US3881222A - Method and apparatus for controlling the moisture content of fibrous stock - Google Patents
Method and apparatus for controlling the moisture content of fibrous stock Download PDFInfo
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- US3881222A US3881222A US417013A US41701373A US3881222A US 3881222 A US3881222 A US 3881222A US 417013 A US417013 A US 417013A US 41701373 A US41701373 A US 41701373A US 3881222 A US3881222 A US 3881222A
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- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01G—PRELIMINARY TREATMENT OF FIBRES, e.g. FOR SPINNING
- D01G99/00—Subject matter not provided for in other groups of this subclass
- D01G99/005—Conditioning of textile fibre during treatment before spinning
Definitions
- Moisture is added to the fibrous stock at a second point located upstream of the first point.
- the amount of moisture which is added to the stock is in accordance with the signal generated at the first point and the fibrous stock is mixed after it has been conveyed past the first point.
- the present invention relates generally to moisture control for textile fibers and more specifically to moisture control during fiber processing.
- the ultimate responsibility for correcting the moisture content if the fibrous stock to a desired value lies with the fiber processer who handles the stock after the ginning operation. During all subsequent processing stages, the machines must produce products of a given weight per unit length.
- a recent attempt to overcome this difficulty has been the provision of a continuous moisture detecting apparatus for the fibrous stock in the opened state. This is accomplished by passing a batt of opened fibers or lap between a pair of electrical contacts which measures the resistance or impedance therebetween and generating a signal which varies with the resistance. This signal is then utilized to operate a moisturizing system which controls the relative humidity in the entire room in which the batt or lap forming machinery is located.
- a moisturizing system which controls the relative humidity in the entire room in which the batt or lap forming machinery is located.
- the object of the invention is accomplished by providing means for and method of forming the fibrous stock into a batt, measuring the moisture content of the batt, adding moisture directly to the opened stock at a point directly upstream of the point of measurement in accordance with the measured moisture content and opening, mixing and blending the fibrous stock after the addition of moisture.
- the desired amount of moisture is added directly to the fibrous stock and is absorbed during the subsequent processing stages.
- a gradient in moisture content may exist from one side of the batt to the other. This is overcome by mixing and blending the moisturized stock, which achieves a uniformity of moisture content for additional fiber processing stages.
- the opened stock is then mixed prior to being formed into a batt. This raises the moisture content of the fibrous stock to an intermediate level before it is formed into a batt.
- the additional moisturizing stage serves to top off the addition of moisture at a controlled value. This minimizes the moisture gradient through the batt at the point that it is sensed. This approach is most desirable with types of fibrous stock which are highly variable in initial moisture content and with stock to which it may be necessary to add a relatively large amount of moisture.
- FIG. I is a diagramatic plan view of the preferred embodiment of the invention.
- FIG. 2 is a diagramatic side elevation. looking in the direction of arrow 2 in FIG. I;
- FIG. 3 is a plan view of the moisture detecting means on an enlarged scale
- FIG. 4 is a fragmentary view of first modification
- FIG. 5 is a fragmentary view of a second modification.
- FIGS. I and 2 a conventional fiber processing mill is schematically illustrated and is divided into an opening room and a fiber processing room 12.
- the fibrous stock to be processed is derived from bales I4 arranged in rows on the floor of the opening room.
- the bales 14 are fed into hoppers 16 of a typical opening, blending and mixing mechanism I8.
- Mechanism 18 may be any of the many types which are available, an example of which is shown in US. Pat. No. 2,885,741 to Leineweber, .Ir. dated May l2, I959.
- the stock emerges from mechanism 18 as a loose substantially fluffy fibrous mass. This mass is drawn through a conveyor duct 20 by a fan l9 to a cleaning apparatus 22 which cleans and mixes the stock.
- An example of such an apparatus is shown in US. Pat. No. 3,046,6l2 to Kyame et al dated July 3i, I962.
- batt forming machine 24 such as a picker which converts the stock into a batt or lap 26.
- Batt forming machine 24 may also comprise apparatus as shown in my U.S. Pat. No. 3,562,866 dated Feb. 16, 1971. Only one batt forming machine 24 is shown but it is to be understood that a plurality of such machines would normally be employed.
- Batt 26 is deposited on a foraminous conveyor 28 which conveys the batt in the direction of arrow 30 toward a mixing apparatus 32, an example of which is shown in U.S. Pat No. 3.051.998 to Rust, Jr.. et al.. dated Sept. 4. I962.
- Apparatus 32 breaks the batt into loose fibers, mixes the fibers and deposits them onto a second conveyor 34 as a mass of fluffy fibers indicated at 36. This mass of fibers is conveyed in the direction of arrow 38 to subsequent fiber processing apparatus.
- Sensing means 40 includes a plurality of sensing fingers 42a and 42b alternately mounted on an insulated support 44 in contact with batt 26. Fingers 42a and 42b are connected to terminals of opposite polarity in a control unit 46 and function as contacts for the small current flow between the fingers 42a and 42b. Variations in fiber moisture causes changes in the electrical resistance between sensing fingers which is reflected by changes in current flow. The greater the moisture content. the greater the current flow. Fingers 42a and 42b are arranged across the width of the batt so that the total current flow between each finger and its adjacent finger or fingers is indicative of the average moisture content across the width of the batt.
- This total current flow represents a signal which is amplified by control unit 46 to an output signal for controlling an electromechanical actuator 47 for a proportional valve 48 which controls steam flow from a source of steam, not shown, to upper and lower multi-ported steam nozzles 50 and 52, respectively via pipes 53.
- Nozzle 52 is located just beneath the upper run of conveyor 28 and directs steam through the foraminous conveyor to the lower face of the batt 26.
- Nozzle 50 directs steam to the upper face of the batt.
- Valve 48 is controlled by unit 46 so that as the total current flow between sensing fingers 42a and 42b decreases the amount of steam to nozzles 50 and 52 increases.
- a preliminary moisturizing system is employed to add moisture to the fibers while they are in the baled state.
- the preliminary moisturizing system is indicated generally at 54 and comprises spray nozzles 56 located just over the bales 14 which are arranged in rows on the floor of the opening room 10. Spray nozzles 56 are located over the bales 14 so that they will spray moisture in the form of water directly onto the bales. Moisture is supplied to nozzles 56 from a valve 58 through pipes 60. Moisture is supplied to valve 58 from a supply source. not shown.
- Valve 58 may be a proportional valve such as 48 and controlled by unit 46 which acts through an electro-mechanical actuator 59 or simply an open-shut" valve which is opened when the measured moisture content of the batt falls below a predetermined value. Regardless of what type of valve is used. the amount of moisture which is added to the bales is less than required to bring the moisture content of the fibers to the desired value. The moisture which is added to the bales is not absorbed uniformly throughout the bales but by the time the bales are opened and the fibers mixed. cleaned and formed into a batt 26, the moisture content of the fibrous stock is substantially uniform. The addition of moisture by the steam nozzles 50 and 52 represents a topping off" stage to bring the moisture content to a predetermined value. Control unit 46 may be adjusted by a rheostat 62 so that more or less moisture will be added for a given total measured current between the fingers 42a and 42!).
- FIG. 4 there is shown a modified appa ratus for adding moisture to the batt 26 between the sensing means 40 and picker 24.
- This apparatus is indicated generally at 64 and includes a multi-ported spray head 66 which is located above and extends across the upper face of the batt 26.
- the flow of moisture to spray head 66 is regulated by a proportional valve 68 which is controlled by unit 46 through an electro-mechanical actuator 69 in the same manner as valve 48 and actuator 47.
- moisture is added to the fibrous stock as it is being conveyed in the duct 20 by moisturizing apparatus generally indicated by the reference numeral 70.
- This apparatus comprises a housing 72 which forms part of the conveyor duct 20 and an atomizing spray head 74 which extends through the wall of the housing.
- Moisture is supplied to the spray head 74 from a source of supply, not shown, through a proportional valve 76.
- Pressurized air is supplied to spray head 74 from a hose 78.
- Valve 76 is automatically adjusted by an electro-mechanical actuator 77 which is controlled by unit 46 in the same manner as valves 48 and actuator 47.
- Moisturizing apparatus may be used as the primary moisturizing apparatus in place of nozzles 50 and 52 and used in combination with these nozzles as a preliminary moisturizing system in which case it can be used instead of spray nozzles 56 or in addition to these nozzles.
- a process for controlling the moisture content of fibrous stock processed from bales which comprises:
- Moisture control apparatus for processing of fibrous stock from bales. comprising:
- control means connected to said means for applying moisture and to said sensing means for applying moisture to said batt in accordance with the signal generated by said sensing means;
- g. means for disintegrating and mixing said fibrous batt after it has been conveyed past said first point.
- a proportional valve located between said source of steam and said nozzles under control of said control means.
- a process for controlling the moisture content of 5 fibrous stock processed from bales which comprises:
- a process for controlling the moisture content of fibrous stock processed from bales which comprises:
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Abstract
Moisture control method and apparatus for processing of textile fibrous stock whereby bales of stock are opened and formed into a uniform batt which is conveyed past a first point whereupon the moisture content of the batt is sensed and a signal is generated which varies with variations in the moisture content of the batt. Moisture is added to the fibrous stock at a second point located upstream of the first point. The amount of moisture which is added to the stock is in accordance with the signal generated at the first point and the fibrous stock is mixed after it has been conveyed past the first point.
Description
United States Patent 1191 1111 3,881,222
Roberson 1 1 May 6, 1975 METHOD AND APPARATUS FOR 3,005,238 10/1961 Manning 19/66 R CONTROLIJNG THE MOISTURE CONTENT 3,821,833 7/1974 Wildbolz et a1 19/66 R OF FIBROUS STOCK [75] Inventor: James H. Roberson, Greenville, SC.
[73] Assignee: Crompton & Knowles Corporation, Worcester, Mass.
[22] Filed: Nov. 19, 1973 [21] Appl. No.: 417,013
[52] US. Cl 19/66 R [51] Int. Cl D01b 3/04 [58] Field of Search 19/66 R, 105; 236/44 R [56] References Cited UNITED STATES PATENTS 2,079,407 5 1937 Hess 1. 19/105 2,155,598 4/1939 Holt et al 19/[05 X Primary Examiner Dorsey Newton {57] ABSTRACT Moisture control method and apparatus for processing of textile fibrous stock whereby bales of stock are opened and formed into a uniform batt which is conveyed past a first point whereupon the moisture content of the ham is sensed and a signal is generated which varies with variations in the moisture content of the batt. Moisture is added to the fibrous stock at a second point located upstream of the first point. The amount of moisture which is added to the stock is in accordance with the signal generated at the first point and the fibrous stock is mixed after it has been conveyed past the first point.
1 l I E i l l i l METHOD AND APPARATUS FOR CONTROLLING THE MOISTURE CONTENT OF FIBROUS STOCK BACKGROUND OF THE INVENTION The present invention relates generally to moisture control for textile fibers and more specifically to moisture control during fiber processing.
It has long been recognized that the moisture content of fibers plays a very important role in the processing and handling characteristics of fibers. If the fibers are too dry, static electrical charges build up which causes the fibers to stick to the various mechanisms and cause jams. Dry fibers are also apt to be brittle and more likely to rupture during handling. If the fibers have too little moisture, the forces or power required to open, separate or otherwise handle the stock increases significantly.
There is some attempt to control the moisture content during ginning but precise control of the moisture content is not too important as long as it isnt too wet."
The ultimate responsibility for correcting the moisture content if the fibrous stock to a desired value lies with the fiber processer who handles the stock after the ginning operation. During all subsequent processing stages, the machines must produce products of a given weight per unit length.
Most mills begin the moisture conditioning process in the opening room by laying down" fibrous stock and controlling the relative humidity to a desired value. A major weakness of this conditioning procedure is that it is too slow. At high production rates there is in sufficient time for the stock to reach true equilibrium since it is difficult to exchange moisture between the atmosphere and the bales. A longer exposure period could be obtained by increasing the floor space available for an increase in the amount of laydown. This is, of course, not very economical and also increases the plant's air conditioning load.
A recent attempt to overcome this difficulty has been the provision of a continuous moisture detecting apparatus for the fibrous stock in the opened state. This is accomplished by passing a batt of opened fibers or lap between a pair of electrical contacts which measures the resistance or impedance therebetween and generating a signal which varies with the resistance. This signal is then utilized to operate a moisturizing system which controls the relative humidity in the entire room in which the batt or lap forming machinery is located. An example of such a system is illustrated in US. Pat. No. 3,005,238 to C. R. Manning, dated Oct. 24, 1961. This system is still time dependent. The opened fibers will absorb moisture from the atmosphere at a greater rate than fibers in the baled state but not at a rate sufficient for present day rates of production. There is a considerable time lag between the detection of a moisture content below a set value and the raising of the moisture content to that value by the moisturizing system. This results in fluctuations of the moisture content of the batt of fibers as it is processed.
SUMMARY OF THE INVENTION It is a principle object of the invention to overcome the disadvantages and problems encountered in present day moisture control systems for fibrous stock.
The object of the invention is accomplished by providing means for and method of forming the fibrous stock into a batt, measuring the moisture content of the batt, adding moisture directly to the opened stock at a point directly upstream of the point of measurement in accordance with the measured moisture content and opening, mixing and blending the fibrous stock after the addition of moisture. In this way the desired amount of moisture is added directly to the fibrous stock and is absorbed during the subsequent processing stages. A gradient in moisture content may exist from one side of the batt to the other. This is overcome by mixing and blending the moisturized stock, which achieves a uniformity of moisture content for additional fiber processing stages.
It is a further object of the invention to also provide means, responsive to the sensing means, for moisturizing the fibrous stock while it is still in the baled state. The opened stock is then mixed prior to being formed into a batt. This raises the moisture content of the fibrous stock to an intermediate level before it is formed into a batt. The additional moisturizing stage serves to top off the addition of moisture at a controlled value. This minimizes the moisture gradient through the batt at the point that it is sensed. This approach is most desirable with types of fibrous stock which are highly variable in initial moisture content and with stock to which it may be necessary to add a relatively large amount of moisture.
BRIEF DESCRIPTION OF THE DRAWINGS FIG. I is a diagramatic plan view of the preferred embodiment of the invention;
FIG. 2 is a diagramatic side elevation. looking in the direction of arrow 2 in FIG. I;
FIG. 3 is a plan view of the moisture detecting means on an enlarged scale;
FIG. 4 is a fragmentary view of first modification; and
FIG. 5 is a fragmentary view of a second modification.
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT Referring to FIGS. I and 2, a conventional fiber processing mill is schematically illustrated and is divided into an opening room and a fiber processing room 12.
The fibrous stock to be processed is derived from bales I4 arranged in rows on the floor of the opening room. The bales 14 are fed into hoppers 16 of a typical opening, blending and mixing mechanism I8. Mechanism 18 may be any of the many types which are available, an example of which is shown in US. Pat. No. 2,885,741 to Leineweber, .Ir. dated May l2, I959. The stock emerges from mechanism 18 as a loose substantially fluffy fibrous mass. This mass is drawn through a conveyor duct 20 by a fan l9 to a cleaning apparatus 22 which cleans and mixes the stock. An example of such an apparatus is shown in US. Pat. No. 3,046,6l2 to Kyame et al dated July 3i, I962. The stock is then conveyed from the cleaning apparatus 22 to batt forming machine 24 such as a picker which converts the stock into a batt or lap 26. Batt forming machine 24 may also comprise apparatus as shown in my U.S. Pat. No. 3,562,866 dated Feb. 16, 1971. Only one batt forming machine 24 is shown but it is to be understood that a plurality of such machines would normally be employed.
Means for sensing the moisture content ofthe batt 26 are generally indicated at 40, see also FIG. 3. Sensing means 40 includes a plurality of sensing fingers 42a and 42b alternately mounted on an insulated support 44 in contact with batt 26. Fingers 42a and 42b are connected to terminals of opposite polarity in a control unit 46 and function as contacts for the small current flow between the fingers 42a and 42b. Variations in fiber moisture causes changes in the electrical resistance between sensing fingers which is reflected by changes in current flow. The greater the moisture content. the greater the current flow. Fingers 42a and 42b are arranged across the width of the batt so that the total current flow between each finger and its adjacent finger or fingers is indicative of the average moisture content across the width of the batt. This total current flow represents a signal which is amplified by control unit 46 to an output signal for controlling an electromechanical actuator 47 for a proportional valve 48 which controls steam flow from a source of steam, not shown, to upper and lower multi-ported steam nozzles 50 and 52, respectively via pipes 53. Nozzle 52 is located just beneath the upper run of conveyor 28 and directs steam through the foraminous conveyor to the lower face of the batt 26. Nozzle 50 directs steam to the upper face of the batt. Valve 48 is controlled by unit 46 so that as the total current flow between sensing fingers 42a and 42b decreases the amount of steam to nozzles 50 and 52 increases.
Under certain conditions where a higher moisture level is desired or extra dry fibers are being processed, a preliminary moisturizing system is employed to add moisture to the fibers while they are in the baled state. The preliminary moisturizing system is indicated generally at 54 and comprises spray nozzles 56 located just over the bales 14 which are arranged in rows on the floor of the opening room 10. Spray nozzles 56 are located over the bales 14 so that they will spray moisture in the form of water directly onto the bales. Moisture is supplied to nozzles 56 from a valve 58 through pipes 60. Moisture is supplied to valve 58 from a supply source. not shown. Valve 58 may be a proportional valve such as 48 and controlled by unit 46 which acts through an electro-mechanical actuator 59 or simply an open-shut" valve which is opened when the measured moisture content of the batt falls below a predetermined value. Regardless of what type of valve is used. the amount of moisture which is added to the bales is less than required to bring the moisture content of the fibers to the desired value. The moisture which is added to the bales is not absorbed uniformly throughout the bales but by the time the bales are opened and the fibers mixed. cleaned and formed into a batt 26, the moisture content of the fibrous stock is substantially uniform. The addition of moisture by the steam nozzles 50 and 52 represents a topping off" stage to bring the moisture content to a predetermined value. Control unit 46 may be adjusted by a rheostat 62 so that more or less moisture will be added for a given total measured current between the fingers 42a and 42!).
Referring to P16. 4, there is shown a modified appa ratus for adding moisture to the batt 26 between the sensing means 40 and picker 24. This apparatus is indicated generally at 64 and includes a multi-ported spray head 66 which is located above and extends across the upper face of the batt 26. The flow of moisture to spray head 66 is regulated by a proportional valve 68 which is controlled by unit 46 through an electro-mechanical actuator 69 in the same manner as valve 48 and actuator 47.
Referring to FIG. 5, there is shown a still further modification. in this modification moisture is added to the fibrous stock as it is being conveyed in the duct 20 by moisturizing apparatus generally indicated by the reference numeral 70. This apparatus comprises a housing 72 which forms part of the conveyor duct 20 and an atomizing spray head 74 which extends through the wall of the housing. Moisture is supplied to the spray head 74 from a source of supply, not shown, through a proportional valve 76. Pressurized air is supplied to spray head 74 from a hose 78. Valve 76 is automatically adjusted by an electro-mechanical actuator 77 which is controlled by unit 46 in the same manner as valves 48 and actuator 47. Moisturizing apparatus may be used as the primary moisturizing apparatus in place of nozzles 50 and 52 and used in combination with these nozzles as a preliminary moisturizing system in which case it can be used instead of spray nozzles 56 or in addition to these nozzles.
Having now described my invention. I claim:
1. A process for controlling the moisture content of fibrous stock processed from bales which comprises:
a. opening said bales of fibrous stock;
b. forming said opened stock into a substantially uniform batt;
c. sensing the moisture content of said batt at a first point; and
d. applying moisture directly to said batt at a second point located upstream of said first point in accordance with the sensed moisture content at said first point.
2. The process as set forth in claim I, which further comprises:
a. adding moisture to said bales when the moisture content sensed at said first point is below a designated value; and
b. mixing said opened stock before it is formed into said batt.
3. The process as set forth in claim 1 wherein said moisture is added to said batt and said process further comprises:
a. adding moisture to said opened fibrous stock before it is formed into said batt when the moisture content sensed at said first point is below a designated value; and
b. mixing said opened stock before it is formed into said batt.
4. Moisture control apparatus for processing of fibrous stock from bales. comprising:
a. means for continuously opening said bales of fibrous stock;
b. means for forming a substantially uniform batt from said opened stock;
c. means for conveying said batt;
d. means for sensing the moisture content of said batt as it is conveyed past a first point and for generating a signal which varies with variations in the moisture content of said batt;
e. means for applying moisture directly to said batt at a second point located upstream of said first point;
f. control means connected to said means for applying moisture and to said sensing means for applying moisture to said batt in accordance with the signal generated by said sensing means; and
g. means for disintegrating and mixing said fibrous batt after it has been conveyed past said first point.
5. The moisture control apparatus as set forth in claim 4, wherein the means for applying moisture to said batt comprises:
a. a source of steam;
b. a plurality of steam nozzles located at said second point for directing steam into said batt; and
c. a proportional valve located between said source of steam and said nozzles under control of said control means.
6. The moisture control apparatus as set forth in claim 5, wherein there are a plurality of said steam nozzles for directing steam into opposite faces of said batt.
7. The moisture control apparatus as set forth in claim 4, comprising:
a. an opening room for containing said bales of ti brous stock;
b. means connected to said control means for adding moisture to said bales; and
c. means for mixing said opened stock before it is formed into said batt.
8. A process for controlling the moisture content of 5 fibrous stock processed from bales which comprises:
a. opening said bales of fibrous stock;
b. forming said opened stock into a substantially uniform batt;
c. sensing the moisture content of said batt at a first point;
d. applying steam directly to said batt at a second point located upstream of said first point in accordance with the sensed moisture content at said first point; and
e. disintegrating said batt and mixing said fibrous stock obtained therefrom.
9. A process for controlling the moisture content of fibrous stock processed from bales which comprises:
a. opening said bales of fibrous stock;
b. forming said opened stock into a substantially uniform batt;
c. sensing the moisture content of said batt at a first point;
d. applying steam to opposite faces of said batt upstream of said first point; and
e. disintegrating said batt and mixing said fibrous stock obtained therefrom.
Claims (9)
1. A process for controlling the moisture content of fibrous stock processed from bales which comprises: a. opening said bales of fibrous stock; b. forming said opened stock into a substantially uniform batt; c. sensing the moisture content of said batt at a first point; and d. applying moisture directly to said batt at a second point located upstream of said first point in accordance with the sensed moisture content at said first point.
2. The process as set forth in claim 1, which further comprises: a. adding moisture to said bales when the moisture content sensed at said first point is below a designated value; and b. mixing said opened stock before it is formed into said batt.
3. The process as set forth in claim 1 wherein said moisture is added to said batt and said process further comprises: a. adding moisture to said opened fibrous stock before it is formed into said batt when the moisture content sensed at said first point is below a designated value; and b. mixing said opened stock before it is formed into said batt.
4. Moisture control apparatus for processing of fibrous stock from bales, comprising: a. means for continuously opening said bales of fibrous stock; b. means for forming a substantially uniform batt from said opened stock; c. means for conveying said batt; d. means for sensing the moisture content of said batt as it is conveyed past a first point and for generating a signal which varies with variations in the moisture content of said batt; e. means for applying moisture directly to said batt at a second point located upstream of said first point; f. control means connected to said means for applying moisture and to said sensing means for applying moisture to said batt in accordance with the signal generated by said sensing means; and g. means for disintegrating and mixing said fibrous batt after it has been conveyed past said first point.
5. The moisture control apparatus as set forth in claim 4, wherein the means for applying moisture to said batt comprises: a. a source of steam; b. a plurality of steam nozzles located at said second point for directing steam into said batt; and c. a proportional valve located between said source of steam and said nozzles under control of said control means.
6. The moisture control apparatus as set forth in claim 5, wherein there are a plurality of said steam nozzles for directing steam into opposite faces of said batt.
7. The moisture control apparatus as set forth in claim 4, comprising: a. an opening room for containing said bales of fibrous stock; b. means connected to said control means for adding moisture to said bales; and c. means for mixing said opened stock before it is formed into said batt.
8. A process for controlling the moisture content of fibrous stock processed from bales which comprises: a. opening said bales of fibrous stock; b. forming said opened stock into a substantially uniform batt; c. sensing the moisture content of said batt at a first point; d. applying steam directly to said batt at a second point located upstream of said first point in accordance with the sensed moisture content at said first point; and e. disintegrating said batt and mixing said fibrous stock obtained therefrom.
9. A process for controlling the moisture content of fibrous stock processed from bales which comprises: a. opening said bales of fibrous stock; b. forming said opened stock into a substantially uniform batt; c. sensing the moisture content of said batt at a first point; d. applying steam to opposite faces of said batt upstream of said first point; and e. disintegrating said batt and mixing said fibrous stock obtained therefrom.
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US4074546A (en) * | 1976-11-24 | 1978-02-21 | Crompton & Knowles Corporation | Fluid treating system for textile fibers |
US4103397A (en) * | 1977-01-03 | 1978-08-01 | Jackson Samuel G | Lint slide grid humidifier |
US4140503A (en) * | 1978-01-19 | 1979-02-20 | Vandergriff Arvel L | Vapor condenser and lint humidifier system |
US4527306A (en) * | 1982-07-31 | 1985-07-09 | Trutzschler Gmbh & Co. Kg | Spinning preparation system and method for air-conditioning the same |
EP0191713A1 (en) * | 1985-01-10 | 1986-08-20 | Australian Wool Corporation | Conditioning baled material |
US4726096A (en) * | 1986-09-19 | 1988-02-23 | Farmers Gin And Grain Of Humboldt, Inc. | Electric moisture control device for cotton gin |
EP0275812A1 (en) * | 1986-12-23 | 1988-07-27 | Australian Wool Corporation | Conditioning of baled materials |
EP0412446A1 (en) * | 1989-08-10 | 1991-02-13 | Maschinenfabrik Rieter Ag | Method to influence the conditioning of fibre processing in a spinning machine |
US5052080A (en) * | 1988-06-23 | 1991-10-01 | Maschinenfabrik Rieter, Ag | Method and apparatus for controlling yarn preparation operations to enhance product uniformity |
EP0459828A1 (en) * | 1990-06-01 | 1991-12-04 | E.I. Du Pont De Nemours And Company | Method for baling cut fibers and product |
US5121522A (en) * | 1989-12-22 | 1992-06-16 | Trutzschler Gmbh & Co., Kg | Humidity and temperature air conditioning in a textile processing line |
US5361450A (en) * | 1992-12-31 | 1994-11-08 | Zellweger Uster, Inc. | Direct control of fiber testing or processing performance parameters by application of controlled, conditioned gas flows |
US6237195B1 (en) * | 2000-03-14 | 2001-05-29 | Thomas R. Shoemaker | Fiber moisture cell for humidifying cotton and method |
US20060141260A1 (en) * | 2004-12-29 | 2006-06-29 | Enamul Haque | Sandwich composite material using an air-laid process and wet glass |
US20060137798A1 (en) * | 2004-12-29 | 2006-06-29 | Enamul Haque | Polymer/WUCS mat for use in sheet molding compounds |
US20060137799A1 (en) * | 2004-12-29 | 2006-06-29 | Enamul Haque | Thermoplastic composites with improved sound absorbing capabilities |
US20080050571A1 (en) * | 2004-12-28 | 2008-02-28 | Enamul Haque | Polymer/WUCS mat for use in automotive applications |
US20080057283A1 (en) * | 2006-08-29 | 2008-03-06 | Arthur Blinkhorn | Reinforced acoustical material having high strength, high modulus properties |
US20080251187A1 (en) * | 2003-10-17 | 2008-10-16 | Enamul Haque | Composite material with improved structural, acoustic and thermal properties |
US20110121482A1 (en) * | 2003-10-17 | 2011-05-26 | Roekens Bertrand J | Methods of forming low static non-woven chopped strand mats |
US20200299870A1 (en) * | 2017-11-14 | 2020-09-24 | Autefa Solutions Germany Gmbh | Monitoring process for nonwoven fabrication plants |
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US2079407A (en) * | 1933-11-03 | 1937-05-04 | Rieter Joh Jacob & Cie Ag | Card feeding device |
US2155598A (en) * | 1936-05-29 | 1939-04-25 | Holt Thomas William | Production of slivers from textile fibers |
US3005238A (en) * | 1957-06-04 | 1961-10-24 | Deering Milliken Res Corp | Moisture control arrangement and method |
US3821833A (en) * | 1968-04-16 | 1974-07-02 | Rieter Ag Maschf | Apparatus for supplying cards by means of a pneumatic flock transporting system |
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1973
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Publication number | Priority date | Publication date | Assignee | Title |
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US2079407A (en) * | 1933-11-03 | 1937-05-04 | Rieter Joh Jacob & Cie Ag | Card feeding device |
US2155598A (en) * | 1936-05-29 | 1939-04-25 | Holt Thomas William | Production of slivers from textile fibers |
US3005238A (en) * | 1957-06-04 | 1961-10-24 | Deering Milliken Res Corp | Moisture control arrangement and method |
US3821833A (en) * | 1968-04-16 | 1974-07-02 | Rieter Ag Maschf | Apparatus for supplying cards by means of a pneumatic flock transporting system |
Cited By (25)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4074546A (en) * | 1976-11-24 | 1978-02-21 | Crompton & Knowles Corporation | Fluid treating system for textile fibers |
US4103397A (en) * | 1977-01-03 | 1978-08-01 | Jackson Samuel G | Lint slide grid humidifier |
US4140503A (en) * | 1978-01-19 | 1979-02-20 | Vandergriff Arvel L | Vapor condenser and lint humidifier system |
US4527306A (en) * | 1982-07-31 | 1985-07-09 | Trutzschler Gmbh & Co. Kg | Spinning preparation system and method for air-conditioning the same |
EP0191713A1 (en) * | 1985-01-10 | 1986-08-20 | Australian Wool Corporation | Conditioning baled material |
US4726096A (en) * | 1986-09-19 | 1988-02-23 | Farmers Gin And Grain Of Humboldt, Inc. | Electric moisture control device for cotton gin |
EP0275812A1 (en) * | 1986-12-23 | 1988-07-27 | Australian Wool Corporation | Conditioning of baled materials |
US5052080A (en) * | 1988-06-23 | 1991-10-01 | Maschinenfabrik Rieter, Ag | Method and apparatus for controlling yarn preparation operations to enhance product uniformity |
EP0412446A1 (en) * | 1989-08-10 | 1991-02-13 | Maschinenfabrik Rieter Ag | Method to influence the conditioning of fibre processing in a spinning machine |
US5121522A (en) * | 1989-12-22 | 1992-06-16 | Trutzschler Gmbh & Co., Kg | Humidity and temperature air conditioning in a textile processing line |
EP0459828A1 (en) * | 1990-06-01 | 1991-12-04 | E.I. Du Pont De Nemours And Company | Method for baling cut fibers and product |
US5361450A (en) * | 1992-12-31 | 1994-11-08 | Zellweger Uster, Inc. | Direct control of fiber testing or processing performance parameters by application of controlled, conditioned gas flows |
US6237195B1 (en) * | 2000-03-14 | 2001-05-29 | Thomas R. Shoemaker | Fiber moisture cell for humidifying cotton and method |
US20080251187A1 (en) * | 2003-10-17 | 2008-10-16 | Enamul Haque | Composite material with improved structural, acoustic and thermal properties |
US20110121482A1 (en) * | 2003-10-17 | 2011-05-26 | Roekens Bertrand J | Methods of forming low static non-woven chopped strand mats |
US20080050571A1 (en) * | 2004-12-28 | 2008-02-28 | Enamul Haque | Polymer/WUCS mat for use in automotive applications |
US20060141260A1 (en) * | 2004-12-29 | 2006-06-29 | Enamul Haque | Sandwich composite material using an air-laid process and wet glass |
US20060137798A1 (en) * | 2004-12-29 | 2006-06-29 | Enamul Haque | Polymer/WUCS mat for use in sheet molding compounds |
US20060137799A1 (en) * | 2004-12-29 | 2006-06-29 | Enamul Haque | Thermoplastic composites with improved sound absorbing capabilities |
US7252729B2 (en) * | 2004-12-29 | 2007-08-07 | Owens-Corning Fiberglas Technology Inc. | Polymer/WUCS mat for use in sheet molding compounds |
US20080006361A1 (en) * | 2004-12-29 | 2008-01-10 | Enamul Haque | Polymer/WUCS mat for use in sheet molding compounds |
US8057614B2 (en) | 2004-12-29 | 2011-11-15 | Owens Corning Intellectual Capital, Llc | Polymer/WUCS mat for use in sheet molding compounds |
US20080057283A1 (en) * | 2006-08-29 | 2008-03-06 | Arthur Blinkhorn | Reinforced acoustical material having high strength, high modulus properties |
US8652288B2 (en) | 2006-08-29 | 2014-02-18 | Ocv Intellectual Capital, Llc | Reinforced acoustical material having high strength, high modulus properties |
US20200299870A1 (en) * | 2017-11-14 | 2020-09-24 | Autefa Solutions Germany Gmbh | Monitoring process for nonwoven fabrication plants |
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