Methods of pulp fiber treatment

a technology of pulp fiber and pulp fiber, applied in the field of pulp fiber treatment, can solve the problems of reducing fiber yield and fiber strength, damage to cellulose fiber, and damage to cellulose fiber, and achieve the effect of high activity

Inactive Publication Date: 2017-06-08
CLEAN CHEM
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Benefits of technology

[0066]In some embodiments, the peracetate oxidant is generated at, or near, the point of use as an aqueous solution due to its high activity and relatively short half-life of minutes to hours depending on concentr

Problems solved by technology

Reactive oxygen radical species such as superoxide and peroxyl radicals are known to form during higher pressure and temperature oxygen delignification processes and can cause damage to cellulose fibers.
It is generally known in the art that cellulose fibers are susceptible to damage by radical species, which reduces fiber yield and fiber strength.
However, excessive alkali concentrations or exposure times will also cause damage to cellulose fiber.
Relying on a dye mediated photooxidation process is not practical for pulp delignification due to optically opaque pulp mixtures and the rapid breakdown of photosensitive dyes by singlet oxygen and other ROS.
Furthermore, there are few economically viable options for delignification of wood and non-wood pulps on smaller scales than those feasible for traditional pulp and kraft pulp mills.
Oxygen delignification has very high capital costs and significant operating and maintenance costs.
A small fraction of the sodium peracetate can be present as peracetic acid, however, peracetic acid is consumed by reactions with sodium peracetate and does not reach significant concentrations in solution.
Exposure to sodium peracetate solution is limited to inhalation of an aerosol or mist and exposure to liquid concentrates.
The use of elevated concentrations of chlorine dioxide in water treatment is particularly hazardous.
Pulp bleaching operations using chlorine dioxide at several hundred to several thousand mg/L concentrations and elevated temperatures pose severe exposure hazards over large areas if not properly contained.
Gases are more difficult to contain than liquid solutions with low vapor pressures.
Water used in chlorine and chlorine dioxide bleaching stages is not compatible with recovery boilers and other process equipment outside of the bleaching circuit due to the highly corrosive chloride and chlorate content.
Chlorides would accumulate in closed loop processes in a pulp mill used upstream of the bleaching circuit causing corrosion damage to conventional process equipment.
Corrosivity of radical compounds used in the delignification, brightening and bleaching stages is another issue, especially when these compounds come in contact with various process materials such as steel, copper and brass alloys.
Compounds that are gases in their native form are the most volatile and present the greatest corrosion and occupational exposure hazards, including chlorine, chlorine dioxide and ozone.
Importantly, when biofilms and their detritus detach from surfaces in the wet end papermaking process, they can cause holes and other defects in finished paper products.
Some bacteria are pathogenic, for example, Legionella pneumophila, which poses health risks.
Some algae, such as cyanobacteria, produce algal toxins that pose potential health hazards.
Commonly used oxidizing biocides

Method used

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embodiments

[0093]In some embodiments, the ROS-generating peracetate formulation of the present invention may be used for delignification and extraction of materials from pulp fibers for brightening and bleaching purposes. It may also be used for extracting lignin from cellulosic fibers for the recovery of lignin from the black liquor or spent oxidant liquor.

[0094]In some embodiments, the ROS generated by the parent peracetate formulation, particularly singlet oxygen, are the primary chemical species doing the delignification, brightening and bleaching of fibers. The direct reaction of peracetate with pulp is minimal, which contrasts with the use of peracetic acid in combination with hydrogen peroxide as the primary oxidants, which have much lower performance efficiency (and therefore, higher cost) for delignification, brightening and bleaching.

[0095]In some embodiments, the peracetate oxidant formulation of this invention produces singlet oxygen as the primary reactive oxidant species and ther...

example 1

Paper Mill Treatment

[0204]Sodium peracetate oxidant solution is used to control microbial growth in a printing paper mill in stock preparation and white water recovery. White water entrains fiber, chemicals and microbes from the paper web. Microbes have an opportunity to propagate during extended residence time in the white water chest. Pulp sources entering the machine chest, such as boke and recovered fiber, will carry elevated microbial loads after their recovery form the paper machine process. Microbial concentrations can exceed 106 to 107 cells / mL, a level that reduces paper quality, accelerates biofilm growth and microbially influenced corrosion, increases paper defects and odor problems. These problems increase the frequency of down time for maintenance and increase paper reject.

[0205]Several points exist where the peracetate oxidant solution can be added to the paper mill process. Ideally the peracetate solution is added to a fluid (water and pulp) where there is a contact t...

example 2

Disinfection of Feedstocks for Bio-Based Chemical Production

[0210]Sodium peracetate oxidant was used for microbial disinfection of polysaccharide feedstock materials used for producing succinic acid and lactic acid in a fermentation process. The peracetate is blended with the feedstock mixture in a blending tank to make an initial sodium peracetate concentration of up to about 130 ppm (by weight) and this mixture is heated to around its fermentation temperature of about 50-60° C. In this temperature range thermal activation of the peracetate oxidant occurs which increases antimicrobial activity and the rate of oxidant consumption such that the treatment is more rapidly finished and oxidant residual is eliminated before entering the fermentation stage containing the engineered microbes.

[0211]The thermally activated peracetate disinfection treatment is conducted for 30 to 90 minutes depending on the oxidant consumption rate, solids loading and particle size of the feedstock materials....

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Abstract

In some embodiments, a method may include treating pulp in pulp and paper mills. The methods may include providing a peracetate oxidant solution and generating a reactive oxygen species. The peracetate solution may include peracetate anions and a peracid. In some embodiments, the peracetate solution may include a pH from about pH 10 to about pH 12. In some embodiments, the peracetate solution has a molar ratio of peracetate anions to peracid ranging from about 60:1 to about 6000:1. In some embodiments, the peracetate solution has a molar ratio of peracetate to hydrogen peroxide of greater than about 16:1. The peracetate oxidant solution may provide enhanced treatment methods of bleaching, brightening, and delignifying pulp fibers involving the use of peracetate oxidant solutions.

Description

PRIORITY CLAIM[0001]This application claims priority to U.S. Provisional Patent Application No. 62 / 263,900 entitled “METHODS OF MICROBIAL CONTROL” filed on Dec. 7, 2015, all of which is incorporated by reference herein.BACKGROUND OF THE INVENTION[0002]1. Field of the Invention[0003]The present disclosure generally relates to pulp fiber treatment using peracetate oxidant solutions. The disclosure more particularly relates to methods of bleaching, brightening, and delignifying pulp fibers involving the use of peracetate oxidant solutions.[0004]2. Description of the Relevant Art[0005]A variety of methods have been developed for delignification of wood pulp fibers after the initial pulping to achieve brighter unbleached grades and bleachable grades (e.g., kappa number 10-15). Common delignification methods include reductive methods (e.g., extended or enhanced sulfide digestion), oxidative methods (e.g., oxygen delignification, alkaline hydrogen peroxide extraction and combinations), and...

Claims

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Application Information

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IPC IPC(8): D21C9/16C12P3/00
CPCC12P3/00D21C9/166C02F1/76C02F2209/04C02F2103/28C02F1/02C02F1/722C02F1/766C02F2303/02C02F2303/04C02F2303/08C02F2303/20C02F2101/345C02F2209/36C02F2103/32D21C9/1063D21C9/147C02F1/008C02F1/50C02F9/00C02F2103/007C02F2103/023
Inventor BUSCHMANN, WAYNE E.WATERS, DAMON C.
Owner CLEAN CHEM
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