Combined experiences of thermal hydrolysis and anaerobic digestion – latest thinking on thermal hydrolysis of secondary sludge only for optimum dewatering and digestion

2008 ◽  
Vol 2008 (15) ◽  
pp. 1964-1978 ◽  
Author(s):  
P. Camacho ◽  
W. Ewert ◽  
J Kopp ◽  
K. Panter ◽  
S. I. Perez-Elvira ◽  
...  
Data in Brief ◽  
2021 ◽  
pp. 107323
Author(s):  
Mohamed N.A. Meshref ◽  
Seyed Mohammad Mirsoleimani Azizi ◽  
Wafa Dastyar ◽  
Rasha Maal-Bared ◽  
Bipro Ranjan Dhar

2008 ◽  
Author(s):  
W. Qiao ◽  
W. Wang ◽  
R. Xun ◽  
Kazuyuki Tohji ◽  
Noriyoshi Tsuchiya ◽  
...  

2018 ◽  
Vol 72 ◽  
pp. 186-192 ◽  
Author(s):  
Michael Bjerg-Nielsen ◽  
Alastair James Ward ◽  
Henrik Bjarne Møller ◽  
Lars Ditlev Mørck Ottosen

2012 ◽  
Vol 65 (10) ◽  
pp. 1839-1846 ◽  
Author(s):  
S. I. Pérez-Elvira ◽  
F. Fdz-Polanco

Experimental data obtained from the operation in a pilot plant are used to perform mass and energy balances to a global process combining units of thermal hydrolysis (TH) of secondary sludge, anaerobic digestion (AD) of hydrolysed secondary sludge together with fresh primary sludge, and cogeneration from biogas by using a gas engine in which the biogas produces electricity and heat from the exhaust gases. Three scenarios were compared, corresponding to the three digesters operated: C (conventional AD, 17 days residence time), B (combined TH + AD, same time), and A (TH + AD at half residence time). The biogas production of digesters B and A was 33 and 24% better, respectively when compared with C. In the case of the combined TH + AD process (scenarios A and B), the key factors in the energy balance were the recovery of heat from hot streams, and the concentration of sludge. The results of the balances showed that for 8% DS concentration of the secondary sludge tested in the pilot plant, the process can be energetically self-sufficient, but a fraction of the biogas must by-pass the gas engine to be directly burned. From an economic point of view, scenario B is more profitable in terms of green energy and higher waste removal, while scenario A reduces the digester volume required by a half. Considering a population of 100,000 inhabitants, the economic benefit is 87,600 €/yr for scenario A and 132,373 €/yr for B. This value can be increased to 223,867 €/yr by increasing the sludge concentration of the feeding to the TH unit to a minimum value that allows use of all the biogas to produce green energy. This concentration is 13% DS, which is still possible from a practical point of view. Additional benefits gained with the combined TH + AD process are the enhancement of the digesters rheology and the possibility of getting Class A biosolids. The integration study presented here set the basis for the scale-up to a demonstration plant.


2008 ◽  
Vol 3 (1) ◽  
Author(s):  
Julien Chauzy ◽  
Didier Cretenot ◽  
Anne Bausseron ◽  
Stéphane Deleris

Veolia Water has developed during these last years its own THP (Thermal Hydrolysis Process) named BIOTHELYS® in order to enhance MAD (mesophilic anaerobic digestion) of municipal or industrial sludge. The first reference BIOTHELYS® has been installed at Saumur in France, an extended aeration biological nutrient removal facility, and commissioned in April 2006. The thermal hydrolysis of dewatered sludge is realised by steam injection at a temperature of 160°C for duration of circa 30 minutes. The THP reactors are paired in order to recover flash steam and heat sludge economically. The MAD of hydrolysed sludge is done within a HRT of 15 days and reaches volatile reduction of more than 45% on extended aeration biological sludge. BIOTHELYS® turns the MAD of extended aeration biological sludge into a very attractive solution while producing green energy with biogas. MAD is thus no more only reserved for mixed sludge but also for pure biological sludge when using THP.


2018 ◽  
Vol 132 ◽  
pp. 158-166 ◽  
Author(s):  
Kine Svensson ◽  
Oda Kjørlaug ◽  
Matthew J. Higgins ◽  
Roar Linjordet ◽  
Svein J. Horn

2002 ◽  
Vol 2002 (3) ◽  
pp. 442-451 ◽  
Author(s):  
James L. Barnard ◽  
Pat Coleman ◽  
Phil Weston

2017 ◽  
Vol 122 ◽  
pp. 557-569 ◽  
Author(s):  
Matthew J. Higgins ◽  
Steven Beightol ◽  
Ushma Mandahar ◽  
Ryu Suzuki ◽  
Steven Xiao ◽  
...  

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