US2755513A - Apparatus for drying loose fibrous materials - Google Patents

Apparatus for drying loose fibrous materials Download PDF

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Publication number
US2755513A
US2755513A US401319A US40131953A US2755513A US 2755513 A US2755513 A US 2755513A US 401319 A US401319 A US 401319A US 40131953 A US40131953 A US 40131953A US 2755513 A US2755513 A US 2755513A
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Prior art keywords
air
cylinders
drying
perforated
loose fibrous
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US401319A
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Fleissner Hans
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Fleissner & Sohn Maschf
Fleissner & Sohn Maschinenfabrik Firma
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Fleissner & Sohn Maschf
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B17/00Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement
    • F26B17/28Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed by rollers or discs with material passing over or between them, e.g. suction drum, sieve, the axis of rotation being in fixed position
    • F26B17/288Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed by rollers or discs with material passing over or between them, e.g. suction drum, sieve, the axis of rotation being in fixed position the materials being dried on perforated drums or rollers, e.g. sieve or suction drums
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06CFINISHING, DRESSING, TENTERING OR STRETCHING TEXTILE FABRICS
    • D06C3/00Stretching, tentering or spreading textile fabrics; Producing elasticity in textile fabrics
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06CFINISHING, DRESSING, TENTERING OR STRETCHING TEXTILE FABRICS
    • D06C2700/00Finishing or decoration of textile materials, except for bleaching, dyeing, printing, mercerising, washing or fulling
    • D06C2700/05Tenters or driers for fabrics with diagonal displacement
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S68/00Textiles: fluid treating apparatus
    • Y10S68/902Devices for storage and reuse of soap suds

Definitions

  • the apparatus is of the type comprising a disintegrating unit and a pair of superposed perforated cylinders to which the disintegrated flakes are conveyed by means of a circulating current of air.
  • the air current is generated by a fan and is made to pass a radiator on its Way to the cylinders; part of the air current is branched otf and made to travel to the rear side of the upper perforated cylinder.
  • the disintegrated fibers or flakes are made to adhere to thecircumference of the perforated cylinders, where an even thick fleece is formed depending on the feeding of the air current and the adjustment of guideplates covering part of the cylinders.
  • the eddy formation at the upper cylinder is caused primarily by an unsatisfactory air circulation in the known machines.
  • the fan In these machines, the fan is enclosed completely in a spiral casing from which air is withdrawn through an adjustable flap. This air removal causes a strong turbulence which, as stated above, is a serious drawback in the operation of the machines of this type.
  • the machine according to the invention comprises a scroll housing which completely encloses a fan for the generation of an air circulating system.
  • the casing contains two separated air ducts, one of which serves for feeding air over a heater to the disintegrating unit, whereas the other duct conveys air to the rear side of the upper of two perforated cylinders.
  • a further characteristic feature of the invention is the arrangement of a completely closed system of the circulating air passing by the disintegrating unit-
  • a flap has to be provided as an outlet for the air drawn into the system at another place. This is necessary because of the irregularity of the admission of fresh air by the fan action of. the beater.
  • the before-mentioned arrangement causes considerable heat losses in the whole system since the air is at high temperature at the withdrawal spot of the circulating system.
  • the disintegrating unit which preferably contains a spiked drum,v is included in the drying chamber and the air circulating system is completely closed. It is thereby accomplishd that the heat in the air is retained in its entirety, since no fresh air is admitted which could cool down the circulating air and'could lead to moisture precipitation in the perforated cylinders.
  • a machine built according to the invention operates continuously without condensation of moisture occurring on the cylinder walls and without other disturbances. Furthermore, the drying efficiency of the machine is increased due to the fact that a drying action is already performed in the take-in-cylinders which is equal to about half the drying action of one of the perforated driers.
  • Fig. l is a vertical longitudinal section through the center of my device provided with a drier of the straining drum type.
  • Fig. 2 is a vertical longitudinal section through the center of another embodiment of my invention in which a belt drier is used.
  • Fig. 3 is partly a sectional view along line III-III of Fig. l and shows one of the large driers in elevation;
  • Fig. 4 is a section along line IV-IV of Fig. 2.
  • numeral 1 desig nates a conveyor band onto which the fibrous goods to be dried are placed by hand or by any mechanical device. Before this happens, water is eliminated from the goods by a centrifuging or sqeeuzing process.
  • a pair of takein rollers 2 Arranged ahead of the conveyor 1 is a pair of takein rollers 2, which are arranged in the neighborhood of the spikes of the disintegrator 3. The spikes are so close to rollers 2 that there is hardly any gap left. The spikes are driven past at high speed and tear the fiber material emerging from the rollers into fine flakes, which are thrust by centrifugal force through a channel 4 to take-in cylinders 5 and 6.
  • the cylinders 5 and 6 are open atboth ends and are connected to a fan 7 which sucks out air from the interior of cylinders 5 and 6 through ducts 8 and 9.
  • Fan 7 is so constructed that it returns part of the air by the shortest route 12 to the upper cylinder, whereas the remaining part is conducted by Way of heaters 10 and a channel 11 to pass disintegrator 3 and is carried through channel 4 to the front side of cylinders 5 and 6. Where the air passes the disintegrator 3, the channel 11 is very narrow and air velocity is great, whereby the flakes are withdrawn and carried along from the spikes of the disintegrator.
  • the fan casing is so constructed that two separate air ducts 12 and 13 are provided therein.
  • Duct 12 carries air at reduced pressure to the rear side of the upper cylinder, whereas duct 13 presses air through heaters 10 and by way of channels 11 and 4 returns it to the front side of the cylinders.
  • the air movement is enhanced by the rapid rotation of the disintegrator 3.
  • guide plates 14 and 15 are arranged, which prevent the aspiration of air through the covered part of the cylinder wall. These plates serve the purpose of preventing fiber flakes to adhere to those parts of the cylinder walls where their adherence is not desired. In the free portions of the cylinders, flakes will adhere at the front and fleece will form at the rear, whereafter the fleece is caused to travel from one larger drier 20 to another one, while being under the suction of dry air.
  • the fleece formed in the take-in cylinders may also be placed onto one or more conveyor bands 21 and carried through the drying chamber thereon (see Figs. 2 and 4).
  • heaters for the upper cylinder 5 are shown at 16 and 17; heaters for the lower cylinder 6 are designated by 18, 19. These heaters may be of any known design.
  • a device for drying loose fibrous material comprising a fiber-disintegrating unit, a pair of perforated cylinders one arranged above the other, means for generating an air current capable of transporting the particles disintegrated in said unit to said cylinders, means for heating said air current, and means for drying a fleece of said fibers formed on said cylinders, said device being provided with a scroll housing; a fan arranged therein for generating said air current; two separated air ducts one of them discharging air over said heating means to said disintegrating unit, the other one supplying air to the rear of the upper one of said two cylinders.
  • a device for drying loose fibrous material according to claim 1 including additional heating means inside the perforated cylinders.
  • a device for drying loose fibrous material according to claim 1 including additional heating means outside the perforated cylinders.
  • a device for drying loose fibrous material according to claim 1 including additional heating means both inside and outside the perforated cylinders.

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  • Engineering & Computer Science (AREA)
  • Textile Engineering (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Drying Of Solid Materials (AREA)

Description

July 24, 1956 H. FLEISSNER 2,755,513
APPARATUS FOR DRYING LOOSE FIBROUS MATERIALS Filed Dec. 30, 1953 m m gv NWWAV \YNA 77 73 1V 7 APPARATUS FOR DRYING LOGSE FIBROUS' MATERIALS Hans Fleissner, Egelsbach Kreis Olfenbach (Main), Germany, assignor to Firma Fleissner & Sohn, Maschinenfabrik, Egelsbach Kreis Oifenbach (Main), Germany The present invention relates to an apparatus for drying loose fibrous materials.
The apparatus is of the type comprising a disintegrating unit and a pair of superposed perforated cylinders to which the disintegrated flakes are conveyed by means of a circulating current of air. The air current is generated by a fan and is made to pass a radiator on its Way to the cylinders; part of the air current is branched otf and made to travel to the rear side of the upper perforated cylinder.
In machines of this known type, the disintegrated fibers or flakes are made to adhere to thecircumference of the perforated cylinders, where an even thick fleece is formed depending on the feeding of the air current and the adjustment of guideplates covering part of the cylinders.
The known machines, however, have the inconvenience that the air circulation has to be under constant surveyance by operating a number of flaps. When the-control and adjustment of these flaps are not carried out at the proper time, disturbances are likely to come up in the fleece formation and the machine can no longer be operated continuously. A very marked disadvantage is, furthermore, the occurrence of a strong eddy formation at the rear of the upper perforated cylinder. This is likely to interfere with the entire air circulationsystem. The eddies disturb fleece formation at the rear of the cylinder to such an extent that some places of the" cyliinder become completely uncovered. This, in turn, interferes with the vacuum in the upper cylinder so that the whole air circulation is disturbed.
In addition to this drawback, there is a further inconvenience interfering with the air circulation. This is the fact that in the known machines the beaters, too, have a certain fan action while disintegrating the starting material into flakes. Cold air is thereby admitted into the system which lowers the temperature of the hot air reaching the perforated cylinder. This in turn reduces the temperature of the cylinder itself to an extent that water is condensed on the cylinder from the moist air. Such condensation is, of course, another in conveniece which counteracts the drying action of the machine.
The eddy formation at the upper cylinder is caused primarily by an unsatisfactory air circulation in the known machines. In these machines, the fan is enclosed completely in a spiral casing from which air is withdrawn through an adjustable flap. This air removal causes a strong turbulence which, as stated above, is a serious drawback in the operation of the machines of this type.
It is the object of the present invention to overcome the shortcomings of the known machines and to provide an apparatus permitting a continuous flawless formation.
It is a further object of the invention to provide means for continuous operation without adjustment of the machinery during. said operation at the time when new material is fed thereto.
Finally, it is an object of the invention to provide machinery in which materials of varying moisture content can be driedunder even working conditions.
Other objects and advantages of this invention will become apparent from the following, description and the acompanying drawings.
The machine according to the invention comprises a scroll housing which completely encloses a fan for the generation of an air circulating system. The casing contains two separated air ducts, one of which serves for feeding air over a heater to the disintegrating unit, whereas the other duct conveys air to the rear side of the upper of two perforated cylinders. By this air circulation through separate ducts, which is brought about by the subdivision of the spiral easing into two parts, the air current at the rear of the perforated cylinder is calmed down to such an extent that no more disturbances in fleece formation will occur; the air circulation in the entire machine is very uniform and operation can be made to function continuously, without interruption.
A further characteristic feature of the invention is the arrangement of a completely closed system of the circulating air passing by the disintegrating unit- In the known drying apparatus of the present type, a flap has to be provided as an outlet for the air drawn into the system at another place. This is necessary because of the irregularity of the admission of fresh air by the fan action of. the beater. The before-mentioned arrangement causes considerable heat losses in the whole system since the air is at high temperature at the withdrawal spot of the circulating system.
According to the invention, the disintegrating unit, which preferably contains a spiked drum,v is included in the drying chamber and the air circulating system is completely closed. It is thereby accomplishd that the heat in the air is retained in its entirety, since no fresh air is admitted which could cool down the circulating air and'could lead to moisture precipitation in the perforated cylinders.
The: use of a spiked drum conjointly employed with the air circulating system according to the invention has the advantage that spikes have a far lower fan action and will therefore not suck in fresh air from their environment into the circulating system.
It is a further advantage of the present invention that additional heaters are provided inside and/ or outside of the perforated cylinders, so that the cylinders will be heated up to a degree that will insure their remaining dry at all times.
A machine built according to the invention operates continuously without condensation of moisture occurring on the cylinder walls and without other disturbances. Furthermore, the drying efficiency of the machine is increased due to the fact that a drying action is already performed in the take-in-cylinders which is equal to about half the drying action of one of the perforated driers.
An apparatus according to the present invention is shown more fully in the accompanying drawing, in which corresponding parts are designated by the same numerals in the various figures of the drawing.
Fig. l is a vertical longitudinal section through the center of my device provided with a drier of the straining drum type.
Fig. 2 is a vertical longitudinal section through the center of another embodiment of my invention in which a belt drier is used.
Fig. 3 is partly a sectional view along line III-III of Fig. l and shows one of the large driers in elevation; and
Fig. 4 is a section along line IV-IV of Fig. 2.
Referring more particularly to Fig. l, which shows a disintegrating unit with the perforated take-in cylinders, an associated fan and the heaters for the cylinders, as well as the large driers in cross-section, numeral 1 desig nates a conveyor band onto which the fibrous goods to be dried are placed by hand or by any mechanical device. Before this happens, water is eliminated from the goods by a centrifuging or sqeeuzing process.
Arranged ahead of the conveyor 1 is a pair of takein rollers 2, which are arranged in the neighborhood of the spikes of the disintegrator 3. The spikes are so close to rollers 2 that there is hardly any gap left. The spikes are driven past at high speed and tear the fiber material emerging from the rollers into fine flakes, which are thrust by centrifugal force through a channel 4 to take-in cylinders 5 and 6.
The cylinders 5 and 6 are open atboth ends and are connected to a fan 7 which sucks out air from the interior of cylinders 5 and 6 through ducts 8 and 9. Fan 7 is so constructed that it returns part of the air by the shortest route 12 to the upper cylinder, whereas the remaining part is conducted by Way of heaters 10 and a channel 11 to pass disintegrator 3 and is carried through channel 4 to the front side of cylinders 5 and 6. Where the air passes the disintegrator 3, the channel 11 is very narrow and air velocity is great, whereby the flakes are withdrawn and carried along from the spikes of the disintegrator.
For that purpose, the fan casing is so constructed that two separate air ducts 12 and 13 are provided therein. Duct 12 carries air at reduced pressure to the rear side of the upper cylinder, whereas duct 13 presses air through heaters 10 and by way of channels 11 and 4 returns it to the front side of the cylinders. The air movement is enhanced by the rapid rotation of the disintegrator 3.
In the interior of the cylinders S and 6, guide plates 14 and 15 are arranged, which prevent the aspiration of air through the covered part of the cylinder wall. These plates serve the purpose of preventing fiber flakes to adhere to those parts of the cylinder walls where their adherence is not desired. In the free portions of the cylinders, flakes will adhere at the front and fleece will form at the rear, whereafter the fleece is caused to travel from one larger drier 20 to another one, while being under the suction of dry air.
The fleece formed in the take-in cylinders may also be placed onto one or more conveyor bands 21 and carried through the drying chamber thereon (see Figs. 2 and 4). r
In Fig. 1, heaters for the upper cylinder 5 are shown at 16 and 17; heaters for the lower cylinder 6 are designated by 18, 19. These heaters may be of any known design.
What I claim is:
1. A device for drying loose fibrous material, comprising a fiber-disintegrating unit, a pair of perforated cylinders one arranged above the other, means for generating an air current capable of transporting the particles disintegrated in said unit to said cylinders, means for heating said air current, and means for drying a fleece of said fibers formed on said cylinders, said device being provided with a scroll housing; a fan arranged therein for generating said air current; two separated air ducts one of them discharging air over said heating means to said disintegrating unit, the other one supplying air to the rear of the upper one of said two cylinders.
2. A device for drying loose fibrous material according to claim 1, wherein the disintegrating unit consists of a spiked drum built into said drying chamber and completely enclosed therein.
3. A device for drying loose fibrous material according to claim 2, wherein the air system is a circulating, completely closed system.
4. A device for drying loose fibrous material according to claim 1 including additional heating means inside the perforated cylinders.
5. A device for drying loose fibrous material according to claim 1 including additional heating means outside the perforated cylinders.
6. A device for drying loose fibrous material according to claim 1 including additional heating means both inside and outside the perforated cylinders.
References Cited in the file of this patent UNITED STATES PATENTS 423,598 Duncan Mar. 18, 1890 663,868 Crean Dec. 18, 1900 868,063 Angus Oct. 15, 1907 930,756 Howarth et al Aug. 10, 1909 1,377,793 Schwartz May 10, 1921 1,774,309 Anderson Aug. 26, 1930
US401319A 1953-01-17 1953-12-30 Apparatus for drying loose fibrous materials Expired - Lifetime US2755513A (en)

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Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2876500A (en) * 1954-08-26 1959-03-10 Curlator Corp Machine for fiber cleaning
US2981007A (en) * 1956-11-23 1961-04-25 Fleissner & Sohn Maschf Willow drier
US2996808A (en) * 1956-12-07 1961-08-22 Fleissner & Sohn Maschf Willow drier for loose fibrous material
US3028682A (en) * 1958-03-19 1962-04-10 Fleissner & Sohn G M B H & Co Treatment plant for continuous lengthy material in particular for textile materials
US3043018A (en) * 1958-06-02 1962-07-10 Fleissner & Sohn G M B H & Co Screen cylinder drier for fibrous material
US3251140A (en) * 1963-06-03 1966-05-17 Edward H Fraenzel Dryer for heating and removing moisture for aggregate material
US3835671A (en) * 1972-03-27 1974-09-17 Vepa Ag Apparatus for the continuous treatment, particularly dyeing, of fibrous material

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1036800B (en) * 1956-03-07 1958-08-21 Fleissner & Sohn Maschinenfabr Multi-drum dryer for loose fiber material
DE3228672A1 (en) * 1982-07-31 1984-02-02 Trützschler GmbH & Co KG, 4050 Mönchengladbach METHOD AND DEVICE FOR AIR-CONDITIONING A SPINNING PREPARATION PLANT

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US423598A (en) * 1890-03-18 Drier and conveyer
US663868A (en) * 1899-01-03 1900-12-18 Francis Charles Crean Treatment of wood-pulp.
US868063A (en) * 1902-05-26 1907-10-15 William Angus Pulp-flaker.
US930756A (en) * 1908-09-14 1909-08-10 Thomas Howarth Drying apparatus.
US1377793A (en) * 1919-10-20 1921-05-10 Philadelphia Textile Machinery Drier
US1774309A (en) * 1929-03-18 1930-08-26 Puget Sound Pulp And Timber Co Method and apparatus for shredding and drying pulp

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US423598A (en) * 1890-03-18 Drier and conveyer
US663868A (en) * 1899-01-03 1900-12-18 Francis Charles Crean Treatment of wood-pulp.
US868063A (en) * 1902-05-26 1907-10-15 William Angus Pulp-flaker.
US930756A (en) * 1908-09-14 1909-08-10 Thomas Howarth Drying apparatus.
US1377793A (en) * 1919-10-20 1921-05-10 Philadelphia Textile Machinery Drier
US1774309A (en) * 1929-03-18 1930-08-26 Puget Sound Pulp And Timber Co Method and apparatus for shredding and drying pulp

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2876500A (en) * 1954-08-26 1959-03-10 Curlator Corp Machine for fiber cleaning
US2981007A (en) * 1956-11-23 1961-04-25 Fleissner & Sohn Maschf Willow drier
US2996808A (en) * 1956-12-07 1961-08-22 Fleissner & Sohn Maschf Willow drier for loose fibrous material
US3028682A (en) * 1958-03-19 1962-04-10 Fleissner & Sohn G M B H & Co Treatment plant for continuous lengthy material in particular for textile materials
US3043018A (en) * 1958-06-02 1962-07-10 Fleissner & Sohn G M B H & Co Screen cylinder drier for fibrous material
US3251140A (en) * 1963-06-03 1966-05-17 Edward H Fraenzel Dryer for heating and removing moisture for aggregate material
US3835671A (en) * 1972-03-27 1974-09-17 Vepa Ag Apparatus for the continuous treatment, particularly dyeing, of fibrous material

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GB745398A (en) 1956-02-22
FR1091119A (en) 1955-04-07

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