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Flow reactor experiments on the selective non-catalytic removal of nitrogen oxides
dc.creator | Gentemann, Alexander M.G. | |
dc.date.accessioned | 2012-06-07T23:04:28Z | |
dc.date.available | 2012-06-07T23:04:28Z | |
dc.date.created | 2001 | |
dc.date.issued | 2001 | |
dc.identifier.uri | https://hdl.handle.net/1969.1/ETD-TAMU-2001-THESIS-G46 | |
dc.description | Due to the character of the original source materials and the nature of batch digitization, quality control issues may be present in this document. Please report any quality issues you encounter to digital@library.tamu.edu, referencing the URI of the item. | en |
dc.description | Includes bibliographical references (leaves 251-261). | en |
dc.description | Issued also on microfiche from Lange Micrographics. | en |
dc.description.abstract | Three flow reactor studies, using an electrically heated laminar flow reactor, were performed at 1 atm pressure and various temperatures. To establish inert conditions inside the reactor, a quartz tube was used. The experiments were conducted with the use of a Fourier transform infrared (FT-IR) spectrometer to obtain both a complete qualitative and quantitative analysis of the reaction products. A urea/water solution was tested in a decomposition study in a temperature range between 800 and 1300 K. The solution was preheated to the vaporization temperature of the water and injected into pure nitrogen or into nitrogen/oxygen mixtures with 1, 10, or 15% oxygen. The study showed ammonia, HNCO and CO₂ as the major decomposition products; and N₂O and NO were also found. Selective non-catalytic removal of nitric oxide using a water/urea solution was performed in a temperature range between 800 and 1300 K. Different combinations of simulated exhaust gas were tested, which contained various fractions of O₂ and CO. NO removal up to 98% was observed. Oxygen and CO were necessary to obtain such results. N₂O was observed to be a product species at 1000 to 1200 K. Selective non-catalytic removal of nitrogen dioxide using ammonia was performed in a temperature range between 800 and 1300 K. Different combinations of simulated exhaust gas were tested, which contained various fractions of O₂ and CO. NO₂ removal could be observed for temperatures above 1050 K, where conversion to NO took place followed by the removal of NO. N₂O was a by-product of the process found between 1000 and 1300 K with CO and O₂ present. The results for urea decomposition as well as the removal study of NO₂ have not been reported in the literature before. A study on the complete products of NO removal using urea was also conducted for the first time with such a wide range of gas compositions. | en |
dc.format.medium | electronic | en |
dc.format.mimetype | application/pdf | |
dc.language.iso | en_US | |
dc.publisher | Texas A&M University | |
dc.rights | This thesis was part of a retrospective digitization project authorized by the Texas A&M University Libraries in 2008. Copyright remains vested with the author(s). It is the user's responsibility to secure permission from the copyright holder(s) for re-use of the work beyond the provision of Fair Use. | en |
dc.subject | mechanical engineering. | en |
dc.subject | Major mechanical engineering. | en |
dc.title | Flow reactor experiments on the selective non-catalytic removal of nitrogen oxides | en |
dc.type | Thesis | en |
thesis.degree.discipline | mechanical engineering | en |
thesis.degree.name | M.S. | en |
thesis.degree.level | Masters | en |
dc.type.genre | thesis | en |
dc.type.material | text | en |
dc.format.digitalOrigin | reformatted digital | en |
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