HYDROGENATING SHALE OIL TO CATALYTIC REFORMING STOCK

[1] COMPOSITION OF COLORADO SHALE-OIL NAPHTHA [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1949, 41 (03): : 581 - 587

[2] BALL JS, 1954, BUR MINES ADM PUBL, P47

[3] HYDROFINING THERMALLY CRACKED SHALE-OIL NAPHTHA [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1956, 48 (07): : 1146 - 1151

[4] CRECELIUS RL, 1956, PETROL REFINER, V35, P171

[5] DINNEEN GU, 1954, PETROL REFINER, V33, P113

[6] COMPOSITION OF CRUDE SHALE OILS [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1952, 44 (11): : 2632 - 2635

[7] HOOG H, 1951, OIL SHALE CANNEL COA, V2, P562

[8] SHALE OIL REFINING [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1951, 43 (01): : 27 - 32

[9] EQUIVALENT ISOTHERMAL TEMPERATURES FOR NONISOTHERMAL REACTORS [J]. AICHE JOURNAL, 1955, 1 (04) : 528 - 530

[10] MURPHY WIR, 1954, BUR MINES ADM PUBL, P111

[1] COMPOSITION OF COLORADO SHALE-OIL NAPHTHA [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1949, 41 (03): : 581 - 587

[2] BALL JS, 1954, BUR MINES ADM PUBL, P47

[3] HYDROFINING THERMALLY CRACKED SHALE-OIL NAPHTHA [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1956, 48 (07): : 1146 - 1151

[4] CRECELIUS RL, 1956, PETROL REFINER, V35, P171

[5] DINNEEN GU, 1954, PETROL REFINER, V33, P113

[6] COMPOSITION OF CRUDE SHALE OILS [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1952, 44 (11): : 2632 - 2635

[7] HOOG H, 1951, OIL SHALE CANNEL COA, V2, P562

[8] SHALE OIL REFINING [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1951, 43 (01): : 27 - 32

[9] EQUIVALENT ISOTHERMAL TEMPERATURES FOR NONISOTHERMAL REACTORS [J]. AICHE JOURNAL, 1955, 1 (04) : 528 - 530

[10] MURPHY WIR, 1954, BUR MINES ADM PUBL, P111