JPH07236801A - Distiller utilizing mechanical vibration - Google Patents

Distiller utilizing mechanical vibration

Info

Publication number
JPH07236801A
JPH07236801A JP2946094A JP2946094A JPH07236801A JP H07236801 A JPH07236801 A JP H07236801A JP 2946094 A JP2946094 A JP 2946094A JP 2946094 A JP2946094 A JP 2946094A JP H07236801 A JPH07236801 A JP H07236801A
Authority
JP
Japan
Prior art keywords
heat transfer
transfer pipe
wire
mechanical vibration
distiller
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.)
Granted
Application number
JP2946094A
Other languages
Japanese (ja)
Other versions
JP3229742B2 (en
Inventor
Masatoshi Yamamoto
正俊 山本
Junichi Shingu
淳一 新宮
Seiichi Nonaka
誠一 野中
Koichi Takahashi
浩一 高橋
Koichiro Terada
晃一郎 寺田
Tsukasa Motooka
司 元岡
Yuko Takatsu
祐子 高津
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.)
Mitsui Toatsu Chemicals Inc
Original Assignee
Mitsui Toatsu Chemicals Inc
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 Mitsui Toatsu Chemicals Inc filed Critical Mitsui Toatsu Chemicals Inc
Priority to JP02946094A priority Critical patent/JP3229742B2/en
Publication of JPH07236801A publication Critical patent/JPH07236801A/en
Application granted granted Critical
Publication of JP3229742B2 publication Critical patent/JP3229742B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related 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

PURPOSE:To enhance the heat transfer efficiency of a heat transfer pipe, in a distiller wherein the heat transfer pipe is inserted in the bottom part of a column, by arranging a wire transmitting mechanical vibration in the vicinity of the heat transfer pipe and applying mechanical vibration to the liquid present in the bottom part of the column to prevent the adhesion of scale to the heat transfer pipe. CONSTITUTION:In a distiller wherein a heat transfer pipe 3 is inserted in the bottom part of a column, a wire 7 transmitting mechanical vibration is arranged in the vicinity of the heat transfer pipe 3 and the contact surface of the heat transfer pipe 3 with the liquid present in the bottom part of the column is vibrated. The wire 7 transmitting mechanical vibration is pref. composed of a piano wire or a coil wire low in the coefficient of thermal expansion and excellent in durability. Vibration is applied to the wire by attaching the wire to an oscillator under tension. By this constitution, in the case of a liquid containing low, medium and high b.p. components and easy to generate scaling on the heat transfer pipe during distillation, the recovery efficiency of the medium b.p. component being a product is enhanced and the heat efficiency of the heat transfer pipe can be enhanced and the number of times of the cleaning of the heat transfer pipe can be reduced.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は機械的振動を利用した蒸
留器に関する。詳しくは本発明は機械的振動を利用した
蒸留器および当該蒸留器を用いて供給原料から低沸分と
中沸分を回収する方法に関する。
FIELD OF THE INVENTION The present invention relates to a distiller utilizing mechanical vibration. More particularly, the present invention relates to a still using a mechanical vibration and a method for recovering low boiling components and medium boiling components from a feedstock using the still.

【0002】[0002]

【従来の技術】蒸留器の熱源供給はリボイラーで行なっ
ているが、リボイラーの設置の仕方によって蒸留器ボト
ム内に設置する内挿型と蒸留器外部にリボイラーを設置
し、加熱された処理液を供給する外挿型がある。ここで
リボイラーで処理液に熱源を供給している時、処理液に
よってリボイラーの伝熱管(板)にスケールが発生する
事がある。例えば熱劣化しやすい処理液とか蒸発残渣が
伝熱管に付着しやすい時など、スケールが付着しやす
い。こういった処理液を蒸留器で処理した時、スケール
が付着し熱効率が低下する。特にリボイラー内挿型にお
いてはスケール付着により補修しようとしても装置の稼
動を中止したりする必要があったり、補修がやりにくく
補修期間が長くなったりする事からスケールの付着防止
は必要である。
2. Description of the Related Art The heat source of a distiller is supplied by a reboiler. Depending on how the reboiler is installed, the reboiler is installed inside the distiller bottom and the reboiler is installed outside the distiller. There is an extrapolation type to supply. Here, when a heat source is supplied to the treatment liquid by the reboiler, a scale may be generated in the heat transfer tube (plate) of the reboiler by the treatment liquid. For example, when the treatment liquid which is easily deteriorated by heat or the evaporation residue is easily attached to the heat transfer tube, the scale is easily attached. When such a treatment liquid is treated with a distiller, the scale adheres to reduce the thermal efficiency. Particularly, in the reboiler interpolating type, it is necessary to stop the operation of the device even if it is attempted to repair due to scale adhesion, or it is difficult to repair and the repair period becomes long, so it is necessary to prevent scale adhesion.

【0003】スケール付着防止対策として今まで行なっ
ていることは、スケール付着の原因となる成分を蒸留器
に入る前に除去する方法が取られる事が多い。又、装置
においては伝熱管を回転させて処理液と伝熱管の間に剪
断力を与える事により付着防止を計り自ら清掃しながら
伝熱させる方法も取られている。又は伝熱管の表面状態
を平滑にしてスケールの付着防止を図る方法も取られて
いる。
As a measure for preventing scale adhesion, what has been carried out so far is often a method of removing components causing scale adhesion before entering a distiller. Further, in the apparatus, a method of rotating the heat transfer tube to apply a shearing force between the processing liquid and the heat transfer tube to prevent adhesion and to transfer heat while cleaning itself is also adopted. Alternatively, a method of smoothing the surface condition of the heat transfer tube to prevent the scale from adhering to it has been adopted.

【0004】[0004]

【発明が解決しようとする課題】本発明の目的は伝熱管
にスケールが付着しない蒸留器およびこれを利用した蒸
留方法を提供することにある。
SUMMARY OF THE INVENTION An object of the present invention is to provide a distiller in which no scale adheres to a heat transfer tube and a distillation method using the distiller.

【0005】[0005]

【課題を解決するための手段】本発明者らは、上記課題
を解決するために鋭意検討した結果、これらの欠陥を解
消するために伝熱管の近傍に線あるいはコイルを張り、
これに機械的振動を与え、伝熱管と塔底部に存在する液
の接触面を音波で振動させればよいことを見出し、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 set a wire or a coil near the heat transfer tube in order to eliminate these defects,
It was found that mechanical vibration may be applied to this to vibrate the contact surface between the heat transfer tube and the liquid existing at the bottom of the tower with a sound wave, and the present invention has been completed.

【0006】すなわち本発明は、塔底部に伝熱管を内挿
する蒸留器において、伝熱管近傍に機械的振動を伝える
線を配置し、塔底部に存在する液に機械的振動を与える
ことを特徴とする機械的振動を利用した蒸留器であり、
更には前記した蒸留器により供給原料から低沸分を分離
し、次いで中沸分を分離することを特徴とする供給原料
から低沸分と中沸分を回収する方法である。
That is, the present invention is characterized in that, in a distiller in which a heat transfer tube is inserted at the bottom of a column, a wire for transmitting mechanical vibration is arranged in the vicinity of the heat transfer tube to impart mechanical vibration to the liquid existing at the bottom of the column. Is a distiller utilizing mechanical vibration,
Further, it is a method of recovering low boiling point and medium boiling point from the feed material, characterized in that low boiling point content is separated from the feed material by the above-mentioned distiller, and then middle boiling point content is separated.

【0007】図1は伝熱管近傍に機械的振動を伝える線
を配置した塔底部の概要を示す斜視図である。機械的振
動を伝える線は、ピアノ線あるいはそのコイル状のもの
であり、熱膨張係数が少なく耐久性にすぐれるものが良
い。具体的にはピアノ線A種(SWP−A)、弁ばね用
クロムバナジウム鋼オイルテンパー線、弁ばね用シリコ
ンクロム鋼オイルテンパー線、弁ばね用シリコンマンガ
ン鋼オイルテンパー線などが例示される。線の太さは
0.5m/mφ〜5.0m/mφが好ましく、線と伝熱
管の距離は1m/m〜10m/mである。特に2m/m
φ〜3m/mφが良い。機械的振動周波数としては10
〜500Hzの低周波が良い。
FIG. 1 is a perspective view showing an outline of a tower bottom portion in which a wire for transmitting mechanical vibration is arranged near the heat transfer tube. The wire for transmitting mechanical vibration is a piano wire or a coil thereof, and it is preferable that the wire has a small coefficient of thermal expansion and excellent durability. Specific examples include piano wire type A (SWP-A), chrome vanadium steel oil temper wire for valve springs, silicon chrome steel oil temper wire for valve springs, and silicon manganese steel oil temper wire for valve springs. The thickness of the wire is preferably 0.5 m / mφ to 5.0 m / mφ, and the distance between the wire and the heat transfer tube is 1 m / m to 10 m / m. Especially 2m / m
φ to 3 m / mφ is good. 10 as mechanical vibration frequency
A low frequency of up to 500 Hz is good.

【0008】線に振動を伝える方法として、図2のごと
く発振子から線を張る方法が例示される。
As a method of transmitting vibration to a wire, a method of drawing a wire from an oscillator as shown in FIG. 2 is exemplified.

【0009】本発明の蒸留器で処理される液は、低沸
分、中沸分および高沸分から構成される液であり、蒸留
中に伝熱管にスケーリングが発生しやすい液である。よ
り具体的には処理液に硫酸カルシウムなどの逆溶解性の
物質が入っていたり、熱に不安定で、加熱により伝熱管
に付着しやすい物質が混入している場合である。とりわ
けフェノールとアセトンの反応混合物から塩酸触媒と水
を除去したものであり、低沸分が未反応フェノール、か
つ中沸分がビスフェノールAである液が処理液として挙
げられる。
The liquid treated in the still of the present invention is a liquid composed of a low-boiling component, a medium-boiling component and a high-boiling component, and is a liquid in which scaling occurs easily in the heat transfer tube during distillation. More specifically, it is a case where a reverse-dissolving substance such as calcium sulfate is contained in the treatment liquid, or a substance which is unstable to heat and easily adheres to the heat transfer tube by heating is mixed. In particular, a solution obtained by removing a hydrochloric acid catalyst and water from a reaction mixture of phenol and acetone, in which a low-boiling component is unreacted phenol and a medium-boiling component is bisphenol A is mentioned as a treatment liquid.

【0010】蒸留中は処理液の種類に応じて適宜蒸留器
の真空度、加熱温度が選ばれて設定される。
During distillation, the degree of vacuum and heating temperature of the distiller are appropriately selected and set according to the type of treatment liquid.

【0011】[0011]

【実施例】以下、実施例により本発明を詳しく説明す
る。 実施例1 図1は装置概要を示す斜視図である。図1において、1
は処理液の入口、2は処理液の出口、3は45φ/39
φ(SUS 33TP−S)の伝熱管、4は通路壁(高
さ157mm)、5は充填カラム(サイズ:700φ×
1260mm、ラシヒリング(300mm)が充填され
ている。)、6は塔底部(サイズ:2700×142
0)である。機械的振動を与える線7と伝熱管3の距離
は2m/mであった。処理液を塔底部に装入し、熱媒を
用いて加熱を開始した。熱媒の温度は280℃であっ
た。蒸留器の真空度は5mmHg absであった。図
2は伝熱管と機械的振動を与える線の関係を表わす部分
の拡大図である。図3は発振子と機械的振動を伝える線
の関係を表わす概要図である。図3において8は発振子
である。機械的振動を伝える線は材質がステンレス鋼
(SUS)であり、太さは2mmφであった。機械的振
動を与えながら処理液の蒸留を行なった。機械的振動の
周波数は250Hz発振子から与えた。蒸留の結果を表
1に示す。
The present invention will be described in detail below with reference to examples. Example 1 FIG. 1 is a perspective view showing the outline of the apparatus. In FIG. 1, 1
Is the inlet of the processing liquid, 2 is the outlet of the processing liquid, 3 is 45φ / 39
φ (SUS 33TP-S) heat transfer tubes, 4 passage walls (height 157 mm), 5 packed columns (size: 700φ ×
1260 mm, filled with Raschig rings (300 mm). ), 6 is the bottom of the tower (size: 2700 × 142)
0). The distance between the wire 7 giving mechanical vibration and the heat transfer tube 3 was 2 m / m. The treatment liquid was charged into the bottom of the tower, and heating was started using a heat medium. The temperature of the heating medium was 280 ° C. The degree of vacuum in the still was 5 mmHg abs. FIG. 2 is an enlarged view of a portion showing the relationship between the heat transfer tube and the line giving mechanical vibration. FIG. 3 is a schematic diagram showing the relationship between the oscillator and the line transmitting mechanical vibration. In FIG. 3, 8 is an oscillator. The wire for transmitting mechanical vibration was made of stainless steel (SUS) and had a thickness of 2 mmφ. The treatment liquid was distilled while applying mechanical vibration. The frequency of mechanical vibration was given from a 250 Hz oscillator. The results of distillation are shown in Table 1.

【0012】比較例1 実施例1の装置で機械的振動を与えないまま処理液の加
熱を行なった。蒸留の結果を表1に示す。
Comparative Example 1 The treatment liquid was heated in the apparatus of Example 1 without applying mechanical vibration. The results of distillation are shown in Table 1.

【0013】[0013]

【表1】 BPA:ビスフェノールA LB:低分子量のフェノール誘導体 HB:高分子量のフェノール誘導体 OP−BPA:オルト−パラ位に配位しているビスフェ
ノールA co-dimer:共重合体 比較例1は機械的振動を与えなかった場合、実施例1は
機械的振動を与えた場合の分離結果を表している。
[Table 1] BPA: Bisphenol A LB: Low molecular weight phenol derivative HB: High molecular weight phenol derivative OP-BPA: Ortho-para coordinated bisphenol A co-dimer: Copolymer Comparative Example 1 gives mechanical vibration. If not, Example 1 represents the separation result when mechanical vibration was applied.

【0014】目的であるBPA成分の収率は比較例1で
6,704.66/6,827.57=98.2%に対し、実施例1は6,761.77
/6,827.57=99.03 %となった。又、熱媒は280℃で供
給したところ、比較例1は272℃で出て温度差は8℃
あったが、実施例1は270℃で若干熱効率は上がっ
た。スケーリング防止対策として、比較例1では年2回
の清掃回数が必要であったが、実施例1では年1回の清
掃回数となった。
The yield of the desired BPA component was the same as in Comparative Example 1.
In contrast to 6,704.66 / 6,827.57 = 98.2%, Example 1 has 6,761.77.
/6,827.57=99.03%. Also, when the heating medium was supplied at 280 ° C., Comparative Example 1 came out at 272 ° C. and the temperature difference was 8 ° C.
However, in Example 1, the thermal efficiency slightly increased at 270 ° C. As a scaling prevention measure, the number of cleanings required twice a year in Comparative Example 1, but the number of cleanings performed once a year in Example 1.

【0015】[0015]

【発明の効果】製品である中沸分の回収効率が向上し、
伝熱管の熱効率の向上、伝熱管の清掃回数の減少が可能
となった。
EFFECT OF THE INVENTION The efficiency of recovering the medium boiling point product is improved,
It has become possible to improve the thermal efficiency of the heat transfer tube and reduce the number of times the heat transfer tube is cleaned.

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

【図1】 伝熱管の近傍に機械的振動を伝える線を配置
した塔底部の概要を示す斜視図である。
FIG. 1 is a perspective view showing an outline of a tower bottom portion in which a wire for transmitting mechanical vibration is arranged near a heat transfer tube.

【図2】 伝熱管と機械的振動を与える線の関係を表わ
す部分の拡大図である。
FIG. 2 is an enlarged view of a portion showing a relationship between a heat transfer tube and a line that gives mechanical vibration.

【図3】 発振子と機械的振動を伝える線の関係をあら
わした概要図である。
FIG. 3 is a schematic diagram showing a relationship between an oscillator and a line for transmitting mechanical vibration.

【符号の説明】[Explanation of symbols]

1 処理液の入口 2 処理液の出口 3 伝熱管 4 通路壁 5 充填カラム 6 塔底部 7 機械的振動を与える線 8 発振子 1 Treatment Liquid Inlet 2 Treatment Liquid Outlet 3 Heat Transfer Tube 4 Passage Wall 5 Packed Column 6 Tower Bottom 7 Mechanical Vibration Line 8 Oscillator

───────────────────────────────────────────────────── フロントページの続き (72)発明者 高橋 浩一 愛知県名古屋市南区丹後通2丁目1番地 三井東圧化学株式会社内 (72)発明者 寺田 晃一郎 愛知県名古屋市南区丹後通2丁目1番地 三井東圧化学株式会社内 (72)発明者 元岡 司 愛知県名古屋市南区丹後通2丁目1番地 三井東圧化学株式会社内 (72)発明者 高津 祐子 愛知県名古屋市南区丹後通2丁目1番地 三井東圧化学株式会社内 ─────────────────────────────────────────────────── ─── Continuation of front page (72) Koichi Takahashi, 2-chome, Tango-dori, Minami-ku, Nagoya, Aichi Prefecture Mitsui Toatsu Chemical Co., Ltd. (72) Koichiro Terada, 2-chome, Tango-dori, Minami-ku, Aichi Prefecture Mitsui Toatsu Chemical Co., Ltd. (72) Inventor Tsukasa Motooka 2-1, Tango-dori, Minami-ku, Aichi Prefecture Nagoya-shi Mitsui Toatsu Chemical Co., Ltd. (72) Yuko Takatsu Tango-dori, Minami-ku, Nagoya-shi, Aichi 2-1, 1 Mitsui Toatsu Chemical Co., Ltd.

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 塔底部に伝熱管を内挿する蒸留器におい
て、伝熱管近傍に機械的振動を伝える線を配置し、塔底
部に存在する液に機械的振動を与えることを特徴とする
機械的振動を利用した蒸留器。
1. A distiller in which a heat transfer tube is inserted at the bottom of a column, wherein a line for transmitting mechanical vibration is arranged near the heat transfer tube, and mechanical vibration is applied to a liquid existing at the bottom of the column. Distiller that utilizes dynamic vibration.
【請求項2】 請求項1の蒸留器により供給原料から低
沸分を分離し、次いで中沸分を分離することを特徴とす
る供給原料から低沸分と中沸分を回収する方法。
2. A method for recovering a low boiling point component and a medium boiling point component from a feed material, which comprises separating a low boiling point component from a feed material by the distiller of claim 1 and then separating a medium boiling point component.
【請求項3】 供給原料がフェノールとアセトンの反応
混合物から塩酸触媒と水を除去したものであり、低沸分
が未反応フェノールであり、かつ中沸分がビスフェノー
ルAであることを特徴とする請求項2の方法。
3. A feedstock obtained by removing a hydrochloric acid catalyst and water from a reaction mixture of phenol and acetone, wherein the low boiling point is unreacted phenol and the medium boiling point is bisphenol A. The method of claim 2.
JP02946094A 1994-02-28 1994-02-28 Distillers using mechanical vibration Expired - Fee Related JP3229742B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP02946094A JP3229742B2 (en) 1994-02-28 1994-02-28 Distillers using mechanical vibration

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP02946094A JP3229742B2 (en) 1994-02-28 1994-02-28 Distillers using mechanical vibration

Publications (2)

Publication Number Publication Date
JPH07236801A true JPH07236801A (en) 1995-09-12
JP3229742B2 JP3229742B2 (en) 2001-11-19

Family

ID=12276718

Family Applications (1)

Application Number Title Priority Date Filing Date
JP02946094A Expired - Fee Related JP3229742B2 (en) 1994-02-28 1994-02-28 Distillers using mechanical vibration

Country Status (1)

Country Link
JP (1) JP3229742B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5653852A (en) * 1995-11-08 1997-08-05 Meng; Ching Ping Distilling device
US6127511A (en) * 1997-12-11 2000-10-03 Mitsui Chemicals, Inc. Preparation process of phenol aralkyl resins
CN117303672A (en) * 2023-11-28 2023-12-29 山东戴克生物科技有限公司 Imidazole waste water treatment device

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5653852A (en) * 1995-11-08 1997-08-05 Meng; Ching Ping Distilling device
US6127511A (en) * 1997-12-11 2000-10-03 Mitsui Chemicals, Inc. Preparation process of phenol aralkyl resins
CN117303672A (en) * 2023-11-28 2023-12-29 山东戴克生物科技有限公司 Imidazole waste water treatment device
CN117303672B (en) * 2023-11-28 2024-02-09 山东戴克生物科技有限公司 Imidazole waste water treatment device

Also Published As

Publication number Publication date
JP3229742B2 (en) 2001-11-19

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