Impregnation with black liquor prior to white liquor introduction

Description

BACKGROUND AND SUMMARY OF THE INVENTION

[0001] For several decades, continuous cooking of comminuted cellulosic fibrous material (e.g. wood chips) to produce pulp, particularly kraft pulp, has been an extremely efficient system for producing the pulp. Whenever continuous cooking is practiced, however, care must be taken to ensure uniformity of the end product. An important part of ensuring uniform quality of the end product is ensuring proper impregnation of the material with cooking liquor (white liquor). It has long been known that freshly cut wood, with high moisture content, will impregnate quickly and uniformly, whereas stored wood, with low moisture and high air content, requires efficient presteaming and favorable impregnation conditions in order to be uniformly impregnated. Despite the fact that this has been known for many years, this fact has not normally been effectively utilized to ensure uniform impregnation of cellulosic material, such as wood chips.

[0002] As energy conservation becomes more important, it also becomes important to minimize energy use during cooking. Typically, a substantial amount of energy in the form of high pressure steam is consumed in a continuous pulping facility by heating the white liquor to an appropriate cooking temperature (e.g. approximately 160-180°C), and also for heating of the impregnation liquor, e.g black liquor.

[0003] According to the present invention, a method of continuously treating comminuted cellulosic fibrous material to produce paper pulp, particularly kraft pulp, is provided which has enhanced uniformity and minimized energy requirements. According to the present invention, a method is provided of continuously treating comminuted cellulosic fibrous material to produce kraft pulp, comprising the steps of continuously:

(a) slurrying comminuted cellulosic fibrous material with liquid to produce a slurry:

(b) feeding the slurry into an impregnation zone;

(c) impregnating the slurry with heating and soaking liquid in the impregnation zone;

(d) feeding the slurry from the impregnation zone into a cooking zone;

(e) treating the slurry with kraft cooking liquor at cooking temperature in the cooking zone to effect digestion of the material in the slurry, to produce kraft pulp;

(f) withdrawing black liquor from the cooking zone, at cooking temperature; and.

(g) feeding at least a portion of the black liquor withdrawn in step (f) to the impregnation zone to provide at least a part of the impregnation liquid in step (c).

[0004] The latter is described in US-A-3 303 088.

[0005] Our invention is distinguished from US-A-3 303 088 in that said slurrying is effected in a high-pressure feeder and that said impregnation in step (c) is effected by rapid displacement heating of the comminuted cellulosic fibrous material by introducing black liquor, substantially at cooking temperature, then effecting rapid diffusion impregnation by introducing white liquor into the material in order to effect continuous kraft cooking of the material.

[0006] Hence, in contrast to US-A-3 303 088 our invention teaches the use of rapid displacement heating of the fibrous material by introducing black liquor substantially at cooking temperature, i.e. according to our invention the existing moisture within the chips (e.g. condensate from the steaming) is displaced by hot black liquor which provides for an effective heating and impregnation of the chips, and also other advantages.

[0007] The chips which now are impregnated with hot black liquor, are highly amenable to the diffusion of chemicals. Accordingly the effective chemicals of the white liquor, which are introduced after the impregnation, will very quickly move into each chip and start the actual digesting process.

[0008] There is preferably also the further step (h) of preheating the cooking liquor before feeding it into cooking zone by passing it into heat exchange relationship with a first portion of the black liquor withdrawn in step (f), while a second portion of the black liquor withdrawn in step (f) is used in step (g).

[0009] Step (b) may be practiced in part by withdrawing a portion of the liquid from the slurry at a withdrawal area above the impregnation zone, pressurizing the withdrawn liquid, and introducing the pressurized withdrawn liquid into the slurry, above the withdrawal area, with a primarily downward vector. Steps (c) and (g) are preferably practiced by withdrawing a portion of the liquid from the slurry in the impregnation zone at a withdrawal area, recirculating the withdrawn liquid back into the impregnation zone above the withdrawal area, and adding black liquor from step (f) to the recirculating withdrawn liquid. Step (a) is preferably practiced by slurrying the material with black liquor. Steps (b)-(f) are preferably practiced in a single vertical vessel, the material moving downwardly in the vessel during treatment.

[0010] According to a still further aspect of the present invention, a method of treating a slurry of comminuted cellulosic fibrous material in an upright vessel having a top and bottom, and at least first, second, and third sets of screens, vertically spaced from each other with the first set of screens the topmost screens, and the third set the bottom most, is provided. This method comprises the steps of: (a) Introducing the slurry into the top of the vessel, to flow downwardly therein. (b) Withdrawing a part of the liquid from the slurry with the first set of screens, and recirculating the withdrawn liquid back into the vessel above the first set of screens. (c) Withdrawing a part of the liquid from the slurry with the second set of screens, and recirculating the withdrawn liquid back into the vessel above the second set of screens. (d) Withdrawing a part of the liquid from the slurry with the third set of screens, and passing at least a portion of the withdrawn liquid from the third set of screens into the withdrawn liquid from the first set of screens, to be introduced into the vessel with the recirculated liquid from step (b). And, (e) discharging pulp from the bottom of the vessel, below the third set of screens. A fourth set of screens is also preferably utilized, above the first set. Liquid is withdrawn through the fourth set of screens, pressurized, and then introduced above the fourth set of screens with a substantially downward velocity vector so as to assist in movement of the material.

[0011] It is the primary object of the present invention to provide for the continuous cooking of pulp with substantial energy economy and simultaneously improved uniformity of the end product. This and other objects of the invention will become clear from an inspection of the detailed description of the invention, and from the appended claims.

BRIEF DESCRIPTION OF THE DRAWING

[0012] FIGURE 1 is a schematic view of an exemplary apparatus for practice of the method according to the present invention.

DETAILED DESCRIPTION OF THE DRAWING

[0013] Many of the components of the apparatus illustrated in FIGURE 1 are the same as, or comparable to, parts of the apparatus of US-A-3,802,956. That patent shows apparatus for effecting continuous pulping, particularly kraft pulping, of comminuted cellulosic fibrous material, with a view toward proper impregnation of the material.

[0014] Apparatus of the system of FIGURE 1 that is generally comparable to that in said patent 3,802,956 includes a chips bin 11 (which may be a steaming chips bin), communicating with a low pressure valve 13 with a conventional steaming vessel 14. Low pressure steam, e.g. one atmosphere over pressure, is supplied to the vessel 14 through a conduit 15, and air is driven off through conduit 17. The chips ultimately pass through chute 18 into the conventional high pressure feeder 19, circulating liquid being forced by pump 20 to entrain chips -- or like cellulosic fibrous material -- dropping from chute 18 into the transfer device 19 in the circulating liquid.

[0015] According to the invention, the chips from high pressure feeder 19 pass in conduit 21 to the top of a substantially vertical digester 22. The slurry of chips in liquid passes into apparatus at the top of the digester 22 for separating a portion of the liquid, the apparatus preferably comprising a strainer girdle 25 with a feed screw 27 therein, and the withdrawn liquid passing in conduit 23 back to the pump 20. A screen 28 is provided adjacent to the top of the digester 22, but below the girdle 25 and screw 27, connected to pump 26, which in turn is connected to nozzles 24. A portion of the liquid withdrawn from the slurry through screen 28 is pressurized by pump 26 and then forced through the nozzles 24 back into the vessel, above the screen 28, with a substantially downward velocity vector. This system is primarily for producing a downward thrust on the material for operational purposes, so that it flows concurrently with liquid initially down into the digester 22. A portion of the liquid withdrawn by screen 28 is passed via conduit 30 to the second effect 90 of a flash tank system, as hereinafter described.

[0016] The chips are flushed into the high pressure feeder 19 through chute 18 via liquid flowing in loop 37 under the influence of pump 35. Excess liquid passes into level tank 39 and is returned therefrom through conduit 41 and pump 29 to the high pressure side. Additionally, make-up liquor --which may be black liquor from source 33, white liquor from source 31, or a combination of both (as metered by valve 48), and valves 10, 12, may be provided. This liquid passes to the top exterior of the strainer girdle 25 -- i.e. the high pressure loop -- via conduit 50.

[0017] Below the screen 28 adjacent the top of the vessel 22 is an impregnation zone. A screen 40, connected to a pump 42, is provided in the impregnation zone. The pump 42 withdraws a portion of the liquid from the slurry moving downwardly in the vessel 22, and recirculates it in loop 43 to the inlet tube 46 above the screen 40. Liquid introduced thereby tends to flow countercurrently to the chips moving downwardly in the vessel 22, ultimately being withdrawn by screen 28. A heater, such as an indirect heater (heating liquid with steam), may be provided in the circulation loop 43, but is not necessary according to the invention.

[0018] Below the screen 40, cooking zone is provided. Within the impregnation and cooking zone are one or more screens 63, 87, and 92. A portion of the liquid in the slurry moving downwardly at the screen 63 is withdrawn therefrom via pump 65, and passed through conventional indirect steam heater (heat exchanger) 67 to be heated, the withdrawn liquid being recirculated and introduced at central return conduit 69 into the chips column above the screen 63. According to the present invention, kraft cooking liquor (white liquor) from source 31 may be pumped by pump 36 to this recirculation loop, e.g. added to the pump 65 to be introduced with the recirculated liquid.

[0019] The screens 87 and 92 withdraw black liquor from the digester 22. A portion of the black liquor withdrawn by screen 92 under the influence of pump 93 may be recirculated into the digester 22 and introduced at central conduit 95, while another portion passes through valve 32 ultimately to the second stage flash tank 90. The conduct 91 from the bottom of the flash tank 90 may be used to supply black liquor to the source 33. Also, according to the present invention, black liquor withdrawn through screen 87 passes into conduit 110, which is connected to the circulation loop 43 including the pump 42, so that it is introduced at the return conduit 46 into the vessel. The black liquor in conduit 110 is substantially at cooking temperature (e.g. about 160-180°C).

[0020] Another portion of the liquor withdrawn with screens 87 -- which also is at substantially cooking temperature -- is used to preheat white liquor introduced from source 31 into pump 65. This may preferably be accomplished by passing the conduit 112 and the conduit 38 into a heat exchanger 114, whereby the black hot liquor in conduit 112 comes into heat exchange relationship with the cool white liquor in conduit 38, preheating it before it is introduced into pump 65. Typically, the heat exchanger 114 would preheat the white liquor from about 70°C to about 160°C. Little additional energy input is required from the heater 67. After losing a substantial portion of its heat value in heat exchanger 114, the remaining black liquor in conduit 112 is passed to a first stage flash tank 89.

[0021] The arrangement described above, in addition to obviously minimizing energy requirements, also effects very uniform impregnation. The black liquor introduced from conduit 110 soaks and heats the chips, effecting rapid displacement heating thereof. This rapid displacement heating makes the chips much more amenable to impregnation with white liquor. That means when the chips pass downwardly into the cooking zone, and are confronted with hot white liquor, rapid diffusion impregnation of the chips with white liquor occurs. The chips are then cooked at a temperature of about 160-180°C, and then passed downwardly into the lower part of the digester 22 where they are preferably washed.

[0022] Near the bottom of the vessel 22 a screen 79 is connected to a pump 81 heater 83, and central supply conduit 85. Washing liquid is introduced into the conduit 71 to flow countercurrently (that is upwardly) with respect to the downward flowing chips, with a portion of the liquid being withdrawn through screen 79, heated, and recirculated back into conduit 85. The washed, kraft pulp, may then be discharged from the bottom of the vessel utilizing a conventional rotary scraper 99, and a throttling device 101 if desired.

[0023] While the method has been described with respect to a single upright vessel 22, the method may be practiced otherwise (e.g. with more than one vessel), although the single vessel arrangement of FIGURE 1 is greatly preferred.

[0024] According to one aspect of the method of the present invention, a slurry of comminuted cellulosic fibrous material (e.g. wood chips) in liquid (e.g. black liquor combined with steam which condensed on the chips from steaming vessel 14, and any natural liquid in the chips) is fed to the top of the digester 22, and under the influence of the downwardly directed flow of liquid from nozzles 24 moves downwardly in the vessel 22. At a first set of screens 40 part of the liquid in the slurry may be removed, and introduced back into the vessel, with black liquor withdrawn through screen 87 by conduit 110 being introduced into the recirculation loop 43. Thus in the vicinity of the screen 40, and above, the chips are soaked and heated, the black liquor in conduit 110 being substantially at cooking temperature. This rapid displacement heating of the chips makes them susceptible to subsequent impregnation during the continuous processing thereof.

[0025] As the chips move downwardly further in the vessel 22 they encounter the second set of screens 63. A portion of the liquid is withdrawn therethrough, heated by heater 67, and reintroduced by central conduit 69. White liquor from source 31, pumped by pump 36, in conduit 38 is added to the pump 65 in this recirculation loop. Preferably the white liquor is preheated by passing it through the heat exchanger 114, in heat exchange relationship with black liquor in conduit 112. Since the chips are susceptible to impregnation due to their soaking and heating by rapid displacement heating, rapid diffusion impregnation of the chips with white liquor occurs adjacent the screen 63 and thereabove. Below the screen 63, kraft cooking of the chips takes place. The chips are ultimately washed at or above screen 79, and are subsequently discharged from the bottom of the vessel.

[0026] It will thus be seen that according to the present invention a method of effecting substantial energy economy while simultaneously improving uniformity of the pulp produced in a continuous kraft pulping process, is provided.

Claims

1. A method of continuously treating comminuted cellulosic fibrous material to produce kraft pulp, comprising the steps of continuously:

(a) slurrying comminuted cellulosic fibrous material with liquid to produce a slurry:

(b) feeding the slurry into an impregnation zone;

(c) impregnating the slurry with heating and soaking liquid in the impregnation zone;

(d) feeding the slurry from the impregnation zone into a cooking zone;

(e) treating the slurry with kraft cooking liquor at cooking temperature in the cooking zone to effect digestion of the material in the slurry, to produce kraft pulp;

(f) withdrawing black liquor from the cooking zone, at cooking temperature; and.

(g) feeding at least a portion of the black liquor withdrawn in step (f) to the impregnation zone to provide at least a part of the impregnation liquid in step (c), characterized in that said slurrying is effected in a high-pressure feeder (19) and that said impregnation in step (c) is effected by rapid displacement heating of the comminuted cellulosic fibrous material by introducing black liquor (46), substantially at cooking temperature, then effecting rapid diffusion impregnation by introducing white liquor (31, 69) into the material in order to effect continuous kraft cooking of the material.

2. A method as recited in claim 1 wherein step (a) is practiced utilizing black liquor (33) as the slurrying liquid.

3. A method as recited in claim 2 wherein step (e) is practiced by preheating the white liquor (31) before feeding it into the cooking zone by passing it in heat exchange relationship (114) with a first portion of the black liquor withdrawn in step (f), while a second portion of the black liquor withdrawn in step (f) is used in step (g).

4. A method as recited in claim 3 comprising the further step of further heating the cooking liquor, after preheating thereof in step (h), by passing it into indirect heating relationship (67) with steam.

5. A method as recited in claim 1 wherein step (b) is practiced by introducing the white liquor (69) substantially at cooking temperature.

6. A method as recited in claim 3 comprising the further step of (i) introducing the first portion of black liquor, after practice of step (h), into a flash tank (89).

7. A method as recited in claim 1 wherein step (b) is practiced by withdrawing a portion of the liquid from the slurry at a withdrawal area (28) above the zone, pressurizing (26) the withdrawn liquid, and introducing the pressurized withdrawn liquid back into the slurry, above the withdrawal area, with a primarily downward vector.

8. A method as recited in claim 1 wherein steps (c) and (g) are practiced by withdrawing a portion of the liquid from the slurry in the zone at a withdrawal area (40), recirculating (43) the withdrawn liquid back into the zone above the withdrawal area, and adding black liquor (110) from step (f) to the recirculating withdrawn liquid.

9. A method as recited in claim 1 wherein step (e) is further practiced by withdrawing liquid from the cooking zone at a withdrawal area (63), recirculating the withdrawn liquid back to the cooking zone at a point (69) above the withdrawal area, and adding the kraft cooking liquor (31) to the recirculating withdrawn liquid.

10. A method as recited in claim 9 wherein steps (c) and (g) are practiced by withdrawing a portion of the liquid from the slurry in the zone at a withdrawal area, recirculating the withdrawn liquid back into the zone above the withdrawal area, and adding black liquor from step (f) to the recirculating withdrawn liquid.

11. A method as recited in claim 10 wherein step (b) is practiced by withdrawing a portion of the liquid from the slurry at a withdrawal area (28) above the impregnation zone, pressurizing (26) the withdrawn liquid, and introducing the pressurized withdrawn liquid back into the slurry, above the withdrawal area, with a primarily downward vector.

12. A method as recited in claim 11 wherein steps (b) - (f) are practiced in a single vertical vessel (22), and wherein steps (b) and (d) are practiced by feeding the slurry downwardly.

Ansprüche

1. Verfahren zur kontinuierlichen Behandlung zerkleinerten Cellulosefasermaterials zur Herstellung von Kraftzellstoff, bei dem man stufenweise kontinuierlich:

a) zerkleinertes Zellstoffasermaterial mit Flüssigkeit zu einem Stoff aufschlämmt,

b) den Stoff in eine Imprägnierungszone einführt,

c) den Stoff in der Imprägnierungszone mit Heiz- und Tränkungsflüssigkeit imprägniert,

d) den Stoff aus der Imprägnierungszone in eine Kochzone überführt,

e) den Stoff in der Kochzone bei der Kochtemperatur mit Kraftkochlauge behandelt, um das Material in dem Stoff zur Herstellung von Kraftzellstoff aufzuschließen,

f) Schwarzlauge bei der Kochtemperatur aus der Kochzone abzieht und

g) mindestens einen Teil der in Stufe f) abgezogenen Schwarzlauge zur Lieferung mindestens eines Teils der Imprägnierflüssigkeit in Stufe c) in die Imprägnierungszone überführt,
   dadurch gekennzeichnet, daß dieses Aufschlämmen in einem Hochdruckzufuhrgefäß (19) erfolgt und daß man diese Imprägnierung in Stufe c) mittels raschem Verdrängungsaufheizen des zerkleinerten Cellulosefasermaterials durch Einführung von Schwarzlauge (46) im wesentlichen bei der Kochtemperatur durchführt und dann eine rasche Diffusionsimprägnierung durch Einführen von Weißlauge (31, 69) in das Material bewirkt, um eine kontinuierliche Kraftkochung des Materials zu erzielen.

2. Verfahren nach Anspruch 1, worin Stufe a) unter Verwendung von Schwarzlauge (33) als Aufschlämmungsflüssigkeit durchgeführt wird.

3. Verfahren nach Anspruch 2, worin Stufe e) durch Vorwärmen der Weißlauge (31) vor deren Einführung in die Kochzone durchgeführt wird, indem man sie in Wärmeaustausch (114) mit einem ersten Teil der in Stufe f) abgezogenen Schwarzlauge bringt, während ein zweiter Teil der in Stufe f) abgezogenen Schwarzlauge in Stufe g) verwendet wird.

4. Verfahren nach Anspruch 3, einschließlich der weiteren Stufe weiteren Erhitzens der Kochlauge nach deren Vorwärmung in Stufe h), indem man sie indirekt mit Dampf erhitzt (67).

5. Verfahren nach Anspruch 1, worin Stufe b) durch Einführen der Weißlauge (69) im wesentlichen bei Kochtemperatur durchgeführt wird.

6. Verfahren nach Anspruch 3, einschließlich der weiteren Stufe i), wobei man nach der Durchführung der Stufe h) den ersten Teil der Schwarzlauge in ein Entspannungsgefäß (89) leitet.

7. Verfahren nach Anspruch 1, worin Stufe b) durch Abzug eines Teils der Flüssigkeit aus dem Stoff in einem Abzugsbereich (28) über der Zone durchgeführt wird, wobei man die abgezogene Flüssigkeit unter Druck setzt (26) und die unter Druck gesetzte abgezogene Flüssigkeit über dem Abzugsbereich vorwiegend nach unten gerichtet in den Stoff zurückführt.

8. Verfahren nach Anspruch 1, worin die Stufen c) und g) durch Abziehen eines Teils der Flüssigkeit aus dem Stoff in der Zone bei einem Abzugsbereich (40) durchgeführt werden, wobei man die abgezogene Schwarzlauge in die Zone über dem Abzugsbereich rezirkuliert (43) und der rezirkulierten abgezogenen Flüssigkeit Schwarzlauge (110) aus Stufe f) zusetzt.

9. Verfahren nach Anspruch 1, worin Stufe e) ferner durch Abziehen von Flüssigkeit aus der Kochzone in einem Abzugsbereich (63) durchgeführt wird, wobei man die abgezogene Flüssigkeit an einer Stelle (69) über dem Abzugsbereich in die Kochzone rezirkuliert und die Kraftkochlauge (31) der rezirkulierten abgezogenen Flüssigkeit zusetzt.

10. Verfahren nach Anspruch 9, worin die Stufen c) und g) durch Abziehen eines Teils der Flüssigkeit aus dem Stoff in der Zone bei einem Abzugsbereich durchgeführt werden, wobei man die abgezogene Flüssigkeit in die Zone über dem Abzugsbereich rezirkuliert und der rezirkulierten abgezogenen Flüssigkeit Schwarzlauge aus Stufe f) zusetzt.

11. Verfahren nach Anspruch 10, worin Stufe b) durch Abziehen eines Teils der Flüssigkeit aus dem Stoff in einem Abzugsbereich (28) über der Imprägnierungszone durchgeführt wird, wobei man die abgezogene Flüssigkeit unter Druck setzt (26) und die unter Druck gesetzte abgezogene Flüssigkeit über dem Abzugsbereich vorwiegend nach unten gerichtet in den Stoff zurückführt.

12. Verfahren nach Anspruch 11, worin die Stufen b) - f) in einem einzigen senkrechten Gefäß (22) durchgeführt werden, und worin die Stufen b) und d) durch abwärts gerichtete Einführung des Stoffs erfolgen.

Revendications

1. Procédé pour traiter en continu une matière cellulosique fibreuse finement broyée pour produire de la pâte kraft, comprenant les étapes qui consistent à, en continu:

(a) mettre en suspension la matière cellulosique fibreuse finement broyée avec un liquide pour produire une suspension;

(b) charger la suspension dans une zone d'imprégnation;

(c) imprégner la suspension de liquide de chauffage et de trempage dans la zone d'imprégnation;

(d) charger la suspension depuis la zone d'imprégnation dans une zone de cuisson;

(e) traiter la suspension avec une liqueur de cuisson kraft à la température de cuisson dans la zone de cuisson, pour effectuer la digestion de la matière dans la suspension, afin de produire une pâte kraft;

(f) soutirer la liqueur noire de la zone de cuisson à la température de cuisson; et

(g) charger au moins une portion de la liqueur noire soutirée dans l'étape (f) vers la zone d'imprégnation afin d'apporter au moins une partie du liquide d'imprégnation dans l'étape (c), caractérisé en ce que l'on effectue ladite mise en suspension dans une caisse d'alimentation haute pression (19) et en ce que l'on effectue ladite imprégnation dans l'étape (c) en chauffant par un déplacement rapide la matière cellulosique fibreuse finement broyée, par introduction de la liqueur noire (46) essentiellement à la température de cuisson, puis en effectuant une imprégnation par diffusion rapide par introduction de la liqueur blanche (31, 69) dans la matière afin d'effectuer une cuisson kraft continue de la matière.

2. Procédé selon la revendication 1, dans lequel on met en oeuvre l'étape (a) en utilisant la liqueur noire (33) comme liquide de mise en suspension.

3. Procédé selon la revendication 2, dans lequel on met en oeuvre l'étape (e) en préchauffant la liqueur blanche (31) avant de la charger dans la zone de cuisson en la faisant passer dans un échangeur de chaleur (114) où se produit un échange de chaleur avec une première portion de la liqueur noire soutirée dans l'étape (f), tandis que l'on utilise dans l'étape (g) une seconde portion de la liqueur noire soutirée dans l'étape (f).

4. Procédé selon la revendication 3, comprenant l'étape supplémentaire qui consiste à poursuivre le chauffage de la liqueur de cuisson, après son préchauffage dans l'étape (h), en la faisant passer dans un dispositif (67) permettant de la chauffer indirectement à l'aide de vapeur d'eau.

5. Procédé selon la revendication 1, dans lequel on met en oeuvre l'étape (b) en introduisant la liqueur blanche (69) essentiellement à la température de cuisson.

6. Procédé selon la revendication 3, comprenant l'étape supplémentaire qui consiste (i) à introduire la première portion de la liqueur noire, après la mise en oeuvre de l'étape (h), dans une cuve de détente (89).

7. Procédé selon la revendication 1, dans lequel on met en oeuvre l'étape (b) en soutirant une portion du liquide de la suspension au niveau d'une région de soutirage (28), au-dessus de la zone, en pressurisant (26) le liquide soutiré et en ré-introduisant le liquide soutiré pressurisé dans la suspension, au-dessus de la région de soutirage, essentiellement de haut en bas.

8. Procédé selon la revendication 1, dans lequel on met en oeuvre les étapes (c) et (g) en soutirant une portion du liquide de la suspension dans la zone, au niveau d'une région de soutirage (40), en faisant recirculer (43) le liquide soutiré vers la zone au-dessus de la région de soutirage, et en ajoutant de la liqueur noire (110) issue de l'étape (f) au liquide soutiré recirculé.

9. Procédé selon la revendication 1, dans lequel, en outre, on met en oeuvre l'étape (e) en soutirant du liquide de la zone de cuisson au niveau d'une région de soutirage (63), en faisant recirculer le liquide soutiré vers la zone de cuisson en un point (69) situé au-dessus de la région de soutirage, et en ajoutant la liqueur de cuisson kraft (31) au liquide soutiré recirculé.

10. Procédé selon la revendication 9, dans lequel on met en oeuvre les étapes (c) et (g) en soutirant une portion du liquide de la suspension dans la zone au niveau d'une région de soutirage, en faisant recirculer le liquide soutiré vers la zone au-dessus de la région de soutirage, et en ajoutant de la liqueur noire issue de l'étape (f) au liquide soutiré recirculé.

11. Procédé selon la revendication 10, dans lequel on met en oeuvre l'étape (b) en soutirant une portion du liquide de la suspension au niveau d'une région de soutirage (28) située au-dessus de la zone d'imprégnation, en pressurisant (26) le liquide soutiré et en réintroduisant le liquide soutiré pressurisé dans la suspension, au-dessus de la région de soutirage, essentiellement de haut en bas.

12. Procédé selon la revendication 11, dans lequel on met en oeuvre les étapes (b) à (f) dans un seul récipient vertical (22) et dans lequel on met en oeuvre les étapes (b) et (d) en chargeant la suspension de haut en bas.

Drawing