Gasification 262256 226082052 2008-07-16T19:17:40Z Shekhawati 1438228 /* Waste disposal */ {{portal|Energy}} {{For|the water carbonator|Gasogene}} '''Gasification''' is a process that converts carbonaceous materials, such as [[coal]], [[petroleum]], or [[biomass]], into [[carbon monoxide]] and [[hydrogen]] by reacting the raw material at high temperatures with a controlled amount of [[oxygen]] and/or [[steam]]. The resulting gas mixture is called [[synthesis gas]] or [[syngas]] and is itself a fuel. Gasification is a very efficient method for extracting [[energy]] from many different types of organic materials, and also has applications as a clean [[waste disposal]] technique. The advantage of gasification is that using the [[syngas]] is more efficient than direct combustion of the original fuel, more of the energy contained in the fuel is extracted. [[Syngas]] may be burned directly in internal combustion engines, used to produce [[methanol]] and [[hydrogen]], or converted via the [[Fischer-Tropsch process]] into [[synthetic fuel]]. Gasification can also begin with materials that are not otherwise useful fuels, such as [[biomass]] or [[organic material|organic]] waste. In addition, the high-temperature combustion refines out corrosive ash elements such as chloride and potassium, allowing clean gas production from otherwise problematic fuels. Gasification of [[fossil fuels]] is currently widely used on industrial scales to generate [[electricity]]. However, almost any type of [[organic material]] can be used as the raw material for gasification, such as [[wood]], [[biomass]], or even [[plastic]] waste. Thus, gasification may be an important technology for [[renewable energy]]. In particular [[biomass]] gasification can be [[carbon neutral]]. Gasification relies on chemical processes at elevated temperatures >700°C, which distinguishes it from biological processes such as [[anaerobic digestion]] that produce [[biogas]]. == Chemistry == In a gasifier, the carbonaceous material undergoes several different processes: [[Image:pyrolysis.gif|frame|Pyrolysis of carbonaceous fuels]] [[Image:gasification.gif|frame|Gasification of char]] #The ''[[pyrolysis]]'' (or devolatilization) process occurs as the carbonaceous particle heats up. Volatiles are released and [[charring|char]] is produced, resulting in up to 70% weight loss for coal. The process is dependent on the properties of the carbonaceous material and determines the structure and composition of the char, which will then undergo gasification reactions. # The ''[[combustion]]'' process occurs as the volatile products and some of the char reacts with oxygen to form [[carbon dioxide]] and [[carbon monoxide]], which provides heat for the subsequent gasification reactions. Letting '''C''' represent a carbon-containing [[organic compound]], the basic reaction here is <math>{\rm C} + \begin{matrix} \frac{1}{2} \end{matrix}{\rm O}_2 \rarr {\rm CO}</math> #The ''gasification'' process occurs as the char reacts with carbon dioxide and steam to produce carbon monoxide and hydrogen, via the reaction <math>{\rm C} + {\rm H}_2 {\rm O} \rarr {\rm H}_2 + {\rm CO}</math> # In addition, the [[reversible reaction|reversible]] gas phase [[water gas shift reaction]] reaches [[chemical equilibrium|equilibrium]] very fast at the temperatures in a gasifier. This balances the concentrations of carbon monoxide, steam, carbon dioxide and hydrogen. <math>{\rm CO} + {\rm H}_2 {\rm O} \lrarr {\rm CO}_2 + {\rm H}_2</math> In essence, a limited amount of oxygen or air is introduced into the reactor to allow some of the organic material to be "burned" to produce [[carbon monoxide]] and [[energy]], which drives a second reaction that converts further organic material to [[hydrogen]] and additional [[carbon dioxide]]. == History == The gasification process was originally developed in the 1800s to produce [[town gas]] for lighting and cooking. Electricity and natural gas later replaced town gas for these applications, but the gasification process has been utilized for the production of synthetic chemicals and fuels since the 1920s. [[Wood gas generator]]s, called Gasogene or ''Gazogène'', were used to power motor vehicles in [[Europe]] during [[World War II]] fuel shortages.<ref>[http://membres.lycos.fr/rotarysu/nouvelle.htm Gas Generator Project] History of the Gasogene technology.</ref> == Current applications == Industrial-scale gasification is currently mostly used to produce electricity from [[fossil fuels]] such as [[coal]], where the [[syngas]] is burned in a [[gas turbine]]. Gasification is also used industrially in the production of electricity, ammonia and liquid fuels (oil) using Integrated Gasification Combined Cycles ([[Integrated Gasification Combined Cycle|IGCC]]), with the possibility of producing [[methane]] and [[hydrogen]] for fuel cells. IGCC is also a more efficient method of CO<sub>2</sub> capture as compared to conventional technologies. IGCC demonstration plants have been operating since the early 1970s and some of the plants constructed in the 1990s are now entering commercial service. Within the last few years, gasification technologies have been developed that use [[plastic]]-rich waste as a feed. In a plant in Germany such a technology—on large scale—converts plastic waste via [[syngas]] into [[methanol]].<ref>[http://www.svz-gmbh.de/GB/Seiten/rahmtec.html Converting waste to methanol]</ref> Small-scale rural biomass gasifiers have been applied in [[India]] to a large extent, especially in the state of [[Tamil-Nadu]] in South India. Most of the applications are 9 kWe systems used for (drink) water pumping and street lighting operated by the local [[panchayat]] government. Although technically applicable the systems do face a number of problems. There are political, financial and maintenance problems. Most of the systems are no longer running after 1...3 years. == Potential for renewable energy == Gasification can proceed from just about any [[organic material]], including [[biomass]] and [[plastic]] waste. The resulting [[syngas]] burns cleanly into water vapor and [[carbon dioxide]]. Alternatively, [[syngas]] may be converted efficiently to [[methane]] via the [[Sabatier reaction]], or diesel-like [[synthetic fuel]] via the [[Fischer-Tropsch process]]. Inorganic components of the input material, such as metals and minerals, are trapped in an inert and environmentally safe form as ash, which may have use as a fertilizer. Regardless of the final fuel form, gasification itself and subsequent processing neither emits nor traps [[greenhouse gasses]] such as [[carbon dioxide]]. Combustion of syngas or derived fuels does of course emit carbon dioxide. However, [[biomass]] gasification could play a significant role in a [[renewable energy]] economy, because [[biomass]] production removes CO<sub>2</sub> from the atmosphere. While other [[biofuel]] technologies such as [[biogas]] and [[biodiesel]] are also [[carbon neutral]], gasification runs on a wider variety of input materials, can be used to produce a wider variety of output fuels, and is an extremely efficient method of extracting energy from biomass. Biomass gasification is therefore one of the most technically and economically convincing energy possibilities for a [[carbon neutral]] economy <ref>Read, Peter, ''Carbon cycle management with increased photo-synthesis and long-term sinks''. Royal Society of New Zealand, http://www.rsnz.org/topics/energy/ccmgmt.php</ref>. There is at present very little industrial scale biomass gasification being done. The Renewable Energy Network Austria<ref>[http://www.renet.at/main_en.php RENET - The path to energy autonomy<!-- Bot generated title -->]</ref> is associated with several successful biomass gasification demonstration projects, including a plant using dual fluidized bed gasification<ref>[http://www.ficfb.at The FICFB-gasification system<!-- Bot generated title -->]</ref> that has supplied the town of [[Güssing]] with 2&nbsp;MW of electricity and 4&nbsp;MW of heat, generated from wood chips, since 2003. == Gasification processes == Four types of gasifier are currently available for commercial use: counter-current fixed bed, co-current fixed bed, [[fluidized bed]] and entrained flow.<ref>Beychok, M.R., ''Process and environmental technology for producing SNG and liquid fuels'', U.S. EPA report EPA-660/2-75-011, May 1975</ref><ref>Beychok, M.R., ''Coal gasification for clean energy'', Energy Pipelines and Systems, March 1974</ref><ref>Beychok, M.R., ''Coal gasification and the Phenosolvan process'', American Chemical Society 168th National Meeting, Atlantic City, September 1974</ref> The '''counter-current fixed bed ("up draft") gasifier''' consists of a fixed bed of carbonaceous fuel (e.g. coal or biomass) through which the "gasification agent" (steam, oxygen and/or air) flows in counter-current configuration. The ash is either removed dry or as a slag. The slagging gasifiers require a higher ratio of steam and oxygen to carbon in order to reach temperatures higher than the ash fusion temperature. The nature of the gasifier means that the fuel must have high mechanical strength and must be non-caking so that it will form a permeable bed, although recent developments have reduced these restrictions to some extent. The throughput for this type of gasifier is relatively low. Thermal efficiency is high as the gas exit temperatures are relatively low. However, this means that tar and methane production is significant at typical operation temperatures, so product gas must be extensively cleaned before use or recycled to the reactor. The '''co-current fixed bed ("down draft") gasifier''' is similar to the counter-current type, but the gasification agent gas flows in co-current configuration with the fuel (downwards, hence the name "down draft gasifier"). Heat needs to be added to the upper part of the bed, either by combusting small amounts of the fuel or from external heat sources. The produced gas leaves the gasifier at a high temperature, and most of this heat is often transferred to the gasification agent added in the top of the bed, resulting in an energy efficiency on level with the counter-current type. Since all tars must pass through a hot bed of char in this configuration, tar levels are much lower than the counter-current type. In the '''[[fluidized bed reactor]]''', the fuel is [[fluidization|fluidized]] in oxygen and steam or air. The ash is removed dry or as heavy agglomerates that defluidize. The temperatures are relatively low in dry ash gasifiers, so the fuel must be highly reactive; low-grade coals are particularly suitable. The agglomerating gasifiers have slightly higher temperatures, and are suitable for higher rank coals. Fuel throughput is higher than for the fixed bed, but not as high as for the entrained flow gasifier. The conversion efficiency can be rather low due to elutriation of carbonaceous material. Recycle or subsequent combustion of solids can be used to increase conversion. Fluidized bed gasifiers are most useful for fuels that form highly corrosive ash that would damage the walls of slagging gasifiers. Biomass fuels generally contain high levels of corrosive ash. In the '''entrained flow gasifier''' a dry pulverized solid, an atomized liquid fuel or a fuel slurry is gasified with oxygen (much less frequent: air) in co-current flow. The gasification reactions take place in a dense cloud of very fine particles. Most coals are suitable for this type of gasifier because of the high operating temperatures and because the coal particles are well separated from one another. The high temperatures and pressures also mean that a higher throughput can be achieved, however thermal efficiency is somewhat lower as the gas must be cooled before it can be cleaned with existing technology. The high temperatures also mean that tar and methane are not present in the product gas; however the oxygen requirement is higher than for the other types of gasifiers. All entrained flow gasifiers remove the major part of the ash as a slag as the operating temperature is well above the ash fusion temperature. A smaller fraction of the ash is produced either as a very fine dry fly ash or as a black colored fly ash slurry. Some fuels, in particular certain types of biomasses, can form slag that is corrosive for ceramic inner walls that serve to protect the gasifier outer wall. However some entrained bed type of gasifiers do not possess a ceramic inner wall but have an inner water or steam cooled wall covered with partially solidified slag. These types of gasifiers do not suffer from corrosive slags. Some fuels have ashes with very high ash fusion temperatures. In this case mostly limestone is mixed with the fuel prior to gasification. Addition of a little limestone will usually suffice for the lowering the fusion temperatures. The fuel particles must be much smaller than for other types of gasifiers. This means the fuel must be pulverized, which requires somewhat more energy than for the other types of gasifiers. By far the most energy consumption related to entrained bed gasification is not the milling of the fuel but the production of oxygen used for the gasification. ==Applications of Gasification== Syngas can be used for heat production or for mechanical/electrical power generation. Like any other gaseous fuel, producer gas enables a good control over power levels when compared to solid fuels, paving the way for more efficient and cleaner operation. For thermal applications, gasifiers offer a flexible option, as they can be retrofitted with existing gas fueled devices such as ovens, furnaces, boilers, etc. where syngas may replace fossil fuels. [[Heating value]]s of syngas is generally around 4-10 MJ/m<sup>3</sup>. [[Diesel engine]]s can be operated on dual fuel mode using producer gas. Diesel substitution of over 80% at high loads and 70-80% under normal load variations can easily be achieved<ref>[http://www.kedco.com/ind/industrial/principles-of-gasification/ Gasification Appliances Review], 04.02.08</ref>. [[Spark ignition engine]]s and [[Solid oxide fuel cell|SOFC fuel cells]] can operate on 100% gasification gas<ref>[http://orbit.dtu.dk/getResource?recordId=209388&objectId=1&versionId=1 Characterization of biomass producer gas as fuel for stationary gas engines in combined heat and power production], Ph.D. Thesis by Jesper Ahrenfeldt, Technical University of Denmark March 2007</ref><ref>[http://www.biocellus.com/pdf/High_temperature_electrolyte.pdf High temperature electrolyte supported Ni-GDC/YSZ/LSM SOFC operation on two-stage Viking gasifier product gas], Ph. Hofmann et. al in Journal of Power Sources 173 (2007) 357–366</ref>. Mechanical energy from the engines may be used for e.g. driving water pumps for irrigation or for coupling with an alternator for electrical power generation. ==Waste disposal== [[Image:Reactor .jpg|right|thumbnail|150px|High Temperature Conversion of Waste (HTCW) reactor. One of many proposed gasification processes which are still to be proven in real life installments.<ref>[http://www.environment-agency.gov.uk/wtd/679004/679021/679065/980897/?lang=_e&lang=_e KBI Process Review], www.environment-agency.gov.uk/wtd, Retrieved 28.12.06</ref>]] Several gasification processes for thermal treatment of waste are under development as an alternative to [[incineration]]. Waste gasification has several principal advantages over incineration: * The necessary extensive flue gas cleaning may be performed on the syngas instead of the much larger volume of flue gas after combustion. * [[Electric power]] may be generated in [[internal combustion engine|engines]] and [[gas turbine]]s, which are much cheaper and more efficient than the [[Rankine cycle|steam cycle]] used in incineration. Even [[fuel cell]]s may potentially be used, but these have rather severe requirements regarding the purity of the gas. * Chemical processing of the syngas may produce other [[synthetic fuel]]s instead of electricity. * Some gasification processes treat ash containing heavy metals at very high temperatures so that it is released in a glassy and chemically stable form. A major challenge for waste gasification technologies is to reach an acceptable (positive) gross electric efficiency. The high efficiency of converting syngas to electric power is counteracted by significant power consumption in the waste preprocessing, the consumption of large amounts of pure oxygen (which is often used as gasification agent), and gas cleaning. Another challenge becoming apparent when implementing the processes in real life is to obtain long service intervals in the plants, so that it is not necessary to close down the plant every few months for cleaning the reactor. Several waste gasification processes have been proposed, but few have yet been built and tested, and only a handful have been implemented as plants processing real waste, and always in combination with fossil fuels<ref>[http://www.environment-agency.gov.uk/wtd/679004/679021/679065/ Gasification case studies] by the [[Environment Agency]] of England and Wales</ref>. One plant (in [[Chiba, Chiba|Chiba]], [[Japan]] using the Thermoselect process<ref>[http://www.thermoselect.com Thermoselect website] - a waste gasification plant supplier</ref>) has been processing industrial waste since year 2000, but has not yet documented positive net energy production from the process. == See also == {{EnergyPortal}} {{Portal|Sustainable development|Sustainable development.svg}} *[[Biofuel]] *[[FutureGen]] zero-emissions coal-fired power plant *[[Fluidized bed]] *[[Fluidized bed combustion]] *[[Isle of Wight gasification facility]] *[[List of solid waste treatment technologies]] *[[Plasma arc waste disposal]] *[[Renewable natural gas]] *[[Synthetic fuel]] ==External links== {{Wiktionary}} *[http://www.juniper.co.uk/services/Our_services/P&GFactsheet.html Pyrolysis and Gasification Factsheet] *[http://www.rsnz.org/topics/energy/ccmgmt.php#2 Carbon cycle management with increased photo-synthesis and long-term sinks], *[http://www.heatxfer.com Heat Transfer International Biomass Technology Experts] *[http://cgpl.iisc.ernet.in "Gasification Technology" Experts from CGPL, Indian Institute of Science] *[http://www.gasification.org "Gasification Technologies Council"] == References == <references/> [[Category:Chemical engineering]] [[Category:Energy conversion]] [[Category:Power station technology]] [[Category:Thermal treatment]] [[Category:Waste treatment technology]] [[Category:Unit processes]] [[Category:Fuel gas]] [[cs:Zplyňování]] [[da:Forgasning]] [[de:Kohlevergasung]] [[es:Gasógeno]] [[it:Gassificazione]] [[pl:Zgazowanie]] [[pt:gás de síntese]] [[ru:Газификация]] [[sv:Förgasning]] [[th:Gasification]] [[uk:Газифікація]]