JPS5924009A - Rotary dryer or dry distillation - Google Patents

Rotary dryer or dry distillation

Info

Publication number
JPS5924009A
JPS5924009A JP13257782A JP13257782A JPS5924009A JP S5924009 A JPS5924009 A JP S5924009A JP 13257782 A JP13257782 A JP 13257782A JP 13257782 A JP13257782 A JP 13257782A JP S5924009 A JPS5924009 A JP S5924009A
Authority
JP
Japan
Prior art keywords
combustion chamber
air
duct
carbonized gas
rotary dryer
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.)
Granted
Application number
JP13257782A
Other languages
Japanese (ja)
Other versions
JPS6143482B2 (en
Inventor
平野 治行
金子 恒之
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.)
Niigata Engineering Co Ltd
Original Assignee
Niigata Engineering 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 Niigata Engineering Co Ltd filed Critical Niigata Engineering Co Ltd
Priority to JP13257782A priority Critical patent/JPS5924009A/en
Publication of JPS5924009A publication Critical patent/JPS5924009A/en
Publication of JPS6143482B2 publication Critical patent/JPS6143482B2/ja
Granted legal-status Critical Current

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Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 本発明は、主としてアスファルトプラントにおいて骨材
の乾燥1こ用いられる乾留ガス用ロータリドライヤfこ
関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a rotary dryer for carbonization gas used primarily for drying aggregate in asphalt plants.

アスファルトプラントにおいで骨ヰ4を乾燥するロータ
リドライヤは、熱源として一般昏こ重油を用いていたが
、石油の高81こより仙のM源が倹8・すされ、LPG
、都市ガス等の気体燃料や、石炭、コークス等の固体燃
料が一部導入されている。
The rotary dryer that dries bones in asphalt plants used ordinary heavy oil as a heat source, but instead of petroleum, which is 81 times more expensive, the rotary dryer that dries bones is used as a heat source.
, gaseous fuels such as city gas, and solid fuels such as coal and coke have been partially introduced.

ところで、近時、エネルギーコストと貧源再利用の見地
から、上記気体燃料や固体燃料より有利な、古タイヤの
乾留ガスを利用することが考えられているが、発生ガス
掖を、II(接、時時刻刻j関節することが容易でない
ため、こn、を必要としないアルミ等の溶解炉や温水ボ
イラ等1こ限られ、含水量が幅広く変動する上、設定温
度±5℃俣度の加熱精度を要求される骨材乾燥用のロー
タリドライヤにはこれを用いることができなかった。
By the way, recently, from the viewpoint of energy cost and resource reuse, it has been considered to use carbonized gas from old tires, which is more advantageous than the gaseous fuel or solid fuel mentioned above. Since it is not easy to adjust the time and time, it is limited to one type, such as aluminum melting furnaces and hot water boilers, which do not require this, and the water content fluctuates widely, and the set temperature is ±5 degrees Celsius This could not be used in a rotary dryer for drying aggregates, which requires high heating accuracy.

本発明は、乾留ガス発生炉1こ連絡ダクトを介して連絡
された燃焼室に、送気パイプにより送られてくる空気を
噴出しベンチュリー効果によって乾留ガスを燃焼室(こ
送り出す一次空気の噴射ノズルと、外気を燃焼室に送り
込む二次空気の送込みパイプを設け、また上記連絡ダク
トに放出ダクトを設けるとともに、上記連絡ダクトと上
記放出ダクトにゲート弁と調節バルブを個々に設けるこ
とにより上記の問題点を解消したもので、加熱温度を迅
速に微814節できる上、エネルギーコストが低くて経
済的な、古タイヤの乾留ガスをM ViNとするローク
リドライヤを提供することを目的とする。以下、本発明
を図面(こ基づいて詳細に駁、明する。
The present invention utilizes a primary air injection nozzle which blows out air sent from an air supply pipe to a combustion chamber connected to a carbonization gas generating furnace through a communication duct, and sends carbonization gas to the combustion chamber (from the combustion chamber) using the Venturi effect. In addition, a secondary air feed pipe is provided to send outside air into the combustion chamber, and a discharge duct is provided in the communication duct, and a gate valve and a control valve are individually provided in the communication duct and the discharge duct. An object of the present invention is to provide a low dryer which solves the problems, can quickly reduce the heating temperature to a fine 814 degrees, has a low energy cost and is economical, and uses carbonization gas from old tires as MViN. Hereinafter, the present invention will be explained in detail with reference to the drawings.

添付図面は本発明の一実施例を示すもので、図中1は回
転筒である。この回転筒1は周知のもので、骨材等の乾
燥材料の投入口1aを一個の端部に、また排出口1bを
他側の端部にそれぞれ有し、上記投入口1aを高く、か
つ排出口1bを低くするとともに、回転流1の外周fこ
巻き付けられた環状レール2を支持台4に固定された4
個のローラ3の上にのせて支持台4の上に斜めEこ支持
され、駆動装置(図示せず)1こよって周方向に回転さ
ぜられるようになっている。上記投入口1aの部分1こ
は、骨材等の乾燥材料を投入口1aから回転筒1内1こ
送り込むベルトコンベヤ等の搬送装v5と、上記乾燥材
料の加熱に働いた排ガスを外部に排出する排気ダクト6
が設けられ、また排出口1bの部分1こは燃焼室7が連
設されている。この燃焼室は、−次空気の噴敦ノズル8
々二次望気の送込みパイプ9を(+j4え、古タイヤを
乾留する周知の乾留ガス発生炉10にゲート弁15を備
えた連絡ダク)11で連絡されている。
The attached drawings show one embodiment of the present invention, and in the drawings, reference numeral 1 indicates a rotating cylinder. This rotary cylinder 1 is well known and has an input port 1a for dry materials such as aggregates at one end and a discharge port 1b at the other end. In addition to lowering the discharge port 1b, the annular rail 2 wrapped around the outer circumference f of the rotating flow 1 is fixed to a support base 4.
It is placed on two rollers 3 and supported obliquely on a support base 4, and is rotated in the circumferential direction by a drive device (not shown) 1. The portion 1 of the input port 1a includes a conveyor device v5 such as a belt conveyor that feeds dry materials such as aggregate into the rotary cylinder 1 from the input port 1a, and discharges exhaust gas that has worked to heat the dry material to the outside. Exhaust duct 6
A combustion chamber 7 is connected to a portion 1 of the exhaust port 1b. This combustion chamber has a secondary air injection nozzle 8.
A secondary air supply pipe 9 is connected by a connecting duct 11 (+j4 and a connecting duct equipped with a gate valve 15 to a well-known carbonization gas generating furnace 10 for carbonizing old tires).

上記噴射ノズル8は一次空気を燃焼室7fこ勢いよく噴
射し、その際生じるベンチュリー効果1こよりて乾留ガ
スを燃焼室7に送り出して・燃焼させるものであり K
fM節パルプ12を備えた送気パイプ13を介して送気
装置14(こ卓結さイ1.ている。更に、上ト七鼎絡ダ
クト11の、上記乾留ガス発生炉10と上記ゲート弁1
5の間には開閉弁16を備えた乾留ガスを逃がす放出ダ
クト17が設けらイ11、また送込みパイプ9には開閉
ダンパ18が役けられている。上記回転筒1の排出口1
bの部分には、ここから外部(こ排出される9材等の乾
燥材料の温度を検出する/晶IJtセンサ19が妃役さ
f’1.、また上記稠1ン1)バルブ12、ゲート弁1
5、開閉弁16には、1h4Vセンサ19から出される
指令を直腰或いは間接的(こ受けてそれらの開閉を制御
llIする制御値d20,21.22が個々に設けられ
る一方、前記搬送装置、15には、γ照度センサ19か
ら出される指令を直接或いは間接的に受けて・け材等の
乾燥材料の回転筒1への投大敵を加減する制61す装置
23が設けら11.ている。
The injection nozzle 8 powerfully injects the primary air into the combustion chamber 7F, and uses the Venturi effect 1 generated at this time to send the carbonized gas to the combustion chamber 7 and burn it.
An air supply device 14 (table connected 1. 1
A discharge duct 17 equipped with an on-off valve 16 for releasing the carbonized gas is provided between the pipes 5 and 5, and an on-off damper 18 is provided on the feed pipe 9. Discharge port 1 of the rotating cylinder 1
In part b, there is an external IJt sensor 19 that detects the temperature of dry materials such as the discharged materials f'1., and a valve 12 and a gate. Valve 1
5. The on-off valves 16 are individually provided with control values d20, 21.22 that directly or indirectly receive commands issued from the 1h4V sensor 19 and control their opening and closing, while the conveyance device, 15 is provided with a device 23 which directly or indirectly receives commands issued from the γ illuminance sensor 19 and controls the amount of dry material such as slag material thrown into the rotary cylinder 1. .

次(こ上イ己のように構成さ11.た本発明の乾留ガス
用ロークリドライヤの作用を説明する。
Next, the operation of the carbonization gas rotary dryer of the present invention constructed as described above will be explained.

送気装d14を作動させて噴射ノズル8から一次2ト・
λを燃焼室7内(こI忰いよ<1貧出させ、乾留ガス発
生炉lOにて発生せしめられた、古タイヤの乾留ガスを
ベンチュリー効果により一次空気と一緒に燃焼室7(こ
送り込んで燃焼させながら、回転中の回転筒l内lこ搬
送装置5から骨材等の乾燥材料を投入する。上記の作動
によって骨材等は回転筒1内を転動しなから余々(こ移
動し乾燥されて排出口1bから外部1こ取り出される。
Activate the air supply system d14 to inject primary 2-ton air from the injection nozzle 8.
The carbonized gas from old tires generated in the carbonized gas generator 1O is pumped into the combustion chamber 7 together with primary air by the Venturi effect. Dry materials such as aggregates are fed into the rotating cylinder 1 from the conveying device 5 while being burnt.Due to the above operation, the aggregates etc. do not roll inside the rotating cylinder 1 and are not moved. After drying, one piece is taken out from the outlet 1b.

運転当初1こおいては、骨材等の乾燥材料を、キャリブ
ティションや計→、(こより熱源にマツチした供給計よ
り幾分少なく回転筒1内に投入し、また、放出ダクト1
7の開閉プf’16を全閉するとともfこ、ゲート弁1
5を全開(こして乾留ガス発生炉101こて発生せしめ
られた乾留ガスの全量を燃焼室7にて燃焼させる。
During the first period of operation, dry materials such as aggregates are charged into the rotary cylinder 1 in a quantity slightly smaller than the supply meter matched to the heat source, and the discharge duct 1 is
When the opening/closing valve f'16 of 7 is fully closed, the gate valve 1
5 is fully opened (the entire amount of the carbonized gas generated by the carbonized gas generating furnace 101 is combusted in the combustion chamber 7.

このため、排出口1bから排出される乾燥材料の温度は
、所定温度より幾分高くなるが、これが温度センサ19
によってfirメト3さイ9.たら、直ち(こゲート弁
15を少し閉じるとともに開閉弁16を明けて乾留ガス
の一部を放出ダクト171こ流し、燃焼室7内での燃焼
量を低下させる。またこれと同時に骨材等の投入量を幾
分増加させる。この媒作]こよって、排出口1bから排
出される乾燥材料の温度は降下する。乾燥材料の温度が
所定温度より低下したら、再び、開閉弁16を全閉し、
ゲート弁15を全開して乾留ガスの全量を燃焼室7にて
燃焼させ、燃焼帳度を上昇させる一方、乾燥拐料の投入
量を少なくして運転当初の伏線に戻す。以下上記を繰り
返えして乾燥温鼓を所定の温l(範囲1こ保つが、乾留
ガスhtまたは乾燥材料の投入量のいずれか一方のみを
かえて乾燥温度を1i17J節することもできる。乾留
ガスの燃焼状態を調節する場合は、I4節バルブ12や
開閉ダンパ18の操作(こより一次空気や二次空気の骨
を調節して行なう。
Therefore, the temperature of the dry material discharged from the discharge port 1b becomes somewhat higher than the predetermined temperature, but this is due to the temperature sensor 19.
by fir met 3 sai 9. Immediately, the gate valve 15 is slightly closed and the on-off valve 16 is opened to allow some of the carbonized gas to flow through the discharge duct 171 to reduce the amount of combustion in the combustion chamber 7.At the same time, the aggregate, etc. As a result, the temperature of the dry material discharged from the discharge port 1b decreases.When the temperature of the dry material falls below the predetermined temperature, the on-off valve 16 is fully closed again. death,
The gate valve 15 is fully opened to combust the entire amount of carbonized gas in the combustion chamber 7 to increase the degree of combustion, while reducing the input amount of drying material to return to the original foreshadowing of the operation. Thereafter, the above procedure is repeated to maintain the drying drum at a predetermined temperature l (range 1), but it is also possible to change the drying temperature by changing only either the carbonization gas ht or the input amount of drying material. When adjusting the combustion state of the carbonized gas, it is done by operating the I4 section valve 12 and the opening/closing damper 18 (by adjusting the flow of the primary air and secondary air).

なお、余刺1乾留ガスを大気裔こ放出したのでは不経済
であるので% J131 ’/?S 、放出ダクト17
は加熱を心安とする温水器等に連冶される。
It should be noted that it is uneconomical to release one carbonization gas into the atmosphere, so %J131'/? S, discharge duct 17
It is connected to water heaters etc. that can be heated safely.

以上説明したよう(こ、本発明の乾留ガス用ロークリド
ライヤは熱源(こ古タイヤの乾留ガスを用いるものであ
るから、エネルギーコストが低く経済的である。また、
温度調節は、連絡ダクトに設けられたゲート弁と放出ダ
クトに設けられた開閉弁(こより迅速かつ僅易になすこ
とができるので、骨材等の乾燥材料を所定の温度に加熱
してこれを効率的に乾燥することができる。
As explained above, since the carbonized gas carbonization dryer of the present invention uses carbonized gas from old tires as a heat source, it is economical with low energy costs.
Temperature adjustment can be done quickly and easily using the gate valve installed in the connecting duct and the opening/closing valve installed in the discharge duct. Can be dried efficiently.

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

第1図は一部分を破断して示した本発明のロークリドラ
イヤの側面図、第2図は燃焼室と1質射ノズル及びゲー
ト弁等の関係を示す断1)0図、第3図は連絡ダクトと
放出ダクトの関係を示す平面図である。 1・・・・・・回転面、1a・・・・・・投入口、1b
・・・・・排出口、4・・・・・・支持台、7・・・・
・・燃焼室、8・・・・・噴射ノズル、9・・・・・・
送込みパイプ、10・・・・・・乾1■ガス発生炉、1
1・・・・・・連絡ダクト、12・・・・・・)調節バ
ルブ、13・・・・・・送気パイプ、15・・・・・・
ゲート弁、16・・・・・・1i11閉弁、17・・・
・・・放出ダクト。 出願人 株式会社新潟鉄工所 佐田建設株式会社、1、
Fig. 1 is a partially cutaway side view of the rotary dryer of the present invention, Fig. 2 is a cross-sectional view showing the relationship between the combustion chamber, the injection nozzle, the gate valve, etc., and Fig. 3 is It is a top view showing the relationship between a communication duct and a discharge duct. 1...Rotating surface, 1a...Input port, 1b
...Discharge port, 4...Support stand, 7...
...Combustion chamber, 8...Injection nozzle, 9...
Feed pipe, 10...Dry 1■ Gas generator, 1
1... Connection duct, 12...) Control valve, 13... Air supply pipe, 15...
Gate valve, 16...1i11 closed, 17...
...Discharge duct. Applicant: Niigata Iron Works Co., Ltd. Sada Construction Co., Ltd., 1.

Claims (1)

【特許請求の範囲】[Claims] 骨材等の乾燥材料の投入口と排出口を有し支持台の上(
こ周方向に回転自在に支持された回転筒に、連絡ダクト
を介して乾留ガス発生炉に連絡された燃焼室が連投さt
ll、上記連絡ダクト(こはゲート弁が設けられるとと
もfこ、上記燃焼室には送気パイプにより送られてくる
9気を燃焼ネ(こ噴出しベンチュリー効果によって乾留
ガスを燃焼室)こ送り出す一次空気の(+lf射ノズル
と、外気を燃焼室に送り込む二次空気の送込みパイプが
設けられ、上記送気パイプには調節バルブが設けら0.
る一方、上記連絡ダクトの上記乾留ガス発生炉とゲート
弁の間に、開閉9′Fを有する放出ダクトが設けられて
成ることを特徴とする乾留ガス用ロータリドライヤ。
It has an inlet and an outlet for dry materials such as aggregates, and is placed on a support stand (
A combustion chamber connected to a carbonization gas generating furnace via a communication duct is connected to the rotating cylinder that is rotatably supported in the circumferential direction.
ll, The above-mentioned communication duct (this is also provided with a gate valve), and the above-mentioned combustion chamber is injected with carbonized gas by the Venturi effect to combust air sent from the air supply pipe to the combustion chamber. A (+lf) injection nozzle for primary air to be sent out and a feed pipe for secondary air to send outside air into the combustion chamber are provided, and the air feed pipe is provided with a control valve.
A rotary dryer for carbonized gas, characterized in that a discharge duct having an opening/closing angle of 9'F is provided between the carbonized gas generating furnace and the gate valve of the communication duct.
JP13257782A 1982-07-29 1982-07-29 Rotary dryer or dry distillation Granted JPS5924009A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13257782A JPS5924009A (en) 1982-07-29 1982-07-29 Rotary dryer or dry distillation

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13257782A JPS5924009A (en) 1982-07-29 1982-07-29 Rotary dryer or dry distillation

Publications (2)

Publication Number Publication Date
JPS5924009A true JPS5924009A (en) 1984-02-07
JPS6143482B2 JPS6143482B2 (en) 1986-09-27

Family

ID=15084570

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13257782A Granted JPS5924009A (en) 1982-07-29 1982-07-29 Rotary dryer or dry distillation

Country Status (1)

Country Link
JP (1) JPS5924009A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0554605U (en) * 1991-12-20 1993-07-23 田中鉄工株式会社 Crusher drying plant dryer
JP2006299675A (en) * 2005-04-21 2006-11-02 Nikko Co Ltd Asphalt plant using combustible gas generated from biomass
JP2016061548A (en) * 2014-09-22 2016-04-25 住友精化株式会社 Liquefied natural gas vaporization system

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0554605U (en) * 1991-12-20 1993-07-23 田中鉄工株式会社 Crusher drying plant dryer
JP2006299675A (en) * 2005-04-21 2006-11-02 Nikko Co Ltd Asphalt plant using combustible gas generated from biomass
JP2016061548A (en) * 2014-09-22 2016-04-25 住友精化株式会社 Liquefied natural gas vaporization system

Also Published As

Publication number Publication date
JPS6143482B2 (en) 1986-09-27

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