nitrogen in both nature and wastewater treatment plant (WWTP). So, understanding of the effect of organic carbon on nitrification and the competition between nitrifying bacteria and heterotrophic bacteria is important for both microbial ecology and WWTP design and operation. Despite the fact that the nitrification process of ammonia to nitrate has been extensively investigated, it is not known how the process of nitrite oxidization is affected by organic carbon when heterotrophic bacteria are present. By measuring different physiological and biochemical parameters, as well as using genomic DNA and proteome analysis, we investigated the influence of organic (acetate) on nitrite oxidizing performance, community structure and metabolic function of nitrite-oxidizing and heterotrophic bacteria under laboratory conditions. The dissertation involves two parts: Part one deals with the effect of organic matter on functional performance and bacterial community shift of nitrite-oxidizing and heterotrophic bacteria under suspended state. The bacteria were prepared in a continuous-flow stirred reactor under autotrophic condition; after two months, the nitrification rate of the culture reached about 20 mg N/ (L·d); then the bacteria were harvested for the next batch experiments. The initial concentrations of nitrite were 126 ± 6 mg N/ L in all flasks, and sodium acetate (C) to nitrite (N) ratios were 0, 0.44, 0.88, 4.41, and 8.82, respectively. The results showed that at low C/N ratios (0.44 or 0.88), the nitrite removal rate was higher than that obtained under autotrophic condition and the bacteria had single growth phase, while at high C/N ratios (4.41 or 8.82), continuous aerobic nitrification and denitrification occurred besides higher nitrite removal rates, and the bacteria had double growth phases. The community structure of total bacteria strikingly varied with the different C/N ratios; the dominant populations shifted from autotrophic and oligotrophic bacteria (NOB, and some strains of Bacteroidetes, Alphaproteobacteria, Actinobacteria, and green nonsulfur bacteria) to heterotrophic and denitrifying bacteria (strains of Gammaproteobacteria, especially Pseudomonas stutzeri and P. nitroreducens). Part two describes the influence of acetate on nitrite oxidizing performance, community structure and metabolic function of nitrite-oxidizing and heterotrophic bacteria in biofilms. Bacterial enrichments was transferred into flasks with polypropylene carriers and cultured under agitated and autotrophic condition. After two month, the biofilms grown on the carriers had a nitrification rate of about 20 mg N/ (L·h); then the biofilms were refreshed with mixotrophic medium (nitrite were 200 mg N/ L in all flasks, and C/N ratios was the same as above) every 12 h. the results show: normal nitrite oxidization reactions were performed when C/N = 0, but nitrite oxidization and partial denitrification occurred with low C/N ratios (0.44 or 0.88). At high C/N ratios (4.41 or 8.82), we mainly observed denitrification. In contrast to C/N = 0, the nitrite oxidization rate was unaffected when C/N = 0.44, but decreased with C/N = 0.88. The structure of bacterial communities varied significantly between autotrophic and mixotrophic conditions. Nitrobacter was hard to detect by PCR-DGGE while heterotrophs and especially denitrifiers were in the majority under mixotrophic conditions. Real-time PCR indicated that the Nitrobacter population decreased from 2.42 × 104 to 1.34 × 103 16S rRNA gene copies/ ng DNA, while the quantity of denitrifiers obviously increased from 0 to 2.51×104 nosZ gene copies/ ng DNA with an increasing C/N ratio. SDS-PAGE indicated the complexity of and a certain difference between the proteome of nitrite-oxidizing and heterotrophic bacteria at different C/N ratios. We conclude that the influence of organic matter on nitrite oxidation and the community structure of NOB and heterotrophic bacteria is complex. In this dissertation, we focused on how sodium acetate influenced the system both under suspended state and in biofilms. We observed that acetate did not necessarily have a negative impact on nitrification. Instead, an appropriate amount of acetate benefited both nitrite oxidization and denitrification. These findings provide a greater understanding about the relationship between organics and nitrification; they fill the gaps in the field of microbial ecology of nitrifying bacteria; they also provide insight into how to minimize the negative impact of heterotrophic bacteria and maximize the benefit of nitrogen removal in biological treatment systems.

Z=105质量数为259的新同位素的合成和鉴别(英文)

利用 1 2 0MeV的2 2 Ne离子束轰击2 41　Am靶 ,通过2 41　Am(2 2 Ne ,4n) 2 5 9　Db反应合成了一个Z =1 0 5,质量数为 2 59的新同位素 .反应产物是用氦喷嘴技术和转动轮装置传输收集的 .借助一系列金硅面垒探测器探测到了反应产物及其子核的α衰变 .新同位素的原子序数Z和质量数A是借助该同位素和已知的2 5 5 　Lr核之间的遗传关系得到了确定的鉴别 .新同位素2 5 9　Db的测量半衰期为 (0 51± 0 1 6)s;它的α粒子能量为 9 4 7MeV .由本实验导出的2 5 9　Db的Qα 值同理论预言结果能够较好地符合

Elastic Scattering of He-6 + p at 82.3 MeV/nucleon

Differential cross sections for the elastic scattering of halo nucleus He-6 on proton target were measured at 82.3 MeV/u. The experimental results are well reproduced by optical model calculations using global potential KD02 with a reduction of the depth of real volume part by a factor of 0.7. A systematic analysis shows that this behavior might be related to the weakly bound property of unstable nuclei.

Pd/sulfated alumina - a new effective catalyst for the selective catalytic reduction of NO with CH4

Sulfated alumina (SA) is firstly found to be an effective support for Pd catalyst used in the SCR of NO with methane. The sulfation is important to increase support's acidity which is essential for the reduction of NO over Pd catalysts. On consideration of the lower cost and easier availability of SA, we believe that SA is more promising to act as the commercial support for Pd catalyst used in the SCR of NO with methane.

Effect of drying methods on the structure and catalytic combustion activity of Mn-substituted hexaaluminate catalysts

Conventional oven drying (COD) and supercritical drying (SCD) methods were applied to the preparation of Mn-substituted hexaaluminate (BaMnA(11)O(19-alpha)) catalysts. The effect of drying methods on phase composition, specific surface area, pore structure and combustion activity of the samples was investigated. The samples obtained by SCD have higher surface area, narrower pore size distribution, and higher combustion activity than those obtained by COD.

Thermodynamic investigation on properties of gasohol

The heat capacities (C-p) of three types of gasohol (which consisted of 20 wt % ethanol and 80 wt % unleaded gasoline 93(#) (system S1), 30 wt % ethanol and 70 wt % unleaded gasoline 931 (system S2), 40 wt % ethanol and 60 wt % unleaded gasoline 930 (system S3), where "93(#)" denotes the octane number) were measured by adiabatic calorimetry in the temperature range of 80320 K. A glass transition was observed at 94.24, 95.15, and 95.44 K for system S1, S2, and S3, respectively. A solid-solid phase transition and solid-liquid phase transition were observed at 135.18 and 151.30 K for system S1, 131.82 and 152.10 K for system S2, and 121.29 and 155.09 K for S3, respectively. The polynomial equations for C, with respect to the thermodynamic temperature (T), and with respect to the content of ethanol (x), were established through the least-squares fitting. The thermodynamic functions and the excess thermodynamic functions of the three samples were derived using these thermodynamic relationships and equations.

Thermodynamic study of ibuprofen by adiabatic calorimetry and thermal analysis

Molar heat capacities of ibuprofen were precisely measured with a small sample precision automated adiabatic calorimeter over the temperature range from 80 to 400 K. The polynomial functions of C-p,C-m (J K-1 mol(-1)) versus T were established on the heat capacity measurements by means of the least fitting square method. The functions are as follows: for solid ibuprofen, at the temperature range of 79.105 K less than or equal to T less than or equal to 333.297 K, C-p,C-m = 144.27 + 77.046X + 3.5171X(2) + 10.925X(3) + 11.224X(4), where X = (T - 206.201)/127.096; for liquid ibuprofen, at the temperature range of 353.406 K less than or equal to T less than or equal to 378.785 K, C-p,C-m = 325.79 + 8.9696X - 1.6073X(2) - 1.5145 X-3, where X = (T - 366.095)/12.690. A fusion transition at T = 348.02 K was found from the C-p-T curve. The molar enthalpy and entropy of the fusion transition were determined to be 26.65 kJ mol(-1) and 76.58 J mol(-1) K-1, respectively. The thermodynamic functions on the base of the reference temperature of 298.15 K, (H-T - H-298.15) and (S-T - S-298.15), were derived. Thermal characteristic of ibuprofen was studied by thermo-gravimetric analysis (TG-DTG) and differential scanning calorimeter (DSC). The temperature of fusion, the molar enthalpy and entropy of fusion obtained by DSC were well consistent with those obtained by adiabatic calorimeter. The evaporation process of ibuprofen was investigated further by TG and DTG, and the activation energy of the evaporation process was determined to be 80.3 +/- 1.4 kJ mol(-1). (C) 2003 Elsevier B.V. All rights reserved.