Fluidized and allied carbonization processes developed abroad are reviewed. The processes developed by Pittsburgh Consolidation Coal Co., Institute of Gas Technology, Bureau of Mines and United Engineers and Constructors Inc., are described. The first two processes propose to treat both non-caking as well as caking coals with the object of producing semi-coked char for blanding and power generation. The Bureau of Mines process which has been developed commercially is limited to coals with oxygen content above 12%, heating value less than 14250 B.t.u./lb. on pure coal basis. The process developed by United Engineers & Constructors Inc., operates continuously with any coal but it has not been tried on any large plant. The two processes develo...
The history of development of coal gasification technologies is reviewed. The basic fea- ...
This progress report is divided into two parts. In Part A, the results of the first three progress r...
Three different Western Canadian coals were gasified with air and steam in a fluidized bed of 0.73 m...
The authors describe in this paper batchwise carbonization of Jambad-Bowlah coal at 480-510ºC in a 2...
IN 1948, CERCHAR, (the Centre d'Etudes et de Recherches des Charbonnages de France), star...
This paper reports the work done on fluidized carbonization of non-caking coals from Raniganj field,...
Considering the future demand gor hydrogen, advanced coal gasification technology is a promising alt...
This report is a final brief summary of development of a mild-gasification and char conversion proce...
The properties of fluidized beds can be drastically altered by the insertion of various types of int...
Thesis (M.S.) Massachusetts Institute of Technology. Dept. of Chemical Engineering, 1945.Bibliograph...
The paper presents a global review on the advances in the field of high temperature carbonization un...
Char, the major co-product of mild coal gasification, represents about 70 percent of the total produ...
© 1955 G. L. KennedyAfter the successful production of hard charfrom Yallourn brown coal had been de...
Three different Western Canadian coals were gasified with air and steam in a fluidized bed of 0.73 m...
Morgantown Energy Technology Center (METC) of DOE has sponsored, and continues to sponsor, programs ...
The history of development of coal gasification technologies is reviewed. The basic fea- ...
This progress report is divided into two parts. In Part A, the results of the first three progress r...
Three different Western Canadian coals were gasified with air and steam in a fluidized bed of 0.73 m...
The authors describe in this paper batchwise carbonization of Jambad-Bowlah coal at 480-510ºC in a 2...
IN 1948, CERCHAR, (the Centre d'Etudes et de Recherches des Charbonnages de France), star...
This paper reports the work done on fluidized carbonization of non-caking coals from Raniganj field,...
Considering the future demand gor hydrogen, advanced coal gasification technology is a promising alt...
This report is a final brief summary of development of a mild-gasification and char conversion proce...
The properties of fluidized beds can be drastically altered by the insertion of various types of int...
Thesis (M.S.) Massachusetts Institute of Technology. Dept. of Chemical Engineering, 1945.Bibliograph...
The paper presents a global review on the advances in the field of high temperature carbonization un...
Char, the major co-product of mild coal gasification, represents about 70 percent of the total produ...
© 1955 G. L. KennedyAfter the successful production of hard charfrom Yallourn brown coal had been de...
Three different Western Canadian coals were gasified with air and steam in a fluidized bed of 0.73 m...
Morgantown Energy Technology Center (METC) of DOE has sponsored, and continues to sponsor, programs ...
The history of development of coal gasification technologies is reviewed. The basic fea- ...
This progress report is divided into two parts. In Part A, the results of the first three progress r...
Three different Western Canadian coals were gasified with air and steam in a fluidized bed of 0.73 m...