* The water main is placed in a separate trench, or
* The water main is located on a bench of undisturbed earth at a minimum horizontal separation of three feet from the sewer.
If it is not possible to obtain a horizontal separation of three feet and a vertical separation of 18 inches between the bottom of the water main and the top of the sewer, a linear separation of at least two feet shall be provided, and one of the following shall be utilized:
* The water main shall be enclosed in watertight casing pipe with an evenly spaced annular gap and watertight end seals, or
* The sewer shall be constructed of water main materials.
The separation distance between the water main and the sewer shall be the maximum feasible in all cases.
* The bottom of the water main shall not be placed closer than six inches above the top of a sewer, or
* The top of the water main shall not be placed closer than 18 inches below the bottom of a sewer.
When a water main crosses below or less than 18 inches above a sanitary or combined sewer, one of the following shall be utilized within ten feet measured edge to edge horizontally, centered on the crossing:
* The water main shall be enclosed in watertight casing pipe with an evenly spaced annular gap and watertight ends, or
* Sewer pipe of water main material shall be installed.
The separation distance shall be the maximum feasible in all cases. Wherever a water main crosses a sanitary or combined sewer, the water main and sanitary or combined sewer pipes must be adequately supported. A low permeability soil shall be used for backfill material within ten feet of the point of crossing along the water main.
* The water main shall be constructed of ductile iron pipe with gaskets impermeable to hydrocarbons, or
* The water main shall be enclosed in watertight casing pipe with an evenly spaced annular gap and watertight end seals, or
* Storm sewer pipe of water main material shall be installed, or
* Reinforced concrete pipe storm sewers shall be constructed with gaskets manufactured in accordance with ASTM C443.
* The water main shall be constructed of ductile iron pipe with gaskets impermeable to hydrocarbons, or
* The water main shall be enclosed in watertight casing pipe with an evenly spaced annular gap and watertight end seals, or
* Storm sewer pipe of water main material shall be installed, or
* Reinforced concrete pipe storm sewers shall be constructed with gaskets manufactured in accordance with ASTM C443.
Length of permitted water main | Rate |
First 1,000 ft. | $100 |
Next 19,000 ft. | $0.10/ft. |
Next 300,000 ft. | $0.01/ft. |
Over 320,000 ft. | No additional charge |
Estimated construction cost | Rate |
First $50,000 | $100 |
Next $950,000 | 0.2% of estimated construction cost |
Next $14,000,000 | 0.1% of estimated construction cost |
Over $15,000,000 | No additional charge |
Categories | Rate |
Change orders, addenda, and permit supplements for water mains | $0.10/ft. of additional water main, minimum fee: $50 |
Change orders, addenda, and permit supplements for non-water-main-related construction costs | 0.2% of additional non-water-main-related construction costs, minimum fee: $50 |
Request for time extension | $50 |
The additional users must have been included in the system's hydraulic analysis that has been approved by the department. The water demands of the additional users must be consistent with the water demands in the approved hydraulic analysis.
* An up-to-date hydraulic analysis of the system, prepared and submitted by a licensed professional engineer, must be either on file with the department or submitted with the permit application. The hydraulic basis of flow (gallons per minute per connection) used in the analysis must be acceptable to the department. The hydraulic analysis shall include:
* All existing water mains within the system;
* All proposed water mains intended to be covered by the permit;
* A demonstration that the system has adequate hydraulic capacity to serve the existing and new users under peak flow conditions without causing the pressure to fall below 20 psi anywhere within the system;
* The location of all potential users of the system;
* The diameter of all existing and proposed pipes;
* The projected system flows; and
* The static and dynamic pressures anticipated throughout the system with the addition of the new users incorporated in the analysis.
* A completed Schedule 1b, Minor Water Main Construction Permit Application (Form 542-3151), listed in 567-subrule 40.3(1).
However, if the proposed well is for an existing noncommunity water system and is replacing an existing well that either does not meet the current standards or is in poor condition, the requirement of 200-foot legal control may be waived by the department provided that:
* The proposed well is located on the best available site;
* The existing facility does not have adequate land to provide the 200-foot control zone;
* The owner has attempted to obtain legal control without success; and
* There is no other public water supply available to which the supply could connect.
After a surface water impoundment has received preliminary approval from the department for use as a raw water source, the owner of the water supply system shall submit proof of legal control through ownership, lease, easement, or other similar means, of contiguous land for a distance of 400 feet from the shoreline at the maximum water level. Legal control shall be for the life of the impoundment and shall control location of sources of contamination within the 400-foot distance. Proof of legal control should be submitted as part of the construction permit application and shall be submitted prior to issuance of a permit to construct.
Subsequent water testing shall be conducted consistent with the water system's water supply operation permit monitoring schedule.
TABLE A: SEPARATION DISTANCES
SOURCE OF CONTAMINATION | REQUIRED MINIMUM LATERAL DISTANCE FROM WELL AS HORIZONTAL ON THE GROUND SURFACE, IN FEET | |
Deep Well1 | Shallow Well1 | |
WASTEWATER STRUCTURES: | ||
Point of Discharge to Ground Surface | ||
Sanitary & industrial discharges | 400 | 400 |
Water treatment plant wastes | 50 | 50 |
Well house floor drains | 5 | 5 |
Sewers & Drains2 | ||
Sanitary & storm sewers, drains | 0 - 25 feet: prohibited 25 - 75 feet if water main pipe 75 - 200 feet if sanitary sewer pipe | 0 - 25 feet: prohibited 25 - 75 feet if water main pipe 75 - 200 feet if sanitary sewer main pipe |
Sewer force mains | 0 - 75 feet: prohibited 75 - 400 feet if water main pipe 400 - 1000 feet if sanitary sewer pipe | 0 - 75 feet: prohibited 75 - 400 feet if water main pipe 400 - 1000 feet if sanitary sewer main pipe |
Water plant treatment process wastes that are treated onsite | 0 - 5 feet: prohibited 5 - 50 feet if sanitary sewer pipe | 0 - 5 feet: prohibited 5 - 50 feet if sanitary sewer main pipe |
Water plant wastes to sanitary sewer | 0 - 25 feet: prohibited 25 - 75 feet if water main pipe 75 - 200 feet if sanitary sewer pipe | 0 - 25 feet: prohibited 25 - 75 feet if water main pipe 75 - 200 feet if sanitary sewer main pipe |
Well house floor drains to sewers | 0 - 25 feet: prohibited 25 - 75 feet if water main pipe 75 - 200 feet if sanitary sewer pipe | 0 - 25 feet: prohibited 25 - 75 feet if water main pipe 75 - 200 feet if sanitary sewer main pipe |
Well house floor drains to surface | 0 - 5 feet: prsohibited 5 - 50 feet if sanitary sewer pipe | 0 - 5 feet: prohibited 5 - 50 feet if sanitary sewer main pipe |
Land Disposal of Treated Wastes | ||
Irrigation of wastewater | 200 | 400 |
Land application of solid wastes3 | 200 | 400 |
Other | ||
Private sewage disposal systems and onsite treatment systems - open portion of treatment system4 | 200 | 400 |
Private sewage disposal systems and onsite treatment systems - closed portion of treatment system4 | 100 | 200 |
Lagoons | 400 | 1000 |
Mechanical wastewater treatment plants | 200 | 400 |
CHEMICALS: | ||
Chemical application to ground surface | 100 | 200 |
Chemical & mineral storage above ground5,6 | 100 | 200 |
Chemical & mineral storage on or under ground | 200 | 400 |
Transmission pipelines (such as fertilizer, liquid petroleum, or anhydrous ammonia) | 200 | 400 |
ANIMALS: | ||
Animal pasturage | 50 | 50 |
Animal enclosure | 200 | 400 |
Earthen silage storage trench or pit | 100 | 200 |
Animal Wastes | ||
Land application of liquid or slurry | 200 | 400 |
Land application of solids | 200 | 400 |
Solids stockpile | 200 | 400 |
Storage basin or lagoon | 400 | 1000 |
Storage tank | 200 | 400 |
MISCELLANEOUS: | ||
Basements, pits, sumps | 10 | 10 |
Cemeteries | 200 | 200 |
Cisterns | 50 | 100 |
Flowing streams or other surface water bodies | 50 | 50 |
GHEX loop boreholes | 200 | 200 |
Railroads | 100 | 200 |
Private wells | 200 | 400 |
Solid waste landfills and disposal sites7 | 1000 | 1000 |
1Deep and shallow wells, as defined in 567-40.2 (455B): A deep well is a well located and constructed in such a manner that there is a continuous layer of low permeability soil or rock at least 5 feet thick located at least 25 feet below the normal ground surface and above the aquifer from which water is to be drawn. A shallow well is a well located and constructed in such a manner that there is not a continuous layer of low permeability soil or rock (or equivalent retarding mechanism acceptable to the department) at least 5 feet thick, the top of which is located at least 25 feet below the normal ground surface and above the aquifer from which water is to be drawn.
2The separation distances are dependent upon two factors: the type of piping that is in the existing sewer or drain, as noted in the table, and that the piping was properly installed in accordance with the standards.
3Solid wastes are those derived from the treatment of water or wastewater. Certain types of solid wastes from water treatment processes may be land-applied within the separation distance on an individual, case-by-case basis.
4Private sewage disposal system is defined in 567-subrule 69.1(2). "Onsite treatment system" includes any wastewater treatment system not included in the definition of a private sewage disposal system that is utilizing onsite wastewater treatment technologies to treat domestic waste, such as those specified in 567-Chapter 69 (but excluding waste stabilization ponds). Open portions of treatment systems include subsurface absorption systems, mound systems, intermittent sand filters, constructed wetlands, open bottom media filters, and waste stabilization ponds. Closed portions of treatment systems include septic tanks, aerobic treatment units, fully contained media filters and impervious vault toilets. These separation distances also apply to septic systems that are not considered privately owned.
5The minimum separation distance for liquid fuel storage associated with standby power generators shall be 50 feet if secondary containment is provided. Secondary containment shall provide for a minimum of 110 percent of the liquid fuel storage capacity. Double-walled storage tanks shall not be considered as secondary containment. The separation distance for liquefied petroleum gas (LPG) storage shall be 15 feet.
6Electrical power transformers mounted on a single utility pole are exempt from the minimum separation distance requirements.
7Solid waste means garbage, refuse, rubbish, and other similar discarded solid or semisolid materials, including but not limited to such materials resulting from industrial, commercial, agricultural, and domestic activities.
ORGANIC CONTAMINANT | GAC | PTA | OXID |
Alachlor | x | ||
Aldicarb | x | ||
Aldicarb sulfone | x | ||
Aldicarb sulfoxide | x | ||
Atrazine | x | ||
Benzene | x | x | |
Benzo(a)pyrene | x | ||
Carbofuran | x | ||
Carbon tetrachloride | x | x | |
Chlordane | x | ||
2,4-D | x | ||
Dalapon | x | ||
Dibromochloropropane (DBCP) | x | x | |
o-Dichlorobenzene | x | x | |
p-Dichlorobenzene | x | x | |
1,2-Dichloroethane | x | x | |
cis-1,2-Dichloroethylene | x | x | |
trans-1,2-Dichloroethylene | x | x | |
1,1-Dichloroethylene | x | x | |
Dichloromethane | x | ||
1,2-Dichloropropane | x | x | |
Di(2-ethylhexyl)adipate | x | x | |
Di(2-ethylhexyl)phthalate | x | ||
Dinoseb | x | ||
Diquat | x | ||
Endothall | x | ||
Endrin | x | ||
Ethylene dibromide (EDB) | x | x | |
Ethylbenzene | x | x | |
Glyphosate | x | ||
Heptachlor | x | ||
Heptachlor epoxide | x | ||
Hexachlorobenzene | x | ||
Hexachlorocyclopentadiene | x | x | |
Lindane | x | ||
Methoxychlor | x | ||
Monochlorobenzene | x | x | |
Oxamyl (Vydate) | x | ||
Pentachlorophenol | x | ||
Picloram | x | ||
Polychlorinated biphenyls (PCB) | x | ||
Simazine | x | ||
Styrene | x | x | |
2,4,5-TP (Silvex) | x | ||
Tetrachloroethylene | x | x | |
1,2,4-Trichlorobenzene | x | x | |
1,1,1-Trichloroethane | x | x | |
1,1,2-Trichloroethane | x | x | |
Trichloroethylene | x | x | |
2,3,7,8-TCDD (Dioxin) | x | ||
Toluene | x | x | |
Toxaphene | x | ||
Vinyl chloride | x | ||
Xylene | x | x |
INORGANIC CHEMICAL | BAT(s) |
Antimony | 2, 7 |
Arsenicd | 1,2,5,6,7,9, 11e |
Asbestos | 2, 3, 8 |
Barium | 5, 6, 7, 9 |
Beryllium | 1, 2, 5, 6, 7 |
Cadmium | 2, 5, 6, 7 |
Chromium | 2, 5, 6b, 7 |
Cyanide | 5, 7, 12 |
Mercury | 2a, 4, 6a, 7a |
Nickel | 5, 6, 7 |
Nitrate | 5, 7, 9 |
Nitrite | 5, 7 |
Selenium | 1, 2c, 6, 7, 9 |
Thallium | 1,5 |
Key to BATs
1=Activated Alumina | 5=Ion Exchange | 9=Electrodialysis |
2=Coagulation/Filtration* | 6=Lime Softening* | 10=Chlorine |
3=Direct and Diatomite Filtration | 7=Reverse Osmosis | 11=Oxidation/Filtration |
4=Granular Activated Carbon | 8=Corrosion Control | 12=Alkaline Chlorination (pH greater than or equal to 8.5) |
*not BAT for systems with less than 500 service connections
aBAT only if influent Hg concentrations are less than or equal to 10 micrograms/liter.
bBAT for Chromium III only.
cBAT for Selenium IV only.
dBAT for Arsenic V. Preoxidation may be required to convert Arsenic III to Arsenic V.
eTo obtain high removals, iron to arsenic ratio must be at least 20:1.
SMALL SYSTEM COMPLIANCE TECHNOLOGIES FOR ARSENIC1
Technology | Affordable for listed small system categories2 |
Activated alumina | All size categories |
Coagulation/filtration3 | 501 - 3,300 and 3,301 - 10,000 |
Coagulation-assisted microfiltration | 501 - 3,300 and 3,301 - 10,000 |
Electrodialysis reversal4 | 501 - 3,300 and 3,301 - 10,000 |
Enhanced coagulation/filtration | All size categories |
Enhanced lime softening (pH >10.5) | All size categories |
Ion exchange | All size categories |
Lime softening3 | 501 - 3,300 and 3,301 . 10,000 |
Oxidation/filtration5 | All size categories |
Reverse osmosis4 | 501 - 3,300 and 3,301 . 10,000 |
1Technologies are for Arsenic V. Preoxidation may be required to convert Arsenic III to Arsenic V.
2There are three categories of small systems: those serving 25 to 500 people, those serving 501 to 3,300 people, and those serving 3,301 to 10,000 people.
3Unlikely to be installed solely for arsenic removal. May require pH adjustment to optimal range if high removals are needed.
4Technologies reject a large volume of water. May not be appropriate for areas where water quantity may be an issue.
5To obtain high removals, iron to arsenic ratio must be at least 20:1.
RADIONUCLIDE BAT
Contaminant | Best Available Technology |
Gross alpha particle activity (excluding radon and uranium) | Reverse osmosis |
Beta particle and photon radioactivity | Ion exchange, reverse osmosis |
Combined radium-226 and radium-228 | Ion exchange, reverse osmosis, lime softening |
Uranium | Ion exchange, reverse osmosis, lime softening, coagulation/filtration |
RADIONUCLIDES SMALL SYSTEM COMPLIANCE TECHNOLOGIES
Contaminant | Compliance Technologya |
Gross alpha particle activity | 2 |
Beta particle and photon radioactivity | 1, 2 |
Combined radium-226 and radium-228 | 1, 2, 3, 4, 5, 6, 7 |
Uranium | 1, 2b, 3b, 8, 9 |
aCompliance technologies are listed with their corresponding number and potential limitations for use, as follows:
1: Ion exchange. The regeneration solution contains high concentrations of the contaminant ions. Disposal options should be carefully considered before choosing this technology.
2: Reverse osmosis. Reject water disposal options should be carefully considered before choosing this technology.
3: Lime softening. The complexity of the water chemistry may make this technology too complex for small systems.
4: Green sand filtration. Removal efficiencies can vary depending on water quality.
5: Coprecipitation with barium sulfate. This technology has limited applications to small systems, and is most applicable to systems with sufficiently high sulfate levels that already have a suitable filtration treatment train in place.
6: Electrodialysis/electrodialysis reversal.
7: Pre-formed hydrous manganese oxide filtration. This technology is most applicable to small systems that have existing filtration technology.
8: Activated alumina. The regeneration solution contains high concentrations of the contaminant ions. Disposal options should be carefully considered before choosing this technology. Handling of chemicals required during regeneration and pH adjustment requires an adequately trained operator.
9: Enhanced coagulation/filtration. This technology assumes that it is a modification to an existing coagulation/filtration process.
bNot recommended for systems serving 25 to 500 persons.
DBP MCL or MRDL | Best Available Technology |
Bromate MCL | Control of ozone treatment process to reduce production of bromate |
Chlorite MCL | Control of treatment processes to reduce disinfectant demand and control of disinfection treatment processes to reduce disinfectant levels |
HAA5 and TTHM MCL running annual average | Enhanced coagulation or enhanced softening or GAC10, with chlorine as the primary and residual disinfectant |
HAA5 and TTHM MCL LRAA | * Non-consecutive system: Enhanced coagulation or enhanced softening, plus GAC10; or nanofiltration with a molecular weight cutoff that is less than or equal to 1000 Daltons; or GAC20 * Consecutive system serving at least 10,000 persons*: Improved distribution system and storage tank management to reduce residence time, plus the use of chloramines for disinfectant residual maintenance * Consecutive system serving fewer than 10,000 persons*: Improved distribution system and storage tank management to reduce residence time |
MRDL | Control of treatment processes to reduce disinfectant demand and control of disinfection treatment processes to reduce disinfectant levels |
* Applies only to the disinfected water that consecutive systems buy or otherwise receive.
Iowa Admin. Code r. 567-43.3