| Production and Refining of Gasolines | ||||
| TOM Reel |
Bag | Item | Frames | |
|
GASOLINE from coal |
165 |
597-643 |
||
|
737-763 |
||||
|
Illegible |
772-773 |
|||
|
783-817 |
||||
|
824-856 |
||||
|
167 |
999-1009 |
|||
|
“ production (radio speech by Dr. Pier) |
118 |
0 ‘1-0 ‘9 |
||
|
GELSENBERG catalytic cracking plant, L-gasoline from |
162 |
107-110 |
||
|
GERMAN distilled gasoline, aviation gasoline from |
221 |
90 ‘101-90 ‘103 |
||
|
HIGH anti-knock fuel status at end of December 1940 |
23 |
12..109-12..125 |
||
|
“ anti-knock isoparaffin motor fuels, preparation of, by alkylation of aliphatic hydrocarbons, by Pohl |
138 |
III |
0 ‘3-0 ‘37 |
|
|
“ -test gasolines, accelerated production of |
212 |
30 ‘86-30 ‘94 |
||
|
“ -test motor fuel from petroleum |
126 |
583-586 |
||
|
HYDROGENATION gas fractions, high octane gasoline from |
14 |
1314-1319 |
||
|
“ of brown coal tar, L-gasoline by |
162 |
29-30 |
||
|
“ of residual oils, gasoline from; plant and products |
14 |
1331-1339 |
||
|
INCREASED yield in combination process, L-gasoline |
162 |
104-106 |
||
|
ISOPARAFFIN and their use as motor fuels, most important data and preparation methods of some |
138 |
VIII |
0 ‘63-0 ‘64 |
|
|
LEAD tetraethyl content of B4, lowering by precipitation with hydrochloric acid |
212 |
20 ‘1-20 ‘18 |
||
|
20 ‘24-20 ‘29 |
||||
|
20 ‘41-20 ‘44 |
||||
|
LIGHT gasoline, production of |
148 |
573-582 |
||
|
“ gasolines, production of, under different pressures |
221 |
90 ‘104-90 ‘106 |
||
|
L GASOLINE (O.N. 100), report on production of, 1939 |
212 |
30 ‘98-30 ‘122 |
||
|
MICHAEL naphtha, refining of |
166 |
816-817 |
||
|
MIDDLE oil, gasoline from |
167 |
937-947 |
||
|
1018-1022 |
||||
|
MIDDLE oil, gasoline production from |
190 |
23597-23617 |
||
|
23876-23903 |
||||
|
OCTANE rating of hydrogenation gasoline, improving by closer fractionating |
216 |
10 ‘12-10 ‘20 |
||
|
OPPAU alcohols, hydrogenation of to -110° gasoline |
173 |
843-846 |
||
|
PLANT and operations details, Schaffgotsch |
49 |
175-262 |
||
|
PRODUCTION, conversion of gasoline from endpoint 150 to endpoint 180°C |
173 |
1-2 |
||
|
12-13 |
||||
|
202 |
588-589 |
|||
|
212 |
20 ‘37-20 ‘40 |
|||
|
213 |
50 ‘28-50 ‘55 |
|||
|
PRODUCTION methods, correspondence on various gasoline |
210 |
50 ‘3-50 ‘32 |
||
|
“ records, 1932-1934, miscellaneous |
115 |
50 ‘9-50 ‘17 |
||
|
“ situation, gasoline, discussion of, February 1944 |
177 |
1921-1922 |
||
|
REFINING of gasoline, November 1944 |
40 |
3453 |
24 |
30 ‘1-30 ‘9 |
|
RUSSIAN gasolines, improving various |
173 |
682-691 |
||
|
“ gasoline, processing of |
173 |
666-680 |
||
|
Do. |
202 |
201-207 |
||
|
SKETCH CS 183a of Arobin plant |
194 |
30264 |
||
|
SOYA bean oil, studies on manufacture of aviation gasoline from, by N. Sakota |
231 |
30 ‘36-30 ‘43 |
||
|
SULFURIC acid, engineering experience in working up of, by Ihlenburg |
193 |
23283-23297 |
||
|
“ acid recovery, by Menschick |
193 |
23272-23282 |
||
|
“ acid recovery plant, equipment and operation of, by Milz |
193 |
23298-23308 |
||
|
TAR, gasoline from |
167 |
1023 |
||
|
TWO stages, gasoline production in |
165 |
415-418 |
||