CN202237594U - Tar separator for biomass generation furnace - Google Patents
Tar separator for biomass generation furnace Download PDFInfo
- Publication number
- CN202237594U CN202237594U CN201120321791XU CN201120321791U CN202237594U CN 202237594 U CN202237594 U CN 202237594U CN 201120321791X U CN201120321791X U CN 201120321791XU CN 201120321791 U CN201120321791 U CN 201120321791U CN 202237594 U CN202237594 U CN 202237594U
- Authority
- CN
- China
- Prior art keywords
- cylinder
- inner cylinder
- outer cylinder
- tar separator
- biomass
- 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
Links
- 239000002028 Biomass Substances 0.000 title claims abstract description 25
- 239000007788 liquid Substances 0.000 claims abstract description 14
- 238000002309 gasification Methods 0.000 claims abstract description 7
- 239000000203 mixture Substances 0.000 claims abstract description 6
- 238000009423 ventilation Methods 0.000 claims description 4
- 210000003437 trachea Anatomy 0.000 claims 1
- 238000005192 partition Methods 0.000 abstract description 14
- 238000000926 separation method Methods 0.000 abstract description 11
- 238000012423 maintenance Methods 0.000 abstract description 5
- 239000000428 dust Substances 0.000 abstract description 2
- 238000005265 energy consumption Methods 0.000 abstract description 2
- 230000000694 effects Effects 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 238000004891 communication Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 230000007812 deficiency Effects 0.000 description 1
- 230000003670 easy-to-clean Effects 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
Images
Landscapes
- Industrial Gases (AREA)
Abstract
本实用新型为一种生物质发生炉焦油分离器,包括外筒,外筒通过侧壁上设置的外筒进气口承接生物质汽化炉产生的油汽混合物,还包括位于外筒内部并与外筒同轴向的内筒,内筒与外筒仅通过设置在内筒侧壁上的内筒进气管连通,内筒的一个底面上设置有与外筒的外部连通的出气管,内筒的另一个底面上通过连接筒与出液口连接,出液口通往外筒的外部,本实用新型采用了简单的旋风分离除尘与隔板气体过滤器的组合结构,内部不设置滤网,提高了可靠性,减少了维修;气体经过过滤器的时候,阻力小,降低了能耗,保证了系统的正常工作;系统维护工作量小,仅仅需要定期将底部的焦油排出,能够与一般小型生物质发生器相匹配。
The utility model relates to a tar separator for a biomass generator, which includes an outer cylinder, which accepts the oil-vapor mixture produced by a biomass gasification furnace through an air inlet of the outer cylinder provided on the side wall, and also includes a The outer cylinder is coaxial with the inner cylinder, and the inner cylinder and the outer cylinder are only connected through the inner cylinder air inlet pipe arranged on the side wall of the inner cylinder, and one bottom surface of the inner cylinder is provided with an air outlet pipe communicating with the outside of the outer cylinder, and the inner cylinder The other bottom surface of the tank is connected to the liquid outlet through the connecting cylinder, and the liquid outlet leads to the outside of the outer cylinder. The utility model adopts a simple combination structure of cyclone separation dust removal and partition gas filter, and no filter screen is arranged inside. Improve reliability and reduce maintenance; when the gas passes through the filter, the resistance is small, which reduces energy consumption and ensures the normal operation of the system; the maintenance workload of the system is small, and only the tar at the bottom needs to be discharged regularly, which can be compared with ordinary small Biomass generators to match.
Description
技术领域 technical field
本实用新型属于气液粗分离领域,涉及生物质汽化炉产生的水汽与焦油的分离器械,特别涉及一种生物质发生炉焦油分离器。The utility model belongs to the field of coarse gas-liquid separation, and relates to a device for separating water vapor and tar produced by a biomass gasification furnace, in particular to a tar separator for a biomass generator.
背景技术 Background technique
现有的生物质发生炉焦油分离器一般采用一级分离,如果仅仅采用旋风分离,分离效果不是很好,同时,设备的体积很大。如果采用金属滤网进行分离,滤网由于粘接焦油,很容易堵塞。The existing biomass generator tar separator generally adopts one-stage separation. If only cyclone separation is used, the separation effect is not very good, and at the same time, the volume of the equipment is large. If a metal filter is used for separation, the filter is easily blocked due to bonding tar.
实用新型内容 Utility model content
为了克服上述现有技术的不足,本实用新型的目的在于提供一种生物质发生炉焦油分离器,能将生物质汽化炉产生的水汽、焦油有效分离,同时又同时避免了堵塞现象,不需要进行清洗,能够长期使用而不进行维护。In order to overcome the deficiencies of the above-mentioned prior art, the purpose of this utility model is to provide a kind of biomass generator tar separator, which can effectively separate the water vapor and tar produced by the biomass gasification furnace, and at the same time avoid the clogging phenomenon. It is easy to clean and can be used for a long time without maintenance.
为了实现上述目的,本实用新型采用的技术方案是:In order to achieve the above object, the technical solution adopted by the utility model is:
一种生物质发生炉焦油分离器,包括外筒4,外筒4通过侧壁上设置的外筒进气口8承接生物质汽化炉产生的油汽混合物,还包括位于外筒4内部并与外筒4同轴向的内筒3,内筒3与外筒4通过设置在内筒3在侧壁上的内筒进气管5连通,内筒3的一个底面上设置有与外筒4的外部连通的出气管1,内筒3的另一个底面上通过连接筒6与出液口7连接,出液口7通往外筒4的外部。A biomass generator tar separator, comprising an
其中,所述外筒进气口8沿外筒4截面的切向与外筒4连接。Wherein, the
为进一步提高分离效果,所述内筒3中还设置隔板2,隔板2上设置有多个通气孔9,隔板2将内筒3分成两部分,内筒进气管5和出气管1分别位于隔板2的两边。In order to further improve the separation effect, a
所述隔板2的数量大于一个,平行间隔设置形成隔板组,内筒进气管5和出气管1分别位于隔板组的两边。The number of the
所述内筒3在与连接筒6连接的一端为锥形,连接筒6位于锥底位置,连接筒6通过其上的连通孔10与外筒4连通,外筒4在该端为锥形。The
内筒进气管5和出气管1的长度保证能伸入到内筒3中。The length of the inner cylinder
内筒进气管5位于内筒3侧壁上中间或中间偏下的位置。The inner cylinder
本实用新型与现有技术相比,具有以下优点:Compared with the prior art, the utility model has the following advantages:
1)采用了简单的旋风分离除尘与隔板气体过滤器的组合结构,内部不设置滤网,提高了可靠性,减少了维修。1) The combined structure of simple cyclone separation dust removal and clapboard gas filter is adopted, and there is no filter screen inside, which improves reliability and reduces maintenance.
2)气体经过过滤器的时候,阻力小,降低了能耗,保证了系统的正常工作。系统维护工作量小,仅仅需要定期将底部的焦油排出,是一般小型生物质发生器的的最佳匹配设备。2) When the gas passes through the filter, the resistance is small, which reduces energy consumption and ensures the normal operation of the system. The maintenance workload of the system is small, and only the tar at the bottom needs to be discharged regularly, which is the best matching equipment for general small biomass generators.
3)设备的投资低,便于推广。3) The equipment investment is low and easy to popularize.
附图说明 Description of drawings
图1为本实用新型结构示意图。Fig. 1 is the structural representation of the utility model.
图2为图1的俯视图。FIG. 2 is a top view of FIG. 1 .
图3为隔板结构示意图。Figure 3 is a schematic diagram of the partition structure.
具体实施方式 Detailed ways
下面结合附图和实施例对本实用新型做进一步详细说明。Below in conjunction with accompanying drawing and embodiment the utility model is described in further detail.
如图1和图2所示,本实用新型为一种生物质发生炉焦油分离器,包括外筒4,外筒4通过侧壁上设置的外筒进气口8承接生物质汽化炉产生的油汽混合物,外筒进气口8沿外筒4截面的切向与外筒4连接。还包括位于外筒4内部并与外筒4同轴向的内筒3,内筒3与外筒4仅通过设置在内筒3在侧壁上的内筒进气管5连通,内筒进气管5的长度保证能伸入到内筒3中。内筒3的一个底面上设置有与外筒4的外部连通的出气管1,出气管1的长度保证能伸入到内筒3中;内筒3的另一个端为锥形,锥底处设置有连接筒6,连接筒6与出液口7连接,出液口7通往外筒4的外部。在外筒4的内部,连接筒6通过其上的连通孔10与外筒4连通,以保证分离的焦油与水汽能够很好的流出,同样的,外筒4在该端为锥形。As shown in Figures 1 and 2, the utility model is a biomass generator tar separator, which includes an
其中,所述内筒3中还设置隔板2,隔板2的数量为任意多个,其上设置有多个通气孔9,隔板2为一个时,其将内筒3分成两部分,内筒进气管5和出气管1分别位于隔板2的两边,隔板2为多个时,平行间隔设置形成隔板组,内筒进气管5和出气管1分别位于隔板组的两边。Wherein, a
如图3所示,为隔板2的结构示意图,其与内筒3的纵切面形状一致,板上设置多个通气孔9。As shown in FIG. 3 , it is a schematic diagram of the structure of the
本实用新型的工作方式是:The mode of work of the present utility model is:
生物质汽化炉产生的油汽混合物从外筒进气口8进入到外筒4,进入的时候沿着外筒4的切向进入,形成一定的旋风效果,在旋风过程中,焦油与水汽在离心作用下,被甩到外筒4的内壁上,沿着内壁,在重力作用下流到底部中积液,形成一次气体-液体分离;其余混合物从内筒进气管5进入到内筒3中,由于进入具有一定的速度,直接冲击到隔板2上,液体被进一步分离,沿着内筒3的内壁流下,而气体则通过隔板2上的通气孔9流入到内筒3的另一部分,最终由出气管1排出。根据焦油分离器的体积,可以设置多个隔板,以达到良好的气液分离效果。不过,为了不增加气体的流动阻力,隔板2上设置的通气孔9的数量,以及最后的总体通流面积,要合理配置。The oil-vapor mixture produced by the biomass gasification furnace enters the
出气管1和内筒进气管5要有一定的长度,伸入到内筒3的筒体之内,以保证气体进入的时候,粘接在侧壁上的液体不通过管道流入到下一个腔室内,或者排出到洁净气体管道之中,内筒进气管5位于内筒3侧壁上中间或中间偏下的位置,更有利于分离。The
Claims (9)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201120321791XU CN202237594U (en) | 2011-08-30 | 2011-08-30 | Tar separator for biomass generation furnace |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201120321791XU CN202237594U (en) | 2011-08-30 | 2011-08-30 | Tar separator for biomass generation furnace |
Publications (1)
Publication Number | Publication Date |
---|---|
CN202237594U true CN202237594U (en) | 2012-05-30 |
Family
ID=46098899
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201120321791XU Expired - Fee Related CN202237594U (en) | 2011-08-30 | 2011-08-30 | Tar separator for biomass generation furnace |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN202237594U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102772955A (en) * | 2012-08-27 | 2012-11-14 | 北京雪迪龙科技股份有限公司 | Water-steam separator |
-
2011
- 2011-08-30 CN CN201120321791XU patent/CN202237594U/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102772955A (en) * | 2012-08-27 | 2012-11-14 | 北京雪迪龙科技股份有限公司 | Water-steam separator |
CN102772955B (en) * | 2012-08-27 | 2015-08-19 | 北京雪迪龙科技股份有限公司 | A kind of steam trap |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN202610203U (en) | Combined type rotational flow coalescer for offshore platform natural gas purification | |
CN206881174U (en) | A kind of detachable type high-efficiency gas-liquid separation device | |
CN202173849U (en) | Gas-liquid separator | |
CN102408922A (en) | Adopt whirl board vapour and liquid separator's gas clean system fountain saturator | |
CN202238348U (en) | A multi-tubular cyclone separator for natural gas purification | |
CN204380328U (en) | A kind of gas-liquid separator | |
CN202237594U (en) | Tar separator for biomass generation furnace | |
CN202751847U (en) | Gas-liquid separator | |
CN202341948U (en) | Air-dust separation device | |
CN203591665U (en) | Gas-liquid separation mechanism for spiral tube | |
CN104043302B (en) | Water filtration air purification device suitable for household | |
CN203235341U (en) | High-efficiency cyclone dust remover integrating gravity dust removal | |
CN104728894B (en) | Inertial separation and automatic collection lampblack purifying system | |
CN202277704U (en) | Underwater separator | |
CN210218119U (en) | High-efficiency steam-water separator | |
CN211435406U (en) | Gas-liquid cut-off equipment | |
CN202237566U (en) | Irrigation water filtering device | |
CN207838580U (en) | Smoke and dust purifier for being pyrolyzed desorption | |
CN203187675U (en) | Marsh gas tank with gas-liquid separator | |
CN203017879U (en) | Gas-water separator for tubular products | |
CN203091135U (en) | Cyclone hydraulic separator | |
CN205145871U (en) | Online demister | |
CN207539038U (en) | A kind of decompression muffling type vacuum water separator | |
CN201921596U (en) | Steam and water separating device | |
CN207462911U (en) | A kind of centrifugal dust collection device for food production |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C17 | Cessation of patent right | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20120530 Termination date: 20120830 |