CN201704260U - Biomass material pyrolysis furnace - Google Patents
Biomass material pyrolysis furnace Download PDFInfo
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- CN201704260U CN201704260U CN2010201694163U CN201020169416U CN201704260U CN 201704260 U CN201704260 U CN 201704260U CN 2010201694163 U CN2010201694163 U CN 2010201694163U CN 201020169416 U CN201020169416 U CN 201020169416U CN 201704260 U CN201704260 U CN 201704260U
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
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Abstract
The utility model relates to a biomass material pyrolysis furnace which comprises a furnace body; a feed opening is arranged at the upper part of the furnace body; a gas outlet is arranged on the top end of the furnace body; and the bottom end of the furnace body is provide with an electric heater. An anaerobic pyrolysis environment can simplify the structure of the pyrolysis furnace, so that only the electric heater can meet the energy needs of pyrolysis. Compared with the prior art, the process can prepare more natural gas and obtain more heat based on biomass material with the same mass, in particular to the agricultural and forestry waste.
Description
Technical field
The utility model relates to energy field, is specifically related to the employed pyrocrack furnace of biomass material thermo-cracking.
Background technology
Energy problem enjoys various countries to show great attention to as world today's difficult problem.The oil of China, coal, Sweet natural gas workable reserve per capita have only 11%, 55%, 4.3% of world average level; Lower by 40% than advanced international standard at aspects such as Energy efficiency, energy consumption of unit product, gap is fairly obvious.How on the basis of improving efficiency, realize that the optimization of energy structure has become the key that can China realize Sustainable development.For this reason, country encourages the development of renewable energy source energetically, has formulated " renewable energy source method " and a series of relevant policies and has been helped.At biomass energy, point out especially " make full use of biogas and agriculture and forestry organic waste material gasification technology and improve the combustion gas ratio of Rural areas life with energy, and the important measures of gasifying biomass cracking as solution countryside wastes and industrial organic waste environmental improvement ".
But the situation of utilizing of biomass material utilization, the especially countryside wastes of China allows of no optimist at present, and most of vapourizing furnace that uses is lighted countryside wastes and then gathered the inflammable gas that produces under aerobic state.The input gasification cost of this kind mode is generally lower, is direct burning mostly, though there is inflammable gas to produce, calorific value is lower, can not satisfy civilian and industrial requirement.
The biomass through pyrolysis technology then is to make biomass under the situation of basic no oxygen (isolated with air), by the thermochemistry conversion, generates the process of liquids and gases product.According to the difference of gas phase residence time, heat-up rate, top temperature, the proportion of composing of gas, oil, liquid is also different in the product.The method that prior biological pledge material thermo-cracking prepares Sweet natural gas mainly may further comprise the steps: material grinding----drying forming----thermo-cracking, wherein thermo-cracking is carried out in pyrocrack furnace, can obtain the product of gas-liquid two class forms after the thermo-cracking, gaseous product cooling back obtains biological fuel gas, burnt oil and vinegar liquid respectively by purification separation.
Above preparation method still can feed air in certain amount in thermal cracking processes, make material carry out heat scission reaction under a small amount of aerobic environment, oxygen exist in the efficient that has influence on thermo-cracking on certain program, thereby influence the release of calorific value.
The utility model content
The utility model is at above the deficiencies in the prior art, a kind of biomass material employed pyrocrack furnace in complete anaerobic thermal cracking processes is provided, comprises body of heater, opening for feed is located at upper of furnace body, the top of body of heater is located in the air outlet, and described body of heater bottom is provided with electric heater.
Paddle is established in described electric heater unit top, and described paddle connects the vertical power set of body of heater by agitator arm.
Described opening for feed place establishes hopper.
The utility model is suitable under a kind of situation of complete anaerobic biomass material being carried out the method for thermo-cracking, and this method has greatly improved thermo-cracking efficient, has greatly increased the release rate of calorific value.
This method is achieved through the following technical solutions:
The biomass material thermo-cracking prepares the method for Sweet natural gas, and described method comprises the steps:
(1) material is pulverized---and make material reach desired particle size by pulverizing;
(2) drying materials---make material water ratio 0～12% by oven dry;
(3) thermo-cracking---material enters thermal cracker and carry out thermo-cracking under anaerobic state, and the ceiling temperature of thermo-cracking is 400～1000 ℃, obtains the gaseous state resultant by thermo-cracking;
(4) refrigerated separation---gaseous state resultant obtains inflammable gas and liquid through after the refrigerated separation.
(5) compression separates---and inflammable gas obtains the Sweet natural gas that can directly utilize after overdraft separates.
The material water ratio of described step (2) is 0～7%.
Described step (3) is to carry out in evacuated pyrocrack furnace.
When temperature surpasses 200 ℃, the water vapour in the pyrocrack furnace is discharged in the described step (3).
Reaction principle of the present utility model is: biomass are through thermochemical treatment, and promptly biomass are under the condition of isolated or minor amounts of oxygen, and pyrolytic reaction obtains inflammable gas, solid charcoal and liquid bio oil three series products, claims biomass through pyrolysis (biomass pyrolytic) again.Biomass pyrolytic divides low temperature pyrolysis at a slow speed (＜400 ℃), and product is based on charcoal; In warm fast pyrogenation (400～650 ℃), product is based on bio oil; High-temperature flash pyrolysis (700～1000 ℃), product is based on inflammable gas.
The beneficial effects of the utility model are: the thermo-cracking environment that utilizes anaerobic, can simplify the structure of pyrocrack furnace, only use electric heater just to be enough to satisfy the energy requirement of thermo-cracking, compared with prior art based on the biomass material of equal in quality especially agriculture and forestry organic waste material, use this law can make more Sweet natural gas, obtain more calorific value.
The Sweet natural gas that makes by above method, by analysis report as can be known wherein hydrogen be 16.2%; Methane is 42.2%; Ethane is 31.6%; Propane is 0.4%; Carbonic acid gas is 9.3%; Propylene is 0.3% and the carbon monoxide that also comprises 2.0ppm.Above composition meets the content demand of Sweet natural gas fully, and the content of wherein inflammable gas methane, ethane and hydrogen is especially higher, so can produce more calorific values by the identical cubical Sweet natural gas of this law preparation.
Description of drawings
Fig. 1 is the structural representation of the utility model pyrocrack furnace;
Fig. 2 is the process flow sheet of the utility model institute usability methods;
Fig. 3 is the concrete implementing process figure of the utility model institute usability methods.
Among the figure: 1 is pyrocrack furnace; 2 is condenser; 3 is surge tank; 4 is low pressure compressor; 5 is low pressure storage tank; 6 is high pressure compressor; 7 is the water vapour exhaust-valve; 8 is liquid collection tank; 9 is reducing valve; 10 is body of heater; 11 is opening for feed; 12 is the air outlet; 13 is power set; 14 is stirring rod; 15 is paddle; 16 is electric heater; 17 is hopper.
Embodiment
Below in conjunction with the drawings and specific embodiments the utility model is described in further details.
As shown in Figure 1, the utility model provides a kind of biomass material employed pyrocrack furnace 1 in complete anaerobic thermal cracking processes, comprises body of heater 10, and body of heater 10 tops are provided with opening for feed 11, and hopper 17 is located on the opening for feed 11.Body of heater 10 tops are provided with air outlet 12, the bottom has added electric heater 16, and the power set 13 that the body of heater top is provided with has connected a paddle 15 by stirring rod 14, paddle 15 be located at electric heater 16 on be convenient to the material that adds in the pyrocrack furnace 1 is stirred, so that the material thermally equivalent, the efficient of raising thermo-cracking.
The utility model is suitable under a kind of situation of complete anaerobic biomass material being carried out the method for thermo-cracking, and this method has greatly improved thermo-cracking efficient, has greatly increased the release rate of calorific value.By illustrated in figures 1 and 2, the method that the biomass material thermo-cracking prepares Sweet natural gas comprises the steps:
(1) material is pulverized---and make material reach desired particle size by pulverizing,, then can use the bigger particle of screen cloth filtering to meet the requirements of size if pulverize the requirement that does not still reach size through for several times; But less and even as the size of fruit granule own, then need not to pulverize again, such as rice husk, sawdust etc.
(2) drying materials---make material water ratio 0～12% by oven dry, more excellent water content is 0～7%, can greatly reduce the water vapour that the thermo-cracking step is produced like this, not only help shortening the follow-up refrigerative time, also improve the purity of collected gas simultaneously.
(3) thermo-cracking---material enters evacuated pyrocrack furnace 1, carries out thermo-cracking under anaerobic state.Pyrocrack furnace 1 carries out scission reaction by the mode that progressively heats up, and when surpassing 200 ℃, the water vapour in the pyrocrack furnace is discharged by water vapour exhaust-valve 7, and finally make temperature remain on 400～1000 ℃, obtains the gaseous state resultant by thermo-cracking.Ceiling temperature is difference to some extent according to the difference of employed biomass material especially agriculture and forestry organic waste material, when reaching 500～600 ℃, can produce the gaseous state resultant as straw, just produces the gaseous state resultant when weedtree then reaches 900～1000 ℃.As shown in Figure 3, the needed origin of heat of thermo-cracking is in electric heater 16.
(4) the gaseous state resultant that is produced in refrigerated separation---the pyrocrack furnace 1 enters cooling system, what generally adopt is condenser 2, the gaseous state resultant can be told gas part and liquid portion after overcooling, gas partly is biological fuel gas, top output by condenser 2, liquid portion drains in the liquid collection tank 8 via the bottom of condenser 3, and purification separation can obtain burnt oil and vinegar liquid again.
(5) compression separates---and inflammable gas can carry out the secondary separation of gas via high pressure compressor 6.But aborning in order to guarantee the stability of collected gas, generally carry out the buffering of gas earlier via surge tank 3 by the gas of output in the condenser 2, greatly reduce the danger of inflammable gas, again by low pressure compressor 4 with gas storage in low pressure storage tank 5, during use gas via reducing valve 9 enter high pressure compressor 6 with inflammable gas according to different pressure: during 5MPa, liquefaction such as ethane are separated out; 7.5MPa the time, co 2 liquefaction is separated out; During 20MPa, methane and liquefaction of hydrogen are separated out, so just the Sweet natural gas that can obtain compressing.
The Sweet natural gas that makes by above method, by analysis report as can be known wherein hydrogen be 16.2%; Methane is 42.2%; Ethane is 31.6%; Propane is 0.4%; Carbonic acid gas is 9.3%; Propylene is 0.3% and the carbon monoxide that also comprises 2.0ppm.Above composition meets the content demand of Sweet natural gas fully, and the content of inflammable gas methane wherein and hydrogen is especially higher, so can produce more calorific values by the identical cubical Sweet natural gas of this law preparation.
The accessible biomass material of present method source is wide, be easy to get very much, especially agriculture and forestry organic waste material, comprise rice husk, Pericarppium arachidis hypogaeae, shell, cotton bar, soya bean stalk, sesame stalk, corn stalk, straw, corn ear, corn cob etc., utilize this method not only to obtain the very valuable energy, also solved the problem of the offal treatment difficulty in present vast rural area, kill two birds with one stone, both improved agriculture output, increased farmers' income, alleviated peasant's labour intensity, can reduce pollution again, promote ecological benign cycle.
The utility model utilizes the thermo-cracking environment of anaerobic, can simplify the structure of pyrocrack furnace, only use electric heater just to be enough to satisfy the energy requirement of thermo-cracking, compared with prior art based on the biomass material of equal in quality especially agriculture and forestry organic waste material, use this law can make more Sweet natural gas, obtain more calorific value.
Claims (3)
1. the biomass material pyrocrack furnace comprises body of heater, and opening for feed is located at upper of furnace body, and the top of body of heater is located in the air outlet, it is characterized in that described body of heater bottom is provided with electric heater.
2. pyrocrack furnace according to claim 1 is characterized in that establishing paddle above the described electric heater unit, and described paddle connects the vertical power set of body of heater by agitator arm.
3. pyrocrack furnace according to claim 1 is characterized in that described opening for feed place establishes hopper.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010201694163U CN201704260U (en) | 2010-04-23 | 2010-04-23 | Biomass material pyrolysis furnace |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010201694163U CN201704260U (en) | 2010-04-23 | 2010-04-23 | Biomass material pyrolysis furnace |
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| Publication Number | Publication Date |
|---|---|
| CN201704260U true CN201704260U (en) | 2011-01-12 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN2010201694163U Expired - Fee Related CN201704260U (en) | 2010-04-23 | 2010-04-23 | Biomass material pyrolysis furnace |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101805647A (en) * | 2010-04-23 | 2010-08-18 | 倪建辉 | Method for preparing natural gas by biomass material thermal cracking and thermal cracking furnace used by same |
| CN104099115A (en) * | 2014-07-24 | 2014-10-15 | 陕西鼓风机集团西安锅炉有限责任公司（西安特种汽车厂） | Destructive distillation testing device and destructive distillation method |
-
2010
- 2010-04-23 CN CN2010201694163U patent/CN201704260U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101805647A (en) * | 2010-04-23 | 2010-08-18 | 倪建辉 | Method for preparing natural gas by biomass material thermal cracking and thermal cracking furnace used by same |
| CN104099115A (en) * | 2014-07-24 | 2014-10-15 | 陕西鼓风机集团西安锅炉有限责任公司（西安特种汽车厂） | Destructive distillation testing device and destructive distillation method |
| CN104099115B (en) * | 2014-07-24 | 2016-05-11 | 陕西鼓风机集团西安锅炉有限责任公司（西安特种汽车厂） | A kind of retort experiment device and method for destructive distillation |
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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: 20110112 Termination date: 20140423 |