Hospital Wastewater Treatment System Design Nepal: Flow, Loads and Process Train
Hospital wastewater treatment system design Nepal work starts from 0.2 to 0.5 m³/bed/day. A 100-bed hospital at that rate needs 20–50 m³/day. Inland gazette figures used by WECS set BOD at 50 mg/L and COD at 250 mg/L. MoHP's 2021 WASH reprint in 2023 sets facility water use, not this effluent table.
Installed cost in the original project range is $50,000–$200,000 for 50–300 beds and 10–100 m³/day, when the train reaches >95% COD removal and 99% pathogen kill. Most plants we size for valley hospitals land near the low end of 0.2 to 0.5 m³/bed/day if laundry is separated. A buyer note that still reads wastewatwer treatment plant hospital in nepal is asking for that same capacity band.
Hospital wastewater contains antibiotics, pathogens and chemical residues. Ciprofloxacin, metronidazole and lipid regulators show up with patient excreta. The train below is screening, equalization, solids removal, biology and a disinfectant. Domestic package plants miss the last two duties.
Why Hospital Wastewater in Nepal Requires Specialized Treatment
Hospital wastewater in Nepal carries antibiotics, pathogens and chemical residues at higher load than domestic sewage. Earlier compilations used a ResearchGate 2022 note that hospital COD can be 2–5 times domestic sewage. A WHO 2023 note in that same draft says hospital wastewater can account for 30–50% of AMR genes in urban water. Treat both figures as background until the site lab sheet is in hand.
Earlier hospital briefs required a Biological Oxygen Demand (BOD) of less than 50 mg/L, COD less than 100 mg/L, and fecal coliform counts below 1,000 Most Probable Number (MPN) per 100mL. Domestic sewage limits in those briefs were looser. Chemotherapy drugs, radiopharmaceuticals and disinfectants need steps that a standard domestic STP does not include.
According to ENPHO, 361 raw samples taken across Nepal from 2012 to 2017 had a mean BOD of 459 mg/L and a mean COD of 774 mg/L, all sources combined. The hospital subset in that note shows pH 7.5 (±0.5), DO 1.0 (±1.1) mg/L, oil and grease 15 (±22) mg/L and EC 1373 (±485) µS/cm. On plants we sample before design, grease sits nearer that hospital mean than a food-factory peak.
| Contaminant Type | Typical Hospital Wastewater (mg/L or MPN/100mL) | Typical Domestic Sewage (mg/L or MPN/100mL) | Health/Environmental Impact |
|---|---|---|---|
| COD | 300-800+ | 150-300 | Oxygen depletion in receiving waters, toxicity |
| BOD | 150-400+ | 100-250 | Oxygen depletion in receiving waters |
| TSS | 100-300+ | 50-150 | Turbidity, habitat degradation |
| Fecal Coliform | 106-108+ | 105-107 | Pathogen transmission, waterborne diseases |
| Antibiotics | Trace to significant levels | Negligible | Antimicrobial resistance (AMR) development |
| Heavy Metals (e.g., Mercury, Silver) | Variable, often higher | Low | Toxicity to aquatic life, bioaccumulation |
| Radiopharmaceuticals | Trace levels (from nuclear medicine) | None | Radioactive contamination, long-term health risks |
| Chemotherapy Drugs | Trace levels (from oncology units) | None | Cytotoxicity, genotoxicity, environmental persistence |
hospital effluent compliance mohp standards nepal
Hospital effluent compliance with MoHP standards in Nepal is a WASH duty on the facility, while the numeric discharge table still comes from the environment gazette.

Earlier guidance in hospital briefs used a MoHP 2023 set: BOD of 50 mg/L, COD of 100 mg/L, TSS of 30 mg/L, fecal coliform below 1,000 MPN/100mL, and zero detectable E. coli. Those briefs also said Gazette Notification 2023/11 applied to hospitals with more than 20 beds, and that hospitals exceeding 100 beds needed an EIA. The MoHP National Standards on WASH for Healthcare Facilities, 2021, reprinted in 2023, do not contain that effluent table.
According to that MoHP text, drinking water must meet E. That zero is a tap-water limit, not an effluent limit. MoHP Schedule 10 sets IPD supply at 40-60 litres/patient/day plus 15 litres/caregiver/day, and staff use at 50-100 litres/person/day. Supply is not the sewer flow used for tank volume.
According to the WECS paper at the 21st WEPA meeting on 8 September 2025, inland surface limits come from the Nepal Gazette of 30 April 2001 and 23 June 2003. Those inland maxima are BOD 50 mg/L at 20 degree C, COD 250 mg/L, TSS 30-200 mg/L and pH 5.5–9.0. Public sewer maxima in that table are BOD 400 mg/L, COD 1000 mg/L and TSS 600 mg/L. Ammoniacal nitrogen is 50 mg/L max on both outfalls.
Oil and grease is 10 mg/L max to inland water and 50 mg/L max to a public sewer. Mercury is 0.01 mg/L max in that gazette table. ENPHO cites a GoN 2012 inland table at BOD 100 mg/L, COD 250 mg/L and TSS 200 mg/L. Most permits we read still paste the inland row even when the pipe joins a sewer, so design to the number the clearance actually writes.
| Outfall in the Nepal Gazette table (30 April 2001 and 23 June 2003) | BOD5 at 20 degree C (mg/L, max) | COD (mg/L, max) | TSS (mg/L, max) | pH |
|---|---|---|---|---|
| Inland surface water | 50 | 250 | 30-200 | 5.5–9.0 |
| Public sewer | 400 | 1000 | 600 | 5.5–9.0 |
Which effluent limits should the permit use?
Use the limit written for the outfall, not a remembered hospital sheet. Inland surface water in the 2001 and 2003 gazette table is BOD 50 mg/L and COD 250 mg/L, while a public sewer in that table is BOD 400 mg/L and COD 1000 mg/L. ENPHO's GoN 2012 inland row is BOD 100 mg/L and COD 250 mg/L. If the clearance still says COD of 100 mg/L, design to 100 mg/L and file the gazette number beside it.
The comparison table below is the earlier MoHP 2023 brief. Keep it as the project target only when the permit copies those cells. pH 6.0 - 9.0 in that brief is tighter on the low side than gazette pH 5.5–9.0.
| Parameter | MoHP 2023 Standard (mg/L or MPN/100mL) | Domestic Wastewater Standard (Typical, mg/L or MPN/100mL) | Relevance |
|---|---|---|---|
| BOD5 | < 50 | < 100-200 | Measures organic pollution, impacts dissolved oxygen |
| COD | < 100 | < 250-400 | Measures total organic pollutants, including non-biodegradable |
| TSS | < 30 | < 50-100 | Impacts water clarity, habitat smothering |
| Fecal Coliform | < 1,000 | < 1,000-10,000 | Indicator of fecal contamination and pathogen presence |
| E. coli | 0 (Non-detectable) | < 1,000-10,000 | Specific indicator of human fecal contamination |
| pH | 6.0 - 9.0 | 6.0 - 9.0 | Ensures aquatic life compatibility |
| Total Nitrogen (TN) | (Emerging concern, often <10-15) | (Variable) | Eutrophication potential |
| Total Phosphorus (TP) | (Emerging concern, often <1-2) | (Variable) | Eutrophication potential |
mbr membrane bioreactor for hospital effluent nepal
An MBR membrane bioreactor for hospital effluent in Nepal is the secondary step when COD removal must reach 95+ percent and pathogen removal must reach 99+ percent on a small plot.
The comparison table rates that footprint about 60% smaller than a conventional plant. Operating cost sits in the moderate-to-high band because of power and membrane replacement. Fouling is the usual failure, not a lack of biology. A clean every six months kept the Kathmandu case inside its COD limit.
When does an MBR fit a Nepal hospital?
An MBR fits when land is tight and the outfall is at or below inland gazette BOD of 50 mg/L. A constructed wetland in the same table removes 60-85 percent of COD and needs a large plot. Plants we size on inner Kathmandu plots pick the MBR row for that footprint. A site with spare land can still use the wetland row at $0.05 - $0.15 per m³.
chlorine dioxide disinfection hospital wastewater nepal
Chlorine dioxide disinfection for hospital wastewater in Nepal is a tertiary kill step, rated in the comparison table at 99.9% for bacteria and viruses.
The same row lists a very compact footprint and no harmful disinfection byproducts, unlike a heavy chlorine contact tank. Generation is on site, and the dose should see low solids or the chemical spends itself on particles. COD removal is not the job of this stage, and the table marks COD removal as N/A.
Neither number is a wastewater residual setpoint. Plants we commission place ClO₂ generation after the membrane so the dose is not wasted on sludge.
Where should chlorine dioxide sit in the train?
Chlorine dioxide sits after biological treatment and solids removal, as the last barrier before the outfall. Put it downstream of an MBR when pathogen removal must reach 99+ percent in the membrane and 99.9% at the disinfectant. Do not use the MoHP surface-cleaning strength as the generator setpoint. Confirm residual and contact time on the cleared design, not from a floor-mop recipe.
Treatment Technologies for Hospital Wastewater in Nepal: A Comparison
Treatment technology for hospital wastewater in Nepal is a balance of effluent limit, plot area, power and the contaminants that actually arrive. MBR systems in this comparison reach over 99% pathogen removal and 95% COD reduction, with a footprint up to 60% less than conventional tanks. DAF, used as pre-treatment, can take 90–95% of suspended solids and fats, oils and grease. That step earns its keep when the kitchen shares the ward drain.
Constructed wetlands remove 60-85 percent of COD at very low power, but they need land. A two-stage constructed wetland was built at Dhulikhel Hospital, which shows the option is real where area exists. A combined train is common: DAF, then MBR, then chlorine dioxide. Plants we compare skip DAF only when a grease trap already keeps kitchen oil off the sewer.
| Technology | Primary Application | Typical COD Removal (%) | Typical Pathogen Removal (%) | Footprint | Operating Cost | Key Advantages | Key Disadvantages |
|---|---|---|---|---|---|---|---|
| MBR Membrane Bioreactor | Secondary and Tertiary Treatment | 95+ | 99+ | Compact (60% smaller than conventional) | Moderate to High (energy, membrane replacement) | High effluent quality, small footprint, effective for difficult-to-treat wastewater | Higher capital cost, requires skilled operation, membrane fouling potential |
| Dissolved Air Flotation (DAF) | Pre-treatment, Solids/FOG Removal | Variable (depends on feed) | Low to Moderate | Moderate | Moderate (energy, chemical coagulants) | Effective for suspended solids and FOG, improves downstream process efficiency | Chemical costs, sludge production, not a complete treatment solution |
| Chlorine Dioxide (ClO₂) Disinfection | Tertiary Treatment (Disinfection) | N/A | 99.9% (bacteria, viruses) | Very Compact | Moderate (chemical production) | High disinfection efficacy, no harmful byproducts, effective against a broad spectrum of microorganisms | Requires on-site generation equipment, potential for oxidation of some compounds |
| Constructed Wetlands | Secondary/Tertiary Treatment | 60-85 | 70-90 | Large (requires significant land area) | Very Low (minimal energy, chemicals) | Low operating cost, low energy consumption, robust and resilient | Large land requirement, performance can be affected by climate, slower treatment rates |
Engineering Specifications for Hospital Wastewater Treatment Systems

Design flow for a hospital plant in Nepal is 0.2 to 0.5 m³/bed/day on the figures used in this guide. A 100-bed hospital then needs 20–50 m³/day of capacity. Influent COD is typically 300–800 mg/L, BOD is 150–400 mg/L, suspended solids run 100–300 mg/L, and fecal coliform can reach 106–108 MPN/100mL. The earlier MoHP 2023 targets in the spec table are COD < 100 mg/L, BOD < 50 mg/L, TSS < 30 mg/L and fecal coliform < 1,000 MPN/100mL.
Pre-treatment starts with screening, and many sites use rotary bar screens ahead of an equalization tank that buffers flow and concentration. Primary solids and FOG can go to DAF, biology follows, and disinfection closes the train. MoHP also asks for at least two days of stored water supply on the facility, and that tank is potable backup, not the wastewater equalizer.
For the packaged hospital train, specify the Medical & Hospital Wastewater Treatment System when the plot cannot hold separate civil tanks. Match its duty to measured flow, not to the nameplate of a neighbouring hotel. Hold chemotherapy waste and radiopharmaceuticals off this drain. They are not a load the biological stage is meant to digest.
| Parameter | Typical Influent (Hospital Wastewater, Nepal) | Target Effluent (MoHP 2023 Standard) | Units | Notes |
|---|---|---|---|---|
| Flow Rate | 0.2 - 0.5 (per bed) | N/A (System Capacity Dependent) | m³/bed/day | Example: 100-bed hospital = 20-50 m³/day system |
| COD | 300 - 800+ | < 100 | mg/L | High organic load from pharmaceuticals, excreta |
| BOD5 | 150 - 400+ | < 50 | mg/L | Biodegradable organic matter |
| TSS | 100 - 300+ | < 30 | mg/L | Suspended solids, sludge |
| Fecal Coliform | 106 - 108+ | < 1,000 | MPN/100mL | Indicator of fecal contamination and pathogens |
| E. coli | 105 - 107+ | 0 (Non-detectable) | MPN/100mL | Strict requirement for human health safety |
| Ammonia Nitrogen (NH3-N) | Variable (can be high) | < 10-20 (depending on discharge) | mg/L | Requires nitrification/denitrification in biological stage |
| Total Nitrogen (TN) | Variable | < 10-15 (for sensitive receiving waters) | mg/L | Eutrophication potential |
| Total Phosphorus (TP) | Variable | < 1-2 (for sensitive receiving waters) | mg/L | Eutrophication potential |
| pH | 5.5 - 8.5 | 6.0 - 9.0 | - | Neutral range for biological processes and discharge |
hospital wastewater eia permitting nepal
Hospital wastewater EIA permitting in Nepal follows the Environment Protection Act 2019 and the Environment Protection Rules 2020, not a bed-count line inside the MoHP WASH reprint.
WECS states that the Act mandates EIA and IEE for prescribed projects, including wastewater activities, and that the government sets effluent standards. The Environment Protection Rules, 2020 set the clearance steps, and effluent volume is not explicitly defined. The facility is identified when the IEE or EIA is registered, and earlier briefs said hospitals with more than 20 beds must treat and hospitals exceeding 100 beds must file an EIA. Ask the approving ministry which schedule row applies before the plot is frozen.
MoHP WASH categories are about service level, not a discharge permit. Category I covers a general hospital with 100 to 300 beds, Category II covers a general hospital with 25 to 50 beds, and Category III is a basic health service centre. Files we see stall when equipment is ordered before the IEE starts. WECS also lists a pharmaceutical industry standard dated 13 August 2012, and a hospital ward is not that factory row.
When does a hospital wastewater EIA apply?
A hospital wastewater project needs an IEE or an EIA when the proposal is a prescribed project under the Environment Protection Rules, 2020. WECS states that the facility number comes from that registration, not from a published cubic-metre cutoff. Earlier briefs tied a full EIA to hospitals exceeding 100 beds. Use that bed count as a planning flag, then confirm the schedule with the ministry that approves the file.
Cost Breakdown: Hospital Wastewater Treatment Plants in Nepal
Capital cost in the Nepal benchmarks used here runs from $1,000 to $3,000 per m³/day of capacity. A 50 m³/day MBR system (MBR integrated wastewater treatment) falls between $50,000 and $150,000. Operating cost is $0.20 and $0.50 per m³ treated, covering power, chemicals, sludge and labour, as estimated by industry benchmarks in Nepal (Ion Exchange Nepal 2024). Plants we cost at 50 m³/day usually land inside the $75,000 - $150,000 MBR band before freight and civil works.
The payback column in the table assumes a fine is actually assessed. Under the Environment Protection Act 2019 the fine is up to NPR 500,000 for a breach of EIA or IEE conditions. Earlier notes convert that sum as approximately $3,800 USD and describe it as NPR 500,000 annually if the breach repeats. Avoided penalties are not a revenue line, and reuse for irrigation or cooling can cut freshwater purchase only after the permit allows that reuse.
Financing paths named in earlier notes include the Nepal Climate Fund, ADB and World Bank loans, and BOOT contracts.
| Technology | Estimated Capital Cost (50 m³/day) | Estimated Operating Cost (per m³) | Key Cost Drivers | Payback Period (from avoided fines) |
|---|---|---|---|---|
| MBR System | $75,000 - $150,000 | $0.30 - $0.50 | Membrane replacement, energy, skilled labor | 2-4 years |
| DAF + Biological Treatment + ClO₂ Disinfection | $60,000 - $120,000 | $0.25 - $0.45 | Chemicals (coagulants, ClO₂), energy, sludge handling | 2-3 years |
| Constructed Wetlands (Multi-stage) | $30,000 - $70,000 (Requires significant land) | $0.05 - $0.15 | Land acquisition, initial planting, minimal maintenance | 1-2 years (if fines are high) |
Case Study: Hospital Wastewater Treatment System in Kathmandu

A 200-bed hospital in Kathmandu was generating about 40 m³/day with high organic and microbial load. The installed train was a HydropureWater WSZ Series MBR system (/product/1-wsz-underground-integrated-sewage-treatment.html) followed by chlorine dioxide disinfection (/product/11-chlorine-dioxide-generator.html). Influent COD of 650 mg/L fell to 45 mg/L, under the 100 mg/L limit used on that job. Fecal coliform near 107 MPN/100mL fell to less than 10 MPN/100mL.
Capital cost was $95,000, and operating cost averaged $0.35 per m³. Against a potential fine of NPR 500,000 per year, the notes give a payback of about three years from avoided penalties alone. Operator training and a membrane clean every six months were the two lessons that kept that result. Plants we revisit still need that six-month clean even when the last sample passed.
WECS records Bagmati stretches with BOD above 300 mg/L, so a Kathmandu outfall is not discharging into clean water. Plot limits and an equipment checklist for that city sit in Hospital Wastewater Treatment in Kathmandu: 2026 Engineering.
Who This Design Note Is For
This note is for the engineer sizing a plant at a Nepal hospital that discharges to a river or a municipal sewer. MoHP Category I is a general hospital with 100 to 300 beds. Category II includes a general hospital with 25 to 50 beds. Most inquiries that reach a sizing desk are 50–300 bed sites, which matches the capital band of $50,000–$200,000.
Look elsewhere if the site is a Category III clinic with no laboratory, laundry or inpatient ward. MoHP Schedule 13 allows a two-chamber septic tank held for four hours and emptied every five years, with sludge taken to a treatment plant. That tank is not an MBR substitute once wards, a kitchen and a lab share one drain.
Lock these checks before equipment is ordered.
- Name the outfall: inland surface water or public sewer.
- Copy BOD, COD, TSS and pH from the clearance, and keep the gazette row beside them.
- Measure the drain before locking 0.2 to 0.5 m³/bed/day.
- Keep kitchen FOG off the biological line when oil and grease is near 15 mg/L or higher.
- Keep chemotherapy waste and radiopharmaceuticals on a separate controlled path.
- Plan a membrane clean every six months and a sample log for the approving agency.
Non-compliance with an approved EIA or IEE can draw a fine up to NPR 500,000. WECS also notes blacklisting for up to 5 years, and DoEnv inspects 100 to 150 industrial sites a year, so do not wait for an inspector to find a missed sample. Send bed count, measured flow and outfall type with a hospital plant design request so the train is sized to the permit.
Frequently Asked Questions
What are the main challenges in treating hospital wastewater in Nepal?
The main challenge is a mixed load of antibiotics, pathogens and disinfectants that a domestic plant is not sized to cut to gazette limits. Hospital COD often sits at 300-800+ mg/L, against domestic sewage at 150-300 mg/L, and fecal coliform can reach 106-108+ MPN/100mL. Many sites also lack a trained operator for membrane cleaning. ENPHO lab records for Nepal, covering samples from 2012 to 2017, show hospital oil and grease averaging 15 mg/L.
How does hospital wastewater differ from domestic sewage?
Hospital wastewater carries antibiotics, disinfectants and sometimes chemotherapy drugs that domestic sewage does not. Research notes cited in this guide put hospital COD at 2–5 times domestic sewage, with table values of 300-800+ mg/L versus 150-300 mg/L. Fecal coliform sits at 106-108+ MPN/100mL in hospital wastewater versus 105-107 MPN/100mL in domestic sewage. Heavy metals such as mercury and silver are variable on the hospital side and low in domestic sewage.
What is the role of MBR technology in hospital wastewater treatment?
An MBR membrane bioreactor combines aeration with membrane separation and is the secondary step when the permit needs both low solids and high pathogen removal. The comparison table gives typical COD removal of 95+ percent and pathogen removal of 99+, in a footprint about 60% smaller than a conventional plant. Membrane replacement and power keep operating cost in the $0.30 - $0.50 per m³ band shown for a 50 m³/day unit.
Can hospital wastewater be reused in Nepal?
Treated hospital wastewater can be reused for irrigation or cooling makeup only after disinfection and a permit check. The Kathmandu case cut COD from 650 mg/L to 45 mg/L and fecal coliform from about 107 MPN/100mL to less than 10 MPN/100mL. That water is for non-potable use. Drinking water is a separate standard: MoHP sets E. coli at 0 cfu/100 ml in Nepal Gazette 2079/03/02.
What are the typical penalties for non-compliance with hospital effluent standards in Nepal?
The Environment Protection Act 2019 allows a fine up to NPR 500,000 for a breach of EIA or IEE conditions, according to the WECS briefing at the 21st WEPA meeting on 8 September 2025. The same briefing notes blacklisting for up to 5 years when an approved IEE or EIA is ignored. Earlier notes in this guide also cite about $3,800 USD and, in severe cases, facility closure.