US20070227682A1 - Method and a Device for Removing Gas from Wood Chips - Google Patents

Method and a Device for Removing Gas from Wood Chips Download PDF

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Publication number
US20070227682A1
US20070227682A1 US11/568,697 US56869705A US2007227682A1 US 20070227682 A1 US20070227682 A1 US 20070227682A1 US 56869705 A US56869705 A US 56869705A US 2007227682 A1 US2007227682 A1 US 2007227682A1
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United States
Prior art keywords
wood chips
steam
vessel
wood
feeding means
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.)
Abandoned
Application number
US11/568,697
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English (en)
Inventor
Rami Lampinen
Lasse Hernesniemi
Antti Tuominen
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Valmet Technologies Oy
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Metso Paper Oy
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Filing date
Publication date
Priority claimed from FI20040637A external-priority patent/FI20040637A/fi
Application filed by Metso Paper Oy filed Critical Metso Paper Oy
Assigned to METSO PAPER, INC. reassignment METSO PAPER, INC. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: TUOMINEN, ANTTI, LAMPINEN, RAMI, HERNESNIEMI, LASSE
Publication of US20070227682A1 publication Critical patent/US20070227682A1/en
Assigned to VALMET TECHNOLOGIES, INC. reassignment VALMET TECHNOLOGIES, INC. CHANGE OF NAME (SEE DOCUMENT FOR DETAILS). Assignors: METSO PAPER, INC.
Abandoned legal-status Critical Current

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    • 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
    • D21C1/00—Pretreatment of the finely-divided materials before digesting
    • D21C1/02—Pretreatment of the finely-divided materials before digesting with water or steam
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21B—FIBROUS RAW MATERIALS OR THEIR MECHANICAL TREATMENT
    • D21B1/00—Fibrous raw materials or their mechanical treatment
    • D21B1/02—Pretreatment of the raw materials by chemical or physical means

Definitions

  • the invention relates to a method for removing gas from wood chips according to the preamble of the appended claim 1 .
  • the invention also relates to a device for implementing the aforementioned method in accordance with the preamble of the appended claim 12 .
  • the ligno-cellulose-containing wood chips used as raw material are cooked in an alkaline solution in order to separate the fibres and lignin contained in them from each other.
  • the manufacture comprises several stages, both before and after the cooking.
  • the wood chips are directed to the gas removal phase, where gases, primarily air, are removed from both inside the wood chips and the spaces between them by directing hot steam to the wood chips. Removing gas from the spaces between the wood chips decreases the amount of gases disturbing the operation of the digester.
  • the chips absorb cooking chemicals better, which improves the yield of the cooking and the quality of the pulp it provides.
  • Vertical bins or vessels or horizontal screws are generally used for removing gas from wood chips.
  • the screws being used are generally wood chip conveyor screws, which convey wood chips, for example, from chipping to the digester. Generally, this type of screws are installed horizontally or only in a small angle with the horizontal level.
  • the steam needed for removing gas is generally fed from nozzles installed on the lower surface of the shell forming the bottom of the screw.
  • the loading of the screws varies in relation to time, i.e. in relation to the length of the screw, the amount of wood chips moving inside varies, resulting in slow warming of individual wood chips to the maximum temperature and varying their delay in the screw. Consequently, the processing of the wood chips is not uniform.
  • the delay of the wood chips in the screw is not long enough in order for the gas removal to be complete.
  • the wood chips When using vertical bins or vessels in removing gas, the wood chips are generally fed to the bin from its upper end and the steamed wood chips are removed from the lower end of the bin.
  • the steam is generally fed to the lower part of the bin and it flows upwards against the direction of motion of the wood chip material.
  • This kind of a solution for steaming wood chips is disclosed, for example, in the U.S. Pat. No. 4,867,845, where wood chips are fed to a bin with an downward-increasing diameter from the upper end of the bin and the steamed wood chips are removed from the lower end of the bin, by means of a rotating discharger installed at the bottom of the bin.
  • Steam is fed vertically to the centre of the bin, via a steam pipe installed parallel to the vertical central axis of the bin. The end of the steam pipe extending close to the bottom of the bin, from where the steam is discharged to the bin, is formed as an expanding taper. Steam flows upwards from the steam pipe, through the wood chip column packed in the bin
  • US-publication 5,628,873 discloses a downwards-tapered steam bin, where steam is fed to the wood chip flow flowing downward in the chip bin from above the conical narrowing part. Steam feeding takes place both via the shell of the bin and the steam feeding pipes installed within the bin.
  • the purpose of the present invention is therefore to provide a method for removing gas from wood chips, which avoids the above-mentioned problems and in which the gas removal from wood chips takes place in such a manner that all the wood chips receive an identical steam processing.
  • the pulp resulting from the cooking following the gas removal is homogenous.
  • the method according to the invention is primarily characterized in what will be presented in the characterizing part of the independent claim 1 .
  • the device according to the invention is primarily characterized in what will be presented in the characterizing part of the independent claim 12 .
  • the invention is based on the idea that gas removal from wood chips is preformed in a vertical, elongated gas removal vessel, to which the wood chips are fed from the upper part of the vessel and the wood chips are removed from its lower part. Steam is fed to the wood chips to the wood chip flow travelling downwards in the vessel from the middle and edges of the flow, in cross-direction in relation to the wood chip flow.
  • the feed rate of wood chips to the vessel and the discharge rate from it are maintained on a level that the wood chip flow is moving as a so-called plug flow, in which case the wood chips move evenly in relation to the entire cross-section area of the vessel. Therefore, steam is fed into these wood chips in the plug flow.
  • the level of the surface of wood chips in the vessel is controlled by means of the feed rate and discharge rate of the wood chips.
  • the surface of the wood chips is maintained on such a level that the steam fed to the wood chips does not escape directly to the steam space in the upper part of the vessel.
  • the steam feeding means are thus arranged to feed steam to a distance from the surface of the wood chips, inside the wood chip flow.
  • the height of the gas removal vessel and the placement of the steam feeding means in relation to the height of the vessel is arranged in such a manner that the delay time of wood chips in the vessel is long enough for the gas removal to be as efficient as possible.
  • the majority of the steam required in the gas removal from wood chips is fed via the steam feeding pipe arranged in the middle of the wood chip flow and the rest of the steam is fed from around the wood chip flow, via steam feeding means arranged in the shell of the vessel.
  • the temperature of the wood chips in the vessel is raised quickly to approx. 100° C. and maintained there substantially over the entire time the wood chips remain in the vessel.
  • the amount of the steam being fed is controlled by means of the temperature and pressure measurements of the steam gathering in the upper part of the vessel.
  • the steam forming in the gas removal is removed from the upper part of the vessel, from above the surface of the wood chips and the condensate is removed from the lower part of the vessel.
  • An advantage of the gas removal method according to the invention is that as a result of both the design of the gas removal vessel and the transverse steam flow, which does not prevent the flow of the wood chips, an even, downward plug flow of wood chips is created, resulting in each wood chip receiving an equally long and identical steam processing. Consequently, the gas removal within individual wood chips is efficient and fast.
  • the transverse steam flow does not prevent the downward flow of the wood chips either.
  • the quick raising of the temperature of the wood chips to the processing temperature with a transverse steam flow ensures enough delay time for the wood chips in the processing temperature, which improves gas removal significantly.
  • the dimensions of the gas removal vessel and the placement of the steam feeding means in relation to the height of the vessel improve gas removal.
  • the gas removal device used in implementing the method i.e. the gas removal vessel is simple to manufacture and easy to install in its place and it takes little room in the cramped device environments of pulp and paper mills.
  • the invention can also be applied in renewing equipment in factories, which manufacture pulp. Thus, acquiring a completely new gas removal device can be avoided and economical savings can be created.
  • FIG. 1 shows a schematic side view of a device according to the invention
  • FIG. 2 shows a schematic side view of another device according to the invention.
  • FIG. 3 shows a schematic side view of a steam feeding device used in a device according to an embodiment of the invention.
  • FIGS. 1, 2 and 3 the same numerals refer to corresponding parts and they will not be explained separately later on, unless required by the illustration of the subject matter.
  • FIG. 1 shows a device 1 for removing gas from wood chips.
  • the device is placed in a pulp and/or paper factory before the digester where the cooking of pulp takes place.
  • the device comprises is an elongated, by its diameter downwards tapered and advantageously conical vessel 2 installed in the vertical direction.
  • the vessel can be any vessel suitable for the purpose, such as, for example, a bin 2 .
  • the wood chips are fed to the bin 2 by means of a feeding device 3 , from the upper end of the bin.
  • the feeding device 3 is, for example, a rotary vane feeder or a screw.
  • the wood chips can be fed directly to the bin 2 by means of the feeding device or, such as in the advantageous embodiment shown in the figure, the wood chips are fed with the feeding device to a chip packer 4 arranged between the roof 19 closing the upper part of the bin and the feeding device.
  • the chip packer 4 spreads the wood chips as an even layer to the gas removal vessel 2 by means of the steam fed to the chip packer.
  • the steam fed to the packer also increases the temperature of the wood chips before they fall to the bin 2 .
  • the steam fed to the chip packer also melts the wood chips.
  • the amount of steam fed to the chip packer 4 is controlled by the temperature of the wood chips.
  • the operation of the chip packer is obvious to a man skilled in the art, which is why it is not described more in detail here.
  • the wood chips that have gone through the gas removal process are removed from the bin 2 by the discharge means 5 that are connected to the bottom of the bin.
  • the discharge means comprises several pushing means 6 , which move the wood chips to a discharge opening 7 that is centralized with the midpoint of the bottom of the bin 2 .
  • the pushing means 6 are placed substantially evenly over the periphery of the entire shell of the bin 2 defining the bottom of the bin.
  • the power transmission of the discharge means is implemented, for example, hydraulically.
  • the discharge opening is connected to a discharge means arranged under it, i.e. to a screw 8 , by means of which the gas-free wood chips are transferred forward.
  • the wood chips fed to the bin fill the bin 2 substantially evenly to the level of the surface 9 of the wood chips.
  • the surface of the wood chips settles within a distance from the roof 19 of the bin.
  • a free space, i.e. a gas space 13 remains between the surface 9 of the wood chips and the roof of the bin.
  • the level of the surface 9 of the wood chips in the bin is controlled by controlling the feed rate of the wood chip feeding device 3 and/or the discharge rate of the wood chip discharge means 5 and the screw 8 discharging the wood chips from the bin.
  • the discharge rate is controlled according to the production of the digester.
  • one or more sensors 10 measuring the level of the surface of the wood chips are arranged in the bin 2 .
  • the controller 21 controls the rate of the feeding device 3 and/or the discharge means 5 and the screw 8 and at the same time the delay time of the wood chips in the delay zone 25 between the steam feeding means 11 and 12 as well as the discharge means 5 .
  • the surface level of the wood chips is to be the wood chips must be controlled onto such level that the wood chip surface extends all the time above the steam feeding openings of the steam feeding means 11 and 12 feeding steam to the bin. Thus, the steam is prevented from directly escaping to the steam space 13 above the surface of the wood chips.
  • the wood chips move downward in the bin 2 by forming a downward moving wood chip flow, which is described with the arrow A in the figure.
  • the downward movement and the effect of the steam fed to the wood chip flow causes the wood chip flow to become dense, thus forming a so-called plug flow.
  • the downward expanding design of the bin promotes the even movement of the flow in such a manner that no blockages or other obstacles blocking the even flow form in it.
  • the wood chip flow is guided by means of the flow controller 14 arranged in the lower part of the bin, which flow controller evens the chip flow in the bin.
  • the flow controller 14 prevents the wood chips from directly discharging to the discharge opening 7 and thus the blockage of the discharge opening 7 .
  • the first steam feeding means 11 i.e. the steam feeding pipe 11 is arranged in the middle of the bin 2 .
  • the steam feeding pipe 11 thus directs steam to the middle of the bin 2 in such a manner that at least a part of its length combines with the vertical mid-axis of the bin.
  • the end of the steam feeding pipe 11 that extends inside the bin is closed, preventing the steam from flowing into the chip flow directly, in the same direction with it.
  • steam distribution means 15 which can be a perforation extending around the feeding pipe, or some suitable means attached to the feeding pipe, such as, for example, a screen, which distributes steam from the steam feeding pipe 11 evenly to the wood chips horizontally on every side of the pipe.
  • a screen 15 for dividing steam is arranged in the steam feeding pipe.
  • the steam feeding pipe 11 thus feeds steam to the middle of the bin in a cross-direction in relation to the wood chip flow, which steam is marked with arrows in the figure.
  • the second steam feeding means 12 extending around the entire shell of the bin.
  • the second steam feeding means comprising a distribution chamber 12 and a steam distribution means 20 direct steam to the bin in a cross-direction in relation to the wood chip flow.
  • the distribution means 12 is arranged on the outer surface of the bin and it extends around the entire bin shell.
  • the steam distribution means 20 is, for example, a screen and it is arranged on the inner surface of the bin shell, in connection with the distribution chamber and also extends around the bin shell.
  • the cross-directional steam flow enables the quick raising of the temperature of the wood chips to a temperature that is advantageous for gas removal. It has been experimentally established that gas removal from wood chips takes place in approx. 100° C. The wood chips are quickly heated by means of the steam directed to the bin to this temperature and are maintained in this temperature by means of continuous steam feeding.
  • the majority of the steam required in gas removal is fed from the steam feeding pipe 11 .
  • the rest of the steam is fed from the steam feeding means 12 and/or the steam feeding units 17 arranged on the bottom of the discharge means 5 .
  • Controlling the gas removal temperature is done by controlling the amount of steam fed to the bin.
  • the amount of steam is controlled by measuring the temperature prevailing in the delay zone 25 below the second steam feeding means 12 by means of a controller 23 , which sends a control message to the steam feeding means (not shown in the figure).
  • the control message is in the figure referred to with the letter B and dashed lines.
  • the delay time of an individual wood chip piece in the delay zone 25 should be approximately 10 to 30 minutes, advantageously approximately 15 to 25 minutes in order for the gas removal from it to be as complete as possible.
  • the steam feeding means 11 and 12 are placed in relation to the height of the bin 2 in such a manner that below the second steam feeding means 12 , between the steam feeding means 11 and 12 and the wood chip discharge means is formed a so-called delay zone 25 , where an adequate delay time, which is required for gas removal, is guaranteed for the downward flowing wood chips.
  • the delay zone is approximately 2 ⁇ 3 of the height of the vessel 2 .
  • the steam gases can be sucked from only one of the steam feeding means at a time, because feeding enough steam to the wood chip flow and maintaining a high enough temperature in it must be guaranteed throughout the entire gas removal process.
  • the temperature sensor 22 arranged in the gas space 13 above the wood chip surface 9 By means of the temperature sensor 22 arranged in the gas space 13 above the wood chip surface 9 , the temperature of the gas space 13 above the wood chip surface is monitored. If the temperature rises too high, it is a sign of a malfunction of the bin, in which case an alarm is given.
  • the temperature prevailing in the gas space 13 above the wood chip surface is lower than the processing temperature of the wood chips. This is because a part of the steam fed to the wood chips flows upstream in the upper part of the wood chip column towards the surface 9 of the wood chips and displaces the colder gas in the wood chips, which flows upwards to the gas space 13 .
  • the condensate formed in connection with the wood chip gas removal flows to the bottom of the discharge means 5 connected to the lower part of the bin and are removed from there via the condensate removal units 18 .
  • the condensate can also be removed from the screw 8 (not shown in the figure).
  • FIG. 2 shows another embodiment of the gas removal device 1 according to the invention. This embodiment differs from the above-described embodiment of FIG. 1 for the part of the wood chip discharge means. Gas removal from the wood chips takes place in a corresponding manner as is described in connection with FIG. 1 .
  • the downward flowing wood chip flow formed by wood chips is removed from the bin 2 , such as in the embodiment of FIG. 1 , by means of the wood chip discharge means 5 in connection with the bottom of the bin 2 .
  • the screw 8 moves the gas-free wood chips forward. In this embodiment no separate flow controller is required for directing the wood chip flow to the discharge means 5 .
  • FIG. 3 shows an in the bin 2 arranged steam feeding pipe 11 having a closed, downward convergent tapered flow guide 24 attached to the lower surface of a screen provided in the steam feeding pipe.
  • the effect of the flow guide is based on that it prevents the sudden expansion of the free cross-sectional area of the bin after the screen 15 and thus evens the wood chip flow downwards.
  • the gas removal vessel can thus also be of the same diameter in relation to its entire height, a vessel that is round in its cross section.
  • the steam used in gas removal can be used either fresh steam or expansion steam received from another process of the pulp or paper mill.
  • the steam gas received from the gas removal device can be compressed and recycled back as heating steam to the device.

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Paper (AREA)
  • Chemical And Physical Treatments For Wood And The Like (AREA)
US11/568,697 2004-05-05 2005-04-26 Method and a Device for Removing Gas from Wood Chips Abandoned US20070227682A1 (en)

Applications Claiming Priority (5)

Application Number Priority Date Filing Date Title
FI20040637A FI20040637A (fi) 2004-05-05 2004-05-05 Menetelmä ja laite kaasun poistamiseksi paloiksi pilkotusta materiaalista
FI20040637 2004-05-05
FI20055098 2005-02-28
FI20055098A FI123037B (fi) 2004-05-05 2005-02-28 Menetelmä ja laite kaasun poistamiseksi hakkeesta
PCT/FI2005/050133 WO2005106111A1 (en) 2004-05-05 2005-04-26 A method and a device for removing gas from wood chips

Publications (1)

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US20070227682A1 true US20070227682A1 (en) 2007-10-04

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US11/568,697 Abandoned US20070227682A1 (en) 2004-05-05 2005-04-26 Method and a Device for Removing Gas from Wood Chips

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US (1) US20070227682A1 (fi)
AT (1) AT504589B1 (fi)
CA (1) CA2562901C (fi)
FI (1) FI123037B (fi)
SE (1) SE0602327L (fi)
WO (1) WO2005106111A1 (fi)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20130062031A1 (en) * 2011-09-11 2013-03-14 Andrew Kallmes Digester and digestion process
US9115214B2 (en) 2012-09-24 2015-08-25 Abengoa Bioenergy New Technologies, Llc Methods for controlling pretreatment of biomass

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2515518C1 (ru) * 2010-07-09 2014-05-10 Метсо Пейпер Свиден Аб Способ и система пропитки щепы
FI126802B (fi) * 2014-09-12 2017-05-31 Andritz Oy Menetelmä ja hydraulinen vuokeitinjärjestelmä kemiallisen massan tuottamiseksi

Citations (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2901039A (en) * 1954-12-20 1959-08-25 Sven A Salmonson Apparatus for preconditioning chips in a digester
US4135966A (en) * 1974-09-10 1979-01-23 Gloeersen Stig Method and device for equalizing the moisture content of porous material
US4155805A (en) * 1978-01-19 1979-05-22 Kamyr Aktiebolag Method for continuously digesting cellulosic fiber by evenly spreading the fiber material over the digestion vessel with steam
US4592804A (en) * 1983-06-27 1986-06-03 Mo Och Domsjo Ab Method for pre-treating lignocellulosic material in two steaming zones
US4632729A (en) * 1984-05-01 1986-12-30 Laakso Oliver A Chip presteaming and air washing
US4746404A (en) * 1984-05-01 1988-05-24 Laakso Oliver A Chip presteaming and air washing
US4867845A (en) * 1988-06-15 1989-09-19 Kamyr, Inc. Vertical steaming vessel
US5547546A (en) * 1994-10-04 1996-08-20 Ahlstrom Machinery Inc. Chip bin with steaming control and a gas vent containing a vacuum and pressure relief device
US5617975A (en) * 1994-02-01 1997-04-08 Ahlstrom Machinery Inc. Chip feed system
US5635025A (en) * 1994-12-05 1997-06-03 Ahlstrom Machinery Inc. Digester system containing a single vessel serving as all of a chip bin, steaming vessel, and chip chute
US5795438A (en) * 1996-11-04 1998-08-18 Ahlstrom Machinery Inc. Method and apparatus for feeding multiple digesters
US6199299B1 (en) * 1998-04-06 2001-03-13 Andritz-Ahlstrom Inc. Feeding of comminuted fibrous material to a pulping process
US20030047297A1 (en) * 2001-08-30 2003-03-13 Jack T. Baker Apparatus and method for treatment of loose material

Patent Citations (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2901039A (en) * 1954-12-20 1959-08-25 Sven A Salmonson Apparatus for preconditioning chips in a digester
US4135966A (en) * 1974-09-10 1979-01-23 Gloeersen Stig Method and device for equalizing the moisture content of porous material
US4155805A (en) * 1978-01-19 1979-05-22 Kamyr Aktiebolag Method for continuously digesting cellulosic fiber by evenly spreading the fiber material over the digestion vessel with steam
US4592804A (en) * 1983-06-27 1986-06-03 Mo Och Domsjo Ab Method for pre-treating lignocellulosic material in two steaming zones
US4632729A (en) * 1984-05-01 1986-12-30 Laakso Oliver A Chip presteaming and air washing
US4746404A (en) * 1984-05-01 1988-05-24 Laakso Oliver A Chip presteaming and air washing
US4867845A (en) * 1988-06-15 1989-09-19 Kamyr, Inc. Vertical steaming vessel
US5617975A (en) * 1994-02-01 1997-04-08 Ahlstrom Machinery Inc. Chip feed system
US5628873A (en) * 1994-02-01 1997-05-13 Ahlstrom Machinery Inc. Chip bin assembly including a hollow transition with one dimensional convergence and side relief
US5547546A (en) * 1994-10-04 1996-08-20 Ahlstrom Machinery Inc. Chip bin with steaming control and a gas vent containing a vacuum and pressure relief device
US5635025A (en) * 1994-12-05 1997-06-03 Ahlstrom Machinery Inc. Digester system containing a single vessel serving as all of a chip bin, steaming vessel, and chip chute
US5795438A (en) * 1996-11-04 1998-08-18 Ahlstrom Machinery Inc. Method and apparatus for feeding multiple digesters
US6199299B1 (en) * 1998-04-06 2001-03-13 Andritz-Ahlstrom Inc. Feeding of comminuted fibrous material to a pulping process
US20030047297A1 (en) * 2001-08-30 2003-03-13 Jack T. Baker Apparatus and method for treatment of loose material

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20130062031A1 (en) * 2011-09-11 2013-03-14 Andrew Kallmes Digester and digestion process
US9115214B2 (en) 2012-09-24 2015-08-25 Abengoa Bioenergy New Technologies, Llc Methods for controlling pretreatment of biomass

Also Published As

Publication number Publication date
CA2562901A1 (en) 2005-11-10
WO2005106111A1 (en) 2005-11-10
SE0602327L (sv) 2006-11-03
AT504589B1 (de) 2010-06-15
FI20055098A0 (fi) 2005-02-28
FI20055098A (fi) 2005-11-06
AT504589A1 (de) 2008-06-15
CA2562901C (en) 2013-02-26
FI123037B (fi) 2012-10-15

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Owner name: METSO PAPER, INC., FINLAND

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STCB Information on status: application discontinuation

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