PROCESS AND APPARATUS FOR REMOVING GASEOUS CONTAMINANTS FROM GAS STREAM COMPRISING GASEOUS CONTAMINANTS
THE INVENTION PROVIDES A PROCESS AND A DEVICE FOR REMOVING GASEOUS CONTAMINANTS FROM A FEED GAS STREAM WHICH COMPRISES METHANE AND GASEOUS CONTAMINANTS, IN WHICH PROCESS THE TEED GAS STREAM IS COOLED TO OBTAIN A SLURRY WHICH COMPRISES SOLID CONTAMINANT, LIQUID PHASE CONTAMINANT AND A METHANE ENRICHE...
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creator | GEERS, HENRICUS ABRAHAM VAN SANTEN, HELMAR |
description | THE INVENTION PROVIDES A PROCESS AND A DEVICE FOR REMOVING GASEOUS CONTAMINANTS FROM A FEED GAS STREAM WHICH COMPRISES METHANE AND GASEOUS CONTAMINANTS, IN WHICH PROCESS THE TEED GAS STREAM IS COOLED TO OBTAIN A SLURRY WHICH COMPRISES SOLID CONTAMINANT, LIQUID PHASE CONTAMINANT AND A METHANE ENRICHED GASEOUS PHASE, THE SLURRY SO OBTAINED IS INTRODUCED INTO A CRYOGENIC SEPARATION DEVICE (4) IN WHICH FROM THE TOP THE METHANE ENRICHED GASEOUS PHASE IS REMOVED (5), THE SLURRY IS DILUTED WITH LIQUID PHASE CONTAMINANT (6) AND INTRODUCED AS SUCTIOR.FLUID INTO AN EJECTOR (9) VIA WHICH IT IS PASSED INTO A HEAT EXCHANGER (10) ARRANGED OUTSIDE THE SEPARATION DEVICE AND WHEREIN SOLID CONTAMINANT IS MELTED INTO LIQUID PHASE CONTAMINANT, PART OF THE LIQUID PHASE CONTAMINANT SO OBTAINED IS RECYCLED (6) TO DILUTE THE SLURRY OF CONTAMINANTS INSIDE THE SEPARATION DEVICE AND PART (13) IS INTRODUCED INTO THE BOTTOM PART OF THE SEPARATION DEVICE, LIQUID PHASE IS WITHDRAWN (14) FROM THE BOTTOM PART OF THE SEPARATION DEVICE, AND PART OF THE WITHDRAWN LIQUID PHASE CONTAMINANT IS RECOVERED AS A STREAM PROAUCT (16) AND PART IS RECYCLED (17) TO THE EJECTOR FOR USE A MOTIVE FLUID. |
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CONTAMINANTS FROM A FEED GAS STREAM WHICH COMPRISES METHANE AND GASEOUS CONTAMINANTS, IN WHICH PROCESS THE TEED GAS STREAM IS COOLED TO OBTAIN A SLURRY WHICH COMPRISES SOLID CONTAMINANT, LIQUID PHASE CONTAMINANT AND A METHANE ENRICHED GASEOUS PHASE, THE SLURRY SO OBTAINED IS INTRODUCED INTO A CRYOGENIC SEPARATION DEVICE (4) IN WHICH FROM THE TOP THE METHANE ENRICHED GASEOUS PHASE IS REMOVED (5), THE SLURRY IS DILUTED WITH LIQUID PHASE CONTAMINANT (6) AND INTRODUCED AS SUCTIOR.FLUID INTO AN EJECTOR (9) VIA WHICH IT IS PASSED INTO A HEAT EXCHANGER (10) ARRANGED OUTSIDE THE SEPARATION DEVICE AND WHEREIN SOLID CONTAMINANT IS MELTED INTO LIQUID PHASE CONTAMINANT, PART OF THE LIQUID PHASE CONTAMINANT SO OBTAINED IS RECYCLED (6) TO DILUTE THE SLURRY OF CONTAMINANTS INSIDE THE SEPARATION DEVICE AND PART (13) IS INTRODUCED INTO THE BOTTOM PART OF THE SEPARATION DEVICE, LIQUID PHASE IS WITHDRAWN (14) FROM THE BOTTOM PART OF THE SEPARATION DEVICE, AND PART OF THE WITHDRAWN LIQUID PHASE 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PROPERTIES ; SEPARATION ; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BYSUBCLASSES C10G, C10K ; TECHNICAL GASES CONTAINING CARBON MONOXIDE ; TRANSFORMERS ; TRANSPORTING ; WEAPONS</subject><creationdate>2017</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=20170714&DB=EPODOC&CC=MY&NR=162713A$$EHTML$$P50$$Gepo$$Hfree_for_read</linktohtml><link.rule.ids>230,308,780,885,25563,76318</link.rule.ids><linktorsrc>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&date=20170714&DB=EPODOC&CC=MY&NR=162713A$$EView_record_in_European_Patent_Office$$FView_record_in_$$GEuropean_Patent_Office$$Hfree_for_read</linktorsrc></links><search><creatorcontrib>GEERS, HENRICUS ABRAHAM</creatorcontrib><creatorcontrib>VAN SANTEN, HELMAR</creatorcontrib><title>PROCESS AND APPARATUS FOR REMOVING GASEOUS CONTAMINANTS FROM GAS STREAM COMPRISING GASEOUS CONTAMINANTS</title><description>THE INVENTION PROVIDES A PROCESS AND A DEVICE FOR REMOVING GASEOUS CONTAMINANTS FROM A FEED GAS STREAM WHICH COMPRISES METHANE AND GASEOUS CONTAMINANTS, IN WHICH PROCESS THE TEED GAS STREAM IS COOLED TO OBTAIN A SLURRY WHICH COMPRISES SOLID CONTAMINANT, LIQUID PHASE CONTAMINANT AND A METHANE ENRICHED GASEOUS PHASE, THE SLURRY SO OBTAINED IS INTRODUCED INTO A CRYOGENIC SEPARATION DEVICE (4) IN WHICH FROM THE TOP THE METHANE ENRICHED GASEOUS PHASE IS REMOVED (5), THE SLURRY IS DILUTED WITH LIQUID PHASE CONTAMINANT (6) AND INTRODUCED AS SUCTIOR.FLUID INTO AN EJECTOR (9) VIA WHICH IT IS PASSED INTO A HEAT EXCHANGER (10) ARRANGED OUTSIDE THE SEPARATION DEVICE AND WHEREIN SOLID CONTAMINANT IS MELTED INTO LIQUID PHASE CONTAMINANT, PART OF THE LIQUID PHASE CONTAMINANT SO OBTAINED IS RECYCLED (6) TO DILUTE THE SLURRY OF CONTAMINANTS INSIDE THE SEPARATION DEVICE AND PART (13) IS INTRODUCED INTO THE BOTTOM PART OF THE SEPARATION DEVICE, LIQUID PHASE IS WITHDRAWN (14) FROM THE BOTTOM PART OF THE SEPARATION DEVICE, AND PART OF THE WITHDRAWN LIQUID PHASE CONTAMINANT IS RECOVERED AS A STREAM PROAUCT (16) AND PART IS RECYCLED (17) TO THE EJECTOR FOR USE A MOTIVE FLUID.</description><subject>ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE ORUNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL</subject><subject>BASIC ELECTRIC ELEMENTS</subject><subject>BLASTING</subject><subject>CHEMISTRY</subject><subject>COMBINED HEATING AND REFRIGERATION SYSTEMS</subject><subject>CURRENT COLLECTORS</subject><subject>ELECTRICITY</subject><subject>FIRELIGHTERS</subject><subject>FUELS</subject><subject>FUELS NOT OTHERWISE PROVIDED FOR</subject><subject>HEAT PUMP SYSTEMS</subject><subject>HEATING</subject><subject>INDUCTANCES</subject><subject>LIGHTING</subject><subject>LINE CONNECTORS</subject><subject>LIQUEFACTION SOLIDIFICATION OF GASES</subject><subject>LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS</subject><subject>LIQUEFIED PETROLEUM GAS</subject><subject>LUBRICANTS</subject><subject>MAGNETS</subject><subject>MANUFACTURE OR STORAGE OF ICE</subject><subject>MECHANICAL ENGINEERING</subject><subject>METALLURGY</subject><subject>MIXTURES BY PRESSURE AND COLD TREATMENT</subject><subject>NATURAL GAS</subject><subject>PEAT</subject><subject>PERFORMING OPERATIONS</subject><subject>PETROLEUM, GAS OR COKE INDUSTRIES</subject><subject>PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL</subject><subject>REFRIGERATION OR COOLING</subject><subject>SELECTION OF MATERIALS FOR THEIR MAGNETIC PROPERTIES</subject><subject>SEPARATION</subject><subject>SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BYSUBCLASSES C10G, C10K</subject><subject>TECHNICAL GASES CONTAINING CARBON MONOXIDE</subject><subject>TRANSFORMERS</subject><subject>TRANSPORTING</subject><subject>WEAPONS</subject><fulltext>true</fulltext><rsrctype>patent</rsrctype><creationdate>2017</creationdate><recordtype>patent</recordtype><sourceid>EVB</sourceid><recordid>eNrjZEgPCPJ3dg0OVnD0c1FwDAhwDHIMCQ1WcPMPUghy9fUP8_RzV3B3DHb1Bwo6-_uFOPp6-jn6hQBVBPn7gmQUgkOCXB19gZK-AUGewbjU8zCwpiXmFKfyQmluBjk31xBnD93Ugvz41OKCxOTUvNSSeN9IQzMjc0NjR2OCCgD74DTN</recordid><startdate>20170714</startdate><enddate>20170714</enddate><creator>GEERS, HENRICUS ABRAHAM</creator><creator>VAN SANTEN, HELMAR</creator><scope>EVB</scope></search><sort><creationdate>20170714</creationdate><title>PROCESS AND APPARATUS FOR REMOVING GASEOUS CONTAMINANTS FROM GAS STREAM COMPRISING GASEOUS CONTAMINANTS</title><author>GEERS, HENRICUS ABRAHAM ; VAN SANTEN, HELMAR</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-epo_espacenet_MY162713A3</frbrgroupid><rsrctype>patents</rsrctype><prefilter>patents</prefilter><language>eng</language><creationdate>2017</creationdate><topic>ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE ORUNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL</topic><topic>BASIC ELECTRIC ELEMENTS</topic><topic>BLASTING</topic><topic>CHEMISTRY</topic><topic>COMBINED HEATING AND REFRIGERATION SYSTEMS</topic><topic>CURRENT COLLECTORS</topic><topic>ELECTRICITY</topic><topic>FIRELIGHTERS</topic><topic>FUELS</topic><topic>FUELS NOT OTHERWISE PROVIDED FOR</topic><topic>HEAT PUMP SYSTEMS</topic><topic>HEATING</topic><topic>INDUCTANCES</topic><topic>LIGHTING</topic><topic>LINE CONNECTORS</topic><topic>LIQUEFACTION SOLIDIFICATION OF GASES</topic><topic>LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS</topic><topic>LIQUEFIED PETROLEUM GAS</topic><topic>LUBRICANTS</topic><topic>MAGNETS</topic><topic>MANUFACTURE OR STORAGE OF ICE</topic><topic>MECHANICAL ENGINEERING</topic><topic>METALLURGY</topic><topic>MIXTURES BY PRESSURE AND COLD TREATMENT</topic><topic>NATURAL GAS</topic><topic>PEAT</topic><topic>PERFORMING OPERATIONS</topic><topic>PETROLEUM, GAS OR COKE INDUSTRIES</topic><topic>PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL</topic><topic>REFRIGERATION OR COOLING</topic><topic>SELECTION OF MATERIALS FOR THEIR MAGNETIC PROPERTIES</topic><topic>SEPARATION</topic><topic>SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BYSUBCLASSES C10G, C10K</topic><topic>TECHNICAL GASES CONTAINING CARBON MONOXIDE</topic><topic>TRANSFORMERS</topic><topic>TRANSPORTING</topic><topic>WEAPONS</topic><toplevel>online_resources</toplevel><creatorcontrib>GEERS, HENRICUS ABRAHAM</creatorcontrib><creatorcontrib>VAN SANTEN, HELMAR</creatorcontrib><collection>esp@cenet</collection></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext_linktorsrc</fulltext></delivery><addata><au>GEERS, HENRICUS ABRAHAM</au><au>VAN SANTEN, HELMAR</au><format>patent</format><genre>patent</genre><ristype>GEN</ristype><title>PROCESS AND APPARATUS FOR REMOVING GASEOUS CONTAMINANTS FROM GAS STREAM COMPRISING GASEOUS CONTAMINANTS</title><date>2017-07-14</date><risdate>2017</risdate><abstract>THE INVENTION PROVIDES A PROCESS AND A DEVICE FOR REMOVING GASEOUS CONTAMINANTS FROM A FEED GAS STREAM WHICH COMPRISES METHANE AND GASEOUS CONTAMINANTS, IN WHICH PROCESS THE TEED GAS STREAM IS COOLED TO OBTAIN A SLURRY WHICH COMPRISES SOLID CONTAMINANT, LIQUID PHASE CONTAMINANT AND A METHANE ENRICHED GASEOUS PHASE, THE SLURRY SO OBTAINED IS INTRODUCED INTO A CRYOGENIC SEPARATION DEVICE (4) IN WHICH FROM THE TOP THE METHANE ENRICHED GASEOUS PHASE IS REMOVED (5), THE SLURRY IS DILUTED WITH LIQUID PHASE CONTAMINANT (6) AND INTRODUCED AS SUCTIOR.FLUID INTO AN EJECTOR (9) VIA WHICH IT IS PASSED INTO A HEAT EXCHANGER (10) ARRANGED OUTSIDE THE SEPARATION DEVICE AND WHEREIN SOLID CONTAMINANT IS MELTED INTO LIQUID PHASE CONTAMINANT, PART OF THE LIQUID PHASE CONTAMINANT SO OBTAINED IS RECYCLED (6) TO DILUTE THE SLURRY OF CONTAMINANTS INSIDE THE SEPARATION DEVICE AND PART (13) IS INTRODUCED INTO THE BOTTOM PART OF THE SEPARATION DEVICE, LIQUID PHASE IS WITHDRAWN (14) FROM THE BOTTOM PART OF THE SEPARATION DEVICE, AND PART OF THE WITHDRAWN LIQUID PHASE CONTAMINANT IS RECOVERED AS A STREAM PROAUCT (16) AND PART IS RECYCLED (17) TO THE EJECTOR FOR USE A MOTIVE FLUID.</abstract><oa>free_for_read</oa></addata></record> |
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subjects | ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE ORUNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL BASIC ELECTRIC ELEMENTS BLASTING CHEMISTRY COMBINED HEATING AND REFRIGERATION SYSTEMS CURRENT COLLECTORS ELECTRICITY FIRELIGHTERS FUELS FUELS NOT OTHERWISE PROVIDED FOR HEAT PUMP SYSTEMS HEATING INDUCTANCES LIGHTING LINE CONNECTORS LIQUEFACTION SOLIDIFICATION OF GASES LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS LIQUEFIED PETROLEUM GAS LUBRICANTS MAGNETS MANUFACTURE OR STORAGE OF ICE MECHANICAL ENGINEERING METALLURGY MIXTURES BY PRESSURE AND COLD TREATMENT NATURAL GAS PEAT PERFORMING OPERATIONS PETROLEUM, GAS OR COKE INDUSTRIES PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL REFRIGERATION OR COOLING SELECTION OF MATERIALS FOR THEIR MAGNETIC PROPERTIES SEPARATION SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BYSUBCLASSES C10G, C10K TECHNICAL GASES CONTAINING CARBON MONOXIDE TRANSFORMERS TRANSPORTING WEAPONS |
title | PROCESS AND APPARATUS FOR REMOVING GASEOUS CONTAMINANTS FROM GAS STREAM COMPRISING GASEOUS CONTAMINANTS |
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