Classifications

• • 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
  • D21H17/03—Non-macromolecular organic compounds
  • D21H17/05—Non-macromolecular organic compounds containing elements other than carbon and hydrogen only
  • D21H17/17—Ketenes, e.g. ketene dimers
• • 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
  • D21H17/03—Non-macromolecular organic compounds
  • D21H17/05—Non-macromolecular organic compounds containing elements other than carbon and hydrogen only
  • D21H17/14—Carboxylic acids; Derivatives thereof
  • D21H17/15—Polycarboxylic acids, e.g. maleic acid
  • D21H17/16—Addition products thereof with hydrocarbons
• • 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
  • D21H17/65—Acid compounds
• • 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
  • D21H21/00—Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties
  • D21H21/06—Paper forming aids
  • D21H21/12—Defoamers

Definitions

• the present invention is concerned with reducing the problems caused by foam formation during the production of paper.
• Paper produced under alkaline or neutral conditions using cyclic acid anhydrides, especially alkyl or alkenyl succinic anhydrides (ASA) as sizes.
• ASA alkyl or alkenyl succinic anhydrides
• Sizing paper with alkenyl succinic anhydrides (ASA) at or about a neutral pH, using paper stock containing calcium carbonate as a neutral whitening filler is a well known process, but it is known to produce an unacceptable amount of foam in the paper machine white water recycle.
• the foam accumulates as white pitches in the white water recycle and is transported with the paper stock to the paper machine head box. Although silicones and other anti-foam additives are sometimes added they do not give adequate foam reduction.
• the sizing is carried out by metering ASA as an emulsion into the paper stock in the wet end of the paper machine just before feeding the diluted paper stock to the Fourdrinier table.
• the paper stock contains 20-30% (on dry cellulose) calcium carbonate as an inert filler. More recently it has been proposed in European Patent
• Suitable technologies have been developed to produce emulsion involving both dynamic and static mixing (US Patent R 29960) , ancillary materials, classified as activators, promoters and stabilizers, to optimise ASA emulsions with respect to sizing, retention and paper machine runnability.
• the place to introduce the ASA emulsion in the paper machine can be chosen according to various plant needs, it is customary to select a position to minimize hold time and where the fluid is turbulent to facilitate ASA mixing with the paper stock
• ASA are easily hydrolysable compounds which produce alkenyl succinic acid on reaction with water.
• the acid is not active in sizing paper (TAPPI Journal 70 12 117-121 1987) .
• TAPPI Journal 70 12 117-121 1987 it builds up in the white water recycle to a point when the production of foam and of white pitches occurs with the appearance of dark spots in the paper.
• Plating out of the white pitches also occurs on several critical places of the paper machine (such as the Fourdrinier net, the drying section's felts, the head box and in the piping system) with a consequent productivity decrease mainly due to press picking, felt soilage and lowered drainage.
• ASA's hydrolysis kinetics indicate a rapid reaction whose rate increases with temperature and pH and it is a function of the emulsion's particle size (TAPPI Alkaline Papermaking 1985 17-20) .
• the ASA emulsion in water is therefore generally produced on site just before its introduction in the paper machine to minimize hydrolysis.
• ASA emulsions A number of formulations are available to the paper industry to prepare ASA emulsions see (TAPPI Alkaline Papermaking 1985 113-133, TAPPI Sizing short course 1987 89-91) . They are based on an emulsifier compound (such as sulfosuccinates, nonylphenol adducts with ethylene and propylene oxides and the like) and natural and synthetic organic compounds bearing positive charges (such as cationized starch, polyamines and the like) .
• an emulsifier compound such as sulfosuccinates, nonylphenol adducts with ethylene and propylene oxides and the like
• natural and synthetic organic compounds bearing positive charges such as cationized starch, polyamines and the like
• An improved sizing process which maximizes ASA first pass retention, involves metering ASA neat or in solution, as a fine spray,
• SUBSTITUTE SHEET directly into the paper stock through a nozzle is described in European Patent Application 8930617.8.
• the improved retention obtainable with the spray-mixing technique depends on several parameters including: ASA particle diameter distribution, presence of ASA-soluble, inert compounds, absence of emulsifiers, a 2-3 orders of magnitude lower contact time with water compared with the emulsion process, etc.
• the main purpose of the present invention is to eliminate the technical and cost problems, as previously described, encountered due to foam formation particularly in the ASA-based paper sizing technology.
• the foam is composed of calcium carbonate mixed with small amounts of fines and traces of calcium succinate, an ionic surfactant. It includes also moderate to large amounts of air.
• air microbubbles when brought into contact with a calcium carbonate surface, do not spontaneously adhere thereto.
• a hydrophobic material such as an alkenyl succinic moiety, coats the surface of the calcium carbonate particle the air microbubbles may attach readily to it floating the calcium carbonate particles typically of diameter 0.2-0.5 microns to the surface so that they accumulate as a frothy foam on top of the process liquid.
• ASA hydrolysates are essentially alkyl or alkenyl succinic acid dissolved in or dissolving unhydrolysed ASA. They produce a hydrophobic material adhering by chemisorption to calcium carbonate and in part reacting with the production of calcium succinate.
• foam in the paper making process may be depressed by addition to the paper stock of water soluble salts of a polybasic acid such as sodium hydroxide-treated polymerised silica of the general formula NA2 ⁇ -mSi ⁇ 2-nH2 ⁇ where m and n are the number of Si0 2 and H2O moles relative to one mole of Na2 ⁇ .
• a polybasic acid such as sodium hydroxide-treated polymerised silica of the general formula NA2 ⁇ -mSi ⁇ 2-nH2 ⁇ where m and n are the number of Si0 2 and H2O moles relative to one mole of Na2 ⁇ .
• salts which may be used as foam depressants include sodium derivatives of polyacids such as polyphosphoric acids, polyphosphonic acids, ethylene tetracetic acid, polyacrylic acids, hydrocolloids, polysaccarides, etc.
• the present invention therefore provides the use as a foam suppressant in alkaline or neutral paper making containing calcium carbonate of a water soluble salt of a polybasic acid or its water colloidal dispersion.
• the invention provides a process for making paper under alkaline or neutral conditions comprising adding thereto an amount sufficient to depress foam formation of a water soluble salt of a polybasic acid or its water colloidal dispersion.
• the invention provides such a use or such a process as previously described in which the paper is sized with a cyclic acid anhydride particularly an alkyl or alkenyl succinic acid anhydride.
• the treatment of the calcium carbonate with the foam dispersant is carried out either batchwise or preferably on-line when the pigment slurry is added to the paper stock. While the foam suppressant and calcium carbonate introduction points could be different, we prefer they are the same and are preferably positioned downstream of the position at which the size is added to the paper stock
• foam depression by surface blocking occurs because the depressants preferably bind themselves to the calcium carbonate surface thus preventing air microbubbles from adhering to calcium carbonate particles and floating them upward (A.T. Taggart, Elements of ore dressing, John Wiley & Sons Inc. , New York 1951 pages 263 to 281) .
• SUBSTITUTE SHEET This invention may be applied to the production of paper or similar products, such as board, cardboard etc. , based on cellulose or synthetic fibres.
• Paper, board, cardboard and other similar products are produced by first dispersing the cellulose or synthetic fibres in large quantities of water and the dispersion passed to a paper making machine where the water is removed to form the continuous paper web.
• the product is treated with various chemicals which may be injected into the aqueous dispersion of the fibres.
• One particular treatment common to most paper making processes is sizing.
• Sizing of paper is well known, two typical sizing materials are alkyl-ketene di ers and alkenyl succinic anhydrides. These products are generally used in emulsion form as described in, for example, Japanese Patent Publications 62-231099; 61-146898; 61-160495; 52-25102; 60-20905. Whilst the present invention is concerned with sizing in general it is particularly concerned with sizing with alkenyl succinic anhydrides, and alkyl ketene dimers.
• United Kingdom Patent 1492104 describes the use of polyoxyalkylene alkyl or arylalkyl ethers, or the corresponding mono- and di-esters derivatives to produce emulsions of cyclic acid anhydrides with a low input of shear energy. Such emulsions are used to disperse intimately the anhydrides into the cellulose stock to produce sized paper. The sizing emulsion can be produced in-situ, within the cellulose stock, or prior to introduction into the cellulose stock.
• the emulsions are preferably prepared in the presence of cationised stabilisers such as cationized starches, polyaminoethyl acrylate resins, polyamide resins having free amino groups, reacted or not with epichlorohydrin etc.
• cationised stabilisers such as cationized starches, polyaminoethyl acrylate resins, polyamide resins having free amino groups, reacted or not with epichlorohydrin etc.
• cationic stabilizers The main function of these cationic stabilizers is to charge positively the emulsion's particles favouring their absorption by Coulombic attraction on the negatively charged surface of the cellulose fibres.
• the reactive synthetic sizing compound is continuously dispersed in the form of fine droplets into the wet-end of the paper machine, preferably in places where the cellulose stock water slurry is under high turbulence, to obtain rapid and complete contact of the sizing compound with the paper stock. If necessary turbulence can be controlled by the provision of baffles and stirrers in the flow of the slurry.
• the absorption of the sizing compound droplets on the cellulosic fibres is aided by a cationizing treatment either the fibres may have undergone such treatment either on-line or in the paper stock preparation tubs alternatively the size may be cationised by for example, addition together with a cationising compound.
• a cationizing treatment is a standard technique in paper production to favour the retention of wet-strength resins, of mineral charges, etc, which otherwise would be in large part lost.
• the cationization is generally carried out with long chain fatty amines, synthetic polymers containing amines, cationic modified starches, polyamide-amine resins and other cationized products. Typically 0.02 to 3.50 wt% of cationizing agent based on the weight of dry fibre is used.
• the combined action of the extremely low contact time with the process water and the natural hydrophobicity of the sizing compound prevent its hydrolytic degradation and the resulting waste. Moreover, by lowering the droplets diameter to very low values, the interactions with the cellulose fibres and the sizing compound absorption can be improved thus increasing the sizing yield to a level beyond that which can be achieved with the current emulsion technology.
• the solutions of certain gases, such as methane, propane, butane, chlorofluoro hydrocarbons, carbon dioxide, etc. , in the synthetic sizing compound are sprayed in form of fine droplets directly into the wet-end of the paper machine or onto the formed paper web before the machine drying section, or in the size press.
• a range of gas-sizing compound compositions may be used.
• a preferred composition could be experimentally determined because it may depend from the type of paper produced in a given machine and from the process parameters.
• the dissolved gas concentration may be in the range 20 to 50% on the sizing compound although for economic reasons it is preferable that gas concentrations be kept in the range 1 to 19% if the cost factor is very important.
• the sizing compound gas solutions could also be obtained by previously mixing gas types with low and high solubility into the
• SUBSTITUTESHEET sizing compound such as nitrogen and carbon dioxide, nitrogen and methane.
• the reactive synthetic sizing compound is first dissolved in an anhydrous, aprotic, water-soluble, inert solvent.
• the solution is sprayed with one or more nozzles as fine droplets directly into the water-cellulose slurry at the paper machine wet-end.
• the inert solvent is dissolved by the process water thus protecting the reactive sizing compound droplets from water's hydrolytic action and generating in-situ a fresh surface in the presence of cellulose.
• aprotic compounds examples include ketones, esters, ethers, aromatic and aliphatic hydrocarbons, (for example acetone, methylethyl ketone, acetonyl acetone, methyl acetate, ethylene glycol diacetate, dioxane, etc) .
• a range of solvent concentrations in the solutions with the sizing compound can be considered. The preferred composition will be determined by experiment depending on the process parameters. Cost considerations would indicate that solvent concentrations in the range 1 to 19% may be preferred to concentrations in the range 20 to 50% or higher, also to avoid the solvents accumulation in the water recycle system.
• the reactive sizing compound is dissolved in an anhydrous, protic, water soluble compound immediately before being sprayed and transformed into fine droplets.
• Preferred concentrations of the protic anhydrous solvent with the reactive sizing compound are as previously disclosed in the case of the aprotic solvents.
• Classes of such solvents include alcohols, etheralcohols, esteralcohols (e.g. methyl alcohol, ethyl alcohol, 2-butoxyethanol, ethylene glycol monoacetate, 2-(2 butoxyethanol) , etc.
• the paper web is dried by heating to temperatures in the range 90 to 120°C thus favouring the reaction between the reactive sizing compound and the hydroxyl groups of the cellulose. This may be performed by the heated cylinders which provide also the pressure needed to impregnate the paper web surface and thickness with the reactive sizing compound.
• the preferred synthetic reactive sizing compounds are cyclic acid anhydrides of the general formula
• R;L is an organic hydrophobic group. More preferred are the liquid cyclic acid anhydrides in which R ] ⁇ is a branched chain C 8 -C 16 alkenyl group.
• Typical examples of cellulose that may be treated with the sizing compounds are derived from hardwoods and softwoods, bleached or not bleached, semi-chemical, groundwood and combinations thereof. Synthetic rayon or regenerated cellulose fibres may also be used as well as waste paper and cardboard.
• Bleached sulphate cellulose (60% hardwood, 40% softwood) of freeness 35°SR and concentration 40 g per litre in tap water (hardness 17 French degrees) is treated with 0.25 to 0.50% hydrated aluminium sulphate (alum) as a 100 g per litre solution in tap water.
• Cationized potato starch (Roquette Fr. HICAT 180 brand) , of concentration around 5% in demineralized water, is cooked at 85-90 ⁇ C for 30 minutes and subsequently diluted about 5 times. Limited amounts of starch are cooked and normally used within 12-24 hours from cooking to prevent ageing effects.
• Calcium carbonate (Craie Micronic 0 brand) is pre-slurried in tap water at the concentration 350 g per litre.
• SUBSTITUTESHEET D Alkenyl succinic anhydride (Exxon Chemical Co. brand) , having a C 12 branched side chain, and FIBRAN 76 (Roquette Fr. brand) , having a C ⁇ Q - ⁇ Q side chain, are used as sizing agents.
• An amount of the paper stock A previously treated with 0.25% alum is fed to a 5 m 3 feed tub and it is treated with 0.5% cooked cationic potato starch B.
• the paper stock amount is limited to about 1 hour of machine feed to prevent unwanted ageing effects.
• a piston metering pump connected to a spraying nozzle is used to spray-mix neat FIBRAN 76 D into a stream of tap water at 40-50°C and the mixture is fed at the rate of 0.5m 3 Ton -1 dry cellulose to the suction side of the pump feeding the alum-treated paper stock to the paper machine.
• FIBRAN 76 is fed at the rate of 0.25% to maximize foaming effects, if any.
• the paper machine is constructed by SICMA, Terni, Italy. It is fitted with a Fourdrinier net width 0.56m and a series of 22 steam-heated drying cylinders, running at the speed of 40 m. in" 1 and producing about 100 kg paper per hour. The grammage is kept at about 80-85 g.m 2 .
• polyacrylamide F 0.038% polyacrylamide F is finally added to the paper stock just before it enters the head box.
• the paper web is dried in the machine drying section, whose steam-heated cylinders are programmed to reach temperatures in the range 50-110°C, before being wound up.
• Comparative Example 1 is repeated by using a branched chain C 12 alkenyl succinic anhydride D (EXXON CHEMICAL CO) as the sizing agent.
• a branched chain C 12 alkenyl succinic anhydride D EXXON CHEMICAL CO
• SUBSTITUTESHEET Severe foaming is also observed and formation of white pitches. An average 950 dark spots per m 2 is counted in the paper produced making it totally unsuitable for sale.
• Comparative Example 2 is repeated in runs 1, 2, 3 and 4.
• Sodium polysilicate G is metered on-line into the paper stock on the suction side of the fan pump together with calcium carbonate slurried in water.
• the paper stock pH after addition is in the range 7.2 to 7.6.
• Runs 3 and 4 were carried out with a paper stock pretreated with 0.5% alum and Run 4 with 0.3% of the size to maximise foaming and white pitches, if any.
• SUBSTITUTE SHEET Small amounts or no foam is produced and absence of white pitches are observed in all runs. The presence of dark spots in the paper produced averaged about 30-35 units per m 2 indicated that the treatment with sodium polysilicate has drastically decreased white pitches formation.
• Comparative Example 2 is repeated in Runs 5, 6, 7, 8 and 10.
• Run 9 is carried out with FIBRAN 76 as sizing agent for comparison. In all cases, the size concentration is 0.25%.
• Sodium Polysilicate G or polyphosphonic acid H are metered on-line into the paper stock on the suction side of the fan pump together with calcium carbonate slurried in water. The paper stock pH after addition is in the range 7.2 to 7.6.
• Runs 6, 7, 8, 9 and 10 are carried out with decreasing amount of polyacrylamide (from 0.038% as in Comparative Example 1 to 0.019 and 0.0%) .
• Head box paper stock cone g.l -1
• Example 2 is repeated in runs 11 and 12 by using respectively branched chain C ⁇ 2 alkenyl succinic anhydride D (EXXON Chemical Company) and mixture of 92.7% wt of the same with 7.3% wt alkyl ketene dimer E as sizing agents both at the concentration of 0.15%.
• paper stock A is not previously treated with alum and cationized potato starch B.
• a piston metering pump connected to a spraying nozzle, is used to spray-mix neat C.2 alkenyl anhydride D or its mixture with alkyl ketene dimer E into a stream of cationized potato starch demineralized water at the concentration of 1.3% at the rate of 0.38 m 3 .Ton ⁇ 1 dry cellulose.
• Sodium polysilicate G (COMPOZIL) is metered on-line into the paper stock at the rate of 0.33 parts of commercial material pe 100 parts of cellulose on the suction side of the fan pump together with calcium carbonate slurried in water.

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• Chemical & Material Sciences (AREA)
• Inorganic Chemistry (AREA)
• Paper (AREA)
• Investigating Or Analyzing Materials By The Use Of Ultrasonic Waves (AREA)
• Ultra Sonic Daignosis Equipment (AREA)
• Complex Calculations (AREA)
• Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
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• 1991
  • 1991-01-21 DK DK91903705.1T patent/DK0512038T3/da active
  • 1991-01-21 WO PCT/GB1991/000089 patent/WO1991010776A1/en active IP Right Grant
  • 1991-01-21 AT AT91903705T patent/ATE118848T1/de not_active IP Right Cessation
  • 1991-01-21 CA CA002074066A patent/CA2074066A1/en not_active Abandoned
  • 1991-01-21 EP EP91903705A patent/EP0512038B1/en not_active Expired - Lifetime
  • 1991-01-21 DE DE69107611T patent/DE69107611T2/de not_active Expired - Fee Related
  • 1991-01-21 JP JP3503787A patent/JPH10502134A/ja active Pending
  • 1991-01-21 ES ES91903705T patent/ES2068570T3/es not_active Expired - Lifetime
  • 1991-01-22 YU YU39791A patent/YU39791A/sh unknown
  • 1991-01-22 PT PT96547A patent/PT96547B/pt not_active IP Right Cessation
• 1992
  • 1992-07-14 NO NO92922782A patent/NO922782L/no unknown
  • 1992-07-21 FI FI923316A patent/FI923316A0/fi not_active Application Discontinuation

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