http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-4248608-A

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http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_566c0ba83d6f43c65ee3525f835faed1
classificationCPCInventive http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D53-1425
classificationIPCInventive http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D3-14
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D53-14
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D3-00
filingDate 1979-04-27^^<http://www.w3.org/2001/XMLSchema#date>
grantDate 1981-02-03^^<http://www.w3.org/2001/XMLSchema#date>
inventor http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_f40aadb060c67e301ea83b7134ad1bf2
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_09511a3b12312dc7405aee6bbce6b823
publicationDate 1981-02-03^^<http://www.w3.org/2001/XMLSchema#date>
publicationNumber US-4248608-A
titleOfInvention Process for purifying liquids and/or regenerating absorbent solutions
abstract The process for the purification of liquids and in particular the regeneration of spent absorbent solutions is essentially based on the use of a first preliminary regeneration zone to which the entire solution to be purified is delivered and the use of two terminal regeneration zones operating respectively at a higher and a lower pressure. The semi-regenerated solution issuing from the preliminary purification zone is split into two fractions which are delivered respectively to the low pressure and the high pressure terminal zones. The fraction delivered to the high pressure terminal zone is regenerated by steam yielded by means of the supply of external heat to the bottom of the zone. The fraction delivered to the low pressure terminal zone is regenerated by steam produced by heat recovered from the high pressure terminal zone.
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http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-2008127831-A1
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-2006032377-A1
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-7485274-B2
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priorityDate 1978-04-27^^<http://www.w3.org/2001/XMLSchema#date>
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