SCIENTIFIC ABSTRACT SLINKO, I. - SLINYAKOVA, I.B.

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• Collection: Scientific Abstracts
• Document Number (FOIA) /ESDN (CREST): CIA-RDP86-00513R001651320013-9
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• Document Creation Date: November 2, 2016
• Document Release Date: August 25, 2000
• Sequence Number: 13
• Publication Date: December 31, 1967
• Content Type: SCIENTIFIC ABSTRACT

SLINIKO, I., inzhener.
Improved method of roof control. Hast.ugl. 6 no-5:10-11 MY '57,
(MM 10:7)
(Karaganda BAsin--Conl mines and mining)

FOMAZANOVSKIY, Yu.; SLINIKO 1.
Load the cutter-loader fully-. Sov. shakht. U no.6:10-11 Je
163. (KERA 16:9)
(Donets Basin--Coal mining machinery)

I.S., POPOV, N?F-
Improved method,of roof control in the OTysheerednii,3 *Sloistyi"
and "Shestifutovyi* seams. Nauch. trady KNrU1 no.2:28-55 158*
(KIRA 13:8)
(laragailda Basin-Coal mines and mining)
,,(Nine timbering)

KVMSNIK@ OJ@5 -SLINIKO, I.S.
Combi.vat-ion of :Lndustrial procesc-es in cutter-loader mined
steep seam longwalls. Ugoll 40 no.3:51-54 Mr 1065. (MIRA 18:4)
1. Donetskily nauchno-iasledovatellskiy ugoliny-y institut.

NR, SOURCE 0 E: UR/0125/66/666/W4-/106i-~7602:7-7,'
AUTHORS: Malinochka, Ya. N.; Favlova, S. D.; Slin1ko, L. A.
ORG: Dnepropetrovsk Institutoof Iron MetaljLirg (Daepropetrovskiy institut chernoy
metallia;-g-ii)
TITLEi Structure and properties of welded seams in low alloy steel pipes
SOURCE: Avtomaticheskaya svarka, no. 4, 1966, 13-17
TOPIC TAGSt metal welding, seam welding, metal property, alloy steel / lLKhGS alloy
steel, 17GS alloy steel, 14GN alloy steel
ABSTRACT: The structure and properties Pf welded Joints we investigated before ant
after heat treatment to determine the @asonj," Or crac 1@f welded joints in 1020-
GN eel. Photographs of the
. I
mm. diameter steel pipes made of 14KhGS, 17GS,
weld rderostructures are presented for various corAitions of heat treatment, and the
strength properties of the base metal under various temperOure conditions were
determined. A considerable amount of martensite is forme2n the seam, increasing
its strength and hardness but decreasing its plasticity. racks are formed during
expansion of the pipe under low temperature conditions, and these grow along
interaxial dendrite portions of the weld. These cracks can be prevented by temperinE
of the welded seam at 450-500C. N. M. Yan and E. & Novikov helped with ..,he
experimental work. Orig. art. has.- figures*
4z CODE: 13
SUM DATE.- IBDec65/ ORIG REF:.
(@Vrg 171 '7@ I=. C&-7Q'L-M)i-12!669.15-191L

@' I _Aj k c , I- _. J, -
USSR/Zooparasitology - Acarina and Insect--Vectors of Disease G-4
Pathogens.
Abs Jour Ref Zhur - Biol., No 3, 1958, loo98
Author Nellzinal E.N., Slinko, L.I.. Kadrtskaya, K.P., Ivanov,
K.A., Yamshchikova, i1'.G'_._',"`P_O'lt&vtsev, N.N., Skirda, G.I.
Inst
Title Ixodic Ticks (Parasitiformes, family Ixodidae) of Rodents
in Northwestern Caspian Coast.
Orig Pub : Sb. tr. Astrakhansk. protivochumn. st., 1955, No 1, 416-
433
Abstract : The fauna of ixodic ticks in the district studied is com-
paratively sparse (5 species, more or less, are numerous);
individual specimens may be regarded as of Kirgiz and
European-Siberian origin. Closest biocenotic ties with
rodents are found in Ixodes laguri laguri ancl Thipicepha-
lus schulzei. 11he first of these (steppe species) is con-
nected with rodents who build deep, comparatively
Card 1/2

USSR/Zooparasitology - Acarina and Insect-Vectors of Disease G-4
Pathogens.
Abs Jour - Ref Zhur - Biol., No 3, 1958, loo98
permanent burrows (susliks, hamsters) and is surmised to
play a substantial role in the epizoology of tularemia
and some ricketsioses amng susliks, hamsters and field
mice. Rh. schulzei inhabits semideserts; its principal
hosts are the sTmll and yellow susliks.
Card 2/2

GEYSBERG, S.M.; SLINIKO. L.Y.
Ways of increasing the strength of staple fiber. Khim.volok.
no.6:73-74 159. (MIRA 13:5)
1. Leningradgkir 2avod.
(Rayon)

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MALVII X. K IURYM71 ". L.
Sulfuric Acid
"Production of sulfuric acid." Reviewed by D. A. Yepshteyn, Zhur.prikl.khim. 25 No. 4, 1
9. Monthly List of Russian Accessions, Library of Congress, August -195@, Uncl.
2

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USSR/Chemistry - Catalysts; Sulfuric I Sep 53
Acid
"Catalytic Activity of Ketals and of Platinum-
Gold Alloys in Respect to the Oxidation of Sulfur
Dioxide,* G. K. Boreskov, M. G. Slin1ko, and Ye. I.
Volkova,
DAN SSSR, Vol 92, No 1, pp 109,110
Studied the catalytic activity of Cr, Rh, Pd, Ag,
W, Pt, Au, and of an alloy consisting of 5% Au and
95% Pt on the oxidation of S02- Most of the above
aetals had a low activity due to their instability
under the conditions of the reaction. At 5600 Pt
274TI2
is more active than Au, but the Pt-Au alloy has a
lov activity. Refutes the conclusions of D. A.
Dovden, Chem Soc, Issue 1, 245, 1950. Presented
by Acad M. M. Dubinin 3 Jul 53.

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LURIYE,G.E., redaktor; BCRESKOV,G.K., redaktor; NABEREZ-9NM,M.Ye..
redaktor; PSHBZHETSKIT,S.Ya., redaktor; SLINtKO M.G., redaktor;
TEMKIII,M.I., redaktor; CHRMNICHKNKO,V.M., redaktor-,- SHPAK,Ye.G.,
teldinicheskiy redaktor
[Heterogeneous catalysis in the chemical industry; papers from the
All-Union Conference, 1953] Geterogennyi katalis v khimicheskoi
promyshlennosti; materialy Voesoiuznogo soveshchaniin 1953 god&.
Moskva, Goa. nauchno-tekhn. izd-vo khim. lit-rY, 1955. 494 p.
(KILPA 9:2)
1. Russia (1923- U.S.S.R.) Hinisterstvo khimicheskq promyshlen-
nosti. (Catalysis)

1721
USSR/Chemi.ctry - Cutalysis FD-1729-
Card 1/1 : Pub. 50-5/18
Authors : Prof. Boreskov, G. K., Dr Chem Sci; Slin'ko, M. G., Cand Chem Sci
Title : Experimental methods of determining catalytic activity
Periodical : Xhim. prom., No 1, 19-26., Jan-Feb 1955
Abstract : On comparing the static methods, dynamic circulation methods, and
stationary circulation methods for the laboratroy testing of catalysts,
arrive at the conclusion that the stationary circulation methods are
the most reliable. Point out that stationary circulation methods cannot
be easily applied to the testing of catalysts on a large scale and should
be replaced by simpler, although less exact circulation methods for that
purpose. Describe all of these methods and the diaphragm method. Six
figures. Twenty nine references; 25 USSR, 23 since 1940.

AF701597 TREASURE ISLAND BOOK REVIEW AID 813 - S
(Phys.-Chem. Institute im. L. Ya. Karpov)
(Discussion). In Problemy kinetiki I kataliza
(Problems of Kinetics and -da-talysis), vol. 8. Izdatellstvo
Akademil Nauk SSSR, 1955. Section II: General problems of the
theory of catalysis. p. 148-150.
A study of kinetics and mechanism of the interaction between hydro-
en and oxygen In order to establish the role of surface chains
Laboratory of Technical Catalysis, Physico-Chemical Institute im.
T
L. Ya. Karpov) showed that at temperatures of 180CCand above the
catalytic activity of Pt, in the presence of excess oxygen, is
readily established and-does not change for a rolonged period of
time (about 7 months). At low temperatures ( 1tOOC and below), the
activity of Pt depends on the following: 1. The activity of Pt
is high on rapid trans-ition from high to low temperatures;
2. After evacuation of air for a short time'or a prolonged break
in work at low temperatures (560C), the activity of Pt is low;
3. The energy of activation in the region of high activity is
@'-2400 cal and - 10,000 cal in the region of-"low activity.
4. Oxygen adsorbed on Pt does not react with hydrogen at low
temperatures.
1/1

) ':'@ "", .I.- .1 Z-I1 11 11 1@
. '. i
BORESKOV, G.K., doktor khim.nnuk, prof.; SLIWK0, M.G., knnd.khim.nauk.
Applying the fluidized bed method to heterogeneous cntalysis
processes. Khim.prom. no.6:321-330 S 157. (MIRA 11:1)
l.Fiziko-khimichaskiy institut imeni L.YFI. Karpova.
(Catalysis) (Fluidization)

AVDIUNKO, M.A. BOB KOV, G.K.; SLIN'KO, M.G.
Catalytic activity of metals in respect to hosomolecular isotopic
exchange of hydrogen. Probl. kin. i kat. 9:61-75 '57. (MIRA 11:3)
(Catalysis) (Radioactive tracers)

DYKE=, N.M., kand.khim.nauk; CHERITYSHEV, B.A., inzh., SLINIKO, M.G.,
kand.khim.nauk.
Removal of argon from oxygen by means of catalytic h,7drogenatuion.
Kislorod 10 no.4:14-24 157. (MIRA 11:2)
(Argon) (Oxygen) (Hydrogenation)

.-V " 14 @," I , , @
SLINIKO, M.G.
-. .
Georgii Konstantinovich Boreskov; on ihe occasion of
birthday. Zhurfis.khim-31 no.7.'1670-1671 JI '57.
(Boreskov, Georgii Konstantinovich,
his 50th
(MIRA 10:12)
1907-)

The Effect of the Processes of Mass and Heat 64-58-3-3/2o
Transfer on the Reaction Velocity of the Ethylene Oxidation
kinetics were thoroughly investigated by A. 1. Kurilenko,
It. A. Rybakova, 1-1. V. Kullkova and 14. 1. Temkin (Reference 9)
--ho p
ointed to the kinetics at stationary and standard compo-
sition of the catalyst. The computation equations as obtained
by t@,e.%i are given as -;,,ell as mathematical deviations for the
influence of the process of the transfer to the external
surface of the catalyst grains. For that purpose the value
RT2
- 0 is used which was introduced by D. A. Frank-Yamerietakiy
E
(Reference 2) and it was stated that with a difference between
Vie temperatures of the catalyst surface and of the gas which
is smaller than the mentioned value the conditions of the
kinetic range are given. The publications of Mazzolini (Refer-
ence lo), T. I. Adrianova and 0. M. Todes (Reference 7) con-
tain virong propositions as they assumed a diffusion range
instead of a kinetic range. In the explanations of the influence
of the process of transfer to the internal surfaces of the cata-
Card 2/3 lyst grains among other things an equation is obtained ana-

Effect of the Processes of Mass and Heat 64-58-3-3/2o
Transfer on the Aeaction Velocity of the Ethylene Oxidation
lo@ous to that of G. K. Boreskov (Reference 3) with sulfuric
acid catalysts, and it is stated - as was done in the experi-
nental investi-lition (Reference 9) - that the catalyst acti-
bI
vity up to 300 io independent of the grain size. It was statea
that in order tG guarantee a stationary process in the kinetic
range t"ie difference between the temperatures of the center of
the reaction pipe and of the pipe surface must not exceed
2
1,37 RTQ_ and that the difference between the
E
tem;)eraturas of the reacting .---s and of the cooling liquid must
2
be s;naller than Te, The individual experimental results
E
which are @iven in tabular and in Graphical form refer to ex-
peri@-ientaal conditions nainly at 2180C. There are 6 figures, 3
tables and 11 relerences, 8 of which are Soviet.
1. Ethylene--Oxidation 2. Silver catalvsts--Performance
3. Catalysts--Tempez-ature factors 4. Chemical reactions--Feat
-transfer

SLINIKO, M.G.
- --I.-,----Bffcidt of mass and heat transfer processes on the velocity of the
oxidation of ethylene. Khim. prom. no.3:138-146 k-D-MY(I 58.
(Nthylene) (Oxidation) MIRA 11:6)

AUTHOR: G. 76-32-4-36/43
Slin1ko
M
.
,

TITLE: On filr@@ed by Mass and Heat Transfer in the Production
of Ethylene Oxide (0 roli masso- i teploperedachi Y protsesse
polucheniya okisi etilena)
PERIODICAL: Zhurnal Fizicheskoy Khimii, 1958, Vol. 32, Nr 4, PP. 943--944
(USSR)
ABSTRACT: The equation formed by Mazzolini (Refs 1,2) according to which
the reaction velocity of ethylene oxidation is equal to the
velocity of the mass transfer of ethylene to the catalyst's
surface is insufficient, as it has to be taken into account
that the velocity of mass transfer and1heat 'transfer are very
similar. Two equations of the material balances an*eat ba-
lances are given which can furnish one or three solutions. One
solution always corresponds to the field of external diffus-
ion, while the three solutions correspond: one to the regime
of the kinetic field, the second to the regime of external
diffusion and the third to an unstable regime which once pass-
es over to the first and another time to the third. At a con-
tent of 3% ethylene of the air and a 6oc/a selectivity the adia-
batic combustion amounts to 6450C and the surface temperature
of the calalyst to 8450C (at a gas temperature of 2ooOC).At
Card 1/2 this temperature ethylene oxide oxidizes to carbon dioxide and

On the Part Played by Mass and Heat Transfer in the Production 76-32-4-36/43
of Ethylene Oxide
water so that the temperature of the catalyst still rises
further, from which fact is concluded that the assumptions by
Mazzolini are incorrect. It is proved by data that the latter
carried out his experiments under conditions where the velocity
of mass transfer of ethylene had no effect on the general re-
action velocity. Similar errors wore committed by T. 1. And-
rianova and 0. X. Todes (Ref 3) in their worka. There are 5
references, 3 of which are Soviet.
ASSOCIATION: Fiziko-khimicheskiy institut im. L. Ya. Karpova, Moskva
(Moscow Physico-chemical Institute imeni L. Ya. Karpov)
SUBMITTED: October 19, 1957
AVAILABLE: Library of Congress
1. Ethylene--Oxidation 2. Ethylene--Catalysis
Card 2/2

5W
AUTHOR: Slinlk:), M. Go, SOV/76-32-12-28/32
TITLE- -The Ulse-@@,,is@q-Liquid Layer for Heating and Cooling in
Laboratory Investigations (Primeneniye psevdoozhizhenjiog0(a.1oya
dlya obogTeva i okhlazhdeniya pri laboratornykh issledovaniyaKh)
PERIODICAL: Zhurnal fizicheskoy khimii, 1958, Vol 32, Nr 12, pp 2841-2842
(USSR)
ABSTRACT: The use of tube furnaces and liquid baths is inconvenient and
often not appropriate. It is difficult to effect transitions
to other temperatures. These difficulties can be avoided by
using the pseudo-liquid layer of an inert, nonvolatile,
noncaking material such as aluminum oxide, silica gel,
carborundum, sand, aluminum silicates, etc. as heat transferring
agents. A figure illustrates such an apparatus. Advantages:
1. no temDerature differences throughout the furnace;
2. intensive heat exchange; 3- fast and continuous temperature
changes are pessible; 4. there is no danger of inflammation or
of poisoning by organic compounds which are otherwise used as
heat transferring agents. There are 2 fig-ares.
Card 1/2

5W SOV/20-127-1-39/65
AUTHORS3 Khartkovskaya, Ye. N., Boreskov# G, X., Corresponding Member
AS USSR, Slin1ko, M. G.
TITLEt The Kinetics of Interaction Between Hydrogen and Oxygen on
Platinum (Kinetika reaktaii vzaimodeystviya vodoroda a
kislorodom na platine)
PERIODICALi Doklady Akademii nauk SSSRI 1959, Vol 127, Ur Ig PP 145-148
(USSR)
ABSTRACTs The measuring results hitherto supplied by publications
concerning the interaction mentioned in the title are contra-
dietory (Refs 1-5)- Ibcpariments were made within too narrow
concentration ranges or under conditions that did not allow
accurate measurements. The mentioned internotion was therefore
carried out at temperatures of from 20 to 1800, pressure of
from 50 to 750 torr and different compositions of the reaction
mixtures in a circulation system, Investigations were made on
hydrogeng nitrogen-hydrogen mixturesp nitrogen-oxygen mixtures
and oxygen. FlatiAum, was used in the torm of 0,1 mm gauge wire,
The circulation rate varied between 400 and 1100 1/h. The
reaction rate proved to be independent of the circulation rate
Card 1/4 and of the nitrogen partial pressurel it depended only on the

The Kinetics of Interaction Between Hydrogen OOV/20-127-1-39/65
and Oxygen on Platinum
partial pressure of hydrogen and oxygen, Pigs 1-3 show the
miasuiing results for the different concentrations and
temperatures as well as the influence of the pre-treatment of
platinum with hydrogen at inoreaeed temperatureng figure 4 the
dependence of the reaction rate on the H2_ and 02 concentration
at 1800. Experimental data are indicative of a complicated
catalytic process. In mixtures with hydrogen excess, the
reaction of the first order (referred to 0 2) and its being
little dependant on the pressure of H2 , permit the conclusion
to be drawn that here the interaction between chemically sorbed
atomic hydrogen, which covers the platinum surface, and
molecular oxygen, forms the limiting stage. The oxygen reaction
is made easier by interaction with the d-electrons of the
catalyst (adsorption type C according to Dowden, Ref 11).
If the oxygen is not altogether removed from the platinum
surface, O-atoms remain adsorbed to the surface by means of the
d-electrons of the metal (type B)j and the activity of platinum
Card 2/4 drops. When passing over to stoiohiometric 92-0 2-mixtures,

The Kinetics of Interaction Between Hydrogen SOV/20.;127-1-39/65
and Oxygen on Platinum
the platinum surface is freed from hydrogen, and a chemical
sorption of the oxygen with dissociation into atoms is made
possible. (Type A). In this range the reaction proceeds by
interaction of the atomically adsorbed oxygen Yrith H 2; this
requires less activating energy, and causes an increased
reaction rate. In the case of oxygen excess, two stationary
conditions are possibler which differ by the reaction rate and
dependence on concentration of the components. The readily
occurring reaction is likely to be related with a chain
process, in which high-energy endothermal products participater
which are regenerated in the course of reaction. On lowering
the temperature and temporarily evacuating the system, these
unstable products vanish, and there only remains a relatively
tightly platinum-adsorbed oxygen which reacts with hydrogen
slowly and with increased energy demand. The decreased
Card 3/4

The Kinetics of Interaction Between Hydrogen SOY/20-127-1-39/65
and Oxygen on Platinum
reaction rate at increased oxygen pressure is probably due to
a partial blocking of the platinum surface by tightly adsorbed
oxygen. There are 4 figures and 11 references, 8 of which are
Soviet.
ASSOCIATION: Nauchno-@-isoledovateltskiy fiziko-khimicheskiy institut im.
L. Ya. Karpova (Scientific Research Institute of Physical
Chemistry imeni L. Ya. Karpov)
SUBMITTED: March 30, 1959
Card 4/4

S/064/60/000/01/04/024
3022/B008
AUTHOR: Slintko, K,
TITLE: On the Role of lase-transfer Processes In the Catalytic
Oxidation of Naphthalenelto Phthalic Phydride.lRemarks on
the Paper bX 1. 1. Ioff-e and 1. F. Grigorov "K teorii
skorostey reakteiy v pseydoozhizhennom sloye katalizatora"
("On the Theory of Reaction Rates in a Pseudo-liquid Layer
of the Catalyst")
PERIODICAL- Xhimicheskaya promyshlennostIq 1960, No. 1, pp. 24 - 25
TEXT: It is stated in the paper by I. I. Ioffe and A. F. Grigorov, which
is critically examined, that the reaction rate mentioned in the title is
determined by the rate of mass transfer of naphthalene from the gas cur-
rent to the surface of the catalyfit grains and that with a low rate of thez
gas currenty external diffusion and the transition range are characteristic
of the processes concerned. These statements are refuted by the author.
The dependence of the mass-transfer coefficient on the diameter of the
particles and the rate of the gas current, is mentioned (Table). There are
1 table and 12 references., 3 of which are Soviet.
Card 1/1

Computation of Catalytic Processes in S/064/60/000/03/03/022
Industrial Reaction Apparatus BO1O/BO08
stroyeniya (Institute of Computer Construction)p as well aa -3r-csponding
diagrams a@plying the data by M. I. 7emkin et 1. (Ref. 3) are -hown
(Figs. 798 . Computatione for the application of apparatu, with pseudo-
liquid layer in exothermic processes are also mentioned. Uumputations of
the limit of stable working conditions of contact apparatus are explained
for heterog6neous catalyses by means of pseudoliquid catalyst layers, the
method by A. M. Lyapunov (Ref- 5) applied in mechanics as well as a paper
by D. A. Frank-Kamenetskiy (Ref. 8) are ment-;oned, andan explanation of the
critical conditions is given. It is finally pointed out that electronic
computers permit the solution of complicated computations of the course
of catalytic procesBesq such as multi-stage processes with reactions
developing parallel and successively, catalyses in which the activity of
the catalyst drops quicklyg etc. There are 10 figures, 1 tableg and
8 references: 7 Soviet and 1 American.
Card 2/2

,@SLINIXO, M.G.
Determination of stability conditions for exothermal contact
processes in a fluidized bed. Kin. i kat. 1 no.1:153-161 Ny-Je
16o. (MIRA 13:8)
1. Institut kataliza Sibirskogo otdelenlya AN SSSR.
(Heat-Transmission) (Catalysis)

BOiWKOV, G.K.; SLINIKO. M.G.
Second European Symposium on Chemical Technological Processes.
Kin. i kat. 1 no. 3:483-487 B-0 16o. (MIRA 13:11)
(Europe--Chemistry, Technical--Congresses)

I
I- -SLINIKO, M.G.
Methods of generalizing the experimental data on the rates of
contact processes. Khim.prom. no-4:265-267 Ap 161.
(Imu 14:4)
(Catalysis)

CHESNOIKOV, B.B.; SLINIKO, M.G.; JERNENW, V.Sh.
Determination of the crftical velocity of gas fluidizaticin under
pressure. Khim.prom. no.11:767-768 N 161. UaRi 15a)
(Fluidization)

SLIN2KO, M.G.; BESKOV, V.S.
Design of contact apparatus with adia ic beds of catalysts for
the oxidation of sulfur dioxide (design of contact apparatus with
intermdiate boa exche ars). Khlm.prcmi. no.22-.826-831 D 161.
NIFLA 15 -.1)
(Sulfur dioxide) (Chemical engineering-Equipment and supplies)

SLINIKO, M.G.
All-Union Conference on methods for determining the activity of
catalysts. Khim.prom. no.12:870-871 D 161. (MIRA l5c-1)
(Catalysis-Congresses)

S/195/61/002/003/009/009
E030/E433
AUTHORS: Slinlko, M.G., Muler, A.L.
TITLE. On the stability of adiabatic contact plant iviLh licat
exchange
PERIODICAL:Kinetilta i kataliz, v.2, no.3, ig6i, 467-1,78
TEXT: A theory is developed for the stability of apparatus
consisting of a heat exchanger with a bypass recirculator and a
reactor. ifithin the reactor, external diffusion holds if the
velocity of the process exceeds that of introducing the reacting
gases (as in oxidation of methyl alcohol to formaldehyde) and
otherwise internal diffusion holds (as in oxidation of ethylene -to
thylene-oxide, the oxidation of sulphur dioxide etc); both cases
.are treated. Using inass balance and heat flow equations, for
general order of reaction a series of equations are developed using
the Frank-Kamenetskiy method (Ref.5: D.A.Frank-KaiaenetsRiy,
Diffusion and heat transfer in chemical kinetics, Izd-vo AN SSSR,
M.-L., 19117) and are expressed as a dimensionless form:
Card 1/4

S/195/61/002/003/009/009
On the stability of adiabatic ... E030/7-433
Type of Form of Equation (13) Parameter
rimction function of C
20

b -C
0
I/
0.5th. order C0.5 A .+i
1+4e' e O
L el =
k,,,r
0 1
lst order C AOjA 0 1 + Cle Ob.+L El = k@j
2nd order C2
- -L I
e- Ob.+i 61 +
6 I

--tC
CL - -jj@
i'A ,,
,
Ob.+I Ob'.+l
ele- Go- +10
1
Limited by
CT 0
reaction products + ele
AO@A eL k,,T
20
+ + E2e 0604-1 -1 2e, (a + 1) e
I r Ob.+i
Card 2/4

S/195/61/002/003/009/009
On the stability of adiabatic E030/E433
C is concentration of reacting gas, Llgaft is the change in
temperature on adsorption of the gas on the,catalyst and'
0 the mean temperature expressed dimensionlessly as
2
T = 0RTO + To
E
where T is the initial gas temperature,, x is the time of
contact. a is a constant, as is bo, Co is the initial gas
concentration and' kH the velocity constant of the reaction,
Eq@(13) is the general form of @a = El@ bo)o The.
transitions between thi diffusion regions are determined by Ej,
n-
which equals 1/kHTCO and its- magnitude relative to the
coefficient of mass tra smission P and the dimensionless
,n-1. to -
parameter E2 = P/kH 0 Acknowledgments are expressed - zhz
Corresponding Member of AS USSR G.K.Boreskov for discussing @_hs
results of the present work. There are 9 figures and
6 references-. 3 Soviet-bloc, 1 Russian translation from non-Sov-J&v
authors and 2 non-Soviet-bloc, The two references to Enilish
language publications read as follows-
Card'3/4

S/195/61/002/003/009/009
On the stability of adiabatic ... E03O/E433
Ref.2: C. van Heerden, Ind. Eng. Chem., v.45, 1242,, 1953i
Ref.3'. C. van Heerden, Chemical Reaction Engineering, 1,
Pergammon Press, N.Y., 1957, P@133-
ASSOCIATIONS,. Institut kataliza SO.AN SSSR
(Institute of Catalysis, SO AS USSR)
F!ziko-kh!m!cheskiy institut im, L,Ya,Karpova
(Physicochemical Institute imeni L.Ya.Kar-pova)
SUBMITTED5 April 8, ig6i
Card 4/4

SLINfKO, M.G.; YEPIELIYANOV, I.D.
t--- - - - -
Stability of reversible exothermic processes in a fluidized bed.
Kin.i kat. 2 no,4:622-625 J1-P9 '61- (KMA 14:10)
1. Institut kataliza Sibirskogo otdeleniya All SSSR.
(Fluidization)

SOKOLY D.; SLINIKO, M.G.
First International Conference In Prague on Fluidization Techniques.
KinA kat. .2 m.4:637-638 31-Ag 761. (@aRA 14:10)
(Fluidization-Congresses)

LELZAHINEVA, K.A.; BORISOVA, T.I.; SLINIXO, M.G.
Anodic oxidation of sulfui-dkiid@@on gold and platinum-gold
alloys. Kin.i kat. 2 no.0':854-861 N-D 161. (MA 14-12)
1. Fiz@ko-khimicheskiy institut imeni L.Ya. Karpova.
(Sulfur dioxide)
(Oxidation) (Platinum-gold alloys)

SLINIKO, M.G., kand.khimicheskikh nauk
Use of electronic calculating machines for the design of contact
apparatus. Zhur.VKHO 6 no.5:544-548 161. (IMA 14:10)
(Electronic calculating machines) (Chemical apparatus)

BORESKOV, G.K.; SLINIKO, M.G., -kand.khim.nauk
Modeling of catalytic processes. Vest. AN SSSR 31 no.10:29-35
I
0 '(11. (MIRA 14:9)
1. Chlen-korrespondent AN SSSR (for Boreskov).
(Catalysis)

S/06J/62/000/003/001/007
'B 110/3101
AUTHORS: Slinlko_, Ostrovskiy, G. It.
TITLE: Use of computers for controlling contact processes
PERIODICAL: Khimicheskaya promyshlennost', no. 3, 1962, 1 - 7
TEXT: As re.-ards computer control, contact processes fall into the
following groups: (A) steady processes in the stable region, using
catalysts of long-sustained effect, requiring either (a) maintenance of
the optimum made that corresponds to given initial conditions, or (b)
optimum conditions close to the permissible limit. (B) steady processes
in the unstable region with catalysts of long-sustained effect, (C) un-
steady processes with decreasing catalyst activity, (D) contact processes
with variable composition of the reaction mixture. The following are cases
corresponding to each of these groupsi (A) (a) reversible exothermal pro-
cesses (sulfur dioxide oxidation, NH3 synthesis, reaction of CO with H 20
va.por etc.). Here the optimum conditions can be.tabulated with the aid of
computers. (b) Irreversible exothermal processes (partial hydrocarbon
oxidation; production of ethylene oxide, maleic anhydride, phthalic.
Card 1/2

S/195/62/003/001/008/010
E071/E136
AUTHO'R,S Slinlko, j%I.G., Buzhdan, Ya.!,'., Beskov, V.S., and
Yemellyanov, I.D.
TITLE: Optii;@al conditions for the production of
ethylene oxide
1@-",,IODICAL: Kitietika i kata'liz, v.3, no.1, 1()()2, 145-1511
TEXT: The use of coi,,iputers in the design of multilayer
contact Dlants is illustrated on an example of determining the
optilralm technolo.gical conditions for the process of oxidation
of ethylene in consecutive layers of a catalyst w-ith an ideal
mixing and in a stationary layer at ideal displacement. It was
shoun that for two parallel reactions in which the energy of
activation of the side reaction is higher than that of useful
reaction, the temperature should increase with an increasing
degree of conversion. The necessary arrount of catalyst for
various outputs of ethylene oxide was calculated.
There are 6 figures and 4 tables.
Card 1/2

BORESKOV.0 G,K.; VASILEVICH., L@A.; CURIYANOVAp R.N,,; KERNERMAN) V.Sh.;
SLINIKOIV M.G.; FILIPPOVA, A.G.; CHESNOKOV, B.B.
Oxidation of ethylene in a fluidized bed of a catalyst. Kin.i
kat. 3 no.2-214-220 Mr-Ap 162. (MIRA 15'.11)
1. Institut kataliza Sibirskogo otdeleniya AN SSSR i Fiziko-khimi-
cheskiy institut imeni L.Ya.Karpova.
(Ethylene) (Oxidation) (Fluidization)

SLINtKO, M.G.; OSTROVSKIY, G.M.
Use of calculating -a hines in the control of catalytic processes.
Khim.prom. no.3:153-159 Mr 162. (MIRA 1514)
(Catalysis) (Calculating machines)

SLINIKOP M.G.; TYURY-AYEV, I.Ya.; KUZNETSOV, Yu.1.
Optim= operating conditions for hydrocarbon dehydrogenation
columns. Khim.prom. no.4:253-259 A 162 (MIM 15:5)
(Hydrocarbons) (Dehydrogenation@ (Ca;alyisis)

BORESKOV, G.K.; SLINIK@@
Theory of similitude principles applied to heterogeneous
catalysis. Khim.prom. no.6:418-421+ le 162. (KFA 15:11)
(Catalysis) (Chemical models)

SLINIKOY M.G.; BESKOV, V.S.; SKOMOROKHOV, V.B.
Stability of contact apparatus having internal heat exchange.
Khim.prom. no.9t641-647 S 163- (MERA l6s12)

BF3KOV, 710,3.:, BUZ-.qDkN,. Y&.M.w 3LIN'KO,, M.G.,@ P-'-J.TllM8.l' -W@Ilastlye AKIMUTINP
. N. IM @ 1 -1-1 .. @ I
Design of @:ontttct with beeds of a Zatalyab for
tlif3 oxiliation of' sulfur diaxide. Khim. prom. no.10i.-721-724 0 163.
(MIRA 1'7 a 6)

VOLIN@ Yu.M.; OSTROVSKIY, G.M.; ST,INIKO, M.G.
Principle of the maximum in deteraining the optJ-rnum conditionis of'
exothermic processes. KInJ kat. 4 no.5:7604-767 S-O 163.
(MIRA 16@-12)
1. Fiziko-khimicheskil institut imeri L.Ya.Karpova i Institut
kataliza Sibirskogo ofdeleriiya AN SSSR.

BORESKOVI G.K.; SLINKO, M.G. (Slintko, M.G.]
Application of the methods of s itVe theory in heterogenous
'T L7 189 Ap-je 63.
catalysis. Analele chimie 18 no k
I
I

BORESKOV, G.K.; SLIWKO@.M.G.
Basic principles of the modeling and optimalization of chemical
reactors, Khim.prom. no.lt22-29 Ja 164. (MIRA 17:2)

BESKOV, V.S.; LIBEAZON@ L.M.; 44P@'-Koo M.G.; Prinimali uchastiye. A&XTIN,,
N.M. BURYAK, K.A.; SHINDEROVAO T.A.
Determining the static characteristics of a contact apparatus for
the oxidation of sulfur dioxide in order to achieve the optimiza-
tion of the process. Khim. prom. 40 no.9:678-680 S 164. (MIRA 17:11)
1. Institut kataliza Sibirskogo otdeleniya AN SSSR (for Akimutin).
2. Nauchnyy instAtut udobreniy i insektofungisidov imeni professora
Ya.V. Samoylov@# (for Shinderova).

KAGAN, Yu.B.; ROZOVSEY, A.Ya.; SLINIKO, M.G.; PONOMAREUKO, A.T.
Kinetics of heterogeneous catalytic reactions as a function of
ignition conditions. Part 2; Reaction of an arbitrary order.
Kin.1 kat. 5 no.6:1111-1114 N-D 164.
(MIRA 18:3)
1. Iritititub neVtekhImichesIcogo :iinteza Lmeni Topchiyeva AN SSSR
i Institut kataliza Sib:Lrckof,,o otdolenlya AN SSSRO

NEDUMOVAI Ye.S.; BOUSKOV, G.K.; SLINIKOY M.G.
Kinetics of isotope exchange between hydrogen and water
vapors on nickel catalysts. Part 1: Effect of transport
processes on the reaction rate. Kin. i kat. 6 no.1:65-73
Ja-F 165. (14W 18: 6)
1. Moskovskiy khimiko-tekhnologicheskiy institut imeni
Mendeleyevs. i Institut kataliza Sibirskogo otdeleniya
AN SSSR.

-- . ...I
--, -@ - *,,-,- , , , ',@-UZIII, V.,_9 . . '0, @ C,- t --s'
.. @ Is 11.1 @ - @ -ne bed Of a ca.-aij-@.
ical ill t, " - -1
. - I - chem- - . -_:t:o,
0@, 1@,r
-. 41 no - 1: L-9 Ja
P-r"j"

j
L 8495-66 94T(.m)/FWP(J)/T/]W.P(.t)/94P('?). JDAM
ACC NR: AP5026478 SOFRCE CODE- UR/0195/65/006/005/0909/0915
AUTHOR: Yermakov, Yu. I.; Boreskov , G KSlinsko M G ; Skomorokhov, V. B.
ne-
ORG: 7institute of Catalysis, SO AN SSSR (Institut kataliza, SO AN SSSR)
TITLE: Kinetics and mathematical modeling of the process of suspension polymerization
of ethylenegon a chromium trio.-dde catalyst
SOURCE: tika i kataliz, v. 6, no. 5, 19651 909-915
TOPIC TAGS: polymerization rate, ethylene, mathematic model, chromium oxide
ABSTRACT: The IdnetiqXelationships obtained by studying the suspension polymerization
so
of ethylene on a chromiuN trioNide catalyst are considered mathematically. The proce
was simulated on an MN-14 a-ha-Mi-e'voinputer. The experimental curves of the polymeri-
zation rate versus catalyst concentration and ethylene pressure are compared with the
curves obtained by the computer, and it is shown that the mathematical description
correctly expresses the relationships found experimentally. The proposed mathematical
description may be used for calculating the optimum conditions of the reactor unit in an
industrial application of the process of suspension polymerization. Orig. art. has:
4 figures and 14 formulas.
Ca,d 1/2 UDC 541.124:542.952.6:547.313.2

Card V2

SLIMO, M-G-
B (DR-E, 5 1@ nV
of che,,I-cal reactors.
-139
a A. gt65,
la&3ei Io no.9:30--33 ya AN SSSR.
S!bsAr:3.k!)90 oldeler,11
zelnh. tOP
@EFJ-,

SLIN'KO.,-N.F.-;--FEDQHENKO,, G.I.
Increasing the durability of tapping hole and trough,rqfractorios.
Metallurg 6 no,-5:7-9 114y 161. MPU 14-- 5)
1. Zamestitell nachalinika domennogo tsekha Krivorqp@skogo meta.Uur-
gicheskogo zavoda (for Slinlko). 2. Master domennoy pechi Krivorozh-
.5kcgo metallurgicheskogo zavoda (for Fedorenko).
(Blast furnaces-EquIpment andai lies)
(Apfractox-y materialT

ZAGYL,,,BA, A.V.; SLINKIKO, N.F.; FlaORENKO, G.I.
Calculation and correction of the burden during the blast
furnace process. Metallurg 6 no.10:1-7 0 '61. (14IRA 14:9)
1. Yrivorozhskiy metallurgicheskiy zavod. 2. Nachallnik
domennogo tsekhaAkivorozhskogo metallurgicheskogo zavoda, (for
Zagreba). 3. Zamestitell nachallnika domennogo tsekha
Krivorozhskogo metallurgicheskogo zavoda (for Sliniko).
4. Master Krivorozhskogo metallurgicheskogo zavoda (for Fedor-
enk,o).
(Blast furnaces-Equipment and supplies)

ZAGRE-EA, AN.; SLI"I'K3, FLLQUM@O, -.!.
Bi.-3winu-out and the, ouerations of a blast furnace with a 20CC m3
- - I Ja '62, (Y-ULA 1':l)
capacity, eleta,Ilur@: 7 no,1:8-13 -1
(Bl2st furnaces)

Distr: 4E2c/4E4j
4T - -4,7j. -I
trfc det=tfau o ul
U
a WA S
e i5 e
cjutscPj.theTl, Thedetn.issmde.
%vith the afd Of sulf0salicYlic acid ir. an ammonjacal medium
io that the Ti is fixed in a ,olortL-_- complex

4-Tf,@jZVA, L@LINKO V. G CHLAI !jOV I . A.
Bu; "%li.31@'J. J, $
"Characteristics of the Course and Early Dermal Plastic Surgery of Thied
Degree Thermal Burns in Animals Affected by Penetrating Radiation," p. 44
Military 1,L-dicine 1956
lecture delivered at a conference of Soviet military physicians at the
Military Medical AcadeMi, im. S.M. Kirov, Leningrad, 29-Octuolber - 2 Nov 56.

BURMISTROV, VA.. knnd.med.nnuk (Lenitigrnd, ul. PetrP Lnvrorn, d.48, kr.1)
SLINKO, V.G., kand.med.aank.
Necrectomy and dermoplasty in third-degrea thermal burns in the latent
period of radiation sickness [with nummar-i in English]. Vest.1rhir,
80 no.6:74-78 Je 158 (MLU 11:7).
1. Iz Voyenno-meditninakoy ordena Lenina akademii im. S.M. Kirova.
(RADIATION, eff.
on skin trnnspl. after third degree erper. burns
in animals (Rus))
(BURNS. exper.
eff. of radintions on skin trnnspl. in e:roer. third.
degree burns in animals (Rue))
(SKIN TRANSPLANTATION, exper.
eff. of x-irradistions on auto & homogrRftn in exper.
third degree burns in animals (Rus))

BURMISTROV, V.M., mayor meditsinskoy sluzhby, kand.med.nauk; PMTKO, V.G.,
kand.med.nauk
Local course of third degree burns in radiation sickness. 703M.-med.
zh-dr. no.8212-16 Ag'58. (MIRA 16-.'7)
(BURNS AND SCALDS) (RADIATION SICEMS)

?F7-', A., :iau(,@inyy setrudnik; V11116S, Ya.A., nauclinyy
Sy@jl(jj.j (;f' the autcmatic --On'ur,,jl of -1o,E- frame saws. Trudy
rio.8:-,-13 163. 18:11)
1. flai-Jiallnirk lahoraturli elektrotekhriikli i avtoinntiki
riaitclirio-is--Ieclovatellskogo i proyektnogo
In-s', leninoy i (ioi-,)voobi-aLxit.yvayiiri,,ci,~:!y proillyshle-luosti
(for To"fe). 2. Laborariya elektro-teklinikli i avtornatAki
iiaucr~no--Lssledovatellskogo i proyektnogo
irist@tuta lesnoy i derevoobrat~--t~-.rayus~.er,.ey promyshlennosti
(fo- -*:'!;,nk,)-,i-, Fur;gs).

Cq)
TFe -ro1O-f-S-T1--U-C-C 0 an'larpow's In n,, L-
0
T -
-
-,
!
,
@.
-
I
i, I .
mittography. 1. r . ,,, IVA., =.
,
-
I
Ciit-vucal bstr: etf, IssfedlVairlya
K
IVIU.
'
'
-
'
~iji,ejhclztiiii)-,zKhroijiiilop .1
u-30pic.
,ail. Nuak S.S.S.R
l
,
,
Vol- 48 (R). 5 11
Oldd. Khhu- Xank 1950, US-10-16

Mar. 10
1954 of CH, from Ans. in heptatte by SiO., gc-I specimens it
, higil or lo%v degrees of poroiity showed that SCICI'LiVv
G