Jianzhong
Ma
*ab,
Jiamin
Zhao
a,
Hui
Zhang
a,
Zhenhua
Tian
*a,
Qiwu
Liu
a,
Na
Yang
a and
Wenbo
Zhang
bc
aCollege of Bioresources Chemical and Materials Engineering, Shaanxi University of Science & Technology, Xi'an 710021, P.R. China. E-mail: majz@sust.edu.cn; Tel: +86 029 8613 2559
bCollege of Chemistry and Chemical Engineering, Shaanxi University of Science & Technology, Xi'an 710021, P.R. China
cShaanxi Collaborative Innovation Center of Industrial Auxiliary Chemistry and Technology, Shaanxi University of Science & Technology, Xi'an 710021, P.R. China
First published on 16th October 2023
Acrylic polymers are widely used in pharmaceutical, leather, textile and other industries, and are prepared via the polyreaction of acrylic monomers, such as acrylic acid, acrylamide and acrylic esters. Acrylic acid and acrylamide have been proven to participate in the Mannich reaction to achieve cationization; however, the Mannich reaction of methyl acrylate has not been reported. At present, the main role of catalysts in the Mannich reaction is to provide products of specific spatial configuration, and there are few studies on improving the degree of cationic modification. The participation of acrylic acid, acrylamide and methyl acrylate in the Mannich reaction by means of the catalyst NaH was studied in this work. The optimal reaction conditions for the homopolymers were obtained via orthogonal experiments. At room temperature, the optimal reaction conditions for polyacrylic acid were as follows: the molar ratio of polyacrylic acid, glutaraldehyde and diethanolamine was 1.0:
1.4
:
1.0, and the amount of catalyst was 7%. The optimal reaction conditions for polyacrylamide were as follows: the molar ratio of polyacrylamide, glutaraldehyde and diethanolamine was 1.1
:
1.1
:
1.2, and the amount of catalyst was 9%. The optimum reaction conditions for methyl polyacrylate were as follows: the molar ratio of methyl polyacrylate, glutaraldehyde and diethanolamine was 1.1
:
1.2
:
1.0, and the amount of catalyst was 9%. As a result, the maximum degrees of modification of polyacrylic acid, polyacrylamide and methyl polyacrylate were 63.0%, 33.5% and 39.0%, respectively. The range analysis of the orthogonal experiments showed that the effects on the modification degree of vinyl homopolymers, in sequence from strong to weak, were as follows: amount of catalyst > amount of amine > amount of aldehyde. Subsequently, polyacrylate–acrylamide–methyl acrylate (P(AA–AM–MA)) was synthesized using acrylic acid, acrylamide and methyl acrylate as monomers, and then modified via the catalyzed Mannich reaction. A novel amphoteric acrylic acid copolymer retanning agent (HCP(AA–AM–MA)) with a 50.2% degree of modification was obtained, and its properties as a retanning agent in leather-making were investigated. The dye-uptake and K/S value of the dyed leather retanned with HCP(AA–AM–MA) were 91.5% and 18.5, respectively, an increase of 18.4% and 3.4 in comparison with those of dyed leather retanned with P(AA–AM–MA). The results indicated that the dyeing-assistant performance of HCP(AA–AM–MA) was improved. Moreover, the elongation at break and tensile strength of the retanned leather were 82.0% and 31.9 MPa, respectively, which were higher than those of P(AA–AM–MA)-retanned leather (78.9% and 27.4 MPa).
However, acrylic polymers are a type of anionic polymer, which has restricted their application range. Cationic modification can give them unusual properties. For example, acrylamide polymer flocculants for wastewater treatment have better absorbability after cationization than the products without cationization; acrylate coatings after cationization have excellent antibacterial activity.11,12 Cationic acrylic polymer tanning agents have good retanning and auxiliary dyeing properties.13–15 Therefore, acrylic-polymer cationization is necessary. One of the cationic modification methods is the Mannich reaction, a three-component (acid component, aldehyde component, and amine component) reaction.16 The method is operationally simple, the raw materials are cheap and the reaction is stable.
The main acrylic monomers used in industries are acrylic acid, acrylamide, acrylonitrile and acrylate monomers.17,18 Acrylate monomers are common raw materials due to their advantages of low cost, easy preparation and easy function adjustment. They play a pivotal role in the processing and production of industrial chemicals.19,20 Acrylic acid and acrylamide have been proven to participate in the Mannich reaction to achieve cationization in previous studies, but the same for methyl acrylate has not been reported.21 The difficulty here is that the α-H of methyl acrylate is too inert to participate in the reaction. At present, the main role of catalysts in the Mannich reaction is to provide products of specific spatial configuration, and there are few studies on improving the degree of cationic modification.22,23
Can the degree of cationic modification of acrylic polymers in the Mannich reaction be improved by a catalyst? Wang et al. utilized toluene sulfonic acid as an acid catalyst for the organic chemical reactions in the synthesis of α-substituted N-amino aryl acetals. The experimental results showed that after the addition of catalyst Sc(OTf)3, glyoxal dimethyl acetal, aryl amines and ketones were successfully reacted with 1,3-dicarbonyl compounds in a Mannich reaction, which allowed the synthesis of a number of heterocyclic compounds such as indoles.24 Li et al. carried out the Mannich reaction in anhydrous ethanol using acetophenone, diphenylamine and benzaldehyde as the reaction raw materials and tin tetrachloride (SnCl4) as the reaction catalyst, and the experimental results showed that catalyzing the Mannich reaction by using SnC14 could effectively reduce the reaction time, increase the reaction yield, and enhance the reaction efficiency.25 Yamashita et al. used potassium bis(methylsilyl)diamine (KHMDS) as a base catalyst for the Mannich reaction using N-o-methoxyphenylbenzenecarboximide and tert-butyl isobutyrate as the raw materials. When KHMDS was used as a catalyst, the tert-butyl isobutyrate monomer was deprotonated by KHMDS to produce a hydrogen molecule and the corresponding potassium enol compound. The reaction continued with N-o-methoxyphenylbenzaldehyde imine to produce a Mannich-base intermediate with a potassium ion, and then the intermediate was protonated by reaction with the tert-butyl isobutyrate monomer to get the desired products, the Mannich base and a potassium enol compound. The catalytic cycle was completed by the reaction of this enol with the tert-butyl isobutyrate monomer to remove the proton and obtain the Mannich base, which then further gives the desired product as well as the potassium enol compound. The results show that these catalysts can successfully catalyze the Mannich reaction to obtain the desired products, extending the scope of application of the Mannich reaction.26 In this work, acrylic acid, acrylamide and methyl acrylate were used as acid components, glutaraldehyde and diethanolamine were used as the aldehyde component and the amine component, and NaH was used as a catalyst to participate in the Mannich reaction. An amphoteric acrylic acid retanning agent was prepared and used in leather-making, where the retanning and dyeing-assistant properties were investigated.
MA and benzoperoxide were added to a 250 mL flask equipped with a nitrogen gas system and stirred at 80 °C. A certain amount of ethanol was added dropwise into the flask over the course of 1 h and the mixture was stirred for 4 h. PMA was prepared. The reactions are summarised in Fig. 1.
The optimized conditions in terms of GA, DEA and NaH were obtained by orthogonal experiments. The specific parameters are shown in Table 1. Fixing the number of moles of acid components for the Mannich reaction as 1, the molar ratio of the amount of glutaraldehyde, the molar ratio of the amount of diethanolamine, and the percentage of catalyst relative to the overall solids content were chosen as the key factors for optimization.
Level of factor |
n(GA)![]() ![]() |
n(DEA)![]() ![]() |
Amount of catalyst |
---|---|---|---|
1 | 0.8 | 0.8 | 3% |
2 | 1.0 | 1.0 | 5% |
3 | 1.2 | 1.2 | 7% |
4 | 1.4 | 1.4 | 9% |
An orthogonal table, L16 (43), with 3 factors and 4 levels, was selected; the specific experimental parameters are shown in Table 2.
Entry | A | B | C |
---|---|---|---|
1 | 1 | 1 | 1 |
2 | 1 | 2 | 2 |
3 | 1 | 3 | 3 |
4 | 1 | 4 | 4 |
5 | 2 | 1 | 2 |
6 | 2 | 2 | 1 |
7 | 2 | 3 | 4 |
8 | 2 | 4 | 3 |
9 | 3 | 1 | 3 |
10 | 3 | 2 | 4 |
11 | 3 | 3 | 1 |
12 | 3 | 4 | 2 |
13 | 4 | 1 | 4 |
14 | 4 | 2 | 3 |
15 | 4 | 3 | 2 |
16 | 4 | 4 | 1 |
The range size of the orthogonal test data is usually analyzed, including the total response value Ki, the average response value ki and the range value R. Ki means that when the row value in any column of the orthogonal table is i, the sum of the corresponding test results. ki is equal to Ki/s, where s is the number of occurrences at each level in a given column. R is equal to the maximum value of ki minus the minimum value of ki, indicating the degree of influence of each factor on the experimental results.
Process | Chemicals | Dosaged (%) | Temperature (°C) | Time (min) | Remarks | ||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|
a Sodium bicarbonate was diluted with 10 times water (relative to the quality of sodium bicarbonate). b Retanning agent and formic acid were respectively dissolved in 20 times water (relative to the quality of Retanning agent and formic acid). c Synthetic fatliquor was emulsified with hot water. d Based on tare weight of wet-blue. | |||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
Pretreatment | Water | 200 | 45 | 120 | |||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
Degreasing agent | 0.2 | ||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
Wetting agent | 0.5 | ||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
Wash, drain | |||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
Neutralization | Water | 150 | 30 | 30 | |||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
Sodium formate | 1.0 | ||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
Neutralizing syntan | 2.0 | ||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
Sodium bicarbonatea | 1.5 | 30 × 2 | pH 5.5+; drain | ||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
Wash, drain | |||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
Retanning | Water | 100 | 30 | 15 × 4 + 60 | |||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
Retanning agentsb | 10 | ||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
Formic acidb | 1.0 | 20 × 3 + 30 | pH ∼ 3.8 | ||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
Stop operation for 12 h | |||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
Dyeing and fatliquoring | Water | 150 | 50 | ||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
Sodium bicarbonatea | pH ∼ 5.0 | ||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
Black dye | 3 | 60 | |||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
Synthetic fatliquorc | 12 | 60 | |||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
Fixing | Formic acidb | 2.0 | 20 × 3 | pH ∼ 3.5; drain |
![]() | (1) |
![]() | (2) |
Entry |
n(GA)![]() ![]() |
n(DEA)![]() ![]() |
Amount of catalyst | Degree of modification |
---|---|---|---|---|
1 | 1 | 1 | 1 | 50.50% |
2 | 1 | 2 | 2 | 52.00% |
3 | 1 | 3 | 3 | 58.00% |
4 | 1 | 4 | 4 | 55.00% |
5 | 2 | 1 | 2 | 54.00% |
6 | 2 | 2 | 1 | 52.00% |
7 | 2 | 3 | 4 | 61.00% |
8 | 2 | 4 | 3 | 62.50% |
9 | 3 | 1 | 3 | 54.50% |
10 | 3 | 2 | 4 | 62.00% |
11 | 3 | 3 | 1 | 50.50% |
12 | 3 | 4 | 2 | 61.50% |
13 | 4 | 1 | 4 | 55.50% |
14 | 4 | 2 | 3 | 63.00% |
15 | 4 | 3 | 2 | 60.00% |
16 | 4 | 4 | 1 | 51.50% |
k 1 | 53.88% | 53.63% | 51.13% | |
k 2 | 54.88% | 57.25% | 56.88% | |
k 3 | 57.13% | 57.38% | 59.50% | |
k 4 | 57.50% | 57.63% | 58.38% | |
R | 3.62% | 4.00% | 8.37% |
As shown in Fig. 3b, the C–H stretching vibration peak of –CH2– and –CH3– appears at 2851 cm−1, and the CO stretching vibration peak appears at 1701 cm−1. There is a strong absorption peak at 1566 cm−1 in the FT-IR spectrum of MPAA, which was attributed to the stretching vibration of C–N. The C–N structures that appear in the FT-IR spectrum indicated that PAA was modified successfully by the Mannich reaction.
Entry |
n(GA)![]() ![]() |
n(DEA)![]() ![]() |
Amount of catalyst | Degree of modification |
---|---|---|---|---|
1 | 1 | 1 | 1 | 22.50% |
2 | 1 | 2 | 2 | 26.00% |
3 | 1 | 3 | 3 | 29.50% |
4 | 1 | 4 | 4 | 29.00% |
5 | 2 | 1 | 2 | 27.00% |
6 | 2 | 2 | 1 | 25.00% |
7 | 2 | 3 | 4 | 33.50% |
8 | 2 | 4 | 3 | 33.00% |
9 | 3 | 1 | 3 | 28.50% |
10 | 3 | 2 | 4 | 32.50% |
11 | 3 | 3 | 1 | 27.00% |
12 | 3 | 4 | 2 | 32.50% |
13 | 4 | 1 | 4 | 29.00% |
14 | 4 | 2 | 3 | 33.00% |
15 | 4 | 3 | 2 | 32.00% |
16 | 4 | 4 | 1 | 28.50% |
k 1 | 26.75% | 26.75% | 25.75% | |
k 2 | 29.63% | 29.13% | 29.38% | |
k 3 | 30.13% | 30.50% | 31.00% | |
k 4 | 30.63% | 30.75% | 31.00% | |
R | 3.88% | 4.00% | 4.25% |
As shown in Fig. 4b, the O–H stretching vibration peak appears at 3250–3400 cm−1, the N–H stretching vibration peak appears at 3186 cm−1. The peaks at 1456 cm−1 and 1404 cm−1 in the FT-IR spectrum of MPAM were attributed to stretching vibration peaks of –CH– and –CH2– connected to N. The C–N structures appearing in the FT-IR spectrum indicated that PAM was modified successfully by the Mannich reaction.
Entry |
n(GA)![]() ![]() |
n(DEA)![]() ![]() |
Amount of catalyst | Degree of modification |
---|---|---|---|---|
1 | 1 | 1 | 1 | 31.50% |
2 | 1 | 2 | 2 | 35.00% |
3 | 1 | 3 | 3 | 37.50% |
4 | 1 | 4 | 4 | 38.00% |
5 | 2 | 1 | 2 | 35.00% |
6 | 2 | 2 | 1 | 33.50% |
7 | 2 | 3 | 4 | 38.00% |
8 | 2 | 4 | 3 | 38.50% |
9 | 3 | 1 | 3 | 37.50% |
10 | 3 | 2 | 4 | 39.00% |
11 | 3 | 3 | 1 | 32.50% |
12 | 3 | 4 | 2 | 38.50% |
13 | 4 | 1 | 4 | 37.00% |
14 | 4 | 2 | 3 | 37.50% |
15 | 4 | 3 | 2 | 36.00% |
16 | 4 | 4 | 1 | 33.00% |
k 1 | 35.50% | 35.25% | 32.63% | |
k 2 | 36.25% | 36.25% | 36.13% | |
k 3 | 36.88% | 36.00% | 37.75% | |
k 4 | 35.88% | 37.00% | 37.00% | |
R | 1.38% | 1.75% | 5.12% |
As shown in Fig. 5b, the asymmetrical stretching vibration peak of –CH2– appears at 2969 cm−1, and the CO stretching vibration peak appears at 1739 cm−1. There is a stretching vibration peak of N–H at 3330 cm−1 in the FT-IR spectrum of MPMA, and a tensile vibration peak of C–N appears at 1105 cm−1, which indicated that PMA was modified successfully by the Mannich reaction.
The α-H of poly(methyl acrylate) was abstracted by NaH, which was used as the catalyst, to form H2 and the corresponding sodium enolate. Then, sodium enolate reacted with the imine, which was formed by diethanolamine reacting with glutaraldehyde, to form the required Mannich base.
Sample | Mn | Mw | Mp | Mz | Mz + 1 | PDI |
---|---|---|---|---|---|---|
P(AA–AM–MA) | 110![]() |
173![]() |
217![]() |
218![]() |
249![]() |
1.56 |
HCP(AA–AM–MA) | 140![]() |
221![]() |
265![]() |
276![]() |
314![]() |
1.57 |
P(AA–AM–MA) | HCP(AA–AM–MA) | MTA | |
---|---|---|---|
Elongation at break (%) | 78.9 ± 4.3 | 82.0 ± 3.7 | 73.6 ± 6.1 |
Tensile strength (MPa) | 27.4 ± 1.6 | 31.9 ± 2.1 | 22.8 ± 4.3 |
Softness (mm) | 8.1 ± 0.1 | 8.0 ± 0.1 | 21.4 ± 0.6 |
Thickening rate (%) | 19.7 ± 0.3 | 21.4 ± 0.6 | 22.1 ± 0.8 |
Dye uptake (%) | 77.3 ± 0.4 | 91.5 ± 0.2 | 85.5 ± 0.7 |
K/S value | 15.1 ± 0.5 | 18.5 ± 0.15 | 16.5 ± 0.2 |
The elongation at break and tensile strength of HCP(AA–AM–MA)-retanned leather were 82% and 31.9 MPa, respectively, which are higher than those of P(AA–AM–MA)-retanned leather (78.9% and 27.4 MPa). The elongation at break and tensile strength of MTA-retanned leather (73.6% and 22.8 MPa) were poor. The molecular weight of HCP (AA–AM–MA) is higher than that of P (AA–AM–MA), eliminating site differences in leather. Therefore, the physical and mechanical properties of HCP(AA–AM–MA)-retanned leather were better than those of P(AA–AM–MA)-retanned leather.
There was no obvious change in the softness of the leather after retanning with the three retanning agents. As for the thickening rate of crust leather, a higher molecular weight of the retanning agent leads to a higher thickening rate. HCP(AA–AM–MA) has a higher molecular weight, so its thickening rate for leather was higher than that of P(AA–AM–MA).
HCP(AA–AM–MA) (1 kg) | Traditional Mannich reaction modified acrylic retanning agent (1 kg) | |||||
---|---|---|---|---|---|---|
Chemicals | Input (g) | Cost (US $) | Chemicals | Input (g) | Cost (US $) | |
AA | 229.25 | 2.83 | AA | 229.25 | 2.83 | |
AM | 27.25 | 0.40 | AM | 27.25 | 0.40 | |
MA | 7.06 | 0.08 | AN | 55.00 | 4.08 | |
APS | 0.50 | 0.01 | APS | 0.50 | 0.01 | |
NaHSO3 | 36.00 | 0.48 | NaHSO3 | 36.00 | 0.48 | |
NaH | 23.72 | 1.04 | GA | 71.47 | 1.39 | |
THF | 151.60 | 2.98 | Diethanolamine | 93.82 | 0.80 | |
GA | 71.47 | 1.39 | NaOH | 58.00 | 0.51 | |
Diethanolamine | 93.82 | 0.80 | ||||
Total | 10.01 | 10.50 |
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