VACUUM DEGASSING APPARATUS, APPARATUS FOR PRODUCING GLASS PRODUCTS AND PROCESS FOR PRODUCING GLASS PRODUCTS
    2.
    发明申请
    VACUUM DEGASSING APPARATUS, APPARATUS FOR PRODUCING GLASS PRODUCTS AND PROCESS FOR PRODUCING GLASS PRODUCTS 有权
    真空脱脂装置,生产玻璃制品的装置和生产玻璃制品的方法

    公开(公告)号:US20110016922A1

    公开(公告)日:2011-01-27

    申请号:US12895930

    申请日:2010-10-01

    IPC分类号: C03B5/225 C03B5/16

    CPC分类号: C03B5/2252 C03B5/2257

    摘要: A vacuum degassing apparatus having a throughput of at least 200 tons/day without causing problems such as a stagnation of molten glass flow in the molten glass flow path, an increment of flow rate of the molten glass flow in a local area, an excessive increment of pressure loss of the molten glass flow.A vacuum degassing apparatus comprises a vacuum degassing vessel, and an uprising pipe and a downfalling pipe which are connected with the vacuum degassing vessel, wherein the vacuum degassing vessel includes a wide portion for providing a molten glass flow path, and in the wide portion, the proportion W1/L1 of the breadth of molten glass flow path W1 to the length of molten glass flow path L1 is at least 0.2 and that in the vacuum degassing vessel, the breadth of molten glass flow path W2 of the portion connected with the uprising pipe and the breadth of molten glass flow path W3 of the portion connected with the downfalling pipe are narrower than the breadth of molten glass flow path W1 in the wide portion, and the position of the bottom of molten glass flow path of the portion connected with the uprising pipe and the position of the bottom of molten glass flow path of the portion connected with the downfalling pipe are lower than the position of the bottom of molten glass flow path of the wide portion.

    摘要翻译: 具有至少200吨/天的生产量的真空脱气装置,不会引起熔融玻璃流道中的熔融玻璃流停滞,局部熔融玻璃流量的增加,过度增量 的熔融玻璃流的压力损失。 真空脱气装置包括真空脱气容器,与真空脱气容器连接的上升管和下降管,其中真空脱气容器包括用于提供熔融玻璃流动路径的宽部分,并且在宽部分中, 熔融玻璃流路W1的宽度与熔融玻璃流路L1的长度的比例W1 / L1为至少0.2,而在真空脱气槽中,与上升部分连接的部分的熔融玻璃流路W2的宽度 管道和与下降管连接的部分的熔融玻璃流动路径W3的宽度比宽部分中的熔融玻璃流动路径W1的宽度窄,并且该部分的熔融玻璃流动路径的底部位置与 上升管和与下降管连接的部分的熔融玻璃流动路径的底部的位置低于熔融玻璃流动路径的底部的位置 的广泛部分。

    Method for producing high silicate fibres
    6.
    发明授权
    Method for producing high silicate fibres 失效
    高硅酸纤维生产方法

    公开(公告)号:US08414807B2

    公开(公告)日:2013-04-09

    申请号:US12602886

    申请日:2007-06-05

    摘要: The invention relates to a method for producing continuous chopped, coarse, staple inorganic fibers from such natural minerals and rocks as sand, quartz, reduced quartz sand stone and quartzite. The inventive method consists in melting silicon-based stone, which is used in the form of a raw material, at a temperature of 1750-1850° C., the melt being homogenated and stabilized at said temperature, in forming a decompression zone on the path of the melt flow to the discharge orifice die, in which the melt flow is shaped in the form of a strip with a thickness of 3-20 mm, and in passing said strip through the decompression zone at a speed V=(7 . . . 9)10−4 m/s. The air pressure in the decompression zone above the melt flow is maintained within a range of 0.10-0.30 Pa. The inventive device comprises a furnace for producing melt, a feeder, at the output of which a transfer chamber is mounted, a discharge orifice, a stream feeder assembly and a fiber producing mechanism. A homogenizer in the form of two cylinders, which are vertically and coaxially arranged with a gap one inside the other, is situated between the furnace and the feeder. A vertical baffle for producing a melt flow in the form of a strip is placed in the external cylinder. A clarifying chamber is provided with a unit for forming vacuum in the cavity thereof. Said invention makes it possible to increase the strength and chemical resistance of produced fibers by providing conditions for reducing the number of foreign, in particular, gaseous inclusions.

    摘要翻译: 本发明涉及从诸如沙,石英,还原石英砂石和石英岩等天然矿物和岩石生产连续的切碎,粗,无机纤维的方法。 本发明的方法包括在1750-1850℃的温度下熔化以原料形式使用的硅基石料,熔体均匀化并在所述温度下稳定,形成减压区 熔体流动到排出孔模头的路径,其中熔体流动形式为厚度为3-20mm的条带形式,并且使所述条带以通过减压区域的速度V =(7°)传递。 9)10-4m / s。 在熔体流动以上的减压区中的空气压力保持在0.10-0.30Pa的范围内。本发明的装置包括一个用于生产熔体的炉子,一个输送器,其输出端安装一个传送室,一个排放孔, 流供料器组件和纤维生产机构。 两个圆柱体形式的均质器位于炉子和进料器之间,两个圆柱体的垂直和同轴布置有间隙,位于另一个之间。 用于产生带状熔体流的垂直挡板放置在外筒中。 澄清室设置有用于在其空腔中形成真空的单元。 通过提供减少外来物质,特别是气态夹杂物的数量的条件,可以提高生产的纤维的强度和耐化学性。

    GLASS MELTING FURNACE AND METHOD FOR MELTING GLASSES
    7.
    发明申请
    GLASS MELTING FURNACE AND METHOD FOR MELTING GLASSES 审中-公开
    玻璃熔炼炉和熔化玻璃的方法

    公开(公告)号:US20100175427A1

    公开(公告)日:2010-07-15

    申请号:US12161968

    申请日:2008-04-25

    申请人: Helmut Sorg

    发明人: Helmut Sorg

    IPC分类号: C03B5/18 C03B5/16

    摘要: A glass melting furnace with a tank and a superstructure with a furnace crown and a total internal length (“Lg”), with a preheating zone for charging material and a combustion zone with burners. A single radiation wall is located between the preheating zone and the combustion zone such that the length of the preheating zone is between 15 and 35% of the total internal length and the length of the combustion zone is between 65 and 85% of the total internal length. The preheating zone is designed for use solely with preheating of the charging material within the furnace. The oxidation gas supply contains at least 85 volume percent oxygen and at least one outlet for the waste gases from the preheating zone is connected to the atmosphere without a heat exchanger.

    摘要翻译: 具有罐和具有炉冠和总内部长度(“Lg”)的上部结构的玻璃熔炉,具有用于充电材料的预热区域和具有燃烧器的燃烧区域。 单个辐射壁位于预热区和燃烧区之间,使得预热区的长度在总内部长度的15%至35%之间,燃烧区的长度在总内部的65%至85%之间 长度。 预热区设计仅用于对炉内的充电材料进行预热。 氧化气体供应包含至少85体积%的氧气,并且用于来自预热区域的废气的至少一个出口连接到没有热交换器的大气。

    FINING MOLTEN MATERIAL USING REDUCED PRESSURE

    公开(公告)号:US20240166545A1

    公开(公告)日:2024-05-23

    申请号:US17990027

    申请日:2022-11-18

    摘要: A glass fining system, multi-stage vacuum housing, and method are disclosed. The glass fining system includes a multi-stage vacuum housing comprising a first melt receipt tank configured to receive molten material, where the first melt receipt tank is disposed in a first vacuum chamber; a first refining channel configured to flow the molten material from the first melt receipt tank through a second vacuum chamber; a second melt receipt tank configured to receive the molten material from the first refining channel, where the second melt receipt tank is disposed in a third vacuum chamber; and a second refining channel configured to flow the molten material from the second melt receipt tank and through a fourth vacuum chamber; and a glass melter coupled to the multi-stage vacuum housing.