| 序号 | 专利名 | 申请号 | 申请日 | 公开（公告）号 | 公开（公告）日 | 发明人 |
|---|---|---|---|---|---|---|
| 101 | 新型立式无烟节能锅炉 | CN02252934.9 | 2002-08-30 | CN2562071Y | 2003-07-23 | 荣文清 |
| 本实用新型公开了一种新型立式无烟节能锅炉，包括炉体1、烟道9、炉门10和封火门11，在炉体1内燃烧室3上部安装分散式火管6，分散式火管6上部还连接着烟气缓冲室7，烟气缓冲室内装有横置水冷管8；它还设有喷气装置和助燃装置。蒸汽产生装置的侧下端通过上水管4－2与补水箱4－1相连接，上端通过蒸汽喷管4－4将产生的蒸汽喷向燃烧室内煤层上端的火焰；助燃装置由风机5－1和助燃风管5－2组成。蒸汽助燃加二次风助燃装置使煤炭在炉膛内燃烧充分，火势更猛，因而使得锅炉热效率有了显著提高，节煤节电，消烟除尘效果好。适用于有效热功率在0.02—1.4MW范围内的炉型，适应各类杂煤、原煤、混煤，具有良好的推广价值，应用范围十分广泛。 | ||||||
| 102 | 水火管工业锅炉 | CN02210975.7 | 2002-03-30 | CN2536904Y | 2003-02-19 | 于晓斌 |
| 本实用新型涉及的是DZ系列水火管工业锅炉，为解决现有锅炉存在的翼形烟道受热面布置受控于其炉膛受热面布置的缺陷，本技术在锅炉本体连通管中段处设置一中层集箱，从而使翼形烟道布管独立于炉膛受热面布置。本技术具有受热面布置灵活方便、热效率高、锅炉安全运行性能高的优点。 | ||||||
| 103 | 一种锅炉 | CN99217342.6 | 1999-07-30 | CN2390097Y | 2000-08-02 | 夏雪东 |
| 本实用新型公开了一种锅炉,以解决现有锅炉燃料燃烧不完全、热交换率不够理想、不易清除灰尘等问题。本实用新型包括出烟孔、水腔、烟道、清灰通道、燃烧室、炉排在内的锅炉本体,水腔分为炉脚水腔,燃烧室水腔及炉胆水腔三部分,燃烧室水腔为燃烧室的侧壁,炉胆水腔位于燃烧室上部;烟道为折回塔式结构;清灰通道为2—3个;在燃烧室的上部设有带若干通孔的二次燃烧板,本实用新型换热率高,清灰容易,可在生产及生活中得到广泛的应用。 | ||||||
| 104 | 水火管锅壳锅炉 | CN96226517.9 | 1996-06-06 | CN2263270Y | 1997-09-24 | 吴连武; 刘金山 |
| 本实用新型公开了一种水火管锅壳锅炉，它是在现有火水管锅壳锅炉基础上，突破这种锅炉结构上的常规，把最高对称两排水冷壁管上端位置提高，由原来在锅壳筒体水平中心线以下15°位置，提高到水平中心线以上10°-45°位置。它增加了锅壳筒体的受热面积，在确保锅炉基本参数及节能、环保性能优良的前提下，可收到大幅度节省钢材的显著效果。 | ||||||
| 105 | 高效全能锅炉 | CN95205690.9 | 1995-03-15 | CN2214600Y | 1995-12-06 | 何挺佳 |
| 本实用新型公开了一种高效全能锅炉，由内炉体、炉胆、热交换火管等组成，其特征是卧式安装，火管与炉胆垂直，炉胆上是蒸饭池，余热回收蒸汽管外连接有蛇形冷却管。优点是五分钟出开水，锅炉消音、消烟、除尘、自动脱垢，热利用率高达100％，可用柴、煤、气、油等作燃料，可蒸饭、蒸酒、煮粥、煮菜、还具有自动化程度高，安装使用简便，造价低等特点，适于居家、旅业、机关、部队、学校等使用。 | ||||||
| 106 | 全回程水火管锅炉 | CN92201383.7 | 1992-01-27 | CN2110137U | 1992-07-15 | 张国权 |
| 本实用新型公开了一种结构新颖的全回程水火管锅炉。该锅炉除了具有下水管及后水管外，还在锅筒的上部和前部增设了上水管和前水管，后水管有上、中、下三排，在锅炉内部可形成上下两个烟道，一个前烟室和主副两个后烟室，烟气热经过上下烟道可两次加热锅筒和水管，提高了烟气热的利用率，减少了热损失。火管有直管和弯管两种，同步与烟室、烟道连通，使管板受热均匀，温差小，减少了爆管现象的发生，扩大了水火管锅炉使用范围。 | ||||||
| 107 | 可以燃烧褐煤的高温水汽水两用锅炉 | CN87207837 | 1987-05-07 | CN87207837U | 1988-11-16 | 董珊; 李忠基; 刘淑文; 凌人宾 |
| 一种可以燃烧褐煤的高温水汽水两用锅炉。它是在自然循环水管蒸汽锅炉的基础上，对汽水循环回路、烟气回路以及锅炉结构等方面作了调整和改进，特别是放大了锅筒，增加水容积，增设了饱和水引出管及锯齿形边缘的喇叭状引水口；压低和拉长了炉膛的后拱，从而形成一个有助于燃烧完全的燃烬室；采用了大倾斜角度的往复式炉排，使锅炉能够燃烧褐煤。该锅炉可以专门提供热水或蒸汽，也可以同时提供热水和蒸汽。 | ||||||
| 108 | 폐기물소각로를 이용한 보일러 가열장치 | KR2019860002636 | 1986-03-05 | KR2019900006507Y1 | 1990-07-26 | 이교원 |
| 내용 없음. | ||||||
| 109 | 분해조립식 증기 보일러 | KR2019820000329 | 1982-01-16 | KR2019830001420Y1 | 1983-08-11 | 최진우 |
| 내용없음. | ||||||
| 110 | 도시락가열용보이라 | KR2019630000680 | 1963-05-24 | KR2019630000155Y1 | 1963-09-20 | 박근범 |
| 111 | 固形燃料用のチェーンストーカ火格子を用いる複合式蒸気ボイラ | JP2015162107 | 2015-08-19 | JP2016166723A | 2016-09-15 | キム,ジン ス |
| 【課題】不完全燃焼を最小化することができ、伝熱効果を極大化することができる、固形燃料用のチェーンストーカ火格子を用いる複合式蒸気ボイラを提供する。 【解決手段】固形燃料が燃焼する燃焼室17の上部に、燃焼ガスを伝達する多数の煙管6を内蔵する上部蒸気ドラム1を配置すると共に、燃焼室17の下部左右両端に下部水ドラム2を配置し、燃焼室内の気密保持及び伝熱面積の増大のためのフィン部材を介して互いに一定の間隔を保持し、下部水ドラム2から上部蒸気ドラム1の方向に垂直状態を保持する多数の垂直曲線管3、及び下部水ドラム2の下部に配置されて燃焼室17の底部を構成するチェーンストーカ火格子12を具備した。多数の垂直曲線管3は、経路を異なるようにして上部蒸気ドラム1に接続される複数の垂直曲線管群から構成し、その異なる経路の間に燃焼ガス流れの通路15を設けた。 【選択図】図2 |
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| 112 | Assembly of the inlet pipe to the heat exchanger unit of the flue gas in the tube | JP52676497 | 1996-12-30 | JPH11502607A | 1999-03-02 | エルンスト サベルシュトレーム，ヴィルヘルム; ホーカン ニルスン，スベン |
| (57)【要約】 円筒蒸気ボイラ（１０）の煙道ガスから熱を回収する熱交換器ユニット（１３）であって、前記熱交換器ユニットは、煙道ガス・チューブ（１４）と熱交換チューブ（１６）とを有し、そして、熱交換チューブは、煙道ガス・チューブ（１４）内において、湾曲入口パイプ（１９）−これは、煙道ガス・チューブ（１４）の周壁部の下部開口部（２０）から熱交換チューブ（１６）の下部外向き膨出端壁部（２２）の入口開口部（２１）へと延在する−と、出口パイプ（２２）−これは、熱交換チューブ（１６）の周壁部上部部分の出口開口部（２４）から煙道ガス・チューブ（１４）の周壁部の上部開口部（２５）へと延在する−とを介し同芯的に支持されている。 入口パイプ（１９）は、第一の水平、直線端部部分（１９Ａ）と、第二の上向き直線端部部分（１９Ｂ）と、および中間の湾曲部分（１９Ｃ）とを有する。 ここで、湾曲部分の湾曲角度（α）は９０°を越えると共に、他方の端部部分（１９Ｂ）が、熱交換チューブ（１６）の下部端壁部（２２）の部分的球面部分の曲率中心へ向け前記湾曲角度（α）で定まる傾斜をもって延在され、入口開口部（２１）が、前記端壁部内において熱交換チューブ（１６）の中心長手方向軸線に対して偏心的に配置されている。 | ||||||
| 113 | Water supply treatment method of the exhaust heat recovery boiler | JP11341790 | 1990-04-27 | JP2635798B2 | 1997-07-30 | NAGASHIMA TAKAYUKI |
| 114 | Boiler | JP33711693 | 1993-12-28 | JPH07190301A | 1995-07-28 | IKEBE HIROSHIGE; WATANABE TATSUO |
| PURPOSE: To provide a compact boiler which has a large steam separating surface, can obtain steam of high dryness and high quality and has a small occupied area and a simple structure. CONSTITUTION: The boiler comprises an annular water header 21 having a water tube wall 21 formed of water tubes 19 connected via fins 19a in a cylindrical shape and provided at its lower end with a feed water tube 21a, an annular outer header 22 provided at an upper end, and an air dispersing plate 23 horizontally arranged on an inner periphery of the header 21. The boiler further comprises a cylindrical fluidized bed boiler body 27 having a combustion chamber 26 which has a wind box 25 formed at a lower side of the plate 23 and a fluidized bed part 28 and a free board 29 formed at an upper side of the plate 23, and a smoke tube boiler 36 arranged at an upper part of the body 27 and having a plurality of smoke tubes 35 vertically extended and communicating with the chamber 26 in a vessel 32, wherein the header 22 communicates with the vessel 32 via a communicating tube 37, and the vessel 32 communicate with the header 21 by a return tube 38. COPYRIGHT: (C)1995,JPO | ||||||
| 115 | Fire tube boiler | JP19079693 | 1993-07-03 | JPH0719401A | 1995-01-20 | MIURA TAMOTSU; MIURA MASATOSHI; HIGUCHI ISAO |
| PURPOSE:To provide a fire tube boiler by which a harmful exhaust matter containing NOx and CO is further reduced. CONSTITUTION:A fire tube boiler is provided with a combustion chamber 3 having a burner 4 and a group of fire tubes 8 associated with this combustion chamber 3. In the combustion chamber 3, a heat exchanger 5 for heat- exchanging with a burning flame from the burner 4 is provided. The combustion chamber 3 is divided into a first combustion chamber 31 and a second combustion chamber 32 by providing the heat exchanger 5. | ||||||
| 116 | Treatment of water supply in waste heat recovery boiler | JP11341790 | 1990-04-27 | JPH049483A | 1992-01-14 | NAGASHIMA TAKAYUKI |
| PURPOSE: To prevent a steam condenser from being damaged by excess hydrazine by changing the loadings of hydrazine for removing oxygen in water supply in accordance with the operation conditions of an electric power plant and holding the concn. of hydrazine in the inlet of a waste heat recovery boiler constant in the plant dependent on this boiler. CONSTITUTION: In an electric power plant which is equipped with a power generator 17 directly connected with a steam turbine 16 and is dependent on a waste heat recovery boiler 3, hydrazine is added in the inlet of a low pressure fuel economizer 4 to supply water to the boiler 3 from a steam condenser 1 by a pump 2. After dissolved oxygen is removed by change into aqueous ammonia, water is supplied to the steam turbine 16 via a high pressure evaporator 9 and a high pressure overheater 11. In this case, the amount of hydrazine added to water supply is controlled by the load signal of the power generator 17 and the temp. of exhaust gas of a gas turbine 15 directly connected with the power generator 17. It is prevented that plenty amounts of hydrazine remain in the water returned to the steam condenser 1 and plenty amounts of ammonia are increased thereby and the cooling pipe of the steam condenser 1 is eroded and corroded. COPYRIGHT: (C)1992,JPO&Japio | ||||||
| 117 | Condensing system of electric power plant | JP16399389 | 1989-06-28 | JPH0331601A | 1991-02-12 | KANBAYASHI TAKESHI |
| PURPOSE: To make equipment cost low and save the power consumed in a plant by utilizing a recirculation pump which is used for returning the water at the outlet of a condensing and desalting device to its inlet to carry out the operation of condensate retaining circulation. CONSTITUTION: During the operation of condensate retaining circulation valves 26 and 27 between a recirculation pump 22 and condensing and desalting device 7 are closed, and a valve 37 between a condenser 3 and the recirculation pump 22 and a valve 38 between the recirculation pump 22 and a condensate filtering device 6 are opened. With this arrangement the pressure of the condensate in the condenser 3 is raised through a piping 35 by the recirculation pump 22, and it is led to the condensate filtering device 6 through pipings 23 and 26, and, further, it flows to the condensing and desalting device 7, and the impurities in the condensate are removed. After this the condensate returns to the condenser 3 via a condensate pressurizing pump 8 or its bypass pipe 19, supply water heater 9, supply water pump bypass pipe 20, and a condensate supply recirculation pipe 21. By the way during this return of the condensate a condensate pump 4 is stopped. COPYRIGHT: (C)1991,JPO&Japio | ||||||
| 118 | JPS61141504U - | JP2053185 | 1985-02-18 | JPS61141504U | 1986-09-01 | |
| 119 | JPS60181507U - | JP6799884 | 1984-05-09 | JPS60181507U | 1985-12-02 | |
| 120 | JPS60181505U - | JP6799684 | 1984-05-09 | JPS60181505U | 1985-12-02 | |
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