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Pressure Drop Correlation Covering Dilute to Dense Regimes of Solid Particle-Gas Flow in a Vertical Conveying Pipe

Journal of Engineering and Technological Sciences · Vol. 41 No. 1 (2013) · hlm. 65–76

DOI
10.5614/itbj.eng.sci.2009.41.1.5
ISSN
2338-5502, 2337-5779
Terbit
2013-09-13
Penerbit
Directorate for Research and Community Services, Institut Teknologi Bandung
Bahasa
eng

Abstrak

More general correlations between pressure drop and gas-solid flow variables are developed from the present experimental data. The correlation was modeled for a pneumatic conveying system in a vertical pipe. The transition boundary between dense and dilute regimes is constructed from the pressure drop correlations. The gas-solid particle flow variables are quantified by the gas Reynolds (Nref) and the solid Froude (Frp) numbers. The dense flow regime is indicated by the decrease of the pressure drop with the increase of the gas Reynolds number. In contrary, the dilute regime exhibits the increase of the pressure drop with the gas Reynolds number. The proposed correlations were built at the range of gas Reynolds number f from 360 to 500 and solid Froude number from 0,01 to 0,02.

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  • Bandung Institute of Technology
  • Sultan Ageng Tirtayasa University
  • Pertamina (Indonesia)
  • IPB University
  • Diponegoro University
  • Institut Teknologi Sepuluh Nopember
  • Sumatera Institute of Technology
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Rekan penulisOrganisasiArtikel bersama
Yogi Wibisono BudhiBandung Institute of Technology5
Anton IrawanSultan Ageng Tirtayasa University3
Subagjo SubagjoBandung Institute of Technology3
Mohammad EffendyBandung Institute of Technology3
Hafid AlwanSultan Ageng Tirtayasa University2
Teguh KurniawanSultan Ageng Tirtayasa University2
Tjokorde Walmiki SamadhiBandung Institute of Technology2
Elfa Susanti ThamrinSumatera Institute of Technology1
Endang WarsikiIPB University1
Ono SuparnoIPB University1
Asep Bayu Dani NandiyantoIndonesia University of Education1
Darisman DarismanSultan Ageng Tirtayasa University1
Dina PujiantiSultan Ageng Tirtayasa University1
Muhammad Saifullah Abu BakarUniversiti Brunei Darussalam1
Aprilina PurbasariDiponegoro University1
IGBN MakertiharthaAfiliasi tidak diketahui1
Luqman BuchoriDiponegoro University1
Muhammad Dani SupardanUniversitas Syiah Kuala1
Renanto RenantoAfiliasi tidak diketahui1
Wahono SumaryonoBadan Pengkajian dan Penerapan Teknologi1
Achmad RoesyadiInstitut Teknologi Sepuluh Nopember1
Semuel Pati SendaInstitut Teknologi Sepuluh Nopember1
Vita WonoputriBandung Institute of Technology1
Abdullah Nur AzizJenderal Soedirman University1
Yul Yunazwin NazaruddinBandung Institute of Technology1
Parsaulian Ishaya SiregarBandung Institute of Technology1
Pasymi PasymiBandung Institute of Technology1
Made Tri Ari Penia KresnowatiBandung Institute of Technology1
Fathya RahminaBandung Institute of Technology1
Elvi RestiawatyBandung Institute of Technology1
Soen StevenBandung Institute of Technology1
Septhian MarnoPertamina (Indonesia)1
Oki MurazaPertamina (Indonesia)1
Jenny RizkianaBandung Institute of Technology1
Pandit HernowoInstitut Sains dan Teknologi Al-Kamal1
Carolus Borromeus RasrendraBandung Institute of Technology1
Yana MelianaPertamina (Indonesia)1

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Sumber metadata: OAI-PMH (metadata jurnal) https://journals.itb.ac.id/index.php/jets/oai, pertama di-harvest 9 Nov 2026, terakhir terlihat 9 Nov 2026.
Metadata asli (oai_dc) 
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	<dc:title xml:lang="en-US">Pressure Drop Correlation Covering Dilute to Dense Regimes of Solid Particle-Gas Flow in a Vertical Conveying Pipe</dc:title>
	<dc:creator>Bindar, Yazid</dc:creator>
	<dc:creator>Sutrisniningrum, N. A.</dc:creator>
	<dc:creator>Santiani, D.</dc:creator>
	<dc:description xml:lang="en-US">More  general  correlations  between  pressure  drop  and  gas-solid  flow variables are developed from the present experimental data. The correlation was modeled  for  a  pneumatic  conveying  system  in  a  vertical  pipe.  The  transition boundary  between  dense  and  dilute  regimes  is  constructed  from  the  pressure drop correlations. The gas-solid particle flow variables are quantified by the gas Reynolds  (Nref)  and  the  solid  Froude  (Frp)  numbers.  The  dense  flow  regime  is indicated  by  the  decrease  of  the  pressure  drop  with  the  increase  of  the  gas Reynolds  number.  In  contrary,  the  dilute  regime  exhibits  the  increase  of  the pressure  drop  with  the  gas  Reynolds  number.  The  proposed  correlations  were built at the range of gas Reynolds number f from 360 to 500 and solid Froude number from 0,01 to 0,02.</dc:description>
	<dc:publisher xml:lang="en-US">Directorate for Research and Community Services, Institut Teknologi Bandung</dc:publisher>
	<dc:date>2013-09-13</dc:date>
	<dc:type>info:eu-repo/semantics/article</dc:type>
	<dc:type>info:eu-repo/semantics/publishedVersion</dc:type>
	<dc:format>application/pdf</dc:format>
	<dc:identifier>https://journals.itb.ac.id/index.php/jets/article/view/117</dc:identifier>
	<dc:identifier>10.5614/itbj.eng.sci.2009.41.1.5</dc:identifier>
	<dc:source xml:lang="en-US">Journal of Engineering and Technological Sciences; Vol. 41 No. 1 (2009); 65-76</dc:source>
	<dc:source>2338-5502</dc:source>
	<dc:source>2337-5779</dc:source>
	<dc:language>eng</dc:language>
	<dc:relation>https://journals.itb.ac.id/index.php/jets/article/view/117/113</dc:relation>
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