A METHOD AND A DEVICE FOR CONTINUOUS CONVERSION OF ORGANIC WASTE
The present invention concerns a method and a device for continuous conversion of organic waste, in particular, highly contaminated waste plastics and worn out vehicle tyres. A method for continuous conversion of worn out vehicle tyres and other organic waste, in particular, highly contaminated wast...
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| creator | ZBIGNIEW TOKARZ |
| description | The present invention concerns a method and a device for continuous conversion of organic waste, in particular, highly contaminated waste plastics and worn out vehicle tyres. A method for continuous conversion of worn out vehicle tyres and other organic waste, in particular, highly contaminated waste plastics, in which the charge is liquefied and then cracked giving the product in the gaseous phase, wherein the charge is introduced into a reactor with a hot bath, in the form of liquid inorganic medium, displaced through the melting zone and the decomposition zone and then the gaseous products of the decomposition are collected at the top and the impurities are removed by means of at least one conveyer, according to the present invention is characterized in that the decomposition reactions are carried out catalytically above the hot bath (14) in the liquefied layer of the charge (13) formed around melting elements, advantageously in the form of the system. of parallel melting guide bars (15A) protruding above the surface of the hot bath (14), comprising liquid inorganic medium, wherein the charge (17) is horizontally and obliquely, downwards the inlet guide (12), introduced above the surface of melting guide bars (15A), and afterwards the charge (17) is displaced along the surface of melting guide bars (15A) by means of the thrusting and combing fingers (40). A device for continuous conversion of organic waste, according to the present invention is characterized in that the separate loading device (19) comprises a press to introduce the charge (17) horizontally and obliquely, downwards the inlet guide (12), above the surface of melting guide bars (15A), the charge (17) displacing system comprises at least one set of urging and cleaning drums (36) to displace the charge (17) along the surface of melting guide bars (15A) by means of the thrusting and combing fingers (40) and the impurities removal system comprises at least two different type conveyers in series arrangement, wherein the first conveyer (48) removes the impurities obliquely upwards above the surface of the bath (14). |
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| fullrecord | <record><control><sourceid>epo_EVB</sourceid><recordid>TN_cdi_epo_espacenet_PT1664240EE</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><sourcerecordid>PT1664240EE</sourcerecordid><originalsourceid>FETCH-epo_espacenet_PT1664240EE3</originalsourceid><addsrcrecordid>eNrjZHBwVPB1DfHwd1Fw9ANiBRfXME9nVwU3_yAFZ3-_EE-_UP_QYBAzzDUo2NPfT8HfTcE_yN3Rz9NZIdwxOMSVh4E1LTGnOJUXSnMzKLi5hjh76KYW5MenFhckJqfmpZbEB4QYmpmZGJkYuLoaE6EEACteKjE</addsrcrecordid><sourcetype>Open Access Repository</sourcetype><iscdi>true</iscdi><recordtype>patent</recordtype></control><display><type>patent</type><title>A METHOD AND A DEVICE FOR CONTINUOUS CONVERSION OF ORGANIC WASTE</title><source>esp@cenet</source><creator>ZBIGNIEW TOKARZ</creator><creatorcontrib>ZBIGNIEW TOKARZ</creatorcontrib><description>The present invention concerns a method and a device for continuous conversion of organic waste, in particular, highly contaminated waste plastics and worn out vehicle tyres. A method for continuous conversion of worn out vehicle tyres and other organic waste, in particular, highly contaminated waste plastics, in which the charge is liquefied and then cracked giving the product in the gaseous phase, wherein the charge is introduced into a reactor with a hot bath, in the form of liquid inorganic medium, displaced through the melting zone and the decomposition zone and then the gaseous products of the decomposition are collected at the top and the impurities are removed by means of at least one conveyer, according to the present invention is characterized in that the decomposition reactions are carried out catalytically above the hot bath (14) in the liquefied layer of the charge (13) formed around melting elements, advantageously in the form of the system. of parallel melting guide bars (15A) protruding above the surface of the hot bath (14), comprising liquid inorganic medium, wherein the charge (17) is horizontally and obliquely, downwards the inlet guide (12), introduced above the surface of melting guide bars (15A), and afterwards the charge (17) is displaced along the surface of melting guide bars (15A) by means of the thrusting and combing fingers (40). A device for continuous conversion of organic waste, according to the present invention is characterized in that the separate loading device (19) comprises a press to introduce the charge (17) horizontally and obliquely, downwards the inlet guide (12), above the surface of melting guide bars (15A), the charge (17) displacing system comprises at least one set of urging and cleaning drums (36) to displace the charge (17) along the surface of melting guide bars (15A) by means of the thrusting and combing fingers (40) and the impurities removal system comprises at least two different type conveyers in series arrangement, wherein the first conveyer (48) removes the impurities obliquely upwards above the surface of the bath (14).</description><language>eng ; por</language><subject>CHEMISTRY ; CRACKING HYDROCARBON OILS ; DESTRUCTIVE DISTILLATION OF CARBONAGEOUS MATERIALS FORPRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS ; DISPOSAL OF SOLID WASTE ; FUELS ; LUBRICANTS ; METALLURGY ; MINERAL WAXES ; PEAT ; PERFORMING OPERATIONS ; PETROLEUM, GAS OR COKE INDUSTRIES ; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVEHYDROGENATION, OLIGOMERISATION, POLYMERISATION ; RECLAMATION OF CONTAMINED SOIL SOIL ; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, ORGASES ; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS ; REFORMING OF NAPHTHA ; TECHNICAL GASES CONTAINING CARBON MONOXIDE ; TRANSPORTING</subject><creationdate>2008</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=20081015&DB=EPODOC&CC=PT&NR=1664240E$$EHTML$$P50$$Gepo$$Hfree_for_read</linktohtml><link.rule.ids>230,308,776,881,25544,76293</link.rule.ids><linktorsrc>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&date=20081015&DB=EPODOC&CC=PT&NR=1664240E$$EView_record_in_European_Patent_Office$$FView_record_in_$$GEuropean_Patent_Office$$Hfree_for_read</linktorsrc></links><search><creatorcontrib>ZBIGNIEW TOKARZ</creatorcontrib><title>A METHOD AND A DEVICE FOR CONTINUOUS CONVERSION OF ORGANIC WASTE</title><description>The present invention concerns a method and a device for continuous conversion of organic waste, in particular, highly contaminated waste plastics and worn out vehicle tyres. A method for continuous conversion of worn out vehicle tyres and other organic waste, in particular, highly contaminated waste plastics, in which the charge is liquefied and then cracked giving the product in the gaseous phase, wherein the charge is introduced into a reactor with a hot bath, in the form of liquid inorganic medium, displaced through the melting zone and the decomposition zone and then the gaseous products of the decomposition are collected at the top and the impurities are removed by means of at least one conveyer, according to the present invention is characterized in that the decomposition reactions are carried out catalytically above the hot bath (14) in the liquefied layer of the charge (13) formed around melting elements, advantageously in the form of the system. of parallel melting guide bars (15A) protruding above the surface of the hot bath (14), comprising liquid inorganic medium, wherein the charge (17) is horizontally and obliquely, downwards the inlet guide (12), introduced above the surface of melting guide bars (15A), and afterwards the charge (17) is displaced along the surface of melting guide bars (15A) by means of the thrusting and combing fingers (40). A device for continuous conversion of organic waste, according to the present invention is characterized in that the separate loading device (19) comprises a press to introduce the charge (17) horizontally and obliquely, downwards the inlet guide (12), above the surface of melting guide bars (15A), the charge (17) displacing system comprises at least one set of urging and cleaning drums (36) to displace the charge (17) along the surface of melting guide bars (15A) by means of the thrusting and combing fingers (40) and the impurities removal system comprises at least two different type conveyers in series arrangement, wherein the first conveyer (48) removes the impurities obliquely upwards above the surface of the bath (14).</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>DISPOSAL OF SOLID WASTE</subject><subject>FUELS</subject><subject>LUBRICANTS</subject><subject>METALLURGY</subject><subject>MINERAL WAXES</subject><subject>PEAT</subject><subject>PERFORMING OPERATIONS</subject><subject>PETROLEUM, GAS OR COKE INDUSTRIES</subject><subject>PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVEHYDROGENATION, OLIGOMERISATION, POLYMERISATION</subject><subject>RECLAMATION OF CONTAMINED SOIL SOIL</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><subject>TRANSPORTING</subject><fulltext>true</fulltext><rsrctype>patent</rsrctype><creationdate>2008</creationdate><recordtype>patent</recordtype><sourceid>EVB</sourceid><recordid>eNrjZHBwVPB1DfHwd1Fw9ANiBRfXME9nVwU3_yAFZ3-_EE-_UP_QYBAzzDUo2NPfT8HfTcE_yN3Rz9NZIdwxOMSVh4E1LTGnOJUXSnMzKLi5hjh76KYW5MenFhckJqfmpZbEB4QYmpmZGJkYuLoaE6EEACteKjE</recordid><startdate>20081015</startdate><enddate>20081015</enddate><creator>ZBIGNIEW TOKARZ</creator><scope>EVB</scope></search><sort><creationdate>20081015</creationdate><title>A METHOD AND A DEVICE FOR CONTINUOUS CONVERSION OF ORGANIC WASTE</title><author>ZBIGNIEW TOKARZ</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-epo_espacenet_PT1664240EE3</frbrgroupid><rsrctype>patents</rsrctype><prefilter>patents</prefilter><language>eng ; por</language><creationdate>2008</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>DISPOSAL OF SOLID WASTE</topic><topic>FUELS</topic><topic>LUBRICANTS</topic><topic>METALLURGY</topic><topic>MINERAL WAXES</topic><topic>PEAT</topic><topic>PERFORMING OPERATIONS</topic><topic>PETROLEUM, GAS OR COKE INDUSTRIES</topic><topic>PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVEHYDROGENATION, OLIGOMERISATION, POLYMERISATION</topic><topic>RECLAMATION OF CONTAMINED SOIL SOIL</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><topic>TRANSPORTING</topic><toplevel>online_resources</toplevel><creatorcontrib>ZBIGNIEW TOKARZ</creatorcontrib><collection>esp@cenet</collection></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext_linktorsrc</fulltext></delivery><addata><au>ZBIGNIEW TOKARZ</au><format>patent</format><genre>patent</genre><ristype>GEN</ristype><title>A METHOD AND A DEVICE FOR CONTINUOUS CONVERSION OF ORGANIC WASTE</title><date>2008-10-15</date><risdate>2008</risdate><abstract>The present invention concerns a method and a device for continuous conversion of organic waste, in particular, highly contaminated waste plastics and worn out vehicle tyres. A method for continuous conversion of worn out vehicle tyres and other organic waste, in particular, highly contaminated waste plastics, in which the charge is liquefied and then cracked giving the product in the gaseous phase, wherein the charge is introduced into a reactor with a hot bath, in the form of liquid inorganic medium, displaced through the melting zone and the decomposition zone and then the gaseous products of the decomposition are collected at the top and the impurities are removed by means of at least one conveyer, according to the present invention is characterized in that the decomposition reactions are carried out catalytically above the hot bath (14) in the liquefied layer of the charge (13) formed around melting elements, advantageously in the form of the system. of parallel melting guide bars (15A) protruding above the surface of the hot bath (14), comprising liquid inorganic medium, wherein the charge (17) is horizontally and obliquely, downwards the inlet guide (12), introduced above the surface of melting guide bars (15A), and afterwards the charge (17) is displaced along the surface of melting guide bars (15A) by means of the thrusting and combing fingers (40). A device for continuous conversion of organic waste, according to the present invention is characterized in that the separate loading device (19) comprises a press to introduce the charge (17) horizontally and obliquely, downwards the inlet guide (12), above the surface of melting guide bars (15A), the charge (17) displacing system comprises at least one set of urging and cleaning drums (36) to displace the charge (17) along the surface of melting guide bars (15A) by means of the thrusting and combing fingers (40) and the impurities removal system comprises at least two different type conveyers in series arrangement, wherein the first conveyer (48) removes the impurities obliquely upwards above the surface of the bath (14).</abstract><oa>free_for_read</oa></addata></record> |
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| language | eng ; por |
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| subjects | CHEMISTRY CRACKING HYDROCARBON OILS DESTRUCTIVE DISTILLATION OF CARBONAGEOUS MATERIALS FORPRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS DISPOSAL OF SOLID WASTE FUELS LUBRICANTS METALLURGY MINERAL WAXES PEAT PERFORMING OPERATIONS PETROLEUM, GAS OR COKE INDUSTRIES PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVEHYDROGENATION, OLIGOMERISATION, POLYMERISATION RECLAMATION OF CONTAMINED SOIL SOIL RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, ORGASES REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS REFORMING OF NAPHTHA TECHNICAL GASES CONTAINING CARBON MONOXIDE TRANSPORTING |
| title | A METHOD AND A DEVICE FOR CONTINUOUS CONVERSION OF ORGANIC WASTE |
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