CN203203013U - 生物质蒸汽发生器 - Google Patents
生物质蒸汽发生器 Download PDFInfo
- Publication number
- CN203203013U CN203203013U CN 201320176898 CN201320176898U CN203203013U CN 203203013 U CN203203013 U CN 203203013U CN 201320176898 CN201320176898 CN 201320176898 CN 201320176898 U CN201320176898 U CN 201320176898U CN 203203013 U CN203203013 U CN 203203013U
- Authority
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- China
- Prior art keywords
- heater
- communicated
- steam generator
- furnace
- heat exchanging
- 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 - Fee Related
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- 239000002028 Biomass Substances 0.000 title claims abstract description 32
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances data:image/svg+xml;base64,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 data:image/svg+xml;base64,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 O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 65
- 238000002485 combustion reaction Methods 0.000 claims abstract description 27
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- 239000003500 flue dust Substances 0.000 description 8
- 239000003546 flue gas Substances 0.000 description 4
- 239000007789 gas Substances 0.000 description 4
- UGFAIRIUMAVXCW-UHFFFAOYSA-N carbon monoxide Chemical compound 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- 238000010521 absorption reaction Methods 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound 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[C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 239000003245 coal Substances 0.000 description 2
- 238000004200 deflagration Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 239000002918 waste heat Substances 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 1
- CURLTUGMZLYLDI-UHFFFAOYSA-N carbon dioxide Chemical compound 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O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
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- 235000021049 nutrient content Nutrition 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N sulfur Chemical compound 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[S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
Abstract
本实用新型提供了一种生物质蒸汽发生器，属于燃料设备技术领域。它解决了现有的蒸汽发生器燃烧成本高、热转化率低的问题。本生物质蒸汽发生器，包括底座、设于底座上方的炉体一和炉体二，炉体一的下侧部具有进料口，炉体一的顶部具有出烟管一，炉体二的侧部具有进烟管，进烟管与出烟管一连通，炉体二的顶部设有出烟管二，燃烧室与炉体一之间形成换热腔一，炉体一的上侧部设有水位计，炉体一上还设有进水口一和出汽口；换热室与炉体二之间形成换热腔二，炉体二上还设有与该换热腔二连通的进水口二和出水口，出水口与进水口一连通。本实用新型具有燃烧成本低、热转化效率高等优点。
Description
生物质蒸汽发生器
技术领域
[0001] 本实用新型属于燃料设备技术领域，涉及一种蒸汽发生器，特别是一种生物质蒸汽发生器。
[0002] 背景技术
[0003] 蒸汽发生器是利用燃料或其他能源的热能把水加热成为热水或蒸汽的机械设备，广泛应用于各种领域，如餐饮、桑拿等，为人们的生活带来了便利。如今蒸汽发生器基本采用燃气加热的方式，市场常用的燃气蒸汽机均是比较机械式的，不够智能化，在安全防护方面明显不足，特别是水位控制方面和点火控制方面基本没有非常健全的安全防护，机器工作容易出现爆燃现象，轻则损坏机器，重则危害人们的身体健康以及财富。
[0004] 为此，人们经过长期的探索，提出了各种各样的解决方案，有些还申请了专利。例如，中国专利公开了一种燃气蒸汽发生器[申请公布号为CN 102679304A]，包括蒸汽发生器主体、内胆、设于蒸汽发生器主体一侧的自来水进水口、蒸汽供出口、排烟管、底座、支撑脚、设于底座下方的燃烧器，蒸汽发生器主体为圆柱形，在蒸汽发生器主体的侧壁上设有电子控制器面板，燃烧器采用纯电子式控制火焰的安全控制技术。
[0005] 上述的燃气蒸汽发生器虽然工作更智能化，杜绝了爆燃现象，增强了安全性。其依然存在以下缺点:在实际使用过程中，大量消耗石化能源，使用成本很高，不利于大市场的推广。所以人们不断开发新能源，生物质成型燃料是一种低碳环保型的清洁能源，在燃烧时能达到二氧化碳的零排放，含硫量仅是煤的20%左右。其养分含量高，容易点燃，燃烧率高于煤，生产成本低，资源分布广。因此，需要提供一种燃烧生物质颗粒燃料的蒸汽发生器。
[0006] 发明内容
[0007] 本实用新型的目的是针对现有的技术存在上述问题，提出了一种热量转换率高的生物质蒸汽发生器。
[0008] 本实用新型的目的可通过下列技术方案来实现:
[0009] 本生物质蒸汽发生器，包括底座、设于底座上方的其内部具有燃烧室的炉体一和其内部具有换热室的炉体二，所述炉体一的下侧部具有其内端与燃烧室连通的进料口，所述炉体一的顶部具有伸出至炉体一的出烟管一，所述炉体二的侧部具有其内端与换热室连通的进烟管，所述的进烟管与上述的出烟管一连通，所述炉体二的顶部设有出烟管二，其特征在于，所述的燃烧室与炉体一之间形成用于蓄水的换热腔一，所述炉体一的上侧部设有与该换热腔一连通的水位计，所述的炉体一上还设有与换热腔一连通的进水口一和出汽口 ；所述的换热室与炉体二之间形成用于蓄水的换热腔二，所述的炉体二上还设有与该换热腔二连通的进水口二和出水口，所述的出水口与上述的进水口一连通。
[0010] 燃烧过程:生物质燃料在送料结构的作用下进入到进料口内，对其进行点火，生物质燃料在燃烧室内燃烧，烟尘随着出烟管一进入到进烟管内，随后烟尘进入到换热室内，最后经出烟管二排出，烟尘在本发生器内停留的时间较长，所以，与水的热交换时间也越长。热交换过程:冷水首先从进水口 二进入到换热腔二内，吸收换热室内烟气的热量，水温升高；水温升高的水经出水口流入到换热腔一内，吸收燃烧室内烟尘的热量，水温再次升高，部分水变为水蒸气，从出汽口排出，供人们使用。
[0011] 换热腔一内的水位可由水位计读出，其水位不能超过规定值。
[0012] 在上述的生物质蒸汽发生器中，所述的燃烧室上穿设有若干均匀分布的换热管，所述换热管的两端分别与上述的换热腔一连通，所述的若干换热管倾斜设置。
[0013] 在上述的生物质蒸汽发生器中，所述炉体一的顶部设有用于测量换热腔一内压力的压力表，所述炉体一的顶部还设有安全阀。
[0014] 在上述的生物质蒸汽发生器中，所述炉体二的上侧部还具有与换热腔二连通的溢水口，所述的进水口二位于出水口的上方。
[0015] 在上述的生物质蒸汽发生器中，所述的炉体二上设有托架，所述的托架上设有一净水器，所述净水器的下部具有一水泵，所述的水泵设于底座上。
[0016] 在上述的生物质蒸汽发生器中，所述换热室的下部具有一呈倒锥形的除尘器，所述除尘器的下部具有一集灰腔，所述集灰腔的侧壁具有一其外端伸出至炉体二的清灰口。
[0017] 在上述的生物质蒸汽发生器中，所述换热腔一的底部处设有排污管，所述排污管的外端伸出至炉体一的侧壁。
[0018] 与现有技术相比，本生物质蒸汽发生器具有以下优点:
[0019] 采用换热管增大热交换面积，提高热量转化率；在炉体一的上部设有安全阀，当换热腔一内的压力大于设定压力时，安全阀打开，自动化程度高，避免主体内压力过高，有效降低主体爆炸的概率，提高了本蒸汽发生器的安全性；还设置有炉体二，在炉体二内设有换热腔二，对烟气进行余热回收，提高了对生物质燃料燃烧的利用率，有效节约资源。
[0020] 附图说明
[0021] 图1是本实用新型提供的一种较佳实施例的结构示意图。
[0022] 图2是本实用新型提供的图1的后视图。
[0023] 图3是本实用新型提供的图1的俯视图。
[0024] 图中，1、底座；2、炉体一 ；21、燃烧室；22、进料口 ；23、出烟管一 ；24、换热腔一；25、水位计；26、进水口一 ；27、出汽口 ；28、排污管；3、炉体二 ；31、换热室；32、进烟管；33、出烟管二 ；34、换热腔二 ；35、进水口二 ；36、出水口 ；37、溢水口 ；38、除尘器；39、清灰口 ；4、压力表；5、安全阀；6、托架；7、净水器；8、水泵。
[0025] 具体实施方式
[0026] 以下是本实用新型的具体实施例并结合附图，对本实用新型的技术方案作进一步的描述，但本实用新型并不限于这些实施例。
[0027] 本生物质蒸汽发生器，其结构如图1和图2所示，它包括底座1、设于底座I上方的其内部具有燃烧室21的炉体一 2，还包括设于底座I上的其内部具有换热室31的炉体二 3。如图1和图2所示，炉体一 2的下侧部具有其内端与燃烧室21连通的进料口 22，炉体一 2的顶部具有伸出至炉体一 2的出烟管一 23，炉体二 3的侧部具有其内端与换热室31连通的进烟管32，进烟管32与出烟管一 23连通，炉体二 3的顶部设有出烟管二 33。如图1和图2所示，在燃烧室21与炉体一 2之间形成用于蓄水的换热腔一 24，炉体一 2的上侧部设有与该换热腔一 24连通的水位计25，炉体一 2上还设有与换热腔一 24连通的进水口
一 26和出汽口 27。如图1和图2所示，换热室31与炉体二 3之间形成用于蓄水的换热腔
二 34，炉体二 3上还设有与该换热腔二 34连通的进水口二 35和出水口 36，出水口 36与进水口一 26连通。如图1和图2所示，换热腔一 24内的水位可由水位计25读出，其水位不能超过规定值。
[0028] 如图1和图2所示，在燃烧室21上穿设有若干均匀分布的换热管，换热管的两端分别与换热腔一 24连通，若干换热管倾斜设置。设置换热管，可增加换热面积，提高换热效率。
[0029] 如图3所示，炉体一 2的顶部设有用于测量换热腔一 24内压力的压力表4，炉体一2的顶部还设有安全阀5。
[0030] 如图1和图2所示，炉体二 3的上侧部还具有与换热腔二 34连通的溢水口 37，进水口二 35位于出水口 36的上方。
[0031] 本实施例中，如图1和图2所示，在炉体二 3上设有托架6，托架6上设有一净水器7，净水器7的下部具有一水泵8，水泵8设于底座I上。
[0032] 如图1和图2所示，换热室31的下部具有一呈倒锥形的除尘器38，除尘器38的下部具有一集灰腔，集灰腔的侧壁具有一其外端伸出至炉体二 3的清灰口 39。
[0033] 如图1和图2所示，在换热腔一 24的底部处设有排污管28，排污管28的外端伸出至炉体一 2的侧壁。
[0034] 本实施例中，发生器的燃烧过程为:生物质燃料在送料结构的作用下进入到进料口 22内，对其进行点火，生物质燃料在燃烧室21内燃烧，烟尘随着出烟管一 23进入到进烟管32内，随后烟尘进入到换热室31内，最后经出烟管二 33排出，烟尘在本发生器内停留的时间较长，所以，与水的热交换时间也越长。
[0035] 发生器的热交换过程为:冷水首先从进水口二 35进入到换热腔二 34内，吸收换热室31内烟气的热量，水温升高；水温升高的水经出水口 36流入到换热腔一 24内，吸收燃烧室21内烟尘的热量，水温再次升高，部分水变为水蒸气，从出汽口 27排出，供人们使用。
[0036] 本生物质蒸汽发生器采用换热管增大热交换面积，提高热量转化率；在炉体一 2的上部设有安全阀5，当换热腔一 24内的压力大于设定压力时，安全阀5打开，自动化程度高，避免主体内压力过高，有效降低主体爆炸的概率，提高了本蒸汽发生器的安全性；还设置有炉体二 3，在炉体二 3内设有换热腔二 34，对烟气进行余热回收，提高了对生物质燃料燃烧的利用率，有效节约资源。
[0037] 本文中所描述的具体实施例仅仅是对本实用新型精神作举例说明。本实用新型所属技术领域的技术人员可以对描述的具体实施例做各种各样的修改或补充或采用类似的方式替代，但并不会偏离本实用新型的精神或者超越所附权利要求书定义的范围。
Claims (7)
1.一种生物质蒸汽发生器，包括底座(I )、设于底座(I)上方的其内部具有燃烧室(21)的炉体一(2 )和其内部具有换热室(31)的炉体二( 3 )，所述炉体一(2 )的下侧部具有其内端与燃烧室(21)连通的进料口(22)，所述炉体一(2)的顶部具有伸出至炉体一(2)的出烟管一(23)，所述炉体二(3)的侧部具有其内端与换热室(31)连通的进烟管(32)，所述的进烟管(32)与上述的出烟管一(23)连通，所述炉体二(3)的顶部设有出烟管二(33)，其特征在于，所述的燃烧室(21)与炉体一(2)之间形成用于蓄水的换热腔一(24)，所述炉体一(2)的上侧部设有与该换热腔一(24)连通的水位计(25)，所述的炉体一(2)上还设有与换热腔一(24 )连通的进水口一(26)和出汽口(27);所述的换热室(31)与炉体二( 3 )之间形成用于蓄水的换热腔二(34)，所述的炉体二(3)上还设有与该换热腔二(34)连通的进水口二(35)和出水口(36)，所述的出水口(36)与上述的进水口一(26)连通。
2.根据权利要求1所述的一种生物质蒸汽发生器，其特征在于，所述的燃烧室(21)上穿设有若干均匀分布的换热管(27)，所述换热管(27)的两端分别与上述的换热腔一(24)连通，所述的若干换热管(27)倾斜设置。
3.根据权利要求1或2所述的一种生物质蒸汽发生器，其特征在于，所述炉体一(2)的顶部设有用于测量换热腔一(24)内压力的压力表(4)，所述炉体一(2)的顶部还设有安全阀(5)。
4.根据权利要求1或2所述的一种生物质蒸汽发生器，其特征在于，所述炉体二(3)的上侧部还具有与换热腔二(34)连通的溢水口(37)，所述的进水口二(35)位于出水口(36)的上方。
5.根据权利要求1或2所述的一种生物质蒸汽发生器，其特征在于，所述的炉体二(3)上设有托架(6)，所述的托架(6)上设有一净水器(7)，所述净水器(7)的下部具有一水泵(8),所述的水泵(8)设于底座(I)上。
6.根据权利要求4所述的一种生物质蒸汽发生器，其特征在于，所述换热室(31)的下部具有一呈倒锥形的除尘器(38)，所述除尘器(38)的下部具有一集灰腔，所述集灰腔的侧壁具有一其外端伸出至炉体二(3)的清灰口(39)。
7.根据权利要求1或2所述的一种生物质蒸汽发生器，其特征在于，所述换热腔一(24)的底部处设有排污管(28)，所述排污管(28)的外端伸出至炉体一(2)的侧壁。
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