CA2083406C - Press felt conditioner for neutral and alkaline papermaking systems - Google Patents
Press felt conditioner for neutral and alkaline papermaking systems Download PDFInfo
- Publication number
- CA2083406C CA2083406C CA002083406A CA2083406A CA2083406C CA 2083406 C CA2083406 C CA 2083406C CA 002083406 A CA002083406 A CA 002083406A CA 2083406 A CA2083406 A CA 2083406A CA 2083406 C CA2083406 C CA 2083406C
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- Prior art keywords
- fatty acid
- felts
- felt
- neutral
- press
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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Links
- 230000007935 neutral effect Effects 0.000 title claims description 8
- 235000014113 dietary fatty acids Nutrition 0.000 claims abstract description 21
- 239000000194 fatty acid Substances 0.000 claims abstract description 21
- 229930195729 fatty acid Natural products 0.000 claims abstract description 21
- 238000000034 method Methods 0.000 claims abstract description 19
- 230000008569 process Effects 0.000 claims abstract description 17
- 230000008021 deposition Effects 0.000 claims abstract description 14
- 230000003750 conditioning effect Effects 0.000 claims description 16
- 150000004665 fatty acids Chemical class 0.000 claims description 12
- MTNDZQHUAFNZQY-UHFFFAOYSA-N imidazoline Chemical compound C1CN=CN1 MTNDZQHUAFNZQY-UHFFFAOYSA-N 0.000 claims description 11
- 230000014759 maintenance of location Effects 0.000 claims description 10
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical group [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 9
- 125000000217 alkyl group Chemical group 0.000 claims description 7
- 230000002401 inhibitory effect Effects 0.000 claims description 7
- 239000012736 aqueous medium Substances 0.000 claims description 4
- 230000001143 conditioned effect Effects 0.000 claims 1
- -1 fatty acid imidazoline compound Chemical class 0.000 abstract description 12
- 239000013618 particulate matter Substances 0.000 abstract 1
- 239000003795 chemical substances by application Substances 0.000 description 13
- 238000000151 deposition Methods 0.000 description 13
- 239000000356 contaminant Substances 0.000 description 12
- 229920000642 polymer Polymers 0.000 description 10
- 238000012360 testing method Methods 0.000 description 8
- 238000004513 sizing Methods 0.000 description 7
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 6
- 239000002002 slurry Substances 0.000 description 6
- 239000007787 solid Substances 0.000 description 6
- 239000000126 substance Substances 0.000 description 6
- 239000004094 surface-active agent Substances 0.000 description 6
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 5
- 239000000306 component Substances 0.000 description 5
- 239000002245 particle Substances 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 239000002253 acid Substances 0.000 description 4
- 239000004927 clay Substances 0.000 description 4
- 229910052570 clay Inorganic materials 0.000 description 4
- 238000011109 contamination Methods 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 239000011236 particulate material Substances 0.000 description 4
- BDHFUVZGWQCTTF-UHFFFAOYSA-M sulfonate Chemical compound [O-]S(=O)=O BDHFUVZGWQCTTF-UHFFFAOYSA-M 0.000 description 4
- 238000011282 treatment Methods 0.000 description 4
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 3
- 229920002125 Sokalan® Polymers 0.000 description 3
- 125000000129 anionic group Chemical group 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 3
- 229910000019 calcium carbonate Inorganic materials 0.000 description 3
- 125000002091 cationic group Chemical group 0.000 description 3
- 239000011248 coating agent Substances 0.000 description 3
- 238000000576 coating method Methods 0.000 description 3
- 239000000835 fiber Substances 0.000 description 3
- 229920000126 latex Polymers 0.000 description 3
- 229920000847 nonoxynol Polymers 0.000 description 3
- 230000035699 permeability Effects 0.000 description 3
- 239000004584 polyacrylic acid Substances 0.000 description 3
- 239000011734 sodium Substances 0.000 description 3
- 229910052708 sodium Inorganic materials 0.000 description 3
- 239000002023 wood Substances 0.000 description 3
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 description 2
- NIXOWILDQLNWCW-UHFFFAOYSA-N 2-Propenoic acid Natural products OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 2
- DUIOKRXOKLLURE-UHFFFAOYSA-N 2-octylphenol Chemical compound CCCCCCCCC1=CC=CC=C1O DUIOKRXOKLLURE-UHFFFAOYSA-N 0.000 description 2
- ROSDSFDQCJNGOL-UHFFFAOYSA-N Dimethylamine Chemical compound CNC ROSDSFDQCJNGOL-UHFFFAOYSA-N 0.000 description 2
- 229910019142 PO4 Inorganic materials 0.000 description 2
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 2
- 150000007513 acids Chemical class 0.000 description 2
- XXROGKLTLUQVRX-UHFFFAOYSA-N allyl alcohol Chemical compound OCC=C XXROGKLTLUQVRX-UHFFFAOYSA-N 0.000 description 2
- WNROFYMDJYEPJX-UHFFFAOYSA-K aluminium hydroxide Chemical compound [OH-].[OH-].[OH-].[Al+3] WNROFYMDJYEPJX-UHFFFAOYSA-K 0.000 description 2
- 229920006318 anionic polymer Polymers 0.000 description 2
- 239000003945 anionic surfactant Substances 0.000 description 2
- 150000001732 carboxylic acid derivatives Chemical class 0.000 description 2
- 229920006317 cationic polymer Polymers 0.000 description 2
- 150000002194 fatty esters Chemical class 0.000 description 2
- 230000016615 flocculation Effects 0.000 description 2
- 238000005189 flocculation Methods 0.000 description 2
- 238000009472 formulation Methods 0.000 description 2
- 150000002462 imidazolines Chemical class 0.000 description 2
- 239000011256 inorganic filler Substances 0.000 description 2
- 229910003475 inorganic filler Inorganic materials 0.000 description 2
- 239000004816 latex Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000002609 medium Substances 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 239000002736 nonionic surfactant Substances 0.000 description 2
- SNQQPOLDUKLAAF-UHFFFAOYSA-N nonylphenol Chemical class CCCCCCCCCC1=CC=CC=C1O SNQQPOLDUKLAAF-UHFFFAOYSA-N 0.000 description 2
- 239000010452 phosphate Substances 0.000 description 2
- 239000000049 pigment Substances 0.000 description 2
- 229920002689 polyvinyl acetate Polymers 0.000 description 2
- 239000011347 resin Substances 0.000 description 2
- 229920005989 resin Polymers 0.000 description 2
- 230000004044 response Effects 0.000 description 2
- 229920005552 sodium lignosulfonate Polymers 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 239000004408 titanium dioxide Substances 0.000 description 2
- HRPVXLWXLXDGHG-UHFFFAOYSA-N Acrylamide Chemical compound NC(=O)C=C HRPVXLWXLXDGHG-UHFFFAOYSA-N 0.000 description 1
- BRLQWZUYTZBJKN-UHFFFAOYSA-N Epichlorohydrin Chemical compound ClCC1CO1 BRLQWZUYTZBJKN-UHFFFAOYSA-N 0.000 description 1
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 1
- 239000005977 Ethylene Substances 0.000 description 1
- IAYPIBMASNFSPL-UHFFFAOYSA-N Ethylene oxide Chemical compound C1CO1 IAYPIBMASNFSPL-UHFFFAOYSA-N 0.000 description 1
- 241000208565 Lignosus Species 0.000 description 1
- UFWIBTONFRDIAS-UHFFFAOYSA-N Naphthalene Chemical compound C1=CC=CC2=CC=CC=C21 UFWIBTONFRDIAS-UHFFFAOYSA-N 0.000 description 1
- 229920002472 Starch Polymers 0.000 description 1
- 239000002174 Styrene-butadiene Substances 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 150000001336 alkenes Chemical class 0.000 description 1
- 125000005907 alkyl ester group Chemical group 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 125000003277 amino group Chemical group 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- MTAZNLWOLGHBHU-UHFFFAOYSA-N butadiene-styrene rubber Chemical compound C=CC=C.C=CC1=CC=CC=C1 MTAZNLWOLGHBHU-UHFFFAOYSA-N 0.000 description 1
- 238000005266 casting Methods 0.000 description 1
- 230000015271 coagulation Effects 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 238000004581 coalescence Methods 0.000 description 1
- 238000013329 compounding Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 150000004985 diamines Chemical class 0.000 description 1
- WASQWSOJHCZDFK-UHFFFAOYSA-N diketene Chemical compound C=C1CC(=O)O1 WASQWSOJHCZDFK-UHFFFAOYSA-N 0.000 description 1
- 125000000118 dimethyl group Chemical group [H]C([H])([H])* 0.000 description 1
- 239000002270 dispersing agent Substances 0.000 description 1
- 230000001804 emulsifying effect Effects 0.000 description 1
- 238000009313 farming Methods 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 239000008394 flocculating agent Substances 0.000 description 1
- WSFSSNUMVMOOMR-UHFFFAOYSA-N formaldehyde Substances O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 description 1
- 239000013505 freshwater Substances 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 239000003112 inhibitor Substances 0.000 description 1
- 239000003446 ligand Substances 0.000 description 1
- 230000000670 limiting effect Effects 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 125000005395 methacrylic acid group Chemical group 0.000 description 1
- 239000000178 monomer Substances 0.000 description 1
- PZNOBXVHZYGUEX-UHFFFAOYSA-N n-prop-2-enylprop-2-en-1-amine;hydrochloride Chemical compound Cl.C=CCNCC=C PZNOBXVHZYGUEX-UHFFFAOYSA-N 0.000 description 1
- 229920000620 organic polymer Polymers 0.000 description 1
- 150000003014 phosphoric acid esters Chemical group 0.000 description 1
- 229920000962 poly(amidoamine) Polymers 0.000 description 1
- 229920002401 polyacrylamide Polymers 0.000 description 1
- 229920000768 polyamine Polymers 0.000 description 1
- 239000011118 polyvinyl acetate Substances 0.000 description 1
- 230000002028 premature Effects 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 238000010526 radical polymerization reaction Methods 0.000 description 1
- 150000003254 radicals Chemical class 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 230000002829 reductive effect Effects 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 150000003333 secondary alcohols Chemical class 0.000 description 1
- 238000004904 shortening Methods 0.000 description 1
- 239000008107 starch Substances 0.000 description 1
- 235000019698 starch Nutrition 0.000 description 1
- 239000011115 styrene butadiene Substances 0.000 description 1
- 229920003048 styrene butadiene rubber Polymers 0.000 description 1
- 229940014800 succinic anhydride Drugs 0.000 description 1
- 150000003871 sulfonates Chemical class 0.000 description 1
- 229920003169 water-soluble polymer Polymers 0.000 description 1
- 230000004584 weight gain Effects 0.000 description 1
- 235000019786 weight gain Nutrition 0.000 description 1
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
- 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
- D21H21/02—Agents for preventing deposition on the paper mill equipment, e.g. pitch or slime control
-
- 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
- D21H17/07—Nitrogen-containing compounds
Landscapes
- Paper (AREA)
- Filtering Materials (AREA)
- Color Printing (AREA)
- Cleaning Implements For Floors, Carpets, Furniture, Walls, And The Like (AREA)
- Treatments For Attaching Organic Compounds To Fibrous Goods (AREA)
Abstract
A process for the felts of a papermaking operation in order to inhibit the deposition of particulate matter in the felt comprising applying to the felt a fatty acid imidazoline compound.
Description
0-%30 PRESS FELT CONDITIONER FOR NEUTRAL
AND ALKALINE PAPERMAKING SYSTEMS
FIELD OF THE INdENTION
The present invention relates to inhibiting the deposition of particulate materials in the press felts of a papermaking operation. Specifically, this invention pertains to the use of a press felt conditioner directed at controlling the deposition of polymerically flocculated particulate materials in neutral to alkaline papermaking systems.
I0 BACKGROUND OF THE INIfENTION
In a paper manufacturing process, ionically charged, rela-tively high molecular weight, water soluble polymers are often emplq~ed to enhance retention of cellulosic fibers, fines, and .inorganic fillers. The addition of these polymers produces a cleaner process stream by reducing the solids level in the process filtrate. The high molecular weight, ionically charged polymers control solids by adsorbing onto solid particulate surfaces in the papermaking furnish slurry and invoking charge newt ralixation (coagulation) and/or bridging (flocculation) mechanisms which cause the solid particles to flocculate. The flocculate can be retained by the formed mat of cellulosic fibers more easily than smaller individual particles. However, these flocculated particulate materials can be transferred from the surface of the sheet to the papermachine press felts. In the flocculated state, the particles cannot pass through the fine, porous structure of the press felts) and become entrapped therein. If not controlled by adequate felt IO conditioning practices, these agglomerated particulate substances can severely impair the ability of the press felts to absorb water thereby requiring reduced production rates and shortening the useful.life of the felts. In addition, it has been found that common polymeric retention aids can render normally effective prior 15 art felt conditioners useless or marginally effective.
Typical polymers employed as retention aids are generally relatively high in molecular weight; far example, copolymers made from monomers such as; acrylic acid, acrylamide, dimethyl/diallyl ammonium chloride, dimethylamine, epichlorohydrin, and ethylene 20 diamine. Typically, polymeric retention aids have average molecular weights greater than 1,000,000 and can range up to around ZO,OQA,000 for anionically charged polymers and up to 15,000,000 forrcationically charged polymers. These ionically charged poly-mers adsorb onto the various solid particulate surfaces within the 25, papermaking furnish causing flocculation.
'~~ a~~~
In neutral and alkaline papermaking (pH approximately s.0 -8.5), the utilization of polymeric retention aids is particularly critical for efficient operation. Without them, such common system additives as cellulosic reactive sizes, Alkenyl Succinic Anhydride (ASA) and Alkene Ketene Dimer (AKD), can cycle up on the process system and hydrolyze causing numerous operational problems, particu-larly in the press section. Subsequently, most of the particulates that are transferred from the sheet to the press felts in the neu-tral and alkaline papermaking system are generally in a flocculated IO state and are therefore too large to easily pass through a press felt. Subsequently, these contaminants are either embedded into the felt structure or transferred back to the sheet and cause spots, holes, etc., ar deposit in the dryer section and cause problems there. Because of their size', they are relatively unresponsive to prior art felt conditioning treatments.
In addition to the aforementioned contaminants, most press felts associated with coated alkaline fine paper experience exces-sive filling due to white pitch deposition. This arises from natural wood resins such as fatty esters, fatty acids,, resin acids ZO and othertypical papermaking furnish components .such as sizing agents, alumina and fiber fines. The paper coating binders such as polyvinyl acetate or styrene butadiene latices and inorganic coating pigments such as clay, calcium carbonate and titanium dioxide also contribute to,the felt filling. If not effectively controlled by adequate chemical and mechanical press felt conditioning practices, this high level of contaminating material plugging or filling the _g_ ~~".~a~~~~i paper machine press felt severely impairs their water absorbancy capability, which in turn, reduces paper machine production rates, produces paper quality defects and/or requires the premature removal and replacement of the expensive felts.
.Chemical analyses of used press felts associated with coated neutral and alkaline papermaking also reveal a number of ,, polymerically flocculated components. Significant quantities of inorganic fillers such as calcium carbonate, clay and titanium dioxide are typically found in addition to normally smaller amounts of sizing agents and wood pitch components.
While various anionic or nonionic surfactant-type felt conditioners commonly employed in the art demonstrate substantial efficacy for conditioning press felts subject to wood pitch and/or paper sizing agent-related contamination, they have proven to possess limited efficacy against white pitch contamination at commercially viable treatment dosage levels.
DESCRIPTION OF THE RELATED ART
Processes to inhibit contamination deposition in pape,r-maE~ng felts are known in the art. U.S. Pat. No. 4,715,931, Shellhamer et al., discloses a process for inhibiting aluminum hydroxide deposition in papermaking systems which comprises adding to the felts a hydroxylated carboxylic acid. The use of -~-~~~ i~~r~~
the carboxylic acid in combination with surfactants, such as octyi phenol ethoxylates, nonyl phenol ethoxylates and others listed therein inhibit aluminum hydroxide deposition and associated organic contaminants.
In addition to the control of inorganic contaminants, pitch formation is of concern in papermaking systems. Filler materials can become trapped within the organic matrix formed by pitch coalescence compounding deposition problems. Methods of controlling the pitch deposition formation are known in the art.
U.S. Pat. No. 4,184,912, Payton, discloses a method of preventing pitcy formation by dispersing and emulsifying pitch particles in the pulp furnish to an exceptionally fine state and uniformally distributing the particles throughout the finished paper. The pitch deposition is controlled by the addition of a three com-ponent formulation comprising a nonionic surfactant plus an anionic surfactant and a low molecular weight anionic polymer.
The three component mixture is added to the papermaking pulp system at a point.prior to where pitch deposits normally form.
In U.S. Pat. No. 3,992,249, Farley, a process for inhibiting pitch deposition is disclosed wherein the pulp is washed with an aqueous solution of anionic polymer having between 25 to 85 mole percent.
hydrophobic-oleophilic linkages and 15 to TO mole percent hydro-philic acid linkages to complex with the pitch. The pitch-polymer complex is washed away with water.
'~;~~ ~~~~~~a U.S. Pat. No. 3,873,417, Otrhalek et al., discloses a pitch and pigment dispersant which comprises a neutralized solution of polymer prepared by free radical polymerization of an'alpha, beta unsaturated acid with an alkyl ester and an allyl alcohol.
Another pitch control process is disclosed in U.S. Patent No. 3,398,047, Michalski. The patentee teaches that the use of an organic polydentate ligand such as aminopolycarboxylic acids, and an organic sulfonate offer an efficient pitch deposition inhibitor.
Of further interest is U.S. Patent No. 3,582,461, Lipowski et al., which discloses a pitch control process utilizing a dicyandiamide-formaldehyde condensate compound.
U.S. Patent No. 3,642,572, Endres et al., discloses that polyamidoamines are useful not only as flocculants, but also as retention aids and dewatering agents in papermaking processes.
Additional polyamines are disclosed by Ziemann et al., in U.S.
Patent No. 3,893,885 as being useful as retention aids and dewatering agents.
Some treatment programs are directed specifically at the reduction of contaminants within the felt or other sheet farming surfaces. EP 0359590, Aston et al., addresses the control of deposits on and within papermill felts by employing the use of a cationic polymer in conjunction with nonionic or cationic surface tants. The base products used to create the cationic polymers preferably contain amine groups. U.S. Patent No. 4,895,622, ~~C'~~~'~~~
Barnett et al., discloses a felt conditioner comprising a relatively low molecular weight anionic organic polymer and a hydrophilic anionic or nonionic surfactant. The polymers preferably contain acrylic acid or methacrylic acid moieties.
DETAILED DESCRIPTION OF THE INVENTION
The present invention is directed toward inhibiting the deposition of polymerically flocculated particulate material in a felt in the press section of a papermaking system. Several functionally similar members of fatty acid imidazolines are surprisingly effective when employed as felt conditioning agents for inhibiting contamination of press felts subjected to the aforementioned flocculated particulate .
substances. An effective inhibiting amount of these felt conditioning agents may be metered into one or more fresh water showers directed onto a press felt on its runs between the press nip and the vacuum or uhle box utilized for dewatering the treated felts.
Also surprisingly, other types of fatty acid imida-zolines did not produce positive results when employed as felt conditioners.
Examples of highly effective fatty acid imidazolines that can be utilized in accordance with this invention are represented by the general structure:
~ H2 ~---C CH2 where R is an alkyl hydrophobe, radical with a preferred carbon chain length of C12 or greater, more preferably C18.
Fatty acid imidazolines, according to this invention, will provide for an effective continuous press felt conditioning treat-ment when the press felts are subjected to significant quantities of the aforementioned polymerically flocculated particulate substances originating from coated neutral and alkaline pH papermaking furnishes, with or without sizing agent being present. The choice of the fatty acid imidazoline appears to be critical and the imida-zoline embodied in this invention may fall within a hydrophobe carbon chain length of C12 or greater with the preferred hydrophobe chain length of C18.
Furthermore, it is also believed that the embodied invention can also be effectively used to prevent these same types of contami-nant~.=from building up on paper machine press section press rolls whet fed continuously through an aqueous shower directed upon the press rolls. .In either case, the required amount or concentration of fatty acid imidazoline will depend on, among other things, the volume of shower water employed, the production rate, and the concentration of poiymerically flocculated contaminants. Generally the total concentration of fatty acid imidazoline added to the aqueous showering medium is from 10 to 1500 parts per million parts of the aqueous medium. Preferably, they are added at concentrations from 100 parts to 300 parts per million parts o~f aqueous. showering medium..
.. In order to more clearly illustrate the present invention the following data were generated. The following examples are included as illustrations of the present invention and should not be construed as limiting the scope thereof.
EXAMPLES
The examples contained herein will demonstrate the unexpected superior responses produced by the present invention.
The results were obtained utilizing a continuous press felt conditioning test apparatus and a~simulated caated alkaline fine paper contaminant system. The testing incorporates a clean (unused) press felt sample of known initial weight and air permeability placed on a heavy-mesh support screen through which the treated or untr~ted contaminant solution is pressed. The simulated coated alts-line fine papermaking contaminant test slurry consisted of the following: ~ .
_1o-Ingredient Concentration (PPm) Ground Calcium Carbonate 375.00 Clay , 125.00 Fatty ester/fatty acid pitch mixture 50.00 *Coating solids (cured, redispersed 1596 slurry) 300.00 Alkaline Size (ASA/starch, 1:3 ratio, 1096 slurry) 48.75 Cationic Retentian Aid (High Molecular freight, Cationic Polyacrylamide) 2.00 * Pre-cured casting formulation contains:
5~ PVAc latex, 5% S8R latex, 32~ Clay, 8~ Ti02 and 50~ water Table 1 contains data generated in this slurry syst em showing the performance characteristics of several commercially available surfactants and polymers as defined below, employed in the art for continuous or intermittent conditioning of paper machine press felts in comparison to the fatty acid imidazolines according to the invention. Table 2 s~immarizes data generated to evaluate the effectiveness of the present invention in the same slurry sy stem excluding the alkaline size.
As can be seen from Tables 1 and 2, the results show that in two critical test parameters, namely percent weight gain and percent permeability loss, the values for the fatty acid imidazolines with a hydrd~hobe carbon chain length of C12 to C18 were significantly lower than the control or any other surfactant or polymer commonly employed in the continuous or intermittent conditioning of paper machine felts.
-11- ~~~ a~~°~a Examples are listed below of the conventional surfactants known in the art which were compared against the fatty acid r imidazolines of the present invention:
Alkyl or dialkyl phenol ethoxylates represented by the general structure: ' .. R p OCH2CHZ)nOH
R
where, R = H or alkyl group R' = H or alkyl group n = moles of ethylene oxide;
Sodium lignosulfonates;
Ethoxylated secondary alcohols;
Quaternary imidazolines;
Phosphate esters;
Polymethylnapthalene sulfonates;
Polyacrylic acid; and Sodium alkylnapthalene sulfonate.
~~~W
Performance of various surfactants and fatty acid imidazolines in a felt conditioning test system utilizing a simulated polymerically (retention aid) flocculated coated alkaline fine paper contaminant system (with sizing agent present).
CONDITIONING % WT. GAIN % PEPMEABILITY
AGENT OF TEST FELT LOSS
(over clean control) (over clean control) Untreated Control 24.4 83.4 Fatty Acid Imidazoline H.ydrophobe carbon chain length a) Clg 4.1 38.1 b) C16 5.7 41.4 c) C12 13.6 54.2 ~ d) C$ 26.I 81.2 Quaternized Fatty Imidazoline ~i_ydrophobe carbon chain le~th a) C18 22.2 71.2 "b) C16 19.4 73.3 -,~_ .
Phosphate ester ~ 16.1 59.9 Sodium Lignosulfonate ' 23.8 79.6 Palymethylnapthalene Sulfonate I9.2 61,8 Ethoxylated nonyl phenol 18.9 56.9 E~hoxylated octyl phenol * 19.1 70.6 Polyacrylic acid ~ 27.4 80.5 * Untreated Control Data were: 28.3% Wt. Gain and 84.4%
Permeabi 1 i~ty- Loss ~r'~~~,~~, ~-.
i:)s9 :v:'~~:) Performance of various surfactants and fatty acid imidazolines in a felt conditioning test system utilizing a simulated polymerically (retention aid) flocculated coated alkaline fine paper (no sizing agent employed) contaminant system.
CONDITIONING % WT. GAIN % PERMEABILITY
,. AGENT OF TEST FELT LOSS
(over c lean control) (over clean control) Untreated Control 27.9 80.4 Fatty Acid Imidazoline Hvdroohobe carbon chain len th a) C18 6.5 44.8 b) C16 6.2 33.9 c) C12 16.1 52.4 d) C8 30.3 84.7 Quaternized Fattv lmi~a'gline Hvdrophobe carbon chain length a) C18 21.0 68.2 .b) C16 23.1 71.0 Phosphate ester 20 . 75.0 Sodium Lignosu'lfonate 20 . 74.2 Polymethylnapthalene Sulfonate 20 . 77.1 Ethoxylated nonyl phenol 17 . 68.8 Ethoxylated octyl phenol 19 . 70.6 Polyacrylic acid 20 . 70.9 Sodium alkyl napthalene sulfonate19 . 75.6 la-It is clear that the process of the present invention provides a significant positive felt conditioning response to prevent the aforementioned polymerically flocculated particulate substances from depositing in the felts, regardless of whether a sizing agent is present or not.
While this invention has been described with respect~to particular embodiments thereof, it is apparent that numerous other forms and modifications of the invention will be obvious to those skilled in the art. The appended claims and this invention should be construed to cover all such otivious forms and modifications which are within the true spirit and scope of the present invention.
AND ALKALINE PAPERMAKING SYSTEMS
FIELD OF THE INdENTION
The present invention relates to inhibiting the deposition of particulate materials in the press felts of a papermaking operation. Specifically, this invention pertains to the use of a press felt conditioner directed at controlling the deposition of polymerically flocculated particulate materials in neutral to alkaline papermaking systems.
I0 BACKGROUND OF THE INIfENTION
In a paper manufacturing process, ionically charged, rela-tively high molecular weight, water soluble polymers are often emplq~ed to enhance retention of cellulosic fibers, fines, and .inorganic fillers. The addition of these polymers produces a cleaner process stream by reducing the solids level in the process filtrate. The high molecular weight, ionically charged polymers control solids by adsorbing onto solid particulate surfaces in the papermaking furnish slurry and invoking charge newt ralixation (coagulation) and/or bridging (flocculation) mechanisms which cause the solid particles to flocculate. The flocculate can be retained by the formed mat of cellulosic fibers more easily than smaller individual particles. However, these flocculated particulate materials can be transferred from the surface of the sheet to the papermachine press felts. In the flocculated state, the particles cannot pass through the fine, porous structure of the press felts) and become entrapped therein. If not controlled by adequate felt IO conditioning practices, these agglomerated particulate substances can severely impair the ability of the press felts to absorb water thereby requiring reduced production rates and shortening the useful.life of the felts. In addition, it has been found that common polymeric retention aids can render normally effective prior 15 art felt conditioners useless or marginally effective.
Typical polymers employed as retention aids are generally relatively high in molecular weight; far example, copolymers made from monomers such as; acrylic acid, acrylamide, dimethyl/diallyl ammonium chloride, dimethylamine, epichlorohydrin, and ethylene 20 diamine. Typically, polymeric retention aids have average molecular weights greater than 1,000,000 and can range up to around ZO,OQA,000 for anionically charged polymers and up to 15,000,000 forrcationically charged polymers. These ionically charged poly-mers adsorb onto the various solid particulate surfaces within the 25, papermaking furnish causing flocculation.
'~~ a~~~
In neutral and alkaline papermaking (pH approximately s.0 -8.5), the utilization of polymeric retention aids is particularly critical for efficient operation. Without them, such common system additives as cellulosic reactive sizes, Alkenyl Succinic Anhydride (ASA) and Alkene Ketene Dimer (AKD), can cycle up on the process system and hydrolyze causing numerous operational problems, particu-larly in the press section. Subsequently, most of the particulates that are transferred from the sheet to the press felts in the neu-tral and alkaline papermaking system are generally in a flocculated IO state and are therefore too large to easily pass through a press felt. Subsequently, these contaminants are either embedded into the felt structure or transferred back to the sheet and cause spots, holes, etc., ar deposit in the dryer section and cause problems there. Because of their size', they are relatively unresponsive to prior art felt conditioning treatments.
In addition to the aforementioned contaminants, most press felts associated with coated alkaline fine paper experience exces-sive filling due to white pitch deposition. This arises from natural wood resins such as fatty esters, fatty acids,, resin acids ZO and othertypical papermaking furnish components .such as sizing agents, alumina and fiber fines. The paper coating binders such as polyvinyl acetate or styrene butadiene latices and inorganic coating pigments such as clay, calcium carbonate and titanium dioxide also contribute to,the felt filling. If not effectively controlled by adequate chemical and mechanical press felt conditioning practices, this high level of contaminating material plugging or filling the _g_ ~~".~a~~~~i paper machine press felt severely impairs their water absorbancy capability, which in turn, reduces paper machine production rates, produces paper quality defects and/or requires the premature removal and replacement of the expensive felts.
.Chemical analyses of used press felts associated with coated neutral and alkaline papermaking also reveal a number of ,, polymerically flocculated components. Significant quantities of inorganic fillers such as calcium carbonate, clay and titanium dioxide are typically found in addition to normally smaller amounts of sizing agents and wood pitch components.
While various anionic or nonionic surfactant-type felt conditioners commonly employed in the art demonstrate substantial efficacy for conditioning press felts subject to wood pitch and/or paper sizing agent-related contamination, they have proven to possess limited efficacy against white pitch contamination at commercially viable treatment dosage levels.
DESCRIPTION OF THE RELATED ART
Processes to inhibit contamination deposition in pape,r-maE~ng felts are known in the art. U.S. Pat. No. 4,715,931, Shellhamer et al., discloses a process for inhibiting aluminum hydroxide deposition in papermaking systems which comprises adding to the felts a hydroxylated carboxylic acid. The use of -~-~~~ i~~r~~
the carboxylic acid in combination with surfactants, such as octyi phenol ethoxylates, nonyl phenol ethoxylates and others listed therein inhibit aluminum hydroxide deposition and associated organic contaminants.
In addition to the control of inorganic contaminants, pitch formation is of concern in papermaking systems. Filler materials can become trapped within the organic matrix formed by pitch coalescence compounding deposition problems. Methods of controlling the pitch deposition formation are known in the art.
U.S. Pat. No. 4,184,912, Payton, discloses a method of preventing pitcy formation by dispersing and emulsifying pitch particles in the pulp furnish to an exceptionally fine state and uniformally distributing the particles throughout the finished paper. The pitch deposition is controlled by the addition of a three com-ponent formulation comprising a nonionic surfactant plus an anionic surfactant and a low molecular weight anionic polymer.
The three component mixture is added to the papermaking pulp system at a point.prior to where pitch deposits normally form.
In U.S. Pat. No. 3,992,249, Farley, a process for inhibiting pitch deposition is disclosed wherein the pulp is washed with an aqueous solution of anionic polymer having between 25 to 85 mole percent.
hydrophobic-oleophilic linkages and 15 to TO mole percent hydro-philic acid linkages to complex with the pitch. The pitch-polymer complex is washed away with water.
'~;~~ ~~~~~~a U.S. Pat. No. 3,873,417, Otrhalek et al., discloses a pitch and pigment dispersant which comprises a neutralized solution of polymer prepared by free radical polymerization of an'alpha, beta unsaturated acid with an alkyl ester and an allyl alcohol.
Another pitch control process is disclosed in U.S. Patent No. 3,398,047, Michalski. The patentee teaches that the use of an organic polydentate ligand such as aminopolycarboxylic acids, and an organic sulfonate offer an efficient pitch deposition inhibitor.
Of further interest is U.S. Patent No. 3,582,461, Lipowski et al., which discloses a pitch control process utilizing a dicyandiamide-formaldehyde condensate compound.
U.S. Patent No. 3,642,572, Endres et al., discloses that polyamidoamines are useful not only as flocculants, but also as retention aids and dewatering agents in papermaking processes.
Additional polyamines are disclosed by Ziemann et al., in U.S.
Patent No. 3,893,885 as being useful as retention aids and dewatering agents.
Some treatment programs are directed specifically at the reduction of contaminants within the felt or other sheet farming surfaces. EP 0359590, Aston et al., addresses the control of deposits on and within papermill felts by employing the use of a cationic polymer in conjunction with nonionic or cationic surface tants. The base products used to create the cationic polymers preferably contain amine groups. U.S. Patent No. 4,895,622, ~~C'~~~'~~~
Barnett et al., discloses a felt conditioner comprising a relatively low molecular weight anionic organic polymer and a hydrophilic anionic or nonionic surfactant. The polymers preferably contain acrylic acid or methacrylic acid moieties.
DETAILED DESCRIPTION OF THE INVENTION
The present invention is directed toward inhibiting the deposition of polymerically flocculated particulate material in a felt in the press section of a papermaking system. Several functionally similar members of fatty acid imidazolines are surprisingly effective when employed as felt conditioning agents for inhibiting contamination of press felts subjected to the aforementioned flocculated particulate .
substances. An effective inhibiting amount of these felt conditioning agents may be metered into one or more fresh water showers directed onto a press felt on its runs between the press nip and the vacuum or uhle box utilized for dewatering the treated felts.
Also surprisingly, other types of fatty acid imida-zolines did not produce positive results when employed as felt conditioners.
Examples of highly effective fatty acid imidazolines that can be utilized in accordance with this invention are represented by the general structure:
~ H2 ~---C CH2 where R is an alkyl hydrophobe, radical with a preferred carbon chain length of C12 or greater, more preferably C18.
Fatty acid imidazolines, according to this invention, will provide for an effective continuous press felt conditioning treat-ment when the press felts are subjected to significant quantities of the aforementioned polymerically flocculated particulate substances originating from coated neutral and alkaline pH papermaking furnishes, with or without sizing agent being present. The choice of the fatty acid imidazoline appears to be critical and the imida-zoline embodied in this invention may fall within a hydrophobe carbon chain length of C12 or greater with the preferred hydrophobe chain length of C18.
Furthermore, it is also believed that the embodied invention can also be effectively used to prevent these same types of contami-nant~.=from building up on paper machine press section press rolls whet fed continuously through an aqueous shower directed upon the press rolls. .In either case, the required amount or concentration of fatty acid imidazoline will depend on, among other things, the volume of shower water employed, the production rate, and the concentration of poiymerically flocculated contaminants. Generally the total concentration of fatty acid imidazoline added to the aqueous showering medium is from 10 to 1500 parts per million parts of the aqueous medium. Preferably, they are added at concentrations from 100 parts to 300 parts per million parts o~f aqueous. showering medium..
.. In order to more clearly illustrate the present invention the following data were generated. The following examples are included as illustrations of the present invention and should not be construed as limiting the scope thereof.
EXAMPLES
The examples contained herein will demonstrate the unexpected superior responses produced by the present invention.
The results were obtained utilizing a continuous press felt conditioning test apparatus and a~simulated caated alkaline fine paper contaminant system. The testing incorporates a clean (unused) press felt sample of known initial weight and air permeability placed on a heavy-mesh support screen through which the treated or untr~ted contaminant solution is pressed. The simulated coated alts-line fine papermaking contaminant test slurry consisted of the following: ~ .
_1o-Ingredient Concentration (PPm) Ground Calcium Carbonate 375.00 Clay , 125.00 Fatty ester/fatty acid pitch mixture 50.00 *Coating solids (cured, redispersed 1596 slurry) 300.00 Alkaline Size (ASA/starch, 1:3 ratio, 1096 slurry) 48.75 Cationic Retentian Aid (High Molecular freight, Cationic Polyacrylamide) 2.00 * Pre-cured casting formulation contains:
5~ PVAc latex, 5% S8R latex, 32~ Clay, 8~ Ti02 and 50~ water Table 1 contains data generated in this slurry syst em showing the performance characteristics of several commercially available surfactants and polymers as defined below, employed in the art for continuous or intermittent conditioning of paper machine press felts in comparison to the fatty acid imidazolines according to the invention. Table 2 s~immarizes data generated to evaluate the effectiveness of the present invention in the same slurry sy stem excluding the alkaline size.
As can be seen from Tables 1 and 2, the results show that in two critical test parameters, namely percent weight gain and percent permeability loss, the values for the fatty acid imidazolines with a hydrd~hobe carbon chain length of C12 to C18 were significantly lower than the control or any other surfactant or polymer commonly employed in the continuous or intermittent conditioning of paper machine felts.
-11- ~~~ a~~°~a Examples are listed below of the conventional surfactants known in the art which were compared against the fatty acid r imidazolines of the present invention:
Alkyl or dialkyl phenol ethoxylates represented by the general structure: ' .. R p OCH2CHZ)nOH
R
where, R = H or alkyl group R' = H or alkyl group n = moles of ethylene oxide;
Sodium lignosulfonates;
Ethoxylated secondary alcohols;
Quaternary imidazolines;
Phosphate esters;
Polymethylnapthalene sulfonates;
Polyacrylic acid; and Sodium alkylnapthalene sulfonate.
~~~W
Performance of various surfactants and fatty acid imidazolines in a felt conditioning test system utilizing a simulated polymerically (retention aid) flocculated coated alkaline fine paper contaminant system (with sizing agent present).
CONDITIONING % WT. GAIN % PEPMEABILITY
AGENT OF TEST FELT LOSS
(over clean control) (over clean control) Untreated Control 24.4 83.4 Fatty Acid Imidazoline H.ydrophobe carbon chain length a) Clg 4.1 38.1 b) C16 5.7 41.4 c) C12 13.6 54.2 ~ d) C$ 26.I 81.2 Quaternized Fatty Imidazoline ~i_ydrophobe carbon chain le~th a) C18 22.2 71.2 "b) C16 19.4 73.3 -,~_ .
Phosphate ester ~ 16.1 59.9 Sodium Lignosulfonate ' 23.8 79.6 Palymethylnapthalene Sulfonate I9.2 61,8 Ethoxylated nonyl phenol 18.9 56.9 E~hoxylated octyl phenol * 19.1 70.6 Polyacrylic acid ~ 27.4 80.5 * Untreated Control Data were: 28.3% Wt. Gain and 84.4%
Permeabi 1 i~ty- Loss ~r'~~~,~~, ~-.
i:)s9 :v:'~~:) Performance of various surfactants and fatty acid imidazolines in a felt conditioning test system utilizing a simulated polymerically (retention aid) flocculated coated alkaline fine paper (no sizing agent employed) contaminant system.
CONDITIONING % WT. GAIN % PERMEABILITY
,. AGENT OF TEST FELT LOSS
(over c lean control) (over clean control) Untreated Control 27.9 80.4 Fatty Acid Imidazoline Hvdroohobe carbon chain len th a) C18 6.5 44.8 b) C16 6.2 33.9 c) C12 16.1 52.4 d) C8 30.3 84.7 Quaternized Fattv lmi~a'gline Hvdrophobe carbon chain length a) C18 21.0 68.2 .b) C16 23.1 71.0 Phosphate ester 20 . 75.0 Sodium Lignosu'lfonate 20 . 74.2 Polymethylnapthalene Sulfonate 20 . 77.1 Ethoxylated nonyl phenol 17 . 68.8 Ethoxylated octyl phenol 19 . 70.6 Polyacrylic acid 20 . 70.9 Sodium alkyl napthalene sulfonate19 . 75.6 la-It is clear that the process of the present invention provides a significant positive felt conditioning response to prevent the aforementioned polymerically flocculated particulate substances from depositing in the felts, regardless of whether a sizing agent is present or not.
While this invention has been described with respect~to particular embodiments thereof, it is apparent that numerous other forms and modifications of the invention will be obvious to those skilled in the art. The appended claims and this invention should be construed to cover all such otivious forms and modifications which are within the true spirit and scope of the present invention.
Claims (6)
1. A process for conditioning the felts of a papermaking system in order to inhibit polymeric retention aid flocculated particulate deposition in the felts comprising applying to the felts an effective inhibiting amount of a fatty acid imidazoline having a structure:
where R is an alkyl hydrophobe radical having a carbon chain length of C12 or more.
where R is an alkyl hydrophobe radical having a carbon chain length of C12 or more.
2. The process of claim 1 wherein R is an alkyl hydrophobe radical having a carbon chain length of C18.
3. The process of claim 1 wherein the papermaking system is pH neutral or alkaline.
4. The process of claim 1 wherein the felt is conditioned by showering with an aqueous medium containing the fatty acid imidazoline.
5. The process of claim 4 wherein the fatty acid imidazoline is added in an amount of from about 10 to about 1,500 parts per million parts of the aqueous medium.
6. The process of claim 5 wherein the fatty acid imidazoline is added in an amount of from about 100 to about 300 parts per million parts of the aqueous medium.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
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US81620092A | 1992-01-02 | 1992-01-02 | |
US07/816,200 | 1992-01-02 |
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CA2083406A1 CA2083406A1 (en) | 1993-07-03 |
CA2083406C true CA2083406C (en) | 2004-01-06 |
Family
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Application Number | Title | Priority Date | Filing Date |
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CA002083406A Expired - Fee Related CA2083406C (en) | 1992-01-02 | 1992-11-20 | Press felt conditioner for neutral and alkaline papermaking systems |
Country Status (6)
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EP (1) | EP0550230B1 (en) |
AT (1) | ATE126557T1 (en) |
CA (1) | CA2083406C (en) |
DE (1) | DE69204154T2 (en) |
FI (1) | FI97553C (en) |
NO (1) | NO300226B1 (en) |
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CA2131143A1 (en) * | 1993-10-07 | 1995-04-08 | Betzdearborn Inc. | Method of inhibiting wet strength resin deposition in papermaking felts |
GB2284833A (en) * | 1993-11-02 | 1995-06-21 | Steven Frederick Finch | Inhibiting the deposition of sticky particles on paper mill dryer fabrics |
DE19519268C1 (en) * | 1995-05-31 | 1997-01-23 | Stockhausen Chem Fab Gmbh | Use of pulp and paper making agents |
DK174460B1 (en) * | 2002-02-08 | 2003-03-31 | Dan Web Holding As | Cleaning apparatus parts in binder/glue application apparatus, comprises collecting excess release agent solution in suction slot behind application area, and conducting further on to pipe system, ventilator, and suction box |
ES2733528T3 (en) | 2014-11-25 | 2019-11-29 | Buckman Laboratories Int Inc | Felt conditioner and cleaner |
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DE2509743A1 (en) * | 1975-03-06 | 1976-09-23 | Basf Ag | Anti foaming agent for dish washing compsn - contg. alkoxylated amine or acid |
AR247436A1 (en) * | 1988-09-16 | 1994-12-29 | Dearborn Chemical Company Ltd | Controlling deposits on paper machine felts and the like |
DE4020271A1 (en) * | 1990-06-26 | 1992-01-02 | Henkel Kgaa | SALTS OF FATTY ACID AMIDES AND FATTY ACID IMIDAZOLINES |
-
1992
- 1992-11-20 CA CA002083406A patent/CA2083406C/en not_active Expired - Fee Related
- 1992-12-21 EP EP92311638A patent/EP0550230B1/en not_active Expired - Lifetime
- 1992-12-21 AT AT92311638T patent/ATE126557T1/en not_active IP Right Cessation
- 1992-12-21 DE DE69204154T patent/DE69204154T2/en not_active Expired - Fee Related
- 1992-12-28 FI FI925886A patent/FI97553C/en active IP Right Grant
- 1992-12-28 NO NO925022A patent/NO300226B1/en not_active IP Right Cessation
Also Published As
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FI925886A0 (en) | 1992-12-28 |
DE69204154T2 (en) | 1996-01-04 |
NO300226B1 (en) | 1997-04-28 |
DE69204154D1 (en) | 1995-09-21 |
NO925022D0 (en) | 1992-12-28 |
EP0550230B1 (en) | 1995-08-16 |
ATE126557T1 (en) | 1995-09-15 |
FI925886L (en) | 1993-07-03 |
FI97553C (en) | 1997-01-10 |
EP0550230A1 (en) | 1993-07-07 |
NO925022L (en) | 1993-07-05 |
CA2083406A1 (en) | 1993-07-03 |
FI97553B (en) | 1996-09-30 |
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