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Title: Detailed project plan: Design, construction and operation of pilot scale Charfuel{reg_sign} process. Topical report, Task 2

Abstract

In this project, a pilot-scale facility for the flash hydropyrolysis of coal will be designed, built and operated to demonstrate the integrated operation of critical components of the CHARFUEL process and to obtain scale-up data for subsequent demonstration facility for the production of a clean coal slurry fuel. This report presents project plans which includes detailed construction plan; procurement of materials and equipment; construction, test and start-up; potential problems and solutions during operations; data collection and analysis; and feasibility analysis.

Publication Date:
Research Org.:
USDOE Morgantown Energy Technology Center, WV (United States); CHAR-FUELS Associates Ltd., Englewood, CO (United States)
Sponsoring Org.:
USDOE, Washington, DC (United States)
OSTI Identifier:
10182425
Report Number(s):
DOE/MC/29268-3401
ON: DE93040035
DOE Contract Number:
FC21-92MC29268
Resource Type:
Technical Report
Resource Relation:
Other Information: PBD: [1993]
Country of Publication:
United States
Language:
English
Subject:
01 COAL, LIGNITE, AND PEAT; COAL; PYROLYSIS; HYDROGENATION; PLANNING; DESIGN; CONSTRUCTION; PILOT PLANTS; OPERATION; 010409; PYROLYSIS AND CARBONIZATION

Citation Formats

Not Available. Detailed project plan: Design, construction and operation of pilot scale Charfuel{reg_sign} process. Topical report, Task 2. United States: N. p., 1993. Web. doi:10.2172/10182425.
Not Available. Detailed project plan: Design, construction and operation of pilot scale Charfuel{reg_sign} process. Topical report, Task 2. United States. doi:10.2172/10182425.
Not Available. 1993. "Detailed project plan: Design, construction and operation of pilot scale Charfuel{reg_sign} process. Topical report, Task 2". United States. doi:10.2172/10182425. https://www.osti.gov/servlets/purl/10182425.
@article{osti_10182425,
title = {Detailed project plan: Design, construction and operation of pilot scale Charfuel{reg_sign} process. Topical report, Task 2},
author = {Not Available},
abstractNote = {In this project, a pilot-scale facility for the flash hydropyrolysis of coal will be designed, built and operated to demonstrate the integrated operation of critical components of the CHARFUEL process and to obtain scale-up data for subsequent demonstration facility for the production of a clean coal slurry fuel. This report presents project plans which includes detailed construction plan; procurement of materials and equipment; construction, test and start-up; potential problems and solutions during operations; data collection and analysis; and feasibility analysis.},
doi = {10.2172/10182425},
journal = {},
number = ,
volume = ,
place = {United States},
year = 1993,
month = 9
}

Technical Report:

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  • This document is the third interim report on tests that were conducted at the Duct Injection Test Facility (DITF) operated for the Department of Energy at Unit 5 of the Ohio Power Company's Muskingum River station in Beverly, Ohio. At the DITF dry calcium hydroxide (Ca(OH)2), an aqueous slurry of Ca(OH)[sub 2] (prepared by slaking quicklime), or a mixture of one of these sorbents with waste ash from earlier tests was injected into a slipstream of flue gas from the Unit 5 boiler to achieve partial removal of SO[sub 2] in the flue gas. Up to 50,000 acfm of fluemore » gas was taken from the inlet to the Unit 5 electrostatic precipitator (ESP) for these tests. Water was injected separately with the dry sorbent or as part of the slurry to cool the flue gas and increase the water vapor content of the flue gas. The addition of water, either as a separate spray or in the slurry makes the reaction between the sorbent and the SO[sub 2] more complete; the presumption is that water is effective in the liquid state when it can physically wet the sorbent particles, and not especially effective in the vapor state. Higher values of calcium utilization were obtained with slurry injection than with dry sorbent injection and humidification. Slurries made from reagent slaked lime, mixtures of reagent slaked lime and recycle ash, and from recycle ash alone were injected through the same nozzles used for humidification. The focus of most of these tests was on the constant addition of recycle ash to reduce the amount of slaked lime required for SO[sub 2] removal (for best economics). Testing was continued until the amount of Ca(OH)[sub 2] in the recycle ash equaled that predicted for equilibrium Two test cases were evaluated: a low Ca/S ratio (1.0 reagent, 44[degrees]/F approach) for 50% SO[sub 2] removal and a high Ca/S ratio (1.7 reagent, 24[degrees]F approach) for 88% SO[sub 2] removal.« less
  • This document is the third interim report on tests that were conducted at the Duct Injection Test Facility (DITF) operated for the Department of Energy at Unit 5 of the Ohio Power Company`s Muskingum River station in Beverly, Ohio. At the DITF dry calcium hydroxide (Ca(OH)2), an aqueous slurry of Ca(OH){sub 2} (prepared by slaking quicklime), or a mixture of one of these sorbents with waste ash from earlier tests was injected into a slipstream of flue gas from the Unit 5 boiler to achieve partial removal of SO{sub 2} in the flue gas. Up to 50,000 acfm of fluemore » gas was taken from the inlet to the Unit 5 electrostatic precipitator (ESP) for these tests. Water was injected separately with the dry sorbent or as part of the slurry to cool the flue gas and increase the water vapor content of the flue gas. The addition of water, either as a separate spray or in the slurry makes the reaction between the sorbent and the SO{sub 2} more complete; the presumption is that water is effective in the liquid state when it can physically wet the sorbent particles, and not especially effective in the vapor state. Higher values of calcium utilization were obtained with slurry injection than with dry sorbent injection and humidification. Slurries made from reagent slaked lime, mixtures of reagent slaked lime and recycle ash, and from recycle ash alone were injected through the same nozzles used for humidification. The focus of most of these tests was on the constant addition of recycle ash to reduce the amount of slaked lime required for SO{sub 2} removal (for best economics). Testing was continued until the amount of Ca(OH){sub 2} in the recycle ash equaled that predicted for equilibrium Two test cases were evaluated: a low Ca/S ratio (1.0 reagent, 44{degrees}/F approach) for 50% SO{sub 2} removal and a high Ca/S ratio (1.7 reagent, 24{degrees}F approach) for 88% SO{sub 2} removal.« less
  • Project CFB was initiated at the University of North Dakota Energy and Environmental Research Center (EERC) in May 1988. Specific goals of the project were to (1) construct a circulating fluidized-bed combustor (CFBC) facility representative of the major boiler vendors` designs with the capability of producing scalable data, (2) develop a database for use in making future evaluations of CFBC technology, and (3) provide a facility for evaluating fuels, free of vendor bias for use in the - energy industry. Five coals were test-burned in the 1-MWth unit: North Dakota and Asian lignites, a Wyoming subbituminous, and Colorado and Pennsylvaniamore » bituminous coats. A total of 54 steady-state test periods were conducted, with the key test parameters being the average combustor temperature, excess air, superficial gas velocity, calcium-to-sulfur molar ratio, and the primary air-to-secondary air split. The capture for a coal fired in a CFBC is primarily dependent upon the total alkali-to-sulfur ratio. The required alkali-to ratio for 90% sulfur retention ranged from 1.4 to 4.9, depending upon coal type. While an alkali-to-ratio of 4.9 was required to meet 90% sulfur retention for the Salt Creek coal versus 1.4 for the Asian lignite, the total amount of sorbent addition required is much less for the Salt Creek coal, 4.2 pound sorbent per million Btu coal input, versus 62 pound/million Btu for the Asian lignite. The bituminous coals tested show optimal capture at combustor temperatures of approximately 1550{degree}F, with low-rank coals having optimal sulfur capture approximately 100{degree}F lower.« less
  • This manual establishes the general safety requirements for all plant activities and operations. The safety rules and regulations prescribe safe methods and procedures for insuring continuity of operations, safeguarding personnel, and preventing property damage. All plant safety programs will be continuously evaluated to insure that the minimum requirements of the program are always present.