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US3035962A - Digesting apparatus - Google Patents

Digesting apparatus Download PDF

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Publication number
US3035962A
US3035962A US789600A US78960059A US3035962A US 3035962 A US3035962 A US 3035962A US 789600 A US789600 A US 789600A US 78960059 A US78960059 A US 78960059A US 3035962 A US3035962 A US 3035962A
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Prior art keywords
vessel
column
steam
pressure vessel
materials
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Expired - Lifetime
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US789600A
Inventor
Schinn Ernst
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Sulzer Escher Wyss GmbH
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Escher Wyss GmbH
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Publication of US3035962A publication Critical patent/US3035962A/en
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    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21CPRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
    • D21C7/00Digesters
    • D21C7/10Heating devices

Definitions

  • This invention relates to an apparatus for continuously digesting brous vegetable materials, for example wood chips, which comprises a vertically mounted elongated vessel, in which the materials form a downwardly moving column, the said materials being introduced into the top of the pressure vessel, heated and digested by a supply of steam and, after the completion of the pulping, delivered from the bottom of the pressure vessel.
  • An apparatus of this type in which the heating steam is fed to those parts of the materials which are situated in the lower part of the column of material in the pressure vessel.
  • the invention has for its object to ensure a better heating, a more intensive digestion and ⁇ a lower consumption of steam than in the known construction.
  • the steam is for this purpose fed to the upper part of the colum of material, means being thereby provided for distributing the steam within the material.
  • the steam in the space above the column of material is substantially at fresh steam pressure Iand thus forces the column of material toward the delivery end of the vessel, so that no mechanical means are required for the conveyance of the material.
  • the column of material is in addition compressed, its compactness increasing with the increasing degree of pulping towards the delivery end.
  • the compact lower power part of the column separates the steam space of the vessel and that part of the column which carries the free steam from the delivery chamber, so that substantially no steam escapes during the delivery.
  • a constructional example of the subject of the invention is illustrated in simplified vform in the drawing, which shows a vertical section through a pressure vessel and a container for receiving the materials delivered therefrom.
  • the illustrated arrangement comprises a pressure vessel 1, a feed hopper 2 and a rotary valve 3 driven by a motor 31.
  • a delivery deviceV 7 driven by a motor 71 and an exhausting valve 8 are provided at the bottom of the vessel 1.
  • An exhaust duct 9 leads into lan expansion container 10.
  • a column of material 11 is maintained at :a constant level by means of a feeler member 12 controlling the exhausting valve 8, whereby the digested material is continuously discharged from the bottom of the vessel 1.
  • la steam space 13 Situated above the column of material 11 is la steam space 13.
  • the material previously impregnated with the chemicals necessary lfor the digestion is introduced in portions without surrounding liquor into the pressure vessel 1 through the hopper 2 by way of the rotary valve 3.
  • the material supply is quasi-continuous.
  • the introduced material falls through the steam space 13, in which it is preheated, on to the column of material 11. ln the uppermost part of the column of material 11, the material is further heated and above all uniformly permeated with the steam, which is supplied through the pipes 6.
  • the material is thus brought to digesting temperature already on the upper part of the material column.
  • the steam may be supplied with a temperature of about C. and a pressure of Iabout 8 to 10 kg./cm.2 tabs. m-ay be maintained Within the vessel.
  • the pressure vessel is constructed with a double jacket.
  • the lwall 1 of the Vessel forms the outer jacket, and the jacket 4 is the inner jacket.
  • the inner jacket 4 comprises a sieve-like portion in the region of the uppermost part of the material column.
  • the steam introduced through the pipes 6 is uniformly distributed in the intermediate space of the double jacket 1, 4 and -then passes through the holes 41 into the column of material 11.
  • the holes 41 are distributed over the circumference of the jacket 4.
  • the pipe 5 extending from above the material column 11 in the vertical direction through the uppermost part of the column 11 is provided, which is formed with lateral holes 51 for distributing the steam Within the column.
  • two or more pipes may be provided for the supply of steam to the interior of the -material column 11.
  • the pipe 5 extends in the direction of movement of the compact column off material 11 where it comes into contact with the latter, and extends transversely to the direction of movement of the materialy only in the steam space 13, where the material is still loose.
  • the jacket 4 of the pressure vessel 1, which surrounds the column of material 11, widens conically in the downward direction, in order that the column of material 11 may pass through the vessel 1 with minimum resistance.
  • the pressure vessel has a double jacket throughout, but it could -alternatively be only partially double-jacketed, preferably in its upper part.
  • Apparatus for continuously digesting fibrous vegetable materials comprising in combination a vertically mounted elongated pressure vessel; means at the top of said vessel for continuously introducing iibrous vegetable materials impregnated with digesting liquor into said pressure vessel; means for continuously discharging digested material from the bottom of said pressure vessel; means, responsive to the level of the column of material in said vessel, controlling the rate of discharge through said discharge means so as to maintain a constant level of said column of material intermediate the upper and lower ends of said pressure vessel; and means tor introducing steam into the space in said vessel above said level by distributedly introducing steam through the uppermost part of said column of material.
  • said last-mentioned means comprises a jacket encircling at least a portion of the side Walls of said pressure vessel below the level of material therein, said portion of the side walls being provided with a circumferential series of apertures; aand conduit means extending into said pressure vessel and including a perforated portion in the region of the uppermost part of said column of material.
  • said 'conduit means comprises at least one pipe extending from above the column of material in a vertical direction through the uppermost part of Ithe material column, said pipe being provided with lateral holes yfor introducing steam distributedly through the uppermost part of said column.

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Description

May 22, 1962 E. scHlNN DIGESTING APPARATUS Filed Jan. 28, 1959 INVENTQR. Ern sc Schmn 5f ,dwf SLW Aornegs 3,35h2 Patented May 22, 1962 3,035,962 D1GESTING APPARATUS Ernst Sebina, Weingartsbof, near Ravensburg, Win-temberg, Germany, assignor to Escher Wyss G.m.b.H.,
Ravensburg, Wurttemherg, Germany, a corporation of Germany Filed Jan. 28, 1959, Ser. No. 789,600 Claims priority, application Germany Feb. 6, 1958 Claims. (Cl. 162-17) This invention relates to an apparatus for continuously digesting brous vegetable materials, for example wood chips, which comprises a vertically mounted elongated vessel, in which the materials form a downwardly moving column, the said materials being introduced into the top of the pressure vessel, heated and digested by a supply of steam and, after the completion of the pulping, delivered from the bottom of the pressure vessel.
An apparatus of this type is known, in which the heating steam is fed to those parts of the materials which are situated in the lower part of the column of material in the pressure vessel.
The invention has for its object to ensure a better heating, a more intensive digestion and `a lower consumption of steam than in the known construction. In accordance with the invention, in an arrangemet of the above-described type, the steam is for this purpose fed to the upper part of the colum of material, means being thereby provided for distributing the steam within the material.
ln this way, a rapid and uniform heating of the introduced impregnated material can be effected. The steam in the space above the column of material is substantially at fresh steam pressure Iand thus forces the column of material toward the delivery end of the vessel, so that no mechanical means are required for the conveyance of the material. The column of material is in addition compressed, its compactness increasing with the increasing degree of pulping towards the delivery end. The compact lower power part of the column separates the steam space of the vessel and that part of the column which carries the free steam from the delivery chamber, so that substantially no steam escapes during the delivery. There is merely formed by the pressure difference between the pressure vessel and the delivery duct expansion steam which can be used for conveying the delivered materials.
A constructional example of the subject of the invention is illustrated in simplified vform in the drawing, which shows a vertical section through a pressure vessel and a container for receiving the materials delivered therefrom.
The illustrated arrangement comprises a pressure vessel 1, a feed hopper 2 and a rotary valve 3 driven by a motor 31. A jacket 4 formed with holes 41 and a pipe 5 formed with holes 51, together with feed pipes 6, serve for the supply of the steam. A delivery deviceV 7 driven by a motor 71 and an exhausting valve 8 are provided at the bottom of the vessel 1. An exhaust duct 9 leads into lan expansion container 10. In the pressure vessel 1, a column of material 11 is maintained at :a constant level by means of a feeler member 12 controlling the exhausting valve 8, whereby the digested material is continuously discharged from the bottom of the vessel 1. Situated above the column of material 11 is la steam space 13.
The material previously impregnated with the chemicals necessary lfor the digestion is introduced in portions without surrounding liquor into the pressure vessel 1 through the hopper 2 by way of the rotary valve 3. The material supply is quasi-continuous. The introduced material falls through the steam space 13, in which it is preheated, on to the column of material 11. ln the uppermost part of the column of material 11, the material is further heated and above all uniformly permeated with the steam, which is supplied through the pipes 6. The material is thus brought to digesting temperature already on the upper part of the material column. The steam may be supplied with a temperature of about C. and a pressure of Iabout 8 to 10 kg./cm.2 tabs. m-ay be maintained Within the vessel.
Means are here provided for the uniform distribution of the steam throughout the entire cross-section of the column of material. The pressure vessel is constructed with a double jacket. The lwall 1 of the Vessel forms the outer jacket, and the jacket 4 is the inner jacket. The inner jacket 4 comprises a sieve-like portion in the region of the uppermost part of the material column. The steam introduced through the pipes 6 is uniformly distributed in the intermediate space of the double jacket 1, 4 and -then passes through the holes 41 into the column of material 11. The holes 41 are distributed over the circumference of the jacket 4.
In order that the column of material 11 may at the same time also receive steam from the inside, the pipe 5 extending from above the material column 11 in the vertical direction through the uppermost part of the column 11 is provided, which is formed with lateral holes 51 for distributing the steam Within the column. Instead of a single pipe 5 two or more pipes may be provided for the supply of steam to the interior of the -material column 11.
The pipe 5 extends in the direction of movement of the compact column off material 11 where it comes into contact with the latter, and extends transversely to the direction of movement of the materialy only in the steam space 13, where the material is still loose.
The jacket 4 of the pressure vessel 1, which surrounds the column of material 11, widens conically in the downward direction, in order that the column of material 11 may pass through the vessel 1 with minimum resistance.
In the illustrated constructional example, the pressure vessel has a double jacket throughout, but it could -alternatively be only partially double-jacketed, preferably in its upper part.
What is claimed is:
1. Apparatus for continuously digesting fibrous vegetable materials comprising in combination a vertically mounted elongated pressure vessel; means at the top of said vessel for continuously introducing iibrous vegetable materials impregnated with digesting liquor into said pressure vessel; means for continuously discharging digested material from the bottom of said pressure vessel; means, responsive to the level of the column of material in said vessel, controlling the rate of discharge through said discharge means so as to maintain a constant level of said column of material intermediate the upper and lower ends of said pressure vessel; and means tor introducing steam into the space in said vessel above said level by distributedly introducing steam through the uppermost part of said column of material.
2. The combination deiined in claim 1 in which said last-mentioned means comprises a jacket encircling at least a portion of the side Walls of said pressure vessel below the level of material therein, said portion of the side walls being provided with a circumferential series of apertures; aand conduit means extending into said pressure vessel and including a perforated portion in the region of the uppermost part of said column of material.
3. The combination dened in claim v2 in which said 'conduit means comprises at least one pipe extending from above the column of material in a vertical direction through the uppermost part of Ithe material column, said pipe being provided with lateral holes yfor introducing steam distributedly through the uppermost part of said column.
4. The method of digesting fibrous vegetable materials in a vertically mounted pressure vessel, Which method consists in continuously feeding said materials, impregnated with digesting liquor, into the upper end of said vessel; removing the digested material from the lower end of said vessel; automatically controlling the rate of removal inresponse to the level of the column of 4the ibrous material in said vessel so as to maintain a constant level of material therein intermediate its upper and lower ends, thereby forming a space in said vessel above the level of said column of material and through which said materials fed to the vessel fall; and introducing steam into said space in said vessel by distributedly introducing said steam through the uppermost part of said column.
References Cited in the le of this patent UNITED STATES PATENTS Ball Feb. 16, Hildebrandt May 5, Brubacher July 16, Campbell Aug, 17, Natwick Apr. 13, Richter Nov. 23, Becker Nov. 6, Obenshain Apr. 16, Durant Oct. 28, Schandroch Mar. 3,

Claims (1)

  1. 4. THE METHOD OF DIGESTING FIBROUS VEGETABLE MATERIALS IN A VERTICALLY MOUNTED PRESSURE VESSEL, WHICH METHOD CONSISTS IN CONTINUOUSLY FEEDING SAID MATERIALS, IMPREGNATED WITH DIGESTING LIQUOR, INTO THE UPPER END OF SAID VESSEL; REMOVING THE DIGESTED MATERIAL FROM THE LOWER END OF SAID VESSEL; AUTOMATICALLY CONTROLLING THE RATE OF REMOVAL IN RESPONSE TO THE LEVEL OF THE COLUMN OF THE FIBROUS MATERIAL IN SAID VESSEL SO AS TO MAINTAIN A CONSTANT LEVE OF MATERIAL THEREIN INTERMEDIATE ITS UPPER AND LOWER ENDS, THEREBY FORMING A SPACE IN SAID VESSEL ABOVE THE LEVEL OF SAID COLUMN OF MATERIAL AND THROUGH WHICH SAID MATERIALS FED TO THE VESSEL FALL; AND INTRODUCING STEAM INTO
US789600A 1958-02-06 1959-01-28 Digesting apparatus Expired - Lifetime US3035962A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DEE15320A DE1080848B (en) 1958-02-06 1958-02-06 Device for the continuous digestion of fibrous vegetable substances in the pulp industry

Publications (1)

Publication Number Publication Date
US3035962A true US3035962A (en) 1962-05-22

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US789600A Expired - Lifetime US3035962A (en) 1958-02-06 1959-01-28 Digesting apparatus

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US (1) US3035962A (en)
CH (1) CH368375A (en)
DE (1) DE1080848B (en)
FR (1) FR1214711A (en)
GB (1) GB908702A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3293118A (en) * 1963-03-27 1966-12-20 Improved Machinery Inc High density pulp and steam mixing
US3434921A (en) * 1966-04-18 1969-03-25 Improved Machinery Inc Continuous digester with multiple column discharger
US4867845A (en) * 1988-06-15 1989-09-19 Kamyr, Inc. Vertical steaming vessel
US5114540A (en) * 1989-09-05 1992-05-19 Kwei-Nam Law Apparatus for chemical treatment of lignocellulosic materials
US10087578B2 (en) 2013-08-09 2018-10-02 Inbicon A/S Device for discharging pretreated biomass from higher to lower pressure regions

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
SE453673B (en) * 1985-07-02 1988-02-22 Kamyr Ab SEE CONTINUOUS COOKING TO HEAT THE FIBER MATERIAL AT THE COOKER'S TOP
CN102517951A (en) * 2011-12-14 2012-06-27 中国制浆造纸研究院 Heating device for cooking boiler

Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US336078A (en) * 1886-02-16 Charles e
US1803444A (en) * 1928-11-20 1931-05-05 Howard B Salkeld Digester
US2008635A (en) * 1932-05-05 1935-07-16 Brubacher William Process of and apparatus for producing pulp
US2089992A (en) * 1932-03-14 1937-08-17 Int Paper Co Continuous bleaching process and apparatus
US2675311A (en) * 1948-08-09 1954-04-13 John W Natwick Paper pulp process and apparatus
US2695232A (en) * 1950-07-08 1954-11-23 Kamyr Ab Apparatus for heating and controlling the temperature of a continuously operating cellulose digester
US2769710A (en) * 1954-01-12 1956-11-06 Cellulose Dev Corp Ltd Process for the continuous treatment of vegetable fibers
US2789051A (en) * 1951-12-06 1957-04-16 West Virginia Pulp & Paper Co Method for continuous cooking of chips in the manufacture of pulp
US2858213A (en) * 1956-04-20 1958-10-28 Condi Engineering Corp Wood chip digestion
US2876098A (en) * 1956-01-11 1959-03-03 Hans Werner Meyer Process of and apparatus for the continuous manufacture of cellulose or hemicellulose from cellulosic fibrous materials

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE404506C (en) * 1921-12-01 1924-10-18 A Olier Sa Des Ets Process and device for the production of pulp from wood-containing raw material
US1807544A (en) * 1929-02-26 1931-05-26 Morterud Einar Directly heated pulp digester
DE941529C (en) * 1942-10-15 1956-04-12 Kamyr Ab Method and device for opening up fiber material under pressure
DE868695C (en) * 1943-10-10 1953-02-26 Kamyr Ab Device for loading pulp digesters under pressure
DE897798C (en) * 1948-04-21 1953-11-23 Kamyr Ab Method and device for introducing and discharging fibrous materials in the event of a pressure difference, especially for continuous cookers
FR1048798A (en) * 1951-07-27 1953-12-23 Process and devices for the preparation of semi-celluloses and celluloses

Patent Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US336078A (en) * 1886-02-16 Charles e
US1803444A (en) * 1928-11-20 1931-05-05 Howard B Salkeld Digester
US2089992A (en) * 1932-03-14 1937-08-17 Int Paper Co Continuous bleaching process and apparatus
US2008635A (en) * 1932-05-05 1935-07-16 Brubacher William Process of and apparatus for producing pulp
US2675311A (en) * 1948-08-09 1954-04-13 John W Natwick Paper pulp process and apparatus
US2695232A (en) * 1950-07-08 1954-11-23 Kamyr Ab Apparatus for heating and controlling the temperature of a continuously operating cellulose digester
US2789051A (en) * 1951-12-06 1957-04-16 West Virginia Pulp & Paper Co Method for continuous cooking of chips in the manufacture of pulp
US2769710A (en) * 1954-01-12 1956-11-06 Cellulose Dev Corp Ltd Process for the continuous treatment of vegetable fibers
US2876098A (en) * 1956-01-11 1959-03-03 Hans Werner Meyer Process of and apparatus for the continuous manufacture of cellulose or hemicellulose from cellulosic fibrous materials
US2858213A (en) * 1956-04-20 1958-10-28 Condi Engineering Corp Wood chip digestion

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3293118A (en) * 1963-03-27 1966-12-20 Improved Machinery Inc High density pulp and steam mixing
US3434921A (en) * 1966-04-18 1969-03-25 Improved Machinery Inc Continuous digester with multiple column discharger
US4867845A (en) * 1988-06-15 1989-09-19 Kamyr, Inc. Vertical steaming vessel
US5114540A (en) * 1989-09-05 1992-05-19 Kwei-Nam Law Apparatus for chemical treatment of lignocellulosic materials
US10087578B2 (en) 2013-08-09 2018-10-02 Inbicon A/S Device for discharging pretreated biomass from higher to lower pressure regions

Also Published As

Publication number Publication date
GB908702A (en) 1962-10-24
CH368375A (en) 1963-03-31
FR1214711A (en) 1960-04-11
DE1080848B (en) 1960-04-28

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