Introduction

Zinc oxide nanoparticles constitute one of the important metal oxides materials that have been widely applied in materials science due to its unique physical, chemical, and biological properties such as biocompatible, environmentally friendly, low cost and non-toxic nature (Alwan et al. 2015; Salahuddin et al. 2015; Ruszkiewicz et al. 2017). Owing to its exceptional properties, ZnO nanoparticles have been applied as a functional advanced material to solve different societal problems especially in the field of catalysis for wastewater treatment and also as cosmetics and antimicrobial additives (Ruszkiewicz et al. 2017). ZnO nanoparticles have several advantages which include unique chemical and thermal stability, robustness, and long shelf life over other metal oxides such as TiO2, WO3, SiO2, and Fe2O3. Zinc oxide exists in the following phases: hexagonal quartzite, cubic zinc blende, and cubic rock salt (Belver et al. 2019). The wurtzite structure is the most common due to its stability at ambient conditions, where every zinc atom is tetrahedrally coordinated with four oxygen atoms (Barhoum et al. 2019). In each phase, zinc oxide nanoparticles (ZnONPs) are a semiconductor material with a direct wide bandgap of ∼ 3.3 eV (Senol et al. 2020). It has advantages such as stabilization on substrate especially the zincblende form with a cubic lattice structure (Parihar et al. 2018). Food and Drug Administration (FDA) includes also zinc oxide as one of the safest metal oxides that can be used in food industries (Bettini et al. 2016).

Zinc oxide nanoparticles have been synthesized via different chemical and physical methods, namely sol–gel, hydrothermal, precipitation and co-precipitation, chemical vapour deposition, spray pyrolysis, magnetic sputtering, microwave-assisted technique, solvothermal, biological routes amongst others (Ul-Haq et al. 2017). Each of the listed methods has advantages and disadvantages and as such different morphologies of ZnO nanoparticles according to characterization tools ranging from nanoplates, nanostars, nanobelts, nanotubes have been reported (Ambika and Sundararajan 2015). Different zinc salts such as zinc acetate dehydrate (ZN(C2H3O2)2·2H2O)), zinc nitrate hexahydrate (Zn(NO3)2·6H2O) zinc sulfate (Zn(SO4)2·7H2O) and zinc chloride (ZnCl2) as precursor have been used to prepare ZnO nanoparticles (Ambika and Sundararajan 2015; Ezhilarasi et al. 2016; Sierra et al. 2018).

However, the problems of stability, dispersion and crystalline structures control of ZnO nanoparticles in aqueous medium constitute a serious bottleneck to industrial application of the material. In order to surmount the challenges, many researchers have focused on the investigation of factors affecting the properties of stable zinc oxides nanoparticles (Yu and Dong 2016). These factors include pH of the reaction mixture, synthesis and calcination temperature, reaction time, concentrations of precursors, solvent medium and surfactant concentration among others (Hajiashafi and Motakef-Kazemi 2018). The aforementioned factors directly influence the particle size, morphology, phase, and surface area of the zinc oxide nanoparticles (Hajiashafi and Motakef-Kazemi 2018; Perillo et al. 2018; Jamal et al. 2019).

Zinc oxide nanoparticles display some properties such as high chemical and thermal stability, unsaturated surfaces, and excellent adsorption behaviour towards organic and inorganic pollutants in aqueous matrix. ZnO nanoparticles possess higher photon absorption efficiency, high surface area, and oxidizing power compared to the other semiconductors and are easily available, non-toxic, and cost-effective for the purification of wastewater (Ray and Shipley 2015). These characteristics have encouraged many scientists in recent years to study the adsorptive potentials of ZnO nanoparticles for the removal of heavy metals from industrial wastewater (Yuvaraja et al. 2018). Different shapes of ZnO nanoparticles have been reported to have high removal efficiency for heavy metals. For instance, a spherical shape ZnO nanoparticles removed lead (Pb2+), cadmium (Cd2+) and mercury (Hg2+) from aqueous solution (Angelin et al. 2015). Additionally, ZnO nanorods, flowers and nanocubes were used as nanoadsorbent to remove arsenic (As3+), chromium (Cr6+) from wastewater (Yuvaraja et al. 2018). Several researchers have synthesized ZnO nanoparticles based on the variation of different process parameters such as pH, stirring speed, reaction time, reaction temperature, mixing ratio, calcination temperature and precursor concentration. However, there is a paucity of information on the comprehensive review on the effects of these synthesis parameters on the shape, size, and phase of zinc oxides. Not only that, the application of ZnO nanoparticles as nanoadsorbent has also not been comprehensively reported by researchers. Herein, the review of some of these process parameters such as the effect of pH, reaction time, and synthesis and calcination temperature on the properties of zinc oxide nanoparticles such as morphology, crystallite size, and surface area is provided. The review also focuses on the application of ZnO nanoparticles as nanoadsorbent for the removal of heavy metals in different wastewater.

Crystal structure of zinc oxide nanoparticles

Zinc oxide (ZnO) is a water insoluble white powder used as an additive in different products especially foods, paints, sunscreens, lubricants, sealants, and batteries (Chandramohan et al. 2017; Perveena et al. 2020). Although ZnO occurs naturally as the mineral zincite, most zinc oxides are chemically produced under different conditions in the laboratory. Zinc oxide nanoparticles can exist in three forms, namely hexagonal-wurtzite, cubic zincblende, and cubic rocksalt (see Fig. 1). The shaded black and gray spheres represent oxygen and zinc atoms (Wang and Zhang 2005). The wurtzite structure is most common and stable at ambient conditions due to its ionicity that resides exactly at the borderline between the covalent and the ionic materials (Chandramohan et al. 2017). The zinc blend ZnO structure can only be stabilized by growing on cubic substrates and the rocksalt structure can be obtained at relatively high pressures, 10 GPa (Özgür et al. 2005). As found with most group II-VI elements, the bonding in ZnO is largely ionic with 0.074 nm for zinc ions (Zn2+) and 0.140 nm for the oxygen ion (O2−) as corresponding radii. This property is responsible for the preferential formation of wurtzite rather than zinc blend structure (Phillips), as well as its high piezoelectricity.

Fig. 1
figure 1

Different phases/network structures of ZnO nanoparticles a cubic rocksalt, b cubic zincblende, c Hexagonal-Wurtzite

Classification of zinc oxide nanomaterials

Classification of ZnO nanoparticles is based on the number of dimensions, which are not confined to the nanoscale range (< 100 nm). The main types based on the dimensions and structures are: zero-dimensional (0D), one-dimensional (1D), two-dimensional (2D), and three-dimensional (3D) nanomaterials (Zhang et al. 2018) and their detail descriptions and morphological properties are provided in Table 1.

Table 1 Different dimension and descriptions of zinc oxide nanoparticles

Morphology of ZnONPs

Different morphologies of zinc oxide nanoparticles have been reported by researchers due to the variation of various process parameters. These include nanorods (Ghannam et al. 2019), nanowires (Hu et al. 2007), nanospheres (Nejati et al. 2016), nanoflowers (Peng et al. 2013), nanotubes (Wang and Cui 2009), nanotetrapods (Jin et al. 2013), nanoplate (Tan et al. 2015) and nanotripods (Azhar et al. 2017). The formation of different morphologies of ZnO nanoparticles shown in Table 2 depends on the applied synthesis conditions.

Table 2 Different morphology of zinc oxides methods and reaction conditions of ZnO nanoparticles

Table 2 shows a description of different morphologies of ZnO nanoparticles synthesized by different researchers. The table revealed different morphologies of ZnO nanoparticle such as nanospheres, nanorods, nanoflowers, nanotubes, nanotetrapods, nanoplates and nanotripods obtained under different synthesis conditions and synthesis methods in the laboratory. The formation of the desired shape of ZnO nanoparticles depends on the role played synthesis parameters such as solution pH, template agents, reaction temperature, reaction time, stirring speed, solvent types, calcination temperature, calcination time and others. The effects of some of the aforementioned factors on the properties of ZnONPs irrespective of the synthesis approach are explained as follows:

Factors influencing the synthesis of ZnO nanoparticles

pH of reaction mixture

pH of the reaction mixture determines the types of ZnO nanoparticles formed (Aziz and Jassim 2018). The crystallite size, morphology, phases, and surface areas of ZnO nanoparticles depend largely on the amount of positively and negatively charge ions present in the medium during the preparation (Chitha et al. 2015; Swaroop and Somashekarappa 2014). This is because solution pH alters the electrical charge of molecules and such alteration will affect their reduction (Hasan et al. 2018). During the synthesis of ZnO in an acidic medium (pH ˂ 7), the amount of hydroxyl ions (OH) is usually low in the solution which hinders hydrolysis and condensation processes, leading to the smaller aggregates at the end of poly-condensation process (Tourné-Péteilh et al. 2018). The decrease in the crystallite size of the zinc nanoparticle in an acidic medium was attributed to the preferential corrosion of the ZnO crystal structure (Rafaie et al. 2014). At the pH of 7 (neutral), the hydrogen ion (H+) and the hydroxyl ion (OH) concentrations are equal, therefore, making the solution having little or no influence at the interfaces of zinc oxide crystals (Mohammadi and Ghasemi 2018). When the pH of the reaction mixture is greater than 7, the number of OH ions is usually high causing strong attraction between the positively charged Zn+ and OH ion; subsequently, increase crystallization and formation of a smaller ZnO nanoparticle. Under high concentration of the hydroxyl ions in a solution, intermediate products such as zinc hydroxide (Zn(OH)2) (see Eq. 1) and salt-containing tetrahydroxozincate ion ([Zn(OH)4]2−) (see Eq. 2) are formed (Rafaie et al. 2014). The drying in the oven and calcination of the products in the furnace as shown in Eqs. (1) and (2) usually lead to the formation of zinc oxide nanoparticles of large crystallite size (Buazar et al. 2016).

The reaction mechanism of growth of ZnO nanoparticles with respect to variation of solution pH from acidic to basic region is shown in Eqs. 16

$${\text{Zn}}^{2 + } + 2{\text{OH}}^{ - } \leftrightarrow {\text{Zn}}({\text{OH}})_{2}$$
(1)
$${\text{Zn}}({\text{OH}})_{2} + 2{\text{OH}}^{ - } \leftrightarrow [{\text{Zn}}({\text{OH}})_{4} ]^{2 - }$$
(2)
$$[{\text{Zn}}({\text{OH}})_{4} ]^{2 - } \leftrightarrow {\text{ZnO}}_{2}^{2 - } + 2{\text{H}}_{2} {\text{O}}$$
(3)
$${\text{ZnO}}_{2}^{2 - } + 2{\text{H}}_{2} {\text{O}} \leftrightarrow {\text{ZnO + 2OH}}^{ - }$$
(4)
$${\text{ZnO}} + {\text{OH}}^{ - } \leftrightarrow {\text{ZnOOH}}^{ - }$$
(5)
$${\text{ZnOH}}^{ - } + {\text{Na}}^{ + } \leftrightarrow {\text{ZnOOH}} - {\text{Na}}$$
(6)

The [Zn(OH)4]2− formed in Eq. (2) can also exist in the form of Zn(OH)+, Zn(OH)2, or Zn(OH)3−, depending on the process parameters, such as the concentration of the zinc ion (Zn2+) and hydroxyl ion (OH) ion during the chemical reaction (Purwaningsih et al. 2016). When the concentration of Zn2+ and OH reaches the super-saturation degree, ZnO nuclei are formed based on reaction (4) (Osman and Mustafa 2015). The previous findings showed that the pH of the reaction mixture influenced the crystallite size and the morphology of zinc oxide nanoparticles. Researchers such as Ogbomida et al. (2018) reported the synthesis of ZnO nanoparticles via sol–gel method using Zn (CH3COO)2·2H2O and NaOH as starting materials. The mixture was stirred for 2 h and subsequently dried for 1 h. ZnO nanoparticles produced were characterized using XRD, SEM, and UV–visible/diffuse reflectance spectroscopy and the calculated crystallite sizes 49.98 nm, 48.31 nm, 38.32 nm, and 36.65 nm for the solution pH of 8, 9, 10 and 11, respectively. The authors found that the ZnO nanoparticles formed were mostly spherical in shape with an optimum solution pH of 9. On the contrary, Ikono et al. (2012) employed Zn (CH3COOH)2·0.2H2O as a precursor, NaOH (precipitating agent) and ethanol solutions to prepare ZnO nanoparticles via sol–gel. The mixture was stirred for 2 h at 25 °C after which the precipitates were washed and dried for 15 min at 80 °C and the size of the crystals formed was directly proportional to the solution pH. The crystallite size increases from 10.94, 17.44, and 38.27 to 74.04 nm with a corresponding increase in the solution pH from 7, 8, 10, and 12, respectively. More so, the mineralogical phase of the prepared ZnO nanoparticles was examined using XRD and the authors observed that as the solution pH increases from 7, 8, 10, and 12, the purity of ZnO nanoparticles also increases and the percentage yield increased from 42.9%, 62.2%, 64.7%, to 100%, respectively. The differences in the crystallite size were linked to the reaction conditions used during the synthesis of the ZnO nanoparticle. In addition, Goryacheva (2016) demonstrated the green synthesis of ZnO nanoparticles using an aqueous extract of Citrus aurantifolia as a stabilizer and zinc nitrate as zinc salt precursor. The synthesis was carried out at 90 °C at pH 5, 7, and 9, respectively. The precipitates formed were washed, dried and annealed in air at 300 °C yielding nanorods with a crystallite size of 100 nm. XRD and SEM analysis confirmed the formation of pure hexagonal wurtzite ZnO nanostructure of different shapes irrespective of solution pH. The authors reported spherical shape at pH 5 and nanorods at pH of 7and 9, respectively. The increase in particle size and change in the morphology of the ZnO nanoparticles synthesized at the pH of 5, 7, and 9 further suggest that solution pH plays an important role in the crystallite size and morphology of ZnO. The results and other research findings carried out by different workers on the effect of solution pH on the crystallite size and morphology on the synthesis of ZnO nanoparticles are summarized in Table 3 as follows.

Table 3 Effect of variation of solution pH on the properties of ZnONPs

Table 3 shows the result of analysis from different researchers due to variation of solution pH. The results revealed that the solution pH plays an important role during the synthesis of ZnO nanoparticle. The ZnO nanoparticles synthesized at lower solution pH (acidic medium) had a smaller crystallite size irrespective of the method and the reaction conditions compared to the neutral and basic medium. This is an indication that the acidic medium affects the ZnO crystal structure leading to the formation of smaller crystallite sizes. At a higher solution pH, a different trend was observed by different authors as shown in Table 3 due to the formation of an intermediate compound, which allows the formation of larger crystallite size. Generally different morphologies of ZnO nanoparticles were observed at different solution pH and the crystallite size is a function of solution pH.

Reaction temperature

The physical methods mostly employed to synthesize nanoparticles require a higher temperature above 350C, while chemical route used for the synthesis of nanoparticles can be carried out at room temperature (Kvitek et al. 2016). The chemical method is the easiest way to synthesize ZnO nanoparticles (Ul-Haq et al. 2017). It has been reported that higher temperature resulted to increase in reaction rate causing rapid consumption of metal ion and hence formation of nanoparticle of a smaller size (Kumari et al. 2016; Saxena et al. 2016). On the contrary, another researcher reported a smaller size of ZnO nanoparticle even at a lower temperature (Pelicano et al. 2016). However, a study by Liu et al. (2020) observed that reaction temperature played critical role in the actual crystallite size of nanoparticles so also the concentration of metal salt precursors. The authors found that low concentration of the precursors often leads to the formation of smaller crystalline size either at a lower or higher temperature, due to the competition between nucleation and growth processes. The research by Pushpanathan et al. (2012a) showed a reduction of particle size from 26 to 17 nm when the temperature of the reaction medium was increased from ambient temperature to 50 °C. The synthesized ZnO nanoparticles were characterized by SEM, XRD, and UV–visible spectrophotometer. From their result, it was noticed that an increase in reaction temperature resulted to a quick reduction of Zn+ ions and subsequent formation of ZnO nanoparticles with a smaller crystallite size. It was also suggested that synthesis of ZnO nanoparticles carried out at lower temperature can also lead to formation of smaller crystallite sizes while at higher temperature nucleation was more favoured. Research by Khan et al. (2014) revealed that employing zinc acetate dihydrate, NaOH and cetyltrimethylammonium bromide (CTAB) as precursors produced flower-shaped like ZnO nanoparticle at different reaction temperatures (25 °C, 35 °C, 55 °C, and 75 °C). The synthesized ZnO nanoparticles were examined using XRD, SEM, EDS, and UV–visible spectrophotometer. The authors revealed average crystallite sizes to be 23.7 nm, 82.5 nm, 69.6 nm, and 88.8 nm for ZnO nanoparticles prepared at 25 °C, 35 °C, 55 °C, and 75 °C, respectively. The increase in the crystallite size of the ZnO nanoparticle in a solution as the temperature increases was attributed to two phenomena, namely Oswald ripening and oriented attachment as shown in Fig. 2. The SEM results showed the existence of two types of flower petal morphologies (slender needle-like and wide-arrow-like). The slender needle-like petals were found in excess at lower temperatures compared to the large arrow-like petals in the different flower bunches of the ZnO colonies. These observations suggested that the temperature exerted great influence on the crystallite size and morphology of the ZnO nanoparticles. The differences as reported by the previous workers (Pushpanathan et al. 2012a) may be due to the differences in synthesis methods and the nature of capping agents used. Similarly, Manzoor et al. (2015) reported the synthesis of ZnO nanoparticles via co-precipitation method using zinc acetate with potassium hydroxide and ethanol as precursors. The mixture was stirred for 1.3 h under the influence of different synthesis temperature from 65 °C, 70 °C to 75 °C. The final product was dried in the oven at 60 °C for 8 h and characterized using SEM, XRD, FTIR, and UV–visible spectrophotometer. The average crystallite sizes of the ZnO nanoparticle obtained at three studied temperatures were 98 ± 43, 135 ± 77, and 458 ± 243 nm, respectively. The authors established a direct relationship between the reaction temperature and crystallite sizes. Furthermore, Pelicano et al. (2016) employed precipitation method involving mixing zinc acetate dihydrate as the precursor, with ethanol and dimethyl sulfoxide; tetramethyl, ammonium hydroxide as solvent and precipitating agents to produce ZnO nanoparticles. The prepared ZnO nanoparticles were investigated by TEM, UV–visible spectrophotometer, and PL. The TEM result indicated an increase in crystallite size (4.72 nm, 5.24 nm, 6.70 and 7.61 nm) as the reaction temperature increases (26 °C, 40 °C, 60 °C and 80 °C). The authors attributed the increment in the crystallite size to the increase in the critical particle radius and coalescence of the smaller particles to complement the growth into larger based on Ostwald ripening (for more soluble materials) and oriented fixing (for less soluble crystals) as shown in Fig. 2.

Fig. 2
figure 2

Schematic of the stage wise-growth of ZnO nanocrystals in solution created based on the research by Layek et al. (2012)

From Fig. 2, the first stage in the synthesis of ZnO nanoparticles is the nucleation of a solid ZnO crystal (E1); this is made possible via rapid precipitation reaction of a zinc salt by the precipitating agents such as sodium hydroxide, (NH4)2CO3 and NH4OH (Herrera-Rivera et al. 2017). The second stage involved the growth of nucleus by diffusion of ZnO molecules from solution onto the surface of the nucleated particle (E2), followed by collision and fusion (E3) of two particles via the oriented attachment (OA) and E4 depict the Ostwald ripening (OR) which involved inter-particle growth via exchange (dissolution and diffusion) of molecules between various particles (Zhang et al. 2010). Other reported researches on the effect of reaction temperature on the crystallite size and morphology of the ZnO nanoparticles are summarized in Table 4.

Table 4 Effect of reaction temperature on the properties of ZnONPs

Synthetic temperature plays a very vital role as shown in Table 4. The Table revealed that the crystallite size of the ZnO nanoparticles increases as the synthesis temperature increases except for the result reported by Indramahalakshmi (2017) who employed the green method for the synthesis of ZnONPs. This implies that the increase or decrease in the crystallite sizes of ZnO nanoparticles also did not only depend on the reaction temperature but also on the method of synthesis.

Calcination temperature

Calcination involves heat-treating a material at a controlled temperature and in a controlled environment. During the calcination process, the particles fuse and enlarge its primary crystallite size (Ruys 2019). This process is called particle coarsening, a phenomenon in solid (or liquid) solutions often used for the growth of larger crystals from those of smaller size and lead to reduction in the number of smaller particles while larger particles continue to grow (see Fig. 3). The particle coarsening phenomenon occurs due to the fact that the smaller nanoparticles are less energetic and unstable compared to the well-packed nanoparticle with a large crystallite size. This process can also take place at room temperature and however can be accelerated during heating process. Different researchers have studied the effect of calcination temperature on properties of zinc oxide nanoparticle and these are reviewed as follows: (Parra and Haque 2014) synthesized ZnO nanoparticles via aqueous chemical route using zinc acetate dihydrate and sodium hydroxide (NaOH) as precursor material for 15 min at 60 °C. The ZnO nanoparticles synthesized were identified by XRD, SEM, EDX, AFM and UV–visible spectrophotometer. The authors reported that as the calcination temperature increases from 200 °C, 400 °C to 500 °C, the particle size also increases from 30, 41, and 44 nm, respectively. Besides, Ashaf et al. (2015) studied the effect of calcination temperature on properties of ZnO nanoparticles by sol–gel using zinc acetate as a precursor. The XRD results indicated the formation of pure phase hexagonal wurtzite ZnO; however the crystallite size decreases from (24–17 nm) as the calcination temperature increased to 300 °C. Further increase in calcination temperature to 500 °C resulted to increase in the crystallite size to 19 nm. Moreover, a similar trend was reported by Mallika et al. (2015) that employed sol–gel method to prepare zinc oxide nanoparticles using zinc nitric and polyvinyl alcohol (PVA) as a precursor and stabilizing agent, respectively. The authors varied the calcination temperature from (400 °C, 500 °C, and 600 °C to 700 °C) at holding time of 1 h. The synthesized ZnO nanoparticles were characterized using XRD, SEM, EDS, FTIR, and UV–visible Spectrophotometer and the average crystallite sizes were 7, 23, 35, and 35 nm. The authors found that as annealing temperatures increase, the grain growth also increases in sizes. A similar trend was observed when citric acid (CA) was used as reducing agent under the same calcination temperature and holding time. They reported an increase in the crystallite size from 13, 23, 30, and 40 nm. ZnO nanoparticles have been synthesized by sol–gel technique using zinc acetate dihydrate and diethanolamine as the precursor materials. The effects of calcination temperatures (300 °C, 500 °C, 650 °C, 700 °C, and 750 °C) were studied. The properties of the ZnO nanoparticles were examined by SEM, XRD, FTIR, and UV–visible Spectrophotometer. The XRD result according to Scherer equation indicated that the crystallite size increased with increasing calcination temperature (Kayani et al. 2015). Generally, it was found that as the calcination temperature increases, the crystallite sizes of the ZnO nanoparticles increase which can also affect its purity and morphology.

Fig. 3
figure 3

Scheme of nanoparticle growth controlled by: a Ostwald ripening mechanism; b oriented attachment mechanism created based on the research by Kyoung-Ku et al. (2019)

Furthermore, the growth of ZnO nanoparticle usually occurs via two mechanisms, namely oriented attachment (OA) and Ostwald repining (OR). Oriented attachment is a physical process that is important during crystallization process and involved direct self-organization of the primary nanoparticles and subsequent conversion by interface fusion to single crystals through sharing a common crystallographic orientation (Cao et al. 2019), as illustrated in Fig. 3. Ostwald ripening involved diffusive transfer of the dispersed phase from the smaller to the larger droplets. The Ostwald Ripening occurs because larger particles are thermodynamically stronger than smaller particles. High temperature influences Ostwald ripening due to its effect on interfacial energy, coefficients of growth rate, and solubility (Westen and Groot 2018). Oriented attachment happens because the aggregation decreases the system's interphase boundary and total surface energy (Dalod et al. 2017). Previous works on the variation of calcination temperature on the properties of ZnO nanoparticles are summarized in Table 5.

Table 5 Influence of variation of calcination temperature on the properties of ZnONPs

Table 5 revealed direct relationship between calcination temperature and crystallite sizes. The higher the calcination temperature, the larger the crystallite size of the ZnO nanoparticles irrespective of the method, solvent and other synthesis conditions. Calcination temperatures also affect the morphology of ZnO nanoparticles and in most cases spherical shape of ZnO nanoparticles predominate.

Effect of different zinc salts precursor

The synthesis of ZnO nanoparticles using different zinc salts precursor such as zinc acetate (Zn (CH3COO)2, zinc nitrate(Zn(NO3)2, zinc sulfate (ZnSO4) and zinc chloride (ZnCl2) has been widely investigated (Ambika and Sundararajan 2015; Ezhilarasi et al. 2016; Sierra et al. 2018). The use of different zinc salt precursors also influenced the morphological, textural and optical properties of ZnO nanoparticles (Mayekar et al. 2014). For instance, Gusatti et al. (2011) used different zinc salts (ZnCl2 and Zn (NO3)2·6H2O) as precursors to synthesize ZnO nanoparticles. The mixture of zinc salts, ethanol and sodium hydroxide was stirred at 90 °C for 1 h and later the precipitate was washed severally and dried at 65 °C for a few hours. It was noticed that the average crystallites size of ZnO nanorods obtained using ZnCl2 was 23 nm while morphology of ZnO nanoparticles prepared using Zn(NO3)2·6H2O precursor was mixture of nanoprisms and nanorods shape with an average crystallite size of 18.91 nm. Also, Mayekar et al. (2014) utilized zinc nitrate, zinc chloride and zinc acetate and sodium hydroxide to prepare ZnO nanoparticles via sol–gel method. The mixture was maintained at 70 °C for 1 h, and the gel was later dried at 65 °C for several hours. The properties of the ZnO nanoparticle were identified using XRD, SEM, EDX, and UV–visible spectrophotometer, and it was found that the crystallite size was 36.06 nm (Nanoflowers), 38.90 nm (Rice-like), and 39.91 nm (Spherical) for ZnO nanoparticles prepared using zinc nitrate, chloride and acetate, respectively. The result also indicated that the ZnO nanoparticles synthesized using zinc acetate possessed highest purity while ZnO nanoparticles synthesized from using other zinc salts have similar crystallite size but different shapes. Moreover, Gusatti et al. (2011) employed hydrothermal method to synthesize ZnO nanoparticles using zinc nitrate, zinc acetate and zinc sulfate, sodium hydroxide as precipitating agent. The reaction was maintained at 120 °C for 3 h and dried at 70 °C. The ZnO nanoparticles produced were characterized by XRD, SEM, and TEM. The results showed successful synthesis of ZnO nanoflowers (100 nm), nanoflakes (125 nm) and nanoprisms (100 nm) from zinc nitrate, zinc acetate and zinc sulfate, respectively (Yu and Dong 2016). This implies that different zinc salts produced different shapes of ZnO nanoparticles with little or no effect on the crystallite size of zinc oxide nanoparticles. Different zinc precursors such as zinc nitrate (ZnNO3), zinc chloride (ZnCl2), and zinc sulfate (ZnSO4) were used to synthesize ZnO nanoparticles via chemical precipitation method. The authors established that the crystallite size was the same (9.63 nm) irrespective of the zinc salt precursor and other synthesis conditions (Stirred at room at temperature for 2 h, dried at 80 °C for 15 h). This further confirmed that the source of precursor (Zn) from different zinc salts did not have any significant effect on the crystallite size of the ZnO nanoparticles produced. The influence of using different zinc salt precursors for the synthesis of ZnO nanoparticles as reported by different researchers is summarized in Table 6.

Table 6 ZnO nanoparticles synthesized based on variation of the different zinc salts precursor

From Table 6, it is obvious that different zinc salts have little or no effects on the crystallite size of ZnO nanoparticles but greatly affect its morphology. Additionally, the variation in crystallite sizes of ZnO nanoparticles also depends on the adopted synthesis methods and other factors.

Concentration of precursors, precipitating and capping agents

The morphology and crystallite size of ZnO particles often depend on the concentration of metal salt precursors precipitating, and capping agents used (Phan and Nguyen 2017). Thus, these factors play an important role in the synthesis of ZnO nanoparticles and other nanostructured materials and thus very frequently used to avoid over growth of nanomaterial (Gulati et al. 2016). Capping agent is responsible for the control of growth rate, particle size, and prevention of particle aggregation (Bakshi 2015). Moreover, it has been reported by Al-Hada et al. (2014) that the nanoparticles can be stabilized by immobilization on a support such as organic ligand shell, polymers, dendrimers, cyclodextrins, and polysaccharides (See Fig. 4). The capping agents must be stable enough and withstand enough heat to prevent aggregation of the nanoparticles at temperatures suitable for synthesis (Gulati et al. 2016). Many researchers including (Borghei et al. 2013) have reported that the synthesis of ZnO nanoparticles using low concentration of zinc precursor always leads to the formation of nanoparticles of smaller crystallite size. In their research, zinc acetate dihydrate and sodium hydroxide, ethanol were mixed together and the particles formed were dried at 100 °C for 5 h and later calcined at 250 °C for 3 h to obtain ZnO nanoparticles with crystallite size ranging from 20, 27, 30 to 36 nm at different mixing ratio of sodium hydroxide to zinc salts precursor (1:1, 1:2, 1:3, and 1:4), respectively. Different morphologies such as Cauliflower-like, irregularly shaped, and non-uniform were obtained by increasing the concentration ratio of the reactant raw materials. From this result, it was suggested that a higher ratio of sodium hydroxide/zinc salt precursor resulted to the formation of larger crystallites size of ZnO. Similarly, Alami et al. (2015) employed spray pyrolysis method to prepare ZnO nanoparticles using different concentrations of Zn (NO3)2, 6H2O (0.05, 0.1, and to 0.2 M). The reaction was carried out at solution spray rates of 2 ml/min onto a preheated glass substrate at 500 °C for 10 min. The crystallite sizes obtained were 9.95, 27.40, and 32.35 nm for 0.05, 0.1, and 0.2 M concentration of the Zn salt which confirm the earlier analysis that the concentration of zinc salt greatly affects the crystallite size of the ZnO nanoparticles.

Fig. 4
figure 4

Selected capping agents used in synthesis of ZnONPs, possible mechanism of formation of ZnO nanoparticles using plant Extract (a) and a proposed mechanism of the interaction between zinc ions (Zn+) and polyvinyl pyrrolidone (PVP) (b)

Table 7 contains summarized works on the effects of salt precursor, precipitating and capping agents on the nature of ZnO nanoparticles carried out by different researchers.

Table 7 Effect of variation of concentration of zinc salt precursors with sodium hydroxides on the nature of ZnO nanoparticles

Table 7 reveals that as the concentration of the zinc salt precursors increases, the crystallite size of ZnO nanoparticle produced also increased. Similarly, the crystallite sizes of the zinc oxide nanoparticles also increases as the concentration of the PVA and NaOH increases, respectively.

Reaction time

Reaction time is the time required for completion of all steps during the synthesis of nanoparticles including the reduction and formation of nanoparticles. Reports have shown that the formation of nanoparticles starts within minutes after the addition of the metal salt precursors and increases as the reaction time increases (Chitra and Annadurai 2014). For instance, Manzoor et al. (2015) prepared ZnO nanoparticles via co-precipitation method using zinc acetate with potassium hydroxide and ethanol as precursors. The final product was dried in the oven at 60C for 8 h and characterized using SEM, XRD, FTIR, and UV–visible spectrophotometer. The mixture was stirred for 1.3 h by varying the nucleation time and they found that the crystallite size of the ZnO nanoparticles to be 20, 24, and 57 nm for nucleation time of 0, 2, 8 min. The authors found the ZnO nanoparticles have a nearly spherical shape with narrow particle size distribution. From the result above, it can be deduced that the reaction time is proportional to the crystallite size of ZnO nanoparticles. The step by step involved on the variation of reaction time during the synthesis of ZnO nanoparticles is shown in Fig. 5.

Fig. 5
figure 5

Schematic illustration for effect of reaction time on the synthesis of ZnO nanoparticles (Polte et al. 2010)

The first step 1(T1) in Fig. 5 depicts the nucleation process (the process whereby nuclei (seeds) act as templates for crystal growth) which is the first step in the formation of ZnO oxide nanoparticles. This process takes place within a few seconds of the reaction (Thanh et al. 2014). Step 2 involves the growth of the nanoparticles up to an average crystallite size of 5.2 nm as the time increases from T1 to T3. However, it has been reported by Smolkova et al. (2017) that diffusion mechanism controlled the growth of nanoparticles during the synthesis which only occurs over a few seconds. The fourth stage is a rapid consumption of the zinc salt left in solution where the particle size increases rapidly from 5.2 to 7.7 nm. ZnO nanorods have been successfully synthesized by combination of sol–gel and chemical precipitation methods using zinc acetate and sodium hydroxide as starting materials. The authors reported crystallite particle size of 33 nm, 35, 38, and 42 nm for different synthetic time (2, 4, 6, and 8 h), respectively. The synthesized ZnO nanoparticles were dried in the oven at 100 °C for 2 h and later calcined at 100 °C for 2 h. The prepared ZnO nanoparticles were characterized by XRD, FTIR, SEM, UV–visible spectrophotometer and PL and it was established that the nucleation time affects the crystallite sizes of ZnO nanoparticles. Their result indicates that the crystallite size increases as the nucleation time increases. Similar trends have been reported by various researchers as summarized in Table 8.

Table 8 Effect of reaction time on the nature of ZnO nanoparticles

Table 8 shows that different crystallites size is a function of nucleation time. A longer nucleation time leads to the formation of larger crystallite size. This trend observed in Table 8 may be because the particles have enough time to fuse and further fusion yielded large ZnO.

The effect of other synthesis conditions on the surface area, porosity and the crystal structure of ZnO

In evaluating the adsorption capacity of any adsorbent, surface area and the total pore volume play an important role. Studies have shown that the high surface area of ZnO nanoparticles, the greater adsorptive capacity and better the removal rate of heavy metal ions in wastewater (Shaikh and Ravangave 2015). The effects of other synthesis conditions or factors are on the textural properties, and crystals structure of ZnO nanoparticles is summarized in Table 9.

Table 9 Effect of reaction temperature on the properties of ZnO nanoparticles

The results of different analyses summarized in Table 9 indicate that the surface area of ZnO nanoparticles increases so also the stirring rate and concentration of the zinc precursor, while the surface area reduces as reaction temperature and calcination temperature increase. The results also show that the change in surface area as the synthesis condition changes has little or no effect on the crystal structure of the ZnO nanoparticles produced. The effect of solution pH suggests that large surface area is obtained as the pH approaches a basic medium. The effect of different zinc salt did not have any major effect on the surface area of the ZnO nanoparticles. The next section of the review focuses on the application of ZnO nanoparticles for wastewater treatment.

Water pollution

Water pollution occurs when unwanted materials enter into water bodies, change its quality, and later become harmful to the environment and human health (Alrumman et al. 2016). Water is an important natural resource that needs to be protected against foreign toxic materials (Subramanian 2018). In fact, water pollution is the leading worldwide cause of deaths and diseases more war (Ladu et al. 2018). The discharge of the untreated wastewater into the water bodies has been attributed to the growing number of several diseases such as cholera, typhoid fever among others (Singh et al. 2018). It has been estimated that the world generates more than 5–10 billion tons of industrial wastes, much of which is pumped untreated into rivers, oceans, and other waterways (UNEP-Global. Marine Litter 2020). The wastewater is associated with several pollutants ranging from organic, microbial to inorganic such as heavy metals which include lead (Pb), zinc (Zn), nickel (Ni), arsenic (As), copper (Cu), chromium (Cr), iron (Fe), selenium (Se), vanadium (V), cobalt (Co), cadmium (Cd), and mercury (Hg) as a result of industrial activities (Alalwan et al. 2020). These heavy metals are recognized as a major toxic hazardous material to humans and the aquatic system (Akpor et al. 2014).

Effect of heavy metals and treatment methods

Globally, heavy metals pollution in water has caused serious health effects to humans and the ecosystem since they are non-biodegradable and highly toxic (Ogbomida et al. 2018). These heavy metals are distributed in the environment through natural and anthropogenic activities (Engwa et al. 2016). Exposure to metals such Pb, Zn, Ni, As, Cu, Cr, Fe, Se, V, Co, Cd, and Hg can affect growth and development causing mental disorder, cancer, damage the liver, kidneys, lungs, and in extreme cases, death depending on the exposure dose and time (Monisha et al. 2014). The specific effects of some of the heavy metals have been summarized (see Table10). The possible removal of these pollutants from the wastewater before the discharge to the environment has recently become the focus of many researchers owing to its negative effect on the environment. Effective wastewater treatment is a major prerequisite for a growing economy in the current era of water scarcity. Methods for removing these pollutants from wastewater include chemical precipitation, ion exchange, photocatalytic technology, coagulation, electrocoagulation, membrane bioreactor, flocculation, chemical oxidation and reduction, reverse osmosis, ultrafiltration electrodialysis, and activated carbon adsorption (Abbas et al. 2016). However, the aforementioned methods have some limitations such as sensitive operating conditions, high reagent requirement, low removal efficiency, high cost, and generation of toxic secondary pollutants (Gunatilake 2015). Among the methods used for removal of heavy metals, adsorption technique platform with nanotechnology has been recognized as the most suitable method for removal of heavy metals due to their unique properties which include, low cost, high efficiency, ease of operation, simple design, cost-effective and, regeneration potentials (Cai et al. 2019; Wołowiec et al. 2019). Furthermore, it has been reported that adsorption did not produce secondary pollutants (Gupta et al. 2014). Many materials such as activated carbon from agricultural waste chitosan, clay, polymer biopolymers, graphene-based are known for their efficiency for the removal of heavy metals (Sharma et al. 2017; Maduabuchi 2018). Many other nanoadsorbents developed include metal oxide nanoparticles such as zinc oxide, ferric oxides, magnesium oxides, titanium oxides, manganese oxides, silicon oxides, cerium oxides, and aluminum oxides nanoparticles, nanocomposites and rubber tire, multiwalled carbon nanotubes, carbon nanotubes (Ihsanullah et al. 2015; Mahmoodian et al. 2015). Among the aforementioned, metal oxides such as ZnO have been widely recognized as a suitable nanostructure material that can solve the deficiencies associated with many adsorbents. Zinc oxide is the most popular due to its excellent properties such as high surface area, easy removal after sorption, and pronounced selectivity of pollutants at trace concentrations, antimicrobial activities, nontoxicity, and simple synthetic methods among others metal oxide nanoparticle (Kumar et al. 2013). ZnO nanoparticles have been the major focus of many researchers as a new adsorbent that could be used to remove heavy metals from industrial wastewater due to its exceptional chemical and thermal resistance and others (Gupta et al. 2014).

Table 10 The MCL standards for the most hazardous heavy metals. Source: Babel and Kurniawan (2003)

Adsorption technology

Adsorption is a mass transfer process that involves accumulation of substances at the interface between two phases, such as liquid–solid, liquid–liquid, liquid–gas, and solid–gas interface and becomes bound by physical or chemical interaction (Girish and Murty 2017). Adsorption is an effective and inexpensive process used for the treatment of wastewater (Lata et al. 2019). The removal of pollutants usually occurs when an adsorbate in a solution comes into contact with the adsorbent, concentrates or accumulates on another surface as shown in VIII. Adsorption process is often reversible, since the adsorbents can be regenerated by desorption process (Cai et al. 2019). Adsorption can be classified into physical adsorption (physisorption) and chemical adsorption (chemisorption) and depend on the properties of both the adsorbate and the adsorbent (Ziółkowska et al. 2016). An adsorbent material must have certain important properties, such as high surface area, the distribution of pores, and the existence of the pores that have a significant influence on the form of the adsorption process, high internal volume accessible to the various target components (Kyzas and Kostoglou 2014). If the forces of attraction that exist between adsorbate and adsorbent have a physical nature, the process is called physisorption. This process is characterized by the formation of weak intermolecular forces such as van der Waals forces, reversible process, and formation of multilayer of adsorbate on the adsorbent, decrease with increase in temperature and has a low enthalpy of adsorption. On the other hand, if the interaction between the adsorbent and adsorbate has a chemical nature, the process is known as chemisorption, thus resulting to the formation of a strong chemical bond (Abas et al. 2013). The chemisorption process is characterized by the formation of a monolayer of adsorbate on the adsorbent, has a high enthalpy of adsorption and can take place at all temperatures and in most cases not reversible (see Fig. 6).

Fig. 6
figure 6

Adsorption process and adsorption types created based on research by Christmann (2010)

Mechanisms of adsorption technology

The mechanism of adsorption involves the sorption of sorbate molecules on the surface of the sorbent through molecular interactions, and diffusion of sorbate molecules from the surface into the interior of the sorbent materials, either by monolayer or multilayer (Bushra et al. 2017). Adsorption process involves the binding of metal ions by physical (van der Waals forces) or chemical (ion exchange, chelation, precipitation, binding, complexation, and reduction). Various factors such as the nature of adsorbent, temperature, dosage, adsorption time, the reaction temperature, and the surface area played an important role in the removal of heavy metals by ZnO nanoparticle (Iftekhar et al. 2018). The adsorption of heavy metals from wastewater using ZnO nanoparticles could be complex depending on the nature of capping agents used during the synthesis of ZnO nanoparticles, because the capping agent may contain different functional groups that may greatly influence the removal of the heavy metals through metal ion exchange, chelation, precipitation, binding, complexation, and reduction (see Fig. 7.). The adsorption process may be simple or complex depending on the number of contaminants in the aqueous matrix. There are instances where the adsorption process may contain one, two, three or more pollutants in the wastewater and in most cases serious competition for the active surface sites among the adsorbates becomes an issue. The selectivity factor for the adsorbents also comes into play and may be in the form of electrostatic repulsion (desorption) or electrostatic attraction (adsorption) between the adsorbate and adsorbents.

Fig. 7
figure 7

Adsorption mechanisms created based on research by Mathew et al. (2016)

Physical adsorption (physisorption) is the simplest immobilization method; it occurs when the attractive forces present between adsorbate and adsorbent are weak such as van der Waals forces, hydrophobic interactions, and hydrogen bonding (Sandhyarani 2019). This process occurs readily at low temperatures and decreases with increasing temperature. Physical adsorption has been reported to have a low enthalpy of adsorption (< − 40 kJ/mol) with a multilayer adsorbate on adsorbent (Chakraborty et al. 2009). Chemical Adsorption (chemisorption) involves a chemical reaction between the adsorbent and adsorbate and usually leads to chemical bond formation and have a higher enthalpy of adsorption in the range of 80–240 kJ/mol (Mahmoud 2015).

Zinc oxide Nanoparticles as Nano-adsorbent for removal of heavy metals from aqueous matrix

Different researchers have employed ZnO nanoparticles to remove heavy metals from simulated and industrial wastewater. For instance, Mahdavi et al. (2012) investigated the removal of Cd2+, Cu2+ Ni2+, and Pb2+ from aqueous solutions using ZnO nanoparticles as an adsorbent. The XRD result in the ZnO nanoparticles revealed a crystallite size of 16.70 nm while SEM analysis confirmed the formation of rod-like shape with a crystallite size of 25 nm. The BET analysis of the revealed specific surface area, total pore volume, and pore size of 31.20 m2/g, 12.09, and 15.81 nm, respectively. The authors found that the adsorption of the heavy metal ions increases as the pH of the solution increases from acidic to alkaline. It was noticed that the pH of the solution played an important role in the adsorption of heavy metals by nanoadsorbents. This is expected because, at lower pH (acidity conditions), the hydrogen ions strongly compete with heavy metal ions in the solution (Ouyang et al. 2019). Moreover, the authors also observed that an increase in the absorbent dose (0.5 to 5 g/l) resulted to an increase in the removal efficiency of Cd2+, Cu2+, Ni2+ and Pb2+ with Pb2+, having the highest percentage removal of 81.5% at a dosage of 5 mg/g. The observed trend was attributed to the increase in the number of binding sites as the nanoabsorbents increase (Xie et al. 2015). The maximum removal efficiency was achieved for all the four ions after 180 min and there was no significant increase in the removal efficiency of the metal ions after 180 min to 24 h. The maximum uptake of the metal ions was reported to be 114.5 mg/g. In addition, Salmani et al. (2013) reported removal efficiency of 89.6% for Cd2+ion using ZnO nanoparticles. The authors found that the Cd2+ ion removal followed the pseudo-second-order and Langmuir isotherms model and the efficiency was highly sensitive to the change in pH and ionic strength. They also confirmed that removal efficiency increases as the pH of the solution increases from 4 to 7. The result showed that the maximum removal of Cd2+ion was achieved at lower contact time and later decrease despite increase in the contact time. This shows that the solution pH, contact time, concentration of metal, and temperature affect the removal of metal ions using ZnO nanoparticle as an adsorbent. Moreover, other works done by various researchers on the application of ZnO nanoparticles as a nanoadsorbent for the removal of heavy metals from wastewater is presented in Table 10

Table 11 shows ZnO nanoparticle of different sizes and morphologies were synthesized by different methods. The result revealed that the ZnO nanoadsorbents show adsorptive removal efficiency between 61 and 100% with ZnO nanoparticle with a spherical shape has the highest (100%) removal for Cu2+. From the Table 11, Bi3+ has the lowest adsorption using spherical ZnO nanoparticles. The adsorptive capacities of ZnO nanoparticles depend majorly on several factors particularly the methods of synthesis which have direct link to the textural, morphology and optical properties of the material under review.

Table 11 Summary of ZnO nanoparticles as nanoadsorbent for the removal of heavy metals from aqueous matrix

Effect of solution pH on removal efficiency of heavy metals

pH is one of the most significant control factors that directly influence removal of heavy metals during adsorption process. It can also influence the binding sites on the surface of the nanoadsorbent and also affect the degree of heavy metals ionization and chemical nature of the adsorbent (Jin et al. 2011; Duan et al. 2016). For instance, Degen and Kosec (2000) studied the effect of pH on the removal of heavy metals from an electroplating wastewater using ZnO nanoparticles as an adsorbent and found that at a pH below 7 (acidic), the solution was highly protonated (H+) resulting in a high positive surface charge on the surface of the adsorbent which repels the positively charged metal ions and subsequently low removal efficiency. However, due to dominant hydroxide ions (OH) at a pH greater than 7, the adsorbent surface becomes negatively charged resulting to a high negative charge density that attracts more metal ions (see Fig. 8) They also reported that at a pH above 6, there is possibility that the metals could precipitate to form hydroxides as a result, the adsorption process is hindered. Furthermore this trend showed that electrostatic interaction played a major role in the removal of heavy metals.

Fig. 8
figure 8

Effect of pH on the adsorption of heavy metals created based on research by Abbar et al. (2017)

Conclusion

In summary, the effects of different synthesis parameters on the textural, optical and microstructural properties of ZnO nanoparticles have been provided. The adsorptive behaviour of ZnO nanoparticles for the removal of heavy metals especially at different solution pH has also been summarized. Based on the review, the following conclusions were drawn. Acidic medium favoured the formation of smaller size of ZnO nanoparticles compared to alkaline medium. Several reports indicated a decrease in the crystallite size of ZnO nanoparticles as the pH increases from 7 to 12. Reaction time, reaction temperature and calcination temperatures influenced the crystallite size of ZnO nanoparticles. Different zinc salts have little effect on the crystallite size but exerted greater influence on the morphology of the ZnO nanoparticle produced. The concentration of the zinc precursor shows increases in the crystallite size at a higher concentration of zinc in the solution. These findings indicated that these factors strongly affect the crystallite size and the morphology of the zinc oxide nanoparticles. The crystallite sizes with respect to each parameter also depend on the methods of synthesis of ZnO nanoparticles. There are still divergent views as reported by the researchers on the increase and decrease in the particle size of the ZnO nanoparticle. The mechanisms of the increase or decreases in the crystallite size with respect to the variations of solution pH, synthesis temperature, different salt precursor, and synthesis time are not clearly understood and still require further investigation. Optimization of all these parameters should be carried out to fully understand the mechanism of the synthesis of ZnO nanoparticles. Regeneration of the ZnO should be performed to evaluate the cost effectiveness of ZnO as an adsorbent. Future research should focus on the immobilization of ZnO nanoparticles on suitable supports for easy separation after usage.