公开(公告)号：US20140123707A1

公开(公告)日：2014-05-08

申请号：US14152068

申请日：2014-01-10

Applicant: ASAHI GLASS COMPANY, LIMITED

Inventor： Kuniaki Hiromatsu ,  Masanobu Shirai ,  Junichi Miyashita ,  Tomohiro Yonemichi ,  Takeo Endo

IPC: C03C17/245 ,  C03B25/08

CPC classification number: C03C17/2456 ,  C03B25/08 ,  C03C17/002 ,  C03C2218/1525 ,  C23C16/402 ,  C23C16/405 ,  C23C16/407 ,  C23C16/45578 ,  C23C16/46 ,  C23C16/52 ,  C23C16/545 ,  H01L31/0392 ,  H01L31/1884 ,  Y02E10/50

Abstract: A method for manufacturing a laminated film-coated glass substrate in which a laminated film is formed on a glass ribbon by a CVD method by means of a plurality of injectors disposed in the annealing furnace, wherein: the laminated film is formed at Tg+50° C. or lower; and in each of the injectors, if a quantity of heat exchanged between the injector and the glass ribbon is expressed by Q1 (kW), a quantity of heat exchanged between a heater paired with the injector and the glass ribbon is expressed by Q2 (kW), and an output of the glass is expressed by P (tons/day), then the relational expression |Q1|−P×0.116≦|Q2|≦|Q1| is satisfied.

Abstract translation: 一种层叠薄膜涂覆玻璃基板的制造方法，其中通过CVD法在玻璃带上形成的层叠薄膜包覆玻璃基板的方法，该方法通过设置在退火炉中的多个注射器形成，其中：层压膜形成为Tg + 50 ℃或更低; 并且在每个喷射器中，如果在喷射器和玻璃带之间交换的热量以Q1（kW）表示，则与喷射器成对的加热器与玻璃带之间交换的热量由Q2（kW ），玻璃的输出用P（吨/天）表示，则关系式| Q1 | -P×0.116＆nlE; | Q2 |＆nlE; | Q1 | 满意

公开(公告)号：US09309148B2

公开(公告)日：2016-04-12

申请号：US14152078

申请日：2014-01-10

Applicant: ASAHI GLASS COMPANY, LIMITED

Inventor： Kuniaki Hiromatsu ,  Masanobu Shirai ,  Junichi Miyashita ,  Tomohiro Yonemichi ,  Takeo Endo

IPC: C03C17/245 ,  C03C17/00 ,  C03B25/08 ,  C23C16/455 ,  C23C16/46

CPC classification number: C03C17/2456 ,  C03B25/08 ,  C03C17/002 ,  C23C16/45572 ,  C23C16/45595 ,  C23C16/46

Abstract: An area S (m2) of a facing surface of each of injectors which faces a glass ribbon is set so as to satisfy: S≦(0.0116×P×Cg×T)/{ε×F×σ(Tgla4−Tinj4)}, wherein P is an output (ton/day) of the glass ribbon; Cg is a specific heat (J/(kg·° C.)) of the glass; T is an acceptable temperature drop (° C.); ε is radiation factor; F is a surface-to-surface view factor; σ is Boltzmann's constant; Tgla is a temperature (K) of the glass ribbon represented by K=(Tin+Tout)/2 where Tin and Tout are measured values of the glass ribbon at the inlet and outlet of the injector, respectively; and Tinj is a temperature (K) of the facing surface of the injector.

Abstract translation: 将每个喷射器的面对玻璃带的面对面的面积S（m2）设定为满足：S＆NlE;（0.0116×P×Cg×T）/ {＆egr;×F×＆sgr（Tgla4-Tinj4 ）}，其中P是玻璃带的输出（吨/天）; Cg是玻璃的比热（J /（kg·℃））; T是可接受的温度降（℃）; ＆egr 是放射因子; F是一个表面到地面的视图因子; ＆sgr 是玻尔兹曼常数; Tgla是由K =（Tin + Tout）/ 2表示的玻璃带的温度（K），其中Tin和Tout分别是在喷射器的入口和出口处的玻璃带的测量值; Tinj是喷射器的面对表面的温度（K）。