全部 标题 作者
关键词 摘要

OALib Journal期刊
ISSN: 2333-9721
费用:99美元

查看量下载量

相关文章

更多...

大孔fcc催化剂的制备及裂化性能研究

, PP. 1092-1097

Keywords: 聚苯乙烯,脱油残渣,大孔,重油,fcc催化剂

Full-Text   Cite this paper   Add to My Lib

Abstract:

?利用聚苯乙烯(ps)颗粒和脱油残渣(vr)乳液为模板剂制备了大孔重油催化裂化催化剂,与未加模板的参比催化剂相比,比表面积分别增加了38.0%和46.2%,孔体积分别增加了20.6%和35.8%,平均孔径分别增加了54.5%和27.3%。微反评价结果表明,大孔催化剂活性较高,对重油的转化率分别提高了9.8%和12.2%,总液收分别提高了10.2%和7.3%。与参比催化剂相比,积炭后ps颗粒和vr乳液模板大孔催化剂的活性有一定程度的降低,但是当积炭量相同时,大孔催化剂的重油转化率和总液体产物收率都比参比催化剂要高,且两类大孔催化剂的数据比较接近。催化剂的基质经模板扩孔后,由于具有微孔-介孔-大孔的梯度孔分布,孔径分布更加合理,重油分子在催化剂孔道内的扩散速率更快,容炭能力更强,所以大孔催化剂具有较好的裂化性能。

References

[1]  庞新梅,孙书红,赵连鸿,丁伟.一种催化裂化催化剂及其制备方法:中国,cn02103907.2002-02-07.(pangxin-mei,sunshu-hong,zhaolian-hong,dingwei.anewfcccatalystanditspreparationmethod:cn,02103907.2002-02-07.)
[2]  祁彦平,陈胜利,董鹏,徐克琪,申宝剑.新型孔结构渣油催化裂化催化剂[j].燃料化学学报,2006,34(6):685-689.(qiyan-ping,chensheng-li,dongpeng,xuke-qi,shenbao-jian.novelmacroporousresiduafcccatalysts[j].journaloffuelchemistryandtechnology,2006,34(6):685-689.)
[3]  陈胜利,董鹏,祁彦平,徐克琪.重质油加工大孔催化裂化催化剂合成方法:中国,200510082624.2005-07-06.(chensheng-li,dongpeng,qiyan-ping,xuke-qi.preparationmethodofmacroporousfcccatalystforheavyoilprocessing:cn,200510082624.2005-07-06.)
[4]  王仁安,胡云翔,许志明,苏桐.超临界流体萃取分馏法分离石油重质油[j].石油学报(石油加工),1997,13(1):53-59.(wangren-an,huyun-xiang,xuzhi-ming,sutong.anewfractionatingmethodforheavyoilofpetroleumbysupercriticalfluidextractionandfractionation[j].actapetroleisinica(petroleumprocessingsection),1997,13(1):53-59.)
[5]  徐克琪.新型重油催化裂化催化剂的研究[m].北京:中国石油大学,2006.(xuke-qi.researchonnovelresiduafcccatalysts[m].beijing:chinauniversityofpetroleum,2006.)
[6]  朱洪法.催化剂载体制备及应用技术[m].北京:石油工业出版社,2002:66-67.(zhuhong-fa.preparationandapplicationtechnologyofcatalystsupport[m].beijing:petroleumindustrypress,2002:66-67.)
[7]  魏晓丽,王巍,张久顺.催化裂化汽油在催化剂上裂化生焦的研究[j].石油炼制与化工,2003,34(6):5-9.(weixiao-li,wangwei,zhangjiu-shun.studyofcokeformationoncatalystsduringfccnaphthacracking[j].petroleumprocessingandpetrochemicals,2003,34(6):5-9.)
[8]  maitysk,ancheytaj,soberanisl,alonsof,llanosme.alumina-titaniabinarymixedoxideusedassupportofcatalystsforhydrotreatingofmayaheavycrude[j].applcatala,2003,244(1):141-153.
[9]  chensl,dongp,xuk,qiy,wangd.largeporeheavyoilprocessingcatalystspreparedusingcolloidalparticlesastemplates[j].cataltoday,2007,125(3/4):143-148.
[10]  qiy-p,chens-l,dongp,xuk-q,shenb-j.novelmacroporousresiduafcccatalysts[j].jfuelchemtechnol,2006,34(6):685-689.
[11]  朱华元,何鸣元,宋家庆,张庆.催化剂的大分子裂化性能与渣油裂化[j].炼油设计,2000,30(8):47-51.(zhuhua-yuan,heming-yuan,songjia-qing,zhangqing.residecrackingandbulkymoleculecrackingabilitiesofrfcccatalysts[j].petroleumrefineryengineering,2000,30(8):47-51.)
[12]  liuz,chens,gex,dongp,gaoj,xuz.measurementofdiffusioncoefficientofheavyoilinfcccatalysts[j].energyfuels,2010,24(5):2825-2829.
[13]  wolfeh,alfania.catalystdeactivationbycoking[j].catalrevscieng,1982,24(3),329-371.
[14]  lamyl,santosads,roncolattoreetal.crackingcatalystcomposition:us,us20020165083a1.2002-11-07.

Full-Text

Contact Us

service@oalib.com

QQ:3279437679

WhatsApp +8615387084133