THERMAL PHENOMENA |
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TOM REEL |
BAG |
ITEM |
FRAMES |
|
ALCOHOL still, heat transfer conditions in |
118 |
20 ‘110-20 ‘121 |
||
ALKALI dehydrogenation of primary alcohols, heats of reaction of, by Geib |
193 |
23431-23434 |
||
ALUMINUM oxide plates, heat transfer coefficient of |
46 |
3446 |
761-763 |
|
BOMBS similar to combustion chambers, heat transfer losses in |
93 |
1022-1029 |
||
BUTADIENE synthesis, summary of heats of reaction for compounds entering into |
31 |
2078 |
1..15-1..22 |
|
BUTENEDIOL, heat of formation of |
31 |
2078 |
8..52-8..74 |
|
CATALYST tube, heat transfer in high pressure |
118 |
60 ’31-60 ‘50 |
||
“ tube, heat transmission and distribution in 250 mm |
103-II |
7253-7270 |
||
CATALYTIC polymerization of olefin-containing liquefied gases, heat transfer experiments in high pressure plant for |
109 |
9100-9134 |
||
“ reactions, heat transfer problems in |
190 |
23585-23595 |
||
COAL paste, heat exchange of |
201 |
540-542 |
||
218 |
90 ’52-90 ‘55 |
|||
“ paste, measurements of heat transfer in |
201 |
157-158 |
||
COOLANTS, heat conductivity, specific heat and heat transfer of |
111 |
11069-11071 |
||
COOLING down and heating up processes, theory of, by Pfriem |
172 |
331-358 |
||
DEHYDROGENATION, calculation of heat of reaction of, by Dr. Donath |
164 |
133-142 |
||
DILUTION of hydrochloric acid, heat of, diagram |
24 |
3391 |
46 |
|
“ of sulfuric acid, heat of, diagram |
24 |
3391 |
45 |
|
EQUATIONS of state of real gases and their use for calculating Joule-Thomson effect on hydrogen |
174 |
560-570 |
||
FINNED tubes in grouped arrangement |
111 |
11043-11047 |
||
FISCHER hydrocarbon synthesis, heat relationships in |
26 |
10..424-10..480 |
||
HEAT balance and temperature relationships in liquid phase, Scholven III |
11 |
2247 |
9 |
40 ’25-40 ‘31 |
Translation T-39 |
237 |
20 ’13-20 ‘18 |
||
“ balances in liquid phase stall, actual and ideal |
214 |
30 ’96-30 ‘99 |
||
“ conduction in periodically changing (quasi stationary) temperature fields, theory of, thesis by Pfriem |
172 |
293-323 |
||
“ conductivity of catalysts |
46 |
3446 |
66-69 |
|
“ conductivity of vessels |
182 |
7935-7940 |
||
“ efficiency of hydrogenation |
181 |
6633-6636 |
||
Translation T-48 |
237 |
30 ’56-30 ‘58 |
||
“ engineering |
118 |
50 ’13-50 ‘120 |
||
60 ‘1-60 ‘19 |
||||
“ of combustion of uncommon fuels, theoretical computation of |
112 |
513-522 |
||
“ of polymerization of gasol, determination of |
16 |
2628-2647 |
||
107 |
29214-29232 |
|||
“ of reaction, drawing to report on, Scholven, BK 187-16 |
89 |
2243 |
5 |
40 ‘42 |
“ of reaction during polymerization of olefins, December 5, 1938 |
106 |
28976-28979 |
||
“ problems, discussions of |
19 |
174.3017-174.3100 |
||
“ transfer and heat transfer numbers |
71 |
178-179 |
||
“ transfer number, variations of from November 1941 to October 1942 in one stall, Poelitz |
78 |
42-43 |
||
HEAT transfer coefficient of preheater, approximate calculations of |
162 |
572-576 |
||
Translation T-61 |
237 |
40 ’41-40 ‘45 |
||
“ transfer coefficient of spiral regenerator filling, Kislorod 1947, No. 3, pp. 28-35, in Russian |
258 |
60 ‘9-60 ‘12 |
||
“ transfer measurements with engine cooler using different coolants |
111 |
11055-11060 |
||
“ transfer, principles of and design of heat exchangers |
32-II |
2078 |
242.1800-242.181* |
|
“ transfer values of heat exchanger and preheater of Welheim extract hydrogenation stall, by H. Schappert |
9 |
2733 |
10 |
30 ’85-30 ‘93 |
HIGH pressure synthesis installations, heat transfer problems in |
188 |
20174-20224 |
||
“ “ , high temperature heating at 250 atm, reported by E. W. Halbach |
240 |
30 ’43-30 ‘51 |
||
“ “ tubes 160 mm i.d. with fins 340 x 400 mm, measurement of heat transfer of |
111 |
11072-11079 |
||
“ “ tubes with expansion fins, determination of outward heat transfer values of |
111 |
11036-11042 |
||
“ “ tubes with slipped-on fins, determination of outward heat transfer values of |
111 |
11027-11035 |
||
HOT gas recycle (vapor phase), removal of heat of reaction by |
201 |
65-67 |
||
214 |
30 ’33-30 ‘40 |
|||
HYDROGENATION, heats of reaction of, hydrogen requirements |
162 |
373-376 |
||
“ of Silesian bituminous coal, heat transfer characteristics during |
145 |
108 |
||
IRON sulfide-crusted high pressure pipe, report on heat transfer of |
103-II |
7175-7182 |
||
METHANOL synthesis, heat of reaction and thermodynamic equilibrium of |
192 |
22272-22279 |
||
OILS, heat conductivity and specific heat of |
111 |
11048-11054 |
||
OUTSIDE heat exchange in high pressure tubes, measurement of |
109 |
8794-8810 |
||
PERIODIC heat transfer, problems of with reference to piston engines |
172 |
367-380 |
||
PIPES with welded or pressed fins, heat transfer by |
103-II |
7146-7156 |
||
RAPIDLY changing temperatures of gases and liquids, measurement of, by Pfriem |
172 |
259-366 |
||
SHIFT reaction at Auschwitz, heat balance in |
2 |
2168 |
10 |
10 ’77-10 ‘85 |
SPECIFIC heat of coal paste and middle oil |
11 |
9 |
40 ’32-40 ‘35 |
|
Translation T-34 |
237 |
10 ‘111-10 ‘114 |
||
“ heats, average, of diatomic gases, CO2 and steam. Reprint from Zeitschrift fur Technikal Physik, 1928. Illegible. |
213 |
40’42-40 ‘53 |
||
“ heats of coal paste, middle oils, gasolines and technical gases |
164 |
417-427 |
||
TAR, heat of evaporation and condensation of |
189 |
20977-20987 |
||
TEMPERATURE dependence of reactions which occur in hydrogenation of bituminous coal liquefaction middle oil over 5058, 7846 and 8376 (7846 W 250) |
254 |
170-185 |
||
THERMAL conductivity of multi-coated pipes |
107 |
29076-29086 |
||
“ conductivity of two rolled tubes, measurement of |
107 |
29309-29321 |
||
UNIT cooler, heat transfer and flow resistance of various liquids in specially designed, (hydrogenation process), by M. Josenhans |
188 |
20016-20110 |
||
VAPOR phase, diagrammatic heat flow and heat balance of |
24 |
3..226 |
||
WASTE heat utilization, Leuna |
9 |
4(d) |
||
Translation |
143 |
20 ’84-20 ‘89 |