JPH02129240U - - Google Patents
Info
- Publication number
- JPH02129240U JPH02129240U JP3696089U JP3696089U JPH02129240U JP H02129240 U JPH02129240 U JP H02129240U JP 3696089 U JP3696089 U JP 3696089U JP 3696089 U JP3696089 U JP 3696089U JP H02129240 U JPH02129240 U JP H02129240U
- Authority
- JP
- Japan
- Prior art keywords
- line
- solvent
- section
- supply line
- heating medium
- 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
Links
- 239000002904 solvent Substances 0.000 claims description 15
- 238000001179 sorption measurement Methods 0.000 claims description 12
- 238000000926 separation method Methods 0.000 claims description 10
- 238000011084 recovery Methods 0.000 claims description 9
- 238000010438 heat treatment Methods 0.000 claims description 8
- 238000009833 condensation Methods 0.000 claims description 6
- 230000005494 condensation Effects 0.000 claims description 6
- 238000004064 recycling Methods 0.000 claims description 4
- 238000003795 desorption Methods 0.000 claims description 2
- 238000010586 diagram Methods 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 2
Landscapes
- Treating Waste Gases (AREA)
- Separation Of Gases By Adsorption (AREA)
Description
第1図は本考案の一実施例を示す概略構成図、
第2図は第1図に示す溶剤回収装置の一部欠切概
略正面図、第3図は第2図の概略平面図、第4図
は従来の溶剤回収装置の概略構成図、第5図は実
験例の結果を示すグラフ、第6図は比較実験例の
結果を示すグラフである。
1a,1b……吸着塔、2a,2b……吸着フ
イルタ、4a,4b……排出口、6,6a,6b
……処理ガス供給ライン、8,8a,8b……加
熱媒体供給ライン、16……凝縮部、17……分
離部、18……リサイクルライン、20……圧力
調整部。
FIG. 1 is a schematic configuration diagram showing an embodiment of the present invention;
Fig. 2 is a partially cutaway schematic front view of the solvent recovery device shown in Fig. 1, Fig. 3 is a schematic plan view of Fig. 2, Fig. 4 is a schematic configuration diagram of a conventional solvent recovery device, and Fig. 5 is a graph showing the results of the experimental example, and FIG. 6 is a graph showing the results of the comparative experimental example. 1a, 1b...Adsorption tower, 2a, 2b...Adsorption filter, 4a, 4b...Discharge port, 6, 6a, 6b
... Processing gas supply line, 8, 8a, 8b ... Heating medium supply line, 16 ... Condensation section, 17 ... Separation section, 18 ... Recycling line, 20 ... Pressure adjustment section.
補正 平1.10.11
考案の名称を次のように補正する。
考案の名称 溶剤回収装置
実用新案登録請求の範囲、図面の簡単な説明を
次のように補正する。Amendment 1.10.11. The name of the invention is amended as follows. Title of the invention: Solvent recovery device The scope of the claims for utility model registration and the brief description of the drawings are amended as follows.
【実用新案登録請求の範囲】
吸着フイルタを収容し、開閉自在な排出口を有
する吸着塔と、該吸着塔に溶剤含有処理ガスを供
給する処理ガス供給ラインと、吸着塔に脱着用加
熱媒体を供給する加熱媒体供給ラインと、加熱媒
体により脱着した溶剤を凝縮する凝縮部と、凝縮
された溶剤を分離する分離部と、該分離部の気相
を前記処理ガス供給ラインに合流させるリサイク
ルラインとを有する溶剤回収装置において、上記
凝縮部と分離部との間のライン、分離部又は上記
リサイクルラインに、ラインの圧力変動に対応し
て容量が可変する圧力調整部が設けられているこ
とを特徴とする溶剤回収装置。[Scope of Claim for Utility Model Registration] An adsorption tower that houses an adsorption filter and has a discharge port that can be opened and closed, a processing gas supply line that supplies a solvent-containing processing gas to the adsorption tower, and a heating medium for desorption to the adsorption tower. a heating medium supply line, a condensation section that condenses the solvent desorbed by the heating medium, a separation section that separates the condensed solvent, and a recycle line that joins the gas phase of the separation section to the processing gas supply line. In the solvent recovery device, the line between the condensation section and the separation section, the separation section, or the recycling line is provided with a pressure adjustment section whose capacity is variable in response to pressure fluctuations in the line. Solvent recovery equipment.
【図面の簡単な説明】
第1図は本考案の一実施例を示す概略構成図、
第2図は第1図に示す溶剤回収装置の一部欠切概
略正面図、第3図は第2図の概略平面図、第4図
は従来の溶剤回収装置の概略構成図、第5図は実
験例の結果を示すグラフ、第6図は比較実験例の
結果を示すグラフである。
1a,1b……吸着塔、2a,2b……吸着フ
イルタ、4a,4b……排出口、6,6a,6b
……処理ガス供給ライン、8,8a,8b……加
熱媒体供給ライン、16……凝縮部、17……分
離部、18……リサイクルライン、20……圧力
調整部。[BRIEF DESCRIPTION OF THE DRAWINGS] FIG. 1 is a schematic diagram showing an embodiment of the present invention;
Fig. 2 is a partially cutaway schematic front view of the solvent recovery device shown in Fig. 1, Fig. 3 is a schematic plan view of Fig. 2, Fig. 4 is a schematic configuration diagram of a conventional solvent recovery device, and Fig. 5 is a graph showing the results of the experimental example, and FIG. 6 is a graph showing the results of the comparative experimental example. 1a, 1b...Adsorption tower, 2a, 2b...Adsorption filter, 4a, 4b...Discharge port, 6, 6a, 6b
... Processing gas supply line, 8, 8a, 8b ... Heating medium supply line, 16 ... Condensation section, 17 ... Separation section, 18 ... Recycling line, 20 ... Pressure adjustment section.
Claims (1)
する吸着塔と、該吸着塔に溶剤含有処理ガスを供
給する処理ガス供給ラインと、吸着塔に脱着用加
熱媒体を供給する加熱媒体供給ラインと、加熱媒
体により脱着した溶剤を凝縮する凝縮部と、凝縮
された溶剤を分離する分離部と、該分離部の気相
を前記処理ガス供給ラインに合流させるリサイク
ルラインとを有する溶剤回収装置において、上記
凝縮部と分離部との間のライン、分離部又は上記
リサイクルラインに、ラインの圧力変動に対応し
て容量が可変する圧力調整部が設けられているこ
とを特徴とする溶剤回収装置。 an adsorption tower that houses an adsorption filter and has an outlet that can be opened and closed; a processing gas supply line that supplies a solvent-containing processing gas to the adsorption tower; a heating medium supply line that supplies a heating medium for desorption to the adsorption tower; In a solvent recovery device having a condensation section that condenses the solvent desorbed by a heating medium, a separation section that separates the condensed solvent, and a recycle line that joins the gas phase of the separation section to the processing gas supply line, A solvent recovery device characterized in that a line between a condensation section and a separation section, a separation section, or the recycling line is provided with a pressure adjustment section whose capacity is variable in response to pressure fluctuations in the line.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3696089U JPH0515934Y2 (en) | 1989-03-29 | 1989-03-29 |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3696089U JPH0515934Y2 (en) | 1989-03-29 | 1989-03-29 |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH02129240U true JPH02129240U (en) | 1990-10-24 |
JPH0515934Y2 JPH0515934Y2 (en) | 1993-04-27 |
Family
ID=31543651
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3696089U Expired - Lifetime JPH0515934Y2 (en) | 1989-03-29 | 1989-03-29 |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0515934Y2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2020203780A1 (en) * | 2019-03-29 | 2020-10-08 | 東洋紡株式会社 | Organic solvent recovery system |
-
1989
- 1989-03-29 JP JP3696089U patent/JPH0515934Y2/ja not_active Expired - Lifetime
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2020203780A1 (en) * | 2019-03-29 | 2020-10-08 | 東洋紡株式会社 | Organic solvent recovery system |
Also Published As
Publication number | Publication date |
---|---|
JPH0515934Y2 (en) | 1993-04-27 |
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