CN109123606A - A kind of selected rice is manufactured to mix reconciliation syrup and its manufacturing process - Google Patents
A kind of selected rice is manufactured to mix reconciliation syrup and its manufacturing process Download PDFInfo
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- CN109123606A CN109123606A CN201810871023.8A CN201810871023A CN109123606A CN 109123606 A CN109123606 A CN 109123606A CN 201810871023 A CN201810871023 A CN 201810871023A CN 109123606 A CN109123606 A CN 109123606A
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- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
- A23L29/00—Foods or foodstuffs containing additives; Preparation or treatment thereof
- A23L29/30—Foods or foodstuffs containing additives; Preparation or treatment thereof containing carbohydrate syrups; containing sugars; containing sugar alcohols, e.g. xylitol; containing starch hydrolysates, e.g. dextrin
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Abstract
The formula of mixing reconciliation syrup made of a kind of selected rice of the present invention, including maltose, fructose, rock sugar and food additives, the main source of the maltose is selected rice or selected one of cracks rice or composition, and preparation mixing reconciliation syrup is carried out by 8 steps, mixing molasses made of the technique provided according to the present invention have more preferably palatability, can in human body better Absorption And Metabolism, blood-sugar content can quickly be supplemented, preparation method control provided by the present invention is stringent, production process is rigorous, it is accurate for the control of reaction, progress and the moving direction of reaction can preferably be controlled, production technology of the present invention is stringent and can accurately control the processing stage of selected rice, guarantee that the activity of selected rice is maintained in the state of highest and keeps active degree at most, break through traditional destructive production method , the nutritional ingredient in selected rice can be effectively saved, is suitble to be promoted and applied in food production processing industry.
Description
Technical field
The present invention relates to food-making technology fields, are to be related to a kind of manufactured mixing of selected rice more particularly
Reconciliation syrup and its manufacturing process.
Background technique
With being gradually increased for Modern Live quality so that people for every aspect involved in daily life all
Progress requires humanizedly, based on people's lives requirement, is all being researched and developed and is being reformed to all trades and professions in society.
As for a various daily neces saries compared with based on, its use scope gradually becomes from flavouring syrup
The more concept of diversification, traditional syrup is merely possible to a kind of sweetener presence, and assigns under present band social development
The new concept of syrup, such as toner etc..
As the use scope of syrup is more and more wider, people carry out more and more careful draw for the Property requirements of syrup
Point, there are heavy syrup, seasoning syrup, medicinal syrup, cocktail reconciliation syrup etc. for functional perspective, it will thus be seen that sugared
Slurry has different functions in different industries.
The people of requirement with to(for) health is higher and higher, and traditional reconciliation syrup is due to public with more base-material
Repelled, especially on the safe diet for being related to children, traditional reconciliation syrup has poor safety.
Based on the scientific achievement of Yuan Longping professor, guarantee that the whole nation there are more rice to be processed on the basis of having enough
Prerequisite, and more come into the market using rice as the product of raw material, it is a kind of solution food safety from source in itself
A kind of behave, and rice is added in the production process of syrup as raw material, more safeties can not only be increased for syrup
Matter, additionally it is possible to which the applicable human rights for expanding syrup more protect human-body safety, add a power for food safety.
Summary of the invention
It is agreeable to the taste to solve mixing molasses in the prior art that the present invention provides a kind of mixing molasses with broad applicability
The bad and bad assimilation effect problem of property.
In order to solve the above-mentioned technical problem, the embodiment of the invention discloses following technical solutions:
A kind of formula of the manufactured mixing reconciliation syrup of selected rice, including maltose, fructose, rock sugar and food additives, institute
The main source for stating maltose is selected rice or selected one of cracks rice or composition, the food additives include saccharification
Enzyme, high temperature enzyme and food acids alkaline agent.
A kind of formula of the manufactured mixing reconciliation syrup of selected rice, is 100g meter according to gross mass, following ingredients
Quality is as follows:
Maltose: 20-40g；
Fructose: 50-70g；
Rock sugar: 10-20g；
Food additives: 0.1-0.3g.
A kind of manufacturing process of the manufactured mixing reconciliation syrup of selected rice:
Step 1- prepares Rice & peanut milk: selected rice or selected crack rice are crushed and are made Rice & peanut milk, add deionization in crushing process
Water is simultaneously stirred until homogeneous suspended liquid status, after standing 2h, obtains Rice & peanut milk semi-finished product after being stirred for 0.5h, for use；
Mixing speed in step 1 is speed change stirring, Rice & peanut milk of the mixing speed in 90rd/s-150rad/s, step 1
Concentration carries out selecting to determine concentration in 16-18Be/ and according to the syrup purposes of configuration.
The liquefaction of step 2- Rice & peanut milk: Rice & peanut milk semi-finished product in step 1 are put into reaction kettle and are added high temperature enzyme, and stirring is extremely
Uniformly, and the pressure in reaction kettle and temperature are adjusted, Rice & peanut milk first product is made in Rice & peanut milk semi-finished product；
Reaction pressure in step 2 is 0.5-0.6MPa, reaction temperature within the scope of 103-110 DEG C, the Rice & peanut milk first product
Saccharification value is within the scope of 14-18.
Step 3- saccharification:
Carry out the saccharification of fructose and rock sugar respectively: fructose and rock sugar are referred to as base sugar, add carbohydrase in base sugar after the purification
It is saccharified, the base sugar obtains the primary sugars within the scope of suitable saccharification value by certain saccharificatinn period at a constant temperature:
Fructose saccharification: being classified as two classes sugar of one kind sugar and saccharification value of the saccharification value within the scope of 45-55 greater than 95 for fructose,
One type sugar is filtered by Buchner funnel, is decolourized to obtain a kind of base sugar secondly by active carbon, by a kind of base sugar
Sugar at the beginning of ion exchange obtains one kind is carried out by semi-permeable membrane；Wherein two class sugar are filtered by Buchner funnel, secondly by work
Property charcoal decolourized to obtain two class bases sugar, the two class base sugar obtained after decoloration carry out isomerization after ion exchange, by isomery
The two class base sugar changed are concentrated, and the two class base sugar that saccharification value is 42 in two class base sugar after concentration are separated, and will remain
Two remaining class base sugar are added in knockout tower and are refined, and two class base sugar after purification carry out secondary concentration, and obtaining saccharification value is 90
Two class bases sugar, the two class base sugar that saccharification value is 42 and the two class base sugar that saccharification value is 90 are carried out being mixed to get saccharification value being 55
Two class bases sugar；
Rock sugar saccharification: the rock sugar of monolith being ground, and smashed rock sugar is dissolved to obtain rock sugar turbid, will
Rock sugar turbid is filtered by Buchner funnel, obtains rock sugar solution, and rock sugar solution is concentrated to give saccharification value and is not less than
98 rock sugar centrotheca；
The range of rock sugar solution temperature described in step 3 is within the scope of 80 DEG C -90 DEG C.
In step 3 in decolorization the flow of active carbon in 2kg/m3- 3kg/m3In range.
Saccharificatinn period in step 3 is within the scope of 40h-80h.
Environment acid of the ion-flow rate of step 3 intermediate ion exchange within the scope of 8m3/n-10m3/n, under ion exchange conditions
Basicity is not less than 4, and the conductivity under switched environment is not more than 50us.
Isomerization operations are further limited in step 3: two class base sugar are passing through addition after ion exchange
PH value is adjusted in food acids alkaline agent, and the pH value of the two classes base sugar is not less than 7.0 or is not less than in 7.5 ranges, i.e., two
Class base sugar it is weakly acidic, the saccharification value in isomerization exit is not less than 43.
In step 3 under atmospheric pressure of the concentration reaction under the vacuum degree not less than 650/mmHg within the scope of 0.5-0.6MPa
It is reacted, concentration reaction kettle middle outlet temperature is not more than 65 DEG C, and concentration reaction kettle middle outlet concentration is not less than 71 DEG C.
It carries out separating a kind of sugar and two classes sugar by separator in step 3.
Step 4- mixing: three kinds of primary sugars obtained in step 3 are carried out according to the proportion to be mixed to get second level sugar；
Step 5- material: the second level sugar in step 4 is dissolved at 80 DEG C -90 DEG C, is adjusted according to F42+F90 → F55
The whole ratio being suitble to that matches out obtains three-level sugar；
Step 6- detection adjustment: three-level sugar obtained in step 5 is detected, and the detection element is followed successively by three-level sugar
Saccharification value, pH value, viscosity, activation number and concentration value, examining qualification is primary syrup；
Step 7- is qualitative: primary syrup obtained in step 6 being sieved, obtains fineness in the slurries of 80 mesh and at 105 DEG C
The lower high-temperature sterilization carried out in the 3min-5min time, and the alternating temperature sterilization process in 80 DEG C -90 DEG C is carried out in 30min again,
It is finally cooled to 60 DEG C and obtains finished product syrup；
Step 8- is canned: the progress canning sealing of finished product syrup obtained in step 7 is obtained mixing reconciliation syrup.
Above technical scheme as it can be seen that the present invention is using rice has the nature of rice as reconciliation syrup made of raw material
Faint scent, the syrup that reconciles is finer and smoother, has preferable extension cup effect, and mixing molasses manufactured according to the present invention have more preferably
Palatability, can in human body better Absorption And Metabolism, can quickly supplement blood-sugar content, people is helped quickly to carry out energy
Supplement, preparation method control provided by the present invention is stringent, and production process is rigorous, accurate for the control of reaction, can be preferable
Control reaction progress and moving direction, production technology of the present invention is stringent and can accurately control the processing journey of selected rice
Degree guarantees that the activity of selected rice is maintained in the state of highest and keeps active degree at most, breaks through traditional destructiveness
Production method can effectively save the nutritional ingredient in selected rice, be suitble to carry out promoting in food production processing industry to answer
With.
Specific embodiment
Embodiment 1
A kind of formula of the manufactured mixing reconciliation syrup of selected rice, is 100g meter, the quality of following ingredients according to gross mass
It is as follows:
Maltose: 24g；
Fructose: 65.85g；
Rock sugar: 10g；
Food additives: 0.15g.
A kind of manufacturing process of the manufactured mixing reconciliation syrup of selected rice:
Step 1- prepares Rice & peanut milk: selected rice or selected crack rice are crushed and are made Rice & peanut milk, add deionization in crushing process
Water is simultaneously stirred until homogeneous suspended liquid status, after standing 2h, obtains Rice & peanut milk semi-finished product after being stirred for 0.5h, for use；
The liquefaction of step 2- Rice & peanut milk: Rice & peanut milk semi-finished product in step 1 are put into reaction kettle and are added high temperature enzyme, are stirred until homogeneous,
And the pressure in reaction kettle and temperature are adjusted, Rice & peanut milk first product is made in Rice & peanut milk semi-finished product；
Step 3- saccharification:
Carry out the saccharification of fructose and rock sugar respectively: fructose and rock sugar are referred to as base sugar, add carbohydrase in base sugar after the purification
It is saccharified, the base sugar obtains the primary sugars within the scope of suitable saccharification value by certain saccharificatinn period at a constant temperature:
Fructose saccharification: being classified as two classes sugar of one kind sugar and saccharification value of the saccharification value within the scope of 45-55 greater than 95 for fructose,
One type sugar is filtered by Buchner funnel, is decolourized to obtain a kind of base sugar secondly by active carbon, by a kind of base sugar
Sugar at the beginning of ion exchange obtains one kind is carried out by semi-permeable membrane；Wherein two class sugar are filtered by Buchner funnel, secondly by work
Property charcoal decolourized to obtain two class bases sugar, the two class base sugar obtained after decoloration carry out isomerization after ion exchange, by isomery
The two class base sugar changed are concentrated, and the two class base sugar that saccharification value is 42 in two class base sugar after concentration are separated, and will remain
Two remaining class base sugar are added in knockout tower and are refined, and two class base sugar after purification carry out secondary concentration, and obtaining saccharification value is 90
Two class bases sugar, the two class base sugar that saccharification value is 42 and the two class base sugar that saccharification value is 90 are carried out being mixed to get saccharification value being 55
Two class bases sugar；
Rock sugar saccharification: the rock sugar of monolith being ground, and smashed rock sugar is dissolved to obtain rock sugar turbid, will
Rock sugar turbid is filtered by Buchner funnel, obtains rock sugar solution, and rock sugar solution is concentrated to give saccharification value and is not less than
98 rock sugar centrotheca；
Step 4- mixing: three kinds of primary sugars obtained in step 3 are carried out according to the proportion to be mixed to get second level sugar；
Step 5- material: the second level sugar in step 4 is dissolved at 80 DEG C -90 DEG C, is adjusted according to F42+F90 → F55
The whole ratio being suitble to that matches out obtains three-level sugar；
Step 6- detection adjustment: three-level sugar obtained in step 5 is detected, and the detection element is followed successively by three-level sugar
Saccharification value, pH value, viscosity, activation number and concentration value, examining qualification is primary syrup；
Step 7- is qualitative: primary syrup obtained in step 6 being sieved, obtains fineness in the slurries of 80 mesh and at 105 DEG C
The lower high-temperature sterilization carried out in the 3min-5min time, and the alternating temperature sterilization process in 80 DEG C -90 DEG C is carried out in 30min again,
It is finally cooled to 60 DEG C and obtains finished product syrup；
Step 8- is canned: the progress canning sealing of finished product syrup obtained in step 7 is obtained mixing reconciliation syrup.
Mixing speed in step 1 is speed change stirring, and the mixing speed is in 90rd/s-150rad/s, step 1
Rice & peanut milk concentration carries out selecting to determine concentration in 16-18Be/ and according to the syrup purposes of configuration.
Reaction pressure in step 2 is 0.5-0.6MPa, reaction temperature within the scope of 103-110 DEG C, the Rice & peanut milk just at
The saccharification value of product is within the scope of 14-18.
The range of rock sugar solution temperature described in step 3 is within the scope of 80 DEG C -90 DEG C.
In step 3 in decolorization the flow of active carbon in 2kg/m3- 3kg/m3In range.
Saccharificatinn period in step 3 is within the scope of 40h-80h.
The ion-flow rate of step 3 intermediate ion exchange is in 8m3/n-10m3Environment soda acid within the scope of/n, under ion exchange conditions
Degree is not less than 4, and the conductivity under switched environment is not more than 50us.
Isomerization operations are further limited in step 3: two class base sugar are passing through addition after ion exchange
PH value is adjusted in food acids alkaline agent, and the pH value of the two classes base sugar is not less than 7.0 or is not less than in 7.5 ranges, i.e., two
Class base sugar it is weakly acidic, the saccharification value in isomerization exit is not less than 43.
In step 3 under atmospheric pressure of the concentration reaction under the vacuum degree not less than 650/mmHg within the scope of 0.5-0.6MPa
It is reacted, concentration reaction kettle middle outlet temperature is not more than 65 DEG C, and concentration reaction kettle middle outlet concentration is not less than 71 DEG C.
It carries out separating a kind of sugar and two classes sugar by separator in step 3.
The higher reconciliation syrup of selected rice concentration is obtained in embodiment 1, it is suitable as a kind of reconciliation syrup compared with Gao meter Xiang
Cooperate the base-material for the base-material of child's medicament and the health beverages of the elderly, for during cocktail rectification can based on
It is fragrant and carry out using preferable palatability and more beautiful salubrious color can be obtained.
Embodiment 2
A kind of formula of the manufactured mixing reconciliation syrup of selected rice, is 100g meter, the quality of following ingredients according to gross mass
It is as follows:
Maltose: 36g；
Fructose: 53.7g；
Rock sugar: 10g；
Food additives: 0.3g.
A kind of manufacturing process of the manufactured mixing reconciliation syrup of selected rice:
Step 1- prepares Rice & peanut milk: selected rice or selected crack rice are crushed and are made Rice & peanut milk, add deionization in crushing process
Water is simultaneously stirred until homogeneous suspended liquid status, after standing 2h, obtains Rice & peanut milk semi-finished product after being stirred for 0.5h, for use；
The liquefaction of step 2- Rice & peanut milk: Rice & peanut milk semi-finished product in step 1 are put into reaction kettle and are added high temperature enzyme, are stirred until homogeneous,
And the pressure in reaction kettle and temperature are adjusted, Rice & peanut milk first product is made in Rice & peanut milk semi-finished product；
Step 3- saccharification:
Carry out the saccharification of fructose and rock sugar respectively: fructose and rock sugar are referred to as base sugar, add carbohydrase in base sugar after the purification
It is saccharified, the base sugar obtains the primary sugars within the scope of suitable saccharification value by certain saccharificatinn period at a constant temperature:
Fructose saccharification: being classified as two classes sugar of one kind sugar and saccharification value of the saccharification value within the scope of 45-55 greater than 95 for fructose,
One type sugar is filtered by Buchner funnel, is decolourized to obtain a kind of base sugar secondly by active carbon, by a kind of base sugar
Sugar at the beginning of ion exchange obtains one kind is carried out by semi-permeable membrane；Wherein two class sugar are filtered by Buchner funnel, secondly by work
Property charcoal decolourized to obtain two class bases sugar, the two class base sugar obtained after decoloration carry out isomerization after ion exchange, by isomery
The two class base sugar changed are concentrated, and the two class base sugar that saccharification value is 42 in two class base sugar after concentration are separated, and will remain
Two remaining class base sugar are added in knockout tower and are refined, and two class base sugar after purification carry out secondary concentration, and obtaining saccharification value is 90
Two class bases sugar, the two class base sugar that saccharification value is 42 and the two class base sugar that saccharification value is 90 are carried out being mixed to get saccharification value being 55
Two class bases sugar；
Rock sugar saccharification: the rock sugar of monolith being ground, and smashed rock sugar is dissolved to obtain rock sugar turbid, will
Rock sugar turbid is filtered by Buchner funnel, obtains rock sugar solution, and rock sugar solution is concentrated to give saccharification value and is not less than
98 rock sugar centrotheca；
Step 4- mixing: three kinds of primary sugars obtained in step 3 are carried out according to the proportion to be mixed to get second level sugar；
Step 5- material: the second level sugar in step 4 is dissolved at 80 DEG C -90 DEG C, is adjusted according to F42+F90 → F55
The whole ratio being suitble to that matches out obtains three-level sugar；
Step 6- detection adjustment: three-level sugar obtained in step 5 is detected, and the detection element is followed successively by three-level sugar
Saccharification value, pH value, viscosity, activation number and concentration value, examining qualification is primary syrup；
Step 7- is qualitative: primary syrup obtained in step 6 being sieved, obtains fineness in the slurries of 80 mesh and at 105 DEG C
The lower high-temperature sterilization carried out in the 3min-5min time, and the alternating temperature sterilization process in 80 DEG C -90 DEG C is carried out in 30min again,
It is finally cooled to 60 DEG C and obtains finished product syrup；
Step 8- is canned: the progress canning sealing of finished product syrup obtained in step 7 is obtained mixing reconciliation syrup.
Mixing speed in step 1 is speed change stirring, and the mixing speed is 90rd/s, and the Rice & peanut milk concentration in step 1 is
18Be/ simultaneously carries out selecting to determine concentration according to the syrup purposes of configuration.
Reaction pressure in step 2 is 0.6MPa, and reaction temperature is the saccharification of the Rice & peanut milk first product within the scope of 110 DEG C
Value is in 14 ranges.
The range of rock sugar solution temperature described in step 3 is within the scope of 90 DEG C.
In step 3 in decolorization the flow of active carbon in 3kg/m3In range.
Saccharificatinn period in step 3 is within the scope of 40h-80h.
The ion-flow rate of step 3 intermediate ion exchange is in 8m3/n-10m3Environment soda acid within the scope of/n, under ion exchange conditions
Degree is not less than 4, and the conductivity under switched environment is not more than 50us.
Isomerization operations are further limited in step 3: two class base sugar are passing through addition after ion exchange
PH value is adjusted in food acids alkaline agent, and the pH value of the two classes base sugar is not less than 7.0 or is not less than in 7.5 ranges, i.e., two
Class base sugar it is weakly acidic, the saccharification value in isomerization exit is not less than 43.
In step 3 under atmospheric pressure of the concentration reaction under the vacuum degree not less than 650/mmHg within the scope of 0.5-0.6MPa
It is reacted, concentration reaction kettle middle outlet temperature is not more than 65 DEG C, and concentration reaction kettle middle outlet concentration is not less than 71 DEG C.
It carries out separating a kind of sugar and two classes sugar by separator in step 3.
This example demonstrates that syrup made by the present invention can carry out in the case where low sugar as critical power replenishers
It uses, can promptly supplement blood glucose, provide energy in time to generate the crowd of adverse reaction after women and strenuous exercise.
Embodiment 3
On the basis of the above embodiments to auxiliary enzymes are increased in video additive, the auxiliary enzymes are in digestive ferment or probiotics
One kind or composition, by the using effect of the addition optimization syrup of auxiliary enzymes and profitable strain, enhancing blood glucose is in vivo
Accretion rate.
In conclusion the embodiment of the present invention is compared with prior art, there is more extensive use scope, on the market can
Stronger competitiveness is enough generated, for production, the mechanization that is more suitable large-scale production can significantly promote production effect
Rate generates preferable economic benefit, while can optimize purification food production processing industry.
Claims (10)
1. mixing made of a kind of selected rice reconciles the formula of syrup, it is characterised in that: including maltose, fructose, rock sugar and
Food additives, the main source of the maltose be selected rice or it is selected one of crack rice or composition, the food
Additive includes carbohydrase, high temperature enzyme and food acids alkaline agent.
2. the formula of mixing reconciliation syrup made of a kind of selected rice according to claim 1, it is characterised in that: according to
Gross mass is 100g meter, and the quality of following ingredients is as follows:
Maltose: 20-40g；
Fructose: 50-70g；
Rock sugar: 10-20g；
Food additives: 0.1-0.3g.
3. the manufacturing process of mixing reconciliation syrup made of a kind of selected rice, it is characterised in that:
Step 1- prepares Rice & peanut milk: selected rice or the selected mixing speed cracked rice in 90rd/s-150rad/s are crushed simultaneously
Rice & peanut milk is made, Rice & peanut milk concentration adds deionized water within the scope of 16-18Be/, in crushing process and is stirred until homogeneous suspended liquid
State after standing 2h, obtains Rice & peanut milk semi-finished product after being stirred for 0.5h, for use；
The liquefaction of step 2- Rice & peanut milk: Rice & peanut milk semi-finished product in step 1 are put into reaction kettle and are added under the pressure of 0.5-0.6MPa
Enter high temperature enzyme, be stirred until homogeneous under the reaction temperature within the scope of 103-110 DEG C, and adjusts the pressure in reaction kettle and temperature,
Rice & peanut milk first product is made in Rice & peanut milk semi-finished product, the saccharification value of the Rice & peanut milk first product is within the scope of 14-18；
Step 3- saccharification:
Carry out the saccharification of fructose and rock sugar respectively: fructose and rock sugar are referred to as base sugar, add carbohydrase in base sugar after the purification
It is saccharified, the base sugar obtains the primary sugars within the scope of suitable saccharification value by certain saccharificatinn period at a constant temperature:
Fructose saccharification: being classified as two classes sugar of one kind sugar and saccharification value of the saccharification value within the scope of 45-55 greater than 95 for fructose,
One type sugar is filtered by Buchner funnel, is decolourized to obtain a kind of base sugar secondly by active carbon, by a kind of base sugar
Sugar at the beginning of ion exchange obtains one kind is carried out by semi-permeable membrane；Wherein two class sugar are filtered by Buchner funnel, secondly by work
Property charcoal decolourized to obtain two class bases sugar, the two class base sugar obtained after decoloration carry out isomerization after ion exchange, by isomery
The two class base sugar changed are concentrated, and the two class base sugar that saccharification value is 42 in two class base sugar after concentration are separated, and will remain
Two remaining class base sugar are added in knockout tower and are refined, and two class base sugar after purification carry out secondary concentration, and obtaining saccharification value is 90
Two class bases sugar, the two class base sugar that saccharification value is 42 and the two class base sugar that saccharification value is 90 are carried out being mixed to get saccharification value being 55
Two class bases sugar；
Rock sugar saccharification: the rock sugar of monolith being ground, and smashed rock sugar is dissolved to obtain rock sugar turbid, will
Rock sugar turbid is filtered by Buchner funnel, obtains rock sugar solution, and rock sugar solution is concentrated to give saccharification value and is not less than
98 rock sugar centrotheca；
Step 4- mixing: three kinds of primary sugars obtained in step 3 are carried out according to the proportion to be mixed to get second level sugar；
Step 5- material: the second level sugar in step 4 is dissolved at 80 DEG C -90 DEG C, is adjusted according to F42+F90 → F55
The whole ratio being suitble to that matches out obtains three-level sugar；
Step 6- detection adjustment: three-level sugar obtained in step 5 is detected, and the detection element is followed successively by three-level sugar
Saccharification value, pH value, viscosity, activation number and concentration value, examining qualification is primary syrup；
Step 7- is qualitative: primary syrup obtained in step 6 being sieved, obtains fineness in the slurries of 80 mesh and at 105 DEG C
The lower high-temperature sterilization carried out in the 3min-5min time, and the alternating temperature sterilization process in 80 DEG C -90 DEG C is carried out in 30min again,
It is finally cooled to 60 DEG C and obtains finished product syrup；
Step 8- is canned: the progress canning sealing of finished product syrup obtained in step 7 is obtained mixing reconciliation syrup.
4. the manufacturing process of mixing reconciliation syrup made of a kind of selected rice according to claim 3, it is characterised in that:
The range of rock sugar solution temperature described in step 3 is within the scope of 80 DEG C -90 DEG C.
5. the manufacturing process of mixing reconciliation syrup made of a kind of selected rice according to claim 3, it is characterised in that:
In step 3 in decolorization the flow of active carbon in 2kg/m3- 3kg/m3In range.
6. the manufacturing process of mixing reconciliation syrup made of a kind of selected rice according to claim 3, it is characterised in that:
Saccharificatinn period in step 3 is within the scope of 40h-80h.
7. the manufacturing process of mixing reconciliation syrup made of a kind of selected rice according to claim 3, it is characterised in that:
For the ion-flow rate of step 3 intermediate ion exchange within the scope of 8m3/n-10m3/n, the environment pH value under ion exchange conditions is not small
Conductivity under 4, switched environment is not more than 50us.
8. the manufacturing process of mixing reconciliation syrup made of a kind of selected rice according to claim 3, it is characterised in that:
Isomerization operations are further limited in step 3: two class base sugar are eating soda acid by being added after ion exchange
PH value is adjusted in agent, and the pH value of the two classes base sugar is not less than 7.0 or is not less than in 7.5 ranges, i.e. two class bases sugar
Weakly acidic, the saccharification value in isomerization exit is not less than 43.
9. the manufacturing process of mixing reconciliation syrup made of a kind of selected rice according to claim 3, it is characterised in that:
It is reacted under atmospheric pressure of the concentration reaction under the vacuum degree not less than 650/mmHg within the scope of 0.5-0.6MPa in step 3,
Reaction kettle middle outlet temperature is concentrated and is not more than 65 DEG C, concentration reaction kettle middle outlet concentration is not less than 71 DEG C.
10. the manufacturing process of mixing reconciliation syrup, feature made of a kind of selected rice according to claim 3 exist
In: it carries out separating a kind of sugar and two classes sugar by separator in step 3.
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Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101433283A (en) * | 2008-12-31 | 2009-05-20 | 保龄宝生物股份有限公司 | Syrup for roasting and preparation method thereof |
| CN101979643A (en) * | 2010-10-01 | 2011-02-23 | 曾爱民 | Preparation process of rice high fructose syrup |
| CN103156109A (en) * | 2013-04-06 | 2013-06-19 | 肇庆焕发生物科技有限公司 | Special syrup for baking in preparation of moon cakes and bread and preparation method thereof |
| CN103695568A (en) * | 2013-12-12 | 2014-04-02 | 朱辉 | Syrup |
| CN105410884A (en) * | 2015-12-01 | 2016-03-23 | 青岛新中新新材料有限公司 | Anti-hardening syrup |
| CN106923310A (en) * | 2017-04-12 | 2017-07-07 | 盐城宇峰食品科技有限公司 | A kind of syrup dedicated production technology of drink |
-
2018
- 2018-08-02 CN CN201810871023.8A patent/CN109123606A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101433283A (en) * | 2008-12-31 | 2009-05-20 | 保龄宝生物股份有限公司 | Syrup for roasting and preparation method thereof |
| CN101979643A (en) * | 2010-10-01 | 2011-02-23 | 曾爱民 | Preparation process of rice high fructose syrup |
| CN103156109A (en) * | 2013-04-06 | 2013-06-19 | 肇庆焕发生物科技有限公司 | Special syrup for baking in preparation of moon cakes and bread and preparation method thereof |
| CN103695568A (en) * | 2013-12-12 | 2014-04-02 | 朱辉 | Syrup |
| CN105410884A (en) * | 2015-12-01 | 2016-03-23 | 青岛新中新新材料有限公司 | Anti-hardening syrup |
| CN106923310A (en) * | 2017-04-12 | 2017-07-07 | 盐城宇峰食品科技有限公司 | A kind of syrup dedicated production technology of drink |
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