yuk kerjain packed column

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Soal Kelompok 8 Keterangan Laju Gas dan Kandungan Solut dalam Umpan Udara, 13 %-berat Cl Kandungan Solut dalam Ca#ran $en erap & ppm '!' Konstanta (enr 1,2) * 1+ mm(g ! .emperatur dan .ekanan /peras# 0en#s $a k#ng etal as "#g #ng Ketentuan 4C5 & kg! m2 gaug operas# berjalan #sotermal dan tekanan konstan persen re o er 7% a#ran pen erap mendekat# a#r bole" menggant# jen#s dan ukuran pa k#ng pola al#ran ounter- urrent laju a#ran pada keadaan opt#mal

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SoalSoal Kelompok 8KeteranganLaju Gas dan Kandungan Solut dalam UmpanUdara, 13 %-berat Cl2, 6000 kg/hKandungan Solut dalam Cairan Penyerap7 ppm w/wKonstanta Henry1,25 x 10^4 mmHg /fraksi-molTemperatur dan Tekanan Operasi40C; 7 kg/cm2 gaugeJenis PackingMetal Raschig RingKetentuanoperasi berjalan isotermal dan tekanan konstanpersen recovery 90%cairan penyerap mendekati airboleh mengganti jenis dan ukuran packingpola aliran counter-currentlaju cairan pada keadaan optimal

kurva kesetimbanganKetentuanfraksi beratfraksi molMr Cl271gr/molCl213% w/w130.0572229209Mr udara28.84gr/molx27ppm w/w7.00E-030.0000017747Mr air18gr/molH1.25E+04mmHg /fraksi-mol1.25E+04Ptot7kg/cm2 gauge5910mmHg7.7763157895atmGas6000kg/hY10.0606961308X12.78E-02Y20.0060696131X20.0000017747fraksi air di liquid0.9999982253fraksi uddar0.9427770791O20.1979831866N20.7447938925batasData KesetimbanganyiYipixiXiy10.05722292090.0606961308338.18746260642.71E-022.78E-020.05179702650.0546265177306.12042684332.45E-022.51E-020.04630831620.0485569046273.68214847272.19E-022.24E-020.04075569260.0424872916240.86614310181.93E-021.96E-020.03513803290.0364176785207.66577443881.66E-021.69E-020.02945418780.0303480654174.07424981851.39E-021.41E-020.02370298060.0242784523140.08461556941.12E-021.13E-020.01788320680.0182088392105.68975221478.46E-038.53E-030.01199363270.012139226270.88236950065.67E-035.70E-03y20.00603299510.006069613135.65500124552.85E-032.86E-0300Figure 11.40m2.1681y1/y29.48499371180.250.60.651.052.358mGm/Lm0.50.60.70.80.911.11.21.3Nog3.53.754.3556.058.416.4Nog rumus3.31359576813.70059850384.21892887234.96069788926.1437415921ERROR:#DIV/0!18.8716550339ERROR:#NUM!ERROR:#NUM!y1-y20.0511899258mGm/Lm0.60.01416630020.80.0188884003mGm/Lm0.8Nog5Column DiameterGas flow rate1.6666666667kg/s0.0577901063kmol/sLiq flow rate2.8191314147kg/s0.1566184119kmol/s563.8262829404Jenis PackingMetal Raschig RingD packing3.80E-02mFp270m-1gas density at 40C9.509kg/m3313Kliq density 996.1801266131kg/m3liq viscosity0.00066Ns/m2

Flv0.1652589764

Figure 11.44K40.7K4 flooding2.3percentage flooding55.1677284367%satisfactoryFrom eq 11.118Vw*2.7762388365kg/m2sColumn Area Required0.6003325956m2Diameter0.8741050664m0.85Column Area0.5676785714m2Packing size to column diameter22.3684210526Percentage flooding at selected diameter58.3410881995%Cornell Methodsutherland constant Cv Cl2 =37.7v Udara =20.1Dv0.0000017938m2/s =2.60Vm Cl2 =0.0484Dl2.36E-09m2/sv1.91E-05PasScv1.1197302639Scl2.80E+02Lw*4.9660698088Figure 11.41K30.87Figure 11.42h81.5Figure 11.43h0.0595w =998.23kg/m3w =1.01E-03kg/msw72.96dyne/cm0.07296N/ml69.49dyne/cm0.06949N/m

f10.9340240188f21.0025728284f31.0397525901estimasi Z25.0227871712mCorrection2.3Hl0.3619489384Hg2.7803101375Hog5.0045582475Z25.0227912377mselisih Z0.0000040665

coba duluNumber of stages