CN102242523B - Antifoaming agent for low-temperature paper making system - Google Patents

Antifoaming agent for low-temperature paper making system Download PDF

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CN102242523B
CN102242523B CN 201110178514 CN201110178514A CN102242523B CN 102242523 B CN102242523 B CN 102242523B CN 201110178514 CN201110178514 CN 201110178514 CN 201110178514 A CN201110178514 A CN 201110178514A CN 102242523 B CN102242523 B CN 102242523B
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higher alcohols
parts
consumption
wax
paper making
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CN102242523A (en
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吴飞
朱少勇
钟翔
曹添
刘扬
孙颖欣
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JIANGSU SIXIN SCIENTIFIC-TECHNOLOGICAL APPLICATION RESEARCH INSTITUTE CO., LTD.
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Sixin Science & Technology Applied Inst Co Ltd Nanjing City
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Abstract

The invention provides a high-alcohol emulsion type antifoaming agent for a low-temperature paper making system. The antifoaming agent comprises the components of high alcohol, a nonionic surfactant, an anionic surfactant, high alcohol polyether ester, a wax-shaped substance, a thickening agent and water. In the invention, after the high alcohol polyether ester is introduced, the problem that the antifoaming effect of the high alcohol emulsion is poor under a low temperature condition is solved, thus the high alcohol emulsion can keep outstanding antifoaming performance under the low temperature paper making system, and the storage stability of the high alcohol emulsion can also be enhanced.

Description

A kind of antifoaming agent for low-temperature paper making system
Technical field
The present invention relates to a kind of paper industry and copy paper system defoamer, be under the jurisdiction of technical field of fine chemical preparations.
Technical background
Paper industry comprises slurrying, copies the operations such as paper and coating.Because various impacts with surface-active auxiliary agent in the wet end chemistry, be easy in water, produce the foam of a large amount of difficult eliminations, simultaneously, contained various string hydroxyls in the pulping raw material, be easy to make fiber surface and inner absorption to be difficult to remove the tiny bubble foam with common defoamer in a large number, have a strong impact on the quality of subsequent handling and product, therefore, the selection of defoamer and use, particularly important for machine hand's order.
The Main Function of defoamer for papermaking is that the bubble that will be adsorbed on the fiber fines is first peeled away, and then so that minute bubbles gather into bulla floats on the liquid level, the bubble vacuolar membrane attenuation on the last water surface is finally broken.The paper of copying of existing better performances is generally the higher alcohols emulsion defoamer with defoamer, take higher alcohols as main active, forms emulsion oil-in-water by emulsifying process.For example, US4976888 discloses a kind of higher alcohols emulsion defoamer that is comprised of higher alcohols, high-carbon alcohol ester, high boiling aliphatic hydrocarbon, Tissuemat E and emulsifying agent; US5679286 discloses a kind of higher alcohols emulsion defoamer that is comprised of higher alcohols, letones and emulsifying agent; US430359 discloses a kind of higher alcohols emulsion defoamer that is comprised of higher alcohols, aliphatic acid and saponified emulsifier; EP0149812 discloses a kind of higher alcohols emulsion defoamer that is comprised of higher alcohols, high-carbon alcohol ester, higher boiling aliphatic hydrocarbon, water-soluble acrylic (acrylamide) polymer and emulsifying agent; CA02493055 discloses a kind of higher alcohols emulsion defoamer that is comprised of higher alcohols, polyglycereol stearate, mineral oil, the two stearic amides of ethylenediamine, fatty acid ester and emulsifying agent.
Although present papermaking technology constantly promotes, the water temperature of plain boiled water is also on the rise, but because China is vast in territory, north-south climate differs greatly, cause in the winter time under the environment, the water temperature when Some Enterprises is copied paper is on the low side, existing higher alcohols emulsion defoamer, therefore can not adapt to the bubbling system under the low temperature, disappear and press down the bubble ability and become relatively poor.Simultaneously, because emulsion is non-stability system at thermodynamics, the higher alcohols emulsion defoamer is through long term storage or more likely occur easily being separated after the long term storage under the low temperature, thereby affects the use of defoamer.
The inventor by to wherein adding the higher alcohols polyether ester, can effectively solve the problem of the froth breaking variation of higher alcohols emulsion under cryogenic conditions through a large amount of experimental study and the field, has also strengthened the storage stability of higher alcohols emulsions simultaneously.
Summary of the invention
The objective of the invention is: provide a kind of under cryogenic conditions the good higher alcohols emulsion-type defoamer for papermaking of antifoam performance, its bin stability is good, preparation condition is gentle.
Antifoaming agent for low-temperature paper making system of the present invention is grouped into by following several one-tenth:
(1) higher alcohols.The higher alcohols that are suitable for defoamer of the present invention comprise carbon number be 12~28 monobasic to trihydroxylic alcohol, the higher alcohols of patent of the present invention are selected from dodecanol, tetradecanol, hexadecanol, octadecanol, eicosanol, tadenan, the pure and mild n-octacosanol of lignocerane.These alcohol use separately or multiple alcohol mixing is used.
(2) non-ionic surface active agent.General structure is as follows:
R 1O(EO) mH
R wherein 1For carbon number is 8~28 alkyl, m is 10~60 integer.Take the consumption of higher alcohols as 100 parts by mass, then the consumption of non-ionic surface active agent is 0.01~10 part.
(3) anion surfactant.The froth breaking active component is dispersed in water, forms O/W type emulsion.Because it has stronger electric charge, therefore, be adsorbed on the mixed fatty alcohol microparticle surfaces after, can be so that the fatty alcohol particulate has stronger electric charge, thus stop the gathering of particle.Its structural formula is as follows:
Figure BSA00000527196100021
R in the formula 2Saturated alkyl for carbon number 8~20.Take the consumption of higher alcohols as 100 parts by mass, then the consumption of emulsifying agent is 0.01~5 part.
(4) higher alcohols polyether ester.Described higher alcohols polyether ester represents with following structural formula:
R 3O(EO) x(PO) yCOR 4
R wherein 3For carbon number is 12~24 alkyl, x is 0~10 integer, and y is 1~30 integer; R 4For carbon number is 8~20 alkyl, take the consumption of higher alcohols as 100 parts by mass, the consumption of shellfish higher alcohols polyether ester is 10~50 parts.
(5) wax.Wax among the present invention is selected from paraffin, montan wax, microwax, Brazil wax, oxidized polyethlene wax, husky rope Fischer-Tropsch wax, Tissuemat E and beeswax.Take the consumption of higher alcohols as 100 parts by mass, then the consumption of wax is 16~40 parts.
(6) thickener.The effect of thickener is the stability that improves emulsion.Thickener of the present invention comprises xanthan gum, guar gum, polyvinyl alcohol, sodium carboxymethylcellulose, hydroxyethylcellulose and esters of acrylic acid, is preferably esters of acrylic acid, and its consumption is adjusted according to the required viscosity of reality.
(7) water.The consumption of water determines the solid content of final products, and final solid content is controlled at 0.1~35% for good, preferred 30%.
Said components is prepared the higher alcohols emulsion defoamer as follows: higher alcohols, non-ionic surface active agent, anion surfactant, higher alcohols polyether ester, wax are mixed, be warming up to 70~95 ℃; 70~95 ℃ water are slowly added said mixture, then by the further emulsification of high speed shear, replenish again suitable quantity of water to desired concn; At last, add thickener, be adjusted to required viscosity and get final product.
The specific embodiment
Embodiment 1
With 16 parts of octadecanols, 6 parts of Brazil waxs, 6 parts of higher alcohols polyether ester (C 12H 26O (EO) 1(PO) 30COC 9H 19), 1 part of non-ionic surface active agent (C 12H 26O (EO) 40H), 1 part of anion emulsifier (disodium 4-dodecyl-2,4 '-oxydibenzenesulfonate) adds reactor, mix being warming up to 70 ℃, after stirring, add 70 parts 75 ℃ water, obtain emulsion by high-speed shearing equipment, add the acrylic ester thickener adjusting viscosity, obtain defoamer.
Embodiment 2
With 20 parts of eicosanols, 4 parts of microwaxes, 4 parts of higher alcohols polyether ester (C 16H 34O (EO) 5(PO) 20COC 13H 27), 1 part of non-ionic surface active agent (C 16H 34O (EO) 20H), 1 part of anion emulsifier (octyl group diphenyl ether sodium disulfonate) adds reactor, mix being warming up to 85 ℃, after stirring, add 70 parts 75 ℃ water, obtain emulsion by high-speed shearing equipment, add the acrylic ester thickener adjusting viscosity, obtain defoamer.
Embodiment 3
With 18 parts of tetracosanols, 6 parts of Tissuemat Es, 4 parts of higher alcohols polyether ester (C 22H 46O (EO) 9(PO) 8COC 15H 31), 1 part of non-ionic surface active agent (C 20H 42O (EO) 60H), 1 part of anion emulsifier (cetyl diphenyl ether sodium disulfonate) adds reactor, mix being warming up to 90 ℃, after stirring, add 70 parts 75 ℃ water, obtain emulsion by high-speed shearing equipment, add the acrylic ester thickener adjusting viscosity, obtain defoamer.
Embodiment 4
With 10 parts of octadecanols, 6 parts of tadenans, 6 parts of paraffin, 6 parts of higher alcohols polyether ester (C 14H 30O (EO) 9(PO) 2COC 19H 37), 1 part of non-ionic surface active agent (C 14H 30O (EO) 40H), 1 part of anion emulsifier (disodium 4-dodecyl-2,4 '-oxydibenzenesulfonate) adds reactor, mix being warming up to 95 ℃, after stirring, add 70 parts 75 ℃ water, obtain emulsion by high-speed shearing equipment, add the acrylic ester thickener adjusting viscosity, obtain defoamer.
Embodiment 5
With 10 parts of hexadecanols, 10 parts of eicosanols, 4 parts of Brazil waxs, 2 parts of higher alcohols polyether ester (C 20H 42O (EO) 7(PO) 10COC 11H 23), 1 part of non-ionic surface active agent (C 18H 38O (EO) 20H), 1 part of anion emulsifier (myristyl diphenyl ether sodium disulfonate) adds reactor, mix being warming up to 80 ℃, after stirring, add 70 parts 75 ℃ water, obtain emulsion by high-speed shearing equipment, add the acrylic ester thickener adjusting viscosity, obtain defoamer.
Embodiment 6
With 8 parts of eicosanols, 10 parts of n-octacosanols, 4 parts of paraffin, 6 parts of higher alcohols polyether ester (C 18H 38O (EO) 3(PO) 16COC 17H 35), 1 part of non-ionic surface active agent (C 22H 46O (EO) 60H), 1 part of anion emulsifier (octadecyl diphenyl ether sodium disulfonate) adds reactor, mix being warming up to 90 ℃, after stirring, add 70 parts 75 ℃ water, obtain emulsion by high-speed shearing equipment, add the acrylic ester thickener adjusting viscosity, obtain defoamer.
Comparative Examples 1
With 10 parts of eicosanols, 12 parts of tadenans, 6 parts of microwaxes, 1 part of non-ionic surface active agent (C 8H 18O (EO) 60H), 1 part of anion emulsifier (disodium 4-dodecyl-2,4 '-oxydibenzenesulfonate) adds reactor, mix being warming up to 87 ℃, after stirring, add 70 parts 75 ℃ water, obtain emulsion by high-speed shearing equipment, add the acrylic ester thickener adjusting viscosity, obtain defoamer.
Comparative Examples 2
With 20 parts of octadecanols, 8 parts of Tissuemat Es, 1 part of non-ionic surface active agent (C 12H 26O (EO) 40H), 1 part of anion emulsifier (octyl group diphenyl ether sodium disulfonate) adds reactor, mix being warming up to 90 ℃, after stirring, add 70 parts 75 ℃ water, obtain emulsion by high-speed shearing equipment, add the acrylic ester thickener adjusting viscosity, obtain defoamer.
Performance test:
Defoamer in embodiment and the Comparative Examples is tested as follows:
1, viscosity test
Adopt NDJ-8 type viscosity apparatus to carry out viscosity test.Measure in the emulsion certain hour 20 ℃ and 40 ℃ of lower viscosity situations of change of storing.Specifically see Table 1:
The viscosity of table 1 higher alcohols emulsion defoamer
Figure BSA00000527196100041
As shown in Table 1, the viscosity that has added the emulsion of part higher alcohols polyether esters changed not obvious in 60 day time, and did not add the emulsion of higher alcohols polyether ester, and it is large that viscosity becomes.
2, the mensuration of antifoaming performance
Key instrument device: Portable circulation bubbling instrument
Test condition: 20 ℃ of temperature, flow 9L/min, defoamer addition: 5ul
Tested media: corrugated paper plain boiled water
Concrete method of testing: the Portable circulation bubbling instrument is cleaned up, the foaming medium that adds ormal weight, be heated to design temperature, the turn-on flow rate pump, setting under the flow, circulation bubbling to foam volume is 300ml, then adds the defoamer sample of ormal weight, and record foam volume V is along with the Changing Pattern of time.Same time inner foam height is lower, and antifoaming performance is better.
Test result is as follows:
The antifoaming performance of table 2 higher alcohols emulsion
Figure BSA00000527196100051
By as seen from Table 2, the paper of copying of the present invention's preparation has good antifoaming performance at low temperatures with the higher alcohols emulsion defoamer.

Claims (3)

1. antifoaming agent for low-temperature paper making system is characterized in that consisting of the following composition:
(1), higher alcohols, for carbon number be 12~28 monobasic to trihydroxylic alcohol, described higher alcohols use separately or multiple alcohol mixes and uses;
(2), non-ionic surface active agent, general structure is: R 1O (EO) m H, wherein R 1For carbon number is 8~28 alkyl, mIt is 10~60 integer; Take the consumption of higher alcohols as 100 parts by mass, then the consumption of non-ionic surface active agent is 0.01~10 part;
(3), anion emulsifier, its general structure is as follows:
Figure 786587DEST_PATH_IMAGE001
R wherein 2Be the saturated alkyl of carbon number 8~20, take the consumption of higher alcohols as 100 parts by mass, then the consumption of anion emulsifier is 0.01~5 part;
(4) higher alcohols polyether ester, general structure is: R 3O (EO) x (PO) y COR 4, R wherein 3It is 12~24 alkyl for carbon number; xBe 0~10 integer, yIt is 1~30 integer; R 4It is 8~20 alkyl for carbon number; Take the consumption of higher alcohols as 100 parts by mass, then the consumption of higher alcohols polyether ester is 10~50 parts;
(5) wax is selected from paraffin, montan wax, microwax, Brazil wax, oxidized polyethlene wax, husky rope Fischer-Tropsch wax, Tissuemat E, Carnauba wax and beeswax, and take the consumption of higher alcohols as 100 parts by mass, then the consumption of wax is 16~40 parts;
(6) thickener is selected from xanthan gum, guar gum, polyvinyl alcohol, sodium carboxymethylcellulose, hydroxyethylcellulose and esters of acrylic acid, and its consumption is adjusted according to the required viscosity of reality;
(7) water;
Described antifoaming agent for low-temperature paper making system is prepared by following methods: higher alcohols, non-ionic surface active agent, anion surfactant, higher alcohols polyether ester, wax are mixed, be warming up to 70~95 ℃; 70 ~ 95 ℃ water are slowly added said mixture, then by the further emulsification of high speed shear; Replenish suitable quantity of water to desired concn; At last, add thickener, be adjusted to required viscosity and get final product.
2. a kind of antifoaming agent for low-temperature paper making system as claimed in claim 1, wherein (1) described higher alcohols are selected from dodecanol, tetradecanol, hexadecanol, octadecanol, eicosanol, tadenan, the pure and mild n-octacosanol of lignocerane.
3. a kind of antifoaming agent for low-temperature paper making system as claimed in claim 1, wherein (6) described thickener is esters of acrylic acid.
Figure 641410DEST_PATH_IMAGE002
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CN102600647B (en) * 2012-03-29 2014-05-07 南京四新科技应用研究所有限公司 Method for preparing stable aliphatic emulsion
CN103866610B (en) * 2014-02-25 2016-08-17 苏州恒康新材料有限公司 A kind of paper pulp defoamer and preparation method thereof
CN105220488A (en) * 2015-10-20 2016-01-06 湖州国信物资有限公司 A kind of novel polyethylene defoamer and preparation method thereof
CN106351064A (en) * 2016-08-28 2017-01-25 山东成泰化工有限公司 Antifoaming agent containing cyclohexane phthalate high alcohol ester
CN112023450A (en) * 2019-06-03 2020-12-04 武汉秦曹环保科技有限公司 Special defoaming agent for nuclear power plant and preparation method thereof

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CN100427671C (en) * 2004-12-10 2008-10-22 曹治平 Moderate temperature prnited and dyed organosilicon anti-bubbling and its preparing method
CN100358607C (en) * 2005-10-09 2008-01-02 南京四新科技应用研究所有限公司 Preparation of highly efficient water phase system non-organic silicon defoaming agent
CN101530759B (en) * 2009-03-11 2011-02-09 南京四新科技应用研究所有限公司 Method for dispersing higher fatty alcohol mixture
CN101690857B (en) * 2009-10-10 2011-12-28 南京四新科技应用研究所有限公司 Natural high class fatty alcohol emulsion and preparation method thereof

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