CN102308908B - Puffing techniques for soybean and feed and products produced by same - Google Patents
Puffing techniques for soybean and feed and products produced by same Download PDFInfo
- Publication number
- CN102308908B CN102308908B CN2010102178068A CN201010217806A CN102308908B CN 102308908 B CN102308908 B CN 102308908B CN 2010102178068 A CN2010102178068 A CN 2010102178068A CN 201010217806 A CN201010217806 A CN 201010217806A CN 102308908 B CN102308908 B CN 102308908B
- Authority
- CN
- China
- Prior art keywords
- soybean
- microwave
- mass percent
- mixed feed
- heating
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Images
Landscapes
- Fodder In General (AREA)
Abstract
The invention discloses a puffing technique for a soybean. The puffing technique includes the following steps: (1) soybeans are immersed aqueous solution containing tschermigite or sodium bicarbonate and salt or cane sugar for more than two hours, wherein the tschermigite or sodium bicarbonate is 0.2 to 2 percent by mass, and the salt or cane sugar is 0.2 to 5 percent by mass; (2) the products obtained in step 1 are dried until the moisture content in the soybeans is 10 to 30 percent by mass; (3) the products obtained in step 2 are heated by microwave, and thereby puffed soybeans are produced. The invention also discloses the soybean produced by the puffing technique, a puffing technique for a compound feed and the compound feed produced by the puffing technique. In the puffing techniques, the soybean-puffing effect is good, the cost is low, and nutrient loss is little.
Description
Technical field
The bulking process that the present invention is specifically related to a kind of soybean and feed reaches by its product that makes.
Background technology
Expanded structuring or the systematism of claiming again, expanded generation starch gelatinization, destroy the ANFs in the raw material and have the effect of eliminating various bacteriums, utilize expanded principle that feedstuff is carried out preliminary treatment, nutritive loss is few in the expanding processing process, can reach the purpose that improves protein, being conducive to animal digestion absorbs, therefore some cheap raw materials are through expanding treatment, can replace valuable raw material, and do not affect quality of the fodder, reduced cost, the exploitation feed resource has been played important function, as required can expanded full-fat bean, corn, millet, dregs of rice class (is used for supporting lonely, ermine, ground squirrel, otter), feed for pet (is used for supporting dog, cat), feeding feed stuff and view and admire the class animal feed and (be used for shrimp in the water, crab, eel, catfish, the floating feed such as goldfish and batrachia), livestock and poultry pellet, but puffed rice, corn, jowar is as the materials such as inserts of food and foundry binders.
Microwave is that frequency is at the electromagnetic wave of 300 megahertzes to 300 gigahertzs.The material medium is by polar molecule and nonpolar molecule tissue, and under electromagnetic field effect, these polar molecules transfer to according to direction of an electric field from the random distribution state and carry out orientations.And under the microwave electromagnetic field action, these orientation movements constantly change with the billions of inferior frequencies of per second.Cause strenuous exercise and the collision friction of molecule, thereby produce heat, reach electric energy and be converted into the interior heat energy of medium.Therefore, heating using microwave is dielectric material own loss electric field energy and generating heat.
Microwave applications has following advantage in feedstuff processing: heating using microwave is to carry out the surface integral body heating consistent with inside by microwave energy and feedstuff direct interaction, and firing rate is fast, the time is short, product quality is high, homogeneous heating.And heating process has the automatic thermal balance performance, is quick on the draw to be easy to control, and the thermal efficiency is high, and occupation area of equipment is few etc.
The microwave bulking technology is a special applications of micro-wave drying.Its principle is that microwave energy arrives material deep layer energy transform into heat energy, to make material deep layer moisture evaporate rapidly the higher internal vapor pressure of formation, force material expanded, and the expansive force that relies on gas drives the structure sex change of polymer substance in the component, have network structure's feature thereby make it to become, typing becomes the process of cellular material.
Recent years, along with people deepen the understanding of expanded full-fat bean nutritive value and the gradual perfection of bulking process, full-fat bean just more and more is used for the feeds such as broiler chicken, piglet as high energy high protein feed resource, in production of fodder, reduce cost with full-fat bean, increase the benefit, tool is of great significance.
Traditional expanded soybean is that whole soybean carried out hot-working with expanded machinery equipment, and expanding treatment forms.Expanding treatment is in order to make cell wall rupture, to increase its nutritional utilization and be worth, especially having improved the utilization rate of grease.Traditional extrusion is that soybean enters the machine thorax to extruding finished product less than 30s, curing temperature in process can reach 130～145 ℃ Celsius, to destroy ANFs, be unfavorable for the composition of animal digestion as trypsin ihhibitor, urease, hemagglutinin etc.According to years of researches, expanded pellet diet has many advantages, and also simultaneously with the shortcomings such as destruction of HTHP to the part nutriment, the nutritionist designs a lot of ways and deals with, but still some fine solutions of failing are arranged.
And microwave bulking process time is short, the energy-and time-economizing, and the nutritional labeling storage rate is high, and expanded, sterilization, drying are finished simultaneously.Therefore, microwave applications can overcome the shortcomings such as extrusion content is high, energy consumption is large in the production of expanded pellet diet raw material, has very wide application prospect in feed industry production.
In recent years, the production stable development of China's grain, herding and aquatic products, output significantly improves, and plurality of raw materials is badly in need of transforming processing, and therefore, the dilated product of feed and the production of dilated product are the certainty of industrial development.
Summary of the invention
Technical problem to be solved by this invention is that heat loss is large in existing soybean and the expanded feed technique, cost is high in order to overcome, the defective that nutritive loss is large, and provide the bulking process of a kind of soybean and feed to reach by its product that makes.In the bulking process of the present invention, soybean puffing is effective, cost is low, nutritive loss is few.
The present invention relates to the bulking process of a kind of soybean, it comprises the following step:
(1) soybean is being comprised ammonia-alum (NH
4Al (SO
4)
212H
2O) or sodium bicarbonate (NaHCO
3), and soaked in the aqueous solution of salt and/or sucrose 2～24 hours, wherein, the mass percent of ammonia-alum or sodium bicarbonate is 0.2%～2%, the mass percent of salt and/or sucrose is 0.2%～5%;
(2) product with step (1) gained carries out drying, and making the water content in the soybean is mass percent 10%～30%;
(3) product with step (2) gained carries out heating using microwave, gets final product to get expanded soybean.
In the step (1), what the time of described immersion was better is 3～6 hours; What the mass percent of ammonia-alum or sodium bicarbonate was better is 0.5%～1%; What the mass percent of salt and/or sucrose was better is 0.5%～1%.
In the step (2), the method for described drying better for naturally drying or drying up with air blast.
In the step (3), better, described heating using microwave comprises the following steps: the soybean that step (2) makes is inserted feeding warehouse, under the transmission device effect, soybean is transported to the heating using microwave district, heating using microwave 60-180 second, be transported to again discharging opening, blower cools.
Among the present invention, in described heating using microwave, microwave output power 12KW-400KW; Input apparent energy 15KWA-450KWA; What the equipment operating voltage was better is three-phase 380V ± 10%; That microwave operational frequencies is better is 2450MHz ± 50Hz.The process of heating using microwave also can comprise the process with the soybean slaking.What the time of heating using microwave was better is 60-180 second, and better is 90-120 second.
The invention further relates to the expanded soybean that the bulking process of above-mentioned soybean makes.
Among the present invention, after the bulking process of soybean, can soybean be packed according to the packing method of routine, make feedstuff.
The invention still further relates to a kind of preparation method of mixed feed, it comprises the following step: the above-mentioned expanded soybean after will pulverizing adds in the mixed feed, then carries out routine and granulates, and gets final product.Wherein, the mass percent of described expanded soybean in mixed feed is 1%-25%, and better is 5%～15%.
The invention further relates to the mixed feed that above-mentioned preparation method makes.
The invention still further relates to a kind of bulking process of mixed feed, it comprises the following step: with soybean and water, and ammonia-alum or sodium bicarbonate, and raw material commonly used mixes in the mixed feed of this area, the salt and/or the sucrose that also comprise mass percent 0.2%～1% in the mixed feed, then conventional the granulation or pulverizing carry out heating using microwave, gets final product; In mixed feed, the mass percent of soybean is 5%～30%, and the mass percent of water is 10%～30%, and the mass percent of ammonia-alum or sodium bicarbonate is 0.2%～5%.Wherein, each condition of described heating using microwave is all ditto described, the microwave heating process that is about to aforementioned base materials and is soybean become raw material be above-mentioned conventional granulate or pulverize after feed get final product.
Wherein, in the mixed feed of described this area raw material commonly used better be in corn, wheat, dregs of beans, rapeseed dregs and the cotton dregs one or more.
The invention still further relates to the feed that the bulking process of above-mentioned mixed feed makes.
Among the present invention, described salt, ammonia-alum and sugar are all better to be conventional commercially available food grade.
Except specified otherwise, raw material of the present invention and reagent is commercially available getting all.
Positive progressive effect of the present invention is:
1, soybean puffing technique of the present invention and mixed feed bulking process are compared with the extruding-puffing technique of routine, and expansion rate is high, and the nutritional labeling loss is few.
The feed that the bulking process of 2, expanded soybean of the present invention, and mixed feed makes can be mass-produced, and it is expanded that output is higher than conventional extrusion.
3, the energy consumption of soybean puffing technique of the present invention and mixed feed bulking process is expanded far below conventional extrusion.
4, soybean puffing technique of the present invention and mixed feed bulking process are safe and reliable, stay in grade, and the animal good palatability of products obtained therefrom can be eliminated the ANFs in the feed effectively, and with low cost, can increase substantially the feeding value of feed.
Description of drawings
Fig. 1 is the expansion effect figure of the expanded soybean that makes of embodiment 4 and 9.
Fig. 2 is the expansion effect figure of the expanded soybean that makes of embodiment 6 and 11.
The specific embodiment
The below further specifies the present invention with embodiment, but the present invention is not limited.
Embodiment 1
Take middle swine feed (raw materials used buy for conventional market) as example.
According to the concrete formula rate of table 1, preparation microwave bulking mixed feed.Each homogeneous chemical composition is mixed, granulate, get final product.Wherein, the moisture in the mixed feed requires between the 10%-30%.
Microwave bulking technique: take the microwave equipment model of roc continent, Guangzhou microwave equipment Co., Ltd production: PZ-30MT as example, adopt the continuous swelling method.Microwave parameters is: microwave output power: 12KW (adjustable); Input apparent energy: 30KWA; Equipment operating voltage: three-phase 380V ± 10%; Microwave operational frequencies: 2450MHz ± 50Hz.Microwave treatment time is 90 seconds.
The computing formula of puffed degree is: expansion rate=(the expanded front volume of expanded rear volume ÷) * 100%
After expanded, carry out the cold wind cooling.
Swine feed prescription in the table 1
| The raw material numbering | Material name | Cost of material/unit | Content % |
| 1401 | Corn | 1800 | 50.0 |
| 1582 | Full-fat bean | 3900 | 13.0 |
| 1502 | Soybean Meal | 3000 | 11.0 |
| 1406 | Wheat | 1400 | 10.0 |
| 1473 | Cotton dregs | 3000 | 2.0 |
| 2010 | Wheat bran | 1320 | 10.0 |
| 2015 | Fish meal (CP62.5) | 6300 | 1.0 |
| 9006 | B B-complex | 18000 | 0.2 |
| 9110 | The complex mineral element | 12000 | 0.5 |
| 1610 | Calcium monohydrogen phosphate | 1300 | 0.9 |
| 1800 | Lysine (Lys) | 20000 | 0.46 |
| 1642 | Zinc oxide | 8000 | 0.32 |
| 1803 | Methionine (DL-Met) | 23000 | 0.31 |
| 1600 | Stone flour | 120 | 0.9 |
| 1805 | Threonine (Thr) | 30000 | 0.11 |
| 1615 | Salt | 1000 | 0.3 |
| 1253 | Sodium bicarbonate | 1200 | 0.3 |
Its expansion rate is 136.7%
Embodiment 2
Take middle swine feed (raw materials used buy for conventional market) as example.
Raw material proportioning, bulking process change the sodium bicarbonate in the raw material into ammonia-alum with example 1.
Equally reach the effect of expanded pellet diet with example 1.
Its expansion rate is 142.5%
Embodiment 3
Take feedstuff soybean (commercially available) as example.
The water soaking soybean of the salt with 0.3% and 0.2% ammonia-alum 3 hours dries or dries, and wherein, the moisture in the soybean requires 10%-30%.
Microwave bulking technique: take the microwave equipment model of roc continent, Guangzhou microwave equipment Co., Ltd production: PZ-30MT as example, adopt the continuous swelling method.Microwave parameters is: microwave output power: 45KW (adjustable); Input apparent energy: 30KWA; Equipment operating voltage: three-phase 380V ± 10%; Microwave operational frequencies: 2450MHz ± 50Hz.Microwave treatment time is 90 seconds.
The soybean puffing rate is up to 150%.Nutrition (vitamin, amino acid, protein etc.) is lost less, fragrance is dense, the mouthfeel delicious and crisp.
The computing formula of puffed degree is: expansion rate=(the expanded front volume of expanded rear volume ÷) * 100%
After expanded, carry out the cold wind cooling.
Expansion rate is 158.6%
Embodiment 4
Take feedstuff soybean (commercially available) as example.
The water soaking soybean of the salt with 0.3% and 0.8% ammonia-alum 3 hours dries or dries, and wherein, the moisture in the soybean requires greater than 10%-30%.
The same example of microwave parameters, microwave treatment time are 90 seconds.After expanded, carry out the cold wind cooling.The microwave bulking effect is seen Fig. 1.
Expansion rate is 172.5%
Embodiment 5
Take feedstuff soybean (commercially available) as example.
The water soaking soybean of the salt with 0.3% and 2% ammonia-alum 3 hours dries or dries, and wherein, the moisture in the soybean requires greater than 10%-30%.
The same example of microwave parameters, microwave treatment time are 90 seconds.After expanded, carry out the cold wind cooling.
Expansion rate is 170.3%
Embodiment 6
Take feedstuff soybean (commercially available) as example.
The water soaking soybean of the salt with 0.3% and 0.2% sodium bicarbonate 3 hours dries or dries, and wherein, the moisture in the soybean requires greater than 10%-30%.
Microwave bulking technique: take the microwave equipment model of roc continent, Guangzhou microwave equipment Co., Ltd production: PZ-30MT as example, adopt the continuous swelling method.Microwave parameters is: microwave output power: 45KW (adjustable); Input apparent energy: 30KWA; Equipment operating voltage: three-phase 380V ± 10%; Microwave operational frequencies: 2450MHz ± 50Hz.Microwave treatment time is 90 seconds.
The computing formula of puffed degree is: expansion rate=(the expanded front volume of expanded rear volume ÷) * 100%.
After expanded, carry out the cold wind cooling.Expansion effect is seen Fig. 2.
The soybean puffing rate is up to 152%.
Embodiment 7
Take feedstuff soybean (commercially available) as example.
The water soaking soybean of the salt with 0.3% and 0.8% sodium bicarbonate 3 hours dries or dries, and wherein, the moisture in the soybean requires greater than 10%-30%.
The same example of microwave parameters, microwave treatment time are 90 seconds.After expanded, carry out the cold wind cooling.
The soybean puffing rate is up to 156%.
Embodiment 7
Take feedstuff soybean (commercially available) as example.
The water soaking soybean of the salt with 0.3% and 2% sodium bicarbonate 3 hours dries or dries, and wherein, the moisture in the soybean requires greater than 10%-30%.
The same example of microwave parameters, microwave treatment time are 90 seconds.After expanded, carry out the cold wind cooling.
The soybean puffing rate is up to 160.5%.
Embodiment 8
Take feedstuff soybean (commercially available) as example.
The water soaking soybean of the sucrose with 0.3% and 0.2% ammonia-alum 3 hours dries or dries, and wherein, the moisture in the soybean requires 10%-30%.
Microwave bulking technique: take the microwave equipment model of roc continent, Guangzhou microwave equipment Co., Ltd production: PZ-30MT as example, adopt the continuous swelling method.Microwave parameters is: microwave output power: 45KW (adjustable); Input apparent energy: 30KWA; Equipment operating voltage: three-phase 380V ± 10%; Microwave operational frequencies: 2450MHz ± 50Hz.Microwave treatment time is 90 seconds.
The soybean puffing rate is up to 150%.Nutrition (vitamin, amino acid, protein etc.) is lost less, fragrance is dense, the mouthfeel delicious and crisp.
The computing formula of puffed degree is: expansion rate=(the expanded front volume of expanded rear volume ÷) * 100%
After expanded, carry out the cold wind cooling.
Expansion rate is 150.1%
Embodiment 9
Take feedstuff soybean (commercially available) as example.
The water soaking soybean of the sucrose with 0.3% and 0.8% ammonia-alum 3 hours dries or dries, and wherein, the moisture in the soybean requires greater than 10%-30%.
The same example of microwave parameters, microwave treatment time are 90 seconds.After expanded, carry out the cold wind cooling.The microwave bulking effect is seen Fig. 1.
Expansion rate is 170.2%
Embodiment 10
Take feedstuff soybean (commercially available) as example.
The water soaking soybean of the sucrose with 0.3% and 2% ammonia-alum 3 hours dries or dries, and wherein, the moisture in the soybean requires greater than 10%-30%.
The same example of microwave parameters, microwave treatment time are 90 seconds.After expanded, carry out the cold wind cooling.
Expansion rate is 169.3%
Embodiment 11
Take feedstuff soybean (commercially available) as example.
The water soaking soybean of the salt with 0.3% and 0.2% sodium bicarbonate 3 hours dries or dries, and wherein, the moisture in the soybean requires greater than 10%-30%.
Microwave bulking technique: take the microwave equipment model of roc continent, Guangzhou microwave equipment Co., Ltd production: PZ-30MT as example, adopt the continuous swelling method.Microwave parameters is: microwave output power: 45KW (adjustable); Input apparent energy: 30KWA; Equipment operating voltage: three-phase 380V ± 10%; Microwave operational frequencies: 2450MHz ± 50Hz.Microwave treatment time is 90 seconds.
The computing formula of puffed degree is: expansion rate=(the expanded front volume of expanded rear volume ÷) * 100%.
After expanded, carry out the cold wind cooling.Expansion effect is seen Fig. 2.
The soybean puffing rate is up to 151%.
Embodiment 12
Take feedstuff soybean (commercially available) as example.
The water soaking soybean of the sucrose with 0.3% and 0.8% sodium bicarbonate 3 hours dries or dries, and wherein, the moisture in the soybean requires greater than 10%-30%.
The same example of microwave parameters, microwave treatment time are 90 seconds.After expanded, carry out the cold wind cooling.
The soybean puffing rate is up to 153%.
Embodiment 13
Take feedstuff soybean (commercially available) as example.
The water soaking soybean of the sucrose with 0.3% and 2% sodium bicarbonate 3 hours dries or dries, and wherein, the moisture in the soybean requires greater than 10%-30%.
The same example of microwave parameters, microwave treatment time are 90 seconds.After expanded, carry out the cold wind cooling.
The soybean puffing rate is up to 162%.
Embodiment 9 microwave bulkings and extrusion cost analysis
Take expanded soybean (soybean is as commercially available) as example:
The cost analysis of table 2 extrusion
| Title | Expense (yuan/ton) | Remarks |
| Soybean | 3780 yuan/tons of soybean | Take soybean as Basis, because of the different prices differences in region |
| The electricity charge | (360+7.5)=367.5*0.9 unit/degree=332 | Soybean puffing machine output is pressed 50kg/h, and per hour power consumption 18 degree calculate.Pulverize electricity consumption 7.5 degree/ton. |
| Labour cost | 360+10=370 | By three workmans of two equipment, per tour work 10 hours, 60 yuan of per capita salaries, the expense of every expanded 1 ton of feather meal is: 360 yuan.Pulverize, pack by 10 yuan/tons of calculating. |
| Equipment loss | 30 | 20 yuan/tons of consumable accessory expenses, 10 yuan/tons of other maintenance costs |
| Packing | 40 | |
| In advance charging | 18 | |
| Add up to | 4200 yuan/tons |
The cost analysis of table 3 microwave bulking
| Title | Expense (yuan/ton) | Remarks |
| Soybean | 3780 yuan/tons of soybean | Take soybean as Basis, because of the different prices differences in region |
| The electricity charge | (18+7.5)=25..5*0.9 unit/degree=22.95 | Soybean microwave bulking machine output is pressed 1000kg/h, and per hour power consumption 18 degree calculate.Pulverize electricity consumption 7.5 degree/ton. |
| Labour cost | 6+10=16 | By 2 workmans of 2 equipment, per tour work 10 hours, 60 yuan of per capita salaries, the expense of every expanded 1 ton of soybean is: 6 yuan.Pulverize, pack by 10 yuan/tons of calculating. |
| Equipment loss | 2 | 1 yuan/ton of consumable accessory expense, 1 yuan/ton of other maintenance cost |
| The additive cost | 5 yuan/tons of soybean | |
| Packing | 40 | |
| In advance charging | 18 | |
| Add up to | 3861 yuan/tons |
Analyzed as can be known by table 2 and table 3, the soybean cost behind the extrusion is 4200 yuan/tons, and the microwave bulking cost then is 3861 yuan/tons, and as seen, on economic benefit and cost, microwave bulking has very large advantage.
Claims (11)
1. the bulking process of a soybean is characterized in that comprising the following step:
(1) soybean is being comprised ammonia-alum or sodium bicarbonate, and soaking 2～24 hours in the aqueous solution of salt or sucrose, wherein, the mass percent of ammonia-alum or sodium bicarbonate is 0.2%～2%, and the mass percent of salt or sucrose is 0.2%～5%;
(2) product with step (1) gained carries out drying, and making the water content in the soybean is mass percent 10%～30%;
(3) product with step (2) gained carries out heating using microwave, gets final product to get expanded soybean; The time of described heating using microwave is 60-180 second; In described heating using microwave, microwave output power 12KW～400KW; Input apparent energy 15KWA-450KWA; The equipment operating voltage is three-phase 380V ± 10%; Microwave operational frequencies is 2450MHz ± 50Hz.
2. the bulking process of soybean as claimed in claim 1, it is characterized in that: in the step (1), the time of described immersion is 3～6 hours; The mass percent of ammonia-alum or sodium bicarbonate is 0.5%～1%; The mass percent of salt and/or sucrose is 0.5%～1%;
In the step (2), the method for described drying is that nature dries or dries up with air blast.
3. the bulking process of soybean as claimed in claim 1, it is characterized in that: in the step (3), the time of heating using microwave is 90-120 second.
4. the bulking process of soybean as claimed in claim 1, it is characterized in that: described heating using microwave comprises the following steps: the soybean that step (2) makes is inserted feeding warehouse, under the transmission device effect, soybean is transported to the heating using microwave district, heating using microwave 60-180 second, be transported to again discharging opening, blower cools.
5. the expanded soybean that makes such as each described bulking process of claim 1～4.
6. the preparation method of a mixed feed is characterized in that comprising the following step: in the expanded soybean adding mixed feed claimed in claim 5 after will pulverizing, then carry out routine and granulate, get final product.
7. the bulking process of a mixed feed, it is characterized in that comprising the following step: with soybean and water, and ammonia-alum or sodium bicarbonate, and raw material commonly used mixes in the mixed feed, the salt or the sucrose that also add mass percent 0.2%～1% in the mixed feed, then conventional the granulation or pulverizing carry out heating using microwave, gets final product; In mixed feed, the mass percent of soybean is 5%～30%, and the mass percent of water is 10%～30%, and the mass percent of ammonia-alum or sodium bicarbonate is 0.2%～5%; The time of described heating using microwave is 90-120 second.
8. the bulking process of a mixed feed, it is characterized in that comprising the following step: with soybean and water, and ammonia-alum or sodium bicarbonate, and raw material commonly used mixes in the mixed feed, the salt or the sucrose that also add mass percent 0.2%～1% in the mixed feed, then conventional the granulation or pulverizing carry out heating using microwave, gets final product; In mixed feed, the mass percent of soybean is 5%～30%, and the mass percent of water is 10%～30%, and the mass percent of ammonia-alum or sodium bicarbonate is 0.2%～5%; Described heating using microwave comprises the following steps: that the routine that will make is granulated or the material of pulverizing is inserted feeding warehouse; the routine that will make under the transmission device effect is granulated or the material of pulverizing is transported to the heating using microwave district; heating using microwave 60-180 second, be transported to again discharging opening, blower cools.
9. the bulking process of a mixed feed, it is characterized in that comprising the following step: with soybean and water, and ammonia-alum or sodium bicarbonate, and raw material commonly used mixes in the mixed feed, the salt or the sucrose that also add mass percent 0.2%～1% in the mixed feed, then conventional the granulation or pulverizing carry out heating using microwave, gets final product; In mixed feed, the mass percent of soybean is 5%～30%, and the mass percent of water is 10%～30%, and the mass percent of ammonia-alum or sodium bicarbonate is 0.2%～5%; In described heating using microwave, microwave output power 12KW～400KW; Input apparent energy 15KWA-450KWA; The equipment operating voltage is three-phase 380V ± 10%; Microwave operational frequencies is 2450MHz ± 50Hz.
10. such as the bulking process of each described mixed feed of claim 7～9, it is characterized in that: raw material commonly used is one or more in corn, wheat, dregs of beans, rapeseed dregs, the cotton dregs in the described mixed feed.
11. the feed that makes such as the bulking process of each described mixed feed of claim 7～10.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010102178068A CN102308908B (en) | 2010-07-02 | 2010-07-02 | Puffing techniques for soybean and feed and products produced by same |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010102178068A CN102308908B (en) | 2010-07-02 | 2010-07-02 | Puffing techniques for soybean and feed and products produced by same |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN102308908A CN102308908A (en) | 2012-01-11 |
| CN102308908B true CN102308908B (en) | 2013-04-10 |
Family
ID=45422775
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010102178068A Active CN102308908B (en) | 2010-07-02 | 2010-07-02 | Puffing techniques for soybean and feed and products produced by same |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN102308908B (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104543357B (en) * | 2014-12-09 | 2017-12-26 | 杭州青春元生物制品有限公司 | A kind of microwave-infrared preparation method for the flavored type feedstuff that is carbonized |
| CN104543339A (en) * | 2015-01-26 | 2015-04-29 | 中国农业大学 | Microwave conditioning production process of feeds |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1353948A (en) * | 2000-11-22 | 2002-06-19 | 石晓岭 | Soybean full-cream protein feed and its production process |
| CN1385092A (en) * | 2002-04-15 | 2002-12-18 | 山东农业大学 | Puffed granular fodder for silkworm |
| CN1618313A (en) * | 2004-11-19 | 2005-05-25 | 吉林省农业科学院 | Natural plant type forage additive, and prepn, method therefor |
| CN101669591A (en) * | 2009-08-01 | 2010-03-17 | 遵义市金鼎农业科技有限公司 | Early creep feed for porket |
-
2010
- 2010-07-02 CN CN2010102178068A patent/CN102308908B/en active Active
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1353948A (en) * | 2000-11-22 | 2002-06-19 | 石晓岭 | Soybean full-cream protein feed and its production process |
| CN1385092A (en) * | 2002-04-15 | 2002-12-18 | 山东农业大学 | Puffed granular fodder for silkworm |
| CN1618313A (en) * | 2004-11-19 | 2005-05-25 | 吉林省农业科学院 | Natural plant type forage additive, and prepn, method therefor |
| CN101669591A (en) * | 2009-08-01 | 2010-03-17 | 遵义市金鼎农业科技有限公司 | Early creep feed for porket |
Non-Patent Citations (6)
| Title |
|---|
| 大豆分离蛋白变性对物料微波膨化的影响及机理探讨;李作为等;《粮食与饲料工业》;20041231(第7期);22-23 * |
| 张立彦等.蛋白质对淀粉物料微波膨化的影响.《华南理工大学学报自然科学版》.2002,第30卷(第2期),56-59. |
| 微波加热对不同大豆品质的影响;杨慧萍等;《食品技术》;20031231(第3期);12-15 * |
| 李作为等.大豆分离蛋白变性对物料微波膨化的影响及机理探讨.《粮食与饲料工业》.2004,(第7期),22-23. |
| 杨慧萍等.微波加热对不同大豆品质的影响.《食品技术》.2003,(第3期),12-15. |
| 蛋白质对淀粉物料微波膨化的影响;张立彦等;《华南理工大学学报自然科学版》;20020228;第30卷(第2期);56-59 * |
Also Published As
| Publication number | Publication date |
|---|---|
| CN102308908A (en) | 2012-01-11 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103238727A (en) | Puffed wheat nursery pig feed and preparation method thereof | |
| CN103340318B (en) | Feed applicable to industrial aquaculture of tilapia, and preparation method and feeding method thereof | |
| CN103719549A (en) | Animal feed and preparation method thereof | |
| CN103766649A (en) | Fish and shrimp aquaculture feed and preparation method thereof | |
| CN102293350B (en) | Preparation method of shrimp and crab biological feed added with yellow rice wine lees | |
| CN103416594A (en) | High-protein multi-dimensional puffed saccharified compressed fodder capable of being stored for long time and processing method | |
| CN109043126A (en) | A kind of big dragon shrimp feed and preparation method thereof | |
| CN102308908B (en) | Puffing techniques for soybean and feed and products produced by same | |
| CN103931882B (en) | A kind of agent of feed for nursing using slaking cereal materials to improve child care pig production performance | |
| CN101756000A (en) | Biological high-energy feed and preparation method thereof | |
| CN103549196A (en) | Cattle and sheep pellet feed and preparation method thereof | |
| CN103519019A (en) | Production technology of suckling pig feed | |
| CN103918881B (en) | Utilize processing technology and the using method of slaking cereal materials on creep feed, child care material of infrared radiation energy slaking cereal materials | |
| CN106615686B (en) | A kind of feed addictive containing shrimp processing byproduct albumen powder and preparation method thereof, application | |
| CN112244171A (en) | Preparation method of low-carbon water baked cat food | |
| CN105639504B (en) | A kind of euphausia superba powder of lipid-rich and preparation method thereof | |
| CN101317626A (en) | Preparation for puffy full scream soybean meal for livestock and poultry feedstuff with wet-process | |
| CN103918880A (en) | Milk replacer using cured grain raw materials to improve production performance of piglets | |
| CN102178041B (en) | Sustained release non-protein nitrogen feed and preparation | |
| CN103156050A (en) | Feed microwave vacuum drying puffing machining process | |
| CN103875928A (en) | Piglet compound feed and preparation method thereof | |
| CN102165997A (en) | Amino acid coating method for aquatic feeds | |
| CN102550873A (en) | Microgranular concentrated feed for growing-finishing pigs and preparation method thereof | |
| CN105876206A (en) | Growth-promoting and disease-preventing piglet feed | |
| CN106360112A (en) | Feed for prawns |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20160617 Address after: 242000 Anhui Province Economic and Technological Development Zone Xuancheng Bai Jian Road No. 51 Patentee after: Xuancheng nine ducks Health Science and Technology Co., Ltd. Address before: 201516, Shanghai Jinshan District corridor town No. 6988 Gallery Road Patentee before: Shanghai Harmony Feed Co., Ltd. |