Sewage treatment plant/Incinerator Flashcards
Sketch an Aerobic Sewage Treatment Plant.
see EOOW IAMI/ORAL Sketch Pack
With reference to an aerobic sewage plant:
a) Explain the need for continuous aeration. (6)
b) Describe the hazards that may be present when the plant requires internal maintenance or inspection (10)
a.) aerobic sewage treatment plant uses bacteria for treating waste. these bacteria are aerobic which means they require oxygen to survive. continuous aeration ensures that oxygen is being supplied to the bacteria for treating and stabilising water. without the bacteria the sewage waste cant be removed so it would just accumulate until there is an overflow problem. of course you can direct sewage waste from toilet system into the sewage holding tank but even this has a limited capacity so overflow can still occur. if the bacteria die due to a lack of oxygen it takes approximately 2 weeks for bacteria to recolonize so for that time sewage would just have to accumulate this could cause an overflow problem depending on amount of sewage produced. another reason that continuous aeration is important is it promotes aerobic biodegradation, which is the breakdown of organic pollutants (sewage) by microorganisms (bacteria) when oxygen is present. in other words bacteria can only breakdown the sewage into water and sludge when they are in optimum oxygen conditions. One other reason for continuous aeration done by air blowers is if oxygen supply is interrupted anaerobic bacteria form. this type of bacteria will produce toxic and explosive gases like ammonia, methane and hydrogen sulphide (H2S).
b.) If an entry is required within the plant for maintenance or
inspection has to be considered as an enclosed space entry so all permits and procedures have to be followed with accordance to the ships SMS and enclosed space permit has to be obtained. Additional hazards that can be present when working within the
STP can include gases such as H2S and Methane. These will be identified through the use of a calibrated Atmosphere monitor. Continuous ventilation of the plant must be maintained. Bacteria found within the sewage plant can also be dangerous to
personal if contact is made therefore appropriate full protective
clothing, masks, eye goggles etc listed in the risk assessment shall be worn
what are some of the main components in a vacuum sewage treatment plant?
Main components of the vacuum sewage treatment plant on board ship are ejector (for creating vacuum in toilets), pressure switch (to maintain vacuum in the system) and level switch for the operation of treated effluent discharge pump.
describe the operation of a air ejector
The air ejector consists of a jet tube of stainless steel, a check valve and a nozzle. The driving water for the ejector is supplied from the collecting tank with the help of a pump and the discharge is fed back to the tank.Sewage is pumped from the tank through thenozzle of the ejector creating a venturi effect whereby air and waste are inducted from the toilet piping, mixed with thesewage jet and passed into the collecting tank.When the pump stops, the rubber flap of the check valve is drawn into the closed position by the vacuum, which isthereby maintained.
what maintenance is carried out for air ejector?
Tightness of the ejector flap shall be checked periodically.
Once a year:
Open and clean ejector check valve
Every five years:
Change ejector flap
Clean ejector nozzle
Check and clean ejector from build-up of deposit
Describe the Operation of Pressure Switch
The vacuum level in the system is controlled by a pressure switch.The pressure switch or switches and the vacuum gauge should be installed on a separate manifold, to reduce thechance of impurities entering the switch or gauge. The instrument branch must have 5° slope. Water in theinstrument branch will cause malfunctions.
The switch starts a pump when the vacuum level in the system falls below a pre-set value. If the vacuum level stillkeeps declining, another pump will be started (provided that there is more than one pump in the system). As soonas the required vacuum level has been reached, the pump will be stopped.
1.Set the stop pressure by turning the knob. As you turn the knob, the indicator on the scale will move. It should beset between-0.4 bar and -0.6 bar (40-60% vacuum). This is the vacuum level at which the pumps will be turned off.Note that in each system the optimal setting may vary.
2.Set the start pressure by turning the knurled knob, reached by removing the cover of the switch. Turning the knobwill set the starting vacuum level somewhat lower than the “stop “level set by the knob. In effect, whenever the“stop”level is changed by turning the knob, the starting level will also be changed.
3.The plant can be provided with a low level pressure switch for low vacuum alarm. Set the “off” pressure to-0.3 bar.
4.The setting of the switch may vary from system to system depending on the individual requirements.
5.The vacuum gauge installed, in each system enables you to check that pressure switches are functioning properly.
what maintenance must be carried out for pressure switch?
Once a year:
Check the operation of both pressure switch and vacuum gauge.
Every five years:
Clean or change piping and components between switch and gauge.
Describe the Operation of magnetic Level Switch
The liquid level in the tank is controlled by magnetic level switches, which start and stop the pump.The switches consist of a float, a body, a rubber gaiter, a mounting flange, a switch mechanism in the body, andtwo permanent magnets in repulsion, one in the float, the other in the switch insert.As the float and its magnets move up and down with the liquid level, the magnet in the switch insert movescorrespondingly and either opens or closes the circuit controlling the pump or an alarm function.
Describe the maintenance carried out for a magnetic Level Switch
Once a year (or during tank cleaning):Clean the level switch
Before starting to remove a switch, make sure that liquid level in the tank is below it. If necessary, dischargeto required level, but be careful not to let the pumps run dry. Then switch off the electrical supply, remove the securingnuts, and pull out the switch. Clean the float and check that it moves freely.
Under certain conditions an excessive amount of foam may appear in the tank. Should the level switchesreact to the surface of the foam, instead of the actual liquid level, malfunctioning may occur in the system. To avoid oreliminate this problem, see underTrouble Shooting of Biological Vacuum Sewage Treatment Plant.
what Precautions must be followed when Operatingaerobic Sewage Treatment Plant
Following precautions in operating biological vacuum sewage treatment plant must be followed to maintain optimal process conditions and effluent quality.
1.If there is no counter pressure for the discharge pump, a bend piping arrangement must be done with a pipeloop (goose neck) over tank’s water level to prevent siphoning.
2.The unit must be incontinuousoperation to maintain biological activity.
3.It will take about one month before effective biomass will overtake the process after first start-up or aftermaintenance break. During this bacteria breeding period unit is not working as designed.
4.Never discharge both aeration chambers totally at same time. Ensure always that there isbacterialpopulationleft in either chamber I or chamber II to avoid collapse of the biological process.
5.Amount of the needed dilution water can be calculated. Needed dilution water is 1 x incoming black water(vacuum system). The amount of black water in vacuum toilet system is15 l/person/day. A total dilution water needcan be calculated:Dilution water per day = (1 x 15 l/person/day) x persons on board.
6.Dilution water can be fresh, brackish or technical water. Dilution water is added into aeration chamber I.
7.Dilution is not needed, if vessel’s grey water is also processed in the treatment plant.
8.Some antifoaming chemicals has a very high BOD5 value. It is recommended to use antifoaming chemicalswhich have low BOD5 value.
9.All substances which might be harmful to the biological process such as large amounts of grease, acids,alkaline, etc. are not allowed to be led to treatment unit.
10.Never let the pump run dry. Mechanical seals may be damaged.
11.Effluent quality is within IMO’s limits after about one month of the start up.
12.Take a sludge content test at least every week or every time when sludge “SLUDGE ALARM” is displayed.
13.Make sure that the unit is well ventilated and there is enough fresh air in the chamber if you have to goinside to avoid inhaling toxic fumes and suffocation. One person must stay outside of the tank and keep eye onperson who is working inside the unit.
14.Make sure that the waste water is lead to a proper holding tank (hull tank or collection tank) during shutdownor maintenance break.
what alarms are provided in Sewage Treatment Plant
HIGH LEVEL ALARM
Water level is over high level switch LSH over presetted time, timer setting 30s.
VACUUM FAILURE/COLLAPSE
Led is on (vacuum failure), ejector pump has been running over presetted time, timer setting 15min.
Led is blinking (vacuum collapse), vacuum level below presetted value -0.2bar (Pressure switch alarm) over presetted
time, timer setting 2min.
COMMON ALARM
Emergency stop, emergency stop pressed down.
High level alarm, see above.
Blower overload, circuit breaker tripped.
Discharge pump overload, circuit breaker tripped.
Control voltage failure, circuit breaker tripped.
Chlorination pump overload, circuit breaker tripped.
Antifoaming pump overload, circuit breaker tripped.
SLUDGE ALARM
Presetted number of discharge times reached, counter setting 200 times.
with reference to a vacuum sewage treatment plant
provide causes and remedies for each of the following problems
- Vacuum is not created
even though pump is
running. - discharge pump will not start
- discharge pump will not stop
- Discharge pump is running but not
pumping. - overflow in system.
- Air blower does not run.
- Air blower is running, but not creating sufficient pressure (low pressure)
- Plant smells strongly.
- There is too much black sludge on
surface in settling tank compartment III. - There is no residual chlorine in the
discharge water.
- causes
Tank empty
Foam instead of liquid in tank
Valves are shut
Incorrect rotation of motor
Blockage or leakage in piping system.
remedies
1.If the tank is empty, fill to at least to thelow level switch. Check the condition ofthe pump according to the manufacturer´sinstruction.
2.If the pump is pumping foam instead ofliquid, this will be evident due to severevibration. Add water to the tank and try
again. If adding water does not help,reduce the level of foam by pouringantifoam agent into the tank (1 cup per 2cubic metres of foam and sewage).
3.Check that shut-off valves are fully openand not clogged.
4.If the direction of rotation of the pump iswrong, change wiring accordingly.
Close the valves that isolate the collectingunit from the piping system and start thepump again. If vacuum now builds up, there
must be a leak in the piping system.
- causes
1.Motor defect
2.No power
3.Automatic fuses off
4.Impeller defect
5. Failure in float switch.
remedies
1.Replace motor.
2.Check the electrical system.
3.Check reason for this before
switching fuses on.
4.Measure clearance of impeller.
5. Check float switch and wiring, repairor replace.
- causes
1.Failure in float switch.
2. Too much water enters the plant.
remedies
1.Check float switch and wiring, repairor replace.
2. reduce peak flow.
- causes
1.Wrong rotation direction.
2.Impeller defect.
3.Valve in discharge system closed
or defect.
remedies
1.Change phases on electrical motor.
2.Replace impeller.
3.Check valves in discharge system.
- causes
1.Pump is clogged.
2.Discharge pump defect.
3.Too much water enters the plant.
remedies
1.Open and clean pump.
2.Open bypass and repair/replace
discharge pump.
3.Allowed in peak periods. Try to
reduce peak flow.
- causes
Screen in aeration chamber clogged.
* Timer wrongly adjusted.
* No power.
* Automatic fuses off .
* Motor defect.
* Impeller defect.
* Defect non-return valve and water in air blower.
remedies
Clean screen and remove dirt.
* Check and adjust timer .
* Check the electrical system.
* Check reason for this before
switching fuses on.
* Replace or repair.
* Replace impeller.
* Repair and replace valve.
! NOTE: In case of emergency, use
vessel’s air system, but pressure
must be less than 1.5 bar.
- causes
1.Defect non-return valve.
2.Wrong direction of rotation.
remedies
1.Repair or replace.
2.Change phases on electrical motor.
The direction of a 3 phase motor can be reversed by swapping any two phase connections. This reverses the direction of the rotating magnetic field and causes the rotor to run in the reverse direction.
- causes
1.Too much mineral sludge.
2.Bacterias killed. Brown sludge
indicates normal bacteria life. Blacksludge indicates that bacteria arekilled.
remedies
1.Check sludge content anddischarge if required.
2.Check air blower function by openingthe man holes. Surface bubblesmust be seen during bloweroperation.
9.causes
1.Insufficient operation of sludge return pump.
remedies
1.Check and adjust return sludge air
valve. Check air hoses.
- causes
1.Dosing pump is not operating.
2.Disinfectant tank is empty.
3.Dosage rate is too low.
Disinfection chlorine is obsolete.
remedies
1.Check pump operation.
2.Fill it up with approved disinfectant.
3.Increase dosage by adjusting dosingpump. Replace with “fresh” chlorine.
what is sludge testing?
Sludge Testing
It is important to keep a sludge content within certain limits i.e. a good biological balance for the treatment process inthe sewage treatment unit.
Sludge content test, aeration chambers I and II
Measure the sludge levels in aeration tanks I and II using test cocks while blowers are running.
Fill the glass funnel with 1000ml and throw the first “sample” water away immediately. This action will “clean” thesample valve and increases test result significantly.
Fill the glass funnel with 1000ml of waste water from the test cock of aeration chamber I or aerationchamber II while the blower is running.
Let the sludge settle for 30 minutes in this glass.
Observe the colour of the sludge and odour. If the biological process is running well, sample colour is grey or brown andsample will not smell significantly. If the sample colour is black and/or it smells, it is a indication that biological process does not work properly.
Read the sludge quantity from the side of the glass.
Interpretation of Results
Sludge content measurementbelow 300 ml/l = sludge content too low for biological process.
Between 300 ml/l and 600 ml/l = normal
Above 600 ml/l = sludge content too high, discharge sludge.
with reference to sewage treatment plants;
a,) what is disenfection?
b.) what chemical is used for disinfecting?
c.) why is disenfection and residual testing carried out ?
d.) describe how to carry out residual chlorine testing
Disinfection is a process that reduces the numbers of micro-organisms to a level at which they are not harmful. conductedto ensure compliance with environmental regulations and to assess the effectiveness of the ship’s sewage treatment system.
When sailing in areas where chlorine disinfection of treated waste water is required, the chemical dosing systemshould be prepared as follows:
Check that the chlorine container is filled. Fill it if needed.
Check that dosing pump is on and adjusted correctly.
Chlorine concentration must be monitored regularly. Residualchlorine should be 2-5 ppmin effluent. If chlorine testshows that residual chlorine is higher than 5 ppm or lower than 2 ppm, adjust chlorine pump’s stroking rate.
Disinfection chemical
Recommended disinfection chemical is sodium hypochlorite (NaClO), technical quality, concentration 10% activechlorine.The storage of chlorine solution should be in a dark room, temperature in between 10-15 °C otherwise it willloose free chlorine. The maximum storage time is 180 days at +10°C. The maximum storage time depends on storingtemperature i.e. the maximum storage time is only 50 days at +25°C if redundancy is 50%..
Disinfection
Disinfection chemical (e.g. Sodium hypochlorite (NaClO), solution, active chlorine 10%) is added to the clarified waterin the disinfection chamber to meet IMO’s requirements regarding presence of coliform bacteria in treated water.Residual chlorine must be kept between 2 ppm and 5 ppm. Residual chlorine can be adjusted by the dosing pump’ssettings and/or timer settings. Treated water can be pumped to sea or ashore by the discharge pump.
Residual chlorine test
Take a discharge water sample from a test cock after discharge pump while a discharge pump is running. Measurethe free chlorine content from the effluent with a test kit.
Test procedure:
1.Fill the sample glass and throw the first “sample” water away immediately. This action will increases test accuracy
significantly.
2.Fill the sample glass from the test cock after discharge pump while the discharge pump is running.
3.Immerse test paper in effluent.
4.Read the residual chlorine by comparing test papers color to the reference color map. For detailed information see
the test kit’s instructions.
describe the maintenance carried out on aerobic sewage treatment plants
Maintenance
Periodical maintenance of sewage treatment plant is required to ensure treatment process is running as designed and there is nomalfunctions with the risk of anaerobic process resulting formation of methane gas and toxic fumes. The tanks require de-sludging, usually every 3 months, this involves pumping the first
stage out via the discharge pump, the tank should never be totally emptied whilst it is still in operation or all the bacteria will be removed. Air diffusers are changed periodically as the diffuser holes enlarge over time and reduce the effectiveness of the aeration process. Air compressor inlet filters must be cleaned regularly and the compressor vanes must be checked for wear. The level in the chlorinator must be regularly checked and topped up as necessary. Observe that the treatment unit is operating normally and there is no alarms displayed. Check that sludge flows through the sludge return hose (by air lift) when the air blower is running. Check a smell of the unit. If the unit is smelling, it is most probably that aeration is not working and treatmentprocess has changed to anaerobic. These plants run well if not disturbed, it is best to leave them on line even during long passages where they do not have to run legally. If the flow of sewage into the plant is kept constant the size of the colony of bacteria will remain steady at the correct amount to fully digest all the sewage. If the flow is stopped and started the colony will die off and then have to expand instantly to digest the new sewage, this is not possible and the plant will not operate correctly. If the colony of bacteria are allowed to die off it will take between 7 and 14 days for a new colony to be established. Operation of the air lifts and air compressor outlet pressure (0.2 bar) must be checked every watch. Chlorine tablet level or dosing tank level must be maintained in coastal waters, within 12 n.m.
Every week
1.If the chemical dosing system is in use, check the chlorine content in the effluent water regularly.
2.Test sludge content in activation chamber I to ensure that mineral sludge content is within acceptable limits.
Take a sludge content test at least every week or every time when sludge “SLUDGE ALARM” is displayed.
Every month
1.Check that there is no obstruction in the aeration piping and in the air distributors.
2.Check that there is no obstruction in the overflow between the aeration chamber II and the settling chamber.
3.Check that there is no obstruction in the overflow between the settling chamber and the disinfection chamber.
4.Check that there is no obstruction in the venting line.
5.Inspect the tank’s external and internal coatings for corrosion.
6.Check vacuum function.
Every year
1.Empty and clean the unit.
2.Make sure that the unit is well ventilated and there is enough fresh air in the chamber if you have to goinside to avoid inhaling toxic fumes and suffocation. One person must stay outside of the tank and keep eye onperson who is working inside the unit.
3.Make sure that the waste water is lead to a proper holding tank (hull tank or collection tank) during shutdownor maintenance break.
4.Perform the maintenance for the components of the unit according to the component maintenance program.