CN104130805A - Biomass gas purifying cabinet - Google Patents
Biomass gas purifying cabinet Download PDFInfo
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- CN104130805A CN104130805A CN201410308276.6A CN201410308276A CN104130805A CN 104130805 A CN104130805 A CN 104130805A CN 201410308276 A CN201410308276 A CN 201410308276A CN 104130805 A CN104130805 A CN 104130805A
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- Prior art keywords
- dividing plate
- cabinet
- inlet pipe
- pipe
- type washing
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Abstract
A biomass gas purifying cabinet comprises a cabinet body; the upper part of the cabinet body is provided with a gas outlet, and the bottom of the cabinet body is provided with a water outlet; the cabinet body is inside successively provided with a water inlet pipe, a labyrinth-type water washing chamber and a gas inlet pipe from top to bottom; and the pipe orifice of the gas inlet pipe is lower than the liquid level at the lower part in the cabinet body. According to the cabinet, tar is pre-removed through a water body, and the gas inlet speed is adjusted by matching with the efficiency of removing tar through subsequent labyrinth-type water washing, so that maximum optimum removal rate of quantitative biomass gas is realized.
Description
Technical field
The present invention relates to a kind of purifying tank, is a kind of purifying tank for decontamination of biological matter gas specifically.
Background technology
The features such as it is abundant, cheap, renewable, clean that biomass energy has, along with holding of in December, 2009 Copenhagen, Denmark Global climate change meeting, on the earth, the mineral substance energy consumes rapidly, demand is growing, distribute a large amount of CO in finiteness and use thereof
2, SO
2, NO
xdeng gas and the environmental problem such as the atmospheric aerosol causing, acid rain, Global warming, depletion of the ozone layer causes the thinking of people's profound level again, the exploitation of biomass energy causes again people's extensive concern with application, and gasifying biomass is a kind of conventional biomass energy switch technology, coal-tar middle oil in gasification is inevitable by product.At high temperature can there is cracking in tar, be gaseous phase together with gasification gas, but lower than 200 DEG C in the situation that, just start to be condensed into liquid, become the sticky oily matter of black, affect that equipment for gasification is stable, safe operation, cause energy wastage, reduce gasification efficiency; And polynuclear aromatic family in tar ingredients is purifying and environment and human health are formed to serious harm when burning.Taking suitable treatment process to gasification gas is coal-tar middle oil, reduce the component of tar in gasification gas, improve gasification makings amount, is an important subject of biomass gasification technology.
The purification of biological fuel gas there are at present the physical methods such as the chemical process such as thermo-cracking, catalytic pyrolysis and filtration both at home and abroad, wet filter method is that WATER-WASHING METHOD is that water is taken away the part tar in combustible gas, because it is easy to operate, cost is low, is therefore widely used.As disclosed spray chamber in 201010215797.9 of applicant's earlier application, adopt enterprising gas port air inlet, in multilayer labyrinth type washing chamber, cross water and clean, remove the tar containing in biogas.But the biogas that burning produces directly cleans by cascade, even if extended gas circuit footpath by labyrinth type, but it is still very fast in the time constantly supplying gas purification, to cross gas speed, and cleaning performance is poor.
Summary of the invention
After producing for biogas in prior art, directly by the deficiency of water washing cleaning, the invention provides one simple in structure, can effectively take into account the biogas purifying tank of the rate of supplying gas and tar clearance.
The technical solution used in the present invention is: a kind of biogas purifying tank, comprise cabinet, described cabinet top is provided with air outlet, and bottom of cabinet bulk is provided with water outlet, in cabinet, be provided with successively water inlet pipe, labyrinth type washing chamber and inlet pipe from top to bottom, the mouth of pipe of inlet pipe is lower than bottom liquid level in cabinet.
Further, the mouth of pipe of described inlet pipe is inverted cone shape, and the inverted cone shape mouth of pipe down.
Further, described labyrinth type washing chamber is made up of an above side dividing plate and an above upper and lower alternate intervals of central dividing plate, side dividing plate is connected on cabinet sidewall and air passing hole is left in centre, central dividing plate is arranged between cabinet center and cabinet sidewall and left gas gap, and labyrinth type washing chamber orlop dividing plate is side dividing plate.
Further, between the described inlet pipe inverted cone shape mouth of pipe and cabinet sidewall, leave the corresponding air inlet gap of crossing gas gap.
Further, side dividing plate and the central dividing plate of described labyrinth type washing chamber are provided with upper and lower interleaved water hole.
Again further, on the described labyrinth type washing side dividing plate of chamber and the edge of central dividing plate, be equipped with the water eliminator that exceeds its plane.
Adopt technique scheme, the invention has the beneficial effects as follows: the inverted cone shape mouth of pipe of inlet pipe passes in cabinet under liquid level down, by inlet pipe lead to into biogas first pass in water, remove part tar; Biogas is again by glowing upward through air inlet gap in water, by adjusting the middle air passing hole of the undermost side dividing plate in corresponding labyrinth type washing chamber, air inlet gap, control the washing efficiency that air inlet rate meets labyrinth type washing, guarantee quantitative biomass gas air inlet, cross air water and wash, to reach maximum, best tar clearance.
The present invention adopts and removes in advance tar by water body, coordinates the efficiency of follow-up corresponding labyrinth type washing tar removing to adjust air inlet, realizes the maximum of quantitative biomass gas, best clearance.
Brief description of the drawings
Fig. 1 is structural representation of the present invention.
In figure: cabinet 1, water inlet pipe 2, water outlet 3, inlet pipe 4, side dividing plate 5, air passing hole 6, central dividing plate 7, crosses gas gap 8, water hole 9, the inverted cone shape mouth of pipe 10, air inlet gap 11, air outlet 12, water eliminator 13.
Embodiment
Below in conjunction with drawings and Examples, the invention will be further described.
Shown in Fig. 1, a kind of biogas purifying tank comprises cabinet 1, water inlet pipe 2, water outlet 3, inlet pipe 4, side dividing plate 5, central dividing plate 7 and water hole 9.Cabinet 1 top is provided with air outlet 12, and cabinet 1 bottom is provided with water outlet 3, is provided with successively water inlet pipe 2, labyrinth type washing chamber and inlet pipe 4 in cabinet 1 from top to bottom, and the mouth of pipe of inlet pipe 4 is inverted cone shape, and the inverted cone shape mouth of pipe 10 is down and lower than the interior bottom of cabinet 1 liquid level, labyrinth type washing chamber is by an above side dividing plate 5 and an above central dividing plate 7, lower alternate intervals composition, side dividing plate 5 is connected on cabinet sidewall and air passing hole 6 is left in centre, central dividing plate 7 is arranged between cabinet center and cabinet sidewall and left gas gap 8, labyrinth type washing chamber orlop dividing plate is side dividing plate, side dividing plate and the central dividing plate of labyrinth type washing chamber are provided with upper and lower interleaved water hole 9, on the edge of side dividing plate and central dividing plate, be equipped with the water eliminator 13 that exceeds its plane, between the inlet pipe inverted cone shape mouth of pipe 10 and cabinet sidewall, leave the corresponding air inlet gap 11 of crossing gas gap.
Claims (6)
1. a biogas purifying tank, comprise cabinet, it is characterized in that: described cabinet top is provided with air outlet, and bottom of cabinet bulk is provided with water outlet, in cabinet, be provided with successively water inlet pipe, labyrinth type washing chamber and inlet pipe from top to bottom, the mouth of pipe of inlet pipe is lower than bottom liquid level in cabinet.
2. a kind of biogas purifying tank according to claim 1, is characterized in that: the mouth of pipe of described inlet pipe is inverted cone shape, and the inverted cone shape mouth of pipe down.
3. a kind of biogas purifying tank according to claim 2, it is characterized in that: described labyrinth type washing chamber is made up of an above side dividing plate and an above upper and lower alternate intervals of central dividing plate, side dividing plate is connected on cabinet sidewall and air passing hole is left in centre, central dividing plate is arranged between cabinet center and cabinet sidewall and left gas gap, and labyrinth type washing chamber orlop dividing plate is side dividing plate.
4. a kind of biogas purifying tank according to claim 3, is characterized in that: between the described inlet pipe inverted cone shape mouth of pipe and cabinet sidewall, leave the corresponding air inlet gap of crossing gas gap.
5. according to a kind of biogas purifying tank described in claim 3 or 4, it is characterized in that: side dividing plate and the central dividing plate of described labyrinth type washing chamber are provided with upper and lower interleaved water hole.
6. according to a kind of biogas purifying tank described in claim 3 or 4, it is characterized in that: on the described labyrinth type washing side dividing plate of chamber and the edge of central dividing plate, be equipped with the water eliminator that exceeds its plane.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201410308276.6A CN104130805A (en) | 2014-07-01 | 2014-07-01 | Biomass gas purifying cabinet |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN201410308276.6A CN104130805A (en) | 2014-07-01 | 2014-07-01 | Biomass gas purifying cabinet |
Publications (1)
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CN104130805A true CN104130805A (en) | 2014-11-05 |
Family
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Family Applications (1)
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CN201410308276.6A Pending CN104130805A (en) | 2014-07-01 | 2014-07-01 | Biomass gas purifying cabinet |
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Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CA2324053A1 (en) * | 2000-10-20 | 2002-04-20 | Malahat Systems Corporation | Gasifier |
CN2829863Y (en) * | 2005-08-25 | 2006-10-25 | 张红胜 | Wet flue gas purifier |
CN101402882A (en) * | 2008-11-04 | 2009-04-08 | 中国科学院广州能源研究所 | Purification apparatus and method for biomass gas |
CN201704285U (en) * | 2010-07-02 | 2011-01-12 | 江苏云江生物能源科技有限公司 | Biomass gasification device |
CN203002202U (en) * | 2012-12-26 | 2013-06-19 | 中冶长天国际工程有限责任公司 | Acid mist absorbing device for hydrochloric acid container |
CN204079927U (en) * | 2014-07-01 | 2015-01-07 | 江苏金江生物能源科技有限公司 | A kind of biogas purifying tank |
-
2014
- 2014-07-01 CN CN201410308276.6A patent/CN104130805A/en active Pending
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CA2324053A1 (en) * | 2000-10-20 | 2002-04-20 | Malahat Systems Corporation | Gasifier |
CN2829863Y (en) * | 2005-08-25 | 2006-10-25 | 张红胜 | Wet flue gas purifier |
CN101402882A (en) * | 2008-11-04 | 2009-04-08 | 中国科学院广州能源研究所 | Purification apparatus and method for biomass gas |
CN201704285U (en) * | 2010-07-02 | 2011-01-12 | 江苏云江生物能源科技有限公司 | Biomass gasification device |
CN203002202U (en) * | 2012-12-26 | 2013-06-19 | 中冶长天国际工程有限责任公司 | Acid mist absorbing device for hydrochloric acid container |
CN204079927U (en) * | 2014-07-01 | 2015-01-07 | 江苏金江生物能源科技有限公司 | A kind of biogas purifying tank |
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Application publication date: 20141105 |