SYSTEM AND METHOD FOR CONTROLLING PROCESS FLUIDS IN A PLANT FOR MANUFACTURING WEB-LIKE PAPER MATERIAL
20230295872 · 2023-09-21
Inventors
Cpc classification
International classification
Abstract
Herein described is a plant (10) for manufacturing web-like paper material which comprises a system for controlling process fluids. The plant (10) comprises a first wet half-hood (14), a second dry half-hood (16) and four unidirectional flow regulating devices (28, 30; 34, 40) which, suitably positioned on the return circuits (22; 24) of the mist from both half-hoods (14; 16), allow the parallel operation of such half-hoods (14; 16). A fifth bidirectional flow regulating device (40) allows to selectively operate the half-hoods (14; 16) both in reverse cascade mode, that is releasing the mist coming from the first wet half-hood (14) on the return circuit (24) of the second dry half-hood (16), and then release all the mist coming from both the half-hoods (14; 16), and in direct cascade mode, that is releasing the mist coming from the second dry half-hood (16) into the return circuit (22) of the first wet half-hood (14), to release all the mist coming from both half-hoods (14; 16) into the atmosphere once again.
Claims
1. A plant (10) for manufacturing a web-like paper material starting from a slurry of paper material to be desiccated, the plant (10) comprising: a first drying device comprising at least one rotating Yankee cylinder (12), fed by pressurized steam, wherein said slurry of paper material dynamically adheres to the lateral surface of said Yankee cylinder (12); a second drying device comprising at least one hood (14, 16) which at least partially surrounds said Yankee cylinder (12), wherein said hood (14, 16) consists of a first half-hood (14) and at least one second half-hood (16) which are both capable of blowing high temperature dry air onto said slurry of paper material wound on the lateral surface of said Yankee cylinder (12), and of suctioning the hot and moist fumes, released by said slurry of paper material, wherein said first half-hood (14) is a wet half-hood arranged at the inlet side of said slurry of paper material on said Yankee cylinder (12), and wherein said second half-hood (16) is a dry half-hood arranged at the outlet side of said slurry of paper material from said Yankee cylinder (12); at least one first delivery circuit (18) for feeding said high temperature air to said first half-hood (14); at least one second delivery circuit (20) for feeding said high temperature air to said second half-hood (16); at least one first return circuit (22) for suctioning said fumes from said first half-hood (14); at least one second return circuit (24) for suctioning said fumes from said second half-hood (16); a first interface duct (26) for a fluid connection between said first return circuit (22) and said second return circuit (24), wherein along said first interface duct (26) there are installed a first flow regulating device (28), which is designed to allow the fluid to flow unidirectionally from said first interface duct (26) to said first return circuit (22), and a second flow regulating device (30), which is designed to allow the fluid to flow unidirectionally from said first interface duct (26) to said second return circuit (24); and a second interface duct (32) for a fluid connection between said first return circuit (22) and said second return circuit (24), wherein said second interface duct (32) is arranged upstream of said first interface duct (26) and wherein along said second interface duct (32) there are installed a third flow regulating device (34), which is designed to allow the fluid to flow unidirectionally from said first return circuit (22) to said second interface duct (32), and a fourth flow regulating device (36), which is designed to allow the fluid to flow unidirectionally from said second return circuit (24) to said second interface duct (32), the plant (10) being characterized in that between said first return circuit (22) and said second return circuit (24) there is interposed at least one third interface duct (38), which is independent from said first interface duct (26) and from said second interface duct (32), wherein along said third interface duct (38) there is installed at least one fifth flow regulating device (40), which is designed to allow the fluid to flow bidirectionally between said first return circuit (22) and said second return circuit (24) through said third interface duct (38).
2. The plant (10) according to claim 1, characterized in that it comprises at least one air supply duct (42), which is placed in fluid connection with said first interface duct (26) and which is designed to supply air, coming from the environment outside the plant (10), to said first (28) and second (30) flow regulating device.
3. The plant (10) according to claim 1, characterized in that it comprises at least one exhaust pipe (44), which is placed in fluid connection with said second interface duct (32) and which is designed to discharge at least one part of the fumes which flow through said second interface duct (32).
4. The plant (10) according to claim 2, characterized in that it comprises at least one first delivery duct (46), which is placed in fluid connection with said first delivery circuit (18) and with said first return circuit (22) and which is designed to send to said first delivery duct (18) at least one part of the fumes which flow through said first return circuit (22) and at least one part of the air coming from said at least one air supply duct (42).
5. The plant (10) according to claim 4, characterized in that: between said first return circuit (22) and said first delivery duct (46) there is interposed at least one first fan (50), which is designed to transfer to said first delivery duct (46) the air and/or fumes coming from said first return circuit (22); and between said first delivery duct (46) and said first delivery circuit (18) there is interposed at least one first heat generator (52), which is designed to heat both the air and fumes coming from said first delivery duct (46), and further air coming from the environment outside the plant (10) through a further air supply duct (58) which is placed in fluid connection with said first heat generator (52).
6. The plant (10) according to claim 2, characterized in that it comprises at least one second delivery duct (48), which is placed in fluid connection with said second delivery circuit (20) and with said second return circuit (24) and which is designed to send to said second delivery duct (20) at least one part of the fumes which flow through said second return circuit (24) and at least one part of the air coming from the air supply duct (42).
7. The plant (10) according to claim 6, characterized in that: between said second return circuit (24) and said second delivery duct (48) there is interposed at least one second fan (54), which is designed to transfer to said second delivery duct (48) the air and/or fumes coming from said second return circuit (24); and between said second delivery duct (48) and said second delivery circuit (20) there is interposed at least one second heat generator (56), which is designed to heat and dry both the air and fumes coming from said second delivery duct (48), and further air coming from the environment outside the plant (10) through a further air supply duct (60) which is placed in fluid connection with said second heat generator (56).
8. The plant (10) according to claim 1, characterized in that at least one of said first (28), second (30), third (34), fourth (36) and fifth (40) flow regulating device consists of a sealed regulating valve.
9. The plant (10) according to claim 1, characterized in that at least one of said first (52) and second (56) heat generator consists of a burner.
10. A method for controlling process fluids in a plant (10) for manufacturing a web-like paper material according to claim 1, the method selectively comprising the steps of: keeping said first (28), second (30), third (34) and fourth (36) flow regulating device at least partially open and keeping said fifth flow regulating device (40) closed, so that said first half-hood (14) and said second half-hood (16) operate simultaneously, without fluid exchange between said first return circuit (22) and said second return circuit (24); or keeping said first (28), fourth (36) and fifth (40) flow regulating device at least partially open and keeping said second (30) and third (34) flow regulating device closed, so that there is allowed the unidirectional fluid exchange between said second return circuit (24) and said first return circuit (22), so that the fumes coming from said second half-hood (16) are sent to said first half-hood (14); or keeping said second (30), third (34) and fifth (40) flow regulating device at least partially open and keeping said first (28) and fourth (36) flow regulating device closed, so that there is allowed the unidirectional fluid exchange between said first return circuit (22) and said second return circuit (24), so that the fumes coming from said first half-hood (14) are sent to said second half-hood (16).
Description
BRIEF DESCRIPTION OF THE DRAWING
[0015] The features and advantages of a system and a method for controlling process fluids in a plant for manufacturing web-like paper material according to the present invention will be more apparent from the following exemplifying and non-limiting description, with reference to the attached drawings in which the only FIGURE is a schematic view which shows both a part of the drying and desiccating equipment and a preferred embodiment of a system according to the present invention for controlling process fluids in a plant for manufacturing web-like paper material.
DETAILED DESCRIPTION
[0016] With reference to
[0017] In detail, the drying and desiccating equipment of the plant 10 comprises a first drying device, in turn comprising at least one rotary dryer 12 supplied with pressurised steam. The slurry of paper material adheres dynamically on the lateral surface of the dryer 12. Therefore, the cylinder 12 is of the so-called “Yankee” type and it is supplied with live steam at a predefined operating pressure, preferably comprised between about 4 bar G and about 10 bar G. Condensing on the inner surface of the Yankee cylinder 12, the steam transfers heat to the outer surface of the Yankee cylinder 12, that is the surface on which the slurry of paper material being dried adheres.
[0018] The drying and desiccating equipment of the plant 10 further comprises a second drying device, in turn comprising at least one hood 14, 16 which at least partially wraps the Yankee cylinder 12. The hood consists of a first half-hood 14 and at least one second half-hood 16 which are both capable of blowing high temperature dry air on the slurry of paper material wound on the lateral surface of the Yankee cylinder 12 and suctioning the hot and moist fumes released by the slurry of paper material. In detail, the first half-hood 14 is a so-called wet half-hood, which is arranged at the inlet side of the slurry of paper material on the Yankee cylinder 12, while the second half-hood 16 is a so-called dry half-hood, which is arranged at the outlet side of the slurry of paper material from the Yankee cylinder 12.
[0019] The drying and desiccating equipment of the plant 10 further comprises at least one first delivery circuit 18, designed to supply high temperature air to the first wet half-hood 14, and at least one second delivery circuit 20, designed to supply high temperature air to the second dry half-hood 16. As a result, there are provided for at least one first return circuit 22, designed for suctioning the fumes from the first wet half-hood 14, and at least one second return circuit 24, designed to suction the fumes from the second dry half-hood 16.
[0020] As shown in
[0021] Between the first return circuit 22 connected to the first wet half-hood 14 and the second return circuit 24 connected to the second dry half-hood 16 there is further interposed, upstream of the first interface duct 26, a second interface duct 32, also placed in fluid connection both with the first return circuit 22 and with the second return circuit 24. Along this second interface duct 32 there are installed a third flow regulating device 34 and a fourth flow regulating device 36. As shown by the arrows of
[0022] As shown in
[0023] Still with reference to
[0024] The pre-heated air is replenished in the first wet half-hood 14 through a first delivery duct 46, which is placed in fluid connection with the first delivery circuit 18 and with the first return circuit 22 and which is designed to send—to the first delivery duct 18—at least one part of the fumes which flow through the first return circuit 22 and at least one part of the air coming from the air supply duct 42. Similarly, pre-heated air is replenished in the second dry half-hood 16 through at least one second delivery circuit 48, which is placed in fluid connection with the second delivery duct and with the second return circuit 24 and which is designed to send—to the second delivery duct 20—at least one part of the fumes which flow through the second return circuit 24 and at least one part of the air coming from the air supply duct 42.
[0025] Between the first return circuit 22 and the first delivery duct 46 there is interposed at least one first fan 50, which is designed to transfer—to the first delivery duct 46 the air and/or fumes coming from the first return circuit 22. Between the first delivery duct 46 and the first delivery circuit 18 there is instead interposed at least one first heat generator 52, such as for example a burner, which is designed to heat both the air and fumes coming from the first delivery 46, and further air coming from the environment outside the plant 10 through a further air supply duct 58 (burner comburent air) which is placed in fluid connection with such first heat generator 52.
[0026] Between the second return circuit 24 and the second delivery circuit 48 there is also interposed at least one second fan 54, which is designed to transfer—to the second delivery duct 48—the air and/or the fumes coming from the second return circuit 24. Between the second delivery duct 48 and the second delivery circuit 20 there is therefore also interposed at least one second heat generator 56, such as for example a burner, which is designed to heat and dry the air and fumes coming from the second delivery duct 48, as well as further air coming from the environment outside the plant 10 through a further air supply duct 60 (burner comburent air) which is placed in fluid connection with such second heat generator 56.
[0027] According to the invention, between the first return circuit 22 connected to the first wet half-hood 14 and the second return circuit 24 connected to the second dry half-hood there is interposed at least one third interface duct 38. This third interface duct 38 is independent both from the first interface duct 26, on which there are installed the valves 28 and 30 for replenishing pre-heated air, and from the second interface duct 32, on which there are installed the valves 34 and 36 for extracting fumes.
[0028] Along the third interface duct 38 there is installed at least one fifth flow regulating device 40 which, as shown by the arrows of
[0029] This fifth flow regulating device 40 allows, whenever need arises, to transfer the fumes coming from the first return circuit 22 of the first wet half-hood 14, which is arranged at the inlet side of the slurry of paper material on the Yankee cylinder 12, on the second return circuit 24 connected to the second dry half-hood 16, which is arranged at the outlet side of the slurry of paper material from the Yankee cylinder 12. In this operating mode, the first heat generator 52, which is connected to the first wet half-hood 14 remains activated, while the second heat generator 56, which is connected to the second dry half-hood 16, may remain switched off. From the second dry half-hood 16, all the fumes, that is the one coming from both half-hoods 14 and 16, may be released into the atmosphere through the exhaust pipe 44 and an appropriate adjustment of the valves 34 and 36 for extracting fumes. Basically, this is the reverse cascade operating mode. However, the bidirectionality of the fifth flow regulating device 40 also allows to obtain the direct cascade operating mode.
[0030] Basically, the method for controlling process fluids in the plant 10 described up to now may selectively comprise the steps of: [0031] keeping the first flow regulating device 28, the second flow regulating device 30, the third flow regulating device 34 and the fourth flow regulating device 36 at least partially open, instead keeping only the fifth flow regulating device 40 closed; therefore, the first wet half-hood 14 and the second dry half-hood 16 operate simultaneously, without fluid exchange between the respective first return circuit 22 and second return circuit 24;
or: [0032] keeping the first flow regulating device 28, the fourth flow regulating device 36 and the fifth flow regulating device 40 at least partially open, instead keeping the second flow regulating device 30 and the third flow regulating device 34 closed; this allows the unidirectional fluid exchange between the second return circuit 24 and the first return circuit 22, so that the fumes coming from the second dry half-hood 16 are sent to the first wet half-hood 14, according to the direct cascade operating mode;
or: [0033] keeping the second flow regulating device 30, the third flow regulating device 34 and the fifth flow regulating device 40 at least partially open, instead keeping the first flow regulating device 28 and the fourth flow regulating device 36 closed; this allows the unidirectional fluid exchange between the first return circuit 22 and the second return circuit 24, so that the fumes coming from the first wet half-hood 14 are sent to the second dry half-hood 16, according to the reverse cascade operating mode.
[0034] Therefore, it has been observed that the system and the method for controlling process fluids in a plant for manufacturing web-like paper material according to the present invention attain the objects outlined above. The introduction of a specific bidirectional flow regulating device into the plant allows the plant to operate selectively according to three different working conditions of the half-hoods, ensuring maximum operating flexibility of the plant for all possible paper manufacturing grammage.
[0035] The system for controlling process fluids of the present invention thus conceived is in any case susceptible to various modifications and variants, all falling within the same inventive concept; furthermore, all details can be replaced by technically equivalent elements. Basically, the materials used as well as the shapes and dimensions may vary according to the technical needs.
[0036] Therefore, the scope of protection of the invention is defined by the attached claims.