US4136831A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method and apparatus for minimizing steam consumption in the production of pulp for fiberboard and the like
Assignee: Isel SA
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Filing: 1977-08-04
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Granted: 1979-01-30
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Expires: 1997-08-04
Abstract
Abstract Method and apparatus for minimizing steam consumption in the production of pulp used for the manufacture of fiberboard and the like, in which chips of cellulosic material are ground in a defibrator or refiner in an environment of saturated steam above 100° C and corresponding steam pressures. The chips are normally presteamed with atmospheric steam separated from the pulp at the discharge end of the defibrating process to a temperature between 90° C and 100° C and compressed and dewatered to a dryness of at least 50% and then passed into a preheater which forms part of the defibrating or refining apparatus, where the compressed and dewatered chips are heated to the desired defibrating or refining temperature, usually ranging between 130° C and 200° C, by a portion of the high-temperature high-pressure steam generated by the heat of friction in the grinding space of the defibrator, which portion, upon discharge from the grinding housing, is separated from the pulp and recirculated under increased pressure above the discharge pressure. If the other portion of the discharged atmospheric steam, upon separation from the pulp, should not have sufficient heat content to presteam the raw chips to the desired temperature, fresh pressurized steam may be added to the recirculated portion of the steam to impart to the other portion of the discharged steam the required capacity.
Inventors
- 👤 Karl Cederquist
- 👤 Bernard Marechal
- 👤 Stig Selander
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-25 05:17
CPC Classifications
D; D21; D21B; D21B1/00; D21B1/04; D21B1/12
Claims Analysis
Total Claims: 10
Claim 1
Independent Claim
164 words
In the method of producing pulp for fiberboard and the like, in which raw chips of lignocellulosic material are defibrated in a defibrator in an atmosphere of saturated steam at predetermined defibrating temperatures above 100° C. and corresponding steam pressures, the chips prior to being passed to the inlet side of the defibrator having been presteamed to a predetermined temperature by atmospheric steam released from the mixture of steam and pulp at the outlet side of the defibrator, compressed and dewatered to a dryness of at least 50%, the improvement for minimizing steam consumption, comprising: (a) separating a portion of the high-pressure high-temperature steam from the mixture of steam and pulp discharged at the outlet end of the defibrator; (b) increasing the pressure of said separated portion to impart thereto sufficient heat content to heat the presteamed chips at the inlet side of the defibrator to the predetermined defibrating temperature; and (c) recirculating said pressurized separated portion to the inlet side of the defibrator.
Claim 2
Dependent Claim
164 words
In the method of producing pulp for fiberboard and the like, in which raw chips of lignocellulosic material are defibrated in a defibrator in an atmosphere of saturated steam at predetermined defibrating temperatures above 100° C. and corresponding steam pressures, the chips prior to being passed to the inlet side of the defibrator having been presteamed to a predetermined temperature by atmospheric steam released from the mixture of steam and pulp at the outlet side of the defibrator, compressed and dewatered to a dryness of at least 50%, the improvement for minimizing steam consumption, comprising: (a) separating a portion of the high-pressure high-temperature steam from the mixture of steam and pulp discharged at the outlet end of the defibrator; (b) increasing the pressure of said separated portion to impart thereto sufficient heat content to heat the presteamed chips at the inlet side of the defibrator to the predetermined defibrating temperature; and (c) recirculating said pressurized separated portion to the inlet side of the defibrator.
Claim 3
Dependent Claim
51 words
A method according to claim 1, in which fresh pressurized steam is passed into the recirculated steam in an amount sufficient to impart to the mixture of steam and pulp separated from the recirculated steam, power to provide for its transportation to a cyclone for separation of steam from the pulp.
Claim 4
Dependent Claim
57 words
A method according to claim 1, in which fresh pressurized steam is passed to the circulating steam in an amount such that the heat content of the atmospheric steam released from the mixture of steam and pulp discharged from the defibrator is sufficient to preheat the raw chips to a temperature between 90° C. and 100° C.
Claim 5
Dependent Claim
39 words
A method according to claim 3, in which the amount of fresh pressurized steam passed into the circulating steam is controlled by a temperature indicator, which keeps the temperature of the raw chips preheated with released atmospheric steam constant.
Claim 6
Dependent Claim
167 words
In an apparatus for producing pulp for fiberboard and the like from lignocellulosic material, in which raw chips are defibrated in a defibrator in an atmosphere of steam at predetermined defibrating temperatures above 100° C. and corresponding steam pressures, the chips prior to being passed to the inlet side of the deribrator having been presteamed to a predetermined temperature by atmospheric steam released from the mixture of pulp and steam at the outlet side of the defibrator, compressed and dewatered to a dryness of at least 50%, the improvement comprising: (a) means for separating a portion of the high-pressure high-temperature steam from the mixture of pulp and steam discharged at the outlet side of the defibrator; (b) means for increasing the pressure of said separated steam to impart thereto a heat content sufficient to heat the presteamed chips at the inlet side of the defibrator; and (c) conduit means for recirculating said pressurized separated steam to the inlet side of the defibrator to the predetermined defibrating temperature.
Claim 7
Dependent Claim
167 words
In an apparatus for producing pulp for fiberboard and the like from lignocellulosic material, in which raw chips are defibrated in a defibrator in an atmosphere of steam at predetermined defibrating temperatures above 100° C. and corresponding steam pressures, the chips prior to being passed to the inlet side of the deribrator having been presteamed to a predetermined temperature by atmospheric steam released from the mixture of pulp and steam at the outlet side of the defibrator, compressed and dewatered to a dryness of at least 50%, the improvement comprising: (a) means for separating a portion of the high-pressure high-temperature steam from the mixture of pulp and steam discharged at the outlet side of the defibrator; (b) means for increasing the pressure of said separated steam to impart thereto a heat content sufficient to heat the presteamed chips at the inlet side of the defibrator; and (c) conduit means for recirculating said pressurized separated steam to the inlet side of the defibrator to the predetermined defibrating temperature.
Claim 8
Dependent Claim
57 words
An apparatus as claimed in claim 5, in which the inlet side of the defibrator comprises a preheater for receiving the presteamed chips, and the outlet side comprises a pressure vessel for receiving said portion of high-pressure high-temperature steam, said pressure vessel being connected to said conduit means for recirculating said portion of steam to the preheater.
Claim 9
Dependent Claim
16 words
An apparatus as claimed in claim 6, further comprising a compressor interposed in said conduit means.
Claim 10
Dependent Claim
20 words
An apparatus as claimed in claim 5, including a connection for supply of fresh pressurized steam to said conduit means.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1982-01-29 | 1982-07-31 | 1983-01-30 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1986-01-29 | 1986-07-31 | 1987-01-30 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1990-01-29 | 1990-07-31 | 1991-01-30 | $7700.00 | Window Closed / Lapsed |