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Brian Loncto

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Strong push in late 1960s and 1970s to use chrome-magnesite refractories. ... Chrome oxide is traditionally frowned upon due to possible contamination of color ... – PowerPoint PPT presentation

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Title: Brian Loncto


1
Refractories in Contact with Glass Melts
  • Brian Loncto
  • Tony Rodbourn
  • School of Engineering
  • NYS College of Ceramics
  • Alfred University, Alfred, NY

2
Glass Furnace Design
  • Tank refractory is in contact with glass
  • Superstructure refractory is in contact with
    atmosphere above the melt
  • Regenerators refractory is used to store heat
    to save on utilities

3
Refractory Selection
- Silica used mostly in superstructure advanta
ge silica is the main component in glass
melts, contamination is not as important
cheap disadvantage low use temperatures -
Fused-cast AZS used mainly in the
tank advantage good resistance to acid
(glass) attack more wear-resistant than
silica disadvantage high cost
4
Refractory Selection
- Basic Refractories not used except in certain
situations Why? - low resistance to chemical
attack by acidic liquids (siliceous batch)
5
Chrome-Magnesite
Strong push in late 1960s and 1970s to use
chrome-magnesite refractories. - problems arose
in refractories using sea-water magnesite as a
raw material Henthorn, R.S. and Jackson, B.
(1969) - tested refractories and their
resistance to siliceous batch attack - found
that chrome-magnesite refractories warped
significantly
6
Chrome-Magnesite
INSERT PICTURE FROM 1969 HERE!
7
Fused-Cast AZS
  • Highly resistant to wear, especially at the
    liquid-solid-vapor line (flux line)
  • Busby, T.S. et al (1978) - tested high
    content alumina, fused-cast AZS, and
    aluminosilicate refractories for wear at the
    flux line - general trend noticed that
    increasing silica content increased wear

8
Fused-Cast AZS
  • Underwood, W. A. and Thomas, E. A. (1978)
  • Tested bonded, sintered and fused cast AZS bodies
  • Bonded heterogeneous bodies
  • Sintered lower porosity and more homogenous
  • Bonded AZS (lower zirconia, higher porosity),
    corroded at a higher rate than sintered AZS

9
Fused-Cast AZS
  • Underwood, W. A. and Thomas, E. A. (1978)
  • - Slightly greater static corrosion rate of
    sintered v. fused cast body
  • This despite difference in zirconia content and
    porosity
  • Can be contributed to much lower glassy phase of
    the sintered body

10
Glass Furnace Bottom
  • Begley, E. R. (1988)
  • Discusses Facts, Myths and Trends
  • Driving forces for research
  • Amount of energy lost out bottom of tank
  • Reduction of cost of refractory while maintaining
    high glass quality

11
Glass Furnace Bottom
  • Begley, E. R. (1988)
  • -Myth 1
  • - With careful refractory selection, metal
    drilling can be stopped
  • - Metal becomes encapsulated in zircon layer and
    drilling stops
  • - Both are wrong
  • Begley, Herndon, and Schmidt (1972) state that
    metal drilling is proportional to metal line
    resistance of refractory

12
Glass Furnace Bottom
  • Begley, E. R. (1988)
  • - Begley, Herndon, and Schmidt (1972) state that
    metal drilling is proportional to metal line
    resistance of refractory
  • - Only way to prevent metal drilling is to
    prevent metal from entering furnace

13
Glass Furnace Bottom
  • Begley, E. R. (1988)
  • - Myth 2
  • - Increased temperatures do not make very much
    difference in refractory corrosion
  • - Corrosion rates increase exponentially with
    temperature
  • - Corrosion rate doubles every 50C

14
Glass Furnace Bottom
  • Begley, E. R. (1988)
  • - Myth 3
  • -Zirconia inversion from the monolithic to
    tetragonal phase causes large joints to open on
    furnace bottom
  • - Never seen in industry
  • - Can only be produced in carefully controlled
    lab experiments

15
Looking to the Future (2000)
  • Glass industry consumes 400,000 tons of
    refractory each year
  • Due to collaboration between glass and
    refractories industry, consumption has dropped by
    2 per year for 30 years
  • Over this time, refractory cost has increased 50

16
Looking to the Future (2000)
  • Benefits of extending furnace life
  • Refractories are largest single cost to build
    and repair of glass furnace
  • Therefore, extending furnace lives reduces cost
    by reducing amount of refractory needed
  • Glass contact area biggest determinant of
    furnace life
  • Chrome oxide refractories display superior
    corrosion resistance, amid concerns

17
Looking to the Future (2000)
  • Benefits of extending furnace life
  • Chrome oxide is traditionally frowned upon due
    to possible contamination of color
  • Advances in technology are allowing for its use
  • Oxy-fuel firing is attractive to glassmakers due
    to higher efficiency and lower emissions
  • Oxy-fuel firing increases refractory wear though
  • Companies are working to develop a more resistant
    refractory

18
Current Bottom Design
  • Pilkington, North America Laurinburg, NC plant
  • - flat bottom design using
  • 3 fused-cast AZS
  • 12 clay

19
References
1. Henthorn, R.S. et al Refractories for the
Superstructure and Ancillary Parts of
Glass-making Furnaces, British Ceramic Society
Proceedings, No. 14, p. 41, August 1696. 2.
Busby, T.S. et al The solution of some
commercial refractories in soda-lime glass in the
temperature range 1200-1350ºC, Glass Technology,
vol. 19, no. 3, p. 54-56, 1978. 3. Underwood,
W.A. et al How to Avoid Problems When Applying
AZS Refractories, Glass Industry, p. 14-17,
September 1986. 4. Begley, E.R. Glass Furnace
Bottom Construction Trends, Facts, and Myths
A Review, Ceram. Eng. Sci. Proc., vol. 9, no. 3,
p. 306-314, 1988. 5. Evans, G. Glassmaking
Refractories looking to the future, Glass
Tech. vol. 41, no. 4, p. 109-111, 2000.
20
References (2)
6. Roux, J.M. Refined solutions for bottom
superstructure construction, Glass Ind., p.
18-19, March 2001. 7. Dunkl, M. et al Criteria
for the Selection of Refractories for Special
Glass Melting Tanks, Cer. Eng. Sci. Proc., vol.
24, no. 1, p. 197-210, 2003. 8. Varner, J.R.,
Glass-Tank Refractories, CES 414
Refractories, PowerPoint presentation, 2005. 9.
Faulkner, J., Pilkington Furnace Process
Engineer, conversation on April 25, 2005.
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