JPH0575461B2 - - Google Patents

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Publication number
JPH0575461B2
JPH0575461B2 JP58078812A JP7881283A JPH0575461B2 JP H0575461 B2 JPH0575461 B2 JP H0575461B2 JP 58078812 A JP58078812 A JP 58078812A JP 7881283 A JP7881283 A JP 7881283A JP H0575461 B2 JPH0575461 B2 JP H0575461B2
Authority
JP
Japan
Prior art keywords
platinum
group
compound
hydrogen
tin
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.)
Expired - Lifetime
Application number
JP58078812A
Other languages
Japanese (ja)
Other versions
JPS59203640A (en
Inventor
Kazuo Tano
Keiichi Sato
Tooru Oogoshi
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Chemical Corp
Original Assignee
Mitsubishi Chemical Industries Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Mitsubishi Chemical Industries Ltd filed Critical Mitsubishi Chemical Industries Ltd
Priority to JP58078812A priority Critical patent/JPS59203640A/en
Publication of JPS59203640A publication Critical patent/JPS59203640A/en
Publication of JPH0575461B2 publication Critical patent/JPH0575461B2/ja
Granted legal-status Critical Current

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Classifications

    • 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
    • Y02P20/52Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts

Landscapes

  • Catalysts (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Description

【発明の詳现な説明】[Detailed description of the invention]

本発明は癜金−錫觊媒の補造法に関するもので
ある。 ヒドロホルミル化反応によるアルデヒド補造甚
癜金−錫觊媒は、皮々の有機化孊反応の觊媒ずし
お䜿甚するこずが可胜であり、特にヒドロホルミ
ル化反応の觊媒ずしお、良奜な觊媒掻性および工
業的䟡倀の高い盎鎖アルデヒドぞの高遞択性など
の優れた性質を有しおいる。 癜金−錫觊媒の調補法ずしお、埓来、癜金化合
物、配䜍子化合物および錫化合物をヒドロホルミ
ル化反応の反応系に䟛絊し、該反応系内で反応掻
性な癜金−錫觊媒を圢成させる手法が知られおい
る。しかしながら、該手法においおは掻性皮が圢
成されるたでに反応誘導期が生じる。そのため、
あらかじめ反応掻性な癜金−錫觊媒を調補しおお
くこずが望たれおいる。 氎玠ず䞀酞化炭玠ずの混合ガスの存圚䞋に癜金
−錫錯䜓を調補する方法ずしお、trans−PtHCl
〔C6H53〕2ずSnCl2・2H2ずから錯䜓、PtH
SnCl3CO〔C6H53〕2を調補するこずは
知られおいる。〔J.Amer.Chem.Soc.973553
1975〕しかしながら、氎玠たたは氎玠ず䞀酞化
炭玠ずの混合ガスの存圚䞋に、癜金化合物、配䜍
子化合物及び錫化合物を反応させるず、しばしば
癜金のメタルが析出しお癜金−錫錯䜓が圢成され
るのに至らず、高䟡な癜金が有効に䜿甚されない
こずがある。 本発明者らは、䞊蚘実情に鑑み、鋭意怜蚎を重
ねた結果、䞊蚘の反応に際しおハロゲン化氎玠を
共存させるこずにより、癜金のメタルの析出なし
に癜金−錫觊媒が調補され、か぀、これをヒドロ
ホルミル化反応に甚いた堎合、高掻性であり、た
た実質的に誘導期が解消されるこずを認めお本発
明を完成した。 即ち、本発明は優れたヒドロホルミル化反応に
よるアルデヒド補造甚癜金−錫觊媒を工業的に有
利に補造する方法を提䟛するこずを目的ずし、癜
金化合物、呚期埋衚の第5B族元玠を含む配䜍子
化合物、錫化合物およびハロゲン化氎玠を、溶媒
䞭で、氎玠たたは氎玠ず䞀酞化炭玠ずの混合ガス
の存圚䞋に、反応させるこずを特城ずするヒドロ
ホルミル化反応によるアルデヒド補造甚癜金−錫
觊媒の補造法、を芁旚ずするものである。 以䞋に本発明に぀きより詳现に説明する。なお
本明现曞䞭においお「呚期埋衚」ずは、特に断わ
らない限り、IUPAC Comptes Rendus
Conferencep.1831965に蚘茉された元玠の呚
期埋衚を指すものずする。 癜金化合物ずしおは、䟡、䟡たたは䟡の
癜金化合物を䜿甚するこずができるが、本発明で
はハロゲン化氎玠を䜿甚するため、その䜿甚量を
䜎枛化するには、ハロゲンを含有する䟡たたは
䟡の癜金化合物を䜿甚するこずが奜たしい。本
発明においおは癜金化合物に加えお呚期埋衚の第
5B族元玠を含む配䜍子化合物を䜵甚するが、こ
のこずによ぀お錯䜓の安定性、及び觊媒反応に䟛
する堎合の掻性が向䞊する。これらの化合物は
別々に反応系に仕蟌むこずもできるが、第5B族
元玠を含む配䜍子化合物を配䜍子ずする癜金錯䜓
を予め調補したうえで反応系に仕蟌むこずもでき
る。 本発明で䜿甚し埗る癜金化合物ずしおは、䟋え
ば二塩化癜金、四塩化癜金等のハロゲン化癜金、
ヘキサクロロ癜金酞、ヘキサクロロ癜金酞ナトリ
りム、ヘキサクロロ癜金酞カリりム、ヘキサブロ
モ癜金酞カリりム、テトラクロロ癜金酞、テトラ
クロロ癜金酞カリりム等のハロゲノ癜金酞および
その塩、ゞクロロ−シクロオクタゞ゚
ン癜金、ゞクロロビスベンゟニトリル
癜金、ゞクロロビスアセトニトリル癜
金、ゞクロロビスピリゞン癜金、
ゞクロロビストリプニルホスフむン癜金
、ゞクロロビストリブチルホスフむン癜
金、ゞクロロ〔−−む゜プロピリ
デン−−ゞヒドロキシ−−ビスゞ
プニルホスフむノブタン〕癜金
The present invention relates to a method for producing a platinum-tin catalyst. Platinum-tin catalysts for the production of aldehydes by hydroformylation reactions can be used as catalysts for various organic chemical reactions, and are particularly useful as catalysts for hydroformylation reactions to produce linear aldehydes with good catalytic activity and high industrial value. It has excellent properties such as high selectivity to Conventionally, as a method for preparing a platinum-tin catalyst, a method has been known in which a platinum compound, a ligand compound, and a tin compound are supplied to a reaction system for a hydroformylation reaction, and a reactive platinum-tin catalyst is formed in the reaction system. It is being However, in this method, a reaction induction period occurs before active species are formed. Therefore,
It is desirable to prepare a reactive platinum-tin catalyst in advance. As a method for preparing platinum-tin complex in the presence of a mixed gas of hydrogen and carbon monoxide, trans-PtHCl
[P(C 6 H 5 ) 3 ] 2 and SnCl 2 2H 2 O complex, PtH
It is known to prepare ( SnCl3 ) (CO)[P( C6H5 ) 3 ] 2 . [J.Amer.Chem.Soc.97, 3553
(1975)] However, when platinum compounds, ligand compounds, and tin compounds are reacted in the presence of hydrogen or a mixed gas of hydrogen and carbon monoxide, platinum metal often precipitates and a platinum-tin complex is formed. The expensive platinum may not be used effectively. In view of the above circumstances, the present inventors have made extensive studies and found that by coexisting hydrogen halide during the above reaction, a platinum-tin catalyst can be prepared without precipitation of platinum metal, and The present invention was completed based on the recognition that when used in a hydroformylation reaction, it has high activity and substantially eliminates the induction period. That is, the present invention aims to provide an industrially advantageous method for producing a platinum-tin catalyst for aldehyde production by an excellent hydroformylation reaction, and aims to provide a method for industrially advantageously producing a platinum-tin catalyst for producing aldehydes by an excellent hydroformylation reaction. A platinum-tin catalyst for producing aldehydes by a hydroformylation reaction, which is characterized in that a child compound, a tin compound, and a hydrogen halide are reacted in the presence of hydrogen or a mixed gas of hydrogen and carbon monoxide in a solvent. The gist is the manufacturing method. The present invention will be explained in more detail below. In this specification, "periodic table" means IUPAC Comptes Rendus unless otherwise specified.
Refers to the Periodic Table of Elements as listed in Conference, p. 183 (1965). As the platinum compound, a zero-valent, divalent or tetravalent platinum compound can be used, but since hydrogen halide is used in the present invention, in order to reduce the amount of hydrogen halide used, it is necessary to use a halogen-containing platinum compound. Preference is given to using valent or tetravalent platinum compounds. In the present invention, in addition to platinum compounds,
A ligand compound containing a group 5B element is used in combination, which improves the stability of the complex and the activity when subjected to a catalytic reaction. These compounds can be charged separately into the reaction system, but a platinum complex having a ligand compound containing a Group 5B element as a ligand can also be prepared in advance and then charged into the reaction system. Examples of platinum compounds that can be used in the present invention include platinum halides such as platinum dichloride and platinum tetrachloride;
Halogenoplatinic acids and their salts such as hexachloroplatinic acid, sodium hexachloroplatinate, potassium hexachloroplatinate, potassium hexabromoplatinate, tetrachloroplatinic acid, potassium tetrachloroplatinate, dichloro(1,5-cyclooctadiene)platinum ( ), dichlorobis(benzonitrile)
Platinum (), dichlorobis(acetonitrile) platinum (), dichlorobis(pyridine) platinum (),
Dichlorobis(triphenylphosphine)platinum(), dichlorobis(tributylphosphine)platinum(), dichloro[2,3-o-isopropylidene-2,3-dihydroxy-1,4-bis(diphenylphosphine)butane 〕platinum()

【化】 ゞクロロ〔−ビスゞプニルホスフむノ
メチルシクロブタン〕癜金
[Chemical] Dichloro[1,2-bis(diphenylphosphinomethyl)cyclobutane]platinum ()

【匏】以䞋、PtCl2 DPCBず蚘す。などの癜金錯䜓が挙げられ
る。 呚期埋衚の第5B族元玠を含む配䜍子化合物ず
しおは、䞀般匏AR4R5R6 匏䞭、はリン、ヒ玠、アンチモン、ビスマ
スたたは窒玠を衚わし、R4はアルキル基、シク
ロアルキル基、アリヌル基、アラルキル基、アル
コキシ基、アリヌルオキシ基たたは−−A′R5
R6䜆し、は眮換基を有しおいおもよいアルキ
レン基もしくはアリヌレン基たたはアルキレン基
もしくは酞玠原子を介しおたたはA′に結合す
るアルキレン基、シクロアルキレン基、アリヌレ
ン基もしくはビシクロアルキレン基を衚わし、
A′はリン、ヒ玠、アンチモン、ビスマスたたは
窒玠を衚わす。で瀺される基を衚わし、R5およ
びR6はアルキル基、シクロアルキル基、アリヌ
ル基、アラルキル基、アルコキシ基たたはアリヌ
ルオキシ基を衚わす。 で瀺される単座あるいは二座の配䜍子が奜適に䜿
甚される。具䜓的には、単座配䜍子ずしおトリフ
゚ニルホスフむン、トリトリルホスフむン、トリ
スクロロプニルホスフむン、トリスメト
キシプニルホスフむン、ベンゞルゞプニル
ホスフむン、ビス−シアノ゚チルプニル
ホスフむン、トリシクロヘキシルホスフむン、ゞ
゚チルプニルホスフむン、トリ゚チルホスフむ
ン、トリプロピルホスフむン、トリブチルホスフ
むン、トリナフチルホスフむン、トリベンゞルホ
スフむン、ゞプニレンプニルホスフむン等の
第䞉玚ホスフむン、トリ゚チルホスフむツト、ト
リプロピルホスフむツト、トリブチルホスフむツ
ト、トリデシルホスフむツト、トリプニルホス
フむツト、トリスクロロプニルホスフむツ
ト等の第䞉玚ホスフむツト、トリプニルアルシ
ン、トリトリルアルシン、トリ゚チルアルシン等
の第䞉玚アルシン、トリブチルスチビン、トリフ
゚ニルスチビン等の第䞉玚スチビン、トリプニ
ルビスムチン等の第䞉玚ビスムチン、トリブチル
アミン、トリプニルアミン等の第䞉玚アミンが
挙げられ、二座配䜍子ずしお−ビスゞフ
゚ニルホスフむノ゚タン、−ビスゞフ
゚ニルホスフむノプロパン、−ビスゞ
プニルホスフむノブタン、−ビスゞ
プニルホスフむノペンタン、−ゞプニ
ルホスフむノ−−ゞプニルアルシノ゚タ
ン、−ビスゞプニルアルシノ゚タ
ン、−プニレンビスゞメチルアルシン、
−プニレンビスゞプニルホスフむン、
−ビスゞプニルホスフむノメチルベ
ンれン、2′−ビスゞプニルホスフむノメ
チル−1′−ビナフチル、2′−ビスゞ
プニルホスフむノオキシ−1′−ビナフチ
ル、2′−ビスゞプニルホスフむノメチ
ルシクロヘキサン、−ビスゞプニル
ホスフむノメチルシクロブタン、−ビス
ゞプニルアルシノメチルシクロブタン、
−−む゜プロピリデン−−ゞヒドロキ
シ−−ビスゞプニルホスフむノブタ
ン、trane−−ビスゞプニルホスフむ
ノメチルビシクロ〔〕オクタン等が
挙げられる。 これらの配䜍子化合物は、第5B族元玠に換算
しお癜金に察しお〜10倍モルの範囲内で䜿甚さ
れるこずが奜たしい。 錫化合物は無機及び有機の錫化合物から皮々遞
択可胜であるが、奜適には 䞀般匏ArSnR1R2R3 匏䞭Arは眮換基を有しおいおもよいアリヌ
ル基を衚わし、R1R2およびR3は氎玠原子、ヒ
ドロキシ基、アシルオキシ基、ハロゲン原子たた
は眮換基を有しおいおもよいアルキル基、アルケ
ニル基、アリヌル基もしくはアルケニル基を衚わ
す。 で瀺されるアリヌル錫化合物、及び 䞀般匏Sn 匏䞭は酞玠原子たたはアシルオキシ基を、
はたたはである敎数を衚わす。 で瀺されるオキシ錫化合物が䜿甚される。 䞊蚘アリヌル錫化合物ずしおは䟋えばC6H5
SnCl3−CH3・C6H42SnCl2C6H52
SnCl2C6H53SnClC6H53SnBrC6H53
SnIC6F53SnClC6H53SnOCH3C6H53
SnCH3C6H53SnCH2・CH2OHC6H53
SnCH2CHCH2などが挙げられる。 䞊蚘アリヌル錫化合物のうち特に奜適なもの
は、 䞀般匏Ar3SnX 匏䞭Arはアリヌル基を衚わし、は氎玠原
子、ヒドロキシル基たたはアシルオキシ基を衚わ
す。 で瀺されるトリアリヌル錫化合物であり、具䜓的
にはC6H53SnHC6H53SnOHC6H53
SnOCOCH3C6H53SnOCOC6H5などが挙げら
れる。 次に前蚘オキシ錫化合物の具䜓䟋を挙げれば
SnOSnO2SnOCOCH32SnOCOCH34な
どであり、特にSnOCOCH32が奜適である。 これら錫化合物は、癜金に察しお0.5〜倍モ
ルの範囲内で䜿甚されるのが奜たしい。 ハロゲン化氎玠ずしおは、フツ化氎玠、塩化氎
玠、臭化氎玠およびペり化氎玠が䜿甚される。こ
れらの反応系に添加されるに際しおの圢態は特に
制限されるものではなく、気䜓状態あるいは氎溶
液ハロゲン化氎玠酞あるいはメタノヌル、゚
タノヌル、アセトン、ゞオキサンなどの有機溶媒
に溶解させお䜿甚する事も可胜である。溶媒に溶
解させお䜿甚する堎合のハロゲン化氎玠の濃床は
特に限定されず、溶解床の範囲内で任意に調敎さ
れる。たずえば塩酞の堎合、入手容易な垂販品濃
床の35品で充分である。 これらハロゲン化氎玠の䜿甚量は、甚いられる
癜金化合物の圢態などにより倉化し、必ずしも䞀
矩的に決められるものではない。たずえば䟡の
癜金化合物を甚いれば、癜金ぞの酞化的付加によ
りハロゲン化氎玠が消費されるため、ゞハロゲン
化癜金型の化合物よりも、より倚くの䜿甚量が必
芁である。たた倚量に䜿甚すれば、腐食等の問題
が生ずるため、癜金−錫觊媒が圢成される範囲内
で出来るだけ少ない量で䜿甚されるのが奜たし
く、通垞、癜金に察し0.05〜倍モルの範囲で䜿
甚されるのが奜たしい。 本発明方法においおは、溶媒が䜿甚される。溶
媒の具䜓䟋ずしおは、メタノヌル、゚タノヌル、
−プロピルアルコヌル、む゜プロピルアルコヌ
ル、−ブチルアルコヌル、Sec−ブチルアルコ
ヌル、シクロヘキサノヌル等のアルコヌル類、ゞ
゚チル゚ヌテル、ゞオキサン、テトラヒドロフラ
ン等の゚ヌテル類、アセトン、メチル゚チルケト
ン、ゞ゚チルケトン等のケトン類、アセトアミ
ド、プロピオンアミド、−ゞメチルホルム
アミド、−ゞメチルアセトアミド等のアミ
ド類、アセトニトリル、プロピオニトリル、ベン
ゟニトリル等のニトリル類、酢酞゚チル、プロピ
オン酞メチル等の゚ステル類、ゞメチルスルホキ
シド等のスルホキシド類、酢酞等のカルボン酞
類、ピリゞン、メチルピリゞン等のピリゞル類、
アセトアルデヒド、プロピオンアルデヒド等のア
ルデヒド類、ベンれン、トル゚ン、キシレン、デ
カン等の炭化氎玠類、塩化メチレン、四塩化炭
玠、−ゞクロロベンれン等のハロゲン化炭化氎
玠などが挙げられ、これらは単独で、あるいは
皮以䞊の混合物ずしお䜿甚される。特に奜たしい
溶媒は、ベンれン、トル゚ン、アセトン、ゞオキ
サン、テトラヒドロフランなどである。 これらの溶媒の䜿甚量は、癜金化合物、第5B
族元玠を含む配䜍子化合物および錫化合物を溶解
し埗る量以䞊であれば特に限定されるものではな
い。 本発明の実斜にあた぀お、反応枩床は通垞、宀
枩〜200℃、奜たしくは50〜150℃の範囲内で遞択
され、氎玠たたは氎玠ず䞀酞化炭玠ずの混合ガス
の圧力は、反応枩床にもよるが通垞、垞圧〜300
気圧、奜たしくは〜200気圧の範囲内で遞択さ
れる。氎玠ず䞀酞化炭玠ずの混合ガスのH2CO
モル比は通垞、0.1〜10、奜たしくは0.3〜の範
囲内で遞択される。反応時間は、通垞10分〜時
間皋床でよい。 生成する癜金−錫觊媒は、垞法により晶析させ
お単離するこずができる。 本発明方法により補造される癜金−錫觊媒はヒ
ドロホルミル化反応によるアルデヒド補造甚の均
䞀系錯䜓觊媒反応に䜿甚し埗るが、このような堎
合には癜金−錫觊媒を単離するこずなく、反応生
成液をそのたた、あるいは癜金−錫觊媒は析出し
た堎合は、適圓な溶媒を加えお溶解させたのち、
觊媒液ずしお䜿甚するこずもできる。かかる堎合
には、觊媒反応に䜿甚される溶媒䞭で癜金−錫觊
媒を補造するのが特に奜たしい。 次に本発明を実斜䟋により曎に具䜓的に説明す
るが、本発明はその芁旚を越えない限り、以䞋の
実斜䟋によ぀お限定されるものではない。 実斜䟋  内容積100mlのステンレススチヌル補スピナヌ
攪拌匏ミクロオヌトクレヌブに、PtCl2DPCB
0.18、C6H53SnOCOCH30.102、35塩酞
0.025mlおよびゞオキサン20mlを仕蟌み、オヌト
クレヌブ内を窒玠眮換20Kgcm2・×回
し、氎玠ず䞀酞化炭玠ずの混合ガスH2COモ
ル比1.0を60Kgcm2・たで圧入し、100℃で
時間反応させた。 反応終了埌、取り出した反応液は、黄色均䞀溶
液であ぀た。アルゎンガス雰囲気䞋に玄10倍容量
の−ヘキサン䞭に滎䞋し、析出した沈殿を別
し真空也燥するこずにより0.196の黄色固䜓を
埗た。埗られた固䜓の元玠分析倀を䞋に瀺す。 Pt Sn  20.3 14.6 7.4 Cl   12.4 40.5 3.7wt 参考䟋  内容積200mlのステンレススチヌル補䞊䞋攪拌
匏オヌトクレヌブに、実斜䟋で埗た黄色固䜓
0.098およびトル゚ン50mlを仕蟌み、密閉した
埌、オヌトクレヌブ内を窒玠眮換し、プロピレン
10.5を圧入した。次いでオヌトクレヌブ内を
100℃たで玄20分で昇枩し、これに氎玠及び䞀酞
化炭玠の混合ガスH2COモル比1.0を圧入
し、オヌトクレヌブ内の圧力を100Kgcm2・ず
した。オヌトクレヌブの内枩を100℃に保ち぀぀
攪拌を続け、内圧が100Kgcm2・ずなるように、
氎玠及び䞀酞化炭玠の混合ガスH2COモル比
1.0を補絊し、所定時間反応を行぀た。反応終
了埌、取り出した反応液は、黄色均䞀溶液であ぀
た。ガスクロマトグラフを甚いお生成物を分析し
た結果および補絊した氎玠及び䞀酞化炭玠の混合
ガスの䟛絊速床より求めた反応速床を衚−に瀺
す。Run− 掻性を比范するために、癜金−錫觊媒をあらか
じめ調補せずに、前蚘黄色固䜓のかわりにPtCl2
DPCB0.0755およびC6H53SnOCOCH3
0.0429を甚いたこず以倖は同様に凊理したずこ
ろ反応液䞭に少量の黒色析出物が認められた。反
応結果を衚−に䜵蚘する。Run−
Examples include platinum complexes such as [Formula] (hereinafter referred to as PtCl 2 (DPCB)). A ligand compound containing an element of group 5B of the periodic table has the general formula: AR 4 R 5 R 6 (wherein A represents phosphorus, arsenic, antimony, bismuth or nitrogen, R 4 is an alkyl group, Cycloalkyl group, aryl group, aralkyl group, alkoxy group, aryloxy group or -B-A'R 5
R 6 (However, B is an alkylene group or arylene group that may have a substituent, or an alkylene group, cycloalkylene group, arylene group, or bicycloalkylene group bonded to A or A' via an alkylene group or an oxygen atom) represents,
A′ represents phosphorus, arsenic, antimony, bismuth or nitrogen. ), and R 5 and R 6 represent an alkyl group, a cycloalkyl group, an aryl group, an aralkyl group, an alkoxy group, or an aryloxy group. ) A monodentate or bidentate ligand represented by is preferably used. Specifically, monodentate ligands include triphenylphosphine, tritolylphosphine, tris(chlorophenyl)phosphine, tris(methoxyphenyl)phosphine, benzyldiphenylphosphine, and bis(2-cyanoethyl)phenylphosphine. , tricyclohexylphosphine, diethyl phenyl phosphine, triethyl phosphine, tripropyl phosphine, tributyl phosphine, trinaphthyl phosphine, tribenzyl phosphine, diphenylene phenyl phosphine, etc., triethyl Phosphite, tertiary phosphite such as tripropylphosphite, tributylphosphite, tridecylphosphite, triphenylphosphite, tris(chlorophenyl)phosphite, tertiary arsine such as triphenylarsine, tritolylarsine, triethylarsine, etc. , tertiary stibines such as tributylstibine and triphenylstibine, tertiary bismuthins such as triphenylbismuthin, tertiary amines such as tributylamine and triphenylamine, and 1 as a bidentate ligand. , 2-bis(diphenylphosphino)ethane, 1,3-bis(diphenylphosphino)propane, 1,4-bis(diphenylphosphino)butane, 1,5-bis(diphenylphosphino)pentane , 1-(diphenylphosphino)-2-(diphenylarsino)ethane, 1,2-bis(diphenylarsino)ethane, o-phenylenebis(dimethylarsine),
o-phenylene bis(diphenylphosphine),
1,2-bis(diphenylphosphinomethyl)benzene, 2,2'-bis(diphenylphosphinomethyl)-1,1'-binaphthyl, 2,2'-bis(diphenylphosphinooxy)-1 , 1'-binaphthyl, 1,2'-bis(diphenylphosphinomethyl)cyclohexane, 1,2-bis(diphenylphosphinomethyl)cyclobutane, 1,2-bis(diphenylarsinomethyl)cyclobutane, 2 
3-o-isopropylidene-2,3-dihydroxy-1,4-bis(diphenylphosphino)butane, trane-2,3-bis(diphenylphosphinomethyl)bicyclo[2,2,2]octane, etc. can be mentioned. These ligand compounds are preferably used in an amount of 1 to 10 times the mole of platinum in terms of Group 5B elements. The tin compound can be selected from various inorganic and organic tin compounds, but preferably has the general formula: ArSnR 1 R 2 R 3 (wherein Ar represents an aryl group that may have a substituent, and R 1 , R 2 and R 3 represent a hydrogen atom, a hydroxy group, an acyloxy group, a halogen atom, or an alkyl group, an alkenyl group, an aryl group, or an alkenyl group that may have a substituent. and General formula: Sn(R)n (wherein R is an oxygen atom or an acyloxy group,
n represents an integer of 1, 2 or 4. ) is used. Examples of the above aryltin compound include (C 6 H 5 )
SnCl 3 , (p-CH 3・C 6 H 4 ) 2 SnCl 2 , (C 6 H 5 ) 2
SnCl 2 , (C 6 H 5 ) 3 SnCl, (C 6 H 5 ) 3 SnBr, (C 6 H 5 ) 3
SnI, (C 6 F 5 ) 3 SnCl, (C 6 H 5 ) 3 SnOCH 3 , (C 6 H 5 ) 3
SnCH 3 , (C 6 H 5 ) 3 SnCH 2・CH 2 OH, (C 6 H 5 ) 3
Examples include SnCH 2 CH=CH 2 . Particularly preferred among the above aryltin compounds are triaryltin compounds represented by the general formula: Ar 3 SnX (wherein Ar represents an aryl group, and X represents a hydrogen atom, a hydroxyl group, or an acyloxy group). Yes, specifically (C 6 H 5 ) 3 SnH, (C 6 H 5 ) 3 SnOH, (C 6 H 5 ) 3
Examples include SnOCOCH 3 , (C 6 H 5 ) 3 SnOCOC 6 H 5 . Next, a specific example of the oxytin compound is given.
SnO, SnO 2 , Sn(OCOCH 3 ) 2 , Sn(OCOCH 3 ) 4 and the like, with Sn(OCOCH 3 ) 2 being particularly suitable. These tin compounds are preferably used in an amount of 0.5 to 2 moles relative to platinum. Hydrogen fluoride, hydrogen chloride, hydrogen bromide and hydrogen iodide are used as hydrogen halides. The form in which they are added to these reaction systems is not particularly limited, and they may be used in a gaseous state or dissolved in an aqueous solution (hydrohalic acid) or an organic solvent such as methanol, ethanol, acetone, or dioxane. It is possible. The concentration of hydrogen halide when used dissolved in a solvent is not particularly limited and can be arbitrarily adjusted within the range of solubility. For example, in the case of hydrochloric acid, a commercially available product with a concentration of 35% is sufficient. The amount of these hydrogen halides to be used varies depending on the form of the platinum compound used and is not necessarily uniquely determined. For example, if a zero-valent platinum compound is used, hydrogen halide is consumed by oxidative addition to platinum, so a larger amount is required than a dihalogenated platinum type compound. Also, if used in large amounts, problems such as corrosion will occur, so it is preferable to use as little as possible within the range in which a platinum-tin catalyst is formed, usually in the range of 0.05 to 5 times the mole of platinum. It is preferably used in A solvent is used in the method of the invention. Specific examples of solvents include methanol, ethanol,
Alcohols such as n-propyl alcohol, isopropyl alcohol, n-butyl alcohol, Sec-butyl alcohol, cyclohexanol, ethers such as diethyl ether, dioxane, tetrahydrofuran, ketones such as acetone, methyl ethyl ketone, diethyl ketone, acetamide, propion Amides, amides such as amide, N,N-dimethylformamide and N,N-dimethylacetamide, nitriles such as acetonitrile, propionitrile and benzonitrile, esters such as ethyl acetate and methyl propionate, and sulfoxides such as dimethyl sulfoxide. , carboxylic acids such as acetic acid, pyridyls such as pyridine and methylpyridine,
Examples include aldehydes such as acetaldehyde and propionaldehyde, hydrocarbons such as benzene, toluene, xylene, and decane, and halogenated hydrocarbons such as methylene chloride, carbon tetrachloride, and o-dichlorobenzene. 2
Used as a mixture of more than one species. Particularly preferred solvents are benzene, toluene, acetone, dioxane, tetrahydrofuran, and the like. The amount of these solvents used is
There is no particular limitation as long as the amount is at least capable of dissolving the ligand compound containing the group element and the tin compound. In carrying out the present invention, the reaction temperature is usually selected within the range of room temperature to 200°C, preferably 50 to 150°C, and the pressure of hydrogen or a mixed gas of hydrogen and carbon monoxide is adjusted to the reaction temperature. It depends, but usually normal pressure ~ 300
The pressure is preferably selected within the range of 5 to 200 atmospheres. H 2 /CO, a gas mixture of hydrogen and carbon monoxide
The molar ratio is usually selected within the range from 0.1 to 10, preferably from 0.3 to 3. The reaction time may generally be about 10 minutes to 4 hours. The resulting platinum-tin catalyst can be isolated by crystallization using a conventional method. The platinum-tin catalyst produced by the method of the present invention can be used in homogeneous complex catalytic reactions for the production of aldehydes by hydroformylation reactions, but in such cases the reaction product can be obtained without isolating the platinum-tin catalyst. Either leave the liquid as it is, or if the platinum-tin catalyst precipitates, add an appropriate solvent to dissolve it.
It can also be used as a catalyst liquid. In such cases, it is particularly preferred to prepare the platinum-tin catalyst in the solvent used for the catalytic reaction. Next, the present invention will be explained in more detail with reference to Examples, but the present invention is not limited to the following Examples unless the gist of the present invention is exceeded. Example 1 PtCl 2 (DPCB) was placed in a stainless steel spinner-stirring micro autoclave with an internal volume of 100 ml.
0.18g, (C 6 H 5 ) 3 SnOCOCH 3 0.102g, 35% hydrochloric acid
Charge 0.025ml and 20ml of dioxane and replace the inside of the autoclave with nitrogen (20Kg/cm 2・G x 3 times)
Then, a mixed gas of hydrogen and carbon monoxide (H 2 /CO molar ratio 1.0) was injected up to 60 kg/cm 2 G, and the mixture was heated at 100°C for 30 minutes.
Allowed time to react. After the reaction was completed, the reaction solution taken out was a yellow homogeneous solution. The mixture was dropped into about 10 times the volume of n-hexane under an argon gas atmosphere, and the precipitate was separated and dried under vacuum to obtain 0.196 g of a yellow solid. The elemental analysis values of the obtained solid are shown below. Pt Sn P 20.3 14.6 7.4 Cl C H 12.4 40.5 3.7 (wt%) Reference example 1 The yellow solid obtained in Example 1 was placed in a stainless steel vertically stirred autoclave with an internal volume of 200 ml.
After charging 0.098 g and 50 ml of toluene and sealing the autoclave, the inside of the autoclave was replaced with nitrogen and propylene was added.
10.5g was press-fitted. Then inside the autoclave
The temperature was raised to 100° C. in about 20 minutes, and a mixed gas of hydrogen and carbon monoxide (H 2 /CO molar ratio 1.0) was pressurized to bring the pressure inside the autoclave to 100 Kg/cm 2 ·G. Continue stirring while keeping the internal temperature of the autoclave at 100℃, and keep the internal pressure at 100Kg/cm 2・G.
Mixed gas of hydrogen and carbon monoxide (H 2 /CO molar ratio
1.0) was replenished, and the reaction was carried out for a predetermined period of time. After the reaction was completed, the reaction solution taken out was a yellow homogeneous solution. Table 1 shows the reaction rate determined from the results of analyzing the product using a gas chromatograph and the supply rate of the supplied mixed gas of hydrogen and carbon monoxide. (Run-1) In order to compare the activity, PtCl 2 was used instead of the yellow solid without preparing the platinum-tin catalyst in advance.
(DPCB) 0.0755g and (C 6 H 5 ) 3 SnOCOCH 3
When the same treatment was carried out except that 0.0429 g was used, a small amount of black precipitate was observed in the reaction solution. The reaction results are also listed in Table-1. (Run-2)

【衚】 比范䟋  塩酞を甚いないこず以倖は、実斜䟋ず同様に
凊理したずころ、取り出した反応液䞭にメタル化
により生じた黒色沈殿物が認められた。 実斜䟋  前蚘ミクロオヌトクレヌブにPtCl2〔C6H5
〕20.395、C6H53SnOCOCH30.20435塩
酾0.05mlおよびアセトン15mlを仕蟌み、反応時間
を時間ずしたこず以倖は、実斜䟋ず同様に凊
理したずころ取り出した反応液は、黄色均䞀溶液
であり、該液より同様に橙色固䜓0.385を埗た。
このうち0.192をアセトンに溶解し−ヘキサ
ンで再沈殿粟補を行぀た結果、0.09の赀橙色の
固䜓が埗られた。元玠分析の結果より、15.6wt
のPt17.5wtのSn5.5wtのが含有されお
いた。 比范䟋  塩酞を甚いないこず以倖は、実斜䟋ず同様に
凊理したずころ、取り出した反応液䞭には黒色沈
殿物が認められた。 実斜䟋  C6H53SnOCOCH3およびアセトンのかわり
に、SnOCOCH320.118およびゞオキサン25ml
をそれぞれ甚いたこず以倖は実斜䟋ず同様に凊
理しお橙色固䜓0.339を埗た。 参考䟋  実斜䟋で埗た橙色固䜓0.17を甚いたこず以
倖は参考䟋ず同様にプロピレンのヒドロホルミ
ル化反応を実斜したずころ、反応は誘導期なく進
行するこずが認められた。
[Table] Comparative Example 1 When the same treatment as in Example 1 was performed except that hydrochloric acid was not used, a black precipitate caused by metalization was observed in the taken out reaction solution. Example 2 PtCl 2 [P(C 6 H 5 )] was added to the micro autoclave.
3 ] 2 0.395 g, (C 6 H 5 ) 3 SnOCOCH 3 0.204 g, 0.05 ml of 35% hydrochloric acid and 15 ml of acetone were charged, and the same procedure as in Example 1 was taken, except that the reaction time was 2 hours. The reaction solution was a yellow homogeneous solution, and 0.385 g of an orange solid was similarly obtained from the solution.
Of this, 0.192 g was dissolved in acetone and purified by reprecipitation with n-hexane, resulting in 0.09 g of a reddish-orange solid. Based on the results of elemental analysis, 15.6wt%
of Pt, 17.5 wt% of Sn, and 5.5 wt% of P. Comparative Example 2 The same procedure as in Example 2 was carried out except that hydrochloric acid was not used, and a black precipitate was observed in the reaction solution taken out. Example 3 Instead of (C 6 H 5 ) 3 SnOCOCH 3 and acetone, 0.118 g of Sn(OCOCH 3 ) 2 and 25 ml of dioxane
0.339 g of an orange solid was obtained by processing in the same manner as in Example 2, except that each of these was used. Reference Example 2 When a hydroformylation reaction of propylene was carried out in the same manner as in Reference Example 1 except that 0.17 g of the orange solid obtained in Example 3 was used, it was observed that the reaction proceeded without an induction period.

Claims (1)

【特蚱請求の範囲】  癜金化合物、第5B族元玠を含む配䜍子化合
物、錫化合物およびハロゲン化氎玠を、溶媒䞭
で、氎玠たたは氎玠ず䞀酞化炭玠ずの混合ガスの
存圚䞋に、反応させるこずを特城ずするヒドロホ
ルミル化反応によるアルデヒド補造甚癜金−錫觊
媒の補造法。  特蚱請求の範囲第項に蚘茉のヒドロホルミ
ル化反応によるアルデヒド補造甚癜金−錫觊媒の
補造法においお、該錫化合物が、 䞀般匏ArSnR1R2R3 匏䞭、Arは眮換基を有しおいおもよいアリ
ヌル基を衚わし、R1R2およびR3は氎玠原子、
ヒドロキシル基、アシルオキシ基、ハロゲン原
子、たたは眮換基を有しおいおもよいアルキル
基、アルケニル基、アリヌル基もしくはアルコキ
シ基を衚わす。 で瀺される化合物であるこずを特城ずする方法。  特蚱請求の範囲第項に蚘茉のヒドロホルミ
ル化反応によるアルデヒド補造甚癜金−錫觊媒の
補造法においお、該錫化合物が、 䞀般匏Sn 匏䞭、は酞玠原子たたはアシルオキシ基
を、は、たたはである敎数を衚わす。 で瀺される化合物であるこずを特城ずする方法。
[Claims] 1. Reaction of a platinum compound, a ligand compound containing a Group 5B element, a tin compound, and a hydrogen halide in the presence of hydrogen or a mixed gas of hydrogen and carbon monoxide in a solvent. 1. A method for producing a platinum-tin catalyst for producing an aldehyde by a hydroformylation reaction. 2. In the method for producing a platinum-tin catalyst for producing an aldehyde by a hydroformylation reaction according to claim 1, the tin compound has the general formula: ArSnR 1 R 2 R 3 (wherein Ar represents a substituent). represents an optional aryl group, R 1 , R 2 and R 3 are hydrogen atoms,
It represents a hydroxyl group, an acyloxy group, a halogen atom, or an alkyl group, an alkenyl group, an aryl group, or an alkoxy group that may have a substituent. ) A method characterized in that the compound is a compound represented by 3. In the method for producing a platinum-tin catalyst for producing aldehydes by hydroformylation reaction according to claim 1, the tin compound has the general formula: Sn(R)n (wherein R is an oxygen atom or acyloxy n represents an integer of 1, 2 or 4).
JP58078812A 1983-05-04 1983-05-04 Production method of platinum-tin catalyst Granted JPS59203640A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58078812A JPS59203640A (en) 1983-05-04 1983-05-04 Production method of platinum-tin catalyst

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58078812A JPS59203640A (en) 1983-05-04 1983-05-04 Production method of platinum-tin catalyst

Publications (2)

Publication Number Publication Date
JPS59203640A JPS59203640A (en) 1984-11-17
JPH0575461B2 true JPH0575461B2 (en) 1993-10-20

Family

ID=13672253

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58078812A Granted JPS59203640A (en) 1983-05-04 1983-05-04 Production method of platinum-tin catalyst

Country Status (1)

Country Link
JP (1) JPS59203640A (en)

Also Published As

Publication number Publication date
JPS59203640A (en) 1984-11-17

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