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1. Field of the Invention
The present invention relates to continuous batch washers or tunnel washers. More particularly, the present invention relates to an improved method of washing textiles or fabric articles (e.g. clothing, linen, etc.) in a continuous batch tunnel washer wherein the textiles are moved sequentially from one module or zone to the next module or zone including initial pre-wash zones, a plurality of main wash and pre-rinse zones, and then transferred to an extractor that removes water. More particularly, the present invention relates to an improved method of washing textiles in a continuous batch tunnel washer wherein a counter flow of wash liquor from one module or zone to the next module or zone is stopped, allowing for a standing bath. Chemicals are then added to separate soil from the goods and suspend the soil in the wash liquor. After a period of time, counter flow is commenced again to remove the suspended soil. The pre-rinsed goods are spray rinsed during extraction of excess water so that soil is not redeposited eliminated graying of the goods.
2. General Background of the Invention
Currently, washing in a commercial environment is conducted with a continuous batch tunnel washer. Such continuous batch tunnel washers are known (e.g. U.S. Pat. No. 5,454,237) and are commercially available (www.milnor.com). Continuous batch washers have multiple sectors, zones, stages, or modules including pre-wash, wash, rinse and finishing zone. Commercial continuous batch washing machines utilize a constant counter flow of liquor and a centrifugal extractor or mechanical press for removing most of the liquor from the goods before the goods are dried. Some machines carry the liquid with the goods throughout the particular zone or zones.
Currently, a counter flow is used during the entire time that the fabric articles or textiles are in the main wash module zone. This practice dilutes the washing chemical and reduces its effectiveness. Additionally, while the bath liquor is being heated, this thermal energy is partially carried away by the counter flow thus wasting energy while a desired temperature value is achieved.
A final rinse with a continuous batch washer has been performed using a centrifugal extractor or mechanical press. In prior art systems, if a centrifugal extractor is used, it is typically necessary to rotate the extractor at a first low speed that is designed to remove soil laden water before a final extract.
Patents have issued that are directed to batch washers or tunnel washers. The following table provides examples.
The present invention improves the current art by reducing water consumption, improving rinsing capability, reducing the number of components required to perform the function of laundering fabric articles or textiles, and saving valuable floor space in the laundry.
The present invention reduces and/or combines zones, sectors, or modules and improves the method of processing the textiles. Rinsing is done in two zones, first in the continuous batch washer itself in an intermediate rinse zone after each main wash zone(s) and a pre-rinse in the last zone(s). A final rinse is then done in a mechanical water removal machine such as a centrifugal extractor or mechanical press.
When the goods are initially transferred into the main wash modules, the counter flow of wash liquor into the modules is stopped allowing for a standing bath. Chemicals are added to separate the soil from the goods and suspend the soil in the wash liquor. If needed, the wash liquor to the separate module bath is raised in temperature to facilitate the release of soil from the goods and activate the chemicals.
Once the soil has been released from the textiles, there is no more work for the chemicals to perform. At this time, the process can be described as “chemical equilibrium”. At this point, water by counter flow is commenced to remove the suspended soil. This rinsing is termed “intermediate rinse” in the wash zone(s) and a pre-rinse after the last wash zone. A final rinse can be performed in a centrifugal extractor or mechanical press.
The process of the present invention uses fresh water that can be supplied through an atomizing nozzle while the goods are being extracted. Because the free soil has already been removed in the pre-rinse zone, the spray rinse while extracting will not re-deposit soil on the linen thereby reducing or eliminating graying of the goods. It is not necessary to centrifuge (and drain at a low speed) the soil laden water before the final extract. With the present invention the process time is reduced. The amount of fresh water required compared with conventional processes is reduced.
The method of the present invention uses less water than in current art because the counter flow is stopped for part of the cycle. The spray rinse in the centrifugal extractor or mechanical press is more effective than the current practice of draining the free water from the linen and then refilling.
The method of the present invention preserves the washing effectiveness of current counter flow washers to wash heavy soil classifications because the amount of soil dilution is the same even though there are less zones, stages, or modules. The present invention provides a higher effective rinsing provided by the spray rinse in the centrifugal extractor because of the pre-rinse.
For a further understanding of the nature, objects, and advantages of the present invention, reference should be had to the following detailed description, read in conjunction with the following drawings, wherein like reference numerals denote like elements and wherein:
The total number of modules 14-18 can be more or less than the five (5) shown in
Inlet end portion 12 can provide a hopper 19 that enables the intake of textiles or fabric articles to be washed. Such fabric articles, textiles, goods to be washed can include clothing, linens, towels, and the like. An extractor 20 is positioned next to the outlet end portion 13 of tunnel washer 11. Flow lines 21, 25, 26, 27, 27A are provided for adding water and/or chemicals to tunnel washer 11 as will be described more fully hereinafter.
When the fabric articles, goods, linens are initially transferred into the main wash modules 16, 17, 18, a counter flow of wash liquor into these modules 16, 17, 18 is reduced, preferably stopped allowing for a standing bath. Chemicals are then added as indicated by arrows 26, 27 to the modules 16, 17 and/or 18. In
Once the maximum soil has been released from the textiles or fabric articles, there is no more work for the chemicals to perform. At this time, the process can be described as chemical equilibrium. The flow of water is stopped for a time period sufficient to release soil from the goods such as for example between about 20 seconds and one hundred twenty (120) seconds. However, this time interval can be between about ten (10) and three hundred (300) seconds.
After this time interval of having no counter flow, water by counter flow is commenced to remove the suspended soil. This rinsing can be termed pre-rinse. A final rinse is then performed in a centrifugal extractor or mechanical press 20. The process of the present invention uses fresh water that can be supplied through an atomizing nozzle for example while the goods are being extracted using the extractor 20. The process of the present invention uses fresh water in the extractor that can be supplied through an atomizing nozzle for example while the goods are being extracted at high speed (e.g. between about 200 and 1,000 g's) using the extractor 20.
Flow line 21 transmits water to hopper 19 as indicated by arrow 22. Flow line 21 also carries water to pre-wash module 15 as indicated by arrow 23. Arrow 24 indicates a flow of water from module 14 to module 15 as part of the pre-wash.
In
In
In
In
The method of the present invention thus conducts rinsing in two zones. Rinsing is first conducted in the tunnel washer 11 in a pre-rinse zone which occurs after the main wash. In
Because the free soil has already been removed in the pre-rinse zone at modules 16, 17, 18 of
An additional benefit of the pre-rinse concept of the present invention is to permit the mechanical press or extractor to have more time extracting the free water. This result follows because the effect of the pre-rinse is to remove most of the suspended soil. The amount of fresh water required for final rinse is thus greatly reduced. The time for rinsing is reduced, allowing this saved cycle time for water removal.
The method of the present invention preserves the washing effectiveness of current counter flow washers 11 to wash heavy soil classifications because the amount of soil dilution is the same even though there are fewer zones or stages or modules.
The present invention provides a higher effective rinsing provided by the spray rinse 30 and the centrifugal extractor 20 because of the pre-rinse that is conducted in the modules 16, 17, 18 as discussed above.
In
Starch tank 41 contains starch that is to be pumped via flow line 42 to nozzle 60 and then to extractor 20. Fresh water tank 43 can also be used to pipe fresh water to extractor 20, flowing through valve 45 to nozzle 60. Valves 44, 45 and 46 are provided for controlling the flow of either starch or fresh water or a combination thereof to nozzle 60 as shown in
Flow line 49 is a flow line that carries extracted water to tank 51 as it is purged from the fabric articles, clothing or linens contained in extractor 20. Starch can be recovered via flow lines 49, 50 to starch recovery tank 52. Valves 44, 47 are provided for valving the flow of starch from tank 41 to extractor 20 via flow line 42. Valve 48 enables tank 41 to be emptied for cleaning or adding new starch.
In
A mounting plate 65 can be provided having one or more openings 66 for attaching (for example, bolting) spray nozzle 60 to extractor 20 or to a frame that supports extractor 20.
The discharge end portion 63 of spray nozzle 60 provides a nozzle tip 67. The nozzle tip 67 provides a nozzle outlet 70 formed by side plates 71, 72, upper plate 73 and lower plate 74. Atomizing water nozzle 68, 69 are provided next to nozzle outlet 70. The atomizing water nozzle 68 is mounted to upper plate 73. The atomizing water nozzle 69 is mounted to lower plate 74 as shown in
As part of the method of the present invention, all starch flow lines 42, 60 can be purged with hot water from fresh water tank via flow line 75.
The following is a list of parts and materials suitable for use in the present invention.
All measurements disclosed herein are at standard temperature and pressure, at sea level on Earth, unless indicated otherwise. All materials used or intended to be used in a human being are biocompatible, unless indicated otherwise.
The foregoing embodiments are presented by way of example only; the scope of the present invention is to be limited only by the following claims.
This is a continuation of U.S. patent application Ser. No. 12/400,497, filed Mar. 9, 2009, which is a non-provisional patent application of U.S. Provisional Patent Application Ser. No. 61/046,118, filed Apr. 18, 2008, each of which is incorporated herein by reference. Priority of U.S. Provisional Patent Application Ser. No. 61/046,118, filed Apr. 18, 2008, incorporated herein by reference, is hereby claimed.
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Number | Date | Country | |
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20110225741 A1 | Sep 2011 | US |
Number | Date | Country | |
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61046118 | Apr 2008 | US |
Number | Date | Country | |
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Parent | 12400497 | Mar 2009 | US |
Child | 13052898 | US |