Sop mpcb etp

O & M RELATED ETP COMPONENTS .................................................................... 7
O & M REQUIREMENT IDENTIFICATION................................................................. 8
ETP O & M STAFF REQUIREMENTS ...................................................................... 9
ETP STAFF COMPETENCY .................................................................................... 11
ETP STAFF TRAINING ............................................................................................. 14
GUIDELINES FOR SAFETY IN ETP OPERATION.................................................. 17
Hazard Identification ................................................................................................. 17
Dos and Don’ts in ETP Operation for Safety ............................................................. 18
Personnel Protective Equipment (PPE) for ETP O & M............................................. 19
Safe Handling of Chemicals ...................................................................................... 20
Safe Handling of Chlorine ......................................................................................... 21
Safety in Handling of Corrosive substances such as Acids, Alkalis........................... 25
PLANT PERFORMANCE MONITORING................................................................. 30
GUIDELINES FOR RECORD KEEPING.................................................................. 32
CRITERIA FOR APPOINTING OPERATION & MAINTENANCE AGENCY ........... 38
Statutory registrations & clearance certificates - MUST .............................................38
Financial requirement (minimum) ................................................................................39
Experience (minimum) ................................................................................................39
INDEX

7
The components of ETP that need O & M are :
y HT Receiving / LT Sub-station including Transformer
y Coarse Bar Screens
y Equalization basins / Raw Effluent Sump (Wet Well)
y Raw Effluent Pumping Station (Dry Well)
y Raw Effluent Pumps and Motors
y Fine Screens
y Grit Removing Channel
y Grit Removing Mechanism
y Flow Distribution Chamber
y Primary Settling Tank including sludge scrapers
y Primary Sludge Sump (Wet Well)
y Primary Sludge Pumping Station (Dry Well)
y Primary Sludge Pump (s)
y Anaerobic Sludge Digester (s)
y Aerobic Treatment Processes
§ Trickling Filter (s)
§ Rotating Biological Discs/ Oxidation Ditch(es) / Carrousal(s)
§ Aerated Lagoons using Mechanical Aerators (Floating / Fixed)
§ Aeration Tanks using Mechanical Aerators (Floating/Fixed) or Diffused Air
y Secondary Settling Tank (s)
y Secondary Sludge Sump (s) (Wet Well)
y Secondary Sludge Pumping Station (Dry Well)
y Secondary Sludge Handling Pumps
y Sludge Thickener (s)
y Sludge Drying Beds
y Plant Laboratory for testing of Environmental Parameters of pollution
y Treated Effluent Channel to the outfall stream
O & M Related ETP Components

8
An ETP installation needs to equip itself with proper protocol for O & M. The first step
in preparation for O & M is preparing inventory of maintenance requirements. This
inventory is generally included in the Operation & Maintenance (O&M) Manual written
down for the installation by the contractor who designs and builds the installation. He
on completion of the work hands over this manual to the Principal for whom he builds
the installation.
The following sections of the O & M Manual would lay down the maintenance require-
ments:
1. Maintenance of Equipment: This section provides schedules that list periodic
maintenance requirements for the various equipments and also includes record-keep-
ing forms as necessary.A list of equipment suppliers and service representatives along
with telephones is also given therein. Also, the manufacturer’s O&M requirement is
provided in this section. The ETP maintenance staff / the Operation & Maintenance
contractor should particularly review this section of the O&M Manual.
2. Storeroom and Spare Parts Inventory: It includes a list of critical replacement
parts that may have long delivery times associated with them.Contact details of manu-
facturers or dealers of various equipment used in the installation, who are located
nearby is helpful in seeking recommendations/ guidance. This section also indicates
where the spares are to be stored. To optimise spare parts inventory, the ETP Staff/
O&M Contractor can make/ procure computerized maintenance software programs to
help keep track of spares, supplies and lubricants.
3. Manufacturer’s O&M Literature. In the O & M manual, cut-sheets and other
manufacturer’s literature are also contained.
ETP staff/ O & M Contractor should familiarize itself with all these documents to ensure
proper planning and execution of O & M activities.
In case these documents are not available the same should be prepared based on
study of the plant, process, equipments, past experience, and interaction with manu-
facturers/suppliers.
O & M Requirement Identification

9
The manpower requirement for ETP O & M can broadly be listed as follows:
Plant Manager: is an individual with environmental engineering or science background
with experience of at least three years on similar plant(s). He must have thorough
understanding of unit operations and application of microbiology and environmental
chemistry in the effluent/ sewage treatment. He should be able to take decisions to
divert / bypass/ distribute the flow in the event of disruptions / breakdown of mechani-
cal or electrical equipment until resumption is in place and repairs / replacements are
successfully carried out. He should understand and be able to plan a forecast and use
of chemicals / nutrients for the plant operations and the laboratory. He should be well
versed in working out dosages of chemicals and nutrients based on the raw effluent
quality and change it as the treatment progresses and results start forthcoming. AS
ETP Manager, he should prepare a weekly roster of duties for each individual and
broadly lay down in writing the duties and responsibilities of each category of staff. He
should ensure that the staff on plant should get rotated in various shifts during each
month. Needless to mention that he is the backbone of ETP operation.
Plant Operator(s): comprise a team of qualified / trained operators who work in shifts
in operating and maintaining screens, grit removal devices, pumps, aerators, valves,
etc. in directing the effluent and settled sludge to various units for / after treatment.
They should be able to sense troubles and act as ears and eyes of the Plant manager.
They should also assist the electrical / mechanical maintenance technician(s) in carry-
ing out the preventive and breakdown maintenance tasks.
Electrical / Mechanical Technician (s): form team of qualified maintenance techni-
cians with the ability and experience of diagnosing health of equipment and motors
with the aim of taking these on for preventive maintenance, assigning causes and
reasons for faults and ultimate failure, quickly carrying out minor repairs / replace-
ments by reaching, removing, stripping / opening, repairing, assembling of routine
electrical and mechanical machines / equipment including piping and valves.
Laboratory Analyst: is a qualified individual who has knowledge of water and waste
water chemistry and is trained in preparation of laboratory chemicals, use of laboratory
instruments, collection and preservation of water / waste water samples and analysis
for various environmental parameters such as pH, SS, BOD, COD, TDS etc.
ETP O & M Staff Requirements

10
Labour / Helpers: In addition to the above trades, labour / helpers are required to
assist the above individuals and upkeep and maintenance of the various units, struc-
tures, areas, floors, rooms, equipment, tanks, vessels, beds etc. and removal, loading,
haulage/carriage of wastes, screenings, stores and chemicals and other such material
as the need be.
It is essential that each ETP staff shall be well trained in related tasks and be equipped
in resources such as tools, spares and tackles.
ETP O & M skills are acquired mostly through on-job training.Trainees usually start as
attendants or operators-in-training and learn their skills on the job under the direction
of an experienced operator. They learn by observing and doing routine tasks such as
recording meter readings, taking samples of liquid waste and sludge, and performing
simple maintenance and repair work on pumps, electric motors, valves, and other plant
equipment. ETP Operators need mechanical aptitude and should have knowledge of
basic mathematics, chemistry, and biology. They must have the ability to apply data to
formulas prescribing treatment requirements, flow levels, and concentration levels.
ETP operation is a team work. It requires proper team selection, training need assess-
ment, training, on-job moulding, laboratory and statistical analysis for ensuring desired
performance, trouble forecasting and trouble shooting. O & M staff profile should ad-
dress all these requirements.
Since it is not feasible to position a Repair/Maintenance Shop at the site to carry out
major overhauls / repairs to electrical and mechanical equipment, it is essential to
identify back-up workshop facilities. A good ETP operating contractor may have his
own central resources in place within workable co-ordinates which will help to carry
out such heavy repairs and maintenance or he may have agreement to move such
resources, own or from trade, to the site with matching capability to establish tempo-
rarily for completion of task.This should be taken in to account if ETP operation is to be
outsourced.

11
ETP Staff Competency
1. Plant Manager:
a) A Post -graduate in Environmental Sciences or a Graduate Environmental
Engineer / Chemical Engineer with one year experience or a Diploma in
Environmental / Chemical Engineering/ Graduate in Environmental Sciences
/Microbiology with three years experience in an in Maintenance or Design of
ETP
b) Should be physically fit and mentally alert.
c) Should accept tasks allotted by higher offices and complete these without
any further guidance as also have own initiative to find, assign and super-
vise tasks to his own subordinates to achieve goals assigned to him by the
organization.
d) Should have worked / trained on the operation of a Sewage / Effluent Treat-
ment Plant for at least one year.
e) Should have attended and participated in a training /refresher course in Ef-
fluent Treatment Design/Operation.
2. Plant Operator (s):
a) Should be at least a High School Pass with sciences and be physically fit
and mentally alert.
b) Should have attended and passed an ITI trade.
c) Should accept assigned tasks willingly and complete these without any
further guidance as also have initiative to find work and willingly under-
take it on his own for the betterment / achievement of organizational
goals.
d) Should have attended training / refresher course for personnel working
on a Effluent Treatment Plant operation.
e) Should have at-least one year experience in the operation of Pumps and
Valves at a Pumping Installation.

12
f) Or should have been a helper for five years and helped Electrical / Me-
chanical maintenance teams for at least three years.
3. Electrical / Mechanical Technician (s):
a) Should be at least an SSC Pass with Sciences and be physically fit and
mentally alert.
b) Should accept assigned tasks willingly and complete these without any
further guidance as also have initiative to find work and willingly under-
take it on his own for the achievement of organizational goals.
c) Should have attended and passed an ITI in the electrical / mechanical
fitter trade.
d) Should have attended a training / refresher cadre for personnel working
on Effluent Treatment Plant.
e) Should have at least one year experience in the operation as well as
maintenance of Pumps, Motors, Switch gears, Reduction Gears, Valves
and Pipes at a Effluent Treatment Plant or at a Water Supply Installation.
f) Or should have been a Plant operator for five years and helped Electrical
/ Mechanical maintenance teams for at least three years.
4. Labour /Helper:
a) Should at least be Class VII pass and be physically fit and mentally alert.
b) Should accept assigned tasks willingly and complete these without su-
pervision and further guidance.
5. Laboratory Analyst:
a) Should be at least B.Sc. with Chemistry with three years analytical expe-
rience or M.Sc. with Chemistry with one year analytical experience.
b) Should have attended a training / refresher cadre for Laboratory Ana-
lysts for working on Effluent Treatment Plant laboratory.

13
c) Should be able to draw an Analysis Program for collection and analysis
of daily, weekly and monthly samples and follow it and report results as
per time schedule thus agreed upon.
d) Draw out a program to undertake performance studies from time to time
and have it approved from the higher offices through his plant manager
before execution.
e) Be responsive and prepared to undertake additional responsibility of the
Plant Manager when the incumbent is away for short durations.
f) Be bold to report deficiencies in treatment as shown by effluent quality
analysed at the Laboratory.

14
“Training Need Identification, ImpartingTraining, Training Effectiveness Evaluation, and
Re-Training” is the Mantra for ensuring reliable ETP operation. This is more so due to
high turn-over of ETP staff.
Training can be imparted at ETP site by academic/research institutions, by in-house
experts, or by sending staff to courses offered by professional bodies. However, expe-
rience shows that the best options is training by experienced ETP operating agency.
Such training will be rich in the terms of practical hints, case-studies, and participants
will find it easier to communicate with the faculty.
Training courses may be run for 6 to 10 working days at a stretch with residential
facilities for batches of 10 – 12 individuals at a time. Shorter courses may be arranged
for senior engineers from industry/municipal bodies.
The emphasis in training should be on the following aspects:
1. The Course should commence with a quick visit to the Effluent Treatment Plant
where the participants are made conversant with the units / processes that shall be
dealt with subsequently in the course syllabus.
2. Introduction of,
a) Various unit operations and processes (Separation by Screening, Floata-
tion, Settling / Sedimentation, Filtration, Neutralization, Coagulation, Floc-
culation, Absorption, Adsorption, Chemical Reactions, Oxidation/Reduc-
tion, Dissolution, Ion exchange, Chlorination)
b) Operation of Units such as Screens (Coarse / Fine Bar screens, Manual
/ Mechanically operated), Sumps and Pumping Stations including Pumps,
Motors and Panels (Centrifugal Horizontal / Vertical Turbine), Valves
(Sluice gates, Non return, Reflux), Pipes/Specials and Pipe Joints, Grit
Removal Units. Primary Sedimentation / Settling tanks, Scraping Mecha-
nisms, Sludge withdrawal, Sludge Sumps, Sludge Pumps, Aeration tanks
and Aerators, Secondary Settling Tanks, Secondary Sludge Sumps,
Pumps, Sludge Thickeners, Sludge Digesters, Gas Production, Sludge
handling and Drying.
ETP Staff Training

15
c) Maintenance of Pumps and Motors, Electrical Panels (Starters, Meters
(Energy, Voltage, Amperage, Power factor), Manual or Electrically Oper-
ated Trolley Gantry, Blow out Fuses, Valves, Gates, Scraping Bridge Trol-
ley, Aerators, Reduction Gears, Open Air Weather Casings for Motors,
Sprocket wheels and Chains for Mechanical Grit and Screen removing
devices.
d) Introduction to Quality aspects of Raw and Treated Effluent and the im-
portance of each of the quality parameters and corresponding unit op-
eration / process that plays a part in influencing quality parameters.
3. Identification of flaws and troubles with treatment and its trouble shooting where
it is not due to inbuilt flaws in design / design criteria, such as bulking of sludge
in the lower layers and floating of sludge lumps in a settling tank, foul smelling in
an Aeration Tank, heading up in the Settling Tanks or Aeration tanks, passing of
undue flocs in the settled effluent from settling tanks, disruption of operation by
failure of main power supply and malfunctioning of scraping mechanism in the
clarifiers.
4. Undertaking segregation of a motor and pump from the manifold at suction and
delivery, its disconnection from the panel, hauling up of both pump and motor to
the maintenance platform, dissembling of the pump, replacement of shaft / im-
peller, reassembly of the pump, check motor for its characteristics, haul back to
the mounting location, couple up / connect the pump and motor and reconnect
power and rejoin with suction and delivery manifold.
5. Undertaking replacement of a mechanical surface aerator in an Aeration Tank
and undertake replacement of a Reduction Gear Assembly including its mainte-
nance.
6. Removing and Replacing of a Sluice Gate Valve from a mains and undertaking
maintenance of the Sluice Gate Valve.
7. Maintaining a Power Factor, methodology and upkeep of the Power Factor Bat-
tery Bank.
8. The role of each of the category of tradesmen on site in bringing the final efflu-
ent quality better than the discharge standards.

16
A separate laboratory training course should be run for only Laboratory Analysts for a
period of 6 Working days. It may include:
a) Introduction to items at Serials 1 & 2 above.
b) Importance of quality and plant performance parameters e.g. pH, TS, SS, TDS,
BOD, COD, DO, Temperature, MLSS, MLVSS and SVI including methods of
determination.
c) A three day regular analysis program in which the participants in pairs are given
a sample of effluent for analysis for pH, TS, SS, TDS, BOD, COD, DO, Tempera-
ture and a sample of Aeration Tank discharge for determination of MLSS, MLVSS
and SVI. The results should be discussed and candidates should be encour-
aged to express their views as to how these can further be improved.
d) Preparing sampling schedule (locations, numbers, frequency, grab/continuous),
sample preservation methods, statistical tools
Daily training must be followed by a Quiz Test for all cadres before the close of the day
and the participants be evaluated based on the outcome of the course results. The
participants be presented “Participation Certificates” at the end of the course. This
serves as an excellent incentive.

17
Guidelines for Safety In ETP Operation
Hazard Identification
Effluent treatment plant operators work both indoors and outdoors and are exposed to
noise from machinery and to unpleasant odours.Operators’work is physically demanding
and work is often is performed in unclean locations. Moreover, plants operate 24 hours
a day, 7 days a week; therefore, operators work one of three 8-hour shifts, including
weekends and holidays, on a rotational basis. Operators may be required to work
overtime.
Also, ETP operators are exposed to a variety of hazardous chemical agents, contained
in the effluents and to the reagents used in the waste water processing, or generated
during the waste waters treatment.These chemical agents may cause acute poisoning,
chemical accidents (e.g., skin burns, injury to the eyes, etc.) damage to the respiratory
system, allergies, dermatitis, chronic diseases, etc.
Occupational safety and health (OSH) considerations are becoming integral part of
modern day operations. In view of this it is necessary to identify hazards and devise
preventive and remedial measures to mitigate OSH risks in ETP operation.
The hazards in ETP O & M are listed below:
1. Slips and falls on floors made slippery by water, aqueous solutions or solvents.
2. Blows and contusions caused by falling heavy articles, including containers of
chemical reagents, e.g., from overhead conveyers, or by contact with moving
machinery or vehicles.
3. Falls into ponds, pits, clarifiers or tanks causing injuries or drowning.
4. Hazards related to entry into confined spaces - suffocation due to oxygen
deficiency, poisoning (e.g. by hydrogen sulphide), etc.
5. Burns, by steam or hot vapours, by splashes of hot plating baths, solvents and
other liquids, by contact with hot surfaces (e.g., annealing ovens), etc.
6. Electric shock caused by contact with faulty electrical equipment, cables, etc.
7. Cuts and pricks by sharp tools sharp edges of articles to be plated sharp deposits
on jigs, etc.

18
8. Injuries (especially of eyes) caused by flying particles, in particular from rotating
brush cleaning or wheel grinding.
9. Fire and explosions due to the formation and release of flammable gases during
processing (e.g., methane, hydrogen).
10. Vigorous chemical reactions caused by uncontrolled mixing of chemicals (e.g.,
if water is mixed with concentrated sulphuric acid) during the preparation of
reagents for wastewater treatment.
11. Acute poisoning caused by various chemicals present in the wastes, used as
reagents (e.g., gaseous chlorine), or released during the treatment; a particular
hazard is caused by the possible release of a number of poisonous gases, e.g.,
hydrogen-cyanide (from metal plating or heat treatment wastes upon
acidification), hydrogen-sulphide, etc.
12. Acute intoxication caused by erroneous drinking of untreated wastewater.
13. Poisoning by phosgene, which may be formed if a worker smokes in the presence
of chlorinated-solvent vapours, or if welding or other flames or arcs are used.
14. Chemical burns by corrosive liquids Damage to eyes by splashes of irritating or
corrosive liquids.
15. Diseases caused by infectious agents (bacteria, viruses, protozoa, helminthes
and fungi – see appendix) present in the raw domestic wastewater (mainly from
human origin) and in agricultural wastes.
Dos and Don’ts in ETP Operation for Safety
1. Use safety shoes or boots with non-slip soles.
2. Wear personal protective equipment and chemical resistant clothing to avoid
exposure of skin or eyes to corrosive and/or polluted solids, liquids, gases or
vapours.
3. Do NOT mix chemicals without the supervision of a qualified chemist or safety
professional.
4. Obey all safety-instructions regarding the storage, transport, handling or pouring
of chemicals.

19
5. Check electrical equipment for safety before use; verify that all electric cables
are properly insulated; take faulty or suspect electrical equipment to a qualified
electricity technician for testing and repair.
6. Wear safety goggles in all cases where the eyes may be exposed to dust, flying
particles, or splashes of harmful liquids.
7. Wear respirator, or gas mask, when exposed to harmful aerosols, dusts, vapours
or gases.
8. Take extreme care when handling highly corrosive agents such as liquid or
gaseous chlorine, concentrated acids or alkalis, or when toxic gases may be
emitted from the reagents, etc.
9. Obey all safety instructions concerning entry into confined spaces, e.g., check
atmosphere for oxygen or for poisonous gases, use respiratory protection
equipment if needed, have a co-worker stand guard in case of need for help,
etc.
10. Do not smoke, eat or drink in areas where chemical or biological contamination
may be expected.
11. Use non-latex gloves if sensitivity to latex has been diagnosed.
12. All workers should undergo periodic examinations by occupational physician to
reveal early symptoms of possible chronic effects or allergies.
13. Learn and use safe lifting and moving techniques for heavy or awkward loads
such as containers of chemicals; use mechanical aids to assist in lifting.
Personnel Protective Equipment (PPE) for ETP O & M
While planning the list of PPE, the following types of situations should be catered for:
1. Impact / Penetration / Compression while doing maintenance tasks
2. Chemical Handling
3. Heat/cold and wetting
4. Harmful dust
5. Oxygen deficiency
6. Obnoxious odours of decomposing matter

20
7. Hydrogen Sulphide presence
8. Light (optical) radiation
9. Biological exposure from raw / treated effluents and sludge handling
10. Noise of machines and vibrations.
11. Electric shock
12. Rain / Storm
General List of PPE:
1. Safety Boots with non-skid soles and Steel Toes.
2. Electrical Hazard safety Toe shoes
3. Gas Masks and Face Shields
4. Oxygen meters for ascertaining type of atmosphere in a confined area.
5. Single-use Ear Plugs / Ear-muffs
6. Safety Goggles
7. Helmets / Hard Hats
8. Latex Rubber/ Butyl Rubber/ Fabric / Chemical Resistant Gloves
9. Overall Clothing
10. Aprons for laboratory Personnel
11. Safety Belts
12. First Aid Box
13. Fire extinguishers
14. Respiratory Protective mask with man pack cylinders
Safe Handling of Chemicals
Since handling of chlorine and corrosive chemicals form part of many ETPs, special
attention should be given to safe handling of these chemicals.

21
Safe Handling of Chlorine
Pure chlorine comes in two forms: gas and liquid. Chlorine gas is easily liquefied under
pressure.Typically, a commercial cylinder contains liquefied gas under pressure.Chlorine
gas has a disagreeable, sharp, pungent, penetrating odour. In airborne concentrations
above 1000 parts per million (ppm) it has a greenish-yellow colour. In smaller
concentrations it is colourless. Chlorine gas is 2½ times heavier than air and tends to
flow downhill and pool in lower areas.Wind and weather, however, will cause a chlorine
gas cloud to disperse, spreading it in all directions, even uphill.
Liquid chlorine is a transparent, amber-coloured, oily fluid that is 1½ times heavier
than water. Liquid chlorine has a high compression ratio. The ratio of liquid to gas is 1
to 460, which means that 1 L of liquid chlorine expands to form 460 L of pure chlorine
gas. The maximum allowable concentration of chlorine a person can be exposed to in
an eight-hour period is 0.5 ppm,
Chlorine gas is mainly used as a disinfectant in:
1. Swimming pools
2. Water treatment plants
3. Sewage treatment
4. Community water supplies, including water used for irrigation
Chlorine is also used in:
1. Pulp and paper industries
2. Pool chemical products
3. Cleaning products
4. Mining processes
5. Bleach manufacturing
6. Plastics manufacturing
Chlorine is corrosive. It can burn moist body surfaces such as the eyes, nose, throat,
lungs, and wet skin because it forms harmful acids when it reacts with moisture.
Repeated exposure to chlorine does not produce an immunity or tolerance. Long
term exposure to low concentrations of chlorine may cause a gradual decrease in lung
efficiency. A single exposure to a high concentration can cause the same effect.

22
Concentration Effect
0.03 – 0.1 ppm Range of odour threshold (many specify this as 0.08
ppm)
1 – 3 ppm May cause mild irritation of the eyes, nose, and throat
3 – 5 ppm Stinging or burning in eyes, nose, and throat; may
cause headache, watering eyes, sneezing, cough-
ing, breathing difficulty, bloody nose, and blood-
tinged sputum
5 ppm or more Severe irritation of the eyes, nose, and respiratory
tract
14 – 25 ppm May be fatal after 30 minutes of exposure
25 ppm or more Immediate breathing difficulty resulting in pulmonary
edema (fluid build-up in lungs), possibly causing suf-
focation and death 1000 ppm or more Fatal after a
few breaths
1000 ppm or more Fatal after a few breaths
Toxic Effects of Chlorine
(Chlorine gas is not visible as a greenish-yellow cloud at concentrations below 1000
ppm)
Exposure Limits of Chlorine
Concentration Effect
0.5 ppm Maximum allowable concentration averaged over an
eight-hour period
1 ppm Maximum allowable short-term exposure (15 min-
utes)
10 ppm or more Immediately Dangerous to Life and Health as pub-
lished by National Institute for Occupational Safety
and Health in the United States (NIOSH).

23
Handling Chlorine equipment: Changing chlorine cylinders
1. Turn on the light and visually ensure that the room is safe to enter (there may be
visible signs of damage).
2. Put on appropriate personal protective equipment (be specific about the type of
equipment).This procedure requires a respirator other than an escape respirator
3. Turn on the exhaust ventilation before entering the room.
4. Close the main chlorine container valve.
5. Allow the system to purge itself of chlorine. Ensure that the float drops to the
bottom of the feed-rate indicator (rotameter). Verify that there is a high vacuum
and that the weigh scale reads zero.
6. Loosen the chlorinator (auxiliary valve or vacuum regulator) and remove it from
the empty cylinder.
7. Replace the cylinder cap on the empty chlorine cylinder and remove the cylinder
to secured storage.
8. Secure the new cylinder into place.
9. Remove the protective hood from the new cylinder.
10. Ensure that there is no chlorine leaking from the packing gland. Use ammonia
vapour from the ammonia test bottle, which contains a strong ammonia solution.
11. Ensure that the cylinder valve is closed. Do not open the valve yet.
12. Remove the cylinder outlet cap and check that the cylinder outlet face is clean
and smooth.
13. Using a new washer, connect the vacuum regulator or the yoke assembly (be
specific for the system in use) to the valve outlet using the supplied wrench only.
Note: Never use oil-based material or water to clean the mating surfaces.
14. Crack open the chlorine cylinder valve and then quickly close it again. This will
let enough chlorine into the lines to charge them.The valve should open with no
more than a sharp rap from the heel of your hand. Never use a “helper” wrench
or a larger wrench than the one supplied. If the valve will not open, carefully
loosen the packing gland slightly.
15. Check all the connections you have made to ensure there are no leaks. Use the
vapour from the ammonia test bottle (see step 10). If a leak is indicated, activate

24
the leak control procedure (see paragraph serial 2 in leak detection and control
below).
16. When no leaks are indicated, open the chlorine cylinder valve no more than half
a turn and leave the cylinder wrench on the valve.
17. Open any additional system valves (be specific for your facility) and test for
leaks as each stage is charged with chlorine.
18. Check for leaks again with the ammonia test bottle to be sure that everything is
in order.
19. Ensure that the alarm system is functioning.
20. Turn off the exhaust ventilation and lights and close the door when you leave.
21. Remove your respirator and other personal protective equipment.
Chlorine Leak detection and control
It has two components:
1. What to do if a leak is indicated after a cylinder change?
2. What to do if the chlorine alarm is activated during routine operation of the
system?
1. If the ammonia test indicates a leak after a cylinder change, follow these
steps. (Note that the worker will already be wearing a respirator):
a) Immediately close the main cylinder valve.
b) As long as the monitor reads less than 10 ppm, the cylinder hook-up
procedure may be repeated.
c) Open (and close) the main cylinder valve and repeat the ammonia test.
d) If a leak is still indicated, make a third and final attempt to get a good seal
using a new lead washer.
e) If the leak cannot be corrected after three attempts, remove the cylinder
from service and contact the supplier. Ensure that there is no leak from
this cylinder with the main valve closed. A different cylinder must be
connected to the chlorination system.
f) Leave the chlorine room and remain nearby to restrict access to the room
or provide other assistance, as directed, until the chlorine alarm has
automatically shut off.

25
2. If the chlorine alarm has been activated during routine operation of the system,
at least two people must respond. Follow these steps:
a) Approach the location cautiously.
b) If chlorine gas can be smelled in the open, immediately leave the area
and activate full emergency procedures. Do not attempt to turn on the
exhaust ventilation.*
c) If there is no smell of chlorine gas outside the room, put on respiratory
protection and check the monitor readout.
d) If the chlorine concentration is less than 10 ppm:
i) Put on the appropriate personal protective equipment.
ii) Enter the room and close the main cylinder valve.
iii) Turn on the ventilation system and leave the area until the alarm
stops.
iv) While still wearing the respirator, enter the room after the alarm
has stopped, isolate the leak, and perform necessary repairs.
Remember that all chlorine lines must be free of oil, grease, and
moisture before re-opening the chlorine cylinder.
e) If the continuous monitor indicates a chlorine concentration greater than
10 ppm, immediately leave the area and activate full emergency
procedures. Do not turn on the ventilation system* and do not wait
downwind of the building for help to arrive.
Note: Never apply water to a chlorine leak. Moist chlorine is more
corrosive than dry chlorine and the leak will worsen rapidly
if water is applied to it. Remember also that a chlorine leak
never gets better, it always gets worse.
Safety in Handling of Corrosive substances such as Acids, Alkalis
General Chemicals used in Effluent Treatment:
1. Neutralization / pH correction: Hydrochloric acid, Sodium Hydroxide / Lime
2. Coagulant / Settling Aids:Aluminium Sulphate, Ferric Aluminium Sulphate, Ferric
Sulphate, Ferric Chloride, these may be independent or in combination with
Poly Electrolytes (Polymers).

26
3. For Specific Ion removal, chemicals required as per chemistry of treatment.
4. Nutrients: Urea, Di-ammonium Phosphate
5. Disinfectant: Chlorine, Bleaching Powder (Sodium Hypo-chlorite), Ozone
6. Adsorption / Absorption: Activated Carbon
7. Ion Exchange – based on the specific ion to be removed.
Few Examples of Corrosive Substances used in ETP
1. Sulphuric acid
2. Chromic acid
3. Stannic chloride
4. Ammonium bi-fluoride
5. Bromine
6. Ammonium hydroxide
General Characteristics of ETP Chemicals
1. Acids and Alkalis fall into the category of Corrosive chemicals. Corrosives are
most commonly acids and alkalis, but many other materials can be severely
damaging to living tissue.
2. Corrosives can cause visible destruction or irreversible alterations at the site of
contact. Inhalation of the vapour or mist can cause severe bronchial irritation.
Corrosives are particularly damaging to the skin and eyes.
3. Certain substances considered non-corrosive in their natural dry state are
corrosive when wet such as when in contact with moist skin or mucus membranes.
Examples of these materials are lithium chloride, halogen fluorides, and alkyl
iodide.
4. Sulphuric acid is a very strong dehydrating agent and nitric acid is a strong
oxidizing agent. Dehydrating agents can cause severe burns to the eyes due to
their affinity for water.
Use and Storage of Corrosives
1. Always store acids separately from bases. Also, store acids in acid storage
cabinets away from flammables since many acids are also strong oxidizers.

27
2. Do not work with corrosives unless an emergency shower and continuous flow
eyewash are available.
3. Add acid to water, but never add water to acid.This is to prevent splashing from
the acid due to the generation of excessive heat as the two substances mix.
4. Never store corrosives above eye level. Store on a low shelf or cabinet.
5. It is a good practice to store corrosives in a tray or bucket to contain any leakage.
6. When possible, purchase corrosives in containers that are coated with a
protective plastic film that will minimize the danger to personnel if the container
is dropped.
7. Store corrosives in a wooden cabinet or one that has a corrosion-resistant lining.
Corrosives stored in an ordinary metal cabinet will quickly damage it. If the
cabinet supports that hold up the shelves become corroded, the result could be
serious. Acids should be stored in acid storage cabinets specially designed to
hold them and Nitric acid should be stored in a separate cabinet or compartment
Use and Storage of Hydrofluoric Acid
1. Hydrofluoric acid is extremely hazardous and deserves special mention.
Hydrofluoric acid can cause severe burns and inhalation of anhydrous hydrogen
fluoride can be fatal. Initial skin contact with hydrofluoric acid may not produce
any symptoms.
2. Only persons fully trained in the hazards of hydrofluoric acid should use it.
3. Always use hydrofluoric acid in a properly functioning fume hood. Be sure to
wear personal protective clothing!
4. If you suspect that you have come in direct contact with hydrofluoric acid: wash
the area with water for at least 15 minutes, remove clothing, and then promptly
seek medical attention.If hydrogen fluoride vapours are inhaled, move the people
immediately to an uncontaminated atmosphere (if safe to do so), keep the person
warm, and seek prompt medical attention.
5. Never store hydrofluoric acid in a glass container because it is incompatible
with glass.
6. Store hydrofluoric acid separately in an acid storage cabinet and keep only that
amount necessary in the lab.
7. Creams for treatment of hydrofluoric acid exposure are commercially available.

28
Health Hazards Associated with Corrosives:
1. All corrosives possess the property of being severely damaging to living tissues
and also attack other materials such as metal.
2. Skin contact with alkali metal hydroxides, e.g., sodium hydroxide and potassium
hydroxide, is more dangerous than with strong acids. Contact with alkali metal
hydroxides normally causes deeper tissue damage because there is less pain
than with an acid exposure.The exposed person may not wash it off thoroughly
enough or seek prompt medical attention.
3. All hydrogen halides (HF, HCl, HBr and HI) are acids that are serious respiratory
irritants and also cause severe burns.Hydrofluoric acid is particularly dangerous.
At low concentrations, hydrofluoric acid does not immediately show any signs
or symptoms upon contact with skin.It may take several hours for the hydrofluoric
acid to penetrate the skin before you would notice a burning sensation.However,
by this time permanent damage, such as second and third-degree burns with
scarring, can result.
Acute Health Effects:
Inhalation irritation of mucus membranes, difficulty in breathing, fits
of coughing, pulmonary edema
Ingestion irritation and burning sensation of lips, mouth, and throat;
pain in swallowing; swelling of the throat; painful abdominal
cramps; vomiting; shock; risk of perforation of the stomach
Skin Contact burning, redness and swelling, painful blisters, profound
damage to tissues, and with alkalis; a slippery, soapy feeling
Eye Contact stinging, watering of eyes, swelling of eyelids, intense pain,
ulceration of eyes, loss of eyes or eyesight
Chronic Health Effects
Symptoms associated with a chronic exposure vary greatly depending on the chemi-
cal. For example, the chronic effect of hydrochloric acid is damage to the teeth; the
chronic effects of hydrofluoric acid are decreased bone density, fluorosis, and anaemia;
the chronic effects of sodium hydroxide are unknown.

29
Inhalation Remove person from source of contamination if safe to do so.
Get medical attention. Keep person warm and quiet and do not
leave unattended.
Ingestion Remove person from source of contamination if safe to do so.
Get medical attention. Keep person warm and quiet and do not
leave unattended.
Skin Contact Remove person from source of contamination and take immedi-
ately to an emergency shower or source of water. Remove cloth-
ing, shoes, socks, and jewellery from affected areas as quickly
as possible, cutting them off if necessary. Be careful not to get
any chemical on your skin or to inhale the vapours. Flush the
affected area with water for a minimum of 15 minutes. Get medi-
cal attention.
Eye Contact Areas as quickly as possible, cutting them off if necessary. Be
careful not to get any chemical on your skin or to inhale the
vapours. Flush the affected area with water for a minimum of 15
minutes. Get medical attention.
Eye Contact Areas as quickly as possible, cutting them off if necessary. Be
careful not to get any chemical on your skin or to inhale the
vapours. Flush the affected area with water for a minimum of 15
minutes. Get medical attention.
First Aid:
Personal Protective Equipment
Always wear the proper gloves when working with acids. Neoprene and rubber gloves
are effective against most acids and bases. Polyvinyl chloride (PVC) is also effective
for most acids. A rubber coated apron and goggles should also be worn. If splashing is
likely to occur, wear a face shield over the goggles. Always use corrosives in a chemi-
cal fume hood.

30
Plant Performance Monitoring
The following parameters are an essential part of analysis at the on-site laboratory.
The location of sampling and the parameters that are required to be tested for are also
given in the table below.
1. pH
2. Total Solids (TS)
3. Suspended Solids (SS)
4. Total Dissolved Solids (TDS)
5. Biochemical Oxygen Demand (BOD)
6. Chemical Oxygen Demand (COD)
7. Dissolved Oxygen (DO)
8. Temperature
9. Chlorine Demand
10. Residual Chlorine
11. Mixed Liquor Suspended Solids (MLSS)
12. Mixed Liquor Volatile Suspended Solids (MLVSS) and Sludge Volume Index
(SVI)

31
DAILY TESTING SCHEDULE FOR VARIOUS PARAMETERS
(1000 & 1600 HOURS)
TEST / PA-
RAMETER
INLET TO
RAW
SUMP/ EQT
INLET PST
OUTLET
PST
FROM
AERATION
TANK (S)
INLET TO
SST
OUTLET
SST
FINAL
DIS-
CHARGE
pH ü ü ü
TS ü ü
SS ü ü ü ü ü ü
TDS ü ü ü
DO ü ü ü ü
TEMP. ü ü ü
BOD ü ü ü ü ü ü
COD ü ü
O&G ü ü ü
Cl2
DEMAND ü
RESIDUAL Cl2
ü
MLSS ü
MLVSS ü
SVI SLUDGE
ANY SPECIFIC As required

32
Guidelines for Record Keeping
Running Records are required to be kept for various operating machines such as Me-
chanical Screens, Mechanical Grit Removers, Pumps, Motors, Scrapers, Aerators,
Chemical consumption, Chlorine consumption etc. as maintained by the operators and
kept at Control Room or duty room of the operators that is closer to the location of the
machines.
The records of effluent quality and other laboratory tests are kept in the laboratory as
per daily sample collection and testing schedules.
The record with respect to flow need to be maintained by operators as per Table below.
The daily log sheet is passed to the Plant Manager on the subsequent day duly signed
by the operator in the first shift. All operators shall be responsible to fill up their part of
observations and calculations. The Plant Manager shall verify the daily record as well
as the calculations and shall be responsible to generate further data using these.
It is pertinent to mention that there shall be a requirement of drawing site spe-
cific procedures and formats / forms for keeping records.This shall be the
responsibility of the Plant Manager.
Hourly record of Flow as measured / recorded
through the Notch/ Weir/ Flow meter:
Date / Time
HEAD OVER
THE NOTCH /
WEIR
RATE OF
FLOW
AVERAGE
RATE OF
FLOW IN
PAST HOUR
FLOW
QUANTITY
__/__/__ m3
m3
/ HOUR m3
/ HOUR m3
0800- - -
0900
1000
1100
1200
1300
1400

33
Date / Time
HEAD OVER
THE NOTCH /
WEIR
RATE OF
FLOW
AVERAGE
RATE OF
FLOW IN
PAST HOUR
FLOW
QUANTITY
__/__/__ m3
m3
/ HOUR m3
/ HOUR m3
1500
1600
1700
1800
1900
2000
2100
2200
2300
2400
0100
0200
0300
0400
0500
0600
0700
0800
Total flow in the past 24 hour;
0800 hrs on October 14 to 0800 on Oct 15, 2004 ∑ =

34
Date / Month /
Year
Daily
Flow
Raw
Effluent
Treated
Effluent
Organic
load
removed
SS
passed
into
outfall
BOD BODSS SS
m3
/day mg/L mg/L mg/L mg/L Kg/day Kg/day
Computations of daily figures for the System:
Record of consumption of Electricity from the Energy meter:
Date
Energy Meter
Reading At
0800 Hours
Daily
Energy
Consumed In
Past 24 Hours
Rate / Unit Of
Energy
Energy
Expenses
Per Day
KHW KHW Rs. Rs.
Total for the month Units. Σ = Rs. Σ =

35
Record of Chemicals / Spares Consumption:
This record has to be prepared using a page for each chemical.
NAME OF THE CHEMICAL / SPARES: Alum OR Bearing
Date Quantity
Procured
Rate
Procured
Quantity
Consumed
Balance in
Stock
Cost of
Consumption
Kg./Ltrs. Rs./Kg./Ltr. Kg./Ltrs. Kg./Ltrs. Rs.
Total for the month Units. Σ = Rs. Σ =

FUEL
REPAIRS FROM
TRADE
MAINTENANCE
SPARES
TOTAL
SPARES FOR
REPAIRS TO
INSTALLATION
MAINTENANCE FUEL /
OILS / GREASES/
CIVIL / GARDENING
RENEWALS
FROM TRADE
HIRING
TRANSPORTATION
TOTAL
STOCK CHEMICALS
CHLORINE
TOTAL
VEHICLES /
TRUCKS
PLANT MACHINES/
EQUIPMENT /
PIPES / VALVES
EFFLUENT
TREATMENT
Record of monthly Expenses:
HEAD ITEM
EXPENSES
DURING
THE MONTH
EXPENSES IN
THE PAST
MONTH
PROJECTIONS
FOR THE
NEXT MONTH
Rs. Rs. Rs.
SALARIES
CONVEYANCE
TRAVEL
PF BY EMPLOYER
ESIS BY EMPLOYER
ARREARS OF WAGES
TOTAL
STAFF
36

HEAD ITEM
EXPENSES
DURING
THE MONTH
EXPENSES IN
THE PAST
MONTH
PROJECTIONS
FOR THE
NEXT MONTH
Rs. Rs. Rs.
LABORATORY CHEMICALS &
REAGENTS
EQUIPMENT
INSTRUMENTS
GLASSWARE
ENERGY
FUEL
TOTAL
PLANT VISITS
OFF PLANT
TOTAL
SUNDRY PAYOFFS
SUNDRY GIFTS
TOTAL
GRAND TOTAL
FLOW TREATED
DURING THE
MONTH
COST OF
TREATMENT/ CUM
ENTERTAINMENT
MISCELLANEOUS
ANY OTHER
37

Criteria for appointing Operation & Maintenance Agency
A well-designed ETP may not perform if it is not operated properly. However, as ETP
operation is a skilled job requiring expertise in environmental engineering, environ-
mental sciences, mechanical electrical trades, laboratory analysis, and trouble shoot-
ing, it may not be possible to undertake ETP operation in-house. Hence, many a times
ETP operation is outsourced. Listed below are essential criteria for selecting ETP op-
erating agency:
Statutory registrations & clearance certificates - MUST
1. Recognized Environmental Laboratory u/s.12 of the Environment (Protection)
Act, 1986 approved by Ministry of Environment & Forests, Govt. of India, New
Delhi
2. Provident Fund
3. Employee State Insurance Scheme
4. Sales Tax
5. Central Excise for Service Tax
6. Income Tax PAN No.
7. Works Contract Tax
8. Maharashtra Jeevan Pradhikaran Contractor for Rs.50 lakhs; or Contract value
whichever is less
9. Electrical Contractor for Rs.25 lakhs; or 50% Tender Value whichever is less
10. Public Works Department for Rs.300 lakhs; or Tender Value whichever is less
11. Should have the documented capability to run courses for training of various
trades and personnel employed for the operation and maintenance of the STP
/ ETP Installation, showing details of various courses run by him in the past for
own as well as industrial clients.
12. Tax Clearance Certificates - in respect of above wherever applicable
38

***
Financial requirement (minimum)
1. Annual turnover of 10 times the Tender Value for the last 3 years
2. At least 3 jobs of 50% of Tender Value in the last 3 years
3. Bank Solvency of Rs.50 lakh or equal to Tender Value, whichever is less
Experience (minimum)
1. Execution of 3 similar orders (in respect of process, volume, type of units, scope
of work) from Government or reputed Semi-Govt. Company, in last 3 years, for
at least 50% flow of tendered Effluent Treatment Plant.
2. Satisfactory job completion Certificate that should have been signed by Execu-
tive Engineer or rank above; certifying the detailed scope of work handled to
include Electrical Installations, Programmable Logic Control Panels, Pumping
Station, Digester, Chlorination and having maintained an on-site Pollution Test-
ing Laboratory.
3. Minimum 1 Post Graduate Environmental Engineer should have been a perma-
nent employee for the last 3 years (Proof in terms of PF / ESIS No. / Salary
Returns to be given).
4. Minimum 1 Post Graduate Environmental Scientist should have been a perma-
nent employee for the last 3 years (Proof in terms of PF / ESIS No. / Salary
Returns to be given).
39

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