JP2003103108A - Distillation method for easily polymerizable substance and manhole structure of distillation column - Google Patents
Distillation method for easily polymerizable substance and manhole structure of distillation columnInfo
- Publication number
- JP2003103108A JP2003103108A JP2001304589A JP2001304589A JP2003103108A JP 2003103108 A JP2003103108 A JP 2003103108A JP 2001304589 A JP2001304589 A JP 2001304589A JP 2001304589 A JP2001304589 A JP 2001304589A JP 2003103108 A JP2003103108 A JP 2003103108A
- Authority
- JP
- Japan
- Prior art keywords
- manhole
- distillation column
- polymerizable substance
- distillation
- column
- 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.)
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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
- 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、分子中に二重結合
を有するビニル化合物で代表される易重合性物質の蒸留
方法および易重合性物質の蒸留に用いる蒸留塔のマンホ
ール構造に関する。TECHNICAL FIELD The present invention relates to a distillation method for an easily polymerizable substance represented by a vinyl compound having a double bond in the molecule and a manhole structure of a distillation column used for the distillation of the easily polymerizable substance.
【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4は、易重合性物質の蒸留に通常使用さ
れる蒸留塔を示している。この蒸留塔は、内部に充填物
を充填した充填層30、31が設けられている。原料は
原料供給口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、上部の蒸気出口35から排出される。ま
た、36は還流液入口、37は液出口である。FIG. 4 shows a distillation column normally used for distilling easily polymerizable substances. This distillation column is provided with packed layers 30 and 31 filled with packing. The raw material is supplied from the raw material supply port 33 into the tower. On the other hand, steam is introduced from the lower steam inlet 34, rises in countercurrent contact with the raw material, and is discharged from the upper steam outlet 35. Further, 36 is a reflux liquid inlet, and 37 is a liquid outlet.
【0004】このような蒸留塔においては、充填物抜き
出し等のために複数のマンホール38、39、…44が
設けられている。図5は、このようなマンホールの構造
を示しており、塔の壁面45に取り付けられ壁面45か
ら突出したマンホール胴板46と、このマンホール胴板
46の先端外周に取り付けられたフランジ47と、マン
ホール胴板46の先端開口を塞ぐ蓋部48と、この蓋部
48とフランジ47との間に介在するガスケット49と
からなる。そして、蓋部48およびフランジ47に設け
たボルト挿通孔にボルト50を通し、ナット51と螺合
させ、マンホール胴板46の先端開口を蓋部48で塞
ぐ。蓋部48の表面には取っ手52が取り付けられてい
る。In such a distillation column, a plurality of manholes 38, 39, ... 44 are provided for extracting the packing material and the like. FIG. 5 shows the structure of such a manhole. The manhole body plate 46 is attached to the wall surface 45 of the tower and protrudes from the wall surface 45, the flange 47 attached to the outer periphery of the tip of the manhole body plate 46, and the manhole. It comprises a lid portion 48 that closes the tip end opening of the body plate 46, and a gasket 49 that is interposed between the lid portion 48 and the flange 47. Then, the bolt 50 is passed through the bolt insertion holes provided in the lid portion 48 and the flange 47 and screwed with the nut 51 to close the tip opening of the manhole body plate 46 with the lid portion 48. A handle 52 is attached to the surface of the lid portion 48.
【0005】前記の蒸留装置を用いて易重合性物質の蒸
留を行う際に、前記のマンホール部位において重合物が
生成することがあった。蒸留工程で重合物が生成する
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 distillation apparatus, a polymer was sometimes formed at the manhole site. When a polymer is produced in the distillation step, it becomes a nucleus and gradually grows and accumulates to increase the pressure in the column, which eventually blocks the column. 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.
【0006】[0006]
【発明が解決しようとする課題】本発明の主たる目的
は、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
を可能にする蒸留塔のマンホール構造を提供することで
ある。DISCLOSURE OF THE INVENTION The main object of the present invention is to distill a readily polymerizable substance typified by a vinyl compound, to reduce the production of a polymer and to enable continuous operation of a distillation column. Is to provide a method. Another object of the present invention is to provide a manhole structure of a distillation column which reduces the production of polymer and enables continuous operation of the distillation column.
【0007】[0007]
【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。そして、蒸留
塔に設置されたマンホールを加熱することで、前記易重
合性物質を含む蒸気がマンホール部位のような重合禁止
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. Then, by heating the manhole installed in the distillation column, the vapor containing the easily polymerizable substance is prevented from condensing at a portion such as the manhole portion which is difficult to contact with the liquid containing the polymerization inhibitor, thereby distilling. The inventors have found that it is possible to prevent the formation of a portion where the easily polymerizable substance is easily polymerized in the tower, and have completed the present invention.
【0008】すなわち、本発明の易重合性物質の蒸留方
法は、易重合性物質の蒸留を行うに際して、蒸留塔のマ
ンホールを加熱することを特徴とする。That is, the method for distilling the easily polymerizable substance of the present invention is characterized by heating the manhole of the distillation column when the easily polymerizable substance is distilled.
【0009】重合禁止剤は、通常、還流液に混合して蒸
留塔の塔頂より供給される。重合禁止剤は実質的に不揮
発性であるため、蒸留塔内で蒸気が凝縮して生じる凝縮
液中には重合禁止剤が含まれていない。したがって、凝
縮液は非常に不安定で重合しやすい。この凝縮液は、蒸
留塔上部より流下する重合禁止剤を含む液と接触、混合
されることによって安定化され、重合防止が図られる。
よって、前記の通り、蒸留塔内で蒸気が凝縮して、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
が易重合性物質の重合しやすい部位となる。The polymerization inhibitor is usually mixed with the reflux liquid and supplied from the top of the distillation column. Since the polymerization inhibitor is substantially non-volatile, the polymerization inhibitor is not contained in the condensate generated by the vapor condensation in the distillation column. Therefore, the condensate is very unstable and easy to polymerize. This condensate is stabilized by being contacted with and mixed with a liquid containing a polymerization inhibitor flowing down from the upper part of the distillation column to prevent polymerization.
Therefore, as described above, the site where the vapor is condensed in the distillation column and the liquid is easily accumulated in the absence of the polymerization inhibitor is the site where the easily polymerizable substance is easily polymerized.
【0010】本発明者らは、蒸留塔内で重合が生じる原
因についてさらに鋭意検討した結果、蒸留塔のマンホー
ル部は図5に示すように、塔内空間から凸状に突出して
おり、かつ当該突出部53では外気の影響を受けて冷却
されるため、易重合性物質を含む蒸気が凝縮しやすいこ
と、およびマンホール部は重合禁止剤を含む還流液と接
触しにくいため、マンホール部での凝縮液は非常に不安
定で、重合物が生成しやすいことを見出した。本発明で
は、前記の通り、蒸留塔のマンホールを加熱して放熱量
以上の熱量を蒸気に与えることで、易重合性物質を含む
蒸気の冷却を防止する。これにより、蒸留塔のマンホー
ル部のような重合禁止剤を含む還流液と接触しにくく、
非常に重合しやすい部位での易重合性物質の凝縮を防止
することができ、前記部位での重合を防止することがで
きる。As a result of further studies on the cause of the polymerization in the distillation column, the present inventors have found that the manhole part of the distillation column is convexly projected from the space inside the column as shown in FIG. Since the projecting portion 53 is cooled by the influence of the outside air, the vapor containing the easily polymerizable substance is likely to condense, and the manhole portion is less likely to come into contact with the reflux liquid containing the polymerization inhibitor, so that the manhole portion is condensed. It was found that the liquid is very unstable and a polymer is easily generated. In the present invention, as described above, the manhole of the distillation column is heated to give the steam a heat amount equal to or more than the heat radiation amount, thereby preventing the steam containing the easily polymerizable substance from being cooled. This makes it difficult to contact the reflux liquid containing the polymerization inhibitor like the manhole part of the distillation column,
It is possible to prevent condensation of the easily polymerizable substance at the site where polymerization is very easy, and prevent polymerization at the site.
【0011】本発明の蒸留方法では、前記マンホール部
の温度を、好ましくは塔内温度以上に、より好ましくは
塔内温度より高い温度で、かつ塔内温度から100℃を
越えない温度範囲に加熱するのがよい。これにより、マ
ンホール部で易重合性物質が凝縮して重合するのを防止
できる。In the distillation method of the present invention, the manhole temperature is preferably heated to a temperature higher than the temperature inside the column, more preferably higher than the temperature inside the column, and within a temperature range not exceeding 100 ° C. from the temperature inside the column. Good to do. This can prevent the easily polymerizable substance from condensing and polymerizing in the manhole portion.
【0012】本発明の蒸留塔のマンホール構造は、易重
合性物質の蒸留を行う蒸留塔に設けられるマンホールの
構造であって、蒸留塔の壁面に取り付けられ壁面から突
出したマンホール胴板と、前記マンホール胴板の先端開
口を塞ぐ蓋部と、前記マンホールに設けられたマンホー
ル胴板および/または蓋部を加熱するための加熱手段と
を備えたことを特徴とする。The manhole structure of the distillation column of the present invention is the structure of the manhole provided in the distillation column for distilling the easily polymerizable substance. The manhole body plate is attached to the wall of the distillation column and protrudes from the wall, It is characterized in that it is provided with a lid portion that closes the front end opening of the manhole body plate, and a heating means for heating the manhole body plate and / or the lid portion provided in the manhole.
【0013】前記加熱手段としては、前記マンホールの
胴板および/または蓋部の外表面に熱媒体を通すトレー
ス配管を接触させたものや前記マンホールの胴板および
/または蓋部の外表面に加熱ジャケットを設けたものが
好適である。As the heating means, the outer surface of the body plate and / or the lid portion of the manhole is brought into contact with a trace pipe for passing a heat medium, or the outer surface of the body plate and / or the lid portion of the manhole is heated. A jacket is preferable.
【0014】[0014]
【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はこの実施形態にかかるマンホール構造を示す
分解断面図である。BEST MODE FOR CARRYING OUT THE INVENTION One embodiment of the present invention is shown in FIG. FIG. 1 is an exploded sectional view showing a manhole structure according to this embodiment.
【0015】図1に示すマンホールは、前記した易重合
性物質の蒸留を行う蒸留塔に設けられたものである。蒸
留塔の塔壁1に設けられた開口部2の外側周縁には、円
筒状のマンホール胴板3が溶接等によって一体に取り付
けられている。このマンホール胴板3の先端外周にはフ
ランジ4が溶接等によって取り付けられている。このフ
ランジ4と蓋部5との間にはガスケット6が介在し、フ
ランジ4および蓋部5に設けたボルト挿通孔にボルト7
を通し、ナット8と螺合させ、マンホール胴板3の先端
開口を蓋部5で塞いでいる。蓋部5の表面には取っ手9
が取り付けられている。The manhole shown in FIG. 1 is provided in a distillation column for distilling the above-mentioned easily polymerizable substance. A cylindrical manhole body plate 3 is integrally attached to the outer peripheral edge of the opening 2 provided in the column wall 1 of the distillation column by welding or the like. A flange 4 is attached to the outer periphery of the tip of the manhole body plate 3 by welding or the like. A gasket 6 is interposed between the flange 4 and the lid 5, and a bolt 7 is inserted in a bolt insertion hole provided in the flange 4 and the lid 5.
Through, and is screwed with the nut 8 to close the front end opening of the manhole body plate 3 with the lid portion 5. A handle 9 is provided on the surface of the lid 5.
Is attached.
【0016】前記マンホール胴板3には、熱媒体を通す
トレース配管10が螺旋状に巻き付けられている。必要
に応じて、マンホール蓋部にもトレース配管を設置して
も良い。熱媒体は供給口10aから供給され、排出口1
0bから排出される。必要に応じて供給口と排出口を逆
にして使用しても良い。このトレース配管10内の熱媒
体からマンホール胴板3に伝わる熱により、マンホール
胴板3は少なくとも塔内温度とほぼ等しい温度ないしは
塔内温度より高い温度に維持され、好ましくは塔内温度
より高い温度、より好ましくは塔内温度より高い温度
で、かつ塔内温度から100℃を越えない温度範囲、さ
らに好ましくは塔内温度より高い温度で、かつ塔内温度
から20℃を越えない温度範囲に維持される。これによ
り、マンホール部で易重合性物質が凝縮するのを防ぐこ
とができる。マンホール胴板3の温度が塔内温度より過
剰に高い温度範囲で長期間連続運転を行うと、エネルギ
ー的にも不利であり、重合禁止剤及び付着した重合物が
焦げるといった不具合が生じることがあるので好ましく
ない。A trace pipe 10 for passing a heat medium is spirally wound around the manhole body plate 3. If necessary, trace piping may be installed on the manhole cover. The heat medium is supplied from the supply port 10a, and the discharge port 1
It is discharged from 0b. If necessary, the supply port and the discharge port may be reversed and used. Due to the heat transmitted from the heat medium in the trace pipe 10 to the manhole body plate 3, the manhole body plate 3 is maintained at a temperature substantially equal to or higher than the tower temperature, preferably higher than the tower temperature. More preferably, the temperature is higher than the temperature inside the column, and is maintained within a temperature range not exceeding 100 ° C from the temperature inside the column, and more preferably, is higher than the temperature inside the column, and is more preferably maintained within a temperature range not exceeding 20 ° C from the temperature inside the column. To be done. This can prevent the easily polymerizable substance from condensing in the manhole portion. If continuous operation is performed for a long period of time in a temperature range in which the temperature of the manhole body plate 3 is excessively higher than the temperature inside the tower, it is disadvantageous in terms of energy, and a problem may occur such that the polymerization inhibitor and the attached polymer are burnt. It is not preferable.
【0017】前記トレース配管10に通す熱媒体として
は、温水、スチーム、オイル等が使用できる。As the heat medium passed through the trace pipe 10, hot water, steam, oil or the like can be used.
【0018】図2は本発明の他の実施形態にかかるマン
ホール構造の概略を示す分解断面図である。図2に示す
蒸留塔の塔壁11に設けられた開口部12の外側周縁に
は、円筒状のマンホール胴板13が溶接等によって一体
に取り付けられている。このマンホール胴板13の外側
には熱媒体(前記した温水、スチーム、オイル等)を通
す加熱ジャケット15が付設されている。必要に応じ
て、マンホール蓋部にも加熱ジャケットを設置しても良
い。加熱ジャケット15の表面には、熱媒体の供給口1
5aおよび排出口15bがそれぞれ設けられている。必
要に応じて供給口と排出口を逆にして使用しても良い。
この加熱ジャケット15内の熱媒体からマンホール胴板
13に伝わる熱により、マンホール胴板13は少なくと
も塔内温度とほぼ等しい温度ないしは塔内温度より高い
温度に維持され、好ましくは塔内温度より高い温度、よ
り好ましくは塔内温度より高い温度で、かつ塔内温度か
ら100℃を越えない温度範囲、さらに好ましくは塔内
温度より高い温度で、かつ塔内温度から20℃を越えな
い温度範囲に維持される。FIG. 2 is an exploded sectional view schematically showing a manhole structure according to another embodiment of the present invention. A cylindrical manhole body plate 13 is integrally attached by welding or the like to the outer peripheral edge of the opening 12 provided in the column wall 11 of the distillation column shown in FIG. On the outside of the manhole body plate 13, a heating jacket 15 through which a heat medium (hot water, steam, oil, etc. described above) passes is attached. If desired, a heating jacket may be installed on the manhole cover. On the surface of the heating jacket 15, a heat medium supply port 1
5a and a discharge port 15b are provided respectively. If necessary, the supply port and the discharge port may be reversed and used.
Due to the heat transmitted from the heat medium in the heating jacket 15 to the manhole shell plate 13, the manhole shell plate 13 is maintained at a temperature substantially equal to or higher than the tower internal temperature, preferably higher than the tower internal temperature. More preferably, the temperature is higher than the temperature inside the column and is maintained within a temperature range not exceeding 100 ° C. from the temperature inside the column, and more preferably, is maintained at a temperature higher than the temperature inside the column and not exceeding 20 ° C. from the temperature inside the column. To be done.
【0019】前記加熱ジャケット15の先端外周にはフ
ランジ14が溶接等によって取り付けられている。この
フランジ14と蓋部5との間にはガスケット6が介在
し、フランジ14および蓋部5に設けたボルト挿通孔に
ボルト7を通し、ナット8と螺合させ、マンホール胴板
13の先端開口を蓋部5で塞いでいる。蓋部5の表面に
は取っ手9が取り付けられている。A flange 14 is attached to the outer periphery of the end of the heating jacket 15 by welding or the like. A gasket 6 is interposed between the flange 14 and the lid 5, and a bolt 7 is passed through a bolt insertion hole provided in the flange 14 and the lid 5 and screwed with a nut 8 to open the tip opening of the manhole body plate 13. Is covered with the lid 5. A handle 9 is attached to the surface of the lid 5.
【0020】図3は本発明のさらに他の実施形態にかか
るマンホール構造を示す分解断面図である。FIG. 3 is an exploded sectional view showing a manhole structure according to still another embodiment of the present invention.
【0021】図3に示すマンホールは、前記した易重合
性物質の蒸留を行う蒸留塔に設けられたものである。す
なわち、蒸留塔の塔壁1に設けられた開口部2の外側周
縁には、円筒状のフランジ部21が溶接等によって一体
に取付けられる。フランジ部21の表面には、その周方
向に沿って適宜な間隔で複数の立て込みボルト22が立
設されている。The manhole shown in FIG. 3 is provided in a distillation column for distilling the above-mentioned easily polymerizable substance. That is, a cylindrical flange portion 21 is integrally attached to the outer peripheral edge of the opening 2 provided in the column wall 1 of the distillation column by welding or the like. On the surface of the flange portion 21, a plurality of standing bolts 22 are provided upright along the circumferential direction at appropriate intervals.
【0022】フランジ部21の表面には蓋部23の周縁
内面がガスケット27を介して当接し、前記蒸留塔の開
口部2を塞いでいる。蓋部23は円形の板状体である。
蓋部23の上面には熱媒体(温水等)を通す加熱ジャケ
ット24が付設される。加熱ジャケット24の表面に
は、熱媒体の供給口24aおよび排出口24bがそれぞ
れ設けられる。加熱ジャケット24により、蓋部23は
少なくとも塔内温度とほぼ等しい温度ないしは塔内温度
より高い温度に維持され、好ましくは塔内温度より高い
温度、より好ましくは塔内温度より高い温度で、かつ塔
内温度から100℃を越えない温度範囲、さらに好まし
くは塔内温度より高い温度で、かつ塔内温度から20℃
を越えない温度範囲に維持される。蓋部23の温度が塔
内温度よりも低い場合には、凝縮した液が蓋部23に付
着して重合物や凝結物が蓄積しやすくなる。The inner surface of the peripheral edge of the lid portion 23 abuts on the surface of the flange portion 21 via a gasket 27 to close the opening 2 of the distillation column. The lid 23 is a circular plate-shaped body.
A heating jacket 24 for passing a heat medium (hot water or the like) is attached to the upper surface of the lid portion 23. A heating medium supply port 24a and a heating medium discharge port 24b are provided on the surface of the heating jacket 24, respectively. The heating jacket 24 maintains the lid portion 23 at least at a temperature substantially equal to or higher than the temperature inside the column, preferably higher than the temperature inside the column, more preferably higher than the temperature inside the column, and more preferably higher than the temperature inside the column. Temperature range from the internal temperature to not exceeding 100 ° C, more preferably at a temperature higher than the internal temperature and from the internal temperature to 20 ° C
Is maintained within a temperature range not exceeding When the temperature of the lid portion 23 is lower than the temperature in the tower, the condensed liquid adheres to the lid portion 23, and the polymerized material and the condensed material are likely to accumulate.
【0023】また、前記蓋部23の周縁には、前記立て
込みボルト22に対応するボルト挿通孔25が設けられ
る。そして、このボルト挿通孔25を挿通して突出した
前記フランジ部21の立て込みボルト22にナット26
が螺合される。これにより、蓋部23をフランジ部21
の表面に圧接固定することができる。なお、蓋部23の
内面および/またはフランジ部の表面にはライニングが
施されているのが好ましい。A bolt insertion hole 25 corresponding to the stand-up bolt 22 is provided on the peripheral edge of the lid portion 23. Then, the nut 26 is attached to the stand-up bolt 22 of the flange portion 21 which is projected by being inserted through the bolt insertion hole 25.
Are screwed together. As a result, the lid portion 23 is replaced with the flange portion 21.
It can be pressed and fixed to the surface of. In addition, it is preferable that the inner surface of the lid portion 23 and / or the surface of the flange portion be lined.
【0024】以上のように、本発明では、トレース配管
10や加熱ジャケット15を設けることでマンホール胴
板および/または蓋部が塔内温度より高い温度に維持さ
れている。これにより、マンホール部で易重合性物質の
蒸気が凝縮して液溜まりをつくることがないため、重合
物が生成するのを防止することができる。As described above, in the present invention, by providing the trace pipe 10 and the heating jacket 15, the manhole body plate and / or the lid portion is maintained at a temperature higher than the temperature inside the tower. As a result, the vapor of the easily polymerizable substance does not condense to form a liquid pool in the manhole portion, and thus it is possible to prevent the generation of the polymer.
【0025】本発明のマンホール構造は、図4に示すよ
うな通常の蒸留塔に適用され、特に重合の激しい充填物
抜出し用マンホールに使用するのに好適である。また、
蒸留操作においては、重合禁止剤を還流液や供給液に添
加して供給してもよい。重合禁止剤としては、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。The manhole structure of the present invention is applied to an ordinary distillation column as shown in FIG. 4, and is particularly suitable for use as a manhole for discharging a packing which undergoes severe polymerization. Also,
In the distillation operation, the polymerization inhibitor may be added to the reflux liquid or the supply liquid and supplied. Examples of the polymerization inhibitor include one kind or two or more kinds of metal salts of dibutyldithiocarbamic acid (copper, manganese, etc.), phenothiazine, methoquinone, hydroquinone and the like.
【0026】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, 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.).
【0027】なお、マンホール胴板3の加熱手段として
は、前記したトレース配管10に代えて、電気ヒータ等
の他の加熱手段を採用してもよい。As the heating means for the manhole body plate 3, other heating means such as an electric heater may be adopted instead of the trace pipe 10 described above.
【0028】[0028]
【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.
【0029】実施例1
アクリル酸を蒸留するための図4に示すような蒸留塔に
おいて、充填物抜出し用マンホールを図1に示すような
構造に変更し、長期連続運転を行った。この蒸留装置は
理論段6段相当の充填塔であり、塔頂圧力55tor
r、留出率80%、還流比0.8の条件で運転を行っ
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、缶部液層部に空気を
一定量供給して運転した。トレース配管10に温水を通
水し、マンホール胴板3を塔内温度よりも2〜5℃高い
温度である74〜77℃に維持した。連続運転の間、定
期的に蒸留塔内の圧力上昇傾向とマンホールへの重合物
付着状況とを調べた。Example 1 In a distillation column for distilling acrylic acid as shown in FIG. 4, the packing extraction manhole was changed to the structure as shown in FIG. 1, and long-term continuous operation was performed. This distillation apparatus is a packed column equivalent to 6 theoretical plates, and the top pressure is 55 torr.
The operation was performed under the conditions of r, a distillation rate of 80%, and a reflux ratio of 0.8. At this time, a small amount of phenothiazine and metoquinone as polymerization inhibitors were added to the reflux liquid, and a constant amount of air was supplied to the liquid portion of the can portion for operation. Hot water was passed through the trace pipe 10, and the manhole body plate 3 was maintained at 74 to 77 ° C, which is a temperature 2 to 5 ° C higher than the temperature inside the tower. During the continuous operation, the tendency of pressure increase in the distillation column and the state of adhesion of the polymer to the manhole were periodically examined.
【0030】実施例2
トレース配管10に温水を通水し、マンホール胴板3を
塔内温度よりも20℃高い温度である92℃に維持した
他は、実施例1と同様にして長期連続運転を行った。連
続運転の間、定期的に蒸留塔内の圧力上昇傾向とマンホ
ールへの重合物付着状況とを調べた。Example 2 Long-term continuous operation was carried out in the same manner as in Example 1 except that hot water was passed through the trace pipe 10 and the manhole shell plate 3 was maintained at 92 ° C. which was 20 ° C. higher than the temperature inside the tower. I went. During the continuous operation, the tendency of pressure increase in the distillation column and the state of adhesion of the polymer to the manhole were periodically examined.
【0031】比較例
図4に示すマンホールを備えた図4に示すような蒸留塔
を用いた他は、実施例1と同様にして長期連続運転を行
った。連続運転の間、定期的に蒸留塔内の圧力上昇傾向
とマンホールへの重合物付着状況とを調べた。Comparative Example A long-term continuous operation was carried out in the same manner as in Example 1 except that the distillation column shown in FIG. 4 equipped with the manhole shown in FIG. 4 was used. During the continuous operation, the tendency of pressure increase in the distillation column and the state of adhesion of the polymer to the manhole were periodically examined.
【0032】実施例1、実施例2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 1, 2 and Comparative Example.
【表1】 [Table 1]
【0033】実施例1について
長期連続運転の結果、3ヶ月経過時点で、蒸留塔内の圧
力が上昇し始めた。また、目視観察の結果、僅かに重合
物が生成していたものの、蓋部5は容易に開けることが
できた。
実施例2について
長期連続運転の結果、4ヶ月経過時点でも蒸留塔内の圧
力上昇は見られなかった。また、目視観察の結果、重合
物の生成は見られず、蓋部5は容易に開けることができ
た。
比較例について
長期連続運転の結果、2ヶ月経過時点で蒸留塔内の圧力
が上昇し始めた。また、マンホールへ重合物が蓄積した
ことにより、マンホールの蓋部5は治具なしでは開ける
ことができない状態になっていた。As a result of the long-term continuous operation of Example 1, the pressure in the distillation column started to rise after 3 months. Further, as a result of visual observation, although the polymer was slightly produced, the lid 5 could be easily opened. As a result of long-term continuous operation of Example 2, no pressure increase in the distillation column was observed even after 4 months. In addition, as a result of visual observation, no production of a polymer was found, and the lid 5 could be easily opened. As a result of long-term continuous operation of the comparative example, the pressure in the distillation column started to rise after 2 months. Further, since the polymer was accumulated in the manhole, the manhole cover 5 could not be opened without a jig.
【0034】以上のように、蒸留塔のマンホールを塔内
温度以上に加熱することによって、重合物の生成が抑制
されることがわかった。As described above, it was found that by heating the manhole of the distillation column to a temperature equal to or higher than the internal temperature of the column, the production of the polymer is suppressed.
【0035】[0035]
【発明の効果】本発明によれば、マンホール胴板および
/または蓋部にトレース配管、加熱ジャケット等の加熱
手段を設けることでマンホール胴板および/または蓋部
を塔内温度以上の温度に維持できるため、易重合性物質
を含む蒸気が前記部位において凝縮するのを防止するこ
とができる。マンホール部では重合禁止剤を含む還流液
と接触しにくいため易重合性物質を含む蒸気が凝縮する
と非常に不安定で重合しやすくなるが、本発明では前記
の通り、易重合性物質を含む蒸気が凝縮するのを防止す
ることができるため、マンホールでの重合物の生成が低
減され、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 manhole body plate and / or the lid portion is provided with a heating means such as a trace pipe and a heating jacket to maintain the manhole body plate and / or the lid portion at a temperature higher than the temperature in the tower. Therefore, it is possible to prevent the vapor containing the easily polymerizable substance from condensing at the site. In the manhole part, since it is difficult to contact with the reflux liquid containing the polymerization inhibitor, the vapor containing the easily polymerizable substance is very unstable and easily polymerized, but in the present invention, as described above, the vapor containing the easily polymerizable substance is vaporized. Since it can be prevented from condensing, the production of the polymer in the manhole is reduced, and the distillation column can be continuously operated.
【図1】本発明の一実施形態であるマンホール構造を示
す分解断面図である。FIG. 1 is an exploded cross-sectional view showing a manhole structure according to an embodiment of the present invention.
【図2】本発明の他の実施形態であるマンホール構造の
概略を示す分解断面図である。FIG. 2 is an exploded sectional view schematically showing a manhole structure according to another embodiment of the present invention.
【図3】本発明のさらに他の実施形態であるマンホール
構造の概略を示す分解断面図である。FIG. 3 is an exploded cross-sectional view schematically showing a manhole structure which is another embodiment of the present invention.
【図4】通常の蒸留塔を示す概略図である。FIG. 4 is a schematic view showing an ordinary distillation column.
【図5】従来のマンホール構造を示す分解断面図であ
る。FIG. 5 is an exploded sectional view showing a conventional manhole structure.
1 塔壁 2 開口部 3 マンホール胴板 4 フランジ 5 蓋部 6 ガスケット 7 ボルト 8 ナット 9 取っ手 10 トレース配管(加熱手段) 10a 供給口 10b 排出口 11 塔壁 12 開口部 13 マンホール胴板 14 フランジ 15 加熱ジャケット(加熱手段) 15a 供給口 15b 排出口 1 tower wall 2 openings 3 Manhole body plate 4 flange 5 Lid 6 gasket 7 volts 8 nuts 9 handle 10 Trace piping (heating means) 10a supply port 10b outlet 11 tower wall 12 openings 13 Manhole body plate 14 Flange 15 Heating jacket (heating means) 15a supply port 15b outlet
───────────────────────────────────────────────────── 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 AA01 AA13 AA16 AA22 BB01 BB03 CD41 CD43 DA14 DA22 JA02 4H006 AA02 AA04 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 AA01 AA13 AA16 AA22 BB01 BB03 CD41 CD43 DA14 DA22 JA02 4H006 AA02 AA04 AD11 BD82 BS10
Claims (7)
塔のマンホールを加熱することを特徴とする易重合性物
質の蒸留方法。1. A method for distilling a readily polymerizable substance, which comprises heating a manhole of a distillation column when distilling the easily polymerizable substance.
温度に加熱する請求項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 temperature of the manhole is heated to a temperature higher than the temperature inside the tower.
温度で、かつ塔内温度から100℃を越えない温度範囲
に加熱する請求項1記載の易重合性物質の蒸留方法。3. The method for distilling a readily polymerizable substance according to claim 1, wherein the temperature of the manhole is heated to a temperature higher than the temperature inside the column and within a temperature range not exceeding 100 ° C. from the temperature inside the column.
求項1〜3のいずれかに記載の易重合性物質の蒸留方
法。4. The method for distilling an easily polymerizable substance according to claim 1, wherein the easily polymerizable substance is a vinyl compound.
れるマンホールの構造であって、蒸留塔の壁面に取り付
けられ壁面から突出したマンホール胴板と、前記マンホ
ール胴板の先端開口を塞ぐ蓋部と、前記マンホールに設
けられたマンホール胴板および/または蓋部を加熱する
ための加熱手段とを備えたことを特徴とする蒸留塔のマ
ンホール構造。5. A structure of a manhole provided in a distillation column for distilling a readily polymerizable substance, the manhole body plate being attached to a wall surface of the distillation column and protruding from the wall surface, and closing a front end opening of the manhole body plate. A manhole structure for a distillation column, comprising a lid and a heating means for heating the manhole body plate and / or the lid provided in the manhole.
び/または蓋部の外表面に熱媒体を通すトレース配管を
接触させたものである請求項5記載のマンホール構造。6. The manhole structure according to claim 5, wherein the heating means is such that a trace pipe for passing a heat medium is brought into contact with the outer surface of the manhole body plate and / or the lid portion.
び/または蓋部の外表面に熱媒体を通す加熱ジャケット
を設けたものである請求項5記載のマンホール構造。7. The manhole structure according to claim 5, wherein the heating means is provided with a heating jacket for passing a heat medium on the outer surface of the manhole body plate and / or the lid portion.
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2009120535A (en) * | 2007-11-15 | 2009-06-04 | Mitsubishi Rayon Co Ltd | Device for treating easily polymerizable material |
JP2009149587A (en) * | 2007-12-21 | 2009-07-09 | Mitsubishi Rayon Co Ltd | Apparatus for handling easily polymerizable substance |
WO2019029955A1 (en) * | 2017-08-10 | 2019-02-14 | Basell Poliolefine Italia S.R.L. | Polymerization unit with improved manhole |
WO2023210075A1 (en) * | 2022-04-27 | 2023-11-02 | 株式会社日本触媒 | Device for handling easily polymerizable substance |
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JPS5765304A (en) * | 1980-08-29 | 1982-04-20 | Asahi Chem Ind Co Ltd | Distillation apparatus |
JP2001081050A (en) * | 1999-09-10 | 2001-03-27 | Nippon Shokubai Co Ltd | Apparatus and method for handling readily polymerizable compound |
-
2001
- 2001-09-28 JP JP2001304589A patent/JP4943605B2/en not_active Expired - Lifetime
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
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JPS5765304A (en) * | 1980-08-29 | 1982-04-20 | Asahi Chem Ind Co Ltd | Distillation apparatus |
JP2001081050A (en) * | 1999-09-10 | 2001-03-27 | Nippon Shokubai Co Ltd | Apparatus and method for handling readily polymerizable compound |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2009120535A (en) * | 2007-11-15 | 2009-06-04 | Mitsubishi Rayon Co Ltd | Device for treating easily polymerizable material |
JP2009149587A (en) * | 2007-12-21 | 2009-07-09 | Mitsubishi Rayon Co Ltd | Apparatus for handling easily polymerizable substance |
WO2019029955A1 (en) * | 2017-08-10 | 2019-02-14 | Basell Poliolefine Italia S.R.L. | Polymerization unit with improved manhole |
US11084016B2 (en) | 2017-08-10 | 2021-08-10 | Basell Poliolefine Italia S.R.L. | Polymerization unit with improved manhole |
WO2023210075A1 (en) * | 2022-04-27 | 2023-11-02 | 株式会社日本触媒 | Device for handling easily polymerizable substance |
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