APP(2013)机理[16]
5,10,15,20-四(4-氨基苯基)卟啉的合成进展

5,10,15,20-四(4-氨基苯基)卟啉的合成进展邹太和;罗通;罗华锋;田婧;雷开键;薛智【摘要】There are two synthetic approaches of 5,10,15,20-tetrakis (4-aminophenyl) porphyrin (TAPP). One is called Adler��s method, in which benzaldehyde with 4-radical (4-acetamido, 4-nitro-, or 4-halogen) is converted by condensa⁃tion with pyrrole under acidic condition. Then the target product is obtained by hydrolysis, reduction or amination of this intermediate respectively. Another method is carried on benzaldehyde and pyrrole to gain 5,10,15,20-tetrakis-phenylpor⁃phyrin (TPP). After that, TPP is nitrated and reduced to afford TAPP. Although the second method includes more steps than Adler��s method, it involves much cheaper raw material, so it is easier to be manipulated, and is more fitful for mass production.%5,10,15,20-四(4-氨基苯基)卟啉的合成主要有两大途径:一是根据传统Adler方法,以4位官能团(酰氨基,硝基,卤素)取代的苯甲醛与吡咯在酸性条件下进行缩合,所得卟啉中间体再进一步水解或还原或者氨化可得目标产物;二是由无取代的苯甲醛与吡咯缩合得到5,10,15,20-四苯基卟啉,该中间体再经外围硝化,还原得到目标产品。
聚磷酸铵的合成及改性研究进展

聚磷酸铵的合成及改性研究进展张晖;赖小莹;艾常春;何宾宾;胡意;刘洋;冯碧元【摘要】In order to solve the key scientific problems in the process of research about ammonium polyphosphate (APP) , and improve our country's core competitiveness in the international market, we summarized the latest research results of crystallization Ⅱ ammonium polyphosphate (APP- Ⅱ ) at home and abroad, analyzed the flame retardant mechanism, synthesis methods and the superiority and inferiority of the different modification methods. The results show that APP- Ⅱ is simultaneous as the acid source and gas source in the process of flame retardant; on the one hand, water vapor, ammonia, nitrogen and nonflammable gas are released when APP- Ⅱ is decomposed; on the other hand, APP-Ⅱ generates polyphosphoric acid after heating, which enables the retardant dehydrating to carbide, then carbide on the substrate surface forms a dense expansion carbon layer, thereby preventing the gas diffusion. Synthetic materials generally consist of ammonium dihydrogen phosphate and phosphorus-containing substances, synthesis conditions determine the level of the degree of polymerization. APP-Ⅱ modified technology mainly includes four methods of microencapsulation coating technology, surfactant modified melamine modified and coupling agent. Among them, the coupling agent is the,focus of current research; the rest methods have some limitations.%为了解决聚磷酸铵阻燃剂在研究中存在的关键科学问题,提高我国聚磷酸铵产品在国际市场的核心竞争力,综述了国内外的结晶Ⅱ型聚磷酸铵最新研究成果,分析了其阻燃机理、合成方法以及不同改性方法的优劣.结果表明,其阻燃机理为:结晶Ⅱ型聚磷酸铵在阻燃过程中除了作酸源外也可兼作气源,一方面受热分解时释放出水蒸气、氨气和氮气等不燃性气体;另一方面,受热后生成强脱水剂聚磷酸,聚磷酸可使被阻燃物表面脱水生成碳化物,碳化物在基质表面形成致密性膨胀炭层,从而阻止气体扩散.其合成的原料一般为磷酸二氢铵和含磷物质,合成条件的控制决定聚合度的高低.结晶Ⅱ型聚磷酸铵改性技术主要有微胶囊化包覆技术、表面活性剂改性、三聚氰胺改性以及偶联剂改性四种方法,其中偶联剂改性是目前研究的热点,前三种方法均有一定的局限性.【期刊名称】《武汉工程大学学报》【年(卷),期】2012(034)010【总页数】5页(P32-36)【关键词】Ⅱ型聚磷酸铵;机理;合成;改性【作者】张晖;赖小莹;艾常春;何宾宾;胡意;刘洋;冯碧元【作者单位】云南磷化集团有限公司,云南昆明650113;国家磷资源开发利用工程技术研究中心,云南昆明650113;武汉工程大学,湖北武汉430074;国家磷资源开发利用工程技术研究中心,云南昆明650113;武汉工程大学,湖北武汉430074;云南磷化集团有限公司,云南昆明650113;国家磷资源开发利用工程技术研究中心,云南昆明650113;武汉工程大学,湖北武汉430074;武汉工程大学,湖北武汉430074;国家磷资源开发利用工程技术研究中心,云南昆明650113;武汉工程大学,湖北武汉430074【正文语种】中文【中图分类】TQ314.24+80 引言随着合成材料的广泛应用,阻燃剂的消耗量日益增加,在塑料助剂中已跃居第二位[1].阻燃剂主要有卤系、磷系以及铝镁系等[2].有机卤系阻燃剂效果比较好,但在阻燃材料着火过程中会释放出毒性气体,危害很大.欧盟于2006开始颁发一系列政策,逐步取消卤系阻燃剂的使用,并开展了新型阻燃剂的研究与开发[3].氢氧化铝及氢氧化镁不含有毒物质,发烟量小,是真正环保的无卤阻燃剂,但是其阻燃效率低、添加量大且密度高,大幅提高了材料的成本并破坏其力学性能[4-5].膨胀型阻燃剂(IFR)是一种典型的无卤阻燃剂[6].聚磷酸铵(APP)是IFR常用组分之一,其阻燃机理为:聚磷酸铵受热后脱去氨气生成强脱水剂聚磷酸,聚磷酸可使被阻燃物表面脱水生成碳化物,碳化物在基质表面形成致密性膨胀炭层,炭层可减弱聚合物与热源间的热量传递,并阻止气体扩散,由于没有足够的燃料和氧气,因而终止燃烧起到阻燃作用[7-8].APP是目前无机阻燃剂效果最好的一种阻燃材料,且价格低廉,对人体无毒无害.在水中的溶解度随温度的升高而增加,外观呈白色粉末状,有水溶性和水难溶性两种,其中聚合度n在10~20为水溶性,称为短链APP (即结晶Ⅰ型APP),n> 20为水难溶性的长链APP (即结晶Ⅱ型APP).然而APP-I具有多孔性颗粒状结构,吸湿现象严重,而且其与聚合物相容性差,易从聚合物中渗出,严重影响材料的力学性能;另外,热稳定性差.而APP-II为正交晶型,结构紧密,且颗粒表面十分圆滑,耐水性强于APP-I,其聚合度也比APP-I高,所以近年有较多关于APP-II合成及改性的研究报道[9-13].1 APP-II结构与性质APP按其结构分为结晶型和无定型玻璃体两种形态,无定型APP聚合度小、易溶于水、疏松结构.而结晶态APP则为水不溶性长链状聚磷酸盐,其pH值近中性,无腐蚀作用,聚合度愈大,水溶性愈小.从X射线衍射结果可知,APP有5种不同的结晶形式(I-V型),这些晶型中只有II型和V型难溶于水,其中APP-II型具有规则的外表面,属正交(斜方)晶系,晶胞参数:a=0.425 6,b=0.647 5,e=1.204 nm.最有可能的空间结构为P212121,其结构式为[3].2 APP-II阻燃机理Camino G等[14]在20世纪80年代中期对膨胀型阻燃体系的机理做过研究.膨胀型阻燃体系主要成分可分为酸源、碳源、气源3个部分.在受热时成炭剂(如季戊四醇及其二缩醇、三嗪衍生物等)在酸源作用下脱水成炭,并在气源分解的气体作用下,形成蓬松有孔封闭结构的炭层,炭层可减弱材料与热源间的热量传递,并阻止气体扩散,材料由于没有足够的燃料和氧气,因而终止燃烧,达到阻燃目的[15]. APP-II在阻燃过程中除了作酸源外也可兼作气源.一方面受热分解时可释放出水蒸气、氨气和氮气等不燃性气体;另一方面,在较低温度下,先由APP-II分解形成强脱水剂聚偏磷酸等酸性物质,它能与成炭剂形成酯,酯然后脱水形成炭,同时释放大量的气体使炭层膨胀[16-17].厚的炭层提高了材料表面与炭层表面的温度梯度,使材料表面温度较火焰温度低得多,减少了材料进一步降解释放可燃性气体的可能性,同时隔绝了外界氧的进入,因而在相当长的时间内可以对材料起阻燃作用[18].3 APP-II的合成工艺关于APP-II的制备方法研究国内文献报道极少,国外关于高聚合度APP-II的制备报道较多,最多的是以五氧化二磷为主要制备原料.比如美国专利5139758[19]中介绍,在控制一定氨气浓度下,以磷酸二氢铵和五氧化二磷(1∶1)为原料,于170~350 ℃温度下反应1~2 h,得到不溶性链状APP-II产品.US5277887[20]专利中也提到利用正磷酸铵与五氧化二磷为原料制备水难溶性链状APP-II.Shen C Y等人[21]介绍了首先利用正磷酸铵和尿素合成APP-I,然后在封闭容器中于300 ℃温度下反应60 h得到APP-II;日本Chisso公司以磷酸氢二铵和尿素为原料合成了长链型APP-II 产品.Chisso公司的研究发现,在加热熔融时,磷酸氢二铵与尿素反应形成的熔体是由无定形的APP 和未氨化的APP 构成,当湿氨气通过此熔体时,熔体中的羟基与氨气形成铵盐,与此同时即形成晶格,此时加入APP-II型晶品种则会使晶体按APP-II所需的形状增长,最后成为所需的APP-II型晶体[22].国内黄祖狄等[23]采用正磷酸铵与五氧化二磷在氨气气氛中能够制备长链的水溶性低的的APP-II产品,溶解度在0.05 g以下,分解温度在300 ℃以上.吴大雄等[24]采用化学合成法制备了平均聚合度为28 的聚磷酸铵(APP) 样品,通过球磨2浮选处理后获得200 nm左右,粒度均匀的超细APP样品.张正元等[25]研究了在常压条件下以湿法磷酸生产的工业级磷酸一铵和尿素为原料生产聚磷酸铵( APP) 的合成工艺条件,制备了平均聚合度为400 的聚磷酸铵.刘丽霞等[26]以磷酸和尿素为原料合成聚磷酸铵,并通过X射线粉末衍射和红外光谱对产品晶型进行分析鉴定.张健等[27]深入研究了以磷酸脲与尿素为原料制取聚磷酸铵的合成工艺,采用模拟气氛→探讨温度→讨论其它因素→优化工艺条件的实验路线.4 APP-II表面改性技术对APP-II进行表面改性主要是降低APP-II的水溶性,改善其与树脂的相容性,提高热稳定性.目前,APP-II改性技术主要有微胶囊化包覆技术、表面活性剂改性、三聚氰胺改性以及偶联剂改性,下面就这四种改性技术分别进行介绍.4.1 微胶囊包覆技术微胶囊包覆技术是指将APP-II利用天然的或合成的高分子材料包覆,形成一种直径1~50 μm的具有半透性或封闭膜的微型胶囊APP-II产品,与APP-I相比具有更高的热稳定性、耐水性以及相容性[28].国外知名企业赫司特公司、孟山都公司及Albright Wilson公司均生产高聚合度APP-II产品.微胶囊的外形可以是球状的,也可以是不规则的形状;胶囊外表可以是光滑的,也可以是折叠的;微胶囊的囊膜既可以是单层,也可以是双层或多层结构.微胶囊技术的优势在于形成微胶囊时,囊芯被包覆而与外界环境隔离,它的性质能毫无影响的被保留下来,而在适当条件下壁材被破坏时又能将囊芯释放出来,给使用带来许多便利.微胶囊化的目的主要是降低阻燃剂的水溶性,增加阻燃剂与材料的相容性,改变阻燃剂的外观及状态,提高阻燃剂的热裂解温度以及掩盖阻燃剂的不良性质.其制备方法主要有化学法,物理化学法,机械法[16].欧洲专利EP 3531500[29]报道,用三聚氰胺甲醛树脂包覆APP-II,形成微胶囊化APP-II产品,其水溶性大幅度下降,且阻燃效果达到UL-94 V-0级.Kun W等[30]利用聚乙烯醇改性三聚氰胺-甲醛树脂包覆APP-II,并将其与双季戊四醇以不同比例混合阻燃聚丙烯,研究结果表明,所得微胶囊可以大幅度降低材料的热释放速率,同时三聚氰胺-甲醛树脂预聚物中PVA的含量对微胶囊的耐水性和材料的阻燃性能有重要影响.特别是PVA含量为15%时,材料氧指数可达32,材料燃烧等级通过UL-94 V-0.国内也在做大量的研究,但均处于实验室阶段.章驰天等[31]以三聚氰胺、甲醛单体为原料制得了微胶囊化APP-II.研究人员为了考察制得的微胶囊化APP-II对PP的阻燃性能,在PP塑化后分别加入普通APP-II和微胶囊化APP-II,发现微胶囊化APP-II的阻燃性能明显增强.刘琳等[32]采用原位聚合法制备了以环氧树脂( EP) 为壁材,聚磷酸铵( APP) 为芯材的微胶囊阻燃剂(MCAPP).研究了不同含量的壁材对MCAPP溶解度的影响,结果发现,与未包覆的APP相比,在25 ℃和80 ℃条件下,MCAPP的溶解度都有较大幅度降低.4.2 表面活性剂改性APP-II用碳原子数为14~18的脂肪酸及其金属盐(形成阴离子表面活性剂)或其混合物(镁盐、锌盐、钙盐、铝盐)处理后,其吸水性会显著降低[33].此外,还可以利用阳离子或非离子表面活性剂对APP-II进行改性,如带有酰基的碳原子数为14~18的脂肪酸,二甲基氯铵等,其中非离子表面活性剂亲水亲油平衡值控制在5~10之间.Chakrabarti P M[34]利用阳离子或非离子表面活性剂来对APP-II进行改性.改性后的APP-II防水绝缘性能大幅度提高,在树脂方面应用较广.4.3 采用三聚氰胺进行改性采用三聚氰胺进行改性是利用三聚氰胺将APP-II表面包裹,然后使用交联剂把三聚氰胺与已经包裹的APP-II颗粒连接起来,提高APP-II分子链之间的键合力,改善吸湿性[35].廖凯荣等[36]通过热处理APP-II与三聚氰胺的混合物, 获得热稳定性较高( 起始失重温度达250 ℃以上) 和吸湿性较低的膨胀型阻燃剂MPPA,实验表明MPPA与季戊四醇复配后对聚丙烯的阻燃作用显著增强.王学宝等[37]研究了三聚氰胺包覆聚磷酸铵(MPP)与季戊四醇(PER)阻燃环氧树脂的燃烧性能.通过热重分析初步探讨了MPP/PER阻燃剂对环氧树脂的阻燃机理.徐定红[8]采用热活化后的APP与三聚氰胺反应制备热活化改性APP,并与未改性APP作对比,重点比较初始水溶解性和pH值等性能指标,发现改性后的APP水溶性逐渐减小,水溶液由弱酸性变成中性.一般来说,经三聚氰胺改性后的APP-II仍不能满足需要,由于在产品粉碎之后,不能保证APP-II包覆的均匀性,所以包覆后的APP-II仍具有较大的吸湿性.日本有报道用含有活性氢的化合物处理用三聚氰胺改性后的APP-II,其耐水等性能大幅提升[38].4.4 用偶联剂改性进行改性偶联剂是一类具有两不同性质官能团的物质,其分子结构的最大特点是分子中含有化学性质不同的两个基团,一个是亲无机物的基团,易与无机物表面起化学反应;另一个是亲有机物的基团,能与合成树脂或其它聚合物发生化学反应或生成氢键溶于其中.常用的偶联剂有硅烷、钛酸酯、磷酸酯、铝酸酯等类型,其中硅烷偶联剂是品种最多的一种.偶联剂本身具有一定的阻燃性,所以将偶联剂加入到APP-II中,既能够增加阻燃性,又能够改善所填充材料的韧性、耐热性以及吸水率[39].Hiroyuki M[40]利用硅烷偶联剂将小的有机分子加到APP-II分子链上改善APP-II吸湿性与分散性,如低分子的烷烃与烯烃.张晓光等[41]采用动态热机械分析(DMA)、热重分析(TG)与氧指数测定(LOI)等研究APP和表面用偶联剂处理过的聚磷酸铵(T-APP)对聚氨酯泡沫阻燃性能和力学性能的影响.结果表明,APP 与T-APP 都提高了聚氨酯泡沫的燃烧氧指数,后者效果更加明显;当聚磷酸铵用偶联剂处理后,一定程度上改善了加入纯的聚磷酸铵对聚氨酯泡沫的压缩强度和模量的破坏行为.郝建薇等[39]采用氨基硅烷偶联剂对APP进行了表面改性,结果表明,改性后的APP具有良好的疏水性;氨基硅烷偶联剂与APP发生了键合反应,降低了APP的水溶性,提高了阻燃效果及与材料的相容性.5 结语随着APP-II的应用越来越广泛,对其品质的要求不断的提高,致使制备及改性APP-II的方法也会越来越受到重视.有关高质量APP-II产品在国外早已投入市场,其聚合度高达2 000,溶解度几乎为0,且白度指数较高.我国由于在生产设备、工艺等方面的不足,生产出的大部分为稳定性差、聚合度很低的APP-I产品.随着中国阻燃剂市场的不断开发,市场对聚磷酸铵的需求量将进一步大幅度增长.因此首先应找出高聚合度APP-II合成原理与方法,形成APP-II产品绿色合成技术路线,从而合成聚合度高的APP-II产品;其次采用合适的改性技术改性APP-II,提高材料与阻燃剂之间的相容性等.参考文献:[1] Gou S L, Wen Y C. A novel process to prepare am-monium polyphosphate with crystalline form Ⅱ and its comparison with melamine polyphosphate[J]. Ind Eng Chem Res, 2010, 49(1): 12148-12155.[2] 高苏亮,戴进峰,李斌. 改性聚磷酸铵对三嗪类膨胀阻燃聚丙烯性能的影响[J]. 塑料科技, 2009, 37(7): 138-142.[3] 马庆文. 高聚合度聚磷酸铵的制备[D]. 昆明: 昆明理工大学化学工程学院,2007: 1-69.[4] 张世伟,李天祥. 水难溶性聚磷酸铵的合成技术研究进展[J].化工中间体, 2006, 5(1): 1-3.[5] 郭冬冬. 高效无机阻燃剂-聚磷酸铵的制备研究[D]. 北京: 中国石油大学理学院,2009: 1-72.[6] 宋同彬,古思廉,梅毅,等. Ⅰ-型聚磷酸铵晶型转化研究[J]. 广东化工, 2010, 37(203): 69-70.[7] 郝冬梅,林倬仕,陈涛,等. 不饱和聚酯树脂微胶囊化聚磷酸铵对阻燃聚丙烯性能的影响[J].塑料助剂, 6(72): 43-47.[8] 徐定红,秦军,于杰,等. 不同聚合度聚磷酸铵对HDPE阻燃性能影响研究[J]. 贵州工业大学学报:自然科学版, 37(5): 68-70.[9] 杨杰,陶文亮. 聚磷酸铵的改性一聚磷酸酯的研究进展[J]. 贵州化工, 2009,34(4): 1-3.[10] 李蕾,杨荣杰,王雨钧. 聚磷酸铵(APP)的合成与改性研究进展[J]. 消防技术与产品信息, 2003, 6(1): 43-45.[11] 傅亚,陈君和,贾云. 高聚合度Ⅱ-型聚磷酸铵的合成[J]. 合成化学, 2005,13(6): 610-613.[12] 骆介禹,骆希明. 结晶I型和Ⅱ型聚磷酸铵的性能差异[J].上册.阻燃材料与技术, 2005, 1(5): 13-15.[13] 曹建喜,罗立文,郭冬冬. 高效无机阻燃剂聚磷酸铵的合成[J]. 中国石油大学学报:自然科学版, 2009, 33(6): 132-135.[14] Camino G, Costa L, Trossarelli L. Study of the mechanism of intumescence in fire retardantpoly-mers: Part II-Mechanism of action inpolypropy-lene ammonium polyphosphate pentaerythritolmix-tures [J]. Polymer Degradation and Stability, 1984, 7(1): 25-31.[15] 蔡晓霞,王德义,彭华乔,等. 聚磷酸铵/膨胀石墨协同阻燃EVA 的阻燃机理[J]. 高分子材料与工程, 2008, 24(1): 109-112.[16] 倪健雄. 核-壳型聚磷酸铵阻燃剂的制备及其阻燃聚氨酯性能与机理的研究[D]. 合肥: 中国科学技术大学化学化工学院, 2009: 1-111.[17] 殷锦捷,姜军. 聚磷酸铵对聚丙烯/聚乙烯复合材料阻燃性能的影响[J]. 塑料助剂, 2008, 4(70): 43-45.[18] 张青,陈英红,武慧智. 聚磷酸铵基复合膨胀型阻燃剂的制备及其对聚甲醛的阻燃作用[J]. 塑料科技, 2011, 37(11): 41-47.[19] Thomas S, Renate A. Process for the preparation of ammonium polyphosphate: United States, 5139758[P].1992-08-18.[20] Thomas S, Wolfgang B, Herbert N. Process for the preparation of ammonium polyphosphate: United States, 5277887[P].1994-01-11. [21] Shen C Y. Preparation and characterization of cry-stalline long-chain ammonium polyphosphates [J]. J Am Chem Soc, 1969, 91(2):62-67. [22] 丁著明,范华. 阻燃剂聚磷酸铵的生产和应用[J]. 阻燃材料与技术, 2003, 4(1): 4-14.[23] 黄祖狄,赵光琪.长链聚磷酸铵的合成[J].化学世界, 1986, 27(11): 483-484.[24] 吴大雄,郭家伟. 超细聚磷酸铵的制备及有机包覆[J]. 化工新型材料. 2008, 36(9): 84-86.[25] 张正元,张志业. 聚磷酸铵的合成[J]. 磷肥与复肥. 2008, 23(2): 16-24.[26] 刘丽霞,陶文亮,李龙江. 聚磷酸铵的合成及其阻燃性能研究[J]. 贵州化[27] 张健. 聚磷酸铵合成工艺研究[J]. 成都:四川大学化工学院, 2005: 1-80.[28] 唐慧鹏. 微胶囊化多聚磷酸铵的制备及其在聚丙烯中的应用[D]. 保定: 河北大学理学院, 2010: 1-44.[29] Pieper W, Staendeke H, Elsner G. Method for the preparation of hydrolysis-stable finely divided flame retardants based on ammonium polyphosphate: EP, 3531500[P]. 1986-05-14.[30] Kun W, Zheng Z W, Yuan H. Microencapsulated ammonium polyphosphate with urea-melamine-formaldehyde shell: preparation, characterization and its flame retardance in polypropylene [J]. Polymers for Advanced Technilogies, 2008, 19(12): 1118-1125.[31] 章驰天,苏新清. 凹凸棒对聚丙烯/聚磷酸铵/季戊四醇复合材料阻燃性能及力学性能的影响[J]. 塑料, 2010, 39(2): 113-114.[32] 刘琳, 张亚楠,李琳,等. 环氧树脂包覆聚磷酸铵微胶囊的制备及表征[J]. 高分子材料科学与工程, 2010, 26(9): 136-138.[33] 徐定红. 聚磷酸按的改性及其在HOPE中的应用研究[D]. 贵阳: 贵州大学化学与化工学院, 2009, 1-73.[34] Chakrabarti P M. Surface-moldified ammonium polyp-hosphate: United States, 5109037 [P]. 1992-04-28.[35] 张美玲,曲敏杰,代新英. 聚磷酸铵/三聚氰胺/聚氨酯复合阻燃聚甲醛的研究[J]. 化工新型材料, 2010, 38(10): 76-79.[36] 廖凯荣,卢泽俭.多聚磷酸铵的改性剂其对聚丙烯的阻燃作用[J]. 高分子材料科学与工程, 1998, 14(4): 87-92.[37] 王学宝,杨守生. 三聚氰胺包覆聚磷酸铵阻燃环氧树脂的研究[J]. 塑料科技,[38] 崔小明.阻燃剂聚磷酸铵的改性和应用进展[J]. 塑料科技, 2009, 7(1): 82-85.[39] 郝建薇,刘国胜,杜建新,等. 聚磷酸铵表面处理及阻燃聚丙烯应用研究[J]. 北京理工大学学报, 2009, 29(6): 556-559.[40] Hiroyuki M, Kensho N, Takashi T. Compound amm-onium polyphosphate particle and its production: J P, 9227110[P]. 1996-02-22.[41] 张晓光,孟现燕,叶玲,等. 偶联剂处理聚磷酸铵/硬质聚氨酯泡沫[J]. 化工进展, 2010, 29(6): 1107-1111.。
酶催化反应机制.pptx

(四) 共价催化:
标志:催化过程中形成共价中间物1 亲核催化: 带有多余电子对的基团或原子攻击缺少电子而带有部分正电性的原子或基团并形成不稳定的共价中间物的催化方式。 亲核试剂: Glu-COO- Asp-COO- His-咪唑基2 亲电催化: 由缺少电子的亲电试剂从带负电的基团上夺取一对电子并形成共价中间物的催化方式。 亲电试剂: -NH3+
第2页/共19页
(二) 底物形变与诱导楔合
底物形变(distortion)和诱导契合(induced fit): 酶与底物在构象上相互诱导以便更好配合,作用力的产生往往导致底物形变,使被作用的底物敏感键极易断裂例如:溶菌酶催化时使底物糖环由椅式转变为半椅式
第3页/共19页
(三) 广义酸碱催化及共催化:
第8页/共19页
第二节 几种酶作用机制举例
一 溶菌酶(Lysozyme EC 3.2.1.17 ):存在于鸡蛋清和动物分泌物中,单肽链129个aa,14,600,折叠成近球状(4.53 3nm), 底物为NAG和NAM相间 排列或NAG的单聚物催化过程: ①与底物结合: 6个糖环第 3个必须是NAG;其它 糖环和酶形成氢键放能 并导致第4个糖环D由 椅式转变为半椅式 (4kcal/mol)
二 酶与底物相互作用——过渡态
E + S ES* E+P 酶通过与底物形成过渡态中间物, 降低反应活化能而加速反应。过渡态中间物的维持力主要是一 些次级键:氢键、离子键、疏水力等, 形成过程中放出大量能量,抵消了部分活化能处于过渡态的酶与底物的具有很高的亲和力,比底物或产物高出几个数量级底物过渡态类似物: 例如天然具有半椅式结构的环内酯作为溶菌酶的底物,对酶的亲和力比一般糖环高3600倍。
聚合物合成工艺学试题库

选择题1.聚合反应在生产中究竟选择哪一种方法,须由()来决定。
a.单体的性质b.聚合产物的用途c.单体的性质和聚合产物的用途2.聚氯乙烯聚合常用的引发剂是()。
a.有机过氧化物b.偶氮类引发剂c.复合型引发剂3.ABS树脂是()三元共聚物。
a.丙烯腈-丁二烯-苯乙烯b.丙烯腈-异戊二烯-苯乙烯c.丙烯腈-丁二烯-乙烯5.生产丙纶的主要单体是()。
a.丙烯b.乙烯c.丙烯腈6. 丙烯酸应用下列那种方法精制()A 碱洗水洗蒸馏B 重结晶C 减压蒸馏D 萃取7.乳液聚合生产过程中,破乳方法不包括(B )。
A 强烈搅拌B 加热C 加入电解质D 调节pH8.对于粘度很高流动性差的合成橡胶溶液聚合,反应釜应选择(A )搅拌器。
A 螺带式B 平浆式C 锚式D 旋浆式9.本体法生产有机玻璃的特点不包括()。
A 提高聚合速率,分子量降低B 反应体系粘度高,散热困难C 分子量分布窄D 产品后处理简单12.乙烯高压自由基本体聚合中,得到的是(D )。
A HPLDPEB HPHDPEC LLDPED LHDPE13.乳液聚合的主要场所是(B)。
A 胶束B 增容胶束C 单体液滴D 单体分子14.C4馏分中所含的丁烷、丁二烯、丁烯各异构体的沸点非常相近,可通过(C )的方法进行分离。
A 闪蒸B 水蒸气蒸馏C 萃取精馏D 减压蒸馏15.自由基聚合中,可以同时提高反应速率和分子量的聚合是(B)。
A 本体聚合B 乳液聚合C 悬浮聚合D 溶液聚合16.自由基聚合中,悬浮聚合在较高温度下进行时,可以选用()做分散剂。
A 聚乙烯醇B 羟丙基纤维素C 明胶D 碳酸镁17.用无机粉末做分散剂的自由基悬浮聚合结束后,用()洗涤以除去分散剂。
A 稀碱B 稀酸C 去离子水 D十二烷基苯磺酸钠18.BPO常常和()组成氧化还原引发体系用于自由基聚合。
A 亚硫酸钠B 硫代硫酸钠C 二甲苯胺D 硫酸亚铁20.可以制成AB型,多嵌段等不同形式的嵌段共聚物的主要聚合方法为()。
OSHA现场作业手册说明书

DIRECTIVE NUMBER: CPL 02-00-150 EFFECTIVE DATE: April 22, 2011 SUBJECT: Field Operations Manual (FOM)ABSTRACTPurpose: This instruction cancels and replaces OSHA Instruction CPL 02-00-148,Field Operations Manual (FOM), issued November 9, 2009, whichreplaced the September 26, 1994 Instruction that implemented the FieldInspection Reference Manual (FIRM). The FOM is a revision of OSHA’senforcement policies and procedures manual that provides the field officesa reference document for identifying the responsibilities associated withthe majority of their inspection duties. This Instruction also cancels OSHAInstruction FAP 01-00-003 Federal Agency Safety and Health Programs,May 17, 1996 and Chapter 13 of OSHA Instruction CPL 02-00-045,Revised Field Operations Manual, June 15, 1989.Scope: OSHA-wide.References: Title 29 Code of Federal Regulations §1903.6, Advance Notice ofInspections; 29 Code of Federal Regulations §1903.14, Policy RegardingEmployee Rescue Activities; 29 Code of Federal Regulations §1903.19,Abatement Verification; 29 Code of Federal Regulations §1904.39,Reporting Fatalities and Multiple Hospitalizations to OSHA; and Housingfor Agricultural Workers: Final Rule, Federal Register, March 4, 1980 (45FR 14180).Cancellations: OSHA Instruction CPL 02-00-148, Field Operations Manual, November9, 2009.OSHA Instruction FAP 01-00-003, Federal Agency Safety and HealthPrograms, May 17, 1996.Chapter 13 of OSHA Instruction CPL 02-00-045, Revised FieldOperations Manual, June 15, 1989.State Impact: Notice of Intent and Adoption required. See paragraph VI.Action Offices: National, Regional, and Area OfficesOriginating Office: Directorate of Enforcement Programs Contact: Directorate of Enforcement ProgramsOffice of General Industry Enforcement200 Constitution Avenue, NW, N3 119Washington, DC 20210202-693-1850By and Under the Authority ofDavid Michaels, PhD, MPHAssistant SecretaryExecutive SummaryThis instruction cancels and replaces OSHA Instruction CPL 02-00-148, Field Operations Manual (FOM), issued November 9, 2009. The one remaining part of the prior Field Operations Manual, the chapter on Disclosure, will be added at a later date. This Instruction also cancels OSHA Instruction FAP 01-00-003 Federal Agency Safety and Health Programs, May 17, 1996 and Chapter 13 of OSHA Instruction CPL 02-00-045, Revised Field Operations Manual, June 15, 1989. This Instruction constitutes OSHA’s general enforcement policies and procedures manual for use by the field offices in conducting inspections, issuing citations and proposing penalties.Significant Changes∙A new Table of Contents for the entire FOM is added.∙ A new References section for the entire FOM is added∙ A new Cancellations section for the entire FOM is added.∙Adds a Maritime Industry Sector to Section III of Chapter 10, Industry Sectors.∙Revises sections referring to the Enhanced Enforcement Program (EEP) replacing the information with the Severe Violator Enforcement Program (SVEP).∙Adds Chapter 13, Federal Agency Field Activities.∙Cancels OSHA Instruction FAP 01-00-003, Federal Agency Safety and Health Programs, May 17, 1996.DisclaimerThis manual is intended to provide instruction regarding some of the internal operations of the Occupational Safety and Health Administration (OSHA), and is solely for the benefit of the Government. No duties, rights, or benefits, substantive or procedural, are created or implied by this manual. The contents of this manual are not enforceable by any person or entity against the Department of Labor or the United States. Statements which reflect current Occupational Safety and Health Review Commission or court precedents do not necessarily indicate acquiescence with those precedents.Table of ContentsCHAPTER 1INTRODUCTIONI.PURPOSE. ........................................................................................................... 1-1 II.SCOPE. ................................................................................................................ 1-1 III.REFERENCES .................................................................................................... 1-1 IV.CANCELLATIONS............................................................................................. 1-8 V. ACTION INFORMATION ................................................................................. 1-8A.R ESPONSIBLE O FFICE.......................................................................................................................................... 1-8B.A CTION O FFICES. .................................................................................................................... 1-8C. I NFORMATION O FFICES............................................................................................................ 1-8 VI. STATE IMPACT. ................................................................................................ 1-8 VII.SIGNIFICANT CHANGES. ............................................................................... 1-9 VIII.BACKGROUND. ................................................................................................. 1-9 IX. DEFINITIONS AND TERMINOLOGY. ........................................................ 1-10A.T HE A CT................................................................................................................................................................. 1-10B. C OMPLIANCE S AFETY AND H EALTH O FFICER (CSHO). ...........................................................1-10B.H E/S HE AND H IS/H ERS ..................................................................................................................................... 1-10C.P ROFESSIONAL J UDGMENT............................................................................................................................... 1-10E. W ORKPLACE AND W ORKSITE ......................................................................................................................... 1-10CHAPTER 2PROGRAM PLANNINGI.INTRODUCTION ............................................................................................... 2-1 II.AREA OFFICE RESPONSIBILITIES. .............................................................. 2-1A.P ROVIDING A SSISTANCE TO S MALL E MPLOYERS. ...................................................................................... 2-1B.A REA O FFICE O UTREACH P ROGRAM. ............................................................................................................. 2-1C. R ESPONDING TO R EQUESTS FOR A SSISTANCE. ............................................................................................ 2-2 III. OSHA COOPERATIVE PROGRAMS OVERVIEW. ...................................... 2-2A.V OLUNTARY P ROTECTION P ROGRAM (VPP). ........................................................................... 2-2B.O NSITE C ONSULTATION P ROGRAM. ................................................................................................................ 2-2C.S TRATEGIC P ARTNERSHIPS................................................................................................................................. 2-3D.A LLIANCE P ROGRAM ........................................................................................................................................... 2-3 IV. ENFORCEMENT PROGRAM SCHEDULING. ................................................ 2-4A.G ENERAL ................................................................................................................................................................. 2-4B.I NSPECTION P RIORITY C RITERIA. ..................................................................................................................... 2-4C.E FFECT OF C ONTEST ............................................................................................................................................ 2-5D.E NFORCEMENT E XEMPTIONS AND L IMITATIONS. ....................................................................................... 2-6E.P REEMPTION BY A NOTHER F EDERAL A GENCY ........................................................................................... 2-6F.U NITED S TATES P OSTAL S ERVICE. .................................................................................................................. 2-7G.H OME-B ASED W ORKSITES. ................................................................................................................................ 2-8H.I NSPECTION/I NVESTIGATION T YPES. ............................................................................................................... 2-8 V.UNPROGRAMMED ACTIVITY – HAZARD EVALUATION AND INSPECTION SCHEDULING ............................................................................ 2-9 VI.PROGRAMMED INSPECTIONS. ................................................................... 2-10A.S ITE-S PECIFIC T ARGETING (SST) P ROGRAM. ............................................................................................. 2-10B.S CHEDULING FOR C ONSTRUCTION I NSPECTIONS. ..................................................................................... 2-10C.S CHEDULING FOR M ARITIME I NSPECTIONS. ............................................................................. 2-11D.S PECIAL E MPHASIS P ROGRAMS (SEP S). ................................................................................... 2-12E.N ATIONAL E MPHASIS P ROGRAMS (NEP S) ............................................................................... 2-13F.L OCAL E MPHASIS P ROGRAMS (LEP S) AND R EGIONAL E MPHASIS P ROGRAMS (REP S) ............ 2-13G.O THER S PECIAL P ROGRAMS. ............................................................................................................................ 2-13H.I NSPECTION S CHEDULING AND I NTERFACE WITH C OOPERATIVE P ROGRAM P ARTICIPANTS ....... 2-13CHAPTER 3INSPECTION PROCEDURESI.INSPECTION PREPARATION. .......................................................................... 3-1 II.INSPECTION PLANNING. .................................................................................. 3-1A.R EVIEW OF I NSPECTION H ISTORY .................................................................................................................... 3-1B.R EVIEW OF C OOPERATIVE P ROGRAM P ARTICIPATION .............................................................................. 3-1C.OSHA D ATA I NITIATIVE (ODI) D ATA R EVIEW .......................................................................................... 3-2D.S AFETY AND H EALTH I SSUES R ELATING TO CSHO S.................................................................. 3-2E.A DVANCE N OTICE. ................................................................................................................................................ 3-3F.P RE-I NSPECTION C OMPULSORY P ROCESS ...................................................................................................... 3-5G.P ERSONAL S ECURITY C LEARANCE. ................................................................................................................. 3-5H.E XPERT A SSISTANCE. ........................................................................................................................................... 3-5 III. INSPECTION SCOPE. ......................................................................................... 3-6A.C OMPREHENSIVE ................................................................................................................................................... 3-6B.P ARTIAL. ................................................................................................................................................................... 3-6 IV. CONDUCT OF INSPECTION .............................................................................. 3-6A.T IME OF I NSPECTION............................................................................................................................................. 3-6B.P RESENTING C REDENTIALS. ............................................................................................................................... 3-6C.R EFUSAL TO P ERMIT I NSPECTION AND I NTERFERENCE ............................................................................. 3-7D.E MPLOYEE P ARTICIPATION. ............................................................................................................................... 3-9E.R ELEASE FOR E NTRY ............................................................................................................................................ 3-9F.B ANKRUPT OR O UT OF B USINESS. .................................................................................................................... 3-9G.E MPLOYEE R ESPONSIBILITIES. ................................................................................................. 3-10H.S TRIKE OR L ABOR D ISPUTE ............................................................................................................................. 3-10I. V ARIANCES. .......................................................................................................................................................... 3-11 V. OPENING CONFERENCE. ................................................................................ 3-11A.G ENERAL ................................................................................................................................................................ 3-11B.R EVIEW OF A PPROPRIATION A CT E XEMPTIONS AND L IMITATION. ..................................................... 3-13C.R EVIEW S CREENING FOR P ROCESS S AFETY M ANAGEMENT (PSM) C OVERAGE............................. 3-13D.R EVIEW OF V OLUNTARY C OMPLIANCE P ROGRAMS. ................................................................................ 3-14E.D ISRUPTIVE C ONDUCT. ...................................................................................................................................... 3-15F.C LASSIFIED A REAS ............................................................................................................................................. 3-16VI. REVIEW OF RECORDS. ................................................................................... 3-16A.I NJURY AND I LLNESS R ECORDS...................................................................................................................... 3-16B.R ECORDING C RITERIA. ...................................................................................................................................... 3-18C. R ECORDKEEPING D EFICIENCIES. .................................................................................................................. 3-18 VII. WALKAROUND INSPECTION. ....................................................................... 3-19A.W ALKAROUND R EPRESENTATIVES ............................................................................................................... 3-19B.E VALUATION OF S AFETY AND H EALTH M ANAGEMENT S YSTEM. ....................................................... 3-20C.R ECORD A LL F ACTS P ERTINENT TO A V IOLATION. ................................................................................. 3-20D.T ESTIFYING IN H EARINGS ................................................................................................................................ 3-21E.T RADE S ECRETS. ................................................................................................................................................. 3-21F.C OLLECTING S AMPLES. ..................................................................................................................................... 3-22G.P HOTOGRAPHS AND V IDEOTAPES.................................................................................................................. 3-22H.V IOLATIONS OF O THER L AWS. ....................................................................................................................... 3-23I.I NTERVIEWS OF N ON-M ANAGERIAL E MPLOYEES .................................................................................... 3-23J.M ULTI-E MPLOYER W ORKSITES ..................................................................................................................... 3-27 K.A DMINISTRATIVE S UBPOENA.......................................................................................................................... 3-27 L.E MPLOYER A BATEMENT A SSISTANCE. ........................................................................................................ 3-27 VIII. CLOSING CONFERENCE. .............................................................................. 3-28A.P ARTICIPANTS. ..................................................................................................................................................... 3-28B.D ISCUSSION I TEMS. ............................................................................................................................................ 3-28C.A DVICE TO A TTENDEES .................................................................................................................................... 3-29D.P ENALTIES............................................................................................................................................................. 3-30E.F EASIBLE A DMINISTRATIVE, W ORK P RACTICE AND E NGINEERING C ONTROLS. ............................ 3-30F.R EDUCING E MPLOYEE E XPOSURE. ................................................................................................................ 3-32G.A BATEMENT V ERIFICATION. ........................................................................................................................... 3-32H.E MPLOYEE D ISCRIMINATION .......................................................................................................................... 3-33 IX. SPECIAL INSPECTION PROCEDURES. ...................................................... 3-33A.F OLLOW-UP AND M ONITORING I NSPECTIONS............................................................................................ 3-33B.C ONSTRUCTION I NSPECTIONS ......................................................................................................................... 3-34C. F EDERAL A GENCY I NSPECTIONS. ................................................................................................................. 3-35CHAPTER 4VIOLATIONSI. BASIS OF VIOLATIONS ..................................................................................... 4-1A.S TANDARDS AND R EGULATIONS. .................................................................................................................... 4-1B.E MPLOYEE E XPOSURE. ........................................................................................................................................ 4-3C.R EGULATORY R EQUIREMENTS. ........................................................................................................................ 4-6D.H AZARD C OMMUNICATION. .............................................................................................................................. 4-6E. E MPLOYER/E MPLOYEE R ESPONSIBILITIES ................................................................................................... 4-6 II. SERIOUS VIOLATIONS. .................................................................................... 4-8A.S ECTION 17(K). ......................................................................................................................... 4-8B.E STABLISHING S ERIOUS V IOLATIONS ............................................................................................................ 4-8C. F OUR S TEPS TO BE D OCUMENTED. ................................................................................................................... 4-8 III. GENERAL DUTY REQUIREMENTS ............................................................. 4-14A.E VALUATION OF G ENERAL D UTY R EQUIREMENTS ................................................................................. 4-14B.E LEMENTS OF A G ENERAL D UTY R EQUIREMENT V IOLATION.............................................................. 4-14C. U SE OF THE G ENERAL D UTY C LAUSE ........................................................................................................ 4-23D.L IMITATIONS OF U SE OF THE G ENERAL D UTY C LAUSE. ..............................................................E.C LASSIFICATION OF V IOLATIONS C ITED U NDER THE G ENERAL D UTY C LAUSE. ..................F. P ROCEDURES FOR I MPLEMENTATION OF S ECTION 5(A)(1) E NFORCEMENT ............................ 4-25 4-27 4-27IV.OTHER-THAN-SERIOUS VIOLATIONS ............................................... 4-28 V.WILLFUL VIOLATIONS. ......................................................................... 4-28A.I NTENTIONAL D ISREGARD V IOLATIONS. ..........................................................................................4-28B.P LAIN I NDIFFERENCE V IOLATIONS. ...................................................................................................4-29 VI. CRIMINAL/WILLFUL VIOLATIONS. ................................................... 4-30A.A REA D IRECTOR C OORDINATION ....................................................................................................... 4-31B.C RITERIA FOR I NVESTIGATING P OSSIBLE C RIMINAL/W ILLFUL V IOLATIONS ........................ 4-31C. W ILLFUL V IOLATIONS R ELATED TO A F ATALITY .......................................................................... 4-32 VII. REPEATED VIOLATIONS. ...................................................................... 4-32A.F EDERAL AND S TATE P LAN V IOLATIONS. ........................................................................................4-32B.I DENTICAL S TANDARDS. .......................................................................................................................4-32C.D IFFERENT S TANDARDS. .......................................................................................................................4-33D.O BTAINING I NSPECTION H ISTORY. .....................................................................................................4-33E.T IME L IMITATIONS..................................................................................................................................4-34F.R EPEATED V. F AILURE TO A BATE....................................................................................................... 4-34G. A REA D IRECTOR R ESPONSIBILITIES. .............................................................................. 4-35 VIII. DE MINIMIS CONDITIONS. ................................................................... 4-36A.C RITERIA ................................................................................................................................................... 4-36B.P ROFESSIONAL J UDGMENT. ..................................................................................................................4-37C. A REA D IRECTOR R ESPONSIBILITIES. .............................................................................. 4-37 IX. CITING IN THE ALTERNATIVE ............................................................ 4-37 X. COMBINING AND GROUPING VIOLATIONS. ................................... 4-37A.C OMBINING. ..............................................................................................................................................4-37B.G ROUPING. ................................................................................................................................................4-38C. W HEN N OT TO G ROUP OR C OMBINE. ................................................................................................4-38 XI. HEALTH STANDARD VIOLATIONS ....................................................... 4-39A.C ITATION OF V ENTILATION S TANDARDS ......................................................................................... 4-39B.V IOLATIONS OF THE N OISE S TANDARD. ...........................................................................................4-40 XII. VIOLATIONS OF THE RESPIRATORY PROTECTION STANDARD(§1910.134). ....................................................................................................... XIII. VIOLATIONS OF AIR CONTAMINANT STANDARDS (§1910.1000) ... 4-43 4-43A.R EQUIREMENTS UNDER THE STANDARD: .................................................................................................. 4-43B.C LASSIFICATION OF V IOLATIONS OF A IR C ONTAMINANT S TANDARDS. ......................................... 4-43 XIV. CITING IMPROPER PERSONAL HYGIENE PRACTICES. ................... 4-45A.I NGESTION H AZARDS. .................................................................................................................................... 4-45B.A BSORPTION H AZARDS. ................................................................................................................................ 4-46C.W IPE S AMPLING. ............................................................................................................................................. 4-46D.C ITATION P OLICY ............................................................................................................................................ 4-46 XV. BIOLOGICAL MONITORING. ...................................................................... 4-47CHAPTER 5CASE FILE PREPARATION AND DOCUMENTATIONI.INTRODUCTION ............................................................................................... 5-1 II.INSPECTION CONDUCTED, CITATIONS BEING ISSUED. .................... 5-1A.OSHA-1 ................................................................................................................................... 5-1B.OSHA-1A. ............................................................................................................................... 5-1C. OSHA-1B. ................................................................................................................................ 5-2 III.INSPECTION CONDUCTED BUT NO CITATIONS ISSUED .................... 5-5 IV.NO INSPECTION ............................................................................................... 5-5 V. HEALTH INSPECTIONS. ................................................................................. 5-6A.D OCUMENT P OTENTIAL E XPOSURE. ............................................................................................................... 5-6B.E MPLOYER’S O CCUPATIONAL S AFETY AND H EALTH S YSTEM. ............................................................. 5-6 VI. AFFIRMATIVE DEFENSES............................................................................. 5-8A.B URDEN OF P ROOF. .............................................................................................................................................. 5-8B.E XPLANATIONS. ..................................................................................................................................................... 5-8 VII. INTERVIEW STATEMENTS. ........................................................................ 5-10A.G ENERALLY. ......................................................................................................................................................... 5-10B.CSHO S SHALL OBTAIN WRITTEN STATEMENTS WHEN: .......................................................................... 5-10C.L ANGUAGE AND W ORDING OF S TATEMENT. ............................................................................................. 5-11D.R EFUSAL TO S IGN S TATEMENT ...................................................................................................................... 5-11E.V IDEO AND A UDIOTAPED S TATEMENTS. ..................................................................................................... 5-11F.A DMINISTRATIVE D EPOSITIONS. .............................................................................................5-11 VIII. PAPERWORK AND WRITTEN PROGRAM REQUIREMENTS. .......... 5-12 IX.GUIDELINES FOR CASE FILE DOCUMENTATION FOR USE WITH VIDEOTAPES AND AUDIOTAPES .............................................................. 5-12 X.CASE FILE ACTIVITY DIARY SHEET. ..................................................... 5-12 XI. CITATIONS. ..................................................................................................... 5-12A.S TATUTE OF L IMITATIONS. .............................................................................................................................. 5-13B.I SSUING C ITATIONS. ........................................................................................................................................... 5-13C.A MENDING/W ITHDRAWING C ITATIONS AND N OTIFICATION OF P ENALTIES. .................................. 5-13D.P ROCEDURES FOR A MENDING OR W ITHDRAWING C ITATIONS ............................................................ 5-14 XII. INSPECTION RECORDS. ............................................................................... 5-15A.G ENERALLY. ......................................................................................................................................................... 5-15B.R ELEASE OF I NSPECTION I NFORMATION ..................................................................................................... 5-15C. C LASSIFIED AND T RADE S ECRET I NFORMATION ...................................................................................... 5-16。
rprop算法原理

rprop算法原理
RPROP算法,全称为"Resilient Propagation Algorithm",是一种用于神经网络的优化算法。
其基本原理是:首先为各权重变化赋一个初始值,设定权重变化加速因子与减速因子。
在网络前馈迭代中,当连续误差梯度符号不变时,采用加速策略,加快训练速度;当连续误差梯度符号变化时,采用减速策略,以期稳定收敛。
网络结合当前误差梯度符号与变化步长实现BP (反向传播),同时,为了避免网络学习发生振荡或下溢,算法要求设定权重变化的上下限。
以上信息仅供参考,建议查阅关于RPROP算法的书籍或咨询专业人士获取更准确的信息。
聚丙烯基础知识

第一章 聚丙烯的结构和性质第一节 聚丙烯的结构一、分子结构由丙烯聚合的高分子化合物,聚合反应中链增长的方式,即下一个单体连接到分子链上的形式决定了分子链的形状和甲基的空间排列,决定其立构规整度,进而决定其结晶结构、结晶度、密度及相关的物理机械性能。
1.等规聚丙烯(iPP )、间规聚丙烯(sPP )和无规聚丙烯(aPP )聚丙烯立构中心的空间构型有D 型和L 型两种:如果此立构中心D 型或L 型单独相连,就构成iPP :如果立构中心D 型和L 型交替连接,就构成sPP :如果立构中心D 型和L 型无规则地连接,甲基无规则地分布在主链平面两侧,就构成了aPP :或等规聚丙烯是高结晶的高立体定向性的热塑性树脂,结晶度60%~70%,等规度>90%,吸水率0.01%~0.03%,有高强度、高刚度、高耐磨性、高介电性,其缺点是不耐低温冲击,不耐气候,静电高。
间规聚丙烯结晶点较低(与等规聚丙烯相比),为20%~30%,密度低(0.7~0.8g/cm3),熔点低(125~148℃),分子量分布较窄(M w/M v=1.7~2.6),弯曲模量低,冲击强度高,最为优异的是透明性、热密封性和耐辐射性,但加工性较差(以茂金属催化剂聚合可得间规度大于80%的间规聚丙烯)。
无规聚丙烯分子量小,一般为3000至几万,结构不规整,缺乏内聚力,在室温下是非结晶、微带粒性的蜡状固体。
2.无规共聚物、抗冲共聚物和多元共聚物丙烯-乙烯无规共聚物:使丙烯和乙烯的混合物聚合,所得聚合物的主链上无规则地分布着丙烯和乙烯链段,乙烯含量一般为1%~4%(质量分数),乙烯抑制丙烯结晶,使无规共聚物结晶度下降,熔点、玻璃化温度、脆化点降低,结晶速度变慢,材料变软,透明度提高,韧性、耐寒性、冲击强度均较均聚物提高,主要用于高抗冲击性和韧性制品。
丙烯-乙烯嵌段共聚物:在单一的丙烯聚合后除去未反应的丙烯,再与乙烯聚合所得产物,通常嵌段共聚体中乙烯含量为5%~20%(质量分数)。
3GPP 5G基站(BS)R16版本一致性测试英文原版(3GPP TS 38.141-1)

4.2.2
BS type 1-H.................................................................................................................................................. 26
4.3
Base station classes............................................................................................................................................27
1 Scope.......................................................................................................................................................13
All rights reserved. UMTS™ is a Trade Mark of ETSI registered for the benefit of its members 3GPP™ is a Trade Mark of ETSI registered for the benefit of its Members and of the 3GPP Organizational Partners LTE™ is a Trade Mark of ETSI registered for the benefit of its Members and of the 3GPP Organizational Partners GSM® and the GSM logo are registered and owned by the GSM Association
- 1、下载文档前请自行甄别文档内容的完整性,平台不提供额外的编辑、内容补充、找答案等附加服务。
- 2、"仅部分预览"的文档,不可在线预览部分如存在完整性等问题,可反馈申请退款(可完整预览的文档不适用该条件!)。
- 3、如文档侵犯您的权益,请联系客服反馈,我们会尽快为您处理(人工客服工作时间:9:00-18:30)。
Flame retardant mechanism of an efficientflame-retardant polymeric synergist with ammonium polyphosphate for polypropyleneZhao-Zan Xu,Jian-Qian Huang*,Ming-Jun Chen,Yi Tan,Yu-Zhong Wang*Center for Degradable and Flame-Retardant Polymeric Materials,National Engineering Laboratory of Eco-Friendly Polymeric Materials(Sichuan),State Key Laboratory of Polymer Materials Engineering,College of Chemistry,Sichuan University,Chengdu610064,Chinaa r t i c l e i n f oArticle history:Received4April2013 Received in revised form30May2013Accepted8July2013Available online18July2013Keywords:Flame retardancy PolypropyleneIntumescenceSynergism a b s t r a c tAn efficientflame retardant polymeric synergist poly[N4-bis(ethylenediamino)-phenyl phosphonic-N2, N6-bis(ethylenediamino)-1,3,5-triazine-N-phenyl phosphonate](PTPA)was designed and synthesized from cyanuric chloride,ethylenediamine and phenylphosphonic dichloride.It was characterized by Fourier Transform Infrared(FTIR),1H NMR and31P NMR,Elemental Analysis(EA)and Inductively Coupled Plasma Atomic Emission Spectrometry(ICP-AES).Combined with ammonium polyphosphate (APP),a new intumescentflame retardant(IFR)was obtained.Theflammability behaviors of poly-propylene(PP)/IFR system were investigated by limiting oxygen index(LOI),vertical burning test(UL-94) and cone calorimetry.With25wt%of IFR(APP:PTPA¼2:1),the PP/IFR system could achieve a LOI value of34.0%and UL-94V-0rating,and the heat release rate(HRR),peak heat release rate(PHRR),total heat release(THR)and smoke production rate(SPR)were considerably reduced,especially HRR and SPR were decreased by85%and79%,respectively.The results indicate that there is an excellent synergism between APP and PTPA,which endows PP with both goodflame retardancy and good smoke suppression. Furthermore,the thermal degradation mechanism of IFR and theflame-retardant mechanism of PP/IFR system were investigated by thermogravimetric analysis(TGA),FT-IR,TG-FTIR and scanning electron microscope(SEM).The study on theflame-retardant mechanism of IFR indicated that a structure con-taining e CN was formed due to the reaction between APP and PTPA.Ó2013Elsevier Ltd.All rights reserved.1.IntroductionPolypropylene(PP)is widely used in apparel,floor covering, upholstery,medical,geotextile and automobile due to its low cost, light weight,good mechanical properties and excellent resistant to many chemicals.However,PP is a highly combustible material, which restricts its application in manyfields.Therefore,it is essential to endow PP with goodflame retardancy[1].In the research for environmentally friendlyflame retardants for PP,intumescentflame retardants(IFR)have attracted considerable attention[2e19].However,there are some shortcomings with traditional IFR,such as not high enoughflame-retardant efficiency, low thermal stability and low water resistance[20].In the efforts to improve theflame-retardant efficiency of IFR system,the synthesis and application of the phosphorus-nitrogen containing intumes-centflame retardants become a trend for the synergistic effect between phosphorus and nitrogen.Among them,triazine and its derivatives attracted the interest of scientists due to its high ther-mal stability and structure of tertiary nitrogen[4,17,21e24].Cya-nuric chloride is an excellent raw material to design and synthesize differentflame retardants because of its high selectivity[4,21,24]. Some phosphorus-nitrogen containing IFR systems with low mo-lecular weights have been synthesized from cyanuric chloride [25,26].They might endow polymer withflame retardancy alone or together with APP.Literature indicated that some reactive phos-phonic amides were used as the curing agents for epoxy resins and showed good thermal stability and charring ability[27,28].It was shown that phosphorus oxynitride structure was helpful for the formation of stable char layer[29].However,the research of the compound containing both triazine ring and phosphorus oxynitride structure is not reported. To further improve theflame-retardant efficiency of IFR,it deserves more efforts to design and prepare new IFRs.In the present article, we mainly aim to design and synthesize a novel polymericflame retardant named PTPA containing triazine ring,benzene ring and phosphorus oxynitride structure,which might exhibit better ther-mal stability and charring bining this polymericflame*Corresponding authors.Tel.:þ862885410755;fax:þ862885410259.E-mail addresses:aaa_16@(J.-Q.Huang),yzwang@ (Y.-Z.Wang).Contents lists available at ScienceDirectPolymer Degradation and Stability journal homepage:w ww.elsevi /locate/polydegstab0141-3910/$e see front matterÓ2013Elsevier Ltd.All rights reserved./10.1016/j.polymdegradstab.2013.07.010Polymer Degradation and Stability98(2013)2011e2020retardant with APP,a new high-efficient IFR for PP is obtained.The structure of PTPA is characterized by FT-IR,1H NMR,31P NMR,EA and ICP-AES.Theflame-retardant properties,thermal degradation mechanism andflame-retardant mechanism are investigated in detail.2.Experimental2.1.MaterialsCyanuric chloride was purchased from the Yingkou Sanzheng Organic Chemical Industry Co.,Ltd.,China.Ethylenediamine,so-dium hydroxide and chloroform were supplied by Changzheng Chemical Reagent Co.,China.Phenylphosphonic dichloride was provided by Weili Flame Retardant Chemicals Industry Co.,Ltd (Chengdu,China).Ammonium polyphosphate(APP)was supplied by Sichuan Shifang Chuanhong Phosphorus Chemical Co.,Ltd. China.Polypropylene(PP)resin(T30S)used in this work was pur-chased from Lanzhou Petroleum Chemical Co.,China.2.2.Preparation of poly[N4-bis(ethylenediamino)-phenyl phosphonic-N2,N6-bis(ethylenediamino)-1,3,5-triazine-N-phenyl phosphonate](PTPA)The synthesis route of PTPA is shown in Scheme1.N,N0-bis(2-aminoethyl)-phenyl phosphorodiamidate(BPPA) was synthesized according to literature[28].Ethylenediamine (126g)and chloroform(400ml)were added in a1000ml four-necked reaction vessel provided with a stirrer,a thermometer, and a constant pressure dropping funnel,followed by simulta-neously dropwise adding a solution of phenylphosphonic dichlor-ide(117g)dissolved in chloroform while keeping the temperature atÀ5 C to5 C with stirring.After the completion of the dropwise addition,the mixture was further agitated at the same temperature for6h,thenfiltered to remove ethylenediamine hydrochloride and got the solution of BPPA which would be used immediately in the following reaction.Cyanuric chloride(92g)and chloroform(500ml)were added into a1000ml four-necked reaction vessel with a stirrer,a ther-mometer and two constant pressure dropping funnels,followed by simultaneous dropwise addition of half of the BPPA solution and an aqueous solution of sodium hydroxide(20g),while keeping the temperature atÀ5 C to5 C with stirring.After completion of the dropwise addition,the mixture was further agitated at the same temperature for6h,followed by heating it up to room temperature, dropwise adding the other half of the BPPA solution and sodium hydroxide(20g)dissolved in water.After the completion of the reactant addition,the mixture was agitated under reflux for8h at 61 C.The intermediate wasfiltered and dispersed in the aqueous solution of BPPA and keeping pH at6to8by adding sodium hy-droxide for8h at100 C.The mixture was then cooled down to room temperature,followed byfiltration,washing the product with water,drying it to a constant weight in vacuum at80 C,and150g of yellowish solid was obtained.Its solubility in100g water at70 C was0.09Æ0.01g.2.3.Preparation offlame-retardant PP samplesAll samples with different compositions of PP/flame retardants (FR)were prepared in a parallel co-rotating twin-screw extruder with a length/diameter ratio of40and a screw diameter of25mm. The PP/FR samples were extruded at190 C at the screw speed of 80rpm.Then,the specimens for LOI and UL-94tests were compression-molded by means of a vulcanizing press at200 C under10MPa for3min to obtain3.2mm thick plaques.Finally,the compressed sheets were cut into standard testing bars.2.4.CharacterizationThe structures of BPPA and PTPA were characterized by NMR(1H NMR,31P NMR,Bruker FT-80A NMR),FT-IR(Nicolet FTIR170SX infrared spectrophotometer,KBr powder)and Elemental Analysis (EA).The phosphorus content of PTPA was analyzed using an IRIS ADV Inductively Coupled Plasma-Atomic Emission Spectrometry (ICP-AES).Thermogravimetry(TG)was carried out on an SDT Q600 thermal analyzer in a60ml/minflowing N2at a heating rate of 10 C/min.Theflame retardancy and burning behaviors were determined by LOI test(JF-3oxygen index meter,Jiangning,China; using sheet dimension of130mmÂ6.5mmÂ3mm according to ASTM D2863-97),UL-94measurement(CZF-2-type,Jiangning, China;using sheet dimension of130mmÂ13mmÂ3mm ac-cording to ASTM D3801)and cone calorimetry test(FTT cone calorimeter;square specimens,100mmÂ100mmÂ3mm were irradiated at a heatflux of50kW/m2according to ISO5660stan-dard procedures).3.Results and discussion3.1.Characterization of BPPA and PTPAFig.1shows the FT-IR spectra of BPPA(a)and PTPA(b).For the spectrum of BPPA,the absorptions of N e H(primary)at3440andScheme1.The synthesis route of PTPA.Z.-Z.Xu et al./Polymer Degradation and Stability98(2013)2011e202020121652cm À1,N e H (secondary)at 3264cm À1,phenyl (1600,1557and 1517cm À1),P-phenyl bond (1431cm À1)and P e N e C (1384,1044and 740cm À1)are in keeping with literature [28].For PTPA,the absorptions at 3416and 3256cm À1(N e H in e NH 2and e NH e group),1227cm À1(P ]O),2928and 2869cm À1(C e H bond in e CH 2e CH 2e )and 1421cm À1(P e Ph bond)are observed.The ab-sorptions of 1580cm À1(C ]N bond of triazine ring),1620and 1506cm À1(C ]C bond of benzene ring)and the appearance of 1336cm À1(C triazine e NH e )indicate the successful reaction between BPPA and cyanuric chloride.Fig.2shows the 1H (a)and 31P (b)NMR spectra of BPPA.The signals at 7.66e 7.39ppm correspond to five hydrogen protons of benzene ring and signals at 2.78e 2.67ppm corresponds to eight hydrogen protons of two e CH 2e CH 2e moieties [28].The peak area ratio 1:1.63is in keeping with the calculated value 1:1.60.No resonance of e NH e or e NH 2proton appears because of the addi-tion of D 2O.The signal of phosphate is observed at 17.49ppm.On the basis of the above results,it can be concluded that BPPA has been synthesized successfully.Fig.3shows the 1H NMR spectrum (600MHz,CF 3COOD)of PTPA.The multiplet between 7.52and 7.92ppm corresponds to the hydrogen protons of benzene ring.The signals at 3.87e 4.08ppm correspond to the hydrogen protons of e CH 2e in middle repeating units [28].The peaks at 3.60and 3.64ppm correspond to the hydrogen protons of e CH 2e in end group.With the peak area ratioof hydrogen protons of e CH 2e in end group and hydrogen protons of e CH 2e in middle repeating units,the n value we calculated is 22and the number-average molecular weight of PTPA is 1.26Â104g/mol.To further con firm the structure of the product,ICP-AES was used to measure the actual phosphorus content,and the contents of nitrogen,carbon,and hydrogen were measured by EA.Table 1shows the EA and ICP-AES data of PTPA.The actual content of carbon,hydrogen,nitrogen,and phosphorus is mainly in accord with their calculated content respectively.All the results above indicate that the object product has been synthesized successfully.3.2.Flammability of PP/IFR systemsPTPA was mixed with APP and PP to get a new intumescent flame-retardant PP.The results of the limiting oxygen index (LOI)and vertical burning test (UL-94)were given in Table 2.When the two components (APP and PTPA)act separately,the flame retard-ancy is not so good.However,when the additive amount of IFR which combines APP with PTPA (2:1by weight)is 25wt%,the LOI value of PP/APP/PTPA is increased to as high as 34.0%and the UL-94rating is V-0,showing an excellent synergy between APP and PTPA.When the additive amount of IFR (APP/PTPA ¼3:1)is decreased to 18wt%,the LOI value of PP/APP/PTPA is decreased to 32.1%and the UL-94rating is V-0,showing a high flame-retardant ef ficiency.The cone calorimeter is one of the most effective bench-scale methods to study the flammability of materials.Some of the flame-retardant PP samples were studied by cone calorimeter.All samples were repeated three times and the deviation of their data was within Æ10%.Time to ignition (TTI),Heat release rate (HRR),especially the peak of HRR (PHRR),total heat release (THR)and smoke production rate (SPR)are important parameters for evalu-ating flame retardancy and flammability of polymeric materials.Figs.4and 5and Table 3show the cone calorimetry tests data of pure PP and PP/IFR systems at an external heat flux of 50kW/m 2.Fig.4and Table 3show that TTI is shortened after addition of flame retardant.That is because APP,PTPA and IFR degrades at lower temperature than PP.HRR value of pure PP increases very fast after ignition,and a sharp HRR peak (809kW/m 2)appears at pared with pure PP,the PHRR is decreased by about a half with adding APP or PTPA separately.However,combining PTPA with APP together to form IFR,the PHRR of PP/IFR is decreased to 121kW/m 2at 330s,indicating that the flammability of the PP/IFR systems is obviously restrained and the rate of fire spreading isdecreasedFig.2.1H (a)and31P (b)NMR spectra ofBPPA.Fig.1.FT-IR spectra of BPPA (a)and PTPA (b).Z.-Z.Xu et al./Polymer Degradation and Stability 98(2013)2011e 20202013largely.It is noticeable that for PP/IFR,HRR increases very fast after ignition (up to 92kW/m 2),then dramatically decreased and grad-ually raised up again till the maximum.This phenomenon is closely related with the fast formation of compact char layer.When poly-propylene burns fast releasing a lot of heat,a compact intumescent char layer forms in a short time with the degradation of APP and PTPA.The char layer covers the sample and prevents the flammable gaseous products of PP to permeate.The flammable volatiles can almost only escape from the edge of char layer and burns slowly as shown in Fig.10f.Thus the release rate decreases.But due to the continuous thermal radiation of weak fire,PP under char layer degrades and produces lots of flammable volatiles.The gases escape from the edge of char layer and burn fast.It comes to be the main burning stage.Consequently the heat release rate increases and gradually rises up to its second maximum.On the other hand,comparing the time to PHRR (T PHRR )and PHRR of pure PP with flame-retardant PP,adding APP or PTPA separately cannot form compact char layer in time to inhibit the fire.As a result,the heat release rate rises up directly to the maximum.We can conclude that the speed of char layer formation and the compactness of char layer have a strong impact on the reduction of the heat release rate and the flame retardancy.From Fig.4and Table 3,it can be seen that the value of THR of PP/IFR is reduced considerably,and the total burning time is also obviously prolonged compared with that of pure PP.Fig.5(a)and Table 3indicate that the smoke emission is retarded and delayed during the whole emission process with PP/APP/PTPA system.The curves of mass loss rate (MLR)against combustion time of pure PP and PP/IFR are shown in Fig.5(b).It can be seen that the IFR composed of APP and PTPA could effectively prohibit the decomposition of PP and form an amount of char on the surface.The barrier effect of char layer reduces the smokeproduction rate and the heat release rate.The mass loss behavior of the composite is in accord with the heat release behavior and the smoke emission behavior.From the data above,it can be demonstrated that the heat transfer and flammable volatiles transfer between the flame and the polymer are decreased greatly.Thus the flame retardancy of the intumescent flame-retardant PP system is improved considerably with IFR composed of PTPA and APP.3.3.Flame-retardant mechanism3.3.1.Thermal degradation of flame retardantsFig.6shows TGA (a)and DTG (b)curves of PTPA,APP,IFR (APP:PTPA ¼2:1)and IFR calculation in N 2,respectively.The data of thermal degradation are shown in Table 4.The TGA and DTG curves show that the initial decomposition temperature of PTPA is 269 C based on 5wt%mass loss.It can be seen that PTPA undergoes two stages of thermal degradation process at 269e 359 C and 359e 700 C,respectively.The weight loss is 15wt%for the first stage and 47wt%for the second stage leaving 33.16wt %of char residue at 700 C.It can be seen that there are three degradation steps for IFR composed of APP and PTPA at 285e 310 C,310e 450 C and 450eFig.3.1H NMR spectrum (600MHz,CF 3COOD)of PTPA.Table 1EA and ICP-AES data of PTPA.Content (wt %)CH N P Calculated value 49.14 6.1628.6510.56Actual value42.425.9329.858.04Table 2The formulation and the flame properties of PP/IFR system.Sample PP/%APP/%PTPA/%LOI/%UL-9411000017.6No rating 27525020.6No rating 37502520.6No rating 4758.316.726.1No rating 57512.512.532.5V-067516.78.334.0V-077518.75 6.2532.5V-087520 5.033.0V-198013.33 6.6733.0V-010829.09.028.5No rating 118212 6.032.0No rating 128213.5 4.532.1V-0138412428.5No rating 148412.83.228.5No ratingZ.-Z.Xu et al./Polymer Degradation and Stability 98(2013)2011e 20202014700 C,respectively.The mass loss rate of IFR is much higher than the calculated value in the temperature range from 337 C to 433 C,but it is lower than the calculated value in the temperature range from 433 C to 700 C.The second maximum weight loss rate (À3.8%/min)is much quicker than the calculated value (À1.8%/min).However,the first and third maximum weight loss rates are smaller than the calculated values.It can be inferred that there is a reaction between the decomposition products of PTPA and APP which not only promotes their degradation and volatilization of their products,but also promotes the formation of more thermal stable char residue at lower temperature.Therefore,we can see that the mass loss rate of IFR is small at temperature above 450 C and the amount of IFR residue is more than the calculated value.Fig.7(a)shows the FT-IR spectra of volatile products of PTPA at different temperatures in N 2.During the first stage (from 269 C to 359 C),the gas released is ammonia whose absorptions are observed at 964and 930cm À1and the volume of ammonia is increased with the temperature increased.During the second stage (from 359 C to 604 C),the gas released is composed of ammonia,ole fin compounds (3080,1648and 1470cm À1),aromatic compounds (3058cm À1),nitrile com-pounds (2251and 2285cm À1),vaporing phosphonates (1244cm À1)and volatiles with P e NH e bond (3333,1391,1304,1220and 713cm À1).The gaseous production gradually increases with the increase of temperature,maximizing and then going down.During the third stage of degradation (from 604 C to 700 C),the unstable partial of the char residue is further decom-posed.Only non flammable gas composed of nitrile and vaporing compounds with P ]O bond and P e NH e bond is observed.Fig.7(b)shows the FT-IR spectra of condensed products of PTPA at different temperatures in N 2.At 25 C,the absorptions of original PTPA are observed at 3416and 3256cm À1(N e H in e NH 2and e NH e group),1269cm À1(P ]O),2928and 2869cm À1(C e H bond in e CH 2e CH 2e ),1580cm À1(C ]N bond of triazine ring),1620and 1506cm À1(C ]C of benzene ring)and 1336cm À1(C triazine e NH e bond).With the increase of temperature,the absorption at 3416cm À1becomes gradually weaker,meaning the chain scission of e NH 2,P e NH e and C e NH e .The same is observed with the ab-sorptions at 2928and 2869cm À1.Also,a new absorption at 2168cm À1(e CN)appears obviously in the spectrum of residue at 435 C (the second weight loss step)and disappears in the spec-trum of residue at 700 C,which means the new nitrile compound is generated during decomposition and then decomposed at higher temperature.The absorptions at 1620cm À1,1421cm À1,897cm À1become wider and stronger at 435 C,suggesting that the new ar-omatic compound and the new compound with P e N bond form during the combustion.Fig.8(a)shows the FT-IR spectra of volatile products of IFR at different temperatures in N 2obtained from TG-FTIR technology.IFR is the mixture of APP and PTPA with the weight ratio of 2:1.DuringFig.4.HRR (a)and THR (b)plots of pure PP and PP/IFR systems obtained from conecalorimetry.Fig.5.SPR (a)and Mass Loss (b)plots of pure PP and PP/IFR systems obtained from cone calorimetry.Z.-Z.Xu et al./Polymer Degradation and Stability 98(2013)2011e 20202015the first stage,ammonia from decomposition of PTPA and APP is evolved.During the second stage of weight loss from 337 C to 543 C,gaseous product of thermal decomposition of IFR is the mixture of carbon dioxide (2318and 2357cm À1),ammonia and a little amount of aromatic hydrocarbons (3060cm À1).At the tem-perature above 543 C,char residue further degrades and vaporing compound with P ]O bond and P e NH e bond evolves.To further investigate the thermal degradation behavior,the char residues of PTPA and IFR (APP:PTPA ¼2:1)burned at different temperatures are investigated by FT-IR.Fig.8(b)shows the FT-IR spectra of condensed products of IFR at different temperature in N 2.The FTIR spectrum of IFR at 25 C in Fig.8(b)shows that typical absorptions of APP are evident at 1252cm À1(P ]O)and 883cm À1(P e O e P),whereas those of PTPA are observed at 1632cm À1(C ]C of benzene ring)and 3000e 2800cm À1(e CH 2e ).With the increase of temperature,the ab-sorptions of e CH 2e groups at 3000e 2800cm À1,e NH 2at 3202cm À1and aromatic hydrocarbons (3050cm À1)are signi fi-cantly decreased,whereas there is a new absorption appearing at 2137cm À1(e CN).The exact association of these absorptions to speci fic bonds (P e N or P e O)is not easy by FTIR because of broad and overlapping peaks [30].Moreover,the absorptions at 3430and1655cm À1and the broad tail at 2800e 2400cm À1could indicate the presence of polyphosphoric acid [29].Based on the results above,possible decomposition mechanism of PTPA and IFR is shown in Scheme 2.The phosphorus oxynitride structure in PTPA is stable to high temperature.On one hand,the polymerization or aromatization of carbon e carbon double bonds formed from the degradation of PTPA might promote to produce stable char residue [29].On the other hand,the P e O e P bonds in the polyphosphate chain are broken down and probably form stable cross-linking structures.An alternative route for polyphosphate chain scission is due to the reaction between the decomposition products of PTPA and APP which involves the formation of non flammable vaporing compounds and some stable compounds containing P e N bond which is shown in Scheme 2.3.3.2.Flame-retardant mechanism of PP/IFR systemFig.9and Table 5present the TG (a)and DTG (b)curves and data of the flame-retardant PP with 25%PTPA,25%APP and 25%IFR,respectively.It can be seen that pure PP begins to degrade at 380.6 C and the maximum decomposition temperature is at 445.8 C with almost no char residue left at 700 C.However,the initial decomposition temperature of PP/IFR is 355.8 C which is related with the decomposition and cross-linking reactions,form-ing the char which can protect the matrix from heat and decomposition.When the temperature is increased,PP with IFR is further decomposed,further cross-linked and char is formed.The char residue of flame-retardant PP is much more than that of pure PP,PP/PTPA and PP/APP at 700 C.The maximum weight loss rate is smaller and appears at higher temperature than that of pure PP,which means that the matrix is protected during burning.Table 3Data obtained from cone calorimetry of pure PP and PP/IFR system.SampleTTI (s)PHRR (kW/m 2)T PHRR (s)THR (MJ/m 2)SPR (m 2/s)Residue (%)PP20809130960.09958.975%PP-25%APP 1139765870.064621.575%PP-25%PTPA 1252980880.10709.875%PP-25%IFR11121330810.021317.1Fig.6.TGA (a)and DTG (b)curves of PTPA,APP,IFR and IFR calculation in N 2.Table 4Thermogravimetric data of flame retardants in N 2.Samples T onset a ( C)T max1b ( C)R max1c (%min À1)T max2( C)R max2(%min À1)T max3( C)R max3(%min À1)Char residues (%)at 700 C PTPA 269288À1.4435À4.4No 33.16APP 297315À1.9353À1.3572À2.550.60IFR285296À1.5404À3.8513À0.947.13IFR-calculation286315À1.7435À1.8573À1.944.86a T onset :the initial temperature at 5wt%mass loss.b T max :the temperature at the maximum mass loss rate.cR max :the maximum mass loss rate value.Z.-Z.Xu et al./Polymer Degradation and Stability 98(2013)2011e 20202016Fig.10shows the digital photographs of residual char after cone calorimeter test for different systems.The thermal insulation and physical barrier to mass transfer through the intumescent char was previously shown to be of paramount importance in the fire retardance mechanism [31].The compact and firm carbon layer obviously reduces heat release rate,weight loss rate and smoke production release rate.We can see that the residual char of sample 75%PP-25%APP (Fig.10b)is continuous with lots of holes.The char surface of sample 75%PP-25%PTPA (Fig.10c)is fragmented by cracks orholes.Fig.7.FT-IR spectra of volatile products (a)and condensed products (b)of PTPA inN2.Fig.8.FT-IR spectra of volatile products (a)and condensed products (b)of IFR in N 2.Scheme 2.Possible pyrolysis mechanism of PTPA and IFR.Z.-Z.Xu et al./Polymer Degradation and Stability 98(2013)2011e 20202017Both of them cannot segregate oxygen and combustible gases effectively.The carbon layer of 75%PP-25%IFR (APP:PTPA ¼2:1)(Fig.10d)is continuous,compact and thick.The thick carbon layer means the intumescent ratio is very high,suggesting that the decomposed gases can hardly permeate through the char layer (Fig.10e).The combustible gases can only escape from the loweredge of char layer and keep burning very slowly just like showing in Fig.10f.In order to clarify the morphology of the char formed after combustion,the surfaces of char residues after cone calorimetry test for different systems were investigated by SEM,as shown in Fig.11.The char residue of PP/PTPA (Fig.11a-1and a-2)is coralloid network structure with lots of cavities.That is because PTPA is rich in carbon (charring agent)and nitrogen (blowing agent),but poor in phosphorus (acid source).Thus,the char layer becomes frag-mented when plenty of decomposed gases easily permeate through the char layer.The char residue of PP/APP (Fig.11b-1and b-2)is continuous with some holes and spherical shape tubers in the surface because the cross-linked polyphosphoric acid formed on heating could provide a stable softened glassy coating on the sur-face of the polymer,but it is not firm enough.It can be permeated through by decomposed gases,thus holes are formed.TheFig.9.TG (a)and DTG (b)curves of the flame-retardant PP.Table 5Thermal degradation data for PP with 25%PTPA,25%APP and 25%IFR in N 2.SampleT onset a ( C)T max b ( C)R max c (%min À1)The char residues (%)at 700 C Pure PP 380.6445.8À22.380.1875%PP-25%PTPA 341.9450.3À14.758.7175%PP-25%APP 366.0461.6À16.7414.9775%PP-25%IFR 355.8464.5À14.4912.24a T onset :the initial temperature at 5wt%mass loss.b T max :the temperature at the maximum mass loss rate.cR max :the maximum mass loss ratevalue.Fig.10.The digital photographs of residual char after cone calorimeter test for different systems,a:PP,b:75%PP-25%APP,c:75%PP-25%PTPA,d:75%PP-25%IFR (APP:PTPA ¼2:1),e:75%PP-25%IFR,f:the burning sample of 75%PP-25%IFR.Z.-Z.Xu et al./Polymer Degradation and Stability 98(2013)2011e 20202018。