JP2008086928A - Regeneration method of catalyst for producing methacrylic acid and production method of methacrylic acid - Google Patents

Regeneration method of catalyst for producing methacrylic acid and production method of methacrylic acid Download PDF

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JP2008086928A
JP2008086928A JP2006271586A JP2006271586A JP2008086928A JP 2008086928 A JP2008086928 A JP 2008086928A JP 2006271586 A JP2006271586 A JP 2006271586A JP 2006271586 A JP2006271586 A JP 2006271586A JP 2008086928 A JP2008086928 A JP 2008086928A
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catalyst
methacrylic acid
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regenerated
compound
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JP4715707B2 (en
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Yoshihiko Oishi
Eiichi Shiraishi
Junya Yoshizawa
純也 吉澤
嘉彦 大石
英市 白石
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Sumitomo Chemical Co Ltd
住友化学株式会社
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/584Recycling of catalysts

Abstract

Provided is a method for regenerating a catalyst for producing methacrylic acid having excellent catalytic activity and sustainability, and a method for producing methacrylic acid with good conversion and selectivity using the regenerated catalyst. .
A mixture containing a deterioration catalyst, an ammonium root, a nitrate root and water is dried and then molded, and the resulting molded body is obtained at 40 to 100 ° C. for 0.5 to 10 hours and a relative humidity of 10 to 60%. The catalyst for producing methacrylic acid composed of a heteropolyacid compound containing phosphorus and molybdenum is regenerated by exposing to an atmosphere of In the presence of this regenerated catalyst, a compound selected from methacrolein, isobutyraldehyde, isobutane and isobutyric acid is subjected to a gas phase catalytic oxidation reaction to produce methacrylic acid.
[Selection figure] None

Description

  The present invention relates to a method for regenerating a catalyst for producing methacrylic acid. Moreover, it is related also to the method of manufacturing methacrylic acid using the catalyst obtained by this method.

  When a catalyst for methacrylic acid production comprising a heteropolyacid compound containing phosphorus and molybdenum is used for a long time in a gas phase catalytic oxidation reaction using methacrolein or the like as a raw material, the catalytic activity decreases due to heat load, etc. It is known to deteriorate.

  As a method for regenerating such a deteriorated catalyst, Japanese Patent Application Laid-Open No. 61-283352 (Patent Document 1) discloses a molded article obtained by drying and molding a mixture containing a deteriorated catalyst, an ammonium root, a nitrate root and water. Is described.

  In JP-A-63-130144 (Patent Document 2), after drying a mixture of a deterioration catalyst and aqueous ammonia, the obtained dried product is dispersed in water, and a nitrogen-containing heterocyclic compound, amine or ammonium carbonate Are added, mixed, dried, molded, and the resulting molded body is fired.

  In JP-A-60-232247 (Patent Document 3), after a deteriorated catalyst is dispersed in water, a nitrogen-containing heterocyclic compound and nitric acid are added and mixed, dried and molded, and then the molded product obtained. Is described.

  In Japanese Patent Laid-Open No. 2001-286762 (Patent Document 4), after a deteriorated catalyst is dispersed in water, a nitrogen-containing heterocyclic compound and nitric acid are added, and a compound containing a disappearing constituent element of the catalyst is added and mixed. Then, after drying and molding, a method of firing the obtained molded body is described.

  JP-A 2001-286863 (Patent Document 5) discloses a molded article obtained by dispersing a deterioration catalyst in water, adding a nitrogen-containing heterocyclic compound, ammonium nitrate and nitric acid, mixing, drying and molding. Is described.

JP-A-61-283352 JP-A-63-130144 JP 60-232247 A JP 2001-286762 A JP 2001-286863 A

  However, in the above regeneration method, the recovery effect of the catalyst activity is not necessarily sufficient, and the catalyst activity and the sustainability of the obtained regeneration catalyst are not always satisfactory. Therefore, an object of the present invention is to provide a method for effectively recovering the catalytic activity of a deteriorated catalyst and regenerating a catalyst for producing methacrylic acid having good durability. Another object of the present invention is to provide a method for producing methacrylic acid with a good conversion rate and selectivity using the regenerated catalyst obtained by this method.

  As a result of diligent research, the inventors of the present invention have regenerated the deteriorated catalyst, dried the mixture containing the deteriorated catalyst, ammonium root, nitrate root and water, then molded, and performed a specific treatment on the resulting molded body. It has been found that the above object can be achieved by applying and then firing, and the present invention has been completed.

  That is, the present invention relates to a method for regenerating a catalyst for methacrylic acid production comprising a heteropolyacid compound containing phosphorus and molybdenum, and after drying a mixture containing a deterioration catalyst, an ammonium root, a nitrate radical and water, the molded article is obtained. Provided is a method for regenerating a catalyst for methacrylic acid production, which comprises subjecting the formed article to 40 to 100 ° C. in an atmosphere having a relative humidity of 10 to 60% for 0.5 to 10 hours and then firing. It is.

  Further, the present invention regenerates a catalyst for producing methacrylic acid by the above method, and subjecting the compound selected from methacrolein, isobutyraldehyde, isobutane and isobutyric acid to a gas phase catalytic oxidation reaction in the presence of the regenerated catalyst. It also provides a method for producing an acid.

  According to the present invention, the activity of a deteriorated catalyst can be effectively recovered, and a catalyst for producing methacrylic acid having good durability can be regenerated. Then, methacrylic acid can be produced with good conversion and selectivity using the regenerated catalyst thus obtained.

  Hereinafter, the present invention will be described in detail. The catalyst for methacrylic acid production to be regenerated by the present invention is composed of a heteropolyacid compound essentially containing phosphorus and molybdenum, and may be composed of a free heteropolyacid or a salt of a heteropolyacid. It may be. Especially, what consists of an acidic salt (partially neutralized salt) of heteropolyacid is preferable, More preferably, it consists of an acidic salt of Keggin type heteropolyacid.

  The catalyst preferably contains vanadium as an element other than phosphorus and molybdenum, and at least one element selected from potassium, rubidium, cesium and thallium (hereinafter sometimes referred to as X element) or the like. It is desirable that at least one element selected from copper, arsenic, antimony, boron, silver, bismuth, iron, cobalt, lanthanum, and cerium (hereinafter sometimes referred to as Y element) is included. Usually, a catalyst containing phosphorus, vanadium, X element and Y element at a ratio of 3 atoms or less to 12 atoms of molybdenum is preferably used.

  When such a methacrylic acid production catalyst is used in the production of methacrylic acid or receives a thermal history, decomposition of active sites, reduction of specific surface area, and the like occur, and as a result, catalytic activity decreases. In the present invention, a so-called deteriorated catalyst having a reduced catalytic activity is a target for regeneration treatment. In addition, about the decomposition | disassembly of an active site, it can be confirmed by performing XRD (X-ray diffraction) analysis, and whether the molybdenum trioxide which is a decomposition product of a catalyst is detected. About the specific surface area of a catalyst, BET It can be determined by specific surface area measurement.

  In the regeneration treatment, first, a mixture containing a deterioration catalyst, an ammonium root, a nitrate root and water is prepared. There is no particular limitation on the preparation method. For example, after suspending the deterioration catalyst in water, a raw material compound of ammonium root and nitrate radical may be added, or the deterioration catalyst is added to an aqueous solution containing ammonium root and nitrate root. It may be suspended.

  When the deterioration catalyst is a molded body, it may be suspended as it is, or the molded body may be pulverized and suspended. However, if the molded body contains fibers or the like that develop the strength of the catalyst, there is a concern that the strength may decrease when the molded body is cut. Therefore, when pulverizing, the fibers or the like should not be cut. Is preferred.

  Examples of the ammonium root raw material compound include ammonia and ammonium salts such as ammonium nitrate, ammonium carbonate, ammonium hydrogen carbonate, and ammonium acetate, and preferably ammonia and ammonium nitrate. Examples of the nitrate radical material compound include nitric acid and nitrates such as ammonium nitrate, and preferably nitric acid and ammonium nitrate. The amount of these raw material compounds is appropriately adjusted so that the ammonium root is usually about 0.1 to 15 moles and the nitrate radical is usually about 0.1 to 15 moles per 12 moles of molybdenum in the mixture. Good.

  Usually, ion-exchanged water is used as a water supply source. The usage-amount of water is 1-20 weight part normally with respect to 1 weight part of molybdenum in the said mixture.

  The mixture is then dried, but it is preferable to perform a heat treatment before drying.

  Examples of the method for drying the mixture include methods usually used in this field, such as an evaporation to dryness method, a spray drying method, a drum drying method, and an airflow drying method.

  When heat treatment is performed before drying, such heat treatment can be performed in a closed container, and the heat treatment temperature is preferably 100 ° C. or higher. The heat treatment time is usually 0.5 hours or longer, preferably 2 hours or longer, more preferably 2 to 10 hours.

  The obtained dried product is formed into a ring shape, a pellet shape, a spherical shape, a cylindrical shape, or the like by tableting or extrusion. At this time, in order to increase the strength, a molding aid such as ceramic fiber or glass fiber may be used as necessary.

  In this invention, the obtained molded object is exposed to the atmosphere of 10-60% of relative humidity at 40-100 degreeC for 0.5 to 10 hours. By treating under such conditions, the catalytic activity and its sustainability can be recovered well. The treatment may be performed, for example, in a temperature-controlled and humidity-controlled tank, or by spraying a temperature-controlled and humidity-controlled gas on the molded body. In addition, as the atmospheric gas for the treatment, air is usually used, but an inert gas such as nitrogen may be used.

  If the treatment temperature is too low, the activity of the obtained regenerated catalyst is not sufficient, and if it is too high, the selectivity of the obtained regenerated catalyst is not sufficient. Even if the treatment time is too short or too long, the activity of the obtained regenerated catalyst is not sufficient. If the relative humidity during the treatment is too low, the selectivity of the regenerated catalyst obtained is not sufficient. If it is too high, the activity of the regenerated catalyst obtained is not sufficient, and the strength of the molded article after treatment is not sufficient. Therefore, the handleability is deteriorated.

  A regenerated catalyst can be obtained by firing the molded article after the treatment. Such firing may be performed in an atmosphere of an oxidizing gas such as oxygen, or may be performed in an atmosphere of a non-oxidizing gas such as nitrogen, and is preferably performed at 300 ° C. or higher. Moreover, it is preferable to perform heat treatment (pre-firing) by maintaining the temperature in the atmosphere of the oxidizing gas or the non-oxidizing gas at a temperature of about 180 to 300 ° C. before the firing.

  The regenerated catalyst thus obtained is made of a heteropolyacid compound and may be made of a free heteropolyacid or a salt of a heteropolyacid. Especially, what consists of an acidic salt of heteropolyacid is preferable, and what consists of acidic salt of a Keggin type heteropolyacid is more preferable. In addition, it is more preferable that a Keggin type heteropolyacid salt structure is formed during the heat treatment (pre-firing).

  Such a regenerated catalyst has approximately the same catalytic activity and sustainability as the new catalyst. In the presence of the regenerated catalyst, methacrylic acid can be produced with good conversion and selectivity by subjecting a raw material compound such as methacrolein to a gas phase catalytic oxidation reaction.

  The production of methacrylic acid is usually carried out by filling a fixed bed multitubular reactor with a catalyst and supplying a raw material gas containing oxygen and a raw material compound selected from methacrolein, isobutyraldehyde, isobutane and isobutyric acid. However, it is also possible to adopt a reaction format such as fluidized bed or moving bed. As the oxygen source, air is usually used, and the raw material gas may contain nitrogen, carbon dioxide, carbon monoxide, water vapor and the like as components other than the raw material compound and oxygen.

For example, when methacrolein is used as a raw material, the concentration of methacrolein in the raw material gas is usually 1 to 10% by volume, the molar ratio of oxygen to methacrolein is 1 to 5, and the space velocity is 500 to 5000 h −1 (standard condition standard ), The reaction temperature is 250 to 350 ° C., and the reaction pressure is 0.1 to 0.3 MPa. The raw material methacrolein is not necessarily a highly purified product, and for example, a reaction product gas containing methacrolein obtained by a gas phase catalytic oxidation reaction of isobutylene or t-butyl alcohol can be used.

When isobutane is used as a raw material, the isobutane concentration in the raw material gas is usually 1 to 85% by volume, the water vapor concentration is 3 to 30% by volume, the molar ratio of oxygen to isobutane is 0.05 to 4, and the space velocity is 400. The reaction is carried out under conditions of ˜5000 h −1 (standard condition standard), reaction temperature of 250 to 400 ° C., and reaction pressure of 0.1 to 1 MPa. When isobutyric acid or isobutyraldehyde is used as a raw material, generally the same reaction conditions are employed as when methacrolein is used as a raw material.

  Examples of the present invention will be described below, but the present invention is not limited thereto. The air used in each example contains 2% by volume of moisture (corresponding to the atmosphere), and the nitrogen used in each example is substantially free of moisture. The conversion rate and selectivity are defined as follows.

  Conversion (%) = moles of methacrolein reacted ÷ moles of methacrolein fed × 100. Selectivity (%) = number of moles of methacrylic acid produced / number of moles of reacted methacrolein × 100.

Reference Example 1 (Preparation of new catalyst and evaluation of new catalyst)
In 224 kg of ion-exchanged water heated to 40 ° C., 38.2 kg of cesium nitrate [CsNO 3 ], 27.4 kg of 75% by weight orthophosphoric acid, and 25.2 kg of 70% by weight nitric acid were dissolved, and this was designated as solution A. On the other hand, after dissolving 297 kg of ammonium molybdate tetrahydrate [(NH 4 ) 6 Mo 7 O 24 · 4H 2 O] in 330 kg of ion-exchanged water heated to 40 ° C., ammonium metavanadate [NH 4 VO 3 ] 8.19 kg was suspended and this was used as B liquid. The liquid A and the liquid B were adjusted to 40 ° C., and the liquid A was added dropwise to the liquid B with stirring. Then, the liquid was stirred at 120 ° C. for 5.8 hours, and then antimony trioxide [Sb 2 O 3 ] 10 .2 kg and 10.2 kg of copper nitrate trihydrate [Cu (NO 3 ) 2 .3H 2 O] were suspended in 23 kg of ion-exchanged water and then stirred in a sealed container at 120 ° C. for 5 hours. . The mixture thus obtained was dried with a spray dryer, and 4 parts by weight of ceramic fiber, 13 parts by weight of ammonium nitrate, and 9.7 parts by weight of ion-exchanged water were added to 100 parts by weight of the dried powder and kneaded to obtain a diameter. Extrusion molding was performed in a cylindrical shape of 5 mm and 6 mm in height. The molded body was dried at a temperature of 90 ° C. and a relative humidity of 30% for 3 hours, and then heat-treated (pre-fired) in the order of 22 hours at 220 ° C. in an air stream and 1 hour at 250 ° C. in an air stream. The temperature was raised to 435 ° C. in an air stream and held at that temperature for 3 hours. Furthermore, after cooling to 300 ° C. in a nitrogen stream, nitrogen was switched to air, the temperature was increased to 390 ° C. in the air stream, and the temperature was maintained for 3 hours. Then, after cooling to 70 degreeC in air stream, the catalyst was taken out. This catalyst is an acid salt of a Keggin type heteropolyacid containing phosphorus, molybdenum, vanadium, antimony, copper and cesium in atomic ratios of 1.5, 12, 0.5, 0.5, 0.3 and 1.4, respectively. It consisted of.

[Detection of molybdenum trioxide by XRD measurement]
The catalyst obtained above was subjected to XRD measurement by a powder method. Molybdenum trioxide (XRD) corresponding to the acid salt of Keggin type heteropolyacid as the main component with respect to the strength of d = 3.38 to 3.41 ( The intensity ratio (%) of the peak intensity of XRD corresponding to MoO 3 ) = 3.24 to 3.26 was measured. The measurement results are shown in Table 1.

[BET specific surface area measurement]
About 1 g of the catalyst obtained above was vacuum degassed and then dehydrated at 120 ° C., and the BET specific surface area was measured. The measurement results are shown in Table 1.

[Catalyst activity test]
9 g of the catalyst obtained above was filled in a glass microreactor having an inner diameter of 15 mm, and 4 vol% methacrolein prepared by mixing methacrolein, air, steam and nitrogen, 12 vol% molecular oxygen, A raw material gas having a composition of 17% by volume of water vapor and 67% by volume of nitrogen is supplied at a space velocity of 670 h −1 , and the reaction is carried out at a furnace temperature (furnace temperature for heating the microreactor) of 280 ° C. The conversion rate and selectivity at the lapse of 1 hour were determined. Next, in order to evaluate the sustainability of the catalyst activity, the raw material gas having the same composition as described above is supplied at the same space velocity, the reaction is performed at the furnace temperature of 355 ° C., and the catalyst is forcibly deteriorated. The raw material gas having the same composition as above was supplied at the same space velocity as described above, and the reaction was performed at a furnace temperature of 280 ° C., and the conversion rate and selectivity after 1 hour from the start of the reaction were determined. Table 1 shows the conversion rate and selectivity before and after forced deterioration.

Reference Example 2 (Acquisition of degraded catalyst and evaluation of degraded catalyst)
The new catalyst prepared in Reference Example 1 was treated at 450 ° C. for 5 hours under an air stream to prepare a deteriorated catalyst. The obtained deteriorated catalyst was subjected to XRD measurement, BET specific surface area measurement, and activity test in the same manner as in Reference Example 1. These results are shown in Table 1.

Example 1 (Regeneration of catalyst and evaluation of regenerated catalyst)
200 g of the deteriorated catalyst obtained in Reference Example 2 was suspended in 400 g of ion-exchanged water heated to 80 ° C. and held for 1 hour. The solution was allowed to cool to room temperature, 60.2 g of ammonium nitrate [NH 4 NO 3 ] was added, the temperature was raised to 70 ° C., and the temperature was maintained for 1 hour. Thereafter, 17.9 g of 25 wt% aqueous ammonia was added. After holding at 70 ° C. for 1 hour, the temperature was lowered. The obtained mixture was dried at 110 ° C., 6 parts by weight of ion-exchanged water was added to 100 parts by weight of the obtained dried product, and the mixture was kneaded and extruded into a cylindrical shape having a diameter of 5 mm and a height of 6 mm. The molded body was exposed to an atmosphere of 90 ° C. for 3 hours and a relative humidity of 30%, and then heat treated (pre-fired) in the order of 22 hours at 220 ° C. in an air stream and 1 hour at 250 ° C. in an air stream. Thereafter, the temperature was raised to 435 ° C. in a nitrogen stream and held at the same temperature for 3 hours. Furthermore, after cooling to 300 ° C. in a nitrogen stream, nitrogen was switched to air, the temperature was increased to 390 ° C. in the air stream, and the temperature was maintained for 3 hours. Then, after cooling to 70 degreeC in air stream, the catalyst was taken out. The regenerated catalyst obtained was subjected to XRD measurement, BET specific surface area measurement, and activity test in the same manner as in Reference Example 1. These results are shown in Table 1.

Example 2 (Regeneration of catalyst and evaluation of regenerated catalyst)
In Example 1, the same operation as in Example 1 was performed, except that the mixture before drying at 110 ° C. was stirred and heat-treated in a sealed container at 120 ° C. for 5 hours. Table 1 shows the results of XRD measurement, BET specific surface area measurement, and activity test.

Comparative Example 1
In Example 1, the same operation as in Example 1 was performed, except that the molded body was not exposed to an atmosphere of 90% relative humidity at a temperature of 90 ° C. for 3 hours. Table 1 shows the results of XRD measurement, BET specific surface area measurement, and activity test.

In contrast to the new catalyst of Reference Example 1, the deteriorated catalyst of Reference Example 2 had an increase in molybdenum trioxide, a catalytic decomposition product, and a decrease in specific surface area, and the conversion rate was significantly reduced. With respect to such a deteriorated catalyst, the regenerated catalyst of Example 1 in which the molded body was treated at 90 ° C. for 3 hours in an atmosphere with a relative humidity of 30%, the molybdenum trioxide strength ratio and the conversion rate were well recovered. It was. Furthermore, in the regenerated catalyst of Example 2 in which the mixture before drying was heat-treated at 120 ° C. for 5 hours, the molybdenum trioxide strength ratio and the conversion rate recovered well, and in addition, the conversion rate after forced deterioration The catalyst activity was also excellent in sustainability. On the other hand, in the catalyst of Comparative Example 1 in which the treatment for the molded body and the heat treatment for the mixture before drying were not performed, a large amount of molybdenum trioxide remained, the conversion rate after forced deterioration was low, and the sustainability of the catalyst activity. Was not fully recovered.

Claims (4)

  1.   A method for regenerating a catalyst for methacrylic acid production comprising a heteropolyacid compound containing phosphorus and molybdenum, comprising drying a mixture containing a deteriorated catalyst, an ammonium root, a nitrate radical and water, and then molding the resulting molded article. A method for regenerating a catalyst for methacrylic acid production, comprising exposing to an atmosphere of 10 to 60% relative humidity at -100 ° C for 0.5 to 10 hours, and then firing.
  2.   The regeneration method according to claim 1, wherein the mixture is heat-treated at 100 ° C. or more for 2 hours or more and then dried.
  3.   The heteropolyacid compound contains vanadium, an element selected from potassium, rubidium, cesium and thallium, and an element selected from copper, arsenic, antimony, boron, silver, bismuth, iron, cobalt, lanthanum and cerium. Also, the reproducing method according to 2.
  4. A catalyst for producing methacrylic acid is regenerated by the method according to any one of claims 1 to 3, and a compound selected from methacrolein, isobutyraldehyde, isobutane and isobutyric acid is reacted in a gas phase catalytic oxidation reaction in the presence of the regenerated catalyst. The manufacturing method of methacrylic acid attached | subjected to.


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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102010010588A1 (en) 2009-03-09 2010-11-18 Sumitomo Chemical Co. Ltd. Process for the regeneration of a catalyst for the production of methacrylic acid and process for the preparation of methacrylic acid
DE102010010587A1 (en) 2009-03-09 2010-11-18 Sumitomo Chemical Co. Ltd. Reproduction of catalyst for methacrylic acid production consists of heteropolyacid compound involves preparing aqueous slurry, drying to obtain solid heteropolyacid compound, preparing another aqueous slurry, drying and baking
JP2011167678A (en) * 2010-01-19 2011-09-01 Sumitomo Chemical Co Ltd Method for regenerating catalyst for producing methacrylic acid, and method for producing methacrylic acid
DE102012012317A1 (en) 2011-06-22 2012-12-27 Sumitomo Chemical Co., Ltd. Regenerating catalyst useful for preparing methacrylic acid, comprises obtaining first aqueous slurry and second aqueous slurry, and mixing aqueous slurries with each other to obtain third aqueous slurry, and drying and calcining it

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61283352A (en) * 1985-06-05 1986-12-13 Mitsubishi Rayon Co Ltd Preparation of oxidizing catalyst
JPS63130144A (en) * 1986-11-20 1988-06-02 Mitsubishi Rayon Co Ltd Regeneration of oxidizing catalyst
JP2001286763A (en) * 2000-04-06 2001-10-16 Nippon Shokubai Co Ltd Regeneration method of heteropoly acid based catalyst and production method of methacrylic acid

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61283352A (en) * 1985-06-05 1986-12-13 Mitsubishi Rayon Co Ltd Preparation of oxidizing catalyst
JPS63130144A (en) * 1986-11-20 1988-06-02 Mitsubishi Rayon Co Ltd Regeneration of oxidizing catalyst
JP2001286763A (en) * 2000-04-06 2001-10-16 Nippon Shokubai Co Ltd Regeneration method of heteropoly acid based catalyst and production method of methacrylic acid

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102010010588A1 (en) 2009-03-09 2010-11-18 Sumitomo Chemical Co. Ltd. Process for the regeneration of a catalyst for the production of methacrylic acid and process for the preparation of methacrylic acid
DE102010010587A1 (en) 2009-03-09 2010-11-18 Sumitomo Chemical Co. Ltd. Reproduction of catalyst for methacrylic acid production consists of heteropolyacid compound involves preparing aqueous slurry, drying to obtain solid heteropolyacid compound, preparing another aqueous slurry, drying and baking
JP2011167678A (en) * 2010-01-19 2011-09-01 Sumitomo Chemical Co Ltd Method for regenerating catalyst for producing methacrylic acid, and method for producing methacrylic acid
DE102012012317A1 (en) 2011-06-22 2012-12-27 Sumitomo Chemical Co., Ltd. Regenerating catalyst useful for preparing methacrylic acid, comprises obtaining first aqueous slurry and second aqueous slurry, and mixing aqueous slurries with each other to obtain third aqueous slurry, and drying and calcining it

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