Patent Application
20210207046
The disclosure broadly relates to renewable electricity, and more particularly, to a method and system for managing solids flow in a gasifier, specifically fixed bed gasifiers such as downdraft, updraft or crossdraft gasifiers, by automatic equipment.
Gasification can convert carbon-containing materials to useful chemical products. These chemical products typically involve synthesis gas (syngas), which can be combusted to produce electricity, or chemically reacted to produce oxygenates or hydrocarbons in catalytic systems. The most common form of gasification in large scale industry is coal gasification, which is practiced on a worldwide basis, most notably by electricity producing power plants. Coal is delivered via gravity methods or via a slurry, and solids flow is not an issue at large scales. On the other hand, gasification using biomass is desirable from the point of view of decreasing greenhouse emissions, as biomass use is essentially a carbon neutral process. Biomass use also reduces a country's dependence on fossil fuels. Due to its portability and widespread availability, biomass is used extensively in small scale gasification systems. As an example, biomass gasification was practiced extensively during World War II in automobiles and trucks. The most common method for managing the flow of biomass through gasification systems utilizes gravity drop equipment. Major challenges with biomass flow in gasifiers include removing bridging within the gasifier, along with the need to manually shake and jiggle the biomass within the gasifier to remove jams. The clearing often necessitates stopping the gasifier, incurring a double cost of lost production and labor costs for the personnel tasked with the clearing.
Prior art methods for managing solids flow in gasifier include a rotatable grate feature in U.S. Pat. No. 5,192,514 issued to Sasol, Inc. applicable to a fixed bed coal gasifier. In this gasifier configuration, coal flow is controlled via a coal lock. A rotatable grate mechanism at the bottom of the gasifier is rotatable about the vertical axis of the ash discharge outlet and includes at least one upwardly projecting finger or disturbing formation to disturb the ash bed formed in use above and around the rotatable grate, when the rotatable grate is rotated.
U.S. Pat. No. 5,230,716 issued to US Department of Energy discloses a rotating conical grate assembly which crushes agglomerates of clinkers at the bottom of a fixed bed gasifier by pinching them between stationary bars and angled bars on the surface of the rotating conical assembly. U.S. Pat. No. 4,764,184 teaches a rotating grate with scraping blades. U.S. Pat. No. 4,652,342 teaches a motor driven anti-bridging mechanical agitator having a crankshaft. The agitator is comprised of pushrods having scoop arms, the pushrods are driven in a reciprocating manner upwards and downwards via the crankshaft. U.S. Pat. No. 4,134,738 discloses a poking system comprising a retractable pokerod assembly used to agitate a coal bed and having means for temperature sensing clinker formation, and position sensing relative to the housing which are used to determine the frequency and extent of the actuation of the pokerod assembly. U.S. Pat. No. 4,853,992 discloses a biomass gasifier which uses a rotatable grate in conjunction with stationary bars above the grate to shear large charcoal particles so that they may be channeled through the grate.
Bridging can be a more significant issue in biomass gasifiers than in those operating with coal. Biomass undergoes significant changes in particle size and density as it traverses a gasifier, transforming to materials possessing different physical properties and different flow characteristics in the distinct drying, pyrolysis, combustion, and gasification zones. Excessive tar buildup can also lead to a coating on the biomass which acts as an effective bridge between biomass particles. When this coating precipitously reaches the combustion zone, a rapid highly exothermic event can occur which destroys the zone architecture. In gasifiers that are run in conjunction with an engine, bridging can have deleterious effects on engine operation if synthesis gas is not supplied at a constant rate.
Embodiments of the present disclosure are directed toward methods for preventing biomass and charcoal bridging by automating solid flow of feed material and gasification products in a fixed bed gasifier. These methods are applicable to a wide range of biomass materials and wide range of moisture levels. Constant feed rate through the gasifier is desired without logjams or congestion points. Processes are provided for clearing logjams and congestion as input biomass is converted to char or ash in vertical column gasifiers. Some methods use aliquot metering of biomass regulated by feedback from sensors that monitor the extent of combustion of biomass in the gasifier. Other methods use processes to disturb solids in a radial direction without significantly disturbing the solids in the vertical direction. These methods destroy bridging without mixing combustible material with hot char. Other methods rely on shocks to shake material to assure continued movement. In some embodiments, this shock method is linked to a grate rotation to dislodge bridge particles. Still other methods use size selectivity of material as the material is reduced in size through the various stages of the gasifier, resulting in a uniform or semi-uniform product flow. Additional agitation methods also include methods for vibrationally exciting the gasifier walls and the material within.
A specific implementation of these various methods is disclosed. Aliquot distribution is implemented via intake augers that receive feedback from optical sensors and outtake augers that remove material once it is fully processed. The radial mixing without vertical displacement method is implemented via a shaft that is attached an auger having a large void volume and which is inserted into the reduction regime to radially mix the material in this region. Size selectivity is implemented via an adjustable grate assembly that varies its opening depending on particle size and interactively responds to solids flow through the gasifier. This is useful particularly for passing through certain types of particles, such as biochar particles. The implementation of shock-induced displacement method relies on a rotatable grate assembly that is actuated by hammer-like impacts that impinge on the grate assembly. Vibration excitation of gasifier walls is achieved via a vibrating motor attached to the gasifier walls. In some embodiments, the gasifier is selected from downdraft, updraft or co-current gasifiers.
The full nature of the advantages of the disclosure will become more evident from the following detailed description.
Certain embodiments of the present disclosure will hereinafter be described in detail, by way of example only, with reference to the accompanying drawings, in which:
The figures are not intended to be exhaustive or to limit the disclosure to the precise form disclosed. It should be understood that the disclosure can be practiced with modification and alteration, and that the disclosure be limited only by the claims and the equivalents thereof.
In the following paragraphs, embodiments of the present disclosure will be described in detail by way of example with reference to the attached drawings. Throughout this description, the preferred embodiment and examples shown should be considered as exemplars, rather than as limitations on the present disclosure. As used herein, the “present disclosure” refers to any one of the embodiments of the disclosure described herein, and any equivalents. Furthermore, reference to various feature(s) of the “present disclosure” throughout this document does not mean that all claimed embodiments or methods must include the referenced feature(s).
Embodiments of the disclosure utilize various processes and agitation methods for facilitating the flow of solids through a gasifier.
The raw form input is a biomass input, a term for the biodegradable fraction of agricultural products, residual or not, forestry products, industrial or municipal solid waste. Biomass generally refers to material originating from plant matter, in particular material containing cellulose, hemicellulose, lignins, lignocellulosic polymers, and extractives as composition. Forest products refers may refer to forest residue, wood pellets, wood shavings, bark, peat, waste wood, energy crops, virgin wood, recycled wood, sludge, sawdust, wood chips, as well as as black liquor and other products derived from pulp and paper operations. Biomass may also refer to herbaceous material such as Miscanthus, rice husk, straw, and and Sorghum as well as waste edible materials such as seeds and grains. Biomass may also refer to animal derived products such as manure. The term may also be used for a mixture of one or more of the above.
As the input material flows through a gasifier, it experiences several processes, including drying, pyrolysis, partial combustion and, finally, char gasification. At each of these stages, material properties change, either as density changes or chemical transformations, and there is a consequent need to process material of differing properties. Conventional methods primarily use gravity to direct material flow with no direct intervention or intervention methods that are quite different from those described herein. The active approach of the present disclosure as shown in
An implementation of these methods in a gasifier system is shown in
As the gasification process proceeds several zones of drying, pyrolysis, partial combustion and gasification are established. Agitation device 238 implementing method 25 is actuated by assembly 215 and is used to radially mix the gasification zone without disturbing the biomass, pyrolysis, or combustion zones. Agitation device 238 comprises a retractable shaft welded to an auger with large void volume. As material is gasified, it builds up a layer of char and ash. Depending on extent of gasification, material passes through displaceable grate assembly 250, which is an implementation of method 35. An agitation device 240 implementing method 45 is attached to grate assembly 250 and enables the transmission of hammer like impacts upon gasifier walls. This agitation device is linked to grate assembly 250 and enables grate rotation. Material exits through outflow assembly 260 which incorporates one or two gate valves and also implements aliquot method 15. The components of this implementation by reference of the particular method represented will now be described.
Aliquot distribution method 15 comprises dispensing and removing metered amounts of material from the gasifier. Input biomass is dispensed into the gasifier using feedback from sensors indicating fill level in the gasifier. Material is removed from a reservoir container system and deposited into the gasifier by various techniques, such as auger or belt transport, based on sensor input identifying a need for more material. The reservoir system stores a volume of material that is significantly more than the amount of material in the gasifier at any one time. The advantage of this method is that it decouples the solids flow inside the gasifier from the input or output flow. An implementation of this method is shown in
Referring to
The radial mixing without vertical displacement method 25 exerts minimal disturbance of the drying, pyrolysis, and combustion zones, while effecting radial mixing in the reduction zone. This is important for preventing premature mixing of the zones, as such a mixture can result in an explosive event. In a typical auger drilling operation, the rotation of the blade causes material to be removed out of the hole being drilled. In a gasifier with multiple zones, this simple drilling, while destroying bridging, would result upon retraction of the auger in a conduit which would allow hot gases to escape to the feed zone, leading to premature combustion. By contrast, the disclosed method destroys bridging without destroying gasifier performance. The method is implemented by agitation device 238 which comprises guide tube 425, solid shaft 428, and flattened wire 427 which spirals around solid shaft 428. Shaft 428 is attached or welded to wire 427 only at select shaft protrusions, leaving significant void space between the shaft and the wire. This void space enables the assembly to be retracted without removing material or intermixing material between each zone. The void space also allows material to be radially mixed whenever the shaft rotates, thereby breaking the tar interface causing crusting. The two extremes of position for the retractable assembly are shown in
The solids flow method 35 uses particle size discrimination in processing material through the gasifier. This method selectively passes particles of a size or structure, such as ash or char particles, through an adjustable grate assembly and deters large size particles from passing through. The particle discrimination can be effected via different ways, such as a variable sieve assembly, a variable grate assembly, or other means able to control orifice dimensions for material exiting the gasifier. This particle discrimination allows control of material residence in the reduction zone, and can be used to control the ratio of carbonaceous material to syngas production. An implementation of this method is embodied in the variable grate assembly shown in
The shock-prompted agitation method 45 is another method to break bridging that relies on hammer-like impacts to dislodge particles. An implementation of this method is illustrated in
An additional method which can be used in conjunction with the present disclosure is vibrational excitation of gasifier walls. This method is implemented, as shown in
Material exiting the grate assembly drops onto exit auger assembly 260 which conveys the char or ash particles out of the gasifier. Generally, as shown in
Another embodiment illustrating these principles is shown in
Data from the pressure sensors is fed to processor 1030 which can send signals to activate adjustable agitation device 1120 and/or activate the adjustable intake auger 1110. The agitation device has typically a duty cycle of 2-3 seconds on, and % min to 1 min in the off position. Typically a pressure differential preferentially less than 30-40 inches of water between pressure sensors 1061 and 1062 indicates a proper biomass and biochar flow rate without jamming. If the pressure differential is more than these values, the processor sends a signal to vibrate the agitation device until the pressure differential returns to normal range.
This pressure differential within the system may be maintained with either positive or negative pressure on the gasifier system. An embodiment of a negative pressure system 1400 is shown in
Yet another embodiment illustrating these principles is shown in
Data from the pressure sensors is fed to processor 1330, which can send signals to activate either adjustable agitation device 1420 and/or activate the adjustable intake auger 1410 and/or activate the adjustable air intake 1310. The agitation device typically has a duty cycle of 2-3 seconds on, and ½ min to 1 min in the off position. Typically a pressure differential preferentially less than 30-40 inches of water between pressure sensors 1361 and 1362 indicates a proper biomass and biochar flow rate without jamming. If the pressure differential is more than these values, the processor sends a signal to vibrate the agitation device until the pressure differential returns to normal range.
This pressure differential within the system may be maintained with either positive or negative pressure on the gasifier system. An embodiment of a negative pressure system 1700 is shown in
The present disclosure allows fast start-up with consequent hydrogen production.
One skilled in the art will appreciate that the present disclosure can be practiced by other than the various embodiments and preferred embodiments, which are presented in this description for purposes of illustration and not of limitation, and the present disclosure is limited only by the claims that follow. It is noted that equivalents for the particular embodiments discussed in this description may practice the disclosure as well.
While various embodiments of the present disclosure have been described above, it should be understood that they have been presented by way of example only, and not of limitation. Likewise, the various diagrams may depict an example architectural or other configuration for the disclosure, which is done to aid in understanding the features and functionality that may be included in the disclosure. The disclosure is not restricted to the illustrated example architectures or configurations, but the desired features may be implemented using a variety of alternative architectures and configurations. Indeed, it will be apparent to one of skill in the art how alternative functional, logical or physical partitioning and configurations may be implemented to implement the desired features of the present disclosure. Also, a multitude of different constituent module names other than those depicted herein may be applied to the various partitions. Additionally, with regard to flow diagrams, operational descriptions and method claims, the order in which the steps are presented herein shall not mandate that various embodiments be implemented to perform the recited functionality in the same order unless the context dictates otherwise.
Although the disclosure is described above in terms of various exemplary embodiments and implementations, it should be understood that the various features, aspects and functionality described in one or more of the individual embodiments are not limited in their applicability to the particular embodiment with which they are described, but instead may be applied, alone or in various combinations, to one or more of the other embodiments of the disclosure, whether or not such embodiments are described and whether or not such features are presented as being a part of a described embodiment. Thus the breadth and scope of the present disclosure should not be limited by any of the above-described exemplary embodiments.
Terms and phrases used in this document, and variations thereof, unless otherwise expressly stated, should be construed as open ended as opposed to limiting. As examples of the foregoing: the term “including” should be read as meaning “including, without limitation” or the like; the term “example” is used to provide exemplary instances of the item in discussion, not an exhaustive or limiting list thereof; the terms “a” or “an” should be read as meaning “at least one,” “one or more” or the like; and adjectives such as “conventional,” “traditional,” “normal,” “standard,” “known” and terms of similar meaning should not be construed as limiting the item described to a given time period or to an item available as of a given time, but instead should be read to encompass conventional, traditional, normal, or standard technologies that may be available or known now or at any time in the future. Likewise, where this document refers to technologies that would be apparent or known to one of ordinary skill in the art, such technologies encompass those apparent or known to the skilled artisan now or at any time in the future.
A group of items linked with the conjunction “and” should not be read as requiring that each and every one of those items be present in the grouping, but rather should be read as “and/or” unless expressly stated otherwise. Similarly, a group of items linked with the conjunction “or” should not be read as requiring mutual exclusivity among that group, but rather should also be read as “and/or” unless expressly stated otherwise. Furthermore, although items, elements or components of the disclosure may be described or claimed in the singular, the plural is contemplated to be within the scope thereof unless limitation to the singular is explicitly stated.
The presence of broadening words and phrases such as “one or more,” “at least,” “but not limited to” or other like phrases in some instances shall not be read to mean that the narrower case is intended or required in instances where such broadening phrases may be absent. The use of the term “module” does not imply that the components or functionality described or claimed as part of the module are all configured in a common package. Indeed, any or all of the various components of a module, whether control logic or other components, may be combined in a single package or separately maintained and may further be distributed across multiple locations.
Additionally, the various embodiments set forth herein are described in terms of exemplary block diagrams, flow charts and other illustrations. As will become apparent to one of ordinary skill in the art after reading this document, the illustrated embodiments and their various alternatives may be implemented without confinement to the illustrated examples. For example, block diagrams and their accompanying description should not be construed as mandating a particular architecture or configuration.
This application claims priority to U.S. Provisional Patent Application No. 62/958,245 filed on Jan. 7, 2020, the content of which is incorporated herein by reference in its entirety.
| Number | Date | Country | |
|---|---|---|---|
| 62958245 | Jan 2020 | US |
