Pongamia, a leguminous, oilseed-bearing tree, is a potential resource for renewable fuels in general and sustainable aviation fuel in particular. The present work characterizes physicochemical properties of reproductive materials (seeds and pods) from pongamia trees grown in different environments at five locations on the island of Oahu, Hawaii, USA. Proximate and ultimate analyses, heating value, and elemental composition of the seeds, pods, and de-oiled seed cake were determined. The oil content of the seeds and the properties of the oil were determined using American Society for Testing and Materials and American Oil Chemist's Society methods. The seed oil content ranged from 19 to 33 wt % across the trees and locations. Oleic (C18:1) was the fatty acid present in the greatest abundance (47 to 60 wt %), and unsaturated fatty acids accounted for 77 to 83 wt % of the oil. Pongamia oil was found to have similar characteristics as other plant seed oils (canola and jatropha) and would be expected to be well suited for hydroprocessed production of sustainable aviation fuel. Nitrogen-containing species is retained in the solid phase during oil extraction, and the de-oiled seed cake exhibited enrichment in the N content, ∼5 to 6%, in comparison with the parent seed. The pods would need further treatment before being used as fuel for combustion or gasification owing to the high potassium and chlorine contents.
Pongamia, a leguminous, n>an class="Chemical">oilseed-bearing tree, is a potential resource for renewable fuels in general and sustainable aviation fuel in particular. The present work characterizes physicochemical properties of reproductive materials (seeds and pods) from pongamia trees grown in different environments at five locations on the island of Oahu, Hawaii, USA. Proximate and ultimate analyses, heating value, and elemental composition of the seeds, pods, and de-oiled seed cake were determined. The oil content of the seeds and the properties of the oil were determined using American Society for Testing and Materials and American Oil Chemist's Society methods. The seed oil content ranged from 19 to 33 wt % across the trees and locations. Oleic (C18:1) was the fatty acid present in the greatest abundance (47 to 60 wt %), and unsaturated fatty acids accounted for 77 to 83 wt % of the oil. Pongamia oil was found to have similar characteristics as other plant seed oils (canola and jatropha) and would be expected to be well suited for hydroprocessed production of sustainable aviation fuel. Nitrogen-containing species is retained in the solid phase during oil extraction, and the de-oiled seed cake exhibited enrichment in the N content, ∼5 to 6%, in comparison with the parent seed. The pods would need further treatment before being used as fuel for combustion or gasification owing to the high potassium and chlorine contents.
In 2017, biofuel accounted for about 1.0% of global totn>an class="Chemical">al energy
consumption.[1] Production and use of renewable
alternative transport fuels, such ashydroprocessed esters and fatty
acids (HEFAs), have grown significantly over the last 5 years. In
2017, HEFA accounted for approximately 6% of total biofuel production
by energy content, contributed to in part by increased demand for
sustainable aviation fuel.[2] The market
for aviation fuel is unique from that of other transportation sectors,
in that only alternative fuels qualified by the American Society for
Testing and Materials (ASTM) D4054-19[3,4] approval process
can be substituted for the petroleum incumbent. In addition, there
is no current opportunity for electrification, particularly for long
haul flights.
Millettia pinnata, n>an class="Chemical">also called karanja or pongamia, is indigenous
to the Indian subcontinent
and Southeast Asia;[5] it is a monotypic
genus with a single known species.[6] As
a nitrogen-fixing and self-pollinating tree, pongamia can be cultivated
easily, even in nonfertile lands and waste lands,[7] and is often found in humid and subtropical environments[8,9] with minimum mean monthly temperatures ranging from 10 to 50 °C.
Optimal growth requires temperatures in the range of 16–40
°C.[10] The plant has been introduced
to humid tropical regions as well as parts of the United States.[5] In general, the pongamia tree can grow to 15–25
m in height, commence flowering at 3–4 years of age, reach
maturity in 4–5 years, and produce up to 90 kg of seeds per
year.[11] The leaves, wood, and seeds from
pongamia trees have various value-added applications.[7,11] Pongamia pods and seeds usually develop from flowering to harvest
in 8–10 months in three stages: (i) early green immature pod
stage; (ii) half brown pod stage; and (iii) late dark brown pod stage,[12] The oil content of the seeds increases with
maturity stages and remains constant after full seed maturity is reached.[12] Additional information on cultural practices
was reviewed by Morgan et al.[13]
Biofuels
have been clasn>an class="Chemical">sified as first or second generation based
on the feedstocks utilized for production (sugars, grains, or seeds
(first generation) versus nonedible lignocellulose or vegetable oils
(second generation).[14,15] Critical questions regarding
energy crops considered for second generation feedstocks include ranges
of yields, variation in the characteristics of the feedstock components,
and their capacity to be productive in lower quality environments.[15] Pongamia hasalso been recognized as a potentialfeedstock for second generation sustainable aviation fuel production
due to the high oil content of its seed, 27–39%, and the presence
of toxic and antinutritional compounds, such as pongamol, karanjin,
and glabrin, which render it inedible.[11] Pongamia oil, generally yellowish orange to brown in color, has
an energy content of 34–38.5 MJ/kg, similar to soybeanoil,
making it suitable for fuel production.[16] In addition, the oil yields from pongamia trees are in the range
of 2.0–4.0 Mg/ha/year,[17,18] slightly higher than
the inedible oil plant jatropha at 2.0–3.0 Mg/ha/year.
To date, research on pongamia oil hn>an class="Chemical">as focused almost entirely on
the production of biodiesel or direct combustion of the oil,[5,7,11,16,17,19−25] with very few published studies on sustainable aviation fuel production.[26,27] Klein-Marcuschamer et al. conducted a technoeconomic analysis of
HEFA jet fuel from pongamia oil and found it would be competitive
with petroleum jet fuel when the price of crude oil exceeded $374/barrel.[26] The modeled price of pongamia seeds was ∼$590/Mg
in 2013,[26] which is slightly higher than
the market price of soybeans (average price for soybeans in 2013 was
$538/Mg).[28] Future technological improvements
and an increased oil content in pongamia seeds reduced the price at
which would be competitive with jet fuel to $255/barrel of crude oil.[26] Cox et al. modeled the environmental impacts
of producing aviation biofuel from pongamia oil and concluded that
the pongamia pathway can realize 43% greenhouse gas abatement on a
life cycle basis (reduction in emissions relative to the reference
fossil fuel, aviation kerosene), avoid eutrophication, and reduce
water use in comparison with sugarcane.[27]
In the present study, pongamia trees grown at five locations
on
the island of Oahu in Hawaii were idenn>an class="Chemical">tified for investigation. The
essential biomass properties, including seed oil content, proximate
composition, heating value, iodine value, free fatty acid content,
and nitrogen content of the oil, seed cake, and pods were measured.
The seed oil was obtained through two different oil extraction methods,
conventional solvent extraction and mechanical extraction. The oil
properties, including the free fatty acid contents, fatty acid profiles,
phase transition temperatures, iodine values, and H/C ratios, were
determined and compared to that of commercialcanola oil. The characteristics
of oil extraction byproducts, i.e., pod and seed cake, were also determined
to explore their potential coproducts.
Materials
and Methods
Materials
Pongamia seed pods were
collected from five locan>an class="Chemical">tions on Oahu: (1) Bachman Hall, University
of Hawaii at Ma̅noa (21°17′49.60″N, 157°49′11.06″W);
(2) Foster Botanical Garden (21°19′0.92″N, 157°51′31.94″W);
(3) Ke‘ehi Lagoon Beach Park (21°19′48.09″N,
157°53′52.42″W); (4) Hawaii Agriculture Research
Center, Kunia, HI (21°22′58.9″N, 158°02′21.8″W)
(TerViva Planting); and (5) TerViva Oahu orchard, Haleiwa, HI (21°34′28.7″N,
158°03′42.4″W). Pongamia seed pods from location
(4) were provided by TerViva Inc. and collected from May 2016 to August
2018 with seven batches in total. The collected seed pods from locations
(1)–(3) and (5) were oven dried at 35 ± 1 °C for
7 days. Afterward, pods and seeds were separated, followed by additional
drying at 40 ± 1 °C for 7 days until the mass was constant.
Note that the literature review revealed that there were no common
agreements upon conditions for drying pongamia seed pods.[13]
Seed pods were hand harvested from trees
at location (4) and then (1) soaked in a bleach/water solution for
1 min, (2) placed on a mesh screen and dried in full sun for 2–3
h, and (3) stored in an air conditioned room at ∼21 °C
in loosely woven mesh bags. The seed pods from location (4) were analyzed
as received without further processing.All the dried seeds
were milled into fine powder at −196
°C using a cryogenic ball mill (Retsch Cryomill, Düsseldorf,
Germany), and the dried pods were milled to a <0.2 mm particle
size using an ultracentrifugal mill (Retsch ZM200, Düsseldorf,
Germany). Canola oil (Wesson Foods, lot number: 2130532400X23:545,
1 gallon size) was purchased from a retail grocery. A summary of the
sample preparation and oil extraction process is shown in Figure S1.
Oil Extraction
Methods
Pongamia oil
wn>an class="Chemical">as extracted from the seeds by conventional solvent extraction (CSE)
and mechanical extraction (ME). CSE was conducted using milled pongamia
seeds and hexanesas solvents. The milled sample (20–25 g)
was mixed with 250 ± 5 mL of hexane (boiling point 65.5–68.3
°C) in a 500 mL flat bottom boiling flask. The mixture was boiled
with vapor reflux on a water bath at 80 °C with a stirring bar
at 300 rpm for 60 ± 1 min. The supernatant was separated from
the residues by filtration under a vacuum (filter paper pore size,
25 μm), and the solvent was then evaporated at 70 °C with
a rotary evaporator under a vacuum to obtain oil samples. ME was conducted
using a manualoil expeller (Piteba, The Netherlands) for which the
whole seeds from location (1) were first size-reduced using a food
processor and then fed into the expeller heated with an alcohol lamp.
The oil obtained from the expeller was filtered with a 0.45 μm
syringe filter (MilliporeSigma SLHV033NS) to exclude seed particles.
Oil Fatty Acid Profile
The oil sampn>les
were converted to their correspn>onding n>an class="Chemical">fatty acid methyl esters (FAMEs)
by KOH-catalyzed transesterification. Oil samples (40 μL) were
dissolved in a mixture of 4 mL of hexane and 4 mL of KOH–methanol
solution (0.5 mol/L) and vortexed for 5 min.[29,30] After 5 min, 12 mL of saturated NaCl was added to the mixture and
vortexed for 1 min. The resulting mixture was centrifuged for 5 min
at 4000 rpm. The ∼2 mL upper phase of the liquid mixture was
filtered with a 0.45 μm PTFE syringe filter and transferred
to a 2 mL vial. This sample was analyzed using a Bruker 436-GC gas
chromatograph and SCION-MS select and single quadrupole mass spectrometer
(Bruker Corp., Billerica, MA). The gas chromatograph was equipped
with a 60 m Agilent DB1701 column (low/mid polarity (14%-cyanopropyl-phenyl)-methylpolysiloxane)
with a 15 m guard column before the back flush valve and operated
at a helium flow rate of 1.5 mL/min. A reference standard containing
10 mg/mL each of palmitic acid methyl ester, linolenic acid methyl
ester, stearic acid methyl ester, methyl cis-9-octadecenoate,
linoleic acid methyl ester, methyl cis-9-hexadecenoate,
and myristic acid methyl ester was purchased (AccuStandard, New Haven,
CT) and used for chemical identification and quantification.
Property Determination
Proximate Analysis
The milled pongamia
seeds, pods, and de-oiled seed cake were subjected to proximate ann>an class="Chemical">alysis
using a macro thermogravimetric analyzer (TGA801, LECO Corporation,
St. Joseph, MI) based on ASTM E1756,[31] E872,[32] and E1755[33] for moisture,
volatile matter, and ash content determination, respectively. The
instrument has the capacity to analyze batches of 19, ∼1 g
samples in individual ceramic crucibles. Details on the TGA measurement
process were included in the Supporting Information. Note that this study reports the amounts of ash, volatile matter,
and fixed carbon on a dry basis. The fixed carbon content was calculated
by subtracting the ash and volatile matter contents from 100%.
Ultimate Analysis
A LECO CHN628
with n>an class="Chemical">sulfur module (LECO Corp., St. Joseph, MI) was employed to determine
the carbon, hydrogen, nitrogen, and sulfur contents of pongamia seeds,
pods, oils, and seed cake. The furnace and afterburner temperatures
of the CHN628 system were set at 950 and 850 °C, respectively.
For solid phase samples, approximately 50 mg of sample was placed
in tin foil and sealed. For liquid oil samples, ∼50 mg of sample
was placed in a tin foilcup and then covered with ∼200 mg
Com-Aid (>99% Al2O3, LECO Corp., part no.
501-427)
and sealed. The sulfur content of the solid samples wasmeasured with
the sulfur module with the furnace temperature set at 1350 °C.
The solid sample (∼100 mg) was placed into a crucible and covered
with ∼1 g of Com-Cat (>95% tungsten(VI) oxide, LECO Corp.,
part no. 501-321). Sulfur analysis was not performed on the oil samples.
X-ray Fluorescence Analysis
Quantitan>an class="Chemical">tive
element analysis of the solid seeds, pods, and CSE residues (seed
cake) was performed using a Bruker S8 TIGER X-ray Fluorescence (XRF)
spectrometer (Bruker Corp., Billerica, MA) to determine the ash-forming
and nutrient elements (e.g., Na, Mg, Al, Si, P, S, K, Ca, Mn, and
Fe) and environmentally important elements (e.g., S, Cl, Ti, Pb, Cd,
As, and Hg). The pellets for XRF were prepared by: (1) mixing 4–5
g of milled sample (<200 μm in diameter) with 1–2
g of Hoechst wax C powder (Bruker AXS, ethylene bis(stearamide), C38H76N2O2, with a grain size
of approximately <10 μm); (2) pressing the mixture using
an Angstrom model 4451AE Briquet Press (Belleville, MI USA) with 40
mm steel die and a stable, applied pressure of 345 MPa held for 30
s.[34−36] The pellets obtained were mechanically stable, with 40 mm in diameter
and 4–5 mm in height, and stored in a desiccator until analyzed.
The Bruker S8 TIGER XRF uses a 4 kW (limited to 3 kW for this analysis)
water-cooled X-ray tube with an Rh anode, a 75 μm Be window,
and a 60 kV maximum acceleration voltage. Spectrum recording and evaluation
were performed with QuantExpress software using the best detection
mode (Bruker AXS). The instrument and method have been described in
detail in a previous study.[34]
Other Physicochemical Properties
A Parr 6200 Isopn>eribol calorimeter
(Parr Instrument Company, Moline, IL) was used to measure the heat
of combustion based on ASTM D4809[37] and
reported as the higher heating value (HHV).A Setaflash Series 8 closed cup flash
point analyzer (model 82000-2 U) was used to measure the flash point
of oil samples according to the ASTM D3828 method[38] (hot wire ignition).The free fatty acid contents (FFAs)
and iodine values (IVs) of the pongamia oils were determined using
American Oil Chemist’s Society (AOCS) methods Ca 5a-40[39] and Cd 1d-92,[40] respectively.Differenn>an class="Chemical">tial scanning calorimetry
(DSC)
analyses were conducted using a TA Q2000 system (TA Instruments, New
Castle, DE) equipped with an RCS90 temperature control, which permits
operation over the temperature range of −90 to 400 °C.
The DSC measurement method has been described in detail in a previous
publication.[41] The cooling scan was analyzed
to determine the crystallization onset temperature (FO) and the crystallization
peak temperature (FP), which reflect the low-temperature quality of
the oils.
An Anton Paar
SVM3000 Stabinger viscometer
(Anton Paar USA Inc., Ashland, VA) was used to measure the viscosity
and density of the pongamia oil samples at temperatures according
to the ASTM D7042 method.[3]The instruments and methods for the above mentioned
analysis have been described in detail in previous studies.[42,43]
Results and Discussion
Pongamia Seeds and Pods
The pongamia
pods contained one or two seeds and were collected from five locations
on Oahu, Hawaii (shown in Figure ) after reacn>an class="Disease">hing stage (iii), i.e., the late dark brown
pod stage, after naturally falling from the tree. The size of the
pods and seeds varied, but the lengths of the pods and seeds were
typically in the ranges of 4–6 and 2–3 cm, respectively.
It should be noted that pods with two seeds usually have a one bigger
seed (2–3 cm long) and one smaller seed (0.5–1 cm long).
Figure 1
Pongamia
tree, flower, seed, pod, and sampling location on Oahu,
HI, USA.
pan class="Chemical">Pongamia
tree, flower, seed, pod, and sampling location on Oahu,
HI, USA.
The five sites are witn>an class="Disease">hin 25 km
radius and have similar mean annual
temperature and solar insolation, while the other growing conditions
are different (see Table ). Locations (1) and (2) have only a single tree, whereas
locations (3)–(5) have 13, 49, and 7976 trees, respectively.
The pongamia trees at locations (1), (2), (4), and (5) are planted
in relatively deep productive soils, whereas the soil at location
(3) is a mixed fill land located within 100–150 m from a brackish
water estuary and ∼1 m above sea level.[9] Tree ages vary from <5 years at the Haleiwa location to 65 years
for the Bachman tree. Ages at the Foster and Ke‘ehi locations
are minimums based on available records. The combined total of rainfall
and mechanically applied irrigation water ranges from 1900 to 2500
mm per year, with the Bachman and Kunia locations at the lower end
of the range and the remaining three sites toward the upper end. Yellowed
leaves are often apparent on trees at location (3), possibly due to
heat, drought, or salt stress.[9]
Table 1
Environmental Factors at the Five
Locations of Pongamia Trees on Oahu, HI, USA
location
elevation (m)
soil type
mean annual
rainfall (mm)
annual supplemental irrigation
water (mm)
solar insolation (kWh m–2 d–1)
mean annual temperature (°C)
tree age (years)
Bachman
21
Makiki stony clay loam
931
972
5.2–5.8
23.5
63
Foster
6
Ka‘ena clay
833
1737
5.2–5.8
23.8
>47
Ke‘ehi
1
fill land, mixed
695
1862
5.2–5.8
23.7
>35
Kunia
72
Moloka‘i silty clay loam
621
1321
5.2–5.8
23.3
<5
Haleiwa
208
Wahiawa
silty clay
1050
1321
5.2–5.8
22.3
<5
Figure presents
the proximate analyn>an class="Chemical">sis results of the seeds and pods; data and error
estimates are presented in Tables S1 and S2. The values reported for location (4) are averages of seven batches;
data for individual batches are included in the Supporting Information. The slightly higher volatile matter
of the seeds from locations (4) and (5) compared to locations (1)–(3)
results from their higher oil content, all >25 wt % ( see Table and Table S8). Materials from trees under stress at location (3)
had comparable proximate analysis results to those collected from
locations (1) and (2). As expected, the fixed carbon content of the
pods are all higher than the seeds, ∼6–11 wt % (absolute),
and the values from all locations differ by <3% (absolute). In
general, the VM/FC ratio is regarded as an indicator of the reactivity
or combustibility of biomass. The VM/FC ratios of the seeds from locations
(1)–(5) are approximately 100% (relative) greater than those
of the pods from the corresponding locations. This higher reactivity
results from the volatile/combustible oil present in the seeds.[44]
Figure 2
Proximate analysis results of pongamia seeds, pods, and
de-oiled
cake; x axis labels refer to locations in Figure .
Table 2
Properties of Pongamia Seeds, Pods,
and Seed Cake after Conventional Solvent Extraction with Soybean Seed
Cake Data Shown for Comparisona
seed
pod
cake
location
H/C
XRF ash wt
%
oil content (%)
H/C
XRF ash wt %
H/C
XRF ash wt
%
Bachman
1.81
3.12 ± 0.22
24.82 ± 1.09
1.68
5.64 ± 0.06
1.76
3.24 ± 0.01
Foster
1.88
3.44 ± 0.28
22.26 ± 2.34
1.74
6.01 ± 0.01
1.77
4.63 ±
0.13
Ke‘ehi
1.85
2.84 ± 0.16
19.65 ± 1.56
1.71
6.61 ± 0.02
1.77
3.39 ± 0.03
Kunia
1.92
N/A
26.86 ± 1.86
1.80
6.23 ± 0.80
1.95
4.17 ±
0.19
Haleiwa
1.85
N/A
32.45 ± 0.27
1.65
3.88 ± 0.06
1.89
4.76 ± 0.04
(1) XRF ash wt % values are calculated
with the C6H10O5 matrix as the mean
± standard error of six analyses (3 pellets and 2 sides); (2)
XRF analysis was not conducted for Kunia and Haleiwa seeds due to
high oil contents; and (3) the Kunia values are averages of seven
sample batches.
Proximate analysis results of pongamia seeds, pods, and
de-oiled
cake; x axis labels refer to locations in Figure .(1) XRF ash wt % values are calculated
with the C6H10O5 matrix as the mean
± standard error of six analyses (3 pellets and 2 sides); (2)
XRF analysis was not conducted for Kunia and Haleiwa seeds due to
high oil contents; and (3) the Kunia values are averages of seven
sample batches.The ash
content of the pod sampn>les wn>an class="Chemical">as ∼2–3% (absolute)
higher than the seed samples at all locations. This is consistent
with the lower energy content of the pods (shown in Figure ) compared to the seeds. A
similar trend was observed when the mass fractions of the oxide forms
of the elements identified by XRF are summed (listed in Table ). The greater ash content of
the pods compared to the seeds is associated with the significantly
increased amounts of several elements, i.e., sodium (Na), chlorine
(Cl), potassium (K), calcium (Ca), and silicon (Si) shown in Tables S3 and S4. The pods collected from location
(5) have a slightly lower ash content in comparison with other four
locations, which may be associated with tree age or increased water
supply (rainfall + irrigation). Prasad et al.[45] also conducted a proximate analysis on pongamia pods collected from
New Delhi, India (see Table S2). Although
the volatile matter and fixed carbon content of the pod samples reported
by Prasad et al.,[45] 80.13 and 13.42%, respectively,
are different from the values obtained in this study, the ash content
of the pod samples, 6.45%,[45] is within
the range of the values obtained in this study, i.e., 4.09–6.67
wt %. The energy content (HHV) of the pods reported by Prasad et al.,[45] 16.81 MJ/kg, is comparable to the values of
the pods collected at sites (1), (2), (3), and (5). Location (4) was
slightly lower, 16.01 MJ/kg.
Figure 3
Energy content analysis results of pongamia
seeds, pods, de-oiled
cake, and oil; legend labels refer to locations in Figure .
Energy content analysis results of pongamia
seeds, pods, de-oiled
cake, and oil; legend labels refer to locations in Figure .Proximate analysis results obtained from macro thermogravimetric
analysis were in good agreement with the results obtained from conventionalmethods, see Figure S1. The root mean square
deviation between the TGA and conventionalmeasurements is 1.21%.
This confirms the interchangeability of the automated LECO TGA method
and the manualASTM method for determining proximate analysis.Ultimate ann>an class="Chemical">alysis results of seeds and pods are shown in Figure A–C; complete
data and error estimates are presented in Tables S1 and S2. The seed samples generally have a higher carbon
content and hydrogen content in comparison with the pod samples (shown
in Figure A). The
carbon and hydrogen contents of the seeds from locations (3) and (4)
are higher than that of the other locations due to the higher oil
content of the seeds. As observed in the proximate analysis, the carbon
and hydrogen contents of the pod samples did not show significant
differences that could be attributed to tree locations. The H/C ratio
calculated from the ultimate analysis (listed in Table ) is an indicator of the combustibility
of the fuel,[46] and the greater H/C ratios
of the seeds in comparison with pods agree with the trends predicted
by the VM/FC ratio.
Figure 4
Ultimate analysis results of pongamia seeds, pods, and
de-oiled
cake: (A) summary of C, H, and N analysis; (B) nitrogen content analysis;
and (C) sulfur content analysis: x axis labels refer
to locations in Figure .
Ultimate analysis results of pongamia seeds, pods, and
de-oiled
cake: (A) summary of C, H, and N analysis; (B) nitrogen content analysis;
and (C) sulfur content analysis: x axis labels refer
to locations in Figure .The nitrogen contents of the seeds
and pods vary with the sampn>ling
locan>an class="Chemical">tion (shown in Figure B). Overall, the nitrogen contents of the seed samples are
at least three times greater than that of the corresponding pod samples,
indicative of a higher seed protein content.[47] The highest nitrogen contents of seeds were from location (3), the
site with the most severe environmental conditions. Location (2) has
the highest pod nitrogen content of the five locations, but all were
in a range from 0.7 to 1.2 wt %. Figure C displays the sulfur content of the pongamia
seeds and pods. Similar to the nitrogen content, the sulfur content
of the seeds from all five locations is at least twice that of the
corresponding pods. Seeds and pods from location (4) have the highest
sulfur contents, 0.25 and 0.12 wt %, respectively. Although clean
wood fuels typically contain <0.1 wt % sulfur, the sulfur content
of pongamia seeds and pods is still far lower than coal.
Figures and 6 present the XRF analyn>an class="Chemical">sis results of the pongamia
seeds and pods, respectively (data and error estimates presented in Tables S3 and S4). The limit of detection (LOD),
defined as the minimum detectable concentration of an element in a
matrix, is also included. The LOD value is the average based on all
the measurements on the seed, pod, and de-oiled cake materials in
the wax pellets/matrix. Samples with element concentrations higher
than the LOD are reported in tables. The XRF system background was
determined by analyzing blank samples, i.e., Hoechst wax C powder
binder. Results indicate that the XRF system background has trace
amounts of Ru (21.6 ± 1.2 ppm), Fe (8.4 ± 0.6 ppm), and
Cu (4.9 ± 0.7 ppm). XRF limits of quantification (LOQ) four times
of the LOD were used for this study. The LOQ is the minimum concentration
that the system can quantify accurately. XRF analysis was not conducted
on seeds from locations (4) and (5) because their high oil content
prevented the formation of a stable pelleted sample.
Figure 5
XRF elemental analysis
results of pongamia seeds; legend labels
refer to locations in Figure . XRF analysis of seeds from other two locations was not conducted
because their oil content prevented the formation of a stable pelleted
sample.
Figure 6
XRF elemental analysis results of pongamia pods;
legend labels
refer to locations in Figure 1.
XRF elemental analysis
results of pongamia seeds; legend labels
refer to locations in Figure . XRF analysis of seeds from other two locations was not conducted
because their oil content prevented the formation of a stable pelleted
sample.XRF elemental analysis results of pongamia pods;
legend labels
refer to locations in Figure 1.As observed in the ash content from the proximate analysis, the
total mineral content of pods is much higher than the corresponding
seeds from locations (1)–(3). Of the elements quantified with
XRF, potassium is present in the highest concentrations in both seeds
and pods, ranging from 0.9 to 1.2 and 1.8 to 3.4 wt %, respectively.
Phosphorus (P) and Ca are both present in roughly equal concentrations,
0.25 to 0.35 wt % in the seed. Ca occurs in a wider range of concentrations
in the pod, 0.4 to 1 wt %, but P is reduced to levels of 200–500
ppm. Magnesium and sulfur are present at levels above 1000 ppm in
the seed with the remaining elements present at concentrations below
this benchmark.The Na content of the pods is approximately
six n>an class="Chemical">times higher than
that of seeds from locations (1) and (2), and over 12 times higher
for location (3). The Na contents of seeds from all three locations
are similar, <0.05 wt %, whereas the Na content of the pods from
location (3) is ∼1.5 to 4 times higher than the other four
locations. The Cl content of pods wasalso elevated compared to seed
values. The molar ratio of Na:Cl for the seed and pods varied from
0.70 to 1.19 and 0.27 to 0.79, respectively. The elevated concentrations
in the pods and the molar ratio values suggest origins resulting from
dry and wet deposition of both elements on the external surface of
the pod due to proximity (∼100 m to 3 km) to the ocean. The
water table at the Ke’ehi Lagoon location (100–150 m
from the ocean) is tidally influenced,[48] indicating that pongamia is to some degree salt tolerant.[49] Salinity measurements at nearby monitoring wells
recorded salinity levels of 0.5%, a sevenfold dilution compared to
seawater.[48]
Sulfur concentran>an class="Chemical">tions
in the seeds and pods at the five locations
were determined by both LECO CHN628sulfur module (Tables S1 and S2) and Bruker XRF (Tables S3 and S4), except for seeds from locations (4) and (5). The
two measurement methods are in general agreement, with most of the
differences falling within the levels of the reported measurement
error for the pods. The LECO S values for the seeds were consistently
higher than the XRF values, and the differences ranged from 200 to
550 ppm, 1.7 to 9.4 times the value of the corresponding XRF measurement
error.
Required plant micronutrients include Fe, n>an class="Chemical">Zn, Mn, Mo,
Cu, and B.
Fe was quantified in both the seed and pods at concentrations of 40–60
and 25–115 ppm, respectively. The higher concentrations of
the pods may be due to soil dust deposited on their external surfaces.
Zinc present at concentrations of ∼30 ppm wasmeasured in the
seed samples but were below the LOQ or undetectable in the pods. Mn
was only present above the LOQ in the Haleiwa pod material. Mo was
detected in all pod samples but only locations (3) and (4) contained
amounts greater than the LOQ. Copper was detected in all seed and
pod samples but was only slightly (<3 ppm) above the LOQ in two
samples. Boron was not detected in any of the samples.
Strontium
(n>an class="Chemical">Sr) was detected in both seed and pod materials, in
ranges from 19 to 61 and 30 to 170 ppm, respectively. Basalt lava,
Asian dust, and rainfall (ocean derived) are the three main sources
of Sr in Hawaii.[50] Although the origin
of the Sr was not determined in these pongamia samples, Sr quantified
in leaf tissue samples of Metrosideros polymorpha, an ‘o̅hi‘a lehua tree endemic to Hawaii, was
determined to be of soil origin.
These preliminary property
analyn>an class="Chemical">sis results indicate that Milletia pinnata seeds are a source of protein, and
the pods have potential use as energy or byproduct feedstock. The
seeds have a comparably high protein content, 17–21% (based
on nitrogen content analysis and a Jones factor of 5.18 for seeds
and nuts),[47] and the nitrogen concentration
of the seeds and pods do not appear to be significantly affected by
adverse growing conditions, as demonstrated at location (3).
As fuels conn>an class="Chemical">sidered for thermochemical energy conversion, the pods
have desirably low sulfur and nitrogen contents. The elevated K and
Cl concentrations, however, will require attention if pods are considered
for combustion and gasification applications.[51,52] Their concentrations in the fuels range from 1.3 to 2.6 kg (Na2O + K2O) GJ–1 and 0.13 to 0.7
kg Cl GJ–1. Prior experience indicates that ash
from fuels with values of >0.33 are almost certain to produce fouling
and slagging without active management. Miles et al.[53] reported a K concentration of ∼27,000 ppm in almond
hulls and found K-enriched deposits accumulated on simulated boiler
tubes under combustion conditions. More than 80% of the potassium
and 100% of the chlorine present in almond hulls were water-soluble.
Opportunities to improve fuel properties of pongamia pods that should
be explored as post-harvest processing techniques are developed. Fuel
additives, advanced reactor designs, and conversion system operating
strategies can also contribute to controlling impacts.
Pongamia Oil
Table lists the oil content of the seeds from
locan>an class="Chemical">tions (1)–(5) using the conventional solvent extraction
(CSE) method. The seeds from location (3) were found to have the lowest
oil content, which may result from its more severe growth condition.[9] The seeds from the younger trees at locations
(4) and (5) exhibited a higher oil content compared to the older trees
at locations (1)–(3). Figure shows the fatty acid composition of the pongamia seed
oils (data and error estimates are presented in Table S5) along with that of canola, soybean,[54] jatropha,[54] and carinata oil.[55] The fatty acid profile of pongamia oil varies
with location, but the major acid is oleic (C18:1) in all cases, 47.4–60.1
wt %. This is consistent with the 41.4 to 71.3% range of the C18:1
content in pongamia oil reported in the literature.[13,16] The major difference between the profiles is the linoleic acid (C18:2)
content. In location (1), its concentration is approximately 30–100%
(relative) higher than that from other four locations. The fractions
of unsaturated fatty acid present in oil from location (1), 82.61
and 82.09 from the CSE and ME processes, respectively, are similar
to the values obtained from locations (4) and (5) but approximately
5% (absolute) higher than that from locations (2) and (3).
Figure 7
Fatty acid
profile of pongamia oils in comparison with that of
canola, soybean,[54] jatropha,[54] and carinata oil:[55]x axis labels refer to locations in Figure ; CSE and ME are conventional
solvent and mechanical extraction, respectively
Fatty acidprofile of pongamia oils in comparison with that of
canola, soybean,[54] jatropha,[54] and carinata oil:[55]x axis labels refer to locations in Figure ; CSE and ME are conventional
solvent and mechanical extraction, respectivelyThe overall n>an class="Chemical">fatty acid profile of the pongamia oil is somewhat
similar to canola and jatrophaoils (Figure ) for which the major fatty acid is also
C18:1, 73.7, and 42.8 wt %, respectively, followed by C18:2, 11.8,
and 35.4 wt %, respectively. The unsaturated acid fraction of pongamia
oil (77.0–82.6 wt %) is closer to the values of soybean and
jatrophaoils, 83.57 and 78.48 wt %, respectively,[54] than to the canola oil, 92.85 wt %. Brassica
carinata, a promising oil crop for the southeastern
and northern United States, however, exhibits a significantly different
fatty acid profile in comparison with soybean, jatropha, and pongamia,[55] and over 40% of the fatty acid profiles are
heavy erucic acid (C22:1). Note that HEFA jet fuel typically contains
C8 to C19 hydrocarbons.[56]
The physicochemicn>an class="Chemical">al
properties of pongamia seed oil obtained from
CSE and MEmethods and commercialcanola oil were measured; results
are presented in Table . In general, the presence of free fatty acids (FFAs) in vegetable
oils is associated with cells in the parent seed tissue damaged during
the harvesting, storage, transportation, or initial processing. Up
to 5% FFA may be found in crude vegetable oils.[57] The FFAs of the oils from all five locations were found
to be of a normal level (i.e., <5%) and within the range reported
by Gaurav and Sharma,[16] 2.53–20%.
It should be noted that the FFAs of oil from locations (1)–(3)
were only measured once without repetition due to sample limitation.
Seeds from location (1) were extracted using both ME and CSE processes,
and oil from the former was found to have a slightly higher FFA content.
This may result from the alcohol lamp used to heat the expeller during
the ME process, as cell damage can occur under elevated temperature
conditions,[57] or it may be due to a less
effective extraction resulting in only partial recovery of oil components.
The FFA of commercialcanola oil is much lower, only 0.1%, in comparison
with the pongamia oil obtained in this study (0.57–2.67%),
as most of the FFAs in commercialcanola oil have been removed in
the refining process.[58] The HHVs of the
pongamia oil obtained from the five locations are very similar and
close to that of commercialcanola oil. The iodine values of the oils
extracted from locations (1)–(3) are all close to the literature
reported range for pongamia oils, 85–110,[59,60] and lower than that of canola oil, which is consistent with the
fatty acid profile analysis results shown in Figure . The iodine values of oil from locations
(4) and (5), however, are significantly lower than that from other
three locations, even though their unsaturated fatty acid fraction
is similar to that from location (1). The pongamia oil obtained from
the ME process in location (1) wasalso subjected to flash point,
kinematic viscosity, and density measurements. The flash point of
the oil from location (1), 210 ± 2 °C, is within the range
reported by Gaurav and Sharma,[16] 205–270
°C, and much lower than that of canola oil, 315 ± 2 °C,
whereas the kinematic viscosity (46.764 mm2 s–1 at 40 °C) and density (0.9415 g cm–3 at 15
°C), are slightly higher than the reported ranges, 27.84–38.2
mm2 s–1 at 40 °C and 0.912–0.940
g cm–3 at 15 °C, respectively.[8]
Table 3
Summary of Measured Properties of
Pongamia Oil from Trees in Five Locations on Oahu and Commercial Canola
Oil (Shown for Comparison)a
properties
Bachman-ME
Bachman-CSE
Foster-CSE
Ke‘ehi-CSE
Kunia-CSE
Haleiwa-CSE
canola oil
C wt %
77.2 ± 0.24
77.28 ± 0.20
77.24 ± 0.15
76.88 ± 0.19
76.31 ± 0.30
76.45 ± 0.14
77.37 ± 0.22
H wt %
11.4 ± 0.03
11.55
± 0.05
11.78 ± 0.04
11.78 ±
0.10
11.78 ± 0.10
11.98 ± 0.01
12.41 ± 0.05
O wt %
11.2 ± 0.21
11.17 ± 0.24
10.97
± 0.19
11.33 ± 0.21
11.91 ±
0.31
11.57 ± 0.15
10.13 ± 0.20
FFA %
0.92
0.63
2.67
0.57
0.71 ± 0.06
0.37 ± 0.02
0.10 ± 0.00
iodine value
93.9 ± 0.3
85.0 ± 0.5
72.94 ± 0.23
71.5
± 1.2
51.8 ± 13.6
44.6 ±
1.2
114.4 ± 2.7
H/C
1.78
1.79
1.83
1.83
1.85
1.88
1.93
Tonset/°C
4.05
5.35
15.49
15.16
1.37 ± 0.25
6.88
–22.59
Tpeak/°C
2.98
4.47
15.13
14.34
0.25 ± 0.63
4.7
–58.39
HHV MJ kg–1
35.18 ± 0.12
38.50 ± 0.09
38.93 ± 0.14
38.85 ± 0.00
38.20 ± 0.28
38.71 ± 0.32
39.31
± 0.09
(1) Iodine value is the mean ±
standard error for three analyses; (2) FFA values for Bachman, Foster,
and Ke‘ehi Lagoon and all oil flash point values are reported
from a single measurement due to limited sample mass; the flash point
standard error is the system analysis uncertainty, 2 °C; (3) Tonset and Tpeak values
are determined from a single analysis; and (4) the Kunia values are
averages of seven sample batches.
(1) Iodine vn>an class="Chemical">alue is the mean ±
standard error for three analyses; (2) FFA values for Bachman, Foster,
and Ke‘ehi Lagoon and all oil flash point values are reported
from a single measurement due to limited sample mass; the flash point
standard error is the system analysis uncertainty, 2 °C; (3) Tonset and Tpeak values
are determined from a single analysis; and (4) the Kunia values are
averages of seven sample batches.
The ultimate ann>an class="Chemical">alysis results of the pongamia oil
obtained in this
study and commercialcanola oil are listed in Table . The nitrogen content of all the oil samples
was not included, as the values were below the detection limit (<200
ppm based on the ∼50 mg sample used for analysis, LECO CHN628
system N detection limit: 0.01 mg). The oxygen content was calculated
by subtracting the carbon and hydrogen contents from 100. The carbon
contents of the oil samples are tightly grouped, whereascanola oil
possesses a slightly higher hydrogen content, which results in its
slightly higher HHV (also shown in Figure ) and H/C ratio.
The low-temperature
properties of n>an class="Chemical">pongamia oil obtained from the
five locations and two extraction methods were investigated using
DSC, and the results were compared with those for canola oil. Figure presents the cooling
scan of the oil samples. Oils with a higher degree of unsaturation
usually have lower solid–liquid phase transition temperatures.
The results confirm this, as the CSE pongamia oil from locations (1),
(4), and (5) exhibited lower crystallization onset temperatures, 5.35,
1.37, and 6.88 °C, respectively, in comparison with that from
locations (2) and (3), 15.79 and 15.16 °C, respectively, consistent
with the fatty acid profile. Owing to its higher fraction of unsaturated
fatty acids, the crystallization onset temperature of canola oil,
−22.59 °C, is significantly lower than that of pongamia
oils. As expected, the oils obtained from ME and CSE processes have
similar low-temperature properties, i.e., the crystallization onset
temperatures from location (1) are 4.05 and 5.35 °C, respectively.
Figure 8
DSC cooling
curve of pongamia oils: legend labels refer to locations
in Figure ; CSE and
ME are conventional solvent and mechanical extraction, respectively.
DSC cooling
curve of pongamia oils: legend labels refer to locations
in Figure ; CSE and
ME are conventional solvent and mechanical extraction, respectively.
De-oiled Pongamia Seed
Cake
The characteristics
of the de-oiled pongamia seed cakes obtained from CSE were determined
and compared with that of a soybean cake.[61] Similar to the seeds, the pongamia cake from locations (1)–(5)
have a similar volatile matter, ash, and fixed carbon content (shown
in Figure ), and the
results are consistent with literature values.[62] The pongamia cake samples exhibited slightly higher ash
and fixed carbon contents in comparison with the corresponding seed
samples due to the removal of the volatile organic oil fraction from
the seeds. In addition, pongamia cake possesses a lower ash content
than that of a soybean cake, 6.14 wt %.[61]The ultimate ann>an class="Chemical">alysis of the cake samples in Figure A shows that the soybean cake
has a lower H/C ratio, 1.41,[61] than the
pongamia cakes (listed in Table ) owing to the higher carbon content in soy meal. The
soybean cake, however, exhibited a greater heat of combustion, 23.23
MJ/kg,[61] than that of the pongamia cake
(shown in Figure ).
The HHVs of pongamia cakes from location (3) are slightly higher than
those from other four locations, although the HHVs of the seed from
location (5) are the highest. Similar to the fixed carbon content
obtained from proximate analysis in Figure , the pongamia cake samples were also found
to have higher nitrogen (Figure B), sulfur (Figure C), and metal (i.e., Na, Mg, P, Cl, K, and Ca shown
in Figure ) contents
in comparison with the corresponding seed samples (Figure ), as the oil samples are mainly
composed of hydrocarbons. The de-oiled seed cake exhibited enrichments
in N and S compared to the parent seed, indicating that nitrogen and
sulfur are retained in the seed cake during oil extraction. Thus,
the seed cake may serve as a source of protein, 17–21% protein
content (based on nitrogen content analysis and a Jones factor of
5.18 for seeds and nuts).[47]
Figure 9
XRF elemental
analysis results of de-oiled seed cake; legend labels
refer to locations in Figure .
XRF elemental
analysis results of de-oiled seed cake; legend labels
refer to locations in Figure .
Conclusions
Seeds and pods collected from pongamia trees grown in five different
locan>an class="Chemical">tions on the island of Oahu in Hawaii were studied. The physicochemical
properties of the seeds, pods, oils, and the de-oiled seed cakes were
determined and compared with those from pongamia trees grown in South
Asia and other oil plants. The oil content of pongamia seeds was found
to range from 19 to 32.5% with younger trees producing higher oil
concentrations. Although the fatty acid profiles of the extracted
oils varied with collection location, oleic (C18:1) and linoleic (C18:2)
acids were present in the highest concentrations in all samples. The
qualities of the pongamia oil are similar to those of jatropha and
canola oils in groups that also included soybean and carinata. The
pongamia seed cakes after oil extraction were found to have a nitrogen
content of ∼5 to 6%, which may be used as a protein source.
The pods contained high concentrations of potassium (∼1 to
3%) coupled with elevated chorine contents and will require management
to avoid deposition and fouling at temperatures typical of combustion
and gasification conditions. Future research on pretreatment and thermochemical
conversion of aged trees removed from production and residues derived
from pongamia seed processing, such as pods and seed cakes, should
be pursued.