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Petroleum Science

, Volume 14, Issue 1, pp 195–202 | Cite as

Factors influencing the aggregation behavior of residual associative polymer in produced oily fluids

  • Shi-Jia Chen
  • Bin Chen
  • Hong-Qing Zhu
  • Cheng-Sheng Wang
  • Xiao-Yan Wu
  • Peng Lv
Open Access
Original Paper
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Abstract

The influence of emulsified oil, suspended solids, Fe3+, Fe2+, cationic water clarifier and sulfate-reducing (SR) bacteria on the aggregation behavior of residual hydrophobic modified polyacrylamide in treated oily wastewater from polymer flooding was studied by fluorescence spectroscopy and dynamic light scattering. The result of I 1 /I 3 showed that the polarity of hydrophobic microdomains increased, whereas the size of the hydrophobic microdomains may be decreased, where the value of I 1 /I 3 represents the ratio of the intensity of peak I 1 (374.0 nm) to that of peak I 3 (385.0 nm) of the vibration fine structure of pyrene monomer emission in residual polymer solution. The results of the ratio of I 1 at 48 h to I 1 at 0 h (I 1,48h /I 1,0h) indicated that oil and cationic water clarifier could inhibit the aggregation to some extent, while Fe2+ and suspended solids were helpful for aggregation, and Fe3+ and SR bacteria had no significant influence on the aggregation of polymer.

Keywords

Aggregation behavior Fluorescence spectrum Residual polymer in treated water Hydrophobic modified polyacrylamide 

1 Introduction

Polymer flooding plays a major role in global crude oil recovery (Wever et al. 2011), and this process can enhance oil recovery by 12% compared with water flooding (Shen et al. 2005; Xu et al. 2010; Lin et al. 2008). In recent years, polymer flooding has been widely used in major oil fields of China, such as Daqing and Shengli Oilfields (Gao et al. 2011; Shi et al. 2010, 2012; Feng et al. 2009; Zhang and Yue 2008; Zhang et al. 2008). One of the most widely used water-soluble polymers is partially hydrolyzed polyacrylamide (HPAM), which controls mobility in reservoirs by increasing the viscosity of the injected water, and more importantly, by reducing the permeability of the formation (Lu et al. 2012; Ren et al. 2006; Guo et al. 2014; Lin et al. 2011). Usually, there is residual polymer in treated oily wastewater produced from polymer flooding (TOWPF) (Yang et al. 2014; Li et al. 2012; Lei et al. 2008). TOWPF can be used for reinjection or polymer flooding (Qu et al. 2014; Liu et al. 2010). In addition, there were many other substances in the TOWPF, such as emulsified oil, suspended solids, Fe3+, Fe2+, cationic water clarifier and sulfate-reducing (SR) bacteria. These substances have great influence on the stability of residual polymer. If the polymer is not stable, then it might aggregate and sediment in the buffer vessel, thereby affecting the reinjection process. Therefore, it is necessary to investigate the aggregation behavior of residual polymer in water. Currently, a large number of reports are focused on the effect of temperature and concentration of salt on the aggregation behavior in water of the polymer used in polymer flooding (Han et al. 2012; Zhao et al. 2009; Liu et al. 2016; Zhong et al. 2010). However, no report has been found which discusses the effect of emulsified oil, suspended solids, Fe3+, Fe2+, cationic water clarifier and SR bacteria, on the aggregation behavior of the residual polymer during the treatment process of produced water. Generally, dynamic light scattering (DLS) and fluorescent microscopy methods (Liu et al. 2016; Zhong et al. 2010) are most frequently used to study the aggregation behavior of polymers in water. Hence, these two methods were adopted in this paper to systematically investigate the effects of emulsified oil, suspended solids, Fe3+, Fe2+, cationic water clarifier and SR bacteria on the aggregation behavior of residual polymer. The results should be helpful for analyzing the stability of residual HMPAM in TOWPF.

2 Experiments

2.1 Materials and instruments

TOWPF was taken from SZ36-1 Oilfield in Bohai Bay in China. In this offshore oil field, the oily wastewater treatment process is shown in Fig. 1.
Fig. 1

Oily wastewater treatment process in one offshore oil field in China

The oil displacement agent was hydrophobic modified polyacrylamide (HMPAM). Therefore, there was residual HMPAM in the produced wastewater. The produced wastewater containing HMPAM was treated by skimmer, air floatation and walnut shell filter in turn, and TOWPF was obtained (Zhang et al. 2015a, b), and then the TOWPF flowed into the buffer vessel. The quality of TOWPF is listed in Table 1. In general, the TOWPF would stay in the buffer vessel for about 2–48 h. During this period, precipitates containing HMPAM would appear at the bottom of the buffer vessel (Hu et al. 2013; Tuncal and Uslu 2014). This phenomenon indicated that the stability of residual HMPAM in TOWPF was reduced for some reason.
Table 1

Water quality of TOWPF in buffer vessel in Fig. 1

HMPAM concentration, mg/L

Oil content, mg/L

Suspended solid content, mg/L

Fe3+ + Fe2+ concentration, mg/L

Cationic water clarifier concentration, mg/L

SR bacteria, ind/mL

60

30

15

0.4

40

110

Cationic water clarifier used was provided by the CNOOC EnerTech-Drilling and Production Co. (Tianjin, China). Pyrene was obtained from Aladdin-Reagent Corporation (Shanghai, China).

The fluorescence spectrum was measured with a LS55 fluorescence spectrophotometer (PerkinElmer Corporation, UK).

Dynamic light scattering (DLS) experiments were performed using Brookhaven Instruments 90Plus/BI-MAS (Brookhaven Instruments, NY, USA). Hydrodynamic radius (R h) was obtained from the DLS results and calculation according to the CONTIN algorithm.

Size exclusion chromatography (SEC) analysis was conducted at 30 °C using a Waters 515 liquid chromatograph connected with a Waters 2410 refractive index detector. The gel permeation column was linear ultrahydrogel (7.8 × 300 mm2), and the solvent used was distilled water. Polymer standards of dextran were used according to National Institute for the Control of Pharmaceutical and Biological Products (NICPBP, China). The polymer samples were dissolved in 0.1 M NaCl solution and analyzed at a flow rate of 0.8 mL min−1. The number average molecular weight (M n), weight average molecular weight (M w) and polydispersity index (PDI) of the polymer samples were measured by SEC.

Intrinsic viscosities ([η]) of polymers were measured by the “five-spot” dilution method using an Ubbelohde viscometer at 30 °C, where the solvent was 1 M NaCl solution. Viscosity average molecular weight (M η ) was calculated through the following Eq. (1) (Feng 1999):
$$[\eta ] = 4.75 \times 10^{ - 3} M_{\eta }^{0.80}$$
(1)

2.2 Extraction of residual HMPAM in TOWPF

Firstly, 2 L TOWPF was concentrated to 200 mL. Then, the concentrated TOWPF was purified with an osmotic membrane, with a molecular weight cutoff of 10,000, for 3 days. At last, after vacuum drying for 8 h at 60 °C, the HMPAM was obtained. The structure of HMPAM is shown in Fig. 2. The hydrophobic group in HMPAM molecule is long-chain alkane dimethyl allyl ammonium chloride (the number of carbon atoms in the long-chain alkane is more than 12). The mole content of hydrophobic groups in HMPAM is about 1%.
Fig. 2

Molecular structure of HMPAM

2.3 Aggregation behavior of residual HMPAM

2.3.1 Preparation of residual HMPAM solution containing pyrene

Firstly, 1 L HMPAM aqueous solution (60 mg/L) was prepared by using simulated formation water as solvent (the composition of simulation formation is listed in Table 2). Then, 5 mL of a solution of 500 mg/L pyrene in ethanol was added into the HMPAM aqueous solution. At last, the mixture was allowed to heat at 65 °C for 2 h to remove the ethanol and HMPAM solution containing pyrene was obtained.
Table 2

Composition of simulation formation, mg/L

NaCl

KCl

CaCl2

MgCl2·6H2O

Na2SO4

Na2CO3

NaHCO3

7341

66

764.7

1327

126

25

429

2.3.2 Mixture of residual HMPAM solution containing pyrene with different substances

Firstly, the substances which are listed in Table 1, such as oil, suspended solids and Fe3+, were added, respectively, to 800 mL HMPAM solution containing pyrene (the dosage of substance is given in Table 1).

Then, the mixture was stirred with an emulsifying machine at 7000 r/min for 15 min. At last, the mixture was distributed into four tubulated bottles (see Fig. 3) for the experiments.
Fig. 3

Picture of tubulated bottle

2.3.3 Fluorescence spectrum and DLS

Firstly, four tubulated bottles were kept at 65 °C for 0, 8, 24 and 48 h, respectively. Then, different samples were obtained successively from the bottom of the tubulated bottle. The first 50 mL was the bottom solution, the intermediate 100 mL was the middle solution, and the last 50 mL was the top solution.

The solutions at different layers were filtered by 0.8-μm microporous membrane, and then, the aggregation behavior of residual HMPAM was investigated by using the fluorescence spectrum and DLS result.

Because hydrophobic groups in HMPAM were not water-soluble, they would aggregate and hydrophobic domains can be formed by hydrophobic groups from one HMPAM molecule or several HMPAM molecules (Zhang et al. 2015a, b; Fang et al. 2014). Pyrene would be soluble in the hydrophobic domain. The vibronic structure of the fluorescence spectrum of the monomeric pyrene is known to be sensitive to the local polarity. In particular, the I 1/I 3 ratio of the intensities of the first and third vibronic peaks increases on going from aliphatic to polar solvents (Aguiar et al. 2003; Kim et al. 2000; Ismail 2008) and can be used as an index of the effective local polarity of the pyrene solubilization site in the hydrophobic domain. The ratio I 1/I 3 is the ratio of the intensity of peak I 1 (374.0 nm) to that of peak I 3 (385.0 nm) of the vibration fine structure of pyrene monomer emission. In addition, usually, the I 1 or I 3 would increase with the number of hydrophobic domains because more pyrene can be soluble in the solution when there were more hydrophobic domains. Therefore, the value of I 1 can reflect the number of hydrophobic domains at the same experimental condition, whereas the R h obtained by DLS can reflect the size of HMPAM aggregates.

3 Results and discussion

3.1 Characterization of residual HMPAM

The characterization of residual HMPAM is listed in Table 3.
Table 3

Characterizations of residual HMPAM

M n, g/mol

M w, g/mol

M η , g/mol

PDI

3.61 × 105

1.41 × 106

1.00 × 106

3.91

As shown in Table 3, the molecular weight of residual HMPAM was not high, but its polydispersity was high. Due to the low molecular weight and its amphiphilic property, its mobility may be similar to that of small molecular weight surfactants. There was intermolecular aggregation for residual HMPAM.

3.2 Fluorescence spectrums

Figure 4 shows the fluorescence spectrums of blank residual HMPAM solution at different layers and different times.
Fig. 4

Fluorescence spectra of blank residual HMPAM solution at different layers and different times

The fluorescence spectra of blank residual HMPAM solution at different layers were very close to each other at the same time. With time increasing, the fluorescence intensity increased. Table 4 lists the I 1/I 3 of blank residual HMPAM solution at different layers and I 1,t /I 1,0h at different times. The results showed that the I 1/I 3 data of blank residual HMPAM solution at different layers were close to each other (about 0.85). In addition, the I 1/I 3 was almost not influenced by time. This phenomenon indicated that for the blank residual HMPAM solution, the polarities of hydrophobic domains formed by residual HMPAM were almost the same at different layers. Therefore, the blank residual HMPAM solution was homogeneous and the polarity of hydrophobic domains was almost unchanged over 48 h. The increasing I 1,t /I 1,0h indicated that the number of hydrophobic domains could increase with time because the formation of hydrophobic domains is a slow process for blank residual HMPAM solution.
Table 4

I 1/I 3 of blank residual HMPAM solution at different layers and I 1,t /I 1,0h at different times

Layer

I 1/I 3

Time, h

I 1,t /I 1,0h

8 h

24 h

48 h

Top layer

0.84

0.83

0.84

8

1.06

Middle layer

0.85

0.84

0.88

24

1.38

Bottom layer

0.85

0.83

0.83

48

1.52

Table 5 shows the influence of different substances on the fluorescence spectra of residual HMPAM solution at different layers and different times.
Table 5

Influence of different factors on the fluorescence spectra of residual HMPAM solution at different layers and different times

Layer

I 1/I 3

Time, h

I 1,t /I 1,0h

8 h

24 h

48 h

The influence of oil

 Top layer

1.03

1.02

1.01

8

1.15

 Middle layer

1.01

1.01

1.01

24

1.19

 Bottom layer

1.04

1.01

1.01

48

1.22

The influence of suspended solids

 Top layer

0.97

0.96

0.95

8

1.13

 Middle layer

0.96

0.96

0.95

24

1.37

 Bottom layer

0.97

0.96

0.95

48

1.62

The influence of Fe3+

 Top layer

1.17

1.17

1.18

8

1.07

 Middle layer

1.15

1.18

1.17

24

1.13

 Bottom layer

1.17

1.17

1.18

48

1.55

The influence of Fe2+

 Top layer

1.17

1.18

1.20

8

1

 Middle layer

1.17

1.19

1.18

24

1.40

 Bottom layer

1.17

1.19

1.17

48

1.89

The influence of cationic water clarifier

 Top layer

1.16

1.18

1.18

8

1

 Middle layer

1.16

1.18

1.20

24

1.06

 Bottom layer

1.16

1.18

1.20

48

1.14

The influence of SR bacteria

 Top layer

1.19

1.19

1.20

8

1.24

 Middle layer

1.19

1.20

1.18

24

1.43

 Bottom layer

1.19

1.20

1.19

48

1.50

After addition of these substances into the residual HMPAM solution, the I 1/I 3 of it was much larger than that of blank ones, indicating that the polarity of hydrophobic domain increased, but was not influenced by time. The increasing I 1/I 3 by addition of oil, suspended solids and SR bacteria may attribute to the adsorption of residual HMPAM on these substances. Because of the amphiphilic structure of the HPAM molecule due to the long alkyl chains, the adsorption of HMPAM on the oil, suspended solids and SR bacteria occurs easily. After the adsorption of HMPAM, the hydrophobic group used to form the hydrophobic domains decreased. Therefore, the polarity of the hydrophobic domains increased. The reason why I 1/I 3 increased after addition of Fe3+, Fe2+ and cationic water clarifier may be the chelation between these substances and carboxyl groups in HMPAM. After the chelation, the moving ability and rotation ability of HMPAM decreased and the hydrophobic group used to formation of hydrophobic domains decreased (see Fig. 5). Therefore, the polarity of hydrophobic domain increased.
Fig. 5

Change in aggregation behavior of residual HMPAM after addition of different substances (taking Fe2+ and cationic water clarifier as example)

Table 5 also showed that after addition of different substances, the I 1,t /I 1,0h increased with time. Compared to the I 1,48h/I 1,0h of blank HMPAM solution, after addition of oil and cationic water clarifier, the I 1,48h/I 1,0h data were much smaller. This result suggested that oil and cationic water clarifier could inhibit the increase in the hydrophobic domains. After addition of Fe3+ and SR bacteria, HMPAM solution had similar I 1,48h/I 1,0h as the blank ones, indicating that Fe3+ and SR bacteria almost had no influence on the increase in hydrophobic domains. However, after addition of Fe2+ and suspended solids, the HMPAM solution had much larger I 1,48h/I 1,0h than blank ones, indicating that Fe2+ and suspended solids were favorable to the increase in hydrophobic domains. Usually, increasing the hydrophobic domains means an increasing degree of aggregation. In summary, with Fe2+, HMPAM solution had the largest aggregation degree (I 1,48h/I 1,0h = 1.89); with cationic water clarifier, HMPAM solution had the smallest aggregation degree (I 1,48h/I 1,0h = 1.14). After addition of Fe2+, the chelation between Fe2+ and the carboxyl groups in HMPAM would increase with time over 48 h. Therefore, the number of hydrophobic domains increased significantly with time. Cationic water clarifier had much larger molecular weight and positive charge than Fe2+, and the electrostatic charge neutralization between cationic water clarifier and HMPAM was strong and fast. Addition of cationic water clarifier would result in larger HMPAM aggregates forming quickly. The number of hydrophobic domains would not increase with time significantly over 48 h.

3.3 DLS results

Usually, the increase in the number of hydrophobic domains may be caused by an increasing number of HMPAM aggregates or increasing size of HMPAM aggregates. The results of DLS can show whether the size of HMPAM aggregates increased or not. Figure 6 shows the effects of Fe2+ and cationic water clarifier on the relationship between R h of HMPAM and time. For blank residual HMPAM solution, the R h had no great change with time. When Fe2+ was added in solution, the R h also had no great change with time, indicating that the increase in I 1,t /I 1,0h was caused by the increasing number of HMPAM aggregates. When cationic water clarifier was added in solution, R h had a significant increase, suggesting that the increase in I 1,t /I 1,0h was caused by the increasing size of HMPAM aggregates.
Fig. 6

Effects of Fe2+ and cationic water clarifier on the relationship between R h of HMPAM and time

In addition, when Fe2+ was added in solution, the R h of it was similar to that of blank sample. But when t cationic water clarifier was added in solution, the R h of it was much larger than that of blank ones. The results also confirmed the aggregation behavior of residual HMPAM shown in Fig. 5.

4 Conclusion

In this research, the influences of emulsified oil, suspended solids, Fe3+, Fe2+, cationic water clarifier and SR bacteria on the aggregation behavior of residual HMPAM in TOWPF were studied by fluorescence spectroscopy and DLS. After the addition of these substances into residual HMPAM solution, the I 1/I 3 was much larger than that of blank and not influenced by time. Oil and cationic water clarifier could inhibit the increase in hydrophobic domains. Fe2+ and suspended solids were helpful for the increase in hydrophobic domains. Fe3+ and SR bacteria had no great influence on the increase in hydrophobic domains. In summary, when there was Fe2+, HMPAM solution had the largest aggregation degree by the increasing number of HMPAM aggregates. When there was cationic water clarifier, HMPAM solution had the smallest aggregation degree because of its strong electrostatic charge neutralization with HMPAM.

Notes

Acknowledgements

We acknowledge the supply of SR bacteria by Dr. Guihong Lan, who works in the School of Chemistry and Chemical Engineering, Southwest Petroleum University, in China. This work was supported by the Scientific Research Project of CNOOC (China) (Grant No. CNOOC-KJ 125 ZDXM 06 LTD NFGC 2014-01).

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© The Author(s) 2016

Open AccessThis article is distributed under the terms of the Creative Commons Attribution 4.0 International License (http://creativecommons.org/licenses/by/4.0/), which permits unrestricted use, distribution, and reproduction in any medium, provided you give appropriate credit to the original author(s) and the source, provide a link to the Creative Commons license, and indicate if changes were made.

Authors and Affiliations

  • Shi-Jia Chen
    • 1
    • 2
  • Bin Chen
    • 1
  • Hong-Qing Zhu
    • 1
  • Cheng-Sheng Wang
    • 1
  • Xiao-Yan Wu
    • 1
  • Peng Lv
    • 1
  1. 1.CNOOC EnerTech-Drilling and Production Co.TianjinChina
  2. 2.State Key Laboratory of Offshore Oilfield ExploitationTianjinChina

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