CN1966707A - Method for direct production of starch sugar from durra and residue-less rapid fermentation of fuel alcohol - Google Patents

Abstract

The invention discloses a method for producing amylaceum saccharum with sorghum, and extracting fuel alcohol with non-dregs fast-fermentation. The method comprises the steps of: dry-grinding sorghum, liquefying with enzymes, acid saccharifying to produce glucose solution, producing glucose for injection, oral taking, food, and industry, and amylaceum saccharum such as glucose slurry, fructose slurry or fructose, adjusting pH with sodium carbonate and magnesium carbonate singly or with mother liquid or producing injecting saccharide, fermenting, vacuum boiling to extract alcohol, press-filtrating mother liquid to recover yeast dregs. Compared with the ropy, large volume mother liquid containing dregs and much water in traditional fermentation, the mother liquid of the invention has little organic matter, and has the advantages of low oxygen consumption, short period, and low cost, thus it is easy to reach the discharge standards. Yeast dregs is fine protein and nucleic acids source, can be multiple-utilized, profits for national food protection and stability, avoids pollution caused by mixed bacteria, reduces environmental pollution, saves water, energy, food, workshops, equipments and labors, improves yield, shortens production period, and reduces production cost.

Description

Chinese sorghum direct production Dian Fentang and residue-less rapid fermentation fuel alcohol method

Technical field: the invention belongs to agricultural byproducts deep processing, sugar and alcohol industrial field.

Background technology: constantly face the especially non-renewable oil of the energy the mankind, coal is day by day and obviously fast under the exhausted severe situation, regenerative resource particularly rapid research and development and the extensive industrialization thereof of bioenergy naturally just becomes countries in the world and one of the regional subject goal of competing and task and is representing its true national power, strong and weak great sign and one of the standard with the sustainable development ability of the national national power of one of internationally recognized comprehensive judge, the regenerative resource so all spare no effort to research and develop in various countries, the world and area, greatly develop renewable alternative energy source such as clears such as China's Eleventh Five-Year Plan outlines, and reach in the agreement of working in coordination aspect the renewable alternative energy source technical development with the same genus energy resource consumption big country U.S., State Council's energy state basic policy also clear will be strengthened technical research and the deposit of regenerative resource energetically, its each ministries and commissions also all formulate successively one after another and have issued the with it serial policy of supporting enforcement, file is first developed especially great state basic policy such as fuel alcohol etc. of the recyclable organism energy such as National Development and Reform Committee.In the research and development and industrialization of renewable energy source, the most wide abiotic energy of raw material and market do not belong to, and is harvesting time that regeneration period starchy material fermentative production fuel alcohol cost short, that output is big, the place of production and area are wide is minimum and prospect is the most wide with chemurgy and growth again wherein.However, little in view of the present global Production of Fuel Ethanol starting time difference, so its fermentation technique and technology substantially all are slightly to improve on traditional wine and alcohol basis and do not have an important breakthrough, heighten as production cycle of very long (more than 150 hours) and corresponding investment wait, all be seriously to restrict the bottleneck that fuel alcohol develops rapidly and lean on present technology to be difficult to go beyond, cause it far can not meet the need of market let alone " substituting " oil; In addition, existing tradition band slag fermentation alcohol Technology is used for the large-scale production fuel alcohol, and volume, energy consumption, water consume and encircle dirty problem and also is difficult to ignore; Have again, because of fuel alcohol is a straight alcohol, to compare output few and price is very low with drinking wine, should the hold concurrently Dian Fentang that produces the wide sugar industry development general trend of market and purposes consumption and the smart ability of the mother liquor second fermentation wine survival and development of comprehensive utilization as crystallised sugar.In addition, doing the alcoholic fermentation raw material with Chinese sorghum is not that China daily staple food grain northeast and national many places abound with Chinese sorghum because of Chinese sorghum, so be beneficial to national food protection and enforcements stable and the expansion renewable sources of energy and the great state basic policies such as raw material and rejuvenating the northeast

For further strengthening understanding and understand, might as well earlier prior art be briefly introduced following, for your guidance with the usefulness of easy analysis: take a broad view of present wine and Alcohol Production, its fermentation by states of matter be broadly divided into solid-state and liquid two big classes, by technology be broadly divided into interruption and continuous two big classes, other is as semicontinuous etc. then substantially belonging to intervenient transitional type, do not have significant essential distinction, it gets wine, and then substantially all to belong to disposable be ripe method-at every turn just get wine one time after the fermentation ends; Solid state fermentation raw material water content is few far beyond the liquid state fermentation raw material, the alcohol that produces in the yeast body is because of few and mobile little the waiting a moment of raw material water content, be difficult to rapidly diffusion and be accumulated in the yeast cells body in and near all and dense, be understood that according to the product enzyme reaction principle that suppresses namely to slow down the solid state fermentation cycle is long, generally need several months and even nearly 1 year and often need again to ferment several times and get that wine such as Maotai needed nearly 10 months and 6-8 fermentation and get wine and just can finish, although the solid state fermentation cycle is long, but because of the accessory substance that also needs in the beverage wine to produce in some alcoholic fermentation process such as aroma-producing substance etc. to increase quality, and the generation that very long batch solid fermentation is beneficial to these materials and accumulation and each other more complicated reaction and product and high-grade wine valency your pupil widely adopted so far and still accounted for main flow and the principal status of public economy with the characteristics such as expensive that remedy length consuming time, as now still be widely used in valency higher in, high-grade distillation beverage wine such as high-quality world's famous brand of wine Maotai, five-Grain Liquor, Jian Nan Chun, Luzhou Old Cellar etc.Yet the intermittent type solid state fermentation and concerning top grade be high price drink advantage the wine obviously be not suitable for fuel alcohol and low-grade be the production that low price is drunk wine, because at first the production cycle is grown and causes cost significantly to improve, and its city field energy is accepted as be that the price of reference price does not have feasibility far below its cost with the petroleum products, secondly fuel alcohol need not any aroma-producing substance etc. at all, and the 3rd is some material such as the glycerine (mainly being to be produced by yeast in the very long fermentation later stage) that produces in the fermenting process, (pyruvic acid that glucose fermentation generates and amino acid such as Gelucystine effect generate fusel main body of oil primary isoamyl alcohol to potato spirit; In addition, pyruvic acid and acetyl-CoA combine, because the lengthening of carbochain, when sucrose exists as is molasses fermented, promote that also higher alcohols is the generation of potato spirit), (glucose and L-glutamic acid generate succsinic acid, also generate glycerine simultaneously) can expend sugar and reduce alcohol output, the 4th is that long-time tight airtight heap fermentation produces that more heat transfer is difficult to again distribute when causing leavening temperature to be higher than 37 ℃ and easily pollution microbes such as acetic bacteria (directly consuming alcohol) generate acetic acid, milk-acid bacteria (consuming pyruvic acid is glucose) generates lactic acid, butyric acid is also by glucose, and Yin Wendu is higher than yeast optimum temperuture (30-34 ℃) and suppresses saccharomycetic breeding with active, these factors all reduce alcohol output, the 5th is also to need to isolate from alcohol when distillation these materials, otherwise can influence the especially higher fuel alcohol quality of purity requirement and further increase process complexity and reduce alcohol yield and increase production cycle and plant and equipment investment of alcohol, the 6th is that solid-state stepwise fermentation operation of intermittent type and workload repeat to increase several times and consumption bent (repeating with bent) (it is bent to repeat training) consuming time consumption grain (repeats to cultivate and use song and is converted into the thalline that can not be transformed into alcohol mostly and consume grain; In addition, each fermentation with get wine the wine consumption all arranged: the most common and loss is difficult to again avoid greatly causes rimose " to leak (alcohol and aroma-producing substance etc.) gas " and oxygen enters and weakens zymamsis ability and output and increase oxygen consumption fermentation and product as poorly sealed surface in the fermenting process is withered, carrying repeatedly, loosely get alcohol and quality and the output such as " spacious gas " that vinasse that ferment that wine uses promptly are commonly called as alcohol and a large amount of volatilizations of aroma-producing substance) lose.More than these factors result single and comprehensive function cause alcohol yield to reduce and the cost increase.

Though liquid state fermentation has interruption, semicontinuous and continuous branch, but all tool and above-mentioned solid-state discontinuous fermentation have essence and be the difference of general character: one-period finishes once fermentation and namely abandons after drinking material and no longer repeat to reach again as fermentation raw material and ferment with getting, this just requires liquid state fermentation to ferment as much as possible thoroughly namely to allow starch in the raw material change into as much as possible glucose sugar and make equally as much as possible conversion of glucose is alcohol, and these processes all require continuously once (one-period) property to finish.For fermenting during with respect to aforesaid solid-state intermittence, liquid state fermentation truly has high because of moisture and therefore has again certain fluidity to make alcohol be easy to dissolving and comparatively be evenly distributed in the whole liquid, alcohol meltage and content in the liquid are increased, therefore and reduce the inner and nearly all alcohol concentrations of yeast, the enzyme reaction rate that causes generating alcohol because of product be alcohol concentration reduce to be accelerated to shorten fermentation period, and reduce the various alcohol losses of aforesaid solid-state batch fermentation and grain consumption and cost and increase, thereby substantially overcome or avoided above-mentioned solid-state batch fermentation to be difficult to serial critical defect and the key restraining factors of low-cost large-scale industrialized production fuel alcohol.But with respect to fuel alcohol high-purity and high yield and the fast series of speed of production is crucial require with bottleneck for, at present liquid state fermentation still has serial major defect, cause Starch Hydrolysis speed slow such as boiling, not thoroughly (be non-glucose as producing the non-direct fermentation sugar such as a large amount of dextrin) and amylodextrin sex change are not aging is difficult to rapidly or thoroughly be hydrolyzed into fermentable sugar and significantly increases fermentation and significantly extend manufacture cycle and equally significantly reduce alcohol output such as primary fermentation (more than 10 hours) especially after fermentation (more than the 40 hours) time for hydrolysate; Starch and dextrin expansion increase liquid viscosity and reduce its flowability, reducing liquid and surface exchange area and the exchange velocity of yeast and the alcoholic fermentation speed that slows down extends manufacture cycle, and easy therefore pollution microbes and reduce alcohol output and quality, only have the high cost that increases the yeast consumption effectively to overcome, or it is mobile to reduce the toughness increase to reduce liquid material concentration, so but this also must be that to reduce unit interval alcohol growing amount be that output is that cost is equally high, though above problem in the prior art can through the agency part of aspergillus carbohydrase generate fermentable sugar and in alcoholic fermentation process the starch in the converted mash and dextrin continue by Glucoamylase hydrolysis namely after saccharification, thoroughly being hydrolyzed into fermentable sugar with respect to the elder generation of the present invention's design is to still have above-mentioned series and the defectives and more serious such as the fermentation of following band slag and accessory substance for fermenting behind the glucose again; The more important thing is band slag boiling and ferment that not only treating capacity is too big, and because increasing, volume takies in a large number equipment and factory building dischargeable capacity and time, space, significantly increase simultaneously and can consume and environmental pollution by water consumption, be that glucose reduces alcohol output because a large amount of proteolysis in the slag cause the thalline excessive multiplication to expend multiple-energy-source also, and as aforementioned same need expend glucose sugar and generate fuel alcohol and do not need and affect its quality and must increase fusel wet goods accessory substance and the corresponding minimizing alcohol outputs of cost to remove such as operation and equipment, time.Above-mentioned series of problems is not as resolving, and the enforcement of Fuel Ethanol Industry and the industry great state basic policy of the inevitable serious national regenerative resource of restriction with regard to being difficult to rapid tremendous development, will seriously restrict the world and human energy resource supply and alternative ability and pace and paces yet.

The state-of-the-art technology progress is for adopting immobilized cell technique to transform traditional technology of alcohol at present, the tool fixed yeast is reusable, useful life is more than 160 days, anti-miscellaneous bacteria ability need not be sterilized by force, no longer need distiller's yeast to cultivate, fermentation time shortens half, Zymolysis Equipment production capacity improves more than 1 times, liquor output rate waits feature ﹠ benefits than traditional zymotic technology raising about 5% under equal fermentation condition, conclude and get up to see mainly be to reduce with bent and cultivation, grain consumption and before, the after fermentation time, but the large-scale production ability of immobilization technology is then littler very limited with the restriction more high core sexual factor of cost price because of the disposal ability that is subjected to the immobilization post, and difficulty has essence to break through or takes on a new look in a short time, add that it still fails to resolve saccharification and purity and concentration, band slag and processing are big, the energy consumption that hard and fast rule are limited in the high serial main body problem of the big cost of the low investment of equipment factory building utilization rate and the 11 5 years development planning outline of the government work report and country, the water consumption, the rigid index of environmental pollution etc. is the serial difficult problem of bottleneck equally, and it is extensive to be difficult to be applicable to that fuel alcohol needs, low-cost production must with the basic demand condition.Also has at present energy-conservation raw material direct fermentation, but fermentation period needs a couple of days in the above cycle to grow up to this height, fermentation load and treating capacity and volume are too big, and easily microbiological contamination, rotten, corruption etc. are therefore all little for low-cost indispensable feasibility and the meaning of requiring of fuel alcohol high-yield quick.

Serve the growth that waits industry and desertification to take up an area along with population and industry and commerce, the whole mankind and everybody are faced with reality and the long-range existence difficult problem that arable land per capita is fewer and feweri and be difficult to overcome, the production cycle that adds traditional main flow sugaring crop sugarcane reaches 10 months, remaining 2 months because being shorter than any main energy sources crops such as carbohydrate beet, it is long-term that former its of the basic growth of oils rape and legume or starch main source Cereal and tuber crops etc. and processing maturation period exhausted perennate substantially, cause main flow carbohydrate Price of Sugar constantly soaring, forcing country to employ on a large scale again and again national treasury deposit sugar stabilizes and the sugared valency of regulation and control, but obviously this is temporary transient, because national treasury and ability of regulation and control thereof and regulation and control space are always limited, only have fundamentally to solve source, sugared source and just can reach the regulation and control purpose.Starch sugar then is the only way and wise the selection, because of its crop species, source and distribute extensively, short, the general 3-5 of output height and growth cycle is about individual month, so but 1 year 2-3 is ripe, and be the higher glucose of nutritive value or quality higher, sweeter fruit glucose (slurry) and fructose, add can large-scale industrial production thus price also cheaper, become developed country main flow sugar source at present, the China that developing country especially has a large population and a few land etc. also should and can become inevitable choice and development general trend.The method Patent Prospectus that the CN1070425A maize enzyme acid is directly produced glucose sugar is exactly a well trial of complying with this trend: it removes slag and namely earlier Raw material processing is produced starch slurry or first starch, selectivity principle according to enzyme adopts three sections liquefaction of high temperature enzyme and sour saccharification namely not to be with the direct high-quality of slag fast (with respect to acid described later again, acid enzyme and holoenzyme method) production glucose, thereby the high smart starch of traditional acid system call for bids and high-temperature high-pressure apparatus and heavy with the big environmental pollution of acid amount have been overcome, the problems such as the serious and amount of by-products of recombination reaction is big, also overcome improved method acid-enzyme hydrolysis method (low with sour amount and temperature and accessory substance than acid system), especially the holoenzyme method takes the shortcomings such as long, but its wet-milling legal system starch slurry technology still must consuming timely reach 48-72 hour, starch runs off big, the water consumption is also big with environmental pollution, starch slurry is processed untimely easy microbiological contamination, rotten, corrupt, starch is because of need power consumption drying and because of the low environmental pollution die valency height of dried dust loss yield, also need again water consumption to convert into starch slurry, sulfurous acid is greatly also unstable to human body and alcoholic fermentation unfavorable (see below and state) and the more expensive and acid weak consumption of lactic acid, and the enzyme-added enzyme that kills again of wet-milling or the three sections liquefaction of dry grinding is valuable and the expensive enzyme wasting of resources, the liter that matches, fall and be incubated the corresponding energy consumption that also increases, time consumption and (cooling and insulation) water consumption be the more important thing is to be heated to 120-140 ℃ and reach 5-8 minute starch denaturalization coking color depth, the refining difficulty of liquid glucose and yield (comprise and fermenting such as alcohol) are descended and the great difficult problems such as unresolved good saccharification and comprehensive utilization and fast thorough fermentation alcohol.

Goal of the invention: the present invention directly produces starch sugar and residue-less rapid fermentation fuel alcohol method for solving the Chinese sorghum that above-mentioned series of problems designs, and the invention solves above-mentioned all and be existing newer documents (requiring to many far beyond the convention that generally is no more than three pieces) altogether also unsolved series of problems produce sugar and alcohol and quick, thorough, pure and be not with the slag fermentation to make that fermentation is equally quick, thorough, accessory substance is few, recovery rate is high, quality better as holding concurrently; Simultaneously slaking of Substratspezifitaet high temperature enzyme liquefaction and except the toxicity that removes slag makes that it is safer, nutrition and mouthfeel better and the feed value height, also thoroughly make saccharification and zymotic fluid concentration height that alcohol output is significantly improved because liquefying, the more important thing is that having solved traditional cooking liquor must qualifiedly have the irreplaceable great innovation of the present technology of above-mentioned series, advantage and advantage because viscosity is high-leveled and difficult with huge workload and high energy consumption, water consumption, environmental pollution and the serial historic difficult problems such as with high investment and cost that slag is processed equally to separate slag.Now again with the innovation brief introduction of main scientific and technological principle of the present invention and other outbalance: the present invention according to enzyme-to-substrate in conjunction with and the height selectivity principle of catalytic reaction, adopt more than 90 ℃ the high-temperature starch hydrolase and under same temperature in specific manner with the starch in the raw material rapidly and thoroughly liquefaction and to other compositions inoperative and simultaneously slaking with remove the slag poison by high-temperature heating treatment, make feed good palatability livestock and poultry like to eat and be of high nutritive value; The more important thing is because the viscosity of the thorough liquefier that liquefies is low so the separation of slag is easy, and the slag after separating because of the low volume of water content and weight all little again not thickness easily transport and little, the easy drying of freight volume also energy-conservation, when saving, joint equipment and space; Because of separate that liquefier volume behind the slag is little, the low concentration of viscosity is big and good fluidity so the saccharification treating capacity is little; Because saccharified liquid is not with slag purity height, thus adopt the aforesaid enzymatic conversion of acid substitution to make to process easily and fast, as enzymatic conversion needed tens of hours and sour saccharification only needs a few hours; The more important thing is that culture propagation alcohol must remain under the sour environment, otherwise fermentation is carried out to the direction that generates glycerine, particularly ferment the later stage, because glycerine mainly produces in the alcoholic fermentation later stage, although especially the later stage may produce acetic acid because of living contaminants such as acetic acid bacteria in alcoholic fermentation, but it is volatile acid, also may pollute lactic acid bacteria and produce lactic acid, but living contaminants and product acid thereof belong to strict the strick precaution and the production accident of controlling in the alcoholic fermentation, though tradition can keep stable acidity of later stage particularly of full phase of alcoholic fermentation with non-volatile acid sulfuric acid, but can produce the material (seeing aftermentioned for details) that people and environment and alcoholic fermentation all are harmful to, and the present invention with the hydrochloric acid saccharification and after direct fermentation alcohol do not have these shortcomings and tool is economized on the main advantages such as acid (seeing aftermentioned for details); Of paramount importance is need utilize the zymotic fluid nutriment such as sugar (starch-containing and dextrin etc.) because of yeast, protein and amino acids, trace element is such as proliferative cell quantity such as magnesium, therefore and the fusel oil (introducing before its mechanism) of generation and if the nitrogenous source that easy utilization is arranged in the karusen exists then can stop or postpone the disintegration of yeast and amino acid whose decomposition and, the height selectivity that adds catalyzed by amylase namely kept except starch other all nutriments and as the above-mentioned compositions such as its catalysate sugar can be used for cell proliferation by yeast, when being saccharification in conjunction with acid catalyzed broad spectrum activity again in liquefier and the saccharified liquid the remaining macromolecular substances such as protein also be catalyzed into the small-molecule substances such as nitrogenous source that amino acid is above-mentioned easy utilization, so enzyme liquefaction and sour saccharification not only the time short and because of liquefier, saccharified liquid and zymotic fluid all are not with slag and treating capacity is little and concentration is high, thereby can accelerate the quick goal of the invention of producing alcohol of enzyme reaction principle realization that enzyme reaction rate improves product concentration by utilization raising reactant concentration, also with the raising quality liquefier and saccharified liquid all need not be made with extra care because the above-mentioned materials such as the remaining protein of need supply acidolysis and acid hydrolysis products thereof to be beneficial to fermentation alcohol, again significantly reduce treating capacity and environmental pollution and significantly save time and cost; In addition, the present invention with its fast and the sour saccharified liquid of low-cost production replace the long-time enzymatic conversion liquid of tradition improve force of labor also be the successful Application enzyme-to-substrate agree with can carry out immediately and accelerate the enzyme reaction principle in the goal of the invention of alcoholic fermentation production practices and theoretical and serial major application thereof be worth as substantially save primary fermentation 10 hours, after fermentation 40 surplus hour be total to about 50 surplus when hour very long time and Yin Jie, energy-conservation, water saving, grain consumes and environmental pollution is little and can effectively prevent living contaminants and improve alcohol quality and yield etc.

What is particularly worth mentioning is that also another great innovation of the present invention is that science is the goal of the invention that the fermentation reaction principle realizes producing fast alcohol with the enzyme that rationally utilizes reduction resultant concentration that enzyme reaction is carried out towards the resultant direction, now also with cardinal principle and advantage brief introduction: though at present which kind of liquid state fermentation alcohol method all be treat (solid-state then is each) ferment finish after disposable extraction alcohol, the surface sees that it seems the technology advantages of simple, will find at an easy rate that its shortcoming much but also very serious but analyze a little, as space is limited, it is for reference now only to make concise and to the point comprehensive analysis: the principle that enzyme reaction is carried out towards the resultant direction according to above-mentioned reduction resultant concentration is counter to be pushed away as can be known resultant and concentration thereof and can seriously hinder fermentation and promptly reduce the alcohol formation speed and first limiting factor often, it is that the influence of concentration of substrate sugar is much bigger than reducing reactant, because the low product speed that just reduces alcohol of sugared concentration, yeast itself is safe from harm promptly can therefore do not weaken the essence ability and the potentiality of its fermentation, and improving constantly along with ethanol concn, it suppresses promptly to reduce the wine speed of producing in feedback ground on the one hand, but this also only is equivalent to the influence that above-mentioned sugar reduces, the prior alcohol that also is can cause irreversible dehydration of cell and albumen irreversible denaturation to make cell and enzyme (albumen) comprise aforesaid traditional enzyme glycolysis technology and saccharifying enzyme sex change thereof, inactivation and directly and non-reversibility ground by its inhibition, passivation even kill, cause fermenting speed to slow down or stop to make fermentation not thorough fully, or make originally very very long as liquid phase process 40 hours of traditional technology, the tens of skies and even the above secondary fermentation process of several months of solid state process become longer, all can seriously reduce production capacity and output; Owing to causing living contaminants, fermentation time length reduces quality and yield, and make the alcohol separating technology complicated with difficulty, reduce yield equally and increase cost, also heighten and significantly reduce throughput, must be with in proportion increase equipment and factory building at least (look production capacity, yield and quality 30% or more and even at double) and invest and remedy for high cost because of fermentation period length takies volume of equipment and plant area; In addition, long and the mother liquor of fermentation time comprise wherein yeast can not or low grade of recycle and reuse rate will cause its energy consumption, grain consumption, ring dirt and water to consume loading etc. increasing the weight of synchronously and unfavorable falling can be lowered consumption and the enforcement of environmental protection state basic policy, therefore production cost also can heighten and weaken produce market share and competitive capacity, and this place of lifeblood of enterprise and product just.

This raw materials technology and liquefaction, the saccharification treatment technology makes full use of enzyme effect specificity principle and good zymin, enzymatic hydrolysis (90 ℃) under comparatively high temps is carried out, thereby solved the realization that directly feeds intake, received the effect of starch liquefacation rate more than 97%, protein is easy to separate with starch, filter easily, liquefier glucose (DE) value is up to 28-30, make saccharification react very rapid and thorough, thereby make and reach in original technology that saccharification period shortens to several hrs more than 50 hours, and make liquefier quality height in the production process, high purity, by product is little, has solved double-enzyme method basically and has injected sugared clarity and be difficult for shortcoming up to standard, make and produce injection, oral, edible and industrial sugar is produced in same set of equipment and is come true, for production has brought great handiness.In addition, because the DE value was more than 99.5 after liquid glucose was refining, oral glucose with this liquid glucose production need not crystallization just reach FCC-" U.S.'s edible chemical code " standard and China Ministry of Public Health oral glucose standard promulgated by the ministries or commissions of the Central Government, produce like product by the injection Standard for Sugars and can guarantee that also more than 70 hours crystallizing cycle of old technology shortens about 8-12 hour, and this technology does not play destruction to protein in the raw material etc., only play inspissation, final the mouthfeel that sugared slag is slaking and detoxification that obtains (palatability) is good, the mash concentrate that nutrition is very abundant is desirable food and feed exploitation basic resource.

Description of drawings:

Fig. 1 is the process flow diagram of Technology of the present invention.

Embodiment:

The invention will be further described below in conjunction with accompanying drawing.

The inventive method is as follows.

A Chinese sorghum dry grinding method is produced and under the rice powder emulsion normal temperature Chinese sorghum ground rotating speed with powder emery is that 800-1000 rev/min of stiffened water mill is fine into the powder emulsus, require powder to be about 40% greater than the ratio of 450um, ratio less than 450um is about 60%, sorghum flour breast concentration 25-30%, it is 6.0-7.0 that lime carbonate or hydrochloric acid are transferred PH.

B enzyme acid is produced Glucose Liquid the sorghum flour breast is pressed the disposable adding Ye Huamei of enzyme-added total amount of a-amylase 50-60 units/gram dry starch, carries out high temperature gelatinization and liquefaction under 90-93 ℃, remains to dextrose equivalent value 25-30 or disappears to Iod R; Conventional filtration removes slag; Filtrate is concentrated in vacuo to 30-35% concentration, adds hydrochloric acid accent PH to 1.2-1.8, and 0.3-0.35 MPa vapour pressure acid saccharification gets Glucose Liquid to DE value 90-95;

The production of c glucose for injection adds the neutralization of 10-15% yellow soda ash, activated carbon decolorizing in the Glucose Liquid of producing glucose for injection after

Filter, plastic resin treatment is done ion-exchange, evaporation concentration is to 1.250/45 ℃ of concentration of proportion under the 0.06-0.067 MPa, under 70-80 ℃, add gac and stir 25-30 minute decolorization filtering, for the second time being concentrated to proportion under the 0.06-0.067 MPa is 1.3450/45 ℃ of concentration, carry out crystallization, centrifugal 50 hours inner control temperature by 44 ℃-22 ℃, vacuum-drying to moisture content less than 5%, injection high purity (the DE value is more than 99.5%) medicine glucose;

The production of d alcoholic fermentation Glucose Liquid adds 10-15% sodium carbonate and 1-5% magnesium carbonate with the described Glucose Liquid of c, and jointly to transfer PH be 4.5-5.1, with the described crystallization of d and centrifugal after mother liquor add hydrochloric acid and transfer PH to be 4.0-4.3, to add 10-15% sodium carbonate and 1-5% magnesium carbonate jointly to transfer PH be 4.5-5.1, be concentrated in vacuo to 30-35% concentration and get the alcoholic fermentation Glucose Liquid again, two kinds of alcoholic fermentations are alone or share with any ratio with Glucose Liquid;

E food with the production d of glucose syrup described in and Glucose Liquid be the food glucose syrup;

Be spray dried into water content with Glucose Liquid during f food is described with d with the production of glucose and get food glucose below 5%;

The production of g oral glucose is spray dried into water content with the Glucose Liquid after concentrating d described for the second time and meets standards of pharmacopoeia and get oral glucose;

The production of h crude dextrose with the described crystallization of d and centrifugal after mother liquor concentrate again, be spray dried into water content below 5% industrial sugar;

The production of i HFCS becomes fructose with equipment with a part of conversion of glucose in the described glucose syrup of e with conventional isomerase and consumption, conventional ion exchange refining HFCS;

The production of j fructose syrup is with the conventional separating levulose slurry of the described high fructose syrup of i;

The production of k fructose gets fructose with the described fructose syrup spraying drying of j;

The fermentation of l fuel alcohol and extraction: by number of yeast cells 1-5 10,000,000/milliliter bent, disposable adding, temperature is controlled at 30-34 ℃; When the temperature of zymotic fluid began to reduce, press filtration separated alcohol liquid and yeast, alcohol is extracted in 30-34 ℃ of boiling of alcohol liquid negative pressure of vacuum; Mother liquor returns former tank with the yeast that separates and adds new sugar solution to demarcating volume, and press filtration separates alcohol liquid and yeast, alcohol is extracted in 30-34 ℃ of boiling of alcohol liquid negative pressure of vacuum when keeping 30-34 ℃ to continue fermentation, temperature reduction; Mother liquor returns former tank with the yeast that separates and adds new sugar solution to demarcating volume, continuing fermentation to no CO ₂Generation, the conventional alcohol that extracts.

Be convenient and the present invention that sharpens understanding, now be described as follows again:

1, Chinese sorghum dry grinding method is produced the sorghum flour breast: under the normal temperature with Chinese sorghum with the corundum mill add the drinking water such as hard water such as running water (calcic take safeguard with improve follow-up High-temperature Liquefaction technology in the high temperature active of α-amylase with stable) levigate (rotating speed is as 800-1000 rev/min) become the powder emulsus, require powder to be about 40% greater than the ratio of 450um, ratio less than 450um is about 60%, keep such powder size total surface area bigger, easier with contacting of enzyme, so liquefied fraction is better, the rate of filtration is also very fast; It is that 6.0-7.0 is the α-amylase Appropriate and eliminates the adstringency material that hydrochloric acid is transferred PH, make slag capable of using as feed and save the soda acid consumption and avoid the subsequent treatment difficulty, because the hydrochloric acid neutralized reaction product is water-soluble calcium chloride and concentration is very low easily removes, but can maintain also the high active calcium ion of above-mentioned functions and purposes in follow-up alcoholic extraction technology; Transfer newborn concentration, control concentration of slurry about 25-30%.

2, Glucose Liquid is produced in the acid of Chinese sorghum enzyme: the disposable adding Ye Huamei of enzyme-added total enzyme concentration of the sorghum flour breast being pressed a-amylase 50-60 units/gram dry starch, concentration is 30-35%, under 90-93 ℃, carry out high temperature gelatinization and liquefaction, remain to dextrose equivalent value (DE value) 25-30 or disappear to Iod R till the liquefaction degree, with this method liquefaction sorghum flour breast, generally can three sections liquefaction of image height temperature equally will also fully liquefy because of the dead starch that the aging difficulty that form of starch small grain liquefies, but there is not starch coking color depth problem and when saving water and energy, sugar and alcohol yield and quality be can improve and saccharification and alcohol secondary fermentation time significantly shortened, conventional filtration removes slag, and slag is made feed; Filtrate changes routine and adds sulfuric acid H ₂SO ₄For hydrochloric acid HCl (its serial important effect and advantage are seen associated viscera described later) transfers PH to 1.2-1.8, under vapour pressure 0.3-0.35 MPa, carry out sour saccharification, keep getting Glucose Liquid in 20-25 minute, be used separately as the raw material liquid glucose of following various glucose (slurry), fructose (slurry) and zymamsis.

3, the production of glucose for injection: in the Glucose Liquid of producing glucose for injection, add in (stating as follows) exhausted gac first time and the pressure filter press filtration of decolouring back; Plastic resin treatment is done ion-exchange and is removed salt etc., evaporation concentration is to 1.250/45 ℃ of concentration of proportion under the 0.06-0.067 MPa, add new gac and stir 25-30 minute decolorization filtering down at 70-80 ℃, for the second time being concentrated to proportion under the 0.06-0.067 MPa is 1.3450/45 ℃ of concentration, carry out crystallization, centrifugal 50 hours inner control temperature by 44 ℃-22 ℃, vacuum-drying to moisture content less than 5%, injection high purity (the DE value is more than 99.5%) medicine glucose.

4, the production of oral glucose: the liquid glucose after concentrating in above-mentioned 3 is spray dried into water content meets standards of pharmacopoeia and get oral glucose.

5, food is with the production of glucose syrup and glucose: the liquid glucose after concentrating in above-mentioned 3 is the food glucose syrup, with liquid glucose be spray dried into water content below 5%, must food glucose.

6, the production of crude dextrose: with crystallization in above-mentioned 3 and centrifugal after mother liquor concentrate again, spray-drying, get industrial sugar, not high to salt and glucose sugar (DE value) content requirement.

7, the production of HFCS: with conventional isomerase and consumption a part of conversion of glucose in the glucose syrup in above-mentioned 3 is become fructose, ion-exchange refining HFCS.

8, the production of fructose syrup and fructose: with the HFCS after refining in above-mentioned 7 conventionally separates, respectively must glucose syrup and fructose syrup, the glucose syrup in this glucose syrup and above-mentioned 3 merges to fully utilize, fructose syrup is used separately or spray-drying gets fructose.

9, zymamsis is with the production of glucose syrup: with crystallization in above-mentioned 3 and centrifugal after mother solution hydrochloric acid to transfer PH be 4.0-4.3, be concentrated to 30-35% concentration, separately or the Glucose Liquid in above-mentioned 2, be used for production zymamsis glucose syrup: adding 10-15% yellow soda ash and 1-5% magnesiumcarbonate respectively at the above-mentioned mother liquor after acidification and glucose liquid glucose, to transfer PH jointly be 4.5-5.1, make fermented liquid be slightly acidic, with ensure fermentation to alcohol but not directions such as glycerine carry out, and the salt that generates be mainly to all harmless sodium-chlor of fermentation and human body and because of its solubleness in water and the equal height of stability be that good water solubility is very easily removed, the carbonic acid that generates is that volatility and decomposability are all very strong and easily remove for the original product in the alcoholic fermentation process for instability extremely, so it is harmless equally to zymamsis, the a small amount of salt that generates is promptly very favourable to the Alcohol Production magnesium chloride that can promote to ferment in addition, this is because generate glucose phosphorylation in the reaction (being called the E-M approach) of pyruvic acid by glucose in alcoholic fermentation process, 1, the 6-hexose diphosphate, 3-phoshoglyceric acid, the generation of 2-phosphoenolpyruvic acid and pyruvic acid all need Mg++ to activate by the reaction of yeast continuation degraded generation alcoholic acid decarboxylation generation acetaldehyde under oxygen free condition, though also contain magnesium in the ortho-water, but because of it is to be insoluble in water and to be heated the littler magnesiumcarbonate of resolution of precipitate degree, be difficult to guarantee the need of above-mentioned reaction, magnesium chloride is all got well because of solubleness and stability does not have these defectives, then can protect the need of fermentation, transfer PH then to generate human body and zymamsis does not need and often harmful as easily make people have loose bowels more than sodium sulfate and sal epsom with sulfuric acid, easily generation can play the sodium bisulfite etc. that addition generates the crystalloid acetaldehyde S-WAT affixture of indissoluble with acetaldehyde, force the acetaldehyde can not be as hydrogen acceptor and must replace it as hydrogen acceptor and generate glycerol 3-phosphate by phosphodihydroxyacetone, under the catalysis of 3-phoshoglyceric acid lipase, generate glycerine and reduce alcohol output and quality, so above-mentioned these designs of the present invention and many-sided excellent effect are to realizing that fermentation is quick and the high yield goal of the invention is necessary and being easy to implement.

10, fuel alcohol fermentation: traditional handicraft be with starchy material through boiling make starch be dissolved state, again through the effect generating portion fermentable sugar of aspergillus carbohydrase, in converted mash, insert saccharomycete and change sugar into alcohol and CO ₂, separate to obtain alcohol product, (starch in the converted mash and dextrin continuation are by Glucoamylase hydrolysis but because of saccharification after thoroughly not the existing of liquefaction and saccharification, generate sugar) effect, also have protein further to generate the effect of low molecule nitrogen-containing compound such as peptide and amino acid etc. under the hydrolysis at Aspergillus proteinase, these materials of generation have is absorbed synthetic yeast somatic cells, another part and then is fermented and generates alcohol and CO by yeast ₂And other accessory substance.Than the present invention not with slag saccharification and fermentation and only the liquefaction of a few hours and saccharification stage just finished these processes, conventional method then with slag and (primary fermentation stage more than 10 hours, after fermentation stage more than 40 hours) the very long time that needs expend surplus in the of 50 hour more just can make starch in the converted mash and the dextrin fermentable sugar of generation that continues to be decomposed; In the mash of alcohol around can any ratio mixing with water, just being dissolved in by the alcohol of discharging in the yeast body, the CO because producing in the fermentation again ₂The littler karusen of solubility is will soon be by it saturated and be adsorbed on yeast cell surface until its CO when surpassing the cell adsorption capacity ₂Become gaseous state, form little bubble rising, again because CO ₂Bubble mutually collides and forms larger bubble and effusion liquid level, CO ₂The rising of bubble has also driven the material in the mash and with the yeast cells wander up and down yeast cells can have been contacted more fully namely to be equivalent to increase reactant concentration so that fermentation is faster more abundant and thorough with sugar in the mash, and alcohol is scattered in more namely be equivalent in the liquid reduce product concentration and Alcohol Production speed is accelerated, such fermentation is called the passive type fermentation, if but fermentation liquid than thickness then bubble to arrive the foam that does not break behind the liquid level and forms lastingly diffusing, sometimes foam also may be overflowed by tank deck and cause sugar loss, such fermentation is called bubble and smears fermentation, and oxygen is many even saturatedly also the bubble fermentation phenomenon can take place in the medium, this mainly is because the undue strong breeding of yeast and undue strong fermentation and karusen are done raw material or the song poor quality causes with fresh potato is dried, increase operation and cost though the employing defoamer can be prevented planting here phenomenon also time-consuming bothersome.In Traditional Method Yin Changwen and the stock media that liquefies for a long time oxygen expenditure slow, add big with the contact with air face and the time long so saccharified liquid contains the oxygen height, also greatly easily cause bubble fermentation because of the not thorough viscosity of liquefaction, saccharification, the present invention because of High-temperature Liquefaction, saccharification so gassiness, to contain oxygen all low, and because of liquefaction, the low bubble breaking loose of the thorough fermentation broth viscosity of saccharification, again because of the fast output height of the big fermentation of concentration, quality better, cycle weak point.Thus also visible serial advantage of the present invention and novelty and the importance in alcoholic fermentation is produced thereof.

Distillery yeast does not contain the amylase such as AMS and beta amylase and lactase and can not directly utilize starch or lactose to carry out alcoholic fermentation, therefore must change into fermentable sugar to starch when utilizing starchy material to produce alcohol and could be used to carry out alcoholic fermentation by yeast.Alcoholic fermentation process can be divided into it following three fermentation different stepss by the outward appearance presentation:

The primary fermentation phase is when distiller's yeast and converted mash adding fermentor tank, because of containing minimal amounts of dissolved oxygen and sufficient nutritive substance in the also few and aforesaid mash of the yeast count in the mash, yeast still can be bred rapidly, dextrin in the tradition method mash also continues to be generated sugar by Glucoamylase hydrolysis, but Yin Wendu turns into slow than low sugar, sugar consumption is also few slow because of yeast count, be generally perdurability about 10 hours, because the not strong mash temperature of fermentative action rises unhappy, this moment, the mash temperature was controlled at 26-30 ℃, the too high meeting of temperature causes yeast old and feeble in early days, crossing to hang down to make yeast growth slow again, this phase yeast quantity is easily suppressed to pay close attention to prevent living contaminants by assorted bacterium less, so should strengthen hygiene control.The inventive method is because of no slag and liquefaction, saccharification thoroughly reaches features such as sugared concentration height, can easyly take directly to improve yeast quantity with respect to traditional method is 1-5 10,000,000/milliliter (deciding on particular cases such as different starch source liquid glucoses) and significantly to reduce the primary fermentation phase that reaches more than 10 hours be only about 2-3 hour and therefore effectively prevent, control incident living contaminants of this phase and pour in down a chimney loss and encircle dirty consequence, though initial apparently with the many and cost height of the bent more traditional method of amount (1,000,000 grades), but the time of saving with the present invention and the specially designed reduction resultant of the present invention concentration and yeast are the touring fermentation of mother liquor to be used and not with slag with specializedly produce the production capacity that the high vigor liquid yeast event of high cell count need not the primary fermentation stage and be difficult for feature (asking for an interview following) raisings such as microbiological contamination and compare then and can ignore with the bent medicine of the output value and saving.

This time phase of lord ferment period is generally about 12 hours, yeast count can reach more than 100,000,000/milliliter in the mash, because the oxygen expenditure in the karusen is complete, saccharomycete stops to breed and mainly carrying out anaerobic basically is the alcoholic fermentation effect, sugar rapid decrease, alcohol divide and CO in the mash ₂Increase gradually, the temperature of karusen rises also very fast at this moment, should strengthen in the production temperature control of this one-phase, preferably can be controlled at 30-34 ℃, this is the suitableeest fermentation temperature of distillery yeast, temperature Tai Gaoyi makes the early stage aging of yeast, lowers yeast activity and easily cause germ contamination, the easier generation that causes the microbiological contamination phenomenon when especially being higher than 37 ℃ with the karusen temperature.The inventive method is not with slag and saccharification thorough because of saccharified liquid, with Traditional Method band slag and liquefaction and saccharification all not completely with the concentration zymotic fluid compare its reactant be high nearly 1/3, the main fermentation of sugared concentration be the main product time therefore than Traditional Method increase nearly 1/3, production capacity is also corresponding with output increases than Traditional Method, add because not being with slag not only to liquefy thorough with saccharification, and liquefier and saccharified liquid concentration can exceed one times with the concentration of slag 13-15% up to 25-30%, ratio tradition, the viscosity that adds zymotic fluid is low, good fluidity and ferment fast, although fast because fermenting, produce (CO ₂) also many (recovery gets final product the many and alcohol that take away of gas routinely, needn't process especially), but still far be not enough to balance, so alcohol generation and dissolving are also many in the zymotic fluid, make its alcohol concentration corresponding to the Traditional Method height, can suppress more by force yeast activity and reproductive capacity and fermentability and speed, so special design of the present invention main fermentation zymotic fluid is carried out separating of yeast and wine liquid and gets wine midway, yeast after will separating again and the mother liquor of getting after drinking return the technology of carrying out circulating fermentation, its principle, necessity and advantage are replenished and to be described below: when the temperature of zymotic fluid reduces gradually but not rises, show that fermentation begins to weaken the heat that namely produces and begins to reduce, sugared content in zymotic fluid this moment is described and the alcohol content rising, because of the two all slow down fermenting speed and alcohol concentration also than Traditional Method height, harm to yeast is just big than Traditional Method, and yeast vigor and proliferative ability at this moment is all just strong, the zymotic fluid of this moment is separated alcohol liquid and yeast with the 1000-3000 rev/min of rotating speed that keeps the yeast cells integrality, with the conventional alcohol that extracts of alcohol liquid, adopt the thermotolerant yeast of the present invention fermentation then needn't separation and fermentation liquid, because it can bear 60-62 ℃ of high temperature, although the alcohol boiling point is 78 ℃ under the normal pressure, but boiling point of 100 ℃ than water is low many for this, add the alcohol highly volatile, just can extract smoothly alcohol so need only simple and regular adopt lower vacuum suction method that its boiling point is dropped to below 60 ℃; Above-mentioned mother liquor and the yeast that separates are returned former tank and add new sugar solution and carry out secondary fermentation to demarcating volume, yeast quantity and proliferation potential in the zymotic fluid can make it again carry out immediately main fermentation at this moment, can go round and begin again in theory and set up benign cycle, but actual from the decay of the continuous dilution of considering living contaminants probability and sugar concentration and the production capacity such as yeast activity and proliferative ability, after finishing twice circulation main fermentation and extracting alcohol midway, change the after fermentation phase (asking for an interview aftermentioned) that is equivalent to Traditional Method over to and take turns circulation with thorough end one, and equipment carried out beginning new round circulation behind the cleaning and sterilizing routinely.Do like this and save in addition song and namely save grain and when joint (one with three, than 2 times at Traditional Method joint), wash number economize on water less and environmental pollution little (three one-periods, only be the Traditional Method of an one-period such as gap method 1/3), in case each fermentation tank is an independently reactor and can just not causing synchronously comprehensively or the main advantages such as large tracts of land stopping production, the underproduction or Quality Down because of many fermentation tanks series connection cleanings, maintenance or microbiological contamination as continuous fermentation method.

Sugar major part in the after fermentation phase mash is consumed by saccharomycete, and still remnant dextrin continuation is by the amylo-1:4,1:6-transglucosidase in the song in the mash, and the effect of 41,6-glucuroide generates glucose.Because the very slow steamed bun that this effect is carried out, the sugar of generation are seldom, so fermentation is also very slow.Therefore, alcohol and CO2 produce also fewly in this stage fermentation wine with dregs.

The secondary fermentation stage is because of traditional method band slag fermentation and liquefaction, the not thorough and sugared concentration of saccharification is low, fermentative action weakens but this stage sugar after Primary Fermentation exhausts substantially, the heat that produces also reduces, the temperature of karusen descends gradually and ethanol concn is still not high enough, alcohol needs the secondary fermentation stage so that because of liquefaction and the not thorough and remaining partial starch of saccharification so traditional method starchy material is produced, dextrin continues saccharification during the fermentation to improve the rate of getting alcohol, and this moment, the mash temperature should be controlled at about 30-32 ℃, if the mash temperature is too low, the effect of saccharifying enzyme will weaken and saccharification is slow, fermentation time will prolong, also can influence the rate of getting alcohol.But nonetheless, after fermentation generally still needs about 40 hours very long time just can finish approximately; The alleged after fermentation of the present invention then is because of the liquid glucose of circulating fermentation dilution and above-mentioned for finishing a circulation main fermentation cycle, being fermenting speed 5-10 hour slightly slowly with respect to main fermentation, so with above-mentioned Traditional Method Starch Hydrolysis and saccharification halfway more than 50 hours long-time after fermentation essential distinction is arranged, all big such as great disparities such as unit interval material treating capacity and alcohol outputs.In addition, although the continuously fermenting of traditional method is in also at the beginning that the Primary Fermentation state promptly also saves the primary fermentation phase than the batch fermentation time for short, but because of saccharification and secondary fermentation total time long (saccharification about 50 hours, fermentation about 60-72 hour, about ATT 115 hours), exceed more than 90 hours about 20 hours than the present invention, deduct that aforesaid the present invention is formerly liquefied and 20 hours of expending approximately of saccharification, still exceed more than 70 hours, so its advantage highly significant still.

Secondary fermentation finishes the back gets wine or conventional method midway by aforementioned Primary Fermentation and extracts waste behind the alcohol, and the yeast slag is quality protein and nucleic acid (RNA) source, can fully utilizes, and stays in other application for a patent for invention and sets forth.

The inventive method also has following main advantages:

1, directly adopting Chinese sorghum is to produce the initiation material of starch sugar rather than adopt commodity starch, is conducive to reduce cost and fully utilize; Only Chinese sorghum is made sorghum flour breast (dry grinding method) rather than makes starch, be conducive to reduce the dust emission in organic wastewater discharging and the dry run, thereby environmental contamination reduction is saved great lot of water resources and energy consumption, grain consumption; Save factory building, equipment and labour, improve yield, reduce cost, shorten the production cycle, avoided pollution microbes to become sour and caused loss.

2, rationally utilize enzyme process and acid system to produce Dian Fentang advantage and mother liquor fermentation alcohol etc. separately and be used in combination order and comprehensive utilization, their shortcomings have separately been overcome, constant product quality, saccharification time is short, crystalline quality is good, the yield height, and can require according to the difference of quality to adjust simplified and traditional degree of production technique and operation, the market adaptability is strong.

3, because of the α-Dian Fenmei in any source all can be cut maltose, the direction unicity and the thoroughness that add acid hydrolytic reaction are very strong, enzymatic liquefaction and acid saccharification all seldom produce difficult disaccharide that utilizes of yeast such as maltose etc., and traditional enzyme glycolysis only contains a α-1 because of saccharifying enzyme is difficult to hydrolysis, the isomaltose of 6 keys, to containing two α-1, the isomaltose of 6 keys then fully can't hydrolysis, add that saccharifying enzyme can cause that the polymerization of glucose and its extent of polymerization also increase with sugared concentration and enzyme concn, transform (alcohol) rate about 3% and improve throughput and alcohol recovery rate and reduce cost so the present invention is beneficial to behind the further saving alcohol diastatic fermentation time and improves starch.

4, with the Chinese sorghum be starting raw material, adopt the method for enzyme acid direct production glucose only to need Chinese sorghum is made the newborn glucose that is converted into step by step of sorghum flour, Ye Huamei hydrolyzed starch under 85-93 ℃ of high temperature only takes at 1.5 to 2.5 o'clock, saccharification under vapour pressure 0.3-0.35 MPa pressure also only 20 to 25 minutes.

5, this project changes into the generation of adopting earlier enzyme to liquefy to prevent or reduce accessory substance in the glucose process at starch, and rear employing acid saccharification guarantees the stable of product quality and performances.

6, this project sorghum flour breast can directly be adjusted concentration for converted starch sugar.

7, the used enzyme of this project enzymatic liquefaction and acid saccharification production Dian Fentang is the high temperature a-amylase of sophisticated large-scale industrial production, used acid is similarly the hydrochloric acid of large-scale industrial production, used isomerase also is the industrialization enzyme, so raw materials cost is low secure.

8, this project enzyme and sour consumption few, press 50-60 units/gram over dry starch with the enzyme amount and calculate, reach 1.2-1.8 calculating with the acid amount by the saccharified liquid pH value.

Embodiment:

1, powder emery mill under the Chinese sorghum normal temperature is added tap water levigate (rotating speed is 1000 rev/mins) and become the powder emulsus, the control concentration of slurry is about 30%.It is 6.5 that hydrochloric acid is transferred PH; The disposable adding α-amylase (press a-amylase 50 units/gram over dry starch and calculate the enzyme amount that always needs) of required total amount that liquefies in liquefier, 90 ℃ of lower liquefactions about 2 hours, Iod R is disappeared, plate and frame filter press filter and remove residue (slag is made feed or food protein raw material), using HCL to transfer PH in stainless cylinder of steel is 1.5, and sour saccharification after 20 minutes under 0.3 MPa vapour pressure, neutralize with 15% sodium carbonate, and add the active carbon used for the first time in the decolouring of stainless steel decolouring bucket, plate and frame filter press filters, ion exchange resin desalination and the ash zwitterion that grades, evaporation and concentration is 1.3450/45 ℃ concentration to proportion under 0.06 MPa; In stainless steel cask, add new active carbon and decoloured in 26 minutes 75 ℃ of lower stirrings, plate compression, being concentrated to proportion for the second time under 0.06 MPa is 1.3450/45 ℃ of concentration, carries out crystallization at stainless steel motion crystallizing tank temp by 44-22 ℃ in 72 hours; Centrifuge centrifuge mother liquor (mother liquor fermentation with) is dried to water content below 9% in the ebullated dryer, pack final products glucose.This example is applicable to produces medicine sugar (oral and injection sugar), and its specification of quality is pressed the Chinese Pharmacopoeia standard.

2, powder emery mill under the Chinese sorghum normal temperature is added tap water levigate (rotating speed is 1000 rev/mins) and become the powder emulsus, the control concentration of slurry is about 30%.It is 6.5 that hydrochloric acid is transferred PH; The disposable adding Ye Huamei (press a-amylase 50 units/gram over dry starch and calculate the enzyme amount that always needs) of required total amount that liquefies in liquefier, 90 ℃ liquefied about 2 hours down, Iod R is disappeared, plate-and-frame filter press filter and remove residue (slag is made feed or food protein raw material), using HCL to transfer PH in stainless cylinder of steel is 1.5, and sour saccharification after 20 minutes under 0.3 MPa vapour pressure, neutralize with yellow soda ash (15%), adding for the first time, the exhausted gac decolours in stainless steel cask, filter press, ion-exchange, being concentrated to proportion under 0.065 MPa is 1.260/45, add new gac in the stainless steel cask and stir decolouring in 28 minutes down at 80 ℃, filter press, carrying out secondary concentration under 0.065 MPa vapour pressure is 1.3450/45 ℃ concentration to proportion, vacuum spray dehydrator spraying drying and granulation (moisture below 9%), pack final glucose product.This example is applicable to food, fermentation and crude dextrose production.The content of glucose and other quality requirement can or be carried out the contract standard (because of the quality standard of no unification of the motherland in these industries) of customer requirements or require the glucose standard with reference to the external same industry according to concrete purposes drawing up the enterprise standard.

3, powder emery mill under the Chinese sorghum normal temperature is added tap water levigate (rotating speed is 1000 rev/mins) and become the powder emulsus, the control concentration of slurry is about 30%.It is 6.5 that hydrochloric acid is transferred PH; The disposable adding α-amylase (press a-amylase 50 units/gram over dry starch and calculate the enzyme amount that always needs) of required total amount that liquefies in liquefier, 90 ℃ of lower liquefactions about 2 hours, Iod R is disappeared, plate and frame filter press filter and remove residue (slag is made feed or food protein raw material), using HCL to transfer PH in stainless cylinder of steel is 1.5, and sour saccharification after 20 minutes under 0.3 MPa vapour pressure, transferring PH with 10% sodium carbonate and 2% magnesium carbonate liquid is 4.9, and evaporation and concentration is 1.3450/45 ℃ concentration to proportion under 0.06 MPa; Or the mother liquor of embodiment 1 is added hydrochloric acid transfer PH to be 4.0-4.3, to add 10-15% sodium carbonate and 1-5% magnesium carbonate jointly to transfer PH be 4.5-5.1, be concentrated in vacuo to 30-35% concentration and get the alcoholic fermentation Glucose Liquid again, two kinds of Glucose Liquids are alone or share in alcoholic fermentation with any ratio; By number of yeast cells 1,000 ten thousand/milliliter bent, disposable adding, temperature is controlled at 33 ℃; When the temperature of zymotic fluid reduced gradually, plate and frame filter press separated alcohol liquid and yeast, alcohol is extracted in 33 ℃ of boilings of alcohol liquid negative pressure of vacuum; Mother liquor returns former tank with the yeast that separates and adds new sugar solution to demarcating volume, and plate and frame filter press separates alcohol liquid and yeast, alcohol is extracted in 30-34 ℃ of boiling of alcohol liquid negative pressure of vacuum when keeping 33 ℃ to continue fermentation, temperature reduction; Mother liquor returns former tank with the yeast that separates and adds new sugar solution to demarcating volume, change after fermentation phase of being equivalent to Traditional Method and technology and operation over to, continuing fermentation to no CO ₂Till the generation, take turns circulation and equipment is carried out beginning new round circulation behind the cleaning and sterilizing routinely with thorough end one; The yeast slag is reclaimed in the mother liquor press filtration, and harmless treatment is to the environment protection standard discharging, the yeast slag because of be rich in (more than the dry matter weight 5-8%) RNA nucleic acid and nucleic acid very costly (more than 100,000 yuan/tons), nucleic acid is carried in former separate case application; Residue protein amount height, event separate case application high protein high-quality feed.

Claims (1)

1, a kind of Chinese sorghum direct production Dian Fentang and residue-less rapid fermentation fuel alcohol method is characterized in that:

A Chinese sorghum dry grinding method is produced and under the rice powder emulsion normal temperature Chinese sorghum ground rotating speed with powder emery is that 800-1000 rev/min of stiffened water mill is fine into powder emulsus, concentration 25-30%, and it is 6.0-7.0 that hydrochloric acid is transferred PH;

B enzyme acid is produced Glucose Liquid the sorghum flour breast is pressed the disposable adding Ye Huamei of enzyme-added total amount of a-amylase 50-60 units/gram dry starch, carries out high temperature gelatinization and liquefaction under 90-93 ℃, remains to dextrose equivalent value 25-30 or disappears to Iod R; Conventional filtration removes slag; Filtrate is concentrated in vacuo to 30-35% concentration, adds hydrochloric acid accent PH to 1.2-1.8, and 0.3-0.35 MPa vapour pressure acid saccharification gets Glucose Liquid to DE value 90-95;

The production of c glucose for injection adds the neutralization of 10-15% yellow soda ash in the Glucose Liquid of producing glucose for injection, the activated carbon decolorizing after-filtration, plastic resin treatment is done ion-exchange, evaporation concentration is to 1.250/45 ℃ of concentration of proportion under the 0.06-0.067 MPa, under 70-80 ℃, add gac and stir 25-30 minute decolorization filtering, for the second time being concentrated to proportion under the 0.06-0.067 MPa is 1.3450/45 ℃ of concentration, carry out crystallization 50 hours inner control temperature by 44 ℃-22 ℃, centrifugal, vacuum-drying is arrived moisture content less than 5%, get injection high purity (the DE value is more than 99.5%) medicine glucose;

The production of d alcoholic fermentation Glucose Liquid adds 10-15% sodium carbonate and 1-5% magnesium carbonate with the described Glucose Liquid of c, and jointly to transfer PH be 4.5-5.1, with the described crystallization of d and centrifugal after mother liquor add hydrochloric acid and transfer PH to be 4.04.3, to add 10-15% sodium carbonate and 1-5% magnesium carbonate jointly to transfer PH be 4.5-5.1, be concentrated in vacuo to 30-35% concentration and get the alcoholic fermentation Glucose Liquid again, two kinds of alcoholic fermentations are alone or share with any ratio with Glucose Liquid;

E food with the production d of glucose syrup described in and Glucose Liquid be the food glucose syrup;

Be spray dried into water content with Glucose Liquid during f food is described with d with the production of glucose and get food glucose below 5%;

The production of g oral glucose is spray dried into water content with the Glucose Liquid after concentrating d described for the second time and meets standards of pharmacopoeia and get oral glucose;

The production of h crude dextrose with the described crystallization of d and centrifugal after mother liquor concentrate again, be spray dried into water content below 5% industrial sugar;

The production of i HFCS becomes fructose with equipment with a part of conversion of glucose in the described glucose syrup of e with conventional isomerase and consumption, conventional ion exchange refining HFCS;

The production of j fructose syrup is with the conventional separating levulose slurry of the described high fructose syrup of i;

The production of k fructose gets fructose with the described fructose syrup spraying drying of j;

The fermentation of l fuel alcohol and extraction: by number of yeast cells 1-5 10,000,000/milliliter bent, disposable adding, temperature is controlled at 30-34 ℃; When the temperature of zymotic fluid began to reduce, press filtration separated alcohol liquid and yeast, alcohol is extracted in 30-34 ℃ of boiling of alcohol liquid negative pressure of vacuum; Mother liquor returns former tank with the yeast that separates and adds new sugar solution to demarcating volume, and press filtration separates alcohol liquid and yeast, alcohol is extracted in 30-34 ℃ of boiling of alcohol liquid negative pressure of vacuum when keeping 30-34 ℃ to continue fermentation, temperature reduction; Mother liquor returns former tank with the yeast that separates and adds new sugar solution to demarcating volume, continuing fermentation to no CO ₂Generation, the conventional alcohol that extracts.