CN106635239A - Gallic acid production waste biomass fuel and preparation method thereof - Google Patents
Gallic acid production waste biomass fuel and preparation method thereof Download PDFInfo
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- CN106635239A CN106635239A CN201610989997.7A CN201610989997A CN106635239A CN 106635239 A CN106635239 A CN 106635239A CN 201610989997 A CN201610989997 A CN 201610989997A CN 106635239 A CN106635239 A CN 106635239A
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- biomass fuel
- waste residue
- gallic acid
- waste
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Classifications
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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
- C10L5/48—Solid fuels essentially based on materials of non-mineral origin on industrial residues and waste materials
-
- 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
- C10L2290/08—Drying or removing water
-
- 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
- C10L2290/14—Injection, e.g. in a reactor or a fuel stream during fuel production
- C10L2290/146—Injection, e.g. in a reactor or a fuel stream during fuel production of water
-
- 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
-
- 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
- C10L2290/54—Specific separation steps for separating fractions, components or impurities during preparation or upgrading of a fuel
- C10L2290/547—Filtration for separating fractions, components or impurities during preparation or upgrading of a fuel
-
- 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)
Abstract
The invention mainly belongs to the technical field of environment-friendly new energy and particularly relates to a gallic acid production waste biomass fuel and a preparation method thereof. The method comprises taking gallic acid production waste as the raw material, adjusting the PH value of the waste, heating the PH-adjusted waste, and then performing filter pressing, drying and granulation on the waste to obtain the gallic acid production waste biomass fuel. By taking the gallic acid production waste as the raw material, the preparation method is simple in process and low in treatment cost, achieves recycling of the waste, saves forestry resources, reduces environmental pollution and provides a granulated biomass fuel environment-friendly new energy.
Description
Technical field
The present invention principally falls into environmentally friendly technical field of new energies, and in particular to produce life using the waste residue for preparing gallic acid
Biomass fuel and preparation method.
Background technology
The production of gallic acid draws powder etc. as raw material with forest products plant gall or tower, by alkali process hydrolysis, neutralization, thick knot
The technical processs such as crystalline substance, decolorizing and refining be obtained, it is a kind of broad-spectrum fine chemical product, be mainly used in organic synthesiss,
Medicine, dyestuff, feedstuff, food, light industry and electronics industry.Wherein, Galla Chinensiss are the traditional woods special product product of China, and Galla Chinensiss are fitted
The mountain area and hills of warm and moist are preferably grown on, in China main producing region Guizhou, Sichuan, Hubei, Hunan, Shaanxi, Yunnan are concentrated on
Deng six provinces, the Gallnut yield in these provinces accounts for more than the 90% of national total output.Tens thousand of tons are used every year in the whole nation, main to use
In production gallic acid, but gallic acid production hydrolysis and subtractive process can produce a large amount of waste residues (mainly containing wood fibre
And activated carbon), often producing 1 ton of gallic acid can produce 0.6 ton of waste residue, all not be reused at present, mostly go out of use, so
Both the wasting of resources had been caused, to cause to topple over occupied ground, and also environmental pollution.
Tower draws (Tara) also known as Caesalpinia spinosaKuntze, vegetable formal name：CaesalpiniaspinosaKuntze, is Caesalpiniaceae Spruce beetle
Perennial plant, mainly originates in the states such as South America northwestward Peru, and its sub- reality is that tower that bean can be processed into tower that glue, tower that evergreen chinquapin
Glue, its soybean pod is tower and draws powder after crushing.Tower draws powder to be actually the mixture of a kind of tannin and wood fibre, wherein effectively into
Part is tannin, and it is that effective ingredient (tannin) content is 50% that tower draws powder, and wood fibre contains 40%, and moisture content is containing 10%.China is annual
Need import tower to draw powder to produce gallic acid, can equally produce a large amount of waste residues (mainly containing wood fibre and activated carbon), often give birth to
Producing 1 ton of gallic acid can produce 0.8 ton of waste residue, all not be reused at present.
Recent years biomass fuel boiler substitutes coal-burning boiler, contributes to energy saving and improves environment, by National Environmental
Protection portion and China environmental protection industry association list best practical technology of environmental protection in China project in.Biomass fuel boiler needs biomass
Fuel, existing biomass fuel mostly is rice husk, Pericarppium arachidis hypogaeae, corn cob, shell of Camelliaoleifera Abel, cotton seed hullss and " three surplus things " and passes through processing
The bulk environmental protection new forms of energy of generation.
At present, do not occur to utilize and prepare gallic acid (with the gallic acid that Galla Chinensiss or tower drawing powder are prepared as raw material)
Produced waste residue occurs for the technology that raw material prepares biomass fuel.
The content of the invention
For above-mentioned technical problem, the present invention provides a kind of waste residue production biomass fuel for utilizing and preparing gallic acid
Method, methods described is to prepare the waste residue of gallic acid as raw material, and process is simple, processing cost is low, makes waste residue be reused,
Forest products resource is saved, environmental pollution is reduced, there is provided block biomass fuel environmental protection new forms of energy.
The present invention is achieved by the following technical solutions：
A kind of method for producing biomass fuel using the waste residue for preparing gallic acid, be with the waste residue for preparing gallic acid
Raw material, a series of process are carried out to waste residue, and acquisition caloric value is big, fuel purity is high and sanitation and hygiene biomass fuels.
Further, methods described is specially：To prepare the waste residue of gallic acid as raw material, the PH of waste residue is adjusted, and it is right
Adjusting the waste residue after PH carries out heat treated, then carries out filter pressing, drying, granulation to waste residue, prepares the biomass fuel
Material.
Further, the waste residue for preparing gallic acid includes wood fibre, activated carbon and water；Wood fibre in waste residue
Mass percent be 25～30%；The mass percent of waste active carbon is 30～40% in waste residue；The quality percentage of water in slag
Number is 30～45%.
Further, the method comprising the steps of：
(1) will be drawn in waste residue of the powder as raw material prepares gallic acid produced by with Galla Chinensiss or tower and add a certain amount of water,
Heat treated is carried out, and PH to 6～7 is adjusted using sodium hydroxide solution；PH is adjusted to into 6～7, can avoid finally preparing
Biomass fuel for acidity, corrode boiler plant.
(2) by the waste residue after step (1) process, processed using filter press so that slag-liquid separation；
(3) slag charge produced in step (2) is dried using vacuum drier；
(4) using wood substance grain granulator, the dried slag charge that step (3) is produced is suppressed, prepares institute
State biomass fuel.
Further, in step (1), when adding water toward waste residue, amount of water is controlled in 1.5～2L/Kg waste residues.
Further, in step (1), the mass fraction of sodium hydroxide solution is 20～50%.
Further, in step (1), the condition of heat treated is specially：Heating-up temperature is 85～95 DEG C, and temperature retention time is
10～30min.Heat treated is carried out under the heating condition, the acidic materials in waste residue can be made to be dissolved completely in water, made
When adding sodium hydroxide, reaction is complete.
Further, in step (3), vacuum drying condition is：Under the conditions of -0.08～-0.09Mpa, 3～5 are dried
Hour, and it is 20～30% to control moisture in dried slag charge；Moisture should be strictly controlled herein, according to granulation
Require, when moisture is too high, Jing pelletings machine biomass fuel moisture out is high, does not reach product requirement, moisture
It is too low, molding effect can be affected.
A kind of biomass fuel using the waste residue production for preparing gallic acid, according to the side of the production biomass fuel
Method is prepared, and the biomass fuel is columned granule, and the diameter of section of biomass fuel pellet is 6～8mm, granule
Length is 24～40ml, and percentage of damage is 1.5～2.0%；In the biomass fuel, mass percent shared by moisture be 10～
15%, mass percent shared by ash is 1～1.5%, and mass percent shared by element sulphur is 0.05～0.07%, chlorine element institute
Mass percent is accounted for for 0.02～0.07%；The caloric value of the biomass fuel is 4200～5200 kilocalories/kg.
The Advantageous Effects of the present invention：
(1) powder is drawn to prepare waste residue produced after gallic acid as raw material as raw material with Galla Chinensiss or tower, because production does not have
Containing 30～40% waste active carbon in produced waste residue after gallate-based, waste active carbon caloric value in 8000 kilocalories/kg or so,
Therefore, the biomass fuel caloric value for preparing is big, and caloric value is in 4200～5200 kilocalories/kg or so.
(2) the biomass fuel purity that the method for the invention is prepared is high, and without other the debris of heat are not produced,
Its phosphorus content 80～85%, ash 3～5%, water content 10～15% is not generated heat heat dissipation on the contrary without gangue, stone etc.
Impurity, will be directly Reducing Cost in Enterprises.
(3) the method for the invention draws powder to prepare waste residue produced after gallic acid as original as raw material with Galla Chinensiss or tower
Material, so the biomass fuel for preparing not sulfur-bearing phosphorus, does not corrode boiler, can prolonged boiler service life, enterprise will receive
Beneficial gangster is shallow；And due to waste residue biomass fuel not sulfur-bearing phosphorus, do not produce sulfur dioxide and phosphorus pentoxide during burning, thus not
Acid rain can be caused to produce, atmosphere pollution, not free from environmental pollution.
(5) the biomass fuel sanitation and hygiene that the method for the invention is prepared, feed intake conveniently, reduce the work of workman
Intensity, significantly improves work situation, and enterprise will be reduced for the cost in terms of labour force.
(6) compared with coal class A fuel A, ash quarrel is few after the biomass fuel combustion that the method for the invention is prepared,
The place for stacking coal quarrel is greatly reduced, muck removal expense is reduced.
(7) potassium content is high in the biomass fuel that the method for the invention is prepared, and obtains after the fuel combustion
Ashes are the high high-quality organic potassic fertilizers of grade, recyclable to make profits.
Description of the drawings
Fig. 1 is flow chart of the present invention using the method for the waste residue production biomass fuel for preparing gallic acid.
Specific embodiment
In order that the objects, technical solutions and advantages of the present invention become more apparent, it is right below in conjunction with drawings and Examples
The present invention is explained in further detail.It should be appreciated that specific embodiment described herein is used only for explaining the present invention, and
It is not used in the restriction present invention.
Conversely, the present invention covers any replacement done in the spirit and scope of the present invention being defined by the claims, repaiies
Change, equivalent method and scheme.Further, in order that the public has a better understanding to the present invention, below to the thin of the present invention
It is detailed to describe some specific detail sections in section description.Part without these details for a person skilled in the art
Description can also completely understand the present invention.
Embodiment 1
A kind of method for producing biomass fuel using the waste residue for preparing gallic acid, wherein, prepare the useless of gallic acid
Cinder ladle includes wood fibre, activated carbon and water；The mass percent of wood fibre is 25～30% in waste residue；Waste active carbon in waste residue
Mass percent be 30～40%；The mass percent of water is 30～45% in slag.
As shown in figure 1, methods described specifically includes following steps：
(1) 1500L tap waters are added in the enamel reaction still of 3000L, stirring slurry is opened, will be given birth to by raw material of Galla Chinensiss
The waste residue 1000Kg (chemically examine water content be 45%) for producing gallic acid is added in reactor；It is heated to 85 DEG C；Add quality point
Number is 30% sodium hydroxide solution, and it is 6 to adjust PH to PH, is incubated 10 minutes；
(2) slag charge and water are separated using filter press, by the Stress control of filter press in 0.2Mpa, obtains slag
Material (chemically examine water content be 45%)；
(3) slag charge for obtaining step (2), is dried through vacuum drier, and control vacuum drier is -0.08
Under the conditions of～-0.09Mpa, it is dried 3 hours；Dried slag charge (chemically examine water content is 25%)；
(4) dried slag charge is suppressed, granule is pressed into using wood substance grain granulator, biomass fuel is obtained
574.71Kg, chemical examination moisture content is 13%, and wherein wood substance grain granulator is Italy's ETS (EcoTreSystem) biomass wood flour
Granulator.
Embodiment 2
A kind of method for producing biomass fuel using the waste residue for preparing gallic acid, methods described specifically includes following step
Suddenly：
(1) 1000L tap waters are added in the enamel reaction still of 3000L, stirring slurry is opened, with tower powder will be drawn to give birth to as raw material
The waste residue 1000Kg (chemically examine water content be 45%) for producing gallic acid is added in reactor；It is heated to 95 DEG C；Add quality point
Number is 50% sodium hydroxide solution, and it is 6.5 to adjust PH to PH, is incubated 30 minutes；
(2) slag charge and water are separated using filter press, by the Stress control of filter press in 0.3Mpa, obtains slag
Material (chemically examine water content be 45%)；
(3) slag charge for obtaining step (2), is dried through vacuum drier, and control vacuum drier is -0.08
Under the conditions of～-0.09Mpa, it is dried 5 hours；Dried slag charge (chemically examine water content is 20%)；
(4) dried slag charge is suppressed, granule is pressed into using wood substance grain granulator, biomass fuel is obtained
561.8Kg, chemical examination moisture content is 11%.
Embodiment 3
A kind of method for producing biomass fuel using the waste residue for preparing gallic acid, methods described specifically includes following step
Suddenly：
(1) 1750L tap waters are added in the enamel reaction still of 3000L, stirring slurry is opened, powder will be drawn with Galla Chinensiss or tower
Waste residue 1000Kg (chemically examine water content be 45%) for raw material production gallic acid is added in reactor；It is heated to 90 DEG C；Plus
Enter the sodium hydroxide solution that mass fraction is 40%, it is 7 to adjust PH to PH, is incubated 20 minutes；
(2) slag charge and water are separated using filter press, by the Stress control of filter press in 0.2～0.3Mpa,
Obtain slag charge；
(3) slag charge for obtaining step (2), is dried through vacuum drier, and control vacuum drier is -0.08
Under the conditions of～-0.09Mpa, it is dried 4 hours；Dried slag charge (chemically examine water content is 20.63%)；
(4) dried slag charge is suppressed, granule is pressed into using wood substance grain granulator, biomass fuel is obtained
555.51Kg, chemical examination moisture content is 9%.
Biomass fuel to being prepared using the methods described of embodiment 1～3 carries out physico-chemical analysis, analytical data such as table
1, product meets GB/T 21923-2008 standards；Powder is drawn to prepare institute after gallic acid as raw material with Galla Chinensiss or tower as shown in Table 1
The waste residue of generation is raw material, and the biomass fuel caloric value for preparing is big, and caloric value is in 4200～5200 kilocalories/kg or so.
Biomass fuel physico-chemical analysis data in the embodiment 1～3 of table 1
Claims (9)
1. a kind of utilization prepares the method that the waste residue of gallic acid produces biomass fuel, it is characterised in that to prepare Galla Turcica (Galla Helepensis)
The waste residue of acid is raw material, and a series of process are carried out to waste residue, and acquisition caloric value is big, fuel purity is high and sanitation and hygiene biomass
Fuel.
2. the method for producing biomass fuel according to claim 1, it is characterised in that methods described is specially：To prepare
The waste residue of gallic acid is raw material, adjusts the PH of waste residue, and carries out heat treated to the waste residue after regulation PH, and then waste residue is entered
Row filter pressing, drying, granulation, prepare the biomass fuel.
3. the method for producing biomass fuel according to claim 1, it is characterised in that the waste residue for preparing gallic acid
Including wood fibre, activated carbon and water；The mass percent of wood fibre is 25～30% in waste residue；Waste active carbon in waste residue
Mass percent is 30～40%；The mass percent of water is 30～45% in waste residue.
4. the method for producing biomass fuel according to claim 1, it is characterised in that the method comprising the steps of：
（1）A certain amount of water is added by drawing in waste residue of the powder as raw material prepares gallic acid produced by with Galla Chinensiss or tower, is carried out
Heat treated, and PH to 6～7 is adjusted using sodium hydroxide solution；
（2）By step（1）Waste residue after process, is processed so that slag-liquid separation using filter press；
（3）By step（2）The slag charge of middle generation is dried using vacuum drier；
（4）Using wood substance grain granulator, to step（3）The dried slag charge for producing is suppressed, and prepares the life
Biomass fuel.
5. the method for producing biomass fuel according to claim 1, it is characterised in that step（1）In, add toward waste residue
During water, amount of water is controlled in 1.5～2L/Kg waste residues.
6. the method for producing biomass fuel according to claim 1, it is characterised in that step（1）In, sodium hydroxide solution
Mass fraction be 20～50%.
7. the method for producing biomass fuel according to claim 1, it is characterised in that step（1）In, the bar of heat treated
Part is specially：Heating-up temperature is 85～95 DEG C, and temperature retention time is 10～30min.
8. the method for producing biomass fuel according to claim 1, it is characterised in that step（3）In, vacuum drying bar
Part is：Under the conditions of -0.08～-0.09Mpa, be dried 3～5 hours, and control in dried slag charge moisture be 20～
30%。
9. a kind of utilization prepares the biomass fuel of the waste residue production of gallic acid, according to the production of one of claim 1～8
The method of biomass fuel is prepared, it is characterised in that the biomass fuel be columned granule, biomass fuel
The diameter of section of grain is 6～8mm, and particle length is 24～40ml, and percentage of damage is 1.5～2.0%；In the biomass fuel,
Mass percent shared by moisture is 10～15%, and mass percent shared by ash is 1～1.5%, mass percent shared by element sulphur
For 0.05～0.07%, mass percent shared by chlorine element is 0.02～0.07%；The caloric value of the biomass fuel is 4200
～5200 kilocalories/kg.
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| CN201610989997.7A CN106635239A (en) | 2016-11-10 | 2016-11-10 | Gallic acid production waste biomass fuel and preparation method thereof |
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Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1887452A (en) * | 2006-07-24 | 2007-01-03 | 乐山三江生化科技有限公司 | Method of recovering and treating gallic acid sludge |
| CN101679893A (en) * | 2006-12-28 | 2010-03-24 | 安塔克有限公司 | Material and/or fuel produced from biomass |
| CN103028591A (en) * | 2012-11-20 | 2013-04-10 | 遵义鑫湘生物科技有限公司 | Novel technology for recovering and treating waste water, waste residue and waste carbon based on production of gallic acid |
| JP2014057949A (en) * | 2012-09-14 | 2014-04-03 | Natoo Kenkyusho:Kk | Treatment method of pollution type waste gypsum and non-pollution type gypsum composition |
-
2016
- 2016-11-10 CN CN201610989997.7A patent/CN106635239A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1887452A (en) * | 2006-07-24 | 2007-01-03 | 乐山三江生化科技有限公司 | Method of recovering and treating gallic acid sludge |
| CN101679893A (en) * | 2006-12-28 | 2010-03-24 | 安塔克有限公司 | Material and/or fuel produced from biomass |
| JP2014057949A (en) * | 2012-09-14 | 2014-04-03 | Natoo Kenkyusho:Kk | Treatment method of pollution type waste gypsum and non-pollution type gypsum composition |
| CN103028591A (en) * | 2012-11-20 | 2013-04-10 | 遵义鑫湘生物科技有限公司 | Novel technology for recovering and treating waste water, waste residue and waste carbon based on production of gallic acid |
Non-Patent Citations (3)
| Title |
|---|
| 潘永康等: "《现代干燥技术》", 31 May 2007, 化学工业出版社 * |
| 秦清: "没食子酸生产废水、废渣、废炭处理回收技术", 《林产化工通讯》 * |
| 罗列万等: "《名优绿茶连续自动生产线装备与使用技术》", 31 October 2015, 中国农业科学技术出版社 * |
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