Ibrahim Y. Yaagoob,
Hasan A. Al-Muallem* and
Shaikh A. Ali*
Chemistry Department, King Fahd University of Petroleum & Minerals, Dhahran 31261, Saudi Arabia. E-mail: hmuallem@kfupm.edu.sa; shaikh@kfupm.edu.sa; Web: http://www.faculty.kfupm.edu.sa/CHEM/hmuallem/ Fax: +966 13 860 4277; Tel: +966 13 860 2378
First published on 20th June 2017
Ammonium persulfate-initiated alternate copolymerization of maleic acid with phosphonic acid monomer [(CH2CH–CH2)2NH+(CH2)3PO3H2Cl−] (I) and phosphonate ester monomer [(CH2
CH–CH2)2NH+(CH2)3PO3Et2Cl−] (II) gave polyzwitterion (PZ): poly[(I–HCl)-alt-maleic acid] III and polyampholyte (PA): poly[(II)-alt-maleic acid] IV, respectively. PA IV, upon ester hydrolysis, gave PZ III. The pH-induced changes of backbone charges in tetraprotic III (with respect to each repeating unit) and diprotic IV were examined by viscosity measurements. PA IV exhibited antipolyelectrolyte character in the presence of neutral salt NaCl. Several protonation constants K of the CO2− and trivalent nitrogen in III and IV have been determined. The performance evaluation as a potential antiscalant in reverse osmosis (RO) plants was examined. III containing acid motifs of –PO3H2 at a concentration of 15 ppm demonstrated remarkable efficiency of ≈100% in inhibition of CaSO4 scale from its supersaturated solution for several days at 40 °C, while precipitation occurred within 10 min in the presence of 20 ppm of IV containing ester motifs of –PO3Et2.
The effectiveness of a desalination process depends on the mitigation of scale formation leading to membrane fouling. In reverse osmosis (RO) membrane desalination, as the concentration of salts, such as calcium sulfate, calcium carbonate, barium sulfate and strontium sulfate, etc., exceeds their saturation levels, the crystallization (i.e. scale formation) on membrane surfaces results in the decline of permeate flux. The feed passages are also often plugged by the scale. There are three commonly employed methods of scale control: acidification, ion exchange softening and antiscalant addition. Antiscalants are surface active materials that interfere with precipitation reactions to keep the scaling salts in supersaturated state.13 As a crystal begins to grow, an antiscalant is adsorbed on its surface thereby disrupting the crystal growth and leading to a soft non-adherent distorted scale. An antiscalant can act as a dispersant; upon adsorption onto a crystal surface, it imparts high anionic charges to keep the crystals separated. The active ingredients in commercial antiscalants are mostly proprietary mixtures of various polycarboxylates and polyacrylates, condensed polyphosphates and organophosphonates.13–15
In this paper, with judicious choice of monomers, Butler cyclopolymerization protocol is utilized to decorate the repeating units with both the carboxylate and phosphonate motifs which are potent functionalities to impart antiscalant behavior. Thus, we report for the first time the copolymerization of 1, 11 and 12 (containing phosphonate pendants) with maleic acid (2) to pH-responsive alternate copolymers (Schemes 1 and 2). The study would examine the mechanism of alternation, the pH-induced transformation and the efficacy of the copolymers as antiscalants.
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Scheme 1 Synthesis of alternate copolymers from monomer 1/maleic acid 2 using cyclopolymerization protocol. |
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Scheme 2 Synthesis of alternate copolymers from monomer 12/maleic acid 2 and monomer complex 13 using cyclopolymerization protocol. |
Entry | Monomer (mmol) | Initiator (APS) (mg) | Yieldb (%) | [η]c (dL g−1) | |||
---|---|---|---|---|---|---|---|
1 | 11 | 12 | 2 | ||||
a Copolymerization reactions were carried out in aqueous solution of two monomers (70 w/w% monomers) in the presence of ammonium persulfate (APS) or (AMPH) at 98° C for 20 min.b Polymer obtained is written in bold followed by isolated yields; the percent conversion determined by 1H NMR analyses of the crude reaction mixture are written in parentheses.c Viscosity of 1–0.25% polymer solution in 0.1 N NaCl at 30° C was measured with Ubbelohde viscometer (K = 0.005317 mm2 s−2).d In the presence of 1 equiv. NaOH.e Polymerization carried out in the presence of 5.0 mmol NaCl.f Polymerization was run for 48 h at 80 °C. | |||||||
1 | 5.0 | — | — | 5.5 | 400 | 4: 55 (90) | 0.0614d |
2 | 5.0 | — | — | 5.0 | 300 | 4: 75 (85) | 0.0872d |
3 | 5.0 | — | — | 5.5 | 300 | 4: 72 (93) | 0.0581d |
4 | 5.0 | — | — | 11.0 | 300 | 4: 66 (91) | 0.0611d |
5 | — | 5.0 | 5.5 | 300 | 14: 66 (98) | 0.0178 | |
6 | — | 10.0 | — | 11.0 | 400 | 15: 73 (90) | 0.0618 |
7e | — | 5.0 | — | 5.5 | 300 | 15: 82 (94) | 0.0253 |
8f | — | 5.0 | — | 5.5 | 60 (AMPH) | 15: 45 (60) | 0.0657 |
Run | ZH2± (mmol) | CTa (mol dm−3) | α-Range | pH-range | Pointsb | Log Ko1c | n1c | R2d |
---|---|---|---|---|---|---|---|---|
a Titrations with NaOH and HCl are described by (−)ve and (+)ve values, respectively.b Data points used.c Parentheses include the standard deviations in the last digit.d R = correlation coefficient.e Log Ki = log Koi + (ni − 1)log[(1 − α)/α]. | ||||||||
1 | 0.2554 (ZH2±) | +0.1222 | 0.03–0.21 | 3.09–2.75 | 11 | 2.54 | 0.36 | 0.9916 |
2 | 0.2812 (ZH2±) | +0.1222 | 0.05–0.21 | 3.08–2.81 | 12 | 2.57 | 0.42 | 0.9887 |
3 | 0.3193 (ZH2±) | +0.1222 | 0.06–0.18 | 3.09–2.85 | 07 | 2.59 | 0.40 | 0.9934 |
Average | 2.58 (3) | 0.41 (4) | ||||||
Log K3e = 2.58 − 0.59 log[(1 − α)/α] for the reaction: ![]() |
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1 | 0.2554 (ZH2±) | −0.09594 | 0.87–0.14 | 3.74–7.74 | 17 | 5.82 | 2.43 | 0.9989 |
2 | 0.3193 (ZH2±) | −0.09594 | 0.88–0.10 | 4.01–8.10 | 19 | 5.83 | 2.33 | 0.9964 |
3 | 0.3831 (ZH2±) | −0.09594 | 0.85–0.20 | 4.06–7.20 | 17 | 5.74 | 2.37 | 0.9965 |
Average | 5.80 (5) | 2.38 (5) | ||||||
Log K2e = 5.80 + 1.38 log[(1 − α)/α] for the reaction: ![]() |
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1 | 0.2554 (ZH2±) | −0.09594 | 0.91–0.58 | 9.65–11.06 | 17 | 11.29 | 1.71 | 0.9911 |
2 | 0.3193 (ZH2±) | −0.09594 | 0.90–0.56 | 9.78–11.17 | 17 | 11.36 | 1.68 | 0.9964 |
3 | 0.3831 (ZH2±) | −0.09594 | 0.88–0.59 | 9.83–11.04 | 18 | 11.31 | 1.73 | 0.9967 |
Average | 11.31 (4) | 1.71 (3) | ||||||
Log K1e = 11.31 + 0.71 log[(1 − α)/α] for the reaction: ![]() |
Run | ZH2± (mmol) | CTa (mol dm−3) | α-Range | pH-range | Pointsb | Log Ko1c | n1c | R2d |
---|---|---|---|---|---|---|---|---|
a Titrations with NaOH is described by (−)ve values.b Data points used.c Parentheses include the standard deviations in the last digit.d R = correlation coefficient.e Log Ki = log Koi + (ni − 1)log[(1 − α)/α]. | ||||||||
Polymer 4 | ||||||||
1 | 0.2416 (ZH4±) | −0.09594 | 0.54–0.09 | 4.65–5.72 | 7 | 4.76 | 0.99 | 0.9842 |
2 | 0.2701 (ZH4±) | −0.09594 | 0.52–0.088 | 4.68–5.66 | 9 | 4.80 | 1.03 | 0.9902 |
3 | 0.2982 (ZH4±) | −0.09594 | 0.51–0.11 | 4.74–5.62 | 9 | 4.74 | 0.96 | 0.9965 |
Average | 4.77 (3) | 0.99 (4) | ||||||
Log K4e = 4.77 − 0.01 log[(1 − α)/α] for the reaction: ![]() |
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1 | 0.2416 (ZH4±) | −0.09594 | 0.89–0.10 | 6.00–8.71 | 9 | 7.27 | 1.59 | 0.9845 |
2 | 0.2701 (ZH4±) | −0.09594 | 0.87–0.12 | 6.05–0.8.65 | 11 | 7.31 | 1.64 | 0.9907 |
3 | 0.2982 (ZH4±) | −0.09594 | 0.86–0.18 | 6.11–8.28 | 8 | 7.21 | 1.62 | 0.9827 |
Average | 7.26 (3) | 1.62 (3) | ||||||
Log K3e = 7.26 + 0.62 log[(1 − α)/α] for the reaction: ![]() |
||||||||
1 | 0.2416 (ZH4±) | −0.09594 | 0.87–0.37 | 9.17–10.43 | 10 | 10.15 | 1.22 | 0.9982 |
2 | 0.2701 (ZH4±) | −0.09594 | 0.85–0.35 | 9.18–10.42 | 12 | 10.20 | 1.29 | 0.9894 |
3 | 0.2982 (ZH4±) | −0.09594 | 0.81–0.30 | 9.19–10.45 | 9 | 9.93 | 1.31 | 0.9913 |
Average | 10.09 (14) | 1.27 (5) | ||||||
Log K2e = 10.09 + 0.27 log[(1 − α)/α] for the reaction: ![]() |
Entry | Sample (ppm) | Percent inhibition at times (min) of | Induction time (min) | |||||
---|---|---|---|---|---|---|---|---|
30 | 60 | 120 | 1000 | 2000 | 14![]() |
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a No induction time was observed.b Three times the concentration of Ca2+ and SO42− found in the concentrated brine of an RO plant. | ||||||||
Polymer 4 | ||||||||
1 | 5 | 100 | 100 | 99 | — | — | — | 170 |
2 | 10 | 100 | 100 | 100 | 100 | 100 | — | 2100 |
3 | 15 | 100 | 100 | 100 | 100 | 100 | 100 | —a |
4 | 20 | 100 | 100 | 100 | 100 | 100 | 100 | —a |
Polymer 15 | ||||||||
5 | 20 | 19 | 5 | — | — | — | — | 10 |
Similar homopolymerization of N-alkyldiallylammonium chloride as well as its copolymerization with maleic acid in aqueous solution using 5 mol% 2,2′-azobis[2-methyl-N-(2-hydroxyethyl)propionamide] (VA086) as initiator for 48 h at 75 °C have been reported to give polymers in low yields (typically below 20%).22,23 High initiator concentrations (up to 5 mol%) were necessary to obtain the polymers, while the use of other initiators (ammonium persulfate, hydrogen peroxide) did not improve the yields.22,23 It is interesting to note in the current work, the use of ammonium persulfate (≈10 mol%) at higher polymerization temperature (98 °C) for a short duration (20 min) afforded the alternate PZ 4 in very good isolated yields (≈70%) (entries 1–4, Table 1). Note that the monomer conversions were ≈90% as determined by 1H NMR analyses; during dialysis, however, low MW molecules left the dialysis tube.
The reactivity ratios for diallylamines/maleic acid copolymerization are very much close to zero, thereby indicating a perfect alternating copolymerization.23 Several reports suggested that the alternating incorporation of the amine and maleic acid monomers may be attributed to the formation of ions pairs (akin to 13, Scheme 2) in solution and their polymerization.24,25 In the current work, both the monomers 1 and 2 are fully protonated, and the extent of ionization in a highly concentrated solution (70:
30 wt ratio of monomer/water) is rather low. This led us to believe that as in the case of the alternating copolymer of styrene and maleic anhydride, the copolymerization described here points towards a preferential combination of electron-rich 1 and electron-poor 2 monomers. Similar argument might as well be put forward against the formation of monomer ion-pair for the cyclopolymerization of 2/12 (Scheme 2). The stronger binding ability of Cl− for the positive nitrogen would preclude the formation of ion-pair involving maleate anion HO2CCH
CHCO2−.
The polymerization of 11/2 monomer-pair as depicted by structure 13 (entries 6–8, Table 1) as well as copolymerization of 12 and 2 (entry 5, Table 1) afforded the same polyampholyte (PA) 15 (Scheme 2). The copolymerization under entry 5 was even run in the presence of NaCl which has excellent ability to bind to positive nitrogen, thereby preventing the maleate to be a part of the ion-pair. The results thus indicate that ion-pair formation is not necessary to form alternate copolymers, rather it is the result of near zero reactivity ratios of the monomers. Note that while the initiator APS afforded copolymers in 20 min reaction-time in very good yields (entries 1–7), the azo initiator AMPH gave polymer 15 in lower yield even after carrying out the polymerization for a duration of 48 h at 80 °C (entry 8).
The isolated yields of the polymers as obtained after dialysis are given in Table 1. However, the actual percent conversion (written in parentheses, Table 1) was determined by 1H NMR analyses (as described below) of the crude reaction mixture. The area A under δ 5.5–6 ppm accounts for 6 olefinic protons of unreacted monomer 12 or 13, while its remaining 20H would appear in the range δ 1.2–4.1 ppm accounting for an area of B [i.e. (A/6) × 20] (Fig. 2a). The total integrated area C in the range δ 1.0–4.1 ppm would belong to area integration of 28H (26H from repeating unit of 12 and 2H from maleic acid 2) of polyzwitterion 15 (Fig. 2c) and 20H of unreacted monomer 12. The area D of the polymer alone would then equate to (C − B). The percent conversion was then calculated using integration of 1H of the polymer 15 and monomer 12 as: 100 × (D/28)/[(D/28) + A/6]. In a similar fashion, the percent conversion to 4 was determined.
Polyzwitterion (±) 4, however, was found to be water-insoluble. pK1 of PO3H2 in (+) 3 and pK1 of CO2H in (+) 14 is expected to be <2 and ≈4, respectively (vide infra). As a result, PO3H− in (±) 4 has more dispersed charge than CO2− in (+ −) 15, thereby making the former motifs less hydrated and hence more capable of manifesting zwitterionic interactions with the positive nitrogens.28 Polyzwitterion 4 was insoluble in salt free water both at room and elevated temperatures (40–70 °C). At 4 wt% in 0.5 M NaCl, PZ 4 was soluble at 0 °C, but became cloudy while heating (50 °C). The lower critical solution temperature (LCST) was determined to be 27 °C. As expected, the PZ was found to be soluble in the presence of NaOH to generate polymers 5–8 (Scheme 1). In the presence of HCl (0.1 M), PZ 4 is transformed to cationic 3 which was found to be water-soluble.
The IR spectra of (±) 4, (+) 14 and (+ −) 15 revealed a strong absorption band at ≈1720 cm−1 attributed to CO stretch of CO2H group. While the absorption peak for CO2− ions in 15 appeared at 1575 cm−1,30 the corresponding peak was absent in the spectrum of 14. Fig. 2 and 3 display the NMR spectra of several polymers. The absence of any signal for residual alkene protons at δ 5.5–6 ppm or carbons at ≈δ 125 ppm suggested the degradative chain transfer31 by abstraction of allylic hydrogens or coupling process for the termination reaction. As compared to homopolymer 1814 (Scheme 2) (Fig. 2b), the spectrum of copolymer (+ −) 15 (Fig. 2c) is broadened presumably as a result of its compact coil conformation and hydrophobic association in aqueous solution.22 The presence of a peak near 180 ppm proves the incorporation of maleic acid in the copolymer (Fig. 3c–e). Note that the 13C NMR signals attributed to the carbons in the polymer backbone marked ‘a’ and ‘b’ are missing in the spectrum of (+ −) 15 (Fig. 3e), while the carbons away from the polymer backbone give well resolved signals. This behavior is a characteristic of many polymerized surfactant, pointing to an immobilization of the polymer backbone. Note that the ester carbons marked ‘h’ and ‘g’ (Fig. 3a, d and e) are absent in the NMR spectra of the hydrolyzed polymers (Fig. 3b and c).
The 13C NMR spectra shed some light on the monomer sequence of repeating units in the current polymers. The backbone carbon marked ‘a’ for homopolymer 19 around δ 27 ppm (Fig. 3b) is shifted downfield in the copolymers' spectra (Fig. 3c and d); the absence of any residual signal around δ 27 ppm points toward a perfect alternation of the repeating units.
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Fig. 4 The viscosity behavior at 30 °C of polyampholyte 15 (entry 6, Table 1) (a) ![]() ![]() ![]() ![]() ![]() ![]() |
The pH-induced changes in the polymer backbone of 14–17 are illustrated in Scheme 3. In 0.1 M HCl, PA (+ −) 15 becomes CPE (+) 14; increased hydrodynamic volume as a result of repulsion among positive charges leads to the increase in the viscosity (Fig. 4c). PA (+ −) 15 is transformed to polyampholyte/anion (+ =) 16 and polydianion (=) 17 upon treatment with one and two equivalents of NaOH, respectively. As expected, the viscosity increases in the presence of NaOH (Fig. 4a and b), the larger charge imbalance in (=) 17 makes it more viscous.
In order to correlate the viscosity values of polyphosphonate ester and polyphosphonic acid, PA (+ −) 15 (entry 6, Table 1) is converted to PZ (±) 4 having identical degree of polymerization. Viscosity plots for PZ (±) 4 are shown in Fig. 5. The pH-induced changes in the polymer backbone of 4–8 are illustrated in Schemes 1 and 4. In the presence of one, two, three and four equivalents of NaOH (per repeating unit), PZ (±) 4 is expected to generate polyzwitterion/anion (PZA) (± −) 5, polyzwitterion/dianion (PZDA) (± =) 6, polyzwitterion/trianion (PZTA) (± ≡) 7, polytetraanion (PTA) (= =) 8, respectively, as the dominant species involved in mobile equilibria with other species. With the increase in NaOH concentrations, the imbalance in favor of negative charges increases, thereby forcing the polymer backbone to adapt more extended conformation to minimize repulsion. This would result in the increase of viscosity values in the order: (= =) 8 > (± ≡) 7 > (± =) 6 > (± −) 5 as determined experimentally (cf. Fig. 5a–d). PZ (±) 4 is insoluble in salt-free water; however, its viscosity plot in 1.0 M NaCl is shown in Fig. 5f. The viscosity plot for PZ (±) 4 in 0.1 M HCl is found to be concave upward, presumably as a result of increasing dissociation to (PZA) (± −) 5 with dilution (Fig. 5e).
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Fig. 5 The viscosity behavior at 30 °C of polyzwitterion 4 (prepared by acid hydrolysis of 15 from entry 6, Table 1) (a) ![]() ![]() ![]() ![]() ![]() ![]() |
The increase in charge imbalance in a polymer backbone leads to an increase in excluded volume, which has been used to rationalize the solution properties of ionic polymers.36–39 Polyzwitterion/anion (PZA) (± −) 5 and polyampholyte/anion (+ =) 16, having identical degree of polymerization, were generated by treating (±) 4 and (+ −) 15, respectively, with one equivalent NaOH. Ionic polymers (± −) 5 and (+ =) 16 having similar imbalances in favor of negative charges were found to have intrinsic viscosity [η] of 0.131 dL g−1 (Fig. 5d) and 0.0928 dL g−1 in 0.1 M NaCl (Fig. 4b). Likewise, polyphosphonic acid derivative polyzwitterion/dianion (PZDA) (± =) 6 was determined to have higher [η] value of 0.168 dL g−1 (Fig. 5c) than the [η] value of 0.120 dL g−1 of diester derivative polydianion (=) 17 having identical DP and charge imbalances (Fig. 4a). The lower [η] values for the ester polymers 16/17 could be attributed to the greater hydrophobic character owing to the presence of ethyl groups in the pendants.
As reported earlier22 and found in the current work, the molar masses of the polymers could not be obtained by GPC presumably owing to the strong interaction of the materials in the GPC column with the amine and carboxy motifs of the polymers. The lower intrinsic values, however, suggest lower molar masses of the polymers because of using higher doses of initiator and a higher temperature of ≈100 °C. Moreover, the degradative chain transfer involving abstraction of allylic hydrogen in the diallylamine salts also lowers the molar masses.31
The molecular weights of the polyzwitterion (±) 4 was estimated from the viscosity data by Mark–Houwink equation ([η] = KMva),40 using K = 1.12 × 10−4 dL g−1 and a = 0.82, which are given for poly(diallyldimethylammonium chloride) for a temperature of 25 °C in 1 M NaCl.41 The [η] of (±) 4 was determined to be 0.0324 dL g−1 (Fig. 5f) which translates into a viscosity average molecular weight Mv ≈ 16640 g mol−1 corresponding to a degree of polymerization of approximately 99 (i.e. number of structural units).
The n values >1 or <1 reflects the “apparent” nature of the basicity constant since the basicity constant changes with the degree of protonation.42,43 A measure of the polyelectrolyte index n is shown in Fig. 6 displaying variation of K with α signifying a polyelectrolyte effect. With increasing α, a gradual decrease of log Ko1 [involving (Z=) 17 + H+ (ZH+ =) 16] and log Ko2 [involving (ZH+ =) 16 + H+
(ZH2+ −) 15] is a result of decreasing overall negative charges that induces protonation. The n values > or <1 confirm the consequence of entropy effects.42,44 PDA (=) 17 having greater charge imbalance is more hydrated than (+ =) 16 which in turn is more hydrated than (+ −) 15. With each protonation, water molecules are released from the hydration shell of the repeating unit that is being protonated. With increasing α, the excess average negative charge in the polymer backbone decreases as does the average number of water molecules in the hydration shell of a repeating unit. Therefore, there will be release of lesser and lesser number of water molecules from the polymer backbones with increasing α, and the associated entropy change dictates the decrease of K with increasing α. The exothermic ΔHo has been reported to be independent of α, the ΔGo is thus controlled by the entropy term.44
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Fig. 6 Plot for the apparent log Ki versus degree of protonation (α) in salt-free water (a) □ (log K3, run 1, Table 3), (b) ■ (log K2, run 3, Table 3) and (c) Δ (log K3, run 3, Table 3). |
The n3 value associated with log Ko3 [involving (ZH2+ −) 15 + H+ (ZH3+) 14] was found to be 0.41. The n value <1 is characteristic of a compact conformation arising out of the presence of ampholytic and zwitterionic motifs. The approach of protons towards (ZH2+ −) 15 becomes easier with the increasing degree of protonation.45,46 The protonation constant log K3 increases progressively with increasing α (Fig. 6a). The macromolecular coil expands as a result of a decrease in the density of the ampholyte motifs (cf. viscosity curves Fig. 4c versus Fig. 4e), thereby exposing the polymer backbone for easier access to protonation. With each protonation, the imbalance in favor of positive charges on the backbone increases. Increased hydration, as a result, leads to entropically favorable release of a greater number of hydrated molecules during protonation.
For polytetraionic (= =) 8, log Ko2, log Ko3 and log Ko4 were determined to be 10.09, 7.26 and 4.77, respectively with the corresponding n values of 1.27, 1.62 and 0.99. Note that the pKa of an acid (HA) is the log Kb (i.e. log[basicity constant]) of its conjugate base (A−). For the pentaprotic acid (ZH5+) 3 and triprotic acid (ZH3+) 14, the pKis of several protic centers are shown in Schemes 3 and 4. The values of pK1 and pK5 were not determined for the reasons mentioned in the experimental, however the pK1 of (ZH5+) 3 (Schemes 1 and 4) is estimated to have a value of <2 since methanephosphonic acid itself is known to have pK1 value of 2.12. The considerable difference is observed in the acidity of the first carboxylic acid groups in 14 (with pK value 2.58) [involving (ZH3+) 14 (ZH2+ −) 15 + H+] (Scheme 3) and 4 (with pK value of 4.77) [involving (ZH4±) 4
(ZH3± −) 5 + H+] (Scheme 4). While the higher acidity of the first CO2H in (ZH3+) 14 is attributable to the electrostatic attraction30,47,48 associated with polyampholyte motifs (ZH2+ −) in its conjugate base 15, the difficulty associated with the removal of a proton from (ZH4±) 4 involves the transformation of a zwitterionic motif to an energetically less favorable zwitterion/anion (ZH3± −) 16 ampholytic/anion (ZH+ =).
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The scaling behavior of a supersaturated solution of CaSO4 containing Ca2+ (2598 ppm) and SO42− (6300 ppm) in the presence of synthesized polymers 4 and 15 was investigated. These are three times the concentration of Ca2+ and SO42− found in the reject brine denoted as 1 CB (i.e. concentrated brine) from a RO plant.49 The PSI by 4 and 15 at various concentrations of the antiscalants is given in Table 4. The onset of CaSO4 precipitation is marked by a sudden drop in the conductivity (Fig. 7). To our satisfaction, the presence of a small concentration (5 ppm) of 4 registered a 99% scale inhibition for about 120 min. In the presence of 10, 15 and 20 ppm of the antiscalant, it registered a PSI of ≈100% for 2000 min. It is indeed astonishing to observe that the antiscalant 4, at a concentration of 15 or 20 ppm, PSI remains ≈100% even after 14000 min (i.e. 9.7 days). An antiscalant needs to be effective at least for a minimum period of ≈30 min which is the residence time for the brine in the osmosis chamber. Note that PA 15 containing ester motifs was ineffective as an antiscalant (Fig. 7) (Table 4); the precipitation of CaSO4 occurred within 10 min as confirmed by a large drop in conductivity. The current PZ 4 has even much superior antiscalant efficacy than its corresponding homopolymer 9 or 10 (Scheme 1).14 As shown in Fig. 7, the onset of precipitation occurs after an induction period. A sharp drop in conductivity is attributed to an accelerated growth of CaSO4 crystals. At a concentration of 5 and 10 ppm, the induction time was observed to be 170 and 2100 min, respectively. For a duration of 14
000 min, induction time was not observed in the presence PZ 4 (15 and 20 ppm). The antiscalant inhibits the crystal growth by complex formation with metal cations, thereby altering the crystal morphology at the time of nucleation.50,51 The precipitation of gypsum, i.e. CaSO4 in mineral form, is an undesirable occurrence in several processes like sea water desalination, water distillation, industrial water recovery and hydrometallurgical operations.52 PZ 4 is remarkably efficient in prolonging the induction period, and thus has the potential to mitigate the membrane fouling as a result of scale formation.
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Fig. 7 Conductivity of a supersaturated solution of CaSO4 in the presence (5, 10, 15, 20 ppm) of 4 and 15 (20 ppm) and in the absence (blank) of antiscalant. |
In comparing the antiscalant activity of 4, 15, 9 or 10, note that polymer 15 with ester motifs cannot bear negative charges on the phosphonate pendants and as such cannot effectively interfere with the positive Ca2+ during nucleation.13–15 The repeating unit in 4 has a greater negative charge density than its homopolymer 9 or 10. The greater negative charges in 4 not only disturb the nucleation process by adsorption onto the developing crystal, they also prevent the agglomeration (i.e. scale formation) by repulsion among the distorted crystals bearing excessive negative charges. The above rationale clearly accounts for the remarkable antiscalant activity of PZ 4.
Some polyzwitterions (PZs) synthesized via cyclopolymerization and their effectiveness as antiscalants in terms of percent scale inhibition (PSI) under conditions like the current work are presented in Scheme 5. Note that PZ 23 performed much better than its counterpart 24 having a monoethyl ester group, thereby confirming the necessity of the presence of the completely hydrolyzed phosphonate motifs to be a better antiscalnt.53 Glutamic acid-based PZ 21,54 aspartic acid-based PZ 2255 and PZ 2512 containing phosphonate and sulfonate pendants as well as 2056 containing carboxyl group in both pendants performed very well imparting similar PSIs. However, the current PZ 4 with greater negative charge density outperformed all the other PZs presented in Scheme 5.
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Scheme 5 Percent scale inhibition (PSI) of some antiscalants synthesized via cyclopolymerization protocol in literature. |
Evaluation of the antiscalant properties using supersaturated solution of CaSO4 revealed that PZ 4 is remarkably effective in inhibiting the formation of calcium sulfate scale for days at 40 °C. The superiority of phosphonic acid motifs in 4 over the phosphonate ester motifs in 15 in scale inhibition is demonstrated as the latter is found to impart no scale inhibition.
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