KR100814004B1 - Method for manufacturing watersoluble amide wax - Google Patents

Method for manufacturing watersoluble amide wax Download PDF

Info

Publication number
KR100814004B1
KR100814004B1 KR1020070026130A KR20070026130A KR100814004B1 KR 100814004 B1 KR100814004 B1 KR 100814004B1 KR 1020070026130 A KR1020070026130 A KR 1020070026130A KR 20070026130 A KR20070026130 A KR 20070026130A KR 100814004 B1 KR100814004 B1 KR 100814004B1
Authority
KR
South Korea
Prior art keywords
acid
water
carbon atoms
polyamide
amide wax
Prior art date
Application number
KR1020070026130A
Other languages
Korean (ko)
Inventor
이준혁
임기갑
유창준
Original Assignee
케이에스케미칼 주식회사
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by 케이에스케미칼 주식회사 filed Critical 케이에스케미칼 주식회사
Priority to KR1020070026130A priority Critical patent/KR100814004B1/en
Application granted granted Critical
Publication of KR100814004B1 publication Critical patent/KR100814004B1/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G69/00Macromolecular compounds obtained by reactions forming a carboxylic amide link in the main chain of the macromolecule
    • C08G69/02Polyamides derived from amino-carboxylic acids or from polyamines and polycarboxylic acids
    • C08G69/26Polyamides derived from amino-carboxylic acids or from polyamines and polycarboxylic acids derived from polyamines and polycarboxylic acids
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L77/00Compositions of polyamides obtained by reactions forming a carboxylic amide link in the main chain; Compositions of derivatives of such polymers
    • C08L77/06Polyamides derived from polyamines and polycarboxylic acids
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L91/00Compositions of oils, fats or waxes; Compositions of derivatives thereof
    • C08L91/06Waxes
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09DCOATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
    • C09D5/00Coating compositions, e.g. paints, varnishes or lacquers, characterised by their physical nature or the effects produced; Filling pastes
    • C09D5/04Thixotropic paints
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G73/00Recovery or refining of mineral waxes, e.g. montan wax
    • C10G73/38Chemical modification of petroleum

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Health & Medical Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Polymers & Plastics (AREA)
  • Medicinal Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • General Chemical & Material Sciences (AREA)
  • Wood Science & Technology (AREA)
  • Materials Engineering (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Paints Or Removers (AREA)
  • Polyamides (AREA)

Abstract

A method for manufacturing water-soluble amide wax is provided to promote sagging control of paints, anti-settling during storage, and stability maintenance of viscosity of the paints for a stirring condition. A method for manufacturing water-soluble amide wax comprises the steps of: mixing primary diamine with 2-8 carbon atoms with relatively excessive dimer carboxylic acids, and dicarboxylic acid with 3-16 carbon atoms or monocarboxylic acid with 2-17 carbon atoms; compounding polyamide; forming salt by neutralizing the polyamide with a base; and manufacturing wax of a state that the polyamide is dispersed in water as a solvent.

Description

수용성 아마이드 왁스의 제조방법{Method for Manufacturing Watersoluble Amide Wax}Method for Manufacturing Water Soluble Amide Wax

한국특허등록 10-0309713-0000Korea Patent Registration 10-0309713-0000

한국특허등록 10-0037627-0000 Korea Patent Registration 10-0037627-0000

한국특허등록 10-0254385-0000 Korea Patent Registration 10-0254385-0000

본 발명은 수용성 현탁물이나 미세한 고상 입자를 함유한 유체 내에서 점탄성 조절제(Thixotropic Agent), 역할을 하는 수용성 아마이드왁스의 제조방법에 관한 것이다. The present invention relates to a process for preparing a water-soluble amide wax that acts as a Thixotropic Agent, in a fluid containing water-soluble suspensions or fine solid particles.

일반적인 유체는 일정하게 점도를 유지하고 있으나 점탄성 조절제가 투입된 유체는 정치 시 겔(Gel) 상태의 성질을 갖고, 외부에서 응력 즉 전단 응력을 가해주면 겔 상태에서 졸(Sol) 상태로 변하여 정치시보다 점도를 낮게 감소시켜 주고, 다시 외부의 응력을 제거하면 졸 상태에서 겔 상태로 환원되어 점도가 회복되는 겔과 졸의 가역변화가 가능한 성질을 갖고 있다.The general fluid maintains a constant viscosity, but the fluid in which the viscoelastic modifier is in a gel state when stationary, and when the external stress or shear stress is applied, the fluid changes from a gel state to a sol state, When the viscosity is lowered and the external stress is removed again, the gel can be reversibly changed from the sol state to the gel state and the viscosity can be recovered.

이러한 성질을 틱소트로피(Thixotropy)라고 하는데, 한국 공업규격(KS M5001)에서는 온도가 일정할 때 교반하면 졸 상이 되고 정치하면 겔 상이 되는 콜로이드 분산체의 가역적인 성질이라고 기재하고 있다.This property is called thixotropy, and the Korean Industrial Standard (KS M5001) states that it is a reversible property of a colloidal dispersion which becomes a sol phase when stirred at a constant temperature and a gel phase when left standing.

점탄성 조절제는 도료, 바니쉬, 인쇄잉크, 접착제, 적층물, 에나멜 등에 첨가하여 작업 시 점도가 적절히 감소되어 유동특성을 양호하게 하고, 작업 후 유체의 흐름성을 억제시켜 주는 성질을 갖고 있을 뿐만 아니라, 저장 시 고상입자의 침강을 방지시켜 주는 특성을 갖고 있다.Viscoelasticity modifiers are added to paints, varnishes, printing inks, adhesives, laminates, enamels, etc. to reduce the viscosity during operation to improve flow characteristics, and to inhibit fluid flow after operation. It has the property of preventing sedimentation of solid particles during storage.

액상 도료 시스템에서 일반적으로 고상 입자가 유체계 내에서 침강하는 속도를 스토크(Stoke)의 식으로 표현할 수 있는데 이를 간단하게 설명하면 다음과 같다.In liquid paint systems, the rate at which solid particles settle in a fluidic system can be expressed by Stoke's equation.

Figure 112007021422710-pat00001
Figure 112007021422710-pat00001

침강 속도를 줄이기 위해서는 분산입자의 반경을 작게 하거나, 유체와 입자의 밀도차이를 적게 하거나, 유체의 점도를 높여주면 해결될 수 있는데, 단순히 점도를 높여 입자의 침강을 방지시켜 줄 경우, 작업 시 점도가 높아 작업성이 불량할 뿐만 아니라, 작업 후 평활성(levelling)이 불량하여 매끈한 표면을 얻을 수 없는 단점이 있다.In order to reduce the settling speed, it can be solved by reducing the radius of the dispersed particles, by reducing the density difference between the fluid and the particles, or by increasing the viscosity of the fluid. It is not only poor workability due to high, there is a disadvantage that a smooth surface can not be obtained because of poor leveling (working).

본 발명은 수용성 금속 도료, 방식도료 또는 침강 방지가 필요한 비중이 큰 안료를 포함한 도료 등에 적용되는 유변성 제제(rheological agent)와 관련된다. 금속 도료에 이용되는 알루미늄과 마이카 안료 그리고 방식도료에 이용되는 안료들은 안료의 입자크기가 매우 크다. 그리고 비중 또한 커서 도료 내에서의 안료 침강은 매우 빠르게 일어난다. 잘 알려진 것처럼 유용성 도료에서는 유용성 아마이드 왁스 또는 폴리에틸렌 옥사이드 왁스들이 침강 방지제로서 이용된다. 하지만 이러한 첨가제들 대부분은 수용성 도료에서는 적합하지 않다.The present invention relates to rheological agents applied to water-soluble metal paints, anticorrosive paints or paints containing high specific gravity pigments that require sedimentation prevention. Aluminum and mica pigments used in metal paints and pigments used in anticorrosive paints have a very large particle size. In addition, the specific gravity is also large, the pigment settling in the paint occurs very quickly. As is well known, oil-soluble amide waxes or polyethylene oxide waxes are used as antisettling agents in oil-soluble paints. However, most of these additives are not suitable for water-soluble paints.

최근에 환경적인 문제로 인해 수용성 도료에 대한 연구가 활발히 이루어지고 있으며, 수용성 도료에 대한 침강 방지제로서 점토(clay) 계열 또는 실리카 계열 들이 무기계 침강 방지제로서 추천된다. 하지만 이러한 무기첨가제들은 광택저하의 원인이 되고 도료제조 후 마지막 단계에서 첨가하는데 어려움이 있다. 뿐만 아니라 첨가제들의 상태가 미립의 분말 상이어서 도료 제조 시 분진의 발생이 매우 심하다.Recently, studies on water-soluble paints are being actively conducted due to environmental problems, and clay- or silica-based silicas are recommended as inorganic sedimentation inhibitors. However, these inorganic additives cause gloss deterioration and are difficult to add at the final stage after paint production. In addition, since the state of the additives in the form of fine powder, the generation of dust in the paint production is very severe.

본 발명은 상기의 문제점들을 해결하기 위한 수용성 아마이드왁스의 제조방법을 제공하는데 그 목적이 있는 것이다.It is an object of the present invention to provide a method for producing a water-soluble amide wax for solving the above problems.

상기 본 발명의 목적은 탄소수 2~8개의 일차 디아민과; 상대적으로 과잉의 다이머 카르복실산 또는 다이머 산과 탄소수 3~16개를 갖는 다른 디카르복실산 또는 탄소수 2~17개를 갖는 모노 카르복실산의 혼합물로서 폴리아미드를 합성하고, 염기로 중화하여 염을 형성시킴으로써 용제인 물에 폴리아미드가 분산된 상태의 왁스를 제조하는 것을 특징으로 하는 수용성 아미드 왁스의 제조방법에 의해 달성된다. The object of the present invention is a primary diamine having 2 to 8 carbon atoms; A polyamide is synthesized as a mixture of a relatively dimer carboxylic acid or dimer acid and another dicarboxylic acid having 3 to 16 carbon atoms or a mono carboxylic acid having 2 to 17 carbon atoms, and neutralized with a base to neutralize the salt. It is achieved by the manufacturing method of the water-soluble amide wax characterized by manufacturing the wax in the state in which the polyamide was disperse | distributed to the water which is a solvent.

본 발명에 사용된 다이머 산은 불포화 지방산들을 이용하여 이합체화 반응을 통하여 얻어진다. 그리고 함께 사용되는 디카르복실산은 숙신산, 아디프산, 아젤라산, 세바스산 등이다. 모노카르복실산은 12-히드록시스테아르산, 올레산, 라우르산, 스테아르산 등이다. 이들 혼합물에서 다이머 산의 몰 비율은 60%이상이다. 60%이상일 경우에 합성된 아마이드 왁스는 수용화가 가능하며, 첨가제로서 효과가 있다.The dimer acid used in the present invention is obtained through dimerization reaction using unsaturated fatty acids. And dicarboxylic acids used together are succinic acid, adipic acid, azelaic acid, sebacic acid and the like. Monocarboxylic acids are 12-hydroxystearic acid, oleic acid, lauric acid, stearic acid and the like. The molar ratio of dimer acid in these mixtures is at least 60%. If more than 60% synthesized amide wax can be solubilized, it is effective as an additive.

본 발명에 사용된 일차 디아민은 m-크실리덴디아민, 에틸렌디아민, 4,4-디아미노-디페닐메탄 등이다.Primary diamines used in the present invention are m-xylidenediamine, ethylenediamine, 4,4-diamino-diphenylmethane and the like.

일차 디아민에 대한 전체 카르복실산의 당량 과잉비율은 1.2~1.5이다. 1.2보다 작을 경우에는 수용화에 어려움이 있고 성능의 효과가 작아진다. 그리고 1.5이상일 경우에는 도료에 적용되었을 경우에 도료 도막의 내수성을 떨어뜨린다.The equivalent excess ratio of total carboxylic acid to primary diamine is 1.2 to 1.5. If less than 1.2, it is difficult to accept and the effect of performance is small. And when it is 1.5 or more, when applied to paint, the water resistance of paint coat falls.

본 발명에 의해 합성된 아마이드의 최종 산가는 40~100mgKOH/g 범위에 있다. 50~90의 범위가 가장 적합하다. 아마이드 합성 반응은 일반적으로 사용되는 공정과 유사하다. 약 180℃에서 5시간 정도 물이 빠져나오는 축합반응으로 진행된다. 이렇게 합성된 아마이드를 약 100℃까지 냉각한 후 점도를 낮추기 위한 유기용제를 투 입하고 내용물을 80~90℃로 유지한 후 중화용 염기가 녹아 있는 물에 소량씩 투입 한다. 이때 반응부는 약50~70℃를 유지하도록 하고, 균일상이 되도록 교반을 해 주어야 한다. 이렇게 중화된 아마이드는 일반적으로 수 시간에서 하루 정도 지난 후에 왁스(paste)의 형태가 된다. 최종 합성품의 고형분은 15~30%이다. The final acid value of the amide synthesized by the present invention is in the range of 40-100 mgKOH / g. The range of 50-90 is most suitable. Amide synthesis reactions are similar to those commonly used. It proceeds with a condensation reaction of water coming out at about 180 ° C. for about 5 hours. After cooling the synthesized amide to about 100 ℃ and then added an organic solvent to lower the viscosity, maintain the contents at 80 ~ 90 ℃ and put a small amount in the water dissolved neutralizing base. At this time, the reaction part should be maintained at about 50 ~ 70 ℃, it should be stirred to become a uniform phase. These neutralized amides generally form waxes after hours to a day. The solid content of the final composite is 15-30%.

이하 실시예를 통해 본 발명을 보다 상세하게 설명한다. The present invention will be described in more detail with reference to the following Examples.

<실시예1>Example 1

4구 플라스크에 다이머 산(0.63mole)과 아젤라산(0.27mole)를 반응부에 넣고 60~70℃까지 교반하며 가열하였다. 이때 내용물의 산화를 방지하기 위하여 질소를 반응초기부터 종료 때까지 지속적으로 주입하였다. 내용물이 액상상태가 되면 헥사메틸렌 디아민(0.65mole)을 반응부에 투입하고 내용물의 온도를 140℃로 승온시켜 1시간 동안 반응시키고 다시 내용물의 온도를 190℃까지 4시간에 걸쳐 승온시켰다. 매시간 마다 산가와 아민가를 측정하며 아민가 5이하, 산가 65이하가 되면 반응을 종료하고 내용물의 온도를 100℃로 냉각시켰다. 이후 합성된 아마이드의 50%에 해당하는 프로필렌글리콜 모노메틸에테르를 투입하고 내용물의 온도를 80℃로 유지하였다. 2-디메틸아미노에탄올(0.35mole)이 녹아 있는 물을 교반하며 중화된 아마이드 용액을 소량씩 투입하였다. 이때 내용물 온도는 60℃를 유지하였다. 추가로 60℃에서 1시간 동안 충분히 교반하고 실온까지 냉각하여 1일 동안 숙성시켰다. 합성품 중의 폴리아마이드 고형분은 약20%였다.In a four-necked flask, dimer acid (0.63 mole) and azelaic acid (0.27 mole) were added to the reaction part, and the mixture was heated with stirring to 60 to 70 ° C. At this time, nitrogen was continuously injected from the beginning to the end of the reaction to prevent oxidation of the contents. When the contents were in a liquid state, hexamethylene diamine (0.65 mole) was added to the reaction part, the temperature of the contents was raised to 140 ° C. for 1 hour, and the temperature of the contents was further raised to 190 ° C. over 4 hours. The acid value and amine value were measured every hour, and when the amine value was 5 or less and the acid value was 65 or less, the reaction was terminated and the temperature of the contents was cooled to 100 ° C. Since propylene glycol monomethyl ether corresponding to 50% of the synthesized amide was added and the temperature of the contents was maintained at 80 ℃. The water in which 2-dimethylaminoethanol (0.35 mole) was dissolved was stirred, and a small amount of neutralized amide solution was added thereto. At this time, the content temperature was maintained at 60 ℃. Further stirred at 60 ° C. for 1 hour, cooled to room temperature and aged for 1 day. Polyamide solids in the synthetic product was about 20%.

실시예 2~6, 비교예1~2를 같은 방법으로 합성하였으며 그 원료 및 물성 시험 결과를 표 1과 표 2에 나타내었다. Examples 2 to 6 and Comparative Examples 1 to 2 were synthesized in the same manner, and the raw materials and the property test results are shown in Tables 1 and 2.

표1. 아마이드왁스 합성Table 1. Amide Wax Synthesis

원료 종류Raw material type 원료명Raw material name 실시예Example 비교예Comparative example 1One 22 33 44 55 66 1One 22 산 (mole) Mountain 다이머 산Dimer acid 0.630.63 0.500.50 0.550.55 0.650.65 0.600.60 0.650.65 0.600.60 0.500.50 아젤라산Azela Mountain 0.270.27 0.150.15 숙신산Succinic acid 0.190.19 0.250.25 12-히드록시스테아르산12-hydroxystearic acid 0.100.10 아민 (mole)Amine 헥사메틸렌디아민Hexamethylenediamine 0.650.65 0.600.60 0.400.40 0.650.65 0.200.20 0.450.45 m-크실리덴디아민m-xylidenediamine 0.300.30 0.420.42 중화제 (mole)Neutralizer (mole) 2-디메틸아미노에탄올2-dimethylaminoethanol 0.350.35 0.400.40 0.360.36 0.430.43 0.450.45 0.370.37 0.780.78 0.150.15 폴리아미드의 산가(mg KOH/g)Acid value of polyamide (mg KOH / g) 6161 7272 6464 7171 7676 6363 125125 2626

표2. 도료 물성 테스트Table 2. Paint property test

시험명 조성물Test Name Composition 실시예Example 비교예Comparative example 1One 22 33 44 55 66 1One 22 수용성 아크릴수지*1 Water Soluble Acrylic Resin * 1 4444 4444 4444 4444 4444 4444 4444 4444 멜라민수지*2 Melamine resin * 2 1010 1010 1010 1010 1010 1010 1010 1010 증류수Distilled water 3434 3434 3434 3434 3434 3434 3434 3434 수용성 알미늄 페이스트*3 Water Soluble Aluminum Paste * 3 1010 1010 1010 1010 1010 1010 1010 1010 Thixotropic AgentThixotropic agent 22 22 22 22 22 22 22 22 도료물성Paint property 1C1C 2C2C 3C3C 4C4C 5C5C 6C6C 9C9C 10C10C Thixo IndexThixo Index 2.642.64 1.801.80 1.551.55 2.382.38 2.032.03 1.311.31 1.951.95 1.261.26 흐름방지성(mils)Flow resistance (mils) 4040 3030 3030 3535 3535 2525 3535 2525 침강방지성(cm)Sedimentation Prevention (cm) 1.91.9 2.52.5 3.03.0 1.81.8 2.02.0 4.54.5 2.02.0 5.05.0 저장성(입자발생)Storability (particle generation) 없음none 없음none 없음none 없음none 없음none 없음none 없음none 있음has exist

*1 : Coatax WF-268* 1: Coatax WF-268

*2 : Cymel 325* 2: Cymel 325

*3 : Silberline Silo-wet TM325AR)* 3: Silberline Silo-wet TM325AR)

각각의 원료들을 투입하고 고속교반기를 이용하여 2000rpm으로 20분간 교반 후에 도료물성을 측정하였다. Thixo Index는 도료를 점도계를 이용하여 같은 조건에서 60rpm과 6rpm로 각각 측정하여 6rpm 측정값을 60rpm 측정값으로 나누어 측정하였다. 흐름 방지성은 ASTM D4400으로 측정하였다. 침강 방지성은 길이 25㎝, 직경 3.7㎝인 유리관에 20㎝까지 액을 채우고 실온에서 15일 방치 후에 안료가 침강되고 윗부분에 남아있는 맑은 액의 높이를 측정하였다. 저장성은 저장용기에 담아 50℃에서 4일간 저장 후에 입자(seed)발생 여부를 KSM5000에 기초하여 측정하였다. Each raw material was added and the paint physical properties were measured after stirring for 20 minutes at 2000 rpm using a high speed stirrer. Thixo Index was measured by dividing the paint at 60 rpm and 6 rpm, respectively, under the same conditions using a viscometer and dividing the 6 rpm reading into the 60 rpm reading. Flow resistance was measured by ASTM D4400. The sedimentation prevention property measured the height of the clear liquid which filled the liquid up to 20 cm in the glass tube of 25 cm in length and 3.7 cm in diameter, and after standing at room temperature for 15 days. Storage performance was measured on the basis of KSM5000 whether the particles (seed) generation after storage for 4 days at 50 ℃ in a storage container.

본 발명의 제조방법은 기존에 광범위하게 사용되고 있는 유용성 아마이드 왁스계 점탄성 조절제의 제조방법과 비교하여 분쇄 및 숙성 공정이 필요 없어 제조 방법이 간단하고 시간과 비용이 절약된다.The manufacturing method of the present invention does not require a pulverizing and aging process as compared with the manufacturing method of the oil-soluble amide wax-based viscoelastic modifier, which is widely used in the related art, and thus the manufacturing method is simple and time and cost are saved.

본 발명의 방법에 의해 이렇게 제조된 왁스는 도료의 흐름성조절(saggingntrol), 저장중 침강 방지(anti-settling), 교반 조건에 따른 도료점도의 안정성 유지 그리고 도료 내 안료 등의 분산제로서의 효과가 있다. 본 발명의 아마이드 왁스는 기존에 광범위하게 사용되고 있는 무기계 점탄성 조절제와 비교하여 사용하기가 용이하며, 성능이 우수하다. 즉, 안료의 침강 방지에 탁월하며, 흐름성 조절, 점도 안정 및 안료 분산에 효과가 있으며 특히 수용성 금속 도료(알루미늄, 마이카 안료)에 적용될 경우 침강 방지 효과와 안료의 배향에도 우수한 성능 을 발휘한다. 도료제조에 사용될 경우 내열성 및 광택이 우수하고, 장기 저장 시 고상입자가 침강하여 굳어지는 현상이 아주 적다. 또한 도료 도막의 건조 후 내수성에 영향을 주지 않는다.The wax thus prepared by the method of the present invention has an effect as a dispersant such as saggingntrol of the paint, anti-settling during storage, maintaining the stability of the paint viscosity according to the stirring conditions, and pigments in the paint. . The amide wax of the present invention is easier to use compared to the inorganic viscoelastic modifiers widely used in the past, and excellent in performance. That is, it is excellent in preventing the settling of pigments, and is effective in controlling flow, stabilizing viscosity, and dispersing pigments. In particular, when applied to water-soluble metal paints (aluminum and mica pigments), it exhibits excellent performance in preventing settling and pigment orientation. When used in paint manufacturing, it has excellent heat resistance and gloss, and there is little phenomenon that solid particles settle and harden during long-term storage. Moreover, it does not affect water resistance after drying of a coating film.

Claims (7)

탄소수 2~8개의 일차 디아민과; 상대적으로 과잉의 다이머 카르복실산과 탄소수 3~16개를 갖는 다른 디카르복실산 또는 탄소수 2~17개를 갖는 모노카르복실산의 혼합물로서 폴리아미드를 합성하고, 염기로 중화하여 염을 형성시킴으로써 용제인 물에 폴리아미드가 분산된 상태의 왁스를 제조하는 것을 특징으로 하는 수용성 아미드 왁스의 제조방법. Primary diamines having 2 to 8 carbon atoms; Solvent by synthesizing polyamide as a mixture of relatively dimer carboxylic acid and other dicarboxylic acid having 3 to 16 carbon atoms or monocarboxylic acid having 2 to 17 carbon atoms, neutralizing with base to form salt A method for producing a water-soluble amide wax, comprising producing wax in a state in which polyamide is dispersed in phosphorus water. 제 1 항에 있어서, 일차 디아민은 m-크실리덴디아민, 에틸렌디아민 또는 4,4-디아미노-디페닐메탄인 것을 특징으로 하는 수용성 아미드 왁스의 제조방법.The method of claim 1 wherein the primary diamine is m-xylidediamine, ethylenediamine or 4,4-diamino-diphenylmethane. 제 1 항에 있어서, 일차 디아민 대 전체 카르복실산의 당량비는 1.2~1.5인 것을 특징으로 하는 수용성 아미드 왁스의 제조방법.2. The process of claim 1 wherein the equivalent ratio of primary diamine to total carboxylic acid is 1.2 to 1.5. 제 1 항에 있어서, 디카르복실산은 숙신산, 아디프산, 아젤라산 또는 세바스산인 것을 특징으로 하는 수용성 아미드 왁스의 제조방법.The method of claim 1 wherein the dicarboxylic acid is succinic acid, adipic acid, azelaic acid or sebacic acid. 제 1 항에 있어서, 모노카르복실산은 12-히드록시스테아르산, 올레산, 라우르산, 또는 스테아르산인 것을 특징으로 하는 수용성 아미드 왁스의 제조방법.The method of claim 1, wherein the monocarboxylic acid is 12-hydroxystearic acid, oleic acid, lauric acid, or stearic acid. 제 1 항에 있어서, 전체 카르복실산 중 다이머 카르복실산의 비율은 몰비로 60% 이상인 것을 특징으로 하는 수용성 아미드 왁스의 제조방법.The method for producing a water-soluble amide wax according to claim 1, wherein the ratio of the dimer carboxylic acid in the total carboxylic acid is 60% or more in molar ratio. 제 1 항에 있어서, 중합시 폴리아마이드의 산가는 40~100mgKOH/g로 조절되는 것을 특징으로 하는 수용성 아미드 왁스의 제조방법.The method of claim 1, wherein the acid value of the polyamide during the polymerization is adjusted to 40 ~ 100mgKOH / g.
KR1020070026130A 2007-03-16 2007-03-16 Method for manufacturing watersoluble amide wax KR100814004B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
KR1020070026130A KR100814004B1 (en) 2007-03-16 2007-03-16 Method for manufacturing watersoluble amide wax

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
KR1020070026130A KR100814004B1 (en) 2007-03-16 2007-03-16 Method for manufacturing watersoluble amide wax

Publications (1)

Publication Number Publication Date
KR100814004B1 true KR100814004B1 (en) 2008-03-14

Family

ID=39398862

Family Applications (1)

Application Number Title Priority Date Filing Date
KR1020070026130A KR100814004B1 (en) 2007-03-16 2007-03-16 Method for manufacturing watersoluble amide wax

Country Status (1)

Country Link
KR (1) KR100814004B1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2022107792A1 (en) * 2020-11-18 2022-05-27 共栄社化学株式会社 Viscosity modifier and film-forming agent containing same

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR900005402B1 (en) * 1987-09-30 1990-07-28 고려화학 주식회사 Process for the preparation of viscosity regulator
US5866675A (en) 1995-11-09 1999-02-02 H. B. Fuller Licensing & Financing, Inc. Nonwoven web comprising water soluble polyamides and articles constructed therefrom
JP2004307817A (en) 2003-04-01 2004-11-04 Rohm & Haas Co High-melting wax useful for sintering metal

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR900005402B1 (en) * 1987-09-30 1990-07-28 고려화학 주식회사 Process for the preparation of viscosity regulator
US5866675A (en) 1995-11-09 1999-02-02 H. B. Fuller Licensing & Financing, Inc. Nonwoven web comprising water soluble polyamides and articles constructed therefrom
JP2004307817A (en) 2003-04-01 2004-11-04 Rohm & Haas Co High-melting wax useful for sintering metal

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2022107792A1 (en) * 2020-11-18 2022-05-27 共栄社化学株式会社 Viscosity modifier and film-forming agent containing same

Similar Documents

Publication Publication Date Title
DK2877445T3 (en) FATIC ACID DIAMIDS INCLUDING HYDROXYSTEARIC ACIDS AS ORGANOGLATIC AGENTS
JP2731532B2 (en) Thixotropic composition
JP6283414B2 (en) Fatty acid diamides based on alicyclic and aliphatic diamines used as organogelators
CN113195592B (en) Viscosity modifier and curable composition
CN113840858B (en) Rheology control additives containing cyclic amides
KR100814004B1 (en) Method for manufacturing watersoluble amide wax
JP6249195B2 (en) Rheology control agent containing a combination of agents
WO2022025203A1 (en) Viscosity adjusting agent and curable composition
JPS6044352B2 (en) Flow property modifier
JP6283415B2 (en) Lactam or amino acid fatty acid amides and their use as organogelators
JP2749364B2 (en) Solvent-based alkyd paint
JP7516548B2 (en) Viscosity modifier for aqueous resin and aqueous coating composition
CN110914376B (en) Anti-settling agent composition for water-based paint
KR20120110306A (en) Powdery polyamide resin composition for thixotropic additive, preparation method thereof, and powdery paints for ship comprising the same
KR100254385B1 (en) Method for preparing thixotropic agent
KR900005402B1 (en) Process for the preparation of viscosity regulator
JP7447106B2 (en) Rheology additive based on 1,5-pentamethylenediamine, which may be bio-based
KR100794929B1 (en) The preparation method of thixotropic agent which is urea modified amide solution
KR20230107745A (en) Viscosity modifier and film forming agent containing the same
KR100309713B1 (en) Method for Manufacturing Thixotropic agent of Amide Wax
CN116670220A (en) Rheology control agent
US20200308106A1 (en) Urea and urethane group containing anti-settling rheology control additive

Legal Events

Date Code Title Description
A201 Request for examination
E701 Decision to grant or registration of patent right
GRNT Written decision to grant
FPAY Annual fee payment

Payment date: 20121217

Year of fee payment: 6

FPAY Annual fee payment

Payment date: 20140129

Year of fee payment: 7

FPAY Annual fee payment

Payment date: 20150129

Year of fee payment: 8

FPAY Annual fee payment

Payment date: 20160302

Year of fee payment: 9

FPAY Annual fee payment

Payment date: 20200108

Year of fee payment: 13