Catalytic mechanism of sulfuric acid in cellulose pyrolysis: A combined experimental and computational investigation
Graphical abstract
Introduction
Conventional fast pyrolysis of biomass is a non-selective thermal conversion process to obtain a very complex liquid product known as bio-oil. The complex chemical composition and poor properties of crude bio-oil significantly limit its utilization in current industries [1]. In order to solve this problem, catalytic pyrolysis has been proposed as a promising way to selectively control the biomass pyrolysis process towards specific bio-oils [2,3]. Inorganic acids have been widely utilized to catalyze the biomass pyrolysis process, including H2SO4 [4,5], phosphoric acid (H3PO4) [6,7] and nitric acid (HNO3) [8]. These acid catalysts are very effective to significantly alter the biomass pyrolysis characteristics as well as product distribution, and can be utilized to prepare value-added chemicals [7,8].
H2SO4 is a common strong inorganic acid, and has been widely employed for catalytic pyrolysis of biomass and its primary components (cellulose, hemicellulose and lignin). The catalytic effect of H2SO4 on cellulose pyrolysis has been preliminarily elucidated as summarized by the following three aspects. Firstly, the initial decomposition temperature of cellulose will be significantly decreased by H2SO4. This fact has been confirmed by previous work [[7], [8], [9], [10]] according to TGA studies on the H2SO4 impregnated cellulose. Secondly, the promoting effect of H2SO4 on dehydration and charring reactions changes the yields of solid, liquid and gas products. Char and water yields increase, while that of organic liquid compounds (organic fraction of bio-oil) decreases. Such catalytic effects will be promoted along with the increase of H2SO4 content [[8], [9], [10], [11]]. Thirdly, pyrolytic product composition will also be altered by H2SO4. In regard to the liquid products, H2SO4 can significantly decrease the yield of levoglucosan (LG) which is the typical depolymerized product and also the most abundant pyrolytic product in bio-oil. Meanwhile, yields of several dehydrated products can be increased, such as 1,4:3,6-dianhydro-α-d-glucopyranose (DGP), furfural (FF) and levoglucosenone (LGO). Detailed H2SO4-catalyzed product distribution generally differed in previous studies due to different impregnation methods, pyrolytic conditions and H2SO4 contents [7]. However, the basic conclusions were not controversial based on the fact that H2SO4 could promote dehydration and cross-linking reactions [12].
Currently, the published studies on H2SO4-catalyzed pyrolysis of cellulose mainly paid attention to the catalytic behaviors of H2SO4, neglecting deep insight into the catalytic mechanism. In regard to the catalytic center of H2SO4 (proton or acid ion), different viewpoints were raised. Nimlos et al. [13,14] proposed the proton-catalyzed mechanism for ethanol pyrolytic reactions based on the quantum chemistry calculation. It was found that protonated ethanol/carbohydrates would readily undergo dehydration reactions with relatively low activation energies. On the contrary, Julien et al. [8] regarded that the pyrolysis reactions were mainly catalyzed by the sulfate ion. In comparison of catalytic pyrolysis of cellulose over different inorganic acids [[4], [5], [6], [7], [8]], both similarities and distinctions exist, indicating that both the proton and the acid ion should play vital roles in influencing the pyrolytic reactions of cellulose. In addition, the stability of ions is questionable under a fluent gas condition in the pyrolysis process, especially the carrier gases (usually N2 and He) having low dielectric constants [15]. Therefore, it is necessary to consider the global effect of the acid molecule on the cellulose pyrolysis.
In the present study, catalytic effect of H2SO4 on cellulose pyrolysis was investigated in detail using computational chemistry methods. Three model compounds, i.e.,1,4-dimethyl-glucose, 4-methyl-glucose and 1-methyl-glucose were selected to investigate the effect of H2SO4 on major cellulose initial decomposition reactions, i.e., depolymerization of cellulose chain, bridged dehydration, ring-opening, ring-contraction and dehydration of the free hydroxyl groups, as shown in Fig. 1. Structural analyses and kinetic analyses were conducted based on the computational results. Meanwhile, TGA and Py-GC/MS experiments were performed to combine with the computational investigation to give an insight into the catalytic mechanism of H2SO4 on cellulose pyrolysis.
Section snippets
Materials
Microcrystalline cellulose (Avicel PH-101, Sigma) was employed for the pyrolysis experiments. H2SO4 impregnated cellulose was prepared by the incipient wetness impregnation method [16]. H2SO4 solutions with different concentrations were prepared by adding concentrated H2SO4 (AR, 98%) to different volumes of deionized water. Then 1 g cellulose was added to 3 ml diluted H2SO4 solution to obtain a gel-like paste. The mixture was treated in the KQ-500DE ultrasonic sonicator (Kunshan Utranonis
TGA results
Fig. 3 shows the thermogravimetry (TG) and differential thermogravimetry (DTG) curves of cellulose samples with different H2SO4 contents. The weight loss below 100 °C was attributed to the evaporation of imbibed water [30]. For pure cellulose, the onset temperature of degradation (Tonset) and the temperature of maximum weight loss rate (Tmax) were 300 °C and 348 °C respectively, which were close to the literature results [9,10,30]. When H2SO4 was impregnated on the cellulose, both Tonset and T
Conclusions
In this study, quantum chemistry calculation was performed with 1,4-dimethyl-glucsoe, 4-methyl-glucose and 1-methyl-glucose as the cellulose model compounds to investigate the catalytic mechanism of H2SO on the major reactions in initial cellulose pyrolysis process, i.e., depolymerization of the cellulose chain, bridged dehydration, ring-opening, ring-contraction and dehydration of the free hydroxyl groups. TGA and Py-GC/MS experiments were also conducted as an assistance for verification. The
Acknowledgments
The authors thank the National Natural Science Foundation of China (51576064, 51676193), National Basic Research Program of China (2015CB251501), Beijing Nova Program (Z171100001117064), Beijing Natural Science Foundation (3172030), Grants from Fok Ying Tung Education Foundation (161051), and Fundamental Research Funds for the Central Universities (2018ZD08, 2018QN057, 2016YQ05) for financial support.
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