Preparation and application of an innovative integrated agent product for phosphorus control and oxygen release

In this study, anoxygen-releasing andphosphorus-controlling agent (ORPC) consistingof calciumperoxide (CaO2), bentonite, cement, stearic acid (SA), citric acid (CA) andfine sandwas synthesized successfully andused topurify phosphorus-rich riverwater. The removal of phosphorususingORPCwas studied in actual river water and the results found that over 75.0% phosphorus was removed by adding ORPC at 30 mL h 1 flow rate in initial phosphorus concentrations of 0.76 mg L . TheORPCwas further used to evaluate the changes of aluminumphosphate (Al-P), ferric phosphate (Fe-P) and calcium phosphate (Ca-P) in sediment. Fe-P, Al-P, and Ca-P in the sediment increased from 0.14, 0.196, and 1.63 mg g 1 to 0.159, 0.372, and 2.74 mg g 1 respectively within 28 days, indicating that the total dissolved phosphorus in the overlyingwater could be adsorbed by ORPC and further transformed into Al-P, Ca-P, and Fe-P in the sediment, thus inhibiting the release of endogenous phosphorus in sediment to thewater. In addition, the performanceofORPCwith various contents of SAandCaO2was investigated. In summary, ORPCcanbeemployed to adsorb phosphorus inwater and prevent phosphorus release from sediment, therefore achieving the purpose of controlling phosphorus and maintaining DO at a reasonable level.

which is characterized by hydrophobic, non-toxic, and easily biodegradable properties (Wang et al. 2021).
Fe 2þ þ HO † ! Fe 3þ þ OH À (4) Therefore, in this work, SA was selected to embed CaO 2 powder to prepare a phosphorus-controlling and oxygen-releasing agent which has a strong mechanical strength. The addition of cement, fine sand, and bentonite during the preparation of the innovative phosphorus-controlling and oxygen-releasing agent (ORPC) can remarkably increase the efficiency of oxygen oxygenrelease utilization and phosphorus removal. Furthermore, compared with other phosphorus-removal agents which exceeded 3 $ kg À1 created by Chen et al. (2016), the 0.5 $ kg À1 ORPC exceeded in this study was cheaper. The lifespan of ORPC surpassed over 28 days, whereas the material prepared by Zhang et al. (2018) and Liang et al. (2018) was merely maintained for about seven days. For the above reasons, therefore, the objectives of this work are to: (a) prepare and characterize the innovative ORPC; (b) investigate the effects of various mass fractions of CaO 2 and SA on phosphorus removal and oxygen-release performance; (c) elucidate the effect of ORPC in removing phosphorus from actual river water; (d) evaluate the inhibitive effect of ORPC on phosphorus release from river sediment and analyze the transformation of various forms of phosphorus in sediment.

Material preparation and characterization
The supplies of the chemicals and other materials used in this study are available in the Supplementary Materials (Text S1).
The ORPC was prepared by the following procedure: first, 2.33 g of SA was added to a sufficient amount of ethanol under magnetic stirring until all SA was dissolved (T ¼ 60°C). Second, CaO 2 powder, bentonite, cement, fine sand, and citric acid (CA) with a mass ratio of 7:1.5:14:10:0.6 were simultaneously added and thoroughly mixed. Then, cylinder-shaped ORPC was manufactured by a tablet press machine. Finally, the ORPC was placed in an oven at 30°C for 12 h drying. Some researchers have prepared oxygen-releasing material by embedding CaO 2 . However, in all of the studies above, a certain amount of water was added to the CaO 2 during material preparation, leading to the loss of available oxygen in advance (Nykänen et al. 2012;Lee et al. 2014). The solvent in the whole preparation process of ORPC in this study was ethanol, which could not react with CaO 2 . Since the other chemicals in the ORPC were unable to react with CaO 2 , the content of CaO 2 in the prepared ORPC was greatly maintained in the whole preparation process. All the materials were stored in a desiccator at room temperature. A scanning electron microscope (Hitachi S-4800 FE-SEM, Japan) was used to characterize the surface microstructure of the CaO 2 powder and ORPC. Infrared spectra were detected by using Fourier transform infrared spectroscopy (Thermo Nicolet 6700, USA). A rotating anode X-ray powder diffractometer (Rigaku Denki Dmax2550, Japan) was used to analyze the structure of the substances.

Batch experimental procedures
The phosphorus solution was prepared by dissolving 0.2207 g solid potassium dihydrogen phosphate with 1 L ultrapure water which was then stored in a cabinet at 25°C. All batch tests were carried out in a 1 L glass reactor. The perforated sealing membrane was used to allow the oxygen in the reactor to escape, but prevent the outside oxygen from entering. The temperature was held at 25°C through being kept in a closed and dark cabinet. Phosphorus-containing water of 1.91 mg L À1 was prepared by adding 10 mL stock phosphorus solution to the 990 mL ultrapure water. In order to assess ORPC performance for oxygen release more intuitionively, the DO of the phosphorus-containing water was set as 0 mg L À1 by nitrogen-stripping initially. A mass of 15 g of ORPC was added to the phosphorus-containing water. At the predetermined time, the samples were taken and filtered by 0.45 μm millipore membrane for measuring changes in phosphorus concentration. DO and pH were continuously monitored within 28 days. DO was measured by using a portable DO meter (model HQ40d, Hach, USA) and pH was recorded by a digital pH meter (Mettler-Toledo DELTA 320, Greifensee, Switzerland). All experiments were carried out three times, and the average values were reported.

Test for the actual river water body in flowing pattern
A mass of 500 g of ORPC was evenly added above 5 centimetres of thick fine sand at the bottom of the reactor loaded at 3,200 g m À2 to simulate the actual river flowing pattern (Figures S1(a) and S1(b)). The river water used in the experiment was obtained from the upstream of the Qingchun River that flows through the Xuhui campus of East China University of Science and Technology (ECUST), Shanghai, China. Potassium dihydrogen phosphate was added to the actual river water to prepare phosphorus-containing river water with three different concentrations, i.e. 0.76, 1.22, and 2.07 mg L À1 , respectively. Then, the river water flowed through the three closed reactors individually at flow rates of 30 mL h À1 , 120 mL h À1 , and 240 mL h À1 , respectively. The changes of TP, DO and pH of the river water and effluent after flowing through the reactor were measured and compared. All experiments were repeated three times, and the average values were reported.
2.4. Test for the actual river water body in flowing pattern with the river sediment on the bottom of the reactor The river sediment was put on the bottom of the reactor with a height of five to six centimetres that simulated an actual flowing river ( Figure S1(c)). A mass of 210 g of ORPC was paved evenly on the surface of the sediment. The sediment and river water used in the experiment were obtained from the Dongshangao pond and the Qingchun River that flowed through the Xuhui campus of ECUST, respectively. River water was pumped through the closed reactor. The changes of TP, DO and pH in the influent and effluent were measured and compared within 28 days. The changes of the various forms of phosphorus on top of the sediments and in the ORPC were measured.

Analytical methods
The active inorganic phosphorus in the water was analyzed with ammonium molybdate spectrophotometry. The active inorganic phosphorus in the sediment was analyzed with the alkali fusion-molybdenum antimony colorimetric method. In accordance with the Lake Eutrophication Investigation Specification, various inorganic forms of phosphorus were extracted and separated from the sediment, and the contents were determined by an ultraviolet spectrophotometer. Details for the determination of the various inorganic forms of phosphorus in this study are available in the Supplementary Materials (Text S2).

Characterization of the prepared ORPC
The surface morphology of the calcium peroxide powder and the prepared ORPC in this study were measured by scanning electron microscope. Figure 1(a) shows the surface of the CaO 2 powder has a rough surface and many protrusions. After being embedded with SA, the surface of the ORPC is regular and smooth (Figure 1(b)). When the CaO 2 reacted with water, the CaO 2 was consumed and decomposed, then causing the ORPC slightly to crack (Figures S2(a) and S2(b)). Compared with the infrared spectra of CaO 2 powder and ORPC (Figure 2(a)), the O-O bond appeared in the CaO 2 at 869 cm À1 and the O-O bond appeared at 875 cm À1 in the ORPC, which would contribute to releasing oxygen (Ż eglinśki et al. 2006). After exhaustion, the peak of the O-O bond in the ORPC became markedly attenuated due to oxygen release caused by the reaction between the ORPC and water. Meanwhile, the peak intensities at 1,474 cm À1 and 1,423 cm À1 in the ORPC decreased, reflecting the reduction in the amount of O-Ca-O (Yan et al. 2009). The characteristic peak at 2,850 cm À1 in the ORPC was a long carbon chain structure that was derived from the SA, indicating the surface of CaO 2 was covered by organic layers. XRD patterns of CaO 2 powder and ORPC are provided in Figure 2(b). Typical peaks corresponding to CaO 2 and ORPC were at 2θ values of 30.09°, 35.44°, and 47.15°(JCPDS No. 03-0865), which also demonstrated CaO 2 was successfully embedded.

Effect of CaO 2 content on ORPC performance
The content of various compositions is an important factor that can significantly affect ORPC performance. The content of CaO 2 was investigated for masses of 1.5 g bentonite, 14 g cement, 10 g fine sand, 0.6 g CA and 2.33 g SA in the ORPC (a bentonite/cement/fine sand/CA/SA mass ratio of 1.5:14:10:0.6:2.33). The mass of CaO 2 was changed from 2.5 g to 4.3 g, 6.2 and 9 g, respectively. The effect of ORPC with various contents of CaO 2 on DO in the glass reactor was monitored within 28 days in which the reactor was shaken regularly (T ¼ 25°C). The result showed that the DO concentration increased with the CaO 2 content (Figure 3(a)). During the first 15 days, ORPC with various contents of CaO 2 slowly increased the concentration of DO in the water. When the content of CaO 2 in the ORPC increased, the oxygen released from the ORPC in the water increased. After the 15th day, the DO in the water began to decrease for the reactors with 2.5 g and 4.3 g CaO 2 in ORPC. However, ORPC with 6.2 and 9 g CaO 2 still increased DO in the water, suggesting that a high content of CaO 2 could increase the concentration of DO in the water much longer. Figure 3(b) shows that various contents of CaO 2 coming from the ORPC could also continuously reduce phosphorus concentration in the water. As the content of CaO 2 increased, the phosphorus removal increased. When the content of CaO 2 in the ORPC was 2.5 g, 4.3 g, 6.2 g, and 9 g individually, the final phosphorus removal reached 78.6%, 82.0%, 84.8%, and 87.2% within 28 days. The phosphorus removal increased with CaO 2 content in the batch reactor, and the alkalinity in the water also increased with CaO 2 content (Figure 3(c)). The pH of the effluent was increased from 7.94 to 8.2 and 8.41 with the flow rate decreasing from 240 mL h À1 to 120 mL h À1 and 30 mL h À1 at the initial phosphorus concentration of 1.22 mg L À1 , respectively, which were only minor changes compared with the influent pH of 7.62. The same elevation of pH value was also observed at the initial phosphorus concentrations of 0.76 mg L À1 and 2.07 mg L À1 . Compared with the influent, the effluent pH in the flowing pattern did not change significantly (see section 3.3, Figure 5(c)). The removal of phosphorus could satisfy the requirement to meet the practical demands by varying the content of CaO 2 .

Effect of SA content on ORPC performance
In this section, the performance of ORPC with various SA contents was tested. The content of SA was investigated for the fixed masses of 1.5 g bentonite, 14 g cement, 10 g fine sand, 0.6 g CA and 6.2 g CaO 2 in the ORPC (a bentonite/cement/ fine sand/CA/CaO 2 mass ratio of 1.5:14:10:0.6:6.2), while the mass of SA was changed from 0.53 g to 1.06 g, 2.13 g and 3.20 g. Figure 4(a) shows the effect of SA content on the oxygen-releasing performance of ORPC. As the content of SA increased, the oxygen-releasing rate decreased in the first 15 days. Because the cement and fine sand on the surface of the ORPC fell off slowly, the oxygen-releasing rate of ORPC which had a high content of SA was increased after 15 days. Figure 4(b) shows the effect of various contents of SA on the phosphorus removal performance of ORPC. When the content Water Supply Vol 00 No 0, 5 corrected Proof of SA in the ORPC was 0.53 g, 1.06 g, 2.13 g, and 3.20 g, respectively, the final phosphorus removal was 82.2%, 79.1%, 74.9%, and 73.3% within 28 days. As the content of SA decreased, the greater was the removal of phosphorus achieved, which clarified that the increase of SA content reduced the rate of ORPC oxygen release (Northup & Cassidy 2008).

Effect of temperature on ORPC performance
In this section, the influence of various temperatures on ORPC (a bentonite/cement/fine sand/CA/SA/CaO 2 mass ratio of 1.5:14:10:0.6:1.06:6.2) performance was tested. The batch experiment was carried out in a 1 L glass reactor. The different temperatures were fixed from 15°C to 35°C through the regulating thermostat of the solution. Nitrogen was used to blow off the oxygen of the phosphorus-containing water to 0 mg L À1 before the beginning of the test, so that the influence of different temperatures on the ORPC could be compared clearly. As demonstrated in Figure S3(a), with the increasing of temperature from 15°C to 25°C and 35°C at the initial phosphorus concentration of the 1.91 mg L À1 , the phosphorus concentration of the water was slightly decreased from 0.38 mg L À1 to 0.34 mg L À1 and 0.29 mg L À1 , respectively. This could be explained by the activity product of Ca 2þ and PO 4 3À becoming larger which promoted the precipitation reaction of calcium phosphate with the increasing of temperature, thus slightly improving phosphorus removal (Song et al. 2002). The change of DO was inconspicuous with the temperature increase ( Figure S3(b)). Wang & Wang (2006) also found that the behavior of CaO 2 for phosphorus removal in river water was only slightly affected by the climatic conditions.

ORPC purification test for the actual river water
A river simulation test was conducted to evaluate the feasibility of ORPC (the bentonite/cement/fine sand/CA/SA/CaO 2 mass ratio of 1.5:14:10:0.6:1.06:6.2) when putting 500 g ORPC evenly at the bottom of the reactor at the loading of Water Supply Vol 00 No 0, 6 corrected Proof 3,200 g m À2 to remove phosphorus from the actual river water and to assess the effect on oxygen-release performance. Potassium dihydrogen phosphate was added to the actual river water to prepare phosphorus-containing river water with concentrations of 0.76 mg L À1 , 1.22 mg L À1 , and 2.07 mg L À1 , respectively. As illustrated in Figure 5(a), the effluent corrected Proof concentration of phosphorus was 0.19 mg L À1 , 0.32 mg L À1 and 0.57 mg L À1 , respectively, after flowing through the reactor at a flow rate of 30 mL h À1 , and in accordance with the phosphorus removal efficiency of 75.0%, 73.8%, and 72.5%, respectively (Table 1). It can be seen that the ORPC displayed a great effect on phosphorus removal in the actual river water. In addition, after flowing through the reactor at the above three different phosphorus concentrations of the actual river water with an initial DO concentration of 5.3 mg L À1 , the concentration of DO in the effluent was raised to 7.0 mg L À1 , 8.3 mg L À1 , and 8.5 mg L À1 , respectively ( Figure 5(b)). Moreover, it is well known that high pH will inhibit the activities of aquatic organisms . As shown in Table 2, when ORPC was applied, the pH of the above three different phosphorus concentrations of actual river water were increased from 8.03, 7.62, and 7.57 to 9.31, 8.41, and 8.69, respectively, which was similar to the pH change observed by Zhang et al. (2012). During the oxygen-releasing process, the change of the raised pH was caused by the formation of Ca(OH) 2 via the reaction between CaO 2 and water. Compared with CaO 2 powder in Figure S4, OH À was generated by ORPC more slowly due to the slower reactive rate of ORPC, resulting in the slow increase in pH. This was similar to the results obtained by Noyma et al. (2016) and Zhou et al. (2020). The above results suggested that ORPC has a great ability to remove phosphorus in actual river water and significantly increase the concentration of DO under complex river conditions. The flow rate of the actual river water was another important factor that could significantly affect the performance of the ORPC. Therefore, the effect of various flow rates on phosphorus removal in river water was investigated. The results showed that the removal of phosphorus increased with the decrease in flow rate (Figure 5(a)). The phosphorus removal efficiency of corrected Proof river water decreased from 75.0% to 40.0% and 14.5% with the flow rate increase from 30 mL h À1 to 120 mL h À1 and 240 mL h À1 at the initial phosphorus concentration of 0.76 mg L À1 , respectively. The same trend was found at the initial phosphorus concentrations of 1.22 mg L À1 and 2.07 mg L À1 (Table 2). These results could be explained by the following reasons. The hydraulic retention time decreased with the increase of flow rate and then the contact time of the ORPC with the river water was reduced, thus causing the decrease of phosphorus reaction with ORPC and resulting in less removal of phosphorus. In addition, the DO of river water in the effluent was determined and the results are shown in Figure 5(b). The DO of river water was increased from 5.9 mg L À1 to 6.3 mg L À1 and 7.0 mg L À1 with the flow rate decrease from 240 mL h À1 to 120 mL h À1 and 30 mL h À1 at the initial phosphorus concentration of 0.76 mg L À1 , respectively, and all DO values increased when compared with the initial influent DO of 5.3 mg L À1 . The same elevation of DO level was also observed at the initial phosphorus concentrations of 1.22 mg L À1 and 2.07 mg L À1 , confirming that the flow rate of the actual river performed an important role for ORPC on effluent phosphorus concentration and effluent DO level with an inverse correlation. Therefore, the phosphorus removal and DO level in river water could be adjusted to meet practical demands by varying the flow rate of the actual river water.

ORPC impact on DO level and the total soluble phosphorus in overlying water
The river simulation experiment was conducted to evaluate the feasibility of using ORPC (a bentonite/cement/fine sand/CA/ SA/CaO 2 mass ratio of 1.5:14:10:0.6:1.06:6.2) when putting 210 g ORPC evenly at the bottom of the reactor under a loading of 4,000 g m À2 to remove phosphorus in the actual river water. In this test, the sediment collected from the actual river was added to a height of 5-6 cm in the reactor to simulate a river and the actual river water flowed through the reactor with a flow rate of 180 mL h À1 . As shown in Figure 6(a), the initial DO was 4.7 mg L À1 without ORPC in the blank control. After flowing through the reactor, the DO concentration in the effluent was less than 1 mg L À1 for the whole 28 days, confirming that it was basically in an anoxic condition (Sugiura et al. 2004). When ORPC was added as an oxygen source, the DO concentration in the effluent was maintained from 2.0 to 3.5 mg L À1 with less change of DO level in the tested condition. It was noted that ORPC could release oxygen for a longer period of time with a slow rate in the water. Even after 28 days, the DO in the effluent was still kept around 3 mg L À1 , indicating that the ORPC was beneficial to providing an oxic environment and therefore would inhibit the endogenous release of phosphorus in sediment, as discussed later ( Jiang et al. 2008).
The removal of phosphorus by using ORPC in the above tested condition was also monitored. As shown in Figure 6(b), around 0.05 mg L À1 phosphorus in the blank was the increase in the effluent compared with the influent, whereas the concentration of phosphorus decreased by 0.07-0.29 mg L À1 in the presence of ORPC, indicating that ORPC had the ability to The flow rate of the river was 30 mL h À1 . corrected Proof solidate phosphorus from water and sediment. The solution pH was also evaluated and the result is provided in Figure 6(c). The pH in the blank was steadily kept between 7 and 8, while the effluent pH was only increased to 8-9 after adding ORPC in 28 days, although the ORPC could generate Ca(OH) 2 during oxygen release (Equation (1)). The slight and reasonable corrected Proof elevation of effluent pH might be due to the sustained and slow release of oxygen by the ORPC that was suitable for the survival and aerobic respiration of microorganisms in the sediment, in which the microorganisms could consume organic matter to produce CO 2 that decreased the pH of the water (Zhou et al. 2017). In addition, SA and CA were also beneficial to inhibiting an excessive rise of pH due to their buffering capacity. Therefore, ORPC was suitable to be applied in removing phosphorus and, at the same time, releasing oxygen with little effect on the pH elevation in the actual river water.

ORPC effect on the species of inorganic phosphorus in sediment
The changes of various species of inorganic phosphorus in the sediment were compared between blank and ORPC groups and the results are shown in Figure 7. In Figure 7(a), only a little difference of Al-P mass concentration was found in the blank group within 28 days, indicating the low conversion efficiency of Al-P to other species of phosphorus. However, the Al-P mass concentration in the sediment was significantly increased from 0.196 mg g À1 to 0.372 mg g À1 with the addition of ORPC (Figure 7(b)). Further, the mass concentration of Al-P in the ORPC which was on the top of the sediment for 28 days evidently increased to 1.040 mg g À1 (Figure 8) due to the adsorption of ORPC to the phosphorus in the water phase which later converted it into Al-P. The reasons for the above results were as follows: (a) Other species of phosphorus such as Cl-P and Fe-P in the sediment could be transformed into Al-P. In the mobile phosphorus fractions, Cl-P and Fe-P were the dominant fractions. Cl-P and the soluble phosphorus were easily desorbed and competitively adsorbed by other ions such as Fe and Al ions (Lin et al. 2017;Song et al. 2020). However, Al(OH) 3 was formed due to the reaction of Al wrapped corrected Proof in ORPC with water, and the settled Al oxyhydroxide flocs adsorbed phosphorus which was displaced from iron-carriers due to the preferential adsorption of phosphorus by Al rather than by Fe ). (b) The total soluble phosphorus in the overlying water was able to be transformed into Al-P in the sediment. (c) Al(OH) 3 was not converted into meta-aluminate acid but could form colloids to further adsorb PO 4 3À in the water . Therefore, the content of Al-P in the sediment kept rising due to the effect of the ORPC. The mass concentration of Ca-P in the blank was maintained around 1.7 mg g À1 , demonstrating the low conversion of Ca-P to other species of phosphorus. After adding ORPC, the mass concentration of Ca-P in the sediment increased tardily and finally rose to 2.74 mg g À1 (Figure 7(b)). At the same time, the mass concentration of Ca-P in the ORPC apparently increased to 1.0 mg g À1 . These results were because the Ca(OH) 2 as formed by Equation (1) could adsorb PO 4 3À in the overlying water, then formed stable Ca-P such as hydroxyapatite (Madsen et al. 1995). With the increase of Ca 2þ concentration, other species of phosphorus such as iron phosphorus also could be converted to Ca-P (Hanh et al. 2005). It further showed that ORPC had achieved the ability of long-term phosphorus removal and the effect of sustained release after CaO 2 was embedded by SA. In Figure 7(a), the mass concentration of Fe-P in the blank slightly decreased from 0.14 mg g À1 to 0.065 mg g À1 , whereas after the addition of ORPC, the mass concentration of Fe-P in the sediment finally rose to 0.159 mg g À1 (Figure 7(b)). The mass concentration of Fe-P in the ORPC slightly increased to 0.0036 mg g À1 . The reasons for the above results were as follows. On the one hand, Fe 2þ in the sediment was transformed to Fe 3þ owing to the slow release of oxygen by the OPRC, which could combine with PO 4 3À to form insoluble Fe-P (Zhou et al. 2012). On the other hand, CaO 2 formed an alkaline environment to produce Fe(OH) 3 colloids. It adsorbed soluble total phosphorus and increased the Fe-P in the sediment.

CONCLUSIONS
In this study, an ORPC product was prepared with CaO 2 , bentonite, cement, SA, CA, and fine sand, and the prepared ORPC was proved to have the ability to control phosphorus and to release oxygen. The phosphorus removal by ORPC grew with the increase of CaO 2 content, while the removal of phosphorus decreased with increasing SA content during ORPC preparation. The effluent phosphorus concentration of the actual river water with initial phosphorus concentrations of 0.76, 1.22, and 2.07 mg L À1 could be reduced after flowing through the reactor with the presence of ORPC. Further, the hydraulic retention time was decreased with the increase of flow rate and then the contact time of the ORPC with the river water was reduced, thus causing the decrease of phosphorus reaction with ORPC and resulting in less removal of phosphorus. The total soluble phosphorus in the overlying water was adsorbed on the ORPC and later converted to Al-P, Ca-P, and Fe-P in the sediment, thus achieving the purpose of adsorbing phosphorus in the water body and preventing the release of phosphorus from sediment. In conclusion, ORPC can maintain DO at a reasonable level and control phosphorus in the water body, therefore displaying the potential for its application in the removal of phosphorus from the actual river and inhibiting phosphorus release from sediment while maintaining DO in the water body.