In Brazil, most of the charcoal production, around 70% comes from the traditional charcoal kilns of
brick kilns, said “rabo-quente furnace.” These furnaces have a low percentage yield by weight in the conversion of
biomass into charcoal and have high long production cycles.
In the traditional process for producing coal in brick kilns type “Rabo-quente “, wood and coal are respectively loaded and unloaded manually, subjecting the furnace operator to severe and harsh working conditions.
In addition, generated gases in the carbonization process are released into the
atmosphere without any control and / or use, resulting in a significant energy waste.
The released gases by these furnaces still harm the operators
working environment, as the
smoke released when in contact with eyes and mucous membranes cause
irritation and may also contain toxic substances.
This
system, although it has been proposed to solve the problems mentioned above, such as shorter carbonization time and improve
process control and improve working conditions for workers, not completely cover all energy, environmental and operational issues.
Furthermore, the system is equipped with only one control valve, which for small volumes can be acceptable, but for industrial furnaces of large volume, such as on the proposal of this invention are not effective, being necessary the
process control in several points of the furnace.
Although the PI 0506224-1 document deals with the Container furnace functionality as a gasifier, is not offered a definitive solution to the production of large scale charcoal, since the charcoal yield in a carbonization furnace which operates as a gasifier is low compared to the traditional process.
However, it still does not present complete solutions for environmental
mechanization,
automation and optimization,
energetics and operational, which will be demonstrated in this application.
Furthermore, the document does not disclose a proposal to solve the rapid or instantaneous unloading the furnace.
However, in the course of development of this research, technically, the addition of two or more exhaust points leads to the need for greater control over the process due to different carbonization fronts formed.
In addition, ignition points at different positions in height and circumference of the furnace lead to unsafe operation because gases generated by one of the carbonization fronts may come into contact with the produced
flame / coal by another front.
In addition, this system does not propose a global solution, that make it viable, technically, economically, environmentally and energetically the operation of an industrial
plant for production of charcoal.
In summary, the presented solution tries to solve the problems inherent to industrial process of charcoal production, but it fails when again it back using the furnace, dimensioned object and designed to withstand the high temperatures, to promote cooling.
Again this solution still does not show a global innovation as the optimization and energetic efficiency, environmentally and operationally of the process for nullifying the exclusive use of the furnace for the carbonization process, for not presenting detailed solutions of
mechanization,
automation and control.
Another flaw presented in the process concerns the proposals for loading and unloading the furnace.
“Topple” the furnace, in other words, remove it from the vertical position and rotate it to landscape, results in a complicated process, especially when working with
large capacity furnaces (up to 30 m3 of
usable volume).
The needed equipment to carry out these operations are costly, decharacterizing the industrial application of this type of loading / unloading for an
industrial furnace.
Another aspect to be considered refers to the
sizing of the furnace, which should have structural reinforcements to meet the proposed charging, resulting in an increase in design cost.
Thus, not only the control strategy becomes more troublesome, but there is great potential for the occurrence of problems such as condensation, incrustation and obstruction because of the condensable gases arising from coal production, such as
tar and pyroligneous.
As in the same reactor simultaneously occurs
pyrolysis, cooling and
drying, there is not possibility to build a tank that specifically meets each of these steps.
One possibility would be a gasometer for gases storage that will be circulated, but due to the presence of condensables, this idea can not be as viable as simple
combustion of an initial amount of wood.
The processes shown in the present
state of art, therefore, flaws in their design and conception and they do not offer complete solutions to the problem of industrial production of charcoal.
All constructions use the furnace for the production of charcoal as a container for promoting coal cooling and there is not a solution comprising technical, economic, energetic and environmental viability simultaneously.
Masonry furnaces for the production of charcoal have as a major drawback the fact that their high time for converting biomass into charcoal, as mentioned above, between 12 and 14 days.
This high time is partly due to bad distribution of gas flow inside the furnace.
Coupled with the absence of proper control of temperature and
oxygen supply, in the “rabo quente” furnace there are presence of cracks and holes in the masonry wall that result in frequent explosions and collapse of the furnaces, with consequent financial loss.