Techno-economic evaluation of methanol production via gasification of vacuum residue and conventional reforming routes

被引:13
作者
Al-Rowaili, Fayez Nasir [1 ,2 ]
Khalafalla, Siddig S. [1 ]
Al-Yami, Dhaffer S. [2 ]
Jamal, Aqil [2 ]
Ahmed, Usama [1 ,3 ]
Zahid, Umer [1 ,4 ]
Al-Mutairi, Eid M. [1 ,5 ]
机构
[1] King Fahd Univ Petr & Minerals, Chem Engn Dept, Dhahran 31261, Saudi Arabia
[2] Saudi Aramco, Res & Dev Ctr, Dhahran 31311, Saudi Arabia
[3] King Fahd Univ Petr & Minerals, Interdisciplinary Res Ctr Hydrogen & Energy Stora, Dhahran 31261, Saudi Arabia
[4] King Fahd Univ Petr & Minerals, Interdisciplinary Res Ctr Membranes & Water Secur, Dhahran 31261, Saudi Arabia
[5] King Fahd Univ Petr & Minerals, Interdisciplinary Res Ctr Refining & Adv Chem, Dhahran 31261, Saudi Arabia
关键词
Methanol; Carbon capture and utilization; Vacuum residue gasification; Economic analysis; Process simulation; NATURAL-GAS; HYDROGEN-PRODUCTION; FUEL-OIL; SIMULATION; CO2; OPTIMIZATION;
D O I
10.1016/j.cherd.2021.11.004
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The continuous rise of global carbon emissions demands the utilization of fossil fuels in a cleaner and sustainable way. Gasification is a potential technology that can convert the dirty fossil fuels for the production of clean and environment friendly fuels in an economical manner. In this study, vacuum residue is employed as a feedstock to produce high grade methanol. A vacuum residue to methanol (VRTM) process is simulated using Aspen Plus for a methanol production capacity of 90 t/h with 99.9 wt.% purity. The developed VRTM process is bench-marked with the conventional steam reforming to methanol (SRTM) process through energy, environmental and economic analysis. The performance of vacuum residue gasifier, natural gas reformer and the methanol synthesis reactor are validated against the plant data and the simulation results are found to be in good agreement. The results showed that the VRTM process offers a process energy efficiency of 49.5% which is 1.6% higher than the SRTM process. The unit cost of methanol product from the VRTM process is $ 317/tCH(3)OH which is 14% lower compared to the SRTM process. In terms of environmental analysis, SRTM process emits less carbon emissions than the VRTM process. However, the VRTM process offers a high purity captured CO2 stream that can be utilized for another application that can further offset the methanol production cost. (C) 2021 Institution of Chemical Engineers. Published by Elsevier B.V. All rights reserved.
引用
收藏
页码:365 / 375
页数:11
相关论文
共 42 条
[2]   Design Modification of Acid Gas Cleaning Units for an Enhanced Performance in Natural Gas Processing [J].
Al-Amri, Amr ;
Zahid, Umer .
ENERGY & FUELS, 2020, 34 (02) :2545-2552
[3]   Apparent Kinetics of Co-Gasification of Biomass and Vacuum Gas Oil (VGO) [J].
Al-Attas, Tareq A. ;
Lucky, Rahima A. ;
Hossain, Mohammad M. .
CHEMISTRY-AN ASIAN JOURNAL, 2021, 16 (05) :507-520
[4]   Conceptual design of syngas production by the integration of gasification and dry-reforming technologies with CO2 capture and utilization [J].
Alibrahim, Hussain A. ;
Khalafalla, Siddig S. ;
Ahmed, Usama ;
Park, Seongho ;
Lee, Chul-Jin ;
Zahid, Umer .
ENERGY CONVERSION AND MANAGEMENT, 2021, 244
[5]   Methanol synthesis through CO2 capture and hydrogenation: Thermal integration, energy performance and techno-economic assessment [J].
Battaglia, Patrizio ;
Buffo, Giulio ;
Ferrero, Domenico ;
Santarelli, Massimo ;
Lanzini, Andrea .
JOURNAL OF CO2 UTILIZATION, 2021, 44
[6]   Combustion performance and emissions of petrodiesel and biodiesels based on various vegetable oils in a semi industrial boiler [J].
Bazooyar, Bahamin ;
Ghorbani, Afshin ;
Shariati, Ahmad .
FUEL, 2011, 90 (10) :3078-3092
[7]   A review on the co-processing of biomass with other fuels sources [J].
Biswas, Shelly ;
Sharma, D. K. .
INTERNATIONAL JOURNAL OF GREEN ENERGY, 2021, 18 (08) :793-811
[8]   Synthesis Gas Processes for Methanol Production via CH4 Reforming with CO2, H2O, and O2 [J].
Canete, Benjamin ;
Gigola, Carlos E. ;
Brignole, Nelida B. .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2014, 53 (17) :7103-7112
[9]  
Carlson EC, 1996, CHEM ENG PROG, V92, P35
[10]   Simulation and optimization of hydrogen production by steam reforming of natural gas for refining and petrochemical demands in Lebanon [J].
Chehade, Aya M. El Hajj ;
Daher, Elie A. ;
Assaf, Jean Claude ;
Riachi, Bassam ;
Hamd, Wael .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2020, 45 (58) :33235-33247