CN105567372A - Preparation method of biomass fuel taking medicine residues as raw materials - Google Patents
Preparation method of biomass fuel taking medicine residues as raw materials Download PDFInfo
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- CN105567372A CN105567372A CN201510966565.XA CN201510966565A CN105567372A CN 105567372 A CN105567372 A CN 105567372A CN 201510966565 A CN201510966565 A CN 201510966565A CN 105567372 A CN105567372 A CN 105567372A
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L5/00—Solid fuels
- C10L5/40—Solid fuels essentially based on materials of non-mineral origin
- C10L5/44—Solid fuels essentially based on materials of non-mineral origin on vegetable substances
- C10L5/445—Agricultural waste, e.g. corn crops, grass clippings, nut shells or oil pressing residues
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L5/00—Solid fuels
- C10L5/40—Solid fuels essentially based on materials of non-mineral origin
- C10L5/44—Solid fuels essentially based on materials of non-mineral origin on vegetable substances
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
- C10L2290/24—Mixing, stirring of fuel components
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
- C10L2290/30—Pressing, compressing or compacting
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
- C10L2290/32—Molding or moulds
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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
-
- 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
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
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- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Solid Fuels And Fuel-Associated Substances (AREA)
- Life Sciences & Earth Sciences (AREA)
- Agronomy & Crop Science (AREA)
Abstract
The invention provides a preparation method of biomass fuel taking medicine residues as raw materials and relates to the technical field of Chinese medicine residue treatment. The preparation method includes the following steps: smashing herbal medicine residues in the medicine residues into herb powder 0.5-5mm in particle size; cutting woody medicine residues and straw in the medicine residues into small sections 10-30mm in length to obtain woody particles; uniformly mixing the herb powder and the woody particles prior to compressing into particles. Since the herbal medicine residues and the woody medicine residues are respectively crushed, and fibers of the straw and the woody medicine residues are destroyed to allow the straw and the woody medicine residues to be easy to burn. Under the action of high temperature, part of combustible fibers in the woody medicine residues and the straw are carbonized in a biomass granulator to form a framework of the biomass fuel, the herbal medicine residues can closely fill fiber clearances of the woody medicine residues, the burning value is heightened, biomass combustion particles can be burnt fully, and smoke produced by straw burning or medicine residue burning is avoided.
Description
Technical field
The present invention relates to Chinese medicine slag processing technology field, being specifically related to a kind of take the dregs of a decoction as the preparation method of the biomass fuel of raw material.
Background technology
In recent years, along with people pursue coming from natural commodity, the continuous progress of multiple isolation technique, purification techniques, the development and utilization of natural resources of Chinese medicinal materials enters the fast-developing phase, Chinese herbal medicine industry annual value of production with annual more than 20% speed development.Constantly there is emerging traditional Chinese medicine enterprise to occur, also constantly have well-established business such as Yangtze River group, Kang Yuan medicine company etc. to expand the scale of production.Chinese herbal medicine industry develops rapidly, creates huge economic benefit.But the dregs of a decoction produced after a large amount of Chinese medicinal material extracts bring urgent need to solve the problem to manufacturer, society, environment.Chinese medicine dreg is generally wet stock, very easily addles, and its taste is smelly different, easily produces waste water, grows germ.For avoiding the impact caused GMP production plant, should speed away after the dregs of a decoction generation plant area, and process rapidly, avoids its pollution on the environment.
The methods such as traditional Chinese medicine Slag treatment mode is mainly stacked, landfill, burning, landfill and stacking need a large amount of land resources and human and material resources, can impact environment simultaneously; The wet dregs of a decoction are high due to water content, burn and more need to waste a large amount of fossil energies; Above treatment process or cause the pollution of environment or cause a large amount of wastes of resource, all can not meet the requirement of environmental protection production, cleaner production, also be difficult to 12 planning of implementing " energy-saving and emission-reduction ".
In addition, the peasant of annual all parts of the country can burn a large amount of stalk, although Duo Di government strengthens management, but most peasants still adopts the mode Treating straw of burning, creates a large amount of smog, causes air On The Deterioration of Visibility Over, visual range reduces, directly affect the normal operation of civil aviaton, railway, motorway, easily cause traffic accident, affect personnel safety.Crop straw burning is also one of the arch-criminal of autumn and winter season haze, can be efficient, and economic Treating straw is also one of each department problem demanding prompt solution.
Summary of the invention
The object of this invention is to provide a kind of take the dregs of a decoction as the preparation method of the biomass fuel of raw material, take up room little, energy consumption is low, environmentally safe, the biomass fuel combustion value of acquisition is higher, and dense smoke significantly reduces.
Object of the present invention adopts following technical scheme to realize.
Take the dregs of a decoction as a preparation method for the biomass fuel of raw material, comprise the steps: the draft dregs of a decoction in the dregs of a decoction to be crushed to the draft powder that particle diameter is 0.5 ~ 5mm; The woody dregs of a decoction and stalk are cut to the segment that length is 10-30mm, obtain woody particle; Draft powder and woody particle are mixed, are compressed into particulate state.
In the present invention, the described dregs of a decoction are dregs of a decoction of generation in MAILUONING ZHUSHEYE, three stubborn sheets, the blue oral liquid in Pu ground, cassia twig and poria cocos soft capsule, Baihu Tang production; Stalk is maize straw, cotton stalk, wheat stalk; The mass ratio of the described dregs of a decoction and stalk is 10:1-15.
In preferred technical scheme, the water ratio of the described dregs of a decoction is 20-35%, and the water ratio of described stalk is 10-20%.
In preferred technical scheme, add lubricant after described draft powder and the mixing of woody particle, then make particulate state; Described lubricant is water, adds 20 ~ 40ml water in every kilogram of dregs of a decoction and stalk mixture.
In the present invention, the particle diameter of described biomass fuel is 5-100mm.
In the present invention, winnowing machine is adopted to be separated with the woody dregs of a decoction by the draft dregs of a decoction in the dregs of a decoction.
In the present invention, described draft powder and woody particle mix in mixing machine, be sent in biomass granulator, make particulate state by worm conveyor, are provided with feeding lubricating device at described worm conveyor entrance end place.
In preferred technical scheme, the granulation conditions of described biomass granulator: compression temperature 220 DEG C ~ 280 DEG C, compression pressure 25Mpa ~ 40Mpa.
In preferred technical scheme, described mixing machine is connected with sack cleaner, the dust collected in described sack cleaner by Cemented filling to worm conveyor entrance end place.
In the present invention, water ratio refers to the ratio of quality moisture in the dregs of a decoction or stalk and the dregs of a decoction or stalk total mass, represents with percentage ratio.
Beneficial effect: the present invention is broken by the draft dregs of a decoction and the woody dregs of a decoction, stalk being carried out difference, make dregs of a decoction distributed components, reduce the dregs of a decoction and pile up volume, reduce the volume of subsequent processing device, change the dregs of a decoction and stalk basic characteristic, for subsequent disposal lays the foundation; Utilize the moisture of not drying in the dregs of a decoction as the tackiness agent of preparation particulate biomass burning, walk around this link of dehydration, not only save energy, and the remaining water of Appropriate application.The dregs of a decoction are processed into biomass fuel eventually through biomass granulator.Due to through difference pulverization process, destroy the fiber of stalk and the woody dregs of a decoction, make it be easy to burning.In biomass granulator under high temperature action; in the woody dregs of a decoction, stalk, part combustible fibre produces the skeleton that charing forms biomass fuel; the draft dregs of a decoction can fill out the fibre gap at the woody dregs of a decoction closely; not only increase fuel value; can allow biomass combustion particle Thorough combustion simultaneously, avoid crop straw burning or burn the smog that the dregs of a decoction produce.The total system of dregs of a decoction compatibility straw biomass fuel of the present invention has that output is high, energy consumption is low, non-secondary pollution, fuel value high, avoid traditional dregs of a decoction, improve the utility value of the draft dregs of a decoction and stalk while environmental pollution that stalk traditional treatment method causes, as promoted, the social concern of crop straw burning atmosphere pollution also can be solved to a certain extent.
Accompanying drawing explanation
Fig. 1 is the device preparing biomass fuel, wherein 1-baking oven, 2-winnowing machine, 3-first disintegrator 4-second pulverizer, 5-travelling belt, 6-mixing machine, 7-worm conveyor, 8-biomass granulator (transmission efficiency can reach more than 95%).
Fig. 2 shows biomass fuel prepared by embodiment 1,2, and diameter is respectively 30mm and 25mm from left to right.
Embodiment
Device in Fig. 1 is adopted to prepare biomass fuel in embodiment 1 and 2.This device comprises baking oven 1, winnowing machine 2, first disintegrator 3, second pulverizer 4, travelling belt 5, mixing machine 6, worm conveyor 7 and biomass granulator 8.First disintegrator 3, second pulverizer 4, mixing machine 6 are connected with sack cleaner respectively, and each sack cleaner is also connected with blower fan.Each sack cleaner is connected with the inlet side mouth of worm conveyor by pipeline, to be added in mixture by the dust of collection.At worm conveyor 7 entrance end, place is also provided with lubricant agent feeding device.
Embodiment 1
The dregs of a decoction that MAILUONING ZHUSHEYE produces in producing: the root of bidentate achyranthes 1 mass parts, radix scrophulariae 1 mass parts, the stem of noble dendrobium 1 mass parts and Japanese Honeysuckle 1 mass parts are mixed, add medicinal material total mass 4 ~ 8 times of water gagings, soak after 0.5 ~ 3 hour, decoct extraction 1 ~ 3 time, each 1 ~ 3 hour, filter the dregs of a decoction obtained and be the Mailuoning production dregs of a decoction.
Getting Mailuoning, to produce dregs of a decoction 80Kg(water ratio be 80%), put into baking oven 1 and dry to water ratio to be 30%, to obtain dry dregs of a decoction 32Kg.Adopt winnowing machine to carry out selection by winnowing the dry dregs of a decoction, be separated the draft dregs of a decoction and the woody dregs of a decoction.Be delivered in first disintegrator 3 by the draft dregs of a decoction, being crushed to particle diameter is 0.5-5mm, obtains draft powder.The dry dregs of a decoction of 16kg(are added and stalk mass ratio is 10:5 in the woody dregs of a decoction) maize straw (water ratio is 14%), adopt the second pulverizer 4 to be cut to the segment that length is 15-25mm, obtain woody particle.Tap density after the pulverizing of the draft dregs of a decoction improves about 70%, and the tap density of the woody dregs of a decoction and maize straw improves about 120%.
Draft powder and woody particle are delivered in mixing machine 6 by travelling belt 5, mix and obtain mixture.Material after pulverizing, in the process of carrying draft powder and woody particle, through setting gauge effect, paves in loose condition (of surface) by travelling belt 5.
The sack cleaner be all connected with first, second pulverizer, mixing machine, for collect cause in pulverizing, mixing process fly upward dust.
By feeding lubricating device, water is delivered to the inlet side mouth of worm conveyor, 1.5L water is added in mixture.Feeding lubricating device can be peristaltic pump, a termination water container of peristaltic pump, the inlet side mouth of another termination worm conveyor.Mixture is delivered to biomass granulator 8 by worm conveyor 7, and in biomass granulator, mixture is pressed into the particulate biomass fuel 1 of 60kg.Biomass granulator granulation conditions: compression temperature is 260 DEG C, pressure is 32Mpa.The particle diameter of biomass fuel is about 25mm.
Dust by Cemented filling to the port of worm conveyor, can be added in mixture, then granulates, can make full use of material like this, avoid dust from flying to affect Working environment and last handling process by the dust that each sack cleaner is collected.Whether dust is collected and is added in compound, very little, almost negligible on the fuel value impact of biomass fuel.
Manufacture contrast biomass fuel 1: according to the manufacture method manufacture contrast biomass fuel 1 of biomass fuel 1, difference is: directly maize straw is added into Mailuoning and produces in the dregs of a decoction (water ratio is 30%), being then jointly crushed to particle diameter is 1-10mm.
Embodiment 2
Ji river medicine company three is broken the dregs of a decoction produced during sheet is produced: by Chinese ephedra 1 mass parts, almond 1 mass parts, the mixing of Radix Glycyrrhizae 1 mass parts, add medicinal material total mass 4 ~ 8 times of water gagings, soak after 0.5 ~ 3 hour, decoct extraction 1 ~ 3 time, each 1 ~ 3 hour, filter the dregs of a decoction obtained and be the three stubborn sheets production dregs of a decoction.
In reference example 1, method prepares biomass fuel 2, difference is: the dregs of a decoction of employing to be water ratio be 85% three stubborn sheets produce the dregs of a decoction, be that 85% dregs of a decoction adopt oven for drying to water ratio to be the dry dregs of a decoction of 28%(by water ratio), maize straw (water ratio 18%) and dry dregs of a decoction mass ratio are 10:10, in every kilogram of dry dregs of a decoction and stalk mixture, the add-on of lubricant water is 20mL, granulation conditions is: compression temperature 240 DEG C, and pressure is 38Mpa.The particle diameter of biomass fuel is about 30mm.
Manufacture contrast biomass fuel 2: according to the manufacture method manufacture contrast biomass fuel 2 of biomass fuel 2, difference is: directly producing the dregs of a decoction (water ratio is 28%) by adding three stubborn sheets in maize straw, being then jointly crushed to particle diameter is 1-10mm.
Embodiment 3
The Baihu Tang dregs of a decoction: by gypsum 50 mass parts, the wind-weed 18 mass parts, Radix Glycyrrhizae 6 mass parts, the mixing of polished rice 9 mass parts, add medicinal material total mass 6 ~ 8 times of water gagings, soak after 0.5 ~ 3 hour, decoct extraction 1 ~ 3 time, each 1 ~ 3 hour, filter the dregs of a decoction obtained and be the Baihu Tang production dregs of a decoction.These Baihu Tang dregs of a decoction and before described embodiment dregs of a decoction difference are, containing this mineral medicine composition of gypsum among its dregs of a decoction.Mineral medicine almost cannot burn, and does not possess fuel value, can cause damage to machine simultaneously, therefore will remove the gypsum in the dregs of a decoction, to prepare biomass fuel.
In reference example 1, method prepares biomass fuel 3, difference is: the dregs of a decoction of employing to be water ratio be 70% Baihu Tang produce the dregs of a decoction, be that 70% dregs of a decoction adopt oven for drying to water ratio to be 25% by water ratio, because density variation is larger, now wherein gypsum component almost will be removed completely by winnowing machine selection by winnowing, obtain the dry dregs of a decoction.Maize straw (water ratio 10%) and dry dregs of a decoction mass ratio are 10:10, and in every kilogram of dry dregs of a decoction and stalk mixture, the add-on of lubricant water is 20mL, and granulation conditions is: compression temperature 240 DEG C, and pressure is 38Mpa.The particle diameter of biomass fuel is about 30mm.
Manufacture contrast biomass fuel 3: according to the manufacture method manufacture contrast biomass fuel 3 of biomass fuel 3, difference is: directly at the production dregs of a decoction (water ratio is 25%) will obtained after adding artificial removal's gypsum in maize straw, being then jointly crushed to particle diameter is 1-10mm.
Embodiment 4
Biomass fuel 2 prepared by the biomass fuel 1 maize straw, the dry dregs of a decoction, embodiment 1 prepared, contrast biomass fuel 1, embodiment 2 and contrast biomass fuel 2, biomass fuel 3 prepared by embodiment 3 and contrast biomass fuel 3 deliver to the fuel value that Center of Analysis & Test, Henan Prov. checks each material, and concrete outcome is in table 1.
The fuel value contrast table of table 1 biomass fuel of the present invention and raw material
As can be seen from Table 1, dregs of a decoction compatibility maize straw ratio (mass ratio), biomass fuel 1, biomass fuel 2 are compared its raw material (i.e. the mixture of maize straw and dry dregs of a decoction quality) and are improved more than 20% with the fuel value of biomass fuel 3, achieve beyond thought technique effect.The reason that the fuel value of biomass fuel 1, biomass fuel 2 and biomass fuel 3 significantly improves be the woody dregs of a decoction and maize straw mixture separate with the draft dregs of a decoction pulverize, excellent fit ratio and treatment process.In biomass granulator, due to the effect of high temperature, the woody dregs of a decoction and stalk can form the skeleton of flammable particle, and the draft dregs of a decoction can fill out the fibre gap at the woody dregs of a decoction closely.During burning, the draft powder that particle diameter is less burns rapidly, release of heat, and as the detonator of the woody dregs of a decoction and stalk and ignition dope, make the woody dregs of a decoction and straw burning more abundant, discharge more heats, and significantly improve fuel value due to Thorough combustion, reduce the generation of dense smoke, products of combustion safety and environmental protection, obtains good effect.
In the process preparing biomass fuel, do not add lubricant water if find in mixture, so mixture water ratio is too low, and cause biomass granule fuel molding effect poor, defect ware is more.Through repeatedly attempting, find that in mixture, add water can obtain desirable molding effect, moisture can increase the oilness of draft powder and woody particle, makes it be easy to flow in machinery, shaping; As free radical requisite between biomass granule, colloid can be mixed to form with the pectin in the dregs of a decoction, starch or carbohydrate, play tackiness agent again.
Claims (9)
1. be a preparation method for the biomass fuel of raw material with the dregs of a decoction, it is characterized in that comprising the steps: the draft dregs of a decoction in the dregs of a decoction to be crushed to the draft powder that particle diameter is 0.5 ~ 5mm; The woody dregs of a decoction and stalk are cut to the segment that length is 10-30mm, obtain woody particle; Draft powder and woody particle are mixed, are compressed into particulate state.
2. the preparation method of biomass fuel according to claim 1, is characterized in that the dregs of a decoction that the described dregs of a decoction are MAILUONING ZHUSHEYE, three stubborn sheets, the blue oral liquid in Pu ground, cassia twig and poria cocos soft capsule, Baihu Tang produce in producing; Stalk is maize straw, cotton stalk, wheat stalk; The mass ratio of the described dregs of a decoction and stalk is 10:1-15.
3. the preparation method of biomass fuel according to claim 2, it is characterized in that the water ratio of the described dregs of a decoction is 20-35%, the water ratio of described stalk is 10-20%.
4. the preparation method of biomass fuel according to claim 3, adds lubricant after it is characterized in that described draft powder and the mixing of woody particle, then makes particulate state; Described lubricant is water, adds 20 ~ 40ml water in every kilogram of dregs of a decoction and stalk mixture.
5. the preparation method of biomass fuel according to claim 4, is characterized in that the particle diameter of described biomass fuel is 5-100mm.
6., according to the preparation method of the described biomass fuel of one of claim 1-5, it is characterized in that adopting winnowing machine to be separated with the woody dregs of a decoction by the draft dregs of a decoction in the dregs of a decoction.
7. the preparation method of biomass fuel according to claim 6; it is characterized in that described draft powder and woody particle mix in mixing machine; be sent in biomass granulator by worm conveyor; make particulate state, be provided with feeding lubricating device at described worm conveyor entrance end place.
8. the preparation method of biomass fuel according to claim 7, is characterized in that the granulation conditions of described biomass granulator: compression temperature 220 DEG C ~ 280 DEG C, compression pressure 25Mpa ~ 40Mpa.
9. the preparation method of biomass fuel according to claim 8, its feature is connected with sack cleaner at described mixing machine, the dust collected in described sack cleaner by Cemented filling to worm conveyor entrance end place.
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106734104A (en) * | 2016-12-30 | 2017-05-31 | 天津横天生物科技有限公司 | A kind of Chinese medicine dreg recycle device |
| CN109280571A (en) * | 2018-12-10 | 2019-01-29 | 怀化正好制药有限公司 | The preparation method and dregs of a decoction biomass fuel of dregs of a decoction biomass fuel |
| CN110064026A (en) * | 2019-03-19 | 2019-07-30 | 安徽拂旦生物科技有限公司 | A kind of Efficient utilization method of meter of dry measure used in former times |
| CN110484324A (en) * | 2019-08-29 | 2019-11-22 | 深圳市洁鑫环保科技有限公司 | A kind of afforestation branch leaf offal treatment production micron biomass fuel |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2004209462A (en) * | 2002-12-18 | 2004-07-29 | Kobe Steel Ltd | Drying method of plant-derived biomass, and production method of biomass fuel |
| CN101676370A (en) * | 2008-09-20 | 2010-03-24 | 康中锡 | Compressed fuel rod |
| CN102250665A (en) * | 2011-06-23 | 2011-11-23 | 天津市东庄生物能源科技有限公司 | Biomass fuel particle and preparation method thereof |
| CN104357119A (en) * | 2014-10-21 | 2015-02-18 | 厦门三和利能源科技有限公司 | Biomass carbon particle and preparation method thereof |
| CN204400939U (en) * | 2014-12-18 | 2015-06-17 | 广东正鹏生物质能源科技有限公司 | A kind of total system of draft dregs of a decoction biomass fuel |
| CN104893780A (en) * | 2015-05-21 | 2015-09-09 | 遵义兴和能源有限公司 | Production system of biomass moulding fuel |
-
2015
- 2015-12-22 CN CN201510966565.XA patent/CN105567372B/en active Active
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2004209462A (en) * | 2002-12-18 | 2004-07-29 | Kobe Steel Ltd | Drying method of plant-derived biomass, and production method of biomass fuel |
| CN101676370A (en) * | 2008-09-20 | 2010-03-24 | 康中锡 | Compressed fuel rod |
| CN102250665A (en) * | 2011-06-23 | 2011-11-23 | 天津市东庄生物能源科技有限公司 | Biomass fuel particle and preparation method thereof |
| CN104357119A (en) * | 2014-10-21 | 2015-02-18 | 厦门三和利能源科技有限公司 | Biomass carbon particle and preparation method thereof |
| CN204400939U (en) * | 2014-12-18 | 2015-06-17 | 广东正鹏生物质能源科技有限公司 | A kind of total system of draft dregs of a decoction biomass fuel |
| CN104893780A (en) * | 2015-05-21 | 2015-09-09 | 遵义兴和能源有限公司 | Production system of biomass moulding fuel |
Non-Patent Citations (1)
| Title |
|---|
| 郑裕国等: "《生物质加工过程与设备》", 31 July 2004, 化学工业出版社 * |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106734104A (en) * | 2016-12-30 | 2017-05-31 | 天津横天生物科技有限公司 | A kind of Chinese medicine dreg recycle device |
| CN109280571A (en) * | 2018-12-10 | 2019-01-29 | 怀化正好制药有限公司 | The preparation method and dregs of a decoction biomass fuel of dregs of a decoction biomass fuel |
| CN110064026A (en) * | 2019-03-19 | 2019-07-30 | 安徽拂旦生物科技有限公司 | A kind of Efficient utilization method of meter of dry measure used in former times |
| CN110064026B (en) * | 2019-03-19 | 2022-07-29 | 安徽拂旦生物科技有限公司 | Utilization method of dendrobe |
| CN110484324A (en) * | 2019-08-29 | 2019-11-22 | 深圳市洁鑫环保科技有限公司 | A kind of afforestation branch leaf offal treatment production micron biomass fuel |
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