b6aa44bb-9003-4bc4-8747-168c8196b20b 48 usamakhan 4 5 decimal

&[DATE] &[TIME] - &[FILENAME]

Hot Purging of Flush Seal Water & Temperature Control via Make Up

Tank.h 188 cm * :

Tank.Dia 1.8 m * :

Tank.Vol π Tank.Dia 2^4 / * Tank.h * : 4.784 m 3^*

ρ 1000 kg m 3^/ * :

~3barg or 4 barA P 4 bar * :

T.A 25 °C * :

Pumps 20 :

Make up demi water has lower temperature T.B T.A 26 range Δ°C * - : °C 232221201951 mat

Flush.rate 7 L min / * :

Flow.A Pumps Flush.rate * : m 3^hr / 8.4

Flow.B x m 3^hr / * :

Recommended temperaturerise T.C T.A 57 range Δ°C * + : °C 30313231 mat

Level is held constant in tank so volume of tank is irrelevant Flow.D Flow.B :

Flow.C Flow.A Flow.D - :

T.D T.C :

Liquid enthalpy [H] at different temperatures. In liquid phase pressure changes to enthalpy are negligible & density remains constant as well Enthalpy.A H T T.A P P Water CoolProp_Props : kJ kg / 105.1967

Enthalpy.B H T T.B P P Water CoolProp_Props vectorize : kJ kg / 96.8349 92.6533 88.4711 84.2883 80.1049 51 mat

Enthalpy.C H T T.C P P Water CoolProp_Props vectorize : kJ kg / 126.0949 130.2738 134.4526 31 mat

Enthalpy.D Enthalpy.C :

Make up water requirement using Enthalpy Balance around flush water tank. ρ is constant so cancels out Flow.B Flow.A Enthalpy.A * Flow.B Enthalpy.B * Flow.C Enthalpy.C * + ≡ x solve vectorize maple m 3^hr / * : m 3^hr / 48.7625 m 5^* - 58.5133 m 5^* - 68.2638 m 5^* - 31 mat

Flow.B 011 mat : i 1 Enthalpy.C length range j 1 Enthalpy.B length range Flow.B j i el Flow.A Enthalpy.A * Flow.B Enthalpy.B j el * Flow.C Enthalpy.C i el * + ≡ x solve maple : 11 line for 11 line for 21 line

Flow.B 1.3922 11 mat Pile vide. Pile vide. Pile vide. Pile vide. Pile vide. Pile vide. Pile vide. Pile vide. Pile vide. Pile vide. Pile vide. Pile vide. Pile vide. Pile vide. 53 mat

Flow.D Flow.B : m 3^hr / #

tmp 011 mat : tmp 11 el 2 : tmp 12 el 4 : tmp 21 el 20 : tmp 22 el 40 : 51 line

2 6 range 1 * Δ°C * Flow.B 3600 * s * augment 1 1 sys

tmp 24204022 mat

data char size clr plot k 1 data rows range r3 k el char : r4 k el size : r5 k el clr : 13 mat for data r3 r4 r5 augment 21 line :

XY 23 96.83 22 92.65 21 88.47 20 84.29 19 80.1 52 mat :

support XY . 14 red plot :

vx XY 1 col : vy XY 2 col : 12 mat x f vx vy x cinterp : 21 mat

Though not visible, maybe ? a slight underlying curvature

x f support 2 1 sys

°C 21.5 :

sanity Hermite °C f 90.56

The only thing I can recognize is the thermal massflow 'kJ/kg' vs °C demand. The all thing subjected to masflow T/hr.

Project 23 96.83 22.9285 96.5311 22.848 96.1946 22.7595 95.8247 22.664 95.4255 22.5625 95.0012 22.456 94.5561 22.3455 94.0942 22.232 93.6198 22.1165 93.137 22 92.65 21.9 92.232 21.8 91.814 21.7 91.396 21.6 90.978 21.5 90.56 21.4 90.142 21.3 89.724 21.2 89.306 21.1 88.888 21 88.47 20.9 88.0522 20.8 87.6343 20.7 87.2165 20.6 86.7986 20.5 86.3806 20.4 85.9626 20.3 85.5446 20.2 85.1265 20.1 84.7083 20 84.29 19.8835 83.8022 19.768 83.3184 19.6545 82.843 19.544 82.38 19.4375 81.9338 19.336 81.5084 19.2405 81.1082 19.152 80.7372 19.0715 80.3998 19 80.1 412 mat :

Hermite discrete population ... export

Project support 2 1 sys