Distillation: processes – thermolytic – And adding disparate gaseous material to the carbonizing zone
Patent
1977-08-26
1979-04-10
Richman, Barry S.
Distillation: processes, thermolytic
And adding disparate gaseous material to the carbonizing zone
201 6, 201 21, 201 20, 201 22, 201 34, 201 37, 201 44, C10B 5712
Patent
active
041486927
ABSTRACT:
A process for producing calcined coke agglomerates characterized by having a low reactivity to carbon dioxide. The process includes calcining green coal agglomerates at a temperature within the range of 1700.degree. F. to 1950.degree. F. (927.degree. C. to 1066.degree. C.) in a calciner. The agglomerates are exposed to a gaseous atmosphere which before cracking contains not less than 20% by volume of at least one straight chain aliphatic hydrocarbon gas containing one to four carbon atoms. The gaseous atmosphere is preheated to a temperature within the range of 200.degree. F. to 700.degree. F.(93.degree. C. to 371.degree. C.) prior to being introduced into the calciner. Carbon produced when the hydrocarbon gas is cracked, is deposited as vitreous carbon on the surfaces, in the fissures and in the pores of the agglomerates. The calcined coke aggglomerates discharged from the calciner have a reactivity to carbon dioxide of between 2% to 8%.
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Benedict Louis G.
Chu Vincent H. K.
Fox Sidney V.
Bethlehem Steel Corporation
O'Keefe Joseph J.
Richman Barry S.
Simitz John S.
Wilkinson Charles A.
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