JPH01214519A - Pneumatic carrying method for bulk material - Google Patents

Pneumatic carrying method for bulk material

Info

Publication number
JPH01214519A
JPH01214519A JP3863788A JP3863788A JPH01214519A JP H01214519 A JPH01214519 A JP H01214519A JP 3863788 A JP3863788 A JP 3863788A JP 3863788 A JP3863788 A JP 3863788A JP H01214519 A JPH01214519 A JP H01214519A
Authority
JP
Japan
Prior art keywords
bulk material
hopper
powder
tank
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.)
Pending
Application number
JP3863788A
Other languages
Japanese (ja)
Inventor
Hiroshi Yamashita
博史 山下
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.)
NIKKEN TECHNO KK
Original Assignee
NIKKEN TECHNO KK
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 NIKKEN TECHNO KK filed Critical NIKKEN TECHNO KK
Priority to JP3863788A priority Critical patent/JPH01214519A/en
Publication of JPH01214519A publication Critical patent/JPH01214519A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To simplify the structure, to improve general usage and to prevent fault by sucking bulk material from a yard and accumulating the bulk material in a covered hopper, thereafter falling the bulk material into a pressure tank and feeding pressure air into the pressure tank in order to take out the bulk material from the tank, and repeating the cycle. CONSTITUTION:Air is sucked from a hopper 1 through a pneumatic pump 3 and a suction pipe 4 in order to accumulate bulk material through the suction pipe 4b into the hopper 1. When the bulk material in the hopper 1 reaches to a predetermined height, an upper limit level gauge 9 functions to open the bottom valve 8 of the hopper 1 thus sucking the outer air through a three-way valve 11 and falling the powder material down into a pressure tank 2. When the bulk material falls down entirely, the valve 8 closes. Consequently, suction of the bulk material is resumed and a discharge three-way valve 12 functions to lead the discharge gas into the pressure tank 2 and carry the bulk material from the pressure tank 2 through a carrying pipe 6. By such arrangement, the bulk material can be carried through simple structure with no fault and general usage can be improved.

Description

【発明の詳細な説明】 (目的)この発明は粉粒体の吸引と圧送を一体化して1
台の空気ポンプで継続的に行うことのできる粉粒体空気
搬送方法に関するものである。
[Detailed description of the invention] (Objective) This invention integrates suction and pressure feeding of powder and granules into one
This invention relates to a method for air conveying powder and granules that can be carried out continuously using a single air pump.

空気管を用いて吸引および圧送をおこなう物質の搬送は
それ自体すぐれた搬送手段であるが、その物質が粉粒体
である場合、その種類によっては大気の温度や湿度の、
影響を受けやすいため機構的にも取扱的にも特別の配慮
を必要とし、これが粉粒体の空気搬送の悴及を妨げてき
た。本発明は従来システムの蓮点を除去し、簡素で故障
の少い汎用システ11を11)ることを目的とする。
Transporting substances by suction and pressure using air pipes is itself an excellent means of transport, but if the substance is in the form of powder or granules, depending on the type of material, the temperature and humidity of the atmosphere may vary.
Because it is easily affected, special consideration is required both mechanically and in handling, and this has hindered the advancement of air conveyance of powder and granular materials. An object of the present invention is to eliminate the disadvantages of the conventional system and create a general-purpose system 11 that is simple and has fewer failures.

(構成および作用)つぎに図面(フローシート)にもと
づいて本発明のシステムを説明すると、本発明はホッパ
(1)と加圧槽(2)と空気ポンプ(3)と吸引管(4
d、4b)と排気管(5a。
(Structure and operation) Next, the system of the present invention will be explained based on drawings (flow sheets).
d, 4b) and exhaust pipe (5a.

5b)と搬送管((3)とフィルタ(7)と開閉弁(8
)と」1限レベル計(9)と下限レベル計(jO)と吸
引側三方j’i(11)と徘傑側三方弁(12)を゛[
段とする。前記譜要素の作用を工程順に説明すると、 1)空気ポンプ(3)の起動により吸引と排気が同時に
起るが、まず吸引管(4a)を通じて粉粒体が置場から
吸引されてホッパ(1)内に入り。
5b), the conveyor pipe ((3), the filter (7), and the on-off valve (8)
), the 1st limit level meter (9), the lower limit level meter (jO), the suction side three-way j'i (11), and the wandering side three-way valve (12).
dan. To explain the operation of the above-mentioned score element in the order of steps, 1) Suction and exhaust occur simultaneously when the air pump (3) is activated, but first the powder is sucked from the storage area through the suction pipe (4a) and sent to the hopper (1). Go inside.

ホッパ内で旋風現象を起して粉粒体は相当の含イ1空気
と分離してホッパ内に堆積し、分離した空気はホッパ内
」一部に取り付けられたフィルタ(7)でろ過されてホ
ッパの蓋に接続した吸引管(4b)を通して空気ポンプ
(3)に向う。
A whirlwind phenomenon occurs in the hopper, and the powder and granules are separated from a considerable amount of air containing air and deposited in the hopper, and the separated air is filtered by a filter (7) attached to a part of the hopper. It goes to the air pump (3) through the suction tube (4b) connected to the hopper lid.

2)ホッパ内の粉粒体が一定の高さに達すると上限レベ
ル、!1 (9)からの信号によってホッパ底開閉弁(
8)が開いて粉粒体をホッパの下方に接続した加圧槽(
2)内に落下させ、落下が終ると閉しろ。
2) When the powder in the hopper reaches a certain height, the upper limit level is reached! 1 (9) The hopper bottom opening/closing valve (
8) is opened and the powder and granules are connected to the lower part of the hopper in the pressurized tank (
2) Let it fall inside and close it when it finishes falling.

3)前記2)の進行中、吸引側三方弁(11)の動作に
よって吸引は外気吸引に切り換えられ、粉粒体の吸引は
中断されているが開閉弁(8)が閉じると粉粒体吸引が
再開され、空気ポンプ(3)内に吸引されたろ過空気は
排気となって排気側三方弁(12)の動作によりn+気
管(5,1)を通って加圧4+11y(2)の13部か
ら槽内に導入さ才しる。
3) While step 2) is in progress, the suction is switched to outside air suction by the operation of the three-way valve (11) on the suction side, and suction of powder and granules is interrupted, but when the on-off valve (8) closes, suction of powder and granules resumes. is restarted, the filtered air sucked into the air pump (3) becomes exhausted, passes through the n+ trachea (5, 1) through the operation of the exhaust side three-way valve (12), and is pressurized to 13 parts of 4+11y (2). It is then introduced into the tank.

4)加圧槽内に4人された空気は槽内に堆積した粉粒体
を押圧して槽武部に接続した搬送管(6)を通じて格外
にハ:送する一方、槽の上部と搬送管をつなぐ411”
−C管(5b)を通って搬送管内に圧入され、粉粒体の
推進を付勢する。
4) The air placed in the pressurized tank presses the powder and granules accumulated in the tank and is sent to the outside through the conveyor pipe (6) connected to the upper part of the tank. 411” that connects
- It is press-fitted into the conveying pipe through the C pipe (5b) and urges the powder and granular material to be propelled.

5)加圧槽内の粉粒体が減少して残量が限度を越すと下
限レベル11(10)が感知して搬送を止めるとともに
開閉弁(8)を開いてホッパ内の粉粒体を加圧槽に受は
入れる。r+jj記諸要素の連係シj作により粉11°
1体のホッパ°内吸引、ホッパから加圧槽への移動、加
h[#!jから外部への圧送がスイッチをリノるまで継
続的に行オ)れる6 (効果)1)ホッパ内に粉粒体を吸引することにより旋
風現象が起って含有空矢をある程度分離するので粉粒体
の純ノνが高まり、人気の温度、湿度から受ける影賢が
少くなって搬送が楽になる。
5) When the amount of powder and granules in the pressurized tank decreases and the remaining amount exceeds the limit, the lower limit level 11 (10) detects this and stops the conveyance, and opens the on-off valve (8) to remove the powder and granules in the hopper. Place the receiver in a pressurized tank. Powder 11° due to the combination of r+jj elements
Suction inside one hopper, transfer from hopper to pressurized tank, pressurization h [#! Pressure feeding from the hopper to the outside continues until the switch is turned off.6 (Effects) 1) By sucking the powder into the hopper, a whirlwind phenomenon occurs and the contained air arrows are separated to some extent. The purity of the powder and granules is increased, and the effects of temperature and humidity are reduced, making transportation easier.

2)1台の空気ポンプで粉粒体の吸引と圧送が行われる
ので経済的であり、設置場所も小さくて済む。
2) It is economical because suction and pressure feeding of powder and granular materials are performed with one air pump, and the installation space is small.

;3)従来の空気搬送システムはほとんどが丈の高いサ
イロ方式によっているが本発明は丈の低いホッパ方式な
ので粉粒体の搬入が百昨であり管理も容易である。
;3) Most conventional pneumatic conveying systems use a tall silo system, but the present invention uses a short hopper system, so powder and granules can be brought in easily and management is easy.

4.1ヌ1而の@jltな説明 図面は本発明のフローシートである。@jlt explanation of 4.1 The drawing is a flow sheet of the present invention.

lはホッパ、2は加圧槽、3は空気ポンプ、4a、4b
は吸引管、、5a、5bは排気管、6は搬送管、7はホ
ッパ内フィルタ、8はホッパ底開閉フ?、≦3は上限レ
ベル計、10は下限レベル計、11は吸引側::、カブ
?、12は排気側三方弁。
l is a hopper, 2 is a pressurized tank, 3 is an air pump, 4a, 4b
is a suction pipe, 5a and 5b are exhaust pipes, 6 is a conveyance pipe, 7 is a filter in the hopper, and 8 is a hopper bottom opening/closing flap. , ≦3 is the upper limit level meter, 10 is the lower limit level meter, 11 is the suction side::, Turnip? , 12 is a three-way valve on the exhaust side.

出願代理人 加々芙歌司Application agent: Kakafu Kaji

Claims (1)

【特許請求の範囲】[Claims] 空気管を用いる粉粒体の搬送方法において、空気ポンプ
の起動により吸引管を通じて粉粒体を置場から有蓋のホ
ッパ内に吸引して堆積させ、一定の高さに達すると上限
レベル計の信号によりホッパ底部の開閉弁が開いて粉粒
体をホッパ下方に接続した加圧槽内に落下させ、落下が
終ると開閉弁を閉じ、一方においてホッパ内部の上方に
取り付けたフィルタによつてろ過された空気は蓋に接続
した吸引管を通じて前記空気ポンプに吸引されるが、吸
引側三方弁の動作によつて外気の吸引に変り、ポンプの
排気となつて排気側三方弁の動作により排気管を通つて
加圧槽内に圧入され、槽内に堆積した粉粒体を押圧して
槽底に接続した搬送管を通じて槽外に搬出し、槽内の粉
粒体が底近くなると下限レベル計の信号によつて前記の
吸引が再開され、以下吸引と圧送が1台の空気ポンプで
継続的に繰り返すことを特徴とする粉粒体の空気搬送方
法。
In a method of transporting powder using an air pipe, the air pump is activated to suck the powder from the storage area into a covered hopper through the suction pipe and deposit it, and when it reaches a certain height, the signal from the upper limit level meter The on-off valve at the bottom of the hopper opens and the powder is dropped into a pressurized tank connected to the bottom of the hopper. When the fall is finished, the on-off valve is closed, and the powder is then filtered by a filter installed above the inside of the hopper. Air is sucked into the air pump through the suction pipe connected to the lid, but by the operation of the three-way valve on the suction side, air is sucked in from outside, which is exhausted from the pump, and then passed through the exhaust pipe by the operation of the three-way valve on the exhaust side. The granules are press-fitted into the pressurized tank, press the powder and granules accumulated in the tank, and transport them out of the tank through a conveyor pipe connected to the bottom of the tank. When the granules in the tank are near the bottom, a signal from the lower limit level meter is signaled. The above-mentioned suction is restarted by , and the suction and pressure feeding are continuously repeated using one air pump.
JP3863788A 1988-02-23 1988-02-23 Pneumatic carrying method for bulk material Pending JPH01214519A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3863788A JPH01214519A (en) 1988-02-23 1988-02-23 Pneumatic carrying method for bulk material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3863788A JPH01214519A (en) 1988-02-23 1988-02-23 Pneumatic carrying method for bulk material

Publications (1)

Publication Number Publication Date
JPH01214519A true JPH01214519A (en) 1989-08-28

Family

ID=12530758

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3863788A Pending JPH01214519A (en) 1988-02-23 1988-02-23 Pneumatic carrying method for bulk material

Country Status (1)

Country Link
JP (1) JPH01214519A (en)

Cited By (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH05106206A (en) * 1991-10-18 1993-04-27 Takashi Takee Concrete finishing method and its equipment
JPH079837U (en) * 1993-07-17 1995-02-10 大洸工業株式会社 Storage tank with deaeration device and powder gas feed device having the same
DE102004045429B3 (en) * 2004-09-18 2006-05-18 Eisenmann Maschinenbau Gmbh & Co. Kg Pump e.g. for supply of powder based media such as lacquer powder, has collecting main container next to application mechanism so that device is assigned to first pump container
JP2007283253A (en) * 2006-04-19 2007-11-01 Taiyo Nippon Sanso Corp Filler filling apparatus
US7846399B2 (en) * 2004-03-23 2010-12-07 W.R. Grace & Co.-Conn. System and process for injecting catalyst and/or additives into a fluidized catalytic cracking unit
CN102091756A (en) * 2010-12-02 2011-06-15 苏州苏铸成套装备制造有限公司 Pneumatic conveying device
CN102267632A (en) * 2011-05-11 2011-12-07 无锡市新标粉体机械制造有限公司 Vacuum feeder
CN102267633A (en) * 2011-04-14 2011-12-07 季胜 Positive/negative pressure combined conveying jar
CN102923484A (en) * 2012-11-21 2013-02-13 秦皇岛燕大源达机电科技有限公司 Positive and negative pressure combined type dense phase powder material pneumatic conveying device
CN103771137A (en) * 2014-02-15 2014-05-07 苏州信文食品有限公司 Controllable feeding device
US8926907B2 (en) 2004-03-23 2015-01-06 W. R. Grace & Co.-Conn System and process for injecting catalyst and/or additives into a fluidized catalytic cracking unit
US9504975B2 (en) 2004-03-23 2016-11-29 W. R. Grace & Co.-Conn. System and process for injecting catalyst and/or additives into a fluidized catalytic cracking unit
US9637325B2 (en) 2011-10-18 2017-05-02 W. R. Grace & Co.-Conn. Systems for injecting catalysts and/or additives into a fluidized catalytic cracking unit and methods of making and using the same
CN110371680A (en) * 2019-08-02 2019-10-25 江苏红光仪表厂有限公司 A kind of defeated grey on-line measuring device of coal electric force and its logic control power-economizing method

Cited By (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH05106206A (en) * 1991-10-18 1993-04-27 Takashi Takee Concrete finishing method and its equipment
JPH079837U (en) * 1993-07-17 1995-02-10 大洸工業株式会社 Storage tank with deaeration device and powder gas feed device having the same
US8967919B2 (en) 2004-03-23 2015-03-03 W. R. Grace & Co.-Conn. System and process for injecting catalyst and/or additives into a fluidized catalytic cracking unit
US8926907B2 (en) 2004-03-23 2015-01-06 W. R. Grace & Co.-Conn System and process for injecting catalyst and/or additives into a fluidized catalytic cracking unit
US7846399B2 (en) * 2004-03-23 2010-12-07 W.R. Grace & Co.-Conn. System and process for injecting catalyst and/or additives into a fluidized catalytic cracking unit
US9504975B2 (en) 2004-03-23 2016-11-29 W. R. Grace & Co.-Conn. System and process for injecting catalyst and/or additives into a fluidized catalytic cracking unit
US8012422B2 (en) 2004-03-23 2011-09-06 W. R. Grace & Co.-Conn. System and process for injecting catalyst and/or additives into a fluidized catalytic cracking unit
US9315738B2 (en) 2004-03-23 2016-04-19 W. R. Grace & Co.-Conn. System and process for injecting catalyst and/or additives into a fluidized catalytic cracking unit
DE102004045429B3 (en) * 2004-09-18 2006-05-18 Eisenmann Maschinenbau Gmbh & Co. Kg Pump e.g. for supply of powder based media such as lacquer powder, has collecting main container next to application mechanism so that device is assigned to first pump container
JP2007283253A (en) * 2006-04-19 2007-11-01 Taiyo Nippon Sanso Corp Filler filling apparatus
CN102091756A (en) * 2010-12-02 2011-06-15 苏州苏铸成套装备制造有限公司 Pneumatic conveying device
CN102267633A (en) * 2011-04-14 2011-12-07 季胜 Positive/negative pressure combined conveying jar
CN102267632A (en) * 2011-05-11 2011-12-07 无锡市新标粉体机械制造有限公司 Vacuum feeder
US9637325B2 (en) 2011-10-18 2017-05-02 W. R. Grace & Co.-Conn. Systems for injecting catalysts and/or additives into a fluidized catalytic cracking unit and methods of making and using the same
CN102923484A (en) * 2012-11-21 2013-02-13 秦皇岛燕大源达机电科技有限公司 Positive and negative pressure combined type dense phase powder material pneumatic conveying device
CN103771137A (en) * 2014-02-15 2014-05-07 苏州信文食品有限公司 Controllable feeding device
CN110371680A (en) * 2019-08-02 2019-10-25 江苏红光仪表厂有限公司 A kind of defeated grey on-line measuring device of coal electric force and its logic control power-economizing method

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