Difference between revisions of "Team:OUC-China/Design"

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         <h3 class="ouc-heading"><strong>Basic fermentation</strong></h3>
 
         <h3 class="ouc-heading"><strong>Basic fermentation</strong></h3>
 
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         The use of plant biomass for biofuel production will require efficient utilization of the sugars in lignocellulose, while in terrestrial plants the content of cellulose is quite hard to use. By contrast, cellulose in macroalgae has looser texture and lower proportion, which makes it an ideal material for biofuel production. As a coastal university, we have a profound theoretical foundation of the sea and of course, algae. Therefore, it is natural that we think of algae as our substrate.  
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         The use of plant biomass for biofuel production will require efficient utilization of the sugars in lignocellulose, while in terrestrial plants the content of cellulose is quite hard to use.[1] By contrast, cellulose in macroalgae has looser texture and lower proportion, which makes it an ideal material for biofuel production.[2] As a coastal university, we have a profound theoretical foundation of the sea and of course, algae. Therefore, it is natural that we think of algae as our substrate.  
 
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         Before the construction of the plasmid, however, we need to deal with glucose repression. We all know that even yeasts engineered to ferment xylose cannot utilize xylose until glucose is completely consumed, which makes the process of fermentation rather slow when in present of glucose. To overcome these bottlenecks, we decide to separate the fermentation of xylose and cellobiose into two yeast strains, which means substrates can be transported into the cell thus isolate glucose from their shared environment and avoid their mutual interference. In other words, intracellular hydrolysis of cellobiose minimizes glucose repression of xylose fermentation. what's more, we can also lighten their metabolic burden using this strategy.
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         Before the construction of the plasmid, however, we need to deal with glucose repression.[3] We all know that even yeasts engineered to ferment xylose cannot utilize xylose until glucose is completely consumed, which makes the process of fermentation rather slow when in present of glucose. To overcome these bottlenecks, we decide to separate the fermentation of xylose and cellobiose into two yeast strains, which means substrates can be transported into the cell thus isolate glucose from their shared environment and avoid their mutual interference. In other words, intracellular hydrolysis of cellobiose minimizes glucose repression of xylose fermentation. what's more, we can also lighten their metabolic burden using this strategy.[4]
 
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         After grinding our <i>Enteromorpha</i> into powder and extract polysaccharide we get the remains of algae which has the same content as <i>Enteromorpha</i> waste. Because in industrial manufacture, the former one can be well utilized, we mainly focus on the residue of algae containing cellulose and hemicellulose majorly. For a higher reaction efficiency and better utilization of cellulose and hemicellulose, we treat the residue with H<sub>2</sub>O<sub>2</sub> to remove the lignin. H<sub>2</sub>O<sub>2</sub> is clean pollution free and low cost, which makes it a perfect reagent for pretreatment. After that, the lignin is mostly removed and the microstructure of cellulose will break down, exposing more binding site, which makes it easier to use.
+
         After grinding our <i>Enteromorpha</i> into powder and extract polysaccharide we get the remains of algae which has the same content as <i>Enteromorpha</i> waste. Because in industrial manufacture, the former one can be well utilized, we mainly focus on the residue of algae containing cellulose and hemicellulose majorly. For a higher reaction efficiency and better utilization of cellulose and hemicellulose, we treat the residue with H<sub>2</sub>O<sub>2</sub> to remove the lignin.[5] H<sub>2</sub>O<sub>2</sub> is clean pollution free and low cost, which makes it a perfect reagent for pretreatment. After that, the lignin is mostly removed and the microstructure of cellulose will break down, exposing more binding site, which makes it easier to use.
 
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         As for cellobiose and xylose, we designed two recombinant yeast strains. For yeast A, we subcloned cellobiose transporter and β-glucosidase genes into a plasmid and introduce it to <i>S.cerevisiae</i>. The cellobiose transporter can help transport cellobiose from the environment into the cell and β-glucosidase will turn cellobiose into glucose, which can then be transformed into ethanol through its own pathway. In the same way, we introduced xylitol dehydrogenase and xylose reductase gene to yeast B. <i>S.cerevisiae</i> naturally has the ability to transport xylose. With xylosereductase (XR), xylose can be reduced to xylitol, which will then be oxidized to xylulose in present of xylitol dehydrogenase. Xylulokinase of wild type <i>S.cerevisiae</i> can then phosphorylate xylulose to xylulose-5-phosphate. Finally, it will join Pentose Phosphate Pathway (PPP) and produce ethanol.
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         As for cellobiose and xylose, we designed two recombinant yeast strains. For yeast A, we subcloned cellobiose transporter and β-glucosidase genes into a plasmid and introduce it to <i>S.cerevisiae</i>. The cellobiose transporter can help transport cellobiose from the environment into the cell and β-glucosidase will turn cellobiose into glucose, which can then be transformed into ethanol through its own pathway.[6] In the same way, we introduced xylitol dehydrogenase and xylose reductase gene to yeast B. <i>S.cerevisiae</i> naturally has the ability to transport xylose. With xylosereductase (XR), xylose can be reduced to xylitol, which will then be oxidized to xylulose in present of xylitol dehydrogenase. Xylulokinase of wild type <i>S.cerevisiae</i> can then phosphorylate xylulose to xylulose-5-phosphate. Finally, it will join Pentose Phosphate Pathway (PPP) and produce ethanol.[7]
 
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Revision as of 17:56, 30 October 2017

Design

Basic fermentation

The use of plant biomass for biofuel production will require efficient utilization of the sugars in lignocellulose, while in terrestrial plants the content of cellulose is quite hard to use.[1] By contrast, cellulose in macroalgae has looser texture and lower proportion, which makes it an ideal material for biofuel production.[2] As a coastal university, we have a profound theoretical foundation of the sea and of course, algae. Therefore, it is natural that we think of algae as our substrate.

However, we soon meet with another problem---the main sugar used by trains of Saccharomyces cerevisiae currently in bioethanol production is glucose. Other saccharides such as xylose and cellobiose are relatively harder to ferment. It means a lot more energy and cost we need to donate to pretreatment. Therefore, if we can design a recombinant strain capable of using xylose or cellobiose, it will be a big step further since the yeast can take the place of chemicals and fulfill the task itself.

Before the construction of the plasmid, however, we need to deal with glucose repression.[3] We all know that even yeasts engineered to ferment xylose cannot utilize xylose until glucose is completely consumed, which makes the process of fermentation rather slow when in present of glucose. To overcome these bottlenecks, we decide to separate the fermentation of xylose and cellobiose into two yeast strains, which means substrates can be transported into the cell thus isolate glucose from their shared environment and avoid their mutual interference. In other words, intracellular hydrolysis of cellobiose minimizes glucose repression of xylose fermentation. what's more, we can also lighten their metabolic burden using this strategy.[4]

Now we can begin our project.

After grinding our Enteromorpha into powder and extract polysaccharide we get the remains of algae which has the same content as Enteromorpha waste. Because in industrial manufacture, the former one can be well utilized, we mainly focus on the residue of algae containing cellulose and hemicellulose majorly. For a higher reaction efficiency and better utilization of cellulose and hemicellulose, we treat the residue with H2O2 to remove the lignin.[5] H2O2 is clean pollution free and low cost, which makes it a perfect reagent for pretreatment. After that, the lignin is mostly removed and the microstructure of cellulose will break down, exposing more binding site, which makes it easier to use.

As for the utilization of cellulose there are three main stages: dense fiber with a high content of lignin, cellodextrin, monosaccharide. Since the process from dense fiber to cellodextrin has been a proven technique, we use enzymes to treat cellulose and hemicellulose into cellobios and xylose. And our major work will be based on these two substrates.

As for cellobiose and xylose, we designed two recombinant yeast strains. For yeast A, we subcloned cellobiose transporter and β-glucosidase genes into a plasmid and introduce it to S.cerevisiae. The cellobiose transporter can help transport cellobiose from the environment into the cell and β-glucosidase will turn cellobiose into glucose, which can then be transformed into ethanol through its own pathway.[6] In the same way, we introduced xylitol dehydrogenase and xylose reductase gene to yeast B. S.cerevisiae naturally has the ability to transport xylose. With xylosereductase (XR), xylose can be reduced to xylitol, which will then be oxidized to xylulose in present of xylitol dehydrogenase. Xylulokinase of wild type S.cerevisiae can then phosphorylate xylulose to xylulose-5-phosphate. Finally, it will join Pentose Phosphate Pathway (PPP) and produce ethanol.[7]

Now we have two strains that can live on either cellobiose or xylose and can produce ethanol through their own metabolic pathways, which means they can ferment cellobiose and xylose synergistically.

Adhesion platform

Through a co-expression platform between heterogeneous cells, we make E.coli the surface display system of S.cerevisiae to enrich its biofunctions and enhance their synergistic effect.

We select the biotin-streptavidin system to accomplish our adhesion because it is known as the strongest covalent binding system in nature. By introducing ice nucleation protein (INP) and monomer streptavidin adhesion (mSA) fusion protein to E.coli, we express mSA on its surface with INP, which is intergrated into the out membrane itself. Meanwhile, we express biotin acceptor peptide (BAP) and biotin ligase (BirA) in the S.cerevisiae strain EBY100. This strain of yeast contains pYD1, which has another surface-display system called Aga1p-Aga2p adhesion system. By using this strain, we will be able to express biotinylated BAP on the yeast surface. Ultimately, E.coli and S.cerevisiae can connect firmly with each other through the covalent binding of biotin and streptavidin.

The following question may better elucidate our designing details:

Q1. Why choose to establish an adhesion platform?

At the beginning of our project, we want to express cellulosome in Saccharomyces cerevisiae, where cellulase can located. Then the cellulase can degrade Enteromorpha into cellobiose and xylose. The latter two can be used by S.cerevisiae as the source of fermentation. Although cellulosome is a method to degrade cellulose with high efficiency, it also have a complex structure combined with multiple scaffold protein and cellulase domain which will accrete the difficulty of experiment design and give the S.cerevisiae a heavier burden. Obviously, too much burden can harm the ferment efficiency.


Fig 2.1

Thus, we think of E.coli to do the part of cellulosome. Because E.coli is a model strain, we can change its feature and function easily, and its plasmid has both proper copy number and size that can lead to a lighter burden than that in Saccharomyces cerevisiae. Moreover, we can separate degradation step and fermentation step through this method, which leads to higher efficiency.

Q2:What’s the preponderance of our platform?

This platform consists of two parts, monomer streptavidin surface display system and biotin surface display system. It is known that avidin can bind with biotin firmly in nature, so we choose the biotin-avidin system to achieve the adhesion between heterogenous cells. An important advantage of this platform is that it is not a traditional co-culture system. Through the exploration of express condition, we break the obstacle of the pollution between heterogenous cells. At the same time, we can use the adhesion platform to build a CBP (consolidated bioprocessing ) degradation and fermentation system.

Q3: Why choose ice nuclear protein as the surface display system of E.coli?

INP is a kind of secretive outer membrane protein that exists in gram-negative bacteria like Pseudomonas syringae. The N-terminator domain contains abundant aspartic acid and hydrophilic serine and threonine, and can be fixed on the surface of cells through glycosyl phosphatidyl inositol(GPI), which is good for the display of macro heterogenous protein. Compared to the Lpp-OmpA fused protein, this system will not lead to an unstable growth of cell, thus, the choice of anchor unit is the key to construct the surface display system. Furthermore, INP surface display system has the following advantages: 1) it can be expressed in many kinds of gram-negative bacteria with a steady expression level. 2) INP can display large molecular weight protein, so it has a larger applicate range. 3) INP naturally has the ability to secrete, locate, and anchor a cell, and can display interest protein without accessory protein. It has been confirmed useful in many reports..


Fig 2.2

Fig 2.3

Q4: Why choose The Yeast Display System with the a-agglutinin receptor?

To stabilize cell-cell interactions during mating and to facilitate fusion between a and α haploid yeast cells, we choose this receptor. The Yeast Display System uses the a-agglutinin receptor of S. cerevisiae to display foreign proteins on the cell surface. The a-agglutinin receptor consists of two subunits encoded by the AGA1 and AGA2 genes. The Aga1 protein (Aga1p, 725 amino acids) is secreted from the cell and becomes covalently attached to β-glucan in the extracellular matrix of the yeast cell wall. The Aga2 protein (Aga2p, 69 amino acids) binds to Aga1p through two disulfide bonds and after secretion remains attached to the cell through its contact with Aga1p. The N-terminal portion of Aga2p is required for attachment to Aga1p, while proteins and peptides can fuse to the C-terminus for presentation on the yeast cell surface. A yeast display system is particularly useful for mammalian cell surface and secreted proteins (e.g., receptors, cytokines) that require endoplasmic reticulum-specific posttranslational processing for efficient folding and activity.


Fig 2.4

Q5: How to establish a functional adhesion platform?

At first, we consider using INP surface display system in E.coli to display mSA thus bind with biotin in S.cerevisiae and use OmpA surface display system to display cellulase and hemicellulase, so that cellulose and hemicellulose can be degraded and utilized by S.cerevisiae. However, we found that OmpA-CenA (a kind of cellulase in part registry) did not have the correct function as we expect. Therefore, we decide to construct the adhesion platform.

We use INP from BBa_K523013, BBa_J23106 and mSA from team Peking to build our part J23106-INP-mSA with a 4X linker. Similarly we acquire BirA from E.coli genome that can biotinylate biotin accepted peptide (BAP). In addition, we use pYD1 to display BAP on the surface of S.cerevisiae.

We co-culture these two strains and explore the proper condition to culture them together. To analyze this system with mathematical model, we also characterize the growth curve of these two strains and the only consumption rate of the corresponding carbon source. With these data, we simulate a co-culture model, feed back to our wet lab and optimize the experiment condition so that we can get the best ethanol production.

Mini system

We work on a mini system including standardized promoters and terminators with concise structure and powerful function in Yeast, providing more potential for large-scale synthetic biology operations on yeast.

For promoters, previous generations established a plasmid-based non-native, core element scaffold to determine the shortest length required for transcription and to serve as a platform for hybrid promoter technology. This core element scaffold was built on distinct, essential sequences for promoter function—a TATA box with consensus sequence of TATAWAWR24 followed by a transcription start site (TSS) with consensus sequence of A(Arich)5NYAWNN(Arich)6.The UAS elements contain transcription factor-binding sites (TFBS) thought to aid in RNAP stabilization and enhanced transcription rates. For Neutral AT-rich spacer, Hal S. Alper draw a conclusion that 30bp may be the minimal spacing required between the TATA box and TSS for S. cerevisiae.


Fig 3.1 Structure of mini promoters.

For terminators, ZIJIAN GUO et al. have identified that the yeast terminator has three domains,suggested that 39-end formation of yeast mRNAs involves signals having the following three degenerate elements: (i) the efficiency element, which functions by enhancing the efficiency of positioning elements; (ii) the positioning element, which positions the poly(A) site; and (iii) the actual site of polyadenylation. Different terminator will affect the stability of the mRNA, thus affecting the amount of protein translation。Hal S. Alper et al. Changed the length and GC ratios of each region and made a combination of qPCR and fluorescence intensity measurements,they found a strong correlation between transcript and fluorescence which suggests these synthetic terminators are affecting protein expression at the transcript level.


Fig 3.2 Structure of mini terminator.

We make different combinations of these promoters and terminators and construct four circuits and import them into yeasts.

In the circuit, the yECtrine is used to characterize the intensity of promoter and the mStrawberry is used to characterize the leakage of terminator. Compare the fluorescent of different circuits and we can draw some conclusions about our mini system in contrast with common promoter CYC1p and terminator CYC1t on post-translational level.

One step further, we will also test the expression of these genes on post-transcriptional level to illustrate the difference from another perspectives and to provide another firm proof of its behaviour.

Fig 3.3

Reference

[1]Klemm, D, et al. "Cellulose: fascinating biopolymer and sustainable raw material. " Angewandte Chemie 44.22(2005):3358.
[2]Jmel, M. A, et al. "Physico-chemical characterization and enzymatic functionalization of Enteromorpha sp. cellulose. " Carbohydrate Polymers 135(2016):274-279.
[3]Gancedo, Juana M. "Yeast Carbon Catabolite Repression." Microbiology & Molecular Biology Reviews Mmbr 62.2(1998):334.
[4]Ha, S. J., et al. "Engineered Saccharomyces cerevisiae capable of simultaneous cellobiose and xylose fermentation." Proceedings of the National Academy of Sciences of the United States of America 108.2(2011):504.
[5]Liu Zhengkun. "The research on transformed craft of biological ethanol of Enteromorpha prolifera"Diss. Qingdao:Ocean University of China, 2011.
[6]Fan, L. H., et al. "Engineering yeast with bifunctional minicellulosome and cellodextrin pathway for co-utilization of cellulose-mixed sugars." Biotechnology for Biofuels 9.1(2016):137.
[7]Zhang, Y., et al. "[Metabolic engineering for microbial production of ethanol from xylose: a review]. " Chinese Journal of Biotechnology 26.10(2010):1436.
[8]Weber, P. C., et al. "Structural origins of high-affinity biotin binding to streptavidin." Science 243.4887(1989):85-8.
[9]Bloois, Edwin Van, et al. "Decorating microbes: surface display of proteins on Escherichia coli." Trends in Biotechnology 29.2(2011):79.
[10]Demonte, Daniel, et al. "Structure‐based engineering of streptavidin monomer with a reduced biotin dissociation rate." Proteins-structure Function & Bioinformatics 81.9(2013):1621.
[11]Tanaka T, Masunari S, Ishii J, et al. Displaying non-natural, functional molecules on yeast surfaces via biotin-streptavidin interaction[J]. Journal of Biotechnology, 2010, 145(1):79-83.
[12]Park M, Jose J, Thömmes S, et al. Autodisplay of streptavidin.[J]. Enzyme & Microbial Technology, 2011, 48(4):307-311.
[13]Artzi, L, E. A. Bayer, and S. Moraïs. "Cellulosomes: bacterial nanomachines for dismantling plant polysaccharides." Nature Reviews Microbiology 15.2(2017):83.
[14]Redden H,Alper HS,The development and characterization of synthetic minimal yeast promoters[J],Nature Communication,2015,6 : 7810
[15]Curran K A, Morse N J, Markham K A, et al. Short Synthetic Terminators for Improved Heterologous Gene Expression in Yeast[J]. Acs Synthetic Biology, 2015, 4(7):824.



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