Patent Application
20130269891
The field of the invention relates to paper pulp bleaching. More particularly, it refers to increasing brightness of pulp in the final chlorine dioxide bleaching stage of a pulp mill bleach plant.
Pulp mills are usually operated to bleach the pulp to the highest possible brightness. This may allow the mill to obtain a higher price on the market or reduce costs in the papermaking process by reducing the amount of expensive additives used when making the paper, such as optical brightening agents. In practice, however, it can be difficult to consistently maintain very high brightness from the bleach plant.
Problems with obtaining and maintaining high brightness can be a result of the chemistry used in typical bleaching operations, as well as limitations resulting from design or equipment limitations. In that regard, it is common for ClO2 bleaching to stall out in later bleaching stages, e.g., the final D2 bleaching stage, where brightness no longer increases and can even decrease as the pulp is retained longer in the bleaching stage. This requires the pH to be closely controlled in order for the the brightness to be maximized for the ClO2 bleaching, which can be difficult due to very long dead time and process variation.
Also, it is common for older pulp mills to run at higher production rates than the rates they were originally designed for. In such a case, retention time in the bleaching process is lower than optimal, resulting in high residual ClO2 and relatively low brightness.
Accordingly, there exists a need to increase brightness of the pulp, while avoiding the problems discussed above.
It has been found that increased pulp brightness can be achieved beyond standard bleaching practices, while avoiding the above mentioned problems, by a process that involves modifying the final D (ClO2 bleaching) stage. This process can also be used to make the bleaching process less pH dependent, so it can produce pulp of more consistent brightness.
It has been discovered that by adding certain additives partway through the final D (ClO2 bleaching) stage, pulp brightness from the stage can be increased. In one embodiment, the additive is an inorganic compound selected from hypochlorous acid or compounds that form hypochlorous acid. Thus, in one embodiment, the hypochlorous acid is added to the final D2 bleaching stage in the form of Cl, Cl water, sodium hypochlorite, or mixtures of these.
In one embodiment, the additive is added to the D2 stage partway through the stage, i.e., after at least a portion the ClO2 has been consumed, in an amount sufficient to increase the brightness of the pulp compared to a final D2 stage without the additive. In an embodiment, the additive is added after about 60% of the D2 stage has been completed, for example, after 2 hours of a 3 hour stage. In another embodiment, the additive is added close to the end of the D2 bleaching stage. In embodiments, the additive is added with less than about 5 minutes remaining, or with less than about 4 minutes remaining or with less than about 3 minutes remaining in the D2 stage. In one embodiment, where the D2 stage has limited retention time, e.g., about 30 minutes, the additive can be added near the end of the stage, as discussed above. In one embodiment, the process is carried out in a D2 stage that follows a D1 bleaching stage with no intermediate extraction stage. In one embodiment, the pulp is a soft wood pulp, e.g., a typical SW pulp from a southern U.S. mill.
Additional objects, advantages and novel features will be apparent to those skilled in the art upon examination of the description that follows.
In an embodiment of the invention, the brightness additive is added near the end of a final D bleaching stage during the last 10% of bleaching stage, as a function of time, i.e., during the period beginning from about the last 10% of remaining time to the end of the bleaching stage. For example, the additive can be added during the last 3 minutes of a 30 minute bleaching stage. In another embodiment, the brightness additive can be added during the last 5% of the bleaching stage.
In an embodiment of the invention, the pH of the pulp slurry in the final D bleaching stage is in the range from about 3 to about 10 at the time the brightening additive is added to the slurry. In other embodiments, the pH of the slurry at the time of addition is in the range of about 4 to about 8, or about 4 to about 7.
In embodiments of the invention, the brightness additive is added to the final D bleaching stage in an amount in the range from about 1 to about 10 kg of additive per ton (1000 kg) of dry pulp, or about 2 to about 9 kg/ton, or about 3 to about 8 kg/ton, expressed as active chlorine (“aCl”). In embodiments, ClO2 is added to the final D bleaching stage in an amount from about 1.5 to about 6 kg/ton (dry pulp), or about 2 to about 5 kg/ton, or about 2 to about 3 kg/ton, expressed as ClO2.
In one embodiment, additional ClO2 is added with the brightness additive in an amount to reduce viscosity drop of the pulp slurry in the bleaching stage. By adding with the additive is meant to include simultaneous addition or addition in relatively close proximity to each other, for example within about 30 seconds, or within about 20 seconds, of each other. In one embodiment, the additional ClO2 and brightness additive are added simultaneously.
Experiments were conducted using an additive in the form of chlorine water or sodium hypochlorite to evaluate the performance of the additive on bleaching at different ClO2 levels, additive levels, point of addition (time it was added) to the D2 stage, and effects on brightness reversion and pulp viscosity.
The pulp used in the experiments was softwood pulp taken from the D1 bleaching stage from a southern U.S. mill.
The impact on brightness was evaluated by adding the bleaching additive at different times throughout the D2 bleaching stage. The results are shown in
A review of
As the likely convenient addition points in an existing mill are at the beginning of the stage and at the end of the stage due to equipment and process constraints, these points will be of interest. It appears that the beginning of the stage is unsuitable since it resulted in lower brightness than the base case. The end of the stage (e.g., after 99% of reaction time) provided positive results, depending on the pH.
The effect of different additives and amounts on brightness as a function of pH was evaluated. The results are shown in
A review of
Evaluation of Residuals from Bleaching Step.
Detailed residual testing was performed to determine the amount of various species present at the end of the stage. The results are shown in
A review of
The impact of the addition point of the bleaching additive on final pH was evaluated. The results are shown in
A review of
Older bleach plants usually run at much higher production rates than they were originally designed for. As a result, the towers are not able to provide as much retention time as desired and the mill can suffer from low brightness and/or high residual ClO2. Accordingly, the effect of the additive on brightness as a function of retention time was evaluated. The results are shown in
A review of
The impact of different amounts of additive on brightness was also evaluated. Different amounts of the additive were added three minutes before the end of the D2 stage to approximate an addition point at the tower dilution. In order to keep the number of bleaches reasonable, a complete pH curve for every level of additive was not plotted. Instead, the optimum NaOH addition rate was assumed to be the same with the additive as it was for the blank. For example, at 6 kg/t of ClO2, the optimum pH without the additive was 4.27. It took 2 kg/t of NaOH to obtain this pH, so 2 kg/t of NaOH was added to each of the runs with 6 kg/t of ClO2 plus the additive. The results are shown in
A review of
The additive appears to work well at all ClO2 addition rates studied. It also appears to give a larger brightness boost at low ClO2 charges. This could be beneficial as a potential replacement of ClO2 in mills that are not pushing their bleach plant to capacity limits.
The effect of using the additive on the amount of residuals of chemicals used in the bleaching process was also evaluated. The results are shown in
A review of
Sodium hypochlorite bleaching stages (H) are believed to cause fairly severe brightness reversion issues. A true H stage, however, runs at high pH (˜10) and contains no ClO2. However, sodium hypochlorite used according to the present invention is believed to be converted to hypochlorous acid due to the stage pH. It is further believed that the hypochlorous acid reacts with the pulp and should not cause severe reversion issues. Accordingly, reverted brightness was tested. The results are shown in
A review of
The effect of the additive on pulp viscosity was also evaluated. The results are shown in
A review of
In order to further evaluate the reason for the viscosity decrease, additional tests were conducted to measure the residuals of the bleaching chemicals as a function of viscosity. The results are shown in
A review of
Based on the above experiments, the following observations can be made:
Good brightness results can be obtained by adding the additive after 120 minutes (with 180 minutes total retention time). An addition point of less than 5 minutes, e.g., 3 minutes, before the end of the stage works well. Putting the additive at the very beginning of the stage generally gives poor results.
Use of the additive resulted in a 3% ISO brightness increase, which is very significant at the end of the bleach plant. The additive gives good results up to and including application rates in amounts up to 10 kg/t aCl. Surprisingly, the brightness increase did not level off at the highest rate examined. Further, the additive works well at all ClO2 application rates studied, including ClO2 rates as low as 2 kg/t (as ClO2).
For a given charge of total active chlorine, more additive and less ClO2 provided higher brightness. The additive provides a consistent brightness increase even for very short (as low as 30 minutes) D2 stages, so it is believed that it can be used to compensate (at least partly) for stages with limited retention time.
Although use of the additive may cause brightness reversion to increase slightly, it still provides significant benefits even when judged on reverted brightness data. Reversion increases with increasing amount of additive. The highest increase in reversion was just under 1% ISO with 10 kg/t of the additive.
Although the additive sometimes gave lower brightness than the base case (without additive) at lower pH, this should not be a significant issue since addition points at the end of the stage had higher final pH than addition points at the beginning or 120 minutes into the stage.
Test revealed that viscosity decreases as more additive is used, but at lower additive charges, the viscosity change is about the same for a given brightness gain as it is when ClO2 is used by itself.
| Filing Document | Filing Date | Country | Kind | 371c Date |
|---|---|---|---|---|
| PCT/EP11/73265 | 12/19/2011 | WO | 00 | 6/21/2013 |
| Number | Date | Country | |
|---|---|---|---|
| 61426179 | Dec 2010 | US |
