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1. 发明专利

JPS5735295A Method for heat recovery of raw gas produced from coke-furnace 失效
标题翻译：从焦炭炉中回收原料气的方法
公开(公告)号：JPS5735295A
公开(公告)日：1982-02-25
申请号：JP11119680
申请日：1980-08-13
申请人： Mitsubishi Heavy Ind Ltd , Nippon Kokan Kk
发明人： CHIKAMOTO TOSHIYA , MAKINO KATSUAKI , OOTA KIYOMICHI , KUNIOKA KAZUO , KONISHI NOBUAKI , KUWATA TOKIO , OZEKI AKIYA
IPC分类号： C10B27/00 , F28D3/00 , F28D19/00 , F28D21/00
摘要： PURPOSE: To provide a stable heat recovery for a long period of time by a method wherein a coke-furnace gas is collected in a gas collector pipe, guided to a cooler of jet flow layer, and heat exchanged, thereafter it is guided to the wet wall cooler and heat exchanged therein.
CONSTITUTION: Coke-furnace gas produced from the coke-furnace 1 is collected to the cooler 13 of jet flow-layer and heat exchanged therein, thereafter guided to the wet wall cooler 14 and also heat exchanged therein. Thus, it is possible to perform a heat recovery operation in two steps with two kinds of heat exchangers capable of preventing a coking, so that a stable heat recovery can be carried out for a long period of time.
COPYRIGHT: (C)1982,JPO&Japio
摘要翻译：目的：通过将焦炉煤气收集在集气管中，引导到喷流层的冷却器进行热交换的方法，长时间提供稳定的热回收，然后将其引导到湿壁式冷却器并在其中进行热交换。构成：从焦炉1产生的焦炉煤气被收集到喷流层的冷却器13中并在其中进行热交换，然后被引导到湿壁冷却器14并且在其中进行热交换。因此，可以通过两种能够防止焦化的热交换器进行两步的热回收操作，从而可以长时间地进行稳定的热回收。

2. 发明专利

JPS59102987A Method for recovering heat of crude gas generated from coke oven 失效
标题翻译：从焦炭炉回收原油气的方法
公开(公告)号：JPS59102987A
公开(公告)日：1984-06-14
申请号：JP21216382
申请日：1982-12-03
申请人： Mitsubishi Heavy Ind Ltd , Nippon Kokan Kk
发明人： CHIKAMOTO TOSHIYA , MAKINO KATSUAKI , TAODA KIYOMICHI , KUWATA TOKIO
IPC分类号： C10B27/00 , C10K1/02 , C10K1/06 , C10K1/18 , F28D21/00
CPC分类号： Y02P20/124
摘要： PURPOSE: To recover the sensible heat of a crude gas generated from a coke oven, by cooling a mixture of a tar flowing down heat transfer tubes with a gas with water spray, separating the cold mixture by the specific gravity, and feeding the resultant diluted tar having a low boiling point to the circulating tar.
CONSTITUTION: A crude gas (G
2 ) generated from a coke oven is brought into contact with a circulating tar 11 charged into a wetted wall cooler 5 and made to flow in vertical heat transfer tubes 12 arranged in the wetted wall cooler 5 to carry out the heat exchange of the crude gas with a fluid flowing around the above-mentioned heat transfer tubes 12 and recover the sensible heat of the crude gas (G
2 ). The resultant mixture of the tar flowing down the heat transfer tubes 12 with the gas is cooled with water spray in a water spray tank 15 and separated in a gas-liquid separation tank 17 by the specific gravity to give a diluted low-boiling tar, which is then fed to the above- mentioned circulating tar 11.
EFFECT: The viscosity of the circulating tar can be reduced without reducing the temperature of the circulating tar, and the following advantages can be obtained; Improvement in cooling performance, reduction in the power of the circulating pump, miniaturization of the apparatus and improved quality of recovered steam.
COPYRIGHT: (C)1984,JPO&Japio
摘要翻译：目的：为了回收焦炉产生的粗气体的显热，通过用喷雾器将冷却下来的传热管与气体的焦油混合物冷却，将冷混合物按比重分离，并将得到的稀释焦油具有低沸点至循环焦油。构成：从焦炉产生的粗气体（G2）与装入湿润壁式冷却器5的循环焦油11接触，使其在布置在湿壁式冷却器5中的垂直传热管12中流动，原料气与在上述传热管12周围流动的流体进行热交换，并回收粗气体（G2）的显热。将由热交换管12向下流动的焦油与气体的混合物在水喷雾槽15中喷雾冷却，并在气 - 液分离槽17中以比重分离，得到稀释的低沸点焦油，然后将其送入上述循环焦油11.效果：可以降低循环焦油的粘度而不降低循环焦油的温度，并且可以获得以下优点; 冷却性能的提高，循环泵功率的降低，设备的小型化和回收蒸汽的质量提高。

3. 发明专利

JPS5949488A Heat retrieving device 失效
标题翻译：热回收装置
公开(公告)号：JPS5949488A
公开(公告)日：1984-03-22
申请号：JP16037382
申请日：1982-09-14
申请人： Mitsubishi Heavy Ind Ltd , Nippon Kokan Kk
发明人： CHIKAMOTO TOSHIYA , MAKINO KATSUAKI , KUNO HIROAKI , TAODA KIYOMICHI , NAMAJIO HIROYUKI , OGAWARA FUMIO , SHIORIDA TOKIO
IPC分类号： F28C3/14 , F27D17/00
CPC分类号： F27D17/004
摘要： PURPOSE:To operate the device stably without effecting decoking operation and improve the retrieving amount of heat by a method wherein high-temperature gas, including a high boiling point constituent, is introduced into a jet layer cooler and is circulated stably by extracting and supplementing particles for heat exchange. CONSTITUTION:The high-temperature dirty gas, including the high boiling point constituent such as tar or the like, is introduced into the jet layer cooler 1 through introducing tubes 10, 9, rises through a draft tube 6 together with the particles 8 and is discharged out of a discharging port 4 after being cooled by providing the particles 8 with heat. The particles 8, which are provided with heat, collide against a collision plate 7 and return to the lower part of the draft tube 6 after passing through the outside of the draft tube 6. The operation is stable when the temperature of the gas is higher than the condensing temperature of the tar, however, when the heat retrieving amount is increased remarkably, the temperature of the gas is reduced, the tar is condensed on the surfaces of the particles and each of them make a block mutually thereby making the circulation and heat retrieval impossible. Accordingly, a given amount of the particles 8 under circulation is released from an extracting tube 21 and is introduced into a reproducer 2 to burn the tar on the surface of the particles 8 on a grating 23 by introducing hot-air from a producer 25 while the given amount of particles is supplemented from a tank 30 when it is extracted.
摘要翻译：目的：为了稳定地操作设备，不进行除焦操作，并且通过将包括高沸点成分在内的高温气体引入喷射层冷却器并通过提取和补充颗粒而稳定地循环的方法来提高回收热量用于热交换。构成：通过引入管10,9将包括高沸点成分如焦油等的高温脏气引入喷射层冷却器1，与颗粒8一起通过引流管6上升，并且是通过使颗粒8发热而冷却后从排出口4排出。具有热量的颗粒8碰撞碰撞板7，并在通过引流管6的外部后返回到引流管6的下部。当气体的温度较高时，操作是稳定的然而，当热回收量显着增加时，气体的温度降低，焦油在颗粒表面上冷凝，并且它们各自相互制成块从而使循环和热回收不可能因此，将一定量的循环中的颗粒8从提取管21中释放出来并被引入到再现器2中，以通过从生产者25引入热空气将颗粒8的表面上的焦油燃烧在光栅23上，同时当提取时，从罐30补充给定量的颗粒。

4. 发明专利

JPS5216861A MTHOD OF TREATING WASTE WATER 失效
公开(公告)号：JPS5216861A
公开(公告)日：1977-02-08
申请号：JP9208875
申请日：1975-07-30
申请人： MITSUBISHI HEAVY IND LTD
发明人： CHIKAMOTO TOSHIYA , KUNO HIROAKI , FUKUNAGA MASAMI , KAWAZOE SANAE
IPC分类号： B01D21/01 , B01D15/00 , B01J20/08 , C02F1/28
摘要： PURPOSE:To provide a method of mechanically absorving and removing COD, BOD, etc. contained in waste water to make the resulted water reusable, use of sludge discharged in cohesion and precipitation, for the purpose of waste water treatment.

5. 发明专利

JPS555749A SELECTING METHOD FOR GARBAGE 失效
公开(公告)号：JPS555749A
公开(公告)日：1980-01-16
申请号：JP7911078
申请日：1978-06-29
申请人： MITSUBISHI HEAVY IND LTD
发明人： CHIKAMOTO TOSHIYA , MAKINO KATSUAKI , KUNO HIROAKI
IPC分类号： B03B9/06
摘要： PURPOSE:To make it possible to select efficiently garbage of high purity, by treating the garbage having been crushed in eddying water in successive steps of removal of metals, removal of rubbers, removal of earth, sand, and glass, and in a concentrating and dehydrating step for the garbage. CONSTITUTION:Garbage A contained in city refuse is roughly separated by a primary selector 1 of plastics B and inorg. matters C and is delivered as a classified garbage D to a fine selector 2. The selector 2 comprises an impeller crusher, a rotary screen, a rubber-removing screen, a pressure floating-concentrating unit, a centrifugal dehydrator, and separates the garbage from metallic, coarse, heavy materials E, coarse light mateials F such as plastics, rubbish, and inorganic materials G such as glass to form garbage H of high purity. The garbage H is treated anaerobically in a dissolving unit 3 to form a soln. I, which is subjected in a methanizing unit 4 to anaerobic fermentation, hereby methan gas J and a garbage of high purity, contg. 96% fermented material, are obtained in a yield of 90%.

6. 发明专利

JPS54156267A MINUTE GARBAGE SEPARATION AND SYSTEM THEREFOR 失效
公开(公告)号：JPS54156267A
公开(公告)日：1979-12-10
申请号：JP6428178
申请日：1978-05-31
申请人： MITSUBISHI HEAVY IND LTD
发明人： CHIKAMOTO TOSHIYA , MAKINO KATSUAKI , KUNO HIROAKI
IPC分类号： B03D1/02 , B03B9/06
摘要： PURPOSE:For decreasing system load, preventing trouble in operation and improving final recovery goods, to separate even fine particles of mud and glass at the same time as the condensation of garbage. CONSTITUTION:The town garbage discharged from a primary separator flows through a line 1 into a separating tank 2 where the materials having stuck to each other are separated in plastics and mud or in pure garbage and mud for example. Thus-obtained mixture of slurry and separated garbage flows into a rising air separator 5 where slurry and heavy materials are separated. Said heavy materials not carried by rising air is discharged through a line 9. In the meanwhile, the lightweight materials carried by said rising air are separated by a paper and plastic separator 11. Thus-obtained plastics, and garbage are fed to a screen 13 and to a pressure flotation tank 24 through an aggregating tank 19 respectively for disposal.

7. 发明专利

JPS51136375A TREATING METHOD FOR FIBROUS WASTE MATERIAL 失效
公开(公告)号：JPS51136375A
公开(公告)日：1976-11-25
申请号：JP6063375
申请日：1975-05-21
申请人： MITSUBISHI HEAVY IND LTD
发明人： CHIKAMOTO TOSHIYA , KUNO HIROAKI
IPC分类号： C02F3/28 , A23K10/32 , B09B3/00 , C02F11/04 , C05F3/00 , C05F3/06 , C05F9/02 , C05G3/00 , C12N1/00 , C12N1/20 , C12R1/01 , C12R1/145
摘要： PURPOSE:To allow easy decomposition of fibrous material with bacteria to elevate the methane gas generating efficiency while improving the waste material treating performance.

8. 发明专利

JPH0839778A VARNISH BRIGHTENING DEVICE FOR SHEET PRINTED MATTER 失效
公开(公告)号：JPH0839778A
公开(公告)日：1996-02-13
申请号：JP17857694
申请日：1994-07-29
申请人： MITSUBISHI HEAVY IND LTD , MIHARA RYOJU ENG KK
发明人： UEMURA YOSHIHARU , CHIKAMOTO TOSHIYA , OSADA MIJURO , KAWATE MASAAKI
IPC分类号： B41F23/08 , B41M7/02
摘要： PURPOSE:To enable high speed transportation and achieve facilitation of operation and energy saving by a method wherein a pressurizing roll and a brightening roll to be heated by a heater are provided, and a sheet printed matter is transported, being synchronized with the rotation of both of the rolls, the forward end thereof being held by a pawl mechanism. CONSTITUTION:The outer surface of a brightening roll 11 is mirror-finished and a heater heats the roll 11. A pressurizing roll 13 is pressed against the roll 11 so as to be rotated in synchronization with the rotation of the roll 11, and a pawl mechanism 6 holds the forward end of a sheet printed matter to transport it in synchronization with the rotation of the roll 11 and roll 13. The matter having been heated and pressed at a nipping region N is surely transferred from a pawl mechanism 116 of the roll 11 to a pawl mechanism 316 of a receiving device 31 at an exit side transfer region (b), as in the case of an inlet side transfer region (a). The matters received by the device 31 reach a taking-off device, where they are stacked regularly in succession. As a result, high speed transportation, prevention of bad separation, facilitation of operation, and energy saving can be achieved.

9. 发明专利

JPS59105817A Dust collection apparatus for waste heat recovery 失效
标题翻译：垃圾收集装置用于废热回收
公开(公告)号：JPS59105817A
公开(公告)日：1984-06-19
申请号：JP21396382
申请日：1982-12-08
申请人： Mitsubishi Heavy Ind Ltd
发明人： CHIKAMOTO TOSHIYA , DEWA AKIO , HIRATA KOUICHI , MAKINO KATSUAKI
IPC分类号： B01D46/34 , F22B1/18 , F23J15/00 , F28C3/14 , F28G1/12 , F28G13/00
CPC分类号： F28G13/00
摘要： PURPOSE: To effectively take out the sensible heat of the exhaust gas from an electric furnace, by a method wherein an apparatus for successively falling particles is provided on the way of the passage of dust-containing high temp. exhaust gas to adhere dust to said particles and a means for recovering the heat of adhered dust is provided to the lower part of said apparatus.
CONSTITUTION: When a plurality of particles are fallen from a particle hopper 14, the semi-molten dust in exhaust gas is adhered to the particles and removed from the exhaust gas while waste heat is recovered by a heat exchanger 10. The dust adhered particles pass a waste heat recovery box 18 and, during this time, waste heat is recovered through a heat conductive pipe 16. The dust adhered particles fallen in the recovery box 18 are heated to a high temp. by the heat held by dust and the exhaust gas and heat the pipe 16 during passage through the recovery box 18 to recover heat. Each particle is constituted of a small sphere made of a heat resistant alloy or a ceramic shere and the diameter thereof is appropriately set by the amount of dust, viscosity or the temp. of the exhaust gas.
COPYRIGHT: (C)1984,JPO&Japio
摘要翻译：目的：为了有效地从电炉取出废气的显热，通过在含尘高温通道的途中设置连续落下的颗粒的装置。废气将粉尘附着在所述颗粒上，并且在所述装置的下部设置用于回收附着灰尘的热量的装置。构成：当多个颗粒从颗粒料斗14掉落时，废气中的半熔融灰尘粘附到颗粒上并从排气中除去，同时通过热交换器10回收废热。尘埃附着颗粒通过废热回收箱18，在此期间通过导热管16回收废热。落在回收箱18中的尘埃附着颗粒被加热到高温。通过由灰尘和废气保持的热量，并且在通过回收箱18期间加热管16以回收热量。每个颗粒由耐热合金或陶瓷板制成的小球构成，其直径由粉尘量，粘度或温度适当设定。的废气。

10. 发明专利

JPS5879093A TREATING METHOD OF CONDENSED TAR 失效
公开(公告)号：JPS5879093A
公开(公告)日：1983-05-12
申请号：JP17557481
申请日：1981-11-04
申请人： MITSUBISHI HEAVY IND LTD , NIPPON KOKAN KK
发明人： CHIKAMOTO TOSHIYA , OKAMOTO YUKIYOSHI , KONISHI NOBUAKI , MAEDA TOMOO
IPC分类号： C10K1/00 , C10K1/04 , C10K1/12
摘要： PURPOSE:To condense components having a relatively low boiling point in a gas and mix and dissolve fine particulate tar in the condensed components, by introducing steam into the condensed tar, changing the tar into fine particles, and spraying the fine particulate tar and a gas at the outlet of a wetted-wall cooler with aqueous ammonia. CONSTITUTION:A high-temperature gas containing tar is cooled and condensed in a watted-wall cooler 12 and stored in the bottom tank 13. On the other hand, the cooled gas is fed into an aqueous ammonia spary tank 15 and brought into contact with the aqueous ammonia and further cooled to about 85 deg.C to condense components having a relatively low boiling point. Only the gas is discharged from a line 20 to the outside of the system. The condensed tar in the tank 13 is always circulated through a line 5 to the top of the wetted-wall cooler 12 when the liquid level is a specific value or above, and subjected to the thermal conversion to increase the viscosity thereof while made to flow down in heat transmitting tubes in contact with the gas. The tar is then passed through lines 6 and 7, introduced into the aqueous ammonia spray tank 15 and dispersed into fine particles with steam fed from the line 7, and the misty tar in the gas is mixed with the condensed components condensed and captured by the aqueous ammonia spray and directly in the liquid state fed into a gas-liquid separation tank 16.

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