scholarly journals Tower bio-vermifilter system for rural wastewater treatment: bench-scale, pilot-scale, and engineering applications

2014 ◽  
Vol 12 (3) ◽  
pp. 1053-1064 ◽  
Author(s):  
E. Nie ◽  
D. Wang ◽  
M. Yang ◽  
X. Luo ◽  
C. Fang ◽  
...  
1985 ◽  
Vol 17 (11-12) ◽  
pp. 287-288 ◽  
Author(s):  
R. Ramadori ◽  
V. Tandoi ◽  
A. Misiti

In connection with studies aimed at developing low-energy wastewater treatment processes considerable interest has been shown in the possibility of removal of phosphorus biologically rather than chemically. The results over one year from bench and pilot scale tests conducted with synthetic and settled domestic wastewaters respectively are reported. The pilot plant was installed in one of the Rome urban wastewater treatment works and consisted of a two stage (anaerobic-aerobic) system. The wastewater was withdrawn downstream from the primary settling tank and conveyed to the anaerobic reactor of the pilot plant. A similar experiment was conducted in a three reactor (two anaerobic and one aerobic) bench scale plant, where a synthetic solution (peptone, sodium acetate and potassium phosphate) was fed under rigorously controlled conditions of temperature, pH and dissolved oxygen. Both bench and pilot scale tests were designed to verify and quantify the biological removal of phosphorus; the performances of both phosphorus removal test scale systems were compared with those from a reference aerobic plant operating under the same conditions. The impact of several parameters on the biological removal of phosphorus were examined. These parameters were: nature of carbonaceous substrate, carbonaceous/phosphorus ratio, sludge age; etc. Considerable care and attention was given to checking phosphorus balances, once the steady state conditions had been obtained. The results can be summarized as follows:-Phosphorus removal was found to be greater in plants with an anaerobic stage than in the reference plants. At pilot scale level this is clearly shown by the plot of the daily phosphate concentration in the effluents. At bench scale it is shown by comparison between P contents in sludges (9.9% vs. 5.0%) and by the fact that, at the end of the experiment, large deposits of inorganic phosphate (mainly of Ca and Mg) were found on the walls of both anaerobic reactors. The unstable operating conditions of the reference plant due to the poor sedimentation characteristics of the sludges leading to uncontrolled losses of biomass meant it was impossible to obtain a reliable mean phosphorus abatement value, which in any case was always well below that found for the P-removal plant.-As reported above, the deficit in the phosphorus balance was due to inorganic phosphate precipitation. In this connection an excellent quantitative agreement was found between the deficit in the balance and the quantity of phosphorus collecting in the anaerobic reactors.-Phosphorus release from the biomass under anaerobic conditions has already been completed in the first anaerobic reactor (where carbonaceous substrate uptake also occurs) and the use of the second anaerobic reactor seems to allow a more complete phosphate precipitation.-Part of the carbonaceous substrate which disappears during the first anaerobic stage is metabolized. In fact, in this reactor, the complete disappearance of organic nitrogen is accompanied by the release of large quantities of ammoniacal nitrogen. Lastly, despite the fact that the values of the main operative parameters, such as hydraulic retention time, sludge age, temperature, pH and dissolved oxygen, were kept rigorously constant, a certain instability was found in the biomass as regards the maintaining of such high phosphorus removal efficiencies over long periods of time. This may be due to the highly variable biological population dynamics.


2021 ◽  
Vol 2021 ◽  
pp. 1-8
Author(s):  
Minh-Trung Dao ◽  
Vo-Chau-Ngan Nguyen ◽  
Thanh-Nha Tran ◽  
Xuan-Du Nguyen ◽  
Duc-Thuong Vo ◽  
...  

Plant-derived coagulants have exhibited a good potential in wastewater treatment due to their “green” characteristics, high coagulating-flocculating activity, cost-effectiveness, and biodegradability. Nevertheless, research studies have focused mainly on bench-scale experiments; pilot-scale and full-scale simulations are still limited. Herein, we firstly report a pilot-scale study of real domestic textile wastewater treatment using Cassia fistula coagulant. The material characterizations using Fourier-transform infrared spectroscopy (FTIR), scanning electron microscope (SEM), and dynamic light scattering (DLS) revealed that the natural gum extracted from C. fistula seed possessed a rough and irregular surface containing a high molecular weight galactomannan. The bench-scale investigation was initially conducted to determine the optimal pollutant concentration, initial pH, and coagulant dosage in the coagulation-flocculation process. The pilot-scale study revealed that C. fistula coagulant is an effective material for real textile wastewater treatment, showing percentage removal of 93.83% at a volume of 30 L and a coagulant dosage of 1.17 mg·L−1. Coagulation-flocculation using C. fistula seed gum could be an efficient primary wastewater treatment prior to membrane or biological methods to meet Vietnamese environmental standards. The main mechanisms of textile wastewater treatment involve adsorption/bridging interactions via hydrogen bonding and electrostatic attraction between negatively charged carboxylate groups of the coagulant and positively charged pollutants.


2008 ◽  
Vol 57 (12) ◽  
pp. 1857-1865 ◽  
Author(s):  
E. O'Reilly ◽  
M. Rodgers ◽  
X.-M. Zhan

A novel laboratory bench-scale sequencing batch biofilm reactor (SBBR) system was developed for the treatment of synthetic domestic strength wastewater, comprising two side-by-side 18 l reactor tanks, each containing a plastic biofilm media module. Aerobic and anoxic conditions in the biofilms were effected by intermittent alternate pumping of wastewater between the two reactors. With a media surface area loading rate of 4.2 g chemical oxygen demand (COD)/m2.d, the average influent COD, total nitrogen (TN) and ammonium-nitrogen (NH4-N) concentrations of 1021 mg/l, 97 mg/l and 54 mg/l, respectively, reduced to average effluent concentrations of 72 mg COD/l, 17.8 mg TN/l, and 5.5 mg NH4-N /l. Using a similar alternating biofilm exposure arrangement, a 16 person equivalent pilot (PE) plant was constructed at a local village treatment works to remove organic carbon from highly variable settled municipal wastewater and comprised two reactors, one positioned above the other, each containing a module of cross-flow plastic media with a surface area of 100 m2. Two different pumping sequences (PS) in the aerobic phase were examined where the average influent COD concentrations were 220 and 237 mg/l for PS1 and PS2, respectively, and the final average effluent COD was consistently less than 125 mg/l – the European Urban Wastewater Treatment Directive limit – with the best performance occurring in PS1. Nitrification was evident during both PS1 and PS2 studies. A 300 PE package treatment plant was designed based on the bench-scale and pilot-scale studies, located at a local wastewater treatment works and treated municipal influent with average COD, suspended solids (SS) and TN concentrations of 295, 183 and 15 mg/l, respectively resulting in average effluent concentrations of 67 mg COD/l, 17 mg SS/l and 9 mg TN/l. The SBBR systems performed well, and were simple to construct and operate.


1982 ◽  
Vol 14 (9-11) ◽  
pp. 1269-1277
Author(s):  
John M Sidwick

The paper considers some of the problems of the scale-up of wastewater treatment processes; from bench-scale to pilot-scale, and from pilot-scale to full-scale. An attempt is made to put the question of scale-up problems into perspective by reference to the experience of the author and the work of others reported in the literature.


2018 ◽  
Vol 68 (12) ◽  
pp. 2752-2755
Author(s):  
Carmen Tociu ◽  
Tania Zaharia ◽  
Elena Diacu ◽  
Cristina Maria ◽  
Florica Marinescu ◽  
...  

This paper depicts the research conducted at a micro-pilot scale on autochthonous cultures in order to develop adequate technological solutions for the treatment of wastewater resulting from shrimp cultures (Palaemonidae) that would ensure the protection of the Black Sea ecosystem and constitute an applicable tool for the development of aquaculture in Romania. The proposed objectives were attained by adopting an integrated system of marine cultures shrimps-mussels-macrophyte algae, followed by a conventional chemical treatment step using aluminium sulphate recovered from metallurgical slags. This system together with wastewater treatment ensures an optimum development of species and a minimum load of pollutants in the aquatic environment.


1996 ◽  
Vol 33 (7) ◽  
pp. 165-171 ◽  
Author(s):  
J. Soares ◽  
S. A. Silva ◽  
R. de Oliveira ◽  
A. L. C. Araujo ◽  
D. D. Mara ◽  
...  

Ammonia removal was monitored in a waste stabilisation pond complex comprising ponds of different geometries and depths under two different operational regimes. It was found that a high degree of ammonia removal commenced in the secondary maturation ponds, with the highest removals occurring in the shallowest ponds as a consequence of improved aerobic conditions. The tertiary maturation ponds produced effluents with mean ammonia concentrations of < 5 mg N/l, the maximum permitted recommended by Brazilian environmental legislation for the discharge of effluents of wastewater treatment plants into surface waters. Ammonia removal in the secondary facultative and maturation ponds could be modelled using equations based on the volatilization mechanism proposed by Middlebrooks et al. (1982).


2010 ◽  
Vol 62 (8) ◽  
pp. 1965-1965
Author(s):  
S. Park ◽  
J. Lee ◽  
J. Park ◽  
I. Byun ◽  
T. Park ◽  
...  

Publisher‘s note. We regret that the published version of this article erroneously denoted the first author as corresponding author; in fact the formal corresponding author of this paper is Professor Taeho Lee, whose address is repeated below.


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