CN102665432A - Method for producing nonaqueous paste-type fat-based food - Google Patents

Method for producing nonaqueous paste-type fat-based food Download PDF

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Publication number
CN102665432A
CN102665432A CN2010800534827A CN201080053482A CN102665432A CN 102665432 A CN102665432 A CN 102665432A CN 2010800534827 A CN2010800534827 A CN 2010800534827A CN 201080053482 A CN201080053482 A CN 201080053482A CN 102665432 A CN102665432 A CN 102665432A
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fatty foods
oil
water system
salt
pasty state
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CN102665432B (en
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野口爱
葛马千里
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Kewpie Corp
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QP Corp
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    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23DEDIBLE OILS OR FATS, e.g. MARGARINES, SHORTENINGS, COOKING OILS
    • A23D9/00Other edible oils or fats, e.g. shortenings, cooking oils
    • A23D9/007Other edible oils or fats, e.g. shortenings, cooking oils characterised by ingredients other than fatty acid triglycerides

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  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Food Science & Technology (AREA)
  • Polymers & Plastics (AREA)
  • Seasonings (AREA)

Abstract

Provided is a method for producing a nonaqueous paste-type fat-based food, whereby appropriate saltiness and sweetness can be obtained in a well-balanced manner and a high productivity can be achieved. The method for producing a nonaqueous paste-type fat-based food comprises mixing a fat base, which comprises 90% or more of a high-melting fat having an elevated melting point of 40-60 DEG C, at a material temperature of 0-35 DEG C with sodium chloride having an average particle diameter equal to or larger than 0.5 mm and sucrose having an average particle diameter equal to or smaller than 0.2 mm.

Description

The manufacturing approach of non-water system pasty state fatty foods
Technical field
But the present invention relates to saline taste and sweet taste and the manufacturing approach non-water system pasty state fatty foods that productivity ratio is excellent that balance demonstrates appropriateness well
Background technology
Known have through on heating and regulating food such as zwieback, pasta, smearing or mixing the non-water system pasty state fatty foods that carries out seasoning with it.For example; In TOHKEMY 2000-228948 communique (patent documentation 1), following record is arranged; Use the rising fusing point be 0~15 ℃ low melting point grease account for 65~99% with the rising fusing point be that high-melting-point grease more than 40 ℃ accounts for 1~35%, use salt powder and Icing Sugar respectively as saline taste of carrying out basic seasoning and sweet taste.And its manufacturing approach be with the cooperation raw material 70~100 ℃ down heating be cooled to room temperature after mixed, leave standstill a few days again and make.
Non-water system pasty state fatty foods not only is used for the seasoning of heating and regulating food such as above-mentioned zwieback, pasta, also hopes as the for example hamburger patty, the steak that use the poultry meat or the flesh of fish, fries in shallow oil meat, fried meat or use the meat heating and regulating food that uses meat in recent years of these hamburger etc. to use with baste.
But; Because of the saline taste and the sweet taste of non-water system pasty state fatty foods of record in the patent documentation 1 incorporates in the base oil, so, not only lack the sense of taste and impact and persistence; Also being difficult to feel sweet taste, is to demonstrate the saline taste of appropriateness and the non-water system pasty state fatty foods of sweet taste hardly.In addition, this manufacturing approach need leave standstill a few days so that base oil is stable, thereby is not suitable for the product of quick shipment.
The prior art document
Patent documentation
Patent documentation 1: TOHKEMY 2000-228948 communique
Summary of the invention
Therefore, but the object of the present invention is to provide balance to demonstrate the manufacturing approach of non-water system pasty state fatty foods saline taste and sweet taste, the productivity ratio excellence of appropriateness well.
The present inventor is for reaching above-mentioned purpose, and the raw material that in the saline taste of non-water system pasty state fatty foods and sweet taste, uses and grease and manufacturing process are furtherd investigate.Its result; Be surprised to find that when the salt of specific size and granulated sugar mixed under specified temp with the base oil of the grease that contains specific fusing point; But balance demonstrates the manufacturing approach of the excellent non-water system pasty state fatty foods of appropriate saline taste and sweet taste and productivity ratio well, thereby has accomplished the present invention.
Be that the present invention is following,
(1) a kind of manufacturing approach of non-water system pasty state fatty foods; It is characterized in that, be that 40~60 ℃ high-melting-point grease accounts for more than 90% and product temperature is 0~35 ℃ base oil, is that salt and average grain diameter more than the 0.5mm is that granulated sugar below the 0.2mm mixes with average grain diameter with the rising fusing point.
(2) manufacturing approach of the non-water system pasty state fatty foods described in the basis (1); It is characterized in that; Said average grain diameter be above salt of 0.5mm and said average grain diameter be the cooperation ratio of the granulated sugar below the 0.2mm for respect to 100 parts of salt, granulated sugar is less than 100 parts more than 10 parts.
Because of manufacturing approach according to non-water system pasty state fatty foods of the present invention; But can obtain balance and demonstrate the saline taste of appropriateness and the non-water system pasty state fatty foods of sweet taste well; So, can expect for example to be applied in the meat heating and regulating food that uses meats such as poultry meat, the flesh of fish with the expansion in the baste etc. to non-water system pasty state fatty foods demand.And manufacturing approach of the present invention need not make base oil stable, and productivity ratio is excellent, so, for example be fit to the food of quick shipment.
The specific embodiment
Below specify the present invention.And among the present invention, " % " refers to " quality % ", and " part " refers to " mass parts ".
Among the present invention, non-water system pasty state fatty foods is meant the moisture that in raw material, contains, with the non-paste food that adds the grease of clear water as the basis consciously.The non-water system pasty state of this kind fatty foods is a primary raw material with grease and powder material, and the present invention too.And non-water system pasty state fatty foods is from the purpose of local flavor etc., and polygamy closes fragrant vegetables such as garlic, caraway, sweet basil.As said fragrant vegetables, can the fragrant vegetables of dry thing, fried processing or fresh state be engaged in the non-water system pasty state fatty foods of the present invention.But, when cooperating the fragrant vegetables of fresh state, state the influence of powder flavorings such as the salt that disperses in the base oil, granulated sugar after receiving sometimes, can't keep the balance of himself osmotic pressure, and in the keeping process, produce dehydration.Because of this dehydration can not dissolved in the base oil, thus separated form water etc. produced sometimes, and diminish the outward appearance of food of the present invention.And also there is the problem that bacterium causes corruption that produces sometimes in dehydration.Therefore, when cooperating greengrocery such as fragrant vegetables, preferably use state after its dry thing, the fried processing etc. minimizing the fragrant vegetables of moisture.Specifically, preferably using moisture is the fragrant vegetables below 10%.
At first, specify the grease on the basis as non-water system pasty state fatty foods of the present invention.Base oil among the present invention is meant the grease part as the basis.Usually in these fatty foods, whole with respect to food, preferably contain more than 60%, more preferably contain the basic grease of conduct more than 70%, the present invention is too.Fatty foods of the present invention need use with respect to this base oil, and to contain more than 90%, preferably contain 95% above rising fusing point be 40~60 ℃, be preferably the fatty foods of 45~55 ℃ high-melting-point grease.
So long as the high-melting-point grease that uses in edible usually can use any high-melting-point grease.Edible oil and fat as the raw material of high-melting-point grease; For example can use soybean oil, rapeseed oil, safflower oil, sunflower oil, rice bran oil, corn oil, cottonseed oil, olive oil, palm oil, coconut oil or with these vegetable oil of the grease after refining etc., the animal wet goods of butter, lard, egg oil, fish oil etc.It particularly is the local flavor that the high-melting-point grease of raw material not only can not damage non-water system pasty state fatty foods of the present invention with the vegetable oil; After in the manufacturing approach of the present invention stated;, product temperature also forms base oil when being 0~30 ℃ easily with suitable viscosity, thus preferred.Usually the high-melting-point grease is to be raw material with the animals and plants wet goods, for making the rising fusing point in the scope of afore mentioned rules, through structural fatty acid being carried out ester exchange or being carried out hydrogenation treatment etc. and make.The present invention also can use this kind high-melting-point grease.
In the base oil of non-water system pasty state fatty foods of the present invention, same with non-water system pasty state fatty foods in the past, preferably contain and be useful on the fragrance grease of giving local flavor.As long as its content contains the degree with desirable local flavor, specifically, though different and different according to the flavor strength of fragrance grease, be preferably 0.1~8% with respect to base oil, more preferably 0.5~5%.The fragrance grease is from fragrant vegetables such as garlic, caraway, sweet basil, ginger, for example obtains through steam distillation, vegetable oil extraction, squeezing etc.
Mostly the fragrance grease is to be aqueous fluid oil down in room temperature (0~30 ℃).Therefore, the high-melting-point grease of the rising fusing point through having above-mentioned scope in the base oil that contains specified quantitative, the manufacturing approach of stating after the use of the present invention can obtain also in the keeping process, not producing that liquid oil separates, the preferred product of excellent storage stability.Even with the rising fusing point during than the high high-melting-point grease of above-mentioned scope or than the low grease of above-mentioned scope; Even use in addition the rising fusing point at the grease of above-mentioned scope but its content than above-mentioned specified quantitative after a little while; The manufacturing approach of stating after the use of the present invention; Also produce liquid oil in the keeping process sometimes and separate, thus not preferred.
And; When rising fusing point in the use than the high high-melting-point grease of above-mentioned scope; The base oil that the product temperature that the present invention uses during fabrication is 0~35 ℃, be preferably 10~30 ℃ is high viscosity; For the even powerful mixers of needs that disperse such as dry thing that make the salt, granulated sugar or the fragrant vegetables that disperse in this base oil, produce rate variance.And the viscosity whole because of resulting non-water system pasty state fatty foods increases, so, for example this food is packed into behind the container, be difficult to take out from container, thereby not preferred.On the other hand; When using the rising fusing point than the low grease of above-mentioned scope, high-melting-point content of oil and grease of the present invention after a little while; The whole viscosity of resulting non-water system pasty state fatty foods reduces; Be suitable viscosity hardly, so the material that in base oil, disperses sometimes can precipitate in the keeping process.In addition, when the non-water system pasty state fatty foods that this kind viscosity is low for example is used in the food such as hamburger, be difficult to be retained in the position of being placed, thus not preferred.
In the non-water system pasty state fatty foods that obtains in the present invention; As saline taste need use average grain diameter as more than the 0.5mm, be preferably the salt more than the 0.7mm; It is so-called crude salt; In addition as sweet taste, need use average grain diameter as below the 0.2mm, be preferably the granulated sugar below the 0.15mm, promptly so-called Icing Sugar.As the salt of afore mentioned rules size, for example can use the crude salt after the rock salt coarse crushing, the slow crude salt behind the crystallization etc.As the granulated sugar of afore mentioned rules size, for example can use the granulated sugar of berry sugar, sugar nibs etc. with the Icing Sugar after the pulverizer pulverizing etc.The crude salt of all size or Icing Sugar all have commercially available, and the salt of afore mentioned rules size and granulated sugar can be from wherein selecting use.
And the big or small not specially provided for of the size of the salt upper limit, granulated sugar lower limit, but consider flavour balance, the use level of the non-water system pasty state fatty foods that obtains among the present invention, the average grain diameter of salt is preferably below the 3mm, more preferably below the 2mm.In addition, the average grain diameter of granulated sugar is preferably more than the 0.01mm, more preferably more than the 0.05mm.
With the manufacturing approach in the past of mixing after the base oil heat is different; The non-water system pasty state fatty foods that obtains through the present invention can not lack the sense of taste and impacts because of saline taste and sweet taste incorporate in the base oil; Even use the Icing Sugar of above-mentioned size but when using than the little salt of above-mentioned crude salt; Can make saline taste outstanding and be difficult to feel sweet taste, thus not preferred.On the other hand, even use the crude salt of above-mentioned size but when using than the big granulated sugar of above-mentioned Icing Sugar, inlet taste shortcoming but the oil flavor is very outstanding, thereby not preferred.In addition, use than the little salt of above-mentioned crude salt and during than the big granulated sugar of above-mentioned Icing Sugar, have only saline taste quite outstanding, thus not preferred.In any case, be so-called crude salt and Icing Sugar if do not use the salt of above-mentioned size and granulated sugar, promptly can not get balance and demonstrate the saline taste of appropriateness and the non-water system pasty state fatty foods of sweet taste well, thereby not preferred.
The average grain diameter of using among the present invention is the salt more than the 0.5mm and the average grain diameter cooperation ratio as the granulated sugar below the 0.2mm; As long as demonstrate the ratio of the degree of saline taste and sweet taste well for fatty foods balance of the present invention; Specifically; With respect to 100 parts of said salt, said granulated sugar is preferably more than 10 parts less than 100 parts, more preferably more than 20 parts below 80 parts.With respect to the said scope of cooperation ratio of the granulated sugar of salt after a little while, has the weak slightly and outstanding trend of oil flavor of inlet taste.On the other hand, the said scope of cooperation ratio of granulated sugar for a long time, the inlet taste has the significant trend of sweet taste, is difficult to balance sometimes and demonstrates saline taste and sweet taste well, thereby not preferred.In addition, as concrete content, get final product so long as present the degree of saline taste and sweet taste, whole with respect to fatty foods, said salt is preferably 0.1~10%, and more preferably 0.5~8%, said granulated sugar is preferably 0.1~10%, and more preferably 0.5~6%.
The present invention is for being that to account for base oil and average grain diameter more than 90% be that salt and average grain diameter more than the 0.5mm is that granulated sugar below the 0.2mm mixes and makes for 40~60 ℃ high-melting-point grease with above-mentioned rising fusing point.
The present invention is different with in the past manufacturing approach, do not need said base oil heating and melting, need than the low-melting product temperature of the rising of high-melting-point grease, be specially 0~35 ℃, be preferably 10~30 ℃ and mix down.
At this, the base oil of said product temperature is mixed with the decentralized photo of salt and granulated sugar etc., be meant mixed processes through said decentralized photo, mix when will remain in the scope of said product temperature as the grease on the basis of decentralized medium.Therefore; Among the present invention; The method that mixed and dispersed phase behind the base oil for preparing said product temperature is in advance not only arranged; For example in the high-melting-point grease of said product temperature, add decentralized photo, add other liquid wet goods of fragrance wet goods for example in mixed process or after mixing, carry out method of mixing when base oil being remained in the scope of said product temperature and be also contained among the present invention.
The base oil that uses among the present invention of this kind product temperature has the viscosity of appropriateness.Base oil through the high-melting-point grease being accounted for the said goods temperature more than 90% mixes with salt of the present invention and granulated sugar; Can make saline taste and sweet taste in the resulting non-water system pasty state fatty foods not incorporate base oil; Thereby but balance demonstrates the saline taste and the sweet taste of appropriateness well; Even for example contain the fluid oil of fragrance wet goods, also be difficult for producing the oil separation of fluid oil.In addition, with the method in the past of mixing behind the base oil heating and melting is different, because of manufacturing approach of the present invention need not leave standstill a few days for base oil is stablized, so productivity ratio is excellent.
With respect to this, when using product temperature than the low base oil of said scope, this base oil is a high viscosity, is that the dry thing that makes the salt, granulated sugar or the fragrant vegetables that disperse in this base oil etc. evenly disperses, and needs powerful mixer, produces rate variance.In addition, when containing the fluid oil of fragrance wet goods, be prone to produce the oil separation of fluid oil, thus not preferred.On the other hand; When using product temperature than the high base oil of said scope, same with manufacturing approach in the past, resulting non-water system pasty state fatty foods incorporates base oil because of saline taste and sweet taste; So be to demonstrate the saline taste of appropriateness and the food of sweet taste hardly; Sometimes base oil is stable need to leave standstill in order to make, and produces rate variance, thereby not preferred.
Mixed base oil of the present invention and salt and granulated sugar; Also mix the dry thing of fragrant vegetables, the fluid oil of fragrance wet goods as required; The mixer that uses during this mixing can use any mixer so long as but mixed base oil is whole and can make salt and granulated sugar etc. be evenly dispersed in the device in the base oil basically.In addition, be to mix usually when mixing, but also mix in the present invention while outgasing like the non-water system pasty state fatty foods among the present invention while outgasing.
In the non-water system pasty state fatty foods that obtains in the present invention, except above-mentioned use raw material, in the scope of not damaging effect of the present invention, can cooperate various raw-food materials.For example, can give an example spice, dry flavoring, pulverous range protein, tackifier, anti-oxidant, mineral matter, emulsifying agent, spices etc.In addition, the non-water system pasty state fatty foods that obtains among the present invention is with same in the past, can be filled in the container of pipe, polybag etc. to seal, and considers keeping quality, can wait down certainly at low temperature (0~10 ℃).
Embodiment
Below, specify the present invention according to embodiment and Test Example.And the present invention is not limited to this.
[ embodiment 1 ]
The manufacturing approach of<non-water system pasty state fatty foods>
According to following cooperation ratio, high-melting-point vegetable fat and garlic oil (flavor oil) are moved into blending tank, under room temperature (20 ℃), mix with the preparation base oil with mixer.With product temperature is that about 20 ℃ base oil adds salt, granulated sugar and the dry sweet basil as remaining raw material when stirring, be mixed to mixer even basically, to make non-water system pasty state fatty foods.Resulting non-water system pasty state fatty foods is packed in the plastic containers of 1kg capacity and seals, low temperature (10 ℃) is keeping down.And base oil is the part that high-melting-point vegetable fat and garlic oil are merged, and is 95.5% with respect to the content of base oil high-melting-point vegetable fat.
The cooperation ratio of<non-water system pasty state fatty foods>
(base oil)
Figure BDA00001683607200071
During edible resulting non-water system pasty state fatty foods, balance demonstrates the saline taste and the sweet taste of appropriateness well.Even and resulting fatty foods takes care of 10 days at low temperatures then in room temperature (20 ℃) held after 1 hour, the oil of also not observing as the fluid oil of flavor oil separates, and is very stable.Thus, manufacturing approach of the present invention is not required to be and makes base oil stable and leave standstill a few days, so productivity ratio is excellent.
[ embodiment 2 ]
The manufacturing approach of<non-water system pasty state fatty foods>
According to the cooperation ratio of embodiment 1, the high-melting-point vegetable fat is moved into blending tank, the use mixer slowly stirs and makes product temperature be about 20 ℃ under room temperature (20 ℃).Begin to mix after adding salt, granulated sugar and dry sweet basil when product temperature is about 20 ℃ high-melting-point grease stirring; Add garlic oil (flavor oil) in the mixed process; It is whole even for basically to use mixer to be mixed to, to make non-water system pasty state fatty foods.Resulting non-water system pasty state fatty foods is packed in the plastic containers of 1kg capacity and seals keeping in refrigerator (4 ℃).And when after adding garlic oil, measuring the product temperature of base oil soon is about 20 ℃.In addition, resulting non-water system pasty state fatty foods to be the fatty foods that obtains among stability and the embodiment 1 after flavor and the low temperature keeping be equal extent.
[ Test Example 1 ]
The influence of the high-melting-point fat content in the analysis foundation oil.The grease that is about to base oil is formed as the ratio shown in the table 1, and other make non-water system pasty state fatty foods according to embodiment 1.To resulting fatty foods, use the state after method low temperature as follows is taken care of to reach the evaluation when in hamburger, using.And high-melting-point grease and flavor oil (fluid oil) are identical with embodiment 1, and it is 5 ℃ grease as the rising fusing point of raw material that the low melting point grease uses with vegetable oil.In addition, resulting each fatty foods balance demonstrates the saline taste and the sweet taste of appropriateness well.
The evaluation of the state after the keeping of<low temperature>
Same with embodiment 1, estimate at low temperature (10 ℃) and take care of 10 days down then at the state (oil separates and viscosity) of room temperature (20 ℃) held after 1 hour.
<when in hamburger, using evaluation>
At the hamburger patty (the about 1cm of the about 10cm * thickness of diameter) that the hamburger after the heating is placed resulting each fatty foods 10g, romaine lettuce, cheese in order and baked on bread (lower floor with), place hamburger after heating at last with bread (upper strata usefulness).Afterwards resulting hamburger is used wrapper.Estimate its state after 5 minutes then.And each fatty foods use the evaluation carried out after above-mentioned<low temperature keeping>after fatty foods.
Table 1
Figure BDA00001683607200091
Table 1 can be regarded as, and as not containing more than 90% the high-melting-point grease that uses in this in the base oil, then is difficult to obtain to be difficult for to produce the non-water system pasty state fatty foods that oil separates, has the viscosity of appropriateness and is applicable to food such as hamburger.Especially preferably containing the high-melting-point grease is more than 95%.
[ Test Example 2 ]
Analyze the different influences that caused of rising fusing point of high-melting-point grease.Promptly replace the high-melting-point grease (the rising fusing point is 50 ℃) among the embodiment 1, use to have the high-melting-point grease of the rising fusing point shown in the table 2 or the low-melting grease that rises, other make non-water system pasty state fatty foods according to embodiment 1.For resulting fatty foods, according to Test Example 1<evaluation of state after the low temperature keeping>estimate.And resulting each fatty foods balance demonstrates the saline taste and the sweet taste of appropriateness well.
Table 2
Figure BDA00001683607200101
Table 2 be appreciated that into, be the high-melting-point grease of 40~60 ℃ scope as not using the rising fusing point, then be difficult to obtain be difficult for producing the non-water system pasty state fatty foods that oil separates, has the viscosity of appropriateness.Especially preferably using the rising fusing point is 45~55 ℃ high-melting-point grease.
[ Test Example 3 ]
Analyze varying in size of salt and granulated sugar to being the influence of flavor property.Promptly replace the salt (average grain diameter is 0.7mm) of embodiment 1 and salt and the granulated sugar that granulated sugar (average grain diameter is 0.1mm) uses the size shown in the table 3, other make non-water system pasty state fatty foods according to embodiment 1.Edible resulting fatty foods is taken care of down at low temperature (10 ℃) then was flavor property at room temperature (20 ℃) held this fatty foods after 1 hour and evaluation in 10 days.Resulting each fatty foods has the viscosity of appropriateness, and the oil of not observing fluid oil separates, and is very stable.In addition, the size in the table is the size of average grain diameter.
Table 3
Table 3 can be regarded as, and is the granulated sugar below the 0.2mm as not using average grain diameter as salt more than the 0.5mm and average grain diameter, then is difficult to obtain balance and demonstrates the saline taste of appropriateness and the non-water system pasty state fatty foods of sweet taste well.Especially preferably use average grain diameter to be the granulated sugar below the 0.15mm as salt more than the 0.7mm and average grain diameter.
[ Test Example 4 ]
The difference of the cooperation ratio of analysis salt and granulated sugar is to being the influence of flavor property.Soon the use level of the salt (average grain diameter is 0.7mm) of embodiment 1 and granulated sugar (average grain diameter is 0.1mm) and cooperation ratio are as the amount shown in the table 4; Whole amount is regulated with the high-melting-point vegetable fat, and other make non-water system pasty state fatty foods according to embodiment 1.Edible resulting fatty foods is taken care of down at low temperature (10 ℃) then was flavor property at room temperature (20 ℃) held this fatty foods after 1 hour and evaluation in 10 days.Resulting each fatty foods has the viscosity of appropriateness, and the oil of not observing fluid oil separates, and is very stable.
Table 4
Figure BDA00001683607200121
Table 4 be appreciated that into, if the cooperation ratio of salt and granulated sugar not with respect to 100 parts of salt, granulated sugar be more than 10 parts less than in 100 parts the scope, then be difficult to obtain balance and demonstrate the saline taste of appropriateness and the non-water system pasty state fatty foods of sweet taste well.Preferred especially is the scope below 80 parts more than 20 parts with respect to 100 portions of granulated sugar of salt.
[ Test Example 4 ]
Analysis is when mixed base oil and salt and granulated sugar, and the product temperature of gene basis oil is different and to the state after the keeping and be the influence of flavor property.Be about to the base oil heating of embodiment 1 or be cooled to the product temperature shown in the table 5, other make non-water system pasty state fatty foods according to embodiment 1.Keeping 10 days is then in the state of room temperature (20 ℃) held after 1 hour down at low temperature (10 ℃) with resulting fatty foods observing, and edible this fatty foods is also estimated and is flavor property.When base oil is lower than 0 ℃, used powerful mixer separately.
Table 5
Table 5 be appreciated that into; If the product temperature base oil in 0~35 ℃ of scope and make non-water system pasty state fatty foods not when use mixing salt and granulated sugar is difficult to then to obtain not observing that oil separates and balance demonstrates the saline taste of appropriateness and the non-water system pasty state fatty foods of sweet taste well.The product temperature of preferred especially base oil is 10~30 ℃ a scope.

Claims (2)

1. the manufacturing approach of a non-water system pasty state fatty foods; It is characterized in that, be that 40~60 ℃ high-melting-point grease accounts for more than 90% and product temperature is 0~35 ℃ base oil, is that salt and average grain diameter more than the 0.5mm is that granulated sugar below the 0.2mm mixes with average grain diameter with the rising fusing point.
2. according to the manufacturing approach of the non-water system pasty state fatty foods described in the claim 1; It is characterized in that; Said average grain diameter be above salt of 0.5mm and said average grain diameter be the cooperation ratio of the granulated sugar below the 0.2mm for respect to 100 parts of salt, granulated sugar is less than 100 parts more than 10 parts.
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