WO2006046758A1 - Process for producing blocked isocyanate compound - Google Patents
Process for producing blocked isocyanate compound Download PDFInfo
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- WO2006046758A1 WO2006046758A1 PCT/JP2005/020151 JP2005020151W WO2006046758A1 WO 2006046758 A1 WO2006046758 A1 WO 2006046758A1 JP 2005020151 W JP2005020151 W JP 2005020151W WO 2006046758 A1 WO2006046758 A1 WO 2006046758A1
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- WIPO (PCT)
- Prior art keywords
- isocyanate compound
- compound
- blocked isocyanate
- iii
- ethylenically unsaturated
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D231/00—Heterocyclic compounds containing 1,2-diazole or hydrogenated 1,2-diazole rings
- C07D231/02—Heterocyclic compounds containing 1,2-diazole or hydrogenated 1,2-diazole rings not condensed with other rings
- C07D231/10—Heterocyclic compounds containing 1,2-diazole or hydrogenated 1,2-diazole rings not condensed with other rings having two or three double bonds between ring members or between ring members and non-ring members
- C07D231/14—Heterocyclic compounds containing 1,2-diazole or hydrogenated 1,2-diazole rings not condensed with other rings having two or three double bonds between ring members or between ring members and non-ring members with hetero atoms or with carbon atoms having three bonds to hetero atoms with at the most one bond to halogen, e.g. ester or nitrile radicals, directly attached to ring carbon atoms
- C07D231/28—Two oxygen or sulfur atoms
- C07D231/30—Two oxygen or sulfur atoms attached in positions 3 and 5
- C07D231/32—Oxygen atoms
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D231/00—Heterocyclic compounds containing 1,2-diazole or hydrogenated 1,2-diazole rings
- C07D231/02—Heterocyclic compounds containing 1,2-diazole or hydrogenated 1,2-diazole rings not condensed with other rings
- C07D231/10—Heterocyclic compounds containing 1,2-diazole or hydrogenated 1,2-diazole rings not condensed with other rings having two or three double bonds between ring members or between ring members and non-ring members
- C07D231/12—Heterocyclic compounds containing 1,2-diazole or hydrogenated 1,2-diazole rings not condensed with other rings having two or three double bonds between ring members or between ring members and non-ring members with only hydrogen atoms, hydrocarbon or substituted hydrocarbon radicals, directly attached to ring carbon atoms
Definitions
- the present invention relates to a process for producing a blocked isocyanate compound, which is a blocked form of an ethyleneically unsaturated group-containing isocyanate, suitable for use as starting monomers of various coating agents, adhesives, and molding materials. More particularly, the present invention relates to a production process that can produce a high-purity blocked isocyanate compound on a commercial scale while avoiding the production of by-products caused by polymerization and the like.
- Blocked isocyanate compounds are compounds produced by reacting an isocyanate group with an active hydrogen group-containing compound (a blocking agent) to render the compounds inert at room temperature. Upon heating of the blocked isocyanate compounds, the blocking agent is dissociated, and the isocyanate group is regenerated.
- blocking agents for blocking the isocyanate group include alcohols, phenols, lactams, oximes, alkyl acetoacetates, alkyl malonates, phthalimides, imidazoles, hydrogen chloride, hydrogen cyanide, and sodium hydrogensulfite.
- Blocked isocyanate compounds produced by blocking the isocyanate group by, among the above blocking agents, substituted phenols, oximes, alkyl acetoacetates, alkyl malonates, phthalimides, imidazoles, hydrogen chloride, hydrogen cyanide, or sodium hydrogensulfite cause dissociation at relatively low temperatures to regenerate the isocyanate group.
- the dissociation temperature upon heating for 20 min is as follows.
- n-Butanol about 170 0 C Phenol: about 16O 0 C Caprolactam: about 160°C Methyl ethyl ketone oxime: about 15O 0 C Acetoacetic ester: about 140 0 C Diethyl malonate: about 130 0 C
- Patent document 2 exemplifies polyblocked isocyanate compounds produced using 1, 2, 4-triazole and 3,5- dimethylpyrazole as the blocking agent
- patent document 3 exemplifies polyblocked isocyanate compounds produced using an acetoacetic ester as the blocking agent
- patent document 4 exemplifies polyblocked isocyanate compounds produced using a diester of malonic acid as the blocking agent.
- patent document 5 exemplifies a method in which polyisocyanate is reacted with 3, 5-dim.ethylpyrazole in an organic solvent at
- patent document 6 exemplifies a method in which polyisocyanate is reacted with a pyrazole compound in an organic solvent at a
- patent document 7 exemplifies a method that comprises heating pyrazole or its derivative to a temperature at or above the melting point for melting, or dissolving or dispersing pyrazole or its derivative in an inert solvent such as toluene or xylene, and adding an ethylenically unsaturated group-containing compound or a solution of the compound dissolved in an inert solvent to the melt or the solution or dispersion.
- This method is advantageous in that the blocked isocyanate compound can be stably produced without causing polymerization of the blocked isocyanate compound and, at the same time, substantially no by-product is produced.
- Patent document 1 Japanese Patent Laid-Open No. 017116/1991
- Patent document 2 Japanese Patent Laid-Open No. 304843/1995
- Patent document 3 Japanese Patent Laid-Open No. 116420/1977
- Patent document 4 Japanese Patent Laid-Open No. 121065/1982
- Patent document 5 Japanese Patent Laid-Open No. 225509/1996
- Patent document 6 Japanese Patent Laid-Open No. 104726/1996
- Patent document 7 Japanese Patent Laid-Open No. 316663/1998
- an object of the present invention is to provide a production process of a blocked isocyanate compound, that is, a production process of a blocked isocyanate compound comprising blocking an isocynate group in an ethylenically unsaturated group-containing isocyanate compound with a pyrazole compound, which production process can produce the compound with higher efficiency without the need to use any inert solvent.
- R 1 represents a hydrogen atom or a methyl group
- R 3 represents an alkylene group having 2 to 6 carbon atoms
- Q 1 and Q 2 each independently represent a hydrogen atom, an alkyl group having 1 to 6 carbon atoms, RCONH-, or ROCO- wherein R represents an alkyl group having 1 to 6 carbon atoms, said process being characterized by comprising reacting a pyrazole compound (I) represented by general formula (I) :
- R 1 and R 2 are as defined above,
- a high-purity blocked isocyanate compound can be produced. Furthermore, in the production process according to the present invention, unlike the prior art technique, since there is no need to use any inert solvent such as toluene or xylene, safety to the human body and environment is excellent and the production processes and equipment can be simplified.
- the blocked isocyanate compound produced by the production process contains no residual inert solvent and is suitable for use in extensive fields such as various coating agents, adhesives, and molding materials.
- Fig. 1 is a 1 H-NMR spectrum of a blocked isocyanate compound produced in Example 1.
- a pyrazole compound (I) is reacted with an ethylenically unsaturated group-containing isocyanate compound (II) at a temperature in the range of
- R 1 , R 2 , Q 1 , and Q 2 are as defined below.
- the pyrozole compound (I] as a starting compound is less likely to be sublimated. Therefore, there is no need to use an excessive amount of the starting compound, and, thus, the blocked isocyanate compound can be produced with good efficiency. Further, since substantially no by-product is produced, a high- purity blocked isocyanate compound can be produced. Furthermore, since there is no need to use any inert solvent, safety to the human body and environment is excellent, and the production processes and equipment can be simplified.
- the pyrazole compound (I) used in the production process of the present invention is represented by general formula (I) :
- Q 1 and Q 2 each independently represent a hydrogen atom, an alkyl group having 1 to 6 carbon atoms, RCONH-, or ROCO- wherein R represents an alkyl group having 1 to 6 carbon atoms, preferably an alkyl group having 1 to 5 carbon atoms. R preferably represents an alkyl group having 1 to 4 carbon atoms .
- pyrazole compound (I) Various compounds, for example, unsubstituted pyrazole, 3, 5-dimethylpyrazole, 3-acetylaminopyrazole, and diethyl pyrazole-3, 5-dicarboxylate may be used as the pyrazole compound (I) .
- 3, 5-dimethylpyrazole is particularly preferred, for example, from the viewpoints of good availability and curability or other physical properties when it is used as a curable resin.
- the pyrazole compound (I) used in the present invention can be produced by the conventional process.
- the ethylenically unsaturated group-containing isocyanate compound (II) used in the production process of the present invention is represented by general formula (ID :
- R 1 represents a hydrogen atom or a methyl group
- R 2 represents -CO- or -COOR 3 - wherein R 3 represents an alkylene group having 2 to 6 carbon atoms, preferably - COOR 3 - wherein R 3 is as defined above.
- Examples of the ethyleneically unsaturated group- containing isocyanate compound (II) include 2- isocyanatoethyl (meth) acrylate, 3- isocyanatopropyl (meth) acrylate, 2-isocyanato-l-methyl ethyl (meth) acrylate, and methacryloyl isocyanate.
- the ethylenically unsaturated group-containing isocyanate compound (II) used in the present invention can be produced by the conventional method.
- the blocked isocynate compound (III) according to the present invention is produced by reacting the pyrazole compound (I) with the ethylenically unsaturated group- containing isocyanate compound (II) at a temperature in the
- the blocked isocyanate compound (III) can be produced, for example, by the following methods: (1) a method in which a pyrazole compound (I) is charged into a reactor and an ethylenically unsaturated group-containing isocyanate compound (II) is added to the reactor with stirring to react the compound (I) with the compound (II) ; (2) a method in which an ethylenically unsaturated group-containing isocyanate compound (II) is charged into a reactor and a pyrazole compound (I) is added to the reactor with stirring to react the compound (I) with the compound (II) ; and (3) a method in which both a pyrazole compound (I) and an ethylenically unsaturated group-containing isocyanate compound (II) are simultaneously added to a reactor with stirring to react the compound (I) with the compound (II) .
- the temperature of the reaction of the pyrazole compound (I) with the ethylenically unsaturated group- containing isocyanate compound (II) may vary depending upon the types of the compound (I) and the compound (II) .
- the reaction temperature is below the melting point of the pyrazole compound (I) and is generally 0°C to 90 0 C, preferably 5°C to 70 0 C, more preferably 10°C to 60°C.
- the reaction temperature is in the above-defined range, the blocked isocyanate compound can be produced with good efficiency. Further, in this case, since substantially no by-product is produced, the purity of the resultant compound is high. Specifically, when the reaction temperature is generally 0°C to 90 0 C, preferably 5°C to 70 0 C, more preferably 10°C to 60°C.
- reaction temperature is below 0°C, the reaction rate is lowered and the lowered reaction rate affects the productivity and thus makes it impossible to produce the blocked isocyanate compound with good efficiency.
- reaction temperature when the reaction temperature is above 90°C, the pyrazole compound (I) is sublimated and, thus, the blocked isocyanate compound cannot be produced with good efficiency. Further, in this case, gelation is likely to occur due to polymerization of the ethylenically unsaturated group and, consequently, the blocked isocyanate compound (III) of high purity cannot be produced.
- the upper limit of the reaction temperature is preferably in such a temperature range that the pyrazole compound (I) is . not sublimated, and is properly determined by the type of the pyrazole compound (I) used.
- This reaction temperature includes a reaction temperature during the addition of the pyrazole compound (I) and/or the ethylenically unsaturated group-containing isocyanate compound (II), for example, by dropping.
- the reaction is generally carried out until the pyrazole compound (I) or the ethylenically unsaturated group-containing isocyanate compound (II) is substantially entirely consumed. Accordingly, the reaction time is not particularly limited. In general, however, the reaction time is about 30 min to 8 hr.
- the disappearance of the pyrazole compound (I) may be confirmed, for example, by the fact that, as a result of high speed liquid chromatography, the level of the compound (I) is below the detection limit.
- the disappearance of the ethylenically unsasturated group-containing isocyanate compound (II) may be confirmed, for example, by the fact that, as a result of IR measurement, the level of absorption based on NCO group is below the detection limit.
- the reaction time includes the time taken for the addition of the pyrazole compound (I) and/or the ethylenically unsaturated group-containing isocyanate compound (II) , for example, by dropping.
- the amount of the pyrazole compound (I) is 0.5 to 2.0 times by mole, preferably 0.8 to 1.5 times by mole, more preferably 1.0 to 1.2 times by mole, the amount of the ethylecially unsaturated group-containing isocyanate compound (II) .
- the reaction ratio between these compounds is theoretically 1 : 1 (molar ratio) .
- the reaction can be allowed to proceed smoothly by adding the compounds in the above-defined molar ratio.
- the sublimation of the pyrazole compound (I) as a starting compound is less likely to occur. Therefore, unlike the prior art technique, there is no need to use the starting compound in an excess amount, and, thus, the blocked isocyanate compound can be produced with good efficiency and the starting compounds (I) and (II) remaining unreacted are not substantially present.
- the addition of a polymerization inhibitor to the reaction system is preferred.
- the polymerization inhibitor is rapidly reacted with free radicals produced from monomers in the free- radical polymerization and thus can stabilize the reaction system so that the free-radical polymerization reaction does not proceed.
- Commonly used polymerization inhibitors for example, phenothiazine, p-methoxy phenol and 2, 6-ditert-butyl-4- methylphenol (BHT) , may be used as the polymerization inhibitor.
- the polymerization inhibitor can be introduced by any method without particular limitation, and examples of introduction methods usable herein include a method in which the polymerization inhibitor, together with the pyrazole compound (I), is introduced into a reactor, a method in which the polymerization inhibitor is dissolved in the ethylenically unsaturated group-containing isocyanate compound (II) and the resultant solution is then introduced into a reactor, a method in which the polymerization inhibitor is mixed to both the pyrazole compound (I) and the ethylenically unsaturated group- containing isocyanate compound (II) and these mixtures are each introduced into a reactor, and a method in which, after the completion of the reaction, the polymerization inhibitor is introduced into the resultant blocked isocyanate compound (III) .
- the reaction of the pyrazole compound (I) with the ethylenically unsaturated group-containing isocyanate compound (II) in the presence of a polymerization inhibitor is preferred.
- the amount of the polymerization inhibitor used varies depending upon the type of the pyrozole compound (I) and the ethylenically unsaturated group-containing isocyanate compound (II) .
- the amount of the polymerization inhibitor used is generally 10 to 20000 ppm, preferably 50 to 10000 ppm, more preferably 100 to 5000 ppm, based on the blocked isocyanate compound (III) produced by the reaction of the compound (I) with the compound (II) .
- the amount of the polymerization inhibitor used is less than 10 ppm, during the production of the blocked isocyanate compound (III) , the polymerization of the ethylenically unsaturated group in the ethylenically unsaturated group-containing isocyanate compound (II) is likely to occur.
- the blocked isocyanate compound (III) represented by general formula (III) according to the present invention may be produced by the above process. A method may also be preferably adopted in which this blocked isocyanate compound (III) is used as a solvent or a dispersant and, in the medium, the blocked isocyanate compound (III) is further prepared.
- the stirring efficiency can be improved and, thus, the reaction of the compound (I) with the compound (II) can be allowed to proceed smoothly. Further, since the reaction can be carried out at a relatively low temperature, the sublimation of the pyrazole compound (I) as the starting compound is less likely to occur. Accordingly, the reaction can be completed without the need to use the starting compound in an excess amount, and, thus, the blocked isocyanate compound can be produced with good efficiency. Further, since substantially no by ⁇ product is produced, a high-purity blocked isocyanate compound can be produced. Furthermore, unlike the prior art technique, since there is no need to use any inert solvent such as toluene or xylene, safety to the human body and environment is excellent and the production processes and equipment can be simplified.
- any inert solvent such as toluene or xylene
- the production of the compound (III) using the blocked isocyanate compound (III) as a solvent or a dispersant can be carried out, for example, by
- a blocked isocyanate compound (III) and an ethylenically unsaturated group-containing isocyanate compound (II) are charged into a reactor, the ethylenically unsaturated group-containing isocyanate compound (II) is dissolved or disperse, and a pyrazole compound (I) dissolved or dispersed in a blocked isocyanate compound (III) is then added to the reactor to react the compound (I) with the compound (II) , and
- the blocked isocyanate compound (III) is produced by any one of the above methods (1) to (7), the fluidity of the starting compounds can be improved. Specifically, the starting compounds can easily be transferred even on a commercial scale to allow the reaction to proceed smoothly.
- the methods (1) to (7) the methods (I) / (6) and (7) are particularly preferred.
- the blocked isocyanate compound (III) is used as the solvent or dispersant
- the use of the same pyrazole compound (I) and ethylenically unsaturated group-containing isocyanate compound (II) as used in the production of the compound (III) is preferable.
- the amount of the compound (III) used is not particularly limited. Preferably, however, the amount of the compound (III) used is 0.01 to 50 times by mole, preferably 0.01 to 10 times by mole, more preferably 0.01 to 5 times by mole, the amount of the pyrazole compound (I) .
- the amount of the compound (III) used is less than 0.01 time by mole, the contemplated effect as the solvent or dispersant cannot be attained, probably, for example, leading to a lowering in reaction rate, although no problem occur in the reaction.
- the above production process according to the present invention can provide a blocked isocyanate compound (III) , according to the present invention, represented by general formula (III) :
- R 1 , R 2 , Q 1 , and Q 2 are as defined above.
- the blocked isocyanate compound (III) according to the present invention may contain a small amount of impurities such as starting compounds remaining unreacted and the polymerization inhibitor as mentioned later. These impurities may be removed by any conventional method for the purification of the product.
- a blocked isocyanate compound (III) In the production process of a blocked isocyanate compound (III) according to the present invention, since the reaction is allowed to proceed at the above temperature, the reaction proceeds smoothly without substantially causing sublimation of the pyrazole compound (I) .
- a high-purity blocked isocyanate compound (III) which does not contain or contains only a small amount (not more than 3% by weight) of the pyrazole compound (I) remaining unreacted or contains only a small amount (not more than 1000 ppm) , of the ethylenically unsaturated isocyanate compound (II) remaining unreacted can be produced.
- the blocked isocyanate compound (III) can be advantageously used, for example, as starting monomers of various coating agents, adhesive, and molding materials.
- Integrator C-R8A, manufactured by Shimadzu Corporation.
- Sample preparation About 0.1 g of a sample was weighed into a 10-ml measuring flask, and the eluent was added to a predetermined volume.
- Sample preparation About 0.1 g of a sample was weighed into a 10-ml measuring flask, and the eluent was added to a predetermined volume.
- Carrier gas He 30 ml/min
- NMR measurement Measurement of nuclear magnetic resonance spectrum
- the blocked isocyanate compound (17.09 g, 0.068 mol) synthesized by the process described in Example 1, 3,5- dimethylpyrazole (19.81 g, 0.204 mol), and BHT (0.2 g, 0.84 mmol) were charged into a 100-ml four-necked flask equipped with a stirrer, a thermometer, a dropping funnel, and a reflux condenser, and the contents of the flask were stirred at room temperature for one hr.
- 2- isocyanatoethyl methacrylate (31.03 g, 0.2 mol) was added dropwise through the dropping funnel over a period of 90 min. Upon the dropwise addition, the internal temperature
- the blocked isocyanate compound (768.97 g, 3.06 mol) synthesized by the process described in Example 1, 3,5-dimethylpyrazole (19.81 g, 0.204 mol), and BHT (0.2 g, 0.84 mmol) were charged into a 2000-ml four-necked flask equipped with a stirrer, a thermometer, a dropping funnel, and a reflux condenser, and the contents of the flask were stirred at room temperature for one hr. Next, solution A was added dropwise through the dropping funnel over a period of 3 hr. Upon the dropwise addition, the internal
- Example 5 As a result, it was found that the same blocked isocyanate compound as produced in Example 1 was produced. As a result of LC analysis (1), it was found that the content of 3, 5-dimethylpyrazole was 0.76% by weight. Further, the product was subjected to GC analysis and was found to have a BHT content of 4400 ppm.
- Example 5 As a result of LC analysis (1), it was found that the content of 3, 5-dimethylpyrazole was 0.76% by weight. Further, the product was subjected to GC analysis and was found to have a BHT content of 4400 ppm. Example 5
- the blocked isocyanate compound (17.09 g, 0.068 mol) synthesized by the process described in Example 1, 2- isocyanatoethyl methacrylate (31.03 g, 0.2 mol), and BHT (0.2 g, 0.84 mmol) were charged into a 100-ml four-necked flask equipped with a stirrer, a thermometer, a dropping funnel, and a reflux condenser, and the contents of the flask were stirred at room temperature for one hr.
- 3, 5-dimethylpyrazole (19.81 g, 0.204 mol) was introduced by portions into the flask over a period of 90 min. Upon the introduction of 3, 5-dimethylpyrazole, a rise in internal temperature was observed. Specifically, the internal temperature of the flask changed from 25°C to 40°C. After the completion of the dropwise addition, stirring was
- the blocked isocyanate compound (768.97 g, 3.06 mol) synthesized by the process described in Example 1 and 3,5- dimethylpyrazole (19.81 g, 0.204 mol) were charged into a 1-L flask, and the contents of the flask were stirred at room temperature for one hr to prepare slurry solution A.
- the blocked isocyanate compound (768.97 g, 3.06 mol) synthesized by the process described in Example 1, 2- isocyanatoethyl methacrylate (31.03 g, 0.2 mol), and BHT (0.2 g, 0.84 mmol) were charged into a 2000-ml four-necked flask equipped with a stirrer, a thermometer, a dropping funnel, and a reflux condenser, and the contents of the flask were stirred at room temperature for one hr.
- slurry solution A was introduced through a plunger pump into the four-necked flask over a period of 3 hr. Upon the introduction of slurry solution A, the internal temperature
- Example 8 The blocked isocyanate compound (768.97 g, 3.06 mol) synthesized by the process described in Example 1 and 3, 5-dimethylpyrazole (19.81 g, 0.204 mol) were charged into a 1-L flask, and the contents of the flask were stirred at room temperature for one hr to prepare slurry solution A.
- the blocked isocyanate compound (768.94 g, 3.06 mol) synthesized by the process described in Example 1 and 2- isocyanatoethyl methacrylate (31.03 g, 0.2 mol) were charged into another 1-L flask, and the contents of the flask were stirred at room temperature for one hr to prepare solution B.
- BHT (0.2 g, 0.84 mmol) was charged into a 2000-ml four-necked flask equipped with a stirrer, a thermometer, a dropping funnel, and a reflux condenser. Slurry solution A and solution B were simultaneously added dropwise to the four-necked flask at room temperature with stirring over a period of 3 hr.
- the internal temperature changed from 25°C to 30°C.
- stirring was continued at an internal temperature in the range of 30°C to 40°C for one hr while regulating the temperature in a water bath.
- a small amount of a sample was obtained from within the reaction system, and an IR spectrum was measured.
- the reaction solution was cooled to room temperature to give 1588.5 g of a light-yellow transparent liquid product. The product was measured for 1 H-NMR.
- Example 9 As a result, it was found that the same blocked isocyanate compound as produced in Example 1 was produced. As a result of LC analysis (1), it was found that the content of 3, 5-dimethylpyrazole was 0.76% by weight. Further, the product was subjected to GC analysis and was found to have a BHT content of 4400 ppm.
- the blocked isocyanate compound (753.84 g, 3.00 mol) synthesized by the process described in Example 1, 3,5- dimethylpyrazole (29.13 g, 0.300 mol), and BHT (0.6 g, 2.54 mmol) were charged into a 1000-ml four-necked flask equipped with a stirrer, a thermometer, a dropping funnel, and a reflux condenser, and the contents of the flask were stirred in a water bath for one hr while regulating the
- 3,5-Dimethylpyrazole (19.81 g, 0.204 mol) and p- methoxyphenol (0.005 g, 0.04 mmol) were charged into a 100- ml four-necked flask equipped with a stirrer, a thermometer, a dropping funnel, and a reflux condenser under a nitrogen atmosphere, and the contents of the flask were cooled in a
- Example 12 The blocked isocyanate compound (16.13 g) synthesized in Example 11, 3, 5-dimethylpyrazole (19.81 g, 0.204 mol) and p-methoxyphenol (0.005 g, 0.04 mmol) were charged into a 100-ral four-necked flask equipped with a stirrer, a thermometer, a dropping funnel, and a reflux condenser under a nitrogen atmosphere, and the contents of the flask were cooled in a water bath of 15°C with stirring.
- a reaction was carried out in the same manner as in Example 1, except that diethyl pyrazole-3, 5-dicarboxylate (43.3 g, 0.202 mol) was used instead of 3,5- dimethylpyrazole.
- diethyl pyrazole-3, 5-dicarboxylate 43.3 g, 0.202 mol
- the reaction was stopped.
- the reaction solution was cooled to room temperature to give 74.3 g of a light- yellow transparent liquid product.
- the product was measured for 1 H-NMR. As a result, it was found that a blocked isocyanate compound represented by the following formula was produced.
- Example 15 The blocked isocyanate compound (16.75 g, 0.067 mol) synthesized by the process described in Example 1, 3,5- dimethylpyrazole (19.42 g, 0.200 mol), and BHT (0.2 g, 0.84 mi ⁇ ol) were charged into a 100-ml four-necked flask equipped with a stirrer, a thermometer, a dropping funnel, and a reflux condenser, and the contents of the flask were stirred at room temperature for one hr. Next, 2- isocyanatoethyl methacrylate (31.03 g, 0.2 mol) was added dropwise to the flask through the dropping funnel over a period of 90 min.
- 2- isocyanatoethyl methacrylate 31.03 g, 0.2 mol
Abstract
Description
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EP05800038.1A EP1812402B1 (en) | 2004-10-29 | 2005-10-27 | Process for producing blocked isocyanate compound |
CN2005800374066A CN101052624B (en) | 2004-10-29 | 2005-10-27 | Process for producing blocked isocyanate compound |
US11/666,696 US7504518B2 (en) | 2004-10-29 | 2005-10-27 | Process for producing blocked isocyanate compound |
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EP2377847A1 (en) | 2010-04-14 | 2011-10-19 | 3M Innovative Properties Company | Process for producing isocyanates |
JP5685839B2 (en) * | 2010-06-23 | 2015-03-18 | 日油株式会社 | Anti-fog coating composition |
US9970246B2 (en) | 2012-04-09 | 2018-05-15 | M-I L.L.C. | Triggered heating of wellbore fluids by carbon nanomaterials |
CN108707092A (en) * | 2012-07-30 | 2018-10-26 | 昭和电工株式会社 | The manufacturing method of blocked isocyanate compound |
WO2015016330A1 (en) * | 2013-08-02 | 2015-02-05 | ダイキン工業株式会社 | Novel compound having unsaturated group and composition including said compound |
JP5737466B1 (en) | 2013-08-02 | 2015-06-17 | ダイキン工業株式会社 | Composition and coated article comprising a fluorine-containing polymer containing at least one group selected from the group consisting of a polymerizable functional group and a crosslinkable functional group |
KR101957476B1 (en) | 2017-03-24 | 2019-03-12 | 한국화학연구원 | Dual cross-linkable low temperature cure blocked isocyanates and composition comprising the same |
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DE2612783C3 (en) * | 1976-03-25 | 1981-11-05 | Hoechst Ag, 6000 Frankfurt | Biurets, processes for their manufacture and their use |
DE3046409A1 (en) | 1980-12-10 | 1982-07-15 | Bayer Ag, 5090 Leverkusen | COATING AGENTS AND A METHOD FOR PRODUCING COVERS |
US5246557A (en) * | 1984-02-29 | 1993-09-21 | The Baxenden Chemical Co. | Blocked isocyanates |
JPH0749462B2 (en) | 1989-06-14 | 1995-05-31 | 日本ポリウレタン工業株式会社 | Blocked isocyanate compound, and low temperature curable composition, coating composition and adhesive composition containing the same |
JP3276440B2 (en) | 1992-03-02 | 2002-04-22 | 富士写真フイルム株式会社 | Electrophotographic color proofing master |
US5395721A (en) * | 1992-03-02 | 1995-03-07 | Fuji Photo Film Co., Ltd. | Electrophotographic material for color proofing |
DE4416750A1 (en) | 1994-05-13 | 1995-11-16 | Bayer Ag | Mixed blocked polyisocyanates |
-
2005
- 2005-10-27 EP EP05800038.1A patent/EP1812402B1/en active Active
- 2005-10-27 WO PCT/JP2005/020151 patent/WO2006046758A1/en active Application Filing
- 2005-10-27 US US11/666,696 patent/US7504518B2/en not_active Expired - Fee Related
- 2005-10-27 CN CN2005800374066A patent/CN101052624B/en active Active
- 2005-10-27 KR KR1020077011948A patent/KR100891790B1/en active IP Right Grant
- 2005-10-28 TW TW094137933A patent/TW200626529A/en unknown
- 2005-10-31 JP JP2005316071A patent/JP4879557B2/en active Active
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
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US5626996A (en) * | 1992-06-04 | 1997-05-06 | Fuji Photo Film Co., Ltd. | Electrophotographic material for color proofing |
US5567762A (en) * | 1994-03-14 | 1996-10-22 | Societe Francaise Hoechst | Acrylate-styrene resins cross-linked by a blocked polyisocyanate preparation and uses as paint and/or lacquer |
EP0713871A1 (en) * | 1994-11-22 | 1996-05-29 | Bayer Ag | Process for the preparation of 3,5-dimethylpyrazol blocked polyisocyanates |
JPH10316663A (en) * | 1997-05-19 | 1998-12-02 | Showa Denko Kk | Pyrazole-based compound and curing composition |
Also Published As
Publication number | Publication date |
---|---|
KR20070073940A (en) | 2007-07-10 |
TWI308562B (en) | 2009-04-11 |
KR100891790B1 (en) | 2009-04-07 |
JP2006151967A (en) | 2006-06-15 |
US20070265454A1 (en) | 2007-11-15 |
US7504518B2 (en) | 2009-03-17 |
EP1812402B1 (en) | 2013-07-17 |
JP4879557B2 (en) | 2012-02-22 |
EP1812402A1 (en) | 2007-08-01 |
TW200626529A (en) | 2006-08-01 |
CN101052624B (en) | 2010-05-12 |
CN101052624A (en) | 2007-10-10 |
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