JPS63267809A - Burner - Google Patents
BurnerInfo
- Publication number
- JPS63267809A JPS63267809A JP10235487A JP10235487A JPS63267809A JP S63267809 A JPS63267809 A JP S63267809A JP 10235487 A JP10235487 A JP 10235487A JP 10235487 A JP10235487 A JP 10235487A JP S63267809 A JPS63267809 A JP S63267809A
- Authority
- JP
- Japan
- Prior art keywords
- fuel
- combustion
- rotation
- cylinder
- diffusion
- 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
- 239000000446 fuel Substances 0.000 claims abstract description 67
- 238000009792 diffusion process Methods 0.000 claims abstract description 56
- 238000002485 combustion reaction Methods 0.000 claims abstract description 48
- 244000249914 Hemigraphis reptans Species 0.000 abstract description 9
- 230000008016 vaporization Effects 0.000 abstract description 9
- 238000009834 vaporization Methods 0.000 abstract description 8
- 239000007788 liquid Substances 0.000 abstract description 2
- 238000000034 method Methods 0.000 abstract 1
- 238000001035 drying Methods 0.000 description 10
- 238000002347 injection Methods 0.000 description 4
- 239000007924 injection Substances 0.000 description 4
- 238000001514 detection method Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000002828 fuel tank Substances 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 230000032258 transport Effects 0.000 description 1
Abstract
Description
【発明の詳細な説明】
産業上の利用分野
この発明は、バーナに関するもので、穀粒を乾燥する乾
燥機に利用できる。DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application This invention relates to a burner and can be used in a dryer for drying grain.
従来の技術
従来は、一定回転で回転する拡散筒内へ供給される燃料
はこの拡散筒内で気化され、この気化燃料は該拡散筒と
噴出燃焼盤との間に設けた噴出口より噴出燃焼するバー
ナであった。Conventional technology Conventionally, fuel supplied to a diffusion cylinder that rotates at a constant rotation is vaporized within this diffusion cylinder, and this vaporized fuel is ejected and combusted from an injection port provided between the diffusion cylinder and an injection combustion disk. It was a burner to do.
発明が解決しようとする問題点
例えば、バーナを穀粒乾燥機に使用した場合では、拡散
筒内へ供給される燃料は、この拡散筒内壁部を流下中に
この拡散筒内で気化されて気化燃料となり、この気化燃
料が該拡散筒と噴出燃焼盤との間で形成した噴出口から
、噴出燃焼して燃焼火炎となり、この燃焼火炎が該乾燥
機に設けた排風機で吸われることにより熱風となり、こ
の熱風に穀粒が晒されて乾燥されるが、乾燥する穀粒量
により、該拡散筒内へ供給される供給燃料量幅が、例え
ば、0.7〜4交/hと広範囲であり、供給燃料量が多
量のときには、該拡散筒内壁を流下中の燃料が多く、該
拡散筒内へ供給される燃焼用空気量も多く、このため適
当な気化が行なわれないままで、燃焼用空気の移行に伴
なって噴出口へいたり、この気化されていない燃料が該
噴出口から噴出燃焼するために赤火燃焼になることがあ
り。Problems to be Solved by the Invention For example, when the burner is used in a grain dryer, the fuel supplied to the diffusion cylinder is vaporized within the diffusion cylinder while flowing down the inner wall of the diffusion cylinder. This vaporized fuel ejects and burns into a combustion flame from the spout formed between the diffusion tube and the jet combustion disk, and this combustion flame is sucked by the exhaust fan installed in the dryer, producing hot air. The grains are exposed to this hot air and dried, but depending on the amount of grains to be dried, the amount of fuel supplied into the diffusion cylinder can vary widely, for example from 0.7 to 4 cycles/h. When the amount of fuel supplied is large, there is a large amount of fuel flowing down the inner wall of the diffusion cylinder, and a large amount of combustion air is supplied into the diffusion cylinder, so that proper vaporization is not performed and combustion occurs. Due to the movement of the air, it may reach the nozzle, and this unvaporized fuel may be ejected from the nozzle and burned, resulting in red-flame combustion.
又供給燃料量が少量のときには、該拡散筒内壁部を流下
中の燃料の膜厚が薄く、該拡散筒内へ供給される燃焼用
空気量も少なく、このため該拡散筒内壁の燃料の途切れ
る部分が過剰に加熱され易く、この拡散筒全体に当該現
象がおよんで、この拡散筒内壁を流下中の燃料がこの内
壁よりはじけて油滴状となり、燃焼用空気の移行に伴な
って該噴出口にいたるため、赤火燃焼になることがあっ
た。Furthermore, when the amount of fuel supplied is small, the film thickness of the fuel flowing down the inner wall of the diffusion cylinder is thin, and the amount of combustion air supplied into the diffusion cylinder is also small, so that the fuel on the inner wall of the diffusion cylinder is interrupted. The area tends to be overheated, and this phenomenon spreads to the entire diffusion tube, causing the fuel flowing down the diffusion tube inner wall to burst from the inner wall and become oil droplets, and as the combustion air moves, the injection There were cases where red flames burned as the fuel reached the exit.
問題点を解決するための手段
この発明は、燃料の供給を受けて回転により誘導拡散す
る拡散筒(1)と、この拡散筒(1)との間には気化燃
料を噴出させる噴出口(2)を形成する噴出燃焼盤(3
)、とを設けると共に、該拡散筒(1)の回転を低速回
転及び高速回転に切換可能に構成してなるバーナの構成
とする。Means for Solving the Problems The present invention provides a diffusion tube (1) that receives fuel supply and guides diffusion through rotation, and a spout (2) that spouts vaporized fuel between the diffusion tube (1). ) forming a jet combustion disk (3
), and the burner is constructed such that the rotation of the diffusion cylinder (1) can be switched between low-speed rotation and high-speed rotation.
発明の作用、および効果
拡散筒(1)内へ供給された燃料は、燃焼火炎の熱を受
ける該拡散筒(1)の内壁部を流下中に気化が促進され
るものであるがζ小燃焼のときには、燃焼用空気が少な
く且つ供給燃料も少ないから、該拡散筒(1)の内壁に
は燃料の途切れる部分が過剰に過熱され易く、徐々にこ
の拡散筒(1)の全体に当該現象がおよんで、該拡散筒
(1)の前端部等において供給燃料はこの拡散筒(1)
内壁部からはじけて(表面側のみ急速に過熱蒸発される
ために生じる現象)油滴状となり易く、そのまま燃焼用
空気の移行に伴なって噴出口(2)へいたり、この噴出
口(2)から噴出燃焼するが、所謂赤火燃焼となる。こ
のとき、該拡散筒(1)の回転を高速回転にすれば、供
給燃料の膜厚をうずくし且つ内壁を流下する速度が早い
ので、均一に液体燃料を蒸発させることができて、上記
の油滴状を解消でき適当な気化作用が受けられることと
なって、上記の赤火燃焼を防止できる。Functions and Effects of the Invention The vaporization of the fuel supplied into the diffusion tube (1) is promoted while it flows down the inner wall of the diffusion tube (1), which receives the heat of the combustion flame. At this time, since there is little combustion air and little fuel to be supplied, the inner wall of the diffusion tube (1) where the fuel is interrupted tends to be overheated, and the phenomenon gradually spreads throughout the diffusion tube (1). Then, at the front end of the diffusion tube (1), the supplied fuel is transferred to the diffusion tube (1).
It tends to burst from the inner wall (a phenomenon that occurs because only the surface side is rapidly superheated and evaporated) into the shape of oil droplets, and as the combustion air moves, it goes to the nozzle (2) or this nozzle (2). The fuel erupts and burns, resulting in so-called red-flame combustion. At this time, if the diffusion tube (1) is rotated at high speed, the film thickness of the supplied fuel will be distorted and the speed at which it will flow down the inner wall will be high, so that the liquid fuel can be evaporated uniformly, and the above-mentioned The appearance of oil droplets can be eliminated and an appropriate vaporization effect can be achieved, thereby preventing the red flame combustion described above.
一方、大燃焼のときには、該拡散筒(1)内壁を流下す
る燃料の膜厚がnいため、該拡散筒(1)回転が速いと
この膜厚がうすくなりすぎ、燃焼用空気量も多いため該
拡散筒(1)内壁を流下する燃料の速度が速く適当な気
化が行なわれないうちに該噴出口(2)へいたり、この
気化されていない燃料が噴出燃焼すると赤火燃焼となり
易く、このようなときには該拡散筒(1)の回転を低速
回転にすれば、十分な気化作用が受けられることとなっ
て、上記の赤火燃焼を防止できる。On the other hand, during large combustion, the film thickness of the fuel flowing down the inner wall of the diffusion tube (1) is small, so if the diffusion tube (1) rotates quickly, this film thickness becomes too thin and the amount of combustion air is large. If the speed of the fuel flowing down the inner wall of the diffusion tube (1) is high and it reaches the injection port (2) before being properly vaporized, or if this unvaporized fuel is ejected and burned, red-flame combustion is likely to occur. In such a case, if the diffusion tube (1) is rotated at a low speed, a sufficient vaporization effect can be obtained, and the above-mentioned red flame combustion can be prevented.
実施例
なお、図例は、乾燥機(5)に使用したバーナ(6)に
ついて説明する。EXAMPLE The illustrated example describes a burner (6) used in a dryer (5).
該乾燥機(5)の機壁(7)は前後方向に長い平面視長
方形状で1前後壁板及び左右壁板よりなり、この前壁板
には該バーナ(6)を内装したバーナケース(8)及び
この乾燥機(5)を始動及び停止等の操作を行なう操作
装置(9)を設け、該後壁板には排風機(10)を設け
た構成であり、該機!i! (7)下部の中央部には移
送螺旋を内装した集穀樋(11)を設け、この集穀樋(
11)上側には下部に繰出バルブ(12)を軸支した乾
燥室(13)を並設して連通させ、この乾燥室(13)
、(13)内側間には熱風室(14)を形成して、該バ
ーナ(6)と連通させた構成であり、この熱風室(14
)内には熱風温度を検出する熱風温度センサー(15)
を設けた構成であり、該乾燥室(13)、(13)外側
には排風1(1B)、(1B)を形成して、この排風室
(18)、(16)と該排風機(lO)とは連通させ、
この排風機(10)はモータ(2B)で回転駆動する構
成である。The machine wall (7) of the dryer (5) has a rectangular shape in plan view that is long in the front and back direction, and consists of one front and rear wall plate and a left and right wall plate, and this front wall plate has a burner case (6) in which the burner (6) is installed. 8) and an operating device (9) for starting and stopping the dryer (5), and an exhaust fan (10) on the rear wall plate. i! (7) A grain collection gutter (11) equipped with a transfer spiral is provided in the center of the lower part, and this grain collection gutter (
11) On the upper side, drying chambers (13) with a feeding valve (12) supported on the lower part are installed in parallel and communicated with each other, and the drying chambers (13)
, (13) A hot air chamber (14) is formed between the inner sides and communicated with the burner (6).
) is a hot air temperature sensor (15) that detects the hot air temperature.
Air exhaust 1 (1B), (1B) is formed outside the drying chambers (13), (13), and these air exhaust chambers (18), (16) and the air exhaust communicate with (lO),
This exhaust fan (10) is configured to be rotationally driven by a motor (2B).
該乾燥室(13)、(13)上側には貯留室(17)を
形成し、この貯留室(17)上側には天井板(18)、
(18)及び移送螺旋を内装した移送樋(18)を設け
、この移送樋(19)中央部には移送穀粒をこの貯留室
(17)内へ供給する供給口を設け、この供給口下側に
は拡散盤(20)を設けた構成であり、該前壁板には窓
(2B)を設け、この窓(23)の横側には収容量を表
示する数値を設けた構成である。A storage chamber (17) is formed above the drying chambers (13), (13), and a ceiling plate (18) is formed above the storage chamber (17).
(18) and a transfer gutter (18) equipped with a transfer spiral; a supply port for supplying transferred grains into the storage chamber (17) is provided in the center of the transfer gutter (19); A diffusion plate (20) is provided on the side, a window (2B) is provided on the front wall board, and a numerical value indicating the storage capacity is provided on the side of this window (23). .
前記前壁板前方部にはパケットコンベアー(21)ベル
トを内装した昇降41 (22)を設け、上端部と該移
送樋(18)始端部との間には投出筒(23)を設けて
連通させ、下端部と前記集穀樋(11)終端部との間に
は供給樋(20を設けて連通させ、該昇穀機(22)上
部にはモータ(25)を設け、このモータ(25)で前
記上下の移送螺旋、前記繰出バルブ(12) 、該拡散
盤(20)及び該バケットコンベアー(21)ベルトを
回転駆動する構成であり、上下方向はぼ中央部には水分
センサー(27)を設け、この水分センサー(27)に
はモータ(28)を内装し、前記操作装置(9)から発
信する電気的測定信号の発信により、このモータ(28
)が回転し、該水分センサー(27)が回転駆動して穀
粒水分値を検出する構成である。A lift 41 (22) equipped with a packet conveyor (21) belt is provided at the front of the front wall plate, and a discharge tube (23) is provided between the upper end and the starting end of the transfer gutter (18). A supply gutter (20) is provided between the lower end and the terminal end of the grain collecting gutter (11) for communication, and a motor (25) is provided on the upper part of the grain hoist (22). 25) rotates the upper and lower transfer spirals, the delivery valve (12), the diffusion plate (20), and the bucket conveyor (21) belt, and a moisture sensor (27) is installed approximately in the center in the vertical direction. ), this moisture sensor (27) is equipped with a motor (28), and this motor (28) is activated by transmitting an electrical measurement signal from the operating device (9).
) rotates, and the moisture sensor (27) is rotationally driven to detect the grain moisture value.
前記バーナ(6)は前記バーナケース(8)下板内壁よ
り−E方へ突出する取付板(30)に装着した構成であ
り、このバーナ(6)は後部に燃焼空気を送風する円筒
状で前後壁板の中央部が開口した送風筒(31)を設け
、この送風筒(31)内には拡散筒(1)の回転を低速
回転及び高速回転等に変更する変速モータ(32)を設
け、この送風筒(31)の該前壁板には中央部が開口し
た燃焼筒(33)を設け、この燃焼筒(33)の該開口
部には先端が開口した円錐状の案内筒(30を設け、該
燃焼筒(33)には気化燃料の一部が噴出する噴出孔(
35)を有し、中央部が開口して内側へ傾斜した傾斜部
を有した噴出燃焼盤(3)を設け、この噴出燃焼盤(3
)と該燃焼筒(33)との間には気化撚ネ4が通過する
通過路(3B)を形成した構成であり、該燃焼筒(33
)外周近傍部には燃料に着火する点火ヒータ(37)及
び燃焼火炎の有無を検出する火炎センサー(38)を設
けた構成であり、該取付板(30)には外気温度を検出
する外気温度センサー(4)を設けた構成である。The burner (6) is attached to a mounting plate (30) that protrudes from the inner wall of the lower plate of the burner case (8) in the -E direction, and the burner (6) has a cylindrical shape that blows combustion air to the rear. A blower tube (31) with an opening in the center of the front and rear wall plates is provided, and a variable speed motor (32) for changing the rotation of the diffusion tube (1) to low speed rotation, high speed rotation, etc. is provided in the blower tube (31). A combustion tube (33) with an open center is provided on the front wall plate of the blower tube (31), and a conical guide tube (30) with an open tip is provided in the opening of the combustion tube (33). The combustion tube (33) has a nozzle hole (33) through which a part of the vaporized fuel is spouted.
A jet combustion disc (3) is provided, which has a central part open and an inwardly inclined part.
) and the combustion tube (33), a passageway (3B) through which the vaporizing twist 4 passes is formed, and the combustion tube (33)
) An ignition heater (37) for igniting fuel and a flame sensor (38) for detecting the presence or absence of combustion flame are provided near the outer periphery, and the mounting plate (30) has an outside temperature sensor for detecting outside air temperature. This configuration includes a sensor (4).
該変速モータ(32)軸端部には燃料ノズル(38)よ
り噴出供給される燃料を受けて回転飛散させる飛散体(
40)及び該案内筒(34)に沿う該拡散筒(1)を固
着し、この拡散筒(1)はコツプの如き形状で口縁部が
外周方向へ折曲し、先端外周縁(41)が円錐状に拡径
し、他端部が小径円筒でこの小径部と該拡径部とを連接
する垂直部を有し、この垂直部と該口縁部との間には燃
料が流出しうる小間隙を有して固着した構成であり、こ
の拡散筒(1)の該拡径部と該噴出燃焼盤(3)の該傾
斜部との間には噴出口(2)を形成し、この噴出口(2
)より気化燃料が噴出し、この気化燃料が噴出燃焼して
燃焼火炎になる構成である。At the shaft end of the variable speed motor (32), there is a scattering body (
40) and the diffusion tube (1) along the guide tube (34), the diffusion tube (1) has a shape like a tip and the mouth edge is bent toward the outer circumference, and the tip outer circumference (41) has a conical diameter expanding into a conical shape, the other end is a small diameter cylinder, and has a vertical part that connects this small diameter part and the wide diameter part, and fuel flows out between this vertical part and the mouth edge part. A jet orifice (2) is formed between the enlarged diameter part of the diffusion cylinder (1) and the inclined part of the jet combustion disc (3), This spout (2
), vaporized fuel is ejected from the combustion chamber, and this vaporized fuel is ejected and combusted to become a combustion flame.
前記乾燥機(5)前部には燃料タンク(42)を設け、
前記バーナケース(8)下板外側部には燃料パルプを有
する燃料ポンプ(43)を設け、該燃料バルブの開閉に
より該燃料タンク(42)から燃料を吸入して、該燃料
ノズル(38)等を経て該飛散体(40)外周部へ噴出
供給する構成である。A fuel tank (42) is provided at the front of the dryer (5),
A fuel pump (43) having fuel pulp is provided on the outer side of the lower plate of the burner case (8), and fuel is sucked from the fuel tank (42) by opening and closing the fuel valve, and the fuel nozzle (38) etc. It is configured to eject and supply to the outer peripheral part of the scattering body (40) through the.
燃焼用空気は前記バーナケース(8)上板外側部に設け
た送風機(44)をモータ(45)で回転駆動し、この
送風41! (44)と連通した吸入筒(46)より吸
入し、該送風機(44)で送風ダクト(47)を経て前
記送風筒(31)内へ送風する構成である。Combustion air is supplied by rotating a blower (44) provided on the outer side of the upper plate of the burner case (8) with a motor (45). The air is sucked in through a suction tube (46) communicating with the air blower (44), and the air is blown into the air tube (31) through a blower duct (47) by the blower (44).
前記操作装置(9)は箱形状で、この箱体の表面板には
前記乾燥機(5)を始動及び停止等の操作を行なう始動
スイッチ(48) 、停止スイッチ(49)、仕上目標
水分値を設定する目標水分設定孤み(50) 、熱風温
度を設定する熱風温度設定撒み(51)及び前記熱風温
度センサー(15)と前記水分センサー(27)とが検
出する検出値を交互に表示する表示窓(52)を設け、
内部には制御装置(53)及び回転制御装置(54)を
設けた構成であり、該各設定孤み(50)、(51)は
ロータリースイッチ方式であり、この設定孤み(50)
を該表面板の仕上目標とする表示数値の位置へ操作する
と仕上目標水分値が設定され、又該設定孤み(51)を
前記貯留室(17)内へ収容した穀粒量を表示した前記
窓(29)の数値を該表面板の表示数値と同じ位置にな
るように操作すると、熱風温度が設定される構成である
。The operating device (9) is box-shaped, and the surface plate of the box has a start switch (48) for starting and stopping the dryer (5), a stop switch (49), and a target finishing moisture value. A target moisture setting knob (50) for setting a hot air temperature, a hot air temperature setting knob (51) for setting a hot air temperature, and a detection value detected by the hot air temperature sensor (15) and the moisture sensor (27) are alternately displayed. A display window (52) is provided to
It has a configuration in which a control device (53) and a rotation control device (54) are provided inside, and each setting knob (50) and (51) is a rotary switch type, and this setting knob (50)
When the surface board is moved to the position of the displayed numerical value as the finishing target, the finishing target moisture value is set, and the setting hole (51) is moved to the position of the displayed numerical value that is the finishing target. The hot air temperature is set by operating the numerical value on the window (29) so that it is in the same position as the numerical value displayed on the surface plate.
該回転制御装置(50は前記外気温度センサー(4)及
び前記熱風温度センサー(15)が検出する検出値がA
−D変換されるA−D変換器(55)、このA−D変換
器(55)で変換された変換値が入力される入力回路(
5B) 、該設定撒み(51)の操作が入力される入力
回路(57) 、これら各入力回路(5B) 、 (
57)から入力される各種入力値を算術論理演算及び比
較演算等を行なうPCU(5B)、このCPU(58)
から指令される各種指令を受けて出力する出力回路(5
9)を設けた構成である。The rotation control device (50 is such that the detection value detected by the outside air temperature sensor (4) and the hot air temperature sensor (15) is A).
- an A-D converter (55) that performs D conversion, an input circuit (to which the converted value converted by this A-D converter (55) is input);
5B), an input circuit (57) into which the operation of the setting spreader (51) is input, each of these input circuits (5B), (
PCU (5B) that performs arithmetic and logical operations, comparison operations, etc. on various input values input from 57), this CPU (58)
Output circuit (5) that receives various commands from the
9).
前記制御装置(53)は水分センサー(27)及び前記
火炎センサー(38)が検出する検出値がA−り変換さ
れるA−D変換器(eo) 、このA−D変換器(60
)で変換された変換値が入力される入力回路(81)
、前記各スイッチ(48)、(49)及び前記設定孤み
(50)の操作が入力される入力回路(82) 、これ
ら各入力回路(81)、(62)から入力される各種入
力値を算術論理演算及び比較演算等を行なう該CPU
(58) 、このCPU(5B)から指令される各種指
令を受けて出力する出力回路(63)を設けた構成であ
る。The control device (53) includes an A-D converter (eo) in which the detection values detected by the moisture sensor (27) and the flame sensor (38) are converted into A-to-A, and this A-D converter (60).
) An input circuit (81) into which the converted value is input.
, an input circuit (82) into which the operations of the switches (48), (49) and the setting knob (50) are input; and various input values input from these input circuits (81), (62). The CPU that performs arithmetic and logical operations, comparison operations, etc.
(58) This configuration includes an output circuit (63) that receives and outputs various commands from the CPU (5B).
前記回転制御装M (54)は前記制御装置(53)へ
前記設定孤み(50)及び前記始動スイッチ(48)の
操作が入力され、この回転制御装ffi (54)へ前
記設定孤み(51)の操作が入力されると、前記乾燥機
(5)が始動すると同時に、前記バーナ(6)及び前記
水分センサー(27)が始動し、前記外気温度センサー
(4)が検出する検出外気温度が入力され、この入力値
が前記CPU(58)へ設定して記憶させた、例えば、
10度〜7度を検出すると、このCPU(58)へ設定
して記憶させた5゜Or、p、@回転前記変速モータ(
32)を高速回転に制御し、前記拡散筒(1)の回転3
000r、p、+sを3500r、p、+wに高速回転
に変更し、7度〜3度を検出すると、 750r、p、
m高速回転に制御し、該拡散筒(1)の回転3000r
、p、mを375Or、P、11に高速回転に変更し、
3度以下を検出すると、1000r、p、+sm高速回
転制御し、該拡散筒(1)の回転3000r、p、mを
400Or、p、mに高速回転に変更する構成であり、
又該設定孤み(51)の操作位置によって、前記燃料ポ
ンプ(43)から該バーナ(6)内へ供給される燃料量
の範囲0.7〜4.01/hの内核CPU(58)へ設
定して記憶させた1例えば、3.5〜4.0交/hであ
れば、該拡散筒(1)の回転3000r、p、mを25
0Or、p、mに低速回転に変更し、 1.2〜3.5
1/hであれば標準回転の、 3000r、p、11と
し、0.7〜1.2Jl/hであれば、 3000r、
P、11を400Or、p、mに高速回転に変更する構
成であり、該バーナ(6)から発生する熱風温度を前記
熱風温度センサー(15)が検出し、この検出熱風温度
と該設定孤み(51)を操作して設定した設定熱風温度
とを比較し、相違していると設定熱風温度と同じ温度に
なるように、該燃料ポンプ(43)の前記燃料バルブの
開閉回数を制御して、この燃料ポンプ(43)で吸入す
る燃料量を変更する構成であり、この吸入する燃料量に
よって前記モータ(45)を制御して、前記送風411
t (44)で送風する燃焼用空気を制御する構成であ
る。The rotation control device M (54) inputs the operation of the setting point (50) and the start switch (48) to the control device (53), and transmits the setting point (54) to the rotation control device ffi (54). When the operation 51) is input, the dryer (5) starts, the burner (6) and the moisture sensor (27) start, and the outside air temperature detected by the outside air temperature sensor (4) starts. is input, and this input value is set and stored in the CPU (58), for example,
When 10 degrees to 7 degrees are detected, the speed change motor (
32) is controlled to a high speed rotation, and the rotation 3 of the diffusion tube (1) is controlled to a high speed.
When changing 000r, p, +s to 3500r, p, +w to high speed rotation and detecting 7 degrees to 3 degrees, 750r, p,
The diffusion tube (1) was rotated at 3000 r by controlling it to m high-speed rotation.
, p, m is changed to 375 Or, P, 11 for high speed rotation,
When 3 degrees or less is detected, the configuration is such that the rotation is controlled at a high speed of 1000r, p, +sm, and the rotation of the diffusion tube (1) is changed from 3000r, p, m to 400or, p, m,
Also, depending on the operating position of the setting knob (51), the amount of fuel supplied from the fuel pump (43) into the burner (6) to the inner core CPU (58) ranges from 0.7 to 4.01/h. For example, if the setting and memorization is 3.5 to 4.0 cycles/h, the rotation of the diffusion tube (1) is 3000 r, p, m to 25
Change to low speed rotation to 0Or, p, m, 1.2 to 3.5
If it is 1/h, the standard rotation is 3000r, p, 11, and if it is 0.7 to 1.2Jl/h, it is 3000r,
P, 11 is changed to high speed rotation to 400 Or, p, m, the hot air temperature sensor (15) detects the hot air temperature generated from the burner (6), and the detected hot air temperature and the set Compare the set hot air temperature set by operating (51), and if there is a difference, control the number of opening and closing times of the fuel valve of the fuel pump (43) so that the temperature becomes the same as the set hot air temperature. , the fuel pump (43) is configured to change the amount of fuel sucked in, and the motor (45) is controlled depending on the amount of fuel sucked in, thereby controlling the air blower 411.
This configuration controls the combustion air blown at t (44).
又前記制御装置(53)は前記設定搬み(50)を操作
して設定した仕上目標水分値と同じ穀粒水分値を前記水
分センサー(27)が検出すると、前記乾燥機(5)を
自動停止する構成である。Further, when the moisture sensor (27) detects a grain moisture value that is the same as the finishing target moisture value set by operating the setting transfer (50), the control device (53) automatically controls the dryer (5). It is configured to stop.
操作装m (9)の各設定孤み(50)、(51)を所
定位置へ操作し、始動スイッチ(48)を操作すること
により、乾燥機(5)が始動すると同時に、バーナ(6
)及び水分センサー(27)が始動し、このバーナ(6
)の点火ヒータ(37)に通電され、この点火ヒータ(
37)が赤熱し、燃料が燃料タンク(42)から燃料ポ
ンプ(43) 、燃料ノズル(39)を経て飛散体(4
0)の外周部へ噴出供給され、この飛散体(40)でこ
の燃料を拡散筒(1)内壁部へ飛散し、この拡散筒(1
)内壁部を流下中にこの拡散筒(1)?置部の小間隙部
より噴出し、この噴出した燃料の一部が赤熱した該点火
ヒータ(37)に飛散し、自動着火して燃焼が開始され
る。By operating the setting knobs (50) and (51) of the operating device m (9) to the predetermined positions and operating the start switch (48), the dryer (5) is started and at the same time the burner (6) is activated.
) and moisture sensor (27) are started and this burner (6
) is energized to the ignition heater (37) of the ignition heater (
37) becomes red hot, and the fuel flows from the fuel tank (42), through the fuel pump (43), through the fuel nozzle (39), and into the flying debris (4).
The fuel is sprayed and supplied to the outer circumference of the diffusion tube (1), and the scattering body (40) scatters this fuel to the inner wall of the diffusion tube (1).
) This diffusion tube (1) while flowing down the inner wall? A part of the ejected fuel is ejected from the small gap in the mounting section, and a portion of the ejected fuel is scattered onto the red-hot ignition heater (37), where it is automatically ignited and combustion begins.
この燃焼で該拡散筒(1)が熱せられ、この拡散筒(1
)内を流下中の燃料が気化され、この気化燃料と送風機
(40で送風される燃焼用空気とが混合して、噴出口(
2)と噴出孔(35)の二個所より噴出燃焼して燃焼火
炎となり、この燃焼炎が熱風となりこの熱風が排風機(
10)で吸われることにより、熱風室(10から乾燥室
(13)を通風し排風室(1B)を経て該排風機(10
)で吸引排風され、該乾燥4!1 (5)の貯留室(1
7)内へ収容した穀粒は、この貯′留室(17)から該
乾燥室(13)内を流下中に、この熱風に晒されて乾燥
され、繰出バルブ(12)で下部へと繰出され、下部の
移送螺旋で移送樋(11) 、供給樋(20を経て昇穀
機(22)内へ移送供給され、パケットコンベアー(2
1)で上部へ搬送され、投出筒(23)を経て移送樋(
19)内へ供給され、上部の移送螺旋でこの移送樋(1
9)を経て拡散盤(20)上へ移送供給され、この拡散
盤(20)で該貯留室(17)内へ均等に拡散還元され
、循環乾燥されて該設定機み(50)で設定した仕上目
標水分値と同じ穀粒水分値を該水分セスサー(27)が
検出すると、該操作装置(9)の制御装置(53)で自
動制御して該乾燥機(5)を自動停止する。This combustion heats the diffusion tube (1), and this diffusion tube (1) is heated.
) The fuel flowing down is vaporized, and this vaporized fuel is mixed with the combustion air blown by the blower ( 40
2) and the nozzle hole (35) eject and burn to form a combustion flame, and this combustion flame turns into hot air, which is then passed through the exhaust fan (
By being sucked in by the hot air chamber (10), the drying chamber (13) is ventilated, and the air is passed through the exhaust chamber (1B) to the exhaust fan (10).
) is suctioned and exhausted, and the drying 4!1 (5) storage chamber (1
7) The grains stored in the storage chamber (17) are exposed to this hot air and dried while flowing down in the drying chamber (13), and are then fed out to the lower part by the feeding valve (12). The grains are transferred and supplied into the grain raising machine (22) via the transfer gutter (11) and the feed gutter (20) by the transfer spiral at the bottom, and are then fed into the packet conveyor (22).
1), is transported to the upper part, passes through the dispensing tube (23), and is transferred to the transfer gutter (
19) and the upper transfer spiral transports this transfer trough (1
9) and onto the diffusion plate (20), where it is evenly diffused and returned into the storage chamber (17), circulated and dried, and set by the setting machine (50). When the moisture cessor (27) detects a grain moisture value that is the same as the finishing target moisture value, the dryer (5) is automatically stopped under automatic control by the control device (53) of the operating device (9).
この乾燥作業開始のときの前記設定機み(51)の操作
位置により、前記バーナ(6)の前記拡散筒(1)の回
転数が前記操作装置(9)の回転制御袋2t (54)
で低速回転、又は高速回転に制御されて該バーナ(6)
は燃焼し、又この燃焼中に外気温度センサー(4)が検
出する検出外気温度を低温度検出に伴ない、該拡散筒(
1)の回転数が該回転制御装置(54)で逐次高速回転
に制御されて該バーナ(6)は燃焼する。Depending on the operating position of the setting machine (51) at the time of starting this drying work, the rotation speed of the diffusion tube (1) of the burner (6) is set to 2t (54) of the rotation control bag of the operating device (9).
The burner (6) is controlled to rotate at low speed or at high speed.
is combusted, and during this combustion, the outside air temperature detected by the outside air temperature sensor (4) is detected as a low temperature, and the diffusion cylinder (
The rotation speed of 1) is sequentially controlled to high speed rotation by the rotation control device (54), and the burner (6) burns.
前記バーナ(6)の燃料を拡散する前記拡散筒(1)の
回転数を制御し、又この制御を供給燃料量と外気温度と
によって、高速回転、又は低速回転に制御することによ
り、該拡散筒(1)内での燃料の気化状態が安定するこ
とになり、該バーナ(6)の燃焼状態が安定する。By controlling the rotation speed of the diffusion cylinder (1) that diffuses the fuel of the burner (6), and controlling this control to high speed rotation or low speed rotation depending on the amount of supplied fuel and the outside temperature, the diffusion can be achieved. The vaporization state of the fuel within the cylinder (1) becomes stable, and the combustion state of the burner (6) becomes stable.
図は、この発明の一実施例を示すもので、第1図はブロ
ック図、第2図はフローチャート図、第3図は拡大側断
面図、第4図は拡大正面図、第5図は乾燥機の一部断面
せる全体側面図、第6図は乾燥機の一部断面せる全体正
面図、第7図は乾燥機の一部の拡大正面図である。
図中、符号(1)は拡散筒、(2)は噴出口、(3)は
噴出燃焼盤を示す。The figures show one embodiment of the present invention, in which Fig. 1 is a block diagram, Fig. 2 is a flowchart, Fig. 3 is an enlarged side sectional view, Fig. 4 is an enlarged front view, and Fig. 5 is a drying FIG. 6 is an overall partially sectional side view of the dryer, FIG. 6 is an overall partially sectional front view of the dryer, and FIG. 7 is an enlarged front view of a portion of the dryer. In the figure, reference numeral (1) indicates a diffusion tube, (2) indicates an ejection port, and (3) indicates an ejection combustion disk.
Claims (1)
)と、この拡散筒(1)との間には気化燃料を噴出させ
る噴出口(2)を形成する噴出燃焼盤(3)とを設ける
と共に、該拡散筒(1)の回転を低速回転及び高速回転
に切換可能に構成してなるバーナ。Diffusion cylinder (1
) and the diffusion tube (1), there is provided a jet combustion disk (3) that forms a jet nozzle (2) for spouting vaporized fuel, and the rotation of the diffusion tube (1) is controlled by slow rotation and low speed rotation. A burner that can be switched to high-speed rotation.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10235487A JPS63267809A (en) | 1987-04-24 | 1987-04-24 | Burner |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10235487A JPS63267809A (en) | 1987-04-24 | 1987-04-24 | Burner |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS63267809A true JPS63267809A (en) | 1988-11-04 |
Family
ID=14325138
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP10235487A Pending JPS63267809A (en) | 1987-04-24 | 1987-04-24 | Burner |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS63267809A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007322093A (en) * | 2006-06-02 | 2007-12-13 | Iseki & Co Ltd | Combustion burner |
-
1987
- 1987-04-24 JP JP10235487A patent/JPS63267809A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007322093A (en) * | 2006-06-02 | 2007-12-13 | Iseki & Co Ltd | Combustion burner |
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