INDUCTION HEATING TYPE DRY DISTILLATION FURNACE

PROBLEM TO BE SOLVED: To improve processing capacity by shortening a time for one batch by continuously performing dry distillation processing without explosively burning a combustible gas generated from a dry-distilled material. SOLUTION: In this induction heating type dry distillation furnace wher...

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Hauptverfasser: TAKE TATSUO, SAKUMA MASAKI
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creator TAKE TATSUO
SAKUMA MASAKI
description PROBLEM TO BE SOLVED: To improve processing capacity by shortening a time for one batch by continuously performing dry distillation processing without explosively burning a combustible gas generated from a dry-distilled material. SOLUTION: In this induction heating type dry distillation furnace wherein a dry distillation tank 2 storing the dry-distilled material 7, is induction-heated in a furnace main body 1 in an inert gas atmosphere to perform dry distillation of the dry-distilled material 7, and the dry-distilled material after processing is discharged from a lower portion of the furnace main body 1, a discharge chamber 12 of a sealed structure is connected with a lower portion of the furnace main body 1, a means for replacing the discharge chamber 12 by an inert gas, is mounted, then the discharge chamber 12 is replaced by nitrogen, and a bottom cover 6 is opened to discharge the dry-distilled material 7 after dry distillation processing, to a discharge tray 10 of the discharge chamber 12. As the outside air does not intrude into the furnace in discharging the dry-distilled material 7, replacement by inert gas in the furnace for charging the next dry-distilled material 7 is unnecessary, and further as the discharge chamber 12 has low oxygen concentration, the discharged dry-distilled material 7 is not oxidized. COPYRIGHT: (C)2006,JPO&NCIPI
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SOLUTION: In this induction heating type dry distillation furnace wherein a dry distillation tank 2 storing the dry-distilled material 7, is induction-heated in a furnace main body 1 in an inert gas atmosphere to perform dry distillation of the dry-distilled material 7, and the dry-distilled material after processing is discharged from a lower portion of the furnace main body 1, a discharge chamber 12 of a sealed structure is connected with a lower portion of the furnace main body 1, a means for replacing the discharge chamber 12 by an inert gas, is mounted, then the discharge chamber 12 is replaced by nitrogen, and a bottom cover 6 is opened to discharge the dry-distilled material 7 after dry distillation processing, to a discharge tray 10 of the discharge chamber 12. As the outside air does not intrude into the furnace in discharging the dry-distilled material 7, replacement by inert gas in the furnace for charging the next dry-distilled material 7 is unnecessary, and further as the discharge chamber 12 has low oxygen concentration, the discharged dry-distilled material 7 is not oxidized. 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SOLUTION: In this induction heating type dry distillation furnace wherein a dry distillation tank 2 storing the dry-distilled material 7, is induction-heated in a furnace main body 1 in an inert gas atmosphere to perform dry distillation of the dry-distilled material 7, and the dry-distilled material after processing is discharged from a lower portion of the furnace main body 1, a discharge chamber 12 of a sealed structure is connected with a lower portion of the furnace main body 1, a means for replacing the discharge chamber 12 by an inert gas, is mounted, then the discharge chamber 12 is replaced by nitrogen, and a bottom cover 6 is opened to discharge the dry-distilled material 7 after dry distillation processing, to a discharge tray 10 of the discharge chamber 12. As the outside air does not intrude into the furnace in discharging the dry-distilled material 7, replacement by inert gas in the furnace for charging the next dry-distilled material 7 is unnecessary, and further as the discharge chamber 12 has low oxygen concentration, the discharged dry-distilled material 7 is not oxidized. COPYRIGHT: (C)2006,JPO&amp;NCIPI</description><subject>BLASTING</subject><subject>CHEMISTRY</subject><subject>DESTRUCTIVE DISTILLATION OF CARBONAGEOUS MATERIALS FORPRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS</subject><subject>DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS,IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KINDOF FURNACE</subject><subject>DISPOSAL OF SOLID WASTE</subject><subject>FUELS</subject><subject>FURNACES</subject><subject>FURNACES, KILNS, OVENS, OR RETORTS IN GENERAL</subject><subject>HEATING</subject><subject>KILNS</subject><subject>LIGHTING</subject><subject>LUBRICANTS</subject><subject>MECHANICAL ENGINEERING</subject><subject>METALLURGY</subject><subject>OPEN SINTERING OR LIKE APPARATUS</subject><subject>OVENS</subject><subject>PEAT</subject><subject>PERFORMING OPERATIONS</subject><subject>PETROLEUM, GAS OR COKE INDUSTRIES</subject><subject>RECLAMATION OF CONTAMINED SOIL SOIL</subject><subject>RETORTS</subject><subject>TECHNICAL GASES CONTAINING CARBON MONOXIDE</subject><subject>TRANSPORTING</subject><subject>WEAPONS</subject><fulltext>true</fulltext><rsrctype>patent</rsrctype><creationdate>2006</creationdate><recordtype>patent</recordtype><sourceid>EVB</sourceid><recordid>eNrjZND39HMJdQ7x9PdT8HB1DPH0c1cIiQxwVXAJilRw8QwO8fTxcQTLuoUG-Tk6u_IwsKYl5hSn8kJpbgYlN9cQZw_d1IL8-NTigsTk1LzUknivACMDAzMjIwNjIwtHY6IUAQBkHCaO</recordid><startdate>20060824</startdate><enddate>20060824</enddate><creator>TAKE TATSUO</creator><creator>SAKUMA MASAKI</creator><scope>EVB</scope></search><sort><creationdate>20060824</creationdate><title>INDUCTION HEATING TYPE DRY DISTILLATION FURNACE</title><author>TAKE TATSUO ; SAKUMA MASAKI</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-epo_espacenet_JP2006220328A3</frbrgroupid><rsrctype>patents</rsrctype><prefilter>patents</prefilter><language>eng</language><creationdate>2006</creationdate><topic>BLASTING</topic><topic>CHEMISTRY</topic><topic>DESTRUCTIVE DISTILLATION OF CARBONAGEOUS MATERIALS FORPRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS</topic><topic>DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS,IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KINDOF FURNACE</topic><topic>DISPOSAL OF SOLID WASTE</topic><topic>FUELS</topic><topic>FURNACES</topic><topic>FURNACES, KILNS, OVENS, OR RETORTS IN GENERAL</topic><topic>HEATING</topic><topic>KILNS</topic><topic>LIGHTING</topic><topic>LUBRICANTS</topic><topic>MECHANICAL ENGINEERING</topic><topic>METALLURGY</topic><topic>OPEN SINTERING OR LIKE APPARATUS</topic><topic>OVENS</topic><topic>PEAT</topic><topic>PERFORMING OPERATIONS</topic><topic>PETROLEUM, GAS OR COKE INDUSTRIES</topic><topic>RECLAMATION OF CONTAMINED SOIL SOIL</topic><topic>RETORTS</topic><topic>TECHNICAL GASES CONTAINING CARBON MONOXIDE</topic><topic>TRANSPORTING</topic><topic>WEAPONS</topic><toplevel>online_resources</toplevel><creatorcontrib>TAKE TATSUO</creatorcontrib><creatorcontrib>SAKUMA MASAKI</creatorcontrib><collection>esp@cenet</collection></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext_linktorsrc</fulltext></delivery><addata><au>TAKE TATSUO</au><au>SAKUMA MASAKI</au><format>patent</format><genre>patent</genre><ristype>GEN</ristype><title>INDUCTION HEATING TYPE DRY DISTILLATION FURNACE</title><date>2006-08-24</date><risdate>2006</risdate><abstract>PROBLEM TO BE SOLVED: To improve processing capacity by shortening a time for one batch by continuously performing dry distillation processing without explosively burning a combustible gas generated from a dry-distilled material. SOLUTION: In this induction heating type dry distillation furnace wherein a dry distillation tank 2 storing the dry-distilled material 7, is induction-heated in a furnace main body 1 in an inert gas atmosphere to perform dry distillation of the dry-distilled material 7, and the dry-distilled material after processing is discharged from a lower portion of the furnace main body 1, a discharge chamber 12 of a sealed structure is connected with a lower portion of the furnace main body 1, a means for replacing the discharge chamber 12 by an inert gas, is mounted, then the discharge chamber 12 is replaced by nitrogen, and a bottom cover 6 is opened to discharge the dry-distilled material 7 after dry distillation processing, to a discharge tray 10 of the discharge chamber 12. As the outside air does not intrude into the furnace in discharging the dry-distilled material 7, replacement by inert gas in the furnace for charging the next dry-distilled material 7 is unnecessary, and further as the discharge chamber 12 has low oxygen concentration, the discharged dry-distilled material 7 is not oxidized. COPYRIGHT: (C)2006,JPO&amp;NCIPI</abstract><oa>free_for_read</oa></addata></record>
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subjects BLASTING
CHEMISTRY
DESTRUCTIVE DISTILLATION OF CARBONAGEOUS MATERIALS FORPRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS,IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KINDOF FURNACE
DISPOSAL OF SOLID WASTE
FUELS
FURNACES
FURNACES, KILNS, OVENS, OR RETORTS IN GENERAL
HEATING
KILNS
LIGHTING
LUBRICANTS
MECHANICAL ENGINEERING
METALLURGY
OPEN SINTERING OR LIKE APPARATUS
OVENS
PEAT
PERFORMING OPERATIONS
PETROLEUM, GAS OR COKE INDUSTRIES
RECLAMATION OF CONTAMINED SOIL SOIL
RETORTS
TECHNICAL GASES CONTAINING CARBON MONOXIDE
TRANSPORTING
WEAPONS
title INDUCTION HEATING TYPE DRY DISTILLATION FURNACE
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