PROCESS FOR THE CRYSTALLISATION OF DIFFICULTLY SOLUBLE MATERIALS AND CRYSTALLISATION APPARATUS FOR CARRYING OUT SUCH PROCESS

Materials dissolved up to satn. level in a solvent wherein they are difficult to dissolve in normal pressure and temp. conditions, esp. terephthalic acid in water, acetic acid, methanol or a mixt. of two of these, are crystallised by removal of heat from the soln. by passing over the soln. a dried c...

Ausführliche Beschreibung

Gespeichert in:
Bibliographische Detailangaben
Hauptverfasser: HADAMOVSKY EUGEN, SCHOENGEN ANTON, SCHROEDER HEINZ DR
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 HADAMOVSKY EUGEN
SCHOENGEN ANTON
SCHROEDER HEINZ DR
description Materials dissolved up to satn. level in a solvent wherein they are difficult to dissolve in normal pressure and temp. conditions, esp. terephthalic acid in water, acetic acid, methanol or a mixt. of two of these, are crystallised by removal of heat from the soln. by passing over the soln. a dried carrier gas which becomes charged with solvent vapour. The gas is then cooled, solvent is removed by condensation, absorption or adsorption, the gas is reheated and fed back into the soln. The gas is initially hotter than the soln. and is introduced below the liq. surface. The vapour pressure difference between the soln. at its entry point and in the container is 0-100 (3-60)bar. The appts. is also claimed. Suitable carrier gases include air, N, H, CO2 and inert gases. Applicable to the basic crystallising unit types with mixed or classified suspensions and mixed or classified prod. removal. The units are of moderate height, undesirably small crystals are not produced, and contamination by by-prods. is reduced.
format Patent
fullrecord <record><control><sourceid>epo_EVB</sourceid><recordid>TN_cdi_epo_espacenet_IN158101B</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><sourcerecordid>IN158101B</sourcerecordid><originalsourceid>FETCH-epo_espacenet_IN158101B3</originalsourceid><addsrcrecordid>eNqFjTEKwkAQRdNYiHoFmQsIBhFsJ5tdMzDuhtnZIlUIslaigVh6eAvTWVj95r33l8W7lWBsjOCCgDYWjHRRkZkiKgUPwUFNzpFJrNxBDJwqtnBBtULIEdDXPxK2LQpq-mYNinTkzxCSQkymgfl0XSxuw33Km3lXxdZZNc0uj88-T-NwzY_86smXx1O5L6vDX-ADlqs6nA</addsrcrecordid><sourcetype>Open Access Repository</sourcetype><iscdi>true</iscdi><recordtype>patent</recordtype></control><display><type>patent</type><title>PROCESS FOR THE CRYSTALLISATION OF DIFFICULTLY SOLUBLE MATERIALS AND CRYSTALLISATION APPARATUS FOR CARRYING OUT SUCH PROCESS</title><source>esp@cenet</source><creator>HADAMOVSKY EUGEN ; SCHOENGEN ANTON ; SCHROEDER HEINZ DR</creator><creatorcontrib>HADAMOVSKY EUGEN ; SCHOENGEN ANTON ; SCHROEDER HEINZ DR</creatorcontrib><description>Materials dissolved up to satn. level in a solvent wherein they are difficult to dissolve in normal pressure and temp. conditions, esp. terephthalic acid in water, acetic acid, methanol or a mixt. of two of these, are crystallised by removal of heat from the soln. by passing over the soln. a dried carrier gas which becomes charged with solvent vapour. The gas is then cooled, solvent is removed by condensation, absorption or adsorption, the gas is reheated and fed back into the soln. The gas is initially hotter than the soln. and is introduced below the liq. surface. The vapour pressure difference between the soln. at its entry point and in the container is 0-100 (3-60)bar. The appts. is also claimed. Suitable carrier gases include air, N, H, CO2 and inert gases. Applicable to the basic crystallising unit types with mixed or classified suspensions and mixed or classified prod. removal. The units are of moderate height, undesirably small crystals are not produced, and contamination by by-prods. is reduced.</description><edition>4</edition><language>eng</language><subject>ACYCLIC OR CARBOCYCLIC COMPOUNDS ; CHEMISTRY ; METALLURGY ; ORGANIC CHEMISTRY ; PERFORMING OPERATIONS ; PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL ; SEPARATION ; TRANSPORTING</subject><creationdate>1986</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&amp;date=19860906&amp;DB=EPODOC&amp;CC=IN&amp;NR=158101B$$EHTML$$P50$$Gepo$$Hfree_for_read</linktohtml><link.rule.ids>230,308,780,885,25563,76318</link.rule.ids><linktorsrc>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&amp;date=19860906&amp;DB=EPODOC&amp;CC=IN&amp;NR=158101B$$EView_record_in_European_Patent_Office$$FView_record_in_$$GEuropean_Patent_Office$$Hfree_for_read</linktorsrc></links><search><creatorcontrib>HADAMOVSKY EUGEN</creatorcontrib><creatorcontrib>SCHOENGEN ANTON</creatorcontrib><creatorcontrib>SCHROEDER HEINZ DR</creatorcontrib><title>PROCESS FOR THE CRYSTALLISATION OF DIFFICULTLY SOLUBLE MATERIALS AND CRYSTALLISATION APPARATUS FOR CARRYING OUT SUCH PROCESS</title><description>Materials dissolved up to satn. level in a solvent wherein they are difficult to dissolve in normal pressure and temp. conditions, esp. terephthalic acid in water, acetic acid, methanol or a mixt. of two of these, are crystallised by removal of heat from the soln. by passing over the soln. a dried carrier gas which becomes charged with solvent vapour. The gas is then cooled, solvent is removed by condensation, absorption or adsorption, the gas is reheated and fed back into the soln. The gas is initially hotter than the soln. and is introduced below the liq. surface. The vapour pressure difference between the soln. at its entry point and in the container is 0-100 (3-60)bar. The appts. is also claimed. Suitable carrier gases include air, N, H, CO2 and inert gases. Applicable to the basic crystallising unit types with mixed or classified suspensions and mixed or classified prod. removal. The units are of moderate height, undesirably small crystals are not produced, and contamination by by-prods. is reduced.</description><subject>ACYCLIC OR CARBOCYCLIC COMPOUNDS</subject><subject>CHEMISTRY</subject><subject>METALLURGY</subject><subject>ORGANIC CHEMISTRY</subject><subject>PERFORMING OPERATIONS</subject><subject>PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL</subject><subject>SEPARATION</subject><subject>TRANSPORTING</subject><fulltext>true</fulltext><rsrctype>patent</rsrctype><creationdate>1986</creationdate><recordtype>patent</recordtype><sourceid>EVB</sourceid><recordid>eNqFjTEKwkAQRdNYiHoFmQsIBhFsJ5tdMzDuhtnZIlUIslaigVh6eAvTWVj95r33l8W7lWBsjOCCgDYWjHRRkZkiKgUPwUFNzpFJrNxBDJwqtnBBtULIEdDXPxK2LQpq-mYNinTkzxCSQkymgfl0XSxuw33Km3lXxdZZNc0uj88-T-NwzY_86smXx1O5L6vDX-ADlqs6nA</recordid><startdate>19860906</startdate><enddate>19860906</enddate><creator>HADAMOVSKY EUGEN</creator><creator>SCHOENGEN ANTON</creator><creator>SCHROEDER HEINZ DR</creator><scope>EVB</scope></search><sort><creationdate>19860906</creationdate><title>PROCESS FOR THE CRYSTALLISATION OF DIFFICULTLY SOLUBLE MATERIALS AND CRYSTALLISATION APPARATUS FOR CARRYING OUT SUCH PROCESS</title><author>HADAMOVSKY EUGEN ; SCHOENGEN ANTON ; SCHROEDER HEINZ DR</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-epo_espacenet_IN158101B3</frbrgroupid><rsrctype>patents</rsrctype><prefilter>patents</prefilter><language>eng</language><creationdate>1986</creationdate><topic>ACYCLIC OR CARBOCYCLIC COMPOUNDS</topic><topic>CHEMISTRY</topic><topic>METALLURGY</topic><topic>ORGANIC CHEMISTRY</topic><topic>PERFORMING OPERATIONS</topic><topic>PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL</topic><topic>SEPARATION</topic><topic>TRANSPORTING</topic><toplevel>online_resources</toplevel><creatorcontrib>HADAMOVSKY EUGEN</creatorcontrib><creatorcontrib>SCHOENGEN ANTON</creatorcontrib><creatorcontrib>SCHROEDER HEINZ DR</creatorcontrib><collection>esp@cenet</collection></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext_linktorsrc</fulltext></delivery><addata><au>HADAMOVSKY EUGEN</au><au>SCHOENGEN ANTON</au><au>SCHROEDER HEINZ DR</au><format>patent</format><genre>patent</genre><ristype>GEN</ristype><title>PROCESS FOR THE CRYSTALLISATION OF DIFFICULTLY SOLUBLE MATERIALS AND CRYSTALLISATION APPARATUS FOR CARRYING OUT SUCH PROCESS</title><date>1986-09-06</date><risdate>1986</risdate><abstract>Materials dissolved up to satn. level in a solvent wherein they are difficult to dissolve in normal pressure and temp. conditions, esp. terephthalic acid in water, acetic acid, methanol or a mixt. of two of these, are crystallised by removal of heat from the soln. by passing over the soln. a dried carrier gas which becomes charged with solvent vapour. The gas is then cooled, solvent is removed by condensation, absorption or adsorption, the gas is reheated and fed back into the soln. The gas is initially hotter than the soln. and is introduced below the liq. surface. The vapour pressure difference between the soln. at its entry point and in the container is 0-100 (3-60)bar. The appts. is also claimed. Suitable carrier gases include air, N, H, CO2 and inert gases. Applicable to the basic crystallising unit types with mixed or classified suspensions and mixed or classified prod. removal. The units are of moderate height, undesirably small crystals are not produced, and contamination by by-prods. is reduced.</abstract><edition>4</edition><oa>free_for_read</oa></addata></record>
fulltext fulltext_linktorsrc
identifier
ispartof
issn
language eng
recordid cdi_epo_espacenet_IN158101B
source esp@cenet
subjects ACYCLIC OR CARBOCYCLIC COMPOUNDS
CHEMISTRY
METALLURGY
ORGANIC CHEMISTRY
PERFORMING OPERATIONS
PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
SEPARATION
TRANSPORTING
title PROCESS FOR THE CRYSTALLISATION OF DIFFICULTLY SOLUBLE MATERIALS AND CRYSTALLISATION APPARATUS FOR CARRYING OUT SUCH PROCESS
url https://sfx.bib-bvb.de/sfx_tum?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2025-01-13T10%3A39%3A53IST&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=HADAMOVSKY%20EUGEN&rft.date=1986-09-06&rft_id=info:doi/&rft_dat=%3Cepo_EVB%3EIN158101B%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