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Engineering >> 2018, Volume 4, Issue 3 doi: 10.1016/j.eng.2018.05.014

Separation-and-Recovery Technology for Organic Waste Liquid with a High Concentration of Inorganic Particles

a National Engineering Laboratory for Industrial Wastewater Treatment, East China University of Science and Technology, Shanghai 200237, China
b Sinopec Luoyang Petrochemical Engineering Corporation, Luoyang 471003, China
c Sinopec Jinling Petrochemical Corporation, Nanjing 210033, China
d Sinopec Dalian (Fushun) Research Institute of Petroleum and Petrochemicals, Fushun 113001, China
e Sinopec Zhenhai Refining and Chemical Company, Ningbo 315207, China

Received: 2017-12-12 Revised: 2018-03-02 Accepted: 2018-05-15 Available online: 2018-05-19

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Abstract

The environmentally friendly and resourceful utilization of organic waste liquid is one of the frontiers of environmental engineering. With the increasing demand for chemicals, the problem of organic waste liquid with a high concentration of inorganic pollutants in the processing of petroleum, coal, and natural gas is becoming more serious. In this study, the high-speed self-rotation and flipping of particles in a threedimensional cyclonic turbulent field was examined using a synchronous high-speed camera technique; the self-rotation speed was found to reach 2000–6000 rad·s−1. Based on these findings, a cyclonic gasstripping method for the removal of organic matter from the pores of particles was invented. A technological process was developed to recover organic matter from waste liquid by cyclonic gas stripping and classifying inorganic particles by means of airflow acceleration classification. A demonstration device was built in Sinopec’s first ebullated-bed hydro-treatment unit for residual oil. Compared with the T-STAR fixed-bed gas-stripping technology designed in the United States, the maximum liquid-removal efficiency of the catalyst particles in this new process is 44.9% greater at the same temperature, and the time required to realize 95% liquid-removal efficiency is decreased from 1956.5 to 8.4 s. In addition, we achieved the classification and reuse of the catalyst particles contained in waste liquid according to their activity. A proposal to use this new technology was put forward regarding the control of organic waste liquid and the classification recovery of inorganic particles in an ebullated-bed hydro-treatment process for residual oil with a processing capacity of 2 × 106 t·a−1. It is estimated that the use of this new technology will lead to the recovery of 3100 ta−1 of diesel fuel and 647 t·a−1 of high-activity catalyst; in addition, it will reduce the consumption of fresh catalyst by 518 t·a−1. The direct economic benefits of this process will be as high as 37.28 million CNY per year.

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References

[ 1 ] Hu G, Li J, Zeng G. Recent development in the treatment of oily sludge from petroleum industry: a review. J Hazard Mater 2013;261(13):470–90. link1

[ 2 ] Xu N, Wang W, Han P, Lu X. Effects of ultrasound on oily sludge deoiling. J Hazard Mater 2009;171(1–3):914–7. link1

[ 3 ] Mrayyan B, Battikhi MN. Biodegradation of total organic carbons (TOC) in Jordanian petroleum sludge. J Hazard Mater 2005;120(1–3):127–34. link1

[ 4 ] Schwab AP, Su J, Wetzel S, Pekarek S, Banks MK. Extraction of petroleum hydrocarbons from soil by mechanical shaking. Environ Sci Technol 1999;33 (11):1940–5. link1

[ 5 ] Armor JN. A history of industrial catalysis. Catal Today 2011;163(1):3–9. link1

[ 6 ] Silvy RP. Future trends in the refining catalyst market. Appl Catal A Gen 2004;261(2):247–52. link1

[ 7 ] Furimsky E. Spent refinery catalysts: environment, safety and utilization. Catal Today 1996;30(4):223–86. link1

[ 8 ] Weber S, Leuschner P, Kämpfer P, Dott W, Hollender J. Degradation of estradiol and ethinyl estradiol by activated sludge and by a defined mixed culture. Appl Microbiol Biotechnol 2005;67(1):106–12. link1

[ 9 ] Liu Y, Wang HL, Xu YX, Fang YY, Chen XR. Sludge disintegration using a hydrocyclone to improve biological nutrient removal and reduce excess sludge. Separ Purif Tech 2017;177:192–9. link1

[10] Yang Q, Li ZM, Lv WJ, Wang HL. On the laboratory and field studies of removing fine particles suspended in wastewater using mini-hydrocyclone. Separ Purif Tech 2013;110(23):93–100. link1

[11] Zhao K, Bai J, Zeng Q, Zhang Y, Li J, Li L, et al. Efficient wastewater treatment and simultaneously electricity production using a photocatalytic fuel cell based on the radical chain reactions initiated by dual photoelectrodes. J Hazard Mater 2017;337:47–54. link1

[12] Neyestani M, Dickenson E, McLain J, Robleto E, Rock C, Gerrity D. Impacts of solids retention time on trace organic compound attenuation and bacterial resistance to trimethoprim and sulfamethoxazole. Chemosphere 2017;182:149–58. link1

[13] Li JP, Yang XJ, Ma L, Yang Q, Zhang YH, Bai ZS, et al. The enhancement on the waste management of spent hydrotreating catalysts for residue oil by a hydrothermal-hydrocyclone process. Catal Today 2016;271(4):163–71. link1

[14] Xue Y, Zhang Y, Zhang Y, Zheng S, Zhang Y, Jin W. Electrochemical detoxification and recovery of spent SCR catalyst by in-situ generated reactive oxygen species in alkaline media. Chem Eng J 2017;325:544–53. link1

[15] Toulhoat H, Szymanski R, Plumail JC. Interrelations between initial pore structure, morphology and distribution of accumulated deposits, and lifetimes of hydrodemetallisation catalysts. Catal Today 1990;7(4):531–68. link1

[16] Rana MS, Sámano V, Ancheyta J, Diaz JAI. A review of recent advances on process technologies for upgrading of heavy oils and residua. Fuel 2007;86 (9):1216–31. link1

[17] Menoufy MF, Ahmed HS. Treatment and reuse of spent hydrotreating catalyst. Energ Source Part A 2008;30(13):1213–22. link1

[18] Merino J, Bucalá V. Effect of temperature on the release of hexadecane from soil by thermal treatment. J Hazard Mater 2007;143(1–2):455–61. link1

[19] Ayen RJ, Swanstrom CP. Low temperature thermal treatment for petroleum refinery waste sludges. Environ Prog Sustain 1992;11(2):127–33. link1

[20] Al-Salem SM, Antelava A, Constantinou A, Manos G, Dutta A. A review on thermal and catalytic pyrolysis of plastic solid waste (PSW). J Environ Manage 2017;197:177–98. link1

[21] Singh R, Gbordzoe E. Modeling FCC spent catalyst regeneration with computational fluid dynamics. Powder Technol 2017;316:560–8. link1

[22] Leyva C, Ancheyta J, Mariey L, Travert L, Maugé F. Characterization study of NiMo/SiO2-Al2O3 spent hydroprocessing catalysts for heavy oils. Catal Today 2014;220–222(5):89–96. link1

[23] Rana MS, Ancheyta J, Sahoo SK, Rayo P. Carbon and metal deposition during the hydroprocessing of Maya crude oil. Catal Today 2014;220–222(4):97–105. link1

[24] Angeles MJ, Leyva C, Ancheyta J, Ramírez S. A review of experimental procedures for heavy oil hydrocracking with dispersed catalyst. Catal Today 2014;220–222(9):274–94. link1

[25] Jackson CR, Stessel RI, Peirce JJ. Passive pulsing air-classifier theory. J Environ Eng 1988;114(1):106–9. link1

[26] Everett J, Peirce JJ. Effect of feed rate and classifier height on air classification. J Environ Eng 1990;116(4):735–45. link1

[27] Duan C, Li H, He J, Zhao Y, Dong L, Lv K, et al. Experimental and numerical simulation of spent catalyst separation in an active pulsing air classifier. Sep Sci Technol 2015;50(5):633–45. link1

[28] Huang Y, Li JP, Zhang YH, Wang HL. High-speed particle self-rotation for coating oil removal by hydrocyclone. Separ Purif Tech 2017;177:263–71. link1

[29] Huang Y, Wang HL, Chen YQ, Zhang YH, Yang Q, Bai ZS, et al. Liquid-liquid extraction intensification by micro-droplet rotation in a hydrocyclone. Sci Rep 2017;7(1):2678. link1

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