Tsiba kwisiqulatho main

k = isoentropic exponent

Ukubaluleka kwe  k  kwivalve yokhuseleko

ihlelwe ngu-Alessandro Ruzza 

Ubungakanani beevalvu zokhuseleko ezenzelwe ukukhupha iigesi okanye imiphunga, ngokwe-lspesl Collection "E", ifuna ulwazi lwe-isoentropic exponent k kwiimeko zokukhupha.

Ukusetyenziswa ngokungakhathali kwe-lspesl Collection "E" isahluko "E.1", ngokumalunga nobungakanani beevalvu zokhuseleko, kunokukhokelela ekugqithiseni ukugqithiswa kwamandla okukhutshwa kweevalve kunye neediski zokuqhawula.

Eli nqaku linika ezinye izikhokelo ukuqikelela ixabiso k kuba iigesi yokwenene kunye
ibalaselisa impazamo ngokuqwalasela u-k olingana nomlinganiselo wobushushu obuthile beCp/Cv

Impazamo yokuqala nenzulu ekufuneka iphetshwe kukusebenzisa ifomula ekuQokelweni kwe-'E', esebenzayo kwiigesi okanye umphunga, kwiimeko apho ukukhutshwa kwezigaba ezibini yolwelo kunye nerhasi/umphunga yenzeka. Kwiimeko ezinjalo, ngokwenene, i-diameters ebalwayo ngokuqinisekileyo iya kuba ngaphantsi xa kuthelekiswa nesidingo sangempela.
Impazamo yesibini, apho kwiimeko ezininzi inokukhokelela kwi ukunciphisa inkqubo yokhuseleko, kukunika i-isoentropic exponent k ixabiso lomlinganiselo we-Cp/Cv. Ngelixa inqaku lokuqala liya kuba ngumxholo woluhlu lwamanqaku alandelayo, apha singathanda ukunika iingcebiso eziluncedo ekubaleni i-isoentropic exponent kwaye sibonise, kwiimeko eziphathekayo, ubungakanani bempazamo enokwenziwa.

Ukuphuma kwe-isoentropic ngombhobho

 

Ifomula [1] esetyenziswa kwingqokelela “E”, nakwesinye isiTaliyane [2] nakwamanye amazwe [3] standIiardi, ekubaleni iivalvu zokhuseleko ekufuneka zikhuphe iigesi okanye umphunga, yileyo yokuphuma kwe-isoentropic ngombhobho phantsi kweemeko ezimandundu zokutsiba, ethi irhasi efanelekileyo ibe:

Ingqokelela yeFomula lspesl “E”

apho i-expansikwi-coefficient C inikwa ngu:

ukuthumelaansikwi-coefficient C

ukuba k i-exponent ye-isoentropic expansikwinxaki: pxv^k=indleko

FluidI-P1 (bar)T1 (°C)q' (kg/h)q (kg/h)(q'/q) x 100
IMethane125014721466100.4
IMethane2320023142267102.1
Ipropane1210022612181103.7
IHexane1217830992740113.1
IHexane2322065195111127.5
IHeptane1221532322821114.4

q'= izinga lokuqukuqela elibalwa nge k = Cp/Cv (20 °C, 1 atm)
q = ireyithi yokuhamba ibalwe nge k = (Cp/Cv) • (Z/Zp)

Ngokuzisa i-coefficient yovavanyo k Ukuphuma kwevalve yokhuseleko, ethathela ingqalelo ukusebenza kokwenyani kwevalve, i-coefficient yokhuseleko ye-0.9 kunye ne-compressibility factor Z.1 kulwelo lokwenyani, sifika kuqulunqo lwengqokelela "E":

(1) [1]

I-isoentropic exponent k inokubonakaliswa ngolu hlobo:

[2] [2]

Ku igesi efanelekileyo, nge P x V / R x T =1 , kuboniswa ukuba k ilingana nomlinganiselo weCp/Cv phakathi kobushushu obuthile kuxinzelelo oluqhubekayo kunye nomthamo.

Ye igesi yokwenene, k inokubonakaliswa (jonga kwiSihlomelo B) ngokuthi:

[3] [3]

apho u-Z ngumba woxinzelelo oluchazwa ngu-Z=P x V / R x T kunye ne-Zp "yi-derived compressibility factor". Xa usebenzisa ifomula [3], ngokwengqokelela "E", amaxabiso eCp/Cv, Z kunye neZp kufuneka avavanywe kwiimeko zokukhutshwa P.1 kunye T1.

I-derived factor compressibility factor Zp ichazwa kwifomula [4] njenge:

[3.1]

I-compressibility factor Z inokubonakaliswa ngolu hlobo:

[4][4]

kwaye ngokufanayo, inokubonakaliswa ngolu hlobo:

[5][5]

apho amaxabiso okuthi Z^0, Z^1, Zp^0, Zp^1 adweliswe kwiSihlomelo A njengomsebenzi wePr kunye neTr.

In [4] kwaye [5], Ω yi Pitzer's acentric factor echazwe ngu:

[10] [10]

Apho iPr^SAT luxinzelelo lomphunga olucuthiweyo oluhambelana nexabiso lobushushu elincitshisiweyo Tr=T/Tc=0,7. ISihlomelo A sibonisa ixabiso le-Ω lolwelo oluthile. I-Z e inokuthi ithathwe ngokuthe ngqo kwi-equation yohlalutyo lwelizwe.

Umzekelo wamanani

 

Ukuguqukela kumzekelo wamanani, cinga ukuba kufuneka sibale umthamo wokukhupha wevalve yokhuseleko phantsi kwezi meko zilandelayo:

Fluidn-Butano
Imeko yomzimbaumphunga oshushu kakhulu
Ubunzima bemolekyuliM58,119
Misa uxinzeleloP19,78 bar
Uxinzelelo olugqithisileyo10%
Ubushushu bolweloT400 K
I-coefficient ye-Efflux0,9
Idayamitha yeOrificeDo100 mm

Uxinzelelo lokukhupha lunikezelwa ngu:

ukuba ye-n-Butane: Tc=425,18 K kunye nePc=37,96 bar, si:

kwaye sisebenzisa iitheyibhile ezikwiSihlomelo A, sinazo:

Ukwazi umthamo othile womphunga kwiimeko zokukhupha (P1, T1) ilingana ne-0,01634 m^3/kg (0,0009498 m^3/g-mole), sinokubala i-Z ukusuka kwi-:

Ukunika umlinganiselo wobushushu obukhethekileyo kuxinzelelo oluqhubekayo kunye nomthamo, kwiimeko zokukhupha (P1, T1), ilingana no-1,36, ukusuka kwifomula [3] si:

147060

Ukusebenzisa ifomula [1], ngokubala izinga lokuhamba

Ukusebenzisa ifomula [1], eyasonjululwa ekubaleni izinga lokuhamba, sinexabiso lokukhupha isantya sokuhamba I-147.060 kg / h.

174848

Ukusebenzisa ifomula [1], usebenzisa ixabiso le-Cp/Cv kwi-1 atm kunye ne-20 °C

Ukuba endaweni yoko sisebenzise ixabiso le-Cp/Cv kwi-1 atm kunye ne-20 °C, ngese k = 1,19 kwaye ukusuka kwifomula [1] ukukhutshwa kwesantya sokuhamba kwe I-174.848 kg / h.

Oku bekuya kusikhokelela ekubeni ukuqikelela kakhulu ukukhutshwa umthamo wevalve yokhuseleko ngokujikeleza 19%

Isilumkiso:

Imposiso enokwenziwa ngokunika ixabiso Cp/Cv ku k ingaba phezulu kakhulu kulo mzekelo.

NGAPHEZU kwe-20%

Ukunika ingcamango, le theyibhile ilandelayo ibonisa izinga lokuhamba kwe-orifice ye-18-mm kwezinye ii-hydrocarbons ezigcweleyo, ezibalwe kwiimeko ezimbini. Ubalo lwenziwe nge-develo ekhethekileyoped Software.

FluidI-P1 (bar)T1 (°C)q' (kg/h)q (kg/h)(q'/q) x 100
IMethane125014721466100.4
IMethane2320023142267102.1
Ipropane1210022612181103.7
IHexane1217830992740113.1
IHexane2322065195111127.5
IHeptane1221532322821114.4

Isoftware ayisebenzisi iifomula [4] [5] kodwa, ukuqala kuhlengahlengiso Redlich kunye Kwong equation karhulumente, ibala ixabiso le-isoentropic exponent usebenzisa ulungelelwaniso lwe-thermodynamic.

IsiHlomelo A kunye no-B
ukuvela kweefomula

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