The invention relates to a machine for the manufacture of a material web, in particular a paper or card web, having a forming zone including at least one circulating, endless, dewatering belt.
The invention is based on the object of further optimizing the machine of the initially named kind, in particular with respect to the dry content and/or paper quality obtained after the pressing.
This object is satisfied in accordance with the invention in that the machine includes at least one pressing zone combined with a suction system.
As a result of this design an additional gain in dry content and/or paper quality is achieved after the pressing.
In a preferred practical embodiment the machine includes a former with two circulating dewatering belts which converge while forming a material web gap and which are subsequently guided as an inner belt and an outer belt respectively over a forming element, such as in particular a forming roll.
The pressing zone combined with a suction system is expediently provided in the web running direction in front of a nip formed between a dryer cylinder, preferably a Yankee cylinder, and a counter element.
For the formation of the pressing zone combined with a suction system an element to which suction can be applied is preferably provided. In this arrangement this element to which suction can be applied can, for example, include a suction roll or the like.
In a preferred practical embodiment of the machine of the invention the fiber material web is led together with the inner belt to the pressing zone.
A further dewatering belt can be guided around the element to which suction can be applied in addition to the inner belt which is supported on the latter, with the fiber material web lying between the inner belt and the further dewatering belt.
In accordance with an expedient practical embodiment a belt arranged within the loop of the further dewatering belt is tensioned around the element to which suction can be applied.
The further dewatering belt which is led around the element to which suction can be applied can be formed by a conventional, in particular non-structured screen or by a structured screen.
In an advantageous practical embodiment the further dewatering element which is led around the element to which suction can be applied is formed by a TAD screen (TAD=Through-Air-Drying).
In addition, the further dewatering belt which is led around the element to which suction can be applied can in particular also be formed by a dewatering screen with differing screen permeability zone-wise, such as in particular a so-called DSP screen etc.
Screens with differing permeability zone-wise are for example known from SE 427053. In accordance with this, the relevant screens can, for example, consist of a fabric in which longitudinal threads and transverse threads provided in one plane or in a plurality of planes are interwoven in accordance with a pre-determinable pattern, so that systematically distributed zones of suitable size result in which the number of crossing points is equal to zero or are significantly smaller than in the woven structure of the remaining fabric.
Screens of the type which are described in PCT/GB99/02684 can, for example, also be considered as screens having differing permeability zone-wise. In accordance with this, the relevant screen can in particular consist of a fabric in which threads extending in a first direction in one plane or in a plurality of planes are so interwoven with threads extending in the second direction that a grid results which separates a plurality of systematically distributed zones of pre-determinable configuration from one another and correspondingly determines them, with the systematically distributed zones including at least three threads extending in the one direction and at least three threads extending in the other direction. The threads can in particular be weft threads and warp threads.
The tension of the belt tensioned around the element to which suction can be applied and which is arranged within the loop of the further dewatering belt can in particular be larger than or equal to 60 kN/m.
The belt which is tensioned around the element to which suction can be applied and arranged within the loop of the further dewatering belt can have a smooth surface or also a drilled and/or grooved surface or any kind of porosity shape or pattern.
The pressing zone combined with a suction system can form a longitudinal gap or also a normal gap.
In a preferred practical embodiment of the machine in accordance with the invention, the element to which suction can be applied is simultaneously provided as the counter-element which forms the nip together with the dryer cylinder or the Yankee cylinder.
The outer belt can in particular be formed by a dewatering screen. A crescent former can, for example, be provided as the former, with the outer belt of the crescent former being formed by a dewatering screen and its inner belt by a felt.
The dry content of the fiber material web in front of the pressing zone preferably lies in a range from about 8% to about 15% and after the pressing zone in a range of about 40% or higher.
A suction box can be provided between the forming element and the pressing zone. In this arrangement the dry content of the fiber material web directly after the suction box and before the pressing zone can in particular lie in a range of about 23%.
The fiber material web can be fed to the dryer cylinder or the Yankee cylinder with an open nip or with a closed nip.
In an expedient practical embodiment a guide roll for the inner belt which guides the fiber material web with it, in particular an adjustable and/or movable guide roll, is provided in the web running direction after the nip.
The tension of the further dewatering belt expediently amounts to about 5 kN/m.
The tension of the outer belt amounts to about 8 kN/m.
The tension of the inner belt can, for example, amount to about 5 kN/m.
In accordance with a further expedient practical embodiment of the machine of the invention, a double screen former is provided as the former.
A further element to which suction can be applied can be provided within the loop of the further dewatering belt.
This further element to which suction can be applied is preferably only wrapped around by the further dewatering belt.
The further element to which suction can be applied can, for example, be formed by a suction roll or by a suction box.
In an expedient practical embodiment of the machine of the invention the fiber material web can be supplied to the dryer cylinder or to the Yankee cylinder by closing of the nip.
In a further expedient practical embodiment of the machine of the invention both the inner belt and also the further dewatering belt is respectively formed by a felt.
A further advantageous embodiment of the machine of the invention is characterized in that a roll lies opposite to the element to which suction can be applied within the loop of the further dewatering belt. This roll can have a closed surface or can also be grooved and/or blind-drilled.
The roll provided within the loop of the further dewatering belt can in particular be formed by a rigid roll.
Embodiments in which a shoe pressing unit lies opposite to the element to which suction can be applied within the loop of the further dewatering belt are, however, fundamentally also conceivable. A shoe pressing unit of this kind can, for example, include a shoe pressing roll or the like.
In accordance with a further practical embodiment of the machine of the invention a double screen former is provided as the former and the further dewatering belt is formed by a felt.
The invention will be explained in the following with reference to embodiments and to the drawings in which are shown:
The formers 10 shown in FIGS. 1 to 5 are each part of a machine for the manufacture of a fiber material web which can in particular be a paper web or a card web. In this connection at least one pressing zone 14 combined with a suction system is provided in each case.
Whereas the pressing zone 14 combined with a suction system is formed in each of the embodiments shown in FIGS. 1 to 3 by a belt press, a molding press is provided in each of the embodiments of
In accordance with
The fiber material suspension is introduced into the material inlet gap 20 by means of a headbox 22.
The pressing zone 14 combined with a suction system is provided in the web running direction L in front of a nip 30 formed between a dryer cylinder 26, preferably a Yankee cylinder, and a counter element 28.
For the formation of the pressing zone 14 combined with a suction system an element 32 to which suction can be applied is provided which, in the present case, is for example a suction roll.
The fiber material web 12 is supplied together with the inner belt 16 which wraps around the forming roll 22 to the pressing zone 14. In this arrangement a further dewatering belt 34 is led around the element 32 to which suction can be applied in addition to the inner belt 16 which is directly supported on it. The fiber material web 12 lies here between the inner belt 16 and the further dewatering belt 34.
In the present embodiment of
Thus, the further dewatering belt 34 led around the element 32 to which suction can be applied can, for example, be formed by a TAD screen (TAD=Through-Air-Drying) or, for example, by a dewatering screen with differing screen permeability zone-wise, such as in particular a so-called DSP screen.
Screens of the type which are described in PCT/G99/02684 can, for example, be considered as screens with permeability which differs zone-wise. In accordance with therewith, the relevant screens can, in particular, consist of a fabric in which threads extending in a first direction in one plane or in a plurality of planes are interwoven with threads extending in a second direction such that a grid results which separates a plurality of systematically distributed zones of pre-determinable configuration from one another and correspondingly determines them, with the systematically distributed zones each including at least three threads extending in the one direction and at least three threads extending in the other direction. The threads can, in particular, be weft threads and warp threads.
The tension of the belt 36 tensioned around the element 32 to which suction can be applied and arranged within the loop of the further dewatering belt 34 is expediently larger than or equal to 60 kN/m.
The belt 36 tensioned around the element to which suction can be applied and arranged within the loop of the further dewatering belt 34 can have a smooth or closed surface or also a drilled and/or grooved surface.
In the present embodiment in accordance with
As can be recognized with respect to
The outer belt 18 which wraps around the forming roll 22 is formed by a dewatering screen, with the former 10 being provided in the present case as a crescent former of which the outer belt 18 is formed by the dewatering screen and the inner belt 16 is formed by a felt.
The dry content of the fiber material web 12 in front of the pressing zone 14 preferably lies in a range from about 8% to about 15% and after the pressing zone 14 in a range of about 40% or higher.
A suction box 38 can be provided between the forming element 22 and the pressing zone 14. In this connection, the dry content of the fiber material web 12 directly after the suction box 38 and before the pressing zone 14 preferably lies in a range of about 23%.
Depending on whether a higher priority is associated with the quality or with the productivity, the fiber material web 12 can be supplied to the dryer cylinder or to the Yankee cylinder 26 with an open nip or closed nip 30. As can be seen with respect to
The tension of the further dewatering belt 34 can in particular amount to about 5 kN/m. The tension of the outer belt 18 amounts preferably to about 8 kN/m. The tension of the inner belt 16 can in particular amount to about 5 kN/m.
In the present embodiment of
So far as necessary, a suction box 38 can also be used which helps the press to dry the inner belt 16 formed by the felt and the fiber material web 12 in order to provide additional space within the felt and thus to absorb more water from the structure of the fiber material web 12. In this case the dry content of the fiber material web 12 directly after the suction box 38 and in front of the pressing zone 14 preferably lies in a range of about 23%.
The belt press provided here operates as follows:
The fiber material web 12 is basically enclosed in sandwich-like manner between a further dewatering belt 34 formed in particular by a screen and the inner belt 16 which is directly supported on the surface of the element to which suction can be applied, or on the suction roll which supports the inner belt 16. In this arrangement the further dewatering belt 34 can be a conventional, in particular non-structured screen or also a structured screen. Thus, by way of example, as already mentioned, a TAD screen, a dewatering screen with differing screen permeability zone-wise, such as in particular a so-called DSP screen or the like can be provided.
Within the loop of the further dewatering belt 34 a belt 36 (fabric or belt) is arranged which is tensioned at a high tension of preferably about 60 kN/m or more and which thus generates a distributed load over the element 32 to which suction can be applied, which is, for example, formed here by a suction roll. The strongly tensioned belt 36, which is, for example, a fabric belt or can be another belt (fabric or belt), can have a smooth or closed surface or also a drilled and/or grooved surface. As a result of the specific extension of the pressing zone 14 the maximum pressing pressure and a specific pressure within this pressing zone 14 which is extended in the web running direction L is very low, i.e. approximately 40 times lower than in a customary suction press, so that paper of high quality is produced having regard to the so-called bulk or volume.
For the transfer of the fiber material web 12 onto the surface of the dryer cylinder or Yankee cylinder 26 there are fundamentally two basic possibilities: If quality stands at the forefront, then the nip 30 formed between the element 32 to which suction can be applied, and which is preferably formed here by a suction roll, and the dryer cylinder or Yankee cylinder 26 can remain open. The fiber material web 12 is only transferred in that attention is paid to a specific wrapping angle of the inner belt formed here by a felt around the dryer cylinder or Yankee cylinder 26. In this arrangement one can proceed in such a way that the guide roll 40 for the inner belt 16 is correspondingly moved or adjusted directly after the drier cylinder or the Yankee cylinder. If, in contrast, productivity stands in the forefront, then the nip 30 is closed and in this case the fiber material web 12 is dried to a much greater degree in conjunction with an increase of the production.
A further advantage of this arrangement lies in the fact that a pressing zone 14 is provided which is combined with a suction system. In the event of a shoe pressing unit is associated with the drier cylinder or Yankee cylinder 26 only pressure is generated. With a suction roll associated with the dryer cylinder or the Yankee cylinder 26 the surface of the dryer cylinder or Yankee cylinder 26 does not permit any air flow through the nip 30 despite the presence of vacuum.
This is the only press which simultaneously enables an air flow through the nip 30 during pressing. As a consequence, one obtains after the press an additional gain in dry content.
As indicated at “42” the suction in the region of the element 32 can in particular take place at least substantially over the entire machine width.
In the embodiment of
One can in particular term the suction box 38 here also as a “wet shaping box”. It removes some water from the paper and simultaneously produces cushions on the sheet structure. In this case the dry content of the paper lies directly after the wet shaping box and prior to the pressing step preferably at about 20%. After the press a dry content of about 40% is expected.
The furter dewatering belt 34 is formed in the present case by a felt, the tension of which expediently amounts again to about 5 kN/m.
Within the loop of the further dewatering belt 34 or felt a further element 44 to which suction can be applied is provided for the drying of the further dewatering belt or felt 34. As can be seen with reference to
In the present case, the transfer of the fiber material web 12 to the dryer cylinder or Yankee cylinder 26 takes place simply by closing of the nip 30. In this case the sheet structure is not destroyed since the pressing takes place using a dewatering belt or screen (wire) through which only a part of the sheet is pressed.
In other respects, this embodiment in accordance with
In the embodiment of
In the present case not only the inner belt 16, but also the further dewatering belt 34 is formed by a felt. In the region of the pressing zone 14 combined with a suction system the fiber material web 12 thus lies in sandwich-like manner between two felts.
An adjustable guide roll 40 for the inner belt 16 can in particular also be provided again.
In other respects, this embodiment in accordance with
In the embodiment of
As can be seen with respect to
As a result of the further dewatering belt or screen 34 in the pressing zone 14 the sheet surface is not fully pressed whereby paper of high quality is obtained.
In other respects this embodiment in accordance with
In the embodiment of
Within the loop of the dewatering belt 34 or felt a further element 44 to which suction can be applied can be provided for the drying of the dewatering belt or felt 34. As can be seen with reference to
In other respects the present embodiment of
In
In other respects, the present embodiment of
In
In other respects, the present embodiment of
Number | Date | Country | Kind |
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03021859.8 | Sep 2003 | EP | regional |
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/EP04/52224 | 9/17/2004 | WO | 12/7/2006 |