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Environmental Monitoring Part 3 potx

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Air Pollution Analysis with a Possibilistic and Fuzzy Clustering Algorithm Applied in a Real Database of Salamanca (México) 11 station we observe that either SO 2 or PM 10 pollutant concentrations are highest. At the DIF monitoring station we observe t he highest PM 10 concentrations in the AEMN network. The main proposal in this work is to apply the PFCM clustering algorithm to the AEMN in Salamanca as well to integrate the pollutant measures f r om the three monitoring stations. The PFCM initial parameters (a, b, m and η) are very important in order to reduce the outlier effects in the pattern prototypes. Pal et al, i n Pal et al. (2005) recommend of b parameter value larger than the a parameter value in o r der t o reduce the mentioned effects. On the other hand, a small value for η and a value greater than 1 for m are recommended. nevertheless, choosing a too high of a value of m reduces the effect of membership of data to the clusters, and the algorithm behaves a s a simple PCM. Taking into account the previous recommendations, the initial parameters for the PFCM clustering algorithm were set as follows: a = 1, b = 5, m = 2andη = 2. The found prototypes ( a and b)areshowninFig.4. In Fig. 4(a) the daily averages of SO 2 concentrations are presented for each monitoring station together with the corresponding prototypes. It is observed also that Cruz Roja monitoring station receives the highest emissions of SO 2 concentrations: this is due to its location near to the refinery. The prototypes in this case were very low in comparison with the observed SO 2 concentrations, because only one station observed high SO 2 concentrations (Cruz Roja). According with the analyzed patterns the emitted pollutant is only measured by the Cruz Roja monitoring station (see Fig. 4). Fig. 4(b) shows the daily averages of PM 10 concentrations and result prototypes. In this case, the observed averages are very similar at the three monitoring stations. The PM 10 pollutant dispersion is more uniform then the SO 2 pollutant dispersion in the city. Table 2 shows the correlation results among SO 2 and PM 10 pollutants and the meteorological variables. T he database used in the correlation anal ysis correspond to year 2004 of Nativitas. This period was taking because contains more meteorological registrations. The obtained results o f the SO 2 correlation coefficient show a high positive correlation between SO 2 pollutant and Wind Speed, also a high and negative correlation between SO 2 pollutant and Wind Direction is observed. The other m eteorological variables have not impact. For the PM 10 pollutant, the meteorological variable with more impact is the Relative Humidity. We observe, when the Relative Humidity increases the pollutant concentration decreases. The PM 10 particles are caught and fall to the ground during rain. SO 2 PM 10 SO 2 1 0.0731 PM 10 0.0731 1 WS 0.4756 -0.1385 WD -0.6151 0.1478 T -0.0329 -0.0007 RH -0.0322 -0.4416 BP 0.1462 0.1806 SR -0.021 -0.1207 Table 2. Correlation Coefficient between pollutant concentration and meteorological variables. 61 Air Pollution Analysis with a Possibilistic and Fuzzy Clustering Algorithm Applied in a Real Database of Salamanca (México) 12 Environmental Monitoring 0 5 10 15 20 25 30 0 20 40 60 80 100 120 Number of Days SO 2 Concentration (ppb) Comparison among monitoring points and prototype CR DF NA Prototype (a) SO 2 0 5 10 15 20 25 30 0 20 40 60 80 100 120 Number of Days PM 10 Concentration( μ gr/m 3 ) Comparison among monitoring points and prototype CR DF NA Prototype (b) PM 10 Fig. 4. Comparison between air pollutant averages and estimated prototypes. 62 Environmental Monitoring Air Pollution Analysis with a Possibilistic and Fuzzy Clustering Algorithm Applied in a Real Database of Salamanca (México) 13 5. Conclusions Nowadays, there is a program to improve the air quality in the city of Salamanca, Mexico. Besides, this program has established thresholds for several levels of contingencies depending on the SO 2 and PM 10 pollutant concentrations. However, a particular level of contingency for the city is declared taking into account the highest pollutant concentration provided by one of the thre e monitoring stations. For example, i f a p ollutant concentration exceeds a given threshold in a single monitoring station, the alarm of contingency applies to the whole city. This value is normally provided by the Cruz Roja station, due to its proximity to the refinery and power generation industries. Looking for local and general contingency levels in the city, we have proposed to estimate a set of prototypes such that they can represent a calculated measure of pollutant concentrations according to the values measured in the three fixed stations. In such a way, a local alarm of contingency can be activated in the area of impact of the pollution depending on each station, and a general alarm of contingency according to the values provided by the prototypes. Nevertheless, the last case requires adjusting the thre sholds, as the actual values would be only used for l ocal contingency because they depend on the measured values of pollutant concentrations, and the general contingency requires thresholds as a function of calculated values. 6. References Andina, D. & Pham, D. T. (2007). Computational Intelligence,Springer. Barron-Adame, J. M., Herrera-Delgado, J. A., Cortina-Januchs, M. G., Andina, D. & Vega-Corona, A. (2007). Air pollutant level estimation applying a self-organizing neural network, Proceedings of the 2nd international work-conference on Nature Inspired Problem-Solving Methods in Knowledge Engineering. IWINAC-07, pp. 599–607. Bezdek, J. C . (1981). Pattern Recognition With Fuzzy Objective Function Algorithms,Kluwer Academic. Bezdek, J. C., Keller, J., Krishnapuram, R. & Pal, N. R. (1999). Fuzzy Models and Algorithms for Pattern Recognition and Image Processing,firstedn,Boston,London. Celik, M. B. & Kadi, I. (2007). The re lation between meteorological factors and pollutants concentration in karabuk city, G.U. Journal of science 20(4): 87–95. Cortina-Januchs, M. G., Barron-Adame, J. M., Vega-Corona, A. & Andina, D. ( 2009). Prevision of industrial so2 pollutant concentration applying anns, Proceedings of The 7th IEEE International Conference on Industrial Informatics (INDIN 09), pp. 510–515. Dunn, J. (1973). A fuzzy relative of the isodata process and its use in detecting compact well-separated clusters, Journal of Cybernetics 3(3): 32–57. EPA (2008). Air quality and health, chap ter Environmental Protection A gency, National Ambient Air Quality Standards (NAAQS). Fenger, J. (2009). Air pollution in the last 50 years - from local to global, Journal of Atmospheric Environment 43(1): 13–22. Hoppener, F., Klawonn, F., Kruse, R. & Runkler, T. (2000). Fuzzy Cluster Analysis, Methods for classification, data analysis and image recognition, Chistester, United Kingdom. INE (2004). Programa para mejorar la calidad del aire en S alamanca, 2 edn, Instituto de Ecología del Estado de Guanajuato, Calle Aldana N.12, Co l. Pueblito de Rocha, 36040 Guanajuato, Gto. 63 Air Pollution Analysis with a Possibilistic and Fuzzy Clustering Algorithm Applied in a Real Database of Salamanca (México) 14 Environmental Monitoring INEGI (2005). National Population and Housing Census 2, National Institute of Geography and Statistics. www.inegi.org.mx. Krishnapuram, R. & Keller, J. (1993). A possibilistic approach to clustering, International Conference on Fuzzy Systems 1(2): 98–110. Krishnapuram, R. & Keller, J. (1996). The possibilistic c-means algorithm: Insights and recommendations, International Conference on Fuzzy Systems 4, no 3: 385–393. Ojeda-Magaña, B., Quintanílla-Dominguez, J., Ruelas, R. & Andina, D. (2009b). Images sub-segmentation with the pfcm clustering algorithm, Proceedings of The 7th IEEE International Conference on Industrial Informatics (INDIN 09), pp. 499–503. Ojeda-Magaña, B., Ruelas, R., Buendía-Buendía, F. & Andina, D. (2009a). A greater knowledge extraction coded as fuzzy rules and based on the fuzzy and typicality degrees of the GKPFCM clustering algorithm, In Intelligent Automation and Soft Computing 15(4): 555–571. Pal, N. R., Pal, S. K. & Bezdek, J. C. (1997). A mixed c-means clustering model, IEEE International Conference on Fuzzy Systems, Spain, pp. 11–21. Pal, N. R., Pal, S. K., Keller, J. M. & Bezdek, J. C. (2004). A new hybrid c-means clustering model., Proceedings of the IEEE International Conference on Fuzzy Systems, FUZZ-IEEE04, I. Press, Ed. Pal, N. R., Pal, S. K., Keller, J. M. & Bezdek, J. C. (2005). A possibilitic fuzzy c-means clustering algorithm, IEEE Transactions on Fuzzy Systems 13(4): 517–530. Pérez, P., Trier, A. & Reyes, J. (2000). P rediction of pm 2.5 concentrations several hours in advance using neural networks in santiago, chile, Atmospheric Environment 34(8): 1189–1196. Ruspini, E. (1970). N umerical method for fuzzz clustering, Information Sciences 2(3): 319–350. Timm, H., Borgelt, C., Döring, C. & Kruse, R. (2004). An extension to possibilistic fuzzy cluster analysis, Fuzzy Sets and systems 147, no 1: 3–16. Timm, H. & Kruse., R. (2002). A modification to improve possibilistic fuzzy cluster analysis., Conference Fuzzy Systems, FUZZ-IEEE, Honolulu, HI, USA. WHO (2008). Air quality and health, chapter World Health Organization. Zamarripa, A. & Sainez, A. (2007). Medio Ambiente: Caso Salamanca, Instituto de Investigación Legistativa, H. Congreso del Estado de Guanajuato, LX legislatura. Zuk, M., Cervantes, M. G. T. & Bracho, L. R. (2007). Tercer almanaque de datos y tendencias de la calidad del aire en nueve ciudades mexicanas, Technical report, Secretaría de Medio Ambiente, Recursos Naturales Instituto Nacional de Ecología, México, D.F. 64 Environmental Monitoring 5 Real-Time In Situ Measurements of Industrial Hazardous Gas Concentrations and Their Emission Gross F.Z. Dong et al. * Anhui Institute of Optics and Fine Mechanics, Chinese Academy of Sciences, Science Island, Hefei, P. R. China 1. Introduction Over the past few decades environmental protection has been of greatly worldwide concerns due to the fact of global warming and air quality deterioration particularly in the fast developing countries like China and India (Platt, 1980; Edner, 1991; Sigrist, 1995; Culshaw, 1998; Fried, 1998; Linnerud, 1998; Weibring, 1998; Nelson, 2002; Liu, 2002; Christian, 2003 & 2004; Taslakov, 2006; de Gouw, 2007; Karl, 2007 & 2009; http://www.cnemc.cn). These have resulted in large demands and tremendous efforts for new technology developments to monitor and control industrial gas pollution (Lindinger, 1998; Dong, 2005; Kan, 2006 & 2007; Wang Y.J., 2009; Wang F., 2010; Xia, 2010; Zhang, 2011). CO 2 , CO, NH 3 , H 2 S, HF, HCI, and volatile organic compounds (VOCs) are very important gases generated in many industrial processes; therefore to implement on-line monitoring of these industrial emitted gases is a key factor for industrial process control. Furthermore if one can simultaneously measure the gas flow path-averaged velocity and gas concentrations in a smokestack, all the industrial emissions from the targeted smokestack would be real- time obtained. This could be much beneficial to the administrative implementation of global environmental protection policy on reduction of gas pollution and environmental management. Tunable diode laser absorption spectroscopy (TDLAS) is a kind of technology with advantages of high sensitivity, high selectivity and fast responsibility. It has been widely used in the applications of green-house measurements (Feher, 1995; Nadezhdinskii, 1999; Kan, 2006), hazardous gas leakage detection (May, 1989; Uehara, 1992; Iseki, 2000 & 2004), industry process control (Linnerud, 1998; Deguchi,2002) and combustion gas measurements (Zhou, 2005; Rieker, 2009). Proton transfer reaction—mass spectrometry (PTR-MS) is a relatively new technology firstly developed at the University of Innsbruck, Austria, in the 1990s (Hansel, 1995). PTR-MS has been found being an extremely powerful and promising technology for on- line detection of VOCs at trace level (Smith, 2005; Jordan, 2009). Optical flow sensor (OFS-2000) based on the concept of optical scintillation to measure airflow velocity (Wang T.I., 1981; * W.Q. Liu, Y.N. Chu, J.Q. Li, Z.R. Zhang, Y. Wang, T. Pang, B. Wu, G.J. Tu, H. Xia, Y. Yang, C.Y. Shen, Y.J. Wang, Z.B. Ni and J.G. Liu Anhui Institute of Optics and Fine Mechanics, Chinese Academy of Sciences, Science Island, Hefei, P. R. China. Environmental Monitoring 66 http://www.opticalscientific.com), which is first developed by Optical Scientific INC., has been widely used in the market. OFS-2000 utilizes the high frequency signal of optical scintillation cross-correlation (OSCC) which is from the fluctuations of temperature or refractive index. However, OFS-2000 is not applicable when the temperature fluctuation within the measurement area is small or even ignorable. Recently we have developed a new kind of optical flow sensor which is based on the low frequency signal of OSCC resulting from the particle concentration fluctuations. Therefore the newly developed optical flow sensor could also measure the particle concentration in the stack. The content of this chapter will first briefly describe the operational principles based on TDLAS, PTR-MS and OSCC technologies for industrial pollution on-line monitoring. Then the instruments developed by our group to measure the emission gross will be introduced. In the third section some experimental results from the field test will be presented. Finally the discussions and conclusions will be given. 2. Basic operational principles of the instruments 2.1 TDLAS technique For detecting low concentration gases at atmospheric pressure with TDLAS technique, two- tone modulations and harmonic detection method are commonly adopted. The diode laser is modulated with the homemade current and temperature controllers to the wavelength of 1.567μm which precisely locates at the selected absorption line central of target gas CO. The laser wavelength is scanned through the selected absorption line by a saw-tooth signal at low frequency of 147Hz and simultaneously modulated by a sinusoidal signal at frequency of 20 KHz. The modulated laser beam is divided into two parts with a 1×2 fiber splitter. One arm (20%) is used to go through a 10cm calibration cell as a reference signal, while the other arm (80%) is used to measure the flue gas concentrations. Two transmitted laser beams are collimated and then collected by two coincident InGaAs photodiodes after passing through absorption gases, respectively. These two current signals are then transmitted into the digital control module (DCM) to gain the harmonic signals. At last, these signals are sent to computer for processing and harmonic signal detection technique is used for calculation of the target gas concentration. The schematic diagram of the online TDLAS experimental setup is shown in Figure 1. flue gas DFB-Laser TEC CUR Digital control module 16bit 1f、2f harmonic signals collimating system focusing system Fiber splitting detector Calibration cell Serial port acquisition flue gas DFB-Laser TEC CUR Digital control module 16bit 1f、2f harmonic signals collimating system focusing system Fiber splitting detector Calibration cell Serial port acquisition TEC: thermo-electronic cooler; CUR: current controller. Fig. 1. On-line experimental apparatus for TDLAS system. Real-Time In Situ Measurements of Industrial Hazardous Gas Concentrations and Their Emission Gross 67 When the light passes through flue gases, lots of factors can reduce the light intensity, like dust scattering and absorption in transmission medium. Considering about the intensity reduction by gas absorption, Beer-Lambert law is used. The responses can be described as: 0 exp( ) I kL I  (1) Where I represents the light intensity after passing the absorption gas, and I 0 represents the light intensity before passing the absorption gas, k is a reducing coefficient and L denotes the path length. When the gas absorption is very small, i.e., kL≤0.05 (Reid, 1981; Cassidy, 1982), equation (1) can be simplified as: 0 11() I kL CL I    (2) Where σ(ν) is the absorption coefficient. C and L stand for gas concentration and total optical length. The intensity of second harmonic (2f) signal can be expressed as below (Reid, 1981; Kan, 2006): I 2f ∝ I 0 σ 0 CL (3) Where I 2f is proportional to the incident laser intensity I 0 and absorption coefficient σ 0 at the central wavelength of the absorption line. . Nonlinear least square multiplication method is used to fit the 2f signal with reference signal for gaining the calibration coefficient a (Kan, 2007): I 01 C Mea L 01 = a I 02 C Ref L 02 (4) Where C Mea and C Ref are the concentrations of the target gas to be measured and reference gas in the calibration cell, respectively; I 01 , I 02 are the initial intensities of the two laser beams; L 01 and L 02 are the length of measurement optical path and the calibration cell, respectively. From equation (4), we could obtain: C Mea = a I 02 C Ref L 02 / I 01 L 01 (5) While a saw-tooth current is added on the DFB diode laser, the light wavelength will scan in a certain region, then the gas can be detected if there is a gas absorption line in that region. For detection of high concentration gas, direct absorption method is often used. This method is very simple but the sensitivity is suffered from massive random noises, which is mainly the 1/f noise from the diode laser and the photon detector. However, for low concentration gas detection, in order to eliminate serious noises in the system and enhance the sensitivity, another high frequency sine modulation current is added on the ramp signal. The gas absorption signal can be then achieved with high SNR by monitoring the second harmonic signal of absorption in a very narrow frequency band using a lock-in amplifier (LIA). If one does not pay enough attention, there will be so many factors like dust scattering and imperfect performance of laser source itself affecting the measurement accuracy. In addition, for a practical TDLAS system there are always various noises inevitably existed resulting from predictable or unpredictable sources. For instance, quickly changing random noise affects the sensitivity, and slow signal distortion limits long-term stability of the system Environmental Monitoring 68 because of its large amplitude. It has been reported that a lot of reasons like wavelength drifts and etalon fringe structure change because of thermal effect can result to slow 2f signal distortion (Werle, 1996). Few technologies had been reported to eliminate those distortions like rapid background subtraction (Cassidy & Reid, 1982) and digital signal processing (Reid, 1980), but there are some limits of those ideas when the condition is changed. In fact it is inconvenient to get the background structure in real time for a in situ gas analytical system, particularly when the interference or distortion has similar frequency with the absorption signal in which the digital method could not work well. Over the past decades many advanced digital signal processing methods for TDLAS system development have been reported. Peter Werle et al (Werle, 1996 & 2004) have demonstrated a method to avoid the effects of noise disturbances and laser wavelength drifts during integration and background changes. To decrease high frequency noise and enhance the stability of a practical TDLAS system, except of optimizing hardware, advanced signal processing algorithm is also needed and have been explored by our group (Xia,2010;Zhang,2010). One of the novel features in our research is the use of digital signal processing for harmonic signals for which the laser output wavelength can be locked at the absorption line center and fit with reference harmonic signal by utilizing nonlinear least squares routine. The signal-correlation must be computed rapidly. The Fast Fourier Transform (FFT), low-pass filter and Inverse Fast Fourier Transform (IFFT) algorithm are adopted. The correlation version for an N-point spectrum signal is: 0 (,) Ref Ref Mea Mea N i jij j CSS S S S S       (6) Where S Ref and S Mea are the reference and measurement signals acquired during calibration and subsequent measured harmonic signal, respectively with the lag represented by i. Using the discrete FFT the correlation signal C(S, S) i can be written as: * (,) ( ) ( ) Ref M ea ij j CSS F S F S (7) where F j (S) stands for the FFT of S. The low pass filter is used to remove high frequency noise simultaneously in the process. The IFFT result between measured signal and reference signal in the above process is used to get the correlation data. Then using the peak-find routine the drift MAX-value position is obtained. At last, the corrected signal position is translated getting the proper data to decrease effects caused by the temperature, current and other external uncertain factors. 2.2 PTR-MS Proton transfer reaction mass spectrometry (PTR-MS) was first developed at the Institute of Ion Physics of Innsbruck University in the 1990’s. Nowadays PTR-MS has been a well- developed and commercially available technique for the on-line monitoring of trace volatile organic compounds (VOCs) down to parts per trillion by volume (ppt) level. PTR-MS has some advantages such as rapid response, soft chemical ionization (CI), absolute quantification and high sensitivity. In general, a standard PTR-MS instrument consists of external ion source, drift tube and mass analysis detection system. Fig. 2 illustrates the basic composition of the PTR-MS instrument constructed in our laboratory using a quadrupole mass spectrometer as the detection system. Real-Time In Situ Measurements of Industrial Hazardous Gas Concentrations and Their Emission Gross 69 Fig. 2. Schematic diagram of the PTR-MS instrument that contains a hollow cathode (HC), a source drift (SD) region, an intermediate chamber(IC) and a secondary electron multiplier (SEM). Perhaps the most remarkable feature of PTR-MS is the special chemical ionization (CI) mode through well-controlled proton transfer reaction, in which the neutral molecule M may be converted to a nearly unique protonated molecular ion MH + . This ionization mode is completely different from the traditional MS where electron impact (EI) with energy of 70 eV is often used to ionize chemicals like VOCs. Although the EI source has been widely used with the commercial MS instruments most coupled with a variety of chromatography techniques, these MS platforms have a major deficiency: in the course of ionization the molecule will be dissociated to many fragment ions. This extensive fragmentation may result in complex mass spectra pertain especially when a mixture is measured. If a chromatographic separation method is not used prior to MS, then the resulting mass spectra from EI may be so complicated that identification and quantification of the compounds can be very difficult. In PTR-MS instrument, the hollow cathode discharge is served as a typical ion source [Blake, 2009], although plane electrode dc discharge [Inomata, 2006] and radioactive ionization sources [Hanson, 2003] recently have been reported. All of the ion sources are used to generate clean and intense primary reagent ions like H 3 O + . Water vapor is a regular gas in the hollow cathode discharge where H 2 O molecule can be ionized according to the following ways (Hansel, A.,1995). e+H 2 O → H 2 + +O+2e (8) e+ H 2 O → H + + OH+2e (9) e+H 2 O → O + + H 2 + 2e (10) e+H 2 O → H 2 O + +2e (11) Environmental Monitoring 70 The above ions are injected into a short source drift region and further react with H 2 O ultimately leading to the formation of H 3 O + via ion-molecule reactions: H 2 + +H 2 O → H 2 O + +H 2 (12a) → H 3 O + +H (12b) H + +H 2 O → H 2 O + +H (13) O + +H 2 O → H 2 O + +O (14) OH + +H 2 O → H 3 O + +O (15a) → H 2 O + +OH (15b) H 2 O + +H 2 O → H 3 O + +OH (16) Unfortunately, the water vapor in the source drift region can inevitably form a few of cluster ions H 3 O + (H 2 O) n via the three-body combination process H 3 O + (H 2 O) n-1 +H 2 O+A→ H 3 O + (H 2 O) n +A (n≥1) (17) where A is a third body. In addition there are small amounts of NO + and O 2 + ions occurred due to sample air diffusion into the source region from the downstream drift tube. Thus an inlet of venturi-type has been employed on some PTR-MS systems to prevent air from entering the source drift region (Duperat, 1982; Lindinger, 1998). At last the H 3 O + ions produced in the ion source can have the purity up to > 99.5%. Thus, unlike SIFT-MS technique (Smith, 2005), the mass filter of the primary ionic selection is not needed and the H 3 O + ions can be directly injected into the drift tube. In some of PTR-MS, the ion intensity of H 3 O + is available at 10 6 ~10 7 counts per second on a mass spectrometer installed in the vacuum chamber at the end of the drift tube. Eventually the limitation of detection of PTR- MS can reach low ppt level. Instead of H 3 O + , other primary reagent ions, such as NH 4 + , NO + and O 2 + , have been investigated in PTR-MS instrument (Wiche, 2005; Blake, 2006; Jordan, 2009). Because the ion chemistry for these ions is not only proton transfer reaction, the technique sometimes is called chemical ionization reaction mass spectrometry. However, the potential benefits of using these alternative reagents usually are minimal, and to our knowledge, H 3 O + is still the dominant reagent ion employed in PTR-MS research (Blake, 2009; Lindinger, 1998; de Gouw, 2007; Jin, 2007). The drift tube consists of a number of metal rings that are equally separated from each other by insulated rings. Between the adjacent metal rings a series of resistors is connected. A high voltage power supplier produces a voltage gradient and establishes a homogeneous electric field along the axis of the ion reaction drift tube. The primary H 3 O + ions are extracted into the ion reaction region and can react with analyte M in the sample air, which through the inlet is added to the upstream of the ion reaction drift tube. According to the values of proton affinity (PA) (see Table 1), the reagent ion H 3 O + does not react with the main components in air like N 2 , O 2 and CO 2 . In contrast, the reagent ion can undergo proton transfer reaction with M as long as the PA of M exceeds that of H 2 O (Lindinger, 1998). [...]... HCN HCOOH C6H6 C3H6 CH3OH CH3COH C2H5OH CH3CN CH3COOH C7H8 CH3CH2COH C8H10 CH3COCH3 CH2C(CH3)CHCH2 NH3 C6H7N 4 20 40 32 28 44 16 28 30 28 18 34 27 46 78 42 32 44 46 41 60 92 58 106 58 68 17 93 Table 1 Proton affinities of some compounds Proton affinity(NIST database) (kJ mol-1) 177.8 198.8 36 9.2 421 4 93. 8 540.5 5 43. 5 594 596 .3 680.5 691 705 712.9 742 750.4 751.6 754 .3 768.5 776.4 779.2 7 83. 7 784 786 796... instrument 84 Environmental Monitoring 8.00E-0 13 37amu Ion intensity (Amps) 7.00E-0 13 A u g u st 9 ,2 0 1 0 6.00E-0 13 33amu 5.00E-0 13 4.00E-0 13 3.00E-0 13 2.00E-0 13 79amu 1.00E-0 13 95amu 0.00E+000 20 40 60 80 100 120 140 160 180 m /z Fig 19 The total mass scans of VOCs inside the stack measured with PTR-MS -2 1 4 x 1 0 -2 1 2 x 1 0 -2 1 0 x 1 0 -2 8 0 x 1 0 -3 6 0 x 1 0 -3 4 0 x 1 0 -3 2 0 x 1 0 Emission... C r 2 3 , ( l0  r  L0 ) (33 ) 2 where C is the structure constant of extinction coefficient and r is the distance of two arbitrary points in turbulence field, l0 and L0 are the inner-scale and out-scale of turbulence, respectively Replacing  with the out-scale of turbulence L0 in Eq (30 ), and insert Eq (33 ) into Eq (30 ), we then obtain: R ( x , l  v )  1 2 23 C ( L0  r 2 3 ) , 2 (34 ) where... scintillation spectrums in part of low frequency is -8 /3 Fig 13 The received data signal from both receivers 1 0.1 0.01 f 1E -3 -8 /3 1E-4 wlnI(f)/Hz -1 1E-5 1E-6 1E-7 1E-8 1E-9 1E-10 1E-11 1E-12 1E- 13 1E-14 1E-15 0.1 1 10 100 1000 f/Hz Fig 14 The low frequency part of optical scintillation spectrum The low frequency of optical scintillation caused by stack gas flow is relative to the particle concentration... ) , 2 (34 ) where r  x 2  ( l  v )2 , while r  L0 , R  0 Inserting Eq (34 ) into Eq (28), L 2 C ln I ( l ,  )  C  ( L  x )( L0 2 3  r 2 3 )dx , ( r  x 2  ( l  v )2 ) 0 Fig.4 shows the numerical simulation results of Eq (35 ) (35 ) 76 Environmental Monitoring Fig 4 The numerical computer simulations of Eq (35 ) Here ν=5m/s, L=2m and L0=10m In Fig 4, the time delay at the peak of the cross-correlation... Spectrometry, 19, 33 56 -33 62 Xia, H.; Dong, F.Z.; Tu, G.J.; et al (2010) High sensitive detection of carbon monoxide based on novel multipass cell , Acta Optica Sinica, Vol .30 , No.9, pp2596-2601(in Chinese) Yuan, Z F.; Wang, X D.; Zhou, J.; Pu, X G & Cen, K F (20 03) Experimental studies on measurement of particle flow velocity using optical scintillation cross-correlations Thermal Power Generation, Vol .3, pp46-50... (2010) Simultaneous measurement on gas concentration and particle mass concentration by tunable diode laser, Flow Measurement and Instrumentation, Vol.21, No .3, pp382 -38 7 Wang J.; Maiorov M.; Baer D.S.; Garbuzov D.Z.; Connolly J.C & Hanson R.K (2000) In situ combustion measurements of CO with diode-laser absorption near 2 .3 um Appl Opt., 39 (30 ), pp5579-5589 Wang, T.I.; Ochs, G.R.& Lawrence, R.S (1981)... laboratory with the developed PTR-MS instrument 80 Environmental Monitoring 3. 3 OSCC instrument developed for gas flow velocity measurement In order to measure gas flow velocity in stack, a gas flow velocity sensor was constructed based on the low frequency part of the double-path optical scintillation cross correlation The schematic diagram of velocity and particle concentration measuring system is shown... temporal crosscorrelation of the optical scintillations,Appl Opt., Vol.20, No. 23, pp40 73- 4081 Wang ,Ting-I (20 03) .,United States Patent 6,661 ,31 9 B2 Wang, Y.J.; Han, H.Y.; Shen, C.Y.; Li J.Q.; Wang, H.M & Chu, Y.N (2009) Control of solvent use in medical devices by proton transfer reaction mass spectrometry and ion 90 Environmental Monitoring molecule reaction mass spectrometry Journal of Pharmaceutical... 0 x 1 0 -3 4 0 x 1 0 -3 2 0 x 1 0 Emission rate(kg/h) 1 6 x 1 0 -3 33am u 45am u 59am u 79am u 95am u 0 0 0 201 -7 -6 0 0 0 00 :0 0 0 :0 0 0 :0 0 7 :0 0 :0 0 9 :0 0 :0 0 0 :0 1 9 :0 0 : 0 0 :0 7 :0 0 9 1 9 :0 1 1 9 :0 3 7: 9 2 7: -1 -9 -7 -8 -1 1 0 -8 -2 5 -7 -1 1 0 -7 -3 1 -1 0 0 1 0 2 0 1 0 -9 010 010 010 2 2 2 2 20 20 Fig 20 On-line monitoring results of the VOCs emission rate measured with PTR-MS . in Eq. (30 ), and insert Eq. (33 ) into Eq. (30 ), we then obtain : 23 23 2 0 1 (, ) ( ) 2 Rxlv CL r     , (34 ) where 22 ()rxlv   , while 0 rL , 0R   . Inserting Eq. (34 ) into. Acetonitrile CH 3 CN 41 779.2 Acetic acid CH 3 COOH 60 7 83. 7 Toluene C 7 H 8 92 784 Propanal CH 3 CH 2 COH 58 786 O-xylene C 8 H 10 106 796 Acetone CH 3 COCH 3 58 812 Isoprene CH 2 C(CH 3 )CHCH 2 . sulphide H 2 S 34 705 Hydrogen cyanide HCN 27 712.9 Formic acid HCOOH 46 742 Benzene C 6 H 6 78 750.4 Propene C 3 H 6 42 751.6 Methanol CH 3 OH 32 754 .3 Acetaldehyde CH 3 COH 44 768.5

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