Pub Date : 1990-01-01DOI: 10.1016/0144-4565(90)90076-V
J.Q. Yan, K.V. Lo, P.H. Liao
Anaerobic treatment of cheese whey using a 17·5 litre upflow anaerobic sludge blanket reactor was investigated in the laboratory over a range of influent concentration from 4·5 to 38·1 g COD litre−1 at a constant hydraulic retention time of 5 days. The results indicated that two sludge distribution regions, a sludge bed and a sludge blanket, as well as two distinct reaction phases, acidogenic and methanogenic, were formed. However, as the substrate loading was increased, the acidogenic region extended into the methanogenic region in the upper portion of the reactor until the whole region was acidogenic, leading to the failure of the reactor.
在实验室研究了17.5升上流式厌氧污泥毯式反应器对奶酪乳清的厌氧处理,进水浓度为4.5至38.1 g COD升- 1,水力保持时间为5天。结果表明:污泥床和污泥毯两个污泥分布区,形成了不同的产酸和产甲烷反应相。但随着底物负荷的增加,反应器上部的产酸区向产甲烷区延伸,直至整个区域发生产酸,导致反应器失效。
{"title":"Anaerobic digestion of cheese whey using an upflow anaerobic sludge blanket reactor: III. Sludge and substrate profiles","authors":"J.Q. Yan, K.V. Lo, P.H. Liao","doi":"10.1016/0144-4565(90)90076-V","DOIUrl":"10.1016/0144-4565(90)90076-V","url":null,"abstract":"<div><p>Anaerobic treatment of cheese whey using a 17·5 litre upflow anaerobic sludge blanket reactor was investigated in the laboratory over a range of influent concentration from 4·5 to 38·1 g COD litre<sup>−1</sup> at a constant hydraulic retention time of 5 days. The results indicated that two sludge distribution regions, a sludge bed and a sludge blanket, as well as two distinct reaction phases, acidogenic and methanogenic, were formed. However, as the substrate loading was increased, the acidogenic region extended into the methanogenic region in the upper portion of the reactor until the whole region was acidogenic, leading to the failure of the reactor.</p></div>","PeriodicalId":100179,"journal":{"name":"Biomass","volume":"21 4","pages":"Pages 257-271"},"PeriodicalIF":0.0,"publicationDate":"1990-01-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://sci-hub-pdf.com/10.1016/0144-4565(90)90076-V","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"81549286","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 1990-01-01DOI: 10.1016/0144-4565(90)90065-R
K.V. Lo, P.H. Liao
The anaerobic treatment of baker's yeast wastewater was studied using an anaerobic biological contact reactor (AnRBC) and a fixed-film reactor. The AnRBC had an active biomass developed within the reactor before this study commenced; however, the fixed-film reactor was started without attached biomass in a support structure. The gas production rates obtained for the AnRBC were between 0·55 and 0·61 litre methane per litre reactor per day. However, a gas production rate of only 0·46 litre methane per litre reactor per day was achieved after a four-month operating period for the fixed-film reactor. Higher chemical oxygen demand reduction was also found in the AnRBC. The results indicated that the presence of high sulfate concentration in baker's yeast wastewater affected teh start-up process. The reactor with fully developed active biomass was less susceptible to sulfate inhibition and showed improved anaerobic digestion. Results indicate that the reactor should be innoculated by feeding nutrient-balanced substrate before it was subjected to the digestion of baker's yeast wastewater. The fixed-film reactor was also fed with the substrate contianing sodium molybdate, an inhibitor of sulfate-reducing bacteria. The results indicated that both methanogenic and sulfate-reducing bacteria were inhibited.
{"title":"Anaerobic treatment of baker's yeast wastewater: I. Start-up and sodium molybdate addition","authors":"K.V. Lo, P.H. Liao","doi":"10.1016/0144-4565(90)90065-R","DOIUrl":"10.1016/0144-4565(90)90065-R","url":null,"abstract":"<div><p>The anaerobic treatment of baker's yeast wastewater was studied using an anaerobic biological contact reactor (AnRBC) and a fixed-film reactor. The AnRBC had an active biomass developed within the reactor before this study commenced; however, the fixed-film reactor was started without attached biomass in a support structure. The gas production rates obtained for the AnRBC were between 0·55 and 0·61 litre methane per litre reactor per day. However, a gas production rate of only 0·46 litre methane per litre reactor per day was achieved after a four-month operating period for the fixed-film reactor. Higher chemical oxygen demand reduction was also found in the AnRBC. The results indicated that the presence of high sulfate concentration in baker's yeast wastewater affected teh start-up process. The reactor with fully developed active biomass was less susceptible to sulfate inhibition and showed improved anaerobic digestion. Results indicate that the reactor should be innoculated by feeding nutrient-balanced substrate before it was subjected to the digestion of baker's yeast wastewater. The fixed-film reactor was also fed with the substrate contianing sodium molybdate, an inhibitor of sulfate-reducing bacteria. The results indicated that both methanogenic and sulfate-reducing bacteria were inhibited.</p></div>","PeriodicalId":100179,"journal":{"name":"Biomass","volume":"21 3","pages":"Pages 207-218"},"PeriodicalIF":0.0,"publicationDate":"1990-01-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://sci-hub-pdf.com/10.1016/0144-4565(90)90065-R","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"76334554","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 1990-01-01DOI: 10.1016/0144-4565(90)90021-B
D.C. Elliott , E.G. Baker , D. Beckman , Y. Solantausta , V. Tolenhiemo , S.B. Gevert , C. Hörnell , A. Östman , B. Kjellström
This paper discusses the results of a technoeconomic assessment of direct biomass liquefaction processes converting wood to gasoline and diesel fuels. The study was carried out by the Working Group of the International Energy Agency Direct Biomass Liquefaction Activity, in which Canada, Finland, Sweden, and the US participated. The processes chosen for detailed analysis were Atmospheric Flash Pyrolysis (AFP) and Liquefaction In Pressurized Solvent (LIPS). The assessment covered three steps for each process from feed to final product:
1.
1. primary liquefaction to a crude oil product,
2.
2. catalytic hydrotreating to upgrade the crude product to a deoxygenated product oil,
3.
3. refining the deoxygenated product to gasoline and diesel fuel.
Present technology cases and potential future technology cases were evaluated. A consistent analytical basis was used throughout to allow comparison of the processes. This assessment shows that AFP is more economical than LIPS both for the production of boiler fuel oil as the primary liquefaction product and for the production of gasoline and diesel fuel products. The potential for future cost reduction through research and development is also clearly demonstrated.
{"title":"Technoeconomic assessment of direct biomass liquefaction to transportation fuels","authors":"D.C. Elliott , E.G. Baker , D. Beckman , Y. Solantausta , V. Tolenhiemo , S.B. Gevert , C. Hörnell , A. Östman , B. Kjellström","doi":"10.1016/0144-4565(90)90021-B","DOIUrl":"10.1016/0144-4565(90)90021-B","url":null,"abstract":"<div><p>This paper discusses the results of a technoeconomic assessment of direct biomass liquefaction processes converting wood to gasoline and diesel fuels. The study was carried out by the Working Group of the International Energy Agency Direct Biomass Liquefaction Activity, in which Canada, Finland, Sweden, and the US participated. The processes chosen for detailed analysis were Atmospheric Flash Pyrolysis (AFP) and Liquefaction In Pressurized Solvent (LIPS). The assessment covered three steps for each process from feed to final product: </p><ul><li><span>1.</span><span><p>1. primary liquefaction to a crude oil product,</p></span></li><li><span>2.</span><span><p>2. catalytic hydrotreating to upgrade the crude product to a deoxygenated product oil,</p></span></li><li><span>3.</span><span><p>3. refining the deoxygenated product to gasoline and diesel fuel.</p></span></li></ul><p>Present technology cases and potential future technology cases were evaluated. A consistent analytical basis was used throughout to allow comparison of the processes. This assessment shows that AFP is more economical than LIPS both for the production of boiler fuel oil as the primary liquefaction product and for the production of gasoline and diesel fuel products. The potential for future cost reduction through research and development is also clearly demonstrated.</p></div>","PeriodicalId":100179,"journal":{"name":"Biomass","volume":"22 1","pages":"Pages 251-269"},"PeriodicalIF":0.0,"publicationDate":"1990-01-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://sci-hub-pdf.com/10.1016/0144-4565(90)90021-B","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"86738232","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 1990-01-01DOI: 10.1016/0144-4565(90)90039-M
A.N. Pereira, K.L. Kohlmann, M.R. Ladishh
The analysis of water-soluble cellodextrins using liquid chromatography is readily achieved with a variety of packings. Direct injection of enzyme incubation mixtures allows quantitation of 10 mM cellodextrins in hydrolysis mixtures, resulting in a method which is useful for kinetic studies. Reported here are operating procedures for a 4% cross-linked, styrene-divinyl benzene cation exchanger (Aminex 50W-X4 (Bio Rad Lab., Griffin, CA, USA), 20–30 μm particle size) in the Ca++ form, packed in a column of dimensions 6 mm i.d. × 60 cm long. Using this column, resolution of the cellodextrins, celloheptaose through cellobiose and glucose was possible with 91 mM H2SO4 as the eluent. Requirements of the separation system included use of a pulsation free syringe pump to minimize baseline fluctuations, the use of Ca++ as the counterion to give a column operational life of 500–1000 injections, and injection of sample volumes of up to 25 μL. cellodextrins were quantified at sub-microgram (nmole) levels using a differential refractometer as the detector. Examples of this technique for analysis of the acid hydrolysis of cellodextrins and enzymatic hydrolysis of cellodextrins and carboxymethylcellulose are described.
用液相色谱法分析水溶性纤维素糊精可以很容易地用各种填料实现。直接注射酶孵育混合物允许在水解混合物中定量10mm的纤维素糊精,从而产生一种对动力学研究有用的方法。本文报告了4%交联苯乙烯-二乙烯基苯阳离子交换剂(Aminex 50W-X4)的操作程序。(Griffin, CA, USA),粒径20-30 μm),以CA ++形式存在,包装在尺寸为6mm直径× 60cm长的柱中。采用该柱,以91 mM H2SO4为洗脱液,纤维素糊精、纤维素七糖可通过纤维素二糖和葡萄糖分离。分离系统的要求包括:使用无脉动注射泵以减少基线波动,使用Ca++作为反离子使色谱柱的使用寿命为500-1000次,进样量为25 μL。用差示折射计作为检测器,定量测定了纤维素糊精的亚微克(nmol)水平。描述了该技术用于分析纤维素糊精的酸水解和纤维素糊精和羧甲基纤维素的酶水解的实例。
{"title":"Analysis of sub-microgram quantities of cellodextrins by aqueous liquid chromatography using a differential refractometer","authors":"A.N. Pereira, K.L. Kohlmann, M.R. Ladishh","doi":"10.1016/0144-4565(90)90039-M","DOIUrl":"10.1016/0144-4565(90)90039-M","url":null,"abstract":"<div><p>The analysis of water-soluble cellodextrins using liquid chromatography is readily achieved with a variety of packings. Direct injection of enzyme incubation mixtures allows quantitation of 10 m<span>M</span> cellodextrins in hydrolysis mixtures, resulting in a method which is useful for kinetic studies. Reported here are operating procedures for a 4% cross-linked, styrene-divinyl benzene cation exchanger (Aminex 50W-X4 (Bio Rad Lab., Griffin, CA, USA), 20–30 μm particle size) in the Ca<sup>++</sup> form, packed in a column of dimensions 6 mm i.d. × 60 cm long. Using this column, resolution of the cellodextrins, celloheptaose through cellobiose and glucose was possible with 91 m<span>M</span> H<sub>2</sub>SO<sub>4</sub> as the eluent. Requirements of the separation system included use of a pulsation free syringe pump to minimize baseline fluctuations, the use of Ca<sup>++</sup> as the counterion to give a column operational life of 500–1000 injections, and injection of sample volumes of up to 25 μL. cellodextrins were quantified at sub-microgram (nmole) levels using a differential refractometer as the detector. Examples of this technique for analysis of the acid hydrolysis of cellodextrins and enzymatic hydrolysis of cellodextrins and carboxymethylcellulose are described.</p></div>","PeriodicalId":100179,"journal":{"name":"Biomass","volume":"23 4","pages":"Pages 307-317"},"PeriodicalIF":0.0,"publicationDate":"1990-01-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://sci-hub-pdf.com/10.1016/0144-4565(90)90039-M","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"81937367","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 1990-01-01DOI: 10.1016/0144-4565(90)90011-8
Nels S. Christopherson, James A. Mattson
The International Energy Agency (IEA) has recognized the importance of the proper use of current technologies in researching the concept of biomass as a renewable energy source. An early program included one project that dealt entirely with the mechanization of harvesting trees grown under short-rotation intensive culture (SRIC) forestry. The Bioenergy Agreement that ended 31 December 1988 expanded this involvement with mechanization by creating a separate Activity called ‘Production Technology’. This Activity investigated the current state of technology for establishing, managing and harvesting SRIC forests or plantations. Five countries participated: Canada, Denmark, Sweden, the UK, and the US. Several workshops were held, and a final joint project evolved. As the final effort, a ‘Sourcebook’ of Production Technology will be made available. A summary of the main findings is provided here. This document will be published by the IEA and updated in future years as needed.
{"title":"Mechanization of the operational aspects of short-rotation forestry","authors":"Nels S. Christopherson, James A. Mattson","doi":"10.1016/0144-4565(90)90011-8","DOIUrl":"10.1016/0144-4565(90)90011-8","url":null,"abstract":"<div><p>The International Energy Agency (IEA) has recognized the importance of the proper use of current technologies in researching the concept of biomass as a renewable energy source. An early program included one project that dealt entirely with the mechanization of harvesting trees grown under short-rotation intensive culture (SRIC) forestry. The Bioenergy Agreement that ended 31 December 1988 expanded this involvement with mechanization by creating a separate Activity called ‘Production Technology’. This Activity investigated the current state of technology for establishing, managing and harvesting SRIC forests or plantations. Five countries participated: Canada, Denmark, Sweden, the UK, and the US. Several workshops were held, and a final joint project evolved. As the final effort, a ‘Sourcebook’ of Production Technology will be made available. A summary of the main findings is provided here. This document will be published by the IEA and updated in future years as needed.</p></div>","PeriodicalId":100179,"journal":{"name":"Biomass","volume":"22 1","pages":"Pages 123-133"},"PeriodicalIF":0.0,"publicationDate":"1990-01-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://sci-hub-pdf.com/10.1016/0144-4565(90)90011-8","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"91143844","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 1990-01-01DOI: 10.1016/0144-4565(90)90027-H
Thomas A. Milne
The endeavors of the 1986–88 International Energy Agency activity on ‘Voluntary Standards’ are discussed and summarized. The goal of the work is to facilitate the intercomparison of research and technology results from different laboratories and countries. Three major activities are underway: (1) the carrying out of selected interlaboratory comparisons in biochemical and thermochemical conversion and in feedstock analysis; (2) the establishment of standard reference materials from both woody and herbaceous species; and (3) the assembly of a ‘Sourcebook of Methods of Analysis for Biomass for Fuels and Chemicals’. Progress on these three elements is summarized and contacts given for those wishing to participate in this activity.
{"title":"Voluntary standards for biomass for fuels and chemicals","authors":"Thomas A. Milne","doi":"10.1016/0144-4565(90)90027-H","DOIUrl":"10.1016/0144-4565(90)90027-H","url":null,"abstract":"<div><p>The endeavors of the 1986–88 International Energy Agency activity on ‘Voluntary Standards’ are discussed and summarized. The goal of the work is to facilitate the intercomparison of research and technology results from different laboratories and countries. Three major activities are underway: (1) the carrying out of selected interlaboratory comparisons in biochemical and thermochemical conversion and in feedstock analysis; (2) the establishment of standard reference materials from both woody and herbaceous species; and (3) the assembly of a ‘Sourcebook of Methods of Analysis for Biomass for Fuels and Chemicals’. Progress on these three elements is summarized and contacts given for those wishing to participate in this activity.</p></div>","PeriodicalId":100179,"journal":{"name":"Biomass","volume":"22 1","pages":"Pages 343-351"},"PeriodicalIF":0.0,"publicationDate":"1990-01-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://sci-hub-pdf.com/10.1016/0144-4565(90)90027-H","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"83930161","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 1990-01-01DOI: 10.1016/0144-4565(90)90032-F
Mária Mikulášová , Štefan Vodný , Alexandra Pekarovičová
The effect of some lignin degradation products, which can be present in wood hydrolysates, on biomass production by Candida sp. was studied. Suspected inhibitors were used as supplements in growth media for C. utilis and C. albicans containing pure glucose as a carbon energy source. The metabolism of inhibitors by C. utilis and C. albicans is approximately the same and is extremely sensitive to the structure and concentration of the phenolic additive. ID50 and ID100 values for a 50% or a 100% growth inhibition for 20 lignin monomer model compounds during Candida sp. cultivation were established. Comparison of ID values has shown that the least toxic compounds for C. utilis and C. albicans biomass growth and yield are vanillyl alcohol, conipheryl alcohol and syringic acid. The most toxic compounds are salicylic acid, cinnamic acid, benzoic acid and o-vanillin.
{"title":"Influence of phenolics on biomass production by Candida utilis and Candida albicans","authors":"Mária Mikulášová , Štefan Vodný , Alexandra Pekarovičová","doi":"10.1016/0144-4565(90)90032-F","DOIUrl":"10.1016/0144-4565(90)90032-F","url":null,"abstract":"<div><p>The effect of some lignin degradation products, which can be present in wood hydrolysates, on biomass production by <em>Candida</em> sp. was studied. Suspected inhibitors were used as supplements in growth media for <em>C. utilis</em> and <em>C. albicans</em> containing pure glucose as a carbon energy source. The metabolism of inhibitors by <em>C. utilis</em> and <em>C. albicans</em> is approximately the same and is extremely sensitive to the structure and concentration of the phenolic additive. ID<sub>50</sub> and ID<sub>100</sub> values for a 50% or a 100% growth inhibition for 20 lignin monomer model compounds during <em>Candida</em> sp. cultivation were established. Comparison of ID values has shown that the least toxic compounds for <em>C. utilis</em> and <em>C. albicans</em> biomass growth and yield are vanillyl alcohol, conipheryl alcohol and syringic acid. The most toxic compounds are salicylic acid, cinnamic acid, benzoic acid and o-vanillin.</p></div>","PeriodicalId":100179,"journal":{"name":"Biomass","volume":"23 2","pages":"Pages 149-154"},"PeriodicalIF":0.0,"publicationDate":"1990-01-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://sci-hub-pdf.com/10.1016/0144-4565(90)90032-F","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"79182011","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 1990-01-01DOI: 10.1016/0144-4565(90)90005-5
Louis Zsuffa
Seven countries participated in the 3-year programme (1986–1988) of the Willow Breeding Activity, Task 2 of the International Energy Agency's Bioenergy Agreement. The objectives of the activity were to facilitate the development of superior, high yielding willow clones for energy plantations by (a) exchange of genetic stock, (b) exchange of information on breeding studies, and (c) joint actions. The results of this cooperative activity are discussed accordingly. Significant achievements are in (a) enrichment of the genetic stock, especially of North American willow species; (b) evaluation and stimulation of genetic studies and breeding programmes; and (c) joint actions on disease surveys, clonal identification problems, joint testing methods and willow feedstock qualities for energy conversion. The development of high yielding stock (30 odt/ha per year or more) seems to be within reach.
{"title":"Genetic improvement of willows for energy plantations","authors":"Louis Zsuffa","doi":"10.1016/0144-4565(90)90005-5","DOIUrl":"10.1016/0144-4565(90)90005-5","url":null,"abstract":"<div><p>Seven countries participated in the 3-year programme (1986–1988) of the Willow Breeding Activity, Task 2 of the International Energy Agency's Bioenergy Agreement. The objectives of the activity were to facilitate the development of superior, high yielding willow clones for energy plantations by (a) exchange of genetic stock, (b) exchange of information on breeding studies, and (c) joint actions. The results of this cooperative activity are discussed accordingly. Significant achievements are in (a) enrichment of the genetic stock, especially of North American willow species; (b) evaluation and stimulation of genetic studies and breeding programmes; and (c) joint actions on disease surveys, clonal identification problems, joint testing methods and willow feedstock qualities for energy conversion. The development of high yielding stock (30 odt/ha per year or more) seems to be within reach.</p></div>","PeriodicalId":100179,"journal":{"name":"Biomass","volume":"22 1","pages":"Pages 35-47"},"PeriodicalIF":0.0,"publicationDate":"1990-01-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://sci-hub-pdf.com/10.1016/0144-4565(90)90005-5","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"82534428","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 1990-01-01DOI: 10.1016/0144-4565(90)90019-G
Olav Gislerud
A relatively large number of storing and drying studies of wood fuels have been carried out within the countries participating in the International Energy Agency (IEA) Bioenergy Programme. The main purpose of the studies has been to contribute to the knowledge of the processes taking place during storing and drying, and to formulated guidelines for practical storage of wood fuels. This report gives an overview of research carried out over the last few years within the countries participating in the IEA Bioenergy cooperation.
{"title":"Drying and storing of comminuted wood fuels","authors":"Olav Gislerud","doi":"10.1016/0144-4565(90)90019-G","DOIUrl":"10.1016/0144-4565(90)90019-G","url":null,"abstract":"<div><p>A relatively large number of storing and drying studies of wood fuels have been carried out within the countries participating in the International Energy Agency (IEA) Bioenergy Programme. The main purpose of the studies has been to contribute to the knowledge of the processes taking place during storing and drying, and to formulated guidelines for practical storage of wood fuels. This report gives an overview of research carried out over the last few years within the countries participating in the IEA Bioenergy cooperation.</p></div>","PeriodicalId":100179,"journal":{"name":"Biomass","volume":"22 1","pages":"Pages 229-244"},"PeriodicalIF":0.0,"publicationDate":"1990-01-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://sci-hub-pdf.com/10.1016/0144-4565(90)90019-G","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"76388666","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}