New Flare Requirements in MACT CC Jeff Greif
- Slides: 56
New Flare Requirements in MACT CC Jeff Greif Air Permits Division Texas Commission on Environmental Quality Environmental Trade Fair 2017
Objectives 1. Requirements 2. Significant Changes 3. TCEQ Perspective & Permitting
The Past
Modern History • 40 CFR § 60. 18 • 40 CFR § 63. 11(b) • RG-109 DRAFT
Permit Boiler Plate
The Focus 1. Always Have a Flame 2. No Smoke 3. Keep It Lit A. Sufficient Heating Value B. Limited Velocity 4. Monitor
The Future
January 30, 2019
Changes § 60. 18 § 63. 670
Changes? § 63. 11(b) 1. Always Have a Flame 2. No Smoke 3. Keep It Lit A. Sufficient Heating Value B. Limited Velocity 4. Monitor § 63. 670 1. Operate With a Pilot Flame 2. No Smoke or Tell Me All About It! 3. Keep It Lit A. Count the Added Steam and Air Effect on Heating Value B. Limited Velocity 4. MONITOR & Report!
Pilot Flame
Pilot Flame “…when regulated material is routed to the flare. ” VS. “…at all times vent gas may be directed to the flare(s). ”
Visible Emissions. . …No Steam assist off Steam assist on
No Visible Emissions Old Hat • Method 22 • 5 minutes in 2 hours What’s New • Specify the Smokeless Design Capacity • Monitor
Smokeless Design Capacity Air Assisted Flare Measured at 99. 4% Efficiency
Visible Emissions & TCEQ Permits No Smoking Over 5 min in 2 hr Monitor per § 63. 670(h)
VE Monitoring Method 22 Daily Video Surveillance
Velocity and Heat Content “…regulated material is routed to the flare for at least 15 -minutes”
Flare Tip Velocity • 60 ft/s • Vmax to 400 ft/s
Flare Tip Velocity Log 10 (Vmax) = NHVvg + 1, 212 850
I. D. M Flare Tip Area I. D. M Pilot Stability Tabs Modules
Flare Tip Area Calculation Atip-unob = NM * (∏ * (I. D. M)2/4 – XT * AST Where: Atip-unob = Unobstructed Cross Sectional Area of Flare Tip I. D. M = Inside Diameter of One Tip Module NM = Number of Modules XT = Number of Stability Tabs per Module AST = Area of a Stability Tab
Flare Tip
NHVvg Net heating value of flare vent gas, Btu/scf Remember § 63. 641 Definitions
The New Standards Combustion Zone Operating Limits CO 2 H 2 O NOX CO fuel Dilution Operating Limits
What Does This Mean?
NHVcz versus NHVdil NHVcz NHVdil All Flares Receiving Perimeter Assist Air for
NHVvg Composition Monitoring Continuous Compositional Analysis (15 -min) or Method 18 Canister (8 -hr) -------------Continuous Calorimeter w/ H 2 Option --------------Demonstrated Consistent Composition
NHVvg from Continuous Monitors Options: Feed-Forward or Direct Calculation Data applied in the following 15 -min block vs. Data applied in the block it is available
15 -Minute Block Time 8: 00 to 8: 15, 8: 15 to 8: 30, etc.
GC Heating Value Example 12: 00 12: 15 12: 30 12: 45 1: 00 12: 05 12: 10 12: 23 12: 25 12: 38 12: 40 12: 53 • • Event Starts Measurement A Taken Result A (560) Available Measurement B Taken Result B (340) Available Measurement C Taken Result C (300) Available
GC Heating Value Example Feed Forward 12: 00 12: 15 12: 30 12: 45 1: 00 12: 05 12: 10 12: 23 12: 25 12: 38 12: 40 12: 53 560 Btu/scf 340 Btu/scf 300 Btu/scf Result A (560) Available Result B (340) Available Result C (300) Available
GC Heating Value Example Direct Calculation 12: 00 12: 15 12: 30 12: 45 1: 00 12: 05 12: 10 12: 23 12: 25 12: 38 12: 40 12: 53 560 Btu/scf 340 Btu/scf 300 Btu/scf Result A (560) Available Result B (340) Available Result C (300) Available
Hmmm… Time NHVvg Feed Forward Direct 12: 10 560 560 12: 25 340 560 12: 40 300 560 340
Flare Supplemental Gas Purchased Natural Gas 925 Btu/scf Heat Value Accounting from Flow
Flow Monitoring • Flare Vent Gas • Steam Assist – All • Air Assist – Premix – Perimeter • Supplemental Natural Gas
Flow Monitoring Methods are Flexible Standard Conditions are Not 68°F 1 Atm 385. 3 SCF/lb-mol
Flow Monitoring Options • Measure Volumetric Flow or Mass Flow • Use Fan Speed or Power With Fan Curves • Use Molecular Weight, Pressure, and Temperature With Engineering Calculations
Objective The Number of Standard Cubic Feet Q Q
Steam Assist Style Flare Tip • Perimeter Steam • Uses S/A Tubes • High Smokeless
Upper Steam Ring Injection Nozzles Steam Assist Style Flare Tip Lower Steam Ring Outlet for Steam/Air Mixture Flare Gas Unobstructed Exit Area is Gap Between the Tubes Over the Shell Upper Steam Ring Lower Steam Ring Center Steam Inlet Flange Injecting Steam Only Directly Into Flare Barrel Lower Steam Injector Into Internal Tube With Air Inspiration Flare Gas Inlet Range Upper Steam Ring Inlet
Assist Air Premix Assist Air ---------Perimeter Assist Air
Air Assist Style Flare Tip
Steam and Air Issue Flare Tip With Lower Steam Flare tip with lower induction steam tubes addition. Legend Ambient Air Steam Flare Gas
Combustion Zone Gas NHVcz 270 Btu/scf NHVcz = Qvg x NHVvg (Qvg + Qs + Qa, premix)
Net Heating Value Dilution Parameter NHVdil = 22 Btu/ft 2 Qvg x Diam x NHVvg (Qvg + Qs + Qa, premix + Q a, perimeter)
Flare Monitoring Systems Continuous Parameter Monitoring System (CPMS) • • • Operational Requirements Monitoring Plan Out of Control Periods Data Reduction Gas Chromatographs
CPMS Operation • • Table 13 Readily Accessible 15 Minute Cycles Minimum Continuous When Regulated Materials Flow
Table 13 Parameters • Temperature • Flow Rate for All Flows Other Than Flare Vent Gas • Flare Vent Gas Flow Rate • Pressure • Net Heating Value by Calorimeter • Net Heating Value by Gas Chromatograph • Hydrogen Analyzer
Table 13 Minimum Accuracy Requirements Temp ± 1% or 2. 8°C, which ever is greater
Table 13 Calibration Requirements • Cal check annually • Cal check if measurement exceeds range for 24 hrs or install new • Inspect components and electrical connections quarterly, unless redundant • Record results • Locate so representative and shielded
Emergency Flaring Provisions § 63. 670(o) 1) Plan 2) Submit the Plan 3) Smoking … Root Cause 4) Corrective Action
Emergency Flaring Provisions • • Force Majeure Good Maintenance No Mistakes 1 Event / 3 Years EPA
Emergency Flaring Provisions • • Operator Error Poor Maintenance 2 Same Cause 3 in 3
Flare Systems
And that is all I have Good to say about that! Reference Material: Parameters for Properly Designed and Operated Flares Contacts: Jeff Greif – jeff. greif@tceq. texas. gov Rick Goertz – richard. goertz@tceq. texas. gov
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