Zobrazeno 1 - 10
of 47
pro vyhledávání: '"Sunun Limtrakul"'
Publikováno v:
ACS Omega, Vol 6, Iss 45, Pp 30451-30464 (2021)
Externí odkaz:
https://doaj.org/article/7d824a409d5847cb96b72e6121e04c6a
Autor:
Kainakhone Pathoumthong, Putong Ratanamalaya, Sunun Limtrakul, Terdthai Vatanatham, Palghat A. Ramachandran
Publikováno v:
Industrial & Engineering Chemistry Research. 61:17077-17091
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::8776091503db38d665bc525fe85d362c
https://doi.org/10.1021/acs.iecr.2c03634
https://doi.org/10.1021/acs.iecr.2c03634
Autor:
null Ekaroek Phumnok, null Waritnan Wanchan, null Matinee Chuenjai, null Panut Bumphenkiattikul, null Sunun Limtrakul, null Sukrittira Rattanawilai, null Parinya Khongprom
Publikováno v:
CFD Letters. 14:115-133
Stirred tanks are prevalent in various industries, including chemical, biochemical, and pharmaceutical industries. These reactors are suitable for ensuring efficient mass and heat transfer because adequate mixing can be achieved. Numerous studies hav
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::63909eb809fd473f90f5edef5ffab910
https://doi.org/10.37934/cfdl.14.6.115133
https://doi.org/10.37934/cfdl.14.6.115133
Publikováno v:
ACS Omega, Vol 6, Iss 45, Pp 30451-30464 (2021)
ACS Omega
ACS Omega
The amidation reaction to produce fatty acid diethanolamide is an important unit process to produce surfactants from renewable sources rather than from petroleum sources. Amidation is a liquid-phase reaction between diethanolamine with a fatty acid m
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_dedup___::83a7abc753fadf02d29b34e014933b60
https://doaj.org/article/7d824a409d5847cb96b72e6121e04c6a
https://doaj.org/article/7d824a409d5847cb96b72e6121e04c6a
Autor:
Terdthai Vatanatham, Chompunoot Banthaothook, Palghat A. Ramachandran, Attasak Jaree, Papop Bannatham, Sunun Limtrakul
Publikováno v:
Industrial & Engineering Chemistry Research. 60:15972-15988
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::d650867394333401f6a7be7ccff11ad5
https://doi.org/10.1021/acs.iecr.1c03009
https://doi.org/10.1021/acs.iecr.1c03009
Publikováno v:
ACS omega. 7(41)
Natural rubber (NR) has restricted its application due to its potential for thermal- and oil-resistant materials. The weakness of NR can be eliminated by chemical modification to enhance aging properties. Formic acid and hydrogen peroxide have been u
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_dedup___::99cf79be99f561b8ca113f5ab6846481
https://pubmed.ncbi.nlm.nih.gov/36278086
https://pubmed.ncbi.nlm.nih.gov/36278086
Autor:
Parinya Khongprom, Supawadee Ratchasombat, Waritnan Wanchan, Panut Bumphenkiattikul, Sunun Limtrakul
Publikováno v:
RSC advances. 12(33)
The practical realization of the scaling up of gas-solid multiphase flow reactors with chemical reactions is hindered by chaotic flow behaviors and complex heat and mass transfers in the reactor. In addition, a law to scale up complex reaction mechan
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_dedup___::37a0159aeb12a210e4e9ae90f35aa819
https://pubmed.ncbi.nlm.nih.gov/35975037
https://pubmed.ncbi.nlm.nih.gov/35975037
Publikováno v:
Chemical Engineering Research and Design. 156:442-455
Circulating fluidized bed (CFB) riser reactors are widely used in several industrial gas–solid flow systems to achieve a high reaction rate and a high heat of reaction. Thus, understanding wall-to-bed heat transfer is essential for optimizing CFB o
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::0696231dd97395fc692f8e7e5e1fe18a
https://doi.org/10.1016/j.cherd.2020.02.021
https://doi.org/10.1016/j.cherd.2020.02.021
Autor:
Supawadee Ratchasombat, Parinya Khongprom, Waritnan Wanchan, Sunun Limtrakul, Panut Bumphenkiattikul
Publikováno v:
RSC Advances. 10:2897-2914
Circulating fluidized bed downer reactors (downer reactors) exhibit good heat and mass transfer, and the flow behavior approaches the ideal plug flow. This reactor is superior for catalytic cracking reactions in which the intermediate is the desired
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_dedup___::187dc0a5a725139bdfbcca9ea3ab6dde
https://doi.org/10.1039/c9ra10080f
https://doi.org/10.1039/c9ra10080f
Autor:
Sunun Limtrakul, Palghat A. Ramachandran, Sornsawan Teeraboonchaikul, Papop Bannatham, Terdthai Vatanatham
Publikováno v:
Powder Technology. 354:779-791
Hydrodesulfurization of heavy oil is usually operated in a trickle bed reactor. Analysis and design of this reactor require modeling both at the macro-reactor scale and micro-catalyst scale. The paper is focused on the catalyst-level modeling and tak
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::6c7e03306578600e4659aac37de996f7
https://doi.org/10.1016/j.powtec.2019.06.047
https://doi.org/10.1016/j.powtec.2019.06.047