In general, this invention belongs to the tobacco production and processing sector and more specifically it refers to the method of producing cut rag tobacco for cigarettes and other products from green tobacco leaves by the innovative integration of the GLT and Primary processes, with lower investment and operational production costs, while generating cut rag tobacco with high filling power while maintaining a flavor approximately equal to that of the original tobacco.
The worldwide tobacco industry, excluding China which alone represents nearly 42% of global tobacco production and consumption, has undergone significant change during the last 30 years. Brazil as the second largest green leaf producing country and single largest tobacco leaf exporting nation, represents well the general tendency seen worldwide, excluding China. From 1990 thru 2004, Brazil increased total green leaf tobacco production from approximately 300 million kilograms to nearly 700 million kilograms, of which flue cured Virginia tobacco represented 85 percent of the total; an overall increase of 133% in a 15 year time span. Brazilian tobacco production growth occurred partly as a result of significant reductions during that time period in the USA, Zimbabwe, and Europe. During the latest 15-year period, 2005 till 2020, Brazilian production has decreased from 700 to 500 million kilograms of green leaf tobacco; now nearly 90 percent flue cured Virginia tobacco. Total decrease during that 15-year period in Brazil has been nearly 30%; the rest of world tobacco production decreased approximately 20%, excluding China which reduced domestic green leaf production slightly, but also increased leaf tobacco imports to maintain domestic cigarette production relatively stable.
With projected worldwide conventional cigarette consumption continuing its decades long term tendency of annual consumption decrease of 2-3 percent, it is probable that the entire tobacco production global supply chain from farmers, to tobacco leaf processors (GLT) thru to cigarette manufacturers (including their Primaries and Secondaries); will continue their current trend of industry wide consolidation and overall reduction of conventional cigarette production and overall tobacco consumption. Successful companies to survive in this environment will have to either differentiate their products from the competition (which is difficult in a commodity type market such as tobacco); or more probably exert all efforts to be a low cost producer in their respective niche of the tobacco market.
In view of this overall worldwide situation, the invention herein described, contributes to the ability of the tobacco industry to reduce capital employed in tobacco production and industrial processes, reduce overall operating costs of cigarette production, maintain cigarette production quality standards at internationally acceptable standards, and contribute to the Sustainable Development Goals (SDG 9 “Industrial innovation and infrastructure” and SDG 12 “Responsible consumption and production”) as determined by the United Nations.
Therefore, some conventional terms to define tobacco processing and cigarette manufacturing are important to describe:
During the pre-industrial phase, farmers:
After packed in bales at the farmer location, the green tobacco in bundles or loose leaves are sent to a conventional GLT. Nearly all GLT processing worldwide currently of green tobacco is done similarly as in
Some patent documents illustrate the currently known process techniques:
In addition, a threshing plant (GLT) is a factory which receives the tobacco green leaves from the farmers and goes through the following steps:
The conventional tobacco Primary process receives the GLT lamina strips and stems for the following process:
The lamina bales move forward on a blending line, passing thru a slicer before entering the DCCC (Direct Conditioning and Casing Cylinder) where conditioning and casing process takes place according to different blends. The moistened tobacco next enters the lamina bin silos for storage and bulking. Optionally it can also go through the steam tunnel for additional conditioning. Then, the lamina goes to the cutters, generating cut rag. Optionally, you can also go through the steam tunnel for further conditioning and/or expansion before the dryer. After the lamina has been cut, it goes to the dryer to attain the required moisture, desired expansion and tobacco taste profile expected for each blend being dried. Optionally it can go to the cooler and/or objectionable stem removal (normally 1% maximum of dried lamina input). At the Primary lamina line add-back station, the dried cut rag lamina is combined with the dried cut rag stems (see B—stem line) coming from the stem silos and other tobacco products, such as Recon, DIET, Scraps. After passing thru (optional) shaker(s), product passes thru a final cut rag blend flavor cylinder. After receiving the flavor, the combined product is conveyed to the Final Product Silos (optional) for homogenization plus assurance of required moisture as per blend or to the last step, which is to send final cut rag blend to Secondary for cigarette manufacture, or press/pack the product in cardboard cases (with optional Polyliner bag). Product can be used as needed wherever in the world, ideally within 6 to 12 months from final packing date.
The stem cardboard cases are fed inside the tipper. It then goes to the washer for cleaning and the equipment for conditioning. Then the moistened stem tobacco enters the stem bin silos for storage and bulking, optional steam conditioning, and then sent to the cutters. After the stem has been cut, it goes to the dryer to attain the required moisture and desired expansion and then is stored in cut stem silos or other packaging to further add-back to the lamina cut rag.
The following characteristics differ from the conventional process and can operate individually or jointly between one or all:
In order for this invention to be fully understood and put into practice by any technician in this technological sector, it will be described in a clear, concise, and sufficient manner, based on the attached drawings listed below that illustrate and provide complementary information about it:
In general, the method illustrated with
Tobacco leaves coming from the farmers are cured, but not fermented, and normally have relative moisture approximately 18 to 19%.
“Fermented” tobacco is a specific, labor intensive process where the tobacco leaves are manipulated in piles, increasing the temperature and humidity levels, to achieve a distinct character different from green farmer kiln dried tobacco produced normally worldwide. It should be noted that the invention does not normally utilize “fermented” tobacco, but does not restrict the use.
The invention avoids three fundamental steps if compared to a conventional GLT (
The invention utilizes cured green tobacco coming directly from the farmers, with the following steps:
According to the invention, the combined tobacco lamina strips go then through the following steps:
The naked green stems, resulting from the threshing, can be dried in a drier and pressed/packed similar as in the conventional GLT process (
Several embodiments are described to support this invention, the first of which relates to leaf lamina performance. The process generates an improved better green strip lamina due to a special tipping setup, consisting preferably in 2 to 5 adjustable cutting knives, spaced approximately 1″ to 2″ (25 to 50 mm), which represents approximately 30-35% in total lamina weight for “Filler” and/or “Leaf”, generating more and larger leaf tip and strips fragments, by-passing the threshing sector. Therefore, only a reduced butt portion is threshed, resulting in better lamina overall total fragmentation.
The limit of the tipping cut will also help determine the quantity and width of threshing stages necessary for a certain throughput; however, up to approximately 20% reduction is possible. As an example, when compared to a conventional GLT (
The special tipping setup can generate the presence of objectionable stem pieces in the cut rag tobacco after the lamina cutter machines, which is detrimental to cigarette quality, resulting in rejection during production particularly on today's high-speed cigarette makers. To minimize this problem, an air separator(s) is introduced after the cut rag dryer (
Green stem processed and cut as per the invention (
The naked green stems, resulting from the threshing, can be dried in an apron drier and pressed/packed for future use in a conventional Primary (
The invention process avoids intermediate stems drying and pressing/packing. The naked green stems are first cut to be dried in sequence in a Rotary Dryer, giving a higher filling capacity stem as an additional advantage of the invention.
The final cut rag produced as a result of the invention allows today's typical individual King Size cigarette cut rag weights of 725 to 735 mg, to be reduced to levels of 675 to 700 mg when invention produced cut rag is included at a percentage of 20 to 40 percent of total blend; individual cigarette cut rag weights below 675 mg may be obtained by increasing invention produced cut rag lamina and stem to 41-100 percent of the total blend. Each cut rag blend and cigarette maker requires production trials to determine final optimization.
Finally, the product obtained utilizing the invention results in cigarettes with less cut tobacco weight per cigarette, uniform rod firmness with low incidence of loose ends, improved runnability and lower cigarette rejection rates for modern medium and high speed cigarette makers. Also equally important is that the cut rag tobacco produced utilizing the invention maintains original farmer cured green tobacco taste and aroma at levels at least equal to conventional GLT and Primary processes.
With the invention process, it is possible to reduce the conventional threshing lines capacities by up to two stages of the threshing line, or approximately 20% of a conventional GLT (
The method does not require a conventional 5-stage line, but allows the utilization of existing GLT and Primary equipment which can be rearranged with the elimination and/or substitution of steps and equipment in order to achieve the results of the invention process.
If a company already has a conventional GLT, it can be used to convey lamina strips from whatever stage separator (ideally after the 1st and 2nd stages) of the GLT directly to the casing cylinder of the Primary, when GLT and Primary are in the same site; or packed in cases when need to be transported to the Primary elsewhere or need to be blended with other grades at the Primary. This modality, however, must be in balance with this process and all its relevant embodiments.
This embodiment describes an alternative feature of the invention. The conversion or adaptation of a GLT or Primary processing lines, or any feature derived therefrom to achieve the results of the invention is part of this Patent.
The invention does not require specific types of equipment for threshing nor drying. The invention process can use vertical thresher/separator (VT), conventional horizontal thresher, Counterflow separator (CF), Multisep (MS), or a combination for threshing; and rotary dryer or flash dryer for drying lamina, and/or apron dryer or rotary dryer for stem, depending on end use. Even hand stripped tobacco can be used instead of mechanical threshing, followed by the subsequent steps outlined in the Patent.
The invention process allows existing and/or used equipment along with possible certain new equipment to be relocated and repositioned in order to achieve invention process results.
The theme of carbon credits or exchange in the carbon market is covered in the production concept of the invention, as it will reduce greenhouse gas emissions and, consequently, increase the amount of emissions available for sale, if it is below the limit, or will reduce the quantity of emission to buy if it is above the limit. This is only applicable in countries where it is legally required or possible.
The invention motivates changes in the economic production of cut tobacco for cigarettes by the effective reduction of electric power and fuel for steam generation due to elimination of double drying process, double pressing process and less threshing/separators and transports between stages.
The invention is adherent to the Sustainable Development Goals (SDG 9: “Industrial innovation and infrastructure” and SDG 12: “Responsible consumption and production”), also known as the Global Goals, adopted by all United Nations Member States in 2015 as an universal call to action to protect the planet by 2030, with special focus on environmental sustainability.
Considering the elimination of two industrial apron dryers for lamina and stem, we get an economy of steam and consequently of boiler fuel, whether of hydrocarbon, firewood, coal, electricity or other origin. To quantify the energy gain with elimination of the lamina and stem dryers at a conventional GLT, the following criteria can be used:
Therefore, the economy for a 10,000 kg tobacco line (8,000 kg lamina and 2,000 kg stem) will be 3,600 kg/h of steam for the lamina dryer and 700 kg/h of steam for the stem dryer in a total of 4,300 kg/h steam which represents an economy of approximately 2.9 cubic meters/h with wood logs (40% moisture/75% energy efficiency), or 290.6 kg/h of BPF oil (90% of energy efficiency). Considering that a conventional 10 ton/h GLT requires an average of 6,000 to 7,000 Kg/h of steam, the 4,300 Kg/h due the elimination of both lamina and stem apron dryers, correspond to 70 to 60% less steam with the invention.
Considering 1 shift of 8 hours, 22 days per month:
Regarding carbon credits, the absorption of carbon dioxide from the atmosphere by the growth of trees is made from the determination of the potential carbon stock of the species of tree and generates carbon credits due to the sequestration of greenhouse gases. According to Silva (1996) et al in the Embrapa publication (ISSN 1980-3958, August, 2011), the formula for estimating carbon stocks by reducing Eucalyptus biomass used for steam generation is: Content of C=(wood logs volume+25%)×(basic density 0.49)×(carbon content 0.42).
Considering that the reduction of wood consumption due the invention is 2.9 m3/h with wood logs or 510.4 cubic meters/month, the content of C=(510.4+127.6)×0.49×0.42=131.3 carbon stock/month operating in 1 shift, 8 hours/day, 22 days/month.
The invention removes several conventionally used steps that allow a significant reduction in equipment and energy savings:
Total Kw eliminated by the steps reduction: approximately 600 Kw, which represent 105,600 Kw/month, considering 1 shift of 8 hours, 22 days. Considering that a conventional threshing line for 8 to 10 ton/h capacity has an average of 1,500 Kw of electric energy consumption, this reduction represents an average of 40% less energy.
In the conventional process the tobacco leaves come from the farmers at about 18/19% (relative moisture) and in the final step of the process dry to 12.5% for packing. Consequently, is necessary to re-order from 12.5% back again to 23/24% for cutting, and then again reduce to 11-14%; for final cut blend; whereas in the invention process, the moisture gradient from green tobacco to cut tobacco is only from green tobacco (18/19%), to threshed and tipped lamina at the cutter (23/26%) to final cut tobacco (11/14%). This represents a reduction in steam requirement of 10% to 20%.
The direct connection between GLT and Primary (
The tipping setting together with the stem separation in the Primary, instead of in the GLT, allows only three stages compared with the conventional 5 stages lines for equivalent throughput, with an additional important energy savings. The invention uses horizontal multi-separators in the 1st and 2nd stages and a vertical separator as the 3rd and final stage. However, this 3rd stage could also be horizontal. The invention does not require specific types of equipment for threshing, and is able to use a vertical thresher/separator (VT), horizontal thresher, “Counterflow” (CF) type separators, Multi-separators (MS), or even hand stripping, or combinations. The basic difference is 3 stages versus 5 conventional ones and maintaining the same production by cutting tips increased with the removal of the stems from the tips in the Primary process.
The invention produced cut rag can be utilized not only as add-back in a conventional Primary process to be added to other blend components, but also dried and packed according to the invention concept (
Optionally, it can be fed directly to a cigarette maker in the Secondary (
This embodiment represents also the worldwide flexibility for integration of Primary and Secondary operations. The invention allows, among also others, the following options for cigarette making operations:
The invention process eliminates the duplication of the pressing and packaging steps as per conventional GLT and conventional Primary (
Regarding threshing capacity, the invention concept is more compact and economic than a conventional 5 stages threshing line. Total installed threshing capacity of the invention process compared to conventional GLT lines, can be approximately 20 percent less.
The invention tipping cut, which represents 30-35% in total lamina weight for Flue Cured “Filler” and/or for Flue Cured “Leaf”, result in a better lamina fragmentation. This concept allows a better lamina fragmentation even with only 2 or 3 threshing stages in comparison with the 5 stages lines.
The process generates more stem percentage processed thru the lamina cutter, compared to conventional Primary, which need to be removed by the utilization of an adequate stem separator, after the cut rag dryer.
The invention does not need the expensive apron driers used in the conventional GLT's for lamina strips. It also does not need the presses with high chargers and piston stroke necessary to handle the volume of the lamina strips after the apron dryer, common in conventional GLT.
If the cut rag from the final blending silo (
It is important to note that the figures and descriptions do not have the ability to limit the forms in which this invention may be executed, but rather to illustrate and make the conceptual innovations revealed in this solution understandable. Thus, the descriptions and images must be interpreted in an illustrative and non-limiting manner, and there may be other equivalent or similar ways of implementing this invention concept that do not escape the protection spectrum outlined in the proposed solution.
Number | Date | Country | |
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Parent | PCT/BR2020/050517 | Dec 2020 | US |
Child | 17805317 | US |