JP2013173088A - Catalyst for manufacturing unsaturated carboxylic acids and method for manufacturing unsaturated carboxylic acid using the catalyst - Google Patents
Catalyst for manufacturing unsaturated carboxylic acids and method for manufacturing unsaturated carboxylic acid using the catalyst Download PDFInfo
- Publication number
- JP2013173088A JP2013173088A JP2012038295A JP2012038295A JP2013173088A JP 2013173088 A JP2013173088 A JP 2013173088A JP 2012038295 A JP2012038295 A JP 2012038295A JP 2012038295 A JP2012038295 A JP 2012038295A JP 2013173088 A JP2013173088 A JP 2013173088A
- Authority
- JP
- Japan
- Prior art keywords
- catalyst
- unsaturated carboxylic
- carboxylic acid
- acid
- solid
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Abstract
Description
本発明はラクトンを開環化し異性化する反応に用いる触媒及びその方法に関する発明である。 The present invention relates to a catalyst used in a reaction for ring-opening and isomerizing a lactone and a method thereof.
従来から不飽和カルボン酸を合成する技術は多く提案されている。一般的な方法はプロピレンなどの不飽和炭化水素を酸化しアクリル酸などの不飽和カルボン酸を得る方法であり、この方法には不飽和炭化水素から直接不飽和カルボン酸を得る直接酸化法と、不飽和炭化水素を不飽和アルデヒドに酸化し更に不飽和カルボン酸に酸化する二段法があり、これらの反応は特に文献を挙げるまでもない一般的な技術である。また、不飽和アルデヒドを酸化する方法として気相で反応する気相反応法、液相で反応する液相法（特許文献１）がある。 Many techniques for synthesizing unsaturated carboxylic acids have been proposed. A general method is a method of oxidizing an unsaturated hydrocarbon such as propylene to obtain an unsaturated carboxylic acid such as acrylic acid, which includes a direct oxidation method for directly obtaining an unsaturated carboxylic acid from an unsaturated hydrocarbon, There is a two-stage method in which an unsaturated hydrocarbon is oxidized to an unsaturated aldehyde and then further oxidized to an unsaturated carboxylic acid, and these reactions are general techniques that need not be specifically cited. As a method for oxidizing unsaturated aldehydes, there are a gas phase reaction method for reacting in the gas phase and a liquid phase method for reacting in the liquid phase (Patent Document 1).
また、近年グリセリンを脱水し不飽和アルデヒドとした後、不飽和カルボン酸を得る方法が提案されている（特許文献２）。 In recent years, a method for obtaining an unsaturated carboxylic acid after dehydrating glycerin to obtain an unsaturated aldehyde has been proposed (Patent Document 2).
古くは、ラクトンをアルコールからアクリル酸エステルとアクリル酸を製造する方法が提案されているが（特許文献３）、アクリル酸とアクリル酸エステルを同時に製造するものでありアクリル酸を製造する方法として選択率が低くならざるをえないものであり、目的とする反応自体が異なるものである。 In the old days, a method for producing acrylate and acrylic acid from alcohol was proposed (Patent Document 3). However, acrylic acid and acrylate are produced at the same time and are selected as a method for producing acrylic acid. The rate must be low, and the target reaction itself is different.
上記、公知技術の多くはアルデヒドを酸化しカルボン酸を得る方法であり、カルボン酸を得るに際して製造方法の工程が一本化している。しかし、アルデヒドを原料として用いることができなくなったとき、不飽和カルボン酸は化学製造工程において多く製品の原料となるため化学産業に大きな影響を及ぼすものである。 Many of the above known techniques are methods for obtaining carboxylic acids by oxidizing aldehydes, and the steps of the production method are unified when obtaining carboxylic acids. However, when aldehydes can no longer be used as raw materials, unsaturated carboxylic acids have a great influence on the chemical industry because they become a raw material for many products in the chemical production process.
本発明者らは上記課題を解決するために鋭意検討の結果、下記技術を見出し、発明を完成するに至ったものである。以下に本発明を説明するが本発明の趣旨に反しない限り以下の記載に限定されるものではない。 As a result of intensive studies to solve the above problems, the present inventors have found the following technique and have completed the invention. The present invention will be described below, but the present invention is not limited to the following description unless it is contrary to the gist of the present invention.
本発明は、ラクトンを開環し異性化し不飽和カルボン酸を得る触媒であって、当該触媒が固体酸であることを特徴とする不飽和カルボン酸製造用触媒である。更に、当該触媒の存在下にラクトンを開環異性化し不飽和カルボン酸を得ることを特徴とする不飽和カルボン酸製造方法である。 The present invention is a catalyst for producing an unsaturated carboxylic acid, wherein the lactone is ring-opened and isomerized to obtain an unsaturated carboxylic acid, which is a solid acid. Furthermore, the present invention provides an unsaturated carboxylic acid production method characterized in that an unsaturated carboxylic acid is obtained by ring-opening isomerization of a lactone in the presence of the catalyst.
本発明は不飽和カルボン酸の製造方法に関して新たな工程を提案するものである。 The present invention proposes a new process for the production method of unsaturated carboxylic acid.
本発明は、ラクトンを開環し異性化し不飽和カルボン酸を得る触媒であって、当該触媒が固体酸であることを特徴とする不飽和カルボン酸製造用触媒である。好ましくは、当該固体酸が、固体リン酸、固体超強酸、ゼオライト、ヘテロポリ酸、層状ケイ酸塩、粘土鉱物及び固体化スルフォン酸からなる群から選ばれる少なくとも一種であり、当該触媒形状がハニカム、ペレット、サドル状等のものを用いることができる。 The present invention is a catalyst for producing an unsaturated carboxylic acid, wherein the lactone is ring-opened and isomerized to obtain an unsaturated carboxylic acid, which is a solid acid. Preferably, the solid acid is at least one selected from the group consisting of solid phosphoric acid, solid superacid, zeolite, heteropoly acid, layered silicate, clay mineral, and solidified sulfonic acid, and the catalyst shape is a honeycomb, Pellets and saddles can be used.
更に、当該触媒の存在下に、ラクトンを開環異性化し不飽和カルボン酸を得ることを特徴とする不飽和カルボン酸製造方法である。 Furthermore, the present invention provides an unsaturated carboxylic acid production method characterized in that an unsaturated carboxylic acid is obtained by ring-opening isomerization of a lactone in the presence of the catalyst.
（不飽和カルボン酸製造用触媒）
本発明にかかる触媒は、固体酸であり、好ましくは固体リン酸、固体超強酸、ゼオライト、ヘテロポリ酸、層状ケイ酸塩、粘土鉱物及び固体化スルフォン酸からなる群から選ばれる少なくとも一種である。具体的には、固体リン酸としては、ＡｌＰＯ４、ＢＰＯ４、Ｃａ１０（ＰＯ４）６（ＯＨ）２などが挙げられる。固体超強酸としては、ＳＯ４／ＺｒＯ２、ＳＯ４・ＳｎＯ２などの硫酸化金属酸化物、ＷＯ３−ＺｒＯ２，ＭｏＯ３−ＺｒＯ２などの金属酸化物超強酸などが挙げられる。ゼオライトとしては、Ａ型、ＺＳＭ−５、ベータ、モルデナイトなどのケイ酸塩系、ＡｌＰＯ−５や１１などのリン酸塩系などが挙げられる。層状ケイ酸塩としては、モンモリロナイト、ハイドロタルサイトなどが挙げられる。固定化スルフォン酸としては、ポリスチレン架橋スルフォン酸、ペルフルオロスルフォン酸などが挙げられる。
(Catalyst for unsaturated carboxylic acid production)
The catalyst according to the present invention is a solid acid, preferably at least one selected from the group consisting of solid phosphoric acid, solid superacid, zeolite, heteropolyacid, layered silicate, clay mineral, and solidified sulfonic acid. Specifically, examples of solid phosphoric acid include AlPO 4 , BPO 4 , and Ca 10 (PO 4 ) 6 (OH) 2 . Examples of the solid superacid, SO 4 / ZrO 2, SO 4 · SnO 2 sulfated metal oxides such as, WO 3 -ZrO 2, MoO 3 metal oxides such -ZrO 2 such superacid and the like. Examples of zeolite include silicates such as A-type, ZSM-5, beta, and mordenite, and phosphates such as AlPO-5 and 11. Examples of the layered silicate include montmorillonite and hydrotalcite. Examples of the immobilized sulfonic acid include polystyrene-crosslinked sulfonic acid and perfluorosulfonic acid.
当該固体酸は単独で使用することもできるが混合することもできる。また多孔質の担体に担持し使用することもできる。 The solid acid can be used alone or in combination. It can also be used by being supported on a porous carrier.
当該触媒形状が顆粒状、球形粒子、円柱状、リング状、ホイール状、ハニカム、ペレット、サドル状である。 The catalyst shape is granular, spherical particle, columnar, ring, wheel, honeycomb, pellet or saddle.
当該触媒の相当直径が１〜１００ｍｍ、長さが１〜１００ｍｍであり、好ましくは相当直径が２〜５０ｍｍである。長さは好ましくは２〜５０ｍｍである。 The catalyst has an equivalent diameter of 1 to 100 mm and a length of 1 to 100 mm, preferably an equivalent diameter of 2 to 50 mm. The length is preferably 2 to 50 mm.
当該触媒の比表面積が０．１〜１，０００ｍ２／ｇ、好ましくは１０〜５００ｍ２／ｇである。当該比表面積の測定方法はＮ２によるＢＥＴ法により測定されるものである。 The specific surface area of the catalyst is 0.1 to 1,000 m 2 / g, preferably 10 to 500 m 2 / g. The specific surface area is measured by the BET method using N 2 .
また当該触媒の平均細孔径は０．１ｎｍ〜５００μｍである。 The average pore diameter of the catalyst is 0.1 nm to 500 μm.
なお、当該細孔容積及び平均細孔径の測定は水銀圧入法により測定されるものである。 The pore volume and average pore diameter are measured by mercury porosimetry.
（触媒の調製方法）
本発明の市販の固体酸を用いることができるが、好ましくは上記範囲内の物性を有する固体酸を調製するものである。また、触媒の形状は、錠剤成形機、押出成形機などにより成形することができる。
(Method for preparing catalyst)
Although the commercially available solid acid of this invention can be used, Preferably the solid acid which has a physical property within the said range is prepared. The shape of the catalyst can be formed by a tablet molding machine, an extrusion molding machine or the like.
（反応条件）
本発明にかかる反応は、ラクトンを開環異性化し不飽和カルボン酸を得ることを特徴とする不飽和カルボン酸製造方法である。
(Reaction conditions)
The reaction according to the present invention is a method for producing an unsaturated carboxylic acid, wherein the lactone is subjected to ring-opening isomerization to obtain an unsaturated carboxylic acid.
反応ガスはラクトンを含むものである。ラクトンとしては、α−アセトラクトン、β−プロピオラクトン、γ−ブチロラクトン若しくはδ−バレロラクトン又はこれらの誘導体であり、好ましくはβ−プロピオラクトンである。 The reaction gas contains lactone. The lactone is α-acetolactone, β-propiolactone, γ-butyrolactone, δ-valerolactone or a derivative thereof, preferably β-propiolactone.
不飽和カルボン酸は上記ラクトン個々を開環異性化し、得られる不飽和カルボン酸である。例えば、β−プロピオラクトンを開環異性化したアクリル酸である。 The unsaturated carboxylic acid is an unsaturated carboxylic acid obtained by ring-opening isomerization of each of the above lactones. For example, acrylic acid obtained by ring-opening isomerization of β-propiolactone.
反応ガスにおけるラクトン以外のガスは反応に不活性なガスを併用することができ、例えば、窒素、あるいは、アルゴンなどの希ガス類元素であり、この場合ラクトンの濃度は１〜５０容量％、好ましくは５〜３０容量％である。 A gas other than the lactone in the reaction gas can be used in combination with an inert gas. For example, nitrogen or a rare gas element such as argon. In this case, the concentration of the lactone is 1 to 50% by volume, preferably 5%. ~ 30% by volume.
反応時の空間速度は、当該不飽和カルボン酸製造方法における空間速度が１，０００〜１００，０００ｈｒ−１であり、好ましくは空間速度が５，０００〜５０，０００ｈｒ−１である。 Space velocity during the reaction, the space velocity in the unsaturated carboxylic acid production process is 1,000～100,000Hr -1, preferably space velocity 5,000~50,000hr -1.
反応温度は、１００〜３５０℃であり、好ましくは１５０〜２５０℃である。 The reaction temperature is 100 to 350 ° C, preferably 150 to 250 ° C.
上記要件を満たす触媒であれは何れのものであっても良いが、説明を簡潔なものとするため、代表例として以下の実施例を用いて発明を詳細に説明するが本発明の効果を奏するものであれば以下の実施例に限定されるものではない。 Any catalyst may be used as long as it satisfies the above requirements. However, in order to simplify the description, the present invention will be described in detail using the following examples as representative examples, but the effects of the present invention are achieved. As long as it is a thing, it is not limited to a following example.
（実施例１）
固体超強酸として、ＷＯ３−ＺｒＯ２反応管に設置し、反応ガスとして、プロピオラクトン２０容量％、窒素を８０容量％含む反応ガスを、当該反応管に導入し、反応温度を２００℃にして反応した。その結果は収率９０％でアクリル酸を得た。上記結果から本発明にかかる触媒の有効性が分かるものである。
Example 1
As a solid super strong acid, installed in a WO 3 -ZrO 2 reaction tube, as a reaction gas, a reaction gas containing 20% by volume of propiolactone and 80% by volume of nitrogen is introduced into the reaction tube, and the reaction temperature is set to 200 ° C. Reacted. As a result, acrylic acid was obtained with a yield of 90%. From the above results, the effectiveness of the catalyst according to the present invention can be understood.
本発明は不飽和カルボン酸製造技術に関するものであり、特に新規なアクリル酸製造分野に展開することができるものである。 The present invention relates to an unsaturated carboxylic acid production technique, and can be developed particularly in the novel acrylic acid production field.
Claims (4)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2012038295A JP5818716B2 (en) | 2012-02-24 | 2012-02-24 | Catalyst for producing unsaturated carboxylic acids and method for producing unsaturated carboxylic acid using the catalyst |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2012038295A JP5818716B2 (en) | 2012-02-24 | 2012-02-24 | Catalyst for producing unsaturated carboxylic acids and method for producing unsaturated carboxylic acid using the catalyst |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JP2013173088A true JP2013173088A (en) | 2013-09-05 |
| JP5818716B2 JP5818716B2 (en) | 2015-11-18 |
Family
ID=49266546
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2012038295A Expired - Fee Related JP5818716B2 (en) | 2012-02-24 | 2012-02-24 | Catalyst for producing unsaturated carboxylic acids and method for producing unsaturated carboxylic acid using the catalyst |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP5818716B2 (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2017165344A1 (en) | 2016-03-21 | 2017-09-28 | Novomer, Inc. | Acrylic acid, and methods of producing thereof |
| US20180305286A1 (en) * | 2016-03-21 | 2018-10-25 | Novomer, Inc. | Systems and Processes for Producing Organic Acids Direct from Beta-Lactones |
| JP2020183353A (en) * | 2019-05-07 | 2020-11-12 | 旭化成株式会社 | Method for producing hydroxy acid |
| JP2021528478A (en) * | 2018-06-29 | 2021-10-21 | ノボマー， インコーポレイテッド | Systems and processes for producing organic acids directly from beta-lactone |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106205758B (en) * | 2016-07-19 | 2018-03-20 | 上海交通大学 | The preparation method of firming body based on the silicon substrate heteropoly acid salt compound adsorbent after absorption caesium |
-
2012
- 2012-02-24 JP JP2012038295A patent/JP5818716B2/en not_active Expired - Fee Related
Cited By (18)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP3433226A4 (en) * | 2016-03-21 | 2019-11-06 | Novomer, Inc. | Improved acrylic acid production process |
| US20180305286A1 (en) * | 2016-03-21 | 2018-10-25 | Novomer, Inc. | Systems and Processes for Producing Organic Acids Direct from Beta-Lactones |
| US10662139B2 (en) | 2016-03-21 | 2020-05-26 | Novomer, Inc. | Acrylic acid production process |
| WO2017165344A1 (en) | 2016-03-21 | 2017-09-28 | Novomer, Inc. | Acrylic acid, and methods of producing thereof |
| CN109153628A (en) * | 2016-03-21 | 2019-01-04 | 诺沃梅尔公司 | improved acrylic acid manufacturing process |
| JP2019509307A (en) * | 2016-03-21 | 2019-04-04 | ノボマー， インコーポレイテッド | Acrylic acid and method for producing the same |
| JP2019512527A (en) * | 2016-03-21 | 2019-05-16 | ノボマー， インコーポレイテッド | Improved acrylic acid production process |
| EP3433222A4 (en) * | 2016-03-21 | 2019-11-06 | Novomer, Inc. | Acrylic acid, and methods of producing thereof |
| US11827590B2 (en) * | 2016-03-21 | 2023-11-28 | Novomer, Inc. | Acrylic acid, and methods of producing thereof |
| WO2017165323A1 (en) | 2016-03-21 | 2017-09-28 | Novomer, Inc. | Improved acrylic acid production process |
| CN108884000A (en) * | 2016-03-21 | 2018-11-23 | 诺沃梅尔公司 | acrylic acid and its manufacturing method |
| US20210139402A1 (en) * | 2016-03-21 | 2021-05-13 | Novomer, Inc. | Acrylic acid, and methods of producing thereof |
| CN114736111A (en) * | 2016-03-21 | 2022-07-12 | 诺沃梅尔公司 | Improved acrylic acid manufacturing process |
| JP6997459B2 (en) | 2016-03-21 | 2022-02-04 | ノボマー， インコーポレイテッド | Improved acrylic acid manufacturing process |
| CN109153628B (en) * | 2016-03-21 | 2022-04-26 | 诺沃梅尔公司 | Improved acrylic acid manufacturing process |
| JP2021528478A (en) * | 2018-06-29 | 2021-10-21 | ノボマー， インコーポレイテッド | Systems and processes for producing organic acids directly from beta-lactone |
| JP7113784B2 (en) | 2019-05-07 | 2022-08-05 | 旭化成株式会社 | A method for producing a hydroxy acid. |
| JP2020183353A (en) * | 2019-05-07 | 2020-11-12 | 旭化成株式会社 | Method for producing hydroxy acid |
Also Published As
| Publication number | Publication date |
|---|---|
| JP5818716B2 (en) | 2015-11-18 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JP5818716B2 (en) | Catalyst for producing unsaturated carboxylic acids and method for producing unsaturated carboxylic acid using the catalyst | |
| JP5970542B2 (en) | Process for producing molded catalyst and process for producing diene or unsaturated aldehyde and / or unsaturated carboxylic acid using the molded catalyst | |
| JP5993084B2 (en) | Catalytic conversion of lactic acid to acrylic acid | |
| Rubio-Caballero et al. | Acetalization of furfural with zeolites under benign reaction conditions | |
| Rao et al. | Selective conversion of furfuryl alcohol into butyl levulinate over zinc exchanged heteropoly tungstate supported on niobia catalysts | |
| Kassaee et al. | Nano TiO2 as a heterogeneous catalyst in an efficient one-pot three-component Mannich synthesis of β-aminocarbonyls | |
| TW201247318A (en) | Catalyst for producing acrylic acids and acrylates | |
| PT2265565E (en) | Process for manufacturing acrolein or acrylic acid from glycerin | |
| JP5914655B2 (en) | Improved dehydration method | |
| US20100016644A1 (en) | Maleic anhydride catalyst and method for its preparation | |
| IN2014DN10247A (en) | ||
| JPWO2015008815A1 (en) | Process for producing unsaturated aldehyde and / or unsaturated carboxylic acid | |
| SG142248A1 (en) | Method for regenerating catalyst for the production of methacrylic acid and process for preparing methacrylic acid | |
| RU2016114683A (en) | CATALYST FOR SYNTHESIS OF UNSATURATED CARBONIC ACID BY GAS-PHASE OXIDATION OF UNSATURATED ALDEHYDE | |
| CN103191782A (en) | Supported solid acid catalyst, and method for preparing ester perfumes through applying it | |
| KR20190078594A (en) | How to make dienes | |
| SG156571A1 (en) | Method for regenerating catalyst for the production of methacrylic acid and process for preparing methacrylic acid | |
| US20070173653A1 (en) | Method of performing sugar dehydration and catalyst treatment | |
| WO2014175113A1 (en) | Catalyst for producing unsaturated aldehyde and/or unsaturated carboxylic acid, method for producing catalyst, and method for producing unsaturated aldehyde and/or unsaturated carboxylic acid using catalyst | |
| CN102267882B (en) | Method for preparing acrolein by catalyzing dehydration of glycerol with immobilized acidic ionic liquid | |
| CA1042449A (en) | Method for preparing a catalyst | |
| US20120022291A1 (en) | Catalyst for production of acrolein and acrylic acid by means of dehydration reaction of glycerin, and process for producing same | |
| CN102952014B (en) | A kind of method preparing ethylene glycol monomethyl ether acetate | |
| Nishimura et al. | Selective oxidation of biomass-derived alcohols with supported metal catalysts | |
| CN101862678A (en) | Method for preparing tungstosilicic acid-supported catalyst for use in preparation of menthyl lactate |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| A621 | Written request for application examination |
Free format text: JAPANESE INTERMEDIATE CODE: A621 Effective date: 20141006 |
|
| A977 | Report on retrieval |
Free format text: JAPANESE INTERMEDIATE CODE: A971007 Effective date: 20150409 |
|
| A131 | Notification of reasons for refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A131 Effective date: 20150507 |
|
| A521 | Request for written amendment filed |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20150605 |
|
| TRDD | Decision of grant or rejection written | ||
| A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 Effective date: 20150908 |
|
| A61 | First payment of annual fees (during grant procedure) |
Free format text: JAPANESE INTERMEDIATE CODE: A61 Effective date: 20150929 |
|
| R150 | Certificate of patent or registration of utility model |
Ref document number: 5818716 Country of ref document: JP Free format text: JAPANESE INTERMEDIATE CODE: R150 |
|
| LAPS | Cancellation because of no payment of annual fees |