公开(公告)号：US08806899B2

公开(公告)日：2014-08-19

申请号：US13147277

申请日：2010-01-22

申请人： Matthias Lindig ,  Helmut Sorg ,  Alexander Sorg

发明人： Matthias Lindig ,  Helmut Sorg ,  Alexander Sorg

IPC分类号： C03B5/20 ,  C03B5/225 ,  C03B5/23

CPC分类号： C03B5/2257 ,  C03B5/04 ,  C03B5/20 ,  C03B5/23

摘要： A glass melting oven for producing a glass melt in a row arrangement, having a loading opening for raw glass materials, a melting region, a refining region, a constriction, a conditioning region and an overflow into a processing unit. To remove flaws from the melt that remain visible in the end product, a method includes the steps of a) arranging a refining bench between the melting region and the beginning of the refining region; b) arranging side burners and extraction openings for flue gases between the loading opening and the refining bench; c) delimiting the constriction at both ends by end walls that leave narrow flow cross-sections above the glass melt for flue gases; and d) cooling the glass melt inside the constriction. The glass melting oven is particularly suited for producing flat glass and panels for solar elements. The oxidants for the fuels may also be preheated.

摘要翻译： 一种用于生产玻璃熔体的玻璃熔融炉，其具有用于原料玻璃材料的加载开口，熔化区域，精炼区域，收缩部分，调节区域和溢流到处理单元中。 为了从最终产品中保持可见的熔体中除去缺陷，一种方法包括以下步骤：a）在熔化区域和精炼区域的开始之间布置精炼台; b）在装载开口和精炼台之间布置侧面燃烧器和用于烟气的提取开口; c）通过在玻璃熔体上方的烟道气留下窄流横截面的端壁限定两端的收缩; 和d）冷却收缩部内的玻璃熔体。 玻璃熔化炉特别适用于生产用于太阳能元件的平板玻璃和面板。 燃料的氧化剂也可以被预热。

公开(公告)号：US20120017643A1

公开(公告)日：2012-01-26

申请号：US13147277

申请日：2010-01-22

申请人： Matthias Lindig ,  Helmut Sorg ,  Alexander Sorg

发明人： Matthias Lindig ,  Helmut Sorg ,  Alexander Sorg

IPC分类号： C03B5/04 ,  C03B5/23 ,  C03B5/225

CPC分类号： C03B5/2257 ,  C03B5/04 ,  C03B5/20 ,  C03B5/23

摘要： A glass melting oven for producing a glass melt in a row arrangement, having a loading opening for raw glass materials, a melting region, a refining region, a constriction, a conditioning region and an overflow into a processing unit. To remove flaws from the melt that remain visible in the end product, a method includes the steps of a) arranging a refining bench between the melting region and the beginning of the refining region; b) arranging side burners and extraction openings for flue gases between the loading opening and the refining bench; c) delimiting the constriction at both ends by end walls that leave narrow flow cross-sections above the glass melt for flue gases; and d) cooling the glass melt inside the constriction. The glass melting oven is particularly suited for producing flat glass and panels for solar elements. The oxidants for the fuels may also be preheated.

摘要翻译： 一种用于生产玻璃熔体的玻璃熔融炉，其具有用于原料玻璃材料的加载开口，熔化区域，精炼区域，收缩部分，调节区域和溢流到处理单元中。 为了从最终产品中保持可见的熔体中除去裂纹，一种方法包括以下步骤：a）在熔化区域和精炼区域的开始之间布置精炼台; b）在装载开口和精炼台之间布置侧面燃烧器和用于烟气的提取开口; c）通过在玻璃熔体上方的烟道气留下窄流横截面的端壁限定两端的收缩; 和d）冷却收缩部内的玻璃熔体。 玻璃熔化炉特别适用于生产用于太阳能元件的平板玻璃和面板。 燃料的氧化剂也可以被预热。

公开(公告)号：US20130309622A1

公开(公告)日：2013-11-21

申请号：US13824755

申请日：2011-12-13

申请人： Matthias Lindig ,  Helmut Sorg

发明人： Matthias Lindig ,  Helmut Sorg

IPC分类号： F27D7/02

CPC分类号： F27D7/02 ,  C03B3/023 ,  F28C3/14 ,  F28D7/0058 ,  F28D2021/0045 ,  Y02P40/53

摘要： A device for preheating charging material for glass melting installations using its exhaust gases, having a vertical preheating shaft through which a heat exchanger extends conducting exhaust gases, the shaft upper end having a charging material opening, the lower end having a preheated charging material discharge device, the inlet of the heat exchanger connected to an exhaust gas supply line and the outlet connected to an exhaust gas outlet line. To recuperate a high portion of the exhaust gas heat, and to reduce environmental contamination and the suctioning of environmental air as false air, the exhaust gas supply line has an outlet line branch for drawing oft part of the hot gases and the outlet line is connected to a downwardly open sealing gas line in the region of the charging material above the heat exchanger exhaust gas passage for the hot gas emission into the charging material.

摘要翻译： 一种用于使用其废气预热用于玻璃熔化装置的充电材料的装置，具有垂直预热轴，热交换器通过该垂直预热轴延伸导电废气，所述轴上端具有充电材料开口，所述下端具有预热的充电材料放电装置 ，热交换器的入口连接到排气供应管线，并且出口连接到排气出口管路。 为了恢复废气热量的大部分，为了减少环境污染和作为假空气的环境空气的吸入，排气供给管线具有用于抽出一部分热气体的出口管路分支，并且出口管路连接 到热交换器废气通道上方的充电材料区域中的向下开口的密封气体管线，用于将热气体排放到充电材料中。

公开(公告)号：US5573569A

公开(公告)日：1996-11-12

申请号：US524165

申请日：1995-08-31

申请人： Helmut Sorg ,  Richard Sims

发明人： Helmut Sorg ,  Richard Sims

IPC分类号： C03B7/06 ,  C03B5/18 ,  C03B5/225 ,  C03B5/23

CPC分类号： C03B7/06 ,  Y02P40/57

摘要： A continuously flowing glass stream is conditioned and homogenized along a conditioning stretch, which extends from an entry side to at least one extraction point, and at the beginning of which there is a cooling zone, to which a homogenizing zone for the glass temperature is connected. This method is preferentially used for the manufacture of molded glass articles, such as containers and pressed articles. In order to achieve the necessary conditioning and homogenization, even at high throughputs, the glass stream in the cooling zone has a cross section with a depth/width ratio D/W of a maximum 0.6 or 0.5, or 0.4, or 0.3, or 0.2, whereby the maximum depth Dmax amounts toa) 300 or 250 or 200 mm when the cooling zone is situated in a working end or in a distribution channelb) 150 or 120 or 100 mm when the cooling zone is situated in a feeder or in a forehearthand, at least 30, or 40 or 50% of that amount of energy which corresponds to the necessary temperature reduction is removed from the glass bath per meter of flow path at the beginning of the cooling zone.

摘要翻译： 将连续流动的玻璃流沿着从进入侧延伸至至少一个提取点的调理拉伸条件进行调理和均化，并且其开始处具有冷却区，玻璃温度的均质化区域连接到该冷却区 。 该方法优选用于制造模制玻璃制品，例如容器和压制制品。 为了实现必要的调节和均质化，即使在高通量下，冷却区中的玻璃流具有深度/宽度比D / W最大为0.6或0.5，或0.4，或0.3或0.2的横截面 ，其中当冷却区位于工作端或分布通道b）中时，最大深度Dmax等于a）300或250或200mm，当冷却区位于进料器或在 在冷却区开始处，从每米流路的玻璃浴中除去对应于必要的温度降低的能量的至少30或40或50％。

公开(公告)号：US5002600A

公开(公告)日：1991-03-26

申请号：US440867

申请日：1989-11-22

申请人： Helmut Sorg ,  Matjaz Bucar

发明人： Helmut Sorg ,  Matjaz Bucar

IPC分类号： C03B7/14 ,  C03B7/02

CPC分类号： C03B7/02

摘要： A plurality of conduit segments contact on another which run vertically and transversely to the direction in which molten glass is channelled. Each segment includes at least one trough section and at least one cover section, an insulation of individual formed bodies, and an external casing. The segments are coupled together on support beams and may have removable insulation at joints to facilitate inspection.

摘要翻译： 多个导管段在另一个管道段上接触，其垂直且横向于熔融玻璃被引导的方向。 每个部分包括至少一个槽部分和至少一个盖部分，各个成形体的绝缘体和外部壳体。 这些段在支撑梁上联接在一起，并且可以在接头处具有可移除的绝缘体以便于检查。

公开(公告)号：US5536291A

公开(公告)日：1996-07-16

申请号：US290184

申请日：1994-08-15

申请人： Helmut Sorg ,  Helmut Pieper

发明人： Helmut Sorg ,  Helmut Pieper

IPC分类号： C03B5/04 ,  C03B5/20

CPC分类号： C03B5/04

摘要： In a furnace for melting glass, a preheating zone, a melting zone, a refining zone with a refining bank raised above the rest of the floor and an homogenizing zone, are arranged lengthwise behind one another between the charging end for the glass raw materials and a throat for the molten glass. The furnace chamber formed between two end walls is split up by dividing walls with the exception of flow paths for the glass and waste gases. The melting zone, the refining zone, several burners and the homogenizing zone have a common combustion chamber in the superstructure. A first flow path "L1" for the glass is defined between the inside face of the first end wall and the vertical center line (E) of the final dividing wall in front of the refining zone, and a second flow path "L2" is defined in the combustion chamber between the vertical center line (E) and the inside face of the second end wall. The ratio of the length "L2" to the total length ("L1"+"L2") is chosen to be at least 0.5, preferably at least 0.53. The lengths "L1" and "L2" are the horizontal components of the corresponding flow paths. The greater part of the heating energy is supplied to the glass melt in front of the refining bank in the melting zone, and the heating and melting energy for the raw materials is applied from above from the waste gases, and from below solely from the current in the glass melt which extends as far as the charging end. Therefore, the charging end of the melter does not require any electrical heating, at least during continuous operation.

摘要翻译： 在用于熔化玻璃的炉子中，在玻璃原料的充电端和玻璃原料的充电端之间纵向彼此纵向地布置预热区，熔化区，具有在地板的其余部分上方提升的精炼库的精炼区和均质区， 用于熔融玻璃的喉咙。 在两个端壁之间形成的炉室除了用于玻璃和废气的流动路径之外，被分隔壁分开。 熔化区，精炼区，几个燃烧器和均质区在上层建筑中具有共同的燃烧室。 玻璃的第一流路“L1”被限定在第一端壁的内表面和精炼区前面的最终分隔壁的垂直中心线（E）之间，第二流路“L2” 限定在燃烧室中的垂直中心线（E）和第二端壁的内表面之间。 长度“L2”与总长度（“L1”+“L2”）的比率选择为至少0.5，优选至少0.53。 长度“L1”和“L2”是相应流路的水平分量。 将大部分加热能量供应到熔融区内的精炼库前面的玻璃熔体，原料的加热和熔融能从上面从废气中施加，从下面仅仅从电流 在玻璃熔体中，其延伸至充电端。 因此，至少在连续操作期间，熔化器的充电端不需要任何电加热。

公开(公告)号：US5035735A

公开(公告)日：1991-07-30

申请号：US450346

申请日：1989-12-13

申请人： Helmut Pieper ,  Hartmut Zschocher ,  Helmut Sorg

发明人： Helmut Pieper ,  Hartmut Zschocher ,  Helmut Sorg

IPC分类号： B09B3/00 ,  C03B3/00 ,  C03B5/00 ,  C03B5/027 ,  C03B5/20 ,  C03B5/26 ,  C03B7/02 ,  C03C1/00 ,  G21F9/30

CPC分类号： C03B5/262 ,  B09B3/005 ,  B09B3/0066 ,  C03B3/00 ,  C03B5/005 ,  C03B5/027 ,  C03B7/02 ,  C03C1/00 ,  C03C1/002 ,  G21F9/305 ,  Y02P40/52

摘要： Process for vitrifying environmentally hazardous waste material in a glass melting furnace includes forming a batch including the waste material and no more than 30 weight percent additives including phonolite and SiO.sub.2 containing substances. A gall layer 2-5 cm thick including alkali salts or alkaline earth salts is produced on the molten glass, and batch is added so that a batch layer over 5 cm thick is formed on top of the gall layer. After the batch layer is formed, the molten glass is heated solely by electrodes, and the thickness of the batch layer is maintained to produce a steep enough temperature gradient therein so that the furnace atmosphere remains relatively cool, and substantially all of the condensable components which emerge from the molten glass condense in the batch layer.

摘要翻译： 在玻璃熔炉中对环境有害废料进行玻璃化的方法包括形成包含废料的批料和不超过30重量％的包括挥发岩和含SiO 2物质的添加剂。 在熔融玻璃上产生2-5厘米厚的包含碱金属盐或碱土金属盐的胆酸层，并加入批料，使得在胆汁层顶部形成5厘米厚的批料层。 在形成批料层之后，熔融玻璃仅由电极加热，并且保持间歇层的厚度以在其中产生足够陡峭的温度梯度，使得炉气氛保持相对冷却，并且基本上所有的可冷凝组分 从熔融玻璃中出现的凝聚在批料层中。

公开(公告)号：US4687504A

公开(公告)日：1987-08-18

申请号：US782404

申请日：1985-10-01

申请人： Helmut Pieper ,  Adolf Knauer ,  Helmut Sorg

发明人： Helmut Pieper ,  Adolf Knauer ,  Helmut Sorg

IPC分类号： C03B5/027 ,  C03B5/182 ,  C03B5/185 ,  C03B5/20

CPC分类号： C03B5/185 ,  C03B5/027 ,  C03B5/182

摘要： A glass melting furnace including a melting tank heated from above by burners and comprising a melting section as well as a refining and homogenizing section provided with electrodes for the supply of electrical energy; a dam which separates the melting section from the refining and homogenizing section and the upper edge of which is disposed below the surface of the (glass) melt bath; and an outlet for the glass disposed in the bottom portion of the refining and homogenizing section; wherein the bottom of the refining and homogenizing section is in a position deeper than the bottom of the melting section, and the electrodes are arranged in one or more planes (levels) of the refining section, the glass melting furnace being configured such that on the side of the refining section there is provided adjacent to the dam a bottom portion which is disposed at a level substantially above the bottom of the homogenizing section.

摘要翻译： 一种玻璃熔炉，包括由上述燃烧器加热并且包括熔化部分的熔化槽以及具有用于供应电能的电极的精炼和均质部分; 将熔融部分与精炼均化部分分离并且其上边缘设置在（玻璃）熔融浴表面下方的坝; 以及设置在精炼均化部的底部的玻璃的出口; 其特征在于，所述精制均化部的底部处于比所述熔融部的底部更深的位置，所述电极配置在所述精炼部的一个以上的平面（水平）上，所述玻璃熔融炉的配置为： 所述精炼部分的侧面设置在所述坝附近，所述底部部分设置在基本上在所述均匀化部分的底部的上方。

公开(公告)号：US6154481A

公开(公告)日：2000-11-28

申请号：US286741

申请日：1999-04-06

申请人： Helmut Sorg ,  Helmut Pieper

发明人： Helmut Sorg ,  Helmut Pieper

IPC分类号： C03B5/04 ,  C03B5/182 ,  C03B5/185 ,  C03B5/193 ,  C03B5/20 ,  C03B5/225 ,  C03B5/027

CPC分类号： C03B5/182 ,  C03B5/04 ,  C03B5/185 ,  C03B5/193 ,  C03B5/20 ,  C03B5/225

摘要： In a glass melting furnace, a radiation screen wall is installed between a melting area and a refining area with a refining bank. This radiation screen wall leaves a flow path above the melt surface of the glass bath for the return flow of at least part of the combustion gases from the refining area to the melting area. In order to suppress a return flow of already refined and very hot glass melt from the refining area into a melting area, but still allow the charging material to melt completely as early as possible, the furnace is operated to produce at least one upward current between the middle of the melting area and the front face of the refining bank in the glass melt. Within the glass melt and before the melt surface is reached, this upward current is divided into a first partial current which flows upstream into the melting area and a second partial current which flows downstream over the refining bank, whereby a return current of the glass melt from the refining area into the melting area is prevented by the second partial current flowing downstream. This upward current is achieved by the use of one or more of the following arrangements: a row of bubblers; a step projecting upwards from the furnace bottom; and/or at least two heating electrodes which are installed before the front face of the refining bank.

摘要翻译： 在玻璃熔炉中，在熔化区域和精炼区域之间安装有辐射屏蔽壁与精炼库。 该辐射屏蔽壁在玻璃浴的熔融表面之上留下流动路径，用于使至少部分燃烧气体从精炼区域返回到熔化区域。 为了抑制已经精炼和非常热的玻璃熔体从精炼区域到熔化区域的回流，但是仍然允许充电材料尽可能早地完全熔化，炉子被操作以产生至少一个向上的电流， 熔化区的中间和玻璃熔体中的精炼库的前面。 在玻璃熔体内并且在熔体表面达到之前，该向上的电流被分成在熔融区域上游流动的第一部分电流和在精炼库上游流动的第二部分电流，由此玻璃熔体的回流 从精炼区域进入熔化区域被第二部分电流流向下游。 该向上的电流通过使用以下一种或多种布置来实现：一排起泡器; 从炉底向上突出的台阶; 和/或至少两个加热电极，其安装在精炼库的前表面之前。

公开(公告)号：US5630860A

公开(公告)日：1997-05-20

申请号：US238245

申请日：1994-05-04

申请人： Helmut Sorg ,  Richard Sims

发明人： Helmut Sorg ,  Richard Sims

IPC分类号： C03B5/187 ,  C03B5/23 ,  C03B7/06 ,  C03B5/18

CPC分类号： C03B5/23 ,  C03B5/187 ,  C03B7/06 ,  Y02P40/57

摘要： A continuously flowing glass stream is conditioned and homogenized along a conditioning stretch, which extends from an entry side to at least one extraction point, and at the beginning of which there is a cooling zone, to which at least one homogenizing zone for the glass temperature is connected. In the working end or the distribution channel the temperature is reduced from the entry temperature T1 to an outlet temperature T2. In order to achieve the necessary conditioning and homogenization, even at high throughputs, the glass stream in the at least one cooling zone of the working end or distribution channel has a cross section with a depth/width ratio D/W of a maximum 0.6, or 0.5, or 0.4, or 0.3 or 0.2, whereby the maximum depth Dmax amounts to 300 or 250 or 200 mm, achieved by at least one bank raised from the bottom, and at least 50, or 60, or 70% of that amount of energy which corresponds to the temperature difference between T1 and T2 is removed from the glass bath along the total length of all the cooling zones.

摘要翻译： 将连续流动的玻璃流沿着从进入侧延伸至至少一个提取点的调理拉伸条件进行调理和均化，并且其开始处具有冷却区，至少一个用于玻璃温度的均化区 已连接。 在工作端或分配通道中，温度从入口温度T1降低到出口温度T2。 为了实现必要的调节和均化，即使在高通量下，工作端或分配通道的至少一个冷却区中的玻璃流具有最大0.6的深度/宽度比D / W的横截面， 或0.5或0.4或0.3或0.2，其中最大深度Dmax达到300或250或200mm，由至少一个从底部升起的堤岸达到，并且该量的至少50％，60％或70％ 对应于T1和T2之间的温度差的能量沿着所有冷却区的总长度从玻璃浴中除去。