[go: up one dir, main page]

US20150308049A1 - Chlorine dioxide treatment compositions and processes - Google Patents

Chlorine dioxide treatment compositions and processes Download PDF

Info

Publication number
US20150308049A1
US20150308049A1 US14/795,630 US201514795630A US2015308049A1 US 20150308049 A1 US20150308049 A1 US 20150308049A1 US 201514795630 A US201514795630 A US 201514795630A US 2015308049 A1 US2015308049 A1 US 2015308049A1
Authority
US
United States
Prior art keywords
chlorine dioxide
peroxidase
pulp
polyporus
processes
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Abandoned
Application number
US14/795,630
Inventor
Hui Xu
Kim Bloomfield
Henrik Lund
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Novozymes AS
Novozymes North America Inc
Original Assignee
Novozymes AS
Novozymes North America Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Novozymes AS, Novozymes North America Inc filed Critical Novozymes AS
Priority to US14/795,630 priority Critical patent/US20150308049A1/en
Publication of US20150308049A1 publication Critical patent/US20150308049A1/en
Abandoned legal-status Critical Current

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/72—Treatment of water, waste water, or sewage by oxidation
    • C02F1/76—Treatment of water, waste water, or sewage by oxidation with halogens or compounds of halogens
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/71—Mixtures of material ; Pulp or paper comprising several different materials not incorporated by special processes
    • D21H17/74—Mixtures of material ; Pulp or paper comprising several different materials not incorporated by special processes of organic and inorganic material
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00—Biological treatment of water, waste water, or sewage
    • C02F3/34—Biological treatment of water, waste water, or sewage characterised by the microorganisms used
    • C02F3/342—Biological treatment of water, waste water, or sewage characterised by the microorganisms used characterised by the enzymes used
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
    • D21C5/00—Other processes for obtaining cellulose, e.g. cooking cotton linters ; Processes characterised by the choice of cellulose-containing starting materials
    • D21C5/005—Treatment of cellulose-containing material with microorganisms or enzymes
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H11/00—Pulp or paper, comprising cellulose or lignocellulose fibres of natural origin only
    • D21H11/02—Chemical or chemomechanical or chemothermomechanical pulp
    • D21H11/04—Kraft or sulfate pulp
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/005—Microorganisms or enzymes
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/63—Inorganic compounds
    • D21H17/67—Water-insoluble compounds, e.g. fillers, pigments
    • D21H17/675—Oxides, hydroxides or carbonates
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/26—Nature of the water, waste water, sewage or sludge to be treated from the processing of plants or parts thereof
    • C02F2103/28—Nature of the water, waste water, sewage or sludge to be treated from the processing of plants or parts thereof from the paper or cellulose industry
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
    • D21C3/00—Pulping cellulose-containing materials
    • D21C3/18—Pulping cellulose-containing materials with halogens or halogen-generating compounds
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
    • D21C9/00—After-treatment of cellulose pulp, e.g. of wood pulp, or cotton linters ; Treatment of dilute or dewatered pulp or process improvement taking place after obtaining the raw cellulosic material and not provided for elsewhere
    • D21C9/10—Bleaching ; Apparatus therefor
    • D21C9/12—Bleaching ; Apparatus therefor with halogens or halogen-containing compounds
    • D21C9/14—Bleaching ; Apparatus therefor with halogens or halogen-containing compounds with ClO2 or chlorites

Definitions

  • the present invention relates to methods and compositions for improving chlorine dioxide treatment processes, such as, pulp delignification and bleaching processes.
  • Chlorine dioxide is one of the most widely used delignification/bleaching agents in the pulp and paper industry, providing a high-quality, low-cost delignification and bleaching process. Chlorine dioxide treatment is superior to chlorine bleaching processes in that it virtually eliminates all dioxin discharges into the environment, and has accordingly, helped pulp and paper manufactures to employ environmentally friendly processes and to meet environmental requirements. Accordingly, the use of chlorine dioxide treatment is increasing and most pulp and paper mills now have at least one chlorine dioxide delignification or bleaching stage. Chlorine dioxide treatment has also been used to treat wastewater, sludge and other process streams.
  • New compositions and methods are needed to improve the efficiency and effectiveness of chlorine dioxide treatment, including, chlorine dioxide delignification and bleaching processes.
  • the present invention relates to methods and compositions for chlorine dioxide delignification and/or bleaching processes by reacting pulp with chlorine dioxide and a peroxidase and/or a laccase.
  • a peroxidase and/or a laccase is/are added to a chlorine dioxide delignification and/or bleaching step.
  • the addition of a peroxidase and/or a laccase to a chlorine dioxide treating composition is believed to result in the regeneration of chlorine dioxide from chlorite, resulting in improved delignification and/or brightening during bleaching of pulp.
  • the present invention relates to methods and compositions for chlorine dioxide treatment of wastewater, sludge or any other process stream.
  • a peroxidase and/or a laccase is added to a chlorine dioxide treatment step to improve the chlorine dioxide treatment process.
  • a “peroxidase” means a peroxidase (E.C.1.11.1.7) and/or a haloperoxidase, such, as, preferably, a chloride peroxidase (E.C.1.11.1.10).
  • the peroxidase is an acid stable peroxidase.
  • Peroxidases may be obtained from any suitable source, such as, e.g., from plants (e.g., a soy bean or horseradish peroxidase) and from microorganisms (fungi and bacteria, such as, e.g., the peroxidase may be obtained from a strain of Coprinus, e.g., C. cinerius or C. macrorhizus, or of Bacillus, e.g. B. pumilu ).
  • plants e.g., a soy bean or horseradish peroxidase
  • microorganisms fungi and bacteria
  • the peroxidase may be obtained from a strain of Coprinus, e.g., C. cinerius or C. macrorhizus, or of Bacillus, e.g. B. pumilu ).
  • Some preferred fungal sources include strains belonging to the subdivision Deuteromycotina, class Hyphomycetes, e.g., Fusarium, Humicola, Tricoderma, Myrothecium, Verticillum, Arthromyces, Caldariomyces, Ulocladium, Embellisia, Cladosporium or Dreschlera, in particular, Fusarium oxysporum (DSM 2672), Humicola insolens, Trichoderma resii, Myrothecium verrucana (IFO 6113), Verticillum alboatrum, Verticillum dahlie, Arthromyces ramosus (FERM P-7754), Caldariomyces fumago, Ulocladium chartarum, Embellisia alli or Dreschlera halodes.
  • DSM 2672 Fusarium oxysporum
  • Humicola insolens Trichoderma resii
  • Myrothecium verrucana IFO 6113
  • Other preferred fungal sources include strains belonging to the subdivision Basidiomycotina, class Basidiomycetes, e.g., Coprinus, Phanerochaete, Coriolus or Trametes, in particular Coprinus cinereus f. microsporus (IFO 8371), Coprinus macrorhizus, Phanerochaete chrysosporium (e.g., NA-12) or Coriolus versicolor (e.g., PR4 28-A).
  • Further preferred fungal sources include strains belonging to the subdivision Zygomycotina, class Mycoraceae, e.g., Rhizopus or Mucor, in particular, Mucor hiemalis.
  • Some preferred bacterial peroxidase sources include strains of the order Actinomycetales, e.g., Streptomyces spheroides (ATTC 23965), Streptomyces thermoviolaceus (IFO 12382) or Streptoverticillum verticillium ssp. verticillium.
  • Other preferred bacterial sources include Bacillus pumillus (ATCC 12905), Bacillus stearothermophilus, Rhodobacter sphaeroides, Rhodomonas palustri, Streptococcus lactis, Pseudomonas purrocinia (ATCC 15958) or Pseudomonas fluorescens (NRRL B-11).
  • Haloperoxidases may be obtained form any suitable source. Haloperoxidases, for example, have been isolated from various organisms, including mammals, marine animals, plants, algae, a lichen, fungi and bacteria (for reference see Biochimica et Biophysica Acta 1161, 1993, pp. 249-256). Suitable choloroperoxidases include the chloroperoxidase obtained from the fungus Curvularia inaequalis (see SWISS-PROT:P49053), the chloroperoxidase obtained from the fungus Curvularia verruculosa (see WO 97/04102) and the chloroperoxidases disclosed in Svendsen et al, U.S. Pat. No. 6,372,465.
  • Laccases may be obtained from any suitable sources, such as, from a genus selected from the group consisting of Aspergillus, Botrytis, Collybia, Fomes, Lentinus, Myceliophthora, Neurospora, Pleurotus, Podospora, Polyporus, Scytalidium, Trametes, and Rhizoctonia.
  • the laccase is obtained from a species selected from the group consisting of Humicola brevis var. thermoidea, Humicola brevispora, Humicola grisea var.
  • thermoidea a thermoidea, Humicola insolens, and Humicola lanuginosa (also known as Thermomyces lanuginosus ), Myceliophthora thermophila, Myceliophthora vellerea, Polyporus pinsitus, Scytalidium thermophila, Scytalidium indonesiacum, and Torula thermophila.
  • the laccase may be obtained from other species of Scytalidium, such as Scytalidium acidophilum, Scytalidium album, Scytalidium aurantiacum, Scytalidium circinatum, Scytalidium flaveobrunneum, Scytalidium hyalinum, Scytalidium lignicola, and Scytalidium uredinicolum. Rhizoctonia solani and Coprinus cinereus.
  • the laccase may be obtained from other species of Polyporus, such as Polyporus zonatus, Polyporus alveolaris, Polyporus arcularius, Polyporus australiensis, Polyporus badius, Polyporus biformis, Polyporus brumalis, Polyporus ciliatus, Polyporus colensoi, Polyporus eucalyptorum, Polyporus meridionalis, Polyporus varius, Polyporus palustris, Polyporus rhizophilus, Polyporus rugulosus, Polyporus squamosus, Polyporus tuberaster, and Polyporus tumulosus.
  • Polyporus zonatus such as Polyporus zonatus, Polyporus alveolaris, Polyporus arcularius, Polyporus australiensis, Polyporus badius, Polyporus biformis, Polyporus brumal
  • chlorine dioxide treatment means any chloride dioxide treatment process, such as, for example, chlorine dioxide treatment stages used in pulp and paper mills and chlorine dioxide treatment of wastewater and/or sludge, for example, plant wastewater or ordinary household sewage or wastewater.
  • chlorine dioxide treatment is applied in a pulp and paper mills in delignification and pulp bleaching processes.
  • Any suitable pulp may be treated, although preferably, the pulp is a lingocellulosic pulp.
  • the pulp may be treated with other delignification and/or bleaching agents prior to, during or following the chlorine dioxide treatment, such as, e.g., oxygen delignification, peroxide treatment, and enzyme treatment processes.
  • the chlorine dioxide used in the treatment process may be generated by any suitable method. However, because chlorine dioxide is unstable as a gas and can only stored as a solution, it is usually generated on-site, e.g., at the pulp mill. Once in solution, however, chlorine dioxide is fairly stable.
  • Chlorine dioxide is generally added in amounts effective to treat the pulp or process waters (e.g., waste water), as are known in the art.
  • chlorine dioxide treatment of pulp is carried out at a temperature from about 40 to 80° C. for a period of about 15 to 120 min.
  • the effectiveness of the chlorine dioxide depends in part on pH, and is maximized at a pH of about 2 to 4. Because the pH of pulp streams and other process waters are typically more basic, acid may be added to the treatment water to reduce the pH. In some processes, the pH of the process water may be controlled by applying excess amounts of chlorine dioxide.
  • the peroxidase and/or laccase is/are applied directly to the chlorine dioxide process stream in an amount effective to improve the chlorine dioxide treatment process, as exemplified below.
  • the peroxidase and/or laccase may be applied as part of the chlorine dioxide solution, a part of a filtrate used to prepare the process water (e.g. delignification or bleaching liquour), in the recycled process water, and/or by a separate addition.
  • the peroxidase and/or laccase are applied in an amount effective to improve the chlorine dioxide treatment process, such as, as measured by improved pulp delignification and/or improved pulp bleaching.
  • An example of an effective amount of a peroxidase is 0.005 mg-10 g/L of process water, more preferably 0.01-1000 mg/L of process water, and most preferably 0.05-500 mg/L of process water.
  • such effective amount of a peroxidase will include 0.01 g-20 kg/ton of pulp, more preferably 0.1 g-5 kg/ton of pulp, and most preferably 1 g-2 kg/ton of pulp.
  • an effective amount of a laccase is 0.005 mg-10 g/L of process water, more preferably 0.01-1000 mg/L of process water, and most preferably 0.05-500 mg/L of process water.
  • such effective amount of a laccase will include 0.01 g-20 kg/ton, more preferably 0.1 g-5 kg/ton, and most preferably 1g-2 kg/ton.
  • the peroxidases and laccases are preferably selected based their compatibility with the process conditions for the pulp treatment or waste water/sludge treatment, e.g., pH optimum, temperature optimum, acid stability.

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Microbiology (AREA)
  • Organic Chemistry (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Inorganic Chemistry (AREA)
  • Biochemistry (AREA)
  • Biodiversity & Conservation Biology (AREA)
  • General Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Paper (AREA)
  • Enzymes And Modification Thereof (AREA)
  • Treatment Of Sludge (AREA)

Abstract

The present invention relates to methods and compositions for chlorine dioxide delignification and/or bleaching processes by reacting pulp with chlorine dioxide and a peroxidase and/or a laccase.

Description

    CROSS-REFERENCE TO RELATED APPLICATIONS
  • This application is a division of U.S. 11/910,987 filed Nov. 27, 2007, now pending, which is a 35 U.S.C. 371 national application of PCT/US2005/015577 filed May 4, 2005, which claims priority or the benefit under 35 U.S.C. 119 of U.S. provisional application No. 60/567,488 filed May 3, 2004, the contents of which are fully incorporated herein by reference.
    • FIELD OF THE INVENTION
  • The present invention relates to methods and compositions for improving chlorine dioxide treatment processes, such as, pulp delignification and bleaching processes.
    • BACKGROUND
  • Chlorine dioxide is one of the most widely used delignification/bleaching agents in the pulp and paper industry, providing a high-quality, low-cost delignification and bleaching process. Chlorine dioxide treatment is superior to chlorine bleaching processes in that it virtually eliminates all dioxin discharges into the environment, and has accordingly, helped pulp and paper manufactures to employ environmentally friendly processes and to meet environmental requirements. Accordingly, the use of chlorine dioxide treatment is increasing and most pulp and paper mills now have at least one chlorine dioxide delignification or bleaching stage. Chlorine dioxide treatment has also been used to treat wastewater, sludge and other process streams.
  • During the chlorine dioxide treatment processes some of the chlorine dioxide is converted to chlorate and chlorite, which decreases the efficiency of the chlorine dioxide treatment. Methods have been proposed to improve the efficiency of the chlorine dioxide treatment process by reducing chlorate and chlorite formation. Seger et al., Chiang, Tappi J., 1992, 75(7):174-180, for example, discloses a two step high-pH and low-pH process, which is believed to reduce the formation of chlorate at the higher pH and chlorite becomes reactive in the low-pH step. Joncourt et al., International Symp. Wood Pulping Chemistry, Montreal, Jun. 9-12, 1997, discloses the use of iron to regenerate chlorine dioxide from chlorite. Jiang et al, U.S. Pat. No. 6,235,154, discloses process for improving chlorine dioxide delignification or bleaching by regenerate chlorine dioxide from the chlorite using formaldehyde.
  • New compositions and methods are needed to improve the efficiency and effectiveness of chlorine dioxide treatment, including, chlorine dioxide delignification and bleaching processes.
    • SUMMARY OF THE INVENTION
  • The present invention relates to methods and compositions for chlorine dioxide delignification and/or bleaching processes by reacting pulp with chlorine dioxide and a peroxidase and/or a laccase. In accordance with the present invention, a peroxidase and/or a laccase is/are added to a chlorine dioxide delignification and/or bleaching step. Although not limited to any one theory of operation, the addition of a peroxidase and/or a laccase to a chlorine dioxide treating composition is believed to result in the regeneration of chlorine dioxide from chlorite, resulting in improved delignification and/or brightening during bleaching of pulp.
  • The present invention relates to methods and compositions for chlorine dioxide treatment of wastewater, sludge or any other process stream. In accordance with the present invention, a peroxidase and/or a laccase is added to a chlorine dioxide treatment step to improve the chlorine dioxide treatment process.
    • DETAILED DESCRIPTION
  • A “peroxidase” means a peroxidase (E.C.1.11.1.7) and/or a haloperoxidase, such, as, preferably, a chloride peroxidase (E.C.1.11.1.10). Preferably, the peroxidase is an acid stable peroxidase.
  • Peroxidases may be obtained from any suitable source, such as, e.g., from plants (e.g., a soy bean or horseradish peroxidase) and from microorganisms (fungi and bacteria, such as, e.g., the peroxidase may be obtained from a strain of Coprinus, e.g., C. cinerius or C. macrorhizus, or of Bacillus, e.g. B. pumilu). Some preferred fungal sources include strains belonging to the subdivision Deuteromycotina, class Hyphomycetes, e.g., Fusarium, Humicola, Tricoderma, Myrothecium, Verticillum, Arthromyces, Caldariomyces, Ulocladium, Embellisia, Cladosporium or Dreschlera, in particular, Fusarium oxysporum (DSM 2672), Humicola insolens, Trichoderma resii, Myrothecium verrucana (IFO 6113), Verticillum alboatrum, Verticillum dahlie, Arthromyces ramosus (FERM P-7754), Caldariomyces fumago, Ulocladium chartarum, Embellisia alli or Dreschlera halodes. Other preferred fungal sources include strains belonging to the subdivision Basidiomycotina, class Basidiomycetes, e.g., Coprinus, Phanerochaete, Coriolus or Trametes, in particular Coprinus cinereus f. microsporus (IFO 8371), Coprinus macrorhizus, Phanerochaete chrysosporium (e.g., NA-12) or Coriolus versicolor (e.g., PR4 28-A). Further preferred fungal sources include strains belonging to the subdivision Zygomycotina, class Mycoraceae, e.g., Rhizopus or Mucor, in particular, Mucor hiemalis.
  • Some preferred bacterial peroxidase sources include strains of the order Actinomycetales, e.g., Streptomyces spheroides (ATTC 23965), Streptomyces thermoviolaceus (IFO 12382) or Streptoverticillum verticillium ssp. verticillium. Other preferred bacterial sources include Bacillus pumillus (ATCC 12905), Bacillus stearothermophilus, Rhodobacter sphaeroides, Rhodomonas palustri, Streptococcus lactis, Pseudomonas purrocinia (ATCC 15958) or Pseudomonas fluorescens (NRRL B-11).
  • Haloperoxidases may be obtained form any suitable source. Haloperoxidases, for example, have been isolated from various organisms, including mammals, marine animals, plants, algae, a lichen, fungi and bacteria (for reference see Biochimica et Biophysica Acta 1161, 1993, pp. 249-256). Suitable choloroperoxidases include the chloroperoxidase obtained from the fungus Curvularia inaequalis (see SWISS-PROT:P49053), the chloroperoxidase obtained from the fungus Curvularia verruculosa (see WO 97/04102) and the chloroperoxidases disclosed in Svendsen et al, U.S. Pat. No. 6,372,465.
  • Laccases (EC 1.10.3.2) may be obtained from any suitable sources, such as, from a genus selected from the group consisting of Aspergillus, Botrytis, Collybia, Fomes, Lentinus, Myceliophthora, Neurospora, Pleurotus, Podospora, Polyporus, Scytalidium, Trametes, and Rhizoctonia. In a more preferred embodiment, the laccase is obtained from a species selected from the group consisting of Humicola brevis var. thermoidea, Humicola brevispora, Humicola grisea var. thermoidea, Humicola insolens, and Humicola lanuginosa (also known as Thermomyces lanuginosus), Myceliophthora thermophila, Myceliophthora vellerea, Polyporus pinsitus, Scytalidium thermophila, Scytalidium indonesiacum, and Torula thermophila. The laccase may be obtained from other species of Scytalidium, such as Scytalidium acidophilum, Scytalidium album, Scytalidium aurantiacum, Scytalidium circinatum, Scytalidium flaveobrunneum, Scytalidium hyalinum, Scytalidium lignicola, and Scytalidium uredinicolum. Rhizoctonia solani and Coprinus cinereus. The laccase may be obtained from other species of Polyporus, such as Polyporus zonatus, Polyporus alveolaris, Polyporus arcularius, Polyporus australiensis, Polyporus badius, Polyporus biformis, Polyporus brumalis, Polyporus ciliatus, Polyporus colensoi, Polyporus eucalyptorum, Polyporus meridionalis, Polyporus varius, Polyporus palustris, Polyporus rhizophilus, Polyporus rugulosus, Polyporus squamosus, Polyporus tuberaster, and Polyporus tumulosus.
  • A “chlorine dioxide treatment” means any chloride dioxide treatment process, such as, for example, chlorine dioxide treatment stages used in pulp and paper mills and chlorine dioxide treatment of wastewater and/or sludge, for example, plant wastewater or ordinary household sewage or wastewater.
  • Typically chlorine dioxide treatment is applied in a pulp and paper mills in delignification and pulp bleaching processes. Any suitable pulp may be treated, although preferably, the pulp is a lingocellulosic pulp. The pulp may be treated with other delignification and/or bleaching agents prior to, during or following the chlorine dioxide treatment, such as, e.g., oxygen delignification, peroxide treatment, and enzyme treatment processes.
  • The chlorine dioxide used in the treatment process may be generated by any suitable method. However, because chlorine dioxide is unstable as a gas and can only stored as a solution, it is usually generated on-site, e.g., at the pulp mill. Once in solution, however, chlorine dioxide is fairly stable.
  • Chlorine dioxide is generally added in amounts effective to treat the pulp or process waters (e.g., waste water), as are known in the art.
  • Typically, chlorine dioxide treatment of pulp is carried out at a temperature from about 40 to 80° C. for a period of about 15 to 120 min. The effectiveness of the chlorine dioxide depends in part on pH, and is maximized at a pH of about 2 to 4. Because the pH of pulp streams and other process waters are typically more basic, acid may be added to the treatment water to reduce the pH. In some processes, the pH of the process water may be controlled by applying excess amounts of chlorine dioxide.
  • The peroxidase and/or laccase is/are applied directly to the chlorine dioxide process stream in an amount effective to improve the chlorine dioxide treatment process, as exemplified below. The peroxidase and/or laccase may be applied as part of the chlorine dioxide solution, a part of a filtrate used to prepare the process water (e.g. delignification or bleaching liquour), in the recycled process water, and/or by a separate addition.
  • The peroxidase and/or laccase are applied in an amount effective to improve the chlorine dioxide treatment process, such as, as measured by improved pulp delignification and/or improved pulp bleaching. An example of an effective amount of a peroxidase is 0.005 mg-10 g/L of process water, more preferably 0.01-1000 mg/L of process water, and most preferably 0.05-500 mg/L of process water. In regard to pulp applications, such effective amount of a peroxidase will include 0.01 g-20 kg/ton of pulp, more preferably 0.1 g-5 kg/ton of pulp, and most preferably 1 g-2 kg/ton of pulp. An example of an effective amount of a laccase is 0.005 mg-10 g/L of process water, more preferably 0.01-1000 mg/L of process water, and most preferably 0.05-500 mg/L of process water. In regard to pulp applications, such effective amount of a laccase will include 0.01 g-20 kg/ton, more preferably 0.1 g-5 kg/ton, and most preferably 1g-2 kg/ton. The peroxidases and laccases are preferably selected based their compatibility with the process conditions for the pulp treatment or waste water/sludge treatment, e.g., pH optimum, temperature optimum, acid stability.
  • Although the invention herein has been described with reference to particular embodiments, it is to be understood that these embodiments are merely illustrative of the principles and applications of the present invention. It is therefore to be understood that numerous modifications may be made to the illustrative embodiments and that other arrangements may be devised without departing from the spirit and scope of the present invention as defined by the appended claims.
    • EXAMPLES Example 1
  • 160 mg of NaClO2 was dissolved in 100 mL of DI water. 10 mL aliquots of the NaClO2 solution were added to different test tubes. 20 uL of acetic acid were added to each tube and the pH was adjusted to about 3.5. Then 100 uL of enzyme was added to the solution. After 30 min of incubation at ambient temperature, the solution was diluted 3 times by DI water. ClO2 formation was detected by UV absorbency at 360 nm. It is evident that all of the enzymes can generate ClO2 to some extent under the conditions used in this experiment.
  • TABLE 1
    Enzymatic Chlorine Dioxide Generation
    Absorbency
    No. Sample at 360 nm
    1 Control 0.155
    2 Peroxidase from Coprinus cinereus 0.764
    (Novozymes)
    3 Haloperoxidase from Curvularia verruculosa 0.168
    (Novozymes)
    4 Laccase from Trametes villosa 0.802
    (Novozymes)
    5 Laccase from Coprinus cinereus 0.190
    (Novozymes)
    6 Laccase from Myceliophthora thermophila 0.197
    (Novozymes)
    7 Chloroperoxidase from Caldariomyces fumago 0.393
    (Sigma, C-0278)
    • Example 2
  • 5 g (o.d. dry) of unbleached kraft pulp was added to each beaker and diluted to about 5% consistency. The pulp was adjusted to various pH by 2N H2SO4. 10 mL of 11.3/L of NaClO2 was added to each beaker. 500 ul of peroxidase (Coprinus cinereus peroxidase, Novozymes) was added to the solution and the beaker was incubated at 60° C. for 1 hr. After bleaching, the pulp was rinsed with DI water and handsheets were made and tested for brightness. Brightness was tested according to Tappi standard (T452). It is clear the peroxidase improved pulp brightness in all the pH range.
  • pH Sample Brightness
    3 Control 50.4
    3 Peroxidase 51.4
    4 Control 46.8
    4 Peroxidase 47.3
    5 Control 43.3
    5 Peroxidase 44.2
    6 Control 42.8
    6 Peroxidase 45.0

Claims (4)

1. A method for delignifying and/or bleaching of a pulp, comprising reacting chlorine dioxide, a haloperoxidase and a pulp.
2. The method of claim 1, wherein the haloperoxidase is a chloride peroxidase.
3. The method of claim 1, wherein the haloperoxidase is a Coprinus peroxidase, a Bacillus peroxidase, a soy bean peroxidase or a horseradish peroxidase.
4. The method of claim 2, wherein the chloride peroxidase is a Curvularia inaequalis peroxidase or a Curvularia verruculosa peroxidase.
US14/795,630 2004-05-03 2015-07-09 Chlorine dioxide treatment compositions and processes Abandoned US20150308049A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US14/795,630 US20150308049A1 (en) 2004-05-03 2015-07-09 Chlorine dioxide treatment compositions and processes

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
US56748804P 2004-05-03 2004-05-03
PCT/US2005/015577 WO2006126983A1 (en) 2005-05-04 2005-05-04 Chlorine dioxide treatment compositions and processes
US91098707A 2007-11-27 2007-11-27
US14/795,630 US20150308049A1 (en) 2004-05-03 2015-07-09 Chlorine dioxide treatment compositions and processes

Related Parent Applications (2)

Application Number Title Priority Date Filing Date
PCT/US2005/015577 Division WO2006126983A1 (en) 2004-05-03 2005-05-04 Chlorine dioxide treatment compositions and processes
US11/910,987 Division US20080190573A1 (en) 2005-05-04 2005-05-04 Chlorine Dioxide Treatment Compositions and Processes

Publications (1)

Publication Number Publication Date
US20150308049A1 true US20150308049A1 (en) 2015-10-29

Family

ID=37452302

Family Applications (2)

Application Number Title Priority Date Filing Date
US11/910,987 Abandoned US20080190573A1 (en) 2005-05-04 2005-05-04 Chlorine Dioxide Treatment Compositions and Processes
US14/795,630 Abandoned US20150308049A1 (en) 2004-05-03 2015-07-09 Chlorine dioxide treatment compositions and processes

Family Applications Before (1)

Application Number Title Priority Date Filing Date
US11/910,987 Abandoned US20080190573A1 (en) 2005-05-04 2005-05-04 Chlorine Dioxide Treatment Compositions and Processes

Country Status (7)

Country Link
US (2) US20080190573A1 (en)
EP (1) EP1880053B1 (en)
CN (2) CN101171386B (en)
BR (1) BRPI0520253B1 (en)
CA (1) CA2607827C (en)
PT (1) PT1880053T (en)
WO (1) WO2006126983A1 (en)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6306818B2 (en) 2009-12-24 2018-04-04 ビーシーアール・エンバイロンメンタル・コーポレーションＢｃｒ Ｅｎｖｉｒｏｎｍｅｎｔａｌ Ｃｏｒｐｏｒａｔｉｏｎ Improved digestion of biosolids in wastewater
WO2012001145A1 (en) * 2010-07-01 2012-01-05 Novozymes A/S Bleaching of pulp
BR112016002498B1 (en) * 2013-08-09 2022-05-24 Novozymes A/S Method for reducing the content of hexenuronic acids in a chemical pulp and/or improving the brightness of chemical pulp and using a haloperoxidase
CN103454237B (en) * 2013-09-25 2015-07-08 陕西师范大学 Method for detecting nitrite content based on chloroperoxidase method
AR104939A1 (en) 2015-06-10 2017-08-23 Chemsenti Ltd OXIDATIVE METHOD TO GENERATE CHLORINE DIOXIDE
AR104940A1 (en) 2015-06-10 2017-08-23 Chemsenti Ltd METHOD FOR GENERATING CHLORINE DIOXIDE

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5147793A (en) * 1990-10-18 1992-09-15 The Mead Corporation Biocatalytic oxidation using soybean peroxidases
US5785811A (en) * 1992-11-09 1998-07-28 The Mead Corporation Process for treating lignocellulosic material with soybean peroxidase in the presence of peroxide
US20030124710A1 (en) * 2001-10-23 2003-07-03 Novozymes A/S Oxidizing enzymes in the manufacture of paper materials
US20120193047A1 (en) * 2005-04-13 2012-08-02 Novozymes North America, Inc. Methods for reducing chlorine dioxide associated corrosion
US20130105100A1 (en) * 2011-10-27 2013-05-02 Buckman Laboratories International, Inc. Method And Composition For Enzymatic Treatment Of Fiber For Papermaking, And Paper Products Made Therewith
US20160177503A1 (en) * 2013-08-09 2016-06-23 Novozymes A/S Reducing content of hexenuronic acids in cellulosic pulp

Family Cites Families (43)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3574052A (en) * 1967-02-28 1971-04-06 Chemech Eng Ltd Chemical pulping and bleaching in an enclosed reaction zone,by reduction of chlorate
USRE28887E (en) * 1968-12-26 1976-06-29 Hooker Chemicals & Plastics Corporation Sequential bleaching of kraft pulp with chlorine dioxide followed by chlorine
USRE28777E (en) * 1969-02-06 1976-04-20 Ethyl Corporation Refining of vegetable matter and delignification of the refined matter with chlorine dioxide
JPS4943481B1 (en) * 1971-06-14 1974-11-21
US4128454A (en) * 1977-12-07 1978-12-05 Ingersoll-Rand Co. System and method for gas phase pulp bleaching
WO1991005909A1 (en) * 1989-10-19 1991-05-02 North Carolina State University High efficiency chlorine dioxide pulp bleaching process
FI85389C (en) * 1989-12-12 1992-04-10 Enso Gutzeit Oy FOERFARANDE FOER TILLVERKNING AV MASSA.
FI905954L (en) 1990-12-03 1992-06-04 Enso Gutzeit Oy FOERFARANDE FOER BLEKNING AV CELLULOSAMASSA.
CA2044100A1 (en) * 1991-06-07 1992-12-08 Janice Hamilton Biobleaching process
CA2115881C (en) * 1993-02-25 2000-05-23 Michael G. Paice Non-chlorine bleaching of kraft pulp
US5324432A (en) * 1993-06-17 1994-06-28 Nalco Chemical Company Treatment of process waters to destroy filamentous bacteria
GB2279955B (en) * 1993-07-15 1998-02-18 Solvay Xylanase derived from a Bacillus species, expression vectors for such xylanase and other proteins, host organisms therefor and use thereof
FI95607C (en) * 1994-06-03 1996-02-26 Valtion Teknillinen Process and enzyme preparations for treating cellulose pulp
JP3810794B2 (en) * 1994-07-26 2006-08-16 ノボザイムス アクティーゼルスカブ Process for producing lignocellulose base product and product obtainable by said process
DK127894A (en) * 1994-11-04 1994-11-04 Novo Nordisk As Pulp waste water treatment
EP0843729B1 (en) * 1995-07-14 2006-12-06 Novozymes A/S Haloperoxidases from curvularia verruculosa and nucleic acids encoding same
NL1001583C2 (en) * 1995-11-07 1997-05-13 Akzo Nobel Nv Conversion of chlorite into chloride and oxygen.
JP3970930B2 (en) * 1996-02-08 2007-09-05 ノボザイムス アクティーゼルスカブ Method for producing lignocellulosic material and product obtained by the method
EP0905306A1 (en) * 1997-09-26 1999-03-31 Consortium für elektrochemische Industrie GmbH Multicomponent system for modifying, decomposing or bleaching lignin or lignin-containing materials and method of using this system
JP2002506935A (en) 1998-03-16 2002-03-05 パルプ アンド ペーパー リサーチ インスチチュート オブ カナダ Chlorine dioxide bleaching with additives
US6221821B1 (en) 1998-03-18 2001-04-24 Novozymes A/S Patents Haloperoxidases with altered pH profiles
EP1082486B1 (en) * 1998-04-16 2002-09-18 Pulp and Paper Research Institute of Canada Oxidase process for pulp and dye oxidation
US6610172B1 (en) * 1999-05-06 2003-08-26 Novozymes A/S Process for treating pulp with laccase and a mediator to increase paper wet strength
CA2390639C (en) * 1999-11-08 2009-04-28 Cbd Technologies Ltd. Process and composition for preparing a lignocellulose-based product, and the product obtained by the process
AU2001246402A1 (en) * 2000-04-14 2001-10-30 Novozymes A/S Polypeptides having haloperoxidase activity
US7320741B2 (en) * 2001-01-18 2008-01-22 Iogen Bio-Products Corporation Method of xylanase treatment in a chlorine dioxide bleaching sequence
CA2450709A1 (en) * 2001-06-29 2003-01-09 Novozymes North America, Inc. Preparation of cellulosic materials
AU2003208216A1 (en) * 2002-03-06 2003-09-16 Iogen Bio-Products Corporation Xylanase treatment of chemical pulp
US20040000012A1 (en) * 2002-06-26 2004-01-01 Borregaard Chemcell Treatment of a mixture containing cellulose
CN1176269C (en) * 2002-08-01 2004-11-17 山东轻工业学院 pulp bleaching process
US20040112555A1 (en) * 2002-12-03 2004-06-17 Jeffrey Tolan Bleaching stage using xylanase with hydrogen peroxide, peracids, or a combination thereof
US20050003516A1 (en) * 2003-04-16 2005-01-06 Novozymes A/S Enzymatic treatment of paper making
EP1668113B1 (en) * 2003-08-11 2013-06-19 Verenium Corporation Laccases, nucleic acids encoding them and methods for making and using them
US7285217B2 (en) * 2003-12-02 2007-10-23 Siemens Water Technologies Corp. Removing odoriferous sulfides from wastewater
US8317975B2 (en) * 2004-04-20 2012-11-27 The Research Foundation Of The State University Of New York Product and processes from an integrated forest biorefinery
CN101384769A (en) * 2006-02-14 2009-03-11 诺维信北美公司 Chemical pulp treatment compositions and methods
EP1996762B8 (en) * 2006-03-13 2016-12-21 FPInnovations Near-neutral chlorine dioxide bleaching of pulp
US7976676B2 (en) * 2006-12-18 2011-07-12 International Paper Company Process of bleaching softwood pulps in a D1 or D2 stage in a presence of a weak base
US7976677B2 (en) * 2006-12-18 2011-07-12 International Paper Company Process of bleaching hardwood pulps in a D1 or D2 stage in a presence of a weak base
CA2777801C (en) * 2009-10-16 2017-05-02 Aracruz Celulose S.A. Differentiated cellulosic fibres from an enzymatic treatment having an acid step
WO2012015452A1 (en) * 2009-11-11 2012-02-02 International Paper Company Effect of low dose xylanase on pulp in prebleach treatment process
WO2012001145A1 (en) * 2010-07-01 2012-01-05 Novozymes A/S Bleaching of pulp
FR2980805B1 (en) * 2011-09-30 2013-09-20 Arkema France ENZYMATIC PRETREATMENT OF WOOD IN A PROCESS FOR THE MANUFACTURE OF MECHANICAL PAPER PULP

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5147793A (en) * 1990-10-18 1992-09-15 The Mead Corporation Biocatalytic oxidation using soybean peroxidases
US5785811A (en) * 1992-11-09 1998-07-28 The Mead Corporation Process for treating lignocellulosic material with soybean peroxidase in the presence of peroxide
US20030124710A1 (en) * 2001-10-23 2003-07-03 Novozymes A/S Oxidizing enzymes in the manufacture of paper materials
US20120193047A1 (en) * 2005-04-13 2012-08-02 Novozymes North America, Inc. Methods for reducing chlorine dioxide associated corrosion
US20130105100A1 (en) * 2011-10-27 2013-05-02 Buckman Laboratories International, Inc. Method And Composition For Enzymatic Treatment Of Fiber For Papermaking, And Paper Products Made Therewith
US8652301B2 (en) * 2011-10-27 2014-02-18 Buckman Laboratories International, Inc. Method and composition for enzymatic treatment of fiber for papermaking, and paper products made therewith
US20140069599A1 (en) * 2011-10-27 2014-03-13 Buckman Laboratories International, Inc. Method And Composition For Enzymatic Treatment Of Fiber For Papermaking, And Paper Products Made Therewith
US8784613B2 (en) * 2011-10-27 2014-07-22 Buckman Laboratories International, Inc. Method and composition for enzymatic treatment of fiber for papermaking, and paper products made therewith
US20160177503A1 (en) * 2013-08-09 2016-06-23 Novozymes A/S Reducing content of hexenuronic acids in cellulosic pulp

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
KEGG, integrated database retrieval system for ENZYME 1.11.1.7, DATE UNKNOWN. *

Also Published As

Publication number Publication date
WO2006126983A1 (en) 2006-11-30
US20080190573A1 (en) 2008-08-14
PT1880053T (en) 2019-11-04
BRPI0520253B1 (en) 2016-09-06
EP1880053A1 (en) 2008-01-23
EP1880053B1 (en) 2019-07-31
CN101171386B (en) 2011-11-16
CN102392380A (en) 2012-03-28
CN101171386A (en) 2008-04-30
CA2607827C (en) 2013-11-19
CA2607827A1 (en) 2006-11-30
BRPI0520253A2 (en) 2009-09-15
EP1880053A4 (en) 2013-01-23

Similar Documents

Publication Publication Date Title
US20150308049A1 (en) Chlorine dioxide treatment compositions and processes
KR100303620B1 (en) Enrichment of enzyme reaction
US5700769A (en) Enhancement of enzyme reactions
KR100197048B1 (en) Composition for modifying, decomposing or bleaching lignin, lignin containing materials or similar substances
Ali et al. Aquatic toxicity from pulp and paper mill effluents: a review
EP0772717B1 (en) Process for preparing a lignocellulose-based product, and product obtainable by the process
Moreira et al. Biobleaching of oxygen delignified kraft pulp by several white rot fungal strains
US6258209B1 (en) Multi-component system for modifying, degrading or bleaching lignin, lignin-containing materials or similar substances
US9222078B2 (en) Bleaching of pulp
EP0879318B1 (en) Process for increasing the negative charge on a lignocellulosic material and a modified lignocellulosic material with increased charge density
Shankar et al. Environmental contamination, toxicity profile, and bioremediation approaches for detoxification of paper mill wastewater
CA2826916A1 (en) Chlorine dioxide treatment compositions and processes
Lema et al. Clean biological bleaching processes in the pulp and paper industry
CN1718918B (en) A method for synergistic action of multiple enzymes to remove resin in pulp
Gupta et al. Bioresources, environmental aspects, and patent scenario for biobleaching in pulp and paper industry
Moreira et al. Oxalic acid extraction as a posttreatment to increase the brightness of kraft pulps bleached by white-rot fungi
Devakumari Fungal Enzymes in Decolorizing Paper Pulp
Gutiérrez Suárez et al. The biotechnological control of pitch in paper pulp manufacturing
Tachibana et al. Studies on Biological Treatment of Mechanical Pulps (I) Screening of Wood-Rot Fungi depressing Color Reversion of Mechanical Pulps
JPH0625986A (en) Method for bleaching pulp with ozone

Legal Events

Date Code Title Description
STPP Information on status: patent application and granting procedure in general

Free format text: FINAL REJECTION MAILED

STCV Information on status: appeal procedure

Free format text: NOTICE OF APPEAL FILED

STCB Information on status: application discontinuation

Free format text: ABANDONED -- FAILURE TO RESPOND TO AN OFFICE ACTION