WO2013159403A1 - 液晶制程中炉体的双路循环冷却系统 - Google Patents

液晶制程中炉体的双路循环冷却系统 Download PDF

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Publication number
WO2013159403A1
WO2013159403A1 PCT/CN2012/075276 CN2012075276W WO2013159403A1 WO 2013159403 A1 WO2013159403 A1 WO 2013159403A1 CN 2012075276 W CN2012075276 W CN 2012075276W WO 2013159403 A1 WO2013159403 A1 WO 2013159403A1
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Prior art keywords
cooling
pipe
furnace body
liquid crystal
water
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French (fr)
Inventor
邓鸿韬
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TCL China Star Optoelectronics Technology Co Ltd
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Shenzhen China Star Optoelectronics Technology Co Ltd
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Priority to US13/515,285 priority Critical patent/US9513063B2/en
Publication of WO2013159403A1 publication Critical patent/WO2013159403A1/zh
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    • GPHYSICS
    • G02OPTICS
    • G02FOPTICAL DEVICES OR ARRANGEMENTS FOR THE CONTROL OF LIGHT BY MODIFICATION OF THE OPTICAL PROPERTIES OF THE MEDIA OF THE ELEMENTS INVOLVED THEREIN; NON-LINEAR OPTICS; FREQUENCY-CHANGING OF LIGHT; OPTICAL LOGIC ELEMENTS; OPTICAL ANALOGUE/DIGITAL CONVERTERS
    • G02F1/00Devices or arrangements for the control of the intensity, colour, phase, polarisation or direction of light arriving from an independent light source, e.g. switching, gating or modulating; Non-linear optics
    • G02F1/01Devices or arrangements for the control of the intensity, colour, phase, polarisation or direction of light arriving from an independent light source, e.g. switching, gating or modulating; Non-linear optics for the control of the intensity, phase, polarisation or colour 
    • G02F1/13Devices or arrangements for the control of the intensity, colour, phase, polarisation or direction of light arriving from an independent light source, e.g. switching, gating or modulating; Non-linear optics for the control of the intensity, phase, polarisation or colour  based on liquid crystals, e.g. single liquid crystal display cells
    • G02F1/1303Apparatus specially adapted to the manufacture of LCDs

Definitions

  • the present invention relates to a cooling system, and more particularly to a two-way circulating cooling system for a furnace body in a liquid crystal process. Background technique
  • FIG. 1 it is a schematic perspective view of a furnace body in a conventional liquid crystal process.
  • the furnace body 10 in order to maintain the cleanness level in the furnace body 10, the furnace body 10 is usually provided with an air supply and exhaust system, and clean air is introduced through the purification pipe 11 to form the inside of the furnace body 10. Positive pressure, and exhausted outward through the exhaust pipe 12, the direction of gas flow is indicated by an arrow. Further, both the shutter side 13 and the rear service door side 14 of the furnace body 10 can be opened to operate the inside of the furnace body 10.
  • the furnace body In order to ensure the quality of the liquid crystal products, the furnace body needs to be maintained from time to time. At present, the liquid crystal process is cooled by the natural cooling method in the current furnace body. It takes a long time (about 6 hours) from the high temperature of 150 ° C (example temperature) to below 60 ° C, which becomes the maintenance cost of the entire liquid crystal production line. The bottleneck at the time.
  • the present invention provides a two-way circulating cooling system for a furnace body in a liquid crystal process, comprising a water pump, a water tank, a water suction pipe, a return pipe, a first cooling pipe, and a second cooling pipe, the water pump and the water tank
  • the pumping pipe and the return pipe are located outside the furnace body, and the first cooling pipe and the second cooling pipe are two parallel rows of cooling pipes located inside the furnace body; the water pump is accommodated in the water tank through the water pipe
  • the cooling material is pumped into the first cooling pipe and the second cooling pipe inside the furnace body, and the cooling material takes away the heat inside the furnace body and then is discharged into the water tank through the return pipe, the first cooling pipe and the second cooling pipe.
  • the in-lane coolant flows in the opposite direction.
  • the water pump is a self-priming water pump.
  • the cooling material is recovered water of a liquid crystal dropping process.
  • the water tank is a temporary buffer for recovering water from the liquid crystal dropping process used for the edging process.
  • the first cooling pipe and the second cooling pipe are stainless steel pipes.
  • the first cooling pipe and the second cooling pipe are ceramic pipes.
  • the first cooling pipe is installed in an exhaust pipe inside the furnace body.
  • the second cooling pipe is installed in an exhaust pipe inside the furnace body.
  • the first cooling duct and the second cooling duct are installed in an exhaust pipe inside the furnace body.
  • the pipe shape of the first cooling pipe and the second cooling pipe is a square wave line.
  • the two-way circulating cooling system of the furnace body in the liquid crystal process of the invention can accelerate the cooling speed in the furnace and reduce the ineffective cooling time, thereby shortening the maintenance time of the entire production line and improving the production efficiency; the invention adopts the cooling water circulation system in the furnace
  • a double-channel cooling water circulation system is installed in the body, and the water in the buffer tank (Buffer Tank) is pumped into the furnace body by the water pump, and the entire furnace body is cooled uniformly without any additional cost; the existing furnace body can be modified and used.
  • a small cost achieves a better cooling effect.
  • FIG. 1 is a schematic perspective view of a furnace body in a conventional liquid crystal process
  • FIG. 2 is a schematic structural view of a preferred embodiment of a two-way circulating cooling system for a furnace body in a liquid crystal process according to the present invention
  • FIG. 3 is a schematic structural view of a first cooling pipe and a second cooling pipe of a preferred embodiment of a two-way circulating cooling system for a furnace body in a liquid crystal process according to the present invention
  • FIG. 4 is a side view of an exhaust pipe obtained by modifying a furnace body in a conventional liquid crystal process according to the present invention.
  • FIG. 5 is a front view of the exhaust pipe of FIG. detailed description
  • FIG. 2 it is a schematic structural view of a preferred embodiment of a two-way circulating cooling system for a furnace body in a liquid crystal process of the present invention.
  • the two-way circulating cooling system of the furnace body in the liquid crystal process comprises a water pump 2, a water tank 5, a water suction pipe 3, a return pipe 4, a first cooling pipe and a second cooling pipe.
  • the pump body 1 is externally added with a pump (Pump) 2 and related circulating pipelines, and a return pipe 4, which is used without
  • the self-priming water pump 2 which is introduced into the water, draws the recovered water 6 in the water tank 5 into the cooling system inside the furnace body 1, removes the heat, and discharges it into the water tank 5.
  • the recovered water 6 is the recovered water of the liquid crystal dropping process (ODF) as the cooling material, and the heat in the furnace body 1 is discharged out of the furnace in time by the low temperature and high specific heat characteristics of the cooling water, so that the furnace temperature is rapidly lowered.
  • the cooling material adopts the recycled water in the existing liquid crystal process to realize comprehensive recycling of the recovered water and reduce the cost.
  • the water pipe 3 and the recovered water 6 in the return pipe 4 flow in the direction of the arrow, and flow through the first cooling pipe in the furnace body 1 in the direction of the solid triangle arrow, and flow through the second inside the furnace body 1 in the direction of the dotted triangle arrow. Cool the piping.
  • the water tank 5 is a buffer (liquidizer) in the liquid crystal dropping process (ODF).
  • the buffer (Buffer) of the recovered water is used for the edging process to realize efficient recycling of the recovered water.
  • the dual cooling water circulation system can be retrofitted to existing furnaces at almost no cost and based on existing liquid crystal processes.
  • FIG. 3 there is shown a schematic structural view of a first cooling circuit and a second cooling circuit of a preferred embodiment of a two-way circulating cooling system for a furnace body in a liquid crystal process of the present invention.
  • the first cooling line 7 and the second cooling line 8 are two parallel rows of cooling lines located inside the furnace body 1.
  • the shape of the tubes of the first cooling line 7 and the second cooling line 8 may be square waveforms. Polyline.
  • the first cooling line 7 and the second cooling line 8 may be made of stainless steel (SUS) tubes or ceramic tubes of high strength and high temperature resistance.
  • the shape of the cooling pipe as long as possible can achieve a better cooling effect.
  • the two rows of cooling pipes have the same shape and the opposite direction of cooling water flow can ensure uniform cooling.
  • FIG. 4 and 5 are side views showing an exhaust pipe obtained by modifying a furnace body in a conventional liquid crystal process according to the present invention
  • Fig. 5 is a front view of the exhaust pipe of Fig. 4.
  • the exhaust pipe 22 is an existing pipeline structure in the furnace body, and only the exhaust pipe 22 is modified during the modification, and a new cooling pipe 15, an exhaust pipe 22 and a cooling pipe are embedded in the exhaust pipe 22.
  • a gas discharge passage 16 is formed between the 15 and a cooling water passage 17 is formed in the cooling line 15, so that the supply and exhaust system can be normally used during production, and the cooling line 15 can also be used during maintenance to take away heat and ensure the furnace body as soon as possible. Cool down.
  • the two cooling pipes may all be installed in the exhaust pipe, or may be partially disposed in the exhaust pipe and partially disposed outside the exhaust pipe.
  • the cooling of the furnace temperature by using the two-way circulating cooling system of the furnace body in the liquid crystal process of the invention can effectively accelerate the cooling process of the furnace body, save equipment maintenance time and improve production efficiency;
  • a two-way cooling water circulation system is installed, and almost no cost is added, so that the entire furnace body is cooled uniformly; the existing furnace body can be modified, and a better cooling effect can be achieved with a small cost.

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  • Physics & Mathematics (AREA)
  • Nonlinear Science (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Chemical & Material Sciences (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • General Physics & Mathematics (AREA)
  • Optics & Photonics (AREA)
  • Furnace Details (AREA)
  • Liquid Crystal (AREA)

Description

液晶制程中炉体的双^环冷却系统 技术领域
本发明涉及冷却系统, 尤其涉及一种液晶制程中炉体的双路循环冷却 系统。 背景技术
在现有液晶制程中的烘干、 固化、 退火等步骤都需要用到用于加热的 炉体。 参见图 1 , 其为现有液晶制程中一种炉体的立体结构示意图。 现有 液晶制程中所使用的炉体 10, 因要保持炉体 10内的洁净等级, 炉体 10内 通常配有供排气系统, 通过净化管 11通入洁净空气, 使炉体 10内形成正 压, 并通过排气管 12 向外排气, 气体流动方向以箭头表示。 此外, 炉体 10的遮板侧 13和后维修门侧 14均可以打开以操作炉体 10的内部。
为保证液晶产品的质量, 炉体需要时常进行养护。 目前, 液晶制程上 于目前炉体内降温采用自然冷却的方式, 从高温 150°C (示例温度) 降至 60°C以下所需时间较长(约 6 小时) , 成为整条液晶产线保养耗时的瓶 颈。
这是由于炉体降温时间较长, 而此段时间由于高温导致人员无法进行 保养, 属无效时间。 因无效时间过长, 导致了炉体保养耗时过长, 单台炉 体至少需要一天, 从而导致整条产线(Line ) 的保养时间过长。 发明内容
因此, 本发明的目的在于提供一种加速炉体内降温速度的液晶制程中 炉体的双路循环冷却系统。
为实现上述目的, 本发明提供一种液晶制程中炉体的双路循环冷却系 统, 包括水泵、 水槽、 抽水管、 回流管、 第一冷却管路及第二冷却管路, 所述水泵、 水槽、 抽水管及回流管位于炉体外部, 所述第一冷却管路和第 二冷却管路为位于炉体内部的平行并列的两排冷却管路; 所述水泵经由抽 水管将水槽中容纳的冷却物抽至炉体内部的第一冷却管路和第二冷却管路 中, 冷却物带走炉体内部的热量后再经由回流管排入水槽中, 第一冷却管 路和第二冷却管路内冷却物流动方向相反。
其中, 所述水泵为自吸式水泵。 其中, 所述冷却物为液晶滴入制程的回收水。
其中, 所述水槽为供磨边制程使用的液晶滴入制程回收水的暂存緩 沖。
其中, 所述第一冷却管路及第二冷却管路为不锈钢管。
其中, 所述第一冷却管路及第二冷却管路为陶瓷管。
其中, 所述第一冷却管路安装于炉体内部的排气管中。
其中, 所述第二冷却管路安装于炉体内部的排气管中。
其中, 所述第一冷却管路及第二冷却管路安装于炉体内部的排气管 中。
其中, 所述第一冷却管路及第二冷却管路的管路形状为方波形折线。 本发明液晶制程中炉体的双路循环冷却系统可以加速炉内降温速度, 减少无效的降温时间, 从而缩短整条产线的保养维护时间, 提高生产效 率; 本发明采用冷却水循环系统, 在炉体内加装双路冷却水循环系统, 通 过水泵将緩沖槽(Buffer Tank ) 中的水抽至炉体内, 几乎不用增加任何成 本, 使整个炉体降温均匀; 可以依现有炉体进行改造, 用较小的费用达到 较好的冷却效果。 附图说明
下面结合附图, 通过对本发明的具体实施方式详细描述, 将使本发明 的技术方案及其他有益效果显而易见。
附图中,
图 1为现有液晶制程中炉体的立体结构示意图;
图 2为本发明液晶制程中炉体的双路循环冷却系统一较佳实施例的结 构示意图;
图 3 为本发明液晶制程中炉体的双路循环冷却系统一较佳实施例的第 一冷却管路及第二冷却管路的结构示意图;
图 4为依照本发明改造现有液晶制程中炉体得到的排气管的侧视图; 图 5为图 4中排气管的主视图。 具体实施方式
参见图 2, 其为本发明液晶制程中炉体的双路循环冷却系统一较佳实 施例的结构示意图。 该液晶制程中炉体的双路循环冷却系统包括水泵 2、 水槽 5、 抽水管 3、 回流管 4、 第一冷却管路及第二冷却管路。 炉体 1外部 增加水泵(Pump ) 2 及相关循环管路抽水管 3、 回流管 4, 采用一无需加 入引水的自吸式水泵 2, 将水槽(Water Tank ) 5中的回收水 6抽至炉体 1 内部的冷却系统内, 带走热量后再排入水槽(Water Tank ) 5中。 回收水 6 作为冷却物为液晶滴入制程(ODF ) 的回收水, 利用冷却水的低温、 高比 热的特性, 将炉体 1 内热量及时排出炉外, 使炉温迅速降低。 冷却物采用 现有液晶制程中的回收水, 实现回收水综合重复利用, 降低成本。 抽水管 3、 回流管 4 中的回收水 6按照箭头方向流动, 按实线三角箭头方向流经 炉体 1 内的第一冷却管路, 按虚线三角箭头方向流经炉体 1 内的第二冷却 管路。 水槽 5 为液晶滴入制程(ODF ) 中洗净机(清洗机) 回收水的暂存 緩沖 (Buffer ) , 以供磨边制程使用, 实现回收水的高效循环利用。 双路 冷却水循环系统可以加装在现有的炉体上, 几乎不用增加任何成本而且基 于现有的液晶制程来实现。
参见图 3 , 其为本发明液晶制程中炉体的双路循环冷却系统一较佳实 施例的第一冷却管路及第二冷却管路的结构示意图。 第一冷却管路 7和第 二冷却管路 8为位于炉体 1 内部的平行并列的两排冷却管路, 第一冷却管 路 7及第二冷却管路 8的管路形状可以为方波形折线。 为达到降温迅速及 降温速率等同, 特采用双路循环, 分别从炉体 1 最下段和最上段接入平行 并列的两排冷却管路, 第一冷却管路 7和第二冷却管路 8为完全或大体上 平行并列, 两管路内冷却水采用反向流动, 既加快冷却速度, 又可使整个 炉体 1降温均匀, 以免发生事故。 第一冷却管路 7及第二冷却管路 8可采 用不锈钢 (SUS ) 管或高强度耐高温导热的陶瓷管。 尽可能长的冷却管路 形状可以实现较好的降温效果, 两排冷却管路形状相同且冷却水流动方向 相反可以保证降温均匀。
如果依现有炉体的结构进行改造, 可以用较小的费用达到较好的冷却 效果。 参见图 4及图 5为依照本发明改造现有液晶制程中炉体得到的排气 管的侧视图, 图 5为图 4 中排气管的主视图。 排气管 22为炉体中已有的 管路结构, 改造时只需对排气管 22进行改造, 在排气管 22内部嵌入新增 的冷却管路 15, 排气管 22和冷却管路 15之间形成气体排出通道 16, 冷 却管路 15 内形成冷却水通道 17, 这样生产时供排气系统可正常使用, 保 养时冷却管路 15 也可使用, 以带走热量, 确保炉体尽快降温。 基于现有 液晶制程中炉体的排气管实际分布情况, 两路冷却管路可以全部安装于排 气管中, 也可以一部分设置于排气管中, 一部分设置于排气管外。 通过改 造原有的炉体, 可以省去重新制造和更换炉体的费用。
综上, 使用本发明液晶制程中炉体的双路循环冷却系统对炉温进行冷 却后能有效加速炉体降温过程, 节省设备维护时间, 提高生产效率; 本发 明在炉体内加装双路冷却水循环系统, 几乎不用增加任何成本, 使整个炉 体降温均匀; 可以依现有炉体进行改造, 用较小的费用达到较好的冷却效 果。
以上所述, 对于本领域的普通技术人员来说, 可以根据本发明的技术 方案和技术构思作出其他各种相应的改变和变形, 而所有这些改变和变形 都应属于本发明后附的权利要求的保护范围。

Claims

权 利 要 求
I、 一种液晶制程中炉体的双路循环冷却系统, 包括水泵、 水槽、 抽 水管、 回流管、 第一冷却管路及第二冷却管路, 所述水泵、 水槽、 抽水管 及回流管位于炉体外部, 所述第一冷却管路和第二冷却管路为位于炉体内 部的平行并列的两排冷却管路; 所述水泵经由抽水管将水槽中容纳的冷却 物抽至炉体内部的第一冷却管路和第二冷却管路中, 冷却物带走炉体内部 的热量后再经由回流管排入水槽中, 第一冷却管路和第二冷却管路内冷却 物流动方向相反。
2、 如权利要求 1 所述的液晶制程中炉体的双路循环冷却系统, 其 中, 所述水泵为自吸式水泵。
3、 如权利要求 1 所述的液晶制程中炉体的双路循环冷却系统, 其 中, 所述冷却物为液晶滴入制程的回收水。
4、 如权利要求 1 所述的液晶制程中炉体的双路循环冷却系统, 其 中, 所述水槽为供磨边制程使用的液晶滴入制程回收水的暂存緩沖。
5、 如权利要求 1 所述的液晶制程中炉体的双路循环冷却系统, 其 中, 所述第一冷却管路及第二冷却管路为不锈钢管。
6、 如权利要求 1 所述的液晶制程中炉体的双路循环冷却系统, 其 中, 所述第一冷却管路及第二冷却管路为陶瓷管。
7、 如权利要求 1 所述的液晶制程中炉体的双路循环冷却系统, 其 中, 所述第一冷却管路安装于炉体内部的排气管中。
8、 如权利要求 1 所述的液晶制程中炉体的双路循环冷却系统, 其 中, 所述第二冷却管路安装于炉体内部的排气管中。
9、 如权利要求 1 所述的液晶制程中炉体的双路循环冷却系统, 其 中, 所述第一冷却管路及第二冷却管路安装于炉体内部的排气管中。
10、 如权利要求 1 所述的液晶制程中炉体的双路循环冷却系统, 其 中, 所述第一冷却管路及第二冷却管路的管路形状为方波形折线。
II、 一种液晶制程中炉体的双路循环冷却系统, 包括水泵、 水槽、 抽 水管、 回流管、 第一冷却管路及第二冷却管路, 所述水泵、 水槽、 抽水管 及回流管位于炉体外部, 所述第一冷却管路和第二冷却管路为位于炉体内 部的平行并列的两排冷却管路; 所述水泵经由抽水管将水槽中容纳的冷却 物抽至炉体内部的第一冷却管路和第二冷却管路中, 冷却物带走炉体内部 的热量后再经由回流管排入水槽中, 第一冷却管路和第二冷却管路内冷却 物流动方向相反;
其中, 所述水泵为自吸式水泵;
其中, 所述冷却物为液晶滴入制程的回收水;
其中, 所述水槽为供磨边制程使用的液晶滴入制程回收水的暂存緩 沖;
其中, 所述第一冷却管路及第二冷却管路为不锈钢管;
其中, 所述第一冷却管路安装于炉体内部的排气管中;
其中, 所述第二冷却管路安装于炉体内部的排气管中;
其中, 所述第一冷却管路及第二冷却管路的管路形状为方波形折线。
PCT/CN2012/075276 2012-04-28 2012-05-10 液晶制程中炉体的双路循环冷却系统 Ceased WO2013159403A1 (zh)

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