| 289 - 290 |
An acceptable scenario for oil shale industry
Reinsalu E |
| 291 - 301 |
Dictyonema shale and uranium processing at Sillamae
Lippmaa E, Maremae E |
| 303 - 313 |
Reactivity of oil shale ashes towards sulfur dioxide - 3. Recurrent use of ash for flue gas purification
Kuusik R, Kaljuvee T, Veskimae H, Roundygin Y, Keltman A |
| 315 - 329 |
Long-term deposition patterns of airborne wastes in the North-East of Estonia
Kaasik M, Liblik V, Kaasik H |
| 331 - 336 |
Upgrading of estonian shale oil distillation fractions - 3. Hydrogenation of light mazute
Luik H, Maripuu L, Vink N, Lindaru E |
| 337 - 342 |
Upgrading of Estonian shale oil distillation fractions - 4. The effect of time and hydrogen pressure on the yield and composition of light mazute hydrogenation products
Luik H, Vink N, Lindaru E, Maripuu L |
| 343 - 349 |
Comparative characterization of semicoking oils obtained from rubber wastes and from co-processing of kukersite oil shale and rubber wastes in solid heat-carrier unit
Vysotskaya V, Liiv M, Kann J |
| 350 - 358 |
Influence of different factors on hydrogen ion exponent (pH) of the tar water from Kiviter vertical retorts
Yefimov V, Doilov S |
| 359 - 368 |
Viscosity of SHC process shale oil binary blends
Molder L, Loit M, Tamvelius H, Tiikma L |
| 369 - 376 |
Condensation of methylolphenols
Christjanson P, Koosel A, Suurpere A |
