CN102032591A - 一种煤粉点火系统及其控制方法 - Google Patents
一种煤粉点火系统及其控制方法 Download PDFInfo
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- CN102032591A CN102032591A CN2009101750682A CN200910175068A CN102032591A CN 102032591 A CN102032591 A CN 102032591A CN 2009101750682 A CN2009101750682 A CN 2009101750682A CN 200910175068 A CN200910175068 A CN 200910175068A CN 102032591 A CN102032591 A CN 102032591A
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- UGFAIRIUMAVXCW-UHFFFAOYSA-N carbon monoxide Chemical compound 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- GQPLMRYTRLFLPF-UHFFFAOYSA-N nitrous Oxide Chemical class 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[O-][N+]#N GQPLMRYTRLFLPF-UHFFFAOYSA-N 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N phosphorus Chemical compound 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Abstract
本发明涉及一种煤粉点火系统，包括煤粉储仓和点火燃烧器，所述煤粉储仓的出煤管道与送风管道和风粉管道连通，使所述出煤管道输出的煤粉与所述送风管道输入的风混合，进入所述风粉管道；所述风粉管道与所述点火燃烧器连接，使煤粉通过所述风粉管道进入所述点火燃烧器；所述点火燃烧器的出口与循环流化床锅炉连接，所述点火燃烧器内设高温热源和内燃筒，所述高温热源在所述内燃筒中点燃煤粉，喷射到所述循环流化床锅炉内。本发明还公开一种煤粉点火系统的控制方法。本发明在循环流化床锅炉点火启动时，不需燃油加热循环流化床锅炉，可节省大量的燃油，具有较好的经济性，并且防止燃烧污染物通过烟囱直接排放到大气中，具有良好的环保性。
Description
一种煤粉点火系统及其控制方法技术领域[0001] 本发明涉及燃烧器领域，特别是涉及一种应用于循环流化床锅炉的煤粉点火系统 及其控制方法。背景技术[0002] 循环流化床（CFB)锅炉在工作时，炉膛内的煤粒被吹起呈沸腾状态悬浮燃烧，同 时在炉膛出口将高温烟气进行分离，并将收集到的含碳量较多的飞灰送回炉膛再燃烧。因 具有燃料适应范围广、燃烧效率高、易于实现脱硫、氮氧化物排放浓度低、机组负荷调节范 围大等优点，CFB锅炉已被广泛应用在水泥、冶炼、发电等领域。[0003] 参见图1，示出现有的循环流化床锅炉结构，CFB锅炉101内设有点火床料102，点 火床料102为石子、炉渣等材料。在CFB锅炉101启动时，点火床料102吸收并储存点火燃 料释放出来的热量，当点火床料102温度升高至一定程度后，用来加热、点燃主燃料。CFB锅 炉101的炉膛下方为点火风道107，点火风道107在CFB锅炉101工作时，将空气高速送入炉膛。[0004] 一般情况下，CFB锅炉101使用冷态点火启动方式，先在炉膛内铺设点火床料102， 用大油枪111将点燃的燃油喷入炉膛，油燃烧释放出的热量加热点火床料102和炉膛内空 气，当点火床料102和炉膛内空气温度升高到可以维持燃料煤的燃烧后，向炉膛内投入燃 料煤，并退出大油枪111，CFB锅炉101完成点火启动。[0005] CFB锅炉101在使用一段时间后，会因炉膛内灰含量较大，受热面磨损严重等原 因，导致机组运行稳定性较低，CFB锅炉101启停操作频率较高，每次点火启动都需大量的 燃油，使年燃油消耗量较大，造成能源浪费。以一台机组容量为135MW的CFB锅炉101为例， 每年需要消耗大约400-500吨燃油，以一吨燃油6000元计算，每年燃油花费为240-300万元。[0006] CFB锅炉101点火启动和燃烧时，炉膛内会产生大量的飞灰等污染物，CFB锅炉101 通过电除尘器可去除该污染物，避免污染环境。但在上述点火启动期间，为防止未燃尽的油 滴附着在电除尘器的极板上，使电除尘器失效，电除尘器不投入运行，导致大量飞灰等污染 物通过烟®直接排放到大气中，造成环境污染。发明内容[0007] 本发明所要解决的技术问题是提供一种煤粉点火系统，该煤粉点火系统应用到 CFB锅炉，在CFB锅炉点火启动时，不需耗费大量的燃油，并可防止飞灰等污染物直接排放 到大气中，具有较好的经济性和环保性。[0008] 本发明还提供一种煤粉点火系统的控制方法，该控制方法在CFB锅炉点火启动期 间，不需耗费大量的燃油，并可防止飞灰等污染物直接排放到大气中，具有较好的经济性和 环保性。[0009] 本发明公开一种煤粉点火系统，包括煤粉储仓和点火燃烧器，所述煤粉储仓的出煤管道与送风管道和风粉管道连通，使所述出煤管道输出的煤粉与所述送风管道输入的风 混合，进入所述风粉管道；所述风粉管道与所述点火燃烧器连接，使煤粉通过所述风粉管道 进入所述点火燃烧器；所述点火燃烧器的出口与循环流化床锅炉连接，所述点火燃烧器内 设高温热源和内燃筒，所述高温热源在所述内燃筒中点燃煤粉，喷射到所述循环流化床锅 炉内。[0010] 优选的，所述高温热源为等离子体发生器或小油枪。[0011 ] 优选的，所述高温热源轴向或径向插入所述点火燃烧器中。[0012] 优选的，所述煤粉储仓的出煤管道上设有给粉机，所述给粉机将所述煤粉储仓中 落下的煤粉送入所述风粉管道。[0013] 优选的，所述煤粉储仓的出煤管道与送风管道和风粉管道通过风粉混合器连通， 所述风粉混合器在所述风粉管道上产生局部负压区域，使煤粉进入风粉管道与一次风气流混合ο[0014] 优选的，所述点火燃烧器的出口与所述循环流化床锅炉的点火风道连通，或与所 述循环流化床锅炉的炉膛连通。[0015] 优选的，所述循环流化床锅炉上安装至少两个所述点火燃烧器，所述点火燃烧器 的出口与所述循环流化床锅炉的炉膛和/或点火风道连通。[0016] 优选的，所述煤粉储仓上设有粉位计、压力表、和/或温度表。[0017] 优选的，所述煤粉储仓上设有安全阀，所述安全阀在所述煤粉储仓内压力超过设 定值时，释放所述煤粉储仓内的气体。[0018] 本发明还公开一种如权利要求1-9所述煤粉点火系统的控制方法，该控制方法包 括：打开所述煤粉储仓的出口，输出煤粉；在所述送风管道通入高速风；所述点火燃烧器内 的高温热源启动，释放热量点燃煤粉，燃烧的煤粉加热所述循环流化床锅炉的点火床料和 炉膛内空气；所述点火床料和空气的温度升至预设温度时，退出所述点火燃烧器，所述循环 流化床锅炉完成点火启动。[0019] 与现有技术相比，本发明具有以下优点：[0020] 本发明利用点火燃烧器点燃煤粉释放出的热量，以加热点火床料和炉膛内的空 气，相对图1所示现有技术中，用大油枪将点燃的燃油喷入炉膛，加热点火床料和炉膛内空 气，本发明不需燃油加热，因此，可节省大量的燃油，具有较好的经济性。[0021] 本发明使用燃烧的煤粉加热点火床料和炉膛内空气，煤粉燃烧生成气态的(X)2或 C0，不会有未燃尽的液体或固体附着在电除尘器的极板上，损坏电除尘器。因此，在CFB锅 炉点火启动时，电除尘器可投入运行，去除燃烧污染物，防止燃烧污染物通过烟囱直接排放 到大气中，具有良好的环保性。附图说明[0022] 为了更清楚地说明本发明实施例中的技术方案，下面将对现有技术和实施例中所 需要使用的附图作简单地介绍，显而易见地，下面描述中的附图仅仅是本发明的一些实施 例，对于本领域普通技术人员来讲，在不付出创造性劳动的前提下，还可以根据这些附图获 得其他的附图。[0023] 图1为现有的循环流化床结构示意图；[0024] 图2为本发明煤粉点火系统第一实施例示意图；[0025] 图3为本发明煤粉点火系统第二实施例示意图；[0026] 图4为本发明煤粉点火系统第三实施例示意图。具体实施方式[0027] 为使本发明的上述目的、特征和优点能够更加明显易懂，下面结合附图和具体实 施方式对本发明作进一步详细的说明。[0028] 参见图2，示出本发明煤粉点火系统第一实施例，该点火系统包括CFB锅炉101、煤 粉储仓103、及点火燃烧器104。煤粉储仓103的出口连接出煤管道1031输入端，出煤管道 1031输出端与风粉管道109的输入端和送风管道108连通，使出煤管道1031输出的煤粉 与送风管道108输入的风混合，进入风粉管道109 ；风粉管道109的输出端连接点火燃烧器 104的输入端，使煤粉可以通过风粉管道109进入点火燃烧器104 ；点火燃烧器104安装在 CFB锅炉101上，点火燃烧器104的出口与CFB锅炉101的炉膛连通。[0029] 点火燃烧器104内设高温热源105和内燃筒106，内燃筒106是点火燃烧器104的 内燃空间。高温热源105在内燃筒106中点燃煤粉，使煤粉在内燃筒106中燃烧。点火燃 烧器104将燃烧的煤粉喷射到CFB锅炉101内，煤粉在CFB锅炉101内继续燃烧。[0030] CFB锅炉101内设有点火床料102，点火床料102为石子、炉渣等材料。CFB锅炉 101的炉膛下方为点火风道107，点火风道107在CFB锅炉101工作时，将空气高速送入炉 膛。[0031] 煤粉储仓103设置在CFB锅炉101附近，煤粉储仓103的容量满足锅炉点火所需 的煤粉。煤粉储仓103的上具有可打开的进口，用以装入煤粉。现以上述煤粉点火系统为 例，具体说明本发明煤粉点火系统的控制方法。[0032] 步骤一，CFB锅炉101点火启动时，打开煤粉储仓103的出口，并在送风管道108通 入高速的一次风；煤粉通过出煤管道1031输出，与送风管道108输入的一次风混合后形成 煤粉气流，进入风粉管道109，并通过风粉管道109送入点火燃烧器104内。[0033] 步骤二，点火燃烧器104内的高温热源105启动，释放热量将煤粉点燃，煤粉中的 C元素大量反应生成(X)2或CO气体，反应生成物及未燃尽的煤粉一同由点火燃烧器104的 出口进入CFB锅炉101炉膛，煤粉在炉膛内继续燃烧反应，释放大量的热量，加热点火床料 102和炉膛内的空气。[0034] 步骤三，当点火床料102和炉膛内空气的温度升至预设温度时，给入主燃料煤，主 燃料煤被高温的点火床料和空气点燃，点火燃烧器104退出运行，CFB锅炉101完成点火启 动，CFB锅炉101进入正常运行状态。预设温度是指满足向CFB锅炉101投入主燃料煤后， 主燃料煤点燃并维持燃烧的温度。[0035] 本发明利用点火燃烧器104点燃的煤粉，以加热点火床料102和炉膛内的空气，相 对图1所示现有技术中，用大油枪将点燃的燃油喷入炉膛，加热点火床料102和炉膛内空 气，本发明不需燃油加热，因此，可节省大量的燃油，具有较好的经济性。[0036] 本发明使用燃烧的煤粉加热点火床料和炉膛内空气，煤粉燃烧生成气态的(X)2或 C0，不会有未燃尽的液体或固体附着在电除尘器的极板上，损坏电除尘器。因此，在CFB锅 炉101点火启动时，电除尘器可投入运行，去除燃烧污染物，防止燃烧污染物通过烟囱直接排放到大气中，具有良好的环保性。[0037] 本发明通过煤粉储仓103存储CFB锅炉101点火所需的煤粉，不需再设置磨煤机 系统生产煤粉，可降低企业生产成本。[0038] 本发明点火燃烧器104含有高温热源105，优选地，高温热源105为等离子体发生 器或小油枪。如高温热源105为小油枪，燃油点火燃烧器喷射燃烧的油料作为点火源，在燃 烧器内点燃煤粉，直接向CFB锅炉101内喷射火焰。相对于CFB锅炉101的炉膛，内燃筒 106体积非常小，只需少量燃油即可使内燃筒106温度升高到可直接点燃煤粉，每次点火启 动所需燃油量非常少，因此，上述点火燃烧器104可更好的节省燃油，具有良好的经济性。[0039] 如高温热源105为等离子体发生器，等离子体发生器以等离子体电弧为点火源， 点燃煤粉，不需耗费燃油，具有更佳的经济性。应用等离子体发生器还可取消提供燃油所需 的输油管道等附属设备，避免消防安全隐患，提高整个煤粉点火系统的安全性。[0040] 当然，本发明点火燃烧器104还可以是燃气点火装置、激光点火装置等。[0041] 高温热源105可以轴向或径向方式布置在点火燃烧器104内。轴向布置时，煤粉 气流流动方向与高温热源105的设置方向相同，点火燃烧器104内烧损的几率小；采用径向 布置时，煤粉气流大部分直接与高温热源105接触，点火较容易。[0042] 实施例二。[0043] 本发明CFB锅炉101上可以安装一台或多台点火燃烧器104，点火燃烧器104的出 口可与CFB锅炉101的炉膛相连接，也可与CFB锅炉101的点火风道107连接。[0044] 参见图3，示出示出本发明粉煤点火系统第二实施例，该点火系统包括CFB锅炉 101、煤粉储仓103、及两个点火燃烧器104。煤粉储仓103的出口连接出煤管道1031输入 端，出煤管道1031输出端与风粉管道109的输入端和送风管道108连通，风粉管道109具 有两个输出端，两个输出端分别连接两个点火燃烧器104的输入端。[0045] 两个点火燃烧器104，其中一个的出口与CFB锅炉101的炉膛连通，另一个的出口 与CFB锅炉101的点火风道107连通。[0046] CFB锅炉101点火启动时，煤粉通过出煤管道1031输出，与送风管道108输入的一 次风混合后形成煤粉气流，进入风粉管道109，并通过风粉管道109分别送入两个点火燃烧 器104内。[0047] 两个点火燃烧器104分别将煤粉点燃，并从上、下两个方向加热点火床料102和 炉膛内的空气，可在较短的时间内使点火床料102和空气迅速升温，达到达到预设温度，使 CFB锅炉101快速点火启动，提高点火启动效率。[0048] 本发明可在CFB锅炉101上安装一个点火燃烧器104，点火燃烧器104的出口与点 火风道107连接或与CFB锅炉101的炉膛相连接。本领域人员应知，本发明可在CFB锅炉 101上安装多个点火燃烧器104，多个点火燃烧器104的出口可全部与点火风道107连接， 也可全部与炉膛连接，还可部分与点火风道107连接，部分与炉膛连接。[0049] 多个点火燃烧器104在点火启动阶段同时燃烧煤粉，以提高CFB锅炉101点火启 动效率，在此不一一赘述。[0050] 实施例三。[0051] 在生产现场，送风管道108内的压力很可能高于煤粉储仓103内的压力，使得煤粉 储仓103中的煤粉不能顺利进入风粉管道109，造成输送困难。本发明可通过给粉机，也可通过风粉混合器使煤粉顺利输送到CFB锅炉101。[0052] 参见图4，示出本发明粉煤点火系统第三实施例，包括CFB锅炉101、煤粉储仓103、 及点火燃烧器104。煤粉储仓103的出口连接出煤管道1031输入端，出煤管道1031输出 端、风粉管道109的输入端、及送风管道108的输出端都连接在风粉混合器202上，通过风 粉混合器202连通，出煤管道1031上安装有给粉机201 ；风粉管道109的输出端连接点火燃 烧器104的输入端，点火燃烧器104安装在CFB锅炉101上，点火燃烧器104的出口与CFB 锅炉101的炉膛连接。[0053] 给粉机201强制将煤粉储仓101中落下的煤粉排出，使煤粉进入出煤管道1031。[0054] 而风粉混合器202在内部气流压力较高的送风管道108和风粉管道109内产生一 定的负压区，使煤粉能够有效克服管道阻力，进入风粉混合器202，与一次风混合后，送入风 粉管道109。[0055] 本发明通过给粉机201或风粉混合器202可实现煤粉的顺利输送，可只安装给粉 机210或风粉混合器202，也可二者都安装。[0056] 本发明可在煤粉储仓101内设置粉位计，测量煤粉储仓101内煤粉的堆积高度。 era锅炉ιοί启动前，将点火需要用到的煤粉装入煤粉储仓ιοί中，借助粉位计的测试值，生 产人员可了解煤粉储仓ιοί内的煤粉量是否足够点火所需，在点火启动过程中还可监视剩 余煤粉量。[0057] 本发明还可在煤粉储仓101内设置压力表、温度表、及安全阀，压力表和温度表监 测煤粉储仓101内的压力、温度等参数，防止煤粉储仓101因压力、温度过高发生爆炸危险。 安全阀在煤粉储仓101内部压力较高时释放部分气体，使煤粉储仓101内部压力恢复到正 常值，避免发生危险。[0058] 以上所述仅是本发明的优选实施方式，应当指出，对于本技术领域的普通技术人 员来说，在不脱离本发明原理的前提下，还可以做出若干改进和润饰，也可以上述具体实施 方式的进行组合，这些改进、润饰及组合形成的技术方案也应视为本发明的保护范围。
Claims (10)
1. 一种煤粉点火系统，其特征在于，包括煤粉储仓和点火燃烧器，所述煤粉储仓的出煤 管道与送风管道和风粉管道连通，使所述出煤管道输出的煤粉与所述送风管道输入的风混 合，进入所述风粉管道；所述风粉管道与所述点火燃烧器连接，使煤粉通过所述风粉管道进 入所述点火燃烧器；所述点火燃烧器的出口与循环流化床锅炉连接，所述点火燃烧器内设高温热源和内燃 筒，所述高温热源在所述内燃筒中点燃煤粉，喷射到所述循环流化床锅炉内。
2.如权利要求1所述的煤粉点火系统，其特征在于，所述高温热源为等离子体发生器 或小油枪。
3.如权利要求2所述的煤粉点火系统，其特征在于，所述高温热源轴向或径向插入所 述点火燃烧器中。
4.如权利要求1或2所述的煤粉点火系统，其特征在于，所述煤粉储仓的出煤管道上设 有给粉机，所述给粉机将所述煤粉储仓中落下的煤粉送入所述风粉管道。
5.如权利要求1或2所述的煤粉点火系统，其特征在于，所述煤粉储仓的出煤管道与送 风管道和风粉管道通过风粉混合器连通，所述风粉混合器在所述风粉管道上产生局部负压 区域，使煤粉进入风粉管道与一次风气流混合。
6.如权利要求1或2所述的煤粉点火系统，其特征在于，所述点火燃烧器的出口与所述 循环流化床锅炉的点火风道连通，或与所述循环流化床锅炉的炉膛连通。
7.如权利要求1或2所述的煤粉点火系统，其特征在于，所述循环流化床锅炉上安装至 少两个所述点火燃烧器，所述点火燃烧器的出口与所述循环流化床锅炉的炉膛和/或点火 风道连通。
8.如权利要求1或2所述的煤粉点火系统，其特征在于，所述煤粉储仓上设有粉位计、 压力表、和/或温度表。
9.如权利要求1或2所述的煤粉点火系统，其特征在于，所述煤粉储仓上设有安全阀， 所述安全阀在所述煤粉储仓内压力超过设定值时，释放所述煤粉储仓内的气体。
10. 一种如权利要求1-9所述煤粉点火系统的控制方法，其特征在于，该控制方法包括：打开所述煤粉储仓的出口，输出煤粉；在所述送风管道通入高速风；所述点火燃烧器内的高温热源启动，释放热量点燃煤粉，燃烧的煤粉加热所述循环流 化床锅炉的点火床料和炉膛内空气；所述点火床料和空气的温度升至预设温度时，退出所述点火燃烧器，所述循环流化床 锅炉完成点火启动。
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105910134A (zh) * | 2016-04-14 | 2016-08-31 | 北京大学 | 一种等离子体点火助燃系统 |
| CN109433398A (zh) * | 2018-10-24 | 2019-03-08 | 大唐湘潭发电有限责任公司 | 中间储仓式制粉系统锅炉余粉开机节油方法 |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105910134A (zh) * | 2016-04-14 | 2016-08-31 | 北京大学 | 一种等离子体点火助燃系统 |
| CN105910134B (zh) * | 2016-04-14 | 2018-07-17 | 北京大学 | 一种等离子体点火助燃系统 |
| CN109433398A (zh) * | 2018-10-24 | 2019-03-08 | 大唐湘潭发电有限责任公司 | 中间储仓式制粉系统锅炉余粉开机节油方法 |
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