Corrigendum to “Steam gasification of polyethylene terephthalate (PET) with CaO in a bubbling fluidized bed gasifier for enriching H2 in syngas with Response Surface Methodology (RSM)” [APEN 348 (2023) 121536] (Applied Energy (2023) 348

Shouzhuang Li; Muddasser Inayat; Mika Järvinen

doi:10.1016/j.apenergy.2024.123134

Corrigendum to “Steam gasification of polyethylene terephthalate (PET) with CaO in a bubbling fluidized bed gasifier for enriching H2 in syngas with Response Surface Methodology (RSM)” [APEN 348 (2023) 121536] (Applied Energy (2023) 348

Shouzhuang Li^*
, Muddasser Inayat
, Mika Järvinen

^*Corresponding author for this work

Not published at VTT

Aalto University

Research output: Contribution to journal › Other journal contribution › Scientific

Abstract

The authors regret to inform the readers that there was a typo in Eq. (9). The coefficient of the term T2 should be −0.000253 instead of −0.0025. Therefore, the correct Eq. 9 should be: [Formula presented] Correspondingly, the contour of CO yield in Fig. 6 (A) based on Eq. (9) should also be replotted.[Formula presented] Other results and conclusions would not be affected by this corrigendum. For example, the validation in Table 6 was conducted with the correct coefficient. The authors would like to apologize for any inconvenience caused.

Original language	English
Number of pages	123134
Journal	Applied Energy
Volume	364
DOIs	https://doi.org/10.1016/j.apenergy.2024.123134
Publication status	Published - 15 Jun 2024
MoE publication type	B1 Article in a scientific magazine

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Steam gasification of polyethylene terephthalate (PET) with CaO in a bubbling fluidized bed gasifier for enriching H₂ in syngas with Response Surface Methodology (RSM)
Li, S., Inayat, M. & Järvinen, M., 15 Oct 2023, In: Applied Energy. 348, 121536.
Research output: Contribution to journal › Article › Scientific › peer-review

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title = "Corrigendum to {\textquotedblleft}Steam gasification of polyethylene terephthalate (PET) with CaO in a bubbling fluidized bed gasifier for enriching H2 in syngas with Response Surface Methodology (RSM){\textquotedblright} [APEN 348 (2023) 121536] (Applied Energy (2023) 348",

abstract = "The authors regret to inform the readers that there was a typo in Eq. (9). The coefficient of the term T2 should be −0.000253 instead of −0.0025. Therefore, the correct Eq. 9 should be: [Formula presented] Correspondingly, the contour of CO yield in Fig. 6 (A) based on Eq. (9) should also be replotted.[Formula presented] Other results and conclusions would not be affected by this corrigendum. For example, the validation in Table 6 was conducted with the correct coefficient. The authors would like to apologize for any inconvenience caused.",

author = "Shouzhuang Li and Muddasser Inayat and Mika J{\"a}rvinen",

year = "2024",

month = jun,

day = "15",

doi = "10.1016/j.apenergy.2024.123134",

language = "English",

volume = "364",

journal = "Applied Energy",

issn = "0306-2619",

publisher = "Elsevier",

}

Corrigendum to “Steam gasification of polyethylene terephthalate (PET) with CaO in a bubbling fluidized bed gasifier for enriching H2 in syngas with Response Surface Methodology (RSM)” [APEN 348 (2023) 121536] (Applied Energy (2023) 348. / Li, Shouzhuang; Inayat, Muddasser; Järvinen, Mika.
In: Applied Energy, Vol. 364, 15.06.2024.

Research output: Contribution to journal › Other journal contribution › Scientific

TY - JOUR

T1 - Corrigendum to “Steam gasification of polyethylene terephthalate (PET) with CaO in a bubbling fluidized bed gasifier for enriching H2 in syngas with Response Surface Methodology (RSM)” [APEN 348 (2023) 121536] (Applied Energy (2023) 348

AU - Li, Shouzhuang

AU - Inayat, Muddasser

AU - Järvinen, Mika

PY - 2024/6/15

Y1 - 2024/6/15

N2 - The authors regret to inform the readers that there was a typo in Eq. (9). The coefficient of the term T2 should be −0.000253 instead of −0.0025. Therefore, the correct Eq. 9 should be: [Formula presented] Correspondingly, the contour of CO yield in Fig. 6 (A) based on Eq. (9) should also be replotted.[Formula presented] Other results and conclusions would not be affected by this corrigendum. For example, the validation in Table 6 was conducted with the correct coefficient. The authors would like to apologize for any inconvenience caused.

AB - The authors regret to inform the readers that there was a typo in Eq. (9). The coefficient of the term T2 should be −0.000253 instead of −0.0025. Therefore, the correct Eq. 9 should be: [Formula presented] Correspondingly, the contour of CO yield in Fig. 6 (A) based on Eq. (9) should also be replotted.[Formula presented] Other results and conclusions would not be affected by this corrigendum. For example, the validation in Table 6 was conducted with the correct coefficient. The authors would like to apologize for any inconvenience caused.

UR - https://www.scopus.com/pages/publications/85189668694

U2 - 10.1016/j.apenergy.2024.123134

DO - 10.1016/j.apenergy.2024.123134

M3 - Other journal contribution

SN - 0306-2619

VL - 364

JO - Applied Energy

JF - Applied Energy

ER -

Corrigendum to “Steam gasification of polyethylene terephthalate (PET) with CaO in a bubbling fluidized bed gasifier for enriching H2 in syngas with Response Surface Methodology (RSM)” [APEN 348 (2023) 121536] (Applied Energy (2023) 348

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Research output

Steam gasification of polyethylene terephthalate (PET) with CaO in a bubbling fluidized bed gasifier for enriching H2 in syngas with Response Surface Methodology (RSM)

Cite this

Steam gasification of polyethylene terephthalate (PET) with CaO in a bubbling fluidized bed gasifier for enriching H₂ in syngas with Response Surface Methodology (RSM)