Classifications

• • D—TEXTILES; PAPER
  • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
  • D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
  • D21C7/00—Digesters
  • D21C7/06—Feeding devices

Definitions

• chips were fed into the top of the chip bin, e. g. through an air lock, where they were subjected to steam before moving downwardly through the bin into a chip meter, and then a low pressure feeder, subsequently to a horizontal steaming vessel where the removal of air in the chips with steam was completed, and then either a feed mechanism on top of a batch digester, or more commonly to a high pressure feeder for a continuous digester.
• the chip bin provides a storage volume sufficient to insure supply of the continuous digester, and/or like components, on a regular basis even though the chips are not continuously fed from a chip heap or pile to the pulping system. This is especially important in winter weather conditions in cold climates, where many pulp mills are located, because of interruptions in an ability to continuously feed chips from a heap or pile to the pulping system due to freezing of the chips in the pile, or other weather related disruptions. Numerous problems of channeling or "rat-holing" are caused by inhomogeneous chip feed. Frozen chips have different flow properties than normal chips, wet different than dry, and sawdust and pin chips different than whole chips.
• a method and apparatus are provided which specifically address the problems of reliability and maintenance of conventional vibratory discharges, and the problems of chip bin pluggage, bridging and/or channelling. While the invention is primarily directed to chip bins having a maximum diameter of about twelve feet or more, many aspects thereof are appropriate for bins in general, and of almost any size.
• the invention utilizes mass flow (as contrasted with the "funnel flow" of co-pending application serial no. 08/130,525) in the chip bin, which has significant benefits in promoting uniform steaming, and in minimizing channeling.
• the vibratory discharge is replaced with a simpler, less troublesome, more easily maintained structure while not only not sacrificing discharge efficiency and the ability to steam the chips, but actually enhancing them.
• the chip meter a conventional and necessary piece of equipment associated with most chip bins for continuous digester systems — can be eliminated without elimination of its metering function, thereby resulting in the potential for equipment and maintenance savings for the chip feeding system as a whole.
• comminuted cellulosic material is fed to a digester using a vertical open interior chip bin having a top and bottom, and a maximum diameter of about twelve feet or more (e.g. fourteen feet or more), and a discharge operatively connected to a digester.
• the discharge has a cross-sectional area much less than half of the cross-sectional area of the chip bin (e.g. less than one-tenth).
• the method comprises the steps of: (a) Feeding the comminuted cellulosic material into the top of the chip bin, to flow downwardly in a column in the chip bin toward the bottom, (b) Causing the comminuted cellulosic material to move into a gradually restricting open flow path in the open interior of the chip bin having a cross-sectional area less than half of the area at the maximum diameter of chip bin.
• Step (e) may be practiced by feeding the material directly from the discharge to a low pressure feeder and then ultimately to a digester, or alternatively the material may be fed directly from the discharge to a chip meter, and then ultimately to the digester.
• Steps (b) and (c) may be practiced by causing the comminuted cellulosic material to flow into two distinct volumes each comprising about half of a main volume defined by a substantially circular cross-section top and a substantially rectangular cross-section bottom, and a larger cross-sectional area at the top thereof than at the bottom thereof, and opposite non-vertical gradually tapering sides, and causing the material to move from each distinct volume to the discharge using oppositely rotating feed screws (or opposite handed feed screws rotated by a common shaft), the discharge being located approximately midway between the two distinct volumes.
• Steps (b) and (c) may be further practiced by causing the material to flow into distinct volumes wherein the degree of taper of the opposite non- vertical gradually tapering sides is about 20-35°.
• steps (b) and (c) may be practiced by causing the comminuted cellulosic material to flow through a transition having one dimensional convergence and side relief between a first volume having a circular cross-section of at least about twelve feet and a discharge having a circular cross-section of much less than half of the first volume.
• Step (d) is typically practiced by adding steam to the distinct volumes by introducing the steam into a substantially vertical chip bin wall interruption in at least one non-vertical gradually tapering side of each of the distinct volumes.
• a bin is provided in general. While the bin has specific utility as a chip bin, particularly for diameters of about twelve feet or more, it is useful for almost any size chip bin, and for other bin constructions in general.
• the bin comprises: A hollow substantially right circular cylindrical main body portion having a substantially vertical central axis, a top and an open bottom. A top wall closing off the top of the main body portion, and having means for introducing particulate material into the hollow main body portion mounted thereon.
• a hollow transition portion connected to the bottom of the main body portion having a substantial! ⁇ 7 circular cross-section open top and a substantially rectangular cross-section open bottom, and a larger cross-sectional area at the top thereof than at the bottom thereof, and opposite non-vertical gradually tapering side walls.
• At least one feed screw mounted adjacent the open bottom of the transition portion, in a housing.
• a discharge operatively connected to the feed screw housing. And, means for rotating the at least one feed screw to move particulate material from the bottom of the transition portion to the discharge.
• the bin may further comprise means for introducing steam to the hollow transition portion, the means comprising a steam conduit, and a substantially vertical wall interruption of at least one of the non-vertical gradually tapering side walls of the transition portion, the steam conduit connected to the substantially vertical wall interruption.
• the non-vertical gradually tapering side walls of the transition portion may each have a degree of taper that is about 20- 35° (typically about 25-30°) with respect to vertical, which is about 10-20° greater than the mass flow angle for the material handled (the mass flow angle for most chips is about 10-15°).
• the at least one feed screw may comprise first and second feed screws mounted at the bottom of the transition portion, a junction provided between the screws, and each mounted for rotation about a common generally horizontal axis; and the means for rotating the at least one feed screw may comprise means for rotating the first and second screws about the axis in different directions (or opposite handed feed screws rotated by a common shaft).
• the structure also preferably includes a baffle disposed within the transition portion above the screw junction; and, the discharge may comprise a substantially right rectangular parallelepiped discharge operatively moimted to the screws substantially at the screw junction and remote from the transition portion, the discharge for receipt of particulate solid material from both the screws.
• the discharge may be offset from the main body portion in which case the at least one screw comprises a single screw that transports particulate material substantially horizontally in a single direction from the transition portion to the offset discharge.
• the at least one screw comprises first and second screws, one mounted above the other for rotation about parallel axes, the first screw having a housing mounted to the transition portion and having an outlet therefrom offset from the main body portion, and the second screw having a housing with an inlet connected to the first screw housing outlet, and having the discharge as the outlet, the discharge being substantially concentric with the main body portion.
• the means for rotating the at least one screw comprises means for rotating the first and second screws so that they transport particulate material in opposite substantially horizontal directions.
• the transition portion comprises a first transition portion, and further comprises a second hollow transition portion between the first transition portion and the at least one screw, the second transition comprising a hollow substantially right triangular prism with an open top and open bottom and having a larger cross-sectional area at the bottom than at the top, and the cross-sectional area of the top being approximately the same as the cross-sectional area of the bottom of the first transition portion.
• the bottom of the second transition portion has a length at least five times its width; and the discharge from the screw trough is a rectangular in cross section, having a diameter approximately equal to the width of the bottom of the second transition portion, and is substantially concentric with the main body portion.
• the at least one feed screw comprises first and second feed screws mounted at the bottom of the transition portion, a junction provided between the screws and each mounted for rotation about a common generally horizontal axis.
• the means for rotating the feed screw comprises means for rotating the first and second screws about the axis in different directions.
• the discharge from the screw trough may comprise a substantially right rectangular parallelepiped discharge operatively mounted to the screw substantially at the screw junction and remote from the transition portion, the discharge for receipt of particulate solid material from both the screws.
• An agitator may also be provided at the screw junction, and a chip meter, operated by a motor, may be connected to the discharge.
• a controller coordinates the operation of the chip meter motor and the means for rotating the first and second screws.
• a chip bin assembly comprising the following elements: A hollow substantially right circular cylindrical main body portion having a substantially vertical central axis, a top and a bottom, and having a first diameter. A top wall closing off the top of the main body portion, and having means for introducing wood chips into the hollow- main body portion mounted thereon. A hollow substantially right rectangular parallelepiped discharge having a second diameter with is less than one half of the first diameter. A hollow transition portion disposed between the main body portion and the discharge having one dimensional convergence and side relief. Means for introducing steam to the hollow interior of the bin. And, means for connecting the discharge to a digester.
• the assembly may also comprise first and second feed screws mounted adjacent the bottom of the transition portion, a junction provided between the screws, and each mounted for rotation about a common generally horizontal axis; and means for rotating the screws about the axis in different directions (or opposite handed feed screws rotated by a common shaft) to move wood chips from the transition portion to the discharge conduit.
• the transition portion may include at least one substantially planar non-vertical wall portion; and the means for introducing steam into the bin preferably introduces steam into the transition portion, and comprises a steam conduit, and a substantially vertical wall interruption of the substantially planar non-vertical wall portion of the transition portion, the steam conduit connected to the substantially vertical wall interruption.
• a chip bin assembly which takes the place of conventional chip bins, and which feeds down to a circular cross section discharge which is typically connected to a conventional chip meter or low pressure feeder, ultimately being connected to a high pressure feeder which feeds chips under pressure to the top of a substantially vertical continuous digester.
• the preferred chip bin assembly comprises the following components: A hollow substantially right circular cylindrical main body having a substantially vertical central axis, a top and a bottom, and having a first diameter. A top wall closing off the top of the main body, and having an inlet for introducing wood chips into the hollow main body. A non-vibrating discharge operatively connected to the bottom of the main body.
• the means for introducing steam preferably includes means for introducing steam into the least one of the generally triangular shapes of the side faces of the second portion of the hollow transition, and preferably into both side faces. Also, steam is also preferably introduced into the main body. At least one air blaster is preferably mounted to the hollow transition — such as first and second air blasters mounted to each of the first and third portions of the hollow 7 transition on opposite sides ' of the first and third portions spaced from the faces having generally triangular shapes — to break up hung-up wood chips in the transition.
• the main body may include at least one conical ring insert for relieving compaction pressure on chips in the main body, such as disclosed in copending application Serial No. 08/130,525 filed October 1, 1993 (the disclosure of which is hereby incorporated by reference herein).
• the discharge is preferably circular in i l
• the discharge is typically operatively connected to the high pressure feeder (e.g. through a chip meter and/or low pressure feeder), and to a continuous digester.
• a system for making chemical pulp from wood chips comprising the following components: A substantially vertical continuous digester having a top and a bottom, and an inlet adjacent said top. A high pressure feeder for feeding wood chips to the continuous digester inlet.
• a chip bin for supplying wood chips to the high pressure feeder, the chip bin comprising: a hollow substantially right circular cylindrical main body having a substantially vertical central axis, a top and a bottom, and having a first diameter; a top wall closing off the top of said main body, and having an inlet for introducing wood chips into the hollow main body; a non-vibrating discharge operatively connected to said bottom of the main body; a hollow transition disposed between the discharge and the main body, the hollow transition comprising: a first, uppermost, portion having a generally right rectangular parallelepiped configuration including opposite side faces having generally triangular shapes, and providing one dimensional convergence and side relief; a second portion tapering from a generally rectangular parallelpiped configuration at an upper part thereof to a generally circular configuration at a lower part thereof and having opposite side faces having generally triangular shapes which align with the first portion generally triangular shapes to define substantially diamond shaped wall portions; a third portion substantially the same as the first portion, only smaller, and connected to the second portion lower part; and a
• FIGURE 1 is a schematic side view of a chip bin according to the present invention in association with conventional other equipment for the production of chemical pulp;
• FIGURE 2 is a schematic front view, with some portions cut away for clarity of illustration of the internal components, of one embodiment that the chip bin of FIGURE 1 can take;
• FIGURE 3 is a side view, with the screw motor and end housing removed for clarity of illustration, of the chip bin embodiment of FIGURE 2; l ⁇
• FIGURE 4 is a top plan view of the transition portion of the chip bin of FIGURES 2 and 3;
• FIGURE 5 is a side detail cross-sectional view schematically illustrating the manner in which steam can be introduced into the transition portion of the chip bin of FIGURES 2 through 4;
• FIGURES 6 and 7 are views like that of FIGURES 2 and 3 only for a second embodiment of a chip bin according to the invention.
• FIGURES 8 and 9 are views like those of FIGURES 2 and 3 for a third embodiment of a chip bin according to the present invention.
• FIGURE 10 is a detail front view, with portions cut away to illustrate internal components, of a modified form of the transition and screw components only of the embodiment of FIGURES 2 and 3;
• FIGURES 11 and 12 are views like those of FIGURES 2 and 3, but for only the transition and screw component portions, of a further modification of the chip bin embodiment of FIGURES 2 and 3;
• FIGURE 13 is a top plan view of the transition and like portions of the embodiment of FIGURES 11 and 12;
• FIGURES 14 and 15 are views like those of FIGURES 2 and 3 for yet another modification of the transition, screw feed, and like components, of a chip bin according to the invention
• FIGURES 16 and 17 are views like those of FIGURES 6 and 7 only for the transition and screw feed portions only, of yet another embodiment according to the present invention, the plan view of the structures of FIGURES 16 and 17 being essentially the same as the plan view of FIGURE 13;
• FIGURE 18 is .a side view, partly in cross section and partly in elevation, of another embodiment of a chip bin assembly according to the invention and showing schematically connected up to a low pressure feeder and a digester;
• FIGURE 19 is a bottom plan view of the chip assembly in FIGURE 18;
• FIGURE 20 is a detailed side cross sectional view showing an exemplary nozzle connection to the transition for mounting of an air blaster in the vessel of FIGURES 18 and 19;
• FIGURE 21 is a side view of a modified form of the hollow transition of the assembly of FIGURES 18 and 19.
• FIGURE 1 schematically illustrates a chip bin 10 according to the present invention, having a closed top 11 with a conventional inlet 12 in the top thereof for the introduction of wood chips or other comminuted cellulosic material.
• an air lock 13 is preferably connected to the inlet 12, and a vent pipe 14 is next to the inlet 12. Chips are introduced through the air lock 13 in the conduit 12 through the top 11 of the chip bin 10, as indicated schematically 10
• the chip bin 10 also has other conventional vents, reliefs, and the like associated therewith, and also typically has an internal level sensing mechanism, such as a conventional gamma source level control illustrated schematically by reference numeral 17 in FIGURE 1.
• a conventional gamma source level control illustrated schematically by reference numeral 17 in FIGURE 1.
• Steam is supplied to the chip bin 10 to start steaming of the chips within it.
• the steam is typically low pressure steam, such as provided through lines 18 and 19 from conventional sources within the pulp mill.
• Line 18, in the exemplary embodiment illustrated, is shown connected to the main body portion of the chip bin 10, while line 19 is operatively connected to a lower portion thereof.
• the mechanisms for control of the steam addition to the chip bin, and for sensing and control of the level of chips within the bin 10, the control of air lock 13, and the control of various vents associated therewith, are conventional.
• the chip bin 10 is a vertical vessel with a discharge at the bottom thereof typically connected to a chip meter 21.
• the chip meter 21 is shown illustrated in dotted line in FIGURE 1 since it is not necessary in all embodiments of the chip bin according to the invention. In some of the embodiments of the chip bin according to the invention metering action is inherently provided by components of the chip bin which take the place of a conventional vibratory discharge (such as shown in U.S. patent 4,124,440).
• Below the chip bin 10, and below the chip meter 21 if provided, is a low pressure feeder 22 which feeds the chips after initial steaming from the chip bin 10 into a conventional horizontal steaming vessel 23.
• the vessel 23 typically has a vent conduit 24, and a header 25 connected to the low pressure steam source 19 for the introduction of steam, and a chips outlet 26.
• An internal screw is typically provided in the steaming vessel 23. From the outlet 26 the steamed chips are then lb
• FIGURES 2 through 17 illustrate various embodiments and details of the chip bin 10 of FIGURE 1.
• the accessories such as an air lock, vent pipes, steam conduits, etc. are not shown associated therewith, but would of course commonly be provided.
• the chip bin 10 according to the present invention typically has a maximum diameter of twelve feet or more (typically fourteen feet or more), which is where significant problems occur in conventional systems having vibratory discharges, there are many aspects of the invention that are applicable to chip bins of any size, and some aspects of the invention applicable to bins in general.
• the internal conical-insert bin, construction of co-pending application serial no. 08/130,525 may be utilized.
• FIGURES 2 through 5 illustrate one embodiment of a chip bin according to the invention which may be referred to as a "chisel design".
• the vibratory discharge conventional in prior art chip bins has been eliminated.
• components comparable to those in FIGURE 1 are shown by the same reference numeral only preceded by a "1".
• the chip bin 110 includes a hollow substantially right circular cylindrical main body portion 30 having a substantially vertical central axis, a top 111, and an open bottom 29. It has a maximum (and preferably substantially uniform) internal diameter 31, which typically is twelve feet or more (e.g. fourteen feet or more, for example sixteen feet).
• the top 111 is defined by a top wall which has the conduit 112 (connected to the conventional air lock, etc., not shown in FIGURES 2 through 5) which comprises means for introducing particulate material, typically wood chips or other comminuted cellulosic fibrous material, into the main body portion 30.
• a steam introduction header 32 which introduces steam at a plurality of points around the circumference of the main body 30, may be provided as the sole, or as one of several, mechanisms for steaming chips within the bin 110.
• the bin 110 also comprises a hollow transition portion 33 having a substantially circular cross-section open top 34 and a substantially rectangular cross-section open bottom 35 (see FIGURE 4 in particular).
• the transition portion 33 top 34 ⁇ which is continuous with the bottom 29 of the main body portion 30 ⁇ has opposite side non-vertical gradually tapering side walls 36.
• the side walls 36 make an angle 37 (see FIGURE 3) with respect to the vertical, which angle 37 is typically about 20-35°, and preferably about 25-30°, but will vary depending upon the particular material handled by the bin 110 (e.g. the particular species of wood chips commonly used).
• the ends 38 of the transition 33 are continuously curved surfaces, as indicated by the shading in FIGURES 2 and 3, and as also seen in FIGURE 4.
• the main body portion 30 is welded to the transition portion 33 to provide a continuous fluid-tight wall so that steam introduced into the hollow interior of the portions 30, 33 cannot escape, except through designed vents.
• the transition 33 has a height 39 which is typically less than the diameter 31 (e.g. in one embodiment for a diameter 31 of sixteen feet the height 39 would be about twelve feet).
• a baffle 40 is illustrated within the transition 33 for causing the chips flowing downwardly from the main body portion 30 to flow into two different volumes on opposite sides thereof.
• the baffle 40 is not seen in FIGURE 4, but spans the entire volume between the non-vertical gradually tapering side walls 36, and makes an angle with respect to the vertical approximately the same as the angle 37.
• two feed screws 41, 42 are provided mounted on separate shafts 43, 44 driven by motors 45, 46 respectively, and with a junction 47 therebetween.
• the details of the bearings, etc. for mounting the shafts 43, 45 are not illustrated, nor are the details of the feed screws 41, 42.
• the feed screws 41, 42 are conventional per se, and may be single screws, multiple screws, or any suitable conventional type.
• the motors 45, 46 rotate the screws 41, 42 in opposite directions, so that the screws feed the chips toward the middle (below the baffle 40), typical screw speeds being about 10-100 rpm.
• the first and second feed screws 41, 42 may be different hand (right and left) screws on a common shaft (43) rotated by a common motor (45). In both cases the screws are "oppositely directed".
• the housing for the screws 41, 42 preferably has substantially the same width as the width of the open bottom 35 of the transition 33.
• Operatively connected to the feed screw housing remote from the transition 33 (typically on the opposite side thereof) is the discharge 49.
• the discharge 49 typically comprises a hollow substantially right rectangular parallelepiped conduit, connection, or transition, centrally located just below the junction 47, and having a diameter 50 which is approximately the same as the width of the housing for the screws 41, 42 (essentially the same as the screw 41, 42 diameters).
• the length of each screw 41, 42 should be at least about 2.5 times the diameter of the screws, and these dimensions will be taken into account when designing the diameter 50, the screws 41, 42, etc.
• the discharge 49 may be connected directly to a conventional low pressure feeder 122 (that is a chip meter is not necessary), and in fact the discharge 49 may comprise the inlet connection to the low pressure feeder 122. Since the screws 41, 42 provide a metering action (which is controlled by controlling the speed of rotation thereof by controlling the motors 45, 46) the typically necessary chip meter (21 in FIGURE 1) can be eliminated.
• steam may be introduced into the transition 33.
• the preferred manner in which this is done is illustrated in FIGURE 5.
• Steam introduction is not effective in inwardly angled walls such as the gradually tapering side walls 36 of the transition 33 since the steam ports would have a tendency to clog.
• this problem is alleviated according to the present invention, as illustrated in FIGURE 5, by providing a substantially vertical wall interruption 53 of at least one of the non- vertical gradually tapering side walls 36 (and preferably at multiple locations along each of the walls 36).
• a steam conduit 54 such as connected to a steam header 55 supplied with low pressure steam, 2(J
• FIGURE 5 is provided in each of the subsequent embodiments of chip bins according to the invention, but will not be shown or described in detail with respect to the other embodiments.
• FIGURES 6 and 7 illustrate another embodiment of chip bin according to the invention. Components in the FIGURES 6 and 7 embodiment comparable to those in the FIGURES 1 through 5 embodiments are shown by the same two digit reference numeral only preceded by a "2".
• the hollow substantially right circular cylindrical main body portion 230 is the same as the main body portion 30 in the FIGURES 2 through 5 embodiment, as are the screws 241, 242, and associated components at the bottom of the chip bin 210 to their counterparts.
• the difference between the FIGURES 6 and 7 embodiment and the FIGURES 2 and 3 embodiment is the nature of the transition 233.
• the transition 233 of FIGURES 6 and 7 incorporates the basic design features of U.S. patent 4,958,741 (the disclosure of which is hereby incorporated by reference herein) which is supplied commercially under the trademark "Diamond Back Hopper” by J.R. Johanson, Inc. of San Luis Obispo, California.
• the hollow transition portion 233 has one dimensional convergence and side relief, provided by triangular shaped substantially flat side panels 58 connected together by curved end wall portions 59, the portions 58 making an angle 237 comparable to the angle 37 in the FIGURES 2 and 3 embodiment (e.g. about 20-35°).
• a second hollow transition 61 having generally the configuration of a rectangular parallelepiped (with rounded ends) has 2 ⁇
• Expansion joints 63 preferably mount each of the sides of second transition 61 defining different flow paths to, the housing for screws 241, 242.
• FIGURES 8 and 9 embodiment components comparable to those in the FIGURES 1 through 7 embodiments are shown by the same two digit reference numeral only preceded by a "3".
• the chip bin 310 of FIGURES 8 and 9 no screws 41, 42, 241, 242 are provided, and rather the metering function they provide is instead supplied by the conventional chip meter 321.
• one dimensional convergence and side relief is provided, in this case using components having the same basic configuration as those illustrated in FIGURES 1 and 2 in U.S. patent 4,958,741.
• transition 333 is substantially the same as the transition 233, the transition 361 is different, having the triangular side walls 68 which are substantially flat, and connected together by the curved end portions 69, providing the smooth transition from the substantially rectangular bottom of the transition 333 to the circular discharge 349, having a configuration similar to that of a truncated right triangular prism.
• FIGURE 10 In the construction of the FIGURES 2 through 5 embodiment, some time there are restrictions on the sizes of components that are too restrictive for some installations.
• the necessary dimensional relationship that provides such restrictions is ⁇ as earlier indicated — the necessity of having the length of the outlet of the transition at least about 2.5 times the outlet width for proper feeding.
• this is accommodated by providing a single screw 71 in a screw housing 70 mounted to the substantially rectangular open bottom 35 of the transition 33, the screw 71 driven by the motor 72 and moving the chips in the direction of the arrow illustrated in FIGURE 10 to an outlet 73 that is offset with respect to the main body portion 30 (and transition 33).
• a conduit 74 may be provided in the housing 70 at the end thereof remote from the outlet 33 to act as a vent, or to allow steam for steaming the chips to be introduced thereat.
• the outlet 73 As the direct connection to a low pressure feeder, or the rest of the digester system 27 (from FIGURE 1), however in many situations it is more desirable to have the ultimate discharge from the chip bin to be concentric with the vertical axis of the main body portion 30.
• a second screw 76 in screw housing 75 located below the first screw 71 and first screw housing 70, and illustrated in dotted line in FIGURE 10, is provided.
• the screw 76 driven by motor 77, moves the chips from the conduit 73 back toward the center of the chip bin 110 to the substantially right rectangular parallelepiped discharge 49 which is concentric with the main body portion 30.
• the screws 71, 76 preferably rotate about parallel axes in a common substantially vertical plane.
• FIGURES 11 through 12 deals with the same dimensional problem that the FIGURE 10 embodiment deals with only in a different way.
• a second hollow transition portion 80 is provided between the first transition portion 33 and the at least one screw (screws 41, 42 in FIGURES 11 through 13).
• the second hollow transition 80 has a cross-sectional configuration substantially the same as a race course oval with substantially vertical side walls 81 but with the end walls 82 thereof slightly curved, and with a baffle 2b
• FIGURE 13 illustrates the dimensional relationship that is highly desirable, namely the width W o-f the bottom 35/top 84 (which is essentially the same as the diameter of the screws 41, 42) requires an outlet length (for each screw 41, 42) greater than about 2.5 W.
• the discharge 49 is substantially concentric with the main body portion 30 yet the desired dimensional relationship W/greater than 2.5 W, is readily achieved.
• the baffle 83 divides the flow of chips into two different volumes, and prevents short circuiting of the chips directly to the discharge 49.
• FIGURES 14 and 15 show an embodiment similar to that in FIGURES 2 and 3 only without a baffle. Since the central discharge 49 could be prone to short circuiting, a conventional chip meter 121 is included in this embodiment, run by a motor 86, even though the screws 41, 42 are provided. With such an arrangement it is necessary to control the speeds of the motors 45, 46 (or a single motor taking the place of motors 45, 46), 86 to prevent starvation of the chip meter 121, as by using the controller 87. Also in this embodiment there is the possibility of chip hangup at the junction between the screws 41, 42, and to eliminate this possibility it is desirable to provide the agitator 88, driven b3 7 a motor 89, located at the junction between the screws 41, 42.
• the. screws 41, 42 do not provide a metering function (as they do, for example, in the FIGURES 2 and 3 embodiment), but rather only a transporting function, facilitated by the agitator 88.
• the same advantages with respect to the length/diameter ratio of the screws 241, 242 as are obtained in the FIGURES 11 through 13 embodiment for the "chisel" bin design are obtained for the "Diamond Back"® design of FIGURES 6 and 7.
• a truncated substantially right triangular prism (with rounded ends, simulating a race tack oval) transition 90 is provided, having substantially vertical planar side plates 91, and the rounded ends 92.
• a baffle 93 is mounted within the transition 90 above the junction 247 for the screws 241, 242 to divide the chips flow into two different volumes.
• the second transition 90 has a substantially rectangular shaped open top 94 and a substantially rectangular shaped open bottom 95, the area of the open top 94 being significantly less than the area of the open bottom 95.
• chip bins according to the invention can be used as bins per se rather than exclusively in chemical pulping systems, they are particularly suitable for use with a method of feeding comminuted cellulose material to a digester and where they have a maximum diameter of about twelve feet or more, and with a discharge which is operatively connected to a digester and has a cross-sectional area less than half of the cross-sectional area of the chip bin.
• the comminuted cellulose material is fed into the top of the chip bin 110 through the conduit 112, to flow downwardly in a coliunn in the chip bin 110 toward the bottom (where the discharge 49 is located).
• the comminuted cellulose material is caused to move in a gradually restricting open flow path in the interior of the chip bin until the open flow path has a cross-sectional area (in the transition 33) less than half of the cross-sectional area at the 2o
• the comminuted cellulosic material is steamed, as by introducing steam at 32 and 55 (see FIGURES 2 and 5), and subsequently the partially steamed comminuted cellulosic material is discharged from the bottom of the transition 33, metered by the screws 41, 42, into the discharge 49. From the discharge 49 the cellulose material is fed to the digester (27 in FIG. 1), as through the low pressure feeder 122 and the other conventional components illustrated in FIGURE 1.
• FIGURES 18 through 20 is a preferred embodiment for use in place of conventional chip bin assemblies.
• the chip bin assembly illustrated in FIGURES 18 and 19 is shown generally by reference numeral 400, and includes a hollow substantially right circular cylindrical main body 401 having a substantially vertical center axis 402, a top (see 403 in FIGURE 18), a bottom 404, and a first diameter 405. Typically the diameter 405 is greater than 12 feet, e.g. about 15 feet. An inspection portal 406 may be provided too.
• the top is defined by a top wall 403 which closes off the main body 401, and includes an inlet 407 for introducing wood chips (or like comminuted cellulosic fibrous material) into the hollow main body 401.
• a nonvibrating discharge 408 is operatively connected to the bottom 404 of the main body 401, through the hollow transition 410.
• the discharge 408 is circular in cross section, having a second diameter 411 which is typically much less than - e.g. about 1/3 or less — than the first diameter 405.
• diameter 411 (see FIGURE 19 may be about 4 feet when the first diameter is about 15 feet).
• the discharge 408 is a combination expansion joint and transition. As an expansion joint it accommodates thermal expansion in the assembly 400, and between assembly 400 and adjoining assemblies (e.g. pipes, chip meters, feeders, etc.).
• the discharge 408 is operatively connected to a continuous digester, typically through a high pressure feeder 413.
• a chip meter 414, and associated other conventional components such as a low pressure feeder 412, a horizontal steaming vessel (not shown), and chip chute are provided for supplying wood chips to the low pressure circulation of the high pressure feeder 413.
• high pressure pump 416 displaces the chips from the high pressure feeder 413 and feeds them to the top of a continuous digester.
• the low pressure feeder 412 and associated steaming vessel and chip chute may be replaced by a slurry pump (not shown) connected directly to the high pressure feeder 413. In this case high pressure feeder exhaust is connected to line 437.
• the hollow transition 410 for the chip bin assembly 400 provides for the optimum feeding of the chips while allowing steaming during feeding, and minimizing the chance for chip hangup even though the chips flow path is greatly reduced in size (e.g. from a 15 foot diameter to a 4 foot diameter).
• the preferred hollow transition 410 illustrated in FIGURES 18 and 19 comprises a double Diamondback® type of configuration, sold by J. R. Johanson, Inc. of San Luis Obispo, California, and as generally disclosed in U.S. Patent 4,958,741.
• the hollow transition 410 includes a first uppermost portion 418 having a generally right rectangular parallelapiped configuration (with opposite end faces curved) and including opposite side faces having generally triangular shapes 419, and providing one dimensional convergence and side relief.
• a second portion 420 tapers from a generally rectangular parallelapiped configuration at an upper part 421 thereof to a generally circular configuration at the lower part 422 thereof. It also has opposite side faces having generally triangular shapes 423 which align with the first portion 418 generally triangular shapes 419 to define substantially diamond shaped wall portions, as clearly seen in FIGURE 18.
• the transition 410 also includes a third portion 426 which is substantially the same as the first portion 418 (including the generally triangular shapes 427 on opposite side faces), only smaller, and a fourth portion 429 substantially identical to the second portion 420, only smaller, and including the generally triangular shapes 430 which cooperate with the shapes 427 to define substantially diamond shaped wall portions as also clearly seen in FIGURE 18.
• the lower part 422 of the second portion 420 has a third diameter which is generally intermediate the first and second diameters, typically being at least 50% greater than the second diameter and at least 30% less than the first diameter. For example, where the first diameter is about 15 feet and the second diameter is about 4 feet, the third diameter — indicated at 432 in FIGURE 19 - is about 8 feet.
• the chip bin assembly 400 also includes means for introducing steam into at least one of the main body 401 and hollow transition 410 to steam w 7 ood chips therein.
• steam is introduced into both.
• a conventional steam header assembly 433 (see FIGURE 18) introduces steam into one or more places along the main body 401, while steam is introduced from source 434 into the hollow ⁇
• transition 410 low pressure steam from source 434 is introduced into the transition 410 utilizing conduits 435 provided in the faces 423 of the second portion 420.
• steam relief 437 from the low pressure feeder 412 may be provided to one of the generally triangular shapes 423, via conduit 438, as seen in both FIGURES 18 and 19.
• a wide variety of other mechanisms for introducing steam, utilizing headers, branches, conduits, nozzles, or the positioned wherever desired, may also be provided.
• the main body 401 also may include conical ring inserts, such as the conical insert 440 seen in FIGURE 18, for relieving compaction pressure on chips in the main body 401.
• conical insert rings 440 are fully described in copending application Serial No. 08/130,525, filed October 1, 1993, the disclosure of which is hereby incorporated by reference herein.
• transition 410 is normally effective to prevent hangups, because there is such a large diameter reduction from the main body 401 to the discharge 408, and because no vibratory action is provided at the discharge 408 (or other components), it is preferred that some sort of mechanism be utilized to break up hangups if they do occur.
• This is preferably provided by utilizing one or more air blasters, such as shown schematically at 442 in FIGURES 18 through 20, connected at the appropriate places to the transition 410.
• Air blasters are conventional structures per se, which supply either high powered air, nitrogen, or like gas, for the purpose of dislodging trapped or hung-up solids (wood chips).
• the air blasters 442 may be of the conventional type manufactured by Global Manufacturing, Inc. of Little Rock, Arkansas.
• first and second air blasters (which may include first and second connections to a common air blaster) are provided connected to nozzles 443 on the end walls (generally perpendicular to the side faces containing the generally triangular portions 419) of the first portion 418, and nozzles 444 connected to the end walls of the third portion 426.
• the nozzle 443 is disposed at an angle 446 — which is preferably about 45 degrees — to the end wall of the portion 418, and is disposed within a support ring 447 which extends outwardly from the portion 418.
• the dimension 448 may be about 6 inches, and the dimension 449 about one foot.
• the air blasters 442 may be operated manually when the hangup is noticed by an operator, or blasters 442 may be operated automatically by sensing the flow rate through the discharge 408, or in other desired manners.
• the blasters 442 may be mounted elsewhere in the main section of the bin (i.e. not necessarily within support rings 447).
• the shapes 419, 423, 427, 430 need not be truly triangular.
• the term "generally triangular" as used in the present specificatino and claims includes shapes such as those illustrated at 419' and 423' in FIGURE 21 (the reference numerals in FIGURE 21 are the same as those in FIGURE 18, only followed by a '""), or other modifications thereof.

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• Paper (AREA)
• Processing Of Stones Or Stones Resemblance Materials (AREA)
• Disintegrating Or Milling (AREA)
• Filling Or Emptying Of Bunkers, Hoppers, And Tanks (AREA)

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• 1995
  • 1995-01-17 CA CA002181892A patent/CA2181892C/en not_active Expired - Lifetime
  • 1995-01-17 PT PT95909253T patent/PT742854E/pt unknown
  • 1995-01-17 ES ES95909253T patent/ES2182889T3/es not_active Expired - Lifetime
  • 1995-01-17 CN CN95191451A patent/CN1048778C/zh not_active Expired - Lifetime
  • 1995-01-17 DE DE69528252T patent/DE69528252T2/de not_active Expired - Lifetime
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  • 1995-01-17 EP EP95909253A patent/EP0742854B1/de not_active Expired - Lifetime
  • 1995-01-17 WO PCT/US1995/000616 patent/WO1995021287A1/en active IP Right Grant
  • 1995-01-17 AU AU17279/95A patent/AU1727995A/en not_active Abandoned
  • 1995-01-17 RU RU96117654A patent/RU2124600C1/ru active
  • 1995-01-17 JP JP7520629A patent/JP2991500B2/ja not_active Expired - Lifetime
• 1996
  • 1996-07-29 FI FI963000A patent/FI119329B/fi not_active IP Right Cessation

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