首页> 外国专利> METHOD FOR CONTINUOUS GLASS MELTING UNDER CONTROLLED CONVECTION OF GLASS MELT AND GLASS MELTING FURNACE FOR MAKING THE SAME

METHOD FOR CONTINUOUS GLASS MELTING UNDER CONTROLLED CONVECTION OF GLASS MELT AND GLASS MELTING FURNACE FOR MAKING THE SAME

机译:在玻璃熔体的受控对流下连续进行玻璃熔化的方法和使玻璃熔窑相同的方法

摘要

Energy sources, such as industrial glass burners (11), heating electrodes (10) and other suitable heating energy sources operate on the molten glass melt (6) containing undissolved particles, especially glass sand and bubbles, in the longitudinal axis of the melting space, or in a direction parallel with this longitudinal axis, until creation of one or more longitudinal temperature barriers in the glass melt (6) and until the arising of the cross temperature gradient [K.m-1] which generates spiral-type flowing of the glass melt (6) with a rotary movement across the melting space, and in fact perpendicularly to the longitudinal axis of the melting part. This spiral-type flowing proceeds in the direction from the front wall (2) to the submerged cross refractory barrier (7) in the glass melt (6), or in the direction from the front wall (2) to the cross row (9) of the energy sources. The transversal temperature gradient [K.m-1] of each spiral-type flowing is always set as higher than longitudinal temperature gradient [K.m-1] between the front wall (2) and the submerged cross refractory barrier (7) in the glass melt (6), or between the front wall (2) and the cross row (9) of the energy sources, as a consequence of which it is possible to utilise 0.6 to 0.8 multiple of the total melting space. The ratio of the cross temperature gradient [K.m-1] to the longitudinal temperature gradient [K.m-1] is higher than 1 and lower than 30, preferably it is within the range from 5 to 20. Energy sources, such as heating electrodes (10) and/or industrial glass burners (11) in the melting space are arranged for creation of one or more longitudinal temperature barriers in the glass melt (6) and for generation of the spiral-type flowing of glass melt (6) with a rotary movement across the melting part, in fact perpendicularly to the longitudinal axis of the melting part, and for the setting of the cross temperature gradient [K.m-1] of the spiral-type flowing higher than the longitudinal temperature gradient [K.m-1].
机译:能源,例如工业玻璃燃烧器(11),加热电极(10)和其他合适的加热能源,在熔融空间的纵轴上对熔融玻璃熔体(6)进行操作,该熔融玻璃熔体(6)包含未溶解的颗粒,尤其是玻璃砂和气泡,或在平行于此纵轴的方向上,直到在玻璃熔体(6)中形成一个或多个纵向温度屏障,并且直到产生交叉温度梯度[Km -1 ]为止,玻璃熔体(6)呈螺旋状流动,并在熔体空间内旋转运动,并且实际上垂直于熔体部件的纵轴。这种螺旋形的流动沿从玻璃熔体(6)中的前壁(2)到浸没的交叉耐火材料屏障(7)的方向进行,或沿从前壁(2)到交叉行(9)的方向进行。 )的能源。每个螺旋型流动的横向温度梯度[Km -1 ]始终设置为高于前壁(2)之间的纵向温度梯度[Km -1 ]。以及在玻璃熔体(6)中或在能量源的前壁(2)和横排(9)之间的浸入式交叉耐火材料屏障(7),因此可以利用0.6到0.8总熔化空间的倍数。交叉温度梯度[Km -1 ]与纵向温度梯度[Km -1 ]之比大于1且小于30,优选在范围为5到20。设置能量源,例如熔化空间中的加热电极(10)和/或工业玻璃燃烧器(11),以在玻璃熔体(6)中创建一个或多个纵向温度屏障,并进行发电实际上以垂直于熔融部分的纵轴的旋转运动穿过熔融部分的方式旋转的玻璃熔体(6)的流动,并且用于设定交叉温度梯度[Km -1 < / Sup>]的螺旋型流动高于纵向温度梯度[Km -1 ]。

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