CA2066181C - Displacement heating in continuous digesters - Google Patents
Displacement heating in continuous digestersInfo
- Publication number
- CA2066181C CA2066181C CA002066181A CA2066181A CA2066181C CA 2066181 C CA2066181 C CA 2066181C CA 002066181 A CA002066181 A CA 002066181A CA 2066181 A CA2066181 A CA 2066181A CA 2066181 C CA2066181 C CA 2066181C
- Authority
- CA
- Canada
- Prior art keywords
- liquor
- chips
- chamber
- digester
- temperature
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
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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
- D21C7/14—Means for circulating the lye
-
- 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
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- Paper (AREA)
- Chemical And Physical Treatments For Wood And The Like (AREA)
Abstract
An apparatus and method for treating cellulosic wood chips in a digestion process for the liberation of pulp in a caustic hydroxide solution at high pressures and temperatures by delivering preconditioned wood chips to a first chamber (10) and circu-lating a low temperature black liquor through the chamber (10) to preheat the chips, while continuosly feeding the chips through the chamber (10) to a second chamber (21) at high temperature and pressure, circulating high temperature black liquor to the chips in the second chamber (21) to advance them to cooking temperature, feeding white liquor and the chips to a digester (33) for the digestion process over a predetermined period of time, and removing digested pulp and delivering the pulp to a washer with the black liquor for washing being utilized for the first chamber (10), and heating the white liquor through a heat exchange pro-cess with the high temperature black liquor.
Description
6 6 1 ~1 ... .
PATENT APPLICATION
TITLE
Displacement Heating in Continuous Digesters TECHNICAL FIELD OF THE INVENTION
- The present invention relates to improvements in apparatus and methods for the fiber liberating digestion of continuously fed comminuted cellulosic fiber material by cooking liquor and subsequent washing of the liberated fiber material. More particularly, the invention relates to an improved apparatus and process utilizing spent black liquor for heating the chips to effect savings in thermal energy, and for accomplishing high sulfidity cooking without changes to the overall sulfide balance of the system to accomplish a pulp having improved mechanical characteristics, to improve pulp yield, and to achieve extended delignification.
BACKGROUND OF THE INVENTION
In producing chemical wood pulps, it has become the practice to use cooking liquors cont~;n;ng various cooking chemicals for liberating the pulp fibers. The so-called kraft or sulphate pulp is produced by cooking the raw chipped wood in a liquor wherein materials such as sodium hydroxide and sodium sulfide serve as the essential fiber liberating chemicals. The so-called soda pulp derives its name from the caustic soda-cont~;n;ng cooking liquor which is produced, namely a liquor cont~;n;ng principally caustic soda as the active pulping chemical. There are modifications of these processes based on the use of liquors cont~in;ng caustic soda and sodium sulphite or containing caustic soda, and sodium sulphide. All of these processes are, however, performed similarly with respect to the cooking being effected with an amount of liquor over a period of time requiring the addition of heat to maintain the process at the proper cooking temperature, approximately 170C.
= ~
PATENT APPLICATION
TITLE
Displacement Heating in Continuous Digesters TECHNICAL FIELD OF THE INVENTION
- The present invention relates to improvements in apparatus and methods for the fiber liberating digestion of continuously fed comminuted cellulosic fiber material by cooking liquor and subsequent washing of the liberated fiber material. More particularly, the invention relates to an improved apparatus and process utilizing spent black liquor for heating the chips to effect savings in thermal energy, and for accomplishing high sulfidity cooking without changes to the overall sulfide balance of the system to accomplish a pulp having improved mechanical characteristics, to improve pulp yield, and to achieve extended delignification.
BACKGROUND OF THE INVENTION
In producing chemical wood pulps, it has become the practice to use cooking liquors cont~;n;ng various cooking chemicals for liberating the pulp fibers. The so-called kraft or sulphate pulp is produced by cooking the raw chipped wood in a liquor wherein materials such as sodium hydroxide and sodium sulfide serve as the essential fiber liberating chemicals. The so-called soda pulp derives its name from the caustic soda-cont~;n;ng cooking liquor which is produced, namely a liquor cont~;n;ng principally caustic soda as the active pulping chemical. There are modifications of these processes based on the use of liquors cont~in;ng caustic soda and sodium sulphite or containing caustic soda, and sodium sulphide. All of these processes are, however, performed similarly with respect to the cooking being effected with an amount of liquor over a period of time requiring the addition of heat to maintain the process at the proper cooking temperature, approximately 170C.
= ~
(2) PCT/US90/05443 ~
2Q6-6~ 81 Two basic processes have been used for performing the chip cooking. The first is batch cooking in which the chips are placed in a digester, liquor is added, the temperature and pressure are raised and the "batch" is maintained at the elevated temperature and pressure to reach the desired stage of delignification. The digester is then emptied, and a subsequent fill is started for another batch. In continuous digesting, the second basic process, a chip column continuously moves through the digester with hot liquor circulating therethrough. Process conditions are controlled such that the desired stage of delignification has occurred when the chips flow out of the digester.
Various advances have been made in batch cooking processes utilizing spent liquor or black liquor in transferring heat to the chips, but effective heat conserving processes for continuous cooking have not been developed to an advanced stage for attA;n;ng m~x;mum heat energy conservation.
In conventional continuous digesters, the spent liquor is allowed to flash and steam is generated. The steam is normally utilized to pre-steam the chips and to generate hot water. The heat and cooking chemicals could be utilized more efficiently if the spent liquors were used to preheat and precondition the chips and to preheat the cooking chemicals such as white liquor in kraft processes which enters the process.
SUMMARY OF THE INVENTION
It is accordingly an object of the present invention to provide a continuous digestion cooking process wherein an improved saving in thermal energy is effected.
A further object of the invention is to provide a continuous digestion process wherein the used black cooking liquors and the white liquors are utilized in a unique 2~6~18~
2Q6-6~ 81 Two basic processes have been used for performing the chip cooking. The first is batch cooking in which the chips are placed in a digester, liquor is added, the temperature and pressure are raised and the "batch" is maintained at the elevated temperature and pressure to reach the desired stage of delignification. The digester is then emptied, and a subsequent fill is started for another batch. In continuous digesting, the second basic process, a chip column continuously moves through the digester with hot liquor circulating therethrough. Process conditions are controlled such that the desired stage of delignification has occurred when the chips flow out of the digester.
Various advances have been made in batch cooking processes utilizing spent liquor or black liquor in transferring heat to the chips, but effective heat conserving processes for continuous cooking have not been developed to an advanced stage for attA;n;ng m~x;mum heat energy conservation.
In conventional continuous digesters, the spent liquor is allowed to flash and steam is generated. The steam is normally utilized to pre-steam the chips and to generate hot water. The heat and cooking chemicals could be utilized more efficiently if the spent liquors were used to preheat and precondition the chips and to preheat the cooking chemicals such as white liquor in kraft processes which enters the process.
SUMMARY OF THE INVENTION
It is accordingly an object of the present invention to provide a continuous digestion cooking process wherein an improved saving in thermal energy is effected.
A further object of the invention is to provide a continuous digestion process wherein the used black cooking liquors and the white liquors are utilized in a unique 2~6~18~
(3) PCT/US90/05443 manner in the process so as to obtain a saving in thermal energy, and to effect an improvement in the resultant qualities of the pulp which is produced.
Yet another object of the present invention is to provide a process for achieving high sulfidity cooking without significant changes to the overall sulfide balance of the cooking system, and for achieving extended delignification in a continuous digesting system while improving pulp yield over existing continuous digesting systems.
A feature of the invention is the provision of a continuous digestion process wherein a plurality of containers are used in sequence, with the first container receiving preconditioned chips and the chips being preimpregnated and heated in the first container with a low temperature black liquor. Further heating of the chips is accomplished with higher temperature liquors in the second and subsequent containers, and after the chips are brought up to the desired elevated temperature, a white liquor is circulated through the chips at the digestion temperature and pressure. The chips are continuously fed from the last of the preimpregnation containers to the digester for cooking. The cooked delignified chips are removed as pulp from the bottom of the digester and circulated to final washing. The wash liquor from the washer is utilized in two or more stages to displace from the digester the free liquor and liquor within the chips.
In accordance with the principles of the present invention, the hot spent liquor is utilized to heat the incoming materials for the continuous digester. The spent liquor, having been extracted from the digester, is accumulated in pressure vessels substantially at digester temperature. Lower temperature liquors from final displacement stages are also accumulated. The incoming chips are first exposed to the lower temperature liquors and then the higher temperature liquors. The white liquor is 2 0 6 ~ (4 W O 91/05103 PC~r/US90/0~443 preheated in a heat exchanger, utilizing a portion of hot spent liquor. The white liquor can be stored in a hot white liquor accumulator whereas the hot spent liquor, after having given energy to the white liquor, goes to the low temperature accumulator.
Practically, the process can be accomplished wherein a first initial chamber or vessel is utilized, being fed by a screw conveyor feeder to press the chips downwardly. The vessel may be employed with an extraction screen at the top and with a recirculation screen further down the vessel, with the recycled liquor flowing through a central pipe ending at the screen level. Low temperature liquor is fed from a low temperature tank to a circulation pump, and the liquor is evenly spread over the vessel area. By extracting liquor from the top screen, a portion of the added liquor flows in a countercurrent path to the movement of the chips, thus transferring the heat and residual chemicals in the liquor to the chips. The duration of time that the chips are in that zone, and the liquor flow rate will determine the efficiency of the heat transfer. The amount of liquor extracted from the top screen is an amount that generally corresponds to the white liquor charge, wood moisture and the dilution factor. The extracted liquor goes to the evaporators. The rem~in;ng part of the liquor goes with the chips downwardly in the chamber.
The treatment with hot spent liquor takes place in a vessel at principally digester pressure. Preferably, this high pressure vessel is located underneath the first vessel, and the transfer of material takes place in utilizing a high pressure feeder. The arrangement for heat exchange is, in principal, essentially the same as in the first lower temperature vessel. The hot spent liquor is introduced in a recirculation circuit, and a portion of the liquor flows countercurrent to the chips, being extracted from a top screen. Thus, the low temperature liquor is being displaced and substituted by a hot spent liquor. The low temperature 2Q~66181 ~ WO91/05103 (5) PCT/US90/05443 .
liquor which leaves the top screen is conveyed back to the low temperature tank.
A portion of the hot spent liquor is utilized to preheat the white liquor that is introduced in the bottom of the high pressure vessel. In the event a mechanical device is utilized to feed chips out of the high pressure vessel, white liquor should be added after that mechanical device to avoid pulp deterioration. This can be done by utilizing a vessel which forms part of the continuous digester and is integrated into the digester apparatus itself.
Other objects, advantages, and features will become more apparent with the teaching of the principles of the invention in connection with the disclosure of the preferred embodiments thereof in the specification, claims, and drawings, in which:
BRIEF DESCRIPTION OF THE DRAWINGS
Figure 1 is a schematic drawing of a process for operating in accordance with the principles of the present invention.
Figure 2 is a schematic drawing of a modification of the process shown in Figure 1, wherein the high pressure preimpregnation vessel forms a part of the continuous digester.
DESCRIPTION OF THE PREFERRED EMBODIMENTS
As illustrated in Figure 1, wood chips are delivered to a first chamber or container 10 through a screw delivery mechanism 11. The chips may be preconditioned, such as by being heated by steam, in a supply container 12.
In the first container, which is a warm liquor preimpregnator, the preheating occurs by a supply of low temperature black liquor supplied from a low temperature (6) -2066 1 8 1 black liquor tank 13 through a supply line 14. The black liquor is circulated through the chips through a recirculating mechanism including a recirculating line 15 and a recirculating pump 16.
Excess black liquor, after having spent its heat energy and residual chemicals, is removed near the top of the chamber 10 through a line 17 controlled by a valve 18 to flow to an evaporator 19 where the black liquor is reprocessed and reclaimed in the manner which will be recognized and understood by those versed in the art.
Screens lOa and lOb are provided for the liquor outlets to the evaporator 19 and the recirculating line 15, respectively.
-In the process depicted in Figure 1, preheated woodchips are forcibly conveyed downwardly to a second container 21, which is a hot liquor preimpregnator in which the wood chips are subjected to liquor for a predetermined time at a higher temperature and high pressure than in the first container. For delivering the wood chips to the second container 21, a mechanism such as a rotary delivery valve 20 is employed. Such valves are well-known to those skilled in the art and will not be described further herein.
To preheat the chips in the hot liquor preimpregnator to approach the digestion temperature, hot black liquor is delivered to the second container by line 23, which receives hot black liquor from a hot black liquor tank 22 delivered by a pressure pump 22a. The hot black liquor is recirculated through the moving chips by recirculation line 24, with the liquor being circulated by a ~ 24a. A
~portion of the liquor is removed through a line 24b, controlled by a valve 24c, to be delivered back to the low temperature black liquor tank 13, preferably upstream of a delivery pump 13a which pumps the low temperature black liquor to the first container 10.
. 2~61~1 ~ VVO 91/05103 ( 7) P Cl`/US90/05443 -~ Arranged in the second container 21 are screens 21a, 21b, and 21c, which allow for the removal of the liquor, with the screen 21a facilitating the removal of the excess black liquor through the line 24b, and the screens 21b and 21c facilitating the recirculation of the high temperature black liquor in two recirculation paths.
For the digestion process, white liquor is delivered to the second container 21 through a line 25. Alternatively, the white liquor can be supplied through a line 25a, shown by dotted line in Figure 1, as the chips leave the second cont~iner.
The white liquor is obtained from a high temperature white liquor tank 27, being delivered therefrom by a pump 27a. The white liquor is preheated before delivery to the second container 21 in a heat exchanger 28, with the white liquor being supplied to the heat exch~nger from a supply source not shown and a supply line 29. The heat exchanger is heated by hot black liquor supplied through a line 30 leading from the high temperature black liquor tank 22, and, after passing through the heat exchanger, the black liquor flows through a line 31 to the low temperature black liquor tank 13.
The preimpregnated chips and cooking liquor exit the bottom of the second cont~;ner 21 through a discharge line 32, which connects the bottom of the second container 21 to the upper end of the digester 33. Cooking liquor is recirculated at the top of the digester through a circuit 34 having a recirculation pump 34a and extraction screen 34b therein. Temperature adjustment of the cooking liquor may be achieved with a trim heat exchanger 34c heated by steam from a steam source 34d. A portion of the cooking liquor is removed from the digester through a line 38 by a pump 38a, and is delivered through a line 39 to the location where the chips exit the second container. This recirculated cooking liquor further dilutes the chips and liquor exiting the 2 ~ 6 ~ 1 WO9l/05103 PCT/US90/05~3 second container to facilitate transport of the chips to the digester.
In the digester 33, the chips move continuously downward, and are cooked to the desired level of delignification. Recirculation takes place through an extraction line 35, an extraction screen 35a, a recirculation line 36, and a pump 36a. A portion of the recirculated liquor is directed to the hot liquor tank 22, controlled by a valve 36b.
In the lower part of the digester, washer filtrate from a line 50 is recirculated through a circuit 52 by a pump 54, to el;m;n~te temperature and spent liquor concentration gradients. The filtrate is added between an extraction screen 56 and the pump 54, so that the extracted liquor volume is less than the flow into the digester through circuit 52, causing an upward flow of filtrate in the bottom of the digester. A second recirculation circuit 60, including a pump 62, is provided to extract a portion of the upward flowing filtrate at an extraction screen 64, together with rem~;n;ng hot spent black liquor. A portion of the extracted filtrate and liquor is directed to the low temperature tank 13, through line 66 controlled by a valve 68.
A blow line 80 is provided for removing pulp from the digester to a washer. The m~nner in which the pulp is moved from the digester, including any secondary dilution, is well-known in the art of continuous digesters and will not be described further herein.
In operation, preconditioned pulp is delivered via a screw conveyor 11 into a first chip preheating container 10 where it is heated by low temperature black liquor obtained from a low temperature black liquor tank 13. The preheated chips pass downwardly through a rotary delivery valve 20 to a second chamber 21, where the chips are further preheated WO 91/05103 (9) 2066 1 8~T~Us9O~05443 by high temperature black liquor received from a high temperature black liquor tank 22.
The high temperature and low temperature black liquors are obtained from the pulp washer with the high temperature liquor also being utilized for heating the white liquor through the heat exchanger 28. White liquor delivered through the screen 21c from a white liquor supply line 25, is added to the chips before the chips enter digester 33.
In the digester, delignification takes place as the chip column and liquor move downwardly. The volume of filtrate added through supply line 50 should be sufficient to displace the free hot black liquor extracted through screen 35a and the warm liquor extracted through screen 64.
The countercurrent flow of liquor in the area between screen 35a and screen 64, and between 64 and screen 56 creates a condition in which liquor held by the chips is displaced and removed, so that the chips leaving through blow line 80 are substantially free from cooking liquor.
The region of the countercurrent flow between screen 64 and screen 35a should be sufficiently long that the filtrate is heated by the chips substantially to cooking temperature, and the liquor and filtrate removed through line 35a are at or near cooking temperature.
It is known that the sulphide ions in cooking liquors that are absorbed by the chips prior to cooking are liberated from the wood chips later in the cooking process, so that approximately 90 percent of the sulphide is left in the spent liquors. It is critical to cooking selectivity to precondition chips with sulphide prior to bulk delignification. In the present invention, liquor leaving the top of the first chamber contains essentially the same amount of sulphide as conventional spent liquors going to evaporation. The sulphide concentration in the low temperature tank is even higher than that coming from the first chamber, and the sulphide concentration in the hot ~O~gl WO91/05103 ) PCT/US90/05443 black liquor tank is even higher. These concentrations, in combination with the elevated temperatures, give an efficient preconditioning of the wood chips with sulphide prior to cooking.
It should be recognized that the various components of the present process can be rearranged to achieve the desired preimpregnation and preheating, with appropriate recirculation. Additional preimpregnation containers can be utilized, joined as shown in Figure l, or by other suitable means. The two container process described also can be alternatively arranged. For example, Figure 2 illustrates, in schematic format, a process in which the second chamber 21 is continguous with the digester. Corresponding parts of the process depicted in Figure 2 have been numbered similarly to Figure l. Thus, the various extraction screens, recirculation circuits, pumps, and the like for both the high pressure preimpregnation process and the final digestion process are contained in the combined preimpregnation and digester vessel.
Thus, it will be seen that I have provided an improved method and apparatus for a continuous digestion process which meets the objectives and advantages above set forth.
It will be recognized that various modifications of the process and apparatus within the spirit and scope of the invention may be employed without departing from the principles of the invention.
Yet another object of the present invention is to provide a process for achieving high sulfidity cooking without significant changes to the overall sulfide balance of the cooking system, and for achieving extended delignification in a continuous digesting system while improving pulp yield over existing continuous digesting systems.
A feature of the invention is the provision of a continuous digestion process wherein a plurality of containers are used in sequence, with the first container receiving preconditioned chips and the chips being preimpregnated and heated in the first container with a low temperature black liquor. Further heating of the chips is accomplished with higher temperature liquors in the second and subsequent containers, and after the chips are brought up to the desired elevated temperature, a white liquor is circulated through the chips at the digestion temperature and pressure. The chips are continuously fed from the last of the preimpregnation containers to the digester for cooking. The cooked delignified chips are removed as pulp from the bottom of the digester and circulated to final washing. The wash liquor from the washer is utilized in two or more stages to displace from the digester the free liquor and liquor within the chips.
In accordance with the principles of the present invention, the hot spent liquor is utilized to heat the incoming materials for the continuous digester. The spent liquor, having been extracted from the digester, is accumulated in pressure vessels substantially at digester temperature. Lower temperature liquors from final displacement stages are also accumulated. The incoming chips are first exposed to the lower temperature liquors and then the higher temperature liquors. The white liquor is 2 0 6 ~ (4 W O 91/05103 PC~r/US90/0~443 preheated in a heat exchanger, utilizing a portion of hot spent liquor. The white liquor can be stored in a hot white liquor accumulator whereas the hot spent liquor, after having given energy to the white liquor, goes to the low temperature accumulator.
Practically, the process can be accomplished wherein a first initial chamber or vessel is utilized, being fed by a screw conveyor feeder to press the chips downwardly. The vessel may be employed with an extraction screen at the top and with a recirculation screen further down the vessel, with the recycled liquor flowing through a central pipe ending at the screen level. Low temperature liquor is fed from a low temperature tank to a circulation pump, and the liquor is evenly spread over the vessel area. By extracting liquor from the top screen, a portion of the added liquor flows in a countercurrent path to the movement of the chips, thus transferring the heat and residual chemicals in the liquor to the chips. The duration of time that the chips are in that zone, and the liquor flow rate will determine the efficiency of the heat transfer. The amount of liquor extracted from the top screen is an amount that generally corresponds to the white liquor charge, wood moisture and the dilution factor. The extracted liquor goes to the evaporators. The rem~in;ng part of the liquor goes with the chips downwardly in the chamber.
The treatment with hot spent liquor takes place in a vessel at principally digester pressure. Preferably, this high pressure vessel is located underneath the first vessel, and the transfer of material takes place in utilizing a high pressure feeder. The arrangement for heat exchange is, in principal, essentially the same as in the first lower temperature vessel. The hot spent liquor is introduced in a recirculation circuit, and a portion of the liquor flows countercurrent to the chips, being extracted from a top screen. Thus, the low temperature liquor is being displaced and substituted by a hot spent liquor. The low temperature 2Q~66181 ~ WO91/05103 (5) PCT/US90/05443 .
liquor which leaves the top screen is conveyed back to the low temperature tank.
A portion of the hot spent liquor is utilized to preheat the white liquor that is introduced in the bottom of the high pressure vessel. In the event a mechanical device is utilized to feed chips out of the high pressure vessel, white liquor should be added after that mechanical device to avoid pulp deterioration. This can be done by utilizing a vessel which forms part of the continuous digester and is integrated into the digester apparatus itself.
Other objects, advantages, and features will become more apparent with the teaching of the principles of the invention in connection with the disclosure of the preferred embodiments thereof in the specification, claims, and drawings, in which:
BRIEF DESCRIPTION OF THE DRAWINGS
Figure 1 is a schematic drawing of a process for operating in accordance with the principles of the present invention.
Figure 2 is a schematic drawing of a modification of the process shown in Figure 1, wherein the high pressure preimpregnation vessel forms a part of the continuous digester.
DESCRIPTION OF THE PREFERRED EMBODIMENTS
As illustrated in Figure 1, wood chips are delivered to a first chamber or container 10 through a screw delivery mechanism 11. The chips may be preconditioned, such as by being heated by steam, in a supply container 12.
In the first container, which is a warm liquor preimpregnator, the preheating occurs by a supply of low temperature black liquor supplied from a low temperature (6) -2066 1 8 1 black liquor tank 13 through a supply line 14. The black liquor is circulated through the chips through a recirculating mechanism including a recirculating line 15 and a recirculating pump 16.
Excess black liquor, after having spent its heat energy and residual chemicals, is removed near the top of the chamber 10 through a line 17 controlled by a valve 18 to flow to an evaporator 19 where the black liquor is reprocessed and reclaimed in the manner which will be recognized and understood by those versed in the art.
Screens lOa and lOb are provided for the liquor outlets to the evaporator 19 and the recirculating line 15, respectively.
-In the process depicted in Figure 1, preheated woodchips are forcibly conveyed downwardly to a second container 21, which is a hot liquor preimpregnator in which the wood chips are subjected to liquor for a predetermined time at a higher temperature and high pressure than in the first container. For delivering the wood chips to the second container 21, a mechanism such as a rotary delivery valve 20 is employed. Such valves are well-known to those skilled in the art and will not be described further herein.
To preheat the chips in the hot liquor preimpregnator to approach the digestion temperature, hot black liquor is delivered to the second container by line 23, which receives hot black liquor from a hot black liquor tank 22 delivered by a pressure pump 22a. The hot black liquor is recirculated through the moving chips by recirculation line 24, with the liquor being circulated by a ~ 24a. A
~portion of the liquor is removed through a line 24b, controlled by a valve 24c, to be delivered back to the low temperature black liquor tank 13, preferably upstream of a delivery pump 13a which pumps the low temperature black liquor to the first container 10.
. 2~61~1 ~ VVO 91/05103 ( 7) P Cl`/US90/05443 -~ Arranged in the second container 21 are screens 21a, 21b, and 21c, which allow for the removal of the liquor, with the screen 21a facilitating the removal of the excess black liquor through the line 24b, and the screens 21b and 21c facilitating the recirculation of the high temperature black liquor in two recirculation paths.
For the digestion process, white liquor is delivered to the second container 21 through a line 25. Alternatively, the white liquor can be supplied through a line 25a, shown by dotted line in Figure 1, as the chips leave the second cont~iner.
The white liquor is obtained from a high temperature white liquor tank 27, being delivered therefrom by a pump 27a. The white liquor is preheated before delivery to the second container 21 in a heat exchanger 28, with the white liquor being supplied to the heat exch~nger from a supply source not shown and a supply line 29. The heat exchanger is heated by hot black liquor supplied through a line 30 leading from the high temperature black liquor tank 22, and, after passing through the heat exchanger, the black liquor flows through a line 31 to the low temperature black liquor tank 13.
The preimpregnated chips and cooking liquor exit the bottom of the second cont~;ner 21 through a discharge line 32, which connects the bottom of the second container 21 to the upper end of the digester 33. Cooking liquor is recirculated at the top of the digester through a circuit 34 having a recirculation pump 34a and extraction screen 34b therein. Temperature adjustment of the cooking liquor may be achieved with a trim heat exchanger 34c heated by steam from a steam source 34d. A portion of the cooking liquor is removed from the digester through a line 38 by a pump 38a, and is delivered through a line 39 to the location where the chips exit the second container. This recirculated cooking liquor further dilutes the chips and liquor exiting the 2 ~ 6 ~ 1 WO9l/05103 PCT/US90/05~3 second container to facilitate transport of the chips to the digester.
In the digester 33, the chips move continuously downward, and are cooked to the desired level of delignification. Recirculation takes place through an extraction line 35, an extraction screen 35a, a recirculation line 36, and a pump 36a. A portion of the recirculated liquor is directed to the hot liquor tank 22, controlled by a valve 36b.
In the lower part of the digester, washer filtrate from a line 50 is recirculated through a circuit 52 by a pump 54, to el;m;n~te temperature and spent liquor concentration gradients. The filtrate is added between an extraction screen 56 and the pump 54, so that the extracted liquor volume is less than the flow into the digester through circuit 52, causing an upward flow of filtrate in the bottom of the digester. A second recirculation circuit 60, including a pump 62, is provided to extract a portion of the upward flowing filtrate at an extraction screen 64, together with rem~;n;ng hot spent black liquor. A portion of the extracted filtrate and liquor is directed to the low temperature tank 13, through line 66 controlled by a valve 68.
A blow line 80 is provided for removing pulp from the digester to a washer. The m~nner in which the pulp is moved from the digester, including any secondary dilution, is well-known in the art of continuous digesters and will not be described further herein.
In operation, preconditioned pulp is delivered via a screw conveyor 11 into a first chip preheating container 10 where it is heated by low temperature black liquor obtained from a low temperature black liquor tank 13. The preheated chips pass downwardly through a rotary delivery valve 20 to a second chamber 21, where the chips are further preheated WO 91/05103 (9) 2066 1 8~T~Us9O~05443 by high temperature black liquor received from a high temperature black liquor tank 22.
The high temperature and low temperature black liquors are obtained from the pulp washer with the high temperature liquor also being utilized for heating the white liquor through the heat exchanger 28. White liquor delivered through the screen 21c from a white liquor supply line 25, is added to the chips before the chips enter digester 33.
In the digester, delignification takes place as the chip column and liquor move downwardly. The volume of filtrate added through supply line 50 should be sufficient to displace the free hot black liquor extracted through screen 35a and the warm liquor extracted through screen 64.
The countercurrent flow of liquor in the area between screen 35a and screen 64, and between 64 and screen 56 creates a condition in which liquor held by the chips is displaced and removed, so that the chips leaving through blow line 80 are substantially free from cooking liquor.
The region of the countercurrent flow between screen 64 and screen 35a should be sufficiently long that the filtrate is heated by the chips substantially to cooking temperature, and the liquor and filtrate removed through line 35a are at or near cooking temperature.
It is known that the sulphide ions in cooking liquors that are absorbed by the chips prior to cooking are liberated from the wood chips later in the cooking process, so that approximately 90 percent of the sulphide is left in the spent liquors. It is critical to cooking selectivity to precondition chips with sulphide prior to bulk delignification. In the present invention, liquor leaving the top of the first chamber contains essentially the same amount of sulphide as conventional spent liquors going to evaporation. The sulphide concentration in the low temperature tank is even higher than that coming from the first chamber, and the sulphide concentration in the hot ~O~gl WO91/05103 ) PCT/US90/05443 black liquor tank is even higher. These concentrations, in combination with the elevated temperatures, give an efficient preconditioning of the wood chips with sulphide prior to cooking.
It should be recognized that the various components of the present process can be rearranged to achieve the desired preimpregnation and preheating, with appropriate recirculation. Additional preimpregnation containers can be utilized, joined as shown in Figure l, or by other suitable means. The two container process described also can be alternatively arranged. For example, Figure 2 illustrates, in schematic format, a process in which the second chamber 21 is continguous with the digester. Corresponding parts of the process depicted in Figure 2 have been numbered similarly to Figure l. Thus, the various extraction screens, recirculation circuits, pumps, and the like for both the high pressure preimpregnation process and the final digestion process are contained in the combined preimpregnation and digester vessel.
Thus, it will be seen that I have provided an improved method and apparatus for a continuous digestion process which meets the objectives and advantages above set forth.
It will be recognized that various modifications of the process and apparatus within the spirit and scope of the invention may be employed without departing from the principles of the invention.
Claims (14)
PROPERTY OR PRIVILEGE IS CLAIMED ARE DEFINED AS FOLLOWS:
1. A digester apparatus for the liberation of cellulosic fibrous material for papermaking pulp using cooking liquor at a high pressure and a high temperature in a continuous process, comprising in combination:
a first chamber;
feed means for delivering cellulosic wood chips to said first chamber;
a low temperature liquor tank connected to the first chamber for circulating low temperature black liquor through the chips in said first chamber for the exchange of heat energy to increase the temperature of the chips and to convey residual chemicals to the chips;
a second chamber connected to receive chips preheated by said low temperature liquor from the first chamber;
a feed mechanism connected between said chambers for delivering the chips to the second chamber;
a high temperature liquor tank connected to said second chamber for circulating high temperature black liquor through the chips for the exchange of heat energy to bring the temperature of the chips near digesting temperature and to convey residual chemicals to the chips;
an outlet means leading from the second chamber for a continuous delivery of preheated chips to a digester;
means for supplying white liquor to the chips for furthering delignification of the chips in the digester;
a recirculation means in the upper portion of the digester for recirculating hot liquor in the digester, and including diversion means for directing a portion of the recirculating hot liquor to the hot liquor tank;
a first recirculation means in the lower portion of the digester for recirculating liquor in the lower portion, including means for adding washer filtrate to recirculating liquor;
and a second recirculation means in the lower portion of the digester including extracting means for directing liquor to the low temperature liquor tank.
a first chamber;
feed means for delivering cellulosic wood chips to said first chamber;
a low temperature liquor tank connected to the first chamber for circulating low temperature black liquor through the chips in said first chamber for the exchange of heat energy to increase the temperature of the chips and to convey residual chemicals to the chips;
a second chamber connected to receive chips preheated by said low temperature liquor from the first chamber;
a feed mechanism connected between said chambers for delivering the chips to the second chamber;
a high temperature liquor tank connected to said second chamber for circulating high temperature black liquor through the chips for the exchange of heat energy to bring the temperature of the chips near digesting temperature and to convey residual chemicals to the chips;
an outlet means leading from the second chamber for a continuous delivery of preheated chips to a digester;
means for supplying white liquor to the chips for furthering delignification of the chips in the digester;
a recirculation means in the upper portion of the digester for recirculating hot liquor in the digester, and including diversion means for directing a portion of the recirculating hot liquor to the hot liquor tank;
a first recirculation means in the lower portion of the digester for recirculating liquor in the lower portion, including means for adding washer filtrate to recirculating liquor;
and a second recirculation means in the lower portion of the digester including extracting means for directing liquor to the low temperature liquor tank.
2. A digester apparatus for the liberation of cellulosic fibrous material for papermaking pulp using cooking liquor at a high pressure and a high temperature in continuous process constructed in accordance with claim 1:
including a recirculation means for the first chamber for receiving low temperature liquor from said low temperature tank and for recirculating the liquor through the chips in the first chamber countercurrent to the continuous movement of chips through said first chamber.
including a recirculation means for the first chamber for receiving low temperature liquor from said low temperature tank and for recirculating the liquor through the chips in the first chamber countercurrent to the continuous movement of chips through said first chamber.
3. A digester apparatus for the liberation of cellulosic fibrous material for papermaking pulp using cooking liquor at a high pressure and a high temperature in a continuous process constructed in accordance with claim 1:
including a recirculating means for the second chamber connected to receive liquor from the high temperature tank, for recirculation of the high temperature liquor through the second tank countercurrent to the continuous movement of chips therethrough for raising the temperature of the chips therein.
including a recirculating means for the second chamber connected to receive liquor from the high temperature tank, for recirculation of the high temperature liquor through the second tank countercurrent to the continuous movement of chips therethrough for raising the temperature of the chips therein.
4. A digester apparatus for the liberation of cellulosic fibrous material for papermaking pulp using cooking liquor at a high pressure and a high temperature in a continuous process constructed in accordance with claim 1:
including a white liquor recirculation means connected to the digester for recirculating the white liquor countercurrent to the chip movement during the digesting process.
including a white liquor recirculation means connected to the digester for recirculating the white liquor countercurrent to the chip movement during the digesting process.
5. A digester apparatus for the liberation of cellulosic fibrous material for papermaking pulp using cooking liquor at a high pressure and a high temperature in a continuous process constructed in accordance with claim 1:
including a heat exchanger connected to the high temperature liquor tank and connected to the white liquor container for increasing the temperature of the white liquor utilizing the thermal energy in the liquor in said high temperature liquor tank.
including a heat exchanger connected to the high temperature liquor tank and connected to the white liquor container for increasing the temperature of the white liquor utilizing the thermal energy in the liquor in said high temperature liquor tank.
6. A digester apparatus for the liberation of cellulosic fibrous material for papermaking pulp using cooking liquor at a high pressure and a high temperature in a continuous process constructed in accordance with claim 1:
including a connection to a pulp washer for transferring the delignified pulp from the digester.
including a connection to a pulp washer for transferring the delignified pulp from the digester.
7. A digester apparatus for the liberation of cellulosic fibrous material for papermaking pulp using cooking liquor at a high pressure and a high temperature in a continuous process constructed in accordance with claim 1:
including a liquor removal line connected to the first chamber for the removal of low temperature liquor.
including a liquor removal line connected to the first chamber for the removal of low temperature liquor.
8. A continuous digestion process for treating chipped wood, comprising the steps:
delivering wood chips to a first chamber;
moving said chips continuously through said chamber;
circulating a black liquor therethrough at moderate temperatures in said first chamber to heat the chips and recycle residual chemicals;
continuously feeding the preheated and chemically preconditioned chips and moderate temperature liquor to a second chamber at a higher temperature and pressure;
displacing the moderate temperature black liquor with hot black liquor;
circulating the hot black liquor through the chips in the second chamber to further increase the temperature of the chips and to further recycle residual chemicals;
transporting said chips in a continuous flow to a digester;
delivering white liquor to the hot chips for displacing the hot black liquor;
moving said chips through said digester at a rate, temperature, and pressure for completing desired delignification while said chips are in said digester;
displacing liquor from the digested pulp using a lower temperature liquid;
separately collecting moderate temperature and hot temperature liquors displaced in the process as well as diverted during the liquor circulating steps; and removing digested pulp from the digester after being subjected to the effect of the white liquor for a predetermined time.
delivering wood chips to a first chamber;
moving said chips continuously through said chamber;
circulating a black liquor therethrough at moderate temperatures in said first chamber to heat the chips and recycle residual chemicals;
continuously feeding the preheated and chemically preconditioned chips and moderate temperature liquor to a second chamber at a higher temperature and pressure;
displacing the moderate temperature black liquor with hot black liquor;
circulating the hot black liquor through the chips in the second chamber to further increase the temperature of the chips and to further recycle residual chemicals;
transporting said chips in a continuous flow to a digester;
delivering white liquor to the hot chips for displacing the hot black liquor;
moving said chips through said digester at a rate, temperature, and pressure for completing desired delignification while said chips are in said digester;
displacing liquor from the digested pulp using a lower temperature liquid;
separately collecting moderate temperature and hot temperature liquors displaced in the process as well as diverted during the liquor circulating steps; and removing digested pulp from the digester after being subjected to the effect of the white liquor for a predetermined time.
9. The method of treating cellulosic wood chips in a continuous, high pressure, high temperature, digestion process for the liberation of pulp, in accordance with the steps of claim 8:
including delivering the digested pulp to a washer and utilizing the wash liquor in the first chamber for preheating the chips.
including delivering the digested pulp to a washer and utilizing the wash liquor in the first chamber for preheating the chips.
10. The method of treating cellulosic wood chips in a continuous, high pressure, high temperature, digestion process for the liberation of pulp, in accordance with the steps of claim 8.
including recirculating the black liquor in said first chamber over a predetermined time to preheat and chemically precondition the chips.
including recirculating the black liquor in said first chamber over a predetermined time to preheat and chemically precondition the chips.
11. The method of treating cellulosic wood chips in a continuous, high pressure, high temperature digestion process for the liberation of pulp, in accordance with the steps of claim 8:
including utilizing hot black liquor for preheating the white liquor.
including utilizing hot black liquor for preheating the white liquor.
12. The method of treating cellulosic wood chips in a continuous, high pressure, high temperature, digestion process for the liberation of pulp, in accordance with the steps of claim 8:
including removing black liquor from the first chamber for reprocessing the liquor.
including removing black liquor from the first chamber for reprocessing the liquor.
13. The method of treating cellulosic wood chips in a continuous, high pressure, high temperature, digestion process for the liberation of pulp, in accordance with the steps of claim 8:
including recirculating the hot black liquor in the second chamber.
including recirculating the hot black liquor in the second chamber.
14. The method of treating cellulosic wood chips in a continuous, high pressure, high temperature, digestion process for the liberation of pulp, in accordance with the steps of claim 8:
including removal of black liquor from the digester and supplying said liquor to the first chamber.
including removal of black liquor from the digester and supplying said liquor to the first chamber.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US41392089A | 1989-09-28 | 1989-09-28 | |
| US413,920 | 1989-09-28 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CA2066181A1 CA2066181A1 (en) | 1991-03-29 |
| CA2066181C true CA2066181C (en) | 1995-09-26 |
Family
ID=23639200
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA002066181A Expired - Fee Related CA2066181C (en) | 1989-09-28 | 1990-09-25 | Displacement heating in continuous digesters |
Country Status (10)
| Country | Link |
|---|---|
| EP (1) | EP0502852B1 (en) |
| JP (1) | JPH0674557B2 (en) |
| KR (1) | KR0171423B1 (en) |
| CN (1) | CN1021980C (en) |
| CA (1) | CA2066181C (en) |
| DE (1) | DE69004438T2 (en) |
| ES (1) | ES2045948T3 (en) |
| FI (1) | FI921373A (en) |
| NO (1) | NO179016C (en) |
| WO (1) | WO1991005103A2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103080417A (en) * | 2010-07-07 | 2013-05-01 | 斯托拉恩索公司 | Process for production of precipitated lignin from black liquor and precipitated lignin produced by the process |
Families Citing this family (21)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE69111165T2 (en) * | 1990-09-20 | 1995-11-16 | Kvaerner Pulping Tech | Soak with black liquor before adding the white liquor. |
| US5302247A (en) * | 1992-11-02 | 1994-04-12 | Kamyr, Inc. | Top circulation line cooling for a modified cook digester |
| CN1071997C (en) * | 1993-06-18 | 2001-10-03 | 叶隆清 | Plant growth accelerator and method for preparing same |
| SE502039C2 (en) * | 1993-12-29 | 1995-07-24 | Kvaerner Pulping Tech | Methods and apparatus for continuous cooking of pulp |
| US5824187A (en) * | 1993-12-29 | 1998-10-20 | Kvaerner Pulping Ab | Method for the continuous cooking of pulp |
| US6248208B1 (en) | 1995-06-02 | 2001-06-19 | Andritz-Ahlstrom Inc. | Pretreatment of chips before cooking |
| AT403301B (en) * | 1996-04-04 | 1998-01-26 | Impco Voest Alpine Pulp Tech | CONTINUOUS LIQUID MANAGEMENT |
| US6159336A (en) * | 1997-08-07 | 2000-12-12 | Kvaerner Pulping Ab | Method and device for the continuous cooking of pulp |
| SE518738C2 (en) * | 2001-12-17 | 2002-11-12 | Kvaerner Pulping Tech | Wood chip impregnation method for chemical pulping, comprises impregnating chips with liquid in different temperature zones of vessel |
| SE518957C2 (en) * | 2002-01-24 | 2002-12-10 | Kvaerner Pulping Tech | Process for increasing the heating economy of the boiler system during continuous boiling |
| SE527058C2 (en) * | 2004-02-09 | 2005-12-13 | Kvaerner Pulping Tech | Continuous cooking process with improved heat economy |
| CN101906730B (en) * | 2010-07-15 | 2013-01-23 | 轻工业杭州机电设计研究院 | Non-wood fiber continuous cooking method and device |
| CN102154398A (en) * | 2010-12-28 | 2011-08-17 | 国润金华（北京）国际能源投资有限公司佛山高明分公司 | High-temperature and high-pressure cellulose-to-sugar process |
| CN103597139B (en) * | 2011-03-25 | 2016-03-30 | S·L·凯斯瓦尼 | Method and system for extracting black liquor from a horizontal tube continuous digester |
| CN102154874B (en) * | 2011-04-29 | 2012-11-21 | 白福安 | Replacement cooking pulping method |
| CN102797189A (en) * | 2012-08-11 | 2012-11-28 | 李肥生 | Two-section self-heating helical-structure boiling separator |
| US9644317B2 (en) * | 2014-11-26 | 2017-05-09 | International Paper Company | Continuous digester and feeding system |
| FR3039567A1 (en) * | 2015-07-31 | 2017-02-03 | Commissariat Energie Atomique | DEVICE AND PROCESS FOR TREATING BLACK LIQUOR FROM THE PREPARATION OF PAPER PULP BY HYDROTHERMAL LIQUEFACTION |
| CN108611896A (en) * | 2016-12-20 | 2018-10-02 | 丁永新 | Using paper grade (stock) slurry made of wood, bamboo raw material |
| KR102295018B1 (en) | 2019-09-11 | 2021-08-30 | 한병엽 | Automatic ordering device for packaging container |
| KR102490233B1 (en) | 2020-11-24 | 2023-01-18 | 한병엽 | Pos apparatus, method for processing order information of pos apparatus, recording medium |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FI63610C (en) * | 1981-12-31 | 1983-07-11 | Ekono Oy | REQUIREMENTS FOR CONTAINER UPPSLUTNING AV FINFOERDELAT MATERIAL |
| SE452482B (en) * | 1982-04-28 | 1987-11-30 | Sunds Defibrator | PROCEDURE FOR BATCH PREPARATION OF SULPHATE Pulp WITH HIGH DEGREE |
| JPS6059189A (en) * | 1983-08-24 | 1985-04-05 | ベロイト コ−ポレ−ション | Multi-stage digestion of wood pulp |
| FI71176C (en) * | 1983-11-30 | 1991-12-03 | Ekono Oy | Process for preparing cellulose with batch boiling |
-
1990
- 1990-09-25 EP EP90914988A patent/EP0502852B1/en not_active Expired - Lifetime
- 1990-09-25 DE DE90914988T patent/DE69004438T2/en not_active Expired - Fee Related
- 1990-09-25 JP JP2514062A patent/JPH0674557B2/en not_active Expired - Lifetime
- 1990-09-25 CA CA002066181A patent/CA2066181C/en not_active Expired - Fee Related
- 1990-09-25 KR KR1019920700696A patent/KR0171423B1/en not_active IP Right Cessation
- 1990-09-25 WO PCT/US1990/005443 patent/WO1991005103A2/en active IP Right Grant
- 1990-09-25 ES ES90914988T patent/ES2045948T3/en not_active Expired - Lifetime
- 1990-09-28 CN CN90108125A patent/CN1021980C/en not_active Expired - Fee Related
-
1992
- 1992-02-18 NO NO920630A patent/NO179016C/en unknown
- 1992-03-27 FI FI921373A patent/FI921373A/en not_active Application Discontinuation
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103080417A (en) * | 2010-07-07 | 2013-05-01 | 斯托拉恩索公司 | Process for production of precipitated lignin from black liquor and precipitated lignin produced by the process |
Also Published As
| Publication number | Publication date |
|---|---|
| NO920630D0 (en) | 1992-02-18 |
| EP0502852B1 (en) | 1993-11-03 |
| EP0502852A1 (en) | 1992-09-16 |
| NO179016C (en) | 1996-07-17 |
| FI921373A0 (en) | 1992-03-27 |
| CA2066181A1 (en) | 1991-03-29 |
| KR920703920A (en) | 1992-12-18 |
| DE69004438D1 (en) | 1993-12-09 |
| JPH0674557B2 (en) | 1994-09-21 |
| CN1050579A (en) | 1991-04-10 |
| WO1991005103A2 (en) | 1991-04-18 |
| ES2045948T3 (en) | 1994-01-16 |
| KR0171423B1 (en) | 1999-05-01 |
| DE69004438T2 (en) | 1994-05-11 |
| FI921373A (en) | 1992-03-27 |
| WO1991005103A3 (en) | 1991-05-16 |
| JPH05503739A (en) | 1993-06-17 |
| NO920630L (en) | 1992-02-18 |
| CN1021980C (en) | 1993-09-01 |
| NO179016B (en) | 1996-04-09 |
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Legal Events
| Date | Code | Title | Description |
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| EEER | Examination request | ||
| MKLA | Lapsed |
