SCIENTIFIC ABSTRACT PALEY, P. N. - PALEYEV, I. I.
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December 31, 1967
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SCIENTIFIC ABSTRACT
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DAVYDOV, A.V.; MY-P.SSOYEDOV, B.F.; NOVIKOV, Yu.P.; PAUY, P,N,.-, PALISHIN. Ye.S.
-onc-entrAtlan and purfificatiGn c;f pe123' and F,&2~13. -rT_~-jy Mjm, an,
khlm. 15164-7c) '65 ', K~' -.-l A I F i " ,
DEBERDFYPVA, R.Yu.; NFVOD,,ItIK, A.A.; PAIEY, P.N.
DeterimirAtIon o-" uranium in solutiows of tributyl ph-isphate, ir keros-ire
and synthine A-11 thiOCYRnate. Radlokhlzuila " no.,-ii?.171-273 11-5.
(MI RA 18 11
13
kccLWON Oil 0',
ce d,
ikbb th ia :6f vii tals' ld If dd)~U U
Ine C Abi
p
_
-
Ot eupcedd'100.-~'L-Pqrdetq fil ths)idigon bding t B b
h
ApAlyz
2 g (TV ked~~ toza
ne_(~ -is, on, a 10610 u- tM*tUaD~ oftp amm N
_g
-
,
ei'd - -
on craidl
ne jores
CCDEi- 10--
iuBwaTTEDt- 09A 8 UB,
Nor
fo~ sovi
-
COAL
-
PALEY. P.N.; NFMODRUK, A.A.; DEBERDEYEVA, R.Yu.
Determination of uranium in chloride-fluoride sol,itions. Radickhimia
6 nc,.4-459-463 '64. 'MJRA 18:41
1
7~
Vw
_
id~
At Uitift-Of thi jillm" 4 ft
folft- M* so -aft vtth
b W-OldcI
_66~.Jkut theAte ity bf tu-44MI-solut v -3.
00 Oo ~41:.
tut IML,-al tot
10001
*eft
to
~
it - th
*
UnA
7
j-_-
Odi
SN--HNO
.yo ab
Mlil"
Man
be tshlAd out aaw
d V
4E~ 'n"
kcr,gs=N. mil AT50136
JjO4~ft 7tWI
owl-halmAtiot 001= a-wltv I bbtabed U ce
-presepoe
P-99' -sud-urmlimcau b6'd6Wrml6ed **6
c jRdd AcWc
-- idl* thit the-tWt of me" 01~
dwAmung
VBPI-Sobliiow~ un ibr tm. Pirpose- Of
TBP
f
t prom,11404W jog,
IWO Of" 4*r-aifi vii -
5 il~
-wl T- (V ftct:old
read, d,
th 1) In
Ilia"
Ift
r
'W
RYABCFIKOV, D.1., otv. red.; ALD-.k".1',*, I.F., red. - PAL--'vI-,. F N
red.; ziORISOVA, L.V., reea.; ZCIO"OV, Tu.A., red.;
SEiYAVIN, red.; U,,~YAKIN, A.V., red.;
M.P., re
[Modern methods of analysis; method3 of studying the
chemical composition and structure of substances. On
the seventieth birthday of Academician A.F.Vinogrado-I
Sovrenw3qw. - sa; metody issledoveniia Jrhizzl-
cheskogo sostava i stroeniia veshchestv. K semidesiati-
letiiu akaderLika A.F.Vinogradova Mqnkn--p Navksp 1965.
333 P. (MIPA 1817)
1. Akademiya nauk SSSR. Institut geokhimii i analitiche-
skoy khimii. 2. Chlen-korrespondent 0 SSSR (for
Ryabchikov).
Adeksaridr Aii_:.-c"%,,v-.0r~
;
',!I; &GRADO'. I A. glav. -e,1. FALDY :,ed.
knallyt~ cal _ e.,- '3t:--v kna t f a a
L
~-)C4. 28-
(~T:,_A -I)
PALEY,--P.TJ.; RYAXHROV, D.I.; DEDKOV, Yli.M.; ZOLOTOV, Yu.A.
Methods of concentration in an-plytical chemistry. Zasv.lat. '-'?
no.12:1270-1280 163. (MIRA lr,:14)
KHAIKIN, V,A.; PALEY, F.N.; NEMIODRUK, A.A.
Extracti,on of tel-ravalent plul-mium from nitric acid srluticns
with oxygon-rontaining fixtractants. Radlokhimiin 5 no.2:21~-2-112
P63. (MIRA lollo)
NIMODR!'E, A.A.; -PAIY.Y, F.N.i KOCIIETOVA, N.Ye.
Gomparative study of --agents for the photometric determination
of plutonium. RadiokhImiia 5 no.3g335-342 163. (MIRA 16-10)
(Plutonium--Analysis) (Photometry)
(Chemisal tests and reagents)
I
il -
IX V , 11. F. ; PA L'Sli A , Ye ~. ; : f , J. y , I , N.
I!, T A S C: R I
Separation ~' Fr, 'a c*.~.-r -~:~merj*.~- by ' -1
with N-benzoylpreny--i,.yr-,rcx-1,~.L.T....e. I L'.. i I a r1p, I . K'', - - . - f '.
105- 1 10 164. .- -,
.. InslAt ~t gt-,,krAl-,,-.- ' ana-..*~'. I
I
AN MC)SIM-V,-.
-7 __7~
M.
NAT'
---- ---- - ----- -
TrV
WAW -:'A"_w3"2
at '~Xl "i iw on Of plat cli;i,.: L_--
Jid
ts - ukdatt", -A ODOM
lAl
7f
of., tec 0 Ii, arsonLso 11,
ruld or=
Gro' la bii ulim';p~d
-r .
r& w6f-t ~Milw
ort
_P IM
.1. lut PO nt4d I fn The fttu%.
or, soon To_wm. We
OL
Me' mrow :mip
for, ftW -t ,b
d 02 IV* ln:the~ ewmil~UCWI~of p2utoimluu
has
art I
" .,7: T
. . . . . . . . . . .
NEMDRUIEV A.A.; _~A~, P.N.
Photometric study of the reaction of tetravalent
arsenazo IU. Zhur.anal.khim. 18 no.4s479-485 Ap
(Uranium.-Analysis)
(Arsenazo)
(Photometry)
urvAium with
163.
(MIRA 16-6)
y,t T.A!;( V, Kui.anau, i tile i
P . , -,
I "L -, I I.
"Leterrainati3r, of it~-nriiri -,i with ~h~ k-'~; )f Xicro ,- ai
'~'ikrooiol 0 4
L .-ya, j, 521. 1 A c; .
PALEY, T. Ya.
I'Determi nation of Vitwidr, P, ly .-i.eans of Micro
OrF&nisms," Y.Ikrobiol., 9, No. 5, 1040
SHUBERK"HUBIN, L.A.; KWH, P.T., lnzh.; KAPLAN, M.P., inzh.;
PALEYJO V,A., inzh.
Gas turbines for large power stations. Teploenergetika F no.1-1:
5-12 N 161. (MIRA 14: 10)
1. Kharlkovskiy turbinryy zavod. 2, C-Llen-korrespondert
ANI USSR ~ for ShubenkowShubin) -
(Gas turbines)
(Pover'OnstneerLmg)
B.V- Kand. takhn. na
pp.,,:,v. V.P., . 3~0,.'AYM-H,, -ak
S tudy :;f ti-VE -, till'.K- Ing ot' a high-temperature cylinder.
--., nc.-,,14-4 Ap 165. (Ml.;;,A 18: 6)"
PALEY, V.Ya. . inzh.
9- fv 14- 4
~ NS,
Redleigning of two--circuit reinforced concrete 110 kv. A
power tranmission line poles. Energetik 12 no.1la25-28 -A J. K
N 163. (MIRA 16~,11)
LENOVICH, A.S., inzh.; DUBINETS, A.Ya., inzh.; PALEY, Ya.M., Jnzh.
Increase in the oparational reliability of rolling mill muotors.
Prom. energ. 20 no.6i4-9 Je 165. (MIRA l8z6'
PALEY, Ya.M.; LENOVICH, A.S.; DUBINETS, A.Ya.
A composite slippage regulator for asynchronous motors. Ener I
elektrotekh.pron. no.4%67-69 O-D 162. (MIRA 1671
1. Kommmarskiy metallurgicheakiy zavod.
(Electric motors, Induction)
LENOVICH, A.S.; DUBINETS, A.Ya.; PALEY Ya.M
zzj_i:_*
Automatic temperature control and limiting of the heating of
the armatures of d.c. motors of rolling mills. Energ. i
elektrotnKh. prom. no.2:6-7 -Ap-Je 163. (MIRA 16:7)
1. Kommunarskiy metallurgicheskiy zavod.
(Electric motors-Goo,ling)
(Rolling mills-Electric driving)
LENOVICII, A.S., inzh.; DIJBINETS, A.Ya., Inzh.; PALEY, Ya.M., Inzh.
Continuous automatic- control and limit4ng of tt,e ~ieating of armature
windings of the main l.c. motors )f rr"-I.ing aills. Elaktro*---krmiia
35 no.4:42-43 Ap 164. (MIRA 1":4)
PALEY, Ye . Kh -
Our Work Experience
so; Veterinariye; Vol 30; No. 4; 10; APril 1953 Unclassified. Trans. #121 by L. Lulich
Central Zooveterinary District, Chimilinskiy Rayon, Moldavian SM
MST, TeAh.. voterinarVy vrach.
I
Our work experience. Vetarinariia 30 no.4:1-13 Ap '53.(K6HA 6:41
1. Uentrall W sooveterinarnvy uchastok Chimish-linakogo rayona,
Noldavskoy &SR.
1. PALEY, Ye. Ri.; D. V. 1.1.
2. USSR (600)
4. Veterinary Medicine
7. Our work exoerience. Veterinariia 30, No. 4, 1953.
9. lonthly List of Russian Accessions, Library of Congress, April 1953. Unclassified.
1 ~7 - :~8 - i;q
Translation Irmw 11v1vr;jtivT,yy zlilirtiil Mclall,jr8t~;i l'68. Nr i, p 199(USSR)
AUTHORS: Zav"yalov, A S. . Pak-% Ye Ya
TITLE: Types of Carbide-, in Sir,., lural Stvvis ind Pro( v-,sv~ 1-f Their
Formation and Dissoltition (Tipv karl,idt,% kmistriiktsicliotlv~!i
staley i protsessy ikh c)bra-zovaniva i rastvureniya)
PERIODICAL : V sb : Metallcivedeni~e. Leningrad. Siidpromgiz, 1();7
pp 2120-z~"
ABSTRACT: The processes of forn-~ation and dissolution of carbides in
structural steels alloyed with Mn, Cr. W, Mo, V, Ti, and Nh
were investigated. Steel sampie,, which have been tempered
and annealed at different tern pe rat tj res, were subjected 1c) ani)di(
dissolution in an ele(ir(Ay-e (-ontaining i percent Fe SO
4
~'
~
-ide
e c
a
I percent NaCl, and 0.2 percent of Rochelle salt T
powders precipitated were inve-,tigated by means cof (.h(~rrii(a;'
and X-ray analyses Types of carbides, as well as tempera!;ires
of their formation and dissolution, were established. It is
that in certain steels the (>( phase is supe r-saiii rated with C
at annealing ternpuratures arouy)d 700'C T h t- ( a r b) ri f- -, J c, r rn t- d
Card I /Z in the process of stepwise annealing are of tht same type as
1 37 - 58 - 5 - 58Y)
Types of Carbides in Structural Steeis (cont. )
those formed in standard annealing processes, but are richer in carbide-
forming elements. The process and the mechanism of formdtion and dii-
solution of carbides is described.
V. G
Card 2/2
DVIZUOV. P.P., otvetetvennyy redaktor; AVTSTN. A.P., redaktor; VINOGRADOVA,
T.F.. redaktor; DIRGACHEV, I.S., redaktor; KUYAZEV.A, G.D.. redairtor;
PALmYW,_j,Z redaktor; WOPOBT, Ta.L.. radairtor; SMOL'YA2131XOV.
A-.'T., redaktor; UGRYUMOV, B.P.. redfjktor; SHTM. R.D.. redaktor;
KCKAROVA, Z.N.. redaktor; ZAKHAROVA. A.I.. tekhnicheskiy redaktor
(Proceedings of the All-Union Conference of Pathoanatomitite. Lenin-
grad. July 4-9. 1954] Trudy Voesoluznoy konferentaii patologo-
anstomov 4-9 iiulta 1954 g. Leningrad. Moskva. Gos. Izd-vo med.
lit-ry. 1956. 411 p. (IGRA 10:3)
1. Veosoyuznaya konferentstya patologonnatomov. Leningrad, 1954.
(ANATWY. PATHOLOG ICA L-CONGIUSSICS)
kazid.med.nauk
Manifestation a-w reatment ~.)f allergy. Aad.sestra 22
8-13 MY163. (1,Ji,.A 16.8)
1. 1z Klinicheskoy orderia 1,ardris bollnitsy imeni S.F.botkina,
llosk-ix.
(ALLERGY)
SOV/1 12-59-2-3138
Translation from: Referativnyy zhurnal. Elektrotekhnika, 1959, Nr 2, p 128 (USSR)
AUTHOR: Paleyes, R. A.
TITLE: Application of Electricity for Roasting Cacao Beans
(Primeneniye elektroobogreva dlya podzharivaniya bobov kakao)
PERIODICAL: Khlebopek. i konditersk. prom-st', 1958, Nr 1, p 45
ABSTRACT: Bibliographic entry.
Card 1/1
SOV/ 112-59 -1-1438
Translation from: Referativnyy zhurnal. Elektrotekhnik
1959, Nr 1, p 197 USSR)
AUTHOR: Paleyes, R A.
T T LEI A qvd- 1 Dvd)e for Packaging Cacao Powder
IT
PERIODICAL: Khlebopek. i konditersk. prom-st', 1958, Nr 2, p 33
ABSTRACT: A semi-controller designed by N. V. Pyrinov at the Sormovo Pastry
Factory is briefly described. Two illustrations.
Card I / 1
COW" IV
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.0%9 town d bdg%g of Vm* asp. A. M. Pakev.
Zes"it 1"J, NoA, 16-23.-P. d6man tbc type of
the pan* bend over because of t he un-
Judging in Which theym
balonced comWbm the umvy tops and poor strength of
the loom part of the pkwit. P. sMws that durin the tuilk
stap by"yals of the coll bre componentsimllulose.
xylan, and Agnin) takes pl". This metion Prevails all
through the rest of the growing peo during which the
stews low 20-Ml% of cellulose, xylan. and lignin. W3
pbcnwmmon, While Pus. for grain formation. is neg. for
Inech. support. 1. S. fake
PAIE74.0410 M chemical Abet.
Vol* 40
APT. 20 v 1954 1
jBiological Cheldort"
FAIIN Of Brilln culture plAut9. A. hf. Pulvev. Poklady
Akad. Nonk 92, 43S.8(I9M).--It Is Anwis that
the falling of grain plants (Vgtka rye) resulling froin stein
breakw in t eir upper sect is umally occurs during the
-phase of early ripening and is c2mvel by partial to" or de-
conspri. of the woody stein skrkton. At this phase the
cubohydrate components such &3 xylans, ccliulose, and
lipin been to 6how a decline. G. hl. Kosolapoff
PAIW1160".; SMCHKV, V.N., Wmdemik.
Problems of grain crop lodging. DokI.AN SSSR 92 no.2:435-438 S '53.
(MI-RA 6:9)
1. Akademiya nauk SSSR (for Sukachav). (Grain-Diaeases and pests)
T'ALEYP', A.Y.
The role of the cell- wF,11 carbohydrfites of the prain and leaves
of .9. CEREALE In the formit4on of the grain. A. M. PALEY1*1. ( LAB. OF PLAW,
PITYSIOLOGY OF TT~E PEDAGOGIC INST, RYASAN) vol.3, no.2, p. 2'P, 103F.
PALEYEV, Aleksandr Michaylovich
(Chuvash Agricultural Inst), Academic Degree of Doctor of liological
Sciences, based on his defense, 29 April 1955, in the Council of the
Institute of Physiology of Plants imeni Timiryazev, Acad '~ci U'9-SR, of
his dissertation entitled, "Role of Components ~f callular membrane
in the exchange of plant substances" and academic title of Professor.
Chair: "Chemistry."
Academic degree and/or title: Doctor of Sciences and Professor.
30: Decisions of VAK, List no. 24, 26 Nov 55, Byulleten' MIVO SSSR, No. 20,
Oct 57, Moscow, pp 22-24, Uncl. JPRS/'~Y-471
r?,nyl,~~',
,*hpmic,,ni corqx)sitlon of Vie ce'.11LIpir of the prP5~.-,, S.
cereale. A.M. '~ALFYFV. ( 400r) !," 1,,
I. I IrA-L SCIErl IFIC I~ET. MOFm4 )
vol. 1, no.6, p .654, 1936.
F. AT, -D.-r 7 , I'. . 1.1/ .
I
.he dynamics of the formtiori of different compcnents of -he
ceEiCtr vT-32s of rye, grass ( S. CEREALE ) A.M. PA1-FY-FV (The wood chemical
Scientific Reseprch Institute, moscow) Vol. 2, no.1, p. 3, 1037.
PAL=.
"Pole of the CeIj Co.--.~onents of the f3ce~71 Caps~de Lin the Plant
Sci Inst of Plant. :Io :e:-K azev, .~Xa : 3c'
(KL, No 1L,
SO: Stri. No. 704, 2 :;'ov S-,Lr-ve, of 3cient-i"'ic and '.ecl-,nical
at USSR Urher Educational List itUt4 ons (i(
K C,N D RA T I',"- ', 1 . ;j;jq~,-,I,~, , ~ . , ;.! ~ , ' , jKttl"N, A., irah.; S"ADNICITUK, 1,.,
- I
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PAIZYEV, 1. 1.
USSR/Wtals Roasting FDA
Card 1/1 Pub. 153 - 3/18
Author Gurevich, M. A.; Paleyev, 1. 1.; Timoshin, Yu. A.
Title The process of roasting the fuel impurities out of porous materials
Periodical Zhux. tekh. fiz. 24, 599-609, Apr 1954
Abstract A thecretical and experimental work attempting to fully solve the
problem concerning the roasting of admixtures of carbon and other
nonvolatiles from porous materials such as ceramics, briquets, etc.
Acknowledge participation ol S. M. Pavlov, A. N. Frolova, and L. A.
Shilov in the experiments and of D. S. Gorshkov in the Integration
of the eqiiations.
1nstitution
Submitted November 11, 1953
PAIJ M . I.I.; TUDIN, Y.Y.
Reaction of water vapor and fuel carbon. Gaz.prom. no.5:10-16 My
'57. (MLRA 10:5)
(Steam) (Coal gasification)
I
A /- ~- ri-- ~ i'-
P
PALITU, I.I.: TOM, V.P.
Iffoct of the injection of steam into the air blast on the fuel
temperature in a gas generator. Gaz.pron. no.9:9-11 S 157.
(KIRA 10:10)
(Coal gasification) (Gas producers)
L C/ 114-8-106
AUTHOR: paleyevp I.I., Doctor of Technical Sciences and Gufevich,
of Technical Sciences.
TITLE: ()n a cause of mechanical incomplete combustion in a
fumace with a 'boiling' layer. (Ob odnoy prichine
ipyashchim' slo'Yem)
mekhanicheskogo nedozhoga v topke s 1k _
PERIODICAL. Tnerg-omashinocaj~~eix~i?ll (power Machinery Construction)
-L2i=-
177, Vol-3, No pp. 15 19 (U.S.S.R.)
ABSTFACT: A special feature of furnaces with a 'boiling' layer is
a good mixing of the fuel at all cross-sections of the layer.
In large inclastrial installations in which there is a consid-
erable distance between the points of fuel supply and ash
removal, mi:ring within the length Of the layer is much weaker*
But in small installations and particularly in ex.perimental
rigs for investigations on the boiling" layer there is
intense mixing throughout the volume of the layers. This
article considers a device represented in Fig.1 in which the
-fuel particles are delivered into the combustion chamber
through an upper aperture, the ashes are drawn from the bottom
to another aperture and drauk~lt is applied throu0i a grid.
In such installations there is considerable mechanical
incomplete combustion even when the mean time for vbich part-
icles remain in the chamber is muchgreater than the time
Card 1/3
the problem in certain simple cases.
in order to determine the compositions of the ash or
material in the chamber the laws of probability may be used.
if the course on the process of combustion of'fuel with time
is known it is possible to determine the avurage amount that
is not consumed for each group of particle size as a function
of the ratio between the mean time of residence of this
fraction in the furnace and tAe time necessary for complete
combustion.
Card 2/3 The mathematical analysis is then given under the following
the law of co 6 tu dime of resi-
e residue Of fuel in the ash; mbu-Stion Of fuel Particles;
combustion chambei and the residue 0~ fuel in the
It is POin-ced out that the distribution functions derived
are applicable not
also to o her furn, Only to il'urnaces with a lboilingr layer but
U Ices Ivith intensive mixi
the mil _n. * 0j,
in6 is not ins the fu_~2.
-uantaneous E
a whole must be allowed for. P movement of the fuel layer as
tnis case. Difficulties are encOun~,,.L-ed i
It is evident that calculiti-n of t1le L,;ean fuel _n
"Osidue (in the ash and in the chamber) can 'be made for any
desired law Of combustion Of Particles with time so lon, as the
law is Imown from theoretical cons-,ru 'tion or from ex-ce
riment a l
data.
There are 3 figures and 6 Slavic references.
'-VA1DkB1X': Library of Congress
Card 3/3
AUTHORS Agafonova,F.A. Gurevioh, N.A. 57-6-23/36
Paleyev. I.I.
TITLE I-Vontribution to the Theory of Burning of the Liquid
Fuel Drop.
(K teoril goreniya, kapli zhidkogo, topliva.)
PERIODICAL Zhurnal Tekhn. Pis., 1957, Vol. 27, Nr 6, pp. 1818-1625
(USSR)
ABSTRACT Calculations based on a number of simplified assumptions,
which are consequently of approximate nature, are given.
Inspite of these insufficiencies they make possible the
following conclusions: I.- The fact that the diffusion theory
in the case of the experiment offers coinciding evaporation
- velocity values can not yet be taken as proof for a
combustion process of liquid fuel taking place on the
basis of pure diffusion. Practically the same evaporation
velocities are obtained in the case of a taking account of
the finite velocity of the chemical reaction.
2*- The consideration of the velocity of the chemical
reaction leads to much smaller calculation of the maximum
temperature in the case of the same evaporation velocity.
This Is proved qualitatively by the experiment.
Taking into account the velocity of chemical reaction
CARD 1/2 leads to an aproach between the zone with maximum
PMEM, 1. 1., kgafonova, F. A.,
IfInvestigation cf V-e- C=buEt_'on ~;f Dzrcplets of a Li-iuid Fuel," Aer,~~Jij-_._~_-
and Heat Transfer Prot-'ems '.n Bo'-'er and Fjrna:~e ?-r--cesses; A --'
Articles, Moscow, Gosenergoizdat, 1)5d. 322LI) P.
Purpose: The book is intended for engineers aid combustion special-` sts
with the design and opemtion of heating equipment and it is a1sc for s:~J.eit"ii:
workers and students of vtuzes.
82805
3/124/60/00o/005/004/007
A005/A00l
Translation from: Referativnyy zhurnal, Meldianika, 1960, No. 5, PP. 49-50, # 58`4
AUTHORS: Paleyev, I.I.j Agafonova, P.A.
TITLE: Investigation of the Combustion of Liquid Fuel Droplets
PERIODICAL- V sb.: Vopr. aerodinamiki I teploperedachi v kotel'no-topochn,
protsessakh. Moscow-Leningrad, Gosenergoizdat, 1958, PP. 57-80
>I
TE(T: The combustion rate of droplets of solar oil and mazout was studied
under conditions similar to the conditions of the combustion within the combustion
chambers of gas turbines. It Is shown in comVitatilonal way that the temperat,.,re
at the combus+Aon surface can be assumed to be equal to the thecretical fuel
combustion temperature within a medium having the same temperature and constl-
tution, when the excess-air coefficient amounts to OG = 1; this result is based
on the G. A. Varshavskiy formulae (for calculating the combustion of a droplet
having at a definite instant a prescribed dimension), developed on the as-
sumption that the losses by emitting Into the surrounding medium (cnambers
with high forcing) are relatively small and that the equality D = 0(,',-q valld
Card 1/4
82W
S11 24/60/000/005/004/007
A005/AOO1
Investigation of the Combustion of Liquid Puel Droplets
(D is the dif-Ausion coefficient,v Is the thermal-diffusivity coefficient". it
was stated in experimental way that thle partial vapor press-are (when the d-rop-
let evaporates during the combustion process) is determined, ic a first apprcx-
Imation, by the medium fraction corresponding approximately t-) 50% distilla-
tion. It turned out that the computational combustion rate a-cording to the
diffusion theory appears too high in comparison with the experimental rate,
when the maximum actual temperature in the driplet's vicinity is used in cal-
culations. Some conditions are mentioned, which are not taken Intc account by
the computation procedure and may lead perhaps to a raise of the combustion
duration. A special experimental unit was built for perfcrming the first series
of experiments with relatively large fuel droplets supplied into the stream near
the thermo-couple joint and burnt at the thermo-couple. The temperature within
the furnace.was maintained constant at ab3ut 1,0000C, the relative f1cw velocity
amounted to 0.5 - 1.0 m/sec. The air cons,.Lmption amounted to 170 cm3/ser- of
st. air. The sequence of engaging the equipment from the instant of ~rcplet
supply into the stream was performed automatically. The evaporation temperature
was recorded wit-h an accuracy up to 0.5% by a platinum-iridium thermo-couple with
an electrode diameter of 10 LA-. The droplet dimension amounted to 0.9-1.5 mm.
Card 2/4
82805
ft4/6P, 7
S/1 24 /60/0X/,00 5/
A005/AOO1
Investigation of the Combustion of Liquid F~-,ei Droplets
Curves of the variations of the droplet's diameter and temperature versus the
time are plotted by evaluating t1he experimental data. It Is stated in the first
part of the experimental work that the d�ffusion theory may be applied to ~al-
culating the combustion rate of an individual droplet under the condition ',,hat
the Nusselt number is assumed to be 1.3 - 3.0 times greater than it results from
the Reynolds number. A seriAs of tests was performed with benzene for refining
the calculation scheme; benzene differs from tht polyfractioned mazout and
solar.oil by the definiteness of the physical constants. It turned out that the
computational temperature Is lower than the experimental, which may be explained
to a considerable extent by heat supply to the thermo-couple electrodes, In the
second part of the experimental work, the combustion of mazout- and sclar oil
droplets in suapended state was investigated, The test unit consisted of a vertical
furnace with d = 75 mm and H - 550 mm and with a window along thewall having '10 mm
in width and-400 mm In height, of a pneumatic sprayer with cooled diaphragms, an
air preheater, a fuel tank, delivery pumps, and a photocamera. The temperature of
the furnace walls was matntained constant within the limits from 930 t3 9500C. The
rate of air flow through. the furnace amounted tc 700-800 cn-j-3/see -of Et. air. The
combustion of solar oil uroplets of 193, 161 and 150,U diameter and w6zout droplets
Card 3/4
82805
AOO - /A~Y_- 1
Investigation of the Combustion of Liquid Puel Droplets
of 196/Jdiameter was studied. The film ln the photocamera moved a,
a velocity from 100 to 400 mm/sec. 7ne trails cf the burning drople-.s, the upper
and lower edges of-the window, and a chr-:,nopher (a neon lamp --onnected t~ the
alternating current net with 50 cps freqliency) were filmed simultaneously. The
duration of preheating and burning of the droplet was determined from the phcto-
record. The maximum average temperature In the stream was 5600C. A tiible of tne
evaluation results from recording is given for solar oil- and mazout droplets:
the table contains also computational data on '~he evaporation time deter~znlnation.
It is concluded: for obtaining by calculation the experimental duration of com-
bustion, the average value of the Nusselt numberfor combustion must be equ3L.-
to 3.65 for solar oil and to 4.5 for mazoul., at T2 = 0.65 '-.heor- If the tempera-
ture of combustion is assumed to be equal Tc, the theore"Acal temperature, th e
Nusselt number will be equal to 2.75 for solar oil and 3.47 for mazout. Srhemes
oscillograms, photographs, experimental. graphs, and a table are presented.
V.P. Veselagc
Translator's note: This is the full translation of 'he .r.'g-Inall Russian abstract.
Card 4/4
Sc
AUTHOR: Paleyev, I.I. (Dr.Tech.Sci.) & Svyatskiy, Z.M. (Cand.Tect
TITLE: The aerodynamics of multi-register combustion chambers.
(Aerodinamika mnogoregistrovykh kamer agoraniya)
PERIODICAL: Teploenergetika, 1938, Vol-5 No.3. pp. 16-20 (USSIL)
ABSTRACT: Modern combustion chambers are subject to high thermal loading 4ich
can only be achieved by efficient mixing of fuel and oxidant. A
prumising way of accomplishing this mixing is to instal a 'register'
round each mozzle which sets up its own aerodynamic zone so that
each burner can be considered as an independent fuel cozbustion unit.
An analysis of the operation of a multi-register burner, showed that
the combustion process is very efficient. The aerodynamics of a
rjulti-register chamber were accordingly studied to obtain an
understanding of the motion of flow in the chamber. Me tests were
carried out on a model chamber illustrated in Fig.l. The length of
the measuring section from the registers to the exhaust is 2 metres,
the internal diameter is 240 mm. The tests were made with four and
five registers installed on a spherical dime at an angle of 230 to
the horizontal. Each register contained four stumped blades set at
an angle of 701 to the inlet air. Outlet air velocities were up to
30 metres/second. The fifth register, vdien used, was (n the centre
line. Velocity and pressure measurements were made by probes at
Dard 1/3 pusitions given in the Table. Air that has passed through the
The Aerodynamics of mati-register combustion chambers
9i-3-5 A
registers acquires a spiral motion, centrifugal forces then set up
the presaure field shown in Fig.2. Axial velocity distri!)utitn curves
iii dimentionless units at five places in the chamber are given in
Fig.3. These curves show that near the registers each quadrint of
the chamber acts as an independent register. The axial velocity is
much lower in the central part of the common flow. The character of
flow rotation in a multi-register chamber, beyond the second
measuring point, is analogous with that of a single re.gister chamber.
11adial velocity curves at later sections of the chamber are given in
Table 5. Test results obtained with a five register model chamber
are then discussed. The method of measurement was the tiame as
before. The pressure field at the section nearest the registers is
shown in Fig.O. and here the influence of the central register is
appreciable. The axial velocities are of particular interest and it
is seen from Fig.7. that, at the first measuring section, the axial
velocities have five inflections. Thus the flows from the different
registers can be considered an independent. Reverse flows are small.
Beyond the second measuring section the axial velocities are similar
to those obtained with a four register chamber. The axial velocity
gradient is, of course, most important for turbulent mixing and it is
therefore advantageous to use a multi-register chamber with a central
Card 2/3 register. The conditions of mixing in a multi-register chariber are
The aerodynamics of multi-register combustion chambers. 90-3-512r,
then analysed mathematically. An expression is given for the
transfer equation and a similar equation can be written for heat
exchange. Expressions are obtained for the co-efficient of
turbulent diffusion and for the kinematic viscosity. 'MiS latter
is determined only approximately. Nevertheless the turbulent
exchange curves given in Fig.S. provide a comparative characterisLic
and show that in a multi-register chamber the exchange co-efficient
is several times greater than in a single register chamber. A
further advantage of the central register is that if need he it
can be used alone at light loads. There are 8 figures.
ASSOCIATION: Central Boller and Turbim Institute (Tsentml Inyy Kotloturbianyy
AVAILABLE: LiDr,,,ry of Conert--:
Card 3/3
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tarbulent ~~r;d SL;P-10('-~tS Liz,
citing the dimens ri n s j f t h +-- c,-,T, u -,i s r, z i n, F n,,:. t.v-
(!1 7, orna n ) a nd 41 n i v 1. n v e.,; L' i ga i e t n e r,
netter approximat ion in a 1-j"Int 1 t.;-tive 0:* t hC
f -!r tr:e ne,,, trans fer from bodies --)f' di ffc-rc-n~
a r d rs , n(1 i rig gus ' i,)ws by i rt t ri- a -j c i ng t ti i-
New i ri ncical , n Techn.,cal tnys ~~nV -, ' - 28-
s j r!'- c i-, ad a c ria ra c' t. r it, , i c ~ e ng. r '. F. E! 7
-:,inj !_,iri ty, A. i -. usnyin a pproacnea tne sam ne
case of a proD,em DI, ji,~ernai f.-j;- Tnp snort nc,.t(-S
Murasnl(o anc V . i . : ;li t, , ~ ti a c &,v R o ;i, a t ine
cs?,egory ol- pr,~Dien.~. `,,.vs~ n
probiems of sciii cec-z,r,,,4 atia D,, - ni n,,,. . exctiar.g, i. S-, _s
Tnt- note by :-. M.Kfiay.L.)v ~s h_z,, ' * ; : z ,;- ; a.
cleal ing w i tn convc7ctiun dry ing, 'as wt I i as ' ni t r!.v .V
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of awtermining optic.~il cf)pficients .:~C ma ei- i r~
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I oc, f, -;- ill;, I h I ii , ! 7t:* s r , t,!, t' -: ~- I r,) F- (: . --
I)T)!l 19 tp deppiri~_-nf i por T 1! - c r. , c1 ~ s h, 1*
b;:,,-: i fj is t ties c- t,ap (-rs . :-, t rLei 5 ur., :,sh-I ~n ;
Card whicri N. ':. ':vetiTskiy, 1 Anv, o, i i~
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I
I.. I . Tkacliov. and 1'. 'a. RFIS'.qK-Ija kre 'ne - .1 -
per I OU 1 ca 1 ti 1 su i ncorpo ra t es 1 t ems o f "Cr i t i,,a I -iev , ews ti. '-
Bi b1 i ograpi,..,, .. ,"F rc,m ~ L) ruad " , a na "Chron i c 1 e" .
SUBMITTE'D : JulY 10, 1958
Card 4 4
AUTHORS- Aref'yev, K,M,, Maslienenko, P,A
Paleyev,
TITLE! Calculating the evapcratlon c," liquid I r, ~i hc 1 J2:t!. w Eir:l
estimating the possibilltv - igniting t.,-.e f-r-ming
PERIODICAL; Referativnyy zhurnal, Mashinostroyenlye, zic 8, 1__, a,_s,raC-.
BI52 ("Nauchno_tekrLn. lnf.:rrT. tyl, Leningr p-Diltektr, '-r.-
no. 8, z, - 4)
TEXT, The authcr-q give an account of the calco-,ilation metncJ cf tne eva;:,~ra_
tion of a semi-dispersed aggregation of drops of liquid f-ael taking cons!-
deration the steam oxidation and the anisothermal character of the pr,~,cess, This
method is somewhat coinditional, but taken as a wh,Die it preee:,,-,s a true 2hara,--
teristic of the process and a correct order of magnitudes. Calc~la,t:,n reE_~-ts
are givEn, There are 11 1-1gures and 8 reterencers,
[Abstracter's note! Complete translationi,
Card 1/1
PALIM, I.I. prof.. doktor to)-hn.nauk: WiSLIGHMO, P.A., kand.tekbn.
nauk, RNUT , V-Ch., inzh.
Order of the reaction between stem and the coke of natural
fuel. 12V.r3rs.uchab.zav.: energ. 2 no.4:102-108 Ap 159.
(KIRA 12:9)
1. leningradakiy polital-hnicheakiy Inatitut imeni X.I.Xalinina.
Predstavlans kRfedroy toplofitiki.
(Chemical reaction. Rate of) (Stean) (Coke)
s/lq6/6i/ooo/oo6/ooq/oi4
E073/E535
AUTHOR Paleyev. I.I.
TITLE; On the behaviour of individual drops of heavy fuel in
chambers with a twisted flow
PERIODICAL: Referativnyy zhurnal, Elektrotekhnika i energetika,
1961. No.6, pp.8-9. abstra:t 6G56. (Sb. 3-e Tses.
xove*h.hAniye po tootli goroniya, T.2., M., 1960,
89-94)
TEXT; In mazout f~.red zombustion chambers of gas turbines,
a disturbance of the hydraulic conditions is frequently observed,
part:i(ularly at low load and no-load operation, which is caused by
the formation of appreciable deposits of coke on the walls of the
combustion chamber. This is due tc the fact that a small number
of drops of the heavy fuel hit the walls and adhere to it.
When this fuel in partly burned, cokt. 1.9 formed. Therefore,
it is necessary to establish whether all the fuel drops evaporate
without reaching the Drops which hit the wall may bounce
off and break up, The danger arises wher, +he combustion at the
wall is sluggish and a dense low-reactivity cQke forms.
Calculations were made on the evaporation of drcps in a combustion
Card 1/3
S/196/61/000/006/009/014
On the behaviour of individual E073/E535
chamber of 500 mm diamelor with a h1nde cnscade at 4S rh e
calculations are babed on spetd fields obtained on a cold model at
a pressure of 5 atm sx_-ess fee.-iing p.-imar~ air through a lattice
with an excess a - 1~2 , It is as!:umed that , due to reverse
currents and ignition of a part of the fuel behind the lattice,
the temperature of thf- flow riats from 200 to 1250'', It in 111AO
*j%L%umed Oini the 1.11ftision combustllun of the drops liroceeds at a
temperature of 23000C, The results are given of calculations for
drops with initial dimensions of IM 250 and 600 vL from which it
follows that the final dimensions of the drops at the wall are,
respectively, 0, 150 and 540 U. Consequently, under the considered
conditions mazout drops with an 1nitial diameter of about 250 4 will
no longer manage to evaporate and will hit the wall of the chamber.
The behaviour of thz drops on the wall was investigated on an
experimental rig in the form of a vertical tubular furnace. Into
this, drops of equal controlled dimensions were fod at a frequency
varying between 1/12-th and 1/25-th sec. The trace of the burning
drop was photographed. Into the furnace a plate was introduced,
the temperature of which could be controlled by built-in electric
Card 2/3
On the behaviour of individual S/196/61/000/006/009/014
E073/E535
cooling and electric heating, The drops heating the plate were
also photographed. Various cases of formation of spheroids, break-
ing up of drops during bouncing off and atomization of the fuel
along the plate were observed. The degree of combustion of the
drops was measuredo It is pointed out that if mazout is used
a a fuel it is advantageous for the walls of the chamber to be
t the maximum permissible temperature.
:
Abstracted by S. Tager.
Abstractor 9 Note~ Complete translationi
Card 3/3
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h a p it n f r.9 - I. Th E u,i 1 ha n,l) n , a I n e d
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E194/13415
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