JPH0420420B2 - - Google Patents
Info
- Publication number
- JPH0420420B2 JPH0420420B2 JP3002684A JP3002684A JPH0420420B2 JP H0420420 B2 JPH0420420 B2 JP H0420420B2 JP 3002684 A JP3002684 A JP 3002684A JP 3002684 A JP3002684 A JP 3002684A JP H0420420 B2 JPH0420420 B2 JP H0420420B2
- Authority
- JP
- Japan
- Prior art keywords
- reaction
- carbonylation
- catalyst
- biphenyl
- alkyl
- 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
Links
- 239000003054 catalyst Substances 0.000 claims description 10
- 239000007789 gas Substances 0.000 claims description 7
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 6
- 229910002091 carbon monoxide Inorganic materials 0.000 claims description 6
- 238000004519 manufacturing process Methods 0.000 claims description 6
- NEQFBGHQPUXOFH-UHFFFAOYSA-N 4-(4-carboxyphenyl)benzoic acid Chemical compound C1=CC(C(=O)O)=CC=C1C1=CC=C(C(O)=O)C=C1 NEQFBGHQPUXOFH-UHFFFAOYSA-N 0.000 claims description 5
- LEMQFBIYMVUIIG-UHFFFAOYSA-N trifluoroborane;hydrofluoride Chemical compound F.FB(F)F LEMQFBIYMVUIIG-UHFFFAOYSA-N 0.000 claims description 4
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 claims description 2
- 229910001882 dioxygen Inorganic materials 0.000 claims description 2
- 238000006243 chemical reaction Methods 0.000 description 19
- ZZLCFHIKESPLTH-UHFFFAOYSA-N 4-Methylbiphenyl Chemical group C1=CC(C)=CC=C1C1=CC=CC=C1 ZZLCFHIKESPLTH-UHFFFAOYSA-N 0.000 description 14
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 12
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 12
- ZUOUZKKEUPVFJK-UHFFFAOYSA-N phenylbenzene Natural products C1=CC=CC=C1C1=CC=CC=C1 ZUOUZKKEUPVFJK-UHFFFAOYSA-N 0.000 description 12
- 238000005810 carbonylation reaction Methods 0.000 description 9
- 239000004305 biphenyl Substances 0.000 description 7
- 235000010290 biphenyl Nutrition 0.000 description 7
- 230000006315 carbonylation Effects 0.000 description 7
- 238000000034 method Methods 0.000 description 6
- SRQOBNUBCLPPPH-UHFFFAOYSA-N 1-ethyl-4-phenylbenzene Chemical group C1=CC(CC)=CC=C1C1=CC=CC=C1 SRQOBNUBCLPPPH-UHFFFAOYSA-N 0.000 description 4
- 238000010521 absorption reaction Methods 0.000 description 4
- 239000002994 raw material Substances 0.000 description 4
- 238000003756 stirring Methods 0.000 description 4
- 229910015900 BF3 Inorganic materials 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 description 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- 150000001299 aldehydes Chemical class 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- 239000003921 oil Substances 0.000 description 3
- 230000003647 oxidation Effects 0.000 description 3
- 238000007254 oxidation reaction Methods 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- KWSHGRJUSUJPQD-UHFFFAOYSA-N 1-phenyl-4-propan-2-ylbenzene Chemical group C1=CC(C(C)C)=CC=C1C1=CC=CC=C1 KWSHGRJUSUJPQD-UHFFFAOYSA-N 0.000 description 2
- ISDBWOPVZKNQDW-UHFFFAOYSA-N 4-phenylbenzaldehyde Chemical group C1=CC(C=O)=CC=C1C1=CC=CC=C1 ISDBWOPVZKNQDW-UHFFFAOYSA-N 0.000 description 2
- KRHYYFGTRYWZRS-UHFFFAOYSA-N Fluorane Chemical compound F KRHYYFGTRYWZRS-UHFFFAOYSA-N 0.000 description 2
- -1 alkyl biphenyl Chemical compound 0.000 description 2
- 125000003118 aryl group Chemical group 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- WTEOIRVLGSZEPR-UHFFFAOYSA-N boron trifluoride Chemical compound FB(F)F WTEOIRVLGSZEPR-UHFFFAOYSA-N 0.000 description 2
- 238000004821 distillation Methods 0.000 description 2
- 229910000040 hydrogen fluoride Inorganic materials 0.000 description 2
- 239000003507 refrigerant Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- DLMYHUARHITGIJ-UHFFFAOYSA-N 1-ethyl-2-phenylbenzene Chemical group CCC1=CC=CC=C1C1=CC=CC=C1 DLMYHUARHITGIJ-UHFFFAOYSA-N 0.000 description 1
- JRMFMZATWIFRMF-UHFFFAOYSA-N 4-phenylbenzaldehyde Chemical compound C1=CC(C=O)=CC=C1C1=CC=CC=C1.C1=CC(C=O)=CC=C1C1=CC=CC=C1 JRMFMZATWIFRMF-UHFFFAOYSA-N 0.000 description 1
- NNJMFJSKMRYHSR-UHFFFAOYSA-N 4-phenylbenzoic acid Chemical compound C1=CC(C(=O)O)=CC=C1C1=CC=CC=C1 NNJMFJSKMRYHSR-UHFFFAOYSA-N 0.000 description 1
- XZIPJISANVLUBR-UHFFFAOYSA-N 5-ethyl-2-(4-ethylphenyl)benzaldehyde Chemical compound C(C)C=1C=C(C(=CC=1)C1=CC=C(C=C1)CC)C=O XZIPJISANVLUBR-UHFFFAOYSA-N 0.000 description 1
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 1
- 239000005977 Ethylene Substances 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- 125000003172 aldehyde group Chemical group 0.000 description 1
- 150000004996 alkyl benzenes Chemical class 0.000 description 1
- 125000000217 alkyl group Chemical group 0.000 description 1
- 230000002152 alkylating effect Effects 0.000 description 1
- 239000004760 aramid Substances 0.000 description 1
- 150000003934 aromatic aldehydes Chemical class 0.000 description 1
- 150000001491 aromatic compounds Chemical class 0.000 description 1
- 229920003235 aromatic polyamide Polymers 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 125000002915 carbonyl group Chemical group [*:2]C([*:1])=O 0.000 description 1
- ZBYYWKJVSFHYJL-UHFFFAOYSA-L cobalt(2+);diacetate;tetrahydrate Chemical compound O.O.O.O.[Co+2].CC([O-])=O.CC([O-])=O ZBYYWKJVSFHYJL-UHFFFAOYSA-L 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 230000001335 demethylating effect Effects 0.000 description 1
- PLXSXOUOWRGVOZ-UHFFFAOYSA-L dibromocobalt;hexahydrate Chemical compound O.O.O.O.O.O.Br[Co]Br PLXSXOUOWRGVOZ-UHFFFAOYSA-L 0.000 description 1
- 230000020169 heat generation Effects 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 238000005984 hydrogenation reaction Methods 0.000 description 1
- 239000005457 ice water Substances 0.000 description 1
- 230000006698 induction Effects 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 229940082328 manganese acetate tetrahydrate Drugs 0.000 description 1
- CESXSDZNZGSWSP-UHFFFAOYSA-L manganese(2+);diacetate;tetrahydrate Chemical compound O.O.O.O.[Mn+2].CC([O-])=O.CC([O-])=O CESXSDZNZGSWSP-UHFFFAOYSA-L 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 229910052763 palladium Inorganic materials 0.000 description 1
- 229920001225 polyester resin Polymers 0.000 description 1
- 239000004645 polyester resin Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 1
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000010936 titanium Substances 0.000 description 1
- 229910052719 titanium Inorganic materials 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/16—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation
- C07C51/21—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen
- C07C51/23—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of oxygen-containing groups to carboxyl groups
- C07C51/235—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of oxygen-containing groups to carboxyl groups of —CHO groups or primary alcohol groups
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C45/00—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds
- C07C45/49—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reaction with carbon monoxide
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/16—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation
- C07C51/21—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen
- C07C51/255—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of compounds containing six-membered aromatic rings without ring-splitting
- C07C51/265—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of compounds containing six-membered aromatic rings without ring-splitting having alkyl side chains which are oxidised to carboxyl groups
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Description
【発明の詳細な説明】
本発明は4,4′−ビフエニルジカルボン酸の製
造法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing 4,4'-biphenyldicarboxylic acid.
4,4′−ビフエニルジカルボン酸(以下BPDC
と称す)は耐熱性、高強度を有する高性能ポリエ
ステル樹脂又はアラミド樹脂の素材として有用で
あり、その製造方法についても種々の方法が提案
されている。しかし従来提案されているいずれの
方法も複雑であるか又は収率が低い等の欠点を有
し、経済的なBPDCの製造方法にはなり難いのが
実情であつた。 4,4'-biphenyldicarboxylic acid (hereinafter referred to as BPDC)
) is useful as a material for high-performance polyester resin or aramid resin having heat resistance and high strength, and various methods have been proposed for its production. However, all of the methods proposed so far have drawbacks such as being complicated or having low yields, and the reality is that it is difficult to provide an economical method for producing BPDC.
本発明者は弗化水素−弗化硼素触媒を用いた芳
香族化合物の一酸化炭素によるカルボニル化反応
について検討する中で、アルキルビフエニルのカ
ルボニル化反応において当初アルキル基の存在す
る芳香族がカルボニル化されると予想されたにも
拘らず他の芳香族の4′位が極めて選択的にカルボ
ニル化されることを見出すと共に、更にはカルボ
ニル化生成物を分子状酸素含有ガスで酸化するこ
とにより高収率でBPDCを得ることが出来ること
を見出し本発明に到達した。即ち本発明は4−ア
ルキルビフエニルを弗化水素−弗化硼素触媒の存
在下、一酸化炭素と反応させて4−アルキル−
4′−ホルミルビフエニルを得、次いでこれを分子
状酸素含有ガスで酸化することにより4,4′−ビ
フエニルジカルボン酸を製造する方法である。 While investigating the carbonylation reaction of aromatic compounds with carbon monoxide using a hydrogen fluoride-boron fluoride catalyst, the present inventor discovered that in the carbonylation reaction of alkyl biphenyl, the aromatic group in which the alkyl group is present initially becomes the carbonyl group. We found that the 4'-position of other aromatic groups was carbonylated very selectively, even though it was expected that the 4'-position would be carbonylated. The inventors have discovered that BPDC can be obtained in high yield and have arrived at the present invention. That is, in the present invention, 4-alkylbiphenyl is reacted with carbon monoxide in the presence of a hydrogen fluoride-boron fluoride catalyst to form 4-alkyl-
This is a method for producing 4,4'-biphenyldicarboxylic acid by obtaining 4'-formylbiphenyl and then oxidizing it with a molecular oxygen-containing gas.
本発明の原料として使用する4−アルキルビフ
エニルとは、4−メチルビフエニル、4−エチル
ビフエニル、4−イソプロピルビフエニル等であ
り、これらは種々の方法で得ることが出来る。た
とえば4−メチルビフエニルはトルエンの脱メチ
ル化によるベンゼンの製造工程での副生高沸油か
ら回収することが出来る。またビフエニルを弗化
水素−弗化硼素触媒存在下に一酸化炭素と反応さ
せカルボニル化して得られる4−ホルミルビフエ
ニル(4−ビフエニルアルデヒド)を水素添加し
ても容易に得ることが出来る。この方法によりビ
フエニルから95%以上の収率で4−メチルビフエ
ニルを得ることが出来る。 The 4-alkylbiphenyl used as a raw material in the present invention includes 4-methylbiphenyl, 4-ethylbiphenyl, 4-isopropylbiphenyl, etc., and these can be obtained by various methods. For example, 4-methylbiphenyl can be recovered from high-boiling oil by-product in the benzene manufacturing process by demethylating toluene. It can also be easily obtained by hydrogenating 4-formylbiphenyl (4-biphenylaldehyde), which is obtained by carbonylating biphenyl by reacting it with carbon monoxide in the presence of a hydrogen fluoride-boron fluoride catalyst. By this method, 4-methylbiphenyl can be obtained from biphenyl in a yield of 95% or more.
ビフエニルのカルボニル化の条件はたとえば触
媒として弗化水素及び弗化硼素を原料に対し4〜
10:1〜1.5:1、好ましくは5〜6:1.2〜1.3:
1の割合で使用し、ベンゼン等の溶媒存在下、一
酸化炭素分圧5〜30Kg/cm2G、好ましくは10〜20
Kg/cm2G、反応温度5〜20℃、好ましくは5〜10
℃で行なうことが出来る。又水素添加の条件はた
とえば活性炭上に担持したパラジウム触媒の存在
下、水素圧5〜50Kg/cm2G、好ましくは10〜30
Kg/cm2G、反応温度100〜200℃、好ましくは120
〜150℃である。 The conditions for carbonylation of biphenyl are, for example, hydrogen fluoride and boron fluoride as catalysts,
10:1-1.5:1, preferably 5-6:1.2-1.3:
1 in the presence of a solvent such as benzene, at a carbon monoxide partial pressure of 5 to 30 Kg/cm 2 G, preferably 10 to 20
Kg/ cm2G , reaction temperature 5-20℃, preferably 5-10
It can be done at ℃. The conditions for hydrogenation are, for example, in the presence of a palladium catalyst supported on activated carbon, hydrogen pressure 5 to 50 Kg/cm 2 G, preferably 10 to 30 G.
Kg/ cm2G , reaction temperature 100-200℃, preferably 120
~150℃.
4−エチルビフエニル、4−イソプロピルビフ
エニルは、ビフエニルをエチレン、プロピレンに
よりアルキル化する方法で現在熱媒油等の用途向
けに製造されており、これらの中から蒸留、晶析
等の物理的手段で製品を得ることは容易である。 4-Ethylbiphenyl and 4-isopropylbiphenyl are currently produced for use as heat transfer oils by alkylating biphenyl with ethylene or propylene. It is easy to get the product.
4−アルキルビフエニルをカルボニル化する方
法は、既に芳香族アルデヒドの工業的な製造プロ
セスとして確立されている通常のアルキルベンゼ
ン類のカルボニル化方法が適用できる。 As a method for carbonylating 4-alkylbiphenyl, a conventional method for carbonylating alkylbenzenes, which has already been established as an industrial production process for aromatic aldehydes, can be applied.
その反応条件は例えば、アルキルビフエニル:
弗化硼素:弗化水素=1:1.1〜1.7:5〜10(モ
ル比)の触媒組成を用い、一酸化炭素分圧10〜20
Kg/cm2G、反応温度0〜20℃で15〜30分間反応さ
せることにより、円滑な反応が進行し、極めて高
収率、高選択率で目的とする4−アルキル−4′−
ホルミルビフエニル(4,4′−アルキルビフエニ
ルアルデヒド)を得ることが出来る。 The reaction conditions are, for example, alkyl biphenyl:
Using a catalyst composition of boron fluoride: hydrogen fluoride = 1:1.1-1.7:5-10 (mole ratio), carbon monoxide partial pressure 10-20
By reacting for 15 to 30 minutes at Kg/cm 2 G and reaction temperature of 0 to 20°C, the reaction proceeds smoothly and the desired 4-alkyl-4'- is produced in extremely high yield and high selectivity.
Formylbiphenyl (4,4'-alkylbiphenylaldehyde) can be obtained.
4−アルキル−4′−ホルミルビフエニルの酸化
によるBPDCへの誘導は同じく比較的容易であつ
て、酢酸等の溶媒存在下、種々の触媒系により、
いずれも高収率でBPDCを得ることが出来る。 Induction of BPDC by oxidation of 4-alkyl-4'-formylbiphenyl is also relatively easy, and can be carried out using various catalyst systems in the presence of a solvent such as acetic acid.
In either case, BPDC can be obtained in high yield.
上述のように、本発明は、入手し易い原料から
単純な工程により有用なBPDCを合理的に製造し
得る方法を提供するものであり、その工業的価値
は高い。 As described above, the present invention provides a method for rationally producing useful BPDC from easily available raw materials through simple steps, and has high industrial value.
実施例 1
(アルキルビフエニルのカルボニル化)
ビフエニルをHF−BF3触媒でCOによりカル
ボニル化し4−ビフエニルアルデヒド(選択率
99%)を得、これをPd/カーボン触媒を用い
てアルデヒド基をメチル還元して調製して得た
4−メチルビフエニルを原料として以下のカル
ボニル化を行なつた。Example 1 (Carbonylation of alkylbiphenyl) Biphenyl was carbonylated with CO using HF- BF3 catalyst to produce 4-biphenylaldehyde (selectivity
The following carbonylation was carried out using 4-methylbiphenyl obtained by reducing the aldehyde group with methyl using a Pd/carbon catalyst as a raw material.
容積5の撹拌機つきオートクレーブをカル
ボニル化反応器として使用した。反応器はジヤ
ケツトの冷媒により冷却出来る。 A stirred autoclave with a volume of 5 was used as the carbonylation reactor. The reactor can be cooled by a jacket of refrigerant.
1136g(純度99.6%、6.73モル)の4−メチル
ビフエニルを568g(7.3モル)のベンゼンに溶解
して反応器に仕込み、続いて撹拌及び冷却を行
ないながら、1200g(60モル)のHF及び640g
(9.4モル)のBF3ガスを仕込み、4−メチルビ
フエニルのHF−BF3コンプレツクス溶液を調
合した。引続き撹拌及び冷却しながらCOガス
を導入し、反応器を20Kg/cm2Gに加圧保持しな
がらカルボニル化を行なつた。約15分で発熱を
伴なうCOの吸収は停止した。この間反応温度
は約10℃に保持した。反応終了後、内容液を氷
水中に抜出し、油層をアルカリ水及び水洗浄し
た後、蒸留により4,4′−メチルビフエニルア
ルデヒド(沸点170℃/4mmHg)を製取した。
4−メチルビフエニルのアルデヒドへの転化率
80%、アルデヒド中の4,4′体の選択率は97%
であつた。 1136 g (99.6% purity, 6.73 mol) of 4-methylbiphenyl was dissolved in 568 g (7.3 mol) of benzene and charged into the reactor, followed by 1200 g (60 mol) of HF and 640 g with stirring and cooling.
(9.4 mol) of BF 3 gas was charged, and an HF-BF 3 complex solution of 4-methylbiphenyl was prepared. CO gas was introduced while stirring and cooling, and carbonylation was carried out while maintaining the pressure of the reactor at 20 kg/cm 2 G. Absorption of CO, which was accompanied by heat generation, stopped in about 15 minutes. During this time, the reaction temperature was maintained at about 10°C. After the reaction was completed, the contents were extracted into ice water, and the oil layer was washed with alkaline water and water, and 4,4'-methylbiphenylaldehyde (boiling point: 170°C/4mmHg) was obtained by distillation.
Conversion rate of 4-methylbiphenyl to aldehyde
80%, selectivity of 4,4′ isomer in aldehyde is 97%
It was hot.
新日鉄化学製サームS600中に52%含有する
4−エチルビフエニルを蒸留、晶析により分離
精製して、カルボニル化原料に用いた。 4-ethylbiphenyl, which was contained in 52% of Nippon Steel Chemical's Therm S600, was separated and purified by distillation and crystallization, and used as a raw material for carbonylation.
2のオートクレーブをカルボニル化反応器
として使用した。オートクレーブにHF1100g
(55モル)を仕込んだ後、撹拌、冷却しながら、
COガスにより反応器を20Kg/cm2Gに加圧維持
した。この状態で定量ポンプにより毎分70g
(0.38モル)の4−エチルビフエニルを70wt%
ベンゼン溶液として供給し、同時に毎分39g
(0.58モル)のBF3ガスをボンベ圧により送入
しながら15分間反応し、送入停止後さらに5分
間反応を継続した後、内液を抜出しと同様に
処理した。反応中、ジヤケツトの冷媒により反
応熱を除き、内温を5℃に維持した。仕込4−
エチルビフエニルに対するアルデヒドの収率は
78%、4,4′−エチルビフエニルアルデヒドへ
の選択率は98%であつた。 Two autoclaves were used as carbonylation reactors. HF1100g in autoclave
After charging (55 mol), while stirring and cooling,
The reactor was kept pressurized at 20 Kg/cm 2 G with CO gas. In this state, the metering pump will give you 70g per minute.
(0.38 mol) of 4-ethylbiphenyl 70wt%
Supplied as a benzene solution, 39g/min at the same time
(0.58 mol) of BF 3 gas was fed into the reactor for 15 minutes by cylinder pressure, and after the feeding was stopped, the reaction was continued for an additional 5 minutes, and then the internal liquid was taken out and treated in the same manner. During the reaction, the heat of reaction was removed by the refrigerant in the jacket, and the internal temperature was maintained at 5°C. Preparation 4-
The yield of aldehyde based on ethylbiphenyl is
The selectivity to 4,4'-ethylbiphenylaldehyde was 98%.
実施例 2
(4,4′−メチルビフエニルアルデヒドの酸
化)
40gの4,4′−メチルビフエニルアルデヒド、
0.44gの臭化コバルト6水塩、0.33gの酢酸マンガ
ン4水塩を200gの95%酢酸と共に、ガス吹込み
口、及び撹拌器を有するチタン製高速電磁撹拌オ
ートクレーブに装入し、反応温度を200℃、圧力
を20Kg/cm2Gに保ちつつ空気を送入する。Example 2 (oxidation of 4,4'-methylbiphenylaldehyde) 40 g of 4,4'-methylbiphenylaldehyde,
0.44 g of cobalt bromide hexahydrate and 0.33 g of manganese acetate tetrahydrate were charged together with 200 g of 95% acetic acid into a titanium high-speed electromagnetic stirring autoclave equipped with a gas inlet and a stirrer, and the reaction temperature was increased. Air is introduced while maintaining the temperature at 200°C and the pressure at 20Kg/cm 2 G.
反応は直ちに生起し、急激な酸素の吸収がみら
れた。反応は実質上酸素吸収を示さなくなつても
更に継続し、合計1.5時間行つた。 The reaction occurred immediately, and rapid oxygen absorption was observed. The reaction continued even when there was no substantial oxygen absorption, for a total of 1.5 hours.
反応液はロ過し、酢酸、水で洗浄後乾燥して粉
末固体として粗4,4′−ビフエニルジカルボン酸
45gを得た。 The reaction solution was filtered, washed with acetic acid and water, and dried to obtain crude 4,4'-biphenyldicarboxylic acid as a powder solid.
Got 45g.
実施例 3
(4,4′−エチルビフエニルアルデヒドの酸
化)
40gの4,4′−ジエチルビフエニルアルデヒド、
40gの酢酸コバルト4水塩を200gの95%酢酸と共
に既述のオートクレーブに装入し、反応温度を
150℃、圧力を20Kg/cm2Gに保ちつつ空気を送入
する。Example 3 (oxidation of 4,4'-ethylbiphenylaldehyde) 40 g of 4,4'-diethylbiphenylaldehyde,
Charge 40g of cobalt acetate tetrahydrate with 200g of 95% acetic acid into the autoclave described above, and adjust the reaction temperature.
Air is introduced while maintaining the temperature at 150°C and the pressure at 20Kg/cm 2 G.
反応は直ちに生起し、急激な酸素の吸収がみら
れた。 The reaction occurred immediately, and rapid oxygen absorption was observed.
反応は1.5時間行なつた。反応液の処理は既述
と同様に行ない、粉末状固体として粗4,4′−ビ
フエニルカルボン酸41gを得た。 The reaction was carried out for 1.5 hours. The reaction solution was treated in the same manner as described above to obtain 41 g of crude 4,4'-biphenylcarboxylic acid as a powdery solid.
Claims (1)
素触媒の存在下、一酸化炭素と反応させて4−ア
ルキル−4′−ホルミルビフエニルを得、次いでこ
れを分子状酸素含有ガスで酸化することを特徴と
する4,4′−ビフエニルジカルボン酸の製造法。1 4-Alkylbiphenyl is reacted with carbon monoxide in the presence of a hydrogen fluoride-boron fluoride catalyst to obtain 4-alkyl-4'-formylbiphenyl, which is then oxidized with a molecular oxygen-containing gas. A method for producing 4,4'-biphenyl dicarboxylic acid, characterized by the following.
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3002684A JPS60174745A (en) | 1984-02-20 | 1984-02-20 | Preparation of 4,4'-biphenyldicarboxylic acid |
GB08502260A GB2155921B (en) | 1984-02-20 | 1985-01-30 | Process for producing 4-alkyl-4'-formylbiphenyl |
DE19853504218 DE3504218C2 (en) | 1984-02-20 | 1985-02-07 | Process for the preparation of 4-alkyl-4'-formylbiphenyl and its use |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3002684A JPS60174745A (en) | 1984-02-20 | 1984-02-20 | Preparation of 4,4'-biphenyldicarboxylic acid |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS60174745A JPS60174745A (en) | 1985-09-09 |
JPH0420420B2 true JPH0420420B2 (en) | 1992-04-02 |
Family
ID=12292314
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3002684A Granted JPS60174745A (en) | 1984-02-20 | 1984-02-20 | Preparation of 4,4'-biphenyldicarboxylic acid |
Country Status (3)
Country | Link |
---|---|
JP (1) | JPS60174745A (en) |
DE (1) | DE3504218C2 (en) |
GB (1) | GB2155921B (en) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS63122645A (en) * | 1986-11-11 | 1988-05-26 | Kureha Chem Ind Co Ltd | Production of biphenyl-4,4'-dicarboxylic acid |
US5068407A (en) * | 1990-01-31 | 1991-11-26 | Monsanto Company | Oxidation of tertiary-alkyl substituted aromatics |
JP2891277B2 (en) * | 1993-07-29 | 1999-05-17 | 三菱瓦斯化学株式会社 | Method for producing 4-formyl-4'-methylbiphenyl |
CN113372208A (en) * | 2021-05-20 | 2021-09-10 | 山东盛华电子新材料有限公司 | Preparation method of trans-4- (trans-4-alkylcyclohexyl) cyclohexanecarboxaldehyde |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB633176A (en) * | 1946-08-24 | 1949-12-12 | Du Pont | Improvements in and relating to the production of aromatic aldehydes |
-
1984
- 1984-02-20 JP JP3002684A patent/JPS60174745A/en active Granted
-
1985
- 1985-01-30 GB GB08502260A patent/GB2155921B/en not_active Expired
- 1985-02-07 DE DE19853504218 patent/DE3504218C2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
DE3504218A1 (en) | 1985-08-22 |
GB2155921B (en) | 1987-09-03 |
JPS60174745A (en) | 1985-09-09 |
GB2155921A (en) | 1985-10-02 |
DE3504218C2 (en) | 1994-06-01 |
GB8502260D0 (en) | 1985-02-27 |
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