JPS63243697A - Heat exchanger provided with shot cleaning device - Google Patents
Heat exchanger provided with shot cleaning deviceInfo
- Publication number
- JPS63243697A JPS63243697A JP7451187A JP7451187A JPS63243697A JP S63243697 A JPS63243697 A JP S63243697A JP 7451187 A JP7451187 A JP 7451187A JP 7451187 A JP7451187 A JP 7451187A JP S63243697 A JPS63243697 A JP S63243697A
- Authority
- JP
- Japan
- Prior art keywords
- water
- hopper
- valve
- steel balls
- 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
- 238000004140 cleaning Methods 0.000 title claims description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 60
- 238000011084 recovery Methods 0.000 claims description 12
- 238000000926 separation method Methods 0.000 claims description 7
- 238000007789 sealing Methods 0.000 claims 2
- 229910000831 Steel Inorganic materials 0.000 abstract description 39
- 239000010959 steel Substances 0.000 abstract description 39
- 239000007789 gas Substances 0.000 abstract description 38
- 239000004071 soot Substances 0.000 abstract description 15
- 239000011261 inert gas Substances 0.000 abstract description 5
- 230000000694 effects Effects 0.000 abstract description 3
- 241001365789 Oenanthe crocata Species 0.000 abstract 1
- 238000010586 diagram Methods 0.000 description 5
- 238000006243 chemical reaction Methods 0.000 description 4
- 238000010926 purge Methods 0.000 description 4
- 239000002341 toxic gas Substances 0.000 description 4
- 239000012530 fluid Substances 0.000 description 3
- 238000007664 blowing Methods 0.000 description 2
- 239000000428 dust Substances 0.000 description 2
- 239000011435 rock Substances 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- 241001062872 Cleyera japonica Species 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 238000001784 detoxification Methods 0.000 description 1
- 238000005553 drilling Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000002309 gasification Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000013020 steam cleaning Methods 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Landscapes
- Cleaning In General (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、排ガスエコノマイザ及び反応容器等に設置さ
れる加圧ガス、毒性ガス、可燃性ガス榊熱交換器におい
て、熱交換部のスートを除去する装置を具えた熱交換器
に関するもので、熱交換器の代シに反応容器に適用し反
応部のスート除去を行うことも可能である。Detailed Description of the Invention [Industrial Application Field] The present invention is a pressurized gas, toxic gas, flammable gas Sakaki heat exchanger installed in an exhaust gas economizer, a reaction vessel, etc. This invention relates to a heat exchanger equipped with a device for removing soot, and can be applied to a reaction vessel instead of a heat exchanger to remove soot from the reaction section.
加圧容器又は毒性ガス、可燃性ガス等の発生容器におい
て、熱交換部のスートを除去するために、鋼球等を使用
するショットクリーニング装置を具えた熱交換器では、
鋼球等の供給、回収に、イナートガス等を使用したロッ
クホッパシステムヲ用いている。In a pressurized container or a container generating toxic gas, flammable gas, etc., in a heat exchanger equipped with a shot cleaning device that uses steel balls etc. to remove soot from the heat exchange part,
A lock hopper system using inert gas is used to supply and collect steel balls, etc.
従来のシステムを、ショットクリーニング装置を具えた
加圧壓熱交換器の1例を示す第4図に従って説明する。A conventional system will be explained with reference to FIG. 4, which shows an example of a pressurized heat exchanger equipped with a shot cleaning device.
同図において、ガスはガス導入部1よシ熱交換器2に入
り、熱交換部3によシ冷却された後、ガス排出部4よシ
器外へ排出される。In the figure, gas enters a heat exchanger 2 through a gas introduction section 1, is cooled by a heat exchange section 3, and is then discharged to the outside of the device through a gas discharge section 4.
ガス中に含まれるスートは主に熱交換部3に付着するス
ートズローに供する鋼球等は受入ホッパ5よシ気密弁6
を通シ供給ロックホッパ7へ入る。The soot contained in the gas mainly adheres to the heat exchange section 3. Steel balls, etc. to be used for the soot flow are transferred to the receiving hopper 5 and then to the airtight valve 6.
It enters the feed lock hopper 7 through the passage.
鋼球がロックホッノ7へ充填されると気密弁6を閉じ、
加圧弁8よシイナートガス等により加圧し、供給ロック
ホッパ7内の圧力を熱又換器2と同圧にした後、供給弁
9を開は鋼球を熱交換器2内へ落下させる。鋼球の落下
が終了すると、供給弁9を閉じると共に、パージ弁10
を開け、供給ロックホッパ7内の圧力を常圧にした後、
再度受入ホッパ5からの供給を待つ、落下した鋼球は、
加圧弁11により熱交換器2と同圧になった回収ホッパ
12に回収弁13を通シ回収される。回収が終了したら
回収弁13を閉じパージ弁14を開は回収ホッパ12内
を減圧した後、排出弁15を開け、コン(ヤ16又は気
流搬送によシ上部の受入ホッパく5へ再度供給される。When the steel balls are filled into the rock hook 7, the airtight valve 6 is closed,
After the pressure in the supply lock hopper 7 is made the same as that in the heat exchanger 2 by pressurizing the supply lock hopper 7 with Cyinert gas or the like through the pressurization valve 8, the supply valve 9 is opened and the steel balls are allowed to fall into the heat exchanger 2. When the steel balls have finished falling, the supply valve 9 is closed and the purge valve 10 is closed.
After opening the supply lock hopper 7 and bringing the pressure inside the supply lock hopper 7 to normal pressure,
The fallen steel balls are waiting to be supplied from the receiving hopper 5 again.
It passes through the recovery valve 13 to the recovery hopper 12 which has the same pressure as the heat exchanger 2 due to the pressurizing valve 11 and is recovered. When the recovery is completed, the recovery valve 13 is closed and the purge valve 14 is opened to reduce the pressure inside the recovery hopper 12, and then the discharge valve 15 is opened, and the waste is again supplied to the receiving hopper 5 at the top of the container by air flow conveyance. Ru.
前述のように鋼球等をショットクリーニングに使用する
熱交換器において、内部のガスが加圧又は可燃性ガス又
は毒性ガスの場合には次の問題点がある。As mentioned above, in a heat exchanger that uses steel balls or the like for shot cleaning, if the gas inside is pressurized, flammable gas, or toxic gas, the following problems occur.
つま#)@球の供給、排出には外部の大気と接触するた
め、ロックホッパ等の容器が必要となシ、この加圧・減
圧のためのイナートガス消費量が膨大となる。Since the supply and discharge of the bulbs come into contact with the outside atmosphere, a container such as a lock hopper is required, and the amount of inert gas consumed for this pressurization and depressurization is enormous.
また容器内部のガスとして毒性ガス等の危険性を有する
ガスを扱う場合は、ロックホッパのノ耐−ジに困難を生
ずる。このため安全性に問題があると共に、加圧媒体に
使用するイナートガス等の消費量が膨大となシ性能の低
下をもたらす。Furthermore, when handling a dangerous gas such as a toxic gas as the gas inside the container, the lock hopper will have difficulty in resisting the leakage. For this reason, there is a problem with safety, and the amount of consumption of inert gas used as a pressurizing medium is enormous, resulting in a decrease in performance.
前述の公知技術における問題点を解消するためして、気
体加圧のロックホッパの替シに、水を用いたホッパを設
ける。即ち、圧、縮性流体である気体加圧でなく、非圧
縮性流体の水を使用し容器内の加圧を行う。In order to solve the problems in the prior art described above, a hopper using water is provided as a replacement for the gas pressurized lock hopper. That is, the inside of the container is pressurized using water, which is an incompressible fluid, instead of pressurizing gas, which is a compressible fluid.
熱交換器の内部ガスとショットクリーニング洗使用する
鋼球等が容易に分離する。事ができ、ユーティリティの
面でも安全性の面でも信頼性が向上する。また内部ガス
が毒性又は可燃性ガスの場合でも、水によシガスを押し
出せるため、パージも必要なくなる。The internal gas of the heat exchanger and the steel balls used for shot cleaning are easily separated. This improves reliability in terms of both utility and safety. Furthermore, even if the internal gas is toxic or flammable, the water can push out the gas, eliminating the need for purging.
第1図において、1はガス導入部、2は熱交換器、3は
熱交換部、4はガス排出部、5は受入ホッノセ、6は気
密弁、7は供給ホッパ、8は分離フィルタ、9は給水ポ
ンプ、10は給水弁、11は均圧弁、12は水ブロー弁
、13は下部水槽、14は供給弁、15は回収ホッパ、
16は給水弁、17は気密弁、18は回収弁、19はジ
ェットポンプ等のポンプ、加は循環水槽、21はオーバ
ー70−管、nは水洗又は蒸気洗浄ノズル、nは分離フ
ィルタ、あけ鋼球、セラミックボール等のショット、5
は鋼球受板である。In FIG. 1, 1 is a gas introduction part, 2 is a heat exchanger, 3 is a heat exchange part, 4 is a gas discharge part, 5 is a receiving valve, 6 is an airtight valve, 7 is a supply hopper, 8 is a separation filter, 9 is a water supply pump, 10 is a water supply valve, 11 is a pressure equalization valve, 12 is a water blow valve, 13 is a lower water tank, 14 is a supply valve, 15 is a collection hopper,
16 is a water supply valve, 17 is an airtight valve, 18 is a recovery valve, 19 is a pump such as a jet pump, addition is a circulation water tank, 21 is an over 70-pipe, n is a water washing or steam cleaning nozzle, n is a separation filter, and a drilling steel. Shots of balls, ceramic balls, etc., 5
is a steel ball receiving plate.
このような装置において、加圧ガス、彬性ガス又は可燃
性ガスは、ガス導入部1より熱交換器2を通シ、熱交換
部3において冷却された後、ガス排出部4よシ器外へ排
出される。ガス中に含まれるスートは主に熱交換部3に
付着する。ショットクリーニングのために、鋼球等を熱
交換器2に供給、し、更に@収する方法を順を追って説
明する。In such a device, pressurized gas, flammable gas, or combustible gas is passed through a heat exchanger 2 from a gas inlet 1, cooled in a heat exchanger 3, and then discharged from a gas outlet 4 to the outside of the device. is discharged to. The soot contained in the gas mainly adheres to the heat exchange section 3. A method for supplying steel balls and the like to the heat exchanger 2 and collecting them for shot cleaning will be explained step by step.
スートプローのショットクリーニングに使用する鋼球等
のショットかは、受入ホッパ5の分離フィルタだ貯えら
れる。気密弁6を開は鋼球Mを水が充満し供給ホッパ7
に落下させる。鋼球は供給ホッパ内部の分離フィルタ8
の上部に貯まる。給水ポンプ9によシ、給水弁1oを介
し供給ホッパ7に水を供給する。水が受入ホッパ5側に
オーバーフローする満水状態にて気密弁6を閉じ、更に
給水ポンプで熱交換器2内のガス圧力と同等の圧力まで
水によシ加圧する。(水圧をあげる)供給ホッパ7の加
圧が終了すると、均圧弁11を開けると共に水ブロー弁
12を開け、供給ホッパ7内部の水を下部水槽13へ落
とす。これ洗より鋼球は分離フィルタ8によシ水と分離
される。Shots such as steel balls used for shot cleaning of the soot blower are stored in the separation filter of the receiving hopper 5. When the airtight valve 6 is opened, the steel ball M is filled with water and the supply hopper 7 is opened.
let it fall. The steel balls are separated by the separation filter 8 inside the supply hopper.
It accumulates at the top of the. The water supply pump 9 supplies water to the supply hopper 7 via the water supply valve 1o. The airtight valve 6 is closed when the water overflows to the receiving hopper 5 side, and the water is further pressurized to the same pressure as the gas pressure inside the heat exchanger 2 using the water supply pump. (Increase the water pressure) When the supply hopper 7 is pressurized, the pressure equalization valve 11 is opened and the water blow valve 12 is opened to cause the water inside the supply hopper 7 to drop into the lower water tank 13. After this washing, the steel balls are separated from the water by a separation filter 8.
次に供給弁14を開は熱交換器2の熱交換部3へ鋼球冴
を落下させ、ショットクリーニングによるスートプロー
を行い、鋼球冴は下部水槽13へ回収される。鋼球Uが
供給ホッパ7から落下したら、供給弁14、水プロー弁
12を閉じ、給水ポンプ9によシ供給ホクノ<7に水を
供給し、内部のガスを均圧弁11を通し下流へ排出し、
供給ホッパ7に水が満たされたら均圧弁11を閉じ、受
入ホッパ5からの鋼球冴の再供給て備える。下部水槽1
3へ落下回収され、器内のスートプローを終了した鋼球
冴は、給水ポンプ9によシ給水弁16を通9水で加圧さ
れた回収ホッパ15へ、気密弁17を通)回収される。Next, the supply valve 14 is opened, and the steel balls are dropped into the heat exchange section 3 of the heat exchanger 2, soot blowing is performed by shot cleaning, and the steel balls are collected into the lower water tank 13. When the steel ball U falls from the supply hopper 7, the supply valve 14 and the water plow valve 12 are closed, water is supplied to the supply tank 7 by the water supply pump 9, and the internal gas is discharged downstream through the pressure equalization valve 11. death,
When the supply hopper 7 is filled with water, the pressure equalization valve 11 is closed, and the steel balls from the receiving hopper 5 are resupplied. Lower water tank 1
The steel balls that have been collected by the water supply pump 9 and have completed the soot blowing in the vessel are collected by the water supply pump 9 through the water supply valve 16 and into the collection hopper 15 pressurized with water (through the airtight valve 17). .
回収が終了すると、気密弁17を再度閉じ、鋼球は回収
弁18を通シジェットポンプ19によシ上部ホッパ5へ
移送する。鋼球24の移送が終了すると、回収ホッパ1
5は再度水により加圧し、再回収に備える。上部ホッノ
ベ5の分離フィルタnに貯えられた鋼球冴は、必要によ
シノズルnより噴出した水又は蒸気によシ鋼球に付着し
たスートを洗浄し、再度循環使用に備える。鋼球の移送
水及び鋼球脚の洗浄水は、排水管21によシ循環水槽加
へ排水され再循環使用される。When the recovery is completed, the airtight valve 17 is closed again, and the steel balls are transferred to the upper hopper 5 through the recovery valve 18 by the jet pump 19. When the transfer of the steel balls 24 is completed, the recovery hopper 1
5 is again pressurized with water to prepare for re-collection. The steel balls stored in the separation filter n of the upper hot pot 5 are cleaned of soot adhering to the steel balls by water or steam spouted from the nozzle n as necessary, and prepared for circulation again. The water for transferring the steel balls and the water for cleaning the steel ball legs are drained to a circulation water tank through a drain pipe 21 and used for recirculation.
なお、前述の実施例におけるジェットポンプ19による
鋼球の移送は、コンベヤ方式による代用も可能である。Note that the conveyance of the steel balls by the jet pump 19 in the above embodiment may be replaced by a conveyor system.
熱交換部3の内部を通る流体は、ガスでも液体でもよい
。熱交換器2としては、例えば、ガス化炉、反応容器、
燃焼装置等のガス冷却装置があや、いかなるガス圧力、
ガス組成に対しても、またガス中のばいじん量の多少に
か\わらず、本発明を実施することによシ、効果的なス
ート除去が可能である。The fluid passing through the heat exchange section 3 may be either gas or liquid. As the heat exchanger 2, for example, a gasification furnace, a reaction vessel,
If a gas cooling device such as a combustion device is
By carrying out the present invention, effective soot removal is possible regardless of the gas composition or the amount of soot and dust in the gas.
なお熱交換器2内部からの鋼球Uの回収に際し、必要に
よ如回収ホッパ13の内部に鋼球愛敬5を設置し、ガス
中のばいじんを効果的にガス排出部4側へガスと一諸に
排出する事も可能である。In addition, when recovering the steel balls U from inside the heat exchanger 2, a steel ball Aikei 5 is installed inside the recovery hopper 13 as necessary to effectively unite the soot and dust in the gas to the gas discharge part 4 side. It is also possible to discharge it to various sources.
第2図は他の実施例であシ、鋼球訊の洗浄装置n′を回
収ホッパ15′内(C設置する。本例では、シロブト後
の鋼球は清浄後に受入ホッパ5へ搬送され、鋼球の受入
れホッパ5への搬送には蒸気又は空気を使用する気流搬
送ノズル19′も使用できる。FIG. 2 shows another embodiment, in which a steel ball cleaning device n' is installed in a recovery hopper 15' (C. A pneumatic conveying nozzle 19' using steam or air can also be used to convey the steel balls to the receiving hopper 5.
その他の構成は第1図の実施例と同様である。The rest of the structure is the same as the embodiment shown in FIG.
また、第1図、第2図では鋼球冴を下部水槽13で回収
しているが、下部水槽13を特に設けない構造も可能で
あシ、この場合供給ホッパ7からのプロー水は直接循環
水槽ヘブローする。この場合の下部構造の1例を第3図
に示す。In addition, although the steel balls are collected in the lower water tank 13 in Figs. 1 and 2, it is also possible to have a structure in which the lower water tank 13 is not particularly provided, and in this case, the plow water from the supply hopper 7 is directly circulated. Aquarium hebrow. An example of the lower structure in this case is shown in FIG.
第3図では熱交換器2の熱交換部3のスートを除去した
鋼球は銅球のみ通過出来ない程度のフィルター8“によ
シ捕果され、気密弁17“を通シ水で充満された回収ホ
ッパ15“へ回収される。それ以外の構成は第1図の実
施例と同様である。In Fig. 3, the steel balls from which soot has been removed in the heat exchange section 3 of the heat exchanger 2 are collected by a filter 8'' that is large enough to only allow the copper balls to pass through, and then filled with water through an airtight valve 17''. The other components are the same as the embodiment shown in FIG. 1.
本発明により、従来ロックホラ・1加圧用に必要であっ
た100〜300 Nm3/hのイナートガスの使用量
がOになると共に、補給水量はわずか1mX程度で済む
。According to the present invention, the amount of inert gas used of 100 to 300 Nm3/h, which was conventionally required for pressurizing a rock hole, can be reduced to 0, and the amount of make-up water can be reduced to only about 1 mX.
またパージガスの処理として従来は必要であったフレア
スタック等の除害装置が不要になる。Furthermore, a detoxification device such as a flare stack, which was conventionally necessary for processing purge gas, becomes unnecessary.
また熱交換部の表面を清浄に保ち、良好な熱交換特性を
維持することができる。Furthermore, the surface of the heat exchange section can be kept clean and good heat exchange characteristics can be maintained.
第1図は本発明シ目ットクリーニング装置を有する熱交
換器の実施例の概略図、第2図は本発明の他の実施例の
概略図、第3図は本発明の更に他の実施例の下部構造の
概略図、第4図は従来装置の概略図である。FIG. 1 is a schematic diagram of an embodiment of a heat exchanger having a seam cleaning device according to the present invention, FIG. 2 is a schematic diagram of another embodiment of the present invention, and FIG. 3 is a schematic diagram of another embodiment of the present invention. FIG. 4 is a schematic diagram of an example lower structure, and FIG. 4 is a schematic diagram of a conventional device.
Claims (1)
に連通して設置されたショットの供給ホッパと、流入部
および流出部にそれぞれ弁を有し熱交換器の下部に連通
して設置されたショットの回収ホッパとを具え、前記供
給ホッパには水の供給、排出手段およびショットと水の
分離フイルタを設け、前記回収ホッパには水の供給、排
出手段を設け、前記供給ホッパにより熱交換器に対する
ショットの供給とガスシールを行ない、前記回収ホッパ
により熱交換器からのショットの回収とガスシールを行
なうようにしたことを特徴とするショットクリーニング
装置を有する熱交換器。A shot supply hopper has valves at the inflow and outflow sections and is installed in communication with the top of the heat exchanger, and a shot supply hopper has valves in the inflow and outflow sections and is installed in communication with the bottom of the heat exchanger. said supply hopper is provided with water supply and discharge means and a shot and water separation filter; said collection hopper is provided with water supply and discharge means; A heat exchanger having a shot cleaning device, characterized in that shot is supplied to the exchanger and gas sealing is performed, and shot is recovered from the heat exchanger and gas sealing is performed by the recovery hopper.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP7451187A JPS63243697A (en) | 1987-03-30 | 1987-03-30 | Heat exchanger provided with shot cleaning device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP7451187A JPS63243697A (en) | 1987-03-30 | 1987-03-30 | Heat exchanger provided with shot cleaning device |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS63243697A true JPS63243697A (en) | 1988-10-11 |
Family
ID=13549425
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP7451187A Pending JPS63243697A (en) | 1987-03-30 | 1987-03-30 | Heat exchanger provided with shot cleaning device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS63243697A (en) |
-
1987
- 1987-03-30 JP JP7451187A patent/JPS63243697A/en active Pending
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