SCIENTIFIC ABSTRACT BUGAY, V.I. - BUGAYENKO, L. T.

• Document Type: CREST
• Collection: Scientific Abstracts
• Document Number (FOIA) /ESDN (CREST): CIA-RDP86-00513R000307320005-1
• Release Decision: RIF
• Original Classification: S
• Document Page Count: 100
• Document Creation Date: November 2, 2016
• Document Release Date: June 9, 2000
• Sequence Number: 5
• Publication Date: December 31, 1967
• Content Type: SCIENCEAB

TRO-SIX.T.f.-VTO, V, T. ; 91 G~`,tY, V. I .
DurLhility of steels as de;--endent o:~ Thw plas,.Ic per c:,.r.-:Ie
defc-natJon under corditicEs of ugiforr IUA n0rlZ71form stTesaed
states. Zav. lab. 31 no. 1-2:1501--d"nT 165 (m"P~-,. I-P!I)
1. InstAtit problem mater-Jaleveden4ya AIN

M.' (d) /EWIT 86 IWA (,i)'/WP v4/T,/
-ACC NRi
8660 '-SOUR-CE COM UR/0M0/65/-1'--f/00O/016Q/0269
AUTHORS: Bugay, V. 1. (Kiev); Pinaronko, G. Ss (Academician All (Kiov);
TroshchenRoj-17, T* tmv)
ORG. none
67e-l
TITLE: A study of inelastic deformations in metals under cyclic deformation
SOURCE: Vsesoyuznoye soveshchaniye po, voproaam, statichaskoy i dinamichoskoy
m-, -Rs I pr3. jai
prochnost atorialov j ko-n-s-fr-
i u
--ILe4~~r uFal-N,- -Ti-ri-o-pr-oc-ao-st--EEt-eria=ov-71-Wohbti~0;ltsiotfliykll--olementov--(ThenmI
strength of materials and construction elements); materialy soveshchaniya. Kiev,
Naukova dtu!fl-.a, 2.965, 160-169
circuit design
TOPIC TAGS: /fatiCue strength, metal stress, strain, plastic deformation, hysteresis
loop, copper, si;eel / 45 steel) 25 steel) 20Kh steel, E1726 steel, M18NIOT steel,
TsDM PU-10 testing machine 61
ABSTRACT: The courso of plastic deformations in metals and alloys as a function of
the stresses ading cyclos,& studied. The work was done to obtain
qLmiber of lo r
criteria for the ~ 1s. A system developed ear"er by V.
~ atigue strength of mate.
T. Troshchenh-o (Novyyo mashiny-1 probory dlya ispytaniya notal V, M., I'llotall gi zdat
1963) underlies the method, The 10-ton East Gorman TsIM Pb-10~3 chino "nic %d for
mechanical loading of up to P a =-j4-9kFT. The frequency can be varied sinoothrly from
Card 113

L -2181P-66
FA-CE-NR--,-
AT6008660
500 to 2000 cycles per minute. A dynamic hysteresbo loop in coordinates proportional
to 0- and & is obtained on the screen of an oscillographIduring testing (see Fig. 1).
Fig, 1. Circudt for recording dynamic hysteresis
loops with cyclic variable loading;
1 - oucillograph; 2, 10 - filters;
3 - amplifier; 4 - tensostation;
6 - PIN switch; 5p 71 8p 9 re-
sistance pickups.
Card 2/3

211818-66
ACC NR
AT6008660
Copper and 45, 25, 2RY~hj KI7261 and M18111M stools wore
Fig. 2.
2. Pi
-T1
Change in width of hysteresis loop versus stress: a - first
loading; b - second loading; 1 - E1726; 2 - 25 stool; 3 - 20Kh
steel; 4 - 45 steel; 5 - M181110T Stool; 6 - copper.
With cyclic stress and strain, opening of the hysteresis loop for the steels tested
is observed with much smaller stresses than with static loading. For the stools,
with stresses exceeding the fatigue limit, the width of the hystoresiri loop in-
creases regularly with the number of loading cycles until destruction of the spec-
imon. Orig. art. has: 2 diagrams, 3 graphs, 2 photographs, 2 tables., and 4 formu-
las.
SUB CODE: 20, la)6UBM DATE: lgAug65/ ORIG REF: 002
3 13 ~'

I-1683DZ43 o/t s
DS Amirconc/AsD
APCESSION NR;i AF3003Z65 S/OZ86/631000/003/0036/0036
AUTHORa i. JNLsT, Ye. A..' arfolomec~ev,.D. 7.*, Zaelatskaya, L. M Prokof 1yeva,".
'Ye M,
lb
TITLE: Methcd of increasing stability of gasoline. Class C 10g, V. 1 sub:04.1
No..152924
SOURCE: Byul. izobretenLy i tovarnykh znakov, no. 3, 1963, 36
TOPIC TAGS: gasoline, inhibitor, phenolic oil, oxidation, oxidation inhibitor!
ABSTRACT: Method of increasing the stability of gasolines by adding oxidatim:
inhibitors. its distinguf1shing feature is that the oxidation inhibitor used
1s acid phenolic oil. /Ustracter's note: complete translation.7 (3rig. ari.:
has no figures, tables,-or formulas.
.,.ASSOCIATION: none
SU%1ITTED: OqApr62 DATE ACQ: 23jul6Y ENCL: 00
SUB CODE: FL NO REF SM 000 OTHER: OOCi
ar4
L
1A

IWGAY., Ye.A.- - --
Device for mea.,3uring the Inner diameter of furiace tubes.
Neftianik 6 no.2:23-24 '1 161. (.'.0,RA 14: 10)
1. Nachallnik tsekha Ufimskogo neftepererabatyvayushchego
zavoda.
(Petroleum refineries-Equipment and supplies)

VARFOL%IEYEV, D.F.; BITGAY, Ye.A.; DUDIN, V.N.; ZAGRYATSKAYA, L.M.; ANTIPIN,
M.K.; MARKINA, A.I.; POLINSKAYA, M.R.;
Recovering spent caustic using flue gases. Trudy Bash NIJNP no.5:
319-322 162. (MIRA 17:10)
1. Ordona Lenina Ufimskiy neftepere.-abatyvayushchiy zavod.

ACCESSION NR: AP4036978 S/0065/64/000/005/0017/0022
AUTHOR: Masagutov, R. M.; Berg, G. A.; Varfolomeyev, D. F.; Selivanov
T. I.; Bugay. Ye. A.; Mukhametov, M. N.; Kulinich, G. H.; Sokolovs,
V. 1.
TITLE, Development of a process for high-purity cy'clohexane
SOURCE,i Khimiya i tekhnologiyn topliv i masel, no. 5. 1964. 17-22
TOPIC TAGS: cyclohexane, benzene, benzene hydrogenation, catalyst,
nickel on kieselguhr, benzene purification, thiophene, sulfur com-
pound, cyclohexane production
ABSTRACT: An industri.al.p-raceas for cyclohexane has been developed
on the basis of prel,inipary pilot tentm. Cvclohexanp of adenunte
purity was produced by the-one-step hydrogenatton of benzene (cyclo-.-
hexane content, < 0.4%; thiophene content, < 0.00001%) on technical-
-grada. nickel on kieselguhr catalyst under the following conditions:
Pressure 10 kg/cm2 gage; space velocity of benzene feed, 0.5-0.6 hr-1
maxinum reactor temparature,120-150C; hydrogen/benzene ratio, 3000
Card 1/3

ACCESSION HR: AP4036978
M3/m3. Catalyst activity did not drop after 15 days of continuous
z,ervice. However, the degree of conversion of benzene containLnp
0.08% thiophene and 0.010% carbon disulfide dropped rapidly from 100
to 60%. Thus, a study was made of the possibilities for the prelim-
inary purification of benzene to remove sulfur compounds. The study
took into account data from the literature which indicate that thiophene
in contact with the catalyst surface simultaneously blocka five
active nickel atoms. In hydrocen the adsorbed thiophene tiolecule can
decompose with the formation of a hydrocarbon molecule and of an S
atom. The S atom combines with n nickel atom. but the hydrocarbon
molecule desorbs from the catalyst surface, liberates four previously
bound Ni atoTas, and increases the S adsorption capacity of the
catalyst. The results of the study and laboratory experiments have
made it possible to develop a large-scale unit for the productioi f
cyclohexane from benzene (containing 0.1-0#8% cyclohexene, up t-
0.03% hexane, 0.02% other hydrocarbons, and 0.01-0.04% total sulfur)
under the following Japproximative) conditionst pressure, normal;
temperature, 110 to 15OC; space vslocity of benzene feed, 0.2-0,85hr-I
hydrogen/bentene molar ratio, 9.5,1-20* The procassi is conducted in
Card 213

ACCESSION NRs AP4036978
two steps: purification of benzene from 5 compounds ':and hydrogenation
on two reactors connected in series. The unit has been in operation
for two years. The cyclohexane is being used for making polyethylene.
OrLg. art. hast 3 figures and 2 tables*
ASSOCIATION& BashNIINP; OLUNPZ
SUBMITT'ED: 00 DATE ACQ: 05Jun64 ENCL: 00
SUB CODE: GG NO REP SOVs 014 OTHER% 006
3/3
Ccrd - ------

ACCESSION NR: AT043277 S/2744/64/ooO/007/0121/0127,
AUMORt Hasagutov.. Re Me$ Berg, G 9 A., Varfolomayev, D. J?.0 Selivanov., T. I.,
Aop Kulinich"G, Me, Sokolova, V. Ill, Mukhawtorp Me N.
'TITLE: Purification of benzene by chemitorption
SOURCE: Ufa. Bashkirskly nauchno-issiedovatellskiy Institut po pererevotke nefti.-
Trudy*, no. 7, 1964. Sernisty*ye neftl I produkty* lkh pererabotki (Sour crude
oil and products of refining), 121-127
1 TOPIC TAGS: benzene, desulfurization, chemisorpti6n, nickel kieselquhr~catalyst,
thiophene, carbon disulfide, cyclohexane, puri'fication
ABSTRACT: Since neither sulfuric acid treatment nor hydrofining guarantee com-
I plete removal of sulfur from 'benzene, the authors investigated'the'chemical de-
suffurization.of a beiizene sample containing 0.08% (by welght)~-thiophene, 0.0102%
carbon disulfide and 0.3% cyc,lohexane,'using a commercial nickel catalyst on
ki'ese'tguW(d-93 qj(~c. bulk density) with 60% nickel. Desulfurization was more
effective at higher temperatures than at room temperature. The high degreeof
'i'betwee:n the
purifl6ation obtaln4~i4 at 170-IBOC may be due both to a better co tac, I
When 6 were
6igidne ind the catalyst and a higher diffusion rate. en-z"einle. samples
J, driffe~d'it 170-180C:wlth the addition of hydrogen, the ads6rptivity of the cata-
P
wasAncreased 4.4 times as compared to'the usual ddsorptjon:,qndItlons. This

L 22570-65 ZPF(c)/~~I-.T(m)/T Pre-4 WE
ACCESSION NR: APS001627 S/0318/64/000/01210003/0006
AIMOR: Has gjLt~ov, _ It, Me. Berg, G. A.. Varfo omeye Selivanov, 1, 13
Kulinich, G. Me, Hironov, A. A., Pau, G. Me, Bugay, Ye. A.
TITLE: Results of the operation of a hydrofining unit for diesel fuel
SOURCE: Nefteparerabotka I neftakhimiya, no. 12. 1964a 3-6
TOPIC TAGS: petroleum refining, hydrofining, diesel fuel, catalytic cracking.
sulfur content
ABSTRACT: The report describes the basic design and the results of 7 months oper-9
ation of a hydrofiner at the Ufa refinery. Straight-run diesel fuel and thermal '
and catalytic cracking fractions with 1-2.1 wt.% sulfur content and iodine numberf
of 5-20 were blended, heated in exchangers and in a tubular furnace to 380-420C. 1
and refined over an alumina -cobalt -molybdenum catalyst. Uydrogen-containing gases
ware separated, scriibbed in a monoethanolamint unit, and recirculated. After re-
moval of the gaseouc fractions, the product was passed through a stabilizer to re-
cover 95.5 wt.% dispel fuel and 1.5 wt.% gasoline per feed. The sulfur concentra-
tion in the feed varied from 1.04 to 1.4 wt.%; it was reduced Initially to 0.02 wt.
% and after 7 sonthu operation to 0.15 wt.% in the diesel fuelg and the catalyst
Card 1/2

L 2257o-65
ACCESSION NR: AP5001627
was regenerated when the product sulfur content reached 0.25% after 240 days.
Since hydrogen deliveries from catalytic reforming and the ~team-iron reaction
were inadequate, only one of two available refiners was operated. The design
pressure of the refLner was reduced from 50 to 34-36 to decrease the hydrogen con-
sumption. The design temperature was not changed, and the product quality was not
affected. Various improvements made on unsatisfactorily performing units are des-
cribed. Orig. art. has: 2 tables and I figure.
ASSOGIAXION; Ufimalriy ordeva lAntas nefteparerabatywayushchly savod (~ft petrol-
a= refinery),, BashKEINP
SUMC=Dt 00 Unt 00 OR 00M YP
NO REF SOVt 002 arm: 000
Card 2/2 .

A C C N";
AU Tz' 0.-
0`~G: U fa Potroli~tr-,
porora ,-vayishchilv
bat,
A.; Prok
RDf inerr of the Order of
Ilavi
Li
nskiy or"ona :~z)nina nefte-
TITL~: "ions of dostruc+--vO sulf.ur
x CL~eration of cal"..i.irtic crackin-. unit undor
rumoval from the diesol fuol fractionli
S UP., 0 E, 17aftenerarabotk;;. i noftokhim~ya, no. 0
'10"IC catalytic crackinr,
A -I 1~ 1:~ - . -
ur-az
:1-Ca. :.;L -alf ,ear's 07,cr~.-o.,-. c".' un-. r - s fur
concii-t~-Lons at, tht- putrol,3-,:r-. ().L:' thc St-:-us oil thu iin4~t wa!%7,
an' rals-
-In :) r -a rto i-inrove th,-.) -~-(-c`
C, 1 t t -e nz~ccw,,,; of sulfi:.- re.7-.-oval. L) c
nrocass Of n, z-;If Vr
is of ~~iosf I -1i a C1 1. 7 a
s. a' `50 0.
ona incroa.-,os ',tie EtfficienC-r of the c--roc,--ss, ~-Inccj ',h~:-. crac',.in- ta'.--
fractions occurrin.7 -i:,.-oltaneously vit'- tho is ass-Cc., tle 'o-.-
nation of an additional quantity of target products which offset the losses of tha
diesel fraction taking place during the destructive sulfur removal from the main por-
Card 1/2 UDC: 665.6~~.2.05:665.65LZ6-,

L h5677-66
ACC NR: AP6023621
L-on of the stac,:. Distillates o-r' socondary orL-in (in addit-on ~o the Straigh',-rnun
d"-',e-,el on:.) ara ~d'-;L) used as Stec', in """j Sulf"Ir ronc proct~s.-_ -I-
tion of sulfur Lmor,:~ the fractions of s'L-lor-11 ai-.d pl,rifie-
t"'-,o catal,,~Uc crac"Izin- is c;iven. Th-3 ~;ut- -as -,z'Fol4ne ob~a` &d du.-in- tl~o
t1rification Drocess are equivalent in quality to tha sano products of' catalytic crack-
Ing. it is concluded that practically all the indicators of the procoss wore improved!
'by the modifications introduced. Orig. art. has: 2 figures and 5 tables.
SUB CODE: 11/ SUBIM DATE; none

ACC 114R: AP601.8619 SOURCE CODE: IJR/0065/66/000/006/0007/0010
AUTHOR: A. ; S-elivanov, T. I.; Akhmetshin, M. I.; D'yachenko, A. Ye.;
i--k" V. i.
,Mironov,-A.' A.; Nikuli &
ORG: Nov-o-Ufimsk Petroleum Ilefinery (Novo-Ufimskiy neftepexerabatyvayushchiy zavod)
TITLE: Experiences in tile production of gasoline and diesel fuel from highly scur
crudes
SOURCE: Khimiya i tekhnologiya topliv i masel, no. 6, 1966, 7-10
TOPIC TAGS: gasoline, diesel fuel, petroleum refining, petroleum refinery equipment
IABSTRACT: A destructive-adsorptive desulfurization process for sour feedstocks was
Ideveloped in laboratory and full-scale runs at the Ufa Order of Lenin Petroleum Re-
ifinery,(Ufimskiy neftepercrabatyvayushchiy zavod) to reduce production costs and
!particularly the consumption of hydrogen, the insufficient supply of which is limiting~:
,the output of hydrodesulfurized fuels. An aluminum silicate catalyst and the catalytic,
'Cracker type 43-102 were used at 390-420C and 1.2-1.81ir-I space velocity to produce
i 1
75.7-82.2% and 7.9-11.1% yields of diesel. fuel and naphtha, respecLively, decreasing;-
ithe sulfur content to approximately 50% of the input value and to not more than 1-2
lafter blending with light straight-run fractions. The cost of diesel fuel was ap-
1proximately 20% lower as compared with hydrorefined fuels. Use of the cracking unit
Ifor the process is recommended when heavy feedstocks for catalytic cracking are in
!short supply. The unit was also employed for desulfurization of thermal cracking
Card 1.17

L 4 107 C
ACC NR. AP6018619
naphtha at 410-420C and 0.75hr-I space velocity, thus reducing 8-fold the amount of
required blending stocks for production of type A-66 gasolines.:' The following werc
among those who participated in laboratory and industrial experiments: G.J..
Chmutov, S. G. Prokopyuk, R.__4. K os~ova ]~. N. Mukhametov, Ye. M. Varfolomeyeva,
B. N. Rays, K. F. Pr-y~-khina, M. R. Polinskay-p,-A. V. Tenikova. L. F. Yevstifey.~_y, and
A. S. Kononov. Orig. art. has: I figure and 4 tables.
SUB CODE: 11, 21/ SUBM DATE: none/ ORIG REF: 0?-2
t !

YASAGUTOV, R.M.; DAINILOVA, R.A.; ZAITOVA, A.Ya.; GILYAZ~11, N.G.;
ZAGII,YATSKAYA, L.M.; _40GAY, Ye.O.; PRIAMINA, K.F.
lfigh-temperat,ure cateLlytic cracking of heavy fractions of
straight-run gasoline. Trudy BAshNII NP no.6:14-18 '63.
(MIPA 17:5)

yt/.

9.3150, 24.2120 776Y)
30';/",7 -30 -3
AIJ711OP:, Sth'.1
nikov, K I -01"V' V. 7 1 ?;,:w~v, N I.,
,
ixu~.,~Pvj Ja V. A.
TITLEa I1,v1..t!(*!,,.1(,nn or Ion Cyclmr,n ~-nancr In

FER10DICALs Zhur:1,11 VnI JO, Ur 3,
vi 7t~,3-2,'w
AB3TRACTi The heatlln,, up of pla!;-i urvl~-r lon -.-.clotrc..-, reno-
nance, dirctly tn.
f th C ~ I ctric firld, la a pro-na %!:-Ich
1.1 H~P- L. utJI.- f., nl,-h 1-1~
t ~,ituvrn Iwory developd by ~,,Ixjve
f)
Indi ,atcd ta'a at plami dclisItifs or I , C
x
and m re, onp could Ft-nerate and tr.~mall-P %o-
Cal Iod Ion cyolotrQn wi%,3. The autnori, therefore,
lnv,,,,,F,,t,d I.n 1.tr- -env- 1.
a or d,cyC
i
101~ , 3
dr. _ , --It
h
~n
l.

Card 1/ 11
.
,
g
-10
y
,nd,
p
m
iMr-alSe CondIL1,11S, -Ing a dcvlre drgcrlbed on P1Z.3-
ASSOCIATIOHt rhy lco-Technical InstltuteASUkrSSR, Khar-kov
(A1Z,DtO-tekhnjchc~kjy jn3t 1tut AN USSFt, Mar -kov)
SUBMITTED: 00tober 22, 1959
Card 11/11

SINELINIKOV, LD~,, TOLOK, V.T.3 NAZARGV, N.I.; BAKAYbT, I.I.; BONDAREV,
V.A., BUGAY, Yu.P.
Investigation of ionic cyclotron resonance in a dense plasma.
Zhur.tekh.fiz. 30 no.3:282-288 1,h- ~60. 04IRA l4t8)
1. Fiziko-teh1uA.,,heskiy institut AN WSRY Khar1kov.
(Plasma (Ionidzed gases)) (Cyclotrun resonance)

S/781/62/000/000/001/036
Sinellnikov, K. D., Tolok, V. Nazarov, N. I., Bukayev, 1. L, Bondarev. V. A..
Bugay, Yu. P. ., Loginov, A. S., Kononenko, V. 1.
Investigation of ton cyclotroif resonance In a dense plasma
PERIODICAL: Fizika plazmy I problemy upravlyayemogo termoyadernogo sinteza; doklady I
konferentaii po fizike plazmy i probleme upravlyayemykh termoyadernykh
reaktsiy. Flz.-.tekh. inst. AN Mr. SSR. Kiev, Izd-vo AN Ukr. SSR, 1962, 3-8
TEXT: Ion cyclotron-resonahce heating of plasma,* whereby field energy is transferred to
the ions directly, Is a promising method of rapidly attaining high ion temperatures. The
article describes investigations of ion cyclotron resonance in a plasma produced by direct
discharge in a glass tube 60 cm long and 6 cm In' diameter. The discharge was produced by
a rectangular voltage pulse of duration upto 800 microseconds and current up to 600 amp.
The discharge tube was placed In a magnetic field produced by a solenoid fed from a capact-
tor bank with maximum stored energy 40,000 J, charged to 5 M The time required for the
Card 1/2

S/781/62/000/"000/ODI/036
Investigation of Ion cyclotron resonance In . . .
mapetic field to reach maxiinuni was 4.7 Y 10-3 sec.
The experiments have shown that there exist optimum values of hydrogen pressure and
discharge current for the absorption of high frequency power by the plasma. The half-width
of the resonant curves increases monotonically with increasing gas pressure, indicating that
the accelerating ion interacts strongly with the neutral atoms. An increase in the discharge
current and.consequently in the ion density in the discharge also shifts the resonant peak
toward magnetic field values below the resonant field. Density measurements in the hydrogen
plasma have shown that at 300 amp a plasma of 6 x 1013cm-3 d3nsity has a lifetime of 150
microsecoi-ids after the termination of the discharge. It is also noted that the resonant [leak
becomes asymmetrical with increasing plasma density, this being possibly due to the diver-
sion of part of the high frequency power to the generation of Ion cyclotron waves. It is also
likely 'that at densities above cptimal the screening of the plasma against the high frequency
field comes into play.
There are eight figures and five references. The English language references are: K. S. W.
Champion, Proc. Phys. Boo. 70, 446, B, 212 (1957), and translated articles by T. N. StiX and
R. W. Palladino.
Card 2/2

RASTREPIN, A.B.; ZOLOTOTRUBOV, I.M.; BUGAY, Yu.P.
Mass-spectrometric study of the energy distribution of ions in
a plasma. Izv. AN SSSR. Ser. fiz. 27 no-8tlU3-1117 Ag 163.
(MIRA 16:10)
1. Fiziko-tekhnicheskiy institut AN UkrSSR.

L 10928-67 Za i ' 1 SQ13___uZG
A_(T_NR,__AT6022 2S5.. SOURCE CODE: uk-loOOq6-6'160-61000-10080-100-8-4--'I
AUTHOR: Chervov, V. G.; Bugay, Yu. P.
ORG: none
TITLE: Some aspects of functional simulation of nerve elements and systems
0
1.)
SOURCE: Vsesoyuznaya nauchnaya sessiya, posvyashchennaya Dnyu radio. 22d, 1966.
Sektsiya bionik~. L/ Doklady. Moscow, 1966, 80-84
TOPIC TAGS: bionics, model, nervous system, physiologic parameter
ABSTRACT: The large amount of factual material accumulated in neurophysiology should
be used more widely for the design of appropriate models of nerve elements and
systems. The great complexity and dynamic characteristics of ihe parameters of nerve
tissues can be broadly reproduced on models with readily available means if the model-
ing process is based on the internal processes of the nervous cell taking into account
its dynamic properties and the universality of its characteristics. The study of the
characteristics of the nervous tissue during transitions between functional states
permits the incorporation of the totality of the known physiological properties of
nerve elements into a system and to supplement the physiological simulation premises
by new facts, not previously used for simulation.
SUB CODE: 06/ SUBM DATE: O8Apr66/ ORIG REF: 004
Card 111,61i

h3762
S/081/62/000/023/085/120
B144/B186
AUTHORs Bugaychuk, A. M,
TITLE% Commercial isooctylene as a raw material for the production
of alkyl phenol
PERIODICAL: Referativnyy zhurnal. Khimiya, no. 23, 1962, 595-:-596,
abstract 23M216 (Novosti neft. i gaz. tekhn. Neftepererabot-
ka i neftekhimiya, no. 5, 1962, 19 - 20)
TEM In the production of the additive Taiatim-339 (solution of the barium
salt of alkyl phenol sulfide in mineral oil) which is used for motor oils'
phenol is alkylated by polymer-gasoline in the presence of benzene sulfonic
acid as catalyst. The non-reacted polymer-gasoline and the low-molecular
alkyl phenols are distilled with water vapor in vacuo from the reaction
mixture (the distillate is recycled for the alkylation of the phenol).
The residue, alkyl phenol with a flash point of Z-115 0C, is treated, after VY
washing with water and drying, with S 2Cl2 and then with Ba(OH)2' The
results are given which were obtained in industrial experiments on the use
Card 112

s/oal/62/000/023/085/120
Commercial isooctylene B144/B186
of commercial isooctylene (I) (b. P. 77 - 2050C, molecular weight 116-125)
instead of polymer-gasoline for the alkylation of phenol. For the alkyla-
tion of phenol with 1, the following optimum conditions were found:
temperature 65 - 780C, molecular phenoltItbenzene sulfonic acid ratio
1:2-5: 0.1, time 8 hrs, after addition of the entire I the temperature of
the mixture in the reactor was increased to 1100C and the mixture was cir-
culated through a tubular cooler into the reactor for 4 hrs; properties of
the alkyl phenol obtained (afterodistillation of"the tops6 washing and dry~
ing): d38 0.92, flash point 115 C, viscosity 5.4 cst/100 C, molecular
weight 4 209; from (in kg) 1300 phenol, 3200 1, 1200 alky~lation tops, and
180 benzene sulfonic acid were obtained 4200 alkyl phenol and 1200 top
distillate. Industrial batches of the qualitative additive Taiatim-339
prpepared on the basis of alkyl phenol obtained by using I have only a via-
cosity of -13.5 cst/1000C, which is thus lower than that of the commercial
product ( >,15 cst/1000C). [Abstracter's notes Complete translation
Card 2/2

7-L
s/ool/63/009/004/027/C'51
B149/B186
AUTHORt Bugayc!Lu ~,A
TITLES Factors affecting the synthesis of alkyl phenols
PERIODICALS Referativnyy zhurnal. Xhimiya, no- 4, 1963, 453 454t ab-
stract 41139 (Novosti neft. i gaz. tekhn. Refteparerabotka i
'neftekhimiyall, no. 6, 1962, 13 - 15)
TEXT: A series of experiments was carried out under industrial conditions
at 60 - 1060 in order W determine the optimum temperature for catalytic
alkylation of.5henol (I) by an extended fraction of technicalpolymer-
diotillate (I , which is a product of catalytic polymerization of the
amylene-butylene fraction of the cracking and reforming gases, and contains
C - C olefins. The catalyst was benzene sulfonic acid (III) containing
5 11
90 - 9459 monosulfonic acid. Two sorts of II-wera used in the investigation
- one with an iodine number of 136 and 7Z evaporation up to 1270, and the
second with an iodine number of 127 and 1 ep evaporation up to 1270 - with
a molecular ratio of IiIIMI - 1t2-510.1 and a feed rate for II of 1100
kg/hr. It was found that on raising the temperature of the process the
total yield of alkyl phenols increased the more markedly, the higher the
Card 1/2

S/081/63/000/00-1/027/051
Factors affecting the synthesis of ... B149/B186
concentration of low-boilinG olefins in II. The maximum yield of alkyl
phenol occurs at 96 - 950. Further increase of temperature causes enhanced
polymerization of crude olefins and intense evaporation of the olefins with
low molecular weight,..with a drop in the yield of alkyl phenol. At 80-850,
the olefins with low molecular weight do not react completely with 1, but
are for the most part lost during the alkylation itseli and, to 8ome extent,
during the washing vith water and drying of the alkyl phenol obtained. To
reduce the evaporation of the olefins with low molecular weight which are in
the vapor phase at 90-950, it has been suggestqd that Il be introduced into
the reaction mixture through a layer of a molten mixture of I and III. The
alkyl phenol obtained at 90-950 has lower viscosity and specific gravity
than that obtained at 60-650 because of the presence of alk 1 phencls with
shorter alkyl chains. Howeverp the UIAAThM-339 (TsIATIM-339~ additive
prepared on the basis of this allcyl phenol is not inferior in its qualita,
tive indices to that obtained from the more viscous one, and is superior
to it in terms of ash content, despite the lower viscosity. Comparative
characteristics of the additives are supplied. Lkbotracter's note; Com-
plete translation.3
Card 2/2

BUGAYCHUK, A.M.
- ---- ---- - 1. - -- - ~ -
Mastering and Improving techniques used in the production of'
formaldehyde condensation additives. Nefteper. I neftekhim.
no.1:9-14 163. (MIRA 16:10)
1. Permskiy opytno-promyshlennyy neftemaslozavod.

--BUGAYCHUI,, A.M.
FXf icient methf d for the neutralization of alkyl pheno2-9 by
barium-Hydrooxide. Nefteper. i neft,-;khim. no.7,t2l-25 "63
(M)M 17C7)
1. PemskI7 oputno-promysViewivy neftewslo-mcmd.

BUGAYCIIUK, A.M.
Use of T11- and 0711-6W centrifuges for the filtration of TsIATIY,-
339 additives. NefteDer. i neftekhim. no.10:35-40 163.(MIRA 17:2)
1. Permskiy neftemaslozavod.

hr

L 05895-67 EWN
ACC NR, AR6031251 (Aj SOURCE COED: UR/0081/66/000/011/MO261 M026
AUTHOR: Kravchenko, 1. V.; Vlasova, M. T.; Yudovich, B. E.; Krykhtin, G. S.
Kirillov, Yu. D.; Turkot, 1. M.; Sfi-orokh, I. N.; Bugaychuk, A. V.
TITLE; The production of a quick -hardening cement at a Zdolbunov Cement-Slate
Plant
\4 1-Z 0
SOURCE: Ref. zh. Khimiya, Pamll, Abs. 1IM192
REF SOURCE: Nauchn. soobshch. i Goa, Vses. n, -i, in-t tsementn. prom-Bti;
no. 20(51), 1965, 36-41
TOPIC TAGS: cement, quick hardening cement/Zdolbunovskiy Cement Slate Plant
ABSTRACT: A technology was developed for manufacturing very quick-hardening
cement with a hardening strength of 300 kg/CM2 after one day, 450 kg/cm2 after
three days, and 700 kg/cm2 after 28 days. At the Zdolbunov Cement-Slite Plant
the base mixture is mnde from hard chalk, clay, -and loams, containing a consider-
able quantity of large-crystal quartz; calcining was conducted in rotating furnaces.
118 and 170 m long. The physicochemical properties of the base components were
studied, and the effect of the following factors on the cement stren& ww analyzed:
1/2

67
NR1 AR6031251
the' type of fuel, the method of grinding the clinker, and the reactiviiy of the
components. The reactivity of the base mixtures was found to be low, since 30--
4516 SiO2waq present in the form of quartz particles larger than 15,Ac. The cross-
sectional view of the mmiufactured slurry showed large quartz 'rystals, 250/4.
The best results with respect to cement strength and furnace. productivity were
obtained with clinkers containing 55-63%C3S and 7-8%'.C3A when n w 2.3-26,
and p = 1. 2-1. 4. The required cement strength wah obtained when the specific
3500-4000 cm2/g, whil 'e the specific surface should be 5000 cm2/g when calcining
the clinker in a solid fuel. Mills, operating in open or closed cycles can be used:
the temperature of the clinker being fed into the mill should not exceed 70-801 in
the first case and 1001 in the second came, and 1001 at ihe outlet from the mill.
[Translation of abstract)
SUB CODE: 071
kh
Card 212

I,BUG_,,.YCH'UK,_I.S.; SIRGIUNKC, V.V.
Replacing cross switches with a crane. Pat' i put.khoz. 4
no. 5:5-6 Yv 160. (MIRA 13:11)
1. Starshiy dorozhnyy master, stantsiya Kazatin, Yugo-
Zapadnoy dorogi (for Bugaychuk). 2. Nachalinik distantaii puti,
stanteiya Kazatin, Yugo-Zapadnoy dorogi (for Sargiyenko).
(Railroads--Switches)

BUGAYCHUY,, A.P.
Using a ballaster for lifting switches. Put' i put.khoz, 5 no.4:21
Ap 161. (VIEU 14-.7)
1. Starshiy dorozbnyy master st. Kazatin,, Yugo-Zapadnoy dorogi.
(Railroads-Equi*ent and supplies)

'*Io i)zhnyy mastel, (Stantsiya Kol-khoznyy, Yuzhnoy dorogi);
OLEYNIKY A.P.,, c. r
,,BUGAYCHUK, I.S., starshiy dorozhW master (Stantsiya Kiizatin,
Yug5~~-D M-y---dorogi); LIPMAN, L.P., inzh. (g. Kazan');
AutrgEuv, le.ve. mostovay nuter (S~mtmiy& Belev, Monlicovskoy
dorogi)
TA#ers to the editor. Put' put.khoz. 5 no.9:47 S 161.
(MDU 14:10)
(Pa.Uroads)

BEZRUKOV A. M.; PnBUDIKO, N. S.; BUG~YCHUK I S.
Iaying switches on blocks of reiWforoed concrete. Put' i put.
khoz. 7 no.3:3-6 163. (MBU 16:4)
1. Nachallnik Kazatinskoy dls~fitsii Vuti Yugo-Zapadnoy dorogi
(for Bezrukov). 2. Zamestitel nachal nika Kazatinskoy distantaii
puti Yugo-Zapadnoy dorogi (for PribudIko). 3. Xachallnik mekhani-
sirovannogo uchastka Kazatinskoy distantaii puti Yugo-Zapadnoy
dorogi (for Bugaychuk).
(Railroads--Switches)

MAKHORIN, K.Ye.; BUGAYUKO, B.P.
Selecting furnacesand fuels for the magnetization roasting of
Krivoy Rog quartzites. Metallurg 5 no.10:3-7 0 160.
(MIRA 13:9)
1. Institut ispollzovrntya gaza AN USSR.
(Krivoy Rog-Quartzite)
Ore dressing)

BUGAYCHENKO, MJ., inzhoner-makhanik.
-, -
Description of machinery for working fallow in the southern steppe.
Mekh. oil'. hosp. 8 no.9:28-29 S '57. Offin 10:9)
(Ukraine--Agricultural machinery)

IKUNIMN[O, N.V. [Th, icheako, N.Y.], izxzh.-mekhanik
What we expoet from Irubertsy machinery builders. Mekh.sill
hosp. 11 no.2;26 1 160. (KTRA 13:6)
(1g,ubertay--Agricultural machinery industry)

-G-
e
nk
vnth thin wh
NO. Mai I
The author,
di i6nal flo

I :urv6d
s ightly c
iWofiles are eR6
else '4*c:perpCP4
as being due - tc
-o-tdbui~d .46ng
-of tile ~ortcx-di!
intf
-g

Fquatilon can

case 1 Munk's fi
pmfiles, of smal
tile floW is coil
infiriky 11,11d bvi
the
Source:

p

i~ p
G.A.
BUGA 11K03
r~
K voprosu a struinom obtel-anii beskonechnoi reshetki gazom v priblizhennoi postaro-
,.rlce S.A. Chaplygina. (Ilrikladnaia niatematika i mekhanika, 19L9j v. 13, no.h, P.449-
hc~6, diagrs.)
Title tr.: Problem of gas flow over an infinite cascade using ChaplyFin's approxi-
rpation.
QA801.P7 19L9
SO: Aeronautical Sciences and Aviation in the Soviet Union, Library of Congress,
1955

BUGA~NKO, G. A.
'N
On the problem of gas flow over an infinite cascade using Cha gin's approximation.
Washington, 1951. 14j.p., diagro. (U. S. NACA TM no. 1298~
Trans. of K voprosu o struinom obtekanii beekonechnoi reshetki gazom v
priblizhemoi postanovke S. A. Chaplygikm.
TL507-U57 nol 1298
SO: Aeronautical Sciences and Aviation in the Soviet Union, Library of
Congress, 1955

BUGAYENKO, G. A.
''Swing of a Pendulum," Fiz. v Shkole, No-5, 1952

'.%W)&O~s~es'_' Convection FD-656
Card 1/1 : Pub. 85 - 11/20
Author : Bugayenko, G, A. (Molotov)
Title : Free convection in an inclined cylinder
Periodical Prikl. mat. i mekh., 18, 212-214, Mar/Apr 1954
Abstract Treats the gravitational-thermal convection in cyl--*nder which',is
inclined to the vertical, and studies the stationary current vhose
lines of flow are parallel to the axis. Two references, including
G. A. Ostroumov, Svobodnaya konvektsiya v usloviyakh vnutrenney
zadachi (Free convection under conditions of the internal problem),
Chapter 7, GITTL, 1952.
Institution
Submitted January 18, 1954

SOV/124-57-9-10245
Translation from: Referativnyy zhurnal, Mekbanika, 1957, Nr 9, p 50 (USSR)
AUTHOR: Bugayenko, G. A.
TITLE: Flow About a Plane Hydrodynamic Cascade According to the Principles
of the Vanishing-viscosity Theory (Obtekaniye ploskoy gidrodinami-
cheskoy reshetki po skheme teorii ischezayushchey vyazkosti)
PERIODICAL: Uch. zap.**Molotovsk. un-ta, 1955, Vol 9, Nr 4, pp Z5-28
ABSTRACT: The well-known solution to the problem of the incompressible fluid
flow about. an isolated fluid foil according to the principles of the
vanishing-viscosity theory [ Kochin N. Ye. , Kibel' 1. A. , Roze N. V.
Teoreticheskaya gidrodinamika (Theoretical Hydrodynamics), Part 11.
Gostekhteoretizdat, 1948] is expanded to include an infinite cascade
of straight fluid foils placed in a straight line perpendicular to the direct-
ion of the impinging flow. It is presumed that beyond each profile of
the cascade there is an infinite vortex region separated from the basic
non-vortex flow by two semi-straightline segments originating at the
edges of the fluid foil and extending parallel to the impinging flow. The
liquid slips along the face of the fluid-foil facing the stream and adheres
Card 1/3 to its far side. The study of the flow velocity field is reduced to the

SOV/IZ4-57-9-IOZ45
Flow About a Plane Hydrodynamic Cascade According to the Principles (cont. )
determination of an an.al.ytic function w,(z) in the z plane of the flow which is
regular in the region of flow and is characterized by the property that on the se.g-
mental boundaries along the imaginary axis simulating the cascade arg dw, dz
assumes a prescribed value and that for Rez- + - the derivative dw,/dz tends
to approach a prescribed limit. This is equivalent to finding the function Li = i -
loge dw/dz which is regular in the region of the flow that has a prescribed Re W
value on the segmental boundaries and that tends to approach a prescribed limit
at Re - + o0 . The solution of this problem is obtained by conformally reflecting
each p'eriodic band of the region of flow that contains a single profile of the cascade
on the portion of the Riemann ~ surface external to the unit circumference so that
each profile is transformed into a unit circumference and the infinite space forward
of the cascade into a point ~c, external to this circumference. After the transfer
to the ~ plane the w function (which is regular for 161 >1 but not for 16,1