Research on Catalytic Cracking Performance Improvement of Waste FCC Catalyst by Magnesium Modification
In this study, the deactivation mechanism caused by high accessibility of strong acid sites for the waste FCC catalyst was proposed and verified for the first time. Based on the proposed deactivation mechanism, magnesium modification through magnesium chloride impregnation was employed for the regen...
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Veröffentlicht in: | 中国炼油与石油化工(英文版) 2018-06, Vol.20 (2), p.48-55 |
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creator | Yuan Chengyuan Tan Zhengguo Pan Zhishuang Zhang Haitao Gao Xionghou |
description | In this study, the deactivation mechanism caused by high accessibility of strong acid sites for the waste FCC catalyst was proposed and verified for the first time. Based on the proposed deactivation mechanism, magnesium modification through magnesium chloride impregnation was employed for the regeneration of waste FCC catalyst. The regenerated waste FCC catalyst was characterized, with its heavy oil catalytic cracking performance tested. The characterization results indicated that, in comparison with the unmodified waste FCC catalyst, the acid sites strength of the regenerated waste FCC catalyst was weakened, with no prominent alterations of the total acid sites quantity and textural properties. The heavy oil catalytic cracking results suggested that the catalytic cracking performance of the regenerated waste FCC catalyst was greatly improved due to the suitable surface acidity of the sample. In contrast with the unmodified waste FCC catalyst, the gasoline yield over the regenerated waste FCC catalyst significantly increased by 3.04 percentage points, meanwhile the yield of dry gas, LPG, coke and bottoms obviously decreased by 0.36, 0.81, 1.28 and 0.87 percentage points, respectively, making the regenerated waste FCC catalyst serve as a partial substitute for the fresh FCC catalyst. Finally, the acid property change mechanism was discussed. |
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Based on the proposed deactivation mechanism, magnesium modification through magnesium chloride impregnation was employed for the regeneration of waste FCC catalyst. The regenerated waste FCC catalyst was characterized, with its heavy oil catalytic cracking performance tested. The characterization results indicated that, in comparison with the unmodified waste FCC catalyst, the acid sites strength of the regenerated waste FCC catalyst was weakened, with no prominent alterations of the total acid sites quantity and textural properties. The heavy oil catalytic cracking results suggested that the catalytic cracking performance of the regenerated waste FCC catalyst was greatly improved due to the suitable surface acidity of the sample. In contrast with the unmodified waste FCC catalyst, the gasoline yield over the regenerated waste FCC catalyst significantly increased by 3.04 percentage points, meanwhile the yield of dry gas, LPG, coke and bottoms obviously decreased by 0.36, 0.81, 1.28 and 0.87 percentage points, respectively, making the regenerated waste FCC catalyst serve as a partial substitute for the fresh FCC catalyst. Finally, the acid property change mechanism was discussed.</description><identifier>ISSN: 1008-6234</identifier><language>eng</language><publisher>Lanzhou Petrochemical Research Center, Petrochemical Research Institute, PetroChina, Lanzhou 730060</publisher><ispartof>中国炼油与石油化工(英文版), 2018-06, Vol.20 (2), p.48-55</ispartof><rights>Copyright © Wanfang Data Co. Ltd. All Rights Reserved.</rights><woscitedreferencessubscribed>false</woscitedreferencessubscribed></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Uhttp://www.wanfangdata.com.cn/images/PeriodicalImages/zgsyjgysyhgjs/zgsyjgysyhgjs.jpg</thumbnail><link.rule.ids>314,776,780</link.rule.ids></links><search><creatorcontrib>Yuan Chengyuan</creatorcontrib><creatorcontrib>Tan Zhengguo</creatorcontrib><creatorcontrib>Pan Zhishuang</creatorcontrib><creatorcontrib>Zhang Haitao</creatorcontrib><creatorcontrib>Gao Xionghou</creatorcontrib><title>Research on Catalytic Cracking Performance Improvement of Waste FCC Catalyst by Magnesium Modification</title><title>中国炼油与石油化工(英文版)</title><description>In this study, the deactivation mechanism caused by high accessibility of strong acid sites for the waste FCC catalyst was proposed and verified for the first time. Based on the proposed deactivation mechanism, magnesium modification through magnesium chloride impregnation was employed for the regeneration of waste FCC catalyst. The regenerated waste FCC catalyst was characterized, with its heavy oil catalytic cracking performance tested. The characterization results indicated that, in comparison with the unmodified waste FCC catalyst, the acid sites strength of the regenerated waste FCC catalyst was weakened, with no prominent alterations of the total acid sites quantity and textural properties. The heavy oil catalytic cracking results suggested that the catalytic cracking performance of the regenerated waste FCC catalyst was greatly improved due to the suitable surface acidity of the sample. In contrast with the unmodified waste FCC catalyst, the gasoline yield over the regenerated waste FCC catalyst significantly increased by 3.04 percentage points, meanwhile the yield of dry gas, LPG, coke and bottoms obviously decreased by 0.36, 0.81, 1.28 and 0.87 percentage points, respectively, making the regenerated waste FCC catalyst serve as a partial substitute for the fresh FCC catalyst. 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Based on the proposed deactivation mechanism, magnesium modification through magnesium chloride impregnation was employed for the regeneration of waste FCC catalyst. The regenerated waste FCC catalyst was characterized, with its heavy oil catalytic cracking performance tested. The characterization results indicated that, in comparison with the unmodified waste FCC catalyst, the acid sites strength of the regenerated waste FCC catalyst was weakened, with no prominent alterations of the total acid sites quantity and textural properties. The heavy oil catalytic cracking results suggested that the catalytic cracking performance of the regenerated waste FCC catalyst was greatly improved due to the suitable surface acidity of the sample. In contrast with the unmodified waste FCC catalyst, the gasoline yield over the regenerated waste FCC catalyst significantly increased by 3.04 percentage points, meanwhile the yield of dry gas, LPG, coke and bottoms obviously decreased by 0.36, 0.81, 1.28 and 0.87 percentage points, respectively, making the regenerated waste FCC catalyst serve as a partial substitute for the fresh FCC catalyst. Finally, the acid property change mechanism was discussed.</abstract><pub>Lanzhou Petrochemical Research Center, Petrochemical Research Institute, PetroChina, Lanzhou 730060</pub><tpages>8</tpages></addata></record> |
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title | Research on Catalytic Cracking Performance Improvement of Waste FCC Catalyst by Magnesium Modification |
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