Scale-up of bubbling fluidized beds with continuous particle flow based on particle-residence-time distribution
Highlights • It was possible to obtain similar RTDs in geometrically similar bubbling fluidized beds. • A simple scaling method was proposed without need of changing particle size and gas velocity. • RTDs of BFBs at different scales could be predicted by using the simple scaling method.
Gespeichert in:
| Autor*in: |
Zhang, Juwei [verfasserIn] |
|---|
| Format: |
E-Artikel |
|---|---|
| Sprache: |
Englisch |
| Erschienen: |
2015 |
|---|
| Schlagwörter: |
|---|
| Umfang: |
9 |
|---|
| Übergeordnetes Werk: |
Enthalten in: Pathologic Outcomes in Borderline Resectable and Locally Advanced Pancreatic Cancer Patients Receiving Neoadjuvant Stereotactic Body Radiation Therapy - Rosati, L.M. ELSEVIER, 2015, Amsterdam |
|---|---|
| Übergeordnetes Werk: |
volume:19 ; year:2015 ; pages:155-163 ; extent:9 |
| Links: |
|---|
| DOI / URN: |
10.1016/j.partic.2014.04.019 |
|---|
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ELV039696650 |
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| 520 | |a Highlights • It was possible to obtain similar RTDs in geometrically similar bubbling fluidized beds. • A simple scaling method was proposed without need of changing particle size and gas velocity. • RTDs of BFBs at different scales could be predicted by using the simple scaling method. | ||
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<?xml version="1.0" encoding="UTF-8"?><collection xmlns="http://www.loc.gov/MARC21/slim"><record><leader>01000caa a22002652 4500</leader><controlfield tag="001">ELV039696650</controlfield><controlfield tag="003">DE-627</controlfield><controlfield tag="005">20230624063555.0</controlfield><controlfield tag="007">cr uuu---uuuuu</controlfield><controlfield tag="008">180603s2015 xx |||||o 00| ||eng c</controlfield><datafield tag="024" ind1="7" ind2=" "><subfield code="a">10.1016/j.partic.2014.04.019</subfield><subfield code="2">doi</subfield></datafield><datafield tag="028" ind1="5" ind2="2"><subfield code="a">GBVA2015007000021.pica</subfield></datafield><datafield tag="035" ind1=" " ind2=" "><subfield code="a">(DE-627)ELV039696650</subfield></datafield><datafield tag="035" ind1=" " ind2=" "><subfield code="a">(ELSEVIER)S1674-2001(14)00152-7</subfield></datafield><datafield tag="040" ind1=" " ind2=" "><subfield code="a">DE-627</subfield><subfield code="b">ger</subfield><subfield code="c">DE-627</subfield><subfield code="e">rakwb</subfield></datafield><datafield tag="041" ind1=" " ind2=" "><subfield code="a">eng</subfield></datafield><datafield tag="082" ind1="0" ind2=" "><subfield code="a">530</subfield></datafield><datafield tag="082" ind1="0" ind2="4"><subfield code="a">530</subfield><subfield code="q">DE-600</subfield></datafield><datafield tag="082" ind1="0" ind2="4"><subfield code="a">610</subfield><subfield code="q">VZ</subfield></datafield><datafield tag="082" ind1="0" ind2="4"><subfield code="a">610</subfield><subfield code="q">VZ</subfield></datafield><datafield tag="084" ind1=" " ind2=" "><subfield code="a">44.40</subfield><subfield code="2">bkl</subfield></datafield><datafield tag="100" ind1="1" ind2=" "><subfield code="a">Zhang, Juwei</subfield><subfield code="e">verfasserin</subfield><subfield code="4">aut</subfield></datafield><datafield tag="245" ind1="1" ind2="0"><subfield code="a">Scale-up of bubbling fluidized beds with continuous particle flow based on particle-residence-time distribution</subfield></datafield><datafield tag="264" ind1=" " ind2="1"><subfield code="c">2015</subfield></datafield><datafield tag="300" ind1=" " ind2=" "><subfield code="a">9</subfield></datafield><datafield tag="336" ind1=" " ind2=" "><subfield code="a">nicht spezifiziert</subfield><subfield code="b">zzz</subfield><subfield code="2">rdacontent</subfield></datafield><datafield tag="337" ind1=" " ind2=" "><subfield code="a">nicht spezifiziert</subfield><subfield code="b">z</subfield><subfield code="2">rdamedia</subfield></datafield><datafield tag="338" ind1=" " ind2=" "><subfield code="a">nicht spezifiziert</subfield><subfield code="b">zu</subfield><subfield code="2">rdacarrier</subfield></datafield><datafield tag="520" ind1=" " ind2=" "><subfield code="a">Highlights • It was possible to obtain similar RTDs in geometrically similar bubbling fluidized beds. • A simple scaling method was proposed without need of changing particle size and gas velocity. • RTDs of BFBs at different scales could be predicted by using the simple scaling method.</subfield></datafield><datafield tag="650" ind1=" " ind2="7"><subfield code="a">Similarity</subfield><subfield code="2">Elsevier</subfield></datafield><datafield tag="650" ind1=" " ind2="7"><subfield code="a">Bubbling fluidized bed (BFB)</subfield><subfield code="2">Elsevier</subfield></datafield><datafield tag="650" ind1=" " ind2="7"><subfield code="a">Residence time distribution (RTD)</subfield><subfield code="2">Elsevier</subfield></datafield><datafield tag="650" ind1=" " ind2="7"><subfield code="a">Scale-up</subfield><subfield code="2">Elsevier</subfield></datafield><datafield tag="700" ind1="1" ind2=" "><subfield code="a">Xu, Guangwen</subfield><subfield code="4">oth</subfield></datafield><datafield tag="773" ind1="0" ind2="8"><subfield code="i">Enthalten in</subfield><subfield code="n">Elsevier</subfield><subfield code="a">Rosati, L.M. 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