50

170-182

AVIATION gasoline by distillation of petroleum gasoline

50

223-250

“ gasoline from Hungarian petroleum

50

183-203

“ gasoline from Roumanian petroleum

50

204-222

57

177-178

BRUCHSAL middle oil processing with catalysts K 8147 and 8074

147

183-202

“ oil with HF-treated terrana, effect of thruput on

148

175-184

BUDAPEST and surroundings, report on refineries located in

15

1478-1480

CATALYTIC cracking of Austrian petroleum

146

93-100

“ cracking of Bruchsal gas oil

146

291-298

“ cracking of paraffin base gas oil (E. Texas)

146

123, 131

“ cracking of petroleum middle oils to aviation gasoline

146

784-794

“ cracking of Panuco oils

146

85-88

“ cracking of Roumanian crude oil

141

320-324

“ cracking of Roumanian crude residue

251

595-618

COMBINATION catalytic cracking and hydrogenation plant for 320,000 te/ann Russian crudes to 200,000 te/ann high test gasoline

147

123-125

“ of catalytic cracking with hydrogenating splitting of petroleum middle and heavy oils

146

237-244

147

115-122

“ processing of petroleum residues and bituminous coal A-middle oil in vapor phase, Poelitz problem of

254

253-268

COMPARISON of heavy naphtha dehydrogenation data of Nienhager crude oil at 5 and 15 atm

126

695-697

“ of hydrogenation and cracking gasolines from petroleum middle oils, by Reitz, Donath, et al

256

266-275

Translation T-374

256

275a-275j

“ “

274

967-976

“ of qualities of hydrogenation and cracking gasolines from petroleum middle oils

146

328-339

147

39-50

COMPLETE hydrogenation of petroleum fractions and waxes

127

765-768

COMPOSITION of paraffin waxes in crude oil, by I. Kagehira and H. Nakao

232

50 ’30-50 ‘37

CRACKED gasoline from hydrogen-rich petroleum middle oil

126

1269-1283

146

263-276

“ gasoline from hydrogen-rich petroleum middle oils, composition of as affected by cracking temperature

141

368-381

CRACKING residues from Laguinillas crude liquid phase middle oil, hydrogenation of over catalysts 6719 and 6434

168

180-187

“ residues, pressure hydrogenation of petroleum

75

419-451

Translation by Phil. Petr. Co.

245

10 ‘102-10 ‘108

CRUDE oil residues, catalytic pressure hydrogenation of

221

100 ’70-100 ‘72

“ oil residues, experimental hydrogenation of to Diesel oil at 600 atm

203

594-597

DECOMPOSITION in hydrogenation of petroleum fractions

80

3185-3188

DEHYDROGENATION at 15 atm and 527°C and extraction, petroleum heavy naphtha

126

672-674

“ bottoms from Poelitz petroleum, hydrogen-rich, as blending agent in 7019 gasoline

126

552-558

“ of Irac, Mid Continent and Texas heavy naphthas under hydrogen pressure with moving catalysts

126

701-715

“ of mineral oil

11

2247

14

50 ’46-50 ‘48

“ of Roumanian gasoline

251

910-918

DEHYDROGENATING Roumanian gasoline with 60% paraffins

77

445-448

DESULFURIZATION of Mosul oil

173

811-813

DEWAXING of Nienhagen residue oil

251

404-418

DHD experiments on Roumanian heavy naphtha

169

320-326

“ gasolines, conversion of Hungarian gasolines to

125

362-370

169

273-276

“ gasoline from petroleum gasoline, properties of

251

919-926

“ gasoline production from Roumanian crude

77

635-642

“ gasoline from Roumanian gasoline

256

100-101

Translation T-455

256

101a-101c

“ residues from Roumanian gasoline, treating for 87 o.n. gasoline or for DHD starting material

173

393-400

DISTILLATION and precision fractionation of Roumanian petroleum gasoline

48

798-802

DUERAG crude, refining process for, at Moosbierbaum

14

1385-1392

EDELEANU process of refining of mineral oils, art and economy of, by G. Cattaneo- Hilversum (Holland), reprint from Z. fur die gesammte Kälteindustrie, September 1928

200

10 ’49-10 ‘53