Table 1.
Plant process stream COD and impurity concentrations.
Process Streams |
Liquid Portion |
Solid Portion |
||||||||
---|---|---|---|---|---|---|---|---|---|---|
# | Name | COD (g/L) | Acetalde-hyde (mg/L) | Prop-anol (mg/L) | Meth-anol (mg/L) | Acetal (mg/L) | Acetalde-hyde (mg/L) | Meth-anol (mg/L) | Prop-anol (mg/L) | Acetal (mg/L) |
1 | Mix Tank Mash | 310 | <DL | <DL | <DL | <DL | 11 | <DL | 3.6 | <DL |
2 | Liquefaction Tank Mash | 290 | <DL | <DL | <DL | <DL | 360 | 33 | <DL | <DL |
3 | Ferm Tank Beer | 230 | 130 | 14 | 390 | <DL | 220 | 860 | <DL | 2.0 |
4 | Beer Well | 280 | 260 | 12 | 170 | <DL | 160 | 990 | 5.0 | 2.0 |
5 | Column Tops | 1200 | 610 | 130 | 380 | 130 | NS | NS | NS | NS |
6 | Mole Sieve Reject | 1200 | 580 | 13 | 1700 | 10 | NS | NS | NS | NS |
7 | Column Bottoms | 120 | <DL | <DL | <DL | <DL | <DL | <DL | <DL | 3.0 |
9,10,11 | Thin Stillage | 150 | <DL | <DL | <DL | <DL | <DL | <DL | <DL | 1.3 |
12 | Corn Oil/Syrup | 52 | <DL | 10 | <DL | <DL | <DL | <DL | <DL | 2.7 |
13 | Evaporated Water | 5 | <DL | <DL | <DL | <DL | NS | NS | NS | NS |
15 | Well Water | 14 | <DL | <DL | <DL | <DL | NS | NS | NS | NS |
17 | CO2 Scrubber Water | 40 | <DL | <DL | 77 | <DL | NS | NS | NS | NS |
18 | Recycled Cook Water | 17 | <DL | <DL | <DL | <DL | NS | NS | NS | NS |
* | Cooling Tower Blow Down | 1 | <DL | <DL | <DL | <DL | NS | NS | NS | NS |
* | Cooling Tower Blow Down + RO Reject | <DL | <DL | <DL | <DL | <DL | NS | NS | NS | NS |
NS = no solids in the process stream and <DL = under detection limit. DL is as follows: COD = 1.0 mg/l; acetaldehyde = 7.5 mg/l; propanol = 9 mg/l; methanol = 9 mg/l; and acetal = 5 mg/l.