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我们的祖先使用玉器,其功能大致为以下几个方面:1、礼仪和宗教、巫术活动用玉。如璧、琮、圭、璋、璜、剑、玺、带、佩等。这类玉器是古代玉器的重要组成部分。玉礼器是中国“礼乐文明”的重要载体之一;2、丧葬用玉。如冶、握、塞、玉衣等;3、装饰佩戴用玉。如坠、块、珠、管、环、镯,以及有使用价值的扳指、梳、带钩、剑首、剑格、如意等。 相似文献
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感冒香蕉、橘子、芦笋汁、羊肉、姜母鸭。咳嗽冰淇淋、橘子、炸(烤)食品、花生、酒、甜食、辣食。急性胃炎油炸食物、辣椒、糯米。慢性胃炎生冷食物、酸酵食物、甜食。 相似文献
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<正>适宜食物1、主食及豆类的选择:绿豆、赤豆、小米等各种主食均可,适当食用粗粮和豆制品。2、肉蛋奶的选择:猪瘦肉、牛肉、鱼肉、鸡肉、鸭肉、动物肝脏等,奶及奶制品,咸鸭蛋、咸鸡蛋、松花蛋、蛋黄等蛋类。3、蔬菜的选择:苦瓜、丝瓜、南瓜、空心菜、马兰头、番茄、蒜苗、茄子、鲜藕、绿豆芽、黄瓜、冬瓜、菜瓜、香菇、紫菜、海带等。4、水果的选择:柑橘、葡萄、草莓、西瓜、梨、甜瓜、桃、杨梅、乌梅、李、红枣等。饮食禁忌1、夏天一定要少吃太热的食物,如羊肉、狗肉等。 相似文献
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文章开始之前,我们先对四川火锅做一个最基础的了解,或许有很多人吃了那么多年的四川火锅。还不知道究童是怎么一回事。火锅古已有之。近代其制作工艺逐渐发展。四川火锅以它的辣而不燥、麻而不烈、风味厚重、久食不腻红遍全国各地。四川火锅用牛骨汤、固体牛油、豆瓣、辣椒、花椒等多种原料、调料配制汤汁。煮汤后,即可将洗净的毛肚、鱼片、鳝鱼片、鸭血等放入锅烫食。烫熟的菜.放入香油碟于.边蘸边吃。吃起来有麻、辣、烫、鲜、嫩、脆等特点。早期的火锅以烫毛肚为主,后来发展为烫食各种荤、素菜。最初多在寒冬腊月吃,现在人们一年四季都爱吃。而且火锅品种繁多,有红锅、白锅、鸳鸯锅。有排骨火锅、肥肠火锅、酸菜鱼火锅.有火锅鸡、火锅鸭、火锅免等.四川人多爱吃火锅,并以此自待客佳肴。 相似文献
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私家御鼎香主料:鱼翅、鱼唇、干鲍、海参、干贝、鸽蛋、蹄筋、鱼肚,虾仁。辅料:浓汤、调料、水淀粉等。做法:将所有原料发制、调好味、放人蒸箱至软熟,净锅放上等浓汤上火,水淀粉勾芡,淋入蒸好的原料中即可。大厨小砧士:这道菜品由高蛋白、高营养的9种原料蒸制而成,鲜香味醇,彼此融合。具有明目养颜、舒筋活血、滋阴健体的养生功效。成菜色彩金亮、汁浓味厚,口感绵而不腻,食后唇齿留香。整道菜肴的食材搭配结构合理,补而不燥。 相似文献
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根据奥氏体化组织转变原理 ,比较明火炉和马弗炉及不锈钢管式半明火炉的工艺特点 ,分析和探讨明火炉的优势和工艺特性。不同的炉子应采用不同的热处理工艺 ,明火炉DV值较高 ,温度高、车速快 ,可以提高热效率。明火炉加热技术是今后的发展方向。 相似文献
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说明钢丝加热、炉体表面散热和电功率计算公式。以具体实例计算出装炉量为8~15 t,最高使用温度为900℃的退火炉在考虑装料炉架、炉盖、内胆、保护气体和冷却水消耗情况下的加热功率为280 kW,并以此为基础,推算出不同退火温度和不同装炉量时的加热时间,为制定退火工艺提供依据。 相似文献
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介绍将琴钢丝热处理马弗炉由煤气加热改造为电加热的情况,从炉型、马弗砖材质及电气控制等方面对比新旧炉型,新炉型在线温的均匀性、力学性能、保温节能、成材率等方面均有明显提高,从而保证了琴钢丝的产品质量。 相似文献
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对比分析了4种铁丝退火炉型,指出井式电阻炉和不锈钢管型连续式电阻炉较适合铁丝的退火.具体选用何种炉型须根据车间位置、燃料情况确定. 相似文献
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井式炉的结构和维护方法 总被引:2,自引:2,他引:0
介绍球化退火井式炉的基本结构,对自预热燃烧器的结构和工作原理进行详述。提出设备重要部件如内筒及对流筒、炉底搅拌风扇、温控和电控系统维护过程中需要注意的问题。在井式炉使用过程中除了检查循环冷却水、炉底搅拌风扇、气氛压力、炉体密封、热电偶等是否正常外,应及时对甲醇裂解炉和甲醇裂解气管道进行除炭。在使用和维护时,应及时检查炉体的密封状况和设备机械传动件的润滑情况,控制进炉物料数量,保证井式炉工艺稳定。 相似文献
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Wang J Levendis YA Richter H Howard JB Carlson J 《Environmental science & technology》2001,35(17):3541-3552
A study is presented on laboratory-scale combustion of polystyrene (PS) to identify staged-combustion conditions that minimize emissions. Batch combustion of shredded PS was conducted in fixed beds placed in a bench-scale electrically heated horizontal muffle furnace. In most cases, combustion of the samples occurred by forming gaseous diffusion flames in atmospheric pressure air. The combustion effluent was mixed with additional air, and it was channeled to a second muffle furnace (afterburner) placed in series. Further reactions took place in the secondary furnace at a residence time of 0.7 s. The gas temperature of the primary furnace was varied in the range of 500-1,000 degrees C, while that of the secondary furnace was kept fixed at 1,000 degrees C. Sampling for CO, CO2, O2, soot, and unburned hydrocarbon emissions (volatile and semivolatile, by GC-MS) was performed at the exits of the two furnaces. Results showed that the temperature of the primary furnace, where PS gasifies, is of paramount importance to the formation and subsequent emissions of organic species and soot. Atthe lowesttemperatures explored, mostly styrene oligomers were identified at the outlet of the primary furnace, but they did not survive the treatment in the secondary furnace. The formation and emission of polycyclic aromatic hydrocarbons (PAH) and soot were suppressed. As the temperature in the first furnace was raised, increasing amounts of a wide range of both unsubstituted and substituted PAH containing up to at least seven condensed aromatic rings were detected. A similar trend was observed for total particulate yields. The secondary furnace treatment reduced the yields of total PAH, but it had an ambiguous effect on individual species. While most low molecular mass PAH were reduced in the secondary furnace, concentrations of some larger PAH increased under certain conditions. Thus, care in the selection of operating conditions of both the primary furnace (gasifier/ burner) and the secondary furnace (afterburner) must be exercised to minimize the emission of hazardous pollutants. The emissions of soot were also reduced in the afterburner but not drastically. This indicates that soot is indeed resistant to oxidation; thus, it would be best to avoid its formation in the first place. An oxidative pyrolysis temperature of PS in the vicinity of 600 degrees C appears to accomplish exactly that. An additional afterburner treatment at a sufficiently high temperature (1,000 degrees C) may be a suitable setting for minimization of most pollutants. To obtain deeper understanding of chemical processes, the experimental results were qualitatively compared with preliminary predictions of a detailed kinetic model that describes formation and destruction pathways of chemical species including most PAH observed in the present work. The modeling was performed forthe secondary furnace assuming plug-flow conditions therein. The experimentally determined chemical composition at the outlet of the primary furnace was part of the input parameters of the model calculation. 相似文献
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介绍X -R控制图的基本控制原理 ,并运用该原理对煤气加热炉的温度进行控制。详细说明炉温数据的收集原则和分组情况。通过实例计算出控制界限和中心线 ,画出X -R控制图 ,给出炉温受控状态的标准和炉温异常的处理方法 ,对炉温控制起到了报警作用。 相似文献