SCIENTIFIC ABSTRACT ROMANKOV, P.G. - ROMANKOVA, A.G.

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SCIENTIFIC ABSTRACT
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1 55 3-58-3-27/ ~`Cl SOV/ tho 'r c ,pproxima tc-. ono o Kinetics of the D~~Sorption 1, 0 (~Ss insilitut imeni Lensoveta ~Lesiin-,-vad T,~chnolo,,-'.cal Institute tn~,ni Lensovet) protsessr-,v 4- al~parktuav (C~ia-ir of '!:et*i~ds and Januar- 1 1958 3/ T ROMMOV, P.G., prof.; BAO CHZHI-TSYUANI [Pao Chih-chlban], kand.tekhn.nauk PATLOV, K.F.. ROXANKOT, P.G., prof.; NOSKOV, A.A.; KMOCHKINA, M.I., red.; KOTS, Y,A., red.; NRLIIH, Te.Te.. takhn.red. [Uamples and problems in a course on the processes and equipment of chemical technology] Primary i zedschi po karsu protsessov i apparatov khimichaskoi tokhnologii. lad.4, dop. i perer. Pod obshchei red. P.G.Romankova. Leningrad, Goa. nauchno-tekbn.izd-vo khim.lit- 1959. 573 P. (KIRA 13:2) (Chemistry, Tachnica,71 25(2) SOV/64-59-1-15/24 AUTHORS: Romankov, P. G., Doctor of Technical Sciences, Yablonskiyq P.A., Candidate---or-Technical Sciences TITLE: The.Influence of.Various Internal Devices in the Separator With Revolving Breaking Blades Upon the Efficiency of Classification (0, vliyanii razlichnykh vnutrennikh ustroystv v separatore a vrashchayushchimisya otboynymi lopatkami na, effektivriost' klassifikataii) PERIODICAL: Khimicheskaya promyahlennost', 1959v Nr 1. pp 68--70 (USSR) ABSTRACT: 'In a former paper (Ref 1) equations (1) and (2) on the extrac- Galilean ofthe Card 1/2 tion fine fraction and for the criterion for,. experimental separators without internal devices (Fig 1) were derived..In the present case expeiimental results are given for the.,following types of classifeator: figure 1-with- out internal device, figure 2 with two deflectors, fi,-,are 3 with one deflector, figure 4 with a derivation of the products from the mixing zone of the blades for repeated classifeation. A barite was classified, the value Re was constantly 5450, and the residue was determined on a control:screen with 63 Graphic representations (Pigs 1-5) of.the experimental results show that the work with the c,lassificator (Fig 4) does not SOV/64-59-1--15/24 The Influence of Various Internal Devices in the Separator With Revolving Breaking Blades Upon the Efficiency of Classification offer.advantages but disadvantages, that the efficiency of the types mentioned in figures 1 and 2 is about the same, but that with reference to the residue on the control screen- the construction scheme of figure 1 is most adequate. A table of the individual data of the 4 types of classification Is .given. There are 5 figures, 1 table ,and I Soviet refereme, Card 2/2 AUTHORS: TIr1U PERIODICAL- ABSTRACT. Card 1/2 W1180-32-5-16152 Medvedev, A.A.,,, Re,5~.;gk Some Problems of the Analo~rj of Diffusion and Thermal Processes. Cominmication. I. Zhunnall P-ikladrioy khimii', 1959, Voll 32, Nr 5, pp 1021-1029 (USSR) The study of diffi-Lsion prooesses is based on the analogy between the phenomena of diffusion and thermal.co-nductivity. The difference of both przcce~5ses is irArestigeted here using the mass,transfer in a .binary solution. 11 r This mass ' ansfer is typical for many processes of chemical technology,especially in a solid body-liquid system. The diffusion coefficient-characterizes the spreading of concentra- tion in space and may be called coefficient of concentration conduc- tivity. The diff-Lsion coefficient D covers inertia as well as mass transfer properties of the system. It may be regarded as analogous to the coefL'icientlo4',t,--mpera,,ure-cordilct,Avity a, but not to,the c0-. efficient of heat-conducti-irityX . Mle criteria of thediffusion similarity are not complete azalogies of the corresponding criteria of the thsz-mal similarity. The criteria derived from boundary con- dition2, like Dful, Bi' and Ki' hold a special place. Inmost cases SOV/80-32-5-16/52 -':-"ome Problem of t-he AD a) ogy of D-4 Lffusf -D.-i vud 'ete-mal Processes. Commmication 1, tt'le criteri- 'NIul and Kil can b d-m em 1-led. La other:cases there is a numerieE~,l ellifferenne 't(aicah s ax~ s e d by th P. de-pendence of the p04'antlptl OfF, the r':'In-pcn,~!nt on its concent-ratio n. , Thanks to t:-,.C- appal 4 'ymn the of* thennoa irreversible processes mentioned c,-)n--l-aziom5 have a ?oientific base and suffiaien-I.-ly eTe ar--. 4 Fraphs and 21, refe-erx-ps, 5 of which are Soviet, 7 -man, 6 Er g I i sh, Fad ench. A-ISMIATION: LenInSrao-ski-,T tekhnologioheslkly inzti-.1at tmeni Lensoveta (Leni~md Tet7,~,ziologpl,%al Distitute '-fueni Le!^"Zcvet) SUBMITTED-. Leceleber 24, 1958 Card 212 5.116o 75663 sov/8o-32-10-12/51 AUTHORS: Siyrde, E. K.., Romankov, P. G. TITLE: Investigation of. Steam Distillat,ion (Communication 11) PERIODICAL: ZhUrnal prilcladnoy, Ichimli, 1959, Vol 321, Nr~10, pp 2197-2207 (USSR) ABSTRACT: This Is a,study of the variables affecting vaporization efficiency (P by means of dimensional analysis and experiment, Pt (3) P', where P1 Is the actual partial pressure of thesub- stance being distilled, and P 1 Is its equilibrium vapor pressure at the distillation temperature. The following substances were.steam-distilled both in two- Card 1/5 and three-phase systemsi CC14 (bp 76.8o c) C6 H6 (80"), _j1___1-__ _F~ Investigation of Steam Distillation 75663 (Communication II) sov/8o-32-10-12/51 C6H5CH (110 8), C6 H 3)2 (139.3), turpentine j c4 011 (154 6 , C H NH (184.4), c H NO (210.9), C H 6 5 2 , 1 6 5 2 10 8 C10H7OH (285-6), shale phenol (240-26o), shale tar (300-320), oleic acid (360, decomposes). The following Variables were studied individually, the other determining variables remaining constant: Fr; MlPl/M0P0; YL/r-, and 0-/TL;, SA/SO ; h, and DA/hOj where M1 is the molecular weight of the sub- stance being distilled, M 0 is the molecular weight of steam; SA is the-apparatus cross,section; SO is the sum'of the steam nozzle cross sections, DA is the apparatus diameter; h is the minimum liquid layer 0 depth, which will not affect.(P; 0- Is the surface 'ten-, sion; -( is the specific weight; and L refers to the Card 2/5 liquid. M lPl/M0P0.9 referred to as the composition cri- Investigation of' Steam Distillation 1-5663 (Communication 11) bUV/OU-j2-10-12/5l terion was experimentally shownto reflect the pro-_ pertles of the substance studied; consequently, the 'V, _.,U, (7, and Pr. of the distilling substance were, dropped from consideration. Three regimes.of bubbling were defined, and the following dimensionless formulas were derived. Bubble regime: D Fr-0.12 SA)0'28 A > 0.84, A10PO ff 1.0. fig) fodm~ regime: Fr-0.12 (ArIP, )0.28 (D 0.84 > 0.735, (13) V110PO ho T-IMP .r (MI Pj)-043 S A)&29 (LA )-0.45 Card 3/5 MAS ho - 11---l ~o I - Investigation of Steam Distillation 75663 (communication II) sov/8o~-32-10-12/51 Equations 19, 20, and 21 were also found applicable to, .the case of steam admittance through a grid; in this case S 0 is the sum of the grid openings. There are, 3 tables; 10 figures; and 10 references, 1 German , 9 Soviet. One Soviet reference associated with CaryJames S., is a 1937 translation of John H. Perry's Chemical Engineering Handbook (U.S.). ASSOCIATION: Tallin Polytechnic Institute (Tallinskiy politekhni- cheskiy institut) SUBMITTED: April 10, 1959 Card 5/5 G/002/60/000/012/00 1/005. Ao75/Ao26 AUTHOR: Romankov, P.G. (Leningrad) TITLE: Application of,the Similitude Theory to Studies of Chemotechnological Processes PERIODICAL: Chemi'sche Technik, 1960, No-12, pp. 699 702 TEM The theory allows to describe,basic operations of the chemical tech- nology as e.g. heat- and diffusion operations, hydraulic operations and chemical reactions. Similitude criterions: till now there are no uniform similitude cri-, teria. The existing similitude criteria should be used to describe experimental data. The criteria of heat transfer should be used on describing diffusion opera- tions. In the following a formula is derived characterizing the nature of-analogy between the classic equation .of diffusion by A. Fick and of heat c6nduction by Fourier. The application of thesimilitude theory to s tudying chemical,processes is difficult because chemical processes mostly are ve .ryIcomplicated. Th erefore a simplification of the chemical processes is necessary. An exact formulation of the limiting conditions is necessary for any mathematical description of a process. Soviet researchers have tried in the past to apply thermodynamical methods to the Card 1/2 G/002/60/000/012/001/005 A075/Ao26 Application of the Similitude Theory to Studies of Chemotechnological Processes analysis and description of chemotechnological processes. It is necessary to write the generally used Similitude criteria uniformly. There are 30 references: IL6 Soviet, 4 German, 6 American, I English, 1 Dutch, 1 Australian and 1 Polish. ASSOCIATION: Leningrad Technological Lensoviet Institute SUBDUTTED: November 24, !959 Card 2/2 S/153/60/003/005/014/016 B013/BO58 A 000 AUTHORS: Yablonskiy, P. A., Romankov, P. G. TITLE: Physical Significance of Some Similitude Criteri a, and Their Influence on the Heat Transfer Coefficient of Liquids PERIODICAL: Izvestiya vysshikh uchebnykh zavedeniy. Khimiya i khimicheskaya tekhnologiya, 1960, Vol. 3, No. 5, pp. 928-932 TEXT: The applicability of equations based on the theory of similitude for the practical calculation of the influence of physical properties of liquids on the heat-transfer intensity, as well as for thermodynamic calculations of chemical apparatus, is analyzed in this paper. The following conclusions were drawn from this analysis: 1) The calculation of 'the influence of physical properties of liquids on the heat-transfer J L .ntens4ty, customary in publications~ which starts from the functional dependence of the Nusselt, Reynolds, Prandtl and Grasho-f criteria, shows that the Nusselt index increases with an increase of the.Prandtl number, (Pr) and constant Reynolds.number (Re). The increase of.the.Pr number is, however, correlated with an increase of the kinematic viscosity v. This Card 1/3 .66289 Physical Significance of Some Similitude S/,53/60/003/005/014/016 Criteria, and Their Influence on the Heat B013/BO58 Transfer Coefficient of Liquids leads simultaneously to a decrease of the Re number. The actual consumption of liquid must, therefore, be increased to warrant Re = const. A calcula- tion made in this way of the influence of physical parameters on the heat- transfer coefficient is not justified in.practical calculations. 2) Thermodynamic calculations of chemical apparatus: a) At a given size.of., the apparatus, the liquid consumption can directly be calculated from the equations for turbulent and laminar flow at Pr = const., since the flow velocity is only contained in the Reynolds number. b) For the calculation of the influence of physical properties on the heat-transfer coefficient, the -index equations for turbulent, laminar, and free flows are to be brought into the form c~ = f(pr-n) or f,(Pr-m), at a constant con- sumption of liquid and equal d. From equations solved according to the heat-transfer coefficient c~, it follows that an increase of the Prandti number reduces the intensity of heat transfer at the same flow velocity. w. S. S. Kutateladze is mentioned. There are 2 Soviet references. 11A~ Card 2/3 86389 Physical Significance of Some Similitude S/153/60/003/005/014/CIV'- Criteria, and Their influence on the Heat B013/BC58 Transfer Coefficient of Liquids ASSOCIATION: Leningradskiy tekhnologichesk4y institut im. Lensove"a, Kafedra protsessov i apparatov (Leningrad Technological institute imeni Lensovet, Department of Processes and Apparatus) SUBIMITTED: Yarch 23, 1950/ Card 3/5 PLANOVSKIY, Aleksandr Nikolayevich; CUREVICH, Daniil Abramovich; MASANOV, N.I., retsenzent- ROMKOV, P.G., doktor tekhn nauk, Prof.v re- tsenzent; PAVIIUSHE~&, ~.khim. nauk,*dots., retsenzent; PASSET, B.V., kand. khim. naukcp retsenzent; AZBELI, D.S., red.; SHFAK, Ye.G., tekhn. red. [Apparatus for the industry of organic intermediate products and dyes] Apparatura promyshlennosti~organicheskikh poluproduktov i krasitelei. Moslowav Goakhimizdat,, 1961., 504 P. (M,IRA 15:6) (Dyes and dyeing-Apparatus) (Chemical apparatus) PAVLOV, K.F,;.-RO14ANKOV, P.G., prof.j NOSKOV, A.A.; KUROCHKINA, M.I.v red.; --T KOT 9 fax--S, r-edo)7=KHt Ye.Ya.9 tekhn. red. [Examples and problems for a course on thw processes and equip- ment of chemical technology] Primery i zadachi po kursu protses- sov i apparatov.khimicheskoi tekbnologii. Izd.5.9 ispr. Pod ob- shchei red. P.GiRamankova. Leningradp Gos. nauchno-tekhn. izd-vo lit-ry, 1961. 573 P. (KM 14:8) (Chemistryp Technical) -I ~,-:A 117- "1 "! -11~4:~- ~ " - . ~,. -- ~-Numw~w I . ~174xiqL - lli~tp Ma- - m 2 99C19 S/170/61/004/012/009/0',! B1b4/B136 AUTHORS~. Shih Yen-fu, Romankov, P. G, TITLE: Number of dimensionless complexes and simplexes obtained by the me~hcd of dimensional analysis PERJODTCAL: Inzhenerrio-f-izichoskiy zhurnal. v, 4. no. '12. 1961. ',02 1015 TEXT: Di,.,iensional analyses are a valuable means for setting up criie- rial equations describing a given phenomenon. The number of independent variables can thus be reduced. and the study concerned can be simplified on the of E~ Buckinghamis 11--theorem (Phys~ Rev,, 4, 345, 1914), 'Phe correct fL )rmulation and the demonstration of the Tt -Theorem have been studied by imany scientists (Sedov LI I., Metody podobiya i razmerncsti 7-i-ekhanike, Goskilimizdat, M,, 1957; Eygenson L. S,,, Modelirovaniye. Gos. izd-~ "Sc)vetskaya naukarl. 1-d., 1952; Van Driest. J. Appl- 1%1ech.. 1, 1-,~d6; Langiiaar H, L. Dimensional Analysis and Theory of Yodel~i. New York- Lc,lndon, 195,). In th,~ authors' opinion. the K-theorem was formulated m-c-st -~xact1y and :nosf completely by Sedov and Eygenson. A proof of this fcrmulation of "he T~tth=eorern is presented in this paper, The authors Card -,,/2 29599 S/- 70/6 1 /004/01 21'. 000~31'0` hImber of dimensionless complexes and BI 04/B 13, I-rom Bu~-,ki-ghamis formulation of the Jr-Theorem to d--mcnst-a~e o icrinL; verslon: An equation interrelating n physical quant-4ties am ng n be -trans- wni-~i there are k quantities having independent dimensions. cd fonmed arl equation that interrelates r.-k dimensionles,- complexes, and z;Impl.-~xE,s composed of n quantities. The number of dimensionless coMpIeYEE is equaI tc, the difference between the number, r. of quanTitiea with un~ like dimensions and the number, k. of quantities with -Independent dimen- ~ i QnS The number of dimensionless simplexes is equal to the difference Oetreen tine, total number., n, of quantities and the number, r, Of qUan~.L- ties -vr,-th unlike dimensions. AS this formul.ation agrees with Zygensorl's, ti-,e au*hors regrard at as correct.. There are 6 references~ 3 50r-iet ard 5 rion-Soviet. The three references to English-language publicatJons read fu 0 f (-., I I oSBuckingham E, Phys, Rev., 4. 34-9. 191A; Van Driest, .7. Appl- IoCn:' JOA6;.LanChaar Fl- L Dimensional Analysis and Theory of 11ode is. N-~w Y-orv--London. 195 1 G C I10 TekhnrjIcgichesV-.;y institut im, Lensovet.~ g, Leningrad "Te-ohnolog-1-ca-I Institute imeni Lensove- Leningra( L. UB" 7 TTED - T 196, KONOVALOVY V.I.; WMAXj~Oy,,_.P.G. FROLOV, V.F.; ROMANKOV, P.G. I -- 11 - - - -.: !'I- .. 11- 1~ , m - , ---- Rotlipi-allov), IP..G. ; RASHKOVSKAYA., N. B. ; GOLTSIKM, A. D. . - -1 1- -- - - .1. ~ - -.- 1-1 .. - -- ~ ~ w- - ROMANKOV, P. G.; RAS-llTOVSF-AYAJ 11. B.; FROLOV, V. F. KOZLOV, T.I., prepod.; KULIfl7,l',KOVA, Ye.Ya., prepod.; 0.10CHKIDA. p--,-epod.; LIEPILD", V.N',- MIEDVEDIX, A.A.; NOSKOV, A.A.~ OVECHKITI, I.Ye.; FAVLUSfENRO, I.S.; PLYUMIKIN, S.A.; RASHKOVSKAYA, N.B.;_J~g~J~I~KOV, P.G.; M-OLOV, V.F.,- YABLONSKIY, [Vanual on practical work in the laboratory on the processes and apparatus of chemical technology] Rukovodstvo k prakti- cheskiff. zaniatiiamlv laboratorii po protsessam i apparatar., khiudcheskoi tekhnologii. Izd.2., ispr..i dop. I!oskva, Khimiia, 1904. 2./+3 p. (MLIA 18:2) f+ I /M~Pllh-Y Pr 'I NIKOL'SKIY ) B.P., glav. red.; GPIGOROV, O.N.. doktor khim. nauk, red.; PORAIY-KOSHIT.S. R.A.,doktev~vi. nauk,,-rod4#~.oPUIN-041=10ifAwi.~ ft-aw ..Fred.;P ,OyANKOV, F.G. J- red.; FRIDRIKHSBERG, ji. A. ;kand. khim. nauk, r-eff-.,-MMTMTMH, V.A., kand. khim. nauk, red.; RACHINSKIY, F.Yu., kand. khim. nauk, red.; ZAYDELI, A.N., doktor fiz.-mat. nauk, red.; ZASLAVSKIY, A.I., kand.khim. nauk, red.; MORAGHEVSKIY, Yu.V., prof., red.; GRIVA, Z.I., red.; KOTS, V.A. red.; TOMARCHRIKO, S.L., red. [Chemist's handbook] Spravochnik khimika. -2.1 izd perer. i doj~. Moskva, Khimiia. Vol.4. -1965. 919 P. (MRA 19:1) 1. Chlen-korrespondent All SSSR (for llikollskiy, Romankov). !TGER E. 0. ; -1130t;Y'll p r Structural viscosity o--;' paste-like materials. Zlmur. khim. 11, 37 no.6:1279,1284 Je (!',!'RA 18:3) 1. Leninpradskiy tekhrololgicheskly instAtUL imeni- Lensakre-,,a~ RCNAHKOV, P.L~, N.B. l4c.dern rj,~ying t,~!-Jjilques and equir-Lumt, iri llhs~- Zhur.VKHO 10 no.lil8-25 165. 1. Gh1pn-korre8pondent AN SS.SR (.fcr qonkinkcrr). 37 I k 1 kh t Fetr Grigortyevich; R-'.~--:KOW~'KAYA, Natallya 113-or-Isovna; KW~GGFIJNIA, 'E.I., red. [Fluidized '-qd di- ying; theory) design and calculations] 3~3hka v kipiashchen! sloe; teoriia, konstruktsii, raschet. -len-ingrad, lzd-vo "Khizmila," .1964. 287 p. (PIRA 17:8) FAVLOV, K.F. ; RGILAk;hOV,- F.G.; P.A.; WvAigWINA, i-I.I.) red:7, I'C"TS, [Examples and problems for the course on the processes and apparatus of chemical technology] Friinery i zadachi po kursu protsessov i apparatov khimicheskoi RMAIRlogii. lzd.6.,, erer. 1 dop. Moskva,,Khimiia, 19(4. 633 jj- OMIRA 17: 10) p A14 13,'-ZR (for TIMMov). 'Ll V.; ROMAUKOV, P.G.; KONOVADN, V.I.; LYUTAYAi N.S. Study of hydrrAyntimics with-jut mlass tranBfer and In the presence of mass transfer in a rotor-disk e7tractor. Zhur. prIkl. kh.1m. 36 no.12%2672.-26SO D'63. (MIRA 17:2) 1. Leningradskiy tellinologicheskiy institut imeni Lensoveta. ROHANKOV,P.G.,prof., red.; KUROCHKINA, M.I., ved. red.; SAFRONOVA, I.M,, tekhn. red. [Transactions of the All-Union Scientificand Technical Conference on Problems.of the Theory and-Practice of Liquid Extraction Processes] Trudy Vsesoiuznogo nauchno-tekhniche- skogo soveshchanila po voprosam teorii i praktiki protsessov zhidkostnoi ekstraktsii, Leningrad, 1961. Leningrad, Gos- toptekhizdat, 1963. 383 P. (MIRA 16:6). 1. Vsesoyuznoye nauchno-tekhnicheskoye soveshchaniye po vop- rosam teorii i prak-tiki protsessov zhidkostnoy ekstraktsii, Leningrad, 1961. (Extraction (Chemistry))-Congresses) (Mass transfer) of (Drying apparatus) (Fluidization) -- I . . -1 - -L~~ 2 ROMAI 0 G., doktor tekhn.nauk; RASHKOVSKAYA, N.B., kand.tekhn.nauk; YABLOVISKIY, P.A., kand.tekhn.nauk; BEREZOVSKAYA, Z.A., kand. tekhn.nauk Drying of a pastelike copper-nickel catalyst in a fluidized bed. Masl.-zhir.prom. 28 no.7:10-13 JI 162. (MIRA 15:11) 1. Leningradskiy tekhnologicheskiy institut imeni Lensoveta. (Nickel catalysts-Drying) (Fluidization) Mm ! In - 1 . --T- ~-- Mvi-Mfir-v4~.,, fia (Adsorption) (Fluidization) ROMANKOV, P.G.; RAShKOVSKAYA, N.B.; MREZOVSKAYA, Z.A.; YABLONSKIY, P.A. ROMANKOV, ROMAN - KOV, Yu. Q "/076/60/034/008/027/039/XX B01 5/BO63 AUTHORS: Figurovskiy, N. A., Yomarova, T. A., and Romanlkov,,Yu. 1. TITLEt Effect of Temparatura on tho Cryetd1lization of, Calcium Salts From Solutions PERIODICALs Zhurnal fizicheskoy khimii, 1960, Vol. 54, No. 89 pp. 1826 1832 TEXT& As the precipitation of easily filterable substances is of great importance for practical analysis, the effect of various factors upon crystallization is frequently studied. The authors have now studied the,,. effect of temperature upon the rate of crystallization of MOV KBrO 31 KI031 KNOV K 2s0 4' and KC1..The supersaturated solutions were prepared Iby VI. M. Fisher's method (Ref-7), and c.-Ystall-ization was studied in a thermo- stat between 00 and 400C. The maximt-m rate of crystallization v was graphically determined from the kinetic curves. In all saltsit was found ~that v increases with temperature and with the super-saturation of the solutions, but is not always greater for those potassium salts which have Card 1/5, Effect of Temperature on the Crystallization S/076/060/034/008/027/039/y-.X~ of Calcium Salts From Solutions B015/BO63 a better solubility. The increase in v is attributed to an increase in the interaction among,ions with an increase in concentration and a decrease of. the interaction among water molecules and between salt ions and water 0 molecules. At 0 C, e.g., KBrO and KCIO have a similar solubility, while 3 3 the corresponding values for v differ !a rgely. KCI and KNO have the highest values of v. K 2so4occupies a special position since v is 0 practically independent of the supersaturation at 0 C. Besides, v in- crea:es on s lightly at a certain relative value of supersaturation 0ly 0 betw en 0 and 40 C, whereas it increases considerably in this range at two otherrelative values of supersaturation. The salts may be divided into three groups: K 2so4 and KC1 exhibit the greatestchange of v between 0 D 0 and 20'C; KC10 3 and KBrO3 show a linear increase of v with temperature; and KNO and KIO show a great increase of v between 20 0 and 3 3 0C. The temperature gradient k of crystallization which is given as I/V V v /(T + 10) T (1) (v and vi+j -.maximum. crystallization i i+1 i i i i Card 2/5 Effeci,of Temperature on the Crystallization S/076/60/034/008/027/039/XX '6f Calcium Salts From Solutions B015/B063 ~rates'at T. and T.. + 10, respectively), drops'with a rise Ofte=erature I 0 0 increases with supersaturation (cf. Table'2). Between.0 band 20 C, the 0 0 drop is more distinct than between 20 and 40 C.; With a rise of temperature, the effectof the type of anion on k is lowered, the mote the smaller is supersaturation. There are 6 figures, 2 tables, and,22 refer--,: fences: 15 Soviet, 4.,Indian, 2 US, and I German. ASSOCIATION: Moskovskiy gosudarstvennyy universitet im. M. V. Lomonosova (Moscor State. University imeni Ju. V. Lomonosov) SUBMITTED: November 27, 1958 Card 3/5 5/076/60/034/008/02~7,/039/U. -t u rt a2 T a G. 113.1teffelISIC TC31fICpaTVpuoro rpaAmIlTa Cf;OjjoeTCil NPUCTawRIJ.11~11a, COtCil upii pa3mmitwx nepecy,rutennax TotIfCPZITYPII14fI I'lWAIlorT k T01IMPATYPItUft rpa.-JUCLIT fria 'Poplyne (1)] 11 Gopayflux (110 IDOpMYne (If] ti 00[)aTfff-tX rpaivicax rpa;tycax OTHOCUTC.Iht[Oe IlepCCUuteltue t. ,c 7 X. - 0.05 X. - 0.10 X. =OtI5 0,0 to 0.15 KC103 KNO, 10-0 0,041 0,060 1 0,062 lo-o 0 047 01052 0,059 0, 90-10 0,029 0 039 0: om) 4 ~10-10 0 : 's 0, On 010ii 0,02-12 0:027 0 02 -0 0042 0,032 0,040 0,021 0, 02) 1 40-30 0,030 /g0-30 0,018 0,033 0,035 KDiO3 KZS04 i0--0 0 094 0: log Im i, 10-0 0 0 070 o,.150 0 olis 0 051 2j) 9 0:038 0 03" 30-20 0,031 0034 1),039 30-20' 0,0072 0 020 0:019 ~)28 _~_3 40-30 010-4 0,()- o,oj6-, 0 Oil 1 0,011 -card;4/5 RGq,aj-TIKOVA, A. G. PA 70T52 Medicine Penicillin "Antaganism Between-Hold Fungi," A. G. Remm.U.*OTa' Sci .Boo Lab, Citric Acid'Vorks, Laulmrad- _Pp "Mikrobiol- Vol ZM, No 2 .Hold'fungi, accompmted by growth and acid. formatim-, of Asp. iiigerin :non6terile ebuditims, are repre- seated by Penicillium- and Ampergilius-.11~~ made. Pen. rugtaoaum are Iaz itagmi-stic to Amp. nlgw. This-- 12 espeowly true when th4 f(irimer contain solutions of 15% eltric acid. GiTes other conclualms based m data obtained. Subzdtted 7 Aug 1946. 70T52. a SHISHKIN,B.K., professor; ROMANKOYA.Ak , kandidat biologicheakikh nauk, starshiy nauchnyysotrudnik; KM(N,G.B., doktor biologicheskikh nauk, dotsent; DANIMSKIT,A.S., kandidat biologicheskikh nauk, dotsent; SHTSYNBM,D.M.. daktor biologichookikh nauk; LOPAGINA.G aspirant; SEUI-HgKW,I.Y., nladshiy nauchnyy sotrudnik; ZHMIN, L.N., doktor biologicheskM neuk. professor; IPATOV,V.S.. student V kursa; VELOV,Y.Te., kandIdat blologicheskikh vauk, starshly uauchnyy sotradnik; NARTASHIV,A.I.. kandidat biologicheakikh nauk, starshiy nauchnyy sotrudnik; NITSUKO,A.A., starshty nauchary so- trudnik; VASILZVSKAYA,V.K.. doirtor biologichookikh nauk, dotsent; RTUNIN,A.V., kandidat.biologichookikh nauk; NAUMN.D.V., kandidat biologicheskikh nauk, mladshiy mauchuyy sotradnik-, KHOZATSKIT.L.I. kandidat biologicheskikh usuk, dotsent; GOROBUS,A.M., kandidat biologicheskikh n;Luk, starsh*y nauchnyy sotrudnik; GODLIVSKIY,V.S. assistent; GMILISKIT,N.L., doktor biologicheskikh nauk. professor; ALFJMANDROV,A.D., professor; KOLCK)TAZHNTT,V.I.; TURBIB,N.Y.; Z&VAD;- SKIY,K.M. [Theory of species and the formation of species]. Vest.Len.un. 9 no.10:43-92 0 154. (NLRk 8:7) 1. Chlen-korrespondent Akademii nauk SSSR (for Shishkin. Aleksandrov) (Condtinned on next card) SHISHKIN.B.K., professor; ROMANKOVA,A.G., kandidat biologicheakikh nauk, starshiy nauchnyy sotrudnik, and others. [Theory of species and the formation of species]. Vest.Len.un. 9 no.10:43-92 0 154. (MIRA 8:7) 2. Leningradskiy gosudarstvennyv universitet (for Shishkin. Romankova, Markov,'Ipatov, Koslov, Kartashev, Godlevskiy, Gerbillskiy, Aleksandrow) 3. Zoologicheskiy institut Akademli nauk SSSR (for Shteynberg, Nmmov) 4. Kafedra entomologii Leningradakogo gosudaretyennogo universitets, (for Danilevskly). 5. Kafedra, darvinizza Leningradskoea gosudaretvennogo universitete (for Lonagin, Gorobets). 6. Kafedragoobetaniki Leningrad- skogo gosudarst*ennogo uitrarsiteta (for Nitsenko). 7. Kafedra botaniki Leningradekogo gosudarstvennog6 universiteta (for Vasilevskaya). 8. Ka- fedra zoologii pozvonochnykh Leningradskogo gosudarstbennogo universi-, teta (for Khozatakiy). 9. Leningradskoye, otdeleniye Vsesoyuznogo in- stituta udobreniy, agropochvovedeniya i agrotekhniki (for Sell'-Beksan). 10. Institut eksperimentallnoy meditainy Akademil, zeditsinskikh nauk SSSR (for Zhinkin) (Origin of species) ROMANKOVA, A.G. ppra sa of natural substrata as media for the development of various groups of the genus Ponicilliwn. Uch.zap.Len.un.no.lql: 87-95 '55. (Penicillium) (KRA 9:7) ~~ ~,,: -~ -- 1- 1-1 -- ---- - - - --imf a (PENICILLIU14) (PROTEINS) (CHllSlt--BACTMRI0IDGT)