Device for seperating gas from liquid
A gas-liquid separating apparatus capable of sufficiently separating gas in gas-liquid mixture fluid from liquid therein, is disclosed. Gas-liquid mixture fluid fed from a boiler evaporator tube enters through a separator inlet 15 into a cylinder 9 of a separator 12 in a tangential direction, thus b...
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creator | YASUSHI MORI NOBUHIRO HOKAO TOKUJI MATSUO |
description | A gas-liquid separating apparatus capable of sufficiently separating gas in gas-liquid mixture fluid from liquid therein, is disclosed. Gas-liquid mixture fluid fed from a boiler evaporator tube enters through a separator inlet 15 into a cylinder 9 of a separator 12 in a tangential direction, thus becomes a rotating flow 8 along the inner wall surface of the cylinder 9, and thereby centrifugal separation between gas and liquid is effected. The separated steam is discharged from a secondary separator 11 through a cap 18 into a gas-phase section within a drum 1. A part of the primary isolated water 8 of the rotating flow has its outflow velocity decelerated by a perforated plate 23, and thereafter flows out to a liquid-phase section within the drum 1. As a result, a flow velocity of the primary isolated water 20 flowing out through a primary isolated water outlet 17 to the liquid-phase section within the drum 1 is decreased as compared to the case where the prior art was employed, and hence, an amount of the primary isolated water drawn into a flow 22 within the drum is reduced. Moreover, since the primary isolated water 21 having flowed out through the perforated plate 23 to the liquid-phase section within the drum 1 has a slow outflow velocity, it becomes an upward blow in the vicinity of the cylinder 9 due to influence of a buoyancy acting upon a steam component. Accordingly, the time available for gravitational separation of gas and liquid in the liquid phase within the drum 1 can be reserved longer than in the case of employing the prior art. |
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fullrecord | <record><control><sourceid>epo_EVB</sourceid><recordid>TN_cdi_epo_espacenet_CN1104743A</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><sourcerecordid>CN1104743A</sourcerecordid><originalsourceid>FETCH-epo_espacenet_CN1104743A3</originalsourceid><addsrcrecordid>eNrjZFB1SS3LTE5VSMsvUihOLUgtSizJzEtXSE8sVkgrys9VyMksLM1M4WFgTUvMKU7lhdLcDPJuriHOHrqpBfnxqcUFicmpeakl8c5-hoYGJuYmxo7GhFUAAI5xJhA</addsrcrecordid><sourcetype>Open Access Repository</sourcetype><iscdi>true</iscdi><recordtype>patent</recordtype></control><display><type>patent</type><title>Device for seperating gas from liquid</title><source>esp@cenet</source><creator>YASUSHI MORI ; NOBUHIRO HOKAO ; TOKUJI MATSUO</creator><creatorcontrib>YASUSHI MORI ; NOBUHIRO HOKAO ; TOKUJI MATSUO</creatorcontrib><description>A gas-liquid separating apparatus capable of sufficiently separating gas in gas-liquid mixture fluid from liquid therein, is disclosed. Gas-liquid mixture fluid fed from a boiler evaporator tube enters through a separator inlet 15 into a cylinder 9 of a separator 12 in a tangential direction, thus becomes a rotating flow 8 along the inner wall surface of the cylinder 9, and thereby centrifugal separation between gas and liquid is effected. The separated steam is discharged from a secondary separator 11 through a cap 18 into a gas-phase section within a drum 1. A part of the primary isolated water 8 of the rotating flow has its outflow velocity decelerated by a perforated plate 23, and thereafter flows out to a liquid-phase section within the drum 1. As a result, a flow velocity of the primary isolated water 20 flowing out through a primary isolated water outlet 17 to the liquid-phase section within the drum 1 is decreased as compared to the case where the prior art was employed, and hence, an amount of the primary isolated water drawn into a flow 22 within the drum is reduced. Moreover, since the primary isolated water 21 having flowed out through the perforated plate 23 to the liquid-phase section within the drum 1 has a slow outflow velocity, it becomes an upward blow in the vicinity of the cylinder 9 due to influence of a buoyancy acting upon a steam component. Accordingly, the time available for gravitational separation of gas and liquid in the liquid phase within the drum 1 can be reserved longer than in the case of employing the prior art.</description><edition>5</edition><language>eng</language><subject>BLASTING ; HEATING ; LIGHTING ; MECHANICAL ENGINEERING ; METHODS OF STEAM GENERATION ; PERFORMING OPERATIONS ; PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL ; SEPARATION ; STEAM BOILERS ; STEAM GENERATION ; TRANSPORTING ; WEAPONS</subject><creationdate>1995</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=19950705&DB=EPODOC&CC=CN&NR=1104743A$$EHTML$$P50$$Gepo$$Hfree_for_read</linktohtml><link.rule.ids>230,308,777,882,25545,76296</link.rule.ids><linktorsrc>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&date=19950705&DB=EPODOC&CC=CN&NR=1104743A$$EView_record_in_European_Patent_Office$$FView_record_in_$$GEuropean_Patent_Office$$Hfree_for_read</linktorsrc></links><search><creatorcontrib>YASUSHI MORI</creatorcontrib><creatorcontrib>NOBUHIRO HOKAO</creatorcontrib><creatorcontrib>TOKUJI MATSUO</creatorcontrib><title>Device for seperating gas from liquid</title><description>A gas-liquid separating apparatus capable of sufficiently separating gas in gas-liquid mixture fluid from liquid therein, is disclosed. Gas-liquid mixture fluid fed from a boiler evaporator tube enters through a separator inlet 15 into a cylinder 9 of a separator 12 in a tangential direction, thus becomes a rotating flow 8 along the inner wall surface of the cylinder 9, and thereby centrifugal separation between gas and liquid is effected. The separated steam is discharged from a secondary separator 11 through a cap 18 into a gas-phase section within a drum 1. A part of the primary isolated water 8 of the rotating flow has its outflow velocity decelerated by a perforated plate 23, and thereafter flows out to a liquid-phase section within the drum 1. As a result, a flow velocity of the primary isolated water 20 flowing out through a primary isolated water outlet 17 to the liquid-phase section within the drum 1 is decreased as compared to the case where the prior art was employed, and hence, an amount of the primary isolated water drawn into a flow 22 within the drum is reduced. Moreover, since the primary isolated water 21 having flowed out through the perforated plate 23 to the liquid-phase section within the drum 1 has a slow outflow velocity, it becomes an upward blow in the vicinity of the cylinder 9 due to influence of a buoyancy acting upon a steam component. Accordingly, the time available for gravitational separation of gas and liquid in the liquid phase within the drum 1 can be reserved longer than in the case of employing the prior art.</description><subject>BLASTING</subject><subject>HEATING</subject><subject>LIGHTING</subject><subject>MECHANICAL ENGINEERING</subject><subject>METHODS OF STEAM GENERATION</subject><subject>PERFORMING OPERATIONS</subject><subject>PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL</subject><subject>SEPARATION</subject><subject>STEAM BOILERS</subject><subject>STEAM GENERATION</subject><subject>TRANSPORTING</subject><subject>WEAPONS</subject><fulltext>true</fulltext><rsrctype>patent</rsrctype><creationdate>1995</creationdate><recordtype>patent</recordtype><sourceid>EVB</sourceid><recordid>eNrjZFB1SS3LTE5VSMsvUihOLUgtSizJzEtXSE8sVkgrys9VyMksLM1M4WFgTUvMKU7lhdLcDPJuriHOHrqpBfnxqcUFicmpeakl8c5-hoYGJuYmxo7GhFUAAI5xJhA</recordid><startdate>19950705</startdate><enddate>19950705</enddate><creator>YASUSHI MORI</creator><creator>NOBUHIRO HOKAO</creator><creator>TOKUJI MATSUO</creator><scope>EVB</scope></search><sort><creationdate>19950705</creationdate><title>Device for seperating gas from liquid</title><author>YASUSHI MORI ; NOBUHIRO HOKAO ; TOKUJI MATSUO</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-epo_espacenet_CN1104743A3</frbrgroupid><rsrctype>patents</rsrctype><prefilter>patents</prefilter><language>eng</language><creationdate>1995</creationdate><topic>BLASTING</topic><topic>HEATING</topic><topic>LIGHTING</topic><topic>MECHANICAL ENGINEERING</topic><topic>METHODS OF STEAM GENERATION</topic><topic>PERFORMING OPERATIONS</topic><topic>PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL</topic><topic>SEPARATION</topic><topic>STEAM BOILERS</topic><topic>STEAM GENERATION</topic><topic>TRANSPORTING</topic><topic>WEAPONS</topic><toplevel>online_resources</toplevel><creatorcontrib>YASUSHI MORI</creatorcontrib><creatorcontrib>NOBUHIRO HOKAO</creatorcontrib><creatorcontrib>TOKUJI MATSUO</creatorcontrib><collection>esp@cenet</collection></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext_linktorsrc</fulltext></delivery><addata><au>YASUSHI MORI</au><au>NOBUHIRO HOKAO</au><au>TOKUJI MATSUO</au><format>patent</format><genre>patent</genre><ristype>GEN</ristype><title>Device for seperating gas from liquid</title><date>1995-07-05</date><risdate>1995</risdate><abstract>A gas-liquid separating apparatus capable of sufficiently separating gas in gas-liquid mixture fluid from liquid therein, is disclosed. Gas-liquid mixture fluid fed from a boiler evaporator tube enters through a separator inlet 15 into a cylinder 9 of a separator 12 in a tangential direction, thus becomes a rotating flow 8 along the inner wall surface of the cylinder 9, and thereby centrifugal separation between gas and liquid is effected. The separated steam is discharged from a secondary separator 11 through a cap 18 into a gas-phase section within a drum 1. A part of the primary isolated water 8 of the rotating flow has its outflow velocity decelerated by a perforated plate 23, and thereafter flows out to a liquid-phase section within the drum 1. As a result, a flow velocity of the primary isolated water 20 flowing out through a primary isolated water outlet 17 to the liquid-phase section within the drum 1 is decreased as compared to the case where the prior art was employed, and hence, an amount of the primary isolated water drawn into a flow 22 within the drum is reduced. Moreover, since the primary isolated water 21 having flowed out through the perforated plate 23 to the liquid-phase section within the drum 1 has a slow outflow velocity, it becomes an upward blow in the vicinity of the cylinder 9 due to influence of a buoyancy acting upon a steam component. Accordingly, the time available for gravitational separation of gas and liquid in the liquid phase within the drum 1 can be reserved longer than in the case of employing the prior art.</abstract><edition>5</edition><oa>free_for_read</oa></addata></record> |
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subjects | BLASTING HEATING LIGHTING MECHANICAL ENGINEERING METHODS OF STEAM GENERATION PERFORMING OPERATIONS PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL SEPARATION STEAM BOILERS STEAM GENERATION TRANSPORTING WEAPONS |
title | Device for seperating gas from liquid |
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