Marco
Piccini
a,
Sofia
Raikova
a,
Michael J.
Allen
cd and
Christopher J.
Chuck
*b
aCentre for Doctoral Training in Sustainable Chemical Technologies, Department of Chemical Engineering, University of Bath, Claverton Down, Bath, UK BA2 7AY
bDepartment of Chemical Engineering, University of Bath, Claverton Down, Bath, UK BA2 7AY. E-mail: c.chuck@bath.ac.uk
cCollege of Life and Environmental Sciences, University of Exeter, Streatham Campus, Exeter, Devon, UK EX4 4QD
dPlymouth Marine Laboratory, Prospect Place, The Hoe, Plymouth, UK PL1 3DH
First published on 26th November 2018
In this investigation a novel synergistic approach for the bioremediation of metal-contaminated water and bioenergy production was developed. Two microalgae, Chlorella vulgaris and Arthrospira platensis (Spirulina), and two macroalgae, Ulva lactuca and Sargassum muticum, were used as passive bioremediation agents for the metals Ni(II), Zn(II), Cd(II) and Cu(II). The metals were added singularly and in combination between 10–150 mM. The metal contaminated biomass was then processed through hydrothermal liquefaction to yield four phases: a bio-crude oil, an aqueous phase, solid residue and gas. Both C. vulgaris and A. platensis gave high bio-crude yields of 39 and 31 wt% respectively, while U. lactuca and S. muticum gave 14% and 9% respectively. Initial studies demonstrated that the addition of up to 150 mM of the target metal sulfates to the biomass feedstock did not significantly affect bio-crude production, and, for microalgae, over 99% of the target metals were partitioned to the solid phase products predominantly as phosphates or oxides. Subsequently, bioremediation of waste water and HTL were successfully coupled, with over 80% of a 10 mM solution of the metals biosorbed, though efficacy depended heavily on the algal species. Upon HTL of the remediating biomass, the yield and composition of the bio-crude were not changed significantly. For the microalgae, the aqueous phase contained significant nitrogen, potassium and phosphate levels, and the majority of the target metals deposited in the solid phase, with over 99.5% metal recovery for Spirulina when all four metals were used. The macroalgal species were not as effective in this process, with limited phosphate recovery in the aqueous phase (albeit with extensive potassium recovery) and with less than 50% of the target metals depositing in the solid residue for the Ulva species examined, presumably due to the affinity of the metals to proteinous species rather than polysaccharide in this species. Combining microalgal bioremediation with hydrothermal liquefaction is therefore a potentially highly effective method of remediating contaminated waste waters, whilst a macroalgae based process may offer a cheaper alternative, albeit with substantially reduced efficacy. The recovery of the target metals and multiple product formation improves the economic viability of the process, thereby valorising the bioremediation process and subsidising environmental clean-up.
Recent technoeconomic analysis has demonstrated the suitability of HTL as a production process for fuels, in particular when the nutrients within the system can be recycled from the aqueous phase, and algal growth can be coupled with a service function such as waste water remediation.3 To this end, a number of studies have demonstrated the suitability of remediating municipal waste water on the pilot scale and the subsequent processing of the algal biomass via HTL, removing N and P from the water using microalgae, and subsequently partitioning them to the aqueous phase of the HTL products.4–7 From these studies, it is suggested that an energy recovery of approximately 50% and an initial solid loading of over 14% would lead to an economically viable process.8
Municipal waste waters generally contain high levels of N and P, and are suitable for algal cultivation all year round. On the other hand, a more challenging area is the bioremediation of heavy metal-contaminated effluents.9 Industrial waste waters often contain heavy metals, and their removal is conventionally achieved through physicochemical processes, including chemical precipitation, ion exchange and adsorption; such processes tend to be expensive, produce no valorisable products and often are not completely effective. The remediation of heavy metal ions using micro- and macroalgae has been heavily researched, with reports on effective remediation from a huge range of micro- and macroalgae species, including species from the genera Chlorella, Arthrospira, Ulva and Sargassum.10–12 Generally microalga can achieve efficiencies of over 95%, under optimal conditions though this necessitates a high biomass loading and extended contact time with the pollutant of hours. While this is generally slower than chemical precipitation,9 which also requires a lower loading, the additional biomass generated can be used for valorisation to reduce the costs of the initial remediation. Additional advantages are potentially lower operating costs, the high efficiency in remediating heavy metals that are present in far lower concentrations and less amount of spent biosorbent for final disposal that has no value.12
Two distinct mechanisms have been investigated: active bioadsorption, where living algae are cultured on diluted solutions of the effluent; and passive, where dead algal biomass binds the metal cations through the hydroxyl, carboxyl, sulfhydryl, amino and phosphate groups present in the proteins, carbohydrates and lipids of the cell wall via ion exchange and complexation.13 The passive adsorption mechanism relies predominantly on the type and number of active sites present and is therefore highly dependent on the properties of the algae species (such as composition, size, surface area), but also on the metal ion (size, charge), together with many additional environmental factors.
Adsorption experiments are generally conducted on single metal species solutions in order to understand the influence of characteristic parameters. It has been demonstrated that, on increasing the initial metal concentration, the metal uptake increases, but the overall efficiency decreases.14,15 One of the most important parameters for metal uptake is pH, as it influences functional group ionisation and complex formation constants. Metal bioadsorption is highly time-dependent: with live algae, the process is usually slow, and can take weeks for the algal biomass to adapt to the culture conditions and reach maximum biomass yield, whilst with dead biomass, it becomes much faster, typically occurring within tens of minutes.16,17 Under optimised conditions, many algae strains have been shown to sequestrate up to tens (sometimes hundreds) of milligrams of metal per gram of biomass.10,11 This elevated remediation potential has been gaining industrial interest, with some processes beginning to be commercialized.11,18 However, many challenges have yet to be faced, and producing an economic process will most likely rely heavily on appropriate biomass generation, supply and reuse, and metal recovery, as well as the valorisation of any products generated.
To this end, a number of studies have attempted to link bioremediation with bioenergy production. For example, Kim et al. demonstrated that an oleaginous algae, Nannochloropsis oculata, could actively remediate Cr from aqueous solutions while still producing reasonable levels of lipids for biodiesel production.19 Further studies have demonstrated this active approach, with high metal removal efficiencies of Zn, Mn, Cd, As and Cu being coupled successfully with lipid production.20–24 However, while these systems produce cleaner water, the problem of the metal contamination is transferred to the wet defatted biomass, which then requires extensive processing to be exploited in an appropriate manner.
Ideally, metals would partition to a minor fraction, which can be disposed of, recovered or reprocessed easily, with the majority of the carbon being transferred directly to the fuel product without fear of metal contamination. We recently reported on the active remediation of acid mine drainage with a mixed algal culture, which was then processed by hydrothermal liquefaction.25 The liquefaction demonstrated that large amounts of Fe had a positive effect on the crude yields, though other heavy metals present, such as Sn(II) and Pb(II), had little effect on the yield. Importantly, the heavy metals targeted were largely retained in the solid residue on liquefaction, offering a potential route to easy metal recovery and bioenergy production. This deposition of metals has also been observed in the liquefaction of swine manure,26 and naturally occuring algal blooms.27
However, in the preliminary study, the active microalgal culture did not grow effectively within the toxic environment generated by the excessive metal contamination, and took a number of weeks to remediate the industrial effluent, emphasising the limitations of the active bioadsorption approach.
To address this, in this investigation we aimed to assess the suitability of HTL to process algal biomass used in the passive bioadsorption remediation of a heavy metal mixture, with two microalgal species (C. vulgaris and Spirulina) and two macroalgal species (U. lactuca and S. muticum). All four algae represent different remediation opportunities and applications with a global footprint: Chlorella and Spirulina are the most widely cultivated microalgae globally due to their fast and reliable growth properties (Chlorella, single cellular) and ability to withstand high pH (Spirulina, chain forming); while Ulva and Sargassum are ubiquitous green and brown macroalgae, respectively, often associated with problematic blooms following eutrophication of waters. The suitability of using HTL to produce a bio-crude oil, an aqueous phase where useful nutrients can be recovered from and a solid residue that would ideally contain the target metals was assessed.
HTL was performed according to previously reported experiments.25 The mixture obtained after bioadsorption was transferred into a stainless steel reactor (approx. volume 50 mL), equipped with a thermocouple, a pressure gauge and a pressure release valve. The reactor was sealed, then placed inside a vertical tubular furnace kept at 700 °C until the temperature inside the reactor reached 340 °C (ca. 12 min), then removed and left to cool to ambient temperature (see ESI† for a typical temperature profile). The gas phase volume was measured, the reactor was opened and the reactor contents filtered through a pre-weighted Fisher qualitative paper filter, allowing the aqueous phase to be collected. Once the filter was dry, the reactor and the filter were washed with chloroform until the solvent ran clear. The solvent was then removed using a rotary evaporator to recover the bio-crude. The filter was allowed to dry to recover the solid phase. The reactions without metals for the four species were done in triplicate to calculate the standard error. This is given in the ESI.†
HHV = 0.3491 C + 1.1783 H + 0.1005 S − 0.1034 O − 0.0151 N − 0.0211 H (MJ kg−1) |
The supernatant phase obtained after bioadsorption and centrifugation was filtered through a 0.45 μm syringe filter and diluted in deionized water. Metals content was analysed by Atomic Absorption Spectroscopy on a Perkin Elmer Analyst 100.
The different phases obtained after HTL were analysed as follows:
The bio-crude yield was calculated gravimetrically from the original weight of the biomass according to the following equation:
The elemental composition (CHN) of the bio-crudes was analysed by OEA Laboratories Ltd, Callington, Cornwall, UK. (Oxygen content was calculated by difference.) The higher heating value (HHV) was calculated using the Channiwala & Parikh equation, assuming negligible ash content. Metal and P analysis was analysed using ICP-OES. Samples were digested in 4 mL aqua regia at 95 °C for 1 hour, then left to digest at ambient temperature for 24 hours before being made up to 20 mL with 10% NaOH solution in deionised water to a pH of approx. 3. The resulting solution was filtered through a 0.45 μm filter membrane prior to analysis. ICP-OES was carried out externally by Yara U.K. Ltd. using an Agilent 700 series inductively coupled plasma optical emission spectrometer.
The aqueous phase was weighed and stored at 4 °C prior to analysis. The sample was sonicated in an ultrasonic bath in order to suspend the precipitated solids and make the mixture homogeneous. A sample of 200 μL was taken, HNO3 70% (1.4 mL) added to dissolve the solids, then the sample was made up to 20 mL with ultrapure water and its metal and P content analysed using ICP-MS at Greenpeace Laboratories, University of Exeter. For all samples out of the calibration range of the ICP-MS, ICP-OES was used as given above (see ESI Table S1†). A 50 μL aliquot of the original sample was diluted in 0.45 mL of HCl 36% and 9.5 mL of water; the sample was then analysed with a Shimadzu Total Organic Carbon Analyser, equipped with a TNM-L total nitrogen analyser unit, to determine its total nitrogen content.
The solid phase yield was calculated gravimetrically. Elemental (CHN) composition analysis was carried out at London Metropolitan University. The metal and P content was determined via ICP-MS (Greenpeace Laboratories, University of Exeter). Prior to being analysed, the solid was digested: to 35 mg of solid in a PTFE vessel, 2 mL of HNO3 70% was added. After 5 min, 2 mL of ultrapure water and 1 mL of 35% H2O2 were added. The samples were then processed in a MARS5 Microwave Accelerated Reaction System at 480 W, heated to 150 °C in 5 min and kept at 150 °C for 10 min. After cooling, the samples were diluted with 5 mL of ultrapure water, filtered and then diluted 1:200 in HNO3 5% v/v for ICP-MS analysis.
In this study, two microalgal feedstocks, Chlorella vulgaris (Chlorella) and Arthrospira platensis (Spirulina), and two macroalgal species, Ulva lactuca (Ulva) and Sargassum muticum (Sargassum) were selected. All four species have been demonstrated to have an affinity for heavy metals, and display good removal efficiencies, as well as being established feedstocks for the HTL process.12,29,35
First, the impact of the target metals on the HTL conversion of the four feedstocks was assessed at 340 °C by directly combining biomass with varying concentrations of the four metals of interest (0, 10, 50, 150 mmol L−1).
Bio-crude yields and energy recovery for the four feedstocks, with no additional metals, were in line with previous reports, with the macroalgal species giving the expected lower crude yields than their microalgal counterparts (Fig. 1a).25,29 The direct addition of the metals to the biomass had little effect on the yield of bio-crude even at 150 mmol L−1, the upper range of what could effectively be bioadsorbed by the algae (Fig. 1a). Likewise, the elemental composition and higher heating values of the bio-crude did not change significantly on increasing the metal concentration (see ESI†). Previously, we demonstrated that, while high loadings of Mg and Fe increased the bio-crude production from Spirulina, Sn and Pb had little effect.25
Analysis of the aqueous phase demonstrated that the total nitrogen concentration was highly dependent on feedstock, with high levels of N depositing in this phase for both microalgal species, though increasing the metal concentration did not have a strong effect (Fig. 1b). The P concentration in the aqueous phase derived from the macroalgal biomass was very low and not unduly affected by heavy metals (Fig. 1c). However, for both Spirulina and Chlorella, P concentration was elevated at low metal loading (1000–1200 mg L−1); this then decreased on increasing metal loading. At 150 mmol L−1 of metals, P concentration was below 200 ppm for both microalgal species, equivalent with their macroalgal counterparts.
On increasing metal concentration, the solid residue yield was increased substantially for all feedstocks examined, with a linear increase with increasing metal concentration (Fig. 1d). The elemental analysis of the solid residue demonstrated that on increasing metal loading, an increasing level of the target metals were deposited (Fig. 2). For the microalgal species, the solid residue was mainly composed of inorganics, oxygen, phosphorus and carbon. As more target metals were added to the system, the target metals recovered in the solid residue increased accordingly. Crucially, at a 150 mmol L−1 metal loading, approximately 0.2 mmol L−1 of P is repartitioned from the aqueous phase, which is then accounted for in the solid phase. This suggests that the elevated phosphates, typical of the two microalgae species tested, in the system react with the metals forming insoluble phosphate compounds depositing into the solid residue; however, other mechanisms are also likely to be playing a role, and metals are also likely to be present in the form of oxides and hydroxides.
Fig. 2 Elemental composition of the solid residue (% w/w) for carbon, hydrogen, nitrogen, phosphorus and the target metals (Ni, Zn, Cu, Cd) and others. |
For the macroalgal species, the solid residue contains substantially higher levels of carbon and hydrogen. This is presumably due to large asphaltene-type compounds, which are known to be produced from high-carbohydrate feedstocks.36 A similar deposition was observed with increasing metal loading, though with lower phosphorus levels in the starting feedstock, lower solid phase P levels were observed overall.
The percentage distribution of the target metals between the bio-crude, the aqueous phase and the solid residue of the system was assessed (Fig. 3). For the microalgal species, between 86.2% and 99.9% of the target metals were deposited in the solid residue at 10 mM loadings, with the rest predominantly depositing in the bio-crude. This was reduced slightly at higher loadings, and whilst recovery was dependent on both the metal type and algal species, even at 150 mM loadings, 90% + metal recoveries were observed in many cases. Sargassum showed a similarly high metal recovery at low loadings, but at 150 mM Zn and Cd were not recovered easily, and rather deposited in the aqueous phase. Similarly, Ulva demonstrated very poor recoveries in the solid residue for Ni, Zn and Cd. These effects were highly dependent on the metal type, with excellent recoveries of Cu for all systems examined, possibly due to the preferential binding to phosphate within the system.
While the brown macroalgal species Sargassum works well in this system, retaining the predominant amount of metals in the solid phase, the green macroalgal species Ulva does not. Potentially this could be due to the mechanism of bioadsorption where the main metal binding is through functional groups on proteins.12 As proteins deposit mainly in the biocrude and aqueous phase this could aid the deposition of a proportion of these metals into these phases. Alternatively the main mechanism for brown alga tend to be through sulphated polysaccharides which would predominantly deposit in the solid.
The results clearly demonstrate that an algal-HTL system for remediation of heavy metals has promise, as even unrealistically high loadings of metals (0.15 M) are partitioned into the solid phase on conversion of the algal biomass, crucially, with no impact on bio-crude production. To further investigate the suitability of the system as a remediation process, the metal salts were then exposed to the four algal species first, under relevant conditions for bioremediation, both individually and as a mixture, prior to their conversion with HTL (Fig. 4).
Fig. 4 Passive bioabsorption efficiency of the algal biomass over 2 hours at room temperature with (a) 10 mM of each metal added singularly (b) 10 mM total of all four metals. |
The metal-containing aqueous solutions (10 mM) were stirred at room temperature with the dried algal biomass for 2 hours, in accordance with literature precedent.12,34 Metal uptake and bioadsorption efficiencies were determined via AAS (Fig. 4). For both microalgae, removal efficiency was very high for all metals (79–91%), except for nickel (42–49%), consistent with previous studies for these species.12 For the macroalgae, Sargassum was highly effective in all cases (73–89%), while Ulva demonstrated the lowest bioabsorption efficiencies (28–61%). Brown macroalgae contain large levels of alginates and sulphated polysaccharides (e.g. fucoidan) in the cell walls, which typically demonstrate higher metal uptake capacities.37 Contrastingly, the cell walls of green macroalgae are primarily composed of cellulose, with a minor protein fraction responsible for the metal bioabsorption. These results are consistent with previous findings demonstrating that green macroalgae show lower heavy metal uptake compared with brown macroalgae.34,37
The experiments were then repeated for each alga with a solution containing all four metals (2.5 mM each, 10 mM total). A similar trend in bioabsorption was observed. For both microalgae, the bioabsorption decreased significantly for zinc and slightly for cadmium. For macroalgae, while Sargassum did not show any change, for Ulva the bioabsorption increased for Ni and decreased for the other metals. Despite lower uptakes, algae were able to sequester a large fraction of the total metal content (69%, 61%, 81% and 45% for Spirulina, Chlorella, Sargassum and Ulva, respectively).
After the bioabsorption phase, metal-containing algae were processed via HTL. Similarly to when the metal sulfates were added to the process, the bio-crude yields were not affected by bioabsorbed metals (Fig. 5a). For both Chlorella and Spirulina, the elemental composition of bio-crudes (see ESI†) was similar to the control, though the elevated presence of zinc appeared to result in lower bio-crude oxygen, and subsequently higher HHV and energy recoveries than the control bio-crudes (Table 1). Microalgal feedstocks gave reasonably high energy recoveries in the bio-crude (42–50% and 49–57% for Spirulina and Chlorella, respectively). Less carbon deposited in the bio-crudes for the macroalgal species, resulting in lower energy recoveries (17–28% and 24–32% for Sargassum and Ulva, respectively). The effect of metals on the bio-crude was less pronounced for the macroalgae, with similar HHV, elemental composition and energy recoveries irrespective of the metal mixture used.
Algae | Metal type | HHV | Energy recovery |
---|---|---|---|
MJ kg−1 | % | ||
Chlorella | — | 33.5 | 56.7 |
Zn(II) | 34.5 | 57.4 | |
Cu(II) | 33.0 | 53.6 | |
Ni(II) | 32.8 | 54.0 | |
Cd(II) | 34.0 | 55.5 | |
4 Metals | 33.2 | 49.4 | |
Spirulina | — | 32.6 | 46.8 |
Zn(II) | 34.3 | 49.5 | |
Cu(II) | 31.2 | 41.9 | |
Ni(II) | 31.4 | 42.7 | |
Cd(II) | 33.2 | 43.2 | |
4 Metals | 33.5 | 42.3 | |
Sargassum | — | 33.4 | 18.7 |
Zn(II) | 32.6 | 21.7 | |
Cu(II) | 33.9 | 17.3 | |
Ni(II) | 31.2 | 28.9 | |
Cd(II) | 31.6 | 25.1 | |
4 Metals | 32.3 | 21.0 | |
Ulva | — | 31.9 | 31.9 |
Zn(II) | 33.1 | 23.6 | |
Cu(II) | 30.6 | 24.9 | |
Ni(II) | 29.7 | 23.5 | |
Cd(II) | 31.4 | 23.5 | |
4 Metals | 32.6 | 24.3 |
The aqueous phases obtained from the HTL process were analysed to assess the suitability for elemental recycle. To this end, total nitrogen, potassium and phosphorus concentration were analysed (Fig. 5b). On the conversion of the biomass used to remediate the metal mixture, elevated levels of N, P and K were recovered in the aqueous phase for both the Spirulina and Chlorella species. This demonstrated that the elevated metals under these conditions did not remove substantial amounts of phosphate from the aqueous phase, and that these three key elements could be recycled to supplement further microalgal growth. Presumably due to the lower starting amount of P in the macroalgal biomass, little phosphate was recovered from the macroalgal species. However, whilst our primary focus is on the bioenergetic products from HTL, the exploitation of the aqueous phase as a fertiliser product is not without merit. Indeed, the extensive potassium partitioning to the aqueous phase is noteworthy following conversion of macroalgal biomass, and suggests that, should the fertiliser product become more predominant as a market driver, a dual microalgae–macroalgae process may prove amenable for deriving bespoke NPK blends for the agricultural market.
The solid residue products were the most strongly affected by the addition of metals (Fig. 6). For Spirulina and Chlorella, the solid residue generally changed composition with increasing metal content. While the target metals were a large part of this, the overall elemental composition also changed depending on metal. For example, for Spirulina, the addition of zinc led to a 3-fold increase in carbon and nitrogen content and a 7-fold increase in hydrogen content. This suggests that the zinc is either catalysing or stabilising the formation of larger organic asphaltene-type molecules that are insoluble in the other phases. This effect is also observed with zinc and Chlorella, though it is less pronounced for the other metals. This corresponded with a slight decrease in the bio-crude yields. Phosphorus is also increased with the additional metal loadings across the samples.
Fig. 6 Yield and elemental composition of the solid residues obtained from the HTL (340 °C, 12 min) of the metal contaminated algal biomass. |
Carbon content of the solids derived from microalgae were relatively low (5–22 wt%), whereas macroalgae lead to a high solid phase C content (37–49 wt%), consistent with their higher carbohydrate content.38 The addition of metal seemed to reduce the carbon content in the solid residue for Ulva biomass in particular, potentially catalysing the decomposition of this phase into gas and soluble aqueous carbon species.
Both the Chlorella and Spirulina systems showed excellent target metal recovery, with over 95% recovery for all the target metals in the solid residue for Spirulina, and between 90–99% for Chlorella (Fig. 7a). This was improved on with the metal mixture. Similar to the model compounds, only trace amounts were deposited in the aqueous phase, ideal for using this for nutrient recycle. As with the model compounds, Cd(II) was deposited overwhelmingly in the solid phase, irrespective of the biomass or the loading of other metals involved. This suggests that it is not down to the relative stability of the sulfate over hydroxyl or phosphate species, but that the resulting cadmium species are extremely stable and insoluble in water. While Sargassum also demonstrated excellent recovery of the target metals to the solid phase, Ulva deposited a large proportion of the Ni, Zn and Cd in to the aqueous phase upon HTL conversion.
Footnote |
† Electronic supplementary information (ESI) available. See DOI: 10.1039/c8se00408k |
This journal is © The Royal Society of Chemistry 2019 |