6. Optimum ANFO, LAN & UF Resin Production & Distribution
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BMC - BOS: Case Study - Multi-Product, Multi-Supply Chain (MPMS) Optimisation - Dr BM Cole, Ph.D.Eng.(Pr. Eng.) Optimisation of Nitrates-based Explosives (ANFO), Fertiliser (LAN) and (UF Resins) Production & Distribution Facility under operational uncertainty B) Basic Flowchart No 2 Ammonia Plant - MP (180 bar) - 180 tons/day No 4 Ammonia Plant - HP (280 bar) - 1,000 tons/day Coal (C) No 7 Nitric Acid Plant - 3.3 bar - 80 tons/day NH3 (N2) H2O (h) No 10 HP Nitric Acid Plant - 8.0 bar No 9 HP Nitric Acid Plant - 8.7 bar - 275 tons/day No 11 DPOP Nitric Acid Plant - 4.0 & 8.0 bar - 695 tons/day NH3 (N4) 55% HNO3 Coal Residue - Solid (R2) + CO/CO2 (G2) No 1 Ammonium Nitrate 88% Solution (ANS)1 Plant - 350 tons/day No 2 Ammonium Nitrate 92% Solution (ANS)2 Plant - 650 No 1 Ammonium Nitrate Plant - 75 tons/day No 2 Ammonium Nitrate Plant - 125 tons/day No 3 Ammonium Nitrate Plant - 125 tons/day No 4 Ammonium Nitrate Plant - 240 tons/day Limestone Ammonium Nitrate Plant (LAN) - 550 tons/day Limestone (L) h7 h9 h10 h11 C2 C4 Coal Residue - Solid (R4) + CO/CO2 (G4) NH3 Sales (N4)s (N2)ANS1 NH3 Sales (N2)s (N4)9 (N4)10 (HN)9 60% HNO3 Nitric Acid (HN)10 (HN)11 (N2)7 (N4)ANS2 (HN)7 55% HNO3 NA Sales NO/NO2 Tailgas (T7) NO/NO2 Tailgas (T9) NO/NO2 Tailgas (T11) NO/NO2 Tailgas (T10) (N4)11 Air (A7) Air (A9) Air (A10) Air (A11) (WV)ANS1 92% ANS Supply Tank 88% ANS Sales (ANS)S 88 (ANS)AN1 (ANS)AN2 (ANS)AN3 (AN)AN1 (AN)AN2 (AN)AN3 (AN)S (WV)AN3 (WV)AN1 (WV)AN2 88% ANS Supply Tank 92% ANS Sales (ANS)S 92 (WV)AN4 (AN)S (ANS)AN4 (ANS)LAN (WV)LAN 60% Nitric Acid Sales LAN Inventort Control SA Agricultural Industry Urea Production - Synthesis (Carbomation) 2NH 3 + CO 2 NH 2 COONH 4 - Decomposition NH 2 COONH 4 NH 2 CONH 2 + H 2 O - Concentration NH3 (Urea) Carbon Dioxide CO2 Heat ANFO Production Fuel Oil Formaldehyde (CH 2 O) UF Resin H-[-NH-C-NH-]n-OH || O pH Control SA Timber Industry Urea (NH 2 CONH 2 ) UF Resin Condensor (Condensation) NH 2 CONH 2 + nCH 2 O Waste Treatmebt Reflux Condenser SA Mining Industry Scenario 1 Max (ANFO) = 259,024 LAN = 70,063 UF Resin = 56, 270 Scenario 2 ANFO = 135,272 Max ( LAN) = 189,750 UF Resin = 56,235 Scenario 3 ANFO = 139,234 (LAN) = 133,901 Max ( UF Resin ) = 63,500
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Transcript of 6. Optimum ANFO, LAN & UF Resin Production & Distribution
BMC - BOS: Case Study - Multi-Product, Multi-Supply Chain (MPMS) Optimisation - Dr BM Cole, Ph.D.Eng.(Pr. Eng.)
Optimisation of Nitrates-based Explosives (ANFO), Fertiliser (LAN) and (UF Resins) Production & Distribution Facility under operational uncertainty
B) Basic Flowchart
No 2 Ammonia Plant - MP (180 bar) - 180 tons/day
No 4 Ammonia Plant - HP (280 bar)
- 1,000 tons/day
Coal (C)
No 7 Nitric Acid Plant
- 3.3 bar
- 80 tons/day
NH3 (N2)
H2O (h)
No 10 HP Nitric Acid Plant
- 8.0 bar
No 9 HP Nitric Acid Plant- 8.7 bar
- 275 tons/day
No 11 DPOP Nitric Acid Plant
- 4.0 & 8.0 bar
- 695 tons/day
NH3 (N4)
55% HNO3
Coal Residue -Solid (R2) +
CO/CO2 (G2)
No 1 Ammonium Nitrate 88% Solution (ANS)1
Plant - 350 tons/day
No 2 Ammonium Nitrate 92% Solution (ANS)2 Plant - 650
No 1 Ammonium Nitrate Plant- 75 tons/day
No 2 Ammonium Nitrate Plant- 125 tons/day
No 3 Ammonium Nitrate Plant- 125 tons/day
No 4 Ammonium Nitrate Plant
- 240 tons/day
Limestone Ammonium Nitrate Plant (LAN)
- 550 tons/day
Limestone (L)
h7
h9
h10
h11
C2 C4
Coal Residue -Solid (R4) +
CO/CO2 (G4)
NH3 Sales (N4)s
(N2)ANS1
NH3 Sales(N2)s
(N4)9
(N4)10
(HN)9
60% HNO3
Nitric Acid
(HN)10
(HN)11
(N2)7
(N4)ANS2
(HN)7
55% HNO3
NA SalesNO/NO2
Tailgas (T7)
NO/NO2
Tailgas (T9)
NO/NO2
Tailgas (T11)NO/NO2Tailgas (T10)
(N4)11
Air (A7)
Air (A9)
Air (A10)
Air (A11)
(WV)ANS192% ANS
Supply Tank
88% ANS Sales (ANS)S
88
(ANS)AN1
(ANS)AN2
(ANS)AN3
(AN)AN1
(AN)AN2
(AN)AN3
(AN)S
(WV)AN3
(WV)AN1
(WV)AN2
88% ANS Supply Tank
92% ANS Sales (ANS)S
92
(WV)AN4
(AN)S
(ANS)AN4
(ANS)LAN(WV)LAN
60% Nitric Acid Sales
LAN Inventort Control
SA Agricultural Industry
Urea Production- Synthesis (Carbomation)
2NH3 + CO2 NH2COONH4
- Decomposition
NH2COONH4 NH2CONH2+ H2O- Concentration
NH3 (Urea)
Carbon Dioxide CO2
Heat
ANFO Production
Fuel Oil
Formaldehyde (CH2O)
UF Res in
H-[-NH-C-NH-]n-OH
||O
pH Control
SA Timber Industry
Urea (NH2CONH2)
UF Resin Condensor(Condensation)
NH2CONH2 + nCH2O
Waste Treatmebt
Reflux Condenser
SA Mining Industry
Scenario 1
Max (ANFO) = 259,024LAN = 70,063
UF Resin = 56, 270
Scenario 2
ANFO = 135,272Max ( LAN) = 189,750
UF Resin = 56,235
Scenario 3
ANFO = 139,234(LAN) = 133,901
Max ( UF Resin ) = 63,500
