JPH0627632B2 - Primary air intake device for gasification burner in grain dryer - Google Patents

Primary air intake device for gasification burner in grain dryer

Info

Publication number
JPH0627632B2
JPH0627632B2 JP59036871A JP3687184A JPH0627632B2 JP H0627632 B2 JPH0627632 B2 JP H0627632B2 JP 59036871 A JP59036871 A JP 59036871A JP 3687184 A JP3687184 A JP 3687184A JP H0627632 B2 JPH0627632 B2 JP H0627632B2
Authority
JP
Japan
Prior art keywords
burner
intake
air
grain
primary air
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.)
Expired - Lifetime
Application number
JP59036871A
Other languages
Japanese (ja)
Other versions
JPS60181574A (en
Inventor
定和 藤岡
仁志 上路
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Iseki Agricultural Machinery Mfg Co Ltd
Original Assignee
Iseki Agricultural Machinery Mfg Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Iseki Agricultural Machinery Mfg Co Ltd filed Critical Iseki Agricultural Machinery Mfg Co Ltd
Priority to JP59036871A priority Critical patent/JPH0627632B2/en
Publication of JPS60181574A publication Critical patent/JPS60181574A/en
Publication of JPH0627632B2 publication Critical patent/JPH0627632B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Landscapes

  • Drying Of Solid Materials (AREA)

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は穀粒乾燥機の乾燥熱源に使用するガス化バーナ
に係り、特に前記バーナの燃焼に必要な一次空気の取入
装置に関する。
Description: TECHNICAL FIELD The present invention relates to a gasification burner used as a heat source for drying a grain dryer, and more particularly to an intake device for primary air required for combustion of the burner.

(従来の技術) ガス化バーナは、灯油のような液体燃料を霧散したうえ
バーナ自体の燃焼熱によりガス化し、これに空気を混合
させ燃焼するもので、発熱量を広範囲に調節でき熱効率
も良好なため穀粒乾燥機の乾燥熱源として既に広く用い
られている。
(Prior Art) A gasification burner is a device that atomizes liquid fuel such as kerosene, gasifies it with the combustion heat of the burner itself, and mixes it with air to burn it. Therefore, it is already widely used as a heat source for drying grain dryers.

(発明が解決しようとする問題点) ここで、ガス化した燃料に混合する空気を一次空気と称
するが、燃料の供給量に比較して一次空気が過剰だと、
バーナの燃料盤より噴焔が飛び散り(リフト)、不足す
ると噴焔が正常な青色から赤色(赤火)に変って、いづ
れも完全に燃焼せずバーナの熱効率が著しく低下する。
(Problems to be Solved by the Invention) Here, the air mixed with the gasified fuel is referred to as primary air, but if the primary air is excessive compared to the supply amount of fuel,
The fuel spray scatters (lifts) from the burner's fuel panel, and when it is insufficient, the fuel spray changes from normal blue to red (red fire), and neither burns completely and the burner's thermal efficiency drops significantly.

従ってガス化バーナを最良の効率で燃焼させるために
は、燃料に対し適当な比率の一次空気を混合してやる必
要がある。しかし、穀粒乾燥機においては、乾燥が進展
するに伴いバーナの熱風が通過する穀粒層の穀粒密度が
高くなって通気抵抗が増大するために、乾燥機本体に付
設した吸引ファンによるバーナ付近の吸引圧が次第に低
減する。この影響で従来はバーナの一次空気取入量が乾
燥時間により変動しがちとなり、安定した完全燃焼状態
を持続するのが困難であるという欠点があった。
Therefore, in order to burn the gasification burner with the best efficiency, it is necessary to mix primary air with an appropriate ratio to the fuel. However, in a grain dryer, as the drying progresses, the hot air of the burner increases the grain density of the grain layer and the ventilation resistance increases, so the burner by the suction fan attached to the dryer main body increases. The suction pressure in the vicinity gradually decreases. Due to this effect, the amount of primary air taken in by the burner tends to fluctuate depending on the drying time, and it is difficult to maintain a stable complete combustion state.

本発明は、このようなバーナ付近の吸引圧の変動に起因
する燃焼状態の変動を解消するもので、バーナ付近の吸
引圧が変動しても吸気箱の前記吸気口とバーナ正面の燃
焼盤とにかかる吸引圧を常時略等しくして、乾燥の全行
程を通じ適量の一次空気をバーナに取入れ最良の燃焼状
態を終始持続することを第1の目的とし、加えて狭い空
間に広い濾過面積のエアフィルタを設置できるようにす
ることを第2の目的とする。
The present invention eliminates the fluctuation of the combustion state due to the fluctuation of the suction pressure in the vicinity of the burner, and even if the suction pressure in the vicinity of the burner changes, the intake port of the intake box and the combustion plate in front of the burner The first purpose is to keep the suction pressure applied to the burner almost the same at all times and take an appropriate amount of primary air into the burner to maintain the best combustion state throughout the entire drying process. A second purpose is to be able to install a filter.

(問題点を解決するための手段) かかる目的を達成するために、本発明は、ガス化バーナ
の熱風を吸引ファンにより吸引して機内を循環する穀粒
に通風させ乾燥する穀粒乾燥機において、前記ガス化バ
ーナの噴焔出口側の下方中央に吸気箱を設置し、吸気箱
の上面に、前記バーナの噴焔出口の中心線に関し左右対
称位置に一対の吸気口を開口し、吸気箱の後部に前記バ
ーナへの一次空気供給用の吸気ダクトを接続する。
(Means for Solving the Problems) In order to achieve such an object, the present invention relates to a grain dryer that dries hot air of a gasification burner by a suction fan to ventilate and dry the grains circulating in the machine. An air intake box is installed in the lower center of the gas outlet of the gasification burner, and a pair of air inlets are opened on the upper surface of the air intake box at symmetrical positions with respect to the center line of the gas outlet of the burner. An intake duct for supplying primary air to the burner is connected to the rear part of the.

また、ガス化バーナの熱風を吸引ファンにより吸引して
機内を循環する穀粒に通風させ乾燥する穀粒乾燥機にお
いて、前記ガス化バーナの噴焔出口側の下方中央に吸気
箱を設置し、吸気箱の上面に、前記バーナの噴焔出口の
中心線に関し左右対称位置に一対の吸気口を開口し、吸
気箱の後部に前記バーナへの一次空気供給用の吸気ダク
トを接続すると共に、前記吸気箱エアフィルタを傾斜さ
せて内装する。
Further, in a grain dryer that sucks the hot air of the gasification burner with a suction fan and ventilates the grains circulating in the machine to dry the grain, a suction box is installed in the lower center on the blowout side of the gasification burner, On the upper surface of the intake box, a pair of intake ports are opened at symmetrical positions with respect to the center line of the combustion outlet of the burner, and an intake duct for supplying primary air to the burner is connected to the rear part of the intake box, and Install the air intake box with the air filter inclined.

(作用) バーナ付近の吸引圧が低減してもそれと同等の圧だけ吸
気口の開口面における吸引圧も低減し、両者の吸引圧の
差は常に略等しい。
(Operation) Even if the suction pressure in the vicinity of the burner is reduced, the suction pressure at the opening surface of the intake port is also reduced by a pressure equivalent to that, and the difference between the suction pressures of the two is always substantially equal.

従って吸引圧の低減による燃焼盤より吸引される一次空
気の減少量は、吸気口の吸引圧の低減により吸気口から
吸われる一次空気の増大量により相殺され、結局、バー
ナに供給される一次空気の量は変わらない。
Therefore, the decrease amount of the primary air sucked from the combustion disk due to the decrease of the suction pressure is offset by the increase amount of the primary air sucked from the intake port due to the decrease of the suction pressure of the intake port, and eventually the primary air supplied to the burner is reduced. The amount of does not change.

また吸気箱の周囲を外気が熱風供給口に向けたえず通過
し吸気箱の後方に風の渦を生ずるが、箱の上面には温は
発生せず整風が流れるので、一次空気は吸気口より円滑
に吸入され、加えて吸気口は燃焼盤の中心線に関し左右
に開口するので、左右より吸入する風量が等しくバーナ
の熱風に偏りを生じない。
In addition, outside air constantly passes around the intake box toward the hot air supply port, creating a swirl of air in the rear of the intake box, but since the upper surface of the box does not generate temperature and regulates air flow, the primary air flows smoothly from the intake port. In addition, since the intake port is opened to the left and right with respect to the center line of the combustion plate, the amount of air taken in from the left and right is equal and the hot air of the burner is not biased.

さらに吸気口は燃焼盤より左右に離れた位置に開口する
ので、バーナの高温の噴焔を直接扱い込むことがなく、
予熱された周囲の暖気を吸うので、バーナを効果的に燃
焼できる。
Furthermore, since the intake port opens to the left and right of the burner, there is no need to directly handle the high-temperature combustion of the burner.
Since the preheated warm air is sucked, the burner can be effectively burned.

また吸気箱エアフィルタを吸気箱に傾斜して内装するの
で、エアフィルタの濾過面積を広く形成できる。
Further, since the air intake box air filter is installed inside the air intake box in a slanted manner, the filtration area of the air filter can be widened.

(実施例) 次に図面に示す実施例にもとづいて本発明を説明する。(Example) Next, the present invention will be described based on an example shown in the drawings.

第1、2および3図は所謂吸引排気型の循環式穀粒乾燥
機を示し、1は貯粒室2の底部に連通する左右一対の乾
燥室で、その内外側面を綱または外孔板のような通気側
板により構成する。
1, 2 and 3 show a so-called suction exhaust type circulating grain dryer, 1 is a pair of left and right drying chambers communicating with the bottom of the grain storage chamber 2, the inner and outer surfaces of which are ropes or outer perforated plates. It is composed of such a vent side plate.

3は乾燥室1の下端排出口にのぞむ集穀室で、その中央
の凹溝に横架する集穀ラセン4の送出端を乾燥機本体に
並設する昇穀機5の下端取入口に接続し、昇穀機5の上
部取出口には貯粒室2の天井に沿って軸架する給穀ラセ
ン6の始端に接続する。7は貯粒室2の天井中央に垂下
する拡散羽根で、その上方に給穀ラセン6の終端を開口
する。
3 is a grain collecting room looking into the lower end discharge port of the drying chamber 1, and the sending end of the grain collecting spiral 4 which is laterally placed in the central concave groove is connected to the lower end intake of the grain raising machine 5 arranged in parallel with the dryer main body. Then, the upper outlet of the grain elevator 5 is connected to the starting end of the grain feeding helix 6 which is mounted along the ceiling of the grain storage chamber 2. Reference numeral 7 denotes a diffusion blade that hangs in the center of the ceiling of the grain storage chamber 2, and the end of the grain feeding spiral 6 is opened above the diffusion blade.

そして後述するガス化バーナBを、左右の乾燥室1、1
の内側の通気側板により囲まれた熱風室の熱風供給口8
aに向けて設置すると共に、乾燥室1、1の外側の通気
側板と乾燥機8の外壁により囲まれた排風室9、9の出
口側に吸引ファン10を取付ける。
Then, a gasification burner B described later is installed in the left and right drying chambers 1, 1
Hot air supply port 8 of the hot air chamber surrounded by the ventilation side plate inside the
The suction fan 10 is installed on the outlet side of the air exhaust chambers 9 surrounded by the ventilation side plates outside the drying chambers 1 and 1 and the outer wall of the dryer 8 while being installed toward the a.

11は熱風供給口8aと反対側の熱風室8を閉鎖する遮
板、12は昇穀機5の下端取入口に連通する穀粒の張込
口、13は穀粒の機外取出口、14は乾燥室1の下端排
出口に軸架する穀粒排出バルブである。
11 is a shield for closing the hot air chamber 8 on the side opposite to the hot air supply port 8a, 12 is a grain inlet communicating with the lower end inlet of the grain raising machine 5, 13 is an outside outlet of the grain, 14 Is a grain discharge valve mounted on the lower end discharge port of the drying chamber 1.

バーナBにより加熱された外気つまり熱風は、吸引ファ
ン10により機内が負圧になるため、熱風供給口8aよ
り熱風室8に吸引され、乾燥室1に進入する。そして貯
粒室2より乾燥室1に流下した穀粒の水分を奪ってその
表層を強く乾燥したのち湿気を含んだ排風となり、乾燥
室1を横断して排風室9を経て吸引ファ10により機外
に排気する。
The outside air heated by the burner B, that is, hot air, is sucked into the hot air chamber 8 through the hot air supply port 8a and enters the drying chamber 1 because the suction fan 10 causes a negative pressure inside the machine. Then, the moisture of the grains flowing down to the drying chamber 1 from the grain storage chamber 2 is removed to strongly dry the surface layer thereof, and then the exhaust air containing moisture is generated. Exhaust to the outside of the machine.

乾燥室1の穀粒は穀粒排出バルブ14の回転に伴い、徐
々に集穀室3に落下し、集穀ラセン4、昇穀機5、およ
び給穀ラセン6を経て回転する拡散羽根7により貯粒室
2に再び戻る。そして貯粒室2内において穀粒中核部の
水分を表層に拡散して調質したのち再び乾燥室1に流下
し、このように機内を循環しながら次第に乾燥する。
The grains in the drying chamber 1 gradually fall into the grain collecting chamber 3 as the grain discharge valve 14 rotates, and are spread by the diffusion blades 7 that rotate through the grain collecting spiral 4, the grain raising machine 5, and the grain feeding spiral 6. Return to the grain storage chamber 2 again. Then, in the grain storage chamber 2, the moisture in the core portion of the grain is diffused to the surface layer to be subjected to conditioning, and then flown back into the drying chamber 1 to gradually dry while circulating inside the machine.

第4および5図は前記のガス化バーナBを示す図であ
る。
4 and 5 show the gasification burner B described above.

ここで15はバーナ収容ケースで乾燥機本体の正面外壁
aにボルトで締結し、バーナBを熱風供給口8aに向け
て設置する。ケース15の背面には防護網16を張りバ
ーナBの後方を覆う。17は図示しない燃料タンクに連
通する給油管、18は椀状の気化筒、19は気化筒18
を回転する気化筒モータ、20は混合室、21は混気室
20の正面を覆う環状の燃焼盤で多数の小孔を穿つ。2
2は同一円周上に沿い多数の通気孔を穿設した放焔皿
で、これに点火栓23を取付ける。
Reference numeral 15 denotes a burner housing case, which is fastened to the front outer wall a of the dryer main body with bolts, and the burner B is installed toward the hot air supply port 8a. A protective net 16 is provided on the back surface of the case 15 to cover the back of the burner B. Reference numeral 17 is an oil supply pipe communicating with a fuel tank (not shown), 18 is a bowl-shaped vaporization cylinder, 19 is a vaporization cylinder 18
A rotating cylinder motor, 20 is a mixing chamber, 21 is an annular combustion plate that covers the front of the mixing chamber 20, and a large number of small holes are drilled. Two
Reference numeral 2 is a flame dish having a large number of ventilation holes formed along the same circumference, and a spark plug 23 is attached thereto.

24はファンモータ25により回転する一次空気供給用
のシロッコ型ファンで、その送風口を送風ダクト26を
介して気化筒モータ19の後方に接続すると共に、ファ
ン24の中心に開口する吸引口に吸気ダクト27を接続
し、さらにダクト27の先端を、次に詳述する吸気箱Q
の背面中央の接続口28に連結する。
Reference numeral 24 denotes a sirocco type fan for supplying primary air which is rotated by a fan motor 25. The blower port is connected to the rear of the vaporizing cylinder motor 19 via a blower duct 26 and is sucked into a suction port opened at the center of the fan 24. The duct 27 is connected and the tip of the duct 27 is connected to the intake box Q which will be described in detail below.
Is connected to the connection port 28 at the center of the rear surface of the.

本発明において吸気箱Qは第6、7図に示すように、2
枚の薄鉄板の略中央を直角に折曲げて上半部29および
下半部30を形成し、下半部30の左右両側に一対の側
板31、32を固着する。
In the present invention, the air intake box Q is 2 as shown in FIGS.
The upper half part 29 and the lower half part 30 are formed by bending the approximate center of a thin iron plate at a right angle, and a pair of side plates 31 and 32 are fixed to both left and right sides of the lower half part 30.

そして上下2枚の通気板33、34の間に合成繊維の不
折布から成る公知の吸気箱エアフィルタ35を挾み、こ
れらにボルト36を貫通して蝶ナット37により締結す
る。
A well-known air intake box air filter 35 made of a non-woven fabric of synthetic fibers is sandwiched between the upper and lower two ventilation plates 33, 34, and a bolt 36 is passed through them to fasten them with a wing nut 37.

次に上半部29と下半部30を内側に向き合せて重ね、
左右の側板31、32の折返片に植立するボルト38、
38を、上半部29の水平面に穿つ連結孔39、39に
挿通して図示しない蝶ナットにより締結すると共に、吸
気箱エアフィルタ35を挾む上下の通気板のうち上部の
通気板33の水平な上下両側板を、上半部29と下半部
30の前後の側縁間で挾着し、これにより全体を直方体
型に組立てた吸気箱Qを構成し、その部の対角線に沿っ
て吸気箱エアフィルタ35を組付ける(第7図)。
Next, the upper half portion 29 and the lower half portion 30 are faced inward and stacked,
Bolts 38 to be installed on the folded pieces of the left and right side plates 31, 32,
38 is inserted into the connection holes 39, 39 bored in the horizontal plane of the upper half portion 29 and fastened by a wing nut (not shown), and the upper ventilation plate 33 of the upper and lower ventilation plates sandwiching the intake box air filter 35 is horizontal. The upper and lower side plates are sandwiched between the front and rear side edges of the upper half part 29 and the lower half part 30, thereby forming an intake box Q in which the whole is assembled in a rectangular parallelepiped shape, and the intake air is drawn along the diagonal line of the part. Assemble the box air filter 35 (Fig. 7).

そしてこの吸気箱QをバーナBの下方で且つ燃焼盤21
と熱風供給口8の中間に横向きにつまり噴焔の放射方向
に直交する方向に設置し、下半部30の垂直面中央すな
わち吸気箱Qの背面中央に前記のとおり接続口28を開
口して吸気ダクト27を連結し、上半部29の水平面す
なわち吸気箱Qの上面にはバーナBの燃焼盤21の中心
線に関し左右対称の位置に一対の吸気口40、40を開
口する(第5図)。
The intake box Q is placed below the burner B and on the combustion board 21.
It is installed laterally between the hot air supply port 8 and the hot air supply port 8 in the direction orthogonal to the radial direction of the injection, and the connection port 28 is opened in the center of the vertical surface of the lower half portion 30, that is, the center of the back surface of the intake box Q as described above. The intake duct 27 is connected, and a pair of intake ports 40, 40 are opened on the horizontal plane of the upper half portion 29, that is, on the upper surface of the intake box Q at positions symmetrical with respect to the center line of the burner plate 21 of the burner B (see FIG. 5). ).

ここで41は吸気口40の口縁に起立する塵埃進入防止
用の障壁で、その後半部には障壁41より高い半円弧状
の整風板42、42を突出させる。
Here, 41 is a barrier for preventing dust from standing upright at the edge of the intake port 40, and semi-circular air conditioning plates 42, 42 higher than the barrier 41 are projected in the latter half of the barrier.

しかしてバーナBに送油した燃料は給油管17の先端よ
り、気化筒モータ19により急速回転する気化筒18の
中心部に滴下し、その遠心力により混合室20に霧散放
出する。一方、ファン24により一次空気が吸気箱Qの
吸気口40より吸引され吸気箱エアフィルタ35により
濾過されたのち、送風ダクト26を経由して混合室20
に進入し、ここで前記の霧状の燃料と混合され点火栓2
3により点火する。
Then, the fuel sent to the burner B drops from the tip of the oil supply pipe 17 into the central portion of the vaporization cylinder 18 which is rapidly rotated by the vaporization cylinder motor 19, and is sprayed into the mixing chamber 20 by its centrifugal force. On the other hand, after the primary air is sucked from the intake port 40 of the intake box Q by the fan 24 and filtered by the intake box air filter 35, the primary air is passed through the air duct 26 and mixed chamber 20.
Into the spark plug 2 where it is mixed with the atomized fuel described above.
Ignition by 3.

点火後はバーナ自体の燃焼熱で気化筒18が加熱される
ため、燃料は気化筒18内で気化して混合室20で一次
空気と混合し、燃焼盤21の小孔より噴焔する。この噴
焔は放焔皿22の多数の通気孔より吸引する二次空気に
よりさらに激しく燃焼する。
After ignition, the vaporization cylinder 18 is heated by the combustion heat of the burner itself, so that the fuel is vaporized in the vaporization cylinder 18, mixed with the primary air in the mixing chamber 20, and injected from the small holes of the combustion plate 21. This flame is further violently combusted by the secondary air sucked from the many ventilation holes of the flame tray 22.

そしてこのように燃焼するバーナBにより、吸引ファン
10がケース15の防護網16を透過して吸い込む外気
を加熱し、この熱風により穀粒を前記のとおり乾燥する
のであるが、乾燥時間が経過するに従い機内の穀粒密度
が疎から密に変り乾燥室1の通気抵抗が増大する。
The burner B thus burning heats the outside air that the suction fan 10 permeates through the protective net 16 of the case 15 and inhales, and the hot air dries the grains as described above, but the drying time elapses. Accordingly, the grain density in the machine changes from sparse to dense and the aeration resistance of the drying chamber 1 increases.

このため吸引ファン10の回転数は一定でもバーナB付
近の吸引圧は低減するが、図面の実施例では一次空気を
取入れる吸気口40、40をバーナBの燃焼盤21と熱
風供給口8aの中間で、燃焼盤21の中心線に関し左右
対称位置に開口するので、燃焼盤21の盤面における吸
引圧が低減してもそれと同等の圧だけ吸気圧40、40
の開口面における吸引圧も低減し、両者の吸引圧は常に
等しい。
For this reason, the suction pressure near the burner B is reduced even if the number of revolutions of the suction fan 10 is constant, but in the embodiment shown in the drawings, the intake ports 40 and 40 for taking in the primary air are provided at the burner B combustion plate 21 and the hot air supply port 8a. In the middle, since the openings open at symmetrical positions with respect to the center line of the combustion plate 21, even if the suction pressure on the plate surface of the combustion plate 21 is reduced, the intake pressures 40, 40 are equal to the suction pressure.
The suction pressure at the opening surface of is also reduced, and the suction pressures of both are always equal.

従って燃焼盤21の吸引圧の低減による燃焼盤21より
吸引される一次空気の減少量は、吸気口40の吸引圧の
低減により吸気口40から吸われる一次空気の増大量に
より相殺され、結局、バーナBに供給される一次空気の
量は変わらない。このことは乾燥室1の通気側板が目詰
まりして通気抵抗が増しこれによりバーナB付近の吸引
圧が低減する場合においても全く同様である。
Therefore, the decrease amount of the primary air sucked from the combustion plate 21 due to the reduction of the suction pressure of the combustion plate 21 is offset by the increase amount of the primary air sucked from the intake port 40 due to the reduction of the suction pressure of the intake port 40, and eventually, The amount of primary air supplied to the burner B does not change. This is exactly the same when the ventilation side plate of the drying chamber 1 is clogged to increase the ventilation resistance, which reduces the suction pressure near the burner B.

また吸気箱Qの周囲を外気が熱風供給口8に向けたえず
通過し吸気箱Qの後方に風の渦を生ずるが、箱Qの上面
には渦は発生せず整風が流れるので、整風板42の作用
と送俟って一次空気は吸気口40より円滑に吸入され、
加えて吸気口40、40は燃焼盤21の中心線に対称位
置に開口するので、左右より吸入する風量が等しくバー
ナの熱風に偏りを生じない。
Further, the outside air passes around the intake box Q toward the hot air supply port 8 and a vortex of wind is generated behind the intake box Q, but no vortex is generated on the upper surface of the box Q and the conditioned air flows. The primary air is smoothly taken in through the intake port 40 due to the action of
In addition, since the intake ports 40, 40 open symmetrically with respect to the center line of the combustion board 21, the amount of air taken in from the left and right is equal and the hot air of the burner is not biased.

さらに吸気口40、40は燃焼盤21より左右に離れた
位置に開口するので、バーナBの高温の噴焔を直接吸い
込むことがなく、予熱された周囲の暖気を吸うので、バ
ーナBを効果的に燃焼できる。
Further, since the intake ports 40, 40 are opened at positions left and right apart from the combustion board 21, the hot air of the burner B is not directly sucked in, but the warm air around the preheated air is sucked in, so that the burner B is effective. Can burn to.

また吸気箱エアフィルタ35を吸気箱Qの対角線に沿い
内装するので、吸気箱エアフィルタ35の濾過面積を広
く形成でき吸塵効率が向上する。なお吸気箱エアフィル
タ35が汚れて吸塵機能が低下したら第6図のように蝶
ナットをゆるめて吸気箱Qを分解しエアフィルタ35を
洗浄したり交換することはいうまでもない。
Further, since the air intake box air filter 35 is installed along the diagonal line of the air intake box Q, the filtration area of the air intake box air filter 35 can be made large and the dust absorption efficiency is improved. Needless to say, when the air intake box air filter 35 becomes dirty and the dust suction function deteriorates, the wing nut is loosened to disassemble the air intake box Q and the air filter 35 is washed or replaced as shown in FIG.

(発明の効果) これを要するに本発明は、ガス化バーナBの噴焔出口の
外縁近傍に吸気箱Qを設置し、その上面左右に一対の吸
気口40、40を開口し、吸気箱Qの背面にバーナBへ
の一次空気供給用の吸気ダクト26を接続するので、乾
燥時間が経過するに伴い機内の穀粒密度が疎から密に変
り乾燥室1の通気抵抗が増大するので、吸引ファン10
の回転数は一定でもバーナンB付近の吸引ファン10に
よる吸引圧は低減するが、一次空気を取入れる吸気口4
0、40を燃焼盤21の下方で且つ燃焼盤21の中心線
に関し左右対称位置に開口するので、燃焼盤21の盤面
における吸引ファン10による吸引圧が低減すると吸気
口40、40の開口面における吸引ファン10による吸
引圧も低減し、吸引ファン10の吸引圧変動前後におけ
る、燃焼盤21と吸気口4との差圧は略等しい。
(Effect of the invention) In short, according to the present invention, the intake box Q is installed near the outer edge of the injection outlet of the gasification burner B, and a pair of intake ports 40, 40 are opened on the left and right of the upper surface of the intake box Q. Since the intake duct 26 for supplying the primary air to the burner B is connected to the back surface, the grain density in the machine changes from sparse to dense as the drying time elapses, and the ventilation resistance of the drying chamber 1 increases. 10
The suction pressure by the suction fan 10 in the vicinity of the burnan B is reduced even if the rotation speed is constant, but the intake port 4 for taking in the primary air is
0 and 40 are opened below the combustion plate 21 and at symmetrical positions with respect to the center line of the combustion plate 21, so that when the suction pressure by the suction fan 10 on the plate surface of the combustion plate 21 is reduced, the opening faces of the intake ports 40 and 40 are reduced. The suction pressure by the suction fan 10 is also reduced, and the pressure difference between the combustion plate 21 and the intake port 4 before and after the fluctuation of the suction pressure of the suction fan 10 is substantially equal.

吸気口40における吸引ファン10の吸引圧が低減する
と、ファン24により吸気口40から吸われる一次空気
は増大しようとする。一方、燃焼盤21の吸引圧の低減
による燃焼盤21より吸い出そうとする力が減少し、こ
れが一次空気の増大しようとする傾向を打ち消し、結
局、バーナBに供給される一次空気の量は吸引ファンの
吸引圧の変動に関係なくファン24の回転により決定さ
れる。このことは乾燥室1の通気側板が目詰まりして通
気抵抗が増しこれによりバーナB付近の吸引圧が低減す
る場合においても全く同様である。
When the suction pressure of the suction fan 10 at the intake port 40 decreases, the primary air sucked from the intake port 40 by the fan 24 tends to increase. On the other hand, the force of sucking out from the combustion disc 21 due to the reduction of the suction pressure of the combustion disc 21 decreases, and this cancels the tendency of the primary air to increase, and eventually the amount of primary air supplied to the burner B is It is determined by the rotation of the fan 24 regardless of the fluctuation of the suction pressure of the suction fan. This is exactly the same when the ventilation side plate of the drying chamber 1 is clogged to increase the ventilation resistance, which reduces the suction pressure near the burner B.

加えて、吸入口40、40は燃焼板21の中心線に関し
左右対称位置に開口するので、吸引ファン10による影
響およびファン24による影響を左側の吸入口40と右
側の吸入口40で等しく受ける。これにより左右より吸
入する風量が等しくバーナの熱風に偏りを生じないこと
も相俟って一次空気を所定の適量に終始維持でき、従っ
て乾燥の全行程を通じてバーナBを最良の効率で燃焼で
きるという効果を生ずる。
In addition, since the suction ports 40, 40 open symmetrically with respect to the center line of the combustion plate 21, the left suction port 40 and the right suction port 40 are equally affected by the suction fan 10 and the fan 24. As a result, the amount of air sucked in from the left and right is equal and the hot air of the burner is not biased, so that the primary air can be maintained at a predetermined appropriate amount from beginning to end, and therefore the burner B can be burned with the best efficiency throughout the entire drying process. Produce an effect.

また本発明では前記吸気箱Bの対角線に沿いエアフィル
タ35を内装するので、その濾過面積を広く形成でき、
防塵効率を向上できるという効果を生ずる。
Further, according to the present invention, since the air filter 35 is installed along the diagonal line of the intake box B, the filtration area can be widened,
The effect that the dustproof efficiency can be improved is produced.

さらに、吸気口40、40がバーナBの噴焔出口の近傍
にあるもののバーナBの噴焔出口の中心線に関し左右対
称位置に一対設けたので、吸気が左右同じになり噴焔出
口近傍の空気流が安定し噴焔を吸込みにくい。さらに噴
焔が最も出ている中心線上に吸気口がないので、噴焔を
吸込み吸気口が焦げるというおそれがなく予熱された周
囲の暖気を吸ってバーナを効果的に燃焼できるという効
果を生ずる。
Further, although the intake ports 40, 40 are located in the vicinity of the combustion outlet of the burner B, a pair of air intakes are provided symmetrically with respect to the center line of the combustion outlet of the burner B. The flow is stable and it is difficult to inhale the blowout. Further, since there is no intake port on the centerline where the spray is most exposed, there is no fear that the spray will be sucked and the intake port will be burnt, and the burner can be effectively burned by absorbing the preheated warm air.

【図面の簡単な説明】[Brief description of drawings]

図面は本発明の実施例を示す。第1図は一部を断面で示
す穀粒乾燥機の全体側面図である。第2図は第1図のII
−II線に沿う断面図、第3図は第1図のIII−III線に沿
う断面図である。第4図はガス化バーナの拡大中央縦断
面図である。ただし吸気箱については中央から左右に外
れた位置の断面を示す。第5図はバーナの拡大背面図
で、一部を断面で示す。第6図は吸気箱の分解拡大斜視
図、第7図は吸気箱の中央縦断面図である。 Bはガス化バーナ、Qは吸気箱、10は吸引ファン、3
5はエアフィルタ、40は吸気口。
The drawings show embodiments of the invention. FIG. 1 is an overall side view of a grain dryer, a part of which is shown in cross section. Figure 2 is II of Figure 1.
-II is a sectional view taken along the line, and FIG. 3 is a sectional view taken along the line III-III in FIG. FIG. 4 is an enlarged central vertical sectional view of the gasification burner. However, for the air intake box, the cross section at a position deviated from the center to the left and right is shown. FIG. 5 is an enlarged rear view of the burner, a part of which is shown in cross section. FIG. 6 is an exploded enlarged perspective view of the intake box, and FIG. 7 is a central longitudinal sectional view of the intake box. B is a gasification burner, Q is an intake box, 10 is a suction fan, 3
5 is an air filter and 40 is an intake port.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】ガス化バーナの熱風を吸引ファンにより吸
引して機内を循環する穀粒に通風させ乾燥する穀粒乾燥
機において、 前記ガス化バーナの噴焔出口側の下方中央に吸気箱を設
置し、吸気箱の上面に、前記バーナの噴焔出口の中央線
に関し左右対称位置に一対の吸気口を開口し、吸気箱の
後部に前記バーナへの一次空気供給用の吸気ダクトを接
続して成るガス化バーナの一次空気取入装置。
1. A grain dryer that dries hot air of a gasification burner by a suction fan to ventilate the grains circulating in the machine to dry the grain, and an intake box is provided in the lower center of the gas outlet of the gasification burner. Install a pair of intake ports on the upper surface of the intake box at symmetrical positions with respect to the center line of the combustion outlet of the burner, and connect an intake duct for supplying primary air to the burner to the rear part of the intake box. Primary air intake device for gasification burner.
【請求項2】ガス化バーナの熱風を吸引ファンにより吸
引して機内を循環する穀粒に通風させ乾燥する穀粒乾燥
機において、 前記ガス化バーナの噴焔出口側の下方中央に吸気箱を設
置し、吸気箱の上面に、前記バーナの噴焔出口の中心線
に関し左右対称位置に一対の吸気口を開口し、吸気箱の
後部に前記バーナへの一次空気供給用の吸気ダクトを接
続すると共に、前記吸気箱エアフィルタを傾斜させて内
装して成るガス化バーナの一次空気取入装置。
2. A grain dryer that dries hot air of a gasification burner by a suction fan to ventilate the grains circulating in the machine to dry the grain, and an intake box is provided at the lower center of the gas outlet of the gasification burner. Installed, a pair of intake ports are opened on the upper surface of the intake box at symmetrical positions with respect to the center line of the injection outlet of the burner, and an intake duct for supplying primary air to the burner is connected to the rear part of the intake box. In addition, a primary air intake device for a gasification burner, in which the air filter of the intake box is tilted and installed internally.
JP59036871A 1984-02-27 1984-02-27 Primary air intake device for gasification burner in grain dryer Expired - Lifetime JPH0627632B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59036871A JPH0627632B2 (en) 1984-02-27 1984-02-27 Primary air intake device for gasification burner in grain dryer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59036871A JPH0627632B2 (en) 1984-02-27 1984-02-27 Primary air intake device for gasification burner in grain dryer

Publications (2)

Publication Number Publication Date
JPS60181574A JPS60181574A (en) 1985-09-17
JPH0627632B2 true JPH0627632B2 (en) 1994-04-13

Family

ID=12481843

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59036871A Expired - Lifetime JPH0627632B2 (en) 1984-02-27 1984-02-27 Primary air intake device for gasification burner in grain dryer

Country Status (1)

Country Link
JP (1) JPH0627632B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH037709Y2 (en) * 1985-12-27 1991-02-26

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5346344B2 (en) * 1974-12-27 1978-12-13
JPS583925B2 (en) * 1975-06-24 1983-01-24 カブシキガイシヤ キト− Ichikenshiyutsusouchi

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5826996Y2 (en) * 1976-09-23 1983-06-11 惣太 山本 Rice husk carbonization type combustion device in grain drying equipment
JPS583925U (en) * 1981-06-30 1983-01-11 日本電気ホームエレクトロニクス株式会社 Automatic dust removal device
JPS58154325U (en) * 1982-04-07 1983-10-15 井関農機株式会社 vaporizer burner
JPS58166824U (en) * 1982-04-28 1983-11-07 三菱電機株式会社 Air filter for combustion machine

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5346344B2 (en) * 1974-12-27 1978-12-13
JPS583925B2 (en) * 1975-06-24 1983-01-24 カブシキガイシヤ キト− Ichikenshiyutsusouchi

Also Published As

Publication number Publication date
JPS60181574A (en) 1985-09-17

Similar Documents

Publication Publication Date Title
JP2004125262A (en) Hybrid hot air heater
JPH0627632B2 (en) Primary air intake device for gasification burner in grain dryer
JPS5843647B2 (en) liquid fuel combustion equipment
JPH0268482A (en) Hot air generator for grain dryer
JPS6133370Y2 (en)
JPH0263129B2 (en)
CN211977242U (en) Gas water heating equipment
JP2517563Y2 (en) Combustion device
JPS6214077B2 (en)
JPS5824685B2 (en) liquid fuel combustion equipment
JPS6021621Y2 (en) oil burner
JPS626419Y2 (en)
JPH07103969B2 (en) Combustion device for dryer
JP3635010B2 (en) Liquid fuel combustion equipment
JPS6144116Y2 (en)
JPS6030571Y2 (en) rotary gasification burner
JPS5827224Y2 (en) liquid fuel combustor
JPS6219650B2 (en)
JPS6322453Y2 (en)
JPS632735Y2 (en)
JPS629477Y2 (en)
JPH0612336Y2 (en) Combustion device
JPH025308Y2 (en)
JP2507052B2 (en) Combustion device
JPS6023245B2 (en) combustion device