Characterization and immobilization of liposome-bound cellulase for hydrolysis of insoluble cellulose.

The liposome-bound cellulase was prepared by covalently coupling cellulase with the enzyme-free liposomes bearing aldehyde groups so that cellulase was located solely on the outer membrane of liposomes. The modified cellulase possessed the higher activity efficiency and lipid-based specific activity than the cellulase-containing liposomes reported previously. The enzyme-free liposomes bearing aldehyde groups were covalently immobilized with the chitosan gel beads and the free cellulase was coupled with the treated gel beads to prepare the immobilized liposome-bound cellulase. The activity efficiency of the immobilized liposome-bound cellulase was much higher than that of the conventionally immobilized cellulase. The results on reusability of the immobilized liposome-bound cellulase in the hydrolysis of either soluble or insoluble cellulose showed that the immobilized liposome-bound cellulase had the higher remaining cellulase activity and reusability than the conventionally immobilized cellulase for the hydrolysis of either type of cellulose. The liposomal membrane was suggested to be efficient in maintaining the cellulase activity during the hydrolysis.

Glucose oxidation catalyzed by liposomal glucose oxidase in the presence of catalase-containing liposomes.

A catalase-containing liposome (CAL) was prepared and characterized in terms of stability during storage and catalysis of the decomposition of hydrogen peroxide (H2O2) that was initially added or produced in the oxidation of glucose catalyzed by the glucose oxidase-containing liposomes (GOL). The reactors used were a test tube and an external loop airlift bubble column as the static liquid and circulating liquid flow systems, respectively. The free catalase (CA) at low concentrations was unstable during storage at 4 degrees C as a result of dissociation of the tetrameric CA subunits. On the other hand, the deactivation of the CA activity in the CAL was depressed because of the high CA concentration in the CAL liposome. The CAL effectively catalyzed the repeated decompositions at 25 degrees C with 10 mM H2O2 added initially, whereas the free CA was significantly deactivated during the repeated reactions. The high stability of the CAL was attributed to the moderately depressed reactivity, which was essentially derived from the diffusion limitation of the CAL membrane to H2O2 in the liquid bulk. In the GOL-catalyzed prolonged oxidation of 10 mM glucose at 40 degrees C in the static liquid in a test tube, both the free CA and CAL could continuously catalyze the decomposition of H2O2 produced. This was because the glucose oxidation rate was small due to the limited reactivity of the GOL to glucose with its low permeability through the GOL membrane. In the glucose oxidation catalyzed by the GOL with the free CA or the CAL in the airlift, much larger oxidation rates were observed compared to those in the test tube because the permeability of the GOL membrane to glucose was increased in the gas-liquid two phase flow in the airlift. The GOL/CAL system in the airlift operated in an acidic condition, which was preferable to the GO activity, gave the largest oxidation rate with negligible accumulation of the H2O2 produced. On the other hand, the GOL/free CA system gave an oxidation rate smaller than that of the GOL/CAL system even under the acidic condition due to an unfavorable interaction of the free CA molecules with the GOL membranes leading to the decreased reactivity of the GOL.

Optimal preparation of immobilized liposome-bound cellulase for hydrolysis of insoluble cellulose in an external loop airlift bioreactor.

Immobilized liposome-bound cellulase (ILC) was optimally prepared for the ILC-catalyzed hydrolysis of insoluble cellulose in an external loop airlift bioreactor. The liposomes with mean diameters of 200, 100, and 50 nm were used to prepare three kinds of ILCs, i.e., ILC(200), ILC(100) and ILC(50), respectively. The activity and stability of ILC(100) were examined with soluble cellulose (CMC) in addition to the insoluble substrate of cellulose powder (CC31) in a shaking flask as well as the airlift bioreactors. The experiments were carried out with 45 degrees C and pH 4.8 being found to be optimal for the activity. The activity of ILC(100) was stable in either airlift or shaking flask bioreactor during the five times repeated hydrolyses of CC31 corresponding to a total reaction time of 240 h. This confirmed that the cellulase molecules were covalently bonded to the liposomes covalently bound to the chitosan gel beads. Nevertheless, the activity of ILC(100) with CMC steadily decreased throughout the repeated reactions, suggesting an adverse effect of CMC on the ILC(100) activity. Among the three ILCs, ILC(50) was found to be the most stable and productive biocatalyst during the repeated hydrolyses of insoluble CC31 in the airlift bioreactor. More than 70% of the initial activity of ILC(50) was retained even after the six times repeated reactions for 288 h. Conversely, the ILC(200) was found to be the most unstable catalyst. Such a difference in stability among these ILCs was suggested to be caused by the difference in physical stability of their liposome membranes to the liquid shear stress due to the rising bubbles and circulating liquid as well as that in the amount of the cellulase molecules unstably incorporated in the membranes. ILC(50) was thus shown to have the most potential for an efficient hydrolysis of insoluble cellulose in a practical airlift bioreactor.

Enhancement of enzyme activity and enantioselectivity by cyclopentyl methyl ether in the transesterification catalyzed by Pseudomonas cepacia lipase co-lyophilized with cyclodextrins.

The solvent effects of cyclopentyl methyl ether (CPME) on the reaction rates and enzyme enantioselectivity in the enantioselective transesterifications of racemic 6-methyl-5-hepten-2-ol (racemic sulcatol: SUL) and racemic 2,2-dimethyl-1,3-dioxolane-4-methanol (racemic solketal: SOL) with a series of enol esters catalyzed by Pseudomonas cepacia lipase co-lyophilized with cyclodextrins (alpha-, beta-, gamma-, partially methylated beta-, and 2,3,6-tri-O-methyl-beta-cyclodextrin: alphaCyD; betaCyD; gammaCyD; Me1.78betaCyD; Me3betaCyD) were investigated and compared with those in diisopropyl ether (IPE). In the case of SUL, enzyme activities of the co-lyophilizate with Me1.78betaCyD in CPME were lower than those in IPE with every acyl source, however, the absolute enantiopreference was shown in the transesterification with vinyl butyrate (VBR) in IPME. When the substrates were SOL and VBR, the enzyme activities in CPME were greatly enhanced as high as 1.6-9.8-fold, while the enantioselectivities in CPME were comparable to those in IPE.

Novel immobilized liposomal glucose oxidase system using the channel protein OmpF and catalase.

The reactivity of immobilized glucose oxidase-containing liposomes (IGOL) prepared in our previous work (Wang et al. [2003] Biotechnol Bioeng 83:444-453) was considerably improved here by incorporating the channel protein OmpF from Escherichia coli into the liposome membrane as well as by entrapping inside the liposome's aqueous interior not only glucose oxidase (GO), but also catalase (CA), both from Aspergillus niger. CA was used for decomposing the hydrogen peroxide produced in the glucose oxidation reaction inside the liposomes. The presence of OmpF enhanced the transport of glucose molecules from the exterior of the liposomes to the interior. In a first step of the work, liposomes containing GO and CA (GOCAL) were prepared and characterized. A remarkable protection effect of the liposome membrane on CA inside the liposomes at 40 degrees C was found; the remaining CA activity at 72 h incubation was more than 60% for GOCAL, while less than 20% for free CA. In a second step, OmpF was incorporated into GOCAL membranes, leading to the formation of OmpF-embedded GOCAL (abbreviated GOCAL-OmpF). The activity of GO inside GOCAL-OmpF increased up to 17 times in comparison with that inside GOCAL due to an increased glucose permeation across the liposome bilayer, without any leakage of GO or CA from the liposomes. The optimal system was estimated to contain on average five OmpF molecules per liposome. Finally, GOCAL-OmpF were covalently immobilized into chitosan gel beads. The performance of this novel biocatalyst (IGOCAL-OmpF) was examined by following the change in glucose conversion, as well as by following the remaining GO activity in successive 15-h air oxidations for repeated use at 40 degrees C in an airlift bioreactor. IGOCAL-OmpF showed higher reactivity and reusability than IGOL, as well as IGOL containing OmpF (IGOL-OmpF). The IGOCAL-OmpF gave about 80% of glucose conversion even when the catalyst was used repeatedly four times, while the corresponding conversions were about 60% and 20% for the IGOL and IGOL-OmpF, respectively. Due to the absence of CA, IGOL-OmpF was less stable and resulted in drastically inhibited GO.

Effects of ultrasonic intensity and reactor scale on kinetics of enzymatic saccharification of various waste papers in continuously irradiated stirred tanks.

Based on the enzymatic saccharification of the various pulps in the previous 0.8 l ultrasonic stirred tank reactor, the ultrasound-enhanced saccharification of waste papers such as newspaper, carton paper, office paper etc. was carried out in the same reactor as well as larger scale stirred tank reactors of size 3.2 and 6.4 l. The saccharification of each waste paper was less enhanced in the larger reactor at a given ultrasonic intensity. This could be attributed to the decrease in the ultrasonic intensity per reaction volume, i.e., the specific ultrasonic intensity. Most waste papers were more efficiently hydrolyzed with increasing specific ultrasonic intensities, although newspaper was less efficiently done for a too high specific intensity. Such an adverse effect might be due to the fact that some impurities in the newspaper such as lignin were activated by an intensive ultrasonic irradiation to form a rigid and closed network, which inhibited the access and adsorption of cellulase on to the substrate surface. The previous kinetic model was found to be applicable to analyze and simulate the saccharification of each waste paper in the different ultrasonic reactors. The ultimate conversion of a substrate based on the total sugar concentration estimated for an infinite reaction time could be correlated as a function of the ratio of initial substrate to enzyme concentrations at a fixed specific ultrasonic intensity. Either the apparent rate constant or the ultimate conversion increased and tended to approach a constant with an increase in the specific ultrasonic intensity except for the case of newspaper, while neither the apparent Michaelis constant, product inhibition constant nor glucose formation equilibrium constant was influenced by the specific ultrasonic intensity.

Mechanism for high stability of liposomal glucose oxidase to inhibitor hydrogen peroxide produced in prolonged glucose oxidation.

Glucose oxidase (GO) was encapsulated in the liposomes composed of POPC (1-palmitoyl-2-oleoyl-sn-glycero-3-phosphocholine) to increase the enzyme stability through its decreased inhibition because of hydrogen peroxide (H(2)O(2)) produced in the glucose oxidation. The GO-containing liposomes (GOLs) were completely free of the inhibition even in the complete conversion of 10 mM glucose at 25 degrees C because the H(2)O(2) concentration was kept negligibly low both outside and inside liposomes throughout the reaction. It was interestingly revealed that the H(2)O(2) produced was decomposed not only by a slight amount of catalase originally contained in the commercially available GO but also by the lipid membranes of GOL. As compared to the GOL-catalyzed reaction, the free GO-catalyzed reaction more highly accumulated H(2)O(2) because of the more rapid glucose conversion despite containing free catalase, leading to the completely inhibited GO before reaching a sufficient glucose conversion. This suggested that only the liposomal catalase could continue to catalyze the H(2)O(2) decomposition. The effect of the glucose oxidation rate, i.e., the H(2)O(2) production rate on the liposomal GO inhibition, was also examined employing the various GOLs with different permeabilities to glucose present in their external phase. It was concluded that the liposomal GO free of the inhibition could be obtained when the GOL-catalyzed H(2)O(2) formation rate was limited by such a suitable lipid bilayer as POPC membrane so that the rate was well-balanced with the sum of the above two H(2)O(2) decomposition rates. The highly stable GOL obtained in the present paper was shown to be a useful biocatalyst for the prolonged glucose oxidation.

Preparation of gemini-type amphiphiles bearing cyclitol head groups and their application as high-performance modifiers for lipases.

Five gemini-type amphiphiles bearing cyclitol head groups, which have abundance of axial hydroxy groups, are newly synthesized. The syntheses are based on a common mixed anhydride method utilizing N,N'-[iminobis(trimethylene)]bisquinamide, prepared from iminobispropylamine and quino-1,5-lactone, and dialkyl N-(3-carboxypropanoyl)-L-glutamates as polar and hydrophobic components, respectively. Candida rugosa lipase (CRL) and Pseudomonas cepacia lipase (PCL) are co-lyophilized with these synthesized gemini-type amphiphiles, and their transesterification activities in organic solvents are evaluated. The modified PCL and CRL prepared by using each amphiphile showed highly enhanced and moderately enhanced enzyme activity, respectively. These results are discussed in terms of the increased preferential exclusion of the hydrophilic heads of the amphiphile and of the topological view of the amphiphile.

Enhancement of apparent substrate selectivity of proteinase K encapsulated in liposomes through a cholate-induced alteration of the bilayer permeability.

Proteinase K-containing liposomes with highly selective membrane permeability properties were prepared. The selectivity obtained was with respect to the two substrate molecules added to the external aqueous phase of the liposomes: acetyl-L-Ala-Ala-Ala-p-nitroanilide (Ac-AAA-pNA) and succinyl-L-Ala-Ala-Ala-p-nitroanilide (Suc-AAA-pNA). The liposome-forming lipid used was POPC (1-palmitoyl-2-oleoyl-sn-glycero-3-phosphocholine) and modulation of the membrane permeability was achieved using the detergent cholate. Proteinase K-containing mixed liposomes (PKCL) were prepared by adding cholate to preformed proteinase K-containing POPC liposomes (PKL) at a defined effective cholate/POPC molar ratio in the liposomal bilayer membrane R(e). Proteinase K was kept inside PKCL with a negligible amount of leakage into the bulk aqueous phase at R(e) < or = 0.30. At higher R(e), leakage of proteinase K was pronounced, even under conditions where POPC/cholate mixed liposomes seemed to be still intact (0.30 < R(e) < or = 0.39). At R(e) < or = 0.30, the reactivity of proteinase K in the PKCL measured with the externally added substrate Ac-AAA-pNA increased with increasing R(e), while the reactivity measured with Suc-AAA-pNA remained low, regardless of the R(e) value. This showed that externally added Ac-AAA-pNA molecules permeated the liposomal membrane more easily than Suc-AAA-pNA by modulating the membrane with cholate. Consequently, Ac-AAA-pNA was hydrolyzed in PKCL with considerably higher apparent substrate selectivity in comparison with the cases of proteinase K in PKL and free proteinase K (without liposomal encapsulation). The results obtained clearly demonstrate that the prepared PKCL can be utilized as a kind of nano-scaled bioreactor system which can take up a particular target substrate with high apparent substrate selectively from the external phase of the liposomes. Inside the liposomes, the target substrate is then converted into the corresponding products.

Stereochemistry of a diastereoisomeric amphiphile and the species of the lipase influence enzyme activity in the transesterification catalyzed by a lipase-co-lyophilizate with the amphiphile in organic media.

Modified Candida rugosa and Pseudomonas cepacia lipase (CRL and PCL) were co-lyophilized with two pairs of synthetic diastereoisomeric amphiphiles, D- and L-2-(3-[bis-[3-(2,3,4,5,6-pentahydroxy-hexanoylamino)-propyl]-carbamoyl]-propionylamino)-pentanedioic acid didodecyl ester (D- and L-BIG2C12CA); D- and L-2-(2,3,4,5,6-pentahydroxy-hexanoylamino)-pentanedioic acid didodecyl ester (D- and L-2C12GE). Enzyme activities of the modified lipase in the transesterification in organic solvent were evaluated. Both pairs of the diastereoisomeric amphiphiles showed enhanced enzyme activity in the transacetylation between racemic sulcatol and isopropenyl acetate in diisopropyl ether, catalyzed by the PCL-co-lyophilizate, by 19-48 fold when compared to the native lipase lyophilized from buffer alone independent of the stereochemistry of the amphiphiles, while in the case of the CRL-co-lyophilizate only the L-BIG2C12CA showed enhanced enzyme activity in the transbutyrylation between racemic solketal and vinyl butyrate in cyclohexane as high as 68-78 fold.

Optimal covalent immobilization of glucose oxidase-containing liposomes for highly stable biocatalyst in bioreactor.

The glucose oxidase-containing liposomes (GOL) were prepared by entrapping glucose oxidase (GO) in the liposomes composed of phosphatidylcholine (PC), dimyristoyl L-alpha-phosphatidylethanolamine (DMPE), and cholesterol (Chol) and then covalently immobilized in the glutaraldehyde-activated chitosan gel beads. The immobilized GOL gel beads (IGOL) were characterized to obtain a highly stable biocatalyst applicable to bioreactor. At first, the glutaraldehyde concentration used in the gel beads activation as well as the immobilizing temperature and time were optimized to enhance the immobilization yield of the GOL to the highest extent. The liposome membrane composition and liposome size were then optimized to obtain the greatest possible immobilization yield of the GOL, the highest possible activity efficiency of the IGOL, and the lowest possible leakage of the entrapped GO during the GOL immobilization. As a result, the optimal immobilization conditions were found to be as follows: the liposome composition, PC/DMPE/Chol = 65/5/30 (molar percentage); the liposome size, 100 nm; the glutaraldehyde concentration, 2% (w/v); the immobilizing temperature, 4 degrees C; and the immobilizing time, 10 h. Furthermore, the optimal IGOL prepared were characterized by its rapidly increasing effective GO activity to the externally added substrate (glucose) with increasing temperature from 20 to 40 degrees C, and also by its high stability at 40 degrees C against not only the thermal denaturation in a long-term (7 days) incubation but also the bubbling stress in a bubble column. Finally, compared to the conventionally immobilized glucose oxidase (IGO), the higher operational stability of the optimal IGOL was verified by using it either repeatedly (4 times) or for a long time (7 days) to catalyze the glucose oxidation in a small-scale airlift bioreactor.

Preparation and characterization of reactive and stable glucose oxidase-containing liposomes modulated with detergent.

Glucose oxidase-containing liposomes (GOL) as well as detergent-modulated glucose oxidase-containing liposomes were prepared and characterized, focusing not only on the reactivity of the liposomes upon external addition of glucose but also on the leakage of the entrapped glucose oxidase (GO) from the liposomes with the aim of developing a reactive and stable liposomal GO system. The membranes of the GOL prepared were composed of 1-palmitoyl-2-oleoyl-sn-glycero-3-phosphocholine (POPC) and modulated with either Triton X-100 or cholate. In the absence of added detergent, no GO leakage from the GOL was observed while its enzymatic activity was very low (low glucose permeability). As detergent-modulated liposomes, mixed POPC/Triton X-100 and mixed POPC/cholate liposomes (abbreviated as TL and CL, respectively) were prepared at different effective detergent/POPC molar ratios (R(e)) ranging from R(e) = 0 to R(e) = R(e) (sat) (R(e) (sat) is the critical value of R(e) at which the liposome membrane is saturated with detergent). The reactivity of GO-loaded TL (abbreviated as GOTL) or GO-loaded CL (GOCL) increased drastically with increase in the respective detergent content in the liposomes. In the case of GOTL, at R(e) (sat) = 0.40, a high reactivity was measured with a simultaneous high extent of GO leakage, suggesting that the observed enzymatic reaction was catalyzed mainly by leaked GO, caused by the interaction of Triton X-100 with the POPC membrane. On the other hand, GOCL prepared at R(e) (sat) = 0.43 showed relatively high reactivity with only a small extent of GO leakage, suggesting that most of the enzyme reaction was limited by the glucose permeation across the bilayers of GOCL. The GO leakage from GOCL was found to occur mostly during the rearrangement of the liposomal membrane during the preparation of the GOCL (mixing the GOL and cholate). Fluorescence polarization measurements of membrane-associated DPH (1,6-diphenyl-1,3,5-hexatriene) indicated that CL prepared by modifying POPC with cholate did not lead to a drastic change in membrane fluidity, indicating that the interacting cholate molecules did not penetrate deeply into the POPC bilayers. In summary, it was clearly shown that the membrane permeability of GOL can be quite simply modulated by mixing it with a certain amount of cholate to form highly reactive and stable GOCL with minimal enzyme leakage.

Enhanced enzyme activity and enantioselectivity of lipases in organic solvents by crown ethers and cyclodextrins.

Lipases from Candida rugosa (CRL) and Pseudomonas cepacia (PCL) were co-lyophilized with cyclic oligoethers including four crown ethers and nine cyclodextrins (CyDs), and their transesterification activity and enantioselectivity in organic solvents were evaluated. The PCL co-lyophilized with each additive showed simultaneously enhanced enzyme activity and enantioselectivity when compared to the native lipase lyophilized from buffer alone; in contrast, such enhancement was not observed for the co-lyophilized CRL. Among the cyclic oligoethers examined, permethylated betaCyD (Me1.78betaCyD), as the most suitable additive, was used for the optimization of both the co-lyophilized PCL preparation and reaction conditions by determining the effects of varying the additive/lipase ratio, aqueous pH, the nature of organic solvents, and temperature. The initial rate determined for the transesterification between racemic 2,2-dimethyl-1,3-dioxolane-4-methanol and vinyl butyrate in diisopropyl ether at 30 degrees C increased by up to 17-fold and the enantioselectivity represented by E could be doubled. While there was an inverse correlation between temperature and enantioselectivity, with the Me1.78betaCyD-PCL co-lyophilizate, the reaction rate even at 0 degrees C was much higher than that at higher temperatures in the native PCL-catalyzed reaction. Hence, this method seems to be of practical use for the large-scale production of optically active compounds.

Structural effects of amphiphiles on Candida rugosa lipase activation by freeze-drying of aqueous solution of enzyme and amphiphile.

Lipases co-lyophilized with water-soluble gemini-type amphiphiles were found to have high enzyme activity in nonaqueous media without washing out of the amphiphile with anhydrous organic solvent. In this study, we obtained freeze-dried complexes of Candida rugosa lipase (CRL) with six water-soluble twin glusitol-headed amphiphiles bearing different types of hydrophobic tails, including newly synthesized ones, and their transesterification activity in organic solvent was evaluated. The results indicate that the increased enzyme activity upon CRL modification at 200 molar ratio of amphiphile/CRL, which are restricted to the ester-containing amphiphiles, is probably due to the surface activation by the interaction between ester-carbonyl of the amphiphile and phenyl group of the tyrosine residue situated on the surface of the lid in the CRL.