Electronic Supporting Information Comparison of Hydrogels Prepared with Ionic-Liquid-Isolated vs Commercial Chitin and Cellulose Xiaoping Shen,†,‡ Julia L. Shamshina,§ Paula Berton,†,║ Jenny Bandomir,† Hui Wang,† Gabriela Gurau§,║ Robin D. Rogers*,†,║ † ‡ Department of Chemistry, The University of Alabama, Tuscaloosa, AL 35487, USA Key Laboratory of Bio-based Material Science and Technology (Ministry of Education), Northeast Forestry University, 26 Hexing Road, Harbin 150040, China § ║ 525 Solutions, Inc., 720 2nd Street, Tuscaloosa, AL 35401, USA Department of Chemistry, McGill University, 801 Sherbrooke St. West, Montreal, QC H3A 0B8, Canada * Corresponding author. E-mail: [email protected] Electronic Supporting Information Comparison of Hydrogels Prepared with Ionic-Liquid-Isolated vs Commercial Chitin and Cellulose EXPERIMENTAL Materials. The IL, 1-ethyl-3-methylimidazolium acetate ([C2mim][OAc], >95%), was purchased from IoLiTec (Tuscaloosa, AL, USA). Deionized (DI) water with specific resistivity of 17.38 MΩ cm at 25 °C was obtained from a commercial deionizer (Culligan Co., Northbrook, IL). Acidic polyoxometalate (POM) in its hydrated form (H5[PV2Mo10O40]·29H2O) was donated by Japan New Metals Co. (Akita, Japan). Other chemical reagents, including sodium chlorite, glacial acetic acid, sodium hydroxide (NaOH) pellets (≥ 98%), urea (99.8%), epichlorohydrin (ECH, ≥ 99%), absolute ethanol, indigo carmine (dye content 91%), and phosphate buffer saline (PBS) tablets (one tablet was dissolved in 200 mL of DI water producing buffer solution of pH = 7.4), were all obtained from Sigma-Aldrich (St. Louis, MO) and used as received without further purification. Pure chitin (from crab shells) and practical grade chitin (PG-chitin; from crab shells) were purchased from Sigma-Aldrich (St. Louis, MO). PG-chitin was additionally purified by IL dissolution and regeneration (see below), obtaining the polymer denoted as Rec. PG. Chitin extracted from shrimp shells (SS, donated by the Gulf Coast Agricultural and Seafood Cooperative (Bayou La Batre, AL)) using [C2mim][OAc] via the procedure described in our previous papers1 (see below) was denoted as IL-chitin throughout the text. Microcrystalline cellulose (MCC) with a degree of polymerization of 270 was purchased from Sigma-Aldrich (Milwaukee, WI). Cellulose-rich materials (CRM-175 and CRM-POM) were reconstituted from poplar wood powder (Populus Alba, sapwood supplied by Harbin Yongxu Company, China) using the procedures described in our previous reports 2 , 3 (see below). All biomass and biopolymers were ground into powder using a lab mill (Janke & Kunkel Ika Labortechnik, Wilmington, NC), separated into different particle sizes of < 125, 125‒250, and 250‒1000 µm using brass sieves (Ika Labortechnik, Wilmington, NC), and stored in an oven (Precision Econotherm Laboratory Oven, Natick, MA) at 80 °C before use. S2 Electronic Supporting Information Comparison of Hydrogels Prepared with Ionic-Liquid-Isolated vs Commercial Chitin and Cellulose Reconstitution of PG-chitin with IL. Since the presence of insoluble traces in the solution of PG-chitin in NaOH/urea influenced the accuracy of viscosity measurement, PG-chitin was first reconstituted from its IL solution (Rec. PG-chitin). 0.4 g PG-chitin powder was added into 19.6 g [C2mim][OAc] in a 80 mL beaker. The mixture was heated at 100 °C for 1 h, then centrifuged at about 2000 rpm for 10 min (Dynac Becton Dickinson Centrifuge model 42010, Sparks, MD) to precipitate the undissolved residues. The supernatant solution was poured into 200 mL DI water to regenerate chitin from the solution. After stirring overnight, chitin was washed with DI water over ten times through centrifugation. The yield of Rec. PG-chitin was about 49.5%. Extraction of IL-chitin. Shrimp shells (SS) were dried at a specialized facility by pressing with a screw press and in a fluidized bed dryer at 160 °C until the material had a final moisture content of less than 5 wt%. This dried material was then pulverized with a hammer mill to particles with diameters ≤ 0.635 cm before shipping to The University of Alabama. 1.3 g of oven-dried SS powder was mixed with 63.7 g of [C2mim][OAc] in a 125 mL Erlenmeyer flask. The mixture was heated via microwave irradiation at 2‒3 s pulses with manual stirring between each pulse for 5 min until a honey-like solution was formed. The warm and flowable solution was transferred into two 50 mL centrifuge tubes and centrifuged at about 2000 rpm for 10 min to remove undissolved residues. The solution was carefully decanted into 400 mL of deionized (DI) water and stirred overnight. After settling for 4 h, the aqueous supernatant was carefully decanted and the remaining suspension was transferred into centrifuge tubes for centrifugation to remove the aqueous phase. Subsequently, fresh DI water was added to each of the centrifuge tubes and the resultant suspension was sonicated (Branson Sonicator 5510-DTH, Danbury, CT) for 20 min. Centrifugation, aqueous phase removal, fresh DI water addition, and sonication steps were consecutively repeated 10 more times. The regenerated chitin was oven-dried overnight at 90 °C, ground and sieved into particles with three different diameters of < 125, 125‒250, and > 250 µm. Ash content was determined as the final constant mass obtained by heating the dry sample in S3 Electronic Supporting Information Comparison of Hydrogels Prepared with Ionic-Liquid-Isolated vs Commercial Chitin and Cellulose a crucible in a muffle furnace at 525 °C.4 Chitin content was determined according to the Black and Schwartz methodology.5 Preparation of CRMs. The mixture of 0.5 g wood powder and 10 g [C2mim][OAc] in a 50 mL beaker was heated in an oil bath at 175 °C for 30 min with vigorous stirring. The biopolymer was then regenerated in 100 mL of water/acetone (1:1, v/v) and filtered to obtain CRM-175. The mixture of 0.5 g wood powder, 10 g [C2mim][OAc] and 0.05 g POM was heated at 110 °C for 2 h under stirring, and CRM-POM was obtained after regeneration in the same way. Determination of lignin content. The lignin content of the original wood and CRMs were determined by a scaled down TAPPI method.6 0.1 g of dried wood or CRM was placed into a 20 mL vial, and 1.5 mL (for wood) or 2.0 mL (for CRM) of 72 wt% H2SO4 aqueous solution was added. The mixture was stirred at room temperature for 2 h and then transferred to a 200 mL round-bottomed flask. The mixture was subsequently diluted with 56 mL (for wood) or 75 mL (for CRM) of DI water, and refluxed for 4 h. The resulting mixture was filtered and dried. Acid insoluble lignin (Klason lignin; LK) was determined gravimetrically. The filtrate was diluted to 200 mL with DI water, and the acid soluble lignin (LAS) was calculated from UV absorbance using the Cary 3C UV-visible Spectrometer (Palo Alto, CA) at 205 nm in Eq. (1): LAS 100% [( A 0.2 ) / 0.1] 110 (1) where A is the UV absorbance of the diluted filtrate, 110 is the extinction coefficient (L g-1 cm-1) of the lignin solution, 0.2 is the volume (L) of the diluted filtrate, and 0.1 is the mass (g) of the dried wood or CRM material used. Determination of hemicellulose content. The determination of hemicellulose content was based on NaClO2 delignification and NaOH treatment.2,7 1 g dried biomass and 37.5 mL DI water were transferred to a 100 mL round-bottom flask equipped with a 25 mL Erlenmeyer flask inverted in the neck of the reaction flask. 0.25 mL glacial acetic acid and 0.3 g sodium chlorite were added successively into the mixture. The flask was placed in an oil bath and heated at 75 °C for 1 h with magnetic stirring. An additional 0.25 mL glacial acetic acid and 0.3 g sodium S4 Electronic Supporting Information Comparison of Hydrogels Prepared with Ionic-Liquid-Isolated vs Commercial Chitin and Cellulose chlorite were added and the reaction mixture was heated for another 1 h. The addition of chemicals and one-hour heating were repeated 2 more times. After reaction, the flask was placed in a refrigerator to cool the reactants below 5 °C. The product was filtered using nylon filter paper, and washed with DI water and acetone successively. The resulting holocellulose (i.e., hemicellulose and cellulose) was oven-dried at 90 °C overnight and weighed. 12.5 mL NaOH aqueous solution (17.5 wt%) was added to a 100 mL beaker containing 0.5 g holocellulose obtained as above. The mixture was stirred at room temperature for 40 min, then 12.5 mL DI water was added to it. After 5 min, the residue was filtered, followed by adding 20 mL acetic acid aqueous solution (10 wt%). The residue was filtered again, and washed with 500 mL boiling water during filtration. The resulting cellulose was oven-dried at 90 °C overnight and weighed. The content of hemicellulose was the difference between the contents of holocellulose and cellulose. Selection of NaOH/urea System for each Biopolymer. Eight freshly-prepared NaOH/urea aqueous systems (2/0, 2/2, 4/4, 6/4, 7/12, 8/4, 12/6, 20/0 wt% NaOH/wt% urea) were used to dissolve 1 wt% of each biopolymer by freeze/thaw (F/T) treatment as follows: 0.02 g of biopolymer powder was added to 1.98 g of NaOH/urea solvent in a vial and the mixture was stirred at room temperature for 2 min. The mixture was then frozen by immersing the vial in a dry ice/ethanol cold bath (ca. -72 °C) for 3 min, followed by thawing at room temperature (ca. 8 min) and subsequent vigorous stirring (5 min). The F/T cycles were repeated several times to achieve full dissolution. If the biopolymer was not dissolved after 12 F/T cycles, it was then designated as insoluble. Viscosity determination of biopolymer solutions. Viscosity values of biopolymer solutions (1 wt%) in NaOH/urea systems were determined using a Cambridge Viscosity Viscometer (VISCOlab 3000, Medford, MA). The sample chamber of the viscometer was cooled by using PVC tubing which was filled with coolant mixture (a 50% v/v mixture of ethylene glycol/H2O) and chilled in a refrigerator before use. This tubing was wrapped around the stainless steel S5 Electronic Supporting Information Comparison of Hydrogels Prepared with Ionic-Liquid-Isolated vs Commercial Chitin and Cellulose exterior of the viscometer chamber to cool it below 10 °C. Approximately 0.7 mL of the biopolymer solution was transferred into the cooled chamber with a 1.0 mL syringe. The correct sized piston according to the expected viscosity range was selected and introduced into the chamber. Then the chamber was heated by the movement and friction between the piston and the solution during measurement. The viscosity and error values with the increase of temperature were recorded. Determination of Maximum Concentration Values. To determine the maximum concentration of a biopolymer that could be dissolved in the optimized NaOH/urea system using the F/T treatment, a 1 wt% biopolymer solution in NaOH/urea was initially prepared. Then, biopolymer was added to increase 0.1 wt% of its concentration in the solution, followed by its dissolution through F/T treatment. The addition of biopolymer was repeated until the solution solidified immediately after thawing at room temperature. Preparation of Physical Hydrogels. The maximum biopolymer concentrations that could be dissolved in the corresponding NaOH/urea system were used to form physical hydrogels. 1 g of the biopolymer/NaOH/urea solution was heated at temperatures of 30‒60 °C for different times, until firm hydrogels were formed. If after 24 h heating no firm gelation was observed, it was determined that no gel formation was possible using that biopolymer solution. The minimum biopolymer concentration needed to get firm physical hydrogels was also determined. 1 g of biopolymer/NaOH/urea solutions at concentrations of 1‒4 wt% were heated at 50 °C (for cellulose) or 60 °C (for chitin) for 4 h. The resulting hydrogels were transferred with a lab spoon into 100 mL of DI water. The water was changed every 8 h until the pH value was neutral (usually after 3 times). Preparation of Chemical Hydrogels. Biopolymers were dissolved in the corresponding NaOH/urea at different concentrations (1 and 2 wt% chitin solutions, 4 wt% MCC and CRM-POM solutions, and 1 wt% CRM-175 solution) using the F/T technique. Then, 0.1 g ECH (in excess relative to the ‒OH groups of the biopolymer in solution) was added as a cross-linker S6 Electronic Supporting Information Comparison of Hydrogels Prepared with Ionic-Liquid-Isolated vs Commercial Chitin and Cellulose to 1 g of the biopolymer solution and stirred at room temperature for 5 min. After removing the stir-bar, the solution was heated at 60 °C for 2 h (for chitinous solutions) or at 50 °C for 1 h (for cellulosic ones) in an oil bath. The obtained hydrogels were washed with 100 mL DI water for 24 h until neutral pH was achieved. Drying of hydrogels. After washing, three different drying techniques were used, i.e., oven-drying (80 °C, overnight), freeze-drying (here kept rotating on a rotary evaporator under vacuum when immersed into 0 °C bath), and supercritical-drying using CO2 (ScCO2-drying). No pretreatment of the hydrogels was needed before oven drying, while for freeze-drying, the hydrogel was frozen in liquid nitrogen before dehydrating. In the case of ScCO2-drying, the hydrogel was immersed in absolute ethanol (ca. 20 mL), and the ethanol was renewed two more times every 3 h, resulting in the formation of an alcogel. The alcogel was Sc-CO2 dried using a DCP-1 critical point dryer (Denton Vacuum Inc., Moorestown, NJ). The alcogel was Sc-CO2 dried using a DCP-1 critical point dryer (Denton Vacuum Inc., Moorestown, NJ). The sample chamber and its exhaust valve were immersed in a water bath (at room temperature), and connected to a liquid CO2 tank. After sealing the chamber for 10 min, the chamber exhaust valve was slightly opened to slowly bleed off the ethanol along with liquid CO2 (for 5 min). The chamber pressure was maintained within 800‒900 psi all along. This sealing/bleeding process was repeated 4 times, until ethanol was completely replaced by CO2. Once the drying was completed, all valves were closed; the cold water in the water bath was removed and replaced with hot water (ca. 50 °C). After the pressure in the chamber rose over 1800 psi, the exhaust valve was slightly opened to slowly vent the chamber, with pressure dropping not faster than 100 psi/min. The obtained aerogel was stored in a sealed vial before use. Calculation of ECH consumption. During hydrogel formation, the loss of biopolymers in the gel was caused by the removal of the stir bar before thermal gelation. Therefore, the real mass of ECH reacted with biopolymers in the chemical gels (mECH) was estimated under the S7 Electronic Supporting Information Comparison of Hydrogels Prepared with Ionic-Liquid-Isolated vs Commercial Chitin and Cellulose assumption that the mass of biopolymers in the chemical gel was equal to that in the physical gel of the same biopolymer concentration, which was calculated in Eq. (2): mECH M ECH nECH M ECH mgel mchemical m physical , M ECH M gel M ECH M Cl M H (2) where MECH is the relative molecular mass of ECH (92.5 g/mol), nECH the mole number of ECH, Δmgel the mass gain of the chemical gel due to the cross-linking compared with the physical gel, ΔMgel the relative molecular mass gain of the biopolymer in the chemical gel due to the cross-linking, mchemical the real mass of the chemical gel, mphysical the real mass of the physical gel. MCl and MH are the relative molecular mass of chlorine (35.5 g/mol) and hydrogen (1 g/mol), respectively. Shrinkage, Density, and Porosity. The shrinkage of the alcogels (Salco) and aerogels (Saero), in comparison with the original hydrogels, was calculated using Eqs. (3) and (4), respectively: Salco (%)= Saero (%)= Valcogel -Voriginal Voriginal Vaerogel -Voriginal Voriginal 100% (3) 100% (4) where Voriginal, Valcogel, and Vaerogel are the volumes of the original hydrogel, alcogel, and aerogel, respectively. The density and porosity of the aerogels were calculated using Eqs. (5) and (6), respectively: aerogel (g / cm3 )= Porosity (%)= (1- M aerogel Vaerogel aerogel ) 100% 8 OD (5) (6) where δaerogel, Maerogel, and Vaerogel are the density, mass, and volume of the aerogel, respectively, and δOD is the density of the corresponding oven-dried gel (assuming no pores were present). S8 Electronic Supporting Information Comparison of Hydrogels Prepared with Ionic-Liquid-Isolated vs Commercial Chitin and Cellulose Rehydration Measurement. An aerogel was immersed in a sealed vial filled with 20 mL DI water at room temperature for 24 h to fully rehydrate. Then the rehydrated hydrogel was taken out with a lab spoon and the water on the surface was gently removed using a Whatman filter paper. The rehydration kinetics of the hydrogel were studied by plotting the mass recovery of the rehydrated hydrogel at each time interval during rehydration, which was calculated using Eq. (7): Mass Recovery % = Mt M original 100% (7) where Mt and Moriginal are the masses of the rehydrated hydrogel at time t and the original hydrogel, respectively. When the hydrogel reached saturation (final time), the mass recovery of the fully rehydrated hydrogel was obtained. The rehydration ratio was calculated using Eq. (8): Rehydration Ratio % = M rehydrated M aerogel 100% (8) where Mrehydrated and Maerogel are the masses of the fully rehydrated hydrogel and the aerogel, respectively. Dye loading and release. 0.005 g indigo carmine dye was dissolved in 5 mL phosphate buffer saline (PBS) solution (pH 7.4) with stirring, to obtain a dye/PBS solution of 1 mg/mL. Further dilutions (0.015, 0.01, 0.008, 0.005, 0.002, and 0.001 mg/mL) were then prepared, and a standard calibration curve of dye concentration was acquired by measuring the absorbance of these 6 groups of dilute dye solutions at 610 nm using a Cary 3C UV-visible Spectrophotometer (Palo Alto, CA). The obtained calibration curve (Fig. S1) showed a good linear correlation (R2=0.99633). S9 Electronic Supporting Information Comparison of Hydrogels Prepared with Ionic-Liquid-Isolated vs Commercial Chitin and Cellulose Fig. S1. Standard calibration curve of dilute dye (indigo carmine) aqueous solutions. To load the dye, there were two methods: a) immersing an aerogel in 5 mL of 1 mg/mL dye aqueous solution, or b) immersing an aerogel in 5 mL of 0.5 mg/mL dye/ethanol solution (due to the lower saturation concentration) in a sealed vial at 25 °C for 24 h. After loading, the hydrogels were taken out and wiped gently with filter paper to remove the dye solution on the surface. The loaded hydrogels from method "a" were transferred into 50 mL fresh PBS to test the dye release, while the ones from method "b" were ScCO2-dried again to conduct PXRD test. For release, the beaker containing the loaded hydrogel and PBS solution was placed in a C25 incubator shaker (New Brunswick Scientific Co., Edison, NJ) at 25 °C and 100 rpm. At certain time intervals, 2 mL of the dye/PBS solution was taken out, diluted to 4 mL with fresh PBS solution, and analyzed by UV-Vis spectrometry. The withdrawn solutions were replaced with 2 mL fresh PBS solution to maintain constant volume of the release medium. The total loading mass (Mloading) of the hydrogels was estimated by determining the dye mass remaining in the loading solution (after dilution). The cumulative dye release of the hydrogel in PBS was then quantified as mass released at time t (Mt) over Mloading. S10 Electronic Supporting Information Comparison of Hydrogels Prepared with Ionic-Liquid-Isolated vs Commercial Chitin and Cellulose Characterization Methods. Powder X-ray diffraction (PXRD) analyses of biopolymers and aerogels were performed at room temperature using a Rigaku D/MAX-2BX horizontal X-ray diffractometer (Rigaku Co., Spring, TX) equipped with Cu-Kα radiation (λ= 1.5418 Å). The samples were scanned within 5–35o (2θ) in continuous mode with a step size of 0.02° and step time of 3 degrees/s. For scanning electron microscopy (SEM), the surface and cross-section of ScCO2-dried aerogels were mounted onto an aluminum sample stub with carbon tape. Cellulosic aerogels were sputter-coated with a gold–palladium alloy to get clearer images (due to the higher magnification used) using an Anatech Hummer 6.6 sputter coater (Union City, CA). Samples were placed into the sample chamber of the Hitachi S-2500 Scanning Electron Microscope (Hitachi Ltd., Tokyo, Japan). SEM was operated at 10 kV accelerating voltage and under high vacuum in the chamber. S11 Electronic Supporting Information Comparison of Hydrogels Prepared with Ionic-Liquid-Isolated vs Commercial Chitin and Cellulose RESULTS AND DISCUSSION Composition of biopolymers Table S1. Chemical Composition of Chitin and Cellulosic Materials. Ash contentb Chitin (%) contentb (%) N/A 34.5(7) 27.2(9) C, N, O, Si, Ca, Mg Pure chitin N/A 0.3(1) 81.8(4) C, N, O PG-chitin N/A 2.2(4) 78.9(7) C, N, O, Si, Cl, Ca IL-chitin 20.8(8) 89.1(5) C, N, O ,Si Chitin Yielda (%) Shrimp shell Cellulosea a CRM yield 0.5(2) a Lignin yield d Lignin b Containing elementsc Hemicellulose b Cellulose (%W) (%L) content (%) content (%) contentb (%) Poplar wood N/A N/A 22.3(6) 30.3(7) 47.4(1) CRM-175 57.6(4) 35.9(5) 12.2(3) 27.0(6) 60.8(3) CRM-POM 60.7(8) 1.0(1) 13.7(4) 6.2(6) 80.1(2) Yield: mass percentage of the recovered biopolymer to the raw material; b Component content: mass c percentage of the component in chitin or CRM; Data were obtained from Ref. 9; d Lignin yield: with regard to lignin in the original wood. S12 Electronic Supporting Information Comparison of Hydrogels Prepared with Ionic-Liquid-Isolated vs Commercial Chitin and Cellulose Viscosity of biopolymer solutions in NaOH/urea Viscosity curves of PG-, IL-chitin, and CRM-175 solutions of 1 wt% concentration showed a slope change point as temperature increased (Fig. S2), which may result from the entanglement of biopolymer chains in the solution. This "junction temperature" varied with different biopolymers, e.g., 28.3 °C for PG-chitin, 27.8 °C for IL- chitin, and 25.5 °C for CRM-175. On the other hand, pure chitin, CRM-POM, and MCC solutions seemed not to entangle at this concentration during viscosity determination, probably due to their lower MWs. Fig. S2. Viscosity of (a) chitin and (b) cellulose solutions (1 wt%) in NaOH/urea as a function of temperature. S13 Electronic Supporting Information Comparison of Hydrogels Prepared with Ionic-Liquid-Isolated vs Commercial Chitin and Cellulose Preparation of physical hydrogels Table S2. Effect of Temperature on Curing Time in Formation of Physical Hydrogels of Chitin and Cellulose at Maximum Concentrations.a Cellulose Chitin Biopolymer a 30 °C Pure chitin Pseudo PG-chitin c 40 °C 50 °C 60 °C Pseudo Pseudo Pseudo 10 h 5h 3h 2h b Rec. PG Pseudo Pseudo Pseudo Pseudo IL-chitin > 12 h 7h 5h 4h MCC Pseudo Pseudo Pseudo Pseudo CRM-POM Pseudo Pseudo Pseudo Pseudo CRM-175 > 12 h 7h 4h 3h Maximum concentrations and their preparation are noted in Table 1; PG-chitin from [C2mim][OAc] to remove impurities; c b Rec. PG: Reconstituted Pseudo-hydrogel: The resulting gel was not strong enough to maintain integrity during transfer independent of heating time. Structural confirmation of chemical cross-linking - FTIR spectroscopy Fig. S3. FTIR spectra of physical and chemical chitin gels. S14 Electronic Supporting Information Comparison of Hydrogels Prepared with Ionic-Liquid-Isolated vs Commercial Chitin and Cellulose Drying methods Fig. S4. Dry chitin and cellulose gels after oven-drying (left), freeze-drying (middle), and ScCO2-drying (right). Chitin gel code XX-m-n, where XX represents the chitin type, m is the chitin concentration, and n is the mass ratio of ECH to chitin. PXRD of aerogels Fig. S5. PXRD patterns of (a) chitin and (b) cellulose particles and corresponding gels after different drying methods. S15 PXRD of loaded aerogels Fig. S6. PXRD patterns of chitin (IL-chitin) and cellulose (CRM-175) aerogels loaded with dye molecules. Electronic Supporting Information Comparison of Hydrogels Prepared with Ionic-Liquid-Isolated vs Commercial Chitin and Cellulose Table S3. Volumes and Masses of Chitin and Cellulose Gels (Original, Alco-, and Aerogels) during Preparation Processes. Items Dimensions (D/h, mm/mm) Volume 3 (cm ) Mass (g) Gel type Physical chitin gels Physical Chemical cellulose gels cellulose gels PG-1-10 IL-1-10 PG-2-5 IL-2-5 PG-2-0 IL-2-0 MCC CRM-POM CRM-175 Ph-CRM-175 Original 13.0/7.0 13.0/7.0 13.0/7.0 13.5/7.5 12.0/6.0 13.0/6.0 13.0/19.0/10.0 19.0/10.0 14.5/8.0 7.0/4.0 Alcogel 11.5/6.0 11.0/6.0 12.5/7.0 12.0/7.0 12.0/6.0 13.0/6.0 8.0/15.0/4.5 13.0/6.0 10.0/7.0 7.0/4.0 Aerogel 9.5/5.5 9.0/5.0 11.0/6.0 10.5/6.5 12.0/6.0 12.0/5.5 7/12.0/3.5 11.0/5.5 7.0/4.0 7.0/4.0 Rehydrated 10/4.5 12.0/5.5 12.0/6.5 13.0/7.5 12.0/6.0 12.5/7.0 12.0/17.0/7.0 12.5/7.5 12.0/6.0 6.5/4.0 Original 0.93(2) 0.93(3) 0.93(1) 1.1(2) 0.68(1) 0.80(1) 2.0(1) 2.8(2) 1.3(1) 0.15(1) Alcogel 0.61(2) 0.58(2) 0.85(3) 0.80(3) 0.67(2) 0.78(3) 0.48(1) 0.81(2) 0.56(2) 0.15(1) Aerogel 0.40(2) 0.33(1) 0.57(1) 0.56(1) 0.67(1) 0.63(1) 0.25(2) 0.52(2) 0.17(1) 0.15(1) Rehydrated 0.36(2) 0.63(2) 0.75(3) 0.99(3) 0.68(1) 0.75(2) 1.2(1) 0.92(3) 0.69(4) 0.13(1) Original 0.96(4) 0.94(3) 1.0(1) 1.0(1) 0.75(3) 0.79(3) 2.3(3) 3.5(1) 1.7(1) 0.17(1) Alcogel 0.39(2) 0.40(3) 0.66(2) 0.65(2) 0.58(2) 0.60(2) 0.39(2) 0.55(3) 0.33(3) 0.13(1) a a 0.043(1) 0.041(2) 0.0099(1) 0.0090(1) 0.061 0.0566 0.0132 0.01 0.92(2) 0.14(1) Aerogel 0.0096(3) 0.00097(3) 0.019(1) 0.019(1) 0.017 Theoretical 0.0128 0.0128 0.0255 0.0255 0.02 Rehydrated a Chemical chitin gels 0.37(2) 0.62(2) 0.76(3) 0.92(3) 0.62(2) 0.017 0.02 0.74(3) 1.2 a 1.3 a The error was too small; Chitin gel code: XX-m-n: XX represents the chitin type, m is the chitin concentration, and n is the mass ratio of ECH to chitin. S17 Electronic Supporting Information Comparison of Hydrogels Prepared with Ionic-Liquid-Isolated vs Commercial Chitin and Cellulose References (1) Shamshina, J. L.; Gurau, G.; Block, L. E.; Hansen, L. K.; Dingee, C.; Walters, A.; Rogers, R. D. Chitin-calcium alginate composite fibers for wound care dressings spun from ionic liquid solution. J. Mater. Chem. B 2014, 2, 3924-3936. (2) Li, W.; Sun, N.; Stoner, B.; Jiang, X.; Lu, X.; Rogers, R. D. Rapid dissolution of lignocellulosic biomass in ionic liquids using temperatures above the glass transition of lignin. Green Chem. 2011, 13, 2038-2047. (3) Cheng, F.; Wang, H.; Rogers, R. D. Oxygen enhances polyoxometalate-based catalytic dissolution and delignification of woody biomass in ionic liquids. ACS Sustain. Chem. Eng. 2014, 2, 2859-2865. (4) AOAC. In Official Methods of Analysis of the Association of Official Analytical Chemists, 13th ed.; W. Horwitz, Ed.; AOAC international: Washington, DC, 1980, pp 289, 508. (5) Miss, M. M. Black; Schwartz, H. M. The estimation of chitin and chitin nitrogen in crawfish waste and derived products. Analyst 1950, 75, 185-189. (6) Sun, N.; Rahman, M.; Qin, Y.; Maxim, M. L.; Rodríguez, H.; Rogers, R. D. Complete dissolution and partial delignification of wood in the ionic liquid 1-ethyl-3-methylimidazolium acetate. Green Chem. 2009, 11, 646-655. (7) Teramoto, Y.; Lee, S. H.; Endo, T. Pretreatment of woody and herbaceous biomass for enzymatic saccharification using sulfuric acid-free ethanol cooking. Bioresource Technol. 2008, 99, 8856-8863. (8) Silva, S. S.; Duarte, A. R. C.; Carvalho, A. P.; Mano, J. F.; Reis, R. L. Green processing of porous chitin structures for biomedical applications combining ionic liquids and supercritical fluid technology. Acta Biomater. 2011, 7, 1166-1172. (9) Qin, Y.; Lu, X.; Sun, N.; Rogers, R. D. Dissolution or extraction of crustacean shells using ionic liquids to obtain high molecular weight purified chitin and direct production of chitin films and fibers. Green Chem. 2010, 12, 968-971. S18
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