# Synthesis and Application of a Spirocompound as Clean Viscosity-Reducer for Crude Oil

Authors: Shijun Chen; Kang Zhao; Gang Chen; Li Bai; Lajun Feng
Journal: Journal of Chemistry
 (2016)

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## Abstract

Heavy oil transportation has become a highly technical operation facing complex difficulties. One of the major difficulties in the pipeline transportation is the high viscosity that requires efficient and economical ways to deal with. The typical polymer viscosity reducers are a negative problem during oil refinement process for their chemical properties. The objective of this study is to seek small molecular compound, different from the traditional polymers, to reduce the viscosity of the crude oil. In this work, a spirocompound, 3,9-diphenyl-2,4,8,10-tetraoxa-spiro[5.5]undecane, was synthesized catalyzed by zeolite and modified zeolite, and the product was fully characterized by NMR, MS, and TG. Then, it was used as viscosity reducer for crude oil. The factors such as dosage and temperature on the viscosity behavior have been studied. The results showed a significant viscosity reduction at different temperature, and the most economical dosage is 500 ppm. The multiphenyl groups can interact with asphaltene by π
-
π stacking, and the spirostructure can fix the stacking in different direction, which can prevent the agglomeration of wax crystals.


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## Body

## 1. Introduction

Oil transportation has become a complex and highly technical operation. One of the major difficulties in the pipeline transportation is the high viscosity that requires efficient and economical ways to deal with [1–3]. Therefore, different methods are used in order to reduce the viscosity of the heavy crude for the pipeline transportation [4, 5], such as dilution with lighter crudes or alcohols, heating, and the use of chemical additives. The typically chemical additives are polymers having a wax-like paraffinic part and a polar component, such as homo- and copolymers of alpha olefins [6], polyalkyl acrylates and methacrylates [7–9], alkyl esters of styrene-maleic anhydride copolymers [10–12], ethylene-vinyl acetate copolymers [13], and alkyl fumarate-vinyl acetate copolymers [14]. But the long molecular chain, large molecular weight, and high thermostability of these polymers are a negative problem during oil refinement process [15]. So it is necessary to seek small molecular crude oil additives. In this paper, a spirocompound, 3,9-diphenyl-2,4,8,10-tetraoxa-spiro[5.5]undecane, was managed to be synthesized and evaluated as a viscosity reducer for crude oil.


## 2. Experimental

### 2.1. Materials

Chemicals were either prepared in our laboratories or purchased from Merck, Fluka, and Aldrich Chemical Companies. All yields refer to isolated products. The products were characterized by comparison of their physical data with those of known samples or by their spectral data. NMR spectrum was recorded in the stated solutions, on a Bruker Drx-500 spectrometer, operating at 500 MHz for1H; δ values are reported in ppm and J values in hertz. Mass spectrum was recorded on a Micromass Platform II spectrometer, using the direct-inlet system operating in the electron impact (EI) mode at 75 eV. Thermal analysis was performed on a TGA/SDTA851e Thermal Analyzer, where the heating rate was 10 K min−1 in the range of 298–880 K.


### 2.2. Method

Initially, the crude oil was homogenized by shaking it for an hour to ensure that the physical properties of the heavy crude oil are the same. After homogenization, the crude oil was used for measurements. The crude oil samples used in this study were obtained from Jinghe Oilfield, China. The density of the used heavy crude oil is 905 kg/m3 at 15°C, and the pour point is 34.8°C. The group compositions of the crude oil are shown in Table 1.Table 1
The group compositions of the crude oil.
Saturated HC (%)
Aromatic HC (%)
Resin (%)
Asphaltene (%)
54.04
25.88
19.24
0.84


### 2.3. Synthesis of 3,9-Diphenyl-2,4,8,10-tetraoxa-spiro[5.5]undecane

Benzaldehyde and pentaerythritol were added in a flask with the molar ratio of 2 : 1, and the toluene was added as the water carrier and the solvent. 5% (wt) solid acid, zeolite, was added as catalyst. The mixture was refluxed until no water can be carried out and was cooled to room temperature. The zeolite was filtrated, and the solvent was evaporated to produce the crude product. Recrystallized in methanol, the pure product was obtained as colorless block. The reaction is described in Scheme1. 1H NMR (500 MHz, CDCl3) δ: 7.22~7.52 (m, 10H), 5.41 (s, 2H), 4.72 (d, J
=
7.5 Hz, 2H), 3.88 (d, J
=
7.5 Hz, 2H), 3.72 (d, J
=
7.0 Hz, 2H), 3.63 (d, J
=
7.0 Hz, 2H); IR (KBr) ν: 3010, 2985, 2885, 1566, 1529, 1480, 1378, 1116 cm−1.Scheme 1
Synthesis of 3,9-diphenyl-2,4,8,10-tetraoxa-spiro[5.5]undecane.


### 2.4. Viscosity of the Treated Crude Oil

Crude oil sample was doped with cyclohexanone pentaerythritol ketal butanol solution with concentrations of 100, 300, 500, 800, or 1000 ppm. The viscosity measurements were carried out at test temperatures of 30–50°C, representative of temperatures greater than, equal to, and lower than the pour point of the crude oil, respectively.


## 2.1. Materials

Chemicals were either prepared in our laboratories or purchased from Merck, Fluka, and Aldrich Chemical Companies. All yields refer to isolated products. The products were characterized by comparison of their physical data with those of known samples or by their spectral data. NMR spectrum was recorded in the stated solutions, on a Bruker Drx-500 spectrometer, operating at 500 MHz for1H; δ values are reported in ppm and J values in hertz. Mass spectrum was recorded on a Micromass Platform II spectrometer, using the direct-inlet system operating in the electron impact (EI) mode at 75 eV. Thermal analysis was performed on a TGA/SDTA851e Thermal Analyzer, where the heating rate was 10 K min−1 in the range of 298–880 K.


## 2.2. Method

Initially, the crude oil was homogenized by shaking it for an hour to ensure that the physical properties of the heavy crude oil are the same. After homogenization, the crude oil was used for measurements. The crude oil samples used in this study were obtained from Jinghe Oilfield, China. The density of the used heavy crude oil is 905 kg/m3 at 15°C, and the pour point is 34.8°C. The group compositions of the crude oil are shown in Table 1.Table 1
The group compositions of the crude oil.
Saturated HC (%)
Aromatic HC (%)
Resin (%)
Asphaltene (%)
54.04
25.88
19.24
0.84


## 2.3. Synthesis of 3,9-Diphenyl-2,4,8,10-tetraoxa-spiro[5.5]undecane

Benzaldehyde and pentaerythritol were added in a flask with the molar ratio of 2 : 1, and the toluene was added as the water carrier and the solvent. 5% (wt) solid acid, zeolite, was added as catalyst. The mixture was refluxed until no water can be carried out and was cooled to room temperature. The zeolite was filtrated, and the solvent was evaporated to produce the crude product. Recrystallized in methanol, the pure product was obtained as colorless block. The reaction is described in Scheme1. 1H NMR (500 MHz, CDCl3) δ: 7.22~7.52 (m, 10H), 5.41 (s, 2H), 4.72 (d, J
=
7.5 Hz, 2H), 3.88 (d, J
=
7.5 Hz, 2H), 3.72 (d, J
=
7.0 Hz, 2H), 3.63 (d, J
=
7.0 Hz, 2H); IR (KBr) ν: 3010, 2985, 2885, 1566, 1529, 1480, 1378, 1116 cm−1.Scheme 1
Synthesis of 3,9-diphenyl-2,4,8,10-tetraoxa-spiro[5.5]undecane.


## 2.4. Viscosity of the Treated Crude Oil

Crude oil sample was doped with cyclohexanone pentaerythritol ketal butanol solution with concentrations of 100, 300, 500, 800, or 1000 ppm. The viscosity measurements were carried out at test temperatures of 30–50°C, representative of temperatures greater than, equal to, and lower than the pour point of the crude oil, respectively.


## 3. Results and Discussion

### 3.1. Synthesis

3,9-Diphenyl-2,4,8,10-tetraoxa-spiro[5.5]undecane has been synthesized using I2 as catalyst with high yield, but it is complex to remove the catalyst after the reaction [16]. In this synthesis, three kinds of zeolite and corresponding sulfonated species were screened, and the results were shown in Figure 1. From the results, it can be found that the catalytic activity is quite different. For the zeolite, NaY and ZSM-5 are active for this reaction, and ZSM-5 is the most effective one with the yield of 97.2%, compared with 3.9% for 4A. After the sulfonation, all the yields are increased. The yield of 3,9-diphenyl-2,4,8,10-tetraoxa-spiro[5.5]undecane increases to 95.0%, 98.2%, and 25.0%, respectively, which may be due to the increased acidity by sulfonation.Figure 1
The yield of 3,9-diphenyl-2,4,8,10-tetraoxa-spiro[5.5]undecane catalyzed by zeolite.In the following work, the effect of the dosage of ZSM-5 on the yield of 3,9-diphenyl-2,4,8,10-tetraoxa-spiro[5.5]undecane was investigated by varying the dosage from 1% to 20%, and the results are shown in Figure2. From the results, it can be seen that the low amount of catalyst is not efficient to cause the reaction to happen. With increasing the amount to 15%, yield of 3,9-diphenyl-2,4,8,10-tetraoxa-spiro[5.5]undecane increases up to 97.2%. The reason for the increased conversion with an increase in the catalyst weight should be attributed to the increase in number of catalytically active sites provided by large amount of ZSM-5. Further increasing the amount of catalyst to 20%, the yield does not increase further.Figure 2
The effect of the dosage of ZSM-5 on the yield of 3,9-diphenyl-2,4,8,10-tetraoxa-spiro[5.5]undecane.


### 3.2. Isomers

For the fixed spirostructure, the 3,9-diphenyl-2,4,8,10-tetraoxa-spiro[5.5]undecane has four kinds of isomers, shown in Figures3(a)–3(d). In molecular (a) and (d), the two phenyl groups aretrans-conformation, and, in molecular (b) and (c), the two phenyl groups arecis-conformation. It should be noticed that molecular (a) can transfer to molecular (d) by rotating with 180°, and molecular (b) can transfer to molecular (c) by the same way as well. So there are two kinds of isomers in fact.Figure 3
The isomers of 3,9-diphenyl-2,4,8,10-tetraoxa-spiro[5.5]undecane.
(a)
(b)
(c)
(d)The NMR spectrum of 3,9-diphenyl-2,4,8,10-tetraoxa-spiro[5.5]undecane shows that multiple peaks atδ 7.22~7.52 (m, 10H) are due to the H of phenyl groups. The single peak at 5.41 (s, 2H) is due to the α-H of the phenyl group, which is inducted by two O atoms resulting in the relatively high chemical shift. For the four CH2 groups, it seems that the four groups are under the same chemical condition and will have the same chemical shift but show four different chemical shifts. Analyzing the stereogenic configuration of isomers (a) and (b) (as shown in Figure 4), it can be found, with the fixed spirostructure, that H atoms of the phenyl groups can correlate with certain stereogenic CH2 group, which can lead to two kinds of CH2 group in each isomer. So as a result, there are four kinds of CH2 groups corresponding to four chemical shifts.Figure 4
The H-H correlations of isomer (a) and (b).
(a)
(b)


### 3.3. Thermal Gravimetric Analysis

The TGA analysis of 3,9-diphenyl-2,4,8,10-tetraoxa-spiro[5.5]undecane was shown in Figure5. It indicates that it is stable below 200°C, but as the temperature increases above 205°C, the crystal starts to lose weight sharply. The first stage of weight loss is only about 1.2% between 25 and 205°C, which may correspond to the loss of absorbed solvent. The second stage of weight loss is about 96% between 205 and 319°C, which corresponds to the decomposition of 3,9-diphenyl-2,4,8,10-tetraoxa-spiro[5.5]undecane. Above 319°C, the remaining weight ratio is only <2.7%, which corresponds to the residues of carbon deposit. The thermal performance indicates 3,9-diphenyl-2,4,8,10-tetraoxa-spiro[5.5]undecane easy decomposition under relative lower temperature than that of polymer, which means it may be a cleaner crude oil additive than polymers additives.Figure 5
The TGA curves of 3,9-diphenyl-2,4,8,10-tetraoxa-spiro[5.5]undecane.


### 3.4. Viscosity-Reducing Performance

3,9-Diphenyl-2,4,8,10-tetraoxa-spiro[5.5]undecane was evaluated as a viscosity reducer for a crude oil, and the results were shown in Figures6 and 7. Figure 6 shows the crude oil viscosity as a function of the dosage under different temperature, respectively. It reduces the crude oil viscosity depending on dosage. At each temperature, the higher the concentrations were, the better the reduction was observed obviously with the dosage below 500 ppm. While the dosage rises up to over 500 ppm (800 ppm and 1000 ppm), the viscosity does not reduce effectively. So the economical use of this kind of viscosity reducer is 500 ppm. Under this condition, the viscosity was reduced from 1460 mPa·s to 882 mPa·s at the relative low temperature of 30°C. If the 1000 ppm was used, the viscosity can be reduced to 186 mPa·s at the 50°C, which can be a usable additive in the present China pipeline transports crude oil. Also, Figure 7 shows the crude oil viscosity is a function of the temperature in the presence of 100, 300, 500, 800, and 1000 ppm, respectively. The behavior of reducing the viscosity after addition of 3,9-diphenyl-2,4,8,10-tetraoxa-spiro[5.5]undecane can thus be attributed to the chemical structure.Figure 6
The relation of dosage and viscosity.Figure 7
The relation of temperature and viscosity.The slight polarity of the benzene ring and the presence of high polarity of oxygen play a role [17, 18]. The steady conformations of isomers (a) and (b) were expressed in Figure 8, which were simulated by a minimized energy of MM2 in Chem 3D. In both conformations, the two phenyl groups display a dihedral angle of about 90°. The multiphenyl groups can interact with asphaltene by π
-
π stacking [19], and the spirostructure can fix the stacking in different direction, which can prevent the agglomeration of wax crystals in crude oil.Figure 8
The steady conformations of isomers (a) and (b).


## 3.1. Synthesis

3,9-Diphenyl-2,4,8,10-tetraoxa-spiro[5.5]undecane has been synthesized using I2 as catalyst with high yield, but it is complex to remove the catalyst after the reaction [16]. In this synthesis, three kinds of zeolite and corresponding sulfonated species were screened, and the results were shown in Figure 1. From the results, it can be found that the catalytic activity is quite different. For the zeolite, NaY and ZSM-5 are active for this reaction, and ZSM-5 is the most effective one with the yield of 97.2%, compared with 3.9% for 4A. After the sulfonation, all the yields are increased. The yield of 3,9-diphenyl-2,4,8,10-tetraoxa-spiro[5.5]undecane increases to 95.0%, 98.2%, and 25.0%, respectively, which may be due to the increased acidity by sulfonation.Figure 1
The yield of 3,9-diphenyl-2,4,8,10-tetraoxa-spiro[5.5]undecane catalyzed by zeolite.In the following work, the effect of the dosage of ZSM-5 on the yield of 3,9-diphenyl-2,4,8,10-tetraoxa-spiro[5.5]undecane was investigated by varying the dosage from 1% to 20%, and the results are shown in Figure2. From the results, it can be seen that the low amount of catalyst is not efficient to cause the reaction to happen. With increasing the amount to 15%, yield of 3,9-diphenyl-2,4,8,10-tetraoxa-spiro[5.5]undecane increases up to 97.2%. The reason for the increased conversion with an increase in the catalyst weight should be attributed to the increase in number of catalytically active sites provided by large amount of ZSM-5. Further increasing the amount of catalyst to 20%, the yield does not increase further.Figure 2
The effect of the dosage of ZSM-5 on the yield of 3,9-diphenyl-2,4,8,10-tetraoxa-spiro[5.5]undecane.


## 3.2. Isomers

For the fixed spirostructure, the 3,9-diphenyl-2,4,8,10-tetraoxa-spiro[5.5]undecane has four kinds of isomers, shown in Figures3(a)–3(d). In molecular (a) and (d), the two phenyl groups aretrans-conformation, and, in molecular (b) and (c), the two phenyl groups arecis-conformation. It should be noticed that molecular (a) can transfer to molecular (d) by rotating with 180°, and molecular (b) can transfer to molecular (c) by the same way as well. So there are two kinds of isomers in fact.Figure 3
The isomers of 3,9-diphenyl-2,4,8,10-tetraoxa-spiro[5.5]undecane.
(a)
(b)
(c)
(d)The NMR spectrum of 3,9-diphenyl-2,4,8,10-tetraoxa-spiro[5.5]undecane shows that multiple peaks atδ 7.22~7.52 (m, 10H) are due to the H of phenyl groups. The single peak at 5.41 (s, 2H) is due to the α-H of the phenyl group, which is inducted by two O atoms resulting in the relatively high chemical shift. For the four CH2 groups, it seems that the four groups are under the same chemical condition and will have the same chemical shift but show four different chemical shifts. Analyzing the stereogenic configuration of isomers (a) and (b) (as shown in Figure 4), it can be found, with the fixed spirostructure, that H atoms of the phenyl groups can correlate with certain stereogenic CH2 group, which can lead to two kinds of CH2 group in each isomer. So as a result, there are four kinds of CH2 groups corresponding to four chemical shifts.Figure 4
The H-H correlations of isomer (a) and (b).
(a)
(b)


## 3.3. Thermal Gravimetric Analysis

The TGA analysis of 3,9-diphenyl-2,4,8,10-tetraoxa-spiro[5.5]undecane was shown in Figure5. It indicates that it is stable below 200°C, but as the temperature increases above 205°C, the crystal starts to lose weight sharply. The first stage of weight loss is only about 1.2% between 25 and 205°C, which may correspond to the loss of absorbed solvent. The second stage of weight loss is about 96% between 205 and 319°C, which corresponds to the decomposition of 3,9-diphenyl-2,4,8,10-tetraoxa-spiro[5.5]undecane. Above 319°C, the remaining weight ratio is only <2.7%, which corresponds to the residues of carbon deposit. The thermal performance indicates 3,9-diphenyl-2,4,8,10-tetraoxa-spiro[5.5]undecane easy decomposition under relative lower temperature than that of polymer, which means it may be a cleaner crude oil additive than polymers additives.Figure 5
The TGA curves of 3,9-diphenyl-2,4,8,10-tetraoxa-spiro[5.5]undecane.


## 3.4. Viscosity-Reducing Performance

3,9-Diphenyl-2,4,8,10-tetraoxa-spiro[5.5]undecane was evaluated as a viscosity reducer for a crude oil, and the results were shown in Figures6 and 7. Figure 6 shows the crude oil viscosity as a function of the dosage under different temperature, respectively. It reduces the crude oil viscosity depending on dosage. At each temperature, the higher the concentrations were, the better the reduction was observed obviously with the dosage below 500 ppm. While the dosage rises up to over 500 ppm (800 ppm and 1000 ppm), the viscosity does not reduce effectively. So the economical use of this kind of viscosity reducer is 500 ppm. Under this condition, the viscosity was reduced from 1460 mPa·s to 882 mPa·s at the relative low temperature of 30°C. If the 1000 ppm was used, the viscosity can be reduced to 186 mPa·s at the 50°C, which can be a usable additive in the present China pipeline transports crude oil. Also, Figure 7 shows the crude oil viscosity is a function of the temperature in the presence of 100, 300, 500, 800, and 1000 ppm, respectively. The behavior of reducing the viscosity after addition of 3,9-diphenyl-2,4,8,10-tetraoxa-spiro[5.5]undecane can thus be attributed to the chemical structure.Figure 6
The relation of dosage and viscosity.Figure 7
The relation of temperature and viscosity.The slight polarity of the benzene ring and the presence of high polarity of oxygen play a role [17, 18]. The steady conformations of isomers (a) and (b) were expressed in Figure 8, which were simulated by a minimized energy of MM2 in Chem 3D. In both conformations, the two phenyl groups display a dihedral angle of about 90°. The multiphenyl groups can interact with asphaltene by π
-
π stacking [19], and the spirostructure can fix the stacking in different direction, which can prevent the agglomeration of wax crystals in crude oil.Figure 8
The steady conformations of isomers (a) and (b).


## 4. Conclusion

The objective of this study is to investigate the small molecular compounds, different from the traditional polymers, to reduce the viscosity of the crude oil. In this work, 3,9-diphenyl-2,4,8,10-tetraoxa-spiro[5.5]undecane was synthesized under optimized conditions. Then, it was evaluated as viscosity reducer for crude oil. A wide range of temperature was covered in this study to examine the effect of temperature on the flow behavior of the crude oil. The results showed that the viscosity was reduced from 1460 mPa·s to 882 mPa·s at the relative low temperature of 30°C with the dosage of 500 ppm; the viscosity can be reduced to 186 mPa·s at the 50°C and with the dosage of 1000 ppm. This work found that the small spirocompound rather than the polymers can be used as viscosity reducer for crude oil.



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*Source: 3827403-2016-03-01.xml*