Variability in fruit oil content and biodiesel yield of 8 selected accessions
To develop L. glauca fruit oils as potential material for biodiesel, it was vital for us to determine ideal accession with high quantity and quality of fruit oils for gaining maximum economic benefits. Based on our recent studies of different germplasms [11, 12], eight plus trees (accessions LG01, LG02, LG03, LG04, LG05, LG06, LG07 and LG08) with high fruit yield were selected to investigate the variability in fruit oil content and biodiesel yield of different accessions. Here, the fruit oil contents varied from 44.12% (LG01) to 60.95% (LG06), followed by LG03 (46.48%), LG02 (47.39%), LG08 (48.52%), LG04 (49.09%), LG07 (51.81%) and LG05 (53.16%), of which the fruits of LG05, LG06 and LG07 had oil content more than 51.5% (Figure 1a). This allowed us to explore the differences in biodiesel yield from fruit oils across all accessions. The biodiesel yield from fruit oils varied among different accessions, ranging from 85.12% (LG01) to 98.71% (LG06) with an average value of 92.17% (Figure 1b), of which biodiesel yield of LG05 (97.26%), LG06 (98.71%) and LG07 (96.81%) was in the standard of EN 14214 (96.5%). These revealed a difference in fruit oil and biodiesel yield across different accessions, and three high oil-bearing accessions (LG05/06/07) with high-yield biodiesel could be valuable as source for developing biodiesel.
Variability in FA profiles of fruit oils from 8 selected accessions
Oil content and FA composition are known as two vital factors for determining whether oil plant can be suitable for biodiesel production. Here, 10 kinds of FA compositions were detected in L. glauca fruit oils of all accessions (Table 1), including capric acid (C10:0), lauric acid (C12:0), palmitic acid (C16:0), palmitoleic acid (C16:1), stearic acid (C18:0), oleic acid (C18:1), linoleic acid (C18:2), linolenic acid (C18:3), arachidic acid (C20:0) and eicosenoic acid (C20:1). The dominant compound was oleic acid (51.24-77.89%) with an average of 59.52%, followed by linoleic acid (16.14-33.87%), palmitic acid (2.65-5.26%) and linolenic acid (1.55-4.85%), but the other showed minor quantities (0.03-0.46 %), of which the maximum value of C18:1 (77.89%) and minimum value of C18:2 (16.14%) and C18:3 (1.55%) were all detected for accession LG06. Also, the total content of C18:1 and C18:2 in fruit oils varied from 84.29% to 94.04%, and three accessions (LG05, LG06 and LG07) had C18:1 content of more than 60 % (Table 1), implying that they were ideal raw material for biodiesel.
The ideal plant oils for high-quality biodiesel production generally contain a small amount of saturated FA (SFA), high amount of monounsaturated FA (MUFA), and low level of polyunsaturated FA (PUFA) [9, 26]. Here, the change analysis for SFA, MUFA and PUFA in fruit oils from different accessions showed that the contents of MUFA and PUFA varied from 52.43% to 78.46%, and from 17.69% to 38.73%, respectively, but the SFA content of all accessions was less than 9% (Figure 1c). Of note, LG06 had the highest content of MUFA (78.46%) and the lowest amounts of PUFA (17.69%) and SFA (3.85%), revealing that the fruit oils from accession LG06 with ideal FA compositions could meet the demand of high-quantity biodiesel production.
Table 1 The changes of FA compositions and relative proportions in L. glauca fruits of different accessions
Accessions
|
C10:0 (%)
|
C12:0 (%)
|
C16:0 (%)
|
C16:1 (%)
|
C18:0 (%)
|
C18:1 (%)
|
C18:2 (%)
|
C18:3 (%)
|
C20:0 (%)
|
C20:1 (%)
|
LG01
|
0.29±0.03
|
0.25±0.03
|
5.26±0.41
|
1.07±0.08
|
1.79±0.13
|
51.24±2.28
|
33.87±2.01
|
4.86±0.78
|
1.25±0.05
|
0.12±0.03
|
LG02
|
0.46±0.03
|
0.14±0.07
|
4.64±0.18
|
1.28±0.24
|
1.69±0.35
|
55.14±2.11
|
31.07±1.45
|
4.63±0.21
|
0.74±0.03
|
0.21±0.05
|
LG03
|
0.25±0.03
|
0.24±0.03
|
5.13±0.22
|
2.33±0.14
|
1.76±0.24
|
52.04±2.29
|
32.25±2.05
|
4.74±0.29
|
1.11±0.13
|
0.15±0.03
|
LG04
|
0.19±0.04
|
0.17±0.04
|
4.04±0.09
|
2.29±0.21
|
1.42±0.28
|
58.30±2.21
|
29.83±1.21
|
3.07±0.19
|
0.61±0.06
|
0.08±0.02
|
LG05
|
0.17±0.03
|
0.08±0.03
|
3.54±0.31
|
2.24±0.17
|
1.16±0.11
|
63.32±3.37
|
26.52±1.21
|
2.48±0.17
|
0.38±0.04
|
0.11±0.04
|
LG06
|
0.04±0.02
|
0.06±0.03
|
2.65±0.18
|
0.54±0.13
|
1.01±0.21
|
77.89±4.21
|
16.14±1.28
|
1.55±0.11
|
0.09±0.04
|
0.03±0.04
|
LG07
|
0.30±0.11
|
0.06±0.02
|
3.85±0.17
|
0.98±0.21
|
1.17±0.11
|
61.28±3.95
|
28.93±1.45
|
2.87±0.13
|
0.41±0.05
|
0.14±0.34
|
LG08
|
0.28±0.09
|
0.21±0.08
|
4.41±0.14
|
1.54±0.31
|
1.47±0.21
|
56.98±2.01
|
30.51±1.43
|
3.96±0.12
|
0.58±0.03
|
0.06±0.02
|
Error bars are standard deviations (SD) of three biological replicates.
Also of note was low ratio of PUFA/MUFA (especially C18:2/C18:1) or C20-24/C16-18 as key parameter for tribological property of plant oils for industrial application [27]. Here, the lowest ratios of PUFA/MUFA (0.225), C18:2/C18:1 (0.207) and C20-24/C16-18 (0.001) were noted for accession LG06, but the other accessions had a relative high ratios of PUFA/MUFA (0.442-0.739), C18:2/C18:1 (0.419-0.661) and C20-24/C16-18 (0.005-0.014) (Figure 1d-f), implying that the fruit oils from LG-06 may have ideal tribological properties.
These outcomes, together with the highest yield of oil and biodiesel for accession LG06, revealed that its fruit oil was the most suitable for biodiesel production.
Evaluation of biodiesel fuel properties of fruit oils from different accessions
Effective evaluation biodiesel fuel properties of iodine value (IV), cetane number (CN), oxidation stability (OS), cloud point (CP), cold filter plugging point (CFPP), density (D) and kinematic viscosity (KV), would provide a vital basis for exploiting biodiesel plants. Given a notable variation on oil content and total proportion of C18:1 and C18:2 in L. glauca fruits of different accessions (Table 1), it was important to assess fuel properties of biodiesel derived from fruit oils of different accessions for determining superior accession as biodiesel production.
CN, one key criteria for ignition delay time and combustion quality of biofuels, was detected to be varied from 48.81 to 51.15 in the FAMEs from fruit oils of all accessions, all of which could satisfy the standard of USA (ASTM D6751: CN>47), and most accessions (except LG01/03) was also in line with China standard (GB/T 20828: CN>49), while only LG06 (51.15) could meet Europe standard (EN 14214: 51<CN<65) (Table 2), implying that the biodiesels from fruit oils of all accessions had good ignition quality. Also, IV is a crucial index for assessing the unsaturated degree (DU) of FA and OS of biodiesel [28]. The IV values of all accessions varied from 102.15 to 115.09 (Table 2), all of which was less than the specified maximum limit (120) of ASTM D6751, EN 14214 and GB/T20828 standards. It is known that the values of both CN and IV are determined greatly by the DU [26]. The DU value presented here varied from 115.39 to 134.75 across all accessions, of which LG-06 had a minimum of 115.39, coincided with the highest CN value (51.15) and the lowest IV value (102.15) (Table 2).
KV is one key parameter for defining flow capability of biodiesel, used for estimating spray penetration and atomization of fuel [28]. The range of KV value (4.31-4.68 kg/m3) of biodiesels from all accessions could meet with the standards of ASTM D6751 (1.9<KV<6.0), EN 14214 (3.5<KV<5.0) and GB/T20828 (1.9<KV<6.0) (Table 2), revealing a good flow or spray capability of biodiesel fuel from L. glauca fruit oils of all accessions. Also, density (D) is one of vital fuel properties for assessing fuel transferred quantity by injection system for combustion [29]. The D value ranged from 871.54 to 887.14 mm/s of the biodiesels (Table 2), which satisfied with the standards of EN 14214 (860<D<900) and GB/T20828 (820<D<900), and thus concluded that the biodiesels from L. glauca fruit oils of all accessions possessed ideal combustion efficiency.
OS, as a crucial parameter, involves in the level and stability of biodiesel reaction with air [28]. In this study, the OS values of biodiesels from fruit oils of all accessions varied from 2.59 to 3.34 h (Table 2), all of which did not reach the minimum limit (6 h) specified in the standards of EN 14214 and GB/T 20828, but only accession LG06 (3.34 h) could meet the ASTM D6751 standard (OS>3.0 h), which was likely attributed to low content of PUFA (17.69%) in the fruit oils of LG06 compared with other accessions (29.01-38.73%) (Figure 1c).
CFPP and CP, two vital low-temperature parameters, are used to describe the maximum of filterability, but not limited by the standards of US and European. The CFPP valve ranged from -12.59°C to -9.74°C for biodiesels across all accessions (Table 2), less than the maximum limit (0°C) of Germany standard (DIN V51606) in summer, and this value for most accessions (except LG01/03) was lower than the minimum limit (-10.0°C) for spring and autumn, implying a good cold flow performance of biodiesel. Also, CP is one indicator for controlling fuel at low temperature [29], and its value ranged from -9.91°C to -7.71°C across all accessions (Table 2), which could meet ASTM D6751 standard (-12°C<CP<-3°C). This implied a better cold flow property of biodiesel from all accessions, especially LG06 with the minimum value of CFPP (-12.59°C) and CP (-9.91°C), which may be mostly attributed to high content of unsaturated FA (Figure 1c) and small amount of length chain saturated factor (LCSF) (Table 2).
Another was concerned about the content of C18:3 and the FAs with four double bonds in the FAMEs. Here, low amount (1.55-4.86 %) of C18:3 in fruit oils of all accessions and no four double-bond FAs (C18:4 and C20:4) in the FAMEs (Table 2) all satisfied the EN14214-2008 specification (< 12 % and 1 %, respectively).
Table 2 Evaluation of biodiesel fuel properties of fruit oils of L. glauca from different accessions
Accessions
|
Biodiesel fuel properties
|
|
|
DU
|
LCSF
|
CN
|
IV (g/100g)
|
CFPP (°C)
|
CP (°C)
|
OS (h)
|
KV (mm2 s-1, 40°C)
|
D (kg/m-3, 15°C)
|
LG01
|
134.75±2.15
|
2.87±0.32
|
48.81±1.14
|
115.09±1.7
|
-9.74±0.14
|
-7.11±0.08
|
2.59±0.03
|
4.38±0.14
|
887.14±1.18
|
LG02
|
132.66±1.64
|
2.37±0.24
|
49.06±1.25
|
113.69±1.4
|
-10.61±0.15
|
-7.89±0.07
|
2.68±0.02
|
4.44±0.08
|
878.23±1.74
|
LG03
|
133.24±2.23
|
2.75±0.18
|
48.98±0.96
|
114.08±1.2
|
-9.94±0.13
|
-7.30±0.07
|
2.65±0.01
|
4.55±0.23
|
883.34±1.65
|
LG04
|
129.54±1.84
|
2.06±0.101
|
49.43±0.87
|
111.61±1.5
|
-11.16±0.13
|
-8.49±0.10
|
2.79±0.02
|
4.68±0.19
|
877.28±1.53
|
Lg05
|
126.15±1.65
|
1.70±0.12
|
49.84±0.68
|
109.34±1.2
|
-11.79±0.16
|
-9.12±0.09
|
2.93±0.02
|
4.36±0.07
|
876.35±1.09
|
LG06
|
115.39±1.24
|
1.24±0.09
|
51.15±1.01
|
102.15±0.9
|
-12.59±0.15
|
-9.91±0.09
|
3.34±0.03
|
4.31±0.06
|
871.54±0.94
|
LG07
|
128.87±1.91
|
1.79±0.12
|
49.52±0.93
|
111.16±1.1
|
-11.63±0.11
|
-8.96±0.09
|
2.82±0.01
|
4.48±0.11
|
876.09±1.09
|
LG08
|
131.48±1.72
|
2.17±0.14
|
49.20±0.79
|
112.90±1.3
|
-10.97±0.09
|
-8.31±0.08
|
2.71±0.02
|
4.58±0.12
|
885.13±1.91
|
DU, degree of unsaturation; LCSF, chain length saturated factor; CN, cetane number; IV, iodine value; CFPP, cold filter plugging point; CP, cloud point; OS, oxidation stability; KV, kinematic viscosity; D, density. Error bars are standard deviations (SD) of three biological replicates.
Construction of prediction model for biodiesel properties of raw fruit oils from different accessions
Determining biodiesel fuel property is very difficult because it takes a lot of time and cost and thus several attempts have been made to use effective methods to calculate or predict fuel property of biodiesel [26, 30, 31]. Recently, triangular predict model was constructed to effectively evaluate fuel properties of biodiesel based on FA compositions of raw oils from developing P. sibirica and L. glauca fruits [9, 14]. Such prediction as an attempt was performed here. To this end, the percentages of SFA, MUFA and PUFA in L. glauca fruit oils of all accessions (Figure 1c) were used as three angular points to establish a triangular graph (Figure 2), in which one specific region (marked in gray) was delineated to predict biodiesel fuel property for fruit oils from all accessions, taking into account the satisfactions of key fuel properties (CN, IN, CFPP, OS and CP). All accessions were presented in the gray area of our constructed triangular graph (Figure 2), of which accession LG06 was located at the far end of PMFA angular point (lower left vertex) and SFA angular point (lower right vertex), indicating that the fruit oils from all accessions (especially LG06) may be as potential material for biodiesel, coincided with our evaluated results of fuel properties for different accessions (Table 2). Thus, triangular predict model for fuel properties by FA compositions of raw oils could provide simple and effective selection of ideal plant resource biodiesel.
Together, the accession (LG05/06/07) with high fruit oil content and biodiesel yield, and ideal fuel property, could be suitable for high-quality biodiesel production. Yet, another question was the mechanism that governed such difference in oil content and FA composition of L. glauca fruits across all accessions (Figure 1a and Table 1). Effective increases in oil content and ideal FA profile require to unravel complex metabolic regulation network. Thus, in the following, our work focused on the identification of key regulators (enzymes, transcription factors and transporters) specific for carbon source supply and oil synthetic process (FA synthesis and TAG assembly) by the comparative analysis of cross-accessions association of fruit oil content with gene transcript level.
Transcript differences of carbon allocation specific for acetyl-CoA generation in fruits of different accessions
In oil plants, acetyl-CoA, one vital precursor for FA synthesis, is mainly derived from PYR via glycolysis or GAP via PPP in both cytosol and plastid by a series of regulatory enzymes [22, 32, 33]. Recently, our transcriptomic assay showed that oil accumulation of developing L. glauca fruits was regulated by differential transcripts of enzymes between plastidic and cytosolic glycolysis [14], including ATP-dependent phosphofructokinase (PFK), hexokinase (HXK), fructose-bisphosphate aldolase (FBA), phosphoglycerate kinase (PGK), triosephosphate isomerase (TPI), enolase (ENO), GAP dehydrogenase (GAPC) and pyruvate kinase (PK). To determine the relative flux of PYR from plastid or cytosol glycolysis destined to oil production in the fruits of different accessions, transcript differences of all enzymes of two glycolytic pathways were analyzed in the fruits of all accessions by qRT-PCR. The transcript levels of plastid glycolytic enzymes (HXK, PFK, FBA, TPI, GPI, GAPC, PGK, PGM, ENO1 and PK) increased with the increasing amount of fruit oils across all accessions, of which the richest transcripts were all noted for accession LG06 with the highest oil content (Figures 1a and 3a). Yet, all cytosolic isoforms showed less transcript across all accessions (Figure 3b). All these revealed a major role of plastid glycolysis in supply PYR for FA synthesis in the fruits of all accessions. Another note with regard to glycolysis was about transporter in interchange of glycolytic intermediate between cytosol and plastid [9, 34-36]. Given that the orthologs for triose phosphate transporter (TPT), G6P transporter (GPT1/2), phosphoenolpyruvate transporter (PPT1/2), xylulose 5-phosphate transporter (XPT), glycolipid transporter (GLT), and bile acid/sodium symporter (BASS2) was marked in developing L. glauca fruits by recent transcriptome analysis [14], it was crucial to explore which of them may contribute to transport glycolytic metabolite from cytosol into plastid for fruit FA synthesis of different accessions. Only GPT1, PPT1 and BASS2 showed high transcript and a high correlation to the amount of fruit oils across all accessions (Figures 1a and 3c), indicating that GPT1/PPT1/BASS2 may contribute to allocate cytosolic glycolytic metabolites (G6P, PEP or PYR) into plastid for FA synthesis destined to the eventual oil production in L. glauca fruits of all accessions.
Aside from glycolysis, FA synthesis was fed by GAP via PPP [9, 37, 38]. Our recent annotation of a complete plastidic PPP with differential transcripts in developing L. glauca fruits by transcriptome assay [14], allowed to address whether the fruit oil contents of different accessions were correlated to the increasing number of their transcripts. All enzymes of plastidic PPP, including 6-phosphogluconate dehydrogenase (6PGDH), transaldolase (TA), 6-phosphogluconolactonase (PGLS), G6P dehydrogenase (G6PDH), ribulose-5-phosphate (RP) epimerase (RPE), RP isomerase (RPI) and transketolase (TK), were detected with the abundantly coordinated transcripts of all accessions by qRT-PCR (Figure 3d), and their transcript levels were associated with the amount of fruit oils across all accessions (Figures 1a and 3d), pointing to a role of plastidic PPP in provision of GAP for FA synthesis.
Another was concerned about acetyl-CoA generation from PYR via acetyl-CoA synthetase (ACS), ATP-citrate lyase (ACL), or PYR dehydrogenase complex (PDC) [33, 39], all of which were marked with differential transcripts in developing L. glauca fruits by our recent transcriptome assay [14]. Hence, we performed the cross-accessions comparisons of transcripts to explore which of them may specifically devote to allocate PYR flux for acetyl-CoA formation destined for FA synthesis in all accession fruits. High transcript of plastidic PDC was closely consistent with the increase of fruit oil content across the accessions (Figures 1a and 4), while transcript level of cytosolic ACLB subunits (ACLB-1/-2) showed no notable up-regulation, and less transcript was detected for mitochondrial PDC, cytosolic ACLA and plastidic ACS (Figure 4), implying that plastid PDC may mostly contribute to acetyl-CoA formation for FA synthesis in all accession fruits. Also of note was the roles of cytosolic ACLB and mitochondrial PYR carrier (MPC), citrate synthase (CS) and dicarboxylate/tricarboxylate carrier (DTC) in cytosolic acetyl-CoA generation for FA elongation [9]. Here, low transcript of mitochondrial MPC, CS4 and DTC was similar to that of cytosolic ACLB and mitochondrial PDC (Figures 3c and 4), corresponding to small amount of C20:0 and C20:1 in fruit oils (Table 1), pointing to a role of them in providing cytosolic acetyl-CoA for FA elongation.
Transcript differences of enzymes and transporters for FA and TAG synthesis in fruits of different accessions
Increasing FA and TAG synthesis and storage oil yield would expand economic value for oil plants [9, 40]. Given differential transcripts of oil synthesis enzymes noted in developing L. glauca fruits by our recent transcriptome assay [14], it was necessary to explore quantitative relationship between the transcript levels of oil-synthesized genes and the amount of fruit oils from all accessions. By qRT-PCR, the abundantly coordinated transcripts were detected for FA synthetic enzymes, including acetyl-CoA carboxylase (ACC), malonyl-CoA-ACP transferase (MAT), fatty acyl-ACP thioesterase A/B (FATA/B), 3-ketoacyl ACP synthase I/II/III (KAS I/II/III), 3-ketoacyl ACP reductase (KAR), hydroxyacyl-ACP dehydrase (HAD), enoyl-ACP reductase (EAR) and 18:0-ACP desaturase 6 (SAD6) in the fruits of all accessions (Figure 5a), which was the case for the enzymes for de novo TAG assembly [acyl-CoA:G3P acyltransferase 9 (GPAT9), acyl-CoA:LPA acyltransferase 2 (LPAAT2), acyl-CoA:DAG acyltransferase 1 (DGAT1) and PA phosphatase 2 (PAP2)] (Figure 5b). A strong correlation of their transcript levels with fruit oil accumulation across all accessions (Figures 1a and 5) emphasized their importance for FA synthesis and TAG assembly. Also of note was the role of FA exporter (FAX) in FA import into ER for TAG synthesis and long chain acyl-CoA synthetase (LACS) in activating free FA to produce acyl-CoA pool [9, 41-43]. High transcript of FAX1/2 and LACS4 (Figures 3c and 5b) was comparable to that of FA-synthesized enzymes (Figures 5a), and showed a pattern that correlated with fruit oil content of all accessions (Figure 1a), and thus referred that both FAX1/2 and LACS4 may be pivotal for FA export from plastid into ER for acyl-CoA pool generation destined to TAG assembly.
ER-located FAD2 and 3 is known for desaturation of C18:1 to produce C18:2 and then C18:3, respectively. Here, FAD2 showed a relative high transcript, but less transcript was marked for FAD3 (Figure 5b), both of which were matched the level of C18:2 (high) and C18:3 (less) in fruit oils of all accessions (Table 1). High transcript similar to FAD2 was noted for acyl-CoA:lysophosphatidylcholine acyltransferase 2 (LPCAT2) (Figure 5b), involved in the transfer of C18:1 into PC for desaturation and release of PUFA into acyl-CoA pool for TAG assembly [23], all of which displayed a strong correlation to the amount of C18:2 in fruit oils across all accessions (Figure 1a), implying a specific contribution of FAD2 or LPCAT2 to PUFA production. Also, lower transcript was identified for PC:DAG cholinephosphotransferase(PDCT) and CDP-choline:DAG cholinephosphotransferase (CPT) (Figure 5b), two enzymes for interconversion of DAG and PC to produce PUFA-rich TAG [23, 44], indicating its unimportance for TAG synthesis. Another was concerned for DAG acyltransferase 1 (PDAT1) for the last assembly of TAG [45], and its low transcript showed no substantial difference across different accessions (Figure 5b), reflecting a very limited contribution of PDAT1 to TAG synthesis in the fruits of all accessions.
Transcript differences in transcription factors for regulating fruit oil accumulation of different accessions
Transcription factors (TFs) have shown to regulate oil biosynthesis of oil plants. Recently, differential transcripts were annotated for the TFs (ABI3, LEC1, WRI1, FUS3, AP2, GL2, HSI2, TT2, PKL and VAL2) in developing L. glauca fruits by our transcriptome analysis [14], which allowed us to explore the possible association of their transcript levels with accumulative amount of fruit oils across all accessions. Here, the transcripts of ABI3, LEC1 and WRI1 increased with the increase in fruit oil content of all accessions, while the transcripts of AP2 and GL2 showed a downtrend with the increase in fruit oil content, and less transcript was detected for TT2, FUS3, HSI2, VAL2 and PKL across all accessions (Figures 1a and 6), reflecting a complex transcriptional regulation for fruit oil synthesis of different accessions. Also, we performed the protein interaction analysis for the above TFs and oil-synthesis enzymes as an attempt to highlight TF-mediated regulation mechanism for fruit oil biosynthesis, and found that the enzymes for oil accumulation (carbon source supply, FA synthesis and TAG assembly) were highly associated with WRI1, and LEC1 showed a strong interaction with WRI1 (Figure 7), and thus considered that LEC1 and its targeted WRI1, located in the center position of interaction network, may contribute to regulate transcriptional expressions of enzymes relevant for fruit oil accumulation of all accessions.