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1

Dunwell, M., Junhua Wang, Y. Yan, and B. Xu. "Surface enhanced spectroscopic investigations of adsorption of cations on electrochemical interfaces." Physical Chemistry Chemical Physics 19, no. 2 (2017): 971–75. http://dx.doi.org/10.1039/c6cp07207k.

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2

Cabrera, A. L., J. Espinosa-Gangas, Johan Jonsson-Akerman, and Ivan K. Schuller. "Kinetics of subsurface hydrogen adsorbed on niobium: Thermal desorption studies." Journal of Materials Research 17, no. 10 (October 2002): 2698–704. http://dx.doi.org/10.1557/jmr.2002.0390.

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The adsorption/absorption of hydrogen and the adsorption of carbon monoxide by niobium foils, at room temperature, was studied using thermal desorption spectroscopy. Two hydrogen desorption peaks were observed with a maximum at 404 and 471 K. The first hydrogen desorption peak is regarded as hydrogen desorbing from surface sites while the second peak, which represents desorption from surface sites stronger bound to the surface, also has a component—due to its tailing to higher temperatures—of hydrogen diffusing from subsurface sites. Carbon monoxide adsorption was used to determine the number of surface sites, since it does not penetrate below the surface. Two carbon monoxide desorption peaks are observed in these experiments: at 425 and 608 K. The first peak is regarded as the adsorption of molecular carbon monoxide, and the second, as carbon monoxide dissociated on the niobium surface. The crystallographic orientation of the foils was determined by x-ray diffraction and showed a preferential (110) orientation of the untreated foil due to the effect of cold rolling. This preferential orientation decreased after hydrogen/heat treatment, appearing strong also in the (200) and (211) orientations. This change in texture of the foils is mainly due to the effect of heat treatment and not to hydrogen adsorption/desorption cycling. The kinetics of hydrogen and CO desorption is compared with that of Pd and Pd alloys.
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3

Wadayama, T., K. Abe, and H. Osano. "Infrared reflection absorption study of carbon monoxide adsorption on Pd/Cu(111)." Applied Surface Science 253, no. 5 (December 2006): 2540–46. http://dx.doi.org/10.1016/j.apsusc.2006.05.014.

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4

Lyons, K. J., J. Xie, W. J. Mitchell, and W. H. Weinberg. "Adsorption of carbon monoxide on Ir(110) investigated by infrared reflection-absorption spectroscopy." Surface Science 325, no. 1-2 (February 1995): 85–92. http://dx.doi.org/10.1016/0039-6028(94)00729-2.

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5

Rakic, Vesna, Vera Dondur, and Radmila Hercigonja. "FTIR study of carbon monoxide adsorption on ion-exchanged X, Y and mordenite type zeolites." Journal of the Serbian Chemical Society 68, no. 4-5 (2003): 409–16. http://dx.doi.org/10.2298/jsc0305409r.

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In this work Fourier transform infrared (FTIR) study has been applied to study the adsorption of carbon monoxide on transition metal (Mn2+, Co2 Ni2+) ion-exchanged zeolites type Y, X and mordenites. The adsorption of CO at room temperature produces overlapping IR absorption bands in the 2120?2200 cm-1 region. The frequency of the band around 2200 cm-1 is found to be dependent not only on the charge-balancing transition metal cation but also on the framework composition. The frequencies of the band near 1600 cm-1 was found to be dependent on the Si/Al ratio of the investigated zeolites.
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6

Wadayama, T., H. Yoshida, S. Oda, and N. Todoroki. "Infrared Reflection Absorption Study for Carbon Monoxide Adsorption on Chromium Deposited Cu(100) Surfaces." MATERIALS TRANSACTIONS 50, no. 4 (2009): 819–24. http://dx.doi.org/10.2320/matertrans.mra2008442.

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7

Wadayama, Toshimasa, Hirosato Yoshida, Naoto Todoroki, and Shogo Oda. "Carbon Monoxide Adsorption on Ni/Pt(111) Surfaces Investigated by Infrared Reflection Absorption Spectroscopy." e-Journal of Surface Science and Nanotechnology 7 (2009): 230–33. http://dx.doi.org/10.1380/ejssnt.2009.230.

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8

Wadayama, T., H. Osano, K. Murakami, T. Maeyama, and H. Yoshida. "Infrared reflection absorption study of carbon monoxide adsorption on Fe-deposited Pt(111) surface." Journal of Physics: Conference Series 100, no. 1 (March 1, 2008): 012007. http://dx.doi.org/10.1088/1742-6596/100/1/012007.

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9

Wadayama, Toshimasa, Hiroshi Osano, Toshiaki Maeyama, Hirosato Yoshida, Koji Murakami, Naoki Todoroki, and Shogo Oda. "Infrared Reflection−Absorption Study of Carbon Monoxide Adsorption on Fe/Pt(111) Bimetallic Surfaces." Journal of Physical Chemistry C 112, no. 24 (May 21, 2008): 8944–50. http://dx.doi.org/10.1021/jp712095w.

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10

Lei, S. Y., S. Luan, and H. Yu. "Co-doped phosphorene: Enhanced sensitivity of CO gas sensing." International Journal of Modern Physics B 32, no. 06 (February 26, 2018): 1850068. http://dx.doi.org/10.1142/s0217979218500686.

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First-principle calculation was carried out to systematically investigate carbon monoxide (CO) adsorption on pristine and cobalt (Co)-doped phosphorenes (Co-bP). Whether or not CO is adsorped, pristine phosphorene is a direct-band-gap semiconductor. However, the bandgap of Co-bP experiences direct-to-indirect transition after CO molecule adsorption, which will affect optical absorption considerably, implying that Co doping can enhance the sensitivity of phosphorene as a CO gas sensor. Moreover, Co doping can improve an adsorption energy of CO to 1.31 eV, as compared with pristine phosphorene (0.12 eV), also indicating that Co-bP is energetically favorable for CO gas sensing.
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11

Kitamura, Fusao, Machiko Takahashi, and Masatoki Ito. "Carbon monoxide adsorption on platinum (111) single-crystal electrode surface studied by infrared reflection-absorption spectroscopy." Surface Science 223, no. 3 (December 1989): 493–508. http://dx.doi.org/10.1016/0039-6028(89)90676-6.

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12

Kitamura, Fusao, Machiko Takahashi, and Masatoki Ito. "Carbon monoxide adsorption on platinum (111) single-crystal electrode surface studied by infrared reflection-absorption spectroscopy." Surface Science Letters 223, no. 3 (December 1989): A593. http://dx.doi.org/10.1016/0167-2584(89)90899-2.

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13

Yee, Nelson, Gary S. Chottiner, and Daniel A. Scherson. "Carbon Monoxide Adsorption on Ru-Modified Pt Surfaces: Time-Resolved Infrared Reflection Absorption Studies in Ultrahigh Vacuum." Journal of Physical Chemistry B 109, no. 12 (March 2005): 5707–12. http://dx.doi.org/10.1021/jp044641i.

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14

Wadayama, T., H. Osano, H. Yoshida, S. Oda, and N. Todoroki. "Carbon monoxide adsorption on Pd-deposited Cu(110) surface: Infrared reflection absorption and temperature programmed desorption studies." Applied Surface Science 254, no. 17 (June 2008): 5380–84. http://dx.doi.org/10.1016/j.apsusc.2008.02.061.

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15

Wadayama, T., Y. Sasaki, K. Shiomitsu, and A. Hatta. "Infrared reflection absorption study of carbon monoxide adsorption on Cu(100)-(2×2)p4g-Pd ordered alloy surface." Surface Science 592, no. 1-3 (November 2005): 72–82. http://dx.doi.org/10.1016/j.susc.2005.06.083.

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16

Lim, Young-Il, Jinsoon Choi, Hung-Man Moon, and Gook-Hee Kim. "Techno-economic Comparison of Absorption and Adsorption Processes for Carbon Monoxide (CO) Separation from Linze-Donawitz Gas (LDG)." Korean Chemical Engineering Research 54, no. 3 (June 1, 2016): 320–31. http://dx.doi.org/10.9713/kcer.2016.54.3.320.

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17

Mizushima, Takanori, Kazuyuki Tohji, and Yasuo Udagawa. "An extended x-ray absorption fine structure study on the morphology change of ruthenium catalyst by carbon monoxide adsorption." Journal of the American Chemical Society 110, no. 13 (June 1988): 4459–60. http://dx.doi.org/10.1021/ja00221a082.

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18

Oda, Ichiro, Hirohito Ogasawara, and Masatoki Ito. "Carbon Monoxide Adsorption on Copper and Silver Electrodes during Carbon Dioxide Electroreduction Studied by Infrared Reflection Absorption Spectroscopy and Surface-Enhanced Raman Spectroscopy." Langmuir 12, no. 4 (January 1996): 1094–97. http://dx.doi.org/10.1021/la950167j.

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19

Yoshida, Hirosato, Koichiro Ogawa, Naoto Todoroki, Yoshinobu Yamada, and Toshimasa Wadayama. "Carbon Monoxide Adsorption on Cobalt-Deposited Platinum Single Crystal Surfaces Investigated by IR Reflection-Absorption and Low-Energy Electron Diffraction." e-Journal of Surface Science and Nanotechnology 8 (2010): 161–66. http://dx.doi.org/10.1380/ejssnt.2010.161.

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20

Huy, Nguyen Nhat, and Bích Thảo Nguyễn Thị. "Thermal oxidation of carbon monoxide in air using various self-prepared catalysts." Science & Technology Development Journal - Engineering and Technology 2, SI2 (July 7, 2020): First. http://dx.doi.org/10.32508/stdjet.v2isi2.469.

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Carbon monoxide (CO) is a very toxic pollutant emitted from wood fired boiler, which is widely used in small and medium enterprises in Vietnam. The treatment of CO containing flue gas faces many difficulties due to the inert property of CO and cannot be removed by traditional adsorption and absorption methods and one of the effective CO treatments is catalytic oxidation. Therefore, we aimed to prepare various catalysts on different carriers for treatment of CO in flue gas, including γ-Al2O3-based metal oxides (Co3O4/Al2O3, Cr2O3/Al2O3, and CuO/Al2O3), CuO–MnOx/OMS-2, and CuO-MnOx/zeolite. The CO removal tests were conducted in a continuous fixed bed reactor in laboratory scale with temperature range of 50 – 550 oC. The characteristics of catalytic materials were then determined by various methods such as Brunauer-Emmett-Teller measurement, X-ray diffraction, energy-dispersive X-ray spectroscopy, Fourier transform infrared spectroscopy, scanning electron microscopy, and thermogravimetric analysis. Results showed that CuO-MnOx/OMS-2 was the best catalyst with high removal efficiency of 98.41% at reactor temperature of 250 oC while gas outlet temperature of < 50 oC, proving the suitability of this material for practical treatment of CO in flue gas. The reaction follows Mars-Van-Krevelen mechanism with the presence of Cu2+-O2--Mn4+ ↔ Cu+-o-Mn3+ + O2 redox in the structure of the material. Moreover, the effect of environmental factors such as flow rate, inlet CO concentration, and catalysts amount on the CO removal efficiency were investigated and noted for designing and operation purposes. Concentration of outlet CO met well QCVN 19: 2009/BTNMT - National technical regulation on industrial emissions for dust and inorganic substances. Therefore, CuO-MnOx/OMS-2 catalyst material could be a potential catalyst for treatment of CO in flue gas of boiler.
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21

Starostin, Andrey G., and Nikolai B. Khodyashev. "EFFECT OF DURATION OF OXYCHLORINATION ON DEGREE OF ACCESSIBILITY FOR CATALYSIS OF PLATINUM CENTERS OF PLATINUM-RHENIUM REFORMING CATALYST." IZVESTIYA VYSSHIKH UCHEBNYKH ZAVEDENII KHIMIYA KHIMICHESKAYA TEKHNOLOGIYA 63, no. 5 (April 14, 2020): 59–64. http://dx.doi.org/10.6060/ivkkt.20206305.6175.

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The work presents the results of a chemisorption analysis of a platinum-rhenium catalyst on an alumina support after regeneration and reduction with hydrogen. Adsorption-desorption diagrams were obtained by stepwise-pulsed chemisorption of carbon monoxide on reforming catalyst samples. With an increase in the number of carbon monoxide injections from 1 to 4, the catalyst sample is poisoned, and subsequent desorption peaks indicate the termination of the interaction. With an increase in the time of oxychlorination, the CO/Pt ratio in the carrier volume increases linearly. The effect of the oxychlorination process on the chemisorption of CO and the subsequent availability of platinum nanoparticles for catalysis has been shown. The absorption on freshly prepared platinum-rhenium catalyst samples reaches a CO/Pt molar ratio of about 0.4. The results show that the duration of oxychlorination for 16–20 h allows us to achieve the value of the ratio CO/Pt, which is in the range of 0.4-0.5. This indicates that the availability of platinum centers in its composition reaches the level of a fresh catalyst, and, on the other hand, taking into account a slight excess of this ratio, we can assume that some of the Re atoms participate in the absorption of CO molecules. The presence of finely dispersed platinum particles in the composition of the regenerated catalyst was confirmed by IR spectroscopy. The analysis of catalyst samples on an IR spectrometer in the frequency range of 1900-2200 cm-1 revealed a rather wide absorption band with a pronounced extremum at 2060 cm-1. In this frequency range, there is another, slightly pronounced extremum at 2149 cm-1. However, for samples with a short duration of oxychlorination, it did not appear. An absorption band with an extremum of 2060 cm-1 can be attributed to linear vibrations of adsorbed CO molecules on the surface of particles of metallic platinum.
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22

Kunimatsu, K., H. Seki, W. G. Golden, J. G. Gordon, and M. R. Philpott. "Carbon monoxide adsorption on a platinum electrode studied by polarization-modulated FT-IR reflection-absorption spectroscopy: II. Carbon monoxide adsorbed at a potential in the hydrogen region and its oxidation in acids." Langmuir 2, no. 4 (July 1986): 464–68. http://dx.doi.org/10.1021/la00070a016.

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23

Wadayama, T., K. Kubo, T. Yamashita, T. Tanabe, and A. Hatta. "Carbon monoxide adsorption on 4 monolayer thick fcc-Fe/Cu(1 0 0): infrared reflection absorption and low energy electron diffraction studies." Applied Surface Science 199, no. 1-4 (October 2002): 254–58. http://dx.doi.org/10.1016/s0169-4332(02)00847-4.

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24

Cabrera, A. L., Erie Morales, and J. N. Armor. "Kinetics of hydrogen desorption from palladium and ruthenium-palladium foils." Journal of Materials Research 10, no. 3 (March 1995): 779–85. http://dx.doi.org/10.1557/jmr.1995.0779.

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The absorption of hydrogen and carbon monoxide at room temperature by palladium and 5% ruthenium-palladium foils was studied using thermal desorption spectroscopy. It was found that hydrogen readily diffused in the palladium and desorbed as one broad peak at about 650 K. Plots of the In (rate) versus inverse absolute temperature indicate that the desorption order is n = 1.25 and the activation energy is about 8.5 Kcal/mol. Carbon monoxide is adsorbed, as two different states, on the surface of the foil and complete coverage is quickly reached below 100 L. Hydrogen also diffuses in 5% ruthenium-palladium foil but to a lesser degree. Two hydrogen desorption peaks are observed in the Ru-Pd alloy. The desorption traces can be fitted with two peaks and the desorption orders are n = 2 for the first peak and n = 1.25 for the second peak. Activation energies of 10.7 and 5.6 Kcal/mol are obtained for the first and second hydrogen peaks, respectively. The first hydrogen desorption peak is regarded as hydrogen desorbing from the surface sites while the second peak is regarded as hydrogen diffusing from below the surface. Activation energies for bulk diffusion were obtained from hydrogen uptake measurements using a sensitive microbalance. These energies corresponded to 4.4 Kcal/mol for Pd foil and 4.9 Kcal/mol for the Ru-Pd alloy. Discussion about the relation between these results with prior studies of hydrogen adsorption on Pd single crystal is included. The appearance of a fractional order for hydrogen desorption is also discussed.
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25

Wadayama, T., H. Osano, K. Hamade, H. Yoshida, and T. Maeyama. "Infrared reflection absorption study of carbon monoxide adsorption on Cu(100)–c(2×2)–Pd surfaces formed by palladium vacuum-depositions at various temperatures." Surface Science 601, no. 10 (May 2007): 2214–22. http://dx.doi.org/10.1016/j.susc.2007.03.033.

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26

Shafarenko, M., and O. Vorobyova. "RESEARCH OF METHANE PRODUCTION PROCESS FROM BIOGAS AND PYROLYSIS GAS." Municipal economy of cities 1, no. 161 (March 26, 2021): 280–83. http://dx.doi.org/10.33042/2522-1809-2021-1-161-280-283.

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The article investigates the separation process of biogas and the pyrolysis gas by application of membrane technology. The urgency of the problem of purification of industrial, agricultural, distillery waste or waste water by means of biological fermentation in anaerobic conditions of organic substances is indicated. If it is not possible to biodegrade waste, use pyrolysis or gasification. Pyrolysis gas, unlike biogas, has hydrogen and carbon monoxide. The process of separating methane from leaving impurities is much more economical than the process of removing impurities to obtain methane. Although for more than a hundred years mankind has known about the principles of gas diffusion and mass transfer through polymer films. But only in the last 40 years, membranes have begun to be used on an industrial scale in gas purification. With a membrane unit, a high methane production efficiency (> 96%) can be achieved. The lack of mechanical complexity and their modular design, which allows them to scale easily to provide significant flexibility, are increasingly gaining attention from the industry. The paper was proposed setting circuit for isolating methane and its operation is described. As a result of the research carried out, graphical dependencies were obtained at the stages: absorption (volume fraction of dissolved methane from the circulation ratio of the absorber), adsorption (absorption capacity of the membrane packing over time) and regeneration (the rate of desorption of the absorber from the membrane packing versus time). Using these dependencies, it is possible to calculate the flow rate of the absorber that is used in the absorption process and to determine the number of membrane elements for the membrane apparatus.
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27

Nurullita, Ulfa, and Mifbakhuddin Mifbakhuddin. "Efektifitas Tanaman Hias, Jamur, dan Carbon Aktif Dalam Menurunkan Konsentrasi Carbon Monoksida di Udara." Jurnal Kesehatan Lingkungan Indonesia 20, no. 1 (October 25, 2020): 15–20. http://dx.doi.org/10.14710/jkli.20.1.15-20.

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Latar belakang: Polusi udara dalam ruangan menjadi masalah kesehatan yang lebih berat dibanding di luar ruangan. Salah satu sumber pencemar udara dalam ruangan adalah rokok. Rokok mengandung setidaknya 200 elemen berbahaya bagi kesehatan, tiga di antaranya yang paling berbahaya, yaitu tar, nikotin, dan karbon monoksida. Kadar CO dari asap rokok pada penelitian sebelumnya berkisar 109-113 ppm. Kadar ini masih di atas nilai ambang batas yang diperbolehkan yaitu 25 ppm. Untuk itu perlu upaya untuk mengurangi CO di udara. Penelitian sebelumnya menyimpulkan adsorben dan absorben terbaik dalam menurunkan CO adalah kaktus, jamur Penicillium sp, dan karbon aktif kulit durian. Tujuan penelitian untuk mengetahui perbedaan kemampuan adsorbsi dan absorbsi CO berdasarkan jumlah kaktus, jamur Penicillium sp, dan karbon aktif kulit durian.Metode: Jenis penelitian adalah eksperimen semu dengan rancangan static group comparison. Obyek penelitian adalah CO udara dalam ruangan, variabel penelitian adalah jumlah adsorben/absorben, jenis adsorben/absorben, dan konsentrasi CO di udara. Pengukuran CO dengan CO meter digital. Analisis data dengan uji anova 1 arah dan uji kruskal wallis dengan tingkat kemaknaan 95%.Hasil: rata-rata CO dengan kaktus 1 batang 63 ppm, 2 batang 56 ppm, 3 batang 46,6 ppm, 4 batang 28 ppm, dan kontrol 106,6 ppm. Rata-rata CO dengan Penicillium sp 150 gram 47,3 ppm, 300 gram 34,7 ppm, dan kontrol 76,6 ppm. Konsentrasi CO dengan karbon aktif kulit durian 1 kg 41,56 ppm, 2 kg 30,89 ppm, dan kontrol 101,4 ppm. Rata-rata CO dengan gabungan semua adsorben adalah 22,9 ppm. Uji perbedaan konsentrasi CO pada berbagai jumlah kaktus nilai p= 0,001, jamur penicilium sp nilai p=0,001, dan uji kruskall wallis untuk karbon aktif kulit durian adalah 0,001.Simpulan: Ada perbedaan kemampuan adsorbsi dan absorbsi CO berdasarkan jumlah adsorben dan absorben. Jumlah kaktus terbaik adalah 4 batang, jamur Penicillium 300 gram, dan karbon aktif 2 kg. Konsentrasi CO dengan penggabungan semua adsorben dan absorben telah berada di bawah nilai ambang batas yang diperbolehkan yaitu 25 ppm.ABSTRACTTitle: The Effectiveness of Ornamental Plants, Fungi, and Activated Carbon in Reducing Carbon Monoxide Concentrations in the AirBackground: Cigarettes contain about 4000 elements and 200 of them are harmful to health. Exposure to cigarette smoke which is quite potential is CO. CO is a toxic gas and is one of the greenhouse gases that damage the earth's ozone layer. Exposure to cigarettes in the room is still widely found. Need to attempt to reduce CO in the air. Previous research concluded that the best type of adsorbent in lowering CO is cactus, Penicilliumsp, and durian skin activated carbon. The aim of this study isto know the difference in CO adsorption ability based on the number of adsorbents. Method: This research type is quasi-experimental with static group comparison design, the object is CO in the room, the variable is the amount of adsorbent, the type of adsorbent, the concentration of CO in the air. Data analysis used 1-way ANOVA test and Kruskalwallis test. Results: on average CO with cactus 1 stem 63 ppm, 2 stems 56 ppm, 3 stems is 46.6 ppm, 4 stems is 28 ppm, and control is 106.6 ppm. The average CO with Penicilliumsp 150 grams is 47.3 ppm, 300 grams is 34.7 ppm, and control is 76.6 ppm. The average CO with 1 kg durian skin activated carbon is 41.56 ppm, 2 kg is 30.89 ppm, and control is 101.4 ppm. The average CO with a combination of all adsorbents is 22.9 ppm. Test the difference in CO concentration in various cactus, pvalues = 0.001, Peniciliumsp p value = 0.001, and the Kruskal wallis test for activated carbon was 0.001. Conclusion: There are differences in CO adsorption and absorption based on the number of cactus, Peniciliium sp, and durian skin activated carbon. The best amount of cactus is 4 stems, 300 grams of Penicillium sp, and 2 kg of activated carbon. CO concentration with all of adsorbent and absorbents has been below the permissible threshold value of 25 ppm.
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28

Tsutaya, H., and J. lzumi. "Carbon monoxide adsorption by zeolite." Zeolites 11, no. 1 (January 1991): 90. http://dx.doi.org/10.1016/0144-2449(91)80386-e.

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29

Allouche, A. "Carbon monoxide adsorption on beryllium surfaces." Surface Science 608 (February 2013): 265–74. http://dx.doi.org/10.1016/j.susc.2012.10.018.

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30

Mohamad, A. B., S. E. Iyuke, W. R. W. Daud, A. A. H. Kadhum, Z. Fisal, M. F. Al-Khatib, and A. M. Shariff. "Adsorption of carbon monoxide on activated carbon–tin ligand." Journal of Molecular Structure 550-551 (September 2000): 511–19. http://dx.doi.org/10.1016/s0022-2860(00)00509-3.

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31

Kuznetsov, M. V., D. P. Frickel, E. V. Shalaeva, and N. I. Medvedeva. "Adsorption of carbon monoxide on Ti(0001)." Journal of Electron Spectroscopy and Related Phenomena 96, no. 1-3 (November 1998): 29–36. http://dx.doi.org/10.1016/s0368-2048(98)00219-9.

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32

Orozco, G., M. C. Pérez, A. Rincón, and C. Gutiérrez. "Adsorption and Electrooxidation of Carbon Monoxide on Silver." Langmuir 14, no. 21 (October 1998): 6297–306. http://dx.doi.org/10.1021/la980157t.

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33

De Haeck, Jorg, Nele Veldeman, Pieterjan Claes, Ewald Janssens, Mats Andersson, and Peter Lievens. "Carbon Monoxide Adsorption on Silver Doped Gold Clusters." Journal of Physical Chemistry A 115, no. 11 (March 24, 2011): 2103–9. http://dx.doi.org/10.1021/jp111257s.

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34

Larin, A. V. "Reversible adsorption of carbon monoxide on copper oxide." Langmuir 3, no. 3 (May 1987): 318–19. http://dx.doi.org/10.1021/la00075a005.

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35

Kuriyama, Takashi, Kimio Kunimori, Takashi Kuriyama, and Hisakazu Nozoye. "Adsorption of carbon monoxide on a SmOx film." Chemical Communications, no. 4 (1998): 501–2. http://dx.doi.org/10.1039/a707932j.

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36

Grillo, M. E., G. R. Castro, and G. Doyen. "Theory of carbon monoxide adsorption on NiAl(110)." Journal of Chemical Physics 97, no. 10 (November 15, 1992): 7786–96. http://dx.doi.org/10.1063/1.463447.

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37

Ghosh, A. C., S. Borthakur, and N. N. Dutta. "Absorption of carbon monoxide in hollow fiber membranes." Journal of Membrane Science 96, no. 3 (December 1994): 183–92. http://dx.doi.org/10.1016/0376-7388(94)00108-1.

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38

KORCZEWSKI, Zbigniew, Jacek RUDNICKI, and Ryszard ZADRĄG. "Laboratory station for research of the innovative dry method of exhaust gas desulfurization for an engine powered with residual fuel." Combustion Engines 168, no. 1 (February 1, 2017): 32–37. http://dx.doi.org/10.19206/ce-2017-105.

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Development of technology for exhaust gas desulfurization in marine engines using the dry method is, nowadays, a priority due to the calendar of introducing restrictions by the Directive of the European Parliament and of the Council 2012/33/EU of 21 November 2012. According to this directive, starting from 1 January 2015, inside the SECA (Sulphur Emission Control Area) the maximum sulfur content of marine fuels used on territorial seas is 0.1% per weight unit. But at the same time the directive allows for the use of exhaust gas desulfurization plant operating in a closed system. The ship equipped with the system will be able to use fuels with a high sulfur content, which will then be removed from the exhaust gas through an applied adsorber, and the reacted adsorbent is received by specialized services stationed in harbors. The International Maritime Organization has set a limit value of the emissions of sulfur oxides in exhaust gases of marine engines at 6 g/kWh (International Convention for the Prevention of Sea Pollution from Ships MARPOL 73/78 Annex VI, Regulation 14). Contemporary methods of exhaust gas desulfurization in marine engines are all expensive methods (4-5 million euro). This is, among other reasons, due to the limited market audience, but primarily due to the monop-olized position of manufacturers offering fabrication and assembly of this type of marine ship installations. Proposed as part of a research project financed by the Regional Fund for Environmental Protection and Maritime Economy in Gdansk, the dry method (adsorption) reducing SOx emissions in exhaust gases of marine engines, is an alternative, and a definitely cheaper and therefore competitive solution, compared to the wet methods (absorption), which are currently the most widely used in marine scrubber installations. Importantly, as confirmed by the results of the study, the proposed dry method, in addition to the effective reduction of sulfur oxides, also reduces emissions of nitrogen oxides and carbon monoxide. The paper presents the configuration and measurement capabilities of the test station built under the project, as well as the representative results of the investigations so far. During the exhaust gas desulfurization test a sodium adsorbent (sodium bicarbonate) and its modifications were used in the process of mechanical, chemical, and thermal activation. Two physicochemical processes were studied during the development of the method: • of adsorbent’s reaction on the chemical emission of the exhaust gas – the effectiveness of SOx and NOx compound removal, with various structural solutions in the process reactor, • the impact of the adsorber on the emission source of sulfur oxides, that is, on the compression-ignition engine. Therefore, one of the priorities of the project, with a utilitarian significance, was to determine the impact of the inclusion of the desulfurization installation in the exhaust gas system on the energy ratios of the engine.
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39

Tamon, Hajime, Kenji Kitamura, and Morio Okazaki. "Adsorption of carbon monoxide on activated carbon impregnated with metal halide." AIChE Journal 42, no. 2 (February 1996): 422–30. http://dx.doi.org/10.1002/aic.690420212.

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Kodi Pandyan, Ramalingam, Sonai Seenithurai, and Manickam Mahendran. "Carbon monoxide adsorption on transition element-doped single wall carbon nanotube." Indian Journal of Physics 86, no. 8 (June 28, 2012): 677–80. http://dx.doi.org/10.1007/s12648-012-0117-z.

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Wen-Xiang, Wang, Xu Jie, and He Guang-Xin. "Determination for Adsorption Heat of Carbon Monoxide on Copper." Acta Physico-Chimica Sinica 6, no. 02 (1990): 252–56. http://dx.doi.org/10.3866/pku.whxb19900223.

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Gottfried, J. M., K. J. Schmidt, S. L. M. Schroeder, and K. Christmann. "Adsorption of carbon monoxide on Au(110)-(1×2)." Surface Science 536, no. 1-3 (June 2003): 206–24. http://dx.doi.org/10.1016/s0039-6028(03)00595-8.

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Ning, Hua, Zhi-Qiang Lan, Jin Guo, and Ming-Qiu Tan. "Carbon-monoxide adsorption and dissociation on Nb(110) surface." Applied Surface Science 328 (February 2015): 641–48. http://dx.doi.org/10.1016/j.apsusc.2014.12.088.

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Bates, Simon, and John Dwyer. "Ab initio study of carbon monoxide adsorption on zeolites." Journal of Physical Chemistry 97, no. 22 (June 1993): 5897–900. http://dx.doi.org/10.1021/j100124a020.

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Gallaba, Dinuka H., Jhonny Villarroel-Rocha, Karim Sapag, and Aldo D. Migone. "Carbon monoxide adsorption in ZIF-8: Kinetics and equilibrium." Microporous and Mesoporous Materials 265 (July 2018): 227–33. http://dx.doi.org/10.1016/j.micromeso.2018.02.020.

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Mucalo, M. R., and R. P. Cooney. "Infrared studies of carbon monoxide adsorption on rhodium hydrosols." Chemistry of Materials 3, no. 6 (November 1991): 1081–87. http://dx.doi.org/10.1021/cm00018a025.

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Ruggiero, Carmine, and Peter Hollins. "Adsorption of carbon monoxide on the gold(332) surface." Journal of the Chemical Society, Faraday Transactions 92, no. 23 (1996): 4829. http://dx.doi.org/10.1039/ft9969204829.

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Veldeman, N., P. Lievens, and M. Andersson. "Size-Dependent Carbon Monoxide Adsorption on Neutral Gold Clusters." Journal of Physical Chemistry A 109, no. 51 (December 2005): 11793–801. http://dx.doi.org/10.1021/jp0556097.

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Gotterbarm, Karin, Carina Bronnbauer, Udo Bauer, Christian Papp, and Hans-Peter Steinrück. "Graphene-Supported Pd Nanoclusters Probed by Carbon Monoxide Adsorption." Journal of Physical Chemistry C 118, no. 43 (October 21, 2014): 25097–103. http://dx.doi.org/10.1021/jp508454h.

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50

Vishnevskii, A. L., and V. I. Savchenko. "Adsorption of carbon monoxide and oxygen on Pt(110)." Reaction Kinetics and Catalysis Letters 38, no. 1 (March 1989): 159–66. http://dx.doi.org/10.1007/bf02126269.

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