JPS6236481Y2 - - Google Patents

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Publication number
JPS6236481Y2
JPS6236481Y2 JP1981030342U JP3034281U JPS6236481Y2 JP S6236481 Y2 JPS6236481 Y2 JP S6236481Y2 JP 1981030342 U JP1981030342 U JP 1981030342U JP 3034281 U JP3034281 U JP 3034281U JP S6236481 Y2 JPS6236481 Y2 JP S6236481Y2
Authority
JP
Japan
Prior art keywords
reboiler
aqueous solution
effect
concentrator
concentration
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.)
Expired
Application number
JP1981030342U
Other languages
Japanese (ja)
Other versions
JPS57145503U (en
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 filed Critical
Priority to JP1981030342U priority Critical patent/JPS6236481Y2/ja
Publication of JPS57145503U publication Critical patent/JPS57145503U/ja
Application granted granted Critical
Publication of JPS6236481Y2 publication Critical patent/JPS6236481Y2/ja
Expired legal-status Critical Current

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  • Heat Treatment Of Water, Waste Water Or Sewage (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Description

【考案の詳細な説明】 本考案はオリゴマを含むラクタム水溶液を多段
で濃縮する多重効用缶の、装置内壁面への析出物
付着を防止することに関するものである。
[Detailed Description of the Invention] The present invention relates to preventing deposits from adhering to the inner wall surface of a multi-effect can for concentrating an aqueous lactam solution containing an oligomer in multiple stages.

たとえばε−カプロラクタムを重合して得られ
た生成物中にはポリカプロラクタムの他に未重合
物(ε−カプロラクタムおよびそのオリゴマ)が
数〜十数%含まれている。これら未重合物はポリ
カプロラクタム本来の優れた特性を劣化させるの
で、温水抽出法などの方法により除去される。こ
こで発生する多量の抽出水中に含まれている数%
の未重合物を回収するため、抽出水は目的とする
濃度まで濃縮される。この濃縮には、多重効用缶
が通常用いられる。
For example, a product obtained by polymerizing ε-caprolactam contains several to ten-odd percent of unpolymerized substances (ε-caprolactam and oligomers thereof) in addition to polycaprolactam. Since these unpolymerized substances deteriorate the original excellent properties of polycaprolactam, they are removed by a method such as hot water extraction. A few percent contained in the large amount of extracted water generated here.
In order to recover unpolymerized products, the extracted water is concentrated to the desired concentration. Multi-effect cans are commonly used for this concentration.

抽出水即ち未重合物含有水溶液の濃縮に用いら
れる多重効用缶としては、従来は、第1図に示す
如き装置が用いられてきていた。第1図は濃縮
缶、前記濃縮缶の外部に設けられた再沸器及び前
記濃縮缶と前記再沸器との間に、濃縮されようと
する水溶液を循環させるために設けられた2本1
組の循環管とを少なくとも具備する濃縮系を複数
(n)段連設してなる多重効用缶であつて、最終
のn段目と(n−1)段目の濃縮系B,Aを示
す。従来の多重効用缶の概略縦断面図である。濃
縮されようとする未重合物含有水溶液は、水溶液
供給管2Aを通つて濃縮系Aに供給され、該濃縮
系Aで一部濃縮された後、次の濃縮系Bに供給さ
れる。水溶液供給管2Bにより供給される水溶液
は、濃縮缶3Bの気相部分8Bあるいは液中部分
に供給される。再沸器1Bは、蒸気管9で移送さ
れてくる前段濃縮缶3A発生蒸気などにより加熱
されているため、濃縮缶3Bにはいつた水溶液
は、濃縮缶3B・再沸器1B間を循環管4Bを通
つて、その密度差により自性循環し、濃縮され
る。この自然循環する量は、再沸器1Bでの加熱
効率と正の相関関係にあり、加熱効率が良いほど
大きい。この循環量が多く、水溶液濃度が低けれ
ば、装置内壁でのオリゴマの析出、堆積はほとん
ど問題とならない。
Conventionally, an apparatus as shown in FIG. 1 has been used as a multi-effect canister used for concentrating extracted water, that is, an aqueous solution containing unpolymerized substances. Figure 1 shows a concentrator, a reboiler installed outside the concentrator, and two tubes 1 installed between the concentrator and the reboiler to circulate an aqueous solution to be concentrated.
This is a multi-effect can consisting of a plurality (n) stages of concentrating systems each having at least a set of circulation pipes, and shows the final n-th stage and (n-1) stage concentrating systems B and A. . FIG. 1 is a schematic vertical cross-sectional view of a conventional multi-effect can. The unpolymerized material-containing aqueous solution to be concentrated is supplied to the concentration system A through the aqueous solution supply pipe 2A, partially concentrated in the concentration system A, and then supplied to the next concentration system B. The aqueous solution supplied by the aqueous solution supply pipe 2B is supplied to the gas phase portion 8B or the submerged portion of the concentrator 3B. Since the reboiler 1B is heated by the steam generated by the pre-concentrator 3A that is transferred through the steam pipe 9, the aqueous solution that has entered the concentrator 3B is passed through the circulation pipe between the concentrator 3B and the reboiler 1B. 4B, it self-circulates and becomes concentrated due to the density difference. This naturally circulating amount has a positive correlation with the heating efficiency in the reboiler 1B, and the better the heating efficiency is, the larger it is. If the amount of circulation is large and the concentration of the aqueous solution is low, precipitation and accumulation of oligomers on the inner walls of the apparatus will hardly be a problem.

ところが、濃縮系が直列につながれている多多
重効用缶においては、順次濃縮がすすんでいくの
で後段の濃縮系ほどオリゴマが析出しやすくなつ
ていき、再沸器1B内、特にその加熱チユーブ内
にオリゴマの付着、堆積が生じて熱効率が低下し
てくる。熱効率が低下してくると水溶液の循環量
が減少し一層オリゴマの付着が多くなるという悪
循環に陥り濃縮効率が急激に低下する。このため
定期的に装置も解体掃除したり、また装置内部を
洗浄したりしてオリゴマの堆積物を除去すること
が必要であつた。
However, in a multi-effect canister in which concentrating systems are connected in series, as the concentration progresses sequentially, oligomers are more likely to precipitate in the later concentrating systems. Thermal efficiency decreases due to adhesion and accumulation of oligomers. As the thermal efficiency decreases, the amount of aqueous solution circulated decreases, leading to a vicious cycle in which more oligomers adhere to the solution, resulting in a sharp decrease in concentration efficiency. For this reason, it has been necessary to periodically dismantle and clean the apparatus and clean the inside of the apparatus to remove oligomer deposits.

そこで本考案は、上述したオリゴマの付着、堆
積を防止することにより長期間解体掃除すること
なく濃縮を行なうことができ、しかも再沸器の熱
効率が改善された多重効用缶を提供することを主
な目的としてなされたものであり、濃縮缶、前記
濃縮缶の外部に設けられた再沸器及び前記濃縮缶
と前記再沸器との間に、濃縮されようとする水溶
液を循環させるために設けられた2本1組の循環
管とを少なくとも具備する濃縮系を複数(n)段
連設してなる多重効用缶において、少なくとも
(n−1)段目の濃縮系からの被濃縮液の供給缶
をn段目の濃縮系の再沸器の底部に接続してな
る、オリゴマを含むラクタム水溶液の濃縮のため
の多重効用缶とすることによつて前記目的を達成
せんとするものである。即ち、本考案は少なくと
も最終のn段目の濃縮系に供給する水溶液を濃縮
缶(気相あるいは液相部分)に供給するのではな
く再沸器の底部に供給することとしたことによ
り、水溶液の循環量を増大させオリゴマの析出、
堆積を防止することを主な特徴とするものであ
る。
Therefore, the main purpose of the present invention is to provide a multi-effect can that can concentrate without having to be dismantled and cleaned for a long period of time by preventing the adhesion and accumulation of oligomers mentioned above, and has improved thermal efficiency of the reboiler. It was designed for the purpose of circulating an aqueous solution to be concentrated between a concentrating can, a reboiler installed outside the concentrating can, and the concentrating can and the reboiler. In a multi-effect can comprising a plurality (n) stages of concentrating systems each having at least one set of two circulation pipes arranged in a row, the liquid to be concentrated is supplied from at least the (n-1)th stage concentrating system. The above objective is achieved by connecting the can to the bottom of the reboiler of the n-th stage concentration system to form a multi-effect can for concentrating an aqueous lactam solution containing oligomers. That is, in the present invention, the aqueous solution to be supplied to at least the final n-stage concentration system is supplied to the bottom of the reboiler instead of being supplied to the concentrator (gas phase or liquid phase part). increases the amount of circulation and precipitates oligomers,
Its main feature is to prevent deposition.

本考案に係る装置を、その一実施態様を示す概
略縦断面図である第2図に沿つて以下に説明す
る。
The apparatus according to the present invention will be described below with reference to FIG. 2, which is a schematic vertical sectional view showing one embodiment thereof.

水溶液供給管2Aを通つて供給された、濃縮さ
れようとするオリゴマ含有ラクタム水溶液は、再
沸器1Aと濃縮缶3Aとにより、従来装置と同様
に一部濃縮され、次いで、水溶液供給管2Bによ
り次の濃縮系Bに、すなわち、再沸器1Bの底部
6Bに供給される。多重効用缶では濃縮系A,
B,……ごとに段々と低い圧力、温度で濃縮を行
なうのであるから、水溶液供給管2B内より再沸
器1Bの底部6Bに水溶液が供給される時、フラ
ツシユペーパーが生じ、再沸器1B内の水溶液循
環が促進される。従つて、水溶液濃度が高くなつ
ても再沸器内にオリゴマの付着、堆積することが
大巾に少なくなり、装置の解体掃除を長期間行な
わずに濃縮作業を続けることができるようにな
る。
The oligomer-containing lactam aqueous solution to be concentrated, supplied through the aqueous solution supply pipe 2A, is partially concentrated by the reboiler 1A and the concentrator 3A, as in the conventional device, and then by the aqueous solution supply pipe 2B. It is then fed to the concentrating system B, ie to the bottom 6B of the reboiler 1B. In multiple effect cans, concentrated system A,
Since concentration is carried out at progressively lower pressure and temperature for each B,..., when the aqueous solution is supplied from the aqueous solution supply pipe 2B to the bottom 6B of the reboiler 1B, flash paper is generated and the reboiler Aqueous solution circulation within 1B is promoted. Therefore, even if the concentration of the aqueous solution increases, the adhesion and accumulation of oligomers in the reboiler is greatly reduced, making it possible to continue concentration work without having to dismantle and clean the device for a long period of time.

再沸器底部6Bに連通させた水溶液供給管2B
にも、従来の供給管同様に、濃縮缶液面コントロ
ール用のバルブ7を設けることが好ましい。
Aqueous solution supply pipe 2B communicated with reboiler bottom 6B
Similarly to the conventional supply pipe, it is preferable to provide a valve 7 for controlling the concentration tank liquid level.

上述した、水溶液供給管2Bを再沸器底部6B
に連設した濃縮系Bは、濃度がかなり高くなつた
未重合物含有水溶液をさらに濃縮する濃縮系、す
なわち最終のn段目のみの濃縮系に適用するのが
最も効果的であり、最終段目と、それ以外の最終
段目から2段目、即ち(n−1)段目の濃縮系に
適用してもよい。
The above-mentioned aqueous solution supply pipe 2B is connected to the reboiler bottom 6B.
It is most effective to apply the concentrating system B, which is connected to It may be applied to the second stage and other stages from the final stage, that is, the (n-1)th stage concentration system.

実施例 第3段目と第4段目の濃縮系として、第1図も
しくは第2図に示した濃縮系を用いた四重効用缶
で、ε−カプロラクタムおよびそのオリゴマを含
む希薄水溶液を濃縮した。第1段目の濃縮系(図
示なし)への水溶液供給量は5000Kg/hr、最終の
第4段目の濃縮系への水溶液供給量は1550Kg/
hr、第3段目の濃縮系の濃縮缶3A内温度は90
℃、第4段目の濃縮系の濃縮缶3B内濃度は40℃
で濃縮操作を行なつた。
Example A dilute aqueous solution containing ε-caprolactam and its oligomer was concentrated in a quadruple-effect can using the concentration system shown in Figure 1 or Figure 2 as the third and fourth stage concentration systems. . The amount of aqueous solution supplied to the first stage concentration system (not shown) is 5000 Kg/hr, and the amount of aqueous solution supplied to the final fourth stage concentration system is 1550 Kg/hr.
hr, the temperature inside the concentration canister 3A of the third stage concentration system is 90
℃, the concentration in the concentrator 3B of the fourth stage concentration system is 40℃
Concentration operation was performed.

本考案に係る四重効用缶(第2図)の場合では
再沸器底部で120Kg/hrのフラツシユペーパーが
発生し、従来の四重効用缶(第1図)の場合に比
べて再沸器の熱効率が約20%改善され、また、解
体清掃を必要とするまでの延べ運転日数も70日か
ら100日に延長することができた。
In the case of the quadruple-effect can (Fig. 2) according to the present invention, 120 kg/hr of flash paper is generated at the bottom of the reboiler, compared to the case of the conventional quadruple-effect can (Fig. 1). The thermal efficiency of the equipment has been improved by approximately 20%, and the total number of days it can be operated before dismantling and cleaning is required has been extended from 70 to 100 days.

【図面の簡単な説明】[Brief explanation of the drawing]

図面は多重効用缶の最終のn段目と(n−1)
段目へ濃縮系を示す概略縦断面であり、第1図は
従来の多重効用缶を、第2図は本考案に係る多重
効用缶の一実施態様を、それぞれ示す。 1A,1B……再沸器、2A,2B……水溶液
供給管、3A,3B……濃縮缶、4A,4B……
循環管、A,B……濃縮系、6B……再沸器の底
部、7B……バルブ。
The drawing shows the final nth stage and (n-1) of the multi-effect can.
FIG. 1 is a schematic longitudinal section showing a concentration system in stages, and FIG. 1 shows a conventional multi-effect can, and FIG. 2 shows an embodiment of the multi-effect can according to the present invention. 1A, 1B...Reboiler, 2A, 2B...Aqueous solution supply pipe, 3A, 3B...Concentrator can, 4A, 4B...
Circulation pipe, A, B...concentration system, 6B...bottom of reboiler, 7B...valve.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 濃縮缶、前記濃縮缶の外部に設けられた再沸器
及び前記濃縮缶と前記再沸器との間に、濃縮され
ようとする水溶液を循環させるために設けられた
2本1組の循環管とを少なくとも具備する濃縮系
を複数(n)段連設してなる多重効用缶におい
て、少なくとも(n−1)段目の濃縮系からの被
濃縮液の供給缶をn段目の濃縮系の再沸器の底部
に接続してなる、オリゴマを含むラクタム水溶液
の濃縮のための多重効用缶。
A concentrator, a reboiler provided outside the concentrator, and a set of two circulation pipes provided between the concentrator and the reboiler to circulate an aqueous solution to be concentrated. In a multi-effect can formed by connecting a plurality (n) stages of concentrating systems having at least A multi-effect canister connected to the bottom of the reboiler for concentrating an aqueous lactam solution containing oligomers.
JP1981030342U 1981-03-06 1981-03-06 Expired JPS6236481Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1981030342U JPS6236481Y2 (en) 1981-03-06 1981-03-06

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1981030342U JPS6236481Y2 (en) 1981-03-06 1981-03-06

Publications (2)

Publication Number Publication Date
JPS57145503U JPS57145503U (en) 1982-09-13
JPS6236481Y2 true JPS6236481Y2 (en) 1987-09-17

Family

ID=29827857

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1981030342U Expired JPS6236481Y2 (en) 1981-03-06 1981-03-06

Country Status (1)

Country Link
JP (1) JPS6236481Y2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013119539A (en) * 2011-12-08 2013-06-17 Unitika Ltd METHOD FOR PURIFYING RECOVERED ε-CAPROLACTAM

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS50148548A (en) * 1974-05-20 1975-11-28

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS50148548A (en) * 1974-05-20 1975-11-28

Also Published As

Publication number Publication date
JPS57145503U (en) 1982-09-13

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