Acid assisted-hydrothermal carbonization of solid waste from essential oils industry: Optimization using I-optimal experimental design and removal dye application

被引:16
作者
El Ouadrhiri, Faical [1 ]
Saleh, Ebraheem Abdu Musad [2 ]
Husain, Kakul [2 ]
Adachi, Abderrazzak [1 ]
Hmamou, Anouar [1 ]
Hassan, Ismail [2 ]
Moharam, Marwa Mostafa [2 ,3 ]
Lahkimi, Amal
机构
[1] Sidi Mohamed Ben Abdellah Univ, Fac Sci Dhar El Mehraz, Lab Engn Mol Organometall Mat & Environm, Fes, Morocco
[2] Prince Sattam Bin Abdulaziz Univ, Coll Arts & Sci, Chem Dept, Wadi Al Dawaser, Alkharj, Saudi Arabia
[3] Cent Met Res & Dev Inst CMRDI, Chem & Electrochem Proc Dept, POB 87, Helwan 11421, Egypt
关键词
Solid waste essential oil extraction industry; Catalytic Hydrothermal car-bonization; I-optimal Design; Response surface methodol-ogy; Dye Adsorption; ACTIVATED CARBON; METHYLENE-BLUE; INTRAPARTICLE DIFFUSION; CHEMICAL ACTIVATION; ADSORPTION; BIOMASS; HYDROCHAR; EQUILIBRIUM; MECHANISM; WATER;
D O I
10.1016/j.arabjc.2023.104872
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
Solid waste (SW) generated from extracting of essential oils from medicinal and aromatic plants (MAPs) is an abundant and renewable resource, but proper recycling is necessary to prevent negative environmental impacts from improper disposal. This study focused on converting SW from essential oil (EO) extraction industry by citric acid-catalyzed hydrothermal carbonization (c-HTC) coupled with chemical activation into a carbonaceous material to remove organic pollu-tants. For this purpose, an I -optimal design coupled with response surface methodology (RSM) was developed to investigate the relationship between the severity factor (SF) of the c-HTC process and citric acid dose (HTCcat) on carbon retention rate (CRR) and hydrochar mass yield (MY). Under optimal conditions (5.32 and 2 g for SF and HTCcat, respectively), an optimized hydrochar (HCop) was characterized by a CRR and MY of 71.02% and 56.14%, respectively. HCop was chem-ically activated by KOH solution (AHCop) and characterized by a specific surface area of 989.81 m2. g_1 , a pore volume of 0.583 cm3.g-1, a higher heating value (HHV) of 37.3 MJ/Kg, oxygenated sur-
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页数:19
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