Illinois Administrative Code
Title 35 - ENVIRONMENTAL PROTECTION
Part 370 - ILLINOIS RECOMMENDED STANDARDS FOR SEWAGE WORKS
Subpart J - DISINFECTION
Section 370.1020 - Chlorine Disinfection
Current through Register Vol. 48, No. 38, September 20, 2024
a) Type of Feed Equipment
The types of chlorine feed equipment include:
b) Selection of Feed Equipment
The selection of the type of chlorine feed equipment shall take into account operator safety and overall public safety relative to the proximity of the sewage treatment plant to populated areas and to the security of the gas cylinder or container storage.
c) Output Capacity of Gas Chlorine Cylinders
Delivery Rates (lbs of chlorine/day) |
|||
Ambient Temp. °F |
100 pound Cylinder |
150 pound Cylinder |
1 Ton Container |
40 |
6 |
9 |
100 |
50 |
14 |
21 |
240 |
60 |
23.7 |
35.5 |
385 |
70 |
32 |
47.5 |
536 |
80 |
41.2 |
62 |
700 |
Some types of vacuum chlorinators can deliver chlorine at rates greater than those listed above under the same conditions. When designs include rates in excess of those indicated above, manufacturer's specifications and test results shall be provided.
d) Standby Equipment and Spare Parts
Standby equipment of sufficient capacity should be available to replace the largest unit during shutdowns. Spare parts shall be available for all chlorinators to replace parts which are subject to wear and breakage.
e) Potable Water Supply Protection
An ample supply of water shall be available for operating the chlorinator. Where a booster pump is required, duplicate equipment should be provided and, when necessary, also standby power (refer to Section 370.550(a)(4) ) . Protection of a potable water supply shall conform to the requirements of Section 370.550(b)(3). In-line backflow preventers are not acceptable.
f) Chlorine Gas Supply
The use of 1-ton containers should be considered where the average daily chlorine gas consumption is over 150 pounds. All upright chlorine cylinders shall be strapped securely to prevent tipping.
Where manifolding of several cylinders or containers will be required to evaporate sufficient chlorine, consideration should be given to liquid drawoff and installation of an evaporator.
A bottle of ammonium hydroxide solution should be available for detecting chlorine leaks. Consideration should also be given to the provision of caustic soda solution reaction tanks for absorbing the contents of leaking 1-ton containers where such containers are in use. Also, when cylinders, containers or tank cars are used, a leak repair kit approved by the Chlorine Institute shall be provided. At installations using over 150 pounds of chlorine gas per day consideration should be given to the installation of automatic gas detection and related alarm equipment.
g) Piping and Connections
h) Housing
Containers and feed equipment should be located indoors, in a suitable fire-resistant building. Gas cylinders should be protected from direct sunlight if not located indoors.
If gas chlorination equipment and chlorine cylinders or containers are to be housed in a building used for other purposes, the chlorine cylinders or containers and equipment shall be located in an isolated room. This room shall not contain any sulfonation equipment, sulfur dioxide cylinders or other equipment unrelated to chlorination. Common walls to other areas of the building shall be gastight. Doors to this room shall open only to the outside of the building and shall be equipped with panic hardware. Rooms shall be at ground level and shall permit easy access to all equipment. Storage areas should be separated from the feed area.
A clear gastight window shall be installed in the chlorinator room to permit the units to be viewed and gauges to be read without entering the room.
Chlorinator housing facilities shall be provided with a means of heating so that a temperature of at least 60° F can be maintained. Where chlorine gas is to be withdrawn from cylinders or containers, the cylinders or containers shall be maintained at essentially room temperature. The room shall be protected from excessive heat. If liquid chlorine is to be withdrawn from the cylinders or containers to an evaporator unit, the feed cylinders or containers may be located in an unheated area.
The controls for the fans and lights shall be provided at those locations where it is necessary to enter the chlorination room and shall automatically operate when the door is opened and continue to operate when the operator enters the room and the door is closed. Provision shall be made for manual operation of controls from the outside of the room without opening the door.
Outdoor shallow cabinet-type units, with wide opening doors, that are shallow enough not to need or require operator entry, may be used to house the containers and feed equipment. Use of such cabinets shall be limited to small plants that provide seasonal disinfection or use less than 10 pounds of chlorine per day. Only two chlorine gas cylinders of 150 pounds or less on line may be housed in the cabinets. The following items shall be provided for in the design:
i) Respiratory Protection Equipment
Respiratory protection equipment meeting the requirements of the National Institute for Occupational Safety and Health (NIOSH) shall be available at all installations where chlorine gas is handled and shall be stored in a convenient location outside of any room where chlorine is used or stored. The respiratory protection units shall use compressed air, have at least a 30-minute capacity, and be compatible with or exactly the same as NIOSH-approved units used by the local fire department. Instructions for using, testing, and replacing mask parts shall be posted. At large installations, consideration should be given to providing acid suits and fire suits.
j) Application of Chlorine
After thorough mixing, a minimum contact period of 15 minutes at design peak hourly flow or maximum rate of pumpage shall be provided.
Chlorinators shall be designed to have a capacity adequate to produce an effluent that will meet the applicable bacterial limits. Where necessary to meet the operating ranges, multiple units shall be provided for adequate peak capacity and for a sufficiently low feed rate on turn down to allow proper chlorine residual. The chlorination system shall be designed on a rational basis and calculations justifying the equipment sizing and number of units shall be submitted for the whole operating range of flow rates, including the minimum turn down capacity for the type of control to be used. System design considerations shall include the controlling sewage flow meter (sensitivity and location), telemetering equipment and chlorinator controls. For treated normal domestic sewage the following dosing capacity, based on design average flow, is suggested (see Section 370.520(c)(1) ) :
Type of Treatment |
Dosage (mg/l) |
|
Primary Settled Sewerage |
20 |
|
Lagoon Effluent (unfiltered) |
20 |
|
Trickling Filter Plant Effluent |
10 |
|
Lagoon Effluent (filtered) |
10 |
|
Activated Sludge Plant Effluent |
6 |
|
Activated Sludge Plants with Chemical Addition |
4 |
|
Filtered Effluent Following Mechanical Biological Treatment |
4 |
k) Contact Tank