Grupo Lwart Lwart Lubrificantes Lwarcel Fibras Especiais Lwart Química

Industrial Process




Preparation of the raw material

The process of pulp production begins with the handling of the raw material which occurs in the wood yard, where the logs are received from the forest with the bark removed. The logs are taken to a storage yard or directly to the chipper according to a pre-determined sequence.

The logs are unloaded onto feeding tables, washed, and carried by conveyors to the chipper. A 12-blade rotating disc transforms the logs in a few seconds into small chips, which are deposited on a chip yard.

Chipping is carried out with a view toward the ideal chip size for the cooking stage. Separation of the chips by size occurs on a vibrating sifter before they enter the contnuous digester’s chip silo. Chips not meeting specifications are removed, to be utilized as fuel for the biomass vessel.

Chips within specifications are transported to the continuous digester’s chip silo on conveyors with metal detection systems to avoid damage.

 




Cooking

In this stage, the objective is to dissolve any lignin present between the wood fibers. These fibers are the actual cellulose pulp.

The wood chips are submitted to chemical action with white liquor (sodium hydroxide plus sodium sulfide) and steam in the contnuous digester (pressure vessel) with controlled temperature, pressure and retention time.

After cooking, the pulp undergoes the first wash in the continuous digester and is then discharged into a discharge tank (blow tank), where it is stored for transfer to the next stage in the process.

 




Alkaline Washing and Purification

In this stage, the objective is to separate the pulp fibers from the lignin disssolved during cooking.

In the alkaline wash, the pulp is washed in a counter-current flow in DD Washer rotational filters. The designation counter-current is applied because the pulp enters the first filter and progresses toward the final filter, while the water or condensate enters the final filter and progresses toward the first, thereby concentrating the black liquor (dissolved lignin and chemicals used in cooking) and leaving the fibers cleaned.

In the stage designated PRE-O, the pulp enters the first filter, passes through the first wash, and is pumped to the oxygen reactors. In the reactors, the pulp is maintained at controlled temperature and pressure, receiving quantities of oxygen and sodium hydroxide sufficient to dissolve the lignin within the fibers, thereby facilitating the bleaching stage.

After the PRE-O stage, the pulp goes through combined purification, where knots from the wood and small clumps of undercooked fibers are removed, leaving the pulp free of impurities. The washing stage is completed with two more DDW rotational filters, followed by the bleaching stage.

 




Bleaching

Pulp’s natural color is white, but during removal of lignin in the early stages of production it is changed to light brown by the oxidation of organic matter in the wood.

To remove this coloration and return it to white, the pulp is submitted to chemical treatment with oxidizing agents in reactors with controlled temperature, pH and retention time. This process is carried out in 3 stages (Ado/EP/D), and at the end of each stage the pulp is washed in DDW rotational filters in order to remove colored oxidized compounds.




Summary of Bleaching Process:

Acid Stage (ADo – A) - The objective is to remove the hexenuronic acids by acid hydrolysis. This stage uses retention times of approximately 3 hours, with controlled pH and temperature. Lwarcel’s acid stage is unique in relation to other pulp plants because it uses residual acid from the chlorine dioxide generating plant rather than sulfuric acid.

Zero Dioxidizing Stage (ADo – Do) - This is the first dioxidizing stage in bleaching. Its objective is to oxidize the compounds which color the pulp, using chlorine dioxide. This stage uses retention times of 15 minutes, with controlled pH and temperature.

Oxidative Extraction Stage with Hydorgen Peroxide (EP) – The objective of this stage is to make soluble in an alkaline medium the chromophoric (color-giving) compounds oxidated in the previous stages and to increase whiteness, utilizing hydrogen peroxide. This stage uses retention times of 90 minutes, with controlled pH and temperature.

Dioxidation Stage (D) - This is the second dioxidation stage. Its objective is to oxidize the compounds which color the pulp, utilizing chlorine dioxide. This stage uses retention times of 3 hours, with controlled pH and temperature.

All bleached pulp is stored in a storage tower before being sent for the final stage in the process.

 




Drying and Packaging

 The objective of this stage is to mold and dry the sheets of pulp and to package them in bales. 

Pulp from the storage tower is pumped to the drying line, passing through a system of pressurized purifiers which removes any impurities still remaining in the pulp.
The drying line, strictly speaking, begins where the pulp enters the molding and compacting section. At this point, the sheets of pulp, 54% to 56% dry, are sent to a drying tunnel, where blown heated air completes the process to approximately 90% dryness.
When they leave the dryer, the sheets are cut and piled in bales, which are then taken by conveyors to the packaging line, where the bales are compressed and wrapped with sheets of the same pulp and stamped for identification.
Each bale of pulp weighs 250 kilograms; bound in groups of 8, they form 2-ton units for shipment. 
The unitized bales are shipped by truck directly to domestic customers or to ports for exportation.