01.
General Equipment Design.
General equipment design shall be such that: (3-24-22)
a. Feeders will be able to supply, at all
times, the necessary amounts of chemicals at an accurate rate, throughout the
range of feed. (3-24-22)
b.
Chemical-contact materials and surfaces are resistant to the aggressiveness of
the chemical solution. (3-24-22)
c.
Corrosive chemicals are introduced in such a manner as to minimize potential
for corrosion. (3-24-22)
d.
Chemicals that are incompatible are not stored or handled together. At
facilities where more than one (1) chemical is stored or handled, tanks and
pipelines shall be clearly labeled to identify the chemical they contain.
(3-24-22)
e. All chemicals are
conducted from the feeder to the point of application in separate conduits.
(3-24-22)
f. Chemical feeders are
as near as practical to the feed point. (3-24-22)
g. Chemical feeders and pumps shall operate
at no lower than twenty percent (20%) of the feed range unless two fully
independent adjustment mechanisms such as pump pulse rate and stroke length are
fitted when the pump shall operate at no lower than ten percent (10%) of the
rated maximum. (3-24-22)
h. Spare
parts shall be on hand for parts of feeders that are subject to frequent wear
and damage. (3-24-22)
i. Redundant
chemical feeders with automatic switchover shall be provided when necessary to
ensure adequate treatment. If the water treatment system includes at least two
(2) process trains of equipment so that the plant design capacity can be
maintained with any component out of service, redundant chemical feeders are
not required on each process train. (3-24-22)
02.
Facility Design. (3-24-22)
a. Where chemical feed is necessary for the
protection of the supply, such as disinfection, coagulation or other essential
processes, a minimum of two feeders shall be provided and a separate feeder
shall be used for each chemical applied. (3-24-22)
b. Chemical application control systems shall
meet the following requirements: (3-24-22)
i.
Feeders may be manually or automatically controlled, with automatic controls
being designed so as to allow override by manual controls. (3-24-22)
ii. Chemical feeders shall be controlled by a
flow sensing device so that injection of the chemicals will not continue when
the flow of water stops. (3-24-22)
iii. Automatic proportioning chlorinators are
required where the rate of flow or chlorine demand is not reasonably constant.
(3-24-22)
iv. A means to measure
water flow must be provided in order to determine chemical feed rates.
(3-24-22)
v. Provisions shall be
made for measuring the quantities of chemicals used. (3-24-22)
vi. Weighing scales shall be provided for
weighing cylinders at all plants utilizing chlorine gas, fluoride solution
feed. (3-24-22)
vii. Weighing
scales shall be capable of providing reasonable precision in relation to
average daily dose. (3-24-22)
viii.
Where conditions warrant, for example with rapidly fluctuating intake
turbidity, coagulant and coagulant aid addition may be made according to
turbidity, streaming current or other sensed parameter.
(3-24-22)
c. Dry chemical
feeders shall measure chemicals volumetrically or gravimetrically, provide
adequate solution water and agitation of the chemical in the solution pot, and
completely enclose chemicals to prevent emission of dust to the operating room.
(3-24-22)
d. Positive displacement
type solution feed pumps must be capable of operating at the required maximum
head conditions found at the point of injection. (3-24-22)
e. Liquid chemical feeders shall be such that
chemical solutions cannot be siphoned or overfed into the water supply, by
assuring discharge at a point of positive pressure, or providing vacuum relief,
or providing a suitable air gap, or providing other suitable means or
combinations as necessary. (3-24-22)
f. Cross connection control must be provided
to assure that the following requirements are satisfied. (3-24-22)
i. The service water lines discharging to
solution tanks shall be properly protected from backflow. (3-24-22)
ii. No direct connection exists between any
sewer and a drain or overflow from the feeder, solution chamber or tank by
providing that all drains terminate at least six (6) inches or two pipe
diameters, whichever is greater, above the overflow rim of a receiving sump,
conduit or waste receptacle. (3-24-22)
g. Chemical feed equipment shall be readily
accessible for servicing, repair, and observation of operation.
(3-24-22)
h. In-plant water supply
for chemical mixing shall be: (3-24-22)
i.
Ample in quantity and adequate in pressure. (3-24-22)
ii. Provided with means for measurement when
preparing specific solution concentrations by dilution. (3-24-22)
iii. Properly treated for hardness, when
necessary. (3-24-22)
iv. Properly
protected against backflow. (3-24-22)
v. Obtained from a location sufficiently
downstream of any chemical feed point to assure adequate mixing.
(3-24-22)
i. Chemical
storage facilities shall satisfy the following requirements: (3-24-22)
i. Storage tanks and pipelines for liquid
chemicals shall be specified for use with individual chemicals and not used for
different chemicals. Off-loading areas must be clearly labeled to prevent
accidental crosscontamination. (3-24-22)
ii. Chemicals shall be stored in covered or
unopened shipping containers, unless the chemical is transferred into an
approved storage unit. (3-24-22)
j. Bulk liquid storage tanks shall comply
with the following requirements: (3-24-22)
i.
A means which is consistent with the nature of the chemical solution shall be
provided in a solution tank to maintain a uniform strength of solution.
Continuous agitation shall be provided to maintain slurries in suspension.
(3-24-22)
ii. Means shall be
provided to measure the liquid level in the tank. (3-24-22)
iii. Bulk liquid storage tanks shall be kept
covered. Bulk liquid storage tanks with access openings shall have such
openings curbed and fitted with overhanging covers. (3-24-22)
iv. Subsurface locations for bulk liquid
storage tanks shall be free from sources of possible contamination, and assure
positive drainage for ground waters, accumulated water, chemical spills and
overflows. (3-24-22)
v. Bulk liquid
storage tanks shall be vented, but shall not vent through vents common with day
tanks. Acid storage tanks must be vented to the outside atmosphere, but not
through vents in common with day tanks. (3-24-22)
vi. Each bulk liquid storage tank shall be
provided with a valved drain, protected against backflow. (3-24-22)
vii. Bulk liquid storage tanks shall have an
overflow that is turned downward with the end screened with a twenty-four (24)
mesh or similar non-corrodible screen, have a free fall discharge, and be
located where noticeable. (3-24-22)
viii. Bulk liquid storage tanks shall be
provided with secondary containment so that chemicals from equipment failure,
spillage, or accidental drainage shall be fully contained. A common receiving
basin may be provided for each group of compatible chemicals. The bulk liquid
storage tank basin or the common receiving basin shall provide a secondary
containment volume sufficient to hold one hundred ten percent (110%) of the
volume of the largest storage tank. Piping shall be designed to minimize or
contain chemical spills in the event of pipe ruptures. (3-24-22)
ix. Where chemical feed is necessary for the
protection of the supply, a means to assure continuity of chemical supply while
servicing a bulk liquid storage tank shall be provided.
(3-24-22)
k. Day tanks
are subject to the requirements in Subsections
531.02.k.i. through
531.02.k.iv. For the purposes of Section
531, day tanks are defined as
liquid chemical tanks holding no more than a thirty (30) hour chemical supply.
(3-24-22)
i. Day tanks shall be provided
where bulk storage of liquid chemicals are provided. The Department may allow
chemicals to be fed directly from shipping containers no larger than fifty-five
(55) gallons. (3-24-22)
ii. Day
tanks shall meet all the requirements of Subsection
531.02.j., with the exception
of Subsection 531.02.j.viii. Shipping
containers do not require overflow pipes or drains as required by Subsection
531.02.j. and are not subject
to the requirements of Subsection
531.02j.viii.
(3-24-22)
iii. Where feasible,
secondary containment shall be provided so that chemicals from equipment
failure, spillage, or accidental drainage of day tanks shall be fully
contained. A common receiving basin may be provided for each group of
compatible chemicals. The common receiving basin shall provide a secondary
containment volume sufficient to hold the volume of the largest storage tank.
If secondary containment is not feasible, day tanks shall be located and
protective curbings provided so that chemicals from equipment failure,
spillage, or accidental drainage of day tanks shall not enter the water in
conduits, treatment, or storage basins. Secondary containment is not required
for a day tank if an Idaho licensed professional engineer demonstrates to the
Department that the chemical concentration and volume, if spilled, will not be
a safety hazard to employees, will not be hazardous to the public health, and
will not harm the environment. (3-24-22)
iv. Day tanks and the tank refilling line
entry points shall be clearly labeled with the name of the chemical contained.
(3-24-22)
l. Provisions
shall be made for measuring quantities of chemicals used to prepare feed
solutions. (3-24-22)
m. Vents from
feeders, storage facilities and equipment exhaust shall discharge to the
outside atmosphere above grade and remote from air intakes.
(3-24-22)
03.
Chemicals. Chemical shipping containers shall be fully labeled to
include chemical name, purity and concentration, supplier name and address, and
evidence of ANSI/NSF certification where applicable. (3-24-22)
04.
Safety Requirements for Chemical
Facilities. (3-24-22)
a. The following
requirements apply to chlorine gas feed and storage rooms: (3-24-22)
i. Each storage room shall be enclosed and
separated from other operating areas. They shall be constructed in such a
manner that all openings between the chlorine room and the remainder of the
plant are sealed, and provided with doors equipped with panic hardware,
assuring ready means of exit and opening outward only to the building exterior.
(3-24-22)
ii. Each room shall be
provided with a shatter resistant inspection window installed in an interior
wall. (3-24-22)
iii. Each room
shall have a ventilating fan with a capacity which provides one (1) complete
air change per minute when the room is occupied. Where this is not appropriate
due to the size of the room, a lesser rate may be allowed by the Department on
a site specific basis. (3-24-22)
iv. The ventilating fan shall take suction
near the floor as far as practical from the door and air inlet, with the point
of discharge so located as not to contaminate air inlets to any rooms or
structures. Air inlets shall be through louvers near the ceiling.
(3-24-22)
v. Louvers for chlorine
room air intake and exhaust shall facilitate airtight closure.
(3-24-22)
vi. Separate switches for
the fan and lights shall be located outside of the chlorine room and at the
inspection window. Outside switches shall be protected from vandalism. A signal
light indicating fan operation shall be provided at each entrance when the fan
can be controlled from more than one (1) point. (3-24-22)
vii. Vents from feeders and storage shall
discharge to the outside atmosphere, above grade. (3-24-22)
viii. Where provided, floor drains shall
discharge to the outside of the building and shall not be connected to any
internal drainage systems or external drainage systems unless the external
drainage systems drain to an approved discharge point. (3-24-22)
ix. Chlorinator rooms shall be heated to
sixty degrees Fahrenheit (60°F) and be protected from excessive heat.
Cylinders and gas lines shall be protected from temperatures above that of the
feed equipment. (3-24-22)
x.
Pressurized chlorine feed lines shall not carry chlorine gas beyond the
chlorinator room. (3-24-22)
xi.
Critical isolation valves shall be conspicuously marked and access kept
unobstructed. (3-24-22)
xii. All
chlorine rooms, buildings, and areas shall be posted with a prominent danger
sign warning of the presence of chlorine. (3-24-22)
xiii. Full and empty cylinders of chlorine
gas shall be isolated from operating areas and stored in definitely assigned
places away from elevators, stairs, or gangways. They shall be restrained in
position to prevent being knocked over or damaged by passing or falling
objects. In addition, they shall be stored in rooms separate from ammonia
storage, out of direct sunlight, and at least twenty (20) feet from highly
combustible materials. Cylinders shall not be kept in unventilated enclosures
such as lockers and cupboards. (3-24-22)
b. Where acids and caustics are used, they
shall be kept in closed corrosion-resistant shipping containers or storage
units. Acids and caustics shall not be handled in open vessels, but shall be
pumped in undiluted form from original containers through suitable hose to the
point of treatment or to a covered day tank. (3-24-22)
c. Sodium chlorite for chlorine dioxide
generation. Proposals for the storage and use of sodium chlorite shall be
approved by the Department prior to the preparation of final plans and
specifications. Provisions shall be made for proper storage and handling of
sodium chlorite to eliminate any danger of fire or explosion associated with
its oxidizing nature. (3-24-22)
i. Chlorite
(sodium chlorite) shall be stored by itself in a separate room. It must be
stored away from organic materials. The storage structure shall be constructed
of noncombustible materials. If the storage structure must be located in an
area where a fire may occur, water must be available to keep the sodium
chlorite area cool enough to prevent heat-induced explosive decomposition of
the chlorite. (3-24-22)
ii. Care
shall be taken to prevent spillage. An emergency plan of operation shall be
available for the clean up of any spillage. Storage drums shall be thoroughly
flushed prior to recycling or disposal. (3-24-22)
d. Where ammonium hydroxide is used, an
exhaust fan shall be installed to withdraw air from high points in the room and
makeup air shall be allowed to enter at a low point. The feed pump, regulators,
and lines shall be fitted with pressure relief vents discharging outside the
building away from any air intake and with water purge lines leading back to
the headspace of the bulk storage tank. (3-24-22)
e. Where anhydrous ammonia is used, the
storage and feed systems (including heaters where required) shall be enclosed
and separated from other work areas and constructed of corrosion resistant
materials. (3-24-22)
i. Pressurized ammonia
feed lines shall be restricted to the ammonia room. (3-24-22)
ii. An emergency air exhaust system, as
described in Subsection
531.04.a., but with an
elevated intake, shall be provided in the ammonia storage room.
(3-24-22)
iii. Leak detection
systems shall be fitted in all areas through which ammonia is piped.
(3-24-22)
iv. Special vacuum
breaker/regulator provisions must be made to avoid potentially violent results
of backflow of water into cylinders or storage tanks. (3-24-22)
v. Consideration shall be given to the
provision of an emergency gas scrubber capable of absorbing the entire contents
of the largest ammonia storage unit whenever there is a risk to the public as a
result of potential ammonia leaks. (3-24-22)
05.
Operator Safety. The Idaho
General Safety and Health Standards, referenced in Subsection
002.02, may be used as guidance
in designing facilities to ensure the safety of operators. The following
requirements are in addition to the requirements of Subsection
501.12. (3-24-22)
a. Respiratory protection equipment, meeting
the requirements of the National Institute for Occupational Safety and Health
(NIOSH) shall be available where chlorine gas is handled, and shall be stored
at a convenient heated location, but not inside any room where chlorine is used
or stored. The units shall use compressed air, have at least a thirty (30)
minute capacity, and be compatible with or exactly the same as units used by
the fire department responsible for the plant. (3-24-22)
b. Chlorine leak detection. A bottle of
concentrated ammonium hydroxide (fifty-six (56) per cent ammonia solution)
shall be available for chlorine leak detection. Where ton containers are used,
a leak repair kit approved by the Chlorine Institute shall be provided.
(3-24-22)
c. Protective equipment.
(3-24-22)
i. At least one pair of rubber
gloves, a dust respirator of a type certified by NIOSH for toxic dusts, an
apron or other protective clothing, and goggles or face mask shall be provided
for each operator. (3-24-22)
ii. A
deluge shower and eyewashing device shall be installed where strong acids and
alkalis are used or stored. A water holding tank that will allow water to come
to room temperature shall be installed in the water line feeding the deluge
shower and eyewashing device. Other methods of water tempering will be
considered on an individual basis. (3-24-22)
iii. For chemicals other than strong acids
and alkalis, an appropriate eye washing device or station shall be provided.
(3-24-22)
iv. Other protective
equipment shall be provided as necessary.
(3-24-22)
06.
Design Requirements for Specific Applications. In addition to
Subsection 531.01 through
531.03, the following design
requirements apply for the specific applications within Subsection
531.06 of this rule. (3-24-22)
a. Sodium chlorite for chlorine dioxide
generation. Positive displacement feeders shall be provided. Tubing for
conveying sodium chlorite or chlorine dioxide solutions shall be Type 1 PVC,
polyethylene or materials recommended by the manufacturer. Chemical feeders may
be installed in chlorine rooms if sufficient space is provided. Otherwise,
facilities meeting the requirements of chlorine rooms shall be provided. Feed
lines shall be installed in a manner to prevent formation of gas pockets and
shall terminate at a point of positive pressure. Check valves shall be provided
to prevent the backflow of chlorine into the sodium chlorite line.
(3-24-22)
b. Hypochlorite
facilities shall meet the following requirements: (3-24-22)
i. Hypochlorite shall be stored in the
original shipping containers or in hypochlorite compatible containers. Storage
containers or tanks shall be sited out of the sunlight in a cool and ventilated
area. (3-24-22)
ii. Stored
hypochlorite shall be pumped undiluted to the point of addition. Where dilution
is unavoidable, deionized or softened water shall be used. (3-24-22)
iii. Storage areas, tanks, and pipe work
shall be designed to avoid the possibility of uncontrolled discharges and a
sufficient amount of appropriately selected spill absorbent shall be stored
on-site. (3-24-22)
iv. Hypochlorite
feeders shall be positive displacement pumps with compatible materials for
wetted surfaces. (3-24-22)
v. To
avoid air locking in smaller installations, small diameter suction lines shall
be used with foot valves and degassing pump heads. In larger installations
flooded suction shall be used with pipe work arranged to ease escape of gas
bubbles. Calibration tubes or mass flow monitors which allow for direct
physical checking of actual feed rates shall be fitted. (3-24-22)
vi. Injectors shall be made removable for
regular cleaning where hard water is to be treated.
(3-24-22)
c. When
ammonium sulfate is used, the tank and dosing equipment contact surfaces shall
be made of corrosion resistant non-metallic materials. Provision shall be made
for removal of the agitator after dissolving the solid. The tank shall be
fitted with a lid and vented outdoors. Injection of the solution should take
place in the center of treated water flow at a location where there is high
velocity movement. (3-24-22)
d.
When aqua ammonia (ammonium hydroxide) is used, the feed pumps and storage
shall be enclosed and separated from other operating areas. The aqua ammonia
room shall be equipped as required for chlorinator rooms with the following
changes: (3-24-22)
i. A corrosion resistant,
closed, unpressurized tank shall be used for bulk storage, vented through an
inert liquid trap to a high point outside and an incompatible connector, or
lockout provisions shall be made to prevent accidental addition of other
chemicals to the storage tank. (3-24-22)
ii. The storage tank shall be designed to
avoid conditions where temperature increases cause the ammonia vapor pressure
over the aqua ammonia to exceed atmospheric pressure. This capability can be
provided by cooling/refrigeration or diluting or mixing the contents with water
without opening the system. (3-24-22)
iii. The aqua ammonia shall be conveyed
direct from storage to the treated water stream injector without the use of a
carrier water stream unless the carrier stream is softened. (3-24-22)
iv. The point of delivery to the main water
stream shall be placed in a region of turbulent water flow. (3-24-22)
v. Provisions shall be made for easy access
for removal of calcium scale deposits from the injector.
(3-24-22)