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Featured researches published by Kim Tran.


Green Chemistry | 2015

Design of low-cost ionic liquids for lignocellulosic biomass pretreatment

Anthe George; Agnieszka Brandt; Kim Tran; Shahrul M. S. Nizan S. Zahari; Daniel Klein-Marcuschamer; Ning Sun; Noppadon Sathitsuksanoh; Jian Shi; Vitalie Stavila; Ramakrishnan Parthasarathi; Seema Singh; Bradley M. Holmes; Tom Welton; Blake A. Simmons; Jason P. Hallett

The cost of ionic liquids (ILs) is one of the main impediments to IL utilization in the cellulosic biorefinery, especially in the pretreatment step. In this study, a number of ionic liquids were synthesized with the goal of optimizing solvent cost and stability whilst demonstrating promising processing potential. To achieve this, inexpensive feedstocks such as sulfuric acid and simple amines were combined into a range of protic ionic liquids containing the hydrogen sulfate [HSO4]− anion. The performance of these ionic liquids was compared to a benchmark system containing the IL 1-ethyl-3-methylimidazolium acetate [C2C1im][OAc]. The highest saccharification yields were observed for the triethylammonium hydrogen sulfate IL, which was 75% as effective as the benchmark system. Techno-economic modeling revealed that this promising and yet to be optimized yield was achieved at a fraction of the processing cost. This study demonstrates that some ILs can compete with the cheapest pretreatment chemicals, such as ammonia, in terms of effectiveness and process cost, removing IL cost as a barrier to the economic viability of IL-based biorefineries.


Proceedings of the National Academy of Sciences of the United States of America | 2014

Efficient biomass pretreatment using ionic liquids derived from lignin and hemicellulose

Aaron M. Socha; R. Parthasarathi; Jian Shi; Sivakumar Pattathil; Dorian Whyte; Maxime Bergeron; Anthe George; Kim Tran; Vitalie Stavila; Sivasankari Venkatachalam; Michael G. Hahn; Blake A. Simmons; Seema Singh

Significance Ionic liquids (ILs) have unique properties applicable to a variety of industrial processes. Nearly universal solvating capabilities, low vapor pressures, and high thermal stabilities make these compounds ideal substitutes for a wide range of organic solvents. To date, the best performing ILs are derived from nonrenewable sources such as petroleum or natural gas. Due to their potential for large-scale deployment, ILs derived from inexpensive, renewable reagents are highly desirable. Herein, we describe a process for synthesizing ILs from materials derived from lignin and hemicellulose, major components of terrestrial plant biomass. With respect to overall sugar yield, experimental evaluation of these compounds showed that they perform comparably to traditional ILs in biomass pretreatment. Ionic liquids (ILs), solvents composed entirely of paired ions, have been used in a variety of process chemistry and renewable energy applications. Imidazolium-based ILs effectively dissolve biomass and represent a remarkable platform for biomass pretreatment. Although efficient, imidazolium cations are expensive and thus limited in their large-scale industrial deployment. To replace imidazolium-based ILs with those derived from renewable sources, we synthesized a series of tertiary amine-based ILs from aromatic aldehydes derived from lignin and hemicellulose, the major by-products of lignocellulosic biofuel production. Compositional analysis of switchgrass pretreated with ILs derived from vanillin, p-anisaldehyde, and furfural confirmed their efficacy. Enzymatic hydrolysis of pretreated switchgrass allowed for direct comparison of sugar yields and lignin removal between biomass-derived ILs and 1-ethyl-3-methylimidazolium acetate. Although the rate of cellulose hydrolysis for switchgrass pretreated with biomass-derived ILs was slightly slower than that of 1-ethyl-3-methylimidazolium acetate, 90–95% glucose and 70–75% xylose yields were obtained for these samples after 72-h incubation. Molecular modeling was used to compare IL solvent parameters with experimentally obtained compositional analysis data. Effective pretreatment of lignocellulose was further investigated by powder X-ray diffraction and glycome profiling of switchgrass cell walls. These studies showed different cellulose structural changes and differences in hemicellulose epitopes between switchgrass pretreatments with the aforementioned ILs. Our concept of deriving ILs from lignocellulosic biomass shows significant potential for the realization of a “closed-loop” process for future lignocellulosic biorefineries and has far-reaching economic impacts for other IL-based process technology currently using ILs synthesized from petroleum sources.


Biotechnology for Biofuels | 2013

Production and extraction of sugars from switchgrass hydrolyzed in ionic liquids

Ning Sun; Hanbin Liu; Noppadon Sathitsuksanoh; Vitalie Stavila; Manali Sawant; Anaise Bonito; Kim Tran; Anthe George; Kenneth L. Sale; Seema Singh; Blake A. Simmons; Bradley M. Holmes

BackgroundThe use of Ionic liquids (ILs) as biomass solvents is considered to be an attractive alternative for the pretreatment of lignocellulosic biomass. Acid catalysts have been used previously to hydrolyze polysaccharides into fermentable sugars during IL pretreatment. This could potentially provide a means of liberating fermentable sugars from biomass without the use of costly enzymes. However, the separation of the sugars from the aqueous IL and recovery of IL is challenging and imperative to make this process viable.ResultsAqueous alkaline solutions are used to induce the formation of a biphasic system to recover sugars produced from the acid catalyzed hydrolysis of switchgrass in imidazolium-based ILs. The amount of sugar produced from this process was proportional to the extent of biomass solubilized. Pretreatment at high temperatures (e.g., 160°C, 1.5 h) was more effective in producing glucose. Sugar extraction into the alkali phase was dependent on both the amount of sugar produced by acidolysis and the alkali concentration in the aqueous extractant phase. Maximum yields of 53% glucose and 88% xylose are recovered in the alkali phase, based on the amounts present in the initial biomass. The partition coefficients of glucose and xylose between the IL and alkali phases can be accurately predicted using molecular dynamics simulations.ConclusionsThis biphasic system may enable the facile recycling of IL and rapid recovery of the sugars, and provides an alternative route to the production of monomeric sugars from biomass that eliminates the need for enzymatic saccharification and also reduces the amount of water required.


Green Chemistry | 2016

Switchable ionic liquids based on di-carboxylic acids for one-pot conversion of biomass to an advanced biofuel

Michael Liszka; Aram Kang; N. V. S. N. Murthy Konda; Kim Tran; John M. Gladden; Seema Singh; Jay D. Keasling; Corinne D. Scown; Taek Soon Lee; Blake A. Simmons; Kenneth L. Sale

Certain ionic liquids have recently been developed as effective solvents for biomass pretreatment, but their adoption has been limited due to availability, production costs, and inhibitory effects on conventional enzymes and microorganisms. We describe here a novel class of ionic liquids based on di-carboxylic acids that have high pretreatment efficiency and are compatible with both commercial enzyme mixtures and microbial fermentation host organisms. This system takes advantage of the two ionization states of di-carboxylic acids to switch from a basic solution that pretreats biomass effectively to an acidic solution with conditions favorable for cellulases and back again for the next round of pretreatment. Lab-scale reactions show 90% conversion of lignocellulosic biomass to fermentable sugars using commercial enzyme mixtures in a one-pot process. We then demonstrate E. coli fermentation of the resulting crude hydrolysate to produce isopentenol without removal of the ionic liquid or inhibitors prior to fermentation. This new process yields high biomass conversion and eliminates several technical and economic problems associated with current ionic liquid-based processes. Our preliminary techno-economic analysis (TEA) suggests biorefineries designed to use these switchable ILs can reduce the minimum selling price (MSP) of their biofuel by more than


Biotechnology for Biofuels | 2017

Ternary ionic liquid–water pretreatment systems of an agave bagasse and municipal solid waste blend

Jose A. Perez-Pimienta; Noppadon Sathitsuksanoh; Vicki S. Thompson; Kim Tran; Teresa Ponce-Noyola; Vitalie Stavila; Seema Singh; Blake A. Simmons

1 gal−1 relative to biorefineries utilizing traditional ILs (e.g., [C2C1Im][OAc]) that have been shown to be very effective at pretreatment but inhibit downstream saccharification and fermentation processes, requiring extensive washing of the pretreated biomass.


Bioenergy Research | 2015

Cell Wall Composition and Bioenergy Potential of Rice Straw Tissues Are Influenced by Environment, Tissue Type, and Genotype

Paul Tanger; Miguel E. Vega-Sánchez; Margaret B. Fleming; Kim Tran; Seema Singh; James B. Abrahamson; Courtney E. Jahn; Nicholas Santoro; Elizabeth Naredo; Marietta Baraoidan; John Danku; David E. Salt; Kenneth L. McNally; Blake A. Simmons; Pamela C. Ronald; Hei Leung; Daniel R. Bush; John K. McKay; Jan E. Leach

BackgroundPretreatment is necessary to reduce biomass recalcitrance and enhance the efficiency of enzymatic saccharification for biofuel production. Ionic liquid (IL) pretreatment has gained a significant interest as a pretreatment process that can reduce cellulose crystallinity and remove lignin, key factors that govern enzyme accessibility. There are several challenges that need to be addressed for IL pretreatment to become viable for commercialization, including IL cost and recyclability. In addition, it is unclear whether ILs can maintain process performance when utilizing low-cost, low-quality biomass feedstocks such as the paper fraction of municipal solid waste (MSW), which are readily available in high quantities. One approach to potentially reduce IL cost is to use a blend of ILs at different concentrations in aqueous mixtures. Herein, we describe 14 IL-water systems with mixtures of 1-ethyl-3-ethylimidazolium acetate ([C2C1Im][OAc]), 1-butyl-3-ethylimidazolium acetate ([C4C1Im][OAc]), and water that were used to pretreat MSW blended with agave bagasse (AGB). The detailed analysis of IL recycling in terms of sugar yields of pretreated biomass and IL stability was examined.ResultsBoth biomass types (AGB and MSW) were efficiently disrupted by IL pretreatment. The pretreatment efficiency of [C2C1Im][OAc] and [C4C1Im][OAc] decreased when mixed with water above 40%. The AGB/MSW (1:1) blend demonstrated a glucan conversion of 94.1 and 83.0% using IL systems with ~10 and ~40% water content, respectively. Chemical structures of fresh ILs and recycle ILs presented strong similarities observed by FTIR and 1H-NMR spectroscopy. The glucan and xylan hydrolysis yields obtained from recycled IL exhibited a slight decrease in pretreatment efficiency (less than 10% in terms of hydrolysis yields compared to that of fresh IL), and a decrease in cellulose crystallinity was observed.ConclusionsOur results demonstrated that mixing ILs such as [C2C1Im][OAc] and [C4C1Im][OAc] and blending the paper fraction of MSW with agricultural residues, such as AGB, may contribute to lower the production costs while maintaining high sugar yields. Recycled IL-water mixtures provided comparable results to that of fresh ILs. Both of these results offer the potential of reducing the production costs of sugars and biofuels at biorefineries as compared to more conventional IL conversion technologies.Graphical abstractSchematic of ionic liquid (IL) pretreatment of agave bagasse (AB) and paper-rich fraction of municipal solid waste (MSW)


Green Chemistry | 2017

Development of an integrated approach for α-pinene recovery and sugar production from loblolly pine using ionic liquids

Gabriella Papa; James Kirby; N. V. S. N. Murthy Konda; Kim Tran; Seema Singh; Jay D. Keasling; Gary F. Peter; Blake A. Simmons

Breeding has transformed wild plant species into modern crops, increasing the allocation of their photosynthetic assimilate into grain, fiber, and other products for human use. Despite progress in increasing the harvest index, much of the biomass of crop plants is not utilized. Potential uses for the large amounts of agricultural residues that accumulate are animal fodder or bioenergy, though these may not be economically viable without additional efforts such as targeted breeding or improved processing. We characterized leaf and stem tissue from a diverse set of rice genotypes (varieties) grown in two environments (greenhouse and field) and report bioenergy-related traits across these variables. Among the 16 traits measured, cellulose, hemicelluloses, lignin, ash, total glucose, and glucose yield changed across environments, irrespective of the genotypes. Stem and leaf tissue composition differed for most traits, consistent with their unique functional contributions and suggesting that they are under separate genetic control. Plant variety had the least influence on the measured traits. High glucose yield was associated with high total glucose and hemicelluloses, but low lignin and ash content. Bioenergy yield of greenhouse-grown biomass was higher than field-grown biomass, suggesting that greenhouse studies overestimate bioenergy potential. Nevertheless, glucose yield in the greenhouse predicts glucose yield in the field (ρ = 0.85, p < 0.01) and could be used to optimize greenhouse (GH) and field breeding trials. Overall, efforts to improve cell wall composition for bioenergy require consideration of production environment, tissue type, and variety.


Green Chemistry | 2011

The effect of ionic liquid cation and anion combinations on the macromolecular structure of lignins

Anthe George; Kim Tran; Trevor J. Morgan; Peter I. Benke; C. Berrueco; Esther Lorente; Ben C. Wu; Jay D. Keasling; Blake A. Simmons; Bradley M. Holmes

In the southeastern US, loblolly pine (Pinus taeda L.) is widely used as a feedstock in the wood, pulp and paper industry. In loblolly pine, the oleoresin is composed of terpenes and has long been a valuable source for a variety of chemicals, and has recently attracted interest from a biofuel perspective for the production of advanced cellulosic biofuels. To date, there have been very few examples where a single conversion process has enabled recovery of both terpenes and fermentable sugars in an integrated fashion. We have used the ionic liquid (IL), 1-ethyl-3-methylimidazolium acetate [C2C1Im][OAc] at 120 °C and 160 °C in conjunction with analytical protocols using GC-MS, to extract α-pinene and simultaneously pretreat the pine to generate high yields of fermentable sugars after saccharification. Compared to solvent extraction, the IL process enabled higher recovery rates for α-pinene, from three tissues type of loblolly pine, i.e. pine chips from forest residues (FC), stems from young pine (YW) and lighter wood (LW), while also generating high yields of fermentable sugars following saccharification. We propose that this combined terpene extraction/lignocellulose pretreatment approach may provide a compelling model for a biorefinery, reducing costs and increasing commercial viability. Our preliminary techno-economic analysis (TEA) revealed that the α-pinene recovery based on hexane extraction after IL pretreatment could reduce the minimum ethanol selling price (MESP) of ethanol generated from fermentation of sugars recovered from pine by


International Journal of Hydrogen Energy | 2009

Scalable synthesis of nanoporous palladium powders.

David B. Robinson; Stephen J. Fares; Markus D. Ong; Ilke Arslan; Mary E. Langham; Kim Tran; W. Miles Clift

0.6–1.0 per gal.


ChemistrySelect | 2016

Sugars Production for Green Chemistry from 2nd Generation Crop (Arundo donax L.): A Full Field Approach.

Luca Corno; Roberto Pilu; Kim Tran; Fulvia Tambone; Seema Singh; Blake A. Simmons; Fabrizio Adani

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Blake A. Simmons

Lawrence Berkeley National Laboratory

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Seema Singh

Sandia National Laboratories

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Anthe George

Sandia National Laboratories

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Bradley M. Holmes

Sandia National Laboratories

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David B. Robinson

Sandia National Laboratories

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Markus D. Ong

Sandia National Laboratories

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Mary E. Langham

Sandia National Laboratories

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Vitalie Stavila

Sandia National Laboratories

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Noppadon Sathitsuksanoh

Lawrence Berkeley National Laboratory

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Stephen J. Fares

Sandia National Laboratories

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