995 resultados para 190-1175
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藏文属于拼音文字,她的书写规则与英语书写规则一样是从左向右,从上到下,但每个单词之间没有空格,只用音节符把每个单词给分隔开。根据藏文文法,藏文的换行只能发生在音节符、单垂符,双垂符与空格的后面。目前主流浏览器(如Firefox,Netscape等)都不能处理藏文的这一断行特性,所以这些浏览器无法正常显示藏文文本,如Firefox将整个一段没有空格文本当作一个单词,造成在屏幕的右边无法换行。结果是用户必须拖动鼠标来浏览整篇文章,给用户带来了很大的麻烦。又由于藏文中大部分的拼音字母的宽度是不同的,在编写HTML文档时候也无法根据藏文字符串的多少来决定字符串的长度。该算法将采用了一个粗略的方法得到一个字符串长度的近似值,再根据行宽的限制在字符串的适当的位置找到一个可断行点进行断行。虽然得到的是近似值,但是基本上解决了主流浏览器无法处理藏文排版的问题。
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分别应用管式炉反应器和热重分析手段对印刷线路板废弃物的热解行为和热解动力学进行了实验研究。在管式炉中,研究不同的热解温度:700~950℃,对产物分布和气体成分分布的影响。实验结果表明:PCB热解气体的主要成分是H2和CO2,气体的热值较低,仅为2.09~5.41MJ/m^3,PCB不适合以气体产物为目标的能源利用方式。应用Friedman方法对PCB的热解动力学进行了研究,求得PCB的热解动力学参数分别是:表观活化能190.92kJ/mol,反应级数5.97,指前因子lnA47.14min^-1。
A tubular furnace and thermogravimetry analysis (TGA) was used to investigate the characteristics of printed circuit'boards (PCB) pyrolysis and its kinetics,respectively. The effect of different temperatures: 700 ~950℃ on the products distribution and gas composition of PCB pyrolysis was explored. The results indicate that the main components of the gas derived from PCB are H2 and CO2 and the gas has a lower heating value (LHV) : 2.09~5.41 MJ/m^3. It can be concluded that PCB is not favorable for energy application directed at gas production. Friedman method was utilized to analyze the pyrolysis kinetics of PCB. The kinetic parameters obtained were: apparent activation energy 190.92 kJ/mol, reaction order 5.97 ,pre-exponential factor lnA 47.14 min^-1.
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国家自然科学基金;广东省自然科学基金
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受迫内流气体发生的理论及实验关联郭开华,陈阵,舒碧芬,蒙宗信(中国科学院广州能源研究所热泵及空调制冷技术研究中心广州510070)关键词气体发生,多相流,混合物,传热传质1引言在吸收式能量转换系统(如吸收人热泵、制冷机、吸收压缩复合式热泵、卡林纳动力...
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Multi-channel effect is important to understand transport phenomenon in phase change systems with parallel channels. In this paper, visualization studies were performed to study the multi-channel effect in a silicon triple-channel condenser with an aspect ratio of 0.04. Saturated water vapor was pumped into the microcondenser, which was horizontally positioned. The condenser was cooled by the air natural convention heat transfer in the air environment. Flow patterns are either the annular flow at high inlet vapor pressures, or a quasi-stable elongated bubble at the microchannel upstream followed by a detaching or detached miniature bubble at smaller inlet vapor pressures. The downstream miniature bubble was detached from the elongated bubble tip induced by the maximum Weber number there. It is observed that either a single vapor thread or dual vapor threads are at the front of the elongated bubble. A miniature bubble is fully formed by breaking up the vapor thread or threads. The transient vapor thread formation and breakup process is exactly symmetry against the centerline of the center channel. In side channels, the Marangoni effect induced by the small temperature variation over the channel width direction causes the vapor thread formation and breakup process deviating from the side channel centerline and approaching the center channel. The Marangoni effect further forces the detached bubble to rotate and approach the center channel, because the center channel always has higher temperatures, indicating the multi-channel effect.
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High speed visualizations and thermal performance studies of pool boiling heat transfer on copper foam covers were performed at atmospheric pressure, with the heating surface area of 12.0 mm by 12.0 mm, using acetone as the working fluid. The foam covers have ppi (pores per inch) from 30 to 90, cover thickness from 2.0 to 5.0 mm, and porosity of 0.88 and 0.95. The surface superheats are from -20 to 190 K, and the heat fluxes reach 140 W/cm(2). The 30 and 60 ppi foam covers show the periodic single bubble generation and departure pattern at low surface superheats. With continuous increases in surface superheats, they show the periodic bubble coalescence and/or re-coalescence pattern. Cage bubbles were observed to be those with liquid filled inside and vented to the pool liquid. For the 90 ppi foam covers, the bubble coalescence takes place at low surface superheats. At moderate or large surface superheats, vapor fragments continuously escape to the pool liquid. Boiling curves of copper foams show three distinct regions. Region I and II are those of natural convection heat transfer, and nucleate boiling heat transfer for all the foam covers. Region III is that of either a resistance to vapor release for the 30 and 60 ppi foam covers, or a capillary-assist liquid flow towards foam cells for the 90 ppi foam covers. The value of ppi has an important effect on the thermal performance. Boiling curves are crossed between the high and low ppi foam covers. Low ppi foams have better thermal performance at low surface superheats, but high ppi foams have better one at moderate or large surface superheats and extend the operation range of surface superheats. The effects of other factors such as pool liquid temperature, foam cover thickness on the thermal performance are also discussed.
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A glutamate biosensor based on the electrocatalytic oxidation of reduced nicotinamide adenine dinucleotide (NADH), which was generated by the enzymatic reaction, was developed via employing a single-walled carbon nanotubes/thionine (Th-SWNTs) nanocomposite as a mediator and an enzyme immobilization matrix. The biosensor, which was fabricated by immobilizing glutamate dehydrogenase (GIDH) on the surface of Th-SWNTs, exhibited a rapid response (ca. 5 s), a low detection limit (0.1 mu M), a wide and useful linear range (0.5-400 mu M), high sensitivity (137.3 +/- 15.7) mu A mM(-1) cm(-2), higher biological affinity, as well as good stability and repeatability. In addition, the common interfering species, such as ascorbic acid, uric acid, and 4-acetamidophenol, did not cause any interference due to the use of a low operating potential (190 mV vs. NHE). The biosensor can be used to quantify the concentration of glutamate in the physiological level. The Th-SWNTs system represents a simple and effective approach to the integration of dehydrogenase and electrodes, which can provide analytical access to a large group of enzymes for wide range of bioelectrochemical applications including biosensors and biofuel cells.