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Enhancing the Ethylene and Propylene Selectivities in the Methanol-to-Olefins Reaction by Exploiting the Intricate Relationship Between Framework Topology and Acidity
Enhancing the Ethylene and Propylene Selectivities in the Methanol-to-Olefins Reaction by ...
Enhancing the Ethylene and Propylene Selectivities in the Methanol-to-Olefins Reaction by Exploiting the Intricate Relationship Between Framework Topology and Acidity

상세정보

자료유형  
 학위논문 서양
최종처리일시  
20260202103651
ISBN  
9798290626024
DDC  
547.3
저자명  
Alshafei, Faisal H.
서명/저자  
Enhancing the Ethylene and Propylene Selectivities in the Methanol-to-Olefins Reaction by Exploiting the Intricate Relationship Between Framework Topology and Acidity
발행사항  
[Sl] : California Institute of Technology, 2023
발행사항  
Ann Arbor : ProQuest Dissertations & Theses, 2023
형태사항  
349 p
주기사항  
Source: Dissertations Abstracts International, Volume: 87-03, Section: B.
주기사항  
Advisor: Davis, Mark E.
학위논문주기  
Thesis (Ph.D.)--California Institute of Technology, 2023.
초록/해제  
요약This thesis describes and presents results from several related projects within the theme of molecular sieve synthesis and catalysis. The early part of the thesis focuses on understanding the link between cage size/dimension and acidity (i.e., acid site density and strength) in the methanol-to-olefins (MTO) reaction. This relationship between cage size and acidity, once identified and investigated, is exploited in the latter parts of the thesis to rationally design materials that are able to steer the light olefins product distribution toward either more ethylene or propylene in a significant improvement over SAPO-34 (CHA), the commercial catalyst.In Chapters 2, 44 zeolites and silicoaluminophosphates (SAPOs) belonging to five frameworks (AEI, CHE, LEV, SWY, and ERI) with a wide range of Si/Al=4-31 and Si/(Al+P)=0.04-0.3, are synthesized and characterized using a myriad of techniques. Their MTO behavior is then systematically investigated to rationalize the effect of cage dimensions on the olefins product distribution as a function of acid site density and strength. The results from this study show that changes in acid site density and strength play a secondary role to the dominating influence of cage architecture on product distribution in AEI- and CHA-type molecular sieves. Decreasing the cage size, in going from AEI and CHA to LEV, SWY, and ERI, however, results in substantial changes in the ethylene-to-propylene ratio (E/P) as a function of acidity. These changes are attributed to differences in the identity and concentration of the hydrocarbon-pool (HP) species that form, particularly in early stages of the reaction.In Chapters 3 and 4, ERI-type molecular sieves (e.g., SSZ-98, UZM-12, ERI-type zeolites, and SAPO-17) are thoroughly investigated as promising methanol-to-ethylene materials due to their narrow cage size. Specifically, numerous ERI-type molecular sieves are synthesized using several organic structure-directing agents (OSDAs) with varied Si/Al or Si/T-atoms ratios. The list of ERI-related materials synthesized and tested in MTO included a new disordered SAPO, denoted as CIT-16P, which upon thermal treatment in air transforms to SAPO-17 (ERI). The reaction results show that decreasing the Si/Al (or increasing the Si/T) ratio, irrespective of other material properties, improves the E/P of ERI-type molecular sieves (E/P=1.1-1.9) over CHA-type molecular sieves (E/P=0.82-0.85) in MTO. Dissolution-extraction experiments reveal that the rapid formation of cyclic intermediates and the shift in their composition toward less-methylated methylbenzenes and methylnaphthalenes are found to be key to enhancing the ethylene selectivity in ERI-type molecular sieves.In Chapter 5, several SAT-type molecular sieves are investigated as promising methanol-to-propylene catalysts. This effort entails the synthesis of CIT-17, an SAT SAPO-type molecular sieve, which is isostructural to STA-2 (MgAPO-SAT). Following the successful synthesis of CIT-17, the MTO behavior of several SAT-type molecular sieves (MgAPO, CoAPO, and SAPO) are investigated in MTO. The combination of low acidity of CIT-17 and unique structural features of the narrow SAT-cage lead to a catalytic pathway and mechanism that predominantly favors propylene (propylene-to-ethylene ratios (P/E) of 2-4.2; propylene selectivity of 40-50%). Indeed, CIT-17 achieves one of the highest P/E ratio values reported for this class of materials.
일반주제명  
Hydrocarbons
일반주제명  
Spectrum analysis
일반주제명  
Catalysis
일반주제명  
Zeolites
일반주제명  
Adsorption
일반주제명  
Dehydration
일반주제명  
Computational chemistry
일반주제명  
Molecular chemistry
키워드  
Methanol-to-olefins
키워드  
Hydrocarbon-pool
키워드  
Ethylene
기타저자  
California Institute of Technology Chemistry and Chemical Engineering
기본자료저록  
Dissertations Abstracts International. 87-03B.
전자적 위치 및 접속  
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MARC

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■020    ▼a9798290626024
■035    ▼a(MiAaPQ)AAI32098744
■035    ▼a(MiAaPQ)Caltech15139
■040    ▼aMiAaPQ▼cMiAaPQ
■0820  ▼a547.3
■1001  ▼aAlshafei,  Faisal  H.
■24510▼aEnhancing  the  Ethylene  and  Propylene  Selectivities  in  the  Methanol-to-Olefins  Reaction  by  Exploiting  the  Intricate  Relationship  Between  Framework  Topology  and  Acidity
■260    ▼a[Sl]▼bCalifornia  Institute  of  Technology▼c2023
■260  1▼aAnn  Arbor▼bProQuest  Dissertations  &  Theses▼c2023
■300    ▼a349  p
■500    ▼aSource:  Dissertations  Abstracts  International,  Volume:  87-03,  Section:  B.
■500    ▼aAdvisor:  Davis,  Mark  E.
■5021  ▼aThesis  (Ph.D.)--California  Institute  of  Technology,  2023.
■520    ▼aThis  thesis  describes  and  presents  results  from  several  related  projects  within  the  theme  of  molecular  sieve  synthesis  and  catalysis.  The  early  part  of  the  thesis  focuses  on  understanding  the  link  between  cage  size/dimension  and  acidity  (i.e.,  acid  site  density  and  strength)  in  the  methanol-to-olefins  (MTO)  reaction.  This  relationship  between  cage  size  and  acidity,  once  identified  and  investigated,  is  exploited  in  the  latter  parts  of  the  thesis  to  rationally  design  materials  that  are  able  to  steer  the  light  olefins  product  distribution  toward  either  more  ethylene  or  propylene  in  a  significant  improvement  over  SAPO-34  (CHA),  the  commercial  catalyst.In  Chapters  2,  44  zeolites  and  silicoaluminophosphates  (SAPOs)  belonging  to  five  frameworks  (AEI,  CHE,  LEV,  SWY,  and  ERI)  with  a  wide  range  of  Si/Al=4-31  and  Si/(Al+P)=0.04-0.3,  are  synthesized  and  characterized  using  a  myriad  of  techniques.  Their  MTO  behavior  is  then  systematically  investigated  to  rationalize  the  effect  of  cage  dimensions  on  the  olefins  product  distribution  as  a  function  of  acid  site  density  and  strength.  The  results  from  this  study  show  that  changes  in  acid  site  density  and  strength  play  a  secondary  role  to  the  dominating  influence  of  cage  architecture  on  product  distribution  in  AEI-  and  CHA-type  molecular  sieves.  Decreasing  the  cage  size,  in  going  from  AEI  and  CHA  to  LEV,  SWY,  and  ERI,  however,  results  in  substantial  changes  in  the  ethylene-to-propylene  ratio  (E/P)  as  a  function  of  acidity.  These  changes  are  attributed  to  differences  in  the  identity  and  concentration  of  the  hydrocarbon-pool  (HP)  species  that  form,  particularly  in  early  stages  of  the  reaction.In  Chapters  3  and  4,  ERI-type  molecular  sieves  (e.g.,  SSZ-98,  UZM-12,  ERI-type  zeolites,  and  SAPO-17)  are  thoroughly  investigated  as  promising  methanol-to-ethylene  materials  due  to  their  narrow  cage  size.  Specifically,  numerous  ERI-type  molecular  sieves  are  synthesized  using  several  organic  structure-directing  agents  (OSDAs)  with  varied  Si/Al  or  Si/T-atoms  ratios.  The  list  of  ERI-related  materials  synthesized  and  tested  in  MTO  included  a  new  disordered  SAPO,  denoted  as  CIT-16P,  which  upon  thermal  treatment  in  air  transforms  to  SAPO-17  (ERI).  The  reaction  results  show  that  decreasing  the  Si/Al  (or  increasing  the  Si/T)  ratio,  irrespective  of  other  material  properties,  improves  the  E/P  of  ERI-type  molecular  sieves  (E/P=1.1-1.9)  over  CHA-type  molecular  sieves  (E/P=0.82-0.85)  in  MTO.  Dissolution-extraction  experiments  reveal  that  the  rapid  formation  of  cyclic  intermediates  and  the  shift  in  their  composition  toward  less-methylated  methylbenzenes  and  methylnaphthalenes  are  found  to  be  key  to  enhancing  the  ethylene  selectivity  in  ERI-type  molecular  sieves.In  Chapter  5,  several  SAT-type  molecular  sieves  are  investigated  as  promising  methanol-to-propylene  catalysts.  This  effort  entails  the  synthesis  of  CIT-17,  an  SAT  SAPO-type  molecular  sieve,  which  is  isostructural  to  STA-2  (MgAPO-SAT).  Following  the  successful  synthesis  of  CIT-17,  the  MTO  behavior  of  several  SAT-type  molecular  sieves  (MgAPO,  CoAPO,  and  SAPO)  are  investigated  in  MTO.  The  combination  of  low  acidity  of  CIT-17  and  unique  structural  features  of  the  narrow  SAT-cage  lead  to  a  catalytic  pathway  and  mechanism  that  predominantly  favors  propylene  (propylene-to-ethylene  ratios  (P/E)  of  2-4.2;  propylene  selectivity  of  40-50%).  Indeed,  CIT-17  achieves  one  of  the  highest  P/E  ratio  values  reported  for  this  class  of  materials.
■590    ▼aSchool  code:  0037.
■650  4▼aHydrocarbons
■650  4▼aSpectrum  analysis
■650  4▼aCatalysis
■650  4▼aZeolites
■650  4▼aAdsorption
■650  4▼aDehydration
■650  4▼aComputational  chemistry
■650  4▼aMolecular  chemistry
■653    ▼aMethanol-to-olefins
■653    ▼aHydrocarbon-pool
■653    ▼aEthylene
■690    ▼a0431
■690    ▼a0219
■71020▼aCalifornia  Institute  of  Technology▼bChemistry  and  Chemical  Engineering.
■7730  ▼tDissertations  Abstracts  International▼g87-03B.
■790    ▼a0037
■791    ▼aPh.D.
■792    ▼a2023
■793    ▼aEnglish
■85640▼uhttp://www.riss.kr/pdu/ddodLink.do?id=T17358153▼nKERIS▼z이  자료의  원문은  한국교육학술정보원에서  제공합니다.

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