Table Of Content

Appendices Appendix A Test Plan TCEQ 2010 Flare Study Flare Test Plan Test Series No. S1: Varying Steam Assist, 2,342 lb/hr Waste Gas Flow, LHV = 2,149 Btu/scf Test Waste Waste Gas Steam/Waste Gas Actual Exit Notes Point Gas Composition Ratio Velocity No. Flow (*) per 40 CFR 60.18 (fps) S1.5 1 1 Incipient Smoke 1.00 Point S1.5 1 1 Increase steam from 1.00 **As to value in Test Pt. Needed S1.6 S1.5 to value for Test Pt. S1.6 S1.6 1 1 < Snuff 1.00 Test Series No. S2: Varying Steam Assist, 937 lb/hr Waste Gas Flow, LHV = 2,149 Btu/scf Test Waste Waste Gas Steam/Waste Gas Actual Exit Notes Point Gas Composition Ratio Velocity No. Flow (*) per 40 CFR 60.18 (fps) S2.1 2 1 Incipient Smoke 0.40 Point S2.1 2 1 Increase steam from 0.40 **As to value in Test Pt. Needed S2.2 S2.1 to value for Test Pt. S2.2 S2.2 2 1 < Snuff 0.40 (*) Exclusive of center steam Waste Gas Flow Legend 1 – 0.25% (nominally) of flare design capacity or 2,342 lb/hr for 36 inch steam-assisted flare burner 2 – 0.1% (nominally) of flare design capacity or 937 lb/hr for 36 inch steam-assisted flare burner Waste Gas Composition & Lower Heating Value (LHV) Legend 1 – 100% Propylene, LHV = 2,149 Btu/scf 2 – 20/80 ratio Tulsa natural gas to propylene diluted with nitrogen to a LHV = 350 Btu/scf 3 – 20/80 ratio Tulsa natural gas to propylene diluted with nitrogen to LHV = 600 Btu/scf TCEQ 2010 Flare Study The University of Texas at Austin A - 2 August 1, 2011 The Center for Energy & Environmental Resources Test Series No. S3: Varying Steam Assist, 937 lb/hr Waste Gas Flow, LHV = 350 Btu/scf Test Waste Waste Gas Steam/Waste Gas Actual Exit Notes Point Gas Composition Ratio Velocity No. Flow (*) per 40 CFR 60.18 (fps) S3.0 2 2 0 0.57 S3.1 2 2 Incipient Smoke 0.57 **1st cycle Point only, less for 2nd & 3rd S3.1 2 2 Increase steam from 0.57 to Incipient Smoke S3.2 Point Value to <Snuff S3.2 2 2 < Snuff 0.57 S3.2 2 2 Change steam from 0.57 to value in Test Pt. S3.3 S3.2 to value in Test Pt. S3.3 S3.3 2 2 2/3 between ISP and 0.57 snuff ratios S3.3 2 2 Change steam from 0.57 to value in Test Pt. S3.4 S3.3 to value in Test Pt. S3.4 S3.4 2 2 1/3 between ISP and 0.57 snuff ratios (*) Exclusive of center steam Waste Gas Flow Legend 1 – 0.25% (nominally) of flare design capacity or 2,342 lb/hr for 36 inch steam-assisted flare burner 2 – 0.1% (nominally) of flare design capacity or 937 lb/hr for 36 inch steam-assisted flare burner Waste Gas Composition & Lower Heating Value (LHV) Legend 1 – 100% Propylene, LHV = 2,149 Btu/scf 2 – 20/80 ratio Tulsa natural gas to propylene diluted with nitrogen to a LHV = 350 Btu/scf 3 – 20/80 ratio Tulsa natural gas to propylene diluted with nitrogen to LHV = 600 Btu/scf TCEQ 2010 Flare Study The University of Texas at Austin A - 3 August 1, 2011 The Center for Energy & Environmental Resources Test Series No. S4: Varying Steam Assist, 2,342 lb/hr Waste Gas Flow, LHV = 350 Btu/scf Test Waste Waste Gas Steam/Waste Gas Actual Exit Notes Point Gas Composition Ratio Velocity No. Flow (*) per 40 CFR 60.18 (fps) S4.0 1 2 0 1.42 S4.1 1 2 Incipient Smoke 1.42 **1st cycle Point only, less for 2nd & 3rd S4.1 1 2 Increase steam from 1.42 to Incipient Smoke S4.2 Point Value to <Snuff S4.2 1 2 < Snuff 1.42 S4.2 1 2 Change steam from 1.42 to value in Test Pt. S4.3 S4.2 to value in Test Pt. S4.3 S4.3 1 2 2/3 between ISP and 1.42 snuff ratios S4.3 1 2 Change steam from 1.42 to value in Test Pt. S4.4 S4.3 to value in Test Pt. S4.4 S4.4 1 2 1/3 between ISP and 1.42 snuff ratios (*) Exclusive of center steam Waste Gas Flow Legend 1 – 0.25% (nominally) of flare design capacity or 2,342 lb/hr for 36 inch steam-assisted flare burner 2 – 0.1% (nominally) of flare design capacity or 937 lb/hr for 36 inch steam-assisted flare burner Waste Gas Composition & Lower Heating Value (LHV) Legend 1 – 100% Propylene, LHV = 2,149 Btu/scf 2 – 20/80 ratio Tulsa natural gas to propylene diluted with nitrogen to a LHV = 350 Btu/scf 3 – 20/80 ratio Tulsa natural gas to propylene diluted with nitrogen to LHV = 600 Btu/scf TCEQ 2010 Flare Study The University of Texas at Austin A - 4 August 1, 2011 The Center for Energy & Environmental Resources Test Series No. S5: Varying Steam Assist, 937 lb/hr Waste Gas Flow, LHV = 600 Btu/scf Test Waste Waste Gas Steam/Waste Gas Actual Exit Notes Point Gas Composition Ratio Velocity No. Flow (*) per 40 CFR 60.18 (fps) S5.0 2 3 0 0.55 S5.1 2 3 Incipient Smoke 0.55 **1st cycle Point only, less for 2nd & 3rd S5.1 2 3 Increase steam from 0.55 to Incipient Smoke S5.2 Point to < Snuff S5.2 2 3 < Snuff 0.55 S5.2 2 3 Change steam from 0.55 to value in Test Pt. S5.3 S5.2 to value in Test Pt. S5.3 S5.3 2 3 1/3 between ISP and 0.55 snuff ratios S5.3 2 3 Change steam from 0.55 to value in Test Pt. S5.4 S5.3 to value in Test Pt. S5.4 S5.4 2 3 2/3 between ISP and 0.55 snuff ratios (*) Exclusive of center steam Waste Gas Flow Legend 1 – 0.25% (nominally) of flare design capacity or 2,342 lb/hr for 36 inch steam-assisted flare burner 2 – 0.1% (nominally) of flare design capacity or 937 lb/hr for 36 inch steam-assisted flare burner Waste Gas Composition & Lower Heating Value (LHV) Legend 1 – 100% Propylene, LHV = 2,149 Btu/scf 2 – 20/80 ratio Tulsa natural gas to propylene diluted with nitrogen to a LHV = 350 Btu/scf 3 – 20/80 ratio Tulsa natural gas to propylene diluted with nitrogen to LHV = 600 Btu/scf TCEQ 2010 Flare Study The University of Texas at Austin A - 5 August 1, 2011 The Center for Energy & Environmental Resources Test Series No. S6: Varying Steam Assist, 2,342 lb/hr Waste Gas Flow, LHV = 600 Btu/scf Test Waste Waste Gas Steam/Waste Gas Actual Exit Notes Point Gas Composition Ratio Velocity No. Flow (*) per 40 CFR 60.18 (fps) S6.0 1 3 0 1.36 S6.1 1 3 Incipient Smoke 1.36 **1st cycle Point only, less for 2nd & 3rd S6.1 1 3 Increase steam from 1.36 to Incipient Smoke S6.2 Point to < Snuff S6.2 1 3 < Snuff 1.36 S6.2 1 3 Change steam from 1.36 to value in Test Pt. S6.3 S6.2 to value in Test Pt. S6.3 S6.3 1 3 1/3 between ISP and 1.36 snuff ratios S6.3 1 3 Change steam from 1.36 to value in Test Pt. S6.4 S6.3 to value in Test Pt. S6.4 S6.4 1 3 2/3 between ISP and 1.36 snuff ratios (*) Exclusive of center steam Waste Gas Flow Legend 1 – 0.25% (nominally) of flare design capacity or 2,342 lb/hr for 36 inch steam-assisted flare burner 2 – 0.1% (nominally) of flare design capacity or 937 lb/hr for 36 inch steam-assisted flare burner Waste Gas Composition & Lower Heating Value (LHV) Legend 1 – 100% Propylene, LHV = 2,149 Btu/scf 2 – 20/80 ratio Tulsa natural gas to propylene diluted with nitrogen to a LHV = 350 Btu/scf 3 – 20/80 ratio Tulsa natural gas to propylene diluted with nitrogen to LHV = 600 Btu/scf TCEQ 2010 Flare Study The University of Texas at Austin A - 6 August 1, 2011 The Center for Energy & Environmental Resources Extra Test Series: Constant Steam Assist, Varying Waste Gas Flow Rate Test Series No. S7: Constant Steam Assist, Waste Gas Flow Varies from 2342 to 937 lbs/hr, LHV = 350 Btu/scf Test Waste Waste Gas Steam Assist Actual Exit Notes Point Gas Composition Velocity No. Flow (*) per 40 lbs/hr CFR 60.18 (fps) S7.1 2342 2 525 lbs/hr upper, - 500 lbs/hr center S7.2 1850 2 525 lbs/hr upper, - 500 lbs/hr center S7.3 1400 2 525 lbs/hr upper, - 500 lbs/hr center S7.4 937 2 525 lbs/hr upper, - 500 lbs/hr center Test Series S7 would be repeated up 2 more times. (*) Exclusive of center steam Waste Gas Flow Legend 1 – 0.25% (nominally) of flare design capacity or 2,342 lb/hr for 36 inch steam-assisted flare burner 2 – 0.1% (nominally) of flare design capacity or 937 lb/hr for 36 inch steam-assisted flare burner Waste Gas Composition & Lower Heating Value (LHV) Legend 1 – 100% Propylene, LHV = 2,149 Btu/scf 2 – 20/80 ratio Tulsa natural gas to propylene diluted with nitrogen to a LHV = 350 Btu/scf 3 – 20/80 ratio Tulsa natural gas to propylene diluted with nitrogen to LHV = 600 Btu/scf 4 – 20/80 ratio Tulsa natural gas to propane diluted with nitrogen to LHV = 600 Btu/scf TCEQ 2010 Flare Study The University of Texas at Austin A - 7 August 1, 2011 The Center for Energy & Environmental Resources Extra Test Series: Constant Steam Assist, Varying Waste Gas Flow Rate Test Series No. S8: Constant Steam Assist, Waste Gas Flow Varies from 2342 to 937 lbs/hr, LHV = 350 Btu/scf Test Waste Waste Gas Steam Assist Actual Exit Notes Point Gas Composition Velocity No. Flow (*) per 40 lbs/hr CFR 60.18 (fps) S8.1 2342 2 525 lbs/hr upper, - 0 lbs/hr center S8.2 1850 2 525 lbs/hr upper, - 0 lbs/hr center S8.3 1400 2 525 lbs/hr upper, - 0 lbs/hr center S8.4 937 2 525 lbs/hr upper, - 0 lbs/hr center (*) Exclusive of center steam Waste Gas Flow Legend 1 – 0.25% (nominally) of flare design capacity or 2,342 lb/hr for 36 inch steam-assisted flare burner 2 – 0.1% (nominally) of flare design capacity or 937 lb/hr for 36 inch steam-assisted flare burner Waste Gas Composition & Lower Heating Value (LHV) Legend 1 – 100% Propylene, LHV = 2,149 Btu/scf 2 – 20/80 ratio Tulsa natural gas to propylene diluted with nitrogen to a LHV = 350 Btu/scf 3 – 20/80 ratio Tulsa natural gas to propylene diluted with nitrogen to LHV = 600 Btu/scf 4 – 20/80 ratio Tulsa natural gas to propane diluted with nitrogen to LHV = 600 Btu/scf TCEQ 2010 Flare Study The University of Texas at Austin A - 8 August 1, 2011 The Center for Energy & Environmental Resources Extra Test Series: Constant Steam Assist, Varying Waste Gas Flow Rate Test Series No. S9: Constant Steam Assist, Waste Gas Flow Varies from 2342 to 937 lbs/hr, LHV = 350 Btu/scf Test Waste Waste Gas Steam Assist Actual Exit Notes Point Gas Composition Velocity No. Flow (*) per 40 lbs/hr CFR 60.18 (fps) S9.1 2342 2 1025 lbs/hr upper, - 0 lbs/hr center S9.2 1850 2 1025 lbs/hr upper, - 0 lbs/hr center S9.3 1400 2 1025 lbs/hr upper, - 0 lbs/hr center S9.4 937 2 1025 lbs/hr upper, - 0 lbs/hr center (*) Exclusive of center steam Waste Gas Flow Legend 1 – 0.25% (nominally) of flare design capacity or 2,342 lb/hr for 36 inch steam-assisted flare burner 2 – 0.1% (nominally) of flare design capacity or 937 lb/hr for 36 inch steam-assisted flare burner Waste Gas Composition & Lower Heating Value (LHV) Legend 1 – 100% Propylene, LHV = 2,149 Btu/scf 2 – 20/80 ratio Tulsa natural gas to propylene diluted with nitrogen to a LHV = 350 Btu/scf 3 – 20/80 ratio Tulsa natural gas to propylene diluted with nitrogen to LHV = 600 Btu/scf 4 – 20/80 ratio Tulsa natural gas to propane diluted with nitrogen to LHV = 600 Btu/scf TCEQ 2010 Flare Study The University of Texas at Austin A - 9 August 1, 2011 The Center for Energy & Environmental Resources

Description:
S1: Varying Steam Assist, 2,342 lb/hr Waste Gas Flow, LHV = 2,149 Btu/scf. Test 2 – 0.1% (nominally) of flare design capacity or 937 lb/hr for 36 inch . TCEQ 2010 Flare Study. The University of Texas at Austin. A - 7. August 1 .. composition of the vent gas being used during each test, a stack t
ebook img

Appendices PDF

541 Pages·2011·21.99 MB·English
by  Vincent Torres
Save to my drive
Quick download
Download
Upgrade Premium
Most books are stored in the elastic cloud where traffic is expensive. For this reason, we have a limit on daily download.

Preview Appendices

Appendices Appendix A Test Plan TCEQ 2010 Flare Study Flare Test Plan Test Series No. S1: Varying Steam Assist, 2,342 lb/hr Waste Gas Flow, LHV = 2,149 Btu/scf Test Waste Waste Gas Steam/Waste Gas Actual Exit Notes Point Gas Composition Ratio Velocity No. Flow (*) per 40 CFR 60.18 (fps) S1.5 1 1 Incipient Smoke 1.00 Point S1.5 1 1 Increase steam from 1.00 **As to value in Test Pt. Needed S1.6 S1.5 to value for Test Pt. S1.6 S1.6 1 1 < Snuff 1.00 Test Series No. S2: Varying Steam Assist, 937 lb/hr Waste Gas Flow, LHV = 2,149 Btu/scf Test Waste Waste Gas Steam/Waste Gas Actual Exit Notes Point Gas Composition Ratio Velocity No. Flow (*) per 40 CFR 60.18 (fps) S2.1 2 1 Incipient Smoke 0.40 Point S2.1 2 1 Increase steam from 0.40 **As to value in Test Pt. Needed S2.2 S2.1 to value for Test Pt. S2.2 S2.2 2 1 < Snuff 0.40 (*) Exclusive of center steam Waste Gas Flow Legend 1 – 0.25% (nominally) of flare design capacity or 2,342 lb/hr for 36 inch steam-assisted flare burner 2 – 0.1% (nominally) of flare design capacity or 937 lb/hr for 36 inch steam-assisted flare burner Waste Gas Composition & Lower Heating Value (LHV) Legend 1 – 100% Propylene, LHV = 2,149 Btu/scf 2 – 20/80 ratio Tulsa natural gas to propylene diluted with nitrogen to a LHV = 350 Btu/scf 3 – 20/80 ratio Tulsa natural gas to propylene diluted with nitrogen to LHV = 600 Btu/scf TCEQ 2010 Flare Study The University of Texas at Austin A - 2 August 1, 2011 The Center for Energy & Environmental Resources Test Series No. S3: Varying Steam Assist, 937 lb/hr Waste Gas Flow, LHV = 350 Btu/scf Test Waste Waste Gas Steam/Waste Gas Actual Exit Notes Point Gas Composition Ratio Velocity No. Flow (*) per 40 CFR 60.18 (fps) S3.0 2 2 0 0.57 S3.1 2 2 Incipient Smoke 0.57 **1st cycle Point only, less for 2nd & 3rd S3.1 2 2 Increase steam from 0.57 to Incipient Smoke S3.2 Point Value to <Snuff S3.2 2 2 < Snuff 0.57 S3.2 2 2 Change steam from 0.57 to value in Test Pt. S3.3 S3.2 to value in Test Pt. S3.3 S3.3 2 2 2/3 between ISP and 0.57 snuff ratios S3.3 2 2 Change steam from 0.57 to value in Test Pt. S3.4 S3.3 to value in Test Pt. S3.4 S3.4 2 2 1/3 between ISP and 0.57 snuff ratios (*) Exclusive of center steam Waste Gas Flow Legend 1 – 0.25% (nominally) of flare design capacity or 2,342 lb/hr for 36 inch steam-assisted flare burner 2 – 0.1% (nominally) of flare design capacity or 937 lb/hr for 36 inch steam-assisted flare burner Waste Gas Composition & Lower Heating Value (LHV) Legend 1 – 100% Propylene, LHV = 2,149 Btu/scf 2 – 20/80 ratio Tulsa natural gas to propylene diluted with nitrogen to a LHV = 350 Btu/scf 3 – 20/80 ratio Tulsa natural gas to propylene diluted with nitrogen to LHV = 600 Btu/scf TCEQ 2010 Flare Study The University of Texas at Austin A - 3 August 1, 2011 The Center for Energy & Environmental Resources Test Series No. S4: Varying Steam Assist, 2,342 lb/hr Waste Gas Flow, LHV = 350 Btu/scf Test Waste Waste Gas Steam/Waste Gas Actual Exit Notes Point Gas Composition Ratio Velocity No. Flow (*) per 40 CFR 60.18 (fps) S4.0 1 2 0 1.42 S4.1 1 2 Incipient Smoke 1.42 **1st cycle Point only, less for 2nd & 3rd S4.1 1 2 Increase steam from 1.42 to Incipient Smoke S4.2 Point Value to <Snuff S4.2 1 2 < Snuff 1.42 S4.2 1 2 Change steam from 1.42 to value in Test Pt. S4.3 S4.2 to value in Test Pt. S4.3 S4.3 1 2 2/3 between ISP and 1.42 snuff ratios S4.3 1 2 Change steam from 1.42 to value in Test Pt. S4.4 S4.3 to value in Test Pt. S4.4 S4.4 1 2 1/3 between ISP and 1.42 snuff ratios (*) Exclusive of center steam Waste Gas Flow Legend 1 – 0.25% (nominally) of flare design capacity or 2,342 lb/hr for 36 inch steam-assisted flare burner 2 – 0.1% (nominally) of flare design capacity or 937 lb/hr for 36 inch steam-assisted flare burner Waste Gas Composition & Lower Heating Value (LHV) Legend 1 – 100% Propylene, LHV = 2,149 Btu/scf 2 – 20/80 ratio Tulsa natural gas to propylene diluted with nitrogen to a LHV = 350 Btu/scf 3 – 20/80 ratio Tulsa natural gas to propylene diluted with nitrogen to LHV = 600 Btu/scf TCEQ 2010 Flare Study The University of Texas at Austin A - 4 August 1, 2011 The Center for Energy & Environmental Resources Test Series No. S5: Varying Steam Assist, 937 lb/hr Waste Gas Flow, LHV = 600 Btu/scf Test Waste Waste Gas Steam/Waste Gas Actual Exit Notes Point Gas Composition Ratio Velocity No. Flow (*) per 40 CFR 60.18 (fps) S5.0 2 3 0 0.55 S5.1 2 3 Incipient Smoke 0.55 **1st cycle Point only, less for 2nd & 3rd S5.1 2 3 Increase steam from 0.55 to Incipient Smoke S5.2 Point to < Snuff S5.2 2 3 < Snuff 0.55 S5.2 2 3 Change steam from 0.55 to value in Test Pt. S5.3 S5.2 to value in Test Pt. S5.3 S5.3 2 3 1/3 between ISP and 0.55 snuff ratios S5.3 2 3 Change steam from 0.55 to value in Test Pt. S5.4 S5.3 to value in Test Pt. S5.4 S5.4 2 3 2/3 between ISP and 0.55 snuff ratios (*) Exclusive of center steam Waste Gas Flow Legend 1 – 0.25% (nominally) of flare design capacity or 2,342 lb/hr for 36 inch steam-assisted flare burner 2 – 0.1% (nominally) of flare design capacity or 937 lb/hr for 36 inch steam-assisted flare burner Waste Gas Composition & Lower Heating Value (LHV) Legend 1 – 100% Propylene, LHV = 2,149 Btu/scf 2 – 20/80 ratio Tulsa natural gas to propylene diluted with nitrogen to a LHV = 350 Btu/scf 3 – 20/80 ratio Tulsa natural gas to propylene diluted with nitrogen to LHV = 600 Btu/scf TCEQ 2010 Flare Study The University of Texas at Austin A - 5 August 1, 2011 The Center for Energy & Environmental Resources Test Series No. S6: Varying Steam Assist, 2,342 lb/hr Waste Gas Flow, LHV = 600 Btu/scf Test Waste Waste Gas Steam/Waste Gas Actual Exit Notes Point Gas Composition Ratio Velocity No. Flow (*) per 40 CFR 60.18 (fps) S6.0 1 3 0 1.36 S6.1 1 3 Incipient Smoke 1.36 **1st cycle Point only, less for 2nd & 3rd S6.1 1 3 Increase steam from 1.36 to Incipient Smoke S6.2 Point to < Snuff S6.2 1 3 < Snuff 1.36 S6.2 1 3 Change steam from 1.36 to value in Test Pt. S6.3 S6.2 to value in Test Pt. S6.3 S6.3 1 3 1/3 between ISP and 1.36 snuff ratios S6.3 1 3 Change steam from 1.36 to value in Test Pt. S6.4 S6.3 to value in Test Pt. S6.4 S6.4 1 3 2/3 between ISP and 1.36 snuff ratios (*) Exclusive of center steam Waste Gas Flow Legend 1 – 0.25% (nominally) of flare design capacity or 2,342 lb/hr for 36 inch steam-assisted flare burner 2 – 0.1% (nominally) of flare design capacity or 937 lb/hr for 36 inch steam-assisted flare burner Waste Gas Composition & Lower Heating Value (LHV) Legend 1 – 100% Propylene, LHV = 2,149 Btu/scf 2 – 20/80 ratio Tulsa natural gas to propylene diluted with nitrogen to a LHV = 350 Btu/scf 3 – 20/80 ratio Tulsa natural gas to propylene diluted with nitrogen to LHV = 600 Btu/scf TCEQ 2010 Flare Study The University of Texas at Austin A - 6 August 1, 2011 The Center for Energy & Environmental Resources Extra Test Series: Constant Steam Assist, Varying Waste Gas Flow Rate Test Series No. S7: Constant Steam Assist, Waste Gas Flow Varies from 2342 to 937 lbs/hr, LHV = 350 Btu/scf Test Waste Waste Gas Steam Assist Actual Exit Notes Point Gas Composition Velocity No. Flow (*) per 40 lbs/hr CFR 60.18 (fps) S7.1 2342 2 525 lbs/hr upper, - 500 lbs/hr center S7.2 1850 2 525 lbs/hr upper, - 500 lbs/hr center S7.3 1400 2 525 lbs/hr upper, - 500 lbs/hr center S7.4 937 2 525 lbs/hr upper, - 500 lbs/hr center Test Series S7 would be repeated up 2 more times. (*) Exclusive of center steam Waste Gas Flow Legend 1 – 0.25% (nominally) of flare design capacity or 2,342 lb/hr for 36 inch steam-assisted flare burner 2 – 0.1% (nominally) of flare design capacity or 937 lb/hr for 36 inch steam-assisted flare burner Waste Gas Composition & Lower Heating Value (LHV) Legend 1 – 100% Propylene, LHV = 2,149 Btu/scf 2 – 20/80 ratio Tulsa natural gas to propylene diluted with nitrogen to a LHV = 350 Btu/scf 3 – 20/80 ratio Tulsa natural gas to propylene diluted with nitrogen to LHV = 600 Btu/scf 4 – 20/80 ratio Tulsa natural gas to propane diluted with nitrogen to LHV = 600 Btu/scf TCEQ 2010 Flare Study The University of Texas at Austin A - 7 August 1, 2011 The Center for Energy & Environmental Resources Extra Test Series: Constant Steam Assist, Varying Waste Gas Flow Rate Test Series No. S8: Constant Steam Assist, Waste Gas Flow Varies from 2342 to 937 lbs/hr, LHV = 350 Btu/scf Test Waste Waste Gas Steam Assist Actual Exit Notes Point Gas Composition Velocity No. Flow (*) per 40 lbs/hr CFR 60.18 (fps) S8.1 2342 2 525 lbs/hr upper, - 0 lbs/hr center S8.2 1850 2 525 lbs/hr upper, - 0 lbs/hr center S8.3 1400 2 525 lbs/hr upper, - 0 lbs/hr center S8.4 937 2 525 lbs/hr upper, - 0 lbs/hr center (*) Exclusive of center steam Waste Gas Flow Legend 1 – 0.25% (nominally) of flare design capacity or 2,342 lb/hr for 36 inch steam-assisted flare burner 2 – 0.1% (nominally) of flare design capacity or 937 lb/hr for 36 inch steam-assisted flare burner Waste Gas Composition & Lower Heating Value (LHV) Legend 1 – 100% Propylene, LHV = 2,149 Btu/scf 2 – 20/80 ratio Tulsa natural gas to propylene diluted with nitrogen to a LHV = 350 Btu/scf 3 – 20/80 ratio Tulsa natural gas to propylene diluted with nitrogen to LHV = 600 Btu/scf 4 – 20/80 ratio Tulsa natural gas to propane diluted with nitrogen to LHV = 600 Btu/scf TCEQ 2010 Flare Study The University of Texas at Austin A - 8 August 1, 2011 The Center for Energy & Environmental Resources Extra Test Series: Constant Steam Assist, Varying Waste Gas Flow Rate Test Series No. S9: Constant Steam Assist, Waste Gas Flow Varies from 2342 to 937 lbs/hr, LHV = 350 Btu/scf Test Waste Waste Gas Steam Assist Actual Exit Notes Point Gas Composition Velocity No. Flow (*) per 40 lbs/hr CFR 60.18 (fps) S9.1 2342 2 1025 lbs/hr upper, - 0 lbs/hr center S9.2 1850 2 1025 lbs/hr upper, - 0 lbs/hr center S9.3 1400 2 1025 lbs/hr upper, - 0 lbs/hr center S9.4 937 2 1025 lbs/hr upper, - 0 lbs/hr center (*) Exclusive of center steam Waste Gas Flow Legend 1 – 0.25% (nominally) of flare design capacity or 2,342 lb/hr for 36 inch steam-assisted flare burner 2 – 0.1% (nominally) of flare design capacity or 937 lb/hr for 36 inch steam-assisted flare burner Waste Gas Composition & Lower Heating Value (LHV) Legend 1 – 100% Propylene, LHV = 2,149 Btu/scf 2 – 20/80 ratio Tulsa natural gas to propylene diluted with nitrogen to a LHV = 350 Btu/scf 3 – 20/80 ratio Tulsa natural gas to propylene diluted with nitrogen to LHV = 600 Btu/scf 4 – 20/80 ratio Tulsa natural gas to propane diluted with nitrogen to LHV = 600 Btu/scf TCEQ 2010 Flare Study The University of Texas at Austin A - 9 August 1, 2011 The Center for Energy & Environmental Resources

Description:
S1: Varying Steam Assist, 2,342 lb/hr Waste Gas Flow, LHV = 2,149 Btu/scf. Test 2 – 0.1% (nominally) of flare design capacity or 937 lb/hr for 36 inch . TCEQ 2010 Flare Study. The University of Texas at Austin. A - 7. August 1 .. composition of the vent gas being used during each test, a stack t
See more

The list of books you might like

Upgrade Premium
Most books are stored in the elastic cloud where traffic is expensive. For this reason, we have a limit on daily download.
DMCA & Copyright: Dear all, most of the website is community built, users are uploading hundred of books everyday, which makes really hard for us to identify copyrighted material, please contact us if you want any material removed.
Copyright @ PDFdrive.to, 2022 | We love our users