CN105271635A - Optical-glass continuous-melting production line automatic charging technology and apparatus - Google Patents
Optical-glass continuous-melting production line automatic charging technology and apparatus Download PDFInfo
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Abstract
本发明的名称为一种光学玻璃连熔生产线自动加料工艺及装置。属于光学玻璃连熔技术领域。它主要是提供一种把熔制光学玻璃的配合料经连续烘干除水后,由陶瓷螺旋推进器连续加入玻璃熔炉的自动加料工艺及装置。其主要特征是:包括由储料仓、烘干炉和网带传输机构构成的加料烘干装置及陶瓷螺旋加料机;将原料平铺到烘干炉内的输送网带上烘干后,由螺旋片匀速将原料推至熔炉的铂金加料口进入融化池。本发明将光学玻璃连熔生产线上加料工艺中的烘干除水环节与漏注加料环节进行整合,达到自动加料的目的,同时减少了融化池温度的波动和易挥发物质的挥发,避免了加料环节的扬尘,提高产品品质。
The name of the present invention is an automatic feeding process and device for an optical glass continuous melting production line. The invention belongs to the technical field of continuous melting of optical glass. It mainly provides an automatic feeding process and device for continuously drying and dewatering batch materials for melting optical glass, and then continuously feeding them into a glass melting furnace through a ceramic screw propeller. Its main features are: including a feeding and drying device composed of a storage bin, a drying furnace and a mesh belt transmission mechanism, and a ceramic screw feeder; The spiral blade pushes the raw material to the platinum feeding port of the furnace at a constant speed and enters the melting pool. The invention integrates the drying and dewatering link and the missing injection feeding link in the feeding process on the optical glass continuous melting production line to achieve the purpose of automatic feeding, and at the same time reduces the fluctuation of the melting pool temperature and the volatilization of volatile substances, and avoids feeding Link dust, improve product quality.
Description
技术领域 technical field
本发明属于光学玻璃连熔技术领域。具体涉及一种把熔制光学玻璃的配合料经连续烘干除水后,由陶瓷螺旋推进器连续加入玻璃熔炉的自动加料工艺及装置。 The invention belongs to the technical field of optical glass continuous melting. Specifically, it relates to an automatic feeding process and device for continuously adding batch materials for melting optical glass into a glass melting furnace through a ceramic screw propeller after continuous drying and dehydration.
背景技术 Background technique
目前在光学玻璃连熔生产线上,大部分都实现了自动加料。自动加料工艺涉及到的加料方式主要包括定时定量、定时不定量、定量不定时等,这几种方式都属于间断投入式,这样会导致融化池玻璃液位有波动,对产品品质有一定影响;而匀速连续投料方式可以保持稳定的液位,但因玻璃熔炉温度很高,采用常规材料无法建立持续加料通道,因此很少采用连续加料方式。 At present, most of the optical glass continuous melting production lines have realized automatic feeding. The feeding methods involved in the automatic feeding process mainly include timing and quantitative, timing and non-quantitative, and quantitative and non-timing, etc. These methods are all intermittent input, which will cause fluctuations in the glass liquid level in the melting pool and have a certain impact on product quality; The constant-speed continuous feeding method can maintain a stable liquid level, but because the temperature of the glass melting furnace is very high, it is impossible to establish a continuous feeding channel with conventional materials, so the continuous feeding method is rarely used.
在光学玻璃研发过程中,为了使光学玻璃达到需要的使用要求,使得该类光学玻璃在熔制过程中,其组分含有易挥发物质(这些物质基本上都是有毒有害气体),且原料在空气中易吸潮产生结晶水而影响熔炼工艺稳定,需要把原料进行烘干后,并在熔炉融化池密封条件下投入熔炉来解决这两个问题。 In the research and development process of optical glass, in order to make the optical glass meet the required use requirements, during the melting process of this type of optical glass, its components contain volatile substances (these substances are basically poisonous and harmful gases), and the raw materials are in the It is easy to absorb moisture in the air to produce crystal water and affect the stability of the smelting process. It is necessary to dry the raw materials and put them into the furnace under the sealed condition of the melting pool of the furnace to solve these two problems.
因此,研究一种解决以上问题的既清洁环保、又保证产品品质的自动加料工艺具有较好的现实价值。 Therefore, it is of good practical value to study an automatic feeding process that solves the above problems, is clean and environmentally friendly, and ensures product quality.
发明内容 Contents of the invention
本发明的目的就是解决一种把熔制光学玻璃的配合料经连续烘干除水后,由陶瓷螺旋推进器连续加入玻璃熔炉的自动加料工艺及装置,以提高光学玻璃连熔技术的自动化水平。 The purpose of the present invention is to solve an automatic feeding process and device for continuously adding the batch materials for melting optical glass into the glass melting furnace by a ceramic screw propeller after continuous drying and dehydration, so as to improve the automation level of the continuous melting technology of optical glass .
本发明自动加料工艺的技术解决方案是:一种光学玻璃连熔生产线自动加料工艺,其特征在于包括以下工艺步骤: The technical solution of the automatic feeding process of the present invention is: an automatic feeding process of an optical glass continuous melting production line, which is characterized in that it includes the following process steps:
⑴由人工将原料或配合料注入储料仓; (1) Manually inject raw materials or batch materials into the storage bin;
⑵原料或配合料经储料仓的出口漏出平铺到烘干炉的输送网带上,烘干炉内温度为160~260℃;原料或配合料在烘干炉内烘烤7~10小时; ⑵Raw materials or batch materials leak out through the outlet of the storage bin and spread them on the conveyor mesh belt of the drying furnace. ;
⑶烘干后的原料或配合料从输送网带尾端落入陶瓷螺旋加料机的导料仓;陶瓷螺旋加料机由导料仓、第二减速机、联轴器、堵板、垫片、出料锥管、套管和螺旋推进片构成,堵板固定在套管的开口端,螺旋推进片位于套管内,其两端分别经垫片安装在堵板及套管的封闭端上,螺旋推进片的一端经联轴器与第二减速机连接,套管一端上部的进料口与导料仓的出仓端口连接,另一端下部的出料口与出料锥管连接,出料锥管下端为锥形管口;烘干后的原料或配合料从导料仓进入套管后,由螺旋推进片转动推至出料锥管出口,之后经熔炉铂金加料口进入融化池。 (3) The dried raw materials or batch materials fall from the end of the conveying mesh belt into the guide bin of the ceramic screw feeder; the ceramic screw feeder consists of a guide bin, a second reducer, a coupling, a blocking plate, a gasket, The discharge cone is composed of a casing, a casing and a screw propulsion piece. The blocking plate is fixed at the opening end of the casing, and the screw propulsion piece is located in the casing. One end of the propulsion plate is connected to the second reducer through a coupling, the upper part of the casing is connected to the outlet port of the guide bin, the lower part of the other end is connected to the discharge cone, and the discharge cone The lower end of the tube is a conical nozzle; after the dried raw materials or batch materials enter the casing from the material guide bin, they are pushed by the screw propeller to the outlet of the discharge cone tube, and then enter the melting pool through the platinum feeding port of the furnace.
本发明自动加料装置的技术解决方案是:一种光学玻璃连熔生产线自动加料装置,其特征在于:包括加料烘干装置和陶瓷螺旋加料机;加料烘干装置包括储料仓、烘干炉和网带传输机构;网带传输机构包括位于烘干炉内的输送网带和传输轮,位于烘干炉外的第一减速机,第一减速机经皮带与传输轮连接;储料仓的出料口穿过烘干炉后位于输送网带的上方;陶瓷螺旋加料机由导料仓、第二减速机、联轴器、堵板、垫片、出料锥管、套管和螺旋推进片构成;堵板固定在套管的开口端,螺旋推进片位于套管内,其两端分别经垫片安装在堵板及套管的封闭端上;螺旋推进片的一端经联轴器与第二减速机连接,套管一端上部的进料口与导料仓的出仓端口连接,另一端下部的出料口与出料锥管连接;出料锥管下端为锥形管口;输送网带的尾端位于导料仓的上方。 The technical solution of the automatic feeding device of the present invention is: an automatic feeding device for an optical glass continuous melting production line, which is characterized in that it includes a feeding drying device and a ceramic screw feeding machine; the feeding and drying device includes a storage bin, a drying furnace and Mesh belt transmission mechanism; the mesh belt transmission mechanism includes a conveying mesh belt and a transmission wheel located in the drying furnace, a first reducer located outside the drying furnace, and the first reducer is connected to the transmission wheel through a belt; the outlet of the storage bin The material port is located above the conveyor belt after passing through the drying furnace; the ceramic screw feeder consists of a material guide bin, a second reducer, a coupling, a blocking plate, a gasket, a discharge cone, a sleeve and a screw propeller Composition; the blocking plate is fixed at the opening end of the casing, the screw propulsion piece is located in the casing, and its two ends are respectively installed on the closed end of the blocking plate and the casing through the gasket; one end of the screw propulsion piece is connected to the second through the coupling The reducer is connected, the upper feed port at one end of the casing is connected to the discharge port of the guide bin, and the discharge port at the lower end of the other end is connected to the discharge cone; the lower end of the discharge cone is a tapered nozzle; the conveyor belt The tail end is located above the guide bin.
本发明自动加料装置的技术解决方案中所述的螺旋推进片位于套管封闭端最里侧的一圈螺旋片与其它螺旋片旋转方向相反,且位于套管的出料口处。 The spiral propulsion piece described in the technical solution of the automatic feeding device of the present invention is located at the innermost side of the closed end of the casing, and the rotation direction of the other spiral pieces is opposite to that of the other spiral pieces, and is located at the discharge port of the casing.
本发明自动加料装置的技术解决方案中所述的出料锥管上部与套管的出料口为锥套连接或法兰连接。 In the technical solution of the automatic feeding device of the present invention, the upper part of the discharge conical pipe and the discharge port of the casing are connected by a taper sleeve or a flange.
本发明自动加料装置的技术解决方案中所述的套管、螺旋推进片、垫片和堵板均为由纯度在99.99%以上的氧化铝烧制而成的陶瓷套管、陶瓷螺旋推进片、陶瓷垫片和陶瓷堵板。 The sleeve pipe, screw propeller, gasket and blocking plate described in the technical solution of the automatic feeding device of the present invention are all ceramic sleeves, ceramic spiral propellers, Ceramic gaskets and ceramic blocking plates.
本发明自动加料装置的技术解决方案中所述的储料仓的出口为矩形扁口。 The outlet of the storage bin described in the technical solution of the automatic feeding device of the present invention is a rectangular flat mouth.
本发明由于采用由储料仓、烘干炉和网带传输机构构成加料烘干装置,由导料仓、减速机、联轴器、堵板、垫片、出料锥管、套管和螺旋推进片构成的陶瓷螺旋加料机,因而原料(配合料)先由人工注入储料仓,从储料仓的出口漏出平铺到烘干炉的输送网带上,调节储料仓的出口下端距离网带的高度即可控制所敷设原料的厚度,储料仓的出口的长度可作为原料敷设在网带上的宽度,当烘干炉的网带在第一减速机驱动下匀速前进时,可将原料均匀、平稳的输送至陶瓷螺旋加料机上方的导料仓,此时烘干炉内的温度控制在160~260℃,原料视敷设厚度及加料需求量,通过控制第一减速机的速度使原料在烘干炉内烘烤7~10小时,以充分除去原料中的水分,原料从导料仓进入陶瓷螺旋加料机,螺旋片的转动将原料均匀推至熔炉加料口进入融化池。本发明将光学玻璃连熔生产线上加料工艺中的烘干除水环节与漏注加料环节进行整合,达到自动加料的目的。原料连续烘干除水、连续加入熔炉保证融化池液位稳定,陶瓷漏料口与铂金加料口锥形密封作用,减少了融化池温度的波动和易挥发物质的挥发,避免了加料环节的扬尘。本发明主要适用于光学玻璃连熔生产线的自动加料工艺。 The present invention adopts the feeding and drying device composed of a storage bin, a drying furnace and a mesh belt transmission mechanism; The ceramic screw feeder composed of pusher pieces, so the raw materials (batch materials) are first manually injected into the storage bin, leaked from the outlet of the storage bin and spread on the conveyor belt of the drying furnace, and the distance between the lower end of the outlet of the storage bin is adjusted The height of the mesh belt can control the thickness of the laid raw material. The length of the outlet of the storage bin can be used as the width of the raw material laid on the mesh belt. When the mesh belt of the drying furnace advances at a constant speed driven by the first reducer, it can The raw materials are evenly and stably transported to the material guide bin above the ceramic screw feeder. At this time, the temperature in the drying furnace is controlled at 160-260°C. The raw materials depend on the laying thickness and the feeding demand, by controlling the speed of the first reducer The raw materials are baked in the drying furnace for 7 to 10 hours to fully remove the moisture in the raw materials. The raw materials enter the ceramic screw feeder from the material guide bin, and the rotation of the spiral blades pushes the raw materials evenly to the furnace feeding port and enters the melting pool. The invention integrates the drying and water removal link and the missing injection feeding link in the feeding process on the optical glass continuous melting production line to achieve the purpose of automatic feeding. The raw materials are continuously dried to remove water and continuously added to the furnace to ensure the stability of the liquid level in the melting pool. The conical sealing effect between the ceramic leakage port and the platinum feeding port reduces the temperature fluctuation of the melting pool and the volatilization of volatile substances, and avoids dust in the feeding process. . The invention is mainly applicable to the automatic feeding process of the optical glass continuous melting production line.
附图说明 Description of drawings
图1是本发明光学玻璃连熔生产线自动加料装置的示意图。 Fig. 1 is a schematic diagram of the automatic feeding device of the optical glass continuous melting production line of the present invention.
图2是本发明陶瓷螺旋加料机的示意图。 Fig. 2 is a schematic diagram of the ceramic screw feeder of the present invention.
图中:1-储料仓;2-烘干炉;3-导料仓;4-陶瓷螺旋加料机;5-铂金加料口;41-螺旋推进片;42-套管;43-出料锥管;44-垫片;45-堵板;46-联轴器;47-第二减速机。 In the figure: 1-storage bin; 2-drying furnace; 3-guide bin; 4-ceramic screw feeder; 5-platinum feeding port; 41-screw propeller; Tube; 44-gasket; 45-blocking plate; 46-coupling; 47-second reducer.
具体实施方式 detailed description
如图1、图2所示,本发明自动加料装置包括加料烘干装置和陶瓷螺旋加料机4。加料烘干装置包括储料仓1、烘干炉2和网带传输机构,其中,网带传输机构包括位于烘干炉2内的输送网带和传输轮,位于烘干炉2外的第一减速机,第一减速机经皮带与传输轮连接。储料仓1的出料口穿过烘干炉2后位于输送网带的上方,储料仓1的出口为矩形扁口。储料仓1的扁矩形出口长度控制原料敷设在网带上的宽度,储料仓1的扁矩形出口下端距离烘干炉2网带的高度为所敷设原料的厚度,设定第一减速机转速后,即可计算出单位时间内烘干炉2的烘干输送原料的量(体积或重量),当烘干炉2的网带在第一减速机驱动下匀速前进时,可将原料均匀、平稳的输送至陶瓷螺旋加料机4上方的导料仓3。陶瓷螺旋加料机4由导料仓3、第二减速机47、联轴器46、堵板45、垫片44、出料锥管43、套管42和螺旋推进片41构成。其中,堵板45固定在套管42的开口端,螺旋推进片41位于套管42内,其两端分别经垫片44安装在堵板45及套管42的封闭端上。螺旋推进片41位于套管42封闭端最里侧的一圈螺旋片与其它螺旋片旋转方向相反,且位于套管42的出料口处,使得原料在推进至出料口时能够被挤压进出料口,减轻原料对套管42底部的挤压力,提高陶瓷螺旋加料机4的寿命。螺旋推进片41的一端经联轴器46与第二减速机47连接,套管42一端上部的进料口与导料仓3的出仓端口连接,另一端下部的出料口与出料锥管43连接。陶瓷螺旋加料机4的出料锥管43与套管42可做成锥套连接或法兰连接方式,一旦出料锥管43被高温腐蚀损坏后,只做局部零件更换即可,减少生产成本。出料锥管43下端为锥形管口,与铂金加料口5锥形结合,可起到密封作用,减少了融化池温度的波动和易挥发物质的挥发,避免了加料环节的扬尘。输送网带的尾端位于导料仓3的上方。原料从导料仓3进入陶瓷螺旋加料机4,螺旋推进片41的转动将原料推至熔炉的铂金加料口5进入融化池。套管42、螺旋推进片41、垫片44和堵板45均为由纯度在99.99%以上的氧化铝烧制而成的陶瓷套管、陶瓷螺旋推进片、陶瓷垫片和陶瓷堵板。第一减速机与第二减速机47转速可调速,根据加料量设定各自的转速,使烘干炉2送料量与陶瓷螺旋加料机4加料量保持平衡。 As shown in Fig. 1 and Fig. 2, the automatic feeding device of the present invention includes a feeding drying device and a ceramic screw feeder 4. The feeding and drying device includes a storage bin 1, a drying furnace 2 and a mesh belt transmission mechanism, wherein the mesh belt transmission mechanism includes a conveying mesh belt and a transmission wheel located in the drying furnace 2, and the first one outside the drying furnace 2 Reducer, the first reducer is connected with the transmission wheel through a belt. The discharge port of the storage bin 1 is located above the conveying mesh belt after passing through the drying furnace 2, and the outlet of the storage bin 1 is a rectangular flat mouth. The length of the flat rectangular outlet of the storage bin 1 controls the width of the raw material laid on the mesh belt. The height of the lower end of the flat rectangular outlet of the storage bin 1 from the mesh belt of the drying furnace 2 is the thickness of the laid raw material. Set the first reducer After the rotation speed, the amount (volume or weight) of the drying and transporting raw materials in the drying furnace 2 can be calculated per unit time. When the mesh belt of the drying furnace 2 advances at a constant speed driven by the first reducer, the raw materials can be evenly , Stable delivery to the guide bin 3 above the ceramic screw feeder 4. The ceramic screw feeder 4 is composed of a material guide bin 3, a second speed reducer 47, a shaft coupling 46, a blocking plate 45, a gasket 44, a discharge cone 43, a casing 42 and a screw propeller 41. Wherein, the blocking plate 45 is fixed on the open end of the casing 42, the screw propulsion piece 41 is located in the casing 42, and its two ends are installed on the blocking plate 45 and the closed end of the casing 42 through the gasket 44 respectively. The screw propulsion piece 41 is located at the innermost side of the closed end of the casing 42. The rotation direction of the other spiral pieces is opposite to that of the other spiral pieces, and it is located at the outlet of the casing 42, so that the raw material can be squeezed when it is pushed to the outlet. The material inlet and outlet can reduce the extrusion force of the raw material on the bottom of the casing 42 and improve the service life of the ceramic screw feeder 4 . One end of the screw propulsion piece 41 is connected to the second reducer 47 through a coupling 46, the upper feed port of one end of the casing 42 is connected to the discharge port of the guide bin 3, and the lower discharge port of the other end is connected to the discharge cone. Tube 43 is connected. The discharge cone 43 and the casing 42 of the ceramic screw feeder 4 can be connected by a taper sleeve or a flange connection. Once the discharge cone 43 is damaged by high temperature corrosion, only some parts can be replaced to reduce production costs. . The lower end of the discharge conical tube 43 is a conical nozzle, which is conically combined with the platinum feeding port 5, which can play a sealing role, reduce the fluctuation of the temperature of the melting pool and the volatilization of volatile substances, and avoid dust in the feeding process. The tail end of conveying mesh belt is positioned at the top of material guide bin 3. The raw material enters the ceramic screw feeder 4 from the material guide bin 3, and the rotation of the screw propeller 41 pushes the raw material to the platinum feeding port 5 of the melting furnace and enters the melting pool. The casing 42, the screw propeller 41, the gasket 44 and the blocking plate 45 are all ceramic casings, ceramic screw propulsion pieces, ceramic gaskets and ceramic blocking plates fired from alumina with a purity of more than 99.99%. The rotational speed of the first speed reducer and the second speed reducer 47 can be adjusted, and the respective rotational speeds are set according to the feeding amount, so that the feeding amount of the drying furnace 2 and the feeding amount of the ceramic screw feeder 4 are kept in balance.
本发明光学玻璃连熔生产线自动加料工艺包括以下工艺步骤: The automatic feeding process of the optical glass continuous melting production line of the present invention comprises the following process steps:
⑴由人工将原料或配合料注入储料仓1; (1) Manually inject raw materials or batch materials into storage bin 1;
⑵原料或配合料经储料仓1的出口漏出平铺到烘干炉2的输送网带上,烘干炉2内温度控制在160~260℃,原料视敷设厚度及加料需求量,通过控制第一减速机的速度使原料在烘干炉2内烘烤7~10小时,以充分除去原料中的水分; (2) Raw materials or batch materials are leaked from the outlet of storage bin 1 and spread on the conveying mesh belt of drying furnace 2. The temperature in drying furnace 2 is controlled at 160-260°C. The speed of the first reducer makes the raw material baked in the drying furnace 2 for 7 to 10 hours, so as to fully remove the moisture in the raw material;
⑶烘干后的原料或配合料从输送网带尾端落入陶瓷螺旋加料机4的导料仓3,之后从导料仓3进入套管42,由螺旋推进片41转动推至出料锥管43出口,经熔炉铂金加料口5进入融化池。 (3) The dried raw materials or batch materials fall from the end of the conveying mesh belt into the material guide bin 3 of the ceramic screw feeder 4, and then enter the casing 42 from the material guide bin 3, and are pushed by the screw propeller 41 to the discharge cone The outlet of pipe 43 enters the melting pool through the platinum feeding port 5 of the melting furnace.
Claims (6)
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113511797A (en) * | 2021-05-27 | 2021-10-19 | 陕西雷博创新光电科技有限公司 | Automatic feeding process and device for optical glass production line |
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| CN1120332A (en) * | 1993-03-31 | 1996-04-10 | Ppg工业公司 | Method and apparatus for making fibers from waste glass |
| CN201154842Y (en) * | 2007-12-28 | 2008-11-26 | 化工部长沙设计研究院 | A viscous material high temperature conveyor |
| CN201488497U (en) * | 2009-08-19 | 2010-05-26 | 山东招源硅胶有限公司 | Mesh-belt drying device |
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| US3725022A (en) * | 1971-02-12 | 1973-04-03 | Owens Illinois Inc | Method of feeding glass batch |
| CN1120332A (en) * | 1993-03-31 | 1996-04-10 | Ppg工业公司 | Method and apparatus for making fibers from waste glass |
| CN201154842Y (en) * | 2007-12-28 | 2008-11-26 | 化工部长沙设计研究院 | A viscous material high temperature conveyor |
| CN201488497U (en) * | 2009-08-19 | 2010-05-26 | 山东招源硅胶有限公司 | Mesh-belt drying device |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN113511797A (en) * | 2021-05-27 | 2021-10-19 | 陕西雷博创新光电科技有限公司 | Automatic feeding process and device for optical glass production line |
| CN113511797B (en) * | 2021-05-27 | 2023-03-28 | 陕西雷博创新光电科技有限公司 | Automatic feeding process and device for optical glass production line |
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