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HYDROLYSIS OF FISH OIL BY HYPERACTIVATED Rhizomucor 1
miehei IMMOBILIZED BY MULTIPOINT ANION EXCHANGE 2
3
4
Marco Filice2, Marzia Marciello2, Lorena Betancor3, Alfonso V. Carrascosa1, Jose M. 5
Guisan2* and Gloria Fernandez-Lorente 1* 6
7
1: Departament of Microbiology. Instituto de Fermentaciones Industriales. CSIC. 8
C/Juan de la Cierva 3, 2006 CSIC. Madrid. Spain. 9
2: Departament of Biocatalysis. Instituto de Catálisis. CSIC. Campus UAM. Cantoblanco. 10
28049 Madrid. Spain. 11
3: Madrid Institute for Advanced Studies. Campus UAM. Cantoblanco.. Pabellón C 12
Corresponding authors: 13
Prof José M. Guisán / Dr. Gloria Fernández Lorente 14
Instituto de Catálisis. CSIC. Campus UAM-Cantoblanco. 15
28049 Madrid. SPAIN 16
Tel: +34 91 585 48 09 17
E-mail: [email protected] [email protected] 18
ABSTRACT 19
Rhizomucor miehei lipase (RML) is greatly hyperactivated (around 20-25 fold towards 20
small substrates) in the presence of sucrose laurate. Hyperactivation seems to be an 21
intramolecular process because it is very similar for soluble enzymes and covalently 22
immobilized derivatives. The hyperactivated enzyme was immobilized (in the presence 23
of sucrose laurate) on CNBr activated agarose (very mild covalent immobilization 24
through the amino terminal residue), on glyoxyl agarose (intense multipoint covalent 25
immobilization through the region with the highest amount of Lys residues) and on 26
different anion exchangers (by multipoint anionic exchange through the region with 27
the highest density of negative charges). Covalent immobilization does not promote 28
the fixation of the hyperactivated enzyme, but immobilization on Sepharose Q retains 29
the hyper-activated enzyme, even in the absence of detergent. Hydrolysis of fish oils 30
by these hyperactivated enzyme derivatives was 7 fold faster than by covalently 31
immobilized derivatives and 3.5 fold faster than by enzyme hyperactivated on octyl-32
agarose. The open structure of hyperactivated lipase is fairly exposed to the medium 33
and no steric hindrance should interfere with the hydrolysis of large substrates. These 34
new hyperactivated derivatives seem to be more suitable for hydrolysis of oils by RML 35
immobilized inside porous supports. In addition, the hyperactivated derivatives are 36
fairly stable against heat and organic cosolvents. 37
38
Keywords: lipase hyperactivation, fixation of hyperactivated lipases, multipoint 39
interaction with activated supports 40
41
INTRODUCTION 42
Recently, the hydrolysis of fish oils by lipases immobilized on porous supports 43
has been reported (1). Immobilized lipases cannot undergo interfacial activation by 44
interaction with oil or solvent interfaces because oil drops are not able to penetrate 45
inside the porous structure of the catalyst. This lack of interfacial activation can be 46
compensated for by promoting the activation of lipase during its immobilization. 47
Hyperactivation of lipases by the adsorption of lipases on the surface of porous 48
hydrophobic supports already been reported (19 y 21). In this case, the 49
hyperactivation towards small substrates is usually higher than hyperactivation 50
towards large substrates (e.g., oils). The access of large substrates to the enzyme 51
active center can be hindered by the close contact between the open active center and 52
the support surface. 53
On the other hand, several lipases are also hyperactivated with the presence of low 54
concentrations of detergents, even when the active center is fairly well exposed to the 55
reaction medium. In homogeneous aqueous medium, lipases exist in two structural 56
forms, the closed one where a polypeptide chain (lid or flat) isolates the active center 57
from the medium, and the open form where this lid moves and the hydrophobic active 58
center is exposed to the medium (2, 3, 4). This equilibrium may be shifted towards 59
the open form in the presence of detergents that partially cover the hydrophobic 60
active center and make it much more hydrophilic (5). The presence of detergents 61
during the catalytic reaction could interfere with the adsorption of oils on the active 62
center of the immobilized lipase. If the open and active form of lipase promoted by 63
detergents could be fixed after detergent removal, the hyperactivated form of 64
immobilized lipase could be used for the hydrolysis of fish oils. Fixation of these open 65
forms of lipases can be developed on the basis of the distribution of the surface groups 66
of lipases and differences between the open and closed states. In this case, the open 67
structure of the lipase hyperactivated in the presence of an optimal concentration of 68
an optimal detergent could have a very different distribution of negative charges, 69
lysine groups, etc. than the distribution corresponding to the closed structure. This 70
open structure generated in the presence of detergents could be fixed via multipoint 71
physical or chemical immobilization. The immobilized fixed open structure of lipase 72
could then be used in the absence of detergents. 73
The release of omega 3 (e.g., eicosapentaenoic acid (EPA) and 74
docosahexaenoic acid (DHA)) from fish oil represents the first key step in the 75
preparation of highly enriched triglycerides (70 to 90% of content in one or both 76
polyunsaturated fatty acids, PUFAs). These triglycerides have been described as 77
excellent functional ingredients (6). Recently, there has been a dramatic surge in 78
interest among health professionals in the beneficial effects of omega-3 fatty acids 79
derived from fish oils, mainly consisting of EPA and DHA. DHA is required in high levels 80
in the brain and retina as a physiologically essential nutrient to provide for optimal 81
neuronal functioning (learning ability, mental development) and visual acuity in the 82
early stages of life (7). On the other hand, EPA is considered to have beneficial effects 83
in the prevention of cardiovascular diseases in adults (8,9). In this way, the 84
preparation of triglycerides enriched in both of the omega 3 acids (DHA and EPA) or in 85
only one of them could be very interesting. The first key step for the production of 86
triglycerides of omega 3 is the rapid and selective release of polyunsaturated fatty 87
acids from fish oils. 88
Rhizomucor miehei lipase exhibits interesting catalytic properties for the 89
hydrolysis of sardine oil. In addition to a good hydrolytic activity, RML exhibits a good 90
specificity towards EPA (eicosapentaenoic acid) compared with DHA (docosahexaenoic 91
acid), with an 80 % purity in EPA during the initial stages of release of both omega-3 92
acids. Improvement in the activity and/or selectivity could be quite interesting in order 93
to produce very pure omega-3 acids (1). 94
This work studies the hyperactivation of RML by different concentrations of 95
different detergents. Then, the fixation of the most active open form was attempted 96
via intense multipoint anion exchange or intense multipoint covalent attachment. The 97
activity and selectivity of the immobilized and hyperactivated RML were finally 98
evaluated for the hydrolysis of sardine oil. 99
100
101
102
103
104
105
106
107
MATERIALS AND METHODS 108
Materials 109
Sucrose laurate was a generous gift from the Mitsubishi-Kagaku Food 110
Corporation (cat. No. C-1216). Triton® X-100 (TX) was obtained from Sigma. 1,4-111
Dioxane and p-nitrophenyl butyrate (p-NPB) were purchased from Fluka. Octyl 112
sepharoseTM, Q-sepharose, CNBr activated Sepharose 4B (CNBr-agarose) and inert 113
agarose (Sepharose 4B) were purchased from GE Healthcare. The enzyme from 114
Rhizomucor miehei was kindly donated by Novozymes (Palatase 2000L). Sardine oil was 115
a kind gift from BTSA (Madrid, Spain). Docosahexaenoic acid (DHA), eicosapentaenoic 116
acid (EPA) and sodium borohydride (NaBH4) were obtained from Sigma Chemical Co. 117
(St. Louis, USA). Other reagents and solvents used were of analytical or HPLC grade. 118
MANAE y PEI. 119
120
Methods 121
Enzymatic activity assay 122
The activities of the soluble lipases and their immobilized preparations were 123
analyzed spectrophotometrically by measuring the increase in absorbance at 348 nm 124
( = 5150 M-1cm-1) produced by the release of p-nitrophenol (pNP) in the hydrolysis of 125
0.4 mM pNPB in 25 mM sodium phosphate buffer at pH 7 and 25°C. To initialize the 126
reaction, 0.05-0.2 ml of lipase solution (blank or supernatant) or suspension was added 127
to 2.5 ml of substrate solution. Enzymatic activity is given as μmol of pNP produced per 128
minute per mg of enzyme (IU) under the conditions described above. 129
130
131
132
Hyperactivation of RML performed by different detergents 133
To a solution of crude Palatase, (1 ml of crude extract - 1.6 mg of RML - diluted with 19 134
ml of 25 mM NaH2PO4 buffer solution at pH 7.0) various concentrations of different 135
detergents (Triton X-100, Sucrose laurate and CTAB) were added and the activity was 136
periodically checked by the enzymatic activity assay described above. 137
138
Immobilization of RML 139
Usually, the enzyme was incubated with the desired support, and a similar 140
suspension was prepared under identical conditions but using inert agarose. Samples 141
of the suspensions were withdrawn using cut pipette tips, and samples of the 142
supernatants were taken using a filter pipette tip. 143
To perform immobilization and stability studies, each preparation was loaded 144
with 2 mg/g of pure RML in order to prevent diffusion problems. In the enzymatic 145
hydrolysis, highly loaded derivatives (up to 10 mg/g) were prepared. 146
147
Immobilization of RML on octyl-Sepharose 148
A volume of 1.5 ml of Palatase commercial solution (6,5 mg total protein/ml, about 1,6 149
mg RML as determined by Bradford’s assay) (10) were mixed with 30 ml of 10 mM 150
sodium phosphate at pH 7.0 and 4ºC, and then 1 g of octyl-Sepharose previously 151
equilibrated with the immobilization buffer was added. The supernatant and 152
suspension activities were periodically checked by the method above described. After 153
immobilization, the enzyme derivative was recovered by filtration under vacuum. 154
These adsorbed lipases were used as biocatalysts or to purify RML. 155
156
Desorption of the RML from the octyl-Sepharose with sucrose laurate 157
To obtain a pure lipase, RML was desorbed from the RML-octyl-Sepharose; 1 g 158
of this immobilized preparation was suspended in 10 ml of 0.5% (v/v) sucrose laurate 159
in 25 mM NaH2PO4 buffer solution at pH 7.0 for 1 h. The progress of the desorption 160
was monitored by periodically checking the enzymatic activity of the supernatant and 161
suspension until they became equal. The final concentration of the purified lipase 162
solution was 0.2 mg lipase/ml. The enzymatic solution obtained was then used for 163
immobilization of the different supports, when a pure enzyme was required. 164
165
Immobilization of lipases on different ionic supports 166
Standard studies were performed as previously described. Then, 1 g of different 167
ionic exchanger supports (MANAE (11), Q-Sepharose or PEI(12)) equilibrated with the 168
immobilization buffer were added to the pure RML solution obtained as described 169
above (about 2 mg in 10 ml), and the pH was adjusted to 7. The mixture was then 170
stirred at 25ºC. To finalize the immobilization, the supernatant was removed by 171
filtration and the supported lipase was washed several times with distilled water. 172
173
174
Immobilization of lipase on a CNBr-activated support 175
These support and immobilization conditions were used as reference 176
conditions for lipase behavior. In general, immobilization of enzymes under these 177
conditions will occur by only a few bonds (very likely even just one bond), and these 178
immobilized preparations result in a good model of the enzyme properties in absence 179
of intermolecular phenomena (13-16). Lipases have been shown to exhibit a strong 180
tendency to form lipase-lipase aggregates, making it very complex to study isolated 181
lipase molecules in a soluble form (13-16). 182
Commercial CNBr activated Sepharose support was activated prior to use by its 183
suspension in an acidic aqueous solution (pH 2-3) for one hour. Then, the support was 184
dried by filtration under vacuum. Once activated, 1 g of CNBr-Sepharose was added to 185
15 ml of the purified lipase solution (0,2 mg/ml). The mixture was then stirred at 4ºC 186
and 250 rpm for 20 minutes. After that, the solution was removed by filtration, the 187
supported lipase was washed twice with 100 mM NaHCO3 at pH 8 and then re-188
suspended in 15 ml of 1 M ethanolamine at pH 8 for 90 minutes to block the unreacted 189
imido carbonate reactive groups (17). Subsequently, the reaction mixture was filtered 190
and washed with abundant distilled water. The immobilization yield was 60% with a 191
protein loading amount of about 2 mg/g support. Following immobilization, the 192
enzymatic activity assay described above was performed. 193
194
Immobilization of RML on glyoxyl-agarose 195
Glyoxyl agarose support (1 g) (18) was added to 13 ml of RML solution (0.2 mg of 196
enzyme/ml) purified as described above. Immobilization was carried out at pH 10.2 197
over 24 h at 25 ºC under very gentle stirring. To finalize the immobilization reaction, 198
solid NaBH4 was added to the suspension at 1 mg/ml and the suspension was gentle 199
stirred for 30 minutes. Borohydride reduces the Schiff’s bases formed between the 200
enzyme and the support and the unreacted aldehyde groups remaining in de support. 201
Subsequently, the suspension was filtered and the glyoxyl derivative was washed with 202
abundant distilled water. The percentage of immobilization was 60% with about 2 203
mg/g support. The immobilization was followed by the enzymatic assay described 204
above. 205
206
Thermal inactivation of different RML immobilized derivatives. 207
The different RML derivatives loaded at low levels (0.5 mg of enzyme/g of 208
support) were incubated in 25 mM sodium phosphate at pH 7.0 and 50ºC. Samples 209
were withdrawn periodically and their activities were measured using the pNPB assay. 210
The thermal stability of glyoxyl derivatives was studied with an enzymatic hydrolytic 211
assay modified by adding 0.3% of Triton X-100 in the cuvette. The experiments were 212
carried out in triplicate and error was never more than 5%. 213
214
Stability of different RML immobilized preparations in organic solvents 215
The different RML preparations were incubated in 25 mM sodium phosphate 216
at pH 7.0 and 50% of diglyme or isopropanol at 25 ºC. Samples were periodically 217
withdrawn and their activities were checked with the enzymatic activity assay 218
described above. The stability of glyoxyl derivatives was studied with an enzymatic 219
hydrolytic assay modified by adding 0.5% of sucrose laurate in the cuvette. The 220
experiments were carried out in triplicate and the error was never more than 5%. 221
222
Hydrolysis of Fish Oil by immobilized lipases 223
Hydrolysis of fish oil was performed in a water-organic two-phase system. The 224
procedure was as follows: 4.5 ml of cyclohexane, 5 ml of phosphate buffer (0.1 M) at 225
pH 6, and 0.5 ml of sardine oil were placed in a reactor and preincubated for 30 min. 226
The reaction was then initiated by adding 0.3 g of lipase derivative and shaking at 150 227
rpm. A Mettler Toledo DL50 Graphix titrator was used to maintain a constant pH value 228
during the reactions. The concentration of polyunsaturated free fatty acids was 229
determined at various times by HPLC assay. 230
231
Analysis of Polyunsaturated free fatty acids (PUFAS) by HPLC 232
After 10 minutes, 0.1 ml aliquots of the organic phase were withdrawn and dissolved 233
in 0.8 ml of acetonitrile. The unsaturated fatty acids produced were analyzed by RP-234
HPLC (Spectra Physic SP 100 coupled with an UV detector Spectra Physic SP 8450) 235
using a Kromasil C8 column (15 cm × 0.4 cm). Products were eluted at a flow rate of 236
1.0 ml/min using an acetonitrile-10 mM ammonium Tris buffer at pH 8 (70:30, v/v), 237
and UV detection was performed at 215 nm. The retention times for the unsaturated 238
fatty acids were: 9.4 min for EPA and 13.5 min for DHA. 239
240
Determination of Hydrolysis Conversion 241
The percent hydrolysis was computed as the amount of EPA and DHA (PUFAS) released 242
as a percentage of their original content in the oil, considering that the PUFAS content 243
in the fish oil was 30%. The percent of peak area in an experiment was assumed to 244
indicate the percent content of the corresponding compound. PUFAS productivity (%) 245
was calculated according to the following equation: 246
PUFAS (g/min)= PUFAS (%) X fish oil (g/ml), 247
In which fish oil content was the weight of the fish present in the substrate mixture. 248
249
RESULTS 250
251
1. Hydrolysis of a small substrate (pNPB) by soluble RML in the presence of 252
detergents. 253
The presence of several detergents during the hydrolytic assay exerts very different 254
effects on the catalytic activity of soluble RML (Figure 1). Some detergents (e.g., CTAB) 255
promote a strong inhibition even at very low concentrations (0.001%). The presence 256
of TRITON X-100 promotes a small hyperactivation at very low concentrations (0.01%) 257
but exerts inhibitory effects at higher concentrations (0.1% or higher). Sucrose laurate 258
exerts a remarkable hyperactivating effect: the enzyme is 10-fold more active in the 259
presence of 0.4% of this detergent than in the reference assay in the absence of 260
detergents. This hyperactivation of RML is similar to that obtained for the same 261
enzyme adsorbed on octyl agarose (8-10 fold more active than soluble RML) (19). 262
2. Long-term Incubation of soluble RML in the presence of detergents. 263
In order to study the kinetics of hyperactivation as well as to avoid possible inhibiting 264
effects of the presence of high concentrations of detergents in the enzymatic assay, 265
the hyperactivation of RML was also studied by incubating the soluble enzyme in the 266
presence of detergents outside the reaction cell. The catalytic activity of soluble RML 267
increased over 1 hour (figure 2), at which point the concentration of detergent in the 268
assay mixture was almost negligible (lower than 0.01%). The observed activities were 269
constant for 5-10 minutes. Hyperactivation was faster and more intense when using 270
high concentrations of detergent. RML incubated In the presence of 0.5 % sucrose 271
laurate for 30 minutes exhibits a 25-fold increase in activity. This hyperactivation was 272
much greater than that observed in the reaction cell. The enzyme was then 273
hyperactivated for longer incubation times and was assayed in the absence of 274
detergent. The hyperactivation was moderately slow, stable and very high. Similar 275
experiments were conducted with TRITON X-100, in which a 7-fold hyperactivation was 276
observed, also much greater than the hyperactivation previously observed when 277
detergent was added to the reaction cell. 278
279
3. Hyperactivation of RML immobilized on CNBr activated agarose. 280
The mild immobilization of enzyme on CNBr activated agarose conducted here (for 15 281
minutes at 4 ºC) strongly reduces any possibility of multipoint covalent attachment. In 282
fact, these immobilized derivatives of a number of enzymes have activity-stability 283
properties that are very similar to those of the corresponding pure and diluted soluble 284
enzymes in the absence of stirring (17). However, one-point covalently immobilized 285
derivatives fully dispersed on the internal support surface cannot undergo interactions 286
with hydrophobic interfaces (air, oil, solvents) and cannot undergo any kind of 287
intermolecular process (aggregation, proteolysis, etc.) (20). These RML derivatives 288
were hyperactivated similarly to soluble RML (Figure 3). These derivatives were 289
hyperactivated 20-fold in the presence of 0.5 % sucrose laurate. The subsequent 290
washing of the derivatives, done in order to remove the detergent, promoted a slow 291
and complete loss of hyperactivation. This slow and high level of hyperactivation 292
seems to be an intramolecular process that is completely reversible. 293
294
4. Sucrose laurate hyperactivation of RML adsorbed on octyl-agarose. 295
RML was selectively adsorbed and hyperactivated by adsorption on octyl-agarose (an 296
8-10 fold hyperactivation). The adsorbed enzyme could be desorbed away from the 297
support by washing the derivatives with 0.5 % sucrose laurate. The desorbed enzyme 298
was immediately hyperactivated by up to a factor of 20 (very similar to the slow 299
hyperactivation of the soluble enzyme). Hyperactivation by detergent is higher but 300
compatible with the hyperactivation on hydrophobic supports, but full hyperactivation 301
is much more rapid. 302
303
304
5. Immobilization of hyperactivated RML on different activated supports. 305
Hyperactivated soluble RML (purified on octyl-agarose and desorbed away with 0.5 % 306
sucrose laurate) was immobilized using 3 different immobilization protocols (TABLE 1). 307
In protocol a, mild immobilization was performed on CNBr-activated agarose (very 308
likely a one-point immobilization through the most reactive amino group, e.g., the 309
terminal amino group). The enzyme preserved its hyperactivation following 310
immobilization, but this hyperactivation was completely lost when the derivative was 311
washed and the detergent was removed at the end of immobilization. In protocol b, 312
immobilization was performed on highly activated glyoxyl agarose at pH 10 (multipoint 313
covalent attachment through the enzyme region with the highest amount of Lys 314
residues (18). The enzyme lost 50% of its hyperactivation during immobilization and 315
lost 100% after the washing away of derivatives and removal of the detergent at the 316
end of immobilization. In protocol c, the enzyme was physically adsorbed on 317
Sepharose Q (multipoint anion exchange via the enzyme region having the highest 318
density of net negative charge). The enzyme preserved more than 90% of its 319
hyperactivation, and this level of hyperactivation was maintained even after the 320
complete removal of the detergent and after incubation of the derivative for several 321
hours in the absence of detergent. This multipoint anionic exchange allows the 322
fixation, in the absence of detergent, of the hyperactivated form of the enzyme that 323
was previously activated in the presence of 0.5 % sucrose laurate. 324
6. Immobilization of hyperactivated RML on different anion exchangers. 325
A similar fixation of the hyperactivated structure of the enzyme was also attempted 326
using different anion exchangers: ionic exchangers containing a very high 327
concentration of ionized primary and secondary amino groups (MANAE-agarose) (11) 328
and very highly activated polymeric exchangers obtained by chemical modification of 329
aldehyde-agarose with polyethyleneimine (PEI-agarose) (12). In both cases, the 330
hyperactivation was partially maintained (at 50%) and the final results of 331
hyperactivation, evaluated in the absence of detergent, were similar to those obtained 332
by adsorption on hydrophobic octyl-agarose (Table 2). 333
7. Stability of derivatives of hyperactivated RML. 334
The three derivatives where the hyperactivated form of RML was fixed were very 335
stable under mild experimental conditions. For example, they maintained 100% of 336
their activity after incubation for 3 weeks at 25 ºC and pH 7.0. The stability of the 337
derivatives was different under more severe conditions. At 37 ºC, the most stable 338
derivative was RML-Sepharose Q (Figure 4), which preserved 80 % of its activity (20-339
fold enhanced compared with soluble enzyme) after a 24 hr incubation. On the 340
contrary, in the presence of cosolvents (e.g., 30 % of diglyme), RML-Sepharose Q was 341
the least stable. 342
343
8. Hydrolysis of fish oil by different derivatives of RML. 344
The hydrolysis of sardine oil was performed using RML-CNBr-Sepharose, RML-octyl 345
Sepharose and hyperactivated RML-Sepharose Q derivatives (TABLE 3). RML 346
hyperactivated on octyl-Sepharose was 2-fold more active than non-hyperactivated 347
RML immobilized on CNBr Sepharose. This increase was 9.5-fold for the hydrolysis of 348
small substrates (e.g., pNPB). The hyperactivated RML-Sepharose Q was 7-fold more 349
active for oil hydrolysis than non hyperactivated RML-CNBr-agarose and 3.5-fold more 350
active than RML hyperactivated on hydrophobic supports. In this case, the difference 351
was also lower than that obtained using small substrates (an 18-20-fold increase for 352
pNPB when using CNBr agarose derivatives). The EPA/DHA selectivity of these new 353
hyperactivated derivatives could make them attractive for industrial application, for 354
example, allowing the production of 3:1 EPA:DHA mixtures from sardine oil hydrolysis. 355
This hyperactivation of RML is especially important given that once it is immobilized 356
inside porous supports, RML cannot undergo interfacial activation towards drops of oil 357
or drops of solvents containing oil because these drops are unable to penetrate inside 358
the porous structure of the catalyst. 359
360
DISCUSSION 361
The 20-25-fold hyperactivation obtained for soluble or immobilized RML in the 362
presence of high concentrations of sucrose laurate is one of the highest 363
hyperactivations obtained for lipases via non-natural methods (different from 364
interfacial activation on drops of oil): TLL was hyperactivated 20-fold by adsorption on 365
hydrophobic supports (21), BTL was hyperactivated 2-fold in the presence of 366
detergents (22), BTL was hyperactivated 3-fold in the presence of cosolvents (22), and 367
BTL was hyperactivated 3-fold via site-directed chemical modification (23). 368
Furthermore, BTL was hyperactivated 18-fold by the additive effects of chemical 369
modification, detergents and cosolvents (22), etc. However, the experiments reported 370
in this paper represent the first trial in which hyperactivation by detergents was 371
induced outside of the reaction cell and was studied over a long period of time. Similar 372
experiments could likely give similar interesting results with other lipases. However, at 373
the moment, an additional hyperactivation during the desorption by detergents of 374
lipases adsorbed and hyperactivated on hydrophobic supports had never been 375
observed. Hyperactivations on both hydrophobic supports and in the presence of 376
detergents seem to be related to the opening of the lipase active center. This large 377
hydrophobic pocket of the open form of lipases may be stabilized by adsorption on 378
hydrophobic supports and by interaction with the hydrophobic moiety of the 379
detergent. However, in the case of RML, the detergent seems to be more effective 380
than hydrophobic surfaces, and the new active structure of RML could be slightly 381
different from the structure formed on hydrophobic interfaces. 382
383
The fixation of the hyperactivated form of RML by multipoint anion exchange of 384
Sepharose Q is quite interesting. The immobilized enzyme remains hyperactivated 385
after removing the hyperactivating agent (the sucrose laurate). A similar fixation is not 386
possible by very mild (possibly one-point) covalent immobilization on CNBr-activated 387
agarose. Furthermore, the hyperactivated form of the enzyme is not fixed by covalent 388
immobilization on glyoxyl-agarose (multipoint attachment through the enzyme region 389
with the highest amount of Lys). This region seems to be unaltered between the 390
closes and hyperactivated forms of the enzyme. On the contrary, the region with the 391
highest density of net negative charge (involved in the adsorption on Sepharose Q and 392
other anionic exchangers) seems to be dramatically changed when the closed form of 393
the lipase in transformed into the hyperactivated open form. Logically, this region 394
with the highest negative charge is different from the enzyme active center, which is in 395
a large hydrophobic pocket. One important finding from this work is that a complex 396
change in the active center may be associated with a dramatic change in other regions 397
of the enzyme, and the fixation of the associated change preserves the first and most 398
important change in the active center. This type of long-distance stabilization of 399
conformational changes in active centers of enzymes (namely lipases) has not been 400
previously reported in the literature. 401
These results also showed a 7-fold improvement of the hydrolytic activity of 402
RML towards fish oil with a significant selectivity towards EPA versus DHA. This allows 403
for the rapid production of mixtures of omega-3 acids fairly enriched in EPA via 404
enzymatic methods. This system would allow for the exploitation of all of the 405
advantages of lipases immobilized on porous supports: re-use of the biocatalyst, 406
resistance to strongly stirred reactors because of the lack of interaction of hydrophobic 407
interfaces with air, solvents, oils, etc., and resistance to intermolecular phenomena 408
such as aggregation and proteolysis. Additionally, the main drawback of these reaction 409
systems, the absence of interfacial activation on oil drops, is compensated for by the 410
hyperactivation of immobilized derivatives. 411
The hyperactivated RML derivatives are very stable under the mild 412
experimental conditions (e.g., pH 7-0 and 5 ºC) required to hydrolyze fish oil in the 413
absence of undesirable oxidations of omega 3. Therefore, these hyperactivated 414
derivatives could be used for fish oil hydrolysis for a number of reaction cycles. Under 415
more harsh experimental conditions, the derivatives are less stable. The presence of a 416
high concentration of quaternary amino groups on the supports may fix distorted 417
enzyme structures formed under distorting conditions (high temperatures, cosolvents, 418
etc.). The distorted enzyme could interact more with the highly activated support. 419
420
CONCLUSIONS 421
RML was 20-fold hyperactivated (towards small substrates) by incubation in the 422
presence of high concentrations (0.4%) of sucrose laurate. Hyperactivation was 423
intermolecular, slow, moderately stable and completely reversible. Hyperactivation is 424
likely related to the stabilization of the large hydrophobic pocket exposed to the 425
medium in the hyperactivated form of RML. 426
The hyperactivated form of RML was successfully fixed by multipoint adsorption on 427
anionic exchangers and is stabilized even after removing hyperactivating agents (the 428
detergent). The fixed region is not the hydrophobic active center. A clear correlation 429
between the hydrophobic active center and the region with the highest density in net 430
negative charge may be responsible for the stabilization of the hyperactivated form of 431
RML. 432
RML immobilized inside porous supports becomes very active, very stable and fairly 433
selective for the mild hydrolysis of fish oils (25 ºC and pH 7.0) in the absence of 434
undesirable phenomena such as interaction with interfaces and aggregation 435
phenomena. Now, interfacial activation of soluble lipases on drops of oil is not 436
necessary since a similar activation was achieved via a careful non-natural 437
hyperactivation of the immobilized enzyme. 438
439
Acnowledgements 440
This work has been sponsored by the Spanish Ministry of Science and 441
Innovation (project AGL-2009-07625) and the Comunidad Autónoma de Madrid 442
(Project S0505/PPQ/03449). We gratefully recognize to Spanish Ministry of Science 443
and Innovation for “Ramón y Cajal” contract to Dr. Fernandez-Lorente.. 444
445
446
FIGURE LEGENDS 447
Figure 1. Hydrolysis of p-nitrophenyl butyrate in the presence of different 448
concentrations of detergents by soluble RML. Experiments were carried out as 449
described in the Methods section. The activity of the enzyme assayed in the absence 450
of detergents is assigned as 100%. Squares: Hexadecyltrimethylammonium bromide 451
(CTAB); triangles: TRITON X-100; circles: sucrose laurate. 452
453
Figure 2. Time-courses of the hyperactivation of soluble RML incubated in the 454
presence of different concentrations of sucrose laurate. Experiments were carried 455
out as described in the Methods section. The enzyme was incubated in the presence of 456
detergents and aliquots of the incubation mixtures were assayed in the presence of 457
minimal traces of detergent (less than 0.01%). The activity of the enzyme incubated in 458
the absence of detergent was assigned as 100%. Triangles: RML incubated in 0.1 % 459
sucrose laurate; squares: RML incubated in 0.2 % sucrose laurate; circles: RML 460
incubated in 0.5 % sucrose laurate. 461
462
Figure 3. Reversible hyperactivation of immobilized RML incubated in the presence 463
of 0.5% sucrose laurate. RML was very mildly immobilized on CNBr-activated agarose 464
gels. Column 1: activity of immobilized RML before incubation in the presence of 465
detergent; Column 2: activity of immobilized RML after incubation for 1 hour in the 466
presence of 0.5 % sucrose laurate; Column 3: activity of immobilized RML after a final 467
buffer wash that was performed in order to remove the detergent. 468
Figure 4. Time-courses of the thermal inactivation of different RML derivatives 469
(hyperactivated enzyme adsorbed on different anion exchangers). Derivatives were 470
incubated at 37 ºC and pH 7.0. Squares: hyperactivated RML adsorbed on MANAE-471
agarose; triangles: hyperactivated RML adsorbed on PEI-agarose; circles: 472
hyperactivated RML adsorbed on Sepharose Q. 473
474
Figure 5. Time-course of cosolvent inactivation of different RML derivatives 475
(hyperactivated enzyme adsorbed on different anion exchangers Derivatives were 476
incubated in the presence of 30% of diglyme at pH 7.0 and 25 ºC. Squares: 477
hyperactivated RML adsorbed on MANA-agarose; triangles: hyperactivated RML 478
adsorbed on PEI-agarose; circles: hyperactivated RML adsorbed on Sepharose Q. 479
480
481
REFERENCES 482
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486
2. Brady L, Brzozowski AM, Derewenda ZS, Dodson E, Dodson G, Tolley S, Turkenburg, 487
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490
3. Brzozowski, AM, Derewenda, U., Derewenda, Z.S., Dodson, G.G., Lawson, 491
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499
5. Fernández-Lorente G, Palomo JM, Cabrera Z, Fernandez-Lafuente R, Guisán JM 500
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13. Wilson L, Palomo - -533
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540
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Lafuente R (2005) Lipase-lipase interactions as a new tool to immobilize and modulate 542
the lipase properties. Enzyme Microb Technol 36: 447-454. 543
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578
579
580
581
582
Table 1.- Immobilization of hiperactivated RML on different activated 583
supports. Experiments are described in Methods. Relative activities are 584
reported using 100% as the activity of the soluble enzyme before 585
hyperactivation and immobilization. 586
587
588
589
590
591
592
593
594
595
596
Steps Relative activity (%)
Soluble enzyme 100
Adsoption to Octyl-sepharose 950
Desortion with 0.5% lauryl
sucrose 2000
CNBr-
Sepharose
Q-
Sepharose
Glyoxyl-
agarose
Immobilization on different
supports 1800 1880 1200
Immobilized derivatives after
washing and removing the
detergent
100 1800 100
597
598
Table 2.- Immobilization of hiperactivated RML on different anion-599
exchange supports. Experiments are described in Methods. Relative 600
activities are reported using 100% as the activity of the soluble enzyme 601
before hyperactivation and immobilization. 602
603
604
605
606
607
608
Steps Relative activity (%)
Soluble enzyme 100
Adsoption to Octyl-sepharose 950
Desortion with 0.5% lauryl sucrose 2000
Sepharose-
Q MANAE PEI
Adsorption on Anion Exchange
Resins 1880 900 800
Immobilized derivatives after
washing and removing the
detergent
1800 900 800
Table 3.- Hydrolysis of sardine oil catalyzed by different derivatives of 609
RML. Experiments were carried out as described in Methods. 610
611
Activitya represents the rate of hydrolysis of a small synthetic substrate (p-612
nitrophenyl butyrate). Activityb represents the rate of hydrolysis of sardine 613
oil. In both cases, 100% is the activity of derivative obtained by very mildly 614
immobilization on CNBr-activated Sepharose. EPA/DHA is the ration 615
between both omega 3 released in the first stages of hydrolysis of sardine 616
oil (up to a 10% of conversion). ω-3/oleic plus palmitic acid is the ration 617
between both omega3 and saturated and monounsaturated acids 618
obtained in the first stages of hydrolysis of sardine (up to a 10% of 619
conversion) 620
621
622
623
624
625
626
627
628
629
Derivative Activitya (%) Activity b 10-3 EPA/DHA
-3/Oleic
plus palimitic
acids
CNBr- 100 100 2.6 1.4
OCTIL 950 200 3.45 0.89
Q 2000 700 4.2 1.06
0
200
400
600
800
1000
1200
0 0,1 0,2 0,3 0,4 0,5
Re
lati
veac
tivi
ty(%
)
Detergent (%)
Figure 1
630 631
632
633
634
635
636
637
638
639
640
641
642
643
644
645
646
647
Figure 2
648 649
650
651
652
653
654
655
656
657
658
659
660
661
0
200
400
600
800
1000
1200
1 2 3
Re
lati
ve a
ctiv
ity
(%)
662
Figure 3 663
664
665
666
667
668
669
670
671
Figure 4
672 673
674
675
676
677
678
679
680
681
682
683
684
685
686
687
688
689
Figure 5
690 691