Oil LNG gasifaction fractional distillation apparatus
The utility model relates to an oil LNG gasifaction fractional distillation apparatus, including depropanizator, return tank and deethanizer, be provided with feeding control valve on the third pipeline, be provided with ejection of compact control valve on the fourth pipeline, be connected with the...
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| creator | SHOU LUYANG CHEN ZUNZHONG LI FENG YANG CHUNLIANG ZHANG RONGFANG ZHANG QIAOMIN YU LIANSHI |
| description | The utility model relates to an oil LNG gasifaction fractional distillation apparatus, including depropanizator, return tank and deethanizer, be provided with feeding control valve on the third pipeline, be provided with ejection of compact control valve on the fourth pipeline, be connected with the 5th pipeline between feeding control valve and the ejection of compact control valve, and be provided with the pipeline governing valve on the 5th pipeline. The utility model discloses increased the cross -line between feeding control valve the deethanizer before and the ejection of compact control valve after the deethanizer, in the time of need not utilizing component such as deethanizer desorption C2 when refined carbon no. 3, the tank field is delivered to with C3 component autogenous pressure to accessible regulation feeding control valve, ejection of compact control valve, pipeline governing valve, when needs used deethanizer, feeding control valve was opened to the closed pipeline governing valve, and it ca |
| format | Patent |
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The utility model discloses increased the cross -line between feeding control valve the deethanizer before and the ejection of compact control valve after the deethanizer, in the time of need not utilizing component such as deethanizer desorption C2 when refined carbon no. 3, the tank field is delivered to with C3 component autogenous pressure to accessible regulation feeding control valve, ejection of compact control valve, pipeline governing valve, when needs used deethanizer, feeding control valve was opened to the closed pipeline governing valve, and it ca</description><language>chi ; eng</language><subject>CHEMISTRY ; CRACKING HYDROCARBON OILS ; FUELS ; LUBRICANTS ; METALLURGY ; MINERAL WAXES ; PEAT ; PETROLEUM, GAS OR COKE INDUSTRIES ; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVEHYDROGENATION, OLIGOMERISATION, POLYMERISATION ; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, ORGASES ; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS ; REFORMING OF NAPHTHA ; TECHNICAL GASES CONTAINING CARBON MONOXIDE</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=20170118&DB=EPODOC&CC=CN&NR=205893172U$$EHTML$$P50$$Gepo$$Hfree_for_read</linktohtml><link.rule.ids>230,309,781,886,25569,76552</link.rule.ids><linktorsrc>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&date=20170118&DB=EPODOC&CC=CN&NR=205893172U$$EView_record_in_European_Patent_Office$$FView_record_in_$$GEuropean_Patent_Office$$Hfree_for_read</linktorsrc></links><search><creatorcontrib>SHOU LUYANG</creatorcontrib><creatorcontrib>CHEN ZUNZHONG</creatorcontrib><creatorcontrib>LI FENG</creatorcontrib><creatorcontrib>YANG CHUNLIANG</creatorcontrib><creatorcontrib>ZHANG RONGFANG</creatorcontrib><creatorcontrib>ZHANG QIAOMIN</creatorcontrib><creatorcontrib>YU LIANSHI</creatorcontrib><title>Oil LNG gasifaction fractional distillation apparatus</title><description>The utility model relates to an oil LNG gasifaction fractional distillation apparatus, including depropanizator, return tank and deethanizer, be provided with feeding control valve on the third pipeline, be provided with ejection of compact control valve on the fourth pipeline, be connected with the 5th pipeline between feeding control valve and the ejection of compact control valve, and be provided with the pipeline governing valve on the 5th pipeline. The utility model discloses increased the cross -line between feeding control valve the deethanizer before and the ejection of compact control valve after the deethanizer, in the time of need not utilizing component such as deethanizer desorption C2 when refined carbon no. 3, the tank field is delivered to with C3 component autogenous pressure to accessible regulation feeding control valve, ejection of compact control valve, pipeline governing valve, when needs used deethanizer, feeding control valve was opened to the closed pipeline governing valve, and it ca</description><subject>CHEMISTRY</subject><subject>CRACKING HYDROCARBON OILS</subject><subject>FUELS</subject><subject>LUBRICANTS</subject><subject>METALLURGY</subject><subject>MINERAL WAXES</subject><subject>PEAT</subject><subject>PETROLEUM, GAS OR COKE INDUSTRIES</subject><subject>PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVEHYDROGENATION, OLIGOMERISATION, POLYMERISATION</subject><subject>RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, ORGASES</subject><subject>REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS</subject><subject>REFORMING OF NAPHTHA</subject><subject>TECHNICAL GASES CONTAINING CARBON MONOXIDE</subject><fulltext>true</fulltext><rsrctype>patent</rsrctype><creationdate>2017</creationdate><recordtype>patent</recordtype><sourceid>EVB</sourceid><recordid>eNrjZDD1z8xR8PFzV0hPLM5MS0wuyczPU0grgjAScxRSMotLMnNyEsHiiQUFiUWJJaXFPAysaYk5xam8UJqbQcnNNcTZQze1ID8-tbggMTk1L7Uk3tnPyMDUwtLY0NwoNNSYKEUAxIIuKw</recordid><startdate>20170118</startdate><enddate>20170118</enddate><creator>SHOU LUYANG</creator><creator>CHEN ZUNZHONG</creator><creator>LI FENG</creator><creator>YANG CHUNLIANG</creator><creator>ZHANG RONGFANG</creator><creator>ZHANG QIAOMIN</creator><creator>YU LIANSHI</creator><scope>EVB</scope></search><sort><creationdate>20170118</creationdate><title>Oil LNG gasifaction fractional distillation apparatus</title><author>SHOU LUYANG ; CHEN ZUNZHONG ; LI FENG ; YANG CHUNLIANG ; ZHANG RONGFANG ; ZHANG QIAOMIN ; YU LIANSHI</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-epo_espacenet_CN205893172UU3</frbrgroupid><rsrctype>patents</rsrctype><prefilter>patents</prefilter><language>chi ; eng</language><creationdate>2017</creationdate><topic>CHEMISTRY</topic><topic>CRACKING HYDROCARBON OILS</topic><topic>FUELS</topic><topic>LUBRICANTS</topic><topic>METALLURGY</topic><topic>MINERAL WAXES</topic><topic>PEAT</topic><topic>PETROLEUM, GAS OR COKE INDUSTRIES</topic><topic>PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVEHYDROGENATION, OLIGOMERISATION, POLYMERISATION</topic><topic>RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, ORGASES</topic><topic>REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS</topic><topic>REFORMING OF NAPHTHA</topic><topic>TECHNICAL GASES CONTAINING CARBON MONOXIDE</topic><toplevel>online_resources</toplevel><creatorcontrib>SHOU LUYANG</creatorcontrib><creatorcontrib>CHEN ZUNZHONG</creatorcontrib><creatorcontrib>LI FENG</creatorcontrib><creatorcontrib>YANG CHUNLIANG</creatorcontrib><creatorcontrib>ZHANG RONGFANG</creatorcontrib><creatorcontrib>ZHANG QIAOMIN</creatorcontrib><creatorcontrib>YU LIANSHI</creatorcontrib><collection>esp@cenet</collection></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext_linktorsrc</fulltext></delivery><addata><au>SHOU LUYANG</au><au>CHEN ZUNZHONG</au><au>LI FENG</au><au>YANG CHUNLIANG</au><au>ZHANG RONGFANG</au><au>ZHANG QIAOMIN</au><au>YU LIANSHI</au><format>patent</format><genre>patent</genre><ristype>GEN</ristype><title>Oil LNG gasifaction fractional distillation apparatus</title><date>2017-01-18</date><risdate>2017</risdate><abstract>The utility model relates to an oil LNG gasifaction fractional distillation apparatus, including depropanizator, return tank and deethanizer, be provided with feeding control valve on the third pipeline, be provided with ejection of compact control valve on the fourth pipeline, be connected with the 5th pipeline between feeding control valve and the ejection of compact control valve, and be provided with the pipeline governing valve on the 5th pipeline. The utility model discloses increased the cross -line between feeding control valve the deethanizer before and the ejection of compact control valve after the deethanizer, in the time of need not utilizing component such as deethanizer desorption C2 when refined carbon no. 3, the tank field is delivered to with C3 component autogenous pressure to accessible regulation feeding control valve, ejection of compact control valve, pipeline governing valve, when needs used deethanizer, feeding control valve was opened to the closed pipeline governing valve, and it ca</abstract><oa>free_for_read</oa></addata></record> |
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| language | chi ; eng |
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| subjects | CHEMISTRY CRACKING HYDROCARBON OILS FUELS LUBRICANTS METALLURGY MINERAL WAXES PEAT PETROLEUM, GAS OR COKE INDUSTRIES PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVEHYDROGENATION, OLIGOMERISATION, POLYMERISATION RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, ORGASES REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS REFORMING OF NAPHTHA TECHNICAL GASES CONTAINING CARBON MONOXIDE |
| title | Oil LNG gasifaction fractional distillation apparatus |
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