JPH02243652A - Method for purifying naphthalenedicarboxylate - Google Patents
Method for purifying naphthalenedicarboxylateInfo
- Publication number
- JPH02243652A JPH02243652A JP6344289A JP6344289A JPH02243652A JP H02243652 A JPH02243652 A JP H02243652A JP 6344289 A JP6344289 A JP 6344289A JP 6344289 A JP6344289 A JP 6344289A JP H02243652 A JPH02243652 A JP H02243652A
- Authority
- JP
- Japan
- Prior art keywords
- ndca
- water
- aqueous solution
- dialkali salt
- salt
- 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.)
- Pending
Links
- 238000000034 method Methods 0.000 title claims abstract description 33
- KYTZHLUVELPASH-UHFFFAOYSA-N naphthalene-1,2-dicarboxylic acid Chemical compound C1=CC=CC2=C(C(O)=O)C(C(=O)O)=CC=C21 KYTZHLUVELPASH-UHFFFAOYSA-N 0.000 title claims abstract description 13
- 150000003839 salts Chemical class 0.000 claims abstract description 54
- 239000007864 aqueous solution Substances 0.000 claims abstract description 31
- 239000003960 organic solvent Substances 0.000 claims abstract description 24
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 24
- 230000001376 precipitating effect Effects 0.000 claims description 6
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 abstract description 14
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 abstract description 12
- 239000012535 impurity Substances 0.000 abstract description 11
- 239000002994 raw material Substances 0.000 abstract description 6
- 239000003513 alkali Substances 0.000 abstract description 5
- 229920000642 polymer Polymers 0.000 abstract description 2
- 238000000151 deposition Methods 0.000 abstract 1
- 239000013078 crystal Substances 0.000 description 19
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical class [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 7
- 239000003463 adsorbent Substances 0.000 description 7
- 239000007787 solid Substances 0.000 description 7
- 239000002253 acid Substances 0.000 description 6
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 description 6
- 150000002894 organic compounds Chemical class 0.000 description 6
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 5
- 150000001447 alkali salts Chemical class 0.000 description 5
- 125000000217 alkyl group Chemical group 0.000 description 5
- -1 di-substituted naphthalene Chemical class 0.000 description 5
- 238000000746 purification Methods 0.000 description 5
- 239000007806 chemical reaction intermediate Substances 0.000 description 4
- 239000000047 product Substances 0.000 description 4
- 229920006395 saturated elastomer Polymers 0.000 description 4
- JHJLBTNAGRQEKS-UHFFFAOYSA-M sodium bromide Chemical compound [Na+].[Br-] JHJLBTNAGRQEKS-UHFFFAOYSA-M 0.000 description 4
- ARCGXLSVLAOJQL-UHFFFAOYSA-N trimellitic acid Chemical compound OC(=O)C1=CC=C(C(O)=O)C(C(O)=O)=C1 ARCGXLSVLAOJQL-UHFFFAOYSA-N 0.000 description 4
- ZWEHNKRNPOVVGH-UHFFFAOYSA-N 2-Butanone Chemical compound CCC(C)=O ZWEHNKRNPOVVGH-UHFFFAOYSA-N 0.000 description 3
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 3
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 125000003172 aldehyde group Chemical group 0.000 description 3
- 239000007795 chemical reaction product Substances 0.000 description 3
- 239000012043 crude product Substances 0.000 description 3
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 description 3
- 125000001449 isopropyl group Chemical group [H]C([H])([H])C([H])(*)C([H])([H])[H] 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 230000003647 oxidation Effects 0.000 description 3
- 238000007254 oxidation reaction Methods 0.000 description 3
- 238000007086 side reaction Methods 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- IAZDPXIOMUYVGZ-UHFFFAOYSA-N Dimethylsulphoxide Chemical compound CS(C)=O IAZDPXIOMUYVGZ-UHFFFAOYSA-N 0.000 description 2
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 2
- FXHOOIRPVKKKFG-UHFFFAOYSA-N N,N-Dimethylacetamide Chemical compound CN(C)C(C)=O FXHOOIRPVKKKFG-UHFFFAOYSA-N 0.000 description 2
- JUJWROOIHBZHMG-UHFFFAOYSA-N Pyridine Chemical compound C1=CC=NC=C1 JUJWROOIHBZHMG-UHFFFAOYSA-N 0.000 description 2
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 2
- 238000003916 acid precipitation Methods 0.000 description 2
- 150000007513 acids Chemical class 0.000 description 2
- 125000002252 acyl group Chemical group 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- 239000003054 catalyst Substances 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 238000004042 decolorization Methods 0.000 description 2
- 229910001882 dioxygen Inorganic materials 0.000 description 2
- KCIDZIIHRGYJAE-YGFYJFDDSA-L dipotassium;[(2r,3r,4s,5r,6r)-3,4,5-trihydroxy-6-(hydroxymethyl)oxan-2-yl] phosphate Chemical class [K+].[K+].OC[C@H]1O[C@H](OP([O-])([O-])=O)[C@H](O)[C@@H](O)[C@H]1O KCIDZIIHRGYJAE-YGFYJFDDSA-L 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 125000002485 formyl group Chemical group [H]C(*)=O 0.000 description 2
- 229910001385 heavy metal Inorganic materials 0.000 description 2
- 239000000543 intermediate Substances 0.000 description 2
- 150000007524 organic acids Chemical class 0.000 description 2
- 230000001590 oxidative effect Effects 0.000 description 2
- 229910052700 potassium Inorganic materials 0.000 description 2
- 239000002244 precipitate Substances 0.000 description 2
- 239000012266 salt solution Substances 0.000 description 2
- 238000005185 salting out Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000002002 slurry Substances 0.000 description 2
- 229910052708 sodium Inorganic materials 0.000 description 2
- 239000011734 sodium Substances 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- FKOKUHFZNIUSLW-UHFFFAOYSA-N 2-Hydroxypropyl stearate Chemical compound CCCCCCCCCCCCCCCCCC(=O)OCC(C)O FKOKUHFZNIUSLW-UHFFFAOYSA-N 0.000 description 1
- UOBYKYZJUGYBDK-UHFFFAOYSA-N 2-naphthoic acid Chemical compound C1=CC=CC2=CC(C(=O)O)=CC=C21 UOBYKYZJUGYBDK-UHFFFAOYSA-N 0.000 description 1
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 1
- WKBOTKDWSSQWDR-UHFFFAOYSA-N Bromine atom Chemical class [Br] WKBOTKDWSSQWDR-UHFFFAOYSA-N 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- CPLXHLVBOLITMK-UHFFFAOYSA-N Magnesium oxide Chemical class [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 150000001408 amides Chemical class 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- WPYMKLBDIGXBTP-UHFFFAOYSA-N benzoic acid Chemical class OC(=O)C1=CC=CC=C1 WPYMKLBDIGXBTP-UHFFFAOYSA-N 0.000 description 1
- GDTBXPJZTBHREO-UHFFFAOYSA-N bromine Substances BrBr GDTBXPJZTBHREO-UHFFFAOYSA-N 0.000 description 1
- 229910052794 bromium Inorganic materials 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-N carbonic acid Chemical class OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 description 1
- 150000004649 carbonic acid derivatives Chemical class 0.000 description 1
- 125000002915 carbonyl group Chemical group [*:2]C([*:1])=O 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000004040 coloring Methods 0.000 description 1
- HPYNZHMRTTWQTB-UHFFFAOYSA-N dimethylpyridine Natural products CC1=CC=CN=C1C HPYNZHMRTTWQTB-UHFFFAOYSA-N 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 159000000011 group IA salts Chemical class 0.000 description 1
- 150000004679 hydroxides Chemical class 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 150000002576 ketones Chemical class 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000004811 liquid chromatography Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 150000002736 metal compounds Chemical class 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 239000012452 mother liquor Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 235000005985 organic acids Nutrition 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明は、ナフタレンジカルボン酸塩の精製法に関する
。DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a method for purifying naphthalene dicarboxylic acid salts.
[従来の技術]
ナフタレンジカルボン酸く以下、NDCAと略称する)
にはそのカルボニル基の置換位置によって種々の異性体
が存在し、そのうちの幾つかのものはポリマー原料等の
用途に供されており、特にこれらのうち2.6−NDC
へは、物理的、化学的性質に優れたポリエチレン−2,
6−ナフタレート等の製造原料として工業的に有用な化
合物である。[Prior art] Naphthalene dicarboxylic acid (hereinafter abbreviated as NDCA)
There are various isomers depending on the substitution position of the carbonyl group, and some of them are used as polymer raw materials, etc. Among these, 2.6-NDC
Polyethylene-2, which has excellent physical and chemical properties,
It is an industrially useful compound as a raw material for producing 6-naphthalate and the like.
そして、このようなNDCAは、例えば、メチル基、エ
チル基、イソプロピル基等のアルキル基や、ホルミル基
、アシル基等のジ置換ナフタレン又はその酸化中間体を
分子状酸素で酸化する方法や、ヘンケル法等によって製
造されるが、これらの方法で19られたNDCAの粗生
成物中には多くの不純物が含まれており、精製が必要で
ある。Such NDCA can be achieved by, for example, a method of oxidizing an alkyl group such as a methyl group, an ethyl group, an isopropyl group, a di-substituted naphthalene such as a formyl group or an acyl group, or an oxidized intermediate thereof with molecular oxygen, or a method using Henkel. However, the crude NDCA products produced by these methods contain many impurities and require purification.
これを特に工業的に有用な2.6−NDCAについて詳
細に説明すると、以下の通りである。This will be explained in detail with respect to 2.6-NDCA, which is particularly useful industrially, as follows.
すなわち、2.6−NDCへの製造方法としては、アル
キル基としてメチル基、エチル基、イソプロピル基等を
有する2、6−ジアルキルナフタレンをHn、 C。That is, as a method for producing 2.6-NDC, 2,6-dialkylnaphthalene having a methyl group, ethyl group, isopropyl group, etc. as an alkyl group is converted into Hn, C.
等の重金属化合物及びNaBr等の臭素化合物を含む酸
化触媒の存在下に酸化する方法がある。このような方法
で得られた2、6−NDCAの粗生成物中には、着色物
質や反応中間体、副反応物等の不純物が多口に含まれて
おり、例えば樹脂原料等として使用する場合にはその精
製が必要である。そして、これらの不純物の多くは、原
料ジアルキルナフタレン中の2つのアルキル基のうちの
1つがアルデヒド基やカルボキシル基に酸化されたもの
や、1つのアルキル基がカルボキシル基まで酸化され、
伯の1つがアルデヒド基まで酸化されたもの等の反応中
間体、あるいは、トリメリット酸等の副反応物等の有機
化合物である。There is a method of oxidizing in the presence of an oxidation catalyst containing a heavy metal compound such as NaBr and a bromine compound such as NaBr. The crude 2,6-NDCA product obtained by this method contains many impurities such as coloring substances, reaction intermediates, and side reaction products, and cannot be used as a raw material for resins, etc. In some cases, its purification is necessary. In many of these impurities, one of the two alkyl groups in the raw material dialkylnaphthalene has been oxidized to an aldehyde group or a carboxyl group, or one alkyl group has been oxidized to a carboxyl group.
One of the groups is a reaction intermediate such as one oxidized to an aldehyde group, or an organic compound such as a side reaction product such as trimellitic acid.
しかしながら、このような反応によって得られた粗2.
6−NDCAは、これにカリウム、ナトリウム、アンモ
ニウム等のアルカリ水溶液を加えてジアルカリ塩とした
とき、カルボキシル基を有する反応中間体や副反応物の
酸もアルカリ塩となって共に水溶性になり、これらのア
ルカリ塩の水溶液中から単に冷却、濃縮、塩析、酸析等
の方法で2.6−NDCAのジアルカリ塩のみを分離精
製し、不純物を除去して目的物の2.6−NDCAを高
純度で得ることは容易ではない。However, the crude 2.
When 6-NDCA is made into a dialkali salt by adding an aqueous alkali solution of potassium, sodium, ammonium, etc., the reaction intermediate having a carboxyl group and the acid of the side reaction product also become an alkali salt and both become water-soluble. From the aqueous solution of these alkali salts, only the dialkali salt of 2.6-NDCA is separated and purified by methods such as cooling, concentration, salting out, and acid precipitation, and impurities are removed to obtain the target product, 2.6-NDCA. Obtaining high purity is not easy.
また、トリメリット酸等のカルボキシル基を3つ以上有
するベンゼンカルボン酸化合物のアルカリ塩は、水への
溶解性が高く、2.6−NDCAのジアルカリ塩よりも
析出し難いのでその分離は比較的容易であるが、アルキ
ル基の1つのみがアルデヒド基に酸化された有機化合物
等は、アルカリ塩を形成Uず、水に不要なために微細な
粒子として分散し、あるいは、2.6−NDCAのジア
ルカリ塩に付着して存在すると考えられ、この分離は困
難である。In addition, alkali salts of benzenecarboxylic acid compounds having three or more carboxyl groups, such as trimellitic acid, have high solubility in water and are less likely to precipitate than dialkali salts of 2.6-NDCA, so their separation is relatively difficult. Although it is easy to use, organic compounds in which only one alkyl group is oxidized to an aldehyde group do not form alkali salts and are unnecessary in water, so they are dispersed as fine particles or 2.6-NDCA. It is thought that it exists attached to the dialkali salt of , and its separation is difficult.
さらに、2−アルキル−6−カルボキシナフタレンや2
−カルボキシ−〇−ホルミルノーフタレン等の有機化合
物においては、そのアルカリ塩の水に対する溶解性が2
.6−NDCAのジアルカリ塩より低く、容易に析出す
るものと考えられ、これを効率良く除去することは困難
である。Furthermore, 2-alkyl-6-carboxynaphthalene and 2-alkyl-6-carboxynaphthalene
- In organic compounds such as carboxy-〇-formylnophthalene, the solubility of the alkali salt in water is 2.
.. It is thought that it is lower than the dialkali salt of 6-NDCA and precipitates easily, and it is difficult to remove it efficiently.
そこで、このような2.6−NDCAの粗生成物を精製
する方法としては、この2.8−NDCAをジアルカリ
塩水溶液とし、■このジアルカリ塩水溶液を濃縮して飽
和水溶液とした後、冷却してジアルカリ塩を析出させる
方法、■水を蒸発させて濃縮しジアルカリ塩を析出させ
る方法(特開昭48−96.573号公報、特公昭52
−20.994号公報)、■このジアルカリ塩水溶液に
NaCl、に2CO3等の塩を添加して塩析する方法、
等のジアルカリ塩水溶液中から金属塩を析出させる方法
や、ジアルカリ塩水溶液とした債、■I)IIを調節し
ながら酸により酸析する方法(特公昭56−3.858
号)、■CO2等でモノアルカリ塩とする(特公昭52
−20.993号公報)等によりモノアルカリ塩として
析出させ分離する方法等が知られている。Therefore, as a method for purifying such a crude product of 2.6-NDCA, 2.8-NDCA is made into a dialkali salt aqueous solution, 1. This dialkali salt aqueous solution is concentrated to a saturated aqueous solution, and then cooled. (1) Method of precipitating dialkali salt by evaporating water and concentrating it (Japanese Unexamined Patent Publication No. 48-96.573, Japanese Patent Publication No. 52/1986)
-20.994), ■ A method of salting out by adding a salt such as NaCl and 2CO3 to this dialkali salt aqueous solution,
A method of precipitating a metal salt from an aqueous solution of a dialkali salt such as a method of precipitating a metal salt from an aqueous solution of a dialkali salt, and a method of precipitating a metal salt with an acid while adjusting the amount of (i) II
(No.), ■Make monoalkaline salt with CO2 etc. (Special Publication No. 52
20.993), etc., methods of precipitating and separating monoalkaline salts are known.
しかしながら、■及び■の方法には、水の蒸発又は冷却
に多大なエネルギーを要し、温度に対する溶解度差が小
さいという問題があり、■の方法には、塩を固体のまま
添加するとその塩粒子周辺が局部的に高濃度となり、析
出したジアルカリ塩で包み込まれるために不純物が析出
し、純度が向上し雌く、また、塩を飽和水溶液で添加す
る場合にはジアルカリ塩水溶液を飽和水溶液に濃縮する
必要があると共に塩の量が増すという問題があり、■の
方法には、pHを調節しながら酸析するとしても同時に
不純物も析出し易いという問題があり、■の方法には、
工程が複誰でオートクレーブが必要である等の問題点が
あった。However, methods ① and ③ require a large amount of energy to evaporate or cool water, and the solubility difference with respect to temperature is small. The surrounding area becomes locally highly concentrated, and impurities precipitate out because they are surrounded by the precipitated dialkali salt, improving purity.Also, when adding salt as a saturated aqueous solution, the dialkali salt aqueous solution is concentrated to a saturated aqueous solution. There is a problem that the amount of salt increases as well as it is necessary to do so, and method (2) has the problem that impurities are likely to be precipitated at the same time even if acid precipitation is performed while adjusting the pH.
There were problems such as multiple steps and the need for an autoclave.
[発明が解決しようとする課題]
本発明者らは、かかる従来の精製法における問題点を解
決すべく鋭意研究の結果、NDCAのジアルカリ塩水溶
液に水溶性有機溶剤を添加することによって、水の溶解
能を低下させることにより、N0CAのジアルカリ塩を
析出させると共に、粗NDCA中に不純物として存在し
、水に不要な2−アルキル−6−ホルミルナフタレン等
のカルボキシル基を有しない有機化合物や、2−アルキ
ル−6−カルボキシナフタレン等のカルボキシル基を1
つだけしか有しない有機化合物のアルカリ塩等の水に比
較的難溶な有機化合物をその見かけ上容易に水溶液中に
溶解させて析出し難クシ、これによってNDCAのジア
ルカリ塩を選択的に高純度で析出させることができるこ
とを見い出し、本発明を完成した。[Problems to be Solved by the Invention] As a result of intensive research in order to solve the problems in the conventional purification methods, the present inventors found that by adding a water-soluble organic solvent to an aqueous solution of dialkali salt of NDCA, water By lowering the solubility, the dialkali salt of N0CA is precipitated, and organic compounds that do not have a carboxyl group such as 2-alkyl-6-formylnaphthalene, which are present as impurities in crude NDCA and are unnecessary in water, -1 carboxyl group such as alkyl-6-carboxynaphthalene
Organic compounds that are relatively sparingly soluble in water, such as alkaline salts of organic compounds that have only one compound, are apparently easily dissolved in an aqueous solution and difficult to precipitate. The present invention was completed based on the discovery that it can be precipitated using the following methods.
従って、本発明の目的は、種々の方法によって製造され
、種々の不純物を含有する1N()CAを効率良く精製
し、高純度のNDCAを得る方法を提供することにある
。Therefore, an object of the present invention is to provide a method for efficiently refining 1N ()CA produced by various methods and containing various impurities to obtain highly pure NDCA.
[課題を解決するための手段1
すなわち、本発明は、NDCAのジアルカリ塩の水溶液
に、20℃における水への溶解度が100g/100g
−+12o以上の有機溶剤を添加し、NDCAのジアル
カリ塩を析出させる工程を含むナフタレンジカルボン酸
塩の精製法である。[Means for Solving the Problems 1] That is, the present invention provides an aqueous solution of a dialkali salt of NDCA with a solubility in water of 100 g/100 g at 20°C.
This is a method for purifying naphthalene dicarboxylic acid salts, which includes a step of adding an organic solvent of -+12o or higher to precipitate a dialkali salt of NDCA.
本発明方法においてその精製の対象となる粗N0CAは
、例えば、メチル基、エチル基、イソプロピル基等のフ
ルキル基や、ホルミル基、アシル基等を置換基として有
するジ置換ナフタレン又はその酸化中間体を分子状酸素
で酸化することによって得られた粗NDCAや、ヘンケ
ル法により製造された粗NDCへ等であり、好ましくは
数あるNDCAの異性体の中で工業的に特に有用な粗2
.6−NDC八である。なお、ヘンケル法においては反
応中間体であるジアルカリ塩の精製工程で本発明方法が
適用される。The crude NOCA to be purified in the method of the present invention is, for example, a di-substituted naphthalene having a furkyl group such as a methyl group, an ethyl group, an isopropyl group, a formyl group, an acyl group, etc., or an oxidized intermediate thereof. Crude NDCA obtained by oxidation with molecular oxygen, crude NDC produced by the Henkel method, etc., and preferably crude NDCA, which is industrially particularly useful among the many isomers of NDCA.
.. 6-NDC8. In addition, in the Henkel method, the method of the present invention is applied in the purification step of dialkali salt, which is a reaction intermediate.
NDCへの精製工程は、基本的には、■NDCAをジア
ルカリ塩水溶液にする工程、■このNDCAジアルカリ
塩水溶液に水溶性有機溶剤を添加し、NDCAジアルカ
リ塩を析出させ分離する工程、■NDC^NDCAリ塩
からNDCAをMlltさせる工程からなり、ざらに必
要に応じて■と■の工程及び/又は■と■の工程の間に
■固体吸着剤による脱色工程を加えることができる。そ
して、本発明は■の工程に関するものである。The purification process to NDC basically consists of: ■ converting NDCA into a dialkali salt aqueous solution; ■ adding a water-soluble organic solvent to this NDCA dialkali salt aqueous solution to precipitate and separate the NDCA dialkali salt; ■ NDC^ It consists of a step of converting NDCA from NDCA salt, and if necessary, a decolorizing step using a solid adsorbent can be added between the steps (1) and (2) and/or the steps (2) and (2). The present invention relates to the step (2).
■ジアルカリ塩水溶液とせしめる工程
N [)CAの粗生成物にアルカリと水を加えて反応さ
せ、NDCAのジアルカリ塩水溶液にする。(2) Step N of forming a dialkali salt aqueous solution [) Add an alkali and water to the crude product of CA and react to form a dialkali salt aqueous solution of NDCA.
ここで、アルカリとしてはNa、 K 、 N)14等
の水酸化物、炭酸塩ヤHa、に等の炭酸水素塩又はアン
モニアである。これらのアルカリとして良好なものは、
反応速度、溶解度、操作性、価格等の点からNaOH又
はにOHであり、最も良好なものはKO]1である。こ
のアルカリの添加量は粗NDCAの1当記に対して1.
8〜3当量でよい。また、添加する水の爵が多すぎると
、添加する有機溶剤の使用量が多くなって処理mが多く
なり好ましくない。ざらに、溶解速度を増し、操作性を
増すために90℃以下の温度に加熱してもよい。Here, the alkali includes hydroxides such as Na, K, N, etc., hydrogen carbonates such as carbonates, and ammonia. These good alkalis are
From the viewpoints of reaction rate, solubility, operability, cost, etc., NaOH or diOH is preferable, and the best one is KO]1. The amount of this alkali added is 1.
8 to 3 equivalents may be sufficient. On the other hand, if too much water is added, the amount of organic solvent to be added will increase, and the amount of treatment will increase, which is not preferable. Additionally, it may be heated to a temperature below 90° C. to increase the dissolution rate and increase ease of handling.
また、ジアルカリ塩水溶液中に不溶分があればこれを除
去する工程を入れるのが好ましく、あるいは、■の工程
を入れて固体吸着剤と同時に除去してもよい。Furthermore, if there is any insoluble matter in the dialkali salt aqueous solution, it is preferable to include a step to remove it, or alternatively, step (2) may be included to remove it simultaneously with the solid adsorbent.
■水溶性有機溶剤を添加しジアルカリ塩を析出させ分離
する工程
ジアルカリ塩水溶液に添加してNDCAのジアルカリ塩
を析出させるのに使用する水溶性有機溶剤としては、例
えば、メタノール、エタノール、2−プロパツール等の
アルコール類や、アセトン、メチルエチルケトン等のケ
トン類や、N、N−ジメチルホルムアミド、N、N−ジ
メチルアセトアミド等のアミド類や、その他ジメチルス
ルホキシドやピリジン等、有機酸を除く広範な水溶性有
機溶剤を用いることができる。すなわち、有機溶剤は見
かけ上水溶液であれば混合物であってもよく、水に不溶
な有機溶剤を少屋含んでいてもよい。有機溶剤の溶解度
は20℃において100g/100g−u2゜以上であ
ることが必要であり、好ましくは任意の割合で溶解する
のがよい。この有機溶剤を再使用する観点からは、水と
沸点差が5℃以上あるものが好ましく、水よりも低沸点
のものがより好ましい。このような有機溶剤としては、
例えばアセトン、メタノール、エタノール等を挙げるこ
とができる。有機溶剤の使用量は水溶液中のNDCAの
ジアルカリ塩をその10%以上、好ましくは50%以上
析出させるのに必要なωを加えればよく、必要に応じて
この有機溶剤を過剰に使用してもよい。■ Adding a water-soluble organic solvent to precipitate and separate the dialkali salt The water-soluble organic solvent used to precipitate the dialkali salt of NDCA by adding it to the dialkali salt aqueous solution includes, for example, methanol, ethanol, and 2-propanol. Alcohols such as tools, ketones such as acetone and methyl ethyl ketone, amides such as N,N-dimethylformamide, N,N-dimethylacetamide, and other organic acids such as dimethyl sulfoxide and pyridine. Organic solvents can be used. That is, the organic solvent may be a mixture as long as it appears to be an aqueous solution, or may contain an organic solvent that is insoluble in water. The solubility of the organic solvent needs to be 100 g/100 g-u2° or more at 20°C, and preferably it can be dissolved in any proportion. From the viewpoint of reusing the organic solvent, it is preferable that the organic solvent has a boiling point difference of 5° C. or more with water, and it is more preferable that the organic solvent has a boiling point lower than that of water. Such organic solvents include:
Examples include acetone, methanol, ethanol, and the like. The amount of organic solvent to be used is as long as the amount of ω required to precipitate 10% or more, preferably 50% or more of the dialkali salt of NDCA in the aqueous solution, and if necessary, this organic solvent may be used in excess. good.
ジアルカリ塩水溶液は上記工程■で得られた水溶液をそ
のまま用いてもよいが、゛飽和S度近くにしておくこと
が有利である。有機溶剤の添加方法は攪拌下に少量ずつ
添加するのが好ましい。また、この工程に冷却等の操作
を組合わけてもよいが、格別温度差を設けなくてもよい
。Although the dialkali salt aqueous solution obtained in the above step (2) may be used as it is, it is advantageous to keep it close to the saturated S degree. It is preferable to add the organic solvent little by little while stirring. Further, although operations such as cooling may be combined with this step, it is not necessary to provide a particular temperature difference.
このようにして析出させたNDCAのジアルカリ塩の結
晶は、遠心分離、濾過等の適当な手段で分目tすること
ができる。このとき、得られたNDCAのジアルカリ塩
の結晶は、添加したと同じ有機溶剤あるいはその他の水
溶性有機溶剤、水に不要な有機溶剤等の溶剤又はこれら
の混合液、あるいは水を含む混合液等により、リスラリ
−洗浄やリンス洗浄を行い、この結晶中に残留した母液
を除去するのが好ましい。使用した有機溶剤は蒸留等の
適当な手段で回収し、再使用できる。The dialkali salt crystals of NDCA thus precipitated can be separated by suitable means such as centrifugation or filtration. At this time, the obtained dialkali salt crystals of NDCA are mixed with the same organic solvent as added, other water-soluble organic solvents, solvents such as organic solvents unnecessary for water, or mixtures thereof, or mixtures containing water, etc. It is preferable to perform reslurry cleaning or rinsing cleaning to remove the mother liquor remaining in the crystals. The used organic solvent can be recovered by appropriate means such as distillation and reused.
■ジアルカリ塩からNDCAを遊離させる工程ジアルカ
リ塩からNDCAを遊離させるには、NDCAジアルカ
リ塩の結晶を水に溶解させた後、HCI等の鉱酸又は酢
酸等の有機酸を添加すればよい。また、結晶を水に溶解
させたとき、必要に応じて■の工程を入れてもよい。酸
の使用量はジアルカリ塩水溶液のpllが6〜3に達す
るのに必要な量を添加する。析出した結晶は遠心分離、
濾過等の適当な手段で分離する。得られた結晶は水でリ
スラリ−洗浄やリンス洗浄の方法で洗浄し、結晶中の酸
等を除去した後乾燥し、高純度のNDCAを与える。(2) Step of releasing NDCA from dialkali salt To release NDCA from dialkali salt, after dissolving the crystals of NDCA dialkali salt in water, a mineral acid such as HCI or an organic acid such as acetic acid may be added. Further, when the crystals are dissolved in water, step (2) may be added as necessary. The amount of acid used is the amount necessary for the dialkali salt aqueous solution to reach a pll of 6 to 3. The precipitated crystals are centrifuged,
Separate by appropriate means such as filtration. The obtained crystals are washed with water by re-slurry washing or rinsing to remove acids, etc. in the crystals, and then dried to give highly pure NDCA.
■固体吸着剤による脱色工程
この脱色工程は、ジアルカリ塩水溶液に固体吸着剤を添
加し攪拌し、次いでこの固体吸着剤を分離除去する工程
である。固体吸着剤としては、活性炭、活性アルミナ、
活性マグネシア等があり、活性炭が好ましい。使用量は
NDCAの粗生成物に対して0.5〜30重量%でよい
。また、処理方法としては、固体吸着剤の層を通過する
ジアルカリ塩水溶液の流れを形成する方法でもよい。(2) Decolorization step using a solid adsorbent This decolorization step is a step in which a solid adsorbent is added to an aqueous dialkali salt solution, stirred, and then the solid adsorbent is separated and removed. Solid adsorbents include activated carbon, activated alumina,
Examples include activated magnesia, and activated carbon is preferred. The amount used may be from 0.5 to 30% by weight, based on the crude product of NDCA. Alternatively, the treatment method may be a method of forming a flow of an aqueous dialkali salt solution passing through a layer of solid adsorbent.
[実施例]
以下、実施例に基いて、本発明方法を具体的に説明する
。[Example] Hereinafter, the method of the present invention will be specifically explained based on Examples.
なお、実施例中の「部」は「重」部」であり、「%」は
「重母%」である。また、純度は液体クロマトグラフィ
ーによる測定値である。In the examples, "part" means "heavy" part, and "%" means "heavy mass %." Moreover, purity is a value measured by liquid chromatography.
実施例1
2.6−ジイツプロビルナフタレンを重金属及び臭素化
合物を含む酸化触媒の存在下に酸化し、(qられた生成
物を濾過、洗浄、乾燥して粗2.6−NDC^を)qた
。この粗2.6−NDCAは、不純物を含み、濃黄色で
純度95.0%であった。Example 1 2.6-Diituprobylnaphthalene was oxidized in the presence of an oxidation catalyst containing heavy metals and bromine compounds, and the q product was filtered, washed, and dried to yield crude 2.6-NDC^. )qta. This crude 2.6-NDCA contained impurities and was dark yellow in color with a purity of 95.0%.
この租2.6−NDCAI O0部に5%−KOH水溶
液1,150部を加え、攪拌しながら70℃に加熱して
溶解せしめ、活性炭5部を加えて撹拌後濾別した。1,150 parts of a 5% KOH aqueous solution was added to 0 parts of this 2.6-NDCAI O, and heated to 70° C. with stirring to dissolve it. 5 parts of activated carbon was added, stirred, and then filtered.
このようにして得られたジカリウム塩水溶液を300部
を使用し、常温でこれにアセトン450部を添加して2
.6−NDCAジカリウム塩の結晶を析出させた。Using 300 parts of the dipotassium salt aqueous solution obtained in this way, 450 parts of acetone was added to it at room temperature to
.. Crystals of 6-NDCA dipotassium salt were precipitated.
得られたスラリー液を吸引濾過し、ジアルカリ塩の結晶
をアセトン100部でリンス洗浄し、結晶を再び水に溶
解させ、5%−HCIを水溶液のOHが3になるまで添
加し、2.6−N[)CAの結晶を析出させた。The obtained slurry liquid was suction-filtered, the crystals of the dialkali salt were rinsed with 100 parts of acetone, the crystals were dissolved in water again, and 5%-HCI was added until the OH of the aqueous solution reached 3. -N[)CA crystals were precipitated.
このようにして析出させた2、6−NDCAの結晶を吸
引濾過し、水でリスラリ−洗浄、リンス洗浄を行い、結
晶中の酸等を除去した後乾燥し、純白な2゜6−NDC
Aの結晶33部を得た。得られた2、6−NDCAの純
度は99.9%で、その収率は35%であった。The 2,6-NDCA crystals precipitated in this way are suction filtered, re-slurried and rinsed with water to remove acids, etc. in the crystals, and then dried to produce pure white 2゜6-NDCA.
33 parts of crystals of A were obtained. The purity of the obtained 2,6-NDCA was 99.9%, and the yield was 35%.
実施例2
アレトン450部に代えてメタノール700部を使用し
た以外は、実施例1と同様の操作を行い、純白な2.6
−NDCAの結晶62部を得た。得られた2゜6−ND
CAの純度は99.9%で、その収率は65%であった
。Example 2 The same operation as in Example 1 was performed except that 700 parts of methanol was used in place of 450 parts of aretone, and pure white 2.6
-62 parts of NDCA crystals were obtained. Obtained 2゜6-ND
The purity of CA was 99.9% and the yield was 65%.
実施例3
アセトン450部に代えてN、N−ジメチルアセトアミ
ド550部を使用した以外は、実施例1と同様の操作を
行い、純白な2.6−NDCAの結晶83部を得た。得
られた2、 6−NDCAの純度は99.9%で、その
収率は87%であった。Example 3 The same operation as in Example 1 was performed except that 550 parts of N,N-dimethylacetamide was used in place of 450 parts of acetone to obtain 83 parts of pure white 2.6-NDCA crystals. The purity of the obtained 2,6-NDCA was 99.9%, and the yield was 87%.
実施例4
実施例1において、活性炭処理後のジアルカリ塩水溶液
1.200部を濃縮してその仝硲を680部とした後、
この水溶液にアセトン700部を添加して2.6−N[
)CAジアルカリ塩の結晶を析出させ、以後実施例1と
同様の操作を行い、純白な2.6−NDCAの結晶66
.5部を(qだ。得られた2、 6−NDCAのN!度
は99.9%で、その収率は70%であった。Example 4 In Example 1, after concentrating 1.200 parts of dialkali salt aqueous solution after activated carbon treatment to a total volume of 680 parts,
Add 700 parts of acetone to this aqueous solution and add 2.6-N[
) Crystals of CA dialkali salt were precipitated, and the same operations as in Example 1 were performed to obtain pure white 2.6-NDCA crystals 66.
.. The obtained 2,6-NDCA had an N degree of 99.9% and a yield of 70%.
[発明の効果]
本発明方法によれば、種々の不純物を含有する粗ナフタ
レンジカルボン酸を簡便な方法で精製することができ、
しかも、効率良く高純度のナフタレンジカルボン酸を(
qることができる。[Effects of the Invention] According to the method of the present invention, crude naphthalene dicarboxylic acid containing various impurities can be purified by a simple method,
Furthermore, it is possible to efficiently produce high-purity naphthalene dicarboxylic acid (
I can do it.
特許出願人 新日鐵化学株式会社Patent applicant: Nippon Steel Chemical Co., Ltd.
Claims (1)
フタレンジカルボン酸のジアルカリ塩を析出させて精製
するに当り、20℃における水への溶解度が100g/
100g−H_2O以上の有機溶剤を添加し、ナフタレ
ンジカルボン酸のジアルカリ塩を析出させることを特徴
とするナフタレンジカルボン酸塩の精製法。In precipitating and purifying the dialkali salt of naphthalene dicarboxylic acid from an aqueous solution of the dialkali salt of naphthalene dicarboxylic acid, the solubility in water at 20°C is 100 g/
A method for purifying naphthalene dicarboxylic acid salts, which comprises adding 100 g-H_2O or more of an organic solvent to precipitate a dialkali salt of naphthalene dicarboxylic acid.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6344289A JPH02243652A (en) | 1989-03-17 | 1989-03-17 | Method for purifying naphthalenedicarboxylate |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6344289A JPH02243652A (en) | 1989-03-17 | 1989-03-17 | Method for purifying naphthalenedicarboxylate |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH02243652A true JPH02243652A (en) | 1990-09-27 |
Family
ID=13229374
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP6344289A Pending JPH02243652A (en) | 1989-03-17 | 1989-03-17 | Method for purifying naphthalenedicarboxylate |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH02243652A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0787712A1 (en) | 1996-02-05 | 1997-08-06 | Mitsubishi Gas Chemical Company, Inc. | Process for the production of high-purity naphthalenedicarboxylic acid |
CN112679339A (en) * | 2019-10-18 | 2021-04-20 | 中国石油化工股份有限公司 | Method for separating and purifying 2, 6-naphthalenedicarboxylic acid |
CN112679341A (en) * | 2019-10-18 | 2021-04-20 | 中国石油化工股份有限公司 | Separation and purification method of 2, 6-naphthalenedicarboxylic acid |
-
1989
- 1989-03-17 JP JP6344289A patent/JPH02243652A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0787712A1 (en) | 1996-02-05 | 1997-08-06 | Mitsubishi Gas Chemical Company, Inc. | Process for the production of high-purity naphthalenedicarboxylic acid |
CN112679339A (en) * | 2019-10-18 | 2021-04-20 | 中国石油化工股份有限公司 | Method for separating and purifying 2, 6-naphthalenedicarboxylic acid |
CN112679341A (en) * | 2019-10-18 | 2021-04-20 | 中国石油化工股份有限公司 | Separation and purification method of 2, 6-naphthalenedicarboxylic acid |
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