CN103114488A - Normal-pressure multichannel papermaking drying cylinder - Google Patents
Normal-pressure multichannel papermaking drying cylinder Download PDFInfo
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- CN103114488A CN103114488A CN2013100919153A CN201310091915A CN103114488A CN 103114488 A CN103114488 A CN 103114488A CN 2013100919153 A CN2013100919153 A CN 2013100919153A CN 201310091915 A CN201310091915 A CN 201310091915A CN 103114488 A CN103114488 A CN 103114488A
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- heat
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- drying cylinder
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- casing wall
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- 238000001035 drying Methods 0.000 title claims abstract description 48
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 47
- 238000004519 manufacturing process Methods 0.000 claims abstract description 5
- 239000000463 material Substances 0.000 claims description 7
- 229910052751 metal Inorganic materials 0.000 claims description 5
- 239000002184 metal Substances 0.000 claims description 5
- 238000005266 casting Methods 0.000 claims description 4
- 238000000034 method Methods 0.000 claims description 3
- 238000007599 discharging Methods 0.000 abstract description 3
- 230000005540 biological transmission Effects 0.000 description 4
- 238000010586 diagram Methods 0.000 description 4
- 239000004744 fabric Substances 0.000 description 4
- 229910000838 Al alloy Inorganic materials 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 2
- 239000004411 aluminium Substances 0.000 description 2
- 229910052782 aluminium Inorganic materials 0.000 description 2
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 2
- 238000009833 condensation Methods 0.000 description 2
- 230000005494 condensation Effects 0.000 description 2
- 229910052802 copper Inorganic materials 0.000 description 2
- 239000010949 copper Substances 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- 238000009825 accumulation Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 230000007306 turnover Effects 0.000 description 1
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Abstract
The invention discloses a normal-pressure multichannel papermaking drying cylinder which comprises a cylinder body. The drying cylinder is characterized in that a plurality of heat conducting channels which are uniformly distributed are laterally or longitudinally arranged in the cylindrical cylinder wall of the cylinder body; one end of each heat conducting channel is communicated with a steam input pipe, and the other end is communicated with a condensed water output pipe; and the steam input pipe and the condensed water output pipe are respectively communicated with a steam inlet and a condensed water outlet of a rotary joint. When steam enters the heat conducting channels of the cylinder body of the drying cylinder with the structure, the cylindrical cylinder wall of the cylinder body emits heat, heat is transferred to wet paper to be dried on the surface of the cylinder wall, and the wet paper is heated and water evaporates, so that the purpose of drying is achieved. As the drying cylinder body adopts an open structure, and pressure only exists in the heat conducting channels, the drying cylinder body does not belong to a pressure container. The drying cylinder belongs to a normal-pressure drying cylinder, has a simple structure, is high in temperature and heat transfer efficiency, low in weight, smooth in steam flowing and condensed water discharging, and low in manufacture cost.
Description
Technical field
The present invention relates to a kind of drying equipment, especially the paper drying cylinder in the papermaking facility.
Background technology
In at present general papermaking facility, drying section is the main power consumption part of paper machine, and drying cylinder is the major part of Dryer Section of Paper Machine.Existing drying cylinder is mainly constructed and is comprised cylinder body, power transmission shaft, steam and condensed water turnover swivel joint, condensed water discharge siphon pipe and attemperator etc.The main task of drying cylinder is with the l Water Paper page oven dry through cylinder surfaces.The drying cylinder of this structure is in the process with the oven dry of l Water Paper page, ubiquity impeded drainage problem, build up in drying cylinder if in drying cylinder, the condensed water eliminating is bad, when gathering, the higher condensed water of rotating speed forms the condensation water ring when more, because condensation water ring thermal conductivity factor is low, to greatly increase the thermal resistance of drying cylinder, cause the drying efficiency of drying cylinder to descend; When the drying cylinder internal water accumulation, also can greatly increase the power that transmission consumes; When condensed water is discharged not freely off and on, can cause drying section electric load strenuous exercise, the mass dryness fraction of page is unstable, affects the normal operation of paper machine; The transmission balance of drying cylinder is destroyed, thereby caused paper machine running mid frame to produce vibration.Siphon pipe is mainly used to get rid of the drying cylinder condensed water at present, but when the rotating speed requirement was high, the drying cylinder condensed water was got rid of or be undesirable.In addition, existing drying cylinder belongs to airtight pressure vessel, and casing wall and end cap need enough wall thickness to bear steam pressure.Steam pressure is higher, and the casing wall wall thickness is larger, and resistance to heat is also larger, thereby the production capacity raising of drying cylinder is restricted, and the material such as drying cylinder weight and consumption steel increases simultaneously.In order to overcome the shortcoming of traditional drying cylinder, also someone proposes multichannel drying cylinder theory and studies at present, and the major programme of proposition has: 1, at drying cylinder inwall casting groove, and cover cover plate on groove; 2, at drying cylinder outer wall casting groove, and cover cover plate on groove; 3, at the drying cylinder inwall, metal corrugated plate is installed.These schemes still can't realize using because of reasons such as difficulty of processing, stressed, sealings so far.
Summary of the invention
The purpose of this invention is to provide a kind of simple in structure, heat transfer efficiency is high, condensate water discharging is unimpeded, temperature is high and cost is low normal pressure multichannel paper-making drying cylinder.
For reaching above-mentioned purpose, technical scheme of the present invention is:
A kind of normal pressure multichannel paper-making drying cylinder, it comprises cylinder body, it is characterized in that:
In the tubular casing wall of the garden of described cylinder body, laterally or vertically be provided with uniform some passages of heat;
One end of described each passage of heat is connected with steam input pipe, and the other end is communicated with condensate output transistor;
Described steam input pipe, condensate output transistor are communicated with steam inlet and the condensation-water drain of swivel joint respectively.
Described each passage of heat is divided into some groups, and the two ends of every group are communicated with respectively with steam inlet and condensation-water drain respectively.
The drying cylinder of said structure, casing wall is connected with the wheel hub at two ends, and the two ends spoke is separately fixed on the power transmission shaft of both sides, is fixedly connected with swivel joint in an end axle wherein.Vapours is redistributed in the passage of heat of cylinder body from the steam inlet of swivel joint to steam input pipe.Steam enters the passage of heat of cylinder body, makes the garden tubular casing wall heating of cylinder body, and heat passes on the casing wall surface and needs the dry wet paper, the wet paper moisture content that evaporates by heat, thus reach dry purpose.When steam was to the wet paper drying, steam was condensed into water, and the Steam Actuation that is constantly entered in passage of heat, shifted condensed water onto condensation-water drain, discharged from the condensation-water drain of swivel joint at last.Because the drying cylinder structure is opened wide, because passage of heat is less, can bear higher pressure, and only pressure be arranged in passage of heat, so drying cylinder does not belong to pressure vessel.Therefore, drying cylinder of the present invention is a kind of non-pressure vessel, and is simple in structure, and heat transfer efficiency is high, and temperature is high, and is lightweight, the paper drying equipment of the unimpeded and low cost of manufacture of vapor flow and condensate water discharging.
Description of drawings
Fig. 1 is the sectional structure schematic diagram of transverse annular cloth passage of heat of the present invention.
Fig. 2 is the structural representation of analysing and observe along the A-A line in Fig. 1.
Fig. 3 is the sectional structure schematic diagram of the vertical cloth passage of heat of the present invention.
Fig. 4 is the structural representation of analysing and observe along the B-B line in Fig. 3.
In the drawings, left axle 1, bearing 2, wheel hub 3, horizontal passage of heat 4, casing wall 5, steam input pipe 6, condensate output transistor 7, right axle 8, steam swivel joint 9, steam inlet 10, condensation-water drain 11, condensed water excessively manage 12, and steam excessively manages 13, laterally the steam input is in charge of 14, and laterally solidifying water output is in charge of 15, vertically passage of heat 16, vertically solidifying water output is in charge of 17, and vertically the steam input is in charge of 18, siphunculus 19.
The specific embodiment
Below in conjunction with accompanying drawing, the invention will be further described.
Shown in Figure 1, be the sectional structure schematic diagram of transverse annular cloth passage of heat of the present invention; Shown in Figure 2, be the structural representation of analysing and observe along the A-A line in Fig. 1.Come together to see in conjunction with two figure, cylinder body comprises left axle 1, bearing 2, spoke 3, casing wall 5 and right axle 8.Wherein, the inboard, two ends of casing wall 5 is fixedly connected with two spokes 3 respectively, and the centre of both sides spoke 3 is fixedly connected with right axle 8 with left axle 1 respectively, and left axle 1 and right axle 8 can be same axle; Be respectively equipped with bearing 2 at left axle 1 and right axle 8 outsides.In garden tubular casing wall 5, laterally be provided with uniform some horizontal passage of heat 4, one end of each horizontal passage of heat 4 is in charge of 14 by horizontal steam input and is connected with steam input pipe 6, the other end is in charge of 15 by horizontal condensed water output and is communicated with condensate output transistor 7, and by steam excessively excessively manage 12 with steam inlet 10 and the condensation-water drain 11 of swivel joint 9 be communicated with respectively by pipe 13, condensed water for the other end of steam input pipe 6, condensate output transistor 7.
Shown in Figure 3, be the sectional structure schematic diagram of the vertical cloth passage of heat of the present invention, shown in Figure 4, be the structural representation of analysing and observe along the B-B line in Fig. 3.In like manner, come together to see in conjunction with two figure, compare with Fig. 2 with Fig. 1, the passage of heat that just arranges in casing wall 5 with laterally passage of heat 4 is mutually vertical, is vertical passage of heat 16, basic identical with Fig. 1, Fig. 2 of other structure.As we know from the figure, vertically passage of heat 16 sequentially by vertical steam input be in charge of 18, steam input pipe 6, steam excessively manage 13 and be communicated with steam inlet 10, or sequentially export by vertically solidifying water be in charge of 17, condensate output transistor 7, condensed water excessively manage 12 and condensation-water drain 11.Each passage of heat 4 on the same group is communicated with by the siphunculus 19 of an end.See shown in Fig. 3, steam input is in charge of 18, steam input pipe 6, solidifying water output are in charge of 17, condensate output transistor 7 is the outsides that are arranged in cylinder body, in like manner, also can be arranged in the inboard of cylinder body again.
In order to increase the flow velocity of steam in passage of heat 4, each passage of heat 4 can be divided into some groups, and the two ends of every group are communicated with respectively with steam inlet 10 and condensation-water drain 11 respectively.Simultaneously, in order to increase the temperature homogeneity of casing wall 5, adjacent passage of heat 4 be attributed to respectively different groups and steam flow opposite.
Steam swivel joint 9 comprise condensed water excessively pipe 12, steam excessively manage 13, steam inlet 10 and condensation-water drain 11, wherein, condensed water is excessively managed 12 and is communicated with condensation-water drain 11, steam excessively manages 13 and steam inlet 10.Steam swivel joint 9 is prior art products, on sale on the market.
Operation principle of the present invention is: heating steam excessively manages 13 from the steam inlet 10 of steam swivel joint 9 by steam, enter steam input pipe 6, then by the input of horizontal steam be in charge of 14 or vertically the steam input be in charge of 18 be assigned in casing wall 5 horizontal passages of heat 4 or vertically in passage of heat 16.Steam enters that in passage of heat, its heat is delivered on casing wall 5, and the wet paper of casing wall outer surface is carried out heat drying.Simultaneously steam is condensed into water, and by the Steam Actuation in passage of heat, enter horizontal steam input be in charge of 14 or vertically solidifying water output be in charge of 17 and be pooled to condensed water excessively in pipe 12, discharge from the condensation-water drain 11 of swivel joint 9 at last.
In the present invention, arrange in casing wall 5 horizontal passage of heat 4 or vertically the method for passage of heat 16 mainly contain two kinds:
1, the horizontal passage of heat 4 in casing wall 5 or vertically passage of heat 16 adopt the high metal of good heat conductivity, intensity or the pipeline of other material, as steel, iron, aluminium, aluminium alloy or copper pipe etc., are cast as a whole with casing wall.Or
2, the horizontal passage of heat 4 in casing wall 5 or vertically passage of heat 16, adopt the high metal of good heat conductivity, intensity or the pipeline of other material, first with the part of casing wall 5 thickness, i.e. shell casting or manufacturing are completed, and then arrange the passage of heat pipeline at the inner surface of this shell; Then adopt the material of another kind of good heat conductivity, as aluminium, aluminium alloy or copper etc., passage of heat pipeline and shell are cast as are integrated.
Claims (4)
1. normal pressure multichannel paper-making drying cylinder, it comprises cylinder body, it is characterized in that:
In the garden of described cylinder body tubular casing wall (5), laterally or vertically be provided with uniform some passages of heat (4,16);
One end of described each passage of heat (4,16) is connected with steam input pipe (6), and the other end is communicated with condensate output transistor (7);
Described steam input pipe (6), condensate output transistor (7) are communicated with steam inlet (10) and the condensation-water drain (11) of swivel joint (9) respectively.
2. normal pressure multichannel paper-making drying cylinder according to claim 1 is characterized in that:
Described each passage of heat (4,16) is divided into some groups, and the two ends of every group are communicated with respectively with steam inlet (10) and condensation-water drain (11) respectively.
3. normal pressure multichannel paper-making drying cylinder according to claim 1 is characterized in that:
Adjacent passage of heat (4,16) be attributed to respectively different groups and steam flow opposite.
4. normal pressure multichannel paper-making drying cylinder according to claim 1 is characterized in that:
The method that horizontal passage of heat (4) or vertical passage of heat (16) are set in casing wall 5 mainly contains two kinds:
(1) the horizontal passage of heat 4 in casing wall 5 or vertically passage of heat 16 adopt the high metal of good heat conductivity, intensity or pipeline and the casing wall of other material to be cast as a whole; Or
(2) the horizontal passage of heat 4 in casing wall 5 or vertically passage of heat 16, adopt the high metal of good heat conductivity, intensity or the pipeline of other material, first with the part of casing wall 5 thickness, i.e. shell casting or manufacturing are completed, and then arrange the passage of heat pipeline at the inner surface of this shell; Then adopt the material of another kind of good heat conductivity, passage of heat pipeline and shell are cast as are integrated.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201310091915.3A CN103114488B (en) | 2013-03-21 | 2013-03-21 | A kind of normal pressure hyperchannel paper-making drying cylinder |
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CN201310091915.3A CN103114488B (en) | 2013-03-21 | 2013-03-21 | A kind of normal pressure hyperchannel paper-making drying cylinder |
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CN103114488A true CN103114488A (en) | 2013-05-22 |
CN103114488B CN103114488B (en) | 2016-06-01 |
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CN201310091915.3A Expired - Fee Related CN103114488B (en) | 2013-03-21 | 2013-03-21 | A kind of normal pressure hyperchannel paper-making drying cylinder |
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108486946A (en) * | 2018-05-14 | 2018-09-04 | 昆明纳太科技有限公司 | Monoblock type hot vapour drying cylinder and its system applied to UTILIZATION OF VESIDUAL HEAT IN |
CN108691233A (en) * | 2018-05-14 | 2018-10-23 | 昆明纳太科技有限公司 | Assembled hot vapour drying cylinder and its be applied to afterheat utilizing system |
CN109403122A (en) * | 2018-12-28 | 2019-03-01 | 安德里茨(中国)有限公司 | Continuous drying drying cylinder |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5899264A (en) * | 1997-09-17 | 1999-05-04 | Marquip, Inc. | Steam supply and condensate removal apparatus for heated roll |
US5900120A (en) * | 1997-09-22 | 1999-05-04 | Voith Sulzer Paper Technology North America, Inc. | Drying cylinder bearing support in a paper-making machine |
US6032725A (en) * | 1998-06-02 | 2000-03-07 | Marquip, Inc. | Rotary steam joint and valve assembly |
CN2488949Y (en) * | 2001-07-26 | 2002-05-01 | 耿志印 | Drying equipment for paper making |
WO2006057023A1 (en) * | 2004-11-26 | 2006-06-01 | A. Celli Paper S.P.A. | Yankee cylinder for the papermaking industry, with peripheral circulation of the head transfer fluid |
CN201236297Y (en) * | 2008-07-04 | 2009-05-13 | 陕西科技大学 | Cylinder type intermediate layer multicenter drying cylinder |
CN203270374U (en) * | 2013-03-21 | 2013-11-06 | 李春崇 | Normal pressure multi-channel papermaking drying cylinder |
-
2013
- 2013-03-21 CN CN201310091915.3A patent/CN103114488B/en not_active Expired - Fee Related
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5899264A (en) * | 1997-09-17 | 1999-05-04 | Marquip, Inc. | Steam supply and condensate removal apparatus for heated roll |
US5900120A (en) * | 1997-09-22 | 1999-05-04 | Voith Sulzer Paper Technology North America, Inc. | Drying cylinder bearing support in a paper-making machine |
US6032725A (en) * | 1998-06-02 | 2000-03-07 | Marquip, Inc. | Rotary steam joint and valve assembly |
CN2488949Y (en) * | 2001-07-26 | 2002-05-01 | 耿志印 | Drying equipment for paper making |
WO2006057023A1 (en) * | 2004-11-26 | 2006-06-01 | A. Celli Paper S.P.A. | Yankee cylinder for the papermaking industry, with peripheral circulation of the head transfer fluid |
CN201236297Y (en) * | 2008-07-04 | 2009-05-13 | 陕西科技大学 | Cylinder type intermediate layer multicenter drying cylinder |
CN203270374U (en) * | 2013-03-21 | 2013-11-06 | 李春崇 | Normal pressure multi-channel papermaking drying cylinder |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108486946A (en) * | 2018-05-14 | 2018-09-04 | 昆明纳太科技有限公司 | Monoblock type hot vapour drying cylinder and its system applied to UTILIZATION OF VESIDUAL HEAT IN |
CN108691233A (en) * | 2018-05-14 | 2018-10-23 | 昆明纳太科技有限公司 | Assembled hot vapour drying cylinder and its be applied to afterheat utilizing system |
CN108486946B (en) * | 2018-05-14 | 2023-06-20 | 昆明纳太科技有限公司 | Integral hot steam dryer and system applied to waste heat utilization thereof |
CN108691233B (en) * | 2018-05-14 | 2024-03-19 | 昆明纳太科技有限公司 | Assembled hot steam dryer |
CN109403122A (en) * | 2018-12-28 | 2019-03-01 | 安德里茨(中国)有限公司 | Continuous drying drying cylinder |
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CN103114488B (en) | 2016-06-01 |
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Effective date of registration: 20180129 Address after: 530031 No. 9, No. 203, Fenghuang District, 68 Star Road, the Guangxi Zhuang Autonomous Region, Nanning Patentee after: Guangxi Guang Yi environmental protection technology Co., Ltd. Address before: 530031 No. 9, No. 203, Fenghuang District, 68 Star Road, the Guangxi Zhuang Autonomous Region, Nanning Patentee before: Li Chunchong |
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CF01 | Termination of patent right due to non-payment of annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160601 Termination date: 20190321 |