波-流相互作用的缓坡方程及其波作用量守恒

当表面波从开阔海域传播至近岸水域时,普遍的波-流相互作用经受着海底的强烈影响,运用水波Hamil-ton变分原理,建立了近岸水域任意水深变化海底上波-流相互作用的缓坡方程.它可包含波、流和水深一般变化的二阶效应,约化为某些典型的缓坡型方程.据此得出广义程函方程,并且证明该缓坡方程的波作用最守恒.

在光子晶体光纤中实现波长调谐飞秒孤子脉冲输出

介绍了在光子晶体光纤中产生波长调谐飞秒光孤子脉冲的机理及研究进展，并对波长调谐飞秒孤子激光系统进行了分析和比较。

大规模复杂自然场景的时变模拟研究

大规模复杂自然场景真实感生成一直是计算机图形学的难点和热点之一，而用计算机模拟物体风化/老化/枯萎等现象是真实感图形学的新兴热点研究内容。上述两项技术可成功应用于包括计算机动画、虚拟现实、电影特效和数字游戏等方面。本文对这两个领域中的问题进行了研究与探讨，并取得了研究成果。 自然物体具有丰富复杂的细节，并且数据量很大，其在计算机中的真实感表示一直是图形学中一个富有挑战性的问题。随着研究与应用的深入，人们已不再仅仅满足于自然物体的静态真实感效果，而更加关注于自然场景中的动态时变过程，以及所形成的自然现象的整体效果。对于自然物体会发生的风化/老化/枯萎等现象进行时变模拟可以增强已有结果的真实感。本文即针对大规模自然场景中复杂物体的时变模拟进行了研究，提出了真实感表示、时变模型以及加速绘制等方面的一系列解决方法。这些方法与技术为真实感模拟自然物体的时变现象创造了条件，具有很强的实用价值。本文的主要工作和贡献如下：  首次提出了时变纹元的表示结构，可成功地用于模拟复杂自然物体的风化/枯萎等现象。该结构改进了传统三维纹元，加入时变特性方面的描述信息。时变纹元中记录的纹元变化序列，可有效用于表示自然场景中最重要组成部分──大规模草地的枯萎时变过程。本文使用时间-空间划分树对时变纹元数据进行重新组织及有效压缩。采用这种层次树结构处理的时变纹元，并应用GPU上的光线行进算法进行快速体绘制，最终可得到具有真实感的时变模拟结果。  基于时变纹元的表示结构，提出一种新的模型结构转换机制，使之能够采用物理模型/过程模型对复杂自然物体的动态几何形变进行模拟。纹元的三维阵列结构难以处理物体的个体几何形变，因此本文提出借鉴点模型的转换结构以解决这个问题。本文给出了点模型和纹元的转换规则，可通过计算点模型的动态信息而得到纹元的时变序列。该算法充分结合了纹元结构及点模型的优势，为模拟复杂自然物体的时变现象提供了有效新型方法。  首次提出了γ-ton体跟踪算法，可用于对复杂自然物体的风化现象进行模拟。γ-ton跟踪算法是目前能够有效模拟物体风化现象的通用框架之一，可同时计算物体几何形状和材质随时间变化的情况。但是该方法仅适用于跟踪发生在物体表面的时变现象，而无法处理自然物体体结构中的材质及形状的改变。本文提出的γ-ton体跟踪算法可针对复杂自然物体，模拟其体结构上产生的风化/老化现象，增强了算法的适用性。  首次提出了基于纹元结构的重绘制算法来增强图像及视频中的毛发真实感。该算法采用图像分析方法，将图像中的目标区域进行提取并网格化，生成纹元结构并映射到图像网格之上，通过重绘制算法得到增强毛发感的新图像。本文的算法同样可处理视频，首先计算得到视频关键帧的重绘制结果，然后基于目标区域在时间轴上的匹配情况，从关键帧出发进行前向及后向传递，计算视频中的其余帧的重绘制结果，最终得到毛发感增强的新视频。本文的方法提供了一种能够高效生成具备毛发真实感的图像及视频的新型方法，这对于电影制造业有很高的应用价值。

Design and operation of integrated pilot-scale dimethyl ether synthesis system via pyrolysis/gasification of corncob

The integrated pilot-scale dimethyl ether (DME) synthesis system from corncob was demonstrated for modernizing utilization of biomass residues. The raw bio-syngas was obtained by the pyrolyzer/gasifier at the yield rate of 40-45 Nm(3)/h. The content of tar in the raw bio-syngas was decreased to less than 20 mg/Nm(3) by high temperature gasification of the pyrolysates under O-2-rich air. More than 70% CO2 in the raw bio-syngas was removed by pressure-swing adsorption unit (PSA). The bio-syngas (H-2/CO approximate to 1) was catalytically converted to DME in the fixed-bed tubular reactor directly over Cu/Zn/Al/HZSM-5 catalysts. CO conversion and space-time yield of DME were in the range of 82.0-73.6% and 124.3-203.8 kg/m(cat)(3)/h, respectively, with a similar DME selectivity when gas hourly space velocity (GHSV, volumetric flow rate of syngas at STP divided by the volume of catalyst) increased from 650 h(-1) to 1500 h(-1) at 260 degrees C and 4.3 MPa. And the selectivity to methanol and C-2(+) products was less than 0.65% under typical synthesis condition. The thermal energy conversion efficiency was ca. 32.0% and about 16.4% carbon in dried corncob was essentially converted to DME with the production cost of ca. (sic) 3737/ton DME. Cu (111) was assumed to be the active phase for DME synthesis, confirmed by X-ray diffraction (XRD) characterization.

Scale study of direct synthesis of dimethyl ether from biomass synthesis gas

We investigated the synthesis of dimethyl ether (DME) from biomass synthesis gas using a kind of hybrid catalyst consisting of methanol and HZSM-5 zeolite in a fixed-bed reactor in a 100 ton/year pilot plant. The biomass synthesis gas was produced by oxygen-rich gasification of corn core in a two-stage fixed bed. The results showed that CO conversions reached 82.00% and 73.55%, the selectivities for DME were 73.95% and 69.73%, and the space-time yields were 124.28 kg m- 3 h- 1 and 203.80 kg m- 3 h- 1 when gas hourly space velocities were 650 h- 1 and 1200 h- 1, respectively. Deoxidation and tar removal from biomass synthesis gas was critical to the stable operation of the DME synthesis system. Using single-pass synthesis, the H2/CO ratio improved from 0.98-1.17 to 2.12-2.22. The yield of DME would be increased greatly if the exhaust was reused after removal of the CO2.

Design and Operation of A 5.5 MWe Biomass Integrated Gasification Combined Cycle Demonstration Plant

The design and operation of a 5.5 MWe biomass integrated gasification combined cycle (IGCC) demonstration plant, which is located in Xinghua, Jiangsu Province of China, are introduced. It is the largest complete biomass gasification power plant that uses rice husk and other agricultural wastes as fuel in Asia. It mainly consists of a 20 MWt atmospheric circulating fluidized-bed gasifier, a gas-purifying system, 10 sets of 450 kW(e) gas engines, a waste heat boiler, a 1.5 MWe steam turbine, a wastewater treatment system, etc. The demonstration plant has been operating since the end of 2005, and its overall efficiency reaches 26-28%. Its capital cost is less than 1200 USD/kW, and its running cost is about 0.079 USD/kWh based on the biomass price of 35.7 USD/ton. There is a 20% increment on capital cost and 35% decrease on the fuel consumption compared to that of a 1 MW system without a combined cycle. Because only part of the project has been performed, many of the tests still remain and, accordingly, must be reported at a later opportunity.

PH值、氯离子浓度和监酸浓度对于铁的腐蚀电化学行为的影响

本文研究了Armco铁在盐酸溶液中的腐蚀电化学行为，探讨了ψ~-离子和PH值对铁的阳极溶解过程的影响，并进而讨论了ψ~-离子浓度和PH值对铁的腐蚀电化学行为的影响之间是否存在交互效应。在本工作中，作者提出了两个新的研究方法：(a) 从单支弱极化曲线测定腐蚀电流和阴、阳极反应的Tafep斜率；(b)根据交流方波电流扰动的响应函数方程测定极化电阻Rp和界面电容C。设I_c、I_(2c)、I_(3c)及I_(4c)分别为对应于弱极化区内极化电位为ΔE、2ΔE、3ΔE和4ΔE的极化电流，且令a = I_(2c)/I_c, b = I_(3c)/I_c, c = I_(4c)/I_(2c), 而(4b-3a~2)~(1/2)、(3c-2b)~(1/2)、(2c-a~2)~(1/2)则以S_j表示之，则可得到：I_(corr) = I_c/S_j b_c = ΔE/lg((a+s_j)/2) b_a = -ΔE/lg((a-s_j)/2)为了方便，准确地求出动力学参数，可选用一系列的ΔE值，得出相应的极化电流I_λ，求出S_λ，应用统计方法处理数据，可得：I_(corr) = ∑ from i=1 to n I_λ/∑ from i=1 ton S_λ b_c = ∑ form λ to n ΔE_λ/∑ form i=1 to n lg ((a_λ+S_λ)/2) b_a = ∑ form i=1 ton ΔE_λ/∑ form i=1 to n lg ((a_λ-S_λ)/2)在线性极化区间内向腐蚀金属电极体系施加一交流方波电流扰动讯号时，通过Laplace变换分析，得到相应的响应函数方程为：E_1(t) = λ_o(R_s+R_p) - 2λ_oR_p (e~(-(τ-λ)/RpC))/(1+e~(λ/RpC)) (o<τ<λ) E_2(t) = -λ_o(R_s+R_p) + 2λ_oR_p (e~(-(τ-λ)/RpC))/(1+e~(λ/RpC)) (λ<τ<2λ)由此方程可知，它们在E～λ坐标系统中的轨迹为对称兴致勃勃原点的两条直线。由此方程可进一步得到:ΔE = 2λ_oR_p (e~(λ/RpC)-1)/(e~(λ/RpC)+1) = 2λ_oR_p t_(anh)(λ/(2RpC)) Δh = 2λ_o Rs式中ΔE为单支响应直线的长度，Δh则为两条直线最高点之间的距离。上述公式可进一步简化为：Rp =(ΔE)/(2λ_o) λ>>RpC (λ_o)/(ΔE) = C/λ + 1/(2Rp) λ<

垃圾渗滤液场外硝化－原位反硝化脱氮协同填埋场温室气体减排

垃圾卫生填埋是国内外城市垃圾的主要处置方法。垃圾渗滤液是渗入填埋场垃圾的降水混合垃圾降解过程中产生的物质而形成的混合物，是垃圾填埋场向环境排放的主要污染物。渗滤液由于其所含高浓度有机和无机污染物，且其中很多物质有生物毒性或难生物降解，难于治理。特别是到填埋晚期，渗滤液中高浓度的氨氮更是增加了治理的难度。渗滤液场外硝化－原位反硝化是填埋场氮管理的新途径。本文利用从环境中筛选出优势硝化功能菌对渗滤液中的高浓度氨氮进行生物硝化，经硝化后的渗滤液回灌至以垃圾柱模拟的生物反应器填埋场，在填埋场内实现原位反硝化。 上述目标通过以下两部分来实现： 第一部分：渗滤液场外硝化。首先从污水厂的硝化污泥中富集并筛选出硝化功能菌，在模拟氨氮废水中优化。将驯化的硝化功能菌接种于连续式完全混合反应器（CSTR）进行高氨氮渗滤液硝化研究。在200余天的连续运行中，反应器硝化和有机物去除效果良好。在最大氨氮负荷和有机物负荷分别为0.65 g N l-1 d-1 和3.84 g COD l-1 d-1时，氨氮和COD去除率分别高于99%和57%。实验过程中发现，游离氨（FA）和溶解氧（DO）浓度对反应器中亚硝酸盐的积累影响很大。 第二部分：渗滤液原位反硝化。本文利用一个垃圾填充柱模拟生物反应器填埋场，研究了硝化渗滤液回灌对垃圾降解的影响，和回灌的硝化渗滤液中TON（总氧化态氮）对填埋场生物反应器产甲烷作用的影响。最后利用变性梯度凝胶电泳（DGGE）分析了硝化渗滤液回灌对垃圾填埋场菌群结构的影响。结果表明：回灌的TON被完全还原，反硝化为主要反应，最大TON负荷为28.6 mg N kg-1 TS d-1。当垃圾柱TON负荷大于11.4 mg N kg-1 TS d-1时，出现了产甲烷抑制，抑制作用随TON负荷的增加而加强。在此过程中，反硝化逐渐代替产甲烷作用成为填埋场内垃圾降解的主要反应，且更多产生的是清洁的氮气，而非温室气体甲烷。直到实验结束时，回灌硝化渗滤液的垃圾柱的甲烷产量仅相当于对照的2.5%，并且回灌的硝化渗滤液还加速了填埋场垃圾的降解与稳定。通过DGGE进行菌群结构分析发现，由于TON对填埋场的长期作用，反硝化菌增多而产甲烷菌减少。 Landfill still remains the chief method for MSW management around the world. Leachate is a mixture of rainfall permeating through landfill and organic and inorganic matters generated during decomposition of the wastes in the landfills, characterized as highly complicated and refractory wastewater. Ex-situ nitrification and sequential in-situ denitrification represents a novel approach to nitrogen management at landfills. In the present paper, nitrification was carried out in a continuous stirred tank reactor (CSTR) inoculated with nitrifying bacteria which were isolated from municipal WWTP of Chengdu city. The nitrified leachate from CSTR was recirculated to a lab-scale municipal solid waste (MSW) column where in-situ denitrification took place. The above object was achived through two parts as following: First, ex-situ nitification of leachate. After acclimated in simulated wastewater for 3 month, nitrifying bacteria isolated from WWTP nitrifying sludge were added to the CSTR for nitrification. The results over 200 days showed that the maximum nitrogen loading rate (NLR) and the maximum organic loading rate (OLR) was 0.65 g N l-1 d-1 and 3.84 g COD l-1 d-1, respectively. The ammonia and COD removal was over 99% and 57%, respectively. Moreover, the effects of free ammonia (FA) and dissolved oxygen (DO) on nitrification were investigated. Second, in-situ denitrification was studied in a municipal solid waste (MSW) column. Variation of nitrified leachate and its effects on the decomposition of municipal solid waste (MSW) were studied in a lab-scale MSW column to which nitrified leachate was recirculated. Additionally, DGGE was employed to investigate the microbial community of both MSW columns. The results suggested: complete reduction of total oxidized nitrogen (TON) was obtained with maximum TON load of 28.6 mg N kg-1 TS d-1 and denitrification was the main reaction responsible. Methanogenesis inhibition was observed while TON load was over 11.4 mg N kg-1 TS d-1 and the inhibition was enhanced with the increase of TON load. Denitrification gradually took over methanogenesis to become the main reaction responsible for decomposition of MSW while nitrogen gas, a clean byproduct, was generated instead. Till the end of the experiment, the average weekly methane production in the denitrification column was as low as 2.5% of that of the control, and the rate of decompition and stability of MSW was accelerated by the recirculation of the nitrified leachate.Owing to long term exposure of nitrified leachate to landfill, denitrifying bacteria increased and methanogen decreased.

Design optimization of the APF DTL in the SSC-linac

A linear accelerator as a new injector for the SSC (Separated Sector Cyclotron) of the HIRFL (Heavy ton Research Facility Lanzhou) is being designed. The DTL (Drift-Tube-Linac) has been designed to accelerate U-238(34+) from 0.140 MeV/u to 0.97 MeV/u. To the first accelerating tank which accelerates U-238(34+) to 0.54 MeV/u, the approach of Alternating-Phase-Focusing (APF) is applied. The phase array is obtained by coupling optimization software Dakota and beam optics code LINREV. With the hybrid of Multi-objective Genetic Algorithm (MOGA) and a pattern search method, an optimum array of asynchronous phases is determined. The final growth, both transversely and longitudinally, can meet the design requirements. In this paper, the deign optimization of the APF DTL is presented.

黄土旱塬粮食高产记录及其启示

研究了黄土旱塬区历史的与当今的粮食高产记录 ,结果表明 ,目前黄土旱塬各地出现的一料作物单产 15t/hm2 ,在国内其它地区也不多见。据此明确指出 ,黄土旱塬区粮食生产有巨大潜力 ,深入开展粮食高产研究必将推动粮食“高产、高质、高效”的全面发展 ,还将促进农业科学研究取得长足进步以至突破性发展 ,创建粮食高产还可成为治理水土流失与改善生态环境的突破口

中国化肥施用与粮食生产的进程、前景与布局

根据试验研究资料与调查结果，对中国粮食生产与化肥施用进行了时空宏观分析。结果表明，化肥施用量是２０ 世纪中国粮食生产重大成就之一，化肥对粮食产量的贡献率平均为４６．４３％ ，每吨化肥科学施用可增产粮食８．８４ｔ。２１ 世纪中国粮食产量与化肥施量将持续增长。粮食每增产１００×１０６ｔ，则化肥最少需增施１０．２２～１１．０８×１０６ｔ。为实现粮食持续发展与化肥高效施用，必须实施发展东部平原带，提高中部高原带，开发西部高寒荒漠带的战略布局。各带都应大力发展优质粮食与特用粮食生产，以提高国产粮食的市场占有率。