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    • 6. 发明申请
    • OPTICAL FIBER COOLING APPARATUS AND OPTICAL FIBER MANUFACTURING METHOD
    • US20150101368A1
    • 2015-04-16
    • US14510517
    • 2014-10-09
    • SUMITOMO ELECTRIC INDUSTRIES, LTD.
    • Norihiro UENOYAMAIwao OKAZAKIManabu SHIOZAKITadashi ENOMOTO
    • C03B37/02
    • C03B37/02718
    • When a lower gauge pressure of a cooling tube part is set at A, and the number of divided units of the cooling tube part is set at N, and a length of each of the divided units of the cooling tube part is set at Li (i=1 to N), and a radius of each of the divided units of the cooling tube part is set at Ri (i=1 to N), and a gas flow rate of a coolant gas passed through each of the divided units of the cooling tube part is set at Qi (i=1 to N), and a viscosity coefficient of a coolant gas is set at μ1, and a radius of an optical fiber is set at r1, and a drawing speed of the optical fiber is set at V1, and a pressure loss of a straight tube part is set at B, and the number of divided units of the straight tube part is set at n, and a length of each of the divided units of the straight tube part is set at LLj (j=1 to n), and a radius of each of the divided units of the straight tube part is set at RRj (j=1 to n), and a gas flow rate of a pressurized gas passed through the straight tube part is set at Qgas, and a viscosity coefficient of the pressurized gas is set at μ2, and a pressure loss of a pressurizing chamber is set at C, and internal pressure correlation constants of the pressurizing chamber are set at D1 to D5, and a shape correction coefficient of the pressurizing chamber is set at k (1≦k≦2), an optical fiber cooling apparatus satisfies the following formula. A−B−kC≦0 where  [ Mathematical   Formula   1 ] A = ∑ i = 1 N  ( - Q i + π   V 1  ( R i 2 - r 1 2 2   ln  ( r 1 / R i ) + r 1 2 ) π 8   μ 1  ( r 1 2 - R i 2 )  ( r 1 2 + R i 2 + R i 2 - r 1 2 ln  ( r 1 / R i ) ) ) × L i   [ Mathematical   Formula   2 ] B = ∑ j = 1 n  - ( Q gas + π   V 1  ( RR j 2 - r 1 2 2   ln  ( r 1 / RR j ) + r 1 2 ) π 8   μ 2  ( r 1 2 - RR j 2 )  ( r 1 2 + RR j 2 + RR j 2 - r 1 2 ln  ( r 1 / RR j ) ) ) × LL j   [ Mathematical   Formula   3 ] C = D   1 + D   2 × Q gas + D   3 × Q gas 2 + D   4 × V   1 + D   5 × Q gas × V   1