WO2010133119A1 - Salt free, oxidation-resistant zinc cyanamide anticorrosive pigments for environment-friendly mirror back coatings and preparation method thereof - Google Patents
Salt free, oxidation-resistant zinc cyanamide anticorrosive pigments for environment-friendly mirror back coatings and preparation method thereof Download PDFInfo
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- WO2010133119A1 WO2010133119A1 PCT/CN2010/072005 CN2010072005W WO2010133119A1 WO 2010133119 A1 WO2010133119 A1 WO 2010133119A1 CN 2010072005 W CN2010072005 W CN 2010072005W WO 2010133119 A1 WO2010133119 A1 WO 2010133119A1
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- C01—INORGANIC CHEMISTRY
- C01C—AMMONIA; CYANOGEN; COMPOUNDS THEREOF
- C01C3/00—Cyanogen; Compounds thereof
- C01C3/16—Cyanamide; Salts thereof
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- the invention relates to an anticorrosive pigment and a production method in the chemical industry, in particular to a salt-free and anti-oxidation type cyanamide zinc anticorrosive pigment and a production method thereof for the environmental protection mirror back coating.
- the silver or aluminum layer on the mirror is protected by a mirror back coating, but it is highly susceptible to corrosion and decomposition when present in the environment, such as moisture, atmospheric pollutants, salt, hydrogen sulfide, ammonia and chloride.
- a mirror back coating is highly susceptible to corrosion and decomposition when present in the environment, such as moisture, atmospheric pollutants, salt, hydrogen sulfide, ammonia and chloride.
- heavy anti-corrosion primer, zinc phosphate, aluminum tripolyphosphate and the like are often used as anti-corrosion pigments, but the effect is opposite to the expectation, and does not have a good antiseptic effect in the mirror back coating. It actually has a corrosive effect on the silver or aluminum layer.
- the coating used for the mirror back coating is mainly a one-component amino baking varnish cured by a melamine resin, and a metal-containing cyanamide antioxidant pigment can impart an excellent corrosion-resistant mirror back coating.
- the method for producing zinc cyanamide has a calcination method in which zinc oxide is calcined together with an excess amount of urea or dicyandiamide under nitrogen or vacuum, first at 135 ° C to 200 ° C, and then at 600 ° C to 800 ° C. In hours, a zinc cyanamide pigment is obtained.
- the disadvantage of this high energy consumption method is that the resulting product structure is quite "closed”, exhibiting a low specific surface area and porosity, and thus reduced reactivity, and does not have the high corrosion protection activity required for the mirror back coating system.
- the above various routes for preparing zinc cyanamide have the following disadvantages, and are required to be obtained by excessive cyanamide compound, nitrogen or under vacuum, and at a high temperature; or by precipitation of hydrocyanamide salt; or by preparing cyanide.
- the amine hydrogen intermediate product is prepared with zinc oxide, has low product activity, high by-products, high water-soluble salt, high energy consumption and complicated process. Therefore, the development of environmentally friendly mirror back coatings for salt-free, anti-oxidant zinc cyanide anti-corrosion pigments is of great significance to improve the corrosion resistance of mirror coatings.
- the purpose of the invention is to solve the deficiencies of the above-mentioned technologies and to provide a non-environmental mirror-back coating which has less raw materials, low energy consumption, less waste water, less by-products, simple process and good anti-corrosion performance of the pigment. Salt-free, anti-oxidation zinc cyanide anticorrosive pigment and production method.
- the salt-free and oxidation-resistant zinc cyanide anticorrosive pigment for environmentally friendly mirror coatings designed by the present invention is a product obtained by reacting zinc oxide with a cyanamide compound and adding a coupling agent.
- the method for producing the salt-free and anti-oxidation type cyanamide anti-corrosion pigment for the environmental protection mirror back coating designed by the invention is to completely disperse the highly active zinc oxide into the deionized water to prepare a uniform zinc oxide slurry, and slowly add the solution.
- the cyanamide compound starts the exothermic reaction under stirring and dispersion, and when the temperature starts to decrease, it is stirred at a high speed to completely react.
- Through instrumental observation it is found that the tiny particles begin to decrease until there is no particles, the water is statically separated, and the separated water is recycled for the next time to obtain the zinc oxide slurry, and the separated zinc cyanamide precipitate is subjected to pressure filtration to remove water. Then dry at 105 ° C until the moisture is less than 0. 1% or less, pulverization is carried out, and the fineness reaches 320 mesh sieve residue less than 0.05% or less to obtain a zinc cyanamide anticorrosive pigment.
- a coupling agent may be added in the reaction of zinc oxide and a cyanamide compound.
- the weight fraction of zinc oxide, deionized water, cyanamide compound and coupling agent in the reaction is 15-25 parts of zinc oxide, respectively. 55-65 parts of ionized water, 18-23 parts of cyanamide compound, and 1.5-2.5 parts of coupling agent.
- the highly active zinc oxide is ZnO-Xl or ZnO-X2 Or ZnO-Tl or Zn0-T2 or Zn0 -T3 or BA01-05 (type I) or BA01-05 (type II):
- the cyanamide compound is urea or dicyandiamide or hydrocyanamide or monocyanamide.
- the coupling agent is 1121# coupling agent or JN-A coupling agent or TYZOR AA-75 coupling agent or KH-550 coupling agent.
- the core part is made of high-activity zinc oxide, reacted with metal cyanamide compound in an aqueous medium, and completely reacted at room temperature by a specific process technology to achieve impurity-free salt impurities. After adding a coupling agent, it is ensured. Stability, through the filtration, water separation, pressure filtration, drying, pulverization production process, to obtain salt-free, antioxidant-type zinc cyanamide pigment. Due to the use of highly active zinc oxide, the reaction rate is improved, especially through specific reaction equipment and process technology, as well as key process control means, so that the content of water-soluble free salts and impurities of zinc cyanamide is less than 0.2%.
- the product does not contain lead, oil absorption, water soluble free salt and low impurity content, good dispersibility, can inhibit the oxidation of the substrate or metal layer, prevent the saponification of the coating, neutralize the free sulfides and chlorides generated or present during the corrosion process. Ions, save energy, reduce environmental pollution, reduce manufacturing costs, product performance has reached advanced levels in foreign countries, and has good economic benefits.
- the separated water is recycled for the next time to obtain the zinc oxide slurry, and the separated zinc cyanide precipitate is filtered by a plate and frame filter to remove water, and then The stainless steel constant temperature oven is dried at 105 ° C to a moisture content of less than 0.1%, and is transferred to a stainless steel powder machine for pulverization, and the fineness reaches 320 mesh sieve residue of less than 0.05%.
- 15g-20g ZnO-Xl zinc oxide is completely dispersed in 50g-65g deionized water to prepare a uniform zinc oxide slurry, and slowly add 15g-20g dicyandiamide Under stirring and dispersion, the exothermic reaction begins.
- high-speed stirring is carried out to completely react. It is observed by the instrument that the fine particles begin to decrease until no particles are added, and 1.5g-2.0g KH-550 is added. The mixture is stirred evenly, and the water is separated at rest.
- the separated water is recycled for the next time to obtain the zinc oxide slurry, and the separated zinc cyanide precipitate is filtered by a plate and frame filter to remove water, and then the stainless steel constant temperature oven is used.
- the medium is dried at 105 ° C to a moisture content of less than 0.1%, and is transferred to a stainless steel powder machine for pulverization, and the fineness reaches 320 mesh sieve residue of less than 0.05%.
- the separated water is recycled for the next time to obtain the zinc oxide slurry, and the separated zinc cyanide precipitate is filtered by a plate and frame filter to remove water, and then The stainless steel constant temperature oven is dried at l05 ° C to a moisture content of less than 0.1%, and is transferred to a stainless steel powder machine for pulverization, and the fineness reaches 320 mesh sieve residue of less than 0.05%.
- the separated water is recycled for the next time to obtain the zinc oxide slurry, and the separated zinc cyanide precipitate is filtered by a plate and frame filter to remove water, and then The stainless steel constant temperature oven is dried at 105 ° C to a moisture content of less than 0.1%, and is transferred to a stainless steel powder machine for pulverization. The fineness reaches 320 mesh and the residue is less than 0. 05% or less.
- the separated water is recycled for the next time to obtain the zinc oxide slurry, and the separated zinc cyanide precipitate is filtered by a plate and frame filter to remove water, and then The stainless steel constant temperature oven is dried at 105 ° C to a moisture content of less than 0.1%, and is transferred to a stainless steel powder machine for pulverization, and the fineness reaches 320 mesh sieve residue of less than 0.05%.
- Example 1 Performance Example 1
- Example 2 Example 3
- Example 4 Example 5 Exterior White powder White powder White powder White powder White powder Oil absorption value (g/100 g) 12.5 13.5 15 14 16.5 Moisture (%) 0.08 0.05 0.07 0.04 0.08 320 mesh residue (%) 0.02 0.025 0.03 0.01 0.04 No salt (water soluble salt) (%) 0.11 0.25 0.45 0.3 0.7
- the mirror back paint was prepared by the proportion of the coating formulation of the above-mentioned 1-5 examples in the following examples, as shown in Table 2.
- the coating loss extends up to 3.5mm inward.
- the reflective layer has no change point, the protective coating has no change point, and the edge coating loss extends up to 0.13mm.
- the reflective layer has a small number of change points and the protective coating has no change point. More reflective points with a reflective layer diameter of 0.3 mm or more
- the protective coating has many points and the edge coating has a large loss.
- the reflective layer changes a lot and the protective coating begins to fall off. There is no change point in the reflective layer, no change in the protective coating, and the maximum loss of the edge coating extends 0.15mm inward.
- Optical performance visible light reflectance ⁇ 85% 87.73% 82.55% 75.11% 69% 54.85% 86.99%
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Abstract
Description
本发明涉及一种化工行业中防腐颜料及生产方法,特别是一种环保镜背涂料专用无盐、抗氧化型氰胺锌防腐颜料及生产方法。 The invention relates to an anticorrosive pigment and a production method in the chemical industry, in particular to a salt-free and anti-oxidation type cyanamide zinc anticorrosive pigment and a production method thereof for the environmental protection mirror back coating.
镜子上的银层或铝层使用镜背涂层进行保护,但是当环境中存在的水气、大气污染物、盐、硫化氢、氨气和氯化物等时,仍极易腐蚀分解。特别是在钢结构重防腐底漆中,经常用到磷酸锌、三聚磷酸铝等作防腐颜料,但其使用效果却与期望相反,在镜背涂层中并未起到好的防腐作用,实际上对银层或铝层产生腐蚀作用。 The silver or aluminum layer on the mirror is protected by a mirror back coating, but it is highly susceptible to corrosion and decomposition when present in the environment, such as moisture, atmospheric pollutants, salt, hydrogen sulfide, ammonia and chloride. Especially in the steel structure heavy anti-corrosion primer, zinc phosphate, aluminum tripolyphosphate and the like are often used as anti-corrosion pigments, but the effect is opposite to the expectation, and does not have a good antiseptic effect in the mirror back coating. It actually has a corrosive effect on the silver or aluminum layer.
用于镜背涂层的涂料,主要是通过三聚氰胺型树脂固化的单组份氨基烤漆,添加含金属的氰胺抗氧化型颜料,能赋予优良的耐腐蚀镜背涂层。 The coating used for the mirror back coating is mainly a one-component amino baking varnish cured by a melamine resin, and a metal-containing cyanamide antioxidant pigment can impart an excellent corrosion-resistant mirror back coating.
目前生产氰胺锌的方法有煅烧法,是将氧化锌与过量的尿素或双氰胺一起,在氮气或真空下,先于135℃-200℃,再于600℃-800℃下煅烧处理2小时,得到氰胺锌颜料。这种高能耗法的缺点是所得产品结构相当“封闭”,表现为比表面积和孔隙率低,因而反应活性降低,并不具备镜背涂层体系所需的高度防腐蚀活性。 At present, the method for producing zinc cyanamide has a calcination method in which zinc oxide is calcined together with an excess amount of urea or dicyandiamide under nitrogen or vacuum, first at 135 ° C to 200 ° C, and then at 600 ° C to 800 ° C. In hours, a zinc cyanamide pigment is obtained. The disadvantage of this high energy consumption method is that the resulting product structure is quite "closed", exhibiting a low specific surface area and porosity, and thus reduced reactivity, and does not have the high corrosion protection activity required for the mirror back coating system.
还有湿法生产法制取氰胺锌,是将可溶的锌盐用水溶,通过碱金属的氢氰胺盐沉淀来制备。它为了消除副产物,需大量水洗,因此产生大量的废水。更为严重的是由于这可溶盐杂质往往不易完全去除,因此,采用这种方法制取氰胺锌做成的镜背涂料,存在氰胺锌带来微量可溶副产物造成的影响。 There is also a wet process for preparing zinc cyanamide which is prepared by dissolving a soluble zinc salt in water and precipitating it with an alkali metal hydrocyanamide salt. In order to eliminate by-products, it requires a large amount of water to be washed, thus generating a large amount of waste water. What is more serious is that the soluble salt impurities are not easily removed completely. Therefore, the mirror back coating made of cyanamide zinc by this method has the influence of a trace amount of soluble by-products caused by zinc cyanamide.
也有先使溶解的氰胺钙与硫酸和二氧化碳反应,制得氰胺氢的水溶液,接着将此中间产物与氧化锌反应,再将该产品进行过滤干燥粉碎。由于存在大量的碳酸和硫酸,在镜背涂料中应用受到限制。 It is also possible to first react the dissolved calcium cyanamide with sulfuric acid and carbon dioxide to obtain an aqueous solution of cyanamide hydrogen, and then react the intermediate product with zinc oxide, and then filter and dry the product. Due to the large amount of carbonic acid and sulfuric acid, application in mirror back coatings is limited.
以上的各种制取氰胺锌的途径具有以下缺点,需要过量的氰胺化合物、氮气或真空下、及高温等条件下得到:或通过氢氰胺盐沉淀来制取;或通过制取氰胺氢中间产物再与氧化锌制得,产品活性低,副产物多、水溶性盐高,而且能耗高,工艺复杂。因此,研制环保镜背涂料用的无盐、抗氧化型氰胺锌防腐颜料,对提高镜背涂料的耐腐蚀性有着十分重要的意义。 The above various routes for preparing zinc cyanamide have the following disadvantages, and are required to be obtained by excessive cyanamide compound, nitrogen or under vacuum, and at a high temperature; or by precipitation of hydrocyanamide salt; or by preparing cyanide. The amine hydrogen intermediate product is prepared with zinc oxide, has low product activity, high by-products, high water-soluble salt, high energy consumption and complicated process. Therefore, the development of environmentally friendly mirror back coatings for salt-free, anti-oxidant zinc cyanide anti-corrosion pigments is of great significance to improve the corrosion resistance of mirror coatings.
本发明的目的是为了解决上述技术的不足而提供一种使用原料少,能耗低,产生废水少,副产物少,工艺简单且得到的颜料防腐性能好,适用范围广的环保镜背涂料专用无盐、抗氧化型氰胺锌防腐颜料及生产方法。 The purpose of the invention is to solve the deficiencies of the above-mentioned technologies and to provide a non-environmental mirror-back coating which has less raw materials, low energy consumption, less waste water, less by-products, simple process and good anti-corrosion performance of the pigment. Salt-free, anti-oxidation zinc cyanide anticorrosive pigment and production method.
为了达到上述目的,本发明所设计的环保镜背涂料专用无盐、抗氧化型氰胺锌防腐颜料,是通过氧化锌和氰胺化合物反应并加入偶联剂得到的产物。 In order to achieve the above object, the salt-free and oxidation-resistant zinc cyanide anticorrosive pigment for environmentally friendly mirror coatings designed by the present invention is a product obtained by reacting zinc oxide with a cyanamide compound and adding a coupling agent.
本发明所设计的环保镜背涂料专用无盐、抗氧化型氰胺锌防腐颜料的生产方法,是将高活性的氧化锌投入去离子水中完全分散,制取均匀的氧化锌浆,慢慢加入氰胺化合物,在搅拌分散下,开始放热反应,待温度开始下降时,进行高速搅拌,使其完全反应, 通过仪器观察发现,微小颗粒开始减少,直到没有颗粒为止,静止分水,并将分离的水循环用于下次制取氧化锌浆,将分离后的氰胺锌沉淀物进行压滤去除水份,然后于105℃干燥至水份小于0. 1%以下,进行粉碎,细度达到320目筛余物小于0.05%以下得到氰胺锌防腐颜料。 The method for producing the salt-free and anti-oxidation type cyanamide anti-corrosion pigment for the environmental protection mirror back coating designed by the invention is to completely disperse the highly active zinc oxide into the deionized water to prepare a uniform zinc oxide slurry, and slowly add the solution. The cyanamide compound starts the exothermic reaction under stirring and dispersion, and when the temperature starts to decrease, it is stirred at a high speed to completely react. Through instrumental observation, it is found that the tiny particles begin to decrease until there is no particles, the water is statically separated, and the separated water is recycled for the next time to obtain the zinc oxide slurry, and the separated zinc cyanamide precipitate is subjected to pressure filtration to remove water. Then dry at 105 ° C until the moisture is less than 0. 1% or less, pulverization is carried out, and the fineness reaches 320 mesh sieve residue less than 0.05% or less to obtain a zinc cyanamide anticorrosive pigment.
为了提到所得到的氰胺锌防腐颜料的稳定性,可以在氧化锌和氰胺化合物反应时添加偶联剂。 In order to mention the stability of the obtained zinc cyanide anticorrosive pigment, a coupling agent may be added in the reaction of zinc oxide and a cyanamide compound.
为了节约成本,并使本发明所设计的生产方法达到最佳的反应效果,在反应中氧化锌,去离子水、氰胺化合物和偶联剂的重量分数分别为氧化锌15-25份,去离子水55-65份,氰胺化合物18-23份,偶联剂1.5-2.5份。所述的高活性的氧化锌是ZnO-Xl或ZnO-X2 或ZnO-Tl或Zn0 -T2或Zn0 -T3或BA01-05(I型)或BA01-05(II型):所述的氰胺化合物是尿素或双氰胺或氢氰胺盐或单氰胺。所述的偶联剂是1121#偶联剂或JN-A偶联剂或TYZOR AA-75偶联剂或KH-550偶联剂。 In order to save cost and achieve the best reaction effect of the production method designed by the invention, the weight fraction of zinc oxide, deionized water, cyanamide compound and coupling agent in the reaction is 15-25 parts of zinc oxide, respectively. 55-65 parts of ionized water, 18-23 parts of cyanamide compound, and 1.5-2.5 parts of coupling agent. The highly active zinc oxide is ZnO-Xl or ZnO-X2 Or ZnO-Tl or Zn0-T2 or Zn0 -T3 or BA01-05 (type I) or BA01-05 (type II): The cyanamide compound is urea or dicyandiamide or hydrocyanamide or monocyanamide. The coupling agent is 1121# coupling agent or JN-A coupling agent or TYZOR AA-75 coupling agent or KH-550 coupling agent.
本发明所得到的环保镜背涂料专用无盐、抗氧化型氰胺锌防腐颜料的生产方法,主要按下列化学方程式进行: The production method of the salt-free and anti-oxidation type cyanamide anti-corrosion pigment for the environmental protection mirror back coating obtained by the invention is mainly carried out according to the following chemical equation:
Zn0+ H20+H2CN2 →ZnNCN +H2OZn0+ H 2 0+H 2 CN 2 →ZnNCN +H 2 O
核心部分是采用高活性的氧化锌,在水相介质中与金属氰胺化合物反应,通过特定的工艺技术,在常温下使其完全反应,达到无可溶盐杂质,添加偶联剂后确保其稳定性,通过过滤、分水、压滤、干燥、粉碎的生产工艺过程,获得无盐、抗氧化型的氰胺锌颜料。由于采用高活性的氧化锌,改进了反应速度,特别是经过特定的反应装置和工艺技术,以及关键工艺控制手段,使得氰胺锌的水溶游离盐和杂质的含量低于0.2%。 The core part is made of high-activity zinc oxide, reacted with metal cyanamide compound in an aqueous medium, and completely reacted at room temperature by a specific process technology to achieve impurity-free salt impurities. After adding a coupling agent, it is ensured. Stability, through the filtration, water separation, pressure filtration, drying, pulverization production process, to obtain salt-free, antioxidant-type zinc cyanamide pigment. Due to the use of highly active zinc oxide, the reaction rate is improved, especially through specific reaction equipment and process technology, as well as key process control means, so that the content of water-soluble free salts and impurities of zinc cyanamide is less than 0.2%.
本发明的氰胺锌防腐颜料有以下优点: The zinc cyanamide anticorrosive pigment of the present invention has the following advantages:
产品不含铅、吸油值、水溶游离盐和杂质含量低,分散性好,能抑制底材或金属层氧化、防止涂层皂化,中和腐蚀过程中产生的或存在的游离硫化物和氯化物离子,节约能源,减少环境污染,降低制造成本,产品性能达到国外先进水平,具有良好的经济效益。 The product does not contain lead, oil absorption, water soluble free salt and low impurity content, good dispersibility, can inhibit the oxidation of the substrate or metal layer, prevent the saponification of the coating, neutralize the free sulfides and chlorides generated or present during the corrosion process. Ions, save energy, reduce environmental pollution, reduce manufacturing costs, product performance has reached advanced levels in foreign countries, and has good economic benefits.
下面通过实施例结合附图对本发明作进一步的描述。 The invention is further described below by way of embodiments with reference to the accompanying drawings.
实施例1: Example 1:
在一个装有搅拌器、冷凝器的特定反应装置中,将15g-25gZnO-Tl氧化锌投入55g-65g 去离子水中完全分散,制取均匀的氧化锌浆,慢慢加入18g-23g单氰胺,在搅拌分散下,开始放热反应,待温度开始下降时,进行高速搅拌,使其完全反应,通过仪器观察发现,微小颗粒开始减少,直到没有颗粒时,添加1.5g-2.5g KH-550偶联剂搅拌均匀,静止分水,将分离的水循环用于下次制取氧化锌浆,将分离后的氰胺锌沉淀物用板框压滤机压滤去除水份,然后于不锈钢的恒温烘箱中在105℃干燥至水份小于0.1%以下,移到不锈钢粉机中进行粉碎,细度达到320目筛余物小于0.05%以下。 In a specific reaction unit equipped with a stirrer and a condenser, 15g-25g ZnO-Tl zinc oxide is put into 55g-65g Dissolve completely in deionized water, prepare a uniform zinc oxide slurry, slowly add 18g-23g of monocyanamide, start the exothermic reaction under stirring and dispersion, and when the temperature begins to drop, stir it at high speed to make it completely react. The instrument observed that the tiny particles began to decrease until no particles were added, adding 1.5g-2.5g. The KH-550 coupling agent is evenly stirred, and the water is separated at rest. The separated water is recycled for the next time to obtain the zinc oxide slurry, and the separated zinc cyanide precipitate is filtered by a plate and frame filter to remove water, and then The stainless steel constant temperature oven is dried at 105 ° C to a moisture content of less than 0.1%, and is transferred to a stainless steel powder machine for pulverization, and the fineness reaches 320 mesh sieve residue of less than 0.05%.
实施例2: Example 2:
在一个装有搅拌器、冷凝器的特定反应装置中,将15g-20gZnO-Xl氧化锌投入50g-65g去离子水中完全分散,制取均匀的氧化锌浆,慢慢加入l5g-20g双氰胺,在搅拌分散下,开始放热反应,待温度开始下降时,进行高速搅拌,使其完全反应,通过仪器观察发现,微小颗粒开始减少,直到没有颗粒时,添1.5g-2.0gKH-550偶联剂搅拌均匀,静止分水,将分离的水循环用于下次制取氧化锌浆,将分离后的氰胺锌沉淀物用板框压滤机压滤去除水份,然后于不锈钢的恒温烘箱中在105℃干燥至水份小于0.1%以下,移到不锈钢粉机中进行粉碎,细度达到320目筛余物小于0.05%以下。 In a specific reaction device equipped with a stirrer and a condenser, 15g-20g ZnO-Xl zinc oxide is completely dispersed in 50g-65g deionized water to prepare a uniform zinc oxide slurry, and slowly add 15g-20g dicyandiamide Under stirring and dispersion, the exothermic reaction begins. When the temperature begins to decrease, high-speed stirring is carried out to completely react. It is observed by the instrument that the fine particles begin to decrease until no particles are added, and 1.5g-2.0g KH-550 is added. The mixture is stirred evenly, and the water is separated at rest. The separated water is recycled for the next time to obtain the zinc oxide slurry, and the separated zinc cyanide precipitate is filtered by a plate and frame filter to remove water, and then the stainless steel constant temperature oven is used. The medium is dried at 105 ° C to a moisture content of less than 0.1%, and is transferred to a stainless steel powder machine for pulverization, and the fineness reaches 320 mesh sieve residue of less than 0.05%.
实施例3: Example 3:
在一个装有搅拌器、冷凝器的特定反应装置中,将15g-25gZnO-Xl氧化锌投入55g-60g去离子水中完全分散,制取均匀的氧化锌浆,慢慢加入18g-20g双氰胺,在搅拌分散下,开始放热反应,待温度开始下降时,进行高速搅拌,使其完全反应,通过仪器观察发现,微小颗粒开始减少,直到没有颗粒时,添加0.5g-1.5g TYZOR AA-75偶联剂搅拌均匀,静止分水,将分离的水循环用于下次制取氧化锌浆,将分离后的氰胺锌沉淀物用板框压滤机压滤去除水份,然后于不锈钢的恒温烘箱中在l05℃干燥至水份小于0.1%以下,移到不锈钢粉机中进行粉碎,细度达到320目筛余物小于0.05%以下。 In a specific reaction device equipped with a stirrer and a condenser, 15g-25g of ZnO-Xl zinc oxide is completely dispersed in 55g-60g of deionized water to prepare a uniform zinc oxide slurry, and 18g-20g of dicyandiamide is slowly added. Under stirring and dispersion, the exothermic reaction begins. When the temperature begins to decrease, high-speed stirring is performed to completely react. It is observed by the instrument that the fine particles begin to decrease until no particles are added, and 0.5g-1.5g is added. TYZOR The AA-75 coupling agent is evenly stirred, and the water is separated at rest. The separated water is recycled for the next time to obtain the zinc oxide slurry, and the separated zinc cyanide precipitate is filtered by a plate and frame filter to remove water, and then The stainless steel constant temperature oven is dried at l05 ° C to a moisture content of less than 0.1%, and is transferred to a stainless steel powder machine for pulverization, and the fineness reaches 320 mesh sieve residue of less than 0.05%.
实施例4: Example 4:
在一个装有搅拌器、冷凝器的特定反应装置中,将20g-30gBA01-05(II型)氧化锌投入50g-55g去离子水中完全分散,制取均匀的氧化锌浆,慢慢加入18g-25g双氰胺,在搅拌分散下,开始放热反应,待温度开始下降时,进行高速搅拌,使其完全反应,通过仪器观察发现,微小颗粒开始减少,直到没有颗粒时,添加1.5g-2.0g TYZOR AA-75偶联剂搅拌均匀,静止分水,将分离的水循环用于下次制取氧化锌浆,将分离后的氰胺锌沉淀物用板框压滤机压滤去除水份,然后于不锈钢的恒温烘箱小在105℃干燥至水份小于0.1%以下,移到不锈钢粉机中进行粉碎,细度达到320目筛余物小于0. 05%以下。 In a specific reaction device equipped with a stirrer and a condenser, 20g-30g BA01-05 (type II) zinc oxide is completely dispersed in 50g-55g deionized water to prepare a uniform zinc oxide slurry, and slowly add 18g- 25g dicyandiamide, under stirring and dispersion, began to exothermic reaction. When the temperature began to drop, high-speed stirring was carried out to completely react. It was observed by the instrument that the tiny particles began to decrease until no particles were added, and 1.5g-2.0 was added. g TYZOR The AA-75 coupling agent is evenly stirred, and the water is separated at rest. The separated water is recycled for the next time to obtain the zinc oxide slurry, and the separated zinc cyanide precipitate is filtered by a plate and frame filter to remove water, and then The stainless steel constant temperature oven is dried at 105 ° C to a moisture content of less than 0.1%, and is transferred to a stainless steel powder machine for pulverization. The fineness reaches 320 mesh and the residue is less than 0. 05% or less.
实施例5: Example 5:
在一个装有搅拌器、冷凝器的特定反应装置中,将18g-25gBA01-05(II型)氧化锌投入53g-62g去离子水中完全分散,制取均匀的氧化锌浆,慢慢加入18g-21g单氰胺,在搅拌分散下,开始放热反应,待温度开始下降时,进行高速搅拌,使其完全反应,通过仪器观察发现,微小颗粒开始减少,直到没有颗粒时,添加l.5g-2.2g KH-550偶联剂搅拌均匀,静止分水,将分离的水循环用于下次制取氧化锌浆,将分离后的氰胺锌沉淀物用板框压滤机压滤去除水份,然后于不锈钢的恒温烘箱中在105℃干燥至水份小于0.1%以下,移到不锈钢粉机中进行粉碎,细度达到320目筛余物小于0.05%以下。 In a specific reaction device equipped with a stirrer and a condenser, 18g-25g BA01-05 (type II) zinc oxide is completely dispersed in 53g-62g deionized water to prepare a uniform zinc oxide slurry, and slowly add 18g- 21g of monocyanamide, under stirring and dispersion, began to exothermic reaction. When the temperature began to drop, high-speed stirring was carried out to completely react. It was observed by the instrument that the tiny particles began to decrease until no particles were added, and 1.5 g was added. 2.2g The KH-550 coupling agent is evenly stirred, and the water is separated at rest. The separated water is recycled for the next time to obtain the zinc oxide slurry, and the separated zinc cyanide precipitate is filtered by a plate and frame filter to remove water, and then The stainless steel constant temperature oven is dried at 105 ° C to a moisture content of less than 0.1%, and is transferred to a stainless steel powder machine for pulverization, and the fineness reaches 320 mesh sieve residue of less than 0.05%.
将上述1-5实施例中氰胺锌性能测试结果见表1。 The test results of the zinc cyanamide performance in the above 1-5 examples are shown in Table 1.
表1:
将上述1-5实施例中氰胺锌分别按下例涂料配方比例制取镜背漆,详见表2。 The mirror back paint was prepared by the proportion of the coating formulation of the above-mentioned 1-5 examples in the following examples, as shown in Table 2.
表2:
将用上述1-5实施例中氰胺锌制取镜背漆进行抗湿热性能、抗中性盐雾性能、及光学性能试验结果见表3。 The results of the anti-humidity performance, the anti-neutral salt spray performance, and the optical performance of the mirror-back paint prepared by using the zinc cyanamide in the above 1-5 examples are shown in Table 3.
表3:
Claims (7)
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|---|---|---|---|
| CN200910098799.1 | 2009-05-21 | ||
| CN2009100987991A CN101942228A (en) | 2009-05-21 | 2009-05-21 | Special salt-free oxidation resisting zinc cyanamide anticorrosion pigment for environmental-protection mirror back coating and production method thereof |
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| WO2010133119A1 true WO2010133119A1 (en) | 2010-11-25 |
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| PCT/CN2010/072005 Ceased WO2010133119A1 (en) | 2009-05-21 | 2010-04-21 | Salt free, oxidation-resistant zinc cyanamide anticorrosive pigments for environment-friendly mirror back coatings and preparation method thereof |
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| CN (1) | CN101942228A (en) |
| WO (1) | WO2010133119A1 (en) |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5176894A (en) * | 1991-12-06 | 1993-01-05 | Wayne Pigment Corp. | Process for making improved corrosion preventive zinc cyanamide |
| US5487779A (en) * | 1993-11-19 | 1996-01-30 | Wayne Pigment Corp. | Corrosion inhibiting pigment composition and method |
| JPH0841376A (en) * | 1994-08-02 | 1996-02-13 | Nippon Chem Ind Co Ltd | White rust preventive pigment and method for producing the same |
-
2009
- 2009-05-21 CN CN2009100987991A patent/CN101942228A/en active Pending
-
2010
- 2010-04-21 WO PCT/CN2010/072005 patent/WO2010133119A1/en not_active Ceased
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5176894A (en) * | 1991-12-06 | 1993-01-05 | Wayne Pigment Corp. | Process for making improved corrosion preventive zinc cyanamide |
| US5487779A (en) * | 1993-11-19 | 1996-01-30 | Wayne Pigment Corp. | Corrosion inhibiting pigment composition and method |
| JPH0841376A (en) * | 1994-08-02 | 1996-02-13 | Nippon Chem Ind Co Ltd | White rust preventive pigment and method for producing the same |
Non-Patent Citations (1)
| Title |
|---|
| PULUTEMAN, E. P. ET AL.: "ShangHai scientific and technoiogical literature publishing house", SILANE AND TITANATE COUPLING AGENTS, July 1987 (1987-07-01), pages 234, 285 * |
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