Background technology
Different spices can be according to its local flavor, color, and microorganism, the characteristics such as shape are selected different sterilization methods.At present adopt the radiation modes sterilization more, but on the spice color to keep impact larger, and can be restricted when outlet.China a lot of flavouring enterprise adopts irradiance method to carry out sterilization to spice, although with low cost, can cause the residual problem of irradiation product.Although the security of irradiated food there is no final conclusion, many consumers still hold the suspicious attitude to the security of this based food, feel misgivings when buying.And irradiation also can produce harmful effect to the flavor qualities such as color, smell and taste of numerous food product, as meeting make that the color and luster of processed food fades away, taste variation, smell become of inferior quality.China has the export-oriented enterprise of many rice convenient for production, quick-frozen food now, need to use a large amount of spices to make raw material, due to Japan, European Union forbids or strict limiting inlet irradiated food and contain the food of irradiation condiment, force these export-oriented enterprises from the non-irradiation spice of foreign procurement high price, consequence is to increase purchase cost and haulage time, the reduction competitiveness of product in market.
Summary of the invention
On the basis of realizing sterilization effect, keep simultaneously the flavor characteristics of spice, and without radiation treatment, the invention provides a kind of operation cycle short, efficient is high, the extruding sterilizing methods that cost is low.
The technical scheme that the present invention takes is:
A kind of extruding sterilizing methods of spice powder comprises the following steps:
(1) twin (double) screw extruder preheating: be preheating to assigned temperature, 50 ℃~130 ℃ of mixed zones, 80 ℃~160 ℃ of shear zones, 120 ℃~190 ℃ of melting zones after twin (double) screw extruder is started;
(2) spice powder and carrier, water are mixed rear stand-by with mixer, described carrier is one or more in flour, starch, ground rice, corn flour; The weight ratio of described spice, carrier, water is 70~100 parts of spices: 1~30 part, carrier: 1~10 part, water;
(3) compound in step 2 is joined in the loading hopper of extruder, start screw rod, adjusting screw speed is 50~200 rev/mins; At the uniform velocity reinforced, controlling charging rate is 20~100kg/ hour, and batch mixing through transmitting, pushing, is extruded by the mould mouth of extruder in extruder;
(4) the extruding reaction material that squeezes out is cooled to room temperature, obtains spice powder with the pulverizer grinding and sieving.
Further, the weight ratio of spice described in step 2, carrier, water is spice 100: carrier 15: water 7.
Further, the screw speed in step 3 is 100~120 rev/mins, and charging rate is 50~60kg/ hour.
Further, the assigned temperature described in step 1 is 88 ℃~92 ℃ of mixed zones, 100 ℃~110 ℃ of shear zones, 140 ℃~150 ℃ of melting zones.
Further, described spice powder is one or more in green onion, ginger, garlic, anise, fennel seeds, Chinese cassia tree, cloves, nutmeg, dried orange peel, Chinese prickly ash, capsicum, pepper, Radix Glycyrrhizae, basyleave, the root of Dahurain angelica, coriander, sweet basil, tsaoko, rosemary, Xue MingRosma rinus officinalis, Salvia japonica, thyme, wild marjoram, dill.
Further, described spice powder granularity is less than 40 orders.
The invention has the beneficial effects as follows: the one, do not have irradiation product residual, there is not the problem of security concerns, the food that adds this spice can more successfully enter western developed country and the areas such as Japan, European Union; The 2nd, bactericidal effect is desirable, can be with microorganism killing in rational hygienic requirements scope; The 3rd, can also promote the cooking feature of spice in sterilization, the loss of volatilization fragrance component is lacked a lot than traditional heat sterilization mode, can satisfy the needs that essence is produced.
The specific embodiment
Embodiment 1:
Using squeezing technique pushes sterilization to unpasteurized anise powder, gets 100 kilograms, anise powder, adds carrier by following weight ratio:
Raw material |
Weight ratio |
The anise powder |
16 |
Starch |
3 |
Water |
1 |
With above-mentioned powder mixer mixing, be 8.1% through surveying moisture content in proportion.Twin (double) screw extruder is preheating to assigned temperature, and default mixed zone temperature is 60 ℃, and the shear zone is 90 ℃, and melting zone is 120 ℃.Mixed anise powder is joined in the loading hopper of twin (double) screw extruder, start extruder, adjusting screw speed is 60 rev/mins.By the speed of 30Kg/ hour, the anise powder is transported to extruder from hopper and pushes, the extruding reaction material that squeezes out is cooled to room temperature, extruding reaction material diameter 3cm pulverizes this extruding reaction material with pulverizer, excessively obtain the anise powder of powdery after the screen cloth of 1mm.
Final gained anise powder observed watercut is 2.4%, is the brown powder shape, does not detect the pathogenic bacteria such as staphylococcus aureus, salmonella, mould in the anise powder, and total plate count and coliform group count meet national standard.The loss late of fennel essential oil is 5% left and right after measured, compares with former anise powder, and the anise powder fragrance after extruding is more harmonious, and cooking feature is obvious, can play the effect of sterilization.
Other embodiment: