- Page 1 and 2: ANALYSIS OF WATER INJECTION INTO HI
- Page 3 and 4: Thesis CertificateThe Graduate Coll
- Page 5 and 6: ชื่อ : นายปรม
- Page 7 and 8: TABLE OF CONTENTSPageAbstract (in E
- Page 9 and 10: LIST OF TABLESTablePage3-1 Solution
- Page 11: LIST OF FIGURES (CONTINUED)FigurePa
- Page 15 and 16: CHAPTER 1INTRODUCTION1.1 Background
- Page 17 and 18: 31.6.6 Water injected is assumed to
- Page 19 and 20: 6for these working fluid models can
- Page 22 and 23: CHAPTER 3METHODOLOGY FOR ANALYSIS O
- Page 24 and 25: 11perform the necessary calculation
- Page 26 and 27: 13h b P T w−0.2 0.8 −0.55 0.8=
- Page 28 and 29: 15the procedure required Nitrogen(
- Page 30 and 31: 171N22 NEq.3-461 1O+2N2 NOEq.3-472
- Page 32 and 33: 19∂y1 cy ∂y1 cy ∂y 1 c ∂y 1
- Page 34 and 35: 211/2( cy )∂y ∂∂c ∂y∂T
- Page 36 and 37: 23[ A][ ∂y/ ∂ P] + [ ∂f / ∂
- Page 38 and 39: 25⎛ • • •ln ln ⎞⎛⎞( )
- Page 40 and 41: 27( θ= −π)θ>θ bθ>θ W( θ=π
- Page 42 and 43: CHAPTER 4RESULTS AND DISCUSSIONThis
- Page 44 and 45: 31FIGURE 4-1 Comparison of an actua
- Page 46 and 47: 33FIGURE 4-4 Schematic of the port
- Page 48 and 49: 35Temperature (K)250023002100190017
- Page 50 and 51: 37cylinder temperature. So, a more
- Page 52 and 53: 39Thermal efficiency (%)43424140393
- Page 54 and 55: 41Theoretically, the high useful co
- Page 56 and 57: 43Thermal efficiency (%)46454443424
- Page 58 and 59: 45injection-fuel ratio increases gr
- Page 60 and 61: 47Thermal efficiency (%)44434241403
- Page 62 and 63:
49When considering relative tempera
- Page 64 and 65:
51Temperature (K)240021001800150012
- Page 66 and 67:
53When considering relative tempera
- Page 68 and 69:
55Temperature (K)220019001600130010
- Page 70 and 71:
CHAPTER 5CONCLUSIONS AND SUGGESTION
- Page 72 and 73:
REFERENCES1. Ricardo, H.R. The High
- Page 74:
APPENDIX ADerivative equations of i
- Page 78 and 79:
64TABLE A-3 Curve fit coefficients
- Page 80 and 81:
66TABLE A-5 Curve fit coefficients
- Page 82 and 83:
68The following is the derivative v
- Page 84 and 85:
70From the definition of entropyh =
- Page 86 and 87:
72• ⎛ ⎞ • ⎛Tb∂u •b∂
- Page 88 and 89:
74• ⎛1 ⎞ •∂u ⎛∂ ∂
- Page 90 and 91:
76⎛ • • •ln ln ⎞⎛⎞( )
- Page 92 and 93:
78The following is the derivative v
- Page 94 and 95:
80From the definition of entropy h
- Page 96 and 97:
82• ⎛ Tb u ⎞ • • ⎛bmTb
- Page 98 and 99:
84• ⎛1 ⎞ • •∂u ⎛ ⎞
- Page 100 and 101:
86• • • ⎛ u ⎞bmb( hW ub)
- Page 102 and 103:
88Appendix D MATLAB program scripts
- Page 104 and 105:
90[thetawater,pTbWQlHl2]=ode45('Rat
- Page 106 and 107:
92-0.69353550E-14 -0.14245228E+05 0
- Page 108 and 109:
940.21*(1-phi) 0 0]';dcdT=0;else %
- Page 110 and 111:
96dfdp=zeros(4,1);dYdT=zeros(11,1);
- Page 112 and 113:
98dcdT(1)=-dKdT(1)*sqrt(patm)/K(1)^
- Page 114 and 115:
100Iter=Iter+1;[hb,u,v,s,Y,cp,dlvlT
- Page 116 and 117:
102yprime(2)=-Const1/cpb/x*Qconvb+v
- Page 118 and 119:
104masswaterin=massfuel*mwpmf;% Tot
- Page 120 and 121:
106savefile = 'Volume.mat';RTWV=RTW
- Page 122 and 123:
108p=pTarray(:,1);T=pTarray(:,2);hc
- Page 124 and 125:
110gamma_der_tautau = 0;for i = 1 :