Abstract
N,N′-Methylenebisacrylamide (MBAA), which is an important raw material in a widely industrial area, was synthesized using convenient catalysts. The synthesized monomer was fully characterized by the elemental analysis, fourier transform infrared (FT-IR) spectroscopy, thermogravimetric analysis (TGA), 1H-NMR, 13C-NMR, GC/MS, and high performance liquid chromatography (HPLC) analysis. Six different homogeneous and heterogeneous catalysts were used to obtain maximum monomer yield. The MBAA was obtained with 95% yield by using Cu(II) catalyst containing carboxylate groups ligands.
Keywords: N,N′-Methylenebisacrylamide; catalyst; monomer synthesis; Cu(II) complex
1. Introduction
MBAA is a molecule that is used as a crosslinking agent in chemical reactions during the formation of polymers. Acrylamide is one of the most common compounds that use MBAA during the polymerization reactions. The bisacrylamide part of the molecule polymerizes with acrylamide and creates a crosslinked structure as opposed to a linear structure. This crosslinking imparts higher strength and toughness to the polymer in its end-use applications. Being a crosslinking agent, MBAA is used in various polymerization reactions to produce polymers and copolymers [1–10]. As a result, this molecule is in great demand in the chemical industry. The growing need for these polymers in waste water treatment, gel electrophoresis, papermaking, ore processing, tertiary oil recovery and the manufacture of permanent press fabrics has been one of the most important factors governing the demand for MBAA. The debated carcinogenic nature of acrylamides in food has been one of the factors restraining the market in this segment. However, the growing need for stable copolymers and composites is expected to move the market for MBAA along steadily in the near future. Although there are other molecules that can be used as substitute materials for MBAA, its versatility and stability in most polymerization reactions related to acrylonitrile boosts the potential for this molecule in the global market. MBAA can be obtained using acrylamide and formaldehyde in the presence of catalysts (Scheme 1). We report the synthesis of monomer with some types of Cu(II), Fe(II), Ni(II) and Pd(II) catalysts. We want to achieve the synthesis of MBAA which is an important raw material in a widely industrial area such as adhesives, coatings, thickeners etc. [11–13]. Methods for the synthesis of some of these compounds have been the tittle in some previous patents, but the yield of synthesis was not enough [14]. We tried several catalysts for the synthesis of the mentioned compound with different yields. In this study, we achieved synthesize of MBAA by using Cu(II) carboxylate catalyst with 95% yield, which is a high and remarkable percentage. No information has been given about the catalyst structure due to make a patent application.
2. Experimental
2.1. Materials and methods
All chemicals were purchased from a major chemical supplier as high or highest purity grade and used without further purification. Catalysts were synthesized in the laboratory. Melting points were determined with a Digital Melting Point Gallenkamp. IR spectra were measured with Thermo Scientific Nicolet IS10 Model FT-IR Spectrophotometer using ATR method with a resolution of 4 cm−1 at room temperature. HPLC analysis was performed for the characterization and purity of MBAA. For the HPLC analysis a Shimadzu HPLC system equipped with a reversed phase C8 column (250 cm × 4.6 mm column dimensions, 5 μm particle sizes, Ascentis®) was used. CH3OH:CH3CN:H2O (50:20:30, v/v) was used for the separation of the mobile phase. The column temperature was 35 °C, the detection wavelength was 254 nm, the flow rate was 1.0 mL min−1 and the retention time was 15 min. TGA analysis was conducted in nitrogen atmosphere with Perkin Elmer Pyris Diamond TG/DTA equipment at a heating rate of 10 °C min−1. 1H-NMR and 13C-NMR analysis were recorded wit a Bruker Avance III HD 600 MHz Ultra Shield TM. GC/MS analysis was performed by using Thermo Brand chromatograph with TR5MS capillary columns.
2.2. Synthesis of MBAA using Cu(II) acetate as a catalyst
A solution of acrylamide (19.90 g, 280 mmol), formaldehyde (4.20 g, 140 mmol), copper(II) acetate (0.10 g, 0.550 mmol), and concentrated HCl (2 mL, 65.65 mmol) were added succesively into the flask. The mixture was refluxed for 90 min and then cooled at room temperature. The solution mixture was separated from the solid phase and dried at room temperature. Yellow solid obtained was 11.20 g. Yield (52%), M. P. > 300 °C. It is interesting to note that when using NaHSO4 (1.60 g, 13.33 mmol) instead of HCl refluxed 2 h, the yield was increased and 12.78 g yellow solid was obatined. Yield was 60%, M. P. > 300 °C.
2.3. Synthesis of MBAA using Cu(II) glyoxime as a catalyst
A solution of acrylamide (19.9 g, 280 mmol), formaldehyde (4.20 g, 140 mmol), Cu(II) glyoxime (0.10 g, 0.66 mmol), and NaHSO4 (1.60 g, 13.33 mmol) were added succesively into the flask. The mixture was refluxed for 2 h and then cooled at room temperature. The solution mixture was separated from the solid phase and dried at room temperature. Yellow solid obtained was 11.20 g. Yield (52%), M. P. > 300 °C.
2.4. Synthesis of MBAA using Pd(II) glyoxime as a catalyst
The preparation of MBAA was similar to that of the synthesis 2.3 except that Pd(II) glyoxime (0.10 g, 0.51 mmol) was used instead of copper(II)-glyoxime.No conversion was observed.
2.5. Synthesis of MBAA using Fe(II) glyoxime as a catalyst
The preparation of MBAA was similar to that of the synthesis 2.3 except that Fe(II) glyoxime (0.10 g, 0.69 mmol) was used instead of copper(II) glyoxime. No conversion was observed.
2.6. Synthesis of MBAA using Ni(II) glyoxime as a catalyst
The preparation of MBAA was similar to that of the synthesis 2.3 except that Ni(II) glyoxime (0.10 g, 0.68 mmol) was used instead of copper(II) glyoxime. No conversion was observed.
2.7. Synthesis of MBAA using Cu(II) carboxylate as a catalyst
The preparation of MBAA was similar to that of the synthesis 2.3 except that Cu(II) carboxylate (0.10 g, 0.12 mmol) was used instead of copper(II) glyoxime. All ingredient were mixed as mentioned above. The mixture was refluxed (80–85 °C) for about two hours then cooled, was filtered out and dried. Yellow solid obtained was 19.85 g. Yield (95%), M. P. > 300 °C. Anal. Calcd. for C7H10N2O2: C, 54.54; H, 6.54; N, 18.17. Found: C, 54.10; H, 6.14; N, 18.34%. IR data (cm−1): 3300(m), 3065(w), 2955(w), 1656(s), 1625(s), 1538(s), 1408(s), 1383(s), 1304(s), 1225(s), 1120(s), 989(s).
3. Results and discussion
3.1. IR spectra
The infrared spectra of the acrylamide and target compound are shown in Figures 1 and 2. The characteristic two N–H stretch absorptions of the primary amine vibrations in the free acrylamide are found between 3300 and 3500 cm−1 (Figure 1). In the infrared spectra of MBAA (Figure 2), absorption band at 3302 cm−1 is assigned to the stretching vibrations of υ(N–H) in the molecule. The absorption related to the υ(C=CH) and υ(C–H) stretching vibrations of the MBAA were observed at 3065 and 2955 cm−1, respectively [15]. The presences of characteristic bands between 1360 and 1080 cm−1 are assigned to absorption vibrations of υ(C=O). The obtained spectral data of MBAA is in good agreement with the HPLC data of MBAA.
3.2. 1H-NMR and 13C-NMR analysis
The 1H-NMR spectra of the compound are shown in Figures S1–S3. 1H-NMR spectra were consistent with the synthesized structure. The 1H-NMR spectral data of the compound were recorded in DMSO taking TMS as an internal standard. The 1H-NMR spectra of the MBAA exhibited expected signals at δ4.74, δ4.89, δ5.72–5.69 and δ6.29–6.22 ppm, respectively. The protons of –CH2 groups (–CH2–NH) of the MBAA gave a signal at δ4.74 ppm. The proton of –NH groups (–NH–CH2) gave a signal at 4.89 ppm. The –CH2 (–CH2=CH) and –CH (–CH=CH2) proton signals were appeared at δ5.70 and δ6.27 ppm, respectively. The 13C-NMR spectral data of the compound were recorded in methanol and is shown in Figures S4 and S5. The 13C-NMR spectrum of the compound exhibited the expected main signals (Scheme 2). The carbonyl group occured at 165.4 ppm. The methine signals were centered at 131.8 ppm and the methylene signals were centered at 126.4 ppm. Small signal assigned to methanol (43.8 ppm) was present. The methylol amide unit of the cross-linker occured as a strong signal at 40.1 ppm. Obtained data were consistent with the synthesized monomer.
3.3. GC/MS analysis
GC-MS analysis was performed to fully characterize the structure of the synthesized monomer. This technique is a useful method for high-sensitivity analysis of volatile organic compounds and it was used for qualitative analysis of synthesized organic compound. Since the MBAA is obtained in high purity, a single chromatogram has been obtained (Figure S6). The obtained single chromatogram was scanned in WinRep library. As a result of the screening, it was determined that the MBAA was obtained with 99.5% probability (Figure S7).
3.4. Termal analysis
TG analysis was used to examine the thermal stability of the MBAA (Figure 3). It was performed in the temperature range of 25–900 °C under N2 atmosphere at 1 atm with a heating rate of 10 °C min−1 on a Perkin Elmer Diamond TG/DTA. The compound is thermally stable up to 150 °C. The TGA curve exhibited two steps of weight losses above this temperature. The first weight loss between 160 and 230 °C is attributable to the loss of aliphatic alkene groups in formula unit. The second significant weight loss between 300 and 450 °C, corresponds to the decomposition of remaining carboxylic and amine groups. As shown in Figure 3, approximately 5% residue remained at the end of the analysis. ICP analysis was performed for the remained residue and no metal remains were observed. Since the TG analysis was carried out in an oxygen-free environment, the residue was carbonized by pyrolysis at 900 °C. In a related study, Yang et al.’s reported that the black residue, which are the carbonized organic species, could be observed at high temperature under N2 atmosphere [16]. For this purpose, after the TG analysis of MBAA, the obtained black residual solids (Figure 4(a)) were heated in muffle furnace at 900 °C under oxygen environment. It was observed that the carbonized monomer completely decomposed (Figure 4(b)). This result supported that the remained residue solid at 900 °C is carbonized solid of MBAA. TGA result is consistent with the structure of the synthesized compound.
3.5. Catalytic activity study
One of the most important advantages of heterogeneous catalysts is the easy recovery from the reaction medium and their high thermal stabilities. In comparison, homogeneous catalysts usually have low thermal stability, and the catalyst cannot be easily recovered from the reaction medium by filtration. The MBAA was characterized by using HPLC. First of all, the retention time of the MBAA was determined by using technical reference MBAA. As shown in Figure 5, the main product and unknown by product were determined.
The conversion values in different catalysts are given in Table 1. MBAA in this study were synthesized by different methods. Some of them were previously presented as patent. Different evaluated catalysts, including Cu(II) and other metals have been carried out. In the old method, Cu(II) catalyst were used with concentrated hydrochloric acid and it was a short and less heat process with 52% yield. Using the 80–85 °C heat process with NaHSO4, we obtained about 60% yields. Although there was a 8% increase of the product, reaction time was two hours. We did not show any catalytic converisons by using M-glyoxime catalysts (M:Cu(II)/Pd(II)/Fe(II)/Ni(II)) in the same catalytic conditions.
Table 1. Catalytic activity results in different reaction conditions.
No. | Reaction conditions | Catalyst | Reaction time (h) | Yield (%) |
---|---|---|---|---|
1 | Water – HCl | Cu(II) acetate | 1.5 | 52 |
2 | Water – NaHSO4 | Cu(II) acetate | 2 | 60 |
3 | Water – NaHSO4 | Cu(II) glyoxime | 2 | No conversion |
4 | Water – NaHSO4 | Pd(II) glyoxime | 2 | No conversion |
5 | Water – NaHSO4 | Fe(II) glyoxime | 2 | No conversion |
6 | Water – NaHSO4 | Ni(II) glyoxime | 2 | No conversion |
7 | Water – NaHSO4 | Cu(II) carboxylate | 2 | 95 |
When using Cu(II)-carboxylate catalyst system, we obtained very high product conversion. The obtained maximum conversion value was 95% with that catalyst. According to HPLC analysis, any by-product was not observed except MBAA by using Cu(II) catalyst at the end of the catalytic studies (Figure 6). The selectivity was approximately 100% for this reaction.
To determine the reusability of the catalyst, we performed same catalytic procedures for several times. Five sequential reactions were performed for 0.10 g catalyst, using Water -NaHSO4 agents for 2 h at 85 °C. After every reuse, the catalyst was separated from the reaction mixture, filtered off, and washed with acetone (5 mL) and water (25 mL) then dried in a vacuum oven at 50 °C and reused. The conversion values did not decrease significantly after four tests (Table S1). These results showed that the catalyst has long usability in that reaction (Figure 7).
As shown in Table 1, no conversions were observed in catalysts containing glyoxime and different metals. The acetate groups present in the catalysts 1 and 2 are also carboxylate groups. They have shown 52 and 60% conversion values, respectively. Similarly, the catalyst formed in copper and carboxylate at number 7 showed maximum conversion value 95%. This high conversion is therefore not only due to the Cu (II) metal and carboxylate groups. It is known that Cu(II) carboxylate has a regular structure. So this high conversion is thought to originate from the morphological structure and surface area of the catalyst. As emphasized in the text, no information has been given about the catalyst structure due to make a patent application.
4. Conclusions
MBAA has been synthesized using acrylamide, formaldehyde and by varying the metal catalysts. The synthesized MBAA was fully characterized by the FT-IR, 1H NMR, 13C-NMR, GC/MS, TGA, and HPLC measurements. It was found that remarkable increase in the percentage of yield of MBAA, when Cu(II) carboxylate is used as a catalyst. It is important to note that this yield is highest value by using copper catalyst. The catalyst has several reusability since it is heterogeneous. This feature makes the catalyst more important than homogeneous ones and it has great industrial importance. After the patent application is completed, industrial production will be implemented on the synthesis of MBAA.
Funding
This work was supported by Small and Medium Sized Industry and Development Organizations (KOSGEB) [project number 46-(2014/ARGE23)].
Supplemental data
The supplemental data for this article can be obtained online at https://doi.org/10.1080/15685551.2017.1332138.
Disclosure statement
No potential conflict of interest was reported by the authors.
Supplementary Material
Acknowledgements
The authors gratefully acknowledge financial support from the Small and Medium Sized Industry and Development Organizations (KOSGEB) (Project No. 46-(2014/ARGE23).
References
- [1]. Li Q, Ma Z, Yue Q, et al. Synthesis, characterization and swelling behavior of superabsorbent wheat straw graft copolymers. Bioresour Technol. 2003;118:204–209. 10.1016/j.biortech.2012.03.028 [DOI] [PubMed] [Google Scholar]
- [2]. Bin Hasan MS. Synthesis and swelling behavior of rice husk based superabsorbent polymer composite. Pahang: Malaysia Pahang University; 2010. [Google Scholar]
- [3]. Zohuriaan-Mehr MJ, Kabiri K. Superabsorbent polymer materials: a review. Iran Polym J. 2008;17(6):451–477. [Google Scholar]
- [4]. Cash D. Superabsorbent polymers (SAP). 6 CHEM 13 NEWS/May 2007. [Google Scholar]
- [5]. Nexant Inc. Superabsorbent polymers (SAP) Nexant Chem System. PERP Program. 2004:1–6.
- [6]. Kabiri K, Omidian H, Hashemi SA, et al. Synthesis of fast-swelling superabsorbent hydrogels: effect of crosslinker type and concentration on porosity and absorption rate. Eur Polym J. 2003;39(7):1341–1348. 10.1016/S0014-3057(02)00391-9 [DOI] [Google Scholar]
- [7]. Yoshio I, Nobuyuki H, Kinya N, et al. Process for preparing absorbent resin. European Patent EP 0,632,068 A1. 1994. Jun 17.
- [8]. Karadağ E, Saraydın D. Swelling of superabsorbent acrylamide/sodium acrylate hydrogels prepared using multifunctional crosslinkers. Turk J Chem. 2002;26:863–875. [Google Scholar]
- [9]. Garner CM, Nething M, Nguyen P. The syhthesis of a superabsorbent polymer. J Chem Educ. 1997;74:95–96. 10.1021/ed074p95 [DOI] [Google Scholar]
- [10]. Moz R. Cosmetic procedures and products market –global industry analysis, size, share, growth, trends and forecast, 2013–2019, Canada. [Google Scholar]
- [11]. SNF Floerger [cited 2017 Jan 5]. Available from: http://www.snf.us/wp-content/uploads/2014/08/Monomers-FLOCRYL-MBAA-E.pdf
- [12]. Dalton PB (Sun Chemical Co.). US Patent 2.576.502 1951. Nov 27.
- [13]. McEntire EE, Sellstrom KB. U.S. Patent 4.675.441 1987. Jun 23.
- [14]. Lundberg LA, Conn S (American Cyanamid Co.). U.S. Patent 2,475,846 1949. Jul 12.
- [15]. Reddy BV, Rao RB. Vibrational spectra and modified valence force field for N, NC-methylenebisacrylamide. Indian J Pure Appl Phys. 2008;46:611–616. [Google Scholar]
- [16]. Yang J-W, Won JS, Jin DY, et al. Preparation of PAN spinning solution with fine dispersion of cellulose microparticles. Adv Mater Sci Eng. 2015;534241:1–8. [Google Scholar]
Associated Data
This section collects any data citations, data availability statements, or supplementary materials included in this article.