{"title":"INVESTIGATION OF THE GAS MIXTURE ADSORPTION PROCESS IN A\nFIXED LAYER OF THE NaX ADSORBENT","authors":"A. Bayramova","doi":"10.32010/ajcn03032021-38","DOIUrl":null,"url":null,"abstract":"The paper describes a 4-adsorbent installation for cleaning gas mixtures from H2S, CO2\nand NO2 with zeolite. The lower and upper limits of the condensate level in the\nseparator were controlled by electric contact pressure gauges, and the pressure was\nrecorded on the operator panel. The number of adsorbers is 4, the height of the fixed\nzeolite layer is 3.6 m. Long-term operation of the adsorption unit under real operating\nconditions has shown that the temperature of zeolite regeneration largely depends on\nthe quality of the gas entering the adsorption unit. As can be seen, the desorption of\ncarbon dioxide is completed at the beginning, then hydrogen sulfide, and at the end -\nmoisture vapor, and the time for complete desorption of all adsorbed components is\nlimited by internal diffusion inhibition of the sorbed components. The greatest\ndesorption time, as expected, is due to moisture vapors. It has been experimentally\nestablished that when heated with hot gas at the maximum permissible speed, the time\nfor complete desorption of moisture is 150-160 minutes. For practical calculations, the\ntime required for complete dehydration of the zeolite is taken at least 3 hours, which is\nconfirmed experimentally.\nKeywords: adsorption, synthetic zeolite NaX, fixed adsorbent layer, gas mixture,\ndesorbed substances.","PeriodicalId":245302,"journal":{"name":"Azerbaijan Journal of Chemical News","volume":"185 S497","pages":"0"},"PeriodicalIF":0.0000,"publicationDate":"2021-01-07","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Azerbaijan Journal of Chemical News","FirstCategoryId":"1085","ListUrlMain":"https://doi.org/10.32010/ajcn03032021-38","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"","JCRName":"","Score":null,"Total":0}
引用次数: 0
Abstract
The paper describes a 4-adsorbent installation for cleaning gas mixtures from H2S, CO2
and NO2 with zeolite. The lower and upper limits of the condensate level in the
separator were controlled by electric contact pressure gauges, and the pressure was
recorded on the operator panel. The number of adsorbers is 4, the height of the fixed
zeolite layer is 3.6 m. Long-term operation of the adsorption unit under real operating
conditions has shown that the temperature of zeolite regeneration largely depends on
the quality of the gas entering the adsorption unit. As can be seen, the desorption of
carbon dioxide is completed at the beginning, then hydrogen sulfide, and at the end -
moisture vapor, and the time for complete desorption of all adsorbed components is
limited by internal diffusion inhibition of the sorbed components. The greatest
desorption time, as expected, is due to moisture vapors. It has been experimentally
established that when heated with hot gas at the maximum permissible speed, the time
for complete desorption of moisture is 150-160 minutes. For practical calculations, the
time required for complete dehydration of the zeolite is taken at least 3 hours, which is
confirmed experimentally.
Keywords: adsorption, synthetic zeolite NaX, fixed adsorbent layer, gas mixture,
desorbed substances.