How recombinant swollenin from Kluyveromyces lactisaffects cellulosicsubstrates and accelerates their hydrolysis
- Gernot Jäger†1,
- Michele Girfoglio†2,
- Florian Dollo1,
- Roberto Rinaldi3,
- Hans Bongard3,
- Ulrich Commandeur2,
- Rainer Fischer2, 4,
- Antje C Spiess5 and
- Jochen Büchs1Email author
© Jäger et al; licensee BioMed Central Ltd. 2011
Received: 7 July 2011
Accepted: 23 September 2011
Published: 23 September 2011
In order to generate biofuels, insoluble cellulosic substrates are pretreated andsubsequently hydrolyzed with cellulases. One way to pretreat cellulose in a safeand environmentally friendly manner is to apply, under mild conditions,non-hydrolyzing proteins such as swollenin - naturally produced in low yields bythe fungus Trichoderma reesei. To yield sufficient swollenin forindustrial applications, the first aim of this study is to present a new way ofproducing recombinant swollenin. The main objective is to show how swolleninquantitatively affects relevant physical properties of cellulosic substrates andhow it affects subsequent hydrolysis.
After expression in the yeast Kluyveromyces lactis, the resultingswollenin was purified. The adsorption parameters of the recombinant swolleninonto cellulose were quantified for the first time and were comparable to those ofindividual cellulases from T. reesei. Four different insoluble cellulosicsubstrates were then pretreated with swollenin. At first, it could bequalitatively shown by macroscopic evaluation and microscopy that swollenin causeddeagglomeration of bigger cellulose agglomerates as well as dispersion ofcellulose microfibrils (amorphogenesis). Afterwards, the effects of swollenin oncellulose particle size, maximum cellulase adsorption and cellulose crystallinitywere quantified. The pretreatment with swollenin resulted in a significantdecrease in particle size of the cellulosic substrates as well as in theircrystallinity, thereby substantially increasing maximum cellulase adsorption ontothese substrates. Subsequently, the pretreated cellulosic substrates werehydrolyzed with cellulases. Here, pretreatment of cellulosic substrates withswollenin, even in non-saturating concentrations, significantly accelerated thehydrolysis. By correlating particle size and crystallinity of the cellulosicsubstrates with initial hydrolysis rates, it could be shown that theswollenin-induced reduction in particle size and crystallinity resulted in highcellulose hydrolysis rates.
Recombinant swollenin can be easily produced with the robust yeast K.lactis. Moreover, swollenin induces deagglomeration of celluloseagglomerates as well as amorphogenesis (decrystallization). For the first time,this study quantifies and elucidates in detail how swollenin affects differentcellulosic substrates and their hydrolysis.
Naturally occurring lignocellulose is a promising starting material for the sustainableproduction of platform chemicals and fuels [1–6]. The hydrolysis of its main component cellulose to glucose necessitates acellulase system consisting of cellobiohydrolase (CBH, E.C. 126.96.36.199), endoglucanase(EG, E.C. 188.8.131.52) and β-glucosidase (E.C. 184.108.40.206) [7–9]. Besides enzyme-related factors (for example, enzyme inactivation and productinhibition) , the enzymatic hydrolysis of cellulose is limited by its physical properties [11–14]. These properties, in particular, are the degree of polymerization,accessibility and crystallinity [15–18]. Cellulose accessibility, which is determined by cellulose particle size(external surface area) and porosity (internal surface area) [15, 19], is the most important factor for hydrolysis [15, 18, 20–24]. This accessibility reflects the total surface area available for directphysical contact between cellulase and cellulose and, therefore, influences cellulaseadsorption as well as the rate and extent of cellulose hydrolysis [21, 25]. Furthermore, crystallinity is a relevant factor for cellulose hydrolysis,since it influences the reactivity of adsorbed cellulases . Here, it should be noted that crystallinity may also affect cellulaseadsorption [26, 27] and, therefore, cellulose accessibility [15, 21, 28]. Up to now, the relationship between crystallinity and accessibility has notbeen clearly understood [15, 29]. However, for high cellulose hydrolysis rates and yields, celluloseaccessibility needs to be increased and, conversely, its crystallinity reduced [30, 31]. To achieve this and accordingly improve subsequent hydrolysis, pretreatmenttechniques are essential [6, 14, 16, 32].
Since pretreatment can be expensive, there is a prime motivation to screen and improveit [33–37]. Over time, many pretreatment technologies have been developed: physical (forexample, milling or grinding), physicochemical (for example, steam explosion or ammoniafiber explosion), chemical (for example, acid or alkaline hydrolysis, organic solventsor ionic liquids), biological or electrical methods, or combinations of these methods [33, 35]. Some of these techniques entail expensive equipment, harsh conditions andhigh energy input . By contrast, in the past years, non-hydrolyzing proteins have beeninvestigated that pretreat cellulose under mild conditions [17, 20]. After regular lignocellulose pretreatment, these non-hydrolyzing proteinscan be added during cellulose hydrolysis  or they can be utilized in a second pretreatment step in which cellulose isthe substrate .
During this second pretreatment step, cellulose is incubated under mild conditions withnon-hydrolyzing proteins that bind to the cellulose. As a result, cellulose microfibrils(diameter around 10 nm [39, 40]) are dispersed and the thicker cellulose macrofibrils or fibers (diameteraround 0.5 to 10 μm, consisting of microfibrils [39–41]) swell, thereby decreasing crystallinity and increasing accessibility [20, 42–44]. This phenomenon was named amorphogenesis [20, 42]. Furthermore, cellulose-binding proteins can lead to deagglomeration ofcellulose agglomerates (diameter > 0.1 mm, consisting of cellulose fibers) [45, 46], thereby separating cellulose fibers from each other and additionallyincreasing cellulose accessibility. Ultimately, amorphogenesis as well asdeagglomeration promote cellulose hydrolysis .
Various authors have described hydrolysis-promoting effects when pretreating cellulosewith single cellulose-binding domains , expansins from plants [38, 47–49] or expansin-related proteins from Trichoderma reesei , Bacillus subtilis , Bjerkandera adusta  or Aspergillus fumigatus . A prominent expansin-related protein is swollenin from the fungus T.reesei. In contrast to cellulases, the expression levels of swollenin in T.reesei are relatively low (1 mg/L) . Thus, swollenin from T. reesei has been heterologously expressed inSaccharomyces cerevisiae , Aspergillus niger  and Aspergillus oryzae . The expression levels in S. cerevisiae, however, are also low (25μg/L)  and only A. oryzae produces swollenin in higher concentrations (50mg/L) . According to Saloheimo et al. , swollenin can disrupt the structure of cotton fiber or the cell wall of thealgae Valonia macrophysa. Since swollenin shows a high sequence similarity toplant expansins , it may have a similar function and lead to the disruption of cellulosicnetworks within plant cell walls . Thus, swollenin may have an important role in the enzymatic degradation oflignocellulose by T. reesei . Up to now, however, there is no systematic and quantitative analysis of theeffects of swollenin on cellulosic substrates and their hydrolysis.
First, this study presents an alternative way of producing recombinant swollenin inorder to generate sufficient swollenin for industrial applications. Second, the mainobjective is to show how recombinant swollenin quantitatively affects relevant physicalproperties of cellulosic substrates and how it affects their subsequent hydrolysis.
Results and discussion
Production and analysis of recombinant swollenin
To clearly identify the protein band at about 80 kDa (Figure 1Aand 1B), its amino acid sequence was determined by using massspectrometry  and the Mascot search engine . Figure 1C shows the results of mass spectrometryand the expected amino acid sequence of the recombinant swollenin. As shown by a highMascot score of 502 (Figure 1C), the protein at 80 kDa wasclearly identified to be a variant of swollenin from T. reesei. Regardingthe native swollenin sequence, a protein score of greater than 57 (homologythreshold) indicates identity or extensive homology (P < 0.05). Inaddition, potential N- and O-glycosylation sites were detected by using the NetNGlyc1.0 and NetOGlyc 3.1 servers  (Figure 1C). Here, it should be noted that thenative swollenin contains almost no N-glycosylation . Therefore, the difference between the calculated molecular mass of 49kDa, based on the primary sequence of swollenin, and the observed molecular mass of80 kDa (Figure 1A and 1B) may beexplained by O-glycosylation and other post-translational modifications. Proofs aregiven as follows: (i) the linker region of cellulases or cellulase-related proteinsis highly O-glycosylated ; (ii) swollenin contains potential O-glycosylation sites within the linkerregion (Figure 1C); (iii) no peptides of the linker region wereidentified by mass spectrometry, since glycosylation alters the mass/charge ratio ofthe peptides (Figure 1C).
Adsorption of swollenin
Pretreatment of filter paper with swollenin
The non-hydrolytic deagglomeration or amorphogenesis of cellulose was also describedfor single cellulose-binding domains of cellulases [17, 45, 67] and for other expansin-related proteins from B. subtilis , A. fumigatus  or B. adusta . However, there is no detailed and quantitative analysis of differentcellulosic substrates after pretreatment with non-hydrolyzing proteins, especiallywith regard to swollenin.
Effect of swollenin pretreatment on the physical properties of cellulosicsubstrates
To analyze in detail the effect of recombinant swollenin on cellulose, differentcellulosic substrates were pretreated with buffer, BSA or recombinant swollenin.After pretreatment and removal of bound proteins, the physical properties of thepretreated cellulosic substrates were analyzed by laser diffraction, cellulaseadsorption studies and crystallinity measurements.
Maximum cellulase adsorption onto cellulosic substrates after pretreatment withswollenin.
Pretreatment with buffer
Pretreatment with swollenin
A max (cellulase) (mg/g)
A max (cellulase) (mg/g)
Whatman filter paper No.1
Hydrolysis of cellulosic substrates pretreated with swollenin
Recombinant swollenin was easily produced with the yeast K. lactis and purifiedby affinity chromatography. Additionally, the adsorption of swollenin onto cellulose wasquantified for the first time, and its adsorption parameters were comparable to those ofindividual cellulases. The pretreatment with swollenin caused a significant decrease inparticle size as well as in crystallinity of the cellulosic substrates, therebysubstantially increasing maximum cellulase adsorption. Moreover, pretreatment of thecellulosic substrates with swollenin - even in non-saturating concentrations -significantly accelerated the hydrolysis. By correlating particle size and crystallinitywith initial hydrolysis rates, it could be shown that high initial hydrolysis ratesresulted from the swollenin-induced reduction in particle size and crystallinity.Consequently, this study shows an efficient means to produce recombinant swollenin withthe robust yeast K. lactis. Moreover, this study shows that swollenin inducesdeagglomeration of cellulose agglomerates as well as amorphogenesis (decrystallization).For the first time, this study quantifies and elucidates in detail how swollenin affectscellulosic substrates and their hydrolysis.
A pretreatment of cellulosic substrates has been presented here which is simply based onthe incubation of recombinant swollenin under mild conditions. Since the enzymatichydrolysis of cellulose is a rate-limiting processing step in biorefineries , this pretreatment could significantly improve hydrolysis rates. To excludepossible side effects between swollenin and cellulase, swollenin pretreatment wasperformed as a separate step within this study. In future studies, swollenin should bedirectly added during cellulose hydrolysis. Since standard assays are missing fordeagglomeration, amorphogenesis and for the comparison of different non-hydrolyzingproteins, this study may serve as an initial means to establish such assays.
Cellulosic substrates and cellulases
The cellulosic substrates Whatman filter paper No.1, α-cellulose, Avicel PH101and Sigmacell 101 were purchased from Sigma-Aldrich (MO, USA). Physical propertiesand product information have been summarized by various authors [10, 64]. Agglomerates of Whatman filter paper No.1 were prepared by using ahole-punch and quartering the resulting filter paper discs. The final filter paperagglomerates had an average diameter of approximately 3 mm. The cellulase preparationCelluclast® 1.5 L (Novozymes, Bagsværd, DK) - a filtratedculture supernatant of T. reesei  - was used for the hydrolysis of the pretreated cellulosic substrates.According to various authors, Celluclast® contains CBHs (Cel7A andCel6A), EGs (for example, Cel7B and Cel5A) as well as β-glucosidases [81, 82]. To remove salts, sugars and other interfering components,Celluclast® was previously rebuffered with an Äkta FPLC (GEHealthcare, Little Chalfont, UK). Celluclast® was loaded on SephadexG-25 Fine (2.6 cm × 10 cm, GE Healthcare), and 0.05 M sodium acetate (pH 4.8)was used as a running buffer at 110 cm/h. Sephadex G-25 Fine exhibits an exclusionlimit of 1-5 kDa which is comparable to the molecular mass cut-off of dialysismembranes for protein desalting. Since cellulases have a molecular mass of > 25 kDa [62, 83, 84], the mixture of cellulases was not changed during rebuffering.Chromatography was conducted at room temperature, and the automatically collectedfractions were directly cooled at 4°C. To determine specific filter paperactivities, different dilutions of Celluclast® and the rebufferedCelluclast® - applied for all hydrolysis experiments - were testedaccording to Ghose . Here, the following specific filter paper activities (per g protein) weremeasured: 201 U/g (Celluclast®) and 279 U/g (rebufferedCelluclast®).
Genetic engineering for recombinant swollenin
The below-mentioned cloning procedure was designed for secreted protein expressionaccording to the K. lactis Protein Expression Kit (New England Biolabs, MA,USA). The cDNA of the swollenin-coding region was synthesized byreverse-transcription PCR using mRNA isolated from T. reesei QM9414 (swo1gene [GenBank: AJ245918], protein sequence [GenBank: CAB92328]) and reverse transcriptase (M-MLV,Promega, WI, USA) according to the manufacturer's protocol. Specific primers wereapplied to synthesize a cDNA starting from the 19th codon of theswollenin-coding region and, therefore, missing the secretion signal sequence ofT. reesei . By using the aforementioned primers, SalI and SpeI restriction sites wereadded upstream and downstream of the swollenin-coding region, respectively. Theamplified cDNA was cloned into the pCR2.1-TOPO vector (Invitrogen, CA, USA) accordingto the manufacturer's protocol. After DNA sequencing and isolation of a correctclone, the DNA was excised from pCR2.1-TOPO and cloned into the pKLAC1-H vector usingXhoI and SpeI restriction enzymes (New England Biolabs, MA, USA) according to themanufacturer's protocol. The pKLAC1-H is a modified version of the integrative pKLAC1vector (New England Biolabs; [GenBank: AY968582]). The pKLAC1 - developed by Colussi andTaron  - exhibits the α-mating factor signal sequence and can be used forthe expression and secretion of recombinant proteins in K. lactis . The pKLAC1-H was constructed by including an additional SpeI restrictionsite directly followed by a His-tag coding sequence (6xHis) between the XhoI andAvrII restriction sites of pKLAC1. The DNA sequence of the final pKLAC1-H construct(containing the DNA coding for recombinant swollenin) is shown in Additional file1. Moreover, the final amino acid sequence ofrecombinant swollenin (without the α-mating factor signal sequence) is given inFigure 1C.
Expression and purification of recombinant swollenin
All below-mentioned transformation, selection and precultivation procedures -developed by Colussi and Taron  - were performed according to the manufacturer's protocol (K. lactis Protein Expression Kit, New England Biolabs). After cloning, K. lactis GG799 cells were transformed with pKLAC1-H (containing the DNA coding forrecombinant swollenin), and transformed clones were selected (acetamide selection).One clone was precultivated in YPGal (yeast extract, peptone and galactose) medium,consisting of 20 g/L galactose, 20 g/L peptone and 10 g/L yeast extract - all mediacomponents were purchased from Carl Roth (Karlsruhe, Germany). After inoculation with2.5 mL of the preculture, the main culture was cultivated in triplicates in 2 LErlenmeyer flasks with YPGal medium under the following constant conditions:temperature T = 30°C, total filling volume V L = 250mL, shaking diameter d 0 = 50 mm, shaking frequency n =200 rpm. Additionally, a non-transformed K. lactis wild type was cultivatedas a reference. After incubation for 72 h, the main cultures were centrifuged (6000g, 20 min, 4°C), and the pooled supernatants of the triplicates were treatedwith endoglycosidase Hf by using 20 U per μg protein for 12 h  according to the manufacturer's protocol without denaturation (New EnglandBiolabs). Afterwards, the protein solution was concentrated 100-fold at 4°Cusing a Vivacell 100 ultrafiltration system with a molecular mass cut-off of 10 kDa(Sartorius Stedim Biotech, Göttingen, Germany). For affinity chromatography, therecombinant swollenin was previously rebuffered using Sephadex G-25 Fine (2.6 cm× 10 cm, GE Healthcare) at 110 cm/h with a running buffer (pH 7.4) consisting of0.05 M sodium dihydrogen phosphate, 0.3 M sodium chloride and 0.01 M imidazole. Therebuffered sample was loaded on Ni Sepharose 6 Fast Flow (1.6 cm × 10 cm; GEHealthcare) at 120 cm/h. The bound swollenin was eluted with the aforementionedrunning buffer, containing 0.25 M imidazole.
SDS-PAGE and Western blot analysis
SDS-PAGE and Western blot analysis were applied to analyze the purity and to identifythe recombinant swollenin. Novex 12% polyacrylamide Tris-Glycine gels (Invitrogen),and samples were prepared according to the manufacturer's protocol. The PlusPrestained Protein Ladder (Fermentas, Burlington, CA, USA) was used as a molecularmass marker. Finally, the proteins were stained with Coomassie Brilliant Blue andanalyzed densitometrically  using the scanner Perfection V700 (Epson, Suwa, Japan). The molecular massand purity of swollenin was determined using the software TotalLab TL100 (NonlinearDynamics, Newcastle, UK). For Western blot analysis, gels were blotted onto anitrocellulose membrane (Whatman, Springfield Mill, UK) according to themanufacturer's protocol (Invitrogen). The membranes were blocked at room temperaturewith 50 g/L skim milk dissolved in phosphate buffered saline containing 0.5 g/LTween-20 (PBST) for 30 min. To detect the recombinant swollenin, the membranes wereincubated at room temperature for 1.5 h with a rabbit polyclonal antibody againstHis-tag (Dianova, Hamburg, Germany) diluted 1:10,000 in PBST. After the membrane waswashed thrice with PBST, it was incubated with alkaline phosphatase conjugated goatanti-rabbit IgG (Dianova) diluted 1:5,000 in PBST at room temperature for 1 h.Finally, bound antibodies were visualized by incubating the membrane for 5 min withnitro blue tetrazolium/5-Bromo-4-chloro-3-indolyl phosphate (NBT/BCIP) diluted 1:100in phosphatase buffer (100 mM Tris-HCl, 100 mM NaCl, 5 mM MgCl2, pH9.6).
Measurement of protein concentration
Protein concentrations were analyzed with the bicinchoninic acid assay  using the BCA Protein Assay Kit (Thermo Fisher Scientific, MA, USA) andBSA as a standard. Depending on the protein concentration of the samples, thestandard procedure (working range: 0.02 to 2 g/L) or the enhanced procedure (workingrange: 0.005 to 0.25 g/L) was performed according to the manufacturer's protocol. Theabsorbance at 562 nm was measured with a Synergy 4 microtiter plate reader (BioTekInstruments, VT, USA). To quantify swollenin in the culture supernatant of K.lactis, the bicinchoninic acid assay was combined with the aforementionedSDS-PAGE (including densitometric analysis). Here, total protein concentrations weredetermined and multiplied with the ratio of swollenin to total protein (purity).
Mass spectrometry and glycosylation analysis
Mass spectrometry was applied to identify the expressed and purified recombinantswollenin. The protein band (approximately 80 kDa) was excised from theSDS-polyacrylamide gel, washed in water, reduced with dithiothreitol, alkylated withiodoacetamide, and digested with trypsin . Peptide analysis was carried out using a nanoHPLC (Dionex, Germering,Germany) coupled to an ESI-QUAD-TOF-2 mass spectrometer (Waters Micromass, Eschborn,Germany) as previously described . The Mascot algorithm (Matrix Science, London, UK) was used to correlatethe mass spectrometry data with amino acid sequences in the Swissprot database.Thereby, the sequences of the analyzed peptides could be identified, and, ultimately,protein matches could be determined. The Mascot score is derived from the ions scoresof the detected peptides matching the peptides in the database and reflects anon-probabilistic basis for ranking protein hits . By using this database, the peptide mass tolerance was set at ± 0.3Da. Additionally, the following modifications to the amino acids in brackets wereallowed: carbamidomethyl (C), carboxymethyl (C), oxidation (M), propionamide (C).Moreover, potential areas for N-glycosylation and O-glycosylation were identified byusing the NetNGlyc 1.0 and NetOGlyc 3.1 servershttp://www.cbs.dtu.dk/services/.
in which A denotes the amount of adsorbed protein per g cellulose(μmol/g), A max , the maximum protein adsorption per gcellulose at equilibrium (μmol/g), E, the free protein concentration(μmol/L), and K D , the dissociation constant (μmol/L).Within the literature , the association constant K A (L/μmol) issometimes used instead of the dissociation constant K D .
To analyze the effect of swollenin pretreatment (see below) on cellulase adsorption [44, 93], the maximum cellulase adsorption was also determined by incubatingvarious concentrations (0.7 to 2.5 g/L) of rebuffered Celluclast® with 10 g/L pretreated cellulosic substrates. Here, all incubations wereconducted under the aforementioned conditions for 1 h, 1.5 h and 2 h.
Pretreatment with swollenin
Pretreatment experiments were performed with 20 g/L cellulosic substrates and variousconcentrations of swollenin in 0.05 M sodium acetate buffer (pH 4.8). The mixtureswere incubated as triplicates in 2 mL Eppendorf tubes on a thermomixer under thefollowing constant conditions: T = 45°C, V L = 1 mL,d 0 = 3 mm, n = 1000 rpm. To exclude a solemechanical effect on cellulosic substrates due to shaking and to verify a specificeffect of swollenin, blanks without swollenin (buffer) or with 0.4 g/L BSA instead ofswollenin were incubated similarly. To detect a possible hydrolytic activity ofrecombinant swollenin, the sensitive p-hydroxy benzoic acid hydrazide assay  was applied by using glucose as a standard. After incubation for 48 h, thesupernatants of the pretreatment solution were analyzed and the absorbancies weremeasured at 410 nm in a Synergy 4 microtiter plate reader. Subsequently, allcellulosic samples were washed to remove adsorbed proteins. Therefore, the mixtureswere centrifuged (14,000 × g, 10 min, 4°C), and the cellulosicpellets were washed four times with 800 μL 0.05 M citrate buffer (pH 10) , and once with 800 μL distilled water. Finally, the triplicates werepooled. According to Zhu et al. , citrate buffer (pH 10) is an appropriate washing solution, and a singlewashing step with 0.05 M citrate buffer (pH 10) leads to a desorption efficiency of61% in case of fungal cellulases and Avicel. Since no acids or bases are formedduring the washing procedure, the weak buffer capacity of citrate buffer at pH 10 canbe neglected. In this study, the washing procedure was conducted four times to ensurea high desorption of swollenin. The measurements of protein concentration in thewashing supernatants - by applying the aforementioned bicinchoninic acid assay(working range starting from 0.005 g/L) - showed that swollenin desorbed almostcompletely. Already after three washing steps, a total swollenin desorptionefficiency of > 90% was achieved.
Photography and microscopy
Photography and microscopy were applied to visualize the effect of swolleninpretreatment on filter paper. After pretreatment with buffer, BSA or swollenin, thedifferent filter paper solutions were transferred into petri dishes, the particleswere evenly distributed and images were taken with an Exilim EX-FH100 camera (Casio,Tokyo, Japan). Afterwards, the number of filter paper agglomerates (> 0.5 mm) wasdetermined by image analysis using the software UTHSCSA ImageTool 3.0 (freeware) anda ruler as a reference. Light microscopic pictures were taken with an Eclipse E600(Nikon, Tokyo, Japan). Additionally, scanning electron microscopy was performed usinga Hitachi S-5500 (Hitachi, Tokyo, Japan) and a field emission of 5 kV. All washedfilter paper samples were covered with a layer of carbon (3 nm) and, subsequently,with a layer of PtPd (3 nm, 80% to 20%). The images were taken by using secondaryelectrons.
Laser diffraction and X-ray diffraction
where I 002 is the maximum intensity of the crystalline plane(002) reflection (2θ = 22.5°) and I AM is theintensity of the scattering for the amorphous component at about 18° incellulose-I . Here, it should be noted that there are several methods for calculatingCrI from XRD data and these methods can provide significantly differentresults [28, 70]. Although the applied peak height method produces CrI values thatare higher than those of other methods, it is still the most commonly used method andranks CrI values in the same order as the other methods .
Hydrolysis experiments and dinitrosalicylic acid assay
Hydrolysis experiments with 10 g/L pretreated cellulosic substrate and 1 g/Lrebuffered Celluclast® were conducted in 0.05 M sodium acetate buffer(pH 4.8). The mixtures were incubated as triplicates in 2 mL Eppendorf tubes on athermomixer under the following constant conditions: T = 45°C, totalfilling V L = 1 mL, d 0 = 3 mm, n =1000 rpm. In general, attention has to be paid to cellulase inactivation, which wouldreduce the final yield of cellulose hydrolysis . In this current study, however, a shaken system with relatively low shearforces was applied. According to Engel et al. , rebuffered Celluclast® is stable under the appliedincubation conditions, so that cellulase inactivation could be neglected. The shakingfrequency was chosen to ensure the complete suspension of cellulose particles [64, 91]. Thus, mass transfer limitations are excluded, and the whole celluloseparticle surface becomes accessible to the cellulases, thereby optimizing cellulaseadsorption and activity . Three different blanks were incubated similarly: (i) without cellulase,(ii) without substrate, or (iii) without substrate and without cellulase. Thedinitrosalicylic acid assay  was applied to quantify the reducing sugars released during hydrolysis byusing glucose as a standard. After defined time intervals, samples were taken, andthe hydrolysis was stopped (10 min, 100°C). According to Wood and Bhat , low reducing sugar concentrations were quantified by adding 1.25 g/Lglucose to the samples. The absorbancies were measured at 540 nm in a Synergy 4microtiter plate reader. Since the dinitrosalicylic acid assay exhibits a lowersensitivity towards cellobiose than glucose, reducing sugar concentrations may beunderestimated when glucose is used as a standard and β-glucosidase is not inexcess . However, under the applied hydrolysis conditions, cellobiose did notaccumulate (the highest cellobiose to glucose ratio was measured in the case ofSigmacell after 10 h at 0.12) and, therefore, this underestimation was minimal andthe addition of β-glucosidase was not needed. Initial hydrolysis rates (g/(L*h))were calculated by applying a linear fit to the reducing sugar concentration datafrom 0 to 6 h.
in which a, b, c, d, e, f and g denote the various fittingparameters of the non-linear Gaussian cumulative function (-).
List of abbreviations
- a :
non-linear Gaussian cumulative function parameter (-)
- A :
adsorbedprotein per g cellulose (μmol/g)
- A max :
maximum proteinadsorption per g cellulose at equilibrium (μmol/g or mg/g)
- b :
non-linearGaussian cumulative function parameter (-)
bovine serum albumin
- c :
non-linear Gaussian cumulative function parameter (-)
- CrI :
crystallinity index (%)
- d :
non-linear Gaussian cumulativefunction parameter (-)
- d 0 :
shaking diameter (mm)
- e :
non-linear Gaussian cumulative function parameter (-)
- E :
free proteinconcentration (μmol/L)
- f :
non-linear Gaussiancumulative function parameter (-)
- g :
non-linear Gaussian cumulative functionparameter (-)
- I 002 :
maximum intensity of the crystalline plane(002) reflection (1/s)
- I AM :
XRD scattering for the amorphouscomponent at 18o in cellulose-I (1/s)
- K A :
associationconstant (L/μmol) K D : dissociation constant (μmol/L)
- λ :
- n :
shaking frequency (rpm)
nitro blue tetrazolium/5-Bromo-4-chloro-3-indolyl phosphate
- P :
probability forsignificant scores (protein matching) (-)
phosphate buffered saline containingTween-20
- R 2 :
coefficient of determination (-)
- T :
- θ :
diffraction angle (°)
- V L :
filling volume (mL)
mediumcontaining yeast extract, peptone and galactose.
This work was performed as part of the Cluster of Excellence "Tailor-Made Fuels fromBiomass", which is funded by the Excellence Initiative by the German federal andstate governments to promote science and research at German universities.
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