Constituent | AS (µg/L) | CS (µg/L) |
Arsenic (trivalent, dissolved) | 340 X 1.0 *=340 | 150 X 1.0*=150 |
Benzene | 4200 | 860 |
Cadmium (dissolved) | eA+B ln(H) X {1.138672 -[(ln(H))(0.041838) ]}*, where A=-2.918 and B=1.128 | eA+B ln(H) X {1.101672 -[(ln(H))(0.041838)]}*, where A= -3.490 and B=0.7852 |
Chromium (hexavalent, total) | 16 | 11 |
Chromium (trivalent, dissolved) | eA+B ln(H) X 0.316 *, where A=3.7256 and B=0.8190 | eA+B ln(H) X 0.860 *, where A=0.6848 and B=0.8190 |
Copper (dissolved) | eA+B ln(H) X 0.960 *, where A=-1.645 and B=0.9422 | eA+B ln(H) X 0.960*, where A=-1.646 and B=0.8545 |
Cyanide** | 22 | 10 |
Ethylbenzene | 150 | 14 |
Fluoride (total) | eA+B ln(H), where A=6.7319 and B=0.5394 | eA+B ln(H), but must not exceed 4.0 mg/L, where A=6.0445 and B=0.5394 |
Lead (dissolved) | eA+B ln(H) X {1.46203 -[(ln(H))(0.145712) ]}*, where A=-1.301 and B=1.273 | eA+B ln(H) X {1.46203-[(ln(H))(0.145712)]}*, where A=-2.863 and B=1.273 |
Manganese (dissolved) | eA+B ln(H) X 0.9812 *, where A=4.9187 and B=0.7467 | eA+B ln(H) X 0.9812*, where A=4.0635 and B=0.7467 |
Mercury (dissolved) | 1.4 X 0.85 *=1.2 | 0.77 X 0.85*=0.65 |
Nickel (dissolved) | eA+B ln(H) X 0.998 *, where A=0.5173 and B=0.8460 | eA+B ln(H) X 0.997 *, where A=-2.286 and B=0.8460 |
Toluene | 2000 | 600 |
TRC | 19 | 11 |
Xylene(s) | 920 | 360 |
Zinc (dissolved) | eA+B ln(H) X 0.978 *, where A=0.9035 and B=0.8473 | eA+B ln(H) X 0.986 *, where A=-0.4456 and B=0.8473 |
where:
µg/L | = | microgram per liter |
H | = | Hardness concentration of receiving water in mg/L as CaCO3 |
ex | = | base of natural logarithms raised to the x-power |
ln(H) | = | natural logarithm of hardness in mg/L as CaCO3 |
* | = | conversion factor multiplier for dissolved metals |
** | = | standard to be evaluated using either of the following USEPA approved methods, incorporated by reference at 35 Ill. Adm. Code 301.106: Method OIA-1677, DW: Available Cyanide by Flow Injection, Ligand Exchange, and Amperometry, January 2004, Document Number EPA-821-R-04-001; or Cyanide Amenable to Chlorination, Standard Methods 4500-CN-G (40 CFR 136.3) |
Constituent | HHS (µg/L) |
Benzene | 310 |
Mercury (total) | 0.012 |
Phenols | 860,000 |
where:
µg/L | = | microgram per liter |
Concentrations of the following chemical constituents must not be exceeded except in waters for which mixing is allowed under Section 302.102.
Constituent | Unit | Standard |
Chloride | mg/L | 500 |
Iron (dissolved) | mg/L | 1.0 |
Selenium (total) | mg/L | 1.0 |
Silver (dissolved) | µg/L | eA+B ln(H) X 0.85*, where A=-6.52 and B=1.72 |
Sulfate (where H is [GREATER THAN OR EQUAL TO] 100 but [LESS THAN OR EQUAL TO] 500 and C is [GREATER THAN OR EQUAL TO] 25 but [LESS THAN OR EQUAL TO] 500) | mg/L | [1276.7 +5.508(H) -1.457(C)] X 0.65 |
Sulfate (where H is [GREATER THAN OR EQUAL TO] 100 but [LESS THAN OR EQUAL TO] 500 and C is [GREATER THAN OR EQUAL TO] 5 but < 25) | mg/L | [-57.478 + 5.79(H) + 54.163(C)] X 0.65 |
Sulfate (where H > 500 and C [GREATER THAN OR EQUAL TO] 5) | mg/L | 2,000 |
where:
mg/L | = | milligram per liter |
µg/L | = | microgram per liter |
H | = | hardness concentration of receiving water in mg/L as CaCO3 |
C | = | chloride concentration of receiving water in mg/L |
ex | = | base of natural logarithms raised to the x-power |
ln(H) | = | natural logarithm of hardness in milligrams per liter |
* | = | conversion factor multiplier for dissolved metals |
CONSTITUENT | CONCENTRATION (mg/L) |
Ammonia Un-ionized (as N*) | 0.1 |
Arsenic (total) | 1.0 |
Barium (total) | 5.0 |
Cadmium (total) | 0.15 |
Chromium (total hexavalent) | 0.3 |
Chromium (total trivalent) | 1.0 |
Copper (total) | 1.0 |
Cyanide (total) | 0.10 |
Fluoride (total) | 15.0 |
Iron (total) | 2.0 |
Iron (dissolved) | 0.5 |
Lead (total) | 0.1 |
Manganese (total) | 1.0 |
Mercury (total) | 0.0005 |
Nickel (total) | 1.0 |
Oil, fats and grease | 15.0** |
Phenols | 0.3 |
Selenium (total) | 1.0 |
Silver | 1.1 |
Zinc (total) | 1.0 |
Total Dissolved Solids | 1500 |
* For purposes of this Section, the concentration of un-ionized ammonia must be computed according to the following equation:
where:
U | = | Concentration of un-ionized ammonia as N in mg/L |
N | = | Concentration of ammonia nitrogen as N in mg/L |
T | = | Temperature in degrees Celsius |
** Oil must be analytically separated into polar and non-polar components if the total concentration exceeds 15 mg/L. In no case may either of the components exceed 15 mg/L (i.e., 15 mg/L polar materials and 15 mg/L non-polar materials).
Ill. Admin. Code tit. 35, § 302.407
Amended at 20 Ill. Reg. 7682, effective May 24, 1996