Outlet system for transporting comminuted lignocellulosic material from a vessel and vessel comprising such an outlet system
11371185 · 2022-06-28
Assignee
Inventors
- Roger Jansson (Karlstad, SE)
- Jonas Saetheråsen (Hammarö, SE)
- Jerk Söderman (Karlstad, SE)
- Magnus Wilhelmsson (Skoghall, SE)
Cpc classification
B65D88/28
PERFORMING OPERATIONS; TRANSPORTING
International classification
B65D88/28
PERFORMING OPERATIONS; TRANSPORTING
Abstract
The present invention relates to an outlet system for transporting comminuted lignocellulosic material from a vessel, said bottom portion (1) having an upper circumference (15) that is essentially circular and a lower circumference (16) comprising at least two essentially straight portions (16a, 16c) opposite each other. The invention also relates to a vessel having such an outlet system.
Claims
1. An outlet system for transporting comminuted lignocellulosic material from a vessel, said outlet system comprising a bottom portion arranged in or at a bottom of the vessel, said bottom portion having an upper perimeter that is essentially circular and a lower perimeter comprising at least two essentially straight portions opposite each other, and wherein each of the essentially straight portions forms a base for a wedge-shaped surface on a lateral surface of the bottom portion, said wedge-shaped surface being planar and extending upwards to an upper wedge end at the upper perimeter, the outlet system further comprising a chip transfer arrangement that is joined to the lower perimeter and comprises sides that correspond to sides of the lower perimeter, the outlet system comprising an outlet unit that is joined to the chip transfer arrangement and that comprises an outlet that is configured to be connected via a connection portion of the outlet unit to a pump, wherein the outlet unit further has a circular cross-section, and the outlet system further comprising the pump that is connected to the outlet of the outlet system, wherein the pump includes a centrifugal pump, and wherein the lower perimeter is essentially rectangular in shape, comprising four essentially straight portions.
2. The outlet system according to claim 1, wherein said upper wedge end of at least one of the wedge-shaped surfaces is offset in a circumferential direction from a middle point on the base of the wedge-shaped surface.
3. The outlet system according to claim 1, wherein the wedge-shaped surfaces are at a first angle with respect to a plane that coincides with the essentially circular upper perimeter of the bottom portion, said first angle being equal to or less than 120 degrees.
4. The outlet system according to claim 1, wherein the lateral surface of the bottom portion comprises at least four wedge-shaped surfaces, each having one of the essentially straight portions as its base.
5. The outlet system according to claim 1, wherein the outlet unit comprises a conduit that connects the outlet to the outlet unit.
6. The outlet system according to claim 1, further comprising at least one nozzle arranged to supply a fluid into the outlet unit.
7. The outlet system according to claim 1, wherein the connection portion of the outlet unit extends in a first direction, the first direction making an angle with respect to a horizontal direction of +15° to −45°.
8. A vessel for treatment of comminuted lignocellulosic material, the vessel comprising an outlet system according to claim 1.
9. A method for modifying a vessel for treatment of comminuted lignocellulosic material, the method comprising removing a bottom portion from a vessel and connecting an outlet system according to claim 1 to the vessel.
10. The outlet system according to claim 3, wherein said first angle is less than 115 degrees.
11. The outlet system according to claim 7, wherein the first direction makes an angle with respect to a horizontal direction of +5° to −20°.
Description
DRAWINGS
(1) The invention will now be described in more detail with reference to the appended drawings, wherein
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DETAILED DESCRIPTION
(14) The present invention relates generally to an outlet system for feeding comminuted cellulosic fibrous material from a first vessel to a second vessel by means of at least one pump. The comminuted cellulosic fibrous material is typically wood chips, which can have been diluted with liquid, e.g. water, or which are diluted with liquid, e.g. water, in the outlet system itself, e.g. in the first vessel or in a chip chute connected to the first vessel, but the outlet system can be applied also for other types of cellulosic materials. The first vessel can be a vessel for pretreatment of the wood chips (or other cellulosic materials), such as a steaming vessel or a chip bin, while the second vessel can be a continuous digester, a batch digester, an impregnation vessel or a hydrolysis or prehydrolysis vessel, but also other types of vessels with other purposes are conceivable. (The second vessel is, however, not part of an outlet system according to the invention and also does not interact directly with the outlet system.) Generally, at least one pump is arranged below the first vessel, and the comminuted cellulosic material is transported from the first vessel to the pump, either via a connection directly from an outlet provided in or at a bottom portion of the first vessel or via a chip chute. In some cases, there is, however, a need for arranging other devices between the first vessel and the pump. One example of such devices is a metering device, which measures the material or media flow from the first vessel. Another example of such a device is a portion of an existing chip chute which has previously been used in connection with, for example, a high-pressure feeder. As stated below, herein, all such devices or arrangements can be referred to as a “chip transfer arrangement”. Such a chip transfer arrangement is suitable for connecting to an outlet system according to the present invention, but may in some embodiments form part of the outlet system as set out in more detail below. Below, the first vessel is referred to simply as a vessel, since a second vessel does not form part with or interact directly with the present invention.
(15) As used herein, the term “chip transfer arrangement” thus includes all equipment, devices and arrangements which are arranged between a vessel and a pump and to which a bottom portion of the vessel connects. Examples of such equipment, devices and arrangements are a metering device or simply an outlet provided in the bottom portion of the vessel; or a “chip transfer arrangement” can be an existing rectangular chip chute or a portion of a previously arranged rectangular chip chute. Further, it should be understood that an outlet system for feeding comminuted cellulosic materials can be used for feeding of comminuted cellulosic materials that have been diluted with liquid. Such dilution can have taken place before the cellulosic material enters the outlet system of the invention, or the dilution can be done within the outlet system, e.g. in the vessel or in the chip chute. Thus, the term “comminuted cellulosic material” includes comminuted cellulosic material that has been diluted with liquid.
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(17) The vessel itself may have a conventional design and structure that is already well known within the art. It is therefore to be understood that the bottom portion 1 forms the vessel together with at least an upper portion and that the bottom portion 1 may be joined to said upper portion (or to a middle portion that in turn is connected to the upper portion), or alternatively that the bottom portion 1 forms an integrated part of the vessel.
(18) The bottom portion 1 has an upper circumference 15 that preferably has an essentially circular cross-section and a lower circumference 16 that comprises at least two essentially straight portions 16a that are opposite each other, i.e. that are essentially parallel to each other and do not coincide. In the preferred embodiment, the lower circumference 16 comprises four straight portions 16a, 16b, 16c, 16d that form two pairs of straight portions that are opposite each other so that the four straight portions 16a, 16b, 16c, 16d form a rectangle. This can also be seen as the bottom portion 1 having a rectangular shape at the lower circumference. The lower circumference 16 and the upper circumference 15 are connected by a lateral surface 10. Each of the straight portions 16a, 16b, 16c, 16d form a base for a wedge-shaped surface 11, 12, 13, 14 that is planar and extends from the lower circumference 16 towards the upper circumference 15 where each wedge-shaped surface 11, 12, 13, 14 ends in an upper wedge end 11a, 12a, 13a, 14a. The lateral surface 10 is as already mentioned essentially circular at the upper circumference 15 and tapers towards the lower circumference 16 so that a cross-sectional area of the lower circumference 16 is smaller than a cross-sectional area of the upper circumference 15. In the preferred embodiment the lateral surface 10 is essentially cone shaped in those portions that do not form part of any of the wedge-shaped surfaces 11, 12, 13, 14, such portions in the following being referred to as rounded portions.
(19) Each of the wedge-shaped surfaces 11, 12, 13, 14 is connected on either side along a connection curve 11′, 12′, 13′, 14′ to a rounded surface and the connection curve 11′ 12′, 13′, 14′ can be in the form of a straight line but can alternatively have another shape that connects the base 16a, 16b, 16c, 16d and the upper wedge end 11a, 12a, 13a, 14a.
(20) The arrangement of wedge-shaped surfaces 11, 12, 13, 14 on the lateral surface 10 of the bottom portion 1 improves a transport of chip slurry from the vessel towards the bottom circumference 16 of the bottom portion 1, especially since the connection curves 11′, 12′, 13′, 14′ assist in providing a uniform output of chip slurry and prevent creation of areas in the vessel where chip slurry remains so that pockets of remaining chip slurry are formed.
(21) The wedge-shaped surfaces 11, 12, 13, 14 extend at a first angle α with respect to a plane P that coincides with the cross-section of the upper circumference 15, as shown in
(22) The chip transfer arrangement 2 is joined to the lower circumference 16 and comprises sides 21, 22, 23, 24 that correspond to sides of the lower circumference 16 where bases for the wedge-shaped surfaces 11, 12, 13, 14 are formed. Inside the chip transfer arrangement 2 means may be provided for feeding the chip slurry towards the outlet unit 3, or alternatively the chip transfer arrangement 2 may be only a chute that connects the bottom portion 1 to the outlet unit 3.
(23) The outlet unit 3 comprises a connection portion 31 that is joined to a lower end of the chip transfer arrangement 2 and an outlet 32 that is connectable to a pump. The outlet 32 in this embodiment has an essentially circular cross-section in order to connect to a pump having an inlet of the same shape, but it is possible for other types of pumps to provide the outlet 32 with another shape.
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(30) The arrangement of the pump 6 shown in
(31) The outlet system of the present invention has the advantage that only one pump 6 is needed to transport the material to a subsequent vessel. The need for a plurality of pumps arranged in series can therefore be avoided.
(32) In another alternative embodiment the bottom portion 1 can have an asymmetrical cross-section between the upper and the lower circumference 15, 16 that is particularly efficient in transporting chip slurry from the vessel. Such asymmetrical cross-section is preferably realized through an upper wedge end of at least one of the wedge-shaped surfaces being offset in a circumferential direction from a middle point on the base of that wedge-shaped surface. In some embodiments, more than one of the wedge-shaped surfaces can have an upper wedge end that is offset in relation to the base, enabling a design of the lateral surface 10 that is asymmetrical and adapted for a particular application to provide an optimal output of chip slurry from the vessel.
(33) As mentioned above, additional fluid may be added in the chip transfer arrangement 2 or in the outlet unit 3 in order to support the flow of material or to adjust the fluid content in the material. In some embodiments, fluid may be supplied through at least one fluid nozzle provided in the outlet unit 3. This has the particular advantage that clogging of material in the outlet unit 3 or blockage in the outlet unit 3 and the conduit 33 can be dissolved by adding fluid, or alternatively can be avoided completely by constantly adjusting the fluid content to keep a flow of material steady. In one embodiment, the connection portion 31 of the outlet unit 3 may instead protrude in the outlet system in a direction that is +15° to −45° in relation to a horizontal direction, preferably +5° to −20° to a horizontal direction. This means that the feeding of lignocellulosic material in the outlet system towards the outlet 32 may take place in a direction that varies from an upward angle of 15° from a horizontal axis to a downward angle of 45° from the horizontal axis, or preferably from an angle upwards of 5° to a downward angle of 20°. It is preferable to provide the connecting portion 31 extending within the smaller interval of +5° to −20° but the advantage may to some extent also be achieved within the larger interval.
(34) The outlet system 100 of the present invention can advantageously be mounted on a vessel for treatment of lignocellulosic material, such as an impregnation vessel. The method of mounting the outlet system 100 comprises removing a bottom portion of a vessel and mounting an outlet system 100 on the vessel so that the bottom portion 1 of the outlet system 100 forms the bottom portion 1 of the vessel. Thereby, an existing vessel is modified so that the feeding of chip slurry towards the outlet is significantly improved and so that a pump can be connected instead of a rotary pocket feeder. The need for replacing the entire vessel is thereby eliminated and at the same time the above mentioned advantages are achieved, also providing a cost efficient improvement of an existing treatment vessel.
(35) The outlet system according to the present invention is especially advantageous when the vessel in connection with which it is arranged serves to perform both steaming and impregnating of the lignocellulosic material, since the material is in such cases in the form of a fluid when being discharged through the outlet system. The outlet system is especially suited to transporting such fluid lignocellulosic material or slurry to be pumped.
(36) It is to be noted that features from the various embodiments described herein may freely be combined, unless it is explicitly stated that such a combination would be unsuitable. In particular, when one feature of an embodiment has been stated as differing from other embodiments described above, it follows that other features of that embodiment may be similar to those of the other embodiments.