Effect of various design and operation parameters on performance of pilot-scale Sludge Drying Reed Beds

2012 ◽  
Vol 38 (1) ◽  
pp. 65-78 ◽  
Author(s):  
Alexandros I. Stefanakis ◽  
Vassilios A. Tsihrintzis
Keyword(s):  
Pilot Scale ◽  
Reed Beds ◽  
Operation Parameters ◽  
Sludge Drying

Characteristics of Sludge Moisture Content Variation in Sludge Drying Reed Beds

2015 ◽  
Vol 768 ◽  
pp. 515-519
Author(s):  
Xin Nan Deng ◽  
Yu Bo Cui ◽  
Wei Gao ◽  
Rui Chen
Keyword(s):  
Moisture Content ◽  
Pilot Scale ◽  
Coarse Sand ◽  
Reed Beds ◽  
Conventional Drying ◽  
The Media ◽  
The Difference ◽  
Reed Bed ◽  
Sludge Drying ◽  
Media Layer

Sludge moisture content was investigated at different stages during the test. Pilot-scale sludge drying bed and sludge drying reed beds had the same size of 3 m×1 m×1.3 m, and the bed height consisted of a 65 cm media layer and a 65 cm extra height. The media layer is filled with slag (20 cm), gravel (20 cm), coarse sand (5 cm) and quartz sand (24.5 cm) from the bottom in turn. Unit 1 was a conventional sludge drying bed, unit 2 was a sludge drying reed bed. Unit 1 and unit 2 had ventilation pipes which were mounted on the drainage pipes. Unit 3 was a sludge drying reed bed without ventilation pipe. The waste activated sludge was feed into the three units periodically during the experiment. The experiment investigated the sludge moisture content. At the end of the operation, the sludge moisture content in three units decreased by 18.52%, 22.37%, and 20.68%, respectively. It was found that the dewatering effect of the sludge drying reed bed was better than the conventional drying bed. The effect of plant growth on sludge dewatering is greater than the ventilation, but the difference was not significant.

scholarly journals Treatment of septage in sludge drying reed beds: a case study on pilot-scale beds

2009 ◽  
Vol 60 (3) ◽  
pp. 643-653 ◽  
Author(s):  
S. Troesch ◽  
A. Liénard ◽  
P. Molle ◽  
G. Merlin ◽  
D. Esser
Keyword(s):  
Wastewater Treatment Plants ◽  
Bound Water ◽  
Pilot Scale ◽  
Simultaneous Treatment ◽  
Capillary Suction ◽  
Reed Beds ◽  
Operational Conditions ◽  
Rural Zone ◽  
Sludge Drying ◽  
Sanitation Systems

French legislation requires the control of private on-site sanitation systems by local authorities. This will result in a large increase of the quantity of sludge from septic tanks to be treated. Nevertheless, large wastewater treatment plants are not systematically able to treat this sludge because they may have reached their nominal load or they are not so numerous in rural zone to avoid too long transportation. The study concerns both the feasibility of sludge reed beds devoted to the treatment of septage and the assessment of a simultaneous treatment with aerated sludge. The experiments have been carried out on eight pilot-scale drying reed beds (2 m2) planted with Phragmites australis. Two filtration layers of either vegetal compost or sand were tested. The study is focused on the commissioning period (first vegetative year) with a loading rate of 30 kg SS m−2 yr−1. According to these operational conditions, dewatering efficiencies reached approx. 30% DM during summer but less than 20%DM in winter for each filtration layer and sludge. High removal efficiencies, with an average of 96%, 92% and 89% for SS, COD and TKN respectively, were achieved with septage whereas they were lower for the mixture of aerated sludge and septage. The dewaterability of septage and its filtration behaviour were assessed by several parameters (Capillary Suction Time, bound water) which may be some interesting tools for an optimised loading strategy.

Surplus activated sludge dewatering in pilot-scale sludge drying reed beds

2009 ◽  
Vol 172 (2-3) ◽  
pp. 1122-1130 ◽  
Author(s):  
A.I. Stefanakis ◽  
C.S. Akratos ◽  
P. Melidis ◽  
V.A. Tsihrintzis
Keyword(s):  
Activated Sludge ◽  
Pilot Scale ◽  
Sludge Dewatering ◽  
Reed Beds ◽  
Sludge Drying

Small wastewater treatment plants in Flanders (Belgium): standard approach and experiences with constructed reed beds

2000 ◽  
Vol 41 (1) ◽  
pp. 57-63 ◽  
Author(s):  
S. Vandaele ◽  
C. Thoeye ◽  
B. Van Eygen ◽  
G. De Gueldre
Keyword(s):  
Wastewater Treatment ◽  
Removal Efficiency ◽  
Wastewater Treatment Plants ◽  
Treatment Plant ◽  
Pilot Scale ◽  
Surface Flow ◽  
Limiting Factor ◽  
Vertical Flow ◽  
Reed Beds ◽  
Reed Bed

In Flanders (Belgium) an estimated 15% of the population will never be connected to a central wastewater treatment plant (WWTP). Small WWTPs can be a valuable option. Aquafin bases the decision to build SWWTPs on a drainage area study. To realise an accelerated construction the process choice is made accordingly to a standard matrix, which represents the different technologies in function of the size and the effluent consents. A pilot scale constructed two-stage reed bed is used to optimise the concept of the reed beds. The concept consists of a primary clarifier, two parallel vertical flow reed beds followed by a sub-surface flow reed bed. The removal efficiency of organic pollutants is high (COD: 89%, BOD: 98%). Phosphorus removal is high at the start-up but diminishes throughout the testing period (from 100% to 71% retention after 7 months). Nitrogen removal amounts to 53% on average. Nitrification is complete in summer. Denitrification appears to be the limiting factor. In autumn leakage of nitrogen is assumed. Removal efficiency of pathogens amounts to almost 99%. Clogging forms a substantial constraint of the vertical flow reed bed. Problems appear to be related with presettlement, feed interval and geotextile.

Multistage treatment wetland for treatment of reject waters from digested sludge dewatering

2013 ◽  
Vol 68 (6) ◽  
pp. 1223-1232 ◽  
Author(s):  
M. Gajewska ◽  
H. Obarska-Pempkowiak
Keyword(s):  
High Efficiency ◽  
Oxygen Demand ◽  
Pilot Scale ◽  
Nitrogen Compounds ◽  
High Concentration ◽  
Treatment Wetland ◽  
Sludge Dewatering ◽  
Digested Sludge ◽  
Reed Beds ◽  
Colloidal Fraction

The paper presents the influence of sewage composition on treatment in pilot-scale facility for reject waters (RW) from sewage sludge centrifugation. The facility consisted of mechanical (two tanks with 10 d retention each) and biological parts composed of three subsurface flow reed beds working in batch. Two years of monitoring of the facility proved high efficiency removal of predominant pollutants: chemical oxygen demand (COD) 75–80%, biochemical oxygen demand (BOD) 82.2–95.5% and total nitrogen 78.7–93.9% for low ratio of BOD5/COD in discharged RW. The differences in efficiency removal were correlated with the composition of organics and nitrogen compounds rather than with concentrations. It was assumed that high concentration of colloidal fraction of Org-N and COD in discharged RW led to a decrease in efficiency removal.

scholarly journals Utilização de Filtros Plantados com Macrófitas para o Desaguamento e Mineralização de Lodo de Tanque Séptico (Use of Sludge Drying Reed Beds for Dewatering and Mineralization of Sludge from Septic Tank)

2013 ◽  
Vol 5 (6) ◽  
pp. 1271
Author(s):  
Daniel Ferreira de Castro Furtado ◽  
Luiz Sérgio Philippi ◽  
Carla Suntti ◽  
Ricardo Regi
Keyword(s):  
Social Impact ◽  
Hydraulic Retention Time ◽  
Sewage Treatment ◽  
Average Concentration ◽  
Septic Tank ◽  
Reed Beds ◽  
Sewage Treatment Plants ◽  
Complex Processes ◽  
Residual Sludge ◽  
Sludge Drying

Os lodos de esgotos tornaram-se uma importante questão na gestão das cidades devido ao enorme volume produzido diariamente, ao potencial de impacto ambiental e social deste produto e ao fato de seu gerenciamento e disposição serem um dos processos mais complexos em estações de tratamento de esgotos. Os objetivos deste estudo foram avaliar a eficiência de filtros plantados com macrófitas no tratamento de lodo de tanque séptico e monitorar o processo de desaguamento e mineralização do lodo acumulado no leito do filtro. O sistema foi operado semanalmente com taxa de 125 kgST/m².ano e tempo de detenção hidráulica de 6 dias. O filtro apresentou eficiências de 95, 99, 87 e 95% para os parâmetros ST, DQOt, N-NH4+ e P-PO43-, respectivamente. O lodo acumulado apresentou a maior concentração de ST (49%), 83 dias após o último ciclo de alimentação do filtro. A concentração média de ST do lodo acumulado permitiu classificá-lo como sólido duro. Palavras-chave: lodo de tanque séptico; filtros plantados com macrófitas; tratamento de lodo séptico; biossólidos. Use of Sludge Drying Reed Beds for Dewatering and Mineralization of Sludge from Septic Tank ABSTRACT The sewage sludge has become an important issue in the management of cities due to the volume produced daily, the potential environmental and social impact of this product and the fact that its management and disposition to be one of the most complex processes in sewage treatment plants. The objectives of this study were to evaluate the efficiency of sludge drying reed beds in the treatment of septic tank sludge and monitor the process of dewatering and mineralization of the residual sludge. The system was operated weekly, with rate of 125 kgST/m².year and hydraulic retention time of 6 days. The filter presented efficiencies of 95, 99, 87 and 95% for parameters TS, COD, N-NH4+ e P-PO43-, respectively. Residual sludge had the highest concentration of TS (49%), 83 days after the last cycle the filter. The average concentration of TS presented the residual sludge allowed to classify it as a solid hard. Keywords: septic tank sludge; sludge drying reed beds; treatment of septic sludge; biosolids.

Sludge drying reed beds: A key ecotechnology for a sustainable sanitation infrastructure in Brazil

2022 ◽  
pp. 129-159
Author(s):  
André Baxter Barreto ◽  
Gabriel Rodrigues Vasconcellos ◽  
Breno Henrique Leite Cota
Keyword(s):  
Reed Beds ◽  
Sludge Drying ◽  
Sanitation Infrastructure

scholarly journals Sludge drying reed beds: full- and pilot-scale study for activated sludge treatment

2009 ◽  
Vol 60 (5) ◽  
pp. 1145-1154 ◽  
Author(s):  
S. Troesch ◽  
A. Liénard ◽  
P. Molle ◽  
G. Merlin ◽  
D. Esser
Keyword(s):  
Dry Matter ◽  
Loading Rate ◽  
Rest Period ◽  
Matter Content ◽  
Full Scale ◽  
Dry Matter Content ◽  
Loading Frequency ◽  
Reed Beds ◽  
Hydraulic Behaviour ◽  
Sludge Drying

Sludge drying reed beds have been used for dewatering and mineralization of sludge since the beginning of the 90s, but their insufficient performances in terms of Dry Matter [DM] content and mineralization of the sludge have made necessary new studies. Therefore, 8 pilots of 2 m2 each and a full-scale plant (13,000 p.e, 8 beds of 470 m2 in operation for 4 years) have been monitored to examine the influence of the sludge loading rate, the sludge quality and the loading frequency on the dewatering and mineralization efficiencies. Two filtration layers and two loading rhythms were tested on pilots which were fed at a loading rate of 25–30 kg DM m−2 yr−1 during the first year of operation (commissioning period). Hydraulic behaviour (infiltration rate, outflow), O2 and CO2 relative concentrations in the filtration media, redox potential, pollutants removal and dry matter content were assessed during all the study. The rheological quality of the extracted sludge from full scale beds was assessed and showed that its mechanical behaviour exceed those of sludge of comparable dry matter content, making its spreading easier. Therefore, this sludge could easily claim the status of solid and stabilized sludge according to the French regulation. Design and management recommendations (number of beds, loading rates, feeding/rest period) gained from the experiments results are suggested.

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