JPH04131120A - Solvent recovery apparatus - Google Patents

Solvent recovery apparatus

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Publication number
JPH04131120A
JPH04131120A JP2253465A JP25346590A JPH04131120A JP H04131120 A JPH04131120 A JP H04131120A JP 2253465 A JP2253465 A JP 2253465A JP 25346590 A JP25346590 A JP 25346590A JP H04131120 A JPH04131120 A JP H04131120A
Authority
JP
Japan
Prior art keywords
activated carbon
solvent gas
adsorbing
solvent
bed
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
JP2253465A
Other languages
Japanese (ja)
Inventor
Masahito Tanaka
雅人 田中
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.)
Sekisui Chemical Co Ltd
Original Assignee
Sekisui 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 Sekisui Chemical Co Ltd filed Critical Sekisui Chemical Co Ltd
Priority to JP2253465A priority Critical patent/JPH04131120A/en
Publication of JPH04131120A publication Critical patent/JPH04131120A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To restore the function of an activated carbon adsorbing part by constituting the activated carbon adsorbing part of two or more activated carbon beds parallelly arranged in the advance direction of solvent gas and replacing only the activated carbon bed positioned on the suction side of the solvent gas as the outermost bed among the activated carbon beds at the lowering time of capacity. CONSTITUTION:In activated carbon adsorbing part A for adsorbing solvent gas, a desorbing vapor supply part 14 for desorbing the solvent gas adsorbed on the activated carbon adsorbing part A, a condensing part 15 for condensing the desorbed solvent gas and a separation part 16 for separating the condensate in the condensing part 15 are provided. The activated carbon adsorbing part A is constituted of two or more activated carbon beds (e.g. an activated carbon bed 2 for removing high b.p. impurity and a usual activated carbon bed 3) parallelly arranged in the advance direction of the solvent gas. That is, when required adsorbing capacity is not developed because of the lowering of adsorbing capacity due to high b.p. impurity with the elapse of time, only the activated carbon bed positioned in the outermost bed on the suction side of the solvent gas within the activated carbon bed is replaced to restore adsorbing function and running cost is reduced.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、溶剤と空気との混合ガスから溶剤を回収する
際に用いる溶剤回収装置に関する。
DETAILED DESCRIPTION OF THE INVENTION (Industrial Application Field) The present invention relates to a solvent recovery device used for recovering a solvent from a mixed gas of a solvent and air.

(従来の技術) 従来、塗料、印刷、接着テープ、ドライクリーニング等
の産業では、主として揮発性の有機溶剤が使用されるが
、該有機溶剤は高価であり、爆発の危険性があると共に
、人体に対しても有害である為、製造装置或いは加工装
置からの排気等に含まれる溶剤ガスを補足乃至回収して
、浄化された空気を大気中に放出している。そして、こ
の為に用いられる溶剤回収装置は、通常第4図に示すよ
うな活性炭吸着部を有し、該活性炭吸着部は、溶剤ガス
を取り込みこれを吸着させる為の活性炭層aが具備され
、溶剤ガス流入口すより送り込まれた溶剤ガスは、通路
Cを通過したのち、矢印dの方向に流れ、且つ活性炭層
aを通過するときに、これに溶剤ガスを吸着させ、最後
にガス流出口eより流出する。又活性炭層aが経時によ
り溶剤ガスによって飽和に達した為その吸着能力が低下
したときは、溶剤ガスとは逆の方向(矢印fの方向)に
、高圧蒸気をこの活性炭層aに吹きつけて、溶剤を蒸発
させることによりその吸着能力を復活させる(この操作
を「脱着」と称す)のであって、その為に第3図に示し
た本発明装置の配置図のように、脱着用蒸気供給部14
を備えており、又更に、脱着により蒸発した溶剤ガスを
水冷コンデンサー等で凝縮液化する為の凝縮部15と、
該凝縮部15での凝縮液を水と溶剤とに分離する為の分
離部16とを有している。
(Prior Art) Traditionally, volatile organic solvents are mainly used in industries such as paints, printing, adhesive tapes, and dry cleaning, but these organic solvents are expensive, have the risk of explosion, and are harmful to human health. Since the solvent gas is also harmful to the atmosphere, the solvent gas contained in the exhaust gas from manufacturing equipment or processing equipment is captured or collected, and the purified air is released into the atmosphere. The solvent recovery device used for this purpose usually has an activated carbon adsorption section as shown in FIG. 4, and the activated carbon adsorption section is provided with an activated carbon layer a for taking in the solvent gas and adsorbing it. The solvent gas sent from the solvent gas inlet passes through the passage C, flows in the direction of arrow d, and when passing through the activated carbon layer a, it adsorbs the solvent gas, and finally passes through the gas outlet. It flows out from e. In addition, when the activated carbon layer a becomes saturated with the solvent gas over time and its adsorption capacity decreases, high-pressure steam is blown onto the activated carbon layer a in the opposite direction to the solvent gas (in the direction of arrow f). The adsorption capacity is restored by evaporating the solvent (this operation is called "desorption"), and for this purpose, as shown in the layout of the apparatus of the present invention shown in Fig. 3, a vapor supply for desorption is performed. Part 14
Furthermore, a condensing section 15 for condensing and liquefying the solvent gas evaporated by desorption using a water-cooled condenser or the like;
It has a separation section 16 for separating the condensed liquid in the condensation section 15 into water and a solvent.

しかして、第4図に於いて活性炭吸着部aは、溶剤ガス
の流入側gと流出側りにはアングル等の鋼材で格子状に
組まれた金網押さえiと、これに重ねて支持された金網
j(破線で示す)をそれぞれ配置し、溶剤回収装置の胴
周壁、天板及び床板に固定されており、この中に活性炭
(図示しない)を、上部の出入口により投入するように
なっている。
Therefore, in Fig. 4, the activated carbon adsorption part a is supported by overlapping wire mesh retainers i made of steel materials such as angles in a lattice shape on the inflow side g and outflow side of the solvent gas. Wire meshes (indicated by broken lines) are arranged and fixed to the trunk wall, top plate, and floorboard of the solvent recovery device, and activated carbon (not shown) is introduced into the mesh through the entrance/exit at the top. .

(発明が解決しようとする課題) しかしながら、回収すべき溶剤中には高沸点の不純物が
多(含まれている為、この不純物の活性炭層への付着に
よる吸着能力の低下が起こり、吸着・脱着のサイクルを
短(せざるを得なくなる。
(Problem to be solved by the invention) However, since the solvent to be recovered contains many impurities with high boiling points, the adsorption capacity decreases due to the adhesion of these impurities to the activated carbon layer, resulting in adsorption and desorption. This will force the cycle to be shortened.

その結果上記従来の溶剤回収装置では、脱着の為の使用
蒸気量が増大することになり、又これを避けようとすれ
ば活性炭の入替えもしくは再生を頻繁乙こ行う必要があ
り、何れにしてもランニングコストが高くなるという欠
点があった。
As a result, in the conventional solvent recovery equipment described above, the amount of steam used for desorption increases, and to avoid this, it is necessary to frequently replace or regenerate activated carbon. The drawback was that running costs were high.

そこで、本発明者は、斜上のような従来技術の欠点に鑑
み、回収効率の維持に優れ、且つランニングコストの低
い溶剤回収装置を提供すべ(種々研究の結果、高沸点不
純物による吸着能力の低下は、活性炭層の全体について
起こるのではなく、第3図で言えば、溶剤ガスの流入側
の表面jから比較的浅い層に限定されることを見出し、
本発明を完成するに至ったのである。
Therefore, in view of the drawbacks of the prior art such as sloping up, the inventors of the present invention aimed to provide a solvent recovery device that is excellent in maintaining recovery efficiency and has low running costs. It was found that the decrease does not occur in the entire activated carbon layer, but is limited to a relatively shallow layer from the surface j on the solvent gas inlet side in Figure 3.
This led to the completion of the present invention.

(課題を解決する為の手段) 本発明は、溶剤ガスを吸着させる活性炭吸着部と、該活
性炭吸着部に吸着された溶剤ガスを脱着する為の脱着用
蒸気供給部と、脱着された溶剤ガスを凝縮する凝縮部と
、凝縮部での凝縮液を分離する為の分離部とを有する溶
剤回収装置に於いて、前記活性炭吸着部が、溶剤ガスの
進行方向に並設された二層以上の活性炭層からなること
を特徴とする溶剤回収袋をその要旨とするものである。
(Means for Solving the Problems) The present invention provides an activated carbon adsorption unit for adsorbing a solvent gas, a desorption steam supply unit for desorbing the solvent gas adsorbed by the activated carbon adsorption unit, and a desorption vapor supply unit for desorbing the solvent gas adsorbed by the activated carbon adsorption unit. In a solvent recovery device having a condensing section for condensing the liquid and a separating section for separating the condensed liquid in the condensing section, the activated carbon adsorption section has two or more layers arranged in parallel in the direction of movement of the solvent gas. The gist of the bag is a solvent collection bag characterized by being made of an activated carbon layer.

(作用) 本発明は、前記活性炭吸着部が、溶剤ガスの進行方向に
並設された二層以上の活性炭層からなるので、経時によ
り、高沸点不純物による吸着能力の低下の為、所期の吸
着能を発揮しなくなったときは、該活性炭層の内、溶剤
ガスの吸入側の最外層に位置する活性炭層のみを取り替
えることにより、再びその機能が復活する。
(Function) In the present invention, since the activated carbon adsorption section is composed of two or more activated carbon layers arranged in parallel in the direction of movement of the solvent gas, the adsorption capacity decreases over time due to high boiling point impurities. When the adsorption capacity is no longer exhibited, the function can be restored by replacing only the activated carbon layer located at the outermost layer on the solvent gas suction side among the activated carbon layers.

(実施例) 以下に、本発明の実施例を図面を参照しながら詳細に説
明する。
(Example) Hereinafter, an example of the present invention will be described in detail with reference to the drawings.

第1図は本発明装置の内、活性炭吸着部Aの概略正断面
図、第2図は同上の一部切欠平面図であって、図におい
て1は活性炭吸着部の胴周壁であり、全体として円筒状
を呈している。2は高沸点不純物除去用の活性炭層、3
は該高沸点不純物除去用の活性炭層2に重ね合わされた
通常の活性炭層であって、金網押さえ4と、これに重ね
て支持された金網5(破線で示す)とで構成される仕切
り壁6を3枚、高沸点不純物除去用の活性炭層2の方が
やや薄(なるように配置されると共に、何れも活性炭層
床板7に支持され、その両側端縁は胴周壁1に取りつけ
られ、上端縁は天板8に取り付けられている。
Fig. 1 is a schematic front sectional view of the activated carbon adsorption section A of the device of the present invention, and Fig. 2 is a partially cutaway plan view of the same. It has a cylindrical shape. 2 is an activated carbon layer for removing high boiling point impurities, 3
is a normal activated carbon layer superimposed on the activated carbon layer 2 for removing high-boiling point impurities, and a partition wall 6 is composed of a wire mesh retainer 4 and a wire mesh 5 (shown by broken lines) superimposed on and supported by the wire mesh holder 4. The activated carbon layer 2 for removing high-boiling point impurities is slightly thinner. The edge is attached to the top plate 8.

床板9の上には傾斜板10が設けられ、溶剤ガスが上方
に向けて流入し易くなっており、該傾斜板10と活性炭
層床板7との間は、溶剤ガスの通路11となされている
An inclined plate 10 is provided on the floor plate 9 to facilitate the flow of solvent gas upward, and a passage 11 for the solvent gas is formed between the inclined plate 10 and the activated carbon layer floor plate 7. .

本発明装置の作用を上記実施例に基づいて説明すると、
溶剤ガスは、溶剤ガス流入口12より送り込まれ、通路
11を通過したのち、矢印りの方向に流れるが、このと
き、最初に高沸点不純物除去用の活性炭層2を通過し、
その際に、高沸点不純物は高沸点不純物除去用の活性炭
層2で阻止され、引き続き該高沸点不純物除去用の活性
炭層2及び通常の活性炭層3で溶剤ガスが吸着され、最
後にガス流出口13より流出する。
The operation of the device of the present invention will be explained based on the above embodiments.
The solvent gas is sent through the solvent gas inlet 12, passes through the passage 11, and then flows in the direction of the arrow. At this time, it first passes through the activated carbon layer 2 for removing high-boiling point impurities.
At that time, high boiling point impurities are blocked by the activated carbon layer 2 for removing high boiling point impurities, and then the solvent gas is adsorbed by the activated carbon layer 2 for removing high boiling point impurities and the normal activated carbon layer 3, and finally the gas outlet It flows out from 13.

又、脱着の場合は、第3図に示す本発明装置全体の配置
図に於いて、脱着用蒸気供給部14がら圧送された蒸気
が、ガス流出口13より流入し、吸着の場合とは逆の方
向(矢印Fの方向)に通過し、この間に溶剤を吸収して
溶剤ガス流入口12より流出し、次いで脱着された溶剤
ガスを凝縮する凝縮部15に送り込まれ、更に該凝縮部
15により凝縮された凝縮液を分離する為の分離部16
へと送られる。
In addition, in the case of desorption, in the layout of the entire apparatus of the present invention shown in FIG. (in the direction of arrow F), absorbs the solvent during this period, flows out from the solvent gas inlet 12, is then sent to the condensing section 15 where the desorbed solvent gas is condensed, and is further fed into the condensing section 15 where the desorbed solvent gas is condensed. Separation section 16 for separating the condensed liquid
sent to.

この間経時により、高沸点不純物による吸着能力の低下
の為、所期の吸着能を発揮しなくなったときは、該活性
炭層の内、高沸点不純物除去用の活性炭層2のみを取り
替えればよい。この取り替えに際しては、上部の活性炭
出入口17より吸い出して新しい活性炭を投入すればよ
い。
Over time, if the desired adsorption capacity is no longer exhibited due to a decrease in adsorption capacity due to high-boiling impurities, only the activated carbon layer 2 for removing high-boiling impurities among the activated carbon layers needs to be replaced. When replacing the activated carbon, it is sufficient to suck it out from the activated carbon inlet/outlet 17 at the top and insert new activated carbon.

本発明に於ける上記実施例では、活性炭層は高沸点不純
物除去用の活性炭層と、通常の活性炭層とをそれぞれ一
層ずつ並設した例を示したが、必ずしもこの例に限定さ
れず、それぞれの活性炭層は各々幾層並設してもよいの
であって、回収装置全体の寸法、要回収量、溶剤の種類
、送風機能力その他の要素により適宜決定される。
In the above embodiment of the present invention, the activated carbon layer is an example in which an activated carbon layer for removing high-boiling point impurities and a normal activated carbon layer are arranged side by side, but the invention is not necessarily limited to this example, and each The number of activated carbon layers may be arranged in parallel, and is appropriately determined depending on the overall size of the recovery device, the amount to be recovered, the type of solvent, the air blowing function, and other factors.

本発明装置の上記実施例では、装置全体の形状が円筒状
を呈するものを示したが、必ずしもこれに限定されるも
のではなく、横断面が角状のものや扇形状のもの、或い
は継断面が楕円状、角錐状、円錐状のもの等適宜溶剤の
種類や回収すべき濃度、設置空間その他の要素に基づい
て設定すればよい。
In the above embodiments of the device of the present invention, the overall shape of the device is shown to be cylindrical, but the device is not necessarily limited to this. The shape may be appropriately set such as an elliptical shape, a pyramidal shape, a conical shape, etc. based on the type of solvent, the concentration to be recovered, the installation space, and other factors.

本発明装置の上記実施例では、活性炭層における高沸点
不純物除去用の活性炭層と、通常の活性炭層との仕切り
並びに溶剤ガスの流入及び流出側は、金網押さえと、こ
れに重ねて支持された金網とで構成される固定された仕
切り壁を用いたが、装置が比較的小型の場合は、例えば
高沸点不純物除去用の活性炭層と、通常の活性炭層とが
それぞれ別個にそのまま取り出せるように、カセット式
%式% 又、本発明装置の上記実施例では、活性炭層における高
沸点不純物除去用の活性炭層と、通常の活性炭層とは重
ね合わされたものを採用したが、両層の間に空間を設け
てもよい。
In the above embodiment of the device of the present invention, the partition between the activated carbon layer for removing high-boiling point impurities and the normal activated carbon layer, as well as the inflow and outflow sides of the solvent gas, are supported by a wire mesh holder and stacked thereon. A fixed partition wall consisting of a wire mesh was used, but if the device is relatively small, for example, the activated carbon layer for removing high boiling point impurities and the normal activated carbon layer can be taken out separately. Furthermore, in the above embodiment of the device of the present invention, the activated carbon layer for removing high-boiling point impurities in the activated carbon layer and the normal activated carbon layer are overlapped, but there is no space between the two layers. may be provided.

(効果) 本発明溶剤回収装置は、活性炭吸着部が、溶剤ガスの進
行方向に並設された二層以上の活性炭層からなるので、
経時により、高沸点不純物による吸着能力の低下の為、
所期の吸着能を発揮しなくなったときは、該活性炭層の
内、溶剤ガスの吸入側の最外層に位置する活性炭層のみ
を取り替えることにより、再びその機能が復活する。
(Effects) In the solvent recovery device of the present invention, since the activated carbon adsorption section is composed of two or more activated carbon layers arranged in parallel in the direction of movement of the solvent gas,
Over time, the adsorption capacity decreases due to high boiling point impurities.
When the desired adsorption capacity is no longer exhibited, the function can be restored by replacing only the activated carbon layer located at the outermost layer on the solvent gas suction side among the activated carbon layers.

従って、活性炭層の取替え費用は従来の約半分以下にな
り、ランニングコストの逓減を図り得ると共に、回収効
率の長期維持の点で優れた装置を提供することが出来る
Therefore, the cost of replacing the activated carbon layer is about half or less of the conventional cost, making it possible to gradually reduce running costs and providing an apparatus that is excellent in maintaining recovery efficiency over a long period of time.

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

第1図は、本発明装置に用いる活性炭吸着部Aの概略正
断面図、第2図は、同上の一部切欠平面図、第3図は、
本発明溶剤回収装置全体の配置を示す説明図、第4図は
、従来の溶剤回収装置に用いる活性炭吸着部を示す概略
正断面図である。 A・・活性炭吸着部、1・・活性炭吸着部の胴周壁、2
・・高沸点不純物除去用の活性炭層、3・・通常の活性
炭層、4・・金網押さえ、5・・金網、6・・仕切り壁
、7・・活性炭層床板、8・・天板、9・・床板、10
・・傾斜板、11・・溶剤ガスの通路、12・・溶剤ガ
ス流入口、13・ガス流出口、 ・脱着用上記供給部、 ・凝縮部、 ・分離部。
FIG. 1 is a schematic front sectional view of the activated carbon adsorption unit A used in the device of the present invention, FIG. 2 is a partially cutaway plan view of the same, and FIG.
FIG. 4, an explanatory diagram showing the overall arrangement of the solvent recovery device of the present invention, is a schematic front sectional view showing an activated carbon adsorption section used in a conventional solvent recovery device. A... Activated carbon adsorption part, 1... Trunk peripheral wall of activated carbon adsorption part, 2
・・Activated carbon layer for removing high boiling point impurities, 3.・Normal activated carbon layer, 4.・Wire mesh holder, 5.・Wire mesh, 6.・Partition wall, 7.・Activated carbon layer floor plate, 8.・Top plate, 9・・Floor board, 10
... Inclined plate, 11. Solvent gas passage, 12. Solvent gas inlet, 13. Gas outlet, - The above-mentioned supply section for desorption, - Condensation section, - Separation section.

Claims (1)

【特許請求の範囲】[Claims] 1、溶剤ガスを吸着させる活性炭吸着部と、該活性炭吸
着部に吸着された溶剤ガスを脱着する為の脱着用蒸気供
給部と、脱着された溶剤ガスを凝縮する凝縮部と、凝縮
部での凝縮液を分離する為の分離部とを有する溶剤回収
装置に於いて、前記活性炭吸着部が、溶剤ガスの進行方
向に並設された二層以上の活性炭層からなることを特徴
とする溶剤回収装置。
1. An activated carbon adsorption section that adsorbs solvent gas, a desorption steam supply section that desorbs the solvent gas adsorbed on the activated carbon adsorption section, a condensation section that condenses the desorbed solvent gas, and a condensation section that condenses the desorbed solvent gas. A solvent recovery device having a separation section for separating condensate, wherein the activated carbon adsorption section comprises two or more activated carbon layers arranged in parallel in the direction of movement of solvent gas. Device.
JP2253465A 1990-09-21 1990-09-21 Solvent recovery apparatus Pending JPH04131120A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2253465A JPH04131120A (en) 1990-09-21 1990-09-21 Solvent recovery apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2253465A JPH04131120A (en) 1990-09-21 1990-09-21 Solvent recovery apparatus

Publications (1)

Publication Number Publication Date
JPH04131120A true JPH04131120A (en) 1992-05-01

Family

ID=17251767

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2253465A Pending JPH04131120A (en) 1990-09-21 1990-09-21 Solvent recovery apparatus

Country Status (1)

Country Link
JP (1) JPH04131120A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5980306A (en) * 1996-10-31 1999-11-09 The Furukawa Electric Co., Ltd. Electrical connection box
JP2008266370A (en) * 2007-04-16 2008-11-06 Sakata Corp Printing system of organic solvent-based printing ink composition and organic solvent-based printing ink composition utilized in printing system

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5980306A (en) * 1996-10-31 1999-11-09 The Furukawa Electric Co., Ltd. Electrical connection box
JP2008266370A (en) * 2007-04-16 2008-11-06 Sakata Corp Printing system of organic solvent-based printing ink composition and organic solvent-based printing ink composition utilized in printing system

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