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A peek into the future
Barrett O’Donovan
Barrett O'Donovan brings over 14 years in business development, account
and project management. With a Bachelors of Arts in Political Science, he
led teams across the U.S. and Canada for Fortune 1000 and large private
companies.
As a new business development manager, he has expanded company
footprints to new territories and has uncovered and successfully penetrated
new vertical markets.
Barrett will focus on increasingCatalytic Products presence in the following
vertical markets:
Natural Gas Processing
Foundry & Sand Coating
Automotive & Spray Coating
Waste to Energy
RichardTruzpek
Mr.Trzupek has twenty-eight (28) years of experience in the field of air
pollution measurement, consulting, and permitting. He has designed and
managed a variety of air pollution measurement projects at facilities
across the United States. He has lectured on behalf of the USEPA
Emission Measurement Technical Information Center (EMTIC) on
measurement-related issues and has also developed several new
measurement techniques. Mr.Trzupek has served as lead consultant
representing a variety of industries in litigation-based programs and
frequently serves as the facilitator for effective action between the
facility and regulators.
His permitting experience has involved not only the preparation of the
permit document, but includes the collection of data, management, and
organization of data, development of compliance strategies, negotiation
with regulatory and enforcement personnel and effective
implementation of emissions management programs designed to
maintain facility compliance with permit terms.
.
ReleasedApril 2014
Prepared by: Office of Air Quality Planning and Standards
(OAQPS)
Target:
 Methane Emissions
 Volatile Organic Compound (VOC) Emissions
“Pre regulatory development” step in the process
Well Completions
Compressors
Equipment Leaks
Liquids Unloading
Pneumatics
Well Completions
Compressors
Equipment Leaks
Liquids Unloading
Pneumatics
Natural gas well regulations already in place (Subpart OOOO)
National emissions estimates from fracked oil well
completions:
 Methane: 44,000 tpy to 247,000 tpy
 VOC: 37,000 tpy to 116,000 tpy
Methane = Greenhouse gas issue
VOC = Ozone standard issue
EPA suggests “green completions” may be feasible in some
cases
 Recognition that certain pressure/gas content combinations may
present obstacle
Other possibilities:
 Gas reinjection
 NGL recovery
 Use gas to generate on-site power
Validity of emissions estimates
Feasibility of green completions
Other means of methane/VOC control at wellhead?
Current/future availability of infrastructure at oil plays
Well Completions
Compressors
Equipment Leaks
Liquids Unloading
Pneumatics
86,000 tonnes – natural gas productions
724,000 tonnes – natural gas processing
1,260,000 tonnes – natural gas transmission and storage
TOTAL > 2,000,000 tonnes (~50,000,000 tonnes as CO2e)
Reciprocating compressors
 Rod seal maintenance
 Capture and return to process
Centrifugal compressors
 Encourage (require?) dry seals
 Encourage (require?) capture and recovery if wet seals used
Validity of emissions estimates
Technical/financial feasibility of controls suggested
Other options?
Well Completions
Compressors
Equipment Leaks
Liquids Unloading
Pneumatics
Methane:
 332,000 tonnes – natural gas production
 34,000 tonnes – natural gas processing
 114,000 tonnes – natural gas transmission
VOC?
Estimation methodology very sketchy
Move leak detection from portable analyzers to Optical Gas
Imaging (OGI)
 Eg: IR and FLIR cameras
More ambient monitoring
Claim that effective leak detection pays for itself
Validity of emissions estimates
Site/equipment sensitivity to leaks
Other leak detection technologies available?
Cost estimates reasonable?
Well Completions
Compressors
Equipment Leaks
Liquids Unloading
Pneumatics
Older, lower pressure wells targeted
 Small number of wells = majority of GHG andVOC emissions
 Some (not all) blowdowns produce large amounts of emissions
EPA says industry developing new technologies to reduce
blowdowns
 E.g.: plunger lifts
Validity of emissions estimates
Further information of types of wells that produce more
emissions
Additional technologies to reduce emissions?
Feasibility of combustion controls?
Well Completions
Compressors
Equipment Leaks
Liquids Unloading
Pneumatics
Look at controllers and pumps
Encourage (require?) more low bleed controllers
Encourage (require?) more electric generation in field to
provide instrument air
Validity of emissions estimates
Feasibility of emissions reductions techniques
Barriers to installing electric generation/instrument air in field
" A Peek into the Future" of the Oil and Natural Gas Industry
What Is It?
Why Use It?
Where Use It?
" A Peek into the Future" of the Oil and Natural Gas Industry
•Overview of Oxidation Process
•Types of Oxidizers
• Feature & Benefit Analysis
byType
•Time - Typically .5-1.5 seconds
•Temperature – Typically 1300-1600 F
•Turbulence - Mixing to achieve temperature uniformity
How is oxidation achieved?
Thermal
Combustor
Thermal
Recuperative
Regenerative
Thermal
" A Peek into the Future" of the Oil and Natural Gas Industry
" A Peek into the Future" of the Oil and Natural Gas Industry
Historically: Flares commonly used forVOC and methane control
 Cheap
 No test requirement
Now EPA pushing for process safety use only
 Flares not as efficient as thought
 Flare minimization programs on the rise
Inlet DispersionCone
FloatingTube Primary Heat
Exchanger
Stainless SteelTubes
HighVelocity
CombustionTube
Pressurization Chamber / Seal
BurnerCone
CombustionTube Internal Insulation
Hot Gas Bypass Damper
Exhaust Outlet
 Over 99%VOC Removal Efficiency
 Shell &Tube heat exchanger = 70% thermal efficiency
 No moving parts
 Accepts higherVOC concentrations
 Able to handle upset conditions
" A Peek into the Future" of the Oil and Natural Gas Industry
" A Peek into the Future" of the Oil and Natural Gas Industry
CombustionChamber
Cold Face Support
Burner
Valves
Exhaust StackTransition
Internal Insulation
Air Manifold
Ceramic Media
 Up to 99% Destruction Efficiency
 95%Thermal Efficiency
 Near zero fuel use in self sustain mode
 Prepackaged drop in place designs available
" A Peek into the Future" of the Oil and Natural Gas Industry
THERMAL
COMBUSTOR
Low capital cost
Waste gas as fuel
Potential high
operating cost
Simple – no
moving parts
REGENERATIVE
THERMAL
Highest thermal
efficiency- 95%
Lowest
operating cost
Highest capital
cost
Complex has
moving parts
Highest
destruction
efficiency
Heat Recovery
Potential high
Operating Cost
No moving parts
THERMAL
RECUPERATIVE
Barrett O’Donovan
Catalytic Products International
980 Ensell Rd
Lake Zurich, IL 60047
847-438-0334
bodonovan@cpilink.com
www.cpilink.com
RichTrzupek
Trinity Consultants
1S660 Midwest Rd., Ste 250
OakbrookTerrace, IL 61081
630-495-1470
rtrzupek@trinityconsultants.com
www.trinityconsultants.com

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" A Peek into the Future" of the Oil and Natural Gas Industry

  • 1. A peek into the future
  • 2. Barrett O’Donovan Barrett O'Donovan brings over 14 years in business development, account and project management. With a Bachelors of Arts in Political Science, he led teams across the U.S. and Canada for Fortune 1000 and large private companies. As a new business development manager, he has expanded company footprints to new territories and has uncovered and successfully penetrated new vertical markets. Barrett will focus on increasingCatalytic Products presence in the following vertical markets: Natural Gas Processing Foundry & Sand Coating Automotive & Spray Coating Waste to Energy
  • 3. RichardTruzpek Mr.Trzupek has twenty-eight (28) years of experience in the field of air pollution measurement, consulting, and permitting. He has designed and managed a variety of air pollution measurement projects at facilities across the United States. He has lectured on behalf of the USEPA Emission Measurement Technical Information Center (EMTIC) on measurement-related issues and has also developed several new measurement techniques. Mr.Trzupek has served as lead consultant representing a variety of industries in litigation-based programs and frequently serves as the facilitator for effective action between the facility and regulators. His permitting experience has involved not only the preparation of the permit document, but includes the collection of data, management, and organization of data, development of compliance strategies, negotiation with regulatory and enforcement personnel and effective implementation of emissions management programs designed to maintain facility compliance with permit terms. .
  • 4. ReleasedApril 2014 Prepared by: Office of Air Quality Planning and Standards (OAQPS) Target:  Methane Emissions  Volatile Organic Compound (VOC) Emissions “Pre regulatory development” step in the process
  • 7. Natural gas well regulations already in place (Subpart OOOO) National emissions estimates from fracked oil well completions:  Methane: 44,000 tpy to 247,000 tpy  VOC: 37,000 tpy to 116,000 tpy Methane = Greenhouse gas issue VOC = Ozone standard issue
  • 8. EPA suggests “green completions” may be feasible in some cases  Recognition that certain pressure/gas content combinations may present obstacle Other possibilities:  Gas reinjection  NGL recovery  Use gas to generate on-site power
  • 9. Validity of emissions estimates Feasibility of green completions Other means of methane/VOC control at wellhead? Current/future availability of infrastructure at oil plays
  • 11. 86,000 tonnes – natural gas productions 724,000 tonnes – natural gas processing 1,260,000 tonnes – natural gas transmission and storage TOTAL > 2,000,000 tonnes (~50,000,000 tonnes as CO2e)
  • 12. Reciprocating compressors  Rod seal maintenance  Capture and return to process Centrifugal compressors  Encourage (require?) dry seals  Encourage (require?) capture and recovery if wet seals used
  • 13. Validity of emissions estimates Technical/financial feasibility of controls suggested Other options?
  • 15. Methane:  332,000 tonnes – natural gas production  34,000 tonnes – natural gas processing  114,000 tonnes – natural gas transmission VOC? Estimation methodology very sketchy
  • 16. Move leak detection from portable analyzers to Optical Gas Imaging (OGI)  Eg: IR and FLIR cameras More ambient monitoring Claim that effective leak detection pays for itself
  • 17. Validity of emissions estimates Site/equipment sensitivity to leaks Other leak detection technologies available? Cost estimates reasonable?
  • 19. Older, lower pressure wells targeted  Small number of wells = majority of GHG andVOC emissions  Some (not all) blowdowns produce large amounts of emissions EPA says industry developing new technologies to reduce blowdowns  E.g.: plunger lifts
  • 20. Validity of emissions estimates Further information of types of wells that produce more emissions Additional technologies to reduce emissions? Feasibility of combustion controls?
  • 22. Look at controllers and pumps Encourage (require?) more low bleed controllers Encourage (require?) more electric generation in field to provide instrument air
  • 23. Validity of emissions estimates Feasibility of emissions reductions techniques Barriers to installing electric generation/instrument air in field
  • 25. What Is It? Why Use It? Where Use It?
  • 27. •Overview of Oxidation Process •Types of Oxidizers • Feature & Benefit Analysis byType
  • 28. •Time - Typically .5-1.5 seconds •Temperature – Typically 1300-1600 F •Turbulence - Mixing to achieve temperature uniformity How is oxidation achieved?
  • 32. Historically: Flares commonly used forVOC and methane control  Cheap  No test requirement Now EPA pushing for process safety use only  Flares not as efficient as thought  Flare minimization programs on the rise
  • 33. Inlet DispersionCone FloatingTube Primary Heat Exchanger Stainless SteelTubes HighVelocity CombustionTube Pressurization Chamber / Seal BurnerCone CombustionTube Internal Insulation Hot Gas Bypass Damper Exhaust Outlet
  • 34.  Over 99%VOC Removal Efficiency  Shell &Tube heat exchanger = 70% thermal efficiency  No moving parts  Accepts higherVOC concentrations  Able to handle upset conditions
  • 37. CombustionChamber Cold Face Support Burner Valves Exhaust StackTransition Internal Insulation Air Manifold Ceramic Media
  • 38.  Up to 99% Destruction Efficiency  95%Thermal Efficiency  Near zero fuel use in self sustain mode  Prepackaged drop in place designs available
  • 40. THERMAL COMBUSTOR Low capital cost Waste gas as fuel Potential high operating cost Simple – no moving parts REGENERATIVE THERMAL Highest thermal efficiency- 95% Lowest operating cost Highest capital cost Complex has moving parts Highest destruction efficiency Heat Recovery Potential high Operating Cost No moving parts THERMAL RECUPERATIVE
  • 41. Barrett O’Donovan Catalytic Products International 980 Ensell Rd Lake Zurich, IL 60047 847-438-0334 bodonovan@cpilink.com www.cpilink.com RichTrzupek Trinity Consultants 1S660 Midwest Rd., Ste 250 OakbrookTerrace, IL 61081 630-495-1470 rtrzupek@trinityconsultants.com www.trinityconsultants.com

Notas do Editor

  1. FIVE DIFFERENT THERMAL OXIDIZERS ALL BASED ON OUR PROVEN QUADRANT SERIES SYSTEMS
  2. FIVE DIFFERENT THERMAL OXIDIZERS ALL BASED ON OUR PROVEN QUADRANT SERIES SYSTEMS
  3. FIVE DIFFERENT THERMAL OXIDIZERS ALL BASED ON OUR PROVEN QUADRANT SERIES SYSTEMS
  4. THERMAL COMBUSTORS ARE SPEICALLIZED THERMAL OXIDIZERS DEISGNED TO SAFELY AND ECONOMICALLY PROCESS LOW VOLUME – HIGH BTU OFF GAS THESE SYSTEMS ARE DESIGNED TO PROCESS VENT STREAMS IN EXCESS OF 50% LEL WITHOUT MONITORS OR ADDITIONAL DILUTION AIR
  5. THREE DIFFERENT STYLES OF RTO – EACH OFFERING DIFFERENT PERFORMANCE CHARACTERISTICS
  6. THREE DIFFERENT STYLES OF RTO – EACH OFFERING DIFFERENT PERFORMANCE CHARACTERISTICS