Equipment Design of the Ship Sewage Treatment

2011 ◽  
Vol 201-203 ◽  
pp. 1486-1491
Author(s):  
Xian Chao Zhang ◽  
Jian Ping Xu
Keyword(s):  
Escherichia Coli ◽  
Membrane Bioreactor ◽  
Simulation Experiment ◽  
Removal Rate ◽  
Sewage Treatment ◽  
Control Technique ◽  
Treatment Technique ◽  
Biological Method ◽  
Emission Standards ◽  
Cod Removal Rate

A set of equipments for ship sewage treatment, which has been designed according to the characteristics of ship sewage with the advanced sewage treatment technique and the modern automatic control technique, makes ship sewage treatment miniaturized and automatized. The device takes biological method, + MBR Membrane Bioreactor, as the main treatment technique. After the reliability of the technique was justified through the simulation experiment, the mechanical structure of the equipment, including the detailed dimensions and relevant accessories, was designed according to the number of people. Besides, through PLC programmable controller the automatic operation and the automatic alarm have been achieved. As the result of the sewage treatment testing of the prototype, COD removal rate was above 92% , BOD5 removal rate above 98%, SS removal rate above 97%, the test value of heat-resistant Escherichia coli zero, totally meeting the IMO emission standards.

Effect of Rare Earths on Iron-Carbon Micro Electrolysis in Dyeing Wastewater Treatment

2014 ◽  
Vol 1010-1012 ◽  
pp. 190-194
Author(s):  
Xiao Gang Chen ◽  
Ju Chi Kuang ◽  
Min Hua Chen
Keyword(s):  
Wastewater Treatment ◽  
Removal Rate ◽  
Waste Water Treatment ◽  
Sewage Treatment ◽  
Main Role ◽  
Dyeing Wastewater ◽  
Related Factors ◽  
Orthogonal Experiments ◽  
Cerium Ion ◽  
Cod Removal Rate

In the paper we first discussed the principle of wastewater treatment by iron-carbon micro electrolysis. And the experimental methods were stated clear soon afterwards. Then we designed the micro electrolysis orthogonal experiments. Discussion of influences of related factors on waste water treatment followed. The main factors are cerium ion additive quantity, ratio of La3+/Ce4+ and pH in wastewater. The experimental results show that 1) The sequence of factors influence on wastewater micro-electrolysis treatment is Ce4+ > pH > La3+ > iron/carbon ratio; 2) The lanthanum and cerium ions have a synergistic effect in the wastewater treatment, and cerium ion plays a main role; 3) When pH is 6, COD removal rate arrives at maximum 89%, however when the pH is in the case of too high or too low, the effect of sewage treatment is not good.

scholarly journals Evaluation of four different coagulants used for chemical dephosphorization of membrane bioreactor effluent

2020 ◽  
Vol 167 ◽  
pp. 01009
Author(s):  
Qin Cai ◽  
Hui-qiang Li ◽  
Ping Yang
Keyword(s):  
Removal Efficiency ◽  
Phosphorus Removal ◽  
Continuous Flow ◽  
Membrane Bioreactor ◽  
Removal Rate ◽  
Sewage Treatment ◽  
Chemical Reactor ◽  
Domestic Sewage ◽  
Internal Loop ◽  
Polyaluminium Chloride

A continuous flow chemical reactor was constructed to study the dephosphorization effect on the effluent of the oxygen-limited internal-loop fluidized membrane bioreactor (IF-MBR) for domestic sewage treatment. Removal effect of total phosphorus (TP) by four coagulants of AlCl3, FeCl3, polyaluminum ferric chloride (PAFC) and polyaluminium chloride (PAC) was evaluated. Results showed that when the ratio of coagulants to TP was 5 (coagulants in terms of Fe and Al), the removal efficiency of TP by FeCl3 was 92.5% and the addition of FeCl3 resulted in an increase in the chromaticity of the effluent. PAC and PAFC had good removal of TP, and the removal percentage achieved 96.2 and 97.4, respectively. However, the flocs they produced were small and light, and the performance in settlement was poor. AlCl3 performed well as a phosphorus removal agent, the removal rate of TP reached 97.4%, and the flocs were large and dense. Based on this, AlCl3 was the best choice for IF-MBR and then the experiment further optimized the Al/P ratio. Results showed that when the Al/P ratio was above 1:1, the effluent TP concentration was lower than 1mg/L; when the ratio was higher than 2.5:1, the effluent TP was lower than 0.5mg/L.

A Research on the Efficiency of Hydrolysis-AICS in Sewage Treatment Plant in North-Cities

2015 ◽  
Vol 737 ◽  
pp. 635-638
Author(s):  
Ke Zhao ◽  
Zheng Kong
Keyword(s):  
Waste Water ◽  
Low Temperature ◽  
Removal Rate ◽  
Waste Water Treatment ◽  
National Level ◽  
Sewage Treatment ◽  
Sewage Treatment Plant ◽  
Treatment Plant ◽  
Urban Sewage ◽  
Cod Removal Rate

The general existing low temperature problem in winter of north-city sewage treatment plant in the process of waste water treatment seriously affect the efficiency of the work. The research objective of this paper is to conduct investigate in the application of AICS method in Jilin Province, a sewage treatment plant engineering example has been employed to monitor the effluent of the indicators of sewage treatment under the low temperature condition during the winter the winter low temperature under the condition of sewage treatment plant effluent of the indicators; to understand the operation situation of sewage treatment plant, and to study the efficiency of hydrolysis - AICS processing waste-water. The result shows that: hydrolysis - AICS process works well in low temperature condition, the per TN removal rate is 76.79%, average removal rate of NH3 - N is 85.76%, average TP removal rate was 93.4%, the average COD removal rate was 90.6%. The effluent meet the national level A discharge standard requirements of "urban sewage treatment plant pollutant discharge standard". And through the retrenchment of the second pond and other ancillary equipment, Hydrolysis-AICS process could efficiently reduce the costs. Besides, the advantages of Hydrolysis-AICS process also include occupying small area, and operating easily and simply. Therefore Hydrolysis-AICS process is very helpful to achieve the sewage discharging standard in the northern towns.

Performance of Treating Domestic Sewage with Coagulation-Ultrafiltration System

2015 ◽  
Vol 737 ◽  
pp. 557-560
Author(s):  
Hui Yuan Zhong ◽  
Guan Yi Liu ◽  
Jun Xia Li ◽  
Hao Wang
Keyword(s):  
High Efficiency ◽  
Removal Rate ◽  
Low Cost ◽  
Sewage Treatment ◽  
Membrane System ◽  
Integrated Treatment ◽  
Domestic Sewage ◽  
Ultrafiltration Membrane ◽  
Cod Removal Rate ◽  
Organic Particles

This study used coagulation - ultrafiltration technology for domestic sewage treatment, which was used widely in water supply and secondary treatment with sewage, in order to achieve high efficiency, low-cost, integrated treatment of domestic sewage treatment. This article chooses fly ash coagulant is not only simple preparation process, low cost, and with the traditional aluminum chloride and ferric chloride coagulation effect. The research results show that the coagulation can make the organic particles size distribution to move to larger particles area and significantly reduce colloidal substance. Ultrafiltration membrane system can further remove the coagulation treatment failed to completely remove polymer and part in the process of low molecular substances, to achieve high organic matter removal efficiency. The backwash of ultrafiltration membrane can make membrane flux recovery by about 80%. This system of SS can remove more than 95%, COD removal rate can reach 60% ~ 70%.

Study on the membrane bioreactor for treating surfactant wastewater

2018 ◽  
Vol 9 (2) ◽  
pp. 240-248 ◽  
Author(s):  
Zhilin Ran ◽  
Jia Zhu ◽  
Ke Li ◽  
Li Zhou ◽  
Pei Xiao ◽  
...  
Keyword(s):  
Membrane Bioreactor ◽  
Early Stage ◽  
Removal Rate ◽  
Sewage Treatment ◽  
Sewage Treatment Plant ◽  
Treatment Plant ◽  
Oxygen Demand ◽  
Optimal Level ◽  
Linear Alkylbenzene ◽  
Start Up

Abstract The main component of surfactant is linear alkylbenzene sulfonate (LAS), which is toxic to the ecological environment and can cause serious harm. In this study, some activated sludge was taken from the aerobic and anaerobic tank of a sewage treatment plant in Shenzhen, then cultivated and domesticated in a membrane bioreactor with artificial surfactant wastewater. The start-up phase of the reactor adapted the constant-flux filtration, and the HRT was 12 h. The pH was below 5.5, which needed the addition of NaHCO3 after 6 days to adjust to the more optimal level (pH 6.5–7.5). After operation for 20 days, the start-up of the system was considered successful. At the early stage, the removal rates of chemical oxygen demand (COD) and LAS were relatively stable, reaching as high as 85.49%–93.31% and 80%, respectively. When the LAS concentration reached over 175 mg/L and the COD declined to about 83%, the removal rate of LAS also significantly decreased. LAS removal rate further decreased to about 60% when the dosage reached 200 mg/L, indicating that the resistance of microorganisms against LAS toxicity was also limited. LAS degradation could have been mainly driven by Dechloromonas, Gemmata, Pseudomonas and Zoogloea in the system.

Experimental Study on the Treatment of Sewage by Soil

2013 ◽  
Vol 464 ◽  
pp. 179-183
Author(s):  
Xiao Hui Wang ◽  
Yong Zhang ◽  
Chong Hao Huang
Keyword(s):  
Removal Rate ◽  
Soil Column ◽  
Sewage Treatment ◽  
Column Experiment ◽  
Experimental Treatment ◽  
Cod Removal ◽  
Column Experiments ◽  
Soil Thickness ◽  
N Removal ◽  
Cod Removal Rate

The bath static experiments were conducted to study the sewage treatment effects by the typical yellow-brown soil of Xuzhou, the results obtained in this study showed that: The COD removal rate was about 50% or so through experimental treatment. The three days dynamic and intermittent soil column experiments show that: The COD removal rate was more than 80% by the simulated soil column experiments; the dynamic intermittent and soil column experiment both show that soil thickness influence the effect of phosphorus removal, the thicker layers, the better removal rate; the effective depth of NH4-N removal is deeper than 15cm.

High salinity wastewater treatment using yeast and bacterial membrane bioreactors

2002 ◽  
Vol 46 (9) ◽  
pp. 201-209 ◽  
Author(s):  
N.P. Dan ◽  
C. Visvanathan ◽  
C. Polprasert ◽  
R. Ben Aim
Keyword(s):  
Membrane Bioreactor ◽  
High Salinity ◽  
Removal Rate ◽  
Biomass Concentration ◽  
Cod Removal ◽  
Transmembrane Pressure ◽  
Bacterial Membrane ◽  
Average Biomass ◽  
Cod Removal Rate ◽  
Salinity Wastewater

Two laboratory-scale membrane bioreactor systems were investigated to treat high salinity wastewater containing high organic (5,000 mg/L COD) and salt content (32 g/L NaCl), namely: (1) the Yeast Membrane Bioreactor (YMBR) and; (2) Yeast pretreatment followed by Bacterial Membrane Bioreactor (BMBR). In the YMBR system, experimental runs were conducted with a mean biomass concentration of 12 g MLSS/L. Here the maximum COD removal rate of 0.93 g COD/g MLSS.day was obtained at F/M of 1.5 g COD /g MLSS.d. Whereas, the BMBR system was operated with a biomass concentration of up to 25 g MLSS/L, resulting in maximum COD removal rate of 0.32 kg COD /kg MLSS.day at F/M ratio of 0.4. In comparison to BMBR, YMBR could obtain higher COD removal rate at higher organic loading, indicating the potential of a yeast reactor system to treat high salinity wastewater containing high organic concentration. Transmembrane pressure in BMBR was progressively increased from 2 to 60 kPa after 12 d, 6 d and 2 d at a hydraulic retention time (HRT) of 14 h, 9 h and 4 h, with average biomass concentration of 6.1, 15 and 20 g MLSS/L, respectively. Whereas the transmembrane pressure in YMBR has increased from 2 to 60 kPa only after 76 days of operation, with an average biomass concentration of 12 MLSS/L and an operating HRT range of 5-32 h.

Study on Rural Sanitary Sewage Treatment in Compound Purifying Tank

2013 ◽  
Vol 726-731 ◽  
pp. 2599-2603
Author(s):  
Gong Di Xu ◽  
Jin Zhao Hu ◽  
Zhao Hui Huang ◽  
Da Dong Zhan ◽  
Chong Li ◽  
...  
Keyword(s):  
Removal Efficiency ◽  
Removal Rate ◽  
Sewage Treatment ◽  
Cod Removal ◽  
Removal Rates ◽  
Start Up ◽  
Potential Alternative ◽  
Cod Removal Rate

In the present work, a novel compound purifying tank was adopted in the rural sanitary sewage treatment. The cultivation and acclimation of biological film could be completed in a short start-up by aerobic precoating. According to the running results,the average COD removal rate reached 59.62%,and the removal efficiency of TP was 33.4%.For the denitrogenation,the removal rates were not remarkable (21.7 to NH4+-N,21.9 to TN),but the large removal quantity of NH4+-N and TN were abtained as 8.58mg/L and 9.12mg/L,respectively. The study suggests that the compound purifying tank is a potential alternative for rural sanitary sewage treatment.

Flocculation, Anaerobic and Microaerobic Treatment Process of Normal Temperature Low Concentration Domestic Sewage

2012 ◽  
Vol 518-523 ◽  
pp. 2530-2534
Author(s):  
Li Jun Nie ◽  
Hua Wen Zhong ◽  
Mei Huang ◽  
Xu Dong Yin
Keyword(s):  
Retention Time ◽  
Hydraulic Retention Time ◽  
Removal Rate ◽  
Sewage Treatment ◽  
Anaerobic Treatment ◽  
Domestic Sewage ◽  
Uasb Reactor ◽  
Anaerobic Sludge ◽  
Low Concentration ◽  
Cod Removal Rate

Domestic sewage was treated by adopting flocculation, anaerobic and microaerobic combined process under normal temperature. The result demonstrates: total hydraulic retention time is 5.5h (chemical flocculation 1.0h, UASB reactor 2.0h and MUSB reactor 2.5h). UASB reactor can achieve anaerobic sludge granulation under normal temperature and is fairly feasible for low concentration domestic sewage treatment. Compared with single stage UASB reactor, hydraulic retention time of flocculation-UASB combined technique reduces from 4h to 2h. COD removal rate rises from 45% to 50%-60% and suspended COD is mainly removed. DO of microaerobic MUSB technique after anaerobic treatment is 0.2mg/L-0.5mg/L with air and water ratio of 1:1. Effluent quality is stable, in accordance with first standard of Synthetical Draining Standard of Sewage, GB8978—1996.

Comparison of the behaviour of selected micropollutants in a membrane bioreactor and a conventional wastewater treatment plant

2004 ◽  
Vol 50 (5) ◽  
pp. 29-36 ◽  
Author(s):  
M. Clara ◽  
B. Strenn ◽  
M. Ausserleitner ◽  
N. Kreuzinger
Keyword(s):  
Wastewater Treatment ◽  
Activated Sludge ◽  
Removal Efficiency ◽  
Membrane Bioreactor ◽  
Endocrine Disrupting Chemicals ◽  
Sewage Treatment ◽  
Treatment Plant ◽  
Point Sources ◽  
Treated Wastewater ◽  
Treatment Technique

Micropollutants as pharmaceutical active compounds (PhACs), residuals of personal care products or endocrine disrupting chemicals are of increasing interest in water pollution control. In this context the removal efficiencies of sewage treatment plants (STPs) are of importance, as their effluents are important point sources for the release of those substances into the aquatic environment. Activated sludge based wastewater treatment is the worldwide prevalently used treatment technique. In conventional plants the separation of treated wastewater and sludge occurs via sedimentation. A new development is the application of membrane technology for this separation step. The studies focus on the influence of the solids retention time (SRT) on the removal efficiency, as the SRT is the most important parameter in the design of STPs. A conventional activated sludge plant (CASP) and a membrane bioreactor (MBR) were operated at different SRTs. The substances selected are the antiepileptic carbamazepine, the analgesics diclofenac and ibuprofen, the lipid regulator bezafibrate, the polycyclic musks tonalide and galaxolide and the contraceptive 17α-ethinylestradiole. No significant differences in the removal efficiency were detected. Due to the absence of suspended solids in the MBR effluent, substances with high adsorption potential could be retained to slightly higher amounts.

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