CN101289682B - Process for preparing monosaccharide by using cellulose-containing raw material - Google Patents
Process for preparing monosaccharide by using cellulose-containing raw material Download PDFInfo
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Abstract
The invention provides a method of adopting material containing the cellulose to prepare monosaccharide, the method comprises the steps of exploding the material containing the cellulose via stream and zymohydrolyzing the obtained steam explosion product, wherein the water content of the material containing the cellulose is between thirty and sixty weight percent. According to the method of adopting material containing the cellulose to prepare the monosaccharide, the water content of the material containing the cellulose is strictly controlled around between thirty and sixty weight percent to guarantee that the water of the material containing the cellulose is changed to steam under the condition of steam explosion, the steam dashes out of the material containing the cellulose when pressure is relieved to destroy lignin sheath embedding the cellulose and semi cellulose in the material containing the cellulose thoroughly, so as to increase the proportion of the cellulose which can contact with enzyme in the material containing the cellulose and finally increase the productivity of the monosaccharide.
Description
Technical field
The invention relates to a kind of method for preparing monose, more specifically, is the method about the feedstock production monose that adopts cellulose.
Background technology
Prior art can be used the feedstock production monose of cellulose; Gained monose mainly is glucose; Glucose can be used for food, medicine industry, in the printing and dyeing tanning industry, can be used as reductive agent, and glucose commonly used is made reductive agent in industry of system mirror and the glass liner of a thermos flask silver plating process; Gained monose also comprises wood sugar, can make Xylitol through hydrogenation, as the non-caloric sweetener of food.Said monose also can pass through mikrobe (for example yeast) alcohol prepared by fermenting.
The raw material of said cellulose is generally root, stem and the leaf of plant, comprises stalk.Said stalk is remaining, stem and a leaf behind farm crop (being generally herbage) results seed or the fruit; Be mainly stem and leaf, as comprise the cereal grass of corn straw, jowar stalk, rice straw, wheat straw stalk, comprise stalk and the cotton stalk of the oilseed plant of beanstalk.Mierocrystalline cellulose, semicellulose and xylogen are combined closely through covalent linkage and/or non covalent bond in the stalk, and the three accounts for the 70-90 weight % of stalk dry-matter gross weight.The content of Mierocrystalline cellulose, semicellulose and xylogen can the difference to some extent with the different piece of the farm crop of different sources or farm crop in the stalk.
Mierocrystalline cellulose can be degraded into glucose under the effect of cellulase, semicellulose can be degraded into wood sugar under the effect of hemicellulase.But xylogen is a kind of non-polysaccharide material that is polymerized by phenyl-propane, thereby water insoluble, and is difficult to degraded.Since xylogen by the verivate of aromatic hydrocarbon with-C-C-key ,-the O-key is crosslinked in length and breadth; Side chain and semicellulose are with covalent bonds; Form fine and close network structure---xylogen sheath embedding Mierocrystalline cellulose and semicellulose; Thereby making cellulase and hemicellulase be difficult for contacting with semicellulose with Mierocrystalline cellulose, the result causes stalk also to be difficult to degraded.Therefore no matter be feedstock production monose with cellulose; Or feedstock production alcoholic acid saccharification step with cellulose; All need carry out pre-treatment to the raw material of cellulose; Pre-treatment is carried out in general employing steam explosion and/or acid hydrolysis, to destroy the embedding of xylogen to Mierocrystalline cellulose and semicellulose.
For example CN1629321A discloses a kind of method of utilizing stalk plant extract system ethanol with glucose and/or wood sugar; This method comprises at room temperature; According to the stalk plant: the weight ratio of dilute acid soln is that the ratio of 1:4.5-8.5 is mixed stalk with dilute acid soln; Be warmed up to 90-100 ℃ of constant temperature then, the semicellulose in the hydrolyzing straw extracts sugar soln, sugar soln alcohol prepared by fermenting fast.This method also is included in and further adds the Mierocrystalline cellulose that does not dissolve in the cellulase hydrolysis sugar soln in the said sugar soln; The add-on of said cellulase and the weight ratio of stalk are 1:10-1:100; Adjust pH is at 4.5-5.5; Be warmed up to 45-60 ℃ then, obtain containing the aqueous solution of glucose and wood sugar, alcohol prepared by fermenting.
Though acid hydrolysis can destroy xylogen, also can destroy Mierocrystalline cellulose, reduce the productive rate of glucose then, and also need add after the acid hydrolysis in a large amount of alkali and could carry out enzymolysis and fermentation.Therefore more preferably only accomplish preprocessing process, reach the embedding effect of xylogen that destroy Mierocrystalline cellulose and semicellulose through steam explosion.
For example, Zhang Xuefeng and orchid are kindly helped secure the success of in document " to the introduction of straw biomass to alcohol conversion process ", wine brewing, the 29th the 4th phase of volume; The 37-38 page or leaf discloses a kind of method of utilizing straw to produce alcohol in July, 2002, and this method comprises to be removed corn straw after the stone deironing cleans; Cut into 1.5 centimetres segment, water logging 40 minutes feeds 2.5 MPa steam, is incubated 8 minutes; Pressure release, the steam explosion products of washing 1/10th, and this wooden enzyme produces cellulase in said 1/10th steam explosion products, cultivating, and the gained culture is mixed with other 9/10ths steam explosion products; Be incubated 50 ℃ of hydrolysis 24 hours, through filtering 6% liquid glucose, mineral membrane is condensed into the liquid glucose more than 20%, adds Xiu Hata yeast (0.8-1.2 hundred million/milliliter); Fermented 24 hours, and produced wine part 10%, distill 99.5% alcohol.
But in the method and feedstock production alcoholic acid saccharification step of existing feedstock production monose with cellulose with cellulose; The steam explosion pre-treatment destroys inadequately the xylogen sheath of embedding Mierocrystalline cellulose and semicellulose in the raw material of cellulose, thereby causes the productive rate of monose low.
Summary of the invention
The objective of the invention is to overcome the low shortcoming of method monose productive rate of the feedstock production monose of existing employing cellulose, the method for the feedstock production monose of the high usefulness cellulose of a kind of monose productive rate is provided.
During the raw material of prior art steam blasting cellulose-containing, the raw material that it has been generally acknowledged that said cellulose is corn straw for example, fully water logging; Can obtain the effect of better steam explosion, because fully water logging can make the raw material of said cellulose for example contain a large amount of water in corn straw inside, when steam explosion; The raw material of the said cellulose for example inner water of corn straw can be gasificated into water vapor; For example go out corn straw inside by the raw material of said cellulose during pressure release, with the raw material that fully the destroys said cellulose from inside to outside xylogen sheath of corn straw embedding Mierocrystalline cellulose and semicellulose for example, such as (Zhang Xuefeng, orchid are kindly helped secure the success of in above-mentioned " to the introduction of straw biomass to alcohol conversion process "; Wine brewing; The 29th the 4th phase of volume, 37-38 page or leaf, in July, 2002) middle disclosed method; Need just carry out steam explosion with the corn straw water logging after 40 minutes.But contriver of the present invention is surprised to find that; After 40 minutes, the water cut of corn straw is all up to more than the 80 weight % with corn straw (sapphire rice stalk and the dry corn straw) water logging of various water cut, and the water cut of the raw material of the cellulose of steam explosion is low; It is no doubt bad for example to be lower than 30 weight %; If but the water cut of the raw material of cellulose, as be higher than 60 weight %, also can reduce the alcoholic acid yield.
The invention provides a kind of method that adopts the feedstock production monose of cellulose, this method comprises the raw material of steam blasting cellulose-containing, the steam explosion products that enzymolysis obtains, and wherein, the water cut of the raw material of said cellulose is 30-60 weight %.
According to the method for preparing monose of the present invention; The strict water cut of controlling the raw material of the cellulose that is used for steam explosion is 30-60 weight %; Can guarantee under the steam explosion condition, to make the inner aqueous vapor of raw material of cellulose to change into water vapor; Water vapour is gone out by the raw material inside of cellulose when pressure release; Fully destroy the xylogen sheath of embedding Mierocrystalline cellulose and semicellulose in the raw material of cellulose, the cellulose ratios that can contact with enzyme in the raw material with the increase cellulose, thus can improve the productive rate of monose.For example, under all identical situation of other steam explosion condition, the monose productive rate of embodiment 1 reaches 41.3%, and the monose productive rate of Comparative Examples 1 is merely 34.5%, and increase rate is up to 19.7%.
Description of drawings
Fig. 1 is the electron scanning micrograph of natural corn stalk;
Fig. 2 is the electron scanning micrograph according to stalk behind the method steam explosion of Comparative Examples 1 of the present invention;
Fig. 3 is the electron scanning micrograph according to stalk behind the method steam explosion of Comparative Examples 2 of the present invention;
Fig. 4 is the electron scanning micrograph according to stalk behind the method steam explosion of the embodiment of the invention 1.
Embodiment
The method of the feedstock production monose of employing cellulose provided by the invention comprises the raw material of steam blasting cellulose-containing, the steam explosion products that enzymolysis obtains, and wherein, the water cut of the raw material of said cellulose is 30-60 weight %, is preferably 35-50 weight %.
The raw material water content difference of the cellulose of different sources is very big; Water content difference such as the corn straw raw material of different times purchase is just very big; The fresh straw water cut that harvesting is no more than a week reaches more than the 80 weight %, but possibly have only 10% through the air-dry storage stalk water cut of airing.Existing method all adopts the similarity condition water logging to handle for the raw material of the cellulose of different moisture content without exception; Cause the water cut of raw material of cellulose excessive; Under the steam explosion condition; The inner moisture of the raw material of cellulose is gone out with liquid form during pressure release, does not reach the effect of the xylogen sheath of embedding Mierocrystalline cellulose and semicellulose in the raw material that destroys cellulose from inside to outside.
According to method provided by the invention, can obtain the raw material that water cut is the cellulose of 30-60 weight % through variety of way.The raw material of the different batches cellulose that there are differences for water cut can carry out different processing, such as for the high stalk of water cut, can 45-90 ℃ of oven dry part moisture, and make it water cut and be reduced to 30-60 weight %; For the low stalk of water cut, can adopt control water logging time method, the water cut that increases stalk is to 30-60 weight %; Just in time at stalk, can directly carry out steam explosion for water cut to 30-60 weight %.The water cut of the raw material of the preferred said cellulose that is used for steam explosion is 35-50 weight %.Only if specified otherwise; The water cut of the raw material of the said cellulose of wood invention all is meant the initial weight W1 of cellulose containing raw material and under 70-100 ℃, dries poor to the dried meter weight W 2 of the cellulose containing raw material of constant weight; With the weight percent of the initial weight W1 of cellulose containing raw material, i.e. water cut (weight %)=(W1-W2)/W1 * 100%.
Method according to the feedstock production monose with cellulose according to the invention; Can adopt the conventional steam explosion condition of prior art to accomplish steam explosion to the raw material of cellulose; For example; The temperature of said steam explosion can be 180-200 ℃, and the pressure of said steam explosion can be the 1.4-2.0 MPa, and holding time of said steam explosion pressure can be 3-7 minute.More preferably the temperature of said steam explosion is 185-195 ℃, and the pressure of said steam explosion is the 1.5-1.6 MPa, and holding time of said steam explosion pressure is 4-5 minute.Under above-mentioned steam explosion condition, can both fully destroy the xylogen sheath of stalk embedding Mierocrystalline cellulose and semicellulose, realize the object of the invention.
Said enzymolysis step can be accomplished through this area method commonly used, and such as in steam explosion products, adding microbes producing cellulase and/or enzyme, insulation is accomplished under the growth temperature of microbes producing cellulase and/or the great-hearted temperature of enzyme.Said microbes producing cellulase be can eccrine fiber the microbes producing cellulase of plain enzyme.Said enzyme comprises cellulase.
Because microorganism growth can produce by product; Therefore the preferred enzyme that directly adds, the consumption of said enzyme is The more the better, from cost consideration; Preferably with the dry weight basis of the raw material of every gram cellulose; The consumption of said cellulase is the 8-20 enzyme activity unit, more preferably with the dry weight basis of the raw material of every gram cellulose, and the 10-15 enzyme activity unit.The enzyme activity of cellulase according to the invention is according to American National renewable energy source laboratory (National Renewable Energy Laboratory; NREL) standard method that provides---cellulase activity is measured NREL LAP-006 and is measured; The enzyme activity unit of said cellulase is under the condition determination of this standard method regulation, and transforming 1 gram Whatman No.1 filter paper in 1 minute is the micrograms of the required enzyme of glucose.The temperature of said enzymolysis can be any optimum temperature of cellulase, is generally 45-55 ℃, more preferably 48-52 ℃.The longer the better on the time theory of said enzymolysis, considers plant factor, and the time of preferred said enzymolysis is 25-48 hour, more preferably 30-40 hour.The pH value of said enzymolysis can be generally 3.0-7.0 for the righttest any action pH of cellulase, and more preferably the pH value is 4.5-5.5.Because the fluctuation of pH value is little in the enzymolysis process; Therefore the pH value of said enzymolysis can be regulated before adding enzyme according to this area method commonly used; For example earlier steam explosion products and water or substratum (are enzyme-addedly generally mixed with water; Add microbes producing cellulase generally with the substratum of this mikrobe) mix, the solid content that generally makes the gained mixture is 50-70 weight %, according to the pH value of gained mixture; The mixture pH regulator that to treat enzymolysis with sulphuric acid soln or sodium hydroxide more preferably is adjusted to the pH value and is 4.5-5.5 to 3.0-7.0.
Said cellulase is a prozyme, comprises C at least
1The plain enzyme of fiber type, C
XThe plain enzyme of fiber type and three kinds of enzymes of cellose.
C
1Enzyme can make the crystalline Mierocrystalline cellulose change amorphous Mierocrystalline cellulose into.
C
XThe plain enzyme of fiber type is divided into C again
X1Plain enzyme of fiber type and C
X2Two kinds of the plain enzymes of fiber type.C
X1The plain enzyme of fiber type is the endo-type cellulase, can be from the plain intramolecular action of hydration amorphous cellulose in β-1, and the 4-glycosidic link generates cellodextrin and cellobiose.C
X2The plain enzyme of fiber type is a kind of circumscribed-type cellulase, can act on β-1 from the non-reducing end of hydration non-cellulose molecule, and the 4-glycosidic link cuts off β-1 one by one, and the 4-glycosidic link generates glucose.
Cellose then acts on cellobiose, makes the cellobiose enzymolysis generate glucose.
The enzyme that preferred said enzymolysis uses also comprises hemicellulase.Because hemicellulase is degraded into water-soluble wood sugar with semicellulose; So the enzyme that enzymolysis uses comprises hemicellulase; Exposed fibers is plain more fully on the one hand; Increase the contact probability of Mierocrystalline cellulose and cellulase, semicellulose degraded product wood sugar also is important monose product on the other hand.With the dry weight basis of the raw material of every gram cellulose, the consumption of said hemicellulase is the 4.4-8.8 enzyme activity unit.
The enzyme activity unit of hemicellulase according to the invention (U) is under 50 ℃, pH=4.8 condition, and it is that 1 weight % xylan solution produces the required enzyme amount of 1 microgram reducing sugar (in wood sugar) that PM decomposes concentration.
The vigor of hemicellulase according to the invention refers to the unit of activity that every gram hemicellulase is had.It is that hydrolysis 1 weight % xylan produces reducing sugar (in wood sugar) under 4.8 the condition at 50 ℃, pH that the vigor of said hemicellulase utilizes hemicellulase; Gained reducing sugar and excessive 3; Color reaction takes place in 5-dinitrosalicylic acid (DNS), records the proportional mensuration of growing amount of the absorbance value and the reducing sugar (in wood sugar) of reaction solution 550 nanometers with spectrophotometer.Concrete measuring method is following:
Accurately take by weighing 1.000 gram xylans, dissolve, use deionized water constant volume to 100 milliliter then, obtain 1 weight % xylan solution with the 0.1 mol acetate-sodium acetate buffer of 0.5 milliliter of pH=4.8;
Take by weighing 30 the gram Rochelle salts put into 500 milliliters of Erlenmeyer flasks, add 16 the gram NaOH after, add 50 ml deionized water; Speed heating in water bath to solid matter with 5 ℃/minute dissolves, and adds 1 gram, 3,5-dinitrosalicylic acid; To dissolving, be cooled to room temperature, be settled to 100 milliliters with deionized water; Can get 3,5-dinitrosalicylic acid (DNS) solution;
Wood sugar is dried to constant weight for 80 ℃, accurately take by weighing 1.000 grams and be dissolved in 1000 ml waters, it is anticorrosion to add 10 milligrams of sodiumazide, obtains the normal wood sugar soln of 1 mg/ml;
Accurately take by weighing 1.000 gram solid hemicellulases or pipette 1 milliliters of liquid hemicellulase stoste; 0.1 mol acetate-sodium acetate buffer dissolving with 0.5 milliliter of pH=4.8; Use deionized water constant volume to 100 milliliter then, obtain diluting 100 times enzyme liquid to be measured;
Respectively will be in 50 ℃ of heating in water bath 2 milliliters of wood sugar gradient standardized solution (0.1 mg/ml, 0.2 mg/ml, 0.3 mg/ml, 0.4 mg/ml and 0.5 mg/ml of 60 minutes; Said wood sugar gradient standardized solution is mixed with the normal wood sugar soln of deionized water and 1 mg/ml) or deionized water (wood sugar blank); With 2 milliliters of DNS mixing boiling water baths 5 minutes; After the cooling, 15 milliliters of deionized water constant volumes, with the absorbance value of spectrophotometer wood sugar gradient standardized solution after distinguishing assaying reaction under 550 nanometers; With the absorbance value is X-coordinate, and xylose concentration is an ordinate zou drawing standard curve.Can get regression equation y=bx+a by this typical curve, wherein, x is an absorbance value, and y is an xylose concentration, and a is the intercept of gained straight-line equation, and b is the slope of gained straight-line equation;
Get the 0.1 mol acetate-sodium acetate buffer (xylan blank) of 0.2 milliliter of enzyme liquid to be measured and 1.8 milliliters of said 1 weight % xylan solutions or pH=4.8, according to the step test light absorption value identical with above-mentioned wood sugar gradient standardized solution.And according to the vigor of computes hemicellulase:
X is the absorbance value of enzyme liquid to be measured in the formula; B is consistent to b in the regression equation of absorbance value and a with xylose concentration with a; N is the extension rate of enzyme, 60 be expressed as enzymatic reaction time be 60 minutes, 5 for the sampling multiple (from 1 milliliter of enzyme liquid to be measured, having taken out 0.2 milliliter here tests).
Can determine the vigor of concrete hemicellulase according to aforesaid method, and then calculate the consumption of hemicellulase.
In addition, the pressure and temperature of steam explosion can be sterilized, and pollutes the toxin of the enzyme activity that exerts an influence for preventing in enzymolysis process assorted bacterium (mainly being bacterium), preferably before enzymolysis, adds the bacteria antibiotic such as industrial penicillium mould.With every milliliter of enzymolysis solution is benchmark, and said antibiotic add-on is a 1-10 unit.Said enzymolysis solution comprises steam explosion products, enzyme and water.
Because under the high-temperature and high-pressure conditions of steam explosion; The raw material of cellulose can produce the inhibition such as furfural, furans; Said inhibition can reduce the activity of the vigor and the microbes producing cellulase of enzyme; Therefore said method also is included in after the raw material of steam blasting cellulose-containing, before the steam explosion products that enzymolysis obtains, washes said steam explosion products.Said washing is that steam explosion products is mixed with water, stirs, and spinning steam explosion products then owing to above-mentioned inhibition is prone to be dissolved in the water, thereby can be removed inhibition through washing from steam explosion products.The temperature of said washing is high more, and is can the dissolved inhibition many more, considers energy consumption, and the temperature of preferred said washing is 60-90 ℃, more preferably 60-80 ℃.Because the water that washing is added is many more; The inhibition that then dissolves is also many more; But consider the energy consumption of spinning, preferably with the dry weight basis of the said cellulose of every gram, the amount of water of said washing is the 2-10 gram; More preferably with the dry weight basis of the raw material of every gram cellulose, the amount of water of said washing is the 2-3 gram.
Owing to may contain sandstone impurity and iron contamination in the raw material of cellulose such as the corn straw; Can cause damage to steam explosion equipment; Therefore the present invention prepares the alcoholic acid method; Can comprise the existing stone deironing routine operation that removes, such as with the raw material of " wind send " cellulose and the method for attraction.In the method, sandstone can not be delivered in the steam explosion equipment by wind because quality is big, iron contamination since the attraction of magnet can not get in the steam explosion equipment with raw material yet, thereby can accomplish except that the stone deironing.In addition; Because the raw material of cellulose itself is entangled with and the occluding device pipeline easily; Therefore the size of the raw material of preferred said cellulose is 0.2-1 centimetre of a 0.5-3 cm x 0.2-1 cm x, and more preferably the size of the raw material of said cellulose is 0.5-1 centimetre of a 1-2 cm x 0.4-0.6 cm x.
Monose in the enzymolysis product can be through sugar industry method separation and purification commonly used.For example will remove the solid matter (raw material of the cellulose of for example not degraded) in the enzymolysis product through filtration, centrifugation method.Collect filtrating or supernatant, evaporation is removed the portion water branch and is obtained the supersaturation syrup that contents of monosaccharides is 60-65 weight %.In the vacuum crystallization jar, through transpiring moisture the monose crystallization is separated out, crystal and syrup form massecuite; When the crystal volume meets the requirements, massecuite is transferred to crystallizer from the vacuum crystallization jar, cooling is further separated out uncrystallized monose gradually.Carry out solid-liquid separation with whizzer, crystallization monose and molasses get product.Molasses are repeated said process crystallization 2-4 time, can fully extract monose.Crystallisation process can adopt nature graining method, stimulate graining method and nucleus graining method graining, preferably in syrup, adds crystallization with the nucleus graining method graining of kind of paste as crystal seed.
The present invention will be described in more detail below in conjunction with embodiment.
Embodiment 1
Present embodiment explanation the present invention is with the method for the feedstock production monose of cellulose.
(1) steam explosion
Test corn straw raw material as shown in Figure 1; The water cut that records corn straw according to above-mentioned method is 20 weight %; Raw material is cut into the segment of 0.5 centimetre of 1.5 cm x, 0.2 cm x; With vertical steeping cell (the auspicious mechanical ltd in river in Shangdong Province, Shandong) and weight is after 1/3rd water of said corn straw raw material weight mixes, and can get the corn straw of water cut 40 weight %.Getting 1000 gram water cut is the corn straw of 40 weight %, under 195 ℃, keeps 5 minutes with the pressure of 1.6 MPas, and steam explosion is accomplished in pressure release then.The water of gained steam explosion products and 70 ℃ was mixed 30 minutes according to weight ratio 1:3; Use LW400 type horizontal screw centrifuge (Zhangjiagang Huada Centrifugal Manufacturing Co., Ltd.) under 900 rev/mins of rotating speeds, to carry out solid-liquid separation then, obtain 2000 gram solid steam explosion products (water cut is 70 weight %) altogether.
The mensuration of Mierocrystalline cellulose gross weight and semicellulose gross weight in the gained solid steam explosion products:
Get the steam explosion products of 5 grams after the said washing and under 45 ℃, dry to constant weight 1.5 grams, 300.0 milligrams of this dried steam explosion products of weighing are positioned in heavy 80 100 milliliters of dry Erlenmeyer flasks restraining.Add the sulphuric acid soln that 3.00 ml concns are 72 weight % to said Erlenmeyer flask, stirred 1 minute.Then Erlenmeyer flask was heated 60 minutes in 30 ℃ of water-baths, whenever stirred once to guarantee even hydrolysis at a distance from 5 minutes.Water-bath makes the vitriolic concentration dilution to 4 weight % with deionized water after finishing.Filter the steam explosion products acid hydrolysis liquid after the said dilution with B, obtain altogether filtrating 84 milliliters.20 milliliters of filtratings are transferred in the triangular flask of 50 milliliters of dryings.Use 2.5 gram lime carbonate to regulate this pH value of filtrate to 5.5, left standstill 5 hours, collect supernatant liquid.0.2 the supernatant liquid that the micron membrane filtration is collected, the filtrating of gained supernatant liquid is analyzed with Biorad Aminex HPX-87P performance liquid chromatography (HPLC).HPLC condition: sample size 20 microlitres; Moving phase is 0.2 micron membrane filtration, and the HPLC ultrapure water of the sonic oscillation degassing; Flow velocity is 0.6 ml/min; Column temperature 80-85 ℃; Detector temperature 80-85 ℃; Detector is a refractive index detector; Be 35 minutes working time.With D-(+) glucose of 0.1-4.0 mg/ml concentration range and 0.1-4.0 mg/ml concentration range D-(+) wood sugar as standard model.HPLC analyzes and to obtain that glucose concn is 1.62 mg/ml in the steam explosion products acid hydrolysis liquid; The steam explosion products acid hydrolysis that calculating can get after the said washing of 1 gram can obtain the glucose that weight is 0.136 gram; Because being the sulphuric acid soln of 72 weight %, concentration can the Mierocrystalline cellulose of the product of steam explosion all be hydrolyzed into glucose; Therefore the weight of gained glucose is 1.11 times of cellulosic weight in the steam explosion products; Cellulose 0.122 gram in the steam explosion products after the i.e. said washing of 1 gram then is total to cellulose 245 grams in the 2000 gram steam explosion products.HPLC analyzes and to obtain that xylose concentration is 0.38 mg/ml in the steam explosion products acid hydrolysis liquid; The steam explosion products acid hydrolysis that calculating can get after the said washing of 1 gram can obtain the wood sugar that weight is 0.0319 gram; Because being the sulphuric acid soln of 72 weight %, concentration can semicellulose in the product of steam explosion all be hydrolyzed into wood sugar; Therefore the weight of gained wood sugar is 1.11 times of weight of semicellulose in the steam explosion products; Promptly contain semicellulose 0.028 gram in the 1 gram steam explosion products, then contain semicellulose 56 grams altogether in the 2000 gram steam explosion products.
(2) enzymolysis
With remaining washing steam explosion products behind step (1) sampling and testing, mix with 1000 gram water, regulate pH value to 5.0; After being heated to 50 ℃; With the dry weight basis of every gram stalk, add the cellulase (jade of the He family Bioisystech Co., Ltd) of 20 enzyme activity units, and be incubated 40 hours down at 50 ℃.Enzymolysis product is filtered with B, 20 milliliters of filtratings are transferred in 50 milliliters of triangular flasks of exsiccant, left standstill 5 hours, collect supernatant liquid.0.2 the supernatant liquid that the micron membrane filtration is collected, according to the said performance liquid condition of step (1), the glucose of measuring and calculating in the enzymolysis product 248 restrains totally.The glucose weight that said enzymolysis obtains promptly totally 223.4 is restrained by the cellulosic weight of enzymolysis in the steam explosion products divided by 1.11, and according to computes cellulose conversion rate and monose productive rate, calculation result is seen table 1.
Cellulose conversion rate=100% * by the cellulosic weight of enzymolysis/cellulosic gross weight
Glucose weight/stalk dry weight that monose productive rate=100% * enzymolysis obtains
Comparative Examples 1
The method of the feedstock production monose of the usefulness cellulose of this Comparative Examples explanation prior art.
Method according to embodiment 1 prepares monose, and different is that (Zhang Xuefeng, orchid are kindly helped secure the success of, wine brewing according to document " to the introduction of straw biomass to alcohol conversion process "; The 29th the 4th phase of volume; The 37-38 page or leaf, in July, 2002) disclosed method, the corn straw raw material was soaked in water earlier before steam explosion 40 minutes; The water cut that records the corn straw raw material after the immersion reaches 83 weight %, and the result sees table 1.
Comparative Examples 2
Method according to embodiment 1 prepares monose, and different is that the use water cut is that 20 weight % corn straws directly carry out steam explosion, and the result sees table 1.
The electron microscopic observation result:
Amplify 1000 times of steam explosion products of observing Comparative Examples 1, Comparative Examples 2 and embodiment 1 with the JSM-35CF ESEM, the result is respectively like Fig. 2, Fig. 3 and shown in Figure 4.As can beappreciated from fig. 2, because stalk inside does not have moisture can be gasificated into water vapor, so steam explosion can not fully destroy stalk from inside to outside; As can beappreciated from fig. 3, the effect of Comparative Examples 1 corn straw steam explosion and bad, Mierocrystalline cellulose still is pencil, and cellulose surface is residual that the xylogen sheath arranged; And the steam explosion effect of embodiment 1 as shown in Figure 4 is fine, can see the free Mierocrystalline cellulose.
Embodiment 2
Present embodiment explanation the present invention prepares the method for monose.
(1) steam explosion
Getting 1000 gram water cut is the corn straw of 50 weight %; Be cut into the segment of 0.8 centimetre of 1.3 cm x, 0.4 cm x, under 190 ℃, kept 4 minutes pressure release then with the pressure of 1.8 MPas; Accomplish steam explosion, obtain 1200 gram steam explosion products (water cut is 60 weight %) altogether.
Analyze the method for the steam explosion products of sulphuric acid hydrolysis according to the said HPLC of embodiment 1, record in the 1200 gram steam explosion products cellulose 210 grams altogether, semicellulose 60 grams.
(2) enzymolysis
With remaining steam explosion products behind step (1) sampling and testing, mixes with 400 gram water, regulate pH value to 6.0, be heated to 55 ℃ after, with the dry weight basis of every gram stalk, add the cellulase of 15 enzyme activity units, and descend to be incubated 30 hours at 55 ℃.Enzymolysis product is filtered with B, 20 milliliters of filtratings are transferred in the triangular flask of 50 milliliters of dryings, left standstill 5 hours, collect supernatant liquid.0.2 the supernatant liquid that the micron membrane filtration is collected, according to the said performance liquid condition of embodiment 1 step (1), the glucose of measuring and calculating in the enzymolysis product 198.1 restrains totally.The glucose weight that said enzymolysis obtains promptly totally 178.5 is restrained by the cellulosic weight of enzymolysis in the steam explosion products divided by 1.11, and according to computes cellulose conversion rate and monose productive rate, calculation result is seen table 1.
Cellulose conversion rate=100% * by the cellulosic weight of enzymolysis/cellulosic gross weight
Glucose weight/stalk dry weight that monose productive rate=100% * enzymolysis obtains
Embodiment 3
The method of the present embodiment explanation feedstock production monose with cellulose of the present invention.
(1) steam explosion
Getting 1000 gram water cut is the corn straw of 35 weight %, is cut into the segment of 0.7 centimetre of 1.2 cm x, 0.4 cm x, under 200 ℃, keeps 6 minutes with the pressure of 1.7 MPas, and steam explosion is accomplished in pressure release then.The water of gained steam explosion products and 75 ℃ was mixed 50 minutes according to weight ratio 1:2.5; Use LW400 type horizontal screw centrifuge (Zhangjiagang Huada Centrifugal Manufacturing Co., Ltd.) under 900 rev/mins of rotating speeds, to carry out solid-liquid separation then, obtain 2000 gram solid steam explosion products (water cut is 70 weight %) altogether.
Analyze the method for the steam explosion products of sulphuric acid hydrolysis according to the said HPLC of embodiment 1, record in the 2000 gram steam explosion products cellulose 260 grams altogether, semicellulose 78 grams.
(2) enzymolysis
With remaining washing steam explosion products behind step (1) sampling and testing; Mix with 1000 gram water; Regulate pH value to 4.0, be heated to 45 ℃ after, with the dry weight basis of every gram stalk; Add the cellulase of 18 enzyme activity units and the hemicellulase of 6.0 enzyme activity units (Beijing chemical reagents corporation), and be incubated 35 hours down at 45 ℃.Enzymolysis product is filtered with B, 20 milliliters of filtratings are shifted as in the dry 50 milliliters triangular flask, left standstill 5 hours, collect supernatant liquid.0.2 the supernatant liquid that the micron membrane filtration is collected, according to the said performance liquid condition of embodiment 1 step (1), the glucose of measuring and calculating in the enzymolysis product 256.6 restrains totally, and wood sugar is totally 62.5 grams.The glucose weight that said enzymolysis obtains is divided by 1.11; Be totally 231.1 to be restrained by the cellulosic weight of enzymolysis in the steam explosion products; The wood sugar weight that said enzymolysis obtains is divided by 1.11; Be totally 54.8 to be restrained by the weight of the semicellulose of enzymolysis in the steam explosion products, according to computes cellulose conversion rate, semicellulose transformation efficiency and monose productive rate, calculation result is seen table 1.
Cellulose conversion rate=100% * by the cellulosic weight of enzymolysis/cellulosic gross weight
Semicellulose transformation efficiency=100% * by the gross weight of the weight/semicellulose of the semicellulose of enzymolysis
Monose productive rate=100% * (the wood sugar weight that glucose weight+enzymolysis that enzymolysis obtains obtains)/stalk dry weight
Embodiment 4
The method of the present embodiment explanation feedstock production monose with cellulose of the present invention.
(1) steam explosion
Getting 1000 gram water cut is the corn straw of 55 weight %, is cut into the segment of 0.8 centimetre of 2.0 cm x, 0.6 cm x, under 190 ℃, keeps 7 minutes with the pressure of 1.55 MPas, and steam explosion is accomplished in pressure release then.The water of gained steam explosion products and 65 ℃ was mixed 40 minutes according to weight ratio 1:2; Use LW400 type horizontal screw centrifuge (Zhangjiagang Huada Centrifugal Manufacturing Co., Ltd.) under 900 rev/mins of rotating speeds, to carry out solid-liquid separation then, obtain 1800 gram solid steam explosion products (water cut is 78 weight %) altogether.
Analyze the method for the steam explosion products of sulphuric acid hydrolysis according to the said HPLC of embodiment 1, record in the 1800 gram steam explosion products cellulose 184.5 grams altogether, semicellulose 56.2 grams.
(2) enzymolysis
With remaining washing steam explosion products behind step (1) sampling and testing, mixes with 800 gram water, regulate pH value to 3.5, be heated to 50 ℃ after, with the dry weight basis of every gram stalk, add the cellulase of 10 enzyme activity units, and descend to be incubated 48 hours at 50 ℃.Enzymolysis product is filtered with B, 20 milliliters of filtratings are transferred in the triangular flask of 50 milliliters of dryings, left standstill 5 hours, collect supernatant liquid.0.2 the supernatant liquid that the micron membrane filtration is collected, the glucose of measuring and calculating in the enzymolysis product according to the said performance liquid condition of embodiment 1 step (1) 178.8 restrains totally.The glucose weight that said enzymolysis obtains promptly totally 161.1 is restrained by the cellulosic weight of enzymolysis in the steam explosion products divided by 1.11, and according to computes cellulose conversion rate and monose productive rate, calculation result is seen table 1.
Cellulose conversion rate=100% * by the cellulosic weight of enzymolysis/cellulosic gross weight
Glucose weight/stalk dry weight that monose productive rate=100% * enzymolysis obtains
Table 1
| Embodiment or Comparative Examples | Embodiment 1 | Comparative Examples 1 | Comparative Examples 2 | Embodiment 2 | Embodiment 3 | Embodiment 4 |
| Cellulose conversion rate (%) | 91.2 | 76.1 | 74.5 | 85 | 88.9 | 87.3 |
| Semicellulose transformation efficiency (%) | - | - | - | - | 70.3 | - |
| Monose productive rate (%) | 41.3 | 34.5 | 33.8 | 39.6 | (49.1 glucose 39.5 wood sugars 9.6) | 39.7 |
Can find out that from table 1 the method cellulose conversion rate of the embodiment of the invention and monose productive rate are compared all with the method for Comparative Examples 1 and Comparative Examples 2 and be significantly improved.
Claims (5)
1. method that adopts the feedstock production monose of cellulose, this method comprises the raw material of steam blasting cellulose-containing, the steam explosion products that enzymolysis obtains; It is characterized in that; The water cut of the raw material of said cellulose is 40-60 weight %, and the raw material of said cellulose is a stalk, and the temperature of said steam explosion is 180-200 ℃; The pressure of said steam explosion is the 1.4-2.0 MPa, and holding time of said steam explosion pressure is 3-7 minute.
2. method according to claim 1, wherein, the water cut of the raw material of said cellulose is 40-50 weight %.
3. method according to claim 1, wherein, the enzyme that said enzymolysis uses comprises cellulase, with the dry weight basis of the raw material of every gram cellulose, the consumption of said cellulase is the 8-20 enzyme activity unit; The temperature of said enzymolysis is 45-55 ℃, and the time of said enzymolysis is 25-48 hour, and the pH value of said enzymolysis is 3.0-7.0.
4. method according to claim 3, wherein, the enzyme that said enzymolysis uses also comprises hemicellulase, with the dry weight basis of the raw material of every gram cellulose, the consumption of said hemicellulase is the 4.4-8.8 enzyme activity unit.
5. method according to claim 1, wherein, the size of the raw material of said cellulose is 0.2-1 centimetre of a 0.2-3 cm x 0.2-1 cm x.
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| CN1233614A (en) * | 1999-04-12 | 1999-11-03 | 中国科学院化工冶金研究所 | Method for producing active oligomeric xylose |
| CN1451755A (en) * | 2002-04-12 | 2003-10-29 | 中国农业大学 | Method for producing alcohol by solid fermentation of stalks |
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| CN1451755A (en) * | 2002-04-12 | 2003-10-29 | 中国农业大学 | Method for producing alcohol by solid fermentation of stalks |
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Application publication date: 20081022 Assignee: COFCO Nutrition and Health Research Institute Co., Ltd. Assignor: Cofco Group Co., Ltd. Contract record no.: 2012990000626 Denomination of invention: Process for preparing monosaccharide by using cellulose-containing raw material Granted publication date: 20120321 License type: Exclusive License Record date: 20120827 |