Recipient Organization
ZESTBIO, INC.
2715 HILLEGASS AVE
BERKELEY,CA 947051229
Performing Department
(N/A)
Non Technical Summary
The United States is uniquely positioned as a world leader in fruit and vegetable processing, including sugar production from sugar beets (37 million tons/yr) and citrus juicing (3 million tons/yr). However, there is a lack ofvalue-adding technologies for these abundantpeel and pulp byproducts.ZestBio, Inc. is developing biotechnologies for the production of specialty chemicals from these agricultural byproducts.The first chemical product from this bioprocessing technology can be formulated for water treatment applications. These formulations exhibit superior heavy metal binding compared to chemcials currently sold. Additionally, these formulations preventmild steel corrosion. Thus, this new ingredientsatisfiesgrowing demand for sustainable and high-performing chemicals.Implementation of our biomanufacturing process can increase overall crop revenue. This offers reduced volatility in crop value, financial sustainability for farmers, and construction of rural-located fermentation facilities to create high paying technical jobs. New ingredients with improved performance in the water treatment industry can help owners of capital equipment that requirecorrosion treatment by extending thelifespan of their equipment and lowered operating costsfrom improved performance. Furthermore, this new ingredient will havean improved environmental footprint (protecting our US waterways) and provide a reliable chemicalsupply sourced from the USA instead of from China and elsewhere abroad.The overall project goal is to prepare the technology for scaling in pilot-scale bioreactors. First, we propose improving the stability of the enzymes we use in our chemical manufacturing process by tweaking their structure. Second, we propose improving the yieldof these enzymes by optimizing the production conditions. Third, we propose optimization and scaling of the chemical synthesis from citrus peel waste and sugar beet pulpinbioreactors. The anticipated results from this work plan are a technology ready for pilot-scale manufacturing.
Animal Health Component
0%
Research Effort Categories
Basic
0%
Applied
0%
Developmental
100%
Goals / Objectives
ZestBio, Inc. is developing technologies for the production of specialty chemicals from prevalent byproducts of the US fruit and vegetable processing industries.The main goal for thisprojectis to develop a benchscale process fora value-adding in vitro enzymatic conversion technology for the conversion of pectic monosaccharides into specialty chemicals. Achieving this goal will mark a key milestone in the technology development where the technology will be ready for scaling into larger pilot conversion reactions.There are three main objectives towards achieving this goal:Reductase screening and engineering with the target of identifying a reductase with a total turnover number of 2,000,000 in 24 hours.Optimization of protein expression for uronate dehydrogenase and the engineered reductase enzyme to improve enzyme units yield per liter of E. coli by 50%Scaling conversion reactions to 2 liter bioreactors via reaction validation and optimization in 200 mL bioreactors including a design of experiments analysis to build a model approximating the impact of different operating parameters on production.
Project Methods
Objective 1: Reductase screening and engineering with the target of identifying a reductase with a total turnover number of 2,000,000 in 24 hours.Methods:BLAST and literature search to identify reductase enzymes to screenCodon optimization of target reductase enzyme protein sequences for expression in E coli using published toolsOrdering of DNA sequencesPCR mutagenesis of select genes of interestCloning and transformation of DNA sequences for T7-inducible expression of proteins in E coliVerification of cloning success via DNA sequencingGrowth of E. coli for protein expression including induction of promotorChemical lysis of E coli cultureEnzymatic conversions setup using E coli lysate in either citrus peel waste or sugar beet pulpMeasurement of sugar and product titers in converted hydrolysate by sampling and running extracts on HPLCEvalulations:Restriction digests of plasmidsDNA sequencing of plasmidsMeasurement of protein activity units via NAD assaysMeasurement of substrate and product concentrations via HPLCObjective 2: Optimization of protein expression for uronate dehydrogenase and the engineered reductase enzyme to improve enzyme units yield per liter of E. coli by 50%Methods:Cloning of reductase and dehydrogenase genes into different expression plasmidsVerification of cloning success by restriction digest and DNA sequencingTransformation of verified plasmids into BL21 E coli cellsGrowth and protein expression for transformed E coli under an array of medias and growth conditionsMeasurement of cell density, chemical lysis, and measurement of activity units in lysateDesign of Experiments analysis of activity yield as a function of different growth conditionsGrowth and protein expression usingE coli in 2L bioreactorsEvaluations:Restriction digests of plasmidsDNA sequencing of plasmidsMeasurement of protein activity units via NAD assaysObjective 3: Scaling conversion reactions to 2 liter bioreactors via reaction validation and optimization in 200 mL bioreactors including a design of experiments analysis to build a model approximating the impact of different operating parameters on production.Methods:Processing of peels/pulp to low particle sizeEnzymatic hydrolysis of peels/pulp to release trapped sugarsFiltrations and washing to remove solids and recover released sugarsEvaporation to concentrate hydrolysatesSonication lysis ofE coli cell pellets and QC via NAD activity assaysSetup and operation of bioreactors with varying operating conditions and varying media compositionsSampling of bioreactors and feeding components such as additional e coli lysatesSample prep and HPLC analysis of sugar substrates and product concentrationsDesign of Experiments modeling of reaction outputs as measured by HPLCEvaluations:Measurement of protein activity units via NAD assaysMeasurement of bioreactor conditions: dissolved oxygen, pH, air flowMeasurement of substrate and product concentrations via HPLC