The First Step to Higher Yield
Pretreatment is widely classified as the second most expensive unit cost in the conversion of biomass to bio-products. The goal of the pretreatment process is to breakdown lignin and increase the accessibility of the pre-treated biomass to saccharification.
At ABPDU, we take a holistic approach to all unit operations, starting with pretreatment. Our focus is on final yield and product cost. We monitor important factors like the loss of biomass to degradation products and inhibitors generated during the pretreatment process that could reduce fermentation or chemical conversion yields.
Getting the most value
We know that no single pretreatment technology offers 100% conversion of carbohydrates into fermentable sugars. In developing an optimum pretreatment process, we place importance on the following:
- The most effective pretreatment catalyst for a given feedstock
- The compatibility of the feedstock-pretreatment catalyst combination
- The possibility of generating co-products, primarily from lignin
- Opex and capex investments
- Energy requirements for solid-liquid handling, separation, etc.
- Co-product value and residue disposal costs at scale
An Optimum Pretreatment Process
Biomass and feedstock diversity, high biomass loading, product and chemical recovery, and process integration for scale up compound the challenges of obtaining the highest yielding pretreatment process.
Our many advantages help us to design the best process for your specifications:
- A broad range of aqueous phase thermochemical pretreatment processes that are suitable for the widest range of biomass and feedstock
- The ability to combine two or more pretreatment processes to achieve the best results across downstream unit operations.
- Careful analysis of the factors that will achieve the best process economics
- Meticulous assessment of the feasibility of integrating with downstream technologies and deploying the technology at a commercial scale.
Pretreatment Process Options
Mechanical Biomass Size Reduction
Related Papers, Articles, and Presentations
Predictive modeling to de-risk bio-based manufacturing by adapting to variability in lignocellulosic biomass supply
Commercial-scale bio-refineries are designed to process 2000 tons/day of single lignocellulosic biomass. Several geographical areas in the United States generate diverse feedstocks that, when combined, can be substantial for bio-based manufacturing. Blending multiple feedstocks is a strategy being investigated to expand bio-based manufacturing outside Corn Belt. In this study, the ABPDU in collaboration with Idaho and Sandia National Laboratories developed a model to predict continuous envelopes of biomass blends that are optimal for a given pretreatment condition to achieve a predetermined sugar yield or vice versa. For example, the model predicted more than 60% glucose yield can be achieved by treating an equal part blend of energy cane, corn stover, and switchgrass with alkali pretreatment at 120 °C for 14.8 h. By using ionic liquid to pretreat an equal part blend of the biomass feedstocks at 160 °C for 2.2 h, we achieved 87.6% glucose yield. Such a predictive model can potentially overcome dependence on a single feedstock.
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Mixed feedstocks can help reduce the risk associated with feedstock availability for bio-based production of fuels and chemicals. This study was performed to evaluate cellulosic hydrolysates for fermentation to biofuels and also probe the possibility of reducing nutrient concentration in the broth media.
The study demonstrated that mixed feedstocks can release 80 -100% of the sugar that is obtained from corn stover alone. A hundred percent of the released sugars from mixed feedstocks can be converted to ethanol. The study also showed that alkali pretreated mixed feedstock has higher ethanol yield but lower glucose yield compared to IL pretreated mixed feedstock due to inhibition of microbial growth by residual EmimAcetate. The same ethanol yield can be achieved with lower nutrient supplied but with longer fermentation time.
This paper presents two case studies on the scale-up and process integration of municipal solid waste conversion technology. In a partnership with Idaho National Labs, we successfully demonstrated 200-fold scale up of MSW blends IL acidolysis. We also developed an integrated process for ionic liquid based deconstruction technologies for MSW blends conversion. The scale up attempt will leverage the opportunity towards a cost-effective MSW blends conversion technology.
Under a DOE Work-For-Others agreement with FATER, ABPDU has been developing and validating an integrated waste-to-energy process. Key outcomes indicate that post-consumer absorbent hygiene products (AHPs) can be readily and economically converted — without using harsh or expensive pretreatment routes — to sugars and fuel intermediates.
Dry matter loss (DML) occurs in high-moisture storage conditions; it remains unclear how storage conditions and degradation impact sugar release and fermentation inhibitor production during conversion. In collaboration with Idaho National Labs, two feedstocks, switchgrass and corn stover, were compared using compositional analysis, alkaline pretreatment, and enzymatic saccharification. Under the tested conditions, switchgrass with 10% and 20% DML and corn stover with 30% DML achieved higher sugar yields compared to samples before storage.
In a collaborative effort with INL, SNL, and JBEI, predictive modeling was used to evaluate and optimize traditional pretreatment methods for biomass mixture compositions to maximize sugar yield and minimize furfural production. The collaboration encompassed compositional analysis of feedstocks, solids loading during pretreatment for mixed feedstock, enzymatic hydrolysis on unwashed solids, and sugar and furfural analysis. Predictive modeling could effectively identify the pretreatment catalyst and treatment conditions for an “optimal” biomass mixture and the optimal biomass mixture for a particular pretreatment system.
A collaboration between ABPDU, INL, and SNL as to whether blends of municipal solid waste (MSW) and corn stover (CS) could meet cost and quality targets yielded valuable results. The team successfully developed an integrated process for ionic liquid (IL) based deconstruction technologies. They also demonstrated a 200-fold scale up MSW/CS blends IL acidolysis. The scale up attempt and process integration will leverage the opportunity towards a cost-effective sugar/lignin production technology.
Sixteen MSW blends provided by INL were screened using the 10mL tube reactor to identify the most promising blend (CS/MSW 4:1) for scaling up test based on the sugar yields as well as the feedstock cost. The collaboration also successfully demonstrated 600-fold (10mL to 6L) scale up of MSW/CS blends IL acidolysis.
ABPDU has been developing and validating an integrated waste-to-energy process under a DOE work-for-others (WFO) agreement with FATER, an Italian JV between Procter & Gamble and the Angelini Industrial Group.
Key outcomes indicate that post-consumer absorbent hygiene products (AHP) can be readily and economically converted — without using harsh or expensive pretreatment routes — to fermentable sugar intermediates as well as biofuel and bio-based chemical products.
Municipal solid waste (MSW) represents an attractive cellulosic resource for sustainable fuel production. However, its heterogeneity is the major barrier to efficient conversion to biofuels. MSW paper mix was generated and blended with corn stover (CS). It has been shown that both of them can be efficiently pretreated in some ionic liquid (ILs) processes with high yields of fermentable sugars. After pretreatment in 1-ethyl-3-methylimidazolium acetate ([C2C1Im][OAc]), over 80% glucose has been released with enzymatic saccharification. We have also applied an enzyme-free process by adding mineral acid and water directly into the IL/biomass slurry to induce hydrolysis. With the acidolysis process in 1-ethyl-3-methylimidazolium chloride ([C2C1Im]Cl), up to 80% glucose and 90% xylose are released. There is a correlation between the viscosity profile and hydrolysis efficiency; low viscosity of the hydrolysate generally corresponds to high sugar yields. Overall, the results indicate the feasibility of incorporating MSW as a robust blending agent for biorefineries.
Technologies developed for bio-based production are based on single feedstock types. While this approach is applicable for corn stover in the MidWest, for states such as California, with abundant but diverse feedstocks, technologies should be developed to accommodate multiple feedstock input to a single biorefinery. This project established the influence of mixing feedstocks on downstream sugar recovery and thereby fuel production for Imperial County as a case study. To de-risk bio-based production, we relied on statistical approaches and developed a predictive model to identify optimal biomass concentrations and reaction types, temperatures, and times to maximize sugar yield and minimize furfural production.