Thursday, March 19, 2020

The Use of ZSM5 Zeolite From the Coal Fly Ash as a Catalyst for the Reduction of Emission

ABSTRACT

Fly ash is considered as a waste byproduct of thermal power station that was disposed into the landfill or ponds which results in environmental pollution. In this paper, we have attempted to utilize that waste fly ash as a raw material for the synthesis of zeolite like material, which is having a wide variety of applications. Naturally occurred zeolites from volcanic fly ash takes more time for the formation, but in our laboratory, the same type of zeolites can be formed with less period.

The fly ash was collected from the thermal power station and was examined using the characterization techniques X-ray diffraction spectroscopy analysis (XRD), and Scanning electron microscopy(SEM). Then the fly ash was subjected to the acid treatment of Hydrochloric acid (HCL) to remove metal oxides in fly ash, then the process synthesis  of zeolite like material was successfully carried out and its characters resembles like commercial zeolite.

INTRODUCTION

Around 71% of electricity generation in India is supplied from the Thermal power station that uses coal or lignite [1]. These thermal power stations operated by coal produce tons of fly ash, bottom ash and other polycyclic aromatic hydrocarbons while burning [2], In that around 65% to 95% were as fly ash and remaining were bottom ash [3]. It has been found that around 131 tons of fly ash particles have been disposed into the landfill of 65000 acres and this is expected to increase in the future [4-5]. The fine particles of fly ash disposed into the landfill may suspend in the air and form haze or smog like substance that during inhalation causes serious health problems [6]. Recycling of fly ash particle is expensive, but these fly ash particles can be utilized for many applications as a raw material in various fields [7]. It has been found that the fly ash particle finds its successful application in the field of construction works [8-12] we have utilized this fly ash for the synthesis of zeolite like material [13] as it is more active catalyst material. The study clearly shows that the two types of zeolites namely zeolite P and faujasite can be formed from the coal fly ash [14]. Keka Ojha et al, have successfully synthesized the X type zeolite from the coal fly ash and examined its characterization and compared it with the commercial 13X zeolite [15]. Anand Srinivasan et al, have synthesized various types of zeolites using hydroxide solution and they have successfully tested its ability to absorb the SO2 using  the synthesized zeolite [16]. Miki Inada et al, have involved in the research of the effect of the silica addition in the formation of the zeolite Na-PI from coal fly ash by the hydrothermal treatment in the presence of alkaline solution [17]. Various types of zeolites were formed by alkali fusion with fly ash followed by the hydrothermal treatment, In that, the effect of the silicon/aluminum ratio, cation exchange capability, acid treatment, and calcination temperature was analyzed in the research work of Vikranth Volli et al [18]. As this conversion of flyash to zeolite is very much useful  for the solid waste management of the thermal power station, we can reduce the waste landfill disposal[19]. Apart from this, the zeolites can be used for various purposes like removing metals from contaminated water, manufacturing of ceramics and glass, as a catalyst and in the synthesis of geopolymers, etc. [20]. The zeolite X can be even prepared in a rapid time of 20 minutes by ultrasound treatment after the alkali fusion of fly ash [21]. Further, the fly ash particle utilization for the production of zeolite in a large scale manner was carried out to check the possibility of the conversion [22].

II. CHARACTERIZATION OF COLLECTED FLY ASH

The samples of fly ash and bottom ash were collected at different Thermal Power station (TPS) from Neyveli Lignite Corporation India Ltd, namely TPS-I, TPS-I Expansion, and TPS-II, TPS- II  Expansion situated Neyveli. After finding the various characterization of collected fly ash, it is understood that SiO2 content in the TPS-I Expansion fly ash is slightly high compared with other fly ash. Hence TPS -I expansion fly ash is chosen for this project work. Bottom ash is not considered because its generation is very low compared to fly ash generation. Figure 1 shows the XRD pattern of the collected fly ash from the TPS I. The mineralogical characterization of received coal fly ash from the TPS I power station was conducted by the Philips Spectrometer PW1404 is used. Induction source is constituted by an XRD lamp among dual anode (Cr- Au) with the highest power of about 2kW [23].

Fig. 1. XRD pattern of TPS-I flyash.

Scanning Electron Microscopy analysis is carried  out with a JEOL-JSM 6610LV electron microscope. The samples are initially coated through a thin layer deposition of platinum to avoid charges into the samples. Micrographs of the samples  are recorded with a 10-20 kV accelerating voltage. Fig. 2 shows the SEM image of TPS-I flyash.

Fig. 2. SEM images of TPS – I Fly ash.

III. CONVERSION OF FLY ASH TO ZEOLITE LIKE MATERIAL

Fig. 4 and 5 shows the block diagram of the synthesis of zeolite like material from fly ash. Figure 6.a to 6.e shows the photographic view of various types of  equipment used for the synthesis process of zeolite. Flyash sample is subjected to sieving to remove coarse particles by a sieve fpr about 180 microns [24]. The fly ash is then treated with Hydrochloric acid to reduce some undesirable components like CaO, Al₂O₃, SO₃, etc. which are present in the sample. The acid treatment of fly ash particles is carried out by taking concentrated  HCl of 200ml and de-ionized water of 800ml and the fly ash sample of about 50g [25]. The solution is powered in a round bottom flask and heated at 80deg Celsius in a reflux assembly for 8 hours and allowed to cool at room temperature for about 4hours. Then the solution is filtered, added with 200ml of de-ionized water and placed in a magnetic stirrer/hotplate and continuously stirred for 15 minutes. The solution is then filtered and added with 200ml of de-ionized water and stirred for 15 minutes. This process is repeated until the solution reaches the pH of de-ionized water and then dried at 120°C in a Muffle furnace for about 4hrs. The acid Treated Fly Ash (TFA) of about 1.25 g was mixed with fumed silica of 0.75 g in 20 ml of de-ionized water and it was placed in a stirrer for mixing. Then 0.5g of sodium hydroxide and 1.5g of tetrapropylammoniumbromide(TPABr) was added to the mixture while stirring. After aging, the final mixture was kept in the autoclave and heated for 120°C for 12 hours and it was allowed to cool down [26]. The synthesized product was filtered, washed with deionized water and dried in an oven at 70°C and the temperature was increased up to 550°C in  the  ramping  rate  of 15°C/min   to burn off TPABr. After cooling down, the product was washed with deionized water and dried in an oven at 70 °C for about 4 hours, then the zsm-5 like zeolite was obtained.

Table 1: Various Equipment used in the synthesis process.


Fig. 3. Block Diagram of Acid Treatment of fly Ash.


Fig. 4. Block Diagram of Zeolite synthesis process.

IV. CHARACTERIZATION OF SYNTHESIZED ZSM-5 ZEOLITE

The zeolite like material was synthesized from the flyash and it was subjected to the various characterization techniques like XRF, SEM and the same was compared with the commercial zeolite. Figure 7 shows the XRD pattern of the synthesized zeolite like material. This pattern will be helpful to identify the components that are present in the zeolite like substance. Figure 8 shows XRD of the commercial zeolite and this was useful to compare the content of the synthesized zeolite like substance to the commercial one. Figure 7 and 8 shows the SEM image of the synthesized zeolite and the commercial zeolite.

Fig. 5. XRD pattern of Synthesized Zeolite.

Fig. 6. XRD pattern of Commercial Zeolite.

Fig. 7. SEM of synthesized Zeolite.

V. RESULTS AND DISCUSSION

Fig. 8. SEM of Commercial Zeolite.

Table 2 shows the result of XRF analysis of fly ash, synthesized zeolite and commercial zeolite

(i) It is noticed from table 2 shows that there is a marked increase in the percentage of Na2O in the zeolite material compared to fly ash. The weight of Na2O is found to increase from 2.7 to 6.9 this is due to the capture of Na+ ions needed to neutralize the negative charges on the aluminate in the zeolite during the synthesis process.
(ii) It is observed from the table that the percentage of SiO2 in the zeolite material is increased to 40.979 from the fly ash 88.372 this is due to the addition of SiO2 powder during the synthesis process.
(iii) The percentage of other materials (Al2O3, MgO, SO3, CaO, TiO2, Fe2O3) are considerably reduced. This is due to the acid (HCL) treatment of raw fly ash before the synthesis process.

Table 2: Chemical composition of fly-ash,Commercial Zeolite and Synthesized Zeolite samples (weight %).

VI. CONCLUSION AND FUTURE SCOPE

Zsm-5 like material was successfully synthesized from fly ash samples and its characters  were found for selecting the correct ash for synthesis. The zeolite like material was synthesized from the selected fly ash and it was compared with the commercial zsm5-zeolite. From the comparison it has been found only a slight variation is observed between the synthesized and commercial zeolite. This work can have a significant economic and  environmental impact in India if the synthesis process is scaled up as it provides a cheaper way to produce a catalyst that has wide application in various fields, and it promotes the valorization of Indian coal fly ash that considered by many as a waste disposal material. The future scope is that the synthesized zsm-5 like zeolite can be utilized as a catalyst to reduce the harmful exhaust emissions in the Automobiles. As the existing catalyst in catalytic convertor was very costly, the use of zsm5 zeolite as a catalyst for the reduction of emission can be a cost effective method. Thus this work can have an important application in the field of automobile exhaust catalyst used for emission control.

Source: G. Elavarasan, P. Rajakrishnamoorthy, D. Karthikeyan and C.G. Saravanan - Annamalai University (Tamil Nadu), India

The 10 largest coal producers and exporters in Indonesia:

  1. Bumi Resouces (BUMI)
  2. Adaro Energy (ADRO)
  3. Indo Tambangraya Megah (ITMG)
  4. Bukit Asam (PTBA)
  5. Baramulti Sukses Sarana (BSSR)
  6. Harum Energy (HRUM)
  7. Mitrabara Adiperdana (MBAP)
  8. Samindo Resources (MYOH)
  9. United Tractors (UNTR)
  10. Berau Coal