Process for enhanced deposition and retention of particulate filler on papermaking fibers

• US 5,679,220 A
• Filed: 01/19/1995
• Issued: 10/21/1997
• Est. Priority Date: 01/19/1995
• Status: Expired due to Term

• Current Assignee: International Paper Company
• Original Assignee: International Paper Company
• Inventors: Hart, Paul, Amidon, Thomas, Matthew, M. C., Patnaik, Sanjay
• Primary Examiner(s): Czaja, Donald E.
• Assistant Examiner(s): Fortuna, Jose A.
• Application Number:
  US08/375,485
• Time in Patent Office: 1,006 Days
• Field of Search: 162/158, 162/181.1, 162/181.2, 162/181.4, 162/182, 162/183, 162/185, 162/9
• US Class Current: 162/181.4
• CPC Class Codes: D21H 17/64 Alkaline compounds
• CPC Class Codes: D21H 17/675 Oxides, hydroxides or carbonates
• CPC Class Codes: D21H 17/70 forming new compounds in situ, e.g. within the pulp or paper, by chemical reaction with other substances added separately
• CPC Class Codes: D21H 21/10 Retention agents or drainage improvers

Abstract

A method for enhancing the deposition and retention of particulate filler on papermaking fibers. In a first vessel, there is formed a slurry of papermaking fibers and in a second vessel there is formed a slurry of lime or its equivalent. The fiber slurry is at a consistency of not greater than about 5%. These separately formed slurries are thereafter combined with a gaseous precipitant in a flow reactor and under conditions whereby the gaseous precipitant is subjected to rapid shear and calcium carbonate is deposited in situ on the fibers. Unexpectedly, the reaction time for the formation and deposition of the calcium carbonate filler is very rapid. Control over the pH of the reactants in the reactor is achieved through the sequence of introduction of the reactants to the reactor. Also, through selection of the molar ratio of the gaseous precipitant and lime, the morphology of the calcium carbonate crystals may be controlled.

Claims

1. A method for the deposition of particulate filler on papermaking fibers comprising the steps of,

in separate vessels,

preparing a first slurry of papermaking fibers,

preparing a second slurry of calcium hydroxide or the equivalent thereof,

and thereafter,

combining said first and second slurries with a gaseous precipitant in a flowing stream, under conditions whereby shear is imparted to said gaseous precipitant,

to form in situ calcium carbonate on at least the external surfaces of the fibers.

2. The method of claim 1 and including the step of recovering the filled fibers in a form suitable for their use in papermaking.

3. The method of claim 1 and including the step of adjusting the sequence of introduction of reactants to said flowing stream to effectuate control over the pH of the flowing stream.

4. The method of claim 1 and including the step of adjusting the molar ratio of gaseous precipitant to calcium hydroxide to a value of between about 0.1 and about 10.

5. The method of claim 1 wherein said gaseous precipitant is gaseous carbon dioxide.

6. The method of claim 1 wherein said slurry of papermaking fibers has a consistency of not greater than about 5% based on the dry weight of the fibers.

7. A process for the in situ deposition, in a reactor, of particulate filler onto papermaking fibers, the steps of:

in separate vessels,

preparing a first slurry containing papermaking fibers,

preparing a second slurry containing calcium hydroxide or the equivalent thereof,

and thereafter,

combining said first and second slurries with a gaseous carbon dioxide precipitant in a flowing stream, under conditions whereby shear is imparted to said gaseous precipitant,

to form in situ calcium carbonate on at least the external surfaces of the fibers,

wherein the order of introduction of said first and second slurries and said precipitant is selected from one of (a) premixing of said first and second slurries prior to their introduction as a single flowing stream into said flowing stream, (b) introducing said first slurry into said flowing stream at a most upstream location, introducing said precipitant to said flowing stream at a downstream location from the location of the introduction of said first slurry to said flowing stream, and introducing said second slurry to said flowing stream at a downstream location from the location of the introduction of said precipitant to and introducing a further portion of said second slurry to said flowing stream at a downstream location from the location of the introduction of said further portion of said precipitant to said flowing stream, or (d) introducing at least a portion of said second slurry or a portion of said gaseous precipitant to said flowing stream at a first location downstream of the location of the introduction of said first slurry to said flowing stream, introducing at a second location downstream of said first location at least a further portion of that one of said second slurry or said gaseous precipitant which was not introduced to said flowing stream at said first location.

8. The process of claim 7 and including the step of selecting the molar ratio of the gaseous carbon dioxide to the calcium hydroxide to a value of between about 0.1 and about 10.

9. The process of claim 7 wherein all or a portion of the gaseous precipitant is the final reactant introduced downstream to the reactor.

10. The method of claim 7 wherein said slurry of papermaking fibers has a consistency of not greater than about 5% based on the dry weight of the fibers.