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Hybrid multistage forward cleaner system with floation cell

a cleaner system and multi-stage technology, applied in reversed direction vortex, manufacturing tools, vortex flow apparatus, etc., can solve the problem of large amount of ink ending up in the pressate, and achieve the effect of increasing the overall efficiency of the system

Inactive Publication Date: 2002-01-31
GPCP IP HLDG LLC
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

[0010] The present invention provides a hybrid system for processing papermaking fibers and includes a multistage array of forward cleaners coupled with a flotation cell which increases overall efficiency of the system. In a typical embodiment, a first rejects aqueous stream from a first stage bank of centrifugal cleaners is treated in a flotation cell before being fed to a second stage bank of centrifugal cleaners.
[0013] As will be appreciated form the discussion which follows, the size and cost of a flotation stage for treating secondary fiber can be reduced by up to 75% if it is installed in centrifugal cleaner system as compared to a full scale treatment of the stock by flotation. The centrifugal cleaner system modeling indicates a 34% reduction in ink speck area of total centrifugal cleaner system accepts by removing ink specks from the first stage rejects with 80% efficiency in a flotation stage and then feeding the flotation accepts forward after centrifugal cleaning of the second stage. (24% reduction if second stage rejects are treated in a similar manner). The ability to feed the centrifugal cleaner rejects forward (after the flotation stage and additional centrifugal cleaning in the next stage) reduces the stock consistency in the first stage, thereby improving the efficiency of the first stage. The capacity of the system is also increased by feeding the second stage centrifugal cleaner accepts forward. The other centrifugal cleaner stages can also be operated more efficiently since more than 50% of the ink in the first stage centrifugal cleaner rejects has been removed in the flotation stage. When the centrifugal cleaner accepts are thickened in a press, a large amount of ink ends up in the pressate. This ink can also be removed by using the ink-laden pressate as dilution water for the centrifugal cleaner rejects going to the flotation stage.
[0015] By sending the first or second stage centrifugal cleaner rejects to a flotation stage (as shown in FIG. 2) it is possible to remove a much higher percentage of the ink specks in office waste. (It was possible to obtain 80% removal of ink specks during a pilot plant trial with a flotation cell operated on second stage centrifugal cleaner rejects.) If the accepts of the flotation cell are cleaned in the next centrifugal cleaner stage, the centrifugal cleaner accepts from that stage can then be fed forward to the thickener. Sending centrifugal cleaner accepts forward reduces the load and improves the efficiency of the previous centrifugal cleaner stage.

Problems solved by technology

When the centrifugal cleaner accepts are thickened in a press, a large amount of ink ends up in the pressate.

Method used

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  • Hybrid multistage forward cleaner system with floation cell
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  • Hybrid multistage forward cleaner system with floation cell

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Embodiment Construction

[0039] Pilot plant trials showed that flotation cells such as the Comer Cybercel .RTM. can successfully deink secondary centrifugal cleaner rejects, with better results obtained if the consistency is kept close to 0.6%. Consistency refers to weight percent fiber or associated solids such as ash unless the context indicates otherwise. Results on 42% office waste (Grade A) and 100% office waste (Grade B) are shown in Table 1.

1TABLE 1 Pilot Plant Results for Brightness Gain, Dirt + Ash Removal Efficiency on Grades A and B at Halsey and Results Used in Simulation Models Grade: A B Model Consistency: 0.69% 0.90% 0.62% Brightness Gain: 18.5% 5.3% Dirt Removal: 77-89% 65-87% 80% Ash removal: 63% 64% 64%

[0040] A simulation model was used to calculate the impact of a Comer Cybercel.RTM. flotation cell to deink forward cleaner rejects on solids loss, ash removal and on removal efficiency of mid-dirt (>150 microns) from a 1.sup.st washer to the deinked pulp (while running grade B at 336 tpd at...

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Abstract

A hybrid system for processing papermaking fibers includes a multistage array of forward cleaners coupled with a flotation cell which increases overall efficiency of the system. In a typical embodiment, a first rejects aqueous stream from a first stage bank of centrifugal cleaners is treated in a flotation cell before being fed to a second stage bank of centrifugal cleaners.

Description

CLAIM FOR PRIORITY[0001] This non-provisional application claims the benefit of the filing date of U.S. Provisional Patent Application Serial No. 60 / 180,348, of the same title, filed Feb. 4, 2000.[0002] The present invention relates generally to papermaking fiber processing and more particularly to a method and apparatus useful for cleaning secondary pulp by way of a multistage forward cleaner system with an integrated flotation cell which cooperates with the forward cleaners to boost efficiency of the system.[0003] Processing of papermaking fibers to remove contaminants is well known in the art, including the use of forward cleaners and flotation cells. Such technology is used, for example, to treat secondary (recycle) fiber sources for re-use in paper products such as towel and tissue, paperboard, coated writing and printing papers and so forth. Following is a brief synopsis of some patents of general interest.[0004] According to U.S. Pat. No. 4,272,315 to Espenmiller waste paper ...

Claims

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Application Information

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IPC IPC(8): D21D5/00D21D5/24D21F1/70
CPCD21D5/00D21D5/24D21F1/70
Inventor JONG, ROBERT DE
Owner GPCP IP HLDG LLC
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