Field test on a methane fermentation treatment system incorporating a membrane module for municipal sewage

Desalination ◽  
1994 ◽  
Vol 98 (1-3) ◽  
pp. 199-206 ◽  
Author(s):  
K. Kiriyama ◽  
Y. Tanaka ◽  
I. Mori
1992 ◽  
Vol 25 (7) ◽  
pp. 135-141 ◽  
Author(s):  
K. Kiriyama ◽  
Y. Tanaka ◽  
I. Mori

We examined a field test plant based on anaerobic sewage treatment to elucidate the process of methane fermentation with a UASB in municipal sewage and domestic waste water. The process consists of a pretreatment system for sparating suspended solids, a hydrolyzation reactor with a membrane module for organic solids, and a UASB reactor. The membrane module increases the sludge residence time in the hydrolyzation reactor. This field test plant is a commercial size system which combines these processes to verify the feasibility of the system. The aim of this practical test is to produce gas with a conversion rate of over 60% when the volumetric organic loading rate is more than 2 kg BOD/reactor m3.d, and to construct a methane gas generation system which generates the gas from raw sewage. This practical test demonstrated gas conversion rates from 57% to 60.0%. Volumetric organic loading rate was 1.4 - 2.0 kg BOD/m3.d; BOD removal was 70 - 80% at ambient temperature, and excess sludge did not exceed 0.04 kg per sewage.m3.


RADIOISOTOPES ◽  
2001 ◽  
Vol 50 (8) ◽  
pp. 343-352 ◽  
Author(s):  
Ayako NAKAMURA ◽  
Susumu OSAKI ◽  
Naofumi HAYABUCHI

2002 ◽  
Vol 45 (12) ◽  
pp. 103-112 ◽  
Author(s):  
N. Kataoka ◽  
T. Suzuki ◽  
K. Ishida ◽  
N. Yamada ◽  
N. Kurata ◽  
...  

A methane fermentation system for treating swine wastes was developed and successfully demonstrated in a field test plant (0.5 m3/d). The system was composed of a screw-press dehydrator, a methanogenic digester, a sludge separator, an oxidation ditch (OD) and composting equipment. A performance evaluation was carried out regarding physical pre-treatment using the screw-press dehydrator, methane fermentation for pre-treated slurry, and post-treatment for digested effluent by OD. Total solids (TS) and chemical oxygen demand (CODCr) removal by the screw-press pre-treatment were 38% and 22%, respectively. Properties of the screenings were as follows: water content 57%, ignition loss 93%, specific gravity 0.33. The pretreated strong slurry was digested under mesophilic conditions. Digestion gas (biogas) production rate was 25 m3/m3-slurry (NTP) and methane content of the biogas was 67%. CODCr removal of 65% with methane fermentation treatment of the slurry operating at 35°C was observed. No inhibition of methane fermentation reaction occurred at the NH4+-N concentration of 3,000 mg/l or less during methane fermentation by the system. Mass balance from the present pilot-scale study showed that 1m3 of mixture of excrement and urine of swine waste (TS 90 kg/m3) was biologically converted to 25 m3/m3-slurry (NTP) of biogas (methane content 67%), 100 kg of compost (water content 40%, ignition loss 75%), and 0.80 m3 of treated water (SS 30-70 mg/l).


1995 ◽  
Vol 31 (12) ◽  
pp. 55-65 ◽  
Author(s):  
F. B. Green ◽  
L. Bernstone ◽  
T. J. Lundquist ◽  
J. Muir ◽  
R. B. Tresan ◽  
...  

There are several basic reasons for concern regarding the fate of carbonaceous material in waste stabilization ponds: accumulation of solids; performance and useful life of the pond system; and, the control of methane emissions. In conventional ponds methane fermentation is minimal, and carbon-rich organic matter is integrated by bacteria and microalgae which grow and settle. The integration of carbon decreases pond volume and treatment capacity and causes the ponds to age prematurely, to produce odor, and to require frequent sludge removal; and, any methane produced escapes to the atmosphere. However, if carbon-rich organics are efficiently converted to methane or to harvested microalgae, the pond system will continue to treat wastewater effectively for an extended period of time. Advanced Integrated Wastewater Pond Systems (AIWPSs) developed at the University of California fully utilize methane fermentation and microalgal cultivation to treat wastewater and to reclaim energy and nutrients. First generation AIWPSs have provided reliable municipal sewage treatment at St. Helena and Hollister, California, for 28 and 16 years, respectively, without the need for sludge removal. However, these first generation systems lack the facilities to recover and utilize the carbon-rich treatment byproducts of methane and algal biomass. The recovery of methane using a submerged gas collector was demonstrated using a second generation AIWPS prototype at the University of California, Berkeley, and the optimization of in-pond methane fermentation, the growth of microalgae in High Rate Ponds, and the harvest of microalgae by sedimentation and dissolved air flotation were studied. Preliminary data are presented to quantify the fate of carbon in the second generation AIWPS prototype and to estimate the fate of carbon in a full-scale, 200 MLD second generation AIWPS treating municipal sewage. In the experimental system, 17% of the influent organic carbon was recovered as methane, and an average of 6 g C/m2/d were assimilated into harvestable algal biomass. In a full-scale second generation AIWPS in a climate comparable to Richmond, California, located at 37° N latitude, these values would be significantly higher--as much as 30% of the influent organic carbon would be recovered as methane and as much as 10 g C/m2/d would be assimilated by microalgae. These efficiencies would increase further in warmer climates with more abundant sunlight.


2006 ◽  
Vol 53 (3) ◽  
pp. 209-218 ◽  
Author(s):  
M. Tandukar ◽  
S. Uemura ◽  
A. Ohashi ◽  
H. Harada

A “fourth generation” down-flow hanging sponge (DHS) Reactor has been developed and proposed as an improved variant of post-treatment system for UASB treating domestic wastewater. This paper evaluates the potential of the proposed combination of UASB and DHS as a sewage treatment system, especially for developing countries. A pilot-scale UASB (1.15 m3) and DHS (0.38 m3; volume of sponge) was installed in a municipal sewage treatment site and constantly monitored for 2 years. UASB was operated at an HRT of 6 h corresponding to an organic load of 2.15 kg-COD/m3 per day. Subsequently, the organic load in DHS was 2.35 kg-COD/m3 per day, operated at an HRT of 2 h. Organic removal by the whole system was satisfactory, accomplishing 96% of unfiltered BOD removal and 91% of unfiltered COD removal. However, nitrification decreased from 56% during the startup period to 28% afterwards. Investigation on DHS sludge was made by quantifying it and evaluating oxygen uptake rates with various substrates. Average concentration of trapped biomass was 26 g-VSS/L of sponge volume, increasing the SRT of the system to 100–125 d. Removal of coliforms obtained was 3–4 log10 with the final count of 103 to 104 MPN/100 ml in DHS effluent.


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