JPH0422440A - Dust collector of grain corporative drying facilities - Google Patents
Dust collector of grain corporative drying facilitiesInfo
- Publication number
- JPH0422440A JPH0422440A JP12754090A JP12754090A JPH0422440A JP H0422440 A JPH0422440 A JP H0422440A JP 12754090 A JP12754090 A JP 12754090A JP 12754090 A JP12754090 A JP 12754090A JP H0422440 A JPH0422440 A JP H0422440A
- Authority
- JP
- Japan
- Prior art keywords
- grain
- drying
- dust
- processes
- grains
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 239000000428 dust Substances 0.000 title claims abstract description 131
- 238000001035 drying Methods 0.000 title claims abstract description 64
- 238000000034 method Methods 0.000 claims abstract description 58
- 235000013339 cereals Nutrition 0.000 claims description 187
- 241000209094 Oryza Species 0.000 claims description 53
- 235000007164 Oryza sativa Nutrition 0.000 claims description 53
- 235000009566 rice Nutrition 0.000 claims description 53
- 238000005498 polishing Methods 0.000 claims description 37
- 238000000227 grinding Methods 0.000 claims description 29
- 238000003825 pressing Methods 0.000 claims description 13
- 238000003860 storage Methods 0.000 claims description 13
- 230000002079 cooperative effect Effects 0.000 claims 1
- 238000005303 weighing Methods 0.000 description 20
- 235000021329 brown rice Nutrition 0.000 description 15
- 239000010903 husk Substances 0.000 description 8
- 239000002245 particle Substances 0.000 description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- 238000012545 processing Methods 0.000 description 6
- 239000010802 sludge Substances 0.000 description 6
- 238000003756 stirring Methods 0.000 description 6
- 238000004891 communication Methods 0.000 description 4
- 239000012530 fluid Substances 0.000 description 4
- 230000005484 gravity Effects 0.000 description 4
- 239000002994 raw material Substances 0.000 description 4
- 239000004575 stone Substances 0.000 description 4
- 241000209140 Triticum Species 0.000 description 3
- 235000021307 Triticum Nutrition 0.000 description 3
- 238000002485 combustion reaction Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000008187 granular material Substances 0.000 description 3
- 238000004806 packaging method and process Methods 0.000 description 3
- 238000009958 sewing Methods 0.000 description 3
- 238000012546 transfer Methods 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 238000009423 ventilation Methods 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- 239000006061 abrasive grain Substances 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 230000002542 deteriorative effect Effects 0.000 description 1
- 210000005069 ears Anatomy 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000007667 floating Methods 0.000 description 1
- 238000003306 harvesting Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000007602 hot air drying Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 238000010422 painting Methods 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 238000009527 percussion Methods 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 230000009291 secondary effect Effects 0.000 description 1
- 239000010902 straw Substances 0.000 description 1
- 235000020985 whole grains Nutrition 0.000 description 1
Landscapes
- Adjustment And Processing Of Grains (AREA)
Abstract
Description
本発明は、ライスセンタやカントリーニレベタといった
穀物共同乾燥施設に係り、特に、穀物共同乾燥施設の集
塵装置に関する。The present invention relates to a grain communal drying facility such as a rice center or a country elm, and more particularly to a dust collection device for a grain communal drying facility.
従来、米麦等の穀物共同乾燥施設においては、荷受から
出荷までに発生する大量の粉塵を回収するため、粉塵の
発生源となる荷受・粗選、乾燥、籾摺(もみすり)・出
荷等の各工程に設置される種々の処理機器並びにこれら
の機器を連絡するバケッ)・エレベータやフローコンベ
ア等の搬送機器に直接、集塵用のダクトを配管したり、
あるいは、各工程単位に仕切壁て囲繞(いにょう)して
ほぼ気密状の部屋に形成し、この部屋内の粉塵を集中的
にダクトで一箇所又は数箇所に空気輸送して集塵を行っ
ていた。Conventionally, in joint drying facilities for rice, wheat, and other grains, in order to collect large amounts of dust generated from receiving to shipping, the main sources of dust such as receiving, rough sorting, drying, hulling, shipping, etc. Various processing equipment installed in each process as well as buckets that connect these equipment) and transport equipment such as elevators and flow conveyors can be directly connected to dust collection ducts,
Alternatively, each process unit is surrounded by a partition wall to form a nearly airtight room, and the dust in this room is collected by air transporting the dust centrally to one or several locations using ducts. Ta.
ところで、穀物共同乾燥施設で発生する粉塵は、米・麦
の枝梗(しこう)501,601、芒(のげ)502,
602及び、特に米粒の外殻表面(外穎=PALEA)
に無数に存する毛主体であり(第合図及び第合図参照)
、゛これらが微細に砕けた状態で穀粒中に混在し、移送
中、風選時及び熱風乾燥時に舞い上がって周囲に飛散す
る。そのため、前述したように、各機器又は各工程(ユ
ニット)単位で雰囲気と共に集中的にダクト輸送し、屋
外に設置した一箇所又は複数の大型集塵機にて集塵が行
われる。
集塵機としては、サイクロンコレクタ等の乾式のものが
あるが、この種の粉塵は非常に軽量であり、かつ、大風
量であるので空気と分離しにくく、はとんどの施設で湿
式集塵機が用いられているのが現状である。
しかしながら、湿式集塵機であっても、通常用いられて
いるものは、経済的な制約から集塵効率は100%とい
う訳ではなく、 5%程度の粉塵は施設周辺に飛散して
公害問題を発生している。ちなみに、2.000 tク
ラスのカントリーエレベータにおいては、1[」に少な
くとも、約400kgの粉塵(粗ゴミを除く)か発生ず
るので、その内20kg程度のものが飛散することにな
る。
加えて、シャワーよって捕集された粉塵はいつまでも湿
ったままで乾燥せず、時間の経過と共にヘドロ化して焼
却等の処理ができなくなり、時間と費用をかけて山中等
に廃棄するしか方法がない。
また、従来、精選・受渡工程等において、芒や枝梗を除
去するための脱芒機が設置されていたが、このものは、
揺動選別機等によってより分けられた−握りの枝梗や芒
付き粒のみを処理すものであり、全穀粒を対象とするも
のではないし、熱論、集塵を目的とするものでもない。
この発明は以上の点にかんがみ、できるだけ安価で、よ
り完全な集塵を行うことのできる穀物共同乾燥施設の集
塵装置を提供することを技術的課題とする。By the way, the dust generated in the grain drying facility consists of 501,601 rice and wheat branches, 502, 502,
602 and especially the outer shell surface of rice grains (PALEA)
It is mainly composed of hair, which exists in countless numbers (see Figure 1 and Figure 1).
``These are mixed in the grain in a finely crushed state, and are blown up and scattered around during transportation, wind selection, and hot air drying. Therefore, as described above, each device or each process (unit) is intensively transported along with the atmosphere through ducts, and dust is collected using one or more large dust collectors installed outdoors. There are dry type dust collectors such as cyclone collectors, but this type of dust is very lightweight and has a large air volume, so it is difficult to separate it from the air, so wet type dust collectors are used in most facilities. The current situation is that However, even wet dust collectors that are normally used do not have 100% dust collection efficiency due to economic constraints, and about 5% of the dust is scattered around the facility, causing pollution problems. ing. By the way, in a 2,000 t class country elevator, at least about 400 kg of dust (excluding coarse garbage) is generated per 1 ['', so about 20 kg of that dust is scattered. In addition, the dust collected by showers remains wet forever and does not dry out, turning into sludge over time and cannot be incinerated or otherwise disposed of.The only way is to dispose of it in the mountains, which takes time and money. Additionally, in the past, an awn removal machine was installed to remove awns and stems during the selection and delivery process, but this machine
It processes only the handful of stalks and awned grains that have been sorted by a shaking sorter, etc., and is not intended for whole grains, nor is it intended for heat treatment or dust collection. In view of the above points, the technical object of the present invention is to provide a dust collector for a grain communal drying facility that can perform more complete dust collection at the lowest possible cost.
前記課題を解決するため本発明は、荷受・粗選、乾燥及
び籾摺・出荷の各工程からなり、これらの工程で発生す
る粉塵を集塵する装置を備えた穀物共同乾燥施設、すな
わちライスセンタ等において、前記各工程のいずれか一
つ若しくは二つ以上又は任意の工程間に、荷受されたほ
ぼ全穀粒の枝梗・芒・外穎毛等を除去するための研穀機
を設けたものである。
上記研穀機は、荷受・粗選、予備乾燥・貯留、乾燥、サ
イロ貯蔵、精選・売渡及び籾摺・出荷の各工程からなり
、これらの工程で発生する粉塵を集塵する装置をそなえ
た穀物共同乾燥施設、すなわちカントリエレベータにお
いて、上記同様に設けられる。
上記研穀機は少なくとも荷受・粗選、乾燥及び籾摺・出
荷の各工程からなり、これらの工程から発生する粉塵を
集塵する装置を備えた穀物共同乾燥施設、すなわちライ
スセンタ又はカントリエレベータにおいて、前記乾燥工
程以前の工程又は工程間に設けられる。
上記研穀機は、少なくとも荷受・粗選乾燥及び籾摺・出
荷の各工程からなり、これらの工程から発生する粉塵を
集塵する装置を備えた穀物共同乾燥施設、すなわちライ
スセンタ又はカントリエレベータにおいて、前記各工程
にあって送風装置を有する機器の前段に設けられる。
また、上記研穀機には、該研穀機以外で発生する粉塵を
集塵する集塵装置とは別に集塵装置を接続すると効果的
である。
上記研穀機としては、一端を供給部に、他端を排出部に
各々連通ずる多孔壁筒内に研磨転子を回転自在に設け、
これら研磨転子と多孔壁筒との間隙を研磨室に形成する
とよい。
そして、上記研穀機の供給部と排出部とに各々脱稲率検
出器を設けるとともに排出口には可動押圧蓋を装着し、
排出部の脱稲率が供給部のそれに対して一定以上増加し
たとき、前記押圧蓋の押圧度を減ずるよう制御装置を設
ける。
更に、上記研穀機の供給部には湿風発生装置からなる穀
粒加湿装置と、穀物の含水率を検知する水分検知器とを
設けるとともに、この水分検知器によって測定する穀物
の含水率が基準値よりも小さいときは加湿量を大とし、
かつ、基準値よりも大きいときは加湿を中止するよう制
御装置を設ける。
また、上記研穀機の排出口には可動押圧蓋を装着すると
ともに、供給部には穀物の含水率を検知する水分検知器
を設け、この水分検知器によって測定する穀物の含水率
が基準値よりも小さいときは前記押圧蓋の押圧度を減じ
、かつ、基準値よりも大きいときは押圧度を増やすよう
制御装置を設ける。In order to solve the above-mentioned problems, the present invention provides a grain communal drying facility, that is, a rice center, which consists of each process of receiving, rough sorting, drying, hulling, and shipping, and is equipped with a device to collect the dust generated in these processes. etc., a grain grinding machine is installed in any one or more of the above steps, or between any steps, to remove the stalks, awns, glumes, etc. of almost all the grains received. It is something. The above-mentioned grain grinding machine consists of each process of receiving and rough sorting, pre-drying and storage, drying, silo storage, sorting and selling, and hulling and shipping, and is equipped with a device to collect the dust generated during these processes. A similar arrangement is provided in a shared grain drying facility, i.e. a country elevator. The above-mentioned grain grinding machine consists of at least each process of receiving, rough sorting, drying, and hulling/shipping, and is installed in a grain common drying facility, i.e., a rice center or a country elevator, which is equipped with a device to collect the dust generated from these processes. , is provided in a step before the drying step or between the steps. The above-mentioned grain grinding machine consists of at least each process of receiving, rough selection and drying, hulling, and shipping, and is installed in a grain common drying facility, that is, a rice center or a country elevator, which is equipped with a device to collect dust generated from these processes. , is provided in the preceding stage of equipment having an air blower in each of the above steps. Further, it is effective to connect a dust collector to the grain grinding machine, in addition to a dust collector that collects dust generated by a device other than the grain grinder. The above-mentioned grain grinding machine has a grinding trochanter rotatably installed in a perforated wall cylinder whose one end communicates with the supply section and the other end communicates with the discharge section,
It is preferable to form a gap between the polishing trochanter and the porous wall cylinder in the polishing chamber. A rice removal rate detector is provided in each of the supply section and the discharge section of the grain grinder, and a movable pressing lid is attached to the discharge port,
A control device is provided to reduce the degree of pressing of the pressing lid when the removal rate of the rice in the discharge section increases by more than a certain level compared to that in the supply section. Furthermore, the feeding section of the grain grinding machine is equipped with a grain humidifying device consisting of a humid air generator and a moisture detector for detecting the moisture content of the grain, and the moisture content of the grain measured by the moisture detector is If it is smaller than the standard value, increase the humidification amount,
In addition, a control device is provided to stop humidification when the humidity is greater than the reference value. In addition, a movable pressure lid is attached to the outlet of the grain grinder, and a moisture detector is installed in the feed section to detect the moisture content of the grain, and the moisture content of the grain measured by this moisture detector is the standard value. A control device is provided to reduce the degree of pressure of the press lid when the value is smaller than the reference value, and to increase the degree of pressure when it is larger than the reference value.
荷受・粗選、乾燥及び籾摺・出荷の各工程からなるライ
スセンタの各工程のいずれか一つ若しくは二つ以上又は
任意の工程間に設けられた研穀機には荷受されたほぼ全
穀粒が供給され、研穀機の研穀作用によってほとんどの
穀粒外殻の芒・枝梗・外穎毛等が強制的に除去される。
これにより、該研穀機の後工程で発生する粉塵が極めて
少なくなり、最終的に集塵する湿式集塵装置等で処理さ
れる粉塵量が減少し、湿式集塵装置等の集塵効率がたと
え従来と同し95%であったとしても、周囲に飛散する
5%の量は非常に少ないものとなる。
上記同様に、荷受・粗選、予備乾燥・貯留、乾燥、サイ
ロ貯蔵、精選・売渡及び籾摺・出荷の各工程からなるカ
ントリエレベータにおいても、最終的に捕集されず、周
囲に飛散する粉塵量は極めて少量となる。
また、ライスセンタ又はカントリエレベータの乾燥工程
以前に研穀機を設けることによって、粉塵が発生しやす
い乾燥の後工程よりも前の工程において、はとんどの穀
粒の外穎毛・芒・枝梗等を強制的に除去する。
これにより、乾燥されて外殻全体がもろくなり粉塵が発
生しやすい乾燥後工程において、外穎毛・芒・枝梗等が
ほとんど除去されているため粉塵量がわずかとなる。そ
のため、乾燥後工程の集塵用の風量が減少でき、最終的
な湿式集塵装置等も小型化できるとともに、乾式集塵装
置であっても、風量が比較的少ないので粉塵と空気との
分離が行いやすい。
ライスセンタ又はカントリエレベータの各工程の送風装
置を有する機器、例えば粗選機、荷受タンク、乾燥機、
精選工程の風選機及び籾摺機の前段に研穀機を設置し、
穀粒がこれらの機器へ供給される前にほとんどの枝梗・
芒・外穎毛等を強制的に除去する。
これにより、粉塵が大量に発生する、送風装置を備えた
機器の前段、つまり直前において枝梗等を除去するので
、これらの機器から発生する粉塵量が減少し、前述のよ
うに最終的な湿式集塵装置等が小型化できるといった効
果がある。
なお、籾摺機の前段に研穀機を設けた場合は、外穎毛等
が除かれた穀粒(籾)が脱桴ロール間に供給されること
により、ロールの摩耗量が減少する、という二次的な効
果がある。
また、各工程で発生する粉塵を集塵する集塵装置とは別
の集塵装置を研穀機に接続して、濃い含塵風を比較的少
風量により乾式集塵機等で集塵する。
これにより、研穀機で除去された大量の粉塵が、専用の
集塵機で効率的に集塵され、大風量を要する各工程用の
集塵装置の集塵効率が従前と同じであっても、捕集され
ずに飛散する粉塵量が微量となり、結果的に全体として
の集塵効率が向上する。
多孔壁筒と研磨転子との間隙に形成される研磨室内に供
給される穀粒は、回転する研磨転子により撹拌され、粒
子と粒子、粒子と多孔壁筒又は粒子と研磨転子との摩擦
により外穎毛・芒・枝梗等が除去され、これらは多孔壁
筒の孔部から漏出する。
このように、研磨室内の穀粒を研磨転子により撹拌する
ことで、容易に、外穎毛等の粉塵の源を除去することが
できる。
そして、上記研穀機の供給部と排出部とに設けた脱桴率
検出器により、研磨作用を受ける前と後との脱桴率が測
定され、制御装置によって、排出部における脱桴率が供
給部におけるそれよりも一定以上増加したときは、排出
口に設けた可動押圧蓋の押圧度を減ずるように働く。
これにより、脱桴しやすい原料であっても、脱秤粒の発
生事故を未然に防止することできる。
更に、研穀機の供給部に設けた水分検知器により、供給
される原料穀粒の含水率を測定し、この測定値が、あら
かじめ定めた基準値よりも小さいときは、制御装置によ
り、湿風発生装置からなる加湿装置によって穀粒外殻に
対して一定の加湿を行い、前記基準値よりも大きいとき
は加湿を中止するよう働く。
これにより、脱桴しやすい過乾燥ぎみの穀粒に一定量の
加湿を行い、研磨中に脱秤粒が発生するのを防止できる
。
また、上記水分検知器の測定値が、あらかじめ定めた基
準値よりも小さいときは、制御装置により可動押圧蓋の
押圧度を減じ、かつ、前記基準値よりも大きいときは、
同押圧度を増加するよう働く。
これにより、上記同様、脱桴しやすい過乾燥気味の原料
のときは押圧蓋の押圧度を減じて、脱秤粒の発生を防止
し、逆に、脱桴しにくい高水分粒のときは、同押圧度を
増やして外顕毛等をより完全に除去することができる。The grain grinding machine installed in one or more of the processes of the rice center, which consists of receiving, rough sorting, drying, hulling, and shipping, or any process between them, handles almost all the received grain. The grains are fed, and most of the awns, stalks, outer glumes, etc. on the outer shell of the grains are forcibly removed by the grain grinding action of the grain grinder. As a result, the dust generated in the post-process of the grain grinder is extremely reduced, the amount of dust that is finally processed by the wet dust collector, etc., is reduced, and the dust collection efficiency of the wet dust collector, etc. is improved. Even if it were 95% as before, the amount of 5% scattered around would be extremely small. Similarly to the above, in the country elevator, which consists of each process of receiving and rough sorting, pre-drying and storage, drying, silo storage, sorting and selling, and hulling and shipping, waste is not ultimately collected and scattered around. The amount of dust will be extremely small. In addition, by installing a grain grinder before the drying process of the rice center or country elevator, it is possible to remove the outer glumes, awns, and branches of most grains in the process before the drying process where dust is likely to be generated. Forcibly remove stems, etc. As a result, in the post-drying process in which the entire outer shell becomes brittle and dust is likely to be generated, the amount of dust is small because most of the outer glumes, awns, and stems are removed. Therefore, the air volume for dust collection in the post-drying process can be reduced, making it possible to downsize the final wet type dust collector, etc., and even with dry type dust collectors, the air volume is relatively small, making it possible to separate dust from air. is easy to do. Equipment with air blowers for each process of rice centers or country elevators, such as rough sorters, receiving tanks, dryers,
A grain grinder is installed before the wind sorter and huller in the selection process.
Most of the stems and stems are removed before the grain is fed to these machines.
Forcibly remove awns, outer glumes, etc. As a result, branches and stems are removed immediately before, or immediately before, equipment equipped with air blowers, which generates a large amount of dust, reducing the amount of dust generated from these equipment, and as mentioned above, the final wet This has the effect that dust collectors and the like can be downsized. In addition, when a grain grinding machine is installed before the hulling machine, the amount of wear on the rolls is reduced by supplying the grains (husks) from which the outer glumes, etc. have been removed, between the dehulling rolls. There is a secondary effect. Further, a dust collector separate from the dust collector that collects the dust generated in each process is connected to the grain grinder, and the dense dust-containing air is collected by a dry dust collector or the like using a relatively small amount of air. As a result, a large amount of dust removed by the grain grinder can be efficiently collected by a dedicated dust collector, and even if the dust collection efficiency of the dust collector for each process that requires a large air volume is the same as before, The amount of dust that is scattered without being collected becomes very small, and as a result, the overall dust collection efficiency is improved. The grains supplied into the polishing chamber formed in the gap between the porous wall cylinder and the polishing trochanter are agitated by the rotating polishing trochanter, and the grains are mixed between particles, between particles and the porous wall cylinder, or between the particles and the polishing trochanter. External glumes, awns, ramus, etc. are removed by friction, and these leak out from the holes in the porous wall tube. In this way, by stirring the grains in the polishing chamber with the polishing trochanter, sources of dust such as outer glumes can be easily removed. Then, the dehulling rate detectors installed in the supply section and the discharge section of the grain grinder measure the dehulling rate before and after receiving the polishing action, and the control device determines the dehulling rate at the discharge section. When the pressure increases by more than a certain level than that in the supply section, the pressure of the movable pressure lid provided at the discharge port is reduced. Thereby, even if the raw material is easily descaled, accidents such as deweighing can be prevented. Furthermore, a moisture detector installed in the feed section of the grain grinder measures the moisture content of the raw material grains to be fed, and if this measured value is lower than a predetermined reference value, the control device A humidifying device consisting of a wind generator performs a certain amount of humidification on the outer grain shell, and when the humidity exceeds the reference value, the humidification is stopped. Thereby, it is possible to humidify a certain amount of grains that are too dry and easily dehulled, and to prevent the occurrence of descaled grains during polishing. Further, when the measured value of the moisture detector is smaller than a predetermined reference value, the control device reduces the pressure level of the movable pressing lid, and when it is larger than the reference value,
It works to increase the degree of pressure. As a result, as mentioned above, when the raw material is too dry and easily de-hulled, the pressure of the press lid is reduced to prevent the occurrence of de-weighed granules, and conversely, when the raw material has high moisture content that is difficult to de-hull, By increasing the degree of pressure, outer hair, etc. can be removed more completely.
以下、本発明の好適な実施例を図面に基づいて説明する
。第1図において、符号1は荷受ユニットを示し、荷受
ユニット1は粗選機2と、この下方に設けた計量機3と
からなり、更に、張込装置4A、4Bと粗選機2とを連
絡する昇降機5と、計量機3の排出部に連絡する昇降機
6とを立設する。
昇降機6は、昇降機7、フローコンベア8A及び二ロ切
換弁(自動)9A・・・を介して荷受タンクIOA〜I
ODに連絡される。荷受タンク1.0A〜1.0Dには
予備乾燥のための送風機11A〜1. I Dが各々接
続される。荷受タンク10A〜IODは、その下方に横
設した搬送用フローコンベア12A及び昇降機13を介
して研穀機14に連絡される。後で詳述するが、研穀機
14にはファン15を介してサイクロン16を接続する
とともにサイクロン16の排風口にバッグフィルタ17
を装着する。
研穀機14の下方にはタンク18を経て流下式の乾燥機
19本体を設けるとともに、乾燥用の熱風を生成する燃
焼炉20及び送風機21を付設する。乾燥機19の排出
部は、昇降機22及び二ロ切換弁23を介して前記研穀
機14に連絡し、これにより、研穀機14を通過した穀
粒が、乾燥機19を経て再び研穀機14及び乾燥機19
を通過するという循環路が形成される。
前記二ロ切換弁23の他方の排出口は、除塵用の風選機
24及びサイロ群の上方に横設する搬入用フローコンベ
ア25Aを介して、貯蔵用の本サイロ26A〜26Gの
すき間に形成される間隙(げき)サイロ27A〜27C
に各々連絡されるとともに、フローコンベア8Bl’二
ロ切換弁9B・・・を介して前述した荷受タンク10A
〜10Dにも連絡しである。
間隙サイロ27A〜27Cは、連絡用フロコンベア28
A〜28C及び二ロ切換弁29A〜29Cを介して、そ
の下方に横設した搬出用フローコンベア12A、1.2
Bに連絡される。
また、前記搬入用フローコンベア25Aは本サイロ26
A〜26Gにも連絡され、本サイロ266A〜26Gの
下端は、適宜に連絡用フロコンベア28A〜28D及び
二ロ切換弁29A〜29Gを介して排出用フローコンベ
ア12A及び同12Bに接続される。
前記一方の搬出用フローコンベア12Aは、前述したよ
うに、昇降機13を経て乾燥機19へ至る乾燥工程に連
絡され、他方の搬出用フロヘーコンベア12Bは精選・
籾摺ユニット30に連絡される。すなわち、搬出用フロ
ーコンベア12Bと接続する昇降機31は、二ロ切換弁
32.33を介して風選機34に連絡された後、昇降機
35を経て揺動選別機36に連絡される。
揺動選別機36の目的は、精選工程において脱秤(ぶ)
粒を除去すること並びに籾摺工程において籾と玄米とを
選別することにあり、傾斜した選別板の傾斜上位側排出
口は玄米用コンベア37に、下位側排出口は籾用コンベ
ア38に、その中間の排出口は混合米用コンベア39に
、各々連絡される。そして、玄米用コンベア37は昇降
機40を介して、回転する多角筒選別網からなる粒選別
機41Aに連絡され、粒選別機41Aの漏出側排出口は
、二ロ切換弁42、未熟粒受箱43及び昇降機44を介
して壷(つぼ)穴式回転選別機45に連絡され、更に、
壷穴式回転選別機45は脱秤粒受箱46と昇降機47と
に接続され、昇降機47は、二ロ切換弁48、昇降機4
9、計量機50、昇降機51、二ロ切換弁52及び昇降
機53を介して搬入用フロコンベア25Bに連絡され、
脱秤粒と分離した籾を本サイロ26A〜26Gに戻すよ
う形成される。他方、粒選別機4]Aの選別筒排出部は
、二ロ切換弁60、昇降機47、二ロ切換弁48、昇降
機49及び計量機50等を介し、前述同様に本サイ26
A〜26Gに戻るよう形成される。
なお、揺動選別機36下方の籾用コンベア38は、従来
、芒や枝梗が付いたいわゆる枝梗粒用として用いられた
ものであり、ゲ?降機54及び二L1切換弁55.56
を介して脱芒機57に連絡され、脱芒機57は、更に、
昇降機31、二ロ切換弁32及び昇降機53を介して搬
入用フローコンベア25Bに連絡され、芒を除去した穀
粒を本サイロ26A〜26Gに戻ずよう形成しであるが
、本実施においては研穀機14により、枝梗粒等は全く
といっていいほど存在しないので、このラインは実質的
に不要となる。
籾摺機80の排出部と連結する混合米用コンベア39は
、昇降機47、二ロ切換弁48、昇降機49、計量機5
0、昇降機51、二]」切換弁52及び昇降機53を介
して搬入用フローコンベア25Bに連絡され、整粒を本
サイロ26A〜26G内に戻すよう形成される。前記籾
摺機80はニロ切換弁79.52及び昇降機51を介し
て計量機50に連絡しである。
そして、一方の排出口を脱芒機57へ連絡する二ロ切換
弁56の他方の排出口は、小型の脱桴・選別装置58か
らなる異種穀粒選別ユニット59に連絡される。
次に、出荷工程について説明する。玄米用コンベア37
は、昇降機40、粒選別機41A。
41B及び二ロ切換弁42.60を介して石抜選穀機6
1に連絡され、石抜選穀機61の排出部は、昇降機62
、計量機63、昇降機64及び二ロ切換弁65を介して
バラ出荷タンク66又はフレコン67に投入するよう形
成される。
更に、バラ出荷タンク66の排出口は、小袋包装のため
の計量包装機68及びミシン69と、昇降機70及び二
ロ切換弁71を介してトラックバースの穀物移送車72
とに連絡される。
次に、集塵用のダクト配管について説明する。
建屋外には、供給ロア2、吐出ロア4及びシャワー用の
ノズル75を備えるとともに、その下方に水洗槽76と
スラッジコンベア77とを設けてなる湿式集塵装置78
が設置される。そして、供給ロア3には、図中○付符号
及び点線で示すように、系統的にダクト配管がなされる
。
すなわち、ダクト■は、荷受ユニット1全体と張込装置
4A、4Bとを45m’/minの風量とし、荷受ユニ
ット1の粗選機2はダクト■によって風量1ftom’
/winとする。異種穀粒選別ユニット59の風選部は
風量40m’/minのダクト■に、荷受タンク10A
〜10Dは風量120 m’ /ffl i n (D
ダクト■に、計量機50、昇降機51及び異種穀粒選別
ユニット59のタンクは風量150m’/minのダク
ト■に、本サイロ26A〜26G1搬入用フローコンベ
ア25A、25B、荷受タンク10A〜IOD用のフロ
ーコンベア8A、8B。
昇降機7,31.53及び風選機34のタンクは風量8
0m’/minのダクト■に、風選機34の一対の風道
は風量120m’/minのダクト■に、搬入用フロー
コンベア25Aの前工程の風選機24は風ff1HIT
l’/+ninのダクト■に、搬出用フローコンベア1
2A、12B及び連絡用フローコンベア28A 〜28
Dは風量36m’/minのダクト■に、出荷工程の計
量機63及び昇降機64.70は風量30m’/min
のダクト0に、乾燥工程の乾燥機19、タンク18及び
昇降機13.22は風量85m’/minのダクト0に
、籾摺機80は風量16m3/ff+inのダクトOに
よって籾殻庫81に接続するとともに同じ<16m’/
minのダクト■に、並びに精選・籾摺ユニット30全
体は風量200m’/minのダクト■に各々連結し、
各ダクトの終端は湿式集塵装置78の供給ロア3に接続
される。以上は、乾燥工程の乾燥機14の前段に研穀機
14を設置した場合の実施例である。
以下、第2図に示す撹拌式の研穀機14Aについて説明
する。一端を開口した中空主軸134を多孔壁除塵筒1
33内に回転自在に軸支するとともに、中空主軸334
には送穀転子144と研磨転子137とを軸着する。多
孔壁除塵筒133は穀粒が漏出しない程度の多数の孔部
を有する多孔板からなる円筒又は多角筒であり、送穀転
子144には送穀用の螺旋を形成し、また、研磨転子1
37は中空状となして、中空主軸134に設けた通風孔
138と連通させ、更に、周面には一つ又は複数の撹拌
突起135を長平方向に突設するとともに、撹拌突起1
35に沿って噴風孔136を形成し、研磨転子137と
多孔壁除塵筒133との間を研磨室139となす。そし
て、送穀転子144側に供給口140を、研磨転子13
7終端部に排出口141を、各々形成するとともに、供
給口140に接続して供給ホッパ132を設け、他方、
排出口]、 4 ]に接続して排出樋160を設けると
ともに、排出口141には押圧蓋調節装置142によっ
て押圧度を調節可能な押圧蓋143が装着される。押圧
蓋調節装置142としては、例えば、特公平1−277
76号で開示されるように(第5図参照)、ケース16
3内に、螺軸164及び回り止め167によって横移動
可能に分銅165を装着するとともに、前記螺軸164
は制御装置161(第4図参照)に接続された正逆回転
モータ162に直結して形成したものがある。
制御装置161は入出力信号処理装置161a1記憶装
置161b及び演算装置161Cからなり、入出力信号
処理装置161aには、供給ホッパ132又はその下方
の漏斗部に装着した水分検知器166が接続される。水
分検知器166としては、例えば、電気抵抗式や静電容
量式等が適宜に採用される。
多孔壁除糠筒133の周囲には、はぼ気密に集塵室14
5を形成し、その下部を集塵ホッパ146となす。集塵
ホッパ146の下端は、ダクト147によってファン1
5の給気口に連結され、ファン15の吐出口はダクト1
48によってサイクロン16に連結しである。
更に、穀粒加湿装置として、中空主軸134の開口端に
望ませて二流体ノズル149を設け、二流体ノズル14
9の供給側の一方は、送水管157、電磁弁153、流
量計154及び流量調節弁155を介して水タンク15
6に接続し、他方は、送風管150及びエアフィルタ1
51を介して空気圧縮機152に接続しである。また、
前記流量調節弁155は制御装置161に接続され、前
記水分検知器166の検出値が、記憶装置161bにあ
らかじめ設定された基準水分値、例えば22〜24%よ
り大きいときは流量を0として風だけ送り、22%未満
のときは120%の流量とするよう制御され、これに加
えて、押圧蓋調節装置142を連動して制御するよう形
成しである。すなわち、前記基準値を超えたときは押圧
度を120%とし、これに満たないときは80%の押圧
度となるようモータ162及び螺軸164によって分銅
165を横移動させる。
以下、上記実施例における具体的作動について説明する
。張込装置4A又は4Bに投入された穀粒(生籾)は、
昇降機5を介して粗選機2に供給されて切れ穂やわらく
ず等の比較的太きい夾雑物(粗ゴミ)はゴミ容器2Aに
、未熟粒は未熟粒受箱2Bにそれぞれ選別されて収容さ
れる。夾雑物や未熟籾粒が除去された籾は、計量機3に
供給されて計量された後、昇降機6゜7及びフローコン
ベア8Aを経て搬送されるとともに、二ロ切換弁9A・
・・によって適当な荷受タンクIOA〜IOD内に投入
される。
荷受タンクIOA〜IOD内に一時貯留される籾は、送
風機11A〜11Dによる通風を受けて変質を防いでい
る。荷受タンク1.0A〜10Dに籾が適当量張込まれ
ると、順次、排出口から搬出用フローコンベア12A上
に流出し、昇降機13を経て研米機14Aに至る。
研米機14Aにおいては(第2図参照)、供給ホッパ1
32内に投入される生籾の含水率を水分検知器166で
検出しながら、送穀転子144によって研磨室139に
送り込む。押圧蓋143による抵抗を受けて研磨室13
9内は適度な圧力となり、研磨転子137の撹拌突起1
35による撹拌作用を受けて、籾粒どうしあるいは籾粒
と多孔壁除塵筒33との摩擦力等を生じ、籾粒表面の外
穎毛及び芒が除去される。このとき、水分検知器166
の検出値が、基準となる水分値22〜24%よりも大き
い、例えば30%の場合は、流量調節弁155を閉して
送風だけとなすとともに、押圧蓋調節装置142の押圧
度を120%又は比例的に増加させて外穎毛等の除去を
効果的に行う。逆に、前記検出値が基準値未満の場合は
、脱秤粒を発生させないように、加湿量を120%増と
し、かつ押圧度を80%とする。なお、この際の加湿量
は、あくまでも穀粒外殻を湿らす程度であり、胚乳部へ
浸透すべきものではない。また、水分に関連して押圧度
又は加湿量のいずれか一方のみによる制御を行ってもよ
い。
こうして、研磨室]39内への送風により籾粒外殻から
容易に離脱した外穎毛や芒等は、多孔壁除塵筒133の
多孔部から漏出し、ファン15の吸引力によって集塵ホ
ッパ146内に落下するとともに、濃い含塵風としてダ
クト148を経てサイクロン16に至る。ファン15の
風量は比較的少風量であるので、粉塵は容易に空気と分
離され、外穎毛や芒は下方へ落下してゴミ収集箱等に収
容され、空気は吐出口から上方へ排出される。なお、こ
の排風中にわずかに含まれる粉塵は、バッグフィルタ1
7によって捕集される。また、ある程度以上に乾燥した
籾の表面に加湿を行うことにより、外穎毛が比較的重く
なり、空気との分離が行いやすい。
研穀機14Aを通過した籾は乾燥機19内を流下し、燃
焼炉20及び送風機21による熱風を浴びて表面の籾殻
の水分を奪われる。このとき、研磨機14Aによって外
穎毛や芒を除去された籾は、熱風を受けても粉塵が比較
的少なく、ダクト0を介して湿式集塵装置78へ輸送さ
れる粉塵量も極めて少ない。乾燥機19を通過して籾殻
がある程度乾燥した籾は、昇降機22及び搬入用フロー
コンベア25Aによって空いている間隙サイロ27A〜
27C内に投入される。
この間隙サイロ27A〜27C内で数時間放置される間
に、玄米の水分が籾殻に移行して平衡化しく調質)、こ
の時点で排出口から流出して再び研穀機14Aを経て乾
燥機19に投入して乾燥作用を施され、乾燥機19を通
過した籾は間隙サイロ27A〜27Cへ搬送される、と
いう工程を複数回繰り返す。そして、荷受ユニット1、
荷受タンクIOA〜IOD及び各搬送工程においてもそ
うであったように、タンク18や乾燥機19において発
生する粉塵は、各ダクトを経て湿式集塵装置78へ送ら
れ、ノズル75からのシャワーによって水洗槽76内に
落下し、スラッジコンベア77によって回収されるので
あるが、乾燥機19に至る籾は、乾燥されるたびに何度
も研穀機14Aを通過して強制的に外穎・芒・枝梗等を
除去するので、各ダクトから湿式集塵装置78に送られ
る粉塵は非常に減少する。そのため、スラッジコンベア
77によって回収されるヘドロ状の粉塵の量は極めて少
なく、容易に処理が可能であるとともに、捕集できずに
周囲に飛散する粉塵量が微量となる。
こうして乾燥を行い、籾が変質しない水分、例えば18
%に至った時点で本サイロ26A〜26G内に投入され
、収穫期の荷受期間が終了するまで貯蔵される。そして
、荷受期間が終了すると、各本サイロ26A〜26G内
の籾は順次排出され、再び、研穀機14Aを通過して乾
燥機19による乾燥作用及び間隙サイロ27A〜27C
による調質作用を繰り返し受けて、例えば、16%にな
るまで乾燥される。このときは、籾の乾燥がある程度進
んでいるので、二流体ノズル149からの湿風が研穀機
1.4 Aの研磨作用及びサイクロン16における分級
作用に有効に働く。
乾燥が終了すると、仕上がった籾は精選工程を経て政府
に売り渡されることになる。すなわち、必要とする籾の
入った本サイロ26A〜26Gの排出口から流出する籾
は、二ロ切換弁29へ〜29G1搬出用フローコンベア
12B1昇降機31及びニロ切換弁32.33を介して
風選機34に供給されて風選された後、訪中に含まれる
脱秤粒(玄米)を除去するため、昇降機35を介して揺
動選別機36に供給される。
揺動選別機35の供給ホッパーに投入された籾は、揺動
作用を受け、比較的比重の大きい脱秤粒は選別盤の粗雑
面によって傾斜上位側へ揺り寄せられ、比較的比重の小
さい枝梗粒は脱秤粒及び籾の上方に浮上しながら傾斜下
位側へ偏流し、大部分を占める籾はこれらの中間部を流
れる層を成す。そして、脱秤粒層は籾・玄米用コンベア
37へ落下し、昇降機40を介して粒選別機41Aに投
入され、脱秤粒のみが選別筒から漏出して二ロ切換弁4
2を介して未熟粒受箱43内に収容され、他方、脱秤粒
以外の籾は、昇降機47等を介して再び揺動選別機36
へ戻される。この脱秤粒は、籾で政府に売り渡す際不要
なものであり、しかも何度も乾燥機19を通過して胴割
れ等の傷害を受けているので廃棄処分される。
なお、研穀機14Aにより、枝梗粒はほとんどないが、
万一、枝梗粒が存在する場合は、傾斜下位側から籾摺コ
ンベア38内に落下し、昇降機54等を介して脱芒機5
7に供給して枝梗を除去した後、昇降機31.53等を
介し、製品として本サイロ26A〜26Gに還元される
ことになる。
一方、脱秤粒や枝梗粒に比べて大量の整籾は混合米用コ
ンベア39上に落下し、昇降機4749を経て計量機5
0で計量された後、昇降機51及び搬入用フローコンベ
ア25Bを介し、政府売渡し米として本サイロ26A〜
26Gに封印して貯蔵されることになる。なお、この精
選工程においても、各機器及び搬送機からダクトを介し
て湿式集塵装置78で集塵が行われるが、乾燥工程で何
度も研穀機14Aを通過しているので粉塵の発生は極め
て少ない。
このようにして本サイロ26A〜26G内に貯蔵された
籾を、次に、籾摺工程を経て出荷する際は、本サイロ2
6A〜26G内の政府光渡米を搬出用フローコンベア1
2B及び昇降機31を介して計量機50に供給して計量
した後、昇降機51等を介して籾摺機80に供給する。
籾摺機80の脱桴ロールによって80〜90%が脱桴さ
れた摺米(混合粒)は、混合米層コンベア39、昇降機
47及び二ロ切換弁48を介して揺動選別機36の供給
タンクに投入される。そして、均分器及び供給樋によっ
て各選別盤に均等に供給され、摺米中の籾を除き、玄米
のみを抽出する。すなわち、揺動する選別盤上に供給さ
れた摺米中、比較的比重の大きい玄米は粗雑面との接触
によって傾斜上位側へ揺り上げられ、比較的比重の小さ
い籾は玄米の上を滑流して傾斜下位側へ偏流し、その中
間部には玄米と籾との混合米が層を成す。これにより、
傾斜下位側の籾は、籾摺コンベア38及び昇降機54を
介して還流し、再び籾摺機80において脱桴される。ま
た、混合米層コンベア39内に落下する混合米は、摺米
と合流して再び揺動選別機36に還流して選別される。
この籾摺工程においては、何度も研穀機14Aを通過し
て外穎毛等が除去された籾が脱桴ロールによって脱桴さ
れるので、脱桴クールの摩耗量が半減し、交換等の手間
が減るとともに経済的である。また、脱桴直後の摺米の
風選においても、籾殻以外の粉塵量が減少する。
一方、玄米用コンベア37内の玄米は、昇降機40を経
て粒選別機41A、41Bに供給されて粒厚選別され、
−室以上の粒厚を有する整粒は、石抜選穀機61を通し
て石が除去された後、昇降機62を介して計量機63で
計量し、フレコンバッグ67詰めするか又はバラ出荷タ
ンク66を経て計量機68で計量し、ミシン69による
袋口の縫製を行って小口包装するか若しくは穀物移送車
72によってバラ出荷される。
なお、以上の各工程においても、穀粒が通過する各処理
機器若しくは計量機又は搬送機で発生する粉塵は(研穀
機14Aによってその量は少ないカリ、それぞれのダク
トを介して湿式集塵装置78に回収されるのは言うまで
もない。
次に、研穀機14の別の実施例を第3図に基づいて説明
する。研穀機14Bは先の実施例の研穀機14Aとほぼ
同様であるが、研磨転子J20が、砥石等からなる研削
式のものである点が異なり、その他、湿風生成用の水タ
ンク等を備えていない。以下、詳述するに、円筒形の多
孔壁除塵筒118内に、一端を開口した中空主軸119
に軸着された送穀転子127と研削式の研磨転子120
とを回転自在に設け、送穀転子127側端部には供給口
122を、その他端には排出口123を設け、供給口1
22に接続して供給ホッパ]24を、排出n J、 2
3に接続して排出樋110を各々設けるとともに、排出
口123には、先の実施例と同様に、押圧蓋調節装置1
25で押圧度を調節可能とした押圧蓋126を装着する
とともに、供給ホッパ124及び排出樋110付近には
制御装置113(第4図参照)を介して押圧蓋調節装置
125のモータ114に連絡する脱桴率検出器11.1
..]12を各々設ける。また、多孔壁除塵筒11−8
の周囲には柴塵室128を形成するとともに、集塵室1
28に接続して集塵ホッパ129を設け、集塵ホッパ1
29下端はダクト130によって送風機15の入口に連
結されている。更に、中空主軸】19の開口端には絵風
装置として送風機115の吐出口を臨ませ、研磨転子1
20の噴風孔116から研磨室121内の穀粒に送風す
るよう形成される。
このように形成した場合は、回転する研磨転子120の
表面砥粒によって、籾殻の外穎毛・芒・枝梗等が削り取
られるように作用する。そして、外穎毛等は送風機11
5からの風によって容易に外殻から離脱して多孔壁除糠
筒118から漏出し、濃い含塵風となってサイクロン1
6に送られ、先の実施例と同様に、空気と分離されて回
収されるのであるが、排風中の粉塵はバッグフィルタ1
7で回収するか、又はダクトにより湿式集塵装置78に
連結してもよい。この際回収される塵は微かであり、従
来のように大量なヘドロと化すことはない。なお、前記
送風機115は、研磨室121内の籾の温度上昇を抑え
るようにも働く。
また、研穀機14Bに供給されるとき及び排出樋160
を落下するときに、脱稲率検出器111、.112によ
って訪中の脱秤粒の混入率が測定される。こうして、各
脱稲率検出器111゜112が一定時間おきに検出する
測定値は、それぞれ制御装置161の入力信号処理装置
161aを経て−たん記憶装置(RAM) 16 l
bに記憶されるとともに演算装置161Cによって平均
化して比較され、両者の脱稲率の平均値の差又は比率が
、あらかじめ記憶装置161bに設定した基準値、例え
ば1.0%の差よりも大きくなった時点で、押圧蓋調節
装置142のモータ162を正又は逆転させることによ
り、前記1.0%の差内となるまで分銅165を押圧蓋
143側へ段階的に横移動させ、押圧蓋143の付勢力
を減じて脱秤粒の大量発生による事故を防止し、安全装
置として働く。
以上、研磨転子として、撹拌式のものと研削式のものに
ついて述べたが、穀粒外殻の研磨を行えるものであれば
よく、その他、ブラシ式(第6図参照)、スクリュー式
(第7図参照)、打撃式(第8図参照)等が用いられる
。
また、上記実施例は研穀機14A、Bをいずれも、乾燥
工程の乾燥機の前段に配置した場合について説明したた
か、第9図に示すように、荷受・粗選工程の粗選機2の
前段に研穀機14Cを、荷受・粗選工程と予備乾燥・貯
留工程との間に研穀機14Dを、各々設けることにより
、乾燥前、少なくとも乾燥完了(約16%)前の穀粒の
外穎毛・芒・枝梗等を除去することになり、穀粒の加湿
をさ程行わなくても脱秤粒が発生する危険が少なく、更
に、乾燥が進み、外穎毛等が離脱して粉塵が発生しやす
くなる前の段階において、強制的にこれらを除去するこ
とができ、当該研穀機の後工程での粉塵発生量が非常に
少なくなり、系統的な集塵装置、例えば湿式集塵装置を
大幅に小型化(安価)できて、未捕集粉塵量も微量とな
る効果がある。
他方、前記研穀機14A−Dとは別に又はこれらに併せ
て、精選・売渡工程に研穀機14Eを、籾摺・出荷工程
に研穀機14Fを各々設けてもよい。特に、前述したよ
うに、精選工程の風選機34や籾摺工程の籾摺機80等
、つまり、送風機を備えた機器の前段に設置することに
より、従来、これらの機器で大量に発生していた粉塵を
減らすことができる。
なお、前記研穀機14A−Fは1台とは限らず、各設置
場所における流量に合致するよう、適宜な台数を並設す
るが、ある程度流量を調節可能な場所、例えば荷受・粗
選工程から荷受タンク群へ至るライン上等に設けること
により、全体として処理能力に影響を及ぼすこがない。Hereinafter, preferred embodiments of the present invention will be described based on the drawings. In FIG. 1, reference numeral 1 indicates a cargo receiving unit, and the cargo receiving unit 1 consists of a rough sorter 2 and a weighing machine 3 provided below this, and further includes tensioning devices 4A, 4B and a rough sorter 2. A communicating elevator 5 and an elevator 6 communicating with the discharge section of the weighing machine 3 are installed upright. The elevator 6 connects cargo receiving tanks IOA to I via an elevator 7, a flow conveyor 8A, and a two-way switching valve (automatic) 9A.
OD will be contacted. The receiving tanks 1.0A to 1.0D are equipped with blowers 11A to 1.0D for preliminary drying. IDs are connected to each other. The receiving tanks 10A to IOD are connected to a grain grinding machine 14 via a transport flow conveyor 12A and an elevator 13 installed horizontally below the receiving tanks 10A to IOD. As will be detailed later, a cyclone 16 is connected to the grain grinder 14 via a fan 15, and a bag filter 17 is connected to the exhaust port of the cyclone 16.
Attach. Below the grain grinder 14, a downstream type dryer 19 body is provided via a tank 18, and a combustion furnace 20 and a blower 21 for generating hot air for drying are also provided. The discharge section of the dryer 19 is connected to the grain grinder 14 via the elevator 22 and the two-way switching valve 23, so that the grains that have passed through the grain grinder 14 are sent through the dryer 19 and ground again. Machine 14 and dryer 19
A circulation path is formed that passes through the The other outlet of the two-way switching valve 23 is formed in the gap between the main silos 26A to 26G for storage via a wind separator 24 for dust removal and a flow conveyor 25A for carrying in horizontally installed above the silo group. Gap silos 27A to 27C
and the above-mentioned receiving tank 10A via the flow conveyor 8Bl' two-way switching valve 9B...
I have also contacted ~10D. The gap silos 27A to 27C are connected to the communication flow conveyor 28.
A to 28C and two-way switching valves 29A to 29C are connected to the flow conveyors 12A and 1.2 for carrying out horizontally installed below the switching valves 29A to 29C.
B will be contacted. In addition, the flow conveyor 25A for carrying in is the main silo 26.
A to 26G are also connected, and the lower ends of the main silos 266A to 26G are connected to discharge flow conveyors 12A and 12B via communication flow conveyors 28A to 28D and two-way switching valves 29A to 29G as appropriate. As mentioned above, one of the flow conveyors 12A for carrying out is connected to the drying process which leads to the dryer 19 via the elevator 13, and the other flow conveyor 12B for carrying out is connected to the drying process that leads to the dryer 19 through the elevator 13.
The rice hulling unit 30 is contacted. That is, the elevator 31 connected to the discharge flow conveyor 12B is connected to the wind sorter 34 via the two-way switching valve 32, 33, and then to the swing sorter 36 via the elevator 35. The purpose of the oscillating sorter 36 is to remove scales during the sorting process.
The purpose is to remove grains and to sort paddy and brown rice in the hulling process, and the inclined upper side discharge port of the inclined sorting board is connected to the brown rice conveyor 37, and the lower side discharge port is connected to the paddy conveyor 38. The intermediate outlets are each connected to a conveyor 39 for mixed rice. The brown rice conveyor 37 is connected via an elevator 40 to a grain sorter 41A consisting of a rotating polygonal tube sorting net. 43 and an elevator 44 to a pot hole type rotary sorter 45, and further,
The pot-and-hole rotary sorter 45 is connected to a de-scaled granule receiving box 46 and an elevator 47, and the elevator 47 is connected to a two-way switching valve 48 and an elevator 4.
9. Connected to the loading flow conveyor 25B via the weighing machine 50, the elevator 51, the two-way switching valve 52, and the elevator 53,
The silos are formed to return the unscaled grains and separated paddy to the main silos 26A to 26G. On the other hand, the sorting cylinder discharge section of the grain sorter 4]A is connected to the main size 26 via the two-way switching valve 60, the elevator 47, the two-way switching valve 48, the elevator 49, the weighing machine 50, etc.
It is formed so as to return to A to 26G. The conveyor 38 for paddy below the oscillating sorter 36 has conventionally been used for so-called husk grains with awns and husk. Disembarkation 54 and two L1 switching valves 55.56
is connected to the awn removal machine 57 via the awn removal machine 57, and the awn removal machine 57 further includes:
It is connected to the flow conveyor 25B for carrying in via the elevator 31, the two-way switching valve 32, and the elevator 53, and is designed to prevent the grains from which awns have been removed from returning to the main silos 26A to 26G. Because of the grain machine 14, there are almost no branch grains, etc., so this line is virtually unnecessary. The mixed rice conveyor 39 connected to the discharge part of the huller 80 includes an elevator 47, a two-way switching valve 48, an elevator 49, and a weighing machine 5.
0, Elevator 51, 2] It is connected to the carry-in flow conveyor 25B via the switching valve 52 and the elevator 53, and is configured to return the sorted particles into the main silos 26A to 26G. The huller 80 is connected to the weighing machine 50 via the Niro switching valve 79, 52 and the elevator 51. The other outlet of the two-way switching valve 56, which connects one outlet to the dehulling machine 57, is connected to a different kind of grain sorting unit 59 consisting of a small dehulling and sorting device 58. Next, the shipping process will be explained. Brown rice conveyor 37
is an elevator 40 and a grain sorter 41A. 41B and two-way switching valve 42.60 to remove stone grain sorter 6
1, and the discharge section of the grain sorting machine 61 is connected to the elevator 62.
, a weighing machine 63, an elevator 64, and a two-way switching valve 65 so as to be fed into a bulk shipping tank 66 or a flexible container 67. Furthermore, the discharge port of the bulk shipping tank 66 is connected to a weighing and packaging machine 68 for packaging small bags, a sewing machine 69, an elevator 70, and a two-way switching valve 71 to a grain transfer vehicle 72 on a truck berth.
will be contacted. Next, the duct piping for dust collection will be explained. Outside the building, there is a wet dust collector 78 which is equipped with a supply lower 2, a discharge lower 4, and a shower nozzle 75, and below which a water washing tank 76 and a sludge conveyor 77 are provided.
will be installed. Further, the supply lower 3 is systematically provided with duct piping, as shown by the symbols with circles and dotted lines in the figure. In other words, the duct ■ allows the entire receiving unit 1 and the tensioning devices 4A, 4B to have an air volume of 45 m'/min, and the coarse sorter 2 of the receiving unit 1 has an air volume of 1 ftom' through the duct ■.
/Win. The wind sorting section of the different grain sorting unit 59 is connected to a duct ■ with an air volume of 40 m'/min, and a receiving tank 10A.
~10D is an air volume of 120 m'/fflin (D
The tanks for the weighing machine 50, the elevator 51, and the different grain sorting unit 59 are connected to the duct ■, which has an air volume of 150 m'/min, and the flow conveyors 25A and 25B for carrying in the main silos 26A to 26G1, and the receiving tanks 10A to IOD are connected to the duct ■. Flow conveyor 8A, 8B. The tanks of elevators 7, 31.53 and wind selector 34 have an air volume of 8
The pair of air passages of the wind selector 34 are connected to the duct ■ with an air volume of 120 m'/min, and the wind selector 24 in the front process of the flow conveyor 25A for carrying in is connected to the wind ff1HIT.
Flow conveyor 1 for carrying out is installed in the duct ■ of l'/+nin.
2A, 12B and communication flow conveyor 28A to 28
D is a duct ■ with an air volume of 36 m'/min, and the weighing machine 63 and elevator 64.70 in the shipping process have an air volume of 30 m'/min.
The dryer 19, tank 18 and elevator 13.22 in the drying process are connected to the duct 0 with an air volume of 85 m'/min, and the huller 80 is connected to the rice husk storage 81 through the duct O with an air volume of 16 m3/ff+in. Same <16m'/
The duct ■ with an air flow rate of 200 m'/min, and the entire selection/hulling unit 30 are connected to the duct ■ with an air volume of 200 m'/min.
The terminal end of each duct is connected to the supply lower 3 of the wet dust collector 78. The above is an example in which the grain grinder 14 is installed before the dryer 14 in the drying process. The stirring type grain grinder 14A shown in FIG. 2 will be described below. The hollow main shaft 134 with one end open is connected to the porous wall dust removal tube 1.
33, and a hollow main shaft 334.
A grain feeding trochanter 144 and a polishing trochanter 137 are attached to the shaft. The porous wall dust removal cylinder 133 is a cylinder or a polygonal cylinder made of a perforated plate having a large number of holes to prevent grains from leaking out. Child 1
37 is hollow and communicates with a ventilation hole 138 provided in the hollow main shaft 134. Furthermore, one or more stirring protrusions 135 are provided on the circumferential surface protruding in the elongated direction, and the stirring protrusion 1
A blow hole 136 is formed along 35, and a polishing chamber 139 is formed between the polishing rotor 137 and the porous wall dust removal cylinder 133. Then, a supply port 140 is provided on the side of the grain feeder 144, and a feed port 140 is provided on the grain feeder 144 side.
7, a discharge port 141 is formed at each end, and a supply hopper 132 is provided connected to the supply port 140;
A discharge gutter 160 is provided connected to the discharge port], 4], and a pressure lid 143 whose degree of pressure can be adjusted by a pressure lid adjustment device 142 is attached to the discharge port 141. As the press lid adjustment device 142, for example, Japanese Patent Publication No. 1-277
As disclosed in No. 76 (see Figure 5), Case 16
3, a weight 165 is mounted so as to be laterally movable by a screw shaft 164 and a detent 167, and the screw shaft 164
is formed by being directly connected to a forward/reverse rotation motor 162 connected to a control device 161 (see FIG. 4). The control device 161 includes an input/output signal processing device 161a, a storage device 161b, and an arithmetic device 161C, and a moisture detector 166 attached to the supply hopper 132 or the funnel portion below it is connected to the input/output signal processing device 161a. As the moisture detector 166, for example, an electric resistance type, a capacitance type, or the like is appropriately adopted. Around the porous-walled bran removal cylinder 133, there is an airtight dust collection chamber 14.
5, and its lower part serves as a dust collecting hopper 146. The lower end of the dust collection hopper 146 is connected to the fan 1 by a duct 147.
The outlet of the fan 15 is connected to the air supply port of duct 1.
48 to the cyclone 16. Further, as a grain humidifying device, a two-fluid nozzle 149 is provided at the open end of the hollow main shaft 134, and the two-fluid nozzle 14
9 is connected to the water tank 15 via a water pipe 157, a solenoid valve 153, a flow meter 154, and a flow rate control valve 155.
6, and the other side is connected to the air pipe 150 and the air filter 1.
It is connected to an air compressor 152 via 51. Also,
The flow rate control valve 155 is connected to a control device 161, and when the detected value of the moisture detector 166 is larger than a reference moisture value preset in the storage device 161b, for example, 22 to 24%, the flow rate is set to 0 and only the wind is turned on. When the flow rate is less than 22%, the flow rate is controlled to 120%, and in addition to this, the press lid adjusting device 142 is also controlled in conjunction with this. That is, when the reference value is exceeded, the pressing degree is set to 120%, and when it is less than this, the weight 165 is moved laterally by the motor 162 and the screw shaft 164 so that the pressing degree is 80%. Hereinafter, specific operations in the above embodiment will be explained. The grains (raw paddy) put into the tensioning device 4A or 4B are
It is supplied to the coarse sorter 2 via the elevator 5, and comparatively large foreign matter (coarse garbage) such as ears and straw waste are sorted and stored in a garbage container 2A and immature grains in an immature grain receiving box 2B. be done. The paddy from which impurities and immature grains have been removed is supplied to the weighing machine 3 and weighed, and then conveyed via the elevator 6゜7 and the flow conveyor 8A.
. . into appropriate receiving tanks IOA to IOD. The rice temporarily stored in the receiving tanks IOA to IOD is prevented from deteriorating in quality by being ventilated by the blowers 11A to 11D. When a suitable amount of rice is loaded into the receiving tanks 1.0A to 10D, it sequentially flows out from the discharge port onto the flow conveyor 12A for carrying out, passes through the elevator 13, and reaches the rice polisher 14A. In the rice polishing machine 14A (see Figure 2), the supply hopper 1
While detecting the moisture content of the raw paddy fed into the polishing chamber 139 using a moisture detector 166, the raw paddy is fed into the polishing chamber 139 by a grain feeding rotor 144. The polishing chamber 13 receives resistance from the pressing lid 143.
9 becomes a moderate pressure, and the stirring protrusion 1 of the polishing trochanter 137
35, a frictional force is generated between the rice grains or between the rice grains and the porous wall dust removal tube 33, and the outer glumes and awns on the surface of the rice grains are removed. At this time, the moisture detector 166
If the detected value is larger than the reference moisture value of 22 to 24%, for example 30%, the flow rate control valve 155 is closed to only blow air, and the pressure level of the pressure lid adjustment device 142 is increased to 120%. Or increase it proportionally to effectively remove the external glume. Conversely, if the detected value is less than the reference value, the humidification amount is increased by 120% and the pressing degree is increased to 80% so as not to cause unscaled particles. Note that the amount of humidification at this time is just enough to moisten the outer shell of the grain and not to penetrate into the endosperm. Further, in relation to moisture, control may be performed using only either the pressure degree or the humidification amount. In this way, the outer glumes, awns, etc. that are easily separated from the outer shell of the rice grains due to the air being blown into the polishing chamber] 39 leak out from the porous part of the porous wall dust removal tube 133, and are transferred to the dust collection hopper 146 by the suction force of the fan 15. At the same time, it reaches the cyclone 16 through the duct 148 as a dense dust-laden wind. Since the air volume of the fan 15 is relatively small, the dust is easily separated from the air, the glumes and awns fall downward and are stored in a garbage collection box, etc., and the air is discharged upward from the discharge port. Ru. Note that a small amount of dust contained in this exhaust air is removed by bag filter 1.
Collected by 7. Furthermore, by humidifying the surface of rice that has dried to a certain level, the outer glumes become relatively heavy, making it easier to separate them from the air. The rice that has passed through the grain grinder 14A flows down in the dryer 19 and is exposed to hot air from the combustion furnace 20 and the blower 21 to remove moisture from the surface of the rice husks. At this time, the rice grains from which the outer glumes and awns have been removed by the polisher 14A contain relatively little dust even when exposed to hot air, and the amount of dust transported to the wet dust collector 78 via the duct 0 is also extremely small. The paddy that has passed through the dryer 19 and whose chaff has been dried to some extent is transferred to the empty gap silos 27A to 27A by the elevator 22 and the flow conveyor 25A for carrying in.
It is put into 27C. While the brown rice is left in the gap silos 27A to 27C for several hours, the moisture in the brown rice transfers to the rice husks and is balanced and tempered. After passing through the dryer 19, the paddy is fed into a dryer 19, subjected to a drying action, and then transported to the interstitial silos 27A to 27C. This process is repeated multiple times. And receiving unit 1,
As in the receiving tanks IOA to IOD and each transport process, dust generated in the tank 18 and dryer 19 is sent to the wet dust collector 78 through each duct, and is washed with water by a shower from the nozzle 75. The paddy falls into the tank 76 and is collected by the sludge conveyor 77, but the paddy that reaches the dryer 19 passes through the grain grinder 14A many times each time it is dried, and is forcibly removed from the hulls, awns, etc. Since branches and stems are removed, the amount of dust sent from each duct to the wet dust collector 78 is greatly reduced. Therefore, the amount of sludge-like dust collected by the sludge conveyor 77 is extremely small and can be easily disposed of, and the amount of dust that cannot be collected and is scattered around is extremely small. Drying is carried out in this way, and the moisture that does not change the quality of the paddy, for example, 18
%, they are put into the silos 26A to 26G and stored until the end of the receiving period during the harvest season. When the receiving period ends, the paddy in each of the main silos 26A to 26G is sequentially discharged, passes through the grain grinder 14A again, and undergoes a drying action by the dryer 19, and is then removed from the gap silos 27A to 27C.
It is repeatedly subjected to the refining action of , and is dried to a concentration of, for example, 16%. At this time, since the drying of the paddy has progressed to some extent, the wet air from the two-fluid nozzle 149 effectively works for the polishing action of the grain grinder 1.4A and the classification action of the cyclone 16. Once drying is complete, the finished paddy goes through a selection process and is sold to the government. That is, the paddy flowing out from the discharge ports of the main silos 26A to 26G containing the required paddy is sent to the Nilo switching valve 29 through the flow conveyor 12B1 for carrying out 29G1 and the elevator 31 and the Nilo switching valve 32, 33. After being supplied to a machine 34 and screened, it is supplied to a swinging sorter 36 via an elevator 35 in order to remove unscaled grains (brown rice) contained in rice. The paddy fed into the supply hopper of the shaking sorter 35 is subjected to shaking action, and the unscaled grains with a relatively high specific gravity are swayed to the upper side of the slope by the rough surface of the sorting plate, and the grains with a relatively low specific gravity are swayed to the upper side of the slope. The kernels flow to the lower side of the slope while floating above the scaled grains and the paddy, and the bulk of the paddy forms a layer flowing in the middle of these. Then, the descaled grain layer falls to the paddy/brown rice conveyor 37 and is fed into the grain sorter 41A via the elevator 40, and only the descaled grains leak out from the sorting cylinder and are transferred to the two-way switching valve 4.
2 and stored in the immature grain receiving box 43, and on the other hand, the undegraded paddy is sent to the swinging sorter 36 again via the elevator 47 etc.
be returned to. This de-weighed grain is unnecessary when it is sold as paddy to the government, and moreover, it has been passed through the dryer 19 many times and has suffered damage such as shell cracking, so it is discarded. Furthermore, due to the grain grinding machine 14A, there are almost no branch grains,
In the event that some grains are present, they will fall from the lower side of the slope into the hulling conveyor 38 and will be transported to the hulling machine 5 via the elevator 54 etc.
7 to remove the branches and stems, the product is returned to the main silos 26A to 26G as products via elevators 31, 53, etc. On the other hand, compared to the unscaled grains and branch grains, a large amount of sized rice falls onto the mixed rice conveyor 39, passes through the elevator 4749, and then passes through the weighing machine 5.
After being weighed at 0, the rice is transferred to the main silos 26A to 26A as government-sold rice via the elevator 51 and the flow conveyor 25B.
It will be sealed and stored at 26G. In this selection process as well, dust is collected by the wet dust collector 78 through ducts from each device and conveyor, but since the grain passes through the grinder 14A many times during the drying process, dust is generated. are extremely rare. When the paddy stored in the main silos 26A to 26G in this way is then shipped through the hulling process, the main silos 26A to 26G are
Flow conveyor 1 for carrying out government light crossings from 6A to 26G
After being supplied to the weighing machine 50 via the elevator 2B and the elevator 31 for weighing, it is supplied to the hulling machine 80 via the elevator 51 and the like. The milled rice (mixed grains) from which 80 to 90% of the hulled rice has been dehulled by the dehulling rolls of the huller 80 is supplied to the oscillating sorter 36 via the mixed rice layer conveyor 39, the elevator 47, and the two-way switching valve 48. is put into the tank. Then, the rice is evenly supplied to each sorting board by the equalizer and supply gutter, removing the paddy from the ground rice and extracting only brown rice. In other words, while the rice is being polished and fed onto the oscillating sorting board, brown rice with a relatively high specific gravity is swung up the slope by contact with the rough surface, while paddy with a relatively low specific gravity slides on top of the brown rice. The rice flows to the lower side of the slope, and in the middle there is a layer of mixed rice consisting of brown rice and paddy. This results in
The rice on the lower side of the slope flows back through the huller conveyor 38 and the elevator 54, and is dehulled again in the huller 80. Further, the mixed rice falling into the mixed rice layer conveyor 39 joins with the ground rice and returns to the swinging sorter 36 where it is sorted. In this hulling process, the paddy that has passed through the grain grinder 14A many times and has had its outer glumes etc. removed is dehulled by the dehulling roll, so the amount of wear on the dehulling roller is halved, and replacement etc. It is economical and reduces the time and effort required. In addition, the amount of dust other than rice husks is reduced during wind sorting of the rolled rice immediately after it is removed from the hull. On the other hand, the brown rice in the brown rice conveyor 37 is supplied to grain sorters 41A and 41B via an elevator 40, and is sorted by grain thickness.
- For granulated grains having a grain thickness greater than a chamber, stones are removed through a stone removal grain sorter 61, then weighed by a weighing machine 63 via an elevator 62, and packed into flexible container bags 67 or bulk shipping tanks 66. After that, the grains are weighed by a weighing machine 68, and a bag opening is sewn by a sewing machine 69 and packaged in small parcels or shipped in bulk by a grain transfer vehicle 72. In addition, in each of the above steps, the dust generated in each processing equipment, weighing machine, or conveying machine through which the grains pass (the amount of dust generated by the grain grinding machine 14A is small) is collected by a wet dust collector through each duct. 78.Next, another embodiment of the grain grinder 14 will be described based on FIG. 3.The grain grinder 14B is almost the same as the grain grinder 14A of the previous embodiment. However, the difference is that the polishing trochanter J20 is a grinding type consisting of a grindstone, etc., and it is not equipped with a water tank for generating wet air. A hollow main shaft 119 with one end opened inside the dust removal cylinder 118
A grain feeding rotor 127 and a grinding type polishing rotor 120
A supply port 122 is provided at the end on the side of the grain feeding rotor 127 and a discharge port 123 is provided at the other end.
22, supply hopper] 24, discharge n J, 2
3, and a discharge gutter 110 is provided in each of the discharge ports 123, as in the previous embodiment.
A pressure lid 126 whose pressure degree can be adjusted is attached at 25, and a motor 114 of a pressure lid adjustment device 125 is connected to the vicinity of the supply hopper 124 and discharge gutter 110 via a control device 113 (see FIG. 4). Demolition rate detector 11.1
.. .. ]12 are provided respectively. In addition, the porous wall dust removal cylinder 11-8
A dust chamber 128 is formed around the dust collection chamber 1.
A dust collection hopper 129 is provided by connecting to the dust collection hopper 1.
The lower end of 29 is connected to the inlet of the blower 15 by a duct 130. Furthermore, the opening end of the hollow main shaft 19 faces the outlet of a blower 115 as a painting device, and the polishing trochanter 1
20 blow holes 116 are formed to blow air to the grains in the polishing chamber 121. When formed in this manner, the surface abrasive grains of the rotating polishing rotor 120 act to scrape off the outer glumes, awns, ramus, etc. of the rice husk. Then, the outer glume etc. are removed by the blower 11.
It easily separates from the outer shell due to the wind from Cyclone 1 and leaks from the porous wall bran removing cylinder 118, becoming a dense dust-laden wind and causing cyclone 1.
6, and as in the previous embodiment, it is separated from the air and collected, but the dust in the exhaust air is sent to the bag filter 1.
7 or may be connected to a wet dust collector 78 by a duct. The amount of dust collected at this time is very small and does not turn into a large amount of sludge as in the case of conventional methods. Note that the blower 115 also works to suppress the temperature rise of the rice grains in the polishing chamber 121. Also, when the grain is supplied to the grain grinding machine 14B and the discharge gutter 160
When the rice drops, the rice removal rate detector 111, . 112, the contamination rate of the unscaled grains during the visit to China is measured. In this way, the measured values detected by each of the rice removal rate detectors 111 and 112 at fixed time intervals are stored in the storage device (RAM) 16l via the input signal processing device 161a of the control device 161, respectively.
b and is averaged and compared by the arithmetic unit 161C, and the difference or ratio between the average values of the rice withdrawal rates between the two is larger than a reference value set in advance in the storage unit 161b, for example, a difference of 1.0%. At this point, the motor 162 of the pressure lid adjustment device 142 is rotated in the forward or reverse direction to move the weight 165 horizontally in steps toward the pressure lid 143 until the difference is within the 1.0% difference. It works as a safety device by reducing the biasing force of the granules to prevent accidents caused by large amounts of unbalanced particles. Above, we have described agitation type and grinding type polishing trochanters, but any polishing trochanter that can polish the outer shell of grains may be used. (see Fig. 7), percussion type (see Fig. 8), etc. are used. Furthermore, in the above embodiment, the grain grinding machines 14A and 14B are both arranged before the dryer in the drying process, or as shown in FIG. By providing a grain grinder 14C at the front stage and a grain grinder 14D between the receiving/rough sorting process and the pre-drying/storage process, grains can be removed before drying, or at least before drying is completed (approximately 16%). By removing the outer glume, awn, ramus, etc., there is less risk of decalcification occurring even without much humidification of the grain, and furthermore, as drying progresses, the outer glume, etc. are detached. It is possible to forcibly remove these particles at a stage before they tend to generate dust, and the amount of dust generated in the subsequent process of the grain grinder is extremely small. This has the effect of making the dust collector significantly smaller (and cheaper) and reducing the amount of uncollected dust to a very small amount. On the other hand, a grain grinder 14E may be provided in the sorting/selling process, and a grain grinder 14F may be provided in the hulling/shipping process, separately from or in addition to the grain grinding machines 14A-D. In particular, as mentioned above, by installing the wind sorter 34 in the sorting process, the huller 80 in the hulling process, etc., in other words, in the front stage of equipment equipped with an air blower, a large amount of waste is generated by these equipment. can reduce dust. Note that the number of the grain grinding machines 14A-F is not limited to one, and an appropriate number of grain grinders may be installed in parallel to match the flow rate at each installation location. By installing it on the line from the to the cargo receiving tank group, it does not affect the processing capacity as a whole.
第1図は本発明を実施したカントリエレベータの系統図
、第2図は第1図における研穀機の拡大断面図、第3図
は研穀機の別の実施例を示す断面図、第4図は制御部を
表すブロック図、+5図は押圧蓋調節装置の一部破断斜
視図、第6図乃至第8図は研磨転子の別実施例を示す断
面図、第9図は第1図の系統図を更に概略化し、研穀機
の設置場所の他の実施例を示す流れ線図、第10図は籾
米の正面図、第11図は麦粒の正面図である。
1・・・荷受ユニット、2・・・粗選機、3・・・計量
機、4A、4B・・・張込装置、5〜7・・・昇降機、
8A。
8B・・・フローコンベア、9A、、9B・・・二ロ切
換弁、1.0A〜10D・・・荷受タンク、IIA〜1
1D・・・送風機、12A、12B・・・搬出用フロー
コンベア、13・・・昇降機、14.144A、14B
・・・研磨機、15・・・ファン、16・・・サイクロ
ン、17・・・バッグフィルタ、18・・・タンク、1
9・・・乾燥機、20・・・燃焼炉、21・・・送風機
、22・・・昇降機、23・・・二ロ切換弁、24・・
・風選機、25A、25B・・・搬入用フローコンベア
、26八〜26G・・・本サイロ、27A〜27C・・
・間隙サイロ、28A〜28D・・・連絡用フローコン
ベア、29A〜29G・・・二ロ切換弁、30・・・精
選・籾摺ユニット、31・・・昇降機、32.33・・
・二ロ切換弁、34・・・風選機、35・・・昇降機、
36・・・揺動選別機、37・・・玄米用コンベア、3
8・・・籾用コンベア、39・・・ 混合米用コンベア
、40・・・昇降機、41A、41B・・・粒選別機、
42・・・二ロ切換弁、43・・・未熟粒受箱、44・
・・昇降機、45・・・壷穴式回転選別機、46・・・
脱秤粒受箱、47・・・昇降機、48・・・二ロ切換弁
、49・・・昇降機、50・・・計量機、51・・・昇
降機、52・・・二〇切換弁、53.54・・・昇降機
、55,56・・・二ロ切換弁、57・・・脱芒機、5
8・・・脱秤・選別装置、59・・異種穀粒選別ユニッ
ト、60・・・二ロ切換弁、61・・・石抜選穀機、6
2・・・昇降機、63・・・計量機、64・・・昇降機
、65・・・二ロ切換弁、66・・・バラ出荷タンク、
67・・・フレコン、68・・・計量包装機、69・・
・ミシン、70・・・昇降機、71・・・二ロ切換弁、
72・・・穀物移送車、73・・・供給口、74・・・
吐出口、75・・・ノズル、76・・・水洗槽、77・
・・スラッジコンベア、78・・・湿式集塵装置、80
・・・籾摺機、110・・・排出樋、111.1.12
・・・脱稲率検出器、113・・・制御装置、114・
・・モータ、115・・・送風機、116・・・噴風孔
、118・・・多孔壁除塵筒、119・・・中空主軸、
120・・・研磨転子、1−21・・・研磨室、122
・・・供給口、123・・・排出口、124・・・供給
ホッパ、125・・・押圧蓋調節装置、126・・・押
圧蓋、127・・・送穀転子、128・・・集塵室、1
29・・・集塵ホッパ、130・・・ダクト、133・
・・多孔壁除塵筒、134・・・中空主軸、135・・
・撹拌突起、136・・・噴風孔、1−37・・・研磨
転子、138・・・通風孔、139・・・研磨室、14
0・・供給口、141・・・排出口、142・・・押圧
蓋調節装置、143・・・押圧蓋、144・・・送穀転
子、145・・・集塵室、146・・・集塵ホッパ、1
47.1.48・・・ダクト、1.49・・・二流体ノ
ズル、150・・・送風管、」51・・・エアフィルタ
、152・・・空気圧縮機、153・・・電磁弁、15
4・・・流量計、155・・・流量調節弁、156・・
・水タンク、157・・・送水管、160・・・排出樋
、161・・・制御装置、162・・・正逆回転モータ
、163・・・ケース、164・・・螺軸、165・・
・分銅、166・・・水分検知器、167・・・回り止
め。
特許出願人 株式会社佐竹製作所
第8
図
第7
図
第6
図
602〈
)、−”502
第11図FIG. 1 is a system diagram of a country elevator embodying the present invention, FIG. 2 is an enlarged sectional view of the grain grinding machine in FIG. 1, FIG. 3 is a sectional view showing another embodiment of the grain grinding machine, and FIG. The figure is a block diagram showing the control unit, Figure +5 is a partially cutaway perspective view of the pressing lid adjusting device, Figures 6 to 8 are sectional views showing another embodiment of the polishing trochanter, and Figure 9 is the figure 1. 10 is a front view of unhulled rice, and FIG. 11 is a front view of wheat grain. 1... Receiving unit, 2... Rough sorting machine, 3... Weighing machine, 4A, 4B... tensioning device, 5-7... elevator,
8A. 8B...Flow conveyor, 9A, 9B...Two-way switching valve, 1.0A~10D...Receiving tank, IIA~1
1D...Blower, 12A, 12B...Flow conveyor for carrying out, 13...Elevator, 14.144A, 14B
... polishing machine, 15 ... fan, 16 ... cyclone, 17 ... bag filter, 18 ... tank, 1
9...Dryer, 20...Combustion furnace, 21...Blower, 22...Elevator, 23...Niro switching valve, 24...
・Wind sorter, 25A, 25B...Flow conveyor for delivery, 268-26G...Main silo, 27A-27C...
・Gap silo, 28A-28D...Communication flow conveyor, 29A-29G...Two-way switching valve, 30...Selection/hulling unit, 31...Elevator, 32.33...
・Niro switching valve, 34... wind sorter, 35... elevator,
36... Oscillating sorter, 37... Brown rice conveyor, 3
8... Conveyor for paddy, 39... Conveyor for mixed rice, 40... Elevator, 41A, 41B... Grain sorter,
42... Niro switching valve, 43... Immature grain receiving box, 44...
・・Elevator, 45 ・Curn hole type rotating sorter, 46・・
Grain removal box, 47... Elevator, 48... Two-way switching valve, 49... Elevator, 50... Weighing machine, 51... Elevator, 52... Twenty-switching valve, 53 .54... Elevator, 55, 56... Two-way switching valve, 57... De-awning machine, 5
8... Deweighing/sorting device, 59... Different kind of grain sorting unit, 60... Two-way switching valve, 61... Stone removal grain sorting machine, 6
2... Lifting machine, 63... Weighing machine, 64... Lifting machine, 65... Niro switching valve, 66... Bulk shipping tank,
67...Flexible container, 68...Measuring and packaging machine, 69...
・Sewing machine, 70... Elevator, 71... Two-way switching valve,
72... Grain transport vehicle, 73... Supply port, 74...
Discharge port, 75... nozzle, 76... washing tank, 77...
...Sludge conveyor, 78...Wet type dust collector, 80
... Husking machine, 110 ... Discharge gutter, 111.1.12
...Rice removal rate detector, 113...Control device, 114.
... Motor, 115 ... Air blower, 116 ... Blower hole, 118 ... Porous wall dust removal cylinder, 119 ... Hollow main shaft,
120... Polishing trochanter, 1-21... Polishing chamber, 122
. . . Supply port, 123 . . . Discharge port, 124 . Dust chamber, 1
29... Dust collection hopper, 130... Duct, 133.
...Porous wall dust removal cylinder, 134...Hollow main shaft, 135...
- Stirring protrusion, 136... Blow hole, 1-37... Polishing trochanter, 138... Ventilation hole, 139... Polishing chamber, 14
0... Supply port, 141... Discharge port, 142... Pressing lid adjustment device, 143... Pressing lid, 144... Grain feeding trochanter, 145... Dust collection chamber, 146... Dust collection hopper, 1
47.1.48...Duct, 1.49...Two-fluid nozzle, 150...Blow pipe, 51...Air filter, 152...Air compressor, 153...Solenoid valve, 15
4...Flowmeter, 155...Flow rate control valve, 156...
・Water tank, 157... Water pipe, 160... Discharge gutter, 161... Control device, 162... Forward/reverse rotation motor, 163... Case, 164... Spiral shaft, 165...
・Weight, 166... Moisture detector, 167... Rotation stopper. Patent applicant Satake Seisakusho Co., Ltd. Figure 8 Figure 7 Figure 6 Figure 602〈 ), -”502 Figure 11
Claims (9)
り、これらの工程で発生する粉塵を集塵する装置を備え
た穀物共同乾燥施設において、前記各工程のいずれか一
つ若しくは二つ以上又は任意の工程間に、荷受けされた
ほぼ全穀粒の枝梗・芒・外穎毛等を除去するための研穀
機を設けたことを特徴とする穀物共同乾燥施設の集塵装
置。(1) In a grain communal drying facility that consists of each process of receiving, rough sorting, drying, and hulling/shipping, and is equipped with a device to collect dust generated in these processes, any one of the above processes or Dust collection for a grain communal drying facility, characterized in that a grain grinding machine is installed between two or more or arbitrary processes to remove the ramus, awn, glume, etc. of almost all received grains. Device.
、精選・売渡及び籾摺・出荷の各工程からなり、これら
の工程で発生する粉塵を集塵する装置を備えた穀物共同
乾燥施設において、前記各工程のいずれか一つ若しくは
二つ以上又は任意の工程間に、荷受けされたほぼ全穀粒
の枝梗・芒・外穎毛等を除去するための研穀機を設けた
ことを特徴とする穀物共同乾燥施設の集塵装置。(2) Grain cooperatives are equipped with equipment to collect the dust generated during these processes, which consist of the following processes: receiving/rough selection, pre-drying/storage, drying, silo storage, sorting/selling, and hulling/shipping. In the drying facility, a grain grinder is installed to remove the stalks, awns, glumes, etc. of almost all the grains received during any one or more of the above steps or between any steps. A dust collector for a grain communal drying facility.
工程からなり、これらの工程から発生する粉塵を集塵す
る装置を備えた穀物共同乾燥施設において、前記乾燥工
程以前の工程又は工程間に、乾燥完了前のほぼ全穀粒の
枝梗・芒・外穎毛等を除去するための研穀機を設けたこ
とを特徴とする穀物共同乾燥施設の集塵装置。(3) In a grain joint drying facility that consists of at least each process of receiving, rough sorting, drying, and hulling/shipping, and is equipped with a device to collect the dust generated from these processes, the processes or processes before the drying process are A dust collection device for a grain communal drying facility, characterized in that a grain grinder is provided between the grains for removing ramus, awn, glume, etc. from almost all the grains before drying is completed.
程からなり、これらの工程から発生する粉塵を集塵する
装置を備えた穀物共同乾燥施設において、前記各工程内
にあって送風装置を有する機器の前段に、荷受けされた
ほぼ全穀粒の枝梗・芒・外穎毛等を除去するための研穀
機を設けたことを特徴とする穀物共同乾燥施設の集塵装
置。(4) In grain joint drying facilities that consist of at least the receiving, rough sorting, drying, and hulling/shipping processes, and are equipped with equipment to collect dust generated from these processes, air blowers are installed in each of the above processes. A dust collection device for a grain communal drying facility, characterized in that a grain grinding machine for removing ramus, awn, glume, etc. from almost all received grains is installed in the front stage of the equipment having the above-mentioned equipment.
集塵する集塵装置とは別に集塵装置を接続してなる請求
項(1)乃至(4)いずれかに記載の穀物共同乾燥施設
の集塵装置。(5) The grain grinding machine according to any one of claims (1) to (4), wherein a dust collection device is connected to the grain grinding machine separately from a dust collection device that collects dust generated by a device other than the grain grinding machine. Dust collection equipment for grain communal drying facilities.
各々連通する多孔壁筒内に研磨転子を回転自在に設け、
れら研磨転子と多孔壁筒との間隙を研磨室に形成してな
る請求項(1)乃至(5)いずれかに記載の穀物共同乾
燥施設の集塵装置。(6) The above-mentioned grain grinding machine is provided with a polishing trochanter rotatably provided in a perforated wall cylinder whose one end communicates with the supply section and the other end communicates with the discharge section,
A dust collector for a grain communal drying facility according to any one of claims 1 to 5, wherein a gap between the polishing trochanter and the porous wall cylinder is formed in the polishing chamber.
器を設けるとともに排出口には可動押圧蓋を装着し、排
出部の脱稲率が供給部のそれに対して一定以上増加した
とき、前記可動押圧蓋の押圧度を減ずるよう制御装置を
設けてなる請求項(5)又は(6)記載の穀物共同乾燥
施設の集塵装置。(7) A rice removal rate detector is installed in each of the supply section and the discharge section of the grain grinder, and a movable pressure lid is attached to the discharge port, so that the rice removal rate in the discharge section is higher than a certain level compared to that in the supply section. The dust collection device for a grain communal drying facility according to claim 5 or 6, further comprising a control device so as to reduce the pressing force of the movable pressing lid when the pressure increases.
粒加湿装置及び穀物の含水率を検知する水分検知器を設
けるとともに、この水分検知器によって測定する穀物の
含水率が基準値よりも小さいときは加湿量を大とし、か
つ、基準値よりも大きいときは加湿を中止するよう制御
装置を設けてなる請求項(5)又は(6)記載の穀物共
同乾燥施設の集塵装置。(8) The feeding section of the grain grinder is equipped with a grain humidifying device consisting of a humid air generator and a moisture detector for detecting the moisture content of the grain, and the moisture content of the grain measured by this moisture detector is the standard. Dust collection for grain communal drying facilities according to claim (5) or (6), further comprising a control device that increases the amount of humidification when the amount is smaller than the reference value and stops the humidification when the amount is larger than the reference value. Device.
ともに、供給部には穀物の含水率を検知する水分検知器
を設け、この水分検知器によって測定する穀物の含水率
が基準値よりも小さいときは前記押圧蓋の押圧度を減じ
、かつ、基準値よりも大きいときは押圧度を増やすよう
制御装置を設けてなる請求項(5)又は(6)記載の穀
物共同乾燥施設の集塵装置。(9) A movable pressure lid is attached to the outlet of the grain grinder, and a moisture detector is installed in the supply section to detect the moisture content of the grain, and the moisture content of the grain measured by this moisture detector is the standard. The grain communal drying facility according to claim 5 or 6, further comprising a control device that reduces the degree of pressure of the pressure lid when the value is smaller than a reference value, and increases the degree of pressure when it is larger than a reference value. dust collector.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP12754090A JPH0422440A (en) | 1990-05-17 | 1990-05-17 | Dust collector of grain corporative drying facilities |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP12754090A JPH0422440A (en) | 1990-05-17 | 1990-05-17 | Dust collector of grain corporative drying facilities |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0422440A true JPH0422440A (en) | 1992-01-27 |
Family
ID=14962541
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP12754090A Pending JPH0422440A (en) | 1990-05-17 | 1990-05-17 | Dust collector of grain corporative drying facilities |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0422440A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2005151886A (en) * | 2003-11-26 | 2005-06-16 | Iseki & Co Ltd | Plant for processing and shipping grain |
-
1990
- 1990-05-17 JP JP12754090A patent/JPH0422440A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2005151886A (en) * | 2003-11-26 | 2005-06-16 | Iseki & Co Ltd | Plant for processing and shipping grain |
JP4552425B2 (en) * | 2003-11-26 | 2010-09-29 | 井関農機株式会社 | Soybean preparation and shipping facility |
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