Drying system for producing dried singulated cellulose pulp fibers

• US 6,865,822 B2
• Filed: 05/07/2002
• Issued: 03/15/2005
• Est. Priority Date: 10/30/2001
• Status: Active Grant

• Current Assignee: International Paper Company
• Original Assignee: Weyerhaeuser Company (Weyerhauser)
• Inventors: Vrbanac, Michael David, Wester, Brian, Dezutter, Ramon Charles, Yancey, Michael James
• Primary Examiner(s): Rinehart, Kenneth B
• Application Number:
  US10/140,973
• Publication Number:
  US 20030140519A1
• Time in Patent Office: 1,043 Days
• Field of Search: 343/29, 343/31, 343/33, 343/37, 343/56, 343/57, 343/97, 34/60, 34/83, 34/84, 342/21, 342/18, 34/90, 345/80, 345/89, 344/27, 343/12, 343/13, 343/16, 343/14, 343/25, 162/146, 162/100, 430/201
• US Class Current: 34/427
• CPC Class Codes: C04B 18/241 Paper, e.g. waste paper; Paper pulp
• CPC Class Codes: C04B 20/02 Treatment
• CPC Class Codes: C08J 2303/02 Starch; Degradation products thereof, e.g. dextrin
• CPC Class Codes: C08J 3/12 Powdering or granulating
• CPC Class Codes: D21C 9/001 Modification of pulp properties purification D21C9/08
• CPC Class Codes: D21C 9/002 by chemical means; preparation of dewatered pulp, e.g. in sheet or bulk form, containing special additives
• CPC Class Codes: D21C 9/007 by mechanical or physical means
• CPC Class Codes: D21C 9/18 De-watering de-watering in general F26B; Elimination of cooking or pulp-treating liquors from the pulpD21C9/002, D21C9/02 take precedence; paper-making machines D21F; strainers in digesters D21C7/00; presses in general B30B
• CPC Class Codes: D21C 9/185 comprising at least one step where the pulp is suspended in a gaseous medium, e.g. flash drying
• CPC Class Codes: D21H 11/20 Chemically or biochemically modified fibres
• CPC Class Codes: D21H 15/04 crimped, kinked, curled or twisted fibres
• CPC Class Codes: D21H 17/38 containing crosslinkable groups
• CPC Class Codes: D21H 17/63 Inorganic compounds
• CPC Class Codes: D21H 27/08 Filter paper self-supporting filtering material B01D39/14; making on paper-making machines D21F11/14
• CPC Class Codes: Y02W 30/91 Use of waste materials as fillers for mortars or concrete

Abstract

This invention provides a dried singulated cellulose pulp fiber product as well as an apparatus and a method for forming singulated and dried fibers. In accordance with the process a feed pulp is delivered to a jet drier. The jet drier singulates and dries the feed pulp. The singulated and dried fibers are collected from the jet drier. The feed pulp may be treated with a treatment substance. The jet drier may be maintained at negative pressure. The product fibers may have low knot count, a low fines count, as well improved kink, curl and twist. The apparatus for carrying out the process may include a pretreatment station for supplying the treatment substance, a pulp feed device designed for pulp, a pulp feed device designed for pulp and foam suspensions, and/or a fiber separation station having a vacuum conveyor.

Claims

1. A drying system for the processing of pulp into singulated and dried fibers comprising:

a jet drier with a jet conduit, a manifold for air intake into the jet conduit, a pulp intake for delivery of pulp into the jet conduit, and a fiber outlet for removal of singulated and dried fibers, outlet air, and fines from the jet conduit;

a pulp supply station coupled to the pulp intake for supplying a feed pulp to the pulp intake;

an air supply station coupled to the manifold for delivering air to the manifold;

an outlet flow conduit coupled to the fiber outlet for the transport of the fibers, outlet air, and fines from the jet conduit;

a fiber separation station coupled to the outlet flow conduit for separating the fibers from the outlet air; and

the pulp supply station including a pulp feed device coupled to the pulp intake for delivering the feed pulp to the pulp intake while minimizing the amount of air flow through the pulp supply station, the pulp feed device being a rotary airlock including a rotor housing and a rotor rotatably mounted within the rotor housing, the rotor having rotor vanes for transporting the feed pulp, wherein the rotor vanes and rotor housing are sized so that a gap exists between the rotor vanes and the rotor housing to prevent the feed pulp from jamming the rotary airlock, said gap between said rotor vanes and said housing is in the range of 0.010 to 0.050 inches.

2. The drying system of claim 1, the pulp supply station further including a first de-watering device and a second de-watering device in flow communication with the first de-watering device;

the first de-watering device receiving a pulp supply having a liquid content, removing a portion of the liquid content, and sending a de-watered supply pulp to the second de-watering device;

the treatment supply source delivering the treatment substance to the de-watered supply pulp prior to entry into the second de-watering device; and

the second de-watering device removing additional liquid content from the treated and de-watered supplied pulp and sending a treated feed to the jet dryer pulp intake;

wherein the pulp supply station further includes a treatment recycle conduit in flow communication between the first de-watering device and the second de-watering device; and

wherein the treatment recycle conduit delivers at least a portion of the additional liquid content from the second de-watering device to the first de-watering device.

3. The drying system of claim 2, wherein the pulp supply station further includes a holding tank device inserted in recycle conduit;

and wherein the holding tank device stores at least a portion of the additional liquid content from the second de-watering device and disperses the additional liquid content to the first dewatering device.

4. The drying system of claim 1, wherein the pulp supply station further includes a treatment recycle conduit in flow communication between the first de-watering device and the treatment supply source;

and wherein the treatment recycle conduit delivers at least a portion of the additional liquid content from the second de-watering device to the treatment supply source.

5. The drying system of claim 4, wherein the pulp supply station further includes a holding tank device inserted in recycle conduit;

and wherein the holding tank device stores at least a portion of the additional liquid content from the second de-watering device and disperses the additional liquid content to the treatment supply source.

6. A drying system for the processing of pulp into singulated and dried fibers comprising:

a jet drier with a jet conduit, a manifold for air intake into the jet conduit, a pulp intake for delivery of pulp into the jet conduit, and a fiber outlet for removal of singulated and dried fibers, outlet air and fines from the jet conduit;

a pulp supply station coupled to the pulp intake for supplying a feed pulp to the pulp intake;

an air supply station coupled to the manifold for delivering air to the manifold;

an outlet flow conduit coupled to the fiber outlet for the transport of the fibers, outlet air, and fines from the jet conduit; and

a fiber separation station coupled to the outlet flow conduit for separating the fibers from the outlet air;

the fiber separation station including a vacuum conveyor having a screen for passing outlet air and retaining fibers to form a mat of fibers on the screen;

a first roller, a second roller, a primary fan, a secondary fan, a primary fan vacuum box, and a secondary fan vacuum box;

said screen being a continuous loop draped about the first and second rollers so that the screen has an upper portion and a lower portion;

the upper portion of the screen having an upper and lower surface;

the upper surface of the screen being associated with the outlet flow conduit;

the primary fan vacuum box being associated with the lower surface and in flow communication with the primary fan;

the primary fan vacuum box being positioned between the lower and upper portions and directly beneath the outlet flow conduit;

the secondary fan vacuum box being associated with the lower surface and in flow communication with the secondary fan;

the secondary fan vacuum box being positioned between the lower and upper portions and between the primary fan vacuum box and the second roller;

the primary fan providing vacuum to the primary fan vacuum box and the outlet flow conduit;

the secondary fan providing vacuum to the secondary fan vacuum box and the upper surface.

7. The drying system of claim 6, wherein the fiber separation station further includes a screen vacuum for removing excess fiber from the screen prior to the screen receiving fibers from the outlet flow conduit, the screen vacuum being associated with the upper surface between the outlet flow conduit and the first roller.

8. The drying system of claim 6, wherein the fiber separation station further includes a separation device, wherein the secondary fan vacuum box has a vertical wall facing the second roller, the separation device being associated with the upper screen directly above the vertical wall so that the mat of fibers may pass over the separation device to release the mat of fibers from the screen as well as from the vacuum of the secondary fan.

9. The drying system of claim 6, wherein the fiber separation station further includes an out feed roller, the out feed roller being associated with the upper surface of the screen between the outlet flow conduit and the second roller so that the out feed roller may contact the mat of fibers and pull the mat of fibers from the outlet flow conduit.

10. The drying system of claim 6, wherein the fiber separation station further includes a head box with a head box shell, an out feed roller and a dynamic lip seal;

the head box shell being a conduit having an inlet and an outlet for the passage outlet air, fibers and fines from the outlet flow conduit to the upper surface;

the head box shell being positioned between the upper surface and the outlet flow conduit and being coupled to the outlet flow conduit and associated with the upper surface;

the out feed roller being movably coupled to the side of the outlet of the head box shell facing the second roller so that the out feed roller may move vertically to adjust for varying mat of fiber thickness;

the dynamic lip seal being movably coupled to the side of the outlet of the head box shell facing the second roller so that the dynamic lip seal may move vertically to adjust for varying mat of fiber thickness while maintaining a vacuum seal with the upper surface.

11. The drying system of claim 10, wherein the head box further includes a pair of drive wheels and a coupling device, the drive wheels being rotatably coupled to the side of the outlet of the head box shell facing the first roller and is associated with the upper surface so that the motion of the upper surface results in the drive wheels rotating, the coupling device being coupled to the drive wheels and the out feed roller so that the rotation of the drive wheels acts on the coupling device which in turn acts on the out feed roller.