• Enzymatic Hydrolysis
    Tests at Celignis

Background on Enzymatic Hydrolysis

Enzymes are biocatalysts and play a key role in biorefinery processes for the biochemical/biological conversion of biomass to biofuels and biobased products.

First generation and second generation biofuels use enzymes for conversion of structural polymers to monomers so that these can then be fermented to the desired fuel by yeast or bacteria.

Starch Biorefinery Enzymes

actions of amylases

Amylases are key enzymes in starch biorefineries. There are two main kinds of amylases that are widely used in industrial applications:


These enzymes are also known as Taka Amylase-A. They are endo-enzymes and are responsible for the initial hydrolysis of starch granules to soluble products. They act in random fashion on alpha (1-4) linkages of amylose and amylopectin, but cannot cleave the branched alpha (1-6) linkages. These enzymes release linear short chain dextrans, oligosachharides, maltose and glucose.


This enzyme, also known as amyloglucosidase, is an exo-acting amylase that can hydrolyse both alpha (1-4) and alpha (1-6) linkages. It works on non-reducing endings of the polysaccharide and releases glucose units.

Lignocellulose Biorefinery Enzymes

Plant biomass is a complex and recalcitrant matrix made of cellulose, hemicellulose and lignin. Lignocellulosic biomass typicaly needs a pre-treatment in order to make cellulose more accessible to enzymes.

The common class of enzymes that are used in lignocellulosic biorefineries are cellulases and xylanases. Lignin-degrading enzymes are also considered important in the biological and biochemical pre-treatment of biomass in order to avoid the formation of inhibitors.

Cellulase Enzymes

actions of cellulases

Cellulases are produced from both bacteria and fungi. Fungal cellulases are a complex of the following individual enzymes: Endoglucanase, exoglucanase and betaglucosidase. Fungal enzymes are the most commonly used cellulases in the advanced biofuels and biorefining industries because of the ability of fungi to produce these enzymes in high titres. The individual enzymes of cellulase act synergistically to breakdown cellulose to glucose:

  • Endoglucanases:

      These enzymes break down the cellulose fibers and expose reducing and non-reducing ends for the action of exoglucanases.

  • Exoglucanases:

      These enzymes further break down the cellulose into the disaccharide cellobiose.

  • Betaglucosidases:

      These enzymes take the cellobiose formed by the action of exoglucanases and break it up into glucose monomers.

  • The products of enzymatic hydrolysis can lead to feedback inhibition on the enzymes. For example, cellobiose has strong inhibition on endo and exo cellulose, but its accumulation beyond a certain concentration is avoided by the action of beta-glucosidase. However, beta-glucosidase itself is feedback-inhibited by glucose and hence cellobiose can accumulate, inhibiting exocellulases and endocellulases. To overcome this, enzyme industries produce mixes of cellulases and individual components of enzymes. In many cases, cellulases are supplemented with excess beta-glucosidases in order to avoid feedback inhibition. Substrate-specific and application-specific enzyme cocktails are developed by supplementing cellulase mixes with individual cellulase components.

    Xylanase Enzymes

    actions of xylanases

    Hemicellulose is a complex branched structure with different sugars and acidic compounds substituted at various positions on a backbone chain. As a result of this, multiple different enzymes are required for the complete hydrolysis of hemicellulose. Xylanases are mixtures of endoxylanases, beta-xylosidases, arabinofuranosidases, galactosidases, acetyl xylan esterases, and alpha-glucuronidases. The mix of xylanolytic enzymes act in synergy to convert xylan polymers to their monomeric constituents.

    Endoxylanases reduce the viscosity of xylan by cleaving the xylan to soluble fragments and beta-xylosidases act on the soluble fragments and xylobiose to release xylose. Arabinofuranosidases and alpha-glucuronidases act on sugar and uronic-acid side groups of xylan.

    Enzymatic Hydrolysis Tests at Celignis

    We are pleased to offer a variety of analysis packages for evaluating both the suitability of biomass for enzymatic digestion and the activities of selected enzymes.

    Evaluation of Biomass and Pre-Treated Biomass for Enzymatic Digestibility

    In analysis package P121 we add an enzyme solution to a sample and incubate it for 3 days, monitoring the sugars that are hydrolysed over time. Subsamples of the hydrolysate are collected after 0, 12, 24, 48, and 72 hours of digestion and are analysed for monosaccharides (glucose, xylose, mannose, arabinose, galactose, rhamnose) and cellobiose using our ion chromatography system. The resulting data allow us to plot a time-series of the concentrations of these sugars in solution and we also provide statistics for the conversion yield and conversion rate of cellulose and xylan.

    These enzymatic hydrolysis tests can be carried out on native biomass and on pre-treated samples and we can either use a commercial enzyme mix or you can supply your own enzymes.

    Evaluation of Pre-Treatment on Enzymatic Digestibility

    Lignocellulose is a recalcitrant feedstock, with cellulose protected by lignin and hemicellulose, so making it less accessible to enzymatic degradation and microbial attack.

    As a result, several pre-treatment strategies to increase the accessibility of cellulose and enhance the digestibility of lignocellulosic biomass by enzymes have been developed. An effective pre-treatment will result in increased accessibility of cellulose to enzymes and thus in high concentrations, yields and productivities of sugars in the enzymatic hydrolysate when compared to the un-treated biomass.

    At Celignis we can undertake the enzymatic hydrolysis of a pre-treated sample using analysis package P121 or we can undertake a more detailed study to evaluate the efficacy of pre-treatment. This study involves analysis package P121 being undertaken on the native (non-pretreated) sample with analysis package P122 used for the enzymatic hydrolysis of the pre-treated sample(s).

    This package allows for the generation of a number of additional statistics outlining the relative advantages of the pre-treated sample(s) as substrates for enzymatic hydrolysis compared with the original sample. These statistics include:

      - Increase in Cellulose Accessibility after Pre-Treatment

    - Percent Increase in Cellulose Conversion Efficiency

    - Percent Increase in Cellulose Conversion Rate

    Fermentation Inhibitors in Enzymatic Hydrolysate

    It should be noted that an increase in digestibility does not always directly result in an increase in fermentability. Inhibitory sugar-degradation products including organic acids (e.g. acetic acid and formic acid), and furans (e.g. furfural and hydroxymethylfurfural) that may be formed during the pre-treatment process can be partially bound to the substrate and may be subsequently released into the enzymatic hydrolysate.

    Based on their concentrations, these inhibitory compounds can negatively affect the fermentation process. For example, furans can inhibit cell replications at higher concentrations whilst weak acids can inhibit fermentation by accumulation of intracellular anions or by uncoupling of cell metabolism. Knowledge of the types of inhibitors in the enzyme hydrolysate and their concentrations will help in developing pre-treatment processes to avoid or reduce inhibitor formation and also to select suitable detoxification processes prior to fermentation.

    We therefore recommend that the analysis of these potentially inhibitory compounds be undertaken when undertaking enzymatic hydrolysis tests, particularly those concerning the evaluation of the efficiency of biomass pre-treatment processes. Our analysis package P124 will determine the concentrations of these important inhibitors in the hydrolysate produced in our enzymatic hydrolysis tests.

    Analysis of the Solid Residue after Enzymatic Hydrolysis

    In order to get the most detailed information about the efficacy of enzymatic digestion, we recommend that the solid residue is analysed for its lignocellulosic composition. The resulting data will show what amounts of the structural polysaccharides have not been hydrolysed and will also help to inform decisions regarding how this residue is valorised.

    In many biorefineries the solid residue after enzymatic hydrolysis is combusted or processed in other thermal conversion technologies (e.g. gasification or pyrolysis) in order to provide process heat and energy. If you would like to evaluate the hdyrolysis residue for this end-use then we recommend that analysis package P40 is also undertaken.

    Cellulase Saccharification Efficiency

    At Celignis we also offer a range of analysis packages for evaluating enzymes and enzyme cocktails. In analysis package P125 we evaluate the efficiency of your enzymes for hydrolysing cellulose. The ability of cellulases to breakdown cellulose to its monomers is called saccharification efficiency and it can vary based on the activity of individual cellulase components. The efficiency is measured by determining the percentage of cellulose converted to glucose under standard/optimum conditions of the enzyme supplied.

    Our cellulose saccharification test can be undertaken using pure cellulose or complex lignocellulosic substrates taken either from Celignis's repository or, alternatively, you can supply these substrates yourself.

    Xylanase Saccharification Efficiency

    The supplementation of xylanases with cellulases is an important strategy to improve the overall saccharification of lignocellulosic biomass. The ability of xylanase to hydrolyse the hemicellulose fraction of lignocellulose to xylose is called xylanase saccharification efficiency. It is measured by determining the percentage of xylan converted to xylose under standard/optimum conditions of the enzyme supplied. This test can be undertaken using pure xylan substrates or xylan-rich complex model substrates taken either from Celignis's repository or, alternatively, you can supply these substrates yourself.

    Amylase Saccharification Efficiency

    The efficiency of amylases to break down the starch polymer to its constituent monomeric sugars is called amylase saccharification efficiency. The level of efficiency and the extent of hydrolysis will depend on the activity of the enzymes alpha-amylase and glucoamylase in the amylase enzyme mix. In analysis package P127 the rate of hydrolysis of starch to glucose and percentage of starch converted to glucose are analysed and given in terms of conversion rate and conversion efficiency respectively.

    Cellulase Activity

    We measure the activity of cellulase enzymes by filter paper assay (FPA) and express the activity in filter paper units (FPU/ml). The conversion of filter paper cellulose to glucose by cellulases is not a linear reaction. Hence, the assay requires enzyme dilutions to release fixed amount of glucose. Because the FPA is based on concentration of product released in a certain time in a nonlinear reaction, a conversion factor is used to approximate a specific activity-type unit.

    Cellulolytic Enzymes Activity

    As described earlier, cellulases are a complex of endocellulases, exocellulases and beta-glucosidases. The total activity of cellulase depends on individual enzymes activities and their ability to act in synergy. In analysis package P129 we can determine the activities of these indivifual enzymes, an important test that will help in understanding the limiting components in the enzyme mix. The different tests undertaken in this analysis package are outlined below:

  • Endoglucanase Activity:

      Endo-b-1,4-D-glucanase (EC randomly cleaves accessible intermolecular b-1,4-glucosidic bonds on the surface of cellulose. We employ the IUPAC-recommended endoglucanase (CMCase) assay which uses carboxymethyl cellulose (CMC) as a substrate and is a fixed conversion method based on 0.5 mg of glucose released under the reaction condition. It is expressed as CMC Units/ml or International Units (IU/ml).

  • beta-Glucosidase Activity:

      Beta-Glucosidase (BGL) acts on Beta-1,4-glucosidic bonds of cellobiose and cellodextrins with a degree of polymerisation (DP) ranging from 3 to 6. It also acts on chromogenic substrates such as para-nitrophenyl glucopyranoside (PNPG). BGL activity can be measured either by using cellobiose or PNPG as substrate. The PNPG assay considers the initial rate of reaction and the enzyme activity is calculated based on the linear range between absorbance and enzyme concentrations. The enzyme activity is expressed in International units (IU/ml).

  • Xylanase Activity:

      D-xylanases are either exo or endo enzymes. Solubilised xylan is used as the substrate for measuring the xylanase activity. Total reducing sugar released by the enzyme is measured and xylanase activity is expressed as international units per ml (IU/ml) which indicates the number of umoles of reducing sugar released per minute per ml of enzyme used.

  • Amylolytic Enzymes Activity

    With analysis package P130 we can determine the activity of amylolytic enzymes. This package involves the following tests:

  • a-Amylase Activity:

      Alpha-amylase is an endo-enzyme and acts randomly on the alpha-1,4 linkages of starch and releases a combination of disaccharides (maltose) and oligosaccharides. One unit of amylase releases 1 mg of maltose in the presence of starch under standard assay conditions. The activity of the enzyme is reported in International units (IU/ml).

  • Glucoamylase Activity:

      Gluco-amylase is both exo-enzyme and acts on both alpha-1,4 and alpha-1,6 linkages of starch. It releases glucose as the final product. One unit of glucoamylase releases 1 mg of glucose in the presence of starch under standard conditions.

  • Summary of Analysis Packages for Enzymatic Hydrolysis and Enzyme Activities

    The analysis packages that we offer for enzymatic hydrolysis and enzyme activities, and the analytes that they determine, are listed below. Click on an entry for further details or go to the Celignis Database to place an order.

    Examples of Cellulosic Biomass Suitable for Enzymatic Hydrolysis Tests

    Publications on Enzymes By The Celignis Team

    Swart, L. J., Bedzo, O. K. K., van Rensburg, E., Gorgens, J. F. (2022) Pilot-scale xylooligosaccharide production through steam explosion of screw press-dried brewers spent grains, Biomass Conversion and Biorefinery 12: 1295-1309


    Brewers spent grains (BSGs) represent the largest quantity of solid waste from brewing, while xylooligosaccharides (XOS) produced from BSG show promising applications in food, beverage and health products. Production of XOS from a Weiss and malt BSG was scaled-up in steam explosion hydrothermal treatment using process conditions from bench-scale liquid hot water optimisations in stirred batch reactors. Three levels of moisture (15, 25 and 32% dry matter) achieved by screw press dewatering were evaluated by varying the treatment temperatures and times. Results show the highest XOS yields (73.1%) were obtained, for both BSGs, at process condition selected (180 C, 10 min) with 25% initial dry matter content. These yields were higher than reported bench-scale optimisations (61%), but obtained using 60% less water; hence, initial dry matter content was an important variable affecting XOS yield. The pilot-scale steam explosion results provide a departing point for a cost-effective commercial production of XOS from BSG.

    Swart, L. J., Bedzo, O. K. K., van Rensburg, E., Gorgens, J. F. (2021) Intensification of Xylo-oligosaccharides Production by Hydrothermal Treatment of Brewers Spent Grains: The Use of Extremely Low Acid Catalyst for Reduction of Degradation Products Associated with High Solid Loading, Applied Biochemistry and Biotechnology 193: 1979-2003


    Brewers' spent grains (BSG) make up to 85% of a brewery's solid waste, and is either sent to landfill or sold as cheap animal feed supplement. Xylo-oligosaccharides (XOS) obtained from BSG are antioxidants and prebiotics that can be used in food formulations as low-calorie sweeteners and texturisers. The effect of extremely low acid (ELA) catalysis in liquid hot water (LHW) hydrothermal treatment (HTT) was assessed using BSG with dry matter contents of 15% and 25%, achieved by dewatering using a screw press. Batch experiments at low acid loadings of 5, 12.5 and 20 mg/g dry mass and temperatures of 120, 150 and 170 C significantly affected XOS yield at both levels of dry mass considered. Maximum XOS yields of 76.4% (16.6 g/l) and 65.5% (31.7 g/l) were achieved from raw BSG and screw pressed BSG respectively, both at 170 C and using 5 mg acid/g dry mass, after 15 min and 5 min, respectively. These XOS yields were obtained with BSG containing up to 63% less water and temperatures more than 20 C lower than that reported previously. The finding confirms that ELA dosing in LHW HTT allows lowering of the required temperature that can result in a reduction of degradation products, which is especially relevant under high solid conditions. This substantial XOS production intensification through higher solid loadings in HTT not only achieved high product yield, but also provided benefits such as increased product concentrations and decreased process heat requirements.

    Swart, L. J., Peterson, A. M., Bedzo, O. K. K., Gorgens, J. F. (2021) Techno-economic analysis of the valorization of brewers spent grains: production of xylitol and xylo-oligosaccharides, Journal of Chemical Technology & Biotechnology 96(6): 1632-1644


    Brewers spent grains (BSG) represents around 85% of a brewery's solid waste and common disposal to landfill is increasingly more difficult. Yet BSG is a food-grade by-product with potential economic valorization that can significantly improve resource efficiency and reduction in carbon emissions. This study investigated valorization of BSG through the application of novel high solids hydrothermal processing technology in a small-scale biorefinery, annexed to a brewery. It focused on three scenarios for the production of: (A) the sugar replacement xylitol; (B) prebiotic xylo-oligosaccharide (XOS); and (C) co-production of xylitol and XOS. Economic assessment was conducted by comparing the capital and operating expenditure from process simulations created in Aspen Plus. The process models developed were supplemented with experimental data to improve accuracy.
    Internal rate of return (IRR) values obtained were greater than the hurdle rate of 9.7% for all scenarios when considering a conservative market price for xylitol and XOS as US$4500 t-1, yet dedicated production of XOS was economically more favourable with a minimum required selling price (MRSP) of US$2509 t-1 compared to US$4153 t-1 for xylitol. Additionally, the scenario for co-production of xylitol and XOS achieved the lowest MRSP of US$2182 t-1. By-products significantly contributed to 32.7%, 14.2% and 27.5% of the revenue generated in scenarios A, B and C, respectively.
    These results provide a good platform from which to develop the cost-effective commercial production of XOS and xylitol from BSG.

    Bedzo, O. K. K., van Rensburg, E. and Gorgens, J. F. (2021) Investigating the effect of different inulin-rich substrate preparations from Jerusalem artichoke (Helianthus tuberosus L.) tubers on efficient inulooligosaccharides production, Preparative Biochemistry and Biotechnology 51(5): 440-449


    Commercial production of inulooligosaccharides (IOS) relies largely on chicory roots. However, Jerusalem artichoke (JA) tubers provide a suitable alternative due to their high inulin content and low cultivation requirements. In this study, three inulin-rich substrate preparations from JA were investigated to maximize IOS production, namely powder from dried JA tuber slices (Substrate 1), solid residues after extracting protein from the JA powder (Substrate 2) and an inulin-rich fraction extracted from protein extraction residues (Substrate 3). The preferred temperature, pH and inulin substrate concentration were determined after which enzyme dosage and extraction time were optimized to maximize IOS extraction from the three substrates, using pure chicory inulin as benchmark. Under the optimal conditions, Substrate 3 resulted in the highest IOS yield of 82.3% (w/winulin). However, IOS production from the Substrate 1 proved more efficient since it renders the highest overall IOS yield (mass of IOS per mass of the starting biomass). In the case of co-production of protein and IOS from the JA tuber in a biorefinery concept, IOS production from the Substrate 2 is preferred since it reduces the inulin losses incurred during substrate preparation. For all the inulin-rich substrates studied, an enzyme dosage of 14.8 U/ginulin was found to be optimal at reaction time less than 6 h. JA tuber exhibited excellent potential for commercial production of IOS with improved yield and the possible advantage of a reduced biomass cost.

    Bedzo, O. K. K., Dreyer, C. B., van Rensburg, E., Gorgens, J. F. (2021) Optimisation of Pretreatment Catalyst , Enzyme Cocktail and Solid Loading for Improved Ethanol Production from Sweet Sorghum Bagasse, BioEnergy Research


    weet sorghum bagasse displays many characteristics rendering it a promising substrate for lignocellulosic ethanol production. In this study, the steam pretreatment catalyst, enzymatic hydrolysis and the substrate loading for the fermentation were investigated in order to maximise the production of ethanol from the feedstock. The results deemed water as a sufficient pretreatment catalyst since the SO2 impregnation of the biomass did not produce any significant beneficial effects on the yield of ethanol produced. The preferred pretreatment and enzymatic hydrolysis conditions were incorporated in a fed-batch simultaneous saccharification and fermentation (SSF) process using pressed-only (not washed) WIS at a final solid loading of 13% (w/w) that resulted in the targeted ethanol concentration of 39 g/L with a corresponding yield of 82% of the theoretical maximum. Yeast inhibition coupled with significant glucose accumulation was observed at higher solid loadings of 16% and 20%. Ultimately, the sweet sorghum bagasse could be integrated into existing ethanol production regimes to improve the global bioenergy production.

    Bedzo, O. K. K., Mandegari, M. and Gorgens, J. F. (2020) Techno-economic analysis of inulooligosaccharides, protein, and biofuel co-production from Jerusalem artichoke tubers: A biorefinery approach, Biofuels Bioproducts & Biorefining-Biofpr 14(4): 776-793


    Jerusalem artichoke (JA) is a crop with excellent potential for application in biorefineries. It can resist drought, pests, and diseases and can thrive well in marginal lands with little fertilizer application. The JA tubers contain considerable quantities of inulin, which is suitable for the production of inulooligosaccharides (IOS), as a high-value prebiotic, dietary fiber. In this study, five JA tuber biorefinery scenarios were simulated in Aspen Plus and further evaluated by techno-economic and sensitivity analyses. Production of IOS, proteins and animal feed was studied in scenarios A and C, applying various biorefinery configurations. Scenario B explored the option of producing only IOS and the sale of residues as animal feed. Scenarios D and E investigated the economic potential of biofuel generation from residues after IOS and protein production by generation of biogas and ethanol respectively, from residues. Based on the chosen economic indicators, scenario B resulted in the lowest minimum selling price (MSP) of 3.91 US$ kg-1 (market price 5.0 US$ kg-1) with correspondingly reduced total capital investment (TCI) and total operating cost (TOC) per mass unit produced of IOS of 18.91 and 2.59 US$ kg-1 respectively, compared with other studied scenarios. Considering the set production scale, it is more profitable when the residues are sold as animal feed instead of being converted into biofuel, due to the capital-intensive nature of the biofuel production processes. The coproduction of protein had a negative impact on the economics of the process as the associated capital and operating expenditure outweighed the associated revenue.

    Bedzo, O. K. K., Mandegari, M. and Gorgens, J. F. (2020) Comparison of immobilized and free enzyme systems in industrial production of short-chain fructooligosaccharides from sucrose using a techno-economic approach, Biofuels Bioproducts & Biorefining-Biofpr 14(4): 776-793


    Short-chain fructooligosaccharides (scFOS) are nutraceuticals with numerous applications in the food and pharmaceutical industries. The production of scFOS using immobilized biocatalysts offers some functional and technical advantages over free enzyme counterparts. To investigate the economic potential of the immobilized enzyme system relative to the free enzyme system, a techno-economic comparison was conducted on three methods of scFOS production (powder and syrup forms) at a capacity of 2000?t per annum (tpa) by enzymatic synthesis from sucrose: the free enzyme (FE), calcium alginate immobilized enzyme (CAIE), and amberlite IRA 900 immobilized enzyme (AIE) systems. These processes were simulated in Aspen Plus to obtain the mass and energy balances and to estimate the operating and capital costs, followed by economic evaluation and sensitivity analysis. Profitability analysis showed that all three systems are economically viable as their associated minimum selling prices (MSP) were well below the scFOS market price of 5 $ kg-1. However, the FE system was the most profitable with the lowest MSP of 2.61 $ kg-1 because the savings on cost as a result of enzyme immobilization could not offset the additional costs associated with immobilization. Sensitivity analysis demonstrated that total operating cost, fixed capital investment, and internal rate of return (% IRR) have the greatest effects on the MSP. Furthermore, the syrup form of scFOS production leads to 29% less MSP, compared to powder form. In addition, the studied plant capacities of 5000 and 1000?tpa showed 10% and 16% reductions on MSP respectively.

    Bedzo, O. K. K., Trollope, K., Gottumukkala, L. D., Coetzee, G., Gorgens, J. F. (2019) Amberlite IRA 900 Versus Calcium Alginate in Immobilization of a Novel , Engineered B-fructofuranosidase for Short-Chain Fructooligosaccharide Synthesis from Sucrose, Biotechnology Progress 35(3): 1-9


    The immobilization of B-fructofuranosidase for short-chain fructooligosaccharide (scFOS) synthesis holds the potential for a more efficient use of the biocatalyst. However, the choice of carrier and immobilization technique is a key to achieving that efficiency. In this study, calcium alginate (CA), Amberlite IRA 900 (AI900) and Dowex Marathon MSA (DMM) were tested as supports for immobilizing a novel engineered B-fructofuranosidase from Aspergillus japonicus for scFOS synthesis. Several immobilization parameters were estimated to ascertain the effectiveness of the carriers in immobilizing the enzyme. The performance of the immobilized biocatalysts are compared in terms of the yield of scFOS produced and reusability. The selection of carriers and reagents was motivated by the need to ensure safety of application in the production of food-grade products. The CA and AI900 both recorded impressive immobilization yields of 82 and 62%, respectively, while the DMM recorded 47%. Enzyme immobilizations on CA, AI900 and DMM showed activity recoveries of 23, 27, and 17%, respectively. The CA, AI900 immobilized and the free enzymes recorded their highest scFOS yields of 59, 53, and 61%, respectively. The AI900 immobilized enzyme produced a consistent scFOS yield and composition for 12 batch cycles but for the CA immobilized enzyme, only 6 batch cycles gave a consistent scFOS yield. In its first record of application in scFOS production, the AI900 anion exchange resin exhibited potential as an adequate carrier for industrial application with possible savings on cost of immobilization and reduced technical difficulty.

    Vodonik M, Vrabec K, Hellwig P, Benndrof D, Sezun M, Gregori A, Gottumukkala L.D, Andersen R.C, Reichel U (2018) Valorisation of deinking sludge as a substrate for lignocellulolytic enzymes production by Pleurotus ostreatus, Journal of Cleaner production 197(1): 253-263

    Disposal of waste sludges produced in large amounts in the pulp and paper industry imposes significant environmental and economical problems. One strategy to address these issues involves revalorization of paper mill sludges by their application as substrates for microbial production of biotechnologically relevant enzymes. The application of lignocellulolytic enzymes in paper, textile and bioenergy industries is encouraged in order to decrease chemicals and energy consumptions. In the following work, deinking sludge was assessed as a substrate for production of lignocellulases. Based on the results of growth and activity screenings, Pleurotus ostreatus PLAB was chosen as the most promising candidate among 30 tested strains and its secretome was further studied by quantitative enzyme assays and mass spectrometry. While endoglucanase and xylanase activities detected in P. ostreatus secretome produced on deinking sludge were similar to activities of cultures grown on other lignocellulosic substrates, average laccase activity was significantly higher (46?000 U/kg DIS). Mass spectrometry identification of the most prominent proteins in the secretome of the target strain confirmed that significant amounts of different lignin-modifying oxidases were produced on this substrate despite its low lignin content, indicating the presence of other inducible compounds. The findings of this study suggest deinking sludge may represent a good substrate for fungal production of the aforementioned enzymes with broad biotechnological applications, including bioremediation, paper and bioenergy industries.

    Gottumukkala L.D, Haigh K, Gorgens J (2017) Trends and advances in conversion of lignocellulosic biomass to biobutanol: microbes, bioprocesses and industrial viability, Renewable and Sustainable Energy Reviews 76: 963-973

    Biobutanol has gained attention as an alternative renewable transportation fuel for its superior fuel properties and widespread applications in chemical industry, primarily as a solvent. Conventional butanol fermentation has drawbacks that include strain degeneration, end-product toxicity, by-product formation, low butanol concentrations and high substrate cost. The complexity of Clostridium physiology and close control between sporulation phase and ABE fermentation has made it demanding to develop industrially potent strains. In addition to the isolation and engineering of superior butanol producing bacteria, the development of advanced cost-effective technologies for butanol production from feedstock like lignocellulosic biomass has become the primary research focus. High process costs associated with complex feedstocks, product toxicity and low product concentrations are few of the several bioprocess challenges involved in biobutanol production. The article aims to assess the challenges in lignocellulosic biomass to biobutanol conversion and identify key process improvements that can make biobutanol commercially viable.

    Gottumukka L.D, Haigh K, Collard F.X, Van Rensburg E, Gorgens J (2016) Opportunities and prospects of biorefinery-based valorisation of pulp and paper sludge, Bioresource technology 215: 37-49

    The paper and pulp industry is one of the major industries that generate large amount of solid waste with high moisture content. Numerous opportunities exist for valorisation of waste paper sludge, although this review focuses on primary sludge with high cellulose content. The most mature options for paper sludge valorisation are fermentation, anaerobic digestion and pyrolysis. In this review, biochemical and thermal processes are considered individually and also as integrated biorefinery. The objective of integrated biorefinery is to reduce or avoid paper sludge disposal by landfilling, water reclamation and value addition. Assessment of selected processes for biorefinery varies from a detailed analysis of a single process to high level optimisation and integration of the processes, which allow the initial assessment and comparison of technologies. This data can be used to provide key stakeholders with a roadmap of technologies that can generate economic benefits, and reduce carbon wastage and pollution load.

    Boshoff A, Gottumukka L.D, Van Rensburg E, Gorgens J (2016) Paper sludge (PS) to bioethanol: Evaluation of virgin and recycle mill sludge for low enzyme, high-solids fermentationl, Bioresource technology 23: 103-111

    Paper sludge (PS) from the paper and pulp industry consists primarily of cellulose and ash and has significant potential for ethanol production. Thirty-seven PS samples from 11 South African paper and pulp mills exhibited large variation in chemical composition and resulting ethanol production. Simultaneous saccharification and fermentation (SSF) of PS in fed-batch culture was investigated at high solid loadings and low enzyme dosages. Water holding capacity and viscosity of the PS influenced ethanol production at elevated solid loadings of PS. High viscosity of PS from virgin pulp mills restricted the solid loading to 18% (w/w) at an enzyme dosage of 20 FPU/gram dry PS (gdPS), whereas an optimal solid loading of 27% (w/w) was achieved with corrugated recycle mill PS at 11 FPU/gdPS. Ethanol concentration and yield of virgin pulp and corrugated recycle PS were 34.2 g/L at 66.9% and 45.5 g/L at 78.2%, respectively.

    Gottumukkala L.D. Gorgens J.F (2016) Biobutanol production from lignocellulosics, Biofuels Production and future perspectives, Singh R.S, Pandey A, Gnansounou E, Taylor & Francis group

    Next-generation biofuels from renewable sources have gained interest among research investigators, industrialists, and governments due to major concerns on the volatility of oil prices, climate change, and depletion of oil reserves. Biobutanol has drawn signicant attention as an alternative transportation fuel due to its superior fuel properties over ethanol. e advantages of butanol are its high energy content, better blending with gasoline, less hydroscopic nature, lower volatility, direct use in convention engines, low corrosiveness, etc. Butanol production through (acetone, butanol, and ethanol) ABE fermentation is a well-established process, but it has several drawbacks like feedstock cost, strain degeneration, product toxicity, and low product concentrations. Lignocellulosic biomass is considered as the most abundant, renewable, low-cost feedstock for biofuels. Production of butanol from lignocellulosic biomass is more complicated due to the recalcitrance of feedstock and inhibitors generated during the pretreatment and hydrolysis process. Advanced fermentation and product recovery techniques are being researched to make biobutanol industrially viable.

    Thomas L, Joseph A, Gottumukkala L.D. (2014) Xylanase and cellulase systems of Clostridium sp.: an insight on molecular approaches for strain improvement, Bioresource technology 158: 343-350

    Bioethanol and biobutanol hold great promise as alternative biofuels, especially for transport sector, because they can be produced from lignocellulosic agro-industrial residues. From techno-economic point of view, the bioprocess for biofuels production should involve minimal processing steps. Consolidated bioprocessing (CBP), which combines various processing steps such as pretreatment, hydrolysis and fermentation in a single bioreactor, could be of great relevance for the production of bioethanol and biobutanol or solvents (acetone, butanol, ethanol), employing clostridia. For CBP, Clostridium holds best promise because it possesses multi-enzyme system involving cellulosome and xylanosome, which comprise several enzymes such as cellulases and xylanases. The aim of this article was to review the recent developments on enzyme systems of clostridia, especially xylanase and cellulase with an effort to analyse the information available on molecular approaches for the improvement of strains with ultimate aim to improve the efficiencies of hydrolysis and fermentation.

    Gottumukkala L.D, Parameswaran B, Valappil S.K, Mathiyazhakan, K (2013) Biobutanol production from rice straw by a non acetone producing Clostridium sporogenes BE01, Bioresource technology 145: 182-187

    Biobutanol from lignocellulosic biomass has gained much attention due to several advantages over bioethanol. Though microbial production of butanol through ABE fermentation is an established technology, the use of lignocellulosic biomass as feedstock presents several challenges. In the present study, biobutanol production from enzymatic hydrolysate of acid pretreated rice straw was evaluated using Clostridium sporogenes BE01. This strain gave a butanol yield of 3.43 g/l and a total solvent yield of 5.32 g/l in rice straw hydrolysate supplemented with calcium carbonate and yeast extract. Hydrolysate was analyzed for the level of inhibitors such as acetic acid, formic acid and furfurals which affect the growth of the organism and in turn ABE fermentation. Methods for preconditioning the hydrolysate to remove toxic end products were done so as to improve the fermentation efficiency. Conditions of ABE fermentation were fine tuned resulting in an enhanced biobutanol reaching 5.52 g/l.

    Singhania R.R, Sukumaran R.K, Rajasree K.P, Mathew A, Gottumukkala L.D, Pandey A (2011) Properties of a major ?-glucosidase-BGL1 from Aspergillus niger NII-08121 expressed differentially in response to carbon sources, Process Biochemistry 46(7): 1521-1524

    Aspergillus niger NII-08121/MTCC 7956 exhibited differences in expression of ?-glucosidase (BGL) in response to carbon sources provided in the medium. Activity staining with methyl umbelliferyl ?-d-glucopyranoside (MUG) indicated that four different isoforms of BGL were expressed when A. niger was grown under submerged fermentation with either lactose or cellulose, whereas only two were expressed when wheat bran or rice straw was used as the carbon source. Among the four isoforms of BGL expressed during lactose supplementation, two were found to retain 92% and 82% activity respectively in presence of 250 mM glucose in the MUG assay. The major ?-glucosidase (BGL1) was purified to homogeneity by electro elution from a Native PAGE gel. The purified 120 kDa protein was active at 50 °C and was stable for 48 h without any loss of activity. The optimum pH and temperature were 4.8 and 70 °C respectively.

    Parameswaran, B, Raveendran S, Singhania, R.R, Surender V, L Devi, Nagalakshmi S, Kurien N, Sukumaran R.K, Pandey A. (2010) Bioethanol production from rice straw: an overview, Bioresource technology 101(13): 4767-4774

    Rice straw is an attractive lignocellulosic material for bioethanol production since it is one of the most abundant renewable resources. It has several characteristics, such as high cellulose and hemicelluloses content that can be readily hydrolyzed into fermentable sugars. But there occur several challenges and limitations in the process of converting rice straw to ethanol. The presence of high ash and silica content in rice straw makes it an inferior feedstock for ethanol production. One of the major challenges in developing technology for bioethanol production from rice straw is selection of an appropriate pretreatment technique. The choice of pretreatment methods plays an important role to increase the efficiency of enzymatic saccharification thereby making the whole process economically viable. The present review discusses the available technologies for bioethanol production using rice straw.

    Aswathy U.S, Sukumaran R.K, Devi G.L, Rajasree K.P, Singhania R.R. (2010) Bio-ethanol from water hyacinth biomass: an evaluation of enzymatic saccharification strategy, Bioresource technology 101(3): 925-930

    Biomass feedstock having less competition with food crops are desirable for bio-ethanol production and such resources may not be localized geographically. A distributed production strategy is therefore more suitable for feedstock like water hyacinth with a decentralized availability. In this study, we have demonstrated the suitability of this feedstock for production of fermentable sugars using cellulases produced on site. Testing of acid and alkali pretreatment methods indicated that alkali pretreatment was more efficient in making the sample susceptible to enzyme hydrolysis. Cellulase and ?-glucosidase loading and the effect of surfactants were studied and optimized to improve saccharification. Redesigning of enzyme blends resulted in an improvement of saccharification from 57% to 71%. A crude trial on fermentation of the enzymatic hydrolysate using the common baker’s yeast Saccharomyces cerevisiae yielded an ethanol concentration of 4.4 g/L.