Water Treatment Unit Comprising a Plurality of Filtration Devices
US-2024308884-A1 · Sep 19, 2024 · US
US10322946B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10322946-B2 |
| Application number | US-201214127725-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jul 10, 2012 |
| Priority date | Jul 11, 2011 |
| Publication date | Jun 18, 2019 |
| Grant date | Jun 18, 2019 |
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The present invention relates to a process for the reduction of pitch in an aqueous medium generated in a papermaking or pulping process, comprising the following steps: a) providing an aqueous medium comprising pitch generated in a papermaking or pulping process; b) providing a ground calcium carbonate and/or a precipitated calcium carbonate; c) providing a hydrophobizing agent selected from an aliphatic carboxylic acid having between 5 and 24 carbon atoms; d) contacting the ground calcium carbonate and/or the precipitated calcium carbonate of step b) with the hydrophobizing agent of step c) for obtaining a hydrophobized ground calcium carbonate and/or a hydrophobized precipitated calcium carbonate; and e) contacting the aqueous medium provided in step a) with the hydrophobized ground calcium carbonate and/or the hydrophobized precipitated calcium carbonate obtained in step d), to the use of a hydrophobized ground calcium carbonate and/or a hydrophobized ground calcium carbonate for reducing the amount of pitch in an aqueous medium as well as to a hydrophobized ground calcium carbonate and/or a hydrophobized ground calcium carbonate and a composite of hydrophobized ground calcium carbonate and/or hydrophobized ground calcium carbonate and pitch.
Opening claim text (preview).
The invention claimed is: 1. A process for reducing pitch from paper pulp in an aqueous medium comprising the following steps: a) providing an aqueous medium comprising pitch from paper pulp, wherein the pitch is natural resin from the paper pulp, wherein the paper pulp is selected from the group consisting of mechanical pulp, ground wood, TMP (thermo mechanical pulp), chemithermomechanical pulp (CTMP), chemical pulp, and kraft or sulphate pulp, and wherein the pulp is not recycled pulp; b) contacting the aqueous medium provided in step a) with calcium carbonate consisting of a partially hydrophobised ground calcium carbonate and/or partially hydrophobised precipitated calcium carbonate so that the calcium carbonate adsorbs pitch in the aqueous medium, wherein the aqueous medium is contacted with 0.05 to 20 wt.-% of the partially hydrophobised ground calcium carbonate and/or the partially hydrophobised precipitated calcium carbonate, based on the total weight of the aqueous medium, wherein the adsorbed pitch is natural resin from the paper pulp, and wherein the partially hydrophobised ground calcium carbonate and/or a partially hydrophobised precipitated calcium carbonate is ground calcium carbonate and/or precipitated calcium carbonate that has been mixed with a hydrophobising agent selected from the group consisting of one or more aliphatic carboxylic acids having between 5 and 24 carbon atoms at a temperature of at least 50 ° C. such that the hydrophobising agent is in a liquid or molten state and less than 20% of the specific surface area of the ground calcium carbonate and/or the precipitated calcium carbonate is covered by a coating consisting of the hydrophobising agent and reaction products thereof; and c) separating the calcium carbonate with adsorbed pitch from the aqueous medium. 2. The process according to claim 1 , wherein the ground calcium carbonate (GCC) is obtained from marble, chalk, calcite, dolomite, limestone or any mixture thereof, and the precipitated calcium carbonate (PCC) is selected from the group consisting of one or more of aragonitic, vateritic and calcitic mineralogical crystal forms. 3. The process according to claim 1 , wherein the ground calcium carbonate and/or the precipitated calcium carbonate is in the form of a powder or in the form of slurry. 4. The process according to claim 1 , wherein the ground calcium carbonate particles and/or the precipitated calcium carbonate particles have a weight median particle diameter d 50 value of from 0.1 to 50 μm, measured according to the sedimentation method. 5. The process according to claim 1 , wherein the ground calcium carbonate particles and/or the precipitated calcium carbonate particles have a weight median particle diameter d 50 value of from 0.1 to 25 μm, measured according to the sedimentation method. 6. The process according to claim 1 , wherein the ground calcium carbonate particles and/or the precipitated calcium carbonate particles have a weight median particle diameter d 50 value of from 0.1 to 15 μm, measured according to the sedimentation method. 7. The process according to claim 1 , wherein the ground calcium carbonate particles and/or the precipitated calcium carbonate particles have a weight median particle diameter d 50 value of from 0.5 to 5 μm, measured according to the sedimentation method. 8. The process according to claim 1 , wherein the ground calcium carbonate particles and/or the precipitated calcium carbonate particles have a specific surface area of from 0.5m 2 /g to 25 m 2 /g, measured using nitrogen and the BET method. 9. The process according to claim 1 , wherein the ground calcium carbonate particles and/or the precipitated calcium carbonate particles have a specific surface area of from 0.5 m 2 /g to 15 m 2 /g, measured using nitrogen and the BET method. 10. The process according to claim 1 , wherein the ground calcium carbonate particles and/or the precipitated calcium carbonate particles have a specific surface area of from 1 m 2 /g to 11 m 2 /g, measured using nitrogen and the BET method. 11. The process according to claim 1 , wherein the hydrophobising agent is selected from the group consisting of pentanoic acid, hexanoic acid, heptanoic acid, octanoic acid, nonanoic acid, decanoic acid, undecanoic acid, lauric acid, tridecanoic acid, myristic acid, pentadecanoic acid, palmitic acid, heptadecanoic acid, stearic acid, nonadecanoic acid, arachidic acid, heneicosylic acid, behenic acid, tricosylic acid, lignoceric acid, and any mixture thereof. 12. The process according to claim 1 , wherein the hydrophobising agent is selected from the group consisting of octanoic acid, decanoic acid, lauric acid, myristic acid, palmitic acid, stearic acid, arachidic acid, and any mixture thereof. 13. The process according to claim 1 , wherein the hydrophobising agent is selected from the group consisting of myristic acid, palmitic acid, stearic acid, and any mixture thereof. 14. The process according to claim 1 , wherein the hydrophobising agent comprises a mixture of two aliphatic carboxylic acids having between 5 and 24 carbon atoms, with the proviso that one aliphatic carboxylic acid is stearic acid. 15. The process according to claim 14 , wherein one aliphatic carboxylic acid is stearic acid and the other one is selected from the group consisting of octanoic acid, myristic acid, palmitic acid, arachidic acid, behenic acid, and lignoceric acid. 16. The process according to claim 1 , wherein the mixing of the ground calcium carbonate and/or the precipitated calcium carbonate with the hydrophobising agent is carried out at a temperature of at least 75 ° C. 17. The process according to claim 1 , wherein the mixing of the ground calcium carbonate and/or the precipitated calcium carbonate with the hydrophobising agent is carried out at a temperature of between 50 ° C. and 120 ° C. 18. The process according to claim 1 , wherein the mixing of the ground calcium carbonate and/or the precipitated calcium carbonate with the hydrophobising agent is carried out at a temperature of between 70 ° C. and 100 ° C. 19. The process according to claim 1 , wherein the partially hydrophobised ground calcium carbonate and/or the partially hydrophobised precipitated calcium carbonate is ground calcium carbonate and/or precipitated calcium carbonate in which between 10% and 19% of its specific surface area is covered by a coating consisting of the hydrophobising agent and reaction products thereof. 20. The process according to claim 1 , wherein the partially hydrophobised ground calcium carbonate and/or the partially hydrophobised precipitated calcium carbonate is ground calcium carbonate and/or precipitated calcium carbonate in which between 13% and 17% of its specific surface area is covered by a coating consisting of the hydrophobising agent and reaction products thereof. 21. The process according to claim 1 , wherein in step b) the aqueous medium is contacted with 0.05 to 10 wt.-% of the partially hydrophobised ground calcium carbonate and/or the partially hydrophobised precipitated calcium carbonate, based on the total weight of the aqueous medium. 22. The process according to claim 1 , wherein in step b) the aqueous medium is contacted with 0.1 to 5 wt.-% of the partially hydrophobised ground calcium carbonate and/or the partially hydrophobised precipitated calcium carbonate, based on the total weight of the aqueous medium. 23. The process according to claim 1 , wherein the partially hydrop
from the paper or cellulose industry · CPC title
using synthetic organic sorbents · CPC title
Non-macromolecular compounds · CPC title
Removal of fats, resins, pitch or waxes; {Chemical or physical purification, i.e. refining, of crude cellulose by removing non-cellulosic contaminants, optionally combined with bleaching (fats, waxes C11B; natural resins C09F1/00; hemicellulose C08B37/14; purification by mechanical means D21D5/00)} · CPC title
Agents for preventing deposition on the paper mill equipment, e.g. pitch or slime control (removal of fats, resins, pitch, or waxes D21C9/08) · CPC title
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