A glass melting tank furnace with two working tanks for melting crystal

1974 ◽  
Vol 31 (10) ◽  
pp. 730-733
Author(s):  
N. A. Senkevich ◽  
O. D. Khait
1979 ◽  
Vol 36 (10) ◽  
pp. 580-582
Author(s):  
V. Ya. Dzyuzer ◽  
V. B. Kut'in ◽  
N. I. Kokarev ◽  
V. Yu. Budovkin

2008 ◽  
Vol 39-40 ◽  
pp. 613-618
Author(s):  
Hans Peter Martinz ◽  
Brigitte Nigg ◽  
Jiri Matej ◽  
Manfred Sulik ◽  
Heike Larcher

The SIBOR® (Si-10B-2C) oxidation protective coating was applied onto molybdenumand molybdenum – 3 wt% zirconia samples by APS (= Atmospheric Plasma Spraying) with a subsequent heat treatment. Then the coated samples were submitted to ramp oxidation tests with heating rates of 10°C / hour up to a temperature of 1450°C. This procedure simulates the heating up of a glass melting tank where SIBOR® coated parts are most frequently used. Some of the samples which could be oxidized without any defect were then immersed in various molten glasses to determine the dissolution rate of the SIBOR® substrate system. This simulates the situation when the glass melting tank is filled and operated with molten glass. SIBOR® proved to be an excellent oxidation protective coating for the molybdenum – zirconia – material like for pure molybdenum. The coating was fairly good dissolved by opal glass and – slightly less – by soda lime glass. With borosilicate glass a much slower interaction was found. In all cases some discolouration and bubbles were found in the glasses after one week.


1983 ◽  
Vol 40 (5) ◽  
pp. 222-226 ◽  
Author(s):  
O. N. Popov ◽  
R. Z. Fridkin ◽  
Z. T. Mamedov
Keyword(s):  

2004 ◽  
Vol 61 (11-12) ◽  
pp. 399-401
Author(s):  
A. Balandis ◽  
G. Vaitskyalionis

1979 ◽  
Vol 36 (5) ◽  
pp. 276-278
Author(s):  
O. N. Popov ◽  
A. G. Gel'mut

2013 ◽  
Vol 361-363 ◽  
pp. 845-849
Author(s):  
Ning Xu ◽  
Yue Xu

The float glass melting tank is huge and complex equipment which the operation parameters are difficult to control in production line. The install of desulfurizer makes the kiln more complex and unstable. In present work, we fulfill the field experiments and obtained the optimal practical operation parameters. The obtained parameters were: aperture of wings gate: 75-85%; aperture of draft fan: 30-35% for draft fan 1, and draft fan 2 were through-type; aperture of conveying fan: 70-85%; temperature of gas into desulfurizer: 180-200°C; the water flow were controlled by thermocouple and diaphragm control valve; Velocity of gas into desulfurizer: 8-10 m/s. Our results provide the guidance for installing the desulfurizer and modifying the whole system in practice.


Sign in / Sign up

Export Citation Format

Share Document