Anaerobic co-digestion of three organic wastes under mesophilic conditions: lab-scale and pilot-scale studies

2020 ◽  
Author(s):  
Lamis Yousra Shahrazed Khelifa Zouaghi ◽  
Hayet Djelal ◽  
Zineb Salem
Keyword(s):  
Pilot Scale ◽  
Organic Wastes ◽  
Mesophilic Conditions

Comparison of microbial communities in pilot-scale bioreactors treating Bayer liquor organic wastes

2010 ◽  
Vol 22 (2) ◽  
pp. 397-407 ◽  
Author(s):  
Naomi J. McSweeney ◽  
Jason J. Plumb ◽  
Amanda L. Tilbury ◽  
Hugh J. Nyeboer ◽  
Matt E. Sumich ◽  
...  
Keyword(s):  
Microbial Communities ◽  
Pilot Scale ◽  
Organic Wastes ◽  
Bayer Liquor

The modar process for the destruction of hazardous organic wastes—Field test of a pilot-scale unit

1989 ◽  
Vol 9 (1) ◽  
pp. 19-26 ◽  
Author(s):  
Kathleen C. Swallow ◽  
William R. Killilea ◽  
Kenneth C. Malinowski ◽  
Carl N. Staszak
Keyword(s):  
Field Test ◽  
Pilot Scale ◽  
Organic Wastes ◽  
Scale Unit

Landfarming in the Treatment by Cetrel of Organic Wastes from a Petrochemical Complex – Design, Operation and Results

1987 ◽  
Vol 19 (8) ◽  
pp. 63-74
Author(s):  
J. O. Alves ◽  
M. C. M. Valente ◽  
M. A. P. Simões ◽  
M. G. Santos
Keyword(s):  
Learning Process ◽  
Pilot Scale ◽  
Organic Wastes ◽  
Industrial Wastes ◽  
Continuous Learning ◽  
Petrochemical Complex ◽  
Complex Design ◽  
Operation Control ◽  
In The Beginning

In the beginning of 1983, CETREL S/A, based on the experiments carried out in other countries, put forth the idea of treating organic industrial wastes generated by COPEC, especially atoxic biodegradable sludges, through LANDFARMING. Therefore, in 1984 two “Farms” were implemented, in an area of 20 hectares. In view of the pioneering ventures in Brazil for the disposal of industrial wastes of various sources, operation controls have been and still are a continuous learning process, stimulating research on the insertion or adaptation of governing parameters in the process. In that connection, it is our intention to show the characteristics and procedures adopted with regard to Design, Operation, Control/Monitoring, Pilot Scale Tests and Results.

scholarly journals Characterization of Polyhydroxyalkanoates Produced at Pilot Scale From Different Organic Wastes

2021 ◽  
Vol 9 ◽  
Author(s):  
Laura Lorini ◽  
Andrea Martinelli ◽  
Giorgio Capuani ◽  
Nicola Frison ◽  
Maria Reis ◽  
...  
Keyword(s):  
Organic Waste ◽  
Pilot Scale ◽  
Organic Wastes ◽  
Organic Fraction ◽  
Waste Streams ◽  
Primary Sludge ◽  
Molecular Weights ◽  
North East ◽  
Mixed Microbial Cultures

Polyhydroxyalkanoates (PHAs) production at pilot scale has been recently investigated and carried out exploiting different process configurations and organic wastes. More in detail, three pilot platforms, in Treviso (North-East of Italy), Carbonera (North-East of Italy) and Lisbon, produced PHAs by open mixed microbial cultures (MMCs) and different organic waste streams: organic fraction of municipal solid waste and sewage sludge (OFMSW-WAS), cellulosic primary sludge (CPS), and fruit waste (FW), respectively. In this context, two stabilization methods have been applied, and compared, for preserving the amount of PHA inside the cells: thermal drying and wet acidification of the biomass at the end of PHA accumulation process. Afterward, polymer has been extracted following an optimized method based on aqueous-phase inorganic reagents. Several PHA samples were then characterized to determine PHA purity, chemical composition, molecular weight, and thermal properties. The polymer contained two types of monomers, namely 3-hydroxybutyrate (3HB) and 3-hydroxyvalerate (3HV) at a relative percentage of 92.6–79.8 and 7.4–20.2 w/w, respectively, for Treviso and Lisbon plants. On the other hand, an opposite range was found for 3HB and 3HV monomers of PHA from Carbonera, which is 44.0–13.0 and 56.0–87.0 w/w, respectively. PHA extracted from wet-acidified biomass had generally higher viscosity average molecular weights (Mv) (on average 424.8 ± 20.6 and 224.9 ± 21.9 KDa, respectively, for Treviso and Lisbon) while PHA recovered from thermally stabilized dried biomass had a three-fold lower Mv.

scholarly journals Co-composting of chicken manure with organic wastes: characterization of gases emissions and compost quality

2020 ◽  
Vol 63 (1) ◽  
Author(s):  
Hyun Young Hwang ◽  
Seong Heon Kim ◽  
Myung Sook Kim ◽  
Seong Jin Park ◽  
Chang Hoon Lee
Keyword(s):  
Swine Manure ◽  
Pilot Scale ◽  
Organic Wastes ◽  
Chicken Manure ◽  
Plant Residues ◽  
Cow Manure ◽  
Compost Quality ◽  
Carbon And Nitrogen ◽  
Selection For

AbstractCo-composting of organic wastes is globally recognized to be effective method to dispose two or more wastes at once and minimize drawbacks of composting such as gases emissions and nutrient reduction. In this study, pilot-scale experiments were conducted to characterize the co-composting process of chicken manure with cow manure (CC), swine manure (CS), plant residues plus mushroom media (CRM), on emissions of greenhouse gas, and ammonia, compost quality, maturity and their correlations. The results showed that cumulative flux of carbon dioxide (CO2), methane (CH4), nitrous oxide (N2O) and ammonia (NH3) widely ranged like 38,211–50,830, 172–417, 98–142 and 118–927 g kg dm−1 day−1 respectively. It indicated the importance of selection for co-composting material. The NH3 emission was significantly increased by 4.3–7.9 times in CS and CRM, compared to OC and CC. Both of CS and CRM also showed longer thermophilic phase and later maturation were also observed in both treatments. Temperature was positively correlated with gases (P < 0.001) except CH4, and nitrogen content, C/N ratio and nitrate nitrogen significantly affected emission of carbon and nitrogen (P < 0.001). In conclusion, for chicken manure composting, sole chicken manure or combination with cow manure could be suitable composting method to improve compost quality and minimize gases losses.

Upscaling of foam forming technology for pilot scale

TAPPI Journal ◽  
2019 ◽  
Vol 18 (8) ◽  
Author(s):  
JANI LEHMONEN ◽  
TIMO RANTANEN ◽  
KARITA KINNUNEN-RAUDASKOSKI
Keyword(s):  
Production Efficiency ◽  
Strength Loss ◽  
Pilot Scale ◽  
Foam Density ◽  
Forming Process ◽  
Production Scale ◽  
Forming Technology ◽  
Wet Pressing ◽  
Foam Forming ◽  
Board Industry

The need for production cost savings and changes in the global paper and board industry during recent years have been constants. Changes in the global paper and board industry during past years have increased the need for more cost-efficient processes and production technologies. It is known that in paper and board production, foam typically leads to problems in the process rather than improvements in production efficiency. Foam forming technology, where foam is used as a carrier phase and a flowing medium, exploits the properties of dispersive foam. In this study, the possibility of applying foam forming technology to paper applications was investigated using a pilot scale paper forming environment modified for foam forming from conventional water forming. According to the results, the shape of jet-to-wire ratios was the same in both forming methods, but in the case of foam forming, the achieved scale of jet-to-wire ratio and MD/CD-ratio were wider and not behaving sensitively to shear changes in the forming section as a water forming process would. This kind of behavior would be beneficial when upscaling foam technology to the production scale. The dryness results after the forming section indicated the improvement in dewatering, especially when foam density was at the lowest level (i.e., air content was at the highest level). In addition, the dryness results after the pressing section indicated a faster increase in the dryness level as a function of foam density, with all density levels compared to the corresponding water formed sheets. According to the study, the bonding level of water- and foam-laid structures were at the same level when the highest wet pressing value was applied. The results of the study show that the strength loss often associated with foam forming can be compensated for successfully through wet pressing.

Application of a Pilot-Scale Pulsed Electrocoagulation system to OCC-Based Paper Mill Effluent

TAPPI Journal ◽  
2009 ◽  
Vol 8 (3) ◽  
pp. 14-20 ◽  
Author(s):  
YUAN-SHING PERNG ◽  
EUGENE I-CHEN WANG ◽  
SHIH-TSUNG YU ◽  
AN-YI CHANG
Keyword(s):  
Water Quality ◽  
Quality Indicators ◽  
Paper Mill ◽  
Pilot Scale ◽  
Operating Conditions ◽  
Optimal Dosage ◽  
Water Quality Indicators ◽  
Paper Mill Effluent ◽  
Treated Effluent ◽  
True Color

Trends toward closure of white water recirculation loops in papermaking often lead to a need for system modifications. We conducted a pilot-scale study using pulsed electrocoagulation technology to treat the effluent of an old corrugated containerboard (OCC)-based paper mill in order to evaluate its treatment performance. The operating variables were a current density of 0–240 A/m2, a hydraulic retention time (HRT) of 8–16 min, and a coagulant (anionic polyacrylamide) dosage of 0–22 mg/L. Water quality indicators investigated were electrical con-ductivity, suspended solids (SS), chemical oxygen demand (COD), and true color. The results were encouraging. Under the operating conditions without coagulant addition, the highest removals for conductivity, SS, COD, and true color were 39.8%, 85.7%, 70.5%, and 97.1%, respectively (with an HRT of 16 min). The use of a coagulant enhanced the removal of both conductivity and COD. With an optimal dosage of 20 mg/L and a shortened HRT of 10 min, the highest removal achieved for the four water quality indicators were 37.7%, 88.7%, 74.2%, and 91.7%, respectively. The water qualities thus attained should be adequate to allow reuse of a substantial portion of the treated effluent as process water makeup in papermaking.

Pilot-scale combustion studies with kraft lignin in a powder burner and a CFB boiler

TAPPI Journal ◽  
2010 ◽  
Vol 9 (6) ◽  
pp. 24-30 ◽  
Author(s):  
NIKLAS BERGLIN ◽  
PER TOMANI ◽  
HASSAN SALMAN ◽  
SOLVIE HERSTAD SVÄRD ◽  
LARS-ERIK ÅMAND
Keyword(s):  
Circulating Fluidized Bed ◽  
Black Liquor ◽  
Chloride Content ◽  
Pilot Scale ◽  
High Energy ◽  
Kraft Lignin ◽  
High Energy Density ◽  
Alkali Chloride ◽  
Cfb Boiler ◽  
Solid Biofuel

Processes have been developed to produce a solid biofuel with high energy density and low ash content from kraft lignin precipitated from black liquor. Pilot-scale tests of the lignin biofuel were carried out with a 150 kW powder burner and a 12 MW circulating fluidized bed (CFB) boiler. Lignin powder could be fired in a powder burner with good combustion performance after some trimming of the air flows to reduce swirl. Lignin dried to 10% moisture content was easy to feed smoothly and had less bridging tendencies in the feeding system than did wood/bark powder. In the CFB boiler, lignin was easily handled and cofired together with bark. Although the filter cake was broken into smaller pieces and fines, the combustion was not disturbed. When cofiring lignin with bark, the sulfur emission increased compared with bark firing only, but most of the sulfur was captured by calcium in the bark ash. Conventional sulfur capture also occurred with addition of limestone to the bed. The sulfur content in the lignin had a significantly positive effect on reducing the alkali chloride content in the deposits, thus reducing the high temperature corrosion risk.

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