JPH02214554A - Method for preventing clogging of gas-solid separation cyclone - Google Patents
Method for preventing clogging of gas-solid separation cycloneInfo
- Publication number
- JPH02214554A JPH02214554A JP3281789A JP3281789A JPH02214554A JP H02214554 A JPH02214554 A JP H02214554A JP 3281789 A JP3281789 A JP 3281789A JP 3281789 A JP3281789 A JP 3281789A JP H02214554 A JPH02214554 A JP H02214554A
- Authority
- JP
- Japan
- Prior art keywords
- gas
- cyclone
- solid
- discharge port
- compressed gas
- 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
- 239000007787 solid Substances 0.000 title claims abstract description 51
- 238000000926 separation method Methods 0.000 title claims abstract description 25
- 238000000034 method Methods 0.000 title claims description 17
- 239000002245 particle Substances 0.000 claims description 26
- JTJMJGYZQZDUJJ-UHFFFAOYSA-N phencyclidine Chemical class C1CCCCN1C1(C=2C=CC=CC=2)CCCCC1 JTJMJGYZQZDUJJ-UHFFFAOYSA-N 0.000 claims description 7
- 239000000463 material Substances 0.000 abstract description 3
- 238000002347 injection Methods 0.000 abstract 3
- 239000007924 injection Substances 0.000 abstract 3
- 239000007789 gas Substances 0.000 description 32
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 description 12
- 239000004202 carbamide Substances 0.000 description 12
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 9
- 229920001577 copolymer Polymers 0.000 description 6
- 239000000843 powder Substances 0.000 description 4
- 229910001873 dinitrogen Inorganic materials 0.000 description 3
- 229910052757 nitrogen Inorganic materials 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 2
- 239000005977 Ethylene Substances 0.000 description 2
- 239000000853 adhesive Substances 0.000 description 2
- 230000001070 adhesive effect Effects 0.000 description 2
- 230000008014 freezing Effects 0.000 description 2
- 238000007710 freezing Methods 0.000 description 2
- 239000003570 air Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Landscapes
- Separating Particles In Gases By Inertia (AREA)
- Cyclones (AREA)
Abstract
Description
【発明の詳細な説明】
(a)発明の目的
(産業上の利用分野)
本発明は、固体粒子を含有する気体、特に付着性や粘着
性に富む固体粒子を含有する気体を分離する気体固体分
離サイクロンの閉塞防止方法に関する。Detailed Description of the Invention (a) Object of the Invention (Field of Industrial Application) The present invention relates to a gas-solid method for separating gases containing solid particles, particularly gases containing highly adhesive and sticky solid particles. This invention relates to a method for preventing blockage of a separation cyclone.
(従来技術)
従来、固体粒子を含有する気体をサイクロンで処理して
固体粒子を気体より分離することは広く行なわれている
。かかる気体固体分離、特に付着性や粘着性に富む固体
粒子を含有する気体のサイクロン分離においては、サイ
クロン内、特にサイクロン上部空間等に固体粒子が付着
し、時間の経過とともにその付着粒子が成長して1分離
能力を低下させることになる。かかる固体粒子の付着及
びその成長を防止する手段として、従来、サイクロン外
部からサイクロン壁面に振動又は衝撃を与えて付着物を
剥離落下させたり、付着物に流動性を与えたりして、下
部排出口から排出させる方法が用いられていた。この方
法は、サイクロン壁面の振動や衝撃により剥離落下した
固形物が下部排出口から排出され、同排出口を閉塞せし
めない限〕において有効である。(Prior Art) Conventionally, it has been widely practiced to treat a gas containing solid particles with a cyclone to separate the solid particles from the gas. In such gas-solid separation, especially in cyclone separation of gases containing highly adhesive and sticky solid particles, solid particles adhere to the inside of the cyclone, especially in the space above the cyclone, and the adhered particles grow over time. This will reduce the separation capacity by 1. Conventionally, as a means to prevent the adhesion and growth of such solid particles, vibration or shock is applied to the cyclone wall surface from outside the cyclone to cause the adhering material to peel off and fall, or to give fluidity to the adhering material, and the lower discharge port is A method was used to discharge it from the This method is effective as long as solid matter that has fallen off due to vibration or impact on the cyclone wall is discharged from the lower discharge port and does not block the discharge port.
しかし、固形物粒子の種類等によっては、前記の壁面の
振動や衝撃によって剥離落下した固形物が下部排出口か
ら排出されずにサイクロン排出口を閉塞させることが起
きる。たとえば、尿素の低濃度空気輸送の場合に、尿素
含有空気よりサイクロンを用い粉末尿素を分離する際に
は、サイクロン下部排出口付近に尿素が固着してブリッ
ジ状の固結物となってサイクロン出口を閉塞させること
になシ、かかるブリッジ状の固結尿素は、前記したサイ
クロン外部からの壁面への振動や衝撃によっても排出さ
せることができない。However, depending on the type of solid particles, the solids that have peeled off and fallen due to the vibration or impact of the wall surface may not be discharged from the lower discharge port and may clog the cyclone discharge port. For example, in the case of pneumatic transport of low concentration urea, when a cyclone is used to separate powdered urea from the urea-containing air, the urea sticks to the vicinity of the lower discharge port of the cyclone and forms a bridge-like solidified substance, leaving the cyclone exit. However, such bridge-shaped solidified urea cannot be discharged even by vibration or impact on the wall surface from outside the cyclone.
(発明の課題) 本発明は、気体固体分離サイクロンを用いて。(Problem to be solved by the invention) The present invention uses a gas-solid separation cyclone.
固体粒子含有気体を分離する際の同サイクロンの閉塞を
防止する方法を提供しようとするものである。The object of the present invention is to provide a method for preventing clogging of the cyclone when separating a gas containing solid particles.
(b)発明の構成
(課題解決のための手段)
本発明の気体固体分離サイクロンの閉塞防止方法は、気
体固体サイクロン内に圧縮気体噴出口を設けておき、該
圧縮気体噴出口より圧縮気体を瞬時に1回又は複数回噴
射することを特徴とする方法である。(b) Structure of the Invention (Means for Solving the Problem) The method for preventing blockage of a gas-solid separation cyclone of the present invention includes providing a compressed gas outlet in the gas-solid cyclone, and discharging compressed gas from the compressed gas outlet. This method is characterized by instantaneously injecting the liquid once or multiple times.
本発明の方法を用いると、サイクロン内に付着した固体
粒子やその剥離落下物によって形成されたブリッジ状の
固結物などは、噴射する圧縮気体の衝撃力によって容易
に破砕されて、サイクロン下部の排出口から容易に排出
されるので、サイクロンの閉塞を極めて有効に防止でき
るのである。When the method of the present invention is used, solid particles adhering to the inside of the cyclone and bridge-shaped solidified objects formed by their peeling and falling objects are easily crushed by the impact force of the injected compressed gas, and the solid particles at the bottom of the cyclone are easily crushed. Since it is easily discharged from the outlet, clogging of the cyclone can be extremely effectively prevented.
本発明における圧縮気体の噴出口を設ける位置は、サイ
クロン下部、好ましくはサイクロン内下部、特に固体粒
子排出口の上部の近辺である。In the present invention, the compressed gas outlet is provided at the lower part of the cyclone, preferably at the lower part of the cyclone, particularly near the upper part of the solid particle outlet.
また、本発明における噴出させる気体は、分離する気体
や固体粒子に化学的に不活性なものが用いられ、その具
体例としては、たとえば空気、窒素、炭酸ガス等があげ
られる。また、特殊な気体固体の分離においては、これ
ら以外の種々の気体も使用することができる。噴射する
圧縮気体の圧力は、通常2〜10 kl//cts2G
、好ましくは3〜61回以上、好ましくは数分又は数秒
間隔で数回〜10回程同行なわせる。Further, the gas to be ejected in the present invention is one that is chemically inert to the gas and solid particles to be separated, and specific examples thereof include air, nitrogen, carbon dioxide, and the like. In addition, various gases other than these can also be used in the separation of special gases and solids. The pressure of the compressed gas to be injected is usually 2 to 10 kl//cts2G
, preferably 3 to 61 times or more, preferably several times to 10 times at intervals of several minutes or seconds.
本発明の方法は、気体固体分離サイクロンの複数基を適
宜に交互に使用して連続的に気体固体分離を行なわせる
場合の、分離に使用していないサイクロンに、圧縮気体
を噴射する態様で実施すると、サイクロンの閉塞を有効
に防止して、気体固体の分離を連続的に長期間行えるよ
うになる。The method of the present invention is carried out in such a manner that compressed gas is injected into the cyclones not used for separation when a plurality of gas-solid separation cyclones are used alternately as appropriate to perform gas-solid separation continuously. This effectively prevents clogging of the cyclone and allows continuous separation of gas and solids over a long period of time.
添付の第1図は、本発明の閉塞防止方法の実施に使用さ
れる気体固体分離サイクロンの一例を示す側面図である
。図中の1は気体固体分離サイクロンの本体であり、2
はその内筒であシ、3は固体粒子含有気体の入口であシ
、この入口はサイクロン下部1に対して接線方向く取付
けられている。The attached FIG. 1 is a side view showing an example of a gas-solid separation cyclone used to carry out the method for preventing blockages of the present invention. 1 in the figure is the main body of the gas-solid separation cyclone, and 2
3 is the inner cylinder, and 3 is the inlet for the solid particle-containing gas, and this inlet is attached tangentially to the cyclone lower part 1.
4は分離された気体の排出口、5は分離された固体粒子
の排出口である。6は圧縮気体?ンペであり、7はその
電磁排出弁である。4 is an outlet for the separated gas, and 5 is an outlet for the separated solid particles. Is 6 a compressed gas? 7 is its electromagnetic discharge valve.
この第1図に示したサイクロンを使用して固体粒子含有
気体をその人口3から接続方向く導入すると、固体粒子
は重力及び遠心力によりて下方に沈降・分離して、排出
口5から適宜に排出される。When the cyclone shown in FIG. 1 is used to introduce solid particle-containing gas from its population 3 in the connecting direction, the solid particles settle and separate downward due to gravity and centrifugal force, and are discharged from the outlet 5 as appropriate. be discharged.
また、分離した気体は上昇して、その排出口4より排出
される。かかる気体固体分離を適宜の時間実施したのち
、−旦固体粒子含有気体の導入を中止してから(又は複
数基のサイクロンを交互に使用して連続的に分離を行な
わせる場合には1分離に使用していない期間中に)、圧
縮気体ざンベの圧縮気体を電磁排出弁7を開いて、1回
又は適当な時間間隔で複数回、適当な圧力で瞬時に噴射
させると、サイクロン内に付着していた固体粒子がその
噴射の衝撃力によって剥離・落下するとともに、その剥
離落下し九固体粒子及び排出口5の近辺に固結していた
固体粒子の固結物も、その噴射の衝撃力によりて破砕さ
れるから、排出口5から容易に排出できることになり、
サイクロンの閉塞を効果的に防止することができるので
ある。Further, the separated gas rises and is discharged from the discharge port 4. After carrying out such gas-solid separation for an appropriate period of time, the introduction of the solid particle-containing gas is stopped (or if multiple cyclones are used alternately to carry out continuous separation, one separation is performed). When the compressed gas in the compressed gas tank is not in use), the electromagnetic discharge valve 7 is opened and the compressed gas is instantly injected at an appropriate pressure once or multiple times at appropriate time intervals. At the same time, the solid particles that had been peeled off and fell off due to the impact force of the jet, and the solid particles that had peeled off and fallen and the solid particles that had solidified near the discharge port 5 were also affected by the impact force of the jet. Since it is crushed by the process, it can be easily discharged from the discharge port 5.
This effectively prevents cyclone blockage.
(実施例) 以下に、実施例をあげて説明する。(Example) Examples will be described below.
実施例1
尿素の低濃度空気輸送系(温度:常温、空気圧:0、0
5 kl/w’G 、空気量: 850 Nm’/hr
、尿素量二4000に9./hr )によ多連続的に送
られてくる尿素粒子含有空気を、2基の尿素貯槽の各頂
部に取付けた2基の気体固体分離サイクロンに、155
分間隔交互に受入れて連続的に処理し、各サイクロンで
分離された尿素を下部の各尿素貯槽に落下させた。Example 1 Low concentration pneumatic transport system for urea (temperature: room temperature, air pressure: 0,0
5 kl/w'G, air volume: 850 Nm'/hr
, the amount of urea is 24,000 to 9. The air containing urea particles, which is continuously sent from
The urea was received alternately at minute intervals and processed continuously, and the urea separated by each cyclone was allowed to fall into each urea storage tank at the bottom.
この場合の尿素合有空気の受入停止後のサイクロンに、
5分間隔で3 ’に97cm Gの圧縮空気を2〜3回
瞬時に噴射させたところ(1回の噴射空気量は81)、
サイクロンの閉塞を効果的に防止でき。In this case, the cyclone after stopping receiving urea-containing air,
When compressed air of 97 cm G was injected instantaneously 2 to 3 times at 3' intervals at 5 minute intervals (the amount of air injected at one time was 81),
Can effectively prevent cyclone blockage.
前記の2基のサイクロンを交互に使用する長期間の連続
運転中にもサイクロンの閉寒は全く起らなかった。Even during long-term continuous operation in which the two cyclones were used alternately, no cyclone freezing occurred.
実施例2
解砕機で破砕されたエチレン・ゾロビレ/共重合体粉末
を加熱窒素ガス金柑いて低濃度窒素乾燥輸送(固体/気
体比=0.2)して、乾燥工程へ移送する場合の、その
送られてくるエチレン・プロピレン共重合体粉末含有窒
素から同衾重体を分離するサイクロンにおいて、本発明
の方法を適用した。Example 2 When the ethylene/zorobire/copolymer powder crushed in a crusher is transported to a drying process using heated nitrogen gas and dry transport with low concentration of nitrogen (solid/gas ratio = 0.2). The method of the present invention was applied to a cyclone that separates copolymer from nitrogen containing ethylene-propylene copolymer powder.
すなわち、かかるエチレン・プロピレン共重合体粉末の
低濃度窒素乾燥輸送においては、その窒素ガスとして約
60〜150℃の温度に加熱されたガスが用いられる。That is, in the dry transport of the ethylene-propylene copolymer powder at a low concentration of nitrogen, a gas heated to a temperature of about 60 to 150° C. is used as the nitrogen gas.
そしてたとえば、製品グレードの切替時のようなサイク
ロンへの共重合体の受入れを一時停止した場合には、停
止したサイクロンは、従来、閉塞を起すのはさけられな
かった。And when the reception of copolymer into a cyclone is temporarily stopped, such as during a product grade changeover, for example, the stopped cyclone has conventionally been unavoidable to become clogged.
しかるに、かかるエチレン・ゾロビレ/共重合体粉末の
受入れ停止時に、その受入停止直後のサイクロンに、本
発明にしたがって1分間隔で3回、3に9/an2Gの
圧縮窒素ガスを瞬時に噴射させたところ、サイクロンの
閉寒を完全に防止することができ喪。However, when the reception of the ethylene/zorobire/copolymer powder was stopped, compressed nitrogen gas of 3 to 9/an2G was instantaneously injected into the cyclone immediately after the reception was stopped three times at 1-minute intervals according to the present invention. However, it is possible to completely prevent the cyclone from freezing.
(c)発明の効果
本発明の方法を用いると、気体固体分離サイクロンの閉
塞を有効に防止することができる。(c) Effects of the Invention By using the method of the present invention, clogging of gas-solid separation cyclones can be effectively prevented.
第1図は本発明の実施に使用される気体固体分離サイク
ロンの側面図であり、図中の各群はそれぞれ下記のもの
を示す。
1・・・サイクロン本体
2山サイクロン内筒
3・・・固体粒子含有気体の入口
4・・・分離気体の排出口
5・・・分離固体粒子の排出口
6・・・圧縮気体メンベ
ア・・・電磁排出弁FIG. 1 is a side view of a gas-solid separation cyclone used in carrying out the present invention, and each group in the figure shows the following, respectively. 1...Cyclone main body Double cyclone inner cylinder 3...Inlet for gas containing solid particles 4...Outlet for separated gas 5...Outlet for separated solid particles 6...Compressed gas membrane... solenoid discharge valve
Claims (3)
けておき、該圧縮気体噴出口より圧縮気体を瞬時に1回
又は複数回噴射することを特徴とする気体固体分離サイ
クロンの閉塞防止方法。(1) A method for preventing blockage of a gas-solid separation cyclone, which comprises providing a compressed gas outlet in the gas-solid separation cyclone and instantaneously injecting compressed gas from the compressed gas outlet once or multiple times.
排出口の上部に設けておく第1請求項記載の方法。(2) The method according to claim 1, wherein the compressed gas outlet is provided above the solid particle outlet in the lower part of the cyclone.
気体固体分離を行ない、分離に使用していないときのサ
イクロン内に圧縮気体を噴射する第1請求項又は第2請
求項記載の方法。(3) The method according to claim 1 or 2, wherein gas-solid separation is performed by alternately using a plurality of gas-solid separation cyclones, and compressed gas is injected into the cyclones when they are not being used for separation.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3281789A JPH02214554A (en) | 1989-02-14 | 1989-02-14 | Method for preventing clogging of gas-solid separation cyclone |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3281789A JPH02214554A (en) | 1989-02-14 | 1989-02-14 | Method for preventing clogging of gas-solid separation cyclone |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH02214554A true JPH02214554A (en) | 1990-08-27 |
Family
ID=12369386
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3281789A Pending JPH02214554A (en) | 1989-02-14 | 1989-02-14 | Method for preventing clogging of gas-solid separation cyclone |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH02214554A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH11147054A (en) * | 1997-11-17 | 1999-06-02 | Hitachi Ltd | Dust removing device |
CN110145736A (en) * | 2019-06-21 | 2019-08-20 | 烟台龙源电力技术股份有限公司 | The adjusting method of cyclone separator, circulating fluidized bed boiler and the Effiency of whirlwind Separator |
-
1989
- 1989-02-14 JP JP3281789A patent/JPH02214554A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH11147054A (en) * | 1997-11-17 | 1999-06-02 | Hitachi Ltd | Dust removing device |
CN110145736A (en) * | 2019-06-21 | 2019-08-20 | 烟台龙源电力技术股份有限公司 | The adjusting method of cyclone separator, circulating fluidized bed boiler and the Effiency of whirlwind Separator |
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