<?xml version="1.0" encoding="UTF-8"?><!DOCTYPE article  PUBLIC "-//NLM//DTD Journal Publishing DTD v3.0 20080202//EN" "http://dtd.nlm.nih.gov/publishing/3.0/journalpublishing3.dtd"><article xmlns:mml="http://www.w3.org/1998/Math/MathML" xmlns:xlink="http://www.w3.org/1999/xlink" dtd-version="3.0" xml:lang="en" article-type="research article"><front><journal-meta><journal-id journal-id-type="publisher-id">IJNM</journal-id><journal-title-group><journal-title>International Journal of Nonferrous Metallurgy</journal-title></journal-title-group><issn pub-type="epub">2168-2054</issn><publisher><publisher-name>Scientific Research Publishing</publisher-name></publisher></journal-meta><article-meta><article-id pub-id-type="doi">10.4236/ijnm.2019.84004</article-id><article-id pub-id-type="publisher-id">IJNM-96919</article-id><article-categories><subj-group subj-group-type="heading"><subject>Articles</subject></subj-group><subj-group subj-group-type="Discipline-v2"><subject>Chemistry&amp;Materials Science</subject><subject> Engineering</subject></subj-group></article-categories><title-group><article-title>
 
 
  Utilization of Various Analogy of Synthetic Nanoporous Zeolites and Composite of Zeolites for Decontamination/Detoxification of CWA Simulants—An Updated Review
 
</article-title></title-group><contrib-group><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Neeraj</surname><given-names>Kumar</given-names></name><xref ref-type="aff" rid="aff1"><sup>1</sup></xref><xref ref-type="corresp" rid="cor1"><sup>*</sup></xref></contrib><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Kautily</surname><given-names>Rao Tiwari</given-names></name><xref ref-type="aff" rid="aff1"><sup>1</sup></xref></contrib><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Km.</surname><given-names>Meenu</given-names></name><xref ref-type="aff" rid="aff1"><sup>1</sup></xref></contrib><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Arti</surname><given-names>Sharma</given-names></name><xref ref-type="aff" rid="aff1"><sup>1</sup></xref></contrib><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Adya</surname><given-names>Jain</given-names></name><xref ref-type="aff" rid="aff1"><sup>1</sup></xref></contrib><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Shikha</surname><given-names>Singh</given-names></name><xref ref-type="aff" rid="aff1"><sup>1</sup></xref></contrib><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Radha</surname><given-names>Tomar</given-names></name><xref ref-type="aff" rid="aff1"><sup>1</sup></xref></contrib></contrib-group><aff id="aff1"><addr-line>School of Studies in Chemistry, Jiwaji University, Gwalior, India</addr-line></aff><pub-date pub-type="epub"><day>30</day><month>10</month><year>2019</year></pub-date><volume>08</volume><issue>04</issue><fpage>35</fpage><lpage>71</lpage><history><date date-type="received"><day>4,</day>	<month>May</month>	<year>2019</year></date><date date-type="rev-recd"><day>27,</day>	<month>October</month>	<year>2019</year>	</date><date date-type="accepted"><day>30,</day>	<month>October</month>	<year>2019</year></date></history><permissions><copyright-statement>&#169; Copyright  2014 by authors and Scientific Research Publishing Inc. </copyright-statement><copyright-year>2014</copyright-year><license><license-p>This work is licensed under the Creative Commons Attribution-NonCommercial International License (CC BY-NC).http://creativecommons.org/licenses/by-nc/4.0/</license-p></license></permissions><abstract><p>
 
 
  In this review, we summaries the past few year work on the chemistry of CWA’s and their simulants on various heterogeneous surfaces of zeolites, composites of zeolites and doped zeolite with transition metal oxides. This review elaborates an updated literature overview on the degradation of CWA’s and its simulants. The data written in this review were collected from the peer-reviewed national and international literature.
 
</p></abstract><kwd-group><kwd>Zeolite</kwd><kwd> Composites</kwd><kwd> Adsorption</kwd><kwd> Decontamination</kwd><kwd> Metal Oxide</kwd><kwd> CWA</kwd><kwd>  Simulants</kwd></kwd-group></article-meta></front><body><sec id="s1"><title>1. Introduction</title><sec id="s1_1"><title>1.1. Zeolites</title><p>Zeolites were first of all observed in 1756 by a Swedish mineralogist, Fredish Cronstedt. Due to its high stability at extreme temperatures, these were named as “Zeolite”. The word zeolite comes from two Greek words i.e. zeo (signifying “to boil”) and lithos (signifying “stone”) [<xref ref-type="bibr" rid="scirp.96919-ref1">1</xref>]. Therefore these are also known as “Boiling Stones”. Zeolites are three dimensional crystalline, micro porous, hydrated aluminosilicates of alkali and alkaline earth metals. The basic structure formula of zeolite is M<sub>x</sub><sub>/n</sub>[(AlO<sub>2</sub>)<sub>x</sub>(SiO<sub>2</sub>)<sub>y</sub>]∙wH<sub>2</sub>O, where M denotes alkali or alkaline earth metal 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 tetrahedral per unit cell. These are composed of primary building unit (PBU) and secondary building units (SBUs) [<xref ref-type="bibr" rid="scirp.96919-ref2">2</xref>] [<xref ref-type="bibr" rid="scirp.96919-ref3">3</xref>]. Primary building units of zeolites are the basic tetrahedral units i.e. [ SiO 4 ] 4 − and [ AlO 4 ] 5 − tetrahedrals which are linked to each other by the sharing of oxygen atoms while secondary building units are different geometrical arrangement or morphology of the tetrahedral units. The secondary building units may be simple polyhedral (cubes, hexagonal prisms) or cubo-octahedra as shown in <xref ref-type="fig" rid="fig1">Figure 1</xref>.</p><p>Till now, 232 unique zeolite frameworks have been identified, and over 40 naturally occurring zeolite frameworks are known [<xref ref-type="bibr" rid="scirp.96919-ref5">5</xref>]. Every new synthesized and naturally obtained zeolite structure has been approved by the International Zeolite Association Structure Commission (IZASC) and receives a three letter designation. Both natural and synthetic zeolites are very useful but synthetic zeolite over the natural zeolite shows higher thermal stability and purity. Hence they possess wide range of chemical properties and pore sizes [<xref ref-type="bibr" rid="scirp.96919-ref6">6</xref>]. According to different arrangements of these units, zeolites can be classified into eight classes: Zeolite-A, Zeolite-N-A, Zeolite-H, Zeolite-L, Zeolite-X, Zeolite-Y, Zeolite-P, Zeolite-O, Zeolite-Ω, Zeolite ZK-4 and Zeolite ZK-5 as shown in <xref ref-type="table" rid="table1">Table 1</xref>.</p><p>Nanocrystalline zeolites are nanoporous materials with crystal sizes within the range of 100 nm. They provide larger surface area with internal surface porosity [<xref ref-type="bibr" rid="scirp.96919-ref7">7</xref>]. Essentially, increase in the surface area provides increased adsorption of reactant molecules on its surface, which results in higher catalytic property. The various kinds of links/bonds form a variety of rings which are responsible for zeolites cages and channels of different window sizes. Zeolites consist of pores and cavities of molecular dimensions [<xref ref-type="bibr" rid="scirp.96919-ref8">8</xref>]. The increase in type and structural diversity of zeolites, as well as unique properties of zeolite such as thermal stability, acidity, hydrophobicity/hydrophilicity of surfaces and ion-exchange capacity, has led to variety of applications of zeolites in various industries [<xref ref-type="bibr" rid="scirp.96919-ref9">9</xref>]. Due to their unique ability to select molecules/atoms/ions on the basis of their respective sizes, zeolites are referred as “molecular sieves”. The major properties of zeolites are: catalysis, adsorption and ion exchange. The ions and water molecules enclosed inside these cavities have considerable freedom of movement permitting ion exchange and reversible dehydration [<xref ref-type="bibr" rid="scirp.96919-ref10">10</xref>].</p></sec><sec id="s1_2"><title>1.2. Framework of Zeolites</title><p>The effective size and shape of the pore opening are determined by following steps:</p><p>&#183; Configuration of T (i.e. Si<sup>4+</sup> and Al<sup>3+</sup> ion) and O atoms relative to each other,</p><p>&#183; SiO<sub>2</sub>/Al<sub>2</sub>O<sub>3</sub> ratio,</p><p>&#183; Size of cation,</p><p>&#183; Location of cation,</p><p>&#183; Temperature.</p><p>Zeolite containing the pore openings is referred as small, medium and large on the basis of number of members in the ring. The 8-membered ring have small pore size, diameters of about 0.30 - 0.45 nm (e.g. zeolite A), 10-membered ring has medium pore size, diameters of about 0.45 - 0.60 nm (e.g. ZSM-5), while 12-membered ring has large pore opening, diameter of about 0.6 - 0.8 nm (e.g. zeolites X, Y). 7, 9, 11, 14, 16, 18 and 20 membered ring was also discovered recently [<xref ref-type="bibr" rid="scirp.96919-ref11">11</xref>]. Some other examples of zeolites with their pore size and ring size are shown in <xref ref-type="table" rid="table2">Table 2</xref>. The framework of zeolite is greatly affected by building elements i.e. silicon (Si) and aluminium (Al). Silicon and aluminium play an effective role in defining different properties of zeolites (thermal stability, catalytic property etc.). On altering the ratio of silicon and aluminium, modification of zeolite takes place (i.e. from zeolite X to zeolite Y) [<xref ref-type="bibr" rid="scirp.96919-ref12">12</xref>]. Breck et al. [<xref ref-type="bibr" rid="scirp.96919-ref2">2</xref>] had reported that this modification occurs when Si/Al ratio is 1.5. When the ratio is lower than this critical point then it characterize zeolite X composition while higher than the critical point characterize zeolite Y composition [<xref ref-type="bibr" rid="scirp.96919-ref13">13</xref>].</p><table-wrap id="table1" ><label><xref ref-type="table" rid="table1">Table 1</xref></label><caption><title> Typical chemical formula of different zeolites [<xref ref-type="bibr" rid="scirp.96919-ref7">7</xref>] [<xref ref-type="bibr" rid="scirp.96919-ref14">14</xref>]</title></caption><table><tbody><thead><tr><th align="center" valign="middle" >Zeolites</th><th align="center" valign="middle" >Typical oxide formula</th></tr></thead><tr><td align="center" valign="middle" >Zeolites A</td><td align="center" valign="middle" >Na<sub>2</sub>O. Al<sub>2</sub>O<sub>3</sub>. 2SiO<sub>2</sub>. 4-5H<sub>2</sub>O</td></tr><tr><td align="center" valign="middle" >Zeolites N-A</td><td align="center" valign="middle" >(Na, TMA)<sub>2 </sub>O. Al<sub>2</sub>O<sub>3</sub>. 4-8SiO<sub>2</sub>. 7H<sub>2</sub>O; TMA – (CH<sub>3</sub>)4N<sup>+</sup></td></tr><tr><td align="center" valign="middle" >Zeolites H</td><td align="center" valign="middle" >K<sub>2</sub>O. Al<sub>2</sub>O<sub>3</sub>. 2SiO<sub>2</sub>. 4H<sub>2</sub>O</td></tr><tr><td align="center" valign="middle" >Zeolites L</td><td align="center" valign="middle" >(K<sub>2</sub>Na<sub>2</sub>)O. Al<sub>2</sub>O<sub>3</sub>. 6SiO<sub>2</sub>. 5H<sub>2</sub>O</td></tr><tr><td align="center" valign="middle" >Zeolites X</td><td align="center" valign="middle" >Na<sub>2</sub>O. Al<sub>2</sub>O<sub>3</sub>. 2-5SiO<sub>2</sub>. 6H<sub>2</sub>O</td></tr><tr><td align="center" valign="middle" >Zeolites Y</td><td align="center" valign="middle" >Na<sub>2</sub>O.Al<sub>2</sub>O<sub>3</sub>.<sub> </sub>4-8SiO<sub>2</sub>.<sub> </sub>8-9H<sub>2</sub>O</td></tr><tr><td align="center" valign="middle" >Zeolites P</td><td align="center" valign="middle" >Na<sub>2</sub>O. Al<sub>2</sub>O<sub>3</sub>. 2-5SiO<sub>2</sub>. 5H<sub>2</sub>O</td></tr><tr><td align="center" valign="middle" >Zeolites O</td><td align="center" valign="middle" >(Na<sub>2</sub>, K<sub>2</sub>, TMA<sub>2</sub>)O. Al<sub>2</sub>O<sub>3</sub>. 7SiO<sub>2</sub>. 3-5H<sub>2</sub>O;TMA – (CH<sub>3</sub>)4N<sup>+</sup></td></tr><tr><td align="center" valign="middle" >Zeolites Ω</td><td align="center" valign="middle" >(Na, TMA)<sub>2</sub> O. Al<sub>2</sub>O<sub>3</sub>. 7SiO<sub>2</sub>. 5H<sub>2</sub>O; TMA – (CH<sub>3</sub>)4N<sup>+</sup></td></tr><tr><td align="center" valign="middle" >Zeolites ZK-4</td><td align="center" valign="middle" >0.85 Na<sub>2</sub>O. 0.15(TMA)<sub>2</sub> O. Al<sub>2</sub>O<sub>3</sub>. 3SiO<sub>2</sub>. 6H<sub>2</sub>O</td></tr><tr><td align="center" valign="middle" >Zeolites ZK-5</td><td align="center" valign="middle" >(R,Na<sub>2</sub>)O. Al<sub>2</sub>O<sub>3</sub>. 4-6 SiO<sub>2</sub>. 6H<sub>2</sub>O</td></tr></tbody></table></table-wrap><table-wrap id="table2" ><label><xref ref-type="table" rid="table2">Table 2</xref></label><caption><title> Zeolite pores and ring size</title></caption><table><tbody><thead><tr><th align="center" valign="middle" >Zeolite Type</th><th align="center" valign="middle" >Pore size (nm)</th><th align="center" valign="middle" >Ring size</th></tr></thead><tr><td align="center" valign="middle" >MCM-22, 49</td><td align="center" valign="middle" >0.6</td><td align="center" valign="middle" >10-membered</td></tr><tr><td align="center" valign="middle" >UTD-1</td><td align="center" valign="middle" >1.0</td><td align="center" valign="middle" >14-membered</td></tr><tr><td align="center" valign="middle" >CIT-5</td><td align="center" valign="middle" >0.8</td><td align="center" valign="middle" >14-membered</td></tr><tr><td align="center" valign="middle" >EMC-2</td><td align="center" valign="middle" >0.7</td><td align="center" valign="middle" >12-membered</td></tr><tr><td align="center" valign="middle" >Colverite</td><td align="center" valign="middle" >1.3</td><td align="center" valign="middle" >20-membered</td></tr></tbody></table></table-wrap><p>High silica content in zeolite shows catalytic properties [<xref ref-type="bibr" rid="scirp.96919-ref15">15</xref>] [<xref ref-type="bibr" rid="scirp.96919-ref16">16</xref>]. Therefore to incorporate higher catalytic property in zeolite dealumination method (chemical and structural modifications take place) is applied. EDTA has the capability to remove half of the framework aluminium atoms while treating with silicon tetrachloride, Al atoms get replaced by silicon atoms [<xref ref-type="bibr" rid="scirp.96919-ref17">17</xref>] [<xref ref-type="bibr" rid="scirp.96919-ref18">18</xref>]. Thus, greater catalytic activity can be achieved. It has been reported that at lower temperature small crystals are synthesized as compared to higher temperature. Lower than 140˚C yield amorphous crystals, at 140˚C smallest crystals and above 140˚C large crystals were observed. Therefore crystal size is directly related to temperature change, on increasing the temperature, crystal size increases [<xref ref-type="bibr" rid="scirp.96919-ref19">19</xref>].</p></sec><sec id="s1_3"><title>1.3. Properties of Zeolites</title><p>There are various properties of zeolites such as physical and chemical, ion exchange, catalytic, adsorption, minrological-morphological properties, crystal structure, framework of zeolite and surface morphology makes zeolite as an useful nanomaterial for multiple applications. The properties of zeolite are discussed below.</p><sec id="s1_3_1"><title>1.3.1. Physical Properties</title><p>The most important physical properties of zeolite are specific gravity (2 - 2.8 g/cm<sup>3</sup>), bulk density, thermal stability, cation exchange proerty and specific surface area. The physical properties of zeolite depend on pore volume of zeolite, their void volume and dissolution of particles in solvents. The most common and general property is their particle size, large variation (2 μm - 800 nm) in particle size permit approxamitely 10% - 60% material by weight to the sieves of zeolite (adsorption) [<xref ref-type="bibr" rid="scirp.96919-ref20">20</xref>] [<xref ref-type="bibr" rid="scirp.96919-ref21">21</xref>].</p></sec><sec id="s1_3_2"><title>1.3.2. Chemical Properties</title><p>Zeolite comprises of different metal oxides within their structure with water molecule in the pores or in the voids. A certain loss in mass of zeolite after calcination at about 500˚C - 600˚C was due to loss of water molecule. Many chemists suggest that for a zeolite material the ratio of silicon and aluminium oxide should be equal and greater than 0.5. The adsorption property, pH value, cation exchange property are some main chemical properties, which depends upon chemical composition of the synthesized nanoporous zeolite materials [<xref ref-type="bibr" rid="scirp.96919-ref22">22</xref>] [<xref ref-type="bibr" rid="scirp.96919-ref23">23</xref>] [<xref ref-type="bibr" rid="scirp.96919-ref24">24</xref>].</p></sec><sec id="s1_3_3"><title>1.3.3. Ion Exchange and Adsorption Properties</title><p>Zeolite having a specific property of cation (H<sup>+</sup>, Na<sup>+</sup>, K<sup>+</sup>, Ca<sup>2+</sup>, Mg<sup>2+</sup>, Ag<sup>3+</sup>, Zn<sup>2+</sup>, Cu<sup>+</sup>, NH 4 + ) exchange by the interaction with sorrunding medium during synthesis. However, the cations are balanced by the negative charge developed on the surface of pores of zeolite. This can be attributed to exchange silicon atom by aluminium in some tetrahedra of [ SiO 4 ] 4 − and converted into [ AlO 4 ] 5 − tetrahedra, which are connected through each other through common oxygen atom in <xref ref-type="fig" rid="fig1">Figure 1</xref>. The heavy metal cations like Cs, Ag, Cd, Pb, Zn, Cu, Hg, Co, Cr, Ni, Ba, Rb, Sr etc. have affanity, zeolite which depends upon hydrated molecular size of the cation and silicon/aluminium molar ratio of the zeolite framework. Due to such properties zeolites have been found good adsorber of gases, liquids materials and separate them for environmental as well as defence purposen [<xref ref-type="bibr" rid="scirp.96919-ref25">25</xref>] [<xref ref-type="bibr" rid="scirp.96919-ref26">26</xref>] [<xref ref-type="bibr" rid="scirp.96919-ref27">27</xref>] [<xref ref-type="bibr" rid="scirp.96919-ref28">28</xref>].</p></sec></sec><sec id="s1_4"><title>1.4. Applications of Zeolites</title><p>Zeolites are used as catalyst in many organic reactions like cracking, isomerisation and hydrocarbon synthesis etc. The reaction occurs inside the pores of zeolites, which permit a considerable product authority. Thus zeolites act as oxidation catalysts, acid catalysts as well as shape-selective catalysts as supports for reagents and active metals. Zeolites are greatly used in petroleum refining, synfuels production and petrochemical production [<xref ref-type="bibr" rid="scirp.96919-ref29">29</xref>]. Zeolites can absorb a variety of materials therefore used in variety of applications like drying, purification, separation and also highly used in degradation of toxic compounds and gases like chemical warfare agents (CWAs), volatile organic compounds (VOCs) etc. They can also act as efficient desiccants i.e. remove water to very low partial pressures. Zeolites also act as ion exchangers due to presence of loosely bounded hydrated cations which can easily exchange with other cations. Hence zeolites can also be widely used in detergent formulations, nuclear industry, and radioactive waste cleanup and in metal removal applications [<xref ref-type="bibr" rid="scirp.96919-ref30">30</xref>].</p></sec><sec id="s1_5"><title>1.5. Methods for the Synthesis of Zeolites</title><p>Most of zeolites present in nature as minerals, and are broadly mined in different parts of the world. Some are synthetic, and are synthesized for specific commercial uses, or synthesized by researchers for understanding the internal chemistry. K. J Murata et al. [<xref ref-type="bibr" rid="scirp.96919-ref31">31</xref>] has recommended that zeolites are formed through alteration of rock-water reactions and which changes into sedimentary rock during and after rock formation. Such reactions are also responsible for the production of other minerals. This transmutation of volcanic spoilage leads to the formation of zeolites in layers structures (“zeolite zones”) called facies. To determine the types of zeolite formed are carried out by various factors. There are many methods for the synthesis of zeolites. Organic templates used in the synthesis of zeolites are generally toxic and expensive. Therefore, green methods or sustainable methods are applied in the synthesis of zeolites. Green methods [<xref ref-type="bibr" rid="scirp.96919-ref32">32</xref>] include ionothermal synthetic method (by using ionic liquids as solvent), solvent free synthetic method (water as solvent is completely avoided) [<xref ref-type="bibr" rid="scirp.96919-ref33">33</xref>]. It was found that particle size was much larger than the sizes obtained via the conventional hydrothermal route [<xref ref-type="bibr" rid="scirp.96919-ref34">34</xref>] and relative high efficient zeolites are synthesized through microwave assisted method [<xref ref-type="bibr" rid="scirp.96919-ref35">35</xref>] (homogeneous heating) and hydrothermal method (high pressure) [<xref ref-type="bibr" rid="scirp.96919-ref36">36</xref>]. Thus, among all the methods mention above hydrothermal method is effective, cost effective, easiest and adopted by IZA (International Zeolite Association).</p><p>Hydrothermal method: Conventional hydrothermal synthesis of zeolites involves heating the reaction mixture in a polytetrafluoroethylene (PTFE) lined steel autoclave (<xref ref-type="fig" rid="fig2">Figure 2</xref>).</p><p>The safety of the equipment is always of concern due to high autogenous pressure. The hydrothermal synthesis of zeolites sometimes takes long times (1 - 20 days) even at relatively temperature (80˚C - 200˚C), therefore considered as high energy cost process.</p></sec><sec id="s1_6"><title>1.6. Description of Some Selected Zeolites</title><p>&#183; Zeolite Beta;</p><p>&#183; Linde Type L;</p><p>&#183; ZSM-22.</p><p>Zeolite beta consists of an intergrowth of two distinct structures termed Polymorphs A and B. The polymorphs grow as two-dimensional sheets and the sheets randomly alternate between the two. Both polymorphs have a three dimensional network of 12-ring pores [<xref ref-type="bibr" rid="scirp.96919-ref38">38</xref>]. Linde Type L (LTL) is one dimensional 12-membered ring channel system has shown as promising material in environmental and industrial applications [<xref ref-type="bibr" rid="scirp.96919-ref39">39</xref>]. ZSM-22 is the member of medium-pore zeolite family (mordenite family) which also includes ZSM-35, ZSM-11and ZSM-5. Almost all members of this zeolite family consist five-membered rings with curvy channels enclosed by ten-membered rings. The free diameter of groove of the channel is ~0.45 &#215; 0.55 nm. The growth of channel was observed in single face direction and having no criss-crossing of the channels [<xref ref-type="bibr" rid="scirp.96919-ref40">40</xref>].</p></sec></sec><sec id="s2"><title>2. Chemical Warfare Agents</title><p>Chemical warfare agents (CWA) are chemical substances that are used in warfare or terrorist activities to kill or seriously injure the people though their physiological effects [<xref ref-type="bibr" rid="scirp.96919-ref41">41</xref>]. A German scientist named Gerhard Schrader accidentally discovered the first nerve agent, Tabun in 1930. With the passes of time many other stable nerve agents have been developed by mid of 1950 and this is known as V-agent in USA nomenclature. Tabun is very poisonous among all toxic substances ever synthesized [<xref ref-type="bibr" rid="scirp.96919-ref42">42</xref>]. Similarly sulfur mustard (C<sub>4</sub>H<sub>8</sub>Cl<sub>2</sub>S) is one of a class of chemical warfare agents known as vesicants because of their ability to form vesicles, blisters on exposed skin. The odor of nerve agent like mustard or garlic, hence it gets its common name sulfur mustard. The first use of nerve agent in war was by Afghanistan in 1979-80 and Iraq-Iran war from 1984-1987. The resulting Iraq-Iran chemical warfare was estimated more than 50,000 casualties. Immediately after the war, researchers were totally focused on studies of nerve agent CWA and their mechanisms. Efforts were made to discover new effective methods of protection against these CWA and its simulants [<xref ref-type="bibr" rid="scirp.96919-ref43">43</xref>] [<xref ref-type="bibr" rid="scirp.96919-ref44">44</xref>] [<xref ref-type="bibr" rid="scirp.96919-ref45">45</xref>] [<xref ref-type="bibr" rid="scirp.96919-ref46">46</xref>]. <xref ref-type="table" rid="table3">Table 3</xref>, describes an overview of all above mentioned toxic chemical warfare agents along with their symptoms method of exposure and toxic manifestations. CWA’s have been used at least twelve conflicts since including the first Iran-Iraq war know as Persian Gulf War. In <xref ref-type="table" rid="table4">Table 4</xref>, we mentioned some major chemical attacks and estimated value of casualties. Although a number of national and international convention have banned the development, production and stockpiling of chemical weapons. In spite of this, these toxic chemicals are still used.</p><table-wrap id="table3" ><label><xref ref-type="table" rid="table3">Table 3</xref></label><caption><title> An overview of CW agents [<xref ref-type="bibr" rid="scirp.96919-ref47">47</xref>] [<xref ref-type="bibr" rid="scirp.96919-ref48">48</xref>] [<xref ref-type="bibr" rid="scirp.96919-ref49">49</xref>]</title></caption><table><tbody><thead><tr><th align="center" valign="middle" >Type of Chemical Warfare Agent</th><th align="center" valign="middle" >Class of Chemical Warfare Agent</th><th align="center" valign="middle" >Toxic Manifestation</th><th align="center" valign="middle" >Exposure Method</th><th align="center" valign="middle" >Symptoms</th></tr></thead><tr><td align="center" valign="middle" >Blister agents</td><td align="center" valign="middle" >HD, HN1 HN2, HN3, L1</td><td align="center" valign="middle" >Slow Fast</td><td align="center" valign="middle" >Inhalation</td><td align="center" valign="middle" >Acute; Eye, Skin and Lung Damage, Rash Skin Blistering</td></tr><tr><td align="center" valign="middle" >Nerve agents</td><td align="center" valign="middle" >GB, GA, GD, GF, DF, VX and RVX</td><td align="center" valign="middle" >Fast</td><td align="center" valign="middle" >Inhalation</td><td align="center" valign="middle" >Sludge, Miotic, Pupils, Weakness, Muscle Spasms, Flaccid Paralysis, Seizures, Shortness of Breath Respiratory Failure, Vomiting and Diarrhea</td></tr><tr><td align="center" valign="middle" >Blood agents</td><td align="center" valign="middle" >CK, AC</td><td align="center" valign="middle" >Fast</td><td align="center" valign="middle" >Inhalation, Skin Absorption, Ingestion</td><td align="center" valign="middle" >Hypotension, Cyanosis, Severe Distress, Cardiac Arrest</td></tr><tr><td align="center" valign="middle" >Choking agent</td><td align="center" valign="middle" >CG CL, PS</td><td align="center" valign="middle" >Slow Fast</td><td align="center" valign="middle" >Inhalation, Skin Absorption, Ingestion</td><td align="center" valign="middle" >Serve Pain in Expose Area, Hyperkalemia, Vomiting, Gastrointestinal Distress</td></tr></tbody></table></table-wrap><table-wrap id="table4" ><label><xref ref-type="table" rid="table4">Table 4</xref></label><caption><title> Chemical warfare agents as chemical weapons in wars and estimated causalities [<xref ref-type="bibr" rid="scirp.96919-ref50">50</xref>] [<xref ref-type="bibr" rid="scirp.96919-ref51">51</xref>]</title></caption><table><tbody><thead><tr><th align="center" valign="middle" >Name of Country</th><th align="center" valign="middle" >Year</th><th align="center" valign="middle" >CWA</th><th align="center" valign="middle" >Causalities (Estimated)</th></tr></thead><tr><td align="center" valign="middle" >Germany</td><td align="center" valign="middle" >1915-18</td><td align="center" valign="middle" >Chlorine, phosgene and Mustard gas</td><td align="center" valign="middle" >120,000</td></tr><tr><td align="center" valign="middle" >Italy</td><td align="center" valign="middle" >1936</td><td align="center" valign="middle" >Mustard gas</td><td align="center" valign="middle" >15,000</td></tr><tr><td align="center" valign="middle" >Japan (Two Times)</td><td align="center" valign="middle" >1937-45 and 1995</td><td align="center" valign="middle" >Mustard gas</td><td align="center" valign="middle" >2500</td></tr><tr><td align="center" valign="middle" >America</td><td align="center" valign="middle" >1962-1967</td><td align="center" valign="middle" >Tear gas and Herbicides</td><td align="center" valign="middle" >2000</td></tr><tr><td align="center" valign="middle" >Afghanistan</td><td align="center" valign="middle" >1979-80</td><td align="center" valign="middle" >Mustard gas</td><td align="center" valign="middle" >2100</td></tr><tr><td align="center" valign="middle" >Iraq</td><td align="center" valign="middle" >1980-88</td><td align="center" valign="middle" >Mustard gas</td><td align="center" valign="middle" >50,000</td></tr><tr><td align="center" valign="middle" >Syria (Four Times)</td><td align="center" valign="middle" >2013-18</td><td align="center" valign="middle" >Sarin gas</td><td align="center" valign="middle" >1000</td></tr></tbody></table></table-wrap><p>Therefore Chemical Warfare Agents (CWAs) are very toxic compounds basically used to kill, injure or harm people as well other living organisms. They are also hazardous to the environment (i.e. contaminate air, water and land). Hence, there is increasing interest in the effective detection as well as degradation of these compounds [<xref ref-type="bibr" rid="scirp.96919-ref52">52</xref>].</p><sec id="s2_1"><title>2.1. Classification of Chemical Warfare Agents</title><p>The CWAs have different characteristic property and thus belong to different categories with distinct physicochemical properties. Thus, they are classified in many ways [<xref ref-type="bibr" rid="scirp.96919-ref53">53</xref>] discussed as follow.</p><sec id="s2_1_1"><title>2.1.1. On the Basis of Volatility, They Are Classified into Two Categories</title><p>&#183; Persistent agents: The less volatile agents i.e. persist in the environment for longer duration like sulfur mustard (HD) and VX come under this category.</p><p>&#183; Non-persistent agents: The more volatile agents (evaporated quickly) are known as non-persistent agents like chlorine, phosgene and hydrogen cyanide.</p></sec><sec id="s2_1_2"><title>2.1.2. On the Basis of Chemical Structure, They Are Classified as Follows</title><p>&#183; Organophosphorus (OP): G-nerve agents such as Tabun (GA), Sarin (GB), Soman (GD), Cyclosarin (GF) etc.</p><p>&#183; Organosulfur: HD or Sulfur mustard.</p><p>&#183; Arsenicals: Ethyldichloroarsine (ED), Methyldichloroarsine (MD), Phenyldichloroarsine (PD) and 2-Chlorovinyldichloroarsine etc.</p></sec><sec id="s2_1_3"><title>2.1.3. On the Basis of Physiological Effects (Harmful/Lethal Effects) by the CWAs, These Can Be Classified into Following Categories</title><p>&#183; Psychomimetic agents:</p><p>Psychomimetic agents also called psychotogenic agents which cause delusions and hallucinations on exposure. Opioid drugs and hallucinogenic drugs come under this category [<xref ref-type="bibr" rid="scirp.96919-ref53">53</xref>].</p><p>&#183; Nerve agents (highly toxic):</p><p>As the name suggests they affect the nervous system functioning. These agents belong to group of Organophosphorus (OP) compounds. The first known nerve agent, Tabun (GA) was developed as new OP insecticides. This nerve agent series is known as the G-agents, which include Sarin (GB), Cyclosarin (GF) and Soman (GD). Then, V-agents were developed which were more stable derivatives of G agents. VX (a sulfur-containing OP) is more stable, less volatile and less water-soluble, acting through direct skin contact, and persisting in the environment up to several weeks after release as compared to other G agents. Atropine and Pralidoxime are used as nerve agent antidotes [<xref ref-type="bibr" rid="scirp.96919-ref54">54</xref>].</p><p>&#183; Vesicants (blistering agents):</p><p>These cause blisters or skin injuries. There are two forms of vesicants: mustards (sulfur and nitrogen mustards), lewisites and arsenicals. Sulfur mustard (commonly known as mustard gas, HD, LOST, Yperite, etc.) is called as the king of CW agents. Few examples of vesicants with their chemical formula are: [<xref ref-type="bibr" rid="scirp.96919-ref55">55</xref>]</p><p>- Sulfur Mustard (HD) ClCH<sub>2</sub>CH<sub>2</sub>SCH<sub>2</sub>CH<sub>2</sub>Cl;</p><p>- Nitrogen Mustard (HN-1) (CH<sub>2</sub>CH<sub>2</sub>Cl)<sub>2</sub>NC<sub>2</sub>H<sub>5</sub>;</p><p>- Nitrogen Mustard (HN-2) (CH<sub>2</sub>CH<sub>2</sub>Cl)<sub>2</sub>NCH<sub>3</sub>;</p><p>- Nitrogen Mustard (HN-3) N(CH<sub>2</sub>CH<sub>2</sub>Cl)<sub>3</sub>;</p><p>- Lewisite (L) ClCH=CHAsCl<sub>2</sub>.</p><p>&#183; Bloods agents (cyanogenic agents):</p><p>These agents get absorbed into the blood by binding with oxygen-carrying hemoglobin in the blood generally known as “cyanide poisoning”, hydrogen cyanide (HCN), cynogen (CN)<sub>2</sub>, phosgene (COCl<sub>2</sub>), arsine (AsH<sub>3</sub>), cynogen chloride (NCCl) and cynogen bromide ((CN)Br) come under this category [<xref ref-type="bibr" rid="scirp.96919-ref56">56</xref>] [<xref ref-type="bibr" rid="scirp.96919-ref57">57</xref>].</p><p>&#183; Choking agents:</p><p>Chocking agent’s also known by the name pulmonary agents. Chlorine gas (Cl<sub>2</sub>), chloropicrin (PS) (Cl<sub>3</sub>CNO<sub>2</sub>), diphosgene (ClCO<sub>2</sub>CCl<sub>3</sub>), disulfur decafluoride (S<sub>2</sub>F<sub>10</sub>), perfluoroisobutene (C<sub>4</sub>F<sub>8</sub>) etc. are some comman examples of such agents. Throat burning, headache, coughing, vomiting, chest pain are major symptoms on inhalation of these agents [<xref ref-type="bibr" rid="scirp.96919-ref58">58</xref>] [<xref ref-type="bibr" rid="scirp.96919-ref59">59</xref>] [<xref ref-type="bibr" rid="scirp.96919-ref60">60</xref>].</p><p>&#183; Riot-control agents:</p><p>Riot control agent’s also known by another name called lachrymatory agents or tear gases. The symptoms of these agents are skin &amp; eye irritation, respiratory, Chest pain, vomiting and even blindness. Capsaicin, CS gas (C<sub>10</sub>H<sub>5</sub>ClN<sub>2</sub>), CR gas (dibenzoxazepine), CN gas (phenacyl chloride), bromoacetone etc. are some comman examples of such agents [<xref ref-type="bibr" rid="scirp.96919-ref61">61</xref>] [<xref ref-type="bibr" rid="scirp.96919-ref62">62</xref>].</p></sec></sec><sec id="s2_2"><title>2.2. Molecular Structure of CWA</title><p>Molecular structure of some CW agents is given in <xref ref-type="table" rid="table5">Table 5</xref>, along with IUPAC name, common names and percentage of each atom in particular CW agent.</p><table-wrap id="table5" ><label><xref ref-type="table" rid="table5">Table 5</xref></label><caption><title> Molecular structure, IUPAC and common name of CW agents</title></caption><table><tbody><thead><tr><th align="center" valign="middle" >Structure of CW Agents</th><th align="center" valign="middle" >IUPAC Name &amp; Composition (%) of Atoms</th><th align="center" valign="middle" >Common Names</th></tr></thead><tr><td align="center" valign="middle" ><inline-formula><inline-graphic xlink:href="/html.scirp.org/file/1-2580114x9.png" xlink:type="simple"/></inline-formula> Sulfur mustard (HD)</td><td align="center" valign="middle" >1-chloro-2-[(2-chloroethyl)sulfanyl]ethane C (30.20%), H (5.07%), Cl (44.57%), S (20.16%)</td><td align="center" valign="middle" >Mustard gas</td></tr><tr><td align="center" valign="middle" ><inline-formula><inline-graphic xlink:href="/html.scirp.org/file/1-2580114x10.png" xlink:type="simple"/></inline-formula> Tabun (GA)</td><td align="center" valign="middle" >EthyN,N,dimethyl phosphoramidocyanidate C (41.10%), H (7.59%), N (19.17%), O (10.95%), P (21.20%)</td><td align="center" valign="middle" >Tabun</td></tr><tr><td align="center" valign="middle" ><inline-formula><inline-graphic xlink:href="/html.scirp.org/file/1-2580114x11.png" xlink:type="simple"/></inline-formula> Sarin (GB)</td><td align="center" valign="middle" >Propanyl methylphosphonofluoridate C (34.29%), H (7.19%), F (13.56%), O (22.84%), P (22.11%)</td><td align="center" valign="middle" >Sarin</td></tr><tr><td align="center" valign="middle" ><inline-formula><inline-graphic xlink:href="/html.scirp.org/file/1-2580114x12.png" xlink:type="simple"/></inline-formula> Soman (GD)</td><td align="center" valign="middle" >Propan-2-yl methylphosphonofluoridate-ethane C (42.35%), H (9.48%), F (11.16%), O (18.80%), P (18.20%)</td><td align="center" valign="middle" >Soman</td></tr><tr><td align="center" valign="middle" ><inline-formula><inline-graphic xlink:href="/html.scirp.org/file/1-2580114x13.png" xlink:type="simple"/></inline-formula> Cyclosarin (GB)</td><td align="center" valign="middle" >Cyclohexylfluorophosphonate C (38.29%), H (3.19%), F (13.56%), O (22.84%), P (22.11%)</td><td align="center" valign="middle" >Cyclosarin</td></tr><tr><td align="center" valign="middle" ><inline-formula><inline-graphic xlink:href="/html.scirp.org/file/1-2580114x14.png" xlink:type="simple"/></inline-formula> Amiton (VX)</td><td align="center" valign="middle" >S-{2-[di (propan-2-yl)amino]ethyl} O-ethyl methylphosphonothioate C (49.41%), H (9.80%), N (5.24%), O (11.97%), P (11.58%), S (11.99%)</td><td align="center" valign="middle" >Amiton</td></tr><tr><td align="center" valign="middle" ><inline-formula><inline-graphic xlink:href="/html.scirp.org/file/1-2580114x15.png" xlink:type="simple"/></inline-formula> Lewisite (L)</td><td align="center" valign="middle" >2-Chlorovinyldichloroarsine C (19.28%), H (2.70%), As (40.09%), Cl (37.94%)</td><td align="center" valign="middle" >Lewisite</td></tr></tbody></table></table-wrap></sec></sec><sec id="s3"><title>3. Simulants of CW Agents</title><p>Chemical warfare agent simulants are less toxic than real agents. These compounds suitable as spectral simulants that give rise to similar spectral characteristics and mimic all the properties of a CWA except for its toxicity. There is recommence interest in the environmental fate of Chemical Warfare Agents attributable to expand threat of chemical weapons use in a terrorist attack. The knowledge acquisition procedures used that influence the providence of Chemical warfare agents such as sulfur mustard, Lewisite, Tabun, Sarin, Soman, VX etc. in the environment are important for evolution of demolition strategies and exposure evaluations. Hence, it is necessary to extremely examine the behavior of Chemical agent by using their simulants because of the toxicity of the agents and diminution. An ideal simulant is the one which shows all the major chemical and physical properties of the CWA without any toxic or lethal properties. No definite simulant is ideal because a single simulant cannot effectively represent all environmental fate properties of a given CWA. Thus, depending on the concerned physical-chemical property, a number of different chemicals are used as chemical warfare agent’s simulants [<xref ref-type="bibr" rid="scirp.96919-ref52">52</xref>] [<xref ref-type="bibr" rid="scirp.96919-ref63">63</xref>] [<xref ref-type="bibr" rid="scirp.96919-ref64">64</xref>]. List of some common simulents are shown in <xref ref-type="table" rid="table6">Table 6</xref>.</p><sec id="s3_1"><title>3.1. HD Simulants</title><p>Sulfur mustards, particularly bis (2-chloroethyl) sulfide (HD) are a well known class of chemical warfare agent (CWA). Pure sulfur mustards are colorless, viscous liquids at room temperature. Sulfur mustards which have the ability to form large blisters on direct contact to skin and in the lungs. Molecular structures of simulents of HD are shown in <xref ref-type="fig" rid="fig3">Figure 3</xref> [<xref ref-type="bibr" rid="scirp.96919-ref53">53</xref>] [<xref ref-type="bibr" rid="scirp.96919-ref64">64</xref>] [<xref ref-type="bibr" rid="scirp.96919-ref65">65</xref>] [<xref ref-type="bibr" rid="scirp.96919-ref66">66</xref>].</p></sec><sec id="s3_2"><title>3.2. G-Agents</title><p>Nerve agents are compounds that have the greater potential to inactivate the enzyme acetylcholinesterase (AChE) which is present in nerve system. The first compounds to be synthesized were known as the G-series agents (“G” stands for German): tabun (GA), sarin (GB) and soman (GD). The organophosphate nerve agents GA, GB, GD, and GF are found very volatile in nature and having most toxic nature. Simulants molecular structures are shown below (Figures 4-6) [<xref ref-type="bibr" rid="scirp.96919-ref6">6</xref>].</p><table-wrap id="table6" ><label><xref ref-type="table" rid="table6">Table 6</xref></label><caption><title> Some common simulents of CW agents</title></caption><table><tbody><thead><tr><th align="center" valign="middle" >S. No.</th><th align="center" valign="middle" >Simulant</th><th align="center" valign="middle" >Type of CWAs</th></tr></thead><tr><td align="center" valign="middle" >1.</td><td align="center" valign="middle" >CEES, CEMS, CEPS</td><td align="center" valign="middle" >HD (Blistering agent)</td></tr><tr><td align="center" valign="middle" >2.</td><td align="center" valign="middle" >DPDP, DMMP, DEEP, TEP, DIMP, TMP</td><td align="center" valign="middle" >G (nerve agent)</td></tr><tr><td align="center" valign="middle" >3.</td><td align="center" valign="middle" >Amiton, DEPPT, Malathion, Parathion</td><td align="center" valign="middle" >V (nerve agent)</td></tr><tr><td align="center" valign="middle" >4</td><td align="center" valign="middle" >Lewisite Oxide , Phenyl arsine oxide</td><td align="center" valign="middle" >Lewisite (L), Blistering agent</td></tr></tbody></table></table-wrap></sec><sec id="s3_3"><title>3.3. VX-Agents</title><p>The V-series agents are class of the group persistent agents, which have low volatility and can remain on skin, clothes, and other surfaces for long periods of time. The consistency of these nerve agents is very much similar to oil and this consistency renders them toxic mainly by dermal exposures. The other agents in the V-series are less known, and the information available about their characteristics is fairly limited in the open, unclassified literature. The other agents also have coded names; including VE, V-gas, VG and VM. Molecular structures are shown in <xref ref-type="fig" rid="fig7">Figure 7</xref> [<xref ref-type="bibr" rid="scirp.96919-ref64">64</xref>] [<xref ref-type="bibr" rid="scirp.96919-ref67">67</xref>].</p></sec><sec id="s3_4"><title>3.4. L-Agents</title><p>Lewisites (L) are Organoarsenic compound and known blister agent and lungs irritant. The Lewisite made as a war gas in 1918 by W. Lee Lewis. It was manufactured in Germany, Japan, US, and the Soviet Union for use as chemical weapon. At room temperature pure lewisite was found more volatile than sulfur mustard. It is colorless oily liquid having “geranium” odor. But the impure lewisites are brown, yellow, violet-black, green, or amber oily liquids. The simulants of lewisite are shown in <xref ref-type="fig" rid="fig8">Figure 8</xref> [<xref ref-type="bibr" rid="scirp.96919-ref64">64</xref>] [<xref ref-type="bibr" rid="scirp.96919-ref68">68</xref>] [<xref ref-type="bibr" rid="scirp.96919-ref69">69</xref>].</p></sec></sec><sec id="s4"><title>4. Physico-Chemical Properties of CWA</title><p>Some essential physical and chemical properties of Chemical Warfare Agent are given in <xref ref-type="table" rid="table7">Table 7</xref>, which provides useful information about particular agent. A verity of compounds has been used as simulent for CWA on the basis of their physico-chemical properties.</p></sec><sec id="s5"><title>5. Decontamination Methods</title><p>Decontamination is a complex process and can be considered in different ways. Some basic fundamental methods of decontamination of chemical warfare agents are physical decontamination, mechanical decontamination, biological decontamination and chemical decontamination (<xref ref-type="fig" rid="fig9">Figure 9</xref>). Decontamination means a method used to reduce or remove and destroy the toxic nature of chemical agents [<xref ref-type="bibr" rid="scirp.96919-ref72">72</xref>]. Different CWAs are degraded by different chemical processes [<xref ref-type="bibr" rid="scirp.96919-ref73">73</xref>].</p><p>HD gas is degraded by dehydrohalogenation (CaO have this property and thus used against the degradation of CEES), aerobic oxidation by the help of catalyst [<xref ref-type="bibr" rid="scirp.96919-ref74">74</xref>], oxidation by using hydrogen peroxide, photo oxidation (TiO<sub>2</sub> have this property). G agents are degraded by two methods: enzymatic hydrolysis and non-enzymatic hydrolysis. In enzymatic hydrolysis organophosphorous hydrolase enzyme (microbial degradation) is involved [<xref ref-type="bibr" rid="scirp.96919-ref75">75</xref>]. Such catalyst yields large amount of acidic products therefore buffer is required to maintain the pH of the reaction in neutral to slightly alkaline range [<xref ref-type="bibr" rid="scirp.96919-ref76">76</xref>]. Non-enzymatic hydrolysis involves chemical compounds (i.e. iodosylcarboxylates) that promote catalytic hydrolysis in which nucleophilic substitution and hydrolysis reaction takes place [<xref ref-type="bibr" rid="scirp.96919-ref77">77</xref>].</p></sec><sec id="s6"><title>6. Zeolites and Composites of Zeolite Used for Decontamination of CWA and Its Simulants</title><p>A survey of literature revealed that zeolites and composite of zeolites play an important role in the welfare of society and emerged as an important field of research due to their diversified applications as these are completely safe and natural material. A lot of research work has been carried out for the degradation of chemical warfare agents by different materials (e.g. metal oxides like MgO [<xref ref-type="bibr" rid="scirp.96919-ref52">52</xref>] [<xref ref-type="bibr" rid="scirp.96919-ref78">78</xref>] [<xref ref-type="bibr" rid="scirp.96919-ref79">79</xref>] [<xref ref-type="bibr" rid="scirp.96919-ref80">80</xref>], CaO [<xref ref-type="bibr" rid="scirp.96919-ref81">81</xref>], Al<sub>2</sub>O<sub>3</sub> [<xref ref-type="bibr" rid="scirp.96919-ref82">82</xref>], ZnO [<xref ref-type="bibr" rid="scirp.96919-ref83">83</xref>], lanthanum oxide and Fe<sub>2</sub>O<sub>3</sub> [<xref ref-type="bibr" rid="scirp.96919-ref84">84</xref>], Y<sub>2</sub>O<sub>3</sub> [<xref ref-type="bibr" rid="scirp.96919-ref85">85</xref>], nanorods [<xref ref-type="bibr" rid="scirp.96919-ref86">86</xref>], nanotubes [<xref ref-type="bibr" rid="scirp.96919-ref87">87</xref>] [<xref ref-type="bibr" rid="scirp.96919-ref88">88</xref>], nanobelts [<xref ref-type="bibr" rid="scirp.96919-ref89">89</xref>], detoxifying catalyst and reactive polymers [<xref ref-type="bibr" rid="scirp.96919-ref73">73</xref>] [<xref ref-type="bibr" rid="scirp.96919-ref90">90</xref>] ). However, a little effort has been made to synthesize zeolites or its derivatives (doped with either by metal oxides [<xref ref-type="bibr" rid="scirp.96919-ref91">91</xref>] or polymers [<xref ref-type="bibr" rid="scirp.96919-ref92">92</xref>] ). This fact has prompted us to synthesize some new metal oxide doped zeolites for the degradation of CWAs.</p></sec><sec id="s7"><title>7. Literature Survey</title><p>F. Carniatoa et al. [<xref ref-type="bibr" rid="scirp.96919-ref93">93</xref>] (2018) have been reported a class of heterogeneous naturally originated and commercially available catalysts bentonite which contain at least 80 wt% of montmorillonite clay. It was designed selectively transform toxic organosulfur and organophosphorus CWAs into non-toxic products at mild conditions and shows negligible effect on health as well as on environment. It was also performed oxidative abetment of 2-chloroethyl ethyl sulphide (CEES), well known simulant of HD in presence of H<sub>2</sub>O<sub>2</sub> as an oxidant. Furthermore decontamination formulation was studied by mixing sodium perborate as an oxidant with iron bentonite. This study conceded a good decontamination test surface among CWAs and about 80% contaminated degradation within 24 hours under ambient conditions.</p><table-wrap id="table7" ><label><xref ref-type="table" rid="table7">Table 7</xref></label><caption><title> Physico-chemical properties of CWA simulants [<xref ref-type="bibr" rid="scirp.96919-ref55">55</xref>] [<xref ref-type="bibr" rid="scirp.96919-ref64">64</xref>] [<xref ref-type="bibr" rid="scirp.96919-ref70">70</xref>] [<xref ref-type="bibr" rid="scirp.96919-ref71">71</xref>]</title></caption><table><tbody><thead><tr><th align="center" valign="middle" >Acronym of CWA</th><th align="center" valign="middle" >V.p* (mmHg) at 25˚C</th><th align="center" valign="middle" >F.p* (C) &#177;2</th><th align="center" valign="middle" >B.p* (C) &#177;2</th><th align="center" valign="middle" >V.d* (air = 1)</th><th align="center" valign="middle" >M.W* (g/mol)</th><th align="center" valign="middle" >Volatility (mg/m<sup>3</sup>) at 25˚C</th><th align="center" valign="middle" >P.s* at 20˚C</th><th align="center" valign="middle" >Persistency</th></tr></thead><tr><td align="center" valign="middle" >HD</td><td align="center" valign="middle" >10</td><td align="center" valign="middle" >14.45</td><td align="center" valign="middle" >218</td><td align="center" valign="middle" >5.5</td><td align="center" valign="middle" >159.07</td><td align="center" valign="middle" >906</td><td align="center" valign="middle" >liquid</td><td align="center" valign="middle" >Persistent</td></tr><tr><td align="center" valign="middle" >GA</td><td align="center" valign="middle" >0.057</td><td align="center" valign="middle" >−50</td><td align="center" valign="middle" >248</td><td align="center" valign="middle" >5.6</td><td align="center" valign="middle" >162.13</td><td align="center" valign="middle" >497</td><td align="center" valign="middle" >liquid</td><td align="center" valign="middle" >Non-persistent</td></tr><tr><td align="center" valign="middle" >GB</td><td align="center" valign="middle" >2.48</td><td align="center" valign="middle" >−56</td><td align="center" valign="middle" >158</td><td align="center" valign="middle" >4.8</td><td align="center" valign="middle" >140.10</td><td align="center" valign="middle" >1.8 &#215; 104</td><td align="center" valign="middle" >liquid</td><td align="center" valign="middle" >Non-persistent</td></tr><tr><td align="center" valign="middle" >GD</td><td align="center" valign="middle" >0.40</td><td align="center" valign="middle" >−42</td><td align="center" valign="middle" >198</td><td align="center" valign="middle" >6.33</td><td align="center" valign="middle" >182.17</td><td align="center" valign="middle" >3.9 &#215; 102</td><td align="center" valign="middle" >liquid</td><td align="center" valign="middle" >Non-persistent</td></tr><tr><td align="center" valign="middle" >VX</td><td align="center" valign="middle" >0.0009</td><td align="center" valign="middle" >−51</td><td align="center" valign="middle" >292</td><td align="center" valign="middle" >9.2</td><td align="center" valign="middle" >267.37</td><td align="center" valign="middle" >10.5</td><td align="center" valign="middle" >liquid</td><td align="center" valign="middle" >Persistent</td></tr><tr><td align="center" valign="middle" >L</td><td align="center" valign="middle" >3.46</td><td align="center" valign="middle" >−1.2</td><td align="center" valign="middle" >196</td><td align="center" valign="middle" >7.1</td><td align="center" valign="middle" >207.32</td><td align="center" valign="middle" >3860</td><td align="center" valign="middle" >liquid</td><td align="center" valign="middle" >Persistent</td></tr></tbody></table></table-wrap><p>V.p* = Vapour pressure, F.p* = Freezing point B.p* = Boiling point, V.d* = Vapour density, M.W* = Molecular mass, P.s* = Physical state.</p><p>S. Abdul Majid et al. [<xref ref-type="bibr" rid="scirp.96919-ref94">94</xref>] (2018) reported sorption efficiency of mordenite versus zeolite-A on nitrate and phosphate. Sorption experiments were investigated between KH<sub>2</sub>PO<sub>4</sub>, NH<sub>4</sub>NO<sub>3</sub> on surface modified zeolite-A and mordenite. For sorption study batch equilibrium method was adopted. Experiment was performed at a range of pH 3, 5, 7, 9 and 11. The results obtained after investigation suggested that the sorption increases with increase in pH values from 3 to 7 and the equilibrium was attained after about 12 hs. It was also found that the sorption percentage increases when the temperature is raised up to 40. Theoretical studies have also implored for mordenite and results are compared with experimental data which helps to explain the respective relation with sorption capacity and efficiency of the ions.</p><p>Y. Liu et al. [<xref ref-type="bibr" rid="scirp.96919-ref95">95</xref>] (2018) the detoxification ability of flexible and breathable poly (m-phenylene isophthalamide) (PMIA) loaded with MgO nanoparticles was demonstrated by gas GC-MS. They found that after 20 h of reaction time approximately 70.56% of the mustard gas surrogates have been decomposed.</p><p>M. Florent et al. [<xref ref-type="bibr" rid="scirp.96919-ref96">96</xref>] (2017) reported an investigation on removal of chemical warfare agent (CWA) surrogates by highly porous carbon textiles. The surface morphology of modified carbon cloths was studied and found that the modified materials has capabilities to remove 2-chloroethyl ethyl sulfide (CEES) and diethyl sulfide (EES), two sulfur mustard gas simulants. The experiment was performed in vapor phase, which might be the circumstances of the real life arrangement of mustard gas. For investigation of reaction was carried out by FTIR, XRD, nitrogen adsorption isotherm, BET, potentiometric titration, TGA and GC-MS techniques. The degradation of CEES through hydrolysis and EES is adsorbed in the nylon’s amides framework network.</p><p>Li Jixiang et al. [<xref ref-type="bibr" rid="scirp.96919-ref97">97</xref>] (2017) reported novel efficient and cost-effective magnetic polymer composite macro particles with highly porous activated carbon carrier adsorbent (CsFeAC) was synthesized by using the sol-gel method. It was found that synthesized polymer composite have higher specific surface area and lower crystalinity which enhance the absorption capacity. Due to its higher capacity of adsorption towards Cu<sup>2+</sup> ions present in water causes a serious threat to the environment and human beings. In this study it was found the adsorption data match better with the Langmuir adsorption isotherm and it shows adsorption is a monolayer adsorption. Furthermore, kinetics studies show that the adsorption adopts the pseudo-second order kinetics.</p><p>M. Sadeghi et al. [<xref ref-type="bibr" rid="scirp.96919-ref98">98</xref>] (2016) in this study, zinc oxide nanoparticles (ZnO NPs) have been surveyed to decontaminate the chloroethyl phenyl sulfide (CEPS simulent of sulfur mustard) as a sulfur mustard agent simulant. Prior to the reaction, ZnO NPs were successfully prepared through sol-gel method in the absence and presence of polyvinyl alcohol (PVA). PVA was utilized as a capping agent to control the agglomeration of the nanoparticles. The formation, morphology, elemental component, and crystalline size of nanoscale ZnO were certified and characterized by SEM/EDX, XRD and FT-IR techniques. The proposed mechanism is given in <xref ref-type="fig" rid="fig1">Figure 1</xref>0.</p><p>M. St’astny et al. [<xref ref-type="bibr" rid="scirp.96919-ref99">99</xref>] (2016) used manganese (IV) oxide for degradation of toxic organophosphorus compounds which was prepared by homogeneous hydrolysis of KMnO<sub>4</sub> with 2-chloroacetamide. The degradation efficiency was determined with parathion methyl using HPLC and for comparative study, synthesized manganese (IV) oxides by direct method (reaction of MnSO<sub>4</sub>&#183;H<sub>2</sub>O and KMnO<sub>4</sub>, and reaction of KMnO<sub>4</sub> with urea in aqueous solution). The sample of KMnO<sub>4</sub> with 2-chloroacetamide showed the greatest degradation efficacy of about 90% within 2 h. Reaction mechanism shown in <xref ref-type="fig" rid="fig1">Figure 1</xref>1.</p><p>M. Sadeghi et al. [<xref ref-type="bibr" rid="scirp.96919-ref100">100</xref>] (2016) have been reported the performance of NiO NPs/Ag-clinoptilolite zeolite as a novel composite adsorbent for the decontamination of two most known sulfur mustard (nerve agent) simulants 2-chloroethyl ethyl sulfide (CEES) and dimethyl methyl phosphonate (DMMP). The reactions were carried out in both methanol and n-hexane solvents and monitored by GC-FID, 31P-NMR and GC-MS analyses subsequently. Moreover, the SEM/EDAX, XRD and FT-IR techniques were applied for characterization of prepared samples. The GC-FID results reveal that the composite material (NiO NPs/Ag-clinoptilolite zeolite) in normal hexane solvent shows excellent 86% decontamination in 12 h at room temperature toward CEES and 31P NMR data reveals that more than 89% decontamination of DMMP within 8 h was found at similar conditions. The calculated value of rate constant and half-life for CEES and DMMP was found 3.8194 &#215; 10<sup>−5</sup> s<sup>−1</sup>, 7.3055 &#215; 10<sup>−5</sup> s<sup>−1</sup> and 1.8640 &#215; 10<sup>4</sup> s<sup>−1</sup>, 9.4860 &#215; 10<sup>3</sup> s<sup>−1</sup> respectively. The product formed during hydrolysis i.e. hydroxyl ethyl ethylsulfide (HEES) and methyl phosphoric acid (MPA) was recognizing by GC-MS analysis.</p><p>A. Hiromichi et al. [<xref ref-type="bibr" rid="scirp.96919-ref101">101</xref>] (2016) reported synthesis of mordenite zeolite and its composite material using for toxic Cs ion decontamination. Reagents SiO<sub>2</sub> and NaAlO<sub>2</sub> used for synthesis without addition of a template and a seed powder. In this reaction, obtained mordenite contains Al/Si ratios 0.085:0.120 was found, at temperature range between 170˚C to 200˚C for 24 h. Initially Mordenite zeolite (1.0 g) show greater than 99% and 85% - 92% adsorption capacity for 100 ppm Cs<sup>+</sup> (100 mL) solutions of water and seawater respectively. The Cs<sup>+</sup> cation exchange capacity was found 180 - 210 cmol kg (centi moles of charge per kilogram) and it increases with varying Al/Si ratio. Furthermore for the magnetic collection composite material of the mordenite and magnetite of 10, 20 and 30 wt% was synthesized and tested for decontamination. It was observed that total Cs<sup>+</sup> ion decontamination rates were also high (more than 95%) by using the magnetic collection material after the Cs<sup>+</sup> adsorption in water. Mordenite zeolite has been found very effective adsorbent for radioactive Cs<sup>+</sup> ion decontamination because of high selectivity. The cation exchange capacity and the Cs<sup>+</sup> adsorption ability in seawater was found in good agreement compared to the synthesized mordenite from diatomite and the natural mordenite because of the low impurities for the material made from the chemical reagents.</p><p>K. Dastafkan et al. [<xref ref-type="bibr" rid="scirp.96919-ref102">102</xref>] (2015) reported 20 wt% MnO<sub>2</sub>NPs-AgY zeolite catalysts in different solvents for decontamination reactions of O,S-diethyl methyl phosphonothiolate (OSDEMP), as an agricultural organophosphorus pesticide. This reaction was studied by GC-FID and GC-MS techniques. The catalyst was synthesized in three different steps: in first step, Na-Y zeolite was prepared by hydrothermal method. In second step, by using ion exchange procedure Ag-Y zeolite was prepared from Na-Y zeolite. In final step, MnO<sub>2</sub>NPs were synthesized by doping of Ag-Y zeolite into manganese (II) nitrate solution. The confirmation of the synthesized material and nanocomposite catalyst was characterized through SEM, XRD, AAS and FTIR spectroscopy techniques. In this study it was found MnO<sub>2</sub>NPs-AgY zeolite composite catalyst (20 wt%) has capacity to convert OSDEMP into a less toxic or non-toxic product. Adsorption, degradation and hydrolysis reactions were studded in different solvents and time intervals at normal temperature and pressure conditions. The procedure for reaction was given in <xref ref-type="fig" rid="fig1">Figure 1</xref>2 and reaction mechanism is shown in <xref ref-type="fig" rid="fig1">Figure 1</xref>3. This study concludes synthesized 20 wt% MnO<sub>2</sub>NPs-AgY zeolite nanocomposite has greater decontamination efficiency towards OSDEMP molecule and it was also found that OSDEMP molecule was perfectly decontaminated (100%) in n-heptanes solvent after 8 hours.</p><p>V. V. Singh et al. [<xref ref-type="bibr" rid="scirp.96919-ref103">103</xref>] (2015) reported CWAs (diethyl chlorophosphate) and BWAs (against E. coli bacteria) detoxification by using silver-exchanged zeolite (AgZ) micromotors. Such multifunctional reactive Ag-zeolite micro-motors are highly efficient on-the-fly for detoxification strategy of chemical and biological threats under ambient conditions. The synthesized new Ag-zeolite micro motor was very much effective towards detoxification of CWAs. The combination of Ag-zeolite micromotors catalyst reflects effective adsorption capacity due to embedded Ag<sup>+</sup> ion and the dynamic moment behavior of the micro motors. The synthesized Ag-zeolite micro motors have a specific function and its components are useful practically sustainable, economical, and eco-friendly. All the studies clearly indicated that the presence of micropores and high surface area of the zeolite facilitate the adsorption of DCP molecules within it. Also the presence of Ag<sup>+</sup> (also have antibacterial activity) leads to stronger interactions and accelerated chemisorptions process. The mechanism of this process is shown in <xref ref-type="fig" rid="fig1">Figure 1</xref>4. These properties and capabilities of zeolite micro motors make it advantageous over recently developed motors and lead to detoxification and to green degradation products.</p><p>J.P. Kumar et al. [<xref ref-type="bibr" rid="scirp.96919-ref104">104</xref>] (2015) synthesized and compared degrading ability (HD gas) of eight different metal oxides (i.e. MgO, CaO, NiO, CuO, Ag<sub>2</sub>O, MnO<sub>2</sub>, CeO<sub>2</sub> and Fe<sub>2</sub>O<sub>3</sub>) and doped with 13-X zeolite. Zeolites were characterized by the help of XRD, TEM and SEM-EDAX while the decontamination reactions were studied by the help of GC and GC-MS. TEM images depicted different shapes of various MO<sub>X</sub>-13X materials. Nanorods in case of NiO-13X while nanobelts in MnO<sub>2</sub>-13X and MgO-13X. XRD graph patterns showed no changes in crystal structure of zeolite by doping with metal oxides. It was also found that surface area has decreased after doping with metal oxide nano-particles and shows better reactivity against decontamination of HD. This is due to blocking of micropores which cause the decrease of micropore volume. The data in <xref ref-type="table" rid="table8">Table 8</xref> shows decontamination efficiency. Maximum efficiency was shown by Ag<sub>2</sub>O-13X which degraded 100% of HD gas in 16 h.</p><table-wrap id="table8" ><label><xref ref-type="table" rid="table8">Table 8</xref></label><caption><title> List of Nanoparticals used as decontamination material</title></caption><table><tbody><thead><tr><th align="center" valign="middle" >Synthesized Nanoparticles</th><th align="center" valign="middle" >Time</th><th align="center" valign="middle" >Decontamination of HD (%)</th></tr></thead><tr><td align="center" valign="middle" >CaO-13X, MnO<sub>2</sub>-13X, MgO-13X</td><td align="center" valign="middle" >48 h</td><td align="center" valign="middle" >100</td></tr><tr><td align="center" valign="middle" >NiO-13X</td><td align="center" valign="middle" >48 h</td><td align="center" valign="middle" >95.8</td></tr><tr><td align="center" valign="middle" >CeO<sub>2</sub>-13X</td><td align="center" valign="middle" >48 h</td><td align="center" valign="middle" >94.5</td></tr><tr><td align="center" valign="middle" >CuO-13X</td><td align="center" valign="middle" >48h</td><td align="center" valign="middle" >94.3</td></tr><tr><td align="center" valign="middle" >Fe<sub>2</sub>O<sub>3</sub>-13X</td><td align="center" valign="middle" >48 h</td><td align="center" valign="middle" >92.2</td></tr><tr><td align="center" valign="middle" >Na-13X</td><td align="center" valign="middle" >48 h</td><td align="center" valign="middle" >66</td></tr><tr><td align="center" valign="middle" >Ag<sub>2</sub>O-13X</td><td align="center" valign="middle" >16 h</td><td align="center" valign="middle" >100</td></tr></tbody></table></table-wrap><p>This unusual efficiency of silver oxide has been explained. Silver ion abstracts chloride ion from HD gas and thus convert it into its degraded products. It was found that silver ion possess relatively higher affinity towards sulfur atom of HD as compared to other metal ions. GC-MS has confirmed that on bare Na-13X zeolite only hydrolysis reaction takes place on its surface while in MO<sub>X</sub>-13X materials have elimination as well as hydrolysis reactions. Reaction of HD on Na-13X results the formation of HM (hemisulfur mustard) and TDG (thiodiglycol) products. While on reaction with MO<sub>X</sub>-13X materials, six different products (1,4-oxathiane, chloroethyl vinyl sulfide, hydroxyl ethyl vinyl sulfide, HM, TDS and divinyl sulfide) were formed. Proposed mechanism is shown in <xref ref-type="fig" rid="fig1">Figure 1</xref>5.</p><p>M. Sadeghi et al. [<xref ref-type="bibr" rid="scirp.96919-ref91">91</xref>] (2014) have synthesized MnO<sub>2</sub>-AgX zeolite nanocomposites. It was a novel adsorbent catalyst for the decontamination against 2-CEPS and 2-CEES (sulfur mustard simulants). The reaction mechanism for the decontamination of Sulfur mustard simulants are shown in <xref ref-type="fig" rid="fig1">Figure 1</xref>6(a) and <xref ref-type="fig" rid="fig1">Figure 1</xref>6(b). Crystalline size and morphology were explained with the help of SEM, AAS, GC-FID, GC-MS and GC analysis. Above characterization techniques reveals that the amounts of silver (10.3 wt%) and manganese (18.4 wt%) were sufficient for complete decontamination (100%) within 12 h and changes these toxic simulants into non toxic products.</p><p>W. A. Khanday et al. [<xref ref-type="bibr" rid="scirp.96919-ref105">105</xref>] (2014) reported the adsorption of dimethyl methyl phosphonate (DMMP) over synthetic zeolite-α. It was observed that initially adsorption of DMMP was found to be high and then it decreases with an increase in the injection volume. Thus adsorption rate was increases with increase in the contact time between zeolite-α and DMMP. The reaction mechamism is shown in <xref ref-type="fig" rid="fig1">Figure 1</xref>7. Zeolite-α shows equilibrium time up to 8 h and after reaching equilibrium, the adsorption rate become almost constant. Further desorption experiment was performed and completed successfully the data demonstrate that desorption exhibit from both strong and weak adsorption sites.</p><p>W. A. Khanday et al. [<xref ref-type="bibr" rid="scirp.96919-ref106">106</xref>] (2013) have been reported that Zeolite-A, Zeolite-X, MCM-22 and Erionite were synthesized by hydrothermal methods and were characterized successfully by X-ray diffraction (XRD), Fourier transform infrared (FTIR) spectroscopy, scanning electron microscopy (SEM), Brunauer-Emmett-Teller (BET) surface area analysis, energy dispersive spectroscopy (EDS) and thermal programmed desorption (TPD). The adsorption of dimethyl methyl phosphate (DMMP) was performed on these synthesized zeolites. The adsorption data demonstrated that highest surface area among all zeolites was shown by Zeolite-X and having highest adsorption capacity followed by Erionite and MCM-22 whereas Zeolite-A shows the least surface area and having least adsorption capacity. On comparing the surface area of synthesized zeolite the order of increasing surface area was found: Zeolite-X &gt; Erionite &gt; MCM-22 &gt; Zeolite-A. In this study it was also found that initially adsorption rate was found to be high for all zeolites and then it decreases with increase in injected volume. Further desorption study was carried out successfully and two types of desorption pattern peaks were observed. The sharp peaks of desorption pattern representing desorption of physisorbed DMMP and broad peaks representing desorption of strongly chemisorbed DMMP. The mechanism of reaction is shown in <xref ref-type="fig" rid="fig1">Figure 1</xref>8.</p><p>S. L. Sharifi Alhashem et al. [<xref ref-type="bibr" rid="scirp.96919-ref107">107</xref>] (2012) have been investigated decontamination of diethyl methyl phosphonate (DEMP,) and 2-chloroethyl phenyl sulfide (CEES) (simulent of Sulphur mustard, HD) by using nano-MnO<sub>2</sub>/Zeolite AgY composite. It was found that, in first case 2-CEPS was produced about 86% by composite after 24 h, and it changed to less toxic chemical products <xref ref-type="fig" rid="fig1">Figure 1</xref>9(b) and in second case absorption of DEMP was found nearly 87% after 30 h <xref ref-type="fig" rid="fig1">Figure 1</xref>9(a). Results are identified by GC-MS and proton NMR respectively.</p><p>R. Satya Agarwal et al. [<xref ref-type="bibr" rid="scirp.96919-ref92">92</xref>] (2012) have been reported the detoxification of Paraoxon (simulent of sarin, nerve agent) by functionalized cellulose/ PET polymer/ zeolites (Linde type A and Mordenite). The stimulant paraoxon detoxification studies by functionalized membranes were successfully obtained.</p><p>The prepared paraoxon stock solution shows UV absorbance value at 6.8 nm. After adding prepared functionalized cellulose/PET polymer/zeolites fibers to stock solution of paraoxon, a decrease in the UV absorbance value of paraoxon solution was observed within time interval of 15 min and 1 hour. This decrease in the UV absorbance value shows that the catalyst containing nanofibers has the capacity to detoxifying harmful agent like organophosphorous. This concludes, functionalized cellulose/PET polymer/zeolites are tested for the decontamination of nerve agent simulant Paraoxon, and stimulant gets hydrolyzed. The rates of hydrolysis for different organophosphate hydrolyzing agents are compared and it was found that the reactivity and amount of adsorption of these catalysts are of higher.</p><p>J. Zhang et al. [<xref ref-type="bibr" rid="scirp.96919-ref108">108</xref>] (2012) have studied the effects of Surface and morphological properties and impedance change on zeolite (NaY) and cerium oxide coating zeolite material towards DMMP (dimethyl methyl phosphonate). Comparative study of three zeolite sensors including pure NaY zeolite based, NaY coated with 30% CeO<sub>2</sub> and 3 &#181;m films was used for detection of ~100 ppm DMMP at 320˚C at fixed frequency of 3 kHz. On increasing the concentrations of CeO<sub>2</sub>, impedance remained unchanged but response time was increased. It was found that membrane of zeolite based material show greater response in comparison to the pressed pellets of NaY and CeO<sub>2</sub>-coated NaY. Finally it has reported that cerium oxide coating can successfully improve the recovery feature of the sensors, leading to desorption of DMMP.</p><p>Y.C Hudiono et al. [<xref ref-type="bibr" rid="scirp.96919-ref109">109</xref>] (2012) a new composite material was synthesized which act as highly breathable barrier material against mustard agent simulant (2-CEES). This composite material consists of two components: diol-RTIL polymer (a cross linked diol-functionalized room temperature ionic liquid polymer) and zeolite (NaY). The hydroxylated polymer component renders high water vapor penetrability whereas the basic zeolite renders reactive blocking of CEES vapor.</p><p>Ji. Xinming et al. [<xref ref-type="bibr" rid="scirp.96919-ref110">110</xref>] (2011) have reported adsorption-desorption behavior of Nanozeolites i.e. silicate-1, ZSM and Cu-ZSM-5 as adsorbent for DMMP (Dimethyl Methyl phosphonate). It has been found that Cu-ZSM-5 had highest adsorption capacity and best selectivity due to increase in proportion to copper content. The sensitivity and detection limit was observed with Cu-ZSM-5 about 8.8 Hz/ppm and 0.3 ppm, respectively, which confirm that zeolite Cu-ZSM-5 is good adsorbent for the detection of DMMP. The maximum adsorption capacity of Cu-ZSM was found when the copper content was more than 2.72%.</p><p>B. Nazari et al. [<xref ref-type="bibr" rid="scirp.96919-ref111">111</xref>] (2010) have been reported comparative study of MgO particles synthesized in laboratory and technical grade. The method of synthesis was used very easier and effective. The ability of different types of MgO particles for the destruction of chemical warfare agents (CWA) simulants malathion (VX simulant) and DMMP (GB simulant). In this investigation it was found that the weight ratios of 1:16 and 1:32 (stimulant: MgO particles) decompose almost all of the CWA simulants. It was also found that the weight ratio of 1:32 could destroy the other destruction products. The characterization techniques UV-Vis and BET used for investigation. BET analysis showed that specific surface area (SSA) of the synthesized MgO particles and technical grade of MgO powders was found ~30.96 m<sup>2</sup>/g and ~166.86 m<sup>2</sup>/g respectively and synthesized MgO particles and technical grade of MgO powders had an average particle size of 75 nm and 20 micrometers, respectively. This study concludes that MgO particles showed a greater potential in the destruction of simulants of chemical warfare agents with a simple and low cost effective method.</p><p>L. Bromberg et al. [<xref ref-type="bibr" rid="scirp.96919-ref90">90</xref>] (2009) reported the compound PANOx and PHA were very reactive and obtained by one-step oximation of polyacrylonitrile and polyacrylamide, respectively. Synthesized compound polyacrylamidoxime (PANOx) and poly (N-hydroxyacrylamide) (PHA) shows nucleophilic hydrolysis towards chemical warfare agents (CWA) S-2-(diisopropylamino) ethyl O-ethyl methylphosphonothioate (VX), O-pinacolyl methylphosphonofluoridate (Soman, or GD), and isopropyl methylphosphonofluoridate (Sarin, or GB). The specific synthesized polymers (PANOx and PHA) were converted into their corresponding oximate salts which have greater pH values than the pKa i.e. 7.5 and 10.8 respectively. The synthesized PANOx and PHA showed spontaneous hydrolysis at moderate temperature and humidity. The conversion of the hydroxamate into the unreactive carboxylic groups was insignificant, so that the polymers maintained reactivity at mild conditions. The half-lives of VX in heterogeneous hydrolysis were measured in the presence of PANOx and PHA from 0.093 to 4.3 and 7.7 h, which obey pseudo-first order kinetics in the polymer dispersions. The rates of hydrolysis of PANOx towards VX exhibited a strong dependency on the degree of conversion of the amidoxime to amidoximate groups and in case of GB half-life was found less than 3 min. The nontoxic nature, greater catalytic efficiency and mode of synthesis for PANOx and PHA polymers make them attractive materials in decontamination. The degradation pathway is shown in <xref ref-type="fig" rid="fig2">Figure 2</xref>0(a) and <xref ref-type="fig" rid="fig2">Figure 2</xref>0(b). This study concludes the compounds PANOx and PHA are obtained by a simple oximation method with high yields and contain 3 - 10 mmol of reactive groups (amidoximate or hydroxamate) per gram of dry polymer.</p><p>In the presence of water, PANOx and PHA hydrolyzed GD and VX with great interest having half lives shorter than those in alkaline water. Due to simplicity in synthetic process, low cost of the precursor and greater degradation efficiency makes PANOx and PHA attractive in today’s scenario.</p><p>H. Grassian et al. [<xref ref-type="bibr" rid="scirp.96919-ref7">7</xref>] (2008) has reported the degradation of DMMP (dimethyl methyl phosphate, simulant of Sarin) nerve agents and 2-CEES (2-chloroethyl ethyl sulphate, simulant of sulfur mustard) blister agents by using three different nanocrystalline zeolites i.e. NaY, NaZSM-5 and silicalite. Nanocrystalline NaZSM-5 was found better degradent than the other two zeolites. It was found that CEES was decomposed by all the three zeolites (NaZSM-5, silicalite and NaY zeolite) whereas DMMP was degraded by only NaY zeolite. The adsorption was monitored by flow reactor apparatus and thermal conductivity detector (TCD) of GC. NaZSM-5 shows greater reactivity than silicalite. 20% more 2-CEES was adsorbed on its surface as compared to silicalite.</p><p>A. Kilincarslan et al. [<xref ref-type="bibr" rid="scirp.96919-ref112">112</xref>] (2007) reported synthesized PAN/zeolite composite has good adsorption capacity towards Th(IV) from aqueous solutions by using a batch technique. The parameters use for thorium adsorption was studied as pH, concentration, shaking time and temperature. The interpreted data fit into Langmuir, Freundlich and D-R type adsorption and desorption isotherms. In this study it was found with hydrochloride acid solution, desorption of Th(IV) is very slow and percent for this adsorbent was only found 14.48%. As a result of this, creating different chemical forms of Th(IV) with some components of the composite adsorbent and investigated the adsorption process. This study concludes that adsorbent is low cost and very effective sorbent for Th(IV) ions and the synthesized PAN/zeolite composite adsorbent exhibited excellent adsorption for Th(IV).</p><p>K. Knagge et al. [<xref ref-type="bibr" rid="scirp.96919-ref113">113</xref>] (2006) have been reported the thermal degradation of nerve agent simulant dimethyl methylphosphonate (DMMP) by using Nanocrystalline NaY. 31P MAS NMR study reported the formation of two non toxic phosphorus species i.e. DMP and HMPA. After complete thermal decomposition of DMMP, the disappearance of all these products with the exception of some strongly adsorbed phosphate species was observed. Adsorption and thermal reaction of DMMP in Nanocrystalline NaY with a crystal size of ∼30 nm. DMMP adsorbs molecularly in nanocrystalline NaY at 25˚C. The FTIR spectroscopy of Gas-phase products of the reaction of DMMP and oxygen in Nanocrystalline NaY at 200˚C was carried out and determined to be carbon dioxide (major product), formaldehyde, and dimethyl ether as products. The reactivity ratio per gram of zeolite sample was comparable to other recent studies of metal oxides like MgO, Al<sub>2</sub>O<sub>3</sub> and TiO<sub>2</sub>. The reaction mechanism is shown in <xref ref-type="fig" rid="fig2">Figure 2</xref>1.</p><p>W. George et al. [<xref ref-type="bibr" rid="scirp.96919-ref114">114</xref>] (1999) investigate the reactions of synthesized zeolites NaY and AgY with CW Agent VX, HD and their simulants DEPPT (O,S-diethyl phenylphosphonothioate) and CEPS (2-chloroethyl phenyl sulfide) at room temperature. The reaction mechanisms are shown in <xref ref-type="fig" rid="fig2">Figure 2</xref>2(a) and <xref ref-type="fig" rid="fig2">Figure 2</xref>2(b). NMR techniques (solid-state magic angle spinning) were used to study the reaction.</p><p>VX molecules undergo hydrolysis with NaY and AgY zeolites and ultimately cleavage of the P-S to yield EMPA (ethyl methylphosphonate) which was slowly convert into ethyl 2-(diisopropylamino)ethyl methylphosphonate. Similar reaction was observed for DEPPT on AgY and silver salt of ethyl phenylphosphonate was observed but DEPPT does not show reaction with NaY. Hence AgY catalyzed hydrolysis reaction was more appropriate for both VX and DEPPT. In Case of HD and CEPS the reactivity of NaY was more as compare to AgY and formed Toxic CH-TG sulfonium ion and non toxic HEPS (2-hydroxyethyl phenyl sulfide) product respectively. In Case of VX hydrolysis of the P-O bond was not observed on either AgY or NaY and the desulfurized by-product yield was found 78%.</p></sec><sec id="s8"><title>8. Conclusion</title><p>The bluff of terrorist attacks and environmental hazards has drawn attention of research scientists towards study of CWA and their simulants. The number of papers was comprised in this review related to decontamination study of CWA and simulants of CWA. Zeolite materials, metal oxides and composites of zeolites due to their readily availability, user-friendly and eco-friendly nature have been the subjects of such studies, and various zeolite materials have been investigated in this regard. Nano-technology could also open a new window for serial formulations with intensify advantages like high surface area, high ion exchange capacity and high surface to volume ratio towards CWA. Nanoscale zeolite are</p><p>more effective because of the presence of large surface area and pore volumes, low crystal defects, high ion exchange capacity etc. The products of degradation of CWA simulants on zeolite nanosurfaces have been examined experimentally. The correlation between the results for the real agents and their simulant implies that experiments performed with the simulant can be extrapolated to understand the mechanism for the real agents. Though large number of experimental results regarding the adsorption and degradation/decontamination of CWA on nanoscale zeolite and their simulants has accumulated over the years, this work has to be done to find materials for the early detection and degradation/decontamination of CWAs as well its simulants. In particular, large porous size and surface area zeolite and doped zeolite nanoparticles need to be explored further, as they have shown promise as future materials for CWA adsorption and degradation. Further research is necessary to determine the yet undetermined parameters like adsorption behaviour and mechanisms in zeolite-composite reactions.</p></sec><sec id="s9"><title>Conflicts of Interest</title><p>Conflict of interest on behalf of all co-authors, the corresponding author states that this article content has no conflict of interest.</p></sec><sec id="s10"><title>Acknowledgements</title><p>I acknowledge all the co-authors of this article particularly my mentor for supporting me to make this review paper possible.</p></sec><sec id="s11"><title>Cite this paper</title><p>Kumar, N., Tiwari, K.R., Meenu, Km., Sharma, A., Jain, A., Singh, S. and Tomar, R. (2019) Utilization of Various Analogy of Synthetic Nanoporous Zeolites and Composite of Zeolites for Decontamination/Detoxification of CWA Simulants—An Updated Review. International Journal of Nonferrous Metallurgy, 8, 35-71. https://doi.org/10.4236/ijnm.2019.84004</p></sec></body><back><ref-list><title>References</title><ref id="scirp.96919-ref1"><label>1</label><mixed-citation publication-type="other" xlink:type="simple">Gangele, R., Pawaiya, P. and Pandey, Y. (2014) Synthetic Zeolites-Structure Properties and Application Area. International Journal of Scientific Research, 3, 78.</mixed-citation></ref><ref id="scirp.96919-ref2"><label>2</label><mixed-citation publication-type="other" xlink:type="simple">Breck, D.W. (1974) Zeolite Molecular Sieves: Structure, Chemistry and Use. 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