Anode coke from low ash coal

Matthew Weisenberger; Rodney Andrews; John Craddock; Terry Rantell; David Whitlow; John Wiseman; James C. Hower

Anode coke from low ash coal

Matthew Weisenberger, Rodney Andrews, John Craddock, Terry Rantell, David Whitlow, John Wiseman, James C. Hower

Research output: Contribution to conference › Paper › peer-review

Abstract

• Low Ash Coal ∼ 1 % • Oil agglomeration was unsuccessful to reduce ash < 0.1 % • Digest in decant oil: • (2:1) solvent:coal, 400 °C, 30 min → 80 - 90 % soluble DAF • Coked at 380 °C (2.5 hr) → 500 °C, Calcined to 1300 °C • Total Coke Yield from coal digests ∼ 35 % • Total Coke Yield from neat solvent ∼ 12 % • Low Sulfur • Coke from coal digests ∼ 0.6 % • Low V and Ni • Coke from coal digests ∼ 10 - 30 ppm • High ash metals (over spec) • Si, Fe, Ca, Na • Optical anisotropy: • Coke from coal digest - Bimodal (fine mosaic, some long range) - Ash • except in anthracene oil (all small, native QI) Lower ash coal digests could be a lower-cost additive to traditional anode pet coke constituents to lower the S content.

Original language	English
State	Published - 2017
Event	34th Annual International Pittsburgh Coal Conference: Coal - Energy, Environment and Sustainable Development, PCC 2017 - Pittsburgh, United States Duration: Sep 5 2017 → Sep 8 2017

Conference

Conference	34th Annual International Pittsburgh Coal Conference: Coal - Energy, Environment and Sustainable Development, PCC 2017
Country/Territory	United States
City	Pittsburgh
Period	9/5/17 → 9/8/17

Bibliographical note

Publisher Copyright:
© 2017 International Pittsburgh Coal Conference. All rights reserved.

ASJC Scopus subject areas

Geochemistry and Petrology
Geotechnical Engineering and Engineering Geology
Energy Engineering and Power Technology

Cite this

@conference{9a7af0bbe56f4592ad5c6031e4e86f76,

title = "Anode coke from low ash coal",

abstract = "• Low Ash Coal ∼ 1 % • Oil agglomeration was unsuccessful to reduce ash < 0.1 % • Digest in decant oil: • (2:1) solvent:coal, 400 °C, 30 min → 80 - 90 % soluble DAF • Coked at 380 °C (2.5 hr) → 500 °C, Calcined to 1300 °C • Total Coke Yield from coal digests ∼ 35 % • Total Coke Yield from neat solvent ∼ 12 % • Low Sulfur • Coke from coal digests ∼ 0.6 % • Low V and Ni • Coke from coal digests ∼ 10 - 30 ppm • High ash metals (over spec) • Si, Fe, Ca, Na • Optical anisotropy: • Coke from coal digest - Bimodal (fine mosaic, some long range) - Ash • except in anthracene oil (all small, native QI) Lower ash coal digests could be a lower-cost additive to traditional anode pet coke constituents to lower the S content.",

author = "Matthew Weisenberger and Rodney Andrews and John Craddock and Terry Rantell and David Whitlow and John Wiseman and Hower, {James C.}",

note = "Publisher Copyright: {\textcopyright} 2017 International Pittsburgh Coal Conference. All rights reserved.; 34th Annual International Pittsburgh Coal Conference: Coal - Energy, Environment and Sustainable Development, PCC 2017 ; Conference date: 05-09-2017 Through 08-09-2017",

year = "2017",

language = "English",

}

TY - CONF

T1 - Anode coke from low ash coal

AU - Weisenberger, Matthew

AU - Andrews, Rodney

AU - Craddock, John

AU - Rantell, Terry

AU - Whitlow, David

AU - Wiseman, John

AU - Hower, James C.

PY - 2017

Y1 - 2017

N2 - • Low Ash Coal ∼ 1 % • Oil agglomeration was unsuccessful to reduce ash < 0.1 % • Digest in decant oil: • (2:1) solvent:coal, 400 °C, 30 min → 80 - 90 % soluble DAF • Coked at 380 °C (2.5 hr) → 500 °C, Calcined to 1300 °C • Total Coke Yield from coal digests ∼ 35 % • Total Coke Yield from neat solvent ∼ 12 % • Low Sulfur • Coke from coal digests ∼ 0.6 % • Low V and Ni • Coke from coal digests ∼ 10 - 30 ppm • High ash metals (over spec) • Si, Fe, Ca, Na • Optical anisotropy: • Coke from coal digest - Bimodal (fine mosaic, some long range) - Ash • except in anthracene oil (all small, native QI) Lower ash coal digests could be a lower-cost additive to traditional anode pet coke constituents to lower the S content.

AB - • Low Ash Coal ∼ 1 % • Oil agglomeration was unsuccessful to reduce ash < 0.1 % • Digest in decant oil: • (2:1) solvent:coal, 400 °C, 30 min → 80 - 90 % soluble DAF • Coked at 380 °C (2.5 hr) → 500 °C, Calcined to 1300 °C • Total Coke Yield from coal digests ∼ 35 % • Total Coke Yield from neat solvent ∼ 12 % • Low Sulfur • Coke from coal digests ∼ 0.6 % • Low V and Ni • Coke from coal digests ∼ 10 - 30 ppm • High ash metals (over spec) • Si, Fe, Ca, Na • Optical anisotropy: • Coke from coal digest - Bimodal (fine mosaic, some long range) - Ash • except in anthracene oil (all small, native QI) Lower ash coal digests could be a lower-cost additive to traditional anode pet coke constituents to lower the S content.

UR - http://www.scopus.com/inward/record.url?scp=85047189035&partnerID=8YFLogxK

UR - http://www.scopus.com/inward/citedby.url?scp=85047189035&partnerID=8YFLogxK

M3 - Paper

AN - SCOPUS:85047189035

T2 - 34th Annual International Pittsburgh Coal Conference: Coal - Energy, Environment and Sustainable Development, PCC 2017

Y2 - 5 September 2017 through 8 September 2017

ER -

Anode coke from low ash coal

Abstract

Conference

Bibliographical note

ASJC Scopus subject areas

Other files and links

Fingerprint

Cite this