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CYPRUS INTERNATIONAL UNIVERSITY
INDUSTRIAL WASTE WATER TREATMENT (OIL REFINERY)
By
ELEGBELEYE OLADIPO AYODAMOPE (20143234)
 INTRODUCTION
 PROCESS UNITS FOUND IN A REFINERY
 OVERVIEW OF OIL REFINERY WASTE PRODUCTION
 REFINERY WATER
 REFINERY WASTEWATER TREATMENT
 WASTEWATER TREATMENT SCHEME
 Environmental Standards for Petroleum Oil Refineries Effluent
 PUBLIC HEALTH CONCERNS
 Dissolved Air Flotation
 Activated Sludge
 Nitrification With Denitrification
 CONCLUSION
 An oil refinery is an industrial process plant
where crude oil is processed and refined into
more useful products such as petroleum
naphtha, gasoline, diesel fuel, asphalt base,
heating oil, kerosene, and liquefied petroleum
gas.
 Oil refineries are typically large, sprawling
industrial complexes with extensive piping
running throughout, carrying streams of fluids
between large chemical processing units.
PROCESS UNITS FOUND IN A REFINERY
•De-salter unit washes out salt from the crude oil before it enters the atmospheric
distillation unit.
•Atmospheric distillation unit distills crude oil into fractions.
•Vacuum distillation unit further distills residual bottoms after atmospheric
distillation.
•Naphtha hydro-treater unit uses hydrogen to desulfurize naphtha from
atmospheric distillation. Naphtha is hydro-treat ed before sending to a catalytic
reformer unit.
•Catalytic reformer unit is used to convert the naphtha-boiling range molecules
into higher octane reformate (reformer product).The reformate has higher content of
aromatics and cyclic hydrocarbons). An important byproduct of a reformer is
hydrogen released during the catalyst reaction. The hydrogen is used either in the
hydrotreaters or the hydrocracker.
•Distillate hydrotreater desulfurizes distillates (such as diesel) after atmospheric
distillation.
•Fluid Catalytic Cracker (FCC) unit upgrades heavier fractions into lighter, more
valuable products.
•Hydrocracker unit uses hydrogen to upgrade heavier fractions into lighter, more
valuable products.
Overview of Oil Refinery Waste
Production
The generation of waste is an inevitable consequence of the
operation of refineries and depots. Waste production in
refineries and terminals represents a high operating cost
and as such its minimization should be a priority. Waste
substances generated by oil refineries fall into two
categories:
• Non-hazardous waste, e.g. scrap metal, spent catalytic
cracking catalyst or “domestic” waste.
• Hazardous waste, e.g. asbestos, acid tars, sludge with a
high lead content or many oil contaminated materials such
as untreated waste water discharges.
Refinery Wastewater Treatment
• In a refinery wastewater treatment system, two steps of oil removal
are typically required to achieve the necessary removal of free oil
from the collected wastewater prior to feeding it to a biological
system.
• This oil removal is achieved by using an APIseparator followed by
a dissolved air flotation (DAF) or induced air flotation (IAF) unit
The wastewater from the secondary oil/water separation unit is
sent to the equalization system that is used to dampen out
variations in flow and concentration in the refinery wastewater.
Refinery Wastewater Treatment
cont’d
• The wastewater is then routed to the aeration
tank/clarifier which constitutes the biological
system
The effluent from the clarifier is then sent to
tertiary treatment (if necessary) prior to discharge.
S
/
N
Parameter Limiting value for concentration
(mg/l, except for pH)
Limiting value for quantum
(kg/1000 tonne of crude processed,
except for pH)
1 Ph 6.0 – 8.5 -
2 Oil and Grease 5 2
3 BOD3, 27o
C 15 6
4 COD 125 50
5 SS 20 8
6 Phenol 0.35 0.14
7 Sulphide 0.5 0.2
8 CN 0.2 0.08
9 Ammonia as N 15 6
1
0
TKN 40 16
1
1
P 3 1.2
1
2
Cr(VI) 0.1 0.04
1
3
TOTAL (Cr) 2.0 0.8
1
4
Pb 0.1 0.04
1
5
Hg 0.01 0.004
1
6
Zn 5.0 2
1
7
Ni 1.0 0.4
1
8
Cu 1.0 0.4
1
9
V 0.2 0.8
2
0
Benzene 0.1 0.04
2
1
Benzo(a)Pyrene 0.2 0.8
Water and solid wastes emanating from refineries has
damaging effect on public health and the environment
when pollution parameters are above the set standards.
Localized waste water discharges and habitat degradation
contaminate water supplies, farming lands and fisheries in
poor regions of Ecuador and the Niger River Delta.
Cancer-causing chemicals such as benzene primarily
affect the health of those living in close proximity to
refineries.
Populations living in inner cities often suffer most from
concentrated air pollution -- soot and ozone -- due to the
proximity with truck and bus routes.
Dissolved Air Flotation
• The first step in a DAF system is coagulation/ flocculation.
Dispersed particles (oil/solids) are stabilized by negative electric
charges on their surfaces, causing them to repel each other.
• they do not settle, since this prevents these charged particles from
colliding to form larger masses, called flocs.
• Chemical coagulation and flocculation are required to assist in the
removal of colloidal particles from suspension.
• These processes, usually done in sequence, are a combination of
physical and chemical procedures.
Dissolved Air Flotation—a Typical DAF
Unit
Activated Sludge
• An activated sludge process is the most effective of all the
biological systems available
• It is used in many refineries around the world and offers a
reliable method of biological treatment.
• Activated sludge is a continuous suspension of aerobic
biological growths in a wastewater containing entrapped
suspended colloidal, dissolved organic and inorganic
materials.
The PACT® (Powdered Activated Carbon Treatment)
system
Nitrification With
DenitrificationThe biological treatment system could include either a
nitrification(by the use of nitrifying bacteria) or a combined
nitrification/denitrification step in some cases when a refinery
site is required to meet tight ammonia or nitrogen limits.
The level of nitrogen compounds in refinery wastewater can
be controlled by avoiding discharges of spent amines and
proper removal of ammonia in the sour water stripper.
Nitrification is the term used to describe the two-step
biological process in which ammonia (NH4-N) is oxidized to
nitrite (NO2-N) and the nitrite is oxidized to nitrate (NO3-N).
Nitrification
Nitrification With Denitrification
• In denitrification, the nitrate is reduced to nitric oxide, nitrous oxide
and nitrogen gas.
 Oil has many benefits and energy is necessary for
all our activities. But each stage in its life cycle
carries hazards for humans, wildlife and the
environmental systems on which we and other
species depend.
 Understanding the health and environmental
consequences of oil use may help decision makers
assess the true costs of our dependence on this
non-renewable resource hence one major reason
why there is the ultimate need to treat our water
and wastewater discharges emanating from all oil
refineries to meet set international standards.
Reference
Gary, James H., Glenn E. Handwerk, and Mark J. Kaiser.
Petroleum refining: technology and economics. CRC press,
2007.
• Leffler, William L. "Petroleum refining for the nontechnical
person." (1985).
• The Environment (Protection) Rule, 1986 are referred to as
principal rules in all subsequent Notifications beginning with
S.O. 32(E), dated 16.2.1987 published in the Gazette No.
66, dated 16.2.1987
.
• EPA Notification [G.S.R 186(E), dt. 18th March, 2008]
Thank You

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Oil and gas refinery

  • 1. CYPRUS INTERNATIONAL UNIVERSITY INDUSTRIAL WASTE WATER TREATMENT (OIL REFINERY) By ELEGBELEYE OLADIPO AYODAMOPE (20143234)
  • 2.  INTRODUCTION  PROCESS UNITS FOUND IN A REFINERY  OVERVIEW OF OIL REFINERY WASTE PRODUCTION  REFINERY WATER  REFINERY WASTEWATER TREATMENT  WASTEWATER TREATMENT SCHEME  Environmental Standards for Petroleum Oil Refineries Effluent  PUBLIC HEALTH CONCERNS  Dissolved Air Flotation  Activated Sludge  Nitrification With Denitrification  CONCLUSION
  • 3.  An oil refinery is an industrial process plant where crude oil is processed and refined into more useful products such as petroleum naphtha, gasoline, diesel fuel, asphalt base, heating oil, kerosene, and liquefied petroleum gas.  Oil refineries are typically large, sprawling industrial complexes with extensive piping running throughout, carrying streams of fluids between large chemical processing units.
  • 4. PROCESS UNITS FOUND IN A REFINERY •De-salter unit washes out salt from the crude oil before it enters the atmospheric distillation unit. •Atmospheric distillation unit distills crude oil into fractions. •Vacuum distillation unit further distills residual bottoms after atmospheric distillation. •Naphtha hydro-treater unit uses hydrogen to desulfurize naphtha from atmospheric distillation. Naphtha is hydro-treat ed before sending to a catalytic reformer unit. •Catalytic reformer unit is used to convert the naphtha-boiling range molecules into higher octane reformate (reformer product).The reformate has higher content of aromatics and cyclic hydrocarbons). An important byproduct of a reformer is hydrogen released during the catalyst reaction. The hydrogen is used either in the hydrotreaters or the hydrocracker. •Distillate hydrotreater desulfurizes distillates (such as diesel) after atmospheric distillation. •Fluid Catalytic Cracker (FCC) unit upgrades heavier fractions into lighter, more valuable products. •Hydrocracker unit uses hydrogen to upgrade heavier fractions into lighter, more valuable products.
  • 5.
  • 6. Overview of Oil Refinery Waste Production The generation of waste is an inevitable consequence of the operation of refineries and depots. Waste production in refineries and terminals represents a high operating cost and as such its minimization should be a priority. Waste substances generated by oil refineries fall into two categories: • Non-hazardous waste, e.g. scrap metal, spent catalytic cracking catalyst or “domestic” waste. • Hazardous waste, e.g. asbestos, acid tars, sludge with a high lead content or many oil contaminated materials such as untreated waste water discharges.
  • 7.
  • 8. Refinery Wastewater Treatment • In a refinery wastewater treatment system, two steps of oil removal are typically required to achieve the necessary removal of free oil from the collected wastewater prior to feeding it to a biological system. • This oil removal is achieved by using an APIseparator followed by a dissolved air flotation (DAF) or induced air flotation (IAF) unit The wastewater from the secondary oil/water separation unit is sent to the equalization system that is used to dampen out variations in flow and concentration in the refinery wastewater.
  • 9. Refinery Wastewater Treatment cont’d • The wastewater is then routed to the aeration tank/clarifier which constitutes the biological system The effluent from the clarifier is then sent to tertiary treatment (if necessary) prior to discharge.
  • 10.
  • 11. S / N Parameter Limiting value for concentration (mg/l, except for pH) Limiting value for quantum (kg/1000 tonne of crude processed, except for pH) 1 Ph 6.0 – 8.5 - 2 Oil and Grease 5 2 3 BOD3, 27o C 15 6 4 COD 125 50 5 SS 20 8 6 Phenol 0.35 0.14 7 Sulphide 0.5 0.2 8 CN 0.2 0.08 9 Ammonia as N 15 6 1 0 TKN 40 16 1 1 P 3 1.2 1 2 Cr(VI) 0.1 0.04 1 3 TOTAL (Cr) 2.0 0.8 1 4 Pb 0.1 0.04 1 5 Hg 0.01 0.004 1 6 Zn 5.0 2 1 7 Ni 1.0 0.4 1 8 Cu 1.0 0.4 1 9 V 0.2 0.8 2 0 Benzene 0.1 0.04 2 1 Benzo(a)Pyrene 0.2 0.8
  • 12. Water and solid wastes emanating from refineries has damaging effect on public health and the environment when pollution parameters are above the set standards. Localized waste water discharges and habitat degradation contaminate water supplies, farming lands and fisheries in poor regions of Ecuador and the Niger River Delta. Cancer-causing chemicals such as benzene primarily affect the health of those living in close proximity to refineries. Populations living in inner cities often suffer most from concentrated air pollution -- soot and ozone -- due to the proximity with truck and bus routes.
  • 13. Dissolved Air Flotation • The first step in a DAF system is coagulation/ flocculation. Dispersed particles (oil/solids) are stabilized by negative electric charges on their surfaces, causing them to repel each other. • they do not settle, since this prevents these charged particles from colliding to form larger masses, called flocs. • Chemical coagulation and flocculation are required to assist in the removal of colloidal particles from suspension. • These processes, usually done in sequence, are a combination of physical and chemical procedures.
  • 14. Dissolved Air Flotation—a Typical DAF Unit
  • 15. Activated Sludge • An activated sludge process is the most effective of all the biological systems available • It is used in many refineries around the world and offers a reliable method of biological treatment. • Activated sludge is a continuous suspension of aerobic biological growths in a wastewater containing entrapped suspended colloidal, dissolved organic and inorganic materials.
  • 16. The PACT® (Powdered Activated Carbon Treatment) system
  • 17. Nitrification With DenitrificationThe biological treatment system could include either a nitrification(by the use of nitrifying bacteria) or a combined nitrification/denitrification step in some cases when a refinery site is required to meet tight ammonia or nitrogen limits. The level of nitrogen compounds in refinery wastewater can be controlled by avoiding discharges of spent amines and proper removal of ammonia in the sour water stripper. Nitrification is the term used to describe the two-step biological process in which ammonia (NH4-N) is oxidized to nitrite (NO2-N) and the nitrite is oxidized to nitrate (NO3-N).
  • 19. Nitrification With Denitrification • In denitrification, the nitrate is reduced to nitric oxide, nitrous oxide and nitrogen gas.
  • 20.  Oil has many benefits and energy is necessary for all our activities. But each stage in its life cycle carries hazards for humans, wildlife and the environmental systems on which we and other species depend.  Understanding the health and environmental consequences of oil use may help decision makers assess the true costs of our dependence on this non-renewable resource hence one major reason why there is the ultimate need to treat our water and wastewater discharges emanating from all oil refineries to meet set international standards.
  • 21. Reference Gary, James H., Glenn E. Handwerk, and Mark J. Kaiser. Petroleum refining: technology and economics. CRC press, 2007. • Leffler, William L. "Petroleum refining for the nontechnical person." (1985). • The Environment (Protection) Rule, 1986 are referred to as principal rules in all subsequent Notifications beginning with S.O. 32(E), dated 16.2.1987 published in the Gazette No. 66, dated 16.2.1987 . • EPA Notification [G.S.R 186(E), dt. 18th March, 2008]