WO2015034259A1 - 이질 유리 제거 장치 및 이를 포함하는 유리 제조 장치 - Google Patents
이질 유리 제거 장치 및 이를 포함하는 유리 제조 장치 Download PDFInfo
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- WO2015034259A1 WO2015034259A1 PCT/KR2014/008266 KR2014008266W WO2015034259A1 WO 2015034259 A1 WO2015034259 A1 WO 2015034259A1 KR 2014008266 W KR2014008266 W KR 2014008266W WO 2015034259 A1 WO2015034259 A1 WO 2015034259A1
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- WO
- WIPO (PCT)
- Prior art keywords
- glass
- gate
- molten glass
- outlet
- accommodated
- Prior art date
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Classifications
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- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B5/00—Melting in furnaces; Furnaces so far as specially adapted for glass manufacture
- C03B5/16—Special features of the melting process; Auxiliary means specially adapted for glass-melting furnaces
- C03B5/26—Outlets, e.g. drains, siphons; Overflows, e.g. for supplying the float tank, tweels
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- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B5/00—Melting in furnaces; Furnaces so far as specially adapted for glass manufacture
- C03B5/16—Special features of the melting process; Auxiliary means specially adapted for glass-melting furnaces
- C03B5/18—Stirring devices; Homogenisation
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B5/00—Melting in furnaces; Furnaces so far as specially adapted for glass manufacture
- C03B5/16—Special features of the melting process; Auxiliary means specially adapted for glass-melting furnaces
- C03B5/20—Bridges, shoes, throats, or other devices for withholding dirt, foam, or batch
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- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B17/00—Forming molten glass by flowing-out, pushing-out, extruding or drawing downwardly or laterally from forming slits or by overflowing over lips
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B5/00—Melting in furnaces; Furnaces so far as specially adapted for glass manufacture
- C03B5/16—Special features of the melting process; Auxiliary means specially adapted for glass-melting furnaces
- C03B5/225—Refining
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B5/00—Melting in furnaces; Furnaces so far as specially adapted for glass manufacture
- C03B5/16—Special features of the melting process; Auxiliary means specially adapted for glass-melting furnaces
- C03B5/24—Automatically regulating the melting process
- C03B5/245—Regulating the melt or batch level, depth or thickness
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B5/00—Melting in furnaces; Furnaces so far as specially adapted for glass manufacture
- C03B5/16—Special features of the melting process; Auxiliary means specially adapted for glass-melting furnaces
- C03B5/26—Outlets, e.g. drains, siphons; Overflows, e.g. for supplying the float tank, tweels
- C03B5/262—Drains, i.e. means to dump glass melt or remove unwanted materials
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- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B5/00—Melting in furnaces; Furnaces so far as specially adapted for glass manufacture
- C03B5/16—Special features of the melting process; Auxiliary means specially adapted for glass-melting furnaces
- C03B5/26—Outlets, e.g. drains, siphons; Overflows, e.g. for supplying the float tank, tweels
- C03B5/265—Overflows; Lips; Tweels
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B7/00—Distributors for the molten glass; Means for taking-off charges of molten glass; Producing the gob, e.g. controlling the gob shape, weight or delivery tact
- C03B7/01—Means for taking-off charges of molten glass
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B5/00—Melting in furnaces; Furnaces so far as specially adapted for glass manufacture
- C03B5/16—Special features of the melting process; Auxiliary means specially adapted for glass-melting furnaces
- C03B5/26—Outlets, e.g. drains, siphons; Overflows, e.g. for supplying the float tank, tweels
- C03B5/265—Overflows; Lips; Tweels
- C03B5/267—Overflows; Lips; Tweels specially adapted for supplying the float tank
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P40/00—Technologies relating to the processing of minerals
- Y02P40/50—Glass production, e.g. reusing waste heat during processing or shaping
- Y02P40/57—Improving the yield, e-g- reduction of reject rates
Definitions
- the present invention relates to a glass manufacturing technique, and more particularly, to a technique capable of effectively and stably removing foreign glass located on the upper surface of the molten glass when the molten glass is supplied from the melting furnace to the molding furnace.
- Glass is produced in various forms, of which the representative form is flat glass.
- Flat glass is used in many different fields, such as window glass, window screens of vehicles, mirrors, and the like, and such flat glass can be manufactured in various ways.
- the glass may be manufactured through a melting step, a stirring step, a stabilizing step, a forming step, a slow cooling step, and the like.
- the melting step is a step of melting (dissolving) the glass raw material to make a molten glass, and may be performed in a melting furnace made of refractory brick or the like.
- a burner is usually used to control the temperature of the molten glass, which may cause a large amount of gas on the upper portion of the molten glass (glass).
- the upper surface of the molten glass in contact with such a gas may react with the gas or volatilize some components having high volatility, thereby deteriorating its properties or generating a heterogeneous glass containing foreign matter.
- the quality of the glass produced may be greatly degraded, so the foreign glass existing on the surface of the molten glass needs to be removed reliably.
- the flow rate overflowed in the overflow zone may be more or less than the proper flow rate. If the flow rate that overflows in the overflow zone is greater than the proper flow rate, the glass manufacturing cost and time can be increased because not only the foreign glass but also the normal molten glass can be excessively removed. On the contrary, when the flow rate overflowed in the overflow zone is less than the proper flow rate, since the foreign glass present on the surface is not sufficiently removed, there is a problem that the quality and production yield of the produced glass may be greatly reduced.
- the present invention has been made to solve the above problems, and an object thereof is to provide an apparatus capable of effectively removing foreign glass present on the upper surface of the molten glass, and a melting furnace and a glass manufacturing apparatus including the same. .
- the inlet and the outlet is formed to receive the molten glass introduced through the inlet, the received molten glass flows out through the outlet, A reservoir having an outlet formed at an upper end thereof such that the molten glass overflows; A first gate provided at an outlet side of the accommodation tank to control a flow rate of the molten glass flowing out through the outlet by adjusting an open area; And a second gate provided at an inlet side of the receiving tank rather than the outlet to adjust the level of the molten glass accommodated in the receiving tank at a portion where the outlet is formed.
- the second gate maintains a constant level of the molten glass accommodated in the storage tank at a portion where the discharge port is formed.
- the heterogeneous glass removing apparatus further includes a water level measuring unit for measuring the level of the molten glass accommodated in the receiving tank at the portion where the outlet is formed.
- the second gate is configured to be movable in the vertical direction, and increases the open area when moving from the bottom to the upper direction.
- the second gate is configured such that the horizontal distance to the discharge port is at least twice the depth contained in the molten glass at the side where the discharge port is located.
- the second gate is configured such that the depth contained in the molten glass at the side where the outlet is located is 10% to 50% of the depth of the molten glass accommodated in the receiving tank at the portion where the outlet is formed.
- the second gate may have a bottom edge rounded.
- the second gate is formed of a refractory material.
- At least a portion of the second gate is coated with platinum.
- the melting furnace according to the present invention for achieving the above object includes a heterogeneous glass removing apparatus according to the present invention.
- the glass manufacturing apparatus which concerns on this invention for achieving the said objective includes the heterogeneous glass removal apparatus which concerns on this invention.
- the foreign glass present on the upper surface of the molten glass molten in the melting furnace can be effectively removed.
- the level of the overflow zone in which the molten glass overflows can be kept constant.
- the level of the overflow zone can be kept constant. Therefore, according to the present invention, the foreign glass present on the upper surface of the molten glass can be stably removed by maintaining the flow rate that overflows.
- the foreign glass is effectively and stably removed from the molten glass flowing into the forming furnace or the like, so that the quality of the glass can be maintained at high quality and the production yield can also be improved.
- FIG. 1 is a perspective view schematically showing the configuration of a foreign glass removing apparatus according to an embodiment of the present invention.
- FIG. 2 is a cross-sectional view taken along line CC ′ in FIG. 1.
- FIG 3 is a perspective view schematically showing the configuration of a second gate according to an embodiment of the present invention.
- FIG. 1 is a perspective view schematically showing the configuration of a foreign glass removing apparatus according to an embodiment of the present invention.
- the heterogeneous glass removing apparatus includes a receiving tank 100, a first gate 200, and a second gate 300.
- the accommodation tank 100 has a space for accommodating the liquid and accommodates the molten glass in such a space.
- the receiving tank 100 is formed with an inlet 110 and an outlet 120 to allow molten glass to enter the accommodation space through the inlet 110, and the molten glass accommodated in the accommodation space through the outlet 120. Allow spills.
- the storage tank 100 accommodates high temperature molten glass, it may be made of a refractory material such as a fire brick.
- the receiving tank 100 may be included in a melting furnace as a component of a melting furnace for melting glass raw materials to produce molten glass, or may be positioned at a rear end of the melting furnace to supply molten glass to a forming furnace such as a float bath.
- the receiving tank 100 the overflow zone may be formed so that a portion of the received molten glass overflows.
- the receiving tank 100 may be formed with one or more outlets 130 on the top.
- two outlets 130 may be installed on the upper side of the receiving tank 100 to allow the molten glass of the upper surface to overflow and be discharged as indicated by arrow a2. have.
- the first gate 200 is provided at the outlet 120 side of the receiving tank 100 so as to be opened and closed.
- the first gate 200 may adjust the flow rate of the molten glass flowing out through the outlet 120 of the receiving tank 100 by adjusting the open area.
- the first gate 200 may be configured to move in the vertical direction, as indicated by b1 in FIG. 1.
- the first gate 200 may adjust the flow rate of the molten glass flowing out in the a1 direction through the outlet 120 by adjusting the distance between the lower end portion and the bottom surface of the accommodation tank 100. For example, when the first gate 200 moves in the upward direction, the flow rate of the molten glass flowing out through the outlet 120 may increase, and when the first gate 200 moves in the downward direction, The flow rate of the molten glass flowing out through the outlet 120 may be reduced.
- the first gate 200 may adjust the open area by measuring the flow rate of the molten glass flowing out through the outlet 120. For example, if the flow rate of the molten glass flowing out through the outlet 120 is greater than the reference flow rate, the open area is reduced. If the flow rate of the molten glass flowing out through the outlet 120 is less than the reference flow rate, the open area is increased. You can.
- the second gate 300 may be provided at the inlet 110 side of the receiving tank 100 based on the outlet 130. That is, referring to FIG. 1, the second gate 300 is provided on the left side of the outlet 130. Therefore, in the heterogeneous glass removing apparatus according to the present invention, the first gate 200 and the second gate 300 are positioned at both sides of the outlet 130. In other words, in the heterogeneous glass removing apparatus according to the present invention, since the outlet 130 is located between the first gate 200 and the second gate 300, the overflow zone is the first gate 200 and the second gate. It may be referred to as a portion located between the 300.
- the second gate 300 may be configured to be opened and closed like the first gate 200.
- the second gate 300 may adjust the level of the molten glass accommodated in the receiving tank 100 at the portion where the outlet 130 is located by adjusting the open area.
- the level control configuration of the second gate 300 will be described in more detail with reference to FIG. 2.
- FIG. 2 is a cross-sectional view taken along line CC ′ in FIG. 1.
- the second gate 300 may be configured to be movable in the vertical direction, as indicated by the arrow b2.
- the vertical movement of the second gate 300 may change the open area by the second gate 300, thereby changing the flow rate of the molten glass flowing through the second gate 300. .
- the water level of the portion where the outlet 130 is formed in the receiving tank 100 may be changed.
- the second gate 300 when the water level (depth) of the molten glass in the portion where the outlet 130 through which the molten glass overflows, that is, the overflow zone, is H1, the second gate 300 is formed. Moves to the upper direction and the open area increases, H1 may increase relatively. On the other hand, when the second gate 300 moves downward to decrease the open area, H1 may be relatively reduced. As such, according to the surface glass removing apparatus of the present invention, the level of the molten glass accommodated in the receiving tank 100 through the second gate 300 can be adjusted.
- the second gate 300 is configured to maintain a constant level of the molten glass accommodated in the receiving tank 100 in the portion where the discharge port 130 is formed. That is, the second gate 300 may adjust the open area so that H1 is kept constant in FIG. 2.
- keeping the level of the molten glass constant may mean that the level of the molten glass is maintained within a constant value or a constant range.
- the level of the molten glass can be kept constant at the portion where the outlet 130 is formed, the amount overflowed through the outlet 130 is constant Can be maintained. Therefore, in this case, the foreign glass present on the upper surface side of the molten glass can be constantly removed, and it is possible to prevent the problem that the foreign glass is removed less or the glass in the normal state is excessively removed.
- the surface glass removing apparatus may further comprise a water level measuring unit.
- the water level measuring unit measures the water level of the molten glass accommodated in the storage tank 100 at the portion where the discharge port 130 is formed.
- the water level measuring unit may measure the distance of H1 in FIG. 2.
- information about the measured water level may be transmitted to the second gate 300 and used to control the operation of the second gate 300.
- the second gate 300 moves upward to increase the open area, so that the portion where the outlet 130 is formed, that is, overflows.
- the level of the molten glass accommodated in the receiving tank 100 in the zone may be raised.
- the second gate 300, the horizontal distance to the outlet 130 is preferably at least two times the depth contained in the molten glass in the side where the outlet 130 is located.
- L1 and H2 should have the following relationship.
- the heterogeneous glass located on the surface of the front side (left side of FIG. 2) of the second gate 300 it is possible to ensure sufficient length for the heterogeneous glass located on the surface of the front side (left side of FIG. 2) of the second gate 300 to pass back to the surface after passing through the second gate 300. have. Therefore, after the heterogeneous glass positioned at the front end side of the second gate 300 passes through the second gate 300, it does not rise to the surface in the process of moving in the direction in which the discharge port 130 is formed (right direction in FIG. 2). As a result, it may be prevented from overflowing to the outlet 130.
- the second gate 300 may include a depth of the molten glass accommodated in the receiving tank 100 at a portion where the outlet 130 is formed by a depth contained in the molten glass at the side where the outlet 130 is located. It is good that it is% to 50%.
- the depth of the second gate 300 contained in the molten glass at the side where the outlet 130 is located is called H2, and the receiving tank 100 is formed at the portion where the outlet 130 is formed.
- H1 and H2 should have the following relationship.
- the flow rate of the molten glass passing through the second gate 300 is lowered to a predetermined level or less to minimize the generation of vortex, and the heterogeneous glass passing through the second gate 300 smoothly back to the surface of the molten glass. By floating, the foreign glass can be surely overflowed and removed.
- the second gate 300 may be formed such that a lower edge thereof is rounded.
- FIG. 3 is a perspective view schematically showing the configuration of the second gate 300 according to an embodiment of the present invention.
- the second gate 300 may be configured in a plate shape, and may be configured to be rounded so that the edge of the lower end thereof is curved. That is, as shown by a portion D in FIG. 3, the second gate 300 may be formed to be rounded so that the shape of the lower end viewed from the front becomes semi-circular. According to this embodiment, the molten glass flowing through the second gate 300 is made smoothly, it is possible to minimize the generation of vortex.
- the present invention is not necessarily limited to this form, and the shape of the second gate 300 may be variously implemented.
- the second gate 300 may be formed of a refractory material. Since the second gate 300 is in contact with the hot molten glass, the second gate 300 may be formed of a refractory material that can withstand high temperatures.
- the second gate 300 may be coated with at least a portion of a surface of a material that does not react with the hot molten glass.
- the second gate 300 may be coated with a platinum that is chemically stable with respect to high temperature molten glass.
- the heterogeneous glass removing apparatus can be applied to a glass melting furnace for melting a glass raw material and supplying molten glass to a forming furnace such as a float bath. That is, the glass melting furnace which concerns on this invention can contain the heterogeneous glass removal apparatus mentioned above. At this time, the bath for receiving the molten glass in the melting furnace may function as the receiving tank 100 of the heterogeneous glass removing device.
- the glass manufacturing apparatus which concerns on this invention can contain the heterogeneous glass removal apparatus mentioned above.
- the glass manufacturing apparatus which concerns on this invention can contain the heterogeneous glass removal apparatus mentioned above in a melting furnace.
- the glass manufacturing apparatus according to the present invention may further include a molding furnace and a slow cooling furnace.
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Glass Melting And Manufacturing (AREA)
- Glass Compositions (AREA)
- Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
Abstract
Description
Claims (11)
- 입구 및 출구가 형성되어 상기 입구를 통해 유입된 용융 유리를 수용하고, 상기 수용된 용융 유리를 상기 출구를 통해 유출시키며, 상기 수용된 용융 유리가 오버플로우되도록 상단에 배출구가 형성된 수용조;상기 수용조의 출구 측에 구비되어 개방 면적을 조절함으로써 상기 출구를 통해 유출되는 용융 유리의 유량을 조절하는 제1 게이트; 및상기 배출구보다 수용조의 입구 측에 구비되어 상기 배출구가 형성된 부분에서 상기 수용조에 수용된 용융 유리의 수위를 조절하는 제2 게이트를 포함하는 것을 특징으로 하는 이질 유리 제거 장치.
- 제1항에 있어서,상기 제2 게이트는, 상기 배출구가 형성된 부분에서 상기 수용조에 수용된 용융 유리의 수위를 일정하게 유지하는 것을 특징으로 하는 이질 유리 제거 장치.
- 제1항에 있어서,상기 배출구가 형성된 부분에서 상기 수용조에 수용된 용융 유리의 수위를 측정하는 수위 측정 유닛을 더 포함하는 것을 특징으로 하는 이질 유리 제거 장치.
- 제1항에 있어서,상기 제2 게이트는, 상하 방향으로 이동 가능하게 구성되고, 하부에서 상부 방향으로 이동할 때, 개방 면적이 증가하는 것을 특징으로 하는 이질 유리 제거 장치.
- 제1항에 있어서,상기 제2 게이트는, 배출구까지의 수평 방향 거리가 상기 배출구가 위치하는 측면에서 상기 용융 유리에 담겨진 깊이의 2배 이상이 되는 것을 특징으로 하는 이질 유리 제거 장치.
- 제1항에 있어서,상기 제2 게이트는, 상기 배출구가 위치하는 측면에서 상기 용융 유리에 담겨진 깊이가 상기 배출구가 형성된 부분에서 상기 수용조에 수용된 용융 유리의 깊이의 10% 내지 50%인 것을 특징으로 하는 이질 유리 제거 장치.
- 제1항에 있어서,상기 제2 게이트는, 하단 모서리가 라운딩지게 형성된 것을 특징으로 하는 이질 유리 제거 장치.
- 제1항에 있어서,상기 제2 게이트는, 내화물 재질로 형성된 것을 특징으로 하는 이질 유리 제거 장치.
- 제1항에 있어서,상기 제2 게이트는, 백금으로 표면 코팅된 것을 특징으로 하는 이질 유리 제거 장치.
- 제1항 내지 제9항 중 어느 한 항에 따른 이질 유리 제거 장치를 포함하는 유리 용융로.
- 제1항 내지 제9항 중 어느 한 항에 따른 이질 유리 제거 장치를 포함하는 유리 제조 장치.
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2016519465A JP6175710B2 (ja) | 2013-09-03 | 2014-09-03 | 異質ガラス除去装置及びそれを含むガラス製造装置 |
US14/426,909 US9862631B2 (en) | 2013-09-03 | 2014-09-03 | Apparatus for eliminating heterogeneous glass and glass manufacturing apparatus comprising the same |
EP14841662.1A EP2949631B1 (en) | 2013-09-03 | 2014-09-03 | Heterogeneous glass removing apparatus and glass manufacturing apparatus comprising the same |
CN201480019771.3A CN105102382B (zh) | 2013-09-03 | 2014-09-03 | 用于消除异质玻璃的装置以及包含所述装置的玻璃制造装置 |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
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KR1020130105602A KR101583372B1 (ko) | 2013-09-03 | 2013-09-03 | 이질 유리 제거 장치 및 이를 포함하는 유리 제조 장치 |
KR10-2013-0105602 | 2013-09-03 |
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WO2015034259A1 true WO2015034259A1 (ko) | 2015-03-12 |
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PCT/KR2014/008266 WO2015034259A1 (ko) | 2013-09-03 | 2014-09-03 | 이질 유리 제거 장치 및 이를 포함하는 유리 제조 장치 |
Country Status (6)
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US (1) | US9862631B2 (ko) |
EP (1) | EP2949631B1 (ko) |
JP (1) | JP6175710B2 (ko) |
KR (1) | KR101583372B1 (ko) |
CN (1) | CN105102382B (ko) |
WO (1) | WO2015034259A1 (ko) |
Families Citing this family (5)
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JP6943136B2 (ja) * | 2017-10-24 | 2021-09-29 | Agc株式会社 | ガラス溶解炉、及びガラス物品の製造方法 |
CN108585446B (zh) * | 2018-07-03 | 2023-10-13 | 海南海控特玻科技有限公司 | 一种用于光电倍增管玻璃的溢流装置 |
CN112119043B (zh) * | 2018-07-04 | 2023-04-14 | 日本电气硝子株式会社 | 玻璃物品的制造方法以及制造装置 |
CN113603337B (zh) * | 2021-08-06 | 2023-03-17 | 中国建材国际工程集团有限公司 | 一种光伏压延玻璃熔窑及其溢流口结构 |
CN115265868B (zh) * | 2022-09-29 | 2022-12-16 | 江苏延陵玻璃有限公司 | 一种异质真空玻璃表面应力检测装置 |
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- 2014-09-03 JP JP2016519465A patent/JP6175710B2/ja active Active
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Also Published As
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CN105102382A (zh) | 2015-11-25 |
KR101583372B1 (ko) | 2016-01-07 |
EP2949631A4 (en) | 2016-10-26 |
EP2949631B1 (en) | 2017-11-15 |
US20160023937A1 (en) | 2016-01-28 |
US9862631B2 (en) | 2018-01-09 |
KR20150026568A (ko) | 2015-03-11 |
CN105102382B (zh) | 2018-06-22 |
EP2949631A1 (en) | 2015-12-02 |
JP6175710B2 (ja) | 2017-08-09 |
JP2016521673A (ja) | 2016-07-25 |
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