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Oxygen content factor 99 volume mixing

机译:氧气含量系数99体积%混合

摘要

PROBLEM TO BE SOLVED: To enable effective vacuum defoaming of a high flow rate of the molten glass even when the degree of vacuum is lowered in order to reduce the difference of liquid surface levels between a melting furnace and a vacuum defoaming vessel by providing the production process with a melting stage for mixing fuel with gaseous oxygen to combust the fuel-oxygen mixture and to melt a glass raw material by the generated heat of combustion, a vacuum defoaming stage and a forming stage for forming the defoamed molten glass into glass articles. ;SOLUTION: In the above vacuum defoaming stage of this production process, the pressure is preferably 0.1 to 0.5 atm. Also, by mixing gaseous oxygen with a natural gas and combusting the resulting mixture, the gaseous combustion product contains water and carbon dioxide in amounts about 3.5 times as much as the amounts of those in the gaseous combustion product when an air-natural gas mixture is combusted and accordingly, comparatively large amounts of water and carbon dioxide are dissolved in molten glass G. Since the amount of dissolved water is sufficiently large, a sufficient defoaming effect is obtained under a ≥0.1 atm pressure, to lower the lifting height of the vacuum defoaming vessel 34 and to solve problems with respect to a similar larger defoaming device. Further, the molten glass G is transmitted to the vacuum defoaming device 30. The vacuum defoaming vessel 34 is placed in a vacuum housing 32 and a riser pipe 36 and a downcomer pipe 38 are placed on the sides of the both ends of the vacuum defoaming vessel 34 respectively and the molten glass G after the defoaming treatment is introduced into a float bath 52.;COPYRIGHT: (C)2000,JPO
机译:解决的问题:为了降低熔融炉与真空消泡容器之间的液面高度差,即使在降低真空度的情况下,也能够对熔融玻璃的高流量进行有效的真空消泡。该方法包括:熔融阶段,用于将燃料与气态氧混合以燃烧燃料-氧气混合物,并通过所产生的燃烧热来熔融玻璃原料;真空消泡阶段;以及用于将消泡的熔融玻璃成型为玻璃制品的成型阶段。 ;解决方案:在该生产过程的上述真空消泡阶段,压力优选为0.1至0.5 atm。同样,通过将气态氧气与天然气混合并燃烧所得混合物,气态燃烧产物中所含的水和二氧化碳的量约为气态天然气混合物中所含气态燃烧产物中水和二氧化碳含量的3.5倍。燃烧并因此将相对大量的水和二氧化碳溶解在熔融玻璃G中。由于溶解的水量足够大,因此在0.1 atm大气压下可获得足够的消泡效果,从而降低了玻璃的提升高度。真空消泡容器34并解决关于类似的较大消泡装置的问题。此外,熔融玻璃G被传送到真空消泡装置30。真空消泡容器34被放置在真空壳体32中,并且在真空消泡的两端的侧面上放置有立管36和下降管38。分别将容器34和消泡处理后的熔融玻璃G引入浮槽52中。版权所有:(C)2000,JPO

著录项

  • 公开/公告号JP4075161B2

    专利类型

  • 公开/公告日2008-04-16

    原文格式PDF

  • 申请/专利权人 旭硝子株式会社;

    申请/专利号JP19980299602

  • 发明设计人 河口 年安;岡田 操;大林 浩治;

    申请日1998-10-21

  • 分类号C03B5/235;B01D19/00;C03B5/225;

  • 国家 JP

  • 入库时间 2022-08-21 20:18:48

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