NASA-CR-135069-1976 Heat pipe materials compatibility《热管材料的兼容性》.pdf
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1、NASA CR-135069TRW 26148-6004-RU-00HEAT PIPEMATERIALSCOMPATIBILITYJ. E. Eninger,G. L. Fleischman,and E. E. LuedkepreparedforNationalAeronauticsand Space AdministrationLewis ResearchCenterCleveland,Ohio 44135ContractNAS 3-19128kNASA-C_-135069) HEAT PIPE MATERIALS N77-12182COMPATIBILITY Final Report (T
2、RW SystemsGr.oup) 46 p HC _.04/MF A01 CSCL 11F Unclas_3/26 56395January 1976% .jONILSPACE_ARK IIEDONDO BEACH.CALIFORNIA 90178i I1977005239Provided by IHSNot for ResaleNo reproduction or networking permitted without license from IHS-,-,-I r l )ti26148-6004-RU-00CTABLEOF CONTENTS SECTION PAGEmmm,_,ABS
3、TRACT ivl.O INTRODUCTION I26148-6004-RU-00t 2.2 PRETESTANALYSISiTo minimizetheeffectof variationsinmaterialcompositionon thegas-generationrate,allsimilarpartsweremanufacturedfromtubeor bar .-.stockof thesameheatnumberandallsimilarwicksfromthesamespoolofwire. All ammoniawas fromthesamecontainerandwas
4、certifiedat 99.998percentpurity(minimum).Pre-testanalyseswerecompletedon thefabricationmaterialsselectedforthisprogram. Photomicrographsof polishedandetchedspecimensweretakenwith an opticalmicroscopeat magnificationsup to 500Xandcomparedwithhandbookmicrostructures.A lotof selected304stainless-steelt
5、ubingwas eliminatedaftermetallurgicalexaminationrevealedthetubingwasnot seamless. Samplesof thealuminumandstainless-steelwerealsoexaminedwitha scanningelectronmicroscopeatmagnificationsup toIO,O00Xto aid in theinterpretationof theopticalmicrographs.All,w_terialscomparedfavorablywith handbookmicrostr
6、uctures.Inaddition,samplesof thematerialsusedin fabricationwere subjectto chemicalanalysis,whichconfirmedthatthematerialsallconformedto handbookspecifications.Analysisof theammoniabyan independentlaboratoryshowedthatintheliquidstateallcontaminants(H2,H20,N2,02,A, C02)were lessthan10 ppm,whichisthe l
7、imitof detectionfortheanalysis. Inthegaseousstate,1.9ppmof hydrogenandO.lppmof nitrogenweredetected. Therestof thecontaminantswerebelowthelimitof detection,which,forthegaseousstate,is 10 ppmforwaterandcarbondioxideandO.lppmforoxygenandargon.2.3 FABRICATION,PROCESS_NDFILLThefabricationandprocessingof
8、 theheatpipesaredescribedin themanufacturingflowchartsand theprocessingspecificationsin theAppendix.ThecleaningprocedurePR2-28-I(summarizedin Table2.2)is a seriesofultrasonlcsolventrinses. Thiswas TRWsstandardheatpipecleaningprocedureat thetlmetheheatpipeswere fabricated.i “8-1977005239-011Provided
9、by IHSNot for ResaleNo reproduction or networking permitted without license from IHS-,-,-r r!?26148-6004-RU-00S,_hcequently, a chemical cleaning procedure (CRP7-12 for stainless steel and CRP/-IO for albminum, in the appendix) was prepared as recommendedin 6forevalumtionin thisprogram. On TRW IR ,LI
10、 iPR2-28-IJ US-FILTEREDSOLVENTS. PR13-6-1ULTRASOtlICCLE_NIN FREONTF,HINIHUMOF 15 MINUTES., DRY iN VACUUMOVENAT 212+_FORM!;I.!UMOF 5 MIrIUTEStCULTRSOIiICCL,.ANINACETOIIE,MINIMUMOF 15 MINUTESDRY IN VACUU4UVE;i;T212+-?OeFIFORMItlIHUMOF 5 HilUTESii i i i,i_ MINIMUMOFlS MIt!.UJESIll I IFORMIIIIMUMOF 5 RI
11、NUTES: T _ 1i ii JJ L =: STOREINSUITABLECONTAINERIITable 2.2. AssemblyCleantng Procedure7, -11 - , , J1977005239-014Provided by IHSNot for ResaleNo reproduction or networking permitted without license from IHS-,-,-EI= I=_= _ o o o o_ -12-1977005239-015Provided by IHSNot for ResaleNo reproduction or
12、networking permitted without license from IHS-,-,-iI2.4 TESTING_ Exceptwhenthetemperatureprofilesaremeasuredat lowtemperatures,theheatpipesareruncontinuouslyat theirrespectiveoperatingtemperature(seeTables2.1and2.3). Periodicallythe heatinputto theheaterblocks_j“Fted t(maintaintherequiredtemperature
13、.As noncondensablegasis evolvedduringoperationof a heatpipe,it iscarriedto thecondenserendcausinga blockage. Thequantityof noncondensablegas iscalculatedfromthetemperatureprofileof thegas-blockedregion.The profileismeasuredwiththeheatpipeoperatingin a -40Cenvironment,whichis providedby a freezer. By
14、 loweringthevaportemperature,andhenceitspressure,thenoncondensablegasexpandsto filla largervolume,andthusit resultsin a largertemperatureprofile. Thisis illustratedin Figure2-4,wheretheGASPIPEIIcomputerprogramwasusedto generatetwotemperatureprofilesforthesameamountof gas (l.OX lO“7 Ib-moles),butdiff
15、erentoperatingtemperatures.Forcalculationof thequantityof _ds,thecondenserregionisdividedinto N intervals,andthetemperatureat thecenterof the ithintervalisdenoted Ti. Thenumberof moles n of noncondensablegas isgivenby the idealgas lawasNi=lwhere V is thevolumeof eachintervalavailableforgasandvaporan
16、dR is theuniversalgasconstant. Thepartialpressureof gas, Pgi is thediferencebetweenthetotalpressuregivenby thevaporpressurePva of ammoniain theadiabaticsectionand thepartialpressure Pviof vaporin the ith interval. A computerprograms usedto calculatethequantityof gasdirectlyfromthewall-temperaturemea
17、surements.ThemeasuredtemperatureprofilesandcalculatedgasareshowninFigure2-5and2-6fortheparticularheatpipeS/N25,whichis allalumlnumand isoperatedat 80C. Thisdatais typicalIn thatthe initialT gas-generatlonret_ Isrelativelyhigh,andAftera monthit levelsout.t-13-1977005239-016Provided by IHSNot for Resa
18、leNo reproduction or networking permitted without license from IHS-,-,-I, ( ! +_,“ 1 I-,L+-I oi (Lt .+-f,- .r-_C_ _ q.l.- Otl OJ “ (“),S. _ . c- _ 0E .,- _ _ _ 0n_ _ l _ U 4J, c) S.- _ _ _ C_r- 1 _ 1-r- O c“ c- O “_“OI_, n 0 0 u o oo0 0 _ _ 0 n 0 _ I- _/_I- _o o O o o DC_ CD cD D cD o cD cD o CD o_,
19、-_ ,_i _ IU I O_ (“O 0“3, ,-.- I_ OOC CO I_ O l.A“): r_ ,- _ O_ 1.13, ,-.“ ,-,-. N oJ _ ,-o,im ,o u:; oJ ,.- ,J + ,.-Ico ,- e.,L _. _._ _O Q O C2 O: OC_ CD D CD _ D 0 C_ CD 0 CDo_o_ +_ ,-.- ,- ,- ,- ,.-. ,-“I ,- ,- i,- ,- o x _ +* _ _ -_. ,._ _ .I _1._ ,.-t,_ d t_ ,.- c_. ,:l.c,i ,- ,- _ c_ c,) ,_ +
20、c,-)i ,“) ,.,o u:)+ LI, I.- (D. _:= IO _ 8 _,._ CD _D CD O C_ + CD O _0 0 0 _1.) O0 CO _ CO ,.- _ CO + CO O0 CO.s _ o. cO oo_ oO oO co O co ooI!+ +,+ -,.+.,- . - _- _ t- t“ t“ E-i-, i,.,- i,- .i,- .r-“ +i“-“ -i-“_. _.,- 8 oi _ o o o o or=. ., , _ ._ o ol o o _ o o o,_ _=- I E .0 O 0 CD _P- CD _DE _.
21、 m_ I “P“ _ I .,-, t._ 03r _ C_+- I.-._L I _ _ I I I I I I I I i +_“_ OP“ 0_I_)-14,-1977005239-017Provided by IHSNot for ResaleNo reproduction or networking permitted without license from IHS-,-,-O-15-1977005239-018Provided by IHSNot for ResaleNo reproduction or networking permitted without license
22、from IHS-,-,-26148-6004-RU-00I I I I I I I I I i _.m,-.-?1977005239-019Provided by IHSNot for ResaleNo reproduction or networking permitted without license from IHS-,-,-!Iir26148-6004-RU-00An overallgasgenerationrateof 5.8x lO“lOIbm/day wascalculatedby a least-squaresfitof a straightlineto thedataof
23、 Figure2-6past3u days. Thedataforall of theheatpipesare summarizedin Table2.4.Detaileddataforeachpipeat eachmeasurementintervalis presentedinTableA-l in theAppendix.k.5 POST-TESTANALYSISPost-testanalyseswereperformedon oneof each typeheatpipetested: AI/SSwick (S/N8),Al/Alwick (S/N27),and SS/SSwick (
24、S/N39).HeatpipeS/N12wasalsoanalyzedto determinethesourceof a leakwhichcausedthepipeto failin test.Massspectrometrygasanalyseswereperformedon ammoniasamplesfromheatpipesS/N8 and S/N27 to determinethenoncondensablegasorgasesgeneratedduringtesting. Valveswereattachedto thetwopipesto alloweasy removalof
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