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Environmental Challenges
 Facing Sugar Sector in
       Pakistan


             By

     Talha Usman
       M.Sc(Env,Science)
Waste produce during sugar
               Production:
Mill  House              Sugar cane
(waste & by product)
Wastewater from bearing house of the mill
contain SS and oil contents also include
washing water used for floor cleaning,which
contain sugar content like Bagasse
Process House              Sugar Juice
(waste & by product)
Filter cake generates aggressive effluents
like BOD5,COD,TDS and Molasses
Boiler   House         Bagasses,Furnace
oil
 (Waste & by product)

 Fly ash, smoke, flue gasses

Cooling   pond          water and
chemical
 (waste & by product)
Environmental Solution

     It can be classified into three main
     categories.

1.   In-House improvement options
     (Waste reduction at source )

2. Air & Noise Emission control measures
3. Waste water treatment technologies for
   NEQS compliance
In-House improvement options
                             ( Waste reduction at source)

Flow   measurement through flow meter and monitoring at
inlet and out let of each consumer unit at the mill for better
water management practices.
Use of optimum imbibitions rate to save energy in terms of
steam consumption and to reduce organic and hydraulic
load from the process house
Dry cleaning of mill floors with bagasse
Efficient operation of evaporators will reduce waste
disposal problems and enhance sugar recovery.overloading
of evaporators and vacuum pans, boiling at excessive rates,
operating them at incorrect liquid levels,and variation of
vacuum lead to a loss of sugar through condenser water.
Recycling of cooling and condenser water
The   simple measure of controlling spillover of molasses
can very significantly reduce the organic pollution
content(BOD5) of the wastewater stream.
Segregation of oil from other effluent will allow for the
recovery and reuse of lubricating oil and reduce soil
contamination when wastewater is applied for irrigation.
Controlling the mixing of filter mud with wastewater can
very significantly reduce the organic and inorganic pollution
content of wastewater stream.
Routine inspection of units, particularly pumps, pipes and
other vessels.
Reducing water used for floor sweeping and washing by
recovering water from various mill processes and reusing it
for cleaning purposes.
Detaining filter cloth washing in a holding tank for a short
time before being allowed to mix with other effluents from
the mill will reduce the contamination in the condenser
Installation  of circular mist eliminators or demisters
constructed of stainless steel in the multiple effect
evaporators can eliminate sugar entry in condenser water.
Bagasse management is of paramount importance in
establishing overall energy efficiency in the mill .steam and
power generation and reduction in fuel oil consumption are
largely dependent on an adequate supply and efficient
utilization of bagasse .Benefits will also result from ensuring
that maximum moisture has been removed before
bagasses is used in the boiler.
As far as air emissions are concerned the first step should
be to set up a system of regular monitoring of stack
emissions with periodic boiler tune ups.this can
considerably increase boiler efficiency and minimization
emissions.
Reduction of the use of Lead sub Acetate(Toxic chemical)
Air and Noise Pollution Control
Air Emission Control Methods:

1.   Regular monitoring of stack emissions
2.   Settling chamber
     (These chamber will remove large particulate matters)
3.   Wet collectors
     (Mostly available in simply spray tower is an
     effective method for removing particulate
     matters.)
4.   Gas Scrubber
5.   Electrostatic precipitator
Air and Noise Pollution Control
Noise Pollution Control Methods:


1.   Sound reduction at source
         (using silencers)
2.   Interrupting the path of the sound
        (using sound barrier)
3.   Protecting the recipient
       (using Ear muffs,plug)
Strategy for wastewater Management
Steps for wastewater minimization:
Arrangement   to divert the washing of Lime house and grit

 washing to condenser water channel to reclaim both the

 water and residual Lime which helps to make up the
 condenser water pH.
Collection and recirculation of leakage from pumps glands
Collection of centrifugal house floor washing and pumping

  it back to raw juice.
Using sugar contaminated condensate for maceration at

  mill house.
Recirculation of all cooling waters.
Reclamation of hot water and vapors from boiler blow
Drainage   within the plant should not be allowed as this
 leads to indiscriminate use of water.
Arrangement for collection of all cooling waters should be

 made designed for cascade cooling of water which follow
 the recirculation.
Boiler feed water requirement will be met by condensation

 from vapors cells, if need be supplemented by the
 condensate from pans, the collection system should be
 tow ways.
Vapour condensate from vapour line juice heaters is

 collected and used in maceration.
The overflow of spray pond and boiler blow downs can be

 used for spraying over bagasse and fly ash in dumping
 yard to prevent the hazard of fire.
Prepare the Do,s and Don,t for the plant personals.
All ground water tube wells have meters. Daily recording
 and monitoring shall help in reduction of ground water
 extraction through effluents generation.
Set up a pit for collecting juice contaminated water to

 reduce sugar content in washing and cleaning water.
Monitor and follow up the quality and quantity of pollution

 sources to prevent additional polluting effluent.
Precipitation and filtration of flue gas washing water will

 regenerate it into a colorless and transparent state. This
 regenerated clean water can be reused in the flue gas
 washing system.
Training and developing the concept of water conservation

  to managers, operators and labors.
Organizing the internal seminar giving opportunity to

 express the views to suite the environmental and company
Wastewater Treatment Technologies
Solution   Technical Characteristics Operational
                                            Characteristics
Lagoon     Anaerobic    lagoons are        BOD5   loading kg/m3? Least
s          deep earthen basins used         efficient
           for high strength organic         BOD5 removal efficiency ?
           wastewater with high solid       85-90%
           concentration.                   Energy requirement for
           Facultative lagoons are         aeration kwh/kg BOD treated ?
           earthen basins filled with       Moderately efficient
           screened or primary              Hydraulic detention time ?
           effluent in which                Very high
           stabilization of east is
                                             mechanical complexity ? low
           brought about by a
           combination of aerobic,          Reactor resilience for power
           anaerobic and facultative        failure and shock loads ?
           bacteria.                        Moderate to high
           Aerobic  lagoons are large,     By-product ? Nil
           shallow earthen basin used for
                                            Land requirement ? large
           treatment of wastewater by
           natural processes.
Solution   Technical Characteristics Operational Characteristics
Lagoons    Maturation    ponds are low   On   –site environmental impact
           rate stabilization ponds       –soil infiltration and aerosols
           usually designed to provide    dispersion
           for secondary effluent         Man power requirement ?
           polishing and seasonal         Skilled
           nitrification.                 Frequency of repair &
                                          maintenance ? medium

Tricking   Wastewater    flows from      BOD5   loading kg/m3 ? Least
Filters    top to bottom, dispersed       efficient
           over filter material           BOD5 removal efficiency ? 85
           (stones,plastic during         90%
           which soluble compounds        Hydraulic detention time ?
           are removed and, to a          Most efficient
           lesser extent, solids are
                                          Land requirement ? Small
           taken up into the biofilm
           adhered to the carrier         Man power requirement ?
           material.                      Skilled
                                          Mechanical complexity ? Low
                                          By product ? nil
Solution   Technical Characteristics Operational Characteristics
Upflow     The   basic idea of this       BOD5   loading kg/m3/d ? Very
Anaerobi   system is that the flocs of     efficient
c Sludge   anaerobic bacteria will tend    BOD5 removal efficiency ? 80
Blanket    to settle under gravity,        90 %
(UASB      when applying a moderate        Energy requirement for aeration
Reactor    up flow velocity of water. In   kwh/kg BOD treated ? Most
           this way no separate            efficient
           sedimentation tank is
                                           Hydraulic detention time ? Mos
           necessary.
                                           efficient
           The waste water passes
                                           Mechanical complexity ? low
           the reactor from the bottom
           to top. To guarantee            By product ? Biogas
           sufficient contact between      On site environmental impact ?
           the incoming wastewater         Nil
           and the bacteria in the         Land requirement ? Small
           sludge layer the
                                           Man power requirement ?
           wastewater is fed evenly
           over the bottom of the          Highly skilled
           reactor .Further mixing is      Frequency of repair &
           brought about by the            maintenance ? low
           production of the gas
Solution    Technical Characteristics Operational Characteristics
Activated   Many    variations of              BOD5   loading kg/m3/d ? Very
Sludge      activated sludge treatment          efficient
Treatmen    exist, depending on load            BOD5 removal efficiency ? 85
t           characteristics. Activated          95%
            sludge treatment is most            Energy requirement for aeration
            appropriate for high                kwh/kg BOD treated ? Least
            organic pollution loads.            efficient
            Most successfully applied if
                                                Hydraulic detention time ?
            hourly flow is low.
                                                Moderately efficient
            System consist only of
                                                 mechanical complexity ? High
            aeration tank (operated as
            fill and draw system ) and          Reactor resilience for power
            mechanical surface                  failure ? Low and for shock loads
            aerators. Aeration and              ? Moderate
            sedimentation takes place           By product ? Nil
            in the same reactor on the          On site environmental
            following cyclical principle:       impacts ? Aerosol dispersion and
            feeding and aeration of the
            reactor during a certain period,    noise
            switch off the aeration, followed   Land requirement ? Moderate
            by settling of the sludge and
                                                Man power requirement ?
            discharge of the effluent.
                                                Highly skilled
End-of-pipe Treatment in sugar mills

Combination of Lagoons in Sequence
(Anaerobic,Facultative and Maturation)

Preliminary design and costing of this option?for a mill generating
6,000 - 7,000mg/l BOD5 ? Suggests that to achieve of 90%
removal efficiency the lagoons system would require a total
surface area of 120 hectares, a total volume of 1.5 million cubic
meters,and a total retention time 216 days.The exorbitant level of
retention time, land requirement and high cost of lining make this
inadvisable for local sugar mills. However, unlined lagoons,
though pose serious threat to ground water quality, can also be
taken into consideration after careful analysis of environmental
condition around the mill.
End-of-pipe Treatment in sugar mills
Combined Treatment System Comprising of a
UASB Reactor and an Activated Sludge System
When used alone, the activated sludge system has a high
operational cost because of the energy required for aeration.
Combining it with a UASB Reactor significantly reduces this cost.
The UASB Reactor can remove about 80 - 90 % BOD5;in
addition, a by-product of the process is methane which can then
be used as a source of energy for the boiler. After passing
through the UASB Reactor, the effluent can passed through the
Activated Sludge System for treatment of remaining BOD5. The
combined system will achieve the same pollutant removal
efficiency as the Activated Sludge System but at lower cost. This
combined system will bring the present BOD5 and suspended
solids level near or below the NEQS.Such a system will require
around 1,500 - 3,000 square meters of land and its annual
operation and maintenance expenditure would be approximately
10% of its total cost .with in–house improvement USAB reactor
as single treatment can be applied.
Health Risks
Bagasses dust, fly ash and high noise levels (reaching up to
109dB)are particularly health irritant.Excessive exposure to
fly ash and bagasse dust may cause irritation to
eyes,asthma,and other respiratory diseases including
bagassosis(a lung disease caused by inhalation of bagasse
dust)Dust prone areas ,including cane preparation and the
boiler house, should be carefully monitored. Nuisance dust
levels should be controlled properly.Dermatitis or skin
disease is a major health complaint resulting from chemical
burns,and contact with lime and sugar.Toxic gasses
including sulfur dioxide,caustic fumes are released at
various stages of the process and are health hazards.Flue
gas which is produce by the combustion of bagasse cause
a visual nuisance and have serious health concern.These
problems are particularly high in boilers due to not equipped
with scrubbing or cyclone systems.
ISO 14001
A set of environmental management
requirements for environmental
management systems.The purpose of this
standard is to help all kinds of organizations
to protect the environment, to prevent
pollution, and to improve their overall
environmental performance.
Components of ISO 14001

Environmental   policy
Planning
Implementation
Monitoring   and evaluation
Review
Requirements for ISO 14001
         Certification
Existence   of EMS
Effective operation of EMS for at least

 three month
Internal audit conducting capacity should

 exist in the company
Environmental training has been imparted

 to its employees
Documents are maintained
Management review has been conducted
ISO 9001 & ISO 14001 will help
             you:
Promote  & Enhance your business &
 marketing efforts
Increase income revenues
Keep your customers happy & satisfied.
By having ISO 9001 & 14001
     Certification,you gain:
Reduced      liabilities & added protection
Extended management & operation tools,

  including those to reduce “non quality” costs.
Improved control, to manage internal and
external
  activities.
Improved quality for products and services.
Improved supply schedules for products and

 services.
A better feeling caused by better managed

 environmental care.
Environmental Management
           Systems:

It is set of policy measures, management
actions, operating procedures,
documentation and record keeping,defined
responsibilities and accountabilities of
personals within an organization to address
its environmental issues.
Concept of EMS

Management             review
 Env, consequences of operation
Environmental           policy
 Set objective for Env,performance
Action     planning
 To achieve objective
Implementation
 To monitor performance against these objectives
Corrective       action
 For continue improvement
Environmental Management
        Systems Benefits
The benefits of an EMS and registration of the
EMS to ISO 14000 are organized into these
categories:

Increased  profits
Operations
Marketing
Regulatory Compliance
Social Status

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Environmental Challenges Facing Pakistan's Sugar Sector

  • 1. Environmental Challenges Facing Sugar Sector in Pakistan By Talha Usman M.Sc(Env,Science)
  • 2. Waste produce during sugar Production: Mill House Sugar cane (waste & by product) Wastewater from bearing house of the mill contain SS and oil contents also include washing water used for floor cleaning,which contain sugar content like Bagasse Process House Sugar Juice (waste & by product) Filter cake generates aggressive effluents like BOD5,COD,TDS and Molasses
  • 3. Boiler House Bagasses,Furnace oil (Waste & by product) Fly ash, smoke, flue gasses Cooling pond water and chemical (waste & by product)
  • 4. Environmental Solution It can be classified into three main categories. 1. In-House improvement options (Waste reduction at source ) 2. Air & Noise Emission control measures 3. Waste water treatment technologies for NEQS compliance
  • 5. In-House improvement options ( Waste reduction at source) Flow measurement through flow meter and monitoring at inlet and out let of each consumer unit at the mill for better water management practices. Use of optimum imbibitions rate to save energy in terms of steam consumption and to reduce organic and hydraulic load from the process house Dry cleaning of mill floors with bagasse Efficient operation of evaporators will reduce waste disposal problems and enhance sugar recovery.overloading of evaporators and vacuum pans, boiling at excessive rates, operating them at incorrect liquid levels,and variation of vacuum lead to a loss of sugar through condenser water. Recycling of cooling and condenser water
  • 6. The simple measure of controlling spillover of molasses can very significantly reduce the organic pollution content(BOD5) of the wastewater stream. Segregation of oil from other effluent will allow for the recovery and reuse of lubricating oil and reduce soil contamination when wastewater is applied for irrigation. Controlling the mixing of filter mud with wastewater can very significantly reduce the organic and inorganic pollution content of wastewater stream. Routine inspection of units, particularly pumps, pipes and other vessels. Reducing water used for floor sweeping and washing by recovering water from various mill processes and reusing it for cleaning purposes. Detaining filter cloth washing in a holding tank for a short time before being allowed to mix with other effluents from the mill will reduce the contamination in the condenser
  • 7. Installation of circular mist eliminators or demisters constructed of stainless steel in the multiple effect evaporators can eliminate sugar entry in condenser water. Bagasse management is of paramount importance in establishing overall energy efficiency in the mill .steam and power generation and reduction in fuel oil consumption are largely dependent on an adequate supply and efficient utilization of bagasse .Benefits will also result from ensuring that maximum moisture has been removed before bagasses is used in the boiler. As far as air emissions are concerned the first step should be to set up a system of regular monitoring of stack emissions with periodic boiler tune ups.this can considerably increase boiler efficiency and minimization emissions. Reduction of the use of Lead sub Acetate(Toxic chemical)
  • 8. Air and Noise Pollution Control Air Emission Control Methods: 1. Regular monitoring of stack emissions 2. Settling chamber (These chamber will remove large particulate matters) 3. Wet collectors (Mostly available in simply spray tower is an effective method for removing particulate matters.) 4. Gas Scrubber 5. Electrostatic precipitator
  • 9. Air and Noise Pollution Control Noise Pollution Control Methods: 1. Sound reduction at source (using silencers) 2. Interrupting the path of the sound (using sound barrier) 3. Protecting the recipient (using Ear muffs,plug)
  • 10. Strategy for wastewater Management Steps for wastewater minimization: Arrangement to divert the washing of Lime house and grit washing to condenser water channel to reclaim both the water and residual Lime which helps to make up the condenser water pH. Collection and recirculation of leakage from pumps glands Collection of centrifugal house floor washing and pumping it back to raw juice. Using sugar contaminated condensate for maceration at mill house. Recirculation of all cooling waters. Reclamation of hot water and vapors from boiler blow
  • 11. Drainage within the plant should not be allowed as this leads to indiscriminate use of water. Arrangement for collection of all cooling waters should be made designed for cascade cooling of water which follow the recirculation. Boiler feed water requirement will be met by condensation from vapors cells, if need be supplemented by the condensate from pans, the collection system should be tow ways. Vapour condensate from vapour line juice heaters is collected and used in maceration. The overflow of spray pond and boiler blow downs can be used for spraying over bagasse and fly ash in dumping yard to prevent the hazard of fire. Prepare the Do,s and Don,t for the plant personals.
  • 12. All ground water tube wells have meters. Daily recording and monitoring shall help in reduction of ground water extraction through effluents generation. Set up a pit for collecting juice contaminated water to reduce sugar content in washing and cleaning water. Monitor and follow up the quality and quantity of pollution sources to prevent additional polluting effluent. Precipitation and filtration of flue gas washing water will regenerate it into a colorless and transparent state. This regenerated clean water can be reused in the flue gas washing system. Training and developing the concept of water conservation to managers, operators and labors. Organizing the internal seminar giving opportunity to express the views to suite the environmental and company
  • 13. Wastewater Treatment Technologies Solution Technical Characteristics Operational Characteristics Lagoon Anaerobic lagoons are BOD5 loading kg/m3? Least s deep earthen basins used efficient for high strength organic  BOD5 removal efficiency ? wastewater with high solid 85-90% concentration. Energy requirement for Facultative lagoons are aeration kwh/kg BOD treated ? earthen basins filled with Moderately efficient screened or primary Hydraulic detention time ? effluent in which Very high stabilization of east is  mechanical complexity ? low brought about by a combination of aerobic, Reactor resilience for power anaerobic and facultative failure and shock loads ? bacteria. Moderate to high Aerobic lagoons are large, By-product ? Nil shallow earthen basin used for Land requirement ? large treatment of wastewater by natural processes.
  • 14. Solution Technical Characteristics Operational Characteristics Lagoons Maturation ponds are low On –site environmental impact rate stabilization ponds –soil infiltration and aerosols usually designed to provide dispersion for secondary effluent Man power requirement ? polishing and seasonal Skilled nitrification. Frequency of repair & maintenance ? medium Tricking Wastewater flows from BOD5 loading kg/m3 ? Least Filters top to bottom, dispersed efficient over filter material BOD5 removal efficiency ? 85 (stones,plastic during 90% which soluble compounds Hydraulic detention time ? are removed and, to a Most efficient lesser extent, solids are Land requirement ? Small taken up into the biofilm adhered to the carrier Man power requirement ? material. Skilled Mechanical complexity ? Low By product ? nil
  • 15. Solution Technical Characteristics Operational Characteristics Upflow The basic idea of this BOD5 loading kg/m3/d ? Very Anaerobi system is that the flocs of efficient c Sludge anaerobic bacteria will tend BOD5 removal efficiency ? 80 Blanket to settle under gravity, 90 % (UASB when applying a moderate Energy requirement for aeration Reactor up flow velocity of water. In kwh/kg BOD treated ? Most this way no separate efficient sedimentation tank is Hydraulic detention time ? Mos necessary. efficient The waste water passes Mechanical complexity ? low the reactor from the bottom to top. To guarantee By product ? Biogas sufficient contact between On site environmental impact ? the incoming wastewater Nil and the bacteria in the Land requirement ? Small sludge layer the Man power requirement ? wastewater is fed evenly over the bottom of the Highly skilled reactor .Further mixing is Frequency of repair & brought about by the maintenance ? low production of the gas
  • 16. Solution Technical Characteristics Operational Characteristics Activated Many variations of BOD5 loading kg/m3/d ? Very Sludge activated sludge treatment efficient Treatmen exist, depending on load BOD5 removal efficiency ? 85 t characteristics. Activated 95% sludge treatment is most Energy requirement for aeration appropriate for high kwh/kg BOD treated ? Least organic pollution loads. efficient Most successfully applied if Hydraulic detention time ? hourly flow is low. Moderately efficient System consist only of  mechanical complexity ? High aeration tank (operated as fill and draw system ) and Reactor resilience for power mechanical surface failure ? Low and for shock loads aerators. Aeration and ? Moderate sedimentation takes place By product ? Nil in the same reactor on the On site environmental following cyclical principle: impacts ? Aerosol dispersion and feeding and aeration of the reactor during a certain period, noise switch off the aeration, followed Land requirement ? Moderate by settling of the sludge and Man power requirement ? discharge of the effluent. Highly skilled
  • 17. End-of-pipe Treatment in sugar mills Combination of Lagoons in Sequence (Anaerobic,Facultative and Maturation) Preliminary design and costing of this option?for a mill generating 6,000 - 7,000mg/l BOD5 ? Suggests that to achieve of 90% removal efficiency the lagoons system would require a total surface area of 120 hectares, a total volume of 1.5 million cubic meters,and a total retention time 216 days.The exorbitant level of retention time, land requirement and high cost of lining make this inadvisable for local sugar mills. However, unlined lagoons, though pose serious threat to ground water quality, can also be taken into consideration after careful analysis of environmental condition around the mill.
  • 18. End-of-pipe Treatment in sugar mills Combined Treatment System Comprising of a UASB Reactor and an Activated Sludge System When used alone, the activated sludge system has a high operational cost because of the energy required for aeration. Combining it with a UASB Reactor significantly reduces this cost. The UASB Reactor can remove about 80 - 90 % BOD5;in addition, a by-product of the process is methane which can then be used as a source of energy for the boiler. After passing through the UASB Reactor, the effluent can passed through the Activated Sludge System for treatment of remaining BOD5. The combined system will achieve the same pollutant removal efficiency as the Activated Sludge System but at lower cost. This combined system will bring the present BOD5 and suspended solids level near or below the NEQS.Such a system will require around 1,500 - 3,000 square meters of land and its annual operation and maintenance expenditure would be approximately 10% of its total cost .with in–house improvement USAB reactor as single treatment can be applied.
  • 19. Health Risks Bagasses dust, fly ash and high noise levels (reaching up to 109dB)are particularly health irritant.Excessive exposure to fly ash and bagasse dust may cause irritation to eyes,asthma,and other respiratory diseases including bagassosis(a lung disease caused by inhalation of bagasse dust)Dust prone areas ,including cane preparation and the boiler house, should be carefully monitored. Nuisance dust levels should be controlled properly.Dermatitis or skin disease is a major health complaint resulting from chemical burns,and contact with lime and sugar.Toxic gasses including sulfur dioxide,caustic fumes are released at various stages of the process and are health hazards.Flue gas which is produce by the combustion of bagasse cause a visual nuisance and have serious health concern.These problems are particularly high in boilers due to not equipped with scrubbing or cyclone systems.
  • 20. ISO 14001 A set of environmental management requirements for environmental management systems.The purpose of this standard is to help all kinds of organizations to protect the environment, to prevent pollution, and to improve their overall environmental performance.
  • 21. Components of ISO 14001 Environmental policy Planning Implementation Monitoring and evaluation Review
  • 22. Requirements for ISO 14001 Certification Existence of EMS Effective operation of EMS for at least three month Internal audit conducting capacity should exist in the company Environmental training has been imparted to its employees Documents are maintained Management review has been conducted
  • 23. ISO 9001 & ISO 14001 will help you: Promote & Enhance your business & marketing efforts Increase income revenues Keep your customers happy & satisfied.
  • 24. By having ISO 9001 & 14001 Certification,you gain: Reduced liabilities & added protection Extended management & operation tools, including those to reduce “non quality” costs. Improved control, to manage internal and external activities. Improved quality for products and services. Improved supply schedules for products and services. A better feeling caused by better managed environmental care.
  • 25. Environmental Management Systems: It is set of policy measures, management actions, operating procedures, documentation and record keeping,defined responsibilities and accountabilities of personals within an organization to address its environmental issues.
  • 26. Concept of EMS Management review Env, consequences of operation Environmental policy Set objective for Env,performance Action planning To achieve objective Implementation To monitor performance against these objectives Corrective action For continue improvement
  • 27. Environmental Management Systems Benefits The benefits of an EMS and registration of the EMS to ISO 14000 are organized into these categories: Increased profits Operations Marketing Regulatory Compliance Social Status