Mesoporous Silica: A Suitable Adsorbent for Amines
© to the authors 2009
Received: 29 January 2009
Accepted: 10 July 2009
Published: 23 July 2009
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© to the authors 2009
Received: 29 January 2009
Accepted: 10 July 2009
Published: 23 July 2009
Mesoporous silica with KIT-6 structure was investigated as a preconcentrating material in chromatographic systems for ammonia and trimethylamine. Its adsorption capacity was compared to that of existing commercial materials, showing its increased adsorption power. In addition, KIT-6 mesoporous silica efficiently adsorbs both gases, while none of the employed commercial adsorbents did. This means that KIT-6 Mesoporous silica may be a good choice for integrated chromatography/gas sensing micro-devices.
Mesoporous materials are proved to be good candidates for gas sensing purposes as well as for many other applications such as environmentally friendly fuels , new generation optical devices , biochemical separations, bioactivity control for medical applications , catalytic adsorption, and molecular sieves [4–6], which have been reported so far. Due to the large surface area of such structures with nano-size pores, mesoporous materials are considered as a good choice for catalytic systems, supports for sophisticated materials, etc. . Among various mesoporous materials studied, mesoporous silica has found a great interest due to its promising physical and chemical properties [8–10]. Various types of mesoporous silica have been produced so far; SBA-15 and KIT-6 are now applied as templates for the synthesis of mesoporous metal oxides for chemical sensors, while other structures such as SBA-16 are also under investigation for gas sensing applications . A complete review of the growth method and achieved structures can be found elsewhere [12, 13].
The template is removed during the preparation process, while the remaining material has a large tendency to receive gas molecules at the surface. Gas sensors based on mesoporous materials use this advantage to show their characteristic response to the target gas. One interesting property of a mesoporous material, on the other hand, can be its adsorption capacity, which means that a large amount of the material touching its surface may remain attached to the surface until a high-temperature desorption process is applied. This means that if performed precisely, such structures may also be good candidates for preconcentrating purposes, especially for low-concentration gases. Bruzzonity et al.  showed that mesoporous silicates have the potentiality to detect environmental pollutants such as trichloroacetic acid (TCA) and haloderivatives (chloroform, 1,1,1-trichloroethane, trichloroethylene, tetrachloroethylene) using chromatography systems.
On the other hand, it is known that preconcentration of amines through adsorption/desorption techniques is rather difficult. Adsorption of ammonia on different surfaces has been a subject of investigation since the 1970s, since this material may be attached to the surface through a chemisorption process leaving some residues after the desorption process [15–17]. Therefore, preparing substrates for effective and reversible adsorption/desorption of amines is an important issue. To our knowledge, this article presents the first results on the application of KIT-6 silica for adsorption/desorption of ammonia (NH3) and trimethylamine (TMA), which can be employed in integrated gas-chromatographic systems .
KIT-6 mesoporous silica was synthesized in acidic conditions using a mixture of Pluronic P123 (BASF) triblock copolymer (EO20PO70EO20) and butanol, as reported in literature [10, 19]: 6 g of P123 was dissolved in 220 g of distilled water and 12 g of concentrated HCl (35%). After 6 h stirring at 35 °C, 6 g of butanol was added while stirring for a further 1 h. Then, 12.48 g of tetraethyl orthosilicate (TEOS, 98%, Aldrich) was added and stirred for 24 h at the same temperature. The mixture was hydrothermally treated at 100 °C for 24 h under static conditions and filtered, washed at room temperature with water, dried in air atmosphere, and calcined at 550 °C.
25 °C (for TMA), 100 °C (for NH3)
Maximum (automatically preformed by preconcentrating device)
For comparison, Hayesep P (of Hayes Separations Inc.123) and Carboxen 569 (of Supelco123) were also purchased and inserted into the glass tubes using the same setup as described for the KIT-6, with the only difference that the amount of KIT-6 used was always 0.1 g.
A portable gas chromatograph (Micro GC 3000, Agilent) with two TCD detectors (for two GC columns that are installed and operated in parallel) was configured to be used for detection of the gases concentrated by preconcentrating material. Two standard columns, “Plot A” and “Plot U”, were selected for these investigations as they are said to be the best columns for the detection of amines according to the providers.123The process was performed/controlled using Soprano software (ver. 2.7.2) developed by SRA-instruments, which takes the responsibility of the entire process from injection to data recording and analysis.
Ammonia samples (in gaseous form, ca. 300 ppm (v/v)) were prepared from a solution of 25% NH3in water (Fluka), whereas TMA samples (in gaseous form, ca. 1,500 ppm (v/v)) were collected from a solution of 45% TMA in water (Fluka). Samples—kept in10 mL glass tubes (evacuated before introducing sample gas)—were injected directly to the preconcentrator.
Variable (Max. 600 s)
Variable (Max. 600 s)
Comparison of results obtained using KIT-6 with those of Carboxen 569 reveals that both materials show almost the same response in “Plot A” column. This was verified through ratio calculation using the Soprano software. In the case of “Plot U”, however, the results differ to some extent; in fact, KIT-6-concentrated sample reveals a wider peak when compared to Carboxen 569 but with almost the same height (not shown here).
In the case of amines (especially TMA), it should be considered that high-concentration TMA liquefies at room temperature and this transition makes it difficult to be sensed using existing sensors or gas chromatographs. Moreover and as revealed in chromatograms, the TMA peak may overlap with a wide peak of humidity. This requires effective removal of humidity before injection.
NH3peaks preconcentrated by KIT-6 and Hayesep P detected by Micro GC
Morrow et al.  showed that if this siloxane bridge is unsymmetrical (one Si atom is electron-deficient), then there will be an initial fast reaction followed by a slow reaction involving highly strained sites, which help chemisorption of NH3 occur at temperatures as low as 20 °C. These strained siloxane rings are normally introduced by applying a force or vacuum treatment of silica at temperatures as high as 800 °C. In the case of mesoporous silica implemented in this work, the calcination temperature has been 550 °C. However, it is very probable that such bridges and rings are formed due to the force applied by surface curvature of nanoparticles. In addition, the existence of water molecules should also be taken into account since they may result in rupture of less-reactive siloxane bridges and form SiOH groups. Moreover, remaining hydroxyl groups can also react with NH3 according to Morrow et al. .
For physisorption of ammonia on silica, the preferred site has been proved to be the hydroxyl group, which is free to bond to ammonia .
One interesting feature of KIT-6, when compared to the commercial materials investigated in this work, can be its functionality for both TMA and ammonia. Carboxen 569 and Hayesep P, as two commercial adsorbent designed for permanent gases and ammonia, respectively, were used for preconcentration of NH3and TMA. A comparison of the peaks (Fig. 5) shows that 30 s of TMA preconcentration with “Hayesep P” results in a peak of about half of the one obtained using KIT-6 under the same conditions. For NH3, as shown in Fig. 4, results are even more interesting since the preconcentration power of KIT-6 is about 15 times larger than that of Carboxen 569. These findings reveal that although both commercial materials can preconcentrate both TMA and ammonia, none of them is as effective as KIT-6, which shows a high adsorption/desorption when exposed to these gases. This is especially important when dilute gases are targeted by the device.
Adsorption of amines on the surface of adsorbents comes with the saturation problem so that a cleaning/conditioning process is needed in order to detach the molecules from the surface effectively. Depending on the material and the gas to be adsorbed, the cleaning step can require high temperatures. For instance, short-time cleaning of the Carboxen 569 at 250 °C and purging with synthetic air do not result in complete desorption of the attached molecules, and cleaning must be performed in several runs. KIT-6 shows the same problem although it takes more runs to be saturated when compared to Carboxen 569. In the case of KIT-6, 1 h cleaning in air at temperatures of about 500 °C was found to remove the adsorbed material effectively.
Gas flow through the adsorbent material is an issue taken into account by producers of commercial materials. This necessitates designing such products in the form of large-grain powders. KIT-6, however, is a compact material that may block flowing gas to some extent. Our observations show that if the total assembly is designed accurately, the problem of KIT-6 is minimized as the total amount of the material needed for preconcentration is quite low thanks to its excellent gas-adsorption properties.
Mesoporous silica was tested as an adsorbent material for both ammonia and trimethylamine. Compared to commercial materials investigated, KIT-6 was found to be more effective, presenting better concentrating power especially in the case of ammonia, which is difficult to be detected by chromatographic systems at low concentrations. Results show that low concentration amines can also be detected thanks to the high adsorption of the gases on the large surface area of the mesoporous structure. Also, none of the commercial materials studied in this work could show effective sensitivity to both gases, while KIT-6 can adsorb/desorb them efficiently. Two limitations, however, may affect the process: back pressure and surface saturation.
1Supelco HayeSep®P 60–80 mesh, descriptions: HayeSep is a registered trademark of Hayes Separations Inc. Adequate temperature range is 20–250 °C, particle size 60–80 mesh, compatible with ammonia, alcohols in water.
2Supelco Carboxen™ 569 20–45 mesh descriptions: Carboxen is a trademark of Sigma–Aldrich Biotechnology LP and Sigma–Aldrich Co. Adequate temperature range is −273–225 °C. Particle size 20–45 mesh, compatible with group of permanent gases.
3HP-“PLOT U” consists of bonded, divinylbenzene/ethylene glycol dimethacrylate coated onto a fused silica capillary, and is suitable for analyzing hydrocarbons (natural gas, refinery gas, C1–C7, all C1–C3 isomers except propylene and propane); CO2, methane, air/CO, water; and polar compounds. In comparison to HP-PLOT Q, HP-”PLOT U” demonstrates greater polarity (RI ethyl acetate 630 vs. 576) and, therefore, different selectivity, better peak shape for some polar compounds like water, and a much lower maximum operating temperature. “PLOT A” is the same as “PLOT U” with one exception: “PLOT A” column is conditioned (by Agilent technologies) to have better sensitivity to amines.
This work has been partially financed by the Spanish Ministry of Education and Science through the projects CROMINA (TEC2004-06854-C03-01) and ISIS (TEC2007-67962-C04-04) and through the program Juan de la Cierva (C.Z).