SCIENTIFIC ABSTRACT SKOBLIN, I.N. - SKOBLO, D.I.

• Document Type: CREST
• Collection: Scientific Abstracts
• Document Number (FOIA) /ESDN (CREST): CIA-RDP86-00513R001551020015-1
• Release Decision: RIF
• Original Classification: S
• Document Page Count: 100
• Document Creation Date: November 2, 2016
• Document Release Date: March 14, 2001
• Sequence Number: 15
• Publication Date: December 31, 1967
• Content Type: SCIENTIFIC ABSTRACT

SKrPLTN, 1. V.
Gidravlichskie dvigateli sallskikh gidroelektrosilovykh ustanovok. Moskva,
Sellkhozffiz, 1950. 168 n.
Hvdraulic motors of rural water-power electric plants.
SO: Manufacturing and Mechanical Engineering in the "oviet Union, Library of
Congress, 1953

P11ASE I BOOK EXPLOITATION SOV/4731
~Ierman, Avraam Llvovichl and Ivan Nikolayevich Skoblin
Montezh, ekspluatatsiya i remont oborudovaniya malykh i sredaikh gidroturbin
(Assembly, Operation, and Repair of the Equipment of Small and Medium-Sized
Hydraulic Turbines) Moscow, Mashgiz, 1959. 260 P. 3,500 copies printed.
Reviewer: V.N. Voroblyev, Engineer; Ed.: N.Ya. Bauman, Engineer; Managing Ed.
(Ural-Siberian Department, Mashgiz): M.A. Bezukladnikov, Engineer; Tech. Ed.:
N.A. Dugina.
PURPOSE: This book is intended for qualified technical personnel engaged in the
asEembly, operation, and repair of the equipment of small and medium-sized
hydroelectric stations.
COVEFAGE: The book gives principles of operation, design, technology of assembly
and repaIr of hydroturbines, automatic speed regulators, and auxiliary equipment.
The authors describe the starting, tuning, and operation of the mechanical equip-
ment of small and medium-sized hydroelectric stations and discuss difficulties
in the operation of hydramechanical equipment. Information is given on the
CarA-1/9--

Assembly, Operation, and Repair of the Equipment (Cont-) SOV/4731
causes of such difficulties and the means for ellmin ing them. Some methods
for increasing the power of hydroelectric stations and the output of electric-
al energy are also discussed. CLnps,1, III, and V were written by Engineer
1.N. Skoblin and 'Chs. II and IV ~y_ Engineer A.L. German. No personalities are
mentioned. There are 31 references, all Soviet.
'rA.BLE 6F COM"ENTS:
Foreword
Cb. T. General Information on the Use of River-Water Energy and on the
3
Water-Pcyjer Equipment of Small and Medium-Sized Hydroelectric
Stations (GES) 5
1. Mechanical enerEy of water and units for measuring stream power 5
2. Basic systems and methods of the use of river-water energy in GES 6
5- Water-power equilnent of GES 9
Impulse hydroturbines 9
Reaction hydroturbines 10
Cavitation 13
Systems and designs of hydrotrubines 14
Velocity of hydroturbines 15
Card 2/9--

C 9- ~ F, r
'T I -U-

Coripositl,,n wid dissaciation const"t of b*-,,,,",
8 I*rom and M. N. ~,z U.;!rzye
i. A.~z*r-WAR-4 rat. Zhur.,
Ut~ne. 1954, 1666d.-The cu-mrs. w:Ls ded. from
tacm~ure P-, rants a. --.e a-ptiml.d. of insms. ijf-O,2-U1 s,,j
of BKNO~), and N:ITCNS faim; ' P. vati-m-i prurwdoivi %vi He
a cun3t. vrji. of the in', t. ivaj riaint~iitivd. Nfax. optint d.
x
iv3q -ibrerved uta raw) jBi '41: (C."I'S-] -1:1. Thin, the
'rile di-s(wll. conit.

BROOM I IMIR
N. I 1 1. H 111 11 a 111 1 IIIIIV w, -m-

-- ----

"ne
a
r 5 c -v a
165.
1l-, ~q ~,U L :710 r 0 10 1
iW no.
AN 5.)
T, A 1 3
Oc
r t

SHAUVICII, A.B.; SEDBLINA, N.M.
Spectral anal7sis of carbon, silicon, and phosphorus in
forromanganese. Zav.lab.22 nos2:195-196 F'56.(MLRA 9:6)
l.Laboratoriya standartn7kh obraztsov pri Urallskom insti-
tuto chernykh metallov.
(Ferromanganese-Spectra)

SKOBLIVA, Z.A.
atomicoradlographic characteristics of the supracondylar
t
actures. Trudy Ukr. nauch.-issl. inst. ortop. i travm.
no.15:155-160 159 (MIRA 16:12)
1. Iz otdela fiziologil i atomekhaniki (zav. otdelom - dok-tor
med. nlauk O.V.Nedrigaylova3 Ukrainskogo nauchno-issledovatell-
skogo institu-ta prtopedii i travmatologii imeni prof. M.I.
Sitenko (dir.-chlen-korrespandent ANN SSSR, prof. N.P.
Novachenko).

SKOBLIPISKIY, A., inzh.; KACHANOV, P., inzh.
Mobile plant for large-panel apartment-house construction.
Zhil. strol. no.1:31 164. (MIRA 18:11)

mm~~ - . . I .. 11 1 1 1
4
%-Xwch"ge -adso .,-a- G- mixed'm edhL . .is-iiui4 a-iii
luleg M==ge In mixed me4lit,
Tt1jjy Knuch.-Is
9~!bynlorkt -~00-076"-N-; : ; I .
10. 103-2ogliO53). The cxcl~21 Itti,
of C-% and 11a for NO aud K " wal StIIIII&I on 941111'0-
nit~.- fit water an(I water-41L. niNts, con1jr. 30,1 50, UVA10
wt.~,'ut,fafc. GL~ucoaitc ptd. with the blvaknt Vitioll UIP"
A:terrewdIngcq4i1..
the Unit. of de3orbed Ot or Da was stAuined to ba uq(vJ to)
the q1t.14thY tit adsvithcAl K or Nd The quafitity of the 3vit
1. from the &.1cit-itle1m-
c~itjmj itt the mborbelit waN citlc(
twun, the ittat.ad-sati)tIon and th,: iltwn(ity Of J910fikdfixt.
Unfler theic! coididons the Nikc!skl' caluattoct (Cj.;,J$,
or
(a. Mot
sisnPl;fiL:;jfio1i: a - tj,, - hi a M Ce - 01, wberra b
tht milligr-on e(Iiiiv. of Oit bivalcut cation doscittird 641M
10 g, of adsorbcv t and etlaals tht clitantity of wity rW tim.
uieat cl.tiua, C-,~ is Olt 1111A. ad4otlit(Oll, Civ 6 ULU Ofilffbtl
cancri. of unlyalcut vatioa in inillimule per I., Itij K islithe-
aesorprinn. eunst. The expfl. rtsultA sue pa-senti!d a
tLernis an codrdinates I/a. a/J/(It)O Q - a?(Cf. Mpto
CqLatiu% C.A. 78, 41LIq') -Ylicre a b tht; quant ty of' Wit In
rag. couiv. desorticil from i0 g, of ad!orbont -sud Ce I%&
bjitL-d co.ica. of the fun huNg adsurbM In mi P

.......... .....-
on v rdin-ate ii(jdo C"!-:"4Fi1n ICTM"I,411, 'o,
or
LZ 34, 4[1
ctiuaJoij). The lintar shap! of Lhe isothe.=1 shows theap.,
plicahlity c( th"e equatium to excluinge renctims In thew
vsterai. Atidn. of a -,olvent wirh a s~i W, dielec. caust.
~iifccd the t-quil loAurd displacenicitt of hNaltrut rations,'j, f
addli. (f Y~I~j) a1.% loviert:0 the valae -if (lie equU. LonitAg q
ha,f. The compri. of the i-ilvent lidt; "no Oka on a. ul
ghucojilfe. Usc of the muddiol Nikul'-~,Ul equatino shispli-,
fiet; tb,! bta4v of catiz-)PiL -~xchnisge. . 11. Erbage of Wfftr-~
ent valfmt calionc on glaucDnlre in dIxxaue-wu1er~msd1%Jzi.
Ibid. 205- G.-,nia ekcharigr 0i Ila for Ka Qn!IAtvQuItL. im
stIL-in-11 in a 7V; toltc tit dioxanc in Irate- The MIS t2
fc) thoze ON. i!1ed for miter-atc. InIlh. -The
a
ion .1.1
0 eGrj~tiwi ;-; "pprecLAIj IQNr than X.1
if"), .111d thi., difierence ijjVr)!AA..i W1111 be cuittlit n[ the
arg. Sk-cra in the mixt. I"luougla ft~jreat. Zhmr Kkim.
1941, Nfj,. 35713, J5714. N1. YinfAl

sm-BLI-6-110K, R. F.
Dissertation: *Investigation of the Adsorpt#n Exchange with Organic and Inorganic
Adsorbents from mixed agents." Cand C~em Sci. l0iarlkov State U. Kharlkov 1954.
(ReferativMy Zhuarmal-17Jurdya, Moscow, No 9, May 54)
SO: SUM 318, 23 Dec 1954

I)b F
ttd. witfs C~1111 w.S 011W114
T19mj- - sit o I Fitid chare-my-&
ti' brated with PhNIIOICI ind the 3 Coluffline-11CI r$,
In Capon's equation. (1/0 - (Ila.) + (K ViI211014t),
the cn-qt. K wm 13.9-15.3 an,) the max. anst. c?. takka tip,
by 10 C. sorbent vrwi D.52-OAZ snect. for Lill 4 salts; thus, lLbc!
intrrmfuction of a Me Voup Imil noeffcct on the loss exchanLe.;
a is the ri~mt. eschanzol (for 10 g, sothent) and s: Is the fin4li
contu. of the maine salt. At high e, the anit. of CaAh&!
PLICLA Wal smolel tkut the 4111t. *f the amille Ukhalup-
pLrk~lpq mul. admittiticsts took uhmt.
J.

DAVYDOV, A.T.; SKOBLIONOK. R.Y.
00000amba4p--
Dependence of cation exchange adsorption on the dielectric constant
of the medium [with English summary in insert]. Koll.zhur. 18 no.2:
163-166 Mr-Ap '56. (MLRA 9:8)
1. Kharlkovskiy gosudarstvannyy universitet imeat A.M. Gor'kogo,
kafedra obshchey khimii.
(Cations) (Adsorption)

USSR/Physical Chemls~-.ry Surface Ph-n~_mera. ChrnmatDgraphy. Ion
ExchangeY B-13
Abst Journal: Referat Zhur - Khimiya, No 19, 1956, 6,1226
Author: Davydov, A. T.J. Skoblionek, R. F.
Institution: None
Title: Investigation of Exchange Adsorptian c,"' Cathi.:)na from Mixed Media
on Volkonskoite
Original
Periodical: Zh. obshch. khimii, 1956, 26, No 2, 350-355
Abstract: Investigation of the correlations in the absorption of Na+ and
K+ by Ba-forms of vat-konskoite, from aqueous alcohol and aqueous
dioxane solutions of'their chlorides. It was found that the ex-
change capacity of the sorbent remains constant with all composi-
tions of the solvent. The equilibrillm cc-nstant calculated in ac-
cordance with the equation of Ye. N. Gapon.7 or B. P. Nikollskiy,
increases with increase of the dielectric permittivity of the
medium.
Card 1/1

DAVYDOV, A.T.; SKO-3LI0110, R.F.
Stud7 of the exchange sorption of organic Ions. Shuroobvkhim. 26
no,7:l86O-lB62 Jl 156. (MA 9:10)
1. Kharlkovskiy goeudaretvanny-y universitet.
(sorption) (Ions)

DAVYDOV. A.T.;_�EOJ14IONOX
.~~R
Structure dependence of ionic sorption exchange, Part 2, The
sorption of bivalent simines. Koll.zhur. 19 no.2:183-187 Mr-Ap
'57. (MLRA 10:5)
l.Khar'kovskiy gosudaretvennyy universitet im, APNO Gorlkogo,
Kafedra obshchey khimii.
(Sorption) (Amines)

'avydov, A. T., SkoblionD
-1. 2 - S - 2
-h n' lu~?nc- -)f "he Me,4-Jum on the Ion Exchange ;!dsorntion
i yar. i y(-, s rE., -1 na ionoolmennu,yu 1-13,-)rbt!iiYu1 T h (2 D, o e r -
0~, th~, :-,x Dlel:lct
-n test- ric Constant o~
jol-v~111. (zavisimost, konstanty obmena ot dielektricheskoy
r. istovannoy rastvorit.)Iya)
D I ':A. 'Zhurnal fizichcskoy khimii, 1q,58, Vol.
~2, Nr 8,
r -)5 'U3'*-
-)p.
hn publicat4ons by J.A. '-hilov 'Ref 12), M.M. Dubinin
-~r Rn
.'i gn --, r an n nny -Kn, 1 enni~ (Ref 9,,
(Ref 1), ).N. Jtrazhesko (Refs 10, 1 1 Krc:~s-
man ~?.ni Kitchener (Ref 3), show that the Influence of the
composition of the liquid phase on absorDtion processes is
by ii?varal factors. To ftnd a possibility of 3,~-
tr,rminin6 the mpximum effact in these processes the authoz,3
inv~!stlgaatei thi-- constant of the solvent. Tne
4-,iter-~eveni.-~ncrt b-2-,.v,2en the exchange constant and t!-c- iiP,,(-C-
trLc constant of th? solvent already observed wty b%,, ex-
plaine', bv a on-nni-, of the activity co-ffficient. To prove
-i r
,,, I I

The Influence of the :Jedium on the Ion SCV/76-32-8-2/37
-i.xc,hange Adsorption. The Dependence of the E'xchang2 Constant on the
~)i,.-I-,ictric Constant of the Solvent
thi:; the -_,r,,ua'1-ions by Nikni Skiy ~'Ref 14) an~:
Gapon (Rof 19) are qxplained and a lerivation of the ellUa-
tions is carried out according to explanat Ions by V,K.
b
Semenchenko (Ref 21), with data y Scatchard (Skatchard'
(Refs 22,23) being used. It was found that the furiction
1g K = f (1'/D) is represente-I by a cur-re of second order, Tn
the case that the radius of the displacing ion is smaller
than that of the displaced ion the summary curve has the
shape of a hyperbola. This is found in the exchange of 'a 2+_
and Ba. 2+_ ions on _K+ and Na +_ ions. If, however, the radius
of the displacing ion is greater than that of the displaced
one a parabolic curve is obtained. It will occur in an ex-
change adsorption of the Li+- ion.
There are 2 figures, 3 tables, and 23 references, 10, of which
are Soviet.
Carl ?/3

Thi,~ infLuc-ncp of the rtetl--iu:a on t4e Ion `V/176-32-8-?!
:,'.%chp-ng,~ Aisor-ption. -D-iv~ ll-pendence of the Exchange Con3tant or, thr-~
;)i,~l-c-ctric Constant of th- 3olven"
gosudarctvcnny~jr univorsitut irli. Gorlkcgo
imeni

SKOBLIONOKY R.F.; DAVYDOV, A.T.
Exchange sorption of ions from nonaqueous media, Part 1, Zbur,
fJz. khim. 37 no.12:2648-2653 D 163. (MIPLA 17:1)
1. Khnrlkovskiy gosudarstvennyy universitet imeni A.M.Gorlkogo.

r: f d
L v l r-, ~i, v a e r. 1~ znijr.
WIHA 17.9)

MJKHAYLOVI P.1.4 SKOBLO, A.I.
Investigati-nIg the hydrodynamic mode of operation oV fireboxes in
pipe-still mode1q. Trudy MINKIfiGP no-37,141-156 '62. OMIRA 1,7.13)

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4110111 one hall to two times as much toots oil was obitained by usdng vacuum as by, the usu&t
method. Stack wax should be of uniform compa. and contain a coo pletr petim of -09
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pww. A. 1. Skoblo ant] G. T. Boahedomov. Awb-
1933, Me. 11-12, -
400
Ar
f 10".-_gots. made with a Koppe coke furnace using .00
aqibpW coutil. 81.3 and 40% vulattle matter were on.
4141

so j -w(Tslactury berause of the cuostructlon of the (urnacr,
rhe coke am td. to 13 and 31.5% anill rontainrd ash .
2*0
0.72. volatile matter O.WI.M. 8 0.63-1AM and 1110
00 2.4%. Its mecb. pwWties depeticittl upon ibir time of
00 j coking. A. A. I'lochtfinSk
46 see
e0
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so
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An L s a *4 a o a i w s,
LOn

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s the following 2 mw% slumild tv di-
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mr.; ll.%~!rbza~f,;zhan und tt4 Sci tntific rrd
Pub.
calculpticn- yiel-is anrl fr;,ctional-
t o n s o f , ra:~ o 1. i n t i n
lovitt -ource':
i-strartt-! -in !'Trt~sur~- islzqn,", on f;,-1.
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SKOBLO A.I.,.-r2Pktor; LUKASHNVICH. I.P., kandidat tmkhatchaskikh nauk,
ON ~ pre.- __6_nt; LIVOVA, L.A., vedushchiy rodaktor; POLOSINA. A.S.,
takhnicheaki.v redaktor
[Tectuiical analysis of fuels and mineral oils] Takhnichaskii analis
topliv i minerallnykh masel. Moskva, dos.naachno-tekha.izd-vo neft.
i gorno-toplivnoi lit-ry, 1951. 566 p. (MLRA 10:9)
(Liquid fuels) (Petroleum products) (Mineral oils)

Or
\/914. Emig -CR- D21", U.411 1,1. All,!TJAL
PURCLaTA.
W,
Ar,A , ct 6 1 ridurmnln n a f t a I I w I s c ravdulltdrl uUMP. In

filz~mc 0 L1P, d[.-.6
kuj, nit ite, foymi ;Anr f !V" V
P it f;
old
WiU. 0~1,
w ti, all I",
it. n, mt.,11rim.1
It, tklid fri'Mit -I iv md jximr,d
llt-rvl~j (1) a 14114~ A 1-11111UuMing
,qu -mol Wevilhill jtlz (J -'tp-a Ivith little
A:
-rh ibe liqubl. ~i::d 13) the iix-.ptirtmut acme
0 r"In eni-,11mcm in il-flivim Sulliv'! C07.tam of
7-, 1-& t1 ;~wp~ mth run

1~ J
iliT I TIT

AUTHORS: Barsukov, Ye.Ya. and Skoblo, A.I. 65-10-5/13
TITIE: On the Hydrodynamic Stability of* a Ca-b-alyst- layer in
Separating Installations of Crude Oil Processing Plants
(0 gidrodinamicheskoy ustoychivosti sloya katalizatora v
separiruyushchikh ustroystvakh apparatov dlya pererabotki
nefti)
PERIODICAL: Khimiya i Tekhnologiya Topliva. i Masel, 1957, No lot
pp. 21 - 28 (USER)
A13STRACT: The results of an investigation carried out by VNII NP
(All-Union Scientific Research Institute of the Petroleum
Industry) of the following problems are described: 1) A study
of the hydrodynamics of the process of separation of gas stream
from a layer of granular material; 2) A study of the cause of
carry-over of a granular material in industrial installations;
3) Development of a method of designing separating equipment
which would permit the choice of optimal operating conditions,
and 4) a comparative evaluation of various types of separating
equipment. In the study of the mechanism of the process of
separation of a gas stream from a layer, transparent models were
used in which the separation process in parallel and counter
current flows could be observed. Measurements of the velocity
Cardl/40f the gas stream leaving a layer of a granular material were

65-10-5/13
On the Hydrodynamic Stability of a Catalyst Layer in Sepa-rating
Installations of Crude Oil Processing Plants
carried out with pneumeters and according to M.E. Aerov's
method (Ref. 6 - the velocity curve of Eas is determined on
the basis of the intensity of the mass transfer from the surface
of naphthalene grains into the gas stream). Both methods gave
similar results. Studies of the mechanism of gas separation
from a layer of stationary and moving granular material indi-
cated that under industrial conditions, three main types of
separation are possible: 1) with low gas velocities the usual
filtering of the gas through the layer takes place. The surface
of the layer formed under the natural repose angle is charact-
erised by the stationary position of particles for a stationary
layer and by their movement in the fields of gravity together
with the whole granular mass for the moving layer. 2) The
second type of separation is determined by the unstable state of
particles in the imii,ediate neighbourhood of the walls of the
separator, similar to boiling, but without breaking of contact
between particles in the remaining part of the layer. 3) At
high gas velocities, the third type of the process takes place.
It is characterised by a break in the normal separation,
accompanied by the grovith of the layer in the free space of the
Card 2/4

65-10-5/13
On the Hydrodynamic Stabilit3r of a Catalyst Layer in Se.parating
Installations of Crude Oil Processing Plants
separator, followed by a carry-over of the granular material
into the gas outlet system. It was established by visual
observations and measurements that the distribution of veloc-
ities of gas leaving the layer is in many cases aon-uniform.
The maximum velocity is at the walls (Fig.2). In order to
establish the influence of the intensity of the gas stream
on the value of maximum velocity, a series of experiments within
a wide range of Reynolds numbers (Re layer = 400 - 5 000) and
wide fractions of granular materials (balls and tabldr.) was
carried out. By mathematical treatment of the experimental
results, formulae for the determination of maximum velocities
of the gas stream of the walls for direct and counter-current
streams were obtained (Eaus. I and 2, respectively). The
choice of the optimum gasodynamic conditions of the operation
of a separator and the determination of the best conditions at
which the process is characterised by a maximum amount of
separated gas consist in finding the critical value of the
maximum velocity above which the normal separation of gas ceaseso
On the basis of the theory of simil2rity and the experimental
data (Table 1), a formula for the critical velocity (9) was
Card3/4

On the Hydrodynamic Stability of a Catalyst Layer in Separating
Installations of Crude Oil Processing Plants
obtained. For practical calculations, simplified formulae (10)
and (11) can be used. Similar formulae (16, 17) 'ere also
obtained by treating the experimental data according to the
Lyakhovskiy method (Ref.9), using Slikhter and Kirpichev
criteria. The equations obtained were used for check calcu-
lations of two types of industrial separators. The initial
data and the -results of calculations are given in Taae 2. The
results obtained confirmed the correctness afthe proposed
method. It was also e2tablished that the efficiency of separ-
ation with descending gas stream can be increased by fixing
dumping plates at an angle of the natural repose to the bottom
part of the walls of the separator. Characteristic distri-
bution curves of gas velocities at the outlet from a layer in
the presence (Curve 1) and absence (Curve 2) of dumpers are
shown in Fig.2. There are 2 figures, 2 tables and 9 Russian
references.
ASSOCIATION: VNII NP
AVAILABLE: Library of Uongress
Card 4/4

HOLOKANOV, Yu.K.; SKOBLO, Aj, , ..
--', j.' - -
Hydrarlic calculations of slots for Plate-column bubbling caps.
Izv. v7s. ucheb. zav.; neft' i gaz no. 3:109-116 158. (MIRA 11:7)
1. Moskovakiy neftyanoy inatitut im. akad. I.M.Gubkina.
(Plate towors)

KCRN.-5T?,V, Yu.K.; SKOBLO, A.I.
Effect of pressure on the relative volatility Index during ex-
tractive distillation. 1zv.vys.ucheb.zav-; neft' i gaz. no.7:57-65
'58- (MIRA 11:11)
1. Moskovskiy neftyanoy institut im alkad. 1.M. GubkInta.
(Distillation) (Essencea and essential oils)

1MUGIA)V, S.A.;
SKOBW, A.I.
Investig~ating convective heat transfer between a granular material
and a gas stream. Xhim I tekh. topl. 1, masel 3 no.3:23-30 Kr '58.
(MIRA 11:3)
1.Moskovskiy neftyano7 institut im akademika I.M. Gubkina.
(Heat--Transmission)
(Fluidization)

BiLAZifl4ILOV, Vasiliy Timofeyevich. Prininol uchaqtiye: MALINOVSKAYA,
H.-P., inzh... SK UQ.-AI , ret3enzent; BONDAIVOKO, B.I.,
retsenzent; YZFREHOVA, T.D., vadushchiy red.; MUKIIINA, E.A.,
tek~m. red.
[Present-day units for wnufacturing lubricating oils]
Sovremennye ustanovki dlis proizvodstva smazochnykh masel.
Moskva, Goa.nauchno-tekhn.izd-vo neft. i gorno-toplivnoi
lit-ry, 1959. 355 P. (HIRA 12:11)
(Lubrication and lubricants)

_Y
r,,),- e s 3 e sof 'ontinuous 'ihermocori -act frinsf.:)rr;al'_JOLI Of ~M-e ~'~il
c.-i ke
emr. -'.-lvrens, 30
:311britted at the .orl AY
C'une 1959. ":Cw -lork.

5(3)i '1(5) SOVI 52-59-7--10/31
AUTHORS: Molokancv, Yu. K., Skoblo, A. I.
TITLE: Mechanical Carrying-over of a Liquid by Gas in Plate Columns
(Mekhanicheskiy unos zhidkost-i gazom v tarellchatykh kolon-
nakh ) -
PERIODICAL: Izvestiya vysshikh uchebnykh zaveden--y. Neft' Ji gaz, 1959,
Nr 1, PP 45-55 (USSR)
ABSTRACT: The investigations referred to in publications (Refs 1-10) show
that the design of the plate in plate columns has a major effest
on the amount of liquid carried over. In the present article
this effect is more closely s 'tudied. In order to do so a model
of the plate was made of organic glass. The setup used is de-
scribed. With regard to the*effect on the carrying-over of the
liquid the plate designs may be classed in two groups: those
with a restricted and those with a free bubbling levels In the
first group the devices for introducing the gas into the liquid
take up only part of the liquid level on the plate. The bubbling
level is formed at 'the expense only of the liquid level not
covered by the above device. This group comprises all cap plate
Card 1/3 designs in which the caps are not submerged. The second group

SOV/ 152--59-1 -10/5,
Mechanical Carrying-over of a Liquid by Gas in Plate Columns
is that of bubbling plateB in which the dpvioes for introducing
the gas InTo 'the liquid are below the liquid level. In th!,s
case a.most all of the free liquid surface makes up the bubbling
level. In this gr,;up we find the net- and grid-plate8 of the
"YunIflaks" type. Formula (1) for -the determination of the amorit
of 1:quid ,arried over is given. The formilla. shows that wlthin
the range of air velocities of 1-3 m/sec the amount carried over
inoreaaes in proportion with the rate of flow of the gau. The
amount of liquid carried over is much greater when the"share" 7
of the bubbling level (i.e. the ratio between -the surface of
the bubbling level and the free surface of the column) is re--
duced: the innrease is proportional to 12. On tile basIs of the
evaluation of data found experimentally formula (2) wae dP-.v_'4e,1
from which the correction factor for various bubbling depths can
be calculated. Furthermore, formula (3) was obtained for the
correction factor in which the degree of dispersion of dropa of
the liquid is considered. Formula (4) is also given, byj4,vhi_,:h
the gas (steam) velocity can be determined, if the amount of
liquid carried over is known. It is shown that the grea:-t ad.-
Card 2/3 vantage of the plate with a free bubbling le-rel over the '~ap

SOT/1, 52-`-9,1;,.'.0 11,
blecham(.ai Carrying-.over of a Liquid by, Gas In Plate Columas
piate6 of regular design liles in the fa:~t that 7 is laxIger,
a1mcst '.. It is also shown that the output of a t-olumn is In-
creased by the 1-7-2-ft;ld if the cap plate J's replaced by a
P"ate wJth a free bubbling level (net- and gr-A*.d-.p'ates or
those of the "Yuniflaks" type). Eventually, the possibility of
obtainivg reliable data by the use Gf models of relative:y
small dimensions is shown. There are 4 figures, I table, and
10 references, 6 of which are Soviet.
ASSOCIATION: Mloskovskiy institut neftekhimicheskoy i gazovoy prmyshiannosti
im. akad. 1. M. Gubkina (Moscow Institfitoof -the Petroleum.-
ohemicai and Gas Industry imeni Academician 1. It. Gubk1n)
:9~8
SUBMITTED: Septemb-gr 2~.
Card 3/3

SOV/1 52-5 IQ -2-21 /N
Skoblo, A. I., Korneyev, Yu. X.
On the Calculation of Rectifyini,, Columns for E.-Itraction
Dictillation.,~ (K raschetu rektifikatsioni~yl:h I-rolonp. dlya
ekstralfts-ionnoy nera-ronkl)
T zvestiya vysshi'h uchebr.,ykh zavod-~niy. II,ftJ i -az,
V
195'~-,', 2, pp 83 - 97
Ac'.~: In 3pi te of the L
xto-sive use niade of e:ctraction distilla-
tion thcre are, Lis y.2t, no reliablo -~-.ethadz at hard for
the clalculation of rectifying columns. The mothod presented
0
in this article is based on the use of the commi-on activity
coefficient yo, which can easily be deter=ined by exp2=i-
on temperature.,
mentation. The dependence of the quantity 10
wh4ch is found experimentally, may further be u1scd for
many other calculations (Ref 8). The application of uni-
vers-ally valid methods for the calculation of the recti-
fyinl-, process of ideal binary mixtures (Ref 9) for the
ext raction distillation requires the d-2tormination of the
C'Ard 1,5' followin,", da"I-a: temparature and pressure in the column,

On Cali.-,Alation of PectiryinC Columns for Extraction SOV, 152-59-2-21/32
~)is ti I lations
coefficient of relative volatility and curvQ of phase
equilibrium, ~jeloction of boilinG point of the
initial fraction, selection of the third component. Tho
basic formula used for the determiliation of ter,:-eraturo
and pressure is the r,inerally known equation
which takes into account the deviation of Uc sy:3tein from
the laws of ideal solutione:
r(1 - z')Ao + PTz' =-T (1)
P and PT: elasticity of hydrocarbon vapora and the third
component at the tcm~,eratures of the systen; z' - molecu-
lar concentration of the third comporic-lat in the liquid
phase; T. - presoure ir. the column; YO - common activity
coefficient of the hy,trocarbon de;~et,dent oii the ter.1perature,
the concentration, azid the prc--jerti,.,r, of t"ic third co.',Illo-
nert (.-Ref 8). Tl;c- coefficient of relative Volatility K
i9 ,,letermined with suf'ficiert ;%ccur,',I(.y by ineans cf the
follwair.- forr.,,ula (Ref 8):
Card 2,/,~

On the Calculation of RectifyinE Columns for Extraction SOV/152-5,9-2-21/32
Distillations
P'xoi (2)
P2~'o2
'. 1: --
P 1 and 11 2 -vapor elasticities of the divisible components at
the particular temperature;X 01 and A o2 - their common acti -
vity coefficients. Due to the temperature differences between
tho upper and lower parts of the rectifying column the
co2fficient of relative volatility is variable. Thus it is
advisable to use the average of this coefficient U average*
The curves for the phase equilibrium are developed according
to the valueCK average found by meane of the curve equation
of the phase equilibrium of the binary system (Ref 9):
Y Xaverage x (4)
1 + N average - 1)X
x and y - subject to the concentration of the more volatile
Card 3/5 component in the equilibrium, liquid, and vapor phases. For

Or, the Calculation of rlectifyin*- ColUlMns for Extraction SOV/152-59-2-21/32
Distillations
determ-in-inc the higho.-it permissible boiling temperature of
the non-aronatic hydrocarbon the followine method is re-
com-iended. With values t w, z', and %2 chosen fron equation
(2), the varor elaotic-ity of the non-axomatic hydrocarbon in
the eliminatinC part of the column is determined:
P fA2 9 o2 P2 (5)
X01
Furthermcre, accordinG to the value P 1 found at the tem,.er-
ature tV its boiling point at 760 torr. is determined I.,y
means of equations or curves by Koks, Ashvort, Dyuring,
Dyuring-Treaubov (Ref 9) etc. The quantity of the third
component dope,.da on its concentration in the liquid phase
on the plates of the column z1, and on the quantity of the
phlegm required. It can be expressed in tLe followin-rr equation:
GI LY-1ZI (6); G, number of moles of the third
Card 4/5 T - Z, T

On the Calculation of Rectifying Columns for Extraction SOV/152-rq-2-21/32
Distillations
component; g' - number of moles of the phlegm. There are
9 references, 2 of which are Soviet.
ASSOCIATION: Mos'lovskiy institut neftekhimicheakoy i Caiovoy promysh-
lennoz;ti im. akad. 1. 1,1". Gubkina (moacow Institute of the
Petroleum Chemical- ar,4 Gas Industry imeni Acadc~,mician
I. I.1. Gubkin)
S UBIT I ~2 -:'E'D October 16, 1958
Card 5/5

MOLOKANOV, Yu.K.Ll
LYO BW .L 1. "
Determining the entrainment speed In plate columns. Izv. vvs.
iichob. zav.; neft' I gaz 2 no.8:55-61 '59. (MRA 12:11)
1.14oskovsn,7 institut rieftekhimicheakoy i gazovoy pron7shlennosti im.
akad. I.M. Gubkina.
(Petroleum--Refining)

SOV/7,--e -1 0--'1/40
.1 H C 7, S Vdovenko , V. ~a~. , Suglobov, D. 11. ,
ilutaal Solubility in the S-2y.9tem HNO H 0 n.Dibit,71
2 30 3 2

Z-RICLICAL: 1~59, Vol Nr 10,
Z!-,urnal nc,~r anicheskoy khi7,ii,
pp 2376 - 2379 WSSR)
A 22 T H A C T T~:e papers hitherto available on the distribation of nitric
acid bet,..f~en water and organic solvents (Rei's 1-4) contain no
data on the question, how much water passes over into the or-
.-~-anic solveni togLther with the acid. In order to clarify
w~-ether such solvents extract not only the acid b-It also acid
- t,=s, t,hle system mentioned in thc.- title was Jnvestigated.
-idra
The resjlts are suinlmarizea in -.-Ole 1 and figAre 1. ir,
crEasii- concentration of thi- acid in the aqueois :)~asse both

2e ar~anic
i's concentration and that of water increases in t~
~)hase. As fi-are- 2 shows, each acid molc-c-ile. takes along 0.6 up
to 0.15 -mclecales water of hydration according to t"le concentra-
tion. At icid concentrations in the ether above a di-stinct
~,,---ydation cf thc- etl,.er occ,.zrs so tlnat the isother= for such

Ca r d 1 j'2 -'n cL-n* rations were nct recorded. The distrib -.t ion of
c. C n

.-I: -I tI S - 111 ir, t 'ne Lyz tem HNO - H 0 - n.Di'b4tyl SOV/'78-.",- 10-31/,,o
E't-er at 250 3 2
nitric acid between water and Ether is illustra-ed -in
in the coordinate system
AV
2
lo- M log M- (m = concentration of the acid in water,
m-= concentration of the acid in fther, activity- coefficient
L +
of the ions H and 1%0 a.,,= activity of water in the a-aeoas
-jolution, h= hydratioA of"the acid in ether). At an aci"d cor,
centration of more than 0.5~',L in the ether a deviation from
Raoult's law can be observed. The negative deviation as it is
characteristic of uranyl nitrate solutions in or-anic solvent,
is preceded bY a chort period of positive deviation is
dat, to considerable interaction of th"e acid diuoles in the
E~thercal solution and indicates an association, of acid molecules
with the cther. The-rf~ aZ:e 3 fijures, 1 table--, 2nd 12 refer-
c-n-ces, 3 of which are Sov4L,.:t.
June 2, 1958
Card 2/2

GURVIGH, V.L. LdeceasedJ; SKOBLO. A.1.; SMIDOVICH, Te.Y.; ZAYTSEVA, II.P.;
KAZAIISKAYA, U.S.; PWROV, V.N.; SUVOTIOV, A.S.; SUCHMERHAKOV, A.A.
Continuous coking of heavy petroleum residues on powdered coke.
Trud.7 I-IIIaMiGP no.24:298-310 '59. (MIRA 13:3)
(Petroleum coke)

I A I 1 11 1 1 i I T I N 1.
!A apt R
I 'a :I

F'undamentals of Synthesis Technology (Cont.) SOV/4659
1. PreLiminary preparation of hydrocarbon gas mixtures 144
2. Purification from mechanical impurities 145
3. Purification from sulfur compounds 146
4. Removal of acetylene 150
5. Dehydration of gases 153
6. Division of gases into fractions (fractionation) 157
7. Extraction of the propane-propylene fraction and separation of
propylene from propane 159
Extraction of ethylene and ethane 163
9. Separation of methane 175
10. Adsorption stripping of gas mixtures 176
11. Same physicochemical problem of hydrocarbon gas fractionation 181
II. Division of liquid petroleum products into fractions (A.I. Skoblo
and V.A. Skoblo] 133
Adsorption 183
1. Nature of the adsorption process 184
2. Characteristics of adsorbents
19
3. Adsorption stripping of hydrocarbon $mixtures 1
4. Regeneration of adsorbents 187
Caz~~
/I

FRIDLAIM, M.I., inzh.;_SKCBLO, A.I., kand-tekha.nauk
I ----
-------
Modeling the process of the entrainment of particles from a
fluidized bed. 1h1m-vA4.~&,--Ao-5.-18-21 S-0 160. (MIRA 13;9)
(Fluidization)

MIDLAND, MJ.; ~IwiOs -A.I,_
Study of the proceso of particle entrainment frm a fluidized bad,
Izv. v-ys. ucheb,' zav.; neft' i 'gaz 3 no.1:71~78 160. (MMA 14:10)
IA, I-loskovskiy,institut neftekhimichaskoy i gazovoy promysh-
lennosti im. akad.,I.M. Gubkim.
(Petroleum-Refining)

ALEKSAM)ROV, I.A.; SKOBLO, A.I.
Studying the operation of demisters. Izv. vys. ucheb. zav.;
neft' i gaz 3 no.4:73-490 160. (MIRA 15.6)
1. Moskovskiy inatitut neftekhimicheskoy i gazovoy promyshlennosti
akademika I.M. Gubkina.
(Oil refineries-Equipment and supplies)

FRIDLANDI M.I.; SKOBLO, A.I. --
Failing of particles through a grid tray. Izv. vys. ucheb. zav.;
neft' i gaz 3 no.9:97-101 160. (MIRA WO
1. Moskovskiy institut neftekhimichaskoy i gazovoy promyshlennosti.
(Gas flow) (Plate towers)

FAMEV, I.G.; RAZLU4,OV, I.M.; SM)BID, A.I.; CHFFUTIOV, O.A.
Porosity of a layer of granular material in continuous motion
in a stand pipe. Izv. vye. ucheb. zav.; neft' i gaz 3 no.11:
67-70 6o. (HIRA 14:1)
1. Moskovskiy institut neftldiimichoskO7 i gazovoy promyshlennosti
imeni akademika I.M. Gubkina, Giproneftemash,
(Catalysis) (Porosity)

AI-EKSANDROV, I.A.; SKORk). A.I.
Mechanical en-trainmentOf liauid by gases from perforated-ty-pe
plates. KhimA tekh.toplA nasal 5 no.9:42-45 S 16o.
(MIRA 13:9)
1. Moskovskiy institut neftekhimicheakoy i gazovoy pronyshlennosti
im.akad.Gubkina.
(Plate towers

~-SKOBLOJI A.I.; ALLIKSANDROV, I.A.
Effect of the entrainment of liquids on the number of plates in
rectification columns. Trudy 141,',IKHiGP no.28;80-92 16o.
(Plate towers) (MIRA 14;4)

FRIDLANDY M.I.; SKOBLO., A-.I-. __
Mechanical entrainment of particles by a gas in apparatus coptaining
a fluidized bed. Trudy MUOUP no.28:93-101 160- IMM4 .14*4)
(Fluidization)

MOLOKANGV, Yu.K,,;-SKODWY AI-I-
Hydrauli,-. calculation of slots for plate-column bubbling caps.
irys. u,--heb. zav,; neft' i ga-z 3 no.7:77-83 160. (MLRA 15%5)
1. Moskov3kiy institut neftekhirdoheskoy i gazovoy
proiwjshlennosti imeni akatlemika I,M., Gubkina.
(Plate towers)

BAGATUROV, Sergey Alekoandrovich; PLANOVSKIY, A.N., doktor tekbn. nauk,
prof., retsenzent; SKORLOI_~J.) dots. retsenzent; TREGUBOVA, I.A.,
dots., retsenzent; BABUSHKTNA, S.I., vedushchiy red.; POLOSINA,
A.S., tekhn. red.
[Theory and calculation of distillation and rectification] Teoriia i
raschet peregonki i rektifikatsii. Moskva, Goo. nauchno-tekhn. izd-
vo neft. i gorno-toplivnoi lit-ry, 1961. 435 Pe (MIRA 14:10)
(Distillation-Tables, calculations, etc.)

ALEKSANDROV, I.A.; -SKOBLO, A.I.
Choosing the amount of fluid entrainment between plates in rectification
columns. Izv. vys. ucheb. zav.; neft' i gaz 4 no.3:53-59 f6l.
(MIRA 16:10)
1. Mookovskiy institut neftekhimicheskoy i gazovoy promyshlennosti
Im. akademika I.M.Gubkina i Gosudarslt*ennyy nauchno-issledovatell-
skiy i proyektnyy institut neftyanogo mashinostroyaniya.

MOLOYANW, Yu.K.; SKOBLO, A.I.
Value of the resistance coefficient of a dry LubUe cup plate.
Izv.vys.uchet,.zav.;khimA khim.tekh. 4 no.4:672-675 '61.
(ULIRK 15: 1)
1. 'eloskovskiy institut neftekbimicheskoy i gazovoy promys~lennosti
impni- I.H.Gubkina, kafedra neftezavodskogo oborudovaniva.
(Plate towers)

KHAMDI, A.M.; 14,01,0KANOV, bi.K.; 3KOH1.0, A.I.
Amount of thr.- Intftal flow of' 11(pild ovar a woIr dosincomer. 17.V.
Vs. ucheb. zav.; neftl i gaz 4 no.12:89-94 161. (19RA 16:12)
1. Moskovskiy institut neftekhimicheskoy I gazovoy promyshlennosti
imeni akademika Leningrad.

FADEYET, I.G.p inzh.1 RAZUMOV, I.M., kand.tekhn.nsukj,SKOBLO, A.I.t kand.tekhn.
nauk; CHEFIRANOV, O.A.0 inzh, RUNINVICH, K.A.'I---ki6a.tekhn.nauk .
Calculation of pressure loss in the transport of a granular
material in a continuous flow. Dim.mash. no.2:26-28 Mr-Ap 161.
(MIRA 14:3)
(Pneumatic-tilbe transportation)

FAIDLAND, m.j.; RAZUMOV, I.M.; SKOBLO, A.I.
Calculation of the amount of particles entrained by a gas in an
apparatus with a fluidized bed. Khim.i tekh. topl.i masel 6 no,2:
36-38 F 161, (MIRA 14:1)
1. Moskovskiy institut neftekhimicheskq4. i gazovoi promyshlennosti
im.akad.Gubkina i Giproneftemash.
(Fluidization)

SKOBLO,-A.I.
Reflux systems of rectification columns. KhIm.i teMi* topLi masel
6 no.2:64-65 F 161. (MIM 14:1)
(Distillation apparatus)

MODDKANOV, Yu.K.; ALEKSANDROV, IOA.; ~KOBLO, A_I._.
Experimental investigation of turbogrid-type plates. KUM. i takh.
topl. i masel 6 no. 5:34-38 My 161. (MIRA 1-4:5)
1. Moskovskiy institut neftekhimicheskoy i gazovoy promyshlennosti
im. akademika Gubkina.
(Plate towers)
&S ..a&

AEROV, M.E.; GORECHENEOV, V.G.; MOLOKANOV, Yu.K.; SUM-Sh"D., L.Ye.;
A.I.; KFIALIF, A.L.; BROZIN, I.A.; SATTAROV, U.G.
Effectiveness and maximum loads of industrial absorbers with various
bubble trays. Gaz. prom. 6 no-11:3-5-38 '61. (MIRA 15:1)
(Mass transfer) (Plate towers)

SKOBLO., Aleksandr Ionovich.-dots.; TREMBOVA, Irina Ananlyevnaj, dots.;
~HOV, Y~Uolay Nikolayevich, dots.; BOIMARENEO, B.I., kand.
tekhn. nauk, retsenzent; BABUSHKVIA, S.I., ved. red.;
KLEPr'_9-TOVA) K.F.J. ved. red.; POIDS131A, A.S., tekhn. red.
[Processes and equipment of the petroleum refining and petro-
chemicals industries] Protsessy i apparaty neftepererabaty-
vaiushchei i neftekhimicheskoi prorgshler-nosti. Moskva, Gos.
nauchno-teIchn.izd--vo neft. i gorno-toplivnoi lit-ryp 1962.
652 p. (Petroleum-Refining) (MIRA 15:2)

ALEKSANDROV, I.A.; SKOBLO) A.I.
MaIn characteristics and application fields of plates of varioUB
design in rectification and absorption col=ns, Khim. i tekh. +op3.
i masel 7 no.1:45-50 Ja 162. (1421 15: 1)
1. Gosudarstvennyy nauchno-Issledovatellskiy i proyektnyy institut
neftyanogo mashinostroyeniya i Moskovskiy institut neftekhimicheskoy
i gazovoy promyshlennosti im. akad.Gurkina.
,(Plate towers)

ALEKSANDROV, I.A.;__~K(~BLO,_.A.I.
Determination of the amount of liquid carried off between plates
in rectification columns. MAm.i tekh.toplei masel 7 m,8:53--58
Ag 162. (MIRA 15:8)
1. ~bskovskiy institut neftekhimichaskoy i gazovoy promyshlennosti
im. akad. Gubkina.
(Plate towers)

-, - , . " ., ....... -,.- , --.- . -
KHAK)1, A.M.; SKOBLO, A.I.; MOLOKANOV, Yu.K.
Determination of overflow head fn plate columns. 1zv.vys.ucheb.zav.;
neft' i gaz 5 no.12-53-57 (~MRA 17:4)
1. Moskovskiy institu-~ nel'tekhimiche3koy i gazovoy promynitlennost-4
imeni akademika I.M.Gubkina.

ADELISONP Soflya Valerlyanovnit; �KOPLO.,__k.;,, dots,, reteenzent;
KLEYMENOVA, K.F., ved. red.; LEVINA, Ye.S., Yed. red.;
VORDNOVA, V.V., tekhn. red-
(Processes and units used in petroleum refining and
petroleum chemistr7] Protsejay i apparaty nefteperera-
botki i neftekhimii. Moskva, Gostoptekhizdat, 1963. 309 P.
(MIRk 16:5)
(Petrolewn refineries--Equipment and supplies)

GORLOV, V.F.; SKC)hLk), A. I.
Tube stilla with a fluidized hed of' powder fuel. Nefteper. i
neftekhim. no. 11:42-46 163. (1,101 17:5)
1. Mo.-kcvukiy institut neftekhimicheakoy i gazovoy promyshlennosti.

ALEKSANDROV, I.A.; SKOBLO, A.I.
Determination from the thermogram of the number of rectification column
plates taking the entrainment of liquid into account. Izv.,rys.ucheb.
zav.;khim.i khim.tekh. 6 no.4:675-682 63. (MIRA 17-.2)
1. Moskovskiy institut neftekhlmicheskoy i gazovoy promyshlennosti Im.
Gubkina. Kafedra neftezavodskogo oborudovaniya.

KHAMj,i, A.M.; SKOBLO, A.I.; tiOLOXANOV, Yu.K.
Problems of' the hydraulics of overflow apparatus in plate columns.
Khim.i tekh.topl.i masel 8 no.2:31-37 F 163. (MIRA 16:10)
1. Moskovskiy institut neftekhimicheskoy i gazovoy promyshlennosti
Im. akademika Gubkina.

GORLOV, V.F.; SKOBLO, A.I.
Properties of a fluidized bed of coke in combustion. Khim.
i tekh. topl. i mauel 8 no.9:11-16 S '63. (MIR-4 16-.n)
1. Moskovskiy institut neftekhimicheskoy i gazovoy
promyshlennosti im. akademika Gubkina.

GGRUN Y V. F. ; A. i .
Change Iri the provertiea of powderud crkm on c(xibul3flon In a
fluidized bed. Trudy MINYMU no.44:258-267 163.
(Mill-A 18: 5)

MIKIIAYLOV, P.J.; SKOBDD., A.!.
Organizing the movement of gases in tubestill beaters. Trudy
MINKRGP no.44:278-284 '63. (MIPA 18:5)

KU1,1LEYLT, M.A.; SKOBLO, A.I.
Determination of the maximum rate of the countercurrent contacting
of liquids with fine-grained materials. Khim. i telffi. topl. i
masel 8 no.12:18-21 D 163. (MIRA 17:1)
1. Vsesoyuznyf nauchno-issledovatellskiy institut pL per---rabotke
nefti i gazov i polucheniyu iskusstvennogo zhidkogo topliva.

I t 1 -1 11 11 1 1 . 1-1 . 1. 1"! f., I 91111f 'JIVII -4 111- pallp, 11.
11H i , 11 . ., : . ; , ; -;, ; ", " ,A . I . ; .1111( ; J POY , D, . 11 11 .
t ti I or. I 1 1 (,ra Loi comp or urany I. Pad 1,,Alzi I a 0 rv, .~,:
'~~4. (111RA 18:2)

~.t"LC'7 , S A
-at pxf.%. -a n ~.7~e I n ai"dd ized bed ~~, tw.: - r a- ~,as rlow and th e
part ic les o~ a ~,:olid heat carrier. iz-. . uchp-~,- . zav.
nef t i r-az P nr . 3 : 59-62 5 -
t7'
instit-ut tic- teZh

a~IHTDZIWIOV, Rauf Tairovich; SKC)BLO,.,,A.I., profop retsenzent;
,IEY~ENGVA, K.F., red.
[Frinciples of technological calculations in petroleur,
refining] Osnov7 tekhnolocicheskikh raschetov v nefte-
0
pererabotke. Yoskva, Khimiia, 1965. 543 p.
(MIRA 18:10)

4 %0 111 so w N III b If 0 If 4 41 u 41
Vu a
14 L~_A_ L CA AV u
111 440 W LfIlli._
O.D1 'L4!t-
801141311 113094M71111- V It 0 1 1
'06 ri4orp,
or
0- ~losp so
wallmil.
)IMIAVI 241. 'A M.4
'101111"Iff
p.%WpAji u4.bq %,Pq t"jvju~Ksjjaj),j
oir copmaimni'll'I"llp jo) IMA&P PAW" vmowy
_. #A.4. .itli-fX4.
imi, 0., 1r ist-t f. I -
A A I I v I
W7.0ols fro it clot* it It it If
Al~

POPOV, V.I. DOBROMDOV~ L.L.. SWITIKOV, V.N.; A J.P.
NMYZ7
MMUSKIY, G.M., professor, reteenzent; SKOBLO,..--P.J-. Imudl-
dal takhnicheek1kh nauk. retmenzent; SXRX6itl']~.V., kandidat
tskhnichesklkh nauk, reteenzent; IZRAIISTICH, L.A., inshener,
re~eenzeut; HAMOVA, Ta.r., redaktor; DMVKINA, N.A., takhni-
chook-ly redaktor.
[Technological equipment for fermentation industries] Tokhno-
logicheekoe oborudoTanle brodtllnykh proizvedsty. Kooky&,
Pishchapromizdat, 1953. 515 P. (MLRA 7:8)
(Pistilling industries) (Brewing industrlea)

Io"Continuoui process for production of alcohol fromyo,
A. F. Berenshttln D I S-ko-blo and S P. Guly3ev. ",Ny
Kiev. FINCIC Spi,rhi, r
krom. 1053, No. 1, 0"7; Refem~. Zhw., Xkin. 1054, r.
968-h.-In-6 - m -tan C.,
e outlined prnce--s the Ist fermenta-tu..
-used for- growing yeast. 77te continuotu fermentation is~,
carried out in 2 stages. In the In of which, compriiint 54
tanks, the grrattr part of the sugar is fermented; Abe fer.41
mentation Is finblied in suemsive tanks which are of smaNr
capacity. Through these tanks the mash is circulated for.
cibly at a rate 3-4 times faster than In the Ist stage. fit
this process the sirup is acid-sterilized in place or meam.
This method of production jrAve a higher yield of tile. pet
ton of starch and resulted in comsiderable economics of water#
M_ lf-
Sun- s, and manpower.

III , I lir .1 ., v[ I T:l . F I 1 11 Iq 1-1. , ". " .. , . ".,. - " . ,
f t", RE 0-. 0 1- i i ~ 4 i ; I . I ; . 11 ;; -~ , ~, -i I !-' " j. ~ 11 IF I ~c 141 i ! 1H P, H PI 1 41 .ww~~~
L

ARONOVIGH, Vladimir Veniaminovich, kandidat tekhnicheskikh nauk; KUZIMTSOV,
reteenzent; SMWIN, P.V., spets
M.H., reteenzent; MEW D.A
redaktor; KASLOVA, fel.-, -'3' tor; GCTLIB, H.M., tekhxticheakiv
redaktor
[instruments
reguliatory
300 P.
and regulators in the distilling industry] Pribory i
spirtovol promyshlennoati. Moak-va. Pishchapromizdat, 1956.
(MM 9:12)
Platilling industries-lquipment and supplies)