Spreadsheet: 0be81552-0507-4bd1-92d5-085ef3b7b9a9
Sheet: Mat Bal

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 |  |  |  |  |  |  |  |  |  |  |  |  |  |  | Str-name | Nat Gas | Burnr Air | CmbstGas | StackGas | Leak Air | Cold Al | Hot Al
 |  |  |  |  |  |  |  |  |  |  |  |  |  |  | Streams | 1 | 2 | 3 | 4 | 5 | 6 | 7
 |  |  |  | From StoichCalc.xlsx |  |  |  |  |  |  |  |  |  |  | Flow
 |  |  | % excess oxidant | 0.18 |  |  |  |  |  |  |  |  |  |  | Al, (c) | 0 | 0 | 0 | 0 | 0
 |  |  | Oxidant/NG volume ratio | 11.269 |  |  |  |  |  |  |  |  |  |  | CH4, (g) |  | 0 | 0 | 0 | 0 | 0 | 0
 |  |  |  |  |  |  |  |  |  |  |  |  |  |  | [NAME], (g) |  | 0 | 0 | 0 | 0 | 0 | 0
 |  |  | From VolCalc.xlsx |  |  |  |  |  |  |  |  |  |  |  | CO2, (g) | 0 | 0 |  |  | 0 | 0 | 0
 |  |  | IUPAC |  |  | converted to |  | AES |  |  |  |  |  |  | H2O, (g) | 0 | 0 |  |  | 0 | 0 | 0
 |  | V, m3 | P, Pa | T, °C | g-mol |  | V, ft3 | P, psia | T, °F | lb-mol |  |  |  |  | N2, (g) |  |  |  |  |  | 0 | 0
 | NatGas | 32 | 101325 | 25 | 1307.96354414675 |  | 1130.063212910972 | 14.69756309834639 | 77 | 2.883873957934385 |  |  |  |  | O2, (g) | 0 |  |  |  |  | 0 | 0
 | Air (18% excess) |  | 101325 | 25 | 14739.11418810369 |  | 12734.39983049052 | 14.69756309834639 | 77 | 32.4976546634731
 |  |  | From HeatCalc.xlsx |  |  |  |  |  |  |  |  |  |  |  | T (°C) | 25 | 25 | 1800 | 800.0000000000001 | 25 | 25 | 550
 |  |  |  | mol/mol NG | Total |  |  |  |  |  |  |  |  |  | Str-unit | Vol (m3) | Vol (m3) | Vol (m3) | Vol (m3) | Vol (m3) | Mass (kg) | Mass (kg)
 |  |  | CO2 produced by combustion | 1.01 |  |  |  |  |  |  |  |  |  |  | Spec-unit | Vol. % | Vol. % | Vol. % | Vol. % | Vol. % | Mass (kg) | Mass (kg)
 |  |  | H2O produced by combustion | 1.99 |  |  |  |  |  |  |  |  |  |  | Str-name | Nat Gas | Air | CmbstGas | StackGas | Leak Air | Cold Al | Hot Al
 |  |  | O2 required for combustion | 2.005 |  |  |  |  |  |  |  |  |  |  | Streams | 1 | 2 | 3 | 4 | 5 | 6 | 7
 |  |  |  |  |  |  |  |  |  |  |  |  |  |  | Flow |  |  | 2733.234284755998 | 1414.837504611769 | 7.941468926553719 | 800 | 799.9999999999998
 |  |  |  | CH4 | 0.95 |  |  |  |  |  |  |  |  |  | Al, (c) | 0 | 0 | 0 | 0 | 0 | 800 | 799.9999999999999
 |  |  |  | C2H4 | 0 |  |  |  |  |  |  |  |  |  | CH4, (g) |  | 0 | 0 | 0 | 0 | 0 | 0
 |  |  |  | [NAME] | 0.03 |  |  |  |  |  |  |  |  |  | [NAME], (g) |  | 0 | 0 | 0 | 0 | 0 | 0
 |  |  |  | C3H8 | 0 |  |  |  |  |  |  |  |  |  | CO2, (g) | 0 | 0 |  |  | 0 | 0 | 0
 |  |  |  | C4H10 + | 0 |  |  |  |  |  |  |  |  |  | H2O, (g) | 0 | 0 |  |  | 0 | 0 | 0
 |  |  |  | H2 | 0 |  |  |  |  |  |  |  |  |  | N2, (g) |  | 0.79 |  |  | 0.79 | 0 | 0
 |  |  |  | CO | 0 |  |  |  |  |  |  |  |  |  | O2, (g) | 0 | 0.21 |  |  | 0.21 | 0 | 0
 |  |  |  | CO2 | 0
 |  |  |  | N2 | 0.02000000000000002 |  |  |  |  |  |  |  |  |  |  | [NAME] balance around stack gas to calculate Leak air flow
 |  |  |  |  |  | Initial (input) material balance ledger
 |  |  | P (atm) | 1 | 1 | 1 | 1 | 1 | 1 | 1
 |  |  | T (C) | 25 | 25 | 1800 | 800 | 25 | 25 | 550
 |  |  | Str-unit | Vol. (m3) | Vol. (m3) | Vol. (m3) | Vol. (m3) | Vol. (m3) | Mass (kg) | Mass (kg)
 |  |  | Spec-unit | Vol. % | Vol. % | Vol. % | Vol. % | Vol. % | Mass (kg) | Mass (kg)
 |  |  | Str-name | Nat Gas | Burnr Air | HotGas | StackGas | Leak Air | Cold Al | Hot Al
 |  |  | Streams | 1 | 2 | 3 | 4 | 5 | 6 | 7 | R #1 | R #2
 |  |  | Flow | 32 | 360.6 | ? | ? | ? | 800 | 800
 |  |  | Al, (c) |  |  |  |  |  | 800 | 800
 |  |  | CH4, (g) | 95 |  |  |  |  |  |  | -1
 |  |  | CO2, (g) |  |  | ? | ? |  |  |  | 1 | 2
 |  |  | H2O, (g) |  |  | ? | ? |  |  |  | 2 | 3
 |  |  | N2, (g) | 2 | 79 | ? | ? | 79
 |  |  | O2, (g) |  | 21 | ? | 3.3 | 21 |  |  | -2 | -3.5
 |  |  | [NAME], (g) | 3 |  |  |  |  |  |  |  | -1
 |  |  |  | Burner (Reactor) |  |  | Furnace (Mixer/Hx Exchanger)
 |  |  | Instreams | Outstreams | Reactions | Heat (kcal) | Instreams | Outstreams | Heat (kcal)
 |  |  | 1 | 3 | 1 | ? | 3 | 4 | ?
 |  |  | 2 |  | 2 |  | 5 | 7
 |  |  |  |  |  |  | 6