SCIENTIFIC ABSTRACTS ABAULINA, L. I. - ABAYEVA, S. M.

• Document Type: CREST
• Collection: Scientific Abstracts
• Document Number (FOIA) /ESDN (CREST): CIA-RDP86-00513R000100110012-5
• Release Decision: RIF
• Original Classification: S
• Document Page Count: 83
• Document Creation Date: November 2, 2016
• Document Release Date: April 3, 2001
• Sequence Number: 12
• Publication Date: December 31, 1967
• Content Type: SUMMARY

S.S.; ABAULINA, L.I.
BATSANOV, I--.- -- - - . - - -.-
Interaction of mercury halides with ~!halc:)gens,, Report No.2.
Izv. Sib. otd. AN SSSR no.10-67-73 161. .,,RA 14:22)
1. Institut neorganicheskoy khimii Sibirskogo otdeleniya AN
SSSRP Novosibirsk.
(Hercux-y halides)
(Chalcogens)

W4Ae_iA,',4 '= -r.
USSRlphys?cz, Crystallography
Car,-, 1/3. ilub 146-21/25
Authcr : Abaulina, E. I., and Zavaritskly, N. V.
Title : Problem of obtaining a metastable modification of thallium
3
Periodical : Zhur. eksp. A. teor. fiz. 28, 250, February 1955
Aktract : In order to clarify the role of the crystalline lattice in the phenomcwn of
superconductivity it is important to investigate the various crystalline mcd-
ifications of one and,the same substance at low temperatures. There are tbre
metals (thallium, titanium, and zirconium) whose alpha-modification is super-
conducting, but their beta-modification at low temperatures has not been in-
vestigated. The authors attempted to obtain and study at low temperatures
the metastable modification of thallium (Y)9.9% pure); tempering was carried
out by several methods. They found that one of the usual methods does not
obtain thallium in its metastable modification and that thus the problem of
the possibility of tempering pure thallium rernins open. They thane: A. 1.
Shallnikov for his interest and N. V. Belov, laboratory assistunt in the In-
stitute of Crystallography, Academy of Sciences LISSR, for roentgen(.
Inntituticm: Inctitute of Physical Problems, Academy of Sciences USSR
Subr,itte(L : September 27, 1954

off
USSR/Physics - photo counter FD-184o
Card 1/1 Pub 146-25/25
Author : neykiii, M. S., and Abaulina, E. I.
Title : Self-quenching light counter with regulated red boundary
Periodical : Zhixr. eksp. I teor. fiz. 28, 254-256, February 1955
Abstract : The counter of photoelectrons Is a sensitive measurer of light flux. The
authors devote the present vork to an attempt to create a light counter
with regulated spectral characteristic, such an instrument in certain prob-
lems of spectral analysis combining the roles of light receptor and spectral
apparatus. The first attempt in this direction was made by V. M. Kudryatseva
(ibid. 4, 557, 1939). They thank Prof. A. I. Shallnikov for his advice.
Institution: Institute of Physical Problems, Academy of Sciences USSR
Submitted : June 29, 1954

-7 6A YX
rs
.JSSR/Electricity - Semiconducto G-3
Abe Jour : Referat Zhur - Fizika, No 5, 1957, la84
Author : Abaulin-Zavaritskaya, E.I.
Inst : Moscov State University, USSR.
Title : Electric Properties of Geronium at Super Low Temperatures
Orig Pub : Zh. eksperim. i teor. fiziki, 1956, 30, No 6, 1158-116o
Abstract : An investiption is made of
( ~ ) of single crystals of germanium (1 ohm-cm at 200)
on the temperature and on the intensity of the electric
field in the temperature range from 0.15 to 200 K.
A very low temperature is obtained by aaabatic aemagneti-
zation of iron-amonia alums. The temperature of the spe-
cimens vas monitored by a calibrated carbon thermometer
,writh accuracy to 5 x lo-30 K. The resistance vas measured
vith an electrometer with negative feedback and with a
Card 1/2

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m''Iffi-ROINEWMEM WINIM918

"I BOV/56-36-5
1he Electric Conductivity of Germanium in Strong -2/76
.electric Fields at Low Temperatures
(u
of
Card 2/3 9
of from I - 6 v/cm at temperaturos of from 4-5 - 6.35 0K
(7 curves~. This dependence is found to have 3 characteristic
ranges: a) the range of applicability of Ohm's law, b) the
range of the monotonous increase of conductivity, and c)
the range of the sudden steep increase of electric
conductivity (the so-called "breakdown" region). The latter
is subjected to close investigation. It was found that the
breakdown effect is connected with the development of a
cascade in the conduction band; it is, however, independent
of the conduction mechanism in germanium at low temperatures.
The other figures show the various physical connections in
this region in form of diagramal thus,figure 4 shows the
Curves Ebr(T), (' br denotes the breakdown field strength)t
figures 5 and 6 show the dependence of conductivity on E, etc.
The formula
A L F2I
E PA _,T or E -const holds
br F TT brF
denotes the velocity of soundt I the ionization energy
the impurities in germanium, and IL the mobility (Figure
shows the course taken by the straight line). The influence

LAie Electric Conductivity of Germanium in Strong SOV56-36-5-2/76
-Lectric Fields at Low Temperatures
exercised by various factors upon Ebr is found to be
due to their influence on carrier mobility. Finally,
the connection between B br and the resistance ? on the
wagnetic field stren-th is investigated. The following holdst
? (H) / ? (0) f,& kE br (H3/E br (0), k m 1 ... 4or
?(11)/ ~ (0) f:w /$-(O)//-b (11). The author finally thanks A. I.
Shallnikov, B. M. Vul# S. G. Kalashnikov and L, V. Keldyah
for their interest and discussions, and V. G. Alekseyeva
for preparing the samples. There are 10 figurea, 2 tables,
and 10 references, I of which is Soviet.
ASSOCIATION: Moskovskiy gosudarstvennyy universitet (Moscow state
University)
SUBMITTED: November 10, 1958
Card 3/3

ABAYArMEV, A.S.: Mpater Goolog-minoralo Scl (diss) --- "The tectonl,-e of the
west-Dorets graben (the ilovomoskovsk-Mozhovava region of the western porbass)".
Dnepropetrovsk; 1c)58, 20 pp (Min Higher Educ Ulcr S,9R, DnIJDropetrovBk order of
Labor Red Banner Mining Tnet ilm Artem), 150 CODiOG (n, No 1, 1959, 116)

AIIA)~~', A *S.
Mineral raw material resources of the Dnepropetrovsk
Province. 17,v. DGI 42:20-25 164. (mim 18:11)

LEM, G*Lop kand*med.nauk;__gATpVj A.I. (Moskva)
Use of the neuroblocking preparations gastripon and gastro-
bamate. lUin.med. no.703-56 '61, (MIRA 1418)
1. Iz 2-y kafedry terapii (zavo - prof. B.Ye. Votohal) TSentrall-
nogo institute. uaovershenstvavaniya vrachey (dir, MOD. Kovrigina)
na bass Klinioheakoy ordera Lenina bollnitsy imeri SOP. Botkina
(glavmy vr4ob - prof* A.K. Shabanov).
(PZPTIC ULM) (AUTOPM10 DRUGS)

. , ~ 1 1
:-- ~ 7- -~ -- I'l- --,I
i IABAYiV,' iA.-- In&h.; PMLISKIY, L,R,, insh. (Dnepropetrovsk).
9
Squipping electric locomotives m station tracks. Slek. i tepl. tiaga
no.12127-28 D 157. (KIRA II.&l)
(Ilsotric locomotlits-Maintenance and repair)

ABA'jTV, A.S., inAh.
Ntermination of an expediency oriterion in the ohango-over of
traction motors to owration with decreased field excItation,
Sbor. trud. DIP no.39tll6-120 163. (MIRA 1814)

pt t Pr-4/ps-4
.-AGS: singia crysEal, single try8tal gro-dtnp, single cryatal
growinq device
C T6- Qr- Scl~ntl fie Reno arch and Flanninr I n attu te o f
--t tte heater with verttcal t l1tt4 which par-mit the di re et

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ACC NRs APT009052
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I-stationary electromagnet; P.-self-adjusting needle bearing
SUB CODE: 20/ SUBM DATE: 19Apr65
Card 2/2._
QMMSMMMM~

AGkDZIU%hW# N.A. 9 mayor meditainakay isluzhbyp kand.med.nauk; A13AIIJ
4 -#
.--D.V.t-podpolkovnik maditoinakoy aluzhby - _- .,
Decompression disorders under conditions of dicreased atmospheric
Mssure, Voen.-mod, zhur* na. 1:58-62 Ja 160. (14IRA 1412)
(DF.CMPMSION SICKNWS) (ATMOSPUMC PRESSIM-PHYSIOLOGICAL EFFECT)
(AVIATION MZDIGINS)

12(4) PHASR I BOOK ZXPWXTA?Zt)X MY/2925

Baku. A.Ze:-bA74zk.An.'kl7 Inotitut tsoftsw-

b7showd.
r'"Aty"7USr-chey Pror-yablennosti Imeni V. V. 104:1
3barnk wn. 2. (Collection of Works, No. 2) balm,
1958. 313 P. treats slip Lzvilrtald. 500
copies printed.
LddItIonal Sponsoring 4-onfli Azzerbaydzhan. WIntatelretva neftyancly
Pro"aftlenno.ti.
ad. or ftt.1r.%ing 111.9e: T.11' ALl't.%n; Editorlial boards V.S. A117wv.
Canoldste of Ch."l,q] V.S. Outma, Doctor or Cbmical
Scie-es, A.st. wirev, D~ctor or ct-mmicai sciences. P.m zachiscow.
CarAldate ':f Technl~al Sclzrneetx V.Yk. Xavumyano Candids;e of,
csse-si:4i sci~r~ex, P.c. 3uieY-%n,,a, candidate or Technical
A.K. t'-shirs, C-31date of ch~~Ical Sciences, N.A. All

e~
Candidate ef Crinicki Scit"as, J.X. or4dtheva. Candiclate
o
f Technics" Sarlsesli:es, N.A. Wellk-Zads, Candidate of Chemical
1,04.
PUPJ=s Thlo
collection of articles is Intended for charselcal
'
enfliseltrav tocwn Icl nx,and refiners evneltreitld with Advanced
methods or pelrol-ast con"rejon.
COVERAMt The "llectlon :)mxqnts an ianslyals or dlff*ront
types 'f crudes ~;strftctod In AtortayUhm and of the pro6asets
recovered rrm tp."P 'rjc~x thmuch Pet "Ituft con,armicas
PrOcesaffs. 1"he de"ter!nCo desaltIng a-,Id d"w1alf7ing of trades
1. dslacrIbcd and th- suitability of these crudeja for thal
d-eco,wry of 11-s-1 Nels 12 diarlipped. Results of catalytic
cracking perfom.-d over a fluidized bad synthetic catalyst
P=,sl that chess*061 C-pneltion of gavollne Produced by two-
Ztfieo rrd~klnn are analysed. AttrItIon and dalactlws~
tIon of cata*yvto an -11 60 Cllt*17111%, CiretlatIOn In VA bjVQa-
no. system are revi-ed. vari.u. iube oil lawlti,sa, as"
thle Production v: dlfrerpnt t-vPvs or oils and of carbon bl&ck
are mtlln*d. Ptlfe.-nzeB -T~P-ny Individual artl 8.

Vollectics, of Works# No. 2
L" X.I. Perrava. Methodology of Antl"Ing
-~n C&I AddItIvel-
. .
a
M.A., A.171. V.IlArjls~.- 4, M.R" V'V~ SUbI&Aft-
Oil by Means of 1"1064tIve
o""7
720topes
t-ih.3-rmsl Conversion or
_11._A~~i~--,. 34asterI.S %4~ T-h..q.. or
F**ro-.~:a-t,?4rInC Sands of K12-MakInak Car-rl&4 out o,"r a nuiax*a
Bad
With Spent ZuIr"It AxId "M Aliqlatlon
Xmc3 , X And_4.11. At&Yc,. Syslte%n for Conceal by '11"er-
4!RON ~Tr"s"bP&r,
card T/S

ISFATLOV, I.K.: ABLTV, G.N.
Regulating "hyperflow' conveying systmo. Sbor.trudASICII XP
Ino.2018-324 Ag '58.. (NIPA
(cryerijimchinery)

1 18o, l o. .100o
S011/6 5 -!',() -.3 -7/19
AUTHOR: Abayev, G. N.
TITLL: Concurninr thc Calcul,ition of' the Consumption of
Solids Dovinj-, 11neuniat,ic
PERIODICAL;
KlAmiya i tolchnologtya topli. i rna-,icl, 1960, Nr 3,
"8,
P : -35 (USSR)
P
ABSTRACT: A lino-ar relat-ion wa,, Ln3tabllnhed betiqe-(ni lozno of poten-
tial onergy and corimunption of' ~,olid material during
pliclunatic conveying.
G
Where
K -. Et(j 4-
+
The following notations were uzsed: G is the amount of
circulating solid particles (kIl/nr or lqr/sec); P is
Card 1/5

Concerninf; the Calculatj.ol-j of t.jj~,. C011- 7119 -JI
m 'i of Solids Du 17,_ '0_.1
u, Ptiol ring Pnel IITFA t i C S 6 -v.1 "D - 19
S
Conveying
pressure drop in conveyor Occlm'); K is coeff,icient
dimensionless); Q ~is O-on~.-'Luliptlion of transportinF niren
(nI3/hr or m3/oec); W,,, j.:; I ,t2j.ocit-,y of, j.11
veyor w1) is 've1o(..i.t-.' of prticles ill Qc),I-
ve-yor (111/SeC); I i:, (UOUIIIC(~ b(.AW~J~Ctl Of
(111); 1, L~~ 1'riction f'actor
(dimull0iolilel3s); a is
Dt i:~ di'llneter of,
I collcon" I id ~~od
i'ud 1 ",;c I ty OF 11
~-X p:1rt ic, i':~! CI' 011
1~; the Cro.;.'; ;Uctiun 01, trall3PI)I't Pipf_-l
of' zolid

the calcul'.1t, loll ()J, tjj(.~
jU,fl-,Vt:iO11 OVA 5 - 6 9 - 3) -,(/ 19
Co I Ic%,; -1. 1 -1
work:'Lng conlition", (ki-,/m'): d i.; vi.~;,co.,ity W' the tran--
,AWC. /In K io cocVr*.1ci.Qnt K
Port'i 11fr
gao (1(1'
experiniental 1y; K ii theoretical
eloration 01, Prec. i'all 9.
ace rrv,; (:~ c r
~;el".,tion Without ch'.111irc, of' tll(-. l'ollowinf,
ning, f'actore, lo condit.i.on 'of' :.;im:i.Jir.JAj-, of
thO 1'lUldi.,ed bect -Vlow:
I
It i:3 inadinisoible to appij the K data withol.it clon,;irl-
oring the oimilar condition,;. The range of the accr--1-
cration zone e3tabliuhed exporimentally Por
sand and pellet catalysto in the range of' trariz;portinE.
gao linear velocity of, m/sec ne-jer exceeds 2-5 m.
The instant con3uniption 1' the :3o!id particle:,, can
found by experimental-aimlytical met-hod 1'rom the -.,al--ie
C,a~-d 3/5 of the potential energy I.oz;s of the gas flow L,, P.

tll~j C"llculatioll of, the Con- TO 3
(a) in the c a 3 e a f I Vp-,
PI;
(i.e., the diffmanometric measurement, of pres-,~"Jre
located above the aoccier,-OAori ,.one).
All'
K
(b) In the c,.i,,;e
ljridf-~r indiu;trial
u,.;(-,d l'or dutci-mining, L;oll.(l pal-Li.c.10" conou.11-1ption
fract. ional conlpb~31t v"ll ot, the c i rc ~~! I -'i t i ni, '.;o 1:1 d

i lie C~,-O.culat.loll of' th(-- Dm-
C, ri o I' So 11 d ~i Di I r, 1. 1 ti, P11C L)III; I t, 1. o v/6,-- - 6)
cow.,c-
G
For controt G and W the ;uc,,estcd method can
1.)Q iil;cd Vov the ol* dii.,iLtil computero. In
!A10 ciloo III Y11 i, 11 J ry 1, o d c, t o rm i I i e
livlitlco~; coolTicient K from ;om(2 otht2r conditions
(tilei-Inal, wil-mice, ex;implu in order 11.-o find G from
AL P. Thel,e 11-e i Cif"kir(" 'j, rind 10
j, Soviet, Th, S (I- ~: ;a I I C! Da i I i (2 1.,;
-3 U. S. U., vt--Fcrt~fic
Reftner, 11'3') '19~10); lixin, Moi~-,ttd, TLEC, 111, 1h, 11118
3", ( 19118
(!949); Voi-t, Wite, 110, F(

ABAYEVI G.N.; GUSMN, T.Ya.
Determination of the rate of the beginning of fluidization
of some catalysts. Khim o.11:796-.798 N 162. (MIU 16:2)
(,l.,d,,,t,O;Tom. n (Catalysts)

DALINp M.A., akademik; LOBKINA, V.V.; ABAYEV, G.N.1 SEREBRYAKOV, B.R.;
PLAKSUNOVA, S.L. - f
Production of acrylonitrile based on propylene and ammonia.
Dokl.AN SSM 145 no.5tlO58-1060 162. (141RA 15:8)
1. AN AserbayA"aneskoy SSR (for Dalin).
(&-trllonitrile) (Propene) (Ammonia)

DALIN, M.A.; SEREBRYAKOVp B.R.; MANGASARYAN, N.A.; ABAYEV, G.N.;
VALLERSHTEYN, A.S. . ~
Synthesis of acrylonitrile by oxidative ammonolysis of propylene
in a fluidized catalyst bed, Azerb.khim.zhur. no.4:28-33 165.
(MIRA 18:12)
1. VNIIolefin. Submitted August 16, 1964.

ABAYEV, G.N,.
Basic criterial equations and criteria of chemical kinetics.
Zhur, prikl. Wine 38 no.10:2242:2252 0 165, ( KT.,IA 18 112) )
1. Submitted Febr. 27, 1964.

NAW-'ETS, Nikolay Ivrnovich, ispolryayushchly obyawnnooti prof.
kand. tekhn. nauk; ZEIRKOVICH, 3argey V1.Rdimirovich,
ispolnyayushchiy obyazannosti prof. kand. tekhn. nauk;
-ABAYEV.-I.I., inzh.; PERCHENKO, A.G., st. pepod.;
dots., kand. tekhn. naukp retsenzentl
YUSTINSKIY, E.A.p inzh.v retsenzent; ANTONOV, V.P.,
tekhn. red.
[Hoisting machinery used in building) Gruzopod"emVe
stroitellnye mashiny. 2-ia chast' posobiia po kursu
stroitallrifth mashin. Kuibyshev, Kuibyshevskii inzhe-
norno-stroite. in-ty 1962. 416 p. (MIRA 17:2)

ABAYEV, H.I.; KORNFELID, M.I.
Measuring the internal friction in solids. Prib. i tekh.
eksp. 9 no.2:150-152 Mr-ApI64. (MIRA 17:5)
1. Institut poluprovodnikov AN SSSR.

ABAYEV, M.
Device for measuring the normal mode and damping constants
of oseillntory systems. Prib. i tekh. eksp. 9 no.2:153-
155 Mr-AP'64. (MIRh 170)
1. Institut poluprovodnikov AN SSSR.

ACCESSION NR: AP4033137 S/0120164/000/002/0150/0152
A UTHORt Abayevs M. L i Xornfelldi M. 1.
TITLE: Measuring internal friction in solid-state bodies
SOURCE: Pribory* I takhnika eksperisnenta, no. Z, 1964. 150-152
TOPIC TAGS: friction, solid body internal friction. internal friction
measurement, internal friction electrostatic measurement
ABSTRACT: A new electrostatic method for measuring internal friction is free
from two shortcomings of the techniques used heretofore: cementing the specimen
to the vibrator and electric contact with the specimen. The 16;x5x 1-mm
specimen rests on two 0.07-mm glass filaments whose ends are welded to a glass
disk (see Enclosure 1). Four Pt electrodes are cathode-sprayed on the disk
surface. Two inner electrodes are Intended for generating cantilever vibrations
in the specimen by an electrostatic field; two outer electrodes, for measuring the
Card 113

ACCESSION NR: AP4033137
vibration amplitude by a variation of capacitance between these electrodes and the
specimen. The device permits measuring the internal friction (from 10 band
higher) in the kc range, within 100-600K, by attenuation of the specimen's free
vibrations. "The authors wish to thank V. V. Sokolov who built the mechanical
part of the device. 11 Orig. art. has: 5 figures and I formula..
ASSOCIATION: Institut poluprovodnikov ANISSSR (Institute of Semiconductors,
AN SSSR)
SUBMITTED: 09Apr63 DATE ACQ: I lMay64 ENCL: 0 1
SUB CODE; SS NO REF BOY: 001 OTHER: 004
Card 2/3

ACCESSION M AP4033137
ZNCLOSVRZ
Device for measuring internal friction
in solid-state materials
Card 3/3

ACCESSION NR: AP4033138 510120/6410001002/015310155
AUTHOR*. Abayev, M. 1.
TITLE., Instrument for measuring the natural frequency and attenuation ratio of
oscillatory systems
SOURCE,. Pribory* i tekhnika eksperin'ienta. no. Z. 1964, 153-155
TOPIC TAGS: natural frequency. frequency measurement, attenuation
measurement, mechanical system frequency measurement, mechanical system
attenuation rneasurement
ABSTRACT: A new digital electronic instrument Is briefly described which is
intended for precision measurement of the frequency and attenuation of quartz
standards, tuning forks. and other mechanical systems. The measuring range is
10 -30 kc with errors of � Oa 005% and = 3%. respectively. The f requency in
determined by counting the number of cycles over a standard time interval, The
Card 1/2

ACCESSION NR: AP4033138
attenuation is determined by the number of cycles corresponding to a decrease in
the amplitude from one set value to another. Vibrations in the test specimen are
set up electrostatically; a capacitive sensor is used to detect them. The
instrument is used as part of an outfit for measuring internal friction in solid-
state bodies. Orig. art. haw 2 figures and Z formulaso
ASSOCIATION: Institut poluprevodnikov AN SSSR (Institute of Semiconductors,
AN SSSR)
SUBMITTED., 09Apr63 DATE ACQ: I lMay64 ENCL; 00
SUB CODE: Cc NO REF SOV: 00 1 OTHER: OOZ
Card Z/Z

ACC NRi AP5022728
~t)/W(b)
SOURCE CODE:
9
AUTHOR: Abayev,.H
q Y 1 5- L;-
ORG: Institute of Semiconductors AN SSISR, Leningrad
SSSRF-
UR/0181/65/007/009/280912815
(Institute poluprovodnikov AN
TITLE: Pore formation during decomposition of solid solutions of bivalent ions in
sodium chloride
SOURCE: Mike tverdogo tela, v. 7, no. 9, 1965, 2809-2815
TOPIC TAGSs sodium chlorid%~.Ilight scattering, solid solution, crystal impurity,
crystal structure, S=tal defect
ABSTRACT: The process of pore formation duri decomposition of solid solutions of
Me2 ions in NaCl is studied. Sirwle crysta pecimens with the following impurities
were used: BaC12, SrC12, CaC12, COC12, NiC12, MnC12, CdC12, ZnC12 and PbC12. A pho-
tomicrograph is given of a crystal with an admixture of BaC12. "Rods" lying along
the axis ara clearly visible, althougb some of them are at a slight angle to
this axis. These 11rods" reach a length of 10-15 -p with thicknesses up to 1 )1. Quench-
ing from 7000C completely eliminates these "rods" which indicates that they appear
during decouposition of the solid solution. It is assumed that these objects are
pores. While there were no visible pores in the other crystals studied, light scat-

L 8850-66
-ACC-N,Ru-APS022728-
tering experiments indicate that th's is because their dimensions lie below the re-
solving power of the microscope. Thede light scattering experiments are described
together with a brief explanation of the equipment used. The specimens were cylinder
10 an in diameter and 15 am long with polished ends. Scattering patterns are shown
for some of the specimens with the light incident at various angles. Scattering pat-
-terns --for-the - NaCl-SrC12 - specimen-are-giv.)n' -as-a-function-of--annealing-time-at-3400C.-
A curve is given for intensity of scatteted light as a function of temperature in the
specimen containing strontium chloride. It is shown that pores are responsible for
the scattering pattern. Subsequent experiments showed that large pores are formed
by p-.vtracted annealing near the temperature corresponding to maximum scattering.
Analysis of the experimental data shows that crystals with admixtures of BaC12,
CaC12, SrC12, COC12 and NiC12 form pores along axes , while those with WC12 and
HnC12 form pores along axes glOO>. The pores forined by decomposition of solid solu-
tions of lead and zinc ions are small and. their shape is uncertain (the scattering
pattern is a.circlel. Sharp spikes on the patterns indicate that the pores are con-
siderably longer than a wavelength of 311ghtt howaver they must be considerably smal-
ler in diameter thLn a wavelength of light since they are invisible under the optical
microscope except for the case noted above. Orig. art. has: 10 figures, I table.
SUB ODDE.- 20/. StMM DATEt 23Apr65/ ORIG REF: 001/ OTH PXF: 004
If".. V k"

ABAYEVVIloy~at.Abayevich; SHNEYER, M.S., red,; IVONTIYEVA, G.A.,
... - ie'k6. red.
(Development of cotton growing in 5:)Yiet Turkmenistan] Raz-
vitie khlopkovodstva aovetskogo Turkmenietana. Aabkhabadt
lzd-vo AN Turkm. SSR, 1963. 167 p. (MIRA 16.11)
(Turk7seniatan-Cotton growing)

SHUKAKOV. V.F., inshanar; PRASOV. H.R., Inshaner; ARAyw Lj~inzhener Po
tru4u; VOLIPNER. Z.V., inshener-teplotnkhn kAWIOVSXIY, L.A.; NIMO,
17:-
B*P9
Mechanizing slag removal from slag pockets In open-hearth furnnese.Metal-
lurg no.9:14-19 S 156. (KLRA 9:10)
I.Stnrehiy inzhener teknicheakoge otdela Metallurgicheakege saveda iment
Voroshilova, (for NRlakhovskiy). 2.Stftrehiy k*nstruktor royaktnoge otdola
HatnllurgichaHkoge savada imani Voreshilava (for Mikhn*3.
(Matnllurgical plants-Equipment and supplies)

AUTHOR - Abavey~? (Gillef C)I, L*'-e llkl!'eail 04, H'Ile SC"1-- 0 f
Open-Hearth Shop NP 2
TITLE: Pototit tal. 1nol-ease of Labor Pvc) litv
Stlop
PERIODiCAL: 140'Lallurg' 196'0' Nr 1, pp 2"-211 (us3y,)
A B S T R~ A C T Since 1,950, steel output ~jt, a
C oni b I ne (Magn It ogovsi~ I v Me 1-.i I UVj! 1-CL-- !:,k i V110~~i W
v.lovker increased by 54. The ~13
iesult.. of: (1) convertltIL7' ol'-Ien -heat: "'L '0
ne~iluyn chrom-lde roof,.:,; (2) Changre of fw't~ace e
Increaseing char,,,e ay-cl I-a-zile
management at stock.Var~l anA DOLIVIM- b~11';
(~
I i., (?
to Ynazut f Iring (pJroleum resIJLU-~

P.11na bz.-iclk foil
(6) using, higl--alUr
re'-enerator size; (B) meclian,Z-qtion oi'
(9 mechanization of cloilrg, tap 1:01e; 16)
Cird from large ladle with two sz-oz~oe-,~z-,

Pot (3,;,, off' Labor Pralli- t, I v I
Ir
mamine; l.')) us!~~,~ equlp7it-,-- f'o:, i!
'i 1 1, ilwt I on of' ;~ tee 1 n the lalles; 1 1:-:
11!~~ot mold volorne i,vo!F, I to I .11f,:~ Irl". liy tile
o f' o rem an I . N' . K,,~ tnN 7 n Z3 2,-. 1 o- ' o Oil, C) -
J~i 1 In a s I El g p o C K e s, -a: e 1, w ~: F i r s r a e
a ellintnatine, !'ouv wori~ers SenlQl' r~aO T e
-ind electrioll,w, F I , ~-, - -e
A. 1. Ku,,ochkin ;
0
the service area for elect r. cla-io zind
extended, reducIng the number of* el ,,,-, e.
-!.r T-ovemen t s vccz u I ed In ~~e 1!; e o a 1, o.,
av.,j t fie de - ro -ise o' ,-Jove 1, ~,C-

In
St.eel_ outpj~~ -C ~or%(,e-
y e
To

ASSOGIATIO;', Magn1togorsk Metal lurgleal Cornblne
ti.etalurglcheskly kombinai.)
Card

ABAYINO YU.I., WCUCHANSKOV, MI.
%Mm
Cond 1A.1 ons for the surviva I of yc,;rtl, roo cn,~ ---- *--~ lus rutilug
be-kel-1) in ths Beyoug and mothods of the
affi.-lency cn the Beysug PC! --lp9wning and Peur'Mg Farm.
Truay -?o.NIIRKH no.66,119-325 163. (MrRA 27-.8)

r
ABAYI.V, Yu.%, KRYLOVA, A,G.
Feedtng habits of young roqch (Rutilus rutilui hockeli) in the
Beysug spawning ground and liman. Trjdy Az-KIRFII, no.6027-131
163. (MMA 1718)

A v ;o
I c
L19.
C-~ntnxl itas Inst 0c :'Viat7cli -'usls
SO Vecheryaya Moskva
Sum 71

- - --- - I - -- t
I ~-, - -w:P, 11 - I I- -'l t ! - , . ~ .1 .
I
M i N 0 m I W., I m W, M!, OF

Cracking of high molecular
Romashkinsk crude oil using
silicate catalyst. (Cont.)
hydrocarbons from the
a natural alumino-
are given in Tables 4 and 5. Structural characteristics
of individual groups of hydrocarbons (in %) - components
of asphalt free starting material and its cracking
products are given in Table 6. The composition(in wt %)
of both starting materials and their cracking products
is given in Table 7. 7 tables and 12 references,
7 of which are Russian.
Card 2/2

65-2-8/12
The Cracking of Individual Groups of Hydrocarbons of Romashkinsk
Goudron in the Pressence of Natural Aluminosilicate Catalysts.
with an activity index equal to 18.5 at a temperature
of 45000 in a mixture with n-pentane (ratio 3:1).
Table 2 gives the ahemical composition of the deasphal-
ted goudron and its fractions and Table 3 the chemical
composition of the cracked petrol; tables 4 and 5 the
properties of the fractions obtained after the crack-
ing of individual components of the deasphalted goudron
at 200 - 35000 and 350 - 4500C respectively. The proper-
ties of the cracking residue boiling above 4500C are
shown in Table 6. The highest degree of decomposition
under catalytic cracking conditions was observed in the
heavy paraffin-naphthenic hydrocarbons which had a com-
plex structure, The degree of adsorption of these para-
fftns on the surface of a catalyst is high, and they do
not poison the catalyst which can be further used for
the kerosene gas oil fractions. There is also a high
degree of decomposition of the light aromatic hydro-
carbons, but the surface of the catlLyst is poisoned by
the hydrocarbons used as starting material, and also
by the kerosene gas oil fractions, which leads to a
decreased formation of cracked petrol and of the gas.
The light aromatic hydrocarbons undergo the highest
Card 2/3 degree of conversion. The main characteristic of the

65-2-8/12
The Cracking of Individual Groups of Hydrocarbons of Romashkinsk
Goudron in the Presence of Natural Aluminosilicate Catalysts.
decomposition of high-mblecular compounds are the
splitting off of the side chains, the rupture of the
aliphatic chains, the rupture of the sulphur - and
possibly other links, which is followed by a decomposi-
tion of the formed middle fractions. The dehydro-
genation of the naphthenic ring is clearly shown, but
is of no great importance. As a result of this reactiont
middle and heavy aromatic hydrocarbons are formed which
possibly partly undergo condensation reaction with a
formation of ashphaltenes and colke. During the crack-
ing of the paraffinic and light aromatic hydrocarbons
the hydrogen atom is transferred. When highly aromatic
or tar raw material is used the surface of the catalyst
is blocked, and a very weak reaction is observed.
Results of investigations show clearly that it is advan-
tageous to use selective catalytic processes for the
treatment of high molecular crude petroleum raNy material.
The processing of the residual fractions'on natural
catalysts should give high yields of kerosene gas oil
Card 3/3 fractions. There are 7 lables and I Russian R;10erence.
ASSOCIATION-.VNII NP.
AVAILABLE: Library of Congress.

SOV/81-59-15-54832
Translation from: Referativnyy zhurna-1. Kh1m1ya, 1959, N~: 15, p 423.(USSR)
"AUTHORS. Agafonov, AN, Abayeva, B.T., Okinchevich, N.A.
TITLE: The Catalytic Cracking of High-Mole-cular Pe-trodeum Raw -Material on
Natural Catalysts as a Possible Source of Raw.Material for the Production
of Oils
PERIODICAL: Tr. Vses. n.-i. in-ta po percrabotke, nefti I gaza 1. poluchehiyu iskusstv,
zhidk. topliva, 1958, Nr 7, pp 181 - Z-02
ABSTRACT; The results of research work on the problem of rational processing of the
high-molocular part of petroleum to engine fuel and lubrication oils are
laid down. Pjaple material on the analy--I,% and the material balance
of products of cracking of petroloUm, mazut, and asphalt petroleum on ! ..
natural Al-Si catalysts Is ppesented. The experiments were oonducted at
11500c, the volume rate of the raw material of 1.0 per hodr, a frequency
of the circulation of the cataIY3t 5:1.- The fr~fltlbns boiling at up to-*--
200, 200 - 350, 350 - 4500C and the. residue were subjected to deta.Ued.
analysis. It has been established that under these conditions the
Card 1/2 asphaltenes and resinous substances as well as medium and light aromatic

1
SOV/81-59-15-54832
7he Catalytle Craoking of High-Moleoular Petroleum Raw Material on Natural Catalysts
as a Possible Source of Raw Material forAhe Production of Oils
compounds, naphthene and paraffin compounds are transformed by 85 - 90%. The principal
direction of the decomposition is the rupture of-the side chains, the decomposition of
the isoparaffin and paraffin hydrocarbons, the rupture of.the naphthene rings and the
dehydrogenation of bi- and polycyclic hydroaromatic hydrocarbons. The fractions
350 - 4500C'dohtain u*p to 35% naphthene, isoparaffin and light aromatic hydrocarbons
suitable for the production of commercial oils. The process is strongly affected by
the presence of low-boiling components in trie initial raw material. In the cracking
of petroleum the components boiling '.'~P 450qC are transformed in the most intensive
manner; the fractions boiling 3500C are little affected.
S. Rozenfelld
Card 2/2

SOV/68-58-11-11+/25
AUTHORS: Vorozhtsov N.N. $ Corresponding Member of the Academy of
Science of the USSR, Doctor of Chemical Science,
Lijit,yn V.N., Candidate of Chemical Science, Agafonov A.V.
and Krasivichov V.V., Candidates of Techpical Science,
and A OVa * . , Candid.ate of Chemical Science
TlTLLI: Transformation of Higinor lio;-iiolo-ues of Phenol into Lower
Ones (Prevrashcheniye vysFhikh gomologov fenola v
nizshiye)
PEaIODICAL: Koks i Khiraiya, 1958, Nr 11, p1) 42-47 (USSR)
ABSTRACT: The results of all investigation on the dealkylation of
technical xylenol with simultaneous alkylation of benzole
in a pilot plant of the All-Union Scientific Researuh
institute of the Petrolewii Indus~'ry in which bead
,aluminosilicate was u!;ed are doz;cribed. This was a
continuation of the previously published work (Ref 1) on
the transformation of xylenols (oil interaction with
benzole) into phenols and cresols on cracking under mild
conditions on an alu,ninosilicate catalyst. The experi-
,ental plant used (Fig 1) is outlined. lt was established
Card 1/3 that,on passing ~:ylonol in mixture with benzole

sc)v/68-58-11-14/25
Transformation of Higher Eomologuos of Phenol into Lower Ones
(1 : 3.65 by weight) over aluninosilicate catalyst at
0
tem:)eraturos in the rang-e 300-1WOoC and volume velo-
lg I
cities of 0.42-1.471u. .up to 60/~ (on weight of starting
xylonol) of phenolic compounds (phenol, o-, m- and p-
cresols, xylenols),includinf- 20_22- of phenolic-cresolic
fractions =e obtained. Simultaneously 11-19,% of benzene
homologuej with a boiling temperature of 100-1850C and
13-18% of neutral compounds with boiling temperatures
above 1850C are formod. 8-25,~ of coke is deposited on
the catalyst. The influence of the temperature of the
reaction$ the volume velocity of reactants (Table 1),
additions of water vapour and various proportions of
benzole (Table 2) on the transformation of xylenol and
changes in the activity of the catalyst with time of
operc It was found that
ation (Table 3) were o3tablished.
at tampYratures 300-'~200C and volume velocities 0.92-
1-47hr- more phenolic-cresolic fraction and less of
neutral com,)ounds and coke on the catalyst is obtained
Card 2/3 (taking into consideration the transformation of xylenol).
At 3000C and a voliunne velocity 0.921ir-1 330k9 of

sov/68-58-11-14/25
'D
Transformation of HiEher Homolo,.-,,uos of Phenol into Lower Ones
phenolic-crosolic fraction and about 200kg of benzene
homologues with a boiling temperature 100-1850C can be
obtained from 1 ton ol' Xylcnol.
There are 3 tables, 3 figures and 6 references (L~ Soviet,
1 English and 1 German)
ASSOCIATION: MTI im. Dj. M-endeleyeva, VNII NP
Card 3/3

sov/65-59-4-4/14
AUTHORSt Agafonov, A*V#j Aba eva, B~T*p Andreyevat A*S.,
Eygenson, AeSol tor, I.I. and Ivchenko, Ye.G.
TITLEz Catalytic Cracking of Crude and Hydro-Purified Vacuum
Gas-Oil from Arlan.. Petroleum (Kataliticheskiy kreking
iskhodnogo i gidroochishchennogo vakuumnogo gazoylya
arlanskoy nefti)
PERIODICAL: Xhimiya i tekhnologiya topliv i masel, 1959, Nr 4,
pp 18-24 (USSR)
ABSTRACT: Vacuum gas-oll from Arlan, petroleum contains 3.2%
sulphur compounds, 0.11% nitrogen compounds and 24%
tarry substances; these quantities are larger than
the corresponding quantities in heavy gas-oil from
Tatar*~& and Bashkix*iA petroleums. These components
block the active surface of the catalyst during
cracking, prevent the access of hydro-carbon molecules
and therefore decrease the degree of conversion of the
crude material. Considerable amounts of coke are
deposited on the catalyst which inhibits secondary
reactions and leads to decreased yields and inferior
quality end-products. Hydro-purification was carried
Card 1/5 out on a continuous apparatus in the VNII NP by

SOV/65-59-4-4/14
Catalytic Cracking of.Crude and Hydro-Purified Vacuum Gas-Oil from
Arlan Petroleum
N.A.Chepurov and R.N.Yudinson; a stationary aluminium-
cobalt-molybdenum catalyst was used at 380*C, a pressure
of 50 atm and space velocity of the supplied crude
material of 0.7 hour-1. The properties of the starting
material and of the hydro-purified vacuum gas-oil are
tabulated (table 1). The octane number of the end
product was appreciably higher then when using
fractional distillation (58.5 as Lompared to 41.0)
and contained considerably less sulphur (0.013 as
against 0.17%). The properties of the gas-oil fractions
are liated in table 2. Cracking experiments of both
the crude and hydro-purified vacuum gas-oil were carried
out on a pilot plant with a synthetic bead catalyst at
temperatures within the limits of 430 to 520*C,
atmospheric pressure and a space velocity of 0.65 to 1-5,
calculated on the volume of the catalyst per hour. The
ratio of the catalyst to the crude material was constant
Card 2/5 in all experiments and equalled 5tl (table 3). Optimum

sov/65-59-4-4/14
Catalytic Cracking of Crude and Hydro-Purified Vacuum Gas-Oil from
Arlan. Petroleum
yields of petrol were obtained at temperatures between
450 and 475% when the optimum space velocity of the
supplied raw material was within the limits of 1.0 to
o.65 hours-1. The hydro-purified vacuum gas-oil
could more easily be processed; an optimum yield of
light components at the same space velocities was
achieved at 50*C. The authors concluded that the
presence of a considerable quantity of light fractions
boiling up to 3500C (37.6 as against 19.4%) influences
the yield of the light components. The optimum yield
at this temperature reached 66 to 67% by weight as
against 58 to 59%. Results of the cracking experiments
indicate (Fig 1) that the hydro-purification of the crude
(by separating thetarry substances, metals, sulphur and
nitrogen) improves the process conditions and also the
yields and properties of the cracking products (compare
table 4). The gasoline obtained by this process is less
unsaturated, contains more aromatic compounds and has
Card 3/5 higher octane numbers (80 to 81.5 as compared to

sov/65-59-4-4/14
Catalytic Cracking of Crude and Hydro-Purified Vacuum Gas-Oil from
Arlan Petroleum
77.7 to 80-7) (Fig 2). A lower content of unsaturated
compounds renders the gasoline more stable. Its
induction period exceeds 600 minutes. The light
catalytic gas-oils, obtained during the cracking of
hydro-purified crudes, show improved properties. Their
cetane number is 34 to 38 (as against 30 to 33) and they
contain 0.21 to 0-38% sulphur (as against 2.6 to 3.3%)
(Fig 3). These light gas-oils can be used directly as
components of diesel fuels. The heavy catalytic gas-oilt
(fractions boiling above 3500C) can be used for the
production of lubricating oils or re-used as recycles.
In both cases 2 to 376 of the tarry (tail) fractions have
to be separated. The gaaeous hydrocarbons produced
by this process are of interest as starting materials
for petro-chemical syntheses. The influence of the
temperature on the ratio of unsaturated and saturated
Card 4/5 hydrocarbons in gaseous reaction products, and on the

sov/65-59-4-4/14
Catalytic Cracking of Crude and Hydro-Purified Vacuum Gas-Oil from
Arlan; Petroleum
content of unsaturated hydrocarbons in the gas, is
shown in a graph (Fig 4). There are 4 figures,
4 tables and 2 English references.
Card 5/5

SOV/65-59-4-7/14
AUTHORSi Agafonov, A.V., Sookind, D.M. and Abayeva, B.T.
TITLEt The Operation and Methods of Re cons t ruc t J-o-n-o-f-1C7a-t-a ly tic
Cracking Plants Where Bead Catalysts are Used (Opyt
ekspluatataii J puti rekonstruktaii ustanovok
kataliticheakogo krekings, a sharikovym katalizatorom)
PERIODICAL:Khimiya i tekhnologiya topliv i masel, 1959, Nr 4,
pp 34-44 (USSR)
ABSTRAM Investigations were carried out in the VNII NP which
made it possible to work out conditions and make
recommendations for the manufacture of high quality
petrols. Heavy distillates, boiling at temperatures
between 300 and 500*C, can be used. The process is
carried out in one stage and, therefore, the efficiency
of the plant increased by 30 to 35%. The properties of
the gas-oil fractions of Romashk6ya petroleum are
given in table 1. It can be seen that the heavy crudes
differ from the kerosine-gas-oil fractions by their high
boiling and solidification points, by their high content
of tar, sulphur and aromatic compounds as well as by
Card 1/3 appreciable content of polycyclic aromatic compounds,

sov/65-59-4-7/14
The Operation and Methods of Reconstruction of Catalytic Cracking
Plants Where Bead Catalysts are Used
asphaltenes and metal salts. Various investigations
carried out in the Novoufimka . plant during 1954 to
1955, and modifications of the plant carried out at the
time, are discussed in detail. The reconstructions,
carried out at present, aim to increase the efficiency
of the plant 1-5-fold (first modification) and 1.7-fold
(second modification) without altering the principal
layout of the plant. A further reconstruction is to
achieve a considerable improvement in the conversion
process which will increase the efficiency of the
plant by 100% (third modification). The first
modification is based on recommendations made by the
authors, the Novoufinka factory Giproneftemash and
Giproneftezavod. This type of reconstruction was carried
out on one plant of the NUNPZ and three plants of the
Salavatskiy factory. The various modifications are
listed in a table on page 40 and the most important of
these discussed in detail. Table 2 shows the improvements
achieved during 1956 to 1957 and the first nine months
Card 2/3 of 1958 in various plants where the recommended

sov/65-59-4-7/14
The Operation and Methods of Reconstruction of Catalytic Cracking
Plants Where Dead Catalysts are Used
reconstructions have been carried out. The second
modification was recommended by GrozNII and
Giproneftezavod and the third by VNII NP and
Giproneftemash. The lay-out of the last plant in given
in Fig 3 and the authors suggest that this last
modification should only be incorporated in newly-
erected plants. There are, however, various drawbacks
e.g. the circulation time of the catalyst is rather low,
the generator is not completely efficient, the cooling
pipes of the regenerator are unsatisfactory and this
leads to an increased catalyst consumption. There are
3 figures and 2 tables.
Card 3/3

V -- V
PEME I BOOK EXPLOITATION SOV/4659
Osnovy tekhnologli neftekbimicheskogo ointeza (Fundamentals of Synthesis Technology
id Petrolem Chemistry) Xoscov, Gostoptekhizdat, 1960. 852 P. 3,800 copies
printed.
Eds.: Diutecs, Arkadiy Illich, Professor, and Lev Aleksan&rbvich Potolovskiy,
Profeesorj Executive Edo: L.A. LIvova; Tech. Ed.: B.A. Mukhina.
PURPOSE: This book is intended for engineers and chemists of petrole= refineries
and chemical plants, for councils of the national econcmy, planning organization4
and scientific research institutes engaged in chemical processing and large-
scale utilization of petrolem stock for the production of synthetic products.
COVERAGRi The book describes important commercial methods of producing hydrocarbm
petrolem. and gas stock and coal stock for the manufacture of alcohols, aldehydeq
ketones, acids, detergents, synthetic fibers, an& synthetic xubber. Flow sheets
axe included, and the badic equi];ment of the petrochemical industry is described.
The pbysicoebenical properties and use of intermediate and end synthetieproducts
are also described. The state of the petra~hemical industry outside the USSR
wad prospects for its develolment are covered. No personalities are mentioned.
Carl= es follow each chapter.'

Fundamentals of Synthesis Technology (Coat.) sov/4659
TABIZ EW CONTMM:
Foreword 3
Ch. 1. Development of Petroleum Refining and Petrochemical Processing 7
1. From straight-run distillation of petroleum to the petrochemical
industry (raw materials for the manufacture of petrochemieslB
[A.I. Dintses] 7
II. Petrochemical processing industry abroad [L.A, Potolovskiy] 15
Ch. II. Processes of Raw Material Production for the Petrochemical Industry
(B.T. Abayeva and AN. Agafonov] 40
I. Destrue ve sUllation of petroleum, the main source of raw
materials for petrochemical processing 40
II. Thermal cracking 41
III. Pyrolysis of hydrocafton gases and liquid petroleum products 47
1. Chemical nature of the pyrolysis process 48
2. Pyrolysis of liquAd raw materials 51
3- Pyrolysis of gaseous rev materials 60
4. Tube heaters for the pyrolysis procesR 69
IV. Cooking of petroleum residue
V. Catalytic cracking of petroleum products 1,6
cant-21"

Fundamentals of Synthesis Technology (Cont.) SOV/4659
1. Development of the catalytic cracking process 76
2. Chemism and kinetics of the catalytic cracking process 81
3. Effect of basic parameters of catalytic cracking on yield of
desired products 83
4. Hydrocarbon composition of liquid cracking products 85
5. Composition of catalytic crfLcking gases 87
6. Yield and quality of products obtained by cracking on micro-
spheric catalysts 89
7. . Catalytic cracking of residual types of stock 92
VI. Catalytic aromatization of gasoline fractions 93
1. 'Development of the aromatization, process 93
2. Chemical conversions of hydrocarbons in the aromatization
process 95
3. Industrial development -7f the catalytic reforming process 100
VII. Prospects of utilizing products of destructive processes of
petroleum refining for the petrochemical industry 105
Ch. III. Refining Processes of Hydrocarbon Gases for Acetylene and
Hydrogen Manufacture 113
C erd--44

AGAMNOV,, A.V.; WMM9 B.T.; OKIMHEVICH9 N.A.
Distribution of sulfur in the cracking products of heavy charge
stockne. Mm.sera-i azotorg.soed.i3odv neft.i nefteprod. 3a83-192
160, (MIRA 14:6)
1. VassoyuzMy nsuohno-issledovatel'skiy institut po parerabotke
nefti i gam i polucheni-yu Ukusstvennogo shidkogo toplivae
(Petrole= jx~oduots) (*Llfur organic ccmpounds)

S/065/63/000/001/004/005
E075/E436
AUTHORS: Morozov, V.I., Agafonov, A.V., 'Abaveva. B.T.,
Ryabov, V.A., Karpenko, L.P., Gilyazetdinov, L.P.
TITLE: The preparation of feedstock carbon black In thermal
cracking units
PERIODICALt Khimiya i tekhnologiya topliv i masel, no.1, 1963,
39-42
TEXT: A threefold increase in the production of carbon black is
scheduled in the current 7-year plan. New feedstocks suitable for
conversion into carbon black are therefore required to dupplement
green and anthracene oils used at present. Catalytic gas-oils and
lubricating oil extracts (phenol extracts) were subjected to thermal
cracking to produce oils suitable for the production of carbon
black. The cracked oils (43.5, 36.o and 54.4% yields of the
feedstock for light gas oil, heavy gas oil and phenol extract
respectively) contained from 70 to 80% of aromatic hydrocarbons,
of which at least 50% were heavy aromatics. The cost of these
oils was about half that of green oil and a quarter of anthracene
oil. The yields of carbon black from the oils ranged from 47 to
Card 1/2

MOHOZOVO V.I.; AGAF(M()V., A,V,; ABkYFVAO B.T.; FARP12.1m,
Results of the Jndustrls-l of the produatic-n of crudcl
for carbon black in thermal cracking devices. Neft'spere i
neftakhim. no-4aM-M t63 (WRA 1737)
1. Diaskly neftaparembatyvuyuabchi-.,r zav,.,d 1 Tsemayumnyy naueb-
no-i3sledovatelinkly in3titut po pererabotke neft! i gaza i
poluobeniyu iskusstvennogo shtdkogn topliva.

GONSALES, A.A.; KURGANOV, V.M.; AGAFONOV, A.V.; ABAYEVA, B.T.;
POLETAYEV, V.B.; VIVIYERp A.S,; RJJDOVICH, M.A.; BLILYAYEVA, Z.Go;
RUTMAN, G.I.
Results of redesigning an industrial catalytic-cracking device.
Nefteper. i neftekhim. noi9:6-10 163. (MIRA 17:8)
1. Salavatakiy kombinat i Vaesoyuznyy nauchno-iraledovatellskiy
institut po pererabotke nefti.

AGAFOICIVI A.V.; ABAYEVA, B.T.; OKINZHEVICil, N.A.
Catalytic cracking products for petrochemical syntheses
Trudy VNII NP no. 9s27-51 163. ( MRA 171g)

ABAYEVA, B.T.; AGAFONOV, A.V.; GILYAZETDINOV, L.P.; GYULIMISARYAN, T.G.;
V.P.; MOROZOV, V.I.
Testing thermocatalytic gas oil In the production of furnace black.
Nefteper. i neftekhim. no.12:17-19 163. (KM 17:4)
1. Vsesoyuznyy nauchno-isoledovatellskiy institut, po pererabotke
nefti i Nauchno-issMovatel'skly institut shinnoy promyshlennosti.

s/o65/63/000/001/004/005
The preparation of feedstock ... E075/E436
56.7%, which compares well with the yields from green oils. The
carbon blacks satisfy the roCT 7885-56 (GOST 7885-56)
specification. There are I figure and 4 tables.
ASSOCIATION: Omskiy Neftepererabatyvayushchiy zavod VNII NP
(Omsk Refinery VNII NP)
ti
Card 2/2

AGAFONOV, A.V.; ABA,YEVA, B.T.; OKINSHEVIGII, N.A.; ANDREYETA, A.S.;
mojlozov~ V$f'o - .
Developing extraction methods for obtaining carbon black
stock from cata:ybically cracked gas oils. Khims i tekh.
topl. i masel 9 no.5213-16 5 W'64 (MIRA 17t7)
1. Vsesoyuznyy nauchno-iseledovatellskiy inStitUt DO pererabotke
nefti i gaza i poluoheniyu iskusstvennogo zhidkogo toplivao

,ABAYEVA,.B.T.; OXINSHEVICHp N&'A.; AGAFONOV, AJI.; SIDLYARENOKO F.S.;
KAZINSKIYO V.L.;-GrULIMISARIHANp T.G,; SUYEMNK09 L.P.;'
GILYAZETDINOV, L.P*
Using extracts as stock for the production of active aud semi-
active carbon black. Nefteper. i neftekhim. no.500-33 164.
(MIRJ 17:8)
1. Vsesoyuznyy nauchno-issledavatellskiy institut po pezerabotke
nefti i gaza i polucheniyu iskusstvennogo zhidkogo topliva,
Kuybyshevskiy nauctino-iaaledovatellskiy institut neftyer,oy
pronyahlennosti i Nauchno-issiodovatellskiy inBtitut sHnnoy
prozkyshlennosti.

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C1E NRi -5-028680 SOURCE COD,E_Uk_/6SfV657OO0/Oll/O02 5 /0028-
AUTHOR: Gyul'misaryaaL T. G.; Oilyntotdinov, L. Pt,-Ak E. I.; Shmeleva
R. L; )Giokhlov, B. P.; Byatrov, k.' M.; ~Qka!9va,_V V,* S1.ga-kn_a_
Okinshevich, N. A.
jORG: NIIShP; VNIINP: Novo-Yaroslavl Carbon Black Plant (Novo-Yaroolavokiy aszhevyy
.zavod); Volgo r0-froubon Blac Plant (Volgogradskly -a&zhavyy xavod); Scientific
Research-Y-cclinological Design Instf-tute (Mauchno-iseledovatel'skiy konstruktorno-
-t--t-ekhno fo-sif-EF"kii- Fn-iViTut)
TITLE: Industrial tests of new types of petroleum stock in the production of
activated PM-70 furnace black
SOURCE: Naftepererabotka i neftekhimiya, no. 11, 1965, 25-28
TOPIC TAGS: activated carbon, petroleum product, gas oil fraction, phenol
ABSTRACT: In order to confirm and develop the results of earlier studies which
indicated that catalytic and thermal gas oil could be used in the production of
activated furnace black, experimental batches of initial sulfur and hydrofined
phenol extracts of catalytic and thermal gas oil were produced. The physicochemLcal
characteristics of the now types of petroleum stock are compared with those of
green oil; in the 3egree of aromatization they are identical, but in fractional
composition, molecular weight, and viscosity, green oil is slightly lighter, in-
dustrial tests confirmed that hydrofined phenol extracts of catalytic gas oil, the
Card 1/2 UDCt .66.095.21:547,21.001.5

L 12807-66
ACC NRt AP5028680
initial sulfur-containing phenol extract of catalytic gas oil, and also mixtures of
thermal gas oil and green oil (in the ratio of 60:40) c&n be used in the pro4uction
of activated PH-70 furnace black in plants equipped vith cyclone reactoral a dry
system being used for trappIng the black, Orig, am has: 2 figures and 3 tables.
SUB CODIs 07 SUBM DATII now ORIG RVI 006
jw
L Card 212

SOV/137-58-12-25541
Translation from: Referativnyy zhurnal. Metallurgiya, 1958, Nr 12, 1) 205 (USSR)
AUTHOR: Abayeva, M - M.
TITLE: Functional Con iti n of the Liver An-Long Lead-shop Workers at tliz
"Elektrot sink" Plant (Funktsional' noye sostoyanive pecheni u rabochikh
svintsovogo tsekha zavoda "El ekt rot sink-)
PERIODICAL: [Tr.] Sev-Osetinsk. , med. in-ta, 1958, Vol 7, Nr 1, pp 119-124
ABSTRACT: As a result of the study of initial insidious stages of Pb attack on the
liver among 100 practically healthy workers with over 5 years of service,
the following conclusions were drawn: 1) 60% of lead-shop workers with
over 5 years' service, who are considered to be practically healthy,
displayed some symptoms of chronic lead poisoning; 2) 77% of workers
who are in contact with Pb for long periods of time exhibit symptoms of
chronic functional insufficiencv of the liver; 3! Regular observation of
the functional condition of the liver among lead-sl-op workers is neces-
sary.
Yu.S.
Card 1/1

BOTFINIX, M.N.; ABAYRFA, S.M.; ZOISHAROVA, L.M.; OLADKIRA, V-A-
Synthesis of 0-dipentidyl derivatives of acylserine and glycolic
acid. Zhur. ob. khts. 30 no-120877-3883 D 160. (MIRA 13:12)
1. Noskovskiy goeudarstvenW universitet.
(Serine) (Glycolic acid)
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USSRI./Cultivated Plants - Comercial. Oil-Bearing. Sugar-Bearing* M-5
Abs Jour : Ref Zhur - Biol., No 7, 1958, 29879
the cotton wool output by 15-23%. Soaking the seeds for
12 hours in a 0.005% solution Of CuS04 boosted their ger-
mimtione The highest cotton wool yield occurred with 12
hour seed soaking and the further spraying of the plants
in a solution of H3BO3.
Card 2/2
- 8 -

Country : U35R M
Category: Cultivated Plants. Co.-marolal. Oil-Bearing.
SuSar-Bearing.
Abs Jour: RZhBiol., No 22, 1953, No 100367
period from. the 3 of June to the 23 Of JulY
chanSed from 0.5 to 0.75 YnilliSrams/k3, In
the horizon of 30-40 centimeters from 0.05 to
0.4, in the horizon of 50-60 centimeters from
0.17 to 0.4 and in the horizon of 70-80 centi-
meters - from 0.17 to 1.5 milligrans/kg of the
soil. It Is -oointed out that the content of
mobile B in t6 soil Is quite sufficient for
the normal development of the cotton plant.
Determinations of B content In the plants
showed that in different periods of the select-
41 Ion of test specimens, the B content In the
Card 2/4

Country : US3R m
Cate3ory: Cultivated Plants. Commercial. Oil-Bearing.
Sugar-Bearing.
~'.bs Jourl UhDlol., No 22, 1958, No 100367
62%, in the upper - by 130%, In the buds and
flowers - by 42%. -- B. P. Pleshkov
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