CN2238253Y - Organic refuse energy sources multifunctional reacting furnace - Google Patents
Organic refuse energy sources multifunctional reacting furnace Download PDFInfo
- Publication number
- CN2238253Y CN2238253Y CN 95222490 CN95222490U CN2238253Y CN 2238253 Y CN2238253 Y CN 2238253Y CN 95222490 CN95222490 CN 95222490 CN 95222490 U CN95222490 U CN 95222490U CN 2238253 Y CN2238253 Y CN 2238253Y
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- China
- Prior art keywords
- heater
- chamber
- gas
- reaction chamber
- fractionation
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- 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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- 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
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/16—Combined cycle power plant [CCPP], or combined cycle gas turbine [CCGT]
- Y02E20/18—Integrated gasification combined cycle [IGCC], e.g. combined with carbon capture and storage [CCS]
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- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
The utility model relates to an organic refuse energy sources multifunctional reacting furnace, belonging to the biomass energy changing technology. The utility model is characterized in that a furnace chamber is provided with two or three waste plastics liquefying and gasifying reaction chambers which are communicated with hydrocarbon oil decomposing and fractionating reaction chambers arranged on a pipe passage and both sides of the furnace chamber. The organic refuse flame and the high-temperature fume are circulating around the furnace chamber and the reaction chambers, a large amount of biomass coal-gas is generated and the waste plastic in the reaction chambers is heated. Vapor, coal, and diesel oil are fractionate through temperature control, and the use heat is used to boil the dogging socket water for heating, distilling, drinking, bathing, etc. The utility model can save energy, reduce pollution, and reduce cost because the reacting furnace uses organic refuse as fuel to produce coal gas and heat source, and uses waste plastic as raw material to produce fuel oil.
Description
It is fuel with organic waste that the utility model relates to a kind of, is the Reaktionsofen of the raw material sources renewable energy resources with the plastic waste.
At present, the use of plastics is more and more general in daily life, face is in industrial and agricultural production, production factors have been become such as plastics film, packing bag, container, tubing, sheet material etc., the consequent is that various waste plastics are everywhere, and plastics can not natural degradation at occurring in nature, thereby environment is caused great harm.And other organic waste in the life is especially than all being.China very payes attention to the energy of this organic waste, a lot of units have developed the equipment of waste plastics recycling oil fuel, this equipment generally heats with coal decomposes plastic waste, imports in the other separation column decomposing gas, makes it to decompose to obtain various oil fuel.This equipment energy consumption is big, the production cost height, and structure is not compact, the cost height, and purposes is single.
The purpose of this utility model provides a kind of organic waste energy polyfunctional reactant stove, it is two or three plastic waste liquefaction gasification reactor chambers of ad hoc meter in the organic waste Reaktionsofen, stove both sides two hydrocarbon ils of design decompose the fractionation chamber, by fill other the various organic waste blast roastings except that plastic waste in stove, the heat release that produces flammable biomass coal gas process comes the pyrolysis plastic waste to refine out premium, diesel oil; And then fully utilize its waste heat, and by hot pipe technique, make the boiling of water of water jacket, realize the function of warming oneself, distilling, drink, wash, taking a shower.
At above-mentioned problem, the technical scheme that the utility model adopted is: by body of heater, and fire grate, the furnace bottom (ash output hole bottom) of the Reaktionsofen that the chimney that can shut is formed has blast orifice, the lower furnace portion wall has air vapor homogenizing plate, makes the gas uniform distribution that blasts.Chimney is only opened when some stove, promptly shuts after stove is lighted.Bottom of furnace body has ash output hole and manhole (access opening), in burner hearth, be provided with two or three plastic waste liquefaction, gasification reactor chamber, each reaction chamber leads to outside the body of heater with pipeline, loading hopper is being set above the pipeline, the thick pushing ram of spiral material is arranged in the pipeline, reaction chamber top has a gas eduction tube road to lead to outside the body of heater, two sides of body of heater respectively have a hydrocarbon ils to decompose fractionation reaction chamber and gas cleaning dry distillation liquid collector, and be connected with burner hearth respectively, decomposing the fractionation reaction chamber is made up of three parts, a part is that hydrocarbon ils decomposes the fractionation reaction chamber in the middle, and a part is smoke chambers in the reaction chamber both sides, and a part is a water jacket at the smoke chamber outer wall.Hydrocarbon ils decomposes the derivation pipeline that there is the fuel oil gas of a gas introduction tube road and fractionation gained fractionation reaction chamber top, from the gas that comes out of liquefaction gasification reactor chamber, decompose fractionation in gas introduction tube importing decomposition fractionation chamber, resulting fuel oil gas is derived from deriving pipeline.Hydrocarbon ils decomposes in the fractionation reaction chamber has temperature regulator to carry out vapour, coal, diesel oil fractionation.The top of body of heater has organic waste and adds bucket, and a spiral material pushing ram is installed, organic waste burn in burner hearth and produce heat and flue gas, be blown into smoke chamber by gas blower by the flue that can regulate size, for decomposing the fractionation chamber, hydrocarbon ils provides heat, and control and decompose the fractionation chambers temp by regulating flue, through the flue gas of heat exchange from smoke chamber through filter screen around to the dividing plate opposite side, under be advanced in the gas cleaning dry distillation liquid collector, behind water washing cleaning, enter burner hearth, so move in circles, carbonic acid gas in the flue gas fully is reduced into inflammable gass such as carbon monoxide and draws with after further handle the air inlet cabinet from the coal gas interlayer, is used for industrial and agricultural production and domestic energy.The plastic waste established in burner hearth liquefaction gasification reactor chamber both can have been established one and also can establish two, three or a plurality of, can look the different sorts of organic waste to be processed and was provided with.Like this, in a liquefaction gasification reactor chamber, carry out the liquefaction gasification reaction of waste material; Can add oil in gasification reactor chamber or glue plant carries out destructive distillation in another liquefaction, thereby make very high wooden oil of economic worth or collose etc., can also obtain high grade activated carbon simultaneously.Can also add hard fruit shell, fruit stone such as Semen Crataegi etc. in the gasification reactor chamber the 3rd liquefaction and make it pyrolysis and extract hawthorn and heat up in a steamer the wet goods precious material, and obtain gac.Can also further extract sylvite from the ashes.
Owing to adopted technique scheme, make that this kind organic waste energy polyfunctional reactant stove can be fuel with organic waste, not only reduced production cost, but also can make the organic matter rubbish pyrolysis obtain coal gas etc. to industrial and agricultural production and the useful material of people's lives, this furnace structure compactness simultaneously, the little effect of body is high, and the material-saving valency is low.Not only can be used for waste plastics recycling fuel, but also can utilize hard fruit shell, fruit stone the like waste to produce gac and other precious material, and produce rosin collose and gac etc. with root, stem, the leaf of plants such as oil or glue plant such as pine tree, peach, apricot; Really accomplished multi-use, turned waste into wealth.
Fig. 1 is the front view of organic rubbish utmost point energy polyfunctional reactant stove;
Fig. 2 is the left view of organic waste energy polyfunctional reactant stove;
Fig. 3 is the vertical view of organic waste energy polyfunctional reactant stove.
Below in conjunction with accompanying drawing the utility model being done one describes in detail: organic waste energy polyfunctional reactant stove as shown in Figure 1, form by body of heater 1, fire grate 2, the chimney 27 that can shut, furnace bottom ash output hole below has blast orifice, the air that blasts makes gas distribution even through air vapor homogenizing plate 20.Ash output hole 3 and manhole (access opening) 28 are arranged at the body of heater bottom, in burner hearth 7, be provided with plastic waste liquefaction, gasification reactor chamber 5, reaction chamber leads to outside the body of heater with pipeline 19, be provided with loading hopper 8 above the pipeline, spiral material pushing ram 15 is arranged in the pipeline, the reaction chamber bottom is provided with agitator 16, liquefaction gasification reactor chamber top has a gas eduction tube road 14 to lead to outside the body of heater, two sides of body of heater respectively have a hydrocarbon ils to decompose fractionation reaction chamber 11 and gas cleaning dry distillation liquid collector 17, decomposing fractionation reaction indoor section three parts forms, a part is that hydrocarbon ils decomposes fractionation reaction chamber 24 between just, a part is smoke chambers 23 in the reaction chamber both sides, a part is a water jacket 22 at the smoke chamber outer wall, purify destructive distillation collector 17, the gas that comes out from gas eduction tube road 14 is through filter dirt, after the condensation, enter into decomposition fractionation chamber 24 by gas introduction tube 10, the top of decomposing the fractionation chamber has oil fuel gas delivery line 12, decompose in the fractionation reaction chamber temperature regulator 9 is arranged, have organic waste on the top of body of heater and add bucket 13, send in the burner hearth 7 by the spiral material pushing ram, organic waste burn in burner hearth and produce flue gas and a large amount of heat, be blown in the smoke chamber 23 by the flue 4 that can regulate size by gas blower, up through filter screen 25, decomposing fractionation chamber 24 to hydrocarbon ils in this process provides heat and heating water jacket 22, and this water can be used for washing plastic waste or heating etc.Regulate decomposition fractionation chamber 24 temperature by the size of regulating flue, walking around dividing plate 18 through the later flue gas of heat exchange enters in the gas cleaning dry distillation liquid collector 17, in the gas cleaning dry distillation liquid collector water is housed, the carbon dioxide gas that flue gas is had dry distillation liquid in one's care after through water washing cleaning returns in the burner hearth 7 through managing 6, so move in circles, carbonic acid gas in the flue gas can fully be reduced into carbon monoxide and hydrogen, after 26 derivation of interlayer 21 upper end gas export controls, make industrial and agricultural production, life fuel usefulness.
Be provided with burner hearth 7 interior three reaction chambers 5, both can be used for the waste plastics recycling fuel oil, also can do xyloid carbonizations such as hard fruit shell, fruit stone and produce gac and other valuable oily substance, perhaps oil, glue plant are extracted wooden oil, collose and gac.
How much are pyrogenous as required substance classes and quantity, and the liquefaction gasification reactor chamber that is arranged in the burner hearth can be one or more.
Claims (3)
1. organic waste energy polyfunctional reactant stove, by body of heater 1, fire grate 2, the chimney 27 that can shut is formed, bottom of furnace body has blast orifice, the lower furnace portion wall has air vapor homogenizing plate 20, ash output hole 3 and manhole 28 are arranged at the bottom of body of heater, in burner hearth 7, also has plastic waste liquefaction gasification reactor chamber 5, reaction chamber leads to outside the body of heater with extra heavy pipe road 19, loading hopper 8 is being set above the pipeline, spiral material pushing ram 15 is arranged in the pipeline, the reaction chamber bottom is provided with agitator 16, liquefaction gasification reactor chamber top has a gas eduction tube 14 to lead to outside the body of heater, two sides of body of heater respectively have a hydrocarbon ils to decompose fractionation reaction chamber 11 and gas cleaning dry distillation liquid collector 17, decomposing the inside of fractionation reaction chamber is made up of three parts: a part promptly is that middle portion is that hydrocarbon ils decomposes fractionation reaction chamber 24, and a part is that the reaction chamber both sides are smoke chambers 23, and another part is that the smoke chamber outer wall is a water jacket 22.Filter screen 25 and dividing plate 18 are arranged in the smoke chamber 23, gas introduction tube 10 and fuel oil gas delivery line 12 are arranged at the top of decomposing the fractionation chamber, temperature regulator 9 is installed in and decomposes in the fractionation reaction chamber, the top of body of heater has organic waste and adds bucket 13, and the spiral material pushing ram is installed, coal gas interlayer 21 is arranged in the burner hearth, and there is gas export control 26 on the top on the interlayer.
2. organic waste energy polyfunctional reactant stove according to claim 1 is characterized in that: the liquefaction, the gasification reactor chamber 5 that are provided with in the burner hearth 7 have two, and lead to outside the body of heater with pipeline 19 respectively.
3. organic waste energy polyfunctional reactant stove according to claim 1 is characterized in that: the liquefaction, the gasification reactor chamber 5 that are provided with in the burner hearth 7 have three, and lead to outside the body of heater with pipeline 19 respectively.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 95222490 CN2238253Y (en) | 1995-09-29 | 1995-09-29 | Organic refuse energy sources multifunctional reacting furnace |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 95222490 CN2238253Y (en) | 1995-09-29 | 1995-09-29 | Organic refuse energy sources multifunctional reacting furnace |
Publications (1)
Publication Number | Publication Date |
---|---|
CN2238253Y true CN2238253Y (en) | 1996-10-23 |
Family
ID=33869798
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN 95222490 Expired - Fee Related CN2238253Y (en) | 1995-09-29 | 1995-09-29 | Organic refuse energy sources multifunctional reacting furnace |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN2238253Y (en) |
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1995
- 1995-09-29 CN CN 95222490 patent/CN2238253Y/en not_active Expired - Fee Related
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C19 | Lapse of patent right due to non-payment of the annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |