RECOVERY OF SOLVENT
PURPOSE:To prevent the deterioration of an adsorbent, in a solvent recovery method using the adsorbent, by repeating an adsorbing cycle after the temp. of the adsorbent subjected desorption is lowered by a standing cooling method, a cooling water pipe method, a vacuum cooling method or a nitrogen ga...
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creator | NAGANO HAYAMI HIRAO MASASHI |
description | PURPOSE:To prevent the deterioration of an adsorbent, in a solvent recovery method using the adsorbent, by repeating an adsorbing cycle after the temp. of the adsorbent subjected desorption is lowered by a standing cooling method, a cooling water pipe method, a vacuum cooling method or a nitrogen gas sealing recirculation method. CONSTITUTION:Air is passed through flow meters F1, F2 through a filter F and a blower B to enter solvent gas generating bins S1, S2 in a low temp. thermostatic tank H. A gas contacted and mixed with air from a diluting air flow meter Fo in a mixer M is passed through a wheat exchanger E to condition the temp. thereof and exhausted through an adsorbing tower T. After adsorption is finished, steam S is sent into the tower T to desorb a solvent therein and the solvent containing steam is supplied to a decanter D through a condenser C to be separated into drain water W and the recovered solvent PS. A cooling pipe and a vacuum cooling mechanism can added to the adsorbing tower T and a nitrogen gas sealing recirculation method can be further applied thereto. |
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CONSTITUTION:Air is passed through flow meters F1, F2 through a filter F and a blower B to enter solvent gas generating bins S1, S2 in a low temp. thermostatic tank H. A gas contacted and mixed with air from a diluting air flow meter Fo in a mixer M is passed through a wheat exchanger E to condition the temp. thereof and exhausted through an adsorbing tower T. After adsorption is finished, steam S is sent into the tower T to desorb a solvent therein and the solvent containing steam is supplied to a decanter D through a condenser C to be separated into drain water W and the recovered solvent PS. A cooling pipe and a vacuum cooling mechanism can added to the adsorbing tower T and a nitrogen gas sealing recirculation method can be further applied thereto.</description><language>eng</language><subject>PERFORMING OPERATIONS ; PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL ; SEPARATION ; TRANSPORTING</subject><creationdate>1983</creationdate><oa>free_for_read</oa><woscitedreferencessubscribed>false</woscitedreferencessubscribed></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&date=19830917&DB=EPODOC&CC=JP&NR=S58156308A$$EHTML$$P50$$Gepo$$Hfree_for_read</linktohtml><link.rule.ids>230,308,780,885,25562,76317</link.rule.ids><linktorsrc>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&date=19830917&DB=EPODOC&CC=JP&NR=S58156308A$$EView_record_in_European_Patent_Office$$FView_record_in_$$GEuropean_Patent_Office$$Hfree_for_read</linktorsrc></links><search><creatorcontrib>NAGANO HAYAMI</creatorcontrib><creatorcontrib>HIRAO MASASHI</creatorcontrib><title>RECOVERY OF SOLVENT</title><description>PURPOSE:To prevent the deterioration of an adsorbent, in a solvent recovery method using the adsorbent, by repeating an adsorbing cycle after the temp. of the adsorbent subjected desorption is lowered by a standing cooling method, a cooling water pipe method, a vacuum cooling method or a nitrogen gas sealing recirculation method. CONSTITUTION:Air is passed through flow meters F1, F2 through a filter F and a blower B to enter solvent gas generating bins S1, S2 in a low temp. thermostatic tank H. A gas contacted and mixed with air from a diluting air flow meter Fo in a mixer M is passed through a wheat exchanger E to condition the temp. thereof and exhausted through an adsorbing tower T. After adsorption is finished, steam S is sent into the tower T to desorb a solvent therein and the solvent containing steam is supplied to a decanter D through a condenser C to be separated into drain water W and the recovered solvent PS. 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CONSTITUTION:Air is passed through flow meters F1, F2 through a filter F and a blower B to enter solvent gas generating bins S1, S2 in a low temp. thermostatic tank H. A gas contacted and mixed with air from a diluting air flow meter Fo in a mixer M is passed through a wheat exchanger E to condition the temp. thereof and exhausted through an adsorbing tower T. After adsorption is finished, steam S is sent into the tower T to desorb a solvent therein and the solvent containing steam is supplied to a decanter D through a condenser C to be separated into drain water W and the recovered solvent PS. A cooling pipe and a vacuum cooling mechanism can added to the adsorbing tower T and a nitrogen gas sealing recirculation method can be further applied thereto.</abstract><oa>free_for_read</oa></addata></record> |
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subjects | PERFORMING OPERATIONS PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL SEPARATION TRANSPORTING |
title | RECOVERY OF SOLVENT |
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