Bleached fiber product production method, apparatus to be used therefor, and bleached fiber product produced thereby

• US 8,486,225 B2
• Filed: 12/26/2007
• Issued: 07/16/2013
• Est. Priority Date: 02/27/2007
• Status: Active Grant

• Current Assignee: Keigo Takeda, Koichi Abe, Shigenori Aono
• Original Assignee: Keigo Takeda, Koichi Abe, Shigenori Aono
• Inventors: Aono, Shigenori, Abe, Koichi, Takeda, Keigo
• Primary Examiner(s): MINSKEY, JACOB T
• Application Number:
  US12/528,534
• Publication Number:
  US 20100116450A1
• Time in Patent Office: 2,029 Days
• Field of Search: 814/91, 814/92, 162/49, 162/263, 162/264, 162/248, 134/13
• US Class Current: 162/49
• CPC Class Codes: D06B 23/28 in response to a test conducted on the treating material
• CPC Class Codes: D06B 5/16 through yarns, threads or filaments
• CPC Class Codes: D06L 4/50 by irradiation or ozonisation
• CPC Class Codes: D06L 4/75 combined with cleaning or washing

Abstract

An inventive method includes the steps of: loading a fiber product in an appropriate form into a treatment vessel; wetting the fiber product; forcibly circulating an ozone-containing liquid in contact with the wetted fiber product to thereby bleach the fiber product; and forcibly circulating an ozone decomposing chemical agent liquid in contact with the ozone-treated fiber product to decompose ozone. This method ensures efficient bleaching of the fiber product with the ozone. Further, the method is advantageous in that the resulting bleached fiber product is less liable to be yellowed over time.

Claims

1. A bleached fiber product production method for bleaching a fiber product mainly including at least one of a natural fiber and a regenerated fiber to produce a bleached fiber product, the method comprising the steps of:

loading the fiber product into a lidded hermetic vessel serving as a treatment vessel;

forcibly circulating a treatment liquid in contact with the fiber product loaded in the treatment vessel through a forcible circulation pipe attached to the treatment vessel and provided with a circulation pump to thereby wet the fiber product;

supplying an ozone gas into the treatment liquid in a minute bubble form via a gas-liquid mixing/ejecting means, the gas-liquid mixing/ejecting means being selected from an ejector, a vortex pump and a mixing pump, to provide an ozone-containing liquid, and forcibly circulating the ozone-containing liquid in contact with the wetted fiber product through the forcible circulation pipe to thereby bleach the fiber product;

forcibly circulating an ozone decomposing chemical agent liquid in contact with the bleached fiber product through the forcible circulation pipe to thereby decompose ozone; and

rinsing the fiber product after the decomposition of the ozone;

wherein an ozone concentration in the treatment vessel is measured over time in the fiber product bleaching step, and maintained within a predetermined range by increasing an ozone gas supply amount if the measured concentration is lower than a predetermined range, and reducing the ozone gas supply amount if the measured concentration is higher than the predetermined range.

2. A bleached fiber product production method as set forth in claim 1,

wherein the treatment vessel is a package type treatment vessel in which the fiber product is treated in a packaged form,

wherein the treatment liquid, the ozone-containing liquid and the ozone decomposing chemical agent liquid are each caused to repeatedly flow into and out of the packaged fiber product to be forcibly circulated in contact with the fiber product.

3. A bleached fiber product production method as set forth in claim 1,

wherein the treatment vessel is a liquid flow type treatment vessel in which the fiber product is transported in a rope form in a liquid stream while being treated in the liquid stream,

wherein the treatment liquid, the ozone-containing liquid and the ozone decomposing chemical agent liquid are each used for generating the liquid stream for transportation of the rope-form fiber product and forcibly circulated in contact with the fiber product.

4. A bleached fiber product production method as set forth in claim 1,

wherein the treatment vessel is a washer type treatment vessel in which the fiber product is treated while being moved in a rotary drum,

wherein the treatment liquid, the ozone-containing liquid and the ozone decomposing chemical agent liquid are each forcibly circulated into and out of the rotary drum in contact with the fiber product.

5. A bleached fiber product production method as set forth in claim 1,

wherein the ozone-containing liquid has an ozone concentration of 10 to 300 g/Nm³,

wherein the ozone-containing liquid is forcibly circulated at a flow rate of 15 to 90 liters/minute per 1 kg of the fiber product.

6. A bleached fiber product production method as set forth in claim 1,

wherein the ozone decomposing chemical agent liquid is a chemical agent liquid mainly containing hydrogen peroxide and an alkali agent.

7. A bleached fiber product production method as set forth in claim 1,

wherein the ozone decomposing chemical agent liquid includes a first chemical agent liquid mainly containing a reducing agent and a second chemical agent liquid mainly containing hydrogen peroxide and an alkali agent.

8. A bleached fiber product produced by a production method as recited in claim 1.

9. A bleached fiber product as set forth in claim 8, the bleached fiber product having a whiteness of not lower than 60 (as measured in conformity with JIS-1991) after being allowed to stand at 20°

C. to 30°

C. for 60 days following the production.

17. A fiber product bleaching apparatus to be used for a bleached fiber product production method as recited in claim 1, the apparatus comprising:

a lidded hermetic vessel serving as a treatment vessel;

fiber product holder means for loading a fiber product in the treatment vessel;

liquid introducing means for introducing a liquid to the fiber product loaded in the treatment vessel;

a forcible liquid circulation pipe provided with a circulation pump through which the liquid introduced into the treatment vessel is repeatedly taken out of the treatment vessel and introduced again into the treatment vessel to be brought into contact with the fiber product loaded in the treatment vessel;

ozone gas supplying means which supplies an ozone gas generated from an ozone generator in a minute bubble form via a gas-liquid mixing/ejecting means being selected from an ejector, a vortex pump and a mixing pump into the liquid circulated through the forcible liquid circulation pipe to provide an ozone-containing liquid for a bleaching treatment;

chemical agent liquid preparing means which supplies an ozone decomposing agent into the liquid circulated through the forcible liquid circulation pipe to provide an ozone decomposing chemical agent liquid for decomposing ozone;

a liquid outlet pipe through which the liquid present in the treatment vessel is drained out of the treatment vessel; and

a gas outlet pipe through which a gas present in the treatment vessel is discharged out of the treatment vessel;

wherein an ozone concentration sensor is provided in the treatment vessel for measuring an ozone concentration in the treatment vessel over time;

wherein the ozone concentration in the treatment vessel is controlled to be maintained within a predetermined range by increasing an ozone gas supply amount if the measured concentration is lower than a predetermined range, and reducing the ozone gas supply amount if the measured concentration is higher than the predetermined range.

18. A fiber product bleaching apparatus as set forth in claim 17,

wherein the treatment vessel is a package type treatment vessel in which the fiber product is treated in a packaged form,

wherein the liquid forcibly circulated through the forcible liquid circulation pipe is caused to repeatedly flow into and out of the packaged fiber product to be brought into contact with the fiber product.

19. A fiber product bleaching apparatus as set forth in claim 17,

wherein the treatment vessel is a liquid flow type treatment vessel in which the fiber product is transported in a rope-form in a liquid stream while being treated in the liquid stream,

wherein the liquid forcibly circulated through the forcible liquid circulation pipe is used for generating the liquid stream for transportation of the rope-form fiber product and brought into contact with the fiber product.

20. A fiber product bleaching apparatus as set forth in claim 17,

wherein the treatment vessel is a washer type treatment vessel in which the fiber product is treated while being moved in a rotary drum,

wherein the liquid forcibly circulated through the forcible liquid circulation pipe is forcibly circulated into and out of the rotary drum in contact with the fiber product.

10. A bleached fiber product production method for bleaching a fiber product mainly including at least one of a natural fiber and a regenerated fiber to produce a bleached fiber product, the method comprising the steps of:

loading the fiber product into a lidded hermetic vessel serving as a treatment vessel;

forcibly circulating a treatment liquid in contact with the fiber product loaded in the treatment vessel through a forcible circulation pipe attached to the treatment vessel and provided with a circulation pump to thereby wet the fiber product;

supplying an ozone gas into the treatment liquid in a minute bubble form via a gas-liquid mixing/ejecting means, the gas-liquid mixing/ejecting means being selected from an ejector, a vortex pump and a mixing pump, to provide an ozone-containing liquid, and forcibly circulating the ozone-containing liquid in contact with the wetted fiber product through the forcible circulation pipe to thereby bleach the fiber product;

forcibly circulating hot water heated up to a temperature not lower than 50°

C. in contact with the bleached fiber product through the forcible circulation pipe to thereby yellow the bleached fiber product;

forcibly circulating an ozone decomposing chemical agent liquid in contact with the yellowed fiber product through the forcible circulation pipe to thereby simultaneously achieve removal of a yellowing substance from the yellowed fiber product and decomposition of ozone; and

rinsing the fiber product after the removal of the yellowing substance and the decomposition of the ozone;

wherein an ozone concentration in the treatment vessel is measured over time in the fiber product bleaching step, and maintained within a predetermined range by increasing an ozone gas supply amount if the measured concentration is lower than a predetermined range, and reducing the ozone gas supply amount if the measured concentration is higher than the predetermined range.

11. A bleached fiber product production method as set forth in claim 10,

wherein the treatment vessel is a package type treatment vessel in which the fiber product is treated in a packaged form,

wherein the treatment liquid, the ozone-containing liquid, the hot water and the ozone decomposing chemical agent liquid are each caused to repeatedly flow into and out of the packaged fiber product to be forcibly circulated in contact with the fiber product.

12. A bleached fiber product production method as set forth in claim 10,

wherein the treatment vessel is a liquid flow type treatment vessel in which the fiber product is transported in a rope form in a liquid stream while being treated in the liquid stream,

wherein the treatment liquid, the ozone-containing liquid, the hot water and the ozone decomposing chemical agent liquid are each used for generating the liquid stream for transportation of the rope-form fiber product and forcibly circulated in contact with the fiber product.

13. A bleached fiber product production method as set forth in claim 10,

wherein the treatment vessel is a washer type treatment vessel in which the fiber product is treated while being moved in a rotary drum,

wherein the treatment liquid, the ozone-containing liquid, the hot water and the ozone decomposing chemical agent liquid are each forcibly circulated into and out of the rotary drum in contact with the fiber product.

14. A bleached fiber product production method as set forth in claim 10,

wherein the ozone-containing liquid has an ozone concentration of 10 to 300 g/Nm³,

wherein the ozone-containing liquid is forcibly circulated at a flow rate of 15 to 90 liters/minute per 1 kg of the fiber product.

15. A bleached fiber product production method as set forth in claim 10,

wherein the ozone decomposing chemical agent liquid is a chemical agent liquid mainly containing hydrogen peroxide and an alkali agent.

16. A bleached fiber product production method as set forth in claim 10,

wherein the ozone decomposing chemical agent liquid includes a first chemical agent liquid mainly containing a reducing agent and a second chemical agent liquid mainly containing hydrogen peroxide and an alkali agent.

21. A fiber product bleaching apparatus to be used for a bleached fiber product production method as recited in claim 10, the apparatus comprising:

a lidded hermetic vessel serving as a treatment vessel;

fiber product holder means for loading a fiber product in the treatment vessel;

liquid introducing means for introducing a liquid to the fiber product loaded in the treatment vessel;

a forcible liquid circulation pipe provided with a circulation pump through which the liquid introduced into the treatment vessel is repeatedly taken out of the treatment vessel and introduced again into the treatment vessel to be brought into contact with the fiber product loaded in the treatment vessel;

ozone gas supply means which supplies an ozone gas generated from an ozone generator in a minute bubble form via a gas-liquid mixing/ejecting means being selected from an ejector, a vortex pump and a mixing pump into the liquid circulated through the forcible liquid circulation pipe to provide an ozone-containing liquid for a bleaching treatment;

heating means which heats the liquid circulated through the forcible liquid circulation pipe up to a temperature not lower than 50°

C. to provide hot water for a yellowing treatment;

chemical agent liquid preparing means which supplies an ozone decomposing agent into the liquid circulated through the forcible liquid circulation pipe to provide an ozone decomposing chemical agent liquid for simultaneously achieving removal of a yellowing substance and decomposition of ozone;

a liquid outlet pipe through which the liquid present in the treatment vessel is drained out of the treatment vessel; and

a gas outlet pipe through which a gas present in the treatment vessel is discharged out of the treatment vessel;

wherein an ozone concentration sensor is provided in the treatment vessel for measuring an ozone concentration in the treatment vessel over time,

wherein the ozone concentration in the treatment vessel is controlled to be maintained within a predetermined range by increasing an ozone gas supply amount if the measured concentration is lower than a predetermined range, and reducing the ozone gas supply amount if the measured concentration is higher than the predetermined range.

22. A fiber product bleaching apparatus as set forth in claim 21,

wherein the treatment vessel is a package type treatment vessel in which the fiber product is treated in a packaged form,

wherein the liquid forcibly circulated through the forcible liquid circulation pipe is caused to repeatedly flow into and out of the packaged fiber product to be brought into contact with the fiber product.

23. A fiber product bleaching apparatus as set forth in claim 21,

wherein the treatment vessel is a liquid flow type treatment vessel in which the fiber product is transported in a rope-form in a liquid stream while being treated in the liquid stream,

wherein the liquid forcibly circulated through the forcible liquid circulation pipe is used for generating the liquid stream for transportation of the rope-form fiber product and brought into contact with the fiber product.

24. A fiber product bleaching apparatus as set forth in claim 21,

wherein the treatment vessel is a washer type treatment vessel in which the fiber product is treated while being moved in a rotary drum,

wherein the liquid forcibly circulated through the forcible liquid circulation pipe is forcibly circulated into and out of the rotary drum in contact with the fiber product.