09/062,266, filed April 17,1998, entitled Pressurized Deinking Module Vent Line, which was a continuation-in-part of Application No.

08/834,606, filed April 14,1997, entitled Multiflow Pressurized Deinking Module, now U. S. Patent No. 5,540,156, the disclosures of which are incorporated herein by reference.

FIELD OF THE INVENTION The present invention relates generally to froth floatation separation and has particular use in the field of deinking of paper in a process for recycling waste paper. More specifically, the invention relates to an apparatus for separating ink-laden foam from a slurry of papermaking stock.

BACKGROUND OF THE INVENTION The manufacture of paper from recycled paper waste, especially post-consumer waste, has become a major industry. Recycling efforts throughout the United States have made large quantities of recycled paper available. This, combined with the high cost of virgin wood fibers, has raised the economic importance of paper manufactured from recycled fibers.

The value of the paper manufactured from recycled fiber, like the value of paper manufactured from virgin fiber, is dependent on the mechanical properties of the paper and the appearance of the paper.

Appearance is chiefly measured in terms of brightness, which for recycled paper means a lack of ink particles and outer dark material endemic to recycled fiber sources.

The principal use of paper is for printing and the vast majority of all printed inks are based on carbon particles. Thus, a pulp manufactured from recycled paper is typically contaminated with a substantial amount of particulate carbon. The carbon from printers'ink is chemically detached from the fiber and must be mechanically separated from the fiber if a high quality sheet is to be manufactured from the recycled stock.

There are three basic ways of cleaning recycled stock: washing the stock, using floatation separation techniques, and using hydrocyclones.

Generally all three techniques are used.

Floatation separation techniques can be particularly advantageous, especially the techniques such as those disclosed in U. S. Patent No.

5,273,624 which is incorporated herein by reference. The 5,273,624 patent shows how a sealed floatation chamber allows the use of vacuum or pressure within the chamber to simplify the collection and removal of the foam containing the carbon particles.

In general the floatation technique (long utilized in the mining industry) utilizes surfactants and various chemical additives to produce a stable foam or froth. The surfactants preferentially attach to the material to be separated and to the surface of a bubble of air, thus attaching the carbon particle to air bubbles introduced into the stock. The air rises through the pulp stock and is removed along with the carbon particles.

Unlike the mining industry, where the material floated to a surface is the desired product, the floatation material in recycling paper is a waste product. Thus the controlling goal is complete removal of carbon from the paper stock and the loss of some fiber with the carbon contamination is acceptable and even desirable.

Although the systems disclosed in the 5,273,624 patent are a significant improvement on prior systems there is considerable economic incentive and need for systems which are more compact and efficient.

Sources of recycled fiber are lower cost than virgin fiber, yet recycled fiber typically requires more processing to improve the quality of the paper manufactured. Thus, any improvement in separation efficiency by reducing the number of cleaning steps makes an important contribution to the economic viability of recycling paper fibers.

SUMMARY OF THE INVENTION The pressurized floatation system of this invention utilizes a cylindrical processing container which has a conical inlet and a conical outlet. A mixture of air and paper stock made from recycled paper is injected into the inlet. The recycled stock contains ink particles which have been chemically released from the wood fibers. Foam forming additives are combined with the stock to create a foam which rises through the stock.

The surfactants encourage the ink particles to adhere to the air bubbles, resulting in a foam containing a concentrated fraction of the ink particles with some included fibers. The foam, being lighter than the surrounding stock, rapidly rises to the top of the container, and carries with it ink particles which can be removed from the stock.

A system of baffles is used to separate the foam containing ink particles from the stock. The stock is separated into a portion for recycling and an accept portion. The recycled portion is passed back to the inlet of the pressurized flotation system. The accept portion may be further cleaned using additional equipment and is used to manufacture paper.

Transverse baffles consisting of foraminous plates with numerous punched holes of about one and one-half inch diameter are positioned to create turbulence within the stock as it flows through the container. A collection baffle is positioned downstream of the transverse baffles to collect foam below and in front of a foam outlet. The foam outlet conducts waste foam consisting of air, ink particles and some fiber stock to a hydrocyclone where the air is separated from the foam and waste is discarded. A second baffle extending above and in front of the accept outlet separates a recirculation outlet from the accept outlet. An additional reject port is positioned behind the collection baffle upstream of the recycle outlet to remove all remaining air and foam before it reaches the recycle outlet.

It is a feature of the present invention to provide a system for removing ink particles from recycled paper pulp which is more efficient.

It is another feature of the present invention to provide a system for removing ink particles from recycled paper pulp for higher brightness paper.

It is a further feature of the present invention to provide a system for removing ink particles from recycled paper which effects a more complete removal of ink particles in a single pass through the system.

Further objects, features and advantages of the invention will be apparent from the following detailed description when taken in conjunction with the accompanying drawings.

BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a schematic side elevational view of the pressurized floatation module of this invention.

FIG. 2 is a schematic side elevational view of an alternative embodiment pressurized flotation model of FIG. 1.

DESCRIPTION OF THE PREFERRED EMBODIMENT Referring more particularly to FIGS. 1-2 wherein like numbers refer to similar parts, a deinking system, or foam floatation module 24 is shown in FIG. 1. The foam flotation module receives stock, indicated by arrows 20, through an inlet pipe 23 which discharges into a container 22. The stock contains 0.5 percent to about five percent paper fiber by weight.

Circumferential turbulence-generating baffles 26 are positioned in the inlet pipe 23 downstream of an air injection port 28 and a foam recirculation port 30. The air injection port 28 and the foam recirculation port 30 introduce air and recirculated foam to be mixed with the stock entering the container 22 from the inlet pipe 23. The container 22 has a generally conical inlet section 32 which widens to a cylindrical body section 34. The inlet pipe 23 discharges fluid into the conical inlet section 32.

Two foraminous baffles 36 extend across the cylindrical body 34 and help mix the air with the stock. The baffles 36 also help to prevent sloshing, or the build up of oscillations within the foam and stock contained in the body section 34 of the container 22. A foam outlet pipe 38 is positioned approximately in the middle of the cylindrical body section 34 of the container 22. The injected air creates a foam 40 which is substantially lighter than the surrounding stock and so will rise rapidly to the top 42 of the container 22. The surface foam 40 is drawn through the top 42 of the container 22 and the out foam outlet pipe 38.

A foam collection baffle 44 is positioned downstream of the foam outlet 38. The foam collection baffle 44 extends across the container cylindrical section 34 and down toward the geometric center of the cylindrical section. The foam collection baffle 44 has portions 46 which extends downwardly and upstream beneath the outlet 38. The baffle section 46 extends downwardly to approximately the centerline of the cylindrical body section 34.

The cylindrical body section 34 ends in a downstream conical section 48. The conical section 48 has an outlet 50 for the cleaned stock. This outlet 50 is covered by a two-part baffle 52. The two-part baffle 52 has a first part 54 which extends almost directly upstream from the outlet 50. A second portion of the two-part baffle 52 depends downwardly from the first part 54. The second portion 56 of the baffle 52 blocks the entrance to the outlet 50 forcing the stock to flow down and under the baffle second portion.

A recirculation port 58 is positioned above the first part 54 of the two-part baffle 52. The recirculation port 58 opens to a recirculation line 60 which has a valve 62 which controls the amount of stock which is recirculated to the foam recirculation port 30 in the inlet pipe 23 of the container 22.

Flow through the foam outlet pipe 38 is controlled by a valve 64 and leads to a cyclone 66 which separates the water, fiber and ink particles from the air.

A vent port 68 communicates with the top of the container 22 between the foam collection baffle 44 and the recirculation port 58. This vent port 68 has been found to significantly reduce the amount of ink particles contained in the stock recirculating through the recirculation port 58. Sixty percent reductions in ink particles have been found when additional foam is withdrawn through the vent port 68. A vent line 67 extends from vent port 68, and a valve 70 is positioned within the vent line 67 to allow adjustment of the foam through the vent line so that air can be largely or completely eliminated from the recirculation port 58. By eliminating air exiting through the recirculation port 58, turbulence in stock exiting the recirculation port 58 is substantially reduced.

Reduction in turbulence of the recirculating stock improves the efficiency of any secondary cleaning which may be performed on the recirculating stock and reduces problems with any feed pumps which may be used with the recirculating stock.

Because the container 22 is sealed, the movement of the surface foam 40 from the container 22 into the outlet pipes 58,68 is affected by system pressure or by a vacuum drawn on the foam outlets 58,68.

Preferably pressures above atmospheric will be used as this minimizes the amount of equipment required and reduces costs, as vacuum equipment is typically more expensive to operate then compressing equipment.

The ability to effectively remove remaining foam and air through the vent port 68 is facilitated by the different properties of air and water. If the valve 70 is only partially opened, it will present a considerable pressure drop or hydraulic resistance. Air, with a much lower in viscosity, can readily pass through the restriction represented by the valve, but the stock, being comprised largely of water can less easily pass through the restriction. In this way a partially opened valve 70 acts to vent air without passing significant quantities of stock.

By increasing the amount of foam removed through the vent port 68 the recirculating stock has a lower ink content and thus the stock flowing into the container 22 has a lower ink content. This improves the overall efficiency or effectiveness of the deinking system 24.

The outlet pipes 38,58 may be connected to a header 74 and lead to a cyclone 66. The cyclone 66 separates the air from the foam leaving a waste stream containing some fiber together with the ink particles suspended in water. A twin-wire press (not shown) is used to dewater the waste stream which is then disposed of, typically as boiler fuel.

A water flush line (not shown) may be used to clean the outlet 50 by flushing with water from time to time.

The container 22 is sealed from the environment because all inputs and outputs to the container are controlled. A valve is not shown on the stock inlet 23 or on the stock outlet 50, however the rate at which stock and air is pumped in controls the pressure in the container 22. Although a valve may be used on the outlet 50, downstream equipment which further processes the stock, for example a pump, can also control the rate at which stock flows out of the container 22. For the deinking system 24 to work properly the valves 62,64,70 connected to the outlet are adjusted until the foam outlet 38 and the vent outlet 68 have essentially only foam and air. The recirculation port valve 62 is adjusted so that stock containing little or no air is removed for recycling. Adjustment of the valves may be by hand in an iterative fashion. Alternatively, a computer, programmable logic controller, et cetera, could be used and could employ sensors in the outlet lines that indicate type or density of flow.

An alternative embodiment deinking system 80 is shown in FIG. 2.

The deinking system 80 has a container 82 with an inlet 84 and an outlet 86. The container 82 has three foraminous baffles 88,90, and 92. The first two baffles 88,90 help to break up and mix the air with the stock and also to prevent sloshing within the container. The third baffle 92, while less critical, is also designed to prevent sloshing and channeling of the flow to the outlet 86. The overall container 82 configuration is similar to the container 24 shown in FIG. 1. A foam outlet 94 is positioned at the top 96 of the container 82. A foam collection baffle 98 is positioned downstream of the foam outlet 94. The foam collection baffle 98 has a portion 99 that extends across the container cylindrical section 100 of the container 82 and down toward the geometric center of the cylindrical section. The foam collection baffle 98 also has a portion 102 which extends downwardly and upstream beneath the outlet 94.

The container cylindrical section 100 ends in a downstream conical section 104. The conical section 104 has an outlet 86 for the cleaned stock. A prismatic baffle 106 extends upstream of the outlet 86 and prevents direct axial flow into the outlet 86. The prismatic baffle 106 has a perpendicular surface 108 which extends across the outlet 86. The perpendicular surface 108 is supported by a surface 110 which leads to the recirculation port 112 and a surface 114 which is parallel to the surface 110 and leads to the upper side of the outlet 86. The perpendicular surface 108 is perpendicular to the streamline arrows 116 indicating fluid flow. This creates a region of flow stagnation immediately upstream of the perpendicular surface 108. This stagnation region allows air bubbles 118 to flow upwardly towards the recirculation port 112. The interior of the prismatic baffle 106 is allowed to be filled by fluid by small holes (not shown) through which the fluid enters and drains from the baffle 106.

A vent port 120 communicates with the top of the container 96 between the foam collection baffle 98 and the recirculation port 112.

A manway 122 positioned upstream of the vent port 120 and allows access to the interior of the container 82 for inspection and maintenance.

A sensor to monitor the interface between the surface foam and the stock in the container 82 is employed just upstream of the foam outlet 94.

Typically a float type sensor (not shown) can be mounted from an attachment fixture 124. The foam sensor provides an additional input to a controller (not shown) for adjusting a valve (not shown) on the foam outlet.

The container 82 is typically operated at a pressure of forty-five to fifty psi so a burst disk pressure relief system 126 is required. The burst disk system 126 is typically designed to vent the container 82 if pressure within the container exceeds 75 psi. As the container 82 must be drained periodically for maintenance, a drain 128 is provided. To prevent collapse of the container 82 due to vacuum forces produced by draining, a check valve may be mounted to an inlet 130 at the top of the container 82. The check valve opens to allow air to enter the container 82 when pressure within the container is less than atmospheric.

The deinking system 80 may be used in groups of four or possibly more units and the mounting feet 132 are designed to fit within brackets 134 on the top of the corresponding deinking containers.

It should be understood that a deinking system 24,80 such as shown in the figures might typically have an inlet pipe 23 which is twenty- four inches in diameter and ten feet long and connected to a container 22 which has a cylindrical body section 34 which is about eighty-two inches in diameter and about twenty-five to thirty-five feet long. Typical flow in such a unit may be about 6,000 gallons per minute.

It is understood that the invention is not limited to the particuiar construction and arrangement of parts herein illustrated and described, but embraces such modified forms thereof as come within the scope of the following claims.