scholarly journals Conversion kinetics of container glass batch melting

2020 ◽  
Vol 104 (1) ◽  
pp. 34-44
Author(s):  
Nanako Ueda ◽  
Miroslava Vernerová ◽  
Jaroslav Kloužek ◽  
Pavel Ferkl ◽  
Pavel Hrma ◽  
...  
Keyword(s):  
Glass Batch ◽  
Container Glass ◽  
Kinetics Of ◽  
Batch Melting

Decomposition kinetics of granulated glass batch

2012 ◽  
Vol 358 (23) ◽  
pp. 3294-3298 ◽  
Author(s):  
Jinshu Cheng ◽  
Zhenlu Deng
Keyword(s):  
Glass Batch ◽  
Decomposition Kinetics ◽  
Kinetics Of

Study of properties of the glass batch melting filter dust

2011 ◽  
Vol 108 (2) ◽  
pp. 493-496
Author(s):  
Zuzana Jakubíková ◽  
Marek Liška ◽  
Alfonz Plško ◽  
Jana Pagáčová
Keyword(s):  
Glass Batch ◽  
Filter Dust ◽  
Batch Melting

Kinetics of corrosion of refractories by a high-alkali container-glass melt

Refractories ◽  
1985 ◽  
Vol 26 (3-4) ◽  
pp. 145-150
Author(s):  
M. N. Kucheryavyi ◽  
O. N. Popov
Keyword(s):  
Container Glass ◽  
High Alkali ◽  
Kinetics Of

scholarly journals Dissolution retardation of solid silica during glass-batch melting

2011 ◽  
Vol 357 (15) ◽  
pp. 2954-2959 ◽  
Author(s):  
Pavel Hrma ◽  
José Marcial
Keyword(s):  
Glass Batch ◽  
Batch Melting

The Use of Bagasse Ash as a Source of Silica for Production of Container Glass

2020 ◽  
Vol 2 (1) ◽  
Author(s):  
J.O. Muhammed ◽  
E.M Alemaka
Keyword(s):  
Calcium Carbonate ◽  
Glass Batch ◽  
Soda Lime ◽  
Batch Composition ◽  
Container Glass ◽  
Pharmaceutical Drugs ◽  
Muffle Furnace ◽  
Soda Lime Silica Glass ◽  
Sugarcane Bagasse Ash ◽  
Sulphur Trioxide

The study focused on the feasibility of recycling sugarcane bagasse ash (SCBA) to produce container glass. The bagasse was calcined through a Gallenkamp muffle furnace at 6000C and then held at 7000C for 1 ½ hrs and large amount of bagasse ash was obtained. 30 and 18 mesh sieves were used simultaneously to produce a fine powdered of the materials. 5g of SCBA sieved, calcium carbonate and sodium carbonate were passed through atomic absorption spectrophotometer. The result reveals SiO2 76.34wt%, Al2O3 8.55wt%, Fe2O3 2.93wt%, Na2O 0.12wt%, TiO2 0.80wt%, K2O 1.50wt%, CaO 0.07wt%, SO3 2.25wt%, Cr2O3 0.05wt%, Mn2O3 0.06wt% and LOI 6.42wt%. Interestingly, the ash contained high amount of silica of 76.34wt% which could supply all SiO2 needed to produce soda lime silica glass. A container glass batch composition was formulated from 95.899g of SCBA, 19.220g of CaCO3 and 25.556g of Na2CO3 and fired in muffle furnace at temperature between 11000C-12000C for 3 hours. The resulting glass was amber in colour which signifies the presence of iron oxide (Fe2O3) and sulphur trioxide (SO3) in bagasse ash. This implies that the ash can be used to produce amber glass for beverages and storing pharmaceutical drugs especially those which are sensitive to light.

scholarly journals Melting behavior of waste glass cullet briquettes in soda-lime-silica container glass batch

2018 ◽  
Vol 10 (1) ◽  
pp. 125-137 ◽  
Author(s):  
Wei Deng ◽  
Richard Wright ◽  
Chris Boden-Hook ◽  
Paul A. Bingham
Keyword(s):  
Glass Batch ◽  
Soda Lime ◽  
Melting Behavior ◽  
Waste Glass ◽  
Container Glass ◽  
Glass Cullet

CO2 Neutral Glass Manufacturing? – A Study of the Possibilities

2008 ◽  
Vol 39-40 ◽  
pp. 425-430
Author(s):  
Bo Jonson ◽  
Björn Zethræus ◽  
Ruud Beerkens ◽  
Adriaan Lankhorst
Keyword(s):  
Energy Efficiency ◽  
Glass Batch ◽  
Theoretical Calculations ◽  
Continuous Furnace ◽  
Melting Rate ◽  
Experimental Investigations ◽  
Carbon Compounds ◽  
Batch Components ◽  
Energy Balances ◽  
Batch Melting

The technological needs to achieve CO2 neutrality during glass manufacturing have been investigated by theoretical calculations on energy balances and experimental investigations on batch reactivity and fining efficiency. The concept is based on the assumption of utilization of woody bio fuel combustion directly over the batch blanket and glass melt bath for heating the glass furnace. Energy balance calculations were made for a “hot top”, 50 tonnes per day continuous furnace. Furthermore, elimination of the chemically bound CO2 in the glass batch has been considered by investigating the possible substitution of the batch carbonates by other compounds not bearing chemically bound CO2. Compounds not emitting oxides of carbon, nitrogen or sulphur were considered as candidate batch components. Studies on the effect of batch melting and fining indicate a beneficial effect on energy efficiency and melting rate when using carbonate substitutes. It is concluded that the combustion concept is theoretically fully possible for glass tank application. The substitution of batch carbonates by non carbon compounds is questionable from an environmental point view since the alternatives are expected to be synthesized by routes emitting CO2.

Interaction between solid, liquid and gas during glass batch melting

1986 ◽  
Vol 84 (1-3) ◽  
pp. 370-380 ◽  
Author(s):  
P. Hrma ◽  
J. Bartoň ◽  
T.L. Tolt
Keyword(s):  
Glass Batch ◽  
Solid Liquid ◽  
Batch Melting
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