CN106362707B - A method of lignin is improved to butanol, acetone, Ethanol Adsorption performance in ABE fermentation liquid - Google Patents

A method of lignin is improved to butanol, acetone, Ethanol Adsorption performance in ABE fermentation liquid Download PDF

Info

Publication number
CN106362707B
CN106362707B CN201611005251.4A CN201611005251A CN106362707B CN 106362707 B CN106362707 B CN 106362707B CN 201611005251 A CN201611005251 A CN 201611005251A CN 106362707 B CN106362707 B CN 106362707B
Authority
CN
China
Prior art keywords
lignin
insoluble
water
ketone
acetone
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.)
Active
Application number
CN201611005251.4A
Other languages
Chinese (zh)
Other versions
CN106362707A (en
Inventor
李�浩
张昕宇
李春利
王洪海
常立芳
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.)
Hebei University of Technology
Original Assignee
Hebei University of Technology
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 Hebei University of Technology filed Critical Hebei University of Technology
Priority to CN201611005251.4A priority Critical patent/CN106362707B/en
Publication of CN106362707A publication Critical patent/CN106362707A/en
Application granted granted Critical
Publication of CN106362707B publication Critical patent/CN106362707B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/22Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
    • B01J20/24Naturally occurring macromolecular compounds, e.g. humic acids or their derivatives
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C29/00Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
    • C07C29/74Separation; Purification; Use of additives, e.g. for stabilisation
    • C07C29/76Separation; Purification; Use of additives, e.g. for stabilisation by physical treatment
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C45/00Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds
    • C07C45/78Separation; Purification; Stabilisation; Use of additives
    • C07C45/79Separation; Purification; Stabilisation; Use of additives by solid-liquid treatment; by chemisorption
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12PFERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P7/00Preparation of oxygen-containing organic compounds
    • C12P7/02Preparation of oxygen-containing organic compounds containing a hydroxy group
    • C12P7/04Preparation of oxygen-containing organic compounds containing a hydroxy group acyclic
    • C12P7/06Ethanol, i.e. non-beverage
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12PFERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P7/00Preparation of oxygen-containing organic compounds
    • C12P7/02Preparation of oxygen-containing organic compounds containing a hydroxy group
    • C12P7/04Preparation of oxygen-containing organic compounds containing a hydroxy group acyclic
    • C12P7/16Butanols
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12PFERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P7/00Preparation of oxygen-containing organic compounds
    • C12P7/24Preparation of oxygen-containing organic compounds containing a carbonyl group
    • C12P7/26Ketones
    • C12P7/28Acetone-containing products
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2220/00Aspects relating to sorbent materials
    • B01J2220/40Aspects relating to the composition of sorbent or filter aid materials
    • B01J2220/48Sorbents characterised by the starting material used for their preparation
    • B01J2220/4812Sorbents characterised by the starting material used for their preparation the starting material being of organic character
    • B01J2220/4837Lignin
    • 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

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Wood Science & Technology (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Zoology (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Biotechnology (AREA)
  • Microbiology (AREA)
  • General Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Biochemistry (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • General Engineering & Computer Science (AREA)
  • General Health & Medical Sciences (AREA)
  • Genetics & Genomics (AREA)
  • Analytical Chemistry (AREA)
  • Preparation Of Compounds By Using Micro-Organisms (AREA)
  • Compounds Of Unknown Constitution (AREA)

Abstract

The present invention be a kind of raising lignin to butanol in ABE fermentation liquid, acetone, Ethanol Adsorption performance method.Lignin is classified as water-soluble fraction and the insoluble fraction of water first with water by the invention, then recycle ketones solvent that the insoluble lignin fraction of water is classified as the molten fraction of ketone and the insoluble fraction of ketone again, it is finally obtained water is insoluble and the insoluble fraction of ketone is used for butanol, acetone, ethyl alcohol in adsorbing separation fermentation liquid.The dissolution stage division relates only to the dissolution classification of lignin, is not related to chemical modification, therefore have the advantages such as simple process and low cost.

Description

A kind of lignin that improves is to butanol in ABE fermentation liquid, acetone, Ethanol Adsorption performance Method
Technical field
The present invention relates to low-concentration organic adsorption technology fields, in particular to a kind of be classified by solvent to improve lignin To butanol in ABE fermentation liquid, acetone, Ethanol Adsorption performance method.
Background technique
Biological butanol is a kind of new bio liquid fuel with high-energy density and high gasoline degree of mixing, because it can make Good organic solvent and fuel performance is excellent, biofermentation production are highly valued.Pass through traditional acetone (Acetone)-butanol (Butanol)-ethyl alcohol (Ethanol) i.e. ABE fermentation method produces biological butanol, and product deposits fermenting microbe In toxicity inhibition, leads to problems such as final product concentrations low and later separation energy consumption is high.(biological fermentation process prepares the product of butanol In be also also known as ABE solvent comprising a large amount of acetone and a small amount of ethyl alcohol equal solvent, product.) it therefore must use effective method Product butanol, acetone and ethyl alcohol are removed in time from fermentation liquid, reduce Product inhibiton, so that improving fermentation production rate reduces production Cost.It is a kind of main isolation technics using absorption method separation and fermentation product, which utilizes adsorbent selective absorption fourth Alcohol, acetone and ethyl alcohol eliminate the purpose of Product inhibiton to realize, by suction-operated, effectively improve butanol, third after fermentation The concentration of ketone and ethyl alcohol reduces energy consumption.Currently, both at home and abroad to the report of butanol adsorbent mainly include active carbon, molecular sieve, Polyvinylpyrrolidone (PVP), diatomite, resin and bamboo charcoal etc..Wherein, the adsorption capacity with higher such as active carbon, bamboo charcoal, But adsorptive selectivity is poor, especially has higher adsorption capacity to the glucose in fermentation liquid, will lead to the loss of fermentation liquid. Because having ion exchangeable, tradable ion can exchange with certain ions in fermentation liquid, cause rear molecular sieve There is biological inconsistent problem during supervention ferment.PVP and resin have the effect of preferably adsorbing, but higher cost, prepare Journey is unfavorable for sustainable development using petrochemical industry synthetic route.It develops and has both high-adsorption-capacity, highly selective, at low cost The adsorbent of the features such as honest and clean, environmental-friendly has important practical significance for the sustainable development of biological butanol industry.
Lignin is the natural biomass macromolecule that reserves are only second to cellulose.Ladisch discovery lignin can adsorb Butanol, acetone and ethyl alcohol in solution, Griffith has reaffirmed that lignin has butanol by tracer method later There is certain adsorption capacity, and points out that lignin is expected the adsorbing separation for biological alcohol fuel.Although lignin is for giving birth to It is shown good application prospect when the adsorbing separation of object alcohol and potentiality, but its complicated structure and polydispersity lead to lignin Performance is inhomogenous, especially non-modified lignin, and application performance is unsatisfactory, limits answering for it to a certain extent With.Currently, mostly using chemical method, but chemical method high production cost greatly to the modification of lignin, process is relative complex, and may produce Raw secondary pollution.
Summary of the invention
It is an object of the present invention to be directed in the adsorption separation technology of current biological butanol fermentation product existing for adsorbent not Foot, provide a kind of raising lignin to butanol in ABE fermentation liquid, acetone, Ethanol Adsorption performance method.The invention first with Lignin is classified as water-soluble fraction and the insoluble fraction of water by water, then recycle ketones solvent by the insoluble lignin fraction of water again It is classified as the molten fraction of ketone and the insoluble fraction of ketone, it is finally obtained water is insoluble and the insoluble fraction of ketone is used in adsorbing separation fermentation liquid Butanol, acetone, ethyl alcohol.The dissolution stage division relates only to the dissolution classification of lignin, is not related to chemical modification, therefore have There are the advantages such as simple process and low cost.Water and ketones solvent for dissolving classification can be recycled by recycling, Any consumption and loss are not generated, therefore have many advantages, such as green, environmental protection.
A method of improving lignin to butanol, acetone, Ethanol Adsorption performance in ABE fermentation liquid, the method includes Following steps:
(1) water-soluble lignin lignin classification insoluble with water: lignin is mixed with distilled water, Sonication assisted treatment 2- Lower layer's solid after sedimentation and filtering is collected in 5min, sedimentation separation after stirring, filtering, and vacuum drying obtains the insoluble lignin of water;Its In, every 0.1-2L distilled water adds lignin 10-50g;
(2) the molten lignin of ketone lignin classification insoluble with ketone: the insoluble lignin of water that upper step obtains is filled with ketones solvent Dividing mixing, Sonication assisted treatment 2-5min is sufficiently stirred, sedimentation separation, filters, lower layer's solid after collecting sedimentation and filtering, Obtain the insoluble lignin of the insoluble ketone of water;Wherein every 0.1-2L ketone reagent adds the insoluble lignin 30-60g of water;
(3) the insoluble lignin of the insoluble ketone of the water obtained upper step is dried in vacuo 12-48h at 20-60 DEG C, bottles, sealing It saves.
The lignin raw material is corn alkali lignin, pine alkali lignin, Wheat Straw Lignin from Alkali Pulping, poplar alkali lignin Or bamboo pulp black liquor alkali lignin.
Ketone reagent is butanone, pentanone, acetone, cyclohexanone or hexanone in the step (2).
Lignin and distilled water incorporation time are 2-28h in the step (1).
The insoluble lignin of water and ketone reagent incorporation time are 2-24h in the step (2).
The sedimentation separation is natural subsidence or is centrifuged at a high speed that filter method is suction filtration or micro-filtration.
Compared with prior art, beneficial effects of the present invention:
The present invention proposes to carry out selective dissolution to lignin using water and organic solvent to obtain high-performance lignin Adsorbent can significantly improve lignin to the adsorption capacity of butanol, acetone, ethyl alcohol in fermentation liquid, help to solve biological fourth The Product inhibiton problem of alcohol fermentation technology.This method is a kind of physical and chemical process, is not related to chemical modification, therefore have preparation It is at low cost, easy to operate, the advantages that process is environmentally protective.Lignin can be improved to low concentration butanol, acetone, ethanol solution Absorption property improves yield to solve the problems, such as the Product inhibiton of biofermentation production butanol, reduces energy consumption.It is embodied in:
(1) adsorption capacity with higher, to butanol, acetone, ethyl alcohol saturated adsorption capacity respectively up to 198mg/g, 151.3mg/g, 98.5mg/g, lignin improves 19.3%, 30.2%, 53.2% respectively before relatively handling.
(2) rate of adsorption is fast.
(3) adsorption process has no toxic side effect, environmentally friendly, prepares that raw material sources are convenient extensively, and preparation cost is cheap.
(4) preparation process is simple, not high to equipment requirement, it is easy to accomplish industrialized production is effectively increased to hair Ferment method produces the adsorbance of the zymotic fluid product of butanol, reduces product inhibition.
Detailed description of the invention
Fig. 1 is the infared spectrum of the insoluble lignin adsorbent material of embodiment 1-3 Central Plains lignin ketone insoluble with water;
Fig. 2 is suction of the insoluble lignin adsorbent material of 4 Central Plains lignin of embodiment ketone insoluble with water to butanol in aqueous solution Attached thermoisopleth;
Fig. 3 is suction of the insoluble lignin adsorbent material of 5 Central Plains lignin of embodiment ketone insoluble with water to acetone in aqueous solution Attached thermoisopleth;
Fig. 4 is suction of the insoluble lignin adsorbent material of 6 Central Plains lignin of embodiment ketone insoluble with water to ethyl alcohol in aqueous solution Attached thermoisopleth;
Fig. 5 is the insoluble lignin adsorbent material of 7 Central Plains lignin of embodiment ketone insoluble with water to butanol in ABE fermentation liquid Adsorption isotherm;
Fig. 6 is the insoluble lignin adsorbent material of 8 Central Plains lignin of embodiment ketone insoluble with water to acetone in ABE fermentation liquid Adsorption isotherm;
Fig. 7 is the insoluble lignin adsorbent material of 9 Central Plains lignin of embodiment ketone insoluble with water to ethyl alcohol in ABE fermentation liquid Adsorption isotherm;
Fig. 8 is the insoluble lignin adsorbent material of the insoluble ketone of water in embodiment 10 to the absorption power of butanol, acetone and ethyl alcohol Learn curve.
Specific embodiment
Below by way of specific embodiment, the present invention will be described in more detail.Embodiment is only to a kind of theory of the invention It is bright, but not to limit the present invention.Embodiment is practical application example, and those skilled in the art are easy to It grasps and verifies.If making certain change on the basis of the present invention, then its essence is without departing from the scope of the present invention.
Embodiment 1:
It the described method comprises the following steps:
(1) water-soluble lignin lignin classification insoluble with water: corn alkali lignin 30g and distilled water 500ml is sufficiently mixed 20h is closed, 40KHz Sonication assisted treatment 2min is sufficiently stirred, sedimentation separation, 0.45 μm of membrane filtration, collects sedimentation and filtering Lower layer's solid afterwards, vacuum drying 20h obtain the insoluble lignin 17g of water.
(2) the molten lignin of ketone lignin classification insoluble with ketone: water insoluble lignin 17g and acetone solvent 500ml is abundant 18h is mixed, 40KHz Sonication assisted treatment 3min is sufficiently stirred, sedimentation separation, 0.45 μm of membrane filtration, collects sedimentation and mistake Lv Hou lower layer solid obtains the insoluble lignin of the insoluble ketone of water.
(3) the insoluble lignin of the insoluble ketone of product water obtains 6 grams after being dried in vacuo 15h at 50 DEG C, and bottling is sealed.
Embodiment 2:
It the described method comprises the following steps:
(1) water-soluble lignin lignin classification insoluble with water: poplar lignin 50g and distilled water 500ml are sufficiently mixed 16h, Sonication assisted treatment 3min, is sufficiently stirred, sedimentation separation, 0.45 μm of membrane filtration, collects lower layer after sedimentation and filtering Solid vacuum drying obtains the insoluble lignin 35g of water for 24 hours.
(2) the molten lignin of ketone lignin classification insoluble with ketone: water insoluble lignin 35g and butanone solvent 500ml is abundant 20h is mixed, Sonication assisted treatment 2min is sufficiently stirred, sedimentation separation, 0.45 μm of membrane filtration, after collecting sedimentation and filtering Lower layer's solid obtains the insoluble lignin of the insoluble ketone of water.
(3) the insoluble lignin of the insoluble ketone of product water obtains 15g after being dried in vacuo 18h at 45 DEG C, and bottling is sealed.
Embodiment 3:
It the described method comprises the following steps:
(1) water-soluble lignin lignin classification insoluble with water: Wheat Straw Lignin from Alkali Pulping 30g and distilled water 1000ml is sufficiently mixed 18h is closed, Sonication assisted treatment 3min is sufficiently stirred, sedimentation separation, 0.45 μm of membrane filtration, under collecting after sedimentation and filtering Layer solid vacuum drying 48h obtains the insoluble lignin 18g of water.
(2) the molten lignin of ketone lignin classification insoluble with ketone: water insoluble lignin 18g and ketones solvent 1000ml is abundant 15h is mixed, Sonication assisted treatment 3min is sufficiently stirred, sedimentation separation, 0.45 μm of membrane filtration, after collecting sedimentation and filtering Lower layer's solid obtains the insoluble lignin of the insoluble ketone of water.
(3) the insoluble lignin of the insoluble ketone of product water obtains 7g after being dried in vacuo 20h at 40 DEG C, and bottling is sealed.
The Fourier transform infrared spectroscopy pair of the insoluble ketone of water obtained by embodiment 1-3 insoluble lignin and lignin raw material According to figure as shown in Figure 1, having been carried out using Fourier Transform Infrared Spectrometer to log quality and the insoluble lignin of the insoluble ketone of water red Outer characterization obtains infrared spectrogram and characteristic peak ownership.If Fig. 1 finds out, the insoluble lignin of the insoluble ketone of water exists in infrared spectrum Hydroxyl at 3399cm-1, phenyl ring C=O, 1510cm-1,1426cm-1 at the CH of methylmethylene at 2936cm-1,1600cm-1 With nuclear skeleton fragrant at 1126cm-1, the C-H deformation vibration of methylmethylene at 1462cm-1, aromatic proton C-C at 1222cm-1 C-O is added to add C=O, the absorption of lignum-vitae phenolic aromatic proton is remarkably reinforced compared with log quality at 836cm-1, and at 2843cm-1 CH2 stretching vibration, the absorption of carboxyl weakens at 1700cm-1.Illustrate compared with lignin stock blend, the insoluble wood of the insoluble ketone of water The hydrophobic grouping of quality increases, and hydrophobic performance is stronger, therefore has better absorption property to butanol, acetone, ethyl alcohol in fermentation liquid.
Embodiment 4:
The insoluble lignin of the insoluble ketone of water adsorbs the application of butanol as adsorbent in aqueous solution, and step is, by embodiment 1 The insoluble lignin of the insoluble ketone of the water of middle preparation is added separately in the butanol aqueous solution of 1-50g/L, adsorbent and solution quality ratio It for 1:100, is mixed using concussion mode, temperature is 25 DEG C, and the time is 24 hours, after completing absorption, carries out separation of solid and liquid water outlet The insoluble lignin adsorbent of insoluble ketone, butanol concentration of aqueous solution after measurement absorption.
The insoluble lignin of the insoluble ketone of water is with lignin raw material to comparison diagram such as Fig. 2 of the adsorption isotherm of butanol.To fourth Alcohol adsorption capacity is obviously improved, and up to 198mg/g, improves 19.3% before being relatively classified.
Embodiment 5:
The insoluble lignin of the insoluble ketone of water adsorbs the application of acetone in aqueous solution, and step is the water that will be prepared in embodiment 1 The insoluble lignin of insoluble ketone is added separately in the aqueous acetone solution of 1-50g/L, and adsorbent and solution quality ratio are 1:100, is adopted It is mixed with concussion mode, temperature is 25 DEG C, and the time is 24 hours, and after completing absorption, it is insoluble to carry out the insoluble ketone of separation of solid and liquid water outlet Lignin adsorbent, aqueous acetone solution concentration after measurement absorption.
The insoluble lignin of the insoluble ketone of water is with lignin raw material to comparison diagram such as Fig. 3 of the adsorption isotherm of acetone.To third Ketone adsorption capacity is obviously improved, and up to 151.3mg/g, improves 30.2% before being relatively classified.
Embodiment 6:
The insoluble lignin of the insoluble ketone of water adsorbs the application of ethyl alcohol in aqueous solution, and step is the water that will be prepared in embodiment 1 The insoluble lignin of insoluble ketone is added separately in the ethanol water of 1-50g/L, and adsorbent and solution quality ratio are 1:100, is adopted It is mixed with concussion mode, temperature is 25 DEG C, and the time is 24 hours, and after completing absorption, it is insoluble to carry out the insoluble ketone of separation of solid and liquid water outlet Lignin adsorbent, ethanol water concentration after measurement absorption.
The insoluble lignin of the insoluble ketone of water is with lignin raw material to comparison diagram such as Fig. 4 of the adsorption isotherm of ethyl alcohol.To second Alcohol adsorption capacity is obviously improved, and up to 98.5mg/g, improves 53.2% before being relatively classified.
Embodiment 7:
The insoluble lignin of the insoluble ketone of water adsorbs the application of butanol in ABE fermentation liquid, and step is will to prepare in embodiment 2 The insoluble lignin of the insoluble ketone of water be added separately to (its in the aqueous solution that butanol concentration is the butanol of 1-50g/L, acetone, ethyl alcohol Middle butanol, acetone, ethyl alcohol mass ratio be 6:3:1), adsorbent and solution quality ratio are 1:100, mixed using concussion mode, Temperature is 25 DEG C, and the time is 24 hours, after completing absorption, carries out being separated by solid-liquid separation the insoluble lignin adsorbent of the insoluble ketone of water outlet, survey Surely butanol concentration in post-fermentation liquid is adsorbed.
The insoluble lignin of the insoluble ketone of water is such as schemed in ABE fermentation liquid with the comparison diagram of the adsorption isotherm of butanol in aqueous solution 5.Competitive Adsorption reduces the insoluble lignin of the insoluble ketone of water to the adsorbance of butanol in fermentation liquid, but competitive Adsorption phenomenon is not Obviously, 192.1mg/g is reached to the adsorbance of butanol in fermentation liquid.
Embodiment 8:
The insoluble lignin of the insoluble ketone of water adsorbs the application of acetone in ABE fermentation liquid, and step is will to prepare in embodiment 2 The insoluble lignin of the insoluble ketone of water be added separately to (its in the aqueous solution that acetone concentration is the butanol of 1-50g/L, acetone, ethyl alcohol Middle butanol, acetone, ethyl alcohol mass ratio be 6:3:1), adsorbent and solution quality ratio are 1:100, mixed using concussion mode, Temperature is 25 DEG C, and the time is 24 hours, after completing absorption, carries out being separated by solid-liquid separation the insoluble lignin adsorbent of the insoluble ketone of water outlet, survey Surely acetone concentration in post-fermentation liquid is adsorbed.
The insoluble lignin of the insoluble ketone of water is such as schemed in ABE fermentation liquid with the comparison diagram of the adsorption isotherm of acetone in aqueous solution 6.Competitive Adsorption reduces the insoluble lignin of the insoluble ketone of water to the adsorbance of acetone in fermentation liquid, but competitive Adsorption phenomenon is not Obviously, 149mg/g is reached to the adsorbance of acetone in fermentation liquid.
Embodiment 9:
The insoluble lignin of the insoluble ketone of water adsorbs the application of ethyl alcohol in ABE fermentation liquid, and step is will to prepare in embodiment 2 The insoluble lignin of the insoluble ketone of water be added separately to (fourth in the aqueous solution that concentration of alcohol is the butanol of 1-50g/L, acetone, ethyl alcohol Alcohol, acetone, ethyl alcohol mass ratio 6:3:1), adsorbent and solution quality ratio are 1:100, are mixed using concussion mode, temperature 25 DEG C, the time is 24 hours, after completing absorption, carries out being separated by solid-liquid separation the insoluble lignin adsorbent of the insoluble ketone of water outlet, after measurement absorption Concentration of alcohol in fermentation liquid.
The insoluble lignin of the insoluble ketone of water is such as schemed in ABE fermentation liquid with the comparison diagram of the adsorption isotherm of ethyl alcohol in aqueous solution 7.Competitive Adsorption reduces the insoluble lignin of the insoluble ketone of water to the adsorbance of ethyl alcohol in fermentation liquid, but competitive Adsorption phenomenon is not Obviously, 95.1mg/g is reached to the adsorbance of ethyl alcohol in fermentation liquid.
Embodiment 10:
Different time condition is lauched the adsorption experiment that the insoluble lignin of insoluble ketone adsorbs butanol in aqueous solution, and step is, The insoluble lignin of the insoluble ketone of the water prepared in embodiment 3 is added separately to containing butanol (18g/L), acetone (9g/L), ethyl alcohol In the aqueous solution of (3g/L), adsorbent and solution quality ratio are 1:100, are mixed using concussion mode, and temperature is 25 DEG C, the time It is 24 hours, after completing absorption, carries out being separated by solid-liquid separation the insoluble lignin adsorbent of the insoluble ketone of water outlet, respectively fourth after measurement absorption Alcohol, acetone, ethanol water concentration.
The curve of adsorption kinetics such as Fig. 8 of the insoluble lignin adsorbent material of the insoluble ketone of water to butanol, acetone and ethyl alcohol.It can See, to balance close after butanol adsorption reaction about 40min, then slowly rises, basically reach adsorption saturation after 50min.It is right Acetone adsorption reaction, close to balance, then slowly rises about after 37min, basically reaches adsorption saturation after 45min.To ethyl alcohol Adsorption reaction, close to balance, then slowly rises about after 30min, basically reaches adsorption saturation after 35min.Can water breakthrough it is insoluble The insoluble lignin adsorbent material of ketone is very fast to the rate of adsorption of butanol, acetone and ethyl alcohol.
Unaccomplished matter of the present invention is well-known technique.

Claims (4)

1. it is a kind of improve lignin to butanol in ABE fermentation liquid, acetone, Ethanol Adsorption performance method, it is characterized in that the side Method the following steps are included:
(1) water-soluble lignin lignin classification insoluble with water: lignin is mixed with distilled water, Sonication assisted treatment 2- Lower layer's solid after sedimentation and filtering is collected in 5min, sedimentation separation after stirring, filtering, and vacuum drying obtains the insoluble lignin of water;Its In, every 0.1-2L distilled water adds lignin 10-50g;
(2) the molten lignin of ketone lignin classification insoluble with ketone: the insoluble lignin of the water that upper step is obtained and ketone reagent are sufficiently mixed It closes, Sonication assisted treatment 2-5min is sufficiently stirred, sedimentation separation, filters, and collects lower layer's solid after sedimentation and filtering, obtains The insoluble lignin of the insoluble ketone of water;Wherein every 0.1-2L ketone reagent adds the insoluble lignin 30-60g of water;
(3) the insoluble lignin of the insoluble ketone of the water obtained upper step is dried in vacuo 12-48h at 20-60 DEG C, and bottling, sealing is protected It deposits;
The lignin raw material is corn alkali lignin, pine alkali lignin, Wheat Straw Lignin from Alkali Pulping, poplar alkali lignin or bamboo Starch black liquor alkali lignin;
Ketone reagent is butanone, pentanone, acetone, cyclohexanone or hexanone in the step (2).
2. improve as described in claim 1 lignin to butanol in ABE fermentation liquid, acetone, Ethanol Adsorption performance method, Feature is that lignin and distilled water incorporation time are 2-28h in the step (1).
3. improve as described in claim 1 lignin to butanol in ABE fermentation liquid, acetone, Ethanol Adsorption performance method, Feature is that the insoluble lignin of water and ketone reagent incorporation time are 2-24h in the step (2).
4. improve as described in claim 1 lignin to butanol in ABE fermentation liquid, acetone, Ethanol Adsorption performance method, Feature is that the sedimentation separation is natural subsidence or is centrifuged at a high speed, and filter method is suction filtration or micro-filtration.
CN201611005251.4A 2016-11-15 2016-11-15 A method of lignin is improved to butanol, acetone, Ethanol Adsorption performance in ABE fermentation liquid Active CN106362707B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201611005251.4A CN106362707B (en) 2016-11-15 2016-11-15 A method of lignin is improved to butanol, acetone, Ethanol Adsorption performance in ABE fermentation liquid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201611005251.4A CN106362707B (en) 2016-11-15 2016-11-15 A method of lignin is improved to butanol, acetone, Ethanol Adsorption performance in ABE fermentation liquid

Publications (2)

Publication Number Publication Date
CN106362707A CN106362707A (en) 2017-02-01
CN106362707B true CN106362707B (en) 2019-01-01

Family

ID=57894082

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201611005251.4A Active CN106362707B (en) 2016-11-15 2016-11-15 A method of lignin is improved to butanol, acetone, Ethanol Adsorption performance in ABE fermentation liquid

Country Status (1)

Country Link
CN (1) CN106362707B (en)

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2007945B1 (en) * 2006-03-29 2011-01-26 Virginia Tech Intellectual Properties, Inc. Cellulose-solvent-based lignocellulose fractionation with modest reaction conditions and reagent cycling
CN102864672B (en) * 2012-09-17 2015-06-24 北京林业大学 Method for extracting lignin

Also Published As

Publication number Publication date
CN106362707A (en) 2017-02-01

Similar Documents

Publication Publication Date Title
CN101863946B (en) Method for extracting high-content mogroside V from dried momordica grosvenori swingle
CN102614834B (en) Method for adsorbing and recovering heavy metals of lead and copper by persimmon tannin-containing metal adsorbent
CN102219866A (en) Method for extracting and separating ganoderma lucidum polysaccharide from ganoderma lucidum sporocarp
CN1243731C (en) Method of combined preparing alliin and galic polysaccharide
CN1263394C (en) Method of combined preparing garlic essential oil and garlic polysaccharide
CN102276679A (en) Method for extracting high-purity tea saponin from oil-tea-cake by decompression boiling
CN103657593B (en) A kind of method of sunflower seed shell biomass carbon adsorbent, preparation method and removal water Methylene Blue
CN103435721A (en) Method for extracting high-purity inulin from jerusalem artichoke by ultrasonic-complex enzyme method
CN104190370A (en) Preparation method of porous adsorbent for adsorbing heavy metals in marine protein enzymatic hydrolyzate
CN102093748B (en) Method for preparing radish red pigment homopolymer and radish proanthocyanidin from red-core radishes
CN102304554A (en) Method for producing gardenia red pigment with high color value
CN108272831A (en) The extracting method of Korean Needle polyphenol compound and its application
CN101912767B (en) Method for preparing modified furfural residue heavy metal adsorbent
CN113577165B (en) Method for extracting polyphenol from camellia japonica
CN106362707B (en) A method of lignin is improved to butanol, acetone, Ethanol Adsorption performance in ABE fermentation liquid
CN107266606A (en) The new technology of fucoidan is extracted in a kind of waste liquid from kelp processing
AU2020103503A4 (en) Boric acid adsorbent material and preparation method
CN104530274A (en) Gulonic acid adsorption separation method utilizing hyper-crosslinked resin
CN105642245B (en) A kind of preparation method of magnetic egg white/luffa sorbing material
CN110385105A (en) A kind of carried active carbon and preparation method thereof and device
CN113527383B (en) High-purity plant tannin prepared from industrial tannin extract and preparation method thereof
CN104262451A (en) Method for extracting holothurin from sea cucumber processing waste fluid
CN109180618A (en) A kind of decoloration process of andrographolide
CN108014176B (en) Method for purifying guava leaf triterpenes
CN112661975A (en) Method for extracting xylose, lignin and cellulose nanocrystals by using bamboo crushed materials

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant