JP5125224B2 - Grain dryer - Google Patents

Description

  The present invention relates to a grain dryer.

Patent Document 1 discloses a technique for controlling drying by calculating a drying time by setting a drying speed and a moisture speed.
Japanese Patent Application Laid-Open No. 11-30481

  In a large grain dryer, harvested grains from different fields may be stacked and stuck on the same grain dryer. If it becomes so, the water | moisture content of the grain at the time of a harvest may differ greatly depending on a field, and the grain layer of a different water | moisture content will be piled up in a grain dryer. For this reason, when normal drying control is performed, the degree of mixing for each grain layer is insufficient, and the set moisture value may be reached with the degree of variation being large, and drying control may be terminated.

  It is an object of the present invention to measure moisture of each grain layer stacked and stuck in a grain dryer, and to perform drying control for eliminating the variation from the degree of variation of the stretched grain. .

In order to solve the above problems, the present invention has taken the following technical means.
That is, in the invention described in claim 1, the circulating means for circulating the stretched grain from the storage chamber (10) to the storage chamber (10) through the drying chamber (11) and the amount of the stretched grain can be set. The tension grain amount setting means (20), the drying means (4) for drying the grain, the moisture measuring device (9) for taking the sample grain from the tension grain and measuring the moisture, and the control unit ( 41),
During the circulation of the stretched grain with the circulation means, the moisture measuring device (9) measures the moisture value for each set interval corresponding to the number of stretched grains, and the distribution state of the moisture value of the stretched grain And calculating a circulation time necessary to eliminate the variation state of the moisture of the grain from the distribution state of the moisture value, and a necessary drying circulation time calculated from the drying speed (Z) is greater than the circulation time. If it is short , the grain dryer is characterized by controlling the ventilation of the difference.

  In the second aspect of the invention, the ventilation control is started after the initial drying control is performed and the moisture value below the set value is detected, and after the time between the drying circulation time and the circulation time is performed, the drying control is performed. The grain dryer according to claim 1, wherein the grain dryer is returned to the finished moisture value.

  In this invention, the water variation of a different grain layer can be eliminated. Further, when the drying circulation time necessary for drying to the moisture value set at the drying speed (Z) is shorter than the dispersion elimination circulation time (H), the difference in circulation time (v) is ventilated. By controlling, it is possible to dry to a preset moisture value and to eliminate moisture variation in the grain layer.

As one of the best modes for carrying out the present invention, a grain dryer will be described in detail.
The grain dryer includes a multi-stage box 1 that contains grains, and a front side of the box 1 is a combustion burner containing chamber 5 that includes an elevator 2 that raises grain and a combustion burner 4 that generates hot air. And an operation panel 6 provided with various switches for operating the drying operation, and the ceiling side of the box 1 is provided with a transport device 3 for conveying the grains cerealed by the elevator 2 to the inside of the box 1, and the box 1 Is provided with an exhaust fan 7 for sucking hot air in the box 1, and an opening / closing door 19 a for opening and closing a slot 19 for feeding grains is provided on the side of the box 1. The elevator 2 is provided with a moisture meter 9 for detecting the moisture of the grain and a grain outlet 18 for discharging the grain in the box 1 to the outside of the machine. 3 is provided with a dust collecting device 50 that collects dust and other foreign matters mixed in the grain conveyed. The operation panel 6 includes a control unit 41 that controls the drying operation.

In the box 1, a storage chamber 10 is provided in the upper stage, and a drying chamber 11 is provided in the lower stage.
In the upper part of the storage chamber 10, diffusion blades 12 for diffusing the grains transported by the upper spiral 3 a in the transport device 3 into the storage chamber 10, and the tension amount of grains for detecting the amount of grains in the box 1 A detection sensor 20 is provided. The stretched grain amount detection sensor 20 has a configuration in which the weight 20a is suspended and supported by the string 20b. The amount of tension is detected by detecting the tension height position of the tension kernel.

  The drying chamber 11 includes a hot air chamber 13 through which hot air generated by the combustion burner 4 passes, a downflow passage 14 through which grains flow down from the storage chamber 10, and an exhaust air chamber 15 that receives the suction action of the exhaust air fan 7. Is done. Note that the combustion surface 4 a of the combustion burner 4 is configured to face the hot air chamber 13. A rotary valve 16 is provided at the lower end portion of the flow-down passage 14 to feed the grains that have flowed down the flow-down passage 14 by a predetermined amount. A lower portion that conveys the grain fed out by the rotary valve 16 to the elevator 2 below the rotary valve 16. A spiral 17 is provided.

  Explaining the operation panel 6, the operation panel 6 includes an extension switch SW0, a ventilation drying switch SW1, a drying switch SW2, a discharge switch SW3, a stop switch SW4, a liquid crystal display screen h for setting a drying speed, a grain type, and the like.

  Here, the drying rate will be described. The drying rate is slow (drying rate 0.6%), slightly slow (drying rate 0.7%), standard (drying rate 0.8%), fast (drying rate) 0.9%) can be set manually.

  The block diagram of FIG. 3 will be described. Information of various sensors such as the outside air temperature sensor SE1, the hot air temperature sensor SE2, the stretched grain amount detection sensor 20, and the grain temperature sensor SE8 is input to the control unit 41. Then, it is output to the combustion burner 4, moisture meter 9, exhaust fan 7, rotary valve 16 that is a circulation means, lower spiral 17, elevator 2, upper spiral 3 a, and diffusion blade 12.

Next, each process from the grain filling process to the drying process will be described.
When the tension switch SW0 is pressed, the lower spiral 17, the elevator 2, the upper spiral 3a, and the diffusion blade 12 start driving, and the operator opens the open / close door 19a and inputs the harvested grains. The input grains are sequentially conveyed by the lower helix 17, the elevator 2, and the upper helix 3 a and are diffused into the storage chamber 10 by the diffusion blade 12.

When the operator presses the stop switch SW4, the driving of the lower spiral 17, the elevator 2, the upper spiral 3a, and the diffusion blade 12 is stopped, and the sticking process is completed.
When the drying switch SW2 is pressed when starting the drying process, the combustion burner 4 starts combustion, the exhaust fan 7 and the dust collector 50 start driving, and the rotary valve 16, the lower spiral 17, the elevator 2, and the upper part. The spiral 3a and the diffusion blade 12 start driving, and the circulation of the grains is performed. The circulating grain is dried while receiving hot air from the hot air chamber 13 when flowing down the grain flow passage 14 of the drying chamber 11, and is dried to the set moisture while being measured by the moisture meter 9 every set time. It will be done.

Next, details of the drying process from the filling process to the end of the drying process and switching of the display screen h will be described with reference to FIGS. 4 and 5.
When the tensioning process is started, the detection value and the overload value of the load current sensor SE7 of the drive motor of the elevator 2 are displayed in time series (screen A). That is, the presence or absence of the grain clogging of the elevator 2 is detected.

  When the operator presses the stop switch SW4, the stretching process is stopped, and the stretched grain amount detection sensor 20 starts detecting the stretched grain amount. During this time, the standby screen (screen b) is displayed, and when the amount of tension is detected, the amount of tension (3000 kg), the level of tension (LV1 to LV10 in this embodiment), and the amount of tension (this In the embodiment, the remaining 3000 kg) is displayed (screen c).

Then, a setting screen (screen d) for drying conditions such as grain type, amount of filling, moisture setting, drying speed and the like is displayed, and although not described in detail, an operator can touch the screen and set as appropriate.
When the operator presses the tension switch SW0 again, the tensioning process is resumed, and the screen is switched to a standby screen (screen a) during the tensioning operation, and the same order as described above is repeated.

  When the tension amount is detected and input to the control unit 41 by the tension amount detection sensor 20 or a manual tension amount setting switch (not shown), it is in accordance with the tension amount as shown in FIG. The moisture measurement count k is performed for each set time within a circulation time t until the amount of squeezed grain is circulated once after the start of drying. In addition, the time t which circulates once is calculated by the control part 41 from the amount of squeezed kernels, and the moisture measurement is performed every time the circulation time t is equally divided by the number of measurement k. For example, as shown in FIG. 8, when the tension level is LV10 and the grain content is 6000 kg, it takes 48 minutes to circulate once, and the number of measurements is 12 times, that is, moisture is measured every 4 minutes. Is.

  When the drying switch SW2 is pressed, the combustion device 4 starts combustion and the grains start to circulate in the box 1. At that time, the screen displays that the operation is in progress (screen e), and the moisture meter 9 performs moisture measurement for each set time for the set number of times until circulation once after the start of drying. At that time, the screen displays that the moisture measurement at the initial stage of drying is being performed (to the screen).

  In addition, in one water | moisture content measurement, as shown in FIG. 7, 32 grains | grains are measured, and the representative moisture value (m) which is the average moisture value is detected each time. And the dispersion | variation degree of the water | moisture content of 32 grains detected by one water | moisture content measurement is displayed on a screen for every measurement (screen G), and a grain layer (LV1-LV10) will be complete | finished once from the start of drying. ) Display the representative moisture value (m) measured every time (screen h and FIG. 10) to display the moisture distribution state of the grain layer.

Immediately after the start of the drying process, the number of times of moisture measurement can be set according to the amount of squeezed grain, so that the moisture distribution state of the grains in each layer in the whole grain dryer can be properly grasped.
Next, the setting of the circulation time and the drying speed for making the moisture variation uniform from the moisture distribution state of each grain layer in the whole grain dryer will be described below.

  The harvested straw is sequentially put into the grain dryer, and the moisture is measured at set intervals for the number of times corresponding to the amount of stretched grain as described above. That is, each moisture value measured at each set interval is set as a representative moisture value m for each grain layer, and FIG. 11 is a graph of each representative moisture value m and the average moisture value n of the representative moisture values. . Each representative moisture value m, that is, FIG. 11 shows that a grain layer having a moisture content of cocoon of about 23% and a grain layer having a different moisture content of about 17% are embedded.

  The average moisture value n of the representative moisture values of all the grain layers is calculated as 21.7%, and the finished moisture set on the operation panel h is set to 14.0%. In addition, the amount of squeezed grain charged into this grain dryer is 4900 Kg, and the circulation capacity of circulating through the grain dryer is 7.5 ton / h.

  In the graph of FIG. 11, a plurality of lines formed between a straight line e indicating the average moisture value n of the representative moisture values m of all the grain layers and a broken line f connecting the representative moisture values m for each grain layer. The area g of each region is calculated and compared, and the absolute value X of the value indicating the area of the widest region is obtained. In addition, the numerical value described in the representative moisture value m of FIG. 11 has shown the difference with the average moisture value n.

Next, the value X is substituted into the following formula to calculate the circulation count R.
X / 0.01 <AR
This formula is derived from the test, and A is a constant for each grain type, with 1.4 for wheat and 2 for wheat.

When R is calculated from the graph of FIG. 11, it is as follows.
When calculating the area g of consecutive measurement points higher than the average moisture value n of all the representative moisture values,
1.6 × 1 + 3.4 × 1 + 2.3 × 1 + 2.5 × 1 + 3.4 × 1 = 13.2
On the other hand, when calculating the area g of consecutive measurement points lower than the average moisture value n of all representative moisture values,
−2.4 × 1 + −3.1 × 1 + −3.5 × 1 + −3.8 × 1 = −12.8
Then, since the absolute value is larger at 13.2, X = 13.2.

And substituting X = 13.2 into the above equation
13.2 / 0.01 <1.4R
1320 <1.4R
Therefore, in order to make the stretched grain substantially uniform at R = 22, the number of circulations is 22 times.

And, the time H required for the circulation for making the stretched grain substantially uniform in the drying operation is H = the number of circulations × the amount of stretched grain / the circulation capacity, so that H = 22 × 4900/7500.
H≈14.4 is calculated.

  In other words, the variation elimination circulation necessary for uniforming the moisture variation of the stretched grain (the difference between the representative moisture value m and the average moisture value n is within the setting range, within 0.5% in the present embodiment). Time H is 14.4 hours.

Next, the necessary drying speed Z is calculated from the variation elimination circulation time H as shown in the following equation.
Z (% / h) = (average moisture value at the time of grain insertion-finishing moisture value) / dispersion elimination circulation time Z = (21.7-14.0) /14.4≒0.53%/h
That is, a rate of drying water by 0.53% per hour, that is, a drying rate is required.

However, since the grain dryer of the present embodiment has the slowest drying speed of 0.6% / h, the circulation time required to reach the finish moisture value is (21.7-14.0) /0.6≈12.8h. It becomes.

  Therefore, for the extra necessary circulation time v of 14.4h-12.8 = 1.6h, the circulation time is switched to the ventilation time during drying. The timing for switching to the ventilation time is to switch to hot air drying after passing an extra circulation time v (1.6 hours) before starting drying, or to some degree of initial drying and lower than the set moisture (about 18%). If it detects, it will change to ventilation, and if extra circulation time v (1.6 hours) is ventilated, it is good to return to hot air drying by the burner 4, and to dry to a finishing set moisture value.

Next, another graph of stretched grains will be described.
The graph of FIG. 12 shows that a grain layer of about 22% to 23% and a grain layer of about 19% to 20% are alternately stacked. Then, the amount of squeezed kernel is 4900 Kg, and is formed between the straight line e indicating the average moisture value n of the representative moisture values of all the grain layers and the broken line f connecting the measured representative moisture values m as in FIG. Find the maximum area.
Since s is the largest area, X = 2.5.

And substituting
X / 0.01 <AR
R = 17,
H = 17 × 4900/7500
H≈11.1
In other words, the variation elimination circulation necessary for uniforming the moisture variation of the stretched grain (the difference between the representative moisture value m and the average moisture value n is within the setting range, within 0.5% in the present embodiment). Time H is 11.1 hours.

Similarly to the above, the necessary drying speed Z is calculated from the variation elimination circulation time H as shown in the following equation.
Z (% / h) = (average moisture value at the time of grain insertion-finishing moisture value) / dispersion elimination circulation time Z = (21.0-14.0) /11.1≒0.63%/h
That is, the drying control is performed at a drying rate of 0.63%.

  In this case, if the drying rate is set to be slightly slow (drying rate 0.7%), the drying time required to reach the set moisture value is shortened accordingly, so that the extra circulation time v is controlled as described above.

  FIG. 11 shows that the representative moisture value m of adjacent grain layers is continuously higher or lower than the average moisture value n, the area g is relatively wide, and there are two grain layers with relatively thick layers. A relatively long circulation time is required to make the variation uniform accordingly. Moreover, in FIG. 12, the representative moisture value m of the adjacent grain layer is high and low across the average moisture value n, the area g is relatively narrow, and thin grain layers are alternately stacked. In order to make the variation uniform, a relatively short circulation time is sufficient.

  Whether or not the control for equalizing the moisture dispersion condition from the grain moisture distribution state of each layer in the whole grain dryer is to automatically correct the moisture distribution dispersion for each grain layer. It is preferable that a switch for selecting is displayed on the display screen h so that the operator can select it.

  Further, the variation elimination circulation time H is calculated on the assumption that the circulation amount of the circulation means including the rotary valve 16 of the present embodiment is constant, but the desired variation elimination circulation time H is set, It is good also as a structure controlled so that the circulation amount of a circulation means may be changed according to it.

  Moreover, although this Embodiment is a thing which eliminates the dispersion | variation in the water | moisture content of a grain layer by control of a circulation time, the grain layer with a high water | moisture content is detected, and the timing when the grain layer passes the drying chamber 11 is detected. It is good also as a structure which calculates from circulation time and raises the combustion temperature of the combustion burner 4 when the grain layer passes a drying chamber, and makes the dispersion | variation in the water | moisture content for every grain layer uniform.

  After the set number of measurements k is completed and the distribution state of the grain layer is displayed, the moisture value is measured for each set time regardless of the amount of the inset grain, and the degree of variation is displayed for each measurement. The measurement interval time is measured at an interval longer than the measurement interval at the start of drying (for example, every 20 minutes), thereby preventing unnecessary use of many sample grains for moisture measurement and storing moisture measurement data. Data capacity to be reduced.

  Then, during the drying process, that is, the progress of grain moisture reduction and the predicted completion of the drying process are displayed on the screen (screen re). In the screen, a solid line indicates past data and a broken line indicates prediction.

  When the set moisture value is reached, the drying process ends, the moisture variation at the end is displayed on the screen (screen n), and then the onset grain amount detection sensor detects the onset grain amount at the end of the drying process. Start (screen le).

  When the amount of squeezed grain is detected, the time required to circulate once based on FIG. 8 is calculated, and ventilation circulation is performed for a desired number of circulations (for example, one time). For example, when the grain amount at the end of the drying process is LV4, the circulation time of one time is calculated as 24 minutes, and the exhaust fan 7, the rotary valve 16, the lower spiral 17, the elevator 2, the upper spiral 3a, and the diffusion blade 12 are calculated. The circulating means starts driving and performs an air circulation process for 24 minutes, and then automatically stops.

According to this configuration, it is possible to perform a ventilation circulation process suitable for the amount of squeezed kernel to cool the squeezed kernel, and thus it is possible to prevent useless power from being used.
As shown in FIG. 9, the screen during the ventilation circulation process displays a graph in which changes in the cereal temperature and the outside air temperature are time-sequentially displayed. For this reason, it is easy to determine whether the grain temperature is suitable for the hulling operation while performing the ventilation circulation process. That is, when the grain temperature reaches the outside air temperature, the operator can manually stop the ventilation circulation process. Further, when the cereal temperature reaches the outside air temperature, the ventilation circulation process may be automatically stopped even if the set time has not been reached, thereby saving the power consumption.

It should be noted that the ventilation circulation step may be configured so that the operator can set the ventilation time after the drying is finished in advance, not according to the amount of tension.
In the present embodiment, changes in grain temperature and outside air temperature are displayed in time series, but changes in moisture values may be displayed on the same graph.

The figure which shows the inside of the grain dryer seen from the front The figure which shows the inside of the grain dryer seen from the side Operation panel diagram of grain dryer The figure which shows the change of the display screen in the insertion process Diagram showing switching of display screen in drying process Block Diagram The figure which shows the measurement result of the moisture measurement immediately after the start of drying Diagram showing the relationship between the amount of tension, one circulation time, and the number of moisture measurements The figure which shows the change of the grain temperature and the outside temperature in the ventilation circulation process in time series Diagram showing moisture distribution for each grain layer Diagram showing moisture distribution for each grain layer Diagram showing moisture distribution for each grain layer Process chart for calculating circulation time and drying speed

4 Combustion device (combustion burner)
DESCRIPTION OF SYMBOLS 10 Reservoir 11 Drying room 20 Stretched grain amount setting means 9 Moisture measuring device 41 Control part m Representative moisture value for each grain layer n Average moisture value of representative moisture value f Line graph e connecting representative moisture values e Representative moisture The average moisture value of the value g The area formed between the line graph and the straight line graph X The absolute value of the maximum area value H Dispersion elimination circulation time Z Drying speed

Claims (2)

Circulating means for circulating the squeezed kernel from the storage chamber (10) through the drying chamber (11) to the storage chamber (10) again, and an squeezed kernel amount setting means (20) capable of setting the amount of squeezed kernel A drying means (4) for drying the grain, a moisture measuring device (9) for taking the sample grain from the stretched grain and measuring the moisture, and a control unit (41),
During the circulation of the stretched grain with the circulation means, the moisture measuring device (9) measures the moisture value for each set interval corresponding to the number of stretched grains, and the distribution state of the moisture value of the stretched grain And calculating a circulation time necessary to eliminate the variation state of the moisture of the grain from the distribution state of the moisture value, and a necessary drying circulation time calculated from the drying speed (Z) is greater than the circulation time. In the case of a short , a grain dryer characterized by controlling ventilation of the difference time.   Ventilation control starts after the initial drying control is performed and the set moisture value or less is detected, and after the difference between the drying circulation time and the circulation time is performed, the drying control is returned to the finished moisture value. The grain dryer according to claim 1.

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