JPS5924051B2 - Solid particulate matter discharge equipment - Google Patents

Solid particulate matter discharge equipment

Info

Publication number
JPS5924051B2
JPS5924051B2 JP51044968A JP4496876A JPS5924051B2 JP S5924051 B2 JPS5924051 B2 JP S5924051B2 JP 51044968 A JP51044968 A JP 51044968A JP 4496876 A JP4496876 A JP 4496876A JP S5924051 B2 JPS5924051 B2 JP S5924051B2
Authority
JP
Japan
Prior art keywords
solid
solid particulate
particulate matter
gas
moving bed
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
Application number
JP51044968A
Other languages
Japanese (ja)
Other versions
JPS52140161A (en
Inventor
貞雄 村田
泰人 岩井
豊太郎 河辺
信夫 大橋
興治 青柳
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.)
Mitsui Toatsu Chemicals Inc
Original Assignee
Mitsui Toatsu Chemicals Inc
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 Mitsui Toatsu Chemicals Inc filed Critical Mitsui Toatsu Chemicals Inc
Priority to JP51044968A priority Critical patent/JPS5924051B2/en
Publication of JPS52140161A publication Critical patent/JPS52140161A/en
Publication of JPS5924051B2 publication Critical patent/JPS5924051B2/en
Expired legal-status Critical Current

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  • Air Transport Of Granular Materials (AREA)
  • Filling Or Emptying Of Bunkers, Hoppers, And Tanks (AREA)

Description

【発明の詳細な説明】 本発明は固体粒子状活性物質から成る移動層と被処理気
体との接触操作を行う連続移動層式気固接触装置の底部
から活性の減少した上記固体物質を排出する装置、特に
該物質の安息角容量を利用して定量的に排出する装置に
関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention discharges the solid substance whose activity has decreased from the bottom of a continuous moving bed type gas-solid contacting device that performs a contact operation between a moving bed consisting of a solid particulate active substance and a gas to be treated. The present invention relates to a device, particularly a device for quantitatively discharging the substance using its angle of repose capacity.

近時、活性炭、触媒のような破損を甚しく嫌う固体粒子
状物質の増扱いの機械および量が急増してきている。
Recently, there has been a rapid increase in the number of machines and quantities that handle solid particulate materials, such as activated carbon and catalysts, which are extremely susceptible to damage.

例えば公害防止を対象とする排煙脱硫或は排煙脱硝のよ
うな硫酸のミストや煤塵の如きダストを含む気体を触媒
の如き易破砕性固体粒子状物質に連続的に接触させて物
理的或は化学的処理を行なう際該物質の性能維持のため
に新鮮物質の継続代謝の目的から活性の減少した固体粒
子を定量的に装置外に連続的に排出させることが必要で
ある。
For example, in exhaust gas desulfurization or exhaust gas denitrification for pollution prevention, a gas containing dust such as sulfuric acid mist or soot is brought into continuous contact with easily friable solid particulate matter such as a catalyst to physically or In order to maintain the performance of the substance during chemical treatment, it is necessary to continuously discharge solid particles whose activity has decreased quantitatively out of the apparatus for the purpose of continuous metabolism of the fresh substance.

すなわち処理気体中のミストが固体粒子状物質に凝縮付
着したり、ダストが付着堆積して目づまりを起すと共に
粒子の活性を減少させるのである。
That is, mist in the processing gas condenses and adheres to solid particulate matter, and dust adheres and accumulates, causing clogging and reducing the activity of the particles.

また被処理気体中に酸化硫黄の如き触媒毒となる成分が
含まれているときも同様に固体粒子状物質の活性が減少
するので装置外1こ排出することが必要である。
Furthermore, when the gas to be treated contains components that act as catalyst poisons, such as sulfur oxide, the activity of the solid particulate matter similarly decreases, so it is necessary to discharge the solid particulate matter outside the apparatus.

さらに、活性炭により、被吸着成分を含む被処理気体を
処理する場合は活性体表面は被吸着性成分で飽和され吸
着能(活性)が低下するので同様に一定時間後には装置
外に排出する必要がある。
Furthermore, when using activated carbon to treat a gas containing adsorbed components, the surface of the activated carbon becomes saturated with the adsorbed components and its adsorption capacity (activity) decreases, so it must be discharged from the device after a certain period of time. There is.

従来かかる気固接触装置からの固体粒子状物質の排出装
置lこは電磁振動フィーダ、ロータリフィーダ、ダンパ
、或はテーブルフィーダ等が用いられてきた。
Conventionally, an electromagnetic vibration feeder, a rotary feeder, a damper, a table feeder, or the like has been used as a device for discharging solid particulate matter from such a gas-solid contact device.

しかしこれらの装置は粒子破損度、保守性、定量性など
の点でそれぞれ一長一短があり、例えば粒子破損度は、
ロークリフィーダ、ダンパ、電磁振動フィーダの順序で
大きい。
However, these devices each have advantages and disadvantages in terms of particle breakage degree, maintainability, quantitative ability, etc. For example, particle breakage degree is
The largest order is the row feeder, damper, and electromagnetic vibration feeder.

保守性についてはそれぞれ構造上から相違するが、振動
による構造上の欠陥の発生、運動部位への物質の噛込み
、回転運動による耐熱性の問題、使用ガスの密封性、開
閉操作時の物質の破損等に対処する手段を必要とする。
Regarding maintainability, each structure is different, but there are problems such as occurrence of structural defects due to vibration, material getting caught in moving parts, heat resistance problems due to rotational movement, gas sealing performance, and material leakage during opening/closing operations. A means to deal with damage etc. is required.

排出の定量性については下部集積部に常時物質が堆積し
、該物質の偏流落下の傾向を生じ均等な排出量を確保す
ることが困難である。
Regarding the quantitative nature of discharge, substances are constantly deposited in the lower accumulation part, and the substances tend to drift and fall, making it difficult to ensure an even discharge amount.

そこで本発明の目的は、連続移動層式気固接触装置にお
いて活性の減少した移動層内の固体粒子状物質を該装置
の底部から定量的にかつ破損を伴わずにしかも大型装置
における偏流落下もなく均一(こ排出できる装置を提供
する1こある。
Therefore, the object of the present invention is to quantitatively remove solid particulate matter in a moving bed whose activity has decreased in a continuous moving bed type gas-solid contact device from the bottom of the device without causing damage, and also to prevent drifting and falling in large devices. There is one device that provides a device that can discharge the water uniformly and uniformly.

すなわち本発明の要旨は、易破砕性の固体粒子状活性物
質により移動層を形成し、該移動層に被処理気体を通過
せしめて接触操作を行う連続移動層式気固接触装置にお
いて、該装置の底部より活性の減少した北記固体物質を
破砕を伴うことなく定量的1こ排出する装置であって、
(1)上記接触装置直下に設けた基台、(2)該基台上
に上記固体物質を安息角形成相当分量排出集積せしめる
上記接触装置下方側壁部に設けた切欠部、(3)および
前記排出された集積物質を一定量掻き摩る上記基台上を
摺動する可変往復運動式スクレーパよりなることを特徴
とする活性の減少した固体粒子状物質の定量排出装置に
ある。
That is, the gist of the present invention is to provide a continuous moving bed type gas-solid contacting apparatus in which a moving bed is formed of an easily shatterable solid particulate active substance, and a gas to be treated is passed through the moving bed to carry out a contact operation. A device for quantitatively discharging one solid substance with reduced activity from the bottom of the container without crushing the solid substance,
(1) a base provided directly below the contact device; (2) a notch provided in the lower side wall of the contact device for discharging and accumulating the solid substance in an amount corresponding to the angle of repose on the base; (3) and the above. The apparatus for quantitatively discharging solid particulate matter with reduced activity is characterized by comprising a variable reciprocating scraper sliding on the base for scraping a fixed amount of discharged accumulated matter.

以下本発明を附図を参照しつつ説明する。The present invention will be explained below with reference to the accompanying drawings.

第1図は本発明のスクレーパを用いた連続移動層式気固
接触装置の立面図、第2図は第1図の装置の平面図であ
る。
FIG. 1 is an elevational view of a continuous moving bed type gas-solid contact apparatus using the scraper of the present invention, and FIG. 2 is a plan view of the apparatus shown in FIG. 1.

第1図において、粒子ホッパ2、バッフルプレート4お
よび5から成る気固接触装置3内に固体粒子状物質9が
充満されている。
In FIG. 1, a gas-solid contact device 3 consisting of a particle hopper 2 and baffle plates 4 and 5 is filled with solid particulate matter 9.

処理ガス導管7,8が前記装置3を横切って取付けられ
、処理ガスは人口Aから入り固体粒子状物質移動層6を
通過して出口Bに流通される。
Process gas conduits 7, 8 are installed across said apparatus 3, with process gas entering at port A and flowing through solid particulate matter transfer bed 6 to outlet B.

気固接触装置3の下方側壁部はその奥行に亘って溝孔形
状に構成されているから該気固接触装置内の物質9は図
示のようにその自重によって基台10上に安息角分量を
形成する(角α入 本発明による装置を実施する排出機構の一実施例ではス
クレーパ1はガス流と直交するバッフルプレート4,5
と平行に基台10上を摺動しつつ往復運動し、前記物質
の定量を掻取る。
Since the lower side wall of the gas-solid contact device 3 is configured in the shape of a slot over its depth, the substance 9 in the gas-solid contact device 3 deposits an angle of repose on the base 10 by its own weight as shown in the figure. In one embodiment of the ejection mechanism implementing the device according to the invention, the scraper 1 has baffle plates 4, 5 orthogonal to the gas flow.
It reciprocates while sliding on the base 10 parallel to the above, and scrapes off a fixed amount of the substance.

掻取り後は気固接触装置内の物質は重力によって直ちに
その安息角を形成し、この容積は一定である。
After scraping, the material in the gas-solid contact device immediately forms its angle of repose due to gravity, and its volume remains constant.

これによって収容物質は極めて自然に、障害を受けずに
常に定量が掻取られると同時に常に爾后の操作の受入準
備状態が完成され粒子の破損も従来の装置に比して極め
て少ない。
As a result, the contained material is always scraped off in a quantitative manner in a very natural and unobstructed manner, and at the same time is always ready for subsequent operation, and particle breakage is significantly less than in conventional devices.

排出機構の運動は往復動であるから操作が簡単かつ平滑
で保守性1こすぐれた定量性が保証される。
Since the movement of the discharge mechanism is reciprocating, the operation is simple and smooth, and excellent quantitative performance with ease of maintenance is guaranteed.

本発明の装置を各種条件および状態下で従来装置と比較
実験した結果を粒子破損度を例として示せば、ロータリ
フィーダ法に対し1/70〜1/110、電磁振動フィ
ーダ法に対し1/2〜1/l 5、ダンパ法に対し11
5〜1/6、テーブルフィーダ法に対しl/1.5〜1
/2であり、定量性とともに抜群の効果を示している。
The results of a comparative experiment of the device of the present invention with a conventional device under various conditions and conditions show that the degree of particle breakage is 1/70 to 1/110 compared to the rotary feeder method and 1/2 compared to the electromagnetic vibration feeder method. ~1/l 5, 11 for damper method
5-1/6, l/1.5-1 for table feeder method
/2, showing outstanding effectiveness as well as quantitative performance.

なお、本発明の装置は、電動機、空気圧等を動力に用い
て自動連続操作方式とすることができ、またタイマーの
使用により任意間欠的に排出せしめることも可能である
The device of the present invention can be operated automatically and continuously using an electric motor, pneumatic pressure, or the like as power, or can be discharged intermittently at will by using a timer.

さらに安息角形成部位を通過する継目なしベルト上に装
備した掻取器を用いることもできる。
Furthermore, it is also possible to use a scraper mounted on a seamless belt that passes through the area where the angle of repose is formed.

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

第1図は本発明による排出装置を用いる連続移動層式気
固接触装置の立面図、第2図は第1図装置の平面図であ
る。 1・・・・・・スクレーパ、2・・・・・・固体粒子状
物質ホッパ、3・・・・・・気固接触装置、4・・・・
・・バッフルプレート、5・・・・・・バッフルプレ〜
ト、6・・・・・・固体粒子状物質移動層、7・・・
・・・導管、8・・・・・・導管、9・・・・・・固体
粒子状物質、10・・・・・・基台。
FIG. 1 is an elevational view of a continuous moving bed type gas-solid contact apparatus using a discharge device according to the present invention, and FIG. 2 is a plan view of the apparatus shown in FIG. 1. 1... Scraper, 2... Solid particulate matter hopper, 3... Gas-solid contact device, 4...
... Baffle plate, 5... Baffle plate ~
g, 6... solid particulate matter transfer layer, 7...
... conduit, 8 ... conduit, 9 ... solid particulate matter, 10 ... base.

Claims (1)

【特許請求の範囲】[Claims] 1易破砕性の固体粒子状活性物質により移動層を形成し
、該移動層に被処理気体を通過せしめて接触操作を行う
連続移動層式気固接触装置において、該装置の底部より
活性の減少した上記固体物質を破砕を伴うことなく定量
的に排出する装置であって、(1)上記接触装置直下に
設けた基台、(2)該基台上に上記固体物質を安息角形
成相当分量排出集積せしめる上記接触装置下方側壁部に
設けた切欠部、(3)および前記排出された集積物質を
一定量掻ぎ取る上記基台上を摺動する可変往復運動式ス
クレーパよりなることを特徴とする活性の減少した固体
粒子状物質の定量排出装置。
1. In a continuous moving bed type gas-solid contact device in which a moving bed is formed of an easily shatterable solid particulate active substance and a gas to be treated passes through the moving bed to perform a contact operation, the activity decreases from the bottom of the device. A device for quantitatively discharging the above-mentioned solid substance without crushing, comprising: (1) a base provided directly below the above-mentioned contact device; (2) an amount of the solid substance equivalent to forming an angle of repose on the base; (3) a notch provided in the lower side wall of the contact device for discharge and accumulation; and a variable reciprocating scraper that slides on the base for scraping a certain amount of the discharged accumulated material. A device for quantitatively discharging solid particulate matter with reduced activity.
JP51044968A 1976-04-22 1976-04-22 Solid particulate matter discharge equipment Expired JPS5924051B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP51044968A JPS5924051B2 (en) 1976-04-22 1976-04-22 Solid particulate matter discharge equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP51044968A JPS5924051B2 (en) 1976-04-22 1976-04-22 Solid particulate matter discharge equipment

Publications (2)

Publication Number Publication Date
JPS52140161A JPS52140161A (en) 1977-11-22
JPS5924051B2 true JPS5924051B2 (en) 1984-06-06

Family

ID=12706267

Family Applications (1)

Application Number Title Priority Date Filing Date
JP51044968A Expired JPS5924051B2 (en) 1976-04-22 1976-04-22 Solid particulate matter discharge equipment

Country Status (1)

Country Link
JP (1) JPS5924051B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5878916A (en) * 1981-06-24 1983-05-12 Daido Steel Co Ltd Supply apparatus and method

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4854662A (en) * 1971-11-11 1973-08-01

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4854662A (en) * 1971-11-11 1973-08-01

Also Published As

Publication number Publication date
JPS52140161A (en) 1977-11-22

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