CN203203008U - Upright pulverized coal corner tube type boiler - Google Patents
Upright pulverized coal corner tube type boiler Download PDFInfo
- Publication number
- CN203203008U CN203203008U CN201220724995.2U CN201220724995U CN203203008U CN 203203008 U CN203203008 U CN 203203008U CN 201220724995 U CN201220724995 U CN 201220724995U CN 203203008 U CN203203008 U CN 203203008U
- Authority
- CN
- China
- Prior art keywords
- boiler
- collection tank
- corner tube
- boiler body
- air preheater
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 239000003245 coal Substances 0.000 title abstract description 23
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 31
- 239000002817 coal dust Substances 0.000 claims 4
- 230000001815 facial effect Effects 0.000 claims 1
- 238000002485 combustion reaction Methods 0.000 abstract description 16
- 239000012528 membrane Substances 0.000 abstract description 14
- 239000000779 smoke Substances 0.000 abstract description 5
- 229910000831 Steel Inorganic materials 0.000 abstract description 3
- 239000010959 steel Substances 0.000 abstract description 3
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 11
- 239000003546 flue gas Substances 0.000 description 11
- 239000000446 fuel Substances 0.000 description 9
- 238000004939 coking Methods 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 4
- 239000002893 slag Substances 0.000 description 4
- 238000004140 cleaning Methods 0.000 description 3
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- 239000010802 sludge Substances 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 230000007812 deficiency Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000006260 foam Substances 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 239000000725 suspension Substances 0.000 description 2
- 239000002028 Biomass Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000009841 combustion method Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000009977 dual effect Effects 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 239000012774 insulation material Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000009991 scouring Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000004071 soot Substances 0.000 description 1
Images
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/34—Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery
Landscapes
- Air Supply (AREA)
Abstract
Description
技术领域technical field
本实用新型属于燃煤工业锅炉领域,具体涉及一种以煤粉或城市污泥、生物质为燃料,用于产生蒸汽的立式煤粉角管式锅炉。The utility model belongs to the field of coal-fired industrial boilers, and in particular relates to a vertical pulverized coal corner tube boiler which uses pulverized coal, urban sludge and biomass as fuel for generating steam.
背景技术Background technique
我国的能源结构是以煤为主,在未来相当长时间内,燃煤工业锅炉仍将是工业锅炉的主导产品。my country's energy structure is dominated by coal. For a long time in the future, coal-fired industrial boilers will still be the leading product of industrial boilers.
传统的工业燃煤锅炉以层燃锅炉为主,缺点是燃烧效率低,污染严重,难以满足节能减排和污染物排放要求。The traditional industrial coal-fired boilers are mainly layer-fired boilers. The disadvantages are low combustion efficiency and serious pollution, which makes it difficult to meet the requirements of energy saving, emission reduction and pollutant discharge.
煤粉燃烧是煤的高效洁净燃烧方式之一,其燃烧效率可达96%以上,是一项成熟的燃烧技术,在大型电站锅炉得到普遍应用。近年来,煤粉燃烧在工业锅炉上也得到应用,均采用卧式内燃锅壳式结构D型双锅筒水管结构或底部布置燃烧器的立式煤粉炉。但存在一定的不足:Pulverized coal combustion is one of the efficient and clean combustion methods of coal, and its combustion efficiency can reach more than 96%. It is a mature combustion technology and is widely used in large-scale power plant boilers. In recent years, pulverized coal combustion has also been applied in industrial boilers, all of which adopt horizontal internal combustion shell structure D-type double drum water pipe structure or vertical pulverized coal furnace with burners arranged at the bottom. But there are certain deficiencies:
1)燃烧不够均匀,前后温差比较大,不利于降低NOX的含量。1) The combustion is not uniform enough, and the temperature difference between front and back is relatively large, which is not conducive to reducing the content of NO X.
2)负荷调节范围小,只能使用单一燃料-煤粉。2) The load adjustment range is small, and only a single fuel - pulverized coal can be used.
3)锅炉灰、渣清理不方便。3) It is inconvenient to clean up boiler ash and slag.
4)锅炉房占地面积大。4) The boiler room occupies a large area.
5)炉膛底部容易结焦。5) The bottom of the furnace is prone to coking.
6)燃烧器检修困难。6) It is difficult to overhaul the burner.
发明内容Contents of the invention
本实用新型针对现有卧式煤粉锅炉的不足,提供一种新型的立式煤粉角管式锅炉。The utility model aims at the deficiency of the existing horizontal pulverized coal boiler, and provides a novel vertical pulverized coal corner tube boiler.
本实用新型是通过以下技术方案实现的:一种立式煤粉角管式锅炉,包括燃烧器、锅炉本体、高温空气预热器、省煤器、低温空气预热器、对流管束、上集箱、顶集箱、锅筒和下集箱,所述的下集箱设置在锅炉本体的底部,所述的上集箱和顶集箱设置在锅炉本体的顶部,并通过汽连通管联通;其特征在于所述的燃烧器设置在锅炉本体的顶部;所述的锅炉本体采用立式膜式水冷壁结构,四角布置4根下降管,所述下降管和膜式水冷壁的两端中分别与所述的上集箱和下集箱联通;所述的对流管束设置在膜式水冷壁的外侧,其底部与炉膛出烟口联通,顶部与所述的高温空气预热器联通;所述的顶集箱与所述锅筒的汽空间联通;所述的上集箱与所述锅筒的水空间联通。The utility model is realized through the following technical solutions: a vertical pulverized coal corner tube boiler, including a burner, a boiler body, a high-temperature air preheater, an economizer, a low-temperature air preheater, a convection tube bundle, an upper set box, top header, drum and lower header, the lower header is arranged at the bottom of the boiler body, the upper header and the top header are arranged at the top of the boiler body, and communicated through the steam connecting pipe; It is characterized in that the burner is arranged on the top of the boiler body; the boiler body adopts a vertical membrane water wall structure, and four downcomers are arranged at the four corners, and the two ends of the downcomer and the membrane water wall are respectively It communicates with the upper header and the lower header; the convection tube bundle is arranged on the outside of the membrane water wall, the bottom of which communicates with the smoke outlet of the furnace, and the top communicates with the high-temperature air preheater; the The top header communicates with the steam space of the drum; the upper header communicates with the water space of the drum.
本实用新型的立式煤粉角管式锅炉,煤粉或城市污泥借一次风通过顶部燃烧器喷入立式炉膛,同时,经低温空气预热器和高温空气预热器加热后的高温空气也进入燃烧器与粉体燃料混合进入炉膛进行猛烈悬浮燃烧;且在炉膛中布置了两级三次风,保证了炉膛有充分的氧气与燃料反应燃烧。在炉膛燃烧换热后的高温烟气转折180°向上进入对流管束进行对流换热,烟气再依次进入高温空气预热器、省煤器和空低温气预热器后排入烟气净化系统。In the vertical pulverized coal corner tube boiler of the utility model, pulverized coal or urban sludge is sprayed into the vertical furnace through the top burner by the primary wind, and at the same time, the high temperature after being heated by the low temperature air preheater and the high temperature air preheater The air also enters the burner and mixes with the powdered fuel and enters the furnace for violent suspension combustion; and two levels of tertiary air are arranged in the furnace to ensure that the furnace has sufficient oxygen and fuel to react and burn. The high-temperature flue gas after combustion and heat exchange in the furnace turns 180° upwards and enters the convection tube bundle for convective heat exchange. The flue gas then enters the high-temperature air preheater, economizer and air-low temperature air preheater in sequence, and then is discharged into the flue gas purification system. .
本项目具有以下优点:This project has the following advantages:
1)锅炉本体采用立式角管式结构布置,四角布置4根大口径下降管,该下降管既是水循环管路,同时也支撑整个锅炉,因此不需要另设支撑钢架,整体结构紧凑、外形布置简单、占地面积小,钢耗低。1) The boiler body is arranged in a vertical corner tube structure, and four large-diameter downpipes are arranged at the four corners. The downpipe is not only a water circulation pipeline, but also supports the entire boiler, so there is no need to set up a supporting steel frame. The overall structure is compact and the shape Simple layout, small footprint and low steel consumption.
2)炉膛采用膜式壁结构,炉墙只需要保温材料,整体密封、保温性能好,漏风少。2) The furnace adopts a membrane wall structure, the furnace wall only needs insulation materials, the overall sealing, good insulation performance, and less air leakage.
3)锅炉水循环压差大,水循环安全可靠。3) The pressure difference of the boiler water circulation is large, and the water circulation is safe and reliable.
4)上集箱与顶集箱用汽连通管连接同时接入锅筒,汽水混合物从受热面进入上集箱,并在上集箱里发生汽水预分离,蒸汽经汽连通管至顶集箱进入锅筒上部的汽空间。由于上集箱均在锅筒的高水位处接入,则蒸汽没有通过水空间而直接接入锅筒,从而避免了泡沫的产生,再加上进入锅筒的蒸汽已进行预分离,因此,大大提高了蒸汽的品质。4) The upper header and the top header are connected with the steam connecting pipe and connected to the drum at the same time, the steam-water mixture enters the upper header from the heating surface, and the steam-water pre-separation occurs in the upper header, and the steam passes through the steam connecting pipe to the top header Enter the steam space in the upper part of the drum. Since the upper headers are all connected at the high water level of the drum, the steam directly enters the drum without passing through the water space, thereby avoiding the generation of foam, and the steam entering the drum has been pre-separated, therefore, Greatly improved the quality of steam.
5)本实用新型的另一个尤为重要的特点是顶部布置燃烧器,这种结构使得本实用新型还具有以下有益技术效果:5) Another particularly important feature of the utility model is that the burner is arranged on the top. This structure makes the utility model also have the following beneficial technical effects:
5.1)可降低锅炉基础高度,缩短基建时间,减少基建费用。5.1) It can reduce the height of the boiler foundation, shorten the construction time and reduce the construction cost.
5.2)火焰形状与炉膛尺寸相匹配,火焰不贴墙触壁;防止火焰冲刷膜式水冷壁,延长锅炉使用寿命。5.2) The shape of the flame matches the size of the furnace, and the flame does not touch the wall; it prevents the flame from scouring the membrane water wall and prolongs the service life of the boiler.
5.3)粉体燃料燃烧完成后剩下的灰渣热被膜式水冷壁吸收冷却后没有高温热源再次加热;因此,掉入落灰斗的灰渣温度较低,有效防止炉膛底部结焦。5.3) After the powder fuel is burned, the remaining ash is absorbed and cooled by the membrane water wall, and there is no high-temperature heat source to reheat; therefore, the temperature of the ash falling into the ash hopper is relatively low, which effectively prevents coking at the bottom of the furnace.
5.4)炉膛火焰流程方向与粉体燃料重力方向一致,炽热灰渣无法靠重力掉入燃烧器区域,有效的避免了燃烧器由于炽热灰渣而引起的结焦现象,大大提高燃烧器的使用寿命。5.4) The flow direction of the furnace flame is consistent with the gravity direction of the powder fuel, and the hot ash cannot fall into the burner area by gravity, which effectively avoids the coking phenomenon of the burner caused by the hot ash and greatly improves the service life of the burner.
5.5)炉膛底部便于落灰渣和布置自动出渣机,降低司劳人员的劳动强度,提高出渣效率。5.5) The bottom of the furnace is convenient for ash and slag discharge and an automatic slag discharge machine is arranged to reduce the labor intensity of laborers and improve the efficiency of slag discharge.
作为本实用新型的进一步改进,所述的燃烧器为两个。双燃烧器布置的好处在于每个燃烧器可单独控制,大大提高燃烧的稳定性和负荷的调节性能,同时可使用两种以上的燃料。As a further improvement of the utility model, there are two burners. The advantage of the dual burner arrangement is that each burner can be controlled independently, which greatly improves the stability of combustion and the performance of load regulation, and can use more than two kinds of fuel at the same time.
作为本实用新型的再进一步改进,所述的对流管束采用旗面管。对流受热面采用旗面管,旗面管按一定角度立式顺列布置,受热面充足,循环可靠,烟气冲刷顺畅,不易积灰,延长锅炉使用寿命。As a further improvement of the utility model, the convection tube bundle adopts flag surface tubes. The convection heating surface adopts flag surface tubes, and the flag surface tubes are vertically arranged in a row at a certain angle. The heating surface is sufficient, the circulation is reliable, the flue gas is washed smoothly, and it is not easy to accumulate dust, which prolongs the service life of the boiler.
作为本实用新型的更进一步改进,采用分级燃烧技术,炉膛内依次送入两级三次风,整个温度场均匀,可有效阻止炉膛结焦和降低氮氧化物的生成。As a further improvement of the utility model, the staged combustion technology is adopted, and two stages of tertiary air are sequentially sent into the furnace, so that the entire temperature field is uniform, which can effectively prevent the furnace from coking and reduce the formation of nitrogen oxides.
附图说明Description of drawings
图1是本实用新型立式煤粉角管式锅炉的结构图。Fig. 1 is a structural diagram of a vertical pulverized coal corner tube boiler of the present invention.
图2是图1的A-A向剖视图。Fig. 2 is a sectional view taken along line A-A of Fig. 1 .
图中,1-低温空气预热器,2-省煤器,3-对流管束,4-高温空气预热器,5-上集箱,6-汽连通管,7-顶集箱,8-锅筒,9-防爆门,10-一级三次风,11-二级三次风,12-下降管,13-炉膛,14-下集箱,15-清灰口,16-检查门,17-燃烧器,18-炉膛出烟口。In the figure, 1-low temperature air preheater, 2-coal economizer, 3-convection tube bundle, 4-high temperature air preheater, 5-upper header, 6-steam connecting pipe, 7-top header, 8- Drum, 9-explosion-proof door, 10-first-level tertiary air, 11-second-level tertiary air, 12-downcomer, 13-furnace, 14-lower header, 15-cleaning port, 16-inspection door, 17- Burner, 18 - furnace smoke outlet.
具体实施方式Detailed ways
参照图1,一种立式煤粉角管式锅炉,包括两个燃烧器17、锅炉炉膛13、高温空气预热器4、省煤器2、低温空气预热器1、对流管束3、上集箱5、顶集箱7、锅筒8和下集箱14,所述的下集箱14设置在锅炉本体的底部,所述的上集箱5和顶集箱7设置在锅炉本体的顶部,并通过汽连通管6联通;所述的燃烧器17设置在锅炉本体的顶部;所述的锅炉本体采用立式角管式结构膜式水冷壁,四角布置4根下降管12,所述下降管12和膜式水冷壁的两端中分别与所述的上集箱5和下集箱14联通;所述的对流管束3采用旗面管,并竖向顺列布置在膜式水冷壁的外侧,对流管束3的底部与炉膛出烟口18联通,顶部与所述的高温空气预热器4联通,省煤器2的烟气进口端与高温空气预热器4另一端联通,出口端连接到低温空气预热器1;所述的顶集箱7与所述锅筒8的汽空间联通;所述的上集箱5与所述锅筒8的水空间联通。Referring to Fig. 1, a vertical pulverized coal corner tube boiler includes two
两个燃烧器17燃烧可独立控制,炉膛13下部设有防爆门9和清灰口15,中部位置布有两级三次风。The combustion of the two
本实用新型的工作原理如下:The working principle of the utility model is as follows:
煤粉或城市污泥借一次风通过顶部两个燃烧器17喷入立式炉膛13,同时,经低温空气预热器1和高温空气预热器4加热后的高温空气也进入燃烧器17与粉体燃料混合进入炉膛13进行猛烈悬浮燃烧;且在炉膛中布置了两级三次风,保证了炉膛有充分的氧气与燃料反应燃烧。在炉膛燃烧换热后的高温烟气从炉膛13下方的炉膛出烟口18处转折180°向上进入旗面管3进行对流换热,烟气再依次进入高温空气预热器4、省煤器2和低温空气预热器1后排入烟气净化系统。在烟气净化系统内,烟气中的固体颗粒被清除掉,干净的预热空气从两个燃烧器17中再次喷入立式炉膛13。高温空气预热器4和低温空气预热器1可利用烟气的余热对空气进行预热,从而达到循环利用和节能的目的。Pulverized coal or urban sludge is sprayed into the
上集箱5、顶集箱7、汽连通管6、下集箱14、炉膛的膜式水冷壁和4根下降管12构成封闭的水循环系统。上集箱5与顶集箱7用汽连通管6连接同时接入锅筒8,汽水混合物从膜式水冷壁的受热面上升进入上集箱5,并在上集箱5里发生汽水预分离,蒸汽经汽连通管6至顶集箱7进入锅筒8上部的汽空间。由于上集箱5均在锅筒8的高水位处接入,则蒸汽没有通过水空间而直接接入锅筒,从而避免了泡沫的产生,再加上进入锅筒8的蒸汽已进行预分离,因此,大大提高了蒸汽的品质。上集箱5里汽水预分离后的水从4根下降管12流入下集箱14,再进入膜式水冷壁内,形成水循环。The upper header 5, the top header 7, the steam connecting pipe 6, the
应该理解到的是:上述实施例只是对本实用新型的说明,而不是对本实用新型的限制,任何不超出本实用新型实质精神范围内的实用新型创造,均落入本实用新型的保护范围之内。It should be understood that: the above-mentioned embodiment is only an illustration of the utility model, rather than a limitation of the utility model, and any utility model creation within the scope of the essential spirit of the utility model all falls within the protection scope of the utility model .
Claims (4)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201220724995.2U CN203203008U (en) | 2012-12-24 | 2012-12-24 | Upright pulverized coal corner tube type boiler |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201220724995.2U CN203203008U (en) | 2012-12-24 | 2012-12-24 | Upright pulverized coal corner tube type boiler |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203203008U true CN203203008U (en) | 2013-09-18 |
Family
ID=49147113
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201220724995.2U Expired - Lifetime CN203203008U (en) | 2012-12-24 | 2012-12-24 | Upright pulverized coal corner tube type boiler |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203203008U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103062748A (en) * | 2012-12-24 | 2013-04-24 | 杭州燃油锅炉有限公司 | Vertical type coal dust corner tube boiler |
-
2012
- 2012-12-24 CN CN201220724995.2U patent/CN203203008U/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103062748A (en) * | 2012-12-24 | 2013-04-24 | 杭州燃油锅炉有限公司 | Vertical type coal dust corner tube boiler |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102644911A (en) | Vertical coal dust corner tube boiler | |
| CN104359098A (en) | Three-return-stroke powder heat conduction oil boiler | |
| CN102374658B (en) | Angular pipe water circulating structure with complete forced upward flowing on heating surface | |
| CN103574594B (en) | Combustion heat supplying system taking living beings as fuel | |
| CN103032864A (en) | Vertical coal powder corner tube boiler | |
| CN203203004U (en) | Horizontal type coal water slurry fired boiler | |
| CN202303349U (en) | Membrane wall type four-flue biomass circulating fluidized bed boiler | |
| CN104359099A (en) | Three-return-stroke powder steam boiler | |
| CN202902245U (en) | Upright-type coal powder corner-tube boiler | |
| WO2008014667A1 (en) | Gas-injection boiler for oil field | |
| CN103134036A (en) | Vertical type modular coal water slurry corner tube boiler | |
| CN203203006U (en) | Upright pulverized coal corner tube type boiler | |
| CN203203008U (en) | Upright pulverized coal corner tube type boiler | |
| CN203203009U (en) | Vertical modularized coal water slurry corner tube boiler | |
| CN202013015U (en) | Vertical half gas positive burning heating boiler | |
| CN203203007U (en) | Upright pulverized coal corner tube type boiler | |
| CN201391999Y (en) | A micro-emission environmentally friendly boiler | |
| CN201753913U (en) | Vertical highly efficient energy-saving environment-friendly boiler | |
| CN103062747A (en) | Vertical type coal dust corner tube boiler | |
| CN201636832U (en) | Steelmaking electric furnace waste heat boiler | |
| CN105485894A (en) | Pulverized coal type water heating boiler | |
| CN204240318U (en) | A kind of three backhaul powder steam boilers | |
| CN205746769U (en) | A kind of pulverized-coal fired boiler | |
| CN204006633U (en) | A kind of modular convection heating surface fire tube boiler | |
| CN102889585A (en) | Environment-friendly energy-saving vertical boiling boiler |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP01 | Change in the name or title of a patent holder |
Address after: Hangzhou City, Zhejiang province 311115 Fengdu Pingyao Town, Yuhang District Industrial Zone Road, Yangcheng Road No. 1-9 Patentee after: HANGZHOU JUNENG ENVIRONMENTAL PROTECTION TECHNOLOGY CO.,LTD. Address before: Hangzhou City, Zhejiang province 311115 Fengdu Pingyao Town, Yuhang District Industrial Zone Road, Yangcheng Road No. 1-9 Patentee before: HANGZHOU JUNENG BOILER Co.,Ltd. |
|
| CP01 | Change in the name or title of a patent holder | ||
| CX01 | Expiry of patent term |
Granted publication date: 20130918 |
|
| CX01 | Expiry of patent term |