Thin granule removes bed gas retort for four sections
The utility model discloses a thin granule removes bed gas retort for four sections. The gas retort is equipped with the feed inlet on dry preheating section upper portion, the downside is equipped with hot flue gas air inlet and the upside is equipped with exhaust port and gas vent, dry preheating...
Gespeichert in:
| Hauptverfasser: | , |
|---|---|
| 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 | LIU CHANGSHENG LUO GUOLIN |
| description | The utility model discloses a thin granule removes bed gas retort for four sections. The gas retort is equipped with the feed inlet on dry preheating section upper portion, the downside is equipped with hot flue gas air inlet and the upside is equipped with exhaust port and gas vent, dry preheating section is equipped with the dry heat exchanger with hot flue gas air inlet and exhaust port intercommunication, dry preheating section feeds through from top to bottom through seal section and dry distillation section, under the dry distillation section, the upside is equipped with high temperature flue gas air inlet and exhanst gas outlet, the dry distillation section is equipped with to be derived mouthful with the dry distillation heat exchanger of high temperature flue gas air inlet and exhanst gas outlet intercommunication and with the oil gas of outer wall vapor recovery system system intercommunication, cooling zone and dry distillation section intercommunication and lower part with headtotail and the downside is equipped with the water inlet, the upside is equipped with the delivery port discharges of the coke, the cooling zone is equipped with the cooling heat exchanger with water inlet and delivery port intercommunication. The utility model has the characteristics of consumption of power is low, oil gas dust volume less, the pyrolysis caloric power of gas is high, resource utilization rate is high. |
| format | Patent |
| fullrecord | <record><control><sourceid>epo_EVB</sourceid><recordid>TN_cdi_epo_espacenet_CN204529748UU</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><sourcerecordid>CN204529748UU</sourcerecordid><originalsourceid>FETCH-epo_espacenet_CN204529748UU3</originalsourceid><addsrcrecordid>eNrjZDANycjMU0gvSswrzUlVKErNzS9LLVZISk1RSE8sBvJL8otKFNLyi4C4tEihODW5JDM_r5iHgTUtMac4lRdKczMoubmGOHvophbkx6cWFyQmp-allsQ7-xkZmJgaWZqbWISGGhOlCAC41i31</addsrcrecordid><sourcetype>Open Access Repository</sourcetype><iscdi>true</iscdi><recordtype>patent</recordtype></control><display><type>patent</type><title>Thin granule removes bed gas retort for four sections</title><source>esp@cenet</source><creator>LIU CHANGSHENG ; LUO GUOLIN</creator><creatorcontrib>LIU CHANGSHENG ; LUO GUOLIN</creatorcontrib><description>The utility model discloses a thin granule removes bed gas retort for four sections. The gas retort is equipped with the feed inlet on dry preheating section upper portion, the downside is equipped with hot flue gas air inlet and the upside is equipped with exhaust port and gas vent, dry preheating section is equipped with the dry heat exchanger with hot flue gas air inlet and exhaust port intercommunication, dry preheating section feeds through from top to bottom through seal section and dry distillation section, under the dry distillation section, the upside is equipped with high temperature flue gas air inlet and exhanst gas outlet, the dry distillation section is equipped with to be derived mouthful with the dry distillation heat exchanger of high temperature flue gas air inlet and exhanst gas outlet intercommunication and with the oil gas of outer wall vapor recovery system system intercommunication, cooling zone and dry distillation section intercommunication and lower part with headtotail and the downside is equipped with the water inlet, the upside is equipped with the delivery port discharges of the coke, the cooling zone is equipped with the cooling heat exchanger with water inlet and delivery port intercommunication. The utility model has the characteristics of consumption of power is low, oil gas dust volume less, the pyrolysis caloric power of gas is high, resource utilization rate is high.</description><language>eng</language><subject>CHEMISTRY ; CRACKING HYDROCARBON OILS ; DESTRUCTIVE DISTILLATION OF CARBONAGEOUS MATERIALS FORPRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS ; 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>2015</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=20150805&DB=EPODOC&CC=CN&NR=204529748U$$EHTML$$P50$$Gepo$$Hfree_for_read</linktohtml><link.rule.ids>230,309,781,886,25569,76552</link.rule.ids><linktorsrc>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&date=20150805&DB=EPODOC&CC=CN&NR=204529748U$$EView_record_in_European_Patent_Office$$FView_record_in_$$GEuropean_Patent_Office$$Hfree_for_read</linktorsrc></links><search><creatorcontrib>LIU CHANGSHENG</creatorcontrib><creatorcontrib>LUO GUOLIN</creatorcontrib><title>Thin granule removes bed gas retort for four sections</title><description>The utility model discloses a thin granule removes bed gas retort for four sections. The gas retort is equipped with the feed inlet on dry preheating section upper portion, the downside is equipped with hot flue gas air inlet and the upside is equipped with exhaust port and gas vent, dry preheating section is equipped with the dry heat exchanger with hot flue gas air inlet and exhaust port intercommunication, dry preheating section feeds through from top to bottom through seal section and dry distillation section, under the dry distillation section, the upside is equipped with high temperature flue gas air inlet and exhanst gas outlet, the dry distillation section is equipped with to be derived mouthful with the dry distillation heat exchanger of high temperature flue gas air inlet and exhanst gas outlet intercommunication and with the oil gas of outer wall vapor recovery system system intercommunication, cooling zone and dry distillation section intercommunication and lower part with headtotail and the downside is equipped with the water inlet, the upside is equipped with the delivery port discharges of the coke, the cooling zone is equipped with the cooling heat exchanger with water inlet and delivery port intercommunication. The utility model has the characteristics of consumption of power is low, oil gas dust volume less, the pyrolysis caloric power of gas is high, resource utilization rate is high.</description><subject>CHEMISTRY</subject><subject>CRACKING HYDROCARBON OILS</subject><subject>DESTRUCTIVE DISTILLATION OF CARBONAGEOUS MATERIALS FORPRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS</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>2015</creationdate><recordtype>patent</recordtype><sourceid>EVB</sourceid><recordid>eNrjZDANycjMU0gvSswrzUlVKErNzS9LLVZISk1RSE8sBvJL8otKFNLyi4C4tEihODW5JDM_r5iHgTUtMac4lRdKczMoubmGOHvophbkx6cWFyQmp-allsQ7-xkZmJgaWZqbWISGGhOlCAC41i31</recordid><startdate>20150805</startdate><enddate>20150805</enddate><creator>LIU CHANGSHENG</creator><creator>LUO GUOLIN</creator><scope>EVB</scope></search><sort><creationdate>20150805</creationdate><title>Thin granule removes bed gas retort for four sections</title><author>LIU CHANGSHENG ; LUO GUOLIN</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-epo_espacenet_CN204529748UU3</frbrgroupid><rsrctype>patents</rsrctype><prefilter>patents</prefilter><language>eng</language><creationdate>2015</creationdate><topic>CHEMISTRY</topic><topic>CRACKING HYDROCARBON OILS</topic><topic>DESTRUCTIVE DISTILLATION OF CARBONAGEOUS MATERIALS FORPRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS</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>LIU CHANGSHENG</creatorcontrib><creatorcontrib>LUO GUOLIN</creatorcontrib><collection>esp@cenet</collection></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext_linktorsrc</fulltext></delivery><addata><au>LIU CHANGSHENG</au><au>LUO GUOLIN</au><format>patent</format><genre>patent</genre><ristype>GEN</ristype><title>Thin granule removes bed gas retort for four sections</title><date>2015-08-05</date><risdate>2015</risdate><abstract>The utility model discloses a thin granule removes bed gas retort for four sections. The gas retort is equipped with the feed inlet on dry preheating section upper portion, the downside is equipped with hot flue gas air inlet and the upside is equipped with exhaust port and gas vent, dry preheating section is equipped with the dry heat exchanger with hot flue gas air inlet and exhaust port intercommunication, dry preheating section feeds through from top to bottom through seal section and dry distillation section, under the dry distillation section, the upside is equipped with high temperature flue gas air inlet and exhanst gas outlet, the dry distillation section is equipped with to be derived mouthful with the dry distillation heat exchanger of high temperature flue gas air inlet and exhanst gas outlet intercommunication and with the oil gas of outer wall vapor recovery system system intercommunication, cooling zone and dry distillation section intercommunication and lower part with headtotail and the downside is equipped with the water inlet, the upside is equipped with the delivery port discharges of the coke, the cooling zone is equipped with the cooling heat exchanger with water inlet and delivery port intercommunication. The utility model has the characteristics of consumption of power is low, oil gas dust volume less, the pyrolysis caloric power of gas is high, resource utilization rate is high.</abstract><oa>free_for_read</oa></addata></record> |
| fulltext | fulltext_linktorsrc |
| identifier | |
| ispartof | |
| issn | |
| language | eng |
| recordid | cdi_epo_espacenet_CN204529748UU |
| source | esp@cenet |
| subjects | CHEMISTRY CRACKING HYDROCARBON OILS DESTRUCTIVE DISTILLATION OF CARBONAGEOUS MATERIALS FORPRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS 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 | Thin granule removes bed gas retort for four sections |
| url | https://sfx.bib-bvb.de/sfx_tum?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2024-12-16T01%3A37%3A08IST&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=LIU%20CHANGSHENG&rft.date=2015-08-05&rft_id=info:doi/&rft_dat=%3Cepo_EVB%3ECN204529748UU%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 |