2017
DOI: 10.1007/s11356-017-9943-z
|View full text |Cite
|
Sign up to set email alerts
|

Heat transfer analysis of cylindrical anaerobic reactors with different sizes: a heat transfer model

Abstract: The temperature is the essential factor that influences the efficiency of anaerobic reactors. During the operation of the anaerobic reactor, the fluctuations of ambient temperature can cause a change in the internal temperature of the reactor. Therefore, insulation and heating measures are often used to maintain anaerobic reactor's internal temperature. In this paper, a simplified heat transfer model was developed to study heat transfer between cylindrical anaerobic reactors and their surroundings. Three cylin… Show more

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
3
1
1

Citation Types

0
2
0
2

Year Published

2019
2019
2024
2024

Publication Types

Select...
6
1

Relationship

0
7

Authors

Journals

citations
Cited by 9 publications
(5 citation statements)
references
References 22 publications
0
2
0
2
Order By: Relevance
“…Among these questions, the distribution of temperature fields in unit operations could affect the overall chemical kinetics and even the final product formation. [ 31 ] As such, the chief design principle of enlarged reaction vessels should focus on advancing the inner heat transfer in fluid during the engineering process. Theoretically, the increase of the fluidic velocity field (or Reynolds number, denoted as R e, the corresponding viscous fluid will change from laminar flow to transition and turbulent flow) can lead to the decreased thickness of the boundary layer, which enhances the convective heat transfer coefficient in turn ( Figure a).…”
Section: Resultsmentioning
confidence: 99%
“…Among these questions, the distribution of temperature fields in unit operations could affect the overall chemical kinetics and even the final product formation. [ 31 ] As such, the chief design principle of enlarged reaction vessels should focus on advancing the inner heat transfer in fluid during the engineering process. Theoretically, the increase of the fluidic velocity field (or Reynolds number, denoted as R e, the corresponding viscous fluid will change from laminar flow to transition and turbulent flow) can lead to the decreased thickness of the boundary layer, which enhances the convective heat transfer coefficient in turn ( Figure a).…”
Section: Resultsmentioning
confidence: 99%
“…5 . Where: Q T is biogas required for fermentation temperature maintaining at time interval of △t (MJ); 21.54 is the caloric value of biogas containing 60% methane (MJ m −3 ); 0.7 is the heat efficiency of biogas conversion and heat exchange for maintaining fermentation temperature 55 . The thermal balance calculation of Q T is described in Supplementary Note 2 .…”
Section: Methodsmentioning
confidence: 99%
“…Related calculations involved in the preliminary energy analysis are shown in Figure 1, where C = specific heat of influent, which approximated to water, 4.18 KJ/(kg • C); V I = the flow volume fed to the digester per day; φ = the electricity energy used for pumping, 0.5 KWh/m 3 (Lu et al, 2008;Mu et al, 2018); ω = the electricity energy used for stirring, 0.08 KWh/(m 3 •d) (Lu et al, 2008;Mu et al, 2018); The material used for the designed reactor was 300 mm thick insulated concrete wall, U = heat transfer coefficient, 1.99 W/(m 2 • • C) (Liu et al, 2017a); A = superficial area of reactor, which was calculated according to the calculation formula, 1152 m 2 ; T 1 = ambient temperature, which is close the average annual temperature in China, 10.3 • C; T 2 = reactor temperature, 35 • C for mesophilic condition or 55 • C for thermophilic condition; The efficiency of the CHP in converting biogas into thermal and electricity energy were 33 and 50%, respectively (Feiz et al, 2019;Valentino et al, 2019), H M = calorific value of methane, 35.8 kJ/L (Chen et al, 2019), and V M = volume of methane produced.…”
Section: Preliminary Energy Analysismentioning
confidence: 99%