A thermostable lipase produced by a newly isolated <Emphasis Type="Italic">Geotrichum</Emphasis>-like strain,R59

Growth and production of lipase by a new Geotrichum-like strain, R59, were studied. Production of extracellular lipase was substantially enhanced when the initial pH of the culture medium, types of carbon and nitrogen sources, substances probably stimulating the lipase biosynthesis, the temperature, and time of growth were optimized. Sucrose and triolein were the most effective carbon sources for lipase production. Maximum lipase activity (146 U/ml^–1) was obtained with urea as the nitrogen source. Growth at 30°C, an initial pH of 6.0 and incubation time of 48 h were found as optimum conditions for cell growth and production of lipase by Geotrichum-like strain R59. The enzyme was thermostable and exhibited very high activity after 1 h incubation at 60°C.     

Glycerolysis of tallow with immobilised lipase

Summary Lipozyme (immobilised Mucor meihei lipase) was used to catalyse glycerolysis of melted tallow to synthesise monoglycerides. At a reaction temperature of 50 °C, a maximum 35% yield of monoglyceride was obtained. Cooling the reaction below 42°C resulted in monoglyceride crystallisation which improved the yield to up to 50% but further yield increases were prevented by solidification of the reaction mixture. Enzyme could be easily recovered by filtration after melting the reaction mixture. The reaction could also be carried out by circulating the reaction mixture through a packed column of lipozyme.     

A lipase preparation with dual pH optima,wide temperature optima and broad substrate specificity for multiple applications

Summary Optimised procedures for the production and recovery of lipase at 25 litre scale by submerged fermentation using aRhizopus species isolated from petroleum-soaked soil are developed. These lipase preparations are characterized by dual pH optima (4.0 and 8.0), wide temperature optima (over 80% activity between 40–57°C), broad specificity for substrates, high degree of tolerance for common salts and excellent stability during usage as well as storage.     

Aminolysis of 2-hydroxy esters catalyzed by Candida antarctica lipase

Candida antarctica lipase catalyzed the aminolysis of 2-hydroxy esters with amines in organic solvents to yield the corresponding 2-hydroxy amides. The reactions proceeded at 28–30 °C in dioxane for 6 h with 3 mM substrates with yields ranging between 45% (w/w) (for branched substrates) to 88% (w/w) (for linear substrates). Although the reaction was not enantioselective, because of its simplicity it represents an alternative method for the synthesis of functionalised amides.     

Lipase-catalyzed synthesis of capsaicin analogs by transacylation of capsaicin with natural oils or fatty acid derivatives in n-hexane

Transacylation of capsaicin with triolein using a commercial lipase gave olvanil in an 85% yield at 70°C for 144 h. When olive oil was employed, the major product was olvanil (62%). Safflower oil gave a mixture of olvanil (39%) and linoleoyl vanillylamide (32%). Perilla oil gave linolenoyl vanillylamide (13%). Myristic acid and its methyl ester could be used as an acyl donor, and myristoyl vanillylamide was obtained in 20–78% using several lipases.     

Transesterification between triolein and stearic acid catalyzed by lipase in CO2 at various pressures

Transesterification between triolein and stearic acid catalyzed by lipase in pressurized CO2 at 50 °C was classified into three regions according to the pressure. Below 5 MPa which was the non-solvent region, the reaction was limited in the liquid triolein phase and the reaction rate was very slow. In the near critical region, from 5 to 10 MPa, the reaction rate was maximal at 5.9 MPa because of the stabilization of the enzyme-substrate complex. In the supercritical region, above 10 MPa, the reaction rate increased with an increase in pressure reflecting the increase in solubility of substrate in supercritical CO2 © Rapid Science Ltd. 1998     

Hepatic triacylglycerol lipase in circulating blood of normal and tumor-bearing mice and its hydrolysis of very-low-density lipoprotein and synthetic acylglycerols

A large amount of triacylglycerol lipase activity was present in the circulating blood of normal mice, and this activity decreased with development of Sarcoma 180 inoculated intraperitoneally. Triacylglycerol lipase in plasma of both normal and tumor-bearing mice was retained on the heparin-Sepharose columns and over 90% of the activity was eluted with 0.75 M NaCl. This enzyme had similar properties to hepatic triacylglycerol lipase and hydrolyzed very-low-density lipoprotein (VLDL)-triacylglycerol. Hepatic triacylglycerol lipase in plasma of normal mice hydrolyzed tricaprin and trilaurin most readily and better than 1-monoacylglycerols with the same acyl chain length. The hydrolyzing activities decreased with increase in the acyl chain length. The activity toward triolein was also higher than that toward 1-monoolein. 1-Monomyristin was hydrolyzed better than trimyristin. In contrast, hepatic triacylglycerol lipase in plasma of mice on day 4 after tumor inoculation hydrolyzed 1-monoacylglycerols better than triacylglycerols with the same acyl chain length. Hydrolysis of triolein by hepatic triacylglycerol lipase in plasma of both normal and tumor-bearing mice was reduced in the presence of 1-monoacylglycerols in the reaction mixture. The orders of their inhibitory effects coincided with the orders of the hydrolyzing activities toward 1-monoacylglycerols.     

Optimization of alkyl ester production from grease using a phyllosilicate sol-gel immobilized lipase**,***

Simple alkyl ester derivatives of restaurant grease were prepared using a lipase from Pseudomonoas cepacia immobilized within a phyllosilicate sol-gel matrix as biocatalyst. Alcoholysis reactions of grease were carried out in solvent-free media using a one-step addition of alcohol to the reaction mixture. The immobilized lipase was active from 40 to 70 °C. Ester yields (60–97%) were highest when using a ratio of reactants of 2 mmol grease to 8 mmol alcohol and the biocatalyst was 10% (w/w) of grease in the presence of molecular sieves.     

Enzymatic synthesis of terpenyl esters by transesterification with fatty acid vinyl esters as acyl donors by Trichosporon fermentans lipase

Enzymatic synthesis of terpenyl esters by esterification or transesterification with fatty acid vinyl esters as acyl donors by celite-adsorbed lipase of Trichosporon fermentans was investigated. In direct esterification of geraniol, the lipase showed high reactivity toward fatty acids with carbon chains longer than C-8, but little reactivity toward fatty acids with shorter chains. With fatty acid vinyl esters as acyl donors, the lipase catalysed the synthesis of geranyl and citronellyl esters with carbon chains shorter than C-6 in with yields of >90% molar conversion. Time course, effects of added water, temperature and substrate concentration were studied for the synthesis of geranyl acetate. Molar conversion yield reached 97.5% after 5 h incubation at 30–40°C with the addition of 3% water. In this reaction, no inhibition by substrates such as geraniol and vinyl acetate was observed.     

Enzymatic properties of lipase and characteristics production byLactobacillus delbrueckii subsp.bulgaricus

Some properties of an extracellular lipase produced byLactobacillus delbrueckii subsp.bulgaricus were studied. Maximum enzyme activity was found against olive and butter oil as enzyme substrates. Addition of 9% acacia gum, 0.1% Na-deoxycholate and 0.01 M CaCl₂ to the enzyme reaction mixture increased-lipase activity from 5.3 to 14.5 (FFA/mg protein/minute) at pH 6.0 and at 40° C. Maximum lipase production was reached in the presence of glucose as a sole source of carbon, wheat bran as nitrogen source, olive oil as a sole lipid source and butyric acid as fatty acid supporting the growth medium. An initial pH value of the culture medium of 6.0 and a temperature of 35° C gave the highest lipolytic activity.     

Freeze or dehydrate: only two options for the survival of subzero temperatures in the arctic enchytraeid<Emphasis Type="Italic"> Fridericia ratzeli</Emphasis>

Hygrophilic soil animals, like enchytraeids, overwintering in frozen soil are unlikely to base their cold tolerance on supercooling of body fluids. It seems more likely that they will either freeze due to inoculative freezing, or dehydrate and adjust their body fluid melting point to ambient temperature as has been shown for earthworm cocoons and Collembola. In the present study we tested this hypothesis by exposing field-collected adult Fridericia ratzeli from Disko, West Greenland, to freezing temperatures under various moisture regimes. When cooled at –1 °C min^–1 under dry conditions F. ratzeli had a mean temperature of crystallisation (T_c) of –5.8 °C. However, when exposed to temperatures above standard T_c for 22 h, at –4 °C, most individuals (90%, n= 30) remained unfrozen. Slow cooling from –1 °C to –6 °C in vials where the air was in equilibrium with the vapour pressure of ice resulted in freezing in about 65% of the individuals. These individuals maintained a normal body water content of 2.7–3.0 mg mg^–1 dry weight and had body fluid melting points of about –0.5 °C with little or no change due to freezing. About 35% of the individuals dehydrated drastically to below 1.1 mg mg^–1 dry weight at –6 °C, and consequently had lowered their body fluid melting point to ca. –6 °C at this time. Survival was high in both frozen and dehydrated animals at –6 °C, about 60%. Approximately 25% of the animals (both frozen and dehydrated individuals) had elevated glucose concentrations, but the mean glucose concentration was not increased to any great extent in any group due to cold exposure. The desiccating potential of ice was simulated using aqueous NaCl solutions at 0 °C. Water loss and survival in this experiment were in good agreement with results from freezing experiments. The influence of soil moisture on survival and tendency to dehydrate was also evaluated. However, soil moisture ranging between 0.74 g g^–1 and 1.15 g g^–1 dry soil did not result in any significant differences in survival or frequency of dehydrated animals even though the apparent wetness and structure of the soil was clearly different in these moisture contents.Abbreviations DW dry weight - FW fresh weight - MP melting point - RH relative humidity - Tc crystallisation temperatures - WC water contentCommunicated by I.D. Hume     

Hydrolysis of animall fats by lipase at temperatures below their melting points

Summary We have studied the hydrolysis of high melting animal fats by the lipase fromCandida rugosa at temperatures between 20°C and 37°C without the addition of surfactants or organic solvents. To establish the practical applications of this process we investigated the optimal conditions of the reaction at high substrate concentrations (50% fat w/v) to achieve 95% hydrolysis (or better) in 24 hours. Experiments were conducted in solid emulsions without constant stirring (500 ml total reaction volume). Under all conditions tested, edible pork lard was a better substrate than inedible beef tallow yielding up to 96% hydrolysis with as low as 0.3 g lipase/Kg fat or 98% hydrolysis with 0.5 g lipase/Kg fat. The optimum temperature for the hydrolysis of edible pork lard was around 30°C. Inedible beef tallow and pork lard did not exhibit a clear optimum temperature. Inedible lard gave results intermediate between those of edible lard and inedible beef tallow.     

Extracellular lipolytic activity in Phoma glomerata

Several properties of the lipolytic activity exhibited by the conidial fungus Phoma glomerata were studied. Lipolytic activity in an aqueous buffer medium was measured on triacylglycerol, phosphoglyceride and cholesterol ester under different experimental conditions. The effect of storage temperature on the stability of the hydrolytic activity, and optimal conditions of temperature and time of maximal activity were determined. The optimal conditions for maximal lipolytic activity were found to be 40–50 °C and 1 h. The activity released to the medium by 1 mg cells for 1 h at 40 °C was stated as the enzyme released unit (ERU). The protein fraction of MW > 50 kDa obtained by ultrafiltration of the medium, was active on the three substrates assayed, and it showed a non-specific hydrolytic activity on both the 1- and 2-acyl esters either in the neutral glyceride or in the phosphoglyceride. A protein of M _r approx. 75 kDa was the only one that showed esterase activity. The crude medium, stored at –15 °C, maintained its initial hydrolytic activity on triacylglycerol for at least 42 days, though when it was kept for 10 days at 4 °C, the activity fell to 50%. Kinetic parameters using substrates such as triolein (TO), dipalmitoyl phosphatidylcholine (DPPC) and cholesteryl oleate (ChoO), were comparatively evaluated. The activity of the enzyme in the hydrolysis of TO showed the highest values, whereas the maximal specific activities were less when the enzyme was assayed against DPPC and ChoO.     

Conversion of fat into yeast biomass in protein-containing waste-water

Summary Candida tropicalis S001 was grown on the lipid fraction of a protein-containing waste-water in order to (i) remove fat from the water, and (ii) produre yeast biomass for feed. The yeast cells were separated from the waste-water by sedimentation. Defatted waste-water was used for methane production and gave a yield of a 0.3 m³ methane/kg reduced chemical oxygen demand. The maximum specific growth rate (µ_max) of C. tropicalis growing on waste-water fat at pH 4.0 was 0.35 h^–1; the fat content was decreased from 8 g/l to about 0.1 g/l within 24 h. In continous culture a corresponding reduction was maintained at dilution rates up to 0.36 h^–1. The effect on growth of pH, temperature and CO₂ concentration was studied with triolein as the major carbon source. The µ_max was nearly constant (0.16 h^–1) in the pH and temperature range of 3.2–4.0 and 30°–38° C, respectively; 10% CO₂ was optimal for growth. Growth on triolein resulted in a biomass yield of 0.70 g dry weight/g fat. Offprint requests to: S. Rydin     

Scanning electron microscopic studies of lipase-catalysed esterification catalysis for the synthesis of stearoyl lactate and p-cresyl laurate

The state of three lipases, two from Rhizomucor miehei and one from porcine pancreas, employed in the esterification reactions leading to the preparation of food additive esters were investigated by scanning electron microscopy (SEM). The lipases employed in the synthesis of stearoyl lactic acid and p-cresyl laurate in 10 ml solvent at 40–60 °C in shake-flask experiments and 150 ml in non-polar solvents at 50–60 °C in bench-scale level experiments were compared. All three lipases, which were subjected to high temperatures and non-polar solvents for a prolonged period of incubation of 72–120 h, showed decrease in the compactness when compared to unused lipase. The presence of buffer preserved the activity and compactness and the absence of the same reduced the amount of enzyme per unit area on the support. R. miehei lipase samples subjected to reaction in presence of 0.0004 ml of 0.1 M buffer/mg enzyme preparation at different pH values (4.0–9.0) showed a decrease in compactness of the enzyme on the surface which correlated to an increase in esterification activity. An increase in volume of buffer (0.0002–0.003 ml/mg enzyme preparation) in the reaction mixture at pH 7.0 showed a decrease in compactness and also a reduction in activity. The studies indicate that a compromise between pH and volume of buffer can lead to variation in the extent of adsorption, distribution and activity, enabling the achievement of maximum conversions in the esterification reactions.     

Production of antibodies against the coenzyme pyrrolequinoline quinone

Rat intestinal epithelial cells were isolated and the activity of the enzyme diacylglycerol lipase (DG lipase, EC 3.1.1.3) was investigated. When cells were treated with Escherichia coli heat-stable toxin (ST) liberation of endogenous glycerol and fatty acids was observed. The enzyme responsible for this effect could be demonstrated to be a DG lipase by using specific substrates. It was found that the activity of DG lipase was increased 5–6-fold with the substrates diolein and 1,2-dioleyl-rac-glycerol and triolein being neutral lipid insensitive to DG lipase. ST had no direct effect on the DG lipase. The enzyme DG lipase was activated via a chain reaction due to the hydrolysis of phosphatidylinositol (PI) by the enzyme PI-specific phospholipase C stimulated by ST.     

Purification of lipase from Cunninghamella verticillata and optimization of enzyme activity using response surface methodology

The fungus Cunninghamella verticillata was selected from isolates of oil-mill waste as a potent lipase producer as determined by the Rhodamine-B plate method. The lipase was purified from C. verticillata by ammonium sulphate fractionation, ion exchange chromatography and gel filtration. The purified enzyme was formed from a monomeric protein with molecular masses of 49 and 42 kDa by SDS–PAGE and gel filtration, respectively. The optimum pH at 40 °C was 7.5 and the optimum temperature at pH 7.5 was 40 °C. The enzyme was stable between a pH range of 7.5 and 9.0 at 30 °C for 24 h. The enzyme activity was strongly inhibited by AgNO₃, NiCl₂, HgCl₂, CdCl₂ and EDTA. However, the presence of Ca²⁺, Mn²⁺ and Ba²⁺ ions enhanced the activity of the enzyme. The activity of purified lipase with respect to pH, temperature and salt concentration was optimized using a Box–Behnken design experiment. A polynomial regression model used in analysing this data, showed a significant lack of fitness. Therefore, quadratic terms were incorporated in the regression model through variables. Maximum lipase activity (100%) was observed with 2 mM CaCl₂, (pH 7.5) at a temperature of 40 °C. Regression co-efficient correlation was calculated as 0.9956.     

Continuous interesterification of butteroil and conjugated linoleic acid in a tubular reactor packed with an immobilized lipase

Modified milkfats were produced via interesterification (acidolysis) reactions of butteroil and conjugated linoleic acid (CLA) in a packed bed reactor containing an immobilized lipase preparation from Candida antarctica. The rate expression for the interesterification reaction is of the generalized Michaelis–Menten form. Significant enrichment of butteroil in CLA residues was accomplished at reactor space times (fluid residence times) of 2–4 h at 40–60°C, but the optimum operating temperature was ca. 50°C. Approximately 80–90% of the free CLA fed to the reactor can be converted to its esterified form.     

Studies on anaerobic proteolytic bacteria of Leh,India

Five anaerobic proteolytic bacteria were isolated from water bodies of Leh, India, where the ambient temperature varies from –25 to 25 °C. Isolates showed growth at all temperatures ranging from 5 to 37 °C except SPL-4 and SPL-5 which showed no growth at 5 °C. The cultures could grow and produce proteases on various protein substrates and the yield varied with the substrates. Two of the cultures showed the presence of spores. Acetate was the dominant VFA during hydrolysis of protein substrates.     

Pilot plant scale extraction of alginates from Macrocystis pyrifera 4. Conversion of alginic acid to sodium alginate, drying and milling

The last three steps of the alginate production process were studied:conversion of alginic acid to sodium alginate, drying, and milling. Threemethods were used to follow the conversion reaction: measuring the pH (a) intheethanol-water liquid of the reaction mixture, (b) after dissolving a sample ofthe fiber taken from the reaction mixture, (c) after dissolving the driedsodiumalginate obtained from the reaction. To obtain a neutral dried sodium alginate,in the first method the pH should be adjusted to 9, and in the second the pHshould be adjusted to 8. The best method to control the reaction was todissolvea sample of the fiber and adjust the pH to 8. The best proportion to reach thecritical point, where pH just begins to rise, was 0.25 parts of sodiumcarbonateto 1 part of alginate in the initial dry algae. A pH above 7 may produce abreakdown of the molecule, reducing significantly the viscosity of the finalalginate. Four different temperatures were used to dry the alginate: 50, 60,70,and 80 °C. Drying time to reach 12% moisture ranged from 1.5h at 80 °C to 3 h at 50°C. The best drying temperature was 60 °C for2.5 h. The effect of drying temperature on alginate viscosity wasdependent on the alginate type. Low and medium viscosity alginates were notsignificantly affected, but alginate with high viscosity was reduced by 40 to54% using the temperature range of 60 to 80 °C. A fixed hammermill was used to reduce the particle size of the dried sodium alginate.Particlesize measurements showed that after a first milling the product contained 76%large particles (20–60 mesh) and 24% fine particles (80–120 mesh).After a third milling the product still contained 42.9% large particles. Nosignificant effect was found on alginate viscosity because of the millingsteps.