MICROBIAL TOOLBOX SUMMARY TABLE: OPTIONS, TREATMENT CREDITS AND CRITERIA
Toolbox Option | Cryptosporidium treatment credit with design and implementation criteria |
Source Protection and Management Toolbox Options | |
(1) Watershed control program... | 0.5 -log credit for director-approved program comprising required elements, annual program status report to director, and regular watershed survey. Specific criteria are in paragraph (B) of this rule. |
(2) Alternative source/intake management... | No prescribed credit. Systems may conduct simultaneous monitoring for treatment bin classification at alternative intake locations or under alternative intake management strategies. Specific criteria are in paragraph (C) of this rule. |
Pre Filtration Toolbox Options | |
(3) Presedimentation basin with coagulation... | 0.5 -log credit during any month that presedimentation basins achieve a monthly mean reduction of 0.5 -log or greater in turbidity or alternative director-approved performance criteria. To be eligible, basins shall be operated continuously with coagulant addition and all plant flow shall pass through basins. Specific criteria are in paragraph (D) of this rule. |
(4) Two-stage lime softening... | 0.5 -log credit for two-stage softening where chemical additional and hardness precipitation occur in both stages. All plant flow shall pass through both stages. Singlestage softening is credited as equivalent to conventional treatment. Specific criteria are in paragraph (E) of this rule. |
(5) Bank filtration... | 0.5 -log credit for 25-foot setback; 1.0 -log credit for 50-foot setback; aquifer shall be unconsolidated sand containing at least 10 per cent fines; average turbidity in wells shall be less than 1 NTU. Systems using wells followed by filtration when conducting source water monitoring shall sample the well to determine bin classification and are not eligible for additional credit. Specific criteria are in paragraph (F) of this rule. |
Treatment Performance Toolbox Options | |
(6) Combined filter performance... | 0.5 -log credit for combined filter effluent turbidity less than or equal to 0.15 NTU in at least 95 per cent of measurements each month. Specific criteria are in paragraph (G) of this rule. |
(7) Individual filter performance... | 0.5 -log credit (in addition to 0.5 -log combined filter performance credit) if individual filter effluent turbidity is less than or equal to 0.15 NTU in at least 95 per cent of samples each month in each filter and is never greater than 0.3 NTU in two consecutive measurements in any filter. Specific criteria are in paragraph (H) of this rule. |
(8) Demonstration of performance... | Credit awarded to unit process or treatment train based on a demonstration to the director with a director-accepted protocol. Specific criteria are in paragraph (I) of this rule. |
Additional Filtration Toolbox Options | |
(9) Bag or cartridge filters (individual filters)... | Up to 2-log credit based on the removal efficiency demonstrated during challenge testing with a 1.0 -log factor of safety. Specific criteria are in paragraph (J) of this rule. |
(10) Bag or cartridge filters (in series)... | Up to 2.5 -log credit based on the removal efficiency demonstrated during challenge testing with a 0.5 -log factor of safety. Specific criteria in paragraph (J) of this rule. |
(11) Membrane filtration... | Log credit equivalent to removal efficiency demonstrated in challenge test for device if supported by direct integrity testing. Specific criteria are in paragraph (K) of this rule. |
(12) Second stage filtration... | 0.5 -log credit for second separate granular media filtration stage if treatment train includes coagulation prior to first filter. Specific criteria are in paragraph (L) of this rule. |
(13) Slow sand filters.... | 2.5 -log credit as a secondary filtration step; 3.0 -log credit as a primary filtration process. No prior chlorination for either option. Specific criteria are in paragraph (M) of this rule. |
Inactivation Toolbox Options | |
(14) Chlorine dioxide... | Log credit based on measured CT in relation to CT table. Specific criteria in paragraph (N)(2) of this rule. |
(15) Ozone... | Log credit based on measured CT in relation to CT table. Specific criteria in paragraph (N)(2) of this rule. |
(16) UV... | Log credit based on validated UV dose in relation to UV dose table; reactor validation testing required to establish UV dose and associated operating conditions. Specific criteria in paragraph (N)(4) of this rule. |
Systems received 0.5 -log Cryptosporidium treatment credit for implementing a watershed control program that meets the following :
Systems receive 0.5 -log Cryptosporidium treatment credit for a presedimentation basin during any month the process meets the following criteria :
log10 (monthly mean of daily influent turbidity) - log10 (monthly mean of daily effluent turbidity).
The daily turbidity measurements shall be taken under normal operating conditions for that day. Presedimentation operations shall not be altered for the sole purpose of influencing sample results.
Systems receive an additional 0.5 -log Cryptosporidium treatment credit for a twostage lime softening plant if chemical addition and hardness precipitation occur in two separate and sequential softening stages prior to filtration. Both softening stages shall treat the entire plant flow taken from a surface water source.
Systems receive Cryptosporidium treatment credit for bank filtration that serves as pretreatment to a filtration plant by meeting the criteria in this paragraph. Systems using bank filtration beginning source water monitoring in accordance with paragraph (A) of rule 3745-81-65 of the Administrative Code shall collect samples as described in paragraph (J)(4) of rule 3745-81-65 of the Administrative Code and are not eligible for this credit.
Systems using conventional filtration treatment or direct filtration treatment receive an additional 0.5 -log Cryptosporidium treatment credit during any month the system meets the criteria in this paragraph. Combined filter effluent (CFE) turbidity shall be less than or equal to 0.15 NTU in at least ninety-five per cent of the measurements. Turbidity shall be measured as described in paragraph (C)(3) of rule 3745-81-27 and paragraph (A) of rule 3745-81-74 of the Administrative Code.
Systems using conventional filtration treatment or direct filtration treatment receive 0.5 -log Cryptosporidium treatment credit, which can be in addition to the 0.5 -log credit under paragraph (G) of this rule, during any month the system meets the criteria in this paragraph. Compliance with these criteria shall be based on individual filter turbidity monitoring as described in paragraphs (B) and (C) of rule 3745-81-74 of the Administrative Code, as applicable.
The director may approve Cryptosporidium treatment credit for drinking water treatment processes based on a demonstration of performance study that meets the criteria in this paragraph. This treatment credit may be greater than or less than the prescribed treatment credits in paragraph (E) of rule 3745-81-67 of the Administrative Code or paragraphs (D) to (N) of this rule and may be awarded to treatment processes that do not meet the criteria for the prescribed credits.
Systems receive Cryptosporidium treatment credit of up to 2.0 -log for individual bag or cartridge filters and up to 2.5 -log for bag or cartridge filters operated in series by meeting the criteria in paragraphs (J)(1) to (J)(10) of this rule. To be eligible for this credit, systems shall report the results of challenge testing that meets the requirements of paragraphs (J)(2) to (J)(9) of this rule to the director. The filters shall treat the entire plant flow taken from a surface water source.
Maximum Feed Concentration = 1 x 104 x (filtrate detection limit)
LRV = LOG10(Cf) - LOG10(Cp)
Where: LRV = log removal value demonstrated during challenge testing; Cf = the feed concentration measured during the challenge test; and Cp = the filtrate concentration measured during the challenge test. In applying this equation, the same units shall be used for the feed and filtrate concentrations. If the challenge particulate is not detected in the filtrate, then the term Cp shall be set equal to the detection limit.
The membrane used by the system shall undergo challenge testing to evaluate removal efficiency, and the system shall report the results of challenge testing to the director. Challenge testing shall be conducted according to the criteria in paragraphs (K)(2)(a) to (K)(2)(g) of this rule. Systems may use data from challenge testing conducted prior to January 5, 2006 if the prior testing was consistent with the criteria in paragraphs (K)(2)(a) to (K)(2)(g) of this rule.
maximum feed concentration = 3.16 x 106 x (filtrate detection limit)
LRV = LOG10(Cf) - LOG10(Cp)
Where:
LRV = log removal value demonstrated during the challenge test; Cf = the feed concentration measured during the challenge test; and Cp = the filtrate concentration measured during the challenge test.
Equivalent units shall be used for the feed and filtrate concentrations. If the challenge particulate is not detected in the filtrate, the term Cp is set equal to the detection limit for the purpose of calculating the LRV. An LRV shall be calculated for each membrane module evaluated during the challenge test.
Systems shall conduct direct integrity testing in a manner that demonstrates a removal efficiency equal to or greater than the removal credit awarded to the membrane filtration process and meets the requirements described in paragraphs (K)(3)(a) to (K)(3)(f) of this rule. A direct integrity test is defined as a physical test applied to a membrane unit in order to identify and isolate integrity breaches (e.g., one or more leaks that could result in contamination of the filtrate).
LRVDIT = LOG10 (Qp /(VCF x Qbreach))
Where:
LRVDIT = the sensitivity of the direct integrity test; Qp = total design filtrate flow from the membrane unit; Qbreach = flow of water from an integrity breach associated with the smallest integrity test response that can be reliably measured; and VCF = volumetric concentration factor. The volumetric concentration factor is the ratio of the suspended solids concentration on the high pressure side of the membrane relative to that in the feed water.
LRVDIT = LOG10(Cf) - LOG10(Cp)
Where:
LRVDIT = the sensitivity of the direct integrity test; Cf= the typical feed concentration of the marker used in the test; and Cp = the filtrate concentration of the marker from an integral membrane unit.
Systems shall conduct continuous indirect integrity monitoring on each membrane unit according to the criteria in paragraphs (K)(4)(a) to (K)(4)(f) of this rule. Indirect integrity monitoring is defined as monitoring some aspect of filtrate water quality that is indicative of the removal of particulate matter. A system that implements continuous direct integrity testing of membrane units in accordance with the criteria in paragraphs (K)(3)(a) to (K)(3)(f) of this rule is not subject to the requirements for continuous indirect integrity monitoring. Systems shall submit a monthly report to the director summarizing all continuous indirect integrity monitoring results triggering direct integrity testing and the corrective action that was taken in each case.
Systems receive 0.5 -log Cryptosporidium treatment credit for a separate second stage of filtration that consists of sand, dual media, GAC, or other fine grain media following granular media filtration if the director approves. To be eligible for this credit, the first stage of filtration shall be preceded by a coagulation step and both filtration stages shall treat the entire plant flow taken from a surface water source. A cap, such as GAC, on a single stage of filtration is not eligible for this credit. The director shall approve the treatment credit based on an assessment of the design characteristics of the filtration process.
Systems are eligible to receive 2.5 -log Cryptosporidium treatment credit for a slow sand filtration process that follows a separate stage of filtration if both filtration stages treat entire plant flow taken from a surface water source and no disinfectant residual is present in the influent water to the slow sand filtration process. The director shall approve the treatment credit based on an assessment of the design characteristics of the filtration process. This paragraph does not apply to treatment credit awarded to slow sand filtration used as a primary filtration process.
CT Values (MG-MIN/L) for Cryptosporidium Inactivation by Chlorine Dioxide 1
Log credit | Water Temperature, Cº | ||||||||||
<= 0.5 | 1 | 2 | 3 | 5 | 7 | 10 | 15 | 20 | 25 | 30 | |
(i) 0.25... | 159 | 153 | 140 | 128 | 107 | 90 | 69 | 45 | 29 | 19 | 12 |
(ii) 0.50... | 319 | 305 | 279 | 256 | 214 | 180 | 138 | 89 | 58 | 38 | 24 |
(iii) 1.0... | 637 | 610 | 558 | 511 | 429 | 360 | 277 | 179 | 116 | 75 | 49 |
(iv) 1.5... | 956 | 915 | 838 | 767 | 643 | 539 | 415 | 268 | 174 | 113 | 73 |
(v) 2.0... | 1275 | 1220 | 1117 | 1023 | 858 | 719 | 553 | 357 | 232 | 150 | 98 |
(vi) 2.5... | 1594 | 1525 | 1396 | 1278 | 1072 | 899 | 691 | 447 | 289 | 188 | 122 |
(vii) 3.0... | 1912 | 1830 | 1675 | 1534 | 1286 | 1079 | 830 | 536 | 347 | 226 | 147 |
1 Systems may use this equation to determine log credit between the indicated values: Log credit = (0.001506 x (1.09116) Temp) x CT.
CT Values (MG-MIN/L) for Cryptosporidium Inactivation by Ozone 1
Log credit | Water Temperature, Cº | ||||||||||
<= 0.5 | 1 | 2 | 3 | 5 | 7 | 10 | 15 | 20 | 25 | 30 | |
(i) 0.25... | 6.0 | 5.8 | 5.2 | 4.8 | 4.0 | 3.3 | 2.5 | 1.6 | 1.0 | 0.6 | 0.39 |
(ii) 0.50... | 12 | 12 | 10 | 9.5 | 7.9 | 6.5 | 4.9 | 3.1 | 2.0 | 1.2 | 0.78 |
(iii) 1.0... | 24 | 23 | 21 | 19 | 16 | 13 | 9.9 | 6.2 | 3.9 | 2.5 | 1.6 |
(iv) 1.5... | 36 | 35 | 31 | 29 | 24 | 20 | 15 | 9.3 | 5.9 | 3.7 | 2.4 |
(v) 2.0... | 48 | 46 | 42 | 38 | 32 | 26 | 20 | 12 | 7.8 | 4.9 | 3.1 |
(vi) 2.5... | 60 | 58 | 52 | 48 | 40 | 33 | 25 | 16 | 9.8 | 6.2 | 3.9 |
(vii) 3.0... | 72 | 69 | 63 | 57 | 47 | 39 | 30 | 19 | 12 | 7.4 | 4.7 |
1 Systems may use this equation to determine log credit between the indicated values: Log credit = (0.0397 x (1.09757) Temp) x CT.
The director may approve alternative chlorine dioxide or ozone CT values to those listed in paragraph (N)(2) of this rule on a site-specific basis. The director shall base this approval on a site-specific study a system conducts that follows a protocol acceptable to the director.
Water Treatment Rule" (November 2006), shall be used as a guide in the technical review of plans submitted for approval of UV facilities. The water research foundation "Guidance for Implementing Action Spectra Correction with Medium Pressure UV Disinfection (Web Report #4376)" shall also be used as a guide in the technical review of plans submitted for approval of medium pressure UV reactor facilities. Approval of plans for UV facilities may be conditioned upon requirements that may be necessary or desirable to ensure that the system being constructed, or of which the proposed project is a part, will be able to meet generally accepted standards for the design, equipping and operation of UV facilities. Systems shall keep daily operational logs used to determine monthly compliance with the percentage of water treated under validated conditions. The operational logs must be signed by an operator of record and kept on a form acceptable to the director. Operational logs must be made available for review upon request.
The treatment credits listed in this table are for UV light at a wavelength of two hundred fifty-four nanometers as produced by a low pressure mercury vapor lamp. To receive treatment credit for other lamp types, systems shall demonstrate an equivalent germicidal dose through reactor validation testing, as described in paragraph (N)(4)(b) of this rule. The UV dose values in this table are applicable only to post-filter applications of UV.
UV Dose Table for Cryptosporidium, Giardia lamblia, and Virus Inactivation Credit
Log credit | Cryptosporidium UV dose (mJ/cm2) | Giardia lamblia UV dose (mJ/cm2) | Virus UV dose (mJ/ cm2) |
(i) 0.5... | 1.6 | 1.5 | 39 |
(ii) 1.0... | 2.5 | 2.1 | 58 |
(iii) 1.5... | 3.9 | 3.0 | 79 |
(iv) 2.0... | 5.8 | 5.2 | 100 |
(v) 2.5... | 8.5 | 7.7 | 121 |
(vi) 3.0... | 12 | 11 | 143 |
(vii) 3.5... | 15 | 15 | 163 |
(viii) 4.0... | 22 | 22 | 186 |
Systems shall use UV reactors that have undergone validation testing to determine the operating conditions under which the reactor delivers the UV dose required in paragraph (N)(4)(a) of this rule (i.e., validated operating conditions). These operating conditions shall include flow rate, UV intensity as measured by a UV sensor, and UV lamp status.
Parameter | Recording Frequency | Required conditions for obtaining disinfection credit. |
Off-specification alarm | At least every 5 minutes | Recording shall continue until the alarm condition has been corrected. |
UV Intensity | At least every 4 hours | The UV intensity shall be greater than or equal to the validated set point. |
UVT (required only if necessary for the dose monitoring strategy (e.g., calculated dose approach)) | At least every 4 hours | The UVT shall be greater than or equal to the minimum UVT validated. |
Validated Dose | At least every 4 hours | The validated dose shall be greater than or equal to the Dreq. |
Lamp Status | At least every 4 hours | Lamps shall be energized if water is flowing through the UV reactor. |
Flow Rate | At least every 4 hours | The flow rate shall be less than or equal to the maximum flow tested in validation. |
Production Volume | Off-specification events and monthly total | The production volume shall be recorded so the off-specification compliance calculation can be completed. |
Calibration of UV Sensors | At least monthly | Calibration shall be conducted in accordance with a protocol acceptable to the director. |
Calibration of On-line UVT Analyzer (required only if necessary for the dose monitoring strategy (e.g., calculated dose approach) | Weekly | Calibration must be conducted in accordance with a protocol acceptable to the director. |
[This rule references the U.S. EPA "Membrane Guidance Manual for the Final Long Term 2 Enhanced Surface Water Treatment Rule," issued November 2005. This document is available from the "U.S. EPA Office of Ground Water and Drinking Water, Ariel Rios Building, 1200 Pennsylvania Ave, NW, Washington, DC 20460-0003, (202) 564-3750." A copy may also be obtained from www.epa.gov/safewater/disinfection/lt2/compliance.html.]
[This rule references the U.S. EPA "Ultraviolet Disinfection Guidance Manual for Final Long Term 2 Enhanced Surface Water Treatment Rule," issued November 2006. This document is available from the "U.S. EPA Office of Ground Water and Drinking Water, Ariel Rios Building, 1200 Pennsylvania Ave, NW, Washington, DC 20460-0003, (202) 564- 3750." A copy may also be obtained from www.epa.gov/safewater/disinfection/lt2/compliance.html.]
Ohio Admin. Code 3745-81-68
Five Year Review (FYR) Dates: 1/22/2020 and 03/01/2027
Promulgated Under: 119.03
Statutory Authority: 6109.04
Rule Amplifies: 6109.03, 6109.04
Prior Effective Dates: 01/08/2010