Synthesis of Zeolite X from Locally Sourced Kaolin Clay from Kono-Boue and Chokocho, Rivers State, Nigeria

This work describes the development of a process to produce zeolite X from mined kaolin clay from Kono-Boue and Chokocho, Rivers State, Nigeria. The procedures involved the beneficiation of the raw kaolin and calcinations at 850°C, to transform the kaolin to a more reactive metakaolin. Afterwards, the extremely reactive metakaolin was purge with sulphuric acid to obtain the much needed silica-alumina ratio for zeolite X synthesis. An alkaline fusion stage was then carried out to transform the metakaolin into zeolite by mixing with aqueous NaOH to form gel then allowed to stay for a duration of seven days at room temperature. The samples were then charged into a propylene container and placed in an oven at a temperature of 100°C for the reaction to take place for 6 h. Identification of the crystalline phases by X-ray Diffraction (XRD), chemical/elemental compositions by X-ray Fluorescence (XRF)/Energy Dispersive Spectroscopic analyses (EDS), surface morphology by Scanning Electron Microscopy (SEM) and molecular vibration of units by Fourier Transform Infrared Spectrophotometry (FT-IR) were done. The results showed that the zeolite synthesized from Chokocho kaolin (CK) was more crystalline/larger with sharper peaks on both XRD and FTIR than that from Kono-Boue. This was also supported by slightly rougher surface morphology of CK over KK on SEM. XRF Si:Al ratios of 10.73 and 14.36 were obtained for KK and CK respectively. EDS results supported the XRF ratios. Sharper zeolitic characteristic O-H stretching bands at 3488 and 3755 cm-1 were recorded for CK than KK. However, both results showed that zeolite X have been produced from both Kono-Boue and Chokocho kaolin clays respectively.


Introduction
The study focused on the synthesis of zeolite X from locally sourced clay from Kono-Boue and Chokocho, Rivers State, Nigeria. Nigeria is abundantly blessed with natural reserves of crude oil with three modern petroleum refineries. Two of them possess profit-boosting units called the Fluid Catalytic Cracking (FCC) units responsible for cracking of heavy refining fractions known as the heavy oil into gasoline and other light and economically viable fuels. Like any other modern refinery, the cracking processes in the FCC units rely completely on availability of this indispensable zeolite catalyst which is continuously imported into Nigeria in millions of tonnes; a scenario which leads to huge capital flight [1].
Zeolites belongs to a well-defined class of naturally occurring and synthetically produced, crystalline aluminosilicate minerals which possesses three-dimensional structures arising from oxygen linked framework of [SiO 4 ] 4− and [AlO 4 ] 5− polyhedra. They have the ability of being facile and can also undergo reversible cation exchange. The collections of tetrahedral shape possessed by zeolites initiate a porous matrix with regular arrays of openings having well-defined dimensions so as to be able to selectively admit some molecules into their interiors, whilst rejecting others on the basis of molecular dimensions, giving them the important characteristics of "molecular sieving." The ion exchange and molecular sieving properties of zeolites have given room to the successful commercialization of zeolites for industrial scale ammonia treatment and in detergent formulations as calcium sequesterants which makes zeolites a potential catalyst for the removal of strong and heavy metals from acid, mine drainage and industrial wastewaters [2].
Catalysts (zeolites) are essentials for production technology especially in this country (Nigeria). It finds a number of applications in numerous industrial processes such as adsorbents for water purification, catalyst in the petroleum refining industry for the fluid cracking of heavy petroleum fractions, advanced materials preparation, etc. Therefore, the idea of producing synthetic zeolite to continuously replace its limited imported analog cannot be overemphasized.
Nigeria though being blessed with abundant kaolin clay and solid mineral deposits scattered in various parts of the country, yet the country still depends on imported zeolites as commercial adsorbent for waste water treatment, catalyst for petroleum industry and other applications [3].
Against this backdrop, it becomes imperative to consider a cheaper way of producing zeolite using available natural resources such as clay from Rivers State, Nigeria in support of what previous researchers have done. Initial studies on the synthesis of zeolite from locally deposited clay have been reported by [4]- [11]. Zeolites are generally synthesized from low priced silica-alumina sources in alkaline phase under hydrothermal conditions [12]. The cheap silica-alumina sources include kaolinite. Zeolites are normally synthesized from kaolinite by a process known as the "hydrogel process" and its formation could be investigated by the presence of a single characteristic broad band associated with O-H stretching vibrations of the catalytic centers (Si-OH-Al sites) located in the region between 3700 -3500 cm −1 [13]. It is therefore very pertinent for researchers, engineers, to Although, Konne, et al. [9] investigated the characterization of Kono-Boue clay sourced from Ogoni land in Rivers state using Energy Dispersive X-ray (EDX), there is no report on the synthesis of zeolites from the Kono-Boue and Chokocho clay yet. Therefore, this work applied locally sourced clay from these two selected towns in Rivers State, Nigeria to the synthesize zeolites which can possibly be used in FCC units, water treatment, etc.
The project will provide a veritable national hub for the synthesis of zeolitic materials and their applications in the oil and gas industry as well as allied industries in Nigeria. The work will help in capacity building in terms of highly trained and skilled personnel and provision of cutting-edge equipment in Rivers State and Nigeria at large.

Sample Collection and Treatment
Clay samples selected for this work were taken from Kono-Boue town situated  [14]. The clay was transformed to a more reactive form by subjecting it to heating at 850˚C for 6 h using a furnace before using it as a reactant. This was because the Si-O or Al-O tetrahedral and octahedral structures possessed by kaolin are inactive to modification or activation which can hinder the direct synthesis of zeolites. Therefore kaolin must be subjected to thermal transformation to change the inert phase into the active phase at elevated temperature with the addition of an alkali hydroxide. Metakaolin is a reactive phase which characterized the fusion process with the addition of sodium hydroxide to form active Al and Si species which have the tendency of forming ring-like structures that are basic unit for zeolite formation.

Zeolitization
The dealumination of 30 g metakaolin with sulphuric acid leached out the structural alumina to meet the silica-alumina mole ratio required for the targeted zeolite. This is because each AlO 4 tetrahedron in zeolite framework bears a net negative charge which is balanced by a cation. The structural formula of zeolite is based on the crystallographic unit cell, represented as Advances in Chemical Engineering and Science where M is an alkali or alkaline earth cation, n is the valence of the cation, w is the number of water molecules per unit cell, x and y are the total number of tetrahedra per unit cell, and the ratio y/x usually has values of 1 to 5 while high silica zeolites', y/x can range from 10 to 100 [15].
A gel from the dealuminated metakaolin and a solution of sodium hydroxide was prepared based on the procedure required for the synthesis of faujasite after which the gel formed was left to age for 7 days at room temperature in a propylene container. The gel sample was heated in a microwave oven set at 100˚C for 6 h.
After the synthesis, the samples were filtered, dried, labelled and characterized.

Sample Analysis (XRD. XRF, SEM, EDS and FT-IR)
X-ray diffraction was used to identify the crystalline phase of the samples while

XRD Analysis
The X-ray diffraction patterns of the crystallized zeolites are shown in Figure   1(a) and Figure 1(b) for zeolites X from the Kono-Boue and Chokocho kaolin, respectively. The reflection patterns showed sharp peaks indicating that both samples were crystalline at this stage. The patterns matched with both synthetic and commercial NaX-zeolite. XRD patterns reported in literature except for weaker intensity of the peak at 2-theta = 6.28˚ [12]. It was also similar to the untreated calcined kaolin reported by Konne, et al. [9] indexed to the Joint Committee on Powder Diffraction Standards (JCPDS) file number: 003-0447. The major difference was the higher crystallinity observed for KK and CK zeolites in this report. The sharper peaks and lower broad background on the XRD pattern of CK indicated that it was more crystalline/of larger particle sizes than KK.

X-Ray Fluorescence (XRF)
The

SEM and EDS
The surface morphologies of the synthesized zeolites of both Kono-Boue and Chokocho showed microporous polycrystallites with rough surfaces of largely smaller particles mixed with scattered larger aggregates Figure 3. The larger aggregated polycrystallites were more on the Chokocho micrograph than Kono-Boue confirming the observed differences in crystallinity shown on the XRD. The EDS showed Si:Al ratios from atomic concentrations as 1.36 (besides Figure 3(a)) and 1.51 (besides Figure 3(b)) for KK and CK respectively. The EDS results supported the empirical ratios obtained from the XRF technique. Similarly, the atomic concentrations of Na were 36.83 and 36.18 for KK and CK respectively which indicated that the Na + ions required to balance the net negative charge of Al tetrahedron varied with Al concentration in the synthesized NaX-zeolites [15].
Both zeolite samples contained low/trace concentrations of other elements associated with mineralogical impurities found in zeolite X which is critical for the nucleation, growth or crystallization of the zeolitic phase [16]. The levels of Fe, Ag, K, Mg and P in CK were higher than KK while Ti, S and Ca in KK were higher than those of CK. In addition, only KK had trace concentration of Zr. The absence of some toxic heavy metals such as Pb, Cd, Cr, etc. from both samples implied that the resultant zeolites were safer than some earlier reports in literature [17].

FT-IR
The results of the FT-IR of the two zeolitic products are shown in This region is followed by a broad band (992 cm −1 ) assigned to asymmetric stretching vibrations of internal bonds of a tetrahedra [16] [18]. The characteristic bending vibration of a four membered ring (tetrahedra) has been associated with the lowest band at 466 cm −1 in zeolites [17]. The presence of absorbed CO 2 and water molecules in the zeolite channels has been associated with bands at 1407 -1482 cm −1 and 1660 -1671 cm −1 respectively. This region was followed by a large broad band with weak peaks at 2380 cm −1 that could not be assigned to any known vibration in the available literature while bands at 2936 cm −1 could be due to H 2 O

Conclusion
Zeolite was successfully synthesized from clay sourced from Kono-Boue and Chokocho, Rivers state, Nigeria after alkaline treatment of its metakaolin. This work demonstrated the development of hydrothermal process to produce an important industrial catalyst (zeolite) from locally sourced catalyst. The X-ray diffraction analysis confirmed the presence of zeolitic mineral phases in both KK and CK crystallized samples respectively. However, the CK sample was more crystalline as shown by sharper intense XRD peaks, rougher surface on the SEM micrograph and sharper bands on the FT-IR. Both samples had similar bands especially the characteristic zeolitic O-H stretching at 3488 cm −1 . The XRF showed the presence of higher silica to alumina ratios of 10.73 and 14.36 after treatments while the EDS showed the absence of some toxic metals implying that the synthesized zeolites were safe and environmentally friendly. The zeolites formed have shown that the hydrothermal modification of reactive kaolin into zeolite X depended solely on the ageing time, reaction temperature, metakaolinization temperature and NaOH concentration.