Name: pretreatment of lignocellulosic biomass with low-cost ionic liquids
Uploaded: 2016-08-10T13:00:00
Description: Watch this Scientific Journal Video about Pretreatment of Lignocellulosic Biomass with Low-cost Ionic Liquids at JoVE.com

The authors acknowledge the Grantham Institute for Climate Change and the Environment, Climate-KIC and EPSRC (EP/K038648/1 and EP/K014676/1) for funding and Pierre Bouvier for providing experimental data for pine pretreatments.

Note: The protic ionic liquids used in the process are synthesized in our laboratory, although some might be or become commercially available. The resulting ionic liquids are acidic and corrosive and probably skin/eye irritants (depending on the amine used), and must therefore be handled with care wearing appropriate PPE (lab coat, safety specs, resistant gloves).
1. Preparation
<ol>
	<li>Preparing and storing the lignocellulosic biomass
	<ol>
		<li>Obtain the lignocellulosi...

<ol>
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Microbiol. Biotechnol. 82 (5), 815-827 (2009).</li><li>Brandt, A., Gr&#228;svik, J., Hallett, J. P., Welton, T. <a target="_blank" href="http://www.ncbi.nlm.nih.gov/entrez/query.fcgi?db=PubMed&cmd=Search&doptcmdl=Citation&defaultField=Title+Word&term=Deconstruction+of+lignocellulosic+biomass+with+ionic+liquids.">Deconstruction of lignocellulosic biomass with ionic liquids.</a> Green Chem. 15, 550 (2012).</li><li>Chen, L., et al. <a target="_blank" href="http://www.ncbi.nlm.nih.gov/entrez/query.fcgi?db=PubMed&cmd=Search&doptcmdl=Citation&defaultField=Title+Word&term=Inexpensive+ionic+liquids:[HSO+4]&#8722;-based+solvent+production+at+bulk+scale).">Inexpensive ionic liquids:[HSO 4]&#8722;-based solvent production at bulk scale).</a> Green Chem. 16 (6), 3098-3106 (2014).</li><li>Brandt, A., Chen, L., van Dongen, B. E., Welton, T., Hallett, J. 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G., Baker, S. R., Decker, <a target="_blank" href="http://www.ncbi.nlm.nih.gov/entrez/query.fcgi?db=PubMed&cmd=Search&doptcmdl=Citation&defaultField=Title+Word&term=NREL/TP-5100-63351.">NREL/TP-5100-63351.</a> Low Solids Enzymatic Saccharificatin of Lignocellulosic Biomass. , (2015).</li><li>Brandt, A., Ray, M. J., To, T. Q., Leak, D. J., Murphy, R. 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The technique for the fractionation of lignocellulosic biomass presented here produces a cellulose-rich pulp and a lignin. Most of the hemicelluloses are dissolved into the ionic liquid and hydrolyzed, but not recovered. If hemicellulose sugars are desired, a hemicellulose pre-extraction step prior to the Ionosolv delignification may be necessary. It has so far been impossible to fully close the mass balance for the biomass, as it is not possible to identify and quantify all degradation products found in the ionic liquid...

Meeting humanity&#39;s energy demand sustainably is one of the greatest challenges that our civilization faces. Energy use is predicted to double in the next 50 years, putting greater strain on fossil fuel resources. 1 The buildup of greenhouse gases (GHG) in the atmosphere through wide-spread fossil fuel use is particularly problematic, as CO2 generated from combustion of fossil fuels is responsible for 50% of the anthropogenic greenhouse effect. 2 Therefore, large-scale application of renewable and carbon neutral technologies is essential for meeting the increased energy and material needs of future generations. 1, 3
Plant biomass is the most versatile renewable resource, as it can be used to produce heat, electricity as well as carbon-based chemicals, materials and fuels. Primary advantages of lignocellulosic biomass over other biomass types are its abundance, potential for high yields per area of land and often much higher CO2 emission savings, which includes high retention of carbon in the soil. 4, 5 Additional benefits of using biomass include local availability, low capital requirements to convert biomass to energy, and soil erosion prevention. 8
Major producers of lignocellulosic feedstocks are the forestry industry and the agricultural sector as well as municipal waste management. 6 Lignocellulose production has the potential to be expanded, with a mind to limiting deforestation and avoiding the replacement of food crops and release of potential pollutants. 7 For renewable biomass to become a viable widespread source of liquid transportation fuels and chemicals, its processing must become economically competitive with fossil fuel conversion technologies. 9, 10 A key to achieving this is to boost the yield and quality of biomass-derived intermediates while reducing cost.
Lignocellulose contains a high proportion of sugars which can be converted to fuels and chemicals via catalytic and microbial conversions. 11 These sugars are present in lignocellulose in polymeric form as cellulose and hemicellulose. They can be hydrolyzed into glucose and other sugar monomers and then used for producing bioethanol and other bio-derived chemicals and solvents. 12
In order to access the cellulosic sugars, pretreatment of the biomass is necessary through physical, chemical, or combined processes. 4 The pretreatment is arguably the most costly step in the valorization of lignocellulosic biomass. Hence research into improved pretreatment processes is imperative.
Various pretreatment technologies are available. Of particular interest are those that separate the lignin from cellulose (fractionative pretreatment). Lignin, the third major component in lignocellulose, limits access of hydrolyzing agents to cellulose and hemicellulose and reduces the sugar yield per ton of feedstock. 11 The separated lignin can be utilized as an additional biorefinery intermediate if it is isolated in suitable quality. 13 One fractionative process is the Kraft process which is the most common pretreatment for paper/cellulose production. In Kraft pulping, wood chips are placed in a mixture of sodium hydroxide and sodium sulfide and heated at elevated temperatures of around 170 &#176;C under high pressure. 14 The alkaline reactions remove hemicellulose and lignin by breaking the polymers down to short fragments via nucleophilic and base catalysis, and by dissolving the lignin fragments via de-protonation of phenolic hydroxyl/alcohol groups. Another common delignification process is the Organosolv process which also fragments and dissolves the lignin and hemicellulose. Rather than using an alkaline aqueous solution, organic solvents such as ethanol and acetic acid are used at high temperatures ranging between 160-200 &#176;C and pressures from 5-30 bar. Organosolv pretreatment has some advantages over Kraft pulping in that it produces less air and water pollution. 15 Both processes possess some economic challenges, if used for production of chemicals and fuels rather than cellulose. 16 The Ionosolv pretreatment uses ionic liquids, which are salts that have melting points below 100 &#176;C and, as a result of their powerful Coulombic interactions, very low vapor pressures. 17 This eliminates air pollution in the pretreatment process, and enables processing at or near atmospheric pressure.
While most ILs are created in laborious, multi-step syntheses, protic ILs can be synthesized in a one-step process from commodity chemicals, which makes them less expensive; it is estimated that some ILs could be produced at bulk scale for a price of $1.24 per kg which is comparable to common organic solvents such as acetone and toluene. 18 The ability to recycle and reuse these customizable ILs in a process that operates at comparatively lower temperatures and pressures makes this a more benign alternative and an economically attractive candidate for biorefining.
This detailed video protocol demonstrates a lab-scale version of the Ionosolv process for the delignification of lignocellulosic biomass and the eventual enzymatic saccharification of the cellulose-rich pulp as well as the recovery of a high-purity odor-free lignin.19

<table border="0" cellpadding="0" cellspacing="0" width="851">
	<tbody>
		<tr height="21">
			<td height="21" style="height:21px;width:339px;">IL synthesis</td>
			<td style="width:116px;"></td>
			<td style="width:131px;"></td>
			<td style="width:267px;"></td>
		</tr>
		<tr height="42">
			<td height="42" style="height:42px;width:339px;">Round bottom flask, with standard ground joint 24/29 NS, 1000 ml</td>
			<td style="width:116px;">Lenz</td>
			<td style="width:131px;">3 0024 70</td>
			<td>VWR product code 271-1309&#160;</td>
		</tr>
		<tr height="42">
			<td height="42" style="height:42px;width:339px;">250mL Addition Funnel, Graduated, 29/26 Joint Size, 0-4mm PTFE Valve</td>
			<td style="width:116px;">GPE</td>
			<td style="width:131px;">CG-1714-16</td>
			<td></td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:339px;">Dish-shaped dewar flask, SCH 31 CAL&#160;</td>
			<td style="width:116px;">KGW-Isotherm</td>
			<td style="width:131px;">1197</td>
			<td></td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:339px;">Volumetric flask, 200 ml</td>
			<td style="width:116px;">VWR</td>
			<td style="width:131px;">612-3745&#160;</td>
			<td></td>
		</tr>
		<tr height="42">
			<td height="42" style="height:42px;width:339px;">Cork rings, pasteur pipettes and teet, wash bottle with deionised water, large magentic stir bar</td>
			<td style="width:116px;"></td>
			<td style="width:131px;"></td>
			<td></td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:339px;">Biomass size reduction</td>
			<td style="width:116px;"></td>
			<td style="width:131px;"></td>
			<td></td>
		</tr>
		<tr height="42">
			<td height="42" style="height:42px;width:339px;">Heavy Duty Cutting Mill SM2000&#160;</td>
			<td style="width:116px;">Retsch&#160;</td>
			<td>Discontinued</td>
			<td style="width:267px;">Replaced with Cutting Mill SM 200 (20.728.0001)&#160;</td>
		</tr>
		<tr height="42">
			<td height="42" style="height:42px;width:339px;">Bottom sieves (10 mesh square holes, for particle size &#60;2 mm)</td>
			<td style="width:116px;">Retsch&#160;</td>
			<td style="width:131px;">03.647.0318</td>
			<td style="width:267px;">Part of cutting mill</td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:339px;">Analytical Sieve Shaker AS 200</td>
			<td style="width:116px;">Retsch&#160;</td>
			<td>30.018.0001</td>
			<td>Part of sieving machine</td>
		</tr>
		<tr height="42">
			<td height="42" style="height:42px;width:339px;">Test Sieve 200 mm &#216; x 50 mm height ISO 3310/1 (180 &#181;m)</td>
			<td style="width:116px;">Retsch&#160;</td>
			<td>60.131.000180</td>
			<td>Part of sieving machine</td>
		</tr>
		<tr height="42">
			<td height="42" style="height:42px;width:339px;">Test Sieve 200 mm &#216; x 50 mm height ISO 3310/1 (850 &#181;m)</td>
			<td style="width:116px;">Retsch&#160;</td>
			<td style="width:131px;">60.131.000850</td>
			<td align="left">Part of sieving machine</td>
			<td></td>
		</tr>
		<tr height="42">
			<td height="42" style="height:42px;width:339px;">Collecting pan, stainless steel, 200 mm &#216;, height 50 mm&#160;</td>
			<td style="width:116px;">Retsch&#160;</td>
			<td style="width:131px;">69.720.0050</td>
			<td>Part of sieving machine</td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:339px;">Rotary evaporator:</td>
			<td style="width:116px;"></td>
			<td style="width:131px;"></td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:339px;">Rotary evaporator (Rotavapor R-210)</td>
			<td style="width:116px;">Buchi&#160;</td>
			<td>Discontinued</td>
			<td>Replaced with Rotavapor R-300</td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:339px;">Water bath (Heating bath B-491)</td>
			<td style="width:116px;">Buchi&#160;</td>
			<td>48201</td>
			<td>Part of rotary evaporator</td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:339px;">Recirculator&#160;</td>
			<td style="width:116px;">Julabo</td>
			<td style="width:131px;">F25</td>
			<td>Part of rotary evaporator</td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:339px;">Vacuum pump (MPC 101 Z)</td>
			<td style="width:116px;">Ilmvac GmbH</td>
			<td style="width:131px;">412522</td>
			<td>Part of rotary evaporator</td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:339px;">Vacuum controller (Vacuum Control Box VCB 521)</td>
			<td style="width:116px;">Ilmvac GmbH</td>
			<td style="width:131px;">600053</td>
			<td>Part of rotary evaporator</td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:339px;">Parallel evaporator:</td>
			<td style="width:116px;"></td>
			<td style="width:131px;"></td>
			<td></td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:339px;">StarFish Base Plate 135mm (for Radleys &#38; IKA)&#160;</td>
			<td style="width:116px;">Radleys</td>
			<td>RR95010</td>
			<td>Part of parallel evaporator</td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:339px;">Monoblock for 5 x 250ml Flasks</td>
			<td style="width:116px;">Radleys</td>
			<td>RR95130&#160;</td>
			<td>Part of parallel evaporator</td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:339px;">Telescopic 5-way Clamp with Velcro</td>
			<td style="width:116px;">Radleys</td>
			<td>RR95400</td>
			<td>Part of parallel evaporator</td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:339px;">Gas/Vacuum Manifold with connectors</td>
			<td style="width:116px;">Radleys</td>
			<td>RR95510&#160;</td>
			<td>Part of parallel evaporator</td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:339px;">650mm Rod</td>
			<td style="width:116px;">Radleys</td>
			<td>RR95665&#160;</td>
			<td>Part of parallel evaporator</td>
		</tr>
		<tr height="42">
			<td height="42" style="height:42px;width:339px;">Quick Release Male, R/A Barbed 6.4mm + Shut-off (3.2mm ID)&#160;</td>
			<td style="width:116px;">Radleys</td>
			<td>RR95520</td>
			<td>Part of parallel evaporator</td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:339px;">Stirrer/hot plate</td>
			<td>Radleys</td>
			<td>RR98072</td>
			<td>Part of soxhlet extractor</td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:339px;">Temperature controller</td>
			<td style="width:116px;">Radleys</td>
			<td>RR98073</td>
			<td>Part of soxhlet extractor</td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:339px;">Elliptical Stirring Bar 15mm Rare Earth</td>
			<td style="width:116px;">Radleys</td>
			<td>RR98097&#160;</td>
			<td>Part of parallel evaporator</td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:339px;">Vacuum cold trap, plastic coated, PTFE stopcock</td>
			<td style="width:116px;">Chemglass</td>
			<td style="width:131px;">CG-4519-01</td>
			<td>Part of parallel evaporator</td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:339px;">Vacuum pump (MPC 101 Z)</td>
			<td style="width:116px;">Ilmvac GmbH</td>
			<td style="width:131px;">412522</td>
			<td>Part of parallel evaporator</td>
		</tr>
		<tr height="42">
			<td height="42" style="height:42px;width:339px;">Tygon tubing E-3603, 6,40 mm (internal) 12,80 mm (external)&#160;&#160;</td>
			<td style="width:116px;">Saint-Gobain/VWR</td>
			<td style="width:131px;">228-1292&#160;</td>
			<td>Part of parallel evaporator</td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:339px;">Parallel Soxhlet extractor:</td>
			<td></td>
			<td></td>
			<td></td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:339px;">StarFish Base Plate 135mm (for Radleys &#38; IKA)</td>
			<td>Radleys</td>
			<td>RR95010&#160;</td>
			<td>Part of soxhlet extractor</td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:339px;">Monoblock for 5 x 250ml Flasks</td>
			<td style="width:116px;">Radleys</td>
			<td>RR95130&#160;</td>
			<td>Part of soxhlet extractor</td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:339px;">Telescopic 5-way Clamp with Velcro</td>
			<td style="width:116px;">Radleys</td>
			<td>RR95400&#160;</td>
			<td>Part of soxhlet extractor</td>
		</tr>
		<tr height="42">
			<td height="42" style="height:42px;width:339px;">Telescopic 5-way Clamp with Silicone Strap and Long Handle</td>
			<td>Radleys</td>
			<td>RR95410&#160;</td>
			<td>Part of soxhlet extractor</td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:339px;">Water Manifold with connectors</td>
			<td style="width:116px;">Radleys</td>
			<td>RR95500&#160;</td>
			<td>Part of soxhlet extractor</td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:339px;">650mm Rod</td>
			<td style="width:116px;">Radleys</td>
			<td>RR95665&#160;</td>
			<td>Part of soxhlet extractor</td>
		</tr>
		<tr height="42">
			<td height="42" style="height:42px;width:339px;">Quick Release Male, R/A Barbed 6.4mm + Shut-off (3.2mm ID)</td>
			<td>Radleys</td>
			<td>RR95520&#160;</td>
			<td>Part of soxhlet extractor</td>
		</tr>
		<tr height="42">
			<td height="42" style="height:42px;width:339px;">Coil condensers with standard ground joints 29/32 NS</td>
			<td>Lenz</td>
			<td>5.2503.04&#160;</td>
			<td>Part of soxhlet extractor</td>
		</tr>
		<tr height="42">
			<td height="42" style="height:42px;width:339px;">Extractor Soxhlet 40mL borosilicate glass 29/32 socket 24/29 cone</td>
			<td>Quickfit</td>
			<td>EX5/43&#160;</td>
			<td>Part of soxhlet extractor</td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:339px;">Stirrer/hot plate</td>
			<td>Radleys</td>
			<td>RR98072</td>
			<td>Part of soxhlet extractor</td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:339px;">Temperature controller</td>
			<td style="width:116px;">Radleys</td>
			<td>RR98073</td>
			<td>Part of soxhlet extractor</td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:339px;">Recirculator</td>
			<td>Grant</td>
			<td>LTC1</td>
			<td>Part of soxhlet extractor</td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:339px;">Cellulose extraction thimble</td>
			<td>Whatman</td>
			<td>2280-228</td>
			<td></td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:339px;">Tweezers</td>
			<td>Excelta</td>
			<td>20A-S-SE</td>
			<td></td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:339px;">Vacuum drying oven:</td>
			<td></td>
			<td></td>
			<td></td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:339px;">Vacuum drying oven</td>
			<td>Binder</td>
			<td>VD 23</td>
			<td>Part of vacuum oven</td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:339px;">Dewar vessel 2L 100x290mm with handle</td>
			<td>KGW-Isotherm</td>
			<td>10613</td>
			<td>Part of vacuum oven</td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:339px;">Vacuum Trap</td>
			<td>GPE</td>
			<td>CG-4532-01&#160;</td>
			<td>Part of vacuum oven</td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:339px;">Other equipment:</td>
			<td style="width:116px;"></td>
			<td style="width:131px;"></td>
			<td></td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:339px;">Analytical balance</td>
			<td style="width:116px;">A&#38;D</td>
			<td style="width:131px;">GH-252</td>
			<td>accuracy to &#177; 0.1 mg</td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:339px;">Volumetric Karl Fischer titrator</td>
			<td style="width:116px;">Mettler Toledo</td>
			<td style="width:131px;">V20</td>
			<td></td>
		</tr>
		<tr height="42">
			<td height="42" style="height:42px;width:339px;">10 mL disposable pipette</td>
			<td style="width:116px;">Corning Inc</td>
			<td style="width:131px;">Costar 4101 10 mL Stripette</td>
			<td></td>
		</tr>
		<tr height="42">
			<td height="42" style="height:42px;width:339px;">Eppendorf&#160;Research&#160;plus pipette, variable volume, volume 100-1000&#160;&#956;L</td>
			<td style="width:116px;">Eppendorf</td>
			<td>3120000062</td>
			<td></td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:339px;">Desiccator</td>
			<td style="width:116px;">Jencons</td>
			<td style="width:131px;">JENC250-028BOM</td>
			<td></td>
		</tr>
		<tr height="42">
			<td height="42" style="height:42px;width:339px;">Ace pressure tube bushing type, Front seal, volume 15&#160;mL&#160;</td>
			<td style="width:116px;">Ace Glass</td>
			<td>8648-04&#160;</td>
			<td></td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:339px;">Ace O-rings, silicone, 2.6&#160;mm, I.D. 9.2&#160;mm&#160;</td>
			<td style="width:116px;">Ace Glass</td>
			<td>7855216</td>
			<td>O-ring for pressure tube</td>
		</tr>
		<tr height="42">
			<td height="42" style="height:42px;width:339px;">Vortex shaker</td>
			<td style="width:116px;">VWR International</td>
			<td style="width:131px;">444-1378 (UK)</td>
			<td></td>
		</tr>
		<tr height="42">
			<td height="42" style="height:42px;width:339px;">Fan-assisted convection oven</td>
			<td style="width:116px;">ThermoScientific</td>
			<td style="width:131px;">HeraTherm OMH60</td>
			<td></td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:339px;">Oven glove (Crusader Flex)</td>
			<td style="width:116px;">Ansel Edmont</td>
			<td>42-325</td>
			<td></td>
		</tr>
		<tr height="42">
			<td height="42" style="height:42px;width:339px;">250 mL Round bottom flask single neck ground joint 24/29 (Pyrex)</td>
			<td style="width:116px;">Quickfit&#160;</td>
			<td style="width:131px;">FR250/3S</td>
			<td></td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:339px;">Rotaflo stopcock adapter with cone 24/29</td>
			<td style="width:116px;">Rotaflo England</td>
			<td style="width:131px;">MF11/2/SC</td>
			<td></td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:339px;">50 mL Falcon&#160; tube</td>
			<td style="width:116px;">Heraeus/Kendro</td>
			<td style="width:131px;">HERA 76002844</td>
			<td></td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:339px;">Centrifuge (Mega Star 3.0)</td>
			<td style="width:116px;">VWR&#160;</td>
			<td style="width:131px;">521-1751</td>
			<td></td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:339px;">Reagents:</td>
			<td style="width:116px;"></td>
			<td style="width:131px;"></td>
			<td></td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:339px;">Ethanol absolute</td>
			<td style="width:116px;">VWR</td>
			<td style="width:131px;">20820.464</td>
			<td></td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:339px;">Triethylamine</td>
			<td style="width:116px;">Sigma-Aldrich</td>
			<td style="width:131px;">T0886</td>
			<td></td>
		</tr>
		<tr height="42">
			<td height="42" style="height:42px;width:339px;">Sulfuric acid 5 mol/l (10N) AVS TITRINORM volumetric solution Safe-break bottle 2,5L</td>
			<td>VWR</td>
			<td>191665V</td>
			<td></td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:339px;">Purified water (15 M&#937; ressitance)</td>
			<td style="width:116px;">Elga</td>
			<td style="width:131px;">CENTRA R200</td>
			<td></td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:339px;">Lignocellulosic biomass:</td>
			<td style="width:116px;"></td>
			<td style="width:131px;"></td>
			<td></td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:339px;">Miscanthus X gigantheus</td>
			<td style="width:116px;"></td>
			<td style="width:131px;"></td>
			<td></td>
		</tr>
		<tr height="21">
			<td height="21" style="height:21px;width:339px;">Pinus sylvestris</td>
			<td style="width:116px;"></td>
			<td style="width:131px;"></td>
			<td></td>
		</tr>
	</tbody>
</table>

pretreatment of lignocellulosic biomass with low-cost ionic liquids

A number of ionic liquids (ILs) with economically attractive production costs have recently received growing interest as media for the delignification of a variety of lignocellulosic feedstocks. Here we demonstrate the use of these low-cost protic ILs in the deconstruction of lignocellulosic biomass (Ionosolv pretreatment), yielding cellulose and a purified lignin. In the most generic process, the protic ionic liquid is synthesized by accurate combination of aqueous acid and amine base. The water content is adjusted subsequently. For the delignification, the biomass is placed into a vessel with IL solution at elevated temperatures to dissolve the lignin and hemicellulose, leaving a cellulose-rich pulp ready for saccharification (hydrolysis to fermentable sugars). The lignin is later precipitated from the IL by the addition of water and recovered as a solid. The removal of the added water regenerates the ionic liquid, which can be reused multiple times. This protocol is useful to investigate the significant potential of protic ILs for use in commercial biomass pretreatment/lignin fractionation for producing biofuels or renewable chemicals and materials.

The exact amount of lignin removal and lignin precipitation, recovered pulp and glucose yield depend on the type of biomass used, the temperature at which the treatment is run and the duration of the treatment. Short pretreatment times and low temperatures lead to incomplete pretreatment while at higher temperatures the cellulose becomes unstable in the ionic liquid, leading to hydrolysis and degradation. The selected ionic liquid also plays an important role in the outcome of the fractio...

Watch this Scientific Journal Video about Pretreatment of Lignocellulosic Biomass with Low-cost Ionic Liquids at JoVE.com

Pretreatment of Lignocellulosic Biomass with Low-cost Ionic Liquids

The pretreatment of lignocellulosic biomass with protic low-cost ionic liquids is shown, resulting in a delignified cellulose-rich pulp and a purified lignin. The pulp gives rise to high glucose yields after enzymatic saccharification.

A number of ionic liquids (ILs) with economically attractive production costs have recently received growing interest as media for the delignification of ...

The overall goal of this experimental method is to use low-cost ionic liquids for isolating lignin and cellulose from lignocellulosic biomass and understand factors affecting the separation and isolation of these biopolymers. This method can help answer key questions in the biorefinery field, such as how to isolate cellulose and a novel lignin using low-cost ionic liquids. Our technique utilizes unique solvent properties of ionic liquids, but our advantage is that these ionic liquids can be easily synthesized using low-cost starting materials.Visual demonstration of this method is critical as there are numerous steps that are a lot easier to learn and carry out once you've seen it, rather than reading a page-long description. Demonstrating this procedure will be Florence, Clem, Wei-Chien, and Lisa. All of whom are graduate students in my laboratory.Determine the water content of the synthesized or purchased ionic liquid solution by volumetric Karl Fischer titration according to instructions issued by the titrator manufacturer. Add a few drops of the ionic liquid into the titrator using a pre-weighed syringe. Enter the weight of liquid added into the titrator and wait until the titrator displays a reading.Record the water content. Reduce the water content to five weight percent below the desired water content using a rotary evaporator, and confirm the new water content by Karl Fischer titration as before. Use 10 grams of ionic liquid solution containing 20 weight percent water and a biomass to solvent ratio of one to 10, and perform the necessary experimental calculations as described in the text protocol.Pre-weigh three 15 milliliter pressure tubes with Teflon caps and silicone O-rings. Visually inspect the pressure tubes to ensure they have no cracks or flaws. With a 10 milliliter pipette, add the required amount of ionic liquid solution into the pressure tube standing on the scale.Use cork rings to keep the tube standing up. Record the weight of the ionic liquid solution added. Then add the calculated amount of water to the solution using a pipette, assuming the density of water to be one gram per milliliter.Add the required amount of air-dried liquid lignocellulose by placing a piece of aluminum foil on a balance, tearing the balance, and weighing out the biomass. Tear the balance again and add the biomass to the tube. Place the empty foil back on the balance and record difference.Close the lid using a Teflon cap with the silicone O-ring. Check for a good seal without over-tightening. Record the weight of the pressure tubes containing the biomass and ionic liquid.Then mix the contents of the tube by using a vortex shaker until all of the biomass is in contact with the ionic liquid. Place the pressure tubes in a fan-assisted oven that has been preheated to the desired temperature. For example, leave the tubes for eight hours at 120 degrees Celsius or for one hour at 150 degrees Celsius.Remove the vials from the oven using an oven glove, and place them in a fume hood to let them cool to room temperature. Check the weight of the vials after cooling to assure no water escaped during cooking. Transfer the contents of each tube into a 50 milliliter centrifuge tube using 40 milliliters of absolute ethanol.Shake the tube using a vortex shaker for one minute to mix well, and leave the tube at room temperature for at least one hour. After vortexing for another 30 seconds, centrifuge the tube for 50 minutes at 2, 000 times G.Separate the liquid and solid by careful decanting. Collect the liquid in a clean 250 milliliter round bottom flask with a stir bar.Add 40 milliliters of fresh ethanol into the 15 milliliter falcon tube and repeat the mixing and centrifugation step three times. Remove the ethanol from the ionic liquid by placing the round bottom flasks on a heating block. Connect each flask to a vacuum pump with a cold trap.Fill the trap with dry ice and set the heating to 40 degrees Celsius. Then switch on the stirring and the pump. Transfer the wet-washed pulp into cellulose thimbles and label each thimble using a pencil.Fill 150 milliliters of absolute ethanol into a clean 250 milliliter round bottom flask with a stir bar. Insert the sample-containing thimble into a 40 milliliter soxhlet extractor and add a condenser. Install everything on the parallel extractor work station connected to a recirculating tiller.When all samples are loaded, begin stirring, set the temperature to 135 degrees Celsius and turn on the recirculator. After 20 hours of extraction, turn off the heating to allow refluxing to come to a halt. Then switch both stirring and cooling off.take the thimbles out of the soxhlet using tweazers, and let the wet pulp dry in the thimble overnight in a fume hood. Add the liquid from the soxhlet extraction to the liquid from the biomass wash and continue evaporating the ethanol from the biomass wash with the parallel evaporator or a rotary evaporator at 40 degrees Celsius. After transferring the air-dried pulp from the thimble onto a piece of teared aluminum foil on an analytical balance, record the air-dried weight of the extracted pulp and transfer it into a labeled plastic bag.Try to recover everything while not scraping thimble material off the wall. Determine the moisture content of the pulp immediately to calculate the oven-dried yield as described in the text protocol. When all of the ethanol has evaporated, precipitate the lignin by transferring the ionic liquid from the round bottom flask into a 50 milliliter centrifuge tube using 30 milliliters of water.Mix the suspension and leave it for at least one hour. Then centrifuge the suspension for 20 minutes at 2, 000 times G, and separate the solution from the solid by decanting. Add 30 milliliters of distilled water to the lignin pellet inside the centrifuge tube.Repeat the mixing incubation for one hour and centrifugation. Repeat this step for a total of three lignin washes. Dry the lignin inside the centrifuge tube using a vacuum oven and a pierced lid at 45 degrees Celsius overnight.To determine the lignin yield, place a piece of aluminum foil on the balance, tear the weight, add lignin from the oven, and record the weight immediately. Finally, transfer the lignin into a vial for storage. The amount of pulp and lignin isolated after pretreatment depends on the reaction conditions, the feedstock, and the ionic liquid.A typical time-course is presented here, where pulp yields initially decrease as lignin and hemicelluloses are extracted, while lignin yields increase over time. The lignin is isolated as a brown solid that had a faint but pleasant smell. The properties of the recovered cellulose pulp strongly depend on the conditions chosen.Running the pretreatment for too long or at too high temperatures will result in the degradation of the cellulose and formation of pseudo-lignin. More differences between the pulp properties become evident when subjecting it to further analysis, such as compositional analysis or enzymatic saccharification. Shown here is the compositional analysis of pine pulp and miscanthus pulp pretreated using same tenmerature and time.As can be seen, the pulp composition is very different as a result of the different types of biomass reacting differently to the same conditions. After watching this video, you should have a good understanding of how to perform pretreatment using low-cost ionic liquids and how to study different experimented parameters. Once mastered, this technique can be completed in around five days.This includes a lot of downtime and waiting, so other tasks can be performed in parallel. Following this procedure, other methods, such as compositional analysis of the pulp, saccharification of the pulp, or lignin NMR, and molecular weight analysis can be carried out. These will further characterize the isolated materials.I had the idea for this method when I discovered that certain ionic liquids move lignin from lignocellulosic biomass after absorbing moisture from air. By varying the water content before and after the pretreatment, I found that I could isolate the lignin easily by adding water after the extraction. Don't forget that working with acids and elevated temperatures can be hazardous, and personal protective equipment, such as lab specs, lab coats, and appropriate gloves, should always be worn while performing this procedure.

Research

JoVE Journal

Environment

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Experimental Protocol for Biodiesel Production with Isolation of Alkenones as Coproducts from Commercial Isochrysis Algal Biomass

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Measuring the Flight Ability of the Ambrosia Beetle, Platypus Quercivorus (Murayama), Using a Low-Cost, Small, and Easily Constructed Flight Mill

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Ammonia Fiber Expansion (AFEX) Pretreatment of Lignocellulosic Biomass

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A Novel Method for the Pentosan Analysis Present in Jute Biomass and Its Conversion into Sugar Monomers Using Acidic Ionic Liquid

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A Flexible Low Cost Hydroponic System for Assessing Plant Responses to Small Molecules in Sterile Conditions

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Construction of a Compact Low-Cost Radiation Shield for Air-Temperature Sensors in Ecological Field Studies

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Construction of a Low-cost Mobile Incubator for Field and Laboratory Use

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BtM, a Low-cost Open-source Datalogger to Estimate the Water Content of Nonvascular Cryptogams

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Visualization of Low-Level Gamma Radiation Sources Using a Low-Cost, High-Sensitivity, Omnidirectional Compton Camera

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