| #P001 | chemical | health | guideline | Carbon tetrachloride | drinking water | MAC | 0.002 mg/L | Maximum acceptable concentration (MAC) | | high |
| #P002 | design | treatment | recommended | Carbon tetrachloride | drinking water | requirement | < 0.0018 mg/L | Maximum final (effluent) concentration | For a drinking water treatment device to be certified to NSF/ANSI Standard 53 or 58 for the removal of carbon tetrachloride or VOCs | high |
| #P003 | design | treatment | recommended | Carbon tetrachloride | drinking water | requirement | 0.078 mg/L | Influent (challenge) concentration | For a drinking water treatment device to be certified to NSF/ANSI Standard 53 for the removal of carbon tetrachloride | high |
| #P004 | design | treatment | recommended | Carbon tetrachloride | drinking water | treatment_goal | > 98 % | Reducing the concentration by more than 98% | For a drinking water treatment device to be certified to NSF/ANSI Standard 53 for the removal of carbon tetrachloride | high |
| #P005 | design | treatment | guidance | Carbon tetrachloride | drinking water | requirement | 5 µg/L | Treatment devices certified specifically for carbon tetrachloride removal can only verify that they would meet this final concentration | Treatment devices certified specifically for carbon tetrachloride removal | high |
| #P006 | design | treatment | guidance | Carbon tetrachloride | drinking water | requirement | < 1.8 µg/L | Final concentration achieved | Only treatment devices certified for the removal of VOCs can verify that this final concentration is achieved | high |
| #P007 | operational | treatment | guidance | Carbon tetrachloride | drinking water | treatment_goal | < 1 µg/L | Effluent concentrations below 1 µg/L is considered feasible | Granular activated carbon (GAC) adsorption under reasonable operating conditions | medium |
| #P008 | operational | treatment | guidance | Carbon tetrachloride | drinking water | treatment_goal | 1 µg/L | Obtain effluent concentrations of 1 µg/L are considered to be achievable | Packed tower aeration (PTA) | medium |
| #P009 | operational | treatment | guidance | Carbon tetrachloride removal efficiency (GAC) | drinking water | treatment_goal | 99 % | A removal efficiency of 99% is considered feasible for carbon tetrachloride under reasonable operating conditions for granular activated carbon adsorption. | Granular activated carbon (GAC) adsorption under reasonable operating conditions | high |
| #P010 | operational | treatment | guidance | Carbon tetrachloride removal efficiency (PTA) | drinking water | treatment_goal | 99 % | Removal efficiencies of 99% to obtain effluent concentrations of 1 g/L are considered to be achievable using packed tower aeration. | Packed tower aeration (PTA) | high |
| #P011 | operational | treatment | guidance | Carbon tetrachloride removal efficiency (Reverse Osmosis) | drinking water | treatment_goal | 70-100 % | Bench-scale investigations demonstrated that selected reverse osmosis membranes were capable of reducing 70-100% of the carbon tetrachloride concentration in water. | Bench-scale investigations; dependent on membrane type, flux, recovery, solubility, molecular weight, etc. | high |
| #P012 | operational | treatment | guidance | Carbon tetrachloride removal efficiency (Membrane air stripping) | drinking water | treatment_goal | 85 % | Pilot-scale studies demonstrated up to 85% reduction of carbon tetrachloride and greater mass transfer coefficients with than with the use of traditional air stripping towers. | Microporous polypropylene hollow fibre membranes | high |
| #P013 | design | treatment | guidance | GAC Empty Bed Contact Time (EBCT) | drinking water | OG | 15 min | Estimated cost-effective design parameter for liquid-phase GAC treatment | To reduce influent concentration of 100 µg/L to 5 µg/L | high |
| #P014 | design | treatment | guidance | GAC Carbon Usage Rate | drinking water | OG | 0.03 kg/m³ | Estimated cost-effective design parameter for liquid-phase GAC treatment | To reduce influent concentration of 100 µg/L to 5 µg/L; equivalent to 0.25/1000 gallons | high |
| #P015 | design | treatment | guidance | PTA Air to Water Ratio | drinking water | OG | 20 ratio | Cost-effective PTA design parameters for plants ranging in size from 1 to 100 ML/day | For reduction of carbon tetrachloride | high |
| #P016 | design | treatment | guidance | PTA Packing Depth | drinking water | OG | 9.6 m | Cost-effective PTA design parameters for plants ranging in size from 1 to 100 ML/day | Equivalent to 31.5 ft | high |
| #P017 | operational | treatment | guidance | E-Beam Removal Efficiency Range | drinking water | treatment_goal | 97.5 - 99.3 % | Pilot-scale experiments for high-energy electron beam (E Beam) treatment | For influent concentrations ranging from 133 to 8490 µg/L | high |
| #P018 | design | treatment | guidance | PTA Air Stripper Length (Typical Full-Scale) | drinking water | OG | 13.7 m | Typical full-scale plant air stripping design parameters | Plant capacity > 8.17 ML/day | high |
| #P019 | operational | treatment | guidance | GAC Bed Life | drinking water | OG | 168 days | Estimated cost-effective design parameter for liquid-phase GAC treatment | Reducing 100 µg/L to 5 µg/L using an EBCT of 15 min | high |
| #P020 | operational | treatment | guidance | Carbon tetrachloride removal efficiency (GAC - Cost Effective) | drinking water | treatment_goal | 95 % | A reduction of carbon tetrachloride in drinking water may be achievable under specific cost-effective parameters. | Influent 100 µg/L, Effluent 5 µg/L, EBCT 15 min, bed life 168 days | high |
| #P021 | design | treatment | guidance | PTA Air to Water Ratio (Typical) | drinking water | OG | 6.2 ratio | Typical full-scale plant air stripping design parameters for reduction of carbon tetrachloride | Plant capacity > 8.17 ML/day | high |
| #P022 | design | treatment | guidance | PTA Packed Column Diameter | drinking water | OG | 1.5 m | Typical full-scale plant air stripping design parameters for reduction of carbon tetrachloride | Plant capacity > 8.17 ML/day | high |