FI94535C - Process for preparing a hydrophobic dispersion - Google Patents
Process for preparing a hydrophobic dispersion Download PDFInfo
- Publication number
- FI94535C FI94535C FI925535A FI925535A FI94535C FI 94535 C FI94535 C FI 94535C FI 925535 A FI925535 A FI 925535A FI 925535 A FI925535 A FI 925535A FI 94535 C FI94535 C FI 94535C
- Authority
- FI
- Finland
- Prior art keywords
- adhesive
- pressure
- alkyl
- hydrophobic
- premix
- Prior art date
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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
- D21H17/14—Carboxylic acids; Derivatives thereof
- D21H17/15—Polycarboxylic acids, e.g. maleic acid
-
- 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
- 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
- D21H21/14—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 characterised by function or properties in or on the paper
- D21H21/16—Sizing or water-repelling agents
Landscapes
- Paper (AREA)
- Adhesives Or Adhesive Processes (AREA)
- Colloid Chemistry (AREA)
- Medicines That Contain Protein Lipid Enzymes And Other Medicines (AREA)
- Steroid Compounds (AREA)
- Processes Of Treating Macromolecular Substances (AREA)
Abstract
Description
...... 94535...... 94535
Hydrofobilumadispersion valmistusprosessi -Process för framställning av en hydrofoblimdispersionHydrophobic dispersion preparation process - Process for the production of hydrophobic dispersion
Hydrofobiliimauksella tarkoitetaan paperin tai kartongin 5 tekemistä enemmän tai vähemmän vettähylkiväksi. Tätä ominaisuutta voidaan mitata esim. nk. Cobb-testillä jossa mitataan veden tunkeutumista paperiin tai kartonkiin ajan funktiona. Tulos ilmoitetaan absorbtiona g/m2. Kunnolla hydrofobiliimatussa tuotteessa arvo on yleensä <25 g/m2 10 kun taas tuotteessa jota ei ole käsitelty hydrofobisuutta lisäävillä liimoilla arvo voi olla > 100 g/m2.By hydrophobic gluing is meant making the paper or board 5 more or less water-repellent. This property can be measured, for example, by the so-called Cobb test, which measures the penetration of water into paper or board as a function of time. The result is expressed as absorption in g / m2. A properly hydrophobically bonded product will generally have a value of <25 g / m2 10 while a product that has not been treated with hydrophobic adhesives may have a value of> 100 g / m2.
Perinteisiä hydrofobiliimana käytettyjä yhdisteitä ovat puusta peräisin olevat hartsihapot ja niiden johdannai-15 set.Conventional compounds used as hydrophobic adhesives include wood-derived rosin acids and their derivatives.
Tänä päivänä paperi- ja kartonkiteollisuus on yhä enemmän siirtynyt käyttämään hydrofobiliimaukseen nk. neutraali-liimoja jotka yleensä ovat alkyyliketeenidimeeri(AKD)-20 taikka alkenyyli-meripihkahappoanhydridi(ASA)- pohjaisia yhdisteitä.Today, the paper and board industry has increasingly switched to the use of so-called neutral adhesives for hydrophobic sizing, which are usually alkyl ketene dimer (AKD) -20 or alkenyl succinic anhydride (ASA) -based compounds.
Hydrofobiliimat toimitetaan yleensä paperi- tai kartonkitehtaille vesidispersiona jossa aktiiviaineen (AKD, ASA, 25 hartsin) osuus tuotteessa on 5 - 50 % välillä. ASA tyyppisen liiman ollessa kyseessä liimadispersio valmistetaan : : . pääsääntöisesti paperi- tai kartonkitehtaalla.Hydrophobic adhesives are usually supplied to paper or board mills as an aqueous dispersion in which the proportion of active substance (AKD, ASA, 25 resin) in the product is between 5 and 50%. In the case of an ASA type adhesive, the adhesive dispersion is prepared:. mainly at a paper or board mill.
• · · · 94535 käytetään mm. kationista tärkkelystä, kationisia polyety-leeni-imiinejä, kationisia polyakryyliamideja, gelatiinia tai kaseiinia.• · · · 94535 is used e.g. cationic starch, cationic polyethyleneimines, cationic polyacrylamides, gelatin or casein.
5 Pinta-aktiivisina aineina käytetään mm. natriumlignosul-fonaattia tai alkyylisulfonaatteja.5 As surfactants, e.g. sodium lignosulfonate or alkyl sulfonates.
Tyypillisiä lisäkemikaaleja ovat biosidit, aluna ja pH-säätökemikaalit.Typical additional chemicals include biocides, alum and pH adjusting chemicals.
1010
Yleinen tapa valmistaa hydrofobiliimadispersio näistä komponenteista on reaktorissa sekoittaen ja lämmittäen valmistaa homogeeninen esiseos joka sisältää sopivassa suhteessa vettä, aktiiviainetta, stabilointiainetta, pin-15 ta-aktiivisia aineita ym. mahdollisia lisäkemikaaleja.A common way to prepare a hydrophobic adhesive dispersion of these components in a reactor is to prepare, by stirring and heating, a homogeneous premix containing the appropriate proportions of water, active ingredient, stabilizer, surface-active agents, and any additional chemicals.
Kun homogeeninen esiseos on aikaansaatu tämä kierrätetään korkeapainehomogenisaattorin, kolloidimyllyn taikka kor-keakierroksisen keskipakopumpun läpi yleensä useamman 20 kerran, kunnes riittävän pieni hiukkaskoko on aikaansaatu (yleensä 0,1 - 10 μιη) . Paine vaihtelee 50 - 500 baarin välillä ja lämpötila 50 - 100°C. Saavutettu dispersio ajetaan tämän jälkeen lämmönvaihtimen kautta tuotesäili-öön. Lämmönvaihtimessa dispersion lämpötila lasketaan < 25 30°C. Näitä periaatteita noudattavia prosesseja on kuvat- ; tu mm. julkaisuissa EP-353 212 ja EP-369 328.Once a homogeneous premix is obtained, this is generally recycled through a high pressure homogenizer, colloid mill, or high speed centrifugal pump 20 more times until a sufficiently small particle size is obtained (usually 0.1 to 10 μιη). The pressure varies between 50 and 500 bar and the temperature between 50 and 100 ° C. The dispersion obtained is then passed through a heat exchanger to the product tank. In the heat exchanger, the dispersion temperature is lowered to <25 to 30 ° C. Processes that follow these principles are pictorial; tu mm. in EP-353 212 and EP-369 328.
» · « · · 4 · * « · · ·»·« · · 4 · * «· · ·
Nyt on yllättäen havaittu että lähinnä tärkkelyksen keit- toa varten suunniteltu korkeapainekeitin (höyry su ihkukei- 30 tin eli ns. Jet-keitin) toimii erittäin hyvänä disper- .. ._ gaattorina hydrofobiliimadispersion valmistuksessa. Täi- * · lainen höyrysuihkukeitinprosessi toimii seuraavasti: • · · • · · . Esiseos valmistetaan reaktorissa 1 samalla periaatteella 35 kuin yllä olevassa prosessissa. Tämän jälkeen seos pumpataan itse keitinosaan 2, jossa seos kohtaa korkeapaineisen höyryvirran 3, ja lämpötila ja paine nousevat (paine 3 94535 yleensä 2-15 baaria ja lämpötila 100 - 200°C). Tämän jälkeen ajetaan muodostunut dispersio putkimaiseen reaktoriin 4, jonka jälkeen paine ja lämpötila lasketaan pai-sutinlaitteessa 5 ja ylimäärä höyryä voidaan erottaa höy-5 rylauhduttimella 6. Tämän jälkeen muodostunut homogeeninen tuote ajetaan lämmönvaihtimen kautta tuotesäiliöön.It has now surprisingly been found that a high-pressure cooker (steam cooker or so-called jet cooker) designed mainly for starch cooking acts as a very good dispersant in the preparation of a hydrophobic glue dispersion. The complete steam jet process works as follows: • · · • · ·. The premix is prepared in reactor 1 according to the same principle 35 as in the above process. The mixture is then pumped into the boiler section 2 itself, where the mixture meets the high-pressure steam stream 3, and the temperature and pressure rise (pressure 3 94535 usually 2-15 bar and temperature 100-200 ° C). The resulting dispersion is then passed to a tubular reactor 4, after which the pressure and temperature are lowered in the evaporator device 5 and the excess steam can be separated by a steam-5 condenser 6. The homogeneous product formed is then passed through a heat exchanger to the product tank.
Prosessin kulku on esitetty kaaviomaisesti oheisessa pii-rustuskuvassa.The flow of the process is shown schematically in the accompanying drawing.
10 Tämä prosessi poikkeaa perinteisestä prosessista seuraavasti:10 This process differs from the traditional process as follows:
Perinteinen prosessi 15Traditional process 15
Paine 50 - 500 baaria lämpöt. 50 - 100°CPressure 50 - 500 bar temp. 50-100 ° C
Höyrysuihku-keitin prosessi 20Steam jet cooker process 20
Paine 2-15 baaria lämpöt. 100 - 200°CPressure 2-15 bar temp. 100-200 ° C
25 Hydrofobiliimadispersion valmistaminen höyrysuihku-keitin tyyppisessä prosessissa mahdollistaa korkeiden kuiva-ainepitoisuuksien käytön prosessoinnin aikana ja koska vii- ve keitin- ja reaktioputkessa on erittäin lyhyt, yleensä • < 2 minuuttia tämä mahdollistaa fyysisiltä mitoiltaan '-tj 30 hyvin pienten yksiköiden käytön, joilla on suuri valmis- • ‘ /:. tuskapasiteetti.25 The preparation of a hydrophobic adhesive dispersion in a steam jet boiler type process allows the use of high dry solids during processing and because the delay in the boiler and reaction tube is very short, usually • <2 minutes this allows the use of very small units with high ready- • '/ :. The pain capacity.
» · « .. . Esim. 1 » * i»·« ... Eg 1 »* i
Laboratoriomittakaavassa valmistettiin seuraavan koostu- » « * *·* *35 muksen omaava steariini/palmitiinialkyyliketeenidimeeri (AKD) esiseos: vettä 800 g AKD 200 g 40 Orotan SN* 3.0 g : Raisamyl 150E** 22 g 4 94535 *Naftaleeniformaldehydisulfonaattikondensaatti, natrium-suola **Kationinen perunatärkkelys (DS = 0,05).On a laboratory scale, a premix of stearin / palmitin alkyl ketene dimer (AKD) with the following composition was prepared: water 800 g AKD 200 g 40 Orota SN * 3.0 g: Raisamyl 150E ** 22 g 4 94535 * Naphthalene formaldehyde sulfonate condensate, sodium ** Cationic potato starch (DS = 0.05).
5 Tärkkelys keitettiin ennen lisäystä.5 The starch was boiled before addition.
Tämä esiseos jaettiin kahteen osaan, joista toinen ajettiin 3 kertaa laboratoriokorkeapainehomogenisaattorin (Rannie) läpi. Paine 200 baaria, lämpötila 70°C. Toinen 10 osa ajettiin laboratoriomittakaavaisen höyrysuihku-keit- timen läpi kerran, lämpötila 120°C, paine 3 baaria. Molemmat emulsiot laimennettiin 12,5 % kuiva-aineeseen ja jäähdytettiin huonelärapöiseksi.This premix was divided into two portions, one of which was run 3 times through a laboratory high pressure homogenizer (Rannie). Pressure 200 bar, temperature 70 ° C. The other 10 parts were passed through a laboratory-scale steam jet cooker once, temperature 120 ° C, pressure 3 bar. Both emulsions were diluted to 12.5% dry matter and cooled to room temperature.
15 Molemmista dispersioista mitattiin seuraavat ominaisuu det, viskositeetti (Brookfield) ja keskimääräinen hiuk-kaskokoThe following properties, viscosity (Brookfield) and average particle size were measured for both dispersions.
Korkeapaine- Hövrvsuihku- 20 homogenisaattori keitinHigh-pressure steam jet 20 homogenizer cooker
Viskositeetti 10 cP 8 cPViscosity 10 cP 8 cP
Keskimääräinen 2 5 hiukkaskoko 0,56 Mm 0,60 μν\ • · • · • · • ♦ ♦ • · * « · · « : Tuloksista nähdään että dispersiot ovat ominaisuuksiltaan :*·.· lähes identtiset.Mean 2 5 particle size 0.56 Mm 0.60 μν \ • · • · • · • ♦ ♦ • · * «· ·«: The results show that the dispersions have almost identical properties: * ·.
• · 30 • · ·• · 30 • · ·
Dispersiot säilytettiin huoneenlämmössä yhden kuukauden ..'.m ajan ja samat mittaukset suoritettiin uudelleen jolloin • · tulos oli seuraavanlainen.The dispersions were kept at room temperature for one month .. '. M and the same measurements were performed again with the following result.
5 945355,94535
Korkeapaine- Hövrvsuihku- homoaenisaattori keitinHigh-pressure steam jet homoenizer cooker
5 Viskositeetti 15 cP 16 cP5 Viscosity 15 cP 16 cP
Keskimääräinen hiukkaskoko 0,86 /im 0,95 /im 10 Tuloksista nähdään että molempien dispersioiden varas-tointikestävyys on samaa luokkaa.Mean particle size 0.86 μm 0.95 μm 10 The results show that the storage stability of both dispersions is of the same order.
Esim. 2 15 Laboratoriomittakaavassa valmistettiin seuraavan koostumuksen omaava alkenyylimeripihkahappoanhydridi1(ASA) esi-seos.Example 2 A premix of alkenyl succinic anhydride (ASA) having the following composition was prepared on a laboratory scale.
vettä 900 g 20 ASA 50 gwater 900 g 20 ASA 50 g
Orotan SN 0,5 gOrotan SN 0.5 g
Raisamyl 150E 100 g * Alkenyylimeripihkahappoanhydridinä käytettiin suoraket- 25 juisista C13 - C20 alfaolefiineistä lähtöisin olevia an-hydridejä.Raisamyl 150E 100 g * Anhydrides derived from straight chain C13 to C20 alpha-olefins were used as alkenyl succinic anhydride.
Tämä esiseos jaettiin taas kahteen osaan, joista toinen : Λ ajettiin korkeapainehomogenisaattorin (paine 200 baaria • 30 lämpötila 50°C) ja toinen höyrysuihku-keittimen (lämpöti- • · · · | la 110°C ja paine 1,5 baaria) läpi.This premix was again divided into two parts, one of which: Λ was passed through a high-pressure homogenizer (pressure 200 bar • 30 temperature 50 ° C) and the other through a steam jet cooker (temperature 110 ° C and pressure 1.5 bar).
• · · · • · t t 1 • « 1• · · · • · t t 1 • «1
Syntyneet dispersiot laimennettiin 7,5 % kuiva-aineeseen • · · ja niistä mitattiin viskositeetti ja keskihiukkaskoko.The resulting dispersions were diluted to 7.5% dry matter and measured for viscosity and mean particle size.
35 »· t • · · » · « · 6 9453535 »· t • · ·» · «· 6 94535
Korkeapaine- Hövrvsuiku- homocrenisaattori keitinHigh pressure- Hövrvsuiku- homocrenizer cooker
5 Viskositeetti 600 cP 520 cP5 Viscosity 600 cP 520 cP
Keskimääräinen hiukkaskoko 0,50 jum 0,65 jum 10The average particle size is 0.50 μm 0.65 μm 10
Tuloksista nähdään että dispersiot ovat lähes samankaltaiset. Yleisesti hyvänä hiukkaskokona tämän tyyppisissä tuotteissa pidetään arvoa < 1 μιη.The results show that the dispersions are almost similar. A value of <1 μιη is generally considered to be a good particle size in this type of product.
15 • « · • · • · * · 115 • «· • · • · * · 1
Il . . Utit liiti 1:1 1 4* - - t · · • · · « ·Il. . Utit joined 1: 1 1 4 * - - t · · • · · «·
Claims (2)
Priority Applications (9)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FI925535A FI94535C (en) | 1992-12-04 | 1992-12-04 | Process for preparing a hydrophobic dispersion |
PCT/FI1993/000481 WO1994013883A1 (en) | 1992-12-04 | 1993-11-15 | Process for the preparation of a hydrophobic sizing agent dispersion |
DE69308035T DE69308035T2 (en) | 1992-12-04 | 1993-11-15 | METHOD FOR PRODUCING A HYDROPHOBIC SIZE |
EP94900166A EP0672213B1 (en) | 1992-12-04 | 1993-11-15 | Process for the preparation of a hydrophobic sizing agent dispersion |
AT94900166T ATE148752T1 (en) | 1992-12-04 | 1993-11-15 | METHOD FOR PRODUCING A HYDROPHOBIC SIZING AGENT |
AU54668/94A AU5466894A (en) | 1992-12-04 | 1993-11-15 | Process for the preparation of a hydrophobic sizing agent dispersion |
TW082109838A TW281637B (en) | 1992-12-04 | 1993-11-23 | |
ZA938796A ZA938796B (en) | 1992-12-04 | 1993-11-24 | Process for the preparation of a hydrophobic sizing agent dispersion |
CN93121599A CN1050165C (en) | 1992-12-04 | 1993-12-04 | Process for the preparation of a hydrophobic sizing agent dispersion |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FI925535 | 1992-12-04 | ||
FI925535A FI94535C (en) | 1992-12-04 | 1992-12-04 | Process for preparing a hydrophobic dispersion |
Publications (4)
Publication Number | Publication Date |
---|---|
FI925535A0 FI925535A0 (en) | 1992-12-04 |
FI925535A FI925535A (en) | 1994-06-05 |
FI94535B FI94535B (en) | 1995-06-15 |
FI94535C true FI94535C (en) | 1997-04-08 |
Family
ID=8536338
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
FI925535A FI94535C (en) | 1992-12-04 | 1992-12-04 | Process for preparing a hydrophobic dispersion |
Country Status (9)
Country | Link |
---|---|
EP (1) | EP0672213B1 (en) |
CN (1) | CN1050165C (en) |
AT (1) | ATE148752T1 (en) |
AU (1) | AU5466894A (en) |
DE (1) | DE69308035T2 (en) |
FI (1) | FI94535C (en) |
TW (1) | TW281637B (en) |
WO (1) | WO1994013883A1 (en) |
ZA (1) | ZA938796B (en) |
Families Citing this family (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1045216C (en) * | 1994-09-10 | 1999-09-22 | 朱国华 | Manufacture of neutral adhesive-applied fiber of alkyl ketene dipolymer |
US5766417A (en) * | 1996-03-06 | 1998-06-16 | Hercules Incorporated | Process for using alkaline sized paper in high speed converting or reprographics operations |
FI109218B (en) * | 1998-09-04 | 2002-06-14 | Kemira Chemicals Oy | A bonding compound used for neutral gluing of paper or paperboard and a method of making paper or paperboard |
FI113874B (en) | 2002-09-27 | 2004-06-30 | Valtion Teknillinen | Polymer solutions and dispersions and process for their preparation |
BR0315421B1 (en) * | 2002-10-24 | 2014-12-23 | Spectra Kote Corp | PAPER AND COATED PAPER OR MATERIAL PRODUCTION PROCESSES AND COMPOSITION |
CN101693927B (en) * | 2009-10-21 | 2013-03-20 | 陕西科技大学 | Long-chain alkyl alcohol modified ASA waterproof fatliquoring agent and process for preparing same |
CN111569816A (en) * | 2020-06-30 | 2020-08-25 | 江苏京控装备有限公司 | Solid-liquid homogeneous mixing pump matched multi-tube reactor |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB8920456D0 (en) * | 1989-09-11 | 1989-10-25 | Albright & Wilson | Active sizing compositions |
DE4001237A1 (en) * | 1990-01-18 | 1991-07-25 | Basf Ag | STABILIZED AQUEOUS ALKYLDICETE EMULSIONS |
-
1992
- 1992-12-04 FI FI925535A patent/FI94535C/en not_active IP Right Cessation
-
1993
- 1993-11-15 DE DE69308035T patent/DE69308035T2/en not_active Expired - Fee Related
- 1993-11-15 EP EP94900166A patent/EP0672213B1/en not_active Expired - Lifetime
- 1993-11-15 WO PCT/FI1993/000481 patent/WO1994013883A1/en active IP Right Grant
- 1993-11-15 AT AT94900166T patent/ATE148752T1/en not_active IP Right Cessation
- 1993-11-15 AU AU54668/94A patent/AU5466894A/en not_active Abandoned
- 1993-11-23 TW TW082109838A patent/TW281637B/zh active
- 1993-11-24 ZA ZA938796A patent/ZA938796B/en unknown
- 1993-12-04 CN CN93121599A patent/CN1050165C/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
DE69308035D1 (en) | 1997-03-20 |
WO1994013883A1 (en) | 1994-06-23 |
CN1089276A (en) | 1994-07-13 |
FI925535A (en) | 1994-06-05 |
FI94535B (en) | 1995-06-15 |
DE69308035T2 (en) | 1997-08-28 |
ATE148752T1 (en) | 1997-02-15 |
EP0672213B1 (en) | 1997-02-05 |
FI925535A0 (en) | 1992-12-04 |
CN1050165C (en) | 2000-03-08 |
AU5466894A (en) | 1994-07-04 |
EP0672213A1 (en) | 1995-09-20 |
ZA938796B (en) | 1994-06-30 |
TW281637B (en) | 1996-07-21 |
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Owner name: RAISIO CHEMICALS OY |
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PC | Transfer of assignment of patent |
Owner name: CIBA SPECIALTY CHEMICALS HOLDING, INC. Free format text: CIBA SPECIALTY CHEMICALS HOLDING, INC. |
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MA | Patent expired |