<?xml version="1.0" encoding="utf-8"?>
<XML>
<JOURNAL>
<YEAR>1399</YEAR>
<VOL>7</VOL>
<NO>3</NO>
<MOSALSAL>28</MOSALSAL>
<PAGE_NO>375</PAGE_NO>


<ARTICLES>

	<ARTICLE> 
		<TitleF>مطالعه کارایی فرایند فوتوکاتالیستی با استفاده از نانوکاتالیست مغناطیسیFe3O4@SiO2@TiO2  در حذف آنتی بیوتیک سفتریاکسون از محلول‌های آبی</TitleF>
		<TitleE>Evaluation of the efficiency of a photocatalytic process using the magnetic nanocatalyst (Fe3O4@SiO2@TiO2) in the removal of ceftriaxone from aqueous solutions</TitleE>
		<TitleLang_ID>1</TitleLang_ID>
		<ABSTRACTS>
			<ABSTRACT>
			<Language_ID>1</Language_ID>
			<CONTENT>زمینه و هدف: آنتی بیوتیک سفتریاکسون به طور گسترده&#8204;ای برای درمان عفونت های مختلف استفاده می&#8204;شود که در آب و فاضلاب انباشته شده و ممکن است مسائل زیست محیطی و بهداشتی ایجاد کند. هدف از این مطالعه بررسی کارایی استفاده از فرآیند فوتوکاتالیستی (Fe3O4@SiO2@TiO2) در حذف سفتریاکسون از محلول&#8204;های آبی بوده است.
مواد و روش&#173;ها: این مطالعه از نوع مطالعات تجربی- کاربردی می&#173;باشد. به&#8204;منظور سنتز نانو ذرات Fe3O4@SiO2@TiO2 از روش سل ژل استفاده گردید و با استفاده از آنالیز های SEM، XRD&#160; وEDX خصوصیات کاتالیست بررسی گردید. اثر متغیر&#8204;ها شامل pH، غلظت کاتالیست، غلظت سفتریاکسون، زمان تماس و آزمایش بازیافتی (7 مرتبه)، تعیین میزان معدنی سازی مورد بررسی قرار گرفت. غلظت باقیمانده سفتریاکسون توسط دستگاه HPLC در طول موج 240 نانومتر تعیین شد.
یافته&#8204;ها: طبق نتایج به&#8204;دست&#8204;آمده در این مطالعه بـالاترین کـارایی فرآینـد در غلظت سفتریاکسون 10 میلی گـرم در لیتر، pH برابر 3 و مقـدار کاتالیسـت برابـر 2 گرم بر لیتر در مـدت زمان 120 دقیقه به میزان 7/96 درصد بـه دسـت آمـد. نتایج نشان داد که حذف سفتریاکسون به&#8204;وسیله این فرآیند از مدل سینتکی درجه اول تبعیت می&#8204;نماید. میزان معدنی سازی پس از پایان زمان واکنش 7/83 درصد تعیین گردید. قابلیت استفاده مجدد کاتالیست تا 7 مرتبه با کاهش راندمان حدود 2/5 درصد را داراست.
نتیجه&#8204;گیری: نتایج به دست آمده نشان داد که فرآیند فوتوکاتالیستی با استفاده از نانوکاتالیست مغناطیسی Fe3O4@SiO2@TiO2&#160; می&#8204;تواند یک روش موثر در حذف سفتریاکسون از محیط&#8204;های آبی باشد.</CONTENT>
			</ABSTRACT>
			<ABSTRACT>
			<Language_ID>2</Language_ID>
			<CONTENT>Background &#38; Objectives: Ceftriaxone is an antibiotic which is extensively used to treat a number of various infections. It is mainly accumulated in water and sewage resulting in the environmental and health problems. This study is centered on the evaluation of the efficiency of a photocatalytic process using Fe3O4@SiO2@TiO2 in the removal of ceftriaxone from aqueous solutions.
Methods: This research was based on an experimental-practical study.&#160; Fe3O4 @ SiO2 @ TiO2 was initially synthesized via a sol-gel method and characterized by SEM, XRD and EDX analyses. The effects of variables such as pH, catalyst concentration, ceftriaxone concentration, contact time, reusability tests (n=7) and degree of mineralization were separately assessed in a laboratory scale. The concentration of ceftriaxone was measured by HPLC at 240 nm.
Results: Based on the results obtained, the highest process efficiency of 96.7% was obtained under the following optimal conditions: concentration of ceftriaxone 10 mg/L, pH=3, the catalyst dosage of 2 g/L and a time contact of 120 min. At the end of the process, the degree of mineralization was determined to be 83.7%. Additionally, the data regarding the reusability of the nanocatalyst demonstrated that a 5.2% loss in the removal efficiency was observed after 7 times of reuse. Finally, the results revealed that the removal process of ceftriaxone follows the first-order kinetic model.
Conclusion: The results demonstrated that the photocatalytic process using the magnetic nanocatalyst (Fe3O4 @ SiO2 @ TiO2) could be effectively used for the removal of ceftriaxone from aqueous media.</CONTENT>
			</ABSTRACT>
		</ABSTRACTS>

		<PAGES>
			<PAGE>
			<FPAGE>229</FPAGE>
			<TPAGE>243</TPAGE>
			</PAGE>
		</PAGES>

		<RECEIVE_DATE>
			2020/05/13
		</RECEIVE_DATE>

		<RECEIVE_DATE_FA>
			1399/2/24
		</RECEIVE_DATE_FA>

		<ACCEPT_DATE>
			2020/05/13
		</ACCEPT_DATE>

		<ACCEPT_DATE_FA>
			1399/2/24
		</ACCEPT_DATE_FA>

		<AUTHORS>
			<AUTHOR>
				<Name>حمیدرضا</Name>
				<MidName></MidName>
				<Family>صبحی</Family>
				<NameE>Hamid Reza</NameE>
				<MidNameE></MidNameE>
				<FamilyE>Sobhi</FamilyE>
				<Organizations>
				<Organization>استادیار، گروه شیمی، دانشگاه پیام نور، تهران، ایران</Organization>
				</Organizations>
				<Countries>
				<Country>ایران</Country>
				</Countries>
				<EMAILS>
				<Email></Email>
				</EMAILS>
			</AUTHOR>

			<AUTHOR>
				<Name>مجتبی</Name>
				<MidName></MidName>
				<Family>یگانه بادی</Family>
				<NameE>Mojtaba</NameE>
				<MidNameE></MidNameE>
				<FamilyE>Yegane Badi</FamilyE>
				<Organizations>
				<Organization>کارشناسی ارشد مهندسی بهداشت محیط، دانشکده بهداشت محیط، دانشگاه علوم پزشکی ایران، تهران، ایران</Organization>
				</Organizations>
				<Countries>
				<Country>ایران</Country>
				</Countries>
				<EMAILS>
				<Email></Email>
				</EMAILS>
			</AUTHOR>

			<AUTHOR>
				<Name>علی</Name>
				<MidName></MidName>
				<Family>اسرافیلی</Family>
				<NameE>Ali</NameE>
				<MidNameE></MidNameE>
				<FamilyE>Esrafili</FamilyE>
				<Organizations>
				<Organization>دانشیار گروه مهندسی بهداشت محیط، دانشکده بهداشت، دانشگاه علوم پزشکی ایران، تهران، ایران</Organization>
				</Organizations>
				<Countries>
				<Country>ایران</Country>
				</Countries>
				<EMAILS>
				<Email></Email>
				</EMAILS>
			</AUTHOR>

			<AUTHOR>
				<Name>مهناز</Name>
				<MidName></MidName>
				<Family>قنبریان</Family>
				<NameE>Mahnaz</NameE>
				<MidNameE></MidNameE>
				<FamilyE>Ghambarian</FamilyE>
				<Organizations>
				<Organization>استادیار گروه پژوهشی صنایع شیمیایی معدنی، پژوهشکده توسعه صنایع شیمیایی جهاد دانشگاهی، البرز، ایران</Organization>
				</Organizations>
				<Countries>
				<Country>ایران</Country>
				</Countries>
				<EMAILS>
				<Email></Email>
				</EMAILS>
			</AUTHOR>
		</AUTHORS>


		<KEYWORDS>
			<KEYWORD>
				<KeyText>Photocatalyst</KeyText>
			</KEYWORD>

			<KEYWORD>
				<KeyText>Magnetic nanoparticles</KeyText>
			</KEYWORD>

			<KEYWORD>
				<KeyText>UV-light</KeyText>
			</KEYWORD>

			<KEYWORD>
				<KeyText>Ceftriaxone</KeyText>
			</KEYWORD>

			<KEYWORD>
				<KeyText>فوتوکاتالیست</KeyText>
			</KEYWORD>

			<KEYWORD>
				<KeyText>نانوذرات مغناطیسی</KeyText>
			</KEYWORD>

			<KEYWORD>
				<KeyText>نور UV</KeyText>
			</KEYWORD>

			<KEYWORD>
				<KeyText>سفتریاکسون</KeyText>
			</KEYWORD>
		</KEYWORDS>

		<REFRENCES>
			<REFRENCE>
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J Colloid Interf Sci 2018;523: 7-17.##6.	Li D, Guo X, Song H, et al. Preparation of RuO2-TiO2/Nano-graphite composite anode for electrochemical degradation of ceftriaxone sodium. J Hazard Mater 2018;351: 250-9.##7.	Palanduz A, Yalçın I, Tonguç E, et al. Sonographic assessment of ceftriaxone‐associated biliary pseudolithiasis in children. J Clin Ultrasound 2000;28(4): 166-8.##8.	Fadaei A, Mohammadi Mf, Mardani G. Efficiency of Advanced H2O2/ZnO Oxidation Process in Ceftriaxone Antibiotic Removal from Aqueous Solutions. Water Wastewater 2017;28(5):39-47. [In Persian]##9.	Zamani M. 4 antibiotics between 10 drugs with high use in Iran. Sepid J 2008;1(5): 2-3. [In Persian]##10.	Diwan V, Tamhankar AJ, Aggarwal M, et al. Detection of antibiotics in hospital effluents in India. Curr Sci 2009: 1752-5.##11.	Zuccato E, Calamari D, Natangelo M, Fanelli R. Presence of therapeutic drugs in the environment. Lancet 2000;355(9217): 1789-90.##12.	Onyango MS, Kojima Y, Aoyi O, et al. Adsorption equilibrium modeling and solution chemistry dependence of fluoride removal from water by trivalent-cation-exchanged zeolite F-9. J Colloid Interf Sci 2004;279(2):341-50.##13.	Oller I, Malato S, Sánchez-Pérez J. Combination of advanced oxidation processes and biological treatments for wastewater decontamination—a review. Sci Total Environ 2011;409(20):4141-66.##14.	Arabzadeh H, Farzadkiya M, Esrafily A, et al. Efficiency of Catalytic Ozonation by MgO Nanoparticles to Remove Ceftriaxone from Aqueous Solution.  Water Wastewater 2018;29(1):60-9. [In Persian]##15.	Xu J, Ao Y, Fu D, Yuan C. Low-temperature preparation of anatase titania-coated magnetite. J Phys Chem Solids 2008;69(8):1980-4.##16.	Homem V, Santos L. Degradation and removal methods of antibiotics from aqueous matrices–a review. J Environ Manage 2011;92(10):2304-47.##17.	Yegane Badi M, Dehghanifard E. Study of the Efficiency of Non-Homogeneous Catalytic Ozonation Process using a Catalyst of Magnetic Nanoparticles of Iron Oxide Doped with Silica and Titanium Dioxide in Removal of Metronidazole from Synthetic Wastewater. J Environ Health Eng 2018;5(4):323-36. [In Persian]##18.	Esrafili A, Khosravi S, Gholami M, et al. Photocatalytic Removal of Metronidazole Using Magnetic TiO2 Nanocatalyst (Fe3O4@SiO2@TiO2): Synthesis, Characterization, and Operational Parameters. J Mazandaran U Med Sci 2018;28(159):97-115. [In Persian]##19.	Khorsandi H, Teymori M, Aghapour AA, et al. Photodegradation of ceftriaxone in aqueous solution by using UVC and UVC/H 2 O 2 oxidation processes. Appl Water Sci 2019;9(4):81.##20.	Badi MY, Azari A, Pasalari H, et al. Modification of activated carbon with magnetic Fe3O4 nanoparticle composite for removal of ceftriaxone from aquatic solutions. J Mol Liq 2018;261:146-54.##21.	Tian H, Liu F, He J. Multifunctional Fe 3 O 4@ nSiO 2@ mSiO 2–Fe core–shell microspheres for highly efficient removal of 1, 1, 1-trichloro-2, 2-bis (4-chlorophenyl) ethane (DDT) from aqueous media. J Colloid Interf Sci 2014;431:90-6.##22.	Kurtan U, Baykal A. Fabrication and characterization of Fe 3 O 4@ APTES@ PAMAM-Ag highly active and recyclable magnetic nanocatalyst: Catalytic reduction of 4-nitrophenol. Mater Res Bull 2014;60:79-87.##23.	Legube B, Leitner NKV. Catalytic ozonation: a promising advanced oxidation technology for water treatment. Catal Today 1999;53(1):61-72.##24.	Wang N, Li X, Wang Y, et al. Evaluation of bias potential enhanced photocatalytic degradation of 4-chlorophenol with TiO2 nanotube fabricated by anodic oxidation method. Chem Eng J 2009;146(1):30-5.##25.	Daghrir R, Drogui P, El Khakani MA. Photoelectrocatalytic oxidation of chlortetracycline using Ti/TiO2 photo-anode with simultaneous H2O2 production. Electrochim Acta 2013;87:18-31.##26.	Yang S, Fu H, Sun C, Gao Z. Rapid photocatalytic destruction of pentachlorophenol in F–Si-comodified TiO2 suspensions under microwave irradiation. J Hazard Mater 2009;161(2-3):1281-7.##27.	Wang S-G, Liu X-W, Zhang H-Y, et al. Aerobic granulation for 2, 4-dichlorophenol biodegradation in a sequencing batch reactor. Chemosphere 2007;69(5):769-75.##28.	Yu C-H, Wu C-H, Ho T-H, Hong PA. Decolorization of CI Reactive Black 5 in UV/TiO2, UV/oxidant and UV/TiO2/oxidant systems: A comparative study. Chem Eng J 2010;158(3):578-83.##29.	Thongkrua S, Ratanatamskul C. Simultaneous removal of lignin and 2, 4-Dichlorophenol in pulp and paper mill wastewater using a supervibration-photocatalytic reactor. Modern Appl Sci 2011;5(1):92.##30.	Safari G, Hoseini M, Seyedsalehi M, et al. Photocatalytic degradation of tetracycline using nanosized titanium dioxide in aqueous solution. Int J Environ Sci Technol 2015;12(2):603-16.##31.	Aghajari N, Yonesi H, Bahramifar N, Ghasemi Z. Photocatalytic removal of Reactive Red 198 from Aqueous Solution using titanium dioxide photocatalyst supported on Fe-ZSM-5 zeolite. J Mazandaran U Med Sci 2017;27(150):137-57. [In Persian]##32.	Espino-Estévez M, Fernández-Rodríguez C, González-Díaz OM, et al. Effect of TiO2–Pd and TiO2–Ag on the photocatalytic oxidation of diclofenac, isoproturon and phenol. Chem Eng J 2016;298: 82-95.##33.	Mai F, Chen C, Chen J, Liu S. Photodegradation of methyl green using visible irradiation in ZnO suspensions: determination of the reaction pathway and identification of intermediates by a high-performance liquid chromatography–photodiode array-electrospray ionization-mass spectrometry method. J Chromatogr A 2008;1189(1-2): 355-65.##34.	Colar La, Ilinoiu Ec, Manea F, Et Al. Photocatalytic Activity Of A Silver Doped Tio 2 Modified Zeolite In The Degradation Of Reactive Yellow 125 Azo Dye. Environ Eng Manage J 2012;11(1):61-8.##35.	Mohammadi R, Massoumi B, Rabani M. Photocatalytic decomposition of amoxicillin trihydrate antibiotic in aqueous solutions under UV irradiation using Sn/TiO2 nanoparticles. Int J Photoenerg 2012:1-11.##36.	Shokri M, Isapour G, Shamsvand S, Kavousi B. Photocatalytic Degradation of Ceftriaxone in Aqueous Solutions by Immobilized TiO2 and ZnO Nanoparticles: Investigating Operational Parameters. J Mater Environ Sci 2016;7:2843-51.##37.	Michael I, Hapeshi E, Michael C, Fatta-Kassinos D. Solar Fenton and solar TiO2 catalytic treatment of ofloxacin in secondary treated effluents: evaluation of operational and kinetic parameters. Water Res 2010;44(18):5450-62.##38.	Klauson D, Babkina J, Stepanova K, et al. Aqueous photocatalytic oxidation of amoxicillin. Catal Today 2010;151(1-2):39-45.##39.	Kermani M, Bahrami Asl F, Farzadkia M, Et Al. Degradation Efficiency And Kinetic Study Of Metronidazole By Catalytic Ozonation Process In Presence Of Mgo Nanoparticles. Urmia Med J 2013;24(10):839-50. [In Persian]##40.	Kashif N, Ouyang F. Parameters effect on heterogeneous photocatalysed degradation of phenol in aqueous dispersion of TiO2. J Environ Sci 2009;21(4):527-33.##41.	Konstantinou IK, Albanis TA. TiO2-assisted photocatalytic degradation of azo dyes in aqueous solution: kinetic and mechanistic investigations: a review. Appl Catal Environ 2004;49(1):1-14.##42.	Behnajady M, Modirshahla N, Hamzavi R. Kinetic study on photocatalytic degradation of CI Acid Yellow 23 by ZnO photocatalyst. J Hazard Mater 2006;133(1-3):226-32.##43.	Khanahmadi M, Hajaghazadeh M, Gholami-Borujeni F. The Study of Photocatalytic Oxidation Process (UV-Fe2O3 (Efficiency for Removal Hydroquinone from Aqueous Solution. J Heal 2018;9(1): 62-74. [In Persian]##44.	Shokoohi R, Mahmoudi MM, Aazami Ghilan R. Efficiency of Magnetic Nanoparticles Modified with Sodium Alginate for Removal of Bisphenol A from Aqueous Solutions Using heterogeneous Fenton Process. J Mazandaran U Med Sci 2017;27(148):88-99. [In Persian]##45.	Xekoukoulotakis NP, Xinidis N, Chroni M, et al. UV-A/TiO2 photocatalytic decomposition of erythromycin in water: Factors affecting mineralization and antibiotic  activity. Catal Today 2010;151(1-2):29-33.##46.	Yang L, Liya EY, Ray MB. Degradation of paracetamol in aqueous solutions by TiO2 photocatalysis. Water Res 2008;42(13):3480-8.##47.	Chakrabarti S, Dutta BK. Photocatalytic degradation of model textile dyes in wastewater using ZnO as semiconductor catalyst. J Hazard Mater 2004;112(3):269-78.## ##</REF>
			</REFRENCE>
		</REFRENCES>

	</ARTICLE>


	<ARTICLE> 
		<TitleF>بررسی کارایی نانولوله کربن مغناطیسی شده در حذف آلاینده آنیلین از محلول آبی</TitleF>
		<TitleE>Investigation the efficiency of magnetized carbon nanotubes in the removal of aniline from aqueous solutions</TitleE>
		<TitleLang_ID>1</TitleLang_ID>
		<ABSTRACTS>
			<ABSTRACT>
			<Language_ID>1</Language_ID>
			<CONTENT>زمینه و هدف: آنیلین ماده ای است که در صنایع شیمیایی و در فرآیندهای مختلفی نظیر تولید آفت کشها، سفید کننده های شیمیایی، رنگهای نساجی و غیره استفاده می گردد. به دلیل اثرات منفی آنیلین بر روی محیط زیست که به دلیل سخت تجزیه بودن این ماده می باشد، روشهای مختلفی جهت حذف این ماده مورد بررسی قرار گرفته است. هدف کاربردی این طرح بررسی کارایی نانولوله کربن مغناطیسی شده در حذف آلاینده آنیلین از محلول آبی می باشد. 
مواد و روش&#173;ها: نانو ذرات مغناطیسی Fe3O4-CNT در مطالعه حاضر به روش هم ترسیبی (Co-Percipitation) تهیه گردید. مورفولوژی سطح جاذب، شکل و اندازه نانوذرات مغناطیسی CNT-Fe3O4 به وسیله میکروسکوپ الکترونی روبشی(SEM ) و میکروسکوپ الکترونی انتقالی (TEM ) بررسی شد. همچنین برای تعیین ویژگی های فیزیکی جاذب نظیر مساحت سطحی، اندازه و حجم حفرات و توزیع آنها بر روی جاذب از آنالیز BET&#160; استفاده شد. به منظور تعیین الگوی پراکنش اشعه ایکس و تعیین خلوص ذرات Fe3O4 تولیدی از دستگاه پراش اشعه ایکس(XRD) استفاده گردید. ویژگی های مغناطیسی جاذب سنتز شده برای قبل و بعد از جذب سطحی به وسیله تکنیک FTIR مورد آنالیز قرار گرفت. به منظور بهینه سازی شرایط جذب و تعیین مقادیر بهینه هر یک از فاکتورهای موثر بر فرایند جذب (pH ، زمان تماس، مقدار جاذب، غلطت اولیه آنیلین و دما) ، آزمایشات جذب انجام شد و غلظت آنیلین توسط روش اسپکتروفتومتری تعیین شد.
یافته&#8204;ها: آنالیزهای SEM , TEM نشان داد که نانو لوله های کربنی مغناطیسی تقریباً به صورت یکنواخت بوده و دارای قطر متوسط 5 نانو متر و طول متوسط 100 نانومتر هستند. همچنین آنالیز XRD نشان دهنده تثبیت اکسید آهنFe3O4 بر روی نانو لوله های کربنی می باشد. آنالیز FTIR مربوط به جذب آلاینده آنیلین بر روی جاذب نانولوله کربن مغناطیسی شده، نشان می دهد که باند آلاینده آنیلین بر روی جاذب پدیدار شده است. 
نتیجه&#8204;گیری: نتایج مطالعه نشان داد که جاذب MWCNT مغناطیسی، قادر به حذف موثر آلاینده آنیلین از محیطهای آبی می&#172;باشد. آنالیزهای آماری نشان داد که پارامترهای pH، غلظت جاذب، غلظت آلاینده، دما و زمان تماس بر روی راندمان حذف آلاینده موثر هستند.</CONTENT>
			</ABSTRACT>
			<ABSTRACT>
			<Language_ID>2</Language_ID>
			<CONTENT>Background &#38;Objectives: Aniline is a substance used in chemical industries and in various processes such as pesticide production, chemical bleaching, textile dyes, etc. In spite of the negative effects of aniline on the environment due the difficult decomposition of this substance, various methods have been investigated to remove this substance from water resources. The aim of this study was to investigate the efficiency of magnetized carbon nanotubes in the removal of aniline from aqueous solutions.
Methods: Fe3O4-CNT magnetic nanoparticles were prepared by co-precipitation method. The morphology of the adsorbent surface, shape and size of CNT-Fe3O4 magnetic nanoparticles was investigated by scanning electron microscopy (SEM) and transfer electron microscopy (TEM). BET analysis was also used to determine the physical properties of the adsorbent such as surface area, size and volume of the cavities and their distribution on the adsorbent. An X-ray diffraction device (XRD) was used to determine the pattern and the purity of the Fe3O4 particles. The synthetic adsorbent properties were analyzed by FTIR technique. In order to optimize the adsorption conditions and determine the optimal values of each of the factors affecting the adsorption process (pH, contact time, adsorbent value, initial aniline error and temperature), adsorption experiments were performed and aniline concentration was determined by spectrophotometric method.
Results: SEM and TEM analyzes showed that the magnetic carbon nanotubes were almost uniform and had an average diameter of 5 nanometers and an average length of 100 nanometers. XRD analysis also showed the stabilization of Fe3O4 on carbon nanotubes. FTIR analysis for the absorption of aniline contaminants on the magnetic carbon nanotubes adsorbent indicated that the aniline contaminant bond has appeared on the adsorbent.
Conclusion: The results of the study showed that magnetic MWCNT adsorbent was able to effectively remove aniline contaminants from aquatic environments. Statistical analysis showed that pH parameters, adsorption concentration, pollutant concentration, temperature and contact time were effective on pollutant removal efficiency.</CONTENT>
			</ABSTRACT>
		</ABSTRACTS>

		<PAGES>
			<PAGE>
			<FPAGE>244</FPAGE>
			<TPAGE>260</TPAGE>
			</PAGE>
		</PAGES>

		<RECEIVE_DATE>
			2020/05/132019/07/18
		</RECEIVE_DATE>

		<RECEIVE_DATE_FA>
			1398/4/27
		</RECEIVE_DATE_FA>

		<ACCEPT_DATE>
			2020/05/132020/01/5
		</ACCEPT_DATE>

		<ACCEPT_DATE_FA>
			1398/10/15
		</ACCEPT_DATE_FA>

		<AUTHORS>
			<AUTHOR>
				<Name>بابک</Name>
				<MidName></MidName>
				<Family>کاکاوندی</Family>
				<NameE>Babak</NameE>
				<MidNameE></MidNameE>
				<FamilyE>Kakavandi</FamilyE>
				<Organizations>
				<Organization>گروه مهندسی بهداشت محیط، دانشکده بهداشت دانشگاه علوم پزشکی البرز، کرج، ایران2مرکز تحقیقات بهداشت، ایمنی و محیط (RCHSE)، دانشگاه علوم پزشکی البرز، کرج، ایران</Organization>
				</Organizations>
				<Countries>
				<Country>ایران</Country>
				</Countries>
				<EMAILS>
				<Email></Email>
				</EMAILS>
			</AUTHOR>

			<AUTHOR>
				<Name>محمد</Name>
				<MidName></MidName>
				<Family>نوری سپهر</Family>
				<NameE>Mohammad</NameE>
				<MidNameE></MidNameE>
				<FamilyE>Noorisepehr</FamilyE>
				<Organizations>
				<Organization>گروه مهندسی بهداشت محیط، دانشکده بهداشت دانشگاه علوم پزشکی البرز، کرج، ایران2مرکز تحقیقات بهداشت، ایمنی و محیط (RCHSE)، دانشگاه علوم پزشکی البرز، کرج، ایران</Organization>
				</Organizations>
				<Countries>
				<Country>ایران</Country>
				</Countries>
				<EMAILS>
				<Email></Email>
				</EMAILS>
			</AUTHOR>

			<AUTHOR>
				<Name>عماد</Name>
				<MidName></MidName>
				<Family>دهقانی فرد</Family>
				<NameE>Emad</NameE>
				<MidNameE></MidNameE>
				<FamilyE>Dehghanifard</FamilyE>
				<Organizations>
				<Organization>گروه مهندسی بهداشت محیط، دانشکده بهداشت دانشگاه علوم پزشکی البرز، کرج، ایران2مرکز تحقیقات بهداشت، ایمنی و محیط (RCHSE)، دانشگاه علوم پزشکی البرز، کرج، ایران</Organization>
				</Organizations>
				<Countries>
				<Country>ایران</Country>
				</Countries>
				<EMAILS>
				<Email></Email>
				</EMAILS>
			</AUTHOR>

			<AUTHOR>
				<Name>محمد</Name>
				<MidName></MidName>
				<Family>رفیعی</Family>
				<NameE>Mohammad</NameE>
				<MidNameE></MidNameE>
				<FamilyE>Rafiee</FamilyE>
				<Organizations>
				<Organization>گروه مهندسی بهداشت محیط، دانشکده بهداشت دانشگاه علوم پزشکی شهید بهشتی، تهران، ایران</Organization>
				</Organizations>
				<Countries>
				<Country>ایران</Country>
				</Countries>
				<EMAILS>
				<Email></Email>
				</EMAILS>
			</AUTHOR>
		</AUTHORS>


		<KEYWORDS>
			<KEYWORD>
				<KeyText>Aniline</KeyText>
			</KEYWORD>

			<KEYWORD>
				<KeyText>Magnetized carbon nanotubes</KeyText>
			</KEYWORD>

			<KEYWORD>
				<KeyText>Surface adsorption</KeyText>
			</KEYWORD>

			<KEYWORD>
				<KeyText>Aqueous solution</KeyText>
			</KEYWORD>

			<KEYWORD>
				<KeyText>آنیلین</KeyText>
			</KEYWORD>

			<KEYWORD>
				<KeyText>نانولوله کربن مغناطیسی شده</KeyText>
			</KEYWORD>

			<KEYWORD>
				<KeyText>جذب سطحی</KeyText>
			</KEYWORD>

			<KEYWORD>
				<KeyText>محلول آبی.</KeyText>
			</KEYWORD>
		</KEYWORDS>

		<REFRENCES>
			<REFRENCE>
				<REF>1. Nemerow NL, Agardy FJ, Sullivan P, Salvato JA. Environmental Engineering: Water, Wastewater, Soil and Groundwater Treatment and Remediation. New York: John Wiley &#38; Sons; 2009.##2. Rappoport Z. The chemistry of Anilines. 1st ed. London: John Wiley &#38; Sons Ltd; 2007. 1163 p.##3. Sarasa J, Cortes S, Ormad P, et al. Study of the aromatic by-products formed from ozonation of anilines in aqueous solution. Water research 2002;36: 3035-44.##4. OSHA. Air Contaminants. Occupational Safety and Health Administration (OSHA), 1993  Contract No.: 29 CFR-1910.##5. USEPA. Aniline Fact Sheet: Support Document. United States Environmental Protection Agency (USEPA), 1994  Contract No.: CAS No. 62-53-3.##6. Bell LS, Devlin JF, Gillham RW, Binning PJ. A sequential zero valent iron and aerobic biodegradation treatment system for nitrobenzene. J Contam Hydrol 2003;66(3-4):201-17.##7. Fabiańska A, Białk-Bielińska A, Stepnowski P, et al. Electrochemical degradation of sulfonamides at BDD electrode: kinetics, reaction pathway and eco-toxicity evaluation. J Hazard Mater 2014;280:579-87.##8. Cheng WB, Ding J, Liu XS, Liu CM, editors. Adsorption Properties of Phenol and Aniline Removal by Poly Aluminium Chloride from the Aqueous Phase. Adv Mater Res 2014;Trans Tech Publ.##9. Liu Y-B, Qu D, Wen Y-J, Ren H-J. Low-temperature biodegradation of aniline by freely suspended and magnetic modified Pseudomonas migulae AN-1. Appl Microbio Biotechnol 2015;99(12):5317-26.##10. Trchová M, Morávková Z, Šeděnková I, Stejskal J. Spectroscopy of thin polyaniline films deposited during chemical oxidation of aniline. Chem Papers 2012;66(5):415-45.##11. Jafari AJ, Dehghanifard E, Kalantary RR, et al. Photocatalytic degradation of aniline in aqueous solution using zno nanoparticles. Environ Eng Manage J 2016;15(1).##12. Huang YH, Su CC, Yang YP, Lu MC. Degradation of aniline catalyzed by heterogeneous Fenton‐like reaction using iron oxide/SiO2. Environ Prog Sustain Energ 2013;32(2): 187-92.##13. Metcalf E, EDDY M. Wastewater engineering: treatment and Resource recovery. McGraw-Hill Education, New York 2014.##14. Asmaly HA, Abussaud B, Saleh TA, et al. Ferric oxide nanoparticles decorated carbon nanotubes and carbon nanofibers: From synthesis to enhanced removal of phenol. J Saudi Chem Soc 2015;19(5):511-20.##15. Asmaly HA, Saleh TA, Laoui T, et al. Enhanced adsorption of phenols from liquids by aluminum oxide/carbon nanotubes: Comprehensive study from synthesis to surface properties. J Mol Liq 2015;206:176-82.##16. Atieh MA. Removal of chromium (VI) from polluted water using carbon nanotubes supported with activated carbon. Proc Environ Sci 2011;4:281-93.##17. Kosa SA, Al-Zhrani G, Salam MA. Removal of heavy metals from aqueous solutions by multi-walled carbon nanotubes modified with 8-hydroxyquinoline. Chem Eng J 2012;181:159-68.##18. Yuwei C, Jianlong W. Preparation and characterization of magnetic chitosan nanoparticles and its application for Cu (II) removal. Chem Eng J 2011;168(1):286-92.##19. Zhong LS, Hu JS, Liang HP, et al. Self‐Assembled 3D flowerlike iron oxide nanostructures and their application in water treatment. Adv Mater 2006;18(18):2426-31.##20. Li S, Gong Y, Yang Y, et al. Recyclable CNTs/Fe 3 O 4 magnetic nanocomposites as adsorbents to remove bisphenol A from water and their regeneration. Chem Eng J 2015;260:231-9.##21. WEF, APHA. Standard methods for the examination of water and wastewater. American Public Health Association (APHA): Washington, DC, USA 2005.##22.Mobasherpour I, Salahi E, Ebrahimi M. Thermodynamics and kinetics of adsorption of Cu (II) from aqueous solutions onto multi-walled carbon nanotubes. J Saudi Chem Soc 2014;18(6): 792-801.##23. Pyrzynska K. Carbon nanostructures for separation, preconcentration and speciation of metal ions. TrAC Trend Analyt Chem 2010;29(7):718-27.##24. Tofighy MA, Mohammadi T. Adsorption of divalent heavy metal ions from water using carbon nanotube sheets. J Hazard Mater 2011;185(1):140-7.##25. Kabbashi NA, Atieh MA, Al-Mamun A, et al. Kinetic adsorption of application of carbon nanotubes for Pb (II) removal from aqueous solution. J Environ Sci 2009;21(4): 539-44.##26. Lü X, Wu Z, Shen J, et al. Electrochemical Behavior of 2, 4-Dinitrophenol at Multi-Walled Carbon Nanotube-Modified Glassy Carbon Electrode and Its Application. Int J Electrochem Sci 2013;8: 2229-37.##27. Pyrzynska K. Application of Solid Sorbents for Enrichment and Separation of Platinum Metal Ions.  Platinum Metals in the Environment: Springer; 2015. p. 67-78.##28. Liu X, Wang M, Zhang S, Pan B. Application potential of carbon nanotubes in water treatment: a review. J Environ Sci 2013;25(7):1263-80.##29. Tóth A, Törőcsik A, Tombácz E, László K. Competitive adsorption of phenol and 3-chlorophenol on purified MWCNTs. J Colloid Interf Sci 2012;387(1):244-9.##30. Li M, Hsieh T-C, Doong R-A, Huang C. Tuning the adsorption capability of multi-walled carbon nanotubes to polar and non-polar organic compounds by surface oxidation. Sep Purif Technol 2013;117:98-103.##31. Lazo-Cannata JC, Nieto-Márquez A, Jacoby A, et al. Adsorption of phenol and nitrophenols by carbon nanospheres: Effect of pH and ionic strength. Sep Purif Technol 2011;80(2):217-24.##32. Freundlich H. Over the adsorption in solution. J Phys Chem 1906;57(385):470.##33. Langmuir I. The adsorption of gases on plane surfaces of glass, mica and platinum. J Am Chem Soc 1918;40(9):1361-403.##34. Kakavandi B, Jonidi A, Rezaei R, et al. Synthesis and properties of Fe3O4-activated carbon magnetic nanoparticles for removal of aniline from aqueous solution: equilibrium, kinetic and thermodynamic studies. J Environ Health Sci Eng 2013;10(1):1.##35. Yu J-G, Zhao X-H, Yang H, et al. Aqueous adsorption and removal of organic contaminants by carbon nanotubes. Sci Total Environ 2014;482:241-51.## ##</REF>
			</REFRENCE>
		</REFRENCES>

	</ARTICLE>


	<ARTICLE> 
		<TitleF>بررسی کارایی حذف آفت کش مالاتیون توسط نانوکامپوزیت g-C3N4/Fe3O4/Ag از محلول‌های آبی در حضور اشعه UV</TitleF>
		<TitleE>Evaluation of Malathion Pesticide Removal Efficiency by g-C3N4/ Fe3O4/Ag Nanocomposites from Aqueous Solutions in the Presence of UV Irradiation</TitleE>
		<TitleLang_ID>1</TitleLang_ID>
		<ABSTRACTS>
			<ABSTRACT>
			<Language_ID>1</Language_ID>
			<CONTENT>زمینه و هدف: ارگانوفسفره&#8204;ها از شایع&#8204;ترین سموم دفع آفات در جهان به شمار می&#8204;روند. از سموم پرمصرف این گروه مالاتیون می&#8204;باشد که توسط EPA در گروه III مواد از نظر سرطانزایی تقسیم می&#8204;شود. بنابراین باتوجه به مصرف زیاد این آفت کش و قدرت بیماری زایی آن باید به شیوه مناسب حذف گردد. یکی از راه&#8204;های حذف استفاده از فرآیندهای اکسیداسیون پیشرفته است. هدف از این مطالعه حذف فتوکاتالیستی آفت کش مالاتیون توسط نانوکامپوزیت g-C3N4/Fe3O4/Ag می&#8204;باشد. 
روش: در این مطالعه از نانوکامپوزیت g-C3N4/Fe3O4/Ag که با استفاده از روش هیدروترمال سنتز گردید، برای حذف فتوکاتالیستی مالاتیون استفاده شد. متغیر&#8204;های مورد بررسی pH، دوز نانوکامپوزیت، غلظت آلاینده بود. هم چنین اثر رادیکال خوارهای اگزالات آمونیوم ، ترت بوتانول و بنزوکینون بر انجام آزمایش سنجش شد. 
یافته ها: بهترین راندمان حذف مالاتیون در 7=pH، دوز 5/0 گرم بر لیتر و غلظت آلاینده 10 میلی گرم بر لیتر و در زمان 60 دقیقه و برابر با 100 % بود. با افزایش دوز کاتالیست تا 5/0 گرم بر لیتر راندمان افزایش یافت. اما با افزایش غلظت آلاینده راندمان حذف روند نزولی داشت. هم چنین راندمان حذف مالاتیون در حضور رادیکال خوارهای اگزالات آمونیوم، ترت بوتانول و بنزوکینون به ترتیب 36/93 %، 78/44 % و 71/90 % به دست آمد و سینتیک واکنش از معادله درجه اول با&#160; 9852/0= R2&#160; پیروی کرد. 
نتیجه گیری: بنابراین g-C3N4/Fe3O4/Ag از پتانسیل بالایی برای حذف مالاتیون برخوردار بوده و می&#8204;تواند برای از بین بردن آلاینده&#8204;های مختلف از محلول&#8204;های آبی استفاده شود.</CONTENT>
			</ABSTRACT>
			<ABSTRACT>
			<Language_ID>2</Language_ID>
			<CONTENT>Background: Organophosphates are one of the most common pesticides in the world. One of the most commonly used toxins in this group is malathion, which is classified by the EPA as Group III carcinogenic substances. Therefore, due to the high consumption of this pesticide and its pathogenicity, it should be eliminated in an appropriate manner. One of the elimination ways is the use of advanced oxidation processes. The aim of this study was to determine the photocatalytic removal of malathion pesticide by g-C3N4/Fe3O4/Ag nanocomposite.
Method: In this study, g-C3N4/Fe3O4/Ag nanocomposites synthesized by hydrothermal method were used for photocatalytic removal of malathion. The variables studied were pH, nanocomposite dose, and contaminant concentration. Furthermore, the radical effects of ammonium oxalate, tert-butanol, and benzoquinone were analyzed on the experiment procedure.
Results: The best removal efficiency of malathion at pH = 7, the dose of 0.5 g/l, and contaminant concentration 10 mg/l at 60 min was 100%. By increasing the catalyst dose up to 0.5 g/L, the efficiency increased. However, with increasing contaminant concentration, the removal efficiency decreased. Additionally, the removal efficiency of malathion in the presence of ammonium oxalate, tert-butanol, and benzoquinone radicals was 93.36%, 44.78%, and 90.71%, respectively, and the reaction kinetics followed the first equation with R2 = 0.9852.&#160;
Conclusion: Therefore, g-C3N4/Fe3O4/Ag has a high potential for malathion removal moreover can be used to remove various pollutants from aqueous solutions.&#160;</CONTENT>
			</ABSTRACT>
		</ABSTRACTS>

		<PAGES>
			<PAGE>
			<FPAGE>261</FPAGE>
			<TPAGE>279</TPAGE>
			</PAGE>
		</PAGES>

		<RECEIVE_DATE>
			2020/05/132019/07/182020/06/28
		</RECEIVE_DATE>

		<RECEIVE_DATE_FA>
			1399/4/8
		</RECEIVE_DATE_FA>

		<ACCEPT_DATE>
			2020/05/132020/01/52020/06/28
		</ACCEPT_DATE>

		<ACCEPT_DATE_FA>
			1399/4/8
		</ACCEPT_DATE_FA>

		<AUTHORS>
			<AUTHOR>
				<Name>علی</Name>
				<MidName></MidName>
				<Family>اسرافیلی</Family>
				<NameE>Ali</NameE>
				<MidNameE></MidNameE>
				<FamilyE>Esrafili</FamilyE>
				<Organizations>
				<Organization>گروه مهندسی بهداشت محیط، دانشکده بهداشت،مرکز تحقیقات تکنولوژی بهداشت محیط، دانشگاه علوم پزشکی ایران، تهران، ایران</Organization>
				</Organizations>
				<Countries>
				<Country>ایران</Country>
				</Countries>
				<EMAILS>
				<Email></Email>
				</EMAILS>
			</AUTHOR>

			<AUTHOR>
				<Name>سودابه</Name>
				<MidName></MidName>
				<Family>قدسی</Family>
				<NameE>Soudabeh</NameE>
				<MidNameE></MidNameE>
				<FamilyE>Ghodsi</FamilyE>
				<Organizations>
				<Organization>دانشجوی کارشناسی ارشد مهندسی بهداشت محیط، دانشکده بهداشت، دانشگاه علوم پزشکی ایران، تهران، ایران</Organization>
				</Organizations>
				<Countries>
				<Country>ایران</Country>
				</Countries>
				<EMAILS>
				<Email></Email>
				</EMAILS>
			</AUTHOR>

			<AUTHOR>
				<Name>روشنک</Name>
				<MidName></MidName>
				<Family>رضایی کلانتری</Family>
				<NameE>Roshanak</NameE>
				<MidNameE></MidNameE>
				<FamilyE>Rezaei Kalantary</FamilyE>
				<Organizations>
				<Organization>گروه مهندسی بهداشت محیط، دانشکده بهداشت،مرکز تحقیقات تکنولوژی بهداشت محیط، دانشگاه علوم پزشکی ایران، تهران، ایران دانشگاه علوم پزشکی ایران، تهران، ایران</Organization>
				</Organizations>
				<Countries>
				<Country>ایران</Country>
				</Countries>
				<EMAILS>
				<Email></Email>
				</EMAILS>
			</AUTHOR>

			<AUTHOR>
				<Name>میترا</Name>
				<MidName></MidName>
				<Family>غلامی</Family>
				<NameE>Mitra</NameE>
				<MidNameE></MidNameE>
				<FamilyE>Gholami</FamilyE>
				<Organizations>
				<Organization>گروه مهندسی بهداشت محیط، دانشکده بهداشت،مرکز تحقیقات تکنولوژی بهداشت محیط، دانشگاه علوم پزشکی ایران، تهران، ایران دانشگاه علوم پزشکی ایران، تهران، ایران</Organization>
				</Organizations>
				<Countries>
				<Country>ایران</Country>
				</Countries>
				<EMAILS>
				<Email></Email>
				</EMAILS>
			</AUTHOR>
		</AUTHORS>


		<KEYWORDS>
			<KEYWORD>
				<KeyText>Photocatalyst</KeyText>
			</KEYWORD>

			<KEYWORD>
				<KeyText>Malation</KeyText>
			</KEYWORD>

			<KEYWORD>
				<KeyText>C3N4/Fe3O4/Ag</KeyText>
			</KEYWORD>

			<KEYWORD>
				<KeyText>فتوکاتالیست</KeyText>
			</KEYWORD>

			<KEYWORD>
				<KeyText>مالاتیون</KeyText>
			</KEYWORD>

			<KEYWORD>
				<KeyText>g-C3N4/Fe3O4/Ag</KeyText>
			</KEYWORD>
		</KEYWORDS>

		<REFRENCES>
			<REFRENCE>
				<REF>1. Hela DG, Lambropoulou DA, Konstantinou IK, Albanis TA. Environmental monitoring and ecological risk assessment for pesticide contamination and effects in Lake Pamvotis, northwestern Greece. J Environ Toxicol Chem 2005;24(6): 1548-56.##2. Sakkas V, Dimou A, Pitarakis K, et al. TiO 2 photocatalyzed degradation of diazinon in an aqueous medium. J Environ Chem Lett 2005;3(2): 57-61.##3. Nasseri S, Borna MO, Esrafili A, et al. Photocatalytic degradation of malathion using Zn 2+-doped TiO 2 nanoparticles: statistical analysis and optimization of operating parameters. Int J Appl Phys 2018;124(2): 175.##4. Kadam A, Dhabbe R, Kokate M, et al. Preparation of N doped TiO2 via microwave-assisted method and its photocatalytic activity for degradation of Malathion. J Spectrochim Acta A Mol Biomol Spectrosc 2014;133: 669-76.##5. De Silva H, Samarawickrema N, Wickremasinghe A. Toxicity due to organophosphorus compounds: what about chronic exposure? J Trans R Soc Trop Med Hyg 2006;100(9): 803-6.##6. Bermúdez-Couso A, Fernández-Calviño D, Pateiro-Moure M, et al. Adsorption and desorption kinetics of carbofuran in acid soils. J Hazard Mater 2011;190(1-3):159-67.##7. Dargahi A, Samarghandi MR, Karami A, et al. Investigation of Residual Concentrations of Organic Phosphorus Pesticides in Surface Water and Groundwater Sources Supplying Drinking Water of Kermanshah Province. J Health Sci 2018;9(2):133-44.##8. Shakerkhatibi M, Mosaferi M, Jafarabadi MA, et al. Pesticides residue in drinking groundwater resources of rural areas in the northwest of Iran. J Health Promot Perspect 2014;4(2): 195.##9. Moussavi G, Hosseini H, Alahabadi A. The investigation of diazinon pesticide removal from contaminated water by adsorption onto NH4Cl-induced activated carbon. J Chem Eng Trans 2013;214: 172-9.##10. Chong MN, Jin B, Chow CW, Saint C. Recent developments in photocatalytic water treatment technology: a review. J Water Res 2010;44(10): 2997-3027.##11. Miguel N, Ormad MP, Mosteo R, Ovelleiro JL. Photocatalytic degradation of pesticides in natural water: effect of hydrogen peroxide. J Int photoenergy 2012;2012.##12. Mohajerani M, Mehrvar M, Ein-Mozaffari F. An overview of the integration of advanced oxidation technologies and other processes for water and wastewater treatment. Int J Eng 2009;3(2): 120-46.##13. Gao E, Wang W, Shang M, Xu J. Synthesis and enhanced photocatalytic performance of graphene-Bi 2 WO 6 composite. J Phys Chem Chem Phys 2011;13(7): 2887-93.##14. Liu L, Bai H, Liu J, Sun DD. Multifunctional graphene oxide-TiO2-Ag nanocomposites for high performance water disinfection and decontamination under solar irradiation. J Hazard Mater 2013;261: 214-23.##15. Amarjargal A, Tijing LD, Im I-T, Kim CS. Simultaneous preparation of Ag/Fe3O4 core–shell nanocomposites with enhanced magnetic moment and strong antibacterial and catalytic properties. J  Chem Eng 2013;226: 243-54.##16. 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Effect of gadollunium doping on visible light photocatalytic performance of Ag3PO4: evaluation of activity in degradation of an anthraquinone dye and mechanism study. J Mol Catal A Chem 2017;426: 257-70.##42. Reddy KH, Martha S, Parida K. Fabrication of novel p-BiOI/n-ZnTiO3 heterojunction for degradation of rhodamine 6G under visible light irradiation. J Inorg Chem 2013;52(11): 6390-401.##43. Ali HM, Abou-Mesalam M, El-Shorbagy M. Structure  and optical properties of chemically synthesized titanium oxide deposited by evaporation technique. J Phys Chem Solids 2010;71(1): 51-5.##44. Dehghani M, Fadaei A. Potoccatalytic oxidation of oganophosphorus pesticides using zinc oxide. Res J Chem Environ 2012;16.##45. Yu H, Wang X, Sun H, Huo M. Photocatalytic degradation of malathion in aqueous solution using an Au–Pd–TiO2 nanotube film. J Hazard mater 2010;184(1-3): 753-8.## ##</REF>
			</REFRENCE>
		</REFRENCES>

	</ARTICLE>


	<ARTICLE> 
		<TitleF>بررسی توزیع، ریسک اکولوژیک و سلامت سورفاکتانت آنیونی (LAS)  به عنوان نشانگر مولکولی تخلیه فاضلاب در سد اکباتان، همدان</TitleF>
		<TitleE>Distribution, Ecological and Health Risk Assessment of Anionic Surfactant (LAS) As a Molecular Marker for Wastewater Discharge in Ekbatan Dam, Hamedan</TitleE>
		<TitleLang_ID>1</TitleLang_ID>
		<ABSTRACTS>
			<ABSTRACT>
			<Language_ID>1</Language_ID>
			<CONTENT>زمینه وهدف: با توجه به افزایش مصرف شوینده&#173; ها و مشکلات آلودگی منابع آبی در اثر رهاسازی فاضلاب&#173; های حاوی مقادیر زیاد شوینده&#173; ها در چند دهه اخیر، در این مطالعه به بررسی غلظت و ارزیابی ریسک سلامت و اکولوژیک آلکیل بنزن سولفانات خطی (LAS) به عنوان مهم&#173;ترین ترکیب شوینده&#173; ها در سد اکباتان همدان پرداخته شده است.
مواد و روش: 31 ایستگاه نمونه&#173; برداری از مخزن سد اکباتان و رودخانه&#173; های ورودی به سد و سرریز سد اکباتان (سد آبشینه) جهت نمونه&#173; برداری آب انتخاب شد. پارامترهایی همچون دمای آب، pH، EC، TDS، DO و ORP در محل نمونه&#173; برداری اندازه&#173; گیری شد. جذب LAS از طریق دستگاه اسپکتروفتومتر(WTW 660) در طول موجnm &#160;650 قرائت شد. 
یافته&#173; ها: نتایج غلظت LAS اندازه &#173;گیری شده را در دامنه mg/L 4/1- 01/0 نشان داد. نتایج آزمون همبستگی اسپیرمن بین LAS و فاکتورهای کیفی آب نشان داد بین LAS با شوری، TDS و EC رابطه مثبت و معنی&#173; دار در سطح 01/0 و بین LAS و DO رابطه منفی در سطح 05/0 وجود دارد.&#160; نتایج محاسبه ارزیابی ریسک اکولوژیک، در 13 ایستگاه ریسک زیاد، در 15 ایستگاه ریسک متوسط و در3 ایستگاه ریسک کم را نشان داد. همچنین محاسبه ارزیابی ریسک سلامت LAS، عدم وجود ریسک در گروه&#173; های مختلف سنی مختلف را نشان داد. نتایج مقایسه غلظت LAS با استاندارد تخلیه سورفاکتانت&#173; ها به داخل آب&#173; های سطحی و مصارف کشاورزی و آبیاری در ایران نشان داد غلظت LAS از نظر تخلیه به داخل آب&#173; های سطحی کمتر حد مجاز (mg/L 5/1) ولی از نظر استفاده برای مصارف کشاورزی و آبیاری مقدار LAS در 7 ایستگاه بیشتر از استاندارد &#160;مربوطه است. &#160;
نتیجه&#173; گیری: نتایج این مطالعه نشان داد سد اکباتان و رودخانه&#173; های منتهی به سد در معرض ورود ترکیبات شوینده ناشی از ورود فاضلاب&#173; های خانگی قرار دارد. بنابراین لازم است اقدامات موثر و پیشگیرانه در جهت کنترل و کاهش ورود فاضلاب&#173; های تصفیه نشده به این سد مهم و حیاتی صورت گیرد.</CONTENT>
			</ABSTRACT>
			<ABSTRACT>
			<Language_ID>2</Language_ID>
			<CONTENT>Background and Aim: Given the increasing use of detergents and the problems of water pollution caused by the release of wastewater containing large amounts of detergents in recent decades, this study aimed to investigate the concentration and health and ecological risk assessment of linear alkylbenzene sulfonate (LAS) as the most important detergent composition in Ekbatan Dam is Hamedan.
Materials and Methods: 31 sampling stations from Ekbatan dam reservoir and Inlet Rivers to Ekbatan dam and overflow dam (Abshineh dam) selected for water sampling. Parameters such as water temperature, pH, EC, TDS, DO and ORP was measured at the sampling site. LAS adsorption was reading through a spectrophotometer (WTW 660) at 650 nm. The pollutant concentration was calculated through the equation of the calibration curve.
Results: The results showed the measured LAS concentration in the range of 0.01-1.4 mg / L. The results of the Spearman correlation test between LAS and water quality factors showed a positive significant relationship between LAS with salinity, TDS and EC at 0.01 level and a negative relationship between LAS and DO at 0.05 levels. The results of the health risk assessment of LAS showed no risk in different age groups. The results of the comparison of LAS concentration with surfactant discharge standard in surface water and irrigation and agricultural applications in Iran showed that the concentration of LAS is below the permissible level (1.5 mg / L) for discharge into surface water. However, in terms of use for agricultural and irrigation purposes, the LAS value at 7 stations was higher than the permissible level (0.5 mg / L).
Conclusion: The results of this study showed that Ekbatan dam and rivers entering the dam are exposed to mild wastewater as a result of human activities. Therefore, it is necessary to take effective and preventive activities to control and reduce pollutants entering this valuable dam.</CONTENT>
			</ABSTRACT>
		</ABSTRACTS>

		<PAGES>
			<PAGE>
			<FPAGE>280</FPAGE>
			<TPAGE>297</TPAGE>
			</PAGE>
		</PAGES>

		<RECEIVE_DATE>
			2020/05/132019/07/182020/06/282020/06/28
		</RECEIVE_DATE>

		<RECEIVE_DATE_FA>
			1399/4/8
		</RECEIVE_DATE_FA>

		<ACCEPT_DATE>
			2020/05/132020/01/52020/06/282020/06/28
		</ACCEPT_DATE>

		<ACCEPT_DATE_FA>
			1399/4/8
		</ACCEPT_DATE_FA>

		<AUTHORS>
			<AUTHOR>
				<Name>فائزه</Name>
				<MidName></MidName>
				<Family>جعفری</Family>
				<NameE>Faezeh</NameE>
				<MidNameE></MidNameE>
				<FamilyE>Jaffari</FamilyE>
				<Organizations>
				<Organization>گروه محیط زیست، دانشکده منابع طبیعی و محیط زیست، دانشگاه ملایر، ملایر، ایران</Organization>
				</Organizations>
				<Countries>
				<Country>ایران</Country>
				</Countries>
				<EMAILS>
				<Email></Email>
				</EMAILS>
			</AUTHOR>

			<AUTHOR>
				<Name>نسرین</Name>
				<MidName></MidName>
				<Family>حسن زاده</Family>
				<NameE>Nasrin</NameE>
				<MidNameE></MidNameE>
				<FamilyE>Hassanzadeh</FamilyE>
				<Organizations>
				<Organization>گروه محیط زیست، دانشکده منابع طبیعی و محیط زیست، دانشگاه ملایر، ملایر، ایران</Organization>
				</Organizations>
				<Countries>
				<Country>ایران</Country>
				</Countries>
				<EMAILS>
				<Email></Email>
				</EMAILS>
			</AUTHOR>
		</AUTHORS>


		<KEYWORDS>
			<KEYWORD>
				<KeyText>Ekbatan dam</KeyText>
			</KEYWORD>

			<KEYWORD>
				<KeyText>Abshineh dam</KeyText>
			</KEYWORD>

			<KEYWORD>
				<KeyText>(LAS)</KeyText>
			</KEYWORD>

			<KEYWORD>
				<KeyText>Ecological risk</KeyText>
			</KEYWORD>

			<KEYWORD>
				<KeyText>Health risk</KeyText>
			</KEYWORD>

			<KEYWORD>
				<KeyText>سد اکباتان</KeyText>
			</KEYWORD>

			<KEYWORD>
				<KeyText>سد آبشینه</KeyText>
			</KEYWORD>

			<KEYWORD>
				<KeyText>(LAS)</KeyText>
			</KEYWORD>

			<KEYWORD>
				<KeyText>ریسک اکولوژیک</KeyText>
			</KEYWORD>

			<KEYWORD>
				<KeyText>ریسک سلامت</KeyText>
			</KEYWORD>
		</KEYWORDS>

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	</ARTICLE>


	<ARTICLE> 
		<TitleF>بهینه سازی و پیش بینی فرآیند بیوفیلمی با بستر متحرک (MBBR) با استفاده از روش‌ پاسخ سطح (RSM) و شبکه عصبی مصنوعی (ANN)</TitleF>
		<TitleE>Optimization and Prediction of Moving Bed Biofilm Reactor (MBBR) Using Surface Response Method (RSM) and Artificial Neural Network (ANN)</TitleE>
		<TitleLang_ID>1</TitleLang_ID>
		<ABSTRACTS>
			<ABSTRACT>
			<Language_ID>1</Language_ID>
			<CONTENT>زمینه و هدف: در این تحقیق بهینه سازی و پیش بینی راندمان راکتور بیوفیلمی با بستر متحرک (MBBR) در تصفیه فاضلاب مصنوعی حاوی آنیلین با استفاده از روش سطح پاسخ (RSM) و شبکه عصبی مصنوعی (ANN) بررسی شده است. 
مواد و روش&#8204;ها: نتایج مدلسازی از راکتور به حجم تقریبی 5 لیتر که با درصد پرشدگی 30، 50 و 70 درصد با سنگدانه&#8204;های سبک لیکا به عنوان محیط رشد میکروارگانسیم&#8204;ها و تشکیل لایه بیوفیلم پر شده بود، استفاده گردید. برای تعیین شرایط بهینه در آزمایش&#173; های انجام شده و همچنین پیش &#173;بینی آزمایش &#173;های انجام نشده، سه عامل میزان خوراک در سطوح بین 100 تا 3000 میلی&#173;گرم بر لیتر، زمان ماند 8 تا 72 ساعت و درصد پرشدگی 30 و 50 و 70 درصد با استفاده از RSM صورت گرفت. دقت و صحت مدلهای ارائه شده به کمک تحلیل واریانس ANOVA بررسی شد. پیش&#173; بینی راندمان حذف سیستم با استفاده از ANN پایه شعاعی نیز بررسی گردید. 
یافته&#8204;ها: بهینه&#173; سازی فرایند نشان داد که شرایط بهینه برای بیشترین حذف در میزان خوراک mg/l 1700 و زمان ماند 72 ساعت در درصد پرشدگی 82/56 درصد می&#173;باشد. نتایج پیش بینی فرایند با استفاده از ANN پایه شعاعی نیز نشان داد که در بهترین ساختار شبکه با توابع انتقال Radbas و خطی (Purelin) با 982/0=R2 قادر به پیش بینی راندمان حذف می&#173;باشد.
نتیجه&#8204;گیری: با مقایسه مدل ANN پایه شعاعی و RSM و مقایسه میزان خطای این دو روش می&#173;توان گفت که روش ANN پایه شعاعی با دقت بیشتر و خطای کمتر روند داده&#173; ها را پیش &#173;بینی کرده است.</CONTENT>
			</ABSTRACT>
			<ABSTRACT>
			<Language_ID>2</Language_ID>
			<CONTENT>Background &#160;In this study, the optimization and prediction of the efficiency of a moving bed biofilm reactor (MBBR) in the treatment of synthetic wastewater containing organic material including aniline was investigated using response surface methodology and artificial neural network.
Materials and Methods: Modeling results were applied to a 5-liter volume reactor filled with 30%, 50% and 70% LECA lightweight aggregates as a growth medium for microorganisms and biofilm layer formation. In order to determine the optimum conditions in the experiments results and also to predict the tests not performed, three factors were feed levels at levels of 100 to 3000 mg/L, retention time of 8 to 72 hours and filling percentage of 30 and 50 and 70% were performed using RSM. The accuracy of the presented models was evaluated by ANOVA. Prediction of system removal efficiency using radial basis ANN was also investigated.
Results: Process optimization showed that the optimum conditions for maximum removal were at feed rate of 1700 mg/l and 72 hours at 56.82% filling percentage. The results of the process prediction using radial basis ANN also showed that in the best network structure with Radbas and linear functions (Purelin) with R2 = 0.982 can predict the efficiency.
Conclusion: By comparing the radial basis ANN model and RSM and comparing the error rates of these two methods, it can be concluded that the radial base ANN method predicts the data process more accurately and with lower error.</CONTENT>
			</ABSTRACT>
		</ABSTRACTS>

		<PAGES>
			<PAGE>
			<FPAGE>298</FPAGE>
			<TPAGE>313</TPAGE>
			</PAGE>
		</PAGES>

		<RECEIVE_DATE>
			2020/05/132019/07/182020/06/282020/06/282020/06/28
		</RECEIVE_DATE>

		<RECEIVE_DATE_FA>
			1399/4/8
		</RECEIVE_DATE_FA>

		<ACCEPT_DATE>
			2020/05/132020/01/52020/06/282020/06/282020/06/28
		</ACCEPT_DATE>

		<ACCEPT_DATE_FA>
			1399/4/8
		</ACCEPT_DATE_FA>

		<AUTHORS>
			<AUTHOR>
				<Name>محمد</Name>
				<MidName></MidName>
				<Family>دلنواز</Family>
				<NameE>Mohammad</NameE>
				<MidNameE></MidNameE>
				<FamilyE>Delnavaz</FamilyE>
				<Organizations>
				<Organization>گروه مهندسی عمران، دانشکده فنی و مهندسی، دانشگاه خوارزمی، تهران، ایران</Organization>
				</Organizations>
				<Countries>
				<Country>ایران</Country>
				</Countries>
				<EMAILS>
				<Email></Email>
				</EMAILS>
			</AUTHOR>

			<AUTHOR>
				<Name>مهسا</Name>
				<MidName></MidName>
				<Family>پیداد</Family>
				<NameE>Mahsa</NameE>
				<MidNameE></MidNameE>
				<FamilyE>Peidad</FamilyE>
				<Organizations>
				<Organization>گروه مهندسی عمران، دانشکده فنی و مهندسی، دانشگاه خوارزمی، تهران، ایران</Organization>
				</Organizations>
				<Countries>
				<Country>ایران</Country>
				</Countries>
				<EMAILS>
				<Email></Email>
				</EMAILS>
			</AUTHOR>
		</AUTHORS>


		<KEYWORDS>
			<KEYWORD>
				<KeyText>Moving Bed Biofilm Reactor</KeyText>
			</KEYWORD>

			<KEYWORD>
				<KeyText>Aniline</KeyText>
			</KEYWORD>

			<KEYWORD>
				<KeyText>Surface Response Method</KeyText>
			</KEYWORD>

			<KEYWORD>
				<KeyText>Artificial Neural Network</KeyText>
			</KEYWORD>

			<KEYWORD>
				<KeyText>راکتور بیوفیلمی با بستر متحرک</KeyText>
			</KEYWORD>

			<KEYWORD>
				<KeyText>آنیلین</KeyText>
			</KEYWORD>

			<KEYWORD>
				<KeyText>روش پاسخ سطح</KeyText>
			</KEYWORD>

			<KEYWORD>
				<KeyText>شبکه عصبی مصنوعی</KeyText>
			</KEYWORD>
		</KEYWORDS>

		<REFRENCES>
			<REFRENCE>
				<REF>1. Delnavaz M, Ayati B, Ganjidoust H. Treatment of Wastewater Containing Aromatic Amine compounds Using Moving Bed Biofilm Reactor (MBBR), Master of Science thesis in Environmental Engineering, Tarbiat Modares University, 2017 [In Persian].##2. Bering S,   Mazur  J, Tarnowski  K, Janus M, Mozia S, Morawski A.W. The application of moving bed bio-reactor (MBBR) in commercial laundry wastewater treatment. Sci Total Environ, 2018;627: 1643-8.##3. Chen S, Sun F, Chung J.S. Treatment of pesticide wastewater by moving-bed biofilm reactor combined with Fenton-coagulation pretreatment. J. Hazard Mater, 2007;144(1-2): 577-84.##4. Devulapalli R, Jones F. Separation of aniline from aqueous solutions using emulsion liquid membranes. J. Hazard Mater, 1999;70(3):157–70.##5. Brillas E, Casado J. Aniline degradation by Electro-Fenton® and peroxi-coagulation processes using a flow reactor for wastewater treatment. Chemosphere 2002;47(3): 241-48.##6. Qi X.H, Zhuang Y.Y, Yuan Y.C, Gu W.X. Decomposition of aniline in supercritical water. J. Hazard Mater, 2002;90(1): 51-62.##7. Zangooei H, Delnavaz M, Asadollahfardi G. Prediction of coagulation and flocculation processes using ANN models and Fuzzy regression, Water Sci Technol, 2016;74(6): 1296-1311.##8. Qaderi, F, Sayahzadeh A,Azizi M. Efficiency optimization of petroleum wastewater treatment by using of serial moving bed biofilm reactors. J. Clean Prod, 2018;192: 665-77.##9. Navamani K.D, Aditya Narayana B.C, Arivazhagan M. Removal of high concentration of sulfate from pigment industry effluent by chemical precipitation using barium chloride: RSM and ANN modeling approach. J environ manage, 2010;206: 69-76.##10. Jaafarzadeh Haghighifard N,  Mehrabani Ardekani M.M,  Nabizadeh Nodehi R,  Yazdanbakhsh A.R. Optimization of Moving Bed Biofilm Reactor Using Taguchi Method, Iranian J Health and Environ, 2009;2(1): 1-14 [In Persian].##11. Zinatizadeh A, Ghaytooli E. Simultaneous nitrogen and carbon removal from wastewater at different operating conditions in a moving bed biofilm reactor (MBBR): process modeling and optimization. J Taiwan Inst Chem Eng, 2015;53: 98-111.##12. Jamali H.A, Dindarloo K, Panahi fard M, Moradnia M. Response Surface Methodology to Optimize Wastewater Treatment in Carpet Industries by Potassium Ferrate, Water Waste, 2018;29(2): 38-47 [In Persian].##13. Delnavaz M, Ayati B, Ganjidoust H. Prediction of Moving Bed Biofilm Reactor (MBBR) performance for treatment of aniline using artificial neural networks (ANN), J. hazard mater, 2010;179(1-3): 769-775. ##14. Montgomery D, Myers R. Response surface methodology: process and product optimization using designed experiments, Raymond H. Meyers, Douglas C. Montgomery, A Wiley-Interscience Publications, 2016.##15. Karimifard S, Alavi Moghaddam M.R. Application of response surface methodology in physicochemical removal of dyes from wastewater: A critical review, Sci Total Environ, 2018; 640–641: 772-97.##16. Nasr M.S, Moustafa M.A.E, Seif H.A.E, Kobrosy G.E.L. Application of Artificial Neural Network (ANN) for the prediction of EL-AGAMY wastewater treatment plant performance-EGYPT Alex Eng J, 2012;  51(1): 37-43.##17. Cohen S, Intrator N. Automatic model selection in a hybrid perceptron/ radial network, Inform Fusion, 2002;3(4): 259–66.## ##</REF>
			</REFRENCE>
		</REFRENCES>

	</ARTICLE>


	<ARTICLE> 
		<TitleF>ارزیابی شاخص‌های آلودگی منفرد و تلفیقی برخی فلزات سنگین در غبار اتمسفری راسب شونده پیرامون صنایع خاک چینی، کاشی سرامیک، شن ماسه و شیشه شهرستان اردکان در زمستان سال 1397</TitleF>
		<TitleE>Evaluation of Individual and Integrated Pollution Indices of Some Heavy Metals in Atmospheric Dust Deposition Around Khak-e-chini, Tile and Ceramic, Sand and Gravel and Glass in Ardakan County Industries in Winter 2018</TitleE>
		<TitleLang_ID>1</TitleLang_ID>
		<ABSTRACTS>
			<ABSTRACT>
			<Language_ID>1</Language_ID>
			<CONTENT>زمینه و هدف: تلاش برای اشتغال&#173; زایی در کشورهای در حال توسعه، هم سو با توسعه صنایع، فلزات سنگین به طور پیوسته به محیط زیست انتشار می&#173; یابند. این مطالعه با هدف سنجش غلظت فلزات سنگین و ارزیابی سطح آلودگی غبار اطراف تعدادی از صنایع با استفاده از شاخص&#173; های اکولوژیکی صورت گرفت.
روش کار: این مطالعه توصیفی تحلیلی و مقطعی در فصل زمستان با نصب 35 تله غبارگیر در اطراف صنایع خاک چینی، کاشی سرامیک، شن ماسه و شیشه در شهرستان اردکان انجام شد. با استفاده از دستگاه ICP-MS غلظت فلزات سنگین در غبار اندازه گیری شد. با استفاده از شاخص &#173;های فاکتور آلودگی (CF)، شاخص آلودگی (PI)، غنی شدگی (EF)، شاخص آستانه آلودگی (PIT)، قدر مطلق بردار شاخص آلودگی (PIvector)، شاخص آلودگی جدید (PIN)، شاخص آلودگی چند عنصره (MEC)، میانگین وزنی شاخص آلودگی (PIwAvg)، شاخص آلودگی تلفیقی (IPI)، فاکتور مواجهه (ExF) و نسبت میانگین محدوده اثرات میانه (MERMQ) سطح آلودگی غبار مورد ارزیابی و در GIS نسخه 5/10 پهنه بندی شد. 
یافته ها: میانگین غلظت فلزات سنگین در غبار به صورت روی (mg/kg 54/3310)&#62; سرب (mg/kg 28/137)&#62; مس (mg/kg 65/63)&#62; نیکل (mg/kg 91/45)&#62; آرسنیک (mg/kg 12/35)&#62; کبالت (mg/kg 73/13)&#62; مولیبدن (mg/kg 40/4) اندازه &#173;گیری شد. در کلیه ایستگاه&#8204;های نمونه برداری شاخص CF عناصر سرب، آرسنیک و روی در کلاس آلودگی بسیار بالا و شاخص PI سرب در کلاس آلودگی شدید قرار گرفت. فلز روی در 30 ایستگاه غنی شدگی خیلی بالا را نشان داد. برای کاربری حفاظت محیط زیست، شاخص PIT عنصر روی در کلیه ایستگاه&#8204;های نمونه برداری در کلاس آلودگی خیلی شدید قرار گرفت. همچنین بر اساس شاخص IPI کلیه ایستگاه&#8204;ها در کلاس شدیدا آلوده قرار گرفتند. فلزات سنگین در 32 ایستگاه بر اساس شاخص MERMQ، دارای 76 درصد سمیت و بر اساس شاخص PIN در کلاس آلوده بودند. بیشترین مقادیر شاخص&#8204;های MEC (43/3) و PIvector (93/35) در ایستگاه&#8204;های 1S و 15S، PIwAvg (27/42) در ایستگاه&#8204;های 1S و 12S و ExF (11/117) در&#160; ایستگاه 1S به دست آمد.
نتیجه &#173;گیری: بر اساس نتایج پهنه&#173; بندی تعدادی از شاخص &#173;های آلودگی، جهت باد غالب منطقه نقش مهمی در افزایش غلظت فلزات سنگین در ایستگاه&#8204;های پایین دست صنایع دارد.</CONTENT>
			</ABSTRACT>
			<ABSTRACT>
			<Language_ID>2</Language_ID>
			<CONTENT>Background and objective: Striving for employment in developing countries, as industries develop, heavy metals are released to the environment continuously. The purpose of this study was to measure heavy metal concentrations and to evaluate dust pollution levels in a number of industries using ecological indices.
Methods: This cross-sectional, descriptive-analytical study was conducted in winter by installing 35 dust traps around the industrial Khak-e-chini, Tile and Ceramic, Sand and Gravel and Glass in Ardakan county. The concentration of heavy metals in dust was measured by ICP-MS. The level of dust pollution was assessed using Contamination Factor, Pollution Index, Threshold Pollution Index, New Pollution Index, Vector Modulus of Pollution Index, Weighted Average of Pollution Index, Enrichment Factor, Multi-Element Contamination, Mean Effects Range-Median Quotient, Exposure Factor and Integrated pollution indices and it was zoned in GIS version 10.5.
Results: Mean heavy metal concentrations in dust were measured in the form of Zinc (3310.54 mg/kg)&#62; Pb (137.28 mg/kg)&#62; Copper (63.65 mg/kg)&#62; Nickel (45.91 mg/kg)&#62; Arsenic (35.12 mg/kg&#62; cobalt (13.73 mg/kg)&#62; molybdenum (4.40 mg/kg). In all sampling stations CF index of lead, arsenic and zinc elements was in very high pollution class and PI index in severe pollution class. Zinc metal showed very high enrichment at 30 stations. For environmental protection user, zinc element PIT index in all sampling stations was very severe in the pollution class. Also, all stations were in severe pollution class based on the IPI index. Based on MERMQ index the heavy metals at 32 stations had 76% toxicity and based on PIN index were in polluted class. Highest values of MEC (3.43) and PIvector (35.93) indices were obtained at S1 and S15 stations, PIwAvg (42.27) at S1 and S12 and ExF (117.11) at S1 stations.
Conclusion: Based on results of zoning a number of pollution indices, dominant downwind in region plays has important role in increase of concentration of heavy metals in downstream stations the industries.</CONTENT>
			</ABSTRACT>
		</ABSTRACTS>

		<PAGES>
			<PAGE>
			<FPAGE>314</FPAGE>
			<TPAGE>337</TPAGE>
			</PAGE>
		</PAGES>

		<RECEIVE_DATE>
			2020/05/132019/07/182020/06/282020/06/282020/06/282020/06/29
		</RECEIVE_DATE>

		<RECEIVE_DATE_FA>
			1399/4/9
		</RECEIVE_DATE_FA>

		<ACCEPT_DATE>
			2020/05/132020/01/52020/06/282020/06/282020/06/282020/06/29
		</ACCEPT_DATE>

		<ACCEPT_DATE_FA>
			1399/4/9
		</ACCEPT_DATE_FA>

		<AUTHORS>
			<AUTHOR>
				<Name>سعید</Name>
				<MidName></MidName>
				<Family>شجاعی برجوئی</Family>
				<NameE>Saeed</NameE>
				<MidNameE></MidNameE>
				<FamilyE>Shojaee Barjoee</FamilyE>
				<Organizations>
				<Organization>گروه محیط زیست، دانشگاه یزد، یزد، ایران</Organization>
				</Organizations>
				<Countries>
				<Country>ایران</Country>
				</Countries>
				<EMAILS>
				<Email></Email>
				</EMAILS>
			</AUTHOR>

			<AUTHOR>
				<Name>حمیدرضا</Name>
				<MidName></MidName>
				<Family>عظیم زاده</Family>
				<NameE>HamidReza</NameE>
				<MidNameE></MidNameE>
				<FamilyE>Azimzadeh</FamilyE>
				<Organizations>
				<Organization>گروه محیط زیست، دانشگاه یزد، یزد، ایران</Organization>
				</Organizations>
				<Countries>
				<Country>ایران</Country>
				</Countries>
				<EMAILS>
				<Email></Email>
				</EMAILS>
			</AUTHOR>

			<AUTHOR>
				<Name>اصغر</Name>
				<MidName></MidName>
				<Family>مصلح آرانی</Family>
				<NameE>Asghar</NameE>
				<MidNameE></MidNameE>
				<FamilyE>Mosleh Arani</FamilyE>
				<Organizations>
				<Organization>گروه محیط زیست، دانشگاه یزد، یزد، ایران</Organization>
				</Organizations>
				<Countries>
				<Country>ایران</Country>
				</Countries>
				<EMAILS>
				<Email></Email>
				</EMAILS>
			</AUTHOR>
		</AUTHORS>


		<KEYWORDS>
			<KEYWORD>
				<KeyText>Heavy metals</KeyText>
			</KEYWORD>

			<KEYWORD>
				<KeyText>Industries</KeyText>
			</KEYWORD>

			<KEYWORD>
				<KeyText>Pollution indices</KeyText>
			</KEYWORD>

			<KEYWORD>
				<KeyText>Atmospheric dust deposition</KeyText>
			</KEYWORD>

			<KEYWORD>
				<KeyText>فلزات سنگین</KeyText>
			</KEYWORD>

			<KEYWORD>
				<KeyText>صنایع</KeyText>
			</KEYWORD>

			<KEYWORD>
				<KeyText>شاخص‌های آلودگی</KeyText>
			</KEYWORD>

			<KEYWORD>
				<KeyText>غبار اتمسفری راسب شونده</KeyText>
			</KEYWORD>
		</KEYWORDS>

		<REFRENCES>
			<REFRENCE>
				<REF>1.	Neurosis B, Rostamy N, Tavakoli M, Rostami nia M. Evaluation of polluting industries effects on soil heavy metals (Case Study: Ilam Cement Factory). Geo and Enviro Studies 2016;5(19): 100-89 [In Persian].##2.	Shojaee Barjoee S, Azimzadeh H, kuchakzadeh MR, et al. Dispersion and Health Risk Assessment of PM10 Emitted from the Stacks of a Ceramic and Tile industry in Ardakan, Yazd, Iran, Using the AERMOD Model. Iran South Med J 2019;22(5): 317-32 [In Persian].##3.	Kamani H, Hoseini M, Safari Gh, al. e. Concentrations of Heavy Metals in surface soil of Zahedan City. J Health 2017;8(2): 182-90 [In Persian].##4.	Shojaee Barjoee S, Azimzadeh H, MoslehArani A, Kuchakzadeh M. Occupational monitoring and health risks assessment of respiratory exposure to dust in an industrial unit of production Khak-e-Chini. Occup Med 2019;11(3): 14-25 [In Persian].##5.	Kuo CC HB, Umans JG, et al. Arsenic exposure, arsenic metabolism, and incident diabetes in the strong heart study. Diabetes Care 2015;38(4): 620-7.##6.	Thongsringklee M, Robson MG, Siriwong W. Health effects of low level exposure to lead among communication radio repair workers at Samutsakhon province, Thailand. HERAJ 2020: 1-8.##7.	Attaeian B, Mortazavi S, Farokhzadeh B, M. K. Evaluation and Mapping Spatial distribution of Copper Pollution in Soil and Water of Vineyard Garden. J Environ Health Eng 2019;6(3): 293-310.##8.	Gupta P. Toxic Effects of Metals and Micronutrients.  Concepts and Applications in Veterinary Toxicology: Springer; 2019. p. 83-119.##9.	Genchi G, Carocci A, Lauria G, et al. Nickel: Human Health and Environmental Toxicology. Int J Environ Res Publ Health 2020;17(3): 679.##10.	Leyssens L VB, Van Der Straeten C, et al,. Cobalt toxicity in humans—A review of the potential sources and systemic health effects. Toxicology 2017(387): 43-56.##11.	Jiang X, Lu W, Zhao H, et al. Potential ecological risk assessment and prediction of soil heavy-metal pollution around coal gangue dump. Nat Hazards Earth Syst Sci 2014;14(6): 1599-610.##12.	Raheleh H KM, Khodai k, shahsawary AA, et al. Evaluation of pollution and ecological risk of heavy metals in surface soils around granitoids of Ahar-East Azarbaijan region. Res Earth Sci 2016;7(26): 1-20 [In Persian].##13.	US EPA. Guidelines for ecological risk assessment: EPA/630/R‐95/002F. Fed Regist 1998;63(93): 26846-924.##14.	Weissmannova, Helena Dolezalova, Pavlovsky Jirl. Indices of soil contamination by heavy metals–methodology of calculation for pollution assessment (minireview). Environ Monit Assess 2017;189(12): 616.##15.	Wu J, Teng Y, Lu S, et al. Evaluation of soil contamination indices in a mining area of Jiangxi, China. PloS one 2014;9(11): e112917.##16.	Ravankhah N, Mirzaei R, Masoum S. Evaluation of geoaccumulation index, contamination factor, and principal component analysis for estimating soil contamination. Iran J Health Environ 2015;8(3): 345-56 [In Persian].##17.	Yadegarnia Naeini F, Azimzadeh HR, Mosleh Arani A, et al. Ecological risk assessment of heavy metals from cement factory dust. Environ Health Engin Manag J 2019;6(2): 1-9.##18.	Siyahati Ardakani GhR, Mirsanjari M, Azimzadeh HR, Solgi E. The environmental assessment of some heavy metals in surface soil around pelletizing industries and Ardakan steel. Iran J Health Environ 2018;11(3): 464-49 [In Persian].##19.	Huang S, Yuan C, Li Q, et al. Distribution and risk assessment of heavy metals in soils from a typical Pb-Zn mining area. Polish J Environ Studies 2017 26(3): 1105-12.##20.	Kwata MG. Comparison of methods for measurement of dust deposition in South African mining sectors (Doctoral dissertation, University of Pretoria). University of Pretoria; 2014.##21.	Wysocka I, Vassileva E. Determination of cadmium, copper, mercury, lead and zinc mass fractions in marine sediment by isotope dilution inductively coupled plasma mass spectrometry applied as a reference method. 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		</REFRENCES>

	</ARTICLE>


	<ARTICLE> 
		<TitleF>بررسی کارایی هیدروکسید لایه‌ای منیزیم-آلومینیوم سنتز شده جهت حذف یون کلرید از پساب سرب و روی انگوران زنجان</TitleF>
		<TitleE>Investigation of the Adsorption Efficacy in Removal of Chloride Ions by Synthesized magnesium–aluminum hydroxide from Zanjan Lead &Zinc Industry wastewater</TitleE>
		<TitleLang_ID>1</TitleLang_ID>
		<ABSTRACTS>
			<ABSTRACT>
			<Language_ID>1</Language_ID>
			<CONTENT>زمینه و هدف: آنیون&#8204;های خورنده در پساب&#8204;های صنعتی می&#8204;توانند مشکلات عدیده&#8204;ای را به لحاظ محیط زیستی و اقتصادی به همراه داشته باشند. در این مطالعه هیدروکسید لایه&#8204;ای منیزیم و آلومینیوم با بار اضافی مثبت سنتز شد و جهت جذب یون&#8204;های کلرید از پساب سرب و روی انگوران زنجان مورداستفاده قرار گرفت. 
مواد و روش&#8204;ها: جهت سنتز، نیترات منیزیم (Magnesium Nitrate) و نیترات آلومینیوم (Aluminum Nitrate) با نسبت مولی4 مخلوط شدند. ماده بلورین سنتز شده با آنالیز پراش اشعه ایکس (XRD) و میکروسکوپ الکترونی روبشی به همراه طیف&#8204;سنجی پراش انرژی، طیف&#8204;سنجی مادون&#8204;قرمز و اندازه&#8204;گیری پتانسیل زتا سطح جاذب موردبررسی قرار گرفت. 
یافته&#8204;ها: نتایج پراش اشعه ایکس ساختار لایه&#8204;ای هیدروکسید منیزیم-آلومینیوم را تایید کرد که&#160; قبل و بعد از جذب تفاوت چندانی به لحاظ ساختار بلورین ایجاد نشده و تنها فاصله بین لایه&#8204;ها تغییر پیداکرده است. تصاویر میکروسکوپ الکترونی روبشی متراکم شدن جاذب بعد از جذب یون کلرید را نشان داد و همچنین طیف&#8204;سنجی پراش انرژی وجود یون&#8204;های کلرید و ترسیب یون کلسیم بعد از جذب را تائید نمود. اندازه&#8204;گیری زتا پتانسیل، بار مثبت سطح جاذب را تایید کرد. یافته&#8204;های حاصل از جذب نشان دادند که با توجه به اینکه جذب از طریق برقراری برهمکنش میان بار مثبت اضافی در لایه&#8204;های جاذب و آنیون موجود صورت می&#8204;گیرد میزان جذب و حذف یون کلرید از پساب به وجود این بار اضافی بستگی دارد. مطالعات ایزوترم جذب تطابق داده&#8204;های تجربی با مدل لانگمویر را نشان داد که نشان&#8204;دهنده وجود برهمکنش میان جاذب و جذب&#8204;شونده است و حداکثر ظرفیت جذب برای نسبت Mg/Al برابر با 4 در دمای C&#176;60 mg/g 8/153 تعیین شد. مرحله تعیین&#8204;کننده سرعت مرحله برقراری برهمکنش میان یون&#8204;های کلرید و هیدروکسید لایه&#8204;ای آلومینیوم-منیزیم تعیین شد. نتایج نشان دادند با افزایش میزان جاذب از 5/1 تا 5/4 گرم میزان جذب افزایش می&#8204;یابد و زمان تعادل از 90 دقیقه در 5/1 گرم جاذب به 4 ساعت در&#160; 5/4 گرم افزایش می&#8204;یابد. درنهایت مطالعات ترمودینامیکی خود به خودی بودن فرایند جذب و قوی&#8204;تر شدن برهمکنش میان جاذب و جذب&#8204;شونده با افزایش دما را نشان داد. 
&#160;نتیجه&#8204;گیری: حذف یون کلرید از طریق تثبیت آن در لایه&#8204;های هیدروکسید آلومینیوم-منیزیم می&#8204;تواند راهکار خوبی جهت کاهش یون کلرید از پساب صنعتی سرب و روی زنجان باشد زیرا که کلرید هیدروکسید آلومینیوم-منیزیم به&#8204;دست&#8204;آمده نسبت به یون کلر اضافی نفوذناپذیر بوده و می&#8204;تواند به&#8204;عنوان ملات ساختمانی در سازه&#8204;های دریایی به&#8204;خوبی استفاده شود.</CONTENT>
			</ABSTRACT>
			<ABSTRACT>
			<Language_ID>2</Language_ID>
			<CONTENT>Background and Purpose: The presence of corrosive anions in industrial wastewater can have many environmental and economic problems.
Materials and methods: In this study, layered magnesium&#8211;aluminum oxide was synthesized which has an extra positive charge and was used for adsorption of chloride ions from waste-water of lead and zinc industry.
Results:&#160;The synthesized crystalline material was investigated by X-ray diffraction spectroscopy, Scanning electron microscopy- energy dispersive spectroscopic analysis. X-ray diffraction spectroscopy results showed that there was no difference in the crystalline structure before and after chloride ion adsorption. Scanning electron microscopy- energy dispersive spectroscopic analysis showed the condensation of adsorbent after chloride ions adsorption and EDX analysis confirmed the presence of chloride and precipitation of Ca2+ ions after adsorption. Measurement of zeta-potential for synthesized layered magnesium&#8211;aluminum hydroxide confirmed the positive surface charge. Isotherm studies have shown the compatibility of experimental data with the Langmuir model, which indicates the interaction between adsorbent and chloride ions, the maximum adsorption capacity for the synthesized adsorbent with Mg / Al ratio of 4 was determined 153.8 mg/g at 60 &#176; C. The obtained values showed the intercalation rate follows pseudo-second-order. The experimental data confirmed adsorption capacity has been increased with increasing the adsorbent dosage from 1.5 to 4.5 gr and the equilibrium time increased from 90 min. to 4 h from 1.5 g adsorbent to 4.5 g. Thermodynamic studies revealed the adsorption occurs spontaneously and positive entropy changes indicated strengthening the interaction between adsorbent and chloride ions with increasing the temperature from 25 to 60&#176;C.
Conclusion: Finally, it can be concluded synthesized double layered Al-Mg hydroxide can be a good candidate to reduce chlorine ions from lead and zinc Industry wastewaters.</CONTENT>
			</ABSTRACT>
		</ABSTRACTS>

		<PAGES>
			<PAGE>
			<FPAGE>338</FPAGE>
			<TPAGE>355</TPAGE>
			</PAGE>
		</PAGES>

		<RECEIVE_DATE>
			2020/05/132019/07/182020/06/282020/06/282020/06/282020/06/292020/06/29
		</RECEIVE_DATE>

		<RECEIVE_DATE_FA>
			1399/4/9
		</RECEIVE_DATE_FA>

		<ACCEPT_DATE>
			2020/05/132020/01/52020/06/282020/06/282020/06/282020/06/292020/06/29
		</ACCEPT_DATE>

		<ACCEPT_DATE_FA>
			1399/4/9
		</ACCEPT_DATE_FA>

		<AUTHORS>
			<AUTHOR>
				<Name>بهار</Name>
				<MidName></MidName>
				<Family>حاجی سامی</Family>
				<NameE>Bahar</NameE>
				<MidNameE></MidNameE>
				<FamilyE>Hajisami</FamilyE>
				<Organizations>
				<Organization>دانش آموخته کارشناسی ارشد مهندسی عمران-محیط‌زیست، گروه محیط‌زیست انسانی، دانشکده محیط‌زیست، کرج، ایران</Organization>
				</Organizations>
				<Countries>
				<Country>ایران</Country>
				</Countries>
				<EMAILS>
				<Email></Email>
				</EMAILS>
			</AUTHOR>

			<AUTHOR>
				<Name>سمیه</Name>
				<MidName></MidName>
				<Family>محمدی</Family>
				<NameE>Somayeh</NameE>
				<MidNameE></MidNameE>
				<FamilyE>Mohammadi</FamilyE>
				<Organizations>
				<Organization>استادیار، گروه محیط‌زیست انسانی، دانشکده محیط‌زیست، کرج، ایران</Organization>
				</Organizations>
				<Countries>
				<Country>ایران</Country>
				</Countries>
				<EMAILS>
				<Email></Email>
				</EMAILS>
			</AUTHOR>

			<AUTHOR>
				<Name>روانبخش</Name>
				<MidName></MidName>
				<Family>شیردم</Family>
				<NameE>Ravanbakhsh</NameE>
				<MidNameE></MidNameE>
				<FamilyE>Shirdam</FamilyE>
				<Organizations>
				<Organization>استادیار، گروه محیط‌زیست انسانی، دانشکده محیط‌زیست، کرج، ایران</Organization>
				</Organizations>
				<Countries>
				<Country>ایران</Country>
				</Countries>
				<EMAILS>
				<Email></Email>
				</EMAILS>
			</AUTHOR>
		</AUTHORS>


		<KEYWORDS>
			<KEYWORD>
				<KeyText>Chloride ions adsorption</KeyText>
			</KEYWORD>

			<KEYWORD>
				<KeyText>Adsorption isotherms</KeyText>
			</KEYWORD>

			<KEYWORD>
				<KeyText>Adsorption kinetics</KeyText>
			</KEYWORD>

			<KEYWORD>
				<KeyText>هیدروکسید دوگانه لایه‌ای</KeyText>
			</KEYWORD>

			<KEYWORD>
				<KeyText>جذب یون‌های کلرید</KeyText>
			</KEYWORD>

			<KEYWORD>
				<KeyText>ایزوترم جذب</KeyText>
			</KEYWORD>

			<KEYWORD>
				<KeyText>سینتیک جذب</KeyText>
			</KEYWORD>

			<KEYWORD>
				<KeyText>پتانسیل تا</KeyText>
			</KEYWORD>
		</KEYWORDS>

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	<ARTICLE> 
		<TitleF>ارزیابی آلودگی محیط‌زیستی عناصر کمیاب در نهشت اتمسفری شهر کرج با استفاده از ضریب غنی شدگی و شاخص مخاطره اکولوژیکی  در سال 1397</TitleF>
		<TitleE>Assessment of the Environmental Pollution of Trace Elements in Atmospheric Deposition of Karaj City Using Enrichment Factor and Ecological Risk Index in 2018</TitleE>
		<TitleLang_ID>1</TitleLang_ID>
		<ABSTRACTS>
			<ABSTRACT>
			<Language_ID>1</Language_ID>
			<CONTENT>زمینه و هدف: نهشت اتمسفری تاثیر قابل&#173; توجهی بر آلودگی محیط&#173;زیستی و سلامت انسان به &#173;دلیل نقش آن در مکانیسم&#173; های انتقال آلاینده&#173; ها دارد. اهداف این مطالعه، بررسی غلظت&#173; ها، منابع و مخاطرات اکولوژیکی عناصر کمیاب در نهشت اتمسفری شهر کرج بود.
مواد و روش&#173;ها: 18 نمونه نهشت اتمسفری از پشت بام ساختمان&#173;های موجود در شش منطقه کرج برداشته شد و سپس غلظت عناصر کروم، مس، روی، نیکل و لیتیم و عناصر کبالت و سرب به&#173; ترتیب به روش طیف&#173;سنجی نشری جفت شده القایی (ICP-OES) و طیف&#173;سنجی جرمی جفت شده القایی (ICP-MS) آنالیز شدند. آنالیز&#173;های همبستگی پیرسون، تجزیه واریانس یک طرفه و تحلیل عاملی برای شناسایی منابع احتمالی عناصر کمیاب استفاده شدند.
یافته ها: میانگین غلظت عناصر مطالعه شده به &#173;صورت سرب، روی، مس، کروم، نیکل، کبالت و لیتیم به ترتیب 73/184، 75/931، 61/94، 79/98، 90/83، 05/21 و 71/24 &#956;g/g بودند. همچنین نتایج نشان داد ضرایب غنی &#173;شدگی (EF) عناصر سرب و روی بالا؛ عناصر مس، نیکل و کروم متوسط بودند، در&#173;حالی&#173;که کبالت غیر آلوده بود. بر اساس آنالیز&#173;های آماری، عناصر کمیاب می&#173; توانند ناشی از منابع متعدد انسانی (منابع نقلیه&#173; ای، انتشارات صنعتی و احتراق سوخت&#173; های فسیلی) &#160;و طبیعی باشند. عناصر روی و مس دارای بیش&#173;ترین غلظت در ایستگاه &#173;های با ترافیک بالا به&#173; ویژه ایستگاه کارخانه &#173;قند در مرکز شهر بودند. بیشینه غلظت کروم، نیکل و کبالت در ایستگاه فردیس در مجاورت نیروگاه برق شهر کرج مشاهده شد. ایستگاه&#173; های صنعتی شامل کمال&#173; شهر، محمد&#173;شهر و ماهدشت بیش&#8204;ترین مقادیر سرب را نشان دادند. در نهایت، شاخص خطر (RI) نشان داد کلیه ایستگاه&#173; های مطالعه شده به استثنای کمال&#173; شهر که ریسک قابل ملاحظه &#173;ای داشت، دارای مخاطره بالقوه پایین هستند.
نتیجه گیری: شهر کرج تحت&#173; تاثیر منابع متعدد انسانی آلودگی محیط&#173;زیستی است که مشکلاتی زیادی را برای سلامت انسان ایجاد می&#173;کنند و آلاینده&#173; ها با افزایش تراکم جمعیتی افزایش یافته&#173; اند. بنابراین ما پایش مداوم عناصر کمیاب به&#173; ویژه سرب و روی را به&#173; منظور کنترل منابع انتشار آن&#173;ها توصیه می&#173; نماییم.</CONTENT>
			</ABSTRACT>
			<ABSTRACT>
			<Language_ID>2</Language_ID>
			<CONTENT>Background: Atmospheric deposition has a significant influence on environmental pollution and human health because of its role on transport mechanisms. The aims of this study were the determination of Concentrations, Sources and Ecological Risks of trace elements in atmospheric deposition of Karaj City, Iran.
Method: 18 atmospheric deposition samples were collected from the flat roof of buildings in six districts and then, the concentration of elements including Cu, Zn, Cr, Ni, Li and other (Co and Pb) were analyzed by Inductively Coupled Plasma Optical Emission Spectroscopy (ICP-OES) and Inductively Coupled Plasma Mass Spectrometry (ICP-MS), respectively. Pearson Correlation, One-Way ANOVA and Factor Analyses were used to identify probable sources of the trace elements.
Results: The mean concentrations of Pb, Zn, Cu, Cr, Ni, Co, and Li were 184.73, 931.75, 94.61, 98.79, 83.90, 21.05 and 24.71 &#956;g/g, respectively. Also, the result showed the Enrichment Factors (EF) of Pb and Zn were high; Cr, Ni, and Cu were moderate while Co was unpolluted. Based on statistical analyses, trace elements could be originated from several anthropogenic (Vehicular Sources, Industrial Emissions and Fossil Fuel Combustion) and natural sources. Zn and Cu showed the highest concentrations at high-traffic stations, especially at Karkhene-Ghand located in city center. Maximum concentrations of Cr, Ni, and Co were observed at Fardis Station closed to Karaj Power Plant. Industrial Stations including Kamalshahr, Mohammadshahr, and Mahdasht had the most amount of Pb. Finally, Risk index (RI) showed all studied stations had low potential risk except of Kamalshar with a considerable risk.
Conclusion: Karaj has influenced by several anthropogenic sources of environmental pollution that are created many human health problems and the pollutants have increased with the population density. Therefore, we would have suggested the continuous monitoring of trace elements, especially Pb and Zn to control of the emission sources.</CONTENT>
			</ABSTRACT>
		</ABSTRACTS>

		<PAGES>
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			<FPAGE>356</FPAGE>
			<TPAGE>375</TPAGE>
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		</PAGES>

		<RECEIVE_DATE>
			2020/05/132019/07/182020/06/282020/06/282020/06/282020/06/292020/06/292020/06/29
		</RECEIVE_DATE>

		<RECEIVE_DATE_FA>
			1399/4/9
		</RECEIVE_DATE_FA>

		<ACCEPT_DATE>
			2020/05/132020/01/52020/06/282020/06/282020/06/282020/06/292020/06/292020/06/29
		</ACCEPT_DATE>

		<ACCEPT_DATE_FA>
			1399/4/9
		</ACCEPT_DATE_FA>

		<AUTHORS>
			<AUTHOR>
				<Name>رخساره</Name>
				<MidName></MidName>
				<Family>عظیمی یانچشمه</Family>
				<NameE>Rokhsareh</NameE>
				<MidNameE></MidNameE>
				<FamilyE>Azimi  Yancheshmeh</FamilyE>
				<Organizations>
				<Organization>دانشجوی دکتری، گروه محیط زیست، دانشکده منابع طبیعی، دانشگاه تهران، کرج، ایران</Organization>
				</Organizations>
				<Countries>
				<Country>ایران</Country>
				</Countries>
				<EMAILS>
				<Email></Email>
				</EMAILS>
			</AUTHOR>

			<AUTHOR>
				<Name>مظاهر</Name>
				<MidName></MidName>
				<Family>معین الدینی</Family>
				<NameE>Mazaher</NameE>
				<MidNameE></MidNameE>
				<FamilyE>Moeinaddini</FamilyE>
				<Organizations>
				<Organization>استادیار، گروه محیط زیست، دانشکده منابع طبیعی، دانشگاه تهران، کرج، ایران</Organization>
				</Organizations>
				<Countries>
				<Country>ایران</Country>
				</Countries>
				<EMAILS>
				<Email></Email>
				</EMAILS>
			</AUTHOR>

			<AUTHOR>
				<Name>سادات</Name>
				<MidName></MidName>
				<Family>فیض نیا</Family>
				<NameE>Sadat</NameE>
				<MidNameE></MidNameE>
				<FamilyE>Feyz Nia</FamilyE>
				<Organizations>
				<Organization>استاد، گروه احیای مناطق خشک و بیابانی، دانشکده منابع طبیعی، دانشگاه تهران، کرج، ایران</Organization>
				</Organizations>
				<Countries>
				<Country>ایران</Country>
				</Countries>
				<EMAILS>
				<Email></Email>
				</EMAILS>
			</AUTHOR>

			<AUTHOR>
				<Name>رضا</Name>
				<MidName></MidName>
				<Family>شهبازی</Family>
				<NameE>Reza</NameE>
				<MidNameE></MidNameE>
				<FamilyE>Shahbazi</FamilyE>
				<Organizations>
				<Organization>دکتری منابع طبیعی، مرکز پژوهش‌های کاربردی زمین شناسی، سازمان زمین شناسی و اکتشافات معدنی کشور، تهران، ایران</Organization>
				</Organizations>
				<Countries>
				<Country>ایران</Country>
				</Countries>
				<EMAILS>
				<Email></Email>
				</EMAILS>
			</AUTHOR>
		</AUTHORS>


		<KEYWORDS>
			<KEYWORD>
				<KeyText>Trace elements</KeyText>
			</KEYWORD>

			<KEYWORD>
				<KeyText>Karaj</KeyText>
			</KEYWORD>

			<KEYWORD>
				<KeyText>Ecological risk</KeyText>
			</KEYWORD>

			<KEYWORD>
				<KeyText>Atmospheric deposition</KeyText>
			</KEYWORD>

			<KEYWORD>
				<KeyText>عناصر کمیاب</KeyText>
			</KEYWORD>

			<KEYWORD>
				<KeyText>مخاطره اکولوژیکی</KeyText>
			</KEYWORD>

			<KEYWORD>
				<KeyText>کرج</KeyText>
			</KEYWORD>

			<KEYWORD>
				<KeyText>نهشت اتمسفری</KeyText>
			</KEYWORD>
		</KEYWORDS>

		<REFRENCES>
			<REFRENCE>
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			</REFRENCE>
		</REFRENCES>

	</ARTICLE>

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