Enzymic Interesterification of fats: Immobilization and Immunogold Localization of Lipase on Ion-Exchange Resins

A 1,3 specific lipase from Mucor miehei has been immobilized to two phenolformaldehyde resins with active tertiary amine groups and different porous structures (Duolite ES562 and ES568N). Duolite ES568N has a more uniform pore structure, allowing more rapid uptake of lipase. Immobilized lipase particles were treated by washing, dehydration with glycolmethacrylate and embedding in polymer. Following immunogold staining of thin sections, examined by electron or light microscopy showed that the location of the lipase was dependent on the pore structure of the support material and the immobilization time.     

Mass transfer effects in solvent-free fat interesterification reactions: influences on catalyst design

The use of solvent-free systems in the oil and fats industry is commonplace. Initial studies on interesterification were carried out in solvent systems because the lipase was immobilized solely by adsorption onto particles of diatomaceous earth. In this study, the mass transfer characteristics associated with the continuous interesterification of olive oil in a solvent-free system have been examined, for lipase immobilized on the three ion-exchange materials: Duolite ES562, Duolite ES568, and Spheroil DEA. The process of immobilization is influenced by the internal structure of the material and this in turn influences the interesterification activity of the catalyst. Individually prepared catalysts for the three support materials have shown that external mass transfer limitations are unlikely even at low flowrates.In the case of Spherosil DEA, with a mean pore diameter of 1480 A, the wide pores would be expected to reduce internal mass transfer limitations; however, it is more likely that the reduction in activity with increased catalyst loading is due to the lipase molecules being immobilized in a tightly packed monolayer. In such a situation, some active sites of the lipase molecules would become inaccessible to substrate molecules leading to an observed reduction in activity. For Duolite ES568, the observed results are very similar to those seen for Spherosil DEA, however, the pore structure of this support material indicate that some internal mass transfer limitations may also be occurring. Yet the contribution of the individual effects cannot be determined. The results observed for the support Duolite ES562 are different than those observed for the other materials and reflect the heterogeneity of Duolite ES562. The large proportion of narrow pores in the support mean that, for the catalysts examined, immobilization is most likely to have occurred in the external pores of the particles, and as such no internal mass transfer limitation is observed.It is clear that for interesterification the material chosen for enzyme immobilization will have an important role in determining the catalyst efficiency. External mass transfer limitations are very minor and observed internal mass transfer limitations may be caused by both internal mass transfer and the manner in which the immobilization process occurs. (c) 1994 John Wiley & Sons, Inc.     

Different phyllosilicates as supports for lipase immobilisation

The aim of this work was to determine the enzymatic activities resulting from the adsorption of Rhizomucor miehei lipase (RML) and Candida cylindracea lipase (CCL) onto three different phyllosilicates (sepiolite, palygorskite and montmorillonite), comparing the resultant activities with those obtained following similar immobilisation technique on a widely used resin (Duolite A-568). Due to the different adsorption mechanisms produced, different derivatives with higher hydrolytic activities can be obtained. Comparing the clays tested, the results showed that, in comparison with the laminar silicate (montmorillonite sample) and Duolite A-568 (spherical particles), fibrous materials (palygorskite and sepiolite) resulted in derivatives with higher hydrolytic activities in the hydrolysis of different ethyl esters. Moreover, according to the data obtained with the electrophoresis, the selectivity of immobilisation for RML in the case of fibrous silicates was optimal. As a conclusion, and according to the activities and selectivities measured, at least two out of the four studied materials (sepiolite and palygorskite) would be useful as supports for immobilisation for proteins of relatively low molecular weight (such as RML) for further use in biotransformations, while for C. cylindracea the immobilisation onto duolite rendered a derivative specially active in the hydrolysis of ethyl formiate (esterasic activity).     

Concentrates of DHA from fish oil by selective esterification of cholesterol by immobilized isoforms of lipase from Candida rugosa

Two lipases (Lip A and Lip B), were purified from a commercial lipase preparation produced by Candida rugosa and partially characterized. The purified lipases were immobilized on Duolite A 568 and used in the selective esterification of cholesterol with free fatty acids from sardine fish oil. The results showed that Lip A and Lip B preferentially esterified saturated and monounsaturated fatty acids allowing a 3.4-fold (Lip B, 24 h) and 4-fold (Lip A, 10 h) enrichment of docosahexaenoic acid in the remaining free fatty acid fraction. Selectivity towards eicosapentaenoic acid was less pronounced. By this selective esterification docosahexaenoic acid was concentrated from 7.4 to 32% with a recovery of 95% of its initial content in sardine fish oil.     

Immobilization of Lipase from Rhizopus Niveus: A Way to Enhance its Synthetic Activity in Organic Solvent

Lipase (EC 3.1.1.3) from Rhizopus niveus was immobilized by physical adsorption on various carriers, including different types of Celite, Spherosil and Duolite. After the enzyme immobilization, the recovered hydrolytic and synthetic activities on the different carriers were then determined. The results showed that the highest synthetic activity was obtained when Duolite XAD 761 was used as the carrier. However the recovered hydrolytic activity after the immobilization on this resin was relatively low although this carrier showed the best protein loading capacity. The highest recovered hydrolytic activity was observed when the lipase was immobilized on Celite Hyflo-Supercel using an immobilization buffer adjusted to pH 4. The comparison of the free and immobilized lipase specific activities suggest that the immobilization on Celite Hyflo-Supercel, Spherosil XOA 200 and silica has enhanced the lipase hydrolytic activity. On the other hand, the use of the lipase immobilized on Duolite XAD 761 as biocatalyst of synthetic reaction, compared to that of the free enzyme, allows the reaction initial velocity to be increased 12.2-fold. In addition, the synthetic activity of the lipase immobilized on Duolite XAD 761 was shown to be maximum at a water activity in the range of 0.32-0.52.     

On the Activities of Glucoamylase Chemically Fixed to Cyanogen Bromide-activated Cellulose

N-Carbamyl-D-amino acid amidohydrolase (DCase), produced with recombinant Escherichia coli cells using a cloned gene from Agrobacterium sp. strain KNK712, has been immobilized for use in the production of D-amino acids. The porous polymers, Duolite A-568 and Chitopearl 3003, were much better than other resins for the activity and stability of the adsorbed enzyme. The activity of DCase expressed on Duolite A-568 and Chitopearl 3003 amounted to 96 units/g-wet-resin and 91 units/g-wet-resin, respectively. DCase immobilized on Duolite A-568 was found to be most stable at about pH 7, and it was further stabilized by reductants such as dithiothreitol, L-cysteine, cysteamine, and sodium hydrosulfite. The stability during the repeated batch reactions was greatly improved when dithiothreitol was in the reaction mixture, and the higher crosslinking degree with glutaraldehyde also stabilized the immobilized enzyme. After 14 times repeated reactions, the remaining activity of the immobilized enzyme cross-linked with 0.1% and 0.2% of glutaraldehyde, and 0.2% of glutaraldehyde with dithiothreitol in the reaction mixture was 12%, 18%, and 63%, respectively. DCase produced with Pseudomonas sp. strain KNK003A and Pseudomonas sp. strain KNK505, which are thermotolerant soil bacteria, and that with Agrobacterium sp. strain KNK712 were also immobilized on Duolite A-568. The stability of the enzymes of thermotolerant bacteria during reactions was superior to that of Agrobacterium sp. strain KNK712, though the activity was lower than that of strain KNK712.     

Internal Mass Transfer Limitation During Enzymatic Esterification in Supercritical Carbon Dioxide and Hexane

A kinetic study of ethyl myristate formation by esterification of myristic acid with ethanol catalysed by a lipase from Mucor miehei immobilized on Duolite A 568, has been carried out.

The reaction was done in a two liquid phase system in which the non-aqueous solvent was supercritical carbon dioxide (P= 12.5 MPa, T = 323 K) or n-hexane (P = 0.1 MPa, T = 323K). In heteregenous catalysis, it is important to study the internal mass transfer limitation. For this, the support was sieved into different size series (from 300 to 600 mm) and the reaction was carried out for each size series. The samples were analyzed by gas chromatography and the esterification was shown to follow Ping Pong Bi Bi kinetics with competitive substrate inhibition. The Thiele modulus values show that there is, in the hexane case, a diffusional control while in SCCO₂ media, we obtained an intermediate rate between reactional and diffusional rates.     

Optimization of invertase immobilization by adsorption in ionic exchange resin for sucrose hydrolysis

This work presents as a main objective to study the immobilization process of yeast invertase by adsorption in the ion exchanging resin Duolite A-568 for invert sugar production. Initially, a kinetic study of the soluble form of the enzyme was carried out. At the sequence was studied the immobilization process of yeast invertase in the weakly exchanging anionic resin Duolite A-568. The influences of the pH, enzyme concentration and temperature in the enzyme immobilization were analyzed through a central composite design (CCD). The results indicated that the retention of the catalytic activity in immobilization was strongly dependent of these variables, being maximum in a pH value of 5.0, with an enzyme concentration of 12.5 g/L (1.875 g of protein per liter) and temperature of 30 °C. The simultaneous influence of pH and temperature on the free and immobilized invertase activity was also studied through a CCD.     

Immobilization of a Thermostable Cellobiose 2-Epimerase from Rhodothermus marinus JCM9785 and Continuous Production of Epilactose

Cellobiose 2-epimerase (CE) efficiently forms epilactose which has several beneficial biological functions. A thermostable CE from Rhodothermus marinus was immobilized on Duolite A568 and packed into a column. Lactose (100 g/L) was supplied to the reactor, kept at 50 °C at a space velocity of 8 h(-1). The epilactose concentration of the resulting eluate was 30 g/L, and this was maintained for 13 d.     

Immobilization of thermotolerant N-carbamyl-d-amino acid amidohydrolase

N-Carbamyl-d-amino acid amidohydrolase (DCase), in which amino acid residues were substituted by mutation, followed by the selection based on thermotolerance, showed improved thermostability, by 5° or 10°C, compared to the native DCase. These DCases were immobilized on a macroporous phenol formaldehyde resin, Duolite A-568, and the immobilized thermotolerant enzymes showed higher activity than the immobilized native DCase. From the results of repeated batch reactions, the half-lives of the activities of immobilized thermotolerant DCase, in which Leu was substituted for Pro 203, and immobilized native DCase were 104 and 58 times, respectively. It was revealed that the higher thermotolerance enabled the immobilized enzymes to be more stable in reactions. A reductant, dithiothreitol, also stabilized the enzymes in reactions. Compared with soluble DCase, immobilized DCase was somewhat stable, and its activity was optimum at a lower pH.     

Stability of lipase immobilized on <Emphasis Type="Italic">O</Emphasis>-pentynyl dextran

O-Pentynyl dextran (PyD), an amphiphilic polysaccharide derivative with a degree of substitution (DS) of 0.43 was compared with ion exchange resins Lewatit VP OC 1600, Amberlite XAD 761 and Duolite A568 for immobilization of Lipase from Rhizopus arrhizus by adsorption method. The immobilized enzymes were employed for esterification of octanoic acid with geraniol in n-hexane as model reaction. PyD showed higher lipase adsorption and with 249 μmol min⁻¹ g⁻¹ significant higher esterification activity than the other supports (67–83 μmol min⁻¹ g⁻¹). Biocatalysts from all types of supports except PyD became completely inactive within 8 weeks storing at −10 °C while lipase immobilized on PyD retained its full esterification activity for at least 14 weeks. In repeated use, yield decreased rapidly after two cycles for all supports except for PyD. For this biopolymeric support, constantly 90% yield was achieved even after eight cycles, when the biocatalyst was washed with n-hexane and water and then freeze-dried. To achieve this yield, prolonged reaction times were required, partly on the account of an increasing delay period, probably to adapt active conformation, until the reaction starts.     

Development of a stable continuous flow immobilized enzyme reactor for the hydrolysis of inulin

A 23.5-fold purified exoinulinase with a specific activity of 413 IU/mg and covalently immobilized on Duolite A568 has been used for the development of a continuous flow immobilized enzyme reactor for the hydrolysis of inulin. In a packed bed reactor containing 72 IU of exoinulinase from Kluyveromyces marxianus YS-1, inulin solution (5%, pH 5.5) with a flow rate of 4 mL/h was completely hydrolyzed at 55 degrees C. The reactor was run continuously for 75 days and its experimental half-life was 72 days under the optimized operational conditions. The volumetric productivity and fructose yield of the reactor were 44.5 g reducing sugars/L/h and 53.3 g/L, respectively. The hydrolyzed product was a mixture of fructose (95.8%) and glucose (4.2%) having an average fructose/glucose ratio of 24. An attempt has also been made to substitute pure inulin with raw Asparagus racemosus inulin to determine the operational stability of the developed reactor. The system remained operational only for 11 days, where 85.9% hydrolysis of raw inulin was achieved.     

Structure and protein environment of the retinal chromophore in light- and dark-adapted bacteriorhodopsin studied by solid-state NMR

Our previous solid-state 13C NMR studies on bR have been directed at characterizing the structure and protein environment of the retinal chromophore in bR568 and bR548, the two components of the dark-adapted protein. In this paper, we extend these studies by presenting solid-state NMR spectra of light-adapted bR (bR568) and examining in more detail the chemical shift anisotropy of the retinal resonances near the ionone ring and Schiff base. Magic angle spinning (MAS) 13C NMR spectra were obtained of bR568, regenerated with retinal specifically 13C labeled at positions 12-15, which allowed assignment of the resonances observed in the dark-adapted bR spectrum. Of particular interest are the assignments of the 13C-13 and 13C-15 resonances. The 13C-15 chemical resonance for bR568 (160.0 ppm) is upfield of the 13C-15 resonance for bR548 (163.3 ppm). This difference is attributed to a weaker interaction between the Schiff base and its associated counterion in bR568. The 13C-13 chemical shift for bR568 (164.8 ppm) is close to that of the all-trans-retinal protonated Schiff base (PSB) model compound (approximately 162 ppm), while the 13C-13 resonance for bR548 (168.7 ppm) is approximately 7 ppm downfield of that of the 13-cis PSB model compound. The difference in the 13C-13 chemical shift between bR568 and bR548 is opposite that expected from the corresponding 15N chemical shifts of the Schiff base nitrogen and may be due to conformational distortion of the chromophore in the C13 = C14-C15 bonds.(ABSTRACT TRUNCATED AT 250 WORDS)     

Activity and stability of chemically modified Candida antarctica lipase B adsorbed on solid supports

The effect of various covalent chemical modifications on the transesterification activity and stability of adsorbed lipase B from Candida antarctica (CALB) was studied in 2-butanone and o-xylene. CALB species modified with either polyethylene glycol 2000 monomethyl ether (MPEG), polyethylene glycol 300 mono-octyl ether (OPEG) or n-octanol (OCT) were used in combination with a hydrophobic (Accurel) and a hydrophilic (Duolite) support. The thermostabilities of adsorbed CALB in both solvents, and that of free CALB in o-xylene were not influenced by the modifications. In contrast, the thermostability of free CALB in 2-butanone decreased 2.5-fold after MPEG modification and increased 1.5-fold after modification with OPEG and n-octanol, compared to that of native CALB. The activities of the native and modified CALB species were up to 9-fold higher after adsorption onto Accurel than those of the corresponding free enzymes. Adsorption of these enzyme species onto Duolite only resulted in a 2- to 3-fold increase in the activity of OPEG- and OCT-modified CALB. The modified CALB species adsorbed onto Accurel show similar or up to 2-fold lower activities than do native adsorbed CALB species, while 1.5- to 6-fold higher activities were found for modified CALB species adsorbed onto Duolite. We propose that hydrophobic modifiers induce conformational changes of CALB during adsorption on a hydrophobic support whereas all three modifiers protect CALB from structural alterations during adsorption onto a hydrophilic support. Received: 18 March 1999 / Received revision: 21 June 1999 / Accepted: 27 June 1999     

Blueprint for a lipase support: Use of hydrophobic controlled-pore glasses as model systems

For the commercial exploitation of lipase biocatalysis to be successful, it is essential that effective supports are selected for lipase immobilization. In this study hydrophobic controlled-pore glasses have been used as model systems for the immobilization of Rhizomucor miehei lipase. The effect of pore diameter and surface chemistry on enzyme efficiency in a typical esterification reaction under essentially nonaqueous conditions has been examined. It has been found that pore diameters of at least 35 nm are needed for the lipase to be able to utilize the internal volume of the support particles in the immobilization process. Despite the small size of the substrates in the esterification reaction, even larger pores (>100 nm) are required for the lipase efficiency to become independent of pore diameter; below 100 nm lipase activity and efficiency are markedly reduced. It has also been shown that the chemical nature of the hydrophobic surface plays an important part in catalyst design. Although lipase will adsorb readily to a wide range of hydrophobic groups, the highest catalyst activities are obtained when the glass surface is derivatized to give long alkyl chains; the presence of unsaturated derivatives gonerally leads to a reduction in activity. (c) 1994 John Wiley & Sons, Inc.     

Evolutionarily stable leaf area production in plant populations

Using an analytical model, it was shown that for a given amount of nitrogen in the canopy of a stand (N(T)), there exists an evolutionarily stable leaf area index (ES-LAI), and therefore an evolutionarily stable average leaf nitrogen content (n(ES)(av);n(ES)(av) =N(T)/ES-LAI), at which no individual plant in the stand can increase its photosynthesis by changing its leaf area. It was also shown that this ES-LAI is always greater than the optimal LAI that maximizes photosynthesis per unit N(T) of the stand. This illustrates that the canopy structure that maximizes photosynthesis of a population is not the same as the canopy structure that maximizes photosynthesis of individuals within a population. It was further derived that the ES-LAI at given N(T) increases with the ratio between the light-saturated photosynthesis and the N content per unit leaf area (leaf-PPNUE) and that it decreases with the canopy extinction coefficient for light (K(L)), the light availability and the apparent quantum yield (phi). These hypotheses were tested by comparing calculated ES-LAI and n(ES)(av) values to actual LAIs and leaf N contents measured for stands of a large variety of herbaceous plants. There was a close correspondence between the calculated and measured values. As predicted by the model, plants with high leaf-PPNUEs produced more leaf area per unit nitrogen than those with low leaf-PPNUEs while plants with horizontal leaves, forming stands with higher K(L) values, produced less leaf area than those with more vertically inclined leaves. These results suggest that maximization of individual plant photosynthesis per unit of nitrogen plays an important role in determining leaf area production of plants and the resulting canopy structure of stands of vegetation. They further suggest this optimization to be a mechanism by which leaf traits such as leaf-PPNUE and leaf inclination angle are causally related to structural characteristics of the population, i.e. the leaf area index of the stand.     

表面改性SBA-15材料固载猪胰脂肪酶

采用试剂y-氯丙基三乙氧基硅烷（cvrEs）对介孔硅材料SBA-15进行表面改性,并通过红外图谱（FT-IR）和N2吸附脱附等温图（BET）对其进行表征。结果表明：改性前原材料的比表面积为460．9m2／g,改性后材料比表面积提高到512．0m2／g。利用改性前和改性后的SBA-15对猪胰脂肪酶进行固载实验,并对实验结果进行比较,发现改性后的SBA-15在脂肪酶活性、pH环境适应性、热耐受性和可操作性都优于改性前的SBA-15,在最优条件下的酶活力提高超过60％。     

Stereoselectivity of Pseudomonas cepacia lipase toward secondary alcohols: a quantitative model

The lipase from Pseudomonas cepacia represents a widely applied catalyst for highly enantioselective resolution of chiral secondary alcohols. While its stereopreference is determined predominantly by the substrate structure, stereoselectivity depends on atomic details of interactions between substrate and lipase. Thirty secondary alcohols with published E values using P. cepacia lipase in hydrolysis or esterification reactions were selected, and models of their octanoic acid esters were docked to the open conformation of P. cepacia lipase. The two enantiomers of 27 substrates bound preferentially in either of two binding modes: the fast-reacting enantiomer in a productive mode and the slow-reacting enantiomer in a nonproductive mode. Nonproductive mode of fast-reacting enantiomers was prohibited by repulsive interactions. For the slow-reacting enantiomers in the productive binding mode, the substrate pushes the active site histidine away from its proper orientation, and the distance d(H(N epsilon) - O(alc)) between the histidine side chain and the alcohol oxygen increases, d(H(N epsilon) - O(alc)) was correlated to experimentally observed enantioselectivity: in substrates for which P. cepacia lipase has high enantioselectivity (E > 100), d(H(N epsilon) - O(alc)) is >2.2 A for slow-reacting enantiomers, thus preventing efficient catalysis of this enantiomer. In substrates of low enantioselectivity (E < 20), the distance d(H(N epsilon) - O(alc)) is less than 2.0 A, and slow- and fast-reacting enantiomers are catalyzed at similar rates. For substrates of medium enantioselectivity (20 < E < 100), d(H(N epsilon) - O(alc)) is around 2.1 A. This simple model can be applied to predict enantioselectivity of P. cepacia lipase toward a broad range of secondary alcohols.     

Structural features of a cold-adapted Alaskan bacterial lipase

The three dimensional model of cold-adapted Alaskan psychrotroph Pseudomonas species (Strain B11-1) lipase has been constructed by homology modeling based on the crystal structure of acetyl esterase from Rhodococcus species and refined by molecular dynamics methods. Our model locates the substrate-binding cavity and further suggests that Ser-155, Asp-250, and His-280 are the members of the catalytic triad. Substrate specificity of the modeled lipase has been examined by docking experiments, which indicates that the ester of C(6) fatty acid has the highest affinity for the enzyme. Our model also identifies the oxyanion hole that plays an important role in the stabilization of the tetrahedral intermediate during catalysis. Comparison of this cold-adapted lipase with the crystal structure of a thermophilic Bacillus stearothermophilus P1 lipase supported the assumption that cold-adapted enzymes have a more flexible three-dimensional structure than their thermophilic counterparts. The conformational flexibility of this modeled cold-adapted lipase at low temperature probably originates from a combination of factors compared to its thermophilic counterpart, i.e., lower number of salt bridges and cation-pi interactions, increase in the non-polar surface area exposed to solvent. Our study may help in understanding the structural features of a cold-adapted lipase and can further be used in engineering lipase that can function at or near extreme temperatures with considerable biotechnological potential.