| Main Title |
Study of Chemically Active Fluid Bed Gasifier for Reduction of Sulfur Oxide Emissions. |
| Author |
Crai, J. W. T. ;
Johne, G. L. ;
Mos, G. ;
Taylo, J. H. ;
Tisdal, D. E. ;
|
| CORP Author |
Esso Research Centre, Abingdon (England). |
| Year Published |
1972 |
| Report Number |
CPA-70-46; R2-72-020; |
| Stock Number |
PB-211 438 |
| Additional Subjects |
( Fuel oil ;
Desulfurization) ;
( Limestone ;
Adsorbents) ;
( Air pollution ;
Sulfur dioxide) ;
( Sulfur inorganic compounds ;
Adsorption) ;
( Fluidized bed processors ;
Air pollution control equipment) ;
( Furnaces ;
Air pollution control equipment) ;
Calcium oxides ;
Gasification ;
Materials recovery ;
Great Britain ;
Combustion products ;
Design ;
Vanadium ;
Scale(Corrosion) ;
Regeneration(Engineering) ;
Pilot plants ;
Performance evaluation ;
Chemically Active Fluid Bed Process ;
Air pollution control ;
Waste gas recovery
|
| Holdings |
| Library |
Call Number |
Additional Info |
Location |
Last
Modified |
Checkout
Status |
| NTIS |
PB-211 438 |
Some EPA libraries have a fiche copy filed under the call number shown. |
|
07/26/2022 |
|
| Collation |
347p |
| Abstract |
The Chemically Active Fluid Bed (CAFB) process involves the desulfurization of a fuel oil using a hot fluidized bed of lime to oxidize and gasify the oil. The lime is then regenerated and reused. The present report discusses the following: Survey operating characteristics of two limestones and one residual fuel oil to determine their suitability; Select the best of the two stones for further testing; Construct two new batch reactor CAFB laboratory experimental units; Measure the effects of important operating variables on the CAFB process using batch reactor experiments with the selected oil-limestone combination; Operate for 200 hours of gasification a continuous CAFB gasification pilot plant. |
