JP2011240340A - Porous organic-inorganic hybrid material, and adsorbent containing the same - Google Patents

Abstract

PROBLEM TO BE SOLVED: To provide a moisture adsorbent having a high moisture adsorbability and exhibits easy desorption even at a relatively low temperature.SOLUTION: The present invention relates to an adsobent using an iron-containing porous organic-inorganic hybrid material having a large surface area and a large pore volume, particularly to a moisture adsorbent. The present invention relates to an adsorbent which can adsorb and desorb easily even at ≤100°C, has a large adsorption amount per 1 weight of the adsorbent, and can be applied to a humidifier, a dehumidifier and a cooler/heater. The present invention relates also to a novel method for manufacturing a porous organic-inorganic hybrid material, particularly to the manufacturing method using no hydrofluoric acid, and to a porous organic-inorganic hybrid material manufactured by the manufacturing method, and to the use thereof as an adsorbent.

Description

  The present invention relates to a method for producing a porous organic / inorganic hybrid, an adsorbent containing the same, and a catalyst application of the organic / inorganic hybrid. More specifically, the present invention relates to an adsorbent that can be easily adsorbed / desorbed even at a low temperature of 100 ° C. or less and has a large difference between the adsorption amount under the adsorption condition and the adsorption amount under the desorption condition. The present invention also relates to an adsorbent using a porous organic / inorganic hybrid having features of nano-sized pores and a very large surface area and pore volume.

  The present invention also relates to a novel production method for producing a porous organic / inorganic hybrid without using hydrofluoric acid, and a novel use as an adsorbent for the porous organic / inorganic hybrid obtained by the production method. Is.

  In particular, the present invention relates to a novel use as a porous organic / inorganic hybrid adsorbent according to the present invention, and the present invention has a high adsorbed amount per weight of an adsorbent that can be easily adsorbed and desorbed even at 100 ° C. Further, the present invention relates to a moisture adsorbent applicable to a humidifier, a dehumidifier, and a cooling / heating machine. The present invention also relates to an application in which the porous organic / inorganic hybrid of the present invention having a large surface area and uniform pore characteristics is used as an adsorbent having excellent adsorption performance for specific harmful substances.

  The porous organic / inorganic hybrid produced by the present invention can be defined as a porous organic / inorganic polymer compound formed by binding a central metal ion (for example, iron ion) to an organic ligand. The said compound means the crystalline compound which contains both organic substance and inorganic substance in frame | skeleton structure, and has a pore structure of molecular size or nanosize.

  Porous organic / inorganic hybrids are terms in a broad sense, and are generally also referred to as “porous coordination polymers” [Angew. Chem. Intl. Ed. , 43, 2334 (2004)], or “metal-organic frameworks” [Chem. Soc. Rev. 32, 276 (2003)].

  Recently, research has focused on the development of such materials by grafting molecular coordination bonds and materials science. Such materials have high surface area and molecular or nano-sized pores and are not only used in adsorbents, gas storage materials, sensors, membranes, functional thin films, catalysts and catalyst supports. It can be used to collect guest molecules that are smaller than the size of the pores or to separate the molecules according to the size of the molecules using the pores.

  Porous organic / inorganic hybrids have been produced by various methods. Typically, by solvent diffusion near room temperature, or by hydrothermal synthesis in which water is used as a solvent for reaction at high temperature, or by solvent thermal synthesis using an organic solvent. Manufactured [Microporous Mesoporous Mater. 73, 15, 2004; Accounts of Chemical Research, 38, 217, 2005].

  Porous organic / inorganic hybrids are suitable for catalysts, catalyst supports, adsorbents, ion exchange materials and gas storage materials because of their characteristics such as high surface area, very regular crystal structure and relatively high thermal stability. It is recognized that it has unique properties that can be used not only for storage, production and separation of nanomaterials, but also as a nanoreactor. In this regard, Cr-MIL-100 [Bulletin of Korean Chemical Society vol. 1] is a MIL-100 (MIL: Materials of Institute Laborator) structure, which is an organic-inorganic hybrid. 26, p. 880 (2005)] was reported.

  However, as described above, in the case of the organic / inorganic hybrid containing Cr, its applicability can only be relatively limited by the Cr component harmful to the human body. In particular, iron-inorganic / inorganic hybrids with Fe as the central metal that are not harmful to the human body are difficult to be formed by the synthesis method of organic / inorganic hybrids having Cr components, and development of a new manufacturing method for this purpose is required. It became.

In the case of synthesis of a porous organic / inorganic hybrid by hydrothermal synthesis, a mixed acid containing nitric acid, hydrofluoric acid, etc. is generally used to adjust the crystal formation rate. A typical porous organic / inorganic hybrid produced by the hydrothermal synthesis has a chemical formula of Cr ₃ O (H ₂ O) ₂ F [C ₆ H _3- (CO ₂ ) ₃ ] ₂ .nH ₂ O MIL-100 (Cr), which is (n to 14.5), and Cr ₃ F (H ₂ O) ₂ O [C ₆ H ₄ (CO ₂ ) ₂ ] ₃ · nH ₂ O (n to 25). MIL-101 (Cr) and others have been reported [Science 23, 2040, (2005); Accounts of Chemical Research, 38, 217, (2005)]. Moreover, the organic / inorganic hybrid having a metal-organic skeleton structure in which a metal other than Cr is substituted has not been reported yet.

  On the other hand, adsorbents that can easily absorb and desorb moisture have various uses. For example, in the dehumidifier, an adsorbent having a property of desorbing moisture can be used by adsorbing moisture at a low temperature and then heating to a high temperature. In addition, if an adsorbent is used in the air conditioner, the humidity of the outdoor room at low temperature can be adsorbed during heating, and then the moisture can flow into the room and be desorbed in a hot room to replace the role of the humidifier. During cooling, moisture in the room at a low temperature is adsorbed, desorbed outside the room at a high temperature, and the moisture can be sent to the outside, so that a comfortable room atmosphere can be obtained.

  US Pat. Nos. 6,978,635, 6,959,875, 6,675,601 and the like have proposed air conditioners and humidity controllers to which such a concept is applied. However, the adsorbent used in such a device is not described in detail, but only mentions that silica gel, zeolite, ion exchange resin is used, or only adsorbent is used. In addition, in the case of such an adsorbent, not only the adsorption amount is low, but also a high temperature of 100 ° C. or higher is required for desorption, which causes an increase in operating cost.

  Therefore, it is very necessary to develop an adsorbent that can be desorbed even at a low temperature and has a large difference between the amount of adsorption and the amount of desorption. However, if the amount of adsorption increases, desorption is difficult, and if the amount of adsorption is small, there is always a problem that the difference between the amount of adsorption and the amount of desorption is small.

  In the past, activated carbon and hydrophobic zeolite have been mainly used as adsorbents that can remove specific harmful substances in the vapor phase or particle phase containing volatile organic compounds (VOCs) and the like. Activated carbon has developed fine cavities, has a very large specific surface area, has a strong adsorptive power to nonpolar molecules, and has excellent exhaust gas removal, odor removal and decolorization effects, whereas zeolite has 3 It is a hydrophilic adsorbent having a pore diameter of about 10 to 10 mm, and has a strong adsorption characteristic for carbon monoxide, carbon dioxide and moisture. However, most of them have only hydrophobic characteristics, and it is difficult to effectively adsorb and remove volatile organic compounds containing water.

US Pat. No. 6,978,635 US Pat. No. 6,959,875 US Pat. No. 6,675,601

Angew. Chem. Intl. Ed. 43, 2334 (2004) Chem. Soc. Rev. 32, 276 (2003) Microporous Mesoporous Mater. 73, 15, 2004 Accounts of Chemical Research, 38, 217, 2005 Bulletin of Korean Chemical Society vol. 26, p. 880 (2005) Science 23, 2040, (2005)

  Thereby, in the first aspect of the present invention, an adsorbent having a high moisture adsorption amount and being easily desorbed even at a relatively low temperature of 100 ° C. or lower, for example, 60 to 80 ° C., is provided. Provide an adsorbent that is superior in adsorption amount and adsorption characteristics by using a hybrid of organic and inorganic materials.

  Accordingly, an object of the present invention is to provide a moisture adsorbent having a high moisture adsorption amount and easy desorption even at a relatively low temperature.

  More specifically, a moisture adsorbent using an iron-containing porous organic / inorganic hybrid having a high surface area and a large pore volume as a substance that has a high moisture adsorption amount and is easily desorbed even at a relatively low temperature. It is an object of the present invention to provide

  Moreover, this invention has the further objective in providing the manufacturing method of the iron containing porous organic-inorganic hybrid body which has the said high surface area and large pore volume.

Conventionally, instead of Cr, which is a metal component contained in a porous organic / inorganic hybrid, an iron precursor containing environmentally friendly Fe is reacted with an organic ligand. When the crystallization reaction is performed by heating the mixture with the solvent in the presence of a mixed acid of nitric acid and hydrofluoric acid, such as a surface area higher than 1700 m ² / g and a pore volume larger than 0.8 ml / g A high surface area and wide pore volume iron-containing porous organic / inorganic hybrid is produced. When this was used as a moisture adsorbent, it was found that desorption was easy at a temperature of 100 ° C. or lower, and the amount of moisture adsorbed per weight of the adsorbent was found to be very high, thus completing the present invention.

  According to the second aspect of the present invention, a relatively small nanoparticle size can be obtained through a novel environmentally friendly production process by producing no porous hydrofluoric acid in some cases in producing a porous organic / inorganic hybrid. It is an object of the present invention to provide a method for producing and purifying a porous organic / inorganic hybrid having the same, and an application as an adsorbent for the porous organic / inorganic hybrid produced by the method.

  Another object of the present invention is to provide a method for producing a porous organic / inorganic hybrid material by microwave irradiation in a rapid and continuous production process. In particular, the present invention relates to use as an adsorbent, and an object of the present invention is to provide an adsorbent excellent in adsorption performance for specific harmful substances such as moisture, VOC, and a harmful substance that induces sick house syndrome.

  The first aspect of the present invention relates to a moisture adsorbent. In particular, the adsorbent is characterized by using a porous organic-inorganic hybrid containing environmentally friendly iron as a metal component.

The present invention provides an adsorbent using a porous organic / inorganic hybrid containing iron, which is easily desorbed even at low temperatures and has a large difference between the low-temperature adsorption amount and the high-temperature adsorption amount. The adsorbent according to the present invention has a surface area of more than 1,700 m ² / g and a pore volume of more than 0.8 mL / g, and contains both organic and inorganic substances as skeleton constituents. The iron-containing porous organic / inorganic hybrid is produced by a reaction of an iron precursor and an organic ligand compound capable of coordinating with the iron precursor.

  When the surface area and pore volume are smaller than the above values, the effect as a moisture adsorbent is not large.

Moreover, the larger the surface area and pore volume, the better. However, the upper limit of the surface area is about 10,000 m ² / g and the upper limit of the pore volume is about 10 mL / g as a practically realizable range in the production method. The iron-containing porous organic / inorganic hybrid according to the present invention has a surface area of 1,700 to 2,500 m ² / g and a pore volume of 0.8 to 1.2 mL / g.

  In the case of a conventional adsorbent, the ratio of the moisture adsorption amount at 100 ° C. to the moisture adsorption amount at room temperature is about 0.5 to 1. Therefore, at a temperature of 100 ° C. or less, 50% or less of the adsorbed moisture is desorbed, and there is a problem that the desorption characteristics at a low temperature are not good. However, the adsorbent according to the present invention has a characteristic that 80% or more, more preferably 90% or more of the adsorbed moisture is desorbed at a temperature of 100 ° C. or less. Further, after drying at 60 to 80 ° C. for 10 to 30 minutes, the moisture adsorption amount is 0.4 to 0.7 g / g per weight of the adsorbent under the condition of the relative humidity 60 to 80%, and the unit weight of the adsorbent. The amount of moisture adsorbed per unit is very high. Therefore, the moisture adsorbent according to the present invention has a very high moisture adsorption amount and is easy to desorb even at a low temperature of 100 ° C. or lower, and has a higher desorption rate than conventional adsorbents, and is used for humidity adjustment. Suitable for use.

  In the second aspect of the present invention, the present invention has an efficient novel method for producing a porous organic / inorganic hybrid, particularly a nano-sized particle size without using hydrofluoric acid during hydrothermal synthesis. Provided is a method for producing a porous organic / inorganic hybrid. The production method of the present invention includes a purification method for increasing the surface area of the porous organic / inorganic hybrid. Further, the present invention is characterized in that the porous organic / inorganic hybrid obtained by the novel production method is used as an adsorbent for removing specific harmful substances such as a moisture adsorbent and VOC (volatile organic compound). It relates to new applications. In addition to volatile organic compounds, the specific harmful substances include vapor phase or particulate phase substances such as formaldehyde, acetaldehyde, tar, nitrosamines, polycyclic aromatic hydrocarbons and the like that cause sick house syndrome. In addition, the present invention is a novel product characterized in that the porous organic-inorganic hybrid obtained by the novel production method is used as a moisture adsorbent, an adsorbent that removes specific harmful substances in the vapor phase or the particle phase. It relates to the use.

  Hereinafter, the present invention will be described in more detail.

In the first aspect of the present invention, the iron-containing porous organic-inorganic hybrid used as the adsorbent according to the present invention is produced by a method comprising the following steps:
(1) a step of mixing a mixed acid containing iron or an iron salt as an iron precursor, an organic ligand, a solvent, and hydrofluoric acid and nitric acid as a reaction accelerator to produce a reactant mixture; and (2) mixing the reactants. Heating the liquid.

）、アミド基（−ＣОＮＨ_２）、スルホン酸基（−ＳО_３Ｈ）、スルホン酸の陰イオン基（−ＳО_３ ⁻）、メタンジチオ酸基（−ＣＳ_２Ｈ）、メタンジチオ酸の陰イオン基（−ＣＳ_２ ⁻）、ピリジン基またはピラジン基等がある。 An organic compound that can act as a ligand, which is another constituent element of the porous organic-inorganic hybrid, is also called a linker, and any organic compound that can be coordinated can be used. . For example, functional groups that can be coordinated include —CO ₂ ⁻ , —N, carboxylic acid groups, carboxylic acid anion groups, amino groups (—NH ₂ ), imino groups (

), Amide group (—CONH ₂ ), sulfonic acid group (—SO ₃ H), anionic group of sulfonic acid (—SO ₃ ⁻ ), methanedithioic acid group (—CS ₂ H), anionic group of methanedithioic acid ( -CS ₂ ^-), and the like pyridine group or a pyrazine group.

  In order to derive a more stable organic / inorganic hybrid, the place where coordination is possible is two or more compounds, for example, bidentate or tridentate. Organic compounds are preferred. As an organic compound, a neutral organic compound such as bipyridine and pyrazine, an anionic organic compound, such as terephthalate, naphthalene dicarboxylate, benzene tricarboxylate, glutarate, succinate, etc., can be used if there is a place to coordinate. In addition to anions of carboxylic acids, cationic substances are possible. In the case of a carboxylic acid anion, in addition to an anion having an aromatic ring such as terephthalate, a linear carboxylic acid anion such as formate, an anion having a non-aromatic ring such as cyclohexyl dicarbonate Any anion such as can be used.

  In addition, organic compounds having a place where coordination can be performed, as well as organic compounds which have a potential coordination place and can be converted to coordinate under reaction conditions can be used. That is, even when an organic acid such as terephthalic acid is used, it can be combined with the metal component as terephthalate after the reaction. Representative examples of organic compounds that can be used include benzenedicarboxylic acid, naphthalenedicarboxylic acid, benzenetricarboxylic acid, naphthalenetricarboxylic acid, pyridinedicarboxylic acid, bipyridyldicarboxylic acid, formic acid, oxalic acid, malonic acid, succinic acid, glutaric acid, An organic acid selected from hexanedioic acid, heptanedioic acid, or cyclohexyldicarboxylic acid, and anions thereof, pyrazine, bipyridine and the like are included. One or more organic compounds can also be mixed and used. It is preferable to use terephthalic acid or benzenetricarboxylic acid.

  The iron-containing porous organic-inorganic hybrid as an adsorbent according to the present invention is sealed after charging an iron precursor, an organic ligand, a solvent, and a mixed acid containing hydrofluoric acid and nitric acid as a reaction accelerator. , Heated to 100 to 250 ° C., but can be produced by maintaining the reaction temperature using microwaves or electricity and maintaining the pressure at an automatic pressure.

As described above, the method for producing an iron-containing organic-inorganic hybrid according to the present invention is characterized by using an acid, preferably a mixed acid of hydrofluoric acid and nitric acid. In particular, the organic / inorganic hybrid containing iron of the present invention exhibits a marked improvement in crystallinity and a reduction in crystal size as compared with the conventional method of synthesis using only hydrofluoric acid. The conventional production method using hydrofluoric acid cannot produce an iron-containing organic-inorganic hybrid having a surface area greater than 1,700 m ² / g and a pore volume greater than 0.8 mL / g. Referring to the results of Examples and Comparative Examples, when existing hydrofluoric acid was used, the BET surface area value was 1,590 m ² / g, and 2,050 m ² / g BET using a mixed acid was used. It is significantly lower than the surface area value. When mixed acid was used, the pore volume was 1.0 ml / g, whereas when hydrofluoric acid was used, it was as low as 0.7 ml / g. In addition, when mixed acid is used, crystallinity is improved and yield is the same, despite a very short reaction time (within 2 minutes when using microwave) compared to the case where mixed acid is not used. It was confirmed to have the effect of. However, when an acid component such as acetic acid or sulfuric acid or a salt such as ammonium fluoride or sodium chloride is used as the other acid, it is difficult to produce an organic / inorganic hybrid having sufficient crystallinity. In the production method of the present invention, in the mixed acid, the mixing ratio of nitric acid and hydrofluoric acid is used in a molar ratio of 0.1 to 1: 1 to 0.1, and the iron-containing organic-inorganic hybrid aimed at by the present invention The body can be manufactured. When nitric acid or hydrofluoric acid deviates from the molar ratio, there are disadvantages in that the yield decreases and the reaction time becomes too long.

  In addition to the metal component and the organic compound, an appropriate solvent is required when producing a porous / inorganic hybrid. As the solvent, any of water, alcohols, ketones, and hydrocarbons can be used, and two or more solvents can be mixed and used. Preferably, water, alcohol having 1 to 10 carbon atoms such as methanol, ethanol, propanol, ketone having 2 to 10 carbon atoms such as acetone, methyl ethyl ketone, and hydrocarbon having 5 to 20 carbon atoms such as hexane, One or a mixture of two or more selected from heptane and octane can be used. More preferably, water can be used.

  The iron precursor and the organic compound can be mixed at a ratio (molar ratio) of 1: 0.1 to 10. The said ratio can be suitably adjusted with the kind of each iron precursor and an organic compound. In the present invention, iron powder or iron salt such as iron nitrate is used as the iron precursor, and terephthalic acid or benzenetricarboxylic acid is more preferable as the organic ligand.

  In the present invention, the reaction temperature for producing the porous organic / inorganic hybrid is not actually limited.

  However, 100 ° C. or higher is appropriate. A temperature of 100 ° C. or higher and 250 ° C. or lower is preferable, and a temperature of 150 ° C. or higher and 220 ° C. or lower is more preferable. If the reaction temperature is too low as less than 100 ° C., the reaction rate is slow and not effective, and if the reaction temperature exceeds 250 ° C. and too high, a substance without pores is easily obtained and the reaction rate is too high. Impurities are easily mixed. Further, the internal pressure of the reactor becomes high, and the configuration of the reactor is uneconomical. The pressure in the reactor is practically unlimited, but it is easy to synthesize the material with the autogenous pressure of the reactants at the reaction temperature. Further, an inert gas such as nitrogen or helium can be added to carry out the reaction at a high pressure. When microwaves are irradiated as the reaction heat source, any microwave having a frequency of about 300 MHz to 300 GHz can be used to heat the reaction product. However, industrially, microwaves with frequencies of 2.45 GHz and 0.915 GHz are generally used.

  Compared with the method using electric heating, the microwave irradiation method has a shorter reaction time, a relatively small porous / inorganic hybrid particle size, a high specific surface area, and a moisture adsorbent. As the characteristics are better.

  Also, for use as an adsorbent in a humidifier or dehumidifier, the adsorption and desorption characteristics within the initial 10 minutes, more preferably within the initial 5 minutes, are important. That is, even if the adsorption amount is large, if the speed is too low, it may not be suitable for use in humidifiers and dehumidifiers. However, among the adsorbents according to the present invention, in the case of the adsorbents produced by the method of irradiating microwaves, the adsorption rate is very high and the desorption rate is also excellent. It has suitable characteristics. That is, after drying for 10 to 30 minutes at 60 to 80 ° C. and after 5 minutes under conditions of 60 to 80% relative humidity, the moisture adsorption amount is 0.35 to 0.45 g / g per weight of the adsorbent. The initial adsorption rate is very high.

  In the said manufacturing method, reaction can be performed by a batch type and a continuous type. The batch reactor has a low production amount per hour and is suitable for producing a small amount of a porous / inorganic hybrid. Continuous reactors are expensive, but are suitable for mass production. In the case of a batch system, the reaction time is suitably about 1 minute to 8 hours. If the reaction time is too long, impurities are likely to be mixed, and it is not easy to produce nanoparticles by growing the particles. When the reaction time is too short, the reaction conversion rate is low. The residence time of the continuous reactor is suitably about 1 minute to 1 hour. If the residence time is too long, the productivity is low and large particles are obtained, and if the residence time is too short, the reaction conversion rate is low. The residence time is more suitably from 1 minute to 20 minutes. The reaction product can be stirred during the batch reaction, and the stirring speed is suitably 100 to 1000 rpm. However, the reaction can be carried out without a stirring process, and not stirring is simple and easy to apply in the configuration and operation of the reactor.

  Microwave reactions occur at a very fast rate, so the microwaves are pre-treated to increase the homogeneity of the reactants or increase the solubility and produce some crystal nuclei. Is preferably irradiated. If the reaction by the microwave is started immediately without pretreatment, the reaction is slow, impurities are mixed, or the particle size uniformity tends to be low. However, the process itself is simple. Pretreatment can be done by treating the reaction with ultrasound or by vigorous stirring. The pretreatment temperature is preferably between room temperature and the reaction temperature. However, if the temperature is too low, the effect of the pretreatment is weak. If the temperature is too high, impurities are easily generated, and the pretreatment equipment must be complicated. The pretreatment time is suitably 1 minute to 5 hours. In the case of ultrasonic treatment, 1 minute or more is suitable, and in the case of stirring treatment, 5 minutes or more is suitable. When the pretreatment step is performed by stirring, the metal component and the organic compound are preferably stirred at 50 to 2,000 rpm for 5 to 600 minutes in the presence of a solvent. It is preferable to irradiate with 30 MHz ultrasonic waves for 1 to 600 minutes. When the preprocessing time is too short, the effect of the preprocessing is weak. If the preprocessing is performed too long, the efficiency of the preprocessing is lowered.

  It is more effective to perform the pretreatment using ultrasonic waves in terms of the pretreatment time and the uniformity of the reaction product.

The second aspect of the present invention relates to a method for producing a porous organic / inorganic hybrid, comprising the following steps:
(1) mixing a metal precursor, an organic compound capable of acting as a ligand, and a solvent to produce a reactant mixture;
(2) heating the reactant mixture; and (3) purifying the porous organic / inorganic hybrid obtained in step (2) by treating with a solution or solvent in which an inorganic salt is dissolved. .

  In the manufacturing method, the step (3) can be selectively performed when necessary.

  The porous organic-inorganic hybrid produced by the production method according to the present invention can be obtained as nanoparticles, and the size of the nanoparticles is about 450 nm or less. Moreover, the porous organic-inorganic hybrid produced by the production method according to the present invention can be in the form of powder, thin film or membrane.

  A porous organic / inorganic hybrid in the form of nanoparticles, thin film or membrane can be easily produced by a method such as heating and microwave irradiation after immersing a substrate in the reaction mixture.

  The method for producing a porous organic / inorganic hybrid according to the present invention is a hydrothermal synthesis for producing a porous nanoporous material, and an organic / inorganic hybrid having a nano-sized particle size without using hydrofluoric acid. To manufacture. Moreover, as a purification method for increasing the surface area of the porous organic / inorganic hybrid, in addition to a commonly used solvent, by using an inorganic salt such as ammonium chloride or potassium fluoride, an organic / inorganic The method further comprises purifying impurities in the pores of the hybrid.

  The porous organic / inorganic hybrid has a novel use as an adsorbent. In particular, the porous / inorganic hybrid adsorbent according to the present invention can be easily adsorbed / desorbed even at a temperature of 100 ° C. or lower, and the adsorbed amount per 1 wt. Therefore, the adsorbent can be used as a moisture adsorbent applicable to a humidifier, a dehumidifier, a cooler / heater, a refrigerator, and the like. Moreover, the porous organic / inorganic hybrid of the present invention having a large surface area and uniform pore characteristics can be used as an adsorbent excellent in adsorption performance for specific harmful substances.

  In the production method of the present invention, any metal can be used as the metal substance which is one of the components contained in the porous organic / inorganic hybrid. Typical metal components are Ti, Zr, Hf, V, Nb, Ta, Cr, Mo, W, Mn, Re, Fe, Ru, Os, Co, Rh, Ir, Ni, Pd, Pt, Cu, Ag. , Au, Zn, Cd, Hg, Mg, Ca, Sr, Ba, Sc, Y, Al, Ga, In, Tl, Si, Ge, Sn, Pb, As, Sb, Bi, and the like. In particular, a transition metal that easily generates a coordination compound is suitable. Of the transition metals, chromium, vanadium, iron, nickel, cobalt, copper, titanium, manganese and the like are suitable, and chromium and iron are most suitable. Besides transition metals, lanthanum group metals as well as typical elements that form coordination compounds are possible. Among typical elements, aluminum and silicon are suitable, and among lanthanum group metals, cerium and lanthanum are suitable. As the metal source, not only the metal itself but also any compound of metal can be used.

  In the second aspect of the present invention, the organic compound that can act as a ligand, which is another component contained in the organic / inorganic hybrid, and the solvent used for the synthesis of the organic / inorganic hybrid are the first Identical to that used in the mode.

  In order to adjust the crystal growth rate of the organic / inorganic hybrid nanoporous material, a mixed acid containing hydrofluoric acid can be used in addition to the acid, particularly nitric acid, hydrochloric acid and hydrofluoric acid.

  On the other hand, in the process using hydrofluoric acid, there was a limitation in using a reactor other than Teflon (registered trademark). Until now, the crystal growth rate of organic / inorganic hybrid nanopores has been known to be relatively high while the nucleation rate is low. Therefore, the reaction product containing hydrofluoric acid has a relatively slow nucleation rate due to the strong binding property between metal ions and fluorine ions, and it is difficult to obtain nanopores with small crystal size. is there.

  Therefore, in a further aspect of the present invention, in order to solve the above-mentioned problems caused by the use of hydrofluoric acid, in the method for producing a porous organic / inorganic hybrid according to the present invention, for producing a porous organic / inorganic hybrid. And an inorganic acid excluding hydrofluoric acid. Thereby, by the said manufacturing method of this invention, the porous organic-inorganic hybrid nanopore body which has a relatively small nanoparticle size can be manufactured, without using hydrofluoric acid at all.

  Further, in order to remove the metal or organic ligand present in the pores of the porous organic / inorganic hybrid produced by the second aspect of the present invention, conventionally, impurities have been removed using a solvent. .

However, in the above case, there is a limit to removing organic or inorganic impurities chelated in the pores. In contrast, in the production method of the present invention, an inorganic salt, particularly a monovalent or divalent cation selected from the group consisting of NH ₄ ⁺ , an alkali metal and an alkaline earth metal, a halogen anion, and a carbonate ion By treating a porous organic / inorganic hybrid with an inorganic salt containing a monovalent or divalent anion selected from the group consisting of (CO ₃ ²⁻ ), nitrate ions and sulfate ions, organic / inorganic hybrids are obtained. Impurities in the pores of the nanopore body can be efficiently removed. Therefore, the organic / inorganic hybrid nanoporous body having a high surface area can be obtained. As the inorganic salt, a salt containing Ca ²⁺ or Mg ²⁺ as a divalent cation, F ⁻ , I ⁻ or Br ⁻ as a monovalent anion, a salt containing a monovalent cation and a divalent anion One or more inorganic salts selected from the group consisting of NH ₄ F, KF, KI and KBr can be used.

  In the present invention, it was confirmed by measuring the surface area that the nitrogen adsorption amount of the organic / inorganic hybrid nanoporous material after the treatment with the inorganic salt increased by about 200 ml / g.

  In addition to the hydrothermal synthesis method of electric heating, the reaction can be hydrothermal synthesis by batch or continuous method by microwave irradiation. The organic / inorganic hybrid membrane or thin film can be produced by a method in which the substrate is immersed in the reaction mixture in the step (1) and then heated by irradiation with microwaves.

According to the production method of the present invention, fluorine is not contained and the chemical formula: M ₃ OH (H ₂ O) ₂ O [C ₆ H ₄ (CO ₂ ) ₂ ] ₃ (M = Fe, Cr, V or Al) or its hydrates or _{formula: M 3 O (H 2 O} ) 2 OH [C 6 H 3 - (CO 2) 3] 2 (M = Fe, Cr, V , or Al) novel porous represented by or a hydrate Organic / inorganic hybrid, especially chemical formula: Cr ₃ OH (H ₂ O) ₂ O [C ₆ H ₄ (CO ₂ ) ₂ ] ₃ · nH ₂ O (n to 25) or chemical formula: Fe ₃ O (H ₂ O) ₂ OH [C ₆ H ₃ — (CO ₂ ) ₃ ] ₂ · nH ₂ O (n to 14.5) can be obtained as a novel porous organic-inorganic hybrid.

  The porous organic / inorganic hybrid obtained by the production method of the present invention can be used as an oxidation reaction catalyst or an acid catalyst.

  Moreover, the porous organic-inorganic hybrid produced by the production method of the present invention can be used as an adsorbent excellent in absorption / desorption performance. In particular, when used as a moisture adsorbent, desorption easily occurs at a low temperature of 100 ° C. or lower, so that very excellent performance can be achieved with a humidifier, a dehumidifier or the like using such characteristics. Moreover, when the porous organic-inorganic hybrid produced by the production method of the present invention is used as an adsorbent such as a VOC or sick house syndrome inducer, a specific harmful substance can be effectively removed.

  In particular, when the porous organic / inorganic hybrid obtained by the production method of the present invention is used as a low-temperature moisture adsorbent, it has a low-temperature desorption characteristic of 100 ° C. or less, preferably 50 to 100 ° C., and an existing HF. -It can confirm that it has a very high moisture adsorption rate compared with an inorganic nanopore body.

  As described above, the iron-containing porous organic-inorganic hybrid produced according to the present invention has a large amount of moisture adsorption and is excellent in desorption amount characteristics at low temperatures. Therefore, it can be used as an adsorbent in a dehumidifier, humidifier, heater or air conditioner. In particular, the desorption temperature is very low, and the operation cost of such equipment can be greatly reduced.

  From another aspect, the porous organic-inorganic hybrid produced by the novel production method of the present invention is a nano-sized nanocrystal having high crystallinity even though hydrofluoric acid is not used during hydrothermal synthesis. It is a hole. In particular, by treating with an inorganic salt such as ammonium chloride or potassium fluoride, the impurities in the pores of the organic / inorganic hybrid nanopore body are removed and purified, thereby increasing the surface area. Can do. Moreover, the porous organic-inorganic hybrid produced by the production method of the present invention can be used as an adsorbent excellent in absorption / desorption performance. In particular, when used as a moisture adsorbent, desorption occurs easily at a low temperature of 100 ° C. or lower. Using such characteristics, very excellent performance can be achieved in humidifiers, dehumidifiers and the like. Moreover, when the porous organic-inorganic hybrid produced by the production method of the present invention is used as an adsorbent such as a VOC or sick house syndrome inducer, a specific harmful substance can be effectively removed.

FIG. 1 is an X-ray diffraction pattern of the organic / inorganic adsorbent of iron benzene tricarboxylate obtained in Example 1. FIG. 2 is a nitrogen isotherm adsorption line of the iron benzene tricarboxylate-containing organic / inorganic adsorbent obtained in Example 1. FIG. 3 is a graph showing the moisture adsorption characteristics of the adsorbents using the iron benzene tricarboxylates of Examples 1 and 2 and the zeolite Y of Comparative Example 1: Desorption of the moisture adsorbent is 70 ° C. (Example 1) And 2) or 200 ° C. (Comparative Example 1), and the adsorption was performed at a relative humidity of 68%. FIG. 4 is a graph showing the results of moisture desorption tests on the adsorbents of Example 1 and Comparative Example 1: Example 1 is the result of moisture desorption at 70 ° C., and Comparative Example 1 is the moisture at 200 ° C. It is the result of desorption. FIG. 5 is a graph of an X-ray diffraction pattern of chromium terephthalate which is a porous organic / inorganic hybrid produced by the production method of Example 3 of the present invention. FIG. 6 shows the results of X-ray diffraction patterns before and after purification of chromium terephthalate, which is a porous organic / inorganic hybrid produced by the purification method of Example 3 of the present invention, and (a) Is the form before purification, and (b) is the form after purification. FIG. 7 shows the results of nitrogen adsorption isotherms on chromium terephthalate, which is a porous organic / inorganic hybrid obtained in Example 4 of the present invention. FIG. 8 is an electron micrograph of iron benzene tricarboxylate, which is a porous organic / inorganic hybrid obtained in Example 5 and Comparative Example 4 of the present invention. FIG. 9 shows the results of moisture adsorption characteristics of the porous organic-inorganic hybrid containing iron obtained in Examples 5 and 6 and Comparative Example 4 of the present invention.

  Example 1: Production of porous organic / inorganic hybrid (Fe-BTC) by microwave irradiation

After adding 1 mmol of metal iron, 1 ml of 1M HNO ₃ , 40 ml of 5M HF (aqueous solution) and 7 mmol of 1,3,5-benzenetricarboxylic acid (BTCA) to a Teflon (registered trademark) reactor, distilled water was added. The final molar ratio of the reactants was Fe: HF: HNO ₃ : BTCA: H ₂ O = 1: 2: 0.6: 0.7: 278. The mixed reaction product was stirred at 500 rpm for 20 minutes at room temperature so that a uniform reaction product was obtained. A Teflon (registered trademark) reactor containing the pretreated reactant was attached to a microwave reactor (CEM, Model Mars-5), and heated to 200 ° C. by irradiation with microwave (2.54 GHz). Then, it was maintained at 200 ° C. for 2 minutes to carry out a crystallization reaction. Next, the reaction product was cooled to room temperature, centrifuged, washed with distilled water, and dried to obtain a porous / inorganic hybrid (Fe-BTC). FIG. 1 shows an X-ray diffraction pattern of the obtained solid phase porous organic / inorganic hybrid. As a result of elemental analysis, it showed a molar ratio of Fe: C: F = 1: 6.5: 0.32, and as a result of nitrogen adsorption experiment, the BET surface area was 2,050 m ² / g and the pore volume was 1.0 ml. / G. The yield of the formed porous particles was 86% (FIG. 2).

The above results indicate that the substance was previously published in the literature [Bulletin of Korean Chemical Society vol. 26, p. 880 (2005)], which shows a crystalline structure similar to that of Cr-MIL-100.
Example 2: Production of porous organic / inorganic hybrid (Fe-BTC) by electric heating

As a heat source, the same as in Example 1 except that a mixed organic / inorganic mixture was produced by heating for 144 hours by an electric heating method using a general convection oven instead of irradiating microwaves. A porous organic / inorganic hybrid was produced by this method. As a result of the XRD analysis, it can be confirmed that the diffraction pattern was obtained at the same position as in Example 1, although the relative intensity of the peaks was different in the crystal structure of the produced organic / inorganic hybrid. As a result of the nitrogen adsorption experiment, it showed a BET surface area of 1,820 m ² / g and a pore volume of 0.9 ml / g.
Comparative Example 1: Zeolite moisture adsorbent

Zeolite Y (Aldrich, Si / Al = 5.6, specific surface area = 827 m ² / g, pore volume = 0.35 ml / g) used as a commercial water adsorbent was prepared.
Comparative Example 2: Production of porous organic / inorganic hybrid (Fe-BTC) using a single acid

A porous organic / inorganic hybrid was produced in the same manner as in Example 1 except that a hybrid was produced using a single acid that was not nitric acid. After adding 1 mmol of metallic iron, 40 ml of 5M HF (aqueous solution) and 7 mmol of 1,3,5-benzenetricarboxylic acid (BTCA) to a Teflon (registered trademark) reactor, distilled water was added. The final molar ratio of the reactants was Fe: HF: BTCA: H ₂ O = 1: 2: 0.6: 278. The microwave irradiation temperature for the organic / inorganic hybrid was 200 ° C., and the reaction was carried out for 1 hour. The yield of the obtained solid-phase porous / inorganic hybrid was 82%. The X-ray diffraction pattern of the porous organic-inorganic hybrid is similar to the result of Example 1, but the overall peak intensity is low. As a result of the nitrogen adsorption experiment, a BET surface area of 1,590 m ² / g and a pore volume of 0.7 ml / g were shown.
Test example 1: moisture adsorption test

  The adsorbents obtained in Example 1 and Example 2 were vacuum-dried at 70 ° C. for 30 minutes, and then a moisture adsorption experiment was carried out by a weight method (FIG. 3). Even at a relative humidity of 68%, the amount of moisture adsorbed per weight of the adsorbent was 0.67 g / g in Example 1 and 0.59 g / g in Example 2.

  Comparing with zeolite Y used as a commercial moisture adsorbent in Comparative Example 1, after the zeolite Y was vacuum dried at 200 ° C. for 30 minutes, the moisture adsorption experiment was the same. It was 35 g / g (FIG. 3). That is, although the desorption temperature for the adsorbent of the example was set to 70 ° C., the adsorbent according to the present invention exhibited a water adsorption amount of 1.6 times or more.

In addition, the adsorbent of Example 1 manufactured using microwaves showed an adsorption amount of 0.46 g / g after the initial 5 minutes and 0.56 g / g after 10 minutes. On the other hand, the adsorbent of Comparative Example 1 showed an adsorption amount of 0.28 g / g after 10 minutes after 0.25 g / g after 5 minutes. Therefore, it can be seen that the adsorbent according to Example 1 of the present invention has a very high initial adsorption rate.
Test example 2: moisture desorption test

  The adsorbent prepared in Example 1 and sodium zeolite Y (NaY) were maintained in the upper layer of a desiccator charged with a saturated aqueous solution of ammonium chloride for 3 days to sufficiently adsorb moisture, and the desorption amount was determined by gravimetric analysis. analyzed. Under desorption conditions, the weight loss of the adsorbent was measured while flowing nitrogen at 300 ml / min. The desorption temperature in the adsorbent of Example 1 was 70 ° C., and the desorption temperature in sodium zeolite Y (NaY) of Comparative Example 1 was 200 ° C.

  FIG. 4 is a graph showing the results of weight reduction over time, with the total weight of the adsorbent adsorbing moisture as 100%. That the weight reduction rate does not decrease any more means that all the desorbable moisture has been desorbed. The results of Example 1 showed a weight loss of about 40% by weight after 10 minutes. In the case of Comparative Example 1, a weight reduction of 25% by weight was shown. In the case of Example 1, the desorbable water adsorption amount per weight of the adsorbent is 40/60 = 0.67 g / g, and in the case of Comparative Example 1, the desorbable water adsorption per weight of the adsorbent The amount is 25/75 = 0.33 g / g. Therefore, it can be seen that the absolute water adsorption amount of the adsorbent of Example 1 is twice or more that of the adsorbent of Comparative Example 1. In addition, the desorption rate within 5 minutes in the initial stage was also shown to be higher for the adsorbent of Example 1 than for the adsorbent of Comparative Example 1.

From the above results, it can be seen that the adsorbent according to the present invention is easy to desorb moisture at a temperature of 100 ° C. and has a high moisture adsorption amount per unit weight. If such characteristics are used and the adsorbent is applied to a humidifier or a dehumidifier, it is expected to exhibit excellent performance in humidity control.
Example 3 (Cr-BDC-1)

A Teflon reactor, after addition of _{Cr (NO 3) 3 · 9H} 2 O and 1,4-benzenedicarboxylic acid (BDCA), distilled water was added, the final molar ratio of the reactants Cr : HNO ₃ : BDCA: H ₂ O = 1: 0.1: 1: 272. Basically, if Cr (NO ₃ ) ₃ is dissolved in water, it will hydrate and become a strong acid. Accordingly, the same effect as that obtained by charging HNO ₃ is exhibited. A Teflon (registered trademark) reactor containing the reaction product was placed in an electric oven, reacted at 210 ° C. for 11 hours, cooled to room temperature, then centrifuged, washed with distilled water, and dried. Chromium terephthalate (Cr-BDC) was obtained as an inorganic hybrid. As a result of X-ray diffraction analysis of the manufactured Cr-BDC, characteristic diffraction peaks having 2θ values of about 3.3, 5.2, 5.9, 8.5 and 9.1 are shown. It can be seen that chromium terephthalate having crystallinity was obtained (FIG. 5). It was confirmed that the XRD form of the chromium terephthalate crystal obtained in this example was consistent with the published literature values [Science 23, 2040, 2005]. Thus, it can be seen that a porous organic-inorganic hybrid can be obtained very effectively even by an environmental friendly process that does not use hydrofluoric acid (HF) as a reactant. As a result of ICP analysis, chromium terephthalate of the obtained porous organic / inorganic hybrid material does not contain F, and its structure is the same as MIL-101, but F is not contained in the structure. It can be confirmed that the substance can be represented by the chemical formula: Cr ₃ OH (H ₂ O) ₂ O [C ₆ H ₄ (CO ₂ ) ₂ ] ₃ · nH ₂ O (n to 25). .
Example 4 (Cr-BDC-2)

1 g of porous organic / inorganic hybrid produced in Example 3 was charged into 50 ml of 1M NH ₄ F, stirred at a temperature of 70 ° C., and not bonded to the crystal structure existing in the pores of the porous body. By removing impurities such as 1,4-benzenedicarboxylic acid and chromium oxide, an organic / inorganic hybrid having an increased surface area was produced. From the X-ray diffraction pattern (FIG. 6), it can be confirmed that the crystallinity is maintained without being impaired after the treatment with ammonium fluoride. Further, the nitrogen adsorption measurement results of the porous organic-inorganic hybrid material before and after the treatment of the ammonium fluoride, the surface area by the processing of the ammonium fluoride is 700m ² / g (pre-treatment of ammonium fluoride 3,373m ² / g → After the treatment, 4,074 m ² / g) increases, and the adsorption amount at P / Po = 0.5 increases by 200 ml / g (1,050 ml / g before treatment of ammonium fluoride → 1,250 ml / g after treatment). It can be seen that an organic / inorganic hybrid having properties can be obtained (FIG. 7).
Example 5: Production of porous organic / inorganic hybrid (Fe-BTC-1) by microwave irradiation

After adding 1 mmol of metallic iron, 60 ml of 1M HNO ₃ and 7 mmol of 1,3,5-benzenetricarboxylic acid (BTCA) to a Teflon (registered trademark) reactor, distilled water was added. The final molar ratio of the reactants was Fe: HNO ₃ : BTCA: H ₂ O = 1: 0.6: 0.7: 278. The reaction was stirred at 500 rpm for 20 minutes at room temperature so that a uniform reaction was obtained. A Teflon (registered trademark) reactor containing the pretreated reactant is attached to a microwave reactor (CEM, Model Mars-5), and heated to 200 ° C. by irradiation with microwave (2.54 GHz). Then, it was maintained at 200 ° C. for 2 minutes to carry out a crystallization reaction. Next, the mixture was cooled to room temperature, centrifuged, washed with distilled water, and dried to obtain a porous / inorganic hybrid (Fe-BTC). The X-ray diffraction pattern can be found in published literature [Bulletin of Korean Chemical Society vol. 26, p. 880 (2005)], which is similar to the structure of Cr-MIL-100. As a result of ICP analysis, the obtained chromic terephthalate of the porous organic / inorganic hybrid does not contain F, and its structure is the same as MIL-100, but F is contained in the structure. It is a substance that can be represented by the chemical formula: Fe ₃ O (H ₂ O) ₂ OH [C ₆ H ₃ — (CO ₂ ) ₃ ] ₂ .nH ₂ O (n to 14.5). I understand. As a result of the nitrogen adsorption experiment, it was confirmed that the surface area of the porous organic / inorganic hybrid (Fe-BTC) was 1,700 m ² / g or more. As a result of electron microscopic analysis, it can be seen that the size of the particles was as small as 200 to 500 nm or less (FIG. 8a).
Example 6: Production of porous organic / inorganic hybrid (Fe-BTC-2) by electric heating

As a heat source, the same method as in Example 3 was used, except that instead of irradiating microwaves, the mixture was heated for 6 hours by an electric heating method using a general electric heating method to produce an organic / inorganic hybrid. A porous organic / inorganic hybrid was produced. As a result of XRD analysis, it was confirmed that in the crystal structure of the organic / inorganic hybrid produced as described above, a diffraction pattern was obtained at the same position as in Example 3, although the relative intensities of the peaks were different. As a result of analysis using an electron microscope, a crystal having a relatively large particle size of 1 μm could be obtained.
Example 7 (Cr-BDC-3)

In Example 3, an organic / inorganic hybrid was produced by the same method as in Example 3 except that a heating method by microwave irradiation, which was not an electric heating method, was used. However, using a microwave reactor with a frequency of 2.5 GHz, a reaction temperature of 210 ° C. and a reaction time of 40 minutes were maintained, and an organic / inorganic hybrid was produced. Analysis of the X-ray diffraction pattern showed that the material had the same structure as Example 3.
Example 8 (Fe-BDC-3)

_{Cr (NO 3) 3 · 9H} 2 O in place of, except for using Fe was prepared the organic-inorganic hybrid material in the same manner as in Example 3. In addition, a pure porous organic-inorganic hybrid was produced using the post-treatment step of Example 4. From the X-ray diffraction pattern, it was found that a substance having the same structure as in Example 3 was obtained.
Example 9 (V-BDC-1)

In Example 8, instead of using a _{Cr (NO 3) 3 · 9H} 2 O, except for using VCl _3, organic-inorganic hybrid by the same method using the post-processing steps of Example 3 and Example 4 The body was manufactured. The X-ray diffraction pattern shows that a material with the same structure as Example 3 was obtained. The photograph of an electron microscope shows that the organic / inorganic hybrid having a uniform particle size characteristic of about 50 to 80 nm can be obtained.
Example 10

  After 0.1 g of each of the Fe-BTCA of the organic / inorganic hybrid obtained in Examples 5 and 6 and Comparative Example 4 was vacuum-dried at 150 ° C. for 30 minutes, a moisture adsorption experiment was performed by a weight method ( FIG. 5).

The moisture adsorption amount per weight of the adsorbent within the initial 5 minutes at a relative humidity of 60% was measured to be 0.36 g / g in Example 5 and 0.34 g / g in Example 6. It was. This shows a result of 24% and 17% improvement from the adsorption amount of 0.29 g / g in Comparative Example 4, respectively. In particular, it was confirmed that the moisture adsorption rate in the entire region from the initial adsorption to 5 minutes was very fast. Thus, when the porous organic / inorganic hybrid according to the present invention is used as a low-temperature moisture adsorbent, the adsorbent can be easily desorbed at 100 ° C. or less, and using such characteristics, a humidifier and a dehumidifier It can be seen that very good performance can be achieved.
Example 11

1 g of benzene, which is a volatile organic compound, was added to 1 g of porous organic-inorganic hybrid Cr-BDC obtained by the method of Example 3, and as a result of performing an adsorption experiment for 1 hour, 0.73 g of benzene was obtained. It was confirmed that it was removed by adsorption. This value was confirmed to be 3.5 times higher than the adsorption amount of 0.19 g of benzene, which is the adsorption amount of Darco activated carbon (surface area 1600 m ² / g) of the same content.
Comparative Example 3 (Cr-BDC-4)

In the production method according to Example 3, a porous organic / inorganic hybrid nanopore was produced using hydrofluoric acid when preparing the reaction mixture. The final molar ratio of the reaction mixture was such that Cr: HF: BDCA: H ₂ O = 1: 1: 1: 272. As a result of the analysis of the surface area of the produced porous organic / inorganic hybrid nanoporous material, the adsorption / absorption amount is 1,044 ml / g and the BET surface area is 3,439 m ² / g when P / Po = 0.5. It was found that a hybrid was obtained.
Comparative Example 4 (Fe-BTC)

In the production method according to Example 5, a porous organic / inorganic hybrid nanopore was produced using hydrofluoric acid when preparing the reaction mixture. The final molar ratio of the reaction mixture was such that Fe: HF: HNO ₃ : BTCA: H ₂ O = 1: 1: 0.6: 0.7: 278. As a result of X-ray diffraction analysis of the produced organic / inorganic hybrid material, instead of obtaining an organic / inorganic hybrid material having the same crystallinity as in Example 5, a material having a very large crystal size (1 to 5 μm) Is obtained (FIG. 8b).

  From the results of the Examples and Comparative Examples, producing a porous organic / inorganic hybrid nanoporous body having the same crystallinity by the production method of the present invention that does not contain hydrofluoric acid, compared to the step using hydrofluoric acid. I confirmed that I was able to. In particular, it was confirmed that the surface area increased by 10% or more when treated with inorganic salts such as ammonium salt and potassium fluoride. Moreover, it was confirmed that the porous organic / inorganic hybrid nanoporous material produced by the production method of the present invention has very high activity as a catalyst. Moreover, the porous organic-inorganic hybrid produced by the production method of the present invention can be used as an adsorbent excellent in absorption / desorption performance. In particular, when it is used as a moisture adsorbent, desorption easily occurs at a low temperature of 100 ° C. or lower, so that such characteristics can be used to achieve very excellent performance in a humidifier, a dehumidifier, or the like. In addition, when the porous organic / inorganic hybrid produced by the production method of the present invention is used as an adsorbent for specific harmful substances such as VOCs and sick house syndrome inducers, specific harmful substances in the vapor phase and the particle phase are used. Substances can be effectively removed.

Claims (19)

Adsorbent containing porous organic / inorganic hybrid material characterized by being produced by the following steps:
(1) mixing a metal precursor, an organic compound capable of acting as a ligand, and a solvent to produce a reactant mixture;
(2) heating the reactant mixture; and (3) purifying the porous organic / inorganic hybrid obtained in step (2) by treating with a solution or solvent in which an inorganic salt is dissolved. Step to do.   The adsorbent according to claim 1, further comprising an acid in the reactant mixture.   The adsorbent according to claim 2, wherein the acid is an inorganic acid excluding hydrofluoric acid. The inorganic salt used in the step (3) is a monovalent or divalent cation selected from the group consisting of ammonium, alkali metal and alkaline earth metal, a halogen anion, a carbonate ion (CO ₃ ²⁻ ), It contains a monovalent or divalent anion selected from the group consisting of nitrate ion and sulfate ion, and purifies impurities in a porous organic / inorganic hybrid obtained by treatment with the inorganic salt. The adsorbent according to claim 1 or 2.   The metal precursor is Ti, Zr, Hf, V, Nb, Ta, Cr, Mo, W, Mn, Re, Fe, Ru, Os, Co, Rh, Ir, Ni, Pd, Pt, Cu, Ag, One or more selected from the group consisting of Au, Zn, Cd, Hg, Mg, Ca, Sr, Ba, Sc, Y, Al, Ga, In, Tl, Si, Ge, Sn, Pb, As, Sb, and Bi The adsorbent according to claim 1, wherein the adsorbent is a metal or a compound thereof.   The adsorbent according to claim 5, wherein the metal precursor is one or more metals selected from the group consisting of Al, Fe, V, Mn, Mg, and Cr, or a compound thereof. Organic compounds that can act as ligands include carboxylic acid groups, anionic groups of carboxylic acids, amino groups (—NH ₂ ), imino groups (

), Amide group (—CONH ₂ ), sulfonic acid group (—SO ₃ H), anionic group of sulfonic acid (—SO ₃ ⁻ ), methanedithioic acid group (—CS ₂ H), anionic group of methanedithioic acid ( -CS 2 ^_-), the adsorbent according to claim 1 or 2, characterized in that a compound or a mixture containing one or more functional groups selected from the group consisting of pyridine group and pyrazine groups.   Compounds having a carboxylic acid group are benzenedicarboxylic acid, naphthalenedicarboxylic acid, benzenetricarboxylic acid, naphthalenetricarboxylic acid, pyridinedicarboxylic acid, bipyridyldicarboxylic acid, formic acid, oxalic acid, malonic acid, succinic acid, glutaric acid, hexanedioic acid, heptane The adsorbent according to claim 7, wherein the adsorbent is derived from a compound selected from the group consisting of diacids and cyclohexyldicarboxylic acids.   The adsorbent according to claim 1 or 2, wherein the porous organic-inorganic hybrid is chromium terephthalate, iron terephthalate, aluminum terephthalate, or vanadium terephthalate.   The adsorbent according to claim 1 or 2, wherein the porous organic-inorganic hybrid is iron benzene tricarboxylate chromium benzene dicarboxylate, aluminum benzene tricarboxylate or vanadium benzene tricarboxylate.   The adsorbent according to claim 1 or 2, wherein the porous organic-inorganic hybrid is produced in the form of nanoparticles.   The adsorbent according to claim 1 or 2, wherein the porous organic-inorganic hybrid is produced in a thin film or membrane form. The porous organic-inorganic hybrid does not contain fluorine, and has the chemical formula: M ₃ OH (H ₂ O) ₂ O [C ₆ H ₄ (CO ₂ ) ₂ ] ₃ (M = Fe, Cr, V Or the adsorbent according to claim 1, wherein the adsorbent is represented by Al) or a hydrate thereof. The porous organic-inorganic hybrid does not contain fluorine and has the chemical formula: M ₃ O (H ₂ O) ₂ OH [C ₆ H _3- (CO ₂ ) ₃ ] ₂ (M = Fe, Cr, The adsorbent according to claim 1 or 2, represented by V or Al) or a hydrate thereof.   A moisture adsorbent characterized by adsorbing moisture using the adsorbent according to claim 1.   The moisture adsorbent according to claim 15, wherein the moisture adsorbent is used for moisture adsorption in a dehumidifier, a humidifier, a cooler, a heater, or a refrigerator.   The adsorbent according to claim 1 or 2, which is used for adsorption of a specific harmful substance in a vapor phase or a particle phase.   The adsorbent according to claim 1 or 2, which is used for adsorption of a volatile organic compound.   3. The method according to claim 1, wherein the substance is used for adsorbing one or more substances selected from the group consisting of formaldehyde, acetaldehyde, tar, nitrosamines, and polycyclic aromatic hydrocarbons that cause sick house syndrome. The adsorbent described.

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