University of Nebraska - Lincoln DigitalCommons@University of Nebraska - Lincoln Biological Systems Engineering--Dissertations, Theses, and Student Research Biological Systems Engineering 7-2014 Characterization of Genetically Modified High Biomass Producing Tobacco Plant Pankaj Singh Kuhar University of Nebraska-Lincoln, [email protected] Follow this and additional works at: http://digitalcommons.unl.edu/biosysengdiss Part of the Bioresource and Agricultural Engineering Commons, and the Plant Breeding and Genetics Commons Kuhar, Pankaj Singh, "Characterization of Genetically Modified High Biomass Producing Tobacco Plant" (2014). Biological Systems Engineering--Dissertations, Theses, and Student Research. Paper 44. http://digitalcommons.unl.edu/biosysengdiss/44 This Article is brought to you for free and open access by the Biological Systems Engineering at DigitalCommons@University of Nebraska - Lincoln. It has been accepted for inclusion in Biological Systems Engineering--Dissertations, Theses, and Student Research by an authorized administrator of DigitalCommons@University of Nebraska - Lincoln. Characterization of Genetically Modified High Biomass Producing Tobacco Plant by Pankaj S. Kuhar A THESIS Presented to the Faculty of The Graduate College at the University of Nebraska In Partial Fulfillment of Requirements For the Degree of Master of Science Major: Agricultural and Biological Systems Engineering Under the Supervision of Professor Deepak R. Keshwani Lincoln, Nebraska July 2014 Characterization of Genetically Modified High Biomass Producing Tobacco Plant Pankaj S. Kuhar, M.S. University of Nebraska, 2014 Advisor: Deepak R. Keshwani Global warming and peak oil has clouded our energy security. In light of this situation, bioethanol as emerged as one of the most amenable solutions to the problem. However bioethanol has its own shortcomings and transgenics seem imperative to exploit its full potential. A high biomass producing line in transgenic tobacco (Nicotiana tabacum cv. Xanthi) was identified during a routine genetic transformation, termed giant recombinant (GR). To characterize the phenotype of the giant line, growth rate and lignocellulosic composition was analyzed relative to the non-transgenic control line. The GR line accounted for 240% more biomass than the untransformed line within 135 days of its germination. Furthermore, there were significant differences in chemical composition within GR line relative to a control line. The GR characteristics are likely due to disruption or activation of an unknown plant gene. Identification of the GR gene responsible for increased biomass productivity could lead to improvement of other plant species to develop feed-stocks for bio-based energy. iii ACKNOWLEDGEMENTS I would like to express my heartfelt regards to my mentors Dr. Deepak R. Keshwani and Dr. Amitava Mitra for their constant support, patience and wisdom. I would like thank Dr. George Meyer for his help and guidance, and my loved ones for their irreplaceable support. iv TABLE OF CONTENTS Pages CHAPTER 1: A Review of Plant Genetic Engineering as a New Tool for Cellulosic Ethanol……………..………………………………………………………………… ….6 Abstract……………………………………………….......................................................6 Introduction ………………………………………………………………………………7 Cellulosic ethanol overview………………………………………………………………9 Genetic manipulation of biomass feedstock……………………………………………..11 Reducing pretreatment cost.……………………………………………………………..13 In planta enzyme production …………………………………………………………....15 Conclusion……………………………………………………………………………….18 References ………………………………………………………….…………………...19 CHAPTER 2: Characterization of Genetically Modified High Biomass Producing Tobacco Plant..…..……………………………………………………………………....25 Introduction …………………………………………………………..............................26 v Material and Methods …………………………………………………………………...28 Result and Discussion …………………………………………………………………...32 Conclusion …..…………………………………………………………………………..49 References …...…………………………………………………………………………..50 APPENDIX Sample SAS code.………………………………………………………………………..56 Files included in CD-ROM………………………………………………………………57 6 Chapter1 A Review of Plant Genetic Engineering as a New Tool for Cellulosic Ethanol Abstract Global warming and peak oil price and availability have threatened our energy security. In light of this situation, bioethanol as emerged as a possible amenable solution to the problem. Developments in sugarcane and corn ethanol have established a potential market for biofuels; however, production is limited due to competition for food and feed. Whereas cellulosic ethanol is a more favorable solution with abundant supplies of nonfood based lignocellulosic biomass around the world. However, due to limitations of the current conversion technology and in vitro enzyme production for cellulosic ethanol, cellulosic ethanol becomes an expensive alternative compared to other solutions. Fortunately with recent developments in plant genetic engineering, it is possible to produce cellulases and hemicellulases in plant systems, improve crop biomass production, and modify its secondary cell wall structure such that would in turn improve ethanol yield per se. 7 Introduction Global warming and fluctuating oil prices have created an international unrest with regard to the future energy security. For instance, rapid industrialization in countries like India and China have increased their dependence on crude oil imports, consequently affecting their economic growth. Even developed nations like United States of America are not left alone, increasing their dependence on foreign petroleum reserves while competing with the international demand undermining economic stability and future energy security1,4. For example, China needs a clear air policy with rising carbon dioxide levels globally. No nation either developing or developed is untouched by the ill effects of incautious fossil fuels usage. Biofuels such as ethanol are being adapted globally as a green alternative for petroleum-based transportation fuels. Biofuels can be produced from abundant supplies of biomass using various agricultural crops such as sugar cane and starchy crops, oil crops, and even animal manure. Additionally, biofuels can have positive environmental impacts such as lower emissions compared to petroleum. Biofuels promise a step toward sustainable and carbon neutral renewable fuels, through reduced greenhouse gas emissions by fixating atmospheric carbon dioxide via photosynthesis27. Starch or sugar based food crops such as corn or sugarcane have been primarily used for production of ethanol globally. Their contribution to global energy market has been small but profitable due to rising crude oil prices16. Sugar cane based bioethanol has been successful in Brazil. Brazil has adapted cost effective approaches to produce bioethanol form sugarcane which fulfills one quarter of its total requirements for transportation fuel. Corn based ethanol in the United States has also been successful. In 2013 alone, the US produced 13 billion gallons of corn based ethanol. However, corn would still only be 8 able fulfill 15% of the total required transportation fuel, even if all the corn grown were converted to ethanol15. On the other hand, corn grain usage for renewable fuels potentially undermines the nation’s food and feed security. For instance, 50.8% of the total US corn grain produce is currently used in livestock feed and nutrition. Increased demand for corn ethanol has already started to impact the food industry due to increased prices in meat and dairy products16. In light of this situation, using cellulosic feedstock for ethanol has been proposed as an alternative. There is an abundance of non-food based lignocellulosic biomass in nature, and, usage of second generation bioethanol promises reduction in greenhouse gases. Additionally, cellulosic ethanol would be sustainable even in countries where climate conditions do not support sugarcane or corn grain production. For example, rice straw can be used as a potential lignocellulosic biomass source which constitutes more than 50% of world’s agronomic biomass, as rice is the staple diet globally. The cellulosic ethanol market is fast growing; significant investment is being provided to support its large scale development, from governmental programs, various venture capitalists, and even traditional fossil fuel companies like British petroleum. Companies like Abengoa, POET and Iogen are building refineries which would process cellulosic biomass into ethanol. However, like all renewable energy sources, cellulosic ethanol has its own limitations. First and foremost is the high cost of production of feedstock, and the development of degrading enzymes. Secondly, and most important, there is not enough cultivable agricultural land to produce sufficient amounts of feedstock to meet increasing demands 9 for liquid fuels, using current industrial conversion technologies14. These two limitations together make the price of cellulosic ethanol less competitive compared to distilled corn grain ethanol. Fortunately with recent developments in plant genetic engineering, it may be possible to improve crop biomass production and modify its secondary cell wall structure that would in turn improve ethanol yield per se16,32. Others developments in plant engineering technology could possibly produce cellulases and hemicellulases within the crop biomass which would reduce or completely eliminate need of external source of enzyme needed for scarification. Cellulosic Ethanol Overview Bioethanol is primarily divided in two main categories: first-generation and secondgeneration bioethanol. Sugar beet, sorghum, corn, sugarcane are first generation sugar or starch bioethanol feed stocks. Second-generation cellulosic ethanol is primarily produced from lignocellulosic biomass such as perennial grasses like switchgrass, miscanthus, eucalyptus, and willow and hybrid poplar. 10 Figure 1: Cellulosic ethanol production Overview Flow diagram showing the essential steps in the production of cellulosic ethanol from biomass feedstock to ethanol recovery 11 Genetic Manipulation of Potential Biomass Feedstock The selection of a suitable bioenergy crop is region and climate specific. There are several criteria for selecting biomass feedstock before recommending it to a local farmer for production: a) potential yield in the given climate conditions, b) agricultural land availability for the bioenergy crop; c) irrigation and cropping system management; d) mode of transportation available and the distance to a functional bio refinery; e) USDA regulations if it is a transgenic crop; f) and most importantly, the level of crop development which is usually determined by its agronomic traits such as biomass yield and lignocellulosic composition. The most important among these selection criteria are the agronomic traits of a lignocellulosic biomass crop. These traits include a) photosynthetic efficiency: (C4 plants are preferred over C3 plants due their high weather tolerance and better water use efficiency); b) canopy duration: longer canopy duration with a short perennial life span; c) translocation of photosynthesized carbohydrate into structural lignocellulose. Such traits are common in perennial species such as miscanthus and switch grass21,32. However, implementation of wild populations of switchgrass and miscanthus as an agricultural crop is slow; unlike traditional food crops, years of traditional breeding has not been performed on these plant species. In light of this situation, plant genetic engineering is an imperative tool to improve agronomic traits of bioenergy feed stocks. The primary tools for plant genetic transformation are Agrobacterium mediated transformation, and gene gun mediated gene transfer. These tools has proven worthwhile in transforming many agricultural crops such as rice, corn, wheat, barley, sorghum and many other for agriculturally relevant traits. However, the effectiveness of these tools on 12 biomass energy crops such as switchgrass and miscanthus has been limited. It has been shown that among all switchgrass genotypes, only few cultivars have been efficiently genetically engineered. The recalcitrance of perennial crops to Agrobacterium mediated transformation is not well understood and needs additional research11. An alternative approach is functional genomics and mutation studies on model plant systems such as tobacco and Arabidopsis. In these studies, genes involved in phytohromone metabolism, cell-cycle machinery or cellulose and hemicellulose biosynthesis pathways are identified, targeted and altered for enhanced plant growth and byproducts. Plant hormones are responsible for regulating growth and development of plants throughout their life span. They interact with each other and other signaling pathways which effect plant growth, in recent literature Gibberellins (GA) and Brassinosteroids have been reported to play a vital role in growth associated with stem elongation and thickness27. In one such study transgenic tobacco was engineered to express GA20oxidase gene from Arabidopsis, showed enhanced biomass accumulation owing to increased plant height and early flowering with increased levels of GA. Similarly transgenic hybrid poplar with increased GA biosynthesis reflected higher growth and an increased biomass accumulation, In another such study, elevated growth rate in tobacco has been reported by over expressing D-type cyclin (CycD2) gene from Arabidopsis responsible for cell division. The transgenic tobacco was reported to have taller stem and elevated overall growth rate with early attainment of flowering8. There have been numerous attempts in the last decade or so to understand the cellulose and hemicellulose biosynthetic pathways by exploiting functional genomics, but still the knowledge in this field of study is limited. Although feedstock biomass can potentially be increased by 13 changing the environmental growth conditions such as carbon allocation in the form of carbon dioxide, oxygen, water supply and soil nutrient content. For instance, a study on maize showed 20% increase in plant biomass by supplementing the environment with higher levels of carbon dioxide29. However it is hard to predict that if this higher yield can be directly co related with higher photosynthetic rate in maize; as photosynthetic rate is highly dependent on synchronization between plant circadian clock11 and external change in light–dark cycle29. Increasing plant biomass by regulating growth rate holds potential for bioenergy crops. Reducing Pretreatment cost Lignocellulosic biomass is primarily composed of long chain carbohydrate polymers mainly cellulose and hemicellulose, and phenolic compounds such as lignin. Cellulose and hemicellulose make up majority of the cell wall dry matter, and are the carbohydrates used for production of bioethanol. Cellulose and hemicellulose are hydrolyzed via enzymatic saccharification to sugars that are then fermented to ethanol. Cellulose contains cellobiose dimers linked by ß-1, 4 glycosidic bonds forming crystalline fibrous polymers made up of individual glucose units. Hemicellulose, another component of lignocellulosic feedstock, is a short chain polymer primarily composed of C-5 and C-6 sugars, like xylose, arabinose and galactose, glucose, mannose respectively. The third most common constituent biomass feedstock is polyphenolic lignin. The primary function of lignin is to provide structural integrity to plants. These three compounds are intertwined and this complex nature of lignocellulosic biomass makes it recalcitrant to enzymatic hydrolysis and adds up the cost of pretreatment processing. However recent developments in plant genetic engineering allows us to better understand lignin 14 biosynthetic pathways, to down regulate lignin composition and modify chemical structure of lignin components9,3. This can potentially bring down the cost of pretreatment processing and increase amenability to enzymatic scarification. Lignin primarily has three precursors: paracoumaryl, coniferyl and sinapyl alcohol, which form the phenylpropanoid unit parahyrdroxuphenyl, guaiacyl and syringyl units respectively through a complex and interconnected lignin biosynthetic pathway17. Similar to cellulose and hemicellulose biosynthetic pathways there is limited knowledge about lignin biosynthetic pathways20. However with recent development in functional genomics and mutant studies plant scientists are able identify novel genes involved in lignin biosynthetic pathways. Also studies have been able to down regulate these genes in various plant species using antisense technology or using RNA interference technology9. For instance in a recent study using annotated expressed sequence tags from xylogenic tobacco culture, gene expression was analyzed for transgenic tobacco lines down regulated for lignin biosynthetic enzymes namely Cinnamate-4-hydroxylase(se4h), Cinnamoyl-C0A-reductase (asccr) and lignin specific peroxidase (asprx), and compared with UDP glucuronic acid decarboxylase (asuxs) involved in nucleotide sugar pathway of Xylan biosynthesis. It was shown that lines down regulated in asprx showed 3 fold improvement in enzymatic saccharification, and lines down regulated in as asuxs improved saccharification by 50% when compared to wild type9. In a similar study, transgenic alfalfa was down regulated for of six different lignin biosynthetic pathway enzymes namely cinnamate 4‑hydroxylase (C4H), hydroxyl cinnamoyl transferase (HCT), 4‑hydroxycinnamate 3‑hydroxylase (C3H), S‑adenosyl-methionine-caffeoyl- 15 CoA/5-hydroxyferuloyl-CoA-O-methyltransferase (CCoA-OMT), ferulate 5-hydroxylase (F5H), or caffeate O-methyltransferase (COMT ), and it was shown that down regulation of these enzymes could completely eliminate need of pretreatment processing in alfalfa6,7. In both alfalfa and tobacco modification of lignin biosynthesis pathway enzymes has been shown to reduce the pretreatment process and improve the efficiency of enzymatic scarification. However, neither alfalfa nor tobacco is a viable bioenergy feedstock. Therefore further investigations are needed to confirm these effects and evaluate the usefulness of down regulating lignin biosynthesis pathway enzymes on potential bioenergy crops such switchgrass or miscanthus. In significant other mutational studies, lignin biosynthetic enzyme, O-methyl transferase (OMT) has been reported to increase overall biomass accumulation in transgenic tobacco without any changes in lignin deposition2,1. In another such study, Cinnamoiyl-COA-reductase (CCR) was down regulated in transgenic tobacco resulting in an overall drop in lignin composition and simultaneous increase in xylan and cellulose composition in tobacco secondary cell wall5,19. In another recent development, transgenic switchgrass was down regulated for caffeic acid 3-O-methyltranferase (COMT) which resulted in lower lignin content with reduced S/G ratio and increased sugar and conversion yield37. In another attempt in switchgrass overexpression of transcription factor PvMYB4 resulted in suppression of lignin biosynthetic pathways genes with enhanced enzymatic scarification efficiency of up to 300% compared to wild type28. In Planta enzyme production Production of second-generation cellulosic ethanol involves use of cellulase enzymes for hydrolysis followed by fermentation. Hydrolysis is the chemical reaction that converts 16 the complex polysaccharides present in the biomass in to simple sugars using a cocktail of cellulose enzymes. There are typically of three kinds of enzymes needed to hydrolyze cellulose into glucose: endoglucanase, exoglucanase and β‑glucosidase. During the hydrolysis process, endoglucanase first randomly cleaves the crystalline cellulose molecule internally; producing additional reduced chain ends thereafter exoglucanase attaches itself to the chain end, results in small cellobiose units. Exoglucanase also attaches itself to amorphous cellulose with exposed chain ends and directly producing small cellobiose units. In the final step β‑glucosidase breaks cellobiose subunits into simple monomers of glucose25. These enzymes work synergistically. For example, increase in cellobiose can hinder exoglucanase activity through feedback inhibition, making β-glucosidase irreplaceable. Therefore, the ratio of these enzymes is critical to ensure complete and efficient hydrolysis. Cost of production of hydrolysis enzymes currently high. They are produced at commercial scale in a microbial bioreactor via fermentation. Research is being carried out to produce hydrolysis enzymes in planta. This approach could lower the energy input by eliminating the cost of industrial production and separation. An important development in this regard has been the characterization of microbes most suitable for synthesizing cell wall degrading enzymes. Among these well characterized microorganisms are either bacterial origins or fungal origins such as Trichoderma reesei30. Most of these micro-organisms share common characteristics such as being able to produce a large variety of cell wall hydrolyzing enzymes that efficiently breakdown recalcitrant lignocellulosic biomass22. 17 This characterization of cell-wall hydrolysis enzymes has made it convenient for plant molecular biologists to target specific species of bacteria to express their microbial protein in planta is using codon alteration, as many of the identified enzymes are of either bacterial or fungal origin. The key issue associated with heterologous expression of cell wall hydrolyzing enzyme are a) in planta storage b) stability c) level of activity and extraction of enzyme from plant biomass. There are numerous ways in which these issues are being dealt with such as by expressing the recombinant enzyme directly into seed endosperm so that biomass and seeds can be easily separated during harvest and used separately. This methodology has been tried on corn and rice grain using seed specific promoters such as glutein and globulin17. In a similar way E1 endocellulase was expressed in tobacco seeds which stayed viable even after a year of storage at room temperature10. This stability is a marketable feature of In Planta enzymes since it simplifies the value chain of storage, extraction and transportation of the enzyme to a biorefinery and companies like Syngenta and Edenspace are working towards exploiting this technology on a commercial scale32. Furthermore, numerous efforts are being taken to produce enzyme within the plant cytosol so that under optimum temperature hydrolysis can occur automatically and pretreatment process can be reduced or eliminated. For example, E1 endocellulase has been expressed at 5% total soluble protein in rice and 2% total soluble protein in maize, however these levels are significantly low to substitute any pretreatment process23,24. In another approach several transgenic enzymes have been targeted to be expressed directly into plant subcellular compartments such as apoplast, chloroplast and endoplasmic reticulum, instead of the plant cytosol. For example increased level of enzymes have been reported to achieved by genetically engineering the 18 chloroplast genome in poplar, which also ensured bioconfinment of transgene as chloroplast genome is maternally inherited. (1) Another potential subcellular compartment for enzyme production is the endoplasmic reticulum as it provides excellent enzyme stability due to its oxidizing environment and presence of minimal proteases compared to cytosol13. Recent literature shows that transgenic enzyme had 10 fold greater activity when retained endoplasmic reticulum then secreted in the cytosol18. In a similarly fashion plant apoplast has been targeted to accumulate transgenic enzyme as this plant subcellular compartment is the largest and can store large amounts of enzyme. Apoplast has also been preferred for expression of thermophilic transgenic enzymes which allows cellulase to cleave plant cell wall internally by just increasing temperature to optimal levels for enzyme activation32. Although in planta enzyme production seems very promising; there is substantial research pending before this technology can be realized on a commercial scale. Most importantly there are significant regulatory hurdles before implementation of these technologies outside laboratory settings. Conclusion Even with all this development in plant genetic engineering to create dedicated bioenergy crops, significant work remains. In general we have identified few challenges which hinder further development in this field. First and for most problem is the recalcitrant nature among wild type perennials crops towards genetic transformation. There needs to be development of a unified genotype-nonspecific genetic transformation technology for bioenergy feedstocks. Secondly we still need to produce sufficient amounts of in planta 19 celluslase enzymes. There is promise in potentially accumulating cellulase in the apoplast, but this technology needs further development. Additional research is also needed to lower lignin content and increase carbohydrate content in the plant cell wall without negatively impacting the physical viability of the feedstock. References 1. Biological Confinement of Genetically Engineered Organisms. 2004. The National Academies Press. 2. Blaschke, L., M. Legrand, C. Mai and A. Polle. 2004. Lignification and structural biomass production in tobacco with suppressed caffeic/5-hydroxy ferulic acid-Omethyl transferase activity under ambient and elevated CO2 concentrations. Physiologia Plantarum 121(1): 75-83. 3. Blee, K. A., J. W. Choi, A. P. O'Connell, W. Schuch, N. G. Lewis and G. P. Bolwell. 2003. A lignin-specific peroxidase in tobacco whose antisense suppression leads to vascular tissue modification. Phytochemistry 64(1): 163-176. 4. Bordetsky, A., R. Hwang, A. Korin, D. Lovaas and L. Tonachel. February 2005. Securing America: Solving our oil dependence through innovation. National resources defense council NewYork. 5. Chabannes, M., A. Barakate, C. Lapierre, J. M. Marita, J. Ralph, M. Pean, S. Danoun, C. Halpin, J. Grima-Pettenati and A. M. Boudet. 2001. Strong decrease in lignin content without significant alteration of plant development is induced by simultaneous down-regulation of cinnamoyl CoA reductase (CCR) and cinnamyl alcohol dehydrogenase (CAD) in tobacco plants. The Plant Journal 28(3): 257270. 20 6. Chapple, C., M. Ladisch and R. Meilan. 2007. Loosening lignin's grip on biofuel production. Nat Biotech 25(7): 746-748. 7. Chen, F. and R. A. Dixon. 2007. Lignin modification improves fermentable sugar yields for biofuel production. Nat Biotech 25(7): 759-761. 8. Cockcroft, Claire E.den Boer, Bart G. W. Healy, J. M. Sandra Murray, James A. H. 2006. Cyclin D control of growth rate in plants. Nature 405(- 0028-0836 (Print); - 0028-0836 (Linking)):. 9. Cook, C. M., A. Daudi, D. J. Millar, L. V. Bindschedler, S. Khan, G. P. Bolwell and A. Devoto. 2012. Transcriptional changes related to secondary wall formation in xylem of transgenic lines of tobacco altered for lignin or xylan content which show improved saccharification. Phytochemistry 74(0): 79-89. 10. Dai, Z., B. Hooker, R. Quesenberry and S. Thomas. 2005. Optimization of Acidothermus cellulolyticus Endoglucanase (E1) Production in Transgenic Tobacco Plants by Transcriptional, Post-transcription and Post-translational Modification. Transgenic research 14(5): 627-643. 11. Dodd, A. N., N. Salathia, A. Hall, E. Kévei, R. Tóth, F. Nagy, J. M. Hibberd, A. J. Millar and A. A. R. Webb. 2005. Plant Circadian Clocks Increase Photosynthesis, Growth, Survival, and Competitive Advantage. Science 309(5734): 630-633. 12. Eriksson, M. E., M. Israelsson, O. Olsson and T. Moritz. 2000. Increased gibberellin biosynthesis in transgenic trees promotes growth, biomass production and xylem fiber length. Nat Biotech 18(7): 784-788. 21 13. Fischer, R., E. Stoger, S. Schillberg, P. Christou and R. M. Twyman. 2004. Plantbased production of biopharmaceuticals. Current opinion in plant biology 7(2): 152-158. 14. Gressel, J. 2008. Transgenics are imperative for biofuel crops. Plant Science 174(3): 246-263. 15. Haigler, C. H. 2006. The Science and Lore of the Plant Cell Wall: Biosynthesis, Structure and Function. 16. Hill, J., E. Nelson, D. Tilman, S. Polasky and D. Tiffany. 2006. Environmental, economic, and energetic costs and benefits of biodiesel and ethanol biofuels. Proceedings of the National Academy of Sciences 103(30): 11206-11210. 17. Hood, E. E., R. Love, J. Lane, J. Bray, R. Clough, K. Pappu, C. Drees, K. R. Hood, S. Yoon, A. Ahmad and J. A. Howard. 2007. Subcellular targeting is a key condition for high-level accumulation of cellulase protein in transgenic maize seed. Plant Biotechnology Journal 5(6): 709-719. 18. Hyunjong, B., D. Lee and I. Hwang. 2006. Dual targeting of xylanase to chloroplasts and peroxisomes as a means to increase protein accumulation in plant cells. Journal of experimental botany 57(1): 161-169. 19. Kavousi, B., A. Daudi, C. M. Cook, J. Joseleau, K. Ruel, A. Devoto, G. P. Bolwell and K. A. Blee. 2010. Consequences of antisense down-regulation of a lignification-specific peroxidase on leaf and vascular tissue in tobacco lines demonstrating enhanced enzyme saccharification. Phytochemistry 71(5–6): 531542. 22 20. Kawagoe, Y. and D. Delmer. 1997. Pathways and Genes Involved in Cellulose Biosynthesis. In 63-87. ed. J. Setlow, Springer US. 21. Knauf, M. and M. Moniruzzaman. 2004. Lignocellulosic biomass processing: a perspective. International Sugar Journal 106(1263): 147-150. 22. Lynd, L. R., P. J. Weimer, W. H. van Zyl and I. S. Pretorius. 2002. Microbial Cellulose Utilization: Fundamentals and Biotechnology. Microbiology and Molecular Biology Reviews 66(3): 506-577. 23. Oraby, H., B. Venkatesh, B. Dale, R. Ahmad, C. Ransom, J. Oehmke and M. Sticklen. 2007. Enhanced conversion of plant biomass into glucose using transgenic rice-produced endoglucanase for cellulosic ethanol. Transgenic research 16(6): 739-749. 24. Ransom, C., V. Balan, G. Biswas, B. Dale, E. Crockett and M. Sticklen. Heterologous Acidothermus cellulolyticus 1,4-β-endoglucanase E1 produced within the corn biomass converts corn stover into glucose. (- 1-12): - 207-219. 25. Rogers, L. A. and M. M. Campbell. 2004. The genetic control of lignin deposition during plant growth and development. New Phytologist 164(1): 17-30. 26. Salas Fernandez, M. G., P. W. Becraft, Y. Yin and T. Lübberstedt. 2009. From dwarves to giants? Plant height manipulation for biomass yield. Trends in plant science 14(8): 454-461. 27. Schlamadinger, B., M. Apps, F. Bohlin, L. Gustavsson, G. Jungmeier, G. Marland, K. Pingoud and I. Savolainen. 1997. Towards a standard methodology for greenhouse gas balances of bioenergy systems in comparison with fossil energy systems. Biomass and Bioenergy 13(6): 359-375. 23 28. Shen, H., C. Poovaiah, A. Ziebell, T. Tschaplinski, S. Pattathil, E. Gjersing, N. Engle, R. Katahira, Y. Pu, R. Sykes, F. Chen, A. Ragauskas, J. Mielenz, M. Hahn, M. Davis, C. N. Stewart and R. Dixon. 2013. Enhanced characteristics of genetically modified switch grass (Panicum virgatum L.) for high biofuel production. Biotechnology for Biofuels 6(1): 71. 29. Sinclair, T. R., L. C. Purcell and C. H. Sneller. 2004. Crop transformation and the challenge to increase yield potential. Trends in plant science 9(2): 70-75. 30. Sternberg, D. 1976. Production of cellulase by Trichoderma. Biotechnology Bioengineering Symposium 6(35-53):. 31. Sticklen, M. B. 2004. In Proceeding 2nd International conference Ukrainian Conference . Ukraine National Academy of science133-136. 32. Sticklen, M. 2006. Plant genetic engineering to improve biomass characteristics for biofuels. Current opinion in biotechnology 17(3): 315-319. 33. Sticklen, M. B. Feedstock Crop Genetic Engineering for Alcohol Fuels. Crop Sci. 47(6): 2238-2248. 34. Sun, Y. and J. Cheng. 2002. Hydrolysis of lignocellulosic materials for ethanol production: a review. Bioresource technology 83(1): 1-11. 35. Warren, R. 1996. Microbial hydrolysis of polysaccharides. Annual Review of Microbiology 50183–212. 36. Yang, D., F. Guo, B. Liu, N. Huang and S. Watkins. 2003. Expression and localization of human lysozyme in the endosperm of transgenic rice. Planta 216(4): 597-603. 24 37. Yee, K., M. Rodriguez Jr, T. Tschaplinski, N. Engle, M. Martin, C. Fu, Z. Wang, S. Hamilton-Brehm and J. Mielenz. 2012. Evaluation of the bioconversion of genetically modified switch grass using simultaneous saccharification and fermentation and a consolidated bioprocessing approach. Biotechnology for Biofuels 5(1): 81. 38. Ziegelhoffer, T., J. Raasch and S. Austin-Phillips. 2001. Dramatic effects of truncation and sub-cellular targeting on the accumulation of recombinant microbial cellulase in tobacco. Molecular Breeding 8(2): 147-158. 25 Chapter 2 Characterization of Genetically Modified High Biomass Producing Tobacco Plant Abstract During a routine transformation experiment, we fortuitously obtained a transgenic tobacco plant that grew to the size of a small tree , The high biomass producing transgenic tobacco (Nicotiana tabacum cv. Xanthi) line, termed giant recombinant (GR), has the potential for a new class of energy crops by converting normal plants to high biomass producing plants.. To characterize the giant line, we analyzed its growth rate and lignocellulosic composition relative to the non-transgenic control line. The growth rate of the plants were measured by tracking stem height, width, and leaf count, length, and width for 126 days. The chemical composition (cellulose, hemicellulose and lignin) of the GR line relative to the control line was quantified using standardized NREL protocol. The GR line accounted for 240% more biomass than the untransformed line within 135 days of its germination. Furthermore we found there were significant differences in chemical composition within GR line, and relative to control line. The GR characteristics are likely due to a disruption or activation of an unknown plant gene. Identification of the GR gene responsible for increased biomass productivity could lead to its utilization in other plant species to develop feed-stocks for bio-based energy. 26 Introduction The World Commission on Environment and Development states sustainable development as “development that meets the needs of the present without compromising the ability of future generations to meet their own needs”. This definition emphasizes on the concepts of protecting needs of the future generation and overcoming technological limitations generated on our environment to meet these needs. However, incautious usages of fossil fuels possess a serious threat to our environmental health and future energy security20. In the last decade scientists and policy makers all over the world have tried to resolve this problem by exploiting various avenues in renewable sources of energy. Bioethanol is an attractive alternative to gasoline; it is environmental friendly, renewable and can be produced on a large scale13. The United States primary production of ethanol is currently corn grain based, and the US government has target to supply 36 billion gallons of biofuels annually by 2022. However, it is projected that corn ethanol itself would be inadequate to meet this overwhelming demand21. Among other alternatives, energy from cellulose based ethanol has been developed as a favorable solution. There is abundance of non-food based lignocellulosic biomass in nature and at the same time usage of second generation bioethanol promises reduction in greenhouse gases20. However like all renewable energy sources cellulosic ethanol has its own limitations. It is estimated that there is not enough cultivable agricultural land to produce sufficient amounts of liquid fuel in support to increasing demands for gasoline, using current conversion technologies12. Fortunately with recent developments in plant 27 genetic engineering it is possible to improve crop biomass production and modify its secondary cell wall structure that would in turn improve ethanol yield per acre13,24. Doing a routine genetic transformation experiment with Nicotiana tabacum cv. Xanthi, a high biomass producing giant recombinant (GR) line of tobacco was identified. We have established that the transgenic GR tobacco phenotype is T-DNA linked and segregates in a Mendelian fashion. Preliminary analysis indicates that the transgenic event contains one copy of T-DNA insert. This T-DNA insertion most likely disrupted the function of a gene or activated a nearby gene10 resulting in the dramatic enhancement in plant growth. In this study we characterized the GR to identify (a) unknown physicochemical differences between GR and control line, (b) to explore the potential avenues for identification of GR gene based on our results. The specific objectives of this study are: 1) To measure growth of GR line relative to control, by tracking change in stem height, width, and leaf count, length, width, and cumulative increase plant dry weight. 2) The second objective is to determine if there were any changes in biomass composition (cellulose, hemicellulose and lignin) of the GR line relative to the control line during plant growth. The phenotypic characterization of the transgenic GR tobacco line may provide clues of the nature of the GR gene. This in turn will be valuable in development of a dedicated energy crop with increase biomass production. 28 Materials and Methods Plant Material and Growth Conditions Nicotiana tabacum cv. Xanthi (control) and giant recombinant (GR) tobacco seeds were obtained from Dr. Mitra, Department of Plant Pathology, University of NebraskaLincoln. Seeds were sterilized with 70% alcohol and 10% house hold bleach. Control seeds were germinated in petri plates containing 3% sucrose, 0.8% agar at pH 5.8 and 10 ml L-1 Amphotericin, whereas growth medium for GR line seeds were supplemented with 50 mg L-1 Kanamycin for selection of T2 GR line. Following germination and selection in growth chamber, 5 seedlings from GR line 3 and 3 control seedlings were transferred to a greenhouse for plant growth measurement. Using the same procedure, 9 seedlings from each GR line 1,2,3,4 and 9 control seedlings were transferred to a greenhouse for composition analysis. Constant growth conditions were maintained in the green house. Plant Growth Measurements: The plants were kept in growth medium up to 1 week after germination so that they were stable and survived the process of transplantation. Seedlings obtained from growth chamber were then transferred from petri-plates to uniform size pots. These pots were then transferred to the green house as seen in image 1, where constant growth conditions were maintained. 29 Image1: Individual plant from control line on the left and GR line on the right growing under constant greenhouse conditions. Five individual plants from GR line 3 and 3 plants from the control line were measured for specific growth parameters. Measurements for specific growth parameters were initiated when plants were 1 months old from the point of germination in growth chamber. Readings were taken on a regular interval of 8 days until plants were 126 days old. Stem Height Measurements: Each individual plant height was measured using a thread from the point of origin of stem above soil. The thread was kept as close to the stem as possible. The start and end point of stem were marked on thread and then measured using measuring tape. 30 Stem Width Measurements: The widest point of plant stem was identified and marked, and change in stem thickness was measured using a Vernier caliper at a regular interval of 8 days. Leaf Length and Width Measurements: The largest leaf for individual plant was identified and marked. The measurements were taken using a measuring tape on a regular interval of 8 days for the identified leaf for its length and width. Leaf petiole lengths were excluded from the measurements, as petioles were absent from the GR line. Number of leafs: Simple count of the number of leafs was kept on an interval of 8 days for each plant. The data represented for the plant growth comparison was computed by averaging every data point from individual plant, and representative curves were plotted from the data set. Each graph shows change in respective growth factor within the limits of experimental error. Standard deviation bars associated with each data set are plotted to show variation between individual plants. The points of observation are represented in GR by square and in control by circle. It is important to note that as plants aged, variation within individual plants became more pronounced. Chemical composition analysis Plants were harvested (excluding root system) from green house at three time points. A) When the plants were 30 days old, B) When plants were 90 days old, and C) When plants were 135 days old. Following each harvest, the plants were measured for total fresh weight and were then dried in oven at 45± 3 °C, until constant weight was obtained. The plant’ dry weights so obtained were used for measuring growth rate in terms of total 31 biomass accumulation. Dried plant tissue samples of GR and control line were ground to pass through 2.00 mm mesh, test sieve (fisher brand). Samples were analyzed for lignocellulosic components: cellulose, hemicellulose and lignin according to the National Energy Research Energy (NREL) protocol23. Klason lignin of the plant biomass was measured with two step acid hydrolysis methodology. Uniformly sized biomass was acid hydrolyzed in a hot water bath at 30 °C with 72% hydrochloric acid for 30 minutes. The hydrolysate was diluted with distilled water and autoclaved at 120°C for 60 minutes. After bringing the hydrolysate to room temperature, it was filtered using Pyrex 30 ml crucibles to separate acid insoluble lignin from acid soluble components in the filtrate. The pre-weighed crucibles and supernatant were then dried at 105°C for four hours and weighed for lignin estimation. Carbohydrates in the acid soluble component of acid hydrolysate were analyzed according to NREL laboratory method # 223. Acid hydrolysate was first neutralized with calcium carbonate, and then filtered through HPLC grade filters into HPLC sample vials. An HPLC (Thermo scientific), fitted with an inline Bio-Rad HPX-87P analytical column with a refractive index detector (Shodex) was used to detect various concentration of carbohydrates present in plant samples. The samples were analyzed at 6000 KPa pressure, 85 °C column temperature and a sample flow rate of 0.6 ml min -1.The polymeric sugars concentrations were calculated from the corresponding concentration of monomeric sugars, using an anhydro correction of 0.88 for C-5 sugars and a correction of 0.90 for C-6 sugars. Following which the percentage of each sugar concentration on an extractives free basis was calculated using NREL protocol23, so obtained sugar concentrations on percent basis were used for statistical analysis. 32 Data Analysis Repeated measures Analysis of covariance (ANCOVA) was used to differentiate between GR and control line based on chemical composition (percent basis) and time of harvest. Data from 30 days and 90 days was used to observe differences within GR line and relative to control line. Date from 135 days was not used in the analysis due to limited number of replicates. Optimal Statistical model was selected from CS (Compound symmetry), AR (1) (Autoregression (1)), TOEP (Toeplitz), Unstructured and ANTE (1) (Ante-dependence) based on lowest values generated for AIC (Akaike information criterion) and BIC (Bayesian information criterion)22. ANTE (1) was configured optimal for our data analysis, due to its ability to estimate both covariance and residual variance within a given experimental unit17. ANTE (1) also gave us lowest values for our selection criteria. Result and Discussion The growth of GR line relative to control line was studied in detail; it is primarily known that the growth of tobacco can be divided into three stages from point of seed germination to flowering25.The first stage is the time period in which the seedlings germinate and establishes itself in the soil. Once in the green house, plants took 1-2 weeks to establish in the soil; this period of adaptation was observed by loss of existing leaves and initiation of newer leaves. Growth measurements were started at the end of the first period when plants appeared well established. 33 Figure1: Change in Stem height for GR (n=5) and control (n=3) line between 30 and 126 days. At time equals zero plants are 1 month old from the point of germination. On X axis time is represented in days and on Y axis height is represented in inches. Figure2: Change in stem thickness for GR (n=5) and control (n=3) line between 30 and 126 days. At time equals zero plants are 1 month old from the point of germination. On X axis time is represented in days and on Y axis thickness is represented in inches. 34 Figure3: Change in leaf number for GR (n=5) and control (n=3) line between 30 and 126 days. At time equals zero plants are 1 month old from the point of germination. On X axis time is represented in days and on Y axis leaf number is represented in numeric values. Figure4: Change in leaf width for GR (n=5) and control (n=3) line between 30 and 126 days. At time equals zero plants are 1 month old from the point of germination. On X axis time is represented in days and on Y axis leaf width is represented in inches. 35 Figure 5: Change in leaf length for GR (n=5) and control (n=3) line between 30 and 126 days. At time equals zero plants are 1 month old from the point of germination. On X axis time is represented in days and on Y axis leaf length is represented in inches. In the first stage of growth some morphological differences could be observed between the GR and control line, leaf petioles were absent in GR line and leafs appeared broader and longer compared to control. It was observed that within the first month of initiation from nodes, GR leafs were at 9.2”(wide)x13.16”(long), whereas the control leafs were at 2.31”x 3.5” as seen in figures 4 and 5. Also the GR stem originated to be wider than the control; GR stem was as wide as 0.6” whereas as control stem was 0.2’’wide as seen in figure2. The second stage was marked by rapid growth in all aspects of the control line from 30 days up till 78 days, however this period of rapid growth extended for GR line until the end of the experiment. During the early second stage from 30 to 54 days leafs for both GR and control line grew to its full potential at 12”x25” and 5”x8” respectively as seen in figure4 and 5. The total number of leafs for both control and GR continued at a similar rate. The most noticeable change in this period was increased accumulation of above ground biomass in terms of stem height and thickness. Growth in control stem 36 increased steadily up till 78 days, thereafter plants started branching profusely. The increase in control height after 78 days was only attributed by branching as seen in figure1, and it also showed signs of budding, which can be marked as the beginning of reproductive stage in control. On the other hand GR line showed steady increase in its stem height and thickness with no signs of budding or branching. Third or the reproductive stage of tobacco plant was marked by flowering in all of individual control plants. The control plants showed branching with no or little increase in stem thickness a seen in figure2. However GR line showed a steady increase in stem height and thickness, and by the end of 126 days GR line showed 3 fold increase in its overall stem height and thickness compared to control line as seen in figure1 and 2. Furthermore GR line showed no signs of decrease in its growth until 126 days. The only similarity observed between GR and control line in all the three stages was the concomitant increase in the total number of leafs as seen in figure3. These changes observed in growth rate of GR line are presumably due to mutation caused by T-DNA insertion; however, we have little information of the disrupted or activated gene in GR genome at this time. In the past, increased growth rate in tobacco plants has been achieved exploiting phytohromone metabolism or altering cell-cycle related genes. Plant hormones are responsible for regulating growth and development of plants throughout their life span. They interact with each other and other signaling pathways which effect plant growth. In recent literature Gibberellins (GA) and Brassinosteroids have been reported to play a vital role in growth associated with stem elongation and thickness19. In a similar study, transgenic tobacco was engineered to express GA20- 37 oxidase gene from Arabidopsis, showed enhanced biomass accumulation, higher levels of lignin and early flowering with increased GA production. (1) However GR line showed no signs of flowering during the control growth cycle. Therefore possibilities of alteration in GA production in GR line can be ruled out. In another such study elevated growth rate in tobacco has been reported by over expressing D-type cyclin (CycD2) gene from Arabidopsis responsible for cell division. The transgenic tobacco was reported to have taller stem and elevated overall growth rate with early attainment of flowering7. However in GR line no flowering was observed during control growth cycle. Therefore possibilities of alteration in GR cell cycle machinery can also be ruled out. Growth Rate Figure6: Change in total biomass accumulation for GR line (n=3), and Control line (n=3) between 30 and 135 days. On Y axis total biomass is represented in grams and on X axis time period represented in months. 38 Plant growth is a complex phenomenon; the carbon dioxide assimilated during photosynthesis may be stored in various plant organelles or used to support growth. The plant growth rate depends upon both environmental and genetic factors9. The total carbohydrate assimilated during plant growth can be directly associated to increase in its total biomass over time. To quantify the plant growth rate usually a parameter R is used. R may be described as the rate of production of dry matter per unit initial dry weight. R can be used as an indicator of efficiency of a given plant to produce biomass per unit of time. R = lnW1 - lnW2 / T2 – T1, Where W1 and W2 are oven dry weight in grams over a discrete growth interval T1 and T2. (9) We calculated R for both GR and control line as .007382 and 0.00444 respectively, and the relative efficiency of GR line to produce biomass was found out to be 1.6 times that of control line. It can also been seen in figure6, that the GR line produces 240% more biomass than control line within 135 days of its germination. These observations reflect the GR potential to produce tremendous amount of biomass in a relatively short duration of time. Chemical composition The plant cell wall in tobacco is broadly classified as primary and secondary cell walls. These are easily distinguishable by the presence or absence of lignin deposition. The primary focus of our study is based on the change in secondary cell wall composition in tobacco leaf and stem during plant growth. The major accumulation of biomass associated with tobacco plants occurs in the secondary cell wall in the form of cellulose, lignin and hemicellulose18. 39 We looked at change in biomass accumulation in four GR lines with respect to control line between 30 days and 90 days. On the basis of our statistical analysis between these two harvest points we found that GR line (1,2,3,4) had higher rate of biomass accumulation compared to control line (5) as seen in figure7. Furthermore we found statistically significant differences between GR lines as summarized in table 1. It was observed that GR line 4 was significantly different from GR lines (2, 3) and it had the highest rate of biomass accumulation within GR lines. Whereas no significant differences occurred between GR line 4 and GR line1 at p>0.05, however at p>0.10 they are different, as can be seen in figure7. Figure7: Change in biomass accumulation for GR lines 1, 2, 3 and 4(n=3), and Control line 5(n=3) between 30 and 90 days. On Y axis total biomass is represented in grams and on X axis time period represented in months. 40 Table1: Statistically significant differences for total biomass accumulation in secondary cell wall of GR and control line between 30 & 90 days. To further understand this change in rate of biomass accumulation in GR lines and control line we compared the change in their respective cellulose, hemicellulose and lignin composition (percent basis) between 30 and 90 days. The major chemical constituents in the secondary cell wall of leaf and stem were similar in GR and control line. However the percentage of structural carbohydrates varied significantly between them. Table 2 shows the Glucan composition in the stems. The analysis indicated that GR line 1 was similar to control line, whereas GR line 2, 3 and 4 were different from control. Furthermore it can be observed that GR line 2 was different from GR line 3 and 4 and no difference occurred between GR line 3 and 4. Whereas no statistically significant differences could be observed in leaf Glucan concentration between GR lines and control 41 line as seen in table 3. However it is important to note that glucan composition dropped in leafs of all the plant lines between 30 and 90 days as seen in figure9. This can be explained by the fact that during rapid growth in tobacco it has been reported that carbohydrates get translocated from leafs to stem to support increasing growth25. Therefore this drop is more prominent in GR line on account of its higher growth rate compared to control .Furthermore it is also important to note that between 30 and 90 days GR lines 2, 4 and 4 stem showed rapid increase in cellulose concentration as seen in figure8. Figure8: Change in cellulose deposition for GR lines 1, 2, 3 and 4(n=3), and Control line 5(n=3) stem between 30 and 90 days. On Y axis Glucan is represented on percent basis and on X axis time period represented in months. 42 Figure9: Change in cellulose deposition for GR lines 1, 2, 3 and 4(n=3), and Control line 5(n=3) leaf between 30 and 90 days. On Y axis glucan is represented on percent basis and on X axis time period represented in months. Table2: Statistically significant differences for change in lignocellulosic composition in secondary cell wall of GR and control line stem between 30 & 90 days 43 Table3: Statistically significant differences for change in lignocellulosic composition in secondary cell wall of GR and control line leaf between 30 & 90 days. Table 2 summarizes the results for xylan composition in the stem. The analysis indicated that all the GR lines were different from control, and there were significant differences within GR lines; GR line 1 was different from 2, 3 and 4 and similarly GR line 2 was different from GR line 1, 3, 4, and no difference occurred between GR line 3 and 4. It was also observed the xylan concentration increased in GR lines 2, 3, and 4, whereas it decreased in control and GR line 1 between 30 and 90 days as seen in figure10. 44 Furthermore on the basis of change in leaf xylan, all GR lines were statistically different control line as summarized in table 3 and there was concomitant drop in xylan and glucan in all GR lines as seen in figure9 and figure11. Figure10: Change in hemicellulose deposition for GR lines 1, 2, 3 and 4(n=3), and Control line 5(n=3) stem between 30 and 90 days. On Y axis Xylan is represented on percent basis and on X axis time period represented in months. Figure11: Change in hemicellulose deposition for GR lines 1, 2, 3 and 4(n=3), and Control line 5(n=3) leaf between 30 and 90 days. On Y axis Xylan is represented on percent basis and on X axis time period represented in months. 45 On the basis of change in lignin in GR and control stem, statistically analyzed results are summarized in table 2. The results prove that all GR lines were different from control lines, and there were significant differences between GR lines; GR line 1 was different from GR line 3 and 4 and GR line 4 was different from GR line 1, 2, and 3. Whereas no difference occurred between GR line 2 and 3, and GR line 1 and 2. Furthermore on the basis of change in leaf lignin, all GR lines were statistically different from control line, and there were differences within GR line as well; GR line 4 was different from GR line 2 and 3, and no differences observed between GR line 1 and GR lines (2, 3, 4) as summarized in table 3. It was also observed that leaf lignin concentration in all plant lines increased between 30 and 90 days as seen in figure13. This can explained by the fact that, as plants leafs get older lignin composition tends to increase18. However it was also observed that stem lignin concentration (percent basis) dropped in GR line 1, 2, and 3, whereas it increased in control line and GR line 4 as seen in figure12. Figure12: Change in lignin deposition for GR lines 1, 2, 3 and 4(n=3), and Control line 5(n=3) stem between 30 and 90 days. On Y axis total lignin is represented on percent basis and on X axis time period represented in months. 46 Figure13: Change in lignin deposition for GR lines 1, 2, 3 and 4(n=3), and Control line 5(n=3) stem between 30 and 90 days. On Y axis Glucan is represented on percent basis and on X axis time period represented in months. These changes in Glucan and Xylan concentration indicate that there was an overall increase in cellulose and hemicellulose in secondary cell wall of GR line relative to control line. Whereas as the lignin dropped in GR lines 1, 2 and 3 compared to control line. These changes may be somehow associated with higher growth rate in GR line and needs further analysis. What we already know about the GR line is that the T-DNA insertion somehow disrupted or activated an unknown plant gene which resulted in such radical changes in GR physiology. It is possible that the GR gene disrupted regulators responsible for plant cell wall biosynthesis. There have been recent developments in functional genomics related to transgenic tobacco specifically altered in its lignocellulosic composition to better understand changes in cellulose, hemicellulose and lignin biosynthetic pathways8,4. It has been established that cellulose, hemicellulose and lignin biosynthetic pathways are interdependent and any increase or decrease in concentration of lignocellulosic components in tobacco secondary cell wall can be 47 directly correlated with concomitant changes in expression of associated gene at transcriptional level8. In a recent study lignin biosynthetic enzyme, O-methyl transferase (OMT) has been reported to increase overall biomass accumulation in transgenic tobacco without any changes in lignin deposition2,4. In another such study Cinnamoiyl-COA-reductase (CCR) was down regulated in transgenic tobacco which resulted in overall drop in lignin and simultaneous increase in xylose and cellulose concentration in tobacco secondary cell wall5,15. These results resonate with our finding in GR line as it showed an overall increase in biomass accumulation with concomitant increase in xylose and cellulose concentration with respect to control line. It was also observed that in GR lines (1, 2, and 3) lignin deposition drops between 30 and 90 days. Therefore there is a possibility that expression of OMT and COMT related genes is being altered in GR line. However it is hard to speculate how lignin concentration changes within GR line stem after 90 days due to experimental limitations, but it was observed that on average lignin concentration in GR line stem at 135 days was higher than control line as seen in figure14. This brings us to another possibility that there may be a delay in in lignin deposition in GR line 1, 2 and 3 between 30 and 90 days. This hypothesis can be correlated with a recent finding where lignin accumulation was delayed in transgenic tobacco with altered expression of phenylpropanoid pathway associated enzyme class II cinnamate 4-hydroxylase3. However to better understand these changes in GR line we need further analysis using proteomics of cell wall related genes. 48 Figure14: Glucan, Xylan and Lignin concentration in GR (n=4) and Control (n=3) line stem at 135 days. Figure15: Glucan, Xylan and Lignin concentration in GR (n=4) and Control (n=3) line stem at 135 days. 49 Conclusion The giant recombinant was obtained after a routine Agrobacterium mediated genetic transformation.GR line was characterized relative to control line; it was concluded that the relative efficiency of GR line to produce biomass was found out to be 1.6 times that of control line. GR line also accounted for 240% more biomass relative to control line within 135 days of its germination. It was also observed that there were significant differences in lignocellulosic composition within GR lines (1, 2, 3, 4) and compared to control line during plant growth which need further analysis and may lead to identification of unknown GR gene. Identification of GR gene with enhanced biomass productivity can provide a breakthrough that will help secure future energy resource. The GR gene could conceivably turn any other plant species and eco-friendly fuel source that can help alleviating global dependence on fossil fuels 50 References 1. Biemelt, S., H. Tschiersch and U. Sonnewald. 2004. Impact of Altered Gibberellin Metabolism on Biomass Accumulation, Lignin Biosynthesis, and Photosynthesis in Transgenic Tobacco Plants. Plant Physiology135(1): 254-265. 2. Blaschke, L., M. Legrand, C. Mai and A. Polle. 2004. Lignification and structural biomass production in tobacco with suppressed caffeic/5-hydroxy ferulic acid-Omethyl transferase activity under ambient and elevated CO2 concentrations. Physiologia Plantarum 121(1): 75-83. 3. Blee, K., J. W. Choi, A. P. O’Connell, S. C. Jupe, W. Schuch, N. G. Lewis and G. P. Bolwell. 2001. Antisense and sense expression of cDNA coding for CYP73A15, a class II cinnamate 4-hydroxylase, leads to a delayed and reduced production of lignin in tobacco. Phytochemistry 57(7): 1159-1166. 4. Blee, K. A., J. W. Choi, A. P. O'Connell, W. Schuch, N. G. Lewis and G. P. Bolwell. 2003. A lignin-specific peroxidase in tobacco whose antisense suppression leads to vascular tissue modification. Phytochemistry64(1): 163-176. 5. Chabannes, M., A. Barakate, C. Lapierre, J. M. Marita, J. Ralph, M. Pean, S. Danoun, C. Halpin, J. Grima-Pettenati and A. M. Boudet. 2001. Strong decrease in lignin content without significant alteration of plant development is induced by simultaneous down-regulation of cinnamoyl CoA reductase (CCR) and cinnamyl alcohol dehydrogenase (CAD) in tobacco plants. The Plant Journal 28(3): 257270. 6. Chris Somerville. February 2007. Biofuels. Current Biology 17(4):. 51 7. Cockcroft, Claire E.den Boer, Bart G. W. Healy, J. M. Sandra Murray, James A. H. 2006. Cyclin D control of growth rate in plants. Nature 405(- 0028-0836 (Print); - 0028-0836 (Linking)):. 8. Cook, C. M., A. Daudi, D. J. Millar, L. V. Bindschedler, S. Khan, G. P. Bolwell and A. Devoto. 2012. Transcriptional changes related to secondary wall formation in xylem of transgenic lines of tobacco altered for lignin or xylan content which show improved saccharification. Phytochemistry 74(0): 79-89. 9. Coombs, J., D. O. Hall and P. Chartier. 1983. Growth and Respiration. Plants as solar collectors. Solar energy R& D in the European community 4(Series E, Energy from biomass): 74-75. 10. Filipenko, E. A., E. V. Deineko and V. K. Shumnyi. 2009. Specific Features of TDNA Insertion Regions in Transgenic Plants. Russian Journal of Genetics 451461-1475. 11. Grabber, J. H. How Do Lignin Composition, Structure, and Cross-Linking Affect Degradability? A Review of Cell Wall Model Studies This paper was originally presented at the Lignin and Forage Digestibility Symposium, 2003 CSSA Annual Meeting, Denver, CO. Crop Sci. 45(3): 820-831. 12. Gressel, J. 2008. Transgenics are imperative for biofuel crops. Plant Science 174(3): 246-263. 13. Hill, J., E. Nelson, D. Tilman, S. Polasky and D. Tiffany. 2006. Environmental, economic, and energetic costs and benefits of biodiesel and ethanol 52 biofuels. Proceedings of the National Academy of Sciences 103(30): 1120611210. 14. Himmel, M. E., S. Ding, D. K. Johnson, W. S. Adney, M. R. Nimlos, J. W. Brady and T. D. Foust. 2007. Biomass Recalcitrance: Engineering Plants and Enzymes for Biofuels Production. Science 315(5813): 804-807. 15. Kavousi, B., A. Daudi, C. M. Cook, J. Joseleau, K. Ruel, A. Devoto, G. P. Bolwell and K. A. Blee. 2010. Consequences of antisense down-regulation of a lignification-specific peroxidase on leaf and vascular tissue in tobacco lines demonstrating enhanced enzymatic saccharification. Phytochemistry 71(5–6): 531-542. 16. Lee, D., R. Nair and A. Chen. 2009. Regulatory hurdles for transgenic biofuel crops. Biofuels, Bioproducts and Biorefining 3(4): 468-480. 17. Macchiavelli, R. E. and E. B. Moser. 1997. Analysis of Repeated Measurements with Ante-Dependence Covariance Models. Biometrical Journal 39(3): 339-350. 18. Rogers, L. A. and M. M. Campbell. 2004. The genetic control of lignin deposition during plant growth and development. New Phytologist 164(1): 17-30. 19. Salas Fernandez, M. G., P. W. Becraft, Y. Yin and T. Lübberstedt. 2009. From dwarves to giants? Plant height manipulation for biomass yield. Trends in plant science 14(8): 454-461. 20. Schlamadinger, B., M. Apps, F. Bohlin, L. Gustavsson, G. Jungmeier, G. Marland, K. Pingoud and I. Savolainen. 1997. Towards a standard methodology 53 for greenhouse gas balances of bioenergy systems in comparison with fossil energy systems. Biomass and Bioenergy 13(6): 359-375. 21. Schnepf, R. and B. D. Yacobucci. 2013. Renewable Fuel Standard (RFS): Overview and Issues. Congressional research services(R40155): 7-5700. 22. Ser, G. 2012. Determination of appropriate covariance structures in random slope and intercept model applied in repeated measures The Journal of Animal & Plant Sciences 22(3)(ISSN: 1018-7081): 552-555. 23. Sluiter, A., B. Hames, R. Ruiz, C. Scarlata, J. Sluiter and D. Crocker. August 2012. Determination of Structural Carbohydrates and Lignin in Biomass. Laboratory Analytical Procedures (April 2008):. 24. Sticklen, M. 2006. Plant genetic engineering to improve biomass characteristics for biofuels. Current opinion in biotechnology 17(3): 315-319. 25. Vickery, H. B., G. W. Pucher, C. S. Leaveworth and A. J. Wakeman. 1935. Chemical investigation of tobacco plant V. Chemical changes that occur during growth. Connecticut Agricultural Experiment Station Bulletin 374557-619. 54 APPENDIX Sample SAS CODE: Data Glucan; do plantline= 1 to 5; do rep=1 to 3; input subject @@; do time=30,90; input Glucan @@; thr=time/30; th2=thr*thr; output; end; end; end; datalines; 1 33.22640489 33.50265384 2 34.16762699 31.90636455 3 35.55962435 33.89666505 4 24.36385764 34.53505701 5 29.71597434 33.79750621 6 28.29800559 32.16857203 7 22.91810191 35.32355045 8 22.56839771 34.44263457 9 22.90929911 34.06263443 10 23.91101249 33.58624802 11 18.31847571 32.89844168 12 19.31516726 33.7919419 13 32.22565317 32.15704768 14 31.66298303 32.12943025 15 30.87524484 32.8612922; proc print; run; title 'Compound Symmetry with full model'; run; proc glimmix data=Glucan; class phenotype subject; model Glucan=phenotype thr phenotype*thr th2 phenotype*th2/htype=1 ddfm=kr; random _residual_/subject=subject type=cs; run; title 'Unstructured with full model'; run; proc glimmix data=Glucan; class phenotype subject; model Glucan=diet thr phenotype*thr th2 phenotype*th2/htype=1 ddfm=kr; random _residual_/subject=subject type=un; run; title 'AR(1) with full model'; run; proc glimmix data=Glucan; class phenotype subject; model Glucan=phenotype thr phenotype*thr th2 phenotype*th2/htype=1 ddfm=kr; 55 random _residual_/subject=subject type=ar(1); run; title 'Toeplitz with full model'; run; proc glimmix data=glucose; class phenotype subject; model Glucan=phenotype thr phenotype*thr th2 phenotype*th2/htype=1 ddfm=kr; random _residual_/subject=subject type=toep; run; title 'Ante-dependence with full model'; run; proc glimmix data=Glucan; class phenotype subject; model Glucan=phenotype thr phenotype*thr th2 phenotype*th2/htype=1 ddfm=kr; random _residual_/subject=subject type=ante(1); run; title 'Ante-dependence with full model'; run; proc glimmix data=Glucan; class phenotype subject; model Glucan=phenotype thr phenotype*thr th2 phenotype*th2/htype=1 ddfm=kr solution; random _residual_/subject=subject type=ante(1); run; title 'Ante-dependence with separate estimates for slope and quadratic by treatment'; run; proc glimmix data=Glucan; class phenotype subject; model Glucan=phenotype thr(phenotype) th2(phenotype)/htype=1 ddfm=kr solution noint; random _residual_/subject=subject type=ante(1); ods output parameterestimates=solf; run; data solf; drop phenotype; set solf; pheno=phenotype; run; proc print data=solf; run; proc sort data=solf; by pheno; run; proc transpose data=solf (keep=pheno effect estimate) out=solpl; by pheno; id effect; var estimate; run; proc print data=solpl; run; data ploteq; set solpl; by pheno; do x=1 to 3 by 1; Glucan=phenotype+thr_phenotype_*x+th2_phenotype_*x*x; output; end; run; 56 proc print data=ploteq; run; title 'Glucan by phenotype over time'; run; goptions colors=(red) i=join; symbol1 v=star; symbol2 v=circle; symbol3 v=square; symbol4 v=triangle; symbol5 v=z; symbol6 v=x; proc gplot data=ploteq; plot Glucan*x=pheno; run; plot Glucan*x=pheno/ autohref lhref=2 chref=lime autovref lvref=5 cvref=pink caxis=blue ctext=red ; run; proc glimmix data=Glucan; class phenotype subject; model Glucan=phenotype thr(phenotype) th2(phenotype)/htype=1 e1 noint solution;* ddfm=kr solution noint; random _residual_/subject=subject type=ante(1); run; proc glimmix data=Glucan; class phenotype subject; model Glucan=phenotype thr(phenotype) th2(phenotype)/htype=1 e1 noint solution;* ddfm=kr solution noint; random _residual_/subject=subject type=ante(1); contrast 'variety 1 vs 2 linear' thr(phenotype) 1 -1 0 0 0 th2(phenotype) 1 -1 0 0 0 ; contrast 'variety 1 vs 3 linear' thr(phenotype) 1 0 -1 0 0 th2(phenotype) 1 0 -1 0 0 ; contrast 'variety 1 vs 4 linear' thr(phenotype) 1 0 0 -1 0 th2(phenotype) 1 0 0 -1 0 ; contrast 'variety 1 vs 5 linear' thr(phenotype) 1 0 0 0 -1 th2(phenotype) 1 0 0 0 -1 ; contrast 'variety 2 vs 3 linear' thr(phenotype) 0 1 -1 0 0 th2(phenotype) 0 1 -1 0 0 ; contrast 'variety 2 vs 4 linear' thr(phenotype) 0 1 0 -1 0 th2(phenotype) 0 1 0 -1 0 ; contrast 'variety 2 vs 5 linear' thr(phenotype) 0 1 0 0 -1 th2(phenotype) 0 1 0 0 -1 ; contrast 'variety 3 vs 4 linear' thr(phenotype) 0 0 1 -1 0 th2(phenotype) 0 0 1 -1 0 ; contrast 'variety 3 vs 5 linear' thr(phenotype) 0 0 1 0 -1 th2(phenotype) 0 0 1 0 -1 ; contrast 'variety 4 vs 5 linear' thr(phenotype) 0 0 0 1 -1 th2(phenotype) 0 0 0 1 -1 ; contrast 'variety 1 vs 2 quadratic' th2(phenotype) 1 -1 0 0 0 ; contrast 'variety 1 vs 3 quadratic' th2(phenotype) 1 0 -1 0 0 ; contrast 'variety 1 vs 4 quadratic' th2(phenotype) 1 0 0 -1 0 ; contrast 'variety 1 vs 5 quadratic' th2(phenotype) 1 0 0 0 -1 ; contrast 'variety 2 vs 3 quadratic' th2(phenotype) 0 1 -1 0 0 ; contrast 'variety 2 vs 4 quadratic' th2(phenotype) 0 1 0 -1 0 ; contrast 'variety 2 vs 5 quadratic' th2(phenotype) 0 1 0 0 -1 ; contrast 'variety 3 vs 4 quadratic' th2(phenotype) 0 0 1 -1 0 ; contrast 'variety 3 vs 5 quadratic' th2(phenotype) 0 0 1 0 -1 ; contrast 'variety 4 vs 5 quadratic' th2(phenotype) 0 0 0 1 -1 ; run; 57 Files included in CD-ROM a) Complete Statistical Analysis b) Calculations EXCEL files
© Copyright 2026 Paperzz