Valorization of Biomass Residues by Biosorption of Microelements in a Closed-Loop Cycle

The concept of the research data presented assumes the valorization of goldenrod residues from supercritical CO2 extraction following the circular economy principles. The biomass was enriched with microelements (Cr, Zn, Cu) by biosorption from single and multielemental solutions in batch and packed bed reactors. Modeling of biosorption equilibrium supported by instrumental analysis (SEM and FTIR) of material properties was employed to explain the metal ions binding mechanism. The preferential biosorption of Cr(III) over the divalent ions, allows the possibility of valorization of goldenrod residue in a garden-scale biosorption tank acting as a fixed-bed reactor working in an open circulation run and fed with microelements diluted in rainwater. The use of fertigation solution in optimal doses of micronutrients did not show any phytotoxic effect. Using the post-sorptive solution as a source of micronutrients for plants showed significant effects on growth parameters (increased chlorophyll content by 54%) compared to groups fertilized with commercial formulation (13% higher sprout mass). Additionally, fertigation with the post-sorption solution leads to the biofortification of cucumber sprouts. The recycling process results in two products: enriched biomass as a potential feed additive (with Cr(III), Cu(II), and Zn(II)) and a post-sorption solution (with Zn(II) and Cu(II) only) used in the fertigation of plants.


Introduction
In recent years, the recovery of resources has become one of the main ideas of the sustainable development concept, circular economy, and zero-waste production approach. Major drivers for changing worldwide perception of this problem are projected scarcity of natural resources due to climate change processes, future depletion of non-renewable resources or limitations of their availability, and many socioeconomic factors [1].
The European Commission's goal is a reduction by 30% of non-renewable resources used in fertilizer production. This can only be accomplished by waste valorization and the circular economy (CE) approach. A circular economy is a system that is based on the recovery of materials. The European Commission introduced this concept as a response to environmental and social problems [1].
Valorization of plant residue of pharmaceutical, cosmetic, and food origin is a new opportunity for a circular economy enabling biomass used as a food supplement for livestock production [2,3]. A good example comes from a soybean meal commonly used in livestock farming as a source of assimilable protein. This biomass enriched with Cr, Zn, Fe and Cu ions, added to the laying hens feed, positively affected egg size and increased the transfer of microelements to the yolk fraction [3,4]. Another waste-turn-intofeed example is cultivated algae Enteromorpha prolifera and Cladophora sp., used as a hens microelement source. Its application enhanced the size and thickness of eggshells [5,6]. The biomass of algae enriched with Cu was used in swine breeding, its bioavailability [7]. Feed additives obtained through sorption of Cr, Zn, Cu and Mn ions on alfalfa biomass were used as potential ingredients in feed for hen husbandry [2].
To be used as a feed additive, biomass should meet the appropriate moisture and ash content (2.2%), contain no more than 100 times the standard content of a given substance in a complete meal and be free of faeces, urine, gut contents, treated leather, wood treated with preservatives, package or municipal solid waste and toxic elements [8]. All these requirements are met by plant residues from a supercritical fluid extraction (SFE) process. Thanks to the low process cost and the lack of necessity for solvents removal, SFE technique fits the trend of green chemistry and political directives limiting the negative impact of industry on the environment [9]. Re-use of the entire remaining post-extraction biomass is the last element required for a waste-free process status acquisition. In this context, valorization of the SFE residues and their usage as a feed additive is in line with the circular economy concept: the use of by-products from one production process as secondary raw material in another.
The by-products of SFE are low-density fibrous materials that are low in nitrogen, soluble carbohydrates, minerals and vitamins, and with varying amounts of lignin and cellulose. The three-dimensional polymer structure of lignocellulose creates the surface area where functional groups suitable for metal binding are localized [10][11][12] (Volesky and Holan, 1995). For example, methoxyl, hydroxylaliphatic, phenolic, hydroxyl, and carboxyl groups were identified in the polysaccharide cell wall of aster group plants. Phenolic groups are present on the lignocellulose matrix of black locust, while amide and amine groups in the case of ginger [13]. Thus, the presence of lignin and cellulose and types and amounts of functional groups involved are factors enabling biomass enrichment with microelements [14]. Moreover, organoleptic properties of biomass such as taste and smell or the content of medical substances (e.g., flavonoids, saponins) are also under great importance for livestock farming.
European goldenrod (Solidago virgaurea) is a perennial flower from the aster family, occurring originally in Europe, central Asia and North America. Beekeepers mainly cultivate this plant because of the positive effect on the taste, colour and health properties of honey [15]. Also, the pharmaceutical industry takes advantage of Solidago virgaurea extracts, which contain from 0.5 to 1.5% of flavonoids and other compounds from anthocyanin groups such as saponins and caffeic acid esters. The inclusion of 7.85% hemicellulose, 52.78% lignin and cellulose (with at least 28% of lignin content) [16], acts as a physical barrier impeding the microbial breakdown of goldenrod residue. Such composition extends its fermentation and creates a problem with its storage. So far, the SFE residue of goldenrod is not recycled or used in an alternative way.
This work aims to valorize locally available large quantities of the European goldenrod residues from SFE process and their valorization as a feed supplement enriched with microelements. Chromium (Cr), zinc (Zn) and copper (Cu) were selected as model trace elements in this study due to their dual function in maintaining proper body function of animals and in reducing the negative effect on the heat stress [17,18]. For example, in the case of laying hens, supplementation with chromium and zinc has been shown to increase the digestibility of nutrients, alleviate effects caused by low ambient temperature [19], and decrease eggshell cracking [20]. Subject to the above, the biosorption of chromium (Cr), zinc (Zn) and copper (Cu) ions was performed in batch mode for one-and two-component solutions to determine the sorption capacity and goldenrod residues affinity for the tested microelements. The instrumental analysis of biomass before and after metal ions uptake was used for sorbent characterization and the identification of functional groups participating in metal ions binding. Analytical methods were used for quantitative analysis of the carboxyl and hydroxyl groups in the lignocellulose matrix. The mechanism of the metal ions uptake was further supported by modeling of sorption equilibrium.
Moreover, to enrich biomass in a waste-free process, postbiosorption metal solutions were used for the biofortification of cucumber sprouts. It is worth mentioning that both copper and zinc are crucial micronutrients of plant enzymatic, metabolic, and photosynthesis reactions [21,22]. In opposite, chromium has a well-known phytotoxicity effect for plants, disordering plant germination, root and stem growth, and leaf development [23]. Thus, because of the possible usage of outlet liquid for plant fertigation, an enrichment of biomass with microelements was carried out in a fixed-bed column with identification of the breakthrough time of Cr(III).

Materials
The biomass of plant residues was obtained as a by-product of the supercritical CO 2 extraction process conducted in the New Chemical Synthesise Institute (Puławy, Poland). As received, post-extraction residues were milled by knife mill (Retsch; grindomix gm300) and sieved to obtain fractions in the range from 0.42 to 0.62 mm.

Characterization of Goldenrod Mass
FT-IR spectroscopy was used to identify the chemical groups present on the biosorbent surface. The infrared spectra of the biosorbent were recorded in the region of 4000-500 cm −1 using a Vertex 70v spectrometer (Bruker). The scanning electron microscope (SEM) images were recorded for surface morphology of both "as received" and metal-enriched biomasses at an acceleration voltage of 10 kV (Microscope SEM/Ga-FIB FEI Helios NanoLab™ 600i). The microscope equipped with X-ray spectrometer (EDX) with Silicon Drift Detector was used to confirm the adsorption of metal ions by sorbent. To identify the electrical charge density (pH pzc ), first, the buffer solution of 0.1 mol/L NaNO 3 was used to adjust pH to a given value by the addition of HNO 3 or NaOH. Then each solution was gently stirred for 30 min with 0.2 g of biomass. The pH pzc was determined by Elemetron PCP-401 pH-meter. The content of carboxylic groups in the biomass was identified following [24]. Weighted mass (0.2 g) of biomass was shaken with 10 mL of 0.1 N NaOH and 10 mL of acetone for 2 h. After that, the solution was titrated with 0.1 N with a standard solution of HCl against phenolphthalein. A blank test was performed simultaneously. The number of carboxylic groups in the sample was calculated from the difference in HCl volumes used for the analyzed sample and the blank test. The content of carboxylic groups was calculated from the formula: where V (mL) is the volume of solution, and m (g) is the dry mass of biomass. The content of hydroxyl groups in the biomass was identified in accordance with the EU quality standard (PN-EN ISO 2554:2001).

Sorption Experiments
Adsorption isotherms were obtained by batch sorption experiments. The samples of goldenrod biomass (0.2 g) were gently mixed with 40 mL solution of single or binary component metal salts in a thermostatic shaker (3033, GFL) at 22 °C with 30 rpm. After stirring for 8 h, the suspension was separated from biomass by syringe filters (45 µm cellulose acetate membrane, Millipore), acidified by the addition of conc. HNO 3 (1.0 mL/L), and analyses for their metal content by the inductively coupled plasma optical atomic emission spectrometer (ICP-OES, Varian Vista MPX). Cr was analyzed at a wavelength of 267,716 nm, Cu of 327,395 nm, and Zn of 206,2 nm. The amount of metal adsorbed per unit mass of adsorbent q e (mmol/g) was calculated from the equation: where C 0 (mmol/L) and C e (mmol/L) are the initial and the equilibrium ion concentrations, respectively.

Modelling of Biosorption Equilibrium
The following empirical models (Eqs. 3, 4, 5) were used to evaluate the metal sorption mechanism in a single-component system: The Langmuir model (L), which assumes homogenous sorption on the finite number of active sites with equal adsorption energy [25]: where K L (L/mmol) is the Langmuir constant associated with sorption free energy and sorbent-metal ion affinity, q m (mmol/g) is the maximum sorption uptake.
The Freundlich (F) model deals with the heterogeneity of the surface of sorbent towards sorbed molecule [26]: where K F signifies sorption capacity per unit concentration (mg/g)/(mg/L), 1/n F provides information of active sites; the lesser value of 1/n F indicates the occurrence of heterogeneous sites and the physical sorption mechanism [27].
The Langmuir-Freundlich (L-F) model is a hybrid model that results from the combination of the previous models to circumvent the limitations of both [28]: where K L-F (L/mmol) is the Langmuir-Freundlich constant, n L-F represents the energetic surface heterogeneity. The model's parameters were estimated with the aid of the non-linear regression using Maple software by minimizing the Sum of the Squares of the Errors (ERRSQ): where p is the number of experimental points, q e,exp and q e,mod are experimental and the modeling equilibrium concentrations in solid phase, respectively. The fit between experimental and calculated data for all models was evaluated using Fisher's Test (FT), standard deviation (σ), and mean error (ME) [29].

Fixed Bed Column Study
The fixed bed experiment was conducted in an open unit run that the main element was a 16 mm (I.D.) glass column of 20 cm height (GE XK 16). The column was packed with a bed (the equivalent of 3 g dry material; 10 cm height). The trinary metal solutions of Cr:Cu:Zn, with an equal (q e,exp − q e,mod ) 2 i concentration of each metal ion (C in = 0.1 mmol/L of each), were fed to the column by a peristaltic pump (Peristaltic pump Lab 2015; Gkisker) at the gravitational with flow rate 9.0 mL/min. Specimens of eluate were captured from the bottom of the column at specific time intervals and analyzed for metal content by the ICP-OES. The feeding of the column was continued up to 5 h. The experiment was repeated three times.

Germination Test
Preliminary functional properties of the fertigation solution were performed in germination tests. where TF is considered as transfer factor (%); C plant represents the content of the component in the dry weight of the sprout (mg/kg) and C substrate provides information about the content of the component in the substrate (mg/kg);

Biomass Analysis
The scanning electron micrograph revealed the surface texture and morphology of biosorbent (Fig. 1). Sieve tubes of stalk fragments (Fig. 1A, top right corner), leaf structures (left part of the center) and fragments of ligneous plants (right bottom) confirm plant origin and the heterogeneity of the tested sample. The measured diameter of perforations (Fig. 1B) found on the biomass surface (5.05-16.5 µm) is, on average, ten times larger than the estimated dimensions of xylem and phloem tissue structures [31]. This phenomenon results from the SFE processing of the biomass when micro-tissue damage occurs [32]. The high diameter of the biomass' perforations, in comparison to the hydrated ionic radius (Cu 4,19 Å < Zn 4,30 Å < Cr 4,61 Å), excludes inner diffusion resistances during ions biosorption [33]. The energy dispersive (EDS) spectra of the goldenrod residue before and after the adsorption of Zn (II), Cu(II), and Cr(III) are shown in Fig. 2. The biomass consisted mainly of C and O. The C:O ratio 1.8:1 is lower than in pure lignin structure (2.16:1) [34]. High surface's C and O content may correlate with the C-C, C-OH, O=C-O, HO-C, O=C, and -OOC-, groups. After metal loading, the EDS analysis of biosorbent identifies the clear peaks of Cr(III), Cu(II), and Zn(II) at 5.6, 8.0, and 8.6 keV, respectively. The obtained percentage by weight of the metals follows the order: Cr > Cu > Zn. The surface mapping of the received biosorbet in Fig. 3 reveals the presence of Zn and Cu and the lack of Cr on the surface, which is in line with the elemental composition determined by . In opposite to Cr(III), both Cu(II) and Zn(II) are essential redox-active metals that participate in many physiological processes in plant materials [35].
The FTIR spectra of goldenrod biomass before and after metal ions sorption are shown in Fig. 4. The presence of broad absorbance in the range of 3500 to 3300 cm −1 represents carbohydrates [36]. The identified peak at 3435 cm −1 is assigned to the carboxylic stretching band or alcohol groups [37]. The peak at 2926 cm −1 may be associated with O-H stretching of the carboxylic acid in the cell wall of the biomass. This peak is followed by the stretching at 2852 visible after metal sorption, corresponding to the aliphatic C-H group of organic chains of the cellulose [38]. The band between 1700 and 1750 cm −1 attributes to C=O stretching vibration indicates the presence of a variety of functional groups: carboxylic, ester, quinone, conjugated aldehyde, conjugated ketone, αβ unsaturated ester and aliphatic ketone [39]. The pick at 1734 cm −1 corresponds to the content of sesquiterpene lactones remaining in plant tissue after extraction [40]. The bands that appeared in the range of 1740-1050 cm −1 are related to polysaccharides with different structures and configurations. The registered band about of 1638 cm −1 , relates to asymmetric and symmetric C=O bands of carboxylic, ester or aldehyde vibrations [41,42]. Their shift after metal ion sorption indicates a degree of carboxyl bonding. The pattern of aromatic vibration near 1600 cm −1 and 1500 cm −1 , along with the peaks near 1200 cm −1 is attributed to aryl-O stretching vibration and confirms the presence of lignin. The visible and narrow peak at 1384 cm −1 appeared only after metal ions sorption and may be attributed to symmetric stretching of -COO- [43]. Two flattened peaks at 1320 and 1254 cm −1 are assigned to CH 2 symmetric and C-H bending caused by the stretching of syringyl and guaiacyl rings of lignin and lignocellulose [44]. These bands can also correspond to the C=O stretching of ester and carboxylate groups [45]. After metal ions sorption, their position and intensity do not remain the same, further confirming the interaction of metal ions with carboxylic groups. The peak at 1052 cm −1 may indicate by the presence of C-O vibrations caused by a large amount of polysaccharides or polysaccharide-like substances [46]. The observed vibrations in the 800-600 range relate to the presence of C-C bonds being the core of the biomass.
The presence of carboxyl and hydroxyl groups was further confirmed by chemical analysis. The total number of identified carboxylic groups was 1.33 mmol/g, while  where M n+ = Zn 2+ , Cu 2+ , and Cr 3+ ions. The formation of M-O bonds between metal ions and the acid functional groups of lignocellulosic sorbents was confirmed by other authors with XPS analysis [47].

Biosorption Isotherms
The experimental data depicted in Fig. 5 represent the equilibrium distribution of the metal ions between the goldenrod biomass and the residual metal concentration in the liquid phase. The data exhibit nonlinearity in the uptake of every metal. As can be seen, the experimental isotherms for all  the obtained pH eq ranges, most of the carboxylic acid groups were ionized (pH eq > pH pzc ), causing a strong electrostatic attraction between the sorbent surface (negatively charged) and the heavy metal ions [48].
The modeling of biosorption equilibrium was done by using three empirical equations. The values of fitting parameters are depicted in Table 1. Among the applied models, the three-parameter Langmuir-Freundlich model best fit the experimental data, as can be seen from the value of statistical tests. This model closely overlapped the Langmuir one. The maximum sorption capacities estimated from both models were higher than the obtained experimentally (q m,exp ). The values of parameter n L-F ≠ 1 provide the multiple and energetically heterogeneous biosorption.
The comparison of q m obtained for single and binary solutions (Fig. 6A) identifies that the efficiency of metal ions biosorption from binary solutions is lower than from a single one. This is the case when metal ions compete for the same active sites and share them [47]. The most remarkable is the magnitude of this effect which differs for a given ionic par. The observed reduction of Cr(III) biosorption in the presence of Zn(II) and Cu(II) is lowered by about 20% and 40%, respectively, in comparison to the single Cr(III) solution. In comparison, the reduction of Zn(II) and Cu(II) biosorption in the presence of Cr(III) is lowered by about 10 times for single solutions. Furthermore, the shape of the binary Cr-Cu and Zn-Cr isotherms (Fig. 6C, D) reveals that the equilibrium concentration of Cr(III) constantly increases in the whole equilibrium range. In turn, the equilibrium concentration of Zn(II) and Cu(II) increases only at low concentrations values, decreasing then sharply. In the case of the Cu-Zn system, a clear co-sorption is seen from overlapping both isotherms at a lower concentration range. Then, the antagonistic effects of Cu(II) over Zn(II) are observed. Cu(II), as a more favorable ion, exchanged Zn(II) in active sites, decreasing its sorption. As stems from the binary isotherms, the affinity of the goldenrod residues for tested metal ions follows the order: Cr(III) > Cu(II) > Zn(II). The linear extensions of the L-F model derived by adding one more concentration term were used for modeling of antagonistic sorption of heavy metal ions [47]: where subscripts 1 and 2 relate to the given pair of metal ions in a binary system (Cr-Cu, Zn-Cr, Cu-Zn). In the binary equilibrium calculation procedure, the parameter sets obtained for single systems were used as an initial guess to (8) minimize the ERRSQ objective function across the concentration range studied [49]. The comparison of the experimental and modeling data in Fig. 6B-D demonstrates that the extended Langmuir-Freundlich model fits the binary equilibrium points reasonably well. The model's parameter values, together with statistical test results, are depicted in Table 2. Apparently, the biosorption capacity of Cr(III) is higher than that of Cu(II) and Zn(II), showing the higher affinity of goldenrod residue for Cr(III). As it steams from Table 2, Cr(III) follows homogenous sorption since n L-F ≈ 1. Nevertheless, the estimated  Tables 2, 3). This results from the fact that modeling calculations were performed only for one molar ratio experimental set (1:1:1) and the obtained isotherms' curves had a grove up tendency.

Triplee-Biosorption Breakthrough Curves
The envisaged higher affinity of the biomass for Cr(III) than Cu(II) and Zn(II) creates an opportunity to the enrichment of the SFE residue in a close free-waste processing cycle. Thus, the competitive biosorption of Cr(III), Cu(II) and Zn(II) ionic mixture under continuous conditions was evaluated on a laboratory scale. The breakthrough curves depicted in Fig. 7 are expressed in terms of normalized concentration, defined as the ratio of effluent metal concentration to influent metal concentration (C/C in ), as a time (t) function. As can be observed from the plots grow up, all breakthroughs obtained have a flatter concave shape. The fastest bed saturation was achieved for Zn(II). In the case of this ion, C/C in > 1, which identified its replacement by competitive ions. The metal ions breakthrough points follow the order: Zn (5 min) > Cu (9 min) > Cr (25 min). The Cr(III) breakthrough point is when the biomass enrichment process should be stopped to prohibit Cr(III) appearance in the liquid outlet. As can be seen from the picture magnification, up to 25 min of liquid flow Cr(III) is sorbed on biomass, while the content of Cu(II) and Zn(II) in the liquid outlet tends to increase. The adsorption loading of metal ions up to 25 min of filtration (magnification on Fig. 7) was obtained by integration of the area under the breakthrough curve, at C in feeding concentration and V flow rate, by using the following equations: where t (min) is time, m b (g) is mass of bed, V is volumetric flow rate (mL/min), C i is an effluent concentration (mmol/L) at given i. The calculated amount of metal ions sorbed by the biomass in the first 25 min of the process, equals 0.39 mgCr/g  . 7 Breakthrough curves for triple metal ions biosorption (0.0075 mmol/g), 0.43 mgCu/g (0.0067 mmol/g) and 0.41 mgZn/g (0.0063 mmol). The obtained biomass enriched with microelements can be used as a feed additive, for e.g., chickens. As demonstrated by scientific studies, the chromium content in a food additive positively affected laying eggs efficiency [50] and on chicken growth [51].
Considering the obtained values of q t for Cu and Zn, their content did not exceed the UE regulation levels allowed in poultry feed (35 and 250 mg/kg, respectively) [52]. Furthermore, the usage of enriched goldenrod residue as a food additive can enrich poultry feed with cellulose, the main fiber component. The concentration of Cr, Cu, and Zn in the outlet solution, which was collected over 25 min of filtration, was calculated from the equation: where V t (mL) is the volume of effluent collected during 25 min of filtration.
The values obtained were as follows: 0 mgCr/L, 0.68 mgCu/L, and 0.80 mgZn/L. The latter two amounts are higher than recommended in commercially available liquid fertilizers for fertigation (0.12 mgCu/L and 0.35 mgZn/L) but lower than recommended for foliar fertilizers (Mikroplus; Intermag). Obviously, for lower concentrations of all metals in column inlet, the binding sides would be occupied slower and more time would be needed to saturate the column bed. However, to delay the breakthrough time of Cr(III) in relation to the divalent ions, it would be more appropriate to reduce its initial concentration in the inlet solution.
The research indicates the potential for biomass enrichment with metal ions in a closed-loop cycle in the fertigation and feed additives industry. For example (Fig. 8), a garden-scale biosorption tank can consist of two intermediate bulk containers, placed one on top of the other.
The top container would act as a rainwater collector with dissolved salt of microelements. It should have a valve to gravitationally feed the bottom container. The latter would act as a fixed bed reactor filled with any lignocellulose residues. The bottom container should be equipped with two punctured shelfs allowing bed packing and preventing biomass floating and with an outlet valve. After filtration, biomass ought to be sun-dried to prevent rotting, while the collected outlet solution, after dilutions, is used for the plants fertigation.
To potentially reduce the construction costs, the selection of the plant components was made based on commercially available components. The model consists of two 1000L Mauzer tanks (1a and 1b) with support system (2), two polypropylene tanks (3a and 3b), a frame supporting  (4), a centrifugal pump (5) and a set of valves and pipes transporting the fluids (6,7,8).
The proposed residue valorization is an energy-free process, using rainwater as a renewable liquid, which would allow achieving circular economy status for the SFE technique (Fig. 9).

Seeds Germination and Plant Growth
Germination tests were conducted at a laboratory scale to evaluate crop promotion products for phytotoxicity and bioavailability of elements [53]. Germination is a crucial stage of plant growth that is influenced by both internal and external factors. The most important factors of the process include moisture, temperature and light, providing these conditions allows for objective assessment of the effectiveness of formulations [54]. This process causes a number of biochemical changes inside the seed and the accumulation of health-promoting components. Extremely high contributions in the initial stages of growth are micronutrients from the group of Cu, Mn, and Zn, which affect the plant's sustainable development [55].
Analyzed parameters of cucumber sprout growth (stem length, fresh sprout weight, chlorophyll content) are presented in Table 4 and Fig. 10. The highest fresh sprout mass (12.0 g) was achieved in the group fertilized with a dose of 100% of micronutrient demand. The obtained sprout mass was about 13% higher compared to the group fertilized with a commercial product. Groups fertigated with doses above the optimum showed a phytotoxic effect. A similar effect can be observed in the case of stem length, where maximum length was found in a group with an applied dose of 100%. For mass and stem length, statistically significant differences were found between almost all groups. A different effect was observed for chlorophyll content, where statistically significant differences occurred only between the zero and control groups and the groups fertigated with the solution after the biosorption process. This effect can be correlated with the high zinc content of fertigated sprouts (Table 5). This element plays a significant role in the structure of chloroplasts [56].
The crucial parameter in assessing the bioavailability of nutrient formulations is TF, which describes the content of micronutrients in the plant relative to the amount applied to the substrate [57]. The coefficient decreases with increasing micronutrient dose, which is closely related to the plant's limited demand for selected micronutrients (Table 4) [58]. At the optimum dose, the TF was twice as high as the group fertilized with commercial fertilizer. After biosorption, the components present in the solution are in ionic form, which is the most bioavailable form, significantly affecting their transfer and accumulation in the plant [59]. Statistically significant differences occurred between almost all groups, excluding the control group and selected fertigated groups.
Preliminary evaluation of solution utilization efficiency after the biosorption process confirmed the possibility of waste management for agricultural purposes. It can be concluded that the high bioavailability of components in the ionic form leads to biofortification of cucumber sprouts, which furtherly can result in the cultivation of highly nutritious functional foods [60].

Summary
The SFE goldenrod residues are lignocellulose materials with a high content of carboxyl and hydroxyl functional groups suitable for metal ions binding. Equilibrium studies for single metal solutions did not identify any preferred sorption of tri or divalent ions. The higher affinity of biomass for Cr(III) has been proved only after the binary equilibrium tests. The obtained sequence of affinity: Cr(III) > > Cu(II) > Zn(II) was furtherly confirmed in the fix-bed study. The breakthrough time for Cr(III) was the longest compared to other ions, and the process termination ensured the absence of Cr(III) in the outlet solution. The metal ions content in enriched biomass for Cr, Cu, and Zn was equal: 0.0075, 0.0067 and 0.0063 mmol/g. Due to the presence of microelements and cellulose, the enriched biomass can be applied as a feed additive. The collected filtration solution contained 0.011 mmol Cu/L and 0.012 mmol Zn/L can be used for the plants fertigation. Using the post-sorptive solution as a source of micronutrients for plants showed significant effects on growth parameters compared to groups fertilized with commercial formulation (13% higher sprout mass).

Conclusions
The enrichment of the SFE residue with microelements with a view of its use as a food additive closes the loop of the goldenrode plant processing cycle. Furthermore, the utilization of post-biosorption metal solutions for fortification of plants makes the enrichment process waste-free. Due to the toxic effect of chromium on plant, the enrichment of biomass with Cr, Cu, and Zn ions should be performed in a fixedbed column, which enables biosorption termination when Cr appears in column outlet. Due to this, it is possible to obtain two products: enriched in Cr, Cu, and Zn food additive, and fertigation liquid containing Cu and Zn. The closed circuit of microelements classifies the presented technique as environmentally friendly according to European Union standards.
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