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Title: Effect of furnace operating conditions on alkali vaporization, batch carryover, and the formation of SO2 and NO in an oxy-fuel fired container glass furnace.

Abstract

No abstract prepared.

Authors:
;  [1];  [2]; ;  [3]
  1. (University of Alabama , Birmingham, AL)
  2. (Sandia National Laboratories, Livermore, CA)
  3. (Gallo Glass Company, Modesto, CA)
Publication Date:
Research Org.:
Sandia National Laboratories
Sponsoring Org.:
USDOE
OSTI Identifier:
964577
Report Number(s):
SAND2006-0498J
TRN: US200921%%35
DOE Contract Number:
AC04-94AL85000
Resource Type:
Journal Article
Resource Relation:
Journal Name: Proposed for publication in Glass Science and Technology.
Country of Publication:
United States
Language:
English
Subject:
32 ENERGY CONSERVATION, CONSUMPTION, AND UTILIZATION; ALKALI METALS; EVAPORATION; FURNACES; GLASS INDUSTRY; SYNTHESIS; SULFUR DIOXIDE; NITRIC OXIDE; PROCESS CONTROL

Citation Formats

Molina, Alejandro, Walsh, Peter M., Shaddix, Christopher R., Blevins, Linda Gail, and Neufeld, John W.. Effect of furnace operating conditions on alkali vaporization, batch carryover, and the formation of SO2 and NO in an oxy-fuel fired container glass furnace.. United States: N. p., 2006. Web.
Molina, Alejandro, Walsh, Peter M., Shaddix, Christopher R., Blevins, Linda Gail, & Neufeld, John W.. Effect of furnace operating conditions on alkali vaporization, batch carryover, and the formation of SO2 and NO in an oxy-fuel fired container glass furnace.. United States.
Molina, Alejandro, Walsh, Peter M., Shaddix, Christopher R., Blevins, Linda Gail, and Neufeld, John W.. Sun . "Effect of furnace operating conditions on alkali vaporization, batch carryover, and the formation of SO2 and NO in an oxy-fuel fired container glass furnace.". United States. doi:.
@article{osti_964577,
title = {Effect of furnace operating conditions on alkali vaporization, batch carryover, and the formation of SO2 and NO in an oxy-fuel fired container glass furnace.},
author = {Molina, Alejandro and Walsh, Peter M. and Shaddix, Christopher R. and Blevins, Linda Gail and Neufeld, John W.},
abstractNote = {No abstract prepared.},
doi = {},
journal = {Proposed for publication in Glass Science and Technology.},
number = ,
volume = ,
place = {United States},
year = {Sun Jan 01 00:00:00 EST 2006},
month = {Sun Jan 01 00:00:00 EST 2006}
}
  • Computer models for coal combustion are not sufficiently accurate to enable the design of pulverized coal fired furnaces or the selection of coal based on combustion behavior. Most comprehensive combustion models can predict with reasonable accuracy flow fields and heat transfer but usually with a much lesser degree of accuracy than the combustion of coal particles through char burnout. Computational fluid dynamics (CFD) modeling is recognized widely to be a cost-effective, advanced tool for optimizing the design and operating condition of the pulverized coal-fired furnaces for achieving cleaner and efficient power generation. Technologists and researchers are paying remarkable attention tomore » CFD because of its value in the pulverized fuel fired furnace technology and its nonintrusiveness, sophistication, and ability to significantly reduce the time and expense involved in the design, optimization, trouble-shooting, and repair of power generation equipment. An attempt to study the effect of one of the operating conditions, i.e., burner tilts on coal combustion mechanisms, furnace exit gas temperature (FEGT), and heat flux distribution pattern, within the furnace has been made in this paper by modeling a 210 MW boiler using commercial CFD code FLUENT. 5 refs., 8 figs.« less
  • Abstract not provided.
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