WO2015099210A1 - Vacuum kiln for producing salt and system using same - Google Patents

Vacuum kiln for producing salt and system using same Download PDF

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Publication number
WO2015099210A1
WO2015099210A1 PCT/KR2013/012056 KR2013012056W WO2015099210A1 WO 2015099210 A1 WO2015099210 A1 WO 2015099210A1 KR 2013012056 W KR2013012056 W KR 2013012056W WO 2015099210 A1 WO2015099210 A1 WO 2015099210A1
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WO
WIPO (PCT)
Prior art keywords
salt
water
vacuum kiln
heating
function
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PCT/KR2013/012056
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French (fr)
Korean (ko)
Inventor
문지은
문민영
Original Assignee
미가식품영농조합법인
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Priority to PCT/KR2013/012056 priority Critical patent/WO2015099210A1/en
Publication of WO2015099210A1 publication Critical patent/WO2015099210A1/en

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    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27—FURNACES; KILNS; OVENS; RETORTS
    • F27B—FURNACES, KILNS, OVENS, OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
    • F27B5/00—Muffle furnaces; Retort furnaces; Other furnaces in which the charge is held completely isolated
    • F27B5/06—Details, accessories, or equipment peculiar to furnaces of these types
    • 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
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27—FURNACES; KILNS; OVENS; RETORTS
    • F27B—FURNACES, KILNS, OVENS, OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
    • F27B5/00—Muffle furnaces; Retort furnaces; Other furnaces in which the charge is held completely isolated
    • F27B5/04—Muffle furnaces; Retort furnaces; Other furnaces in which the charge is held completely isolated adapted for treating the charge in vacuum or special atmosphere

Definitions

  • the present invention relates to a vacuum kiln for producing salt and a system using the same, more specifically, to produce a salt at a constant temperature to maintain a constant amount of minerals included in the salt to improve the taste of the salt, and to a degree of taste
  • the present invention relates to a vacuum kiln and a system using the same, which produce salt capable of maintaining a uniform production rate.
  • Salt is an important cation in human extracellular fluid, which regulates osmotic pressure of body fluids, is involved in acid-base equilibrium, and in addition to neurostimulatory transporters, helps to produce gastric acid to form digestive fluids, participates in enzyme activity, and produces the purest salty taste. Therefore, it is used as a seasoning for flavoring foods and increasing shelf life.
  • Typical decontamination methods include the refining and processing of rock salts, the mechanical decontamination method in which the seawater is directly evaporated and concentrated by evaporation, the sun salt desalination method by evaporating and evaporating salt by solar heat, ion exchange method, and electricity to seawater.
  • the electric resistance using the electric resistance to concentrate the seawater, etc.
  • There is an electric decontamination method which is mostly produced by the sun salt decontamination method in Korea.
  • seawater was evaporated to raise salts by filtering saltwater-produced tidal flat soils or soils with high salt content, and then boiling in a kiln to produce salts by pre-pollution. Have been.
  • An object of the present invention for solving these problems is to maintain a constant content of minerals contained in suicide at the time of suicide formation to improve the taste of suicide, and to produce a salt that can ensure the productivity of suicide It is to provide a kiln and a system using the same.
  • Another object of the present invention is to provide a vacuum kiln for producing salt and a system using the same, which can continuously produce suicide by introducing an automated system and minimize the waste of manpower consumed in suicide production.
  • Still another object of the present invention is to provide a vacuum kiln and a system using the same, which collects water vapor containing minerals generated in the production of magnetic salts and produces mineral water in which water vapor is liquefied by temperature changes.
  • the vacuum kiln for producing salt according to the present invention includes an inlet through which water is introduced, a storage unit in which the function is stored, a heating unit surrounding the outer circumferential surface of the storage unit and heating the storage unit, generated by heating. It includes a water discharge portion for discharging the salt and water from the fryer storage unit and the lead portion for maintaining the storage unit at a lower than atmospheric pressure, characterized in that the function to reach the boiling point at 20 °C to 100 °C.
  • the heating unit is characterized in that formed in at least two multi-layer structure so that heat generated in the heating unit is not lost to the outside.
  • the heating unit is characterized in that for heating the storage unit with a heating medium of any one of steam, electricity or water.
  • the heating unit is characterized in that for heating the storage to 20 °C to 100 °C.
  • the heating unit may include a circulation supply unit and a circulation discharge unit for circulating the heating medium to maintain the internal temperature of the storage unit at 20 ° C to 100 ° C.
  • the heating unit is provided with a screw-shaped wing to form a movement path of the heating medium.
  • the weight of the function characterized in that it further comprises a weighing unit for checking the water level of the function.
  • the material inlet that contains ingredients containing seaweed, plum, aloe, scallop, green tea, mushroom, ginseng, seaweed, garlic, guava, reed, protein, carbohydrate, fat, vitamin, organic acid and inorganic salt It characterized in that it further comprises.
  • the water is characterized in that it further comprises a mineral water tank for generating mineral water by collecting the steam generated while boiling.
  • the salt producing system maintains a state lower than the air pressure and the incoming function reaches a boiling point at 20 °C to 100 °C to heat the function, and then the salt and water produced by heating It is characterized in that it comprises a vacuum kiln for discharging, a centrifuge for centrifuging the salt and the water discharged from the vacuum kiln, a dryer for receiving and drying the salt separated from the centrifuge.
  • a salt tank for storing the dried salt in the dryer, a salt tank for storing the function generated while drying the salt, and the function to provide an impurity separator so that the stored function is mixed with the seawater introduced from the outside It is done.
  • it characterized in that it comprises a condenser for discharging the heating medium to the outside of the vacuum kiln in order to maintain the temperature inside the vacuum kiln at 20 °C to 100 °C.
  • the vacuum kiln is a material containing a seaweed, plum, aloe, cucumber, green tea, mushrooms, ginseng, seaweed, garlic, guava, edible material, protein, carbohydrates, fats, vitamins, organic acids and inorganic salts It is characterized in that it further comprises the inflow.
  • it characterized in that it further comprises a mineral water tank for generating mineral water by collecting the steam generated by boiling the water from the vacuum kiln.
  • the present invention maintains a constant content of minerals included in suicide at the time of generating suicide, thereby improving the taste of suicide and ensuring productivity of suicide.
  • the present invention can be continuously produced by introducing an automated system, there is an effect that can minimize the waste of manpower consumed to produce the salt.
  • the present invention collects the water vapor containing the minerals generated during the production of the magnetic salt, there is an effect that can produce a separate profit by producing a mineral water liquefied by the temperature change.
  • FIG. 1 is a block diagram showing a salt printing system including a vacuum kiln according to an embodiment of the present invention
  • FIG. 2 is a flow chart showing a method of producing salt according to an embodiment of the present invention.
  • FIG. 1 is a block diagram showing a salt printing system including a vacuum kiln according to an embodiment of the present invention.
  • the salt production system 100 including a vacuum kiln includes an impurity separator 15, an impurity tank 15a, a vacuum kiln 30, a centrifuge 40, a dryer 50, and a salt tank 55. ), The water tank 60, the condenser 65, the cooling tank 70, the boiler (75).
  • the impurity separator 15 receives seawater through a seawater supply pipe 10 formed in an external or seawater tank (not shown) through the seawater supply pipe 10.
  • the impurity separator 15 separates impurities from the seawater while washing the seawater with the water provided from the water tank 60.
  • the impurities separated in the impurity separator 15 are discharged to the impurity tank 15a, and the function from which the impurities are separated is introduced into the vacuum kiln 30 through the plurality of inlets 20a to 20e formed in the vacuum kiln 30. .
  • the vacuum kiln 30 boils the water introduced through the inlets 20a to 20e in a state lower than atmospheric pressure to make suicide. Because of this, the boiling point of the water in the vacuum kiln 30 is 20 °C to 100 °C.
  • the vacuum kiln 30 is largely composed of the storage unit 30a and the heating unit 33.
  • the storage unit 30a is a space in which the function introduced through the inlets 20a to 20e is stored, and the heating unit 33 is formed to surround the outer circumferential surface of the storage unit 30a, and the heating unit 33 is the storage unit. It is a space in which a heating medium for heating 30a exists.
  • the heating medium may be steam, water, or electricity.
  • an electric coil is formed in the heating unit 33.
  • the heating portion 33 is formed with a blade (not shown) in the form of a screw can generate a moving path of the heating medium.
  • the water stored in the storage unit 30a is heated by the heating medium of the heating unit 33, and the salt is produced by boiling the water at 20 ° C to 100 ° C by the heated storage unit 30a.
  • the salt is moved to the lower portion of the storage unit 30a by the impeller 34 and discharged to the centrifuge 40 through the water discharge unit 35 formed at the lower end of the vacuum kiln 30.
  • the heating unit 33 heats the storage unit 30a at 20 ° C. to 100 ° C., and includes a temperature sensor inside the storage unit 30 a to store the internal temperature of the storage unit 30 a or the storage unit 30 a.
  • the temperature inside the storage unit 30a is continuously sensed to provide a control unit (not shown) of the system 100 so that the temperature of the stored function does not exceed 100 ° C.
  • the outer wall forming the heating part 33 is formed in a multi-layered structure as shown by reference numerals 33a and 33b, so that heat of the heating part 33 is not lost to the outside.
  • productivity is improved when the temperature of boiling water is high, but a problem occurs that the taste is lowered, and when the temperature is low, the problem is that productivity is reduced instead of the taste is improved.
  • the boiling point of the water is about 120 ° C., when the salt is produced in this state, the amount of minerals contained in the salt is low, and the taste is lost.
  • the vacuum kiln 30 by using the vacuum kiln 30 to maintain the storage unit 30a lower than the atmospheric pressure to lower the boiling temperature of the water to about 100 °C to increase the amount of minerals contained in the salt. For this reason, the taste of the produced magnetic salt can be improved and productivity can also be ensured.
  • the temperature of the storage unit 30a constant, the amount of minerals contained in the salt can be kept constant, and the taste of the magnetic salt is uniform.
  • a lead portion 31 is formed on one side of the upper portion of the vacuum kiln 30 to maintain the inside of the vacuum kiln 30 at a lower than atmospheric pressure.
  • the controller controls the condenser 65 to discharge the heating medium from the heating unit 33.
  • the heating unit 33 is formed with a circulation discharge portion 37 for discharging the heating medium to the condenser 65, the circulation discharge portion 37 is the support frame formed on the other side of the upper portion of the vacuum kiln 30 The 32 is fixed to the vacuum kiln 30.
  • the boiler 75 heats the heating medium having a temperature such that the internal temperature of the storage unit 30a can be maintained at 20 °C to 100 °C It gives to the part 33.
  • the heating medium discharged to the condenser 65 is provided to the cooling tank 70, the heating medium cooled by the cooling tank 70 is provided to the boiler 75 is formed in the lower portion of the vacuum kiln 30
  • the circulation inlet 36 is provided to the heating unit 33. As such, the heating medium continuously performs a circulation operation, thereby increasing the energy efficiency.
  • the vacuum kiln 30 is formed through the support frame 32, the tube is connected to the mineral water tank 80 that can collect the water vapor generated by the boiling of the water. Since the boiling function stored in the storage unit 30a is a function containing minerals, the water vapor generated when the function is boiling contains fine minerals. As such, water vapor containing minerals is converted into mineral water containing minerals while being liquefied by external temperature change and stored in the mineral water tank 80. When mineral water is stored in the mineral water tank 80 in a predetermined amount or more, it may be provided as a separate packaging process for commercializing it. Although not shown, the vacuum kiln 30 may be provided with a condenser in order to provide the water generated by boiling of the water in the storage unit 30a to the mineral water tank 80.
  • the impeller 34 is formed inside the storage unit 30a and rotates 360 degrees with respect to the axis to sink salts heavier than the water into the lower portion of the storage unit 30a and discharge them to the outside.
  • the impeller 34 includes a mixing section 34a and a wing section 34b.
  • the mixing portion 34a sinks the salt heavier than the water into the lower portion of the storage portion 30a
  • the wing portion 34b separates the salt attached to the inner wall surface of the storage portion 30a from the wall surface.
  • the impeller 34 may be adjusted in the height of the storage unit 30a under the control of the controller, and may move to the lower portion of the storage unit 30a until the salt attached to the upper wall surface of the storage unit 30a.
  • the salt moved to the bottom of the storage unit 30a and the function stored in the storage unit 30a are discharged to the water discharge unit 35 formed at the bottom of the vacuum kiln 30, and is provided to the centrifuge 40.
  • the vacuum kiln 30 may include a water level sensor (not shown) for measuring the water level of the function stored in the vacuum kiln 30.
  • the water level measuring sensor may generally be a sensor capable of detecting water, and a weight sensor for measuring the weight of the vacuum kiln 30 to calculate the water level may be used.
  • the control unit checks the water level of the function stored in the storage unit 30a by sensing information provided from the water level measurement sensor, and opens the inlets 20a to 20e to allow the function to flow into the storage unit 30a when the water level is lower than the threshold. Adjust the constant level of the function.
  • the centrifuge 40 is centrifuged to dehydrate the salt and salt discharged from the vacuum kiln 30. Due to this, the separated water is discharged to the water tank 60, and the salt is discharged to the screw conveyor 45 to move to the dryer 50 along the screw conveyor 45.
  • the dryer 50 dries the salt centrifuged in the centrifuge 40.
  • the dried salt means salt, and the salt is discharged to the salt tank 55 is moved to a separate packaging device (not shown) and then packed.
  • the water generated while drying the salt is discharged to the water tank (60).
  • the water tank 60 stores the water discharged from the centrifuge 40 and the dryer 50, and provides the impurity separator 15 for separating impurities from seawater when a predetermined amount or more is stored.
  • the vacuum kiln for producing salt and the system using the same as in the present invention have little manpower consumption by automating all the processes for the production of salt, especially the salt, and can continuously generate the salt, thereby ensuring productivity.
  • the salt since the water is boiled in a state lower than the air pressure lower than the boiling point of the general function, the salt is contained a lot of minerals to improve the taste of the salt.
  • the vacuum kiln 30 further includes a material inlet (not shown), and includes seaweed, plum, aloe, ogapi, green tea, mushroom, ginseng, algae, garlic, guava, and reed through the material inlet.
  • a material inlet includes seaweed, plum, aloe, ogapi, green tea, mushroom, ginseng, algae, garlic, guava, and reed through the material inlet.
  • a functional salt is mixed by mixing the water introduced through the impurity separator 15 and the material introduced through the material inlet. Can be.
  • FIG. 2 is a flowchart illustrating a method of producing salt according to an embodiment of the present invention.
  • step S11 seawater is introduced into the impurity separator 15 through the seawater supply pipe 10, and in step S13, the impurity separator 15 removes impurities contained in the seawater.
  • the impurities separated from the seawater are discharged to the impurity tank 15a, and the function from which the impurities are removed in step S15 is introduced into the vacuum kiln 30.
  • the function is moved from the impurity separator 15 through the seawater inlet pipe, and is introduced into the storage unit 30a of the vacuum kiln 30 through a plurality of inlets 20a to 20e formed in the seawater inlet pipe 20. .
  • the heating unit 33 heats the storage unit 30a in which the function is stored.
  • the heating medium warmed from the boiler 75 is introduced into the heating unit 33 through the circulation inlet 36, and the heating medium is located in the heating unit 33 to heat the storage unit 30a.
  • the internal temperature of the storage unit (30a) is preferably maintained at a maximum of 100 °C, if the temperature is more than 100 °C, the condenser 65 through the circulation medium discharged to the heating medium present in the heating unit 33 To be discharged.
  • the heating medium discharged to the condenser (65) is cooled in the cooling tank (70) and provided to the boiler (75), and the boiler (75) is heated to a temperature such that the temperature of the storage unit (30a) can be maintained at 100 ° C.
  • the heated medium is again introduced into the heating unit 33 through the circulation inlet unit 36.
  • the impeller 34 formed in the storage unit 30a is driven in operation S19 to discharge the salt generated by heating the storage unit 30a to the water discharge unit 35 of the vacuum kiln 30.
  • the impeller 34 is formed by mixing the function evenly, the mixing portion 34a for sinking the heavier salt than the function and the wing portion 34b for scraping off the salt attached to the wall of the storage portion (30a).
  • the impeller 34 may control the height of the inside of the storage unit 30a under the control of the controller to scrape all of the salt attached to the upper wall of the storage unit 30a.
  • step S21 the water discharge unit 35 discharges the salt and water stored in the storage unit 30a to the centrifuge 40, and in step S23, the centrifuge 40 dehydrates the salt and the water by centrifugation. And the centrifuge 40 discharges the dehydrated salt to the screw conveyor 45, the discharge is discharged to the water-containing tank (60).
  • step S25 the dryer 50 is introduced with salt through the screw conveyor 45 to dry the salt.
  • step S27 the dryer 50 discharges the water discharged from the salt into the water tank 60 while drying the salt
  • step S29 the dryer 50 discharges the dried grains of salt into the salt tank 55.
  • the water tank (60) is provided to the impurity separator (15) when the amount of the water flowing from the centrifuge (40) and the dryer (50) is greater than the threshold value to wash the seawater introduced through the seawater supply pipe (10) It is reused to remove impurities.
  • the water vapor is connected to the mineral water tank 80 connected to the vacuum kiln 30.
  • Water vapor stored in the mineral water tank 80 is changed to water, that is, mineral water containing minerals due to a change in temperature, and may be provided in a separate packaging process if a predetermined amount is stored.

Abstract

The present invention relates to a vacuum kiln for producing salt and a system using the same. The vacuum kiln comprises: an inlet through which salt water is introduced; a storage part having the salt water stored therein; a heating part enclosing the outer peripheral surface of the storage part and heating the storage part; a salt water discharge part for discharging salt generated by heating and the salt water from the storage part; and a lead part for maintaining the storage part at a pressure lower than the atmospheric pressure, wherein the salt water reaches a boiling point in the range of 20°C to 100°C.

Description

소금을 생산하는 진공가마 및 이를 이용한 시스템Salt-producing vacuum kiln and system using the same
본 발명은 소금을 생산하는 진공가마 및 이를 이용한 시스템에 관한 것으로서, 보다 구체적으로 일정한 온도에서 자염을 생산하여 자염에 포함되는 미네랄의 양이 일정하게 유지되도록 하여 자염의 맛을 향상시키고, 맛의 정도와 생산량을 균일하게 유지할 수 있는 소금을 생산하는 진공가마 및 이를 이용한 시스템에 관한 것이다.The present invention relates to a vacuum kiln for producing salt and a system using the same, more specifically, to produce a salt at a constant temperature to maintain a constant amount of minerals included in the salt to improve the taste of the salt, and to a degree of taste The present invention relates to a vacuum kiln and a system using the same, which produce salt capable of maintaining a uniform production rate.
소금은 사람의 세포 외액의 중요한 양이온으로 체액의 삼투압을 조절하고 산염기 평형에 관여하며 신경자극 전달물질 뿐만 아니라, 위산의 생성을 도와 소화액을 구성하고, 효소활동에 관여하며, 가장 순수한 짠맛을 내기 때문에 식품의 맛을 내고 저장성을 높이기 위한 조미료로 많이 이용된다. Salt is an important cation in human extracellular fluid, which regulates osmotic pressure of body fluids, is involved in acid-base equilibrium, and in addition to neurostimulatory transporters, helps to produce gastric acid to form digestive fluids, participates in enzyme activity, and produces the purest salty taste. Therefore, it is used as a seasoning for flavoring foods and increasing shelf life.
일반적인 제염방법으로는 암염을 정제 가공하는 방법, 해수를 직접 증발관에 넣어 증발 농축하는 전오염식 기계제염법, 태양열에 의해서 증발 농축하여 염을 석출하는 천일제염법, 이온교환방법, 해수에 전기를 통할 때 전기저항을 이용하여 발열시켜 해수를 농축하는 전기제염법 등이 있으며, 국내에서는 대부분 천일제염법에 의해서 생산되고 있다. Typical decontamination methods include the refining and processing of rock salts, the mechanical decontamination method in which the seawater is directly evaporated and concentrated by evaporation, the sun salt desalination method by evaporating and evaporating salt by solar heat, ion exchange method, and electricity to seawater. When using the electric resistance using the electric resistance to concentrate the seawater, etc. There is an electric decontamination method, which is mostly produced by the sun salt decontamination method in Korea.
1907년경 천일제염법이 도입되기 이전에는 해수가 증발하여 염분이 농축된 갯벌함토나 염분함량이 높은 흙을 해수로 걸러 염도를 높인 후, 가마에서 끓여 염을 석출하는 전오염법에 의한 자염을 생산해왔다.Before the introduction of the Sunil Decontamination Act in 1907, seawater was evaporated to raise salts by filtering saltwater-produced tidal flat soils or soils with high salt content, and then boiling in a kiln to produce salts by pre-pollution. Have been.
그러나 전통의 자염생산 방법은 천일제염법에 의해 연료비 및 인건비가 높아 현재는 거의 행하고 있지 않고, 2001년에 충남 태안에서 과거 소금제조방식인 자염생산방법을 그대로 재현한 바 있다.However, the traditional method of producing self- printing is rarely performed at present due to high fuel cost and labor cost by Cheonil decontamination method, and in 2001, Taean, Chungnam, reproduced the method of producing self- printing, which is a salt production method.
일반적으로 자염 생성 시에 함수를 증발시키기 위한 온도가 너무 높으면 소금에 포함되는 미네랄의 함량이 줄어들어 맛이 저하되는 문제점이 생기고, 맛의 향상을 위해 온도를 낮춰 자염을 생산할 경우에는 생산성이 저하되는 문제점이 발생한다.In general, when the temperature for evaporating water is too high to produce salt, the content of minerals contained in the salt is reduced, resulting in a decrease in taste. In the case of production of salt by lowering the temperature to improve taste, productivity is reduced. This happens.
이에, 자염 생성 시에 맛과 생산성을 확보하고, 인력 낭비를 최소화할 수 있는 기술의 도입이 시급한 실정이다.Therefore, it is urgent to introduce a technology capable of securing taste and productivity and minimizing human waste at the time of generating self salt.
이러한 종래의 문제점들을 해결하기 위한 본 발명의 목적은 자염 생성 시에 자염에 포함되는 미네랄의 함량을 일정하게 유지하도록 하여 자염의 맛을 향상시키고, 자염의 생산성을 확보할 수 있는 소금을 생산하는 진공가마 및 이를 이용한 시스템을 제공하는 것이다.An object of the present invention for solving these problems is to maintain a constant content of minerals contained in suicide at the time of suicide formation to improve the taste of suicide, and to produce a salt that can ensure the productivity of suicide It is to provide a kiln and a system using the same.
본 발명의 다른 목적은 자동화 시스템을 도입하여 연속적으로 자염을 생산할 수 있고, 자염 생산에 소비되는 인력의 낭비를 최소화할 수 있는 소금을 생산하는 진공가마 및 이를 이용한 시스템을 제공하는 것이다. Another object of the present invention is to provide a vacuum kiln for producing salt and a system using the same, which can continuously produce suicide by introducing an automated system and minimize the waste of manpower consumed in suicide production.
본 발명의 또 다른 목적은 자염 생산 시에 발생되는 미네랄이 포함된 수증기를 취합하고, 수증기가 온도변화에 의해 액체화된 미네랄워터를 생산하는 진공가마 및 이를 이용한 시스템을 제공하는 것이다. Still another object of the present invention is to provide a vacuum kiln and a system using the same, which collects water vapor containing minerals generated in the production of magnetic salts and produces mineral water in which water vapor is liquefied by temperature changes.
이러한 목적들을 달성하기 위하여 본 발명에 따른 소금을 생산하는 진공가마는 함수가 유입되는 유입구, 상기 함수가 저장되는 저장부, 상기 저장부의 외주면을 감싸고 상기 저장부를 가열하는 가열부, 가열에 의해 생성된 소금 및 함수를 사기 저장부로부터 배출시키는 함수배출부 및 상기 저장부를 기압보다 낮은 상태로 유지하는 리드부를 포함하고, 상기 함수가 20℃ 내지 100℃에서 끓는점에 도달하도록 하는 것을 특징으로 한다.In order to achieve the above objects, the vacuum kiln for producing salt according to the present invention includes an inlet through which water is introduced, a storage unit in which the function is stored, a heating unit surrounding the outer circumferential surface of the storage unit and heating the storage unit, generated by heating. It includes a water discharge portion for discharging the salt and water from the fryer storage unit and the lead portion for maintaining the storage unit at a lower than atmospheric pressure, characterized in that the function to reach the boiling point at 20 ℃ to 100 ℃.
또한, 상기 가열부는 상기 가열부에서 발생되는 열이 외부로 손실되지 않도록 적어도 두 개의 다층구조로 형성된 것을 특징으로 한다.In addition, the heating unit is characterized in that formed in at least two multi-layer structure so that heat generated in the heating unit is not lost to the outside.
또한, 상기 가열부는 증기, 전기 또는 물 중 어느 하나인 가열매질로 상기 저장부를 가열하는 것을 특징으로 한다.In addition, the heating unit is characterized in that for heating the storage unit with a heating medium of any one of steam, electricity or water.
또한, 상기 가열부는 상기 저장부를 20℃ 내지 100℃로 가열하는 것을 특징으로 한다.In addition, the heating unit is characterized in that for heating the storage to 20 ℃ to 100 ℃.
또한, 상기 가열부는 상기 가열매질을 순환시켜 상기 저장부의 내부온도를 20℃ 내지 100℃로 유지하기 위한 순환공급부와 순환배출부를 포함하는 것을 특징으로 한다.The heating unit may include a circulation supply unit and a circulation discharge unit for circulating the heating medium to maintain the internal temperature of the storage unit at 20 ° C to 100 ° C.
또한, 상기 가열부는 스크류형태의 날개를 구비하여 상기 가열매질의 이동로를 형성하는 것을 특징으로 한다.In addition, the heating unit is provided with a screw-shaped wing to form a movement path of the heating medium.
또한, 상기 함수의 수위를 감지하는 센서부를 포함하는 것을 특징으로 한다.In addition, it characterized in that it comprises a sensor for detecting the water level of the function.
또한, 상기 함수의 무게로 상기 함수의 수위를 확인하는 무게측정부를 더 포함하는 것을 특징으로 한다.In addition, the weight of the function characterized in that it further comprises a weighing unit for checking the water level of the function.
또한, 상기 저장부 내부에서 회전하여 상기 소금을 가라앉히는 임펠러를 포함하는 것을 특징으로 한다.In addition, it characterized in that it comprises an impeller to rotate in the reservoir to sink the salt.
또한, 상기 저장부에 저장된 함수의 온도를 측정하는 온도센서를 포함하는 것을 특징으로 한다.In addition, it characterized in that it comprises a temperature sensor for measuring the temperature of the function stored in the storage.
또한, 함초, 매실, 알로에, 오가피, 녹차, 버섯, 인삼, 해조류, 마늘, 구아바, 갈대를 포함하는 식용소재, 단백질, 탄수화물, 지방, 비타민, 유기산 및 무기염류를 포함하는 소재가 유입되는 소재유입구를 더 포함하는 것을 특징으로 한다.In addition, the material inlet that contains ingredients containing seaweed, plum, aloe, scallop, green tea, mushroom, ginseng, seaweed, garlic, guava, reed, protein, carbohydrate, fat, vitamin, organic acid and inorganic salt It characterized in that it further comprises.
또한, 상기 함수가 끓으면서 발생하는 수증기를 취합하여 미네랄워터를 생성하는 미네랄워터탱크를 더 포함하는 것을 특징으로 한다. In addition, the water is characterized in that it further comprises a mineral water tank for generating mineral water by collecting the steam generated while boiling.
아울러, 본 발명에 따른 소금을 생산하는 시스템은 기압보다 낮은 상태를 유지하고 유입된 함수가 20℃ 내지 100℃에 끓는점에 도달하도록 하여 상기 함수를 가열한 후, 가열에 의해 생성된 소금 및 함수를 배출하는 진공가마, 상기 진공가마로부터 배출된 소금과 함수를 원심분리하는 원심분리기, 상기 원심분리기로부터 분리된 소금을 제공받아 건조하는 건조기를 포함하는 것을 특징으로 한다.In addition, the salt producing system according to the present invention maintains a state lower than the air pressure and the incoming function reaches a boiling point at 20 ℃ to 100 ℃ to heat the function, and then the salt and water produced by heating It is characterized in that it comprises a vacuum kiln for discharging, a centrifuge for centrifuging the salt and the water discharged from the vacuum kiln, a dryer for receiving and drying the salt separated from the centrifuge.
또한, 상기 건조기에서 건조가 완료된 소금을 저장하는 소금탱크, 상기 소금을 건조하면서 생성된 함수를 저장하고, 저장된 함수가 외부로부터 유입된 해수와 혼합되도록 불순물분리기로 제공하는 함수탱크를 포함하는 것을 특징으로 한다.In addition, a salt tank for storing the dried salt in the dryer, a salt tank for storing the function generated while drying the salt, and the function to provide an impurity separator so that the stored function is mixed with the seawater introduced from the outside It is done.
또한, 상기 원심분리기로부터 분리된 소금을 상기 건조기로 이동시키는 스크류형태의 컨베이어를 포함하는 것을 특징으로 한다.In addition, it characterized in that it comprises a screw-type conveyor for moving the salt separated from the centrifuge to the dryer.
또한, 증기, 전기 또는 물 중 어느 하나인 가열매질을 상기 진공가마로 제공하는 보일러를 포함하는 것을 특징으로 한다.In addition, it characterized in that it comprises a boiler for providing a heating medium of any one of steam, electricity or water to the vacuum kiln.
또한, 상기 진공가마 내부의 온도를 20℃ 내지 100℃로 유지하기 위하여 상기 가열매질을 상기 진공가마의 외부로 배출하는 응축기를 포함하는 것을 특징으로 한다.In addition, it characterized in that it comprises a condenser for discharging the heating medium to the outside of the vacuum kiln in order to maintain the temperature inside the vacuum kiln at 20 ℃ to 100 ℃.
또한, 상기 진공가마는 함초, 매실, 알로에, 오가피, 녹차, 버섯, 인삼, 해조류, 마늘, 구아바, 갈대를 포함하는 식용소재, 단백질, 탄수화물, 지방, 비타민, 유기산 및 무기염류를 포함하는 소재가 유입되는 것을 더 포함하는 것을 특징으로 한다. In addition, the vacuum kiln is a material containing a seaweed, plum, aloe, cucumber, green tea, mushrooms, ginseng, seaweed, garlic, guava, edible material, protein, carbohydrates, fats, vitamins, organic acids and inorganic salts It is characterized in that it further comprises the inflow.
또한, 상기 함수가 끓으면서 발생하는 수증기를 상기 진공가마로부터 취합하여 미네랄워터를 생성하는 미네랄워터탱크를 더 포함하는 것을 특징으로 한다.In addition, it characterized in that it further comprises a mineral water tank for generating mineral water by collecting the steam generated by boiling the water from the vacuum kiln.
이와 같이, 본 발명은 자염 생성 시에 자염에 포함되는 미네랄의 함량을 일정하게 유지하도록 하여 자염의 맛을 향상시키고, 자염의 생산성을 확보할 수 있는 효과가 있다. As described above, the present invention maintains a constant content of minerals included in suicide at the time of generating suicide, thereby improving the taste of suicide and ensuring productivity of suicide.
또한, 본 발명은 자동화 시스템을 도입하여 연속적으로 자염을 생산할 수 있고, 자염 생산에 소비되는 인력 낭비를 최소화할 수 있는 효과가 있다. In addition, the present invention can be continuously produced by introducing an automated system, there is an effect that can minimize the waste of manpower consumed to produce the salt.
또한, 본 발명은 자염 생산 시에 발생되는 미네랄이 포함된 수증기를 취합하고, 수증기가 온도변화에 의해 액체화된 미네랄워터를 생산하여 별도의 수익을 창출할 수 있는 효과가 있다.In addition, the present invention collects the water vapor containing the minerals generated during the production of the magnetic salt, there is an effect that can produce a separate profit by producing a mineral water liquefied by the temperature change.
도 1은 본 발명의 실시예에 따른 진공가마를 포함한 자염생산 시스템을 나타내는 구성도1 is a block diagram showing a salt printing system including a vacuum kiln according to an embodiment of the present invention
도 2는 본 발명의 실시예에 따른 소금을 생산하는 방법을 나타낸 순서도2 is a flow chart showing a method of producing salt according to an embodiment of the present invention.
이하, 첨부된 도면들을 참조하여 본 발명의 실시예들을 보다 상세하게 설명하고자 한다. 다만, 실시예들을 설명함에 있어서 본 발명이 속하는 기술 분야에 잘 알려져 있고, 본 발명과 직접적으로 관련이 없는 기술 내용에 대해서는 가급적 설명을 생략한다. 이는 불필요한 설명을 생략함으로써 본 발명의 핵심을 흐리지 않고 더욱 명확히 전달하기 위함이다. Hereinafter, exemplary embodiments of the present invention will be described in detail with reference to the accompanying drawings. However, in describing the embodiments, descriptions of technologies that are well known in the art to which the present invention pertains and are not directly related to the present invention are omitted. This is to more clearly communicate without obscure the core of the present invention by omitting unnecessary description.
도 1은 본 발명의 실시예에 따른 진공가마를 포함한 자염생산 시스템을 나타내는 구성도이다. 1 is a block diagram showing a salt printing system including a vacuum kiln according to an embodiment of the present invention.
도 1을 참조하면, 진공가마를 포함한 자염생산 시스템(100)은 불순물분리기(15), 불순물탱크(15a), 진공가마(30), 원심분리기(40), 건조기(50), 소금탱크(55), 함수탱크(60), 응축기(65), 냉각탱크(70), 보일러(75)를 포함한다.Referring to FIG. 1, the salt production system 100 including a vacuum kiln includes an impurity separator 15, an impurity tank 15a, a vacuum kiln 30, a centrifuge 40, a dryer 50, and a salt tank 55. ), The water tank 60, the condenser 65, the cooling tank 70, the boiler (75).
불순물분리기(15)는 해수공급관(10)을 통해 외부 또는 해수탱크(미도시)에 형성된 해수공급관(10)을 통해 해수를 공급받는다. 불순물분리기(15)는 함수탱크(60)로부터 제공된 함수로 해수를 세척하면서 해수로부터 불순물을 분리한다. 불순물분리기(15)에서 분리된 불순물은 불순물탱크(15a)로 배출되고, 불순물이 분리된 함수는 진공가마(30)에 형성된 복수의 유입구(20a 내지 20e)를 통해 진공가마(30)로 유입된다. The impurity separator 15 receives seawater through a seawater supply pipe 10 formed in an external or seawater tank (not shown) through the seawater supply pipe 10. The impurity separator 15 separates impurities from the seawater while washing the seawater with the water provided from the water tank 60. The impurities separated in the impurity separator 15 are discharged to the impurity tank 15a, and the function from which the impurities are separated is introduced into the vacuum kiln 30 through the plurality of inlets 20a to 20e formed in the vacuum kiln 30. .
진공가마(30)는 유입구(20a 내지 20e)를 통해 유입된 함수를 기압보다 낮은 상태에서 끓여 자염을 만든다. 이로 인해, 진공가마(30)에서 함수의 끓는점은 20℃ 내지 100℃가 된다. The vacuum kiln 30 boils the water introduced through the inlets 20a to 20e in a state lower than atmospheric pressure to make suicide. Because of this, the boiling point of the water in the vacuum kiln 30 is 20 ℃ to 100 ℃.
보다 구체적으로, 진공가마(30)는 크게 저장부(30a)와 가열부(33)로 구성된다. 저장부(30a)는 유입구(20a 내지 20e)를 통해 유입된 함수가 저장되는 공간이고, 가열부(33)는 저장부(30a)의 외주면을 감싸도록 형성된다, 가열부(33)는 저장부(30a)를 가열하기 위한 가열매질이 존재하는 공간이다. 이때, 가열매질은 증기, 물 또는 전기일 수 있으며, 가열매질이 전기일 경우, 가열부(33)에는 전기코일이 형성된다. 아울러, 가열부(33)에는 스크류형태의 날개(미도시)가 형성되어 가열매질의 이동로를 생성할 수 있다. More specifically, the vacuum kiln 30 is largely composed of the storage unit 30a and the heating unit 33. The storage unit 30a is a space in which the function introduced through the inlets 20a to 20e is stored, and the heating unit 33 is formed to surround the outer circumferential surface of the storage unit 30a, and the heating unit 33 is the storage unit. It is a space in which a heating medium for heating 30a exists. In this case, the heating medium may be steam, water, or electricity. When the heating medium is electricity, an electric coil is formed in the heating unit 33. In addition, the heating portion 33 is formed with a blade (not shown) in the form of a screw can generate a moving path of the heating medium.
저장부(30a)에 저장된 함수는 가열부(33)의 가열매질에 의해 가열되고, 가열된 저장부(30a)에 의해 20℃ 내지 100℃에서 함수가 끓으면서 소금이 생산된다. 이때, 소금은 임펠러(34)에 의해 저장부(30a)의 하부로 이동되어 진공가마(30)의 하단에 형성된 함수배출부(35)를 통해 원심분리기(40)로 배출된다. The water stored in the storage unit 30a is heated by the heating medium of the heating unit 33, and the salt is produced by boiling the water at 20 ° C to 100 ° C by the heated storage unit 30a. At this time, the salt is moved to the lower portion of the storage unit 30a by the impeller 34 and discharged to the centrifuge 40 through the water discharge unit 35 formed at the lower end of the vacuum kiln 30.
이때, 가열부(33)는 20℃ 내지 100℃로 저장부(30a)를 가열하고, 저장부(30a)의 내부에는 온도센서를 구비하여, 저장부(30a)의 내부 온도 또는 저장부(30a)에 저장된 함수의 온도가 100℃가 넘지 않도록 저장부(30a) 내부의 온도를 지속적으로 센싱하여 시스템(100)의 제어부(미도시)로 제공한다. 아울러, 가열부(33)를 형성하는 외부벽은 참조번호 33a, 33b와 같이 다층구조로 형성되어, 가열부(33)의 열이 외부로 손실되지 않도록 한다. In this case, the heating unit 33 heats the storage unit 30a at 20 ° C. to 100 ° C., and includes a temperature sensor inside the storage unit 30 a to store the internal temperature of the storage unit 30 a or the storage unit 30 a. The temperature inside the storage unit 30a is continuously sensed to provide a control unit (not shown) of the system 100 so that the temperature of the stored function does not exceed 100 ° C. In addition, the outer wall forming the heating part 33 is formed in a multi-layered structure as shown by reference numerals 33a and 33b, so that heat of the heating part 33 is not lost to the outside.
자염의 경우 함수를 끓이는 온도가 높으면 생산성은 향상되지만, 맛이 저하되는 문제점이 발생하고, 온도가 낮으면 맛은 향상되는 대신에 생산성이 저하되는 문제점이 발생한다. 일반적으로 함수가 끓는 온도는 120℃ 정도가 되기 때문에 이 상태로 자염을 생성하면 소금에 포함되는 미네랄의 양이 적어 맛이 없어지게 된다. In the case of suicide, productivity is improved when the temperature of boiling water is high, but a problem occurs that the taste is lowered, and when the temperature is low, the problem is that productivity is reduced instead of the taste is improved. In general, since the boiling point of the water is about 120 ° C., when the salt is produced in this state, the amount of minerals contained in the salt is low, and the taste is lost.
따라서, 본 발명에서는 진공가마(30)를 사용하여 저장부(30a)를 기압보다 낮은 상태로 유지함으로써 함수의 끓는 온도를 100℃ 정도로 낮춰주어 소금에 포함되는 미네랄의 양을 증가시킨다. 이로 인해, 생성된 자염의 맛을 향상시킬 수 있고, 생산성도 보장할 수 있다. 또한, 저장부(30a)의 온도를 일정하게 유지함으로 인해, 소금에 포함되는 미네랄의 양을 일정하게 유지할 수 있어, 자염의 맛이 균일한 효과가 있다. 이를 위해, 진공가마(30)의 상부의 한쪽에는 진공가마(30)의 내부를 기압보다 낮은 상태로 유지하기 위한 리드부(31)가 형성된다. Therefore, in the present invention, by using the vacuum kiln 30 to maintain the storage unit 30a lower than the atmospheric pressure to lower the boiling temperature of the water to about 100 ℃ to increase the amount of minerals contained in the salt. For this reason, the taste of the produced magnetic salt can be improved and productivity can also be ensured. In addition, by keeping the temperature of the storage unit 30a constant, the amount of minerals contained in the salt can be kept constant, and the taste of the magnetic salt is uniform. To this end, a lead portion 31 is formed on one side of the upper portion of the vacuum kiln 30 to maintain the inside of the vacuum kiln 30 at a lower than atmospheric pressure.
아울러, 저장부(30a)의 온도가 100℃가 넘게 되면 제어부는 응축기(65)를 제어하여 가열부(33)에서 가열매질을 배출하도록 한다. 이를 위해, 가열부(33)에는 가열매질을 응축기(65)로 배출하기 위한 순환배출부(37)가 형성되고, 순환배출부(37)는 진공가마(30) 상부의 다른 한쪽에 형성된 지지프레임(32)에 의해 진공가마(30)에 고정된다. In addition, when the temperature of the storage unit 30a exceeds 100 ° C., the controller controls the condenser 65 to discharge the heating medium from the heating unit 33. To this end, the heating unit 33 is formed with a circulation discharge portion 37 for discharging the heating medium to the condenser 65, the circulation discharge portion 37 is the support frame formed on the other side of the upper portion of the vacuum kiln 30 The 32 is fixed to the vacuum kiln 30.
응축기(65)에 의해 가열매질이 가열부(33)로부터 배출되면 보일러(75)는 저장부(30a)의 내부 온도를 20℃ 내지 100℃로 유지시킬 수 있는 정도의 온도를 지닌 가열매질을 가열부(33)로 제공한다. When the heating medium is discharged from the heating unit 33 by the condenser 65, the boiler 75 heats the heating medium having a temperature such that the internal temperature of the storage unit 30a can be maintained at 20 ℃ to 100 ℃ It gives to the part 33.
또한, 응축기(65)로 배출된 가열매질은 냉각탱크(70)로 제공되고, 냉각탱크(70)에 의해 냉각된 가열매질은 다시 보일러(75)로 제공되어 진공가마(30)의 하부에 형성된 순환유입부(36)를 통해 가열부(33)로 제공된다. 이와 같이, 가열매질이 지속적으로 순환동작을 수행함으로써, 에너지 효율을 높일 수 있는 효과가 있다. In addition, the heating medium discharged to the condenser 65 is provided to the cooling tank 70, the heating medium cooled by the cooling tank 70 is provided to the boiler 75 is formed in the lower portion of the vacuum kiln 30 The circulation inlet 36 is provided to the heating unit 33. As such, the heating medium continuously performs a circulation operation, thereby increasing the energy efficiency.
아울러, 진공가마(30)는 지지프레임(32)을 관통하여 관이 형성되고, 상기 관은 함수의 끓음으로 인해 발생되는 수증기를 취합할 수 있는 미네랄워터탱크(80)와 연결된다. 저장부(30a)에 저장되어 끓는 함수는 미네랄을 포함하고 있는 함수이기 때문에 함수가 끓으면서 발생되는 수증기에는 미세한 미네랄이 포함되게 된다. 이와 같이, 미네랄이 포함된 수증기가 외부의 온도변화에 의해 액체화되면서 미네랄이 함유된 미네랄워터로 변화되어 미네랄워터탱크(80)에 저장된다. 미네랄워터탱크(80)에 일정량 이상 미네랄워터가 저장되면 이를 상품화할 수 있는 별도의 포장공정으로 이를 제공할 수 있다. 도시되진 않았으나, 저장부(30a)에서 함수의 끓음으로 인해 발생되는 수증기를 미네랄워터탱크(80)로 제공하기 위하여 진공가마(30)는 응축기를 구비할 수 있다. In addition, the vacuum kiln 30 is formed through the support frame 32, the tube is connected to the mineral water tank 80 that can collect the water vapor generated by the boiling of the water. Since the boiling function stored in the storage unit 30a is a function containing minerals, the water vapor generated when the function is boiling contains fine minerals. As such, water vapor containing minerals is converted into mineral water containing minerals while being liquefied by external temperature change and stored in the mineral water tank 80. When mineral water is stored in the mineral water tank 80 in a predetermined amount or more, it may be provided as a separate packaging process for commercializing it. Although not shown, the vacuum kiln 30 may be provided with a condenser in order to provide the water generated by boiling of the water in the storage unit 30a to the mineral water tank 80.
임펠러(34)는 저장부(30a)의 내부에 형성되고, 축을 기준으로 360도를 회전하여 함수보다 무거운 소금을 저장부(30a)의 하부로 가라앉혀 외부로 배출시킨다. 이를 위해, 임펠러(34)는 혼합부(34a)와 날개부(34b)를 포함하여 구성된다. 혼합부(34a)는 함수보다 무거운 소금을 저장부(30a)의 하부로 가라앉히고, 날개부(34b)는 저장부(30a)의 내부벽면에 붙은 소금을 벽면으로부터 이탈시킨다. 이때, 임펠러(34)는 제어부의 제어에 의해 저장부(30a) 내부에서 높이가 조절되어, 저장부(30a)의 상부 벽면에 붙어있는 소금까지 저장부(30a)의 하부로 이동시킬 수 있다.The impeller 34 is formed inside the storage unit 30a and rotates 360 degrees with respect to the axis to sink salts heavier than the water into the lower portion of the storage unit 30a and discharge them to the outside. To this end, the impeller 34 includes a mixing section 34a and a wing section 34b. The mixing portion 34a sinks the salt heavier than the water into the lower portion of the storage portion 30a, and the wing portion 34b separates the salt attached to the inner wall surface of the storage portion 30a from the wall surface. At this time, the impeller 34 may be adjusted in the height of the storage unit 30a under the control of the controller, and may move to the lower portion of the storage unit 30a until the salt attached to the upper wall surface of the storage unit 30a.
저장부(30a)의 하부로 이동된 소금과 저장부(30a)에 저장된 함수는 진공가마(30)의 하부에 형성된 함수배출부(35)로 배출되어, 원심분리기(40)로 제공된다. The salt moved to the bottom of the storage unit 30a and the function stored in the storage unit 30a are discharged to the water discharge unit 35 formed at the bottom of the vacuum kiln 30, and is provided to the centrifuge 40.
진공가마(30)는 진공가마(30) 내부에 저장된 함수의 수위를 측정하기 위한 수위측정센서(미도시)를 구비할 수 있다. 수위측정센서는 일반적으로 물을 감지할 수 있는 센서일 수 있고, 진공가마(30)의 무게를 측정해 수위를 계산할 수 있도록 하는 무게센서 등이 이용될 수 있다. 제어부는 수위측정센서로부터 제공된 센싱정보에 의해 저장부(30a)에 저장된 함수의 수위를 확인하여, 수위가 임계치 이하이면 유입구(20a 내지 20e)를 열어 저장부(30a)에 함수가 유입되도록 함으로써, 함수의 일정한 수위를 조절한다. The vacuum kiln 30 may include a water level sensor (not shown) for measuring the water level of the function stored in the vacuum kiln 30. The water level measuring sensor may generally be a sensor capable of detecting water, and a weight sensor for measuring the weight of the vacuum kiln 30 to calculate the water level may be used. The control unit checks the water level of the function stored in the storage unit 30a by sensing information provided from the water level measurement sensor, and opens the inlets 20a to 20e to allow the function to flow into the storage unit 30a when the water level is lower than the threshold. Adjust the constant level of the function.
원심분리기(40)는 진공가마(30)에서 배출된 함수와 소금을 원심분리하여 탈수한다. 이로 인해, 분리된 함수는 함수탱크(60)로 배출하고, 소금은 스크류컨베이어(45)를 따라 건조기(50)로 이동하도록 스크류컨베이어(45)로 배출한다.The centrifuge 40 is centrifuged to dehydrate the salt and salt discharged from the vacuum kiln 30. Due to this, the separated water is discharged to the water tank 60, and the salt is discharged to the screw conveyor 45 to move to the dryer 50 along the screw conveyor 45.
건조기(50)는 원심분리기(40)에서 원심분리된 소금을 건조시킨다. 건조가 완료된 소금은 자염을 의미하며, 자염은 소금탱크(55)로 배출되어 별도의 포장장치(미도시)로 이동된 후 포장된다. 아울러, 소금을 건조하면서 생성된 함수는 함수탱크(60)로 배출한다.The dryer 50 dries the salt centrifuged in the centrifuge 40. The dried salt means salt, and the salt is discharged to the salt tank 55 is moved to a separate packaging device (not shown) and then packed. In addition, the water generated while drying the salt is discharged to the water tank (60).
함수탱크(60)는 원심분리기(40)와 건조기(50)로부터 배출된 함수를 저장하고 있다가, 일정량 이상이 저장되면 해수의 불순물을 분리하는 불순물분리기(15)로 제공한다.The water tank 60 stores the water discharged from the centrifuge 40 and the dryer 50, and provides the impurity separator 15 for separating impurities from seawater when a predetermined amount or more is stored.
이와 같이, 본 발명과 같이 소금을 생산하는 진공가마 및 이를 이용한 시스템은 소금 중에서도 특히, 자염 생산을 위한 모든 공정을 자동화하여 인력소모가 거의 없고, 연속적으로 자염을 생성할 수 있어 생산성이 보장된다. 아울러, 기압보다 낮은 상태에서 함수를 끓이기 때문에 일반적인 함수의 끓는점보다 낮아 자염에 미네랄이 많이 포함되어 자염의 맛이 향상된다.As such, the vacuum kiln for producing salt and the system using the same as in the present invention have little manpower consumption by automating all the processes for the production of salt, especially the salt, and can continuously generate the salt, thereby ensuring productivity. In addition, since the water is boiled in a state lower than the air pressure lower than the boiling point of the general function, the salt is contained a lot of minerals to improve the taste of the salt.
아울러, 도시되지 않았으나, 진공가마(30)는 소재유입구(미도시)를 더 구비하여, 소재유입구를 통해 함초, 매실, 알로에, 오가피, 녹차, 버섯, 인삼, 해조류, 마늘, 구아바, 갈대를 포함하는 식용소재, 단백질, 탄수화물, 지방, 비타민, 유기산 및 무기염류를 포함하는 소재가 유입되면, 불순물분리기(15)를 통해 유입된 함수와 소재유입구를 통해 유입된 소재를 혼합하여 기능성 소금을 생성할 수 있다. In addition, although not shown, the vacuum kiln 30 further includes a material inlet (not shown), and includes seaweed, plum, aloe, ogapi, green tea, mushroom, ginseng, algae, garlic, guava, and reed through the material inlet. When a material containing an edible material, protein, carbohydrates, fat, vitamins, organic acids and inorganic salts is introduced, a functional salt is mixed by mixing the water introduced through the impurity separator 15 and the material introduced through the material inlet. Can be.
도 2는 본 발명의 실시예에 따른 소금을 생산하는 방법을 나타낸 순서도이다.2 is a flowchart illustrating a method of producing salt according to an embodiment of the present invention.
도 1 및 도 2를 참조하면, S11단계에서 해수가 해수공급관(10)을 통해 불순물분리기(15)로 유입되고, S13단계에서 불순물분리기(15)는 해수에 포함된 불순물을 제거한다. 해수에서 분리된 불순물은 불순물탱크(15a)로 배출되고, S15단계에서 불순물이 제거된 함수는 진공가마(30)에 유입된다. 이때, 함수는 해수유입관을 통해 불순물분리기(15)로부터 이동되고, 해수유입관(20)에 형성된 다수의 유입구(20a 내지 20e)를 통해 진공가마(30)의 저장부(30a)로 유입된다.1 and 2, in step S11, seawater is introduced into the impurity separator 15 through the seawater supply pipe 10, and in step S13, the impurity separator 15 removes impurities contained in the seawater. The impurities separated from the seawater are discharged to the impurity tank 15a, and the function from which the impurities are removed in step S15 is introduced into the vacuum kiln 30. At this time, the function is moved from the impurity separator 15 through the seawater inlet pipe, and is introduced into the storage unit 30a of the vacuum kiln 30 through a plurality of inlets 20a to 20e formed in the seawater inlet pipe 20. .
S17단계에서 가열부(33)는 함수가 저장된 저장부(30a)를 가열한다. 이를 위해, 보일러(75)에서 데워진 가열매질이 순환유입부(36)를 통해 가열부(33)로 유입되고, 가열매질이 가열부(33)에 위치하면서 저장부(30a)를 가열한다. 이때, 저장부(30a)의 내부 온도는 최대 100℃를 유지하는 것이 바람직하며, 100℃ 이상이 될 경우, 가열부(33)에 존재하는 가열매질을 순환배출부(37)를 통해 응축기(65)로 배출한다. 응축기(65)로 배출된 가열매질은 냉각탱크(70)에서 냉각되어 보일러(75)로 제공되며, 보일러(75)에서 저장부(30a)의 온도를 100℃로 유지할 수 있을 정도의 온도로 가열된 가열매질이 다시 순환유입부(36)를 통해 가열부(33)로 유입된다.In operation S17, the heating unit 33 heats the storage unit 30a in which the function is stored. To this end, the heating medium warmed from the boiler 75 is introduced into the heating unit 33 through the circulation inlet 36, and the heating medium is located in the heating unit 33 to heat the storage unit 30a. At this time, the internal temperature of the storage unit (30a) is preferably maintained at a maximum of 100 ℃, if the temperature is more than 100 ℃, the condenser 65 through the circulation medium discharged to the heating medium present in the heating unit 33 To be discharged. The heating medium discharged to the condenser (65) is cooled in the cooling tank (70) and provided to the boiler (75), and the boiler (75) is heated to a temperature such that the temperature of the storage unit (30a) can be maintained at 100 ° C. The heated medium is again introduced into the heating unit 33 through the circulation inlet unit 36.
이후, 저장부(30a)가 가열됨에 의해 생성된 소금을 진공가마(30)의 함수배출부(35)로 배출하기 위해 S19단계에서 저장부(30a)에 형성된 임펠러(34)가 구동된다. 임펠러(34)는 함수를 골고루 섞이게 하고, 함수보다 무거운 소금을 가라앉히기 위한 혼합부(34a)와 저장부(30a)의 벽면에 붙은 소금을 긁어내기 위한 날개부(34b)로 형성된다. 임펠러(34)는 제어부의 제어에 의해 저장부(30a) 내부에서 높이 조절을 수행하여 저장부(30a)의 상부 벽면에 붙은 소금도 전부 긁어낼 수 있다. Thereafter, the impeller 34 formed in the storage unit 30a is driven in operation S19 to discharge the salt generated by heating the storage unit 30a to the water discharge unit 35 of the vacuum kiln 30. The impeller 34 is formed by mixing the function evenly, the mixing portion 34a for sinking the heavier salt than the function and the wing portion 34b for scraping off the salt attached to the wall of the storage portion (30a). The impeller 34 may control the height of the inside of the storage unit 30a under the control of the controller to scrape all of the salt attached to the upper wall of the storage unit 30a.
S21단계에서 함수배출부(35)는 저장부(30a)에 저장된 소금과 함수를 원심분리기(40)로 배출하고, S23단계에서 원심분리기(40)는 소금과 함수를 원심분리하여 탈수한다. 그리고 원심분리기(40)는 함수가 탈수된 소금을 스크류컨베이어(45)로 배출하고, 함수는 함수탱크(60)로 배출한다.In step S21, the water discharge unit 35 discharges the salt and water stored in the storage unit 30a to the centrifuge 40, and in step S23, the centrifuge 40 dehydrates the salt and the water by centrifugation. And the centrifuge 40 discharges the dehydrated salt to the screw conveyor 45, the discharge is discharged to the water-containing tank (60).
S25단계에서 스크류컨베이어(45)를 통해 소금이 유입된 건조기(50)는 소금을 건조시킨다. In step S25, the dryer 50 is introduced with salt through the screw conveyor 45 to dry the salt.
S27단계에서 건조기(50)는 소금을 건조시키면서 소금에서 배출된 함수를 함수탱크(60)로 배출하고, S29단계에서 건조기(50)는 건조된 소금알갱이를 소금탱크(55)로 배출한다. 아울러, 함수탱크(60)는 원심분리기(40)와 건조기(50)로부터 유입된 함수의 양이 임계치 이상이 되면 불순물분리기(15)로 제공하여 해수공급관(10)을 통해 유입되는 해수를 세척하여 불순물을 제거하는 용도로 재사용된다. In step S27, the dryer 50 discharges the water discharged from the salt into the water tank 60 while drying the salt, and in step S29, the dryer 50 discharges the dried grains of salt into the salt tank 55. In addition, the water tank (60) is provided to the impurity separator (15) when the amount of the water flowing from the centrifuge (40) and the dryer (50) is greater than the threshold value to wash the seawater introduced through the seawater supply pipe (10) It is reused to remove impurities.
아울러, 도시되지 않았으나, S17단계에서 진공가마(30)가 가열됨으로 인해 저장부(30a)에 저장된 함수가 끓기 시작하면서 수증기가 발생되면, 수증기는 진공가마(30)에 연결된 미네랄워터탱크(80)에 저장된다. 미네랄워터탱크(80)에 저장된 수증기는 온도의 변화로 인해 물 즉, 미네랄이 함유된 미네랄워터로 변화된 후, 일정량이 저장되면 별도의 포장공정으로 제공될 수 있다. In addition, although not shown, if water vapor is generated while the function stored in the storage unit 30a starts to boil due to the heating of the vacuum kiln 30 in step S17, the water vapor is connected to the mineral water tank 80 connected to the vacuum kiln 30. Are stored in. Water vapor stored in the mineral water tank 80 is changed to water, that is, mineral water containing minerals due to a change in temperature, and may be provided in a separate packaging process if a predetermined amount is stored.
지금까지 실시예를 통하여 본 발명에 따른 소금을 생산하는 진공가마 및 이를 이용한 시스템에 대하여 설명하였다. 아울러, 본 발명의 실시예에서는 자염을 생산하는 진공가마 및 이를 이용한 시스템에 대하여 설명하고 있으나, 반드시 이에 한정되는 것은 아니며, 천일염 등을 포함하는 소금 생산 시에도 본 진공가마 및 이를 이용한 시스템을 적용할 수 있음을 명확히 하는 바이다. So far, a description has been given of a vacuum kiln and a system using the same for producing salt according to the present invention. In addition, the embodiment of the present invention has been described with respect to a vacuum kiln for producing a salt and a system using the same, but is not necessarily limited to this, the vacuum kiln and the system using the same can also be applied to the production of salt, including sun salt. I can make it clear.
본 명세서와 도면에서는 본 발명의 바람직한 실시예에 대하여 개시하였으며, 비록 특정 용어들이 사용되었으나, 이는 단지 본 발명의 기술 내용을 쉽게 설명하고 발명의 이해를 돕기 위한 일반적인 의미에서 사용된 것일 뿐, 본 발명의 범위를 한정하고자 하는 것은 아니다. 상기에 기재된 실시예 외에도 본 발명의 기술적 사상에 바탕을 둔 다른 변형예들이 실시 가능하다는 것은 본 발명이 속하는 기술 분야에서 통상의 지식을 가진 자에게 자명한 것이다.In the present specification and drawings, preferred embodiments of the present invention have been disclosed, and although specific terms are used, these are merely used in a general sense to easily explain the technical contents of the present invention and to help understanding of the present invention. It is not intended to limit the scope of. It will be apparent to those skilled in the art that other modifications based on the technical idea of the present invention can be carried out in addition to the embodiments described above.

Claims (19)

  1. 함수가 유입되는 유입구;Inlet through which water is introduced;
    상기 함수가 저장되는 저장부;A storage unit in which the function is stored;
    상기 저장부의 외주면을 감싸고 상기 저장부를 가열하는 가열부;A heating part surrounding an outer circumferential surface of the storage part and heating the storage part;
    가열에 의해 생성된 소금 및 함수를 상기 저장부로부터 배출시키는 함수배출부; 및A water discharge unit for discharging salt and water generated by heating from the storage unit; And
    상기 저장부를 기압보다 낮은 상태로 유지하는 리드부를 포함하고,It includes a lead portion for holding the storage unit lower than the air pressure,
    상기 함수가 20℃ 내지 100℃에서 끓는점에 도달하도록 하는 것을 특징으로 하는 소금을 생산하는 진공가마.Vacuum kiln for producing salt, characterized in that the function to reach the boiling point at 20 ℃ to 100 ℃.
  2. 제1항에 있어서, The method of claim 1,
    상기 가열부는The heating unit
    상기 가열부에서 발생되는 열이 외부로 손실되지 않도록 적어도 두 개의 다층구조로 형성된 것을 특징으로 하는 소금을 생산하는 진공가마.Vacuum kiln for producing salt, characterized in that formed in at least two multi-layer structure so that heat generated in the heating unit is not lost to the outside.
  3. 제1항에 있어서,The method of claim 1,
    상기 가열부는The heating unit
    증기, 전기 또는 물 중 어느 하나인 가열매질로 상기 저장부를 가열하는 것을 특징으로 하는 소금을 생산하는 진공가마.Vacuum kiln for producing salt, characterized in that for heating the reservoir with a heating medium of any one of steam, electricity or water.
  4. 제3항에 있어서,The method of claim 3,
    상기 가열부는The heating unit
    상기 저장부를 20℃ 내지 100℃로 가열하는 것을 특징으로 하는 소금을 생산하는 진공가마. Vacuum kiln for producing salt, characterized in that for heating the storage to 20 ℃ to 100 ℃.
  5. 제3항에 있어서,The method of claim 3,
    상기 가열부는The heating unit
    상기 가열매질을 순환시켜 상기 저장부의 내부온도를 20℃ 내지 100℃로 유지하기 위한 순환공급부와 순환배출부;A circulation supply part and a circulation discharge part for circulating the heating medium to maintain the internal temperature of the storage part at 20 ° C. to 100 ° C .;
    를 포함하는 것을 특징으로 하는 소금을 생산하는 진공가마.Vacuum kiln to produce salt, characterized in that it comprises a.
  6. 제4항에 있어서,The method of claim 4, wherein
    상기 가열부는The heating unit
    스크류형태의 날개를 구비하여 상기 가열매질의 이동로를 형성하는 것을 특징으로 하는 소금을 생산하는 진공가마. Vacuum kiln for producing salt, characterized in that the blade-shaped wing is provided to form a moving path of the heating medium.
  7. 제1항에 있어서,The method of claim 1,
    상기 함수의 수위를 감지하는 센서부;Sensor unit for detecting the water level of the function;
    를 포함하는 것을 특징으로 하는 소금을 생산하는 진공가마. Vacuum kiln to produce salt, characterized in that it comprises a.
  8. 제1항에 있어서,The method of claim 1,
    상기 함수의 무게로 상기 함수의 수위를 확인하는 무게측정부;A weight measuring unit for checking the water level of the function by the weight of the function;
    를 더 포함하는 것을 특징으로 하는 소금을 생산하는 진공가마. Vacuum kiln for producing salt, characterized in that it further comprises.
  9. 제1항에 있어서, The method of claim 1,
    상기 저장부 내부에서 회전하여 상기 소금을 가라앉히는 임펠러;An impeller rotating inside the reservoir to sink the salt;
    를 포함하는 것을 특징으로 하는 소금을 생산하는 진공가마. Vacuum kiln to produce salt, characterized in that it comprises a.
  10. 제1항에 있어서,The method of claim 1,
    상기 저장부에 저장된 함수의 온도를 측정하는 온도센서;A temperature sensor measuring a temperature of a function stored in the storage unit;
    를 포함하는 것을 특징으로 하는 소금을 생산하는 진공가마.Vacuum kiln to produce salt, characterized in that it comprises a.
  11. 제1항에 있어서,The method of claim 1,
    함초, 매실, 알로에, 오가피, 녹차, 버섯, 인삼, 해조류, 마늘, 구아바, 갈대를 포함하는 식용소재, 단백질, 탄수화물, 지방, 비타민, 유기산 및 무기염류를 포함하는 소재가 유입되는 소재유입구;Material inlet into which ingredients including seaweed, plum, aloe, agapi, green tea, mushroom, ginseng, algae, garlic, guava, reed, protein, carbohydrate, fat, vitamin, organic acid and inorganic salts are introduced;
    를 더 포함하는 것을 특징으로 하는 소금을 생산하는 진공가마.Vacuum kiln for producing salt, characterized in that it further comprises.
  12. 제1항에 있어서,The method of claim 1,
    상기 함수가 끓으면서 발생하는 수증기를 취합하여 미네랄워터를 생성하는 미네랄워터탱크;A mineral water tank which collects water vapor generated while boiling the water to generate mineral water;
    를 더 포함하는 것을 특징으로 하는 소금을 생산하는 진공가마.Vacuum kiln for producing salt, characterized in that it further comprises.
  13. 기압보다 낮은 상태를 유지하고 유입된 함수가 20℃ 내지 100℃에서 끓는점에 도달하도록 하여 상기 함수를 가열한 후, 가열에 의해 생성된 소금 및 함수를 배출하는 진공가마;A vacuum kiln for maintaining the state below the atmospheric pressure and allowing the introduced water to reach the boiling point at 20 ° C. to 100 ° C. to heat the water function, and then discharging the salt and the water generated by heating;
    상기 진공가마로부터 배출된 소금과 함수를 원심분리하는 원심분리기;A centrifuge for centrifuging the salt and the water discharged from the vacuum kiln;
    상기 원심분리기로부터 분리된 소금을 제공받아 건조하는 건조기;A dryer provided with the salt separated from the centrifuge and dried;
    를 포함하는 것을 특징으로 하는 소금을 생산하는 시스템.Salt production system comprising a.
  14. 제13항에 있어서,The method of claim 13,
    상기 건조기에서 건조가 완료된 소금을 저장하는 소금탱크;A salt tank for storing the dried salt in the dryer;
    상기 소금을 건조하면서 생성된 함수를 저장하고, 저장된 함수가 외부로부터 유입된 해수와 혼합되도록 불순물분리기로 제공하는 함수탱크;A water tank for storing the function generated while drying the salt and providing the stored function to the impurity separator so that the stored function is mixed with seawater introduced from the outside;
    를 포함하는 것을 특징으로 하는 소금을 생산하는 시스템.Salt production system comprising a.
  15. 제13항에 있어서,The method of claim 13,
    상기 원심분리기로부터 분리된 소금을 상기 건조기로 이동시키는 스크류형태의 컨베이어;A screw conveyor for moving the salt separated from the centrifuge to the dryer;
    를 포함하는 것을 특징으로 하는 소금을 생산하는 시스템. Salt production system comprising a.
  16. 제13항에 있어서,The method of claim 13,
    증기, 전기 또는 물 중 어느 하나인 가열매질을 상기 진공가마로 제공하는 보일러;Boiler for providing a heating medium of any one of steam, electricity or water to the vacuum kiln;
    를 포함하는 것을 특징으로 하는 소금을 생산하는 시스템.Salt production system comprising a.
  17. 제16항에 있어서, The method of claim 16,
    상기 진공가마 내부의 온도를 20℃ 내지 100℃로 유지하기 위하여 상기 가열매질을 상기 진공가마의 외부로 배출하는 응축기;A condenser for discharging the heating medium to the outside of the vacuum kiln to maintain the temperature in the vacuum kiln at 20 ° C to 100 ° C;
    를 포함하는 것을 특징으로 하는 소금을 생산하는 시스템.Salt production system comprising a.
  18. 제13항에 있어서,The method of claim 13,
    상기 진공가마는The vacuum kiln
    함초, 매실, 알로에, 오가피, 녹차, 버섯, 인삼, 해조류, 마늘, 구아바, 갈대를 포함하는 식용소재, 단백질, 탄수화물, 지방, 비타민, 유기산 및 무기염류를 포함하는 소재가 유입되는 것을 더 포함하는 것을 특징으로 하는 소금을 생산하는 시스템.Further comprising the influx of ingredients including seaweeds, plums, aloes, cucumbers, green tea, mushrooms, ginseng, algae, garlic, guavas, reeds, proteins, carbohydrates, fats, vitamins, organic acids and inorganic salts Salt production system, characterized in that.
  19. 제13항에 있어서,The method of claim 13,
    상기 함수가 끓으면서 발생하는 수증기를 상기 진공가마로부터 취합하여 미네랄워터를 생성하는 미네랄워터탱크;A mineral water tank which collects water vapor generated while boiling the water from the vacuum kiln to generate mineral water;
    를 더 포함하는 것을 특징으로 하는 소금을 생산하는 시스템.Salt production system characterized in that it further comprises.
PCT/KR2013/012056 2013-12-24 2013-12-24 Vacuum kiln for producing salt and system using same WO2015099210A1 (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112654259A (en) * 2018-07-23 2021-04-13 杭州尤美特科技有限公司 Functional plant salt and preparation method and application thereof

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100490922B1 (en) * 2002-11-12 2005-05-19 한국해양연구원 Deep Ocean Water
EP1543733A1 (en) * 2003-12-17 2005-06-22 La Perla S.r.l. Manufacture of liquid edible salt
KR20060082338A (en) * 2005-01-12 2006-07-18 김경관 Heating furnace for salt manufacture
KR20110136156A (en) * 2010-06-14 2011-12-21 박정길 Salt vaporization refining apparatus
KR101099128B1 (en) * 2010-06-04 2011-12-26 목포대학교산학협력단 manufacture apparatus of healthful powder salt

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100490922B1 (en) * 2002-11-12 2005-05-19 한국해양연구원 Deep Ocean Water
EP1543733A1 (en) * 2003-12-17 2005-06-22 La Perla S.r.l. Manufacture of liquid edible salt
KR20060082338A (en) * 2005-01-12 2006-07-18 김경관 Heating furnace for salt manufacture
KR101099128B1 (en) * 2010-06-04 2011-12-26 목포대학교산학협력단 manufacture apparatus of healthful powder salt
KR20110136156A (en) * 2010-06-14 2011-12-21 박정길 Salt vaporization refining apparatus

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112654259A (en) * 2018-07-23 2021-04-13 杭州尤美特科技有限公司 Functional plant salt and preparation method and application thereof

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