| 序号 | 专利名 | 申请号 | 申请日 | 公开（公告）号 | 公开（公告）日 | 发明人 |
|---|---|---|---|---|---|---|
| 141 | 自燃炭化熱処理装置及び炭化熱処理システム、並びにこれを使用した炭化物の製造方法 | JP2018130003 | 2018-07-09 | JP2020007462A | 2020-01-16 | 山崎 正一 |
| 【課題】ヤシの実等の高含水率の炭化用材料でも炭化処理することができる自燃炭化熱処理装置を提供する。 【解決手段】自燃炭化熱処理装置100は、円筒状の本体部10と、通気孔20a付きの隔壁板20と、空気を導入する給気経路31と、隔壁板20を貫通して立設され、複数の通気孔40aを有する排気用外筒体40と、上方開口部50aが排気用外筒体40内に位置した状態で排気用外筒体40内に挿入された排気用内筒体50と、隔壁板20の通気孔20aと連通した状態で隔壁板20上に立設された通気孔60a付きの給気用筒体60と、を備えている。排気用内筒体50の上方開口部50aは、排気用外筒体40内の蓋体43から十分に距離をとって離れた位置にあり、これによって、排気用外筒体40の内部において、排気用内筒体50の上方開口部50aの上部に、ガス滞留空間46が形成されている。 【選択図】図1 |
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| 142 | A method for producing the fuel and iron respectively at the same time | JP52230696 | 1996-01-16 | JPH11501985A | 1999-02-16 | アルバート カルデロン |
| (57)【要約】 石炭11と鉄鉱石47とから燃料と鉄とを夫々同時に製造する方法であって、石炭を熱分解炉内で酸素欠乏状態で加熱し、炭化水素を含む粗ガスとコークスを生成し、粗ガスは分留ユニットに送られ、粗ガス内の炭化水素が分留され、脱硫黄分試薬によって硫黄分を除去され、酸素分が増加することによって、粗ガス内の自由な水素量を増大させて還元ガス25とする。 還元ガス25は反応し易くなっており、この還元ガスを還元炉において、鉄鉱石の炉床に通すことによって、鉄鉱石を直接還元して直接還元鉄56とする。 | ||||||
| 143 | Automatic ticket examination machine | JP27907696 | 1996-10-22 | JPH10124713A | 1998-05-15 | OSHIMA HIDEO; TSUCHIYA SHINJI; SUZUKI TAKAHIRO; MAEDA MASAYUKI |
| PROBLEM TO BE SOLVED: To improve user's convenience by allowing exiting on condition that an entry ticket indicating an entry into the ride route of a train ticket is thrown in when the ticket thrown in the throw-in slot of an automatic ticket machine main body allows an entry at the station and indicates no entry. SOLUTION: When a user throw an entry ticket and a commutation ticket in the throw-in slot 1 of the main body (a) one over the other together, a separation part 3b separates them, sheet by sheet, and a read head H1 reads data out of the entry ticket and commutation ticket. Here, the commutation ticket is valid in the ride section from a superior line station to an old line station and allows exiting from this station and the entry ticket includes the ridable route of the commutation ticket; when entry data is written on the ticket thrown in a general ticket barrier at the superior train station, the entry data of the entry ticket is processed as the entry data of the commutation ticket to complement the commutation ticket with the entry data of the entry ticket, thereby allowing exiting from this station. | ||||||
| 144 | Coal and hard coal carbonization | JP11415882 | 1982-07-02 | JPS5845276A | 1983-03-16 | HAINTSU HENTAA; HAINRITSUHI IIGERUBIYUUSHIYAA; HAINRITSUHI GURESHIYU; HERIBERUTO DEBUERUTO |
| 145 | Method and apparatus for converting waste material to fuel gas | JP7087880 | 1980-05-29 | JPS5718786A | 1982-01-30 | DEIBIIDO CHIBOORU SUZOROBODA |
| 146 | Manufacture of semicoke | JP12143379 | 1979-09-20 | JPS5645983A | 1981-04-25 | FUJII MASANORI; TAKAHASHI YUKIO; KAKO HIROYUKI |
| PURPOSE: To manufacture semicoke without troubles due to tar fraction, by a method in which a carburization gas containing tar vapor formed in the manufacture of semicoke is brought into contact with an inert medium to coagulate and arrest the tar vapor. CONSTITUTION: Coal for carburization, having a grain size of 5W10mm, is supplied through the screw conveyer 2 from the hopper 1 into the inside-heating type carburization furnace 7, where the coal is carburized at 600W700°C and semicoke obtained is taken out of the upside of the furnace 7 and stored. On the other hand, the carburization gas containing tar vapor formed at the same time is introduced through the line 9 into the moving bed 10, where it is brought into cocurrentwise contact with an inert medium supplied from the hopper 11, whereby the tar vapor is cogulated and adsorbed on the inert medium. Then, the inert medium is orderly drawn out of the lower part of the moving bed 10 and sent to the fluidized layer 14 for incineration, where the tar fraction is burned at 300W400°C. COPYRIGHT: (C)1981,JPO&Japio | ||||||
| 147 | Treatment of finely divided solid fuel | JP10900379 | 1979-08-27 | JPS5632590A | 1981-04-02 | JINOUI FUYOODOROUITSUCHI CHIYU; JINOUI JINOBIEUITSUCHI CHIYUHA; SERUGEI ANDOREEEUITSUCHI TSUPU; URAJIMIIRU IWANOUITSUCHI SAMUS; WAJIIMU AREKUSEEEUITSUCHI KARA |
| 148 | Treatment of waste water | JP6430178 | 1978-05-31 | JPS54156342A | 1979-12-10 | SEKIGUCHI HIDEAKI; FUJINAMI SHIYOUSAKU; OKAMOTO KIYOUICHI; AKIYOSHI TAKAHARU |
| PURPOSE: To provide a method of the treatment of waste water resulting from pyrolysis treatment of waste, wherein oily substances in the waste water are caused to float and to be separated from the waste water, and solid substances in the waste water are centrifuged to be effectively used as fuel for the pyrolysis treatment. CONSTITUTION: Waste water 1 which has been produced when waste such as urban refuse is subjected to pyrolysis treatment is introduced into an oil separator 2, the resulting floated oily substances 5 are transferred to a mixing tank 7, while the waste water still containing solid substances is transferred to a solid separator 3, and the separated solid substances 6 are transferred to the mixing tank 7. The recovered oily substances and solid substances are stired in the mixing tank to form a slurry, and the slurry is pumped by a slurry pump 8 and is metered through a flowmeter 9 and screw feeder 10 into a combustion furnace 11 to be used as a heating source of heating medium for the pyrolysis treatment. COPYRIGHT: (C)1979,JPO&Japio | ||||||
| 149 | Treatment of waste water | JP6430078 | 1978-05-31 | JPS54156341A | 1979-12-10 | SEKIGUCHI HIDEAKI; FUJINAMI SHIYOUSAKU; OKAMOTO KIYOUICHI; AKIYOSHI TAKAHARU |
| PURPOSE: To provide a method of the treatment of waste water, wherein the waste water resulting from pyrolysis treatment of waste is subjected to coagultation treatment to separate off heavy metals and reducing substances, and then the waste water is subjected to oxidative destruction by the alkali-chlorine method to decompose cyanides in the water, so that the purification of the waste water is effectively carried out. CONSTITUTION: The addition 3 of NaOH to a waste water 1 resulting from pyrolysis treatment of waste is carried out in a tank 2 to adjust the pH value of the waste water 1 to about 10, the waste water 1 is transferred to a coagulation tank 4 where a high-molecular weight coagulant 5 and an inorganic coagulant 6 are added to coagulate and remove heavy metals and reducing subsances, the thus treated water is transferred to an oxidation column 7 where the pH value of the water is adjusted by NaOH to between 10 and 12 followed by the addition 8 of NaOCl to effect primary oxidation of cyanide components and where then the pH value of the water is adjusted to between 8 and 9 by the addition 9 of H 2SO 4 followed by the addition 8 of NaOCl to effect secondary oxidation of the cyanide components. After these oxidation treatments, a high-molecular weight coagulant 12 is added to the thus treated water in a tank 11,the addition 14 of H 2SO 4 is carried out in a tank 13 to neutralize the water, and the water is transferred through a reservoir 15 to a sand filter column 16, then to an active carbon adsorption column 17 where it is subjected to the respective treatments, and thereafter is discharged. COPYRIGHT: (C)1979,JPO&Japio | ||||||
| 150 | Recirculation of fine powders in coking process | JP5289576 | 1976-05-11 | JPS5254705A | 1977-05-04 | DON II BUREIZAA; JIERARUDO SHII RATSUPU |
| 151 | Pressur ized apparatus for gasifying low quality coal | JP6255375 | 1975-05-27 | JPS51138703A | 1976-11-30 | ARISAKI KENJI |
| PURPOSE: Pressurize apparatus for gasifying low quality coal intended for higher thermal efficiency and reduced environmental pollution by the adoption of a gas turbine and pressurized system. COPYRIGHT: (C)1976,JPO&Japio | ||||||
| 152 | Tankasuisonoseizoho oyobi sonoseizosochi | JP2459075 | 1975-02-28 | JPS51100103A | 1976-09-03 | MOROE MICHIO; YOSHIDA TOSHIO |
| 153 | Kaibunshikichokusetsuteikodenkironyorufunryukookusunonetsushoriho | JP10579274 | 1974-09-12 | JPS5159704A | 1976-05-25 | SUNAMI YOSHIHIKO; KUBO TOSHIHIKO; ISHIKAWA KORETAKA; ITO MASAZUMI |
| 154 | JPS4934506A - | JP7691172 | 1972-08-02 | JPS4934506A | 1974-03-30 | |
| 155 | 一种基于塑料与生物质的共热解设备 | CN202320106383.5 | 2023-02-03 | CN219429930U | 2023-07-28 | 邢浩翰; 丛宏斌; 孟海波; 宋威; 沈秀丽 |
| 本实用新型公开了一种基于塑料与生物质的共热解设备,属于生物质热解技术领域，包括共热解炉，共热解炉底部设有共热解产物收集仓，共热解炉和共热解产物收集仓的内腔相连，共热解炉和共热解产物收集仓的内腔之间设置可开合的出料门；共热解炉的顶部开设有出气口，出气管道的末端依次连接第一冷凝器和第二冷凝器，所述第二冷凝器的气体出口连接气体收集罐；共热解炉的进料口连接螺旋输送机，螺旋输送机的进料端设有原料预处理系统；本实用新型能够有效避免热解产物堵塞设备，并可以保持热解设备的干净，增加设备使用寿命；可以提高共热解效率，增加热解气和生物炭的产量。 | ||||||
| 156 | 一种环保型竹炭烧制装置 | CN202220344899.9 | 2022-02-21 | CN217323966U | 2022-08-30 | 赵坚融 |
| 本实用新型涉及一种烧制装置，尤其涉及一种环保型竹炭烧制装置。技术问题为：提供一种不会污染环境的环保型竹炭烧制装置。一种环保型竹炭烧制装置，包括有支撑杆和烤箱，烤箱底部两侧均固接有至少两个支撑杆；保护盖和合页，烤箱的一侧通过合页铰接连接有保护盖，保护盖和烤箱配合；放置架，放置架固接于烤箱内侧下部。本实用新型的第一风扇可以将外界的空气吸入烤箱内，提供氧气，有助于竹子的燃烧，第二风扇可以将烤箱内的烟雾吸入出风管内，滤网可以过滤烟雾中的烟灰，避免烟灰排放到外面，避免污染外界环境，烟灰管可以盛装烟灰，方便人们后续收集烟灰。 | ||||||
| 157 | 一种上下分流式富油煤提油联产合成气一体化装置 | CN202021680560.3 | 2020-08-13 | CN212800251U | 2021-03-26 | 闫琦; 傅祥 |
| 本实用新型公开一种上下分流式富油煤提油联产合成气一体化装置，一体化装置包括活性焦转化炉、富油煤热裂解反应炉、气固分流器、冷却缓冲料斗、锁斗、给料器和细渣冷却缓冲器；实现了粉煤提油及半焦高效转化的直接耦合，焦油收率最高可达20％以上，并在同一个系统内实现活性焦高效转化的制取高品质富氢合成气；突破了常规低阶煤热解、干馏工艺对煤炭资源利用效率低、综合附加值低、焦油收率低，所产生的合成气品质差、工艺过程污染严重等技术缺陷；操作条件温和等竞争优势，可实现连续、安全稳定运行。 | ||||||
| 158 | 一种内热式连续炭化炉 | CN201922097429.8 | 2019-11-29 | CN211570554U | 2020-09-25 | 上官国青; 张教; 王炯; 崔文丽; 查玉平; 程斌伟; 贺勇 |
| 本实用新型公开了一种内热式连续炭化炉，炉体的两侧分别固定有排出管和排入管，排出管和排入管的末端皆焊接有第一法兰盘，所述炉体的一端设置有管道，且管道的两端皆焊接有第二法兰盘，所述管道的末端连接有废气管；本实用新型通过炉体内部的气流带动粉尘向上运动，使气体通过排出管进入到管道中，经过滤尘布袋进行粉尘过滤，然后气流通过排入管回到炉体内部重复利用，当炉体内部的压强增大，电磁阀门关闭，使气流通过废气管排出。(ESM)同样的发明创造已同日申请发明专利 | ||||||
| 159 | 一种利用生物质废弃物高效制氢碳化裂解装置 | CN201920710483.2 | 2019-05-17 | CN209989321U | 2020-01-24 | 俞伟敏; 白根云 |
| 本实用新型涉及机械技术领域，具体为一种利用生物质废弃物高效制氢碳化裂解装置，包括裂解箱，裂解箱上设有电机，电机输出端上设有转盘，转盘的下表面安装有若干个电热棒，裂解箱底端外表面一侧设有下料口，裂解箱位于下料口的位置处设有下料管，下料管的上表面设有插槽，插槽内设有隔板。该利用生物质废弃物高效制氢碳化裂解装置，电机输出端转动时带动转盘一起转动，转盘的下表面设有若干个加热棒，使得电热棒对生物质废弃物进行加热的同时，还能对其进行搅拌，使得加热更加均匀，提高生物质废弃物裂解效率，待裂解完毕，将隔板从下料管上的插槽内抽出，使得废渣通过下料管排出裂解箱，解决生物质废弃物裂解装置加热不均匀的问题。 | ||||||
| 160 | 一种生物质热解炉 | CN201820043896.5 | 2018-01-11 | CN208055264U | 2018-11-06 | 郭泽鑫 |
| 本实用新型公开了一种生物质热解炉，其结构包括放置板、第一支撑柱、煤气灶、第二支撑柱、开关、加热口、输气管、集气罐、导气管、热解炉、罐盖、支撑脚、第一把手、第二把手、加热棒、废料收集盒和隔层，加热棒包括接线柱、金属丝、法兰、电阻、电热管。本实用新型一种生物质热解炉通过设置了加热棒，高频的电流流向被绕制成环状的加热线圈，由于导热管内存在着电阻，通过电阻通电产生热能，所以会产生很多的热能，对生物质加热，解决了生物质的加热不均匀，导致生物质挥发不全的问题。 | ||||||
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