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Sulfur Trioxide Micro-Thermal Explosion for Rice Straw Pretreatment

Written By

Ri-Sheng Yao and Feng-He Li

Submitted: November 16th, 2011 Published: August 29th, 2013

DOI: 10.5772/50428

From the Edited Volume

Cellulose

Edited by Theo van de Ven and John Kadla

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1. Introduction

With the gradual depletion of fossil energy resources in the global scope, the conversion of cellulose into biofuels attracts considerable attentions, since it is the most abundant renewable polysaccharide on the earth. The main sources of cellulose are woods, agricultural residues, hydrophytes and straws (Dieter and Thomas et al. 2003; Hon, 1996). Rice straw is a frequently abandoned crop straw in Asia and is often burned. This wastes cellulose and pollutes the air. Thus, utilizing rice straw to produce biofuel has promise. Generally, the procedure of converting rice straw into fuels is removal of the protective lignin first, followed by transformation of cellulose into glucose and at last, converting these sugars to biofuel by fermentation.

Removing lignin is critical to utilizing cellulose (Reith et al. 2003). Lignin content, crystallinity and particle size, limit the digestibility of cellulose (Hendriks and Zeeman, 2009). Therefore, various pretreatments remove or alter the hemicellulose or lignin and decrease the crystallinity of cellulose to enhance enzymatic hydrolysis efficiency (Goering, et al., 1970; Mosier et al., 2005; Zhao et al., 2009). The major methods include pretreatment by milling (Sato et al., 2009; Delgenés et al., 2002; Chang and Holtzapple, 2000; Palmowski and Muller, 1999), acid (Keikhosro K, 2006; Nguyen, Q, 2004; Ye and Jay, 2005; Taherzadeh and Karimi, 2007; Iranmahboob, F, 2002), steam explosion (Mukhopadhyay and Fangueiro, 2009; Brownell et al., 1986; Negro et al., 1992), liquid hot water (Liu and Wyman, 2005), alkali (Das and Chakraborty, 2009; Goswami et al., 2009; Fengel and Wegener, 1984; Laser et al., 2002), wet oxidation (Palonen and Thomsen, 2004; Kumar and Wyman, 2009), ammonia fiber explosion (AFEX) (Taherzadeh and Karimi, 2008; Li et al., 2009; Zheng et al., 1998; Wu et al., 1999), SO2 catalyzed steam explosion (Balint and Emma, 2010) etc. Although these common pretreatments have made great successes in recycling cellulose from lignocellulosic biomass, they are not appropriate enough for biofuel production by industrialization if considering the disadvantages of them such as low efficient, huge energy consumption, high requirements for conditions of operations, environment pollution and so on.

Recently, rice straw has been pretreated with, ionic liquid (Vitz, J. and Erdmenger, 2009), low-temperature plasma (Li and Yao, 2012), microwave-assisted dilute lye (Li and Yao, 2012). In this chapter, we concentrate upon the novel pretreatment method of rice straw based on sulfur trioxide micro-thermal explosion (STEX), the moderate conditions for the operation of this pretreatment method make it a promising technology to reduce costs and increase the utilization of lignocellulosic cellulose.

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2. Principles of Sulfur trioxide micro-thermal explosion

The principles of STEX can be described by the model diagram shown in Fig.1. sulfur trioxide (SO3) gas diffuses into the interior of rice straw through its capillary channels, reacts with the water in the tissue space and surface. As a result of violent exothermic process of the reaction, the gas in the limited tissue space expands and an in-situ detachment between the cellulose and the lignin will occur, moreover, lignin will be sulphonated partly during this process which may increase the solubility of the lignin in dilute lye. The operation can be performed under atmospheric pressure at about 50℃, it makes the subsequent treatment of stripping off lignin by dilute alkali solution more effectively as compared to the procedure by dilute alkali only (Yao and Hu etc. 2011).

Figure 1.

STEX collaborative dilute alkali model diagram

2.1. Gas diffuse and chemical exotherm in situ generating explosion

Comparing to liquid, gas diffuses more quickly and deeply into interior of rice straw through its capillary channels. When SO3 gas accesses to the interior of rice straw, micro-thermo explosions take place as a result of reaction between SO3 and water remaining in the pores of the rice straw, which make great changes of the interior structure of the rice straw.

The capillary channels presence in the original straw are arranged irregularly and some of its opening have been blocked (Fig.2A). The blocked openings are not conductive to the entry of cellulose hydrolysis enzyme. After straw is treated by SO3 gas, the channels in the straw increase and are bundled, as if the internal structure of the straw are "hollowed out" (Fig.2B), which will promote the access of the substances during the subsequent handling. With increase of the STEX time, the channel structure becomes more obvious (Fig.2C). However, when the STEX time is more than 60 min, channels aggregate together and become not so obvious (Fig.2D and Fig.2E). The elongated STEX time may cause the internal environment of the straw more acidic, and induces acid hydrolysis, thereby major components of the rice straw degrade and the structure of the rice straw is damaged.

2.2. Procedure of sulfur trioxide micro-thermal explosion collaborative dilute alkali

The STEX for rice straw is convenient and can be performed under atmospheric pressure at about 50℃. A typical procedure of this method in the laboratory can be divided into two steps: First, 1g rice straw is cut into small pieces of about 2-3 cm in length, and hung over the upper portion of a test tube with 1mL oleum (Sulfur trioxide 50%) loading in the bottom, after raising the temperature of the system to 50℃ SO3 gas is generated and reacts with the upper straw for 5~120min. Second, the as-prepared rice straw is soaked in NaOH solution (1%, w/v) with the solid-liquid ratio of 1:10, the mixture is stirred at 90rpm with placing the reaction flask in a water bath at 50℃ for 2h, then the solids are washed with 800 mL of deionized water before the subsequent enzymatic hydrolysis procedure.

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3. Structure of rice straw pretreated by SO3 gas

STEX undermines the structure of straw at a microscopic level that makes it conducive to the subsequent alkali stripping. In this section, the results of scanning electron microscope (SEM), X-ray diffraction (XRD), and fourier transform infrared (FTIR) spectroscopy will reveal the effects of STEX on rice straw.

3.1. Surface morphology and crystallinity

3.1.1. Surface morphology observation by SEM

The microscopic morphologies of pretreated-straws are shown in Fig.3. Regarding the untreated straw, a compact structure comprised of plant cell wall compositions such as epidermis, vascular bundles, lumens, dents and parenchyma still remains. To the rice straw treated by sulfur trioxide, the flaking traces and some holes can be observed on the straw surface (Fig.3B). As mentioned previously, gaseous sulfur trioxide can react with water in straw and release great heat in-situ at the same time. As a result, the air and water vapor in the limited interior spaces of the straw expand sharply to make a hot explosion from the interior and cause effective detachment between cellulose and lignin; it makes the subsequent removal of lignin with dilute lye more efficient. As shown in Fig.3C, vesicle shaped particles were stripped away effectively and exposures of cellulose filaments were significant after treatment of STEX treated-straw with 1% w/v NaOH for 2 hours at 50℃.

Figure 2.

SEM of rice straw cross-sectional with the STEX, A-original straw, B-STEX 15min, C-STEX 30min, D-STEX 60min, E-STEX 120min.

Figure 3.

SEM imagines of straw samples with different treatment. A-original straw, B-STEX treated-straw, C-STEX collaborative dilute lye treated-straw

The disruption of the vesicle structure increases with reaction time between rice straw and SO3 (Fig.4). In our experiments, when the reaction time was prolonged to 120 min, the structure of rice straw was almost completely ruptured.

Figure 4.

The SEM images of straw with different STEX time, A-untreated, B-STEX 15min, C-STEX 30min, D-STEX 60min, and E-STEX 120min

3.1.2. Crystalline analyzed by X-ray diffraction (XRD) and the influence of saccharification rate

Crystallinity of cellulose is one of the main obstacles for enzymatic hydrolysis. STEX can reduce the crystallinity of rice straw effectively especially after the assistance of subsequent dilute lye. As shown in Tab.1, the effects of sulfur trioxide collaborative dilute alkali method are remarkable on the crystallinity and saccharification rate of the rice straw comparing with the ones of untreated, sulfur trioxide-treated only, alkali-treated only methods. Although sulfur trioxide-treated method decreases the crystallinity of cellulose, it doesn't significantly improve cellulose hydrolysis without the collaboration of dilute alkali. This result may imply that there are more profound changes occurring on contents and chemical structures of the straw during the process of the pretreatment.

PretreatmentCrystallinity(%)Sugar conversion rate (%)
(A)64.7±0.622.2±0.8
(B)58.5±0.341.8±0.4
(C)55.8±0.764.3±0.6
(D)51.3±0.491.7±0.4

Table 1.

Pretreatment of rice straw had the crystallinity and the rate of saccharification

Sugar conversion rate from pretreated rice straw was calculated as follows: (EQ1)

SR=RGRS×100%

where RG is the dry-weight of reducing sugars in enzyme hydrolysis supernatant, RS is the dry-weight rice straw in pretreated solids.

3.2. Contents and chemical structures

3.2.1. Fourier transforms infrared (FTIR) spectroscopy

Differences between the IR spectra of the untreated, sulfur trioxide-treated and sulfur trioxide collaborative dilute alkali-treated rice straws confirm changes of the rice straw occurring on the chemical level during STEX. As shown in Fig.6, the absorption bands at 3317cm-1 (O-H stretch vibration), 2919 and 2850cm-1 (C-H stretch vibration), 1630cm-1 (C=C stretch vibration) and 1037cm-1 (C=O stretch vibration) are characteristics of the original rice straw. After rice straw is treated by sulfur trioxide, new peaks at 1147cm-1 (S=O stretch vibration) and 876 cm-1(C-SO stretch vibration) appear. To the rice straw treated with sulfur trioxide collaborative dilute alkali, the peaks about 1147cm-1(S=O stretch vibration) and 876 cm-1(C-SO stretch vibration) disappear. These results indicate that lignin is sulphonated partly, then this part is been stripped on the processing with dilute lye. We suggest that not only the detachment between lignin and cellulose but also sulphonation of lignin during STEX may play an important role to the final lignin removal, which means the collaboration of dilute alkali is necessary.

Figure 5.

X-ray diffract diagram: (A) untreated rice straw; (B), rice straw was treated for 30min at 50℃ by sulfur trioxide; (C), rice straw was treated for 7 hours at 50℃ by 1% w/v NaOH. (D), straw was treated with sulfur trioxide for 30min following 1% w/v NaOH treatment for 7 hours at 50℃

3.2.2. Changes of main components in rice straw

The quantities of the components of rice straw change a lot after being treated with STEX collaborative dilute alkali. Results from our work are shown in Table 2. The composition was calculated based on the dry weight of the samples and we found that water-soluble content of the STEX-treated rice straw increased. It indicates water soluble molecules such as oleoresin, lignin/hemicellulose fragments and sulphonated matter have more chances to contact water after STEX-treated. Moreover, the lignin and hemicellulose of the rice straw pretreated by STEX collaborative dilute lye decreased from 19.6% to 6.9% and 21.4% to 13.5%, respectively.

Figure 6.

FTIR spectra: A-Untreated-straw, B-STEX treated-straw, C-STEX collaborative dilute alkali treated-straw.

Composition (%)Untreated straw (100.0 g)STEX treated straw (100.8 g)STEX assist lye treated straw (73.6 g)
Water-Soluble14.1 ± 0.215.9±0.48.6 ± 0.5
Cellulose39.2 ± 0.739.8±0.565.8 ± 1.0
Hemicellulose21.4 ± 0.420.4±0.613.5 ± 0.3
Lignin19.6 ± 0.818.4±0.36.9 ± 0.6
Ash5.7 ± 0.15.5±0.45.2 ± 0.3

Table 2.

Chemical composition (percent by dry weight) of rice straw

The cellulose content increased from 39.2% to 65.8%, that is predominantly attributed to the decrease of lignin and hemicellulose. Removal of lignin can reduce the binding of lignin to hemicellulose/cellulose (Han et al. 1997; Lu et al. 2002; Ahola et al. 2008; Ma et al. 2008), and more removal of hemicellulose implies that the connections between the hemicellulose and cellulose are broken and more cellulose is exposed. In summary, STEX collaborative diluted lye pretreatment will partly break the lignocellulose structure, enhance enzymatic biocatalysis, increase the desired products yield and recycle more cellulose.

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4. Saccharification and fermentation for bioethanol production

Producing ethanol from lignocellulosic materials need a series of chemical and biological procedures, namely opening the bundles of lignocelluloses in order to access the polymer chains of cellulose and hemicellulose, polymers hydrolysis to achieve monomer sugar solutions, fermentation of the sugars to obtain ethanol solution (mash) by microorganisms, purification of ethanol from mash by distillation and dehydration. Figure 7 is a flow figure designed for applying the technology of STEX for producing bioethanol.

Figure 7.

Flow diagram for bioethanol production from rice straw

4.1. Saccharification with enzymatic hydrolysis

4.1.1. Water retention value (WRV) of celluloses

The structure of untreated rice straw is nonporous and tight. The compact structure makes it difficult to moisturize the interior of rice straw and prevents from entering of the cellulase dissolved in water, which will decrease the efficiency of the enzyme hydrolysis. Hence, water retention value (WRV) of cellulose is often used to evaluate accessibility of cellulose for enzyme and we used it to evaluate the effects of the SO3 micro-thermal explosion. The straw water retention values were determined by centrifugation method. The straw was soaked in water at 25℃ for 30 min, then centrifuged at 3000rpm for 15 min. The wet straw was weighed after centrifuging and then reweighed after being dried at 90℃ for 2h, The WRV was calculated as the amount of water which retained in the rice straw after centrifuging comparing with dried weight of straw (Eq2)

WRV=WwWdWd×100%

4.1.2. Water retention value and change of saccharification rate

The impacts of pretreatment manners to WRV and saccharification rate are shown in Fig.8. To STEX treated rice straw, WRV and saccharification rate increased with the treating time during the initial 120min, when the treatment with sulfur trioxide duration was elongated the WRV began to decline rapidly and the saccharification rate just decreased slightly (Fig.8A), we suggest that a little of carbide might form in the rice straw when time of STEX was too long and cellulose became more hydrophobic. To dilute alkali-treated method, the WRV increased during the initial 120 min and then became stable, the saccharification rate increased within initial 180min (Fig.8B). The dilute alkali-treated method removed the lignin in lignocellulosic slowly, slightly destructed the internal structure of cellulose and the off lignin lignocellulosic structure will be opened gradually so that the WRV and the saccharification rate increased. The change of the saccharification rate and WRV of the sulfur trioxide followed by alkali-treated rice straw are shown in Fig.8C, the WRV increased within initial 60min but decreased after 60min and the saccharification rate increased and became stable after 120min.

Figure 8.

The impacts of WRV on saccharification rate by pretreatment. -▲-, saccharification rate; -●-, WRV; (A) rice straw was treated for 4 hours at 50℃ by sulfur trioxide; (B) rice straw was treated for 4 hours at 50℃ by 1% w/v NaOH; (C) straw was treated with sulfur trioxide for 4 hours followed by 1% w/v NaOH treatment for 2 hours at 50℃.

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5. Future perspective

STEX for the pretreatments of cornstalk, rape straw, wheat straw had also been researched in our lab, and the STEX method exibited significant effects on the enhancement of enzyme hydrolysis of these herbs, that means STEX can act as a universal method for lignocellulosic pretreatment, and mdoderate requirements for performing STEX may improve competitiveness of the renewable energy from biomass. While there are also several aspects, which need to be researched for applying the STEX into commercial-scale application (industry), such as pretreatment equipment, clean technology in lower cost, and how to attain the utter utilization of lignocelluloses in order to manufacture high-purity cellulose. Meanwhile, the optimization of the STEX pretreatment process, clean and low-cost application of lignin black liquor and the research of high-efficiency pretreatment technology in the farmland are imminent. Commercial-scale application approach of rice straw with the STEX in the future is showed in Fig.9.

Figure 9.

A platform of SO3/alkali processing technology to achieve each component of straw and utter utilization of biomass

References

  1. 1. HendriksA. T. W. M.ZeemanG.2009Pretreatments to enhance the digestibility of lignocellulosic biomass. Bioresource Technology1001018
  2. 2. Balint Sipos, Emma Kreuger, Sven-Erik Svensson, Kati Reczey, Lovisa Bjornsson, Guido Zacchi,2010Steam pretreatment of dry and ensiled industrial hemp for ethanol production. Biomass & Bioenergy3417211731
  3. 3. BrownellH. H.YuE. K. C.SaddlerJ. N.1986Steam-explosion pretreatment of wood: effect of chip size, acid, moisture content and pressure drop. Biotechnol. Bioeng.28792801
  4. 4. ChangV. S.HoltzappleM. T.2000Fundamental factors affecting enzymatic reactivity. Appl. Biochem. Biotechnol.,537
  5. 5. DasM.ChakrabortyD.2009Effects of alkalization and fiber loading on the mechanical properties and morphology of bamboo fiber composites. II. Resol matrix,” J. Appl. Polym. Sci.112447453
  6. 6. DelgenésJ. P.PenaudV.MolettaR.2002Pretreatments for the enhancement of anaerobic digestion of solid wastes Chapter 8. In: Biomethanization of the Organic Fraction of Municipal Solid Wastes. IWA Publishing,201228
  7. 7. DieterK.Hans-PeterS.ThomasH.2003polysaccharose II-Eukaryotes polysaccharide Chapter 10, cellulose, In: Biopolymers, Wiley-vch publishing,248289
  8. 8. FengelD.WegenerG.1984Wood: Chemistry, Ultrastructure, Reactions. De Gruyter, Berlin.
  9. 9. GoeringH. K.Van SoestP. J.1970Forage fiber analyses (apparatus, reagent, procedure, and some application), Agricultural Handbook379Agricultural Research Service- United States Department of Agriculture (USDA), Washington D.C.,120
  10. 10. GoswamiP.BlackburnR. S.El -DessoukyH. M.TaylorJ.WhiteP.2009Effect of sodium hydroxide pre-treatment on the optical and structural properties of lyocell, Eur. Polym. J.45455465
  11. 11. HonD. N. S.1996Functional polymers: a new dimensional creativity in lignocellulosic chemistry, in: Chemical Modification of lignocellulosic materials,110New York: Marcel Dekker.
  12. 12. IranmahboobF.NadimMonemiS.2002Optimizing previous ermacid-hydrolysis: next term a critical step for production of ethanol from mixed wood chips, Biomass and Bioenergy,22401404
  13. 13. KeikhosroK.et al.2006Conversion of rice straw to sugars by dilute-acid hydrolysis. Biomass and Bioenergy,30247253
  14. 14. LaserM.SchulmanD.AllenS. G.LichwaJ.Antal JrM. J.LyndL. R.2002A comparison of liquid hot water and steam pretreatments of sugar cane bagasse for bioconversion to ethanol. Bioresour. Technol.813344
  15. 15. LiF. H.HuH. J.YaoR. S.WangH.LiM. M.2012Structure and saccharification of rice straw pretreated with microwave-assisted dilute lye. Industrial & Engineering Chemistry Research.
  16. 16. LiF. H.YaoR. S.2012Influence of low temperature plasma on the structure and saccharification of rice straw. Internal communication.
  17. 17. LiR. J.FeiJ. M.CaiY. R.LiY. F.FengJ. Q.YaoJ. M.2009Cellulose whiskers extracted from mulberry: A novel biomass production, Carbohyd. Polym.769499
  18. 18. LiuC. G.WymanC. E.2005Partial flow of compressed-hot water through corn stover to enhance hemicellulose sugar recovery and enzymatic digestibility of cellulose, Bioresour. Technol.9619781985
  19. 19. MosierN.WymanC. E.DaleB. E.ElanderR. T.LeeY. Y.HoltzappleM.LadischM. R.2005Features of promising technologies for pretreatment of lignocellulosic biomass, Bioresource Technol.96673686
  20. 20. MukhopadhyayS.FangueiroR.2009Physical modification of natural fibers and thermoplastic films for composites- A review. J. Thermoplast. Compos.22135162
  21. 21. NegroM. J.ManzanaresP.OlivaJ. M.BallesterosI.BallesterosM.2003Changes in various physical chemical parameters of Pinus Pinaster wood after steam explosion pretreatment. Biomass Bioenergy25301308
  22. 22. NguyenQ.2004Milestone completion report: evaluation of a two-stage dilute sulfuric previous termacid hydrolysisnext term process. Internal Report, National Renewable Energy Laboratory, Golden.
  23. 23. PalmowskiL.MullerJ.1999Influence of the size reduction of organic waste on their anaerobic digestion. In: II International Symposium on Anaerobic Digestion of Solid Waste. Barcelona 15-17 June,137144
  24. 24. PalonenH.ThomsenA. B.TenkanenM.SchmidtA. S.ViikariL.2004Evaluation of wet oxidation pretreatment for enzymatic hydrolysis of softwood. Appl. Biochem. Biotechnol.117117
  25. 25. ReithJ. H.WijffelsR. H.BartenH.2003Bio-methane & Bio-hydrogen. Status and perspectives of biological methane and hydrogen production. Production of the Dutch biological hydrogen production, The Hague.
  26. 26. TaherzadehM. J.KarimiK.2008Pretreatment of lignocellulosic wastes to improve ethanol and biogas production: A review, Int. J. Mol. Sci.91621651
  27. 27. TaherzadehM. J.KarimiK.2007Enzyme-based hydrolysis processes for ethanol from lignocellulosic materials: A review, BioResources2707738
  28. 28. VitzJ.ErdmengerT.HaenschC.SchubertU. S.2009Extended dissolution studies of cellulose in imidazolium based ionic liquids. Green Chem.11417424
  29. 29. WuM. M.ChangK.GreggD. J.BoussaidA.BeatsonR. P.SaddlerJ. N.1999Optimization of steam explosion to enhance hemicellulose recovery and enzymatic hydrolysis of cellulose in softwoods. Appl. Biochem. Biotechnol.,4754
  30. 30. YaoR. S.HuH. J.DengS. S.WangH.ZhuH. X.2011Structure and saccharification of rice straw pretreated with sulfur trioxide micro-thermal explosion collaborative dilute alkali, Bioresour. Technol.102(10), 6340-6343.
  31. 31. YeS.JayJ. C.2005Dilute acid pretreatment of rye straw and bermudagrass for ethanol production. Biochem. Biotechnol.,961415991606
  32. 32. ZhaoX. B.ChengK. K.LiuD. H.2009Organosolv pretreatment of lignocellulosic biomass for enzymatic hydrolysis. App. Microbiol. Biot.82815827
  33. 33. ZhengY.LinH. M.TsaoG. T.1998Pretreatment for cellulose hydrolysis by carbon dioxide explosion. Biotechnol. Progr.,14890896

Written By

Ri-Sheng Yao and Feng-He Li

Submitted: November 16th, 2011 Published: August 29th, 2013