Availability
Thomas H. Fletcher and Ronald J. Pugmire
System Requirements
The CPD model was developed in FORTRAN, and has been used on numerous platforms. It has been included into several comprehensive CFD models (computational fluid dynamics). Typical stand-alone calculations are performed in
less than 1 CPU second on
a personal computer. Generally, two versions of the CPD model are available: (1) particle temperature
versus particle residence time are required input; and (2) gas
temperature and particle residence time are required input. Version
(2) solves the particle energy equation and calls the CPD model
as a subroutine. This version includes effects of convective
heating, simple radiative heat exchange with the walls, and effects
of high mass transfer.
The use of the CPD model is recommended for those technical specialists
with expertise in this technology. The CPD model was developed
as a joint research effort, and is available to all interested
parties at no cost. Should handling charges become excessive,
a small fee for copying and handling will be charged. No support
is available from ACERC in using of this model.
To obtain a copy of the code, contact:
Dr. Thomas H. Fletcher Dept. of Chemical Engineering Brigham Young University 330 EB, Provo, Utah 84602 Phone: (801) 422-2586 Fax: (801) 422-0151
E-mail: tom_fletcher@byu.edu
On-line verions of the code are available as well. Several versions are available:
Input Requirements | Original Version (1992) | NLG version |
Particle temperatures vs. time | CPD | CPD_NLG (1999)* |
Gas temperatures versus distance (requires particle velocities, solves particle energy equation) |
CPDCP | CPDCP_NLG (1999)* |
Constant particle heating rate and subsequent hold time | CPD_heat (2004) | |
Updated for a new swelling correlation | CPDCP_NLG_swell (2011) | |
Matlab version of CPD-Heat | CPD_Heat_MATLAB (2020) |
* (developed by Perry, Genetti, and Fletcher, 1999)
A summary document of the equations
and theory of the CPD model was originally written as a Sandia Technical report
(SAND92-8207; May, 1992; Available NTIS). For ease of transfer, this summary
document is available as a pdf file.
A user's manual is available also
by mail or online as a pdf file.
.
The CPD model has been distributed internationally, and has been
included into two publicly available comprehensive boiler simulation
codes, including:
Richard Buckius | Univ. of Illinois |
M. Pourkashanian | Univ. of Leeds, England |
Alan Sayre | McDermott Technologies, Inc. |
Michael Groenhout | Airflow Sciences |
Lasse Sorensen | RISO National Laboratory, Denmark |
Terry Wall | University of Newcastle, Australia |
and in PCGC-3 (Pulverized Coal Combustion and Gasification - 3-Dimensional;
developed at Brigham Young University) and Fluent (the largest commercial code
for 3-D computational fluid dynamics in the world).
The CPD model was developed by Thomas H. Fletcher and Alan R.
Kerstein at the Combustion Research Facility, Sandia National
Laboratories, Livermore, California 94551-0969, and Ronald J.
Pugmire, Mark Solum, and David M. Grant, Departments of Fuels
Engineering and Chemistry, University of Utah, Salt Lake City,
Utah 84112, with some follow-on work performed by Dr. Fletcher
where he is currently with the BYU Department of Chemical Engineering.
The research at Sandia was supported by the Department of Energy's
Pittsburgh Energy Technology Center's Direct Utilization AR&TD;Program
and the DOE Division of Engineering and Geosciences through the
Office of Basic Energy Sciences. The research at the University
of Utah was supported by the National Science Foundation through
the Advanced Combustion Engineering Research Center (ACERC) at
Brigham Young University and the University of Utah, by the Department
of Energy Division of Chemical Sciences, Office of Basic Energy
Sciences, and by the Associated Western Universities (AWU) who
provided summer faculty fellowships for Professors Pugmire and
Grant to spend time at Sandia. Funds for the ACERC center are
also received from the State of Utah, 75 industrial participants,
and the U.S. Department of Energy.
Brief Description of the CPD model