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Section 11. FOOD WASTES HYBRID BIOLIQUEFACTION AND BIOGASIFICATION FOR PAPAYA PROCESSING WASTES IN THE TROPICS P. Y. Yang, Professor C. Y. Chou, Graduate Research Assistant Agricultural Engineering Department University of Hawaii at Manoa Honolulu, Hawaii 96822 INTRODUCTION Anaerobic fermentation of fruit processing wastes holds potential for producing alternative energy in addition to reducing the pollution problems. The biogas (50-70% of methane) produced from the anaerobic fermentation of fruit processing wastes could have been used in equipment designed for natural gas fuel with no or only minor purification. In order to utilize this potential, the anaerobic fermentation of papaya processing wastes was preliminarily studied and reported in Hawaii [1,2]. It has been indicated that the biogasification of papaya processing wastes for pollution control and energy utilization is feasible. Also, the biogasification process with sludge recycling permits smaller reactor volume without any deterioration of methane production rate and methane content. However, the water addition (about 10 times that of raw papaya wastes) for preparation of slurry prior to methane fermentation is considered as the main weakness. This is not appropriate because of more problems of possible post-treatment or handling of diluted-digested papaya processing wastewater. Although solid state fermentation has been studied for methane production from organic wastes with high solid content [3,4], it requires very long retention time in order to stabilize the organic wastes. Koster [5] investigated the liquefaction and acidogenesis of tomato solid wastes and suggested that recirculation of the effluent from the methane reactor and addition of water should be considered in order to stimulate liquefaction. Combined liquefaction and gasification treatment of organic residues were investigated with various solid agricultural and industrial organic residues including straw, grass, cabbage leaves, waste-onions, sugar-beet pulp, cannery wastes, tomato-plant wastes, municipal solid wastes, etc. [5-10]. This combined system offers a significant advantage by eliminating the post- handling and treatment of the digested effluent and is free of the drawbacks of the dry anaerobic fermentation (i.e., requirement of a long reaction time to stabilize the organic residues). However, they are complicated in both structure and operation. Additionally, the detailed design and operational criteria for the system have not been established yet. Further study is needed to develop a system which is efficient and simple in construction and operation with detailed design and operational criteria. MATERIALS AND METHODS Feedstock Preparation The papaya processing wastes used in this study were collected from a fruit processing plant in Honolulu, the Aloha Produce Corporation. The waste was transported to the Agricultural Engineering Department of the University of Hawaii and was stored in a freezer unit before needed for experiments. It was withdrawn to defrost for two hours before use. Experimental Set-up The hybrid bioliquefaction and biogasification system consisted of an 8-liter bioliquefaction unit and a 20-liter biogasification unit (Figure 1). This system was tested in a walk-in incubation room at 30 ± 1 C. The bioliquefaction unit (Reactor 1), shown in Figure 2, was an acrylic plastic column with a grease-sealed cover and a sieve plate on the bottom. The biogasification unit (Reactor 2), 267
Object Description
Purdue Identification Number | ETRIWC198527 |
Title | Hybrid bioliquefaction and biogasification for papaya processing wastes in the tropics |
Author |
Yang, P. Y. (Ping-Yi) Chou, C. Y. |
Date of Original | 1985 |
Conference Title | Proceedings of the 40th Industrial Waste Conference |
Conference Front Matter (copy and paste) | http://e-archives.lib.purdue.edu/u?/engext,36131 |
Extent of Original | p. 267-278 |
Collection Title | Engineering Technical Reports Collection, Purdue University |
Repository | Purdue University Libraries |
Rights Statement | Digital object copyright Purdue University. All rights reserved. |
Language | eng |
Type (DCMI) | text |
Format | JP2 |
Date Digitized | 2009-07-14 |
Capture Device | Fujitsu fi-5650C |
Capture Details | ScandAll 21 |
Resolution | 300 ppi |
Color Depth | 8 bit |
Description
Title | page 267 |
Collection Title | Engineering Technical Reports Collection, Purdue University |
Repository | Purdue University Libraries |
Rights Statement | Digital copyright Purdue University. All rights reserved. |
Language | eng |
Type (DCMI) | text |
Format | JP2 |
Capture Device | Fujitsu fi-5650C |
Capture Details | ScandAll 21 |
Transcript | Section 11. FOOD WASTES HYBRID BIOLIQUEFACTION AND BIOGASIFICATION FOR PAPAYA PROCESSING WASTES IN THE TROPICS P. Y. Yang, Professor C. Y. Chou, Graduate Research Assistant Agricultural Engineering Department University of Hawaii at Manoa Honolulu, Hawaii 96822 INTRODUCTION Anaerobic fermentation of fruit processing wastes holds potential for producing alternative energy in addition to reducing the pollution problems. The biogas (50-70% of methane) produced from the anaerobic fermentation of fruit processing wastes could have been used in equipment designed for natural gas fuel with no or only minor purification. In order to utilize this potential, the anaerobic fermentation of papaya processing wastes was preliminarily studied and reported in Hawaii [1,2]. It has been indicated that the biogasification of papaya processing wastes for pollution control and energy utilization is feasible. Also, the biogasification process with sludge recycling permits smaller reactor volume without any deterioration of methane production rate and methane content. However, the water addition (about 10 times that of raw papaya wastes) for preparation of slurry prior to methane fermentation is considered as the main weakness. This is not appropriate because of more problems of possible post-treatment or handling of diluted-digested papaya processing wastewater. Although solid state fermentation has been studied for methane production from organic wastes with high solid content [3,4], it requires very long retention time in order to stabilize the organic wastes. Koster [5] investigated the liquefaction and acidogenesis of tomato solid wastes and suggested that recirculation of the effluent from the methane reactor and addition of water should be considered in order to stimulate liquefaction. Combined liquefaction and gasification treatment of organic residues were investigated with various solid agricultural and industrial organic residues including straw, grass, cabbage leaves, waste-onions, sugar-beet pulp, cannery wastes, tomato-plant wastes, municipal solid wastes, etc. [5-10]. This combined system offers a significant advantage by eliminating the post- handling and treatment of the digested effluent and is free of the drawbacks of the dry anaerobic fermentation (i.e., requirement of a long reaction time to stabilize the organic residues). However, they are complicated in both structure and operation. Additionally, the detailed design and operational criteria for the system have not been established yet. Further study is needed to develop a system which is efficient and simple in construction and operation with detailed design and operational criteria. MATERIALS AND METHODS Feedstock Preparation The papaya processing wastes used in this study were collected from a fruit processing plant in Honolulu, the Aloha Produce Corporation. The waste was transported to the Agricultural Engineering Department of the University of Hawaii and was stored in a freezer unit before needed for experiments. It was withdrawn to defrost for two hours before use. Experimental Set-up The hybrid bioliquefaction and biogasification system consisted of an 8-liter bioliquefaction unit and a 20-liter biogasification unit (Figure 1). This system was tested in a walk-in incubation room at 30 ± 1 C. The bioliquefaction unit (Reactor 1), shown in Figure 2, was an acrylic plastic column with a grease-sealed cover and a sieve plate on the bottom. The biogasification unit (Reactor 2), 267 |
Resolution | 300 ppi |
Color Depth | 8 bit |
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