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111. 发明专利

DD151323A1 未知
公开(公告)号：DD151323A1
公开(公告)日：1981-10-14
申请号：DD22156580
申请日：1980-06-04
申请人： POHL WALTER , BAUER EBERHARD , SCHLICKEISER HANS DIETER , REIMANN HANS , MOHRKE WOLFGANG , EMMRICH GERHARD , JAENIG GERALD
发明人： POHL WALTER , BAUER EBERHARD , SCHLICKEISER HANS-DIETER , REIMANN HANS , MOHRKE WOLFGANG , EMMRICH GERHARD , JAENIG GERALD
IPC分类号： C10B17/00

112. 发明专利

DE2619636B2 未知
公开(公告)号：DE2619636B2
公开(公告)日：1980-04-03
申请号：DE2619636
申请日：1976-05-04
申请人： FA. CARL STILL GMBH & CO KG, 4350 RECKLINGHAUSEN
发明人： DUDZIAK, FRANZ, 4350 RECKLINGHAUSEN
IPC分类号： C10B17/00

113. 发明专利

GB1559616A METHOD AND EQUIPMENT FOR HEATING UP A REPAIRED HEATING WALL OF A COKE OVEN BATTERY 未知
公开(公告)号：GB1559616A
公开(公告)日：1980-01-23
申请号：GB4751176
申请日：1976-11-15
申请人： KRUPP KOPPERS GMBH
IPC分类号： C10B29/06 , C10B17/00

114. 发明专利

CA1061738A RECOVERY OF COAL FINES FROM PREHEATER 未知
公开(公告)号：CA1061738A
公开(公告)日：1979-09-04
申请号：CA246003
申请日：1976-02-18
申请人： INLAND STEEL CO
发明人： AKTAY ALI I , HOLOWATY MICHAEL O
IPC分类号： C10B57/06 , C10B57/08 , C10B17/00 , C10B31/00
摘要： Coal particles are heated and further particulized at a preheat stage employing a preheat gas. Some of the finer coal particles are puffed up by the preheating step. Most of the preheated coal particles are separated from the preheat gas, but some of the finer coal particles remain with the preheat gas. The coal particles separated from the preheat gas are oiled and eventually transported by a carrier gas through a pipeline into a coke oven. The preheat gas and the finer coal particles remaining therewith are separated from each other utilizing a wet scrubber at which the finer coal particles undergo flocculation. Oil vapor vented from the coal particles headed for the coke oven is directed to the wet scrubber to aid in the flocculating step. The flocculated coal particles are separated from the scrubber liquid in a flotation cell. The overflow from the flotation cell is filtered, and the filter cake comprising coal particles is employed as a fuel. At least some of the underflow from the flotation cell is recycled as scrubber liquid to the wet scrubber. The liquid from the filtering step is employed to precipitate, in a charging main, fine coal particles discharged with carrier gas into the charging main during charging of the coke oven.

115. 发明专利

ZA777247B PROCESS FOR FURTHER USE OF DIRECT REDUCTION BLAST FURNACE GAS 未知
公开(公告)号：ZA777247B
公开(公告)日：1978-09-27
申请号：ZA777247
申请日：1977-12-05
申请人： DIDIER ENG
发明人： MECKEL J
IPC分类号： C10J1/20 , C10B49/12 , C10B57/08 , C10B57/10 , C21B5/06 , C21B7/00 , F27D17/00 , C10B17/00 , C10B21/02 , C10J3/58

116. 发明专利

DE2053344A1 未知
公开(公告)号：DE2053344A1
公开(公告)日：1972-05-04
申请号：DE2053344
申请日：1970-10-30
IPC分类号： C10B17/00

117. 发明专利

DE1177601B 未知
公开(公告)号：DE1177601B
公开(公告)日：1964-09-10
申请号：DEST016715
申请日：1960-07-22
申请人： STILL FA CARL
发明人： KNAPPSTEIN DR JOHANNES
IPC分类号： C10B17/00 , C10B29/04 , C10B29/06

118. 发明专利

FR830924A 未知
公开(公告)号：FR830924A
公开(公告)日：1938-08-12
申请号：FR830924D
申请日：1937-12-17
申请人： LANCASHIRE METAL SUBLIMING COR
发明人： BLAKEMORE BENJAMIN
IPC分类号： C10B17/00 , C10B21/20

119. 发明专利

TR202101849A2 PİROLİZ GAZ REAKTÖRÜNDE YENİLİK 未知
公开(公告)号：TR202101849A2
公开(公告)日：2021-05-21
申请号：TR202101849
申请日：2021-02-09
申请人： IITECH INVENT INOVASYON VE TEKNOLOJI ANONIM SIRKETI
发明人： KAMİL ENGİN YEŞİL , İRFAN AHMET KURAN
IPC分类号： C10B17/00
摘要： Bu buluş, öğütülmüş katı atık maddelerin gaz ve sıvı yağ olmak üzere faydalı ürüne dönüşümünü, sürekli besleme ile sağlayan, akışkan çalışma kabiliyeti kazanmış piroliz gaz reaktörü ile ilgilidir.

120. 发明专利

BR102017021185A2 processo e reator para produção contínua de carvão vegetal 未知
公开(公告)号：BR102017021185A2
公开(公告)日：2019-04-16
申请号：BR102017021185
申请日：2017-10-02
申请人： VALLOUREC TUBOS DO BRASIL S A
发明人： FERNANDO LATORRE
IPC分类号： C10B17/00 , C10B21/18 , C10B21/22 , C10B31/02 , C10B33/12 , C10B41/08 , C10B47/16 , C10B49/04 , C10B53/02
摘要： a presente invenção refere-se a um sistema para produção contínua de carvão vegetal em um reator vertical tendo uma zona de carregamento (1) de topo e uma zona de secagem (2) concêntricas, uma zona de carbonização (3), uma zona de resfriamento (4) e uma zona de descarga (5), bem como a um método de reaproveitamento energético de gases de carbonização para produção contínua desse carvão, o qual compreende extrair gás de carbonização do topo da zona de secagem (2) do reator (r) e subdividi-lo pelo menos em uma massa de gás recirculante e uma massa de gás de aquecimento e uma parte restante de gás que excede a energia necessária no processo para a geração de energia elétrica; realizar a combustão da massa de gás de aquecimento em um gerador de gases quentes (11); injetar a massa de gás recirculante em um recuperador de calor (9); injetar a massa de gás de aquecimento após a combustão sobre o recuperador de calor (9), para aquecimento indireto da massa de gás recirculante; e reinjetar a massa de gás recirculante aquecida pelo recuperador de calor (9) na base da zona de carbonização (3) do reator (r).

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