US2614923A - Digester filling in sulfate pulping - Google Patents

Digester filling in sulfate pulping Download PDF

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Publication number
US2614923A
US2614923A US725963A US72596347A US2614923A US 2614923 A US2614923 A US 2614923A US 725963 A US725963 A US 725963A US 72596347 A US72596347 A US 72596347A US 2614923 A US2614923 A US 2614923A
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black liquor
digester
chips
liquor
pressure
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US725963A
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Tarkkonen Oma
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Sunila Osakeyhtio
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Sunila Osakeyhtio
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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
    • D21C1/00Pretreatment of the finely-divided materials before digesting
    • D21C1/06Pretreatment of the finely-divided materials before digesting with alkaline reacting compounds

Definitions

  • the invention here presented concerns the method of procedure in the production of sulfate pulp and intends a saving of steam needed for digestion as well as a reduction of the digestion time by utilizing the heat of the black liquor from digesters in which the cook has been completed.
  • This invention has for its object the utilization of the heat contained in the quantity of black liquor to be used in the charge of a digester
  • black liquor is obtained from a preceding completed sulfate cook and is under substantially the pressure and temperature conditions of a finished digestion, by the introduction of the quantity of black liquor to be used as a diluent for the cooking liquor into the digester to be charged before adding the white liquor and simultaneously and together with the chips causing practically the whole charge of the chips to be soaked in black liquor during the process of charging.
  • Another object of this invention is to utilize substantially the entire heat content and pressure of the aforementioned black liquor with the amount of black liquor so employed practically corresponding to thetotal amount of black liquor desired as a diluent for the cook.
  • Still another object of the invention is the utilization of the pressure under which the hot I black liquor is introduced and the steam gen- -erated when this pressure is released, in the act of introduction, to pack the chips in the digester being filled.
  • a quantity of black liquor is transferred under digester pressure from glass measuring gauge on the side of the digester
  • the black liquor thus transferred is most suitably introduced into the digester together with and substantially in the same direction as the entering stream of chips, that is to say at the upper end of the digester.
  • the pressure under which the hot black liquor is introduced and the steam generated when this pressure is released in the act of introduction are utilized to pack the chips in the digester being filled. Since it has proved that using this procedure the chips are wetted completely by the black liquor, the inflow of the 2 liquoris regulated to make the time necessary for introduction into the digester of the entire amount of liquor in question at least approximately equal to the time needed for filling the digester with chips.
  • Such even wetting of 'the chips with black liquor is, of course, partly instrumental in promoting even results in the cook, and a particularly favorable result in this respect is achieved if the hot black liquor under pressure intended to be introduced into the digester to be used as the power medium in a chip distributor of any suitable design operating with pressure.
  • the inflow of black liquor should be regulated to make the time needed to transfer into the digester the whole intended amount of black liquor correspond as nearly as possible to that needed for filling the digester with chips.
  • Figure 1 is a diagrammatic showing of the coupling of the two digesters for the carrying outof the method-of the inverfion, and
  • Figure 2 is an enlarged fragmentary diagrammatic showing of the entrant portion of a digester with a chip distributor applied thereto.
  • the digester l is illustrative of a digester in which a sulfate cook has been completed. It has side relief lines at 2 and 3 from which black liquor may be taken off and run into the line 4 through suitable valves 5 and 6.
  • This digester would normally have a pre-heater such as I, and a recirculating pump such as 8, for recirculating liquor into the digester itself, as controlled by the valves 9, l0 and II.
  • the black liquor from the digester l is piped right through the line 4, past the valves l2 and I3 and through the valve 14 into the upper end [5 of the digester being charged.
  • the black liquor is discharged out of a nozzle, as shown at l 6.
  • the black liquor has been brought substantially directly from the digester I and has been maintained under substantially the same temperature and pressure which it had on leaving the digester I at the completion of the cook in that digester.
  • the pressure is released and it serves to pack the chips, as shown at IT, in the digester l8.
  • the black liquor and the chips are introduced in the same direction and together with each other at the upper end of the digester.
  • Packing is effected by the introduction of the hot black liquor and the steam generated when the pressure on the liquor is released in the act of introduction.
  • the tim for introducing the liquor is equal to the time needed for filling the digester with chips. In this manner, the chips are evenly wetted and impregnated with the black liquor as they are packed in the digester, as shown at l9.
  • the supply of black liquor is shut off and a valve, such as 20, is opened for the introduction of fresh cooking liquor.
  • of a digester 22 is shown as equipped with a suitable chip distributor having a tubular portion 23 extending into the mouth from a conical portion 24 above the same.
  • Black liquor is introduced into the distributo through the nozzle 25 having a downturned end 26 exhausting at 2'! and the black liquor serves as the pressure medium for operating the distributor to distribute the chips as well as packing and impregnating them.
  • the black liquor to be used as a diluent for the cooking liquor is taken under pressure from a completed sulfate cook in another digester and introduced into the digester to be charged without any material loss of pressure.
  • the heat content in the black liquor is substantially completely utilized.
  • the pressure and temperature conditions of a finished digestion are taken advantage of and the chips are caused to be soaked in black liquor during the process ofcharging.
  • the invention achieves its results by the simultaneous introduction of the black liquor and the chips and the taking up of substantially all of the'black liquor by the impregnation of the chips, so that free black liquor to be engaged by fresh cooking liquoris kept to a minimum. Furthermore, economy is enhanced by utilizing the black liquor under substantially the temperature and pressure that it had when leaving the previous digester for the introducing and packing of the chips.
  • the process of manufacturing sulphate pulp which comprises the following steps, simultaneously charging a digester with chips and with. black liquor under pressure, which black liquor has been obtained-from a previous completed sulfate cook, and thereby packing the chips into the digester with said black liquor, said black liquor being substantially under the same temperature and pressure that it had, when withdrawn from said previous cook, said black liquor in said charging operation being in sufficient amount to practically impregnate the whole of said charge of chips with black liquor and,

Description

Patented Oct. 21, 1952 2,614,923 q DIGESTER FILLING IN SULFATE PULPING Oma Tarkkonen, Sunila, FinlandQassignor of one-- half to Sunila Osakeyhtio, Sunila, Finland, a corporation of Finland n Application February 1, 1947, SerialNo. 725,963
In Finland April 19,46
2 Claims.
[The invention here presented concerns the method of procedure in the production of sulfate pulp and intends a saving of steam needed for digestion as well as a reduction of the digestion time by utilizing the heat of the black liquor from digesters in which the cook has been completed.
This invention has for its object the utilization of the heat contained in the quantity of black liquor to be used in the charge of a digester,
which black liquor is obtained from a preceding completed sulfate cook and is under substantially the pressure and temperature conditions of a finished digestion, by the introduction of the quantity of black liquor to be used as a diluent for the cooking liquor into the digester to be charged before adding the white liquor and simultaneously and together with the chips causing practically the whole charge of the chips to be soaked in black liquor during the process of charging.
Another object of this invention is to utilize substantially the entire heat content and pressure of the aforementioned black liquor with the amount of black liquor so employed practically corresponding to thetotal amount of black liquor desired as a diluent for the cook.
Still another object of the invention is the utilization of the pressure under which the hot I black liquor is introduced and the steam gen- -erated when this pressure is released, in the act of introduction, to pack the chips in the digester being filled.
According to this invention a quantity of black liquor is transferred under digester pressure from glass measuring gauge on the side of the digester,
or by means of some other measuring device. The black liquor thus transferred is most suitably introduced into the digester together with and substantially in the same direction as the entering stream of chips, that is to say at the upper end of the digester. The pressure under which the hot black liquor is introduced and the steam generated when this pressure is released in the act of introduction are utilized to pack the chips in the digester being filled. Since it has proved that using this procedure the chips are wetted completely by the black liquor, the inflow of the 2 liquoris regulated to make the time necessary for introduction into the digester of the entire amount of liquor in question at least approximately equal to the time needed for filling the digester with chips. Such even wetting of 'the chips with black liquor is, of course, partly instrumental in promoting even results in the cook, and a particularly favorable result in this respect is achieved if the hot black liquor under pressure intended to be introduced into the digester to be used as the power medium in a chip distributor of any suitable design operating with pressure. In this case alsothe inflow of black liquor should be regulated to make the time needed to transfer into the digester the whole intended amount of black liquor correspond as nearly as possible to that needed for filling the digester with chips. When the digester is filled with chips and the intended amount of black liquor has been simultaneously introduced, the necessary amount of white liquor is added and the cook is carried out in the known manner.
' t Figure 1 is a diagrammatic showing of the coupling of the two digesters for the carrying outof the method-of the inverfion, and
Figure 2 is an enlarged fragmentary diagrammatic showing of the entrant portion of a digester with a chip distributor applied thereto.
In the diagrammatic showing of Figure 1, the digester l is illustrative of a digester in which a sulfate cook has been completed. It has side relief lines at 2 and 3 from which black liquor may be taken off and run into the line 4 through suitable valves 5 and 6. This digester would normally have a pre-heater such as I, and a recirculating pump such as 8, for recirculating liquor into the digester itself, as controlled by the valves 9, l0 and II.
According to the instant invention, however, the black liquor from the digester l is piped right through the line 4, past the valves l2 and I3 and through the valve 14 into the upper end [5 of the digester being charged. The black liquor is discharged out of a nozzle, as shown at l 6. Up until this point the black liquor has been brought substantially directly from the digester I and has been maintained under substantially the same temperature and pressure which it had on leaving the digester I at the completion of the cook in that digester. Thus, when the black liquor emerges at It the pressure is released and it serves to pack the chips, as shown at IT, in the digester l8. As already pointed out, the black liquor and the chips are introduced in the same direction and together with each other at the upper end of the digester. Packing is effected by the introduction of the hot black liquor and the steam generated when the pressure on the liquor is released in the act of introduction. The tim for introducing the liquor is equal to the time needed for filling the digester with chips. In this manner, the chips are evenly wetted and impregnated with the black liquor as they are packed in the digester, as shown at l9.
Once the introduction of black liquor and chips is completed with the quantity of black liquor being substantially what is needed for the impregnation of the chips, the supply of black liquor is shut off and a valve, such as 20, is opened for the introduction of fresh cooking liquor.
In the enlarged showing of Figure 2, the mouth 2| of a digester 22 is shown as equipped with a suitable chip distributor having a tubular portion 23 extending into the mouth from a conical portion 24 above the same. Black liquor is introduced into the distributo through the nozzle 25 having a downturned end 26 exhausting at 2'! and the black liquor serves as the pressure medium for operating the distributor to distribute the chips as well as packing and impregnating them. 7
QFrom the foregoing and from. the accompanying drawing, it will be clearly apparent that the black liquor to be used as a diluent for the cooking liquor is taken under pressure from a completed sulfate cook in another digester and introduced into the digester to be charged without any material loss of pressure. At the same time, the heat content in the black liquor is substantially completely utilized. Thus, the pressure and temperature conditions of a finished digestion are taken advantage of and the chips are caused to be soaked in black liquor during the process ofcharging.
I .The invention achieves its results by the simultaneous introduction of the black liquor and the chips and the taking up of substantially all of the'black liquor by the impregnation of the chips, so that free black liquor to be engaged by fresh cooking liquoris kept to a minimum. Furthermore, economy is enhanced by utilizing the black liquor under substantially the temperature and pressure that it had when leaving the previous digester for the introducing and packing of the chips.
What I claim as my invention is:
1. The process of manufacturing sulphate pulp which comprises the following steps, simultaneously charging a digester with chips and with. black liquor under pressure, which black liquor has been obtained-from a previous completed sulfate cook, and thereby packing the chips into the digester with said black liquor, said black liquor being substantially under the same temperature and pressure that it had, when withdrawn from said previous cook, said black liquor in said charging operation being in sufficient amount to practically impregnate the whole of said charge of chips with black liquor and,
after said impregnated chips are packed in said digester, then adding the requisite amount of white liquor to said digester to digest said impregnated chips.
2. A process as in claim 1 and including utilizing a chip distributor for the packing of the chips into the digester and operating said chip distributor by the introduction of said black liquor under pressure from a completed cook.
OMA ,TARKKONEN.
REFERENCES CITED The following references are of record in the ofthis patent:
UNITED STATES PATENTS OTHER REFERENCES I Manufacture of Pulp and Paper, Third Edition, volume III, section 5, page 5 (1937), published by McGraw-Hill Book Co., Inc., New York.

Claims (1)

1. THE PROCESS OF MANUFACTURING SULPHATE PULP WHICH COMPRISES THE FOLLOWING STEPS, SIMULTANEOUSLY CHARGING A DIGESTER WITH CHIPS AND WITH BLACK LIQUOR UNDER PRESSURE, WHICH BLACK LIQUOR HAS BEEN OBTAINED FROM A PREVIOUS COMPLETED SULFATE COOK, AND THEREBY PACKING THE CHIPS INTO THE DIGESTER WITH SAID BLACK LIQUOR, SAID BLACK LIQUOR BEING SUBSTANTIALLY UNDER THE SAME TEMPERATURE AND PRESSURE THAT IT HAD WHEN WITHDRAWN FROM SAID PREVIOUS COOK, SAID BLACK LIQUOR IN SAID CHARGING OPERATION BEING IN SUFFICIENT AMOUNT TO PARTICALLY IMPREGNATE THE WHOLE OF SAID CHARGE OF CHIPS ARE PACKED IN SAID AFTER SAID IMPREGNATED CHIPS ARE PACKED IN SAID WHITE LIQUOR TO SAID DIGESTER TO DIGEST SAID IMDIGESTER, THEN ADDING THE REQUISITE AMOUNT OF PREGNATED CHIPS.
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Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2747995A (en) * 1952-03-12 1956-05-29 Rayonier Inc Method of pulp production
US2809111A (en) * 1956-02-13 1957-10-08 Condi Engineering Corp Apparatus for wood chip digestion
US2901039A (en) * 1954-12-20 1959-08-25 Sven A Salmonson Apparatus for preconditioning chips in a digester
US2938825A (en) * 1953-01-30 1960-05-31 Babcock & Wilcox Co Method of resisting digester corrosion
US2950757A (en) * 1953-01-30 1960-08-30 Babcock & Wilcox Co Apparatus for avoiding digester corrosion
US3881986A (en) * 1965-02-25 1975-05-06 Svenska Cellulosa Ab Method of producing homogeneously delignified pulp from fibrous material, containing lignocellulose, in a digester partially filled with liquor
US4028171A (en) * 1974-07-05 1977-06-07 Kamyr Aktiebolag Method for continuous treatment of fiber material in a vertical array
US5059284A (en) * 1989-10-30 1991-10-22 Beloit Corporation Apparatus to displace a digester from both ends
US20110005696A1 (en) * 2008-03-31 2011-01-13 Magnus Danielsson Device and method for dilution of cellulose pulp

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1609832A (en) * 1919-08-16 1926-12-07 Rinman Erik Ludvig Process of pretreating wood chips in the production of soda cellulose
US1657048A (en) * 1925-12-07 1928-01-24 George H Tomlinson Method of cooking sulphite pulp
US1694139A (en) * 1927-06-30 1928-12-04 Olsson Elis Charging apparatus for pulp digesters
US1697032A (en) * 1925-12-07 1929-01-01 George H Tomlinson Method of cooking sulphite pulp
US1889158A (en) * 1928-05-18 1932-11-29 Edward Charles Benthall Method of controlling the treatment of vegetable matter to obtain cellulose therefrom by manipulation of the vomit pipes

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1609832A (en) * 1919-08-16 1926-12-07 Rinman Erik Ludvig Process of pretreating wood chips in the production of soda cellulose
US1657048A (en) * 1925-12-07 1928-01-24 George H Tomlinson Method of cooking sulphite pulp
US1697032A (en) * 1925-12-07 1929-01-01 George H Tomlinson Method of cooking sulphite pulp
US1694139A (en) * 1927-06-30 1928-12-04 Olsson Elis Charging apparatus for pulp digesters
US1889158A (en) * 1928-05-18 1932-11-29 Edward Charles Benthall Method of controlling the treatment of vegetable matter to obtain cellulose therefrom by manipulation of the vomit pipes

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2747995A (en) * 1952-03-12 1956-05-29 Rayonier Inc Method of pulp production
US2938825A (en) * 1953-01-30 1960-05-31 Babcock & Wilcox Co Method of resisting digester corrosion
US2950757A (en) * 1953-01-30 1960-08-30 Babcock & Wilcox Co Apparatus for avoiding digester corrosion
US2901039A (en) * 1954-12-20 1959-08-25 Sven A Salmonson Apparatus for preconditioning chips in a digester
US2809111A (en) * 1956-02-13 1957-10-08 Condi Engineering Corp Apparatus for wood chip digestion
US3881986A (en) * 1965-02-25 1975-05-06 Svenska Cellulosa Ab Method of producing homogeneously delignified pulp from fibrous material, containing lignocellulose, in a digester partially filled with liquor
US4028171A (en) * 1974-07-05 1977-06-07 Kamyr Aktiebolag Method for continuous treatment of fiber material in a vertical array
US5059284A (en) * 1989-10-30 1991-10-22 Beloit Corporation Apparatus to displace a digester from both ends
US20110005696A1 (en) * 2008-03-31 2011-01-13 Magnus Danielsson Device and method for dilution of cellulose pulp

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