CN104719616B - A kind of method of the utilization wheaten starch processing byproduct pentosan slurry production rich in functional oligose feed addictive - Google Patents
A kind of method of the utilization wheaten starch processing byproduct pentosan slurry production rich in functional oligose feed addictive Download PDFInfo
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- CN104719616B CN104719616B CN201510141890.2A CN201510141890A CN104719616B CN 104719616 B CN104719616 B CN 104719616B CN 201510141890 A CN201510141890 A CN 201510141890A CN 104719616 B CN104719616 B CN 104719616B
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- pentosan
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- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P60/00—Technologies relating to agriculture, livestock or agroalimentary industries
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- Y02P60/87—Re-use of by-products of food processing for fodder production
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Abstract
The invention discloses a kind of method of utilization wheaten starch processing byproduct pentosan slurry production rich in functional oligose feed addictive.This method includes mixing wheaten starch processing byproduct pentosan slurry, wheat bran and yeast extract, then through fermentation of Aspergillus niger, and tunning centrifugation takes supernatant to be spray-dried, that is, obtains being rich in functional oligose feed addictive.Discarded object in wheaten starch process has been made the method for the invention as raw material promotes animal intestinal tract health, enhancing immunity of organisms and the animal feed additive for improving production performance.
Description
Technical field
The invention belongs to field of feed processing.Wheaten starch processing byproduct pentosan is utilized more particularly, to one kind
Method of the slurry production rich in functional oligose feed addictive.
Background technology
Industrialized production wheaten starch is a kind of wet physical separation process, according to the difference of separation method, production method
Often there are Martin's method, Rui Xiufa, vortex method and three-phase decanter method etc..It is sleeping for three-phase that the more advanced method of wheaten starch is extracted at present
Spiral shell method, three-phase decanter process is the wheaten starch and Gluten separation method of a kind of newer type of Germany's exploitation.It is because in technique
Employ uniqueness patented technology --- three-phase decanter seperator and gain the name.
Pentosan slurry is the light phase material being centrifugally separating to obtain through three-phase decanter during wheat starch production, its mainly into
Dividing includes the nutriments such as Crude starch, pentosan, crude protein.If not handling pentosan slurry, directly discharge, certainly will cause
The a large amount of wastes and the pollution of environment of resource, also seriously govern the development of enterprise.The main difficulty recycled is caused at present
It is due to that water content is higher during pentosan is starched, dry is low, and stickiness is big.It is existing on pentosan starch recycle research and
Report is concentrated mainly on the following aspects：
(1) concentration is dried：Pentosan slurry is by alpha-amylase enzymatic liquefaction, and three-effect counter flow formula falling liquid film negative pressure evaporation is dense
Contracting, the flow such as is concentrated under reduced pressure and is spray-dried, obtain pentosan dry powder.
(2) pentosan and protein are therefrom extracted：On the one hand research is to utilize evaporation, centrifugation, homogeneous and atomization drying etc.
Serial of methods directly extracts pentosan and protein, on the other hand then first by physics or biological enzymolysis means removal of impurities, then
Purified using organic solvent.
(3) production fermentation series of products：Pentosan slurry produces protein feed, calcium lactate, alcohol and fourth as fermenting raw materials
Alcohol, or it is used as medium culture microorganism, such as asparagus, biological flocculant.
Above-mentioned (1) is related to HTHP, requires higher to production equipment；(2) then complex disposal process, put into it is larger,
Industrialization is more difficult；And have reaction condition gentle using biofermentation, the advantages of process is easy.The inventive method utilizes aspergillus niger
Fermentation pentosan slurry, wherein will have anti-nutritional pentosan to degrade, and obtain having promotion animal intestinal tract health, enhancing machine
Therefore body immunity and the functional oligose for improving production performance, pentosan slurry nutritive value get a promotion.Meanwhile, pentosan
Crude starch and crude protein in slurry can as growth carbon source and nitrogen source, raw material is fully used, and has been truly realized change
Waste be changed into values, and a new effective way is provided so as to be utilized for pentosan slurry high efficiente callback.
The content of the invention
It is an object of the invention to provide a kind of discarded object for being directed to and being produced in three-phase decanter wheat starch production technical process
Application way, i.e., the light phase material rich in pentosan being centrifugally separating to obtain to three-phase decanter machine carries out twice laid, production
Method rich in functional oligose feed addictive.
To reach above-mentioned purpose, the technical scheme that the present invention takes is：
Raised the invention provides one kind using the slurry production of wheaten starch processing byproduct pentosan rich in functional oligose
The method of feed additives, this method includes mixing wheaten starch processing byproduct pentosan slurry, wheat bran and yeast extract, Ran Houjing
Fermentation of Aspergillus niger, tunning centrifugation, takes supernatant to be spray-dried, that is, obtains rich in the addition of functional oligose feed
Agent.
In the above method, the preferred weight ratio of the wheaten starch processing byproduct pentosan slurry, wheat bran and yeast extract is
50:(2-3):(0.1-0.2)。
Further, the specific method of fermentation of Aspergillus niger of the present invention is：(1) aspergillus niger spore suspension is prepared；(2) will
The aspergillus niger spore suspension is that 1%-2% is inoculated with according to inoculum concentration；(3) 37 DEG C, rotating speed 150-180r/min and aerobic
Under the conditions of carry out liquid state fermentation, fermentation time is 60-70h.
Wherein it is preferred to, the concentration of the aspergillus niger spore suspension is 1 × 107-5×107Individual/ml.The black-koji mould
It is CMCC (F) 98003 to plant.
In the present invention, the wheaten starch processing byproduct pentosan slurry is sleeping through three-phase in wheaten starch process
The light phase material that spiral shell is centrifugally separating to obtain.Its main component includes the nutriments such as Crude starch, pentosan, crude protein.
In order to reach more preferable effect, it is ensured that product quality, it is preferable that the wheat bran is first crushed, 60 mesh sieves are then crossed, then
Mixed with pentosan slurry and yeast extract.
In the present invention, the spray drying is the routine operation of this area, it is preferable that it is inlet temperature to control its condition
For 150-180 DEG C, 70-80 DEG C of air outlet temperature, wriggling revolution speed 9-12r/min, operating pressure 0.25-0.3Mpa.
Content of reducing sugar is 20%-24% in the feed addictive prepared using the method for the invention, and total reducing sugar contains
Measure as 39%-48%, xylo-oligosaccharide content is 9%-14%.By the method for the invention to wheaten starch processing byproduct penta
Glycan slurry carries out fermentation process, and pentosan degradation rate reaches 60%-80%.
Compared with existing pentosan slurry recovery and utilization technology, the beneficial effects of the invention are as follows：Pentosan slurry is sent out through aspergillus niger
After ferment, having certain anti-nutritional pentosan to be degraded to promoting to nonruminant, animal intestinal tract is healthy, strengthen body
Immunity and the xylo-oligosaccharide for improving production performance, the nutritive value of pentosan slurry are greatly improved, and production technology is easy, equipment
It is required that low, raw material availability is high, is adapted to industrialized production.
Brief description of the drawings
Fig. 1 is production technology schematic diagram of the invention.
Fig. 2 is the high performance liquid chromatography detection figure of the tunning of the present invention.(xylobiose:7.222min；Xylotriose:
6.637min；Xylotetrose:6.459min)
Embodiment
In order to illustrate more clearly of the present invention, with reference to preferred embodiment, the present invention is described further.Ability
Field technique personnel should be appreciated that following specifically described content is illustrative and be not restrictive, and this should not be limited with this
The protection domain of invention.
Embodiment 1
First, optimal bacterial screening technique：
(1) prepared by seed culture medium (PDA)：Distilled water 1000mL, potato leaches powder 6g, glucose 20g, agar 16g,
115 DEG C of sterilizing 30min.
(2) prepared by strain：The mould activated is accessed in PDA culture medium with oese, incubated 3-4d at 30 DEG C,
Treat that spore is ripe.
(3) prepared by spore suspension：Spore is eluted with appropriate sterilized water, the shaking flask equipped with bead is inserted
In, 140r/min levels concussion 1h, after being counted through blood cell plate, it is 1 × 10 that concentration, which is made,7-5×107Individual/mL spore suspension.
(4) fermentation medium：Pentosan is starched：100ml；Wheat bran (crosses 60 mesh sieves)：2g；Yeast extract：250mg；121 DEG C of high temperature
Sterilize 20min
(5) Xylanase activity and xylo-oligosaccharide content in each strain fermentating liquid are determined, as a result as shown in table 1, is passed through
Compare, it is aspergillus niger CMCC (F) 98003 to establish optimal fermented bacterium.
Xylanase activity and xylo-oligosaccharide content in each strain fermentating liquid of table 1
2nd, material preparation technology：
(1) prepared by seed culture medium (PDA)：Distilled water 1000mL, potato leaches powder 6g, glucose 20g, agar 16g,
115 DEG C of sterilizing 30min.
(2) prepared by strain：The aspergillus niger CMCC (F) 98003 activated is accessed in PDA culture medium with oese, 30 DEG C
Under incubated 3-4d, treat that spore is ripe.
(3) prepared by spore suspension：Spore is eluted with appropriate sterilized water, the shaking flask equipped with bead is inserted
In, 140r/min levels concussion 1h, after being counted through blood cell plate, it is 1 × 10 that concentration, which is made,7-5×107Individual/mL spore suspension.
(4) prepared by zymotic fluid：By wheaten starch processing byproduct pentosan slurry, (in wheaten starch process, three-phase crouches
The light phase material that spiral shell is centrifugally separating to obtain), wheat bran (crushing 60 mesh) and yeast extract be according to 1250:50:3 ratio is separately added into
In fermentation tank, after stirring, 121 DEG C of high-temperature sterilization 30min.
3rd, zymotechnique
About 1%-2% spore suspension is added in above-mentioned zymotic fluid, it is 37 DEG C, throughput 1 to control temperature:1.4-1:
1.8, pH value 6-7, stir speed (S.S.) 150-180r/min, fermentation tank tank pressure 60-80kpa.Ferment 60-70h, terminates fermentation, instantaneously
115 DEG C of sterilizing 10min of high temperature；Centrifuged after temperature is down to normal temperature, collect supernatant.
3rd, drying process with atomizing
The supernatant that above-mentioned steps are obtained is spray-dried, the inlet temperature for controlling drying process with atomizing is 150-
180 DEG C, 70-80 DEG C of air outlet temperature.Wriggling revolution speed 9-12r/min, operating pressure 0.25-0.3Mpa.Finally it is made and is rich in
The feed addictive of functional oligose.Utilize wooden two~Xylotetrose content (chromatogram in high effective liquid chromatography for measuring supernatant
Condition is with reference to GB/T23747-2009), DNS methods determine reduced sugar and total sugar content.
The weanling pig of embodiment 2 feeds contrast test
(1) experimental design
Select initial between 126 body weight three way cross close with age in days (Du × length × big) healthy weanling pig, each group
Body weight is without significant difference (P>0.05) 3 groups, are randomly divided into, every group of 6 repetitions each repeat 7 piglets, experimental period 28d.3
Component is：Control group (basal diet), I group (xylo-oligosaccharide commercially available from basal diet+250mg/kg), II group (basal diet+
The feed additive of 875mg/kg embodiments 1).Xylo-oligosaccharide content is consistent in I group and II group of daily ration.
The basal diet formula table of table 2
| Project | Content % |
| Corn (1 grade) | 70.00 |
| Dregs of beans (2 grades) | 13.00 |
| Fish meal | 7.00 |
| Low albumen whey powder | 1.00 |
| Soybean oil | 0.17 |
| Corn protein powder | 6.00 |
| 98.5% hydrochloric acid relies ammonia | 0.43 |
| Stone flour | 0.60 |
| Calcium monohydrogen phosphate | 0.60 |
| Salt | 0.20 |
| Premix | 1.00 |
| Trophic level | |
| DE(MJ/kg) | 13.86 |
| Crude protein | 19.18 |
| Lysine | 1.25 |
| Methionine | 0.39 |
| Calcium | 0.73 |
| Total phosphorus | 0.61 |
Note：140mg containing Fe in every kilogram of premix, Zn150mg, Mn 40mg, Cu105mg, I0.60mg, VA
14250IU, VD33188IU, VE 78IU, VK 5.6mg, VB16.4mg, VB216mg, VB346mg, VB4280mg,
VB560mg, VB110.77mg, VH 0.6mg, V1266.8 μ g, choline 0.55g.
(2) result of the test
The weanling pig of table 3 feeds comparative test result table
| Project | Control group | Ⅰ | Ⅱ |
| Average daily gain (g) | 534.63±84.02 | 602.06±139.80 | 606.67±86.58 |
| Average daily gain (g) | 283.74±43.28 | 333.44±79.97 | 344.13±50.68 |
| Feed-weight ratio | 1.88±0.09 | 1.81±0.07 | 1.77±0.14 |
As shown in Table 3, fed in identical under condition and basal diet, prepared by the addition present invention raises rich in xylo-oligosaccharide
Test group (II) growth performance of material component is substantially better than control group (P ＜ 0.05), and xylo-oligosaccharide contains in guarantee test daily ration
In the case that amount is consistent, II group of feeding effect of experiment is also better than the commercially available xylo-oligosaccharide group (I) of addition.
Embodiment 3
This experiment will be formed sediment with identical zymotechnique with the strain fermentation pentosan sterlings of aspergillus niger CMCC (F) 98003 and wheat
The ferment effect and product of powder processing byproduct pentosan slurry are compared.
1 materials and methods
1.1 pentosan solution：Tri- parts of pentosan 0.638g is weighed, plus distilled water is configured to three parts of 50mL pentosans solution.
The collection of 1.2 tunnings
50mL pentosans solution and 50mL wheaten starch processing byproducts pentosan are starched with the zymotechnique in embodiment 1
Fermented simultaneously (three repetitions respectively), centrifuging and taking supernatant carries out spray drying process drying.Determine zytase in dry powder
Work, total reducing sugar, reduced sugar and xylo-oligosaccharide content, and gross protein value.
2 results
Nutrition content is shown in Table 4 in dry powder after fermentation.
The fermentation pentosan of table 4 and nutrition content in fermentation pentosan slurry product
As shown in Table 4, fermentation pentosan slurry is compared with the pentosan that ferments, and xylanase activity improves 11.11% (P ＜
0.05), total sugar content improves 15.18% (P ＜ 0.05), and xylo-oligosaccharide content improves 28.17% (P ＜ 0.05).In addition, thick egg
White matter content pole is significantly improved 12 times (P ＜ 0.01).
The above embodiment of the present invention explanation is with the method for the invention fermentation wheaten starch processing byproduct pentosan
Slurry is achieved than the simple fermentation more preferable effect of pentosan sterling, to improve starch processing economic benefit added value, reducing resource
Waste and environmental pollution provides good solution and theoretical direction.
Obviously, the above embodiment of the present invention is only intended to clearly illustrate example of the present invention, and is not pair
The restriction of embodiments of the present invention, for those of ordinary skill in the field, may be used also on the basis of the above description
To make other changes in different forms, all embodiments can not be exhaustive here, it is every to belong to this hair
Row of the obvious changes or variations that bright technical scheme is extended out still in protection scope of the present invention.
Claims (6)
1. a kind of method of the utilization wheaten starch processing byproduct pentosan slurry production rich in functional oligose feed addictive,
Characterized in that, this method includes mixing wheaten starch processing byproduct pentosan slurry, wheat bran and yeast extract, then through black song
Mould CMCC (F) 98003 is fermented, tunning centrifugation, takes supernatant to be spray-dried, that is, obtains raising rich in functional oligose
Feed additives, wherein, the weight ratio of the wheaten starch processing byproduct pentosan slurry, wheat bran and yeast extract is 50:（2-3）:
（0.1-0.2）；Content of reducing sugar is 20%-24% in the feed addictive, and total sugar content is 39%-48%, xylo-oligosaccharide content
For 9%-14%.
2. according to the method described in claim 1, it is characterised in that the specific method of the fermentation of Aspergillus niger is：（1）Prepare black
Aspergillus spore suspension；（2）The aspergillus niger spore suspension is inoculated with according to inoculum concentration for 1%-2%；（3）37 DEG C, rotating speed
Liquid state fermentation is carried out under 150-180r/min and aerobic conditions, fermentation time is 60-70h.
3. method according to claim 2, it is characterised in that the concentration of the aspergillus niger spore suspension is 1 × 107-5×
107Individual/ml.
4. according to the method described in claim 1, it is characterised in that the wheaten starch processing byproduct pentosan slurry is wheat
The light phase material being centrifugally separating to obtain in starch process through three-phase decanter.
5. according to the method described in claim 1, it is characterised in that the wheat bran is size-reduced, cross 60 mesh sieves.
6. according to the method described in claim 1, it is characterised in that the condition of the spray drying is that inlet temperature is 150-
180 DEG C, 70-80 DEG C of air outlet temperature, wriggling revolution speed 9-12 r/min, operating pressure 0.25-0.3 Mpa.
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Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1144457A (en) * | 1994-03-02 | 1997-03-05 | 诺沃挪第克公司 | Processing plant material with xylanase |
| CN102573516A (en) * | 2009-04-24 | 2012-07-11 | 丹尼斯科有限公司 | Feed supplement |
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2015
- 2015-03-27 CN CN201510141890.2A patent/CN104719616B/en active Active
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1144457A (en) * | 1994-03-02 | 1997-03-05 | 诺沃挪第克公司 | Processing plant material with xylanase |
| CN102573516A (en) * | 2009-04-24 | 2012-07-11 | 丹尼斯科有限公司 | Feed supplement |
Non-Patent Citations (1)
| Title |
|---|
| 戊聚糖浆对断奶仔猪生长性能、腹泻率和血清生化指标的影响;尹文飞等;《中国畜牧兽医学会动物营养学分会第七届中国饲料营养学术研讨会论文集》;20141016;第40页 * |
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