US2353615A - Method of heating goods - Google Patents

Method of heating goods Download PDF

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US2353615A
US2353615A US385576A US38557641A US2353615A US 2353615 A US2353615 A US 2353615A US 385576 A US385576 A US 385576A US 38557641 A US38557641 A US 38557641A US 2353615 A US2353615 A US 2353615A
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goods
chamber
heating
chute
steam
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US385576A
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Hans O Kauffmann
Edward S Shanley
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BUFFALO ELECTRO CHEM CO
BUFFALO ELECTRO-CHEMICAL COMPANY Inc
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BUFFALO ELECTRO CHEM CO
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    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06MTREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
    • D06M11/00Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with inorganic substances or complexes thereof; Such treatment combined with mechanical treatment, e.g. mercerising
    • D06M11/80Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with inorganic substances or complexes thereof; Such treatment combined with mechanical treatment, e.g. mercerising with boron or compounds thereof, e.g. borides
    • D06M11/82Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with inorganic substances or complexes thereof; Such treatment combined with mechanical treatment, e.g. mercerising with boron or compounds thereof, e.g. borides with boron oxides; with boric, meta- or perboric acids or their salts, e.g. with borax
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10BDESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B21/00Heating of coke ovens with combustible gases
    • C10B21/10Regulating and controlling the combustion
    • C10B21/14Devices for reversing the draught
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10BDESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B5/00Coke ovens with horizontal chambers
    • C10B5/10Coke ovens with horizontal chambers with heat-exchange devices
    • C10B5/12Coke ovens with horizontal chambers with heat-exchange devices with regenerators
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06BTREATING TEXTILE MATERIALS USING LIQUIDS, GASES OR VAPOURS
    • D06B17/00Storing of textile materials in association with the treatment of the materials by liquids, gases or vapours
    • D06B17/02Storing of textile materials in association with the treatment of the materials by liquids, gases or vapours in superimposed, i.e. stack-packed, form; J-boxes
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06LDRY-CLEANING, WASHING OR BLEACHING FIBRES, FILAMENTS, THREADS, YARNS, FABRICS, FEATHERS OR MADE-UP FIBROUS GOODS; BLEACHING LEATHER OR FURS
    • D06L1/00Dry-cleaning or washing fibres, filaments, threads, yarns, fabrics, feathers or made-up fibrous goods
    • D06L1/12Dry-cleaning or washing fibres, filaments, threads, yarns, fabrics, feathers or made-up fibrous goods using aqueous solvents
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06LDRY-CLEANING, WASHING OR BLEACHING FIBRES, FILAMENTS, THREADS, YARNS, FABRICS, FEATHERS OR MADE-UP FIBROUS GOODS; BLEACHING LEATHER OR FURS
    • D06L1/00Dry-cleaning or washing fibres, filaments, threads, yarns, fabrics, feathers or made-up fibrous goods
    • D06L1/12Dry-cleaning or washing fibres, filaments, threads, yarns, fabrics, feathers or made-up fibrous goods using aqueous solvents
    • D06L1/18Working under pressure in closed vessels
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06MTREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
    • D06M11/00Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with inorganic substances or complexes thereof; Such treatment combined with mechanical treatment, e.g. mercerising
    • D06M11/01Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with inorganic substances or complexes thereof; Such treatment combined with mechanical treatment, e.g. mercerising with hydrogen, water or heavy water; with hydrides of metals or complexes thereof; with boranes, diboranes, silanes, disilanes, phosphines, diphosphines, stibines, distibines, arsines, or diarsines or complexes thereof
    • D06M11/05Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with inorganic substances or complexes thereof; Such treatment combined with mechanical treatment, e.g. mercerising with hydrogen, water or heavy water; with hydrides of metals or complexes thereof; with boranes, diboranes, silanes, disilanes, phosphines, diphosphines, stibines, distibines, arsines, or diarsines or complexes thereof with water, e.g. steam; with heavy water
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06BTREATING TEXTILE MATERIALS USING LIQUIDS, GASES OR VAPOURS
    • D06B3/00Passing of textile materials through liquids, gases or vapours to effect treatment, e.g. washing, dyeing, bleaching, sizing, impregnating
    • D06B3/24Passing of textile materials through liquids, gases or vapours to effect treatment, e.g. washing, dyeing, bleaching, sizing, impregnating of fabrics in roped form

Definitions

  • This invention relates to a method of heating textile fibers and goods made therefrom while the goods are padded or dampened with a treating solution.
  • the goods in roped form have been immersed in or dampened with particular treating solutions adapted to perform certain processing steps and change the goods in a; desired fashion.
  • treating solutions adapted to perform certain processing steps and change the goods in a; desired fashion.
  • For heating of goods continuously in rope form various methods and devices are in use or have been proposed.
  • One method of imparting heat to dampened roped goods is to wet out the goods with the treating solution, remove the excess of the treating solution until th goods are damp and then I run the goods in the extended rope form through a heated atmosphere consisting of steam or hot air or a mixture of both. Thereafter the goods are piled into a suitable container to form a bulk in which form they remain until the desired reable container.
  • a heated atmosphere consisting of steam or hot air or a mixture of both.
  • the goods are piled into a suitable container to form a bulk in which form they remain until the desired reable container.
  • Such a method has similar disadvantages.
  • the solutions with which the goods are dampened do not maintain their original characteristics when subjected to high temperatures.
  • a further object of the invention is to provide a method of heating all types of goods .in bulk form at lowliquor ratio.
  • the present invention provides a method of heating goods continuously in rope form and at low liquor ratio producing goods of even characteristics at low cost and with simplified apparatus.
  • the following description illustrates the method of the invention.
  • the roped goods dampened with the .treating solution that is to say, containing suiilcient of the treating solution to perform the expected function thereof but having insufflcient treating solution to drip from the goods, are continuously passed into a heating chamber, of a type more fully described hereinsult is obtained.
  • a heating chamber of a type more fully described hereinsult is obtained.
  • Such a method requires cumand then pile the goods in bulk form in a suit-- to feed end of the heating chamber and out of con- I tact with the heating medium.
  • the dampened goods in rope form fall into the-feed end of the heating chamber and become packed therein, and due to the special construction of this chamber move from the feed end towards the discharge end, but at a rate considerably below the linear speed with which the rope is fed into the device. Due to the fact that the goods are damp they pack in and fill the heating chamber completely. In general, the movement of the packed goods in the heating chamber will be less than about of the rate of movement of
  • the goods in the chamber are heated by directsult.
  • the heating medium is directed upon the main bulk of the goods packed within the heating chamber as this bulk is moved at a relatively low rate of speed, as contrasted with the rate of feeding. Since the goods are continuously withdrawn from the chamber at the discharge end at substantially the same rate as they are fed into the chamber at the feed end, the packed goods move slowlytoward and past the point at which the heating medium is introduced and directed upon the bulkof the goods. It has been found that the goods packed into the chamber are heated up to the desired temperature quickly and uniformly.
  • the procedure produces evenness of heating and the goods are maintained in the..heated condition throughout the period of treatment, and are discharged from the chamber while still hot, the temperature in all parts of the chamber being substantially the same even though the heating medium beintroduced at only a restricted point or area of the heating chamber.
  • FIG. 1 is a side elevation of a species of the improved apparatus
  • Fig. 2 is an enlarged fragmentary portion of the device in front elevation showing the steam connection
  • vat l0 contains a treating solution ll into which goods 12 are fed in roped form;
  • the goods pass under guide bar l3 in order positively to submerge the goods in the solution and evenly and uniformly to impregnate and saturate the goods with the trea ing solution.
  • T e goods are drawn from the bath by means of a pair of squeezer rolls 14 which are set to a pressure to express excess of the treating solution from the goods and to leave 50% to 200% of the treating solution in the goods, based upon the dry weight of the goods.
  • the goods leaving rolls l4 are in the damp condition.
  • Piler or plaiter I5 is posPioncd above a combined J-ciute and heatng chamber I7, to be more fully described hereinafter. in such fashion that roped goods I2 pass in plaited form into the flared feed end l8 of chute I! from side to side as the plaiter l5 revolves about the axis I 9 and reciprocates along this axis.
  • the chut is tapered at 20 to facilitate tight packing of the goods.
  • a substantially vertical leg of the chute is provided below the tapered upper end 20 at 2
  • is joined at elbow 22 with an angularly positioned leg 23, the latter being connected with curved portion 24 terminating in the discharge end 25 of the completed chute.
  • the goods are removed from the chute by rolls 2'! and passed to additional treating apparatus, for instance, a washer, not shown.
  • Chute ll may be fabricated of or lined with any conventional material not adversely affected by the treating solution at the temperature of treatment, as, for instance, wood or metal.
  • the outside of the chute if fabricated from metal may be advantageously covered with insulation.
  • Chute I1 is provided adjacent its feed end motion are heated and goods below the connection are maintained at elevated temperature.
  • steam jacket 28 is attached to a side 34 of chute [1, although the jacket may surround the chute.
  • the jacket is attached to two opposite sides of the chute.
  • a side 34 of chute I! is shown having a band of spaced openings 35 through which the gaseous heating medium enters the interior of the chute to heat the contents thereof.
  • cap 40 is spaced from side wall 34 but attached thereto in any convenient fashion by flanges 4
  • Heating medium such as steam
  • the perforations constitute only a small fraction of the area of the chute and we have found that excellent and uniform heating is obtained with the perforated area of less than 3% of the total area of the chute.
  • a small J-chute was constructed with cross sectional dimension of 1.5 feet by 0.5 feet and a height Steam was admitted and a temperature of 212 F. was obtained and maintained in all parts of the goods, although steam was introduced only at a point adjacent the feed end.
  • Damp goods were continuously fed to the filled J-chute at a rate of three yards per minute and continuously withdrawn at the samerate.
  • the treating time was minutes at this rate of feed, which gave a continuous production of three yards per minute.
  • a J-chute having crosssectional dimensions of 6 feet by 1.5 feet and a total height of thirty feet allows for production of yards per minute or 180,000 yards per 24 hours with a treating time of '75 minutes. By increasing the rate of speed the treating time may be decreased or vice versa.
  • the method of heating textile goods in rope form which comprises piling the unheated rope of goods dampened with about 50% to 200% of treating solution into one end of a heating chamber having a feed end and a discharge end both open to the atmosphere, completely to fill the same and pack therein compactly, admitting steam freely to the chamber at a point sufliciently below the open ieedend to avoid loss of steam therethrough while the desired temperature is maintained throughout the goods and subjecting the so packed goods to the direct action of such steam while conthe other end of the chamber and continually adding dampened unheated goods thereto to be heated, whereby the goods move through the chamber by gravity and the chamber is substantially filled at all times with goods undergoing treatment.
  • the method of heating textile goods in rope tinually withdrawing the so heated goods from form which comprises feeding the unheated rope Y of goods dampened with 50% to 200% of treating solution at a regulated linear speed into one end of a heating chamber having a feed end and a discharge end both open to the atmosphere, completely to fill the same and pack therein compactly and removing the goods from the other end at substantially the same speed whereby the packed goods pass by gravity through the chamber at a linear speed of less than about /20 the linear speed of the goods fed to the chamber, positively feeding steam into the chamber at a point sufficiently below the open feed end to avoid loss of steam therethrough while the desired temperature is maintained throughout the goods, and subjecting the packed goods to the direct action of such steam during their passage through the chamber whereby the bulk of goods is heated to elevated treating temperatures as it moves gradually through the chamber.
  • I 4 The method of heating textile goods in rope form which comprises feeding an unheated rope of goods dampened with about 50 to 200% of treating solution into one end of a heating chamber having a feed end and a discharge end, the former being open to the atmosphere, completely to fill the same and 'pack therein compactly with a bulk of goods, positively directing heating steam into the chamber and into the bulk of goods at a. point about one-third of the length of the chamber from the feed end thereof to avoid loss of steam through such open feed end while the desired temperature is maintained throughout the goods and continuously withdrawing heated goods from the chamber through the discharge end at substantially the same rate as'unheated goods are fed to the chamber whereby the bulk of goods moves through the chamber by gravity at a rate of speed considerably less than the rate of feed.

Description

July 11, 1944. H. o. KAUFFMANN ET AL 2,353,615
METHOD OF HEATING GOODS Filed March 27, 1941 INVENTORS Patented July 11, 1944 METHOD OF HEATING GOODS Hans O. Kauifmann, Eggertsville, and Edward S Shanley, Buffalo, N. Y., assignors to Buffalo Electro-Chemical Company, Inc., Buffalo, N. Y.
Application March 27, 1941, Serial No. 385,576
4 Claims.
This invention relates to a method of heating textile fibers and goods made therefrom while the goods are padded or dampened with a treating solution.
In a great many steps of textile processing it is necessary to heat the goods. It is often necessary to obtain a high temperature in order to perform operations such as dyeing, bleaching, finishing, scouring, boiling, shrinking, etc. These operations may be performed on woven or.knit goods, on yarn or raw stock and in fact in any suitable stage of manufacturing the textile article from the rawto the finished goods. It is a great advantage to carry out such operations in a continuous manner for which purpose the goods must be attached together to form a con-, tinuous strand. This may be accomplished by sewing piece or knit goods end to end, by linking skeins of yarn or by transporting raw stock on a suitable conveyor. This is called the rope form. Goods in this roped form may be handled very conveniently and may be moved from place to place at high speed, it being common practice to transport goods at speeds of 100 to 300 yards per minute, depending upon the type and construction of the goods.
The goods in roped form have been immersed in or dampened with particular treating solutions adapted to perform certain processing steps and change the goods in a; desired fashion. For heating of goods continuously in rope form various methods and devices are in use or have been proposed.
One method of imparting heat to dampened roped goods is to wet out the goods with the treating solution, remove the excess of the treating solution until th goods are damp and then I run the goods in the extended rope form through a heated atmosphere consisting of steam or hot air or a mixture of both. Thereafter the goods are piled into a suitable container to form a bulk in which form they remain until the desired reable container. Such a method has similar disadvantages. Moreover, in many cases the solutions with which the goods are dampened do not maintain their original characteristics when subjected to high temperatures.
In these prior procedures the apparatus employed for handling and moving the goods has been enclosed in the heating chamber. 'The mechanical difiiculties, and the expensive devices that had to be employed, have militated against the introduction of the continuous treating of textiles in rope form at elevated temperatures.
Where goods in roped form are dampened with the treating solution and processed in the unheated solution, it has been common practice to feed and pile the unheated goods in a so-called J-chute. In hot processing, the goods were heated prior to their entrance into the J-chute or the J-chute was enclosed within a heating or steam chamber. In either procedure the devices for carrying out such processing are subjected to the above mentioned disadvantages.
It is an object of the invention to provide a procedure for continuously heating dampened roped goods in bulk form.
A further object of the invention is to provide a method of heating all types of goods .in bulk form at lowliquor ratio.
The present invention provides a method of heating goods continuously in rope form and at low liquor ratio producing goods of even characteristics at low cost and with simplified apparatus.
The following description illustrates the method of the invention. The roped goods dampened with the .treating solution, that is to say, containing suiilcient of the treating solution to perform the expected function thereof but having insufflcient treating solution to drip from the goods, are continuously passed into a heating chamber, of a type more fully described hereinsult is obtained. Such a method requires cumand then pile the goods in bulk form in a suit-- to feed end of the heating chamber and out of con- I tact with the heating medium. The dampened goods in rope form fall into the-feed end of the heating chamber and become packed therein, and due to the special construction of this chamber move from the feed end towards the discharge end, but at a rate considerably below the linear speed with which the rope is fed into the device. Due to the fact that the goods are damp they pack in and fill the heating chamber completely. In general, the movement of the packed goods in the heating chamber will be less than about of the rate of movement of the roped goods entering the feed end of the chamber.
The goods in the chamber are heated by directsult. The heating medium is directed upon the main bulk of the goods packed within the heating chamber as this bulk is moved at a relatively low rate of speed, as contrasted with the rate of feeding. Since the goods are continuously withdrawn from the chamber at the discharge end at substantially the same rate as they are fed into the chamber at the feed end, the packed goods move slowlytoward and past the point at which the heating medium is introduced and directed upon the bulkof the goods. It has been found that the goods packed into the chamber are heated up to the desired temperature quickly and uniformly. Thus the procedure produces evenness of heating and the goods are maintained in the..heated condition throughout the period of treatment, and are discharged from the chamber while still hot, the temperature in all parts of the chamber being substantially the same even though the heating medium beintroduced at only a restricted point or area of the heating chamber.
The drawing appended hereto illustrates a device suitable for carrying out the invention. Like reference characters designate like parts and Fig. 1 is a side elevation of a species of the improved apparatus;
Fig. 2 is an enlarged fragmentary portion of the device in front elevation showing the steam connection; and
Fig. 3 is a section on line 3 3 of'Fig. 2. Referring more particularly to the drawing, vat l0 contains a treating solution ll into which goods 12 are fed in roped form; The goods pass under guide bar l3 in order positively to submerge the goods in the solution and evenly and uniformly to impregnate and saturate the goods with the trea ing solution. T e goods are drawn from the bath by means of a pair of squeezer rolls 14 which are set to a pressure to express excess of the treating solution from the goods and to leave 50% to 200% of the treating solution in the goods, based upon the dry weight of the goods. The goods leaving rolls l4 are in the damp condition.
Goods leaving squeezer rolls l4pass to a rest 29 and then to plaiting device '5 of conventional type. and to this end rolls l6 are provided to pull the goods to this point. Piler or plaiter I5 is posPioncd above a combined J-ciute and heatng chamber I7, to be more fully described hereinafter. in such fashion that roped goods I2 pass in plaited form into the flared feed end l8 of chute I! from side to side as the plaiter l5 revolves about the axis I 9 and reciprocates along this axis.
Below the flared feed end It, the chut is tapered at 20 to facilitate tight packing of the goods. A substantially vertical leg of the chute is provided below the tapered upper end 20 at 2|, the weight of the packed goods inducing movement downwardly within the chute. This vertical leg 2| is joined at elbow 22 with an angularly positioned leg 23, the latter being connected with curved portion 24 terminating in the discharge end 25 of the completed chute. The goods are removed from the chute by rolls 2'! and passed to additional treating apparatus, for instance, a washer, not shown.
Chute ll may be fabricated of or lined with any conventional material not adversely affected by the treating solution at the temperature of treatment, as, for instance, wood or metal. The outside of the chute if fabricated from metal may be advantageously covered with insulation.
Chute I1 is provided adjacent its feed end motion are heated and goods below the connection are maintained at elevated temperature.
Referring to Fig. 2 and Fig. 3, steam jacket 28 is attached to a side 34 of chute [1, although the jacket may surround the chute. In the form illustrated, the jacket is attached to two opposite sides of the chute. Thus, in Fig. 2a side 34 of chute I! is shown having a band of spaced openings 35 through which the gaseous heating medium enters the interior of the chute to heat the contents thereof. In order to form a fluid tight chest, cap 40 is spaced from side wall 34 but attached thereto in any convenient fashion by flanges 4|.
Heating medium, such as steam, is admitted to the steam chestconstituting the space between cap 40 and side wall 34 through nipple 45 and is introduced to the interior of the chute through the band of perforations 35. The perforations constitute only a small fraction of the area of the chute and we have found that excellent and uniform heating is obtained with the perforated area of less than 3% of the total area of the chute.
The following are illustrations of the operation of the invention.
A small J-chute was constructed with cross sectional dimension of 1.5 feet by 0.5 feet and a height Steam was admitted and a temperature of 212 F. was obtained and maintained in all parts of the goods, although steam was introduced only at a point adjacent the feed end.
Damp goods were continuously fed to the filled J-chute at a rate of three yards per minute and continuously withdrawn at the samerate. The treating time was minutes at this rate of feed, which gave a continuous production of three yards per minute.
For larger production a J-chute having crosssectional dimensions of 6 feet by 1.5 feet and a total height of thirty feet allows for production of yards per minute or 180,000 yards per 24 hours with a treating time of '75 minutes. By increasing the rate of speed the treating time may be decreased or vice versa.
What is claimed is:
1. The method of heating textile goods in rope form which comprises piling the unheated rope of goods dampened with about 50% to 200% of treating solution into one end of a heating chamber having a feed end and a discharge end both open to the atmosphere, completely to fill the same and pack therein compactly, admitting steam freely to the chamber at a point sufliciently below the open ieedend to avoid loss of steam therethrough while the desired temperature is maintained throughout the goods and subjecting the so packed goods to the direct action of such steam while conthe other end of the chamber and continually adding dampened unheated goods thereto to be heated, whereby the goods move through the chamber by gravity and the chamber is substantially filled at all times with goods undergoing treatment.
2. The method of heating textile goods in rope tinually withdrawing the so heated goods from form which comprises feeding the unheated rope Y of goods dampened with 50% to 200% of treating solution at a regulated linear speed into one end of a heating chamber having a feed end and a discharge end both open to the atmosphere, completely to fill the same and pack therein compactly and removing the goods from the other end at substantially the same speed whereby the packed goods pass by gravity through the chamber at a linear speed of less than about /20 the linear speed of the goods fed to the chamber, positively feeding steam into the chamber at a point sufficiently below the open feed end to avoid loss of steam therethrough while the desired temperature is maintained throughout the goods, and subjecting the packed goods to the direct action of such steam during their passage through the chamber whereby the bulk of goods is heated to elevated treating temperatures as it moves gradually through the chamber.
ficiently below the open feed end of the chamber to avoid loss of steam through such open feed end while the desired temperature is maintained throughout the goods and continuously withdrawing heated goods from the chamber through the discharge end at substantially the same rate as unheated goods are fed to the chamber whereby the bulk of goods moves through the chamber by gravity at a rate of speed considerably less than the rate of feed.
I 4. The method of heating textile goods in rope form which comprises feeding an unheated rope of goods dampened with about 50 to 200% of treating solution into one end of a heating chamber having a feed end and a discharge end, the former being open to the atmosphere, completely to fill the same and 'pack therein compactly with a bulk of goods, positively directing heating steam into the chamber and into the bulk of goods at a. point about one-third of the length of the chamber from the feed end thereof to avoid loss of steam through such open feed end while the desired temperature is maintained throughout the goods and continuously withdrawing heated goods from the chamber through the discharge end at substantially the same rate as'unheated goods are fed to the chamber whereby the bulk of goods moves through the chamber by gravity at a rate of speed considerably less than the rate of feed.
US385576A 1939-03-29 1941-03-27 Method of heating goods Expired - Lifetime US2353615A (en)

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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2476262A (en) * 1946-06-13 1949-07-12 Rhode Island Lace Works Inc Dividing sheet fabric into strips
US2858184A (en) * 1955-10-05 1958-10-28 Du Pont Heating textile fabrics
US3351338A (en) * 1965-08-18 1967-11-07 Johnson & Johnson Apparatus for transporting and folding a collagen casing
US3457029A (en) * 1967-08-12 1969-07-22 Ilma Ind Lavorazioni Metalli A Apparatus and process for continuously steaming textile fiber materials
US3680334A (en) * 1971-01-20 1972-08-01 Phillips Petroleum Co Apparatus having chamber of oval cross-section for heat treating largedenier tow

Families Citing this family (23)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2433370A (en) * 1940-04-24 1947-12-30 Buffalo Electro Chem Co Method of scouring cellulosic materials
US2521340A (en) * 1945-05-16 1950-09-05 Olin Mathieson Bleaching of cellulosic textiles
US2499987A (en) * 1945-12-18 1950-03-07 Harris Res Lab Process for imparting shrink resistance to wool
US2515532A (en) * 1947-05-28 1950-07-18 Diamond Alkali Co Method of bleaching textiles
US2529991A (en) * 1947-06-18 1950-11-14 Rodney Hunt Machine Co Plaiter
US2554090A (en) * 1947-06-21 1951-05-22 Greenville Steel & Foundry Com Continuous bleaching apparatus
US2653466A (en) * 1948-02-21 1953-09-29 Native Laces & Textiles Inc Apparatus for separating pieces of fabric joined by soluble threads
US2602723A (en) * 1949-09-20 1952-07-08 Allied Chem & Dye Corp Continuous hypochlorite process for bleaching cotton textiles
US2661619A (en) * 1950-01-17 1953-12-08 Chemstrand Corp Apparatus for the fluid treatment of fibers and the like
DE941189C (en) * 1952-10-28 1956-04-05 Maurice Decloux Finishing and washing machine for fabrics
NL97827C (en) * 1953-01-20
US2960752A (en) * 1955-11-04 1960-11-22 American Cyanamid Co Method for producing a crimped tow
GB808518A (en) * 1955-11-04 1959-02-04 American Cyanamid Co Tow of polyacrylonitrile filamentary material and production thereof
US2839353A (en) * 1956-04-26 1958-06-17 Du Pont High speed peroxide textile bleaching process
US2953429A (en) * 1957-02-11 1960-09-20 Best Feeds & Farm Supplies Inc Method for sterilizing granular food
DE1271070B (en) * 1957-03-07 1968-06-27 Kleinewefers Soehne J Method and device for the continuous washing of chemicals from continuous web-shaped textile material
US3078542A (en) * 1959-07-31 1963-02-26 Midland Ross Corp Continuous filament bulked yarn in tow form
US3066006A (en) * 1960-04-29 1962-11-27 American Cyanamid Co Method of processing a tow
US3409919A (en) * 1965-09-28 1968-11-12 Burlington Industries Inc Process for treating textile material sequentially in a series of liquid treatments
US3377825A (en) * 1965-10-14 1968-04-16 Sando Yoshikazu Liquid treating apparatus for a cotton belt
US3991481A (en) * 1975-05-28 1976-11-16 E. I. Du Pont De Nemours And Company Process for recovering volatile organic liquids
TW201610261A (en) * 2014-05-20 2016-03-16 喬治亞太平洋消費者產品公司 Bleaching and shive reduction process for non-wood fibers
TW201544652A (en) 2014-05-20 2015-12-01 Georgia Pacific Consumer Prod Bleaching and shive reduction process for non-wood fibers

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE561481C (en) * 1927-02-26 1932-10-14 Elektrochem Werke Muenchen Ag Process for bleaching textile goods and fibers of all kinds with hydrogen peroxide

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2476262A (en) * 1946-06-13 1949-07-12 Rhode Island Lace Works Inc Dividing sheet fabric into strips
US2858184A (en) * 1955-10-05 1958-10-28 Du Pont Heating textile fabrics
US3351338A (en) * 1965-08-18 1967-11-07 Johnson & Johnson Apparatus for transporting and folding a collagen casing
US3457029A (en) * 1967-08-12 1969-07-22 Ilma Ind Lavorazioni Metalli A Apparatus and process for continuously steaming textile fiber materials
US3680334A (en) * 1971-01-20 1972-08-01 Phillips Petroleum Co Apparatus having chamber of oval cross-section for heat treating largedenier tow

Also Published As

Publication number Publication date
DE898438C (en) 1953-11-30
NL97389C (en) 1900-01-01
FR945647A (en) 1949-05-10
US2267718A (en) 1941-12-30
BE438417A (en) 1900-01-01
NL54898C (en) 1900-01-01
GB542413A (en) 1942-01-08

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