SCIENTIFIC ABSTRACT AGRONOMOV, A. Y. - AGROSKIN, A.A.

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• Collection: Scientific Abstracts
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• Sequence Number: 20
• Publication Date: December 31, 1967
• Content Type: SCIENCEAB

SOV/20..124-3--37/67
The Influence of Various Factors Upon the Size of the Specific Surface
and on the Porosity of Chromium Catalysts
during pressing and drying. These fcrms are not different
crystal modifications, for both are radiographically amorphous.
The production of the hydroxide in ono or the other form de-
pends exclusively on the rate of formation of the precipitate
obtained. If the concentrated mixtures are mixed rapidly, a
greyish.-blue hydroxide precipitate forms immediately, but if
the precipitating agent is added very slowly (in drops) to
the diluted chromium-salt sclution,, the precipitate may dis-
solve, thus forming soluble basic chromium salts, which,
after a further addition of the precipit-ate, furnish a dark
green chromium hydroxide with different properties. The in-
vestigation carr" ad out showed the following: The different
coloring and the different properties of the hydroxide are
caused by the fact that the catalyst formed after dehydro-
genization of the black hydroxide have many fine pores,
whereas by hydrogenization by means of blue hydroxide no
pores are formed. As an example, the isothermal lines of
Card 2/4 various preparations are given. By variation of the rate

SOV/20-124-3-37/67
The Influence of Various Factors Upon the Size of the Specific Surface
and on the Porosity of Chromium Catalysts
of precipitation, preparations of various coloring (from
greyish-blue to dark green) may be obtained, and this
may easily be explained by the different de sea of porosity.
A prolongation of thermal treatment (at 45015 from 2 to
8 hours reduced the specific surface from 70 to 25 m 2/g,
and caused the pores to disappear nearly entirely. The aging
processes of the hydroxide and the increase of precipitation
temperature donduciv~i to tAhese PMMSSP~.s reduced the specific
surface and the weigh", of 1 cubic meter of the dry granular
substance of these preparations. There are 1 figure, 2
tables, and 5 references, 3 of which are Soviet.
ASSOCTATION: Institut obshchey i neorganicheskoy khimii im. N. S.
Kurnakova Akademii nauk SSSR
(Institute for General and Inorganic Chemistry imeni N. S.
Kurnakov of the Academy of Sciences, USSR)
Card 3/4

50) SOV/20-127-2-25/70
AUTHORSt Agronomov, A. Ye., Balandin, A. A.t Academician, Mardaehev,Yu.S,
TITLE: Comparison of the Kinetic Relative Adsorption Coefficients
With Those Determined According to the BET Equation
PERIODICAL: Doklady Akademii nauk SSSRI 1959, Vol 127, Nr 2t PP 325-328
(USSR)
ABSTRACTt The BET equation of the polymolecular adsorption which takes
into account the interactions between adsorbent and adsorbed
substance in the first layer and is related to the entire
surface was derived in reference 1 (1938) (1). its graphic
solution makes the determination of the adsorption coefficient
(AC) o possible. The second author in 1942 (Ref 2) derived an
equation of the kinetics of the monomolecular reaction in a
discharge system. A calculation method of the relative
adsorption coefficient from kinetic data is given as well.
This method made the determination of the value of these
coefficients on the catalytically active centres of the
surface possible, The equation (2) (identical with the'equation
(52) in reference 5) may be used for the determination of the
Card 1/4 relative adsorption coefficients from kinetic data.It was

Comparison of the Kinetic Relative Adsorption SOV/20-127-2-25/70
Coefficients With Those Determined According to the BET Equation
interesting to carry out the comparison given in the title.
The absolute AC differ according to reference 7 by two orders
of magnitude. The authors used the dehydrogenation reaction
of oyclohexane on Ni-catalysts (the latter on carriers). The
BET-AC were graphically determined from the equation (1).
The straight lines for the catalysts Nr 1 and 2 (Table !) are
given in figure 1 as an example (5 catalysts were used and
their method of production is described here). AC according to
BET (a BET) for benzene and cyclohexane were computed from the
tangent of the angle of gradient of this straight line; their
relation could be called the relative AC-BET (zBET) (Table 1 t
columns 1-3). The kinetic relative AC tere determined from the
equation (2). The reaction mentioned was carried out according
to the method of reference 10. The catalyst was used in a certain
quantity (volume V)-3o that the transformation did not exceed
30%. The equation (2) was transformed into (3) in the
experiments with pure cyclohexane. Furthermore, the experiment
Card 2/4 was carried out with a mixture (with benzene) at the same

Comparison of the Kinetic Relative Adscrption SOV/20-127-2-25/70
Coefficients With Those Determined According to the BE? Equation
temperaturet then again with pure cyolohexane. This experiment
confirmed the observation of reference 11 that the activation
energy is not changed up to a mixture containing 104, benzene
for the catalyst Nr 3). The two series of the values
AC according to adsorption-, kinetic data respectively) are
~
very adjacent in the columns 3 and 4 of table 1. Thus, the
BET equation may be used in the case of the cyclohexane
dehydrogeriation (Pig 1). The general equation of the kinetics
of the monomolecular roactions (Ref 4) holds as well in the
investigated region of the mixtura composition, as It follows
from the constancy of z (Table 2). The relative AC of the
catalytic active centers tirrn out to be practically equal. to
the relative AC of the ent-Ire surface. The fact that zk and
Card 3/4

Comparison of the Kinetic Relative Adsorpti:i-n SOV/20-127-2-25/70
Coefficients With Those Determined According to the B.42 Equation
zBET are equal is *assumed to co:Lfirm the second author's
statement (Ref 12) that the pla,'ee with a mean adsorption
intensity are catalytioally Tbere are I figurer
2 tables, and 12 refe'renoe-i~ of which are Sovket.
yy iinli,ersitet !~M. 11. V. Lomon,~sova
ASSOCIATION: Moskovskiy gosudaTstvenr,
Noscow State University imeTC Lt. V,Lomonos-c-v)
Institut organicheskoy khim-11. .1-n. N. D. Zelinskoec Akademii
nauk SSSR
(Institute of organic Chemistry imeni N. D. Zel.inskiy of the
Academy of Sciences, USSR)
SUBMITTED: April 299 1959
Card 4/4

A
i) 0
AUTHORS: Fneydlin, L. K~i-, Balandlrl, A. A., Borunova, N. V
TITLE: Concerning Connections Bet-ween the Microstructure of
Aluminum Oxide and Activity of~' Ntekel-Alumina Catalysts
of Various Nickel Content
PERTODTCAL: I zvestlya Akadem' ' naul~ SSSR .Otdelenilye k1himAcheskikh.
nauk, 196)0, Nr .1. op USSR)
-17ts of ~r.vestigatlons of
ABSTRAM This paper presento the resi
the connection between the micros-Iructure of alumlnurp
oxide and actIvIty of nickel-alumina catalysts of
various NI content. T'he ca'---alysts .%,ere prepared by
impregnation of allumina with NI(NO 5);~- and reduction,
0. he ca"-alysts I
At Witt! H-, at -550 The alumina for t,
and 2 ~See T"able) was prepaved by Ign'tion of com-
0
mercial aluminum oxIde at 500.Al'amina for catalyst
3 was prapared by treatmert of A!," wtth arrmonia.
SU.' Card 1/4 Activity of the catalysts v.1as de*~errr.,I--~d by the degree

th,0
I I IT 0 y~
of' Willow; Colltollls
:111
C a rc.l.
"J
SOV/62-6o

175 20- 101)

15

1 -,1) 25 - I Oil -2
oo

--Ov III
2'
25
10
Ke,
I y
4-o Table on Cari

Conaernlnf~ Comiections Bet,wreen the (80-,~8
01, Alurillnum 071(ie ami SDOV/62-6o-1-4/37
Activity of' Nick-el-Alumina Catualysts
of' Vavloiu,, Nickel Contont
Key to Table 1: (a) number; (b) experiment; (c) sample
of alim-Inum oxide- e t (e)
., ((O'Ni content -in t by w Igh ;
durLation of reduction *.%,1th 112 in hr; (1') specific
surface io-in 2/g; range of pore silze In A; (h)
11""i-ximum J11""tribution of' volumes of pores along the
radivis in A; (I) total amount of benzene absorbed on
saturation.. In millimoles/g; (J) degree of cyclohexane
dehydrogenatiot; in % of theoretical.
Card 4/4

AGRONOMOV, A.Ye.; MARDASHEV, Yu.S.
Selective determination of Vie nickel surface in nickel-aluminum
oxide catalysts, and their specific catalytic activity. Vest.Mosk.
un.Ser. 2: Khim. 15 no.1:25-34 16o. (MIRA 13:7)
1. Kafedra organichookogo kataliza Mookovskogo univeraitata.
(Catalysts, Nickel)

AGROIIOTY,_"Y -*-; MISHCHEIIKO, A.P.
1: --
Dependence of the catalytic activity of the catalyst Go/SiO~ upon
the porosity of the catalyst. Report No.4. Vest.Mosk-.un.Ser.
2: Khim. 15 no.1:35-39 16o. (MIRA 13:7)
1. Kafedra organicheskogo Imtaliza Moskovskogo universiteta.
(Cobalt) (Catalysts)

AGRONOMOV A.Ye.
Synthesis of p-tolueneBulfonic acid. Vest.Mosk.un.Ser. 2: rhim.
15 no.3:78-79 My-Je 160. (MIRA 13-8)
1. Kafedra organicheakogn kataliza Moskovskogo universiteta.
(ToluenOBUlfonic acid)

800M
AUTHORS: AAronomovg A. Yo., Balandin, A. A., S/02 60/131/05/038/069
Yu. S. B004YB014
TITLEt The Dependence of Activation Energy on the Relative Adsorption
Coefficient
PERIODICAL: Doklady Akademii nauk SSSR, 1960, Vol 131, Nr 5, pp 1120-1122 (T"SSR)
TEXT: The authors of the article under review studied several nickel catalysts
within a wide temperature range, using dehydrogenation of oyclohexaneA The same
amount of nickel was applied to different carrier substances (A12019 silica gel,
kieselguhr) in equal proportions by weight. The data listed in tab e I indicate
that the apparent activation energy, Q, calculated from the Arrhenius equations
and the relative adsorption coefficient, z2, of the benzene being formed are
greatly dependent on the nature of the carrier substances These two quantities
are interrelated by Q - E - klogZ2 (E and k are constants). This relationship is
graphically represented in figure lo For all catalysts under consideration it
was found that E-was constant and U kcal/mole approximately. This value cor-
responds to the initial coordinate of the straight line depicted in figure 1,
and thus represents the true activation energy. For nickel applied to silica
gel (second sample) it was found that the value of z2 increased in dependence of
Card 112

800()?
The Dependence of Activation Energy on the Relative S/020/60/131/05/038/069
Adsorption Coefficient B004/BO14
the benzene content of the starting mixture Of C696 + C6H12 (Table 2, Fig 2).
Proceeding from results obtained by other research workers, the authors discuss
this dependence and arrive at the following conclusion: As long as the dehydro-
genatiOn Of C6H12 by means of a nickel catalyst takes place at active points of
mear. activation energy, which are moderately covered with C6H6, z2 does not
depend on the yield, m. However, as soon as these points are covered with a
larger amount Of C6H6, the benzene has an inhibitory effect, and the relation
z2 " f(m) occurs, as may be seen when using catalysts with great values Of z2,
Taking this into account, one obtains a value of E for the second sample, which
is in close agreement with the E-values of the other catalysts. Graphical
solving of the relation Q - E - klOgz2 is recommended as another variant. The
authors refer to a publication by A. A. Balandin and Yu. K. Yurlyev (Ref 10).
There are 2 figures, 2 tables, and 12 references, 10 of which a7e Soviet.
ASSOCIATION: moskovskiy gosudarstvennyy universitet im. M. V. Lomonosova
(Moscow state University imeni M. V. Lomonosov) Institut organi-
cheskoy khimii im. F. D~ Zelinakogo Akademii nauk SSSR (Institute
of OrRanic Chemistry imeni 1. D. Zelinskiv of the keademy-of-
olences
SUBMITTED: December 28, 1959
Card 2/2

81402'
S/020/60/132/06/24/068
B011/B126
AUTHORSt Agronomov, A. Ye., Luzikov, V. N.
TITLEs An Investigation of the Catalytic Properties of Pyrophoric
Manganese f\
IV
PERIODICALs Doklady Akademii nauk SSSR, 1960, Vol. 132, No. 6,
PP- 1315 - 1318
TEXTs In order to obtain pyrophoric manganese black, the authors used the
method described in Refs. 1, 2, 6, and 7. To do this, manganese amalgam
was thermally decomposed in a vacuum. The amalgam is obtained by the
electrolysis of an aqueous solution of manganese chloride on a mercury
cathode. The manganese black produced is covered with absolute benzene iA11(
a vacuum, to preclude the introduction of air. The authors then tested the
purity of the black obtained, while they used mercury with an '9203 con-
tent as cathode in an additional experiment. Manganese obtained in the
above manner is of high chemical activity. There is an exothermic reaction
with ignition when abydrcgen-air mixture is drawn through a freshly produced
Card 1/4

MOT
in investigation of the Catalytic Properties of S/020/60/132/06/24/068
Pyrophoric Manganese B011/B126
sample. The authors have established from the roentgenograms of manganese
black, that a-manganese is produced on the decomposition of the amalgam,
which crystallizes into a complicated cubic lattice of the type A-12
(a-parameter - 8.923 :t 0.020 1). The authors say that this lattice is
less tightly packed than in metallic manganese. The roentgenogram showed
no lines of manganese oxide or its other compounds. As pyrophoric
manganese is oxidized by 'H 20, C029 and even CO, as well as by oxygen, the
authors have restricted themselves to the hydrogenation and dehydrogena-
tion of hydrocarbons. k continuous system with an automatic filling
device was used for the experiments. 23-23.5 ml of manganese black was
brought into the tube without being touched by air. Benzene and air
were removed from the system aA low temperature for two hours by de-
oxidized hydrogen. Cyclohexene'was dehydrogenated 0 0
,,,at 32 -400 C. The
gaseous products analyzed on the BTM-(VTI)device'Xcont&ined, apart from
98-5-99.5~ hydrogen, 0-5-1.5% saturated hycIrocar ons. The ultraviolet
absorption spectra of the catalyst showed, apart from the cyclohexene
used, the presence of benzene. Cyclohexadiene frequencies were not
present. The activity of the catalyst was not stable during the first
Card 2/4

Moz
An Investigation of the Catalytic Properties of S/020/60/132/06/24/068
Pyrophoric Manganese B011/B126
four or five experiments. Only in later ones were reproduceable results
obtained (Table 1). From this it follows that hydrogen does not form on
manganese black only by dehydrogenation of the cyclohexene. The
stabilized catalyst is far less active than a freshly produced one. The
authors believe that no parallel, irreversible catalysis occurs here,
The lattice of the catalyst was somewhat strengthened (according to 1A.
roentgenogram) after eight experiments. There were no manganese oxide
lines here, either. Thus newly produced manganese black, not only catalyzes
the dehydrogenation of cyclohexene, but also cracks it. Manganese carbide,
and an additional quantity of hydrogen are formed. Cyclohexane is neg i-
gibly dehydrogenated at 440-50000, forming cyclohexene. Etql-benzene~is
partially cracked between 300 and 450 0C. Carbon and hydrogen are formed.
Neither benzene nor eyelohexene are hydrogenated between 150 and 215 0C.
There are I table and 13 references$ 5 Soviet, 1 German, 1 French,
1 British, and I US.
ASSOCIATIONs Mookovskiy goBudarstvennyy universitet im. M. V. Lomonosova
(Moscow State University imeni M. V. Lomonosov)
PRESENTEDi February 11, 1960, by A. A. Balandin, Academician
Card 3/4

KLABUNOVSKIY, Ye.I.; VOLKOVA, L.M.;.AGRONOMOV, A.Ye.
New method for obtaining stereospecific silica gels. Izv.AN
SSSR.Otd.khim.nauk no.11:2101 N 161. (MIRA 14:11)
1. Institut organicheskoy khimii im. 'R.D.Zelinskogo Ali' SSSR.
(Silica)

..,AGRONOMOV _AlYej-. LIN LI-DAN (Ling Li-tang]
Activity of copper catalyst as influenced by the structure bf silica
gel used asI icarrle.r. Report 6. Vest.yoak.Un.Ser.2: khim. 16 no.6:
53-61 N-D 161. '(MA 14: 11)
1. Moskovskiy" goaudarstvennyy universitet. Kafedra organicheskago
katalizd.
. (Catalyst, Copper) (Silica)

A-GRONMOV) A.Ye.; MARDASHEV, Yu.S.
Structure 4nd activity of supported nickel catalysts. Part 1:
Structural changes of the catalyst support during the deposition
of nickel. Zhur.fiz.khim. 35 no.8-.1666-1671 A 161,
tmi~ .14:8)
1. Moskovskiy gosudarstvennyy universitet imeni M.V. Lomonosova
i Institut organicheakoy khimi AD SSSR imeni H.D. Zelinskogo.
ZN-ickel) (Catalysts)

AGRONOMOV A.Ye.; ILWASHEV, Yu.S.
Structureand activity of supported nickel catalysts. Zhur.
fiz.khim. 35 no.9:20477-2051 161. (MIRA 14:10)
1. Moskovskiy gosudarstvemyy universitet imeni M.V. Lomonosova
i Institut organicheskoy khimii AN SSSR imeni N.D. Zelinskogo.
(Nickel) - (Catalysis)

BALANDIN., A.A., akademik, red.; KOJ30ZEV; N.I., prof.p red.; LEBMhWp
V.P., dato*p iarn. red.; MALITSEV, A.N., zam. red.; AGIOI.'OEg,-
A.Ye dots,, zwe red.; TOPCIIIYEVA, K.V., prof.., red.; YURIVEV,
-Tu-.K.i prof., red. PAUCIMOV, G.M., prof., red.; SOKOLISKIY,
D.V.0 akademikt red.; VOLIM'SHTLYN, F.F., prof., red.;LAMMIA,
L.V., tekhn. red.
[Catalysis in the institutions of higher learning; papers of the
First Interunivensity Conference on Catalysis)Kataliz v vysshei
shkole; trudy. Moskvap Izd-vo York. univ. No.l. Pt.2. 1962.
325 P. (KMA 15:10)
2. MezhvuzovA6y'6 soveshchaiiiye po katalizu. Ist, 1958, 2. Aka-
deraiya nauk Kazakhskay SSR (for Sokol' skiy)w-3.-Kb:bdt-hnkiy fa-
,,,kulltet Moskovskogo gosudarbtvonnogo universiteta (for Yurlyev).
(Catalysis)

1~ 89/62/0
00/002/001/004
D228/D302
AUTH01ZS: and Mardashevp YuoS.
TITLE: Selective assessment of the surface areas of metallic
catalysts on carriers
PERIODICAL: Moscow. Universitet., Veqtnik. Seriya Ut khimiyat
no. 2, 1962, 21 - 22
TEXT: The authors give more precise information about their previ-
ous study of the chemisorption of phenol. This shows that the diffe-
rence in the size of the Ni part of the surface of the Ni/A120 3 ca-
talystf calcd. by the method of direct detn. and by the method of
comparing the,chemisorption capacity of thiophenol on Ni-black,
A1203t and Ni/A'203P amounts to only 15 %. Thus, it is concluded
that the method of comparison can be used to estimate selectively
the size of the Ni surface in "'/,A'203 catalysts. There are 1 table
and 8 references: 4 Soviet-bloc and 4 non-Soviet-bloo. The referen-
ces to the English-language publications read as follows: P#H-
Card 112

S/189/-62/000/002/001/004
Selective assessment of the surface ... D228/D302
Eimett et alp J. Amer. Chem. Soc. 59t 310# 1937; F.N. Hill et alp
Ibid. 71t 2522t 1949; L. D'Or et alp J. Chem. Phys., 51t 467? 1954;
P.C. Tompkins, Disc. Faraday Soc- 54t 548t 1958.
ASSOOIATION: Kafedra orE;anicheskogo kataliza (Department of Organic
Catalysis)
SUB14ITTED: May 8 p 19 61
IV
Card 2/2

BALANDIN, A.A., akad., red.; KOBDZEV, N.I., prof., red.; LEBEDEV,
V.P.) dots., zam. red.; MALITSEV, A.N., dots., zam. red.;
AGRONMW,_4_Ys., dots., zam. red.; GRO14DV, V.N., red.;
,AZAREVA9 L.V., tekhn. red.
[Transactions of the First Intemniversity Conference on
Catalysis] Trudy Mezhvuzovskogo soves.hchaniia po katalizu,lst.
Moskva, Izd-vo Mosk, univ. No,l. Pt.l. 1962. 475 P.
(M,IRA 16:7)
1. Mezhvuzovskoye soveshch&niye po katalizu. lat. 2. Khimiche-
skii fakul'tat Moskovskogo gosudarstvennogo univeraiteta (for
Balandin, Kobozev, Lebedev). (Catalysis-Congresses)

MARDASHEV, Yu.S.; AGRONOMOV, A.Ya.
Evaluation of the surface area of nickel in Ni/A'203 catalysts.
Zhur.fiz.khim. 36 no.8il785-1787 Ag 162. (KRA 15:8)
1. Moskovskiy gosudarstvannyy universitat imeni Lomonosova...
(Nickel catalysts)

KLABtjNovsxiyf Ye.l.; ~GRDNOWV, A.Te.; VOLKOVA, L.M.; HALMIN, A.A.
Adsorption of racemic and (+ ) -isomers of 2-butanol
stereospecific silica gels. Izv.AN SSSR.Otd.khim.na~Lno.2s
228-234 F 163. (Al 16:4)
1. InBtitut organicheskoy khimii im. N.D.Zelinskogo AN SSBR
Moskovskiy gosudarstvennyy universitet im. M.V.Lomonosova.
(Butanol) (Adsorption) (Silica)

MALITSEV, A. N.; KOBOZEV) N. I-;.AQRDNVMQV,..A. le.; VORONOVA, L. V.
Effect of the size of granule carrier on the macroscopic
distribution of platinum in adsorption catalysts. Zhur. fiz.
khim. 37 no. 3:628-633 Mr 163. (MIRA 1715)
1. Moskovskiy gosudarstvennyy universitet imeni Lomonosova.

BALANDIN, Aleksey Alekoandrovich., akademik;_AMONOVOV,, A.Ye.,
red.; YERMUOT, M.S., tekhn. red.
(Multiplet theory of catalysis] Mulltipletnaia teoriia
kataliza. Moskva., Izd-vo Mosk. univ. Pt.l. 1963. 101 p.
(MIRA 17.2)

A.,
Catalytic propol-ties ()f jt
A,,hricul by the therm-sl
tion of amulgams. Irest. ,. I
o-9k. U!". ser. 19 no.2.-0,4-67
Mr-ApQ4 p t- I
I* Kafedra organjc*~Il
c'E~~O" K'11"~n)lj

Of,'MA

AGRONOMOV, A.Ye.; MTSHOENTKO, A.P.
Catalytic properties of iron obtained by the thermal
amalgams. Vest. Mosk. un. Ser. 2t Khim. 20 no.2:20-24
1. Kafedra oronicheskoy khimi-I Moskovskogo universitota,
decomposition of
Mr-Ap 165.
(MIRA 18:7)

,-G~(ONCMOV.. A.Ye.; MISHCHENKO.. A.P.
PoisonIng effect of benzene on an iron catalyst oblk,-Pirf~d t7
thermal decomposition ef amalgams. Vest. Moak. un. Ser. 2:
KhJm. 20 no.4:34-38 R-Ag 165. NIRA 18:10)
1. Hafedra organiaheslof I-,hilr-,- 14oskrvskogo gosudarstuveruirgo
universiteta.

AGROROMOV) L. jl.
e. At
Thr rartictim, of Ov. i0irldt!'; of 1)
It
1,;A11 ((!TlLidclid;!~ Ow vlodtictq
,if 111t. holljologoll, of Ow Nil:lph'. plilut'lly 1101ldc.
4,1 llivqltllt 11 (MI" 11,11" litli" 11,11, .1i'd li,lio, -I.-,--.,
V.-III - I-sill A IM". ~ It'll, I- "Wh: V-11" =
11-Al. -1 '.TIT,. 11,11% - 11114 it'!] "I I
in, 11,11, 1 it'll"I and 11-111~ - 2TlJI-, o, It, 01,
hi (101:11led-I 1; :11(.111 1111th, III, "Ift] . O1
pd-;. ('-difillol ir :,11(1 :,Ii, %-; lit 'I 1;11~. It 11, , :w I-
rit. 11 %killf ("1l", li'll" 16111 It'll- ~%ilh CAi-
It'll, ~6!11 ..%, " .111.1
%% it It 11, dill N I 11!m- ) , 'I Ir, -ii-1 f W!
'it In dtld, it -1, -d~
fof It P, I,%-
lt4.
ai I II
lif- It(,. it I qt o Ii'll I IIt,101.,
t I I Iit 1(il .Ii. I I III I1,,; 111 111lk ;,!I vi 17
mid II!, I III I I III II I1.1tp ri 11 .1 oI
I,p 1i1- - i I . :~i I 11-1 .
C!1 :1~.I~latlv
Mj1KCW

The stnictures of b
w7w7"C"Cu. T r1rill 1110 'Tit, I
I
II( . 7~.44 T 91
vl.T7A. 33, nviv expli. I c--ijJj:; obinin, it I)"v
-tion FT for 13.11,2NJI, dil
17NV lluM(" 'I
R1 '11 (~ 111V ri-witoll vith ya in h(pli'l alli-
itionia) cat, tic -Mained if thecoruji(j. is (Acri to N,- of IN,
form 1114.NH, 'File moic complex formula (Inopo,vtj liv
Schlesingur wid Burg) Nit,, 11111I.Nil...1111,1- V~ nol Ki,cd
Oil expfl. The atticle givesako a pnq~iblv sch(111W
of thereaction for the fomialinn of ibe compil. 11:11)N thal
agrees with the formula. !Rll,.N]13 for the amninnialt
.P!~nLLr()tu-di4pjang~j'cn referruccs, W. R. Ift-111 I

The structure of bgrpn
a. 111, The xtrjiCWM_,
21
J. tren. (111CM. ku. S. b, x.) lu, 120-4u
v*C7
A. 34, 12671.-Tbe properties of B hydride
ammoniates are clearer If they are regarded as products of
9(e,miplolar addn. of Nth to the H compris. of trivalent D
Ili, 13,11, and B,H&) unsatd. with electrons and imperfect
from the stereochem. point.o -f-view. B.-Hg.2NHj is re-
garded as 2 MON. of Blfi-Nlli, BiKoANH, as 2 mols, of
BHj.NHs + I mol. of NHs.BHjBJfl.NHj, B&HgANIfi
as NH,.BII,BIT..Nff, + NI-1j-B1l2BHl)H3-N1I4- In the
!transformations of these comptis. there is an unequal
affinity of H atoms attached to N and to B (a pos. polariza-
tion of H atoms attached to N and a neg. polarization of 11
atoms attached to B), which Is strengthened by the semi-
,polar bonds N - B. In connection with this there is a
possibility for reactions wMeb split off Ho and which lead
.to, substitution of H (attached to B) by N112 or to the
formation of new semipolar bonds N - B, which can lead
tc, ring c1mure. Owing to the tetrahedral nature of the
D and H atoms this takes place in a 6- or a 5-membered
chain. The study of the effect of various substituents for
replacing electrons and for pola1zing H atoms showed
that the 1-1 atoms are most reactive. From this point of
view the thermal and electrolyti(: dissocn. of 11,11s.2NW
atid BA9.41411s, the reactions of B,H,e.4NHj and BIHO.-
4NH* with HCI, the reaction of 1111111 and 1310H14 with NH3
and the electrolysis of the 131slille soln. in liquid NHi were

AGRJONX21 44~ ~nzhener; BABARLNOV, N.V., k Iandidat tokhnicheskikh nauk.
Thirty-fifth anniversary of using electric welding In Russian
shipbuilding. Sudostroanie 22 no.3:47 Mr 056. (KM 9:8)
(Electric welding) (Shipbuilding)

AQRLCllljM,(T! . S . N
..~var. Dro z,-r. r,

N.
AGRONOMOV. S., inzh.-makhaniko starehiy tekhnolog po avarke.; MARTTHENKD# L,,
khnvUg--jo avarka.
Automatic building up of shafts using the spiral technique. Mor.
flot 18 no.9:17-19 S '58. (KIRA 11: 10)
(Electric welding) (Shafting)

MATURVICH, V.D.,kand.tekhn.nauk; SAGIWVICH, D.N.,insh.; AGRONOROV, S.N.,inth.
Lnteat develapmento in welding. Sudostroenie Ap '58.
(Welding-Congreases) (MIRA 11:4)

PALLADIN) A.V., akademik; FEDORCHENKO, I.M., akademik; GULYY, M.F.,
akademik; BAKULIN, ID.I.; ME-LINIKOV, H.P., kand.tekhn.nauk;
OKERBLOM, N.O,, prdf,, doktor tekhn.nauk; LYUBAVSKII, K.V prof.
doktor tekhn.nauk, laureat Stalinskikh premiy; PORTNOY, N:D.) 1-1~
Icand.tekhmnauk; TSYBANI,, N.G.; KULIKOV, M.S., dotsent; AGRONOMOV,
S N inzh.; POLYAKOV, V.A., inzh.; SIMRSTYUK, V.N., inzR.----
Congratulations on the publication of-the issue na.100 of
the "Avtomaticheskaia Svarka" journal. Avtom.svar. 14 no.1t:
3-8 ii 161. (JJIRA 14:7)
1. Prezidbnt AN USSR (for Palladin). 2 AN LLS4, glaviiyy uchenyy
sekretart AN USSR (for Fedorchenko). 3: AN USSR, predsedatell re-
daktsiomo-izdatellskogo soveta AN USSR (for GulYY)'. 4, Uchenyy,.seImtar'
AN USSR (for Bakulin). 5. Direktor instituta "ProyektstallkonstruktaJyh'~*
(for Mellnikov). 6. Predsedatel sektaii svarochnogo proizvcdstva
TelduAko-okonomicheskogo soveta Loningradskogo sovnarkhoza (for
Okerblom). 7. Glavnyy svarshchik Uralvagonzavoda (for Portnoy).
8. Glavnyy inzh. zavoda im-, Nosenko (for TSybanf). 9. Dallnevostochnyy
politekhaicheskiy institut im. V.V.Kuybyshevv (for Kulikov).
10. Dalizavod (for Agronomov, Polyakov). 11. DaltnevostocluVy
nauchno-issledovatellskiy institut po,stroitellstvu (for Sherstywc).
(Electric welding- PerledicAles)

AGRONOVICHP,V. M.
"Radiation Damage."
report submitted for the Conference on Solid State Theory, held in MOscM?
December 2-12, 1963, sponsored by the Soviet Academy of Sciences,

AGRONSKIY. G.M.
Schedule planning in the building organizations. TransPe
stroi, 11 no.5:31-34 MY 161, (I.IIRA 34:6)
:L, Nachallnik planovogo otdela tresta Sevzaptransstroy.
(Constriction industry-)

USSR/Chemical Technology - Chemical Products.and Their
Application. Carbohydrates and Refinement.
Abs Jour : Ref Zhur - Khimiya, No 1, 1956, 2777
Author : Ostapenko., V.W., Mellnik, P.A.,Agron~k
Inst
Title Comparative Tests of the Maceration-Diffusion Procedure
of Operation of the Diffusion Battery.
Orig Pab Salharnaya prom-st', 1957, No 3, 41-43
Abstract The performnee indices are given for two identical 14-dif-
fuser batteries, one of which was operated in the conventi-
onal manner anf the other according to the maceration-dif-
fusion method (in the t'wo initial diffusers, disconnected
from the system, a preliminary steeping of fresh chips in
juice, was carried out). it was found that on using par-
tially dried and 'frozen beets: 1) output of the battery
operated according to the maceration-diffusion method
was, on the average, higher by 11.4%, and juice circulation
Card 1/12

US&~/Zlectronics - Ciao Disakarge and ORs Disckarge Instruments H-7
Abe Jour : Referat Zhur - Fizika, No 5, 1957'; 12344
Author : Fedorenho, N.V., Agrosimov V V
Inst
Title : Ionization of ftses by Zone of He4, Ne', and Ar* with For-
mation of Multiple-Charged Tons Upon a Single Interaction.
Orig Pub : Zh, tekba, fiziki, 1956, 26, No 91 1941-1954
Abstract : In addition to the setup previously described (Abstract
la343).. the work abstrw.-ted involves the use of a slow-
ion a4al~zer- From the relative inteAsity of the lines
of the'-spectrogram, the authors determine the cross sea-
#ons f9k the formation of slow multiply-charged ions
.1, 0, ) by interaction of He*, Ne4*, and Artvith energies
TI) AC03 -. 180 kev, with atoms. of helium., neon, argon, and
crypton ps. Ze rudom errors in the mea urements amDun-
ted to - 12-5%- Plots som SLT*u for 7-on(TO) for the
fd'~Iowing ions&
Card 1/3

A
A- it r4 9 1 -1-1 AA 0 4 a..
A - -f.
M I Ab psi 11.) 1 t
-00

60
A, A. M11C)SX[N. J. Cktw 'old- (N")Vow)
oe V. $-ills; C.11& art, dirmsed criti-

0* -00
0 -00
-04
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of

90 `
1p 4
ZOO
00 g
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10

i 39
~

A i as A bilrALtoprICAL 1.11911*1 E CLASSIFICATION to 0

I at go 11 11 IT K
Do 9910 069 w a *14 it a
p 0 0000 age go 0 0 0 0 ;e
ur IN 5 a a 3 It.
n 1 :14
0 0 0 g 6 al *so *as a *a

V 4
CCC44 k-A.-M I
a A-
A
!t(Killis 4"0 Pnot 10; t; I !ow I
0& mcleaty of coke clylins. A, A. Atisomm ANI) R. V Vilt-t-ft DO-1 1931,
No, 12, 48-M. cok' 4mu t , * It d6cumrtL the following fee.
_-hirthodifordtij.1 c- --frc ncya"
%ro heing conskirml: (1~ con%umptim of tok"ven gas for beating to cu. m.,,hr.:
ol) beat Taint of gas In cais.lcu. ni,; (31 priAuctioa in tons of coalitir.; (4) mt. ud
Product CA Offliltmstion of ps per cu. m. o(cokt-orrn gm; (M best "lm of product of
LAW(litrustion leaving rator; (4) amt. of air rtquhvd for burning I cu. m. cu; (7)
hmt content of I cu "=Air entering fermersitor; (R) srusibic heat per Cu. in. Of coke.
0 ovrn gas; (w beat lows due to radiation thmigh the wells of the over to cab./hr.
Falfrullim tal,14-1 and Chrl". Analywit nf 1W.4 am given.
0
a
is
-00
-so
.00,
As
so
go 0
zoo
are 0
u AT so mI
0 lot on ON of R
0 0 00
0 si
go a 00

I I 1 4 1 0
A I a A I 1 6 1 Is 11
C M a L S-11 V-1 0

~99
-

CbcW ftw of Cam in a e6ke ma. A. A &21jkAt.--.
.-A
NO
T
R
) IM
S
U
S
d Ck
k
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.
.
.
,
.
". (
Ca
o ail
view ( the imp"Wt imp.-t. -,& in the design
ON! p$ eircuktion and thereby
of coke Ovens to lawle I
excrWye
to SVOW SMW O%"bMtjq, ftaulge to bwiA*W*
ictibed a%
I
d
k
s
r
e oven
loss of bmt, etc. The rtowm co
t in tesped to tafrional ps Cir-
in ImporMt schkYtMtn
James Sorrel
~Culation.

0*0

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Coke win of the Grum-Gfpdm&W type. A. A, Al;xusxtN. Pomrs 1032. No. 1).
00 W-61.-Thc principle of tht Onan-Grih In burning (Ile gas in a
0 wp. chamber and in free chrulation of the products of combustion through continuous
chanoth along the prehati" walls. A description and data of an expU battery of 10
such ovcm. AW of a atuall sncmW a o 1h.sim,aregim. The rosin advantagr& of this !*00
00 a type of own consims In a mWe n&Var= dktribution of hem over the preheating *&)Is and -00
in a simpler emstructiou Ct#k toanbuoJoet chmocla. The ruin disadvantages art

tioessivc Ices of bat Intbe teads psaW DmtWty of having larger rrgencratots. (hi
"
6
the whole, good practical results art obtained In this oven, and the results of this in. .Of

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11pub"Wal "Ithag of Tritawaucaslan waia_j,,_
Kbim. Vwdsjo loplitu 4, itv
.101wiltul%kil coal (1). fuldlysing 1140 11.52
ash OAK) 15.112, vulalik waill-T 34.53 MICII) und 171KIT
and Uvarchrl" coal (U). contg. ll~)
&%h H.12 W~W and total S 1.51 wrfv
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lijo '00
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with dw slaad" tom. A. A, Aumotimpq (KukA
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Coke-oven Ileating with MS from blast -f'ul'll'lcee,.-.
U~xainyp 19371. 166P- M-55873)
TI'336.'A56
niarlkov, Gos. nauch.-techil. izd-vo
'i
1. Coke-ovens. I. Zhuravskii, V. N., A. au.

0 1
ai I
141 0.1. IM) bROM .I, Aw, ji~ '41-101
It 14 .f,f I
a, in osoce of the cokint Telimen on flif TMd and
qu&Uty of chemlW "is, A, A. Agio-kin Khm
Ttwdofo Tvf4im S. n(l
00 tbt consiniction aml t,prration 4 wLe m-cm. .54
A. A. P.
crenca.
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ASO.SLA "TALLURCKAL UTERATWE CLAULFICATICI, Oil- t
&low lWaliv.
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u AV so , , 1 40
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N IF It a 9 ir a w a it u it it ai ma n 1 X4 440
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sea
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III AN J~P Poptoi
r5~ -

rho technical and thmul testa of StAndsird Koppers
Ott coke 0"Go. A. A. Atti-Viij. C.-kro.,f 4 *k,-. ,1:
' .00
oil R.) 1939. No. '21 --14
.- Kl,-. Mr(eml. Zkb,. IQJQ. -00
9, 14-A.-Thr lical Input wal III-fil-rd flout Ih, 111,11 of
00 '10111buttian tA the fuel gas (98.361- 1. heat cutil, tit .1 i1w
'
`
,d air 11A.-Y. Av.
f
life) gas (0. 17%) arki heat .'en
" 09
t. kvist~,thc-ut-
heat km in the chimney Wx% vms 1S.16r
mundint spnee wa% X04%. aml the brit Iran.fffmi wo
the cLham1wr WRIt7r. Exprndmire of h,at w,~
C&I.Ag. of the mist. Im
r~40 0

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0 0
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hoe
so it!" I- V -71 .41 a 1 0 ~4
n it to 44 a a m It r% if tl?" A t
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Ole
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00 00
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-00
so .00
*0 a DirWbution of prmwv in the chamber of the coke evvn
A. .46-Airoskin C*kr and C". (11. S. S. R.) 1939, No. -00
00 ~;;-Vferal. Zkxr, 1939, No 8, 113. - ror the -00
Decker own the utax. 1writurruccurml Ihm altet charg.
ilig, when the clusigr cwtairsed 21%ol volatile mWance, .90
00
oand III M% moistum it 1114%, prekture ii' Idwayl, 011-
"hamber dDw the greater the pfevqurc (luring the I%t part
of the coking protym; during the 2nd halt of the ;wcc--
the urviturr near thr floor 1% mrsallet. W. R. 1frun age
-00
see
99TALLOCKAL LITERAYWR CLAISIF)CATPOW
I Z- Cro 0
sic., tiv~vliw.
alt S,
AV 10 0 AM -I I rW0- w 9
0 wortlobat unitil "OR 118140A ]uk 1* S ii-o 3 .9
0;G 0 0 0 0 0 0 & 0 0 # 0 0 0 a
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00
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4r
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host coulat4amperam diagmm
of cob arms. A. A. Alroskin and
V. A. Fridmiso. Coke and C".
No~ 10-11. 36-40: Kkin. )Wval, Zibr. IOW. No. 7.
12": d. C. A. 36, 11W.-Tbe 14 dias= (which rep-
rewAts gnkpbkay tbe fdation bttwtcn the beat content
of ibe combustion pmduca W their temp.) Is applied to
coke ovem; utilitbV kin gu (bI&A4w=ce gm) Vid rich
su (ooke-overs Ps). GmPVA am constructed Ior deg.
the factors In but babuice (heat of combustion of the bw -
Ing #us, beat content of the hmting p3 &W air, beat Intru-
ductd with the moisture of the vu and air. bmt of flue
I ganj6 relation among the heat capacity, the vol. of the
combustim producU oW The tbearetical consumption of
airIthe m&SWtd& of kwes from incomplete combustion
of the bhst4uroace wW coh-oven gases) R!"Pies of
the CLkxzq. We given.
is .!L& J~IALLU!WAL.LITIIIAIWI CLAWFKATIOP
$&nova .4 SAIS00a .11 0I.T OVE
04 ; 6, ,
U 0 AV so ul; C' I I VaIlluxtitl ICU
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AmosKiAAW
1. ACB)SKIN, A.A.
2. USSR (6-00)
"Hydrostatic Regime of Coking Chambers T~.
Ak. Nauk SSESR~ Otdel. Tekh. Naukq No. 6, 1~5.
.Power Fngineering Institutej Academy of
Sciences, USSR.
9. 4WReport U-1530., 25 Oct 1951

- j a I
4
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100 WSW at the tvtmt into the beatifts systrin sud the tint. (4
seeping Into The Trion. The
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5
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ing Comm in tbecirmlams currmi vw 30-Z%- tlectrs3~-
ing the mt. ot heating p!t inmaied (be tvtati%v sint. of
rocitrulating gx%m TO. tonfinns the %rIf-trjulsving
action of the circulating currtut. W. R. Heiin
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stool
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.
Pnxlu"t' of 'be gas dfgw'n
'

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heat
cak-n from the equfl 1119 Smem, and
still 16 rcinjumpti; 71*lkmlol the rmtent' Of C and 11,
e
'
i
nif 94%. The dem. of the jak
10"m *AV gillipler wil"I
t
,
h
were hmm with
Wall -furnart gal, owl,g ,,
Ile -n-blerablediff
r
t
e
.....b..
'It- the content (It C(h
Illost-filmace go, he coke-civen Cat and thr
W- R. Ifenn
-so
..66
so
ago
got
see
ago
foe 1
u M
17
AA)
A
u a 11 10 11
0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 6 411)* 4
0 0 0 0 0 0 # 0 0 9 0 : 1p'!1
- q_ , -0. _-
t 8
woo
lose
000
1 fm 0 N 0 1 1 A a 3 1 v
1 0 0 0 0 0 0 0 0 0 0 0 0 a 0 0

MOOM"wassa lot &a IM temperature of bog saw by
Nissan of abawift thtnoccopse. A. A. AoaosiaN.
Avlmw- and Tekxwb. [U.S.S.R.1, 6
abstrwted in Oval. Zextr.. IOU, U MOLM.-
temWmtum at go** abinv JAXI T. can be meavAred only
by tzkoustinS til"vewouples, with thm protetlAvv
wrgm for a tempeative pubcat of W'betwcm sm and
wand, with two protecti"i wreem for a maximum radwat
of RAP to 1201. and witla we Pfolective wreen OWY 1w
tcmpcM1Uf*suptG1OUO*to1:)DO'C. Atbennowuplede-
s!gn with thm protectivv offeens and Its pmetW appIks-
tmm we develrihed. MAA.

*
rate
Aj 9
00 COMBUSTION MWERILTURE Of GASM IN MATING SYSTEU OF COKS M31S,
.
Aerooky. A. At (Izveotya'AKad. Kauk, 1942, 606, 41-47). In odder
to determine -the actual ionbustion temperature of pass in the hosting
flue of ooke ovens, specially designed auction thermocouples with
j:: triple screen protection and water cooling =at be used. Tests have 1`9
shown that the 06an tomperaturo of the up-run raises the wall .00
temperature Iry 130-140% (whon hosting with coke Sne). Although the
combustion temperature should theoretic Ily drop during the change-
overs. owing to the reduced air (and ga:) supply the actual combusUon

temperature of the flames is raised during the time because of coo
reduced heat transfer t the wallst, The temperature of the waste Cases
0
re a
in thk vertical flues id lower than the wall, temperature during most
coo
00 pf the change-over timel this also shows She effect of vertical
Coe,
flues on heat transfer in oaks ovens, The Vests gag temperature
in the regenerator changes slightly between phases. Offing to the
see
sharp temperature drop ~n the top of the regenerator, the gas flow
distributbon system =at,, in fact, be considered as a hosting surface.
J
The use of suoti-n themooouples also shows that the actual temperature
oP exhaust gages In the'regenorator damper was 40-b-C. higher than

-
-
- coo
Al
SWICAIMM
CL
Aga-ILA MITALLUKKAL UNRAU01 be

bijill GA Out Lit
wcoo Hit 0MV ad(
6 1 V
ZA An I I OW 0 0 a I W W a 4 3 0 V
P 'g 1 40 A 1 351
0 0 0 0 0 0 0 0 0 * a 0 0 4 0 * 0 0 9 0 0
I
0 0 0 * 00000 0 0 a 6.jL'S 2 2--e-t.Le 0 0 0 0 0 Is a 0 0 9

-
00
0
0 0:
00
:
00
that indicated by rosistanoe thhrmometers and ordinary
thermocouples* 0
so
00 Subutantial corrections should accordingly be allowed for in so
00
0 * measuring thermal efficiienoy in ooke oven operation. (N 6889) 96
00 00
416 00
09 00
90 00
00 00
so 99
00 00
00 00
00 90
00
of 00
00 00
09 00
00 *0
00 0*
of
490

9 e
0 0 we 0 lee
-

A&WSKIIN) A. PITIN, R. 1-4.
Power EnG. Institute, im G. M. Krahizhanovskiy, Academy of
"Application of a Method of Moistening a Coal Charge with
this -.,*.cthod Applicable in the Lral By-,-Iroduct Coke lKills."
Otdel. Tekh. Nauk, No. 74~, IM5- Subnitted ~ Apr 19h5.
Sciences, LSSF.
11-1inute Additions of Oil--
iz. Ak. Nauk Sssh,
U-1582j, 6 Dec. 1951.

'A 4 .1 t1, 14- J- F, . L 0 M, F I Al - 4 ~ I .. -T, _V_Y-17 ~EWAI-I. t t~ -11-
W AID :A,
(A A
46. INGRZASED YI?.LDS FR%1 COU M~NS IN RU.IZIA. Agroskin, A.
, '6:
(Compt. Rend. Aead, Sci. U.R.S.S. 10 Nov. 1945, 42 t. Z
Motill. Engng, June 1946, Up 198t 200).
00 oil Ao
00 C: k1oke plants at Pagnitogorsk, Kuznetsk, and elsewhere in Russia
00 A,:: have for the past three years been using a method ol' washing
00 al coal with gasoline which provides increaSLd yields of coke and also
06 has a favourable effect on the tax. Anthracenic oil has also been
00 j uved as a wash. Much of the technique used is similar to comparable 0
00. develoTments in the U.S.A. 1he chief results so far have been: (1) 7 3.00
00 a , LA 0
Increased proc4uction of coke ovens generally is not less than 5%
00 Z If the ch-irge is moistened with gasoline, and not lee-- than 4% if
00 qnthracenio oil is used. -(2) The increaEed weight of the charge :g
fron the wetting irproves the quality of tars by diminishing crahkigg.
5100, (3) The quality of metalluxgical coke is improved. (4) "he technique
can be rapidly and easily installed in any sort of' coke plant. It we
can be used with all sore Of coal and different degrees of humidity. iuoo
(5) The technique sinplifi *a-a chatning of -.,coke ovens. The. waahed cod boo
A If. SL AAt I At I~461. LIT I A AILS f CL A %%If K ATMNI
AT "IV It a IV Ltp( aa Iqu n rt ~t cot
0000 0 *10 0 0 ID 0 0 0 0 0 0 0 a 0 0000
0 0 *to 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 111 0 0 0 0 0 0 0

004
go IN(IC141#1 AOV
.,o 0
0 di additioll of = junovilts 91 hydrocarbons. A. A.
Compt. tend. norad. vi. U.R.S.S, 49, 273-6-
A."). --A considerable itictoraw in (horis t. of gross rill cval
charp4l to a tvke oven can be secured by adding abuut 0 0
00 is, I Cr toy wt. of ga",-iur ot a mist. of gasoline slid Authors.
vent UU; tile exact aint. required (or OpultuWal refallt% '11111411
00 depends oil the riouisturecontent of tbecW. Foragivrn
%Wl, the d. of tile charge was increased from OXZ X.icr~
09 4
to- 0.75 j,JCc. by the additiots of (W.1'r col jamolitir. Tire 1-00
00 to
M-Clivellem LA tile addii. is lootteml liv addii. of phriwl~,
00 i-%klllvl RIC.. olvic Avid. rote. %%'hit,- oxidalimt 4.4mr,
I she 'A t. to l"CfeleIC JIUMCW1191, OXi.jjti(Jll (11 111C hyllfoo,"411"Ill 00
00 ..it dectraws its effectiveness. The increase in (I. title ill 1.00
otA,ling oil is mottorillistril ill the kli-cre-ist- in Itietion of tire I
ettal particles an Incloo'nored 1)), tile single of rcpow. Thi,
plove" hat'lolind Itrat:114A Jkplicaliml in &-Virl mkc-
00 ovell phints, where it blit; twen found that the iin-orcaw sit 00
,ral put through is not Irsto than So',. with ga-~Iinv alid 00
odo iiot Icss than 4% with authram-ne oil', while the yield of
light oil and espedally toluene is increased. Thequahtyof
tar is Improved and its ~p. gor. lowered. comring to diminished golit
cracking. with all Increimc In jiliencot%. ercsols, and fly-rilihic
lLiscs. The quality of metallutilical coke is improved.
1N& method Is readily adopted Anti simplifies charging
operations as the charge does not tend to freeze together
in the winter. It is believed that tlus process imill ;x:Tmit 00
Ulf
the use of a wider range of coal% in coke ovens. although 1119 0
the tuxit. effect i% iceurtJ uith a coal of medium rank !-%*#
R. W. Rvan
A S L A OtTALLURMAL LITERAYJAE CLAWFOCA11OW
go 0
0 0
0 0
11IN~" oil EN, 4111
to
to it to OOK met sia Knit Ittsmon il" Aft I % a rod 0 is a I
0 Goa "Ill
0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 * 0 0 0 a 0 0 0 0
: 0000000 0 6 0 0 0 0 0 0 0.0 0 do 0 0 0 o 6 0 0 0o

'i"itertaktift'llin Of the it'limPlItilln"S Of miLiD4 Of Whilk-
V; me with the tow milt"*, k. k.
ImAulova. zj"J,kayj LAN.

cartilifly 0.6 41.0 Lig. of the cral mixt. fiv kr 2
4 min.. ta
liam
hs (N)
h)
l
g. eac
, triltli
p
Cr the inkt. hil.) a 114A -illi

a we
*,[.I 'Wt ml, 'd pure Nomit,

a "till Wairl. shAki. Itir 3 filter flit-push A 16114"
vvilp
lot a w
r [
t
il
I
,
A
u
t
m
n a pit limialtrily "riglu,lai.lt t; x
rm. in dialu.) to frimove twilecile vdims$. ok4 fit,- ull tesi'llit
for 15-W inin. Ili a destlecatur, wrlith. and d(l. the jeri.
1
Celli e cimlent of
1
h
ont
ractric In the mist. by tilt, vii. of
f
-
the -
1
rethlue In the dish. It therellidne of a purr 10-mL
gfill-le of benzene evapd. on a water hath iftwo 1b.- kim,
Wi exrml% 11.1.1r.1 S.. the fcglowinj curTroitut mult 1w
:1!4(1c: A - 10 (a - b) (a ii the wt. of the W remiltic it; (lie
[till and b Is the wt, ut the rewiduc front 1U ml. of pute twit-
ItroO. W
. R. firlit
.

of I CiAtittraICAL Lllf%Avvltf CLAWFIC-01.
till uxuan
AV, so LS p It it ft M It l( a K
0 * * 9 0 0 0
at 0 0 0 ooo oqG::::1&8&9*Goqo
1 0 0 a goo 00 & 000 0 0 A.
04. 4!
Joel
I
0 A
.04
CIO 0
fee
fee
lie 0
use
tie*
we*

1*0 A

so Tho th of writing the Cod that V 1611 l-Alf4gi with
small q=ieff of hydiocitibon liquils A Acl..Lo' A
T.
Still %'~ S. it; M Kuh 11 1
I
k
*
I I R.X.S~,
s. i.
..',,S.k I Pull. mod.
Ino.. AkAd. SO. 1
(*I,#,,e ui. ink. 1945. 111&1 '_NQ Addii. 0 vurv mitall -00

Owd, notv .4 Ill,- -11 Lv Ill, . ...... .it '4 m all I

~'41.0.ow film. .4 111. O.Al

o
p I--- (- I' - -d 0-'-d #h" 1- 1-1 -SKI. 1411
'
l
l
i
t
j

l l,
1" -1 i
'
w%r f
le 4judlitliv ov'111t]"
tu
r%* firligrnt (A
-t
o Allumptim layrf) rc%ult~ in IS gicater flm-culati'MI (hall I, too
.,I,tAintd In cxW to which tin rvagrnt bai tx-rn adtioJ, bc-
06 voisr the tApillarv nieiiIwn%e% hinal flit- particir% inmc
.11"I'lly than 41'. llj~ m.-I A-hitt ..1 mIce ovtitr
oll.A.6111 r. III, Al 4.1,111110. till .411.,
ittiml,dift Ill moilu4m li,pild. A,Mst A
00 'j Atiol Ill. tilrk~ fit M. rl~ , dicioa,rd Ito

00 Wiltittel3t (It file INNIII Oldtf(C With Ijy%ll%RAtfKMl4 litittith,
Wetting of the chourge with tannin (it hydr--philic ptoter-
live cyAkhd with a peptising effect) inct.-a-411 boll1cwhat
thewt.titrtW, Covrfing threml %isthu-r "ith a very thin
lAyrf 14 JIVIA11%hr to-Allint Ill lit pokitiAl IlvdtThilizatioll,

"' *0
i
in, Ivanhlo the "1. .4 Ow .."I o,ll%l I.v 1-1 .3 It
01, !see

Ile lorlislillity by uld I11"4r4.nl th, 0
optimunt imMu. 4 thr trAilvitt. A,Idn. 4 ~tiIm':
dvotf44ytes (affecting (lie alluoplion t'i"illitiklill 14 h%dt-
ctution liquilo) demawl mintv%hat the wt, tit ouil linvir,
treatcAl with tufMnflne, (ming to the incTra%r in thr Wild- 0

L a
1 Ina ittlibiliv (if watet. Two reference-. W. R. Ilron
-O
4111A
Ilt'
1CA
llififil
AmPKA K)k
t
uo
1 i
k
k tk
M
6
t 0

u Is AV to 'Is!
I.,

1 it

"Tttplowol Malin Stuff it at ~w it I lit 4.1 0 ew a 4 0
3 9 V

0 j 1~46
to 0 0 0 0 0 0 0 *1* 0 0 0 0 0 6 0 0 0 0 * 0 a 0 0 0 0 0 0 0 0
0 0 0 0 * 0 j-9. Ii-, 0 go* so* 60 s o 0 0 9i

K~, T
AGROS Il~. A. A.
Aro-.a-',-*Lza',;,-'on of 1-')tor Fuels. shnikov, '*.F.
A.A.Acroskin. USSR 66,"42, A-i- 3-1 1c,-,L'iO. Prio to '.Iie arordza,ion
f urnace tile 11,,~ urocamons, cire ";ublected ',,) al tliornll. :)rc-lu-realumen', COF9,
3
craci-IMT, in the vapor ~)Iiase at

- -4 'i I, -&i -1 A--" J Q
00 A

Now tnetbod Im inuea&4 the productiveness and wilth

7
kill 8 111. Ufistir ev. anti : N. Mill. (I 100"I I vu
'
'
. 3, \.. 11m." cf. C.A. 40,110141.
7410."
I*he eft-lency W roking planto WA% ll"eAM%l IIY addillit
11.1 0.;V, Of A IlYttIV17MIKIII 10 111P C041 tit tW MILI'll Still
thoroughly It Will the two.
'
anthrarmne oil. The ium"istv rdrct 6 to
kerumera and
ith-tvatir the At. of a chat gr. I-Ait thiA tt"tmeW Simi im-
I'miVit the quality ril the coking &a% Still the coke. l(alus
vnitit opking of coals which ordinarily air not sultaltir
00 1 oir Cc-kills.
j
.3
4r
MCI
A S X - Il L AAIIIALLORGICAL UTFRA11,41 CLASUPIC.71C.
S .... . ..
u 4%, AS
lt n it n ;k' An I S 1 1. 0 M a I V a.
W D "it Coll pill via it I v
0 0 0 00 0 '0 0 04 0 0 0 0 0 0 0 0 * 00 0 00 0 000
0 0 0 0 *1* 0 0 0 0 0 0 0 0 0 0 6 0 0 0 0 * 010 * 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
-06
.00
111111110
r*O
too
4111114111
see
coo
me!

A 5
LO
sip, I -
7
A :6~
,
Use of W;d additions to hwreale the pour weight of
4 and V. N. 1,mlalipra 0-4wiltrii-
coal A. A. A~
elm-10 Irm- , Krzt-dalimmy,kipso, Mad. Nauk
-h1vtalltivsk4kr4il In-litut Nlorkilso Filiala
and Klibulko
Allaid. Nauk). Ilmll. a.z. All. 11.R-%.S.. (7.1w It.
IIOIJAJAt~ 14 11,411-1 it'.' 'Ittl4tv 44 %NMI
ime
IJ%. The Illm. .111.1w, ItIr It,(% "a I III, hV4111141hOme
%4a1 ml 116111frill it ooltw O'k onti 11VIIII hilic Swill".
'lUfiutc tholtim list-
linbe 18railim-111 wilb 0111111k, 14 0111411 Ijklu'lliti-Il 'Al. ji~
authramme (41. kerowtic. raisked the twur at. by 14 lx-.
Asich, Intilkidaily h~ii Nmj~
11111eIl Willi a hydrimmixtil 4141, wrf~ verv VIL1,6w itk 01clua,
fAir Kiwil.
111111 he IN-ur wt,
11 1
""ll
i
t
t-v #,III Ali
I 2t-
It it St it I, on it a tt It a q IF 'A, 0 a
0 1 ;11 *;6- 1 dm
o Sig 00 0 0 0 * 00 0 0 0
-00
.00
moo
490
0
too

99A
P'#Ktbl(i AND 0111-PtI1111% W' k
got
4,
to
birtrathic the 11ulk Drinity of Coad ley 511cree-Addhiet",
of Oil 11).11roductie of Voking. A A Agrcmkip and R N
1,1111). 11)JI'lim .'1 At. .14-mb-my "/ sririiiri fit V."~S K
o# 4 Tochnival 86,-tict, tim :.1, ;.S;6
rill", oil
'Z I a. S L A MIETAMIRWAL UYINAIM CLASUPKA11011
00
It, IV 0 it 0 44 a CS It 0 it a n
IV,
0
o:::::1oooo6oqo*oooo*
0*0000000000*6
Inv
A I 17A a ped 0 04 1 1 111 Im a III V
&
0 e 0 0 0 e
-so
tip
ago
00
coo
00
coo
a**
zoo
0 o1
09
Its 0

forpi Nis! Sl.V' I

06 A
00
so

008 Influefte of the Suruce TVnqm of 14uld Hydromr.
004 ba" on 7%eIr Effitlefty in WeatberlikC the COO

00 & Charge. A. A. Arromkin and E. N. Loakutova, jour.

*
vial of Applied
Chemistry (U.S.S.p ), v. 19
no
4

00 it
2, .
.
,
1046. P. 349-362. (In Russian.)
00 3 Dependence between surface tenAtin and efficielic
y
".01111W of coal bl. such liquid hydrocarbons hite
I-c('11 InVePtigated. Results show that the reagents
'3 postessinz lower surface tensions produce more

00 Vilicient Wetting.
00
00
Ji
n!;
LittRAVOI ------ Inv
stTALLIOWCAL
L IW 0 0000
in
it at KW
0 0 0 0 e 10 o 0 0 0 0 0 9000
ts AT 00 LS D CT 11 'a, 0 0606 00 0 0 0 09 A)* 0
a 0 0 010 o 0 0 0 0 0 -
01
0900-0010
.00
-00
400
.00
'00
7
k zoo
=00~
coo
LV 0
0
coo
0 0
'00
'00
'00

of
Physicochamical basos for Packing of cost for coking.
1. Kinew of saturation of coal layor organic llq
~ldi.
,
A. A. AgroWn and 1. G. llctretik,.. ~ ApPJwd the..
461-7,60"l)(in Rimian)-The rate of
wetting (%&tn.) of a lay" of eml particles tjy,,rg. liquids iA
'
d b
b
l
h
rxpremw
o
a W t
e tylk- A - W
y a para
, where A i.
h
b
f
e
t
right o
the liquid in riat.. I - timv in min.. and 1k
d
F
4 are misti.
an
m tionlKilar liquid, a tangv% hout tt,4
i(1
to(Ul
tull
7tw, 2A
f
th
l
i
_
a
rott
.
r r-u
og a
t, Air turcutt
jLhV
ditpersion ol the nial; ine-n-a- of derl'i of thr cool layrr
at a given fliqwrviotl lea.14 In dectra~c~ satn. rate. Om-
diml coul. having 0 fibst turfAces. gave loncr hatti. rate
by notipolar liquids. NmimplAr aromatic hydrivt-atlm.m~
1
0 gave file high"t rate (4 %atia.. ft4lotttil in ordrr In, light
00 pr:1rQtiatu fraclion% stid 0-conig. liquids. Ctial fit the
!;i niddle stagrim W carlmiration gave the hight-,t %atit.
00 rates, Coal which has a high order s4 admPrptimi wa,
00 'a li,mn w low 1hr stivx1j"I gAlt" b)' 111VIT dl~pIMN'1111'11t
%ith life ofs. liquids. 11. Angles of natural gradient of a
7
47
-
-l
-Th
l
h
Ib
d
8S
.-
,
coa
c
s
.
-
arp.
e rt
ati-tt (4 flit
natural
gradient 8"gle of coal to the introthirtion of walcr or kctu-
lene into the coal Wyet wm studied. Increase (if the Uri-
'.
id
l
d
ti
cmteut to 14
e
;.
to a strady rie (4 the g7adictit.
The effert is mmideml from the vicujx~nl of c,wfl. of
friction and the presence of ad.-rpt i%r U11.1 M4Vaj,.l qJr.
i
f
f
h
at" o
t
e Cmd part
c1". G. M. ko-klk~JT

A S a I A. A sItALLLUKAL 9_17
LITINAIM CL91SIFKATION

t
wall,

b

Is Al
"
; T_-
III
tt it K
A 7A AM L S IN 0 is I it im ff a 9
KID I M
l to t' to to 0 at It it

Z
:
0 01
., :
0 0 0
00 0000 0 ! ; 0 00 000000 0 0000 0

0 0000
10 0 0 0 0 0 9 0 0 0 0 0 0 0 0
'00
see
=09
0
09
a**
1* 0
09
00
"06
46
tie 0

Coke production with luicto addiflon& of od.
A .14al 6, &P-7(19441)
VX;~!in slid S. At. Grigot'rv.
j coking coal with I). I "; of a mineral it (kcroene,
anthraerne, or a "lilt. of oil,) rairl the pioduction of coke
by pmnittiul a treater charge lirr oven. Addn. (it 3~`e of
Of gr gasification coal and welling lite charxe mith rif all
cial raised the wt, of an even charge by 1.8e;, the yield of
lar by L~e, and the yiOd of crude britzine by 1.247;.
The Increased ovell charge ditl not elll&il an increase in
coking little. -00
coo
00 a
09 go 0
so off
00 see
pso i IF i,
see
MCI.
Uoo
W'W
I Z7
:00
*,a lit- 0.
it ~i)" 0~7
IN] I
04-" ~
I ra I Y rA v Im a 43 0 3 4 IF
U IS IV 143 Orlmnalt oil pq "It" It a W
e 0 0~0 00 0 0 0 0 0 0 0 0 0 0 0 o1 1so 69 0 0 0 0 0 0 0 e 0 0 0 0 0 0 0 0 0 11111~
e.
0 e 0,0 0 o 0

ONCIC11111i AkD porpity.ts MV11
Seltictive witting of coal. A. A. Alit-kip And 1. t..
't-urnko. J. Applied Chem. W.Y'19, 7-1". 46
111114111(i11 Rumiall). --cont art anilk, 0 W'rrr deld. at thv
Im"Intlatirs mial-WaIrr-air and by
14%,hviting the %lititour, .4 the 'Iml. with a I'l.kliv. h'1.1
tit water, hovivJ a neg. writatubly R - em 0. the tisit.
litillill failing 11) 'U'plave the water; the currgy nmv-ary
"I 'Irt-titutir file fol-sirtrwi% it hightr than Iliv vneeltv
Ill-,oalml ill writing. Alli-inall,"I -4 flu wJ,t -I del.w.
111111 14 vi-ater *11.1 til the tit%. 1141110 %ho%t4l thr liv%l"Ims
-( fit litith verb, and to tv of thu mdei A N- 0 - 1, 4
llydrolihilic tw liv Ittipholic vital -
morf of the coal dellends
liquid has farts driuvolt" lir'l. Jill 15. 1-1 li~i 1111;1.
del"rdting at discrete jusillistIf file stalf6tv. 41n,11444 vk4tri
:tW .-f hy1r;Zbon, "Uhing in a -litia"ims (,I the fallr$.
ml tilting the ample, confirtipml the fwtuatiou W a filin
of hydrocarbon on the water surface. Owing tobystercm,,
a water drop hanging vertically frtxn a polibed coal sur-
facir. was not tom off by a spmiwling ki-ro-ene film. despite
the equil. gain in Purfacc rlierly C.M.77-12.4 14.3 erg9isq.
N. I'llon
allAttURGICAC LIURATtift CL#t%WKAt1cx
log) Wit 0"T Ilat 41111110411 biltill &A Ott 114
4 1 4 1 1 1 ", 0 1 T I rho
4 0 a W I III $1 9 all a 3 1 V
U 0 AV 00 11 to 0 to It 0 It a 4 91 R U is
0 0
Z; too
roe
1100
410
1-00
fee to
u 00
tie*

W -A ~&-L lh I
f0 A
1~~! 4~ 0`110 Ill I it I 1111-t I
60 _L --- 00
so
00A 00
00 Efitct of the panulotuetric Composition of the coal
charge on its bulk density and the eff"tiveness at wetting
09 with liquid bydrocarbons. A.A-Uz;ALjn. V. S 00
0 0 21141 It. N. Pitill. P11111. (11J. it i~ 1' 9 "~.S
00 A qif"iiL It1h. 1946, '~19 012(i11 Ro-iianl; cf. C-1, 40, -00
174
Imw(A flint the mlafivc I'mulilig .1 1,1111, '00
06 w0ght hy limi-tille i, flir
00 111111. Iyulk Wright of a Sivro chatp. int-tvam" %%1I1[
00 Ing fineness of the grist. Uncivr normal moWure vowb-
00 lions, file flulk weight incream-ii with inctra,iog cmTm- =0*
rV
nrm; with h"; InOiStUre. A 1,, Ch.Ul)gP it) lilt' VIAS% lit-110A :1
flint. grain c4re gives rise to art av. chatoge of bolk w, ight
The tmlkwcight is forthii inciva,rdby %W,-u- ~00
of
ing of life dikmlity limits; it ran be rai--nll to a 111411. i .00
09 1htoug~ clinlinsition of intetinckliate graill sit". Tllv
4F %viSIlt-lnrtVa4ng effect of 1111"taildnit. of kcitN-rit. i, file 00
more officirnt life firiff the gri,t ami the "itIrt the Innit, of goo
iliqw-rOly; climination of inirroic-liair iir~ avis io lilt,
kaflic dirrvilml. 40 0
X. Tholl 00
'goo
too
eoO
In SLA MITALLURGICAL Lftf4ATURE CLASIIFKAT900
tio o
-4W.
.JIV
183041 a, 1311 off mi 0 0
13 U IS AT 00 It
IT to V It It Pric Nit RsF Plan if RADA 1114AAL I a Iwo NI)c stoncl 341~409
0 0 0 0 o 0 0 0 0 * 0 0 o
0 0 0 0 0 IL 0 0 0 0
0 000 0 0 0 0 0 0 0 0 * 0 0 0 0 0 6 0 6 0 0 0 6.0 * 0 0 0 0 0 9 0 o 0.0 0 o 9 0 0 :i~A

AGROSIA GRIGOHIYAV, S.M.; ZAGRRBBLINATA, V.S.; LOSKMOVA, Ye.H.1
A"WL"" P31TRONKO, I.G.; PITIS, R.N.; CHIZHUSKIY. -H.P., akaaamwotvat-
stvannyy redaktor: VOROVITSKIT, I.B., redak-tor; AUZAN, H.P.,
tekhniche9kly redaktor
[Increase of the weight of coal per cubic meter by microadditives
of liquid hydrocarbon-, a collection of articles] Uvelichanie
nasyphogo veea uglia mikrodobavkami uglevodorodnykh zhidkostel;
abornik rabot. Moskva, Izd-vo Akademil nauk SSSR, 1947. 398 P.
(Coke) (Coal) (MIRA 9:9)

00

Changes in the bulk density o. coal due to fteeting
A, A, Alto4kin and N', ';. ZANfrlxl*ll&YA- 1`11111. Mod. its.

:0 volk d. of c4ml it ptinvirily it luadion of inoWure; typical
i
t
f
I
fi
i
sviras
s
kar ar
rom
t
nit mo
cut% r%-litiw that the d. (till ~w it
tut. ilevirraitic liv &%o Is' " it w 4 "';. and Im-mit
thmigh a non. at ir S.,.jl- ~ with the addu~ L4 Ali t4~tlll)Ula
atilt. Ill Iteiro'cue. the ci~f%v i- i,hifted ticatly smialict to
It"If to higher it. Oil titillill lit exactly' 0" tile maii. it.
I-'(V) K."Vil. &Jm.), (a amilol T C~111;tl 20 !.'4"W;4.rr.1Ch"J
th It% a,hill. j4 olily almmil it i'S', Lm.witt%, luithri ji,l,bl.
tr,ulfliq lit limailv dimitti,hitti: d I*hr rfirct ii rmi itmov
eq '3 umil,rd M -it' v%hrrr th, d 1;141) 1, deviva-A by wldn,.
'4 km-nr from Ih, -rv N-wm-mx. 1:",s ... i; h-mly .
00-3
-increasing effect with initi.tI , uf at least 21 LA)wvr -

60.3 I
1.( the temp. (tom about - V lit about - tr%ultri
l
g
!
c4.11, "I W
a vi I v light fort her t -f I he tI., it
i:l

S.Ile, the it. resumm,l the higlict till- lowrt W,
3.3 to, 11
example: w - 'U1, A. 1. at -- 5' and - 10'. d.
ril) and 773. = and GN it./Sq. dm. Suitul-
M and M2
,
taticouOy with the incrrA~c of the bulk- d.. the cticil. u(
fricti'm ("Irastiml by the "n;k. A vol qxmilatmtu~ 11,linK)
It ill., decirrzt-led thrmah Irrvitng, exampIr. sr C.1. Ilchwe
fwzhig d. (!:N1. A 37.0% Aire Im-,ing d 70. A 32 :,':
le.%~2' bf,*,- ftild after Inexinx d. 'Oil .11d 7 17. 4 411.0 ~tid

Ili industrial pravilve. friviing its wititir little lwi-
'13.4'.
tuitird mi-Julf the wt. of a charge in tilkial; platmi. Ili
Inti-frM lie% Ili the monoiny n4 lmll,%--irl-4is I,-,I h-r the
mill'.
Energetichesviy 1
institut im G. IM. '
Krzhizhanowkogo
Akademii nwuk SSSR.
Predstavleno
aka~
11
demikom N. P
Chizhevskim.
qvIQ.j_.jt ~v 'Jot 0191111dt, a I, I $'I aw a., it,
AA' V D if W I is 9 in a 3 v
U AT go As It to it a It a At IIt MW a
1440 00 0 0 Ole 0 000000 0 9 0 0 0 0 0 eq. It -0-0000000 eq 000 0 90
0
1-04
1100
.00
-90
goo
coo
ago
coo
see
ti

- -",L A.-I
00 4
go
* 0
00
go
09
09
00
00

I of the bulk wellit of the coal on the Rroperties
of the coke ptoduct4. M. t.tigol'vv.
IT
sn't 1. U. pritruko. JIM
I J. 1. X.S N . (11,.e
sci, teA. 1947. ?I15-14(itz Rti-amt). -Itu-tra-v of thr hulk
,J. of mal by wettinK wills mirmamm of liquid hydro.
vAthons IC.A. 41, 2NALU) rt~ult~ io hwr"%ed yivid of =00
mrintim Xical ~Ar. i" Joerra%M m"h. stfvnXth. demram%I 0
imim-liv, ittid Isisher Wilk wt. It prtlolt% Inclu%lon,jor
vokfild putim"P., (it Ps i-tv.11 aqwt% 11o( 411tivOy suitdtdr~ coo
N. r0 0
ASS.I. A
~wi
6A 1) ~ai -
U a IV 10 At U-i I I
0 0 It ft It 0 a 'Witwil mitin Itix
00 0 000 0 0 * 0 * 0 0 00 goo* so
00 0000 000 0 0 0 0 so 0 0 0 0 0_9
0*0
qoo
40
'00
1z bo 0
Ito 0
-6i -a-v~ tit
;i1 I I I OaT
YL t 0 Phi 0 0 6 1 IN Im 3 a a 3 0 T
W
Is 0 0 as 0 q 06 0 o 06 of as 0 41i
& a * a 0 0-000 0 0 0 0 OL 0 00 0 0 of,

of A
of
09
if
PSOCiliti, A.0 POG11411ti,
WettL4 coal chage with micro-additions of inthratens
oil
fi)daxndE.N.La%kutova. SW7.6.9.1-6
jj4? %&A-h4jrc
0 ). ~i
IIKIVM Purpciselof wetting coul with anthramlic Wl
is to tbt' bu Is wt. of the coal. I'll~ optimum
%juallilly 44 allilita'%la. it, IN- tl.,Nl 1, chi.
1IN ~, ahk-h 6 Ali ill
L'I.11141 lhu
mixt. taken in a qtuntliv j4 x 1%lr a btill, , I. m,VA%e
44 PUP- I'm stiihrm~nr ml Ilic
11141lig was 4 in 111will had it, 11"Ir'.11
CAIII VII-vi. I-of KIIA111 Ow -11.1
-I Js'"Ild IN, 11"'t"I prom Ill 1111kifi$. lit Ift-l it-mill, V,(.Ir
Obtaill"I by ati%niiing the ittithr"Ivile 0.1. M. H
-hril
I L a 611ALLUICKAL LITINAUdy CIASSIFKA110M
MI "catiabb *A Salubi 411 Oftv V94
;r--j
0 U 0 AT 10 it TO 0 a to it altaw Rost 111K
0 9 0 0 0 0 0 0 0 0 0 : 0 0 0 0 0 0 0 0 0 a
0 0 0 0 0 Ole 0 0 0 0-0 0-0 0 0 0 9 0 0
a I W so 0 '13 a
a o Ole 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
0 a 0 a a 0 9 0 9 & 0 0 0 0 0 0 0 0 0 0 0 0
90
o*
00
Ore
'00
11109
0
coo
Ire 0
00
1-00
!see
fie 0
tjoe
b 0 0
wee
too,

I 000CISISS AND P6001111its IhR~J- -

782. INFIMCE OF MACE PROPEMES OF SOME ORGANIC LIQUIDS ON
CHAME IN Bmx wrimiop nNs COAL. Agroskin, A. A. and I*mkutmp
09 S6i*. UIS.S.R.), 1947#
(Doklady Akad. Filauk S.S.S.R. (It6p, Acad
00 Vol. 58# 2095-1098; abeir. in Chan. Abstr., 1950, vol. 44, 8088). -00
410 S
4119 it

a
11" Wetting liquids uned-were purified preparations of Vlene, paudp-
0
foe 0=anaj1