SCIENTIFIC ABSTRACT STOROZHUK, YA.P. - STOTIK, A.M.

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CIA-RDP86-00513R001653410018-2
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December 31, 1967
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SCIENTIFIC ABSTRACT
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A. il. of Stll~, r lf~ c tr ic tlm* rospirrAor"r f A C~,t. zt,~Ir. 49 :1145-1352) 1. L.Io.-Acriyu flziolc~j-lli Inctitilt-a f"ZiolrizIl Jr.q.:11 A.A. SILRULN11K, V.M. N the 44~ Iked - !~tentlsl of the -eribvtj cortex w1th Initial nqgHtIvity. Fizial.thu.-. 50 no.lz2O-25 Ja 064. (MIRA 1841) 1. Laborst-orlya elski,rcCiziologii Irst4.tA4,A fiziologli Im6ni A.A. Bwr,aol1'.9a AN Ukr.,~-, Kiyev. V J. Lo (1)"ont)i Cbervyakova, X. 1. (Candidate of bioloi;ical V4n ;'yt (Ampirant)i ValyavskAirs. M. T*. (Fn4lnear); raushanskaj%, 5torothuk. V. 1. (&gIAo*r)j 'serlstakaya. 1. A. (MCIns' (Ln4imor) non.] 3oircri for now op"ratihC conditions In sterilItAtion of ~&AnW goods for pra_'~-cted continuously operative equip"nt Mnistorstyo vywshov-o i smlnoro spetsUllnogo *br&&*v&nIya. promyshlonnosLI, no- 31 1~~. 10)-112 74'ZI food to chnoloj-y, food proearvation. fload storilitAtioA. applied food product machinory. processed plAnt product ';-w oporative conditions for starilittr#4 0-or-ato 4uloo In " Oderas factory '.'Orcol oitt. at the 016s#4 Uchnalogic*1 Inatitutp for the Food &M Refri4oration -try, b4swi on a continuous operation (see IFIr4re 1) with successive best Ing cooll.n.: of 0.5 and 0.2 litor battles fUled with juice at 80-83 C and Imersod in of various temperatures. Dig atariUzation tem;eraturte tested varo too, 95, nessurod with thors"OUPU. Dig C. -Ptaparaturoe bottle *enter wer* a in the ar.1 92 Card ACC NA A-,1;02'/l ~6 .. ~VA, Figure 1. Schematic representation of continuous sterilization dalvi w,)re mthanatic*111 processed according to naueenbamm, a. 1, (P%sbchev&ya tek~nolozly.-- 3. 1959). Zarlier studios on survIT&I of x1croorganisma In tomato war* also conoldored. Ike formulas arrived at were exp*rUwntAUy tested. Ike general foruula applAod, was A (KA. + ICA. + KA. + + KA.~' Lc-,,i C foc ~t, T is tho t1r.- int-rvail wi r i-% r--M-I ~1~e I-nrnxW1z1n*, rop,'flc~.-nt. ",n valet of w.s .-I .:- 1',,'Ator fo; storthrAtion. r, !-"-~rn -i 2S P%Ln for 90 C or 1-2~ ?%.r. f'-r ir vr-'(,7t coul-I b" ohtatr^-1 :6': f4zt~?- A,. :Z,~ C --jj 'n,' 0.2 'bott'Aw 4'. L)"O sano t"j-r4turo. ior 'Ln-P 'I:,aros uaro empArAble to or hl.-.1hor than the 21der orms. 0' -ho stnrilir-ition fornulAs ul*.h luice Infoctwl viuh Panicillium ,is niz"r. yeasts and Bac. rAsontftricus ruber. then sterilized AAM kept at roam tonporstura for 3 months or at hl.~hor k-01 dAyl. r4VO SAtisrse.-tory rowsults. 2io forAulAs vorkod out or* A~',l W C Poml for the 2 #Ito* of %,ottlkas. 'Zius for 0.2 liter bottles 00 C. uh-re the first fliuro IhJkCAtO* that the ;,rf.--ess peo;~-tr is starting. the soconl gives the storIlIt4tion period. &r.1 fifth give sto;wdisa coolln* In water betho of 60. 60 tnat the formulas found he o- I goon proved reliable in t,)sts. Orig. art. hast 10 fl4uros and 8 tomulos. (ZW SUM DA-M rArw/ ORM RVI 0041 am Wo 001 STOR)MUK, U.P., kitnd. tnkhn. nnuk; "IM,75KIT, Z.H., krinl. toik-hn. nai& Himning, fuel oil in the convyustion chamber of gati-turbine Installations. Unnrgomashinnstro4nis 4 no.10:24-28 0 158. Was turbinam) (MIRA 11:11) s/ii4/62/000/003/001/005 A(;T,'IuR; Candidate of Technical Sciences T IT LE The operation of multi-swirler gas-turbine combumtion chambers burning liquid fuel PL-1110DICAL: Energomashinoi%troyeniye, no-3s 196"", 3-7 TLXT: As combuAtion tube diameters increase, the effective- ness of single swirlers falls off and combustion efficiency is it:paired; accordingly multiplo swirlers are being used with large combustion chambers. The TsKT1 has tested three geometrically similar combustion chambers with flame tube diameters of 640. 510 and 4oo mm. The tubes were made of steel 1 1,1 IT (EYaIT), and the tube head carried five cylindrical swirlers with profiled blades installed at an angle of 6o0. Below the head came five conical shells which overlapped with gaps between to admit cooling air. Air from the compressor liaving passed through the air heater is delivered to the bottom of the chamber outside the flame tube. lt enters the tube partially through a mixer located below the conical shells. partly Card 1/4 The operation of multi-swirler ... E194/E155 through the gaps between the conical shells and partly through t1he head. To Improve cooling, the top two shells were ribbed and then firing rates of about 30 x 106 kcal/m3 hour.atm could be achieved with satisfactory combustion. Wien necessary the primary and secondary air supplies could be kept separate. The temperature distribution was measured and gas samples were tests were run on diesel fuel with excena-air analysed. The factors between 1 and 2, with an Inlet air temperature of 100 to 300 OC at an inlet Pressure of 1.25 to 3.8 atm, with a fuel CODSUnIjition of 136 to 490 kX/hour and an exhaust gas temperature of 6do to 700 OC. Single-stage centrifugal nozzles were used. Thr process of fuel combustion was practically identical In all three chambers over a wide range of gas flows. To assess the effect of pressure, tests were run in which the pressure alone was varied, usually between 1.5 and 3 atm, and within this range the nature of combustion was identical for all the chambers te5ted. In multi-swirler combustion chambers the fuel is well mixed with primary air; combustion is complete near the burner throat and the flame temperature is high. The main factora that Card 2/4 'ne oi~eriition Uf multi-swirler s/114/621/000/003/001/005 E194/EI35 limit t!ie rate of f iring are the chanber diameter and the rate or 'Sir f lour at discharge. from the swirlers, which governs the titz-bit lence. The smaller the chamber diameter (and naturally, therefore, the diameter) the greater the maximum possible r.ttc of' firing for a given rate of gas flow. The combu3tion efricleticy can be re-presetited in terms of the same parameters an those used by %.G. Woodward (Ref.2: Sixth Symposium on Combustion, Re in' provided that they are written in I ~iold lub. Corp., 1957), terms or thp rate of riow of air (by weight) at discharge from the swirlers. The distribution of air between different parts of the combustion chamber is disciassed. As the ratio of the air inlet to the discharge temperature alters, the air distribution alters because of' differential. expansion of the chamber body and the fire tubes. The cooling air was not uniformly distributed ,Ijnojlg the slots between the conical shells; and because the expansion is greatest where the metal is hotter, the parts that require most air receive least. This point should be allowed for in desisn. The flow structure was identical in different ,coractrically similar combustion chambers. The axial velocity Card 3/1, The uiwration of rmilti-swirler S/114/62/000/003/001/005 E194/EI55 ,listribut ion is practically sectiun. The tests provide processes or mixing of individual with pulverized fuel and so influence on the process of multi-swirler chambers. There are 7 figures. symmetrical acrosts the chamber a qualitative assessment of the layers of gas-air mixture make it possible to assess their combustion stabilisation in Card 4/4 o f al'a 1; aO Oo on t; U 6111--li-42'1000100410C 1 '008 E 114 /!;,L 54 No, prit-I error r: Cq w, AI W d C;I~. o o r, v v~,, vy n~; J T) thl~' rZ3,31 L ~Icl ;.-i0oth o-com nt 1; o r.-A t empe, ra ture f; i on there was Of ca r. temperature It).- 0 f '-,-14.,. ".I t jcon.,.O.'aal., ;~,crmai loading, ~I;kce~;j ~-mEl Inlet a.'r witli -al,e,;noldls number in ik.-~uLjr FyAp weLve left to vary with presoure. Although ~Lj-y of' C0014n-- aj- -re increa6ed wit'a pressjxe, 4-1 q,j j r of the burner hv~.-acx and the fIrs"11 segmento which *Wkulile ODD03ite the zones of incomplete comba.,;Z;io.,i rose ("a rd 3? 41 i -,,~A 2/C,00/004/001/008 X. -114 514 6 011 f r 0 MA 0 0 6 p 0i, of 3000C 0 U IA ILo X'L 10 norirest the o thr.- cold :4 uloi* `ro~i uiv jl,ii,U; exposed un ;oo The ~r~~a ly x-, uenced by I;Onv;~(;t.lon on Li.~! S-ku~,* bY LIVI I),'10.-;iA e 0 Vr 'I;.; i u b ecoc~lino improved by tlie (;I1111',Aon oAr ,,o*6 'maseS by coolin.; air t ough I hr L A..!: ~ 17 1'31 fle,~ A,; rl,~ 1; 0 wall I A from 'C"; Ion wa: Nu 0.03 Conv, I Re where th--~ effe-ot;ive Rf!yno'd.-; nwaber. J% nomogram is given to tz,e maxiiau;a ;eza.pera Lure of 'VeAe flamu tube segments. Card 4/4 STUPI)ZHUK, Yrt,P., K rind. ts4, hn. nni.~r . ANP'NC'q'SKIT~ V I , 'Anzh. I wammmmm~- Methorim for c,%I'(-,ulottAnv ~hp mnximum temperature of the flues of the comblisticn chamlerp of gma turbine ayst,~np opornting on 11pid , fu,pl . Fnergomashinn5tr..-4~naf~ 1) r,,.,. 1-47-44, J'I '63. (?rARA 16:),) (Gns turbines) ACCESSION NRa AP4007443 S/0096/641000/001/0039/0063 A777!07: _.S_i~9r.qzhuk,_Ya. P. (Candidate of technical sciences) Aioskov, V. A. (Engineer) TITLZ, Problem of approximate modeling of the combustion processes in a GTU (Can turbine unit) combustion chamber SOURCE: Teploenergettka, no. 1, 1964, 59-63 LoriC. TAGSt gas turbine, combustion chamber, combustion process, combustion process modeling, liquid fuel combustion A35TRACT: SI-ilitudc laws for ncaling-up gas turbine combustion chamber models to full-scale units are analyzed on the basis of a generalized relationship for the combustion efficiency in terms of fuel droplet residence time in the combustion zone; full combustion time; evaporation, mixing, and burning times; Reynolds, Karman, Mach, and Prandtl numbers; fuel and air temperatures; air excess factor, and activation energy. From a previously derived relationship for the evaporation time (Yu. Kh. Shaulov, H, 0. Lerner. Goreniyc v zhidkostny*kh reaktivny*kh dvigately4kh, Oborongiz, 1961) the "~,-d 1/4 1 ACCESSION M AP4007443 following criterion for the complete evaporation was derived: Wev a 9 where C Is Y273/SDRO(tk + 273), dk Is the characteristic droplet d I ar! !ter , Lf i is t e f lame-tube length , tk is the vapor temperature , y is the specific weight of fuel, D., is the diffusion coefficient at O'C and 1 atn, and wav is the average gas flow velocity. The Invariance of the ratio of mixing time to residence time with respect to Pe, Fa, H, and Pr is examined, and sclf-modeling regions of Re and Ka are defined. It is concluded that for modeling of a diffuSiOnAl conbu5tion process in chamberi operating under self-moldeling regimes wtth :espect to Re and Ka# the following conditions must be fulfilledi 1) the nodel and the full-scale unit must be geometrically similar; 2) the fuel must be of the same type and have the same temperature; -ind 3) the fuel-air ratios, the temperatures of air and combustion productm, and the evaporAcion crtterLan wev inuat he tdontLVAls Thp Card 2 /14 ACCESSION N'R: AP4007443 results are illustrated by data obtained previously (Yao Pe Storexhuko "ner,-onashinostroyentye, No. 3, 1962) by the combustion of atornized solar oil in high-output combustion chamber models 0.61, 0.51, and 0.4 m in diameter. The graphs (see Fig. I of Enclosure) show that the combustion process was almost identical in all three chambers when the specified modeling conditions were fulfilled. Orig. art. has: 17 formulas, 3 figures, and 2 tables. ASSOCIAi1OXi Tsentral'ny*y kotloturbinny*y institut (Central Boiler- Turbine Institute) SUBMITTED3 00 DATE ACQ: 23Jan64 ENCL: 01 SU3 CODE: PR NO REF SOV: 003 OTHERt 000 Ca,d 3/4 5/0W6/6h/oW/00~'0039/0042 ;!0:1 ;Q-1i AP4012339 A'o-M'0iZi Storozhuk, Ya, P. (C"idate of ttechnJcal sciences); Antonovsklys V. I# (aiginoar) A, attidy of Uio onis3ivo pruportio3 of a flamo in a single dapper combus- tion cliarrboo of a Cai turbine SOORCEo Tej)looncrj-,ot1kn, no, Z, 196hp 39-U !A6.-jj flamo omisnionp combustion chanber, air pressurej excess air COO:ficlanb, amisslon diotributionj flue coolinG, platimim platinum rhodium Liioriwcouplo, vacuum radiation thermal element, thermal radiation flux,, gas blacknoss, Infrared radiat ion ABS' =Ti Ono of tho problore uldch arose with the construction of the experl- menW gas turbino combustion chamber was the cooling of the fluo motal. The development of a reliable mothod for calculatine the wa1l temperature was hxqe6d by the absonce or experimental data on the emission characteristics of f1wa. Experiments ware conducted varrizw, several paranoters (principsUr the air pressure and tho coefficient of excess air)* The chamber. had a divided air nTply ror 1A ACCESSIO14 M AA012339 I independent control of primary and secondary air. Two types of flues were studied., both 364 mi in diameter and joined to a transition cone. One flue was continuousi the other in 3 sections,, with a 4-m annular Cap between sections. For experimen- tal purposes 2 dampers with a 450 and 520 tUt were available. Diesel fuel was sprayed from a centrifugal single-staGo Jet with a 750 flame. The variables of ths~ air and fuel, the flame temperature, the normal total thermal raiiation and gas com,osition wore measured. The latter three were taken at the same cross section at t points along the flue, The flame toq)orature was measured with a auction platimtm jilatinum-rhodium thermocouple, The rross flame radiation (luminous brir;htnoss) wazi measured with a vacuu;4 radiation thermal element (RTE) Vith 2 sensitive elements, one of which was used for comparison of the surrounding temper-.; aturo, It was sonsitivo"to inrrars.-d radiation in the band 0*18-11 tA vldch vas suitable according to the stantards of D. 1. Weeks and Os A, Saunders (Journal of the Inst, of Fuel,, No. 209., 1958). The proscribed normal operating conditions 6 wore: volumotric thermal stress; 4 8 x 10 largo calories/m%hr atmosphere, excess coefficient or primary air cK 1,15-1,8, air flow rate up to 5500 kc/firs air toiVoraturo at chamber inlot ti) 60~200C, pressure in Uio chamber p a 1.05- 2.0) atriospheron, and temperature of exhaust eamos tOx 500-740C. The exporizon. .al installation permitted variation of each parameters The firat studies varied 21% 'S 1 ON UR ti,o a,ir coafficiont. Tho radiation incroasod to a Creator extent. In the stNatlnjiD of the fluo atyl with lower air (;.,I'- - 1.2-1,5),, An increa3o in 4Ai,j iiitako air teq)eratiro lod to a docroano in ti-j.) radiation at the measuring v-, a rest0t, of tho rhiftir4; of the active (:,) 17!f3tion zones to the flano roo". The next -.tudy (corKlAict(Y.1 only on the spi:monted fluo) varied the charb(T The radiation charply increazod with an increase in prossuro at the firsL 2 meanurAng pointap ejpocially with 4 snaU 0 0,90 M posterior 4 7,5 0.4 t 4.3 0.41 I >ONO &23j-0.6; A 403=0.64 O.SO Com , aupragtIca I d orsa a -~ Con tro I o 3 S.13-4.43 7.33-:-0.73