Quantification of Gas Mixtures Using Imaging ... - FlareNet

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Rodrigo B. Miguel 1 , Johannes Emmert 1,2 , Dilan Avşar 1 , Jean-Philippe Gagnon 3 , and Kyle J. Daun 1 1 Department of Mechanical and Mechatronics Engineering, University of Waterloo; 2 Department of Reactive Flows and Diagnostics, Technical University Darmstadt; 3 Telops Inc. Quantification of Gas Mixtures Using Imaging Fourier Transform Spectrometry Motivation The oil and gas industry needs to quantify gaseous emissions in various scenarios, e.g. reporting and mitigating fugitive emissions and assessing flare combustion efficiency. Optical gas imaging provides a two-dimensional representation of concentration in the camera field-of-view. It is passive and nonintrusive, qualifying it for fenceline measurements. Most optical gas imaging techniques focus on quantifying a single species. However, many gas releases consist of mixtures (e,g, BTEX, natural gas, combustion gases, etc. ). These can be quantified using an imaging Fourier transform spectrometer (IFTS). Measurement model The spectral intensity I lη incident in each pixel is related to the gas concentration and temperature along the line- of-sight (LOS) by the radiative transfer equation (RTE). The IFTS data can be used to simultaneously infer the temperature and species column densities. Species column densities are combined with the velocity field computed from a sequence of images to obtain mass flux. Optical flow velocimetry Spectroscopic model Gas State Intensity Residual I Lη = f(X CH4 ,σ, ΔT) ||b meas - b mod (X CH4 ,σ, ΔT)|| 2 X CH4 s ΔT s Column Density L 0 b M X(s)p ds A k T(s) ρ= 6×σ Flare combustion efficiency The IFTS can also infer flare combustion efficiency (CE), the ratio of the mass of carbon affixed to CO 2 to the total mass of carbon in the fuel stream. Flare CE may be impacted by cross-winds (fuel stripping) and steam-assist 4 . Synthetic MW Hyper-Cam data was generated from a CFD large-eddy simulation of a flare in a crosswind at a resolution of 4 cm -1 . Peak species concentrations are inferred through nonlinear regression of modeled data to simulated measurements. CH 4 mass flow Conclusions and future work Imaging Fourier transform spectrometers can estimate mass fluxes of gas mixtures. Methane flux estimates from the Hyper-Cam LW were consistent with ground-truth data. More accurate results can be found using the Hyper-Cam LW Methane (more methane lines) or the Hyper-Cam MW (improved temperature sensitivity). The Hyper-Cam MW can also estimate CO 2 and CH 4 column densities in a flare, which can be used to assess combustion efficiency. The Hyper-Cam MW will be used measure flare CE in the Boundary Layer Wind Tunnel at Western University, and later in a flare at an industrial site. 1 2 3 4 5 6 7 **LES Parameters: Stack ID 10.3 cm, 25.6 g/s of CH4, crosswind at 1.9 m/s [5] CO2 pixel CO2 CH4 N CE N N + Imaging Fourier-transform spectrometer (IFTS) The IFTS generates two-dimensional interferograms, which are transformed into a hypercube of spectally-resolved images. The LW Hyper-Cam is used to measure a 10 slpm CH 4 release at 10 K above ambient temperature with a cloudy sky as background. The data was used to obtain CH 4 column densities in each pixel, which is combined with the estimated velocity field to infer the methane mass flow. OPD /2 Beam splitter Fixed mirror Moving mirror Sensor Source CH 4 column density in g/m 2 x in mm z in mm 50 100 150 200 25 20 15 10 5 0 50 100 150 200 250 normal velocity in m/s x in mm z in mm 50 100 150 200 0.35 0.3 0.25 0.2 0.15 0 50 100 150 200 250 0.1 0.05 Pixel interferogram FT OPD Intensity Intensity Wavenumber Model Resolution [pixels] FOV Spectral Resolution [cm -1 ] Spectral Range [μm ] NESR [W/m 2 sr cm -1 ] Hyper-Cam LW 320×256 6.4 o ×5.1 o Up to 0.25 7.7-11.8 (850-1300 cm -1 ) 20 ×10 -5 Hyper-Cam MW 320×256 6.4 o ×5.1 o Up to 0.25 3-5 (2000-3330 cm -1 ) 4 to 7 ×10 -5 Re-absorbed Blackbody emission Transmittance (1−α η ) Background () { } () () { } L L 0 0 L L b 0 S I I exp - s ds (s) I s exp - s ds ds η η η η η η = κ + κ κ Absorption coefficient * X CH4 =0.2@298K, X CO2 =0.2, X H2O =0.4@400K 0 L I Lη I 0η 2000 2400 2800 3200 0 50 800 1000 1200 1400 0 3.5 κ η in cm -1 * η in cm -1 η in cm -1 CH 4 CO 2 H 2 O×100 H 2 O Outside (weather data) ΔT(fitted) Inside (IFTS sensor) s Temperature s Background H 2 O (fitted using BG pixels) CH 4 (fitted) 100 m L (fitted) Molar fraction The background intensity, I , was obtained from pixels that did not contain CH 4 . The background temperature and ambient humidity were fitted assuming ambient temperature from meteorological data. Species molar fraction and temperature were parametrized as Gaussian profiles along the LOS 2 , and the species absorption coefficient is simulated using the HITRAN spectral line database. Peak molar fraction, peak gas temperature, and plume thickness at four heights were inferred from measured spectra of 4 cm -1 resolution. 1 2 3 20 40 60 80 100 20 40 60 80 100 120 vertical pixels horizontal pixels 2 4 6 8 10 12 14 16 18 75 85 25 35 45 55 65 75 85 95 105 115 CO 2 g/m 2 pixels pixels 75 85 25 35 45 55 65 75 85 95 105 115 0.2 0.4 0.6 0.8 1 1.2 CH 4 g/m 2 pixels 0.3 0.4 0.5 0.6 0.7 0.8 0.9 75 85 25 35 45 55 65 75 85 95 105 115 CE PIXEL pixels Single point sample overestimates global CE The velocity field is estimated by the evolution of brightness patterns in the interferogram data-cube. Changes in pixel brightness between successive timeframes are caused by the CH 4 flow. Image data-cubes are used to derive the temporal and spatial derivatives by the brightness constancy assumption 3 . The underdetermined system of equations is solved by combining the gradient constraint with Laplacian priors on the flow velocities. u v 0 x y t ∂Ι ∂Ι ∂Ι + + = References [1] “Thermal Infrared Cameras.” Telops, https://www.telops.com/. [2] Grauer, S. J. et all., “Gaussian model for emission rate measurement of heated plumes using hyperspectral data,” JQRST, 2018. [3] Horn, B. K., & Schunck, B. G. “Determining optical flow,” Artificial Intelligence, 1981. [4] Johnson, M. R. et all., “A Fuel Stripping Mechanism for Wake-Stabilized Jet Diffusion Flames in Crossflow,” Combust. Sci. Technol., 2001. [5] Flare LES provided by Jeremy Thornock from the Department of Chemical Engineering at The University of Utah. [6] Quantifying & Reducing Impacts of Global Gas Flaring. (2019, October 9). Retrieved from https://www.flarenet.ca/. [1] [6] nozzle Video of the optical flow results Hyper-Cam LW Hyper-Cam MW

Transcript of Quantification of Gas Mixtures Using Imaging ... - FlareNet

Page 1: Quantification of Gas Mixtures Using Imaging ... - FlareNet

Rodrigo B. Miguel1, Johannes Emmert1,2, Dilan Avşar1, Jean-Philippe Gagnon3, and Kyle J. Daun11Department of Mechanical and Mechatronics Engineering, University of Waterloo; 2Department of Reactive Flows and Diagnostics, Technical University Darmstadt; 3Telops Inc.

Quantification of Gas Mixtures Using Imaging Fourier Transform Spectrometry

Motivation The oil and gas industry needs to quantify gaseous emissions in various scenarios, e.g. reporting and

mitigating fugitive emissions and assessing flare combustion efficiency. Optical gas imaging provides a two-dimensional representation of concentration in the camera field-of-view.

It is passive and nonintrusive, qualifying it for fenceline measurements. Most optical gas imaging techniques focus on quantifying a single species. However, many gas releases

consist of mixtures (e,g, BTEX, natural gas, combustion gases, etc. ). These can be quantified using an imaging Fourier transform spectrometer (IFTS).

Measurement model The spectral intensity Ilη incident in each pixel is related

to the gas concentration and temperature along the line-of-sight (LOS) by the radiative transfer equation (RTE).

The IFTS data can be used to simultaneously infer the temperature and species column densities.

Species column densities are combined with the velocity field computed from a sequence of images to obtain mass flux.

Optical flow velocimetrySpectroscopic model

Gas State

Intensity ResidualILη = f(XCH4,σ, ΔT) ||bmeas - bmod(XCH4,σ, ΔT)||2XCH4 s

ΔT s Column DensityL

0b

M X(s)p dsA k T(s)

ρ = ∫6×σ

Flare combustion efficiency The IFTS can also infer flare combustion efficiency (CE), the ratio of the mass of

carbon affixed to CO2 to the total mass of carbon in the fuel stream. Flare CE may be impacted by cross-winds (fuel stripping) and steam-assist4.

Synthetic MW Hyper-Cam data was generated from a CFD large-eddy simulation of a flare in a crosswind at a resolution of 4 cm-1.

Peak species concentrations are inferred through nonlinear regression of modeled data to simulated measurements.

CH4 mass flow Conclusions and future work Imaging Fourier transform spectrometers can estimate

mass fluxes of gas mixtures. Methane flux estimates from the Hyper-Cam LW were

consistent with ground-truth data. More accurate results can be found using the Hyper-Cam LW Methane (more methane lines) or the Hyper-Cam MW (improved temperature sensitivity).

The Hyper-Cam MW can also estimate CO2 and CH4column densities in a flare, which can be used to assess combustion efficiency.

The Hyper-Cam MW will be used measure flare CE in the Boundary Layer Wind Tunnel at Western University, and later in a flare at an industrial site.

1 2

3 4

56 7

**LES Parameters: Stack ID 10.3 cm, 25.6 g/s of CH4, crosswind at 1.9 m/s [5]

CO2pixel

CO2 CH4

NCE N N

≈+

Imaging Fourier-transform spectrometer (IFTS)

The IFTS generates two-dimensional interferograms, which are transformed into a hypercube of spectally-resolved images.

The LW Hyper-Cam is used to measure a 10 slpm CH4 release at 10 K above ambient temperature with a cloudy sky as background.

The data was used to obtain CH4 column densities in each pixel, which is combined with the estimated velocity field to infer the methane mass flow.

OPD /2

Beam splitter

Fixed mirror

Moving mirror

Sensor

Source

CH

4co

lum

n de

nsity

in g

/m2

x in mm

z in

mm

50

100

150

200

25

20

15

10

5

050 100 150 200 250

norm

al v

eloc

ity in

m/s

x in mm

z in

mm

50

100

150

200

0.35

0.3

0.25

0.2

0.15

050 100 150 200 250

0.1

0.05

Pixel interferogram FT

OPD

Inte

nsity

Inte

nsity

Wavenumber

Model Resolution[pixels] FOV Spectral Resolution

[cm-1]Spectral Range

[μm ]NESR

[W/m2 sr cm-1]Hyper-Cam LW 320×256 6.4o×5.1o Up to 0.25 7.7-11.8 (850-1300 cm-1) 20 ×10-5

Hyper-Cam MW 320×256 6.4o×5.1o Up to 0.25 3-5 (2000-3330 cm-1) 4 to 7 ×10-5

Re-absorbedBlackbodyemission

Transmittance (1−αη)Background

( ){ }( ) ( ){ }

L

L 0 0L L

b0 S

I I exp - s ds

(s) I s exp - s ds ds

η η η

η η η

= κ

′+ κ κ

∫∫ ∫

Absorption coefficient

* XCH4=0.2@298K, XCO2=0.2, XH2O=0.4@400K

0L

ILη

I0η

2000 2400 2800 32000

50

800 1000 1200 14000

3.5

κ ηin

cm

-1 *

η in cm-1 η in cm-1

CH4 CO2

H2O×100H2O

Outside (weather data)

ΔT(fitted)Inside (IFTS sensor)

sTem

pera

ture

s

Background H2O (fitted using BG

pixels)

CH4 (fitted)

100 m L (fitted)

Mol

ar fr

actio

n

The background intensity, I0η, was obtained from pixels that did not contain CH4.

The background temperature and ambient humidity were fitted assuming ambient temperature from meteorological data.

Species molar fraction and temperature were parametrized as Gaussian profiles along the LOS2, and the species absorption coefficient is simulated using the HITRAN spectral line database.

Peak molar fraction, peak gas temperature, and plume thickness at four heights were inferred from measured spectra of 4 cm-1 resolution.

1 2 3

20 40 60 80 100

20

40

60

80

100

120

verti

cal p

ixel

s

horizontal pixels

2

4

6

8

10

12

14

16

18

75 85

25

35

45

55

65

75

85

95

105

115

CO2 g/m2

pixe

ls

pixels75 85

25

35

45

55

65

75

85

95

105

115

0.2

0.4

0.6

0.8

1

1.2

CH4 g/m2

pixels

0.3

0.4

0.5

0.6

0.7

0.8

0.9

75 85

25

35

45

55

65

75

85

95

105

115

CEPIXEL

pixels

Single point sample overestimates global CE

The velocity field is estimated by the evolution of brightness patterns in the interferogram data-cube.

Changes in pixel brightness between successive timeframes are caused by the CH4 flow.

Image data-cubes are used to derive the temporal and spatial derivatives by the brightness constancy assumption3.

The underdetermined system of equations is solved by combining the gradient constraint with Laplacian priors on the flow velocities.

u v 0x y t∂Ι ∂Ι ∂Ι

+ + =∂ ∂ ∂

References[1] “Thermal Infrared Cameras.” Telops, https://www.telops.com/. [2] Grauer, S. J. et all., “Gaussian model for emission rate measurement of heated plumes using hyperspectral data,” JQRST, 2018. [3] Horn, B. K., & Schunck, B. G. “Determining optical flow,” Artificial Intelligence, 1981. [4] Johnson, M. R. et all., “A Fuel Stripping Mechanism for Wake-Stabilized Jet Diffusion Flames in Crossflow,” Combust. Sci. Technol., 2001.[5] Flare LES provided by Jeremy Thornock from the Department of Chemical Engineering at The University of Utah.[6] Quantifying & Reducing Impacts of Global Gas Flaring. (2019, October 9). Retrieved from https://www.flarenet.ca/.

[1]

[6]

nozzle

Video of the optical flow results

Hyper-Cam LW Hyper-Cam MW