JP2002167363A - Dimethylterephthalate composition - Google Patents
Dimethylterephthalate compositionInfo
- Publication number
- JP2002167363A JP2002167363A JP2000364638A JP2000364638A JP2002167363A JP 2002167363 A JP2002167363 A JP 2002167363A JP 2000364638 A JP2000364638 A JP 2000364638A JP 2000364638 A JP2000364638 A JP 2000364638A JP 2002167363 A JP2002167363 A JP 2002167363A
- Authority
- JP
- Japan
- Prior art keywords
- dmt
- polyester
- dimethyl terephthalate
- recovered
- dimethylterephthalate
- 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
- WOZVHXUHUFLZGK-UHFFFAOYSA-N dimethyl terephthalate Chemical compound COC(=O)C1=CC=C(C(=O)OC)C=C1 WOZVHXUHUFLZGK-UHFFFAOYSA-N 0.000 title claims abstract description 99
- 239000000203 mixture Substances 0.000 title claims description 20
- 238000000034 method Methods 0.000 claims abstract description 17
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims description 54
- 150000001875 compounds Chemical class 0.000 claims description 20
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 claims description 18
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 9
- 229910052799 carbon Inorganic materials 0.000 claims description 9
- 229910052739 hydrogen Inorganic materials 0.000 claims description 7
- 239000001257 hydrogen Substances 0.000 claims description 7
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 6
- 238000004519 manufacturing process Methods 0.000 claims description 3
- YZCKVEUIGOORGS-OUBTZVSYSA-N Deuterium Chemical compound [2H] YZCKVEUIGOORGS-OUBTZVSYSA-N 0.000 claims description 2
- 229910052805 deuterium Inorganic materials 0.000 claims description 2
- 238000002844 melting Methods 0.000 claims description 2
- 230000008018 melting Effects 0.000 claims description 2
- 229920001283 Polyalkylene terephthalate Polymers 0.000 claims 1
- 229920000728 polyester Polymers 0.000 abstract description 24
- URLKBWYHVLBVBO-UHFFFAOYSA-N Para-Xylene Chemical group CC1=CC=C(C)C=C1 URLKBWYHVLBVBO-UHFFFAOYSA-N 0.000 abstract description 10
- 238000005886 esterification reaction Methods 0.000 description 14
- 238000012691 depolymerization reaction Methods 0.000 description 9
- 229920000139 polyethylene terephthalate Polymers 0.000 description 9
- 239000005020 polyethylene terephthalate Substances 0.000 description 9
- 238000006467 substitution reaction Methods 0.000 description 9
- KKEYFWRCBNTPAC-UHFFFAOYSA-N Terephthalic acid Chemical compound OC(=O)C1=CC=C(C(O)=O)C=C1 KKEYFWRCBNTPAC-UHFFFAOYSA-N 0.000 description 8
- -1 Polyethylene terephthalate Polymers 0.000 description 7
- 239000003054 catalyst Substances 0.000 description 7
- 238000004064 recycling Methods 0.000 description 7
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 6
- 238000004821 distillation Methods 0.000 description 5
- 239000007788 liquid Substances 0.000 description 5
- 239000002994 raw material Substances 0.000 description 5
- 238000003756 stirring Methods 0.000 description 5
- 239000000126 substance Substances 0.000 description 5
- 230000032050 esterification Effects 0.000 description 4
- 239000000047 product Substances 0.000 description 4
- 238000000746 purification Methods 0.000 description 4
- 230000015572 biosynthetic process Effects 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- 229910000029 sodium carbonate Inorganic materials 0.000 description 3
- 238000005406 washing Methods 0.000 description 3
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 150000007942 carboxylates Chemical class 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 239000011521 glass Substances 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 230000000155 isotopic effect Effects 0.000 description 2
- 239000011259 mixed solution Substances 0.000 description 2
- 239000000178 monomer Substances 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 239000002002 slurry Substances 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 238000005809 transesterification reaction Methods 0.000 description 2
- KKEYFWRCBNTPAC-RHQRLBAQSA-N 2,3,5,6-tetradeuterioterephthalic acid Chemical compound [2H]C1=C([2H])C(C(O)=O)=C([2H])C([2H])=C1C(O)=O KKEYFWRCBNTPAC-RHQRLBAQSA-N 0.000 description 1
- WJJGAKCAAJOICV-UHFFFAOYSA-N N-dimethyltyrosine Natural products CN(C)C(C(O)=O)CC1=CC=C(O)C=C1 WJJGAKCAAJOICV-UHFFFAOYSA-N 0.000 description 1
- ZVOOGERIHVAODX-UHFFFAOYSA-N O-demycinosyltylosin Natural products O=CCC1CC(C)C(=O)C=CC(C)=CC(CO)C(CC)OC(=O)CC(O)C(C)C1OC1C(O)C(N(C)C)C(OC2OC(C)C(O)C(C)(O)C2)C(C)O1 ZVOOGERIHVAODX-UHFFFAOYSA-N 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 229910052783 alkali metal Inorganic materials 0.000 description 1
- 150000001340 alkali metals Chemical class 0.000 description 1
- 229910052784 alkaline earth metal Inorganic materials 0.000 description 1
- 150000001342 alkaline earth metals Chemical class 0.000 description 1
- QPKOBORKPHRBPS-UHFFFAOYSA-N bis(2-hydroxyethyl) terephthalate Chemical compound OCCOC(=O)C1=CC=C(C(=O)OCCO)C=C1 QPKOBORKPHRBPS-UHFFFAOYSA-N 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 235000014171 carbonated beverage Nutrition 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
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 239000003651 drinking water Substances 0.000 description 1
- 235000020188 drinking water Nutrition 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000010408 film Substances 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000002372 labelling Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- OJURWUUOVGOHJZ-UHFFFAOYSA-N methyl 2-[(2-acetyloxyphenyl)methyl-[2-[(2-acetyloxyphenyl)methyl-(2-methoxy-2-oxoethyl)amino]ethyl]amino]acetate Chemical compound C=1C=CC=C(OC(C)=O)C=1CN(CC(=O)OC)CCN(CC(=O)OC)CC1=CC=CC=C1OC(C)=O OJURWUUOVGOHJZ-UHFFFAOYSA-N 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 229920001707 polybutylene terephthalate Polymers 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 229920002215 polytrimethylene terephthalate Polymers 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 238000001953 recrystallisation Methods 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 238000001228 spectrum Methods 0.000 description 1
- 238000005292 vacuum distillation Methods 0.000 description 1
Landscapes
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、ポリエステルか
ら、エチレングリコールとメタノールを用いて、ポリエ
ステル原料として回収されたテレフタル酸ジメチルと、
パラキシレンから酸化、エステル化反応を経て新たに製
造されたバージンテレフタル酸ジメチルとを、標識化合
物としてテレフタル酸ジメチルの同位体化合物を添加し
均一に分散させ、これを検知することで識別判定する方
法に関する。TECHNICAL FIELD The present invention relates to a dimethyl terephthalate recovered from a polyester as a raw material of a polyester using ethylene glycol and methanol,
A method of discriminating and judging by adding dimethyl terephthalate, which is newly produced through oxidation and esterification from para-xylene, to a dimethyl terephthalate isotope compound as a labeling compound, and uniformly dispersing the compound. About.
【0002】[0002]
【従来の技術】ポリエチレンテレフタレート(以下PE
Tと略称することがある。)は、その化学的安定性が優
れていることから、繊維、フイルム、樹脂などの生活関
連資材、飲料水、炭酸飲料用ボトル等の食品分野などで
の使用が急速に増大している。2. Description of the Related Art Polyethylene terephthalate (hereinafter referred to as PE)
Sometimes abbreviated as T. ) Is rapidly increasing its use in daily life-related materials such as fibers, films and resins, and in the food field such as drinking water and carbonated beverage bottles because of its excellent chemical stability.
【0003】しかしながら、PET使用量の増大に伴っ
て大量に発生する、使用済みPET、あるいはPET製
造段階で発生する品質不適格品の処理は、大きな社会問
題となっている。[0003] However, treatment of used PET, which is generated in large quantities as the amount of used PET increases, or non-qualified products generated at the PET manufacturing stage, is a major social problem.
【0004】上記の問題に対して、ポリエステルをモノ
マーに変換・回収し、このモノマーを原料にして再度重
合反応によってポリエチレンテレフタレートを製造し再
利用する、いわゆるケミカルリサイクルが検討されてい
る。この方法は基本的にロスの無い、化合物の循環再使
用が可能であり、資源の再利用が可能となる。In order to solve the above-mentioned problem, so-called chemical recycling, in which polyester is converted and recovered into a monomer, and the monomer is used as a raw material to produce and reuse polyethylene terephthalate by a polymerization reaction again, is being studied. This method basically enables loss-free recycling of compounds and resource recycling.
【0005】このケミカルリサイクル方法の一つとし
て、ポリエステルをエチレングリコール(以下、EGと
略称することがある。)で解重合反応し、次いでメタノ
ール(以下、MeOHと略称することがある。)を用い
て置換エステル化反応を行い、さらに分離精製すること
でポリエステル製品製造の原料である、高純度のテレフ
タル酸ジメチル(以下、DMTと略称することがあ
る。)及びEGとして精製・回収する方法などが知られ
ている。この方法は、DMTとして精製することで、ポ
リエステルに含まれる添加剤や少量の第3成分との分離
精製が比較的容易となる利点がある。As one of the chemical recycling methods, polyester is depolymerized with ethylene glycol (hereinafter sometimes abbreviated as EG), and then methanol (hereinafter sometimes abbreviated as MeOH) is used. A method for purifying and recovering high-purity dimethyl terephthalate (hereinafter sometimes abbreviated as DMT) and EG, which are raw materials for the production of polyester products, by subjecting them to a substitution esterification reaction followed by separation and purification. Are known. This method has the advantage that by purifying as DMT, it is relatively easy to separate and purify it from additives and a small amount of the third component contained in the polyester.
【0006】特公昭43−2088号公報には、ポリエ
チレンテレフタレートにエチレングリコールを過剰に加
えて加熱し、解重合反応によりビス−β−ヒドロキシエ
チルテレフタレート(以下、BHETと略称することが
ある。)及び低級オリゴマーを得て、該混合物に対し過
剰のメタノールを加え触媒の存在下、置換エステル化反
応することによりDMTを回収する方法が提案されてい
る。In Japanese Patent Publication No. 43-2088, bis-β-hydroxyethyl terephthalate (hereinafter sometimes abbreviated as BHET) and an ethylene glycol are added to polyethylene terephthalate in an excess amount, heated and depolymerized. A method has been proposed in which a lower oligomer is obtained, excess methanol is added to the mixture, and a substitution esterification reaction is performed in the presence of a catalyst to recover DMT.
【0007】上述のようなEG及びMeOHを用いて回
収・精製されたDMT(以下、回収DMTと略称するこ
とがある。)は、高品質であり外観、酸価・凝固点・溶
融比色・硫酸化灰分・含有微量不純物構成といった品質
特性からでは、パラキシレンより新たに得られたDMT
(以下バージンDMTと略称することがある。)と識別
することが困難である。DMT recovered and purified using EG and MeOH as described above (hereinafter sometimes abbreviated as recovered DMT) has high quality, appearance, acid value, freezing point, melting colorimetric, sulfuric acid. Due to its quality characteristics such as ash content and trace impurities, DMT newly obtained from para-xylene
(Hereinafter sometimes abbreviated as “virgin DMT”).
【0008】しかしながら、ポリエステルのケミカルリ
サイクル方法が循環型社会の形成に貢献するには、ポリ
エステルから回収した原料を確実に使用し、再度ポリエ
ステルとして再生させることが重要であり、誤った認識
や用法により、バージンDMTと、回収DMTを混同す
ると循環型社会の形成に支障を来たす可能性も考えられ
る。そこで回収DMTとバージンDMTとを、明確に識
別できる方法が望まれていた。However, in order for the chemical recycling method of polyester to contribute to the formation of a recycling-oriented society, it is important to surely use the raw materials recovered from polyester and to regenerate it as polyester. It is also conceivable that confusion between virgin DMT and recovered DMT may hinder the formation of a recycling-based society. Therefore, there has been a demand for a method capable of clearly distinguishing recovered DMT from virgin DMT.
【0009】[0009]
【発明が解決しようとする課題】本発明の目的は、上記
従来技術の問題点を解決するため、ポリエステルから回
収したDMT中に、識別化合物として炭素及び/又は水
素の同位体から構成されるDMTを微量に添加し、均一
に分散させることで、ポリエステル回収DMTであるこ
とを識別判定する方法を提供することにある。SUMMARY OF THE INVENTION An object of the present invention is to solve the above-mentioned problems of the prior art by providing a DMT composed of carbon and / or hydrogen isotopes as an identification compound in DMT recovered from polyester. A method for discriminating and determining that the DMT is a polyester-recovered DMT by adding a small amount of the DMT and uniformly dispersing the DMT.
【0010】[0010]
【課題を解決するための手段】発明者らは、上記目的を
達成するため、ポリエステルから回収したDMT中に容
易に添加、均一分散化させることができ、添加した識別
化合物を容易に同定、定量でき、かつDMTから製造し
たポリエステルポリマー中でも容易に同定、定量できる
化合物を選定し、これを回収DMT中に微量に添加させ
ることで、識別可能とする方法について鋭意研究を重ね
てきた。Means for Solving the Problems To achieve the above object, the present inventors can easily add and uniformly disperse DMT recovered from polyester, and easily identify and quantitate the added identification compound. We have intensively studied a method for selecting a compound which can be easily identified and quantified even among polyester polymers produced from DMT and which is added in a small amount to the recovered DMT so as to be distinguishable.
【0011】その結果、ポリエステルをエチレングリコ
ールで解重合反応させ、次いでメタノールによる置換エ
ステル化反応を行い、更に精製して得られたDMTを溶
融させ、炭素及び/又は水素の同位体から構成されるD
MTを微量添加し均一に分散化させることで、バージン
DMTとの識別判定が可能であることを見出し、本発明
を完成するに至った。As a result, the polyester is subjected to a depolymerization reaction with ethylene glycol, followed by a substitution esterification reaction with methanol, and the DMT obtained by further purification is melted and is composed of carbon and / or hydrogen isotopes. D
The present inventors have found that it is possible to discriminate and determine virgin DMT by adding a small amount of MT and uniformly dispersing the same, and have completed the present invention.
【0012】即ち、本発明の目的は、ポリエステルから
EG及びMeOHを用いて回収したDMT中に、1〜1
000重量ppm、好ましくは1〜50重量ppmの炭
素及び/又は水素の同位体から構成されるDMT、好ま
しくは炭素の同位体が13Cであり、水素の同位体が重
水素であるDMTの同位体化合物を、識別化合物として
添加させることを特徴とし、これを検知することで、回
収DMTとバージンDMTとの識別判定が可能となる。That is, an object of the present invention is to provide a DMT recovered from a polyester using EG and MeOH in an amount of 1 to 1%.
2,000 ppm by weight, preferably 1-50 ppm by weight, of DMT composed of isotopes of carbon and / or hydrogen, preferably an isotope of DMT wherein the isotope of carbon is 13 C and the isotope of hydrogen is deuterium It is characterized in that a compound is added as a discriminating compound, and by detecting this, discrimination between the recovered DMT and the virgin DMT can be determined.
【0013】[0013]
【発明の実施の形態】以下、本発明を詳細に説明する。BEST MODE FOR CARRYING OUT THE INVENTION Hereinafter, the present invention will be described in detail.
【0014】本発明の識別方法においては、まず、識別
化合物となるDMTの同位体化合物が必要である。DM
Tの同位体化合物の中でも、テレフタル酸−カルボキシ
−13C−ジメチルエステル、テレフタル酸−カルボキシ
−13C2−ジメチルエステル、テレフタル酸−13C6−ジ
メチルエステル、テレフタル酸−d−ジメチルエステ
ル、テレフタル酸−d4−ジメチルエステルからなる群
から選ばれた少なくとも1種の同位体化合物であること
が好ましい。In the identification method of the present invention, first, an isotope compound of DMT as an identification compound is required. DM
Among the isotopic compound T, then terephthalic acid - carboxy - 13 C-dimethyl ester, terephthalic acid - carboxy - 13 C 2 - dimethyl ester, terephthalic acid - 13 C 6 - dimethyl ester, terephthalic acid -d- dimethyl ester, terephthalic acid -d 4 - is preferably at least one isotopic compound selected from the group consisting of dimethyl ester.
【0015】まず、ポリエステルを既知の解重合触媒存
在下、EG中で解重合反応させる。ここでポリエステル
とは、ポリエチレンテレフタレート、ポリトリメチレン
テレフタレート、ポリブチレンテレフタレートである。
解重合反応で得られた混合物は必要であれば、解重合反
応で用いた過剰なEGを抜出し、その後MeOHと共に
反応器内へ導入し、置換エステル化反応、及び冷却晶析
により、粗DMTを得る。更にこの得られた粗DMTを
蒸留精製することにより、高純度のDMTを得ることが
できる。First, a polyester is subjected to a depolymerization reaction in EG in the presence of a known depolymerization catalyst. Here, the polyester is polyethylene terephthalate, polytrimethylene terephthalate, or polybutylene terephthalate.
If necessary, the mixture obtained in the depolymerization reaction is extracted with excess EG used in the depolymerization reaction, then introduced into the reactor together with MeOH, and the crude DMT is subjected to substitution esterification reaction and cooling crystallization. obtain. Furthermore, by distilling and purifying the obtained crude DMT, high-purity DMT can be obtained.
【0016】以上の工程を経て得られた高純度の回収D
MTを140〜170℃の溶融状態に保ち、既知の方法
でDMTの同位体化合物を添加することができ、回分式
と連続式、どちらでも問題なく採用することができる。
例えば、同位体化合物を添加する時の形態としては、同
位体化合物の微粉末状態、あるいは、例えばメタノール
に代表される有機溶媒のスラリー状態とし、添加した
後、攪拌や液循環によりDMT中に均一に分散させる方
法が挙げられる。The high-purity recovered D obtained through the above steps
The MT is kept in a molten state at 140 to 170 ° C., the DMT isotope compound can be added by a known method, and a batch type or a continuous type can be employed without any problem.
For example, when the isotope compound is added, the form is a fine powder of the isotope compound or a slurry state of an organic solvent represented by, for example, methanol. After the addition, the mixture is uniformly mixed in DMT by stirring or liquid circulation. And a method of dispersing them.
【0017】添加したDMTの同位体化合物は、13CN
MR、1HNMR、ガスクロマトグラフ質量分析計等で
分析を行うことで、バージンDMTとの識別判定が可能
となる。The added DMT isotope compound is 13 CN
Analysis by MR, 1 HNMR, gas chromatograph mass spectrometer, or the like makes it possible to determine the discrimination from virgin DMT.
【0018】ポリエステルのEGによる解重合反応は温
度110〜230℃、圧力0.0〜0.2MPa(ゲー
ジ圧)程度であればよく、この範囲である際には、EG
解重合反応が十分行われる。ここで、解重合反応温度が
110℃未満であると、解重合時間が非常に長くなり効
率的でなくなる。一方、230℃を越えると高圧対応の
反応器が必要となり、運転面や安全面から考えると好ま
しくない。The depolymerization reaction of the polyester by EG may be performed at a temperature of about 110 to 230 ° C. and a pressure of about 0.0 to 0.2 MPa (gauge pressure).
The depolymerization reaction is sufficiently performed. Here, if the depolymerization reaction temperature is lower than 110 ° C., the depolymerization time becomes extremely long and the efficiency becomes inefficient. On the other hand, if the temperature exceeds 230 ° C., a reactor corresponding to a high pressure is required, which is not preferable in terms of operation and safety.
【0019】また、MeOHによる置換エステル化反応
を行う際の反応温度としては、50〜150℃の範囲、
反応圧力としては、0.0〜0.59MPa(ゲージ
圧)の範囲とすることが好ましく、この範囲にある際に
は、置換エステル化反応が十分に行われる。なお、置換
エステル化反応時間は30分〜4時間とすることが好ま
しい。The reaction temperature at the time of performing the substitution esterification reaction with MeOH is in the range of 50 to 150 ° C.
The reaction pressure is preferably in the range of 0.0 to 0.59 MPa (gauge pressure), and in this range, the substitution esterification reaction is sufficiently performed. In addition, the substitution esterification reaction time is preferably set to 30 minutes to 4 hours.
【0020】ここで、解重合触媒及び置換エステル化触
媒として既知の解重合触媒及び置換エステル化触媒のい
ずれも用いることができるが、アルカリ金属及びアルカ
リ土類金属の、炭酸塩、炭酸水素塩、及びカルボン酸塩
からなる群から選ばれた少なくとも1種以上の化合物を
用いることが触媒能の高さの面から好ましい。さらに
は、いずれも炭酸ナトリウムを用いることが特に好まし
い。Here, any of known depolymerization catalysts and substituted esterification catalysts as depolymerization catalysts and substituted esterification catalysts can be used, but carbonates, hydrogencarbonates, alkali metal and alkaline earth metals, and the like. It is preferable to use at least one compound selected from the group consisting of carboxylate and carboxylate from the viewpoint of high catalytic ability. Furthermore, it is particularly preferable to use sodium carbonate in all cases.
【0021】この置換エステル化反応で得られた混合物
中には、DMT、MeOH、EG、及びEG解重合反応
と置換エステル化反応での副生成物が存在する。The mixture obtained by the substitution esterification reaction contains DMT, MeOH, EG, and by-products from the EG depolymerization reaction and the substitution esterification reaction.
【0022】この混合物をそのまま用い再結晶操作、あ
るいはDMTの結晶が完全に溶解しない場合は、加熱し
て混合溶液による溶解操作を行う。この際、置換エステ
ル化反応温度をそのまま、若しくは混合物の組成により
温度を60〜150℃の範囲で一度加熱を行った後、1
0〜50℃の範囲に冷却する。必要であれば溶媒の潜熱
を利用し、混合物を冷却することが好ましい。When this mixture is used as it is, a recrystallization operation is performed, or when the DMT crystals are not completely dissolved, a heating operation is performed to dissolve the mixed solution. At this time, after heating once at the substituted esterification reaction temperature as it is or at a temperature in the range of 60 to 150 ° C. depending on the composition of the mixture,
Cool to 0-50 ° C. If necessary, the mixture is preferably cooled using the latent heat of the solvent.
【0023】混合溶液中でのDMT濃度は、10〜40
wt%の範囲とすることが好ましい。DMTの濃度が1
0wt%未満であると、溶媒の使用量が増大し経済的に
好ましくない。The DMT concentration in the mixed solution is 10 to 40.
It is preferable to be in the range of wt%. DMT concentration of 1
If the amount is less than 0 wt%, the amount of the solvent used increases, which is not economically preferable.
【0024】再結晶処理された混合物は、遠心分離操作
などで固液分離し、次いで得られたケークにMeOHを
加え洗浄を行う。The recrystallized mixture is separated into a solid and a liquid by a centrifugal separation operation, and then the obtained cake is washed with MeOH.
【0025】ここで加えるMeOHの量は、DMTに対
して1〜5倍量の範囲であることが洗浄効果、固液スラ
リーのハンドリング性、経済的にも好ましい。また、洗
浄回数は1〜3回が好ましいが、更に洗浄回数を追加し
ても何ら問題は無い。The amount of MeOH added here is preferably in the range of 1 to 5 times the amount of DMT, from the viewpoint of washing effect, handling property of solid-liquid slurry, and economical. Further, the number of times of cleaning is preferably 1 to 3 times, but there is no problem even if the number of times of cleaning is further added.
【0026】MeOH洗浄、固液分離を終えた粗DMT
ケークは加熱、溶融することでMeOHを更に除去後、
最終的に減圧下で蒸留精製を行い、留分として精製DM
Tが取り出される。Crude DMT after MeOH washing and solid-liquid separation
The cake is heated and melted to further remove MeOH,
Finally, distillation and purification were performed under reduced pressure, and purified DM
T is taken out.
【0027】回収DMTの精製における、通常蒸留精製
条件は、5.3〜13.3kPaの減圧下、塔底温度が
170〜250℃、還流比0.1〜2.0で実施され
る。In the purification of the recovered DMT, the distillation is usually carried out under reduced pressure of 5.3 to 13.3 kPa at a bottom temperature of 170 to 250 ° C. and a reflux ratio of 0.1 to 2.0.
【0028】[0028]
【実施例】以下実施例により本発明の内容をさらに具体
的に説明するが本発明はこれにより何等限定を受けるも
のではない。EXAMPLES The contents of the present invention will be described more specifically with reference to the following examples, but the present invention is not limited by these examples.
【0029】なお、DMT中の同位体化合物は、FT−
NMR装置(日本電子(株)製、JEOL A−60
0)を使用して分析を行った。The isotope compound in DMT is FT-
NMR apparatus (JEOL A-60 manufactured by JEOL Ltd.)
The analysis was performed using 0).
【0030】[実施例1]エチレングリコール200部
を500mlセパラブルフラスコに投入し、さらに炭酸
ソーダ1.5部、ポリエチレンテレフタレート50部を
投入し、撹拌速度100rpmで昇温し185℃とし
た。この状態を4時間保持したところ、PETは溶解し
解重合反応が完結した。得られた解重合物を6.65k
Paの減圧蒸留で濃縮し、留分としてEG150部回収
した。Example 1 200 parts of ethylene glycol were charged into a 500 ml separable flask, 1.5 parts of sodium carbonate and 50 parts of polyethylene terephthalate were further charged, and the temperature was raised to 185 ° C. at a stirring speed of 100 rpm. When this state was maintained for 4 hours, the PET was dissolved and the depolymerization reaction was completed. 6.65k of the obtained depolymerized product
The mixture was concentrated by distillation under reduced pressure of Pa, and 150 parts of EG was recovered as a fraction.
【0031】この濃縮液にエステル交換反応触媒として
炭酸ソーダ0.5部とMeOH100部を投入し、常圧
で液温を75℃、撹拌速度100rpmの状態を1時間
保持し、エステル交換反応を実施した。To this concentrated solution, 0.5 part of sodium carbonate and 100 parts of MeOH were introduced as a transesterification catalyst, and the liquid temperature was kept at 75 ° C. and the stirring speed was 100 rpm at normal pressure for 1 hour to carry out the transesterification reaction. did.
【0032】得られた混合物を40℃まで冷却し、ガラ
ス製3G−4のフィルターで濾過した。フィルター上に
回収できた粗DMTを45部のMeOH中に投入し、4
0℃に加温・撹拌洗浄し、再度ガラス製のフィルターで
濾過した。この洗浄は2回繰り返した。この粗DMTを
蒸留装置に仕込み、圧力6.65kPaの減圧蒸留を実
施し、留分としてDMTを得た。留分は40部回収でき
た。釜残を測定しDMT量を測定すると2部であり、投
入したポリエステルを基準にするとDMTの反応率は9
3重量%であった。The resulting mixture was cooled to 40 ° C. and filtered through a glass 3G-4 filter. The crude DMT collected on the filter was put into 45 parts of MeOH,
The mixture was heated to 0 ° C., washed with stirring, and filtered again with a glass filter. This washing was repeated twice. This crude DMT was charged into a distillation apparatus, and vacuum distillation at a pressure of 6.65 kPa was performed to obtain DMT as a fraction. Forty fractions could be collected. The amount of DMT was 2 parts when the residue was measured and the DMT amount was measured, and the DMT reaction rate was 9 based on the charged polyester.
It was 3% by weight.
【0033】蒸留により精製された回収DMT40部を
更に150℃に溶融させ、テレフタル酸−カルボキシ−
13C2−ジメチルエステル2.0×10−3部を添加
し、攪拌速度100rpmで30分間攪拌を行った。The recovered DMT (40 parts) purified by distillation was further melted at 150 ° C., and terephthalic acid-carboxy-
2.0 × 10−3 parts of 13 C 2 -dimethyl ester was added, and the mixture was stirred at a stirring speed of 100 rpm for 30 minutes.
【0034】得られた回収DMTを、13CNMRで分
析すると、テレフタル酸−カルボキシ−13C2−ジメチ
ルエステル由来と考えられるカルボキシル基炭素のシグ
ナル強度が他の炭素のシグナル強度と比較して添加量に
相当する分高く検出され、明らかに既知のDMTスペク
トルとは異なっていた。When the obtained recovered DMT was analyzed by 13 C NMR, the signal intensity of the carboxyl group carbon considered to be derived from terephthalic acid-carboxy- 13 C 2 -dimethyl ester was compared with the signal intensity of the other carbons in the amount added. It was detected correspondingly higher and clearly different from the known DMT spectrum.
【0035】[比較例1]市販品のPXから製造された
バージンDMTについて、13CNMRで分析を行っ
た。その結果、各炭素のシグナル強度が既知のDMT物
性データとほぼ同程度であった。Comparative Example 1 A virgin DMT manufactured from a commercially available product PX was analyzed by 13 C NMR. As a result, the signal intensity of each carbon was almost the same as the known DMT physical property data.
【0036】[0036]
【発明の効果】本発明の識別方法によれば、ポリエステ
ルから回収したテレフタル酸ジメチルと、パラキシレン
から酸化、エステル化反応を経て新たに製造したテレフ
タル酸ジメチルとを容易に識別することができるので、
誤認や誤報の防止に役立ち、ポリエステルより回収した
原料から、再度ポリエステルとして再生する、ケミカル
リサイクル方法による循環型社会の形成に貢献すること
が可能となる。According to the identification method of the present invention, dimethyl terephthalate recovered from polyester can be easily distinguished from dimethyl terephthalate newly produced from para-xylene through oxidation and esterification. ,
It helps prevent misidentification and misinformation, and contributes to the formation of a recycling-oriented society by a chemical recycling method in which raw materials recovered from polyester are regenerated as polyester again.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 佐藤 和広 愛媛県松山市北吉田町77番地 帝人株式会 社松山事業所内 Fターム(参考) 4H006 AA05 AD40 ────────────────────────────────────────────────── ─── Continuing on the front page (72) Inventor Kazuhiro Sato 77 Kitayoshida-cho, Matsuyama-shi, Ehime Prefecture Teijin Limited Matsuyama Office F-term (reference) 4H006 AA05 AD40
Claims (5)
同位体から構成されるテレフタル酸ジメチルを、テレフ
タル酸ジメチルに対し1〜1000重量ppmを含有す
ることを特徴とするテレフタル酸ジメチル組成物。1. A dimethyl terephthalate composition comprising dimethyl terephthalate composed of carbon and / or hydrogen isotopes as an identification compound in an amount of 1 to 1000 ppm by weight based on dimethyl terephthalate.
テレフタル酸ジメチル組成物。2. The dimethyl terephthalate composition according to claim 1, wherein the carbon isotope is 13 C.
のテレフタル酸ジメチル組成物。3. The method according to claim 1, wherein the isotope of hydrogen is deuterium.
Dimethyl terephthalate composition.
ンテレフタレートをエチレングリコールで解重合し、次
いでメタノールでエステル交換反応して得られたテレフ
タル酸ジメチルとする請求項1のテレフタル酸ジメチル
組成物。4. The dimethyl terephthalate composition according to claim 1, wherein the dimethyl terephthalate is obtained by depolymerizing polyalkylene terephthalate with ethylene glycol and then transesterifying with methanol.
れるテレフタル酸ジメチルをテレフタル酸ジメチルに加
え、溶融させて均一に分散させることを特徴とするテレ
フタル酸ジメチル組成物の製造方法。5. A method for producing a dimethyl terephthalate composition, comprising adding dimethyl terephthalate composed of carbon and / or hydrogen isotopes to dimethyl terephthalate, melting and uniformly dispersing the mixture.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2000364638A JP2002167363A (en) | 2000-11-30 | 2000-11-30 | Dimethylterephthalate composition |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2000364638A JP2002167363A (en) | 2000-11-30 | 2000-11-30 | Dimethylterephthalate composition |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JP2002167363A true JP2002167363A (en) | 2002-06-11 |
Family
ID=18835545
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2000364638A Pending JP2002167363A (en) | 2000-11-30 | 2000-11-30 | Dimethylterephthalate composition |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2002167363A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2470008C1 (en) * | 2011-10-05 | 2012-12-20 | Общество с ограниченной ответственностью "Ростхим" | Method of producing (13c2-carbonyl)dimethyl phthalate |
-
2000
- 2000-11-30 JP JP2000364638A patent/JP2002167363A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2470008C1 (en) * | 2011-10-05 | 2012-12-20 | Общество с ограниченной ответственностью "Ростхим" | Method of producing (13c2-carbonyl)dimethyl phthalate |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JP4908415B2 (en) | Method for producing useful components from dyed polyester fiber | |
| TWI865792B (en) | Method for manufacturing bis-(2-hydroxyethyl)terephthalate and method for manufacturing recycled polyethylene terephthalate | |
| KR20020041829A (en) | Method for separating and recovering dimethyl terephthalate and ethylene glycol from polyester waste | |
| JP4537288B2 (en) | Method for recovering active ingredients from dyed polyester fiber | |
| JP6960709B1 (en) | Method for producing high-purity bis- (2-hydroxyethyl) terephthalate, method for purifying regenerated polyethylene terephthalate, decolorizing solvent and bis- (2-hydroxyethyl) terephthalate. | |
| JPH072738A (en) | Separation and recovery method of naphthalene dicarboxylic acid dimethyl ester and terephthalic acid dimethyl ester | |
| JP2004217871A (en) | Method of recovering useful components from dyed polyester fiber | |
| JP6986813B1 (en) | Method for producing bis- (2-hydroxyethyl) terephthalate and method for producing recycled polyethylene terephthalate | |
| AU2005247887B2 (en) | Recycling 2,6-naphthalenedicarboxylic acid (2,6-NDA) contained in polyethylene naphthalate in a process to produce diesters | |
| JP4365592B2 (en) | Method for recovering active ingredients from polyester waste | |
| JP2002167363A (en) | Dimethylterephthalate composition | |
| JP2002060369A (en) | Method for recycling polyester waste | |
| JP2002161064A (en) | Terephthalic acid composition | |
| JP2002167362A (en) | Dimethylterephthalate composition | |
| JP2002060543A (en) | Method for recycling polyester waste | |
| JP2002087999A (en) | Method for recovering effective component from polyester waste | |
| JP4444443B2 (en) | Method for recovering valuable components from polyester waste | |
| JP4002083B2 (en) | Dimethyl terephthalate composition and method for producing the same | |
| JP2002167354A (en) | Terephthalic acid component | |
| JPH10287741A (en) | Method for recovering dimethyl terephthalate from polyalkylene terephthalate | |
| JP2001294553A (en) | Method for recovering valuable component from polyester waste | |
| JP3866872B2 (en) | Method for recovering dimethyl terephthalate | |
| JP4049921B2 (en) | Method for recovering dimethyl naphthalenedicarboxylate | |
| JPH0134257B2 (en) | ||
| JPH04364152A (en) | Method for recovering catalyst |