Gas mixture estimation model based on response equivalent and orthogonal decomposition of transient response signals
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1 37 4 Vol. 37 No JOURNAL OF NATIONAL UNIVERSITY OF DEFENSE TECHNOLOGY Aug. 15 doi /j. cn http / /journal. nudt. edu. cn * Legendre 15% Legendre TP1. 6 A Gas mixture estimation model based on response equivalent and orthogonal decomposition of transient response signals QIN Guojun 1 ZHONG Ming 3 ZHANG Wenna 1 HU Niaoqing 1 1. Key Laboratory of Science and Technology on Integrated Logistics Support National University of Defense Technology Changsha 4173 China. College of Mechanical Engineering Hunan International Economy University Changsha 4117 China 3. The PLA Unit 696 Wulumuqi 831 China Abstract Based on linear mixture assumption or training the classifiers by large amount of data many methods used to recognize and estimate gas mixtures were adopted the non-orthogonal decomposition of steady response signal. Considering orthogonal decomposition approaches were mainly applied to analyze transient response signals a gas mixture estimation model based on response equivalent and orthogonal decomposition of transient response signals was put forward. A novel nonlinear gas-mixing model was built after the analysis of MOS Metal Oxide Semiconductor gas sensor response characteristics based on the component equivalent expression for different gas responses. A new orthogonal basis function the EQL Extended Quasi-Legendre basis was proposed and applied to the decomposition of a transient response signal from the gas sensor. After the exponential relationship between the coefficients and the gas concentration was verified via regression analysis the components in the gas mixture were separated and their concentrations were estimated simultaneously. Experimental result shows that even though only the prior knowledge of single gas responses was applied to build the model the concentration determined from the transient response of the gas mixture can reach an error within 15%. Key words response equivalent orthogonal decomposition extended quasi-legendre basis transient response signal gas mixture estimation * A qgj@ nudt. edu. cn
2 4 173 o m i = α 1 /β m i m j o α m j β m j = γ 1 /β m i m j c m i α j βm j m i 5 5 m O i O j 5 o m i 11 o j m i O j m o m i N O i i = 1 N m x m = f m o m o m i + + o m N 6 5 m 1-15 O i x m = f m i N 1/β α m m j λ 1 j =1 α m j b m j c j b m j [ ( m i ) i ] 7 1 x m = N γ m j c j β m j 1 /β m [ i β ] m i 8 f m x m 1 /β m i = N γ m j 1 /β m i c j β m j /β m i 9 m O i x m 19 x mi = G m - 1 = f G air mi c i = γ m i c i β m i 1 m 9 G m m O i N G air m m c j N f mi m O i γ m i c j Freundlich β m i M 1 3 K x k m m = 1 M O i m k = 1 K N o m i M K o m i = c i λ m i λ m i O i m x k m 1 /βk m i = N γ k m j 1 /βk m i c j βk m j /βk m i 1 λ m i N 1 M K > N x m i = f m i o m i = α m i λ m i β m i c i β m i = α m i o m i β m i 3 α m i = γ m i /λ β m i m m O j 3 x m j = α m j o m j β m j = γ m j c j β m j 4 x m i = x m j i [ ] ( ) γ m j β m j N O j Legendre Metal Oxide Semiconduct MOS 1
3 t a L n t Legendre Legendre L t = 1 Fourier Wavelet Basel 1 L 1 t = sin( t - α Legendre ) Legendre MOS L k -1 t = sin( kt - k α ) - k -1 C k -1 j-1 L j-1 t 1 < k N + 1 t a L k t = cos( kt - k α ) - k -1 C k j L j t j = 1 k N Legendre Legendre N+m-1 L N+m = t m - C N+m j L j t m = 1 M j = Γ N M = span 1 11 sint cost sint cost sinnt cosnt t t M Fig. 1 1 ~ 8 Legendre Extended quasi-legendre standard orthogonal basis fuctions of L i t i = 8 Gram-Schmidt C k-1 j-1 C k j ( ) α = sin kt - k α L α j-1 t dt ( ) α = cos kt - k α L α j t dt C N+m j = α t m L j t dt α L j t dt L j-1 t dt L j t dt 1 a ~ i α = 1 N = 8 M = ~ 8 Legendre ~ 8 L n t Fourier
4 Legendre 3 Γ N M K + 1 A = a a K T 3. 1 AIRSENSE K r K = - PEN3 3 x i - ^x K i x K i i i 1 MOS 槡 x i ^x i # 6 G 1ml 5ml 1ml ml 5ml 1ml Legendre 1 K 3 1ml 5ml 4h L 3ml l 3 l l l 1 # l - l 1 Fig. Original responses and their reconstruction of sensor in diesel gas l G /G 3 6s 1Hz Fig. 3 Curves of fitting error changes with different K 6s K = 4 3. Legendre x t t a Legendre K ^x K t = K a k L k t 1 k = K = 4 1 # Legendre 4 6 a k k = K Legendre
5 Legendre 3 Legendre 4. 1 a k m 4 1 i 1 Legendre 4 M K m m = 1 1 γ k m i β k m i a k m m = 1 M i = 1 c p i K + 1 N k = 1 K c i i = 1 N a k m i c p k = 1 K p = 1 P P c i i = 1 N a k m i c p 4 N γ k m i β k m i i = 1 N a 1 1 /β 1 i = γ 1 1 /β 1 i c1 β 1 1 /β 1 i + γ /β 1 i c β 1 /β 1 i + + γ 1 N 1 /β 1 i cn β 1 N /β 1 i a K 1 1 /βk 1 i = γ P 1 1 /βk 1 i c1 βk 1 1 /βk 1 i + γ P 1 1 /βk 1 i c βk 1 /βk 1 i + + γ P 1 N 1 /βk 1 i cn βk 1 N /βk 1 i 13 a M 1 /β M i = γ M 1 1 /β M i c1 β M 1 /β M i + γ M 1 /β M i c β M /β M i + + γ M N 1 /β M i cn β M N /β M i a K M 1 /βk M i = γ K M 1 1 /βk M i c1 βk M 1 /βk M i + γ K M 1 /βk M i c βk M /βk M i + + γ K M N 1 /βk M i cn βk M N /βk M i 4. k = a 13 m 1 a m m = a p m i # # 3# 5# 6# 7# 8# 9# Legendre l 13 l 1 r l error 4 5 1# # 3# 5# = l ac - l es /l ac 1% l ac l es 6# 7# 8# 9# Fig. 4 4 Orthogonal decomposition coefficients of diesel gas signals and their fitting results
6 4 177 Fig. 5 5 Orthogonal decomposition coefficients of gear oil gas signals and their fitting results 1 1ml 5ml 15% Tab. 1 1 Estimation result of sample volumes for single gas and the mixture gas l ac /m l es /ml r l error /% l es /ml r l error /% % x m 1 5 x m 13
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