http://rdf.ncbi.nlm.nih.gov/pubchem/patent/KR-20080096675-A

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filingDate 2006-01-24-04:00^^<http://www.w3.org/2001/XMLSchema#date>
inventor http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_ecd11ed1e4665df09c24cb5456bcc8a8
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publicationDate 2008-10-31-04:00^^<http://www.w3.org/2001/XMLSchema#date>
publicationNumber KR-20080096675-A
titleOfInvention Selective conversion of oxygenates to propylene using mobile bed technology and hydrothermally stabilized bifunctional catalyst system
abstract The average propylene cycle selectivity of the oxygenate to propylene (OTP) process using a bifunctional oxygenate conversion catalyst is characterized by (1) mobile phase reactor technology in the hydrocarbon synthesis portion of the OTP flow process, replacing the prior art fixed bed technology; (2) a hydrothermally stabilized bifunctional catalyst system containing molecular sieves dispersed in a phosphorus modified alumina matrix that retains bifunctional capability and contains labile phosphorus and / or aluminum anions; And (3) a combination of up to 400 hours of catalyst on-stream cycle time. These conditions stabilize the catalyst against hydrothermal inactivation and maintain the accumulation of coke deposits on the catalyst to a degree that does not substantially reduce bifunctional catalytic activity, oxygenate conversion and propylene selectivity, thereby substantially cycle initiating average propylene cycle yields. Level or close thereto.
isCitedBy http://rdf.ncbi.nlm.nih.gov/pubchem/patent/WO-2014178543-A1
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-110475604-A
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