BOD, COD, TSS and TDS in ETP Design: What Each Parameter Changes
- Dr. Anubhav Gupta

- Aug 8
- 13 min read
When an industrial ETP fails a laboratory test, four parameters appear repeatedly in discussions with plant teams:
BOD, COD, TSS and TDS.
They are often spoken about together, but they represent very different wastewater characteristics.
A high BOD result may point toward inadequate biological treatment.
High COD may indicate biodegradable load, refractory organics, oils, chemicals, concentrated process wastewater or untreated bypasses.
High TSS usually indicates a solids-separation problem.
High TDS is fundamentally different because dissolved salts cannot be removed by ordinary clarification or biological treatment.
Understanding these differences matters for both ETP design and Pollution Control Board compliance.
An industry whose ETP outlet exceeds its Consent to Operate conditions should not simply increase chemical dosing or install another filter. The correct response is to determine which parameter has failed, what wastewater source creates it, and which treatment stage should control it.
Under India's consent framework, State Pollution Control Boards administer consent requirements under the Water (Prevention and Control of Pollution) Act, 1974 and Air (Prevention and Control of Pollution) Act, 1981. The OCMMS framework notes that Water Act consent applies to industries, processes, treatment/disposal systems and relevant new or altered sewage/trade-effluent discharges.
For industries facing an outlet failure, SARK Engineers & Consultants supports ETP troubleshooting and pollution-control assessment, water balance review, ETP augmentation and compliance-linked technical diagnosis.
Quick Answer: What Do BOD, COD, TSS and TDS Tell You?
BOD indicates the biodegradable organic load that microorganisms may consume.
COD indicates the oxygen-equivalent demand associated with chemically oxidisable substances and is generally broader than BOD.
TSS measures suspended material that can often be removed through settling, clarification or filtration.
TDS represents dissolved salts and other dissolved substances that remain after suspended solids are separated.
In practical ETP design:
Parameter | Main treatment implication |
BOD | Biological treatment capacity |
COD | Source control + chemical/biological/advanced treatment |
TSS | Clarification and filtration |
TDS | Membrane recovery, segregation or evaporation |
BOD/COD ratio | Biodegradability indication |
High TSS + COD | Solids may be carrying organic load |
High TDS + COD | Conventional ETP may not be enough |
The four parameters should therefore never be treated as four versions of the same pollution problem.
What Is BOD?
Biochemical Oxygen Demand
BOD indicates the oxygen consumed by microorganisms while biologically degrading biodegradable organic matter under specified test conditions.
For industrial wastewater, BOD can originate from:
Food residues
Sugars and starches
Biodegradable process chemicals
Organic washing streams
Pulp and paper process water
Domestic sewage
Fermentation residues
Biodegradable oils and organics
A wastewater stream with substantial BOD generally requires biological treatment unless the source can first be eliminated, recovered or segregated.
How BOD Affects ETP Design
Higher BOD can affect:
Aeration requirement
Biological reactor volume
Oxygen-transfer demand
Biomass concentration
Sludge generation
Hydraulic retention time
Food-to-microorganism ratio
Nutrient requirement
Secondary clarifier loading
A biological ETP designed for 500 mg/L BOD cannot automatically be expected to perform satisfactorily if production changes push the actual inlet to 1,500–2,000 mg/L.
The important design quantity is not concentration alone.
It is pollution load.
For example:
Case A
Flow = 100 m³/dayBOD = 500 mg/L
Approximate BOD load:
50 kg/day
Case B
Flow = 50 m³/dayBOD = 1,000 mg/L
Approximate BOD load:
50 kg/day
The concentration is twice as high in Case B, but the total BOD load is similar.
This is why an ETP should be reviewed using both flow and concentration.
What Is COD?
Chemical Oxygen Demand
COD is a broader indicator of oxidisable pollution in wastewater.
Industrial COD may arise from:
Organic chemicals
Oils
Coolants
Dyes
Solvents
Process additives
Surface-treatment chemicals
Cleaning compounds
Pulping chemicals
Product losses
Concentrated washings
Domestic organic matter
Some COD may be readily biodegradable.
Some may biodegrade slowly.
Some may be refractory or toxic to the biological treatment system.
Therefore:
High COD does not automatically mean the aeration tank needs more air.
The source and nature of the COD must first be established.
Why COD Is So Important in Pollution Control Board Compliance
COD is frequently used as an effluent-performance indicator because it provides a broad measure of oxidisable pollution.
When an SPCB laboratory report or consent-monitoring report shows high outlet COD, the industry should investigate:
Actual inlet COD
Source-wise COD contribution
BOD/COD relationship
Oil and grease
Batch cleaning
Concentrated chemical streams
Biological performance
Equalisation
Sludge carryover
Tertiary treatment
Bypass or overflow
Do not assume that one numerical COD limit applies to every industrial facility.
Applicable limits may depend on the industry-specific standards, discharge route and the individual consent conditions. CPCB publishes both general and industry-specific effluent/emission standards, while State Boards incorporate applicable requirements through their consent mechanisms.
BOD vs COD: Why the Relationship Matters
One of the most useful diagnostic indicators is the relationship between BOD and COD.
A simple ratio is often used as an indication of biodegradability:
BOD / COD
A comparatively higher ratio may indicate that a meaningful portion of the organic load can be treated biologically.
A very low ratio can suggest:
Refractory organics
Toxic chemicals
Non-biodegradable COD
Industrial chemical contribution
High oxidation-resistant load
However, the ratio is a screening indicator rather than a complete treatment design criterion.
For industrial wastewater, actual treatability trials may still be required.
Example
Suppose:
COD = 2,000 mg/LBOD = 1,000 mg/L
BOD/COD = 0.50
Compare this with:
COD = 2,000 mg/LBOD = 200 mg/L
BOD/COD = 0.10
The COD concentration is identical, but the treatment challenge can be completely different.
The second wastewater may require much more emphasis on:
Source segregation
Chemical treatment
Oxidation
Adsorption
Recovery
Specialised treatment
rather than simply increasing biological reactor capacity.
What Is TSS?
Total Suspended Solids
TSS represents suspended particles present in wastewater.
Industrial TSS may include:
Metal particles
Fibres
Pulp
Process solids
Precipitated chemicals
Biological flocs
Soil
Grinding solids
Paint solids
Chemical sludge
Product particles
Unlike TDS, suspended solids can often be separated physically.
Treatment may involve:
Screening
Settling
Clarification
Coagulation
Flocculation
DAF
Tube settlers
Sand filtration
Membrane filtration
Why High Outlet TSS Does Not Necessarily Mean Poor Inlet Treatment
An ETP can remove dissolved pollution effectively but still fail TSS because of downstream solids carryover.
Common causes include:
Poor clarifier settling
High hydraulic loading
Excess sludge blanket
Bulking sludge
Pin flocs
Rising sludge
Improper polymer dosing
Filter breakthrough
Excessive backwash interval
Damaged filter media
High TSS can also increase measured COD because suspended organic solids contribute to the overall pollution load.
Therefore, if both TSS and COD rise together, the first investigation should include the clarification and filtration stages.
What Is TDS?
Total Dissolved Solids
TDS represents dissolved material in water rather than suspended particles.
Typical industrial contributors include:
Sodium salts
Chlorides
Sulphates
Calcium
Magnesium
Dissolved process chemicals
Acid/alkali neutralisation products
Cooling-tower blowdown
Boiler blowdown
Softener regeneration
DM-plant regeneration
RO reject
This creates a fundamentally different treatment challenge.
Why Conventional ETP Treatment Does Not Remove TDS Effectively
Screening does not remove dissolved salts.
Clarification does not substantially remove dissolved salts.
Biological treatment does not remove most inorganic dissolved salts.
Sand filtration does not convert dissolved salts into solids.
In fact, chemical treatment can sometimes increase TDS because acids, alkalis, coagulants and other chemicals add dissolved ions.
High-TDS wastewater may therefore require:
Source segregation
Process modification
Water reuse
Reverse osmosis
Nanofiltration in suitable applications
Evaporation
MEE
ATFD/crystallisation
Approved off-site treatment or disposal, where applicable
This is why an industry considering ZLD should first undertake a proper water balance and ZLD feasibility assessment.
BOD, COD, TSS and TDS: What Each Changes in ETP Design
Parameter | ETP design area most affected | Typical response |
BOD | Biological reactor | Aeration, biomass, HRT |
COD | Entire treatment train | Source mapping + treatability |
TSS | Clarifier and filtration | Settling and solids removal |
TDS | Recovery/ZLD system | Segregation, RO, evaporation |
Oil & grease | Pretreatment | Skimming, DAF, oil separation |
Heavy metals | Chemical treatment | pH-controlled precipitation |
Ammonia | Biological treatment | Nitrification |
pH | Equalisation/neutralisation | Controlled chemical dosing |
How These Parameters Affect State Pollution Control Board Compliance
This section is particularly important for industries searching for answers relating to:
Pollution Control Board ETP limits
SPCB effluent standards
ETP outlet COD limit
ETP outlet BOD limit
Pollution Control Board TSS limit
Pollution Control Board TDS limit
CTO wastewater conditions
CTE/CTO wastewater treatment requirements
failed SPCB sample
SPCB show-cause notice for ETP
Pollution Control Board consent renewal
ETP non-compliance
State Boards issue and administer consent under the statutory framework, while their online procedures, checklists, categorisation systems and consent conditions can differ from state to state. Rajasthan, for example, publishes separate procedures for CTE and CTO as well as checklists and consent fee information; its official CTO guidance states that consent is required before commencement of operation under the Water and Air Acts.
Haryana likewise maintains its own consent policy and consent procedures under the Water and Air Acts.
Therefore:
The applicable effluent standard should always be checked against the unit's current CTO, applicable industry-specific standards and approved discharge route—not copied from a generic online table.
Searching for UPPCB, RSPCB, HSPCB or Other State Board ETP Limits?
The engineering interpretation remains broadly similar even though the administrative authority changes.
An industrial unit may encounter searches such as:
Uttar Pradesh
UPPCB ETP outlet standards
UP Pollution Control Board COD limit
UPPCB BOD limit
UPPCB CTO effluent condition
UPPCB ETP failure
UPPCB show cause notice wastewater
Rajasthan
RSPCB ETP outlet limit
Rajasthan Pollution Control Board COD standard
RSPCB CTO wastewater condition
RSPCB ETP show cause
Rajasthan Pollution Control Board consent renewal
Haryana
HSPCB ETP outlet standards
Haryana Pollution Control Board COD limit
HSPCB CTO condition
HSPCB wastewater compliance
Haryana ETP consent renewal
Other states
The same search pattern applies to authorities such as:
Maharashtra Pollution Control Board
Gujarat Pollution Control Board
Punjab Pollution Control Board
Karnataka State Pollution Control Board
Tamil Nadu Pollution Control Board
Madhya Pradesh Pollution Control Board
Bihar State Pollution Control Board
West Bengal Pollution Control Board
Odisha State Pollution Control Board
The safest technical approach is always to verify the current consent and official Board requirements applicable to the actual unit.
What Should an Industry Check When an SPCB Sample Fails BOD?
If BOD exceeds the applicable consent limit, investigate:
Biological loading
Dissolved oxygen
Blower operation
Diffuser condition
Biomass health
Hydraulic retention time
Sludge age
Return sludge
Nutrient availability
Toxic process streams
Also compare inlet and outlet values.
If inlet BOD has increased substantially since the ETP was designed, the problem may be inadequate design capacity rather than operator performance.
What Should an Industry Check When COD Fails?
Check:
Product loss
Chemical wash
Concentrated batch discharge
Oil/coolant
Floor washing
Toxic chemical streams
RO reject mixing
Biological-treatment failure
Bypass
Sludge carryover
A useful diagnostic sequence is:
Source → Equalisation → Chemical treatment → Biological treatment → Clarifier → Filter → Final outlet
This prevents the common mistake of diagnosing only the final treatment stage.
What Should an Industry Check When TSS Fails?
Inspect:
Settling test
Sludge blanket
Clarifier overflow
Hydraulic loading
Return sludge
Excess sludge removal
Tube settler
PSF
Backwashing
Filter media
If the outlet looks cloudy, visible solids may provide an immediate clue.
But laboratory measurement is still required.
What Should an Industry Check When TDS Fails?
Start upstream.
Ask:
Where are salts entering the process?
Is RO reject being mixed into the ETP?
Is regeneration wastewater entering the ETP?
Has chemical dosing increased?
Is cooling-tower blowdown contributing?
Has freshwater TDS changed?
Is recycled water concentrating salts?
Does the plant actually require ZLD?
Increasing biological treatment will not solve a dissolved-salt problem.
What if the SPCB Laboratory Result Is Much Worse Than the Company's Own Report?
Do not immediately assume either laboratory is wrong.
Investigate:
Sampling location
Sampling time
ETP operating condition
Production during sampling
Sample preservation
Composite vs grab sample
Laboratory method
Tank mixing
Sludge carryover
Recent chemical dosing
Rainwater dilution
Bypass condition
The correct response is technical reconciliation followed by representative resampling, not merely obtaining another favourable report.
What if a Pollution Control Board Issues a Show-Cause Notice?
A show-cause notice linked to wastewater treatment should be treated as an engineering and regulatory problem together.
The response should normally be supported by:
Failed laboratory report
Root-cause diagnosis
Immediate containment action
Corrective actions completed
Photographic evidence
Flow records
Chemical-dosing records
ETP operating data
Independent testing
Implementation schedule
Responsible persons
Avoid submitting only a narrative saying:
“The ETP is now operating satisfactorily.”
A stronger response demonstrates what failed, what was corrected and how performance will be verified.
For this type of assignment, see SARK's pollution-control and regulatory support services.
Can a Plant Pass BOD and COD but Still Be Non-Compliant?
Yes.
The outlet may still fail:
TSS
TDS
Oil and grease
Metals
Ammonia
pH
Chlorides
Sulphates
Colour
Other industry-specific parameters
Conversely, visually clear water is not proof of compliance.
A clear sample can still contain high:
COD
TDS
Chlorides
Dissolved metals
Ammonia
Laboratory results must therefore be interpreted together.
Why State Pollution Control Boards Look Beyond One Laboratory Number
Consent compliance is not simply a single COD or BOD result.
State Boards may examine the broader consent and pollution-control arrangement, including matters such as:
Permitted production
Manufacturing process
Water consumption
Trade-effluent generation
Sewage generation
ETP/STP capacity
Air-emission sources
Pollution-control equipment
Waste handling
Discharge/reuse arrangements
Monitoring and records
The Water Act consent framework specifically covers industrial processes, treatment/disposal systems and relevant discharge outlets, which is why changes in production or wastewater configuration can become consent issues rather than only treatment issues.
When ETP Design and CTO Data No Longer Match
This is common in operating factories.
The CTO may show:
Trade effluent: 10 KLD
But actual operation may generate:
18 KLD
Or the consent may show one washing line while two additional lines have subsequently been installed.
This can affect:
Hydraulic load
BOD load
COD load
TDS
Sludge generation
Water consumption
Hazardous waste
ETP capacity
The correct approach is to reconcile:
Consent → Machinery → Production → Water balance → Wastewater → ETP capacity → Outlet quality
This is far stronger than treating an outlet exceedance as an isolated laboratory failure.
Pollution Load Matters More Than Concentration Alone
For any pollutant:
Pollution load = Flow × Concentration
Consider:
Plant A
Flow = 10 KLDCOD = 4,000 mg/L
COD load ≈ 40 kg/day
Plant B
Flow = 50 KLDCOD = 1,000 mg/L
COD load ≈ 50 kg/day
Plant A has a much higher concentration.
But Plant B actually sends more COD mass to the ETP every day.
This distinction is crucial when evaluating:
ETP aeration
Reactor capacity
Chemical requirement
Sludge generation
expansion
augmentation
Common Mistakes Industries Make With BOD, COD, TSS and TDS
Mistake 1: Treating COD and BOD as interchangeable
They indicate related but different wastewater characteristics.
Mistake 2: Increasing aeration for high TDS
Aeration does not remove dissolved salts.
Mistake 3: Increasing chemicals whenever COD rises
Chemicals may not remove dissolved or refractory COD.
Mistake 4: Ignoring flow
Concentration without flow does not describe total pollution load.
Mistake 5: Ignoring wastewater sources
Treatment should begin with source mapping.
Mistake 6: Using one laboratory result as the complete diagnosis
Trend data is much more useful.
Mistake 7: Copying an internet discharge limit
Use the applicable consent and official regulatory standard.
Mistake 8: Assuming clear water means compliant water
Many pollutants are dissolved and invisible.
Mistake 9: Sending every stream into one ETP
Segregation can substantially improve treatment.
Mistake 10: Modifying the plant without revising the water balance
Treatment capacity must reflect actual wastewater generation.
ETP Diagnostic Matrix
Result | Likely first concern | What to verify |
High BOD | Biological failure | DO, MLSS, loading |
High COD + high BOD | Organic overload | Source + biology |
High COD + low BOD | Refractory load | Source segregation |
High TSS | Solids carryover | Clarifier + filters |
High TDS | Dissolved salts | Reject/regeneration streams |
High COD + oil | Oily wastewater | Oil separation |
High TSS + COD | Organic solids carryover | Clarification |
High TDS after chemical treatment | Chemical salt addition | Dosing review |
Variable COD | Batch discharge | Equalisation |
Good outlet but occasional failure | Shock load/bypass | Hourly profiling |
What Data Should Be Reviewed Before Changing the ETP?
Collect at least:
Laboratory data
Inlet BOD
Outlet BOD
Inlet COD
Outlet COD
TSS
TDS
pH
Oil and grease
Relevant metals
Other consent parameters
Flow data
Average flow
Peak flow
Hourly generation
Batch discharge
Process information
Production
Raw materials
Chemicals
Cleaning
Washing
Product change
ETP operating data
Chemical dosing
DO
MLSS
blower hours
pump hours
sludge withdrawal
filter backwash
RO recovery
Regulatory documents
Consent to Establish
Consent to Operate
Latest amendments
Laboratory reports
Board inspection reports
Show-cause notices, if any
How SARK Engineers & Consultants Can Help
SARK Engineers & Consultants undertakes industrial wastewater and pollution-control assessments where laboratory results, ETP performance and consent requirements need to be evaluated together.
Typical scope includes:
BOD/COD/TSS/TDS interpretation
Wastewater characterisation
Source-wise pollution-load mapping
Water balance
ETP capacity verification
Chemical-treatment review
Biological-treatment assessment
Aeration review
Sludge diagnostics
Tertiary-treatment assessment
RO reject review
ZLD feasibility
Consent-condition reconciliation
SPCB notice technical response
ETP augmentation planning
Vendor design review
For plants already experiencing outlet failure, start with ETP troubleshooting and pollution-control consulting.
For plants where wastewater generation itself is uncertain, first rebuild the industrial water balance.
For significant capacity or process changes, SARK's project assessment services can review process, utilities, wastewater and statutory implications together.
Frequently Asked Questions
What is the permissible BOD limit for an ETP outlet?
There is no single number that should be assumed for every industrial ETP. The applicable requirement depends on the industry's consent conditions, applicable standards and discharge route. Industries should verify their current CTO and the official requirements of the relevant State Pollution Control Board.
What is the permissible COD limit under Pollution Control Board consent?
The applicable COD limit can vary according to industry, discharge route and consent conditions. The value written in the unit's current CTO and applicable official standards should be used for compliance assessment.
What should I do if the Pollution Control Board sample fails COD?
First prevent non-compliant discharge where necessary, verify the result and sampling point, identify the COD source, measure inlet and stage-wise COD and inspect equalisation, chemical treatment, biology, clarification and possible bypasses.
Does high COD mean the ETP needs more aeration?
Not necessarily. High COD may be caused by refractory chemicals, oil, concentrated process streams or bypasses that additional aeration will not solve.
Why can BOD be low while COD remains high?
This commonly indicates that a significant part of the COD is not readily biodegradable. Source-wise wastewater characterisation is needed.
Why does TSS remain high after biological treatment?
The biological process may be functioning while clarification or filtration is failing. Check sludge settling, hydraulic loading, sludge blanket and filter performance.
Can conventional ETP treatment reduce TDS?
Conventional physical, chemical and biological treatment generally has limited ability to remove dissolved salts. High TDS often requires segregation, membrane treatment, recovery or evaporation.
Which State Pollution Control Board decides my ETP outlet limit?
The relevant SPCB or Pollution Control Committee administers consent for the location of the facility, while applicable central/state standards and the specific consent conditions govern the unit.
Where should I check UPPCB ETP limits?
Check the current Consent to Operate issued to the facility and current official UPPCB/CPCB requirements applicable to the industry and discharge route rather than relying on a generic third-party table.
Where should I check RSPCB COD and BOD limits?
Check the facility's current Rajasthan State Pollution Control Board consent and applicable official standards. Rajasthan's official website provides CTE/CTO procedures and consent documentation resources.
What should a company do after receiving an SPCB show-cause notice for ETP failure?
The response should combine immediate containment, root-cause analysis, corrective actions, monitoring evidence, laboratory verification and a time-bound compliance plan.
Final Conclusion
BOD, COD, TSS and TDS are four different engineering signals.
BOD asks: can biological treatment handle the biodegradable organic load?
COD asks: what total oxidisable pollution is entering and leaving the system?
TSS asks: is solids separation working?
TDS asks: how will dissolved salts be controlled?
A successful ETP must answer all four questions.
And for regulatory compliance, one more question matters:
Does the actual plant, wastewater load, treatment system and outlet performance still match the current Consent to Operate?
When the answer is uncertain, increasing chemicals is rarely the best starting point.
Measure the flow.
Characterise the streams.
Calculate the load.
Trace the failure.
Then modify the treatment system.




Comments