Classifications

• • 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
  • D21C9/1026—Other features in bleaching processes
  • D21C9/1042—Use of chelating agents
• • 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
  • D21C9/1005—Pretreatment of the pulp, e.g. degassing the pulp
• • 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
  • D21C9/16—Bleaching ; Apparatus therefor with per compounds

Definitions

• the present invention is related to a process for the bleaching of mechanical paper pulp with one or more peroxide oxidizing agents, in which the paper pulp is pretreated with a chelating agent.
• Powerful chelating agents can be of the aminocarboxylic type, such as ethylene diamine tetra-acetic acid and its salts (EDTA), or diethylene triamine penta-acetic acid and its salts (DTPA). Nevertheless, these chelating agents are poorly biodegradable which can generate environmental problems.
• EDTA ethylene diamine tetra-acetic acid and its salts
• DTPA diethylene triamine penta-acetic acid and its salts
• biodegradable chelating agents such as aspartic acid and its derivatives, substituted on the nitrogen, is described in the international application WO 97/30209 .
• Such products include ethylenediamine-N,N'-disuccinic acid (EDDS) and 2,2'-imino-disuccinic acid (IDS).
• EDDS ethylenediamine-N,N'-disuccinic acid
• IDDS 2,2'-imino-disuccinic acid
• the pretreatment step is conducted at a pH from 4 to 8.
• a first disadvantage of this process is that it does not conduct to an optimal brightness of the paper pulp.
• a second disadvantage is that the pH of the pretreatment step must be measured and maintained in a range from 4 to 8 during the whole step.
• the international application WO 99/464.41 describes a process for the bleaching of mechanical paper pulp with one or more peroxide oxidizing agents, in which the pulp is pretreated with one or more chelating agents chosen from aspartic acid and its derivatives, substituted on the nitrogen, and at a pH above 8.
• the pH of the pretreatment step must be measured during the whole step and must be maintained above 8.
• the purpose of the present invention is to provide a simplified bleaching process, avoiding measurement and control of the pH during the pretreatment step, conducting to an optimal brightness of the paper pulp, while still using biodegradable chelating agents during the pretreatment step.
• the present invention therefore relates to a process for the bleaching of mechanical paper pulp with one or more peroxide oxidizing agents, in which the pulp is pretreated in a pretreatment step with one or more chelating agents chosen from aspartic acid and its derivatives, substituted on the nitrogen atom, characterized in that the initial pH of the pretreatment step, just before adding the one or more chelating agents, is above 8.
• One of the essential features of the present invention resides in solely controlling the initial pH of the pretreatment step, which must be above 8 just before adding the one or more chelating agents, and not measuring it after the addition of the chelating agent, and so until the end of the pretreatment step. It has indeed surprisingly been found that, as the critical pH of the pretreatment step is its initial pH, it is therefore not necessary to control it anymore during the rest of the pretreatment step. This is important as it is known that, due to alkaline demand of the paper pulp, the pH will naturally decrease with time. According to this invention, it is not necessary to measure it during the pretreatment step, nor to keep it above 8 by the addition of pH modifying compounds. It follows therefrom that the pretreatment step of the process is advantageously simplified.
• mechanical paper pulps paper pulps obtained by mechanical treatment.
• paper pulps are pressure groundwood (PGW), stone groundwood (SGW), thermomechanical pulp (TMP), refiner mechanical pulp (RMP), chemithermomechanical pulp (CRMP) and alkaline peroxide mechanical pulp (APMP or APP).
• initial pH of the pretreatment step is meant the pH of the paper pulp just before the addition of one or more chelating agents.
• the pH is measured using equipment normally found in pulp mills for such a purpose.
• control of pH is meant the adjustment of the pH to a certain value.
• pH modifying compounds examples include caustic soda (NaOH) or suitable alternative bases.
• NaOH caustic soda
• these compounds are alkalis because the natural pH of mechanical pulps is generally lower than the one required in practice for efficient control of metal ions.
• the chelating agent used in the pretreatment step is chosen from aspartic acid and its derivatives, substituted on the nitrogen.
• the chelating agent can particularly be chosen from N-carboxymethylaspartic acid, N-(1,2-dicarboxyethyl)-aspartic acid, N-(1,2-dicarboxy-2-hydroxyethyl)-aspartic acid, and compounds according to the formula: where n is 1-3, m is 0-3, p is 1-3, R 1 , R 2 , R 3 and R 4 are H, Na, K, Ca or Mg, R 5 and R 6 are H, CH 2 OH, CH 2 CH 2 OH or CH 2 O(CH 2 CH 2 O) 1-10 CH 2 CH 2 OH 3 and mixtures thereof.
• An especially suitable chelating agent is, for example, ethylenediamine-N,N'-disuccinic acid (EDDS), its various isomers or its alkali metal salts or its earth-alkali metal salts.
• EDDS ethylenediamine-N,N'-disuccinic acid
• IDS 2,2'-iminodisuccinic acid
• IDS 2,2'-iminodisuccinic acid
• chelating agent In the process of the invention, good results are obtained using only one chelating agent. Nevertheless, more than one chelating agent can be used. For example, several chelating agents according to the invention can be combined. A chelating agent according to the invention can also be combined with one or more conventional chelating agents such as aminocarboxylated chelating agents such as EDTA or hydroxycarboxylated chelating agents such as glucaric acid.
• aminocarboxylated chelating agents such as EDTA
• hydroxycarboxylated chelating agents such as glucaric acid.
• the paper pulp is pretreated with one or more chelating agents at an initial pH of at least 8,1.
• the pH is in most cases maximum 11. Within this range, the optimum must be established for each particular pulp.
• the optimal pH is for example equal to or higher than 8,5.
• the optimal pH is equal to or higher than 9, and for others it is equal to or higher than 10.
• the pretreatment step with one or more chelating agent is usually carried out at the temperature generated by the mechanical treatment of the wood.
• the temperature can vary widely and is usually at least 40°C. It is generally less than or equal to 95°C. The temperature may vary from 40 to 95°C.
• the pretreatment step with one or more chelating agent is carried out in the presence of water in order to reach a consistency of at least 1% by weight of dry paper pulp.
• the consistency of the paper pulp is usually less than or equal to 50% by weight of dry paper pulp.
• the consistency of the paper pulp can be highly variable within the range from 1 to 50% by weight of dry paper pulp and will be adapted to the type of equipment available for mixing the chelating agents into the process. In the majority of the cases, a consistency of less than or equal to 10% by weight of dry paper pulp, for instance from 3 to 4% by weight of dry paper pulp, will be suitable. In special cases, higher values, up to 45% by weight of dry paper pulp can be used.
• the chelating agent used in the pretreatment step is used at a concentration by weight of dry paper pulp of at least 0,1 %.
• concentration of the chelating agent by weight of dry paper pulp is usually less than or equal to 1,5%.
• concentration of the chelating agent is highly variable within this range and must be optimized, depending on the paper will. Typical values range from 0,2 to 1,0% by weight of dry paper pulp.
• the duration of the pretreatment step with one or more chelating agent is usually from 5 to 120 minutes, varying from mill to mill. Good results are obtained provided the duration of the pretreatment step is of at least 5 minutes duration before the washing step.
• the oxidizing agent used in the bleaching step is usually chosen from hydrogen peroxide, organic peracids such as peracetic acid, and/or a combination thereof.
• the oxidizing agent is preferably hydrogen peroxide, which is advantageously used in an alkaline medium.
• a washing step is usually conducted between the pretreatment step with one or more chelating agent and the bleaching step with a peroxide oxidizing agent.
• the pretreatment step is conducted at a pH above 8.
• the pretreatment step is conducted at a pH between 4 and 8, according to the international application WO 97/30209 .
• the pH was measured with a Knick Portamess pH-meter (911 pH), with an Ag/AgCl electrode (Mettler Toledo, U402-S7/120).
• the electrolyte was a mixture KCl / AgCl 3M.
• the temperature was compensated with a Knick Pt1000 (ZU0156) probe.
• the pH-meter was calibrated with buffer solutions from Mettler Toledo (pH 7,00 buffer with the reference 9865 and pH 4,01 buffer with the reference 9863).
• the brightness of paper pulp was measured using a Datacolor Elrepho spectrophotometer (SF450) according to the ISO standard 2470.
• TMP mechanical paper pulp
• the pretreatment step was carried out at 60°C, during 20 minutes, at a consistency of 10% by weight of dry pulp and with a concentration of 0,3% in RDDS.
• Initial pH of the pretreatment step of examples 1, C2 and C3 was respectively 9,8, 6,0 and 5,0.
• the pH was measured with the standard laboratory glass electrode described above. The pH was not measured nor adjusted after the addition of the chelating agent, until the end of the pretreatment step.
• the washing step was carried out by diluting the pulp to 4% consistency with water and then thickening it with a press to a consistency around 20%.
• the bleaching step was carried out at 70°C, during 120 minutes, at a consistency of 15% by weight of dry pulp, with a bleach liquor containing 3 % hydrogen peroxide, 2.3% NaOH, and 2% sodium silicate by weight of dry pulp.
• the pH was measured with the standard laboratory glass electrode described above. The pH was not measured nor adjusted after the addition of the chelating agent, until the end of the pretreatment step.
• the washing step was carried out as in Examples 1, C2 and C3.
• the bleaching step was carried out at 70°C, during 120 minutes, at a consistency of 15% by weight of dry pulp, with a bleach liquor containing 3% hydrogen peroxide, 2.08% NaOH, and 2% sodium silicate by weight of dry pulp.
• a mechanical paper pulp (PGW) with an initial brightness of 65,6 °ISO was pretreated with EDDS, washed as per the process in Examples 1, C2 and C3, then submitted to a bleaching process with hydrogen peroxide.
• the pretreatment step was carried out at 60°C, during 20 minutes, at a consistency of 10% by weight of dry pulp and with a concentration of 0.5% in EDDS.
• Initial pH of the pretreatment step of examples 8, 9, C10 and C11 were respectively 10,9, 9,5, 6,9 and 5,1.
• the pH was measured with the standard laboratory glass electrode described above. The pH was not measured nor adjusted after the addition of the chelating agent, until the end of the pretreatment step.
• the washing step was carried out as in Examples 1, C2 and C3.
• the bleaching step was carried out at 70°C, during 120 minutes, at a consistency of 15% by weight of dry pulp, with a bleaching liquor containing 3% hydrogen peroxide, 1.8% NaOH, and 1,5% sodium silicate by weight of dry pulp.
• the final pH is the pH of the reacting medium at the end of the pretreatment step.
• a mechanical paper pulp (PGW) with an initial brightness of 67,0°ISO was pretreated with IDS, washed as per the process in Examples 1, C2 and C3, then submitted to a bleaching process with hydrogen peroxide.
• the pretreatment step was carried out at 60°C, during 20 minutes, at a consistency of 10% by weight of dry pulp and with a concentration of 0.5% in IDS.
• Initial pH of the pretreatment step of examples 17, 18, C19 and C20 were respectively 11,0, 9,0, 7,1 and 5,1.
• the pH was measured with the standard laboratory glass electrode described above. The pH was not measured nor adjusted after the addition of the chelating agent, until the end of the pretreatment step.
• the washing step was carried out as in Examples 1, C2 and C3.
• the bleaching step was carried out at 70°C, during 120 minutes, at a consistency of 15% by weight of dry pulp, with a bleaching liquor containing 3% hydrogen peroxide, 1.8% NaOH, and 1,5% sodium silicate by weight of dry pulp.
• the final pH is the pH of the reacting medium at the end of the pretreatment step.

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• 2006
  • 2006-01-24 EP EP06075155A patent/EP1811080A1/de not_active Withdrawn
• 2007
  • 2007-01-22 PL PL07704046.7T patent/PL1979533T3/pl unknown
  • 2007-01-22 CA CA2636355A patent/CA2636355C/en not_active Expired - Fee Related
  • 2007-01-22 US US12/160,805 patent/US20100163193A1/en not_active Abandoned
  • 2007-01-22 EP EP07704046.7A patent/EP1979533B1/de not_active Not-in-force
  • 2007-01-22 WO PCT/EP2007/050578 patent/WO2007085579A1/en not_active Ceased

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