Essential scientific mapping of the value chain of thermochemical converted second-generation bio-fuels

As the largest contributor to renewable energy, biomass (especially lignocellulosic biomass) has significant potential to address atmospheric emission and energy shortage issues. The bio-fuels derived from lignocellulosic biomass are popularly referred to as second-generation bio-fuels. To date, several thermochemical conversion pathways for the production of second-generation bio-fuels have shown commercial promise; however, most of these remain at various pre-commercial stages. In view of their imminent commercialization, it is important to conduct a profound and comprehensive comparison of these production techniques. Accordingly, the scope of this review is to fill this essential knowledge gap by mapping the entire value chain of second-generation bio-fuels, from technical, economic, and environmental perspectives. This value chain covers i) the thermochemical technologies used to convert solid biomass feedstock into easier-to-handle intermediates, such as bio-oil, syngas, methanol, and Fischer-Tropsch fuel; and ii) the upgrading technologies used to convert intermediates into end products, including diesel, gasoline, renewable jet fuels, hydrogen, char, olefins, and oxygenated compounds. This review also provides an economic and commercial assessment of these technologies, with the aim of identifying the most adaptable technology for the production of bio-fuels, fuel additives, and bio-chemicals. A detailed mapping of the carbon footprints of the various thermochemical routes to second-generation bio-fuels is also carried out. The review concludes by identifying key challenges and future trends for second-generation petroleum substitute bio-fuels.

Catalytic upgrading of carboxylic acids and esters to bio fuels and bio chemicals

The research activity was focused on the transformation of methyl propionate (MP) into methyl methacrylate (MMA), avoiding the use of formaldehyde (FAL) thanks to a one-pot strategy involving in situ methanol (MeOH) dehydrogenation over the same catalytic bed were the hydroxy-methylation/dehydration of MP with FAL occurs. The relevance of such research line is related to the availability of cheap renewable bio-glycerol from biodiesel production, from which MP can be obtained via a series of simple catalytic reactions. Moreover, the conventional MMA synthesis (Lucite process) suffers from safety issues related to the direct use of carcinogenic FAL and depends on non-renewable MP. During preliminary studies, ketonization of carboxylic acids and esters has been recognized as a detrimental reaction which hinders the selective synthesis of MMA at low temperature, together with H-transfer hydrogenation with FAL or MeOH as the H-donor at higher temperatures. Therefore, ketonization of propionic acid (PA) and MP was investigated over several catalysts (metal oxides and metal phosphates), to obtain a better understanding of the structure-activity relationship governing the reaction and to design a catalyst for MMA synthesis capable to promote the desired reaction while minimizing ketonization and H-transfer. However, ketonization possesses scientific and industrial value itself and represents a strategy for the upgrade of bio oils from fast pyrolysis of lignocellulosic materials, a robust and versatile technology capable to transform the most abundant biomass into liquid biofuels. The catalysts screening showed that ZrO2 and La2O3 are the best catalysts, while MgO possesses low ketonization activity, but still, H-transfer parasitic hydrogenation of MMA reduces its yield over all catalysts. Such study resulted in the design of Mg/Ga mixed oxides that showed enhanced dehydrogenating activity towards MeOH at low temperatures. It was found that the introduction of Ga not only minimize ketonization, but also modulates catalyst basicity reducing H-transfer hydrogenations.

A Case Study of the Economic and Environmental Impacts from a Bio-fuel Facility (Southwest Georgia Ethanol, LLC) on the Surrounding Communities, Southwest Georgia

Bio-fuels such as ethanol provide an extraordinary opportunity to address our dependency on foreign oil. This case study examines the economic and environmental impacts associated with constructing and operating a dry mill ethanol manufacturing facility in a Southwest Georgia town and surrounding communities. The case study found that the plant had little impact on air quality, water quality, and habitat fragmentation. However, economic results showed the plant produced $1.5 million in tax revenues, and 86 jobs. Ethanol producers and communities must consider both the economic and environmental impacts on a local community when searching or attracting a bio-fuels plant. Likewise, communities should be aware of these challenges when attracting ethanol production plants.

Improvement of bio-oil stability in wood pyrolysis process

Pyrolysis is one of several thermochemical technologies that convert solid biomass into more useful and valuable bio-fuels. Pyrolysis is thermal degradation in the complete or partial absence of oxygen. Under carefully controlled conditions, solid biomass can be converted to a liquid known as bie-oil in 75% yield on dry feed. Bio-oil can be used as a fuel but has the drawback of having a high level of oxygen due to the presence of a complex mixture of molecular fragments of cellulose, hemicellulose and lignin polymers. Also, bio-oil has a number of problems in use including high initial viscosity, instability resulting in increased viscosity or phase separation and high solids content. Much effort has been spent on upgrading bio-oil into a more usable liquid fuel, either by modifying the liquid or by major chemical and catalytic conversion to hydrocarbons. The overall primary objective was to improve oil stability by exploring different ways. The first was to detennine the effect of feed moisture content on bio-oil stability. The second method was to try to improve bio-oil stability by partially oxygenated pyrolysis. The third one was to improve stability by co-pyrolysis with methanol. The project was carried out on an existing laboratory pyrolysis reactor system, which works well with this project without redesign or modification too much. During the finishing stages of this project, it was found that the temperature of the condenser in the product collection system had a marked impact on pyrolysis liquid stability. This was discussed in this work and further recommendation given. The quantity of water coming from the feedstock and the pyrolysis reaction is important to liquid stability. In the present work the feedstock moisture content was varied and pyrolysis experiments were carried out over a range of temperatures. The quality of the bio-oil produced was measured as water content, initial viscosity and stability. The result showed that moderate (7.3-12.8 % moisture) feedstock moisture led to more stable bio-oil. One of drawbacks of bio-oil was its instability due to containing unstable oxygenated chemicals. Catalytic hydrotreatment of the oil and zeolite cracking of pyrolysis vapour were discllssed by many researchers, the processes were intended to eliminate oxygen in the bio-oil. In this work an alternative way oxygenated pyrolysis was introduced in order to reduce oil instability, which was intended to oxidise unstable oxygenated chemicals in the bio-oil. The results showed that liquid stability was improved by oxygen addition during the pyrolysis of beech wood at an optimum air factor of about 0.09-0.15. Methanol as a postproduction additive to bio-oil has been studied by many researchers and the most effective result came from adding methanol to oil just after production. Co-pyrolysis of spruce wood with methanol was undertaken in the present work and it was found that methanol improved liquid stability as a co-pyrolysis solvent but was no more effective than when used as a postproduction additive.

Ethanol production process from banana fruit and its lignocellulosic residues: Energy analysis

Tropical countries, such as Brazil and Colombia, have the possibility of using agricultural lands for growing biomass to produce bio-fuels such as biodiesel and ethanol. This study applies an energy analysis to the production process of anhydrous ethanol obtained from the hydrolysis of starch and cellulosic and hemicellulosic material present in the banana fruit and its residual biomass. Four different production routes were analyzed: acid hydrolysis of amylaceous material (banana pulp and banana fruit) and enzymatic hydrolysis of lignocellulosic material (flower stalk and banana skin). The analysis considered banana plant cultivation, feedstock transport, hydrolysis, fermentation, distillation, dehydration, residue treatment and utility plant. The best indexes were obtained for amylaceous material for which mass performance varied from 346.5 L/t to 388.7 L/t, Net Energy Value (NEV) ranged from 9.86 MJ/L to 9.94 MJ/L and the energy ratio was 1.9 MJ/MJ. For lignocellulosic materials, the figures were less favorable: mass performance varied from 86.1 to 123.5 L/t, NEV from 5.24 10 8.79 MJ/L and energy ratio from 1.3 to 1.6 MJ/MJ. The analysis showed, however, that both processes can be considered energetically feasible. (C) 2010 Elsevier Ltd. All rights reserved.

The role of biomass and biorefineries in a sustainable future

Some o f the biggest issues facing humanity in the 21st century include energy security, global warming and resource scarcity. These issues will affect every nation and Ireland is no exception. There is much research underway to uncover technologies that will allow the world to overcome such problems, but none offer the flexibility o f biomass. Unlike other sustainable technologies, which offer a solution to one or at most two o f the above problems, biomass as demonstrated by the author, can play a part in mitigating all o f the above problems. It has been known for some time that biomass can be used in various ways as a form o f renewable energy, but with the development o f biorefineries biomass can be used to produce material as well as fuel products. In this report the author has looked at the viability and benefits o f biomass, bioenergy and biorefining in Ireland. The author has demonstrated that such technologies when implemented correctly are sustainable from an economic, environmental and societal point o f view. The author has shown in this thesis that abundant supplies o f biomass make bio re fineries a viable business opportunity in Ireland and has shown how a number o f biorefinery scenarios have the potential to be extremely profitable. The author has evaluated the profitability o f material product-based bio re fineries as well as fuel productbased configurations. The author demonstrated that value-added co-products help to make bio refineries profitable even when excise-relief is not granted on bio fuels. In this thesis the author has revealed some o f the problems that bioenergy and biorefineries have had to overcome to date and examines challenges that remain for bioenergy and biorefining, and looks at the future opportunities for bio fuels. This report concludes that biomass and biorefining has exciting business potential while offering unique opportunities to mitigate the problems o f the future.

Fabricació i anàlisi del biodièsel

La producció de biodièsel a partir d'olis de cuina utilitzats, amb l'objectiu de transformar un residu en un producte amb valor comercial i ambiental, és més net que els combustibles fòssils i contribueix a disminuir el gran consum de petroli que estem fent. En una primera part teòrica s’ha realitzat un treball de recerca d' informació del biodièsel per saber si és un bon combustible i si podria ser un possible substitut dels combustibles fòssils. En quant a la part pràctica l'objectiu principal ha estat fabricar el biodièsel . Les matèries primeres són oli de gira-sol i oli de cuina utilitzat, per tal de comparar les seves qualitats. S’ha arribat a la conclusió que presenten característiques molt semblants. Després de fer les anàlisis físico-químics de qualitat vam fer una mescla dels dos biodièsels fabricats, i el vam provar en un motor Dièsel per comprovar si funciona correctament i fer una comparació dels gasos emesos pel nostre combustible amb els emesos pel gasoil comercial. El resultat va ser molt positiu ja que el motor va funcionar correctament, i la comparació de gasos va sortir tal i com esperàvem ja que les quantitats de diòxid i monòxid de carboni emeses eren menors que en el gasoil.

Charting Our Own Course: Today’s Challenges, Tomorrow’s Opportunities, December 2008

The Office of Energy Independence presents Iowa’s second annual energy independence plan, which highlights accomplishments achieved thus far and makes recommendations for the coming year. This plan shows that Iowa has made significant progress in building the foundation for reaching energy independence in just the past year. Continued investment and further efforts will enable Iowa to push toward even greater advances, while creating new jobs and diversifying local economies. With those aims in mind, the state has been investing extensively in the new energy economy. One important example is the Iowa Power Fund, an annual appropriation from the Iowa General Assembly administered by the Office of Energy Independence. In less than one year, the Office has received more than 160 project applications totaling more than $308 million in requests. The projects approved thus far will help advance Iowa’s wind and solar industries, foster new energy efficiency practices, and develop the bio fuels industry for a more economically and environmentally sustainable future. Iowa’s position as a leader in the new energy economy is dependent on the success of the Power Fund, and on the success of this plan. This plan clearly states that Iowa must boldly pursue a strong position in the emerging energy economy worldwide.

Energy Annual Report 2015, April 2015

The Iowa Economic Development Authority (IEDA) Energy Office sets energy policy direction for Iowa and receives designated funding from the State Energy Program Formula from the Department of Energy to carry out designated energy activities. These activities include promoting energy efficiency, bio-fuels and renewable energy.

Yhdyskuntalietteen ja biopolttoaineiden käsittelyketjujen ja polton teknistaloudellinen tarkastelu

Työn tavoitteena on kartoittaa yhdyskuntalietteen ja kierrätys- sekä biopolttoaineiden käsittelyä ja polttoa lietteenpolttolaitoksen tarpeita ajatellen. Lietteen käsittelyketjun ja kierrätys- sekä biopolttoaineketjujen tekninen tarkastelu on siis työn keskeinen tavoite. Lisäksi lasketaan polttolaitoksen suurimpia mahdollisia investointikustannuksia eri polttoainevaihtoehdoilla. Työssä tehdään muun ohella case-tarkastelua Kaakkois- Suomen alueeseen liittyen. Tavoitteena on muodostaa tarkoitukseen soveltuva polttoaineratkaisu kullekin tapauk-selle. Työn alkuosassa tutustutaan yleisesti lietteeseen sekä polttoaineen että jätteen roolissa. Tarkastelu sisältää tietoja lietteen ominaisuuksista sekä lietteenkäsittelyssä olennaisista lainsäädännöllisistä seikoista. Samoin katsastetaan hieman lietteen esikäsittelyä, mekaanista vedenerotusta, termistä kuivausta ja polttoa tarkastellaan yleisessä valossa. Lisäksi alkuosassa keskitytään eri bio- jakierrätyspolttoainevaihtoehtoihin tarkastelemalla niiden yleisyyttä polttoaineena sekä esittelemällä niiden käsittelyketjuja. Työn loppupuoliskolla kiinnitetään huomiota case tapausten avulla polttolaitoksesta saataviin tuottoihin sekä millaisen liikkumavaran eri polttoainevaihtoehdot investointien osalta sallivat. Case-tapauksissa pohditaan Kymenlaakson ja Etelä-Karjalan paikallisia lietteen-polttomahdollisuuksia yhdistettynä kierrätys- tai biopolttoaineisiin. Mekaanisesti kuivattua lietettä käsitellään kyseisissä tapauksissa vuosittain 6000 t ja 15 000 t. Lietteen polton tuottama sähkö- ja lämpöteho näyttävät riippuvan voimakkaasti lietteen kuiva-ainepitoisuudesta, eivät niinkään lietteen muista ominaisuuksista. Lisäksi joko bio- tai kierrätyspolttoaineella saadaan sähkön- ja lämmöntuotantoa nostettua huomattavasti.

100MW:n biokattilan polttoaineiden hankinta ja taselaskenta

Diplomityö tehtiin Anjalankoskella sijaitsevalle Vattenfallin tytäryhtiölle, Vamy Oy:lle. Vamy toimittaa Myllykoski Paper Oy:lle prosessilämpöä ja sähköä. Vuotuinen energiantuotanto on noin 700- 900 GWh prosessilämpöä ja 150- 190 GWh sähköä paperin tuotantomäärästä riippuen. Diplomityön tavoitteena oli parantaa voimalaitoksen kiinteän polttoaineen näytteenottojärjestelmää ja sitä kautta parantaa biokattilan hyötysudetta. Voimalaitoksen biokattila on leijupetikattila, jossa poltetaan tehtaalta tulevaa kuorta ja lietettä sekä tehtaan ulkopuolisia puuperäisiä biopolttoaineita ja turvetta. Työn aikana tehtyjen selvitysten perusteella voimalaitokselle hankittiin polttoainetietojärjestelmä. Lisäksi näytteenotto- ja näytteiden käsittelyohjeet päivitettiin energiaturpeen laatuohjeen 2006 ja kiinteiden biopolttoaineiden CEN teknisten spesifikaatioiden mukaiseksi.

Seospellettien pienpoltto

This work is a part of Vapos research over mixed pellets. In this work combustion of ten different mixed pellets are examined. This is done by two kinds of tests, burning tests and ash melting tests. First there is a short review how different bio fuels burn and what kind of problems they cause. After this burning characteristics and flue gas calculation methods are acquainted. In test part burning tests and ash melting tests and their results are reported. Lastly conclusions and considerations over further study are done.

Radiative Heat Transfer in Boiler Furnaces

Better models are needed for radiative heat transfer in boiler furnaces. If the process is known better, combustion in the furnace can be optimized to produce low emissions. It makes the process to be environmental friendly. Furthermore, if there is a better model of the furnace it can more fully explain what is happening inside the furnace. Using of the model one can quickly and easily analyze how it operates with bio fuels, moist fuels or difficult fuels and improve the operation. Models helps with better estimation of furnace dimensions and result in more accurate understanding of operation. Key component lacking in these models is radiative heat transfer in particle laden gases. If there are no particles than radiative heat transfer can be calculated approximately. There are two problems with current models when used with flow modeling. The first one is a need to account for a particle laden gas and the second one is an absence of a fast algorithm. Fast calculation is needed if radiative heat transfer calculation is done for a large CDF model. Computations slow down if time is required for calculating radiative properties over and over again. This thesis presents a band model for radiative heat transfer in boiler furnaces. Advantage is a quickness of calculation and account of particles in the process.

Biopolttoaineilla toimiva Stirling-voimalaitos

Stirling-moottori on ns. kuumailma moottori, joka toimii kaasun lämpötilaeron avulla. Kuumailma moottorin erityispiirteitä on laitteen ulkopuolella tapahtuva palaminen, josta lämpö johdetaan moottorille. Yleensä polttoaineena on käytetty vähän likaavaa polttoainetta esim. maakaasua mutta fossiilisten polttoaineiden kallistumisen ja niistä aiheutuvien päästöjen vuoksi niiden korvaaminen biopolttoaineella on tullut ajankohtaiseksi aiheeksi. Biopolttoaineiden likaavuuden takia niillä ei kuitenkaan voida lämmittää Stirling-moottoria suoraan vaan tarvitaan ylimääräinen lämmönsiirrin. Tämä diplomityö suoritettiin Lappeenrannan teknilliselle yliopistolle ja sen tarkoituksena oli tutkia juuri tähän laitteistoon suunnitellun, Stirling-moottorin ja polttokammion välisen lämmönsiirtimen suoritusarvoja ja likaantumista. Lisäksi työssä tutkittiin lämmönsiirtimeltä Stirling-moottorille menevien ilmaputkien lämpöhäviöitä. Työssä tultiin siihen tulokseen, että tämän tyyppinen lämmönsiirrin on suoritusarvoiltaan keskiverto kaasu-kaasu lämmönsiirrintä parempi ja ei likaannu erityisen nopeasti. Lämpöhäviöt olivat toisaalta merkittävämmässä asemassa kuin likaantuminen. Suurista lämpötiloista johtuva eristeiden lämmöneristyskyvyn heikkeneminen tai lämmönsiirtimen vuoto aiheutti merkittäviä lämpöhäviöitä.