JP2003103103A - Distillation method for easily polymerizable substance and distillation apparatus used for the same - Google Patents

Distillation method for easily polymerizable substance and distillation apparatus used for the same

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Publication number
JP2003103103A
JP2003103103A JP2001304587A JP2001304587A JP2003103103A JP 2003103103 A JP2003103103 A JP 2003103103A JP 2001304587 A JP2001304587 A JP 2001304587A JP 2001304587 A JP2001304587 A JP 2001304587A JP 2003103103 A JP2003103103 A JP 2003103103A
Authority
JP
Japan
Prior art keywords
distillation
reflux
pipe
polymerizable substance
easily polymerizable
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
Application number
JP2001304587A
Other languages
Japanese (ja)
Inventor
Tomoyuki Watabe
知之 渡部
Takayuki Morifuji
崇行 森藤
Hideki Gondo
秀樹 権藤
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Sumitomo Chemical Co Ltd
Original Assignee
Sumitomo Chemical Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Sumitomo Chemical Co Ltd filed Critical Sumitomo Chemical Co Ltd
Priority to JP2001304587A priority Critical patent/JP2003103103A/en
Publication of JP2003103103A publication Critical patent/JP2003103103A/en
Pending legal-status Critical Current

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  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a distillation method which makes the continuous operation of a distillation column possible by reducing the formation of a polymer in performing distillation of an easily polymerizable substance, as represented by a vinyl compound, such as an acrylic acid, and a distillation apparatus used for the same. SOLUTION: In performing distillation while refluxing the easily polymerizable substance, a reflux liquid is made to flow down from an aperture 1b disposed atop a reflux pipe 1 inserted into the distillation column while wetting an external wall surface 1a of the reflux pipe. As a result, the easily polymerizable substance is prevented from concentrating and growing a polymer on the external wall surface of the reflux pipe.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、分子中に二重結合
を有するアクリル酸等のビニル化合物で代表される易重
合性物質の蒸留方法およびこれに使用する蒸留装置に関
する。
TECHNICAL FIELD The present invention relates to a method for distilling a readily polymerizable substance represented by a vinyl compound such as acrylic acid having a double bond in the molecule, and a distillation apparatus used therefor.

【従来の技術】[Prior art]

【0002】易重合性物質は光や熱等によって重合しや
すい性質を有するため、蒸留工程のような高温下ではき
わめて重合しやすくなる。蒸留塔内で重合が生じると、
ロスにつながるのみならず、連続運転に支障を来し、生
産性が低下する。従って易重合性物質の蒸留精製におい
ては、重合防止は非常に重要な技術であり、従来より重
合禁止剤の種類や量や組み合わせ等に関する数多くの重
合防止方法が提案されている。
[0002] Since the easily polymerizable substance has a property of being easily polymerized by light, heat, etc., it is extremely easily polymerized at a high temperature such as a distillation step. When polymerization occurs in the distillation column,
Not only will it lead to loss, but it will also hinder continuous operation and reduce productivity. Therefore, prevention of polymerization is a very important technique in the distillation and purification of the easily polymerizable substance, and many methods for preventing polymerization have been proposed in the past regarding the type, amount, combination and the like of the polymerization inhibitors.

【0003】図3は、易重合性物質の蒸留に通常使用さ
れる蒸留装置を示している。この蒸留装置は、内部にラ
シヒリング等を充填した充填層30、31、32を備え
る蒸留塔、排出された蒸気を凝縮するためのコンデンサ
ー40等からなる。前記蒸留塔において、原料は原料供
給口33、33から塔内に供給される。一方、下部の蒸
気入口34からは蒸気が導入され、原料と向流接触しな
がら上昇し、上部の塔頂部35から排出される。
FIG. 3 shows a distillation apparatus usually used for distilling easily polymerizable substances. This distillation apparatus comprises a distillation column having packed beds 30, 31, 32 filled with Raschig rings and the like, a condenser 40 for condensing discharged vapor, and the like. In the distillation column, the raw material is supplied into the column through the raw material supply ports 33, 33. On the other hand, steam is introduced from the lower steam inlet 34, rises while coming into countercurrent contact with the raw material, and is discharged from the upper tower portion 35 in the upper part.

【0004】排出された蒸気は循環用の配管39を通じ
てコンデンサー40に送られ、冷却水により冷却されて
凝縮液となる。この凝縮液の一部はポンプ41により循
環用の配管42を通じて還流液入口36から還流液とし
て塔内へ供給され、残りは配管43を通じて留出液とし
て回収される。還流液と留出液との比率は調整弁44、
45により調整される。なお、37は缶出液を排出する
缶出液出口で、38は充填物抜き出し等のために設けら
れたマンホールである。
The discharged steam is sent to a condenser 40 through a circulation pipe 39 and cooled by cooling water to become a condensed liquid. A part of this condensate is supplied to the inside of the tower as a reflux liquid from the reflux liquid inlet 36 through the circulation pipe 42 by the pump 41, and the rest is recovered as a distillate liquid through the pipe 43. The ratio of the reflux liquid and the distillate is adjusted by the adjusting valve 44,
Adjusted by 45. Reference numeral 37 is a bottom liquid outlet for discharging the bottom liquid, and 38 is a manhole provided for withdrawing the filling material and the like.

【0005】図5は、前記塔頂部35周辺の蒸留塔内部
の一例を示した概略図である。前記したように、コンデ
ンサー40により冷却された還流液は、還流液入口36
から塔内へ導入され、蒸留塔内部に挿入された還流パイ
プ46の下面に設けられた開口部46bから液分配器4
7に供給される。この液分配器47は、前記還流液を充
填層30の上部から均一に分散供給するために設けられ
たものである。液分配器47に供給された還流液は、矢
印48で示すように、充填物押さえ50を経て充填層3
0に流下する。一方、蒸気入口34(図3)から導入さ
れ、充填層32、31内を上昇してきた蒸気は、矢印4
9で示すように、充填層30において前記還流液と気液
接触する。その後、蒸気は、塔頂部35内をさらに上昇
し、配管39を通じてコンデンサー40に送られる。
FIG. 5 is a schematic view showing an example inside the distillation column around the column top 35. As described above, the reflux liquid cooled by the condenser 40 is supplied to the reflux liquid inlet 36.
Liquid distributor 4 from the opening 46b provided on the lower surface of the reflux pipe 46 that is introduced into the column from the
7 is supplied. The liquid distributor 47 is provided to uniformly disperse and supply the reflux liquid from the upper portion of the packed bed 30. The reflux liquid supplied to the liquid distributor 47 passes through the packing presser 50 as shown by an arrow 48, and the packed bed 3
Run down to zero. On the other hand, the steam introduced from the steam inlet 34 (FIG. 3) and rising in the packed beds 32 and 31 is
As shown in FIG. 9, in the packed bed 30, the reflux liquid is brought into gas-liquid contact. Then, the vapor further rises in the tower top portion 35 and is sent to the condenser 40 through the pipe 39.

【0006】図6は、塔頂部35周辺における蒸留塔内
部の他の一例を示した概略図である。前記したように、
還流液は、還流液入口36から塔内へ導入され、還流パ
イプ51の開口部51bから液分配器47に供給され
る。
FIG. 6 is a schematic view showing another example of the inside of the distillation column around the column top 35. As mentioned above,
The reflux liquid is introduced into the tower through the reflux liquid inlet 36 and is supplied to the liquid distributor 47 through the opening 51 b of the reflux pipe 51.

【0007】上記のような蒸留装置を用いて易重合性物
質の蒸留を行う際に、蒸留塔の塔頂部に還流液を供給す
るための還流パイプにおいて重合物が生成することがあ
った。ここで生成した重合物が落下して液分配器に体積
すると、液分配器に目詰まりが生じるため、還流液を充
填層へ均一に分散供給することが困難となり、充填層内
部の充填物表面に液濡れ性のわるい部分が生じる。前記
したように、通常、還流液には重合禁止剤が添加されて
おり重合を防止する効果が見られるが、液濡れ性のわる
い部分には重合禁止剤がほとんど存在しないため、前記
充填物表面にも容易に重合物が生成する。このように重
合物が生成すると、それが核となって次第に成長蓄積し
て、塔内の圧力を上昇させ、遂には塔内が閉塞されてし
まうことになる。これが製品のロスを増加させるのみな
らず、蒸留塔の連続運転を妨げ生産性を低下させる大き
な要因になっている。また、生成した重合物を除去する
のは非常に困難であり、除去費用は多大となっている。
When the easily polymerizable substance was distilled using the above-mentioned distillation apparatus, a polymer was sometimes produced in the reflux pipe for supplying the reflux liquid to the top of the distillation column. If the polymer generated here falls and accumulates in the liquid distributor, the liquid distributor will be clogged, making it difficult to uniformly distribute and supply the reflux liquid to the packed bed. A part with poor liquid wettability occurs. As described above, usually, a polymerization inhibitor is added to the reflux liquid and the effect of preventing polymerization is seen, but since there is almost no polymerization inhibitor in the poor liquid wettability portion, the filling surface Also, a polymer is easily formed. When the polymer is generated in this manner, it becomes a nucleus and gradually grows and accumulates to increase the pressure in the tower, and finally the inside of the tower is blocked. This not only increases product loss, but also becomes a major factor that impedes continuous operation of the distillation column and reduces productivity. Further, it is very difficult to remove the produced polymer, and the removal cost is great.

【0008】[0008]

【発明が解決しようとする課題】本発明の主たる目的
は、アクリル酸等のビニル化合物に代表される易重合性
物質の蒸留を行うに際して、重合物の生成を低減し、蒸
留塔の連続運転を可能にする蒸留方法を提供することで
ある。本発明の他の目的は、重合物の生成を低減し、蒸
留塔の連続運転を可能にする蒸留装置を提供することで
ある。
SUMMARY OF THE INVENTION The main object of the present invention is to reduce the production of polymer and to continuously operate the distillation column when distilling easily polymerizable substances represented by vinyl compounds such as acrylic acid. It is to provide a distillation method that enables it. Another object of the present invention is to provide a distillation apparatus which reduces the production of polymer and enables continuous operation of the distillation column.

【0009】[0009]

【課題を解決するための手段】本発明者らは、上記課題
を解決すべく鋭意検討を重ねた結果、蒸留塔内で易重合
性物質が重合しやすい箇所は、易重合性物質を含む蒸気
が凝縮して、重合禁止剤が存在しない状態で液溜まりを
つくりやすい部位であることを見出した。また、蒸気
が、塔頂部内を上昇する際に、低温の還流液によって冷
却された還流パイプの外壁面に接触して冷却されること
により、還流パイプ外壁面において蒸気に含まれる易重
合性物質が凝縮することを見出した。これらのことか
ら、蒸留塔内部に挿入された還流パイプの上面に設けた
開口部から還流液を還流パイプの外壁面を濡らしながら
流下させることで、前記易重合性物質を含む蒸気が還流
パイプの外壁面のような重合禁止剤を含む液と接触しに
くい部位で凝縮しないようにすることにより、蒸留塔内
で易重合性物質が重合しやすい箇所の形成を防止できる
ことを見出し、本発明を完成させるに至った。
Means for Solving the Problems As a result of intensive studies to solve the above-mentioned problems, the present inventors have found that a portion of the distillation column where the easily polymerizable substance is easily polymerized is vapor containing the easily polymerizable substance. It has been found that these are sites that are likely to condense and form a liquid pool in the absence of the polymerization inhibitor. Further, when the vapor rises in the top of the tower, the vapor comes into contact with the outer wall surface of the reflux pipe cooled by the low-temperature reflux liquid to be cooled, so that the easily polymerizable substance contained in the vapor on the outer wall surface of the reflux pipe. Have been found to condense. From these, by allowing the reflux liquid to flow down from the opening provided on the upper surface of the reflux pipe inserted inside the distillation column while wetting the outer wall surface of the reflux pipe, the vapor containing the easily polymerizable substance can flow into the reflux pipe. The present invention has been completed by discovering that it is possible to prevent the formation of easily polymerized substances in the distillation column by preventing condensation at the portions that are difficult to contact with the liquid containing the polymerization inhibitor, such as the outer wall surface, and completed the present invention. Came to let.

【0010】すなわち、本発明における易重合性物質の
蒸留方法は、易重合性物質を還流しながら蒸留するに際
して、蒸留塔内部に挿入された還流パイプの上面に設け
た開口部から還流液を還流パイプの外壁面を濡らしなが
ら流下させることを特徴とする。
That is, in the method of distilling the easily polymerizable substance in the present invention, when the easily polymerizable substance is distilled while refluxing, the reflux liquid is refluxed from the opening provided on the upper surface of the reflux pipe inserted inside the distillation column. The feature is that the outer wall surface of the pipe is made to flow down while being wet.

【0011】このように、還流液を還流パイプの上面に
設けた開口部から外壁面を濡らしながら流下させるの
で、還流パイプ外壁面においてアクリル酸等の易重合性
物質が凝縮して重合物が生成するのを防止することがで
きる。
As described above, the reflux liquid is made to flow down from the opening provided on the upper surface of the reflux pipe while wetting the outer wall surface, so that the easily polymerizable substance such as acrylic acid is condensed on the outer wall surface of the reflux pipe to form a polymer. Can be prevented.

【0012】本発明の蒸留装置は、蒸留塔と、この蒸留
塔から排出された蒸気を凝縮するためのコンデンサー
と、これらを繋ぐ循環用配管とを備えた蒸留装置であっ
て、前記配管から蒸留塔内部に挿入された還流パイプの
上面に開口部を設けたことを特徴とし、前記蒸留方法に
おいて好適に使用することができる。
The distillation apparatus of the present invention is a distillation apparatus equipped with a distillation column, a condenser for condensing the vapor discharged from the distillation column, and a circulation pipe connecting these, and distillation is performed from the pipe. It is characterized in that an opening is provided on the upper surface of the reflux pipe inserted into the inside of the column, and can be suitably used in the distillation method.

【0013】[0013]

【発明の実施の形態】本発明の一実施形態を図1に示
す。図1は、本発明の易重合性物質を蒸留するための蒸
留装置における還流パイプ1周辺の構成を示した概略図
である。
BEST MODE FOR CARRYING OUT THE INVENTION One embodiment of the present invention is shown in FIG. FIG. 1 is a schematic diagram showing a configuration around a reflux pipe 1 in a distillation apparatus for distilling an easily polymerizable substance of the present invention.

【0014】図1に示す本発明で使用する還流パイプ1
は、図3に示した内部にラシヒリング等を充填した充填
層30、31、32を備える蒸留塔の塔頂部35内部に
位置するものである。
A reflux pipe 1 used in the present invention shown in FIG.
Is located inside the column top portion 35 of the distillation column provided with the packed layers 30, 31, and 32 in which Raschig rings or the like are filled inside shown in FIG.

【0015】前記したように、蒸気入口34から導入さ
れた蒸気は、充填層30、31、32で原料と向流接触
しながら上昇し、蒸留塔上部の塔頂部35から排出され
る。塔頂部35から排出された蒸気は、コンデンサー4
0により冷却され凝縮液となる。この凝縮液の一部は、
還流液として還流液入口36から塔頂部35へ導入され
る。残りの凝縮液は配管43を通じて留出液として回収
される。
As described above, the vapor introduced from the vapor inlet 34 rises in countercurrent contact with the raw materials in the packed beds 30, 31, 32, and is discharged from the top 35 of the distillation column. The steam discharged from the tower top 35 is stored in the condenser 4
It is cooled by 0 and becomes a condensate. Some of this condensate is
It is introduced as a reflux liquid from the reflux liquid inlet 36 into the column top 35. The remaining condensate is recovered as a distillate through the pipe 43.

【0016】塔頂部35へ導入された還流液は、還流パ
イプ1の上面に設けた開口部1bから還流パイプ外壁面
1aに沿って流下する。この流下した還流液は、液分配
器47に供給され、さらに矢印48で示すように、充填
物押さえ50を経て充填層30に流下する。
The reflux liquid introduced into the tower top 35 flows down along the outer wall surface 1a of the reflux pipe from the opening 1b provided on the upper surface of the reflux pipe 1. The flowing-down reflux liquid is supplied to the liquid distributor 47, and further flows down to the packed bed 30 via the packing presser 50 as shown by an arrow 48.

【0017】図2は、還流パイプ1を示す部分拡大平面
図である。図2において、矢印2は還流液の流れを示
す。還流パイプ1には、複数の穴1bが設けられてお
り、この穴1bから溢れ出した還流液は、矢印2で示す
ように、還流パイプ外壁面1aに沿って流下する。この
ように、還流液が還流パイプ外壁面1aを濡らしながら
流下するので、この外壁面1aにおいてアクリル酸等の
易重合性物質が凝縮して重合物が生成するのを防止する
ことができる。
FIG. 2 is a partially enlarged plan view showing the return pipe 1. In FIG. 2, arrow 2 indicates the flow of reflux liquid. The reflux pipe 1 is provided with a plurality of holes 1b, and the reflux liquid overflowing from the holes 1b flows down along the reflux pipe outer wall surface 1a as shown by an arrow 2. In this way, the reflux liquid flows down while wetting the outer wall surface 1a of the reflux pipe, so that it is possible to prevent condensation of easily polymerizable substances such as acrylic acid on the outer wall surface 1a to form a polymer.

【0018】前記還流パイプ1に設ける穴1bの個数、
穴径、穴間隔等は、還流液によって還流パイプ1のほぼ
全面が濡れるように設定するのが好ましく、還流量、還
流パイプ1のパイプ径、パイプ長さ等を考慮して決定す
ればよい。具体的には、例えば還流パイプ1のパイプ径
は20〜65mm程度、還流パイプ1に設ける穴1bの
穴径はφ1〜3mm程度のものが一般的である。
The number of holes 1b provided in the reflux pipe 1,
It is preferable to set the hole diameter, the hole interval, and the like so that almost all the surface of the reflux pipe 1 is wet with the reflux liquid, and may be determined in consideration of the reflux amount, the pipe diameter of the reflux pipe 1, the pipe length, and the like. Specifically, for example, the diameter of the return pipe 1 is generally about 20 to 65 mm, and the diameter of the hole 1b provided in the return pipe 1 is generally about 1 to 3 mm.

【0019】また、蒸留操作においては、重合防止剤を
還流液に添加してもよい。重合防止剤としては、例えば
ジブチルジチオカルバミン酸金属塩(銅、マンガン等)、
フェノチアジン、メトキノン、ハイドロキノン等の1種
または2種以上が挙げられる。重合防止剤の添加量は、
還流液100重量部に対して約0.005〜0.1重量
部であるのがよい。
In the distillation operation, a polymerization inhibitor may be added to the reflux liquid. Examples of the polymerization inhibitor include dibutyldithiocarbamic acid metal salt (copper, manganese, etc.),
One or more of phenothiazine, metoquinone, hydroquinone and the like can be mentioned. The amount of polymerization inhibitor added is
It may be about 0.005 to 0.1 part by weight per 100 parts by weight of the reflux liquid.

【0020】前記易重合性物質としては、アクリル酸の
他、メタクリル酸等の共役酸またはそのエステル、アミ
ド、ニトリル等の誘導体(アクリル酸メチル、メタクリ
ル酸メチル、アクリルアミド、アクリロニトリル等)、
共役アルデヒドおよびケトン(アクロレイン、メタクロ
レイン、メチルビニルケトン等)、ハロゲン化ビニル
(塩化ビニル等)、ビニル基置換芳香族化合物(スチレ
ン等)、カルボン酸ビニル(酢酸ビニル等)、ビニルエ
ーテル(メチルビニルエーテル等)、1,3―ジオレフ
ィン(ブタジエン、イソプレン等)、エチレンおよびア
ルキル置換エチレン(プロピレン等)が挙げられる。
Examples of the easily polymerizable substance include, in addition to acrylic acid, conjugated acids such as methacrylic acid or derivatives thereof such as esters, amides and nitriles (methyl acrylate, methyl methacrylate, acrylamide, acrylonitrile, etc.),
Conjugated aldehydes and ketones (acrolein, methacrolein, methyl vinyl ketone, etc.), vinyl halides (vinyl chloride, etc.), vinyl group-substituted aromatic compounds (styrene, etc.), vinyl carboxylates (vinyl acetate, etc.), vinyl ethers (methyl vinyl ether, etc.) ), 1,3-diolefins (butadiene, isoprene, etc.), ethylene and alkyl-substituted ethylene (propylene, etc.).

【0021】なお、開口部としては、上記の一実施形態
で示したような複数の穴からなるものに限定されること
はなく、例えばパイプの長手方向に形成されたスリット
などを採用することもできる。また、本発明において
は、図1に示した還流パイプ1に替えて、図4に示すよ
うなラダーパイプ61を使用することもできる。図4は
ラダーパイプ61の平面図である。このラダーパイプ6
1は、主パイプ62と、この主パイプ62から枝分かれ
した複数のパイプ63とからなる。主パイプ62および
パイプ63の上面には複数の開口部64が設けられてい
る。前記主パイプ62の一端から還流液が供給される
と、この還流液は、前記開口部64から主パイプ62お
よびパイプ63の外壁面に沿って流下する。これによ
り、前記還流パイプ1と同様にして、主パイプ62およ
びパイプ63の外壁面において易重合性物質が凝縮して
重合物が生成するのを防止することができる。
The opening is not limited to the one having a plurality of holes as shown in the above embodiment, and for example, a slit formed in the longitudinal direction of the pipe may be adopted. it can. Further, in the present invention, a ladder pipe 61 as shown in FIG. 4 can be used instead of the reflux pipe 1 shown in FIG. FIG. 4 is a plan view of the ladder pipe 61. This ladder pipe 6
Reference numeral 1 includes a main pipe 62 and a plurality of pipes 63 branched from the main pipe 62. A plurality of openings 64 are provided on the upper surfaces of the main pipe 62 and the pipe 63. When the reflux liquid is supplied from one end of the main pipe 62, the reflux liquid flows down from the opening 64 along the outer wall surfaces of the main pipe 62 and the pipe 63. Thereby, similarly to the reflux pipe 1, it is possible to prevent the easily polymerizable substance from condensing on the outer wall surfaces of the main pipe 62 and the pipe 63 to generate a polymer.

【0022】[0022]

【実施例】以下、実施例および比較例を挙げて本発明を
詳細に説明するが、本発明は以下の実施例のみに限定さ
れるものではない。
The present invention will be described in detail below with reference to Examples and Comparative Examples, but the present invention is not limited to the following Examples.

【0023】実施例 アクリル酸を蒸留により精製するために、図1に示すよ
うな上面に開口部が設けられた還流パイプ1を備えた蒸
留装置を用いて長期連続運転を行った。この時、重合防
止剤として少量のフェノチアジンおよびメトキノンを還
流液に添加して運転した。連続運転の間、定期的に充填
層の差圧上昇傾向と、液分配器47、充填物などへの重
合物付着状況とを調べた。
EXAMPLE In order to purify acrylic acid by distillation, long-term continuous operation was carried out using a distillation apparatus equipped with a reflux pipe 1 having an opening on the upper surface as shown in FIG. At this time, a small amount of phenothiazine and metoquinone as polymerization inhibitors were added to the reflux liquid for operation. During the continuous operation, the tendency of increasing the differential pressure of the packed bed and the state of adhesion of the polymer to the liquid distributor 47, the packing, etc. were periodically examined.

【0024】比較例 アクリル酸を蒸留により精製するために、図5に示すよ
うな下面に開口部が設けられた還流パイプ46を備えた
他は、実施例と同様な蒸留装置を用いて長期連続運転を
行い、定期的に充填層の差圧上昇傾向と、液分配器4
7、充填物などへの重合物付着状況とを調べた。
COMPARATIVE EXAMPLE In order to purify acrylic acid by distillation, a distillation pipe similar to that of the embodiment was used except that a reflux pipe 46 having an opening on the lower surface was provided as shown in FIG. The liquid distributor 4 is operated to periodically increase the differential pressure of the packed bed, and the liquid distributor 4
7. The state of adhesion of the polymer to the filler was investigated.

【0025】実施例および比較例の長期連続運転結果を
表1に示す。
Table 1 shows the long-term continuous operation results of Examples and Comparative Examples.

【表1】 [Table 1]

【0026】[0026]

【発明の効果】本発明によれば、還流液を還流パイプの
上面に設けた開口部から外壁面を濡らしながら流下させ
るので、還流パイプ外壁面においてアクリル酸等の易重
合性物質が凝縮して重合物が生成するのを防止すること
ができ、蒸留塔の連続運転が可能になるという効果があ
る。
According to the present invention, the reflux liquid is made to flow down while wetting the outer wall surface from the opening provided on the upper surface of the reflux pipe, so that the easily polymerizable substance such as acrylic acid is condensed on the outer wall surface of the reflux pipe. It is possible to prevent the formation of a polymer, and it is possible to continuously operate the distillation column.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明の一実施形態である蒸留装置に使用する
還流パイプの周辺を示す概略図である。
FIG. 1 is a schematic view showing the periphery of a reflux pipe used in a distillation apparatus which is an embodiment of the present invention.

【図2】本発明の一実施形態である還流パイプを示す部
分拡大平面図である。
FIG. 2 is a partially enlarged plan view showing a reflux pipe which is an embodiment of the present invention.

【図3】蒸留装置を示す概略図である。FIG. 3 is a schematic diagram showing a distillation apparatus.

【図4】ラダーパイプを示す平面図である。FIG. 4 is a plan view showing a ladder pipe.

【図5】従来の蒸留装置に使用する還流パイプの周辺を
示す概略図である。
FIG. 5 is a schematic view showing the periphery of a reflux pipe used in a conventional distillation apparatus.

【図6】従来の蒸留装置に使用する還流パイプの周辺を
示す概略図である。
FIG. 6 is a schematic view showing the periphery of a reflux pipe used in a conventional distillation apparatus.

【符号の説明】[Explanation of symbols]

1 還流パイプ 1a 還流パイプ外壁面 1b 穴 2 還流液の流れ 1 Return pipe 1a Return pipe outer wall surface 1b hole 2 Flow of reflux liquid

───────────────────────────────────────────────────── フロントページの続き (72)発明者 権藤 秀樹 愛媛県新居浜市惣開町5番1号 住友化学 工業株式会社内 Fターム(参考) 4D076 AA07 AA16 AA21 BB04 CA11 JA02 4H006 AA02 AD11 BD82 BS10    ─────────────────────────────────────────────────── ─── Continued front page    (72) Inventor Hideki Gondo             Sumitomo Chemical 5-1, Soukai-cho, Niihama-shi, Ehime             Industry Co., Ltd. F-term (reference) 4D076 AA07 AA16 AA21 BB04 CA11                       JA02                 4H006 AA02 AD11 BD82 BS10

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】易重合性物質を還流しながら蒸留するに際
して、蒸留塔内部に挿入された還流パイプの上面に設け
た開口部から還流液を還流パイプの外壁面を濡らしなが
ら流下させることを特徴とする易重合性物質の蒸留方
法。
1. When distilling the easily polymerizable substance under reflux, the reflux liquid is made to flow down from an opening provided on the upper surface of the reflux pipe inserted in the distillation column while wetting the outer wall surface of the reflux pipe. And method for distilling easily polymerizable substances.
【請求項2】前記開口部が複数の穴からなる請求項1記
載の易重合性物質の蒸留方法。
2. The method for distilling a readily polymerizable substance according to claim 1, wherein the opening comprises a plurality of holes.
【請求項3】前記易重合性物質がビニル化合物である請
求項1または2記載の易重合性物質の蒸留方法。
3. The distillation method for an easily polymerizable substance according to claim 1, wherein the easily polymerizable substance is a vinyl compound.
【請求項4】蒸留塔と、この蒸留塔から排出された蒸気
を凝縮するためのコンデンサーと、これらを繋ぐ循環用
配管とを備えた蒸留装置であって、前記配管から蒸留塔
内部に挿入された還流パイプの上面に開口部を設けたこ
とを特徴とする、請求項1〜3のいずれかに記載の蒸留
方法に使用する蒸留装置。
4. A distillation apparatus comprising a distillation column, a condenser for condensing vapor discharged from the distillation column, and a circulation pipe connecting these, which is inserted into the distillation column through the pipe. The distillation apparatus used in the distillation method according to any one of claims 1 to 3, wherein an opening is provided on the upper surface of the reflux pipe.
JP2001304587A 2001-09-28 2001-09-28 Distillation method for easily polymerizable substance and distillation apparatus used for the same Pending JP2003103103A (en)

Priority Applications (1)

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Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001304587A JP2003103103A (en) 2001-09-28 2001-09-28 Distillation method for easily polymerizable substance and distillation apparatus used for the same

Publications (1)

Publication Number Publication Date
JP2003103103A true JP2003103103A (en) 2003-04-08

Family

ID=19124485

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Country Status (1)

Country Link
JP (1) JP2003103103A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013213028A (en) * 2012-03-07 2013-10-17 Mitsubishi Chemicals Corp Method for producing conjugated diene

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5294453U (en) * 1977-01-12 1977-07-14
JPS5624901U (en) * 1979-07-31 1981-03-06
JPH0747258A (en) * 1993-08-06 1995-02-21 Mitsubishi Corp Liquid distributor for mass and/or heat exchange tower
JPH0824620A (en) * 1994-05-12 1996-01-30 Mitsubishi Corp Liquid distributor for mass and/or heat exchanging tower with at least two liquid flow paths
JPH11226301A (en) * 1998-02-20 1999-08-24 Nippon Shokubai Co Ltd Method and apparatus for distillation
JP2000239228A (en) * 1999-02-17 2000-09-05 Nippon Shokubai Co Ltd Distillation and distillation apparatus

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5294453U (en) * 1977-01-12 1977-07-14
JPS5624901U (en) * 1979-07-31 1981-03-06
JPH0747258A (en) * 1993-08-06 1995-02-21 Mitsubishi Corp Liquid distributor for mass and/or heat exchange tower
JPH0824620A (en) * 1994-05-12 1996-01-30 Mitsubishi Corp Liquid distributor for mass and/or heat exchanging tower with at least two liquid flow paths
JPH11226301A (en) * 1998-02-20 1999-08-24 Nippon Shokubai Co Ltd Method and apparatus for distillation
JP2000239228A (en) * 1999-02-17 2000-09-05 Nippon Shokubai Co Ltd Distillation and distillation apparatus

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013213028A (en) * 2012-03-07 2013-10-17 Mitsubishi Chemicals Corp Method for producing conjugated diene

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