CN104138718A - 一种改性丁羟聚氨酯渗透汽化膜的制备方法 - Google Patents
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Abstract
本发明公开一种改性丁羟聚氨酯渗透汽化膜的制备方法，其步骤为：首先将端羟基聚丁二烯、端氨丙基聚二甲基硅氧烷与甲苯-2,4-二异氰酸酯混合后溶于二甲苯溶剂中，并加入催化剂二月桂酸二丁基锡，合成预聚体；然后将适量二苯基甲烷二胺逐滴加入到预聚体中，反应得到改性丁羟聚氨酯聚铸膜液；最后将改性丁羟聚氨酯聚铸膜液进行真空脱泡后在聚四氟乙烯板上流延成膜，常温下自然晾干后真空干燥，得到改性丁羟聚氨酯渗透汽化膜。本发明方法生产步骤简单，操作方便，生产成本低，且膜对低浓度的丁醇/丙酮/水具有很好的分离效果，工业应用前景广阔。
Description
技术领域
本发明涉及一种用于渗透汽化优先透过有机物的改性丁羟聚氨酯渗透汽化膜的制备方法，属于渗透汽化膜分离领域。
背景技术
受能源危机影响，石油价格上涨，作为新型生物能源的丁醇越来越受到重视。生物发酵法制备丁醇（ABE发酵）的产物中主要含丙酮、丁醇和乙醇，且三者的比例为3:6:1。主要受产物丁醇的抑制作用，发酵液中总溶剂浓度只能达到约20gL-1，生产能力较低。为了解决上述问题，科学家尝试将一些分离方法，渗透汽化（PV）、吸附、液液萃取、气提和反渗透等，（Ezeji, T.C., N. Qureshi, and H.P. Blaschek, Butanol fermentation research: Upstream and downstream manipulations. Chemical Record, 2004. 4(5): p. 305-314）直接与发酵过程耦合以实现丁醇的原位分离，减轻丁醇对微生物的抑制作用，提高发酵强度和原料利用率。
众多分离方法中，渗透汽化（pervaporation，PV）能够以低的能耗实现蒸馏、萃取、吸附等传统方法难于完成的分离任务，特别适于分离近沸点、恒沸点混合物及同分异构体的分离，对有机溶剂及混合溶剂中微量水的脱除及废水中少量有机污染物的分离具有明显的技术上和经济上的优势。
目前应用于ABE发酵过程分离研究的渗透汽化膜主要有高分子聚合膜，无机膜以及液体膜。无机膜材料价格昂贵，且易收到微生物污染，液体膜稳定性较差等，相对而言，高分子聚合膜研究较多。主要应用于优先透醇的渗透汽化分离膜材料有有机硅聚合物（PDMS、PTMSP），如含氟类聚合物（PTFE、PVDF）和其他聚合物（PDMS/PVDF、PEBA）等，如Srinivasan用硅脂改性的PVDF膜对7.5wt%的丁醇溶液进行渗透汽化分离，50℃条件下，总通量为3.42 kgm-2h-1，分离因子为4.88（Srinivasan, K., K. Palanivelu, and A.N. Gopalakrishnan, Recovery of 1-butanol from a model pharmaceutical aqueous waste by pervaporation. Chemical Engineering Science, 2007. 62(11): p. 2905-2914）。Liu用PEBA制得厚度100μm的聚合膜对二元体系（丙酮－水、丁醇－水、乙醇－水）的分离效果为：分离因子α 丙酮＝4.2、α 丁醇＝8.2和α 乙醇＝2.4，对应的总渗透通量分别为27.4 gm-2h-1、65.3 gm-2h-1和37.2gm-2h-1（Liu, FF; Liu, L; Feng, XS. Separation of acetone–butanol–ethanol (ABE) from dilute aqueous solution by pervaporation[J]. Sep. Purif. Technol. 2005, 42(3): 273-282）。有机硅聚合物虽分离效果较好，但自身成膜性、机械性能差，含氟类聚合物虽然因含氟原子而具有良好的憎水性，但选择性不好，且成本过高，复合膜制备工艺相对复杂。本发明采用的聚氨酯（PU）是一种重要的高分子材料，具有优良的机械强度，经过简单的改性即可提高其对有机物的选择性，成本低，工业化应用价值高，前景广阔。
发明内容
本发明的目的在于针对上述关键技术问题，提供一种优先通过丙酮/丁醇的改性丁羟聚氨酯膜的制备方法。
为实现上述目的，本发明所采取的技术方案是：该改性丁羟聚氨酯膜的制备方法包括以下步骤：
A.在装有氮气保护、机械搅拌和冷凝回流的反应器中加入二甲苯作为溶剂，将端羟基聚丁二烯、端氨丙基聚二甲基硅氧烷与甲苯-2,4-二异氰酸酯混合成混合体，后溶于二甲苯溶剂中，并加入催化剂二月桂酸二丁基锡，搅拌均匀，60-70℃下反应1～3h后冷却至室温，合成预聚体；所述的端羟基聚丁二烯的平均分子量为2500～3000；所述的端氨丙基聚二甲基硅氧烷平均分子量为2200～2700；所述的端氨丙基聚二甲基硅氧烷与端羟基聚丁二烯的摩尔比为0.5～1:1；所述的甲苯-2,4-二异氰酸酯与端羟基聚丁二烯的摩尔比为2～8:1；所述的混合体与二甲苯溶剂的质量比为1:0.5～4；所述的二月桂酸二丁基锡与端羟基聚丁二烯的质量比为0.0005～0.001:1；
B.按照端羟基聚丁二烯与二苯基甲烷二胺摩尔比1:1～2.5称取二苯基甲烷二胺，并逐滴加入到预聚体中，升温至50℃反应1h，即得改性丁羟聚氨酯聚铸膜液；
C.将改性丁羟聚氨酯聚铸膜液进行真空脱泡，后在聚四氟乙烯板上流延成膜，常温下自然晾干后，置于60～100℃真空烘箱中真空干燥6～12h，得到改性丁羟聚氨酯渗透汽化膜。
与现有技术相比，本发明制备的聚氨酯膜以适量的端氨丙基聚二甲基硅氧烷为软段，对丁羟聚氨酯膜进行改性，在保证了膜强机械性能的前提下，使膜的表面水接触角从65°提高到100°以上，有效改善了膜对低浓度有机物的选择性，且该膜不受发酵料液污染，适合与发酵过程耦合，实现原位分离。本发明制备工艺简单、操作方便，原料成分低廉，应用前景广阔。
具体实施方式
以下结合具体实例对本发明的技术方案做进一步的说明。
实施例1：
A.在装有氮气保护、机械搅拌和冷凝回流的反应器中加入二甲苯作为溶剂，将端羟基聚丁二烯、端氨丙基聚二甲基硅氧烷与甲苯-2,4-二异氰酸酯混合成混合体，后溶于二甲苯溶剂中，并加入催化剂二月桂酸二丁基锡，搅拌均匀，65℃下反应2h后冷却至室温，合成预聚体；所述的端羟基聚丁二烯的平均分子量为3000；端氨丙基聚二甲基硅氧烷平均分子量为2200；端氨丙基聚二甲基硅氧烷与端羟基聚丁二烯的摩尔比为0.5:1；甲苯-2,4-二异氰酸酯与端羟基聚丁二烯的摩尔比为2:1；混合体与二甲苯溶剂的质量比为1:1；二月桂酸二丁基锡与端羟基聚丁二烯的质量比为0.0005:1；
B.按照端羟基聚丁二烯与二苯基甲烷二胺摩尔比1:1.5称取二苯基甲烷二胺，并逐滴加入到预聚体中，升温至50℃反应1h，即得改性丁羟聚氨酯聚铸膜液；
C.将改性丁羟聚氨酯聚铸膜液进行真空脱泡，后在聚四氟乙烯板上流延成膜，常温下自然晾干后，置于100℃真空烘箱中真空干燥6h，得到改性丁羟聚氨酯渗透汽化膜。
将本实施例所得的改性丁羟聚氨酯渗透汽化膜对丙酮/水、丁醇/水混合溶液进行渗透汽化分离实验，性能如表1所示：
表1
实施例2：
A.在装有氮气保护、机械搅拌和冷凝回流的反应器中加入二甲苯作为溶剂，将端羟基聚丁二烯、端氨丙基聚二甲基硅氧烷与甲苯-2,4-二异氰酸酯混合成混合体，后溶于二甲苯溶剂中，并加入催化剂二月桂酸二丁基锡，搅拌均匀，60℃下反应3h后冷却至室温，合成预聚体；所述的端羟基聚丁二烯的平均分子量为2500；端氨丙基聚二甲基硅氧烷平均分子量为2500；端氨丙基聚二甲基硅氧烷与端羟基聚丁二烯的摩尔比为1:1；甲苯-2,4-二异氰酸酯与端羟基聚丁二烯的摩尔比为8:1；混合体与二甲苯溶剂的质量比为1: 4；二月桂酸二丁基锡与端羟基聚丁二烯的质量比为0.0008:1；
B.按照端羟基聚丁二烯与二苯基甲烷二胺摩尔比1:2.5称取二苯基甲烷二胺，并逐滴加入到预聚体中，升温至50℃反应1h，即得改性丁羟聚氨酯聚铸膜液；
C.将改性丁羟聚氨酯聚铸膜液进行真空脱泡，后在聚四氟乙烯板上流延成膜，常温下自然晾干后，置于90℃真空烘箱中真空干燥10h，得到改性丁羟聚氨酯渗透汽化膜。
将本实施例所得的改性丁羟聚氨酯渗透汽化膜对丙酮/水、丁醇/水混合溶液进行渗透汽化分离实验，性能如表2所示：
表2
实施例3：
A.在装有氮气保护、机械搅拌和冷凝回流的反应器中加入二甲苯作为溶剂，将端羟基聚丁二烯、端氨丙基聚二甲基硅氧烷与甲苯-2,4-二异氰酸酯混合成混合体，后溶于二甲苯溶剂中，并加入催化剂二月桂酸二丁基锡，搅拌均匀，60℃下反应3h后冷却至室温，合成预聚体；所述的端羟基聚丁二烯的平均分子量为2800；端氨丙基聚二甲基硅氧烷平均分子量为2700；端氨丙基聚二甲基硅氧烷与端羟基聚丁二烯的摩尔比为0.7:1；甲苯-2,4-二异氰酸酯与端羟基聚丁二烯的摩尔比为6:1；混合体与二甲苯溶剂的质量比为1:2.5；二月桂酸二丁基锡与端羟基聚丁二烯的质量比为0.0007:1；
B.按照端羟基聚丁二烯与二苯基甲烷二胺摩尔比1:2称取二苯基甲烷二胺，并逐滴加入到预聚体中，升温至50℃反应1h，即得改性丁羟聚氨酯聚铸膜液；
C.将改性丁羟聚氨酯聚铸膜液进行真空脱泡，后在聚四氟乙烯板上流延成膜，常温下自然晾干后，置于60℃真空烘箱中真空干燥12h，得到改性丁羟聚氨酯渗透汽化膜。
将本实施例所得的改性丁羟聚氨酯渗透汽化膜对丙酮/水、丁醇/水混合溶液进行渗透汽化分离实验，性能如表3所示：
表3
。
Claims (1)
1.一种改性丁羟聚氨酯渗透汽化膜的制备方法，其特征在于该方法包括以下步骤：
A.在装有氮气保护、机械搅拌和冷凝回流的反应器中加入二甲苯作为溶剂，将端羟基聚丁二烯、端氨丙基聚二甲基硅氧烷与甲苯-2,4-二异氰酸酯混合成混合体，后溶于二甲苯溶剂中，并加入催化剂二月桂酸二丁基锡，搅拌均匀，60-70℃下反应1～3h后冷却至室温，合成预聚体；所述的端羟基聚丁二烯的平均分子量为2500～3000；所述的端氨丙基聚二甲基硅氧烷平均分子量为2200～2700；所述的端氨丙基聚二甲基硅氧烷与端羟基聚丁二烯的摩尔比为0.5～1:1；所述的甲苯-2,4-二异氰酸酯与端羟基聚丁二烯的摩尔比为2～8:1；所述的混合体与二甲苯溶剂的质量比为1:0.5～4；所述的二月桂酸二丁基锡与端羟基聚丁二烯的质量比为0.0005～0.001:1；
B.按照端羟基聚丁二烯与二苯基甲烷二胺摩尔比1:1～2.5称取二苯基甲烷二胺，并逐滴加入到预聚体中，升温至50℃反应1h，即得改性丁羟聚氨酯聚铸膜液；
C.将改性丁羟聚氨酯聚铸膜液进行真空脱泡，后在聚四氟乙烯板上流延成膜，常温下自然晾干后，置于60～100℃真空烘箱中真空干燥6～12h，得到改性丁羟聚氨酯渗透汽化膜。
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| CN104312424A (zh) * | 2014-11-13 | 2015-01-28 | 山东华亚环保科技有限公司 | 一种聚氨酯型防腐涂料及制备方法 |
| CN106632970A (zh) * | 2016-10-20 | 2017-05-10 | 合肥创想能源环境科技有限公司 | 一种聚氨酯渗透汽化膜的制备方法 |
| CN109077344A (zh) * | 2018-09-01 | 2018-12-25 | 王婧婧 | 一种奶味香精的制备方法 |
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| CN102743982A (zh) * | 2011-04-21 | 2012-10-24 | 北京工商大学 | 改性聚氨酯渗透汽化苯酚/水分离膜的制备方法 |
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Cited By (3)
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| CN104312424A (zh) * | 2014-11-13 | 2015-01-28 | 山东华亚环保科技有限公司 | 一种聚氨酯型防腐涂料及制备方法 |
| CN106632970A (zh) * | 2016-10-20 | 2017-05-10 | 合肥创想能源环境科技有限公司 | 一种聚氨酯渗透汽化膜的制备方法 |
| CN109077344A (zh) * | 2018-09-01 | 2018-12-25 | 王婧婧 | 一种奶味香精的制备方法 |
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