CN109207228A - A kind of biomass granule fuel drying technology - Google Patents

A kind of biomass granule fuel drying technology Download PDF

Info

Publication number
CN109207228A
CN109207228A CN201811229774.6A CN201811229774A CN109207228A CN 109207228 A CN109207228 A CN 109207228A CN 201811229774 A CN201811229774 A CN 201811229774A CN 109207228 A CN109207228 A CN 109207228A
Authority
CN
China
Prior art keywords
raw material
plant ash
treated
moisture
reaction kettle
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.)
Pending
Application number
CN201811229774.6A
Other languages
Chinese (zh)
Inventor
张建明
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Chizhou Zhongfeng Modern Agricultural Development Co Ltd
Original Assignee
Chizhou Zhongfeng Modern Agricultural Development Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Chizhou Zhongfeng Modern Agricultural Development Co Ltd filed Critical Chizhou Zhongfeng Modern Agricultural Development Co Ltd
Priority to CN201811229774.6A priority Critical patent/CN109207228A/en
Publication of CN109207228A publication Critical patent/CN109207228A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L5/00Solid fuels
    • C10L5/40Solid fuels essentially based on materials of non-mineral origin
    • C10L5/44Solid fuels essentially based on materials of non-mineral origin on vegetable substances
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/10Biofuels, e.g. bio-diesel
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel

Abstract

The present invention relates to biomass fuel processing technique fields, and in particular to a kind of biomass granule fuel drying technology includes the following steps: to be crushed, level-one drying, screening, secondary drying, three-stage drying, molding, granulation.Raw material is broken for the strip that length is not more than 1cm by step 1 of the present invention, to make in subsequent step, plant ash can sufficiently adsorb the moisture in raw material, the plant ash being mixed into raw material is purged, specific implementation is first by will be mixed into raw material and the dry plant ash of unadsorbed moisture screens out, and in raw material adsorption moisture plant ash due to water suction after volume become larger, it is persisted in the feed, so again by way of selection by winnowing, the wet plant ash of adsorption moisture is purged, it ensure that and no longer adulterate plant ash in raw material, finally pass through three-stage drying method again, slough the moisture in raw material thoroughly, solve the problems, such as that efficiency of combustion is low.

Description

A kind of biomass granule fuel drying technology
Technical field
The present invention relates to biomass fuel processing technique fields, and in particular to a kind of biomass granule fuel drying and moulding work Skill.
Background technique
The research and development of bioenergy technology have become one of great heat subject in the world, by countries in the world government with The concern of scientist.Many countries have all formulated corresponding developmental research plan, such as the green energy resource of the sunlight program of Japan, India Engineering, the energy farm in the U.S. etc., wherein the development and utilization of bioenergy occupy sizable share.External many bioenergies Technology and equipment has reached commercial applications degree, compared with other biological mass-energy source technology, biomass granule fuel skill Art is easier to realize large-scale production and use.It can be equal to energy such as combustion gas, fuel oils using the comfort level of bioenergy particle Beauty.By taking the states such as the U.S., Sweden and Austria as an example, the application scale of bioenergy accounts for the disposable energy-output ratio of the state respectively 4%, 16% and 10%;In the U.S., the total installation of generating capacity of bioenergy power generation is more than 1MW, and single-machine capacity is up to 10~25MW; In America and Europe, the biomass granule fuel and matched high-efficiency cleaning burning Heating and cooking stove for general resident's household are very general And.China also attaches great importance to the development and utilization of bioenergy.Since the 1980s, Chinese Government is always by biomass energy Source is classified as emphasis key scientific and technological projects using the research and application of technology, has carried out the research of biomass utilization new technology and has opened Hair, is further improved Biomass Energy Technology.But the research on utilization of Chinese biological mass-energy is concentrated mainly on large and medium-sized livestock and poultry The projects such as field methane engineering technology, gasifying stalk central gas supply technology and garbage loading embeading generation technology, for biomass energy particle The production and processing of fuel product and the research that utilizes of directly burning are also at the early-stage.China is energy consumption big country, adjusts the energy Structure is inevitable choice using biomass energy.After compression forming, volume substantially reduces to be more convenient for transporting biomass Defeated, storage and use, solve the crucial problem that biomass utilizes on a large scale, therefore the technology and equipment are very suitable for biology Matter power generation, the clean energy resource transformation of Industrial Boiler, rural novel cooking fuel.
Summary of the invention
It is an object of the invention to overcome problems of the prior art, a kind of biomass granule fuel is provided and is dried to Type technique, it may be implemented to reduce the humidity in biological particles raw material, improve the calorific value of biological particles.
To realize above-mentioned technical purpose and the technique effect, the present invention is achieved by the following technical solutions:
A kind of biomass granule fuel drying technology comprising following steps:
Step 1 is crushed: by the raw material of biological particles by crusher, being broken into the strip that length is not more than 1cm;
Step 2, level-one are dry: by step 1, treated that raw material is placed in reaction kettle, and vegetation is added into reaction kettle Ash is stirred until homogeneous, and makes the moisture in plant ash absorption raw material;
Step 3, screening: by step 2, treated that raw material screens, and specific steps include:
Step 3.1, by step 2, treated that raw material pours into reciprocating sieve, rejects the plant ash of unadsorbed moisture in raw material, Wherein the sieve mesh number of reciprocating sieve is 100~120 mesh;
Raw material after rejecting plant ash in above-mentioned steps is placed in winnowing machine by step 3.2, is carried out selection by winnowing, is rejected raw material The plant ash of middle adsorption moisture;
Step 4, secondary drying: it specifically includes:
Step 4.1, by step 3, treated that raw material is placed in hydrothermal reaction kettle, slough moisture in raw material, metal from Son;
Step 4.2, by step 4, treated that raw material is placed in vacuum drier dehydrates, and it is dry to adjust vacuum The parameter of dry machine: 350~380mmHg of vacuum degree;
Step 5, three-stage drying: by step 4, treated that raw material is put into dryer, is dried;
Step 6, molding: by step 5, treated that raw material is put into molding machine, and powder-mixed raw material is made;
Step 7 is granulated: powder-mixed raw material obtained in step 6 being placed in pelletizer and carries out extruding pelletization and makes Obtain biological particles.
Further, the ratio of plant ash and raw material is not less than 1.5:1 in the step 2.
Further, in the step 4, the parameter of hydrothermal reaction kettle is adjusted are as follows: 197~206 DEG C of temperature.
Further, the plant ash may be replaced by one of casein, calcium carbonate.
Beneficial effects of the present invention: raw material is broken for the strip that length is not more than 1cm by step 1, to make subsequent step In, plant ash can sufficiently adsorb the moisture in raw material, can be carried out the plant ash being mixed into raw material by step 3 clear It removes, specific implementation is will to be mixed into raw material and the dry plant ash of unadsorbed moisture screens out by step 3.1 first, And in raw material adsorption moisture plant ash due to after water suction volume become larger, be persisted in the feed, so being made again by step 3.2 With the mode of selection by winnowing, the wet plant ash of adsorption moisture is purged, ensure that and no longer adulterate plant ash in raw material, finally again By three-stage drying method, slough the moisture in raw material thoroughly, solve in the prior art, merely by dryer to raw material into Row dehydration and drying, caused by raw material humidity it is big, efficiency of combustion low problem when biological particles being made to burn.
Specific embodiment
In order to be easy to understand the technical means, the creative features, the aims and the efficiencies achieved by the present invention, below will Technical scheme in the embodiment of the invention is clearly and completely described, it is clear that described embodiment is only the present invention A part of the embodiment, instead of all the embodiments.Based on the embodiments of the present invention, those of ordinary skill in the art are not having All other embodiment obtained under the premise of creative work is made, shall fall within the protection scope of the present invention.
Embodiment 1
A kind of biomass granule fuel drying technology comprising following steps:
Step 1 is crushed: by the raw material of biological particles by crusher, being broken into the strip that length is not more than 1cm;
Step 2, level-one are dry: by step 1, treated that raw material is placed in reaction kettle, and vegetation is added into reaction kettle Ash is stirred until homogeneous, and makes the moisture in plant ash absorption raw material;
Step 3, screening: by step 2, treated that raw material screens, and specific steps include:
Step 3.1, by step 2, treated that raw material pours into reciprocating sieve, rejects the plant ash of unadsorbed moisture in raw material, Wherein the sieve mesh number of reciprocating sieve is 100~120 mesh;
Raw material after rejecting plant ash in above-mentioned steps is placed in winnowing machine by step 3.2, is carried out selection by winnowing, is rejected raw material The plant ash of middle adsorption moisture;
Step 4, secondary drying: it specifically includes:
Step 4.1, by step 3, treated that raw material is placed in hydrothermal reaction kettle, slough moisture in raw material, metal from Son;
Step 4.2, by step 4, treated that raw material is placed in vacuum drier dehydrates, and it is dry to adjust vacuum The parameter of dry machine: 350~380mmHg of vacuum degree;
Step 5, three-stage drying: by step 4, treated that raw material is put into dryer, is dried;
Step 6, molding: by step 5, treated that raw material is put into molding machine, and powder-mixed raw material is made;
Step 7 is granulated: powder-mixed raw material obtained in step 6 being placed in pelletizer and carries out extruding pelletization and makes Obtain biological particles.
The ratio of plant ash and raw material is not less than 1.5:1 in the step 2.
In the step 4, the parameter of hydrothermal reaction kettle is adjusted are as follows: 197~206 DEG C of temperature.
Embodiment 2
A kind of biomass granule fuel drying technology comprising following steps:
Step 1 is crushed: by the raw material of biological particles by crusher, being broken into the strip that length is not more than 1cm;
Step 2, level-one are dry: by step 1, treated that raw material is placed in reaction kettle, and cheese is added into reaction kettle Element is stirred until homogeneous, and makes the moisture in casein absorption raw material;
Step 3, screening: by step 2, treated that raw material screens, and specific steps include:
Step 3.1, by step 2, treated that raw material pours into reciprocating sieve, rejects the casein of unadsorbed moisture in raw material, Wherein the sieve mesh number of reciprocating sieve is 100~120 mesh;
Raw material after rejecting casein in above-mentioned steps is placed in winnowing machine by step 3.2, is carried out selection by winnowing, is rejected raw material The casein of middle adsorption moisture;
Step 4, secondary drying: it specifically includes:
Step 4.1, by step 3, treated that raw material is placed in hydrothermal reaction kettle, slough moisture in raw material, metal from Son further, then toluene di-isocyanate(TDI) is added into hydrothermal reaction kettle, and toluene di-isocyanate(TDI) can carry out anti-with water It answers, so that it is dry to take off the moisture in raw material quickly;
Step 4.2, by step 4, treated that raw material is placed in vacuum drier dehydrates, and it is dry to adjust vacuum The parameter of dry machine: 350~380mmHg of vacuum degree;
Step 5, three-stage drying: by step 4, treated that raw material is put into dryer, is dried;
Step 6, molding: by step 5, treated that raw material is put into molding machine, and powder-mixed raw material is made;
Step 7 is granulated: powder-mixed raw material obtained in step 6 being placed in pelletizer and carries out extruding pelletization and makes Obtain biological particles.
The ratio of casein and raw material is not less than 1.5:1 in the step 2.
In the step 4, the parameter of hydrothermal reaction kettle is adjusted are as follows: 197~206 DEG C of temperature.
Embodiment 3
A kind of biomass granule fuel drying technology comprising following steps:
Step 1 is crushed: by the raw material of biological particles by crusher, being broken into the strip that length is not more than 1cm;
Step 2, level-one are dry: by step 1, treated that raw material is placed in reaction kettle, and carbonic acid is added into reaction kettle Calcium is stirred until homogeneous, and makes the moisture in calcium carbonate absorption raw material;
Step 3, screening: by step 2, treated that raw material screens, and specific steps include:
Step 3.1, by step 2, treated that raw material pours into reciprocating sieve, rejects the calcium carbonate of unadsorbed moisture in raw material, Wherein the sieve mesh number of reciprocating sieve is 100~120 mesh;
Raw material after rejecting calcium carbonate in above-mentioned steps is placed in winnowing machine by step 3.2, is carried out selection by winnowing, is rejected raw material The calcium carbonate of middle adsorption moisture;
Step 4, secondary drying: it specifically includes:
Step 4.1, by step 3, treated that raw material is placed in hydrothermal reaction kettle, slough moisture in raw material, metal from Son;
Step 4.2, by step 4, treated that raw material is placed in vacuum drier dehydrates, and it is dry to adjust vacuum The parameter of dry machine: 350~380mmHg of vacuum degree;
Step 5, three-stage drying: by step 4, treated that raw material is put into dryer, is dried;
Step 6, molding: by step 5, treated that raw material is put into molding machine, and powder-mixed raw material is made;
Step 7 is granulated: powder-mixed raw material obtained in step 6 being placed in pelletizer and carries out extruding pelletization and makes Obtain biological particles.
The ratio of calcium carbonate and raw material is not less than 1.5:1 in the step 2.
In the step 4, the parameter of hydrothermal reaction kettle is adjusted are as follows: 197~206 DEG C of temperature.
In order to more intuitively illustrate technical effect of the invention, now to wet in biological particles made from embodiment 1-3 Degree is detected, and wherein comparative example is biological particles made from the prior art, and detection effect is as follows:
The Humidity Detection result of biological particles in embodiment 1: 0.33RH;
The Humidity Detection result of biological particles in embodiment 2: 0.12RH;
The Humidity Detection result of biological particles in embodiment 3: 0.29RH;
The Humidity Detection result of biological particles in comparative example: 0.75RH;
In conclusion the humidity of embodiment 2 is minimum, and drying technology of the invention compared with the prior art have significantly into Step.Wherein Humidity Detection tool is the 635-2 model humidity measurement instrument of De Tu Testo company production.
Present invention disclosed above preferred embodiment is only intended to help to illustrate the present invention.There is no detailed for preferred embodiment All details are described, are not limited the invention to the specific embodiments described.Obviously, according to the content of this specification, It can make many modifications and variations.These embodiments are chosen and specifically described to this specification, is in order to better explain the present invention Principle and practical application, so that skilled artisan be enable to better understand and utilize the present invention.The present invention is only It is limited by claims and its full scope and equivalent.

Claims (4)

1. a kind of biomass granule fuel drying technology, which is characterized in that it includes the following steps:
Step 1 is crushed: by the raw material of biological particles by crusher, being broken into the strip that length is not more than 1cm;
Step 2, level-one are dry: by step 1, treated that raw material is placed in reaction kettle, and plant ash is added into reaction kettle, stirs It mixes to uniform, makes the moisture in plant ash absorption raw material;
Step 3, screening: by step 2, treated that raw material screens, and specific steps include:
Step 3.1, by step 2, treated that raw material pours into reciprocating sieve, rejects the plant ash of unadsorbed moisture in raw material, wherein The sieve mesh number of reciprocating sieve is 100~120 mesh;
Raw material after rejecting plant ash in above-mentioned steps is placed in winnowing machine by step 3.2, is carried out selection by winnowing, is rejected and inhale in raw material The plant ash of attached water point;
Step 4, secondary drying: it specifically includes:
Step 4.1, by step 3, treated that raw material is placed in hydrothermal reaction kettle, sloughs moisture, metal ion in raw material;
Step 4.2, by step 4, treated that raw material is placed in vacuum drier dehydrates, and adjusts vacuum drier Parameter: 350~380mmHg of vacuum degree;
Step 5, three-stage drying: by step 4, treated that raw material is put into dryer, is dried;
Step 6, molding: by step 5, treated that raw material is put into molding machine, and powder-mixed raw material is made;
Step 7 is granulated: powder-mixed raw material obtained in step 6 being placed in pelletizer and carries out extruding pelletization and life is made Material grains.
2. a kind of biomass granule fuel drying technology according to claim 1, which is characterized in that the step 2 The ratio of middle plant ash and raw material is not less than 1.5:1.
3. a kind of biomass granule fuel drying technology according to claim 1, which is characterized in that the step 4 In, the parameter of hydrothermal reaction kettle adjusts are as follows: 197~206 DEG C of temperature.
4. a kind of biomass granule fuel drying technology according to claim 1, which is characterized in that the plant ash It may be replaced by one of casein, calcium carbonate.
CN201811229774.6A 2018-10-22 2018-10-22 A kind of biomass granule fuel drying technology Pending CN109207228A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201811229774.6A CN109207228A (en) 2018-10-22 2018-10-22 A kind of biomass granule fuel drying technology

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201811229774.6A CN109207228A (en) 2018-10-22 2018-10-22 A kind of biomass granule fuel drying technology

Publications (1)

Publication Number Publication Date
CN109207228A true CN109207228A (en) 2019-01-15

Family

ID=64979906

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201811229774.6A Pending CN109207228A (en) 2018-10-22 2018-10-22 A kind of biomass granule fuel drying technology

Country Status (1)

Country Link
CN (1) CN109207228A (en)

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101265426A (en) * 2008-05-08 2008-09-17 西安北方惠安化学工业有限公司 Cleaning type low-pressure low-temperature burning solid fuel
CN102070763A (en) * 2010-12-24 2011-05-25 东莞市源聚德实业有限公司 Medicinal water absorption sponge and preparation method thereof
CN201897375U (en) * 2010-11-08 2011-07-13 苏州市华扬电子有限公司 Energy-saving drying machine
CN106068763A (en) * 2016-06-21 2016-11-09 中国科学院昆明植物研究所 The method for cleaning of pittosporum tobira seed
CN106106434A (en) * 2016-06-28 2016-11-16 咸宁市农业科学院 A kind of method storing cucumber seeds
CN106288669A (en) * 2016-08-30 2017-01-04 上海源耀生物股份有限公司 A kind of method using superabsorbent fiber dry products
CN107213872A (en) * 2017-07-20 2017-09-29 浙江农林大学 A kind of preparation method of the hydro-thermal biomass carbon material of efficient absorption copper ion load calcium carbonate
CN109207223A (en) * 2018-10-09 2019-01-15 池州众丰现代农业发展有限公司 A kind of preparation method of burning-assist biomass granule fuel
US20190292050A1 (en) * 2006-03-23 2019-09-26 Keystone Metals Recovery Inc. Metal chlorides and metals obtained from metal oxide containing materials

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20190292050A1 (en) * 2006-03-23 2019-09-26 Keystone Metals Recovery Inc. Metal chlorides and metals obtained from metal oxide containing materials
CN101265426A (en) * 2008-05-08 2008-09-17 西安北方惠安化学工业有限公司 Cleaning type low-pressure low-temperature burning solid fuel
CN201897375U (en) * 2010-11-08 2011-07-13 苏州市华扬电子有限公司 Energy-saving drying machine
CN102070763A (en) * 2010-12-24 2011-05-25 东莞市源聚德实业有限公司 Medicinal water absorption sponge and preparation method thereof
CN106068763A (en) * 2016-06-21 2016-11-09 中国科学院昆明植物研究所 The method for cleaning of pittosporum tobira seed
CN106106434A (en) * 2016-06-28 2016-11-16 咸宁市农业科学院 A kind of method storing cucumber seeds
CN106288669A (en) * 2016-08-30 2017-01-04 上海源耀生物股份有限公司 A kind of method using superabsorbent fiber dry products
CN107213872A (en) * 2017-07-20 2017-09-29 浙江农林大学 A kind of preparation method of the hydro-thermal biomass carbon material of efficient absorption copper ion load calcium carbonate
CN109207223A (en) * 2018-10-09 2019-01-15 池州众丰现代农业发展有限公司 A kind of preparation method of burning-assist biomass granule fuel

Non-Patent Citations (5)

* Cited by examiner, † Cited by third party
Title
卫强: "《天然药物化学实验指导》", 31 December 2014, 安徽大学出版社 *
李俊贤: "《塑料工业手册 聚氨酯》", 31 July 1999, 化学工业出版社 *
潘永康等: "《现代干燥技术》", 30 September 1998, 化学工业出版社 *
田文富等: "《普通高等院校材料工程类规划教材 硅酸盐热工基础》", 31 March 2017, 中国建材工业出版社 *
薛智勇: "《农业固体废物处理与处置》", 30 November 2016, 河南科学技术出版社 *

Similar Documents

Publication Publication Date Title
CN100443574C (en) Method and device for producing fuels from compressed biomass and use of said fuels
CN108913269A (en) A kind of Wheat Straw biological particles and preparation method thereof
CN103666620A (en) Biomass fuel with good formability
CN101992202B (en) Method for treating biomass process residues
CN102730681A (en) Preparation method of high adsorptive activated carbon
CN104258808A (en) Method and system for increasing specific surface area of sludge biochar
CN106944461A (en) A kind of system and method for domestic rubbish disposal
CN105331376A (en) High-valued treatment device and high-valued treatment method for fresh biomass based on microwave hydrothermal carbonization
CN105710114A (en) Carbonization circulation overall treatment system and method for household refuse and forestry and agricultural residues
CN102851096A (en) Processing method of biomass solid formed fuel
CN109207227A (en) A kind of green environment protective biological matter granular fuel
CN108277237A (en) A kind of countryside wastes processing and utilization method
CN107488479A (en) The method that granular fuel is made using water hyacinth
CN108865314A (en) A kind of resistance to burning biomass particle of novel environment friendly and preparation method thereof
CN102220178A (en) Method for preparing firewood sticks by waste cassava residues and application on charcoal preparation
CN109207228A (en) A kind of biomass granule fuel drying technology
CN108624378A (en) A kind of radix bupleuri dregs of a decoction biological particles and preparation method thereof
CN211057050U (en) Preparation device of sludge-biomass particle fuel rod
CN102492510A (en) Production technology of cassava-potato residue-made fuel rod
TWI527770B (en) Method for integrative conversion of organic sludge and waste cooking oil, refuse derived fuel, and feed additive
CN106190399A (en) A kind of novel biomass shaped fuel
CN105969441A (en) Biomass briquette with good compressive strength and manufacturing method thereof
CN109321305A (en) A kind of biological particles that combustion rate is high
CN110551549A (en) Device and method for preparing sludge-biomass particle fuel rod
CN204824785U (en) Biomass briquette fuel's production system

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication
RJ01 Rejection of invention patent application after publication

Application publication date: 20190115