Introduction

Pickling sludge is a product of the stainless steel pickling waste liquor disposed by the lime neutralization precipitation process. Due to the high concentration of Cr and Ni, pickling sludge was listed in the national hazardous waste list (HW17, China). The conventional sludge disposal methods such as landfill and incineration may pollute the environment; thus, many new physicochemical and biological treatments (Merrylin et al. 2013; Uan et al. 2013; Kavitha et al. 2014a, 2014b; Uma Rani et al. 2014) are proposed to reduce the sludge production. However, there are few studies on how to recycle the pickling sludge which has rich calcium and iron resources. Hence, an advanced and environmentally friendly way of recycling pickling sludge is required. Gypsum (CaSO4·2H2O) containing heavy metals is a solid waste from the lead and zinc production processes of the metallurgical industry. In the Zhuzhou city of China, the heavy metal gypsum is usually piled up in the cropland. However, metals, including lead, arsenic, zinc, cadmium, mercury, chromium and nickel can cause significant damage to the environment (Bååth 1989; Leyval et al. 1997; Nagajyoti et al. 2010; Wu et al. 2010; Tangahu et al. 2011) as a result of their mobility and solubility (Mulligan et al. 2001). These toxic elements in contaminated cropland can end up in the plants and transferred to the food chain, eventually accumulating into the human body, endangering human health, since these elements have been well established as toxic for living systems (Peralta-Videa et al. 2009). Therefore, effective and safe reuse of the heavy metal gypsum and pickling sludge, especially stabilizing and storing heavy metals, is a matter of serious concern and needs to be addressed.

Glass–ceramics are polycrystalline materials with fine microstructure produced by controlled crystallization (devitrification) of glass (Rawlings et al. 2006). Glass–ceramics has fine-grained structure, good mechanical properties and randomly oriented crystals with some residual glass without voids (Sun et al. 2001). Therefore, glass–ceramics is regarded as a new type of building material and can be used for storage of hazardous waste.

The main components of the pickling sludge are calcium fluoride and ferric oxide, which are considered to be good nucleating agents in the production of glass–ceramics (Cheng et al. 2006). Heavy metal gypsum is a good source for CaO. Therefore, pickling sludge and heavy metal gypsum can be used as raw material for Fe2O3, CaF2 and CaO sources, respectively, in the production of glass–ceramics. In this way, toxic elements in pickling sludge and waste gypsum can be stabilized and solidified in glass–ceramics.

However, if the heavy metal gypsum is directly used for the preparation of glass–ceramics, sulfur dioxide gas formed in gypsum desulfurization process is easily volatized at high melting temperature, which can corrode equipment and pollute the environment. If melting temperature is lower, sulfur dioxide gas may remain in the glass liquid and form micropores in the parent glass, which has a negative effect on the mechanical properties of glass–ceramics. To avoid this problem, the waste gypsum should be desulfurized first.

There are several gypsum decomposition methods. The most common methods are using reduction (Van der Merwe et al. 1999; Ma et al. 2010) and/or reducing atmosphere (Diaz-Bossio et al. 1985; Kuusik et al. 1985) to decompose gypsum. However, these methods have high requirements for the reaction atmosphere and easily form sulfur by-products. In order to reduce the requirement of experimental conditions, heavy metal gypsum desulfurization by excessive amounts of glass powder in air is proposed in this work. The intermediate products calcium silicate and silicon dioxide can be directly used in the subsequent preparation of glass–ceramics. Currently, there have been few studies in this field.

The objective of this study was to propose a preparation method of glass–ceramics derived from heavy metal gypsum and pickling sludge, as well as stabilization of Pb, Zn, Cd, As, Hg, Cr and Ni heavy metals. The research was carried out from May 2014 to July 2014 in the Institute of Advanced Materials and Technology, University of Science and Technology, Beijing, China.

Materials and methods

Raw materials

Pickling sludge was provided by the Shanghai Baosteel Group Corporation (Shanghai, China). Heavy metal gypsum was collected from the Zhuzhou city in the Hunan province of China. Waste cullet was collected from the Beijing city in China. The collected solid wastes were ground into powder in a ball mill and sieved to less than 1 mm. Then, the gypsum powder was dried at 573 K for 60 min.

Chemical composition of the heavy metal gypsum, pickling sludge and waste cullet was characterized by X-ray florescence (XRF, Axios, PANaytical,The Netherlands). Leachability of the wastes was evaluated by the Environmental Protection Agency toxicity characteristic leaching procedure (TCLP, EPA method 1311) (USEPA 1990), using acetic acid (2.88 pH) as the leaching agent at a liquid to solid ratio of 20:1. The filtrates were filtered with 0.45-μm membranes for 18 h, then acidified to the pH of 2 with 1 N HNO3 and analyzed for Pb, Zn, Cd, As, Hg, Cr and Ni by the inductively coupled plasma (ICP, iCAP 6300, Thermo Fisher Scientific, US) method.

Heavy metal gypsum desulfurization process

Heavy metal gypsum and glass powder were mixed up at the silicon to calcium ratio of 0.8, 1.5, 2.0 and 2.5, respectively. The four groups of samples were heated in air at 1,173 K, with a heating rate of 10 K/min and kept at 1,173 K for 2 h. In addition, the samples with silicon to calcium ratio of 2.5 were heated at 1,173, 1,273, 1,373 and 1,473 K for 2 h, respectively.

The samples and products were completely dissolved in the mixture of nitric, hydrochloric, hydrofluoric and perchloric acids, and then, the concentration of sulfur in mixtures and products was determined by the ICP.

The desulfurization rate (ζ) of the heavy metal gypsum can be calculated as:

$$ \zeta = \frac{{m_{0} c_{0} - m_{1} c_{1} }}{{m_{0} c_{0} }} \times 100\% $$
(1),)

where m 0 is the raw mix mass in g, m 1 is the product mass in g; c 0 and c 1 is the mass percent of sulfur in the raw mix and in the product, respectively.

Preparation and properties of glass–ceramics

The intermediate product obtained from the sample with silicon to calcium ratio of 2.5 and heated at 1,473 K was used as raw material for the preparation of glass–ceramics. The intermediate product (64.96 wt%), pickling sludge (16.45 wt%), CaO (7.41 wt%) and MgO (11.18 wt%) were blended and melted in corundum crucible in a muffle furnace at 1,733 K with a heating rate of 7 K/min. After 2.5 h, the melted glass liquid was rapidly poured on an iron plate preheated to 873 K in advance, then kept at 873 K for 30 min to remove internal stresses. Parent glass was obtained after cooling to room temperature.

The parent glass was sintered in air at nucleation temperature of 973 K for 2 h with a heating rate of 10 K/min and crystallization temperature of 1,173 K for 1 h with a heating rate of 5 K/min, then the glass–ceramics was obtained.

The obtained glass–ceramics was characterized by a series of tests. The main crystalline phase was identified by X-ray diffraction (XRD, Ultima IV, Cu-Kα, Rigaku, Japan). The microstructure of the fracture surface of the sample etched with HF 0.1 N for 30 s was observed by scanning electron microscopy (SEM, Quanta 250, FEI, USA) and gold covered before microscopic observations. The microhardness was measured five times by the microhardness tester (MH-6, China) with a load of 300 g and a loading time of 10 s. The obtained glass–ceramics was cut into five samples of the same dimension of 3 × 4 × 40 mm3, used for the bending strength test. The bending strength of each sample was determined by the three-point bending strength tester (CDW-5, China). Water absorption was measured after 3-h immersion in boiling distilled water, according to the Chinese National Standard GB/T 3299-2011 (2012). The leaching behavior of heavy metals in the glass–ceramics was determined following the EPA TCLP.

The water absorption (W) of the heavy metal gypsum can be calculated as:

$$ W = \frac{{m_{3} - m_{2} }}{{m_{2} }} \times 100\% $$
(2),)

where m 2 is the glass–ceramics mass without immersion in g and m 3 is the glass–ceramics mass after immersing in boiling water for 3 h in g.

Results and discussion

Characterization of pickling sludge and heavy metal gypsum

Chemical composition of the heavy metal gypsum, pickling sludge and waste cullet is listed in Table 1. The main gypsum components are CaO, SO3 (42.02 and 37.01 wt%, respectively, mainly as CaSO4), SiO2 (3.08 wt%), Fe2O3 (6.11 wt%), along with small amounts of heavy metal oxides (about 3.51 wt%). The pickling sludge main chemical components are Fe2O3 (23.19 wt%), CaO and F (31.95 and 18.72 wt%, respectively, mainly as CaF2). Moreover, the concentration of Cr2O3 and NiO in pickling sludge is 4.55 and 1.67 wt%, respectively. The cullet main chemical components are SiO2 (68.30 wt%) and Na2O (14.37 wt%).

Table 1 Chemical composition of the heavy metal gypsum, the pickling sludge and waste cullet (wt%)

TCLP leachate analysis data are given in Table 2. The leaching of Cd (35.145 ppm) in the gypsum is much higher than the 1 ppm threshold, prescribed in the EPA method 1311. High Zn concentration of 263.433 ppm was observed in the leachate. In addition, high concentration of Cr (159.8 ppm) and Ni (192.2 ppm) was also observed in the leachate of the pickling sludge.

Table 2 Concentration of toxic elements in the leachate (ppm)

Silicon/calcium ratio (Si/Ca) effect on the desulfurization process

Four groups of samples with different silicon to calcium ratios of 0.8, 1.5, 2.0 and 2.5 were heated at 1,173 K. Figure 1 shows the XRD patterns of the products obtained at different silicon to calcium ratios. Every sample has already started to decompose at 1,173 K. As the content of glass powder increased, the amounts of SiO2 and CaSiO3 in products were also improved. The corresponding desulfurization rates of the four samples were calculated, shown in Fig. 2. The desulfurization rates are slightly improved with the silicon to calcium ratio increase. When the silicon to calcium ratio is 0.8, the sample desulfurization rate is 9.7 %, while desulfurization rate is increased to 14.3 % at the silicon to calcium ratio of 2.5. This is because the reaction between CaSO4 and SiO2 occurred at the contact points of the two kinds of powder particles. With the increase of silicon to calcium ratio, the possibility of a CaSO4 particle surrounded by the glass powder becomes higher (Matsuya and Yamane 1981). Therefore, the contact area between gypsum and glass powder could increase with the content of glass powder.

Fig. 1
figure 1

XRD patterns of the products obtained at different silicon to calcium ratios

Fig. 2
figure 2

Desulfurization rates of samples at different silicon to calcium ratios

If the silicon to calcium ratio further increase, calcium content of the raw materials will reduce accordingly. Therefore, more pure calcium oxide should be added in the subsequent process of the preparation of glass–ceramics, and the material cost will also increase. However, the desulfurization of heavy metal gypsum is not sensitive to silicon to calcium ratio; hence, there is no need to increase the silicon to calcium ratio and material cost further. Silicon to calcium ratio of 2.5 is appropriate and can be used in the subsequent experiment.

Temperature effect on the desulfurization process

Four groups of samples with silicon to calcium ratio of 2.5 were heated at 1,173, 1,273, 1,373 and 1,473 K, respectively. The desulfurization rates of the samples were calculated, shown in Fig. 3. The desulfurization rates are significantly improved with the temperature increase, i.e., 14.3, 25.7, 45.7 and 90.3 % at 1,173, 1,273, 1,373, and 1,473 K, respectively. Higher desulfurization rate of heavy metal gypsum means less sulfur dioxide gas formed in the subsequent preparation of glass–ceramics. Since sulfur dioxide gas may corrode equipment and form micropores in the parent glass, high desulfurization rate is good for the preparation of glass–ceramics. The desulfurization rate at 1,473 K is relatively high (more than 90 %), and there is no need to increase the heating temperature and energy consumption further. Therefore, the decomposition product at 1,473 K can be used to prepare glass–ceramics.

Fig. 3
figure 3

Desulfurization rates of samples at different temperatures

With the temperature increase, the glass viscosity is lower. Moreover, the complex ion (Si x O y )z in glass can be depolymerized to small complex anion group by the fluoride ions in gypsum, which breaks the glass network structure, reduces the viscous flow activation energy and increases the rate of mass transfer in the liquid phase, thus accelerates material diffusion and promotes the reaction (Lu 2010). Therefore, the combination of rising the temperature with the fluoride ion may translate the solid–solid reaction between CaSO4 and SiO2 into the solid–liquid reaction. Thus, diffusion along with the reaction between CaSO4 and SiO2 is accelerated and the desulfurization rate increased, significantly promoting gypsum desulfurization.

Properties of glass–ceramics

The XRD pattern of the obtained glass–ceramics is shown in Fig. 4, where the main crystalline phase is akermanite (Ca2MgSi2O7). The main crystalline phase is determined by the mass ratio of calcium oxide, magnesium oxide and silicon dioxide of raw materials. SEM micrographs of the sample are shown in Fig. 5. The glass phase of the glass–ceramics decreased dramatically. Crystallization is induced by bulk nucleation, since crystallization occurs throughout the entire sample volume (Leroy et al. 2001; Liu et al. 2009), giving rise to the three-dimensional connectivity and quite a large amount of fine-grained (0.2–1 μm) microstructure, which has higher strength and fracture toughness, since the expansion of the micro cracks was hindered by a large number of grain boundaries. The three-dimensional connectivity structure was generated by the spinodal decomposition and the split phase. The microcrystal fluoride was in the nucleation center of glass when using fluoride as the nucleating agent, and the formation temperature of fluoride crystal nucleus was usually lower than crystal growth temperature; therefore, the glass–ceramics with fluoride as nucleating agent has a large number of fine-grained crystals, rather than a small number of coarse grains (Cheng et al. 2006).

Fig. 4
figure 4

XRD pattern of the obtained glass–ceramics

Fig. 5
figure 5

SEM micrograph of the obtained glass–ceramics

Other properties, such as microhardness, bending strength and water absorption of glass–ceramics are listed in Table 3. A high microhardness of 5.3 ± 0.02 GPa and a water absorption lower than 0.13 % were obtained. High bending strength is an important mechanical property of architectural glass–ceramics, and the average three-point bending strength is 206 MPa. These excellent mechanical properties are caused by the three-dimensional connectivity and quite a large amount of fine-grained microstructure.

Table 3 Measured properties of glass–ceramics

TCLP leachate analysis data are given in Table 2. For the glass–ceramics from heavy metal gypsum and pickling sludge, the concentrations of toxic elements in leachate are much less than the thresholds and meet the TCLP standard, especially Cd, Cr and Ni metals, of which the leaching toxicities in raw materials exceeded the standard. Therefore, Pb, Zn, Cd, As, Hg, Cr, Ni heavy metals in pickling sludge and waste gypsum can be successfully stabilized and solidified in glass–ceramics.

Conclusion

A preparation method of glass–ceramics derived from heavy metal gypsum and pickling sludge, as well as stabilization of Pb, Zn, Cd, As, Hg, Cr and Ni heavy metals was proposed in this work. First, heavy metal gypsum was desulfurized by glass powder at 1,473 K and kept 1,473 K for 2 h, with silicon to calcium ratio of 2.5. The desulfurization rate was more than 90 %. Second, the intermediate product from the first step and pickling sludge were used as major raw materials of glass–ceramics, using CaO and MgO as composite additives. The obtained fine-grained glass–ceramics has good mechanical properties. A high microhardness of 5.3 GPa and a bending strength higher than 206 MPa were obtained. Water absorption was lower than 0.13 %. Moreover, Pb, Zn, Cd, As, Hg, Cr and Ni heavy metals in pickling sludge and waste gypsum can be successfully stabilized and solidified in glass–ceramics and meet the TCLP standard.

This combined process on disposing heavy metal gypsum and pickling sludge, as well as making heavy metals harmless and stabilized, is an effective potential method for industrial production.