Patent Application
20140182802
This disclosure relates generally to pressure diffuser washers for washing pulp material and particularly relates to the water inlets in a pressure diffuser washer.
The term “pulp” generally refers to comminuted cellulosic material, such as wood chips, that have been processed in a digester vessel to separate the fibers in the wood chips. Chemicals, e.g., liquor, such as alkaline chemicals, are usually injected into the digester vessel to process and cook the cellulosic material to produce the pulp material. Residual chemicals tend to remain with the pulp material as the pulp material is discharged from the digester vessel.
After digestion, pulp material usually flows from the digester vessel to a pressurized diffuser vessel that washes the pulp material to remove the residual chemicals. A pressurized diffuser washer is typically a large vessel, e.g., 50 feet in height and generally houses a reciprocating screen assembly for washing pulp. Pulp with the residual chemicals can enter an annular chamber inside the pressure diffuser vessel and can fill the annular chamber extending much of the height of the pressure diffuser vessel. Wash water is typically injected into the annular chamber within the pressure diffuser vessel and flows through the pulp material to remove, e.g. displace, the residual chemicals from the pulp material. After the wash water flows through the pulp material the wash water is generally known as “wash filtrate” because it now contains the residual chemicals removed from the pulp material. The wash filtrate generally passes from the annular space of the pressure diffuser vessel to an internal screen assembly within the pressure diffuser vessel. The wash filtrate is typically discharged from a bottom outlet in the pressure diffuser vessel. The washed pulp material is typically discharged from the top of the pressure diffuser washer.
The screen assembly usually moves within the pressure diffuser vessel. Traditionally, the screen assembly moves reciprocally up and down during operation of the pressure diffuser washer. The movement of the screen assembly promotes the flow of pulp material through the annulus in the pressure diffuser vessel. Particularly, the upward movement allows the wash filtrate to enter the pulp material displacing dirty filtrate into the screen assembly and into the bottom of the vessel, where dirty filtrate may be removed. The downward movement of the screen assembly may assist in clearing the perforations or screen holes of fibers and particles that may be blocking the perforations.
The pulp material entering the pressure diffuser washer typically includes rocks and other debris. The debris generally moves with the pulp material as the pulp material moves up through the annular chamber in the pressure diffuser vessel. The debris can enter the water inlets on the outer wall of the annular chamber in the pressure diffuser vessel. The wash water inlets are typically gaps extending in a ring around the outer wall of the pressure diffuser vessel. If the gaps become clogged with rocks or other debris, the efficiency of the pulp wash process in the pressure diffuser vessel generally suffers. Removal of the rocks and debris from the wash water inlet gaps generally requires shutting down the pressure diffuser washer to stop wash water flow and allow the debris to be removed. Shutting down a pressure diffuser washer is expensive and interrupts the production of pulp. There is a long felt desire for a pressure diffuser washer that is less prone to loss of efficiencies and operating disruptions due to debris in the pulp material fed to the pressure diffuser vessel for washing.
The problem of debris accumulation in the annular baffle chamber of a pressure diffuser vessel has been solved by fixing an annular baffle screen plate with openings into a gap in the inner wall of the first annular chamber. In exemplary embodiments of this disclosure, wash water or other wash liquid, which may generally be referred to as “wash liquid” may enter the annular baffle chamber of a pressure diffuser vessel through an inlet and communicate with pulp in a first annular chamber through an annular baffle screen plate partially separating the first annular chamber from the annular baffle chamber. Pressure from the wash liquid may prevent debris and other contaminants from flowing backward into the annular baffle chamber. Debris and other chemicals may accumulate and be recovered elsewhere in the manufacturing process, for example, in the pulp storage tank.
A pressure diffuser washer has been conceived comprising: A pressure diffuser washer comprising: an outer wall, an inner wall adjacent to the outer wall, the inner wall defining annular baffle chambers between the outer wall and the inner wall, wherein each of the annular baffle chambers is configured to connect to a source of a wash liquid, a reciprocating screen assembly adjacent to the inner wall, the reciprocating screen assembly defining a first annular chamber between the inner wall and the reciprocating screen assembly, an area in the inner wall defining a gap associated with each of the annular baffle chambers, wherein the wash liquid from an annular baffle chamber flows through the gap into the first annular chamber, and an annular baffle screen plate covering the gap, wherein the annular baffle screen plate defines openings sized to prevent rocks and other large particulate debris from entering the annular baffle chambers. The screen assembly may move reciprocally within the inner wall of the pressure diffuser vessel. The pressure diffuser vessel may have a height of at least 50 feet (15 meters).
The gap may extend around the perimeter of the annular baffle chamber and inner wall, and the annular baffle screen plate may extend around the perimeter of the gap.
The annular baffle screen plate may have openings defined by a screen mesh. In another example embodiment, the annular baffle screen plate may have openings defined by and an arrangement of parallel bars. In yet another example embodiment, a screen mesh and arrangement of parallel bars may define the openings of the annular baffle screen plate. The annular baffle screen plate may be cylindrical, wherein the inner wall is a cylindrical wall. In some example embodiments, the annular baffle screen plate may have upper and lower edges fixed to the inner wall of the pressure diffuser vessel.
In another exemplary embodiment, a pressure diffuser vessel has been conceived comprising: a vertically extending outer cylindrical wall defining an outer portion of a pressurized vessel, a vertically extending inner cylindrical wall coaxial to the vertically extending outer cylindrical wall, the vertically extending inner cylindrical wall defining annular baffle chambers between the vertically extending outer cylindrical wall and the vertically extending inner cylindrical wall, wherein each of the annular baffle chambers is configured to connect to a source of a wash liquid, an area in the vertically extending inner cylindrical wall defining a gap associated with each of the annular baffle chambers, wherein the wash liquid from an annular baffle chamber flows through the gap into a first annular chamber, and an annular baffle screen plate covering the gap into the first annular chamber, wherein the annular baffle screen plate defines openings sized to prevent rocks and other large particulate debris from entering the annular baffle chamber. The gap may extend around the perimeter of the annular baffle chamber and inner wall, and the annular baffle screen plate extends the perimeter of the gap. The screen assembly may moves reciprocally within the pressure diffuser vessel. The pressure diffuser washer may have a height of at least 50 feet (15 meters).
In an example embodiment, the openings of the annular screen plate may be defined by a screen mesh. In another example embodiment, the openings of the annular screen plate may be defined by an arrangement of parallel bars. The annular baffle screen plate may have upper and lower edges fixed to the inner wall of the pressure diffuser vessel. The orientation of the openings in the annular baffle screen plate may be horizontal, such as about 0 degrees to the horizontal axis of the pressure diffuser vessel, vertical, such as about 90 degrees to the horizontal axis of the pressure diffuser vessel, or any angle in between, such as between 0 degrees to 90 degrees, or 30 degrees to 60 degrees. The upper edge and the lower edge of the annular baffle screen plate openings may be curved, rounded, or chamfered. Additionally, the openings may be tapered, having the narrowest opening where the wash liquid enters the opening.
The foregoing will be apparent from the following more particular description of example embodiments of the disclosure, as illustrated in the accompanying drawings in which like reference characters refer to the same parts throughout the different views. The drawings are not necessarily to scale, with emphasis instead being placed upon illustrating embodiments of the disclosed device.
The foregoing will be apparent from the following more particular description of example embodiments of the disclosure, as illustrated in the accompanying drawings in which like reference characters refer to the same parts throughout the different views. The drawings are not necessarily to scale, with emphasis instead being placed upon illustrating embodiments of the disclosed device.
Fresh wash liquid may continually flow via wash liquid pipe 8 into the pulp material as the pulp material moves up through the pressure diffuser washer 10. Wash liquid can be injected into the first annular chamber 12 through injectors 9 positioned at various elevations on the outside of the wall of the pressurized vessel 11. For example, the injectors 9 may be at different elevations such that the injectors 9 are evenly spaced in a vertical direction along the height of the pressurized vessel 11. The injectors 9 may be divided into groups, wherein the injectors 9 in each group may be vertically aligned. The groups may be symmetrically arranged around the pressurized vessel 11.
The injectors 9 are typically coupled to wash liquid conduits to direct wash liquid into the pressurized vessel 11. The injectors 9 may be valves through which wash liquid flows from the conduits into the pressurized vessel 11. The injectors 9 may be arranged at elevations along the height of the pressurized vessel 11. The injectors 9 can provide wash liquid that enters the pressurized vessel 11 along the height of the pressurized vessel 11. From each of the injectors 9, the wash liquid enters an annular baffle chamber 16 extending around the first annular chamber 12. Each annular baffle chamber 16 distributes the wash liquid around the perimeter of the first annular chamber 12 such that the wash liquid enters the first annular chamber 12 through conduits 18 flanking the first annular chamber 12.
The wash liquid flows through the gaps 19 into the pulp material in the first annular chamber 12. Wash filtrate may be extracted through perforations in a cylindrical screen of the internal screen assembly 15 and collected in a large center chamber 20 coaxial with the cylindrical screen and first annular chamber 12. The wash filtrate can be discharged from the large center chamber 20 through a wash filtrate output 21 in the bottom of the pressure diffuser vessel 10.
The gaps 19 are generally open and typically about 2 inches (50 mm) in height. In an example embodiment of this disclosure, each gap 19 may have an annular baffle screen plate 26 with slots, holes or other openings 32, which may collectively be referred to as “openings” to allow wash liquid 24 to flow into the first annular chamber 12. The annular baffle screen plate 26 may be a generally cylindrical plate having upper and lower edges fixed to the inner wall of the pressure diffuser vessel 10. The openings 32 in the annular screen plate 26 are sized to prevent rocks and other large particulate debris from entering the annular baffle chamber 16 associated with the annular screen plate 26. The openings 32 may each have an upper inlet edge formed by an upper corner 36 and a lower inlet edge formed by a lower corner 38. The upper corner 36 and the lower corner 38 may each be any of curved, rounded, chamfered or any combination thereof.
The openings 32 in the annular screen plate 26 may have a collective cross-sectional area sufficient to allow the wash liquid 24 to flow into the first annular chamber 12 preferably without causing an excessive back pressure on the wash liquid 24 in the annular baffle chamber 16. The width of each opening 32 may be on the order of one-half of an inch or several millimeters, such as 5 mm to 20 mm. By forming the opening 32 as a narrow slot, the length of the opening 32 may be substantially greater than its width. For example, the length of a diagonal slot may be 2 or 3 inches (50 mm to 75 mm). It is not necessary for the openings 32 to be sufficiently narrow to prevent the passage of fibers from the pulp material being washed in the pressure diffuser washer 10. The pressure and flushing action of the wash liquid 24 flowing through the openings 32 prevents fibers and pulp material itself from entering the annular baffle chamber 16.
The annular baffle chamber 16 may be an annular passage formed between an inner cylindrical wall 22 and an outside cylindrical wall 28 of the pressurized vessel 11. A baffle 31 may separate annular baffle chambers 16 arranged vertically. In some embodiments, the annular baffle chambers 16 arranged vertically may be separate by empty spaces. The inner cylindrical wall 22 may correspond to an outside wall of the first annular chamber 12. The annular baffle chamber 16 can distribute wash liquid 24 around the first annular chamber 12. The annular baffle chamber 16 may be relatively narrow, such as a thickness of less than one inch and contain one or more baffles 31. The annular baffle chamber 16 may correspond to the one or more injectors 9 (shown in
While the invention has been described in connection with what is presently considered to be the most practical and preferred embodiment, it is to be understood that the invention is not to be limited to the disclosed embodiment, but on the contrary, is intended to cover various modifications and equivalent arrangements included within the spirit and scope of the appended claims.
This application claims priority to and incorporates by reference U.S. Provisional Application Ser. No. 61/747,540, filed Dec. 31, 2012.
| Number | Date | Country | |
|---|---|---|---|
| 61747540 | Dec 2012 | US |
