Process for separating and concentrating formic acid with phosphorus-contained extractant
A process for separating and concentrating formic acid with phosphorus-contained extractant includes such steps as adding said extractant to kerosene, cascade extraction of the aqueous solution of formic acid with the mixed solvent, returning the extracted liquid (water phase) back to hydrolysis rea...
Gespeichert in:
Hauptverfasser: | , , |
---|---|
Format: | Patent |
Sprache: | eng |
Schlagworte: | |
Online-Zugang: | Volltext bestellen |
Tags: |
Tag hinzufügen
Keine Tags, Fügen Sie den ersten Tag hinzu!
|
container_end_page | |
---|---|
container_issue | |
container_start_page | |
container_title | |
container_volume | |
creator | XIANGLAN PU SHENLIN ZHU GUANGSHENG LUO |
description | A process for separating and concentrating formic acid with phosphorus-contained extractant includes such steps as adding said extractant to kerosene, cascade extraction of the aqueous solution of formic acid with the mixed solvent, returning the extracted liquid (water phase) back to hydrolysis reactor, and distilling the solvent phase to obtain the formic acid with more than 85% of mass concentration. The mass concentration of formic acid in residual liquid is less than 2%. The temp of solvent recovery tower is 120-130 deg.C and after depressurized, its temp is lowered to 90-100 deg.C, so saving energy. |
format | Patent |
fullrecord | <record><control><sourceid>epo_EVB</sourceid><recordid>TN_cdi_epo_espacenet_CN1254705A</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><sourcerecordid>CN1254705A</sourcerecordid><originalsourceid>FETCH-epo_espacenet_CN1254705A3</originalsourceid><addsrcrecordid>eNqFzL0KwkAQBOBrLER9BvcFAv4FawkRK7GwsQrL3sYcmL3jdkUf3yvSWwwDw8fM3eOWI7Eq9DGDcsKMFuQJKB4oCrHYtBQwBgKk4OETbIA0RC3Jb62KNAzCHvhbPBmKLd2sx5fyauqFW5_be3OpOMWONWH5Zuua63ZXH46b-rT_L35qPDrK</addsrcrecordid><sourcetype>Open Access Repository</sourcetype><iscdi>true</iscdi><recordtype>patent</recordtype></control><display><type>patent</type><title>Process for separating and concentrating formic acid with phosphorus-contained extractant</title><source>esp@cenet</source><creator>XIANGLAN PU ; SHENLIN ZHU ; GUANGSHENG LUO</creator><creatorcontrib>XIANGLAN PU ; SHENLIN ZHU ; GUANGSHENG LUO</creatorcontrib><description>A process for separating and concentrating formic acid with phosphorus-contained extractant includes such steps as adding said extractant to kerosene, cascade extraction of the aqueous solution of formic acid with the mixed solvent, returning the extracted liquid (water phase) back to hydrolysis reactor, and distilling the solvent phase to obtain the formic acid with more than 85% of mass concentration. The mass concentration of formic acid in residual liquid is less than 2%. The temp of solvent recovery tower is 120-130 deg.C and after depressurized, its temp is lowered to 90-100 deg.C, so saving energy.</description><edition>7</edition><language>eng</language><subject>ACYCLIC OR CARBOCYCLIC COMPOUNDS ; CHEMISTRY ; METALLURGY ; ORGANIC CHEMISTRY</subject><creationdate>2000</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=20000531&DB=EPODOC&CC=CN&NR=1254705A$$EHTML$$P50$$Gepo$$Hfree_for_read</linktohtml><link.rule.ids>230,308,780,885,25564,76547</link.rule.ids><linktorsrc>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&date=20000531&DB=EPODOC&CC=CN&NR=1254705A$$EView_record_in_European_Patent_Office$$FView_record_in_$$GEuropean_Patent_Office$$Hfree_for_read</linktorsrc></links><search><creatorcontrib>XIANGLAN PU</creatorcontrib><creatorcontrib>SHENLIN ZHU</creatorcontrib><creatorcontrib>GUANGSHENG LUO</creatorcontrib><title>Process for separating and concentrating formic acid with phosphorus-contained extractant</title><description>A process for separating and concentrating formic acid with phosphorus-contained extractant includes such steps as adding said extractant to kerosene, cascade extraction of the aqueous solution of formic acid with the mixed solvent, returning the extracted liquid (water phase) back to hydrolysis reactor, and distilling the solvent phase to obtain the formic acid with more than 85% of mass concentration. The mass concentration of formic acid in residual liquid is less than 2%. The temp of solvent recovery tower is 120-130 deg.C and after depressurized, its temp is lowered to 90-100 deg.C, so saving energy.</description><subject>ACYCLIC OR CARBOCYCLIC COMPOUNDS</subject><subject>CHEMISTRY</subject><subject>METALLURGY</subject><subject>ORGANIC CHEMISTRY</subject><fulltext>true</fulltext><rsrctype>patent</rsrctype><creationdate>2000</creationdate><recordtype>patent</recordtype><sourceid>EVB</sourceid><recordid>eNqFzL0KwkAQBOBrLER9BvcFAv4FawkRK7GwsQrL3sYcmL3jdkUf3yvSWwwDw8fM3eOWI7Eq9DGDcsKMFuQJKB4oCrHYtBQwBgKk4OETbIA0RC3Jb62KNAzCHvhbPBmKLd2sx5fyauqFW5_be3OpOMWONWH5Zuua63ZXH46b-rT_L35qPDrK</recordid><startdate>20000531</startdate><enddate>20000531</enddate><creator>XIANGLAN PU</creator><creator>SHENLIN ZHU</creator><creator>GUANGSHENG LUO</creator><scope>EVB</scope></search><sort><creationdate>20000531</creationdate><title>Process for separating and concentrating formic acid with phosphorus-contained extractant</title><author>XIANGLAN PU ; SHENLIN ZHU ; GUANGSHENG LUO</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-epo_espacenet_CN1254705A3</frbrgroupid><rsrctype>patents</rsrctype><prefilter>patents</prefilter><language>eng</language><creationdate>2000</creationdate><topic>ACYCLIC OR CARBOCYCLIC COMPOUNDS</topic><topic>CHEMISTRY</topic><topic>METALLURGY</topic><topic>ORGANIC CHEMISTRY</topic><toplevel>online_resources</toplevel><creatorcontrib>XIANGLAN PU</creatorcontrib><creatorcontrib>SHENLIN ZHU</creatorcontrib><creatorcontrib>GUANGSHENG LUO</creatorcontrib><collection>esp@cenet</collection></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext_linktorsrc</fulltext></delivery><addata><au>XIANGLAN PU</au><au>SHENLIN ZHU</au><au>GUANGSHENG LUO</au><format>patent</format><genre>patent</genre><ristype>GEN</ristype><title>Process for separating and concentrating formic acid with phosphorus-contained extractant</title><date>2000-05-31</date><risdate>2000</risdate><abstract>A process for separating and concentrating formic acid with phosphorus-contained extractant includes such steps as adding said extractant to kerosene, cascade extraction of the aqueous solution of formic acid with the mixed solvent, returning the extracted liquid (water phase) back to hydrolysis reactor, and distilling the solvent phase to obtain the formic acid with more than 85% of mass concentration. The mass concentration of formic acid in residual liquid is less than 2%. The temp of solvent recovery tower is 120-130 deg.C and after depressurized, its temp is lowered to 90-100 deg.C, so saving energy.</abstract><edition>7</edition><oa>free_for_read</oa></addata></record> |
fulltext | fulltext_linktorsrc |
identifier | |
ispartof | |
issn | |
language | eng |
recordid | cdi_epo_espacenet_CN1254705A |
source | esp@cenet |
subjects | ACYCLIC OR CARBOCYCLIC COMPOUNDS CHEMISTRY METALLURGY ORGANIC CHEMISTRY |
title | Process for separating and concentrating formic acid with phosphorus-contained extractant |
url | https://sfx.bib-bvb.de/sfx_tum?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2024-12-31T00%3A36%3A46IST&url_ver=Z39.88-2004&url_ctx_fmt=infofi/fmt:kev:mtx:ctx&rfr_id=info:sid/primo.exlibrisgroup.com:primo3-Article-epo_EVB&rft_val_fmt=info:ofi/fmt:kev:mtx:patent&rft.genre=patent&rft.au=XIANGLAN%20PU&rft.date=2000-05-31&rft_id=info:doi/&rft_dat=%3Cepo_EVB%3ECN1254705A%3C/epo_EVB%3E%3Curl%3E%3C/url%3E&disable_directlink=true&sfx.directlink=off&sfx.report_link=0&rft_id=info:oai/&rft_id=info:pmid/&rfr_iscdi=true |