Influence of Crude Oil Type on Products Quality of the Atmospheric Distillation Unit by Applying Material Flow Cost Accounting Simulation: Part A
The oil refining industry, as one of the most important sources of supply for the people of the world, needs to optimize energy. In the present study, the atmospheric distillation unit of a refinery has been selected as a case study. Using a new method of material flow cost, determining the positive...
Ausführliche Beschreibung
Autor*in: |
Asadollah Karimi [verfasserIn] Elham Mahmoudi [verfasserIn] Esmaeil Fatehifar [verfasserIn] Ali Reza Motavalli [verfasserIn] |
---|
Format: |
E-Artikel |
---|---|
Sprache: |
Englisch |
Erschienen: |
2020 |
---|
Schlagwörter: |
---|
Übergeordnetes Werk: |
In: Iranian Journal of Chemistry & Chemical Engineering - Iranian Institute of Research and Development in Chemical Industries (IRDCI)-ACECR, 2020, 39(2020), 6, Seite 215-227 |
---|---|
Übergeordnetes Werk: |
volume:39 ; year:2020 ; number:6 ; pages:215-227 |
Links: |
Link aufrufen |
---|
DOI / URN: |
10.30492/ijcce.2019.36239 |
---|
Katalog-ID: |
DOAJ070216126 |
---|
LEADER | 01000caa a22002652 4500 | ||
---|---|---|---|
001 | DOAJ070216126 | ||
003 | DE-627 | ||
005 | 20230309091647.0 | ||
007 | cr uuu---uuuuu | ||
008 | 230228s2020 xx |||||o 00| ||eng c | ||
024 | 7 | |a 10.30492/ijcce.2019.36239 |2 doi | |
035 | |a (DE-627)DOAJ070216126 | ||
035 | |a (DE-599)DOAJ1c6c4bfe2d3344ee83ab727ba2fc2f37 | ||
040 | |a DE-627 |b ger |c DE-627 |e rakwb | ||
041 | |a eng | ||
050 | 0 | |a TP155-156 | |
050 | 0 | |a QD1-999 | |
100 | 0 | |a Asadollah Karimi |e verfasserin |4 aut | |
245 | 1 | 0 | |a Influence of Crude Oil Type on Products Quality of the Atmospheric Distillation Unit by Applying Material Flow Cost Accounting Simulation: Part A |
264 | 1 | |c 2020 | |
336 | |a Text |b txt |2 rdacontent | ||
337 | |a Computermedien |b c |2 rdamedia | ||
338 | |a Online-Ressource |b cr |2 rdacarrier | ||
520 | |a The oil refining industry, as one of the most important sources of supply for the people of the world, needs to optimize energy. In the present study, the atmospheric distillation unit of a refinery has been selected as a case study. Using a new method of material flow cost, determining the positive and negative products and their actual valuation, the share of various costs in the unit has been demonstrated. Since about 99.3% of the total costs in this unit are related to the cost of purchasing crude oil as feedstock, the importance of purchasing crude oil in the event of crisis management and the conditions of alternatives are fully characterized. Three crude oils named Maroon, Dezful, and Mansouri were studied as alternatives for Ahwaz crude oil. The results of Maroon crude oil show that, in the same operating conditions, its substitution as the main feedstock obtains the same quality products as Ahvaz crude oil products. The products derived from Dezful crude oil shows a difference of approximately 7 to 8 degrees API. Products from Mansouri crude oil have a difference of between 20°C and 40°C at boiling point and a difference of 5° to 7°API, and with increasing temperature and feed pressure, there is no significant change in the quality of the products. The mixture of Mansouri and Dezful crude oil separately with Ahwaz crude oil does not achieve the desired quality. But proper quality can be obtained by applying changes of 10 °C to 30 °C at inlet temperature, and from 0.5 to 0.7 kg/cm2 at the pressure. Due to the same price of Ahwaz and Maroon and Dezful, there is no change in the cost of purchasing, and products of the same cost are obtained. | ||
650 | 4 | |a refinery | |
650 | 4 | |a atmospheric distillation tower | |
650 | 4 | |a simulation | |
650 | 4 | |a mfca | |
650 | 4 | |a positive products | |
650 | 4 | |a reduce loss | |
653 | 0 | |a Chemical engineering | |
653 | 0 | |a Chemistry | |
700 | 0 | |a Elham Mahmoudi |e verfasserin |4 aut | |
700 | 0 | |a Esmaeil Fatehifar |e verfasserin |4 aut | |
700 | 0 | |a Ali Reza Motavalli |e verfasserin |4 aut | |
773 | 0 | 8 | |i In |t Iranian Journal of Chemistry & Chemical Engineering |d Iranian Institute of Research and Development in Chemical Industries (IRDCI)-ACECR, 2020 |g 39(2020), 6, Seite 215-227 |w (DE-627)501417176 |w (DE-600)2206335-3 |x 10219986 |7 nnns |
773 | 1 | 8 | |g volume:39 |g year:2020 |g number:6 |g pages:215-227 |
856 | 4 | 0 | |u https://doi.org/10.30492/ijcce.2019.36239 |z kostenfrei |
856 | 4 | 0 | |u https://doaj.org/article/1c6c4bfe2d3344ee83ab727ba2fc2f37 |z kostenfrei |
856 | 4 | 0 | |u http://www.ijcce.ac.ir/article_36239_f877f616345454931854ff97b8dc72d3.pdf |z kostenfrei |
856 | 4 | 2 | |u https://doaj.org/toc/1021-9986 |y Journal toc |z kostenfrei |
856 | 4 | 2 | |u https://doaj.org/toc/1021-9986 |y Journal toc |z kostenfrei |
912 | |a GBV_USEFLAG_A | ||
912 | |a SYSFLAG_A | ||
912 | |a GBV_DOAJ | ||
912 | |a GBV_ILN_20 | ||
912 | |a GBV_ILN_22 | ||
912 | |a GBV_ILN_23 | ||
912 | |a GBV_ILN_24 | ||
912 | |a GBV_ILN_39 | ||
912 | |a GBV_ILN_40 | ||
912 | |a GBV_ILN_60 | ||
912 | |a GBV_ILN_62 | ||
912 | |a GBV_ILN_63 | ||
912 | |a GBV_ILN_65 | ||
912 | |a GBV_ILN_69 | ||
912 | |a GBV_ILN_70 | ||
912 | |a GBV_ILN_73 | ||
912 | |a GBV_ILN_95 | ||
912 | |a GBV_ILN_105 | ||
912 | |a GBV_ILN_110 | ||
912 | |a GBV_ILN_151 | ||
912 | |a GBV_ILN_161 | ||
912 | |a GBV_ILN_170 | ||
912 | |a GBV_ILN_213 | ||
912 | |a GBV_ILN_230 | ||
912 | |a GBV_ILN_285 | ||
912 | |a GBV_ILN_293 | ||
912 | |a GBV_ILN_602 | ||
912 | |a GBV_ILN_2014 | ||
912 | |a GBV_ILN_4012 | ||
912 | |a GBV_ILN_4037 | ||
912 | |a GBV_ILN_4112 | ||
912 | |a GBV_ILN_4125 | ||
912 | |a GBV_ILN_4126 | ||
912 | |a GBV_ILN_4249 | ||
912 | |a GBV_ILN_4305 | ||
912 | |a GBV_ILN_4306 | ||
912 | |a GBV_ILN_4307 | ||
912 | |a GBV_ILN_4313 | ||
912 | |a GBV_ILN_4322 | ||
912 | |a GBV_ILN_4323 | ||
912 | |a GBV_ILN_4324 | ||
912 | |a GBV_ILN_4325 | ||
912 | |a GBV_ILN_4335 | ||
912 | |a GBV_ILN_4338 | ||
912 | |a GBV_ILN_4367 | ||
912 | |a GBV_ILN_4700 | ||
951 | |a AR | ||
952 | |d 39 |j 2020 |e 6 |h 215-227 |
author_variant |
a k ak e m em e f ef a r m arm |
---|---|
matchkey_str |
article:10219986:2020----::nlecocueitpopoutqaiyfhamshrcitlainntypligaeil |
hierarchy_sort_str |
2020 |
callnumber-subject-code |
TP |
publishDate |
2020 |
allfields |
10.30492/ijcce.2019.36239 doi (DE-627)DOAJ070216126 (DE-599)DOAJ1c6c4bfe2d3344ee83ab727ba2fc2f37 DE-627 ger DE-627 rakwb eng TP155-156 QD1-999 Asadollah Karimi verfasserin aut Influence of Crude Oil Type on Products Quality of the Atmospheric Distillation Unit by Applying Material Flow Cost Accounting Simulation: Part A 2020 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier The oil refining industry, as one of the most important sources of supply for the people of the world, needs to optimize energy. In the present study, the atmospheric distillation unit of a refinery has been selected as a case study. Using a new method of material flow cost, determining the positive and negative products and their actual valuation, the share of various costs in the unit has been demonstrated. Since about 99.3% of the total costs in this unit are related to the cost of purchasing crude oil as feedstock, the importance of purchasing crude oil in the event of crisis management and the conditions of alternatives are fully characterized. Three crude oils named Maroon, Dezful, and Mansouri were studied as alternatives for Ahwaz crude oil. The results of Maroon crude oil show that, in the same operating conditions, its substitution as the main feedstock obtains the same quality products as Ahvaz crude oil products. The products derived from Dezful crude oil shows a difference of approximately 7 to 8 degrees API. Products from Mansouri crude oil have a difference of between 20°C and 40°C at boiling point and a difference of 5° to 7°API, and with increasing temperature and feed pressure, there is no significant change in the quality of the products. The mixture of Mansouri and Dezful crude oil separately with Ahwaz crude oil does not achieve the desired quality. But proper quality can be obtained by applying changes of 10 °C to 30 °C at inlet temperature, and from 0.5 to 0.7 kg/cm2 at the pressure. Due to the same price of Ahwaz and Maroon and Dezful, there is no change in the cost of purchasing, and products of the same cost are obtained. refinery atmospheric distillation tower simulation mfca positive products reduce loss Chemical engineering Chemistry Elham Mahmoudi verfasserin aut Esmaeil Fatehifar verfasserin aut Ali Reza Motavalli verfasserin aut In Iranian Journal of Chemistry & Chemical Engineering Iranian Institute of Research and Development in Chemical Industries (IRDCI)-ACECR, 2020 39(2020), 6, Seite 215-227 (DE-627)501417176 (DE-600)2206335-3 10219986 nnns volume:39 year:2020 number:6 pages:215-227 https://doi.org/10.30492/ijcce.2019.36239 kostenfrei https://doaj.org/article/1c6c4bfe2d3344ee83ab727ba2fc2f37 kostenfrei http://www.ijcce.ac.ir/article_36239_f877f616345454931854ff97b8dc72d3.pdf kostenfrei https://doaj.org/toc/1021-9986 Journal toc kostenfrei https://doaj.org/toc/1021-9986 Journal toc kostenfrei GBV_USEFLAG_A SYSFLAG_A GBV_DOAJ GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_95 GBV_ILN_105 GBV_ILN_110 GBV_ILN_151 GBV_ILN_161 GBV_ILN_170 GBV_ILN_213 GBV_ILN_230 GBV_ILN_285 GBV_ILN_293 GBV_ILN_602 GBV_ILN_2014 GBV_ILN_4012 GBV_ILN_4037 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4249 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4335 GBV_ILN_4338 GBV_ILN_4367 GBV_ILN_4700 AR 39 2020 6 215-227 |
spelling |
10.30492/ijcce.2019.36239 doi (DE-627)DOAJ070216126 (DE-599)DOAJ1c6c4bfe2d3344ee83ab727ba2fc2f37 DE-627 ger DE-627 rakwb eng TP155-156 QD1-999 Asadollah Karimi verfasserin aut Influence of Crude Oil Type on Products Quality of the Atmospheric Distillation Unit by Applying Material Flow Cost Accounting Simulation: Part A 2020 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier The oil refining industry, as one of the most important sources of supply for the people of the world, needs to optimize energy. In the present study, the atmospheric distillation unit of a refinery has been selected as a case study. Using a new method of material flow cost, determining the positive and negative products and their actual valuation, the share of various costs in the unit has been demonstrated. Since about 99.3% of the total costs in this unit are related to the cost of purchasing crude oil as feedstock, the importance of purchasing crude oil in the event of crisis management and the conditions of alternatives are fully characterized. Three crude oils named Maroon, Dezful, and Mansouri were studied as alternatives for Ahwaz crude oil. The results of Maroon crude oil show that, in the same operating conditions, its substitution as the main feedstock obtains the same quality products as Ahvaz crude oil products. The products derived from Dezful crude oil shows a difference of approximately 7 to 8 degrees API. Products from Mansouri crude oil have a difference of between 20°C and 40°C at boiling point and a difference of 5° to 7°API, and with increasing temperature and feed pressure, there is no significant change in the quality of the products. The mixture of Mansouri and Dezful crude oil separately with Ahwaz crude oil does not achieve the desired quality. But proper quality can be obtained by applying changes of 10 °C to 30 °C at inlet temperature, and from 0.5 to 0.7 kg/cm2 at the pressure. Due to the same price of Ahwaz and Maroon and Dezful, there is no change in the cost of purchasing, and products of the same cost are obtained. refinery atmospheric distillation tower simulation mfca positive products reduce loss Chemical engineering Chemistry Elham Mahmoudi verfasserin aut Esmaeil Fatehifar verfasserin aut Ali Reza Motavalli verfasserin aut In Iranian Journal of Chemistry & Chemical Engineering Iranian Institute of Research and Development in Chemical Industries (IRDCI)-ACECR, 2020 39(2020), 6, Seite 215-227 (DE-627)501417176 (DE-600)2206335-3 10219986 nnns volume:39 year:2020 number:6 pages:215-227 https://doi.org/10.30492/ijcce.2019.36239 kostenfrei https://doaj.org/article/1c6c4bfe2d3344ee83ab727ba2fc2f37 kostenfrei http://www.ijcce.ac.ir/article_36239_f877f616345454931854ff97b8dc72d3.pdf kostenfrei https://doaj.org/toc/1021-9986 Journal toc kostenfrei https://doaj.org/toc/1021-9986 Journal toc kostenfrei GBV_USEFLAG_A SYSFLAG_A GBV_DOAJ GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_95 GBV_ILN_105 GBV_ILN_110 GBV_ILN_151 GBV_ILN_161 GBV_ILN_170 GBV_ILN_213 GBV_ILN_230 GBV_ILN_285 GBV_ILN_293 GBV_ILN_602 GBV_ILN_2014 GBV_ILN_4012 GBV_ILN_4037 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4249 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4335 GBV_ILN_4338 GBV_ILN_4367 GBV_ILN_4700 AR 39 2020 6 215-227 |
allfields_unstemmed |
10.30492/ijcce.2019.36239 doi (DE-627)DOAJ070216126 (DE-599)DOAJ1c6c4bfe2d3344ee83ab727ba2fc2f37 DE-627 ger DE-627 rakwb eng TP155-156 QD1-999 Asadollah Karimi verfasserin aut Influence of Crude Oil Type on Products Quality of the Atmospheric Distillation Unit by Applying Material Flow Cost Accounting Simulation: Part A 2020 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier The oil refining industry, as one of the most important sources of supply for the people of the world, needs to optimize energy. In the present study, the atmospheric distillation unit of a refinery has been selected as a case study. Using a new method of material flow cost, determining the positive and negative products and their actual valuation, the share of various costs in the unit has been demonstrated. Since about 99.3% of the total costs in this unit are related to the cost of purchasing crude oil as feedstock, the importance of purchasing crude oil in the event of crisis management and the conditions of alternatives are fully characterized. Three crude oils named Maroon, Dezful, and Mansouri were studied as alternatives for Ahwaz crude oil. The results of Maroon crude oil show that, in the same operating conditions, its substitution as the main feedstock obtains the same quality products as Ahvaz crude oil products. The products derived from Dezful crude oil shows a difference of approximately 7 to 8 degrees API. Products from Mansouri crude oil have a difference of between 20°C and 40°C at boiling point and a difference of 5° to 7°API, and with increasing temperature and feed pressure, there is no significant change in the quality of the products. The mixture of Mansouri and Dezful crude oil separately with Ahwaz crude oil does not achieve the desired quality. But proper quality can be obtained by applying changes of 10 °C to 30 °C at inlet temperature, and from 0.5 to 0.7 kg/cm2 at the pressure. Due to the same price of Ahwaz and Maroon and Dezful, there is no change in the cost of purchasing, and products of the same cost are obtained. refinery atmospheric distillation tower simulation mfca positive products reduce loss Chemical engineering Chemistry Elham Mahmoudi verfasserin aut Esmaeil Fatehifar verfasserin aut Ali Reza Motavalli verfasserin aut In Iranian Journal of Chemistry & Chemical Engineering Iranian Institute of Research and Development in Chemical Industries (IRDCI)-ACECR, 2020 39(2020), 6, Seite 215-227 (DE-627)501417176 (DE-600)2206335-3 10219986 nnns volume:39 year:2020 number:6 pages:215-227 https://doi.org/10.30492/ijcce.2019.36239 kostenfrei https://doaj.org/article/1c6c4bfe2d3344ee83ab727ba2fc2f37 kostenfrei http://www.ijcce.ac.ir/article_36239_f877f616345454931854ff97b8dc72d3.pdf kostenfrei https://doaj.org/toc/1021-9986 Journal toc kostenfrei https://doaj.org/toc/1021-9986 Journal toc kostenfrei GBV_USEFLAG_A SYSFLAG_A GBV_DOAJ GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_95 GBV_ILN_105 GBV_ILN_110 GBV_ILN_151 GBV_ILN_161 GBV_ILN_170 GBV_ILN_213 GBV_ILN_230 GBV_ILN_285 GBV_ILN_293 GBV_ILN_602 GBV_ILN_2014 GBV_ILN_4012 GBV_ILN_4037 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4249 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4335 GBV_ILN_4338 GBV_ILN_4367 GBV_ILN_4700 AR 39 2020 6 215-227 |
allfieldsGer |
10.30492/ijcce.2019.36239 doi (DE-627)DOAJ070216126 (DE-599)DOAJ1c6c4bfe2d3344ee83ab727ba2fc2f37 DE-627 ger DE-627 rakwb eng TP155-156 QD1-999 Asadollah Karimi verfasserin aut Influence of Crude Oil Type on Products Quality of the Atmospheric Distillation Unit by Applying Material Flow Cost Accounting Simulation: Part A 2020 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier The oil refining industry, as one of the most important sources of supply for the people of the world, needs to optimize energy. In the present study, the atmospheric distillation unit of a refinery has been selected as a case study. Using a new method of material flow cost, determining the positive and negative products and their actual valuation, the share of various costs in the unit has been demonstrated. Since about 99.3% of the total costs in this unit are related to the cost of purchasing crude oil as feedstock, the importance of purchasing crude oil in the event of crisis management and the conditions of alternatives are fully characterized. Three crude oils named Maroon, Dezful, and Mansouri were studied as alternatives for Ahwaz crude oil. The results of Maroon crude oil show that, in the same operating conditions, its substitution as the main feedstock obtains the same quality products as Ahvaz crude oil products. The products derived from Dezful crude oil shows a difference of approximately 7 to 8 degrees API. Products from Mansouri crude oil have a difference of between 20°C and 40°C at boiling point and a difference of 5° to 7°API, and with increasing temperature and feed pressure, there is no significant change in the quality of the products. The mixture of Mansouri and Dezful crude oil separately with Ahwaz crude oil does not achieve the desired quality. But proper quality can be obtained by applying changes of 10 °C to 30 °C at inlet temperature, and from 0.5 to 0.7 kg/cm2 at the pressure. Due to the same price of Ahwaz and Maroon and Dezful, there is no change in the cost of purchasing, and products of the same cost are obtained. refinery atmospheric distillation tower simulation mfca positive products reduce loss Chemical engineering Chemistry Elham Mahmoudi verfasserin aut Esmaeil Fatehifar verfasserin aut Ali Reza Motavalli verfasserin aut In Iranian Journal of Chemistry & Chemical Engineering Iranian Institute of Research and Development in Chemical Industries (IRDCI)-ACECR, 2020 39(2020), 6, Seite 215-227 (DE-627)501417176 (DE-600)2206335-3 10219986 nnns volume:39 year:2020 number:6 pages:215-227 https://doi.org/10.30492/ijcce.2019.36239 kostenfrei https://doaj.org/article/1c6c4bfe2d3344ee83ab727ba2fc2f37 kostenfrei http://www.ijcce.ac.ir/article_36239_f877f616345454931854ff97b8dc72d3.pdf kostenfrei https://doaj.org/toc/1021-9986 Journal toc kostenfrei https://doaj.org/toc/1021-9986 Journal toc kostenfrei GBV_USEFLAG_A SYSFLAG_A GBV_DOAJ GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_95 GBV_ILN_105 GBV_ILN_110 GBV_ILN_151 GBV_ILN_161 GBV_ILN_170 GBV_ILN_213 GBV_ILN_230 GBV_ILN_285 GBV_ILN_293 GBV_ILN_602 GBV_ILN_2014 GBV_ILN_4012 GBV_ILN_4037 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4249 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4335 GBV_ILN_4338 GBV_ILN_4367 GBV_ILN_4700 AR 39 2020 6 215-227 |
allfieldsSound |
10.30492/ijcce.2019.36239 doi (DE-627)DOAJ070216126 (DE-599)DOAJ1c6c4bfe2d3344ee83ab727ba2fc2f37 DE-627 ger DE-627 rakwb eng TP155-156 QD1-999 Asadollah Karimi verfasserin aut Influence of Crude Oil Type on Products Quality of the Atmospheric Distillation Unit by Applying Material Flow Cost Accounting Simulation: Part A 2020 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier The oil refining industry, as one of the most important sources of supply for the people of the world, needs to optimize energy. In the present study, the atmospheric distillation unit of a refinery has been selected as a case study. Using a new method of material flow cost, determining the positive and negative products and their actual valuation, the share of various costs in the unit has been demonstrated. Since about 99.3% of the total costs in this unit are related to the cost of purchasing crude oil as feedstock, the importance of purchasing crude oil in the event of crisis management and the conditions of alternatives are fully characterized. Three crude oils named Maroon, Dezful, and Mansouri were studied as alternatives for Ahwaz crude oil. The results of Maroon crude oil show that, in the same operating conditions, its substitution as the main feedstock obtains the same quality products as Ahvaz crude oil products. The products derived from Dezful crude oil shows a difference of approximately 7 to 8 degrees API. Products from Mansouri crude oil have a difference of between 20°C and 40°C at boiling point and a difference of 5° to 7°API, and with increasing temperature and feed pressure, there is no significant change in the quality of the products. The mixture of Mansouri and Dezful crude oil separately with Ahwaz crude oil does not achieve the desired quality. But proper quality can be obtained by applying changes of 10 °C to 30 °C at inlet temperature, and from 0.5 to 0.7 kg/cm2 at the pressure. Due to the same price of Ahwaz and Maroon and Dezful, there is no change in the cost of purchasing, and products of the same cost are obtained. refinery atmospheric distillation tower simulation mfca positive products reduce loss Chemical engineering Chemistry Elham Mahmoudi verfasserin aut Esmaeil Fatehifar verfasserin aut Ali Reza Motavalli verfasserin aut In Iranian Journal of Chemistry & Chemical Engineering Iranian Institute of Research and Development in Chemical Industries (IRDCI)-ACECR, 2020 39(2020), 6, Seite 215-227 (DE-627)501417176 (DE-600)2206335-3 10219986 nnns volume:39 year:2020 number:6 pages:215-227 https://doi.org/10.30492/ijcce.2019.36239 kostenfrei https://doaj.org/article/1c6c4bfe2d3344ee83ab727ba2fc2f37 kostenfrei http://www.ijcce.ac.ir/article_36239_f877f616345454931854ff97b8dc72d3.pdf kostenfrei https://doaj.org/toc/1021-9986 Journal toc kostenfrei https://doaj.org/toc/1021-9986 Journal toc kostenfrei GBV_USEFLAG_A SYSFLAG_A GBV_DOAJ GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_95 GBV_ILN_105 GBV_ILN_110 GBV_ILN_151 GBV_ILN_161 GBV_ILN_170 GBV_ILN_213 GBV_ILN_230 GBV_ILN_285 GBV_ILN_293 GBV_ILN_602 GBV_ILN_2014 GBV_ILN_4012 GBV_ILN_4037 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4249 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4335 GBV_ILN_4338 GBV_ILN_4367 GBV_ILN_4700 AR 39 2020 6 215-227 |
language |
English |
source |
In Iranian Journal of Chemistry & Chemical Engineering 39(2020), 6, Seite 215-227 volume:39 year:2020 number:6 pages:215-227 |
sourceStr |
In Iranian Journal of Chemistry & Chemical Engineering 39(2020), 6, Seite 215-227 volume:39 year:2020 number:6 pages:215-227 |
format_phy_str_mv |
Article |
institution |
findex.gbv.de |
topic_facet |
refinery atmospheric distillation tower simulation mfca positive products reduce loss Chemical engineering Chemistry |
isfreeaccess_bool |
true |
container_title |
Iranian Journal of Chemistry & Chemical Engineering |
authorswithroles_txt_mv |
Asadollah Karimi @@aut@@ Elham Mahmoudi @@aut@@ Esmaeil Fatehifar @@aut@@ Ali Reza Motavalli @@aut@@ |
publishDateDaySort_date |
2020-01-01T00:00:00Z |
hierarchy_top_id |
501417176 |
id |
DOAJ070216126 |
language_de |
englisch |
fullrecord |
<?xml version="1.0" encoding="UTF-8"?><collection xmlns="http://www.loc.gov/MARC21/slim"><record><leader>01000caa a22002652 4500</leader><controlfield tag="001">DOAJ070216126</controlfield><controlfield tag="003">DE-627</controlfield><controlfield tag="005">20230309091647.0</controlfield><controlfield tag="007">cr uuu---uuuuu</controlfield><controlfield tag="008">230228s2020 xx |||||o 00| ||eng c</controlfield><datafield tag="024" ind1="7" ind2=" "><subfield code="a">10.30492/ijcce.2019.36239</subfield><subfield code="2">doi</subfield></datafield><datafield tag="035" ind1=" " ind2=" "><subfield code="a">(DE-627)DOAJ070216126</subfield></datafield><datafield tag="035" ind1=" " ind2=" "><subfield code="a">(DE-599)DOAJ1c6c4bfe2d3344ee83ab727ba2fc2f37</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="050" ind1=" " ind2="0"><subfield code="a">TP155-156</subfield></datafield><datafield tag="050" ind1=" " ind2="0"><subfield code="a">QD1-999</subfield></datafield><datafield tag="100" ind1="0" ind2=" "><subfield code="a">Asadollah Karimi</subfield><subfield code="e">verfasserin</subfield><subfield code="4">aut</subfield></datafield><datafield tag="245" ind1="1" ind2="0"><subfield code="a">Influence of Crude Oil Type on Products Quality of the Atmospheric Distillation Unit by Applying Material Flow Cost Accounting Simulation: Part A</subfield></datafield><datafield tag="264" ind1=" " ind2="1"><subfield code="c">2020</subfield></datafield><datafield tag="336" ind1=" " ind2=" "><subfield code="a">Text</subfield><subfield code="b">txt</subfield><subfield code="2">rdacontent</subfield></datafield><datafield tag="337" ind1=" " ind2=" "><subfield code="a">Computermedien</subfield><subfield code="b">c</subfield><subfield code="2">rdamedia</subfield></datafield><datafield tag="338" ind1=" " ind2=" "><subfield code="a">Online-Ressource</subfield><subfield code="b">cr</subfield><subfield code="2">rdacarrier</subfield></datafield><datafield tag="520" ind1=" " ind2=" "><subfield code="a">The oil refining industry, as one of the most important sources of supply for the people of the world, needs to optimize energy. In the present study, the atmospheric distillation unit of a refinery has been selected as a case study. Using a new method of material flow cost, determining the positive and negative products and their actual valuation, the share of various costs in the unit has been demonstrated. Since about 99.3% of the total costs in this unit are related to the cost of purchasing crude oil as feedstock, the importance of purchasing crude oil in the event of crisis management and the conditions of alternatives are fully characterized. Three crude oils named Maroon, Dezful, and Mansouri were studied as alternatives for Ahwaz crude oil. The results of Maroon crude oil show that, in the same operating conditions, its substitution as the main feedstock obtains the same quality products as Ahvaz crude oil products. The products derived from Dezful crude oil shows a difference of approximately 7 to 8 degrees API. Products from Mansouri crude oil have a difference of between 20°C and 40°C at boiling point and a difference of 5° to 7°API, and with increasing temperature and feed pressure, there is no significant change in the quality of the products. The mixture of Mansouri and Dezful crude oil separately with Ahwaz crude oil does not achieve the desired quality. But proper quality can be obtained by applying changes of 10 °C to 30 °C at inlet temperature, and from 0.5 to 0.7 kg/cm2 at the pressure. Due to the same price of Ahwaz and Maroon and Dezful, there is no change in the cost of purchasing, and products of the same cost are obtained.</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">refinery</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">atmospheric distillation tower</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">simulation</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">mfca</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">positive products</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">reduce loss</subfield></datafield><datafield tag="653" ind1=" " ind2="0"><subfield code="a">Chemical engineering</subfield></datafield><datafield tag="653" ind1=" " ind2="0"><subfield code="a">Chemistry</subfield></datafield><datafield tag="700" ind1="0" ind2=" "><subfield code="a">Elham Mahmoudi</subfield><subfield code="e">verfasserin</subfield><subfield code="4">aut</subfield></datafield><datafield tag="700" ind1="0" ind2=" "><subfield code="a">Esmaeil Fatehifar</subfield><subfield code="e">verfasserin</subfield><subfield code="4">aut</subfield></datafield><datafield tag="700" ind1="0" ind2=" "><subfield code="a">Ali Reza Motavalli</subfield><subfield code="e">verfasserin</subfield><subfield code="4">aut</subfield></datafield><datafield tag="773" ind1="0" ind2="8"><subfield code="i">In</subfield><subfield code="t">Iranian Journal of Chemistry & Chemical Engineering</subfield><subfield code="d">Iranian Institute of Research and Development in Chemical Industries (IRDCI)-ACECR, 2020</subfield><subfield code="g">39(2020), 6, Seite 215-227</subfield><subfield code="w">(DE-627)501417176</subfield><subfield code="w">(DE-600)2206335-3</subfield><subfield code="x">10219986</subfield><subfield code="7">nnns</subfield></datafield><datafield tag="773" ind1="1" ind2="8"><subfield code="g">volume:39</subfield><subfield code="g">year:2020</subfield><subfield code="g">number:6</subfield><subfield code="g">pages:215-227</subfield></datafield><datafield tag="856" ind1="4" ind2="0"><subfield code="u">https://doi.org/10.30492/ijcce.2019.36239</subfield><subfield code="z">kostenfrei</subfield></datafield><datafield tag="856" ind1="4" ind2="0"><subfield code="u">https://doaj.org/article/1c6c4bfe2d3344ee83ab727ba2fc2f37</subfield><subfield code="z">kostenfrei</subfield></datafield><datafield tag="856" ind1="4" ind2="0"><subfield code="u">http://www.ijcce.ac.ir/article_36239_f877f616345454931854ff97b8dc72d3.pdf</subfield><subfield code="z">kostenfrei</subfield></datafield><datafield tag="856" ind1="4" ind2="2"><subfield code="u">https://doaj.org/toc/1021-9986</subfield><subfield code="y">Journal toc</subfield><subfield code="z">kostenfrei</subfield></datafield><datafield tag="856" ind1="4" ind2="2"><subfield code="u">https://doaj.org/toc/1021-9986</subfield><subfield code="y">Journal toc</subfield><subfield code="z">kostenfrei</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_USEFLAG_A</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">SYSFLAG_A</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_DOAJ</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_20</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_22</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_23</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_24</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_39</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_40</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_60</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_62</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_63</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_65</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_69</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_70</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_73</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_95</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_105</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_110</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_151</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_161</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_170</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_213</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_230</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_285</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_293</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_602</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_2014</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_4012</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_4037</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_4112</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_4125</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_4126</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_4249</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_4305</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_4306</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_4307</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_4313</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_4322</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_4323</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_4324</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_4325</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_4335</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_4338</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_4367</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_4700</subfield></datafield><datafield tag="951" ind1=" " ind2=" "><subfield code="a">AR</subfield></datafield><datafield tag="952" ind1=" " ind2=" "><subfield code="d">39</subfield><subfield code="j">2020</subfield><subfield code="e">6</subfield><subfield code="h">215-227</subfield></datafield></record></collection>
|
callnumber-first |
T - Technology |
author |
Asadollah Karimi |
spellingShingle |
Asadollah Karimi misc TP155-156 misc QD1-999 misc refinery misc atmospheric distillation tower misc simulation misc mfca misc positive products misc reduce loss misc Chemical engineering misc Chemistry Influence of Crude Oil Type on Products Quality of the Atmospheric Distillation Unit by Applying Material Flow Cost Accounting Simulation: Part A |
authorStr |
Asadollah Karimi |
ppnlink_with_tag_str_mv |
@@773@@(DE-627)501417176 |
format |
electronic Article |
delete_txt_mv |
keep |
author_role |
aut aut aut aut |
collection |
DOAJ |
remote_str |
true |
callnumber-label |
TP155-156 |
illustrated |
Not Illustrated |
issn |
10219986 |
topic_title |
TP155-156 QD1-999 Influence of Crude Oil Type on Products Quality of the Atmospheric Distillation Unit by Applying Material Flow Cost Accounting Simulation: Part A refinery atmospheric distillation tower simulation mfca positive products reduce loss |
topic |
misc TP155-156 misc QD1-999 misc refinery misc atmospheric distillation tower misc simulation misc mfca misc positive products misc reduce loss misc Chemical engineering misc Chemistry |
topic_unstemmed |
misc TP155-156 misc QD1-999 misc refinery misc atmospheric distillation tower misc simulation misc mfca misc positive products misc reduce loss misc Chemical engineering misc Chemistry |
topic_browse |
misc TP155-156 misc QD1-999 misc refinery misc atmospheric distillation tower misc simulation misc mfca misc positive products misc reduce loss misc Chemical engineering misc Chemistry |
format_facet |
Elektronische Aufsätze Aufsätze Elektronische Ressource |
format_main_str_mv |
Text Zeitschrift/Artikel |
carriertype_str_mv |
cr |
hierarchy_parent_title |
Iranian Journal of Chemistry & Chemical Engineering |
hierarchy_parent_id |
501417176 |
hierarchy_top_title |
Iranian Journal of Chemistry & Chemical Engineering |
isfreeaccess_txt |
true |
familylinks_str_mv |
(DE-627)501417176 (DE-600)2206335-3 |
title |
Influence of Crude Oil Type on Products Quality of the Atmospheric Distillation Unit by Applying Material Flow Cost Accounting Simulation: Part A |
ctrlnum |
(DE-627)DOAJ070216126 (DE-599)DOAJ1c6c4bfe2d3344ee83ab727ba2fc2f37 |
title_full |
Influence of Crude Oil Type on Products Quality of the Atmospheric Distillation Unit by Applying Material Flow Cost Accounting Simulation: Part A |
author_sort |
Asadollah Karimi |
journal |
Iranian Journal of Chemistry & Chemical Engineering |
journalStr |
Iranian Journal of Chemistry & Chemical Engineering |
callnumber-first-code |
T |
lang_code |
eng |
isOA_bool |
true |
recordtype |
marc |
publishDateSort |
2020 |
contenttype_str_mv |
txt |
container_start_page |
215 |
author_browse |
Asadollah Karimi Elham Mahmoudi Esmaeil Fatehifar Ali Reza Motavalli |
container_volume |
39 |
class |
TP155-156 QD1-999 |
format_se |
Elektronische Aufsätze |
author-letter |
Asadollah Karimi |
doi_str_mv |
10.30492/ijcce.2019.36239 |
author2-role |
verfasserin |
title_sort |
influence of crude oil type on products quality of the atmospheric distillation unit by applying material flow cost accounting simulation: part a |
callnumber |
TP155-156 |
title_auth |
Influence of Crude Oil Type on Products Quality of the Atmospheric Distillation Unit by Applying Material Flow Cost Accounting Simulation: Part A |
abstract |
The oil refining industry, as one of the most important sources of supply for the people of the world, needs to optimize energy. In the present study, the atmospheric distillation unit of a refinery has been selected as a case study. Using a new method of material flow cost, determining the positive and negative products and their actual valuation, the share of various costs in the unit has been demonstrated. Since about 99.3% of the total costs in this unit are related to the cost of purchasing crude oil as feedstock, the importance of purchasing crude oil in the event of crisis management and the conditions of alternatives are fully characterized. Three crude oils named Maroon, Dezful, and Mansouri were studied as alternatives for Ahwaz crude oil. The results of Maroon crude oil show that, in the same operating conditions, its substitution as the main feedstock obtains the same quality products as Ahvaz crude oil products. The products derived from Dezful crude oil shows a difference of approximately 7 to 8 degrees API. Products from Mansouri crude oil have a difference of between 20°C and 40°C at boiling point and a difference of 5° to 7°API, and with increasing temperature and feed pressure, there is no significant change in the quality of the products. The mixture of Mansouri and Dezful crude oil separately with Ahwaz crude oil does not achieve the desired quality. But proper quality can be obtained by applying changes of 10 °C to 30 °C at inlet temperature, and from 0.5 to 0.7 kg/cm2 at the pressure. Due to the same price of Ahwaz and Maroon and Dezful, there is no change in the cost of purchasing, and products of the same cost are obtained. |
abstractGer |
The oil refining industry, as one of the most important sources of supply for the people of the world, needs to optimize energy. In the present study, the atmospheric distillation unit of a refinery has been selected as a case study. Using a new method of material flow cost, determining the positive and negative products and their actual valuation, the share of various costs in the unit has been demonstrated. Since about 99.3% of the total costs in this unit are related to the cost of purchasing crude oil as feedstock, the importance of purchasing crude oil in the event of crisis management and the conditions of alternatives are fully characterized. Three crude oils named Maroon, Dezful, and Mansouri were studied as alternatives for Ahwaz crude oil. The results of Maroon crude oil show that, in the same operating conditions, its substitution as the main feedstock obtains the same quality products as Ahvaz crude oil products. The products derived from Dezful crude oil shows a difference of approximately 7 to 8 degrees API. Products from Mansouri crude oil have a difference of between 20°C and 40°C at boiling point and a difference of 5° to 7°API, and with increasing temperature and feed pressure, there is no significant change in the quality of the products. The mixture of Mansouri and Dezful crude oil separately with Ahwaz crude oil does not achieve the desired quality. But proper quality can be obtained by applying changes of 10 °C to 30 °C at inlet temperature, and from 0.5 to 0.7 kg/cm2 at the pressure. Due to the same price of Ahwaz and Maroon and Dezful, there is no change in the cost of purchasing, and products of the same cost are obtained. |
abstract_unstemmed |
The oil refining industry, as one of the most important sources of supply for the people of the world, needs to optimize energy. In the present study, the atmospheric distillation unit of a refinery has been selected as a case study. Using a new method of material flow cost, determining the positive and negative products and their actual valuation, the share of various costs in the unit has been demonstrated. Since about 99.3% of the total costs in this unit are related to the cost of purchasing crude oil as feedstock, the importance of purchasing crude oil in the event of crisis management and the conditions of alternatives are fully characterized. Three crude oils named Maroon, Dezful, and Mansouri were studied as alternatives for Ahwaz crude oil. The results of Maroon crude oil show that, in the same operating conditions, its substitution as the main feedstock obtains the same quality products as Ahvaz crude oil products. The products derived from Dezful crude oil shows a difference of approximately 7 to 8 degrees API. Products from Mansouri crude oil have a difference of between 20°C and 40°C at boiling point and a difference of 5° to 7°API, and with increasing temperature and feed pressure, there is no significant change in the quality of the products. The mixture of Mansouri and Dezful crude oil separately with Ahwaz crude oil does not achieve the desired quality. But proper quality can be obtained by applying changes of 10 °C to 30 °C at inlet temperature, and from 0.5 to 0.7 kg/cm2 at the pressure. Due to the same price of Ahwaz and Maroon and Dezful, there is no change in the cost of purchasing, and products of the same cost are obtained. |
collection_details |
GBV_USEFLAG_A SYSFLAG_A GBV_DOAJ GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_95 GBV_ILN_105 GBV_ILN_110 GBV_ILN_151 GBV_ILN_161 GBV_ILN_170 GBV_ILN_213 GBV_ILN_230 GBV_ILN_285 GBV_ILN_293 GBV_ILN_602 GBV_ILN_2014 GBV_ILN_4012 GBV_ILN_4037 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4249 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4335 GBV_ILN_4338 GBV_ILN_4367 GBV_ILN_4700 |
container_issue |
6 |
title_short |
Influence of Crude Oil Type on Products Quality of the Atmospheric Distillation Unit by Applying Material Flow Cost Accounting Simulation: Part A |
url |
https://doi.org/10.30492/ijcce.2019.36239 https://doaj.org/article/1c6c4bfe2d3344ee83ab727ba2fc2f37 http://www.ijcce.ac.ir/article_36239_f877f616345454931854ff97b8dc72d3.pdf https://doaj.org/toc/1021-9986 |
remote_bool |
true |
author2 |
Elham Mahmoudi Esmaeil Fatehifar Ali Reza Motavalli |
author2Str |
Elham Mahmoudi Esmaeil Fatehifar Ali Reza Motavalli |
ppnlink |
501417176 |
callnumber-subject |
TP - Chemical Technology |
mediatype_str_mv |
c |
isOA_txt |
true |
hochschulschrift_bool |
false |
doi_str |
10.30492/ijcce.2019.36239 |
callnumber-a |
TP155-156 |
up_date |
2024-07-03T13:38:04.378Z |
_version_ |
1803565278828691457 |
fullrecord_marcxml |
<?xml version="1.0" encoding="UTF-8"?><collection xmlns="http://www.loc.gov/MARC21/slim"><record><leader>01000caa a22002652 4500</leader><controlfield tag="001">DOAJ070216126</controlfield><controlfield tag="003">DE-627</controlfield><controlfield tag="005">20230309091647.0</controlfield><controlfield tag="007">cr uuu---uuuuu</controlfield><controlfield tag="008">230228s2020 xx |||||o 00| ||eng c</controlfield><datafield tag="024" ind1="7" ind2=" "><subfield code="a">10.30492/ijcce.2019.36239</subfield><subfield code="2">doi</subfield></datafield><datafield tag="035" ind1=" " ind2=" "><subfield code="a">(DE-627)DOAJ070216126</subfield></datafield><datafield tag="035" ind1=" " ind2=" "><subfield code="a">(DE-599)DOAJ1c6c4bfe2d3344ee83ab727ba2fc2f37</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="050" ind1=" " ind2="0"><subfield code="a">TP155-156</subfield></datafield><datafield tag="050" ind1=" " ind2="0"><subfield code="a">QD1-999</subfield></datafield><datafield tag="100" ind1="0" ind2=" "><subfield code="a">Asadollah Karimi</subfield><subfield code="e">verfasserin</subfield><subfield code="4">aut</subfield></datafield><datafield tag="245" ind1="1" ind2="0"><subfield code="a">Influence of Crude Oil Type on Products Quality of the Atmospheric Distillation Unit by Applying Material Flow Cost Accounting Simulation: Part A</subfield></datafield><datafield tag="264" ind1=" " ind2="1"><subfield code="c">2020</subfield></datafield><datafield tag="336" ind1=" " ind2=" "><subfield code="a">Text</subfield><subfield code="b">txt</subfield><subfield code="2">rdacontent</subfield></datafield><datafield tag="337" ind1=" " ind2=" "><subfield code="a">Computermedien</subfield><subfield code="b">c</subfield><subfield code="2">rdamedia</subfield></datafield><datafield tag="338" ind1=" " ind2=" "><subfield code="a">Online-Ressource</subfield><subfield code="b">cr</subfield><subfield code="2">rdacarrier</subfield></datafield><datafield tag="520" ind1=" " ind2=" "><subfield code="a">The oil refining industry, as one of the most important sources of supply for the people of the world, needs to optimize energy. In the present study, the atmospheric distillation unit of a refinery has been selected as a case study. Using a new method of material flow cost, determining the positive and negative products and their actual valuation, the share of various costs in the unit has been demonstrated. Since about 99.3% of the total costs in this unit are related to the cost of purchasing crude oil as feedstock, the importance of purchasing crude oil in the event of crisis management and the conditions of alternatives are fully characterized. Three crude oils named Maroon, Dezful, and Mansouri were studied as alternatives for Ahwaz crude oil. The results of Maroon crude oil show that, in the same operating conditions, its substitution as the main feedstock obtains the same quality products as Ahvaz crude oil products. The products derived from Dezful crude oil shows a difference of approximately 7 to 8 degrees API. Products from Mansouri crude oil have a difference of between 20°C and 40°C at boiling point and a difference of 5° to 7°API, and with increasing temperature and feed pressure, there is no significant change in the quality of the products. The mixture of Mansouri and Dezful crude oil separately with Ahwaz crude oil does not achieve the desired quality. But proper quality can be obtained by applying changes of 10 °C to 30 °C at inlet temperature, and from 0.5 to 0.7 kg/cm2 at the pressure. Due to the same price of Ahwaz and Maroon and Dezful, there is no change in the cost of purchasing, and products of the same cost are obtained.</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">refinery</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">atmospheric distillation tower</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">simulation</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">mfca</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">positive products</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">reduce loss</subfield></datafield><datafield tag="653" ind1=" " ind2="0"><subfield code="a">Chemical engineering</subfield></datafield><datafield tag="653" ind1=" " ind2="0"><subfield code="a">Chemistry</subfield></datafield><datafield tag="700" ind1="0" ind2=" "><subfield code="a">Elham Mahmoudi</subfield><subfield code="e">verfasserin</subfield><subfield code="4">aut</subfield></datafield><datafield tag="700" ind1="0" ind2=" "><subfield code="a">Esmaeil Fatehifar</subfield><subfield code="e">verfasserin</subfield><subfield code="4">aut</subfield></datafield><datafield tag="700" ind1="0" ind2=" "><subfield code="a">Ali Reza Motavalli</subfield><subfield code="e">verfasserin</subfield><subfield code="4">aut</subfield></datafield><datafield tag="773" ind1="0" ind2="8"><subfield code="i">In</subfield><subfield code="t">Iranian Journal of Chemistry & Chemical Engineering</subfield><subfield code="d">Iranian Institute of Research and Development in Chemical Industries (IRDCI)-ACECR, 2020</subfield><subfield code="g">39(2020), 6, Seite 215-227</subfield><subfield code="w">(DE-627)501417176</subfield><subfield code="w">(DE-600)2206335-3</subfield><subfield code="x">10219986</subfield><subfield code="7">nnns</subfield></datafield><datafield tag="773" ind1="1" ind2="8"><subfield code="g">volume:39</subfield><subfield code="g">year:2020</subfield><subfield code="g">number:6</subfield><subfield code="g">pages:215-227</subfield></datafield><datafield tag="856" ind1="4" ind2="0"><subfield code="u">https://doi.org/10.30492/ijcce.2019.36239</subfield><subfield code="z">kostenfrei</subfield></datafield><datafield tag="856" ind1="4" ind2="0"><subfield code="u">https://doaj.org/article/1c6c4bfe2d3344ee83ab727ba2fc2f37</subfield><subfield code="z">kostenfrei</subfield></datafield><datafield tag="856" ind1="4" ind2="0"><subfield code="u">http://www.ijcce.ac.ir/article_36239_f877f616345454931854ff97b8dc72d3.pdf</subfield><subfield code="z">kostenfrei</subfield></datafield><datafield tag="856" ind1="4" ind2="2"><subfield code="u">https://doaj.org/toc/1021-9986</subfield><subfield code="y">Journal toc</subfield><subfield code="z">kostenfrei</subfield></datafield><datafield tag="856" ind1="4" ind2="2"><subfield code="u">https://doaj.org/toc/1021-9986</subfield><subfield code="y">Journal toc</subfield><subfield code="z">kostenfrei</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_USEFLAG_A</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">SYSFLAG_A</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_DOAJ</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_20</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_22</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_23</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_24</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_39</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_40</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_60</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_62</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_63</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_65</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_69</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_70</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_73</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_95</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_105</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_110</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_151</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_161</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_170</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_213</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_230</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_285</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_293</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_602</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_2014</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_4012</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_4037</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_4112</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_4125</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_4126</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_4249</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_4305</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_4306</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_4307</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_4313</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_4322</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_4323</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_4324</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_4325</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_4335</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_4338</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_4367</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_4700</subfield></datafield><datafield tag="951" ind1=" " ind2=" "><subfield code="a">AR</subfield></datafield><datafield tag="952" ind1=" " ind2=" "><subfield code="d">39</subfield><subfield code="j">2020</subfield><subfield code="e">6</subfield><subfield code="h">215-227</subfield></datafield></record></collection>
|
score |
7.400141 |