SCIENTIFIC ABSTRACT MOROZOV, N. M. - MOROZOV, N. V.

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CIA-RDP86-00513R001135220011-5
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December 31, 1967
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SCIENTIFIC ABSTRACT
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Cf P 5 V AJTfiuRS t Pahez1h, t.sk ly S u v K:i:ri, n k yatskayrL , V "i r ~ r) C. v a '1' e T IT L E K i n ~- t -~ cs 3 1 !~ e r- -a . i -:~ PERIGL--CAL: Zhurnal fizic~ies',~- ,hi:ii, Vol Nr- pp 23o6 - 2 Ail 5 (JISE-It', .k 5 T I A C~ According -wo A V a! m fc r--j v -a r, a S . Y a . s t h e i a:i - tam y i ~ I f n cr, m i c-, I -D z o n e I I i Li I d p ha s e a -' n s ~t 2 Inv's---11- -~.S o f t her-:~,a I o zc ne d ec o::~,, is 1 t n na v e nc. X 4 n - r- prob' -em . TK-~s , valae3 (,,)f kcal were g--,.en fcr -~I~ ~I tion enfrl,:,y in -Ca' ~~ 3 r's r i t h I s P r K a s n -a A xvi o rt h,/ in ir" tne 'ILA*."; react ion --.9 r,.-, - i o n e u; p ,m e d i u m and i,,,-:ic,~rtrationS ar-J, va.": s a faces a te,:,,,,er,aLre ran~-,e e under at-~c .2 ions 'a'. d e c F 1,~I " e? r v., as d P r Caru~ 30-76CMH9 w-tnin the t em. p:,a 7 e x D e r If. t S 'i col~,Os c , order, "a up to 2 A v--y h~L~,;n d r s, w i r x 7.a- a o e i. t --i va t~ian t -j;;.r -j f: ns ti r.rian fh- e r' I n A r 'K as s r s X, v -a Pcr the f e e:n Ei ry ra mposi-.= cl q- s r !'~x ec o. a n cl -D r s r ~.i e r, i.- ,:L~ b y-i ~i Vlr,,~,re are a --F n~, C ad 2 , a r eS o v ,c 0583~ Kinetics of the Thermal Lecompositicn -,f Ozone 50/76~35-10-,41/45 ASS OCIAT ION: Fiziko -,,.him icheskiy inst it t im . L . Ya . Ka rpov a ;'4oskva (PhY - sicochemical Institute i:~~(~ni L. Ya, Karpov, Moscow 5JBhlIT"_!-Di March 31, 1958 Car~ 3/3 SHCHTBRYA, G.C,.-, Kinetics i-rd rnou.hnninm of a ~P~'.alytic re,-Ict4r).' moroxide uid w8ter vhpor. Fnr-t 2: Renctlinr, copper rxide catFily-t- Kin. I lkat. 1. Fizilko-4,himi luner.- j'n - . Fr~bnmrv Yi, 511CHIBRYA, G.G.; MOROZOr, N.M.; THAIKIN, M.I. Kinetics and mechanism of catalytic reaction between carbon monoxido and vater vapor. Part ls Reaction on ferrochromium oxide catalyst. Kin, i kat. 6 no, 6:1057-1068 N-D 965 (MTRA 19W 1. Fiziko-khiinicheskiy Inatitut imeni Kexpor7a. Submitted February 13, 1965, I 1 .7-1 ~ ~- I --_ , L~ ~;~- ~.;, ;," - . -;- -~ :.. - -- - - - - ~.i . -: , , . .. 1. . _,- --, - , . ,-. - ~- ~J -'- ~ . --- " - -: , , . . Z.- . -- I - .- -- . 1. - : I - -. . -- I actiVatdd formiil-a,-s- -TTE!Yi 29V SUBMI No MOROZOV. N.K., inzh.; POKAMESTOV, V.V., inzh. Kechanized drying of a wet layer of milled peat on the side of piles. Torf. prom. 35 no.6:9-11 '58. (YTRA 11:10) I.Vaesoyuzny3r nauchno-issledovatollskdy institut torfyanoy pro- myshlonnoott (VNIITP) (Peat--Drying) (Pont mitchinery) MOROZOV, N~M. o-" and gas We---.El -,r in, I- okh. nedr. 3C My ' ~u 7yumen3koye '.,: ~.- ('j, t "! , .'~ . - . F: r, I -, - K ' 1.. . I I - : ; " ,,, nd rar ~ r -7. j , , ". . I . 7 . - MORO '70V N.M. - I -I Tr -a ri s p o r '.a t i ~ ri c- f J r- ;* 1 ' '~ . -- -:- ;. " -.., - I ~ - , .;~. - --l.. 43 nc. 1: i?-z 3 .1, t (IM"'. 18:3.) Ji 07 5 / 6 o/ B020/BO61 AUTHOR; Morozovj N. I"i. TITLEi Determination of High Concentrations of ozone PERIODICA"s Zhurnal analiticheskoy khimii, 1960, Vol~ 15, No~ 3, pp. 367-368 TEXTi The e are no accounts of the determination of high concentrationi of ozonelli: publications. The moet widely used method of determining ozone in lcr concentrations depends on its absorption by a potaggium iodide solu ion (Ref. 5) according to the equationg H20 + 2KI + 0 3 ' 2KOH + 1 2 + 02- This method is very simple, and well suited to ice purpose (Ref. 6). However, there are many difficultips irt 1~ 13 the determ nation of high concentrations of ozone, which are atipulat-30 in the firit place by the aggreBeivity of the concentrated ozone, and besides, a local rise in the basicity of the inedium may occur at th~.4 contact p( nts of the analyzed gas with the KI-solution, wh4rh ili~iy -J, in an alke.1 solution, instead of a separation of free indine to ito Card 1/2 ,-germination ol hif_~h oncenzra-.ions o_t Ozone B020/BO64 oxidation under formation of potassium iodate (Ref, "t:- up to some percent lower can be obtained. The method descri")~-d h-~_- makes it possible to avoid these difficuliies, A peculiarJry 3f the method is the use of evacuated weighed flaF;ks with a volume of 200-1~100 (Fig.). The performance of the deter-minati,?n is also described in de+ail. The reproducibility of the refults was tested ~)n ozone - oxygen mi'xturaq of constant composition. A process of producing mixtures of concentr;,1-1, ozone with oxygen is described, and the data obtained from the analysis of such mixtures is given (Table). The temperature fluctuations in the weighing room during weighing were +0.50. The main sources of erro-r are given, their elimination is described, and finally the main advantiFr~n of the method described are detailed. There are I figure. I tRbII7-,. inl 6 non-Soviet references. ASSOCIATIOF~ Fiziko-khimlicheskiy institut im, L. Ya. Ka-,pova, Mcqkva (P~Iljillo-chemical Institute imeni L. Ya. Karpov, Moqrr.)w) SUBN'ITTEDi March 6, 1959 Card 2/2 33488 S/195/61/002/005/013/027 Elll/E485 AUTHORS.~ Temkin, M~I.,, Nakhmanovich, M.L. Morozov, NM ,TITLED. Kinetics and mechanism of isotope exchange and gas reacting on the surface of solids PERIODICAL; Kinetika i kataliz, v.2, no.5, 1961 722 726 TEXT. Use of isotopes as tracer atoms permits dire,~t observation of the different stages in a catalysed reaction., The object of the present work was to illustrate. with simple examples, the relation between the kinetics of reac;tions on th--'.7 surface of solids and the kinetics of tsotope-exchange processes The simplest heterogeneous catalysed reaction can be written as 1~ A + X + I 2. B + (I) ~4y + 41~-- (2) where A and B are reactants, X and Y reaction products ( ) is a vacant site on the surface ard (I) a chemisorbed intermediate particle, Addition gives the overall reaction Card l/ 5 3 3488 S/19 61/002/005/013/027 E1113/E485 Kinetics and mechanism The cases considered are those of the reaction of watergas on a magnetite catalyst at 400 to 500'C, the reaction of .-arbon with C02, the isotope exchange by oxygen or carbon betwisen carbon mono- and dioxide. the exchange of deuterium between water vapours and hydrogen. All these rea:tions can be --onsid-2-r-4A particular cases of a general equation, If the adsorbed intermediate obeys the Langmuir isotherm this equation 16 W Kl.PA"2PB.--H-lPX".-2PY--...- 1PA " " 1PX * "2pB 2P'. where w is the rate of the reaction 41 the rat,~ ronsTant or the first stage in the forward direction H i that in thc- reverse direction (K2 and m 2 same for th-~- 6&-.ond stag,;O PA the partial pressure of A (or the product of theLr par~ia.l pressures if several substances partl,:Ipate and so on) rf th,~ intermediate compound adsorption followb a logarithmi is:therm then Card 2/ 5 33488 S/195/61/002/005/013/027 Kinetics and mechanism ... EIII/E485 I(" Px'4 PY _P sin a;t (X' PA + )'"-,Py)' IPX + )itPB)' (20) Here xO is the value of iij at the greatest adsorption energy of the Iintermediate compound, and so on; a is the proportiona-Lity coefficient between the change in the adsorption energy and the activation energy; f is the ratio of the adsorption-energy change range to RT. Both equations correspond to steady-state conditions. Eq.(20) is supported by some experimental data at medium degrees of surface coverage by the intermediate compound (e.g. Ref.4: V.A.Yevropin, N.V.Kullkova, M.I.Temkin, Zh. fiz. khimii, v.30, 1956, 348). The authors report unpublished work on the reaction HDO + H2 ';�11D + 1120 in a flow systein with water containing 2.2 or 2.5 atomic % deuterium. Since PHDO