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TRANSCRIPT
Filling the void: Introducing aromatic interactions into solvent tunnels towards 1
lipase stability in methanol 2
3
Shalev Gihaz1, Margarita Kanteev1, Yael Pazy2 and Ayelet Fishman1# 4
5
1Department of Biotechnology and Food Engineering, Technion-Israel Institute of 6
Technology, Haifa, 3200003, Israel 7
2Technion Center for Structural Biology, Lorry I. Lokey Center for Life Sciences and 8
Engineering, Technion-Israel Institute of Technology, Haifa, 3200003, Israel 9
10
Running head: Tunnel engineering for lipase methanol stability 11
12
#Address correspondence to Ayelet Fishman: Department of Biotechnology and Food 13
Engineering, Technion-Israel Institute of Technology, Haifa, 3200003, Israel; 14
[email protected]; Tel (972) 48295898. 15
16
Keywords: Lipase, protein engineering, stability, solvent tunnel, organic solvents, 17
biodiesel. 18
AEM Accepted Manuscript Posted Online 14 September 2018Appl. Environ. Microbiol. doi:10.1128/AEM.02143-18Copyright © 2018 American Society for Microbiology. All Rights Reserved.
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ABSTRACT 19
Enhanced stability in organic solvents is a desirable feature for enzymes implemented 20
under industrial conditions. Lipases potential as biocatalysts is mainly limited by 21
denaturation in polar alcohols. In this study we focused on selected solvent tunnels in lipase 22
from Geobacillus stearothermophilus T6 to improve its stability in methanol during 23
biodiesel synthesis. Using rational mutagenesis, bulky aromatic residues were incorporated 24
in order to occupy solvent channels and induce aromatic interactions leading to a better 25
inner core packing. Each solvent tunnel was systematically analyzed with respect to its 26
chemical and structural characteristics. Selected residues were replaced with Phe, Tyr or 27
Trp. Overall, 16 mutants were generated and screened in 60% methanol, from which 3 28
variants showed elevated stability up to 81-fold compared with wild-type. All stabilizing 29
mutations were found in the longest tunnel detected in the “closed-lid” x-ray structure. 30
Combining the Phe substitutions created double mutant A187F/L360F with an increase in 31
Tm of +7°C in methanol and a 3-fold increase in biodiesel synthesis yield from waste 32
chicken oil. Kinetic analysis with p-nitrophenyl laurate revealed that all mutants displayed 33
lower hydrolysis rates (kcat), though mostly their stability properties determined the 34
transesterification capability. Seven crystal structures of different variants were solved 35
disclosing new π-π or CH/π intramolecular interactions emphasizing the significance of 36
aromatic interactions to improved solvent stability. This rational approach could be 37
implemented in other enzymes for stabilization in organic solvents. 38
IMPORTANCE 39
Enzymatic synthesis in organic solvents holds increasing industrial opportunities in many 40
fields, however, one major obstacle is the limited stability of biocatalysts in such a 41
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denaturing environment. Aromatic interactions play a major role in protein folding and 42
stability and we were inspired by this to re-design enzyme voids. Rational protein 43
engineering of solvent tunnels of lipase from Geobacillus stearothermophilus is presented 44
here, offering a promising approach to introduce new aromatic interactions within the 45
enzyme core. We discovered that longer tunnels leading from the surface to the enzyme 46
active site were more beneficial targets for mutagenesis for improving lipase stability in 47
methanol during biodiesel biosynthesis. Structural analysis of the variants confirmed the 48
generation of new interactions involving aromatic residues. This work provides insights 49
into stability-driven enzyme design by targeting solvent channels void. 50
INTRODUCTION 51
Utilization of enzymes in non-aqueous media has been an ongoing aspiration in 52
synthetic chemistry as such biotransformations exhibit several advantages over 53
conventional aqueous media. Some of the benefits include increased solubility of 54
hydrophobic substrates, elimination of microbial contamination and suppression of water-55
dependent catabolic side reactions (1-4). These advantages become more imperative when 56
combining biological catalysts together with chemo-catalysts to improve yields and 57
efficiency of processes (5). 58
Despite the great interest in biocatalysis in organic solvents, the non-trivial 59
combination of water-based enzymes within non-aqueous media presents many challenges, 60
most importantly, the relatively low stability of enzymes compared to their natural habitat 61
conditions (2, 6, 7). Conformational changes in the enzyme's structure are the main reason 62
for deactivation by organic solvents due to impairment of the hydrophilic-hydrophobic 63
interactions balance. Moreover, polar (hydrophilic) solvents can penetrate the enzyme's 64
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hydrophilic core affecting secondary and tertiary conformational changes in parallel with 65
stripping off structured water molecules from the protein hydration shell (2, 8-15). 66
With the growing understanding on enzymes inactivation mechanisms using both 67
structural and computational tools, came the development of enzyme stabilization 68
techniques in organic solvents such as protein engineering and immobilization (2, 13, 16, 69
17). Protein engineering methods include: (a) random mutagenesis, (b) rational design, and 70
(c) semi-rational design (2, 8, 18-20). It was previously shown that these approaches can 71
be applied separately or in combination to tailor enzymes for enhanced stability in organic 72
solvents (1, 9, 12, 18, 21, 22). 73
Protein engineering by rational design requires structural information, and precise 74
regions for mutagenesis are identified usually by computational tools or prior knowledge 75
(17, 22-24). One recently developed concept for enzyme stabilization in organic solvents 76
is modification of residues buried in tunnels within the protein structure. Globular enzymes 77
are comprised of clefts, pockets, channels and cavities, which offer a unique 78
microenvironment for biological functions, such as ligand binding or enzymatic catalysis. 79
The tunnel properties (diameter, length, hydrophobicity, etc.) may alter substrate 80
specificity or improve organic solvent resistance (2, 25-28). The identification of these 81
networks requires computational engines for detecting cavities and tunnels such as CAVER 82
or MOLE generator along with a known structure or model for the target protein (29-31). 83
The profound work of Damborsky and co-workers on stabilizing haloalkane dehalogenase 84
(DhaA) has demonstrated the potential of saturation mutagenesis of residues found in 85
solvent channels. The random substitutions established in these works revealed the effect 86
of small vs. bulky residues on both the activity and stability of DhaA (32, 33). 87
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Lipases have a long history of utilization in organic solvents (34, 35). They are 88
ubiquitous hydrolytic enzymes mostly possessing two unique features; (i) 'interfacial 89
activation' phenomenon with enhanced activity generated at an oil-water interphase, and 90
(ii) a helix 'lid' gating the substrate accessibility which exposes the active site towards 91
catalysis (“open/close” conformations) via a conformational change (36). In a micro-92
aqueous environment, lipases carry out synthesis reactions such as transesterification of a 93
wide range of natural and unnatural substrates (36-38) while one common reaction is the 94
synthesis of fatty acid methyl esters (FAMEs) also known as biodiesel (39-41). Biodiesel 95
is a sustainable and renewable alternative for petroleum-based fossils, which can be 96
produced from a wide range of feedstocks (edible and non-edible animal fats and plant 97
oils). In most cases, methanol serves as a second substrate in FAME production (42, 43). 98
Compared with traditional chemical pathways to synthesize FAMEs, enzymatic routes are 99
preferred regarding energy consumption and downstream operations. Lipase efficiency in 100
converting oil feedstocks into biodiesel is mainly restrained by alcohol-induced 101
inactivation, thus, methanol-stable enzymes are desired (10, 44-46). 102
The thermophilic bacterial lipase from Geobacillus stearothermophilus T6 (LipT6), 103
was previously used for biodiesel synthesis and the wild-type recombinant enzyme 104
(LipT6WT) was stabilized towards methanol by protein engineering (47, 48). LipT6WT 105
crystal structure (PDB 4X6U) revealed tight side-chain packing and a relatively rigid 106
structure while structures of the methanol-stable variants affirmed the enhancement of a 107
surface hydrogen bond network (47, 48). Furthermore, the helix-lid was identified (α9, 108
residues F177-A192) (48), and is expected to have a significant interphase-triggered 109
conformational change as was reported by Carrasco-Lopez et al. for a similar lipase from 110
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Geobacillus thermocatenulatus analyzed in an “open” lid conformation (95% sequence 111
identity) (49). Further stabilization of the methanol-stable variant H86Y/A269T/R374W 112
was obtained through immobilization in sol-gel (50). 113
To date, solvent tunnel engineering of lipases was not applied for improving 114
stability in methanol. Most works aimed to alter enzyme selectivity and substrate 115
specificity (26, 31, 51-54). While the previous report on stabilizing DhaA employed 116
saturation mutagenesis of tunnel residues (33), herein a more systematic rational approach 117
was practiced, incorporating bulky aromatic amino acids for introducing new interactions 118
within the LipT6 inner hydrophobic core. Tighter packing of a protein lipophilic core was 119
previously shown to result in higher stability with correlation to thermophilic nature (55). 120
In particular, aromatic interactions have a major contributing role in protein folding 121
nucleation, membrane anchoring and thermodynamic stability (56-60). Solvent tunnels 122
were selected as target regions for mutagenesis due to their void volume and accessibility 123
to the enzyme centroid. Each solvent tunnel was carefully and logically examined and Phe, 124
Tyr or Trp substitutions were incorporated. Single variants were purified and evaluated for 125
stability features, kinetic parameters and biodiesel synthesis, as well as their double and 126
triple combinations. X-ray structures of 7 mutants revealed the changes induced by the 127
inclusion of bulky residues. Interestingly, we discovered non-trivial correlations among 128
three neighboring stabilizing Phe mutations. 129
130
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RESULTS 131
Tunnels analysis and selection of mutations. Analysis of the LipT6WT structure (PDB 132
4X6U) with MOLE 2.0 generator yielded 9 tunnels, and several nearby residues to these 133
channels (4-5 Å) were identified and selected for mutagenesis (Fig. 1). Overall, 10 134
positions were selected for rational design and 16 single mutants were generated as 135
presented in Table 1. The general considerations were: (i) obstructing solvent tunnels with 136
bulky side chains, (ii) maintaining the native hydrogen bond networks, and (iii) avoiding 137
changes to catalytic and metal binding residues. The geometrical and biochemical 138
properties of each residue dictated the choice of the specific amino acid used for site-139
directed mutagenesis (Phe, Tyr or Trp). The different primers used for mutagenesis are 140
listed in Table 2. 141
Screening for enhanced stability in 60% methanol. The mutants were expressed in E. 142
coli and the soluble cell extract was used for stability evaluation in 60% methanol as 143
previously described (47, 48). Relative hydrolysis activity values of the designed mutants 144
compared with LipT6WT are presented in Table 3. A threshold of 4-fold increase in stability 145
was used to determine which mutations were further combined to investigate a potential 146
additive effect. Of the 16 variants evaluated, only L184F, A187F and L360F had significant 147
improvement of 81.2, 5.3 and 4.5-fold compared with WT, respectively. All three 148
mutations were found in the vicinity of the longest solvent tunnel (tunnel 1) which is 2.9 Å 149
away from catalytic Ser114 as presented in Fig. 2. L184 and A187 are located on the LipT6 150
helix lid while L360 is part of a flexible internal loop. The three mutations were combined 151
in all possible rearrangements to explore their additive effect on LipT6 stability (Table 3). 152
Only two double mutants, L184F/A187F and A187F/L360F, were found to be more stable 153
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than LipT6WT but inferior to L360F, while the triple mutant was a very poor catalyst, 154
suggesting a complex association between these three residues. 155
Stability measurements of purified enzymes in 70% methanol. In order to validate the 156
screening results, single variants and their double mutant combinations were purified and 157
used for stability measurement in 70% methanol during a total incubation time of 6 h (47). 158
The relative activity values (compared with stress-free conditions in buffer) are presented 159
in Fig. 3. An expected decrease in activity occurred in all variants after 1 h, while LipT6WT 160
lost more than 70% of its activity after 6 h of incubation. Single variants L184F, A187F 161
and L360F maintained 37, 47 and 73% of their hydrolytic activity after 6 h, respectively, 162
as was also inferred by the screening results (Table 3). In addition, double mutants 163
L184F/A187F and A187F/L360F showed increase in stability compared to LipT6WT, 164
preserving more than 48 and 58% of their initial activity, respectively. Nevertheless, double 165
mutant L184F/L360F presented lower stability after losing more than 80% of its initial 166
activity after 6 h. As found in the screening stage, only 5 out of 6 mutants were more stable 167
than LipT6WT. 168
Unfolding temperature of LipT6 mutants. The stable mutants (in their purified form) 169
were characterized by their unfolding temperature (Tm) in buffer (native environment) and 170
in organic solvents (denaturing environment). The assay was conducted using differential 171
scanning fluorimetry (50) with 60% methanol solutions resembling biodiesel synthesis 172
reaction conditions (Table 4). Furthermore, Tm values were also measured in 50-70% (v/v) 173
solutions of methanol, ethanol, acetonitrile and DMSO (Table S1). 174
The results in Table 4 clearly indicate that all single mutants were more stable than 175
LipT6WT in both buffer and 60% methanol, while similar results were obtained for 176
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additional organic solvents (Table S1). Among the single mutants, L360F presented the 177
highest thermal stability improvement in buffer and in 60% methanol of more than +3°C 178
and +6°C, respectively. Moreover, it displayed higher thermal stability in all other solvents 179
tested. The addition of A187F to form variant A187F/L360F, resulted in a further 180
improvement of overall +5°C and +7°C in buffer and 60% methanol, respectively. 181
Surprisingly, L184F/L360F exhibited a lower Tm compared with LipT6WT, despite the 182
stabilizing effect observed by L184F and L360F, separately (the same trend was observed 183
in the other organic solvents studied). However, L184F/A187F had minor enhancement in 184
buffer (+1°C) but substantial stability of +7°C in 60% methanol. 185
Kinetic analysis. To investigate the mutation effects on enzyme kinetics, pNPL hydrolysis 186
was selected, based on its wide usage in lipase studies (61-64) including LipT6 (47, 48). 187
The kinetic constants (Table 5) were calculated based on activity in native conditions 188
without methanol. In general, all variants displayed a decrease in kcat values compared with 189
LipT6WT, with L184F/L360F displaying a 70% decline. Single mutants A187L and L360F, 190
and double mutants L184F/A187L and A187F/L360F all had similar lower Km constants, 191
while L184F displayed a similar value as LipT6WT. L184F/L360F had the lowest Km value 192
compared with LipT6WT but also the lowest activity rate. Moreover, the enzyme efficiency 193
parameter kcat/Km of most variants was lower than LipT6WT, except L184F/L360F which 194
displayed a 2-fold increase. Generally, the L360F mutation had the largest negative impact 195
on kcat in the hydrolysis reaction. 196
Biodiesel production from waste chicken oil. Purified single and double variants were 197
used as soluble biocatalysts for biodiesel synthesis from waste chicken oil with 5:1 molar 198
ratio of methanol:oil. Results presented in Fig. 4 emphasize the superior stability and yield 199
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of double mutant A187F/L360F which converted 88% of waste chicken oil into FAME (3-200
fold improvement over LipT6WT yield after 24 h) under conditions tested. Single mutant 201
L360F achieved the second-highest FAME yield of 59% under conditions tested (2-fold 202
improvement). The synthesis yields highly correlated with the increase in Tm, (Table 4) 203
the initial screening results of the soluble cell extracts (Table 2), and the pure enzyme-204
based stability assay in 70% methanol (Fig. 3). Furthermore, L184F and L184F/L360F 205
provided lower FAME conversions compared with LipT6WT as predicted by their Tm values 206
in 60% methanol. Unexpectedly, A187F and L184F/A187F variants displayed a similar 207
increase in transesterification activity contrary to their different Tm. An additive effect in 208
terms of stability was well observed mainly in combining A187F and L360F mutations. 209
On the other hand, L184F mutation had a negative effect in combination with L360F and 210
negligible influence when merged with A187F. 211
Crystal structure determination. In an attempt to gain a deeper understanding of the 212
correlation between structure and stability, the crystal structures of all single and double 213
mutants were solved at resolutions of 1.2 - 2.7 Å (Fig. 5 A-F in comparison with LipT6WT). 214
Crystal parameters and data statistics are summarized in Table S2. Each solved structure 215
was analyzed with two web servers: (a) MOLE 2.0 to re-assess the variants’ new solvent 216
tunnel distribution (30) and (b) Arpeggio for calculating and visualizing unique interatomic 217
interactions in LipT6 mutants compared with LipT6WT. Arpeggio server uses PDB files to 218
calculate all possible intramolecular interactions based on the residues geometrical and 219
biochemical features (65). It was selected due to its versatility in identifying a wide range 220
of interactions and its straightforward user interphase in comparison with other traditional 221
tools. 222
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First, superposition of all mutant structures with LipT6WT ensured there was no 223
significant structural change in the catalytic triad (Ser114, His359, Asp 318), calcium-224
binding site (Glu361, Gly287, Pro367, Asp366), zinc binding site (Asp62, His88, Asp239, 225
His82), and oxyanion hole stabilizing backbone residues (Phe17 and Glu115) (48). Thus, 226
all changes in the variants properties are associated directly to the induced mutations. The 227
electron density around the mutated residues in all variants discussed are presented in Fig. 228
S1. 229
Inspection of solvent tunnels in the new structures using the MOLE server, 230
confirmed the elimination of tunnel 1 which extends from the outer protein surface towards 231
the hydrophobic pocket (Fig. S2). As expected, the phenyl rings obstructed the channel by 232
occupying its volume. Moreover, no other newly-formed tunnels were identified close to 233
the active site region or other locations in variants crystal structures. 234
In all single mutants structures (Fig. 5, A-C), the phenyl side chains orientation is 235
directed towards the former occupied region of tunnel 1. Compared with LipT6WT, the three 236
single mutations did not cause any structural changes in the near environment and overall 237
fold. Analysis of new contacts in the mutants using Arpeggio revealed a new π-π interaction 238
with Phe291 in L184F and A187F (Fig. 5A, 4B). Phe291 is a neighboring residue to the 239
mutated residues, located on a solvent accessible loop (a13) and mainly stabilized by CH/π 240
interactions (Fig. S3). Moreover, Phe184 interacts with Phe17 and several CH/π 241
interactions were formed following mutagenesis. In L360F, a new π-π interaction with 242
catalytic His359 was generated. This residue is stabilized by several other interactions in 243
LipT6WT (Fig. S3). 244
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Examining double mutant structures, of which two were more stable than LipT6WT, 245
showed different bond networks depending on the mutation combinations (Fig. 5, D-F). 246
Stable mutants L184F/A187F and A187F/L360F had a similar residue pose as in the 247
respective single variants. L184F/A187F (Fig. 5D) displayed the same interactions as were 248
found in L184F and A187F separately, creating two new π-π interactions with Phe291. In 249
addition, Phe184 and Phe187 participate in a new aromatic continuum with Phe 291, as 250
was shown in L184F. Likewise, similar to the two single mutants, stable variant 251
A187F/L360F (Fig. 5F) exhibited new π-π interactions with His359 and Phe291 by Phe360 252
and Phe187, respectively. 253
In contrast, methanol-sensitive variant L184F/L360F exhibited a different 254
conformation of Phe184, due to steric hindrance by Phe360 (Fig. 5E). Movement of 255
Phe184 also induced a conformational change of Phe291 now facing “out” into a more 256
solvent accessible orientation (Fig. S4). This movement caused the exclusion of π-π or 257
amide-π interactions formerly stabilizing Phe291. In addition, in its "new" orientation, 258
Phe184 was discarded from any π-π interactions, now stabilized by only hydrophobic 259
interactions. The poor methanol-stability of L184F/L360F is therefore linked to the 260
aromatic rearrangement in the vicinity of the active site, despite the stabilizing effect of 261
L360F alone due to tunnel 1 obstruction. To further strengthen this hypothesis, the crystal 262
structure of triple mutant L184F/A187F/L360F was solved (Fig. S5). The structure 263
displayed the same “flipped” conformation of Phe184 and Phe291 occurring in 264
L184F/L360F. Despite this, Phe187 managed to interact with Phe291 and Phe360 by π-π 265
interactions, but with no effect on the variants’ stability. 266
267
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DISCUSSION 268
Enzyme engineering is one of the major approaches for designing stable 269
biocatalysts for an organic solvent environment (2, 10, 18, 22). Manipulating tunnels for 270
obtaining stability in organic solvents was first introduced on haloalkane dehalogenase 271
DhaA by Koudelakova et al. increasing its stability in DMSO by primarily randomized 272
design (33). Most works on tunnel re-design focus on altering substrate selectivity by 273
influencing substrate access to the active site (26, 31, 52, 53, 66-69). 274
The present work aimed to stabilize LipT6 in methanol by incorporating aromatic 275
residues into solvent channels to induce improved hydrophobic packing via π-involving 276
interactions. Some works suggested that such modifications can potentially restrict 277
unnecessary penetration of polar alcohols into the enzyme core (32). Site-directed 278
mutagenesis at selected positions was performed based on geometric and biochemical 279
properties of the residues. This approach was indeed successful in obtaining new solvent-280
stable mutants of LipT6, with improved Tm and biodiesel synthesis yields. As a rational 281
concept, introducing π-interactions within lipophilic areas in the enzyme inner tunnels can 282
reduce screening efforts, compared with other reported directed evolution approaches. Dror 283
et al. obtained a 2-fold improvement in FAME synthesis yield with LipT6 double mutant 284
H86Y/A269T, when combining mutations selected from random mutagenesis and 285
structure-guided consensus libraries. Isolating these mutations required the screening of 286
over 2200 colonies (47). Greater improvement of 30-fold higher stability in 70% methanol 287
was achieved by Korman et al. who constructed Dieselzyme4 (Proteus mirabilis lipase 288
variant with 13 mutations including one introduced disulfide bond), though their overall 289
screening efforts were estimated in 20,000 colonies (70). On the other hand, a rational 290
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approach by Park et al. yielded 7 variants of Candida antarctica lipase B (CaLB) with 291
potentially enriched hydrogen bonds network while only one mutant possessed 1.5-fold 292
higher stability in 80% methanol (71). Koudelakova et al. discovered stabilizing mutations 293
located in the DhaA access tunnel after screening 5326 colonies from random mutagenesis 294
libraries, towards stability in 42% DMSO. The random positive mutations were added to a 295
previously-known stable DhaA variant and saturation mutagenesis of position Ala171 in 296
the access tunnel was performed. This combined approach resulted in few stable variants 297
possessing superior 2-fold increased stability in 40% DMSO (33). Regarding our screening 298
efforts (16 single variants) and the additive effect accomplished (3-fold improvement in 299
FAME biosynthesis), one can conclude that introduction of aromatic interactions within 300
solvent tunnels is a promising concept in the quest for solvent-stable enzymes. Moreover, 301
focusing on long and deep tunnels could have even reduced labor and cost efforts. 302
Generally, initial screening results emphasized the dependence on tunnel location 303
and length. Stabilizing mutations (3 of 6; 50%) were found exclusively in the longest 304
solvent pathway (tunnel 1) leading from the surface to the active site. The overall structure 305
of LipT6 is rigid and compact similar to other thermophilic homologs in the I.5 family (49, 306
72, 73). Thus, the peripheral tunnels are situated mostly near the hydrophilic surface (Fig. 307
1) and are less prone to stabilization through core hydrophobic interactions. In addition, 308
tunnel 1 is near the active site thus re-designing such surroundings was expected to have 309
some significant outcomes as was presented by Biedermannova et al. for haloalkane 310
dehalogenase LinB (51). Furthermore, Phe and Tyr mutations had significantly diverse 311
stabilization features when occupying the same position (Table 3). For example, L360F 312
was 81.2-fold more stable than wild-type while L360Y was less stable (0.19-fold). These 313
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contradicting outcomes highlight the importance and unique nature of this tunnel, nearby 314
the helix-lid which is expected to have a significant structural rearrangement in the 315
presence of hydrophobic substrates. 316
Three positions within tunnel 1 were selected for further investigation after their 317
Phe mutations resulted in increased stability in 60% methanol. L184 and A187 are located 318
on LipT6 helix-lid (α9) while L360 is found close to the active site. Re-analysis of the 319
variants crystal structures with MOLE 2.0 indicated that the introduced phenyl side chains 320
managed to crowd tunnel 1 (no longer found in mutants, Fig. S2), as intended, and as 321
described beforehand (32, 33). Conversely, Liskovaet et al. have shown that replacing Phe 322
with Gly in DhaA80 caused a decline in stability due to disruption of intramolecular 323
hydrophobic packing (32). These findings correlated with our positive results of replacing 324
Leu or Ala with Phe residues rationally. Stability measurements of purified enzymes in 325
70% methanol validated our screening results as L360F exhibited the highest residual 326
activity after 6 h followed by stable mutants A187F and L184F, respectively. Melting 327
temperature measurements agreed well with initial stability screening results when L360F 328
and A187F mutants presented better thermal stability in both buffer and methanol (along 329
with other organic solvents as presented in Table S1). A similar correlation between Tm 330
and stability in organic solvents was previously obtained for other LipT6 stable variants 331
(47, 48). 332
The superior stability of L360F was greatly related to its unexpected π-π stacking 333
interaction with catalytic His359 (Fig. 5C). Kannan and Vishveshwara previously reported 334
the existence of one aromatic cluster next to the active site in thermophilic enzymes which 335
was lacking in their mesophilic equivalents (55). LipT6 homologous sequence alignment 336
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performed by Dror et al. showed that Leu360 is not an evolutionary conserved position, 337
however the formation of a new aromatic cluster explains the stabilization exhibited by this 338
mutant (47, 55). 339
Both L184F and A187F interacted separately with Phe291 by new aromatic π-π 340
interactions, while A187F had both improved transesterification activity and 341
thermostability. Since L184F exhibited the relatively lowest improvement in Tm and 342
methanol-stability, it can be implied that a minimum stability enhancement threshold is 343
required for improved biodiesel synthesis in comparison with LipT6WT. As previously 344
described by Dror et al., some mutations in LipT6WT induced methanol stability but at the 345
same time led to decreased FAME synthesis. One example is the neighboring position 346
Gln185, which was mutated into Leu and was found to induce alcohol-stability yet a lower 347
transesterification yield of soybean oil (47). This phenomena was attributed to tighter 348
orientation of LipT6 helix-lid limiting the triglycerides accessibility during biodiesel 349
synthesis. It can be assumed that the L184F mutation had a similar affect as was reported 350
for Q185L. In addition, several studies indicated that mutations of the lid can alter 351
thermostability along with selectivity (74, 75). Khan et al. recently reviewed the influence 352
of mutagenesis of the lid on thermostability and activity highlighting the importance of this 353
domain in lipases (76). Some studies indicated a simultaneous change in stability and 354
substrate preferences caused by altering residues on the lid (77, 78). Likewise, decline in 355
activity accompanied with elevated stability was also apparent after introducing bulky 356
residues in the DhaA access tunnel (32, 33). 357
Kinetic analysis revealed a general increase in substrate affinity (lower Km) and 358
decrease in maximum hydrolytic velocity (lower kcat) by most variants. As expected, 359
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mutations in the vicinity to the active site tend to affect enzyme kinetics, selectivity or even 360
mechanism (51, 68, 69). Among single mutants, L360F displayed the lowest kcat with 361
similar Km values, emphasizing the significant interaction with catalytic His359. Lid 362
mutations L184F and A187F also affected LipT6 kinetics as was described previously by 363
Tang et al. on lid mutations of Penicillium expansum lipase (77). Despite the lower activity 364
rates of the mutants in the hydrolysis reaction, most of them performed better in an organic 365
solvent environment, leading to higher biodiesel yields (Fig. 4). 366
Merging stable mutations in all possible double-mutant combinations revealed 367
interesting complex correlations regarding stability in methanol, Tm values and FAME 368
synthesis. The highest stabilizing affect was accomplished by A187F/L360F, displaying 369
the best FAME yield (88% after 24 h) and Tm improvement (+5°C and +7°C compared 370
with LipT6WT in buffer and 60% methanol, respectively). These finding were also 371
confirmed in the purified enzyme stability assay (Fig. 3) and melting temperatures in other 372
polar solvents (Table S1). Relatedly, Stepankove et al. previously showed that different 373
organic solvents can confer different destabilizing effects on enzymes (79). Structural 374
analysis suggests that new aromatic interactions with both catalytic His359 (by Phe360) 375
and Phe291 (by Phe187) are responsible for the improved performance in the non-aqueous 376
environment. Aromatic interactions were previously found to stabilize xylanase, 377
ribonuclease and many other protein structures by improving hydrophobic packing and 378
introducing new π-interactions (80-83). In addition, these two mutations did not dismiss 379
interactions found in LipT6WT, yet enriched the existing network along with occupying 380
tunnel 1. Prior work on LipT6 stabilization highlighted the importance of enhancing the 381
hydrogen bond network among surface residues as well as interactions with water 382
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molecules (47, 48). Here, we have discovered the significance of π-π stacking interactions 383
and CH/π interactions within the LipT6 hydrophobic core to methanol stability. The kinetic 384
properties of A187F/L360F revealed a lower hydrolysis reaction rate and higher affinity 385
towards pNPL (C12). Despite this, triglycerides methanolysis rate and yield was 3-fold 386
higher than wild type. Based on these observations, we conclude that the major factor 387
influencing FAME synthesis in our system is the enzyme stability. This was also shown in 388
other cases (47, 48). Dror et al. showed that LipT6 double mutant H86Y/A269T had similar 389
hydrolysis performance to LipT6WT though its FAME yield from soybean oil was 2-fold 390
higher (47). 391
L184F/A187F variant displayed similar thermostability to A187F/L360F, but its 392
transesterification performance was similar to A187F. Adding L184F did not reduce the 393
already improved transesterification activity of A187F. Only L184F/A187F possess two 394
neighboring lid mutations which may explain this non-correlative relationship between 395
alcohol stability and FAME synthesis, as was shown before (76, 77). Both L184F and 396
L184F/A187F structures revealed a π-π stacking interaction network involving 16 aromatic 397
side chains (Fig. S6). Apparently, thermostability improved due to this branched aromatic 398
continuum, but no significant transesterification improvement occurred compared with 399
A187F variant (55). 400
Interestingly, double mutant L184F/L360F, comprising of two single stabilizing 401
mutations, showed decreased methanol stability, lower Tm (in all solvents tested), lowest 402
kcat, Km and biodiesel yield. Unlike the effect of L184F on A187F (L184F/A187F variant), 403
in combination with L360F a dramatic decrease in stability occurred. Inspecting the crystal 404
structure L184F/L360F showed an aromatic cluster rearrangement involving Phe184, 405
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Phe291 and Phe360 (Fig. 5, S3). Steric collision between static Phe360 (found in the same 406
orientation in all mutants) and Phe184, caused the latter a conformational change leading 407
to movement of Phe291 as well. Subsequently less intramolecular interactions were 408
possible. It was previously shown that helix-stabilizing residues (as Phe291) had an impact 409
on protein stability when comparing thermophilic and mesophilic homologs (84). In 410
addition, analysis of triple mutant L184F/A187F/L360F affirmed that A187F could not 411
restore L184F/L360F stability or favored ring conformation. The fact that stabilizing 412
mutation L360F did not improve the stability of L184F or L184F/A187F, demonstrated the 413
significant impact of Phe291 conformation on LipT6 stability and organic synthesis 414
capability. 415
Overall, this new systematic approach of rational tunnel engineering by 416
incorporating aromatic residues to facilitate π-involving interactions could be considered 417
when stabilizing other enzymes in organic solvents, focusing on deep and long solvent 418
channels. 419
420
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MATERIALS AND METHODS 421
Chemicals. Methanol, glycerol, NaCl and Triton X-100 were purchased from Bio-Labs 422
(Jerusalem, Israel). 2-Propanol , ethanol and sodium citrate were purchased from J.T. Baker 423
(Deventer, The Netherlands). Sodium formate, dimethyl sulfoxide (DMSO) and sodium 424
acetate were purchased from Merck (Darmstadt, Germany). Ethyl acetate was purchased 425
from Gadot (Haifa, Israel) while acetonitrile and CaCl2 from Spectrum Chemical MFG 426
(Gardena, CA, USA). Trizma-base, 4-nitrophenyl laurate (pNPL), polyethylene glycol 427
(PEG) 400, PEG 3350, heptadecanoic acid methyl ester and kanamycin were purchased 428
from Sigma–Aldrich (Rehovot, Israel). Waste chicken oil was kindly donated by Miloubar 429
(Miloubar Mixture Institute ACS, Miluot, Israel). All materials used were of the highest 430
purity available. 431
Bacterial strains, plasmids and enzymes. Recombinant Geobacillus stearothermophilus 432
T6 lipase (EMBL, AF429311.1) fused to a His-tag was expressed in Escherichia coli BL21 433
cells (DE3; Novagen, Darmstadt, Germany) as previously described (47, 48, 50). 434
Solvent tunnels analysis using MOLE 2.0. The crystal structure of LipT6WT (PDB 4X6U) 435
was analyzed for tunnels detection with MOLE 2.0 online generator 436
[http://old.mole.upol.cz/] using default parameters (30). The analysis resulted in 9 tunnels 437
and superposition display (enzyme structure and tunnels' coordinates) was utilized to define 438
the closest residues to these channels (4-5 Å direct distance) using Pymol (85). After 439
eliminating essential residues (catalytic, metal-binding and multiple hydrogen bond donor) 440
and inspecting MOLE 2.0 job review, 10 positions were selected for site-directed 441
mutagenesis (Table 1) alternated into at least one bulky residue (F, Y or W). Mutants were 442
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generated, and subsequently evaluated for activity, stability, and structural 443
characterization. 444
Site-directed mutagenesis of LipT6. Rational mutagenesis of pET9a-LipT6WT plasmid 445
was performed using the QuickChangeTM Protocol for Site Directed Mutagenesis. Reaction 446
mixture is composed of 5µl Taq polymerase buffer, 2µl DNA template (50 ng/µl), 1.5µl of 447
each primer solution (1µg/µl), 2µl dNTP’s (20 mM A:T:C:G 1:1:1:1), 0.5µl Taq 448
polymerase (EurX; Gdańsk, Poland) and 37.5µl bH2O. The different primers are listed in 449
Table 2. Followed by its addition, Taq polymerase was incubated in a thermocycler 450
(Labcycler; SensoQuest, Göttingen, Germany). The PCR program had an initial 451
denaturation step for 1 min at 95 °C, then 20 cycles of 30 s at 95 °C, 45 s at 65 °C and 6 452
min at 68 °C, followed by a final elongation step for 7 min at 68 °C. PCR product was run 453
on agarose gel (1 % w/w) to validate single-band product and the template plasmid was 454
digested for 18 h at 37 °C with a Dpn1 treatment (NEB, Massachusetts, USA). The 455
resulting plasmid was used for transformation and selection on LB agar plates containing 456
25 μg/ml kanamycin. Plasmids from positive colonies were extracted using a plasmid 457
miniprep kit (Qiagen, Hilden, Germany), and sequenced for verification (HyLabs, 458
Rehovot, Israel). 459
Soluble lipase activity assay. The soluble lipase hydrolytic activity on pNPL was 460
determined using a colorimetric assay as described previously (47, 48). This method was 461
also used to determine the specific activity of purified enzyme samples in buffer and in 462
solvent solutions. 463
Stability screen in 60% methanol. Screening for methanol-stable mutants was performed 464
as described previously with few modification (47). TB medium inoculation volume was 465
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35 ml while after centrifugation the cells were resuspended in 9 ml buffer to increase the 466
method’s sensitivity. 467
Purification of LipT6 variants. Purification of LipT6 variants was conducted according 468
to previously described procedures (47, 48), with AKTA Prime Plus (GE Healthcare Bio-469
Sciences AB, Sweden). 470
Unfolding temperature (Tm) determination of purified LipT6 variants. Denaturation 471
temperature determination by using nanoDSF device was conducted according to a 472
previously described procedure (50). 473
Determining kinetic parameters. Km and kcat values for LipT6 purified variants were 474
determined using the pNPL hydrolysis colorimetric assay in 96-well plates as was 475
previously described (47, 48). Results were analyzed using SigmaPlot software. 476
Stability validation of LipT6 variants in 70% methanol. The stability of purified LipT6 477
variants in 70% methanol was determined by measuring the residual hydrolytic activity 478
after incubation for several hours as described previously (47, 48). 479
Enzymatic transesterification of waste chicken oil by soluble lipase. The 480
transesterification reactions were carried out according to the work of Dror et al. (48), in 481
triplicate with few modifications. Roughly, 14 ml closed glass vials were filled with 2 g 482
waste chicken oil while methanol was added in 5:1 alcohol to oil molar ratio followed by 483
the addition of 400 µl of lipase buffer (2 mg/mL enzyme solution, 0.04% enzyme and 20% 484
water content based on oil weight). 485
Gas chromatography analysis of FAME. GC analysis of FAME formation was carried 486
out according to the work of Dror et al. (48). 487
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LipT6 variants crystallization, data collection and structure determination. 488
Crystallization of LipT6 variant was performed as described before with few modification 489
(48). The hanging drop contained 2 μl protein solution (0.5-2 mg/ml) and 2 μl 490
crystallization condition (0.2 M sodium citrate 25 % PEG 3350 or 0.2 M sodium formate 491
20 % PEG 3350). Cryoprotectant solution was crystallization condition enriched with 25% 492
PEG 400. X-ray diffraction data of LipT6 variants were collected at the European 493
Synchrotron Radiation Facility (ESRF), Grenoble, France, at beamlines described in Table 494
S2. Diffraction data was indexed, integrated, and reduced with either Moslfm (86), Scala 495
(87), autoPROC (88) or by EDNA (89). All structures were solved by molecular 496
replacement using Phaser (90) and the coordinates of LipT6WT structure (PDB 4X6U). 497
Refinement was performed using PHENIX (91). Manual model building, real-space 498
refinement, and structure validations were performed using Coot (92). Crystal parameters, 499
ESRF used beamlines and data statistics are summarized in Table S2 in the supplementary 500
material. 501
Calculation and visualization of LipT6 variants interatomic interactions. 502
Determination of interaction repertoire in LipT6WT and other variants was performed by 503
using Arpeggio web served using each mutants PDB file (65). Default setting were used to 504
calculate and analyze each structure including graphical presentation using Pymol (85) as 505
shown in Fig. 5. 506
507
ACKNOWLEDGMENTS 508
We acknowledge the Russell-Berrie Nanotechnology Institute (RBNI) at the Technion for 509
supporting this research. We also thank the staff of the European Synchrotron Radiation 510
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Facility (beamlines ID 29, ID 30a-3) for provision of synchrotron radiation facilities and 511
kind assistance. 512
513
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514
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82. Meurisse R, Brasseur R, Thomas A. 2003. Aromatic side-chain interactions in proteins. Near-713 and far-sequence his–X pairs. BBA Proteins Proteom 1649:85-96. 714
83. Serrano L, Bycroft M, Fersht AR. 1991. Aromatic-aromatic interactions and protein stability: 715 investigation by double-mutant cycles. J Mol Biol 218:465-475. 716
84. Facchiano AM, Colonna G, Ragone R. 1998. Helix stabilizing factors and stabilization of 717 thermophilic proteins: an X-ray based study. Protein Eng 11:753-760. 718
85. DeLano WL. 2002. The PyMOL molecular graphics system:Version 1.3, DeLano Scientific 719 LLC, San Carlos, CA. 720
86. Battye TGG, Kontogiannis L, Johnson O, Powell HR, Leslie AG. 2011. iMOSFLM: a new 721 graphical interface for diffraction-image processing with MOSFLM. Acta Crystallorg D 722 67:271-281. 723
87. Leslie A. 1992. Joint CCP4 and ESF-EACMB. Newsletter on Protein Crystallography 724 26:Daresbury Laboratory, Warrington, United Kingdom, 30. 725
88. Vonrhein C, Flensburg C, Keller P, Sharff A, Smart O, Paciorek W, Womack T, Bricogne G. 726 2011. Data processing and analysis with the autoPROC toolbox. Acta Crystallorg D 67:293-727 302. 728
89. Incardona M-F, Bourenkov GP, Levik K, Pieritz RA, Popov AN, Svensson O. 2009. EDNA: 729 a framework for plugin-based applications applied to X-ray experiment online data analysis. J 730 Synchrotron Radiat 16:872-879. 731
90. McCoy AJ, Grosse-Kunstleve RW, Adams PD, Winn MD, Storoni LC, Read RJ. 2007. Phaser 732 crystallographic software. J Appl Crystallorg 40:658-674. 733
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92. Emsley P, Cowtan K. 2004. Coot: model-building tools for molecular graphics. Acta 737 Crystallorg D 60:2126-2132. 738
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TABLES 740
Table 1. Residues selected for mutagenesis based on LipT6WT tunnels analysis 741
Tunnel number a,b Tunnel length c (Å) Residue Generated
mutation
1 21
L184 F, Y
A187 F, Y
L360 F, Y
2 and 3 (Y-shape) 13.5 and 13.9 R215 F, Y
4 11.5 H154 Y, W
5 7.8 I11 W
7 8.5 F226 Y
K330 Y, W
8 8.8 L380 F
F268 Y
a according to MOLE 2.0 automatic numbering.
b tunnels 6 and 9 were unchanged to maintain their rich hydrogen bond network.
c according to MOLE 2.0 job report.
742
743
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Table 2. Primers for site directed mutagenesis of pET9a-LipT6WT plasmid 744
Position Original
aa
Substitution Nucleotide sequence 5’→3’ (Fw) a
11 I W GCTAACGATGCGCCATGGGTACTTCTCCACGGG
154 H Y TTTGAAGGCGGACATTATTTTGTGTTGAGCGTG
W TTTGAAGGCGGACATTGGTTTGTGTTGAGCGTG
184 L F GATCGCTTTTTTGACTTCCAGAAGGCGGTGTTG
Y CGATCGGTTTTTTGACTATCAGAAGGCGGTGTTG
187 A F GACTTGCAAAAATTCGTGTTGAAAGCAGCGGC
Y GACTTGCAAAAATACGTGTTGAAAGCAGCGGC
215 R F GACCAATGGGGACTGTTTCGCCAGCCAGGTGAA
Y GACCAATGGGGACTGTATCGCCAGCCAGGTGAA
226 F Y GAATCATTCGACCAATATTATGAACGGCTCAAACGG
268 F Y CGAATACGTATTATTTGAGCTATGCCACAGAACGGACG
330 K W ATGAACGGACCATGGCGAGGATCGACAGAT
Y ATGAACGGACCATATCGAGGATCGACAGATCGG
360 L F ACAATGTAGATCATTTCGAAGTCATCGGCGTTG
Y CGTACAACGTAGATCATTATGAAGTCATCGGCGT
380 L F GCCTTTTATTTGCGATTTGCAGAGCAGTTGGCG
L184F/A187F b L F CGCTTCTTCGACTTCCAAAAATTCGTGTTG
a Positions of alternation in mutagenesis primers are indicated in bold.
b Used for the combination of L184F/A187F while A187F (underlined) was used as template.
745
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Table 3. Relative activity of LipT6 variants in 60% methanol 746
Variant a Relative activity b
Sin
gle
mu
tan
ts
L360F 81.2±8.51
A187F 5.3±0.72
L184F 4.5±0.99
F268Y 3.46±0.22
R215F 2.40±0.35
H154Y 1.89±0.25
L184Y 1.51±0.19
R215Y 1.31±0.29
A187Y 1.22±0.43
F226Y 1.08±0.45
H154W 0.94±0.04
K330Y 0.49±0.15
K330W 0.30±0.08
I11W 0.21±0.03
L360Y 0.19±0.09
L380F 0.10±0.05
Dou
ble
mu
tan
ts
A187F/L360F 26.5±7.48
L184F/A187F 19.9±0.89
L184F/L360F 0.46±0.05
Tri
ple
mu
tan
t
L184F/A187F/L360F 0.29±0.06
a Each variant was expressed in E.coli and the soluble cell extract (CE)
was used for the screen. SDS-PAGE analysis ensured an appropriate
expression level and hydrolysis activity in buffer assured no drastic
activity loss. b The relative hydrolysis activity of pNPL was calculated as
(E/E0)/(E/E0)WT by comparing the activity of each variant CE before (E0)
and after (E) 30 min incubation in 60% methanol, divided by the same
value of LipT6WT (E/E0)WT. The results represent an average of
duplicates.
747
748
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Table 4. Unfolding temperature of LipT6 variants in methanol 749
750
751
752
753
754
755
756
757
758
759
760
LipT6 variant Tm
in buffer [°C]
Tm
in 60% methanol [°C]
WT (*) 66.6 ± 0.1 38.9 ± 0.3
L184F 67.5 ± 0.1 41.0 ± 0.2
A187F 70.0 ± 0.2 43.0 ± 0.6
L360F 69.9 ± 0.2 45.6 ± 0.2
L184F/A187F 67.6 ± 0.1 46.1 ± 0.2
L184F/L360F 65.5 ± 0.1 38.1 ± 0.1
A187F/L360F 72.2 ± 0.1 46.2 ± 0.1
*obtained from Gihaz et al. 2016.
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Table 5. Kinetic parameters of LipT6 variants in pNPL hydrolysis 761
762
763
764
765
LipT6 variant Km
(10-2 mM)a
kcat
(103 s-1)
kcat/Km
(103 s-1 mM-1)
WT (b) 7.9±0.6 4.7 59
L184F 8.4±0.9 3.0 36
A187F 5.4±0.6 3.0 55
L360F 5.1±0.5 2.1 41
L184F/A187F 5.1±0.4 2.1 41
L184F/L360F 1.1±0.1 1.3 116
A187F/L360F 5.6±0.7 1.6 30
a values are means ± standard errors of the means. b obtained from Dror et al. 2014.
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766
767
768
769
770
771
772 773 774 775 776 777 778 779 780 781 Figure 1. Visualization of the LipT6
WT solvent tunnels as generated by the computational 782
algorithm MOLE 2.0. The α-helix lid (α9) is marked in red. Calcium and zinc metal ions are 783
shown as green and gray spheres, respectively. Solvent tunnels are shown in blue and target 784
residues intended for mutagenesis are shown as magenta sticks. Catalytic Ser114 is presented in 785
cyan. Numbers in black indicate the tunnel numbering according to MOLE job report. 786
787
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788
789
790 791 792 793 794 795 796 797 798 799 800 801 802 803 804 805 806 Figure 2. Residues found to influence stability in methanol by tunnel engineering. (A) Close-807
up view of tunnel 1, (B) Surface visualization. The α-helix lid (α9) is marked in red. Solvent tunnel 808
is shown in blue and target residues are shown as magenta sticks. Catalytic serine is presented in 809
cyan. 810
811
Leu360
Leu184
Ala187
Ser114
A B
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812
813
Figure 3. Relative residual activity of LipT6 variants after incubation in 70% methanol. 814
Purified LipT6 mutants were incubated in 70% methanol for various time durations and their 815
remaining activity was measured and compared with native conditions (marked as 100% in cyan 816
bars). Samples for pNPL hydrolysis assay were collected after 1, 4 and 6 h of incubation. 817
818
0
10
20
30
40
50
60
70
80
90
100
Rel
ati
ve
acti
vit
y a
fter
in
cub
ati
on
in 7
0%
meth
an
ol
[%
]
0h 1h 4h 6h
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819
Figure 4. FAME biosynthesis from waste chicken oil using soluble LipT6 variants. Reaction 820
conditions: oil (2 g), water (20%), methanol to oil molar ratio 5:1 (60% MeOH) and soluble lipase 821
(0.04% based on the oil weight), 1350 rpm, 45°C. The results represent triplicates (n=3). 822
823
824
825
0
10
20
30
40
50
60
70
80
90
0 5 10 15 20 25
FA
ME
conv
ersi
on [
%]
Time [h]
WT
L184F
A187F
L360F
L184F/A187F
L184F/L360F
A187F/L360F
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826 827 828 829 830 831 832 833 834 835
836
837
838
839
840
841
842
843
844
845
846
847
848
849
850
851
852
853
S114
F17
F291
V188
L184F
A
S114
F291
A187F
L184
B
S114
L360F
H359
I320
D318
H113
F17 C
S114
F291 A187F
L184F
F17
I320
V188
D
S114 L184F
L360F
H359
A187
F291
S114
A187F
F291 L360F
H359
F E
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Figure 5. X-ray structures of LipT6 designed mutants superimposed with LipT6WT
(in gold). 854
(A) L184F in green, (B) A187F in pink (C) L360F in blue, (D) L184F/A187F in cyan, (E) 855
L184F/L360F in brown and (F) A187F/L360F in purple. The α-helix lid in all structures is 856
marked in red and catalytic S114 is presented in all figures. New interactions induced in the 857
mutants compared with LipT6WT (according to Arpeggio server analysis) are marked in dashed 858
lines as followed: π-π in yellow, CH/π in green and amide-π in blue. 859
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