Isothermal Methanol Converter (IMC) UA Distribution Analysis

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Isothermal Methanol

Converter (IMC) UA Distribution Analysis

Case Study: #0630416GB/H ACME Co. 9,000 MTD MeOH

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Methanol Synthesis The synthesis loop comprises a circulator, converter, feed/effluent exchanger, separator, and in some cases a heat recovery exchanger. The optimum operating pressure is typically about 80 bar for large plants, but for smaller plants (less than 600 te/day) a pressure of 50 bar may be economic due to the reduced material requirements. Synthesis gas is mixed with the recycle gas and preheated in a feed/effluent interchanger. The exact arrangement of interchanger is dependent on the type of converter used. The converter effluent is cooled by passing through the feed/effluent interchanger and dependent on the reactor type, a heat recovery exchanger. Prior to the catchpot, the gas is cooled to about 40oC to condense the product methanol. A purge is taken from the recycle gas to remove inerts (N2, CH4, Argon, and surplus hydrogen or carbon oxides) from the loop. This is used as fuel in the reformer. A purge gas expander may be used to recover power from the purge gas as it is let down to the fuel system pressure. There are a number of different types of converters offered by technology licensors; Two key types:

• Multiple beds with intercooling • Single bed with continuous cooling

However, this case study examines the Radial Flow – Isothermal Methanol Converter (IMC) for ACME Co. 9,000 MTD, based on the Casale Isothermal Methanol Converter (IMC) design, detailed below;



The Casale Isothermal Methanol Converter (IMC) Design

This converter uses plates instead of tubes to remove the heat from the reaction gas. The use of the plates and the orientation allow the heat transfer within the converter to be more accurately controlled to follow the maximum rate line. It can be used in either feed heating or steam raising. This converter is a new design which uses less volume than previous designs. Casale Isothermal Methanol Converter (IMC)

APPENDIX 1

ACME Stream Data for Radial Flow Design

Name GCC In Adiabatic Inlet

Adiabatic outlet

GCC Out WCC Out Sat Water to WCC

Sat Water from WCC

Temperature [C] 130 245 275.01242 272.05343 249.72058 204.1463 250.22416Pressure [bar] 85.2 85.2 84.8 83.2 81.2 57 57Molar Flow [kgmole/h 157896.51 157896.51 153219.89 141527.72 134007.4 115017.66 115017.66Mass Flow [kg/h] 1475273.8 1475273.8 1475272.1 1475266.4 1475262.7 2071849.8 2071849.8

Mol % Hydrogen 74.6249% 74.6249% 72.5351% 69.8044% 67.8800% 0.0015% 0.0015%Mol % CO 8.6823% 8.6823% 8.7367% 5.7906% 3.5412% 0.0012% 0.0012%Mol % CO2 7.9769% 7.9769% 6.9048% 7.0112% 7.1714% 0.0190% 0.0190%Mol % Nitrogen 1.1029% 1.1029% 1.1365% 1.2304% 1.2995% 0.0000% 0.0000%Mol % Argon 1.0370% 1.0370% 1.0687% 1.1569% 1.2219% 0.0001% 0.0001%Mol % Methane 5.6334% 5.6334% 5.8053% 6.2849% 6.6376% 0.3372% 0.3372%Mol % H2O 0.2334% 0.2334% 1.5573% 2.1544% 2.5128% 99.6408% 99.6408%Mol % Methanol 0.7092% 0.7092% 2.2544% 6.5603% 9.7220% 0.0002% 0.0002%Mol % Ethanol 0.0000% 0.0000% 0.0003% 0.0015% 0.0030% 0.0000% 0.0000%Mol % 1-Propanol 0.0000% 0.0000% 0.0001% 0.0006% 0.0012% 0.0000% 0.0000%Mol % 1-Butanol 0.0000% 0.0000% 0.0001% 0.0004% 0.0007% 0.0000% 0.0000%Mol % diM-Ether 0.0000% 0.0000% 0.0004% 0.0017% 0.0026% 0.0000% 0.0000%Mol % M-Formate 0.0000% 0.0000% 0.0003% 0.0025% 0.0061% 0.0000% 0.0000%Mol % M-E-Ketone 0.0000% 0.0000% 0.0000% 0.0000% 0.0000% 0.0000% 0.0000%Mol % Acetone 0.0000% 0.0000% 0.0000% 0.0000% 0.0001% 0.0000% 0.0000%

Spreadsheet to calculate optimum UA distribution through a cooled methanol synthesis reactor or calculateperformance given a matrix of UA values.Version 1.13.202 July 2014 – G B HAWKINS

Routines imported from VULCAN Dbase_01 for thermodynamics.Data imported from VULCAN Dbase_01 (see "Data" page in spreadsheet).Routines imported from VULCAN Dbase_02 for kinetics and numerical integration, etc.Fugacity calculations can be incorporated into equilibrium and rate of reaction routines to be consistent with original Cresswell work, but activity data was not evaluated on this basis. To be consistent with what we do in MeOH Bed in VULCANFlow Equilibrium calculations include component fugacities so this has also been implemented in the rate calculations.In design mode, UA values selected such that the temperature at the outlet of each segment is equal to the temperature at which the maximum rate of reaction is achieved for that gas composition.Enthalpies are calculated using ExAPI with no RKS correction for non-ideality. The RKS correction can easily be incorporated (maybe a selection option for a future version), but it makes no obvious difference to the results and slows the calculations down by an order of magnitude.The maximum rate temperature calculation routine is new and is based on a golden section search method.

Catalyst CoolantCO 13386.317 4904.257CO2 10579.521 4505.781 TOTAL CATALYST INLET FLOW = 153218.066 kgmol/hH2 111138.24 42152.167H2O 2386.098 131.839 TOTAL COOLANT FLOW = 56485.3704 kgmol/hCH3OH 3454.185 400.572CH4 8894.922 3182.04N2 & Ar 3378.7827 1208.7144Temperature in 275.0 130Temperature out 275.0 237.2Pressure 84.8 85.2Cooling type Cocurrent Allowable cooling optionsMeOH Act 0.267 CountercurrentWGS Act 0.6141 CocurrentCatalyst Density 1300 BoilingCat Vol 33.04Max Temp 275Lowest Temp 240Calculation options Optimum design Allowable calculation optionsUA Vol Optimum design

0 16.7 Performance0 33.30 50.0

18993970 66.764964795 83.342685509 100.038690425 116.728061213 133.321912675 150.017669275 166.714828944 183.312644692 200.010974170 216.79611459 233.38562234 250.07664689 266.76911728 283.36280182 300.05707710 316.75274975 333.34846534 350.04488382 366.74189670 383.33900681 400.0

CO(% v/v)

CO2(% v/v)

H2(% v/v)

H2O(% v/v)

CH3OH(% v/v)

CH4(% v/v)

N2(% v/v)

Total flow(kgmol/hr)

Heatrelease(MW)

MeOHrate

(kgmol/hr)

Catalysttemp.(°C)

Tubetemp.(°C)

Volume(m3)

Press.(bara)

ML-CO2(°C)

ML-CO(°C)

WGS(°C)

UA(J/hr/m3/k)

Tmaxrate(°C)

8.74 6.90 72.54 1.56 2.25 5.81 2.21 153218.1 0.0 73.9 275.0 130.0 0.0 84.8 367.8 339.5 299.4 0 334.18.71 6.88 72.47 1.59 2.32 5.81 2.21 153016.4 2.3 72.7 275.0 134.7 1.4 84.8 364.7 338.4 301.0 42224289 331.48.69 6.86 72.40 1.62 2.39 5.82 2.21 152817.7 4.5 71.7 275.0 139.3 2.8 84.8 361.8 337.4 302.4 42532357 329.08.66 6.84 72.34 1.65 2.46 5.83 2.21 152621.8 6.8 70.7 275.0 143.9 4.1 84.8 359.1 336.4 303.7 44203345 326.78.64 6.83 72.28 1.68 2.53 5.84 2.22 152428.5 9.1 69.8 275.0 148.6 5.5 84.8 356.6 335.5 304.8 45915122 324.58.61 6.81 72.22 1.70 2.59 5.84 2.22 152237.7 11.3 68.9 275.0 153.2 6.9 84.8 354.3 334.6 305.7 47698170 322.58.57 6.80 72.17 1.72 2.66 5.85 2.22 152049.3 13.6 68.0 275.0 157.8 8.3 84.8 352.2 333.6 306.5 49564753 320.78.54 6.79 72.12 1.74 2.72 5.86 2.22 151863.2 15.8 67.2 275.0 162.4 9.6 84.8 350.2 332.8 307.2 51528595 319.08.51 6.79 72.07 1.76 2.78 5.86 2.23 151679.4 18.1 66.4 275.0 167.0 11.0 84.8 348.3 331.9 307.7 53605179 317.38.47 6.78 72.02 1.78 2.85 5.87 2.23 151497.6 20.4 65.6 275.0 171.6 12.4 84.8 346.5 331.1 308.2 55811924 315.88.44 6.77 71.97 1.79 2.91 5.88 2.23 151318.0 22.6 64.9 275.0 176.2 13.8 84.8 344.9 330.3 308.6 58168748 314.38.40 6.77 71.93 1.81 2.97 5.89 2.24 151140.4 24.8 64.2 275.0 180.7 15.1 84.8 343.3 329.5 309.0 60698638 313.08.36 6.77 71.88 1.82 3.03 5.89 2.24 150964.7 27.1 63.5 275.0 185.3 16.5 84.8 341.8 328.7 309.3 63428125 311.68.33 6.76 71.84 1.84 3.10 5.90 2.24 150790.8 29.3 62.8 275.0 189.8 17.9 84.8 340.3 327.9 309.5 66388670 310.48.29 6.76 71.80 1.85 3.16 5.91 2.24 150618.8 31.5 62.1 275.0 194.2 19.3 84.8 338.9 327.2 309.6 69620298 309.28.25 6.76 71.76 1.86 3.22 5.91 2.25 150448.6 33.7 61.5 275.0 198.7 20.7 84.8 337.6 326.5 309.7 73149243 308.18.21 6.76 71.72 1.87 3.28 5.92 2.25 150280.2 35.9 60.9 275.0 203.1 22.0 84.8 336.4 325.8 309.8 77066575 307.18.17 6.76 71.68 1.88 3.34 5.93 2.25 150113.4 38.1 60.3 275.0 207.4 23.4 84.8 335.2 325.1 309.9 81407458 306.08.13 6.76 71.64 1.89 3.39 5.93 2.25 149948.3 40.2 59.7 275.0 211.8 24.8 84.8 334.0 324.4 309.9 86262663 305.08.09 6.76 71.60 1.89 3.45 5.94 2.26 149784.8 42.3 59.1 275.0 216.1 26.2 84.8 332.9 323.7 309.9 91753876 304.08.05 6.76 71.57 1.90 3.51 5.94 2.26 149622.9 44.5 58.5 275.0 220.4 27.5 84.8 331.8 323.1 309.8 97939414 303.18.01 6.76 71.53 1.91 3.57 5.95 2.26 149462.6 46.6 58.0 275.0 224.6 28.9 84.8 330.8 322.4 309.8 105649126 302.27.97 6.77 71.50 1.92 3.62 5.96 2.26 149303.8 48.7 57.4 275.0 228.8 30.3 84.8 329.8 321.8 309.7 114227434 301.47.94 6.77 71.46 1.92 3.68 5.96 2.27 149146.6 50.8 56.8 275.0 233.0 31.7 84.8 328.9 321.2 309.6 124151256 300.57.90 6.77 71.43 1.93 3.74 5.97 2.27 148991.0 52.9 56.3 275.0 237.2 33.0 84.8 327.9 320.6 309.4 135971899 299.7

Spreadsheet to calculate optimum UA distribution through a cooled methanol synthesis reactor orcalculate performance given a matrix of UA values.Version 1.13.202 July 2014 – G B HAWKINS

Routines imported from VULCAN Dbase_01 for thermodynamics.Data imported from VULCAN Dbase_01 (see "Data" page in spreadsheet).Routines imported from VULCAN Dbase_02 for kinetics and numerical integration, etc.Fugacity calculations can be incorporated into equilibrium and rate of reaction routines to be consistent with original Cresswell work, but activity data was not evaluated on this basis. To be consistent with what we do in MeOH Bed in VULCANFlow, the equilibrium calculations include component fugacities so this has also been implemented in the rate calculations.In design mode, UA values selected such that the temperature at the outlet of each segment is equal to the temperature at which the maximum rate of reaction is achieved for that gas composition.Enthalpies are calculated using ExAPI with no RKS correction for non-ideality. The RKS correction can easily be incorporated (maybe a selection option for a future version), but it makes no obvious difference to the results and slows the calculations down by an order of magnitude.The maximum rate temperature calculation routine is new and is based on a golden section search method.

Catalyst CoolantCO 8195.31CO2 9922.81 22 TOTAL CATALYST INLET FLOW = 141518.07 kgmol/hH2 98792.54H2O 3049.12 114604 TOTAL COOLANT FLOW = 115014 kgmol/hCH3OH 9284.58CH4 8894.92 388N2 & Ar 3378.79Temperature in 272.1 236Temperature out 266.0 225.2Pressure 83.2 57Cooling type Countercurrent Allowable cooling optionsMeOH Act 0.267 CountercurrentWGS Act 0.6141 CocurrentCatalyst Density 1300 BoilingCat Vol 33.04Max Temp 275Lowest Temp 240Calculation options Optimum design Allowable calculation optionsUA Vol Optimum design

0 16.7 Performance0 33.30 50.0

18993970 66.764964795 83.342685509 100.038690425 116.728061213 133.321912675 150.017669275 166.714828944 183.312644692 200.010974170 216.79611459 233.38562234 250.07664689 266.76911728 283.36280182 300.05707710 316.75274975 333.34846534 350.04488382 366.74189670 383.33900681 400.0

CO(% v/v)

CO2(% v/v)

H2(% v/v)

H2O(% v/v)

CH3OH(% v/v)

CH4(% v/v)

N2(% v/v)

Total flow(kgmol/hr)

Heatrelease(MW)

MeOHrate

(kgmol/hr)

Catalysttemp.(°C)

Tubetemp.(°C)

Volume(m3)

Press.(bara)

ML-CO2(°C)

ML-CO(°C)

WGS(°C)

UA(J/hr/m3/k)

Tmaxrate(°C)

5.79 7.01 69.81 2.15 6.56 6.29 2.39 141518.1 0.0 28.4 272.1 236.0 0.0 83.2 294.5 294.2 293.7 0 271.05.77 7.01 69.79 2.16 6.59 6.29 2.39 141440.1 2.9 28.2 270.7 235.0 1.4 83.2 294.3 294.0 293.5 208049343 270.75.75 7.02 69.77 2.16 6.62 6.29 2.39 141362.8 4.2 27.9 270.5 234.6 2.8 83.2 294.1 293.8 293.3 95158783 270.55.72 7.02 69.75 2.16 6.65 6.30 2.39 141286.3 5.5 27.7 270.3 234.1 4.1 83.2 293.8 293.5 293.1 97400060 270.35.70 7.02 69.74 2.17 6.68 6.30 2.39 141210.4 6.8 27.4 270.1 233.6 5.5 83.2 293.5 293.3 292.9 96238048 270.15.68 7.02 69.72 2.17 6.71 6.30 2.39 141135.1 8.2 27.2 269.8 233.2 6.9 83.2 293.3 293.1 292.7 95003390 269.85.66 7.02 69.70 2.17 6.74 6.31 2.40 141060.5 9.4 27.0 269.6 232.7 8.3 83.2 293.0 292.8 292.5 90612931 269.65.64 7.03 69.68 2.18 6.77 6.31 2.40 140986.6 10.7 26.7 269.4 232.3 9.6 83.2 292.8 292.6 292.3 92139771 269.45.62 7.03 69.67 2.18 6.80 6.31 2.40 140913.2 12.1 26.5 269.2 231.8 11.0 83.2 292.6 292.4 292.2 91469780 269.25.59 7.03 69.65 2.18 6.83 6.32 2.40 140840.5 13.3 26.3 269.0 231.4 12.4 83.2 292.3 292.2 292.0 84996951 269.05.57 7.03 69.63 2.18 6.86 6.32 2.40 140768.4 14.5 26.1 268.8 231.0 13.8 83.2 292.1 292.0 291.8 85861492 268.85.55 7.03 69.61 2.19 6.89 6.32 2.40 140696.8 15.8 25.9 268.5 230.5 15.1 83.2 291.9 291.7 291.6 88140059 268.55.53 7.04 69.60 2.19 6.92 6.33 2.40 140625.9 17.0 25.7 268.4 230.1 16.5 83.2 291.6 291.5 291.4 81985398 268.45.51 7.04 69.58 2.19 6.95 6.33 2.40 140555.5 18.2 25.5 268.1 229.7 17.9 83.2 291.4 291.3 291.2 82765986 268.25.49 7.04 69.56 2.19 6.98 6.33 2.41 140485.6 19.4 25.3 267.9 229.2 19.3 83.2 291.2 291.1 291.0 85059440 267.95.47 7.04 69.55 2.20 7.00 6.33 2.41 140416.3 20.6 25.1 267.7 228.8 20.7 83.2 290.9 290.9 290.8 79063585 267.75.45 7.04 69.53 2.20 7.03 6.34 2.41 140347.5 21.8 24.9 267.5 228.4 22.0 83.2 290.7 290.7 290.6 79886806 267.55.43 7.05 69.51 2.20 7.06 6.34 2.41 140279.3 23.0 24.7 267.3 228.0 23.4 83.2 290.5 290.5 290.4 77183253 267.35.41 7.05 69.50 2.20 7.09 6.34 2.41 140211.6 24.1 24.5 267.1 227.6 24.8 83.2 290.3 290.3 290.3 78042066 267.15.39 7.05 69.48 2.21 7.12 6.35 2.41 140144.4 25.3 24.3 267.0 227.2 26.2 83.2 290.1 290.1 290.1 75400372 267.05.37 7.05 69.47 2.21 7.14 6.35 2.41 140077.7 26.4 24.1 266.8 226.8 27.5 83.2 289.9 289.9 289.9 76281060 266.85.35 7.05 69.45 2.21 7.17 6.35 2.41 140011.5 27.6 24.0 266.6 226.4 28.9 83.2 289.6 289.7 289.7 73697800 266.65.33 7.05 69.43 2.21 7.20 6.36 2.41 139945.8 28.7 23.8 266.4 226.0 30.3 83.2 289.4 289.5 289.5 74598566 266.45.31 7.06 69.42 2.22 7.22 6.36 2.42 139880.6 29.8 23.6 266.2 225.6 31.7 83.2 289.2 289.3 289.3 72070477 266.25.29 7.06 69.40 2.22 7.25 6.36 2.42 139815.8 30.9 23.4 266.0 225.2 33.0 83.2 289.0 289.1 289.2 68170156 266.0

"ACME" Methanol Company Case Study: UA Distribution Through a

Methanol Synthesis Converter of a 9000 MTD MeOH Plant

Radial Flow ACME Reactor Set-Up Gas Cooled vs. Water-Cooled Performance

Analysis

PHYSICAL PROPERTIES

Taken from HYSYS Inside Plate Flow Properties - Cool Gas

1. GAS COOLED REACTOR TO TOP OF PLATES P1 Out P2 In P2 Out P3 In P3 Out P4 In P4 Out AveragesFlow (kg/s) 146.611111 146.611111 229.138889 229.138889 311.666667 311.666667 394.444444 394.444444 270.4653

Cooled Bed Vol. Cat. Temp rho(g) mu(g) kg Cpg Density (kg/m3) 22.78 18.48 19.82 17.93 18.99 17.75 18.61 17.73 19.01125m3 C kg/m3 Pa.s W/m.K J/kg.K Viscosity (Pa-s) 0.0000145 0.00001728 0.00001626 0.00001774 0.00001687 0.00001789 0.00001717 0.00001791 1.7E-05

0 275.0124 17.30929 1.86E-05 0.168081 3384.199 Conductivity (W/m-K) 0.1387 0.1626 0.1542 0.1663 0.1593 0.1675 0.1617 0.1676 0.1597383.303994 273.0776 17.42149 1.85E-05 0.167258 3378.427 Heat Capacity (J/kg-K) 3335 3397 3373 3409 3387 3413 3395 3414 3390.3756.607988 271.7302 17.51237 1.85E-05 0.166625 3373.5789.911982 270.8886 17.58528 1.84E-05 0.166143 3369.44513.21598 270.4893 17.64281 1.84E-05 0.165783 3365.88116.51997 270.4818 17.68705 1.84E-05 0.165526 3362.7819.82396 270.8234 17.71978 1.84E-05 0.165353 3360.0623.12796 271.4782 17.7425 1.84E-05 0.165254 3357.65826.43195 272.4143 17.75653 1.85E-05 0.165216 3355.52229.73595 273.6027 17.76304 1.85E-05 0.165231 3353.61233.03994 275.016 17.7631 1.85E-05 0.165291 3351.89536.34393 274.2427 17.74991 1.85E-05 0.164863 3348.06839.64793 273.7978 17.80656 1.85E-05 0.164538 3344.84742.95192 273.6423 17.85306 1.85E-05 0.164285 3341.9946.25591 273.742 17.89072 1.85E-05 0.164094 3339.4449.55991 274.0661 17.92071 1.85E-05 0.163956 3337.15352.8639 274.5862 17.94406 1.85E-05 0.163863 3335.09156.1679 275.2756 17.96171 1.85E-05 0.163807 3333.225

59.47189 276.1087 17.97452 1.86E-05 0.163782 3331.52862.77588 277.0605 17.98326 1.86E-05 0.163784 3329.98166.07988 278.1064 17.98866 1.86E-05 0.163806 3328.56569.38387 277.094 17.97566 1.86E-05 0.163373 3325.02472.68787 276.3609 18.03555 1.86E-05 0.163027 3322.04375.99186 275.8691 18.08676 1.85E-05 0.162742 3319.38279.29585 275.5857 18.13042 1.85E-05 0.162509 3316.99582.59985 275.4816 18.16755 1.85E-05 0.162319 3314.84385.90384 275.5309 18.19903 1.85E-05 0.162166 3312.89589.20784 275.71 18.22564 1.85E-05 0.162043 3311.12492.51183 275.9976 18.24808 1.85E-05 0.161947 3309.50995.81582 276.3741 18.26698 1.86E-05 0.161873 3308.0399.11982 276.8214 18.28289 1.86E-05 0.161817 3306.672102.4238 275.4367 18.27297 1.85E-05 0.161353 3303.282105.7278 274.3422 18.33776 1.85E-05 0.160973 3300.442109.0318 273.4951 18.39393 1.85E-05 0.160653 3297.906112.3358 272.8598 18.44262 1.85E-05 0.160382 3295.63115.6398 272.4059 18.48481 1.85E-05 0.160154 3293.58118.9438 272.1075 18.52136 1.84E-05 0.159962 3291.724122.2478 271.9419 18.55302 1.84E-05 0.159801 3290.038125.5518 271.889 18.58045 1.84E-05 0.159666 3288.501128.8558 271.9314 18.60422 1.84E-05 0.159553 3287.093132.1598 272.0534 18.62486 1.84E-05 0.15946 3285.8

AVERAGE 274.0227 18.03441 1.85E-05 0.163227 3328.377

2. WATER COOLED REACTOR Inside Plate Flow Properties - Cool WaterCooled Bed Vol. Cat. Temp rho(g) mu(g) kg Cpg

m3 C kg/m3 Pa.s W/m.K J/kg.K WCC-QW4-In WCC-QW4ouWCC-QW3-InWCC-QW3-OuWCC-QW2-In Water2Out WCC-QW S-120 Averages0 272.0534 18.51633 1.84E-05 0.159439 3285.546 Flow (kg/s) 101.8889 101.888889 291.388889 291.388889 433.333333 433.333333 575.555556 575.5556 350.5417

5.847353 272.5263 18.54301 1.85E-05 0.159328 3283.578 Density (kg/m3) 742.3 646.2 716.4 650.2 688.6 623.9 665.3 597.4 666.287511.69471 272.6949 18.57817 1.85E-05 0.15916 3281.4 Viscosity (Pa-s) 0.000131 0.000111 0.000123 0.000111 0.000117 0.000109 0.000113 0.000107 0.00011517.54206 272.5927 18.62081 1.85E-05 0.158943 3279.04 Conductivity (W/m-K) 0.662 0.627 0.651 0.628 0.64 0.621 0.632 0.616 0.63462523.38941 272.2515 18.67009 1.85E-05 0.158683 3276.52 Heat Capacity (J/kg-K) 4510 4765 4587 4756 4664 4809 4722 4854 4708.37529.23676 271.7038 18.72517 1.84E-05 0.158386 3273.85835.08412 270.9763 18.78539 1.84E-05 0.158057 3271.07240.93147 270.0942 18.85013 1.84E-05 0.157701 3268.17546.77882 269.0768 18.91896 1.84E-05 0.15732 3265.17952.62618 267.9408 18.99145 1.83E-05 0.156917 3262.09658.47353 266.6989 19.0673 1.83E-05 0.156496 3258.93458.47353 266.6989 18.95566 1.83E-05 0.156474 3258.65564.32088 266.6251 18.99033 1.83E-05 0.1563 3256.7870.16823 266.3487 19.03112 1.83E-05 0.156088 3254.74376.01559 265.8898 19.07748 1.83E-05 0.155841 3252.55981.86294 265.2646 19.12901 1.83E-05 0.155563 3250.23687.71029 264.4894 19.18532 1.83E-05 0.155257 3247.78793.55764 263.5762 19.24613 1.82E-05 0.154925 3245.218

99.405 262.5365 19.31115 1.82E-05 0.154568 3242.538105.2524 261.3782 19.38023 1.82E-05 0.154189 3239.752111.0997 260.1085 19.45318 1.82E-05 0.153789 3236.869116.9471 258.7323 19.5299 1.81E-05 0.153368 3233.892116.9471 258.7323 19.41474 1.81E-05 0.153346 3233.593122.7944 258.688 19.44284 1.81E-05 0.153208 3232.106128.6418 258.4559 19.47718 1.81E-05 0.153032 3230.443134.4891 258.0439 19.51756 1.81E-05 0.152821 3228.612140.3365 257.4574 19.56386 1.81E-05 0.152576 3226.614146.1838 256.7028 19.61597 1.81E-05 0.152297 3224.455152.0312 255.7841 19.67384 1.81E-05 0.151986 3222.137157.8785 254.7052 19.73742 1.80E-05 0.151643 3219.663163.7259 253.4675 19.80676 1.80E-05 0.151269 3217.034169.5732 252.0722 19.88189 1.80E-05 0.150864 3214.254175.4206 250.5184 19.96293 1.79E-05 0.150428 3211.324175.4206 250.5184 19.84438 1.79E-05 0.150405 3211.004181.2679 251.3334 19.83552 1.79E-05 0.150478 3210.784187.1153 251.9884 19.83244 1.80E-05 0.150516 3210.398192.9626 252.4703 19.83553 1.80E-05 0.150518 3209.835

198.81 252.7663 19.84523 1.80E-05 0.150482 3209.081204.6573 252.8607 19.86211 1.80E-05 0.150403 3208.118210.5047 252.7393 19.88671 1.80E-05 0.150281 3206.93216.3521 252.3854 19.91974 1.80E-05 0.150111 3205.495222.1994 251.7805 19.962 1.80E-05 0.149889 3203.789228.0468 250.9012 20.0145 1.79E-05 0.14961 3201.784233.8941 249.7206 20.07843 1.79E-05 0.149268 3199.448

AVERAGE 260.5534 19.37654 1.82E-05 0.153914 3237.757

Prediction of Heat Transfer Coefficients Using Bed Heat Transfer Methods by Yagi & Kunii (1957)

RADIAL FLOW ACME REACTOR SET-UP - Gas-Cooled

- ADIABATIC BED LOCATED FROM OUTSIDE WALL INWARDS

ENTER CATALYST CONTAINING DIAMETER OF REACTOR (Di) = 6 m

ENTER CENTRAL DUCT OUTER DIAMETER (Dduct) = 1.5 m

ENTER OUTER ANNULUS OUTER DIAMETER (Do) = 8 m

OUTER ANNULUS INNER DIAMETER (Di) = 6 m

ENTER MOLAR FLOW OF REACTOR FEED GAS = 153220 kmol/h

ENTER MASS FLOW OF REACTOR FEED GAS = 409.797 kg/s

ENTER REACTOR FEED TEMPERATURE = 245 DEG C AND PRESSURE = 86.2 bar(a)

APPROXIMATE (IDEALITY) VOLUMETRIC FEED FLOW AT 245 DEG C AND 86.2 bar(a) = 76550.4 m3/h

X-SECTIONAL AREA OF ANNULUS = 21.9911 m2

AVERAGE AXIAL (VERTICAL) VELOCITY OF GAS THROUGH ANNULUS = 0.96693 m/s

INTERNALS

ENTER TOTAL CATALYST ACTIVE BULK VOLUME = 180.5 m3

ENTER VOLUME OF ADIABATIC BED = 48.29 m3 (If no adiabatic bed present set as very small value > 0 e.g. 0.001 m3)

Active Volume of Cooled Bed = 132.21 m3

ENTER AVERAGE EMBOSSED PLATE WIDTH = 0.012 m ENTER PLATE MATERIAL THICKNESS = 0.0015 m

ENTER CATALYST PELLET LENGTH = 5.2 mm

ENTER CATALYST PELLET DIAMETER = 5.4 mm

ENTER VOIDAGE OF CATALYST BED = 0.36

ENTER THERMAL CONDUCTIVITY OF CATALYST PELLET = 0.32 W/m.K

ENTER THERMAL CONDUCTIVITY OF PLATE = 17 W/m.K

TO ESTIMATE THE NUMBER OF PLATES INSTALLED ASSUMING ONE SINGLE PLATE LAYER(USE 'SOLVER' ROUTINE IN TOOLS MENU OR PRESS BUTTON BELOW WITH STARTING GUESSES)

Plate Width = 0.012 m

Guess Angle Subtended by Chord of Circle (inner duct) equal to Plate Width = 0.91674 Degrees

Using Sine Rule:

LHS = 1.33329 RHS = 1.33329 Difference = 0 (Should be 0)

ENTER MINIMUM PLATE SPACING AT INNER RADII = 0.055 mGuess Angle Subtended by Arc Forming Plate Spacing = 4.20263 Degrees Chord Gap = 0.055 m

( should equal minimum plate spacing)NUMBER OF PLATES = 70 (Single Layer)

PRESS TO COMPUTE ------------> (N.B. Requires 'Good' Initial Guess Values for Iterated Cells)

CALCULATION OF CATALYST BED HEIGHT FOR SINGLE PLATE LAYER

Guess Diameter of Cooled Bed = 5.24466 m

CATALYST BED HEIGHT = 7.23899 m Assumed Plate Height = 7.23899 mSingle Plate Breadth = 1.87233 m

Cooled Bed Volume = 132.21 m3 Actual Volume = 132.21 m3 DIFFERENCE = -9.5E-07 (Should be 0)

Overall Cooled A/V = 14.3524 m2/m3Cat (Single Plate Layer)

CONSIDER MULTIPLE PLATE LAYERS

NUMBER OF PLATE LAYERS = 3

CALCULATION OF CATALYST BED HEIGHT


CATALYST BED HEIGHT = 7.65648 m Assumed Plate Height = 7.65648 mEquivelant Single Plate Breadth = 1.89431 m

Breadth of Each Plate Bank = 0.63144 m

First Plate Layer (Counting from Central Duct Outwards)Number of Plates = 70

Second Plate Layer



Using Sine Rule:

LHS = 0.72388 RHS = 0.72388 Difference = 6.6E-12 (Should be 0)


( should equal minimum plate spacing)NUMBER OF PLATES IN SECOND PLATE LAYER = 129

Third Plate Layer



Using Sine Rule:



( should equal minimum plate spacing)NUMBER OF PLATES IN THIRD PLATE BANK = 188

TOTAL NUMBER OF PLATES IN REACTOR = 387


Overall Cooled A/V = 28.3033 m2/m3Cat

Area Basis Vol. BasisCatalyst Particle Equivelant/Effective Diameter = 0.0053 m 0.00757 m 0.00769 m Dp (Volume)/Dp (Area) = 1.01653

TO CALCULATE OVERALL BEDSIDE HTC (Bed and Plate Outside Wall HTCs)

Correlation Constants:

Phi1 coeff -1.00234 Phi2 coeff -1.13595-0.49574 -0.728850.04692 0.05113

-0.00194 -0.00131

ks/kg 1.96046

Phi1 0.26837 0.2891698Phi2 0.20113 0.2112543

phi 0.23226 0.2473263

Gamma 1Beta 1Alpha 0.13301 0.1079846Emmis. 0.6Hrv 26.929Hrs 13.7049ke0/kg 1.56282

Equivelant 'Outer' Diameter of Plate = 0.024 m

HTC PROFILES FOR GAS-COOLED PART OF BED (Out - In) INSIDE PLATE - Based on Dittus-Boelter Correlation:

i) 3 Plate Layers Plate Mass Flux = 122.978 kg/m2.sPlate Equivelant 'Inner' Diameter = 0.018 m

Radial Distance From Outside to Inside Of 'Cooled' Bed = 1.89431 For Plate Outer Wall HTC For Plate Inside Wall

Radial Bed Approx. Mass Dp/Gap AB (1) AB (2) Re Pr ke/kg (1) ke/kg (2) ke (1) ke (2) hbed (1) hbed (2) Re Pr Nu h(outerwall) h(overall) bedside Re Pr Nu h(inside plate) h (Plate Solid Wall) OVERALL U OVERALL VOLUMETRIC UADistance Volume Plate Flux 1 2 1 2 1 2 Specific 1 2 1 2 Carman Ergun(m) (m3) Spacing (m(kg/m2.s) (W/m.K) (W/m.K) W/m2.K MJ/hr.m2.K kcal/h.m2.K W/m2.K MJ/hr.m2.K kcal/h.m2.K W/m2.K W/m2.K W/m2.K W/m2.K w/m2.K w/m2.K w/m2.K MJ/hr.m2.K MJ/hr.m2.K A (m2/m3) w/m3.K w/m3.K MJ/hr.m3.K MJ/hr.m3.K bar bar

Outside 0 0 0.07225 3.72756 0.07333 0.13301 0.10798 1067.53 0.37723 55.1284 45.0486 8.99846 7.35315 996.321 3.58676 856.682 814.151 2.93094 700.044 4835.8 0.37723032 129.999 4005.08 797.846 676.61 130577 0.35981 189.169 1678.75 11333.3 516.184 462.562 1.85826 1.66522 0 0 0 0 0 0 0Wall 0.09021 9.7212141 0.06979 3.88074 0.07592 0.13134 0.10759 1111.4 0.37723 56.6292 46.6719 9.24343 7.61812 1059.59 3.81452 911.084 873.279 3.1438 750.885 5034.53 0.37723032 134.256 4136.22 843.506 721.045 130577 0.35981 189.169 1678.75 11333.3 534.918 482.906 1.9257 1.73846 26.7134 14289.5 12900.1 51.4421 46.4403 0.00275 0.00344

0.18041 19.05098 0.06732 4.04705 0.0787 0.12955 0.10716 1159.03 0.37723 58.2051 48.4167 9.50066 7.90292 1128.95 4.06422 970.722 939.092 3.38073 807.474 5250.29 0.37723032 138.839 4277.43 893.204 770.035 130577 0.35981 189.169 1678.75 11333.3 554.483 504.398 1.99614 1.81583 27.8342 15433.6 14039.5 55.561 50.5423 0.00572 0.007180.27062 27.989297 0.06486 4.22826 0.08169 0.12762 0.10669 1210.92 0.37723 59.8599 50.2967 9.77077 8.2098 1205.17 4.33861 1036.26 1012.63 3.64547 870.706 5485.37 0.37723032 143.79 4429.97 947.423 824.225 130577 0.35981 189.169 1678.75 11333.3 574.907 527.098 2.06966 1.89755 29.0532 16702.9 15313.9 60.1304 55.13 0.00894 0.011240.36082 36.536166 0.06239 4.42645 0.08491 0.12554 0.10616 1267.68 0.37723 61.597 52.3279 10.0543 8.54133 1289.13 4.64087 1108.45 1095.14 3.94251 941.652 5742.49 0.37723032 149.158 4595.33 1006.72 884.38 130577 0.35981 189.169 1678.75 11333.3 596.215 551.069 2.14637 1.98385 30.3839 18115.3 16743.6 65.2151 60.277 0.01243 0.015670.45103 44.691586 0.05993 4.64414 0.08841 0.12329 0.10557 1330.03 0.37723 63.4189 54.5285 10.3517 8.90053 1381.85 4.97465 1188.18 1188.13 4.27728 1021.61 6024.9 0.37723032 154.998 4775.25 1071.72 951.411 130577 0.35981 189.169 1678.75 11333.3 618.429 576.373 2.22635 2.07494 31.8422 19692.2 18353 70.8918 66.0708 0.01623 0.020530.54123 52.455558 0.05746 4.88435 0.0922 0.12084 0.10491 1398.82 0.37723 65.3274 56.9199 10.6632 9.29088 1484.49 5.34415 1276.43 1293.44 4.65637 1112.16 6336.52 0.37723032 161.379 4971.84 1143.16 1026.41 130577 0.35981 189.169 1678.75 11333.3 641.566 603.069 2.30964 2.17105 33.4477 21458.9 20171.3 77.2521 72.6165 0.0204 0.025880.63144 59.828081 0.055 5.15076 0.09633 0.1182 0.10417 1475.11 0.37723 67.3381 59.5274 10.9914 9.71649 1598.75 5.7555 1374.68 1413.31 5.08791 1215.23 6682.14 0.37723032 168.383 5187.63 1222.11 1110.71 130577 0.35981 189.169 1678.75 11333.3 665.702 631.216 2.39653 2.27238 35.2236 23448.4 22233.7 84.4144 80.0413 0.02499 0.03180.72164 67.298141 0.07655 5.08169 0.06921 0.13567 0.10858 1455.34 0.37723 76.0448 61.1743 12.4126 9.9853 1297.23 4.67002 1115.41 1043.55 3.7568 897.295 6592.54 0.37723032 166.574 5131.91 1035.48 867.21 130577 0.35981 189.169 1678.75 11333.3 606.188 544.354 2.18228 1.95967 23.8538 14459.9 12984.9 52.0556 46.7457 0.02974 0.037960.81185 74.376752 0.07296 5.3707 0.07262 0.13347 0.10809 1538.1 0.37723 79.0054 64.2783 12.8958 10.492 1414.07 5.09067 1215.89 1150.48 4.14174 989.237 6967.48 0.37723032 174.111 5364.1 1119.07 947.306 130577 0.35981 189.169 1678.75 11333.3 633.907 574.864 2.28206 2.06951 25.1729 15957.3 14471 57.4462 52.0956 0.03469 0.044370.90205 81.063915 0.06937 5.69457 0.07638 0.13105 0.10752 1630.86 0.37723 82.183 67.7119 13.4145 11.0524 1547.11 5.56959 1330.27 1274.69 4.58887 1096.03 7387.63 0.37723032 182.461 5621.35 1213.21 1039.07 130577 0.35981 189.169 1678.75 11333.3 663.051 607.416 2.38699 2.1867 26.6465 17668 16185.5 63.6047 58.2678 0.04018 0.051550.99226 87.359629 0.06577 6.06 0.08055 0.12835 0.10687 1735.51 0.37723 85.5951 71.5286 13.9714 11.6754 1699.32 6.11756 1461.15 1420.06 5.11222 1221.03 7861.71 0.37723032 191.769 5908.13 1319.73 1144.88 130577 0.35981 189.169 1678.75 11333.3 693.651 642.107 2.49715 2.31159 28.3033 19632.6 18173.7 70.6774 65.4255 0.04633 0.059631.08247 93.263895 0.06218 6.47555 0.0852 0.12535 0.10611 1854.52 0.37723 89.2576 75.7944 14.5693 12.3717 1874.38 6.74777 1611.68 1591.66 5.72996 1368.58 8400.81 0.37723032 202.219 6230.07 1440.88 1267.77 130577 0.35981 189.169 1678.75 11333.3 725.721 679.022 2.6126 2.44448 30.1798 21902.1 20492.7 78.8475 73.7738 0.05325 0.068811.17267 98.776712 0.05859 6.95228 0.09042 0.12198 0.10522 1991.05 0.37723 93.1831 80.5905 15.21 13.1546 2076.76 7.47633 1785.69 1796.11 6.46599 1544.38 9019.28 0.37723032 214.044 6594.38 1579.37 1411.62 130577 0.35981 189.169 1678.75 11333.3 759.254 718.225 2.73331 2.58561 32.3227 24541.2 23215 88.3482 83.574 0.06113 0.079321.26288 103.89808 0.055 7.50479 0.09633 0.1182 0.10417 2149.28 0.37723 97.3992 86.0188 15.8982 14.0406 2312.47 8.32488 1988.36 2042.27 7.35217 1756.04 9736.06 0.37723032 227.547 7010.4 1738.88 1581.54 130577 0.35981 189.169 1678.75 11333.3 794.28 759.755 2.85941 2.73512 34.7933 27635.6 26434.4 99.4882 95.1638 0.07016 0.091471.35308 109.11699 0.09469 7.35907 0.05595 0.14 0.11031 2107.55 0.37723 112.867 89.2638 18.423 14.5703 1556.48 5.60334 1338.33 1230.98 4.43154 1058.45 9547.01 0.37723032 224.006 6901.29 1270.04 1044.65 130577 0.35981 189.169 1678.75 11333.3 679.674 609.319 2.44683 2.19355 18.5272 12592.5 11289 45.333 40.6404 0.07967 0.104311.44329 113.94444 0.08808 7.98102 0.06015 0.14 0.1098 2285.67 0.37723 122.274 96.2327 19.9584 15.7078 1812.85 6.52627 1558.77 1426.76 5.13634 1226.79 10353.9 0.37723032 239.027 7364.08 1454.73 1195.2 130577 0.35981 189.169 1678.75 11333.3 729.219 657.635 2.62519 2.36748 20.0296 14606 13172.1 52.5814 47.4197 0.08975 0.117981.53349 118.38045 0.08146 8.7178 0.06504 0.13836 0.10916 2496.67 0.37723 131.875 104.372 21.5255 17.0363 2113.97 7.61028 1817.69 1673.09 6.02314 1438.6 11309.7 0.37723032 256.523 7903.1 1667.84 1380.78 130577 0.35981 189.169 1678.75 11333.3 779.123 710.154 2.80484 2.55655 21.7971 16982.6 15479.3 61.1373 55.7253 0.10157 0.13414 Adiabatic DP

1.6237 122.42501 0.07485 9.60445 0.07079 0.13465 0.10836 2750.6 0.37723 141.28 113.995 23.0608 18.6071 2464.9 8.87365 2119.43 1988.86 7.15989 1710.11 12460 0.37723032 277.191 8539.84 1912.8 1613.17 130577 0.35981 189.169 1678.75 11333.3 828.698 766.979 2.98331 2.76112 23.9067 19811.4 18335.9 71.321 66.0092 0.11562 0.15356 3-Point Average Mass Flux = 3.02644 kg/m2.s1.7139 126.07812 0.06823 10.6919 0.07765 0.13023 0.10733 3062.02 0.37723 151.985 125.534 24.808 20.4906 2908.75 10.4715 2501.07 2402.53 8.64912 2065.81 13870.7 0.37723032 302.025 9304.97 2216.02 1909.5 130577 0.35981 189.169 1678.75 11333.3 880.919 828.078 3.17131 2.98108 26.4684 23316.5 21917.9 83.9393 78.9044 0.13263 0.17734 Carman Ergun

Inner 1.80411 129.33979 0.06162 12.057 0.08599 0.12485 0.10598 3452.97 0.37723 164.184 139.605 26.7993 22.7873 3479.58 12.5265 2991.9 2958.67 10.6512 2544 15641.7 0.37723032 332.5 10243.8 2597.33 2295.64 130577 0.35981 189.169 1678.75 11333.3 935.516 893.234 3.36786 3.21564 29.645 27733.3 26479.9 99.84 95.3276 0.1537 0.20715 0.00715 0.0087 barWall 1.89431 132.21 0.055 13.8217 0.09633 0.1182 0.10417 3958.36 0.37723 178.066 157.107 29.0652 25.6441 4227.67 15.2196 3635.14 3730.05 13.4282 3207.26 17931 0.37723032 370.893 11426.7 3085.93 2812.09 130577 0.35981 189.169 1678.75 11333.3 992.094 961.977 3.57154 3.46312 33.688 33421.7 32407.1 120.318 116.666 0.18054 0.24566

Carman ErgunINSIDE PLATE - Based on Dittus-Boelter Correlation: COOLED DP 0.18054 0.24566 bar TOTAL RADIAL DP = 0.18768 0.25436 bar

i) Single Plate Layer Plate Mass Flux = 229.292 kg/m2.sRadial Distance From Outside to Inside Of 'Cooled' Bed = 1.87233 Plate Equivelant 'Inner' Diameter = 0.018 m

Radial Bed Approx. Mass Dp/Gap AB (1) AB (2) Re Pr ke/kg (1) ke/kg (2) ke (1) ke (2) hbed (1) hbed (2) Re Pr Nu h(outerwall) h(overall) bedside Re Pr Nu h(inside plate) h (Plate Solid Wall) OVERALL U Specific OVERALL VOLUMETRIC UADistance Volume Plate Flux 1 2 1 2 1 2 A (m2/m3) 1 2 1 2 Carman Ergun(m) (m3) Spacing (m(kg/m2.s) (W/m.K) (W/m.K) W/m2.K MJ/hr.m2.K kcal/h.m2.K W/m2.K MJ/hr.m2.K kcal/h.m2.K W/m2.K W/m2.K W/m2.K W/m2.K w/m2.K w/m2.K w/m2.K MJ/hr.m2.K MJ/hr.m2.K w/m3.K w/m3.K MJ/hr.m3.K MJ/hr.m3.K bar bar

Outside 0 0 0.1923 3.62034 0.02755 0.14 0.11288 1036.82 0.37723 56.3197 45.7123 9.19291 7.46149 382.432 1.37676 328.832 310.404 1.11745 266.899 4696.71 0.37723032 126.999 3912.66 348.381 287.589 243460 0.35981 311.386 2763.34 11333.3 301.156 254.627 1.08416 0.91666 0 0 0 0 0 0 0Wall 0.08916 9.91134 0.18577 3.75486 0.02852 0.14 0.11282 1075.35 0.37723 58.3543 47.3284 9.52502 7.72528 410.194 1.4767 352.704 332.689 1.19768 286.061 4871.23 0.37723032 130.76 4028.54 372.287 307.31 243460 0.35981 311.386 2763.34 11333.3 318.856 269.967 1.14788 0.97188 9.11667 2906.9 2461.2 10.4649 8.86032 0.00257 0.0032

0.17832 19.461117 0.17923 3.89977 0.02956 0.14 0.11275 1116.85 0.37723 60.546 49.0664 9.88276 8.00897 441.127 1.58806 379.301 357.488 1.28696 307.384 5059.22 0.37723032 134.782 4152.44 398.765 329.151 243460 0.35981 311.386 2763.34 11333.3 338.082 286.678 1.2171 1.03204 9.46184 3198.88 2712.5 11.516 9.765 0.00532 0.006650.26748 28.649332 0.17269 4.05631 0.03068 0.14 0.11268 1161.68 0.37723 62.9136 50.9405 10.2692 8.31488 475.731 1.71263 409.055 385.195 1.3867 331.208 5262.3 0.37723032 139.093 4285.26 428.195 353.426 243460 0.35981 311.386 2763.34 11333.3 359.002 304.919 1.29241 1.09771 9.83417 3530.48 2998.62 12.7097 10.795 0.00828 0.010370.35663 37.475984 0.16615 4.22594 0.03189 0.14 0.11259 1210.26 0.37723 65.4793 52.9674 10.688 8.64572 514.616 1.85262 442.49 416.283 1.49862 357.939 5482.36 0.37723032 143.727 4428.03 461.036 380.511 243460 0.35981 311.386 2763.34 11333.3 381.804 324.869 1.37449 1.16953 10.237 3908.52 3325.68 14.0707 11.9725 0.01146 0.014380.44579 45.941074 0.15961 4.41038 0.03319 0.14 0.1125 1263.08 0.37723 68.2688 55.1663 11.1433 9.00464 558.519 2.01067 480.24 451.325 1.62477 388.069 5721.64 0.37723032 148.724 4581.97 497.835 410.855 243460 0.35981 311.386 2763.34 11333.3 406.7 346.733 1.46412 1.24824 10.6742 4341.22 3701.11 15.6284 13.324 0.0149 0.018750.53495 54.044601 0.15307 4.61165 0.03461 0.14 0.1124 1320.72 0.37723 71.313 57.5599 11.6402 9.39534 608.344 2.19004 523.081 491.021 1.76768 422.202 5982.75 0.37723032 154.129 4748.51 539.258 445.005 243460 0.35981 311.386 2763.34 11333.3 433.93 370.744 1.56215 1.33468 11.1505 4838.54 4133.98 17.4188 14.8823 0.01862 0.02350.62411 61.786566 0.14654 4.83217 0.03616 0.14 0.11228 1383.87 0.37723 74.6484 60.175 12.1846 9.82219 665.209 2.39475 571.977 536.233 1.93044 461.078 6268.84 0.37723032 159.998 4929.31 586.113 483.623 243460 0.35981 311.386 2763.34 11333.3 463.764 397.165 1.66955 1.42979 11.6713 5412.7 4635.41 19.4857 16.6875 0.02267 0.02870.71327 69.166968 0.14 5.07484 0.03784 0.14 0.11214 1453.37 0.37723 78.3187 63.0434 12.7837 10.2904 730.511 2.62984 628.126 588.032 2.11692 505.617 6583.65 0.37723032 166.394 5126.37 639.397 527.522 243460 0.35981 311.386 2763.34 11333.3 496.502 426.299 1.78741 1.53468 12.243 6078.68 5219.19 21.8833 18.7891 0.0271 0.03440.80243 76.185807 0.13346 5.34317 0.0397 0.14 0.11198 1530.22 0.37723 82.3772 66.2036 13.4462 10.8062 806.009 2.90163 693.043 647.761 2.33194 556.974 6931.76 0.37723032 173.396 5342.09 700.342 577.71 243460 0.35981 311.386 2763.34 11333.3 532.484 458.487 1.91694 1.65055 12.8737 6855.04 5902.42 24.6782 21.2487 0.03196 0.040710.89159 82.843084 0.12692 5.64147 0.04174 0.14 0.1118 1615.65 0.37723 86.8888 69.7018 14.1826 11.3772 893.948 3.21821 768.657 717.121 2.58163 616.613 7318.74 0.37723032 181.098 5579.37 770.496 635.446 243460 0.35981 311.386 2763.34 11333.3 572.088 494.117 2.05952 1.77882 13.5729 7764.89 6706.59 27.9536 24.1437 0.03731 0.04770.98074 89.138798 0.12038 5.97503 0.04401 0.14 0.11159 1711.18 0.37723 91.9339 73.5945 15.0061 12.0126 997.226 3.59001 857.46 798.295 2.87386 686.41 7751.49 0.37723032 189.615 5841.77 851.815 702.32 243460 0.35981 311.386 2763.34 11333.3 615.733 533.627 2.21664 1.92106 14.3524 8837.23 7658.81 31.814 27.5717 0.04326 0.0555

1.0699 95.07295 0.11384 6.35053 0.04654 0.14 0.11134 1818.71 0.37723 97.6132 77.9516 15.9331 12.7238 1119.64 4.0307 962.717 894.118 3.21883 768.803 8238.62 0.37723032 199.089 6133.66 946.809 780.363 243460 0.35981 311.386 2763.34 11333.3 663.88 577.51 2.38997 2.07904 15.2268 10108.8 8793.66 36.3917 31.6572 0.04989 0.064281.15906 100.64554 0.10731 6.77638 0.04937 0.14 0.11105 1940.67 0.37723 104.054 82.86 16.9845 13.525 1266.24 4.55847 1088.77 1008.33 3.62998 867.006 8791.08 0.37723032 209.7 6460.56 1058.73 872.2 243460 0.35981 311.386 2763.34 11333.3 717.03 626.314 2.58131 2.25473 16.2148 11626.5 10155.6 41.8554 36.56 0.05735 0.074211.24822 105.85657 0.10077 7.26345 0.05258 0.14 0.1107 2080.16 0.37723 111.421 88.4294 18.1869 14.4341 1443.86 5.19791 1241.5 1145.93 4.12533 985.319 9422.96 0.37723032 221.674 6829.46 1191.88 981.276 243460 0.35981 311.386 2763.34 11333.3 775.719 680.644 2.79259 2.45032 17.3399 13450.9 11802.3 48.4231 42.4881 0.0658 0.085551.33738 110.70603 0.09423 7.82596 0.05623 0.14 0.11028 2241.26 0.37723 119.929 94.8005 19.5756 15.474 1661.95 5.98302 1429.02 1313.73 4.72942 1129.6 10152.7 0.37723032 235.305 7249.4 1352 1112.18 243460 0.35981 311.386 2763.34 11333.3 840.504 741.151 3.02582 2.66814 18.6327 15660.8 13809.6 56.379 49.7146 0.07547 0.098621.42654 115.19393 0.08769 8.48291 0.06042 0.14 0.10976 2429.4 0.37723 129.865 102.156 21.1975 16.6746 1933.83 6.96178 1662.79 1521.2 5.47633 1308 11005 0.37723032 250.979 7732.29 1546.94 1271.13 243460 0.35981 311.386 2763.34 11333.3 911.948 808.526 3.28301 2.91069 20.1338 18361 16278.7 66.0995 58.6033 0.08664 0.11387

1.5157 119.32027 0.08115 9.26027 0.06529 0.1382 0.10913 2652.03 0.37723 139.825 110.736 22.8232 18.0751 2249.89 8.0996 1934.56 1781.83 6.41459 1532.1 12013.5 0.37723032 269.215 8294.13 1769.81 1466.73 243460 0.35981 311.386 2763.34 11333.3 985.076 883.467 3.54627 3.18048 21.898 21571.2 19346.1 77.6562 69.6461 0.09972 0.13188 Adiabatic DP1.60485 123.08505 0.07461 10.1945 0.07101 0.13451 0.10833 2919.57 0.37723 149.708 120.867 24.4364 19.7288 2620 9.43202 2252.8 2115.27 7.61495 1818.8 13225.4 0.37723032 290.732 8957.02 2027.07 1711.16 243460 0.35981 311.386 2763.34 11333.3 1059.95 966.637 3.81583 3.47989 24.001 25439.9 23200.3 91.5837 83.5209 0.11526 0.15349 3-Point Average Mass Flux = 3.21466 kg/m2.s1.69401 126.48826 0.06808 11.3383 0.07783 0.13011 0.1073 3247.15 0.37723 160.941 132.996 26.2699 21.7086 3087.1 11.1136 2654.43 2551.08 9.1839 2193.54 14709.3 0.37723032 316.548 9752.38 2344.84 2022.12 243460 0.35981 311.386 2763.34 11333.3 1140.79 1058.6 4.10685 3.81095 26.5509 30289.1 28106.7 109.041 101.184 0.13405 0.17992 Carman Ergun

Inner 1.78317 129.52991 0.06154 12.7713 0.08609 0.12478 0.10596 3657.54 0.37723 173.723 147.758 28.3563 24.1182 3686.33 13.2708 3169.67 3135.37 11.2873 2695.93 16568.3 0.37723032 348.167 10726.5 2743.49 2426.19 243460 0.35981 311.386 2763.34 11333.3 1227.57 1159.71 4.41926 4.17495 29.707 36467.5 34451.5 131.283 124.026 0.15727 0.21299 0.00847 0.01039 barWall 1.87233 132.21 0.055 14.6188 0.09633 0.1182 0.10417 4186.65 0.37723 188.246 166.077 30.7268 27.1083 4469.35 16.0897 3842.95 3943.03 14.1949 3390.4 18965.2 0.37723032 387.91 11950.9 3252.86 2964.83 243460 0.35981 311.386 2763.34 11333.3 1320.07 1270 4.75224 4.57199 33.7147 44505.7 42817.6 160.22 154.143 0.18678 0.25559

Carman ErgunCOOLED DP 0.18678 0.25559 bar TOTAL RADIAL DP = 0.19525 0.26598 bar

PRESSURE DROP

PRESSURE DROPESTIMATED CATALYST

ESTIMATED CATALYST

COOLED BED

COOLED BED

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VOLUME FOR CATALYST AND

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Reacted Gas Collected

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Cooled Catalyst Bed Volume (m3)

RADIAL FLOW ACME VOLUMETRIC UA PROFILE GCC - Outside-to-Inside Flow

Design UA - 3 Plate Layers

Estimated Optimum UA

Single Plate Layer

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RADIAL FLOW ACME VOLUMETRIC UA PROFILE GCC - Outside-to-Inside Flow



Single Plate Layer


RADIAL FLOW ACME REACTOR SET-UP - Gas-Cooled

- ADIABATIC BED LOCATED FROM INSIDE WALL OUTWARDS


ENTER CENTRAL DUCT OUTER DIAMETER (Doduct) = 1.5 m

ENTER CENTRAL DUCT INNER DIAMETER (Diduct) = 1.39 m



ENTER MOLAR FLOW OF REACTOR FEED GAS = 153219 9 kmol/h

ENTER MASS FLOW OF REACTOR FEED GAS = 409 7973 kg/s

ENTER REACTOR FEED TEMPERATURE = 245 DEG C AND PRESSURE = 86 2 bar(a)

APPROXIMATE (IDEALITY) VOLUMETRIC FEED FLOW AT 245 DEG C AND 86 2 bar(a) = 76550 43 m3/h

X-SECTIONAL AREA OF INNER DUCT = 1 517468 m2

AVERAGE AXIAL (VERTICAL) VELOCITY OF GAS THROUGH CENTRAL DUCT = 14 01282 m/s

INTERNALS

ENTER TOTAL CATALYST ACTIVE BULK VOLUME = 180 5 m3

ENTER VOLUME OF ADIABATIC BED = 48 29 m3 (If no adiabatic bed present set as very small value > 0 e g 0 001 m3)

Active Volume of Cooled Bed = 132 21 m3

ENTER AVERAGE EMBOSSED PLATE WIDTH = 0 012 m ENTER PLATE MATERIAL THICKNESS = 0 0015 m

ENTER CATALYST PELLET LENGTH = 5 2 mm

ENTER CATALYST PELLET DIAMETER = 5 4 mm

ENTER VOIDAGE OF CATALYST BED = 0 36

ENTER THERMAL CONDUCTIVITY OF CATALYST PELLET = 0 32 W/m K

ENTER THERMAL CONDUCTIVITY OF PLATE = 17 W/m K


Guess Diameter of Adiabatic Bed = 3 228622 m (If no adiabatic bed present this value should equal a fraction greater than the outer diameter of central duct due to calculation method employed)

TO ESTIMATE THE NUMBER OF PLATES INSTALLED ASSUMING ONE SINGLE PLATE BANK

Plate Width = 0 012 m

Guess Angle Subtended by Chord of Circle (inner duct or adi bed) equal to Plate Width = 0 42591 Degrees

Using Sine Rule: PRESS TO COMPUTE --------> (N B Requires 'Good' Initial Guess Values for Iterated Cells)

LHS = 0 619455 RHS = 0 619455 Difference = 1 28E-09 (Should be 0)

ENTER MINIMUM PLATE SPACING AT INNER RADII = 0 055 mEnter Angle Subtended by Arc Forming Plate Spacing = 1 952176 Degrees Chord Gap = 0 055 m



CATALYST BED HEIGHT = 7 521987 m Assumed Plate Height = 7 521987 mAssumed Plate Breadth = 1 385689 m

Cooled A/V = 23 808987 m2/m3Cat

Cooled Bed Volume = 132 21 m3 Actual Volume = 132 21 m3 DIFFERENCE = -1 5E-07 (Should be 0)



Guess Diameter of Adiabatic Bed = 3 189126 m

Breadth of Each Plate Bank = 0 468479 m

First Plate Layer (Counting from Adiabtic Bed/Central Duct Outwards)



Using Sine Rule:

LHS = 0 627127 RHS = 0 627127 Difference = -1 3E-10 (Should be 0)


( should equal minimum plate spacing)NUMBER OF PLATES IN FIRST PLATE LAYER = 149

Second Plate Layer



Using Sine Rule:




Third Plate Layer



Using Sine Rule:



( should equal minimum plate spacing)NUMBER OF PLATES IN THIRD PLATE LAYER = 237


Cooled Bed Volume = 132 21 m3 Actual Volume = 132 21 m3 DIFFERENCE = 1 73E-08 (Should be 0)


Overall Cooled A/V = 31 85279 m2/m3Cat

Area Basis Vol BasisCatalyst Particle Equivelant/Effective Diameter = 0 005298 m 0 007566 m 0 007691 m Dp (Volume)/Dp (Area) = 1 016532



Phi1 coeff -1 00234 Phi2 coeff -1 13595-0 49574 -0 728850 046918 0 05113-0 00194 -0 00131

ks/kg 1 960457

Phi1 0 26837 0 2891698Phi2 0 201126 0 2112543

phi 0 232257 0 2473263

Gamma 1Beta 1Alpha 0 122988 0 1041672Emmis 0 6Hrv 26 92895Hrs 13 70491ke0/kg 1 562824

Equivelant 'Outer' Diameter of Plate = 0 024 m

HTC PROFILES FOR GAS-COOLED PART OF BED (In - Out) INSIDE PLATE - Based on Dittus-Boelter Correlation:

i) 3 Plate Layers Plate Mass Flux = 110 79 kg/m2 sPlate Equivelant 'Inner' Diameter = 0 018 m

Radial Distance from Inside to Outside of Cooled Catalyst Bed = 1 405437 m For Plate Outer Wall HTC For Plate Inside Wall

Radial Bed Approx Mass Dp/Gap AB (1) AB (2) Re Pr ke/kg (1) ke/kg (2) ke (1) ke (2) hbed (1) hbed (2) Re Pr Nu h(outerwall) h(overall) bedside Re Pr Nu h(inside plate) h (Plate Solid Wall) OVERALL U OVERALL VOLUMETRIC UADistance Volume Plate Flux 1 2 1 2 1 2 Specific 1 2 1 2 Carman Ergun(m) (m3) Spacing (m(kg/m2 s) (W/m K) (W/m K) W/m2 K MJ/hr m2 K kcal/h m2 K W/m2.K MJ/hr m2 K kcal/h.m2.K W/m2.K W/m2.K W/m2.K W/m2.K w/m2 K w/m2 K w/m2 K MJ/hr m2 K MJ/hr.m2.K A (m2/m3) w/m3 K w/m3 K MJ/hr m3 K MJ/hr.m3.K bar bar

Inner 0 0 0 055 6 41367 0 096329 0 118204 0 104167 1836 797 0 37723 83 46573 73 73979 13 62388 12 03634 1981 648 7 133933 1703 911 1750 734 6 302643 1505 36 8320 535 0 37723032 200 6716 6182 402 1500 645 1364 371 117635 7 0 359811 174 0159 1544 27 11333 33 713 1802 680 861 2 567449 2 451099 0 0 0 0 0 0 0Wall 0 066926 4 3853965 0 057309 6 101932 0 092449 0 120678 0 104863 1747 519 0 37723 81 11597 70 6903 13 24033 11 53858 1848 285 6 653827 1589 239 1610 729 5 798624 1384 978 7916 113 0 37723032 192 8299 5940 812 1409 703 1267 164 117635 7 0 359811 174 0159 1544 27 11333 33 691 9652 655 7573 2 491075 2 360726 56 15323 38856 08 36822 89 139 8819 132 5624 0 005124 0 006786

0 133851 8 9892557 0 059617 5 819094 0 088869 0 122988 0 105487 1666 518 0 37723 78 88037 67 8786 12 87542 11 07964 1727 751 6 219903 1485 598 1486 774 5 352388 1278 396 7549 183 0 37723032 185 6457 5719 475 1326 914 1180 027 117635 7 0 359811 174 0159 1544 27 11333 33 671 4029 631 6208 2 417051 2 273835 53 48864 35912 43 33784 54 129 2847 121 6243 0 009805 0 0129520 200777 13 811577 0 061925 5 561314 0 085556 0 125125 0 106049 1592 693 0 37723 76 7394 65 27863 12 52596 10 65525 1618 198 5 825514 1391 4 1376 526 4 955493 1183 599 7214 762 0 37723032 179 0369 5515 868 1251 147 1101 611 117635 7 0 359811 174 0159 1544 27 11333 33 651 4418 608 4383 2 34519 2 190378 51 06548 33266 19 31070 19 119 7583 111 8527 0 014099 0 0185790 267702 18 852362 0 064234 5 325404 0 082482 0 127109 0 106557 1525 131 0 37723 74 69168 62 86793 12 19172 10 26176 1518 416 5 466297 1305 603 1278 049 4 600978 1098 925 6908 713 0 37723032 172 9349 5327 874 1181 651 1030 785 117635 7 0 359811 174 0159 1544 27 11333 33 632 0859 586 1923 2 275509 2 110292 48 85235 30878 88 28636 87 111 164 103 0927 0 018055 0 0237370 334628 24 111609 0 066542 5 108694 0 07962 0 128955 0 107017 1463 068 0 37723 72 73467 60 62707 11 87228 9 895988 1427 336 5 13841 1227 288 1189 738 4 283057 1022 991 6627 573 0 37723032 167 2817 5153 708 1117 767 966 5981 117635 7 0 359811 174 0159 1544 27 11333 33 613 3347 564 8612 2 208005 2 0335 46 82308 28718 22 26448 54 103 3856 95 21476 0 021712 0 0284810 401553 29 589319 0 068851 4 908932 0 076951 0 130677 0 107435 1405 859 0 37723 70 86505 58 53915 11 5671 9 555182 1344 021 4 838477 1155 65 1110 249 3 996898 954 6426 6368 419 0 37723032 162 028 4991 85 1058 916 908 2445 117635 7 0 359811 174 0159 1544 27 11333 33 595 1841 544 4205 2 142663 1 959914 44 95568 26756 91 24474 8 96 32486 88 10927 0 025104 0 0328610 468479 35 285491 0 055 4 958496 0 096329 0 118204 0 104167 1420 053 0 37723 64 88296 57 36379 10 59067 9 363332 1540 46 5 545658 1324 558 1361 939 4 902981 1171 057 6432 719 0 37723032 163 3355 5032 131 1179 413 1071 846 117635 7 0 359811 174 0159 1544 27 11333 33 631 4448 599 2472 2 273201 2 15729 35 20541 22230 27 21096 74 80 02898 75 94828 0 028402 0 0371130 535404 40 925817 0 056784 4 770091 0 093303 0 120127 0 104712 1366 096 0 37723 63 46841 55 52412 10 35977 9 063048 1459 528 5 254302 1254 969 1276 84 4 596626 1097 885 6188 299 0 37723032 158 3514 4878 578 1123 431 1011 981 117635 7 0 359811 174 0159 1544 27 11333 33 615 0361 580 0628 2 21413 2 088226 35 55399 21866 99 20623 55 78 72115 74 24477 0 031615 0 0412480 60233 46 784606 0 058568 4 595479 0 09046 0 121961 0 105212 1316 089 0 37723 62 11273 53 79728 10 13849 8 78118 1384 84 4 985424 1190 748 1199 442 4 317992 1031 335 5961 773 0 37723032 153 6969 4735 181 1071 478 957 0238 117635 7 0 359811 174 0159 1544 27 11333 33 599 1323 561 5781 2 156876 2 021681 34 22825 20507 25 19221 83 73 8261 69 1986 0 03461 0 045086

0 669256 52 861858 0 060353 4 4332 0 087786 0 123686 0 105673 1269 615 0 37723 60 80087 52 17346 9 924357 8 516129 1315 516 4 735857 1131 14 1128 849 4 063858 970 6357 5751 245 0 37723032 149 3394 4600 931 1023 012 906 4497 117635 7 0 359811 174 0159 1544 27 11333 33 583 6704 543 7752 2 101214 1 957591 32 99783 19259 86 17943 4 69 33548 64 59623 0 03741 0 0486580 736181 59 157572 0 062137 4 28199 0 085265 0 125313 0 106098 1226 31 0 37723 59 53266 50 64396 9 717351 8 266473 1251 09 4 503925 1075 744 1064 293 3 831453 915 1268 5555 079 0 37723032 145 2503 4474 953 977 738 859 8028 117635 7 0 359811 174 0159 1544 27 11333 33 568 6474 526 6352 2 04713 1 895887 31 85279 18113 01 16774 8 65 20683 60 38929 0 040033 0 0519910 803107 65 671749 0 063921 4 140756 0 082885 0 126848 0 106491 1185 862 0 37723 58 30751 49 201 9 517372 8 030942 1191 141 4 288106 1024 197 1005 107 3 618387 864 2369 5371 854 0 37723032 141 4048 4356 479 935 3884 816 6854 117635 7 0 359811 174 0159 1544 27 11333 33 554 0581 510 1385 1 994609 1 836499 30 78456 17056 44 15704 39 61 40317 56 53581 0 042496 0 0551090 870032 72 404389 0 065705 4 00854 0 080635 0 1283 0 106856 1147 997 0 37723 57 12447 47 83762 9 324269 7 808402 1135 284 4 087022 976 1685 950 7184 3 422586 817 4707 5200 329 0 37723032 137 7811 4244 836 895 7225 776 7494 117635 7 0 359811 174 0159 1544 27 11333 33 539 8963 494 2649 1 943627 1 779353 29 78566 16081 17 14722 57 8922 52 99921 0 044814 0 0580320 936958 79 355491 0 055 4 041529 0 096329 0 118204 0 104167 1157 445 0 37723 53 17326 47 0446 8 679323 7 678959 1262 447 4 544809 1085 509 1116 939 4 020982 960 395 5243 125 0 37723032 138 6874 4272 759 974 5133 885 4694 117635 7 0 359811 174 0159 1544 27 11333 33 567 5551 536 1543 2 043198 1 930155 22 27244 12640 84 11941 47 45 50702 42 98928 0 04708 0 0608851 003883 86 250747 0 056454 3 915478 0 093848 0 119779 0 104614 1121 345 0 37723 52 22993 45 81522 8 525347 7 47829 1208 112 4 349202 1038 789 1059 735 3 815047 911 2082 5079 598 0 37723032 135 2161 4165 812 936 5162 844 8221 117635 7 0 359811 174 0159 1544 27 11333 33 554 4536 520 9768 1 996033 1 875516 22 45283 12449 05 11697 4 44 81659 42 11065 0 049299 0 0636751 070809 93 364466 0 057908 3 797052 0 091492 0 121296 0 105032 1087 429 0 37723 51 31966 44 64797 8 376765 7 287763 1157 25 4 166101 995 0561 1006 805 3 624497 865 6962 4925 962 0 37723032 131 9343 4064 706 900 7893 806 9322 117635 7 0 359811 174 0159 1544 27 11333 33 541 733 506 3158 1 950239 1 822737 21 7633 11789 9 11019 1 42 44364 39 66878 0 051394 0 06631 137735 100 69665 0 059362 3 685579 0 089251 0 122741 0 105422 1055 505 0 37723 50 43459 43 53838 8 232298 7 106649 1109 435 3 993966 953 9425 957 7357 3 447849 823 5045 4781 347 0 37723032 128 8265 3968 958 867 0659 771 5545 117635 7 0 359811 174 0159 1544 27 11333 33 529 3511 492 1563 1 905664 1 771763 21 11486 11177 18 10391 81 40 23784 37 41053 0 053375 0 068774 Adiabatic DP1 20466 108 24729 0 060816 3 580465 0 087117 0 124118 0 105787 1025 402 0 37723 49 57327 42 48241 8 091707 6 934285 1064 416 3 831898 915 2331 912 1641 3 283791 784 32 4644 982 0 37723032 125 8787 3878 14 835 1862 738 4709 117635 7 0 359811 174 0159 1544 27 11333 33 517 2963 478 4827 1 862267 1 722538 20 50395 10606 62 9810 784 38 18382 35 31882 0 055253 0 07111 3-Point Average Mass Flux = 7 879559 kg/m2 s

1 271586 116 0164 0 06227 3 48118 0 085083 0 125431 0 106129 996 9677 0 37723 48 73554 41 47635 7 954966 6 770069 1021 994 3 679179 878 7568 869 7675 3 131163 747 8654 4516 178 0 37723032 123 0784 3791 867 805 0224 707 4863 117635 7 0 359811 174 0159 1544 27 11333 33 505 5633 465 2796 1 820028 1 675007 19 92739 10074 56 9271 809 36 2684 33 37851 0 057035 0 07332 Carman Ergun1 338511 124 00397 0 063724 3 387253 0 083141 0 126683 0 106449 970 0682 0 37723 47 92109 40 51684 7 822026 6 613451 981 9854 3 535148 844 3555 830 2596 2 988935 713 8947 4394 326 0 37723032 120 4145 3709 796 776 4568 678 4264 117635 7 0 359811 174 0159 1544 27 11333 33 494 1464 452 5318 1 778927 1 629115 19 38237 9577 727 8771 139 34 47982 31 5761 0 058729 0 075413 0 099291 0 134944 bar

Outside 1 405437 132 21 0 065178 3 298262 0 081287 0 12788 0 106751 944 5821 0 37723 47 12953 39 60081 7 692822 6 46393 944 2202 3 399193 811 8832 793 3855 2 856188 682 1887 4278 876 0 37723032 117 8769 3631 617 749 3811 651 1346 117635 7 0 359811 174 0159 1544 27 11333 33 483 0393 440 2239 1 738942 1 584806 18 86637 9113 198 8305 427 32 80751 29 89954 0 060342 0 0774Wall Carman Ergun

COOLED DP 0 060342 0 0774 bar TOTAL RADIAL DP = 0 159632 0 212344 bar

ii) Single Plate Layer Plate Mass Flux = 143 6238 kg/m2 sPlate Equivelant 'Inner' Diameter = 0 018 m



Inner 0 0 0 055 6 53941 0 096329 0 118204 0 104167 1872 807 0 37723 85 07127 75 15477 13 88595 12 2673 2019 774 7 271187 1736 693 1784 335 6 423606 1534 252 8483 658 0 37723032 203 8128 6279 177 1528 208 1389 488 152498 3 0 359811 214 1755 1900 659 11333 33 788 1897 749 5926 2 837483 2 698533 0 0 0 0 0 0 0Wall 0 065985 4 2379043 0 057248 6 2294 0 092546 0 120615 0 104846 1784 025 0 37723 82 73541 72 12274 13 50467 11 77239 1887 177 6 793837 1622 68 1645 104 5 922375 1414 535 8081 479 0 37723032 196 0458 6039 888 1437 901 1292 942 152498 3 0 359811 214 1755 1900 659 11333 33 763 4598 720 5655 2 748455 2 594036 35 36998 27003 56 25486 39 97 2128 91 75099 0 005243 0 00696

0 13197 8 6815896 0 059496 5 947454 0 08905 0 122871 0 105456 1703 278 0 37723 80 5111 69 32148 13 1416 11 31515 1767 049 6 361377 1519 389 1521 46 5 477258 1308 22 7715 706 0 37723032 188 9146 5820 185 1355 507 1206 158 152498 3 0 359811 214 1755 1900 659 11333 33 739 5904 692 7857 2 662525 2 494029 33 73204 24947 89 23369 08 89 81242 84 12868 0 010044 0 0132990 197956 13 331056 0 061744 5 689924 0 085807 0 124963 0 106007 1629 525 0 37723 78 37843 66 72628 12 79349 10 89154 1657 607 5 967385 1425 285 1411 178 5 080242 1213 395 7381 609 0 37723032 182 3416 5617 681 1279 937 1127 857 152498 3 0 359811 214 1755 1900 659 11333 33 716 5082 666 22 2 57943 2 398392 32 23909 23099 58 21478 33 83 15847 77 32198 0 014457 0 0190960 263941 18 186303 0 063993 5 453771 0 082793 0 126908 0 106506 1561 894 0 37723 76 33619 64 31577 12 46014 10 49808 1557 7 5 607719 1339 381 1312 414 4 72469 1128 473 7075 245 0 37723032 176 2618 5430 37 1210 475 1056 966 152498 3 0 359811 214 1755 1900 659 11333 33 694 208 640 8313 2 499149 2 306993 30 8727 21432 07 19784 19 77 15546 71 22309 0 01853 0 024420 329926 23 247332 0 066241 5 23644 0 079983 0 128721 0 10696 1499 653 0 37723 74 38203 62 07142 12 14117 10 13174 1466 31 5 278718 1260 8 1223 628 4 405062 1052 131 6793 298 0 37723032 170 6198 5256 55 1146 496 992 5752 152498 3 0 359811 214 1755 1900 659 11333 33 672 6798 616 5802 2 421647 2 219689 29 61742 19923 04 18261 51 71 72294 65 74144 0 022301 0 0293260 395911 28 514141 0 068489 5 035766 0 077357 0 130415 0 107372 1442 182 0 37723 72 5129 59 97702 11 83608 9 789881 1382 542 4 977151 1188 772 1143 531 4 116711 983 2596 6532 961 0 37723032 165 3686 5094 767 1087 447 933 9123 152498 3 0 359811 214 1755 1900 659 11333 33 651 9101 593 425 2 346876 2 13633 28 46023 18553 51 16889 01 66 79263 60 80043 0 025804 0 0338620 461896 33 986731 0 070737 4 849904 0 074899 0 132001 0 107749 1388 954 0 37723 70 72534 58 01838 11 5443 9 470179 1305 604 4 700174 1122 617 1071 031 3 855711 920 9208 6291 842 0 37723032 160 4675 4943 772 1032 84 880 3169 152498 3 0 359811 214 1755 1900 659 11333 33 631 8826 571 323 2 274777 2 056763 27 39006 17307 3 15648 57 62 30629 56 33486 0 029067 0 038070 527881 39 665102 0 072985 4 677275 0 072592 0 133489 0 108093 1339 515 0 37723 69 01565 56 18303 11 26523 9 170599 1234 799 4 445276 1061 736 1005 203 3 61873 864 3189 6067 887 0 37723032 155 8816 4802 487 982 2469 831 221 152498 3 0 359811 214 1755 1900 659 11333 33 612 5789 550 2311 2 205284 1 980832 26 39746 16170 53 14524 7 58 2139 52 28893 0 032115 0 0419830 593867 45 549255 0 075233 4 516512 0 070423 0 134889 0 10841 1293 474 0 37723 67 38009 54 45993 10 99826 8 889343 1169 512 4 210243 1005 599 945 2576 3 402927 812 7752 5859 327 0 37723032 151 5804 4669 974 935 2861 786 1347 152498 3 0 359811 214 1755 1900 659 11333 33 593 9793 530 1059 2 138326 1 908381 25 47429 15131 2 13504 07 54 47232 48 61465 0 034969 0 0456320 659852 51 639188 0 077481 4 366433 0 068379 0 136207 0 1087 1250 493 0 37723 65 81491 52 83932 10 74278 8 624815 1109 2 3 99312 953 7402 890 5181 3 205865 765 7077 5664 628 0 37723032 147 5374 4545 413 891 621 744 6328 152498 3 0 359811 214 1755 1900 659 11333 33 576 0629 510 9046 2 073827 1 839257 24 6135 14178 93 12575 15 51 04413 45 27054 0 037647 0 0490430 725837 57 934902 0 079729 4 226007 0 066451 0 137451 0 108968 1210 277 0 37723 64 31646 51 31251 10 4982 8 375598 1053 382 3 792175 905 7455 840 4019 3 025447 722 6155 5482 452 0 37723032 143 7291 4428 086 850 952 706 3453 152498 3 0 359811 214 1755 1900 659 11333 33 558 8081 492 5849 2 011709 1 773306 23 80899 13304 66 11727 95 47 89676 42 22061 0 040166 0 052240 791822 64 436398 0 081978 4 094332 0 064629 0 138627 0 109215 1172 567 0 37723 62 88122 49 87175 10 26393 8 140427 1001 632 3 605877 861 2488 794 4051 2 859858 683 0654 5311 628 0 37723032 140 1351 4317 361 813 0126 670 9489 152498 3 0 359811 214 1755 1900 659 11333 33 542 1929 475 1056 1 951895 1 71038 23 0554 12500 48 10953 75 45 00171 39 4335 0 042541 0 0552410 857807 71 143674 0 084226 3 970615 0 062904 0 13974 0 109444 1137 136 0 37723 61 50578 48 51011 10 03942 7 91817 953 5727 3 432862 819 9249 752 0904 2 707526 646 6814 5151 128 0 37723032 136 7372 4212 677 777 5647 638 1596 152498 3 0 359811 214 1755 1900 659 11333 33 526 1953 458 4265 1 894303 1 650335 22 34805 11759 44 10244 94 42 33399 36 88179 0 044783 0 0580650 923793 78 056731 0 086474 3 854155 0 061268 0 14 0 109656 1103 783 0 37723 59 85609 47 22137 9 770143 7 707812 903 8702 3 253933 777 1885 713 0768 2 567076 613 1357 5000 043 0 37723032 133 5193 4113 535 741 0408 607 7279 152498 3 0 359811 214 1755 1900 659 11333 33 509 2111 442 5088 1 83316 1 593032 21 68282 11041 13 9594 839 39 74808 34 54142 0 046904 0 0607260 989778 85 175569 0 088722 3 744332 0 059716 0 14 0 109853 1072 331 0 37723 58 19504 45 99993 9 499014 7 508441 856 5195 3 08347 736 4742 677 0309 2 437311 582 1418 4857 568 0 37723032 130 4668 4019 494 706 0635 579 433 152498 3 0 359811 214 1755 1900 659 11333 33 492 4478 427 3151 1 772812 1 538334 21 05604 10369 8997 565 37 32841 32 39123 0 048914 0 063241 055763 92 500189 0 09097 3 640594 0 05824 0 14 0 110036 1042 622 0 37723 56 62603 44 84076 9 242909 7 319232 812 8304 2 926189 698 9083 643 6604 2 317177 553 4483 4722 988 0 37723032 127 567 3930 156 673 5314 553 0798 152498 3 0 359811 214 1755 1900 659 11333 33 476 3991 412 8093 1 715037 1 486114 20 46449 9749 263 8447 931 35 09735 30 41255 0 050821 0 0656181 121748 100 03059 0 093218 3 54245 0 056836 0 14 0 110206 1014 515 0 37723 55 14162 43 73929 9 000612 7 139443 772 4335 2 780761 664 1733 612 7077 2 205748 526 8338 4595 664 0 37723032 124 8083 3845 164 643 2205 528 4947 152498 3 0 359811 214 1755 1900 659 11333 33 461 0323 398 9571 1 659716 1 436246 19 90526 9176 968 7941 345 33 03708 28 58884 0 052634 0 06787 Adiabatic DP1 187733 107 76677 0 095466 3 449458 0 055497 0 14 0 110365 987 8829 0 37723 53 73514 42 69139 8 771037 6 968397 735 0053 2 646019 631 9908 583 9456 2 102204 502 1029 4475 025 0 37723032 122 1803 3764 199 614 9323 505 5231 152498 3 0 359811 214 1755 1900 659 11333 33 446 3162 385 7254 1 606738 1 388612 19 37578 8647 727 7473 733 31 13182 26 90544 0 05436 0 070007 3-Point Average Mass Flux = 8 088957 kg/m2 s1 253718 115 70873 0 097715 3 361224 0 05422 0 14 0 110514 962 6136 0 37723 52 40061 41 69331 8 553205 6 805483 700 2608 2 520939 602 1159 557 1728 2 005822 479 0824 4360 557 0 37723032 119 6736 3686 972 588 4899 484 027 152498 3 0 359811 214 1755 1900 659 11333 33 432 2206 373 0829 1 555994 1 343098 18 87375 8157 622 7041 472 29 36744 25 3493 0 056004 0 072038 Carman Ergun1 319704 123 85648 0 099963 3 277391 0 053001 0 14 0 110653 938 6048 0 37723 51 13265 40 74164 8 34624 6 650144 667 9487 2 404615 574 3325 532 2104 1 915957 457 6185 4251 8 0 37723032 117 2798 3613 221 563 7353 463 8826 152498 3 0 359811 214 1755 1900 659 11333 33 418 7165 360 9996 1 507379 1 299598 18 39707 7703 155 6641 333 27 73136 23 9088 0 057574 0 07397 0 106708 0 145448 bar

Outside 1 385689 132 21 0 102211 3 197638 0 051835 0 14 0 110783 915 7645 0 37723 49 9264 39 83326 8 149348 6 501872 637 8465 2 296247 548 4492 508 8991 1 832037 437 5745 4148 335 0 37723032 114 991 3542 708 540 5273 444 9792 152498 3 0 359811 214 1755 1900 659 11333 33 405 776 349 4469 1 460793 1 258009 17 94387 7281 192 6270 432 26 21229 22 57355 0 059073 0 07581Wall Carman Ergun

COOLED DP 0 059073 0 07581 bar TOTAL RADIAL DP = 0 165781 0 221258 bar

ESTIMATED CATALYSTPRESSURE DROP


COOLED BED

COOLED BED

Do

Di

Doduct

FEED GAS


PLATES


0 5000

10000 15000 20000 25000 30000 35000 40000 45000 50000

0 20 40 60 80 100 120 140

UA

(W/m

3 .K)


RADIAL FLOW ACME VOLUMETRIC UA PROFILE GCC - Inside-to-Outside Flow



Single Plate Layer

Diduct

60

80

100

120

140

160

180

UA

(MJ/

h.m

3 .K)

RADIAL FLOW ACME VOLUMETRIC UA PROFILE GCC - Inside-to-Outside Flow


RADIAL FLOW ACME REACTOR SET-UP - Water-Cooled

- ADIABATIC BED LOCATED FROM OUTSIDE WALL INWARDS


ENTER CENTRAL DUCT OUTER DIAMETER (Dduct) = 1.5 m



ENTER MOLAR FLOW OF REACTOR FEED GAS = 153220 kmol/h

ENTER MASS FLOW OF REACTOR FEED GAS = 409.797 kg/s

ENTER REACTOR FEED TEMPERATURE = 245 DEG C AND PRESSURE = 86.2 bar(a)

APPROXIMATE (IDEALITY) VOLUMETRIC FEED FLOW AT 245 DEG C AND 86.2 bar(a) = 76550.4 m3/h

X-SECTIONAL AREA OF ANNULUS = 21.9911 m2

AVERAGE AXIAL (VERTICAL) VELOCITY OF GAS THROUGH ANNULUS = 0.96693 m/s

INTERNALS

ENTER TOTAL CATALYST ACTIVE BULK VOLUME = 233.9 m3

ENTER VOLUME OF ADIABATIC BED = 0.001 m3 (If no adiabatic bed present set as very small value > 0 e.g. 0.001 m3)

Active Volume of Cooled Bed = 233.899 m3

ENTER AVERAGE EMBOSSED PLATE WIDTH = 0.012 m ENTER PLATE MATERIAL THICKNESS = 0.0015 m

ENTER CATALYST PELLET LENGTH = 5.2 mm

ENTER CATALYST PELLET DIAMETER = 5.4 mm

ENTER VOIDAGE OF CATALYST BED = 0.36

ENTER THERMAL CONDUCTIVITY OF CATALYST PELLET = 0.32 W/m.K

ENTER THERMAL CONDUCTIVITY OF PLATE = 17 W/m.K




Using Sine Rule:




PRESS TO COMPUTE ------------> (N.B. Requires 'Good' Initial Guess Values for Iterated Cells)



CATALYST BED HEIGHT = 9.50149 m Assumed Plate Height = 9.50149 mSingle Plate Breadth = 2.24999 m

Cooled Bed Volume = 233.899 m3 Actual Volume = 233.899 m3 DIFFERENCE = -4E-07 (Should be 0)

Overall Cooled A/V = 12.796 m2/m3Cat (Single Plate Layer)



CALCULATION OF CATALYST BED HEIGHT


CATALYST BED HEIGHT = 10.2916 m Assumed Plate Height = 10.2916 mEquivelant Single Plate Breadth = 2.24999 m

Breadth of Each Plate Bank = 0.75 m

First Plate Layer (Counting from Central Duct Outwards)Number of Plates = 70

Second Plate Layer



Using Sine Rule:




Third Plate Layer



Using Sine Rule:



( should equal minimum plate spacing)NUMBER OF PLATES IN THIRD PLATE BANK = 210



Overall Cooled A/V = 27.7201 m2/m3Cat

Area Basis Vol. BasisCatalyst Particle Equivelant/Effective Diameter = 0.0053 m 0.00757 m 0.00769 m Dp (Volume)/Dp (Area) = 1.01653



Phi1 coeff -1.00234 Phi2 coeff -1.13595-0.49574 -0.728850.04692 0.05113

-0.00194 -0.00131

ks/kg 2.07908

Phi1 0.26163 0.2826695Phi2 0.19349 0.2025676

phi 0.22504 0.2396518

Gamma 1Beta 1Alpha 0.13371 0.1081442Emmis. 0.6Hrv 24.9888Hrs 12.7175ke0/kg 1.60283

Equivelant 'Outer' Diameter of Plate = 0.024 m

HTC PROFILES FOR WATER-COOLED PART OF BED (Out - In) INSIDE PLATE - Based on Dittus-Boelter Correlation:

i) 3 Plate Layers Plate Mass Flux = 123.648 kg/m2.sPlate Equivelant 'Inner' Diameter = 0.018 m

Radial Distance From Outside to Inside Of 'Cooled' Bed = 2.24999 For Plate Outer Wall HTC For Plate Inside Wall

Radial Bed Approx. Mass Dp/Gap AB (1) AB (2) Re Pr ke/kg (1) ke/kg (2) ke (1) ke (2) hbed (1) hbed (2) Re Pr Nu h(outerwall) h(overall) bedside Re Pr Nu h(inside plate) h (Plate Solid Wall) OVERALL U OVERALL VOLUMETRIC UADistance Volume Plate Flux 1 2 1 2 1 2 Specific 1 2 1 2 Carman Ergun(m) (m3) Spacing (m(kg/m2.s) (W/m.K) (W/m.K) W/m2.K MJ/hr.m2.K kcal/h.m2.K W/m2.K MJ/hr.m2.K kcal/h.m2.K W/m2.K W/m2.K W/m2.K W/m2.K w/m2.K w/m2.K w/m2.K MJ/hr.m2.K MJ/hr.m2.K A (m2/m3) w/m3.K w/m3.K MJ/hr.m3.K MJ/hr.m3.K bar bar

Outside 0 0 0.07333 2.43844 0.07225 0.13371 0.10814 711.028 0.38222 37.9414 30.993 5.83971 4.77025 637.06 2.29341 547.773 520.391 1.87341 447.456 3220.9 0.38221833 94.3296 2740.34 516.895 437.34 19311.6 0.85506 57.967 2043.74 11333.3 398.063 349.152 1.43303 1.25695 0 0 0 0 0 0 0Wall 0.10714 17.63496 0.07071 2.54328 0.07492 0.13199 0.10775 741.601 0.38222 39.0145 32.1436 6.00489 4.94735 679.341 2.44563 584.128 559.7 2.01492 481.256 3359.39 0.38221833 97.5607 2834.21 547.991 467.398 19311.6 0.85506 57.967 2043.74 11333.3 416.254 368.048 1.49851 1.32497 26.2616 10931.5 9665.54 39.3534 34.7959 0.0014 0.00167

0.21429 34.527605 0.0681 2.65755 0.0778 0.13013 0.1073 774.922 0.38222 40.1448 33.3847 6.17885 5.13838 725.907 2.61327 624.168 603.67 2.17321 519.063 3510.33 0.38221833 101.052 2935.63 581.995 500.707 19311.6 0.85506 57.967 2043.74 11333.3 435.585 388.393 1.56811 1.39822 27.4156 11941.8 10648 42.9906 38.333 0.00292 0.003490.32143 50.677933 0.06548 2.78258 0.08092 0.12812 0.10681 811.377 0.38222 41.3353 34.7272 6.36208 5.345 777.331 2.79839 668.384 653.062 2.35102 561.533 3675.47 0.38221833 104.838 3045.61 619.274 537.753 19311.6 0.85506 57.967 2043.74 11333.3 456.136 410.32 1.64209 1.47715 28.6757 13080 11766.2 47.0881 42.3584 0.00456 0.005470.42857 66.085946 0.06286 2.91994 0.08429 0.12594 0.10626 851.432 0.38222 42.5889 36.1835 6.55503 5.56915 834.276 3.00339 717.348 708.801 2.55168 609.459 3856.91 0.38221833 108.958 3165.31 660.254 579.12 19311.6 0.85506 57.967 2043.74 11333.3 477.988 433.973 1.72076 1.5623 30.0572 14367 13044 51.7212 46.9585 0.00636 0.007640.53571 80.751643 0.06024 3.07158 0.08795 0.12358 0.10564 895.647 0.38222 43.9079 37.7683 6.75804 5.81308 897.511 3.23104 771.72 772.014 2.77925 663.812 4057.2 0.38221833 113.461 3296.14 705.428 625.509 19311.6 0.85506 57.967 2043.74 11333.3 501.225 459.51 1.80441 1.65423 31.5786 15828 14510.7 56.9808 52.2384 0.00832 0.010030.64286 94.675025 0.05762 3.23982 0.09195 0.121 0.10495 944.706 0.38222 45.2938 39.4989 6.97135 6.07943 967.923 3.48452 832.264 844.087 3.03871 725.784 4279.44 0.38221833 118.407 3439.8 755.37 677.77 19311.6 0.85506 57.967 2043.74 11333.3 525.931 487.101 1.89335 1.75356 33.2622 17493.6 16202.1 62.9771 58.3274 0.01047 0.01268

0.75 107.85609 0.055 3.42756 0.09633 0.1182 0.10417 999.45 0.38222 46.7576 41.3955 7.19665 6.37135 1046.78 3.76843 900.073 926.742 3.33627 796.855 4527.42 0.38221833 123.865 3598.36 810.892 736.945 19311.6 0.85506 57.967 2043.74 11333.3 552.259 516.933 1.98813 1.86096 35.1354 19403.9 18162.7 69.8539 65.3856 0.01286 0.015620.85714 121.22109 0.07857 3.37904 0.06743 0.13682 0.10883 985.303 0.38222 53.129 42.5893 8.17729 6.5551 832.598 2.99735 715.905 667.428 2.40274 573.885 4463.34 0.38221833 122.46 3557.55 674.694 561.993 19311.6 0.85506 57.967 2043.74 11333.3 485.511 424.283 1.74784 1.52742 23.1013 11215.9 9801.49 40.3773 35.2853 0.01533 0.018680.96428 133.84376 0.07464 3.58378 0.07098 0.13453 0.10833 1045 0.38222 55.3364 44.8715 8.51705 6.90636 912.832 3.2862 784.894 740.203 2.66473 636.46 4733.77 0.38221833 128.361 3728.97 733.32 617.608 19311.6 0.85506 57.967 2043.74 11333.3 515.146 455.231 1.85453 1.63883 24.4598 12600.4 11134.9 45.3614 40.0855 0.01791 0.021881.07143 145.72413 0.07071 3.81492 0.07492 0.13199 0.10775 1112.4 0.38222 57.7204 47.4139 8.88398 7.29767 1005.06 3.6182 864.193 825.596 2.97214 709.884 5039.09 0.38221833 134.942 3920.17 799.962 681.971 19311.6 0.85506 57.967 2043.74 11333.3 547.167 489.267 1.9698 1.76136 25.9881 14219.9 12715.1 51.1915 45.7745 0.02079 0.025481.17857 156.86218 0.06679 4.07794 0.07933 0.12914 0.10706 1189.1 0.38222 60.2971 50.2624 9.28057 7.73609 1111.68 4.00206 955.875 926.676 3.33604 796.798 5386.5 0.38221833 142.335 4134.94 876.134 757.021 19311.6 0.85506 57.967 2043.74 11333.3 581.763 526.731 2.09435 1.89623 27.7201 16126.6 14601.1 58.0556 52.5639 0.02404 0.029571.28571 167.25791 0.06286 4.37991 0.08429 0.12594 0.10626 1277.15 0.38222 63.0819 53.4738 9.70919 8.23038 1235.71 4.44857 1062.52 1047.5 3.77101 900.69 5785.37 0.38221833 150.706 4378.13 963.71 845.266 19311.6 0.85506 57.967 2043.74 11333.3 619.122 567.99 2.22884 2.04476 29.6995 18387.6 16869 66.1955 60.7285 0.02773 0.034251.39285 176.91132 0.05893 4.73018 0.08991 0.12232 0.10531 1379.28 0.38222 66.0872 57.1199 10.1718 8.79155 1380.89 4.97121 1187.35 1193.52 4.29667 1026.24 6248.03 0.38221833 160.273 4656.06 1065.03 950 19311.6 0.85506 57.967 2043.74 11333.3 659.423 613.434 2.37392 2.20836 31.9833 21090.5 19619.7 75.9259 70.6308 0.03196 0.03966

1.5 185.82242 0.055 5.14134 0.09633 0.1182 0.10417 1499.17 0.38222 69.3349 61.2918 10.6716 9.43367 1552.23 5.58805 1334.68 1372.17 4.93981 1179.85 6791.13 0.38221833 171.325 4977.11 1183.22 1075.62 19311.6 0.85506 57.967 2043.74 11333.3 702.896 663.47 2.53042 2.38849 34.6476 24353.7 22987.7 87.6731 82.7556 0.03686 0.0461.60714 194.91745 0.10214 5.03294 0.05187 0.14 0.11078 1467.57 0.38222 80.1331 63.7423 12.3336 9.81083 965.992 3.47757 830.603 768.402 2.76625 660.707 6647.95 0.38221833 168.429 4892.98 806.725 664.11 19311.6 0.85506 57.967 2043.74 11333.3 550.323 480.005 1.98116 1.72802 16.9735 9340.89 8147.35 33.6272 29.3305 0.04205 0.052721.71428 203.27017 0.09429 5.50103 0.05619 0.14 0.11028 1604.06 0.38222 87.4368 69.2172 13.4577 10.6535 1141.87 4.11074 981.833 903.935 3.25417 777.245 7266.24 0.38221833 180.848 5253.77 938.003 771.24 19311.6 0.85506 57.967 2043.74 11333.3 608.41 533.576 2.19028 1.92087 18.4819 11244.6 9861.51 40.4805 35.5014 0.04758 0.059921.82142 210.88057 0.08643 6.06511 0.0613 0.14 0.10965 1768.54 0.38222 96.2382 75.7238 14.8124 11.655 1371.07 4.93585 1178.91 1078.81 3.88371 927.608 8011.32 0.38221833 195.537 5680.5 1104.49 906.627 19311.6 0.85506 57.967 2043.74 11333.3 674.339 595.052 2.42762 2.14219 20.2846 13678.7 12070.4 49.2434 43.4535 0.05416 0.068571.92857 217.74865 0.07857 6.75808 0.06743 0.13682 0.10883 1970.6 0.38222 104.655 83.5757 16.1079 12.8635 1640.08 5.90428 1410.21 1309.74 4.71506 1126.17 8926.66 0.38221833 213.215 6194.05 1296.73 1081.13 19311.6 0.85506 57.967 2043.74 11333.3 741.451 665.562 2.66922 2.39602 22.477 16665.6 14959.9 59.9962 53.8555 0.06212 0.079172.03571 223.87441 0.07071 7.62984 0.07492 0.13199 0.10775 2224.8 0.38222 113.838 93.225 17.5212 14.3486 1982.2 7.13593 1704.39 1623.28 5.84382 1395.77 10078.2 0.38221833 234.948 6825.41 1536.1 1311.39 19311.6 0.85506 57.967 2043.74 11333.3 813.978 746.223 2.93032 2.6864 25.2008 20512.9 18805.4 73.8464 67.6995 0.07199 0.09248

Inner 2.14285 229.25786 0.06286 8.75981 0.08429 0.12594 0.10626 2554.29 0.38222 124.561 105.345 19.1716 16.214 2440.03 8.78411 2098.05 2063.61 7.42899 1774.38 11570.7 0.38221833 262.395 7622.76 1848.37 1623.97 19311.6 0.85506 57.967 2043.74 11333.3 894.014 838.006 3.21845 3.01682 28.6757 25636.5 24030.4 92.2912 86.5095 0.08458 0.10969Wall 2.24999 233.899 0.055 10.2827 0.09633 0.1182 0.10417 2998.34 0.38222 137.067 120.981 21.0965 18.6206 3068.58 11.0469 2638.51 2708.46 9.75044 2328.85 13582.2 0.38221833 298.293 8665.64 2266.13 2063.51 19311.6 0.85506 57.967 2043.74 11333.3 981.532 941.49 3.53351 3.38936 33.2622 32647.9 31316 117.532 112.738 0.10123 0.13285

INSIDE PLATE - Based on Dittus-Boelter Correlation: COOLED DP 0.10123 0.13285 bari) Single Plate Layer Plate Mass Flux = 247.296 kg/m2.sRadial Distance From Outside to Inside Of 'Cooled' Bed = 2.24999 Plate Equivelant 'Inner' Diameter = 0.018 m

Radial Bed Approx. Mass Dp/Gap AB (1) AB (2) Re Pr ke/kg (1) ke/kg (2) ke (1) ke (2) hbed (1) hbed (2) Re Pr Nu h(outerwall) h(overall) bedside Re Pr Nu h(inside plate) h (Plate Solid Wall) OVERALL U Specific OVERALL VOLUMETRIC UADistance Volume Plate Flux 1 2 1 2 1 2 A (m2/m3) 1 2 1 2 Carman Ergun(m) (m3) Spacing (m(kg/m2.s) (W/m.K) (W/m.K) W/m2.K MJ/hr.m2.K kcal/h.m2.K W/m2.K MJ/hr.m2.K kcal/h.m2.K W/m2.K W/m2.K W/m2.K W/m2.K w/m2.K w/m2.K w/m2.K MJ/hr.m2.K MJ/hr.m2.K w/m3.K w/m3.K MJ/hr.m3.K MJ/hr.m3.K bar bar

Outside 0 0 0.22 2.39483 0.02408 0.14 0.11308 698.314 0.38222 38.97 31.7844 5.99804 4.89206 218.111 0.7852 187.542 177.894 0.64042 152.961 3163.3 0.38221833 92.9778 2701.07 201.815 166.902 38623.3 0.85506 100.926 3558.36 11333.3 187.818 157.212 0.67614 0.56596 0 0 0 0 0 0 0Wall 0.10714 17.991286 0.21214 2.48783 0.02497 0.14 0.11303 725.431 0.38222 40.4211 32.9429 6.22137 5.07037 234.611 0.8446 201.729 191.207 0.68834 164.408 3286.14 0.38221833 95.8551 2784.66 216.381 178.921 38623.3 0.85506 100.926 3558.36 11333.3 200.371 167.833 0.72134 0.6042 7.92172 1587.28 1329.52 5.71422 4.78628 0.00135 0.00161

0.21429 35.297249 0.20429 2.58834 0.02593 0.14 0.11298 754.739 0.38222 41.9893 34.1934 6.46275 5.26284 253.087 0.91111 217.616 206.098 0.74195 177.212 3418.9 0.38221833 98.9409 2874.31 232.606 192.309 38623.3 0.85506 100.926 3558.36 11333.3 214.207 179.558 0.77115 0.64641 8.23543 1764.09 1478.74 6.35071 5.32345 0.0028 0.003340.32143 51.917887 0.19643 2.69731 0.02697 0.14 0.11291 786.514 0.38222 43.6896 35.5472 6.72445 5.47121 273.869 0.98593 235.485 222.828 0.80218 191.598 3562.84 0.38221833 102.26 2970.71 250.753 207.28 38623.3 0.85506 100.926 3558.36 11333.3 229.502 192.543 0.82621 0.69315 8.575 1967.98 1651.06 7.08473 5.9438 0.00436 0.005220.42857 67.853202 0.18857 2.81586 0.0281 0.14 0.11285 821.083 0.38222 45.5394 37.0176 7.00916 5.69752 297.359 1.07049 255.683 241.714 0.87017 207.837 3719.43 0.38221833 105.84 3074.72 271.137 224.097 38623.3 0.85506 100.926 3558.36 11333.3 246.461 206.97 0.88726 0.74509 8.94378 2204.3 1851.09 7.93546 6.66394 0.00605 0.007250.53571 83.103193 0.18071 2.94531 0.02932 0.14 0.11277 858.83 0.38222 47.5593 38.6202 7.32005 5.94419 324.05 1.16658 278.633 263.143 0.94731 226.262 3890.43 0.38221833 109.715 3187.29 294.145 243.075 38623.3 0.85506 100.926 3558.36 11333.3 265.326 223.054 0.95517 0.80299 9.34571 2479.66 2084.59 8.92677 7.50454 0.00788 0.009460.64286 97.66786 0.17286 3.08724 0.03065 0.14 0.11268 900.215 0.38222 49.7738 40.3736 7.66089 6.21406 354.555 1.2764 304.862 287.594 1.03534 247.286 4077.9 0.38221833 113.924 3309.58 320.247 264.601 38623.3 0.85506 100.926 3558.36 11333.3 286.381 241.048 1.03097 0.86777 9.78546 2802.37 2358.77 10.0885 8.49157 0.00986 0.01189

0.75 111.5472 0.165 3.24354 0.03211 0.14 0.11258 945.79 0.38222 52.2126 42.2999 8.03625 6.51055 389.638 1.4027 335.028 315.664 1.13639 271.422 4284.35 0.38221833 118.515 3442.96 350.025 289.153 38623.3 0.85506 100.926 3558.36 11333.3 309.962 261.258 1.11586 0.94053 10.2686 3182.89 2682.76 11.4584 9.65794 0.01203 0.014550.85714 124.74122 0.15714 3.41651 0.03372 0.14 0.11246 996.226 0.38222 54.9115 44.4258 8.45165 6.83776 430.267 1.54896 369.963 348.105 1.25318 299.317 4512.82 0.38221833 123.545 3589.07 384.207 317.328 38623.3 0.85506 100.926 3558.36 11333.3 336.471 284.044 1.21129 1.02256 10.802 3634.56 3068.25 13.0844 11.0457 0.01441 0.017480.96428 137.24992 0.14929 3.60896 0.03549 0.14 0.11233 1052.34 0.38222 57.9144 46.7838 8.91384 7.20069 477.681 1.71965 410.731 385.875 1.38915 331.793 4767.03 0.38221833 129.082 3749.92 423.707 349.873 38623.3 0.85506 100.926 3558.36 11333.3 366.383 309.843 1.31898 1.11543 11.3938 4174.51 3530.29 15.0282 12.7091 0.01703 0.020741.07143 149.07329 0.14143 3.82439 0.03746 0.14 0.11217 1115.16 0.38222 61.2758 49.4137 9.43121 7.60546 533.484 1.92054 458.714 430.209 1.54875 369.913 5051.59 0.38221833 135.21 3927.95 469.692 387.742 38623.3 0.85506 100.926 3558.36 11333.3 400.269 339.178 1.44097 1.22104 12.0543 4824.95 4088.54 17.3698 14.7188 0.01994 0.024371.17857 160.21134 0.13357 4.06718 0.03967 0.14 0.11198 1185.96 0.38222 65.064 52.3647 10.0143 8.05966 599.787 2.15923 515.724 482.719 1.73779 415.064 5372.28 0.38221833 142.034 4126.2 523.666 432.161 38623.3 0.85506 100.926 3558.36 11333.3 438.813 372.687 1.57973 1.34167 12.796 5615.03 4768.89 20.2141 17.168 0.02318 0.028461.28571 170.66406 0.12571 4.34288 0.04214 0.14 0.11176 1266.35 0.38222 69.3658 55.6988 10.6764 8.57283 679.408 2.44587 584.185 545.545 1.96396 469.084 5736.45 0.38221833 149.686 4348.49 587.601 484.732 38623.3 0.85506 100.926 3558.36 11333.3 482.835 411.141 1.73821 1.48011 13.6349 6583.42 5605.87 23.7003 20.1811 0.02683 0.033091.39285 180.43146 0.11786 4.65867 0.04495 0.14 0.1115 1358.43 0.38222 74.2933 59.4947 11.4348 9.15708 776.181 2.79425 667.395 621.573 2.23766 534.456 6153.58 0.38221833 158.332 4599.66 664.113 547.576 38623.3 0.85506 100.926 3558.36 11333.3 533.325 455.479 1.91997 1.63972 14.5916 7782.06 6646.16 28.0154 23.9262 0.03097 0.03838

1.5 189.51354 0.11 5.02399 0.04816 0.14 0.11118 1464.96 0.38222 79.9935 63.854 12.3121 9.82803 895.429 3.22354 769.93 714.768 2.57316 614.589 6636.13 0.38221833 168.189 4886.02 756.745 623.55 38623.3 0.85506 100.926 3558.36 11333.3 591.467 506.846 2.12928 1.82465 15.6927 9281.69 7953.77 33.4141 28.6336 0.0357 0.044481.60714 197.91029 0.10214 5.45148 0.05187 0.14 0.11078 1589.61 0.38222 86.6637 68.9098 13.3388 10.6062 1044.72 3.76098 898.295 830.696 2.99051 714.27 7200.8 0.38221833 179.544 5215.88 870.383 716.573 38623.3 0.85506 100.926 3558.36 11333.3 658.682 566.638 2.37126 2.0399 16.9735 11180.1 9617.81 40.2484 34.6241 0.04118 0.05161.71428 205.62172 0.09429 5.95849 0.05619 0.14 0.11028 1737.45 0.38222 94.5747 74.84 14.5564 11.5189 1235.09 4.44632 1061.99 977.366 3.51852 840.384 7870.5 0.38221833 192.783 5600.48 1011.93 832.145 38623.3 0.85506 100.926 3558.36 11333.3 736.66 636.546 2.65198 2.29157 18.4819 13614.9 11764.6 49.0136 42.3525 0.04759 0.060021.82142 212.64782 0.08643 6.56948 0.0613 0.14 0.10965 1915.61 0.38222 104.108 81.8877 16.0237 12.6037 1483.19 5.33948 1275.31 1166.62 4.19984 1003.12 8677.54 0.38221833 208.441 6055.37 1191.38 978.17 38623.3 0.85506 100.926 3558.36 11333.3 827.384 718.607 2.97858 2.58698 20.2846 16783.2 14576.7 60.4194 52.4761 0.05522 0.070151.92857 218.9886 0.07857 7.32009 0.06743 0.13682 0.10883 2134.48 0.38222 113.225 90.3926 17.4269 13.9127 1774.38 6.38776 1525.69 1416.57 5.09964 1218.03 9669.01 0.38221833 227.286 6602.82 1398.55 1166.34 38623.3 0.85506 100.926 3558.36 11333.3 922.261 815.231 3.32014 2.93483 22.477 20729.7 18324 74.6269 65.9664 0.06446 0.082562.03571 224.64406 0.07071 8.26434 0.07492 0.13199 0.10775 2409.82 0.38222 123.171 100.844 18.9578 15.5214 2144.72 7.721 1844.13 1755.95 6.32143 1509.85 10916.3 0.38221833 250.453 7275.83 1656.45 1414.56 38623.3 0.85506 100.926 3558.36 11333.3 1027.79 929.199 3.70003 3.34512 25.2008 25901 23416.5 93.2436 84.2996 0.07592 0.09814

Inner 2.14285 229.61419 0.06286 9.48828 0.08429 0.12594 0.10626 2766.71 0.38222 134.786 113.972 20.7454 17.5419 2640.33 9.5052 2270.28 2232.61 8.03738 1919.7 12532.9 0.38221833 279.711 8125.8 1992.81 1751.4 38623.3 0.85506 100.926 3558.36 11333.3 1148.02 1063.56 4.13285 3.82883 28.6757 32920.1 30498.4 118.512 109.794 0.09053 0.11829Wall 2.24999 233.899 0.055 11.1378 0.09633 0.1182 0.10417 3247.69 0.38222 148.332 130.908 22.8304 20.1486 3320.78 11.9548 2855.36 2930.71 10.5505 2519.96 14711.7 0.38221833 317.979 9237.51 2442.67 2224.85 38623.3 0.85506 100.926 3558.36 11333.3 1284.27 1221.4 4.62338 4.39704 33.2622 42717.6 40626.4 153.783 146.255 0.10987 0.14543

COOLED DP 0.10987 0.14543 bar



COOLED BED

COOLED BED

Do

Di

Dduct

FEED GAS


PLATES


0

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30000

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50000

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(W/m

3 .K)


RADIAL FLOW ACME VOLUMETRIC UA PROFILE WCC - Outside-to-Inside Flow



Single Plate Layer

0

50

100

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RADIAL FLOW ACME VOLUMETRIC UA PROFILE WCC - Outside-to-Inside Flow



Single Plate Layer


RADIAL FLOW ACME REACTOR SET-UP - Water-Cooled

- ADIABATIC BED LOCATED FROM INSIDE WALL OUTWARDS


ENTER CENTRAL DUCT OUTER DIAMETER (Doduct) = 1.5 m

ENTER CENTRAL DUCT INNER DIAMETER (Diduct) = 1.39 m



ENTER MOLAR FLOW OF REACTOR FEED GAS = 153219 9 kmol/h

ENTER MASS FLOW OF REACTOR FEED GAS = 409 7973 kg/s

ENTER REACTOR FEED TEMPERATURE = 245 DEG C AND PRESSURE = 86 2 bar(a)

APPROXIMATE (IDEALITY) VOLUMETRIC FEED FLOW AT 245 DEG C AND 86 2 bar(a) = 76550 43 m3/h

X-SECTIONAL AREA OF INNER DUCT = 1 517468 m2

AVERAGE AXIAL (VERTICAL) VELOCITY OF GAS THROUGH CENTRAL DUCT = 14 01282 m/s

INTERNALS

ENTER TOTAL CATALYST ACTIVE BULK VOLUME = 233 9 m3

ENTER VOLUME OF ADIABATIC BED = 0 001 m3 (If no adiabatic bed present set as very small value > 0 e g 0 001 m3)

Active Volume of Cooled Bed = 233 899 m3

ENTER AVERAGE EMBOSSED PLATE WIDTH = 0 012 m ENTER PLATE MATERIAL THICKNESS = 0 0015 m

ENTER CATALYST PELLET LENGTH = 5 2 mm

ENTER CATALYST PELLET DIAMETER = 5 4 mm

ENTER VOIDAGE OF CATALYST BED = 0 36

ENTER THERMAL CONDUCTIVITY OF CATALYST PELLET = 0 32 W/m K

ENTER THERMAL CONDUCTIVITY OF PLATE = 17 W/m K


Guess Diameter of Adiabatic Bed = 1 500045 m (If no adiabatic bed present this value should equal a fraction greater than the outer diameter of central duct due to calculation method employed)

TO ESTIMATE THE NUMBER OF PLATES INSTALLED ASSUMING ONE SINGLE PLATE BANK



Using Sine Rule: PRESS TO COMPUTE --------> (N B Requires 'Good' Initial Guess Values for Iterated Cells)

LHS = 1 333251 RHS = 1 333251 Difference = 0 (Should be 0)





Cooled A/V = 12 795855 m2/m3Cat




Guess Diameter of Adiabatic Bed = 1 500041 m

Breadth of Each Plate Bank = 0 749993 m

First Plate Layer (Counting from Adiabtic Bed/Central Duct Outwards)



Using Sine Rule:



( should equal minimum plate spacing)NUMBER OF PLATES IN FIRST PLATE LAYER = 70

Second Plate Layer



Using Sine Rule:




Third Plate Layer



Using Sine Rule:



( should equal minimum plate spacing)NUMBER OF PLATES IN THIRD PLATE LAYER = 210




Overall Cooled A/V = 27 71993 m2/m3Cat

Area Basis Vol BasisCatalyst Particle Equivelant/Effective Diameter = 0 005298 m 0 007566 m 0 007691 m Dp (Volume)/Dp (Area) = 1 016532



Phi1 coeff -1 00234 Phi2 coeff -1 13595-0 49574 -0 728850 046918 0 05113-0 00194 -0 00131

ks/kg 2 079082

Phi1 0 261634 0 2826695Phi2 0 193489 0 2025676

phi 0 225037 0 2396518

Gamma 1Beta 1Alpha 0 131985 0 1041671Emmis 0 6Hrv 24 98884Hrs 12 71754ke0/kg 1 60283

Equivelant 'Outer' Diameter of Plate = 0 024 m

HTC PROFILES FOR WATER-COOLED PART OF BED (In - Out) INSIDE PLATE - Based on Dittus-Boelter Correlation:

i) 3 Plate Layers Plate Mass Flux = 123 649 kg/m2 sPlate Equivelant 'Inner' Diameter = 0 018 m



Inner 0 0 0 055 10 28233 0 096329 0 118204 0 104167 2998 247 0 382218 137 0624 120 9768 21 09583 18 62003 3068 484 11 04654 2638 422 2708 367 9 750123 2328 777 13581 8 0 38221833 298 2857 8665 419 2266 058 2063 441 19311 77 0 615703 50 83164 1792 168 11333 33 919 5287 884 2938 3 310303 3 183458 0 0 0 0 0 0 0Wall 0 107142 4 6412382 0 062857 8 759583 0 084289 0 125943 0 106261 2554 225 0 382218 124 5573 105 3419 19 17112 16 21361 2439 972 8 783898 2097 998 2063 559 7 428814 1774 342 11570 42 0 38221833 262 3891 7622 597 1848 327 1623 934 19311 77 0 615703 50 83164 1792 168 11333 33 842 2838 792 3886 3 032222 2 852599 99 78345 84045 99 79067 27 302 5655 284 6422 0 016655 0 02316

0 214284 10 024781 0 070714 7 629674 0 074923 0 131985 0 107745 2224 753 0 382218 113 835 93 22289 17 52081 14 34831 1982 169 7 135807 1704 358 1623 257 5 843725 1395 75 10077 94 0 38221833 234 9438 6825 288 1536 07 1311 373 19311 77 0 615703 50 83164 1792 168 11333 33 770 873 709 8351 2 775143 2 555406 86 02491 66314 28 61063 49 238 7314 219 8286 0 029238 0 040370 321426 16 150629 0 078571 6 757958 0 067431 0 136819 0 108833 1970 567 0 382218 104 6527 83 57415 16 10753 12 86324 1640 057 5 904207 1410 196 1309 726 4 715013 1126 162 8926 5 0 38221833 213 2119 6193 963 1296 71 1081 121 19311 77 0 615703 50 83164 1792 168 11333 33 705 5167 636 4624 2 53986 2 291265 75 60077 53337 6 48117 05 192 0154 173 2214 0 039107 0 0536750 428568 23 018781 0 086427 6 065009 0 061301 0 14 0 109652 1768 509 0 382218 96 23673 75 72254 14 81219 11 65476 1371 064 4 935829 1178 903 1078 802 3 883689 927 6031 8011 193 0 38221833 195 5349 5680 432 1104 48 906 621 19311 77 0 615703 50 83164 1792 168 11333 33 644 4868 571 6849 2 320152 2 058066 67 42989 43457 67 38548 65 156 4476 138 7752 0 047073 0 0642760 535709 30 629238 0 094284 5 500952 0 056193 0 14 0 110283 1604 034 0 382218 87 4356 69 21624 13 45757 10 65335 1141 872 4 110738 981 833 903 9346 3 254165 777 2439 7266 137 0 38221833 180 8462 5253 715 938 0013 771 2383 19311 77 0 615703 50 83164 1792 168 11333 33 584 0046 514 7118 2 102417 1 852963 60 85295 35538 41 31321 73 127 9383 112 7582 0 05365 0 0729270 642851 38 982 0 102141 5 032884 0 051871 0 14 0 110779 1467 549 0 382218 80 13222 63 74148 12 33348 9 810711 965 9949 3 477581 830 6061 768 4043 2 766256 660 7088 6647 873 0 38221833 168 4274 4892 939 806 7259 664 1101 19311 77 0 615703 50 83164 1792 168 11333 33 530 2798 464 6855 1 909007 1 672868 55 44499 29401 36 25764 48 105 8449 92 75214 0 059181 0 0801250 749993 48 077066 0 055 5 141282 0 096329 0 118204 0 104167 1499 157 0 382218 69 33412 61 29113 10 6715 9 433567 1552 218 5 587984 1334 667 1372 155 4 939759 1179 841 6791 053 0 38221833 171 3232 4977 065 1183 206 1075 613 19311 77 0 615703 50 83164 1792 168 11333 33 670 52 634 5497 2 413872 2 284379 33 94652 22761 82 21540 75 81 94256 77 54671 0 064368 0 0868480 857135 56 9882 0 058928 4 730133 0 089907 0 122318 0 105308 1379 269 0 382218 66 08655 57 11932 10 17165 8 791468 1380 88 4 971169 1187 343 1193 51 4 296635 1026 234 6247 973 0 38221833 160 2721 4656 021 1065 018 949 9918 19311 77 0 615703 50 83164 1792 168 11333 33 630 8472 588 6303 2 27105 2 119069 34 6472 21857 09 20394 39 78 68552 73 41982 0 069272 0 0931840 964277 66 641638 0 062857 4 379875 0 084288 0 125943 0 106261 1277 137 0 382218 63 08128 53 47339 9 709097 8 230307 1235 706 4 448542 1062 516 1047 496 3 770985 900 6844 5785 32 0 38221833 150 7053 4378 099 963 7035 845 2605 19311 77 0 615703 50 83164 1792 168 11333 33 593 8658 546 6614 2 137917 1 967981 31 98299 18993 61 17483 87 68 37698 62 94193 0 073501 0 0985971 071419 77 037381 0 066785 4 077912 0 07933 0 129142 0 107063 1189 087 0 382218 60 29656 50 26203 9 280489 7 736034 1111 677 4 002038 955 8703 926 6723 3 33602 796 7947 5386 462 0 38221833 142 3342 4134 914 876 1288 757 0177 19311 77 0 615703 50 83164 1792 168 11333 33 559 4082 508 3389 2 01387 1 83002 29 69926 16614 01 15097 29 59 81043 54 35023 0 077189 0 1032771 178561 88 175428 0 070714 3 8149 0 074923 0 131985 0 107745 1112 395 0 382218 57 71994 47 41364 8 88391 7 297626 1005 053 3 618189 864 1896 825 5934 2 972136 709 8825 5039 053 0 38221833 134 9415 3920 151 799 9583 681 969 19311 77 0 615703 50 83164 1792 168 11333 33 527 3473 473 3591 1 89845 1 704093 27 71993 14618 03 13121 48 52 6249 47 23733 0 080436 0 1073651 285703 100 05578 0 074642 3 58376 0 07098 0 134529 0 108329 1044 996 0 382218 55 336 44 87127 8 516989 6 906319 912 83 3 286188 784 8925 740 2023 2 664728 636 4595 4733 742 0 38221833 128 3602 3728 957 733 3175 617 6067 19311 77 0 615703 50 83164 1792 168 11333 33 497 5411 441 4286 1 791148 1 589143 25 98794 12930 07 11471 82 46 54824 41 29855 0 08332 0 1109681 392844 112 67844 0 078571 3 379028 0 067431 0 136819 0 108833 985 2979 0 382218 53 12863 42 58911 8 177244 6 555063 832 5967 2 997348 715 9043 667 4283 2 402742 573 885 4463 315 0 38221833 122 4595 3557 539 674 6933 561 993 19311 77 0 615703 50 83164 1792 168 11333 33 469 8423 412 2691 1 691432 1 484169 24 45966 11492 18 10083 96 41 37186 36 30226 0 0859 0 1141691 499986 126 0434 0 055 3 427547 0 096329 0 118204 0 104167 999 4455 0 382218 46 75736 41 39533 7 196615 6 371323 1046 78 3 768409 900 0691 926 7379 3 336256 796 8511 4527 403 0 38221833 123 8642 3598 346 810 8882 736 9418 19311 77 0 615703 50 83164 1792 168 11333 33 532 075 499 2068 1 91547 1 797145 11 55057 6145 77 5766 123 22 12477 20 75804 0 088375 0 1172311 607128 139 22443 0 057619 3 239807 0 091951 0 120999 0 104951 944 702 0 382218 45 29362 39 49874 6 971326 6 079412 967 9202 3 484513 832 2615 844 0842 3 038703 725 7817 4279 419 0 38221833 118 4062 3439 787 755 3676 677 7677 19311 77 0 615703 50 83164 1792 168 11333 33 507 5943 471 3312 1 827339 1 696792 11 71175 5944 818 5520 114 21 40134 19 87241 0 090758 0 1201721 71427 153 14776 0 060238 3 071566 0 087953 0 123579 0 105644 895 6442 0 382218 43 90774 37 76823 6 758019 5 813062 897 5086 3 231031 771 7185 772 0122 2 779244 663 811 4057 192 0 38221833 113 4611 3296 128 705 4267 625 5072 19311 77 0 615703 50 83164 1792 168 11333 33 484 543 445 4499 1 744355 1 60362 11 08735 5372 3 4938 861 19 34028 17 7799 0 092914 0 122816

1 821412 167 8134 0 062857 2 919935 0 084288 0 125943 0 106261 851 4299 0 382218 42 58874 36 18342 6 555006 5 569138 834 2748 3 003389 717 3472 708 8005 2 551682 609 4587 3856 905 0 38221833 108 9576 3165 299 660 2526 579 1192 19311 77 0 615703 50 83164 1792 168 11333 33 462 7936 421 4113 1 666057 1 517081 10 52616 4871 442 4435 844 17 53719 15 96904 0 094875 0 1252061 928554 183 22134 0 065476 2 782571 0 080917 0 128118 0 10681 811 3756 0 382218 41 33518 34 72712 6 362066 5 344992 777 3303 2 798389 668 3838 653 0622 2 351024 561 5324 3675 462 0 38221833 104 8374 3045 602 619 273 537 7529 19311 77 0 615703 50 83164 1792 168 11333 33 442 2792 399 0728 1 592205 1 436662 10 01905 4431 217 3998 329 15 95238 14 39399 0 096667 0 1273772 035696 199 37159 0 068095 2 65755 0 077805 0 130126 0 107303 774 9206 0 382218 40 14471 33 38467 6 178836 5 138371 725 9069 2 613265 624 1676 603 6702 2 173213 519 0629 3510 324 0 38221833 101 0519 2935 63 581 9944 500 707 19311 77 0 615703 50 83164 1792 168 11333 33 422 9317 378 3014 1 522554 1 361885 9 558548 4042 613 3616 013 14 55341 13 01765 0 098312 0 1293592 142838 216 26414 0 070714 2 543281 0 074923 0 131985 0 107745 741 6006 0 382218 39 01446 32 14354 6 004874 4 947343 679 3412 2 445628 584 1283 559 701 2 014923 481 2562 3359 387 0 38221833 97 56063 2834 208 547 9912 467 3988 19311 77 0 615703 50 83164 1792 168 11333 33 404 6838 358 9737 1 456862 1 292305 9 13852 3698 211 3280 488 13 31356 11 80976 0 099828 0 131175

Outside 2 249979 233 899 0 073333 2 438433 0 072247 0 133711 0 108144 711 0278 0 382218 37 94131 30 99293 5 839701 4 770248 637 0603 2 293417 547 7732 520 3923 1 873412 447 4569 3220 895 0 38221833 94 32956 2740 343 516 8952 437 3411 19311 77 0 615703 50 83164 1792 168 11333 33 387 4698 340 9753 1 394891 1 227511 8 753852 3391 853 2984 847 12 21067 10 74545 0 10123 0 132847Wall

COOLED DP 0 10123 0 132847 bar

ii) Single Plate Layer Plate Mass Flux = 247 2982 kg/m2 sPlate Equivelant 'Inner' Diameter = 0 018 m



Inner 0 0 0 055 11 13738 0 096329 0 118204 0 104167 3247 571 0 382218 148 3267 130 9035 22 82957 20 14789 3320 665 11 95439 2855 258 2930 602 10 55017 2519 864 14711 22 0 38221833 317 9695 9237 247 2442 588 2224 772 38623 57 0 855056 100 9271 3558 381 11333 33 1284 251 1221 38 4 623304 4 396967 0 0 0 0 0 0 0Wall 0 107142 4 2849149 0 062857 9 488004 0 084289 0 125943 0 10626 2766 627 0 382218 134 7818 113 9686 20 74481 17 54137 2640 262 9 504943 2270 217 2232 549 8 037175 1919 646 12532 58 0 38221833 279 7042 8125 612 1992 755 1751 356 38623 57 0 855056 100 9271 3558 381 11333 33 1148 1063 549 4 132801 3 828776 33 26107 38183 71 35374 77 137 4614 127 3492 0 019341 0 027131

0 214284 9 2551431 0 070714 8 264139 0 074923 0 131985 0 107745 2409 757 0 382218 123 1679 100 8418 18 95728 15 52097 2144 681 7 72085 1844 093 1755 923 6 321323 1509 822 10915 99 0 38221833 250 4478 7275 692 1656 414 1414 537 38623 57 0 855056 100 9271 3558 381 11333 33 1027 775 929 1892 3 699989 3 345081 28 67491 29471 35 26644 42 106 0969 95 9199 0 033949 0 0472880 321425 14 910685 0 07857 7 319935 0 067431 0 136818 0 108833 2134 435 0 382218 113 2221 90 3907 17 42648 13 9124 1774 353 6 387672 1525 669 1416 552 5 099588 1218 016 9668 808 0 38221833 227 2819 6602 706 1398 526 1166 327 38623 57 0 855056 100 9271 3558 381 11333 33 922 2534 815 2255 3 320112 2 934812 25 20021 23240 98 20543 86 83 66753 73 95788 0 045403 0 0628670 428567 21 251539 0 086427 6 569364 0 061301 0 14 0 109652 1915 574 0 382218 104 1063 81 88618 16 02342 12 60344 1483 181 5 339453 1275 306 1166 616 4 199817 1003 109 8677 388 0 38221833 208 4384 6055 289 1191 368 978 1624 38623 57 0 855056 100 9271 3558 381 11333 33 827 3808 718 604 2 978571 2 586974 22 4766 18596 71 16151 77 66 94814 58 14638 0 054645 0 0752770 535709 28 277707 0 094284 5 958402 0 056193 0 14 0 110283 1737 423 0 382218 94 5733 74 83885 14 55616 11 51875 1235 089 4 446319 1061 985 977 3648 3 518513 840 3824 7870 376 0 38221833 192 7804 5600 413 1011 924 832 1422 38623 57 0 855056 100 9271 3558 381 11333 33 736 6598 636 5454 2 651975 2 291564 20 28429 14942 62 12911 87 53 79344 46 48275 0 062274 0 0854020 642851 35 989189 0 102141 5 451411 0 051871 0 14 0 110779 1589 588 0 382218 86 6626 68 90883 13 33859 10 60604 1044 72 3 760993 898 2976 830 6979 2 990513 714 2716 7200 699 0 38221833 179 5421 5215 829 870 384 716 5731 38623 57 0 855056 100 9271 3558 381 11333 33 658 6833 566 6387 2 37126 2 039899 18 48164 12173 55 10472 41 43 82478 37 70069 0 068687 0 0938250 749993 44 385983 0 109998 5 023933 0 048166 0 14 0 111176 1464 939 0 382218 79 99255 63 85323 12 31198 9 82791 895 4344 3 223564 769 935 714 7713 2 573177 614 5927 6636 049 0 38221833 168 1877 4885 975 756 748 623 5516 38623 57 0 855056 100 9271 3558 381 11333 33 591 4689 506 8479 2 129288 1 824653 16 97324 10039 15 8602 854 36 14093 30 97027 0 074161 0 1009450 857134 53 468091 0 117855 4 658622 0 044955 0 14 0 111498 1358 417 0 382218 74 29251 59 4941 11 43466 9 156979 776 1875 2 794275 667 4011 621 5778 2 23768 534 4607 6153 514 0 38221833 158 3307 4599 623 664 1175 547 5797 38623 57 0 855056 100 9271 3558 381 11333 33 533 3277 455 4812 1 91998 1 639732 15 69249 8369 238 7147 632 30 12926 25 73148 0 078894 0 1070450 964276 63 235512 0 125711 4 342837 0 042145 0 14 0 111764 1266 337 0 382218 69 36523 55 69829 10 67628 8 572751 679 4151 2 445894 584 1918 545 5509 1 963983 469 0893 5736 397 0 38221833 149 6849 4348 455 587 6059 484 7365 38623 57 0 855056 100 9271 3558 381 11333 33 482 8392 411 1439 1 738221 1 480118 14 59145 7045 324 5999 186 25 36317 21 59707 0 08303 0 1123331 071418 73 688246 0 133568 4 067145 0 039666 0 14 0 111984 1185 947 0 382218 65 06353 52 36426 10 01419 8 059597 599 7946 2 15926 515 7305 482 7251 1 73781 415 0689 5372 239 0 38221833 142 0335 4126 177 523 6719 432 1657 38623 57 0 855056 100 9271 3558 381 11333 33 438 8169 372 6908 1 579741 1 341687 13 63479 5983 177 5081 561 21 53944 18 29362 0 08668 0 1169611 17856 84 826294 0 141425 3 824366 0 037462 0 14 0 11217 1115 155 0 382218 61 2754 49 41332 9 431146 7 605405 533 4919 1 920571 458 7205 430 2151 1 548774 369 9184 5051 556 0 38221833 135 2093 3927 93 469 6975 387 7464 38623 57 0 855056 100 9271 3558 381 11333 33 400 2735 339 1823 1 440985 1 221056 12 79586 5121 842 4340 127 18 43863 15 62446 0 089926 0 121047

1 285702 96 649655 0 149282 3 608939 0 035491 0 14 0 112328 1052 338 0 382218 57 91404 46 78354 8 913785 7 200645 477 6885 1 719679 410 7382 385 8815 1 389174 331 7984 4767 002 0 38221833 129 0811 3749 901 423 713 349 8776 38623 57 0 855056 100 9271 3558 381 11333 33 366 3876 309 8465 1 318995 1 115447 12 05417 4416 5 3734 944 15 8994 13 4458 0 092834 0 1246831 392843 109 15833 0 157139 3 416488 0 033716 0 14 0 112462 996 2208 0 382218 54 91117 44 42559 8 451602 6 837724 430 2745 1 548988 369 9694 348 1113 1 253201 299 3218 4512 795 0 38221833 123 5444 3589 055 384 213 317 3324 38623 57 0 855056 100 9271 3558 381 11333 33 336 4755 284 048 1 211312 1 022573 11 39376 3833 721 3236 375 13 8014 11 65095 0 095457 0 127941 499985 122 35232 0 164996 3 243523 0 032111 0 14 0 112579 945 7856 0 382218 52 21235 42 29969 8 036216 6 510517 389 645 1 402722 335 0344 315 6698 1 136411 271 4272 4284 328 0 38221833 118 5148 3442 943 350 0313 289 158 38623 57 0 855056 100 9271 3558 381 11333 33 309 967 261 2618 1 115881 0 940542 10 80195 3348 249 2822 138 12 0537 10 1597 0 097836 0 1308751 607127 136 23162 0 172852 3 087227 0 030651 0 14 0 11268 900 2111 0 382218 49 77363 40 3734 7 660862 6 214034 354 5619 1 276423 304 8684 287 5995 1 035358 247 291 4077 879 0 38221833 113 9237 3309 566 320 2525 264 6054 38623 57 0 855056 100 9271 3558 381 11333 33 286 3854 241 0525 1 030987 0 867789 10 26859 2940 774 2475 269 10 58679 8 910968 0 100004 0 1335351 714269 150 79623 0 180709 2 945302 0 029318 0 14 0 112768 858 8268 0 382218 47 55914 38 62004 7 32002 5 944167 324 0573 1 166606 278 6391 263 1483 0 947334 226 2668 3890 412 0 38221833 109 7142 3187 279 294 1504 243 0792 38623 57 0 855056 100 9271 3558 381 11333 33 265 3306 223 0575 0 95519 0 803007 9 785419 2596 371 2182 711 9 346935 7 857761 0 101989 0 1359561 82141 166 04616 0 188566 2 815853 0 028097 0 14 0 112846 821 0803 0 382218 45 5393 37 01745 7 009139 5 697506 297 3658 1 070517 255 6885 241 7192 0 870189 207 8411 3719 424 0 38221833 105 8393 3074 71 271 1426 224 1014 38623 57 0 855056 100 9271 3558 381 11333 33 246 4658 206 9738 0 887277 0 745106 9 345674 2303 389 1934 31 8 292201 6 963516 0 103815 0 138171

1 928552 181 9814 0 196423 2 697303 0 026973 0 14 0 112914 786 5121 0 382218 43 68954 35 54708 6 724435 5 471195 273 8757 0 985953 235 4907 222 8332 0 8022 191 6021 3562 833 0 38221833 102 2593 2970 708 250 7578 207 2848 38623 57 0 855056 100 9271 3558 381 11333 33 229 5066 192 5468 0 826224 0 693168 8 943753 2052 65 1722 091 7 38954 6 199527 0 1055 0 1402052 035694 198 60195 0 20428 2 588332 0 025936 0 14 0 112975 754 7371 0 382218 41 98924 34 1933 6 462734 5 262829 253 0934 0 911136 217 6212 206 1028 0 74197 177 2165 3418 894 0 38221833 98 94072 2874 3 232 6111 192 3129 38623 57 0 855056 100 9271 3558 381 11333 33 214 2115 179 5616 0 771162 0 646422 8 574976 1836 859 1539 736 6 612691 5 54305 0 107061 0 1420792 142836 215 90782 0 212137 2 487824 0 024975 0 14 0 11303 725 4297 0 382218 40 42098 32 94283 6 221358 5 070364 234 617 0 844621 201 7343 191 2113 0 688361 164 4121 3286 135 0 38221833 95 85501 2784 658 216 3858 178 9252 38623 57 0 855056 100 9271 3558 381 11333 33 200 3752 167 8362 0 721351 0 60421 8 235406 1650 171 1382 2 5 940616 4 975918 0 108512 0 143813

Outside 2 249978 233 899 0 219993 2 39483 0 024083 0 14 0 113078 698 3134 0 382218 38 96997 31 78433 5 998027 4 892055 218 1166 0 78522 187 5465 177 8982 0 640434 152 9649 3163 3 0 38221833 92 97771 2701 07 201 8193 166 9055 38623 57 0 855056 100 9271 3558 381 11333 33 187 822 157 216 0 676159 0 565977 7 921706 1487 871 1245 419 5 356335 4 483507 0 109864 0 145421Wall

COOLED DP 0 109864 0 145421 bar

PRESSURE DROP


ESTIMATED CATALYST

COOLED BED

COOLED BED

Do

Di

Doduct

FEED GAS


PLATES


0

10000

20000

30000

40000

50000

60000

70000

80000

90000

0 50 100 150 200 250

UA

(W/m

3 .K)


RADIAL FLOW ACME VOLUMETRIC UA PROFILE WCC - Inside-to-Outside Flow



Single Plate Layer

Diduct

100

150

200

250

300

350

UA

(MJ/

h.m

3 .K)

RADIAL FLOW ACME VOLUMETRIC UA PROFILE WCC - Inside-to-Outside Flow



Single Plate Layer

Comparison of Inferred Optimised Volumetric UA Data and Calculated/Achievable UA Data for Synthesis Reactor of a 9000 MTD ACME Plant

1) Gas-Cooled Radial Flow Reactor 2) Water-Cooled Radial Flow Reactor

Bed Volume Bed Volumem3 MJ/.h.m3.K W/m3.K m3 MJ/.h.m3.KW/m3.K0.0 0 0 0.0 0 01.4 42.2242894 11728.97 2.4 208.0493 57791.482.8 42.5323571 11814.54 4.9 95.15878 264334.1 44.2033451 12278.71 7.3 97.40006 27055.575.5 45.9151221 12754.2 9.8 96.23805 26732.796.9 47.69817 13249.49 12.2 95.00339 26389.838.3 49.5647534 13767.99 14.6 90.61293 25170.269.6 51.5285954 14313.5 17.1 92.13977 25594.3811.0 53.6051786 14890.33 19.5 91.46978 25408.2712.4 55.8119237 15503.31 21.9 84.99695 23610.2613.8 58.1687482 16157.99 24.4 85.86149 23850.4115.1 60.6986383 16860.73 26.8 88.14006 24483.3516.5 63.4281254 17618.92 29.3 81.9854 22773.7217.9 66.3886698 18441.3 31.7 82.76599 22990.5519.3 69.6202981 19338.97 34.1 85.05944 23627.6220.7 73.1492426 20319.23 36.6 79.06358 21962.1122.0 77.0665748 21407.38 39.0 79.88681 22190.7823.4 81.407458 22613.18 41.4 77.18325 21439.7924.8 86.2626629 23961.85 43.9 78.04207 21678.3526.2 91.7538764 25487.19 46.3 75.40037 20944.5527.5 97.9394138 27205.39 48.8 76.28106 21189.1828.9 105.649126 29346.98 51.2 73.6978 20471.6130.3 114.227434 31729.84 53.6 74.59857 20721.8231.7 124.151256 34486.46 56.1 72.07048 20019.5833.0 135.971899 37769.97 58.5 68.17016 18936.1534.4 67.0839026 18634.42 60.9 255.7289 71035.8135.8 67.9020654 18861.68 63.4 67.45178 18736.6137.2 69.6666568 19351.85 65.8 64.90638 18029.5538.5 71.5314779 19869.85 68.3 62.73359 1742639.9 73.5071062 20418.64 70.7 62.01384 17226.0741.3 75.6046024 21001.28 73.1 58.95916 16377.5542.7 77.8360288 21621.12 75.6 60.43731 16788.1444.1 80.2159041 22282.2 78.0 56.55738 15710.3845.4 82.7601863 22988.94 80.4 55.30885 15363.5746.8 85.4872551 23746.46 82.9 56.83345 15787.0748.2 88.4182572 24560.63 85.3 53.17849 14771.849.6 91.5778608 25438.29 87.8 52.06093 14461.3750.9 94.9938252 26387.17 90.2 51.04699 14179.7252.3 98.7002927 27416.75 92.6 50.06954 13908.2153.7 102.949676 28597.13 95.1 49.12683 13646.3455.1 107.429529 29841.54 97.5 48.21668 13393.5256.4 112.367192 31213.11 99.9 48.27873 13410.7657.8 117.753316 32709.25 102.4 46.53652 12926.8159.2 123.730446 34369.57 104.8 45.67574 12687.760.6 130.3979 36221.64 107.3 44.88094 12466.9362.0 137.883931 38301.09 109.7 41.74193 11594.9863.3 146.4232 40673.11 112.1 43.35011 12041.764.7 156.024803 43340.22 114.6 42.68299 11856.3966.1 167.063984 46406.66 117.0 40.50203 11250.5667.5 71.5278474 19868.85 119.4 115.8995 32194.3268.8 72.0317333 20008.81 121.9 46.60948 12947.0870.2 73.2254415 20340.4 124.3 42.97901 11938.6171.6 74.45928 20683.13 126.8 44.42562 12340.4573.0 75.7743041 21048.42 129.2 41.94757 11652.174.3 77.0607488 21405.76 131.6 41.42672 11507.4275.7 78.5188597 21810.79 134.1 40.09503 11137.5177.1 79.9285692 22202.38 136.5 39.13899 10871.9478.5 81.4900671 22636.13 138.9 37.40916 10391.4379.8 83.0981293 23082.81 141.4 37.48038 10411.2281.2 84.7835121 23550.98 143.8 38.12846 10591.2482.6 86.5535601 24042.66 146.3 35.15204 9764.45684.0 88.414529 24559.59 148.7 35.2211 9783.63985.4 90.3736503 25103.79 151.1 33.73232 9370.08886.7 92.4389604 25677.49 153.6 33.8459 9401.63988.1 94.6198086 26283.28 156.0 32.43265 9009.07189.5 96.9249159 26923.59 158.4 32.56469 9045.74790.9 99.367027 27601.95 160.9 31.2171 8671.41692.2 102.083761 28356.6 163.3 31.36896 8713.693.6 104.779561 29105.43 165.8 30.08075 8355.76495.0 107.834233 29953.95 168.2 30.25049 8402.91596.4 110.979938 30827.76 170.6 29.01421 8059.50297.7 114.351728 31764.37 173.1 27.25886 7571.90599.1 117.956984 32765.83 175.5 28.70142 7972.615

100.5 66.0341584 18342.82 177.9 0 0101.9 65.9564562 18321.24 180.4 0 0103.3 76.8985733 21360.71 182.8 18.46468 5129.078104.6 89.6481263 24902.26 185.3 30.37507 8437.521106.0 87.7131664 24364.77 187.7 28.07775 7799.375107.4 94.0151188 26115.31 190.1 28.84794 8013.317108.8 92.0890073 25580.28 192.6 25.81038 7169.549110.1 98.9338112 27481.61 195.0 25.8927 7192.416111.5 97.0551011 26959.75 197.4 23.85401 6626.114112.9 99.425349 27618.15 199.9 23.99889 6666.359114.3 102.414663 28448.52 202.3 23.80083 6611.342115.6 105.278621 29244.06 204.8 21.36428 5934.522117.0 108.655339 30182.04 207.2 20.61179 5725.497118.4 111.915977 31087.77 209.6 20.87473 5798.535119.8 115.669326 32130.37 212.1 19.32809 5368.915121.1 119.638039 33232.79 214.5 19.59628 5443.41122.5 123.934932 34426.37 216.9 18.14545 5040.403123.9 128.601227 35722.56 219.4 17.58477 4884.659125.3 128.961207 35822.56 221.8 18.40561 5112.669126.7 138.88865 38580.18 224.3 16.12587 4479.407128.0 145.071106 40297.53 226.7 16.10893 4474.704129.4 146.059772 40572.16 229.1 15.68965 4358.235130.8 158.551261 44042.02 231.6 16.49241 4581.226132.2 156.757824 43543.84 234.0 14.4538 4014.943

Optimum UA Optimum UA



Comparison of Converter types Type Advantages Disadvantages Multiple Adiabatic Beds All the gas sees all the

catalyst – reduces catalyst volume

Large loop interchanger

Johnson Matthey Catalysts Quench Converter

Simple to load/discharge catalyst Heat can be recovered into saturator circuit hence maximizing efficiency

Potential for Cold Cores Large catalyst volume since not all of the gas sees all the catalyst

Casale ARC Converter Haldor Topsøe CMD

Even distribution Low operating temperatures and hence long catalyst lives Robust mechanical design Heat can be recovered into saturator circuit hence maximizing efficiency Can retrofit to existing Quench Converter

Require oxidation prior to catalyst discharge

Johnson Matthey Catalysts Tube Cooled

Integration of catalyst and heat exchange reduces CAPEX Simple catalyst loading All the gas sees all the catalyst – reduces catalyst volume Heat can be recovered into saturator circuit hence maximizing efficiency Easy to operate

Inspection is difficult

Linde Variobar Converter Simple catalyst loading Low operating temperatures giving long catalyst lives All the gas sees all the catalyst – reduces catalyst volume BFW circulated by natural circulation Low heat exchange area

Inspection is difficult



Uhde Steam Raising Lurgi Steam Raising Converter

Low operating temperatures giving long catalyst lives BFW circulated by natural circulation Low byproducts

Catalyst loading needs pressure drop checks to ensure even process gas flow Inspection is difficult High heat exchange area

Toyo MRF Converter Low pressure drop design Suitable for large capacities

Complex catalyst loading Require BFW circulation pumps Inspection is difficult



Troubleshooting The following table should be used as a guide to trouble shooting some common problems that occur in methanol synthesis loops.

Problem Effect Solution Low Circulation Rate High Converter Pressure Drop. Check valve position.

Check converter DPI meter Mesh damage and catalyst passing into outlet pipe. Catalyst breakage.

Low Heat Recovery Fouling of Exchanger. Chemically clean exchanger. Low exit converter temperature. Too little gas through heat recovery exchanger.

High Converter Temperature Spreads

Cold Core. Raise converter temperature. Change catalyst and ensure good catalyst loading.

Instability ARC Low temperatures in converter – large ATE’s exit bed 1.

Drop circulation rate. If this fails then raise converter inlet temperature by 0.5°C.

Instability TCC Operating below minimum stability point. Raise turn temperature. High Turn Temperature in TCC and loss of Production

Too high a recycle rate. Too high a UA.

Gag in circulator. Modify converter internals.

High Temperature on Trip Methanation. De-pressure on loop trip. Valve failure.

Increasing Crude Cooler Exit Temperature

Wax deposition. Shell side fouling.

Reduce CW flow and raise exit temperature. Chemically clean shellside. Maximise CW flow to keep return CW temperature down.

Low Catalyst Activity Catalyst poisoning. Temperature excursions.

Check for sulphur/chlorides etc. De-pressure loop on trip.

Isothermal Methanol Converter (IMC) UA Distribution Analysis

Technology

Transcript of Isothermal Methanol Converter (IMC) UA Distribution Analysis