Mixing Efficiency Comparison of Symmetric and Asymmetric Airfoil Blades in a Continuous Stirred Tank Reactor

2020 ◽  
Vol 142 (5) ◽  
Author(s):  
Manosroi Woradej ◽  
Thongsanitkarn Jirayu ◽  
Ruangsak Parinya

Abstract This study compared mixing efficiencies of the symmetric and asymmetric airfoil blades in a continuous stirred tank reactor (CSTR) at various mixing velocities and angles of attack. The symmetric airfoil blades (NACA0009 and NACA0015) and asymmetric airfoil blades (NACA2414 and NACA4412) were set at different angles of attack and mixing velocities. The tank reactor was equipped with two sets of three airfoil blades at the upper and the lower parts of the stirring shafts at the angles of attack 0 deg, 10 deg, 16 deg, and 20 deg, and the mixing velocities of 80, 110, 140, and 190 rpm. The mixing efficiencies were evaluated from the homogenous appearance of plastic particles (5 mm in diameter) dispersed in water by an image processing technique. The results indicated that the mixing efficiencies of both the symmetric and asymmetric airfoil blades increased with increasing mixing velocities and at the angles of attack 0 deg and 10 deg, and slightly decreased with increasing mixing velocities at the angles of attack 16 deg and 20 deg due to the blade stall and mixing saturation as well as short-circuiting flow from the high flowrate. There was no significant mixing velocity effect on mixing efficiencies at the angles of attack 10 deg, 16 deg, and 20 deg except 0 deg of the symmetric and asymmetric airfoil blade systems. The two asymmetric airfoil blade types gave higher mixing efficiencies than the two symmetric airfoil blade types. The results from this study can be applied for a novel blade design for an efficient mixing flow, which will be beneficial for industrial biogas production.

2010 ◽  
Vol 113-116 ◽  
pp. 1345-1348
Author(s):  
Yong Feng Li ◽  
Jie Xuan Deng ◽  
Hong Chen ◽  
Xin Yao ◽  
Shuang Gao

This study discusses the hydrogen-producing properties of continuous stirred tank reactor (CSTR) after inoculating the Biohydrogenbacterium R3. Biohydrogenbacterium R3 grow well and produce H2 stably at temperature of (35±1)°C and HRT of 6 hours. In this study, the optimum range of pH is 4.5~4.6. The amount of biogas production and H2 content maintained at 3.4 L and 47%, respectively. The main liquid end products are ethanol and acetic acid. Dry cell weight changes showed wavy. COD removal is about 16%~18%.


2018 ◽  
Vol 29 (7) ◽  
pp. 1130-1141 ◽  
Author(s):  
Emmanuel Alepu Odey ◽  
Kaijun Wang ◽  
Zifu Li ◽  
Ruiling Gao

This study investigated the efficiency of biogas production from sewage concentrate through anaerobic digestion. A continuous stirred tank reactor with a 900-mL working volume was used. The experiment was designed to investigate the influence of organic loading rate on the efficiency of biogas production and to determine the most suitable organic loading rate condition for methane production from sewage concentrate by using continuous stirred tank reactor. The reactor was operated at different organic loading rates of 1.8, 0.8, and 0.6 gCOD/(L.d). The methane composition of the biogas produced from the treatment organic loading rate (OLR). The beginning of the experiment recorded low methane production because of the high organic loading rate. However, the later part of the experiment recorded high and stable biogas production because of the relatively low OLR. Results suggested that a 0.6 gCOD/(L.d) OLR was the most efficient setup parameter for ideal methane production from sewage concentrate by using continuous stirred tank reactor.


2013 ◽  
Vol 19 (2) ◽  
pp. 173-179 ◽  
Author(s):  
Taghizade Firozjaee ◽  
Ghasem Najafpour ◽  
Ali Asgari ◽  
Maryam Khavarpour

In the present study, an anaerobic continuous stirred tank reactor (ACSTR) with consortium of mixed culture was operated continuously for a period of 110 days. The experiments were performed with three different hydraulic retention times and by varying initial phenol concentrations between 100 to 1000 mg/L. A maximum phenol removal was observed at a hydraulic retention time (HRT) of 4 days, with an organic loading rate (OLR) of 170.86 mg/L.d. At this condition, phenol removal rate of 89% was achieved. In addition, the chemical oxygen demand (COD) removal corresponds to phenol removal. Additional operating parameters such as pH, MLSS and biogas production rate of the effluents were also measured. The present study provides valuable information to design an anaerobic ACSTR reactor for the biodegradation of phenolic wastewater.


2020 ◽  
Vol 8 (1) ◽  
pp. 022
Author(s):  
Rinjani Rakasiwi ◽  
Wivina Ivontianti ◽  
Eva Sitanggang

Abstract Organic waste is material that has no value but can be used as raw material to produce biogas. It is easier to handle by anaerobic processing. The advantages of biogas by using anaerobic digestion process are minimizes the effects of environmental pollutions, reduce emissions and increase the value of the benefits of waste. The purposes of this research are to design a digester for processing organic waste into biogas and find out the impact of biogas production on emissions reduction. Biogas production was analyzed using gas Chromatography (GC) and emission reductions were calculated using the AP-42 (Compilation of Air Pollutant Emissions Factors) equation. The digester used is a CSTR which is suitable for liquid phase and for organic chemical reactions with large conversions. Parameters that affect the performance of the reactor are the residence time on the flow of substances in the reactor, Hydraulic Retention Time (HRT). HRT can affect the growth of fermentative bacteria corelation with the production of biogas. The optimum volume of biogas of 16.52 Liters / Day with the acquisition of CH4 of 75,893.36 ppm was on the 13th day in a variation of HRT 20. Every 20 kg of organic waste that has been processed in the digester, it will be reducing 76.5 g / day of CO emissions. Keywords: anaerobic digestion, CSTR (Continuous Stirred Tank Reactor), HRT (Hydraulic Retention Time), trashAbstrakSampah organik merupakan bahan yang tidak mempunyai nilai atau tidak berharga tetapi dapat dijadikan sebagai bahan baku pembuatan biogas, karena lebih mudah untuk ditangani dan dapat dilakukan dengan proses anaerobik. Kelebihan dari biogas dengan menggunakan proses anaerobic digestion akan meminimalkan efek dari pencemaran lingkungan, mengurangi emisi dan meningkatkan nilai manfaat dari limbah. Tujuan penelitian ini adalah merancang digester untuk pengolahan sampah organik menjadi biogas dan mengetahui dampak produksi biogas yang dihasilkan terhadap pengurangan emisi. Produksi biogas dianalisa menggunakan Chromatografi gas (GC) dan pengurangan emisi dihitung menggunakna persamaan AP-42 (Compilation of Air Polutant Emissions Factors). Digester yang digunakan merupakan reaktor tipe alir tangki berpengaduk/CSTR untuk reaksi fase cair dan juga digunakan untuk reaksi kimia organik dengan konversi yang besar. Parameter yang mempengaruhi kinerja reaktor yaitu waktu tinggal pada zat alir di dalam reaktor atau disebut dengan Hydraulic Retention Time (HRT). HRT dapat mempengaruhi pertumbuhan bakteri fermentatif yang terkait dengan hasil produksi biogas. Hasil volume biogas optimum sebesar 16,52 Liter/Hari dengan perolehan CH4 sebesar 75.893,36 ppm berada di hari ke- 13 pada variasi HRT 20. Sampah organik sebanyak 20 kg diolah di digester mengurangi 76,5 g/hari emisi CO. Kata kunci: anaerobic digestion, CSTR (Continuous Stirred Tank Reactor), HRT (Hydraulic Retetion Time), sampah.


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