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汽车滤纸用乳液现状及发展趋势段璐璐;刘文波【摘要】汽车滤清器是汽车发动机上的一个很重要的部件。
汽车滤纸作为汽车滤清器的过滤介质,其性能决定了汽车滤清器的质量。
汽车滤纸用乳液主要用来改善和提高滤纸的性能,以满足滤纸加工和使用时等性能要求。
该文就汽车滤纸用乳液的现状、发展过程、改性方法等进行了分析阐述,并对乳液的发展趋势作了展望。
%Automobile filter is a very important component in the automobile engine. As the filtering medium for automobile filter, the property of automobile filter paper certainly decides the quality of the filter. Emulsions developed specially for automobile filter papers are used to enhance the performance of the paper during its finishing processes and application. This article profoundly analyzed the current situation, development history and the modification methods of such emulsions, and it also prospected the development trend of the emulsions.【期刊名称】《造纸化学品》【年(卷),期】2011(000)006【总页数】4页(P5-8)【关键词】汽车滤纸:乳液:改性:趋势【作者】段璐璐;刘文波【作者单位】东北林业大学,黑龙江哈尔滨150040;东北林业大学,黑龙江哈尔滨150040【正文语种】中文【中图分类】TS761.2汽车滤清器是汽车发动机上的一个非常重要的部件,作为滤清器过滤介质的汽车滤纸对滤清器的性能起决定性作用。
摘要目前人们对生活品质的要求在不断提高,绿色环保的理念深入人心,苯丙乳液作为水性涂料的成膜物质具有污染小,成膜温度低,粘结强度高等优点。
但是在耐水性,防腐性,耐磨性等方面存在一些不足,因此对其进行功能化改性受到了广泛的重视。
本文首先综述了近年来石墨烯,有机硅,有机氟,自交联单体等功能性原料改性丙烯酸酯乳液的研究进展,同时详细的介绍了改性后的丙烯酸树脂乳液的应用,并对今后的发展进行展望。
其次利用不同的功能单体对苯丙乳液进行改性,并对制备的乳液的性能进行一系列的分析和研究。
研究结果表明,采用羟甲基丙烯酰胺/丙烯酸、双丙酮丙烯酰胺/己二酸二酰肼、乙烯基三乙氧基硅烷为交联单体,当羟甲基丙烯酰胺/丙烯酸含量为5%时,乳液的吸水率达到最低; 双丙酮丙烯酰胺和己二酸二酰肼比例为1:1时,乳胶膜的交联度最大; 乙烯基三乙氧基硅烷含量为4%时,乳胶膜表现出了优异的耐热性能,且乳液及乳胶膜的综合性能达到最好。
最后采用KH560、KH570和KH590三种硅烷偶联剂对氧化石墨烯进行表面修饰,然后通过机械共混的方法将功能化氧化石墨烯添加到苯丙乳液中完成对苯丙乳液的改性。
结果表明,KH560、KH570和KH590添加量分别为0.5%、0.7%、0.3%时,乳液的防腐蚀性能、耐介质性和耐盐雾性能达到最优。
研究还发现,采用反应型乳化剂SR-10,且当叔碳酸乙烯酯和苯乙烯的质量比为1:9时乳液的吸水率最低,乳液和乳胶膜的综合性能最好。
关键词苯丙乳液;自交联;氧化石墨烯;硅烷偶联剂;叔碳酸乙烯酯AbstractIn recent years, people's requirements for quality of life are constantly improving, and the concept of green environmental protection is deeply rooted in people's minds. As a film-forming substance for water-based paints, styrene-acrylic emulsion has advantages of low pollution, low film forming temperature and high bonding strength. However, styrene-acrylic emulsion has some shortcomings in water resistance, corrosion resistance and wear resistance, so its functional modification has received extensive attention.First, the research progress of acrylate emulsion modified by graphene, silicone, organic fluorine and self-crosslinking monomer in recent years were reviewed in this paper. The application of modified acrylic resin emulsion was introduced in detail, and the future development was prospected. Then styrene-acrylic emulsion was modified by different functional monomers, and the properties of the prepared emulsions were analyzed and studied. The results showed that the water absorption rate of the emulsion was the lowest when the amount of hydroxymethylacrylamide/acrylic acid was 5%, using hydroxymethylacrylamide/acrylic acid, diacetoneacrylamide/adipic acid dihydrazide and vinyltriethoxysilane as crosslinking monomers; when the ratio of diacetone acrylamide to diacylhydrazide adipate was 1:1, the crosslinking degree of latex film was the highest; and when the content of vinyltriethoxysilane was 4%, the latex film showed excellent heat resistance, and the comprehensive properties of the latex and the latex film were the best. Finally, three silane coupling agents KH560, KH570 and KH590 were used to modify the surface of graphene oxide, and then functional graphene oxide was added to styrene-acrylic emulsion by mechanical blending to achieve the modification of styrene-acrylic emulsion. The results showed that the anti-corrosion, medium resistance and salt spray resistance of the emulsion were the best when the dosages of KH560, KH570 and KH590 were 0.5%, 0.7% and 0.3% respectively. It was also found that when reactive emulsifier SR-10 was used and the mass ratio of tertiary vinyl carbonate to styrene was 1:9, the water absorption rate of the emulsion was the lowest, and the comprehensive properties of the emulsion and the latex film were the best.Key words Styrene-acrylic Emulsion;Self-crosslinking;Graphene oxide;Silane coupling agent;Vinyl tertiary carbonate目 录摘要 (I)Abstract (III)第章绪论1 (1)1.1 概述 (1)1.2 丙烯酸乳液的功能化改性 (1)1.2.1 石墨烯改性 (1)1.2.2 环氧树脂改性 (2)1.2.3 有机硅改性 (3)1.2.4 有机氟改性 (3)1.2.5 其他方法改性 (4)1.3 自交联单体对丙烯酸乳液的改性 (5)1.3.1 羟甲基丙烯酰胺及其衍生物的交联体系 (5)1.3.2 酮肼的交联体系 (5)1.3.3 甲基丙烯酸缩水甘油酯(GMA)交联体系 (6)1.4 功能性丙烯酸乳液的应用 (7)1.4.1 功能性涂料 (7)1.4.2 粘合剂 (7)1.5 展望 (7)1.6 本本本的研究目的及意本 (8)1.7 本本本的本要研究内容 (8)1.8 本论文的本本本本 (8)第2章含氟自交联苯丙乳液的改性及性能研究 (9)2.1 概述 (9)实实部分2.2 (9)2.2.1 实实原料和实实设备 (9)2.2.2 乳液的合成 (11)2.2.3 性能测试 (12)2.3 结果与结论 (13)2.3.1 N-MA/AA对乳液性能的影响 (13)2.3.2 DAAM和ADH对乳液性能的影响 (19)2.3.3 硅氧烷(VTES)对乳液性能的影响 (22)2.4 本章小结 (27)第3章石墨烯改性苯丙乳液的制备及性能研究 (29)3.1 概述 (29)3.2 实实部分 (29)3.2.1 实实原料和试实设备 (29)3.2.2 实实过程 (30)3.2.3 性能测试 (31)3.3 结果与结论 (32)3.3.1 不同硅烷偶联剂改性氧化石墨烯的红外分析 (32)3.3.2 不同硅烷偶联剂改性氧化石墨烯的热重分析 (34)3.3.3 不同硅烷偶联剂改性氧化石墨烯的接触角分析 (35)3.3.4 不同硅烷偶联剂改性氧化石墨烯的扫描电镜分析 (36)3.3.5 不同硅烷偶联剂功能化的氧化石墨烯改性苯丙乳液的性能分析 (37)3.4 本章小结 (41)第4章叔碳酸乙烯酯改性苯丙乳液的制备及性能研究 (43)4.1 引引 (43)4.2 实实部分 (43)4.2.1 实实原料和实实设备 (43)4.2.2 乳液的合成 (44)4.2.3 性能测试 (45)4.3 结果与结论 (45)4.3.1 不同叔碳酸乙烯酯含量对苯丙乳液的影响 (45)4.3.2 不同乳化体系对苯丙乳液的影响 (49)4.4 本章小结 (53)结论 (55)参参文献 (57)攻攻硕士学位期攻所发表的论文 (63)致谢 (65)第1章绪论1.1概述近年来全球范围内环保法规的收紧,政府对涂料行业有机化合物(VOC)的排放量提出了更加严格的要求。
含氟丙烯酸酯乳液高疏水性与低氟含量的平衡探索王宇翔;朱逸莉;房嫄;杨茹婷;郭建利;刘引烽【摘要】为了研究含氟丙烯酸酯乳液涂膜的疏水性与氟含量的平衡关系,以甲基丙烯酸十二氟庚酯(DFHM)为含氟单体,双丙酮丙烯酰胺(DAAM)和己二酸二酰肼(ADH)为交联单体,采用半连续核壳乳液聚合的方法合成了一系列自交联含氟丙烯酸酯共聚物乳液.研究表明:含氟单体含量为12%(即氟含量为6.84%,均以聚合单体的总质量计,下同)时,含氟基团在涂膜表面可以达到饱和,乳液固含量可达38.2%;再添加4%交联单体,涂膜的水接触角为116.6°.当含氟单体含量降为4%(氟含量2.28%)时,通过提高成膜温度或添加成膜助剂,也可使涂膜表面的水接触角达到104.2°,具有较好的疏水性能.【期刊名称】《涂料工业》【年(卷),期】2015(045)008【总页数】7页(P8-13,20)【关键词】含氟丙烯酸酯乳液;低氟含量;疏水性;自交联;半连续核壳乳液聚合【作者】王宇翔;朱逸莉;房嫄;杨茹婷;郭建利;刘引烽【作者单位】上海大学材料科学与工程学院高分子材料系,上海200444;上海大学材料科学与工程学院高分子材料系,上海200444;上海大学材料科学与工程学院高分子材料系,上海200444;上海大学材料科学与工程学院高分子材料系,上海200444;上海大学材料科学与工程学院高分子材料系,上海200444;上海大学材料科学与工程学院高分子材料系,上海200444【正文语种】中文【中图分类】TQ630.4氟碳涂料因其良好的防腐、防污、超耐候、耐化学性、防水性等优良性能而得到了广泛应用[1-4]。
随着环境保护要求的日益提高,水性氟碳涂料将是今后氟碳涂料的发展方向[5-6]。
水性氟碳涂料包括含氟丙烯酸酯共聚物、FEVE和PVDF。
其中PVDF氟含量(以氟占氟树脂总质量计算,下同)超过50%;含氟丙烯酸酯共聚物的氟含量最低,通常为10%~15%;而目前市场普遍所用的FEVE是以三氟氯乙烯为主要含氟单体、与烷基乙烯基醚(或酯)及可交联的功能性单体共聚而得的氟树脂,其氟含量为17%~35%[5]。
酮肼交联反应在常温固化丙烯酸酯清漆制备中的应用林毅伟;刘晓国;陈浩锦【摘要】运用溶液聚合法合成了含有双丙酮丙烯酰胺(DAAM)单体的水溶性可常温固化的有机硅改性丙烯酸酯树脂,并添加一定量的中和剂三乙胺(TEA)、快千水(乙醇)、慢干水(丙二醇甲醚)、固化剂己二酸二酰肼(ADH)和助剂,利用酮肼交联反应,配制成丙烯酸酯清漆.考察了DAAM、ADH与TEA用量以及表干时间对漆膜性能、凝胶时间的影响,得出最佳条件为:DAAM用量控制在单体总质量的15.0%,DAAM与ADH的摩尔比为2∶1,表干时间45 min,中和度70%~ 80%.此时漆膜综合性能最好:光亮,硬度3H,附着力0级,耐水浸泡24h完好,耐乙醇擦拭94次.【期刊名称】《电镀与涂饰》【年(卷),期】2015(034)010【总页数】5页(P527-531)【关键词】双丙酮丙烯酰胺;己二酸二酰肼;酮肼交联反应;水稀释型丙烯酸酯树脂;清漆;常温固化【作者】林毅伟;刘晓国;陈浩锦【作者单位】广州大学化学化工学院,广东广州510006;广州大学化学化工学院,广东广州510006;广州大学化学化工学院,广东广州510006【正文语种】中文【中图分类】TQ630.4First-author's address: School of Chemistry and Chemical Engineering,Guangzhou University, Guangzhou 510006,China水性聚丙烯酸酯跟溶剂型聚丙烯酸酯相比,在耐水性、耐溶剂性、耐候性、耐溶剂擦拭等方面都显现出一定的差距,如在其中运用交联技术,则可大大提高主体树脂的综合性能,逐步减小二者差距。
双丙酮丙烯酰胺(DAAM)作为一种功能性的交联单体,在高分子聚合物尤其是丙烯酸酯树脂中的研究和应用近几年来已成为国内外的热点[1]。
将DAAM引入到水性聚丙烯酸酯分子中,以己二酸二酰肼(ADH)作为固化剂,可使聚合物实现常温交联固化,该反应简称“酮肼交联”,机理参见图1。
王进杨军(株洲时代新材料科技股份有限公司湖南株洲412007);张晓君丁智平(湖南工业大学包装与印刷学院湖南株洲412007)一、前言聚合物基阻尼涂料是一种以聚合物为基质的功能材料,能够减少各种机械振动产生的振动及噪音,提高机械的精度及寿命,消除振动及噪音产生的环境污染。
20世纪50年代,西德首先研制出高聚物粘弹阻尼涂料,因其性能优异、价格低廉、使用方便而广泛用于各种设备的减振消噪音。
目前,阻尼高分子材料的设计与研究是国内外关注的热点之一,已有许多高分子聚合物用于减振消噪音系统中。
互穿网络(IPN)聚合物是近年发展起来的一类综合性能良好的高分子材料。
由于各聚合物网络之间互相交叉渗透、机械缠结,起着强迫互容和协同效应作用,为改善聚合物的性能提供了一种有效方法。
这一研究领域正引起众多学者的关注。
本文总结了近年来国内IPN阻尼涂料的研究进展。
二、聚氨酯/聚丙烯酸酯IPN阻尼涂料这是研究最多的一类阻尼涂料。
秦东奇等人制备了100-110℃的宽温域聚氨酯/聚甲基丙烯酸甲酯(PU/PMMA)IPN阻尼涂料,并且发现加入填料能明显加宽温域,提高阻尼效果。
加入石墨、玻璃棉、云母、10-100μm玻璃微球、10-180μm玻璃微球,5种填料的结果表明,不同填料的最佳添加量不同,取得的阻尼效果也相异,,多数以10%为最佳,其中玻璃棉和10-100μm微珠的阻尼因子(tanδ)大于0.5的温度区间都达到110℃(通常tanδ>0.3即可作为一种阻尼涂料),预示着其是一种具有应用开发前景的阻尼涂料。
李文安利用二步合成法合成了PU/PMMA互穿聚合物阻尼涂料,当PU/PMMA质量比为80/20,NCO/OH为1.5时,采用丙酮作溶剂,同时添加一定量的石墨或云母粉,作为涂料具有很好的成膜性能和阻尼性能。
唐冬雁等以甲苯二异氰酸酯预聚体与聚醚反应,合成了一系列高温固化的聚醚氨酯,用于与体型PMMA的IPN研究。
研究发现:-NCO与-OH的组分比及交联密度对网络材料的阻尼性能有明显的影响,随-NCO/-OH比例的减小,PU网络的完善程度增大;随有效交联密度增大,材料的混容性增加,二者共同作用使材料耗损能量的能力增加,表现出良好的阻尼性能;而当PU与PMMA的组分比为60/40时,IPN的阻尼性能较好,其Tg范围在-10-50℃。
产品验收规范FC-ZY-06一. 进厂原料检验规范:1 目的本规范是为了保证本公司所生产产品的质量,对采购产品进行验收及检验质量活动所做的规定。
本规范适用于本公司用于生产双丙酮丙烯酰胺(DAAM)、硫酸铵、己二酸二酰肼(ADH)、乙酰乙酸基甲基丙烯酸乙酯(AAEM)的原料由本公司采购的丙烯晴、丙酮、浓硫酸、甲苯、氨水、甲基丙烯酸羟乙酯、二乙烯酮、甲醇、硫酸、纯碱、80%水合肼等产品2.1本公司采购的产品经技术质量部进行验证和检验合格后方可接收入库,其外观须符合下列要求,如不符合下列要求时应拒收。
产品应标明生产厂名、厂址、产品名称、生产日期、或生产批号、商标、级别、净重、标准编号、许可证号。
2.2产品应有随货质量证明书或检验报告。
2.3产品应有产品合格证。
2.4质量平均副偏差小于0.2kg。
3 采样丙烯晴、丙酮、浓硫酸、甲苯、氨水、甲基丙烯酸羟乙酯、二乙烯酮、甲醇、硫酸、纯碱、80%水合肼等产品按GB/T6680-2003液体化工产品采样通则进行采样。
4 检验4.1结果按GB/T1250中修约值比较法判断验证结果是否符合标准。
4.2如果检验结果中有一项不符合产品标准要求时,应自两倍量的包装单元中重新采样进行复验,复验结果即使有一项指标不符合要求,则整批产品不能验收。
4.3产品按批进行检验,一个运输单元为一批。
5 产品验收时认真填写验收记录二. 过程检验规范:1技术质量部负责收集国家标准,编制《产品质量检验制度》和《成品检验规程》,并提供检测规程,明确检测点、检测频率、抽样方案、检测项目、检测方法、判别依据、使用的检验设备、结果报告等。
2各项检验活动均应建立检验记录,检验记录应满足检验文件要求,应有判定结论,应标有负责产品放行的授权者。
3生产过程中由工序人员依据各工序生产流程卡对过程产品进行检验和试验状态标识。
a. 原材料的检验状态标识按待检、合格和不合格品进行区域标识,检验状态标识应标明待检、合格、不合格。
双丙酮丙烯酰胺与己二酰肼应用常规有光乳胶漆确有因其热塑特性所带来的抗压粘性欠佳的问题。
文章所讨论的官能单体和以此制成的乳液和乳胶漆有室温自交联之特性 , 可大大提高漆膜的抗压粘性。
为适应一般水乳涂料在室温下成膜的要求, 加了交联剂的水乳涂料在室温下成膜时也能交联, 在未进行成膜时该水乳液可以在室温下长期保存, 即所谓的可室温固化的一液型水乳涂料。
这种水乳涂料的聚合物连接剂的合成, 是以少量双丙酮丙烯酰胺参与乳液共聚, 使所得共聚物链上带有酮羰基, 然后在此乳液中加进与酮羰基等当量或略低的己二酰肼, 混匀, 再配上颜料、填料与助剂即得水乳涂料。
这种方法在近年受到了国际上的重视, 现每年在美国化学文摘上可看到数十篇有关这方面的专利文摘即可见一斑。
1 反应机理(1) 双丙酮丙烯酰胺的结构式为:它的普通名称叫双丙酮丙烯酰胺(Diacetone acrylamide) , 简称DAAM 。
为无色针状结晶, 一般商品为浅黄色或白色结晶粉末; 其熔点54 ℃, 溶解度每 100g 溶剂在25 可溶DAAM100g 以上的有水、甲醇、四氢呋喃、乙酸乙酯、CH2Cl2 等; 可溶98g 的有苯乙烯, 在非极性溶剂中正庚烷、石油醚在 30 ℃~60℃仅溶1g 以下。
DAAM 分子上的丙烯酰胺双键可以进行自由基的均聚, 也可以与许多单体共聚[ 1 ] 。
DAAM 上的酮羰基与α-氢可以进行酮与 -活泼氢的多种反应。
所以DAAM 是一种多功能单体。
DAAM 对鼠的口服半致死量LD50 为 1770mg/ kg , 皮肤与眼睛的刺激指数为零。
(2) 己二酰肼的结构式为:普通名称为己二酰肼(Adipic dihydrazide) , 简称 ADH 。
为无色粉末状结晶, 熔点180 ℃~183 ℃, 溶解度每1 00g 溶剂在30 ℃, 水可溶12.54g 、乙醇1.3g 、乙醚不溶解。
ADH 对鼷鼠的LD50 为5000mg/ kg 以上(口服), 它的毒性比肼大大降低。
AAEMA替代双丙酮丙烯酰胺的技术方案AAEM替代双丙酮丙烯酰胺技术方案替代双丙酮丙烯酰胺(DAAM)与乙二酸二酰肼(ADH)的最佳方案为AAEM与乙二胺构成的交联体系。
AAEM与乙二胺构成的交联体系,同DAAM和ADH构成的交联体系相比,除了有成本上的优势,在聚合难度、耐水性上均优于DAAM和ADH,只要技术方案得当,也不会出现成膜变黄等问题。
AAEM的化学名为2- 【〔2- 甲基-1- 氧基-2- 丙烯基〕氧】乙基3- 氧基丁酸酯,在其分子结构中,含有一个端基双键和一个端基乙酰乙酰基团。
位于端基的双键,使得AAEM极容易发生自由基聚合反应;另一端的乙酰乙酰基团由于双羰基的共轭效应,导致中间的亚甲基上的-H极为活泼,易于发生多种基团反应。
特殊的分子结构使得AAEM 在丙烯酸乳液聚合领域具有广泛的用途。
在AAEM和乙二胺构成的常温交联体系应用中,由于使用者技术水平所限,经常会出现乳液发黄发红、不耐热储、成膜发黄等问题。
本公司经过多次对比实验,提出的技术方案如下:乳液聚合的基础技术很重要。
尤其是釜底缓冲剂的应用。
一般来讲,釜底采用小苏打缓冲为宜,用量为乳液总量的千分之二到千分之五。
反应温度。
建议高温法的反应温度控制在83度以下。
如果AAEM的用量达到或者超过单体量的4%。
建议采用低氧化还原聚合法。
反应温度控制在72-75度。
稳定剂的使用。
建议在乳液聚合结束,用氨水调节PH值之前,加入本公司特殊稳定剂SUPER-S,用量为乳液总量的2%。
乙二胺的用量及使用方法:乙二胺用量为AAEM质量的1/4,在氨水调节PH值之后,配为20%的水溶液加入乳液中。
只要注意了以上四点,变黄发红的问题就可以得以解决。
替代DAAM 和ADH就不会成为任何问题。
THE DIACETONE ACRYLAMIDE CROSSLINKING REACTION AND ITS INFLUENCE ON THE FILM FORMATION OF ANACRYLIC LATEXDr. Nicola Kessel, Sun Chemical Ltd, Orpington, Kent, UKDr. Derek R. Illsley, Sun Chemical Ltd, Orpington, Kent, UKDr. Joseph L. Keddie, University of Surrey, Guildford, Surrey, UK ABSTRACTWaterborne colloidal polymers (i.e. latex) represent a promising alternative to organic solvent-based systems in coatings applications. The development of mechanical strength and hardness is often enhanced by chemical crosslinking that creates a three-dimensional network. If extensive crosslinking occurs within the particles prior to their coalescence, however, interdiffusion will be prevented. A weaker product will result. We have explored the inter-relationship between coalescence, crosslinking and surfactant exudation in an acrylic latex containing diacetone acrylamide, exploiting the “keto-hydrazide” crosslinking reaction. The complementary use of spectroscopic techniques on a model system determined that the crosslinking reaction yields an imine product, not an enamine as has been proposed in the literature. Gel fraction measurements were used to probe the rate of crosslinking and identified a slower rate in larger particles, suggesting that the transport of the crosslinking agent is rate-lmiting. The keto-hydrazide reaction was found to be acid catalysed and favoured at lower water concentration. Measurement of the latex pH relative to the polymer mass fraction during film formation clarified the expected point of onset for crosslinking in relation to particle packing. Atomic force microscopy was used to follow surface levelling relative to the competing influence of crosslinking. The rate and total amount of surfactant exudation were found to be influenced by crosslinking, particle deformability (as determined by the temperature relative to the polymer glass transition temperature, T g), and the evaporation rate (as controlled by the relative humidity). There is evidence that surfactant exudation can be triggered by the particle deformation that occurs at film formation temperatures well above the T g. KEYWORDSCrosslinking, diacetone acrylamide, film formation, keto-hydrazide, surfactant. INTRODUCTIONA growing interest in and uses for waterborne polymer coatings have been driven by increasing environmental pressures, especially the need to comply with legislation limiting volatile organic compounds and emissions, associated with the use of solvent borne polymer systems 1, 2, 3, 4. Waterborne colloidal polymers (i.e. “latex”) are used in a wide range of applications, including adhesives, additives for paper, paints and coatings, printing inks, cosmetics, synthetic rubbers, floor polishes and waxes, sealants, and drug delivery systems 4. Colloidal particles may be tailored to exhibit a desired morphology, composition, particle size distribution, surface groups, and molecular weight 5. In turn, these particles can be manipulated during the film formation process in order to create coatings that meet the desired end-userequirements. Here, we consider the effects of several inter-related aspects of film formation 4 on final film structure and properties.The incorporation of crosslinking chemistry in waterborne coatings is recognised to provide a particularly effective means of enhancing the mechanical strength, chemical stability and solvent resistance of the final film 6-11. Recently, a system based on the reaction of a carbonyl pendant group on the dispersed polymer backbone with a diamine, specifically where this amine is a dihydrazide, has been the subject of increased interest 12, 13, 14. This chemistry, termed the keto-hydrazide reaction, offers the advantage of fast, ambient-temperature crosslinking in functionalized acrylic latex, when the dihydrazide is incorporated in the aqueous phase of the latex. Anecdotal evidence 15 also suggests that an added benefit of keto-hydrazide chemistry, particularly in printing ink applications, is the enhancement of adhesion, possibly through hydrogen bonding at the substrate interface, or the formation of permanent covalent bonds between the dihydrazide and carbonyl groups at the treated polymer substrate surface.Our system of interest consists of an acrylic latex containing diacetone acrylamide pendant groups (Figure 1A) on the polymer backbone that reacts with an adipic dihydrazide di-functional cross-linker (Figure 1B). It is conceivable that this reaction will yield either an imine or an enamine, or a mixture of both 12, 13, 14, 15, 16. The precise mechanism has not been reported, and there has been speculation in the literature that there is an enamine product. [reference ] This lack of clarity has motivated this present work.Figure 1: Molecular structure of the model reactants: (A):- Diacetone acrylamide pendant groups on the polymer backbone; (B):- Adipic dihydrazide cross-linker; (C):- 2-Heptanone, modelling the ketone group in the diacetone acrylamide pendant group;(D):- Octanoic hydrazide, modelling the amine group in adipic dihydrazide. Reaction between 2-Heptanone (C) and octanoic hydrazide (D) could yield option (1) anenamine, and/or option (2) an imine.Option (1) Enamine Option (2) Imine CH 3NH NH (CH 2)6CH 3O CH 3N 2C)4NH (CH 2)6CH 3O 2C)3HCAn understanding of the fundamental reaction mechanism and kinetics is essential tooptimise this coating formulation for specific applications and for the development ofnew materials. In this work we use model compounds (Figure 1C and 1D) toestablish the product of the reaction, in order to simplify the spectroscopic analysis.In waterborne systems the time in the film formation process at which crosslinkingoccurs can have a profound effect 17-26. To achieve maximum film strength particlesshould remain relatively free of cross-links in the dispersion but undergo extensivecrosslinking once they have formed a coating on the substrate. This is becausemolecular interdiffusion between neighbouring particles, which is essential for thegeneration of latex film strength, must take place prior to the crosslinking reaction 23-29. Strongly cross-linked particles are unable to inter-diffuse 17, 20, 21. In systems having an external cross-linker that is dissolved in the aqueous phase, its partitioningcharacter between the polymer and water imparts a further complication. If, as thefilm dries, this cross-linker does not readily dissolve within and uniformly distributewithin the polymer particles, then localised crosslinking may result. Although thecompeting effects of crosslinking and interdiffusion in various waterborne systemshave been studied, there are no such reports on keto-hydrazide coatings, until now.Moreover, we address the fact that pH evolves during film formation, and it has acatalytic influence on crosslinking, thus determining when the reaction develops as the film dries.Note that the crosslinking reaction in our system can occur between DAAM groupswithin the same particle or it can occur at the interface between particles. Intra-particle crosslinking will increase the stiffness and strength, but without entanglements at particle/particle interfaces, the films will lack cohesion. Inter-particle crosslinking will generate more cohesion, however, even in the absence of entanglements and interdiffusion.Through the years some strange and unusual observations of surfactant “islands” and “blobs” on coating surfaces have gone unexplained and remain mysterious 30-35. It is known that the presence of surfactants profoundly influence the mechanical strength, durability, adhesion, blocking, gloss and permeability of the final film 36-40. During this research it was discovered that the properties of the latex particles, the stages and conditions of film formation, and crosslinking all influence the rate of surfactant exudation. The processes are inter-related and should not be considered in isolation.EXPERIMENTALReagentsButyl acrylate (BA), methyl methacrylate (MMA), diacetone acrylamide (DAAM), methacrylic acid (MA), styrene (St), acrylic acid (AA) ammonium persulphate (APS), adipic dihydrazide (ADH), octanoic hydrazide and 2-heptanone were used as supplied from Sigma Aldrich Chemicals. Sodium lauryl sulphate (Texapon K-12) was used as supplied from Henkel. Acetone, methanol (HPLC grade), water (HPLC grade), ammonium hydroxide, hydrochloric acid, and litmus, were used as supplied from Fisher Scientific Ltd.Preparation of LaticesThe latices were prepared by a starve-feed emulsion polymerisation process using BA, MMA, DAAM, MAA and St monomers emulsified with sodium lauryl sulphate as the surfactant. APS was used as the initiator. The reaction flask (1 litre) was charged with deionised water and surfactant and heated to 80 ºC via a thermostatically-controlled heating mantle. Care was taken to avoid direct surface contact between the flask and heating mantle in order to prevent scorching of the flask contents.A pre-prepared monomer “seed” mixture, containing all five monomers, was added to the flask, whilst stirring, and the temperature allowed to stabilise. Then an initiator “seed” was similarly added to the reaction vessel. The mixture was left for approximately 15 minutes to allow the latex “seed” to develop, before commencing the monomer feeds. Monomer was fed into the vessel at a rate of 1.5 ml per minute. Initiator was split into six equal portions and then added at half hour intervals during the monomer feeds. Throughout the process the reaction temperature was maintained at 80 ºC, however, once the feeds were completed, the temperature was raised to 83 ºC and allowed to stabilise for 15 minutes. A final portion of initiator was then added and the reaction temperature was maintained at 83 ºC for a further 75 minutes, after which the latex was cooled. The latex was filtered through a mesh in order to remove large aggregates.Particle size was controlled through the surfactant concentration. Portions (100g) of filtered latex were decanted and the pH of the latex was adjusted to 8.5 using 25 wt.% ammonium hydroxide solution. Aliquots (10ml) of the ADH (10 wt.%, 5 wt.% or 2 wt.% aqueous solution) crosslinking agent were thoroughly stirred into portions of the latex. These concentrations correspond to the molar ratios summarised in Table 1. Table 1: Molar ratios of ADH crosslinker to DAAM groups in Standard latex and the number of DAAM groups that can be crosslinked as a function of the wt.% crosslinker in the latex.ADH wt/% added to latex Number of moles ADH:1 moleDAAMNumber of crosslinkableDAAM’s per copolymermolecule1 0.37 60.5 0.18 30.2 0.075 1Mono-phasic latices with solids content of 40% were prepared with differing T g’s and particle sizes. The “standard” composition of latex had a T g of ~52.5 °C and was made with particle sizes of 80, 150 and 300 nm. A latex with a T g of 118 °C was made using St (46.5 wt.%), MMA (46.5 wt.%), DAAM (5% wt.%), and MA (2 wt.%) and will hereafter be referred to as the “high T g latex”. A latex with T g of -2.4 °C was made using BA (69.2 wt.%), MMA (21.7 wt.%), DAAM (7.2 wt.%), and MA (1.9 wt.%) and will hereafter be referred to as the “low T g latex”.Fundamentals of Keto-Hydrazide CrosslinkingThe fundamentals of the keto-hydrazide reaction were studied using model compounds as previously described. Solutions of 2-heptanone (0.1M) and octanoic hydrazide (0.1M) were prepared in methanol and aliquots combined. The reaction solutions were analysed using Fourier Transform Infra Red spectroscopy (Mattson Research Series), Nuclear Magnetic Resonance Spectroscopy (Jeol EX90) and Gas Chromatography Mass Spectroscopy (Thermo Finnigan Trace) in order to establish the nature of the reaction product and the catalytic influence of pH.Chemical Crosslinking During Film FormationThe change in surface pH of drying films was measured using pH indicator paper at the surface as a function of time until the touch-dry point. Gravimetric gel fraction measurements were performed on 1µm films bar-cast on silicon substrates via the extraction of the soluble portion using acetone. The change in percentage gel with drying time was measured as a function of particle size, film thickness and level of cross-linker.An Atomic Force Microscope (AFM) (Veeco Dimension 3100) using ultra sharp silicon tips, of resonant frequency 130-250 kHz, and spring constant 48 N/, was used in intermittent contact (tapping mode) to probe the extent and rate of particle flattening of latex films cast on to glass microscope slides. Unless stated otherwise, film formation was in still air at a temperature of 22 °C.Characterisation of Surface Residues Evolved During Latex Film FormationThe solubility of the surface residue on latex films was established by probing its solubility by comparing AFM scans before and after rinsing with water. X-ray Photoelectron Spectroscopy (XPS) provided surface sensitive chemical information. Cast films were analysed in order to determine the chemical composition of the residue and verify the nature of the film surface.Factors Influencing Surfactant Exudation During Film FormationDuring film formation, the humidity was adjusted through the use of saturated salt solutions in a closed container, and through air flow above the film. Film formation at a temperature of 9 °C was achieved in a refrigerator. Surfactant exudation was studied using AFM height and phase images, and probed as a function of latex T g, temperature, crosslinking (with and without ADH), humidity and evaporation rate. RESULTS & DISCUSSIONFundamentals of Keto-Hydrazide CrosslinkingFTIR analysis revealed that 2-heptanone exhibits a strong carbonyl peak at 1710 cm-1 and octanoic hydrazide exhibits a strong band at 1628 cm-1 attributable to the amide carbonyl and N-H stretching. On reaction, it would be expected that the intensity of the ketone carbonyl and the N-H stretching and bending peaks would be reduced, as they are consumed during crosslinking.On reaction of the model components, a new peak was observed in the region 1670cm-1. Figure 2 shows that with an excess of 2-heptanone (2:1 molar ratio) a newpeak is observed adjacent to the ketone carbonyl. As the level of octanoic hydrazide is low, indicated by the low intensities of the relevant peaks, then this new peak is unlikely to be related to the hydrazide. For a reaction mixture containing equimolar proportions of reactants, the ketone carbonyl is partially masked by the new peak. In the presence of excess octanoic hydrazide (2:1 molar ratio) the new peak appears adjacent to the amide peak. This would seem to rule out any possibility that the new peak is the result of an amide solution shift. Critically, the new peak at ~1670cm-1 is in the correct region for a reaction product containing C=N (1690-1630 cm-1) 41. Figure 2: An overlay of Infra Red showing the presence of an absorption band at 1670 cm-1 in the anticipated region for C=N Imine. Spectrum 1 (red line): 2-heptanone; Spectrum 2 (green line): excess 2-heptanone plus octanoic hydrazide; Spectrum 3 (purple line): Octanoic Hydrazide; Spectrum 4 (blue line): excess octanoichydrazide plus 2-heptanone.The 13C NMR spectrum of 2-heptanone exhibits a peak at around 210 ppm, due to the ketone C=O group. In comparison, the amide ester carbonyl in octanoic hydrazide is observed at around 175 ppm. On reaction the peaks due to the model component are depleted in acidic and neutral solutions as would be expected. Two new peaks are observed at around 160 ppm and 150 ppm. The chemical shift for C=N is expected in the 165 to 145 ppm range 41, and so this indicates that the product is an imine. There are no peaks present in the 140-100 ppm region, where C=C would be expected to be observed. There is evidence in the literature to indicate that the two peaks observed in the NMR spectrum are most probably due to•the result of hydrogen bonding, due to methyl group influence, and•rotation about the C=N bond, altering the field effect on the amide carbonyl, and thereby giving rise to two isomeric forms, as illustrated in the inset in figure 3.Figure 3:13Carbon Nuclear Magnetic Resonance spectrum for reaction product between 2-heptanone and octanoic hydrazide under acidic conditions. The spectrum shows the depleted C=O peak at 210 ppm and four peaks in the 150-180 ppm region attributed to the amide C=O group and the C=N group. Two peaks appear for each of these groups due to the possibility of two rotamer forms (structures shown inset).Analysis of the product of the model reaction using GC/MS Chemical Ionisation highlighted the presence of a molecular ion of 255 amu (M+1), as would be anticipated from options (1) and (2) in Figure 1.GC/MS analysis of alkaline solutions showed the presence of strong peaks for the reactants, 2-heptanone and octanoic hydrazide. In contrast, neutral and acidic solutions show a dominant product peak and diminished reactant responses. Comparison of the initial rates of the reactions under different pH condition clearly show that the chemical reaction rate increases with decreasing pH, as illustrated in figure 4. We conclude then that the reaction is acid catalysed.Figure 4: Graph showing the relationship between solution pH and initial reactionrate for octanoic hydrazide and 2-heptanone.It is known that in a carbonyl group the electronegative oxygen withdraws electrons from the carbon bond resulting in the carbonyl carbon attaining a relative positive charge 42. The electrophilic character of the carbon therefore significantly enhances its susceptibility to nucleophilic attack by electron-rich reagents 42-47. Moreover, the part of the molecule immediately surrounding the carbon is flat, with oxygen, carbon and the two atoms directly bonded to the carbon lying in the same plane. Consequently, this part of the molecule is open and relatively unhindered from attack from above or below, in the direction perpendicular to the plane of the carbonyl group45. As nitrogen exhibits electronegative character, and will readily donate a pair of electrons, it is expected that the carbonyl group will be prone to react with amines. The literature maintains that amines will react with both aldehydes and ketones, with the nature of the product being dependent on the species involved and reaction conditions 46.The susceptibility of the carbonyl group to nucleophilic attack is reduced by its attachment to electron-releasing alkyl groups that reduce the degree of positive charge on the carbon 42, 43. Therefore, as ketone structures comprise two alkyl groups attached to the carbon, compared to alkyl and hydrogen in an aldehyde molecule, then ketones would be expected to be less reactive than aldehydes. Indeed the presence oftwo alkyl groups would also be expected to incur some steric hindrance to attack on the carbon. It has been reported elsewhere that primary amines produce imines on reaction with aldehydes and ketones, although ketones react more slowly than aldehydes, sometimes requiring higher temperatures and longer reaction times 46, 47. In addition the progression of the reaction is inhibited by the formation of water, and the literature identifies that, in reaction studies, the water must be removed either by distillation or with a drying agent 46. This latter behaviour is of particular interest in the case of the waterborne latex. It would seem reasonable to propose then that the presence of water will “block” the crosslinking reaction until, after sufficient drying has occurred. The water content of the film reaches a critical level where the equilibrium of the keto-hydrazide is shifted in favour of crosslinking.Whilst primary amines and carbonyl groups will form imines, it is known that enamines can be formed on the reaction of aldehydes and ketones with secondary amines 46. Furthermore, for carbonyl compounds with an α-proton, a rotamer equilibrium can exist between the imine and the enamine, but in which the imine form predominates 48. Despite the abundance of literature supporting imine formation from reaction between the carbonyl group and primary amines, specific reports on the keto-hydrazide are few.The literature indicates that the reaction of a nucleophile with a carbonyl compound is often catalysed by acid 43, 45, 46. Protonation of the carbonyl oxygen further increases the positive charge at the carbon, making it much more susceptible to nucleophilic attack. So, in the case of a carbonyl compound nucleophilic addition will be favoured by high acidity. However, protonation of the amine produces a species lacking unshared electrons resulting in the loss of nucleophilic character. Thus, with respect to the amine compound, addition is favoured by low acidity. In reality, an efficient reaction condition would be a compromise, with the exact requirements depending on the reactivity of the carbonyl, and the basic character of the reagent.Based on the experimental results of this research work and literature evidence, we propose the mechanism shown in figure 5 for the keto-hydrazide reaction in our latex system.Figure 5: Proposed mechanism for the keto-hydrazide reaction within the waterborne coating yielding an imine – not an enamine as has been proposed elsewhere.In an acid environment the process commences with the formation of a bond between H+and the carbonyl oxygen. The nucleophilic amine group on the hydrazide molecule attacks the electrophilic carbonyl carbon, resulting in the formation of a C-N bond. Proton transfer occurs from the positively charged nitrogen to form a bond between H+and the oxygen, yielding a carbinolamine. Cleavage of the positively charged H2O from the central carbon then occurs, forming a resonance stabilised intermediate. The nitrogen stabilised carbocation is the conjugate acid of the imine and transfer of the hydrogen atom, attached to the nitrogen, to water yields the imine. Chemical Crosslinking During Film FormationGravimetric measurement of latex solids fraction as a function of drying time during film formation was used as a rough indicator of the point of particle close packing. Parallel measurements of the wet film’s pH with indicator paper revealed an increase in acidity over time, reaching a pH of ~6 after six minutes of drying. In a complementary experiment, litmus was added to the wet latex dispersion prior to film formation. This experiment clearly revealed that the film became significantly acidic when dried. The decreasing pH during film formation is attributed to the loss of ammonia through evaporation. Significantly, latex pre-neutralised with non-volatile amine did not exhibit the pH change.Figure 6: Graph showing the change in pH for a thin latex film during film formation with respect to change in wt.% solids. (As the densities of the water and copolymer are nearly identical wt.% will be very close to vol.%.)Combining the pH measurement with the solids fraction measurements (Figure 6), we are then able to establish the solids fraction when crosslinking is favoured. The figure shows that the pH decreases below 7 when a solids content of approximately 68 wt.% is achieved. Depending on the particular packing of the particles, this solids content would correspond to the point of contact between particles. (For mono-size hard particles the maximum solids fraction at close packing is 74 vol.%.) The gas chromatography data clearly showed that the chemical reaction rate increasessubstantially below a pH of 7. Therefore crosslinking in the film is favorable only near and after the point of close packing. Polymer interdiffusion likewise cannot occur until particles have made physical contact, of course. Thus, interdiffusion and crosslinking will probably occur simultaneously. As already noted there is an optimum pH to achieve the fastest reaction rate, and it is expected that the acidity in the polymer phase will be correlated with that in the water phase.The influence of the level of ADH cross-linker on the polymer gel fraction is shown in figure 7. Gel content increases rapidly over the first 15 minutes of film drying, after which the rate slows but never reaches 100%. The rate of increase in gel content and the final gel value are identical for 0.5 wt.% and 1 wt.% ADH, indicating that 0.5 wt.% is sufficient to ensure that ADH reacts with at least one DAAM group per molecule. Hence a film containing 0.2 wt.% achieves a lower gel fraction, being insufficient for the crosslinking of every polymer molecule. In order to investigate this observation further, films subjected to vacuum drying rather than drying in air, were measured also. An increase of around 2 to 3% (not shown) in the final gel fraction was found, but 100% gel was still not attained. These results indicate the presence of some residual water presence in air-dried films.Possible – but unlikely - explanations for why the maximum gel fraction is only around 90% are that some macromolecules do not contain DAAM or that some molecules only have one crosslink. Another possibility is that there is some intra-molecular crosslinking in which two DAAM groups on the same molecule are reacted with an ADH cross-link molecule. Recent simulations of gel fraction [26], which consider the effects of molecular weight polydispersity and the number of crosslink units, offer the most likely explanation.Statistical variation means that some polymer molecules will have greater than average crosslinks per molecule, whilst others will have less than the average or even zero. Simulations [26] show that as polydispersity increases then more crosslinked units are required to achieve a given gel fraction. Thus, a lower polydispersity favours a higher gel fraction for a given number of crosslinks. The “standard” latex has a polydispersity of ~2.7. When 1 wt.% ADH is added it is estimated that there can be up to 6 crosslinks per polymer molecule. In this case it is estimated that approximately 90% gel can be achieved, as was observed in the experiments.To achieve one crosslink per polymer molecule, one half of a molecule of crosslinker is required for each polymer molecule. On average each “standard” latex polymer molecule contains sixteen DAAM groups. Using the previously calculated molar ratio values, Table 1, the number of DAAM groups that can actually be reacted may be calculated. For 1 wt.% ADH added to “standard” latex, there are 0.37 moles of ADH per 1 mole of DAAM. It follows then that 37% of the available DAAM groups can be reacted, corresponding to 6 crosslinks per polymer molecule. In the case of 0.5 wt.% and 0.2 wt.% ADH “standard” latex this reduces to 3 and 1 crosslinks per polymer molecule, respectively. Clearly this indicates that there is insufficient ADH crosslinker present to react with all of the available DAAM groups. The maximum crosslink density cannot be achieved in these formulations, and furthermore ADH is not soluble in water at higher concentrations.Gel fraction measurements (Figure 7) also indicate that the latex particle size influences the rate of increase of the gel content. The gel fraction of latex comprising 80 nm particles reaches a plateau value after around 15 minutes. However, the rate of gelation becomes slower with increasing latex particle size (150 nm and 300 nm). In order to achieve the maximum gel fraction, the ADH must diffuse a distance on the order of the particle radius. The dependence of gelation rate on the particle size indicates that the reaction is limited by the diffusion of ADH into the latex particles. Our results indicate that the ADH is partitioned mainly in the aqueous phase initially and enters the polymer phase during the later stages of film formationFigure 7: Gel Fraction graphs showing the influence of level of cross-linker (top), film thickness (top) and particle size (lower) on the rate of gel evolution in the latexfilm.The film thickness of the latex dispersion was varied in order to probe the influence of water content on the progression of the crosslinking reaction. It has been discussed previously in this work that the keto-hydrazide reaction is inhibited by the presence of water. Therefore that keto-hydrazide crosslinking in a latex film is not expected to occur unless a sufficient fraction of the water component has evaporated. By studying films with different thickness the quantity of water per unit area required to evaporate was therefore varied. It was observed that the onset of crosslinking is delayed in。