SCIENTIFIC ABSTRACT RABINOVICH, F. B. - RABINOVICH, G. D.

• Document Type: CREST
• Collection: Scientific Abstracts
• Document Number (FOIA) /ESDN (CREST): CIA-RDP86-00513R001343810014-6
• Release Decision: RIF
• Original Classification: S
• Document Page Count: 100
• Document Creation Date: January 3, 2017
• Document Release Date: August 1, 2000
• Sequence Number: 14
• Publication Date: December 31, 1967
• Content Type: SCIENTIFIC ABSTRACT

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RABINOVICH, F.D., inzh.
Large-scale serial surveying used in redesigning railroad stations
In England. Transp.stroi. 7 no.7.'25 J1 157. (KRA 10:
(Great Britain--Railronds--Stations) (Photography, Aerialtl

.5/006/60/060/06/14/025
B007/BO05
'AUTHORSs Rabinovich, F. D.,Panygin, A. V.,
TITLEs Sight on the Theodolite Telescope for Observing the Sun in
Azimuth.Determination
PERIODICALt Geodeziya i kartografiya, 100, No. 6, pp. 48- 51
TEXT.-, In 1941, V..'V. Kavrayokiy (Ref.9 Footnote on P. 48) suggested
a now method of sun sighting. It was based on the coincidence,of the coose
wires,with the intersecting (or contact) points of the four sun pictures
formed by a special prism sight in the field of view of the telescope
(Fig. 1). V. V. Kayrayokiy studied such a sight theoretically and made a
model of it (Fig. 2). In 1949, an experimental type was made'according
~to this model'by the sluzhba vremeni (Time Bervice)of the ToXIIG*iK.
It proved to be complicated in production and inconvenient In operation.
In 1957, V.7. Kavrayskiy's scheme was realized in a better construction
by F. D. Rabinoiich. This sight is briefly described and the-toot results
of the experimental type made in 1957 are given. FigEf. 3 and 4 show.sec-
tional,drawings of thissight, as well as the sight mounted on the theodolite.
Card 112

'IT-.e use. of fori.,-,ntes to ~;ct-val4e c,romx- taniAlng
n mi
f7l',,~cc~ Vre. con3=-r,'icn o' chrcm4i-m-, salt3.11 d e r-end e nc e
(Investi:-!-t~on of t'~-
of tho r~msult3 of chzrome tanning, cn the acid, preparat oil the and,
'U~,e com~pooj.tion of thc., tanning bath). Moscow, 195". Min "algher Education
U-33M. Yoscow Technolo 'rical Inst of Light Industry lm,eni L. IM'. Kngcmvich.
(Dissertation for t~~e. ')egree of Cvmlid,--te. of Technical Sciences),
S, 0 Lplo-,4-0 No. 47, 19 November 19515. I'0111colde

wx

STERLIN, R.N. [translator]; KNUNYANTS, I.L., akademik. red.;
YITKOYSLIY, D.P., red.; HABINOVICH, F.T., red.; =SMOMAYA,
T.F., tekhn.red.
[Modern experimental methods in organic chemistry] Soyremennys
matcdy eksperimenta v organicheakol khWi. Pod red. IoL.
Knuniantes. Moskwa,,Gos.nouchno-takhn.izd-vo khim.lit-ry, 1960.
627 P. (KIIIA 14:1)
(Chemistry. Organic-Uperiments)

38392
S/166/62/000/002/004/006
B112/B1,04
AUTHOR: Rabinovich, F.,Ya.

TITLE: A cortribution to the theory of thermal phase shift in
semiconductor rectifiers
PERIODICAL:, Akademiya'nauk Uzbekskoy SSR Seriya
Izvestiya.
,~

,
fiziko-matematicheskikh nauk o. 2, 19~2, 46-54
;
TEXT: The solutions of the boundary value problem
77
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~ACCLSSION NR, AP4038623 s/oio9/64/009/004/0716/0723
AUTHOR: Aronov, D. A.: Rabinovich, F. Ya.
TITLE, Investigating the current-voltage characteristic of tunnel diodes
SOURCE: Radioteklinika i clektronika, V. 9. no. 4, 1964, 716-723
i TOPIC TAGS: semiconductor, "semiconductor diode, diode, tunnel diode,
germanium tunnel diode, current.voltage characteristic
ABSTRACT: A theoretical. study in which a formula (30) is developed describing%
the current-voltage characteristic is reported. in the cases of strong degenera-
tion and very low voltages (under the minimum voltage), the new formula is
2V V
reduced to j J~, i where Irn is the maximum current, V, is the
V.
maximum voltage, V is the supply voltage. The. value and position of the current..
Card

ACCESSION NR: AP4038623
maximum and their temperature dependence (positive or negative) are determined
'by the conditions of production of the tunnel diode. This holds true in both cases:
(a) a strong degeneration and (b) a substantial blurring of the function of carrier
distribution. The new formulas are claimed, to be in good agreement with experi-,
mental data. "In conclusion, the authors consider it their pleasant duty to thank
E. 1. Adirovich for. his valuable comments and useful discussion. Orig. art.
has; 32 formulas.
ASSOCIATION: none
SUBMITTED: 213an63 DATE ACQ: 05jun64 ENCL: 00
SUB CODE: F-C NO REF SOV: 006 OTHER:- 003
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IZABINOVIGH, F. E.
Kaplan, S. I. and Rabinovich,, F. E.,,q A diagram of fusibility of the system
pyramidon-water and the solubility of antipyrine in certain solvsnts. P. 1162.
The solubility of antipyrine in dichloroethanel ethyl alcohol and water iv
studied in a temp. interval 140 to 720. The diagram of fusibility of the system
pyramidon-water is studied, This system forms a eutectic mixture containing.
10011/o pyramidon with melting temp. - 0.1c) . In this system the region of
separation is,established in a concentration interval from 21*/o to 6376 of
pyramidon at 72.5 -730-
The Orzhonikidze All-Union Scientific
Research Inst. of Chemical Pharmacy.
March 18, 1948.
Journal of Applied Chemistry (USSR) 21, No. 11 (1948)

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RUMPIN, V.; ALAINUIWA Go
Mechanized painting of buildino. Zhll,-kom. khoss 8 nosalls-19
Ilr2)
l.Glavn" inshener rewntno-stroltellnogo tresta, DsershInskoiro
rayons Leningrad& (for Kurepin). 2.Nachallzdk prolsvodetweim-tdiud-
cheakogo otdola remontuo-s trot tol I nogo tresta Ikershinkago rayosa
Leningrada (for Rabinovich).
(Spray painting)

(Apartment houses--Knintenance and repair)

-

L 55151-65 Ewr(d)/EEC(k) -2/E[C-4/EIIP(Y)AivP(k)/EWP(h)/EWP(l) Po-4/Pq-4/ A
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ACCIZ31011 nfl AvR6059330 DOOK EXPWITATION LR/
681029002056 1
KonhsrCkiy, D. DO ~~,IeVt J n7novrl, ,,n T.Kh.j qarokhova. j-4.1 9raato&T~kftL.
-I j
1,ribinovich, U. A.; A.; Frrnkr,).'. 1. D. 1-1-IM-MU-NO
j
Automatic devices and rc5ulitoraj handbook material (Aytomaticheekiy~s pribory I
ro[rulyntory; sprnYoohrVio mptorinly) 1.1oacow, Izd-vo "Mauhinostroyenlys", 6he
070h p. illua., fold. diagra. Errata slip inaerted. 19,000 copies printed
TOPIC TA031 AutomAtio control, nutomntla temperature control, automm
tic pressure
otintrul, nutotontio vnouum oontrolt tompornturn Inntrumont, all n
inatrwant, Imounntic P-0m.61a Mur, a
bintrwont, ..flow motor, liquid loyal ..z - Was
PURP35F AND COURAGEtNi %V rc,31~
The book describes the equipment used for automatic c
aignahng, end regulation of tochnologiopl processes, Pnd discusses temperature,
proasure, and level control devices, hydraulic, pneumatic, electric, and adectronle
direct-acting regulators. The book Is intended for engineering and todwaleal
peroonnal angngcd in the design, planning, and operation of,putompted Industrial
enterprises, and may prove useful to students at higher and sscondsz7 speolalimsd
schools.
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Contro! cots of automatic jawhreik,~rn. Gor. zhur. no.~Izzg-~.*~
S 165.
1. Institut, Kluarlkov (for I-Jtlcjv:;ki.y,
binovich). 2. '.?,Lr'kovskJy n -a ucthnc-is oled ova t"ei Is 'k-, y
a
R
elelf-Itrutekhnichesk-ly Iml-titut (for Berlcvskly., Gutrilr~,,O.

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TITM a
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VMICGICALS St.l-. 1959. Or 9. pp 770-776 ~VSSR)
ADSMU4T 1 1. September 1956. th. I.r,;--% fu~-'- in the USSR (and
3
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9 .
7
West--- Bur.p.) as b1.-M I.. It. -ki.x --1--
?h* profile and ostn dia..-L-As r th. C---- are -h9--
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in Fig 1. ?Us blast i. ---t-4 1. 4 tcw.. of -17135 -
beatims area each. allowing & blast temperature of I
low - 1030.C to be am-AtaLa.d. Tt.. blast is supplied
:
b
by a blower of a ..peaLty or ~000 n3/mkn at 3.d &to &be.
The furnace we. operating -&= about 135% *C Cl .. d L~t.r
(basicity O.d - 1.0) a..taLuta& 40-4576 of fin-- 0 - 3.2
=
and a high top pro4o~o of 1.25 t4 1.40 at=. Chsngoa
t
the outpmt* ore lood and bloat voluas during the fire
4maths of operation are showtI in Fig 2 Furnace
"to for embseqnsat perat'l.. (up to t;. and or 1956)
are gives La table 1 0.4 analyses of Iron end lag In
table 3. Darlag DeCeamber 1950. the average daily output
at the tuz~- rose Z. 2231 tons C7 cast- P- d-Y) at - ;~

Card I/S coke rate of 749.6 kg/t.n and slag -*lux. of 882.3 kg/t~.
I

"OS basicity 1.26). It una found %hat the furnace
WT ""Itivs to the degree of filling of the hear th
with 114PAd PF-dUcts (Fig 3). Any retardation in th
*acting or removal of slog considerably decrease* th:
rate Of dOeSgat Of burden materials. Change. I. the
ompoot% tom of the gas phase along the hearth radius
(sayers level) - Pig 41, cb&ngs* in the C02 content of
she top Sea Gloss th &JILrost radius - Fig 51 operating
z
l balances for two operating
a" "tr
Period* - table 3. from the operating experience gained
It to *excluded that largo farmaces can oratI
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on **'
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a Cmar"co of 9100 am diameter is Insufficient and some
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Card 8/3 Measures should be take. to &-rose*
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100141turG coutmt Crom 30 to 4to S/m3 decreased the ..k.
*~s~ptlOu by 2.i* and &mcreased the output by 3.7%.
WN"60064 the utilization of carbon monoxide for
reduction Increased from 39 to 419. the degree of direct
rs*AGSIOD ~~"hat L=r-aa.4 and the participation of
bydregom In the reduction suount.a to about bg;k. The
C.1100104 dOCIOLGA4160 to the rumace design "a listedl
0) blast "An with ttLre* 90* bond@ which load to an
Increase IS the pressure drops bi lack of b.l.,,.
bOtWOOR the GOPOdItY of the scale car and skips which
causes anu* 41"tculti-m ts. the r.m.c. charging (out
6006111114) a" -) the POsItIcalug OC tuJInsla for power
:06106 Wad Water 4061AO In Place. be,.. 1. .4.. or .
:
rush; W
S, the penetration or liquid iron is possible.
Thers are 5 fLgares, and 3 tables.
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83512
S/124/60/000/006/016/039
A005/4001
rh e
Translation from: Lerativiiyy zhurnal, Mekh;anika, ig6o, No. 6, PP-.117-118,
7618
AUTHOR: Rabinovich.-G-D.
TITLE: On the Problem of the Motion of a Particle in a Vertical Liquid,
Stream
PERIODICAL: Tr. In-ta energ. AN BSSR,.1958,:No. 4, pp. 68-84
TEXT: The author considers the motion of a particle of constant dimensions
and mass i n a vertical liquidstreamunrestricted by walls. ~The differential
equation of the particle motion is solved for the case of an isotherrmal liquid
flow. In certairf cases it is necessary to consider-two,stages.of the particle
motion. If themotion of 4 particle,of the specific gravity.Tm proceeds with-in
wa ascending flow of a liquid with the specific gravity -11, then the existence,
of tw Io stages takes place' in' the ca Ise w. u for -rm (when wo is the initial
velocity of the particle., u is the velocity of the flow), and in the case w,-'- u
for 7 m 0 independent of
,time. In the direct-flow heat exchange apparatus the steady
temperature condition is established immediately after the

S=
On the Computation of Heat Exchange Apparatus.III(Refe. 1-3) 57-28-5-28/36
liquid has entered the apparatus. The prescribed.temperatures
of the heat carriers are reached at the exit of the apparatus
when the exit cross section of that liquidisreached which has
the smaller velocity. In the case of counterflow the problem
must be,formulated as follows: On the one side of the heat
exchange surface theliquid 1 flows continuously in te direct-
ion of the negative x-axis. This liquid enters the apparatus
through that section having the coordinate x-1, the temperature
in this section being constat and equal to t' - 0. At the mo-
n
ment t = 0 the liquid 2 begins to flow on the other side enter-
ing through the section x-O and moving,in the directibn of the
positive x-axis, the temperature of~this liquid,in the entran-
ce crDss-section being kept at t" - const. It is required to
find a law for the approximation to the steady state Henge,
the problem is reduced to the solution of a differeniial e"quat-
ion with the following boundary conditions
tIr 0 t lix 0 tit
x
-to X-0
(21)
If the fact it taken into.consideration, that
4rd 2/3

On thdComputation of Heat Exchange Apparatus. III (Refs 1-3) 57-28-5-28/36
t" dt' dt'
n vd- nl"--d7 the law of the approximation to the
X
steady state for the liquid 2 canbe determined, by introduc-
ing the value to
m Mx)
to aA4e(m-MX)A -(7 -j(x
a] +8T2
aePs + 0-QM
into f ormula 33).-There are 4 Soviet references,
SUBMITTED: April 3, 1957
1. Heat exchangers--De gn
Si

06563
24 (8) SOV/170-59-9-4/18
AUTHORS- Rabinovich, G.D., Slobodich, G.N.
TITLE-. 'An Experimental Investigation of the Heat Transfer Process Between a
Pulsating Gas Flow and Solid Particles Suspended in It
PERIODICAL: Inzhenerno-fizicheskiy,zhurnal, 1959, Nr 9, PP 30-37 (USSR)
ABSTRACT: A number of writers dealt with the problem of intensification of,heat_..
transfer: I.T. Ellperin, V.P. Romadin / Ref 5 7, Linke and Hufschmid,
Ref 3_/.- The authors of the present paper describe:the results of,
some preliminary experiments in their investigation of the heat trans-
fer process in a pulsating gas flow. Hot air.heated to 130 IL500C
served as a gas whose,:-'low was periodically interrupted by a pulsator,
which led to pulsations of its velocity. The grains of rye were made
to move in this pulsating air flow. It has been found that the duration
of particle staying in a tube was considerably.-longer for the caselof a
pulsating flow than in the stationary flow; this is shown by Figure 1
and Formula 5. On the other hand, the coefficient of heat transfer de-
creases with an increase In the number of pulsations of the air flow,
as shown by Figure 2. However, the resulting effect of pulsations.,on
Card 1/2 the effectiveness of heat transfer is positive, as shows Figure 3, and

06563
SOV/170-59-9-4/18
An Experimental Investigation of the Heat Transfer Process Between a Pulsating Gas
Flow and Solid Particles Suspended in It.
the effectiveness of this process can be raised by a fac Itor of 3 or.4
in comparison with heat transfer in a stationary flow. This may be of
importance for designing small-size or portable drying and heat trans-
fer devices. Investigations of the following Soviet researchers are
mentioned in the paper: D.N. Lyakhovskiy, ]~.M. Fedorov Z-Ref 9_7,
Z.F. Chukhanov / Ref 117, I.,Gastershtadt / Ref 7~/, N.M. Mikhaylov
Ref 9_7and S.S. Zabrodskiy CRef 12
There are 3 graphs and 13 references, 10 of which are Soviet, 2 English
and 3. American.
ASSOCIATION: Institut energetiki AN BSSR (Institute of Power Engineering of the AS
BSSR), Minsk,
Card 2/2

14(6) 05279
SW/170 59-7-10/20:
AUTHOR:. Rabinovich, G.D.
TITLE: The Calculation of Driving Pressures and Natural Circulation in Steam
Boilers and Evaporators
PERIODICAL: Inzhenerno-fizicheskly zhurnal, 1959, Nr 7, pp 67 74 (USSR)
ABSTRACT:. In view of the fact that the TsKTI.method of.calculating circulation-does
not take into account a number of factors affecting this~process, an
attempt is made-to approach the problem of natural circulation from the
standpoint based on the basic equations of heat transfer (Formulae I and
la). The solutions of these equations leae. to Formulae.8 and 9 expressing
the values of driving pressures P divided by the height of the liquid
column H for thelcases of direct flow and counterflow respectively. The
generalized formula 20 includes all the factors affecting the magnitude
of the driving pressure, i.e.: the ratio of specific gravities,~circula-:
tion ratio, and f3,-factor, taking care of thetemperature of heat carriers
at the ends of the heat transfer surface. The average values of the
Card 1/2 specific gravity of a steam-liquid mixture.is expressed by Formula 16.

24(8) SOV/170-59-9-!6/18,
AUTHOR5 Rabinovich, G.D.~
TITLE. Session on Convective Heat Transfer
PERIODICAL.- Inzhenemo-flzicheskiy zhurnal, 1959, Nr 9, pp 111-112 (USSR)
ABSTRACT,- A session on convective heat transfer took place in the Leningrad House
of Scientists from 15 to 20 June 1959. It was convened by the Commission
on High-Pressure Steam., the Scientific Technical Council of the Leningrad
Sovnarkhoz and TsKTI. About 70 reports were delivered in the Conference.
The reports of M 'A. Styrikovich (ENIN) and V.Ye. Doroshchuk (VTI) dealt
with the problems of the crisis of water boiling. Their conclusions were
similar to those of A.P.
Ornatskly (Kiyev Polytechnic Institute). Two
,
reports, by L D. Berman (VTI) and V.A. Rachko (TsKTI), dealt with the
problem of determining the heat transfer.coefficients of the steam-air
mixture in vacuum. Two reports from ENIN,,delivered by Z.L. Miropol'skiy
and M.Ye. Shitsman were concerned with heat emission of water during its,
cooling In the near-critical region. The reports by N.V. Tarasova (VTI)
and A.P. Orrat*kiy presented the results of investigations of hydraulics
Card 1/2 resist&nce during the boiling of underheated water in tubes. N.I. Semenov

06575
Session on Convective Heat Transfer SOV/170-59-9-16/18
CENIN) reported on an investigation of the hydraulic resistance of the
two-phase mixture during its motion along a vertical non-heated tube. Ses..
Kutateladze communicated on determination of heat transfer coefficients
in a,horizontal tube during.stewn.condensation. A.A.,Gukhman communicated
on amethod of calculating the parameters of a moving substance in nozzles
with small angles of opening. I.I. Novikov (MIFI) expounded the theory of,
thermodynamic similarity in which viscosity and heat conductivity were con-,
sidered not as constant quantities but as thermodynamic variables. A.I.
Leont'yev reported on an investigation of the heat transfer processes at
forced pulsations of air pressure in a short tube, V.P. Matusevich reported
on the theoretical solution of the,heat transfer problem in a head point of
blunted bodies colliding with a gas stream. I.G. Kulakov made a report on
an ingtallation employed in the-ENIN.for producing high heat loads,(up-,to
50.10 kcal/m2.hr).
Card 2/2

am

S/170J60/003/04/1'1/027
B007/B1O2
-AUTHOR: Rabino*iohg_d.* Do
TITLE: Some Problems of Nonsteady Heat xchanxetin a Layer of Disperse
Material
PERIODICAL; Inshonerno-fizichookiy zhurnall 1960, Vol. 3, No. 49 pp. 73 so
TEXT: The author given an analytical solution of son* heat exchange probleas,,vi
concerning heat exchange in a layer with Internal heat sources. In his earlier
papers (Refs. 2, 3, 4) he has shown that heat exchange in a recuperative apparatu:c~
is expressed by partial differential equation of second order. The problems of
heat exchange in a layer can be formulated on the following condition@; 1) The
temperature gradient within the particla~ forming the layer is negligible. This
can be attained already with 2) The amount of heat mutually delivered by
~ha particles by contact heat exchange is negligible compared to the amount of
hoat exchanged by the particles with the liquid flowing through their layer. The
lifferential equationZ (1) and (2) for the heat exchange between the layer with an
Internal heat source of -th4-intinsity q) and the liquid flowing through this
Card 1/2

Some Problems of Nonateady Heat Exchange S/17 60/003/04/11/027
in a Layer of Disperse Naterial B007Y11102
layer are writt n down. Iquation (2) is-solved by the Laplace-Carson transform
yielding formul: (8). From this formula the individual sp*cialcasee can be obtained
according to the dependence of the internal source on coordinate and,tize. The
following cases are investigated: Caee1;:Her~, the internal source does not depend
on coordinate and time (q - const.) and formula (12) is obtained for V. Came 2: 1
The internal source is a function of temperature. Two Vl:ndb of functions are Investi
gated: q w a(t"-t ) where a and t are certain constant quantities, and q - a(t"-btt~1111
0 0
where a and b are constant. The formula@ (19) and (24) are obtained. If q a 0, a - 0
and b - 0 in assumed, formula (26) is obtained for the temperature distribution in
~a layer without internal sources. In the case in which the heat carriers move
crosswise at.900, formula (27) in obtained. Basing on the@* results and on some
additional assumptione,the heat exchange in a moving layer of disperse material in
the case of t 'ranoverse blowing with a gas at the immovable layer can be Investiga-
ted. There are 5 references, 3 of which are Soviet,
ASSOCIATION: Inatitut eiergetiki AN ISSR, g. Kinsir (Institute of Power Rnginoering
of the AS Belorueskaya SSR, City of Ninsi)
Card 2/2

S/170/61/004/003/005/013
B117/B209
0?61
AUTHORt Rabinov,ich, G. D.
TITLEt The problem ofinonsteady cooling of a bounded volume of a
liquid
PERIODICALt Inzhenerno-fizicheskiv zhurnal, v. 4, no. 3, 1961, 58-63
TITLEt The author describes a method of calculating a portable heat ex--
changer for cooling reaction vessels. The heat exchange process is inves-.
in a heat exchanger which is schematically shown in Fig. 1. Reac-
tion vessel 1 contains liquid II; the quantity of water equivalent to the
volume of this liquid is-represented by WII. The liquid is circulated over
p
heatLexchanger 3 by means of pump 2. The second coolant which, at a con-
stant temperature ti, is contained in the heat exchanger, may be circulated
either in or against the direction of coolant II. In the present paper the
concrete case is described,where:the liquid in the reaction vessel contains
an internal source of capacity q with q = 0 outside this,volume. Such a
condition is met, e. g., by homogeneous nuclear reactors.with a detachable
Card 1/4

89927
S/170J61/004/003/005/013,
The problem,of nonsteady B117/B209
cooling surfacej For anyinstance of,time-on,e may write
W (F,-~ dr WOO dt" + qV dr (1) and,
2 [t 2p
p p p
.-Wit t" + V 2p qdr W 1 t~ d (2)0 where V2 denotes the volume
p p
0 0
of liquid II inthe reaction vessel. Formula (1) describes the mixing of
the liquid in the reaction vessel~with.that from the heat exchanger. Eq. (2)
Phows that the amount of heat extracted from liquid.II is equal to that
absorbed by liquid I. Differentiation of (2) with respect tot gives (4):
dt"/dr - (qV r'/W")Ft'(F,-*) - t'. If heat exchanger 3 (Fig.1)
p 2p /Wp R H
operates in direct flow, the differential equation describing the heat ex-
change in such an arrangement has the,form 0f(6):
t, W, + W': I
+'K
+ C + +
+
OY W, W, dya- W" W W's
Y
0.
+ (6)
W~
Card 2/4

S/170/61/004/003/005/013
.
The problem of nonsteady B117/B209
/W where F denotes the heat-exchange area from the entrance of the
kF
X
X
liquid to the cross section x; W' andW" stand for the quantities of water
equivalent to the volume ofthe two coolants. By simultaneous solution of
Eqs. (4) and (6) one can derive formulas (15) and (16) for determining the
heat-exchange area cooling a bounded volume~of liquid with an, internal source
of capacity q:
" tH') (15);
I'41 (t
a qV 2
P
P
(16).
kF/W
w- 1/[l + (W a i-1 + (W
/W
)j)
/W
)1109
j
1
2
1
2
moreover, from thi;-one obtains formula (17) for the estimation of the time-
'
until the steady state is reachedt V-N
e. formulas derived
VaW, (17)7 Th
I
p
were checked by calculating an HRE-type homogeneous test reactor (Yadernyye
It is shown that these formulas.are valid also
reaktory, t. II, IL, 1957)-
,
for counter-flow. A..G. Kasatkin is mentioned. There are 1 figure and'3
Soviet-bloc.refer6nceslou.
Card 3/4

(Heat-Transmission-Periodicals)
(Mass trawfor--Periodicals)

28906 3/17 61/004/011/004/020
B 104%112
AUTHOR:
TITLE: Steady heat exchange between threq..coolants flowing in
parallel flow through a recuperator
PERIODICAL: Inzhenerno-fizicheskiy zhurnal, v- 4, no'. 11, 1961, 37-43.
E,
TEXT: Dr, author studies th6.steady heat exchange between three coolants
in a system shown in Fig '1. Wall 1.1a made of a heat-conducting material,
and wall 2 is an ideal heat insulator. The possible directions of motion
of tile coolants are shown in Fig. 2. The heat exchange in all modes of
coolant motion is described by a homogeneous differential equation of
third order:
d3f d1t dl
+ (P + r) .-2 + P~ 0.
du. du- du.
where X Va 2 4b, r a- A a + A:. Here, R
2 P -2 ki Wvwi; W1 are Aht,
water equivalents of the coolants; u. k31F 31 (x)t"Y P~ k31 F31 /k'1 2F1 29
Card 1 /4~

28906
S/170/61/004/011/004/020,
Steady heat exchange between ... B104/B112
The quantity u is calculated from (12), (14), or (15)- Particular cases
of heat transfer between the three coolants-(Fig. 3) arestudied.- The
case of heat transfer where the liquid-II has an infinitely1arge water
equivalent is considered. A heat exchanger with dissipation is calculated.,
It is shown that the losses may reach high vailues if P< 100. M-A.
Mikheyev (Osnovy teploperedachi (Bases of Heat Transfer), GEI, 1956) is
mentioned. There are 3 figures, 1 table, and 4 references: 3 Soviet and.
1 non-Soviat. The reference to the English-language publication reads as
follows: Gardner K. A., Ind. a. Eng. Chemistry, N 9, 1942.
ASSOCIATION: Institut energetiki All BSSR, g. Minsk (Institute of Power
Engineering, AS BSSR, Minsk)
SUBMITTED: March 27, 1961
Card 3/4

I YU~;GSHITS
T L,. G'. D. " SLOBODKIli, L. S.
"Irrvesti-aticn of t~--- '--inetics of varni's*-.-baki on met-ql 1 -ic backings with
radiative and ccnvective heating."
rer,ort submitted for 2nd Pdl-Union Conf on Heat & Mass Transfer, Minsr., 4-12
-may 1964.
Inst of Heat &,Nlass Transfer, AS BSSR.

L 158o6--6
_5 ESD(t)/AEDC'a)/58!k/BSD,/AFWL/ASD(f)--?--
ACCESSION UR: AP4047826 S/017o/6 01013010135-1
Go Do
AUTHORS: rin, I* To;
e:
TITLE: Second All,-~Union convbcation' for heat and-mass exchange -
SOURCE: Inzhenerno-fizicheskiy zhurnal, no. 10) 1964i 130-135
TOPIC TAGS: heat exchange, heat transferj' mass transfer, mass* exchange, sci tilt
en 1c,
".organization, science'conference-
The Second All-Union Convoc on for Heat and Mass Transfer was held'in
ABSTRACT. ati
Min 1964, for two basic purposes. iew the.the etica
sk on 5 to 9 may) 1) to rev or
and experimental Progress in.the field, realized.over the-3-year- period since,the
first convocation held-in Minsk in,1961., and 2) to Plan basic research objectives
for future work.. The meetingwas attended,by 438 delegatess including 260 from the
o z oteworthy participants;,
E. Toei. (Japanese
ity)j To Evain- (New
e (M ch Upper
rian L. Strakh.9 Ie-.
vakovich and A. Noin