- Page 1 and 2:
Glass Melting Technology: A Technic
- Page 3 and 4:
Disclaimer This document was prepar
- Page 6 and 7:
Glass Melting Technology: A Technic
- Page 8 and 9:
cyclical economy. Specialty glass m
- Page 10:
Reference The report is supplemente
- Page 14 and 15:
Preface The glass industry is under
- Page 16:
While this section was not a major
- Page 19 and 20:
5. All traditional glass segments a
- Page 21 and 22:
• Energy issues Glass melting is
- Page 23 and 24:
The issue of funding for research a
- Page 26 and 27:
Chapter I Technical Assessment of G
- Page 28 and 29:
process when it introduced continuo
- Page 30 and 31:
Figure I.1. Quality, Energy, Throug
- Page 32 and 33:
credible forecasts that energy cost
- Page 34 and 35:
Capital-intensive manufacturing bus
- Page 36 and 37:
silica sand with a variety of indus
- Page 38 and 39:
I.4. Motivation to advance melting
- Page 40 and 41:
would be possible with a more detai
- Page 42:
efining, higher performance refract
- Page 45 and 46:
A major regional producer, the Unit
- Page 47 and 48:
continues to operate using technolo
- Page 49 and 50:
The percentage used for batch melti
- Page 51 and 52:
having fewer producers of major com
- Page 53 and 54:
Flat glass Forecasters predict an a
- Page 55 and 56:
glass fiber in some applications an
- Page 57 and 58:
With the high capital cost of new g
- Page 59 and 60:
The economic viability of electric
- Page 61 and 62:
development and capital investment
- Page 63 and 64:
investment of the traditional glass
- Page 65 and 66:
and increase cooperation on the hig
- Page 67 and 68:
The melting processes for silica-ba
- Page 69 and 70:
In the regenerative furnace, two re
- Page 71 and 72:
• Unit melter The unit melter is
- Page 73 and 74:
Furnace emissions are reduced and t
- Page 75 and 76:
glass. Electric boost is often used
- Page 77 and 78:
materials, state-of-the-art equipme
- Page 79 and 80:
Figure IV.1. PPG P-10 Primary Melte
- Page 81 and 82:
system. Applications for the techno
- Page 83 and 84:
stable and controlled operating pro
- Page 85 and 86:
Four test series using oxy-gas burn
- Page 87 and 88:
In the AGM melting process, mixed b
- Page 89 and 90:
Melter controls are extremely sophi
- Page 91 and 92:
simplify heat exchange technique th
- Page 93 and 94:
square or rectangular hopper locate
- Page 95 and 96:
After operating for over 12 years,
- Page 97 and 98:
The modular design of the device ma
- Page 99 and 100:
A single-phase 600-KW saturable rea
- Page 101 and 102:
IV.9.2. Fusion et Affinage Rapide (
- Page 103 and 104:
gases leave this compartment and gi
- Page 106 and 107:
Chapter V Industry Perspective on M
- Page 108 and 109:
problems that confront the entire i
- Page 110 and 111:
and port structures. Fuel savings o
- Page 112 and 113:
Glass manufacturers of all products
- Page 114 and 115:
here. To remain vigorous and compet
- Page 116 and 117:
RAY RICHARDS holds a BS in chemistr
- Page 118 and 119:
Chapter VI Vision for Glassmaking V
- Page 120 and 121:
VI.3. Economic perspective The majo
- Page 122:
and facility construction and plant
- Page 126: Introduction In the course of gener
- Page 129 and 130: totally replaced by barium, zinc or
- Page 131 and 132: of soda. Other raw materials includ
- Page 133 and 134: Batch melting in combustion furnace
- Page 135 and 136: 1.3. Detailed description of the fu
- Page 137 and 138: increase reactions in soda-lime-sil
- Page 139 and 140: promoted by the addition of fine-gr
- Page 141 and 142: The presence of some distinct solid
- Page 143 and 144: surface and escape from the melt. S
- Page 145 and 146: Homogenization can also be aided by
- Page 147 and 148: Batch melting strongly depends on t
- Page 149 and 150: downstream operations, these bubble
- Page 151 and 152: furnaces generally have better spec
- Page 153 and 154: fundamental change in heat transfer
- Page 155 and 156: or long-term trends and judges the
- Page 157 and 158: Thermal momentum Thermal momentum i
- Page 159 and 160: elative to a defined zero with prec
- Page 161 and 162: glassmaking have proven to be more
- Page 163 and 164: • Fuzzy Control Automation soluti
- Page 165 and 166: • Oxygen furnace (MPC) • Refine
- Page 167 and 168: 3.A. Submerged Combustion Melting N
- Page 169 and 170: • The Year 1 go-no-go decision po
- Page 171 and 172: splitting the fuel-oxidant mixture
- Page 173 and 174: and has proved highly reliable. The
- Page 175: The project team has agreed to form
- Page 179 and 180: Figure 3.B.1. High-Intensity Plasma
- Page 181 and 182: Key innovative components of this p
- Page 183 and 184: glass fibers at a location operated
- Page 185 and 186: Environmental Impacts The plasma ar
- Page 187 and 188: • Pressed/Blown Glass Current Siz
- Page 189 and 190: The major goal of the plasma progra
- Page 191 and 192: operations with minimum capital cos
- Page 193 and 194: However, the fundamental question r
- Page 195 and 196: control per mixer will optimize the
- Page 197 and 198: A. Literature and Patent Review—G
- Page 199 and 200: A variety of products with differen
- Page 201 and 202: steel walls, minimizing pressure lo
- Page 203 and 204: Innovative refining concepts includ
- Page 206 and 207: Appendix A1 Categorization of Liter
- Page 208 and 209: A u tt h o r // t i t l e / y e a r
- Page 210 and 211: RR e c o m m e n d C o m p a n y s
- Page 212 and 213: RR ee c o m m e n d C o m p a n y s
- Page 214 and 215: RR ee c o m m e n d C o m p a n y s
- Page 216 and 217: RR e c o m m e n d s e c oo n d l o
- Page 218 and 219: RR e c o m m e n d C o m p a n y s
- Page 220 and 221: RR e c o m m e n d C o m p a n y s
- Page 222 and 223: RR ee c o m m e n d C o m p a n y s
- Page 224 and 225: RR ee c o m m e n d C o m p a n y s
- Page 226 and 227:
RR ee c o m m e n d C o m p a n y s
- Page 228 and 229:
A u t h o r / tt i t l e / y e a r
- Page 230:
RR e c o m m e n d C o m p a n y s
- Page 233 and 234:
R e cc o mm mm ee nn dd C o mm pp a
- Page 235 and 236:
RR ee cc o m m ee n d C o mm p a n
- Page 237 and 238:
R e c o m m e nn d C o m p a n y s
- Page 239 and 240:
R ee c o m m e n d C o m p a n y s
- Page 241 and 242:
R ee c o m m ee n d C o m p a n yy
- Page 243 and 244:
R e c o m m e nn d s e c o n d l o
- Page 245 and 246:
R e c o m m ee nn d C o m p a n yy
- Page 247 and 248:
R e c o m m e nn d C o m p a n yy s
- Page 249 and 250:
R e c o m m e n d C o m p a n y s e
- Page 251 and 252:
R e c o m m e nn d s e c o n d l o
- Page 253 and 254:
R e c o m m e n d C o m p a n yy s
- Page 255 and 256:
R e c o m m e n d C o m p a n yy s
- Page 257 and 258:
cost of capital: Rate of return tha
- Page 259 and 260:
Proportional-Integral-Derivative (P
- Page 262 and 263:
Appendix C Contributors and Sponsor
- Page 264 and 265:
C.4. Special Contributors Elliott L
- Page 266:
Appendix D Technology Resource Dire
- Page 269 and 270:
Bamford, C. R., Colour Generation a
- Page 271 and 272:
Charles River Associates Incorporat
- Page 273 and 274:
Gushchin, S. N., V. B. Kutin, and P
- Page 275 and 276:
Krause, W., “Glass-melting Strate
- Page 277 and 278:
Nemec, L., “Energy Consumption in
- Page 279 and 280:
Richards, R. S., “Method and Appa
- Page 281 and 282:
“Standard Terminology of Glass an
- Page 283 and 284:
Wagnerova, S., S. Kasa, P. Jandacek
- Page 286:
Tables Table II.1. Key End-Use Mark
- Page 289 and 290:
Energy considerations for glassmaki
- Page 291 and 292:
Segmentation of glass industry, 30-