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US3619348A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for continuous cellulose cooking

Assignee: Valmet AB
•
Filing: 1969-09-05
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Granted: 1971-11-09
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Expires: 1989-09-05
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Abstract

Abstract The invention provides an apparatus and method for producing cellulosic pulp. A downwardly moving column of cellulosic material is contacted with a countercurrent flow of steam in a steaming zone. The steaming zone is maintained at an atmospheric pressure and temperature effective to expel air from the material without causing discoloration thereof. The temperature may be from 100* C. to 120* C. The steamed material is preimpregnated in a zone which is sealed from the ambient air. The preimpregnation is effected by contacting the steamed material with cold liquor having a temperature below that of the steamed material and effective to produce a rapid absorption of liquor therein. The cold liquor temperature is in the range of about 20* C. to about 80* C., and pressures of up to 10 gauge pressures can be employed. A condensate material resulting from the steaming treatment is separated from the cellulosic material after it has been subjected to the steaming treatment. The preimpregnated cellulosic material is sluiced through an impregnating zone containing hot cooking liquor at a temperature and superatmospheric pressure sufficient to effect impregnation thereof. The temperature within the impregnating zone may range from 100* C. to 180* C. and increase in the direction of material movement. The impregnated material is then passed from the impregnating zone for subsequent introduction into any desired pulp vapor phase digesting zone. The disclosed apparatus is used to effect the various process steps of the overall treatment.

Inventors

  • 👤 Arne Johan Arthur Asplund
  • 👤 Karl Nicolaus Cederquist
  • 👤 Rolf Bertil Reinhall

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-08 21:17
CPC Classifications
D; D21; D21C; D21C3/00; D21C3/22; D21C3/24

Claims Analysis

Total Claims: 11
Claim 1
Independent Claim 22 words
The method as defined in claim 1 wherein the contact between the cellulosic material and the cold liquor is effected by immersion.
Claim 2
Dependent Claim 51 words
The method as defined in claim 1 wherein the impregnating zone has an introduction section and an end section and the cooking liquor in the impregnating zone is recirculated frOm the end section to the introduction section thereof to reduce the temperature gradient existing in the impregnating zone between said sections.
Claim 3
Dependent Claim 21 words
The method as defined in claim 1 wherein the cellulosic material is subjected to a hydraulic pressure during the preimpregnating step.
Claim 4
Dependent Claim 17 words
The method as defined in claim 4 wherein the hydraulic pressure is of about 2-10 gauge pressures.
Claim 5
Dependent Claim 24 words
The method as defined in claim 1 wherein the cooking liquor is separated from the impregnated material prior to passing into said digestion zone.
Claim 6
Dependent Claim 32 words
The method as defined in claim 6 wherein the impregnated material is digested in the digesting zone having an atmosphere of steam at a temperature of about 150* C. to 200* C.
Claim 7
Dependent Claim 37 words
The method as defined in claim 7 including the step of passing the digested material from the digesting zone to an evacuation zone where it is cooled to a temperature sufficient to effect further pulp treatment steps.
Claim 8
Dependent Claim 50 words
The method as defined in claim 1 wherein the impregnating zone is filled with hot cooking liquor to a predetermined level with an atmosphere of steam thereabove, such that the mixture of said material and said cold cooking liquor entering the impregnating zone is subjected to said atmosphere of steam.
Claim 9
Dependent Claim 32 words
The method as defined in claim 1 wherein surplus cold liquor from the preimpregnating of the steamed material is cooled and recirculated to its source for further use in the preimpregnating zone.
Claim 10
Dependent Claim 167 words
A continuously operable pulp digesting apparatus for treating cellulosic material comprising a. a steaming vessel in which the cellulosic material to be digested descends in contact with a countercurrent flow of steam, b. a preimpregnating vessel connected to said steaming vessel, said preimpregnating vessel consisting of a transfer valve, c. means for expelling condensate from the cellulosic material before the cellulosic material enters the preimpregnating vessel, d. an impregnating pressure vessel below said preimpregnating vessel and connected thereto, e. means for passing cold liquor through said preimpregnating vessel, f. means for circulating hot cooking liquor from the bottom portion to the top portion of said impregnating vessel, g. a digesting vessel below said impregnating vessel, h. valve means located between said impregnating vessel and said digesting vessel for sluicing impregnated material into the digesting vessel, i. means for evacuating the free cooking liquor through said valve means to return it to said impregnating vessel and j. means for simultaneously evacuating steam and gases from the digesting vessel.
Claim 11
Dependent Claim 22 words
An apparatus as defined in claim 11 wherein a curved tube is located between the transfer valve and the said impregnating vessel.

References Cited (Backward Citations)

US2858213A Cited
US3165436A Cited
US3303088A Cited
US3471365A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1974-11-08 1975-05-10 1975-11-09 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1978-11-08 1979-05-10 1979-11-09 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1982-11-08 1983-05-10 1983-11-09 $7700.00 Window Closed / Lapsed

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