KR200384632Y1 - Treatment apparatus for steam sterilization and dryness - Google Patents

Abstract

The present invention is to maintain the state of high temperature and high pressure by ejecting steam and compressed air into the inner chamber of the processing tank in which the packaged food is accommodated, but the sterilization of the packaged food, steam pipe, steam is injected, compressed air injected air Proportional control valves are installed in the piping, the drain pipe for removing condensed water, and the cooling air pipe into which the cooling air generated by the cooling drying device is injected, respectively. The first mapping table in which the proportional control valve opening rate is mapped to maintain the saturated steam pressure according to the present invention, and the second mapping table in which the proportional control valve opening rate is mapped to maintain the internal pressure of the packaged food according to the cooling drying in the cooling drying section. And a memory having a built-in memory, and the controller controls the proportional control valve using the first mapping table and the second mapping table. The Castle.

Description

Steam Sterilization and Drying Equipment {TREATMENT APPARATUS FOR STEAM STERILIZATION AND DRYNESS}

The present invention relates to an improvement of a sterilization apparatus for sterilizing packaged foods such as retort parch, bottled foods, and canned food with high temperature and high pressure steam.

In general, the sterilization apparatus is connected to a steam pipe and a compressed air pipe to a treatment tank, and a drain pipe is installed at a lower portion of the treatment tank. The inner chamber of the treatment tank is supplied with steam injected through the steam pipe and compressed air injected through the compressed air pipe, respectively, and a part of the mixture of the steam and the compressed air is exhausted through the drain pipe. The inner chamber is maintained at high temperature and high pressure, and the packaged food housed in the inner chamber can be sterilized.

The steam sterilization apparatus of the related art generally uses a valve installed in a pipe or a drain pipe pipe into which steam and compressed air are injected as an on / off valve, thereby completely opening or closing the valve. Steam sterilizer must make saturated room for sterilization during temperature increase or sterilization period. Conventional steam sterilizer using on / off valve is used to precisely control the room inside saturated steam. There is a disadvantage in that the sterilization performance is poor because it can not fit.

In addition, the steam sterilization method of the prior art is a method of raising the temperature with steam and adjusting the pressure of the air, and after the end of sterilization is sprayed (water) to cool by spraying with water. This prior art sterilization method is not suitable where precision control is necessary because the pressure and temperature are not proportionally increased at the time of temperature rise, and water is pouch or product after the sterilization is completed by spraying water during the cooling process. It remained on the surface and could not be packaged immediately. Therefore, after the sterilization treatment, the packaging after natural drying or drying using a separate drying device was inconvenient to be packed.

Therefore, an object of the present invention is to provide a steam sterilization and drying treatment apparatus capable of precise package food sterilization.

Another object of the present invention is to provide a steam sterilization and drying treatment apparatus that can perform steam food sterilization and drying in one place at a time.

Still another object of the present invention is to provide a steam sterilization and drying treatment apparatus capable of lowering the production cost of packaged food sterilization and improving the quality of sterilized products.

According to the above object, the present invention, while maintaining the state of high temperature and high pressure by ejecting steam and compressed air into the inner chamber of the processing tank in which the packaged food is accommodated, the steamed product, steam pipe, compressed steam is injected Proportional control valves are installed in the compressed air pipe into which air is injected, the drain pipe to remove condensed water, and the cooling air pipe into which the cooling air generated by the cooling drying device is injected, respectively. The first mapping table in which the proportional control valve opening rate is mapped to maintain the saturated steam pressure according to the elevated temperature and sterilization temperature, and the proportional control valve opening rate to maintain the internal pressure of the packaged food according to the cooling drying in the cooling drying section. And a memory incorporating a mapped second mapping table, and wherein the control device includes a first mapping table in a temperature rising and sterilizing section and a cooling drying section. The proportional control valve is controlled using the second mapping table.

Hereinafter, exemplary embodiments of the present invention will be described in detail with reference to the accompanying drawings. In the drawings, detailed descriptions of well-known functions and configurations that may unnecessarily obscure the subject matter of the present invention will be omitted.

In the embodiment of the present invention, in order to achieve a proportional increase in pressure and temperature when the temperature rises, a valve installed in each pipe of the steam sterilization apparatus is used as a proportional control valve, and the control device uses a valve control program based on temperature and pressure. To control the proportional control valve. According to the embodiment of the present invention, the proportional control valve is provided with a steam pipe, a steam pipe into which steam is injected, a compressed air pipe into which compressed air is injected, a drain pipe to remove condensed water, and a cooling air pipe into which cooling air is injected. An example of a general steam sterilization apparatus is Korean Patent Publication No. 93-002183 issued "Steam sterilization apparatus" issued March 27, 1993.

In addition, the embodiment of the present invention adds the structure for cooling and drying in the existing steam sterilization apparatus to perform the cooling and drying at the same time steam sterilization, steam sterilization and cooling drying in the control device having an opening and closing control mapping table To perform the control.

1 is a block diagram of a steam sterilization and drying treatment apparatus according to an embodiment of the present invention.

Referring to Figure 1, one side of the open box-shaped processing tank (2) is provided with an opening and closing door (4) for entering and exiting the packaged food in its opening.

The processing tank 2 is connected to a steam pipe 6, a compressed air pipe 8, a cooling air pipe 10, a circulation pipe 12, and a drain pipe 14. The steam pipe 6 is composed of a main steam pipe 16 and a bypass steam pipe 18, and the other end of the main steam pipe 16, one end of which is connected to the steam supply source 8, is the inner chamber of the processing tank 2. It is connected to one end of the blowoff pipe 22 arranged in the upper part. In the main steam pipe 16, a strainer, a pressure reducing valve 24, a pressure gauge (not shown), and a main steam control valve 26 are sequentially disposed from the steam supply source 20 toward the jet pipe 22. have.

 The bypass steam pipe 18 is branched at a position between the pressure gauge (not shown) of the main steam pipe 16 and the main steam control valve 26 to be connected to the inlet of the mixing device 28. A bypass regulating valve 30 is installed in the bypass stamp line 18, and a pressure gauge (not shown) is provided downstream of the bypass steam pipe 18. The outlet of the mixing device 28 is connected to one end of the blowoff pipe 22.

The compressed air pipe 8 includes a main compressed air pipe 32, a bypass compressed air pipe 34, and seal air pipes 36 and 38. The other end of the compressed air pipe 32 communicated with one end of the compressed air source 38 is connected to join the main steam pipe 16 at one end of the blowoff pipe 22. The main compressed air pipe 32 is provided with a pressure gauge (not shown) and a main compressed air control valve 42 in order from the compressed air supply source 40 side to the blowoff pipe 22. Control valves 44, 46, and 48 are also provided in the bypass compressed air pipe 34 and seal air pipes 36 and 38, respectively.

The bypass compressed air pipe 34 is connected to the inlet of the mixing device 28 via the heat exchanger 50, and the other end of the first seal air pipe 36 branched from the main compressed air pipe 32 is a seal chamber. Is connected to 52. An outlet pipe 54 for extracting air is connected to the seal chamber 52, and an air removal valve 56 is installed in the outlet pipe 54.

Meanwhile, in the embodiment of the present invention, there is no cooling water supply device for arithmetic into the internal chamber of the processing tank 2 as before, and a cooling device 60 for supplying cooling air 62 is provided instead of the cooling device 60. ) Is connected to the cooling air piping (10). The cooling air pipe 10 includes a main cooling air pipe 64 and an auxiliary cooling air pipe 66. The other side of the main cooling air valve 64 into which the cooling air 62 flows into one side is a treatment tank 2. Is connected to the air nozzle 64 provided on the indoor ceiling of the room. The other end of the auxiliary air pipe 66 branched from the cooling air pipe 10 is connected to join the main steam pipe 16 at one end of the blowoff pipe 22. Cooling air control valves 68 and 70 are installed in the main cooling air piping 64 and the auxiliary cooling air piping 66.

On the other hand, the drain pipe 14 for discharging the condensed water is connected to the drain port of the inner chamber bottom surface of the processing tank 2 with one end connected to the heat exchange chamber of the heat exchanger 50, and the other end is connected to the drain pipe outlet 58. In the middle of the control valve 72 is installed.

In addition, an exhaust valve 74 is disposed from the inner chamber of the processing tank 2 to the exhaust port, and an adjustment valve 76 is provided in the middle to prevent the chamber pressure from exceeding a predetermined value.

Although not shown in FIG. 1, the processing tank 2 is equipped with a plurality of pressure sensors for detecting the room pressure and a plurality of temperature sensors for detecting the room temperature. The detection signal of the pressure sensors and the detection signal of the temperature sensors provided in the chamber of the processing tank 2 are applied to the control device 80, and the control device 80 injects steam, compressed air and cooling air based on the detection signal. Control valves to adjust the pressure by the valve control program to perform precise valve opening and closing control required in each process.

According to an embodiment of the present invention, the regulating valves for adjusting steam, compressed air, and cooling air injection are proportional control valves, not on / off valves. The proportional control valve can precisely adjust the opening and closing degree of the valve so that the output amount can be linearly output in proportion to the control current value of the control device 80.

In the embodiment of the present invention, in order to precisely control the proportional control valve, the packaged food table the temperature-pressure relationship and the opening ratio of the proportional control valve and mapped them to the memory unit 82 of the control device 80. This will be described later in detail with reference to the memory table map of FIGS. 3 and 4.

In Fig. 1, reference numeral " 84 " not described is an operation panel for the user and the controller 80 to interface.

Existing steam sterilization apparatus is subjected to a packaged food input, preheating process, temperature rising process, sterilization process, cooling process, and takeout of the packaged food, as described in detail in Korean Patent Publication No. 93-002183. In the case where the packaged food is a retorto ruper, the temperature raising step and the sterilization step include a first temperature raising step and a first sterilization step, and a second temperature rising step and a second sterilization step.

On the contrary, the steam sterilization and drying treatment apparatus according to the embodiment of the present invention comprises a packaged food input, a preheating process, a temperature raising process, a sterilizing process, a cooling drying process, and a packaged food removing process.

Conventionally, after performing the cooling process through the sprinkling, the packaged food is taken out of the steam sterilization apparatus and dried by a separate drying apparatus or dried by natural drying, but in the embodiment of the present invention, the sterilization process is performed. The process between the food and the food taking out process is replaced by a cooling drying process so that the drying is performed at the same time with cooling. Thus, the sterilization and drying treatments are simultaneously performed in one place (steam sterilization and drying treatment apparatus). In particular, the cooling drying process according to an embodiment of the present invention uses a cooling method using cooling air, unlike water spraying in the conventional steam sterilization treatment apparatus.

Figure 2 is a characteristic curve for explaining the temperature increase section, sterilization section, cooling drying section during steam sterilization and drying treatment.

In Figure 2, for sterilizing the packaged food steam must go through an elevated temperature and sterilization section, after sterilization must go through a cooling drying section to safely take out the packaged food.

According to an embodiment of the present invention, the control unit 80 adapts to the temperature corresponding to the temperature rise and sterilization of the chamber of the processing tank 2 using the first mapping table of FIG. 3 in the temperature rising section and the sterilization section of FIG. 2. The proportional control valve is controlled to maintain the saturated steam pressure. In addition, the controller 80 adjusts the internal pressure of the packaged food (pouch, can, etc.) of the packaged food using the second mapping table of FIG. The proportional control valve is controlled to maintain similarity.

3 is a mapping table diagram for opening and closing the proportional control valve in the temperature increase and sterilization section according to an embodiment of the present invention, Figure 4 is a mapping table for opening and closing the proportional control valve in the cooling drying section according to an embodiment of the present invention As a diagram, each mapping table is embedded in the memory portion 82 of FIG.

The packaged food is almost sterilized when the indoor temperature of the processing tank 2 rises up to about 130 ° C, and when the indoor temperature is below 60 ° C, the pressure does not have to be adjusted to the saturated steam pressure. You can do it together. Therefore, in the embodiment of the present invention, as shown in Figure 3, the temperature range for adjusting the saturated steam pressure in the temperature increase and sterilization section is set to 60 ℃ ~ 130 ℃, the saturated steam pressure for each temperature in the temperature range is mapped. In addition, the opening ratio (%) of the proportional control valve is mapped according to the difference between the measured actual pressure of the processing tank 2 and the corresponding saturated steam pressure.

In the cooling drying section, as shown in FIG. 4, the temperature range is set to 130 ° C. to 60 ° C., and the internal pressure of the packaged food for each temperature within the temperature range is mapped. In addition, the opening ratio (%) of the proportional control valve is mapped according to the difference between the measured internal pressure of the processing tank 2 and the corresponding mapped food internal pressure.

For reference, in the ideal gas equation PV = nRT, since R is a constant and the volume of the container V is a constant value, the gas pressure has a relationship of P = nT. Therefore, as the temperature T rises, the saturated steam pressure P rises proportionally. The saturated steam pressure according to the temperature can be known within the range of 60 ° C to 130 ° C, and the opening rate of the proportional control valve for adjusting the saturated vapor pressure is obtained through experiments.

Meanwhile, the cooling drying apparatus 60 for generating cooling air for use in the cooling drying section of FIG. 2 may be implemented as a small air conditioner composed of an evaporator, an accumulator, a compressor, and a condenser. Another embodiment of the cooling drying apparatus may be implemented by placing a heat exchanger other than the heat exchanger 50 shown in FIG. 1 in the inner chamber of the processing tank 2 and allowing the coolant to flow through the heat exchanger.

FIG. 5 is a flowchart illustrating a proportional control valve control in a temperature raising and sterilizing section performed by the control device 80 of FIG. 1 according to an embodiment of the present invention, and FIG. It is a control flowchart of the proportional control valve in a cooling drying section performed.

The control device 80 varies depending on the type of packaged food in the elevated temperature and sterilization section, but sterilizes the packaged food by raising the temperature to a maximum of 130 ° C., and maintaining the saturated steam pressure in the elevated temperature and sterilization section. To this end, steam is supplied to the inner chamber of the treatment tank 2 through the steam pipe 6 and compressed air is supplied to the inner chamber of the treatment tank 2 through the compressed air pipe 8.

At this time, the control device 80 measures the current room temperature and the room temperature from the temperature sensors and pressure sensors installed in the room, as in step 100 of FIG. Thereafter, it is determined whether the indoor temperature is in the range of 40 ° C to 130 ° C (step 102). If the controller 80 is within the range, the saturated steam pressure value mapped to the first mapping table (FIG. 3) corresponding to the measured room temperature is read from the memory unit 82 in step 104.

Thereafter, the controller 80 obtains the difference between the measured room pressure and the saturated steam pressure read from the memory unit 82 in step 106 of FIG. 5, and calculates the opening degree of the proportional control valve corresponding to the difference in the first mapping table (FIG. 3). Read from). Thus, the opening and closing of the proportional control valve is precisely controlled based on the opening ratio of the proportional control valve read in step 108 of FIG. 5. At this time, the proportional control valves are regulating valves 42 and 44 for adjusting the compressed air supply.

By controlling the proportional control valve in this way, the saturated steam pressure can be precisely adjusted to the temperature in the temperature raising and sterilizing section.

On the other hand, the control device 80 cools and drys the inner chamber of the processing tank 2 using the cooling drying device 60 in the cooling drying section.

The controller 80 drives the cooling drying apparatus 60 to inject the first cooling air into the chamber of the processing tank 2 through the main cooling air pipe 64 and the auxiliary cooling air pipe 66, and then, for 5 minutes to Continue for about 1 minute to quickly cool the room temperature to 80 ℃ ~ 90 ℃. This type of cooling is effective because some types are sterilized through such rapid cooling.

Thereafter, the control device 80 supplies the cooling air intermittently through the auxiliary cooling air pipe 66 at an interval of 5 to 6 seconds, and slowly cools it to 40 ° C to 10 ° C over 5 minutes to 10 minutes. This control prevents the internal pressure of the treatment tank 2 from dropping drastically and prevents deformation or breakage of the product due to continuous rapid cooling.

The valve opening ratio of the proportional control valves 68 and 70 is adjusted based on the mapping table shown in FIG. 4 in order to match the preset internal pressure of the packaged food according to the room temperature drop when cooling in the cooling section. Thus, even during cooling, the internal pressure of the processing tank 2 can be maintained similar to the internal pressure of the packaged food.

Specifically, referring to FIG. 6, as in step 200 of FIG. 6, the control device 80 measures the current room temperature and the room temperature from temperature sensors and pressure sensors installed in the room. After that, it is determined whether the room temperature is between 40 ° C and 130 ° C (step 202 of FIG. 6). If the control device 80 is within the range, in step 204, the package food internal pressure value mapped to the second mapping table (FIG. 4) corresponding to the measured room temperature is read from the memory unit 82.

Thereafter, the control device 80 obtains the difference between the measured room pressure and the value of the packaged food internal pressure read by the memory unit 82 in step 206 of FIG. 6, and calculates the opening ratio of the proportional control valve corresponding to the difference in the second mapping table. Read on (Figure 4). Therefore, the opening and closing of the proportional control valve is precisely controlled based on the opening ratio of the proportional control valve read in step 208 of FIG. 6. At this time, the proportional control valves are regulating valves 68 and 70 for adjusting the amount of cooling air.

By controlling the proportional control valve as described above, it is possible to adjust the substantial state of the processing tank 2 to be similar to the internal pressure of the packaged food for each temperature in the cooling drying section.

A part of the condensed water formed in the inner chamber of the treatment tank 2 flows to the drain pipe 14. When the inside of the drain pipe 14 drops to the set temperature, for example, to 50 ° C, the main compressed air valve 26, the cooling air regulating valves 68, 70, and the seal inlet on the basis of the detection signal of the temperature sensor installed in the drain pipe 14. At the same time as the valve 32 is closed, the exhaust valve 76 and the air releasing valve 56 are opened.

Since the exhaust valve 76 is opened so that the internal pressure of the processing tank 2 is approximately equal to atmospheric pressure, the opening / closing door 2 is opened and the packaged food can be taken out.

In the above description of the present invention, specific embodiments have been described, but various modifications may be made without departing from the scope of the present invention. Therefore, the scope of the present invention should not be determined by the described embodiments, but should be determined by the equivalent of utility model registration claims and utility model registration claims.

As described above, the present invention enables precise package food sterilization, and also has the advantage of performing steam sterilization and drying of packaged food at one place. In addition, it can lower the production cost of packaged food sterilization and improve the quality of sterilized products.

1 is a block diagram of a steam sterilization and drying treatment apparatus according to an embodiment of the present invention,

Figure 2 is a characteristic curve for explaining the temperature increase section, sterilization section, cooling drying section during steam sterilization and drying treatment,

3 is a memory mapping table for opening and closing the proportional control valve in the temperature increase and sterilization section according to an embodiment of the present invention,

Figure 4 is a memory mapping table for opening and closing the proportional control valve in the cooling dry section according to an embodiment of the present invention,

5 is a flowchart illustrating a proportional control valve control in a temperature raising and sterilizing section performed by a control device according to an embodiment of the present invention;

Figure 6 is a flow chart of the proportional control valve control in the cooling drying section performed by the control device according to an embodiment of the present invention.

<Explanation of symbols for the main parts of the drawings>

2 ... treatment tank 4 ... opening and closing door

6 ... steam piping 8 ... compressed air piping

10 ... cooling air piping 12 ... circulation piping

14 ... drain pipe 16 ... main steam pipe

18 ... bypass steam piping 20 ... steam supply

22 ... Blowoff Pipe 60: Cooling Dryer

80 ... control unit 82: memory unit

Claims (3)

By discharging steam and compressed air into the chamber of the processing tank where the packaged food is accommodated, the packaged food is sterilized by maintaining steam at high temperature and high pressure.The steam pipe is injected with steam, the compressed air pipe is injected with compressed air, and condensed water. Install proportional control valves in the drain pipe for removal and the cooling air pipe into which the cooling air generated by the cooling drying device is injected. The first mapping table in which the proportional control valve opening rate is mapped to maintain the saturated steam pressure according to the elevated temperature and sterilization temperature in the elevated temperature and sterilization sections for the temperature increase and sterilization, and the inside of the packaged food according to the cooling drying in the cooling drying section. A memory having a second mapping table in which a proportional control valve opening rate is mapped to maintain the pressure, and the control device is proportional by using the first mapping table and the second mapping table in the temperature rising and sterilizing section and the cooling drying section. Steam sterilization and drying apparatus, characterized in that configured to control the control valve. The steam sterilization and drying apparatus according to claim 1, wherein the temperature range mapped to the first mapping table and the second mapping table is 40 ° C to 130 ° C. The control apparatus of claim 1, wherein the control apparatus first introduces cooling air into the interior chamber of the treatment tank in the cooling drying section and continuously cools the interior chamber temperature to 80 ° C to 90 ° C for about 5 minutes to 1 minute. Steam sterilization and drying treatment apparatus characterized in that the supply of cooling air intermittently every few seconds, to cool slowly to 40 ℃ to 10 ℃ over 5 minutes to 10 minutes.