US2858212A - Wood chip feeders - Google Patents

Wood chip feeders Download PDF

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US2858212A
US2858212A US565113A US56511356A US2858212A US 2858212 A US2858212 A US 2858212A US 565113 A US565113 A US 565113A US 56511356 A US56511356 A US 56511356A US 2858212 A US2858212 A US 2858212A
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chips
pressure
casing
inlet
chamber
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US565113A
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Leonard G Durant
James E Irvine
Rohe V Pennington
Surino Alphonse
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Condi Engineering Corp
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Condi Engineering Corp
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    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21CPRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
    • D21C7/00Digesters
    • D21C7/06Feeding devices

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  • Another object of this invention is to return to atmospheric pressure the emptychip-earrying devices or compartments under conditions of incremental decrease in pressure that are just the reverse of conditions encountered in their chip-carrying forward motion.
  • an enclosed chamber adapted to subject such chips therein to steam-induced temperature and pressure while having means for evacuating treated chips therefrom and a bin for receiving and holding a supply of chips to be treated while discharging such chips at a uniform rate, characterized by means for receiving such discharging chips and moving them to enter the chamber that comprises a casing having a bore with a top chip-receiving inlet and a bottom chip evacuating outlet, a motivated rotor having an axle in the casing and a hub with a plurality of vanes or blades extending from the hub to the periphery of the bore of the casing with a chip-carrying compartment or pocket formed between pairs of adjacent vanes which during rotation of the rotor receives chips from the top inlet when the register therewith and delivers chips through the outlet from the casing when .in register therewith, and means for incrementally steam-induced super heat and super,
  • Figure l is a diagrammatic showing of the environment of the invention.
  • Figure 2 is a vertical sectional view (from left to right in Figure l) of the feeder mechanism of this invention.
  • Figure 3 shows a side elevational view of the feeder of Figure 2.
  • Figure 4 shows a top plan view of the feeder.
  • Figure 5 is a partial side elevational view looking toward the left in Figure 3.
  • Figure 6 is a partial vertical sectional view (with all pipes omitted) along a line drawn vertically through Figure 4 along the line 6-6.
  • Figure 7 is a partial isometric view with parts broken away, showing parts of the rotor 15 with its arrangement of vanes, seals, flanges, etc.
  • Figure 8 shows a top plan view of the rotor.
  • Figure 9 shows a somewhat diagrammatic view of the superposed zones of different steam pressure in the casing of the feeder.
  • the feeder mechanism F for the chips is usually operated at a constant rate but chips are supplied thereto from a storage bin B for chips to be treated that is provided with an arch breaker A and a star wheel chip discharger S operated by a variable speed motor M, whose speed is controlled and regulated by a regulation circuit R on the tank.
  • the regulator operates so that as the top of the column of chips C drops below a predetermined elevation, the variable speed motor M on the star wheel discharger S speeds up to deliver more chips to the tank, or slows down to deliver fewer chips to the tank when the chips rise above a predetermined elevation.
  • the enclosed tank T contains steam-induced temperature and pressure, with the pressure being the order of pounds per square inch gauge pressure, so the chips, which incidentally are of a size and roughly of a shape ranging from that of a silver dollar downwardly, have to be fed into the tank T starting from atmospheric pressure to 120 p. s. i. g. in the tank.
  • the feeding must be such as to minimize escape of steam and pressure from the tank, and that is to be accomplished by the feeder mechanism F.
  • This feeder mechanism station F comprises a casing 11 that is generally cylindrical but having open ends 12 and 13-. It has an internal bore 14 in which rotates a rotor having a hub 15 secured to a shaft or axle 16 journalled in suitable bearings 17 and 18.
  • the casing has a top chip inlet 20 leading from the star wheel chip discharger S through the pipe 19 and communicating with the bore 14.- It also has a bottom chip outlet 21 likewise communicating with the bore and leading into the tank T, but with the outletbeing larger than the inlet.
  • the hub of the rotor is equipped with a plurality of blades or vanes 22, while formed between pairs of adjacent vanes are chip-carrying closed ended pockets23t
  • Theinletlflt has a side wall 24 that is first encountered or passed under.
  • the outlet 21- also-has a sidewall 28 that;- is first encountered or passed by the moving vanes,-and a side wall 29 that islast passed by them.-
  • each vane-when movingi under the firstencountered side wall 24 of the inlet 20 should be-substantially parallel to that side wall, for a reason given hereinafter. So each pocket 23 is shaped by the intersectingangularity of pairs of-sequentially adjacent vanes which vanes form the sides of the pocket,
  • each pocket has much more in-- clination from the vertical than does the right hand vane when thepock et formed therebetween is under the inlet 20.
  • the bottom 30' of each pocket is rounded as shown, with a radius such that no individual chip is likely to become wedged therein but can always fall freely there-- from whenthe pocket is Lip-ended.
  • the inlet 20 into the casing, .and the outlet 21 therefrom are of a size larger than the mouth of one pocket so that, they always have opening thereinto at least a portion of two pockets.
  • the varies 22 have a sloping free end edge 31, provided with a groove 32 in which is fitted-a seal 33 against loss of steam and pressure. They are made of hard, strong, long-wearing, non-swelling, bearing type material, such as: carbon with a low coefiicient of friction.
  • the end of the seal and the free end of the vanes are slopingly curved to be complementary tothe inner periphery of the bore. 14.
  • the seals are spring biased by stainless steel springs; such as shown at34 for pressing the seals against that periphery. InFig.
  • lateral peripheralflang es 36 The flanges 36 are made steam-tight by packing 40 held in place by flanges -41- on rings 42 held tightly in .place by a series of bolts 43.
  • a recess '45 In the front wall 26 of the inlet 20 there is a recess '45 in which is seated a block 47 removably held by bolts 44, and in the other wall 27 of inlet 20 there is a similar recess 46 in which is seated a block 48 also removably held by bolts such as 44.
  • Therotor with its vanes and the-pockets between'pairs thereof rotate clockwise, as shown in Figure 2 so when a pocket comes to its zenith position and into register with the top chip inlet 20, the pocket becomes filled with chips and carries them along as the rotor rot-ates until a chipbearing pocket comes to its nadir position and into. register with the bottom chip outlet 21 whereupon the, chips slide from the pocket downwardly through the: outlet 21 to the treatment tank T thereoelow. Continued rotation of the rotor carries the empty pocket back up to its zenith position.
  • a pocket Inpassing from zenithposition, to nadirpositiohwhile carrying chips, a pocket is referred to as an outgoing pocket or outbound, whereas in passingfromnadir position to zenith position while not sure maintained in the bore 14 of the casing 11 as shown iii) in Figure 9.
  • the superposed zones are indicated by Z as atthe top witha pressure equalto that of the atmosphere; Z next below with a steam pressure of substantially 45 p. s. i. g.; Z a subjacent zone with a steam pressure of substantially pus. i. g.; Z next below with a steam pressure of substantially p. s. i. g.; and Z a final zone with 'a' steam pressure.
  • Pressure. ofsay: 80 p. s..i. g. is provided in zone a similarv arrangement comprising a series of radial pressure outlets. 60. throughcasingll at the left and a corresponding ,or paired series of. radialpressure inlets: 64,. located about. 180 from outlets 60, through the casingqll. atthe rightthereof connected together. by.
  • InI Figure 2 thereis shown on the right hand wall 251 of. the, top chip inlet, a wiper blade 77 held in place by. bolts- 78 and plates or straps 79, for wipingly removingor rolling back chips, slivers and sawdust from the end edges .of the moving vanes and their seals as theypass under the wall 25.
  • the apparatus of Figure 1 is started up with chips being fed into the storage bin .B where they are. operatedon by the arch breaker A and the star wheel chip 1 discharger S operated by. the variable speed motor 2M; whose speedis controlled and: regulated. by:the regulation: circuit R on the;tank. ;T.
  • the regulator operates'so that 1 as the top of the .column of chips C drops below a pre- ⁇ determined :elevatiomthe variable speedimotor M on the 1 star, wheel: discharger'S speeds up.
  • variable speed motor M on the wheel discharger slows down to deliver fewer chips to that feeder mechanism F since that mechanism is rotated at a constant rate.
  • the chips are passed through that feeder mechanism whose details are shown in. the other figures of the drawing, namely by dropping down the top chip inlet 20 of the casing 11( Figure 2).
  • the chips complete filling the pocket 23 just passing away from under the inlet, and begins filling the pocket 23 coming into register with the inlet 20.
  • This feeding first to the leading edge of a pocket onto its leading inclined blade is important in accomplishing orderly filling of the pockets, and filling them completely.
  • the chips in its top encounter the wiper blade which removes excess chips, slivers, and sawdust from the top of the seals 33.
  • a rotary feeder of this type is subjected to difiicult conditions of temperature change, abrasion, wear, steam loss, and so on, but they all seem to be compensated for in the design of this invention and where wear cannot be resisted, the wear-receiving seals have been made readily renewable.
  • Continuously operable wood-chip digestion apparatus including an enclosed chamber adapted to subject such chips therein to steam-induced temperature and pressure; means for evacuating treated chips from the bottom of the chamber; a bin for receiving and holding a supply of chips to be so treated; means for discharging chips from the bin at a substantially uniform rate; and means for receiving such discharging chips and moving them to enter the chamber while minimizing escape therefrom of steam and pressure
  • both the chip inlet into the casing and pocket the chip outlet from the casing is larger than the mouth of one pocket whereby they always have Opening thereinto at least a portion of two pockets.
  • Apparatus according to claim 1 wherein in the top chip inlet there are hooded conduit means for conducting pressure from a pocket open to the inlet to the atmosphere.
  • Continuously operable wood-chip digestion apparatus including an enclosed pressure-containing chamber adapted to subject such chips therein to steam-induced temperature and pressure, a bin for receiving and holding a supply of chips to be treated, and means for receiving chips therefrom and transporting them to and into the chamber without fiber-degrading mechanical compaction on the chips While minimizing escape from the chamber of steam and pressure; said latter means comprising an'open-ended casing with a bore therein having a top chip inlet from the bin at atmospheric pressure and a bottom chip outlet to the chamber at the super pressure existing in the chamber, an axle in the bore, a rotor secured to rotate with the axle having a.

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Description

Oct. 28, 1958 DURANT ET AL 2,858,212
WOOD CHIP FEEDERS Filed Feb. 15, 1956 3 Sheets-Sheet 1 ATTORNEY 5m .m R0 g 0 r 8 n T h .I D m m dE ms nee mm L J R Alphonse Surino 'Oct 28, 1958 Filed Feb. 13, 1956 L G. DURANT EI'AL WOOD CHIP FEEDERS 3 Sheets-Sheet 3 FIG. 9 2o 74 2s 76 0* 2| 0 To 7 77 7e 57 57 55 Z2 Z3 n H l4 l4 Z3 62 3 62 so 64 Z4 :05
INVENTORS- Leonard G. Durant James E. Irvine Rqhe V. Penningtor Alpho lse Surino M W ATTORNEY WOOD CHIP FEEDERS Application February 13, 1956, Serial No. 565,113 Claims. 01. 92--7 This .invention relates to the paper making industry and more particularly to that station in a paper mill wherein ligno-cellulosie materials such as wood chips are digested. In the digestion or cooking of wood chips, they are subjected to pressure conditions within an enclosed chamber to which chamber they are continually fedatthe top and continually discharged from the bottom. Various means have been devised and used for the continuous introduction of such chips from a bin or hopper'holding a supply thereof while minimizing the escape from the chamber of steam and pressure. Such means have included rotary valves of various kinds, but invariably they have been unsatisfactory. Included among the reasons for this are:'
that the chips carry a lot of abrasive substances like sand that effect excessive wear on the moving parts so toomuch' steam is lost; there is arching of the chips so that the feed through the valve is not-uniform; and the differences between the maximum pressure on some parts compared with the minimum pressure on others, is so great as to interfere with good operation. So it is an object of this invention to devise a rotary feeder that will overcome these difliculties. Some inventors have gone so fares to getaway from rotary valve feeders, by devising reciprocating plungers for forcing the chips under great compaction into the chamber. But it has been foundthat such compaction is degrading to the fibers ultimately recovered from the chips, so it is an object of this invention to ar range the rotary feeder thereof to operate in a manner that will avoid all such degrading compaction. It is another object to devise ways and means for exposing the chips on their way into the steam pressurized chamber from atmospheric pressure to pressure that is increasedincrementally so hat by the time they enter the chamber,
they have been brought up to that pressure, step by step.
Another object of this invention is to return to atmospheric pressure the emptychip-earrying devices or compartments under conditions of incremental decrease in pressure that are just the reverse of conditions encountered in their chip-carrying forward motion.
*These objects, and possibly others that appear hereinafter, can be realized by an enclosed chamber adapted to subject such chips therein to steam-induced temperature and pressure while having means for evacuating treated chips therefrom and a bin for receiving and holding a supply of chips to be treated while discharging such chips at a uniform rate, characterized by means for receiving such discharging chips and moving them to enter the chamber that comprises a casing having a bore with a top chip-receiving inlet and a bottom chip evacuating outlet, a motivated rotor having an axle in the casing and a hub with a plurality of vanes or blades extending from the hub to the periphery of the bore of the casing with a chip-carrying compartment or pocket formed between pairs of adjacent vanes which during rotation of the rotor receives chips from the top inlet when the register therewith and delivers chips through the outlet from the casing when .in register therewith, and means for incrementally steam-induced super heat and super,
nited States Patent increasing steam pressure in sequential zones in the bore of the casing through which the pockets pass on their path toward the chamber from a pressure at the inlet equal to atmospheric to a pressure at the outlet equal to that in the chamber and on their return path toward the inlet whereby corresponding pairs of pockets on each vertical side of the axle are under the same pressure. Other features of importance reside in the construction; shape; location; and relationship between the vanes, the inlet and outlet; and the details of how the equalization of the pressure in the respective pockets is effected; as well as other details described and claimed hereinafter.
The invention is illustrated in the accompanying drawings in which Figure l is a diagrammatic showing of the environment of the invention. Figure 2 is a vertical sectional view (from left to right in Figure l) of the feeder mechanism of this invention. Figure 3 shows a side elevational view of the feeder of Figure 2. Figure 4 shows a top plan view of the feeder. Figure 5 is a partial side elevational view looking toward the left in Figure 3. Figure 6 is a partial vertical sectional view (with all pipes omitted) along a line drawn vertically through Figure 4 along the line 6-6. Figure 7 is a partial isometric view with parts broken away, showing parts of the rotor 15 with its arrangement of vanes, seals, flanges, etc. Figure 8 shows a top plan view of the rotor. Figure 9 shows a somewhat diagrammatic view of the superposed zones of different steam pressure in the casing of the feeder.
Since this invention is devised to perform'a certain function in a certain manner in a particular environment, it is believed that that environment should be understood first, so it has been illustrated in Figure 1, wherein lignocellulosic material such as wood chips are to be treated in the course of their cooking or digestion, in an enclosed steam heated and pressured chamber or tank T into which the chips are continually fed at the top by a feeder mechanism F and discharged from the bottom by an evacuator mechanism E, under conditions that there are always in the tank T a column of chips C, whose height is controlled to be substantially constant while made up of everchanging individual chips which during their treatment in the tank continually move downwardly therein at a controlled rate. The feeder mechanism F for the chips is usually operated at a constant rate but chips are supplied thereto from a storage bin B for chips to be treated that is provided with an arch breaker A and a star wheel chip discharger S operated by a variable speed motor M, whose speed is controlled and regulated by a regulation circuit R on the tank. The regulator operates so that as the top of the column of chips C drops below a predetermined elevation, the variable speed motor M on the star wheel discharger S speeds up to deliver more chips to the tank, or slows down to deliver fewer chips to the tank when the chips rise above a predetermined elevation.
The enclosed tank T contains steam-induced temperature and pressure, with the pressure being the order of pounds per square inch gauge pressure, so the chips, which incidentally are of a size and roughly of a shape ranging from that of a silver dollar downwardly, have to be fed into the tank T starting from atmospheric pressure to 120 p. s. i. g. in the tank. At the same time, the feeding must be such as to minimize escape of steam and pressure from the tank, and that is to be accomplished by the feeder mechanism F.
This feeder mechanism station F comprises a casing 11 that is generally cylindrical but having open ends 12 and 13-. It has an internal bore 14 in which rotates a rotor having a hub 15 secured to a shaft or axle 16 journalled in suitable bearings 17 and 18. The casing has a top chip inlet 20 leading from the star wheel chip discharger S through the pipe 19 and communicating with the bore 14.- It also has a bottom chip outlet 21 likewise communicating with the bore and leading into the tank T, but with the outletbeing larger than the inlet. The hub of the rotor is equipped with a plurality of blades or vanes 22, while formed between pairs of adjacent vanes are chip-carrying closed ended pockets23t Theinletlflt has a side wall 24 that is first encountered or passed under. by the moving vanes, and a sidewall 25 that; is last passed under by the moving vanes as they move clockwise;-as shown in Figure 2. Its two other sidewalls are; shown: at 26 and 27. The outlet 21- also-has a sidewall 28 that;- is first encountered or passed by the moving vanes,-and a side wall 29 that islast passed by them.-
Thevanes eXtendfrom-the rotor at a particulariangle, namely substantially at a tangent to the hub and axle,,orx
perhaps another criterion is that each vane-when movingi under the firstencountered side wall 24 of the inlet 20, should be-substantially parallel to that side wall, for a reason given hereinafter. So each pocket 23 is shaped by the intersectingangularity of pairs of-sequentially adjacent vanes which vanes form the sides of the pocket,
but therighthand vane (Figure 2) has much more in-- clination from the vertical than does the right hand vane when thepock et formed therebetween is under the inlet 20. The bottom 30' of each pocket is rounded as shown, with a radius such that no individual chip is likely to become wedged therein but can always fall freely there-- from whenthe pocket is Lip-ended. The inlet 20 into the casing, .and the outlet 21 therefrom are of a size larger than the mouth of one pocket so that, they always have opening thereinto at least a portion of two pockets. In thecaseof the inlet this allows for the easy incremental loadingof-an aligning pocket with chips since the chips slide down theinclined leading vane to fill the bottom of the pocket firstzand, as the vane continues under the pocket, chips thenfill the, pocket whereupon they are levelled off by the, wiper 77. Similarly, but in reverse,- the outlet permits unloading ofchips from the pockets ro enough time interval takes place to complete the unloading from at least two pockets.
The varies 22 ,have a sloping free end edge 31, provided with a groove 32 in which is fitted-a seal 33 against loss of steam and pressure. They are made of hard, strong, long-wearing, non-swelling, bearing type material, such as: carbon with a low coefiicient of friction. The end of the seal and the free end of the vanes are slopingly curved to be complementary tothe inner periphery of the bore. 14. The seals are spring biased by stainless steel springs; such as shown at34 for pressing the seals against that periphery. InFig. ,2, it can also be seen that the end edges 31 of the vanes are flared outwardly to enclose the ends of the seals, and that the sides 38 and 39 of the rotor provide end walls for the pockets 23, which sides 38 and 39 terminate in a laterally extending peripheral flange 36 on each side of the rotor 15 (see Figures 6 and 7). Indeed the rotor (Figure 8) is an integral unit including the,
vanes 22, pockets 23, side walls 38 and 39, seals 33, and
lateral peripheralflang es 36. The flanges 36 are made steam-tight by packing 40 held in place by flanges -41- on rings 42 held tightly in .place by a series of bolts 43. In the front wall 26 of the inlet 20 there is a recess '45 in which is seated a block 47 removably held by bolts 44, and in the other wall 27 of inlet 20 there is a similar recess 46 in which is seated a block 48 also removably held by bolts such as 44.
Therotor with its vanes and the-pockets between'pairs thereof rotate clockwise, as shown in Figure 2 so when a pocket comes to its zenith position and into register with the top chip inlet 20, the pocket becomes filled with chips and carries them along as the rotor rot-ates until a chipbearing pocket comes to its nadir position and into. register with the bottom chip outlet 21 whereupon the, chips slide from the pocket downwardly through the: outlet 21 to the treatment tank T thereoelow. Continued rotation of the rotor carries the empty pocket back up to its zenith position. Inpassing from zenithposition, to nadirpositiohwhile carrying chips, a pocket is referred to as an outgoing pocket or outbound, whereas in passingfromnadir position to zenith position while not sure maintained in the bore 14 of the casing 11 as shown iii) in Figure 9. The superposed zones are indicated by Z as atthe top witha pressure equalto that of the atmosphere; Z next below with a steam pressure of substantially 45 p. s. i. g.; Z a subjacent zone with a steam pressure of substantially pus. i. g.; Z next below with a steam pressure of substantially p. s. i. g.; and Z a final zone with 'a' steam pressure. equal to the pressure then existing in the treatment tank T, say p. s. i. g. In order to accomplish this pressure zoning or compartmentingof the -pressured areas to be substantially horizontal and deep enough. so that oppositely directed pocketse-one inbound and one outb0und:- -lie in the same. zone ofpressure, there is provided a series of radial pressure outlets. 55- through casing 11 (at the left of Figures; 2 and.9) and a corresponding or paired series of radialpressure inlets 59 at the right of '11, located about from. outlets 55, and-these are connected together by meansaof manifolds 56- and 58. respectively and by a common, pressure-equalizing pipe 57. This piping arrangementyprovides. a pressure of say 45 p. s. i. g..in zone. Z2. Pressure. ofsay: 80 p. s..i. g. is provided in zone a similarv arrangement comprising a series of radial pressure outlets. 60. throughcasingll at the left and a corresponding ,or paired series of. radialpressure inlets: 64,. located about. 180 from outlets 60, through the casingqll. atthe rightthereof connected together. by. meansof manifolds 61 and 63 respectively and by a com monpressure-equalizing pipe 62.- Similarly pressure in: Zais established .and maintained by a series of radial pres sure outlets 65 through casing 11-at the left and a corre" spending or paired seriesof radial pressure inlets 69," located about 180 from outlets65, through the casing 11.- at the right connected together by means of manifolds 66 and 68 respectively and by a common pressure-equalizing pipe 67.. Manifolds 56, .61 and may be said-to be pressure-receiving manifolds while manifolds 58, 63 and. 68 may be saidto be pressure-transmitting. There is also a series, of radial pressure outlets 70 at the .upper left of Figures 2 and 9 leading toia manifold 71 going tothe at mos'phere, and a series-of diametrically opposite pressure. inlets. 72,.leading from a manifold 73 connected to the interiorof the tank T. Finally there is a steam exhaust duct 74hooded as at .75 within the top chip inlet 20 and passing through its wall 24 to connect. with the atmosphere by meansof an exhaust fan 76.
InIFigure 2 thereis shown on the right hand wall 251 of. the, top chip inlet, a wiper blade 77 held in place by. bolts- 78 and plates or straps 79, for wipingly removingor rolling back chips, slivers and sawdust from the end edges .of the moving vanes and their seals as theypass under the wall 25.
When it becomes necessaryto remove and replace any.v oneof the seals 33, this can be done by aligningthe desired blade .22 with the inlet '20 (see Figures 2 and 6); unscrewing the bolts 44; lifting out the blocks 47 and 48; and then lifting out the seal 33 and replacing it with a newone.
In-operation,-the apparatus of Figure 1 is started up with chips being fed into the storage bin .B where they are. operatedon by the arch breaker A and the star wheel chip 1 discharger S operated by. the variable speed motor 2M; whose speedis controlled and: regulated. by:the regulation: circuit R on the;tank. ;T. The regulator operates'so that 1 as the top of the .column of chips C drops below a pre-\ determined :elevatiomthe variable speedimotor M on the 1 star, wheel: discharger'S speeds up. to 'deliver'more chips to jthelfeeder; mechanism F or if the top not the column predetermined level, the variable speed motor M on the wheel discharger slows down to deliver fewer chips to that feeder mechanism F since that mechanism is rotated at a constant rate.
The chips are passed through that feeder mechanism whose details are shown in. the other figures of the drawing, namely by dropping down the top chip inlet 20 of the casing 11(Figure 2). Here, due to the tangential forwardly leaning inclination of the blades 22, the chips complete filling the pocket 23 just passing away from under the inlet, and begins filling the pocket 23 coming into register with the inlet 20. This feeding first to the leading edge of a pocket onto its leading inclined blade is important in accomplishing orderly filling of the pockets, and filling them completely. As the filled pocket moves forward, the chips in its top encounter the wiper blade which removes excess chips, slivers, and sawdust from the top of the seals 33.
Continued rotation of the rotor 15 of the feeder brings the load of chips in each pocket successively into zones of increasing steam pressure Z Z and Z (Figure 9) so that the chips are sequentially brought up to the digester pressure (120 p. s. i. g.) that is being maintained in the treatment tank T. When a pocket comes into register or alignment with the bottom chip outlet, they fall from the pocket into the tank T, and here again the tangential forward inclination of the blades helps also in the discharge of the chips as it did in their loading into the pocket. On the return path of the now-empty pocket, it passes upwardly sequentially through zones of diminishing steam pressure Z Z, to Z whose pressure is atmospheric. However, as has been repeatedly proven in other designs of pocket feeders, there is a greater tendency for steam pressure to be trapped in the pocket rising in Z because of inadequate means for removal of this steam, the pressure in Z will act upwards to prevent chips from entering the pocket so it has been found helpful to provide, at this point, the final steam exhaust duct 75 and its hood 74, connected to exhaust fan 76, that is effective in forcibly reducing the steam pressure in Z to atmospheric or less so that as it comes in register with the chip inlet 20 that is full of descending chips, it thereby insures the positive filling of Z with chips. The residual steam in a pocket coming into register with the chips inlet is highly expanded, and it has been found that even a small amount of such ex panded steam remaining in a pocket significantly retards its being loaded with a new supply of chips.
A rotary feeder of this type is subjected to difiicult conditions of temperature change, abrasion, wear, steam loss, and so on, but they all seem to be compensated for in the design of this invention and where wear cannot be resisted, the wear-receiving seals have been made readily renewable.
As this invention may be embodied in several forms without departing from the spirit or essential characteristic thereof, the present embodiment is therefore illustrative and not restrictive, since the scope of the invention is defined in the appended claims and all changes that fall within the metes and bounds of the claims or that form their functional as well as conjointly cooperative equivalents, are therefore intended to be embraced by those claims.
We claim:
1. Continuously operable wood-chip digestion apparatus including an enclosed chamber adapted to subject such chips therein to steam-induced temperature and pressure; means for evacuating treated chips from the bottom of the chamber; a bin for receiving and holding a supply of chips to be so treated; means for discharging chips from the bin at a substantially uniform rate; and means for receiving such discharging chips and moving them to enter the chamber while minimizing escape therefrom of steam and pressure which comprises a casing with a bore having a top chip inlet connected with the chip-discharging means associated with the bin and a of chips rises above the Z 2 and finally bottom chip outlet connected with the chamber, a moti-w v'ated rotor having a horizontal axle in the casing and a hub with a plurality of vanes extending from the hub to the periphery of the bore of the casing with a chipcarrying pocket formed between pairs of sequentially adjacent vanes which during rotation of the rotor receives chips from the top inlet when in register therewith and delivers chips through the outlet from the casing when in register therewith, and means for incrementally increasing steam pressure in sequential superposed zones in the bore of the casing through which the pockets pass on their path toward the chamber from a pressure at the inlet equal to atmospheric to a pressure at the outlet equal to that in the chamber and the reverse on their return path toward the inlet whereby corresponding pairs of pockets on each vertical side of the axle are under the same pressure.
2. Apparatus according to claim 1, wherein of a pair of sequentially adjacent vanes forming a pocket therebetween, the trailing vane of the pair extends parallel to the first encountered wall of the chip inlet into the casing when a pocket is in register with that inlet.
3. Apparatus according to claim 1, wherein both the chip inlet into the casing and pocket the chip outlet from the casing is larger than the mouth of one pocket whereby they always have Opening thereinto at least a portion of two pockets.
4. Apparatus according to claim 1, wherein that wall of the chip inlet to the casing first passed under by a moving pocket there is a steam escape conduit with which the moving pocket comes into register.
5. Apparatus according to claim 1, wherein the wall of the chip inlet to the casing second passed under by the moving pocket there are wiping means extending from the inlet for removing chips and slivers as well as sawdust from the vanes and their seals.
6. Apparatus according to claim 1, wherein at the free end edges of the vanes there is a replaceable seal outwardly pressed against the casing, and means are provided in the chip inlet to the casing for removing the replaceable seals therethrough and therefrom.
7. Apparatus according to claim 1, wherein in the top chip inlet there are means for conducting pressure from a pocket open to the inlet to the atmosphere.
8. Apparatus according to claim 1, wherein in the top chip inlet there are means for conducting pressure from a pocket open to the inlet to a fan which in turn transfers such pressure to the atmosphere.
9. Apparatus according to claim 1, wherein in the top chip inlet there are hooded conduit means for conducting pressure from a pocket open to the inlet to the atmosphere.
l0. Continuously operable wood-chip digestion apparatus including an enclosed pressure-containing chamber adapted to subject such chips therein to steam-induced temperature and pressure, a bin for receiving and holding a supply of chips to be treated, and means for receiving chips therefrom and transporting them to and into the chamber without fiber-degrading mechanical compaction on the chips While minimizing escape from the chamber of steam and pressure; said latter means comprising an'open-ended casing with a bore therein having a top chip inlet from the bin at atmospheric pressure and a bottom chip outlet to the chamber at the super pressure existing in the chamber, an axle in the bore, a rotor secured to rotate with the axle having a. plurality of intersecting vanes extending from the rotor forming between each pair of adjacent vanes a chip-receiving and chip-carrying pocket, a first pressure-receiving manifold drawing off pressure from a passing pocket along a longitudinal line just in advance of the wall of the top chip-inlet first passed under by passing pockets, a first pressure-transmitting manifold delivering along a longitudinal line just in advance of the wall of the bottom 7 chip-outlet first passed under by passing pockets pressure References Cited in the file of this patent re'ceivedflfrom a passing pocket to the pressure-receiving UN TE J A PATENTS manifold for thus equalizing pressure within two dia- ,p t I metrically. positioned pockets, a secondpressure-receiving manifolddrawing oil pressure from a passing pocket j j g 1937 along a longitudinal line in a horizontal plane with the 2161553 Wes'tberg gg June 1939' axle, and a secondpressure-transmitting manifold deliver- 2474862 Richter v 15949 7 y, mg along a longitudinal line 180 removed from the 2680 683 Obenshain June 8 1954 second.pressure-receiving manifold pressure received from 2766911 Graves: i 195-6 the latter passing pocket for thus equalizing pressure 10 .37 4 Savoca, et a1 Jm'le 1957 within two additional diametrically positioned pockets.
FOREIGN PATENTS 862,400 Germany Ian; 12, 1953 UNITED STATES PATENT OFFICE CERTIFICATE OF CORRECTION Patent No, 2,858,212 October 2a, 1958 Leonard Durant at 11,
It is hereby certified that error appears in the printed specification of the above numbered patent requiring correction and that the said Letters Patent should read as corrected below.
Column 6, line 24, after "and" strike out pocket Signed and sealed this 16th. day of February 1960 (SEAL) Attest:
KARL Ho AXLINE ROBERT C. WATSON Attesting ()fiicer Commissioner of Patents

Claims (1)

1. CONTINUOUSLY OPERABLE WOOD-CHIP DIGESTION APPARATUS INCLUDING AN ENCLOSED CHAMBER ADAPTED TO SUBJECT SUCH CHIPS THEREIN TO STEAM-INDUCED TEMPERATURE AND PRESSURE; MEANS FOR EVACUATING TREATED CHIPS FROM THE BOTTOM OF THE CHAMBER; A BIN FOR RECEIVING AND HOLDING A SUPPLY OF CHIPS TO BE SO TREATED; MEANS FOR DISCHARGING CHIPS FROM THE BIN AT A SUBSTANTIALLY UNIFORM RATE; AND MEANS FOR RECEIVING SUCH DISCHARGING CHIPS AND MOVING THEM TO ENTER THE CHAMBER WHILE MINIMIZING ESCAPE THEREFROM OF STEAM AND PRESSURE WHICH COMPRISES A CASING WITH A BORE HAVING A TOP CHIP INLET CONNECTED WITH THE CHIP-DISCHARGING MEANS ASSOCIATED WITH THE BIN AND A BOTTOM CHIP OUTLET CONNECTED WITH THE CHAMBER, A MOTIVATED ROTOR HAVING A HORIOZONTAL AXLE IN THE CASING AND A HUB WITH A PLURALITY OF VANES EXTENDING FROM THE HUBTO THE PERIPERY OF THE BORE OF THE CASING WITH A CHIPCARRYING POCKET FORMED BETWEEN PAIRS OF SEQUENTIALLY ADJACENT VANES WHICH DURING ROTATION OF THE ROTOR RECEIVES CHIPS FROM THE TOP INLET WHEN IN REGISTER THEREWITH AND DELIVERS CHIPS THROUGH THE OUTLET FROM THE CASING WHEN IN REGISTER THEREWITH, AND MEANS FOR INCREMENTALLY INCREASING STEAM PRESSSURE IN SEQUENTIAL SUPERPOSED ZONES IN THE BORE OF THE CASING THROUGH WHICH THE POCKETS PASS ON THEIR PATH TOWARD THE CHAMBER FROM A PRESSURE AT THE INLET EQUAL TO ATMOSPHERIC TO A PRESSURE AT THE OUTLET EQUAL TO THAT IN THE CHAMBER AND THE REVERSE ON THEIR RETURN PATH TOWARD THE INLET WHEREBY CORRESPONDING PAIRS OF POCKETS ON EACH VERTICAL SIDE OF THE AXLE ARE UNDER THE SAME PRESSURE.
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Cited By (38)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2917344A (en) * 1959-02-02 1959-12-15 Ripco Inc Feed apparatus for granular material
US2933208A (en) * 1957-12-18 1960-04-19 Spront Waldron & Company Inc Pulp manufacture
US2985340A (en) * 1956-11-05 1961-05-23 Clarence W Vogt Blowing head for packaging apparatus
US3009744A (en) * 1958-09-17 1961-11-21 Fuller Co Unloading and conveying apparatus
US3011773A (en) * 1958-01-13 1961-12-05 Metz Paul Apparatus for adding materials in gaseous suspension to metals
US3052383A (en) * 1959-12-28 1962-09-04 Sherman T Transeau Rotary feeder mechanism
US3080074A (en) * 1959-10-16 1963-03-05 Beloit Iron Works Pressure chamber feeder
US3151784A (en) * 1961-10-24 1964-10-06 John P Tailor Rotary air lock
US3171693A (en) * 1962-06-15 1965-03-02 Jr Merle H Gillespie Pneumatic means for feeding cementitious materials
US3178237A (en) * 1963-05-21 1965-04-13 Koppers Co Inc Rotary feeder
US3178235A (en) * 1963-03-29 1965-04-13 Koppers Co Inc Rotary feeder
US3201307A (en) * 1962-10-26 1965-08-17 Bauer Bros Co Pulping equipment and system
US3201007A (en) * 1962-11-13 1965-08-17 Sherman T Transeau Rotary feeder mechanism
US3203738A (en) * 1963-01-08 1965-08-31 Vickers Armstrongs Ltd Pumps
US3206254A (en) * 1962-04-09 1965-09-14 Buell Engineering Company Inc Material handling apparatus
US3219393A (en) * 1961-10-05 1965-11-23 Bauer Bros Co Rotary valve
US3249263A (en) * 1963-07-25 1966-05-03 Phillips Petroleum Co Particulate material feeding
US3249219A (en) * 1964-11-13 1966-05-03 J J Res & Dev Inc Separation of nutmeat fragments from shell fragments
US3273758A (en) * 1964-02-28 1966-09-20 Bauer Bros Co Rotary valve
US3315824A (en) * 1965-05-25 1967-04-25 Pulpamac Inc Method and apparatus for continuous gravity feed of fluent materials
US3347741A (en) * 1964-01-13 1967-10-17 Crane Co Feeder for solid materials
US3516714A (en) * 1966-03-23 1970-06-23 Beloit Corp Chip feeder valve
US3809056A (en) * 1971-01-12 1974-05-07 A Snelling Smoke producers
US3993227A (en) * 1975-09-08 1976-11-23 Esco Corporation Rotary feeder valve
US4111493A (en) * 1977-03-16 1978-09-05 Henry Sperber Feeding apparatus for a pneumatic conveying system
US4155486A (en) * 1977-10-25 1979-05-22 Brown Winfred E Rotary feeder
US4180188A (en) * 1975-11-18 1979-12-25 Kokkoman Shoyu Co., Ltd. Sealing structure for rotary valves
US4231495A (en) * 1978-02-23 1980-11-04 Rader Companies, Inc. Rotary feeder for pneumatic conveying line
US4397657A (en) * 1982-04-19 1983-08-09 Allis-Chalmers Corporation Gas lock system charging particles into a pressurized gasification reactor
US4462740A (en) * 1979-11-28 1984-07-31 Luaaron Metals Ltd. Rotary charger
US5044837A (en) * 1989-09-14 1991-09-03 Phillips Petroleum Company Method and apparatus for continuously feeding particulate solid material into a pressurized system without pressure loss
US5324143A (en) * 1993-01-28 1994-06-28 Sanders Kenneth L Pneumatic grain conveyor and related method
US5544995A (en) * 1993-01-22 1996-08-13 Japan Tobacco Inc. Rotary valve apparatus
US6196154B1 (en) * 1998-02-19 2001-03-06 Leybold Systems Gmbh Air lock for introducing substrates to and/or removing them from a treatment chamber
US20080093391A1 (en) * 2006-10-20 2008-04-24 F.L.Smidth A/S Feeder assembly for bulk solids
US20110049198A1 (en) * 2009-08-26 2011-03-03 Battelle Energy Alliance, Llc Rotary feeders, rotor assemblies for rotary feeders and related methods
US20110185908A1 (en) * 2008-06-30 2011-08-04 Koninklijke Philips Electronics N.V. Device for separating different enclosed spaces and for dosing a food product and machine incorporating said device
US9902561B2 (en) 2015-10-29 2018-02-27 General Electric Company System for discharging dry solids and an associated method thereof

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US1505934A (en) * 1921-12-01 1924-08-19 Olier Sa Ets A Device for the continuous treatment of ligneous materials for their transformation in cellulose
US1871507A (en) * 1929-04-01 1932-08-16 Gardner Mfg Company Ltd Fruit processor
US2084764A (en) * 1935-03-29 1937-06-22 Fuller Co Conveying bulk materials
US2161553A (en) * 1935-09-30 1939-06-06 Westberg Gustave Edward Means of conveying and mixing comminuted material
US2474862A (en) * 1942-10-15 1949-07-05 Kamyr Ab Process and apparatus for continuous digestion of fibrous materials
DE862400C (en) * 1949-10-21 1953-01-12 Kamyr Ab Rotary valve for pulp digester
US2766911A (en) * 1951-11-26 1956-10-16 Grenco Inc Material handling valve
US2680683A (en) * 1951-12-06 1954-06-08 West Virginia Pulp & Paper Co Charging and discharging mechanism for use in continuous cooking of chips in the manufacture of pulp
US2794772A (en) * 1953-03-16 1957-06-04 Socony Mobil Oil Co Inc Method and apparatus for the removal of granular solids from a columnar mass thereof

Cited By (42)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2985340A (en) * 1956-11-05 1961-05-23 Clarence W Vogt Blowing head for packaging apparatus
US2933208A (en) * 1957-12-18 1960-04-19 Spront Waldron & Company Inc Pulp manufacture
US3011773A (en) * 1958-01-13 1961-12-05 Metz Paul Apparatus for adding materials in gaseous suspension to metals
US3009744A (en) * 1958-09-17 1961-11-21 Fuller Co Unloading and conveying apparatus
US2917344A (en) * 1959-02-02 1959-12-15 Ripco Inc Feed apparatus for granular material
US3080074A (en) * 1959-10-16 1963-03-05 Beloit Iron Works Pressure chamber feeder
US3052383A (en) * 1959-12-28 1962-09-04 Sherman T Transeau Rotary feeder mechanism
US3219393A (en) * 1961-10-05 1965-11-23 Bauer Bros Co Rotary valve
US3151784A (en) * 1961-10-24 1964-10-06 John P Tailor Rotary air lock
US3206254A (en) * 1962-04-09 1965-09-14 Buell Engineering Company Inc Material handling apparatus
US3171693A (en) * 1962-06-15 1965-03-02 Jr Merle H Gillespie Pneumatic means for feeding cementitious materials
US3201307A (en) * 1962-10-26 1965-08-17 Bauer Bros Co Pulping equipment and system
US3201007A (en) * 1962-11-13 1965-08-17 Sherman T Transeau Rotary feeder mechanism
US3203738A (en) * 1963-01-08 1965-08-31 Vickers Armstrongs Ltd Pumps
US3178235A (en) * 1963-03-29 1965-04-13 Koppers Co Inc Rotary feeder
US3178237A (en) * 1963-05-21 1965-04-13 Koppers Co Inc Rotary feeder
US3249263A (en) * 1963-07-25 1966-05-03 Phillips Petroleum Co Particulate material feeding
US3347741A (en) * 1964-01-13 1967-10-17 Crane Co Feeder for solid materials
US3273758A (en) * 1964-02-28 1966-09-20 Bauer Bros Co Rotary valve
US3249219A (en) * 1964-11-13 1966-05-03 J J Res & Dev Inc Separation of nutmeat fragments from shell fragments
US3315824A (en) * 1965-05-25 1967-04-25 Pulpamac Inc Method and apparatus for continuous gravity feed of fluent materials
US3516714A (en) * 1966-03-23 1970-06-23 Beloit Corp Chip feeder valve
US3809056A (en) * 1971-01-12 1974-05-07 A Snelling Smoke producers
US3993227A (en) * 1975-09-08 1976-11-23 Esco Corporation Rotary feeder valve
US4180188A (en) * 1975-11-18 1979-12-25 Kokkoman Shoyu Co., Ltd. Sealing structure for rotary valves
US4111493A (en) * 1977-03-16 1978-09-05 Henry Sperber Feeding apparatus for a pneumatic conveying system
US4155486A (en) * 1977-10-25 1979-05-22 Brown Winfred E Rotary feeder
US4231495A (en) * 1978-02-23 1980-11-04 Rader Companies, Inc. Rotary feeder for pneumatic conveying line
US4462740A (en) * 1979-11-28 1984-07-31 Luaaron Metals Ltd. Rotary charger
EP0092931A3 (en) * 1982-04-19 1984-07-11 Allis-Chalmers Corporation Gas lock system for charging particles into a pressurized reactor
EP0092931A2 (en) * 1982-04-19 1983-11-02 Allis-Chalmers Corporation Gas lock system for charging particles into a pressurized reactor
US4397657A (en) * 1982-04-19 1983-08-09 Allis-Chalmers Corporation Gas lock system charging particles into a pressurized gasification reactor
US5044837A (en) * 1989-09-14 1991-09-03 Phillips Petroleum Company Method and apparatus for continuously feeding particulate solid material into a pressurized system without pressure loss
US5544995A (en) * 1993-01-22 1996-08-13 Japan Tobacco Inc. Rotary valve apparatus
CN1062063C (en) * 1993-01-22 2001-02-14 日本烟草产业株式会社 Rotary valve apparatus
US5324143A (en) * 1993-01-28 1994-06-28 Sanders Kenneth L Pneumatic grain conveyor and related method
US6196154B1 (en) * 1998-02-19 2001-03-06 Leybold Systems Gmbh Air lock for introducing substrates to and/or removing them from a treatment chamber
US20080093391A1 (en) * 2006-10-20 2008-04-24 F.L.Smidth A/S Feeder assembly for bulk solids
US7757903B2 (en) * 2006-10-20 2010-07-20 Flsmidth A/S Feeder assembly for bulk solids
US20110185908A1 (en) * 2008-06-30 2011-08-04 Koninklijke Philips Electronics N.V. Device for separating different enclosed spaces and for dosing a food product and machine incorporating said device
US20110049198A1 (en) * 2009-08-26 2011-03-03 Battelle Energy Alliance, Llc Rotary feeders, rotor assemblies for rotary feeders and related methods
US9902561B2 (en) 2015-10-29 2018-02-27 General Electric Company System for discharging dry solids and an associated method thereof

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