User:Milton Beychok/Sandbox: Difference between revisions

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'''Biomass''', a source of [[renewable energy]], is [[biology|biological]] material such as wood, wood waste, municipal solid waste, straw, sugar cane, algae, and many other byproducts derived from agricultural and forestry production as well as other sources. Since biomass derives from plants generated by [[solar energy]] in the [[photosynthesis]] process, it can also be defined as the biological material on [[Earth]] that has stored solar energy in the chemical bonds of the organic material.
 
The [[fossil fuels]] ([[coal]], [[Petroleum crude oil|petroleum]] and [[natural gas]]) are currently thought to have been formed from prehistoric, ancient biomass buried deeply underground over millions of years of [[geological time]]. Therefore, they  are not considered to be renewable sources of energy
 
==Production of fuels and other products from biomass==
 
===Biomass fuel for electric power production===
 
The direct combustion of biomass for producing [[heat]] and [[Electrical power plant|electric power]] provides a ready disposal mechanism for municipal, agricultural, and industrial organic wastes. In 2009, about 11,350 [[Watt (unit)|megawatts]] (MW) of electric power, amounting to 1.1% of the summertime electrical supply in the [[United States]] was generated by burning biomass that included: wood, wood waste, [[municipal solid waste]] (MSW), [[landfill gas]], and agricultural byproducts and waste.<ref>[http://www.eia.doe.gov/cneaf/alternate/page/renew_energy_consump/table4.html U.S. Electric Net Summer Capacity] [[U.S. Energy Information Administration]] (EIA), part of the [[U.S. Department of Energy]] (DOE)</ref>
 
The New Hope Power Partnership in [[Florida]] is the largest [[biomass power plant]] in [[North America]]. It generates 140 MW of power using uses sugar cane fiber ([[bagasse]]) and recycled wood as fuel.<ref>[http://www.psc.state.fl.us/utilities/electricgas/RenewableEnergy/Cepero-OCFC.pdf Agriculture & Renewable Energy: The Partnership for a New Frontier] Florida Power Service Commission (FPSC) Workshop, July 26, 2007.</ref> It has been in operation for more than 10 years. 
 
===Production of liquid transportation fuels===
 
There are several processes  available for converting the [[Energy (science)|chemical energy]] contained in biomass into liquid automotive transport fuels such as [[biodiesel]] and [[ethanol]].<ref>[http://www1.eere.energy.gov/biomass/abcs_biofuels.html ABC's of Biofuels] From the website of the [[Office of Energy Efficiency and Renewable Energy]] (EERE) in the U.S. Department of Energy (DOE).</ref>
 
'''''Ethanol fuel''''':
 
Ethanol fuel is [[Ethanol|ethyl alcohol]] (C<sub>2</sub>H<sub>5</sub>OH) and it is most often used as an automotive [[motor fuel]], mainly as an additive for [[gasoline]]. Ethanol can be produced by [[fermentation]] of [[sugar cane]], [[bagasse]], [[sugar beet]]s, [[barley]], [[potato]]es, [[corn]] and many other grains as well as many agricultural byproducts and wastes.
 
The worldwide production of ethanol for automotive fuel in 2007 was 52,000,000,000 [[litre]]s (13,700,000,000 [[gallon]]s). From 2007 to 2008, the share of ethanol in global gasoline use increased from 3.7% to 5.4%.<ref name=UNEP>[http://www.unep.fr/scp/rpanel/pdf/Assessing_Biofuels_Full_Report.pdf Assessing Biofuels (2009)] From the website of the [[United Nations Environment Programme]] (UNEP)</ref> In 2009, worldwide ethanol fuel production reached 73,900,000,000 litres (19,500,000,000 gallons) and was expected to reach 85,900,000,000 litres (22,700,000,000 gallons) in 2010.<ref name=RFA-News>[http://www.ethanolrfa.org/news/entry/global-ethanol-production-to-reach-85.9-billion-litres-22.7-billion-ga/ Global ethanol production to reach 85.9 billion litres (22.7 billion gallons) in 2010] March 22, 2010. From the website of the Renewable Fuels Association (RFA).</ref>
 
Ethanol fuel is widely used in [[Brazil]] and in the United States, and together both countries were responsible for about 86 percent of the world's ethanol fuel production in 2009.<ref>[http://www.ethanolrfa.org/pages/statistics Ethanol Industry Statistics] ''2009 World Fuel Ethanol Production'' from the website of the Renewable Fuels Association.</ref>
 
'''''Biodiesel fuel''''':
 
[[Biodiesel]] refers to a [[Diesel oil|diesel fuel]] produced by chemically [[Chemical reaction|reacting]] [[lipids]] such as  vegetable oils or animal fats with an [[alcohol]] such as [[methyl alcohol]] (CH<sub>3</sub>OH). The resulting biodiesel consists of [[esters]] of long-chain [[fatty acid]]s. The process is known as "transesterification" and it may be carried out by several methods: the common batch process, supercritical processes and ultrasonic methods.
 
In 2009, the worldwide production of biodiesel was 17,900,000,000 litres (4,730,000,000 gallons). The three countries with the largest annual biodiesel production were [[Germany]] (16%), [[France]] (12%) and the United States (11%).<ref>[http://www.plateforme-biocarburants.ch/en/infos/production.php?id=biodiesel Production of biofuels in the world in 2009] August 30, 2010. From the website of the Biofuels Platform published in Switzerland.</ref>
 
{| border="0" width="240" align="right"
|
{| class = "wikitable" border="1" align="right" width="220"
|+ Worldwide Gasification Plants<br/>as of 2010<ref>[http://www.netl.doe.gov/technologies/coalpower/gasification/worlddatabase/2010_Worldwide_Gasification_Database.pdf Worldwide Gasification Database] [[National Energy Technology Laboratory]] (NETL), U.S. Department of Energy (DOE)</ref>
!Feedstock!!Plants!!Gasifiers
|- align=center
|Coal||53||201
|- align=center
|Petroleum||59||143
|- align=center
|Natural gas||23||&nbsp;59
|- align=center
|Biomass||&nbsp;9||&nbsp; 9
|- align=center
|Totals||144||412
|}
|}
 
===Biomass gasification to produce syngas===
 
[[Gasification]] is a process that reacts [[Carbon|carbon-containing]] materials (such as coal or biomass) at high [[temperature]]s with reagent gases (namely, [[steam]], pure [[oxygen]] and/or [[air]]) to produce a mixture of [[carbon monoxide]] (CO) and [[hydrogen]] (H<sub>2</sub>) commonly called ''syngas'' (a contraction of ''synthesis gas''). It has been in use since the early 1800s when coal and [[peat]] were gasified to produce what was then called ''town gas'' for lighting and cooking ... later to be replace by [[electricity]] and natural gas. As of 2010, 412 modern industrial-scale gasifiers were in operation in 29 countries worldwide (see adjacent table).<ref name=DOE-Overview>[http://www.netl.doe.gov/technologies/coalpower/gasification/pubs/pdf/DOE%20Gasification%20Program%20Overview.pdf DOE Gasification Program Overview] Jenny B. Tennant (December 2010, National Energy Technology Laboratory (NETL), U.S. Department of Energy. An excellent overview of the worldwide gasification technology.</ref>
 
The syngas may be directly burned as a fuel, converted into methyl alcohol or hydrogen, subjected to [[methanation]] to produce [[synthetic natural gas]] (SNG),<ref>M.R. Beychok (May 1975), "Process and environmental technology for producing SNG and liquid fuels", ''[[U.S. EPA]] report EPA-660/2-75-011''.</ref> or converted into synthetic liquid [[hydrocarbon]]s via the [[Fischer-Tropsch]] process.
 
The vessel in which the gasification process takes place is called a ''gasifier''. There are various types of gasifiers in current use,<ref name=DOE-Overview/><ref name=NETL>[http://www.netl.doe.gov/technologies/coalpower/gasification/gasifipedia/4-gasifiers/4-1_types.html Gasifiers in detail: Types of gasifiers] National Energy Technology Laboratory ((NETL), U.S. Department of Energy (DOE)</ref> including:
 
*'''''Counter-current fixed bed gasifier:''''' This gasifier is a vertical, cylindrical vessel containing a bed of carbon-containing material (e.g., coal or biomass) through which steam, oxygen and/or air flow upward. Although commonly  referred to as a fixed bed gasifier, the crushed coal or biomass is fed into the gasifier through a lock hopper mounted on top of the gasifier and the carbonaceous material slowly moves downward as it is converted into syngas, which is removed from the upper portion of the gasifier,  and ash or slag removed from the bottom of the gasifier.<ref name=Visagie>[http://upetd.up.ac.za/thesis/available/etd-07022009-133535/unrestricted/dissertation.pdf Generic gasifier modelling: Evaluating model by gasifier type] J.P. Visagie (October 2008), Master's dissertation, [[University of Pretoria]], [[South Africa]]</ref><ref>{{cite journal|author=M.R. Beychok|title=Coal gasification for clean energy|journal=Energy Pipelines and Systems|volume=|issue=| pages=|date=March 1974|id=|url=}}</ref><ref>M.R. Beychok (September 1974), "Coal gasification and the Phenosolvan process", ''American Chemical Society 168th National Meeting'', [[Atlantic City, New Jersey]]</ref>
 
{{Image|SiemensEntrainedGasifier.png|right|210px|Fig.1: A top-fired, oxygen-blown, dry feed, entrained flow gasifier}}
 
*'''''Co-current fixed bed  gasifier:''''' This gasifier is also a vertical cylindrical vessel, which is quite similar to the  counter-current gasifier type except that the steam, oxygen and/or air enter at the top of the bed, flow downward co-current with the slowly moving bed of carbonaceous material, and the product syngas is removed below the bed. <ref name=Visagie/><ref>M.J. Groeneveld and W.P.M. Van Swaaij, "The Design of Co-Current Moving-Bed Gasifiers Fueled by Biomass" published in this book: {{cite book|author=Jerry Latham Jones and Shirley B. Radding (Editors)| title=Thermal conversion of solid wastes and biomass: based on a symposium|edition=Volume 130 of ACS symposium series|publisher=American Chemical Society|date= 1980|id=ISBN 0-8412-0565-5}}</ref><ref name=Groeneveld>[http://doc.utwente.nl/68447/1/Groeneveld79gas.pdf Gasification and solid waste -- Potential and application of co-current moving bed gasifiers] M.J. Groeneveld and W.P.M. Van Swaaij, [[Twente University of Technology]], [[The Netherlands]].</ref>
 
*'''''Fluidized bed gasifier:''''' This gasifier is again a vertical, cylindrical vessel. It differs from the fixed bed reactors in that the feedstock biomass is very finely crushed before it enters the gasifier and the reaction bed of ground biomass is fluidized by the reagent gases (steam, oxygen and/or air) flowing upward through the bed. The fluidization of the reaction bed increases the height of the bed (as compared to the fixed bed gasifiers) and the finely crushed biomass results in much more biomass surface area being exposed to the reagent gases. The product syngas contains fine particles of crushed biomass which are removed by routing the syngas through a [[cyclone]] to recover the fines and recycle them back into the reaction bed.<ref name=Visagie/><ref name=Kreutz>[http://web.mit.edu/mitei/docs/reports/kreutz-fischer-tropsch.pdf Fischer-Tropsch Fuels from Coal and Biomass] Thomas G. Kreutz et al (October 2008), [[Princeton University]], presented at 25th Annual International Pittsburgh Coal Conference, [[Pittsburgh, Pennsylvania]], September 29 to October 2, 2008.</ref>
 
*'''''Entrained flow gasifier:''''' This gasifier, like the other three discussed above, is also a vertical, cylindrical vessel. The feedstock biomass is finely crushed and flows downward co-currently with pure oxygen. Air is seldom used as a reagent gas in an entrained gasifier. The gasification [[Chemical reaction|reactions]] take place in a dense cloud of fine biomass particles. The syngas exits from the bottom section of the gasifier and is routed through a cyclone (and perhaps a water scrubber) for removal of the fines. Entrained gasifiers operate at temperatures of about 1000 to 1800 °[[Celsius (unit)|C]] and at pressures of 30 to 70 [[Bar (unit)|bar]] which is a much higher pressure than is the case for the other types of gasifiers. The adjacent Fig. 1 depicts an entrained flow gasifier of the type discussed here.<ref name=DOE-Overview/><ref name=Visagie/><ref name=Kreutz/><ref>[http://www.ecn.nl/docs/library/report/2004/c04039.pdf Entrained Flow Gasification of Biomass] A. van der Drift et al (April 2004), [[Energy research Centre of the Netherlands]] (ECN), Report ECN-C--04-039.</ref>
 
====Gasification chemistry====
 
It is difficult to state exactly what chemical reactions occur during gasification. However, most researchers have reached agreement on the primary reactions and the syngas composition ranges shown just below:<ref name=DOE-Overview/><ref name=Visagie/>
 
{{Image|GasifierReax.png|center|476px|}}
 
=== Fischer-Tropsch synthesis of liquid hydrocarbons===
{{Image|BTL.png|right|225px|Fig.2: Biomass-To-Liquids (BTL) process}}
 
Fischer-Tropsch synthesis is a catalytic chemical process developed in the 1920s to convert a mixture of carbon monoxide and hydrogen (i.e., syngas), into hydrocarbon [[Molecule|molecular]] chains of varying lengths.
 
The process was invented by [[Franz Fischer]] and [[Hans Tropsch]] working in [[Germany]]'s [[Kaiser Wilhelm Institute]] (today the [[Max Planck Institute]]) in the 1920's. It was first commercialized in Germany in 1936 and it was used extensively by Germany  during [[World War II]] to produce synthetic fuels. Later, facing isolation and embargoes during the [[apartheid]] era (1948 - 1990), [[South Africa]] turned to coal gasification and the Fischer-Tropsch process to supply significant quantities of its hydrocarbon fuel needs. Since that time, the process has been extensively improved and refined.<ref name=NETL-FT>[http://www.netl.doe.gov/technologies/coalpower/gasification/gasifipedia/5-support/5-11_ftsynthesis.html Fischer-Tropsch (FT) Synthesis]] From the website of the National Energy Technology Laboratory (NETL) in the U.S. Department of Energy.</ref><ref>{{cite journal|author=Hans Schulz|title=Short history and present trends of Fischer–Tropsch synthesis|journal=Applied Catalysis A: General|volume=186|issue=1 - 2| pages = pp. 3 - 12|date=October 4, 1999|id=|url=}}</ref>
 
The process is relatively simple: syngas is fed at high temperatures through [[Catalysis|catalysts]] (usually the transition metals [[cobalt]] or [[iron]]) which facilitate the hydrocarbon formation. When paired with syngas from the gasification of fossil fuels or biomass, the Fischer-Tropsch process is a method of converting any available carbon source into hydrocarbon liquids consisting of [[molecule]]s having from 5 to 20 carbon [[atoms]] in accordance with the following equation for the formation of [[alkane]]s (C<sub>n</sub>H<sub>2n+2</sub>), which are the primary hydrocarbons formed:<ref name=NETL-FT/><ref name=knowl>[http://knol.google.com/k/the-fischer-tropsch-ft-process# The Fischer-Tropsch (FT) Process] From the [[Knowl]] website</ref>
 
:<math>\mathrm{(2n+1)\,H_2} + \mathrm{n\,CO} \rightarrow \mathrm{C_nH_{2n+2}} + \mathrm{n\,H_2O}</math>
 
where n is an integer. For example, if n = 5, the equation represents the formation of [[pentane]] (C<sub>5</sub>H<sub>12</sub>) which is a liquid hydrocarbon that is a component of [[gasoline]] (petrol). As another example, if n = 12, the equation represents the formation of [[decagon]] (C<sub>12</sub>H<sub>26</sub>) which is a liquid hydrocarbon  component of diesel fuel.
 
Lesser amounts of [[alkene]]s (C<sub>n</sub>H<sub>2n</sub>) and [[alcohol]]s (C<sub>n</sub>H<sub>2n+1</sub>OH) are formed in accordance with these equations:<ref name=knowl/>
 
:<math>\mathrm{n\,CO} + \mathrm{2n\,H_2} \rightarrow \mathrm{C_nH_{2n}} + \mathrm{n\,H_2O}</math>
:<math>\mathrm{n\,CO} + \mathrm{2n\,H_2} \rightarrow \mathrm{C_nH_{2n+1}OH} + \mathrm{(n\!-\!1)\,H_2O}</math>
 
 
There are a good many different reactor designs for the Fischer-Tropsch process as well as different operating conditions. There are two general process temperature ranges:<ref name=knowl/><ref name=Davis>[http://accessscience.com/content/Fischer-Tropsch-synthesis/YB109990 Fischer-Tropsch Synthesis] Burtron H. Davis (2010) in AccessScience, McGraw-Hill Companies.</ref>
*Low temperature (200 to 260 °C): Designs using this temperature are referred to LTFT (a contraction of "low temperature Fischer-Tropsch") and generally use a cobalt catalyst.
*High temperature (300 to 350 °C): Designs using this temperature are referred to HTFT (a contraction of "high  temperature Fischer-Tropsch")and generally use an iron catalyst.
 
The LTFT designs produce predominantly hydrocarbons in the [[Boiling point|boiling range]] of diesel fuel and [[Wax|waxes]]. Fixed-bed reactors are considered to be the "conventional" technology for LTFT designs and slurry phase reactors are considered to be "advanced" technology.
 
The HTFT designs produce predominantly gaseous alkene hydrocarbons having 2 to 4 carbon atoms and liquid hydrocarbons in the boiling range of gasoline. Circulating fluidized bed reactors are considered to be the "conventional" technology for HTFT designs and fixed fluidized bed reactors are considered to be "advanced" technology.
 
==References==
{{reflist}}

Revision as of 17:52, 6 April 2011

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