TWI687443B - 吸水性樹脂及吸收性物品 - Google Patents
吸水性樹脂及吸收性物品 Download PDFInfo
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- TWI687443B TWI687443B TW107136055A TW107136055A TWI687443B TW I687443 B TWI687443 B TW I687443B TW 107136055 A TW107136055 A TW 107136055A TW 107136055 A TW107136055 A TW 107136055A TW I687443 B TWI687443 B TW I687443B
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- Prior art keywords
- water
- absorbent resin
- polymer
- post
- crosslinking agent
- Prior art date
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- 239000002250 absorbent Substances 0.000 title claims abstract description 115
- 229920005989 resin Polymers 0.000 title claims abstract description 103
- 239000011347 resin Substances 0.000 title claims abstract description 103
- 230000002745 absorbent Effects 0.000 title claims abstract description 21
- 239000003431 cross linking reagent Substances 0.000 claims abstract description 79
- 229920000642 polymer Polymers 0.000 claims abstract description 71
- 239000000178 monomer Substances 0.000 claims abstract description 67
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 62
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Abstract
本發明提供回收再生資源之際可容易與再生資源分離之吸水性樹脂、以及具備吸收體之吸收性物品,該吸收體包含該吸水性樹脂。
本發明之吸水性樹脂具有水溶性乙烯性不飽和單體之聚合物已利用後交聯劑交聯之結構。(1)對生理食鹽水之保水能為35g/g以上,(2)在4.14kPa荷重下對生理食鹽水之吸水能為10mL/g以上,(3)初始凝膠黏度為3000mPa・s以上,(4)以凝膠分解指數=B/A表示之凝膠分解指數為0.60以下(惟,A表示初始凝膠黏度(mPa・s),B表示1日後凝膠黏度(mPa・s))。
Description
發明領域
本發明是有關於吸水性樹脂及吸收性物品。
發明背景
吸水性樹脂廣泛使用在紙尿布及生理用品等衛生材料、保水劑及土壤改良劑等農園藝材料、封水劑及防結露劑等工業資材等各種領域中。尤其,吸水性樹脂大量使用在紙尿布、生理用品及可攜式簡易馬桶等衛生材料上。
近年,基於環保的觀點,正嘗試回收已使用過的衛生材料(例如紙尿布)中所含再生資源(例如紙漿)將之再利用。在從衛生材料回收再生資源上,首先必須使再生資源從吸水性樹脂分離。但是,一般而言,吸收水分而變成凝膠狀之吸水性樹脂(以下稱「已使用過之吸水性樹脂」)很難與再生資源分離,因此,要從衛生材料除去已使用過之吸水性樹脂而僅回收再生資源有所困難。
為了解決這種問題,現正檢討將已使用過之吸水性樹脂分解後回收再生資源之方法。例如,專利文獻1及2中,將已使用過之紙尿布予以裁斷後,利用混了聚合物分解劑之水將紙尿布中所含已使用過之吸水性樹脂分解成單體,然後將屬於再生資源之紙漿成分予以分離回收。
先行技術文獻
專利文獻
[專利文獻1]特開2000-084533號公報
[專利文獻2]特開2006-289154號公報
發明概要
發明欲解決之課題
但是,專利文獻1及2中,由於在已使用過之吸水性樹脂之分解上必須要聚合物分解劑,因此不僅再生資源之回收作業繁雜,且還有必須隨時保管聚合物分解劑的問題。
本發明係鑑於上述問題而作成者,目的在於提供一種在回收再生資源時可容易將再生資源分離之吸水性樹脂、及具備了含該吸水性樹脂之吸收體的吸收性物品。
用以解決課題之手段
本發明人等發現,若使用吸水後展現優異自我分解特性之吸水性樹脂,不須依靠聚合物分解劑等外在手段,便可輕易使已使用過之吸水性樹脂與再生資源分離,進而專精研究,結果完成了本發明之吸水性樹脂。
具體而言,本發明人等針對在吸水後具有優異自我分解特性之吸水性樹脂反覆研究。結果發現,水溶性乙烯性不飽和單體之聚合物具有已利用後交聯劑進行交聯之結構之吸水性樹脂中,因為所有特定物性充足,因此可獲得吸水後自我分解特性優異之吸水性樹脂,而完成了本發明。
亦即,本發明包含例如以下項目所記載之發明。
項1.一種吸水性樹脂,具有水溶性乙烯性不飽和單體之聚合物已利用後交聯劑交聯之結構,且
(1)對生理食鹽水之保水能為35g/g以上,
(2)在4.14kPa荷重下對生理食鹽水之吸水能為10mL/g以上,
(3)初始凝膠黏度為3000mPa・s以上,
(4)以下述式(I)表示之凝膠分解指數為0.60以下:
式(I):凝膠分解指數=B/A
(惟,上述式(I)中,A表示初始凝膠黏度(mPa・s),B表示1日後凝膠黏度(mPa・s))。
項2.如項1記載之吸水性樹脂,其中前述聚合物係利用前述水溶性乙烯性不飽和單體之逆相懸浮聚合來形成。
項3.一種吸收性物品,具備吸收體,該吸收體包含項1或2記載之吸水性樹脂。
發明效果
本發明之吸水性樹脂在吸水後自我分解特性優異。因此,在回收包含該吸水性樹脂之再生資源時,再生資源與吸水性樹脂可容易分離,可簡便地進行再生資源之回收。
較佳實施例之詳細說明
以下,針對本發明之實施形態詳細說明。再者,本說明書中,關於「含有」及「包含」之表現,包含了「含有」、「包含」、「實質上由…構成」及「僅由…構成」之概念。
另外,本說明書中,以「~」連結之數值範圍意指包含「~」前後數值作為下限值及上限值之數值範圍。當多數下限值與多數上限值以個別記載時,指選擇任意下限值與任意上限值並以「~」連結,即可獲得特定數值範圍。
1.吸水性樹脂
本發明之吸水性樹脂具有水溶性乙烯性不飽和單體之聚合物已利用後交聯劑交聯之結構。尤其,本發明之吸水性樹脂滿足下述(1)、(2)、(3)及(4)規定之要件。
(1)對生理食鹽水之保水能為35g/g以上。
(2)在4.14kPa荷重下對生理食鹽水之吸水能為10mL/g以上。
(3)初始凝膠黏度為3000mPa・s以上。
(4)以下述式(I)表示之凝膠分解指數為0.60以下:
凝膠分解指數=B/A (I)
(惟,上述式(I)中,A表示初始凝膠黏度(mPa・s),B表示1日後凝膠黏度(mPa・s))。
本發明之吸水性樹脂對生理食鹽水之保水能為35g/g以上(即,保水能下限值為35g/g)。另外,該測定方法詳述於實施例項。
本發明之吸水性樹脂由於對生理食鹽水之保水能為35g/g以上,亦即滿足前述(1)規定之要件,因此吸水性能良好,用於吸收性物品時,可對吸收性物品賦予更優異之吸收性能。從吸水性樹脂可具有更優異之吸水性能的觀點來看,保水能下限值以40g/g為佳,45g/g較佳。
再者,保水能上限值可設在例如100g/g,較佳為90g/g,更佳為80g/g。
本發明之吸水性樹脂,在4.14kPa荷重下對生理食鹽水之吸水能為10mL/g以上(即,在4.14kPa荷重下對生理食鹽水之吸水能下限值為10mL/g)。再者,該測定方法詳述於實施例項。
本發明之吸水性樹脂由於在4.14kPa荷重下對生理食鹽水之吸水能為10mL/g以上,亦即滿足前述(2)規定之要件,因此在荷重下之吸水量充分,容易適用於各種用途上。從吸水性樹脂可具有更優異吸水性能之觀點來看,在4.14kPa荷重下對生理食鹽水之吸水能下限以13mL/g為佳,15mL/g較佳。另外,在4.14kPa荷重下對生理食鹽水之吸水能上限值可設為例如40mL/g,較佳為35mL/g,更佳為30mL/g。
本發明之吸水性樹脂,初始凝膠黏度為3000mPa・s以上(即初始凝膠黏度下限值為3000mPa・s)。再者,該測定方法詳述於實施例項。
本發明之吸水性樹脂初始凝膠黏度為3000mPa・s以上,亦即,滿足前述(3)規定之要件,因此可容易製造出使用感優異且同時具有更優異吸收性能之吸收性物品。基於該觀點,初始凝膠黏度下限值以3500mPa・s為佳,4000mPa・s較佳。
初始凝膠黏度上限值宜設為例如20000mPa・s,以15000mPa・s為佳,較佳為13000mPa・s,更佳為9000mPa・s。
本發明之吸水性樹脂凝膠分解指數為0.60以下(即,凝膠分解指數上限值為0.60)。再者,該測定方法詳述於實施例項。
本發明之吸水性樹脂,由於以前述式(I)表示之凝膠分解指數為0.60以下,亦即滿足前述(4)規定之要件,因此吸水後分解迅速(具有優異之自我分解特性)。包含這樣的吸水性樹脂之吸收性物品等,容易回收及廢棄等利於環保,從這個觀點來看頗佳。前述凝膠分解指數之上限值以0.55為佳,0.50較佳。又,凝膠分解指數下限值為例如0.01,以0.1為佳。
本發明之吸水性樹脂具有水溶性乙烯性不飽和單體之聚合物(以下也僅稱為聚合物)已利用後交聯劑交聯之結構。吸水性樹脂藉著具有已利用後交聯劑交聯之結構,吸水性樹脂表面附近的交聯密度變高。
聚合物之內部具有交聯結構。該內部交聯結構是在水溶性乙烯性不飽和單體聚合之際形成的。該交聯結構之交聯密度,藉著在使水溶性不飽和單體聚合之際使用與上述後交聯劑相同交聯劑或別種交聯劑,而可變高。以下,為了與後交聯劑區別,將可用於聚合物內部交聯之交聯劑稱為內部交聯劑。關於可使用之內部交聯劑之例子,詳述於後述「2.吸水性樹脂之製造方法」項。
水溶性乙烯性不飽和單體可廣泛適用例如一般可用於吸水性樹脂之周知單體。
水溶性乙烯性不飽和單體可舉例如(甲基)丙烯酸(本說明書中組合「丙烯」及「甲基丙烯」表記為「(甲基)丙烯」。以下相同)及其鹽;2-(甲基)丙烯醯胺-2-甲基丙磺酸及其鹽;(甲基)丙烯醯胺、N,N-二甲基(甲基)丙烯醯胺、(甲基)丙烯酸2-羥乙酯、N-羧甲基(甲基)丙烯醯胺、聚乙二醇單(甲基)丙烯酸酯等非離子性單體;N,N-二乙基胺基乙基(甲基)丙烯酸酯、N,N-二乙基胺基丙基(甲基)丙烯酸酯、二乙基胺基丙基(甲基)丙烯醯胺等含胺基不飽和單體及其4級化物等。該等水溶性乙烯性不飽和單體可單獨使用,也可組合2種以上(使之共聚合)來使用。當中,從工業性可容易取得之觀點來看,以(甲基)丙烯酸及其鹽、(甲基)丙烯醯胺、N,N-二甲基丙烯醯胺為佳,(甲基)丙烯酸及其鹽尤佳。
使用丙烯酸及其鹽作為該等水溶性乙烯性不飽和單體的情況下,相對於總水溶性乙烯性不飽和單體,宜使用70~100莫耳%之丙烯酸及其鹽來作為主要水溶性乙烯性不飽和單體。
再者,上述水溶性乙烯性不飽和單體為逆相懸浮聚合時,為了使在烴分散介質中的分散效率提升,可作成水溶液來使用。該水溶液中的上述單體濃度並無特別限定,通常令其為20質量%以上飽和濃度以下即可,以25~70質量%為佳,30~55質量%較佳。
水溶性乙烯性不飽和單體為(甲基)丙烯酸、2-(甲基)丙烯醯胺-2-甲基丙磺酸等具有酸基的情況下,因應需要,可採用其酸基已預先利用鹼性中和劑予以中和之物。這種鹼性中和劑並無特別限定,可舉例如氫氧化鈉、碳酸鈉、碳酸氫鈉、氫氧化鉀、碳酸鉀等鹼金屬鹽;氨等。尤其,為了使中和操作簡便,該等鹼性中和劑可製成水溶液狀態來使用。上述鹼性中和劑可單獨使用,亦可組合2種以上。
關於利用鹼性中和劑所行之水溶性乙烯性不飽和單體之中和度,並無特別限定,而為了提高所得吸水性樹脂之滲透壓來提高吸水性能,且為避免因剩餘鹼性中和劑之存在造成安全性等問題產生,以相對於水溶性乙烯性不飽和單體所具有的全部酸基之中和度而言,通常10~100莫耳%為佳,30~80莫耳%較佳。
後交聯劑的種類方面,可廣泛適用例如可用於吸水性樹脂之公知後交聯劑。
後交聯劑可使用具有2個以上反應性官能基之化合物。後交聯劑之具體例方面可舉乙二醇、丙二醇、1,4-丁二醇、三羥甲基丙烷、丙三醇、聚氧乙二醇、聚氧丙二醇、聚丙三醇等多元醇類;(聚)乙二醇二環氧丙基醚、(聚)丙三醇二環氧丙基醚、(聚)丙三醇三環氧丙基醚、三羥甲基丙烷三環氧丙基醚(聚)丙二醇聚環氧丙基醚、(聚)丙三醇聚環氧丙基醚等聚環氧丙基化合物;表氯醇、氧化溴丙烯、α-甲基表氯醇等鹵化環氧丙基化合物;2,4-二異氰酸甲苯酯、二異氰酸六亞甲酯等異氰酸酯化合物;3-甲基-3-氧呾甲醇、3-乙基-3-氧呾甲醇、3-丁基-3-氧呾甲醇、3-甲基-3-氧呾乙醇、3-乙基-3-氧呾乙醇、3-丁基-3-氧呾乙醇等氧呾化合物;1,2-伸乙基雙唑啉等唑啉化合物;碳酸伸乙酯等碳酸酯化合物;雙[N,N-二(β-羥乙基)]己二醯胺等羥烷基醯胺化合物。該等之中,(聚)乙二醇二環氧丙基醚、(聚)乙二醇三環氧丙基醚、(聚)丙三醇二環氧丙基醚、(聚)丙三醇三環氧丙基醚、(聚)丙二醇聚環氧丙基醚、(聚)丙三醇聚環氧丙基醚等聚環氧丙基化合物尤佳。該等後交聯劑可單獨使用,也可併用2種以上。
本發明之吸水性樹脂的中位粒徑為例如100~1000μm,以200~800μm為佳,較佳為250~600μm,更佳為300~500μm。
本發明之吸水性樹脂的形狀為例如球狀、粉碎狀、顆粒狀、橢圓球狀、鱗片狀、棒狀、塊狀等各種形狀。
本發明之吸水性樹脂對生理食鹽水之吸水速度為例如30秒以上,以50秒以上為佳,較佳為70秒以上。再者,該測定方法將於實施例項中詳述。
2.吸水性樹脂之製造方法
本發明之吸水性樹脂例如可利用包含下述步驟之製造方法來製造:將水溶性乙烯性不飽和單體之聚合物予以聚合之步驟(聚合步驟)、自該聚合物除去水分之步驟(乾燥步驟)、及利用後交聯劑處理該聚合物之步驟(後交聯步驟)。以下,針對本發明之吸水性樹脂之製造方法予以詳述。
(聚合步驟)
聚合步驟係將水溶性乙烯性不飽和單體進行聚合而獲得聚合物之步驟。聚合方法並無特別限定,可舉例如逆相懸浮聚合法、水溶液聚合法、乳化聚合法等。考慮到製造步驟之簡便及容易獲得具優異吸水性能等之吸水性樹脂的觀點,以及可容易滿足前述(1)至(4)所規定之要件的觀點,以採用逆相懸浮聚合法為佳。
所謂逆相懸浮聚合是例如在分散介質中,在分散穩定劑存在下,使難溶性單體懸浮於前述分散介質中進行聚合之方法。
逆相懸浮聚合中可使用的分散介質可使用烴分散介質。烴分散介質可舉例如正己烷、正庚烷、正辛烷、石油英等脂肪族烴;環戊烷、甲基環戊烷、環己烷、甲基環己烷等脂環族烴;以及苯、甲苯、二甲苯等芳香族烴等。該等分散介質當中,因工業性取得容易、品質穩定、進而價廉,故適宜使用正己烷、正庚烷、及環己烷。該等分散介質可單獨使用,也可組合2種以上。分散介質可使用例如以混合溶劑而為人所知的Exxsol Heptane(Exxon Mobil Co.製:庚烷及異構物之烴)或Nappar6(Exxon Mobil Co.製:環己烷及異構物之烴)等。
逆相懸浮聚合中可使用的水溶性乙烯性不飽和單體與前述「1.吸水性樹脂」項中已說明之水溶性乙烯性不飽和單體相同。
逆相懸浮聚合中,可因應需要使用增稠劑。增稠劑可使用例如羥乙基纖維素、羥丙基纖維素、甲基纖維素、羧甲基纖維素、聚丙烯酸、聚丙烯酸(部分)中和物、聚乙二醇、聚丙烯醯胺、聚伸乙亞胺、糊精、藻酸鈉、聚乙烯醇、聚乙烯吡咯啶酮、聚環氧乙烷等。
逆相懸浮聚合中使用的分散穩定劑,只要使用界面活性劑即可,可使用例如蔗糖脂肪酸酯、聚丙三醇脂肪酸酯、山梨糖醇酐脂肪酸酯、聚氧乙烯山梨糖醇酐脂肪酸酯、聚氧乙烯丙三醇脂肪酸酯、山梨糖醇脂肪酸酯、聚氧乙烯山梨糖醇脂肪酸酯、聚氧乙烯烷基醚、聚氧乙烯烷基苯基醚、聚氧乙烯蓖麻油、聚氧乙烯硬化蓖麻油、烷基烯丙基甲醛縮合聚氧伸乙醚、聚氧乙烯聚氧丙烯嵌段共聚物、聚氧乙烯聚氧丙基烷基醚、聚乙二醇脂肪酸酯、烷基醣苷、N-葡萄糖醯胺、聚氧乙烯脂肪酸醯胺、聚氧乙烯烷基胺、聚氧乙烯烷基醚之磷酸酯、聚氧乙烯烷基烯丙基醚之磷酸酯等。當中,從單體之分散穩定性的觀點來看,以山梨糖醇酐脂肪酸酯、聚丙三醇脂肪酸酯、蔗糖脂肪酸酯等為佳。該等界面活性劑可單獨使用,亦可併用2種以上。
界面活性劑之使用量,為了使烴分散介質中之水溶性乙烯性不飽和單體保持良好分散狀態、且得到與使用量相應之分散效果,相對於第1階段之水溶性乙烯性不飽和單體100質量份,以0.1~30質量份為佳,較佳為0.3~20質量份。
又分散穩定劑方面,可與界面活性劑一起併用高分子系分散劑。可使用之高分子系分散劑方面可列舉馬來酸酐改質聚乙烯、馬來酸酐改質聚丙烯、馬來酸酐改質乙烯・丙烯共聚物、馬來酸酐改質EPDM(乙烯・丙烯・二烯・三元共聚物)、馬來酸酐改質聚丁二烯、馬來酸酐・乙烯共聚合物、馬來酸酐・丙烯共聚物、馬來酸酐・乙烯・丙烯共聚物、馬來酸酐・丁二烯共聚物、聚乙烯、聚丙烯、乙烯・丙烯共聚物、氧化型聚乙烯、氧化型聚丙烯、氧化型乙烯・丙烯共聚物、乙烯・丙烯酸共聚物、乙基纖維素、乙基羥乙基纖維素等。當中,從單體之分散穩定性觀點來看,以馬來酸酐改質聚乙烯、馬來酸酐改質聚丙烯、馬來酸酐改質乙烯・丙烯共聚物、馬來酸酐・乙烯共聚物、馬來酸酐・丙烯共聚物、馬來酸酐・乙烯・丙烯共聚物、聚乙烯、聚丙烯、乙烯・丙烯共聚物、氧化型聚乙烯、氧化型聚丙烯、氧化型乙烯・丙烯共聚物等為佳。該等高分子系分散劑可單獨使用,亦可併用2種以上。
高分子系分散劑之使用量,為了使烴分散介質中之水溶性乙烯性不飽和單體保持良好分散狀態、且得到與使用量相應之分散效果,相對於第1階段之水溶性乙烯性不飽和單體100質量份,以0.1~30質量份為佳,較佳為0.3~20質量份。
聚合步驟中,可廣泛使用例如公知聚合引發劑。自由基聚合引發劑可舉例如過硫酸鉀、過硫酸銨、過硫酸鈉等過硫酸鹽類;過氧化甲乙酮、過氧化甲基異丁基酮、過氧化二(三級丁基)、三級丁基過氧異丙苯、過氧化氫等過氧化物類;以及2,2’-偶氮雙(2-甲基丙脒)二鹽酸鹽、2,2’-偶氮雙[2-(N-苯基脒基)丙烷]二鹽酸鹽、2,2’-偶氮雙[2-(N-烯丙基脒基)丙烷]二鹽酸鹽、4,4’-偶氮雙(4-氰基纈草酸)等偶氮化合物等。
自由基聚合引發劑可單獨使用,從容易滿足前述(1)至(4)之條件這點來看,以組合2種以上為佳。可併用例如過硫酸鉀等過硫酸鹽類、2,2’-偶氮雙(2-脒基丙烷)二鹽酸鹽等偶氮化合物。
自由基聚合引發劑也可與亞硫酸鈉、亞硫酸氫鈉、硫酸亞鐵、L-抗壞血酸等還原劑併用,作為氧還聚合引發劑。
聚合步驟中使用的自由基聚合引發劑的使用量下限值,相對於使用之水溶性乙烯性不飽和單體1莫耳,例如以0.01毫莫耳為佳,0.05毫莫耳較佳。又,自由基聚合引發劑之上限值,相對於使用之水溶性乙烯性不飽和單體1莫耳,以20毫莫耳為佳,10毫莫耳較佳。藉由在該範圍內使用自由基聚合引發劑,可變得容易滿足前述(1)至(4)之條件。
聚合步驟中,也可因應需要使用鏈轉移劑。鏈轉移劑可例示次磷酸鹽類、硫醇類、硫醇酸類、第2級醇類、胺類等。
聚合步驟中,可因應需要使用內部交聯劑。
內部交聯劑方面,可舉具有2個以上聚合性不飽和基之化合物。內部交聯劑之具體例可例舉:(聚)乙二醇[本說明書中,組合例如「聚乙二醇」與「乙二醇」表記為「(聚)乙二醇」。以下相同]、(聚)丙二醇、三羥甲基丙烷、丙三醇聚氧乙二醇、聚氧丙二醇、以及(聚)丙三醇等多元醇類之二或三(甲基)丙烯酸酯類;使前述多元醇與馬來酸及延胡索酸等不飽和酸類反應而得之不飽和聚酯類;N,N’-亞甲基雙(甲基)丙烯醯胺等雙丙烯醯胺類;使聚環氧化物與(甲基)丙烯酸反應而得之二或三(甲基)丙烯酸酯類;使二異氰酸甲苯酯或二異氰酸六亞甲酯等聚異氰酸酯與(甲基)丙烯酸羥乙酯反應而得之二(甲基)丙烯酸胺甲醯酯類;烯丙基化澱粉;烯丙基化纖維素;鄰苯二甲酸二烯丙酯;N,N’,N”-異氰酸三烯丙酯;二乙烯基苯等。
又,作為內部交聯劑,除了前述具有2個以上聚合性不飽和基之化合物外,還可例舉(聚)乙二醇二環氧丙基醚、(聚)丙二醇二環氧丙基醚、及(聚)丙三醇二環氧丙基醚等含環氧丙基化合物;(聚)乙二醇、(聚)丙二醇、(聚)丙三醇、新戊四醇、伸乙二胺、聚伸乙亞胺、(甲基)丙烯酸環氧丙酯等。該等內部交聯劑也可併用2種以上。該等之中,從低溫下之反應性優異的觀點來看,以(聚)乙二醇二環氧丙基醚、(聚)丙二醇二環氧丙基醚、及(聚)丙三醇二環氧丙基醚及N,N’-亞甲基雙丙烯醯胺為佳。
內部交聯劑之使用量,從容易滿足前述(1)至(4)之條件這點來看,其下限值相對於所使用之水溶性乙烯性不飽和單體1莫耳,以0.0001毫莫耳為佳,0.0005毫莫耳較佳,0.001毫莫耳更佳,0.01毫莫耳尤佳。又,內部交聯劑使用量之上限值,相對於所使用之水溶性乙烯性不飽和單體1莫耳,以5毫莫耳為佳,0.5毫莫耳較佳,0.05毫莫耳更佳。
聚合反應之溫度,可因應自由基聚合引發劑之種類及使用量等適當設定,設定在例如20~110℃即可,較佳可設定在40~90℃。反應時間可設定在例如0.1小時以上4小時以下。
逆相懸浮聚合之聚合步驟,例如可在已溶解有高分子分散穩定劑之分散介質中,因應需要添加包含了經中和處理之水溶性乙烯性不飽和單體、增稠劑、自由基聚合引發劑及內部交聯劑之水溶液,接著添加界面活性劑,藉此做出懸浮狀態來進行。再者,各原料之添加順序並不限定於此。
水溶性乙烯性不飽和單體聚合而生成聚合物。例如,以逆相懸浮聚合而言,可獲得水溶性乙烯性不飽和單體之聚合物已分散之漿體。
逆相懸浮聚合可以1階段來進行,或亦可以2階段以上之多階段來進行。從提高生產性的觀點來看,其階段數以2~3階段為佳。
進行2階段以上之逆相懸浮聚合的情況下,依上述方法進行第1階段逆相懸浮聚合之後,於第1階段之聚合步驟中獲得之反應混合物中添加水溶性乙烯性不飽和單體並混合,利用與第1階段相同的方法進行第2階段以後之逆相懸浮聚合即可。在第2階段以後之各階段中之逆相懸浮聚合中,除了水溶性乙烯性不飽和單體之外,以第2階段以後之各階段中之逆相懸浮聚合時添加的水溶性乙烯性不飽和單體之量為基準計,可在相對於前述水溶性乙烯性不飽和單體之各成分莫耳比範圍內,添加自由基聚合引發劑與因應需要而添加之內部交聯劑,並在與上述方法相同條件下進行逆相懸浮聚合即可。
再者,以多階段進行逆相懸浮聚合的情況下,從容易滿足前述(1)至(4)之條件的觀點來看,每莫耳之逆相懸浮聚合中使用的水溶性乙烯性不飽和單體,宜令聚合引發劑之總量及內部交聯劑使用量之總量分別在上述範圍內。
(乾燥步驟)
乾燥步驟係藉著自外部對聚合物加諸熱等能量而將水分自上述聚合步驟中獲得之聚合物除去之步驟。例如,以逆相懸浮聚合之情況而言,乾燥步驟中,可在上述聚合步驟中獲得之聚合物(含水凝膠)已分散於烴分散介質之狀態下進行共沸蒸餾,藉此自聚合物除去水、烴分散介質等。乾燥步驟在常壓下或減壓下進行均可,為了提高乾燥效率,也可在氮等氣流下進行。乾燥步驟在常壓下進行的情況下,乾燥溫度以70~250℃為佳,80~180℃較佳,80~140℃更佳,90~130℃尤佳。在減壓下進行的情況下,乾燥溫度以40~160℃為佳,50~120℃較佳。
藉由實施乾燥步驟,可調整後述後交聯步驟前之聚合物含水率。再者,乾燥步驟亦可與後述後交聯步驟同時實施。
(後交聯步驟)
後交聯步驟係利用後交聯劑處理前述聚合步驟中獲得之水溶性乙烯性不飽和單體之聚合物的步驟。
後交聯劑之種類方面可例示與前述「1.吸水性樹脂」項中已說明之後交聯劑相同種類。
利用後交聯劑處理聚合物之方法方面,例如混合後交聯劑與溶劑來調製包含後交聯劑之處理液,使該處理液與聚合物接觸,藉此利用後交聯劑來處理聚合物。
用以調整包含後交聯劑之處理液的溶劑並無特別限定,例如可使用後交聯劑溶解性優異之親水性有機溶劑。該溶劑可舉水、此外可舉甲醇、乙醇、正丙醇、異丙醇、丙二醇等低級醇類;丙酮、甲乙酮等酮類;二乙醚、二 、四氫呋喃等醚類;N,N-二甲基甲醯胺等醯胺類;二甲亞碸等亞碸類等。該等親水性有機溶劑可分別單獨使用,也可併用2種以上,或與水作成混合溶劑來使用。
前述處理液例如可使後交聯劑溶解於溶劑中來調製。後交聯劑與溶劑之混合比率並無特別限定,例如每100質量份溶劑,可使交聯劑為0.1~10質量份。
聚合物與前述處理液之接觸,可藉著例如使聚合物與前述處理液以適當方法混合來進行。例如,可採用在容器內直接或在上述烴分散介質中攪拌聚合物並同時添加處理液之方法。
後交聯劑之使用量,從容易滿足前述(1)至(4)之條件這點來看,相對於構成可被後交聯之聚合物之水溶性乙烯性不飽和單體1莫耳,其下限值在0.01毫莫耳為佳,0.05毫莫耳較佳,0.1毫莫耳更佳。又,其上限值相對於水溶性乙烯性不飽和單體1莫耳,以10毫莫耳為佳,5毫莫耳較佳,2毫莫耳更佳。
又,從容易滿足前述(1)至(4)之條件這點來看,後交聯劑以添加至低含水率聚合物為佳。具體來說,後交聯劑宜在聚合物含不足100質量%水分之狀態下進行添加,以在含50質量%以下水分之狀態下添加為佳,在含10質量%以下水分之狀態下添加更佳。再者,聚合物含水率是即將添加後交聯劑前一刻聚合物中所含水分之比率。再者,含水率之測定方法記載於後述實施例。
聚合物含水率之下限值並無特別限定,以0.01質量%為佳,較佳為0.05質量%,更佳為0.1質量%。
再者,聚合物含水率可藉上述乾燥步驟來調整。
後交聯步驟中之反應溫度(即利用後交聯劑處理聚合物之溫度)以50~250℃為佳,60~180℃較佳,60~140℃更佳。又,前述後交聯之反應時間(即在前述反應溫度下利用後交聯劑處理聚合物之時間)會因應反應溫度、後交聯劑種類及使用量等而異因此不能一概而定,不過通常是1~300分鐘,較佳為5~200分鐘。
再者,聚合步驟之後,為了對吸水性樹脂賦予諸性能,可摻混因應目的之添加劑。這種添加劑可舉無機粉末、界面活性劑、氧化劑、還原劑、金屬螯合劑、自由基鏈鎖抑制劑、抗氧化劑、抗菌劑、消臭劑等。例如,相對於吸水性樹脂100重量份,添加0.05~5質量份之非晶質二氧化矽作為無機粉末,可使吸水性樹脂之流動性提升。
3.吸收性物品
利用本發明之吸水性樹脂的吸收體由吸水性樹脂與親水性纖維構成。吸收體之構成可舉例如將吸水性樹脂與親水性纖維混合成均勻組成而獲得之混合分散體、吸水性樹脂包夾於層狀親水性纖維間之夾層結構體、將吸水性樹脂與親水性纖維以薄紙包覆之結構體等,不過本發明並不限定於該例示之物。
吸收體中,亦可添加其他成分,例如用以提高吸收體形態保持性之熱熔著性合成纖維、熱熔接著劑、接著性乳膠等接著性黏結劑。
親水性纖維可舉例如由木材獲得之綿狀紙漿、機械紙槳、化學紙漿、半化學紙漿等纖維素纖維、人造絲、乙酸酯等人工纖維素纖維、經親水化處理之聚醯胺、聚酯、聚烯烴等合成樹脂構成之纖維等。
藉著將上述本發明之吸收體保持於液體可通過之液體透過性片材(表層)與液體無法通過之液體不透過性片材(底層)之間,可作為吸收性物品。液體透過性片材配設於與身體接觸該側、液體不透過性片材配設於與身體接觸之相反側。
液體透過性片材可舉例如聚乙烯、聚丙烯、聚酯等纖維構成之透氣型、紡絲黏合型、化學黏結型、針孔型等不織布及多孔質合成樹脂片材等。
液體不透過性片材可舉例如聚乙烯、聚丙烯、聚氯乙烯等樹脂構成之合成樹脂薄膜等。
吸收性物品之種類並無特別限定。可舉例如上至紙尿布、生理用衛生棉、失禁墊片等衛生材料、寵物用尿吸收材料等,下至包裝填充材等土木建築用資材、滴液吸收劑、保冷劑等食品鮮度保持用材料、土壤用保水材等農園藝用物品、封水材等。
實施例
以下,藉實施例更具體說明本發明,惟本發明並不限定於該等實施例之態樣。
[實施例1]
(由逆相懸浮聚合進行之水溶性乙烯性不飽和單體聚合物之製造)
準備具備迴流冷卻器、滴液漏斗、氮氣體導入管及攪拌翼之內徑110mm且容量2L之圓底圓筒型可分離式燒瓶,該攪拌翼具2段式翼徑50mm之4片傾斜槳翼。於該燒瓶中取正庚烷300g作為烴分散介質,添加蔗糖硬脂酸酯(Mitsubishi-Chemical Foods Co.,RYOTO Sugar Ester S-370)0.74g、馬來酸酐改質乙烯-丙烯共聚物(Mitsui Chemicals, Inc.,Hi-WAX™ 1105A)0.74g,一邊攪拌並加溫溶解之後,冷卻至55℃。
另一方面,於容量500mL之三角燒瓶中取80質量%之丙烯酸水溶液92g(1.02莫耳),自外部一邊冷卻一邊滴液30質量%之氫氧化鈉水溶液102.2g進行75莫耳%之中和。朝其中添加作為增稠劑之羥乙基纖維素0.092g(SUMITOMO SEIKA CHEMICALS CO.,LTD.,HEC AW-15F)、作為偶氮化合物之2,2’-偶氮雙(2-脒基丙烷)二鹽酸鹽0.055g(0.204毫莫耳)、作為過硫酸鹽之過硫酸鉀0.009g(0.034毫莫耳)、作為內部交聯劑之乙二醇二環氧丙基醚0.005g(0.026毫莫耳)及離子交換水48.0g並溶解,調製第1階段聚合步驟用單體水溶液。
將該單體水溶液添加至前述可分離式燒瓶,以氮氣將系統內(指反應可進行之容器內。以下相同)充分取代之後,將燒瓶浸漬於70℃水浴中進行升溫,使聚合反應進行10分鐘,藉此獲得第1階段反應混合物。
另一方面,於另一容量500mL之三角燒瓶取80質量%之丙烯酸水溶液128.8g(1.43莫耳),自外部一邊冷卻一邊滴液30質量%之氫氧化鈉水溶液143.1g進行75莫耳%之中和。朝其中添加作為偶氮系化合物之2,2’-偶氮雙(2-脒基丙烷)二鹽酸鹽0.077g(0.285毫莫耳)、作為過氧化物之過硫酸鉀0.013g(0.048毫莫耳)、作為內部交聯劑之乙二醇二環氧丙基醚0.012g(0.069毫莫耳)及離子交換水12.5g並溶解,調製第2階段聚合步驟用單體水溶液。將前述第1階段反應混合物冷卻至25℃後,將前述第2階段單體水溶液之全量添加至第1階段反應混合物,一邊以氮氣取代系統內並一邊在25℃下保持30分鐘。之後,再度將燒瓶浸漬於70℃水浴並升溫,進行第2階段聚合反應5分鐘,藉此獲得第2階段反應混合物。
再者,第1階段與第2階段聚合步驟中使用之乙烯性不飽和單體(丙烯酸)之量計2.45毫莫耳,內部交聯劑(乙二醇二環氧丙基醚)之量計0.017g(0.095毫莫耳)。內部交聯劑之使用量,相對於第1階段與第2階段聚合步驟中使用之乙烯性不飽和單體(丙烯酸)1莫耳為0.0388毫莫耳。
利用125℃油浴將第2階段反應混合物升溫,利用正庚烷與水之共沸蒸餾,一邊使正庚烷迴流一邊將255g之水引出系統外後,添加作為螯合劑之二伸乙三胺五醋酸・五鈉鹽之4.5%水溶液5.89g(0.53毫莫耳),使正庚烷蒸發獲得聚合物。使獲得之聚合物通過網眼850μm之篩,獲得球狀粒子凝聚之2次粒子形態之聚合物236.6g。
(後交聯步驟)
接著,於100mL燒杯中置入丙二醇10g、離子交換水30g、異丙醇10g、及作為後交聯劑之乙二醇二環氧丙基醚0.5g(2.87毫莫耳),使用磁攪拌器(8mmφ×30mm無環)攪拌5分鐘,藉此調製含有50.5g後交聯劑之處理液。
另一方面,於具備翼徑90mm之氟樹脂製碇型攪拌翼之內徑110mm且容量2L之圓底圓筒型可分離式燒瓶中置入前述聚合物30g,一邊以500rpm進行攪拌並一邊將前述處理液1.12g(含後交聯劑乙二醇二環氧丙基醚0.0636毫莫耳)滴液至該可分離式燒瓶。再者,後交聯劑係在聚合物含水率8%之狀態下添加。含水率之測定方法詳述於次項。後交聯劑之添加量,相對於構成可被後交聯之聚合物之乙烯性不飽和單體(丙烯酸)1莫耳而為0.21毫莫耳。自滴液結束起攪拌1分鐘後,取出聚合物。將該聚合物於經氟樹脂塗覆之底面26×20cm且深度約5cm之槽中擴展開,將該槽靜置於已設定在180℃之熱風乾燥機內(ADVANTEC公司製、FV-320)40分鐘。藉此利用後交聯劑使聚合物交聯(後交聯步驟中之反應溫度為180℃、反應時間為40分)、獲得目的之吸水性樹脂。相對於取得之吸水性樹脂,混合0.2質量%之非晶質二氧化矽(Evonik Japan Co., Ltd.、CARPLEX® #80),依據下述各種試驗方法評價製得之吸水性樹脂。
[含水率測定]
於已預先秤量之鋁箔容器(8號)精秤聚合物約2g(WA
(g))。使上述樣本於內溫已設定在105℃之熱風乾燥機(ADVANTEC公司製、FV-320)中乾燥2小時之後,在乾燥器中放冷,測定乾燥後聚合物之質量WB
(g)。依據以下式算出聚合物含水率。
含水率(%)={[WA
-WB
]/WA
}×100
[實施例2]
於後交聯步驟中,將含有後交聯劑之處理液的使用量變更為3.36g(包含後交聯劑乙二醇二環氧丙基醚0.191毫莫耳),除此之外依與實施例1相同方法製得吸水性樹脂。後交聯步驟中之後交聯劑添加量,相對於使用之乙烯性不飽和單體(丙烯酸)1莫耳為0.62毫莫耳。
[實施例3]
於後交聯步驟中,將含有後交聯劑之處理液的使用量變更為6.72g(包含後交聯劑乙二醇二環氧丙基醚0.382毫莫耳),除此之外依與實施例1相同方法製得吸水性樹脂。後交聯步驟中之後交聯劑添加量,相對於構成可被後交聯之聚合物之乙烯性不飽和單體(丙烯酸)1莫耳為1.24毫莫耳。
[比較例1]
在聚合物含水率高之狀態下添加後交聯劑。具體而言,在逆相懸浮聚合中,調製第1階段聚合步驟用單體水溶液之際,將乙二醇二環氧丙基醚0.005g變更為0.012g(0.069毫莫耳),除此之外依與實施例1相同程序獲得第2階段反應混合物。再者,第1階段與第2階段聚合步驟中使用之內部交聯劑(乙二醇二環氧丙基醚)之量計0.024g(0.138毫莫耳)。內部交聯劑使用量相對於第1階段與第2階段使用之乙烯性不飽和單體(丙烯酸)1莫耳為0.056毫莫耳。
將所獲得之第2階段反應混合物在125℃油浴中升溫,利用正庚烷與水之共沸蒸餾,一邊使正庚烷迴流一邊將255g之水引出系統外。接著,於聚合物中添加作為螯合劑之二伸乙三胺五醋酸・五鈉鹽4.5%水溶液5.89g(0.53毫莫耳)及作為後交聯劑之乙二醇二環氧丙基醚2%水溶液4.42g(0.51毫莫耳),在80℃下保持2小時。再者,後交聯劑係在聚合物含水率23%之狀態下添加。後交聯劑之添加量,相對於構成可被後交聯之聚合物之乙烯性不飽和單體(丙烯酸)1莫耳為0.21毫莫耳。之後,使正庚烷蒸發獲得聚合物。使獲得之聚合物通過網眼850μm之篩,獲得球狀粒子凝聚之形態之吸水性樹脂236.6g。相對於取得之吸水性樹脂0.2質量%,混合非晶質二氧化矽(Evonik Japan Co., Ltd.、CARPLEX® #80),依據下述各種試驗方法評價製得之該吸水性樹脂。
[比較例2]
令所使用之聚合引發劑為1種。具體而言,將第1階段聚合步驟中使用之聚合引發劑變更為過硫酸鉀0.074g(0.272毫莫耳)、第2階段聚合步驟中使用之聚合引發劑變更為過硫酸鉀0.103g(0.381毫莫耳),除此之外依與實施例1相同方法製得吸水性樹脂。
[比較例3]
令所使用之聚合引發劑為1種,同時在聚合物含水率高之狀態下添加後交聯劑。具體而言,將第1階段聚合步驟中使用之聚合引發劑變更為過硫酸鉀0.074g(0.272毫莫耳)、第2階段聚合步驟中使用之聚合引發劑變更為過硫酸鉀0.103g(0.381毫莫耳)、以及在聚合物含水率20%之狀態下添加後交聯劑,此外依與比較例1相同方法製得吸水性樹脂236.6g。
[比較例4]
利用水溶液聚合製作吸水性樹脂。具體而言,在具備攪拌機、攪拌翼、迴流冷卻器、滴液漏斗及氮氣體導入管之內容積2公升之五口圓筒形圓底燒瓶中取80質量%之丙烯酸水溶液92g(1.02莫耳),一邊自外部冷卻一邊滴液30質量%之氫氧化鈉水溶液102.2g進行75莫耳%之中和,調製25質量%丙烯酸部分中和鹽水溶液。
於獲得之丙烯酸部分中和鹽水溶液中添加作為內部交聯劑之乙二醇二環氧丙基醚0.013g(0.075毫莫耳)、作為水溶性自由基聚合引發劑之2,2’-偶氮雙(2-脒基丙烷)二鹽酸鹽0.055g(0.204毫莫耳)、過硫酸鉀0.009g(0.034毫莫耳),將系統內進行氮氣體取代之後,保持在50℃水浴進行1小時水溶液聚合反應。再者,內部交聯劑使用量,相對於乙烯性不飽和單體(丙烯酸)1莫耳為0.074毫莫耳。
將獲得之聚合反應物在SUS製碎肉機粗粉碎後,於140℃熱風乾燥機中使之乾燥1小時。接著,以轉子速率碾磨機粉碎該乾燥物,以網眼850μm之JIS標準篩進行分級,以水溶性乙烯性不飽和單體聚合物(90.7g)形式獲得850μm以下之粒子。
針對獲得之聚合物,在進行後交聯之步驟中,將含有後交聯劑之處理液的使用量變更為10.08g(包含後交聯劑乙二醇二環氧丙基醚0.573毫莫耳)、以及在實施例1之後交聯步驟中後交聯劑添加前添加作為螯合劑之二伸乙三胺五醋酸・五鈉鹽4.5%水溶液0.75g(0.067毫莫耳),除此之外,以與實施例1之後交聯步驟相同方法對30g聚合物施行後交聯,獲得吸水性樹脂。對取得之吸水性樹脂混合0.2質量%之非晶質二氧化矽(Evonik Japan Co., Ltd.製、CARPLEX® #80),依據下述各種試驗方法評價製得之吸水性樹脂。再者,後交聯劑係在聚合物含水率8%之狀態下添加。後交聯劑之添加量相對於構成可被後交聯之聚合物之乙烯性不飽和單體(丙烯酸)1莫耳為1.84毫莫耳。
(評價方法)
針對各實施例及比較例中製得之吸水性樹脂,如以下進行凝膠黏度(初始及1日後)、對生理食鹽水之保水能、在4.14kPa荷重下對生理食鹽水之吸水能及吸水速度之測定。
[凝膠黏度測定]
於500mL燒杯加入蒸餾水299g,使用磁攪拌器(8mmφ×30mm無環)以600rpm進行攪拌。在藉該攪拌而產生之渦流中投入吸水性樹脂1.0g之後,進行攪拌直到渦流消失液面變回水平為止。分別針對製作之300倍膨潤凝膠在室溫(25℃)下靜置1小時後之凝膠黏度(本發明中以之為「初始凝膠黏度」)及在90℃熱風乾燥機(ADVANTEC公司製、FV-320)中靜置1日(24小時)後之凝膠黏度(本發明中以之為「1日後凝膠黏度」),使用Vismetron (SHIBAURA SYSTEM 公司VS-H1型、Rotor No.5、旋轉數20rpm)進行凝膠黏度測定。再者,凝膠黏度測定時係將製作之凝膠置入200mL燒杯中來進行。
[對生理食鹽水之保水能測定]
將評價用吸水性樹脂2.0g置入綿袋內後,對綿袋(細平棉布60號、橫100mm×縱200mm)內流入生理食鹽水(0.9%氯化鈉水溶液)500g並同時使整體浸漬。將綿袋上部以橡皮筋綁縛,浸漬30分鐘後,利用已設定成離心力167G之脫水機(KOKUSAN CO.製、型號:H-122)將綿袋進行脫水1分鐘,測定脫水後包含膨潤凝膠之綿袋重量WC
。又,未於綿袋內放入試料實施相同操作,測定綿袋空重量WD
。然後,依據以下算式算出對生理食鹽水之保水能。
對生理食鹽水之保水能(g/g)=(WC
-WD
)/2.0
[在4.14kPa荷重下對生理食鹽水之吸水能測定]
利用圖1中顯示概略構成之測定裝置X,測定吸水性樹脂在4.14kPa荷重下對生理食鹽水之吸水能。
圖1中顯示測定裝置X由滴定管部1、導管2、測定台3、置於測定台3上之測定部4構成。滴定管部1於滴定管10上部連結有橡膠栓14、下部連結有空氣導入管11與旋塞12,進一步,空氣導入管11上部有旋塞13。從滴定管部1到測定台3安裝有導管2,導管2之直徑為6mm。測定台3之中央部有直徑2mm之孔,連結有導管2。測定部4具有圓筒40、貼附於該圓筒40底部之耐綸篩41、砝碼42。圓筒40之內徑為2.0cm。耐綸篩41形成為200網目(網眼75μm)。然後,耐綸篩41上均勻撒佈了預定量之吸水性樹脂5。砝碼42為直徑1.9cm、質量119.6g。該砝碼42置於吸水性樹脂5上,可將4.14kPa之荷重對吸水性樹脂5均勻施加。
在這種構成之測定裝置X中,首先關閉滴定管部1之旋塞12與旋塞13,自滴定管10上部饋入已調節至25℃之生理食鹽水,以橡膠栓14將滴定管上部上栓之後,開啟滴定管部1之旋塞12、旋塞13。接著,進行測定台3之高度調整使位於測定台3中心部之導管2前端與空氣導入管11之空氣導入口相同高度。這時,進行調整使得與自測定部被吸出之生理食鹽水同體積之空氣會自空氣導入口毫無抵抗地被供給。
另一方面,在圓筒40之耐綸篩41上均勻撒佈0.10g之吸水性樹脂5,於該吸水性樹脂5上放置砝碼42。測定部4係放置成其中心部與測定台3中心部之導管口一致。
自吸水性樹脂5開始吸水之時點起持續性地讀取滴定管10內生理食鹽水之減少量(吸水性樹脂5所吸水之生理食鹽水量)WE
(mL)。依據下式求出從吸水開始起經過60分鐘後之吸水量,作為吸水性樹脂5在荷重下對生理食鹽水之吸水能。
在4.14kPa荷重下對生理食鹽水之吸水能(mL/g)=WE
÷0.10
[吸水速度測定(Vortex法)]
於100mL燒杯中加入生理食鹽水50g,在恆溫槽內保持於25℃。接著,將吸水性樹脂2.00g投入已使用磁攪拌器(8mmφ×30mm無環)以600rpm攪拌之生理食鹽水渦流中,同時開始利用馬錶所進行之計測。以渦流消失液面成為水平之時點為終點,以迄今之時間(秒)為吸水速度。
表1為各實施例及比較例中製得之評價用樣本之評價結果。
可知實施例1至3中製得之吸水性樹脂,自吸水起第1日之凝膠黏度較初始凝膠黏度大幅降低(前述凝膠分解指數均為0.60以下)。從該等結果可知,實施例1乃至3中獲得之吸水性樹脂具有優異的自我分解特性。
相對於此,比較例1至4製得之吸水性樹脂為分解不易進行之性質。
X‧‧‧測定裝置
1‧‧‧滴定管部
2‧‧‧導管
3‧‧‧測定台
4‧‧‧測定部
5‧‧‧吸水性樹脂粒子
10‧‧‧滴定管
11‧‧‧空氣導入管
12‧‧‧旋塞
13‧‧‧旋塞
14‧‧‧橡膠栓
40‧‧‧圓筒
41‧‧‧耐綸篩
42‧‧‧砝碼
圖1為示意圖,顯示用以測定在4.14kPa荷重下對生理食鹽水之吸水能的裝置的概略構成。
Claims (3)
- 一種吸水性樹脂,具有水溶性乙烯性不飽和單體之聚合物已利用後交聯劑交聯之結構,且 (1)對生理食鹽水之保水能為35g/g以上, (2)在4.14kPa荷重下對生理食鹽水之吸水能為10mL/g以上, (3)初始凝膠黏度為3000mPa・s以上, (4)以下述式(I)表示之凝膠分解指數為0.60以下: 式(I):凝膠分解指數=B/A (惟,上述式(I)中,A表示初始凝膠黏度(mPa・s),B表示1日後凝膠黏度(mPa・s))。
- 如請求項1之吸水性樹脂,其中前述聚合物係利用前述水溶性乙烯性不飽和單體之逆相懸浮聚合來形成。
- 一種吸收性物品,具備吸收體,該吸收體包含請求項1或2之吸水性樹脂。
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