Patent Application
20140223810
The present invention relates to the field of torrefaction of biomass. In particular, it relates to a method and a system for efficient cooling of torrefied material which also increases energy yield and hydrophobicity of the torrefied product and decreases clogging of the cooling device.
To be able to compete with and replace fossil fuel energy carriers such as coal, oil and natural gas, lignocellulosic biomass would benefit from some form of pre-treatment method to overcome inherent drawbacks. The pre-treatment method torrefaction has been shown to improve biomass fuel qualities such as energy density, water content and milling, feeding and hydrophobic properties [1-4]. These improvements establish torrefaction as a key process in facilitating an expanding market for biomass raw materials. Torrefaction is a thermal pre-treatment method that normally takes place in a substantially inert (oxygen free) atmosphere at a temperature of about 220-600° C. During the process course a combustible gas comprising different organic compounds is produced from the biomass feedstock in addition to the torrefied biomass.
The process of producing a torrefied material from lignocellulosic biomass can be said to include four stages:
1) a drying step, wherein free water retained in the biomass is removed;
2) a heating step in which physically bound water is released and the temperature of the material is elevated to the desired torrefaction temperature;
3) a torrefaction stage, in which the material is actually torrified and which starts when the material temperature reaches about 220° C.-230° C. During this stage, the biomass partly decomposes and gives off different types of volatiles, such as hydroxy acetone, methanol, propanal, short carboxylic acids etc. In particular, the torrefaction stage is characterized by decomposition of hemicellulose at temperatures from 220° C.-230° C., and at higher torrefaction temperatures cellulose and lignin also starts to decompose and give off volatiles; cellulose decomposes at a temperature of 305-375° C. and lignin gradually decomposes over a temperature range of 250-500° C.;
4) a cooling step to terminate the process and facilitate handling. The torrefaction process is terminated as soon as the material is cooled below 220° C.-230° C.
During the cooling process of torrefied material, the material continues to release gases until the temperature of the material is decreased below about 200° C. However, the material need to be further cooled to below 130° C. to ensure safe self ignition temperatures. Therefore, in the prior art, torrefied material have been directly cooled in a cooling device such as a screw cooler to decrease the temperature to below 130° C., see e.g. WO2009/151367 A1. One problem with this approach is that the gases given off from the torrefied material during the cooling process will condense on cold surfaces within the cooling device leading to fouling or clogging of said device. Another problem with the cooling processes of torrefied material described in the prior art is that the gases given of during the cooling process leads to a decrease in energy yield of the torrefied product. There is thus a demand for an improved method for cooling torrefied material.
The present inventors have solved the problems described above by a method for cooling torrefied material. Said method includes that at least a part of cooled torrefied material is mixed-back with hot torrefied material before the hot material is introduced into a cooling device for further cooling of the torrefied material. This method has several advantages compared to the methods described in the prior art:
Accordingly the present invention relates to a torrefaction method, comprising the steps of:
a) subjecting an optionally pretreated biomass to torrefaction to produce a torrefied material and torrefaction gases;
b) cooling and optionally pelletizing the torrefied material from step a);
c) mixing at least part of the material from step b) with at least part of the torrefaction gases and/or torrefied material from step a) such that torrefaction gas components condense on the material from step b).
Another aspect of the invention relates to a torrefaction system, comprising:
a torrefaction reactor for converting an optionally pretreated biomass to a torrefied material and torrefaction gases;
an arrangement comprising means for cooling and optionally pelletizing the torrefied material, said arrangement comprising an inlet connected to an outlet of the torrefaction reactor;
a mixing zone for mixing the torrefaction gases and/or torrefied material from the torrefaction reactor with material from said arrangement such that torrefaction gas components may condense on the material from said arrangement, wherein the mixing zone is connected to an outlet of said arrangement via means for material transport.
a and 2b show two different torrefaction reactors.
A thermal pre-treatment method that takes place in a virtually inert (oxygen-reduced or oxygen free) atmosphere at a temperature above 220° C. but below 600° C. and which produces a torrefied biomass and combustional gases. During a torrefaction stage, parts of the biomass, in particular hemicellulose, decompose and give off different types of organic volatiles. In a torrefaction process starting from raw biomass, the actual torrefaction stage is preceded by a drying stage wherein free water retained in the biomass is removed and by a heating stage wherein the biomass is heated to the desired torrefaction temperature.
A specific region of a compartment in a torrefaction reactor, located upstream of a torrefaction zone in relation to a biomass inlet of a torrefaction reactor, comprising means for specifically regulating the temperature in said specific region and wherein the temperature of a biomass is increased to a temperature near the desired torrefaction temperature prior to torrefaction.
A specific region of a compartment in a torrefaction reactor, located downstream of a heating zone in relation to a biomass inlet of a torrefaction reactor, comprising means for specifically regulating the temperature in said specific region and wherein the temperature of a previously heated biomass is kept virtually constant at the desired torrefaction temperature for a desired torrefaction time wherein a desired torrefaction temperature is in a range between 220° C. to 600° C.
A specific region of a compartment in a torrefaction reactor, located upstream of a heating zone in relation to a biomass inlet of a torrefaction reactor, comprising means for regulating the temperature in said specific region and wherein a biomass is dried to a water content below 10% prior to heating.
A specific region in a torrefaction reactor located immediately upstream of a heating zone and immediately downstream of a torrefaction zone in relation to a biomass inlet of said torrefaction reactor.
The time the temperature of the material is kept virtually constant at the torrefaction temperature. The residence time of the material in the torrefaction zone may be referred to as the torrefaction time.
In a first aspect the invention relates to a torrefaction method, comprising the steps of:
In one embodiment step b) comprises transportation of the torrefied material through a cooling device. Said cooling device could be a drum and the transportation within said drum could be mediated by means of a screw. In one embodiment the drum is cooled by means for cooling wherein the means for cooling could be heat exchangers. In another embodiment the screw is cooled. In a preferred embodiment the cooling device is a screw cooler. In another embodiment the cooling device comprises a water application device for applying water to the torrefied material. In one embodiment the temperature of the material from step b) is less than 100° C. The torrefied material which has been cooled with the back-mixed (re-circulated) material may be transported through the cooling device together with the backmixed material such that torrefaction gas components can condense on the backmixed material, particularly during the mixing but also in the cooling device. In one embodiment torrefaction gases can also be sucked in to the cooling device together with the torrefied material and cold pellets. If torrefaction gases is sucked in to the cooling device it may be preferred to direct the gases from the cooling device out from the cooling device at a position upstream of an outlet for the torrefied product so that gases having a relatively high content of condensable components can be used for combustion. In other cases it is important to get a product with high hydrophobicity and hence the gases should be diverted from the cooling device later. Therefore, according to one embodiment the cooling device comprise a cooling device gas outlet upstream of an outlet for the torrefied material. The gas outlet may for example be moveable along the cooling device so that the position of the gas outlet can be adjusted. According to another embodiment the torrefaction gases are diverted out of the system for cooling a torrefied material after the mixing zone but prior to the cooling device in order to minimize clogging of the cooling device. In one embodiment the temperature of the diverted gas is adjusted by controlling the amount of cooled torrefied material supplied in the mixing zone. By adjusting the temperature it is for example possible to save organic acids in the gas while tar components condense on the material.
There is a high demand for pellets of torrefied material on the market. The inventors have however found that it is particularly difficult to produce pellets of torrefied material having a sufficient hydrophobicity. This is probably due to the fact that the torrefied material is disintegrated (e.g. refined or ground) in the pelletizing process, such that the hydrophobic surface of the torrefied material is broken down and the interior of individual pieces of torrefied material is exposed. But if the pellets are mixed with torrefied material from the torrefaction reactor such that torrefaction gases condense on the surfaces of the pellets, the hydrophobicity of the whole pellets is increased. Thus, in one embodiment the torrefied material is pelletized in step b) and mixed with the torrefied material from step a) in step c) and then separated from the torrefied material. The pelletized material may for example be separated from the torrefied material by means of a sieve, for example a sieve of mesh or by wind sieving. That is, the separation may be based on size as the pellets are normally smaller than the pieces of torrefied material, in particular when they are derived from wood chips. The separation may also be based on density.
In one embodiment the biomass is dried and optionally heated prior to step a) to generate gases which are not mixed with the torrefaction gases before or in step b). In this way, the humidity of the torrefaction gases may be decreased such that they may be combusted efficiently even though some of their organic material have condensed on the back-mixed material.
In one embodiment the biomass is lignocellulosic biomass, and in a preferred embodiment the biomass is a wood material, such as wood chips.
Generally, the pellets mentioned in the present disclosure can be replaced by other compacted materials such as briquettes. Similarly the pelletizing mentioned in the present disclosure can generally be replaced by other methods of compacting biomass or solid fuels, such as briquette production. Another aspect of the invention relates to a torrefaction system, comprising:
a torrefaction reactor for converting an optionally pretreated biomass to a torrefied material and torrefaction gases;
an arrangement comprising means for cooling and optionally means for pelletizing the torrefied material, said arrangement comprising an inlet connected to an outlet of the torrefaction reactor;
a mixing zone for mixing the torrefaction gases and/or torrefied material from the torrefaction reactor with material from said arrangement such that torrefaction gas components may condense on the material from said arrangement, wherein the mixing zone is connected to an outlet of said arrangement via means for material transport.
In one embodiment the mixing zone is arranged in the connection between the outlet of the torrefaction reactor and the inlet of the arrangement.
When the arrangement comprises means for pelletizing the torrefied material, said system may for example further comprisea device for separating pellets from torrefied material. In one embodiment the separating device is arranged in the arrangement upstream of the means for pelletizing the torrefied material. Also, it may be arranged downstream of the means for cooling the torrefied material. Thus, the back-mixed material and the torrefied material from the torrefaction reactor may be transported through the means for cooling together, In one embodiment the separating device is a sieve or a mesh. In one embodiment the biomass is lignocellulosic biomass and in a preferred embodiment the biomass is wood such as wood chips.
a shows a system for cooling a torrefied material (1), comprising a torrefaction reactor (2) for converting biomass to a torrefied material having a temperature of above 220° C. and torrefaction gases. In connection to an outlet of the torrefaction reactor (2), a mixing zone (3) for mixing cold pellets of torrefied material with hot torrefied biomass from the torrefaction reactor is arranged. The torrefied material that has passed the mixing zone (3) is fed together with the cold pellets into a cooling device (4) for further cooling the torrefied material. Torrefaction gases can also be sucked in to the mixing zone and/or into the cooling device (4) together with the torrefied material and cold pellets. Components of said torrefaction gases, as well as components of gases given of from the torrefied biomass, will condensate on the cooled pellets, which increases the hydrophobicity and energy yield of the pellets and decreases condensation on the interior surfaces of the cooling device (4), which thus reduces clogging of the cooling device (4). The transport of the torrefied material in the cooling device (4) is mediated by the rotation of a screw cooler. The cooled torrefied material exits the cooling device (4) and pellets are separated from the torrefied biomass in a separating device (5) wherein the pellets exits the system for cooling a torrefied material (1) through a first pellet outlet (8). The cooled torrefied biomass is fed into a pelletizer (6) where it is pelletized into pellets. At least part of these pellets are fed back to the mixing zone (3), via means for pellets transport (7), where the pellets are used to cool hot torrefied material from the torrefaction reactor (2). Optionally, part of the pellets from the pelletizer are not fed back to mixing zone. Instead, they may be recovered from a second pellets outlet (9).
The skilled person understands that the pelletizer (6), the separating device and the first pellets outlet (8) can be taken out of the system such that, instead, one part of the cooled torrefied material from the cooling device (4) is fed back via the means for transport (7) and another part of the cooled torrefied material is recovered through the pellets outlet (9).
a shows a torrefaction reactor having a biomass inlet (21) wherein the biomass is introduced in the torrefaction reactor by means of a feeding screw (22). The biomass is dried in a drying zone (23)) wherein heat is supplied to the drying zone (23) by means of a heating media (e.g. hot gases) through a drying zone heating media inlet (24) and wherein the heating media leaves the drying zone through the drying zone heating media outlet (25). Dried biomass is transported through the drying zone (23) at a speed regulated by the feeding speed in the biomass inlet (21) and enters the heating zone (26) where the temperature of the biomass is elevated to a temperature near the desired torrefaction temperature. The heat is supplied to the heating zone (26) by means of a heating media through a heating zone heating media inlet (27) which leaves the heating zone through a heating zone heating media outlet (28). The heated material enters a first torrefaction zone (29) in which the temperature can be controlled by introducing heating media and/or cooling media in the first torrefaction zone heating/cooling media inlet (30) wherein said heating/cooling media exits the first torrefaction zone through the torrefaction zone heating/cooling media outlets (31). The biomass thereafter enters a second torrefaction zone (32) heating/cooling media can be supplied to the second torrefaction zone via the torrefaction zone cooling media inlet (33) and said heating/cooling media exits the torrefaction zone via a torrefaction zone cooling media outlet (34). The material transport in the heating zone (26) and torrefaction zones (29, 32) is driven by a common transport screw which is attached to a drum enclosing the heating zone (26) and torrefaction zones (29, 32).
b shows a torrefaction reactor having a biomass inlet (21) wherein the biomass is introduced in the torrefaction reactor by means of a feeding screw (22). The biomass is dried in a drying zone (23) wherein heat is supplied to the drying zone (23) by means of a heating media (e.g. hot gases) through a drying zone heating media inlet (24) and wherein the heating media leaves the drying zone through the drying zone heating media outlet (25). Dried biomass is transported through the drying zone (23) at a speed regulated by the feeding speed in the biomass inlet (21) and enter the heating zone (26) where the temperature of the biomass is elevated to a temperature near the desired torrefaction temperature. The heat is supplied to the heating zone (26) by means of a heating media through a heating zone heating media inlet (27) which leaves the heating zone through a heating zone heating media outlet (28). The transport of the biomass in the heating zone (26) is mediated by a heating zone transport screw which is fixed to the inner wall of a drum enclosing the heating zone (26). The material transport in the heating zone is controlled by the rotational speed of said drum and the biomass exits the heating zone through a connecting zone and enters a first torrefaction zone (29) and thereafter a second torrefaction zone (32). The temperature in the torrefaction zone can be controlled by introducing heating media and/or cooling media in the torrefaction zone heating/cooling media inlets (30, 33) wherein said heating/cooling media exits the torrefaction zone through the torrefaction zone heating/cooling media outlets (31, 34). The biomass transport in the first torrefaction zone (29) and second torrefaction zone (32) is driven by a common transport screw which is attached to a drum enclosing the first torrefaction zone (29) and second torrefaction zone (32). The material transport in the torrefaction zones (29, 32) is controlled by rotational speed of said drum can be rotated independently of the drum enclosing the heating zone. Hence the material transport in the torrefaction zone can be controlled independently of the material transport in the heating zone.
| Number | Date | Country | Kind |
|---|---|---|---|
| 1150467-8 | May 2011 | SE | national |
| Filing Document | Filing Date | Country | Kind | 371c Date |
|---|---|---|---|---|
| PCT/SE2012/050526 | 5/16/2012 | WO | 00 | 2/3/2014 |
