KR20160144816A - Apparatus For Drying For Agricultural And Marine Products - Google Patents

Apparatus For Drying For Agricultural And Marine Products Download PDF

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Publication number
KR20160144816A
KR20160144816A KR1020150081474A KR20150081474A KR20160144816A KR 20160144816 A KR20160144816 A KR 20160144816A KR 1020150081474 A KR1020150081474 A KR 1020150081474A KR 20150081474 A KR20150081474 A KR 20150081474A KR 20160144816 A KR20160144816 A KR 20160144816A
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KR
South Korea
Prior art keywords
refrigerant
unit
compressor
pipe
drying chamber
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KR1020150081474A
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Korean (ko)
Inventor
정창진
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(주)한국표준환경기술
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Priority to KR1020150081474A priority Critical patent/KR20160144816A/en
Publication of KR20160144816A publication Critical patent/KR20160144816A/en

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    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23LFOODS, 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
    • A23L3/00Preservation of foods or foodstuffs, in general, e.g. pasteurising, sterilising, specially adapted for foods or foodstuffs
    • A23L3/40Preservation of foods or foodstuffs, in general, e.g. pasteurising, sterilising, specially adapted for foods or foodstuffs by drying or kilning; Subsequent reconstitution
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23BPRESERVING, e.g. BY CANNING, MEAT, FISH, EGGS, FRUIT, VEGETABLES, EDIBLE SEEDS; CHEMICAL RIPENING OF FRUIT OR VEGETABLES; THE PRESERVED, RIPENED, OR CANNED PRODUCTS
    • A23B4/00General methods for preserving meat, sausages, fish or fish products
    • A23B4/03Drying; Subsequent reconstitution
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23BPRESERVING, e.g. BY CANNING, MEAT, FISH, EGGS, FRUIT, VEGETABLES, EDIBLE SEEDS; CHEMICAL RIPENING OF FRUIT OR VEGETABLES; THE PRESERVED, RIPENED, OR CANNED PRODUCTS
    • A23B7/00Preservation or chemical ripening of fruit or vegetables
    • A23B7/02Dehydrating; Subsequent reconstitution

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  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Food Science & Technology (AREA)
  • Polymers & Plastics (AREA)
  • Wood Science & Technology (AREA)
  • Zoology (AREA)
  • Health & Medical Sciences (AREA)
  • Nutrition Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Drying Of Solid Materials (AREA)

Abstract

The present invention relates to a drying apparatus for agricultural and marine products, which can be easily manufactured on the basis of a conventional refrigeration system, is excellent in economy, and has improved durability. The composition is; A stacking portion for stacking the objects to be dried; A drying chamber for providing a processing space in which the loading section can be installed; A refrigeration unit for lowering the temperature of the processing space inside the drying chamber according to a refrigeration cycle of compression, condensation, expansion and evaporation of the refrigerant; And a reheat unit;
The refrigeration unit includes: a compressor installed outside the drying chamber; Condenser; Receiver; An expansion valve for expanding the refrigerant supplied from the receiver; And an evaporator installed inside the drying chamber; The reheating unit comprising: An outlet pipe extending diverging from a pipe between the compressor and the condenser; A reheater connected to the drawing tube; A recovery pipe connected between the reheater and the receiver for allowing the refrigerant passing through the reheater to be supplied to the receiver; And a flow control means for selectively supplying the high temperature and high pressure refrigerant supplied to the compressor to the outlet pipe or the condenser.

Description

[0001] Apparatus For Drying For Agricultural And Marine Products [0002]

BACKGROUND OF THE INVENTION 1. Field of the Invention [0002] The present invention relates to a drying apparatus, and more particularly, to a drying apparatus for agricultural and marine products, which can be easily manufactured based on a conventional refrigeration system, and is excellent in economy and durability.

The agricultural and marine product drying apparatus is widely used as a device for drying the harvested agricultural and marine products until the moisture content reaches the desired value, such as farm houses or agricultural / marine product distribution facilities.

These dryers often have refrigeration cycles. Generally, a refrigeration cycle is a system for continuously circulating refrigerant through four processes of compression, condensation, expansion, and evaporation, and discharges the latent heat of the refrigerating space to the outside air during the evaporation of the refrigerant.

Dryers widely used in conventional farms have been used for refrigeration or freeze storage by controlling the load of the refrigeration cycle and have used the drying function in a way of removing water in the refrigeration or freeze storage process. However, since the ambient temperature is low in winter, it is common to store the refrigeration system without operating the refrigeration system. Therefore, during the winter, equipment was used like a warehouse, and agricultural and marine products kept in storage were left untreated.

Korean Patent Application No. 10-2007-0095682 Korean Patent Application No. 10-2010-0101323 Korean Utility Model Registration Application No. 20-2001-0029296

It is an object of the present invention to solve the above problems and to provide a drying apparatus for agricultural and marine products which can dry agricultural and marine products by utilizing a refrigeration system. And more particularly, to provide a drying device having a structure capable of improving the durability of a compressor by reducing load fluctuations of the compressor. Also, it is aimed to overcome the inefficiency that expensive equipment is neglected by sufficiently utilizing the refrigeration equipment provided in the farmhouse as a dryer in winter.

The above-mentioned object is achieved by a storage unit for stacking and storing an object to be dried; A drying chamber for providing a processing space in which the loading section can be installed; A refrigeration unit for lowering the temperature of the processing space inside the drying chamber according to a refrigeration cycle of compression, condensation, expansion and evaporation of the refrigerant; And a reheat unit;

Wherein the refrigerating unit comprises: a compressor for compressing a refrigerant and installed outside the drying chamber; A condenser functioning to heat the high-pressure, high-temperature refrigerant discharged from the compressor by heat exchange with outside air; A receiver for temporarily storing the high-temperature and high-pressure refrigerant liquid liquefied in the condenser; An expansion valve for expanding the refrigerant supplied from the receiver;

And an evaporator installed in the drying chamber for exchanging heat with the processing space through a liquid refrigerant whose pressure has been reduced to a low temperature and a low pressure while passing through the expansion valve to absorb heat through evaporation of the liquid and to supply the evaporated refrigerant to the compressor ;

The reheating unit comprising:

An outlet pipe extending diverging from a pipe between the compressor and the condenser; A reheater connected to the drawing tube and installed in front of the evaporator in the drying chamber to lower the temperature of the refrigerant through heat exchange with the evaporator; A return pipe connected between the reheater and the receiver for allowing the refrigerant passing through the reheater to be supplied to the receiver; Flow rate control means for selectively supplying the high-temperature and high-pressure refrigerant supplied to the compressor to the outlet pipe or the condenser;

And a drying apparatus for agricultural and marine products.

According to an aspect of the present invention, the control unit may control the valve unit to supply the refrigerant to the reheater when the temperature of the refrigerant discharged from the compressor becomes equal to or higher than a set value.

According to an aspect of the present invention, the circulation pipe connecting between the compressor and the condenser and the extraction pipe are branched by a pipe connector;

A first valve installed at a rear end of the pipe connection port of the circulation pipe and being turned on and off by the control unit; And a second valve installed on the drawing tube and being turned on and off by the control unit.

According to another aspect of the present invention, the circulation pipe includes a plurality of unit circulation pipes installed in parallel; The first valve may be constituted by a plurality of first unit valves installed separately for each unit circulation pipe.

According to another aspect of the present invention, the drawing tube includes a plurality of unit drawing tubes installed in parallel; And the second valve may be constituted by a plurality of second unit valves installed separately for each unit take-out pipe.

According to still another aspect of the present invention, the flow rate control means may be a three-way valve installed at a branch point of the take-out pipe.

INDUSTRIAL APPLICABILITY According to the present invention, it is possible to provide a agricultural and marine product dryer that can be used at any time regardless of the season by using a freeze-drying system that has been spread to existing farmhouses. According to the present invention, it is possible to obtain an effect that durability is improved by reducing load fluctuation caused by repeating stop and operation of the compressor. Also, since the existing system can be improved and used, there is no need to construct a separate system, and the initial cost can be greatly reduced.

1 is a system configuration diagram of a drying apparatus for agricultural and marine products according to an embodiment of the present invention.
Figs. 2 (a), 2 (b) and 2 (c) illustrate flow control means of a drying apparatus for agricultural and marine products according to an embodiment of the present invention.

Hereinafter, the present invention will be described in detail with reference to the accompanying FIGS. 1 to 2 (a), (b) and (c).

The loading unit 110 is a shelf mechanism for stacking a large amount of laundry. The loading section 110 is configured so that air can be communicated, respectively. The drying chamber 100 provides a processing space S in which the loading section 110 can be installed. The wall constituting the drying chamber 100 preferably has a heat insulating function. The drying chamber 100 is provided on a scale that can be accessed by the operator. The shape and size of the loading unit 110 and the drying chamber 100 will vary widely and do not limit the scope of the present invention.

A freezing unit is installed around the processing space S of the drying chamber 100. The refrigeration unit performs the process of compressing, condensing, expanding, and evaporating the refrigerant like a normal refrigeration cycle. The freezing unit is for lowering the temperature of the processing space S in the drying chamber 100, and it may be possible to refrigerate and freeze. Hereinafter, the refrigeration unit will be briefly described.

The compressor (1) is for receiving the refrigerant from the evaporator (11) and compressing the refrigerant, and is installed outside the drying chamber (100). The condenser (5) liquefies the high-pressure, high-temperature refrigerant discharged from the compressor (1) by exchanging heat with the outside air. Between the compressor (1) and the condenser (5), a liquid separator (3) for separating oil can be provided. In the description of the present invention, the liquid separator 3 is described by the concept included in the compressor 1. The liquid receiver 7 temporarily stores the high-temperature and high-pressure refrigerant liquid liquefied in the condenser 5 and supplies it to the expansion valve 9. The expansion valve 9 is for reducing pressure by expanding the refrigerant supplied from the receiver 7, and may be installed inside the drying chamber 100. The evaporator 11 installed inside the drying chamber 100 lowers the temperature of the processing space S by exchanging heat with the liquid refrigerant whose pressure has been reduced to a low temperature and a low pressure state while passing through the expansion valve 9. The evaporator (11) absorbs the ambient heat through vaporization of the liquid and supplies the evaporated refrigerant to the compressor (1) to complete the circulation process.

The evaporator 11 is installed at an upper portion of one side of the drying chamber 100 to allow the flow of air as shown by arrow A.

The refrigeration unit described above is a basic configuration of the refrigeration cycle. Therefore, in addition to this, a known additional component such as an accumulator may be installed.

According to the present invention, a reheating unit is included in addition to the freezing unit.

The reheating unit is for supplying coolant in a high-temperature and high-pressure state into the drying chamber 100 to perform heat exchange with the processing space S. The reheat unit serves to lower the relative humidity by raising the temperature of the processing space (S).

The reheat unit includes a reheater (13) installed inside the drying chamber (100). The reheater 13 may have a heat radiating structure for increasing heat exchange efficiency, and may have a fan therein. According to the embodiment of the present invention, the reheater 13 is disposed adjacent to the front of the evaporator 11, that is, on the side of the discharge portion of the evaporator 11 in order to increase the efficiency of reheat.

The outflow pipe 17 for supplying the refrigerant to the reheater 13 is extended in the circulation pipe 19 between the compressor 1 and the condenser 5. The refrigerant that has passed through the reheater 13 is supplied to the receiver through the return pipe 21. The recovery pipe 21 is connected between the reheater 13 and the receiver 7 so that the refrigerant having passed through the reheater 13 is supplied to the receiver 7.

The flow rate control means 15 selectively supplies the high temperature and high pressure refrigerant supplied to the compressor 1 to the reheater 13 or the condenser 5. The reheat unit is started from the beginning only when the reheat unit does not start like the freezing unit and when the reheater unit is in the set state. For example, the control unit controls the flow rate control unit 15 to supply the refrigerant to the reheater 13 when the temperature becomes equal to or higher than the set value based on the temperature of the refrigerant discharged from the compressor 1. [ For example, when the temperature of the refrigerant measured by the thermometer 23 reaches 70 ° C or more, the control unit sends the refrigerant discharged from the compressor 1 to the reheater 13. This temperature corresponds to the temperature at which the refrigeration unit performs the cooling action at normal temperature.

In the case of winter in which the outside temperature is low, the calorific value generated by the freezer may be low and the capacity of the reheater (13) may be insufficient. In this case, the amount of heating heat required by the reheater 13 can be ensured by controlling the flow rate of the indoor unit, that is, the evaporator 11 to induce the high-pressure operation of the compressor 1. [ In addition, the supplementary heater 41 may be installed in the reheater 13 to supplement the insufficient amount of heat.

The flow rate control means 15 can distribute the supplied refrigerant to the reheater 13 or the condenser 5 through various methods. Hereinafter, the flow control means 15 of various methods will be described by way of example.

First, referring to Fig. 2 (a).

The circulation pipe (19) and the take-out pipe (17) are branched by the pipe connector (25). The circulation pipe 19 is a pipe connecting the compressor 1 and the condenser 5. The pipe connection port 25 is a known means of a T (T) type or a W (Y) type.

The first valve 27 which is turned on and off by the control unit is installed in the circulation pipe 19, in particular, in the circulation pipe 19 corresponding to the rear end of the pipe connection port 25. [ And a second valve 29 which is turned on and off by the control unit is installed in the take-out pipe 17. The first and second valves 27 and 29 may be solenoid valves operated on and off by an electrical signal.

According to the present embodiment, the advancing direction of the refrigerant can be selected by opening only one of the valves. In addition, by opening all the first and second valves 27 and 29, the refrigerant can be branched and supplied to the condenser 5 and the reheater 13, respectively.

2 (b).

The circulation pipe (19) includes a plurality of unit circulation pipes (19a, 19b) installed in parallel. The first valve 25 is constituted by a plurality of first unit valves 25a and 25b which are installed separately for each unit circulation pipe 19a and 19b. The unit circulation pipes 19a and 19b and the first unit valves 27a and 27b are each composed of two units.

According to the drawings, the drawing tube 17 may include a plurality of unit drawing tubes 17a and 17b arranged in parallel. The second valve 29 may be constituted by a plurality of second unit valves 29a and 29b, which are provided for each of the unit drawing tubes 17a and 17b and are individually operated. The unit draw-out pipes (17a, 17b) and the second unit valves (29a, 29b) may also be two.

According to the present embodiment, the flow rate can be controlled while selecting the first and second valves 27 and 29 as solenoid valves. This is because all unit valves can be opened to increase the flow rate, or only some unit valves can be opened to lower the flow rate.

The following description will be made with reference to Fig. 2 (c).

According to the present embodiment, the take-out tube 17 is branched and extended from the circulation tube 19 via the three-way valve 31. The three-way valve 31 is a known valve device that allows a flow rate to be selectively supplied in two different directions as one valve. This allows the fluid, that is, the refrigerant, to be supplied only to one pipe. The configuration is simplified, but the selection range of the refrigerant supply method will be reduced.

The configuration shown and described above is merely a preferred embodiment based on the technical idea of the present invention. It will be understood by those skilled in the art that various changes and modifications may be made without departing from the scope of the present invention.

1: compressor 3: liquid separator
5: condenser 7: receiver
9: expansion valve 11: evaporator
13: Reheater 15: Flow control means
17: take-out tube 19: circulation tube
21: recovery pipe 23: thermometer
25: Piping connector 27, 29: 1st and 2nd valves
31: Three-way valve
100: drying chamber 110:

Claims (6)

A stacking portion for stacking the objects to be dried; A drying chamber for providing a processing space in which the loading section can be installed; A refrigeration unit for lowering the temperature of the processing space inside the drying chamber according to a refrigeration cycle of compression, condensation, expansion and evaporation of the refrigerant; And a reheat unit;
Wherein the refrigerating unit comprises: a compressor for compressing a refrigerant and installed outside the drying chamber; A condenser functioning to heat the high-pressure, high-temperature refrigerant discharged from the compressor by heat exchange with outside air; A receiver for temporarily storing the high-temperature and high-pressure refrigerant liquid liquefied in the condenser; An expansion valve for expanding the refrigerant supplied from the receiver;
And an evaporator installed in the drying chamber for exchanging heat with the processing space through a liquid refrigerant whose pressure has been reduced to a low temperature and a low pressure while passing through the expansion valve to absorb heat through evaporation of the liquid and to supply the evaporated refrigerant to the compressor ;
The reheating unit comprising:
An outlet pipe extending diverging from a pipe between the compressor and the condenser; A reheater connected to the drawing tube and installed in front of the evaporator in the drying chamber to lower the temperature of the refrigerant through heat exchange with the evaporator; A return pipe connected between the reheater and the receiver for allowing the refrigerant passing through the reheater to be supplied to the receiver; Flow rate control means for selectively supplying the high-temperature and high-pressure refrigerant supplied to the compressor to the outlet pipe or the condenser;
And a drying device for drying the agricultural and marine products.
The method according to claim 1,
Further comprising a controller for controlling the valve means to supply the refrigerant to the reheater when the temperature of the refrigerant discharged from the compressor becomes equal to or higher than a set value.
The method according to claim 1,
A circulation pipe connecting the compressor and the condenser and the extraction pipe being branched by a pipe connector;
A first valve installed at a rear end of the pipe connection port of the circulation pipe and being turned on and off by the control unit; And a second valve installed on the take-out tube, the second valve being turned on and off by the control unit.
The method according to claim 1,
Wherein the circulation pipe includes a plurality of unit circulation tubes installed in parallel; Wherein the first valve is constituted by a plurality of first unit valves individually provided for each unit circulation pipe.
The method according to claim 1,
Wherein the drawing tube includes a plurality of unit drawing tubes installed in parallel; And the second valve is constituted by a plurality of second unit valves installed separately for each unit take-out pipe.
The method according to claim 1,
Wherein the flow rate control means is a three-way valve installed at a branch point of the take-out tube.
KR1020150081474A 2015-06-09 2015-06-09 Apparatus For Drying For Agricultural And Marine Products KR20160144816A (en)

Priority Applications (1)

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KR1020150081474A KR20160144816A (en) 2015-06-09 2015-06-09 Apparatus For Drying For Agricultural And Marine Products

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR102128516B1 (en) 2019-11-19 2020-06-30 송민철 Low Temperature Storeroom

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20070095682A (en) 2006-03-22 2007-10-01 최종철 Made using methods of use embossed printing
KR20100101323A (en) 2009-03-09 2010-09-17 최영일 Mesh board a manufacturing method

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20070095682A (en) 2006-03-22 2007-10-01 최종철 Made using methods of use embossed printing
KR20100101323A (en) 2009-03-09 2010-09-17 최영일 Mesh board a manufacturing method

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR102128516B1 (en) 2019-11-19 2020-06-30 송민철 Low Temperature Storeroom

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