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1

Xiang, Wen Jun. "The Research on the Current Situation and Advances of Petrochemical Wastewater Treatment." Advanced Materials Research 550-553 (July 2012): 2416–19. http://dx.doi.org/10.4028/www.scientific.net/amr.550-553.2416.

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At present, it is so prominent in the development of the petrochemical industry in China,and it is accompanied by petrochemical wastewater, which has become a big problem need to solve urgently.Because petrochemical wastewater mainly contains benzene-compound, organic matter, high salt wastewater and oil sewage, etc. They are very damaging and highly contaminated. The composition and properties of the petrochemical wastewater were introduced firstly, the current situation of petrochemical wastewater treatment at home and abroad were reviewed in the study. Especially the development of petroche
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2

Jahanshahi, Sasan, Leila Badiefar, Mahvash Khodabandeh, Mohammad Ali Heidarnia, and Bagher Yakhchali. "Bioremediation of a salty petrochemical wastewater containing bisphenol A by a novel indigenous Pseudomonas pseudoalcaligenes." RSC Advances 13, no. 1 (2023): 388–98. http://dx.doi.org/10.1039/d2ra06206b.

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The efficient biodegradation of bisphenol A (BPA) and phenol in salty petrochemical wastewater using a novel indigenous halotolerant, Pseudomonas sp. The bacterium has potential to be used for petrochemical and similar wastewaters treatment.
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3

FROLOV, A. E., and O. N. KOTKOVA. "EFFECT OF TREATMENT PLANTS ON ENVIRONMENTAL SAFETY." Urban construction and architecture 3, no. 4 (December 15, 2013): 68–74. http://dx.doi.org/10.17673/vestnik.2013.04.12.

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Water treatment and returning the treated water into the production is very important for refining and petrochemical industries. The technical condition of wastewater and water treatment with characteristic lesions of structural elements significantly affect the ecology of the environment and the plant area with flooding possible contamination of groundwater. These issues are discussed based on a survey of individual objects petrochemicals.
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4

XIE, B., S. LIANG, Y. TANG, W. MI, and Y. XU. "Petrochemical wastewater odor treatment by biofiltration." Bioresource Technology 100, no. 7 (April 2009): 2204–9. http://dx.doi.org/10.1016/j.biortech.2008.10.035.

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Lahiere, Richard J., and Kenneth P. Goodboy. "Ceramic membrane treatment of petrochemical wastewater." Environmental Progress 12, no. 2 (May 1993): 86–96. http://dx.doi.org/10.1002/ep.670120204.

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6

Gao, Ai Hua, Shui Jiao Yang, Shang Bin Hu, Xiao Qing He, and Zhi Guo Lu. "Discharge Plasma for the Treatment of Industrial Wastewater." Applied Mechanics and Materials 71-78 (July 2011): 3075–78. http://dx.doi.org/10.4028/www.scientific.net/amm.71-78.3075.

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The treatment of industrial wastewaters collected from petrochemical works, gypsum plant, and printing and dyeing mill, was investigated at atmospheric pressure in air discharge plasma. The degradation effects of organic contaminants in water were compared for the printing and dyeing wastewater under different discharging conditions and for the wastewater from the other two plants under the same discharging conditions. The influences of several factors on chemical oxygen demand (COD) remove rate were studied experimentally. The results showed that the treatment effects for the same industrial
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7

Goettems, Ellen M. P., Zeno Simon, Mario L. Baldasso, and Edson S. Ferreira. "SITEL: A Successful Petrochemical Wastewater Treatment System." Water Science and Technology 20, no. 10 (October 1, 1988): 141–62. http://dx.doi.org/10.2166/wst.1988.0133.

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SITEL, Integrated Wastewater Treatment System of South Petrochemical Complex, has been processing liquid wastes from this industrial area since November 1982. The Complex consists of an olefins plant and some second-generation plants that produce mainly thermoplastic resins. In this paper a comprehensive appraisal is presented of the operation of SITEL during the years 1985-1986. Data on the raw effluents produced by the individual contributors are presented, together with information on removal efficiencies of all parameters monitored throughout the different units and phases of treatment. A
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8

Abualhail. "Demonstration Case of Petrochemical Wastewater Treatment Plant." American Journal of Environmental Sciences 6, no. 3 (March 1, 2010): 295–98. http://dx.doi.org/10.3844/ajessp.2010.295.298.

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9

Cheng, Siyu, Xiaomeng Ran, Gengbo Ren, Zizhang Wei, Zhimin Wang, Tiantong Rao, Ruixuan Li, and Xiaodong Ma. "Comparison of Fenton and Ozone Oxidation for Pretreatment of Petrochemical Wastewater: COD Removal and Biodegradability Improvement Mechanism." Separations 9, no. 7 (July 18, 2022): 179. http://dx.doi.org/10.3390/separations9070179.

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Cost-effective pretreatment of highly concentrated and bio-refractory petrochemical wastewater to improve biodegradability is of significant importance, but remains challenging. This study compared the pretreatment of petrochemical wastewater by two commonly used chemical advanced oxidation technologies (Fenton and ozone oxidation), and the mechanisms of biodegradability improvement of pretreated wastewater were explored. The obtained results showed that in the Fenton oxidation system, the COD removal of petrochemical wastewater was 89.8%, BOD5 decreased from 303.66 mg/L to 155.49 mg/L, and BO
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10

An, Dingnian, Junzhen Zhang, and Yi Yuan. "Using bundle filters to process petrochemical secondary effluent for industrial reuse." Water Science and Technology 34, no. 10 (November 1, 1996): 127–31. http://dx.doi.org/10.2166/wst.1996.0248.

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The objective of this project is to study the advanced treatment technique for the secondary effluent from petrochemical wastewater treatment plants in order to meet requirements for the reuse of industrial wastewater. Based on the characteristics of the secondary effluent of petrochemical wastewater, a direct filtration process with highly effective filter is selected and designed. The test results indicate that the process can achieve good results in turbidity and COD removal. It can meet the need for the industrial reuse of the secondary effluent of petrochemical wastewater as the turbidity
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11

Okawa, Y., S. Shinozuka, R. Ota, and S. Matsui. "Experience of 16 Years' Operation and Maintenance of the Fukashiba Industrial Wastewater Treatment Plant of the Kashima Petrochemical Complex – I. Operation and Maintenance." Water Science and Technology 20, no. 10 (October 1, 1988): 193–200. http://dx.doi.org/10.2166/wst.1988.0137.

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The Kashima petrochemical complex and the Fukashiba industrial wastewater treatment plant are described. The complex consists of 19 core factories (petroleum, petrochemicals, and thermal power generation) and 39 other factories (including organic chemicals, foods, metals, machinery, etc.). The total amount of industrial wastewater produced is 59,800 m3/day. The treatment plant also accepts municipal wastewater from the surrounding area, totalling 1,100 m3/d. A system for charging for the industrial wastewater has been introduced. The water quality standards for the industrial wastewater discha
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12

Zaffaroni, C., G. Daigger, P. Nicol, and T. W. Lee. "Wastewater treatment challenges faced by the petrochemical and refinery industry, and opportunities for water reuse." Water Practice and Technology 11, no. 1 (March 1, 2016): 104–17. http://dx.doi.org/10.2166/wpt.2016.012.

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Industrial wastewater differs from municipal wastewater. The limits for treated effluent discharge and targets for re-use are typically the same, and derived from the best available technology for municipal wastewater treatment. The main treatment unitary processes are also the same; although proper adaptation to specific, different, industrial wastewater streams is needed. This paper provides some examples of the challenges presented by specific wastewater sources (high total dissolved solids, high temperature, spent caustic, etc.), lack of previous similar experience – e.g., using membrane b
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13

Juang, Lain-Chuen, Dyi-Hwa Tseng, and Shyh-Chaur Yang. "Treatment of petrochemical wastewater by UV/H2O2 photodecomposed system." Water Science and Technology 36, no. 12 (December 1, 1997): 357–65. http://dx.doi.org/10.2166/wst.1997.0465.

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The potential advantages of the UV/H2O2 process treating petrochemical wastewater as the tertiary treatment or the direct pre-treatment were demonstrated. While the high alkalinity of wastewater was not reduced, the UV/H2O2 process as the tertiary treatment could not obtain removal efficiency of wastewater. If the system pH adjusts to 3, this process will polish the effluent of the current biological process to meet the National Effluent Standards of 1998. The results of the direct pre-treatment with the UV/H2O2 process revealed that the recalcitrant compounds presented in raw wastewater would
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14

Ahmed, Mohd Elmuntasir, Andrzej Mydlarczyk, and Adel Al-Haddad. "EFFICIENCY LIMITING FACTORS OF PETROCHEMICAL WASTEWATER TREATMENT USING HYBRID BIOLOGICAL REACTOR." Journal of Environmental Engineering and Landscape Management 30, no. 3 (October 7, 2022): 380–92. http://dx.doi.org/10.3846/jeelm.2022.17633.

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The wastewater characteristics and some operational control parameters limit the efficiency of attached growth processes for petrochemical wastewater treatment. This study aims to determine the efficiency of a hybrid biological reactor treating actual petrochemical wastewater and to identify the efficiency determining factors. An up-flow biological reactor filled with bio-career was operated at two flow rates, two dissolved oxygen (DO) levels, and under anaerobic conditions. Due to the varying characteristics of actual petrochemical wastewater, efficiency limitations were manifested in many wa
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15

Lakatos, Gyula, Magdolna K. Kiss, Marianna Kiss, and Péter Juhász. "Application of constructed wetlands for wastewater treatment in Hungary." Water Science and Technology 35, no. 5 (March 1, 1997): 331–36. http://dx.doi.org/10.2166/wst.1997.0230.

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This paper presents a brief survey of the Hungarian constructed wetland types that have been established for wastewater treatment in the last thirty years, and gives an analysis of the design and performance of those reed ponds that have been constructed for the polishing of petrochemical wastewaters. Natural treatment processes are in great demand because they are protective of the environment and have low operation costs and satisfactory purification efficiency. Three major types of treatment wetlands are utilized in Hungary: free water surface system, subsurface flow system, and artificial
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16

Ariff, Idzham Fauzi Mohd, and Mardhiyah Bakir. "Dynamic Simulation of Petrochemical Wastewater Treatment Using Wastewater Plant Simulation Software." MATEC Web of Conferences 203 (2018): 03005. http://dx.doi.org/10.1051/matecconf/201820303005.

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A dynamic simulation model was developed, calibrated and validated for a petrochemical plant in Terengganu, Malaysia. Calibration and validation of the model was conducted based on plant monitoring data spanning 3 years resulting in a model accuracy (RMSD) for effluent chemical oxygen demand (COD), ammoniacal nitrogen (NH3-N) and total suspended solids (TSS) of ±11.7 mg/L, ±0.52 mg/L and ± 3.27 mg/L respectively. The simulation model has since been used for troubleshooting during plant upsets, planning of plant turnarounds and developing upgrade options. A case study is presented where the sim
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17

Koshak, Natal′ia, Sergei Novikov, and Ol′ga Ruchkinova. "Improvement scheme of wastewater treatment of petrochemical production." PNRPU Construction and Architecture Bulletin 7, no. 4 (2016): 51–63. http://dx.doi.org/10.15593/2224-9826/2016.4.05.

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18

Jafarzadeh, M. T., N. Mehrdadi, A. A. Azimi, and S. J. Hashemian. "Petrochemical Wastewater Treatment Using an Anaerobic Hybrid Reactor." Pakistan Journal of Biological Sciences 9, no. 6 (March 1, 2006): 1037–42. http://dx.doi.org/10.3923/pjbs.2006.1037.1042.

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19

Kubsad, V., S. K. Gupta, and S. Chaudhari. "Treatment of Petrochemical Wastewater by Rotating Biological Contactor." Environmental Technology 26, no. 12 (December 2005): 1317–26. http://dx.doi.org/10.1080/09593332608618614.

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20

He, Qianfeng, Shihui Si, Leshan Song, Haiyan Yan, Yongge Yao, Di Zhao, and Qunhuan Cai. "Refractory petrochemical wastewater treatment by K2S2O8 assisted photocatalysis." Saudi Journal of Biological Sciences 26, no. 4 (May 2019): 849–53. http://dx.doi.org/10.1016/j.sjbs.2017.07.009.

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21

Santos, Paula G., Cíntia M. Scherer, Adriano G. Fisch, and Marco Antônio S. Rodrigues. "Petrochemical wastewater treatment: Water recovery using membrane distillation." Journal of Cleaner Production 267 (September 2020): 121985. http://dx.doi.org/10.1016/j.jclepro.2020.121985.

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22

Ochiai, E., T. Igarashi, S. Itou, H. Seya, and S. Matsui. "Operation and management of the Fukashiba treatment plant." Water Science and Technology 53, no. 11 (May 1, 2006): 179–87. http://dx.doi.org/10.2166/wst.2006.351.

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Since the opening of the Fukashiba Treatment Plant in 1970, the number of industries and the amount of wastewater requiring treatment in the service area have been steadily increasing. In response to the recent economic downturn in Japan, these rates of increase have slowed, but are not decreasing. The pollution load in the wastewater from these industries has decreased and is now stable. Unlike the case of ordinary domestic sewage, the effects of the various types of substances contained in wastewaters delivered from the petrochemical complex to the treatment plant, for example, corrosion, ar
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23

Trojanowicz, Karol, and Wlodzimierz Wojcik. "Carbonaceous materials in petrochemical wastewater before and after treatment in an aerated submerged fixed-bed biofilm reactor." Chemical and Process Engineering 37, no. 3 (September 1, 2016): 373–82. http://dx.doi.org/10.1515/cpe-2016-0030.

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Abstract Results of the studies for determining fractions of organic contaminants in a pretreated petrochemical wastewater flowing into a pilot Aerated Submerged Fixed-Bed Biofilm Reactor (ASFBBR) are presented and discussed. The method of chemical oxygen demand (COD) fractionation consisted of physical tests and biological assays. It was found that the main part of the total COD in the petrochemical, pretreated wastewater was soluble organic substance with average value of 57.6%. The fractions of particulate and colloidal organic matter were found to be 31.8% and 10.6%, respectively. About 40
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24

Buić, Zdenko, and Bruno Zelić. "Application of Clay for Petrochemical Wastewater Pretreatment." Water Quality Research Journal 44, no. 4 (November 1, 2009): 399–406. http://dx.doi.org/10.2166/wqrj.2009.040.

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Abstract Petrochemical industry wastewater is contaminated with nitrogen and phosphorous compounds, mainly ammonium and ammonium nitrogen, and therefore needs treatment before it is released in the watercourse. Usually, petrochemical wastewater treatment is carried out following the ion exchange principle. One of the possibilities of petrochemical wastewater pretreatment is using bentonite clays. Bentonite decreases the concentration of ions in the incoming wastewater and, as a consequence, the ion exchanger placed subsequently works more efficiently. The experiment was carried out with alkali
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25

Wang, Song, Genwang Zhu, Zhongchen Yu, Chenxi Li, Dan Wang, and Xiaoling Cao. "Mineralization of petrochemical wastewater after biological treatment by ozonation catalyzed with divalent iron tartaric acid chelate." Water Science and Technology 81, no. 10 (May 15, 2020): 2211–20. http://dx.doi.org/10.2166/wst.2020.287.

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Abstract The petrochemical wastewater includes many toxic organic compounds, which are refractory substances. It is difficult for the wastewater to meet discharge standards after biological treatment, therefore, the further effective treatment of post-biochemical petrochemical wastewater has become an urgent problem to be solved. This study used iron tartaric acid chelate (ITC) catalytic ozonation to treat the petrochemical wastewater. Various key factors were investigated, such as hydraulic retention time (HRT), catalyst dosage, ozone concentration, initial pH values and oxidation efficiency.
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26

Venzke, Carla Denize, Marco Antônio Siqueira Rodrigues, Alexandre Giacobbo, Luciana Ely Bacher, Iona Souza Lemmertz, Cheila Viegas, Júlia Striving, and Shaiane Pozzebon. "Application of reverse osmosis to petrochemical industry wastewater treatment aimed at water reuse." Management of Environmental Quality: An International Journal 28, no. 1 (January 9, 2017): 70–77. http://dx.doi.org/10.1108/meq-07-2015-0149.

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Purpose The purpose of this paper is to apply reverse osmosis (RO) to the treatment of industrial wastewater from a large petrochemical complex in Southern Brazil, in order to verify the conditions of liquid effluent reuse and improve them, especially to reduce the consumption of natural water by some production structures such as boilers and cooling towers. Design/methodology/approach The petrochemical wastewater was submitted to pretreatment using a sand filter and activated carbon filters. Tests were conducted using RO equipment with a production capacity of 0.25 m3h−1 composed of a spiral
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27

Rebhun, Menahem, and Noah Galil. "Technological Strategies for Protecting and Improving the Biological Treatment of Wastewater from a Petrochemical Complex." Water Science and Technology 29, no. 9 (May 1, 1994): 133–41. http://dx.doi.org/10.2166/wst.1994.0461.

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The wastewater from a petrochemical complex is characterized by a diversity of pollutants including hydrocarbons, in free and emulsified form, phenols including cresols and xylenols, mercaptans, sulfides, ammonia and cyanides. The wastewater treatment of the reported petrochemical complex is based on a multiple stage treatment approach, consisting of physico - chemical, and biological processes. The biological treatment process could be efficiently protected by preliminary wastewater flow regulation, controlling hydraulic and pollutants loads. Additional protection and improvement of the biolo
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28

Wang, Xi, and Hua Zhao. "Isolation and Characterization of a Bacillus flexus Strain Used in Alkaline Wastewater Treatment." Advanced Materials Research 750-752 (August 2013): 1381–84. http://dx.doi.org/10.4028/www.scientific.net/amr.750-752.1381.

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Biological treatment is one of the considerable choices for removing of organic pollutants present in petrochemical wastewaters. In this study, BS5, the isolate with the highest COD removal rate, was identified asBacillus flexus, based on 16S rDNA sequences. Subsequently, the optimized COD removal conditions of BS5 were investigated. It was indicated that the optimal conditions were 35°C, pH 7.5. Under such circumstance, the removal rate of COD can reach 81.04%. The isolation ofBacillus flexusstrain BS5 provided an alternative for the bioremediation of alkaline wastewater. Lastly, the study sh
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29

Guarino, C. F., B. P. Da-Rin, A. Gazen, and E. P. Goettems. "Activated Carbon as an Advanced Treatment for Petrochemical Wastewaters." Water Science and Technology 20, no. 10 (October 1, 1988): 115–30. http://dx.doi.org/10.2166/wst.1988.0131.

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This paper presents the results of a study conducted with the purpose of establishing the feasibility of using activated carbon as an advanced treatment process for petrochemical wastewaters. Two pilot plants using Powdered Activated Carbon (PAC) and Granular Activated Carbon (GAC), respectively, were operated for a period of 15 weeks, fed with the effluent of a petrochemical wastewater treatment plant. The study was made using all available Brazilian carbons at the time. Isotherm tests and other carbon properties were used to select the carbons for GAC and PAC plants. The two pilot plants wer
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30

Hirose, K., T. Igarashi, E. Ochiai, H. Seya, and S. Matsui. "Improvement of wastewater treatment performance of the Fukashiba treatment plant." Water Science and Technology 53, no. 11 (May 1, 2006): 127–33. http://dx.doi.org/10.2166/wst.2006.345.

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The Fukashiba Treatment Plant Kashima Rinkai Specified Sewage Works has received wastewater from the petrochemical complex (90%) and public sewage of Kamisu and Hasaki town (10%). For this reason, the plant is facing many difficulties in producing good quality effluent. In order to solve these difficulties, we are reviewing the treatment performance and making efforts for its improvement with nitrification inhibition, control of bio-persistent substances and the PRTR approach.
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Kleerebezem, Robbert, Joost Mortier, Look W. Hulshoff Pol, and Gatze Lettinga. "Anaerobic pre-treatment of petrochemical effluents: terephthalic acid wastewater." Water Science and Technology 36, no. 2-3 (July 1, 1997): 237–48. http://dx.doi.org/10.2166/wst.1997.0528.

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During petrochemical production of purified terephthalic acid (PTA, 1,4-benzene dicarboxylic acid), a large quantity of concentrated effluent is produced. Main polluting compounds in this wastewater are terephthalic acid, acetic acid and benzoic acid in decreasing order of concentration. Acetic acid and benzoic acid are known to be rapidly degraded in high rate anaerobic treatment systems, such as Upflow Anaerobic Sludge Bed (UASB) reactors. Concerning the kinetics of anaerobic mineralization of terephthalic acid, however, no information is available in literuature. Therefore our work focused
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Hu, Hua‐Long, Fa‐Sheng Li, and Qiao‐Li Liu. "Preparation of adsorbent material from petrochemical wastewater treatment sludge." Toxicological & Environmental Chemistry 70, no. 1-2 (May 1999): 9–14. http://dx.doi.org/10.1080/02772249909358735.

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Sadeghi, Fatemeh, Mohammad Reza Mehrnia, Ramin Nabizadeh, Mohammad Bagher Bahadori, and Mohammad Hossein Sarrafzadeh. "MBR technology: A practical approach for petrochemical wastewater treatment." Petroleum Science and Technology 35, no. 3 (February 2017): 222–28. http://dx.doi.org/10.1080/10916466.2011.572108.

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Ting, Wang-Ping, Yao-Hui Huang, and Ming-Chun Lu. "Catalytic treatment of petrochemical wastewater by electroassisted Fenton technologies." Reaction Kinetics and Catalysis Letters 92, no. 1 (September 21, 2007): 41–48. http://dx.doi.org/10.1007/s11144-007-5043-2.

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Hsu, E. H. "Treatment of a petrochemical wastewater in sequencing batch reactors." Environmental Progress 5, no. 2 (May 1986): 71–81. http://dx.doi.org/10.1002/ep.670050206.

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Alkenova, Gauhar T., Tatyana V. Kovrigina, Tulegen K. Chalov, and Edil E. Ergozhin. "Electro and Baromembrane Methods of Petrochemical Enterprises' Wastewater Treatment." Remediation Journal 25, no. 4 (September 2015): 111–26. http://dx.doi.org/10.1002/rem.21444.

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Matsui, S., Y. Okawa, and R. Ota. "Experience of 16 Years' Operation and Maintenance of the Fukashiba Industrial Wastewater Treatment Plant of the Kashima Petrochemical Complex – II. Biodegradability of 37 Organic Substances and 28 Process Wastewaters." Water Science and Technology 20, no. 10 (October 1, 1988): 201–10. http://dx.doi.org/10.2166/wst.1988.0138.

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Twenty-eight process wastewaters and thirty-seven organic substances identified in the wastewater of the Kashima petrochemical complex were subjected to biodegradability tests. The tests consisted of the activated sludge degradability method and a supplementary test using the respiration meter method. Both tests utilized the activated sludge of the Fukashiba industrial wastewater treatment plant, which was acclimatized to the wastewater and organic substances. The 28 process wastewaters were classified into biodegradable, less biodegradable, and non-biodegradable according to the percentage TO
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Ahmed, Mohd Elmuntasir, Adel Al-Haddad, and Suad Al-Dufaileej. "Characterization and Profiling of Industrial Wastewater Toxicity in Kuwait." International Journal of Environmental Science and Development 13, no. 2 (2022): 35–41. http://dx.doi.org/10.18178/ijesd.2022.13.2.1369.

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Toxicity reduction is a main criterion in prioritizing industrial wastewater treatment objectives. This paper utilized a comprehensive survey of 41 industrial facilities to characterize their wastewater quality parameters and to assess their wastewater toxicity. The 41 factories were grouped under eleven industrial categories. Microtox relative toxicity test results indicated that industrial wastewater in Kuwait are mostly very toxic to toxic with the exception of farms wastewater which was found to be slightly toxic. The highest ranking toxic wastewaters where found to be metal forming, print
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Zhao, Li-jun, Fang Ma, Jing-bo Guo, and Qing-liang Zhao. "Petrochemical wastewater treatment with a pilot-scale bioaugmented biological treatment system." Journal of Zhejiang University-SCIENCE A 8, no. 11 (October 2007): 1831–38. http://dx.doi.org/10.1631/jzus.2007.a1831.

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40

El Khorassani, H., P. Trebuchon, H. Bitar, and O. Thomas. "Minimisation strategy of petrochemical wastewater organic load." Water Science and Technology 42, no. 5-6 (September 1, 2000): 15–22. http://dx.doi.org/10.2166/wst.2000.0489.

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Industrial wastewater management is nowadays a reality in most industries and particularly in petrochemical ones. As a consequence, some treatment plants appear to be over designed because of waste minimization. Actually supplementary organic loads coming from incidents or external effluents have to be treated. As classical parameters or compound analyses are not well adapted, a new methodology based on the use of UV spectrophotometry is proposed. Starting from several samplesof wastewater in different points of sewage network, a procedure, called UVDIAG is used for the exploitation of the cor
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Parker, W., and G. J. Farquhar. "Treatment of a Petrochemical Wastewater in an Anaerobic Packed Bed Reactor." Water Quality Research Journal 24, no. 2 (May 1, 1989): 195–206. http://dx.doi.org/10.2166/wqrj.1989.011.

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Abstract Wastewater from a used oil rerefinery was tested in laboratory scale anaerobic packed bed reactors for TOC removal, gas production and control of volatile organic emissions. The raw wastewater had a TOC ranging from 3,250 to 5,800 mg/L of which 40 to 45% consisted of total phenolics, acetone, methanol, ethanol and volatile fatty acids. The remaining TOC was not analyzed but was expected to contain potentially harmful constituents. Treatment of the undiluted wastewater achieved acidogenisis but methane production appeared to have been inhibited. A 1:2 dilution of the wastewater produce
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42

Castillo, L., H. El Khorassani, P. Trebuchon, and O. Thomas. "UV treatability test for chemical and petrochemical wastewater." Water Science and Technology 39, no. 10-11 (May 1, 1999): 17–23. http://dx.doi.org/10.2166/wst.1999.0625.

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There is a tendency to design biological units for chemical or petrochemical wastewater treatment. Some of these treatment plants are even sometimes used for the degradation of any external industrial sewage transported for the purpose. In this case, the decision to accept or refuse the waste must be rapid and sure. The aim of this paper is to propose a new treatability test based on a direct far UV photooxidation of the sample, coupled with a UV spectrophotometric survey of the waste quality. The test has been applied on different samples from chemical and petrochemical industries and the res
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43

Eckenfelder, W. Wesley, and A. J. Englande. "Chemical/petrochemical wastewater management—past, present and future." Water Science and Technology 34, no. 10 (November 1, 1996): 1–7. http://dx.doi.org/10.2166/wst.1996.0232.

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This paper summarizes and evaluates past, current and expected actions concerning waste management in the chemical and petrochemical industries. Industrial waste management has evolved from an “end of pipe” treatment mentality to holistic environmental waste management with source reductions as the preferred option. In most cases significant costs savings have resulted and environmental and public health impacts minimized. This current thrust has resulted from recent regulatory actions. Future trends will require management changes. To be effective, the management approach selected must addres
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44

Siddique, M. N. I., B. K. Zaied, S. Krishnan, and M. F. Ahmad. "Improving Methane Generation by Co-Digestion of Sewage Sludge and Petrochemical Wastewater: Influence of Heat and Alkali Pretreatment." Asian Journal of Chemistry 31, no. 10 (August 30, 2019): 2403–9. http://dx.doi.org/10.14233/ajchem.2019.22195.

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With the target of amplifying methane generation from sewage sludge (SS), co-digestion with petrochemical wastewater (PWW) was examined. In addition, the use of both 165 °C heat treatment and alkali pretreatment to mixed SS/PWW wastewater was assessed. Batch tests demonstrated that refractory materials were generated from pretreatment for petrochemical wastewater at the 165 °C heat and alkali pretreatments at the 75 or 115 °C and with pH value of 8, 9 or 10 producing enhanced preliminary methane generation percentage and a little effect for generation capacity of methane of the miscellaneous w
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Zilberman, M. B., E. A. Pichugin, E. V. Zyryanova, and A. S. Solovyeva. "Evaluation of the Effect of Changing the Composition of Wastewater on Biological Treatment when Adding a Mixture of Sulfide Alkali for the Treatment of Petrochemical Wastewater." Ecology and Industry of Russia 26, no. 11 (November 2, 2022): 34–37. http://dx.doi.org/10.18412/1816-0395-2022-11-34-37.

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The influence of a pilot assessment based on the results of a change in the composition of wastewater on the quality of biological wastewater treatment when a sulfide alkali mixture is added to the feedstream of petrochemical enterprises is presented. It was found that the results of wastewater treatment at biological treatment plants are not affected by phenols in sulfide alkali wastewater. It was confirmed that activated sludge retains the ability to extract organic compounds without reference to the proportion of sulfide alkali effluents in the treated water.
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46

Trojanowicz, Karol, and Włodzimierz Wójcik. "Calibration and verification of models of organic carbon removal kinetics in Aerated Submerged Fixed-Bed Biofilm Reactors (ASFBBR): a case study of wastewater from an oil-refinery." Water Science and Technology 63, no. 10 (May 1, 2011): 2446–56. http://dx.doi.org/10.2166/wst.2011.216.

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The article presents a case-study on the calibration and verification of mathematical models of organic carbon removal kinetics in biofilm. The chosen Harremöes and Wanner & Reichert models were calibrated with a set of model parameters obtained both during dedicated studies conducted at pilot- and lab-scales for petrochemical wastewater conditions and from the literature. Next, the models were successfully verified through studies carried out utilizing a pilot ASFBBR type bioreactor installed in an oil-refinery wastewater treatment plant. During verification the pilot biofilm reactor work
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47

Li, Hao, Xinmou Kuang, Congping Qiu, Xiaolan Shen, Botao Zhang, and Hua Li. "Advanced electrochemical treatment of real biotreated petrochemical wastewater by boron doped diamond anode: performance, kinetics, and degradation mechanism." Water Science and Technology 82, no. 4 (August 13, 2020): 773–86. http://dx.doi.org/10.2166/wst.2020.387.

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Abstract Petrochemical wastewater is difficult to process because of various types of pollutants with high toxicity. With the improvement in the national discharge standard, traditional biochemical treatment methods may not meet the standards and further advanced treatment techniques would be required. In this study, electrochemical oxidation with boron doped diamond (BDD) anode as post-treatment was carried out for the treatment of real biotreated petrochemical wastewater. The effects of current density, pH value, agitation rate, and anode materials on chemical oxygen demand (COD) removal and
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Duguet, J. P., B. Dussert, J. Mallevialle, and F. Fiessinger. "Polymerization Effects of Ozone: Applications to the Removal of Phenolic Compounds from Industrial Wastewaters." Water Science and Technology 19, no. 5-6 (May 1, 1987): 919–30. http://dx.doi.org/10.2166/wst.1987.0270.

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Degradation of phenols by ozone has been extensively studied but the oxidative coupling pathway of ozone resulting in a phenol polymerization has not been largely investigated. Application of low ozone dose in solutions of 2.4 dichlorophenol and salicylic acid is characterized by the formation of high molecular compounds which are partially insoluble. Numerous polymers have been identified by gas chromatography coupled with mass spectrometry. Application of the polymerization effect of ozone to petrochemical and coking wastewaters containing phenols give similar results. In each case, phenolic
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Echegaray, D. F., and R. F. Olivieri. "Biologically Resistant Contaminants, Primary Treatment with Ozone." Water Science and Technology 29, no. 8 (April 1, 1994): 257–61. http://dx.doi.org/10.2166/wst.1994.0420.

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Organic effluent oxidation tests were conducted in petrochemical companies, in the Camaçari Petrochemical Complex, to reduce treatment costs and improve the primary treatment efficiency in each industrial process. Ozone achieved 99.96 percent benzene reduction and 100 percent ethyl benzene and toluene reduction. Process efficiency is strongly dependent on the wastewater chemical composition and concentration. For this reason it is necessary to run pilot plant trials for each specific case. Ozone was obtained feeding commercial oxygen through a corona discharge generator and dissolved in the ef
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Ahmed, Mohd Elmuntasir, Abdallah Abusam, and Andrzej Mydlarczyk. "Kinetic Modeling of GAC - IFAS Chemostat for Petrochemical Wastewater Treatment." Journal of Water Resource and Hydraulic Engineering 6, no. 2 (June 30, 2017): 27–33. http://dx.doi.org/10.5963/jwrhe0602002.

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