CN204555722U - 一种熔炼装置 - Google Patents
一种熔炼装置 Download PDFInfo
- Publication number
- CN204555722U CN204555722U CN201520231260.XU CN201520231260U CN204555722U CN 204555722 U CN204555722 U CN 204555722U CN 201520231260 U CN201520231260 U CN 201520231260U CN 204555722 U CN204555722 U CN 204555722U
- Authority
- CN
- China
- Prior art keywords
- smelting
- flue
- melting
- smelting furnace
- furnace
- 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.)
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- 238000003723 Smelting Methods 0.000 title claims abstract description 110
- 229910001338 liquidmetal Inorganic materials 0.000 claims description 10
- 239000002893 slag Substances 0.000 claims description 10
- 238000002844 melting Methods 0.000 abstract description 63
- 239000000446 fuel Substances 0.000 abstract description 7
- 239000000463 material Substances 0.000 description 28
- UGFAIRIUMAVXCW-UHFFFAOYSA-N carbon monoxide Chemical compound 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[O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 24
- 239000003546 flue gas Substances 0.000 description 24
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicium dioxide Chemical compound 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Abstract
本实用新型涉及一种熔炼装置，由三个熔炼炉组成，排列成三角形，并通过连通烟道连成一体；熔炼炉上设有排烟口烟道，连通烟道上设置阀门。采用本实用新型的熔炼装置熔炼铅泥与传统反射炉相比可提高熔炼热效率，降低燃料消耗量约20%。
Description
技术领域
[0001] 本实用新型涉及一种冶炼设备，具体涉及一种熔炼装置。
背景技术
[0002] 废铅酸蓄电池中的铅泥(以下简称铅泥)的熔炼多用传统的反射炉进行，炉体一端燃烧另一端排出废气，排出的废气温度高，热能没有得到有效的利用，导致此种熔炼方法热效率低、燃料消耗量大。
实用新型内容
[0003] 本实用新型的目的是提供一种熔炼装置，以提高熔炼热效率。
[0004] 本实用新型的技术方案为:一种熔炼装置，由三个熔炼炉组成，排列成三角形，并通过连通烟道连成一体；熔炼炉上设有排烟口烟道，连通烟道上设置阀门。
[0005] 所述三个熔炼炉两两之间用连通烟道连接，每段连通烟道上均设有阀门。每个熔炼炉上均设排烟口烟道，排烟口烟道上均设有阀门。每个熔炼炉均设有加料口、烧嘴口、放渣口和液态金属放出口。
[0006] 所述阀门为水冷闸板。
[0007] 优选熔炼炉为圆形，三个熔炼炉排成正三角形。
[0008] 本实用新型专门针对废铅酸蓄电池中的铅泥熔炼而设计，也可以用于类似物料的熔炼，如炼铅铜浮渣的熔炼等。采用本实用新型的熔炼装置熔炼铅泥与传统反射炉相比可提高熔炼热效率，降低燃料消耗量约20%。
附图说明
[0009] 附图1为本实用新型结构示意图。
[0010] 附图2为图1的1-1视图。
[0011] 其中:1.液态金属放出口 2.熔炼炉炉体3.烧嘴口 4.加料口 5.连通烟道6.水冷闸板7.排烟口烟道8.放渣口。
具体实施方式
[0012] 图1、2为本实用新型的熔炼装置一个具体实施例，三个圆形熔炼炉2排列成正三角形，通过连通烟道5连成一体。圆形熔炼炉2由钢板筒体及内砌耐火材料构成。
[0013] 每个圆形熔炼炉2在炉顶分别设有加料口 4，可以是一个也可以是多个；烧嘴口 3设在圆形熔炼炉筒体上，朝筒体内向下有一定的角度，烧嘴口数量可以是一个也可以是多个；放渣口 8设在圆形熔炼炉筒体下部；液态金属放出口 I设在靠近炉底；排烟口烟道7设在圆形熔炼炉筒体上部；排烟口烟道7和连通烟道5上都设有水冷闸板6。
[0014] 本实用新型的熔炼装置可以用于铅泥及类似物料的熔炼，如炼铅铜浮渣的熔炼，操作方法相同。依据图1、图2对本实用新型三位一体式熔炼装置的操作方法作以下描述(为便于描述将三个熔炼炉标上A、B、C)。
[0015] 新炉或大修后的炉子第一次开炉:将铅泥(或待熔炼物料)从加料口 4分别加入到圆形熔炼炉A、B、C内。
[0016] 1.对熔炼炉A内的铅泥(或待熔炼物料)进行熔炼:
[0017] 将熔炼炉A-C之间的连通烟道5上的水冷闸板6闸上，将熔炼炉A、熔炼炉B的排烟口烟道7上的水冷闸板6也闸上。燃料从熔炼炉A烧嘴口 3喷入，对熔炼炉A内的铅泥(或待熔炼物料)进行熔炼，熔炼结束，熔炼渣从放渣口 8放出，铅(或液态金属)从液态金属放出口 I放出。
[0018] 熔炼炉A熔炼时产生的高温烟气通过熔炼炉A-B之间的连通烟道5进入熔炼炉B，加热熔炼炉B内的铅泥(或待熔炼物料)；高温烟气再通过熔炼炉B-C之间的连通烟道5进入熔炼炉C，加热熔炼炉C内的铅泥(或待熔炼物料)，随着高温烟气与熔炼炉B、熔炼炉C内的铅泥(或待熔炼物料)的接触将其加热、熔化，一方面烟气温度得以降低烟气余热得以利用，一方面烟气中的尘会随着烟气温度的降低和与待熔炼物料的接触而部分落入到熔炼炉B和熔炼炉C内，降低了烟气含尘。烟气通过熔炼炉C的排烟口烟道7排出炉外。
[0019] 2.对熔炼炉B内物料进行熔炼:
[0020] 对熔炼炉A内的铅泥(或待熔炼物料)熔炼周期结束后，将熔炼炉A-B之间的连通烟道5上的水冷闸板6闸上，将熔炼炉B、熔炼炉C的排烟口烟道7上的水冷闸板6也闸上，将熔炼炉A的排烟口烟道7上的水冷闸板6打开。燃料从熔炼炉B烧嘴口 3喷入，对熔炼炉B内的铅泥(或待熔炼物料)进行熔炼(同时给熔炼炉A加料)。
[0021] 熔炼结束，熔炼渣从放渣口 8放出，铅(或液态金属)从液态金属放出口 I放出。
[0022] 熔炼炉B熔炼时产生的高温烟气通过熔炼炉B-C之间的连通烟道5进入熔炼炉C，加热熔炼炉C内的铅泥(或待熔炼物料)；高温烟气再通过熔炼炉A-C之间的连通烟道5进入熔炼炉A，加热熔炼炉A内的铅泥(或待熔炼物料)。同样，随着高温烟气与熔炼炉C、熔炼炉A内的铅泥域待熔炼物料)的接触将其加热、恪化，一方面烟气温度得以降低烟气余热得以利用，一方面烟气中的尘会随着烟气温度的降低和与待熔炼物料的接触而部分落入到熔炼炉C和熔炼炉A内。烟气通过熔炼炉A的排烟口烟道7排出炉外。
[0023] 3.对熔炼炉C内物料进行熔炼:
[0024] 对熔炼炉B内的铅泥(或待熔炼物料)熔炼周期结束后，将熔炼炉B-C之间的连通烟道5上的水冷闸板6闸上，将熔炼炉A、熔炼炉C的排烟口烟道7上的水冷闸板6也闸上，将熔炼炉B的排烟口烟道7上的水冷闸板6打开(同时给熔炼炉B加料)。燃料从熔炼炉C烧嘴口 3喷入，对熔炼炉C内的铅泥(或待熔炼物料)进行熔炼，熔炼结束，熔炼渣从放渣口8放出，铅(或液态金属)从液态金属放出口 I放出。
[0025] 熔炼炉C熔炼时产生的高温烟气通过熔炼炉A-C之间的连通烟道5进入熔炼炉A，加热熔炼炉A内的铅泥(或待熔炼物料)；高温烟气再通过熔炼炉A-B之间的连通烟道5进入熔炼炉B，加热熔炼炉B内的铅泥(或待熔炼物料)。同样，随着高温烟气与熔炼炉A、熔炼炉B内的铅泥(或待熔炼物料)的接触将其加热、熔化，一方面烟气温度得以降低烟气余热得以利用，一方面烟气中的尘会随着烟气温度的降低和与待熔炼物料的接触而部分落入到熔炼炉A和熔炼炉B内。烟气通过熔炼炉B的排烟口烟道7排出炉外。
[0026]由于熔炼炉C内的铅泥(或待熔炼物料)受到熔炼炉A、熔炼炉B熔炼时产生的高温烟气的连续加热，炉内的铅泥(或待熔炼物料)已熔化或基本熔化，所以熔炼炉C的熔炼时间会大为缩短。与同规模传统反射炉相比，可降低燃料消耗量约20%。
[0027]同样，对熔炼炉C的熔炼结束后，又开始对熔炼炉A内的铅泥(或待熔炼物料)进行熔炼(同时给熔炼炉C加料)，这时熔炼炉A内的铅泥(或待熔炼物料)受到熔炼炉B、熔炼炉C熔炼时产生的高温烟气的连续加热，炉内的铅泥(或待熔炼物料)已熔化或基本熔化。所以熔炼炉A的熔炼时间同样会大为缩短。
[0028] 以此方法周而复始进行。
Claims (6)
1.一种熔炼装置，其特征在于由三个熔炼炉组成，排列成三角形，并通过连通烟道连成一体；熔炼炉上设有排烟口烟道，连通烟道上设置阀门。
2.根据权利要求1所述的熔炼装置，其特征在于三个熔炼炉两两之间用连通烟道连接，每段连通烟道上均设有阀门。
3.根据权利要求1所述的熔炼装置，其特征在于每个熔炼炉上均设排烟口烟道，排烟口烟道上均设有阀门。
4.根据权利要求1~3之一所述的熔炼装置，其特征在于所述阀门为水冷闸板。
5.根据权利要求1所述的熔炼装置，其特征在于熔炼炉为圆形，三个熔炼炉排成正三角形。
6.根据权利要求1、2、3或5所述的熔炼装置，其特征在于每个熔炼炉均设有加料口、烧嘴口、放渣口和液态金属放出口。
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| CN105506299B (zh) * | 2016-02-15 | 2017-06-06 | 江苏新春兴再生资源有限责任公司 | 一种低品位再生铅熔炼渣烟化炉处理系统及方法 |
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