Paper making and fiber liberation – Processes of chemical liberation – recovery or purification... – With chemical or physical modification of liberated fiber
Reexamination Certificate
2000-06-28
2002-10-29
Alvo, Steve (Department: 1731)
Paper making and fiber liberation
Processes of chemical liberation, recovery or purification...
With chemical or physical modification of liberated fiber
C162S057000, C162S181200, C162S182000, C162S183000
Reexamination Certificate
active
06471825
ABSTRACT:
BACKGROUND OF THE INVENTION
1. Field of the invention
The present invention relates to a method of loading fibers in a fiber suspension for use in a paper-making machine with a chemical compound, and, more particularly, to an apparatus and method for loading fibers in a fiber suspension with calcium carbonate.
2. Description of the Related Art
A paper-making machine receives a fiber suspension including a plurality of fibers, such as wood fibers, which are suspended within an aqueous solution. The water is drained from the fiber suspension and dried in the paper-making machine to increase the fiber content and thereby produce a fiber web as an end product.
The fiber web produced by the paper-making machine typically includes organic wood fibers and inorganic fillers. A known inorganic filler is calcium carbonate, which may be added directly to the fiber suspension (direct loaded calcium carbonate). It is also known to chemically load the fibers within a fiber suspension with calcium carbonate in the lumen and walls of the individual fibers (fiber loaded calcium carbonate). The fiber loaded calcium carbonate increases the strength of the paper compared with a direct loaded calcium carbonate (adding calcium carbonate directly to the fiber suspension) at the same loading (filler) level. This yields an economic advantage in that the filler level of the paper is increased by replacing the more expensive fiber source (wood fibers) with calcium carbonate.
The finished paper web has higher strength properties due to the increased filler levels of the calcium carbonate. In contrast, the strength properties of a finished web using direct loaded calcium carbonate is less.
For example, U.S. Pat. No. 5,223,090 (Klungness, et al.) discloses a method for chemically loading a fiber suspension with calcium carbonate. In one described method, calcium oxide or calcium hydroxide is placed within a refiner unit and carbon
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dioxide is injected into the refiner unit at a specified pressure. The fiber suspension is maintained within the refiner for a predetermined period of time to ensure that a proper chemical reaction and thus proper chemical loading of the fiber suspension occurs. In another described method, a fiber suspension with calcium oxide or calcium hydroxide is introduced into a 20 quart food mixer and carbon dioxide gas is injected into the mixer at a specified pressure. Using either the refiner or the food mixer, both methods utilize a batch processing method for processing only a small amount of the fiber suspension at a time. Because of the large amount of fiber suspension which is required at the wet end of a paper-making machine, a batch process requires that the chemically loaded fiber suspension be transferred to another holding tank for ultimate use in a paper-making machine.
What is needed in the art is an apparatus and a method for chemically loading a fiber suspension for use in a paper-making machine with an adequate output of a chemically loaded fiber suspension which allows commercialization of such a chemical loading process.
SUMMARY OF THE INVENTION
The present invention provides an apparatus and method for continuously loading fibers in a fiber suspension with calcium carbonate using a fluffer for deflocculating the fiber suspension, a series connected auger mixer for mixing the fiber suspension for a predetermined amount of time, and a gas source for pressurizing both the fluffer and mixer with carbon dioxide or ozone.
The invention comprises, in one form thereof, an apparatus for continuously loading fibers in a fiber suspension with a chemical compound. A deflocculating vessel has an interior chamber, a fluid inlet connected with the interior chamber, a fluid out let connected with the interior chamber, and a high shear imparting device disposed within the interior chamber for imparting high shear forces to and thereby deflocculating the fiber suspension. A mixing container has an interior compartment, a fluid inlet connected with both the interior compartment and the fluid outlet of the deflocculating vessel, a fluid outlet connected with the interior compartment, and a low shear imparting device within the interior compartment for imparting low shear forces to the fiber suspension. A gas supply is connected with the interior chamber of the deflocculating vessel and/or the interior compartment of the mixing container. The gas supply is configured for supplying a gas to and pressurizing each of the deflocculating vessel and the mixing container.
An advantage of the present invention is that the fiber loading of the fiber suspension takes place as a continuous process, thereby providing output quantities of loaded fiber suspension sufficient for use in a paper-making machine.
Another advantage is that variables such as flow rate, temperature and pressure which affect the fiber loading process can be accommodated and varied.
The above-mentioned and other features and advantages of. this invention, and the manner of attaining them, will become more apparent and the invention will be better understood by reference to the following description of an embodiment of the invention taken in conjunction with the accompanying drawing.
REFERENCES:
patent: 4278496 (1981-07-01), Fritzvold
patent: 4339206 (1982-07-01), Ahs
patent: 4510020 (1985-04-01), Green et al.
patent: 4820381 (1989-04-01), Brown
patent: 5223090 (1993-06-01), Klungness et al.
patent: 5643415 (1997-07-01), Wise
Doelle Klaus
Heise Oliver U.
Lorenz Kurt William
Matz Robert J.
Witek Werner
Alvo Steve
Taylor & Aust P.C.
Voith Sulzer Paper Technology North Amrica Inc.
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