SCIENTIFIC ABSTRACT LEVIN, A.M. - LEVIN, A.N.

• Document Type: CREST
• Collection: Scientific Abstracts
• Document Number (FOIA) /ESDN (CREST): CIA-RDP86-00513R000929520002-2
• Release Decision: RIF
• Original Classification: S
• Document Page Count: 100
• Document Creation Date: November 2, 2016
• Document Release Date: August 23, 2000
• Sequence Number: 2
• Publication Date: December 31, 1967
• Content Type: SCIENTIFIC ABSTRACT

LEVIN) AA, kand,takhn.nauki SMIPXOV, V.A., kand.takhn.aluk
Hydraulic design of integrated low-pressure grid systems.
Stroi. truboprovod. 6 no.8:15-18 Ag 161. (MIRA 14:8)
1. Institut Giproniigaz, Saratov. I
(Gas distribution)

NECHAYEV., Mikhail Aleksandravicb. Prinimal uchastiye MITROFANOV, I.A.,
in2b.,- ZURAREV, S.A... retsenzent- LEVIN retoenzent;
SIGAL,j IoY&.# retsenzengj 1KOLYADA,-T'.., retsenzent; STOLPM,
Ye.B.,, nauchM7 red.; FE30TOVA., M.I.,. ved. red.; SAFRONOVA, I.M.,
tekbn. red.
[Safety memwes in the transportatioup distribution, and use
of pa ftell TekbnAka bezopeanosti pri transportirovke, ras-
predelenli i ispoltzovanii gazovogo toplivs. Izd.3.,, perer,
i dop. Leningrad,. Gostoptekhizdat, 1962. 299 p iWRA .15:4)
(Gas as fuel-Safety measures)

L40INOVX V.S.p kand. tekhn. nauki otv~ red*; NIKITENKO, P.A.p inth.,
Me otv, red.; IEVIN, I.M kand. tekhn. nauk,, rcd.;
~iu
NMTIN, N.Lp-inzh.# red.; WIMIOV, V.A... kand. tekhn. naukp
red.1 YAKOVIZV, G.A., inzh.p red.
(Construction and devoloyment of the production of household
gas appliances] Konstruirovanie i razvitie proizvodstva byto-
voi gazovoi apparatury, Saratov., Saratavskii in-t
"GIPMIIIGkZ," 1960. 177 p. (KMA 15M
1. Nauabno-tekbnicheakoye soveshchaniye po voprosu "Puti kon-
struirovan1ya i razvitiya proizvodstva bytovoy gazovoy appa-
ratury." Saratov,, 1958. 2, Saratovekiy josIdArOVenivy
nauchno-looledovatellakiy i proyaktnyy institut po ispolIzova-
niyu gaza v narodnom khozyaystva (for Nikitin).
(Gas appliances)

LEVINO A.M.; SMIRNOV, V.A.; CHERKASOVA$ A.Ya.; KUVSHINOVAj V.I.
Using electronic computers for calculating rvIticircular urban Fas
systems* Gat. prom. 6 no.11:33-Y~ 161. (MIRA 15$l)
(O&9 distribution) (Electronic calculating machines)

LEVIN, A. 0; OKSYUTA, a.k.1 KHARINA, M.A.
Experience in the use of gas burner infrared dryers for drying
paint coatings. Lakakr".mat.i ikh prim. no.6:71-72 162.
(KM 16tl)
(Infrared drying apparatus) (Protective coati4m-Drying)

INVIN, A.M.; OKSYUTA, G.M.
%-.
Radiation intensity of infrared radiation-type gas burners, Gas.pm 2.
no.5M-31 163. (MIRA 16t6)
(Gas burners) (Heat--Radiation and absorption)

LEVIN A.
. ---l --~j; BRMHANOV, O.N. I
I
Tooting infrared gas burners. Gaa.prom. 6 no.7sl8-19 161.
(MIRA 17%2)

LEVINO "; BHrUKWOV, OeNe
~ ~ -1
Flame stabilitj in relation to bickfire in gas burners, Gazo
pramo 7 noo9221-24 '62. (MIRL 17:8)

, ~
i : ~.-- . 1 1) .
'I- -~~ st", "
ard ttl,,~, nt~~%*,), I ' , ~ .- 1.
~ I . . -
irifrEirel raiiihLien can blirnerz; w_t% .'.,tp I r,,t;3. ::rtz. "I's
n,-.L:l(_19 t, -, r.,.. I- 2'

LE71N, A.M. kand. t9khn. rinuY-, ERUKHA11OV, O.N., mladshiy nnwihayy gotrudnik;
HA VAP T.A. w~ad3hly nauohnyy sotrudnik; OKS"!ITAI G,M~,
mladshiy nauchW Botrudn:~k, KHAYKINA, M.A., ulaAshl.y nau~:hnyy
sotrudnik
Temperature regimes and upectral characteristics of Infrared
gas burners. Tspo!'. gate v nar. khoz. no.2:53-70 163.
(MIRA 18;9)
1, Laboratoriya bytovykh gazovykh priborov Saratovskogo
gosudarotvannogo nauchno-tasledovatellakogo i proyektnogo
inst-Ituta po -1spollzovan!yu gaza v narodnox khozyaystve.

~Wl ~FWP a )/EWT(m)/T V4i/jv/,,,E/WFj
ACC NR, AR6010522 SOURCE CODE: UR/0196/65/000/010/TO05/TO05
AUTHOR: &~11M. A. .1 Bryukhanov, 0. N.
ly
TITLEt Problems of combustion -stabilItyll
SOURCEt Ref. zh. Elektrotekhnika I energetika, Abs. 10T36
REF SOURCE: Sb. IspolIz. gaza v nar. kh-ve. Vyp. 3. Saratov, 1965, 116-169
TOPIC TAGS: combustion chamber wall temperature, flame propagation, gas flow, fluid flow,
now velocity, combustion mixture
ABSTRACT: Experiments have been performed to determine the value of the critical velocity
gradient of the now of a ps-water mixture and to study the influence of the wall temperature
of the flame channel on the conditions of the origin of &Vn~~umf~j) into brass tubes 6, 8,
and 12 mm In diam. Investigations were performed on the limits of FJ through apertures of
cerAmic plate4ith the aim of establishing the mechanisms of the origin of FJ In flame chan- -
nels of small diameter. Determinations were made of the most efficient dimensions of aper-
tures In M radiation burners. A method to presented for determining the possibility of the
appearance of FJ during the heating-up of the flame channel walls. The Influenoe of the con-
figuration of the flame channels on the FJ was investigated. [translation of abstract 156 Illus
UDC: 662.6

4000~-66
SOURCE CODES UR/0 196/ 655V00-0101-11- VT
~cc NR, AR6014540 F _0 ff _1V/
4
AUTHORS JAvin,, A. X.1 Salikhodthayelt S.
Tl=t Invebtiption of IR burners with metal radiators
SOURCES Ref, she Elektrotekhnika i energetika, Abs. 11TTO
REF SOURCES Sbe IW10s. 9&s& v naro kh-ves VYp* 3. Saratov, 1965, 208-222
TOPIC TAOSs IR research, Z=-. A 0_1 &4AA-Aburner
ABSTRACT: Mcparimental models of IR burners with metal-eacreen radiators ha b
constructed and testedl the7 aW be used aB prototypes for industrial bt 0 a a
experimental burners proved to be stable to the wind pressure and have a highs.
specific thermal load and surface twiperature than the burners with ceramic
radiators# Fourteen figures. Bibliograpby of 3 titles. [In-t Giproniigazp g. Saratov]
V. Spepher [Translation of abstraot3
SUB CcEst 13" 40
1 llb
Mar 1947
Medicine Dermatolo'gy
i *Vrus-DIssa"s in'DVrMftt0l087 (a Review),- A. Me
TAYIn" 9 pp
*70stnlk VenerologIl i Dermtologil" No 3
Zltalled discussion to the general effect that many
#11011mena treated as typical), specific Symptams of
-virus Provenience Of certain akin diseases by certain
4111thors are actually only indirect Indications, and
tbAt awe research Is needed.
UDGt 662.951.2.001.5
loTee

xz
Vow,
'W~Oy. V.A.@ profegoor; WIN, A.M. dotlent.
7ralillng ClInical $pie I- - ,- - I
v8ner6ftl d1seageg olailets 'u ths dspartments
MY-Je '53. In Wedleal lngtltutes. Of dermatOI0,97 and
Yea" deria, nO,3:Z4-,)a
(Redlo (RLRL 6:7)
'no-Stut, and tO&chlng)

COUNTRY I USSR v
roir
CATEGOPY and Tr)x1co1o,,;y, -,'homo thorapvu tic!, j.
AntlbioticS
3MIT 1959, Vo.
P. i Khrliol. Is
Arl 11OR I jqjLn-,-&L V
_L,,; Prorvich, L. V.; la731'el'(!,
MOT. t 1st Voscow 111odical, Institute
TITLE i On the Treatment of Syphilis with Frx-rionnvnc
A~?T% P11P. t Tra 1-go I'losko mod. in-ta, 119-58, 4, %3-11,7
, ~ R.; T T,,'i C Ti ',,'o ibstract
CARD - 1/1

IXTIR, A.M., dots.0 KSAUPOPULO. ?.I., assistent, PRCRYICH, LoYes ansistent
PAOO'*OoonIPra sine In certain pruritic derwitosese Testoderme I vene 32
no-5t63-64 &0 '58 (MIRA 11M)
le Is kafedry koshn1kh I venerichook1kh boloxney (save - prof;
V.A, Ral&manov) I Moskovskogo ordena Len1na moditsinskogo
Institute im, I*K. Sechanovao'
(PMMITIS. ther.
10-( dimethylpmine -2-mothylothyl) phenothiazine
(RUS33
(PMIOTHAZM, related cpda.
10-(2-dinath.vlamine-2-mothylothyl)phonothiA%ine in
pruritis Otue))

ISVIN A K. doteent; ISAMPULO, P,I., assistant; PRORVICH, L.V., assistant
Results of the use of vitamin B12 in certain skin diseases. Vast.
darn, I Tons 33 no.2:54-57 Mr-AP '59. ~ (XIBA 12:7)
1. Is knfedry koshzWkh I venericheskikh bolesnay (sav. - chlon-korre-
snondent AMR SSSR -prof, V. A. I'lakhmanov) I Moskovskogo, ordens, Unina
meditainakogo instituta.
(SKIN DISUSXS, ther.
vitamin 3312 (Rue))
(VITAMIN B12, ther. use,
skin dis. (Rae ))

RM"OT, V.A.1 Lln&_AtMtl RGUNEMj G.7s; KCMISM,, V.19;
MW TA t. V.
f
ZmddUte reindto of the treatment of "phille with bloiniz-3a
T"todem.i ven. 34 nos9137-40 160,, (MIRA 13 9n)
Is Is kafeft kosbr7kh i venericheskikh bolesney I Mookovokogo
or itoiwkogo inetituta inevi I*M* Siaohenova
(za~"7=lwrorre*l3MdSnt AMN SM prof# V*A* Rskbmanov).

Lmmy At M*
Professor V, A. Rakbmanor corresponding member of the Acadaq
of Hadiasil Sciences of UOA.s.R*, on his 60th birthday. Vast,
dorm. i van. no.603-94 161. (Mrft 1514)
(RAMMOV, MTOR ALMLSANDROVICHO 1901')

1.14VPIS A.M.
.I A - . ~ ~.
*Physician's calendar*. Gig. i san. 28 no.It 117-1.18 .4163.
(MI-ItA 16:7)
1. Glavnyy vrach Respublikanskoy sanitarno-epidemiologitheekoy
stantoli Komi ASSR,
(MMICIW,HAMBOOKS, HWAW,, ETC.)

LEVIV'o A.M.
Oitbreak of trichinelliasis In the Komi A.S.S.R. ir, 1964.
Med. paraz. i paraz. bol. 34 no. 5t6U-612 S-0 165
(I-ITPA 19tl)
1. RespublikanakELya san i tarn o-epidemi olog icheskaya stazitsiya,
gorod S3rktyvkars Komi ASSR. Sulnitted May 29, 1965.

UVIN, A.M.; BRYUKHAJ:OV, OZ..
Investigating infrared-radiation gas burners operat'--,g ;,-i
coke-oven gas. Gaz. prom. 8 no.12:20-212 263 (11,12A 18:2)

LZVINJ A.M.; 8AI,TKHOll,','11AYI,V, 3,
Study of the extent of the passage of a flame a netal
grating. Izv. AN UzSSR. Ser. tekh. nauk 8 no.6:(R-65 '64.
(1,111RA 18:3)
1e Inatitut IspolIzovanlya topliva Gosneftekhlmkomiteta pri
Gosplane SSSR.

LEVIN, A.S. (Alma-Ata)
Practical problems. Xat. v shkole no.ls89-91 Ja-F 056.
(Xathematice-Probless, exercises, ate.) (MM 9:4)

I
SMIRMOVA, V.V. (Alma-Ata)
N60888itY Of solving standard probleas. Mat. v shkole no.ls58
Ja-F 163. OGRA 16W
(Mathematice-Problems, exercises, ete.)

LEVIN, A.N.
Cal;;iating the abscrpt4-cr, roeffi--iprnta of monn~!hrrtmrttli
In a nonunifom medium with an arbitrary 1w of charFe im
velocity vith depth. I-Al. geofiz. no,,4001-34 t6
vat-as
.18zi)

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1XVIN A&H, dotsent, kandidat takhnichaskikh nouir; FABRIKANT.T.L..
sotrudulk
Polymerization rate of vinyl chloride in emulsions.' Xhim.prom.
no.2:48-50 F147. (MIRA 8:12)
1. minx A
(3thylene) (Polymers and polymerization)

o *-*-*-or
?f fit I a v 4 of 0 u 'a
0
a CL a afs-A a -1-4. .1 a I A I v 2
4,
A
c
C-dn- '09
lo. **40"IthAway. '00
Jody. MO. I(1. SOS.
M, - I owt,, 4
fiou"Us but. in# xhd M-asilling
hytk twvr4"s is brkdv if wa. M. It-.b 600
00
oleo
see
lj i go*
Lff#f&fW# CUSIVICAMN
a" God 4144slool -618611 *A on Ole
At go a a .1 4 a 14 a Ora i i G" 644
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IRYIN,A.Me. kandidat t ekhnichookikh nauk; SID=CHIMV,B,D., inshener
Continuous production of phenol-formaldehyde molding powders. Xhiso
promeno 10:289-290 0#47. (KW 8:12)
(Plastics industry)

It/calilp jW Nor 207.:
Pz. r::" 312011"10 ~ bili"li"
Out p3mtlof ZrAWtx7 PrO B. 1. VoTaklys A. 1.
ISTIU). WA,*f NW, Of MWM&1-VIO$tp VIF pp
Son
Gmeral 840owki at US gmth of the p2mti" in-
dustryVesp"I'ally AIWO 1931. A large part of the
IMU-stry wdA awed eastwird dwing the var. A very
broad gmulal 2vtoranee -Is Made to am* of the obaml-
641 aspects of the Indust
z7.

Equipment of plastics factories, moRuDYANn?. UVOW.' HASTICASKIKH
VASS. Moscow,, Leningrad. State Sc. Tech. MIA. of Chetdcal Lit.
1950. pp# 267,

Acceferatio of th of
rrudy of,
Whole No. 0), 47-32.--Cjjg:CJjCl J4 IMAY-
rapidly at 30, 40, 60, sod 60* iQ ft'Alcd Ire
Wessell wa ["I sented-gLii ampuls It'l plesen at hA; I,-n-
INJUIM ItC4 no pulymerfu6nn takes place P. D.

LITIN, A.*.; Ruravegly, B.N.
Continuous polymerlsation of vinyl derivatives. Tessoyase Dist
Obahebastvo in. D.I. Mandeleyeva, Tysokosolskal. Soadinenlya No.11,
9-17 '51. (KLRL 4:12)
(CA 47 no.13:6694 153)

V n 7 Colmidal and Iffifti-MAscour
on A. N. 1XVIn and
ol
#Mwv (Trudy &WAkAdmiso p0 gummimll 19jol
307-314).--0n lWomisol. The effect of various adan.
-Ssftt4 (glov, ige detergent, gelatin, p-loluldins skilplonie
Mid, 2 t 7-naphtc,".fi, a oulplwfdo acid, oulphite liqw, solp.
root, &c.) m e4tholle polasization In baths oontS. Cu.40,41-1,0
at varkma o.d. and
1361 H,80, ISO telop. was investi.

and FIK. I. Sh.
FFASE x TREASURE ISIXO BIBILTOGRiAtJ~IAL 1702T AID662 - X
BOOK Call No.: AF653017
Authors: PIK, I. Sit., LEVIN, A. 11.
FU31 Title: FUNDANERALS OF THL MANUFACTURE OF A111TICLFZ FROM PLASTIC MATMIALS
Translitetated Title: Osnovy proizvodstva izdeliy iz plastraass
TUBLISHING DATA
Originating Agency: None
Publishing House: Vaesoyuznoye koo erativnoye izdatel'stvo (All-Union Cooperative
Publishing House~
Date: 1954 No. pp.: 320 No. of copies: 6,000
Editorial Staff
Editort Rutovskiy, B. N.j Frofdasor
FURFOSjj AND EVALUATION: This book is intended for foremen and technicians working
in industrial cooperatives. It can be ua..!d also by en,;ineers and te&nrlio-,ists
in plastics industry 1-lantas ani by students wlio wish to enter thin fit1d. The
book in Interesting because It contains infonnation on Flastics itateri4s used
ift the USSR and practical engineering data on Soviet manufacturing methods
and equipment# However) as a basic works it does not co=Fare favorably with
American or English publications (e.g., SPI Handbooks Modern Plastics,, by If.
Barronp Plastics Kolding, by J. Dalmontes etc.) which -are noro exte ded and
have a more scientific approach.
NOTE: SM card for PIK, 1. 8h. for translation.

11", C, 5 t 1 f-'I t f~ f r er r T. ,,, ol r.
cordo~nsu-c! mid
USSR. Plozrov, Inst of' Chv,-,Ic,)l
(Dlr,cprtntion 'Lvr thr De rs~(, of Lrr-,.nr -,(,ch,dcpl Scllcrcrs).
S o u r c Vnizimayn I(A-is' .io 2"~. 1~

IWIN, A.N.; MLN, S.M.
Pressure casting of thermoplastics In the USA and Great Britain#
Rhim.prom.no.4:246-2.53 Js 156. 1 (Kw 9:10)
(Plasties)

dFL.
I
% my, IMMENWASM
.":i p. g g I , I" SIMM
.'~i,a
.- WIN 5 -
~, .-
I
. m AM am m
H -

'~~datt dd tbo Itymo polyn"et'", Process for i
x9dioctift of poi an's w" "Osecud"d PC d"
v a Ifachliu r .
Mt..*.XG. sp. rem. 37. MI-20J.-Coaddsous
for sty1moPwater tmuWAw WtiAted
by th4 0xidatka--sdjctkm--Ty7Mfw wen developtd, wbkh
"Mww In tbA =ttatim at a high MOCRY, aad per-
Mitted the am of a Coutiaueas stymne g"Aywauatiou pctK-
tal. Two grow#* of formulas were developed; I byasingiso-
udas agents-
Ibeateoe hydruWoxkk w'tb vatkxw
rfM'.* N&.SO,. N.49A); wW (B) with DIA - KAA.
The plOcircd formula wuWaed stymm 104, HpO 209, K
Curves,
VM" srVoduced of the simis. vn. ol the polywan obtAimA
4uring different twAyrnerkwtion timso the kluetic curves at
various tempt., the JAYInerk4dou rafts at difftreat temps,,
the txAywerisAllon rates at diffeltnt I COOCCIg., " the rates
of A&IO. of I to (tie systral. W. Pd.

/,, /~, - ----- - -
1XVIN, A.N., doktor tokhn.nauke
"dontinuous processes in the awnufacture of plastics. XhIm.nauka, i
prom. 2 no-5t630-638 157. (MIU 10: 12)
(Plastics)

67094
-,'A-59-13-542
SOV/W 520 (USSR)
11s, .959, Nr 13P
..hin0strolon
the
On
P300
F&A Cestim
frost logical tors
dMo Pressurs
Several I' in the
Ittects 0 tu% %&chinos
ai
ta jf"1~
in
41
IMODICAL,
wher MOVACT
quan
of pr
relat.
the Ic
Me re,
where X Card 112
Card ~IP,
tone
of- f CBS
Savest-APt"A press-"old 0 - 109
the 97
?"Oure in ~ '(9 P Vol 13P pp On the
of PO ON ,,hinOstr 1951, -mold in dependence
so Id 405UP was
most . inAIL the test Prolsauret and me wide and
Tr . in 0 casting PY longg 20 00 I.,L placess
f pressu plate 155 om ~d In 6
distr'buticum&0terislo 9 601ti a .. ,,Bur4 The fills
ture of test epee a pressure distance$ a
tempsVe As a used. in a 25-01 recorded 0n ter
I tensOM6
was f the specimen the moldWse ,nnel &Sting
4 -2.620 th"OlIt'amth 0 wells of a 6-C1
2. ted Over the tio on the h thrOuSh a sechanicalicn pressure
100& las scillograP ut on arietion rvals
-P the P stio 0 carried 0 with 8, v 0C in Into
Prosigurs W. e0tromap . wore . cycles 210 the inlet
%P0_2 el investigation ; pe f 170 -
fit a 50 1 ture 0 ints from
lifier. The &city of 30- tempera ing PO
aw f a cap C;? at a ,asur
(,bins 0 ud he pressure
or fros Wo to 1, 300 f t;
of 100C. The distance 0
--ctured object.
M.L.P.

.M., T,-~ OR S Arbitman, S. V., Levin, A. I..
TITLE: Continuous Water Emulsion Fc~Vmerization of Styrene
(Nepreryvnvya vodnoemullsionnaya polimerizatsiya stirola)
PERIODICAL: Xhimicheskiya Promyshlennost', 1958; 11r 2, pp. 27-32 (US3R)
ABSTRACT: A method ij described which is initiated by an oxidation
reduction jystem and which takes into account the previous worka
in the fieLd of continuous processes. The plant consists of an
"ideal arrangement" of the apparatus according to the grapho-
analytical computation method for the ideal order of aggregates
for reactJons in homogenous liquid phase. A schematic repre-
sentation of the laboratory plant is given and from it can be
seen that the aqueous solution of the emulsifier together with
the reduc.ng agent, and styrene together with the oxidizing
agent die3olved in it are directed Into the emulsifier throuch
siphons# In the emulsifier being a propeller doing 1000 revs/=in.
From the emulsifier the line leads through a coil in the water
thermostat to the three polymerization vessels which are also
placed ir thermostats. Each polymerizer has a thermometer and
Card 1/3 a stirre;-. From the given operation technique can be soen that

Continuous Water-Emulsion Polymerization of Styrene 64-58-2-5/16
polymerization begins In the last polymerizer, that thtin the
two before this are supplied after each other and that only
then continuous polymerization begins by the full coi.,nection
of the plant. From a table can be seen that the authors worked
according to three methods. The operational parameters of the
aggregates are computed grapho-analytically and the given
diagrams (velocity curves) of the function of time- and monomer
concentration vs. polymerization velocity are obtained by
graphical differentiation. From the obtained velocity curves the
steady concentrations of each individual polymerizer are
computed according to a formula; the practically obtained mean
values coincide sufficiently with those calculated. From th'A.3
is concluded that the grapho-analytical method of co.-;putation
can be used for this operation process. The determination of the
monomer content in styrene was carried out by bromination of
the double bond. It was found that the capacity of the plant
a greed with the calculations, and that it was very high in the
various methods. The schematic representation of a test plant
is also given. Among other it can be seen from it that the
Card 2/3 latex of the last polymerizer is coagulated in a coaGulator

Continuoun dater-&-ulE Ion Vol,nuri-zation or. Ztyrene 64-58-2-5/16
wi th a itator solution of' thu cnai,ulun and Is sc2asated from
the not oi,,t.,r, or acnovi:ini~ to anothar variant is dirf-atly
brouj;h1 Into dryliii, Aomlzer. '171hc latex suspension coululated
a nd t r( atod -with !;tuiji can b& vaighod in two different rti;,r,.
The wa!hed polyner is dried in an air drying a -.paratus.
Thore t re 4 fiEuras, 5 tablea, fLnd 5 rc-feruncos, 4 of which
are 31..vic
AVAIL,#,BLE: Librarr of Con(;ronn
1. Stp-ene--Polymerization 2. Industrial plants--Operation
3. Ind,,istrlal equipment--Operation 4. Mathematics
Card 3/3

ARBITMv SXI LVIt A*"*
I WWWA*040--~- -
ContinuouS aquGous em1glou -polMrizatiOn Of 'Ity"ne- Jods' pros'
no.2tg"6 Mr 158. (Styrelm) (PolMrization) (XIU 110)

LVrN, A-][-# prof o
Ihim.mak
Scientific and technical conference On POlystyrens- (Knu 11:11)
L prom, 3 uod,5:673-674 158.
. (Styrene)

5(5); 15(8) PME I BOOK EXPLOITATI(XI 3011/2814
-Levin., Abram Haumovich, Doctor of Technical Sciences, Professor
Plasthway v mashinostroyenii (Plastics in Mechanical Engineering) Moscow,
Izd-vo "Znwdyeff., 1959- 44 P- (Series: Veesqyuznqye obahchestvo po
rasprostraneniyu po3ltiche6kikh I nauchnykh anan1y. Seriya.IV, 1959,
no. 21) 48,500 copies printed.
Ed.: I.B. Faymboym; Tech. Ed.: L. Ye. Atroshchenko.
PURPOSE: This booklet is for the general reader interested In the applications
of plastics,
COVERAGE: The asithor gives a popular review of various types of plastics and
their use in machine building. The text includes a brief description of the
manufacture of plastics and of their properties as construction material to be
used in machine building. The role of plastics production in the E;even year
Plan 'is stressed through the booklet. No personalities are mentioned. There
are 22 Soviet references.
Card 1/3

Plastics-in Mechanical Engineering
TOLE OF CONTEM,:
The Age of Plastics
Plastics in Automobile Construction
SOV/2814
3
a
Plastics in Shi~building 12
'Plastics in the Aviation Industry 16
Use of P19atics in the Manufacture of Electronic Computing Machines 22
Pladtics In Machine Tool Construction 24
Plastics as Antifriction Materials 25
Plastics In Chemical Machine Building 28
Card 2/3 '

Plastics in Mechanical Engineering
Plastics in Heavy and Textile Machine Building
Plastics in Casting
Bibliography
AVAILABLE: Library of Congress
Card 3/3
SOV/2814
35
38
44
TH/Omp
1-24-60

50); 25(2) PEME I BOOK EXPLOITATION sov/2884
Moscow. Dcm nauchno-tekhnicheekoy propagandy imoltF.E, Dzerzhinskogo
Plastmassy v mashinostroyenI4 (Plastics in Machine Building) Moscow, Mashgiz,
1959. 236 p. Errata s3lp inserted. 8,000 copies printed.
Sponsoring Agency:' Gbshchestvo po rasprostraneniyu politicheskikh I nauchnykh
znaaiy RSFSR.
Ed. (Title page): V.K. Z&Vgorodniy; Ed. (Inside book): B.M. Notkin, Digineer;
Ed. of Publishing House: G*M. Konovalov; Tech. Ed.: A. F. Uvarova;
Managing Ed* for Literature on Machine Building and Instruxent Making
(Mashgiz): N.V. Pokrovskiy, ExV~ineer.
PURPOSE.' This c6l1ection of articles is intended'for engineers and technicians
In the machine-building industry.
COVERAGE: This collection reviews the progress made by the Soviet Union in the
fij,*ld of manufacturing nw plastic materials and fabricating different plastic -
Card 1/4

Plastics In Machine Building
SOV/2684
material articles for use in the. machine-building Industry. FbysIc0=Ch'2"1c&l
and dielectric properties of phenolite, decorrosite, fluoroplastics, epoxy resins,
polyamides,, laminated plastics, and fiberglass plastics are analyzed and their
use in machine buildAng described. Characteristics and composition of adhesives
and bonding agents are given and the technology of the pressing process described.
Methods of coating vith plastics as a protection against corrosion are explained,
and metallization of plastics achieved by vacuum evaporation is revieved,,as vell as
equijpment used for manufacturing and fabricatln~q plastics and artl?jles made of
plastics. Mechanization of certain operations and automatic control of various
processes are discussed. No personalities are mentioned. References accampany
individual articles.
TABLE OF CONTENTS:
Garbar, M.I.,.and.A.K. Levin. New Plastic Materials in Machine Building 3
------------
Rabitap S.M. Ifighly Resistant gaterials of the "K Type 14
Vlasova.. X.Nw and M*K. gatakevicho Polyamide Resins 19
Gorbunov, V.N. Laminated Plastics With Fiberglass Base and Paper
Base Usedan CostructiC6 Xatexjal 29
Card 2/4

Plestics.in Machine Building
sov/M84
Pevzner, L.V. Phenolits and DecorroGite -- Water and Acid Resistant
Plastics for Zlectrical Insulation
Mimmaev" I.I. Bonding of Metals
Pakbcmov,,IV.I. organosilicon Polymers Used in Machine Building
Gurexiy, M.G. Technique of Pressing Themoreactive Plastic Material
Antoshiu, U.N. Applying Plastic Coating by Spraying Burning Gas
Gracheva, B,S, Now Method of Manufacturing Holds and Patterns Made
of EpW Resins
Strelltsov, K.N. Processing Thermoplastic Sheets by Pneumatic and
Va6um Methods
Lapshing V.V.p and V.N. Grinblat. Pressure Cast of Polyamides
C ard 3/4
Plastics in Machine Building SOV/2B84
Perepelkin, VOPO., and IP*I. Skundina. Processing pluoroplastic , 4
Shapenkoy
Articles mpade*P* Prol"ems Pf Designing Press Moids for Fabricating
Of Plastic Material
14Lganp D*F*
Plastics Ach'iyu*N*'K"Msk:'Yt and M-Ya- Nemllkber. Metallization of
eved * High Vacum Evaporation Method
Levin, AoNO Equipment for Fabricating Articles Ma4e of Plastics
ZavgorOdzkiY, V*K. Holding Machines for .FOM1ng Articles From
Holding Povdar'
Zavgorodniy,. V.K. Hydraulic presses for Processing plastic Material
and Autmated Process Control I
Shapiro, GJ* Mechanization and Automation In Mocha:aic&l essi
of Plast1c Material Articles Proc ng
AVAIrABr2: LIbrar7 of Congress
42
55
65
71
83
91
99
109
117
128
136
144
165
187
Card 4/4 TM/M
1-19-60

PHASE I BOOK EXPLOITATION SOV/3814
Petrov, Origoriy Semenovich, and A.N. Levin
Tormoreaktivny3re smoly I plastichaskiye massy (Thermosetting Resins
and Plastics) Moscow, Oonkhimizdat, 1959. 309 P. Errata slip
inserted. 4,500 copies printed.
Ed. (Title page): M.I. Oarbar; Ed,: B.M. Kovarskaya; Tech. Ed.:
Ye.G. Shpak,
PURPOSE: This book is intended for workers in the plastics Industry,,
and for those interested in the processing and application of
synthetic resins. It may also prove useful to students pursuing
rel.ated studies at schools of higher education and tekhnikums.
COVERAGE: In this book the authors have collected and compiled the
results of recent studies in the field of thermosetting plastics.
The production processes and equipment for thermosetting resins
(phenolaldeh d oarbamide Cur6a-formaldehyde] 0 polyester and
epoxy resinal.ea's well as for molding powders, adhesives, and
carwTrg---

Thermosetting Resins (Cont.)
SOV/3814
laminated plastics based on these resins are described. The
characteristics of the initial raw materials and the finished
product are given. The production of wood plastics and organo-
silicon polymers is not Included. The following are mentioned for
their contributions In the field of thermosetting resins and
plasticst G.S. Petrov, I.P. Losev, S.N. Ushakov, and V.V. Korshak.
The book is V"ed on data from Soviet factories and scientific
research organizations, the lectures of G.S. Petrov at the Moskov-
skiy khimikotekhnologicheakiy institut imeni. Mendeleyeva (The
Moscow Institute of Chemical Technolgy imeni Mendeleyev), and
on the work of A.N. Levin at the MoBkovBkiy institut khimicheakogo
mashinostroyeniya (Moscow institute of Machine Manufacturing for
the Chemical Industry). The authors thank B.M.' Kovarskaya,
B.L. Pruzhiner, the personnel of the Nauohno-isal7edovatellakly
institut polimerizatsionnykh plastmase (Scientifib Research In-
stitute of Polymer Plastics), and G.N. Zillberman. There are
355 referencest 233 Soviet, 97 English,, 21 Oerman,, and 4 French.
TABLE OF CONTENTS:
Preface

AFARASOUT, A.M., kand.tekbn.nauk; BABOT, N.I,, kand.takhn.uslak; BXLO-
TITSKIT. A.A.. inzh.; TNSILOTS&IT, T.S.. dolctor takhn.nauk, prof.;
GGRXLIK, B.I., kand.tokhn nauk; DOWIMMOT, I.M., insb.; ZAK. D.L.,
inih.g ITONIN. T.I., insh: [deceased): KLINOT, I.Ye., doktor takhn.
nankil prof,- LEVIN A N,, doktor tekhn.nauk, prof.; LITIN. $*Not
kwdetekhn*~C57; WDr. T.A., kand.tekhn.nauk; LWNT11W. X.L.,
doktor takhn.nauk, prof.; LOXHIVA, P.I,, kand.takhn.nauk-, XATTIMTA,
L.T., iuzh.; MIKKAU-0T, A.N., doktor takhn.neuk, prof.; HUMLIX, Khol*g
kand.takhn.nauk; PERLIN, S.M., Insh.; SALAZKIN, K.A., kand.tekhn.nauk;
SILITMROVICK, %L, kand.tekhn.nauk; SOKCLOYSKAYA, S.I., kand.
takhn.nouk; 11. A.A.. inzh.; INUMMUNSKIY. P.N., doktor takhn.
nauk, prof*; SMrMWN, I.Yu., kand.takhn.nauk; YAMMSKAYA. T.L.
kand.takhn.nauk; POGODI1~-ALXKSZ7ZT, G.I., doktor takhn.nauk, prof.,
red.1 FM OVA, T.I., Insh., red.isd-va; SCKOWTA, T.F., takhn.red.
Effandbook on materials used In the manufacture of machinery] Spra-
vochulk po mashinastroltellnym materialam; Y chatyrakh tomakh. Pod
red.O.I.Pogodina-Alskaseva. Moskva, Goo.nauchno-takhn.isd-vo me-
shinostroltolit-ry. Tol.4. ENonmetallic materials] Nametalli-
obaskis saterialy. PAd.tome A.N.Lovin. 1960, 723 p.
(MIRA 13M
(Xsohinery industry) (Ronmatall1c materials)

87486
AUTHORS: Zlatina, S. A., Levin._k,_X,_
TITLE: New Copolymers of Vinyl Chloride
S/191/60/000/001/001/015
Bo16/BO54
PERIODICALs Plasticheskiye massy, 1960, No. 1, PP- 3-8
TEXTt The authors report on the development of methods of copolymerizing
monomers of much differing specific activities. They used vinyl chloride
copolymerized with a) styrene, b) vinylidene chloride, and c) acrylic acid
nitrile. The purpose of the study was: 1) the production of "genuine" co-
polymers, not only polymer mixtures4 2) the copolymers produced should be
soluble in ordinary cheap solvents. The copolymer yield by weight was de-
termined after precipitating the resin by XaCl from the latex. In the ex-
periments with vinyl chloride and otyrene, it was found that styrene in-
hibits the copolymerization at a ratio to vinyl chloride of 0.0146 : 0.4.
Separate polymerization takes place when the styrene amount is Increased.
From the experimental results (Table 1), the authors conclude that the
polymer amount is independent of the used quantity of initiator (systems:
Card 1/3

New Copolymers of Vinyl Chloride s/iqi/6o/ooq/oo1/oo1/015
B016/B054
potassium persulfate - bisulfate, or cumene hydroperoxide - bisulfite).
The former initiator system warranted a conversion of 90 - 95% without in-
duction period, the latter an 82% conversion with short induction period.
Figs. I and 2 show the dependence of conversion on the time of copolymeri-
zation. The experiments with vinyl chloride, vinylidene chloride, and sty-
yene showed that the latter is the most active one. The authors recommend
to supply the reaction vessel first with the two former monomers together.
Styrene was added by a measuring hopper during the whole process, or by
portions. Pigs. 2 and 3 show results at different temperatures. From
Table 3, the authors concludes 1) that an increase in the vinylidene
chloride amount reduces the viscosity of the copolymer; 2) that a decrease
in the reaction temperature increases the viscosity,'and prolongs the dura-
tion of the proceeal 3) that the optimum weight conditions for the forma-
tion of a low-viecous and (up to 15% concentration) well soluble copolymer
are the followings vinyl chloride s vinyliden8 chloride t styrene -
85 1 10 1 5 at a reaction temperature of 60 C. Experiments with acrylic
cid nitrile (10%) instead of styrene resulted in a lower solubility of
the copolymer. Added in one portion, the acrylic acid nitrile slows down,
Card 2/3

LVINO AIN.
----------- Cos of a extruder in
Investigating the "j^1 for ride Pl"ticAteme Plast-
the processing of I)OUT"WIchlo (KIM 13:6)
massy no.2:36-43 l6o. -
(plastics) ent and supplies)
(Nxtrusion process-lquiPin

83412
T.Ul,oA
9/191J60/000/006/004/015
B004/BO54
AUTHORS: Goncharovt Go So &gXjnp A. ~~ Kikhaylov, G. Do,
1epk1_nPYue A*9 Shushpanov, P. I.
TITLE: Influence of Ultratonics Fon the Polynerizatio% of Styren
in Aqueous Emulsion
PERIODICAL: Plasticheskiya sassy, 1960, No. 6# pp. 8 - 10
TEXT: The'4uthore report on experiments of accelerating the polymeriza-
tion by Imeaus of ultrasonics of varying frequency. The polymerization%%
degree was measured dilatometrically during the experiments by an appara-
tus which is schematically shown in fig. 1. Ultrasonic irradiation was
caryted out at 28 ko/sec (intensity 3 w/cs 2), 8251ko/seo (2 w/ca 2 ), or X
1600 kc/see (0.3 w1cs 2). The characteristic values of the ultrasonic ap-
par&tus are given in a table. The temperature of the dilatometer was kept
at 60+0.50C. The emulsion formula was: 65 g of styrene, 1.3 g of potas-
sium Roinoleate, 130 al of distilled water. K2S2O, was used an initiator.
Card 1/2

83W
Influence of Ultrasonics on the Polymerization S/191/60/000/006/004/015
of Styrene in Aqueous Zmalsion B004/BO54
No polymerization occurred in ultrasonic irradiation without initiator.
An addition of 1% of X25208 effected a faster polymerization after
30 min of ultrasonic irradiation than without such irradiation (Fig, 2)
The ultrasonic effect became mainly evident in a reduction of the in_
hibition period at the beginning of the process. Prolonged ultrasonic
irradiation changes the course of the process only slightly (Fig. 3).
Varying the X S 08 stition between 0.25 and 1% effected that ultrasonics
always exertel In colerating actiong and that the extent of this action
became relatively larger with smaller additions of initiator (Fig. 4).
Turtherp the authors studied the influence of ultrasonics on the do-
gasification of water. The results (Fig. 5) led to the conclusion that
the ultrasonic effect in partly due to the removal of the inhibiting
oxygen dissolved in water.-Under the influence of ultrasonics, the au-
thors observed a slow decomposition of the K29208 (Fig. 6) which is,
however, simulated by the formation of peroxides. These peroxides may
also contribute to a:n accelerated polymerization. There are 6 figures,
I table, and 5 references: 2 Soviet#' I US, and 2 German.
Card 2/2

AUT9ORSo
0
0
sligIV601000100710041015
8004/ .056
TITLEt
Gonabarov, 0. 5.1 Levin A. N.f Mikhaylov, G. D.y
Ropkin, Yu, A.9 Shiii;~al. 1.
noy
Polymerization by th Action of Ultrasonics on Aqueous
ofil2containi4j Folystyrene
Emulsions
PERIODICALt Plasticheskiye massy, 1960s No. 7, Pp. 15 - 16
TEXTt The authors give ayeport on the polymerization of aqueous,~tyrene
emulsions carried out by means of an ultrasonic generator at 28 k see
(3 w/cM2)g 825 ko/seo (2 w/cm2 ), and 1600 ke/sec (0.3 w/cm3). The poly-
merization kingtios was dilatometrically determined. Control experiments
(Table) showed that 1) ultrasonic Irradiation of styrene emulsions without
polystyrone'and initiators does not lead to polymerization; 2) an emulsion
containing 0*5% of polystyrene dissolved in styrene did not polymerize
without ultrasonic irradiation. As soon as this emulsion wast however,
n a
acoustically irradistedl Rolymerizatio 0 st in (Fig. 1)8
1/2

9 5 Ih 'A.

Polymerization by the Aotion of
F
Ultras onics S/191/60/000/007/004/015
on Aqueous Emulsions of Styrene Containing B004/BO56
Polystyrene X

This confirms the mechano-chemi- t;

8
7
cal character of this'procese.
yield

Addition of potassium .12
persulfate as initiator to the I
styrene-polystyrene system
decreased the polymerization
rate (Fig. 2). The iuthors
mention a paper by A. A. Berlin
and B. S. ElItsefon, There are
2 figuresj 1 table, and I Soviet time Cmin3
referenoe. Fig. 1. Effect of ultrasonics upon the
11 tyrene-polystyrene system
0 - 825 ko7sec; 2 - 1600 ko/seol
3 - 28 ko/890)

Card 2/2

KONSTPNTINOV9 V,N.v inzh.j%~~IZVINp A,,N,p prof*9 doktor takhn.nauk
Miltiscrew Masao for processiAg plastic materials. Kh1m. mash,
no. 1: 3-8 A-7 161. (MIRA 14il)
(Ponr presses) (Plastics)

89)42
S/19 61/000/001/002/015
157.1jo4- B101XB205
kUTHORSt Golysheva, Ye. Ya., Fragina, A. R.,_Levln, A- N-
TITLEs Copolymerization of styrene with diallyl fumarate
PERIODICALt Plasticheakiye massy, no. 1, 1961, 7-9
TEXT3 An attempt has been made to obtain a styrene copolymer with a better
resilience and resistivity to heat than exhibited by polystyrene.
Proceeding from papers by Western authors (Ref-7), copolymerization of
styrene with diallyl fumstrate (DAF) has been studied. A) Copolymerization
In emulsion with an addition of 1.5-25% diallyl fumarate to styrene was
performed with sodium hexadecane sulfonate as emulsifier and with the
following initiatorst a) benzoyl peroxidel b) benzoyl peroxide plus FeSO 4;
c) isopropyl benzoyl hydroperoxide plus Na2so 3' The best results were
obtained from the latter initiatort powdery copolymers in a yield of
80-90%. Increasing content of DAP led to slower polymerization than that
of pure styrene. In organic solvents, the copolymers were unsoluble or
only partly soluble. 5-8 and 2.5% of the copolymer separated with 5 and
Card 1/3

893h2
S1 19 V611000100110021015
Copolymerization of styrene... BIOI/B205
10% DAP, respectively. According to an elementary analysis, the copolymers
had the following compositiont
Ratio of initial ratio in the Copolymers with 1.5, 3. and 'i% DAF
monomei I eopollmer could be easily molded at 150 -155 OC and
stZrons DAP stuene DAF 150-180 kg/cm2. Pressing was com-
90 10 76.e 23.2 plicated by a high content of DkF.
e5 15 71.6 28.4 According to Martens, copolymers with
75 25 63.2 36-7 0 1-5-5% DAP withstood a temperature of
64-891C, and with polystyrene, 80 C. Resilience was 4.2-4-5 kg cm CM2
polystyrene, 5-15 kg-cm/r2)j Brinell hardness was 21.5-22.7 ~gYZM2
polystyrensi 16-19 kg/mm.). B) Block copolymerization was carried out in
~
sealed ampoules with 10 6 15, and 20% DAP, 0.1% benzoyl peroxidel the avib-
stance was heated at 600C until a viscous product had formed, after which
it was solidified at 40 C. The entire process took about 200 hr. The
polymerization process was completed by heating at 150-16ooO for 10 hr.
Solid, transparent copolymers could be mechanigally treated. Resistivity
to heatt 88-92001 r*siliencet 15-18 kg-cm/cm I Brinell hardnesst
21.2-22.8 kg/mm2. C) Meltable and soluble copolymers were obtained by
copolymerization in a solvent (varnish copolymerization). The solvent
Card 2/5

89342
S/191/61/000/001/002/015
Copolymerization of styrene... BIOI/B205
was allyl alcohol in a ratio of 3il related to the total number of
monomers. After the end of polymerization, the solvent was boiled down
in vacuo. A 20~4 solution in acetone was prepared from the copolymers,
which had been purified by dissolution and reprecipitation, and was then
applied to metal. After heating, a firmly sticking film of varnish was
obtained, which was unsoluble in acetone and withstood a temperature of
20000 for 200 hr and of 300 C for 3-5 hr. The film was tested by means of
the Dupont apparatus. The laboratory assistants K. V. Valkina and
F. Yo. Shapiro participated in the experiments. There are j 1*.igure,
I table, and 9 references: 4 Soviet-bloc and 6 non-Soviet-bloo.
Card 3/3

8/19 61/000/001/007/015
BlOlYB205
AUTH098s Balashov, M. M., Levin, A. N.
TITLEs Plow of block polystyrene "D", and development of a rheometer
PERIODICALt Plasticheeklys massy, no. 19 1961, 23-30
TKXTt In the introduction to this paper, the theory of flow of non-
Newtonian fluids an applied to the flow of molten polymers is discussed on
the strength of R, 5. Spsnoer!s papers. The methods and apparatuB used so
far for determining rheological properties are said to be cumbersome and
inadequate. In the new rheometer designed by the authors, the molten
polymer is pressed simultaneously through two capillaries of difforent V
lengths. The flow velocity of the material is equal in both capillaries,
and varies continuously in time. The rhoometer is shown in Fig.l.
Socket (1), which is heated by electric heater (2), contains two channels
into which the substance to be tested is introduced. The channels are
closed at the bottom by two tightly linked pistons (25), which contain the
short and the long capillary (3). The material is pressed through the
capillaries by upward motion of the pistons. The pistons are mounted on
Card 1/7
'R 5;AIR

S/191/61/000/001/007/015
Flow of block polystyrene... B101/k05
movable plate (23) which to heated by heater (24 and moved by rod (22).
The material leaves the pistons through outlets 1A). The two channels
are closed on top by stoppers (4) which are mounted on slider (15). The
letter is moved by screw (11) which passes through immobile cross beam
(12). The base of (13) is heated by heater (6). The pressure in the
channels is measured with strain gauges which are made up of elastic
ring (9) bearing several bridge-conneoted wire gauges. The channel
pressure in transferred to the strain gauges by piston (5) and rod (7),
then converted into an electric signal and recorded by an o9cilloscot)
Material leaking through (4) and (5) is discharged through --hannel C
Rings (9) in socket (8) are fastonea to terminals (10). (8) is so-- ty
water flowing through channels which are not shown in the figure.
flow velocity of the material Is proportional to the velocity ef pintons
(25), which is measured with a pickup consisting of armature (14) with
copper winding (15). The armature moves between the poles of a magnet. Tho
pickup has a linear characteristic and must be shielded against external
magnetic fields. Velocity and pressure are recorded simultaneously by an
oscilloscope. The flow curve may be obtained by one single experiment, by
steadily varying the velocity of pistons (25)- When the slider is lifted,
Card 2/7

S/191/61/000/001/007/Ul5
Flow of block polystyrene ... B101/B205
the channels are filled with the material (cylindrical specimens or
granuli) from above and are then compressed by stoppers (4) and screws (ii).
The channels may be filled with previously molten material also through
the feedst and7l. The pistona may be moved by any steady drive. The
figure shown a drive by weight (16), lever (17). toothed *heel (18). and
rack (19). Pressure transfer to rod (22) to effected by cup springs (21),
whose initial tension in adjusted by pin (20). Thermocouples TV T 2# and
T3are used for temperature regulation. The rheological behavior of 'A."
(I'D") polystyrene between 160-2450C and up to 220 atm pressure was tested
with the rhoometer described here. Capillaries 2.6, 2.0. and 1.6 mm in
diameter were used for the purpose. The short capillary wag 10 mm long,
and the long one, 25 mm. Figs.3-5 show various circuit diagrams for the
wire strain gauges. Inspite of considerably spread, measurements have
ghown a sufficiently linear course of the function logAP - f(logAQ)
(q - volume velocity of flow expressed in cm3/sec). The equation
Q/RR3 - [m/(n + )].,n (14) was used for calculation. R is the radius of
w
the capillary; m and n are coefficients; and % is the shear stress. n is
Card 3/7

8/191/61/000/001/007/015
Flow of block polystyrene ... BIOI/B205
Independent of temperature, and equals 3.199 for polystyrene. m is In-
dependont of temperature and obeys the equation m - a exp(bT) (23).
a . 9.502-10- 271 b - 0.0472. The pressure lose AP inp occurring when the
material enters the capillary, was calculated from the equation
Pinp ' (Pc11 - P 11G)All - 10) (PO and P I denote the preas%re in the
ahannels with the short and the long capillary, respectivelyl I I and I
are the lengths of the long and short capillaries, respectively). The
empirical equation Eu inp . K/Reo (24) was obtained for polystyrene. Eu inp
2 -1/N 1/n(.
is Buler's numberl X - constj Re - Qv +3)1-1/nml/n is t~e actual
Reynolds number; Q densityl R - radius of the capillaryl v - Q/nR is the
mean outflow velocity for round capillaries. The linear function
log EU inp " f(logRe) was obtained for X - 147.6, a v 1.037. Kanavets'
plastometer and papers by N. P. Shanin and R. V. Torner are mentioned.
There are 12 figures, 1 table, and 15 references# 6 Soviet-bloo and
8 non-Soviet-bloo.
Card 4/7

Flow of block polystyrene ...
Fig.1
Card 5/7
14
0
A
V-1 WN
S/191/61/000/001/007/015
B101/B205

. Flow of block polystyrene ...
3/191/61/000/001/007/015
B101/B205
R
VC&OUMMS, IQ,.
. 4)
C) x yeasumeflio -
Pig-4
x vrqu"O.*POjP.Q
Fig.3
Card 6/7
C

S/191/61/000/001/007/015
Flow of block polystyrene... BIOI/B205
Legend to Figs. 3-5s K - ring of the strain gauge; R - wire gauges;
9 - coil of the electromagnet of the pickupI A a armature of the pickupi
% a scale resistor; a) inputj b) amplifierl a) to amplifierl d) to
oscilloscope.
Card 7/7

A.N
KHLUNj Ya.])ol q!T -P~ .
Method for the design of extruder feed throats. P3ast-massy no-3:54,W
161. 1 (MIRA 140)
I (utrusion prooses) (Thermoplastics)

UIASHOVY H.H.,, insh.; LM.Nv A.11. doktor tekhn.naukr
Solving some problew of the flow of fused polymers in
screw presses* Shimg, mashe no.6;29-33 N-D 16le
(MIM 15:2)
Polymers)
Power presses)
~

STEPCHEMOs V.N.L-W-I-N-jAJ-i-
Continuous method of producing poly (virql alcohol), Pl"t.m"57
no.8:52-57 161, (KMA 14: 7)
(Vinyl alcohol polymers)

IZVINt Boris Menakhezovichp dots*# kande ekonom. nauki IZVTII,.~-
A!MMXLq)b doktor tekhn. nauk, prof.; MRUSHEV, I.M.,. red.;
fER-STIPMMTS, H.S., red.; C&RASD4CVA, Ye.S.p t8khn. red.
(Using plastics and saving materials in industry] Prime'nenie
plastmass i ekonomiia materialov v proaVshlennosti. Moskva
Mconcmdzdat, 1962. 242 p. (MIRA 15:61
(plastics)

KALINCHEV, E.L.; LEVIN, A.N.
Main processes occurring inside injection molds. Plast.massy
I no.3:57-62 162. (Plastics-Molding) (MIRA 15 t 4)

.iUTNORS:
T 17 L
S/ l C 1 /9, 2/000/00 4/10 1 Vc 17
Bi 1UZB , 78
.4
Goncharov, Vf' . j. , Layin. a. N. , Ryvkin, G - A.
Absor,)tiori method of dryinC. formaldviijac
Plastich4sklye va~i:;y, -13. 4, 19062, 1/0-12
T-,'Zll: The selective water a`.;sox-i;tion of' 3ome oreanic solvents was us.-,d
to dry formulds.-hyde. li,(droc~-rbon3 with limited =iscible -xith Tiater
(benzene, toluene, carbon tetrachlorine, etc.) have Ereater --ater absorptior,
at hii:her temperature. About 800C is the optimum for toluene, oxing to thin,
-1y low vapor pro*zue and hiCh water solubi'ity (-0.)
eormaldeh;jdt. was passud continuouuly through a Hanchii; ring-packed
Losorption tower with carefully dried toluene as absorbent. No traoun of
polymers appeared after 10 hrs. The thermal stability of the polymer
obtained is the criterion of the quality of drying. u-~olyoxy methylene
*.,;as vaporized in the destructor (1, Fie. 2) at 1600C. The cas-vapor
mixture bubbles continuously throuCh dried toluene at 800C, and reacho-s the
zeaction vessel (7) via 3, 4, 5, and 6 for polymerization. The reaction.
medium was anhydrous toluene or Easoline. The Initiator was 0.025 Yo (by
Card '1/2

5/19 62/10CO/0041101""1017
Absorption method of dryine... B1 10Y1, 1 718
-eigh' o-- the reaction medium) calci*"m stearate. No ;;o%-mvr was svparatfid
in cooler and separator. Thii good thc-rmul stability and homo6eneity of the
2olyformaldehyde obtained sho,,-. that the continuous method Is to be
recommended. There are 6 figures.
F1 g. 2.
Diagram of system
_Oor dryine .1ormaldehyde.
-end: (1) destructor,
125 absorption column,
(3) trap, (4) contra-flow
cooler, (5) cooler,
6) Dewar flask,
'reaction vessel,
M
(8) demister.
Card 2/2

KONSTANTINOV, V.N.; LEVIN, A.N.
Performance of multiple-screw Pxtruders with zes~dng wormse.
.1 1
Plast.massy no.5:47-52 '62. ( Yj-RA I ;- ; i.
(Extrusion (Plastics))

L&VINq A.Nj SMIS89VO A.A.
Ways for raising the technical iml of the production
of plutico and plastic goods* Plast,masoy no,10:1-2
162. (MM 15:11)
(mmace industry)

VTKINj VA. j IEVINO A.N.
Block polymerization of styrene in a tube still. Pleat.
massy w.10ig-11 062. (MIRA 15:11)
(styrene) (Polymerization)
1
4

S/l9lj62/000/011/003/019
B101/B186
AUTHORSt Ming V. V. Levin, A. N.
TITLE: Study of the kinetics of styrene bulk polymerization
M"RIODICALs Plasticheskiye massy, no. 11, 1962t 8-9
TEXT: In order to improve the industrial production of bulk polystyrene
the kinetics of the polymerization was studied. Pure styrene was heated
in ampoules in 0.5 atm argon, determining the amount and molecular weight
of polystyrene formed under various temperature conditions. The results
(Fig.) led to the following conclusionst (1) kost of the styrene
polymerizes between 100 and 1500C; (2) an increase from 150 to 2200C in
the late stage of polymerization does not iccelerate it further; (3) ofter
85~* of styrene, is converted it takes another 16-18 hre to polymerize the
crest monomer at 150-2200C, (4) to speed up polymerization the temperature
must be raised in the second stage and toward the end of the procoss;
(5) polymerization according to the data of curve 4 (Fig.) makes it
possible to produce polystyrene with a molecular weight of 80,000 within
40 hrs. There are 1 figure and I table.
Card 1/2

Study of the kinetics of ...
S/191/62/000/011/003/019
B101/B186
Fig. Kinetics of styrene polymerization and change of the molecular
weight. Abscissas hro; ordinates molecular weight,
ZZ
14
IJ
As
;
of
JF--

5

--
F 7 -
1 1 H I
Card 2/2

S/06.3/62/007/OC)2/009/014
A057/Ai26
AUTHORS: Oarbar, M.I., Lev1p, A.N. Professor, Sagalayev, ON.
TITIE. Modern methods for the processing of plastics
PrRIODICAL: "'Uhurnal vseroyijznogo khimicheskogo obshchostva Iment D.I.
t4endcleyeva, v. 7, no. 2, 1962, 207 - 211
TEXT: The scope of the present paper Is to give some directions for the
intensification and development of the Soviet plastics Industry. To increase
the productivity of presses one of the basic problems is the development of quick
hardening of compression materials. The use of pure raw materials In the pro-
cessing of polycondensation plastics and suitable filler compounds is expedient.
An exchange of phthalic anhydride to 16ophthalic acid in the production of non-
-saturated polyester resins Increases considerably the hardening rate and elas-
ticity of the corresponding plastics. To simplify the proportioning of the raw
material the weight of tablettes must be equal to the -weight of the product and
for this reason hydraulic tabletting machines should be used to a greater extent.
High-frequency pre-heating I's of advantage to reduce the holding time. One of
the basic factors for high productivity Is the exact temperature at the compres-
Card 1/,3

3/06,3/62/007/002/009/0 0
Modern Methods for the ..... AU57/A 126
sion. Since automation Is also of great Importance, automatic presses with
high productivity (above 3 - 5 Million Ploces per year) should be constructed.
Another type of automation can be attained with rotor lines of automates, which
Is realized for instance In the Plant "rarbolit" for the production of presned
switch parts. One of' the modern plastics processing method Is casting comprus-
sion applied to thermoreactive materials In the manufacture of electric Irlsulat~
Ing articles. This Method is insufficiently studied yet and besides complicated.
Investigations in die casting, the basic method for the processing of thermo-
plastic materials, should be developed. At the present time several types of
die casting machines were. constructed In the USSR for 8, 16, and 1;2 crL3 articles
without pre-mastication, for 63, 125,2t~O, 500, and 1000 cm3 with 31ngle 3cmw-
-conveyer pre-rantication, and vertical die casting machines "or 2,wJ cr.L3 nr-
ticles with double scmw-conveyer mastication. Casting machines with one cylin-
der used for mold locking and In.,ectlon of the material aria or interest for the
production of articles up to 1W g/cycle. Casting without pressure Is becoming'
more Important for epoxide and polyamide resins and foamed plastics. However,
special attention should be paid here to mechanization and automation. Extrusicn
Is a recently developed ffethod applied to various thermoplastic articles. Rotat-
Ing extruders (oi with rotating cap) am of special Interest for this type of
Card 2/3

S/06 316 2100 7/D0 21W,11() 14
Modern methods t'or the ..... A(j57/A 126
pla:;tlcz procesning. Vacuum molding In used in several vnrlations chiefly for
the production oC sheet materials. Among the different methods of vacuum-mold-
Ing of thermoplastics, the authors recommend the positive molding with mobib
molds. In production of glass-reinforced plastics some special problems should
be considered. OIL' great Importance for the processing of plastics Is the devel-
opmont and standardization of the corresponding equipment. Thus, It Is planned
to manufacture thopsands of' molds by means of modern rwthods and cheaper
materials In special factories. Another important problem Is the development
of theoretical principles for thecalculation " construction of plastics artic-
les. There are 6 figures.
Card .3/3

LEVINg A.N., doktor tekhn. nauk, red.; TROITSKAYA, L.P., red.
'----~:-~NTSZVA, S.V., takhn. red.
I
(Problems in the extrusion of thermoplastics; translated
articles] Voprosy ekstruzii termoplastov; sbornik pereyodov.
Moskva, Izd-vo inostr. lit-ry, 1963. 333 p. (MIRA 16:6)
(Thermoplastics) (Extrusion process)

DOdK
a/
mawzuTixx
AAM387
111norp re Taol ImrIn# As No
Plastics in the dh7s"a-birme~obring Wustr7 (Pla'atmaseyo -w kbimichoskom mash-
Inostroyonii) Mosoew lmaohglsq 1963o 21A po tUuoo,, blblloo# appondo 7500
copies printed* Rev";r Mmw, Be Ael Iditors Proebrashouskly# A* Yuo;
Managing editors Py*bakarap Ve rel Miter of the pmblishlag houses "howa#
X,. P.1 Toohnical, OdIterss DemkIna, go To,, Gordayeva, Le Pol Proofreaders
Piryusevs Pe A. n
TOPM TAGBt plastics,, chatical Imftstr7,, phonalformaldebydep Billoons polymors'l
furyl resinsp opoxMe roolneg Sloss textellboop p*2yvlrql oblerldej, vinyl pUa--
tic,, polyethy2one# polypropylono# fluoreethylsnes,, dderoethylenes,' vIFqI
&sbostoop gnphiten
PURPME AND COVERAMs This book is- Intaided. for engineers and t"Micians is
plaming; organisatimm and plants In the 0 rW and the cheabal
industrieso A my be ef.we also for s#WWaU In engimoring and mohlimmd"Us
~'vulsese The book coutahm Intereatiag and pmotloal Wwutim somermlog
Car& 2/5

T-
AW.=387
n
plastics and their properties m3d application in the chealcal-enginearing Indoo.
U7 both as Independent stauctural mt*rJAIs and " "ective coatingso Charsom,
iterlstla structunVapperstuses wd parts ode of plastics are described# and
methods an given for desIpUS apparatuses mods et famIllar pust"s (TIRA"
fadlites etoo)o Go So TaohJA assisted f4be authars in writing Chapter/T4 and
Chapter InI us wmitten by Ao Te Meldconew and J6 No LOVIne
TAKE Or CCN
Foreword 3
fCho L Pbenolferaddeby4e Plastics
PhenolfwmIde1wde resh4 - - I
The mandacture of oppmtes &M Wividual, Items st pbom armaldagde plastics
f? I- . 40 so 24
Ph*no2fww*2dftd9'nfI&-b~~* blad4re 27
Protectiag sppsnt~s We of fOrs" metals with eaValtless based so pbend.
fama2dftdo repbs is 30
Data cencenUg APPWtift of apmat" Mde of *ftelfw"Idebw" noise.-In.
Cold 2/S

ULIArAW,, E.L.,, insh.j UTD, A.N. doktor takhn.naukp poofe
Calculating the force necessary for closing the molds of molding aact&"B.
Kh1m.mashinostr. no.2s8-10 Mr-,kp 063. (MIw.A 16*.4)
(Plan tico-Molding)

GONCHAROV9 O.S.; IZVINj, A*11*; RIVKU, CA*
Catalytic action o? some substances on the process of the 1
degradation of &-p?lycxymothylene. Plast.masey no.2s62-63
163o (MMA 16 12)
(Polyoiymethylene) (catalysts)

jy,,_A.N. Prinimali uchast1ye: MOLOKANOV, A.V.;
KLIBCYV, I.Ya. ; IZV
VA-SHd-p.G.Z.,- OL'EUEVj B.A., inzh.p retsenzent;
PMBRAZHUSKIY, A.Yu., red.; RYZHOVA, L.P., Inzh., red.
izd-va; DEMKINA, N.F... tekhn. red.; GORDEYEVA, L.P.,
tekhn. red.
[Plastics in the manufacture of chemical machinery] Plast-
massy v khimicheskom mashinostroonii. Moskva, Mashgiz,.
1963. 224 P. (MI RA 17: 1)

ZLATINAV S,A.; LEVIN A#N,
Obtaining chemically uniform copolymers. Plant.massy no.100-7
163. (MIRA 16%10)

MIN, Abram Naumovicbj prof.; FAM0111p I.B., red.
(Plastic material number one] Plastik nomer odin. Mc-
skyap Izd-vo "Znaniep" 1964. 37 p. (Havoe v zhiznI,
naukep tekhnike, XI Serilas Khimiia,, no.3) (MIRA MW

LEVIN, A. N.
"Neprer~,vn3e protsezzv v proizvodstve pollmerov."
report submitted for:15-th Intl Cong, Industrial "'hemistry, Warsaw, Sep
64.

KAPLUN, Ya.B.; IEVIN, A.N.
Design and construction of the inlet area ,-)f ti-,e extruder.
Plast.massy no.109~-46 164. (mm 17..6)