Source: ENCHI CORPORATION submitted to NRP
ACCELERATED CELLULOSIC ETHANOL PRODUCTION USING CONTINUOUS CASCADE FERMENTATION AND ENGINEERED THERMOPHILIC BACTERIA
Sponsoring Institution
National Institute of Food and Agriculture
Project Status
COMPLETE
Funding Source
Reporting Frequency
Annual
Accession No.
1030262
Grant No.
2023-33530-39420
Cumulative Award Amt.
$181,500.00
Proposal No.
2023-02810
Multistate No.
(N/A)
Project Start Date
Jul 1, 2023
Project End Date
Jul 31, 2024
Grant Year
2023
Program Code
[8.8]- Biofuels and Biobased Products
Recipient Organization
ENCHI CORPORATION
610 LINCOLN ST STE 1
WALTHAM,MA 024512189
Performing Department
Terragia Biofuel Incorporated
Non Technical Summary
(N/A)
Animal Health Component
80%
Research Effort Categories
Basic
10%
Applied
80%
Developmental
10%
Classification

Knowledge Area (KA)Subject of Investigation (SOI)Field of Science (FOS)Percent
51170101100100%
Goals / Objectives
We aim to show a > 2-fold reduction in the reaction time required to achieve high conversion compared to conventional batch processing.The overall Phase I objective is to demonstrate and evaluate cascade continuous fermentation as a means of accelerating consolidated bioprocessing. The demonstration will be performed with lignocellulose feedstocks derived from corn, either corn stover or a mixture of stover and kernels containing at least 50% stover. For processing corn stover at 10 to 12.5 weight % solids, we anticipate reducing the reaction time from about 7 days in batch (Table 2) to about 3.5 days.
Project Methods
Stepwise research approach:1) Determine the maximum solids loading at which fractional carbohydrate solubilization is undiminshed in a steady-state semicontinuous fermentor operated at a relatively short (e.g. 15 hour) residence time;2) Implement continuous-followed-by-batch (CFBB)fermentation at the solids loading determined in 1), and measure carbohydrate conversion as a function of reaction time;3) Run batch controls at the solids loading determined in 1), and measure fracdtional carbohydrate solubilization as a function of reaction time;4) Calculate the ratio of reaction time in 3) compared to reaction time in 2) at high carbohydrate solubilization (operationally defined as > 70% of accessible carbohydrate)Other methods:Corn stover will be provided by POET Research. Corn kernels will be obtained whole, and initially milled in a Wiley knife mill. Both materials will then be milled to a 0.5 mm screen size using a Retsch centrifugal mill.Growth medium will be prepared as described previously (Beri et al., 2020). Fermentations will be inoculated with cocultures of strains of C. thermocellum and T. thermosaccharolyticum engineered for high ethanol yield and titer. Fermentation will be monitored by gas evolution using Ritter gas meters, and fermentor viscosity will be monitored using agitator motor energy usage as a proxy. Continuous operation will be initiated by concomitant solids feeding and broth removal to restore a constant fermentation volume. Solubilization will be established by compositional analysis of solids entering and leaving the system as reported in many papers by the Lynd lab. HPLC using an Aminex HPX-87H column will be used to measure ethanol, acetic acid, lactate and formate, as well as monomer sugars with and without quantitative saccharification.

Progress 07/01/23 to 07/31/24

Outputs
Target Audience:The intended audience for the information generated under this project includes potential investors who would provide future financing for R&D and commercialization, or potential commercial partners, such as biofuel producers and technology providers in the biofuel space. Grant program managers and peer reviewers, along with the wider scientific community are also part of the intended audience. Changes/Problems:No changes were made to the objectives or work plan. Although considerable progress was made on developing a custom fermentation system, unexpected operational difficulties prevented us from realizing the central Phase I objective. These difficulties and the activity to overcome them included: 1. Motors and Variable Frequency Drive units powering them failed and had to be replaced. 2. Load cells on the fermentor provided inconsistent data, but a work around was developed. 3. The seal on the fermentor was leaking, so the clamping mechanism was redesigned. Further details are documented in the Final Technical Report. What opportunities for training and professional development has the project provided?This SBIR funding supported a Frenchmechanical engineer, employed by Terragia under a J-1 cultural exchange and training visa. This engineer consucted research and development under the supervision of the Project Directors while fulfilling all requirements of the J-1 visa program. Additionally, a recent graduate with a Masters degree from the University of Illinois was employed as a bioprocess engineer under the OPT (Optional Practical Training)visa. This young engineer received training and practical training in bioprocess research and development. Antechnician who is a US citizen, who received her BS from Univeristy of Texas in 2022, also worked on this project. Shereceivedtraining in lignocellulose bioprocess research, particularly biomass processing and analysis, cultivation of anaerobicthermophilic bacteria, bioprocess optimization and troubleshooting, fermentation analysis and data reporting. The Project Director continued his professional development under thisaward by further advancing his ability to lead and coordinate grant funded research while also furthering business-orientedcommercialization activities. How have the results been disseminated to communities of interest?Members of the board of directors, potential investors, commercial partners and visiting academic scientists have been shown the equipment used in ths study while visiting the Terragia lab. The capabilities of the system as well as the potential impact on lowering the cost of biomass conversion have been explained. Upon completion of the project objectives, the results will be disseminated to the same audience. What do you plan to do during the next reporting period to accomplish the goals?Work is ongoing with corporate funds to meet the project objectivein time to apply for Phase II SBIR funding.

Impacts
What was accomplished under these goals? A key element of the research plan was a continuously-fed bioreactor fermenting the input material with thermophilic bacteria engineered for high ethanol yield. Building on previous work, a newly designed bioreactor system was obtained for this project (without government funds) that is capable of metered delivery of sterile anaerobic corn stover into a continuous fermentor. We demonstrated consistent solids delivery and continuous fementation with the system. Technoeconomic analysis validated the substantial impact of reduced reaction time on the minimum ethanol selling price and overall economic viability. However, various mechanical and operational problems were encountered that prevented us from testing the central Phase I hypothesis. These problems were mostly overcome, although additional troubleshooting is required before the objectives can be met. Activites towards the objective include: 1. Installation, validation and troubleshooting of advanced bioprocessing equipment. 2. Fermentation of corn stover and production of cellulosic ethanol. 3. Technoeconomic analysis. Data generated from these activities include: 1. Data showing metered solids delivery to a fermentation reactor. 2. Data showing measured fermentation products. 3. Improved equipment designs, including controls and automation. 4. Calculations of minimum ethanol selling price under different processing scenarios. Impacts of the project include: 1. Advanced bioprocessing equipment validated and available for future work. 2. Validation of technical aspects of the company's business plans and potential forfuture revenue.

Publications