CN105935246A - Milk preparation method of soybean milk machine adapted to altitudes - Google Patents
Milk preparation method of soybean milk machine adapted to altitudes Download PDFInfo
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- CN105935246A CN105935246A CN201610103050.1A CN201610103050A CN105935246A CN 105935246 A CN105935246 A CN 105935246A CN 201610103050 A CN201610103050 A CN 201610103050A CN 105935246 A CN105935246 A CN 105935246A
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- A—HUMAN NECESSITIES
- A47—FURNITURE; DOMESTIC ARTICLES OR APPLIANCES; COFFEE MILLS; SPICE MILLS; SUCTION CLEANERS IN GENERAL
- A47J—KITCHEN EQUIPMENT; COFFEE MILLS; SPICE MILLS; APPARATUS FOR MAKING BEVERAGES
- A47J31/00—Apparatus for making beverages
- A47J31/002—Apparatus for making beverages following a specific operational sequence, e.g. for improving the taste of the extraction product
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- A—HUMAN NECESSITIES
- A47—FURNITURE; DOMESTIC ARTICLES OR APPLIANCES; COFFEE MILLS; SPICE MILLS; SUCTION CLEANERS IN GENERAL
- A47J—KITCHEN EQUIPMENT; COFFEE MILLS; SPICE MILLS; APPARATUS FOR MAKING BEVERAGES
- A47J31/00—Apparatus for making beverages
- A47J31/44—Parts or details or accessories of beverage-making apparatus
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- A—HUMAN NECESSITIES
- A47—FURNITURE; DOMESTIC ARTICLES OR APPLIANCES; COFFEE MILLS; SPICE MILLS; SUCTION CLEANERS IN GENERAL
- A47J—KITCHEN EQUIPMENT; COFFEE MILLS; SPICE MILLS; APPARATUS FOR MAKING BEVERAGES
- A47J31/00—Apparatus for making beverages
- A47J31/44—Parts or details or accessories of beverage-making apparatus
- A47J31/4403—Constructional details
- A47J31/441—Warming devices or supports for beverage containers
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- A—HUMAN NECESSITIES
- A47—FURNITURE; DOMESTIC ARTICLES OR APPLIANCES; COFFEE MILLS; SPICE MILLS; SUCTION CLEANERS IN GENERAL
- A47J—KITCHEN EQUIPMENT; COFFEE MILLS; SPICE MILLS; APPARATUS FOR MAKING BEVERAGES
- A47J31/00—Apparatus for making beverages
- A47J31/44—Parts or details or accessories of beverage-making apparatus
- A47J31/58—Safety devices
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- A—HUMAN NECESSITIES
- A47—FURNITURE; DOMESTIC ARTICLES OR APPLIANCES; COFFEE MILLS; SPICE MILLS; SUCTION CLEANERS IN GENERAL
- A47J—KITCHEN EQUIPMENT; COFFEE MILLS; SPICE MILLS; APPARATUS FOR MAKING BEVERAGES
- A47J43/00—Implements for preparing or holding food, not provided for in other groups of this subclass
- A47J43/04—Machines for domestic use not covered elsewhere, e.g. for grinding, mixing, stirring, kneading, emulsifying, whipping or beating foodstuffs, e.g. power-driven
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- A—HUMAN NECESSITIES
- A47—FURNITURE; DOMESTIC ARTICLES OR APPLIANCES; COFFEE MILLS; SPICE MILLS; SUCTION CLEANERS IN GENERAL
- A47J—KITCHEN EQUIPMENT; COFFEE MILLS; SPICE MILLS; APPARATUS FOR MAKING BEVERAGES
- A47J43/00—Implements for preparing or holding food, not provided for in other groups of this subclass
- A47J43/04—Machines for domestic use not covered elsewhere, e.g. for grinding, mixing, stirring, kneading, emulsifying, whipping or beating foodstuffs, e.g. power-driven
- A47J43/07—Parts or details, e.g. mixing tools, whipping tools
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- A—HUMAN NECESSITIES
- A47—FURNITURE; DOMESTIC ARTICLES OR APPLIANCES; COFFEE MILLS; SPICE MILLS; SUCTION CLEANERS IN GENERAL
- A47J—KITCHEN EQUIPMENT; COFFEE MILLS; SPICE MILLS; APPARATUS FOR MAKING BEVERAGES
- A47J43/00—Implements for preparing or holding food, not provided for in other groups of this subclass
- A47J43/04—Machines for domestic use not covered elsewhere, e.g. for grinding, mixing, stirring, kneading, emulsifying, whipping or beating foodstuffs, e.g. power-driven
- A47J43/07—Parts or details, e.g. mixing tools, whipping tools
- A47J43/075—Safety devices
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- Food Science & Technology (AREA)
- Mechanical Engineering (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Paper (AREA)
- Dairy Products (AREA)
Abstract
The invention provides a milk preparation method of soybean milk machine adapted to altitudes. The method comprises a pre-heating stage and a crushing and boiling stage. The milk preparation method is characterized in that the pre-heating stage comprises a pre-heating finishing and judgment process; the pre-heating finishing and judgment process comprises following steps: collecting and recording temperature T of mixture between milk-preparing material and water at the time interval Delta t, wherein the temperature corresponding to the nth collection record is T (n); calculating temperature difference Delta T corresponding to continuous k time intervals Delta T, wherein temperature difference in the mth group of continuous k time intervals Delta T corresponds to Detla T (m) and the Detla T (m) is equal to T (m+k)-T(m); and taking temperature Tf at the time point as the crushing temperature and entering the crushing and boiling phase when the temperature difference Delta T is less than the frequency satisfaction pre-set condition of threshold value Delta Td.Due to the fact that monitoring temperature varies with the time changes, mixture between milk-preparing material and water is kept at the boiling point or near to temperature below the altitude prior to the crushing and boiling phase so that nutrients of milk-preparing material can be released and a muting effect is obtained.
Description
Technical field
The present invention relates to the pulping process of a kind of self elevation adaption soy bean milk making machine, belong to food processing field.
Background technology
On market, existing soy bean milk making machine is typically designed to use in plains region, has special plateau soy bean milk making machine for highlands.Two kinds of soy bean milk making machine use different pulping process, and reason is that plains region and highlands boiling point difference are bigger.A set of pulping program of existing soy bean milk making machine can not be compatible with plains region and highlands.Such as, the soy bean milk making machine that plains region uses is when highlands uses, and owing to highlands boiling point is low compared with plains region, this making beating temperature set in resulting in soy bean milk making machine is the most higher, even above the boiling temperature of highlands, at this moment arises that the phenomenon that only heating is not pulverized.When the soy bean milk making machine used when highlands uses in plains region, owing to the boiling point of plains region is higher than highlands, this making beating temperature set in resulting in soy bean milk making machine is the most on the low side, easily occurs that foam is too much unfavorable for the situation of slurrying.It addition, i.e. allowed to pulping process, existing pulping process is also unable to reach preferable effects on slurry making, meets user in slurrying cycle, the requirement of the aspect such as quiet.
Summary of the invention
Pulping process for existing soy bean milk making machine is difficult in adapt to the problem of Different Altitude, the invention provides the pulping process of a kind of self elevation adaption soy bean milk making machine, is achieved through the following technical solutions:
A kind of pulping process of self elevation adaption soy bean milk making machine, including pre-heat phase and pulverizing infusion stage, it is characterized in that, described pre-heat phase includes having preheated judge process, the described judge process that preheated includes procedure below: temperature T of per interval Δ t acquisition and recording pulping materials and the mixture of water, and the corresponding temperature of n-th acquisition and recording is T(n)；Calculate continuous k interval time temperature difference Δ T corresponding to Δ t, m group continuous k interval time temperature difference corresponding to Δ t be Δ T(m), wherein, Δ T(m)=T(m+k)-T(m)；When the temperature difference Δ T number of times less than threshold value Δ Td meets pre-conditioned, then take temperature Tf of this time point for pulverizing temperature and entering the pulverizing infusion stage.
Further, described pulverizing temperature Tf is not less than under this height above sea level below the boiling point of corresponding water 10 degrees Celsius.
Further, described threshold value Δ Td=Δ T(1) * α, wherein, Δ T(1) be the 1st group continuous k interval time temperature difference corresponding to Δ t, α is correction factor, 0 ＜ α ＜ 1.
Further, before having preheated judge process described in, the mixture of pulping materials Yu water is heated to predetermined temperature Tc.
Further, temperature difference Δ T then records once less than threshold value Δ Td, otherwise subtracts once, records temperature Tf then taking this time point for three times for pulverizing temperature and entering the pulverizing infusion stage；Or, continuous i temperature difference Δ T is less than threshold value Δ Td, then take temperature Tf of this time point for pulverizing temperature and entering pulverizing infusion stage, wherein, i=2 to 5.
Further, Δ T(1) * α do not sets in temperature range first, then Δ Td take off one group continuous k interval time temperature difference corresponding to Δ t be multiplied by correction factor α, continuously j Δ T(j) * α is in the first setting temperature range, then Δ Td takes preset value Δ Td ', wherein, described first sets temperature range as Δ Td ' ± M, and M is the deviation of temperature value under the conditions of different operating.
Further, T(n+1)-T(n) do not set in temperature range second, then T(n+1)=T(n)+Δ Td '/k, Δ Td ' is preset value, wherein, described second to set temperature range as (Δ Td ' ± M)/k, M be the deviation of temperature value under the conditions of different operating.
Further, 10 seconds≤k* Δ t≤60 second.
Further, k=2 to 15, the Δ t=2 second was to 5 seconds.
Further, described soy bean milk making machine includes anti-overflow device, and in described pre-heat phase, pulping materials and the mixture touching anti-overflow device of water, then enter and pulverize the infusion stage；Or, described pre-heat phase exceedes scheduled duration, then enter and pulverize the infusion stage；Or, also including between described pre-heat phase and pulverizing infusion stage the mixture of pulping materials Yu water is maintained at the high temperature holding stage pulverizing more than temperature Tf, described high temperature keeps phase duration to be tf；Or, adjust the heating power in the follow-up pulverizing infusion stage according to described pulverizing temperature Tf.
In the present invention, owing in pre-heat phase, pulping materials is not difficult to by touching the high temperature near anti-judgement boiling point or boiling point through pulverizing, use the process changed over time by the temperature of monitoring pulping materials with the mixture of water, accurately judge that pre-heat phase exits time point, it is maintained at the boiling point under this height above sea level or the temperature near boiling point in fact, to reach to promote the release of pulping materials nutrient substance and quiet technique effect now into the mixture of pulping materials and water before pulverizing the infusion stage.
Accompanying drawing explanation
The present invention is described in further detail with detailed description of the invention below in conjunction with the accompanying drawings:
Fig. 1 is the pulping process flow process of the present invention；
Fig. 2 is the schematic diagram that under firm power of the present invention, temperature changes over time；
Fig. 3 is the schematic diagram of the sample record temperature of the present invention each interval time.
Detailed description of the invention
As it is shown in figure 1, the pulping process of a kind of self elevation adaption soy bean milk making machine, including pre-heat phase and pulverizing infusion stage.Soy bean milk making machine includes mash vessel, is placed with the mixture of pulping materials and water in mash vessel.In pulverizing the infusion stage, pulverizing pulping materials and infusion, crushing process and infusion process alternately or synchronize to carry out.nullBefore entering the pulverizing infusion stage，The mixture of pulping materials with water need to be preheated，On the one hand，Promote pulping materials，The especially cell wall imbibition of Semen sojae atricolor，Fiber and pectin are organized in degeneration softening under heat effect simultaneously，Lose compactness and support function，Realize rupturing of cell wall tissue，After degeneration, the soluble fiber in cell wall such as pectin tissue separates from cell wall structure and is dissolved in water，Enhance the stably dispersing of dietary fiber，In addition cell wall forms bigger gap，Intracellular nutritional element is made to be able to dissolution，On the other hand，Pulping materials is made just to be in the process of high temperature bubble bean from the firm incipient stage of pulping process，Pulping materials can be sufficiently softened，In follow-up crushing process，Not only the load of motor can diminish，Noise of motor decreases，Electrical machinery life also gets a promotion，The process of the mash vessel sidewall of pulping materials impact simultaneously also will be buffered，Reduce slurrying noise further，Improve Consumer's Experience.
As shown in Figure 2, under conditions of firm power heats, pulping materials gradually rises with the temperature of the mixture of water, along with temperature rises, and progressively become big with the temperature difference of ambient temperature, heat leakage effect tends to obvious, and the temperature T/ time slope of t progressively diminishes, and will tend towards stability and be maintained at boiling temperature after boiling temperature corresponding under arriving this height above sea level.
Above-mentioned pre-heat phase includes having preheated judge process, require that pre-heat phase reaches uniform temperature backed off after random, enter next pulp stage, in order to reach above-mentioned technique effect, that need to improve pre-heat phase as far as possible exits temperature, so, the boiling temperature under this height above sea level will be the above-mentioned limit exiting temperature, and therefore exiting temperature is the boiling point under this height above sea level or the temperature near boiling point.
Concrete, preheat judge process and include procedure below:
As it is shown on figure 3, temperature T of the mixture of per interval Δ t acquisition and recording pulping materials and water, the corresponding temperature of n-th acquisition and recording is T(n)；Calculate continuous k interval time temperature difference Δ T corresponding to Δ t, m group continuous k interval time temperature difference corresponding to Δ t be Δ T(m), wherein, Δ T(m)=T(m+k)-T(m)；When the temperature difference Δ T number of times less than threshold value Δ Td meets pre-conditioned, then temperature Tf taking this time point for pulverizing temperature and enters the pulverizing infusion stage, and that pulverizes the most above-mentioned pre-heat phase of temperature exits temperature herein.The characteristic disclosed based on Fig. 2, closer to boiling temperature, the slope of temperature T/ time t becomes the least, takes corresponding threshold value Δ Td and the most pre-conditioned can accurately control suitably to pulverize temperature Tf.
For the ease of understanding, below with k=9, the situation of Δ t=3 second is embodiment, and T1 is the temperature of acquisition and recording first, follow-up is followed successively by T2, T3, T4 ..., accordingly, 1st group continuous 9 interval time temperature difference corresponding to Δ t be Δ T(1), Δ T(1)=T(10)-T(1), the 2nd group continuous 9 interval time temperature difference corresponding to Δ t be Δ T(2), Δ T(2)=T(11)-T(2), the like.Visible, to have 8(i.e. k-1 between adjacent Δ T) individual interval time Δ t temperature rise be to overlap, it is worth mentioning that, temperature difference Δ T embodies (i.e. temperature rise in the k* Δ t) time in 27 seconds, suitable extends duration, avoid temperature sensor insensitive to temperature rise in length time shorter, improve the accuracy measured, additionally, before exiting pre-heat phase, in the comparison procedure of temperature difference Δ T and threshold value Δ Td, will (i.e. Δ t) be unit time lengthening, and then avoids the unit interval and longer cause slurrying cycle stretch-out with 3 seconds.Based on above-mentioned analysis, in order to solve the temperature sensor problem to the sensitivity of temperature rise, selecting 10 seconds≤k* Δ t≤60 second, further take into account slurrying periodic problem, select k=2 to 15, the Δ t=2 second was to 5 seconds.
It is pointed out that the size by adjusting threshold value Δ Td, will directly control to pulverize the height of temperature Tf, being appreciated that threshold value Δ Td is the biggest, the temperature difference Δ T condition less than threshold value Δ Td will be the most wide in range, threshold value Δ Td is closer to zero, and the temperature difference Δ T condition less than threshold value Δ Td will be the most harsh.In order to reach the release of above-mentioned promotion pulping materials nutrient substance and quiet technique effect, pulverize below the boiling point of the water that temperature Tf is not less than under this height above sea level correspondence 10 degrees Celsius.
Selection for threshold value Δ Td, default numerical value can be selected, further, different in view of slurrying amount, pulping materials is different from the proportioning of water and the not series of factors on an equal basis of the different heat leakage speed brought such as air pressure, temperature in working environment, even if heating power is certain, the temperature rise of unit interval Δ t also can be different, preferably, take threshold value Δ Td=Δ T(1) * α, wherein, Δ T(1) be the 1st group continuous k interval time temperature difference corresponding to Δ t, α is correction factor, 0 ＜ α ＜ 1.By the 1st group of temperature difference Δ T(1 in threshold value Δ Td and this pulping process) linkage, and then define the control process of closed loop, it is adapted to different operating environment, the most different altitude conditions, on the other hand, by default correction factor α, the size of threshold value Δ Td is adjusted, and then control to pulverize the degree of closeness of the boiling point of the temperature Tf water corresponding with under this height above sea level, reach a high temperature the requirement pulverized.In the present embodiment, the selection of 10 seconds≤k* Δ t≤60 second also have impact on temperature difference Δ T(1), and then affect threshold value Δ Td, if k* Δ t ＞ 60 seconds, then can bring temperature difference Δ T(1) excessive, cause threshold value Δ Td excessive, in turn result in the temperature difference Δ T condition less than threshold value Δ Td the most wide in range.
Further, it is contemplated that the thermometric that temperature sensor fails or transient temperature fluctuation bring is inaccurate, and it is necessary for arranging self-recision process.Above-mentioned self-recision process includes: if Δ T(1) * α would not do not set in temperature range first, then Δ Td takes Δ T(2) * α, i.e. next group continuous k interval time temperature difference corresponding to Δ t be multiplied by correction factor α, judge Δ T(2 again) whether * α set in temperature range first, if j Δ T(j continuously) * α is not in the first setting temperature range, then and Δ Td takes preset value Δ Td '.Generally, j takes 3, does not sets in temperature range first for the most continuous 3 times, then Δ Td takes preset value Δ Td '.Wherein, above-mentioned first sets temperature range as Δ Td ' ± M, and M is the deviation of temperature value under the conditions of different operating.
The determination process being not limited to threshold value Δ Td arranges self-recision process, it is also possible at each T(n) acquisition and recording during self-recision process is set.This self-recision process includes: T(n+1)-T(n) do not set in temperature range second, then T(n+1)=T(n)+Δ Td '/k, Δ Td ' they are preset value, wherein, above-mentioned second to set temperature range as (Δ Td ' ± M)/k, M be the deviation of temperature value under the conditions of different operating.
It is appreciated that above two self-recision process can be arranged simultaneously, it is also possible to arrange time different.In the case of arranging above two self-recision process at the same time, the parameter preset Δ Td ' during two kinds of self-recisions, M should be identical.
You need to add is that, said temperature difference Δ T less than the number of times of threshold value Δ Td meet pre-conditioned in pre-conditioned can be various, the height of temperature Tf is pulverized in impact by pre-conditioned harsh degree equally, also can affect the slurrying cycle.As above-mentioned pre-conditioned preferably embodiment, including: temperature difference Δ T then records once less than threshold value Δ Td, otherwise subtracts once, record temperature Tf then taking this time point for three times for pulverizing temperature and entering and pulverize the infusion stage；Or, continuous i temperature difference Δ T is less than threshold value Δ Td, then temperature Tf taking this time point for pulverizing temperature and enters pulverizing infusion stage, wherein, i=2 to 5, preferably, takes i=3.
Before having preheated judge process, the mixture of pulping materials Yu water is heated to predetermined temperature Tc, i.e. before being heated to predetermined temperature Tc, it is not necessary to record temperature, it is to avoid too much take the operational capability of single-chip microcomputer.Generally, height above sea level more than 6000 meters is depopulated zone, and 6000 meters of corresponding boiling temperatures of height above sea level are 80 degrees Celsius, in view of temperature sensor measurement error or other cause specific, desirable 78-85 degree Celsius of predetermined temperature Tc, preferably, predetermined temperature Tc takes 80 degrees Celsius.Certainly, the process gathering and recording temperature can also run through whole preheating process, in the case of this, has preheated judge process i.e. preheating process.
It is noted that also include between pre-heat phase and pulverizing infusion stage the mixture of pulping materials Yu water is maintained at the high temperature holding stage pulverizing more than temperature Tf, high temperature keeps phase duration to be tf.Reasonably high temperature keeps phase duration tf, by release and the quiet technique effect of further above-mentioned promotion pulping materials nutrient substance.
Further, according to the corresponding relation of boiling point Yu height above sea level, adjust the heating power in the follow-up pulverizing infusion stage according to pulverizing temperature Tf, can reach preferably effects on slurry making.
Additionally, impact in view of different pulping materials, as user's placement the most i.e. produces the pulping materials of a large amount of foam, the risk of spilling is just had at pre-heat phase, soy bean milk making machine includes anti-overflow device, if pulping materials and the mixture touching anti-overflow device of water, then enter and pulverize the infusion stage in pre-heat phase.It is difficult to, in view of other, the special circumstances envisioned, if pre-heat phase exceedes scheduled duration, then enters and pulverize the infusion stage.
Certainly, those skilled in the art are appreciated that above content is only presently preferred embodiments of the present invention, not it is used for limiting the practical range of the present invention, the most all impartial changes made according to the present invention and modification, be all scope of the invention as claimed and contained, illustrate the most one by one.
Claims (10)
1. a pulping process for self elevation adaption soy bean milk making machine, including pre-heat phase with pulverize the infusion stage, it is characterised in that described pre-heat phase includes having preheated judge process, described in preheated judge process and included procedure below:
Temperature T of the mixture of per interval Δ t acquisition and recording pulping materials and water, the corresponding temperature of n-th acquisition and recording is T(n)；
Calculate continuous k interval time temperature difference Δ T corresponding to Δ t, m group continuous k interval time temperature difference corresponding to Δ t be Δ T(m), wherein, Δ T(m)=T(m+k)-T(m)；
When the temperature difference Δ T number of times less than threshold value Δ Td meets pre-conditioned, then take temperature Tf of this time point for pulverizing temperature and entering the pulverizing infusion stage.
The pulping process of self elevation adaption soy bean milk making machine the most according to claim 1, it is characterised in that described pulverizing temperature Tf is not less than under this height above sea level below the boiling point of corresponding water 10 degrees Celsius.
The pulping process of self elevation adaption soy bean milk making machine the most according to claim 1, it is characterised in that described threshold value Δ Td=Δ T(1) * α, wherein, Δ T(1) be the 1st group continuous k interval time temperature difference corresponding to Δ t, α is correction factor, 0 ＜ α ＜ 1.
4. according to the pulping process of the self elevation adaption soy bean milk making machine described in claim 1 or 2 or 3, it is characterised in that described in preheated judge process before the mixture of pulping materials Yu water is heated to predetermined temperature Tc.
5. according to the pulping process of the self elevation adaption soy bean milk making machine described in claim 1 or 2 or 3, it is characterized in that, temperature difference Δ T then records once less than threshold value Δ Td, otherwise subtracts once, records temperature Tf then taking this time point for three times for pulverizing temperature and entering the pulverizing infusion stage；Or, continuous i temperature difference Δ T is less than threshold value Δ Td, then take temperature Tf of this time point for pulverizing temperature and entering pulverizing infusion stage, wherein, i=2 to 5.
The pulping process of self elevation adaption soy bean milk making machine the most according to claim 3, it is characterized in that, Δ T(1) * α do not sets in temperature range first, then Δ Td take off one group continuous k interval time temperature difference corresponding to Δ t be multiplied by correction factor α, j Δ T(j continuously) * α is not in the first setting temperature range, then and Δ Td takes preset value Δ Td ', wherein, described first sets temperature range as Δ Td ' ± M, and M is the deviation of temperature value under the conditions of different operating.
The pulping process of self elevation adaption soy bean milk making machine the most according to claim 1, it is characterized in that, T(n+1)-T(n) do not set in temperature range second, then T(n+1)=T(n)+Δ Td '/k, Δ Td ' is preset value, wherein, described second to set temperature range as (Δ Td ' ± M)/k, M be the deviation of temperature value under the conditions of different operating.
The pulping process of self elevation adaption soy bean milk making machine the most according to claim 1, it is characterised in that 10 seconds≤k* Δ t≤60 second.
The pulping process of self elevation adaption soy bean milk making machine the most according to claim 8, it is characterised in that k=2 to 15, the Δ t=2 second was to 5 seconds.
The pulping process of self elevation adaption soy bean milk making machine the most according to claim 1, it is characterised in that described soy bean milk making machine includes anti-overflow device, in described pre-heat phase, pulping materials and the mixture touching anti-overflow device of water, then enter and pulverize the infusion stage；Or, described pre-heat phase exceedes scheduled duration, then enter and pulverize the infusion stage；Or, also including between described pre-heat phase and pulverizing infusion stage the mixture of pulping materials Yu water is maintained at the high temperature holding stage pulverizing more than temperature Tf, described high temperature keeps phase duration to be tf；Or, adjust the heating power in the follow-up pulverizing infusion stage according to described pulverizing temperature Tf.
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| CN108563262A (en) * | 2018-07-02 | 2018-09-21 | 四川长虹电器股份有限公司 | A kind of adaptive liquid heating control method of High aititude |
| CN108606631A (en) * | 2016-12-13 | 2018-10-02 | 佛山市顺德区美的电热电器制造有限公司 | Electric cooking pot and its anti-overflow discharge control method and device |
| CN109805735A (en) * | 2017-11-22 | 2019-05-28 | 佛山市顺德区美的电热电器制造有限公司 | Method for heating and controlling, device, computer readable storage medium and cooking apparatus |
| CN110393458A (en) * | 2019-08-19 | 2019-11-01 | 九阳股份有限公司 | A kind of boiling point detecting method of food processor |
| CN111012175A (en) * | 2019-12-04 | 2020-04-17 | 宁波拓邦智能控制有限公司 | Control method and device of wall breaking machine, wall breaking machine and computer readable storage medium |
| CN112099550A (en) * | 2020-08-18 | 2020-12-18 | 宁波方太厨具有限公司 | Temperature control method for water heating electric appliance |
| CN112914376A (en) * | 2021-03-30 | 2021-06-08 | 小熊电器股份有限公司 | Method for automatically determining boiling point of food by wall breaking machine and pulping method |
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