KR101349048B1 - Drinking-water manufacturing device and control method for disorder in it - Google Patents

Drinking-water manufacturing device and control method for disorder in it Download PDF

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Publication number
KR101349048B1
KR101349048B1 KR1020130067729A KR20130067729A KR101349048B1 KR 101349048 B1 KR101349048 B1 KR 101349048B1 KR 1020130067729 A KR1020130067729 A KR 1020130067729A KR 20130067729 A KR20130067729 A KR 20130067729A KR 101349048 B1 KR101349048 B1 KR 101349048B1
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KR
South Korea
Prior art keywords
heat exchange
crude oil
beverage
exchange module
homogenizer
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KR1020130067729A
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Korean (ko)
Inventor
김학남
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(주)경원산업
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Priority to KR1020130067729A priority Critical patent/KR101349048B1/en
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Publication of KR101349048B1 publication Critical patent/KR101349048B1/en

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    • AHUMAN NECESSITIES
    • A47FURNITURE; DOMESTIC ARTICLES OR APPLIANCES; COFFEE MILLS; SPICE MILLS; SUCTION CLEANERS IN GENERAL
    • A47JKITCHEN EQUIPMENT; COFFEE MILLS; SPICE MILLS; APPARATUS FOR MAKING BEVERAGES
    • A47J31/00Apparatus for making beverages
    • A47J31/40Beverage-making apparatus with dispensing means for adding a measured quantity of ingredients, e.g. coffee, water, sugar, cocoa, milk, tea
    • A47J31/402Liquid dosing devices
    • AHUMAN NECESSITIES
    • A47FURNITURE; DOMESTIC ARTICLES OR APPLIANCES; COFFEE MILLS; SPICE MILLS; SUCTION CLEANERS IN GENERAL
    • A47JKITCHEN EQUIPMENT; COFFEE MILLS; SPICE MILLS; APPARATUS FOR MAKING BEVERAGES
    • A47J31/00Apparatus for making beverages
    • A47J31/44Parts or details or accessories of beverage-making apparatus

Abstract

The present invention relates to a drink producing device which comprises the following: balance tanks (110, 130) storing and supplying drink raw liquid; a homogenizer (210) connected to the balance tanks (110, 130) for uniformly mixing the drink raw liquid; a heat exchanging module unit (300) connected to the balance tanks (110, 130) and the homogenizer (210) for transferring heat to the drink raw liquid; a charger (400) supplying the drink raw liquid which is passed through the heat exchanging module unit (300) for heat exchanging; and a first malfunction control pipe (112) for supplying the drink raw liquid from the charger (400) to a first balance tank (110). [Reference numerals] (210) Homogenizer; (400) Charger

Description

Drinking-water manufacturing device and control method for disorder in it}

The present invention relates to a beverage production apparatus and a method for controlling abnormality occurrence thereof.

In the process of preparing a beverage, the raw milk is sterilized by high heat treatment, and then, after high heat treatment, the raw water is again low-heated and then injected into the product container at a suitable temperature.

In the heat treatment process of the beverage crude oil, a plurality of heat exchanger modules are used to heat the beverage crude oil with the high temperature heat medium or the low temperature heat medium.

However, in the conventional beverage production process, when a problem occurs in a plurality of heat exchanger modules, the entire process must be stopped to repair the problem, and a problem occurs in the product due to a change in the temperature of the beverage crude oil after a long time for maintenance. do.

An object of the present invention is to provide a beverage production apparatus and a method for controlling the occurrence of abnormalities that can maintain the quality of the product by maintaining the freshness of the beverage oil even when a problem occurs in the heat exchanger module in the beverage production process.

According to one aspect of the invention, the balance tank (110, 130) for storing or supplying the beverage crude oil, the homogenizer 210 is connected to the balance tank (110, 130) to uniformly mix the beverage crude oil, and the A heat exchange module unit 300 connected to the balance tanks 110 and 130 and the homogenizer 210 to heat transfer to the beverage crude oil, and a filler 400 to which the crude oil exchanged through the heat exchange module unit 300 is supplied. Drinking water production apparatus characterized in that it comprises a first or more control pipes 112 formed to deliver the beverage crude oil from the filler 400 to the first balance tank 110 of the balance tanks (110, 130). Can be provided.

In addition, a second abnormality control pipe 114 may be formed between the homogenizer 210 and the first balance tank 110.

The heat exchange module unit 300 is composed of a plurality of heat exchange modules (310, 330, 350, 370), the back pressure valve 810, respectively in the discharge portion of the plurality of heat exchange modules (310, 330, 350, 370) 830, 850, 870 is formed to adjust the pressure of the beverage crude oil and thereby control the temperature of the beverage crude oil.

The beverage crude oil stored in the first balance tank 110 is supplied to the homogenizer 210 via the first heat exchange module 310 of the plurality of heat exchange modules 310, 330, 350, 370, and then the homogenizer. In step 210, the process may be supplied to the second balance tank 130.

On the other hand, in the embodiment of the present invention, when abnormality occurs during the beverage production process in the beverage production apparatus, the beverage crude oil from the filler 400 to the first balance tank 110 through the first abnormal control pipe 112. It is also possible to provide an abnormality generation control method of the beverage production apparatus characterized in that the transfer.

The second heat exchange module 330, the third heat exchanger module 350, and the fourth heat exchange module 370 of the plurality of heat exchange modules 310, 330, 350, and 370 are transferred to the homogenizer 210 in case of failure. The purified beverage crude oil may not be delivered to the second balance tank 130, but may be delivered to the first balance tank 110 through the second abnormal control pipe 114 again.

The back pressure valves 810, 830, 850, and 870 are heat exchanged in the first heat exchange module 310, the second heat exchange module 330, the third heat exchanger module 350, and the fourth heat exchange module 370. The temperature can be controlled by adjusting the pressure of the beverage crude oil.

In an embodiment of the present invention, when a problem such as unsterilization occurs in the beverage crude oil delivered to the filling machine, the beverage crude oil may be delivered to the first balance tank through the first or more control pipe.

Through this, the beverage crude oil can be configured to pass any part of the first heat exchange module to the fourth heat exchange module, so that an appropriate sterilization treatment can be performed.

In addition, in the embodiment of the present invention, the second abnormality control pipe is formed between the homogenizer and the first balance tank so that when the second heat exchange module to the fourth heat exchange module fails, the crude oil delivered to the homogenizer is not transferred to the second balance tank. Instead, the second balance control pipe can be delivered back to the first balance tank.

Through this, the effect of repairing some or all of the failures occurring in the second to fourth heat exchange modules is generated.

1 is a schematic diagram showing an embodiment of the present invention.

Hereinafter, embodiments of the present invention will be described in detail with reference to the accompanying drawings. It is to be understood, however, that the appended drawings illustrate the present invention in order to more easily explain the present invention, and the scope of the present invention is not limited thereto. You will know.

In describing the present embodiment, the same designations and the same reference numerals are used for the same components, and further description thereof will be omitted.

Also, the terms used in the present application are used only to describe certain embodiments and are not intended to limit the present invention. Singular expressions include plural expressions unless the context clearly indicates otherwise. In this application, the terms "comprise" or "have" are intended to indicate that there is a feature, number, step, operation, component, part, or combination thereof described in the specification, and one or more other features. It is to be understood that the present invention does not exclude the possibility of the presence or the addition of numbers, steps, operations, components, components, or a combination thereof.

1 is a schematic diagram showing an embodiment of the present invention.

The beverage production apparatus according to the embodiment of the present invention is connected to two balance tanks 110 and 130 for storing or supplying the beverage crude oil, and a homogenizer for uniformly mixing the beverage crude oil connected to the two balance tanks 110 and 130 ( 210 and the heat exchanger module 300 connected to the two balance tanks 110 and 130 and the homogenizer 210 to heat the beverage crude oil and the heat exchanged beverage crude oil supplied through the heat exchange module 300. It is configured to include a filler (400).

The first balance tank 110 of the two balance tanks (110, 130) is a tank into which the beverage crude oil flows.

The beverage crude oil may be various beverage crude such as orange beverage crude or bottled water or cola.

The beverage crude oil stored in the first balance tank 110 is a temperature of 20 degrees Celsius, and after it is raised to a temperature of 50 degrees Celsius, it is supplied to the homogenizer 210 and homogenized in the homogenizer 210 and then the second balance tank ( 130).

In the present invention, the first heat exchange module 310 is formed in the heat exchange module unit 300 in order to raise the crude oil of 20 degrees Celsius to a temperature of 50 degrees Celsius.

The beverage crude oil stored in the first balance tank 110 is supplied to the homogenizer 210 via the first heat exchange module 310 and then processed through the homogenizer 210 to the second balance tank 130. Supplied.

The beverage crude oil supplied to the second balance tank 130 at 50 degrees Celsius may be supplied to the filler 400 after being heated to 115 degrees Celsius or 98 degrees Celsius.

In order to raise the beverage crude oil of 50 degrees Celsius to a temperature of 115 degrees Celsius or 98 degrees Celsius, the second heat exchange module 330 is formed in the heat exchange module unit 300 in the present invention.

The beverage crude oil supplied to the second balance tank 130 is elevated to a temperature of 115 degrees Celsius or 98 degrees Celsius while passing through the second heat exchange module 330.

On the other hand, when it is necessary to lower the beverage crude oil raised to a temperature of 115 degrees Celsius or 98 degrees Celsius to a temperature of 92 degrees Celsius, the first beverage formed between the second heat exchange module 330 and the filler 400 The three-way valve 510 passes through the holding unit 600 and heats through the third heat exchange module 350 of the heat exchange module unit 300.

The beverage crude oil having a temperature of 92 degrees Celsius via the third heat exchange module 350 is introduced into the second three-way valve 520 formed between the first three-way valve 510 and the filler 400 and then the filler ( 400).

On the other hand, in the situation where it is impossible to send the beverage crude oil raised to the temperature of 115 degrees Celsius or 98 degrees Celsius to the filling machine 400, for example, when the operating capacity of the filling machine 400 is saturated, the first three-way valve The second balance tank 130 after lowering the drinking water crude oil raised to a temperature of 115 degrees Celsius or 98 degrees Celsius through the third three-way valve 530 formed between the 510 and the second three-way valve 520 Flow in.

A fourth heat exchange module 370 is formed in the heat exchange module unit 300 to lower the beverage crude oil raised to a temperature of 115 degrees Celsius or 98 degrees Celsius to 60 degrees Celsius.

Accordingly, the beverage crude oil raised to a temperature of 115 degrees Celsius or 98 degrees Celsius is introduced into the second balance tank 130 after descending to 60 degrees Celsius while passing through the fourth heat exchange module 370.

Meanwhile, an inlet pressure gauge 710 for measuring the inlet pressure and an inlet thermometer 720 for measuring the inlet temperature are formed at each inlet of the first heat exchange module 310 to the fourth heat exchange module 370. The discharge parts of the first heat exchange module 310 to the fourth heat exchange module 370 respectively have a discharge manometer 730 for measuring the discharge pressure, a discharge thermometer 740 for measuring the discharge temperature, and a discharge pressure sensor 750 associated therewith. And discharge temperature control device 760 is formed.

In addition, back pressure valves 810, 830, 850, and 870 are formed at the discharge portions of the first heat exchange module 310 to the fourth heat exchange module 370, respectively, to control the pressure of the beverage crude oil and thereby It also controls the temperature.

In the first heat exchange module 310 and the second heat exchange module 330, a working fluid acting to increase the temperature of the beverage crude oil receives heat from separate heat exchangers 910 and 920 and flows therein, and the third heat exchange module In operation 350 and the fourth heat exchange module 370, a working fluid that acts to lower the temperature of the beverage crude oil receives and receives cold temperature through separate circulation paths 930 and 940.

On the other hand, in the embodiment of the present invention in consideration of the occurrence of abnormalities in the beverage production process, the first abnormal control pipe 112 for transferring the crude oil from the filler 400 to the first balance tank 110 is formed. .

First balance through the first or more control pipes 112 when the crude oil delivered to the filling machine 400 is not the proper temperature or state due to failure of the first heat exchange module 310 to the fourth heat exchange module 370. It is delivered to the tank 110.

This prevents the improper drink crude oil delivered to the filling machine 400 to be transferred to the next process as it is, the effect can be maintained to maintain the quality reliability of the beverage final product.

In addition, in the embodiment of the present invention, the second abnormality control pipe 114 is formed between the homogenizer 210 and the first balance tank 110.

When the second heat exchange module 330 to the fourth heat exchange module 370 is broken, the crude water supplied to the homogenizer 210 is not transferred to the second balance tank 130, and the second abnormal control pipe 114 It is transmitted to the first balance tank 110 through.

That is, when the second heat exchange module 330 to the fourth heat exchange module 370 fail, the first balance tank 110, the first heat exchange module 310, the homogenizer 210, and the second abnormal control pipe 114 ) And the beverage crude oil may flow along the closed circuit formed by the first balance tank 110 to circulate the beverage crude oil until the second heat exchange module 330 to the fourth heat exchange module 370 are repaired.

Referring to the abnormal occurrence control method in the beverage production process of the embodiment of the present invention formed as described above are as follows.

An embodiment of the present invention is the back pressure valve (810, 830, 850, 870) is a function of controlling the temperature by adjusting the pressure of the crude water heat exchanged in the first heat exchange module 310 to the fourth heat exchange module 370 By doing so, the first heat exchange module 310 to the fourth heat exchange module 370 serves to control the occurrence of abnormality caused by the degradation of the function.

That is, the first heat exchange module 310 to the fourth heat exchange module 370 is a plate type heat exchanger module, and foreign matter may accumulate or deteriorate due to its own shape through long use. In this case, the back pressure valve ( 810, 830, 850, 870 is in conjunction with the discharge pressure gauge 730, discharge thermometer 740, discharge pressure sensor 750 and discharge temperature control device 760 to control the pressure of the drinking water crude oil and also controls the temperature.

On the other hand, in the embodiment of the present invention, if a problem such as unsterilized in the beverage crude oil delivered to the filling machine 400, the first crude tank 110 for the beverage crude oil through the first or more control pipe 112 Can be delivered to.

Through this, the beverage crude oil can be configured to pass through any one of the first heat exchange module 310 to the fourth heat exchange module 370, so that an appropriate sterilization treatment can be performed.

In addition, in the embodiment of the present invention, a second abnormality control pipe 114 is formed between the homogenizer 210 and the first balance tank 110, so that the second heat exchange module 330 to the fourth heat exchange module 370 are formed. In the event of a failure, the crude water delivered to the homogenizer 210 may not be delivered to the second balance tank 130, but may be delivered back to the first balance tank 110 through the second abnormal control pipe 114. .

As a result, an effect of repairing some or all of the failures in the second heat exchange module 330 to the fourth heat exchange module 370 is generated.

It will be apparent to those skilled in the art that the present invention may be embodied in other specific forms without departing from the spirit or scope of the invention as defined in the appended claims. . Therefore, the above-described embodiments are to be considered as illustrative rather than restrictive, and the present invention is not limited to the above description, but may be modified within the scope of the appended claims and equivalents thereof.

110: first balance tank 112: the first abnormal control piping
114: second or more control piping 130: second balance tank
210: homogenizer 300: heat exchange module unit
310: first heat exchange module 330: second heat exchange module
350: third heat exchange module 400: filler
510: first three-way valve 520: second three-way valve
530: third three-way valve 810, 830, 850, 870: back pressure valve

Claims (7)

  1. Balance tanks (110, 130) for storing or supplying the drink crude oil,
    A homogenizer 210 connected to the balance tanks 110 and 130 to uniformly mix the beverage oil;
    A heat exchange module unit 300 connected to the balance tanks 110 and 130 and the homogenizer 210 to transfer heat to the beverage crude oil;
    Filler 400 is supplied with the beverage crude oil heat exchanged through the heat exchange module unit 300 and
    The first or more control pipe 112 formed to deliver the beverage crude oil from the filler 400 to the first balance tank 110 of the balance tank (110, 130)
    Drinks production apparatus characterized in that it comprises a.
  2. The method according to claim 1,
    Drinking water production apparatus, characterized in that the second abnormal control pipe 114 is formed between the homogenizer 210 and the first balance tank (110).
  3. The method according to claim 1 or 2,
    The heat exchange module unit 300 is composed of a plurality of heat exchange modules (310, 330, 350, 370), the back pressure valve 810, respectively in the discharge portion of the plurality of heat exchange modules (310, 330, 350, 370) 830, 850, 870 is formed to adjust the pressure of the beverage crude oil and thereby control the temperature of the beverage crude oil.
  4. The method according to claim 3,
    The beverage crude oil stored in the first balance tank 110 is supplied to the homogenizer 210 via the first heat exchange module 310 of the plurality of heat exchange modules 310, 330, 350, 370, and then the homogenizer. Beverage production apparatus characterized in that it is supplied to the second balance tank 130 through the process at 210.
  5. When an abnormality occurs during the beverage production process in the beverage production apparatus of claim 4 characterized in that the raw water is delivered from the filling machine 400 to the first balance tank 110 through the first abnormal control pipe 112. An abnormal control method of the beverage production apparatus.
  6. delete
  7. delete
KR1020130067729A 2013-06-13 2013-06-13 Drinking-water manufacturing device and control method for disorder in it KR101349048B1 (en)

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Application Number Priority Date Filing Date Title
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Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1999021442A1 (en) * 1997-10-23 1999-05-06 Morinaga Milk Industry Co., Ltd. Method and apparatus for continuous heat sterilization of liquid
KR20120007450A (en) * 2010-07-14 2012-01-20 폴 코포레이션 Method for treating a fluid, in particular a beverage
KR20120014558A (en) * 2009-04-01 2012-02-17 네스텍 소시에테아노님 Instant beverage product

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1999021442A1 (en) * 1997-10-23 1999-05-06 Morinaga Milk Industry Co., Ltd. Method and apparatus for continuous heat sterilization of liquid
JP3674685B2 (en) * 1997-10-23 2005-07-20 森永乳業株式会社 Method and apparatus for continuous heat sterilization of liquid
KR20120014558A (en) * 2009-04-01 2012-02-17 네스텍 소시에테아노님 Instant beverage product
KR20120007450A (en) * 2010-07-14 2012-01-20 폴 코포레이션 Method for treating a fluid, in particular a beverage

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