CN111838638A - Full-automatic electromagnetic induction heating and baking purification equipment for alkaline cooked salt - Google Patents
Full-automatic electromagnetic induction heating and baking purification equipment for alkaline cooked salt Download PDFInfo
- Publication number
- CN111838638A CN111838638A CN202010551537.2A CN202010551537A CN111838638A CN 111838638 A CN111838638 A CN 111838638A CN 202010551537 A CN202010551537 A CN 202010551537A CN 111838638 A CN111838638 A CN 111838638A
- Authority
- CN
- China
- Prior art keywords
- electromagnetic induction
- exhaust
- induction heating
- value
- salt
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Images
Classifications
-
- 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
- A23L27/00—Spices; Flavouring agents or condiments; Artificial sweetening agents; Table salts; Dietetic salt substitutes; Preparation or treatment thereof
- A23L27/40—Table salts; Dietetic salt substitutes
-
- 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
- A23L5/00—Preparation or treatment of foods or foodstuffs, in general; Food or foodstuffs obtained thereby; Materials therefor
- A23L5/20—Removal of unwanted matter, e.g. deodorisation or detoxification
- A23L5/21—Removal of unwanted matter, e.g. deodorisation or detoxification by heating without chemical treatment, e.g. steam treatment, cooking
Abstract
The invention discloses full-automatic electromagnetic induction roasting equipment for alkaline cooked salt, which comprises a high-temperature pollution discharge mechanism, a pH value regulating mechanism and a cooling mechanism, wherein the high-temperature pollution discharge mechanism is used for electromagnetically heating and stirring raw materials to enable salt to generate steam at high temperature, and dirty gas is discharged from an outlet and enters a pipeline to be discharged; the pH value regulating mechanism is used for conveying the salt fried by the electromagnetic induction heating blowdown mechanism to the pH value regulating mechanism for pH value conversion to alkalinity of 7.35-9.90; and the cooling mechanism is used for cooling and conveying the raw materials converted by the PH value regulating cylinder to a finished product room. Compared with the prior art, the invention has the beneficial effects that: the invention has the beneficial effects that: 1. the whole production line is automatically regulated and controlled; 2. the requirement of subhealthy groups of society on the pH value of the salt is met, the problem of pollution of plastic micro-particles in the salt is solved under the condition of high-temperature production by adopting the equipment, and Chinese common people can eat safe and reassuring healthy green food.
Description
Technical Field
The invention relates to the field of cooked salt preparation, in particular to full-automatic electromagnetic induction heating purification equipment for baking alkaline cooked salt.
Background
The monitoring data is currently implemented according to the national regulation standards. If the pH value of the package solution is less than 7.00, the package solution is acidic, equal to 7.00, the package solution is neutral, and more than 7.00, the package solution is alkaline. The normal human body fluid has a ph value of 7.35-7.45, which is a healthy body constitution. While the normal uric acid value of male is 149-416 umol/L, the normal uric acid value of female is 89-357 umol/L. The uric acid value is very critical in the detection because the uric acid is too high or too low, which can cause various diseases of the human body. According to the theoretical analysis of medicine, the pH value of less than 7.00 belongs to metabolic acidosis states (such as diseases of obesity, three highs, gout, diabetes, glomerular disease, hyperuricemia, tuberculosis, cancer and the like are raised). A ph value higher than 7.45 is attributed to metabolic alkalosis (such as diseases of infectious diseases, dizziness, frequent emesis, renal tubular acidosis, etc. are increased). Generally, the ph value of the body fluid of the born baby is 7.35-7.45, which is not the case of diabetes of the giant baby. In the growth process of people, the dietary structure is in an unbalanced state for a long time, so that metabolic disturbance is caused, and uric acid is increased.
The pH value of common salt is neutral. In 2013, in experimental detection, the pH value of the processed salt is increased from 7 to 7.35-9.90, and the salt belongs to alkaline cooked salt. According to the standards established by the world health organization, consumers are divided into two groups of people with different ph values, namely healthy people and sub-healthy people after the data are analyzed. According to the requirements of the two groups of people, the invention uses a technology of full-automatic electromagnetic induction roasting equipment and process of alkaline cooked salt, and a method of the equipment and the process by the technology. According to two groups of people with different ph values, two products with different ph values are respectively prepared, one is 'weak alkaline' cooked salt. The other is "basic" boiled salt. The ph value of the weakly alkaline cooked salt is maintained between 7.35 and 8.5, and the salt is edible for general people and healthy people. Is also the best product for pregnant women, children, old people and people with weak body. And the ph value of the other alkaline cooked salt is maintained between 8 and 9.30, and the salt belongs to the group of sub-health (such as gout, nephropathy, hypertension, hyperglycemia, diabetes, hyperuricemia and the like) people. The cooked salt is directly added into purified water to be adjusted into 0.9-10% of weak alkaline saline which is directly drunk by people with diarrhea and hyperhidrosis, and the acidity and alkalinity are scientific. Can be used for anti-inflammation and sterilization, such as gargling (canker sore), bathing (skin itching), foot bath (dermatophytosis), and the like. The alkaline cooked salt can be used for washing meat, vegetables, fruits, tableware and the like, and can effectively remove oil dirt and pesticide residues. The alkaline cooked salt is safe, healthy and relieved, and is energy-saving, environment-friendly and water-saving.
Disclosure of Invention
The invention aims to provide full-automatic electromagnetic induction heating purification equipment for baking alkaline cooked salt, which aims to solve the problems in the background technology.
In order to achieve the purpose, the invention provides the following technical scheme:
a full-automatic electromagnetic induction heating and baking purification device for alkaline cooked salt comprises a high-temperature pollution discharge mechanism, a pH value regulation mechanism and a cooling mechanism, wherein the high-temperature pollution discharge mechanism is used for carrying out electric induction heating and stirring on raw materials to enable salt to generate steam at high temperature and discharge foul gas into a pipeline from an outlet to be discharged; the pH value regulating mechanism is used for frying the high-temperature dehydration and pollution discharge mechanism, and conveying salt to the pH value regulating mechanism to convert the pH value into alkalinity of 7.35-9.90; and the cooling mechanism is used for cooling and conveying the raw materials converted by the PH value regulating cylinder to a finished product room.
As a further scheme of the invention: the high temperature sewage mechanism is including the blowdown section of thick bamboo that dewaters, and fixedly connected with auger in the blowdown section of thick bamboo that dewaters makes the salt caking in order to prevent the blowdown section of thick bamboo high temperature that dewaters, makes the blowdown section of thick bamboo take out the clearance from the zone of heating, and the auger is equipped with automatic clearance function in the blowdown section of thick bamboo that dewaters, the blowdown section of thick bamboo left end that dewaters is equipped with the feed inlet, through auger pay-off access connection between feeder hopper and the feed inlet, auger pay-off access connection upper portion is provided with exhaust passage, installs the exhaust fan between exhaust passage and the total passageway.
As a still further scheme of the invention: the outer side of the heating layer is fixedly connected with a heat insulation layer, the heating temperature of the heating layer is 800 ℃, the heating layer is uniformly heated at 360 ℃, and the dehydration blowdown cylinder is preheated for 10-15 minutes.
As a still further scheme of the invention: the heating layer is a split type between an electric heating net and a dehydration and pollution discharge cylinder.
As a still further scheme of the invention: the dehydration blowdown cylinder is in transmission connection with a power mechanism through a bearing gear pulling chain.
As a still further scheme of the invention: an exhaust passage is arranged at the upper part of the dehydration blowdown cylinder, an exhaust fan is arranged between the exhaust passage and the exhaust heat dissipation main passage, a measuring instrument is arranged on the dehydration blowdown cylinder, and the measuring instrument monitors the temperature, the time and the auger stirring speed of the dehydration blowdown cylinder.
As a still further scheme of the invention: the dehydration waste fitting discharging tube comprises a dehydration waste fitting discharging tube output end, a dehydration waste fitting discharging tube exhaust port is arranged on the upper portion of the discharge port, the lower portion of the discharge port is connected with a storage hopper, an exhaust passage is connected to the upper portion of the storage hopper and connected with the dehydration waste fitting discharging tube exhaust port, an exhaust fan is arranged on the upper portion of the exhaust passage and communicated with a heat dissipation main passage, a detection sampling port is arranged on the upper right portion of the storage hopper, and a packing auger feeding passage is arranged at.
As a still further scheme of the invention: the PH value regulation and control device comprises a PH value regulation and control barrel, wherein paddles are arranged in the PH value regulation and control barrel, the temperature of the paddles is controlled to be 399-719 ℃, the rotation time of the PH value regulation and control barrel is set to be 15-30 minutes, the PH value of raw salt is converted into alkaline boiled salt, a feed inlet is arranged on the left side of the PH value regulation and control barrel, the feed inlet is communicated with an auger feeding channel on a storage hopper, and a discharge outlet is arranged on the right side of the PH value regulation and control.
As a still further scheme of the invention: a heating layer is arranged on the outer side of the pH value regulating cylinder, a heat insulating layer is arranged on the outer side of the heating layer, the temperature of the heating layer is controlled to be 300-800 ℃,
as a still further scheme of the invention: the heating layer is a split type between an electric heating net and a dehydration and pollution discharge cylinder.
As a still further scheme of the invention: and a measuring instrument is arranged on the upper part of the PH value regulating cylinder and used for monitoring the temperature, time and speed of the PH value regulating cylinder.
As a still further scheme of the invention: the lower part of the discharge port is provided with a cooked salt storage hopper, the upper part of the storage hopper is communicated with an exhaust heat dissipation channel, the exhaust heat dissipation channel is communicated with the discharge port, the upper part of the exhaust heat dissipation channel is provided with an exhaust fan, and the exhaust fan is connected with an exhaust heat dissipation main channel.
As a still further scheme of the invention: the lower part of the cooked salt storage hopper is provided with a cooked salt conveying auger, the upper part of the cooked salt storage hopper is provided with a cooked salt sampling port, and the cooked salt conveying auger is connected with a cooling box.
As a still further scheme of the invention: the cooling mechanism comprises a cooling box, an exhaust heat dissipation channel is arranged on the upper portion of the cooling box, an exhaust fan is arranged on the exhaust heat dissipation channel, and the exhaust fan is connected with an exhaust heat dissipation main channel.
As a still further scheme of the invention: the left side of the cooling box is connected with a packing auger feeding channel, the right side of the cooling box is provided with a cooked salt conveying packing auger channel, and alkaline cooked salt is conveyed to a finished product workshop through a packing auger.
Compared with the prior art, the invention has the beneficial effects that: 1. the whole production line is automatically regulated and controlled; 2. the requirement of subhealthy groups of society on the pH value of the salt is met, the problem of pollution of plastic micro-particles in the salt is solved under the condition of high-temperature production by adopting the equipment, and Chinese common people can eat safe and reassuring healthy green food; 3. the high-temperature rolling cylinder can be heated by adopting various heating methods; 4. the pollution discharge cylinder is separated from the heating layer, so that the pollution discharge cylinder is convenient to pump out and clean, and the heating layer can be conveniently maintained; 5, the stirrer stirs uniformly and the like.
Drawings
FIG. 1 is a schematic structural diagram of a full-automatic electromagnetic induction heating purification device for baking alkaline cooked salt;
in the figure: 1-a feed hopper, 2-an auger feeding channel, 3-an auger feeding channel, 4-a feed inlet, 5-a dehydration blowdown cylinder, 6-a first heating layer, 7-a first heat insulation layer, 8-an auger, 9-a first measuring instrument, 10-a discharge outlet, 11-an exhaust outlet, 12-a second exhaust channel, 13-a second exhaust fan, 14-a detection sampling port, 15-an exhaust storage hopper, 16-a storage hopper auger feeding channel, 17-a pH value regulation cylinder feed inlet, 18-a pH value regulation cylinder, 19-a second heating layer, 20-a second heat insulation layer, 21-a paddle, 22-a pH value regulation cylinder measuring instrument, 23-a cooked salt discharge outlet, 24-a cooked salt storage hopper, 25, a cooked salt conveying auger, 26-a cooked salt sampling port, 27-a first exhaust heat dissipation channel, 28-a first heat dissipation fan, 29-a third exhaust channel, 30-a third exhaust fan, 31-a cooling box, 32, a second air heat dissipation channel, 33, a second heat dissipation fan, 34-a cooked salt conveying auger, 35-a finished product workshop, 36-a first exhaust channel, 37-a first exhaust fan and 38-an exhaust heat dissipation total channel.
Detailed Description
The technical solution of the present patent will be described in further detail with reference to the following embodiments.
The first embodiment is as follows: referring to fig. 1, a full-automatic electromagnetic induction heating and baking purification device for alkaline cooked salt comprises a high-temperature pollution discharge mechanism, a PH value regulation mechanism and a cooling mechanism, wherein the electromagnetic induction heating pollution discharge mechanism is used for heating and stirring raw materials at a high temperature to enable salt to generate steam at a high temperature, and foul gas is discharged from an outlet into a pipeline to be discharged; the pH value regulating mechanism is used for conveying the salt fried by the high-temperature pollution discharge mechanism to the pH value regulating mechanism to convert the pH value into alkalinity of 7.35-9.90; and the cooling mechanism is used for cooling and conveying the raw materials converted by the PH value regulating cylinder to a finished product room.
High temperature sewage discharging mechanism is including dehydration blowdown section of thick bamboo 5, and fixedly connected with auger 8 in the dehydration blowdown section of thick bamboo 5, in order to prevent that 5 high temperatures of dehydration blowdown section of thick bamboo from making the salt caking, auger 8 in the dehydration blowdown section of thick bamboo 5 is equipped with the automatic function of clearing up, 5 left ends of dehydration blowdown section of thick bamboo are equipped with feed inlet 4, are connected with auger pay-off passageway 3 through auger pay-off passageway 2 between feeder hopper 1 and the feed inlet 4, and auger pay-off passageway 3 upper portion is provided with first exhaust passage 36, and first exhaust passage 36 upper portion is provided with first exhaust fan 37, and first exhaust fan upper portion intercommunication exhaust heat dissipation total passageway 38, there is zone of heating 6 in the 5.
The outer side of the first heating layer 6 is fixedly connected with a first heat insulation layer 7, the heating temperature of the first heating layer 6 is 800 ℃, the first heating layer 6 can be uniformly heated at 360 ℃, and the dehydration blowdown cylinder 5 is preheated for 10-15 minutes.
The heating layer I6 is an electric heating induction heating net and a movable layer is arranged between the dehydration blowdown cylinder 5, the dehydration blowdown cylinder 5 can be pulled out for cleaning, and meanwhile, the heating layer is convenient to maintain.
The gear pulling chain of the dehydration and pollution discharge cylinder 5 is in transmission connection with the power mechanism, a gear on the feeding port 4 is in transmission connection with a gear at the output end of the motor through the gear pulling chain of the rolling cylinder, and the rotation driving of the rolling heating 4 can be realized through the motor.
The upper part of the dehydration blowdown cylinder 5 is provided with a second exhaust passage 12, a second exhaust fan 13 is arranged between the second exhaust passage 12 and the exhaust heat dissipation main passage 38, the dehydration blowdown cylinder 5 is provided with a first measuring instrument 9, the first measuring instrument 9 is used for measuring the temperature and time of the dehydration blowdown cylinder 5 and the stirring speed of the auger 8, and the first measuring instrument 9 is controlled by a PLC (programmable logic controller).
The output end of the dehydration blowdown cylinder 5 is provided with a discharge port 10, the upper part of the discharge port 10 is provided with an exhaust port 11, the lower part of the discharge port 10 is connected with a storage hopper 15, the upper part of the storage hopper 15 is connected with a third exhaust passage 29, the third exhaust passage 29 is the same as the exhaust port 11, the upper part of the third exhaust passage 29 is provided with a third exhaust fan 30, the third exhaust fan 30 is communicated with a heat dissipation main passage 38, the upper right part of the storage hopper 15 is provided with a detection sampling port 14, and the bottom of the storage hopper 15 is provided with a storage hopper auger feeding passage.
The PH value regulation and control device comprises a PH value regulation and control barrel 18, blades 21 are arranged in the PH value regulation and control barrel 18, the heating temperature of the blades 21 is controlled to be 300-800 ℃, the rotation time of the PH value regulation and control barrel 18 is set to be 15-30 minutes, the PH value of raw salt is converted into alkaline boiled salt by adjusting the temperature through set time, a PH value regulation and control barrel feeding port 17 is arranged on the left side of the PH value regulation and control barrel 18, the PH value regulation and control barrel feeding port 17 is communicated with a storage hopper auger feeding channel 16 on a storage hopper 15, and a boiled salt discharging port 23 is arranged on the right side.
A second heating layer 19 is arranged on the outer side of the pH value regulating cylinder 18, a second heat insulation layer 20 is arranged on the outer side of the second heating layer 19, and the temperature of the second heating layer 19 is controlled to be 300-800 ℃.
The upper part of the PH value regulating cylinder 18 is provided with a second measuring instrument 22, the second measuring instrument 22 monitors the temperature, the time and the speed of the PH value regulating cylinder, and the second measuring instrument 22 is controlled by a PLC.
The lower part of the cooked salt discharge port 23 is provided with a cooked salt storage hopper 24, the upper part of the cooked salt storage hopper 24 is connected with a first exhaust heat dissipation channel 27, the first exhaust heat dissipation channel 27 is communicated with the cooked salt discharge port 23, the upper part of the first exhaust heat dissipation channel 27 is provided with a first exhaust fan 28, and the first exhaust fan 28 is connected with a total exhaust heat dissipation channel 38.
The lower part of the cooked salt storage hopper 23 is provided with a cooked salt conveying auger I25, the upper part of the cooked salt storage hopper is provided with a cooked salt sampling port 26, and the cooked salt conveying auger I25 is connected with a cooling box 31.
The cooling mechanism comprises a cooling box 31, the upper part of the cooling box 31 is provided with a second exhaust heat dissipation channel 32, the second exhaust heat dissipation channel 32 is provided with a second exhaust fan 33, and the second exhaust fan 33 is connected with a main exhaust heat dissipation channel 38.
The left side of the cooling box 31 is connected with a first cooked salt conveying auger 25, the right side of the cooling box is provided with a second cooked salt conveying auger 34, and the converted alkaline cooked salt is conveyed to a finished product workshop 35 through the second cooked salt conveying auger.
Example two: this embodiment is further described as the previous embodiment: the heating modes of the dehydration and pollution discharge cylinder 5 and the PH value regulation cylinder 18 can be natural gas heating, electromagnetic heating, electric heating wire heating and the like.
Instructions for use: adding raw salt into a feed hopper 1, feeding the raw salt into a dehydration blowdown cylinder 5 through an auger feeding channel 2 and an auger feeding channel 3 at the bottom of the feed hopper 1, preparing the raw salt at a high temperature of no more than 800 ℃, arranging a plurality of blowdown exhaust ports on the dehydration blowdown cylinder 5, enabling the raw salt to generate steam at the high temperature, discharging chlorine gas from a first exhaust channel 36, a second exhaust channel 12 and a third exhaust channel 29 to an exhaust and heat dissipation total channel 38, processing the raw salt at the high temperature to obtain semi-finished salt, conveying the salt into a pH value regulating cylinder 18 through an auger feeding channel 16 at the bottom of an exhaust storage hopper 15, controlling the pH value of the semi-finished salt through a pH value regulating cylinder 18 to change, converting the pH value of the salt into alkaline cooked salt according to the control of temperature and time, controlling the temperature of the pH value regulating cylinder 18 to be 319-799 ℃, frying the salt for 20 minutes, and generating alkaline cooked salt between 8 and 9.30, and the cooling box 31 cools the alkaline cooked salt, and conveys the alkaline cooked salt to a finished product 35 through a packing auger conveying channel for packaging and delivery.
It will be evident to those skilled in the art that the invention is not limited to the details of the foregoing illustrative embodiments, and that the present invention may be embodied in other specific forms without departing from the spirit or essential attributes thereof. The present embodiments are therefore to be considered in all respects as illustrative and not restrictive, the scope of the invention being indicated by the appended claims rather than by the foregoing description, and all changes which come within the meaning and range of equivalency of the claims are therefore intended to be embraced therein. Any reference sign in a claim should not be construed as limiting the claim concerned.
Furthermore, it should be understood that although the present description refers to embodiments, not every embodiment may contain only a single embodiment, and such description is for clarity only, and those skilled in the art should integrate the description, and the embodiments may be combined as appropriate to form other embodiments understood by those skilled in the art.
Claims (10)
1. A full-automatic electromagnetic induction heating and baking purification device for alkaline cooked salt comprises a high-temperature pollution discharge mechanism, a pH value regulation mechanism and a cooling mechanism; the method is characterized in that a variable magnetic field is generated by using variable current, the variable magnetic field can generate current, and the heating mechanical equipment is completed by using the eddy current effect of the magnetic field;
The electromagnetic induction heating pollution discharge mechanism is used for carrying out electromagnetic induction heating stirring, pollution discharge and exhaust on the raw materials;
the PH value regulating mechanism is used for carrying out PH value conversion on the raw material fried by the electric heating pollution discharge mechanism;
and the cooling mechanism is used for cooling the cooked salt converted by the pH value regulating mechanism.
2. The full-automatic roasting equipment process of the calcined alkaline salt as claimed in claim 1, which is characterized in that: the electric heating sewage draining mechanism comprises a dehydration sewage draining cylinder (5), a packing auger (8) is fixedly connected in the dehydration sewage draining cylinder (5), the left end of the dehydration blowdown cylinder (5) is provided with a feed inlet (4), the feed inlet (4) is connected with an auger feeding channel (3), the upper part of the auger feeding channel (3) is provided with a first exhaust channel (36), the upper part of the first exhaust channel (36) is provided with a first exhaust fan (37), the upper part of the first exhaust fan is communicated with an exhaust heat dissipation main channel (38), a second exhaust passage (12) is arranged at the upper part of the dehydration blowdown cylinder (5), a second exhaust fan (13) is arranged on the second exhaust passage (12), an exhaust port (11) is arranged on the right side of the dehydration blowdown cylinder (5), the exhaust port (11) is connected with a third exhaust passage (29), and a third exhaust fan 30 is arranged on the upper portion of the third exhaust passage (29).
3. The full-automatic electromagnetic induction heating purification equipment for baking the alkaline cooked salt according to claim 2, characterized in that: a first measuring instrument (9) is arranged on the dehydration and pollution discharge cylinder (5), and the first measuring instrument (9) is controlled by a PLC.
4. The full-automatic electromagnetic induction heating purification equipment for baking the alkaline cooked salt according to claim 2, characterized in that: an electromagnetic induction heating layer I (6) is arranged outside the dehydration and pollution discharge cylinder (5), the heating temperature of the electromagnetic induction heating layer I (6) is 800 ℃, and the heating layer I (6) can be uniformly heated at 360 degrees.
5. The full-automatic electromagnetic induction heating purification equipment for baking the alkaline cooked salt according to claim 2 or 3, characterized in that: and a movable layer is arranged between the electromagnetic induction heating layer I (6) and the dehydration and pollution discharge cylinder (5), and the dehydration and pollution discharge cylinder (5) can be drawn out.
6. The full-automatic electromagnetic induction heating purification equipment for baking the alkaline cooked salt according to claim 2, characterized in that: the output end of the dehydration blowdown cylinder (5) is provided with a discharge port (10), the lower part of the discharge port (10) is connected with a storage hopper (15), the upper right part of the storage hopper (15) is provided with a detection sampling port (14), and the bottom of the storage hopper (15) is provided with a storage hopper auger feeding channel (16).
7. The full-automatic electromagnetic induction heating purification equipment for baking the alkaline cooked salt according to claim 1, characterized in that: the PH value regulation and control device comprises a PH value regulation and control barrel (18), wherein paddles (21) are arranged in the PH value regulation and control barrel (18), the electromagnetic induction heating temperature of the paddles (21) is controlled between 200-800 ℃ according to the granularity, the rotation time of the PH value regulation and control barrel (18) is set between 9-60 minutes according to the granularity, a PH value regulation and control barrel feed inlet (17) is arranged on the left side of the PH value regulation and control barrel (18), the PH value regulation and control barrel feed inlet (17) is communicated with a storage hopper auger feed channel (16) on a storage hopper (15), and a cooked salt discharge outlet (23) is arranged on the right side of the PH value.
8. The full-automatic electromagnetic induction heating purification equipment for baking the alkaline cooked salt according to claim 7, characterized in that: the outer side of the PH value regulating cylinder (18) is provided with a second electric heating layer (19), the outer part of the second heating layer (1) is provided with a second heat insulation layer (20), and the temperature of the second electromagnetic heating layer (19) is controlled to be 300-800 ℃.
9. The full-automatic electromagnetic induction heating purification equipment for baking the alkaline cooked salt according to claim 7, characterized in that: the lower part of the cooked salt discharge port (23) is provided with a cooked salt storage hopper (24), the upper part of the cooked salt storage hopper (24) is connected with a first exhaust heat dissipation channel (27), the upper part of the first exhaust heat dissipation channel (27) is provided with a first exhaust fan (28), and the first exhaust fan (28) is connected with a main exhaust heat dissipation channel (38).
10. The full-automatic electromagnetic induction heating purification equipment for baking the alkaline cooked salt according to claim 1, characterized in that: the cooling mechanism comprises a cooling box (31), a second exhaust heat dissipation channel (32) is arranged on the upper portion of the cooling box (31), a second exhaust fan (33) is arranged on the second exhaust heat dissipation channel (32), and the second exhaust fan (33) is connected with a main exhaust heat dissipation channel (38).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202010551537.2A CN111838638A (en) | 2020-06-17 | 2020-06-17 | Full-automatic electromagnetic induction heating and baking purification equipment for alkaline cooked salt |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202010551537.2A CN111838638A (en) | 2020-06-17 | 2020-06-17 | Full-automatic electromagnetic induction heating and baking purification equipment for alkaline cooked salt |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN111838638A true CN111838638A (en) | 2020-10-30 |
Family
ID=72987236
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202010551537.2A Pending CN111838638A (en) | 2020-06-17 | 2020-06-17 | Full-automatic electromagnetic induction heating and baking purification equipment for alkaline cooked salt |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN111838638A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112535273A (en) * | 2020-12-03 | 2021-03-23 | 安徽强旺生物工程有限公司 | Industrial preparation method of weakly alkaline Maillard peptide flavored cooked salt |
| CN115462518A (en) * | 2021-06-10 | 2022-12-13 | 王锦江 | Nutrient salt and preparation method thereof |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1009736A (en) * | 1963-06-13 | 1965-11-10 | George Garnham Turner | Method for purifying salt |
| CN106579298A (en) * | 2016-12-06 | 2017-04-26 | 金成燮 | Alkaline baking salt and preparation method thereof |
| CN106690247A (en) * | 2016-12-22 | 2017-05-24 | 潍坊千源机械制造有限公司 | Salt baking process and production equipment thereof |
| CN207803388U (en) * | 2017-09-22 | 2018-09-04 | 云南省能源研究院有限公司 | A kind of salt curing range |
| CN108497445A (en) * | 2018-04-02 | 2018-09-07 | 浙江临安三和园竹盐食品有限公司 | The processing method of basic salt |
| CN109043471A (en) * | 2018-10-10 | 2018-12-21 | 山东鲁晶制盐科技有限公司 | A kind of roasting salt manufacture craft improving baking efficiency |
| CN209825126U (en) * | 2019-03-07 | 2019-12-24 | 王锦江 | Automatic alkalescent cooked salt conversion machine |
-
2020
- 2020-06-17 CN CN202010551537.2A patent/CN111838638A/en active Pending
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1009736A (en) * | 1963-06-13 | 1965-11-10 | George Garnham Turner | Method for purifying salt |
| CN106579298A (en) * | 2016-12-06 | 2017-04-26 | 金成燮 | Alkaline baking salt and preparation method thereof |
| CN106690247A (en) * | 2016-12-22 | 2017-05-24 | 潍坊千源机械制造有限公司 | Salt baking process and production equipment thereof |
| CN207803388U (en) * | 2017-09-22 | 2018-09-04 | 云南省能源研究院有限公司 | A kind of salt curing range |
| CN108497445A (en) * | 2018-04-02 | 2018-09-07 | 浙江临安三和园竹盐食品有限公司 | The processing method of basic salt |
| CN109043471A (en) * | 2018-10-10 | 2018-12-21 | 山东鲁晶制盐科技有限公司 | A kind of roasting salt manufacture craft improving baking efficiency |
| CN209825126U (en) * | 2019-03-07 | 2019-12-24 | 王锦江 | Automatic alkalescent cooked salt conversion machine |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112535273A (en) * | 2020-12-03 | 2021-03-23 | 安徽强旺生物工程有限公司 | Industrial preparation method of weakly alkaline Maillard peptide flavored cooked salt |
| CN112535273B (en) * | 2020-12-03 | 2024-02-13 | 安徽强旺生物工程有限公司 | Industrial preparation method of alkalescent Maillard peptide flavored cooked salt |
| CN115462518A (en) * | 2021-06-10 | 2022-12-13 | 王锦江 | Nutrient salt and preparation method thereof |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102578235B (en) | Infant formula milk rice flour and preparation method thereof | |
| CN204848801U (en) | Airtight vacuum melting production facility of animal oil | |
| CN111838638A (en) | Full-automatic electromagnetic induction heating and baking purification equipment for alkaline cooked salt | |
| CN103976036A (en) | Method for preparing kelp bean curd | |
| CN104664222A (en) | Five-cereal health nutrition powder with effect of decreasing blood pressure and blood lipid and manufacturing method thereof | |
| CN103610217A (en) | Technology for automatically peeling and processing walnut kernels | |
| CN209825126U (en) | Automatic alkalescent cooked salt conversion machine | |
| CN102987390A (en) | Canned unpolished rice gruel and making method thereof | |
| CN101147546B (en) | Bean curd filament gravy boiled seasoning automatic production equipment and production method thereof | |
| CN104605131B (en) | A kind of sea-buckthorn jelly work and preparation method thereof | |
| CN106260994A (en) | A kind of diatery supplement preventing, stop or nursing one's health diarrhoea | |
| CN106234965A (en) | A kind of Herba Saussureae Involueratae fruitcake and processing method thereof | |
| CN110506903A (en) | Krill steaming plant and its digesting technoloy | |
| CN209234911U (en) | A kind of soybean dietary fiber production line | |
| CN105559122A (en) | Mechanical apparatus for producing sweet potato cake | |
| CN113150862B (en) | Sea buckthorn oil extraction system and method thereof | |
| CN212971573U (en) | High-efficient thick liquid equipment of cooking of soyfood | |
| CN106465928A (en) | A kind of manufacture method of Jerusalem artichoke characteristic soy sauce | |
| CN106262078A (en) | A kind of Fructus Ananadis comosi honey cake and processing method thereof | |
| CN106261522A (en) | A kind of Fructus Lycopersici esculenti cake and processing method thereof | |
| CN106261725A (en) | A kind of Folium Eriobotryae cake and processing method thereof | |
| CN106106623A (en) | A kind of cake and preparation method thereof | |
| CN106261729A (en) | A kind of yellow millet cake and processing method thereof | |
| CN106235076A (en) | A kind of fresh ginger brown sugar warming up morrhua cake | |
| CN104738648A (en) | Health nutrition powder of cowpea, Chinese yam and longan and preparation method of health nutrition powder |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| WD01 | Invention patent application deemed withdrawn after publication | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20201030 |