Mono- and bimetallic catalytic hollow-fiber reactors for the selective hydrogenation of butadiene in 1-butene
Identifieur interne : 001144 ( Istex/Corpus ); précédent : 001143; suivant : 001145Mono- and bimetallic catalytic hollow-fiber reactors for the selective hydrogenation of butadiene in 1-butene
Auteurs : Chunqing Liu ; Yun Xu ; Shijian Liao ; Daorong YuSource :
- Applied Catalysis A: General [ 0926-860X ] ; 1998.
English descriptors
- Teeft :
- Bers, Bimetallic, Bimetallic catalyst, Butadiene, Butadiene decreases, Butane, Butane butadiene, Catal, Catalysis, Catalyst, Catalytic, Chem, Crude feed, Hydrogenation, Inner side, Isomerization, Liao, Mild conditions, Monometallic, Nabh4, Outer side, Palladium, Partial pressure, Reaction conditions, Reactor, Remarkable synergic effect, Selective hydrogenation, Synergic.
Abstract
Abstract: The monometallic catalytic membrane reactors were established with catalytic hollow fibers prepared by supporting the polymer-anchored monometallic palladium catalyst (PVP-Pd, EC-Pd or AR-Pd) on the inside wall of CA or PSF hollow fibers. PVP=poly(N-vinyl-2-pyrrolidone), EC=ethyl cellulose, AR=melamine-formaldehyde resin, CA=Cellulose acetate, PSF=polysulfone. The selective hydrogenation of butadiene in crude 1-butene was carried out in the catalytic membrane reactors at 40°C under 0.1MPa. Among the above catalytic hollow fibers, the catalytic activity and selectivity of the PVP-Pd/CA monometallic hollow fiber were the best values, but there was still 2.6% 2-butene in the product. In order to inhibit the isomerization reaction of 1-butene, the bimetallic catalytic CA hollow-fiber reactors were produced and used for the above reaction. The bimetallic palladium–cobalt catalyst PVP-PdCl2–0.5Co(OAc)2, supported on the CA hollow fibers was reduced by NH2NH2 or NaBH4. A remarkable synergic effect of palladium and cobalt reduced by NaBH4 was observed.
Url:
DOI: 10.1016/S0926-860X(98)00095-7
Links to Exploration step
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<front><div type="abstract" xml:lang="en">Abstract: The monometallic catalytic membrane reactors were established with catalytic hollow fibers prepared by supporting the polymer-anchored monometallic palladium catalyst (PVP-Pd, EC-Pd or AR-Pd) on the inside wall of CA or PSF hollow fibers. PVP=poly(N-vinyl-2-pyrrolidone), EC=ethyl cellulose, AR=melamine-formaldehyde resin, CA=Cellulose acetate, PSF=polysulfone. The selective hydrogenation of butadiene in crude 1-butene was carried out in the catalytic membrane reactors at 40°C under 0.1MPa. Among the above catalytic hollow fibers, the catalytic activity and selectivity of the PVP-Pd/CA monometallic hollow fiber were the best values, but there was still 2.6% 2-butene in the product. In order to inhibit the isomerization reaction of 1-butene, the bimetallic catalytic CA hollow-fiber reactors were produced and used for the above reaction. The bimetallic palladium–cobalt catalyst PVP-PdCl2–0.5Co(OAc)2, supported on the CA hollow fibers was reduced by NH2NH2 or NaBH4. A remarkable synergic effect of palladium and cobalt reduced by NaBH4 was observed.</div>
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<note type="content">Fig. 1: Structure of the catalytic CA hollow-fiber reactor: (a) H2+N2 feed inlet; (2) crude 1-butene feed inlet; (3) product outlet; (4) tail gas outlet; (5),(6) circulating water, inlet and outlet; (7) glass jacket; (8) catalytic CA hollow fibers; (9) expoxide resin seal.</note>
<note type="content">Fig. 2: Schematic flow diagram of the selective hydrogenation of butadiene in curde 1-butene in a catalytic polymeric hollow-fiber reactor: (1) crude 1-butene feed; (2) H2+N2; (3),(4) preheaters; (5),(6) rotameters; (7) membrane reactor; (8),(9) needle valves; (10),(11) sampling ports.</note>
<note type="content">Table 1: Details of the catalytic CA hollow-fiber reactors</note>
<note type="content">Table 2: Selective hydrogenation of butadiene in 1-butene in different monometallic catalytic hollow-fiber reactors</note>
<note type="content">Table 3: Selective hydrogenation of butadiene in 1-butene in reactor R-1 by the premixed hydrogen</note>
<note type="content">Table 4: Selective hydrogenation of butadiene in 1-butene by the permeated hydrogen</note>
<note type="content">Table 5: The effect of H2/N2 ratios of the H2 and N2 mixture on the selective hydrogenation of butadiene in 1-butene in reactor R-1</note>
<note type="content">Table 6: Selective hydrogenation of butadiene in crude 1-butene with different mono- and bimetallic catalytic hollow-fiber reactors</note>
<note type="content">Table 7: Isomerization pf pure 1-butene with mono- and bimetallic catalytic hollow-fiber reactors</note>
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</ce:author>
<ce:author><ce:given-name>Shijian</ce:given-name>
<ce:surname>Liao</ce:surname>
</ce:author>
<ce:author><ce:given-name>Daorong</ce:given-name>
<ce:surname>Yu</ce:surname>
</ce:author>
<ce:affiliation><ce:textfn>Dalian Institute of Chemical Physics, Chinese Academy of Sciences, PO Box 110Dalian 116023China</ce:textfn>
</ce:affiliation>
<ce:correspondence id="CORR1"><ce:label>*</ce:label>
<ce:text>Corresponding author. Fax: +86 411 469 1570.</ce:text>
</ce:correspondence>
</ce:author-group>
<ce:date-received day="8" month="9" year="1997"></ce:date-received>
<ce:date-revised day="2" month="2" year="1998"></ce:date-revised>
<ce:date-accepted day="27" month="2" year="1998"></ce:date-accepted>
<ce:abstract><ce:section-title>Abstract</ce:section-title>
<ce:abstract-sec><ce:simple-para>The monometallic catalytic membrane reactors were established with catalytic hollow fibers prepared by supporting the polymer-anchored monometallic palladium catalyst (PVP-Pd, EC-Pd or AR-Pd) on the inside wall of CA or PSF hollow fibers. PVP=poly(<ce:italic>N</ce:italic>
-vinyl-2-pyrrolidone), EC=ethyl cellulose, AR=melamine-formaldehyde resin, CA=Cellulose acetate, PSF=polysulfone. The selective hydrogenation of butadiene in crude 1-butene was carried out in the catalytic membrane reactors at 40°C under 0.1<ce:hsp sp="0.25"></ce:hsp>
MPa. Among the above catalytic hollow fibers, the catalytic activity and selectivity of the PVP-Pd/CA monometallic hollow fiber were the best values, but there was still 2.6% 2-butene in the product. In order to inhibit the isomerization reaction of 1-butene, the bimetallic catalytic CA hollow-fiber reactors were produced and used for the above reaction. The bimetallic palladium–cobalt catalyst PVP-PdCl<ce:inf>2</ce:inf>
–0.5Co(OAc)<ce:inf>2</ce:inf>
, supported on the CA hollow fibers was reduced by NH<ce:inf>2</ce:inf>
NH<ce:inf>2</ce:inf>
or NaBH<ce:inf>4</ce:inf>
. A remarkable synergic effect of palladium and cobalt reduced by NaBH<ce:inf>4</ce:inf>
was observed.</ce:simple-para>
</ce:abstract-sec>
</ce:abstract>
<ce:keywords class="keyword"><ce:section-title>Keywords</ce:section-title>
<ce:keyword><ce:text>Catalytic hollow-fiber reactor</ce:text>
</ce:keyword>
<ce:keyword><ce:text>Polymer anchored mono- and bimetallic catalysts</ce:text>
</ce:keyword>
<ce:keyword><ce:text>Synergic effect</ce:text>
</ce:keyword>
<ce:keyword><ce:text>Selective hydrogenation</ce:text>
</ce:keyword>
<ce:keyword><ce:text>Crude 1-butene</ce:text>
</ce:keyword>
</ce:keywords>
</head>
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<mods version="3.6"><titleInfo><title>Mono- and bimetallic catalytic hollow-fiber reactors for the selective hydrogenation of butadiene in 1-butene</title>
</titleInfo>
<titleInfo type="alternative" contentType="CDATA"><title>Mono- and bimetallic catalytic hollow-fiber reactors for the selective hydrogenation of butadiene in 1-butene</title>
</titleInfo>
<name type="personal"><namePart type="given">Chunqing</namePart>
<namePart type="family">Liu</namePart>
<affiliation>Dalian Institute of Chemical Physics, Chinese Academy of Sciences, PO Box 110Dalian 116023China</affiliation>
<role><roleTerm type="text">author</roleTerm>
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</name>
<name type="personal"><namePart type="given">Yun</namePart>
<namePart type="family">Xu</namePart>
<affiliation>Dalian Institute of Chemical Physics, Chinese Academy of Sciences, PO Box 110Dalian 116023China</affiliation>
<description>Corresponding author. Fax: +86 411 469 1570.</description>
<role><roleTerm type="text">author</roleTerm>
</role>
</name>
<name type="personal"><namePart type="given">Shijian</namePart>
<namePart type="family">Liao</namePart>
<affiliation>Dalian Institute of Chemical Physics, Chinese Academy of Sciences, PO Box 110Dalian 116023China</affiliation>
<role><roleTerm type="text">author</roleTerm>
</role>
</name>
<name type="personal"><namePart type="given">Daorong</namePart>
<namePart type="family">Yu</namePart>
<affiliation>Dalian Institute of Chemical Physics, Chinese Academy of Sciences, PO Box 110Dalian 116023China</affiliation>
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<abstract lang="en">Abstract: The monometallic catalytic membrane reactors were established with catalytic hollow fibers prepared by supporting the polymer-anchored monometallic palladium catalyst (PVP-Pd, EC-Pd or AR-Pd) on the inside wall of CA or PSF hollow fibers. PVP=poly(N-vinyl-2-pyrrolidone), EC=ethyl cellulose, AR=melamine-formaldehyde resin, CA=Cellulose acetate, PSF=polysulfone. The selective hydrogenation of butadiene in crude 1-butene was carried out in the catalytic membrane reactors at 40°C under 0.1MPa. Among the above catalytic hollow fibers, the catalytic activity and selectivity of the PVP-Pd/CA monometallic hollow fiber were the best values, but there was still 2.6% 2-butene in the product. In order to inhibit the isomerization reaction of 1-butene, the bimetallic catalytic CA hollow-fiber reactors were produced and used for the above reaction. The bimetallic palladium–cobalt catalyst PVP-PdCl2–0.5Co(OAc)2, supported on the CA hollow fibers was reduced by NH2NH2 or NaBH4. A remarkable synergic effect of palladium and cobalt reduced by NaBH4 was observed.</abstract>
<note type="content">Fig. 1: Structure of the catalytic CA hollow-fiber reactor: (a) H2+N2 feed inlet; (2) crude 1-butene feed inlet; (3) product outlet; (4) tail gas outlet; (5),(6) circulating water, inlet and outlet; (7) glass jacket; (8) catalytic CA hollow fibers; (9) expoxide resin seal.</note>
<note type="content">Fig. 2: Schematic flow diagram of the selective hydrogenation of butadiene in curde 1-butene in a catalytic polymeric hollow-fiber reactor: (1) crude 1-butene feed; (2) H2+N2; (3),(4) preheaters; (5),(6) rotameters; (7) membrane reactor; (8),(9) needle valves; (10),(11) sampling ports.</note>
<note type="content">Table 1: Details of the catalytic CA hollow-fiber reactors</note>
<note type="content">Table 2: Selective hydrogenation of butadiene in 1-butene in different monometallic catalytic hollow-fiber reactors</note>
<note type="content">Table 3: Selective hydrogenation of butadiene in 1-butene in reactor R-1 by the premixed hydrogen</note>
<note type="content">Table 4: Selective hydrogenation of butadiene in 1-butene by the permeated hydrogen</note>
<note type="content">Table 5: The effect of H2/N2 ratios of the H2 and N2 mixture on the selective hydrogenation of butadiene in 1-butene in reactor R-1</note>
<note type="content">Table 6: Selective hydrogenation of butadiene in crude 1-butene with different mono- and bimetallic catalytic hollow-fiber reactors</note>
<note type="content">Table 7: Isomerization pf pure 1-butene with mono- and bimetallic catalytic hollow-fiber reactors</note>
<subject><genre>Keywords</genre>
<topic>Catalytic hollow-fiber reactor</topic>
<topic>Polymer anchored mono- and bimetallic catalysts</topic>
<topic>Synergic effect</topic>
<topic>Selective hydrogenation</topic>
<topic>Crude 1-butene</topic>
</subject>
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<identifier type="ISSN">0926-860X</identifier>
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<detail type="volume"><number>172</number>
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