پیوندهای مفید
آمار
| تعداد نشریات | 21 |
| تعداد شمارهها | 697 |
| تعداد مقالات | 10,088 |
| تعداد مشاهده مقاله | 71,229,851 |
| تعداد دریافت فایل اصل مقاله | 62,958,858 |
بررسی تخریب پی نیتروفنول در راکتور بستر پر شده چرخان در حضور واکنشگر فنتون | ||
| شیمى کاربردى روز | ||
| دوره 18، شماره 66، فروردین 1402، صفحه 79-98 اصل مقاله (1 M) | ||
| نوع مقاله: مقاله علمی پژوهشی | ||
| شناسه دیجیتال (DOI): 10.22075/chem.2022.25076.2022 | ||
| نویسندگان | ||
| مریم قربانی آقبلاغی؛ مهدیه ابوالحسنی* | ||
| دانشکده مهندسی شیمی، نفت و گاز، دانشگاه سمنان، سمنان، ایران | ||
| تاریخ دریافت: 08 آبان 1400، تاریخ بازنگری: 09 اسفند 1400، تاریخ پذیرش: 15 فروردین 1401 | ||
| چکیده | ||
| در این مقاله به بررسی تخریب پی نیترو فنول (PNP) از طریق فناوری گرانش بالا در حضور واکنشگر فنتون پرداخته شده است. در این فرایند از یک راکتور بستر پر شده چرخان با پکینگ تیغهای شامل دوازده تیغه استفاده شد. هدف از این کار بررسی اثر pH (3، 4 و 5)، همچنین سرعت چرخش بستر پر شده چرخان (600، 800، 1000 و 1200 دور بر دقیقه)، سرعت جریان ورودی مایع (50 و100 لیتر بر ساعت)، مقدار هیدروژن پراکسید (1/25، 2/25، 3/25 و 4/25 میلی لیتر) و غلظت سولفات آهن هفت آبه (0/1، 0/3، 0/4، 0/5 و0/6 میلیمولار ) بر میزان تخریب PNP میباشد. محلول اولیه حاوی100 میلی گرم بر لیتر PNP است. نتایج نشان داد که افزایش بیش از حد سرعت چرخش (بیش از 800 دور بر دقیقه) و افزایش نرخ جریان ورودی مایع به 100 لیتر بر ساعت کمکی به تخریب آلاینده نمیکند و موجب کاهش بازده حذف PNP میشود. افزایش مقدار هیدروژن پر اکسید از 1/25 تا 3/25 میلی لیتر موجب بهبود تخریب آلاینده میشود ولی افزایش این مقدار به 4/25 کمکی به بهبود فرایند حذف PNP نمیکند. افزایش غلظت سولفات آهن هفت آبه از 0/1 تا 0/5 میلی مولار موجب کاهش زمان تخریب PNP میشود ولی افزایش غلظت به 0/6 میلی مولار نتیجه عکس دارد. در بهترین حالت، یعنی pH برابر 5، سرعت چرخش800 دور بر دقیقه، سرعت جریان ورودی مایع برابر 50 لیتر بر ساعت، غلظت +Fe2 برابر 0/5میلی مولار و مقدار H2O2 برابر 3/25 میلی لیتر، PNP در 70 دقیقه به طور کامل (100%) تخریب شد. | ||
| کلیدواژهها | ||
| راکتور بستر پرشده چرخان؛ اکسیداسیون فنتون؛ تصفیه آب؛ پی نیتروفنول | ||
| عنوان مقاله [English] | ||
| Investigation of p-nitrophenol degradation in a rotating packed bed reactor in the presence of Fenton reagent | ||
| نویسندگان [English] | ||
| Maryam Ghorbani Aghbolaghi؛ Mahdieh Abolhasani | ||
| Faculty of Chemical, Petroleum and Gas Engineering, Semnan University, Semnan, Iran | ||
| چکیده [English] | ||
| In this paper, the degradation of p-nitrophenol (PNP) by high gravity technology in the presence of Fenton reagent is investigated. In this process, a rotating packed bed reactor with a blade packing consisting of twelve blades was used. The purpose of this study was to investigate the effect of pH (3, 4, and 5), as well as the rotational speed of the rotating packed bed (600, 800, 1000, and 1200 rpm), the flow rate of inlet liquid (50 and 100 l/h), the dosage of hydrogen peroxide (1.25, 2.25, 3.25 and 4.25 ml) and the concentration of ferrous sulfate (0.1, 0.3, 0.4, 0.5 and 0.6 mM) on the PNP degradation. The initial solution contains 100 mg / l PNP. The results showed that excessive increase of rotational speed (more than 800 rpm) and increase of liquid inlet flow rate to 100 l/h did not contribute to the degradation of pollutant and reducing PNP removal efficiency. Increasing the amount of hydrogen peroxide from 1.25 to 3.25 ml improves the degradation of the pollutant, but increasing this amount to 4.25 does not help to improve the PNP removal process. Increasing the concentration of ferrous sulfate from 0.1 to 0.5 mM reduces the degradation time of the contaminant, but increasing the concentration to 0.6 mM has the opposite effect. In the best case, ie pH 5, the rotational speed of 800 rpm, the liquid inlet flow rate of 50 l/h, Fe2 + concentration of 0.5 mM, and H2O2 of 3.25 ml, PNP in 70 minutes destroyed completely (100%). | ||
| کلیدواژهها [English] | ||
| Rotating packed bed reactor, Fenton oxidation, Water treatment, P-nitrophenol | ||
| مراجع | ||
|
[1] Sittig, M. (1977). How to remove pollutants and toxic materials from air and water. Noyes Data Corp.
[2] Nemerow, N. L. (1978). Industrial water pollution: origins, characteristics and treatment. Addison- Wesley, Reading, Massachusetts, pp. 738.
[3] Kumaran, P., & Paruchuri, Y. (1997). Kinetics of phenol biotransformation. Water Research, 31(1), 11-22.
[4] Bowers Jr, G. N., McComb, R. B., Christensen, R., & Schaffer, R. (1980). High-purity 4-nitrophenol: purification, characterization, and specifications for use as a spectrophotometric reference material. Clinical Chemistry, 26(6), 724-729.
[5] Tang, L., Tang, J., Zeng, G., Yang, G., Xie, X., Zhou, Y., Pang, Y., Fang, Y., Wang, J., & Xiong, W. (2015). Rapid reductive degradation of aqueous p-nitrophenol using nanoscale zero-valent iron particles immobilized on mesoporous silica with enhanced antioxidation effect. Applied Surface Science, 333(1), 220-228.
[6] Ji, Q., Li, J., Xiong, Z., & Lai, B. (2017). Enhanced reactivity of microscale Fe/Cu bimetallic particles (mFe/Cu) with persulfate (PS) for p-nitrophenol (PNP) removal in aqueous solution. Chemosphere, 172, 10-20.
[7] Lin, X. Q., Kong, W. M., & Lin, X. (2020). Degradation of high-concentration p-nitrophenol by Fenton oxidation. Water Science & Technology, 81(10), 2260-2269.
[8] Ramshaw, C., & Mallinson, R. H. (1981). Mass transfer process, US Patents.
[9] Shi, X., Xiang, Y., Wen, L.-X., & Chen, J.-F. (2013). CFD analysis of liquid phase flow in a rotating packed bed reactor. Chemical Engineering Journal, 228, 1040-1049.
[10] Yuan, Z., Song, W., Liu, Y., Kang, X., Peng, B., & Wang, T. (2014). Regeneration of SO2-loaded Sodium Phosphate solution in rotating packed bed. Journal of Chemical Engineering of Japan, 47(10), 777-781.
[11] Jiao, W., Liu, Y., & Qi, G. (2010). A new impinging stream–rotating packed bed reactor for improvement of micromixing iodide and iodate. Chemical Engineering Journal, 157(1), 168-173.
[12] Dobie, C. G., & Boodhoo, K. V. (2013). An evaluation of the effectiveness of continuous thin film processing in a spinning disc reactor for bulk free-radical photo-copolymerisation. Chemical Engineering and Processing: Process Intensification, 71, 97-106.
[13] Chang, C.-F., & Lee, S.-C. (2012). Adsorption behavior of pesticide methomyl on activated carbon in a high gravity rotating packed bed reactor. Water Research, 46(9), 286-2880.
[14] Jiao, W., Luo, S., He, Z., & Liu, Y. (2017). Applications of high gravity technologies for wastewater treatment: A review. Chemical Engineering Journal, 313, 912-927.
[15] Peel, J., Howarth, C., & Ramshaw, C. (1998). Process Intensification: Higee Seawater Deaeration. Chemical Engineering Research and Design, 76(5), 585-593.
[16] Haghighi Asl, A., Ahmadpour, A., Fallah, N. (2016). Photocatalytic treatment of spent caustic wastewater in petrochemical industries. Advances in Environmental Technology, 2(3), 153-168.
[17] Mozafari, E., Saki, A., Faghihi, A., & Fathinia, S. (2017). Journal of Environmental Science and Technology, 19(5), 157-167 (In persian).
[18] Neyens, E., & Baeyens, J. (2003). A review of classic Fenton’s peroxidation as an advanced oxidation technique. Journal of Hazardous Materials, 98(1-3), 33-50.
[19] Zeng, Z., Zou, H., Li, X., Sun, B., Chen, J., & Shao, L. (2012). Chemical Engineering and Processing: Process Intensification, 60, 1-8.
[20] Bigda, R. J. (1995). Consider Fentons chemistry for wastewater treatment. Chemical Engineering Progress, 91(12), 62-66.
[21] Kazemi, M., & Abolhasani, M. (2020). Experimental investigation of ultrasound/ Fenton’s reagent oxidation process on the degradation rate constant of p- nitrophenol. Journal of Applied Chemistry, 14(53), 31-42.
[22] Mehrdad, A., Farkhondeh, S., & Hasaspoor, F. (2018). Kinetic study of sonocatalytic degradation of Methylene blue by sonofenton process. Journal of Applied Chemistry, 12(45), 83-89.
[23] Rahman Setayesh, S., Nazari, P., & Askari, N. (2019). Kinetics investigation of environmental pollutants degradation using Fenton process in the presence of iron oxide nanoparticles. Journal of Applied Chemistry, 14(52), 183-198. (In Persian)
[24] Zeng, Z., Zou, H., Li, X., Arowo, M., Sun, B., Chen, J., Chu, G., & Shao, L. (2013). Degradation of phenol by ozone in the presence of Fenton reagent in a rotating packed bed. Chemical Engineering Journal, 229, 404-411.
[25] Lin, M.-L., Zhao, Z.-W., Cui, F.-Y., Wang, Y., & Xia, S. (2012). Effects of initial chlorobenzene concentration, air flowrate and temperature on mass transfer of chlorobenzene by air stripping. Desalination and Water Treatment, 40(1-3), 215-223.
[26] Sulimov, A. A, Ermolaev, B. S., Turuntaev, S. B., Borisov, A. A., & Sukoyan, M. K. (2014). Detonation of explosive Proppant: RDX-containing water-saturated sand. Russian Journal of Physical Chemistry B, 8, 338-344.
[27] Qin, Y., Luo, S., Geng, S., Jiao, W., & Liu, Y. (2018). Degradation and mineralization of aniline by O3/Fenton process enhanced using high-gravity technology. Chinese Journal of Chemical Engineering, 26, 1444-1450.
[28] Zeng, Z.-Q., Wang, J.-F., Li, Z.- H., Sun, B. C., Shao, L., Li, W.-J., Chen, J.- F., & Zou, H.- K. (2013). The Advanced Oxidation Process of Phenol Solution by O3/H2O2 in a Rotating Packed Bed. Ozone: science & engineering. 35(2), 101-108.
[29] Weizhou, J., Youzhi, L., Wenli, L., Jing, L., Fan, S., & Chaoran, W. (2013). Degradation of nitrobenzene-containing wastewater with O3 and H2O2 by high gravity technology. China Petroleum Processing & Petrochemical Technology, 15(1), 85-94.
[30] Chang, C.-C., Chiu, C. -Y., Chang, C. -Y., Chang, C. -F., Chen, Y. -H., Ji, D. -R., Tseng, J. -Y., & Yu., Y. -H. (2009). Pt-catalyzed ozonation of aqueous phenol solution using high-gravity rotating packed bed. Journal of Hazardous Materials, 168(2-3), 649-655.
[31] Chang, C.-C., Chiu, C. -Y., Chang, C. -Y., Chang, C. -F., Chen, Y. -H., Ji, D. -R., Yu, Y. -H., & Chiang, P. -C. (2009). Combined photolysis and catalytic ozonation of dimethyl phthalate in a high-gravity rotating packed bed. Journal of Hazardous Materials, 161(1), 287-293.
[32] Wu, Y., Chang, C. -C., Guan, C. -Y., Chang, C. -C., Li, J. -W., Chang, C. -Y., Yu, C. -P. (2019). Enhanced removal of ammonium from the aqueous solution using a high-gravity rotating packed bed loaded with clinoptilolite. Separation and Purification Technology, 221, 378-384.
[33] Yin, S., Chen, K., Srinivasakannan, C., Guo, S., Li, S., Peng, J., & Zhang., L. (2018). Enhancing recovery of ammonia from rare earth wastewater by air stripping combination of microwave heating and high gravity technology. Chemical Engineering Journal, 337, 515-521.
[34] Zeng, Z., Zou, H., Li, X., Sun, B., Chen, J., & Shao, L. (2012). Ozonation of Phenol with O3/Fe(II) in Acidic Environment in a Rotating Packed Bed. Industrial & Engineering Chemistry Research, 51(31), 10509-10516.
[35] Li, Z.-X., Liu, Y.-Z., Jiao, W.-Z., Wang, Q.-C., & Hou, X.-T. (2012). Experimental Study on Fenton Reagent Treating DNT Wastewater Intensified by Rotating Packed Bed. Initiators & Pyrotechnics, (1), 48-52.
[36] Wei, Q., Qiao, S., Sun, B., Zou, H., Chen, J., & Shao, L. (2015). Study on the treatment of simulated coking wastewater by O3 and O3/Fenton processes in a rotating packed bed. RSC advances, 5, 93386- 93393.
[37] Jiao, W., Qin, Y., Luo, S., He, Z., Feng, Z., & Liu, Y. (2017). Simultaneous formation of nanoscale zero-valent iron and degradation of nitrobenzene in wastewater in an impinging stream-rotating packed bed reactor. Chemical Engineering Journal, 321, 564-571.
[38] Li, W., Yan, J., Yan, Z., Song, Y., Jiao, W., Qi, G., Liu., Y. (2018). Adsorption of phenol by activated carbon in rotating packed bed: Experiment and modeling. Applied Thermal Engineering, 142, 760-766.
[39] Li, P., Wei, X., Shao, S., Gao, W., Jing, J., Jiao, W., & Liu., Y. (2020). Degradation of nitrobenzene in wastewater by O3/FeOOH in a rotating packed bed. Chemical Engineering and Processing - Process Intensification, 153, 107981.
[40] Qiao, J., Luo, S., Yang, P., Jiao, W., & Liu, Y. (2019). Degradation of Nitrobenzene-containing wastewater by ozone/persulfate oxidation process in a rotating packed bed. Journal of the Taiwan Institute of Chemical Engineers, 99, 1-8.
[41] Wang, L., Yun, J., Zhang, H., Si, J., Fang, X., & Shao, L. (2021). Degradation of Bisphenol A by ozonation in rotating packed bed: Effects of operational parameters and co-existing chemicals. Chemosphere, 274, 129769.
[42] Soares, O. S., Rodrigues, C. S., Madeira, L. M., & Pereira, M. F. R. (2019). Heterogeneous Fenton-like degradation of p-nitrophenol over Tailored Carbon-Based Materials. Catalysts, 9(3), 258.
[43] De Graaff, M., Bijmans, M. F., Abbas, B., Euverink, G.-J., Muyzer, G., & Janssen, A. J. (2011). Biological treatment of refinery spent caustics under halo-alkaline conditions. Bioresource Technology, 102(15), 7257-7264.
[44] Rodrigues, C. S. D., Borges, R. A. C., Lima, V. N., & Madeira, L. M. (2018). p-Nitrophenol degradation by Fenton's oxidation in a bubble column reactor. Journal of Environmental Management. 206, 774-785.
[45] Ince, N. H., & Tezcanli-Güyer, G. (2004). Impacts of pH and molecular structure on ultrasonic degradation of azo dyes. Ultrasonics, 42(1-9), 591-596.
[46] Tauber, A., Schuchmann, H.-P., & Von Sonntag, C. (2000). Sonolysis of aqueous 4-nitrophenol at low and high pH. Ultrasonics Sonochemistry, 7(1), 45-52.
[47] WeiZhou, J., YouZhi, L., Fan, S., WenLi, L., Jing, L., Chaoran, W. (2012). Degradation of Wastewater Containing Nitrobenzene by High Gravity-Ultrasonic/Ozonation/Electrolysis Technology. China Petroleum Processing and Petrochemical Technology, 14(3), 96-101.
[48] Jiao, W., Yu, L., Feng, Z., Guo, L., Wang, Y., & Liu, Y. (2016). Optimization of nitrobenzene wastewater treatment with O3/H2O2 in a rotating packed bed using response surface methodology. Desalination and Water Treatment, 57(42), 19996- 20004. | ||
|
آمار تعداد مشاهده مقاله: 679 تعداد دریافت فایل اصل مقاله: 624 |
||