Facile synthesis of mesoporous nano Ni/NiO and its synergistic role as super adsorbent and photocatalyst under sunlight irradiation

Tailoring a material that has a synergistic role as an adsorbent and a photocatalyst for environmental application is an attractive field for research. This article presents a study of facile synthesis of NiO and Ni/NiO with a synergistic role as super adsorbents in the lake of light and photocatalysts under light irradiation. Nano flower-like mesoporous NiO and Ni/NiO were synthesized by the co-precipitation method. XRD, SEM, EDAX, XPS, BET, and DR/UV–Vis spectroscopy techniques were employed for samples’ analysis. The point of zero surface charge of prepared samples was detected by the batch equilibrium method. The adsorption efficiency was investigated in the absence of light using aniline blue as a pollutant model dye. The synergistic effect as an adsorbent and a photocatalyst was investigated under UV and sunlight irradiation. Different parameters affecting the adsorption in the dark have been optimized. The results showed that in the absence of light, the prepared samples are super adsorbents with a maximum adsorption capacity ranging from 210 to 230 mg g−1 and a removal % ranging from 95 to 100% within 2 h. Under UV or sunlight irradiation, the adsorbent/photocatalyst attained a dye removal % of 99.8% within 30 min. The adsorption data matched the pseudo-second-order model, and the equilibrium adsorption data showed compatibility with Langmuir model. The findings of experiments revealed that the adsorption is spontaneous, exothermic, and results in less entropy. Under sunlight irradiation, the dye removal efficiency increased by 19% in the case of Ni/NiO hybrid; it showed a removal efficiency of 99.5% within 30 min under sunlight irradiation versus 80% after 120 min in the dark.


Introduction
Transition metal oxides are interesting materials with unique optical, magnetic, and electrical properties that make them a promising candidate for unlimited applications. One of these oxides is NiO, which was applied to many applications such as memory devices, gas sensors (Tong et al. 2021), batteries (Jia et al. 2021), light-emitting diodes and lighting devices (Taeño et al. 2021b;Zhang et al. 2021), waveguides, and optical resonators (Taeño et al. 2021a). Due to its facile synthesis and stability, NiO was also examined as an adsorbent for a number of organic and inorganic pollutants such as dyes (Al-aoh 2018;Ramesh 2018), phenol (Dehmani and Abouarnadasse 2020), and heavy metals (Ziaeifar et al. 2015;Rajabi Kuyakhi and Tahmasebi Boldaji 2021). NiO is a p-type semiconductor whose band gap ranges from 3.6 to 4.3 eV and is characterized by chemical stability, low toxicity, and high ionization energy (Bonomo 2018;Taeño et al. 2021b). In the last decade, few researchers have utilized NiO as a photocatalyst for some environmental contaminants such as dyes (Jayakumar et al. 2017;Sabouri et al. 2018;Khairnar and Shrivastava 2019), antibiotics (Torki and Faghihian 2017), and free cyanide (Bashir et al. 2019).
In general, photocatalytic efficiency is enhanced by decreasing the rate of recombination of the generated electron-hole. Doping the metal oxides with elements is one of the strategies to enhance their structural and optical properties (Al Boukhari et al. 2020;Bhatt et al. 2020;Ahmed et al. 2021). The partial reduction of NiO into metallic Ni in the NiO matrix leads to the improvement of the electron-hole generation, and hence achieves a better photocatalytic  (Paliwal and Meher 2020;Srinivasa et al. 2021). Ni/NiO hybrid was also studied as an adsorbent for Pb and Cd ions (Shivangi et al. 2020), Congo red and Cr(VI) , catalytic decomposition of ozone (Gong et al. 2020), and also applied for water splitting ). Synthesis' conditions affect the morphology, particle size, and band gap of Ni/NiO particles (Mammadyarova et al. 2021). Ni/NiO has been fabricated by various routes, such as solution combustion using different fuels Srinivasa et al. 2021), thermal annealing of Ni(CH 3 CO 2 ) 2 ·4H 2 O and graphene mixture , precipitation using NaBH 4 and ethylene glycol as a basic precipitant , and precipitation of nickel oxalate in the presence of polyethylene glycol followed by calcination (Shivangi et al. 2020). Tailoring a material that can act as an adsorbent in the lake of light and photocatalyst under light irradiation is a promising field for research Ramesh 2018). Metal oxides that act as semiconductors could be engineered for synergistic functions as adsorbent and photocatalyst. Photocatalysis requires irradiation with light of a definite wavelength, while adsorption occurs even in the absence of light. For photocatalysis applications, different sources of light irradiation were applied as Xe lamp (Zhao et al. 2017, black light UV lamp (Abd-Rabboh et al. 2019), UV lamp (360 nm) , and direct sunlight irradiation Wang et al. 2018).
In this research, a promising approach of using the same material as an adsorbent in the absence of light and a photocatalyst under UV or sunlight irradiation was investigated. To the best of our knowledge, no previous work focused on comparing the adsorption efficiency in the dark with the photocatalytic efficiency under sunlight irradiation for NiO or Ni/NiO hybrid nanoparticles. In this article, a flower-shaped NiO was synthesized by the co-precipitation method. Ni/NiO hybrid samples were prepared via reduction reaction by glucose or urea within the calcination process. Different techniques as XRD, SEM, EDAX, XPS, DR/ UV-Vis, and BET were used for samples' characterization. Various parameters affecting the adsorption of aniline blue as a model dye were optimized. The adsorption efficiency in the absence of light irradiation was compared with the synergistic adsorption-photocatalytic efficiency under UV and direct sunlight irradiation.

Synthesis of NiO nanoparticles
Co-precipitation method was utilized to prepare NiO. Briefly, NH 4 OH was added dropwise to NiCl 2 .6H 2 O solution (10%) under constant stirring till the solution pH reached 11. The resulted mixture was aged for 24 h, then the produced light green precipitate of Ni(OH) 2 was filtered and washed using distilled water. The resultant was dried at 70 °C then calcined at 400 °C for 4 h to get NiO nanoparticles.

Synthesis of Ni/NiO hybrid nanoparticles
One gram of the dried precipitate of Ni(OH) 2 was ground in an agate mortar with either 2 g glucose or 20 g urea as reducing agents then the mixture was calcined in covered crucibles at 400 °C for 4 h. The produced fine powders were labeled as Ni/NiO (g) and Ni/NiO (u), respectively.

Characterization
The structural characteristics of the samples under investigation were examined using X-ray diffractometer (X'Pert Pro, PAN analytical, NL). The X-ray source was Cu Kα radiation (λ = 1.5406 Å) in the 2θ range of (5° to 60°). Samples surface was explored by X-ray photoelectron spectroscopy (XPS) K-ALPHA (Themo Fisher Scientific, USA) with monochromatic X-ray Al K-alpha radiation (− 10 to 1350 eV). The samples' morphology was explored with the field Scheme 1 Chemical structure of aniline blue emission scanning electron microscope (FESEM) (Quanta FEG 250, the Netherlands) after coating the samples with gold. Nitrogen adsorption-desorption isotherm, pore size distribution, and surface area were explored using Quantachrome TouchWin v.1.2. The band gap values of samples were determined using UV-Vis spectrophotometer at ambient temperature (DR/UV-Vis) (Jasco-V570) in the λ range of 200 to 800 nm.

Point of zero charge detection
The isoelectric point or pH pzc (point of zero charge) plays a vital role in the behavior of adsorbents and photocatalysts. pH pzc is the pH value at which the net charge on the dispersed phase's surface is zero. The batch equilibrium method was employed to determine pH pzc . In this experiment, a definite mass of each composition (0.05 g) was dispersed in NaNO 3 solution (50 ml, 0.1 mol L −1 ) of definite initial pH (pH i ) in the range of 1-10. HCl and NaOH solutions (0.1 mol L −1 ) were used to control pH i . After 24 h of shaking at room temperature, the final pH (pH f ) was measured. pH pzc = pH when (pH i − pH f ) equals zero.

Adsorption studies in the lake of light (dark)
In a typical adsorption experiment, a definite mass of each sample (0.05) g was dispersed in dye solution (50 ml) of definite (C o ), and pH was controlled by buffer solutions. The mixtures were kept under continuous stirring till equilibrium. The initial dye concentration (C o ) and equilibrium concentration (C e ) were measured in mg L −1 on a UV-Vis spectrophotometer (Jasco 730) at a wavelength (λ max ) of 607 nm. The removal percentage (%E) and the adsorption capacity, q e (mg g −1 ) were determined according to the following equations.
where m is the mass of dispersed sample (g) and V is the volume of AB solution (L). The effect of different parameters as pH (4-10), adsorption period (0-2 h), initial AB concentration (30-500 mg L −1 ), and temperature (30-60 °C) on the adsorption process was investigated.
For adsorption kinetics studies, each sample was dispersed in AB solution (C o = 50 mg L −1 , pH 6, 20 °C). The mixture was kept under continuous stirring in the dark, and AB concentration was measured at definite time intervals till equilibrium. The experimental data were examined by pseudo-first-order, pseudo-second-order, and intra-particle models.
For detection of maximum adsorption capacity and adsorption isotherms studies, the equilibrium concentration was measured for dye solutions of various C o (30, 50, 130, 200, 300, or 500 mg L −1 ). The obtained data were examined using the well-known isotherms (Freundlich, Langmuir, and Dubinin-Radushkevich).

Synergistic adsorption-photocatalytic effect under UV or sunlight irradiation
The synergistic action of the prepared samples as adsorbent and photocatalyst was examined under UV irradiation or sunlight irradiation. UV irradiation was carried out inside a homemade wooden box irradiator provided with three black light UV lamps (18 W) and a multipoint stirrer. The same experiments were conducted under direct natural sunlight irradiation during May 2020 in Cairo, Egypt where the temperature range was (35 to 40 °C). In these experiments, the sample was dispersed in AB solution (C o = 30 mg. L −1 ) and this dispersion was irradiated for 2 h under constant stirring. Solution temperature was observed during the experiments, and the concentration of AB was measured at definite time intervals. The rate constant values of the photocatalytic degradation ( k pc ) were detected from the slope of ln

XRD
The crystalline structure of the samples was examined by XRD, and the results are shown in Fig. 1. The XRD pattern of NiO showed sharp peaks at 2ϴ of 37.2° (111) and 43.4° (200), which indicate a face-centered cubic crystalline structure that is consistent with JCPDS card no. 47-1049 (Adhikari and Madras 2017). The samples Ni/NiO (g) and Ni/NiO (u) showed extra diffraction peaks at 44.5 (111) and 51.9 (200) that are characteristic of the cubic structure of crystalline Ni (JCPDS card no. 04-0850). Ni/NiO (u) showed a slightly higher intensity for these peaks indicating a higher content of crystalline Ni than Ni/NiO (g) . The used muffle has no air input; therefore, during the calcination process, organic urea or glucose consume the available oxygen during their thermal decomposition, which leads to an oxygen deficiency in the calcination chamber. As a result, some of Ni(OH) 2 is reduced into Ni. Utilization of 20 g of urea versus 2 g of glucose leads to a higher content of Ni in the case of Ni/NiO (u) sample. Assuming a complete combustion, each 20 g of urea requires 16 g oxygen while each 2 g of glucose requires 2.1 g oxygen. These results indicate that using organic hydrocarbons during the calcination process of metal oxides or hydroxides results in the reduction of the metal to some extent.

SEM-EDAX analysis
Figure 2(a−f) represents the SEM images of the samples' surface. As shown in Fig. 2(a, b), neat NiO showed nanosheets, of a thickness ~ 29-50 nm, arranged to form a flower-shaped structure. Similar morphology was obtained for NiO prepared by hydrothermal method (Ding et al. 2016). Ni/NiO (g) showed spherical shapes of polydisperse diameter forming cauliflower-like surface as displayed in Fig. 2(c, d). It seems that the released gases from the thermal decomposition of glucose suppressed the growth of the NiO nanosheets. Similar morphology was shown by Shivangi et al. when Ni/NiO was prepared by calcination of nickel oxalate in the presence of polyethylene glycol (Shivangi et al. 2020). Figure 2(e, f) exhibits agglomerates of irregular shapes with random spherical aggregates in some areas of Ni/NiO (u) surface. This sample showed larger gaps appeared as channels between the agglomerates. This morphology was revealed to the generated gases from the thermal decomposition of urea that raptured the bulk during the calcination. Generally, the presence of glucose or urea during calcination significantly affected the morphology of the samples.

XPS
XPS is used to explore the elemental composition of samples' surfaces and the obtained spectra are presented in Fig. 3. The survey spectra ( Fig. 3(a)) confirmed the presence of Ni 2p and O 1 s peaks in all samples. The spectra and fitting analysis of the three samples ( Fig. 3

Diffuse reflectance measurements
DR/UV-Vis spectrophotometer analysis is usually applied to detect the band gap energy E g for semiconductors. The measurements give the reflectance as a function of wavelength λ. Then, the Kubelka-Munk equation is used to detect the direct optical band gap energy as follows: where R ∞ is the specimen's reflectance at infinite thickness, F(R ∞ ) is the Kubelka-Munk function, E g is the energy gap, hυ is photon energy, and A is a constant. If the linear segment in the curve of (F(R ∞ ). hυ) 2 versus hυ is extrapolated, it touches the x-axis at the direct band gap energy (eV), as displayed in Fig. 4. The direct band gap energy (E g ) values were 3.44, 3.05, and 3.25 eV for NiO, Ni/NiO (g) , and Ni/ NiO (u) , respectively. Ni/NiO hybrid samples showed a slight red shift toward a higher wavelength (the border of visible light) (Adhikari and Madras 2017).

Surface area and particle size analysis
It is well-known that the surface area has a vital function in the efficiency of adsorbents and photocatalysts. In the adsorption process, as the adsorbent's surface area increases, the number of active sites also increases, and thus a greater adsorption capacity is obtained. On the other hand, photocatalysis starts with the irradiation of the catalyst surface to generate an electron-hole, and as the surface area increases, the rate of electron-hole generation increases. Table 1 shows the obtained results from BET analysis where surface area increases in the order of Ni/NiO (g) < NiO < Ni/NiO (u) . Ni/ NiO (u) showed the largest surface area and the smallest average pore size, which suggests the presence of channels that are open from both sides as shown in SEM micrographs ( Fig. 2(e, f)). As shown in Fig. 5(a), the samples have a broad pore radius distribution of mesoporous structure with pore radius ranges from 1 to 3 nm. It is well-known that mesoporous materials are characterized by their large surface areas, which propose the prepared samples as an excellent choice for adsorption applications. The shape of N 2 adsorption-desorption isotherm provides information about the pore size and shape. As shown in Fig. 5(b−d), no vertical adsorption was noticed for all samples at low relative pressure indicating the lack of microporosity. All the samples exhibited isotherms of type IV with H 3 hysteresis loops revealed to the capillary condensation where N 2 gas molecules condense as multilayers filling mesopores. Low pressure hysteresis (relative pressure < 0.6) was observed, which suggests either volume change by swelling of some   pores or cracking of the sample, or irreversible adsorption of N 2 molecules in channels or pores of the same diameter as nitrogen molecules (Alothman 2012). In this case, cracking of the prepared sample is most probable.

Point of zero charge detection
Figure 6(a) shows the pH pzc as evaluated experimentally by the batch equilibrium method. The pH pzc was evaluated as 8.6, 8.3, and 8.5 for NiO, Ni/NiO (g) , and Ni/NiO (u) , respectively, that is similar to the previously published value (Mahmood et al. 2011). The presence of Ni metal did not significantly affect the surface charge of the sample. These results indicate that the net charge of the samples' surface is positive at pH < 8.

Adsorption studies in the lake of light (dark)
The net surface charge of the adsorbent and consequently, the adsorption process is affected by solution's pH.  Figure 6(c) shows the impact of reaction time on (%E). NiO achieved 98% removal after 8 min and equilibrium was attained in 10 min. Ni/NiO (g) and Ni/NiO (u) showed a slower adsorption rate and attained equilibrium after 90 min. Removal (%) was 100% for NiO versus 95.8% and 99.4 for Ni/NiO (g) , and Ni/NiO (u) , respectively, which was revealed to the morphological difference between samples. In general, adsorption takes place on the surface, followed by diffusion inside adsorbent channels or pores. The maximum adsorption capacity for the samples was investigated and the results are illustrated in Fig. 6(d).
Using the adsorbents for concentrated dye solutions of 500 mg L −1 results in q e of 230, 219, and 210 mg/g for NiO, Ni/NiO (u) , and Ni/NiO (g) , respectively. NiO sample showed a faster initial rate, which revealed its morphology characteristics as it has the largest pore volume and pore size. Up to the initial dye concentration of 500 mg L −1 , all the samples did not exhibit saturation, which indicates that the prepared samples are super adsorbents. As initial dye concentration was raised from 30 to 500 mg L −1 , the mass transfer of adsorbate molecules from the solution to the adsorbent was enhanced thus, the adsorption capacity of NiO increased from 29.9 to 230.9 mg g −1 .

Adsorption kinetics
For kinetic studies, the experimental adsorption data were treated by Lagergren (pseudo-first-order), pseudo-secondorder, and intra-particle diffusion models.

Pseudo-first-order model
where q e and q t are the mass (mg) of adsorbed species per mass of adsorbent (g) at equilibrium and at time t, respectively. From the slope of the linear plot of ln (q e − q t ) versus t, rate constant k 1 (min -1 ) was detected. where k 2 is the rate constant of the adsorption (g.mg -1 min -1 ) and is detected from the intercept of the linear plot of t/q t versus t.

Weber and Morris (intra-particle diffusion model)
This model is applied to explore the adsorption mechanism and clarify if the intra-particle diffusion step is the sole ratelimiting step or not. The rate constant of this step could be detected according to the following equation: The plot of q t against (t 0.5 ) gives a straight line of slope = k i (rate constant of the intra-particle diffusion (mg g -1 min -0.5 )) and intercept = C (parameter indicating the boundary layer effect (mg g -1 )). As shown in Table 2, intraparticle diffusion rate constant, k i increased, and boundary layer effect (C) decreased in the order of NiO, Ni/NiO (g) , and Ni/NiO (u) . These observations suggested that the adsorption on NiO was mainly surface adsorption while in the cases of Ni/NiO (g) and Ni/NiO (u) , the surface adsorption was followed by diffusion of AB molecules through the pores inside the adsorbent (Pholosi et al. 2020). Table 2 shows that the experimental data were successfully correlated to pseudo-second-order model with the best correlation coefficients (R 2 ), and q e values close to experimental ones. These results suggest that the adsorption of adsorbate occurs on an energetically heterogeneous surface. Figure 7 displays the plots of q t vs. (t 0.5 ); the two intersecting lines over the studied time range belong to surface adsorption and diffusion through pores or channels followed by equilibrium.
The initial rate of adsorption at a time close to zero was estimated according to the following equation : Surprisingly, R i values were 219.4, 4.8, and 9.3 mg/g min for NiO, Ni/NiO (g) , and Ni/NiO (u) , respectively. These results Table 2 Adsorption kinetics data as obtained from the applied models Adsorbent qe [experimental] (mg g −1 ) Pseudo-first order Pseudo-second order Intra-particle diffusion model q e (mg g −1 ) K 1 × 10 3 (min −1 ) R 2 q e (mg g −1 ) K 2 × 10 3 (g.mg −1 .min −1 )  also indicate that surface adsorption is the predominant step in the case of NiO, while Ni/NiO (g) and Ni/NiO (u) showed a slower rate due to the slow diffusion of dye particles inside the pores and channels of the adsorbent. These findings are consistent with BET analysis results which showed that Ni/ NiO (u) had the largest surface area but the smallest pore size, while Ni/NiO (g) had the smallest surface area and pore volume.

Adsorption isotherms
Adsorption data at equilibrium were examined by the isotherm models of Langmuir, Freundlich, and Dubinin-Radushkevich (D-R).
Langmuir isotherm proposes that the adsorbent surface has a fixed number of active sites with identical activation energy to which the adsorbate molecules are attached as a monolayer neglecting the steric constraint between the adjacent adsorbed molecules . The linear form of Langmuir isotherm model is expressed as follows: The dimensionless constant R L is calculated as follows: Freundlich isotherm suggests the presence of active sites of dissimilar adsorption energies, on the surface of the adsorbent while the adsorbate molecules are arranged as multilayers (Freundlich 1907). The linear form of this model is written as follows: where Q e is the theoretical maximum uptake per unit mass (mg g -1 ) and b the Langmuir constant (L.mg -1 ). Freundlich constant (k f ) [mg g −1 (mg L −1 ) n ] is related to adsorption capacity and the heterogeneity of adsorption sites energies can be indicated via the dimensionless parameter (n). The linear plot of log (q e ) versus log(C e ) is utilized to evaluate the model's parameters (Foo and Hameed 2010).
Dubinin-Radushkevich isotherm model describes the adsorption on a heterogeneous system with a Gaussian energy distribution, and it is applied to investigate the adsorption mechanism (physisorption or chemisorption). This model can be presented by the following equations: where q DR is the maximum adsorption capacity (mg·g −1 ), β is the Dubinin-Radushkevich constant (mol 2 . kJ −2 ), ϵ is Polanyi's potential, R is the general gas constant (8.314 J. K −1 . mol −1 ), and T is the temperature (K). The numerical value E (mean free energy of adsorption) (kJ.mol −1 ) detects the mechanism of adsorption process (physisorption if E < 8 kJ.mol −1 ) or (chemisorption if 8 < E < 16 kJ.mol −1 ) (Hu and Zhang 2019). Table 3 displays the calculated parameters using these models. Langmuir model offered the best fit for the experimental measurements (R 2 = 0.999), suggesting a monolayer adsorption process (0 < R L < 1). Dubinin-Radushkevich isotherm showed a satisfying fit, and E values were < 8 kJ mol −1 suggesting a physisorption mechanism for all samples.

Thermodynamics studies
Thermodynamic functions such as Gibbs energy change (ΔG), enthalpy change (ΔH), and entropy change (ΔS) were found from the adsorption isotherms of AB solutions of C o = 50 mg L -1 for 2 at various temperatures (303, 313, 323, and 333 K). These thermodynamics parameters have been estimated from the subsequent equations:  Table 4 represents all the thermodynamic coefficients obtained from the previous equations. The values of R 2 were 0. 949,0.993,and 0.992 for NiO,Ni/NiO (g) , and Ni/ NiO (u) , respectively. As shown, the negative values of ΔH indicate the adsorption process is exothermic, which was confirmed by the decrease in %E with increasing temperature. In addition, the negative values for entropy change indicate the reduction in randomness due to the arrangement of adsorbate molecules over the adsorbent surface. The spontaneity of the adsorption process of AB on the samples was confirmed by the negative values of Gibbs free energy. Less negative values of ΔG were obtained with raising the temperature from 303 to 333 K. These results reflected that the adsorption process could be suppressed with the temperature increase.

Synergistic adsorption and photocatalytic degradation processes
The synergistic adsorption-photocatalytic degradation process is a promising method that enhances the elimination of organic pollutants from their aqueous solutions. This concept targets the removal of organic pollutants using intelligent materials through an adsorption mechanism in the lake of light and a photocatalytic degradation mechanism under natural sunlight irradiation. The sunlight irradiation is available for free and supplies both ultraviolet and visible light to the earth (Lavand and Malghe 2015). Figure 8 presents the k pc values for AB dye photocatalytic degradation under UV and sunlight irradiation. All samples showed faster photocatalytic degradation under sunlight irradiation than under UV irradiation. This observation supports the fact that the prepared samples are economical candidates for the removal of organic pollutants. Using the free available sunlight instead of UV lamps save electricity. Ni/NiO hybrids had greater values for the rate constant than NiO, which indicates that the presence of metallic Ni improves the electron-hole generation or delays their recombination. Ni/NiO (u) showed a faster rate than Ni/NiO (g) because it has a higher content of metallic Ni as shown by XRD analysis. Srinivasa et al. stated that the enhancement of the photocatalytic efficiency of Ni/NiO revealed to the reduction in the band gap (Srinivasa et al. 2021). However, in these samples, only a slight red shift was noticed for the direct band gap energy. Herein, the enhancement in dye removal % when using Ni/NiO hybrid samples confirms the co-catalytic effect of metallic Ni, which traps the generated electrons and delays the electron-hole recombination (Fig. 8b) (Adhikari and Madras 2017; Gong et al. 2020;Zhong et al. 2020;Wojty and Baran 2021). The photocatalytic degradation mechanism could be briefly explained as follows: when the photocatalyst's surface is irradiated, electron-hole pairs are produced due to the migration of electrons from the valence band to the conduction band. The econverts the dissolved oxygen into (O 2 .− ) while h + generates (HO . ) from H 2 O. These photo-generated active species and (h + ) are accountable for the degradation of the adsorbed dye molecules according to the following equations: Figure 9(a) explores comparative results of the removal % by adsorption in a dark place, without any irradiation, (measurements after 2 h) with that under UV irradiation and sunlight irradiation (after 30 min). All photocatalytic tests were done with a dye solution of C o = 10 mg L −1 , pH 6, and at 40 °C under continuous stirring. All samples showed the best removal % under sunlight irradiation. Ni/NiO hybrid samples showed significant enhancement in removal % (up to 19%) under irradiation. Taking into consideration that the adsorption process takes 2 h versus only 30 min for the photocatalytic degradation process, the removal % was enhanced by 8, 19, and 16% for NiO, Ni/NiO (g) , and Ni/NiO (u) , respectively, under natural sunlight irradiation. Although Ni/NiO (g) has a smaller surface area (4 times less) than Ni/NiO (u) , its narrower band gap significantly enhanced the photocatalytic efficiency, even so it was comparable to that of Ni/NiO (u) . Generally speaking, the three samples successfully exhibit the synergistic role as an adsorbent in the absence of light and photocatalyst under UV or natural sunlight irradiation. In addition, the samples showed acceptable reusability after four consecutive photocatalytic cycles as explored in Fig. 9(b).

Conclusions
The synergistic role of metal/metal oxides as an adsorbent in the lake of light irradiation and as a photocatalyst whenever light irradiation is available is a promising approach for wastewater remediation. In this study, flower-shaped nano mesoporous NiO and mesoporous Ni/NiO have been synthesized via facile co-precipitation reaction followed by partial reduction within the calcination process. The synergistic adsorption-photocatalytic role of these samples was examined using aniline blue as a model pollutant in aqueous solutions. In the absence of light irradiation, the prepared samples worked as super adsorbents where the pseudo-second-order model and Langmuir model were well correlated to the experimental data. The Dubinin model indicated the physisorption nature of the adsorption process. The adsorption occurred in a two-step mechanism, started with surface adsorption followed by the stage of diffusion. Thermodynamics investigations confirmed that the adsorption was exothermic, spontaneous, and resulted in a more ordered system. The dye removal % under sunlight was enhanced by 8, 19, and 18% for NiO, Ni/NiO (g) , and Ni/NiO (u) , respectively, within a shorter time verifying the synergistic effect. After four consecutive cycles of photocatalysis in sunlight, Ni/NiO samples were stable and efficiently reusable. The experimental data showed that the partial reduction of NiO into Ni/ NiO caused a small red shift in the band gap energy and that metallic Ni has a co-catalytic effect on NiO. The synergistic role of Ni/NiO hybrid samples presents them as promising materials for wastewater remediation applications.
Funding Open access funding provided by The Science, Technology & Innovation Funding Authority (STDF) in cooperation with The Egyptian Knowledge Bank (EKB).
Data availability Raw data are available upon request.

Competing interests
The authors declare no competing interests.

Consent to publish
Authors agree to publish the article in "Environmental Science and Pollution Research" journal.
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