| Home | E-Submission | Sitemap | Contact Us |  
Environ Eng Res > Volume 27(6); 2022 > Article
Yang, Li, and He: The synthesis of zirconium and tetraethylenepentamine bi-functionalized TiO2 for efficient CO2 adsorption


In the present work, zirconium-doped metal oxide of TiO2(ZrN) was synthesized and functionalized with different amount of tetraethylenepentamine (TEPA). The physical properties of the materials were tested using temperature-programmed desorption of NH3, X-ray diffractometer, X-ray photoelectron spectrometer, scanning electron microscope, transmission electron microscope, energy dispersion spectrum, Inductively coupled plasma atomic emission spectroscopy, Infrared spectrometer, N2 adsorption-desorption analyzer, energy dispersion spectrum and thermogravimetric analyzer. Zr species has a positive effect on the enhancement of the thermal stability and amine utilization. After the introduction of Zr, the decomposition temperature of TEPA is improved to 180°C. Over TEPA decorated adsorbents, physical adsorption and chemical adsorption occurs simultaneously. When the adsorption time is 75°C, CO2 flow rate is 20 mL/min, the adsorbent of TEPA(40)/TiO2(Zr0.1) exhibit a remarkable amine utilization of 83.5%.

1. Introduction

Carbon dioxide (CO2) is one of important raw materials in C1 family [1, 2]. However, it is also a greenhouse gas blamed for the change of global climate [35]. Consequently, CO2 mitigation is arousing wide concern all over the world. In CO2 mitigation technologies, CO2 adsorption with kinds of solid adsorbents receives a great attention because of the large adsorption capacity and less corrosion to the equipment [6]. For efficient adsorption, various organic amine functionalized adsorbents are developed, such as molecular sieves [710], carbon [1114], metal-organic framework (MOFs) materials [1518], polymer [1921] and bimetal materials [22]. However, only a little amine based metal oxides are reported for CO2 adsorption [23, 24].
Compared with the above materials, the most of metal oxides are difficult to be modified with organic amines on account of little functional species on the surface. Recently, heteroatom-doped molecular sieves, such as Zr-MCM-41 [25] and Zr-SBA-15 [26], were synthesized for the loading of organic amines. Over Zr-MCM-41, Zr species was introduced to the framework, leading to the form of Zr-O-Si bonds and the enhancement of Lewis acidity [25]. Based on this, more amines were grafted on the pore channels, resulting in the improvement of thermal stability and CO2 adsorption capacity. The similar phenomenon was also observed over polyethyleneimine loaded Zr-SBA-15 [26]. The interesting results inspire us to design a new type of metal oxide for the successful loading of organic amines and the improvement of CO2 adsorption performance. Compared with amine decorated traditional supports, the adsorbents synthesized in this way may exhibit a high themal stability and a large amine utilization.
The surface properties of titanium dioxide (TiO2) could be modified by introducing heteroatoms to the framework [23, 24]. Therefore, heteroatom-doped TiO2 could be used as the support for the synthesis of amine immobilized adsorbent. Zirconyl chloride octahydrate (ZrOCl2·8H2O), a Lewis acid with many electron holes, is a good candidate for the doping of Zr species [25, 26]. Besides, tetraethylenepentamine (TEPA) is a good agent for CO2 adsorption based on the following properties: 1) TEPA has enough basic sites (N atoms) for the coordination with acidic sites (Zr species). 2) In small organic amines, TEPA has a high N content (37%) which is used as affinity sites in CO2 adsorption. 3) Compared with polyamine, TEPA with small volume and low viscosity is easier to be dispersed well on the surface of porous materials. 4) TEPA is easy to be dissolved in the traditional solvents compared with polyamine. In the present work, Zr-doped metal oxide of TiO2(ZrN) was first successfully prepared and then functionalized with different amount of TEPA. The TEPA based adsorbents were tested for CO2 adsorption under different conditions. In addition, the optimal adsorbent before and after CO2 adsorption was characterized using Infrared spectroscopy to investigate the adsorption mechanism.

2. Experimental

2.1. Synthesis of TiO2, TiO2(ZrN) and TEPA(n)/TiO2(ZrN)

3 g of polyethylene glycol (PEG) and a desired amount of ZrOCl2·8H2O were dissolved in 100 g of deionized water, and 13.7 g of tetrabutyl titanate was then added dropwise to the above solution. After being stirred for 3 h at 70°C, the resulting mixture was hydrothermally treated at 180°C for 48 h. The product was washed thoroughly with deionized water and dried overnight at 120°C. Finally, PEG was removed through the calcination at 500°C for 6 h. The synthesized material is named as TiO2(ZrN), where N stands for the molar ratio of Zr/Ti and the value is 0, 0.025, 0.05, 0.075, 0.1 and 0.125, respectively. When N is 0, no ZrOCl2·8H2O is added to the solution. In this situation, TiO2 was synthesized.
Tetraethylenepentamine (TEPA) functionalized TiO2(ZrN) was synthesized by a wet impregnation method [22, 25]. Typically, a desired amount of TEPA was dissolved in 10 g of ethanol, and followed by the addition of 0.5 g of as-synthesized TiO2(ZrN). The product was stirred for 3 h, and then dried at 120°C for 24 h. The synthesized adsorbents are labelled herein as TEPA(n)/TiO2(ZrN), where n represents the mass ratio of TEPA/TiO2(ZrN).

2.2. Characterization

Zr-doped TiO2 adsorbents before and after functionalization with TEPA were characterized using: 1) temperature-programmed desorption of NH3 (NH3-TPD) in order to analyze the acidic properties; 2) powder X-ray diffraction (XRD) in order to get the information of their phase; 3) X-ray photoelectron spectroscopy (XPS), inductively coupled plasma atomic emission spectroscopy (ICP), infrared spectroscopy (IR) and energy dispersive spectroscopy (EDS) to analyze their structure and element content; 4) N2 adsorption-desorption to prove their pore structure; 5) thermogravimetric analysis (TGA) to illustrate their thermal stability. 6) scanning electron microscope and transmission electron microscope to characterize the morphology and the loading to amine.

2.3. CO2 Adsorption Measurement

Although the concentration of CO2 originating from many industrial processes is about 10–15%, the concentration of CO2 in the atmosphere is much less than this standard value. Moreover, a great number of adsorbents exhibit a large decrease on CO2 adsorption capacity as the diminution of CO2 concentration. Therefore, a lower concentration of CO2 is necessary for the promotion of CO2 adsorption in atmosphere. For this purpose, 5% CO2 and a lower concentration have been used [25, 27, 28].
Similar to our previous work, CO2 adsorption experiment was carried out using a Micromeritics AutoChem II 2920 Chemisorption analyzer [22, 25]. Typically, a desired amount of adsorbent was exposed to a pure argon flow at 100°C in order to remove the impurities adsorbed on the surface. Then, the gas flow was altered to 5% CO2 for the adsorption. In this study, CO2 adsorption capacity was achieved through the integration of the resulted breakthrough curve, which was obtained by detecting CO2 concentration in the residual gas. After 10 min, the adsorbent was regenerated at 100°C in a stream of pure argon flow (100 mL/min). Similar to the previous work [29], CO2 desorption in the system with enough inert gas of Ar is easier than that in the air. In this situation, the majority of CO2 adsorbed in the surface of amine immobilized porous materials could be removed, leading to the regeneration of the adsorbent.

3. Results and Discussion

3.1. Characterization

3.1.1. NH3-temperature-programmed desorption (NH3-TPD)

Fig. 1 shows the NH3-TPD tested results of TiO2 before and after the doping with Zr species. For all of the supports, the desorption peaks within 100 to 500°C are observed. In addition, the acidity increases first and then declines with the rise of Zr/Ti molar ratio. When the molar ratio of Zr/Ti is 0.1, the maximum surface acidity of 0.679 mmol/g is obtained, which is 1.87 times higher than that of TiO2 without Zr species. According to the previous work [25, 26], the ratio of Zr/Si is very important in the adjustment of surface properties. When Zr/Ti ratio is less than 0.1, Zr species could be dispersed well in the framework of the support. The Lewis acidity increases with the rise of the Zr/Ti molar ratio. In this case, more and more amines react with the support, resulting in the increase of CO2 affinity sites. As a result of this, CO2 adsorption capacity is enhanced. When the Zr/Ti molar ratio is 0.1, the Lewis acidity reaches the maximum value, leading to the maximum amount of CO2 adsorption capacity. Further increase of the Zr/Ti molar ratio causes a distortion of the TiO2 network. In addition, the high Zr content results in the low ordering of the structure, even the collapse of the mesoporous structure. Because of these, less amines could be grafted on the support, leading to the decrement of CO2 adsorption capacity. Therefore, Zr/Ti molar ratio of 0.1 is selected for the grafting of TEPA and good CO2 adsorption performance.

3.1.2. Powder X-ray diffraction (PXRD)

Fig. 2 displays the XRD results of TiO2, TiO2(Zr0.1) and the modifier of TEPA(40)/TiO2(Zr0.1). The diffraction pattern of TiO2 is according to that of PDF#29-1360. The peaks at 25.339°, 27.488°, 30.807°, 37.933°, 48.011°, 54.203°, 55.710° and 63.414° are assigned to the crystals of (111), (110), (121), (131), (211), (231), (320) and (151) [30]. With the doping of Zr, the diffraction patterns does not change, indicating that the structure is preserved. However, the intensity of the (111) peak drops a lot. The (111) peak is a characteristic diffraction peaks of orthorhombic TiO2 which is made up by Ti and O atoms. With the doping of Zr, part of Ti atoms in the lattice are replaced by Zr species, leading to the decrement of (111) peak intensity. Over TiO2(Zr0.1), no diffraction peak of ZrO2 is detected, indicating that Zr species is dispersed well in the framework of TiO2. After the loading of 40% of TEPA, the intensity of the diffraction peaks decreased, which is possibly caused by the filling of TEPA. Besides, the peak shift of (110) plane from 27.488° to 27.446° is observed, which could be explained by the reaction between TEPA and the support [31].

3.1.3. Infrared spectroscopy (IR)

Fig. 3 reveals the IR images of TiO2, TiO2(Zr0.1) and TEPA(40)/TiO2(Zr0.1). As seen, the peak at 663 cm−1 on TiO2 is attributed to the Ti-O-Ti bond [30]. The peak moves to 568 cm−1 after the doping of Zr, which could be explained by the formation of Zr-O-Ti bond [32]. On TiO2(Zr0.1), the peak at 1,626 cm−1 is assigned to the bending vibration of physically adsorbed H2O [30]. Compared with TiO2(Zr0.1), TEPA(40)/TiO2(Zr0.1) shows some new peaks. The peaks: 1) at 3,276 cm−1 is assigned to N-H stretching vibrations [33]; 2) at 2,939 cm−1 and 2,826 cm−1 are attributed to the symmetric and asymmetric stretching vibration of C-H [33, 34]; 3) at 1,667 cm−1 and 1,542 cm−1 are related to N-H bending vibration [33, 34]. 4) at 1,441 cm−1 and 1,368 cm−1 are associated with the deformation of C-H bond [34]. The IR results demonstrating that TEPA is successfully incorporated.

3.1.4. X-ray photoelectron spectroscopy (XPS) and inductively coupled plasma atomic emission spectroscopy (ICP)

Fig. 4 reveals the XPS survey scan results of TiO2, TiO2(Zr0.1) and TEPA(40)/TiO2(Zr0.1). As seen in the full spectra, Ti and O are detected on TiO2, Ti, Zr and O species are detected on TiO2(Zr0.1). The appearance of C atom is related to the adsorbed CO2 on the materials. Besides, Zr-O bonds at 181.9 and 184.3 eV are also observed in the spectra of Zr(3d) over TiO2(Zr0.1) (Fig. 4(c)) [35]. The results are in line with that of IR, suggesting that Zr atoms are successfully introduced to the framework of TiO2. After the loading of TEPA, the peaks at 181.9 and 184.3 eV shift to 181.3 and 183.7 eV, respectively. For TiO2(Zr0.1), the peaks at 181.9 and 184.3 eV are related to the formation of Zr-O bond. Besides, TiO2(Zr0.1) has an acidity of 0.679 mmol/g because of the introduction of Zr species. With the loading of TEPA, amine groups with lone-pair electrons react with Zr atoms. Therefore, the peaks shift are detected. In addition, the signals at 398.1, 399.2 and 400.1 eV assigned to N-Zr, N-H and N-C bonds are detected over the modifier (Fig. 4(d)). The results are in accordance with the previous work [22], which is attributed to the reaction between Zr atoms coming from TiO2(Zr0.1) and N species originating from TEPA. The XPS results provide further evidence for the successfully synthesis of TiO2(Zr0.1) and TEPA(40)/TiO2(Zr0.1).
ICP and XPS are used in combination for the detection of elements content. First, the ICP result displays that the content of Zr and Ti are 0.4567 and 2.417 g/L, respectively. Therefore, Zr/Ti molar ratio is 0.0992. The result is very close to the theoretical value of 0.1, demonstrating that Zr has been successfully introduced to TiO2(Zr0.1). Then, the XPS results show that Ti, Zr, O, C atoms are detected over TiO2(Zr0.1) (Table S1). The appearance of Zr and C species are due to the introduction of Zr in the framework of TiO2 and the adsorption of CO2 on the surface. According to the results, the Zr/Ti molar ratio of 0.0993 is calculated. The value is in accordance with that of ICP, demonstrating that TiO2(Zr0.1) is successfully prepared. After the functionalization, N is observed on TEPA(n)/TiO2(Zr0.1). With the rise of TEPA immobilization, the content of N species increases rapidly. However, some C, N and O species in the air are also be detected, leading to a little deviation. The results of XPS provide further evidence for the successful introduction of TEPA.

3.1.5. N2 adsorption-desorption

Fig. S1 and Table S2 illustrate the N2 adsorption-desorption results of TiO2(ZrN) and TEPA(n)/TiO2(Zr0.1). All of Zr-doped TiO2 supports have been characterized by N2 adsorption/desorption technique. When the molar ratio of Zr/Ti is less than 0.1, the supports exhibit large SBET, pore diameter and pore volume. With the rise of Zr/Ti ratio, the SBET, pore diameter and pore volume decrease gradually. Compared with these supports, the material of TiO2(Zr0.125) displays little SBET, pore diameter and pore volume. The results may be caused by the introduction of Zr species in the framework of TiO2. When the molar ratio of Zr/Ti is large than 0.1, new product of ZrO2 may be dispersed on the surface [36]. Therefore, the SBET, pore diameter and pore volume decreased rapidly and TiO2(Zr0.1) is selected as the support in this paper. In addition, the total pore volume decreases but the microporous volume increases with the increase of Zr and TEPA content. The radius of Zr is larger than Ti. With the doping of Zr, a part of Ti atoms are replaced by Zr species. In addition, the loading of TEPA in the pore channels is beneficial to the further decline of pore volume and the formation of micropores. Therefore, there is an enhancement for the microporous volume and a reduction for the total volume.
TiO2(Zr0.1) shows type IV adsorption-desorption curve with a hysteresis loop. Besides, the pore diameter is within 2–40 nm and the pore volume is about 0.261 cm3/g. The results suggest that the Zr-doped support is a mesoporous material. Similar to the previous work [22, 31], the SBET, Vp and dp decrease rapidly with the rise of TEPA content as a result of the pore filling of TEPA. However, all of the pore diameters are within 2–50 nm. Consequently, both of TiO2(Zr0.1) and the modifiers of TEPA(n)/TiO2(Zr0.1) synthesized in this work are mesoporous materials.

3.1.6. Thermogravimetric analysis (TGA)

Fig. S2 displays the TGA profiles of TiO2(Zr0.1) and TEPA(n)/TiO2(Zr0.1). There is little weight loss over TiO2 and TiO2(Zr0.1), indicating that the support is stable before 600°C. Compared with TiO2(Zr0.1), the modifiers exhibit lower thermal stability as a result of the decomposition of TEPA. Similar to the previous work reported by Kuwahara [26], the decomposition temperature of TEPA(n)/TiO2(Zr0.1) is about 180°C, which is 27°C higher than that of TEPA(40)/TiO2 without Zr species. In addition, the thermalstability of TEPA(n)/TiO2(Zr0.1) is also higher than the traditional adsorbents synthesized by loading amines on SiO2 [25, 26], which is attributed to the condonation bond between Zr and N species. The TGA results suggest that Zr species in the framework has a positive influence on the thermal stability of TEPA immobilized TEPA/TiO2(Zr0.1).
With the rise of TEPA/TiO2(Zr0.1) mass ratio, there is an increase of TEPA weight loss. For TEPA(25)/TiO2(Zr0.1), TEPA(30)/TiO2(Zr0.1), TEPA(35)/TiO2(Zr0.1), TEPA(40)/TiO2(Zr0.1), TEPA(45)/TiO2(Zr0.1) and TEPA(50)/TiO2(Zr0.1), the weight loss of TEPA are 7.83, 8.18, 8.9, 9.35, 13.15 and 13.77%, respectively. There is a significant jump in weight loss between TEPA(40)/TiO2(Zr0.1) and TEPA(45)/TiO2(Zr0.1), which may be associated with the viscosity of TEPA. When the mass ratio of TEPA/TiO2(Zr0.1) is large than 40%, TEPA is excess and could not be dispersed well in the solution. These TEPA molecules coats on the surface of the support. These molecules could not be removed at low temperature. Therefore, the jump is observed. In addition, there is a difference between the theoretical load and the actual load. This phenomenon could be explained by the pore structure of TiO2(Zr0.1), the content of Zr, and the intermolecular repulsion of TEPA. First, TiO2(ZrN) is a mesoporous material. However, the pore volume is too small to accommodate all the TEPA molecules. Besides, the content of Zr is limited. The number of acidic sites will decline rapidly with the reaction between Zr and TEPA, leading to the decrement of the attraction between the support and TEPA. Finally, TEPA in the pore channels have an intermolecular repulsion to that outside the pore. Therefore, some TEPA could not get access to the pore channels. Based on these, the difference is observed.

3.1.7. Scanning electron microscope (SEM), Transmission electron microscope (TEM) and Energy dispersion spectrum (EDS)

Scanning electron microscope (SEM) and transmission electron microscope (TEM) of TiO2(Zr0.1) and TEPA(40)/TiO2(Zr0.1) are used to characterize the morphology and the influence of TEPA. As seen, 1) The SEM images of TiO2(Zr0.1) and the modifier tell us that they are composed of lots of big particles (Fig. S3). 2) The EDS result show that Ti, Zr, O and C are detected on TiO2(Zr0.1). The appearance of C species is related to the physically adsorbed CO2. Except from Ti, Zr, O and C, N species is also detected on TEPA(40)/TiO2(Zr0.1), which is associated with the loading of TEPA (Fig. S3). 3) In the TEM images of TiO2(Zr0.1) and TEPA(40)/TiO2(Zr0.1), a number of big particles are observed (Fig. S4). For TiO2(Zr0.1), Ti, Zr and O atoms are detected in the mapping images (Fig. S5). Compared with TiO2(Zr0.1), C and N species are also observed (Fig. S6). Based on these, we confirm that TEPA is successfully grafted on the support.
Combined with the characterization results and the information in the previous work [22], a possible route for the synthesis of TEPA(n)/TiO2(Zr0.1) could be deduced as displayed in Fig. S7. Zr species are introduced to the framework of TiO2 via the formation of Ti-O-Zr bond. Then, TEPA is grafted on the surface of TiO2(ZrN) through the coordination between N and Zr species.

3.2. CO2 Adsorption

3.2.1. Effect of adsorption time and TEPA amount

Fig. 5 reveals the adsorption capacity of TEPA(n)/TiO2(Zr0.1) at 75°C as a function of adsorption time. One can see that 1) all of the adsorbents accomplish CO2 adsorption within 3 min; 2) compare with TiO2 and TiO2(Zr0.1), the modifiers achieve the saturated adsorption capacity within a longer adsorption time, which is related to the reaction between CO2 and –NH2 groups [22, 31]. 3) the capacity of TEPA(n)/TiO2(Zr0.1) increases with the adsorption time and then keep stable. The phenomenon is similar to the previous work reported by Zhang [37], which can be explained by the consumption of affinity sites over the TEPA-functionalized adsorbents. As seen in Table S2, the pore diameters of TEPA grafted adsorbents are large enough for the diffusion of CO2 which kinetic diameter is only 0.33 nm [25, 38]. With the extension of adsorption time, more and more CO2 are introduced to the adsorption system to react with the basic sites. After 3 min, most of the affinity sites are spent for CO2 adsorption. Therefore, there is no significant increase for the adsorption capacity. 4) the capacities of TEPA(n)/TiO2(Zr0.1) are larger than the support of TiO2(Zr0.1) alone, suggesting that TEPA is a good candidate for the enhancement of CO2 adsorption capacity. The phenomenon is similar to that reported by Xu [31], which is attributed to the chemical reaction between –NH2 groups and CO2 molecules. 5) the capacity increases first and then declines with the rise of TEPA content. When TEPA weight percentage is 40wt%, the maximum adsorption capacity of 113.1 mg/g is achieved. Similar to the previous work reported by Xu [31], the optimal adsorption capacity is higher than that of pure TEPA, indicating that the support exhibits a synergetic effect on CO2 adsorption. With the rise of TEPA amount, more and more basic sites coming from –NH2 groups are introduced to the support. When the amount is larger than 40wt%, TEPA is excess. In this situation, the adsorption capacity decreases with the rise of TEPA loading, which could be explained by a more marked pore occlusion and a reduced accessibility of CO2 towards the amine active sites [31].

3.2.2. Effect of adsorption temperature

The influence of adsorption temperature must be taken into consideration based on the great effect on CO2 adsorption. For instance, polyethylenimine (PEI) functionalized Zr-SBA-15 exhibited the optimized adsorption capacity at 75°C [26]. In this work, the effect of adsorption temperature on TEPA(n)/TiO2(Zr0.1) was investigated and the results are revealed in Fig. 6. For all of the TEPA modified adsorbents, the adsorption capacity decreases with the rise of adsorption temperature. According to the previous work [31], physical adsorption and chemical adsorption occur simultaneously on organic amines occluded solid adsorbents. With the increase of temperature, the chemical adsorption equilibrium shifts to the reverse direction, leading to the decrease of chemical adsorption capacity. Moreover, the physical adsorption capacity decreases with the rise of temperature as a result of the exothermic nature on the surface of porous materials [31, 39]. Therefore, the adsorption capacity decreases with the rise of temperature.
Except adsorption conditions, the tested method has a great effect on CO2 adsorption. In the previous work [22, 25, 31], CO2 adsorption was performed using TG analysis technique. In this way, CO2 adsorption is controlled by the diffusion of gas molecules at low temperature, leading to a poor adsorption capacity. With the rise of adsorption temperature, more and more CO2 molecules react with amines, resulting in the enhancement of CO2 adsorption capacity. When the temperature is higher than the optimal point, the adsorption is dominated by the thermodynamic process. In this situation, the capacity decreases with the temperature on account of the exothermic chemical reaction between CO2 and amines. Therefore, CO2 adsorption capacity is low at low temperature. In this study, the adsorption performance was estimated by the breakthrough experiment. Under this condition, gas molecules are easier to get access to the pore channels and react with amines. Based on these, both of the physical and chemical adsorption capacities decrease rapidly with the rise of temperature. Therefore, CO2 adsorption capacity is high at low temperature.
N2 adsorption of the pristine TiO2 (Fig. S1) is highest among all samples but the CO2 adsorption is lowest (Fig. 6). The phenomenon is associated with the reasons as follows: 1) N2 could be adsorbed in the pore channels of TiO2 and TEPA-functionalized adsorbents, which is associated to the physical adsorption. The pore volume is beneficial to N2 adsorption. Compared with TiO2, TEPA(n)/TiO2(Zr0.1) has less pore volumes because of the filling of TEPA molecules. Moreover, the volumes decrease rapidly with the increase of TEPA loading. Therefore, the adsorption capacity of N2 on the pristine TiO2 is higher than the modifiers. 2) Similar to N2 adsorption, CO2 could also be adsorbed on TiO2 on account of physical adsorption. However, the mechanism of CO2 adsorption on TEPA(n)/TiO2(Zr0.1) is different from this. Before TEPA loading, physical adsorption occurs on TiO2(Zr0.1) and the adsorption capacity of 40.3 mg/g is achieved. After the modification, TEPA could be used as basic sites to afford the chemical adsorption of CO2. Over TEPA(n)/TiO2(Zr0.1), amino groups originating from TEPA react with CO2 molecules, resulting in a positive effect on CO2 adsorption. Compared with TiO2, TEPA(n)/TiO2(Zr0.1) has a high content of TEPA. Consequently, the CO2 adsorption is higher than that on TiO2.

3.2.3. Effect of gas flow rate

Fig. 7 displays the adsorption capacity of TEPA(40)/TiO2(Zr0.1) with the rise of gas flow rate. The breakthrough time decreases with the rise of CO2 flow rate because of the decline of contact time between CO2 molecules and basic sites [22, 40]. When the flow rate is less than 20 mL/min, the adsorption capacity increases rapidly as the rise of flow rate and the maximum amount of 131.1 mg/g is achieved. When the flow rate is large than 20 mL/min, a decrement of adsorption capacity is observed. Before the optimal flow rate, the adsorption process over TEPA(40)/TiO2(Zr0.1) is controlled by the diffusion of CO2 molecules [22]. With the rise of CO2 flow rate, more and more gas molecules get access to the pore channels and react with the affinity sites, leading to the enhancement of adsorption capacity. When CO2 flow rate is beyond the optimal value, CO2 adsorption is dominated by the contact time and the change of mass transfer zone [22, 4042]. With the rise of CO2 flow rate, the contact time between N species and CO2 molecules decreases and an the mass transfer zone over TEPA(40)/TiO2(Zr0.1) increases rapidly. Therefore, the capacity decreases with further rise of flow rate.
CO2 adsorption performance over TEPA(40)/TiO2(Zr0.1), traditional amine-docorated metal oxides and Zr-doped molecular sieves is displayed in Table S3. After the doping of Zr, amine immobilized TiO2(Zr0.1) displays a lager adsorption capacity and N utilization. Compared with amine modified Zr-doped molecular sieves and TiO2 [22, 25, 26, 4147], TEPA(40)/TiO2(Zr0.1) exhibits a larger amine utilization. Amine utilization is calculated according to the equation of (1), where qe and q0 are the saturated adsorption capacity of the modifiers and the supports, M1 and M2 are the molecular weight of amine and CO2, WA is the mass of amine per gram of adsorbent.

3.2.4. Recyclability performance

In practical application of CO2 adsorption, the cyclic adsorption-desorption performance should be considered as one of the most significant factors [12, 15, 17, 19, 20, 22, 25, 26]. In the present study, the cyclical adsorption performance of TEPA(40)/TiO2(Zr0.1) at 30°C and 75°C was tested and the results are presented in Fig. 8. As seen, the capacities keep stable at 30°C and 75°C, demonstrating that TEPA(40)/TiO2(Zr0.1) is a good candidate for CO2 adsorption.

3.2.5. CO2 adsorption mechanism

According to the previous work [22], IR experiment could be used for the investigation of CO2 adsorption mechanism over organic amine modified materials. In this study, TEPA(40)/TiO2(Zr0.1) before and after CO2 adsorption were used to afford the task and the results are illustrated in Fig. S8. After the adsorption, CO2 molecules were adsorbed on the surface, leading to the formation of carbamate [22, 48]. Consequently, C-O, C=O and C-N bonds may be detected. In the image of (B), the peaks at 1,305 and 1,576 cm−1 are observed which are assigned to C-O bonds in –COO. Besides, the peaks at 1,408 and 1,527 cm−1 ascribed to the formation of C-N bonds are also detected. In addition, no peak assigned to HCOO3 is observed. The similar results are also achieved on TEPA modified TiO2. In the image of (D), the peaks at: 1) 1,298 and 1,573 cm−1 assigned to C-O bonds in –COO; 2) at 1,408 cm−1 is ascribed to the formation of C-N bonds; 3) at 1,498 cm−1 is attributed to N-H bonds. The phenomenon is similar to the previous work reported by Yang [22] and Liao [48], suggesting that there is a chemical adsorption on the TEPA decorated TiO2 and TiO2(Zr0.1).
In this study, an adsorption capacity of 40.3 mg/g is obtained over TiO2(Zr0.1) without TEPA, suggesting that a physical adsorption occurs on TiO2(Zr0.1). After the modification with TEPA, amino groups react with CO2 molecules, leading to the formation of C-N bond and –COO species. Therefore, we speculate that physical adsorption and chemical adsorption exist simultaneously over TEPA immobilized TiO2(Zr0.1). The adsorption mechanism was displayed in Fig. S9.

4. Conclusions

Zr-doped metal oxide of TiO2(ZrN) was first synthesized and optimized by adjusting Zr/Ti molar ratio. The optimal support of TiO2(Zr0.1) was functionalized with TEPA and tested for CO2 adsorption. Over the modifiers, TEPA molecules are immobilized on the surface through the coordination between N and Zr species. TEPA treated adsorbents display good thermal stability when the temperature is lower than 180°C. Moreover, the adsorbents exhibit good CO2 adsorption performance in a stream of 5% CO2 concentration. With the rise of TEPA/TiO2(Zr0.1) weight ratio, there is an improvement for the adsorption capacity. The similar phenomenon is also observed with the extension of adsorption time and CO2 flow rate. At 75°C, the maximum adsorption capacity of 113.1 mg/g is achieved for TEPA(40)/TiO2(Zr0.1) in a stream of 10 mL/min. After 20 cycles of adsorption-desorption, the adsorption capacity keep stable.

Supplementary Information


The project was funded by the Natural Science Foundation of Hunan Province (No. 2019JJ50026 and 2017JJ2018), the Scientific Research Projects of Hunan Education Department (18B447) and the Key Project Foundation of Hunan Provincial Education Department (29A085). The authors have no competing interests to this manuscript.


Author Contributions

F.M. (Associate Professor) conducted all the experiments and wrote the manuscript. L.J. (Ph.D student) completed literature consultation. G.W. (Professor) revised the manuscript.


1. Stendardo S, Andersen LK, Herce C. Self-activation and effect of regeneration conditions in CO2-carbonate looping with CaO–Ca12Al14O33 sorbent. Chem Eng J. 2020;220:383–394.

2. Zhang YY, Yin SF, Luo SL, et al. Cycloaddition of CO2 to epoxides catalyzed by carboxyl-functionalized imidazolium-based ionic liquid grafted onto cross-linked polymer. Ind Eng Chem Res. 2012;51:3951–3957.

3. Li BY, Duan YH, Luebke D, et al. Advances in CO2 capture technology: A patent review. Appl Energy. 2013;102:1439–1447.

4. Li L, Zhao N, Wei W, et al. A review of research progress on CO2 capture, storage, and utilization in Chinese Academy of Sciences. Fuel. 2013;108:112–130.

5. Wang MH, Joel AS, Ramshaw C, et al. Process intensification for post-combustion CO2 capture with chemical absorption: A critical review. Appl Energy. 2015;158:275–291.

6. Yu CH, Huang CH, Tan CS. A review of CO2 capture by absorption and adsorption. Aerosol Air Qual Res. 2012;12:745–769.

7. Xian SK, Xu FW, Ma C, et al. Vapor-enhanced CO2 adsorption mechanism of composite PEI@ZIF-8 modified by polyethyleneimine for CO2/N2 separation. Chem Eng J. 2015;280:363–369.

8. Ahmed S, Ramli A, Yusup S. Development of polyethylenimine-functionalized mesoporous Si-MCM-41 for CO2 adsorption. Fuel Process Technol. 2017;167:622–630.

9. Quang DV, Soukri M, Tanthana J, et al. Investigation of CO2 adsorption performance and fluidization behavior of mesoporous silica supported polyethyleneimine. Powder Technol. 2016;30:449–462.

10. Wang Y, Du T, Qiu ZY, et al. CO2 adsorption on polyethylenimine-modified ZSM-5 zeolite synthesized from rice husk ash. Mater Chem Phys. 2018;207:105–113.

11. Li M, Xiao R. Preparation of a dual Pore Structure Activated carbon from rice husk char as an adsorbent for CO2 capture. Fuel Process Technol. 2019;186:35–39.

12. Gholidoust A, Atkinson JD, Hashisho Z. Enhancing CO2 adsorption via amine impregnated activated carbon from oil sands coke. Energy Fuels. 2017;31:1756–1763.

13. Rao LL, Ma R, Liu SF, et al. Nitrogen enriched porous carbons from d-glucose with excellent CO2 capture performance. Chem Eng J. 2019;362:794–801.

14. Rahimi K, Riahi S, Abbasi M. Modification of multi-walled carbon nanotubes by 1,3-diaminopropane to increase CO2 adsorption capacity. J Environ Manage. 2019;242:81–89.
crossref pmid

15. Cheng J, Liu N, Hu LQ, et al. Polyethyleneimine entwine thermally-treated Zn/Co zeolitic imidazolate frameworks to enhance CO2 adsorption. Chem Eng J. 2019;364:530–540.

16. Gaikwad S, Kim SJ, Han S. CO2 capture using amine-functionalized bimetallic MIL-101 MOFs and their stability on exposure to humid air and acid gases. Micropor Mesopor Mater. 2019;277:253–260.

17. Kang JH, Yoon TU, Kim SY, et al. Extraordinarily selective adsorption of CO2 over N2 in a polyethyleneimine-impregnated NU-1000 material. Micropor Mesopor Mater. 2019;281:84–91.

18. Yoo DK, Khan NA, Jhung SH. Polyaniline-loaded metal-organic framework MIL-101(Cr): Promising adsorbent for CO2 capture with increased capacity and selectivity by polyaniline introduction. J CO2 Util. 2018;28:319–325.

19. Yin FQ, Zhuang LZ, Luo XY, et al. Simple synthesis of nitrogen-rich polymer network and its further amination with PEI for CO2 adsorption. Appl Surf Sci. 2018;434:514–521.

20. Irani M, Jacobson AT, Gasem KAM, et al. Facilely synthesized porous polymer as support of poly(ethyleneimine) for effective CO2 capture. Energy. 2018;157:1–9.

21. Sujan AR, Pang SH, Zhu GH, et al. Direct CO2 capture from air using poly(ethylenimine)-loaded polymer/silica fiber sorbents. ACS Sustain Chem Eng. 2019;7:5264–5273.

22. Yang FM, Liu Y, Chen L, et al. Synthesis of amine-modified solid Fe-Zr adsorbents for CO2 adsorption. J Chem Technol Biotechnol. 2016;91:2340–2348.

23. Song FJ, Zhao YX, Zhong Q. Adsorption of carbon dioxide on amine-modified TiO2 nanotubes. J Environ Sci. 2013;25:554–560.

24. Song FJ, Zhao YX, Cao Y, et al. Capture of carbon dioxide from flue gases by amine-functionalized TiO2 nanotubes. Appl Surf Sci. 2013;268:124–128.

25. Yang FM, Chen L, Au CT, et al. Preparation of triethylenetetramine-modified zirconosilicate molecular sieve for carbon dioxide adsorption. Environ Prog Sustain Energy. 2015;34:1814–1821.

26. Kuwahara Y, Kang DY, Copeland JR, et al. Dramatic enhancement of CO2 uptake by poly(ethyleneimine) using zirconosilicate supports. J Am Chem Soc. 2012;134:10757–10760.
crossref pmid

27. Harlick PJE, Sayari A. Applications of pore-expanded mesoporous silica. 5. triamine grafted material with exceptional CO2 dynamic and equilibrium adsorption performance. Ind Eng Chem Res. 2007;46:446–458.

28. Yue MB, Chun Y, Cao Y, et al. CO2 capture by as-prepared SBA-15 with an occluded organic template. Adv Funct Mater. 2006;16:1717–1722.

29. Gray ML, Champagne KJ, Fauth D, et al. Performance of immobilized tertiary amine solid sorbents for the capture of carbon dioxide. Int J Greenh Gas Control. 2018;2:3–8.

30. Zhang G, Zhang YC, Nadagouda M, et al. Visible light-sensitized S, N and C co-doped polymorphic TiO2 forphotocatalytic destruction of microcystin-LR. Appl Catal B-Environ. 2014;144:614–621.

31. Xu XC, Song CS, Andresen JM, et al. Novel polyethylenimine-modified mesoporous molecular sieve of MCM-41 type as high-capacity adsorbent for CO2 capture. Energy Fuel. 2012;16:1463–1469.

32. Wang ZM, Zhao K, Guo XL. Crystallization, phase evolution and ferroelectric properties of sol–gel-synthesized Ba(Ti0.8Zr0.2) O3–x(Ba0.7Ca0.3)TiO3 thin films. J Mater Chem C. 2013;1:522–530.

33. Rezaei F, Sakwa-Novak MA, Bali S, et al. Shaping amine-based solid CO2 adsorbents: effects of pelletization pressure on the physical and chemical properties. Micropor Mesopor Mat. 2015;204:34–42.

34. Wang X, Guo Q, Zhao J, et al. Mixed amine-modified MCM-41 sorbents for CO2 capture. Int J Greenh Gas Control. 2015;37:90–98.

35. Yu XJ, Liu JJ, Yun YC, et al. Preparation and visible light photocatalytic activity of carbon quantum dots/TiO2 nanosheet composites. Carbon. 2014;68:718–724.

36. Chien YCP, Wang H, Liu SH, et al. Photocatalytic decomposition of CCl4 on Zr-MCM-41. J Hazard Mater. 2008;151:461–464.

37. Zhang ZH, Ma XL, Wang DX, et al. Development of silica-gel supported polyethylenimine sorbents for CO2 capture from flue gas. AIChE J. 2012;58:2495–2502.

38. An J, Fiorella RP, Geib SJ, et al. Synthesis, structure, assembly, and modulation of the CO2 adsorption properties of a zinc-adeninate macrocycle. J Am Chem Soc. 2009;131:8401–8403.
crossref pmid

39. Zhao XL, Hu X, Hu GS, et al. Enhancement of CO2 adsorption and amine efficiency of titania modified by moderate loading of diethylenetriamine. J Mater Chem A. 2013;1:6208–6215.

40. Zhao Y, Shen Y, Bai L, et al. Carbon dioxide adsorption on polyacrylamide-impregnated silica gel and breakthrough modeling. Appl Surf Sci. 2012;261:708–716.

41. Song F, Zhao YX, Ding H, et al. Capture of carbon dioxide by amine-loaded as-synthesized TiO2 nanotubes. Environ Technol. 2013;34:1405–1410.

42. Yang FM, Liu Y, Chen L, et al. Triethylenetetramine-modified P123-occluded Zr-SBA-15 molecular sieve for CO2 adsorption. Aust J Chem. 2015;68:1427–1433.

43. Kapica-Kozar J, Michalkiewicz B, Wrobel RJ, et al. Adsorption of carbon dioxide on TEPA-modified TiO2/titanate composite nanorods. New J Chem. 2017;41:7870–7885.

44. Kapica-Kozar J, Pirog E, Kusiak-Nejman E, et al. Titanium dioxide modified with various amines used as sorbents of carbon dioxide. New J Chem. 2017;41:1549–1557.

45. Song F, Zhong Q, Ding J, et al. Mesoporous TiO2 as the support of tetraethylenepentamine for CO2 capture from simulated flue gas. RSC Adv. 2013;3:23785–23790.

46. Tumuluri U, Howe JD, Mounfield WP, et al. Effect of surface structure of TiO2 nanoparticles on CO2 adsorption and SO2 resistance. Chem Eng. 2017;5:9295–9306.

47. Mino L, Spoto G, Ferrari AM. CO2 capture by TiO2 anatase surfaces: a combined DFT and FTIR study. J Phys Chem C. 2014;118:25016–25026.

48. Liao Y, Cao S, Yuan YP, et al. Efficient CO2 capture and photoreduction by amine-functionalized TiO2 . Chem-Eur J. 2014;20:10220–10222.

Fig. 1
NH3-TPD profiles of TiO2 and TiO2(ZrN).
Fig. 2
XRD results of TiO2, TiO2(Zr0.1) and TEPA(40)/TiO2(Zr0.1).
Fig. 3
FT-IR spectra of TiO2, TiO2(Zr0.1) and TEPA(40)/TiO2(Zr0.1).
Fig. 4
XPS spectra of TiO2, TiO2(Zr0.1) and TEPA(40)/TiO2(Zr0.1). (a), (b) the full spectrum of TiO2 and TiO2(Zr0.1); (c) Zr(3d) spectrum over TiO2(Zr0.1) and TEPA(40)/TiO2(Zr0.1); (d) N(1s) on TEPA(40)/TiO2(Zr0.1).
Fig. 5
CO2 uptake of TiO2, TiO2(Zr0.1) and TEPA(n)/TiO2(Zr0.1) as a function of adsorption time.
Fig. 6
CO2 adsorption capacity TiO2(Zr0.1) and TEPA(n)/TiO2(Zr0.1) as a function of adsorption temperature. (Conditions: t = 6 min, adsorbate = 5% CO2, flow rate = 10 mL/min)
Fig. 7
CO2 adsorption capacity of TEPA(40)/TiO2(Zr0.1) as a function of gas flow rates.
Fig. 8
Cyclical adsorption performance of TEPA(40)/TiO2(Zr0.1) at 30°C and 75°C (Conditions: t = 6 min, 5% CO2 in a stream of 10 mL/min flow rate).
PDF Links  PDF Links
PubReader  PubReader
Full text via DOI  Full text via DOI
Download Citation  Download Citation
Supplement  Supplement
Editorial Office
464 Cheongpa-ro, #726, Jung-gu, Seoul 04510, Republic of Korea
TEL : +82-2-383-9697   FAX : +82-2-383-9654   E-mail : eer@kosenv.or.kr

Copyright© Korean Society of Environmental Engineers.        Developed in M2PI
About |  Browse Articles |  Current Issue |  For Authors and Reviewers