Photocatalytic membrane reactor based on Mexican Natural Zeolite: RB5 dye removal by photo-Fenton process

被引:16
作者
Domenzain-Gonzalez, Jose [1 ]
Castro-Arellano, Jose J. [1 ]
Galicia-Luna, Luis A. [1 ]
Rodriguez-Cruz, Martin [2 ]
Hernandez-Lopez, Roberto T. [2 ]
Lartundo-Rojas, Luis [3 ]
机构
[1] Inst Politecn Nacl, Lab Termodinam, SEPI ESIQIE, UPALM, Edif Z,Secc 6,1ER Piso, Cd Mexico 07738, Mexico
[2] Univ Autonoma Metropolitana, Dept Mat, Cd Mexico 02200, Mexico
[3] Inst Politecn Nacl, Ctr Nanociencias & Micro & Nanotecnol, UPALM, Cd Mexico 07738, Mexico
来源
JOURNAL OF ENVIRONMENTAL CHEMICAL ENGINEERING | 2021年 / 9卷 / 04期
关键词
Mexican natural zeolite (MNZ); Extrusion; Photocatalytic membrane reactor (PCMR); Reactive Black5 (RB5); Photo-Fenton; AZO DYES; IRON; DEGRADATION; CATALYSTS; XPS; ADSORPTION; SPECTRA; OXIDES; WATER; TIO2;
D O I
10.1016/j.jece.2021.105281
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
A Mexican natural zeolite (MNZ) of heulandite type was used to develop mesoporous cylindrical membranes based on the extrusion method, the mineral was previously mixed with additives to form a paste with 67.8% of solids. The membranes were calcined at 550 degrees C, the extruded parts suffered erosion upon water contact at lower calcination temperatures, while the structural properties such as surface area, pore volume and hardness were decreasing at higher temperatures. The MNZ had oxidation states Fe2+ and Fe3+ from the Fe3O4, and the bandgap was 2.42 eV. This cylindrical membrane was arranged as a photocatalytic membrane reactor (PCMR) to evaluate the RB5-dye removal by the Photo-Fenton process using a 2.2 W lamp as radiation source. The Fe effect in the solution and the permeation flow was analyzed at pH = 3, [H2O2] = 3 g/L, [RB5](0) = 100 mg/L, lambda(max) = 405 nm (3.06 eV). The highest RB5-dye discoloration (D-30% = 92.3) in the retained was obtained using Fe in solution and a permeation flow which did not show color signals from the reaction beginning (D-t% = 100). A pseudo-first order (n = 1) kinetics was assumed with an apparent kinetic constant of 0.0904 min(-1) at the best reaction conditions. Finally, a total organic carbon removal TOC90% = 60.0 and TOC180% = 66.7 in the retentate flow was attained as well as TOC180% = 89.5 in the permeated flow.
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页数:14
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