JPS62120978A - Cleaning device with spray of crushed ice - Google Patents
Cleaning device with spray of crushed iceInfo
- Publication number
- JPS62120978A JPS62120978A JP25679185A JP25679185A JPS62120978A JP S62120978 A JPS62120978 A JP S62120978A JP 25679185 A JP25679185 A JP 25679185A JP 25679185 A JP25679185 A JP 25679185A JP S62120978 A JPS62120978 A JP S62120978A
- Authority
- JP
- Japan
- Prior art keywords
- ice
- ice particles
- tank
- cyclone
- fine
- 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 abstract description 39
- 239000007921 spray Substances 0.000 title abstract description 12
- 239000002245 particle Substances 0.000 claims abstract description 99
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims abstract description 63
- 239000000126 substance Substances 0.000 claims abstract description 32
- 229910052757 nitrogen Inorganic materials 0.000 claims abstract description 24
- 239000007788 liquid Substances 0.000 claims abstract description 17
- 229910001873 dinitrogen Inorganic materials 0.000 claims abstract description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 157
- 238000002347 injection Methods 0.000 claims description 20
- 239000007924 injection Substances 0.000 claims description 20
- 239000007789 gas Substances 0.000 claims description 18
- 239000007787 solid Substances 0.000 claims description 16
- 238000004519 manufacturing process Methods 0.000 claims description 10
- 238000005406 washing Methods 0.000 claims description 5
- 238000005507 spraying Methods 0.000 claims description 2
- 238000000746 purification Methods 0.000 claims 1
- 229910052785 arsenic Inorganic materials 0.000 abstract description 5
- 229910052698 phosphorus Inorganic materials 0.000 abstract description 5
- 230000002285 radioactive effect Effects 0.000 abstract description 3
- 229910052751 metal Inorganic materials 0.000 abstract description 2
- 239000002184 metal Substances 0.000 abstract description 2
- 230000001627 detrimental effect Effects 0.000 abstract 2
- 235000013339 cereals Nutrition 0.000 description 32
- 238000000034 method Methods 0.000 description 9
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 4
- RQNWIZPPADIBDY-UHFFFAOYSA-N arsenic atom Chemical compound [As] RQNWIZPPADIBDY-UHFFFAOYSA-N 0.000 description 4
- 239000011574 phosphorus Substances 0.000 description 4
- 241000894006 Bacteria Species 0.000 description 3
- 238000000227 grinding Methods 0.000 description 3
- 239000000356 contaminant Substances 0.000 description 2
- 239000008367 deionised water Substances 0.000 description 2
- 229910021641 deionized water Inorganic materials 0.000 description 2
- 238000000605 extraction Methods 0.000 description 2
- 231100000614 poison Toxicity 0.000 description 2
- 230000007096 poisonous effect Effects 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 231100000331 toxic Toxicity 0.000 description 2
- 230000002588 toxic effect Effects 0.000 description 2
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 description 1
- 244000062793 Sorghum vulgare Species 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000001580 bacterial effect Effects 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 210000003746 feather Anatomy 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 239000005457 ice water Substances 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 239000003456 ion exchange resin Substances 0.000 description 1
- 229920003303 ion-exchange polymer Polymers 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 1
- 210000003127 knee Anatomy 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 235000019713 millet Nutrition 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000010422 painting Methods 0.000 description 1
- 244000052769 pathogen Species 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 238000010248 power generation Methods 0.000 description 1
- 239000008213 purified water Substances 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 239000004065 semiconductor Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 230000003746 surface roughness Effects 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B24—GRINDING; POLISHING
- B24C—ABRASIVE OR RELATED BLASTING WITH PARTICULATE MATERIAL
- B24C1/00—Methods for use of abrasive blasting for producing particular effects; Use of auxiliary equipment in connection with such methods
- B24C1/003—Methods for use of abrasive blasting for producing particular effects; Use of auxiliary equipment in connection with such methods using material which dissolves or changes phase after the treatment, e.g. ice, CO2
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Disintegrating Or Milling (AREA)
- Cleaning In General (AREA)
Abstract
Description
【発明の詳細な説明】
〔発明の目的〕
(産業上の利用分野)
放射能を利用する各種の検査、機器、医療機械、或は原
子力を利用する発電装置を含む原子力装置には、放射能
を受けた汚染物質が強固に附着し、又砒素、燐等をイオ
ンとして投射する半導体機器製造装置には、砒素、燐等
の有害物質が附着し、或は又各種の病原体となる細菌を
研究するための細菌培養施設等の機器には、毒性細菌が
強固に附着するので、上述の機器、機械、装置の性能を
維持するためには定期的に上述の附着物を除去しなけれ
ばならない。[Detailed Description of the Invention] [Purpose of the Invention] (Industrial Application Field) Various inspections, equipment, medical machines that use radioactivity, or nuclear power equipment including power generation equipment that uses nuclear power contain radioactivity. In addition, harmful substances such as arsenic and phosphorus adhere to semiconductor device manufacturing equipment that projects arsenic, phosphorus, etc. as ions, and research is being conducted on bacteria that can become various pathogens. Toxic bacteria are strongly attached to equipment such as bacterial culture facilities used to carry out microorganisms, so in order to maintain the performance of the above-mentioned equipment, machinery, and devices, the above-mentioned adhesion must be removed periodically.
この発明は上述の、放射能を受けた汚染物質、砒素、燐
等の1害物質、或は毒性細菌等の附着している装置、機
器の部品の表面より、上述の附着物を氷粒を用いて除去
する、氷粒を噴射するクリーニング装置に関するもので
ある。This invention removes the above-mentioned adhering matter by removing ice particles from the surface of devices and equipment parts to which radioactive contaminants, harmful substances such as arsenic and phosphorus, or toxic bacteria are adhering. This invention relates to a cleaning device that sprays ice particles.
(従来の技術)
上述の附着物を上述の部品より除去するのには、従来は
、酸洗浄を主体とする化学的洗浄法が普通であり、次い
で研削粉を噴射するクリーニング方法も用いられ、最近
では鋼板等の除錆、塗装下地処理に氷粒を吹きつけるア
イスプラスト法が採用されているのに鑑みアイスプラス
ト法の採用も考えられている。(Prior Art) In order to remove the above-mentioned deposits from the above-mentioned parts, conventionally, a chemical cleaning method mainly consisting of acid cleaning has been used, followed by a cleaning method in which grinding powder is sprayed. In view of the recent use of the Ice Plast method, in which ice particles are sprayed on steel plates and the like to remove rust and prepare the base for painting, the use of the Ice Plast method is also being considered.
(発明が解決しようとする問題点)
然し、上述の化学的洗浄法は洗浄工程を何段にも行わね
ばならず複雑となるし、除去する附着物が有害物質、或
は1毒物質となると、後処理を充分行わない場合は公害
問題を起す虞れがあり、研削粉を噴射するり17−ユン
グ法は発生する粉塵の処理、多量の廃研削粒の処理に問
題があり、それらのものに上述の1害物質、1毒物貿が
含まれているとなると公害面粗を充分配慮した後処理が
必要であるし、アイスプラスト法は氷粒を各賞に連続的
に移送供給する方法に未だ問題があり、特に氷粒をプラ
ストする場合、氷粒は表面が融け゛て水となった場合、
氷粒内部の温度が低いと、その水は再冷却され、再び氷
結してしまい、氷粒同志が一緒にかたまり、氷塊状とな
り、噴射に適さない形となってしまうし、氷粒を飽くま
で氷粒の状態に置くため低温下に置くと、機械、装置が
氷結してし7まい期待通り機能しないと云う欠点があっ
た。この発明は叙上の問題点、欠点を解決できた、氷粒
を噴射するクリーニング装置を提供するのをその目的と
する。(Problems to be Solved by the Invention) However, the above-mentioned chemical cleaning method requires multiple stages of cleaning steps and is complicated, and if the adhering material to be removed is a harmful substance or a single poisonous substance, If post-treatment is not carried out sufficiently, there is a risk of pollution problems, and the 17-Jung method, which involves injecting grinding powder, has problems in processing the generated dust and large amounts of waste grinding particles. If it contains the above-mentioned 1 harmful substance and 1 poisonous substance trade, it is necessary to carry out post-treatment with sufficient consideration for pollution surface roughness, and the iceplast method is a method of continuously transporting and supplying ice particles to each prize. There are still problems, especially when plasticizing ice particles, when the surface of the ice particles melts and turns into water.
If the temperature inside the ice grain is low, the water will recool and freeze again, causing the ice grains to clump together and form an ice block, which is not suitable for injection. If it is kept in a granular state at a low temperature, the machines and equipment will freeze and will not function as expected. An object of the present invention is to provide a cleaning device that sprays ice particles, which can solve the above-mentioned problems and drawbacks.
(問題点を解決するだめの手段)
第1番目の発明に係る氷粒を噴射せるクリーニング装置
は一/j℃以下に保持された低温室A内に、液化窒素の
液面に微氷粒を浮遊させる倣氷粒製造用タンクaと、該
タンクa甲の浮遊微氷粒を取出し1一定面処に供給する
微氷粒取出し移送装置すと、前記微氷粒取出し移送装置
すより微氷粒を、−20℃以下の窒素カスを作動用気体
とするジェットポンプCのジェット部3に受けて、粒径
選別用サイクロンdに#微氷粒を送るジェットポンプC
とを前記サイクロンdと共に設け、加工室Bの、−20
℃以下の圧搾窒素ガスを作動用気体とする噴射カンeに
、前記サイクロンdで分離された噴射用氷粒を供給する
ようにしたものであり、
第2番目の発明に係る氷粒を噴射するクリーニング装置
は、−1sr:以下に保持された低温室A内に、液化窒
素の沿面に微氷粒を浮遊させる微氷粒製造用タンクaと
、該タンクa中の浮遊微氷粒を取出して一定箇処に供給
する微氷粒取出し移送装置すと、前記微氷粒取出し移送
装置より微氷粒を、−20℃以下の物素ガスを作動用気
体とするジェットポンプCのジェット部3に受けて、粒
径選別用サイクロンdに該微氷粒を送るジェットポンプ
Cとを、前記サイクロンdと共に設け、少くとも−/3
;’Ch下の低温に保持された加工室Bの、圧搾窒素ガ
スを作動気体とする噴射ガンeに前記サイクロンdで分
離された噴射用氷粒を供給するようにし、前記力n王室
Bの下部のホッパーfよりは使用済氷粒の一部を前記ジ
ェットポンプCのジェット部3に戻すようにしたもので
あり、
第3s目の発明に係る氷粒を噴射するり17 +ニング
装置は、−1sr:以下に保持された低温室A内に、液
化窒素の液面に微氷粒を浮遊させる微氷粒製造用タンク
aと、該タンクa中の浮遊微氷粒を取出して一定箇処に
供給する微氷粒取出し移送装置1bと、前記微氷粒取出
し移送装置より微氷粒を、−20℃以下の窒素ガスを作
動用気体とするジェットポンプCのジェット部3に受け
て、粒径選別用サイクロンdに該微氷粒を送るジェット
ポンプCとを、前記サイクロンdと共に設け、加工室B
の、−20’C以下の圧搾窒素カスを作動気体とする噴
射ガンeに前記サイクロンdで分離された噴射用氷粒を
供給するようにし、前記ホッパーでの下部室f1に溜っ
た使用済氷粒、1IIlけた水、洗浄残査は水固形物分
離用サイクロンtを通して水と固形物とに分離し、大き
い固形物は第一次槽1に、固形物中洗浄残査及び水はフ
ィルターhに夫々送るようにし、前記洗浄残査以外の水
は前記第一次槽iと連通ずる第二次槽jに投入されるよ
うに12、該第二次槽jの水は次いで、有害分質除去装
量にを、経て純水製造装置lに送るようにし、純水製造
装置lにより作られた純水は前記微氷粒製造用夕/りa
に戻すようにしたものである。(Means for Solving the Problem) A cleaning device capable of spraying ice particles according to the first invention sprays fine ice particles on the surface of liquefied nitrogen in a cold room A maintained at 1/j°C or below. A tank a for producing imitation ice particles that is made to float, and an ice particle removal and transfer device that takes out the floating ice particles in the tank a and supplies them to a certain area, and the ice particles are removed from the ice particle removal and transfer device. is received by the jet part 3 of the jet pump C which uses nitrogen sludge at -20°C or lower as the working gas, and sends #fine ice particles to the cyclone d for particle size selection.
is provided together with the cyclone d, and -20
The ice pellets for injection separated by the cyclone d are supplied to the injection can e which uses compressed nitrogen gas at a temperature of ℃ or less as the working gas, and the ice particles according to the second invention are injected. The cleaning device includes a tank a for producing fine ice grains that floats fine ice grains on the surface of liquefied nitrogen in a low temperature chamber A maintained at -1 sr or less, and a tank a for producing fine ice grains that takes out the floating fine ice grains in the tank a. When the ice grains are taken out and transferred to a certain point, the ice grains are transferred from the ice grains taken out and transferred to a jet part 3 of a jet pump C whose operating gas is a substance gas of -20°C or less. A jet pump C is provided together with the cyclone d to send the fine ice particles to the particle size sorting cyclone d, and at least -/3
The ice grains for injection separated by the cyclone d are supplied to the injection gun e, which uses compressed nitrogen gas as a working gas, in the processing chamber B kept at a low temperature under A part of the spent ice grains is returned to the jet part 3 of the jet pump C from the lower hopper f, and the ice grain jetting device according to the third invention is as follows: -1sr: In a cold room A maintained below, there is a tank a for producing ice particles that suspends ice particles on the liquid surface of liquefied nitrogen, and a tank a for producing ice particles that is taken out from the tank a and placed in a certain place. The ice grains are received by the ice grain removal and transfer device 1b and the jet section 3 of the jet pump C, which uses nitrogen gas at -20°C or lower as a working gas, and are A jet pump C for sending the fine ice particles to the diameter sorting cyclone d is provided together with the cyclone d, and the processing chamber B
The ice grains for injection separated by the cyclone d are supplied to the injection gun e which uses compressed nitrogen scum of -20'C or less as a working gas, and the used ice particles accumulated in the lower chamber f1 of the hopper are The grains, water, and washing residue are separated into water and solids through a cyclone t for separating water and solids. Larger solids are sent to the primary tank 1, and the washing residue and water in the solids are sent to the filter h. 12, so that the water other than the cleaning residue is input into a secondary tank j communicating with the primary tank i, and the water in the secondary tank j is then subjected to harmful substances removal. The purified water produced by the pure water producing apparatus 1 is sent to the pure water producing apparatus 1, and the pure water produced by the pure water producing apparatus 1 is sent to the above-mentioned fine ice particle producing column A.
This is what I tried to change back to.
(実施例)
第1番目の発明に係る、氷粒を噴射するクリーニング装
置の一実施例の構成を第1図に基いて詳細に説明すると
、−/jl:以下の低@室A内に、液化窒素の液面/に
微氷粒λを浮遊させる微氷粒製造用タンクaと、この実
施例では該タンクa中の浮遊微氷粒2を掬い上げて一定
箇処に供給する微氷粒取出し移送装置d!′、b(詳細
な構成の説明は後に行う)と、前記微氷粒取出し移送装
置すより、微氷粒2を、’−20C以下の窒素カスをr
f=動用気体とするジェットポンプCのジェット部3に
受けて、噴射クリーニング加工に適する粒径の氷粒を選
別、用すイク07dに該微氷粒を送るジェットポンプC
とヲ前Fee サイノoンd、L4t&でh!r+ @
f’r hn”’r”s P n −36℃以下の圧
搾窒素カスを作動気体とするへ射ガ/θに前記サイクロ
ンdで分藩された1射用氷粒を供給するようにしたもの
である。(Example) The configuration of an example of the cleaning device that sprays ice particles according to the first invention will be described in detail based on FIG. A tank a for producing ice cubes that suspends ice cubes λ on the liquid surface of liquefied nitrogen; and in this embodiment, a tank a for producing ice cubes that scoops up floating ice cubes 2 in the tank a and supplies them to a certain location. Retrieval transfer device d! ', b (detailed configuration will be explained later), and the fine ice grains 2 are transported through the fine ice grain removal and transfer device, and the nitrogen scum with a temperature of -20C or less is r
f = Jet pump C that receives the ice particles into the jet section 3 of the jet pump C as a working gas, selects ice particles with a particle size suitable for the jet cleaning process, and sends the fine ice particles to the pump 07d for use.
Towo Mae Fee Cyno ond, L4t & h! r+ @
f'r hn"'r"s P n Ice grains separated by the above-mentioned cyclone d are supplied to the ice gas/θ which uses compressed nitrogen scum at -36°C or lower as the working gas. It is.
第2番目の発明に係る氷粒を噴射するクリーニング装置
の構成は、第1図に示すように、更に少くとも−15℃
以下の低温に保持した前記な0工室Bの下部のホッパー
fの出ロKri、噴射ガンeより被加工物WK噴射され
た使用済氷粒の一部が溜るようにした棚2.2を設け、
該棚λ2より前記ジェットポンプの前記ジェット部3に
樋23を設け、前記加ニーiiBに充満している窒素ガ
スをブロアー2弘で吸引し、前記棚22上に溜った筺用
済氷粒に吹付けて前記樋23を通して前記ジェット部3
に送るようにしたものである。As shown in FIG.
The outlet Kri of the hopper f in the lower part of the above-mentioned work chamber B maintained at the following low temperature, and the shelf 2.2 on which some of the spent ice grains sprayed from the injection gun e onto the workpiece WK are collected. established,
A gutter 23 is provided in the jet part 3 of the jet pump from the shelf λ2, and the nitrogen gas filling the knee iiB is sucked by a blower 2, and the ice particles accumulated on the shelf 22 are The jet part 3 is sprayed through the gutter 23.
It was designed to be sent to.
又第3@目の発明て係る氷粒を噴射するクリー二:/ダ
装置の一実施例の構成を第9図に基いて詳細シて説明す
ると、−/j’c以下に保持された低温室A内に、液化
窒素の液面に微氷粒と浮遊させる微氷粒製造用タンクa
とこの実施例では該タンクa中の浮遊微氷粒2を掬い上
げて一定箇処に供給する微氷粒取出し移送装置b(詳細
な構成の説明は後に行う)と前記微氷粒取出し移送装置
すより、微氷粒2を、−20℃以下の窒素ガスを作動用
気体とするジェットポンプCのジェット部3に受けて、
噴射クリーニング加工に適する粒径の氷粒を選別する粒
径選別用サイクロンdに該微氷粒を送るジェットポンプ
Cとを前記サイクロンdと共に設け、隣の加工室Bの、
−20℃以下の圧搾窒素ガスをt′1動気体とする噴射
カン・eに前記サイクロンdで分離された賓射用氷粒を
供給するようにし、前記加工室Bの下部のホンバーfの
下部室f、に溜った残りの使用済氷粒、融けた水、洗#
残食等はポンプP、で水、固形物分離用サイクロン2に
送り、水と固形部とに分離し、大きい固形物は第−次伽
1に、固形物中洗浄残査及び水はフィルターhに夫々送
るようにし、前記洗浄残査以外の水は前■上第−次槽1
と連通ずる第二次槽jに投入されるようにし、該第二次
槽jの水は次いでポンプP2により有害分質除去装置k
をhて純水製造装置ぎに送られるようにし純水製造装置
lで1′μられた純水はポンプP3で前記微氷粒製造用
タンクa中に圧搾窒素と共に吹込むようにしたものであ
る。Further, the structure of an embodiment of the cleaner device for jetting ice particles according to the third invention will be explained in detail based on FIG. 9. In room A, there is a tank a for producing fine ice particles, in which fine ice particles are suspended on the liquid surface of liquefied nitrogen.
In this embodiment, a micro ice particle removal and transfer device b (detailed configuration will be explained later) which scoops up floating micro ice particles 2 in the tank a and supplies them to a certain location, and the micro ice particle removal and transfer device Then, the fine ice particles 2 are received by the jet part 3 of the jet pump C which uses nitrogen gas at -20°C or lower as the working gas,
A jet pump C is installed together with the cyclone d to send fine ice particles to a particle size sorting cyclone d that sorts ice particles with a particle size suitable for jet cleaning processing, and a jet pump C is installed together with the cyclone d.
The ice particles separated by the cyclone d are supplied to the injection can e which uses compressed nitrogen gas at -20°C or lower as the dynamic gas at t'1, and the lower part of the homb f at the lower part of the processing chamber B is provided. Remaining used ice particles accumulated in chamber f, melted water, washing #
Leftover food, etc. is sent to water and solid matter separation cyclone 2 by pump P, where it is separated into water and solids. Large solids are sent to the second stage, and cleaning residue and water in the solids are sent to filter h. The water other than the cleaning residue is sent to the upper tank 1.
The water in the secondary tank j is then fed to a harmful substance removal device k by a pump P2.
The deionized water that has been purified by 1'μ in the deionized water manufacturing device 1 is blown into the fine ice grain manufacturing tank a together with compressed nitrogen by the pump P3.
なお、この第1番目乃至第3番目の発明の実施例で使用
する微氷粒を掬い上げる微氷粒取出し移送装置すの一例
を、第3図に基いて詳記すると、微氷粒梨造用タンクa
の基台≠に支柱!を立設し、該支柱!に槓杵6を軸7で
揺動自在に枢支し、該槓杵6の一端砧には、丁度前記タ
ンクaの直径方向に突出し、モーターにで回転できるよ
うにした回転軸りを設け、該回転軸りの端には放射状に
複数(第3図に示すものでは弘個)のアームlOを固定
し、該アーム10の端には、第弘図に拡大した平面図で
示しだように、周囲に前記軸りに近づく程、立上り壁l
/が高くなり、−側に少し突出した放出口/2を1し、
底板13には数多の細孔/≠を弔する掬い羽根/!を1
゛する羽根車l乙を設け、該羽根車/2は前記タンクa
内にて回転できるようにし、−万前記槓杵乙の他端l)
2は前記支柱!に設設けたモーター/7にて減速装置/
♂を介して回転するカム/りに当接させ、7個の羽&/
jがタンクaの直径方向の一部の端からタンクa中の液
中に深くは入り、次いで前記直径方向の他方の端から液
を出る間に、カム/9で槓杵6を作動させ、該羽根/j
が液中に一番深くは入ろうとするのに応じ該回転軸りを
上方に上昇させ、該羽根/jが一回転して前記直径方向
の、前記−万の端に回転してくる間に該回転軸を元の位
置まで降下させるようにし、該羽根ljがタンクaの液
中に深くは入らず、大体液面近くを浅く掬って行くよう
にし、液面に浮遊する微氷粒を多く掬うことができるよ
うにしたものである。An example of the ice particle removal and transfer device used in the first to third embodiments of the invention will be described in detail with reference to FIG. tank a
Prop on the base ≠! erect the corresponding pillar! A mallet 6 is swingably supported by a shaft 7, and one end of the mallet 6 is provided with a rotary shaft that protrudes exactly in the diametrical direction of the tank a and can be rotated by a motor, A plurality of arms 10 (in the case of the one shown in FIG. 3) are fixed radially to the end of the rotation axis, and at the end of the arm 10, as shown in the enlarged plan view of FIG. , the closer you get to the axis, the more rising walls l
/ becomes high and the discharge port /2 that protrudes a little on the - side is set to 1,
The bottom plate 13 has numerous pores/≠ scooping blades/! 1
An impeller l B is provided, and the impeller /2 is connected to the tank a.
The other end of the mallet (l)
2 is the pillar mentioned above! The motor installed in / 7 is the speed reducer /
7 blades &/or
While j is deeply entering the liquid in tank a from one diametrical end of tank a and then exiting the liquid from the other diametrical end, actuating the ram 6 with cam /9; The feather/j
As the blade attempts to enter the deepest part of the liquid, the rotating shaft is raised upwards, and while the blade /j rotates once and rotates to the diametrical end of the The rotating shaft is lowered to its original position, and the blade lj does not go deep into the liquid in tank a, but rather scoops shallowly near the liquid surface to remove as many fine ice particles floating on the liquid surface. It is made so that it can be scooped out.
そして羽根/jが微氷粒を掬い、上方に回動して行くと
微氷粒は、羽根が傾斜するので、放出口/ 2 (II
Iに降下(7て放出口/2よりシュート20中に落下す
るようにしたものである。Then, when the blade /j scoops up the fine ice grains and rotates upward, the fine ice grains are released from the discharge port /2 (II
(7) and falls into the chute 20 from the discharge port /2.
この微氷粒取出し移送装置すは羽根車/乙が回転を続け
れば連続的に多量の微氷粒を7ユート20上に次々に落
下できるので、その為には微氷粒製造用タンクaは液面
に沢山の微氷粒が発生する類のものがよい。If the impeller/B of this ice particle extraction and transfer device continues to rotate, a large amount of ice particles can be continuously dropped onto the 7 units 20, so in order to do so, the ice particle production tank a is The type that produces many small ice particles on the liquid surface is best.
このためこの実施例では液化窒素中に水と窒素ガスとを
混合したものを噴射することにより微氷粒を該液化窒素
表面に浮遊させることのできる微氷粒製造用タンクaを
用いた。タンクaの上部開口に液化窒素面を置くため、
該タンクaの設置される所は一15℃以下の低温室Aで
あることが必要である。なお加工室Bは噴射ガンeより
噴射される一20℃以下の窒素カスにより−71℃以下
に保たれている。For this reason, in this embodiment, a tank a for producing fine ice particles was used, which is capable of suspending fine ice particles on the surface of the liquefied nitrogen by injecting a mixture of water and nitrogen gas into the liquefied nitrogen. To place the liquefied nitrogen surface at the upper opening of tank a,
The place where the tank a is installed needs to be a low temperature room A at -15°C or lower. Note that the processing chamber B is maintained at -71°C or lower by nitrogen scum at -20°C or lower that is injected from the injection gun e.
なお父、純水の一部はホッパーfに供給し、未だ融けて
いない使用済氷粒をサイクロングに移送するのを容易に
しており、サイクロンdより分離された、噴射用氷粒に
適さない大きさの氷粒は配管2/で再びタンクaに戻る
ようにしてあり、フィルターh及び有害物除去装置に中
の有害物除去層に、は取外して洗浄残量、有害物を廃棄
できるようになっている。なお第1図中図面符号mは連
通管を示す。In addition, some of the pure water is supplied to hopper f to facilitate the transfer of unmelted spent ice grains to the cyclone, which is not suitable for the ice grains separated from cyclone d for injection. The ice particles of the same size are returned to tank a via pipe 2/, and the filter h and the harmful substance removal layer in the harmful substance removal device are removed so that the remaining amount of cleaning and harmful substances can be disposed of. It has become. Note that the reference numeral m in FIG. 1 indicates a communicating pipe.
(作 用)
この第1番目乃至第3番目の発明に係る氷粒を噴射する
クリーニング装置の実施例(第1図及び第2図参照)は
叙上のような構成を有するから、微氷粒取出し移送装置
すの羽根車/2にてタンクa中より液体窒素と共に掬い
上げた微氷粒は羽根/!の細孔/≠より液体窒素をきり
、微氷粒だけをシュート2θ上に落下すると、微氷粒は
直ちにジェットポンプCのジェット部3れ、クリーニン
グに適した大きさの氷粒のミ噴射ガンeに送られ、−2
0℃以下の圧搾窒素で噴射され、砒素、燐、放射能によ
る汚染物質等の肩書物質が表面に耐着している被加工物
Wに吹付けられ、前記有害物質を除去する。(Function) Since the embodiment of the cleaning device that sprays ice particles according to the first to third inventions (see FIGS. 1 and 2) has the above-mentioned configuration, fine ice particles can be Fine ice particles scooped up with liquid nitrogen from tank a by impeller/2 of the take-out and transfer device are impeller/! When the liquid nitrogen is removed from the pores/≠ of sent to e, -2
Compressed nitrogen at a temperature of 0° C. or lower is injected onto the workpiece W whose surface is resistant to pollutants such as arsenic, phosphorus, and radioactive contaminants, thereby removing the harmful substances.
又第2番目の発明に係る氷粒を噴射するクリーニング装
置の実施例(第1図参照)では、更ポツパーfの出口に
は棚22を設げ、使用済氷粒の一部を受止め、加工室B
に充満している低温の窒素ガスをブロアーで集め、前記
棚22上の使用済氷粒を吹いて樋23を通してジェット
ポンプCのジェット部3に送るようにし、これを更に前
記サイクロンdに送るようにしたので、使用済氷粒中未
だ噴射に適する氷粒を再利用できる。更に又、第3番目
の発明に係る氷粒を噴射するクリーニング装置の実施例
(第2図参照)では、被加工物Wに氷粒が吹きつけられ
ると、使用済氷粒、1害物質洗浄残査、多少融けた水は
ホッパーfに溜る。この間、低温室Aは−/lc以下に
保有され1おり、710工室B41tF動川気体が一2
0℃以下の圧搾窒素であるので氷粒は、余り融けないが
、ホッパーfに溜ったものは次第KMげ、ポンプP、で
水、固形物分離用サイクロン1に送られ、比較的大きい
固形物は第一次槽1に落下し、比較的大きさの小さい洗
浄残有、有害物質を含んだ水はフィルターhに送られ、
肩書物質を含んだ水没微小の洗浄残有は第二次槽jに落
下し、第二次槽j中の水はポンプP2でM害物質除去装
9kに送られ、有害物質及び微小な洗浄残有を除去され
た水は純水製造属調夕に送られ、周知の、例えは、イオ
ン交換樹脂等の使用により純水とされ、再び微氷粒製造
用夕/りaに戻され、一部はホンバーf内て供給される
。なおサイクロンdで分離されたクリーニングに不適の
大きさの微氷粒は再びタンクaに戻されるのは、第1番
目乃至第3番目の発明の′実施?lJにおいて同様であ
る。Further, in the embodiment of the cleaning device that sprays ice particles according to the second invention (see Fig. 1), a shelf 22 is provided at the outlet of the ice popper f to catch some of the used ice particles. Processing room B
A blower is used to collect the low-temperature nitrogen gas that is filled with the ice, blows out the spent ice particles on the shelf 22, and sends it through the gutter 23 to the jet section 3 of the jet pump C, which is then sent to the cyclone d. Therefore, among the used ice particles, ice particles that are still suitable for injection can be reused. Furthermore, in the embodiment of the cleaning device that sprays ice particles according to the third invention (see FIG. 2), when the ice particles are sprayed onto the workpiece W, the used ice particles and one harmful substance are cleaned. Residue and some melted water accumulate in hopper f. During this period, the temperature in cold room A was kept below -/lc, and the temperature in room B41 was 12.
Since the compressed nitrogen is used at a temperature below 0°C, the ice grains do not melt much, but the ice particles that accumulate in the hopper f are gradually removed and sent to the cyclone 1 for separating water and solids by the pump P, where relatively large solids are removed. The water falls into the primary tank 1, and the water containing relatively small cleaning residues and harmful substances is sent to the filter h.
Submerged minute cleaning residues containing title substances fall into the secondary tank j, and the water in the secondary tank j is sent to the M harmful substance removal device 9k by pump P2, where harmful substances and minute cleaning residues are removed. The water from which the solids have been removed is sent to a pure water production facility, where it is made pure water by using, for example, an ion exchange resin, and then returned to the micro ice particle production facility/rea. The parts are supplied in the honbar f. It should be noted that the fine ice particles separated by the cyclone d and having a size unsuitable for cleaning are returned to the tank a again in accordance with the implementation of the first to third inventions. The same is true for lJ.
なお、又フィルターhに溜った洗浄残有はフィルターh
を外し、又、胸害物質除去装責にの有害物質除去層に、
に溜った肩書物質及び微小な洗浄残有はM害m貰除去層
kを外し何れも廃棄される。In addition, the cleaning residue accumulated in the filter h can be removed from the filter h.
In addition, remove the harmful substance removal layer for removing chest harmful substances,
The title substances and minute cleaning residues accumulated in the M removal layer are removed and both are discarded.
なお、τl−粟間に生じた廃棄さるべき微小物質や氷の
融けた水はホッパーfの下部室f1のコック2K、第一
次槽1の紙部のコック2乙からもrp業休体間に排出廃
棄することができる。In addition, the minute substances to be disposed of between τl and millet and melted ice water are also collected from the cock 2K of the lower chamber f1 of the hopper f and the cock 2O of the paper section of the primary tank 1 during the RP business suspension period. It can be discharged and disposed of.
この発明は叙上のような構成、rF用を徊゛するから、
連続多量に製造された微氷粒は微氷粒のみ111次ジェ
ットポンプにより粒径選別用サイクロンdに迅速に送ら
れ、クリーニングに適した大きさの氷粒のみ更に噴射ガ
ンeに送られるので、金属の被vロエ物Wの表面より有
害物質が除去され、その間氷粒は融は難く、第2番目の
発明では、使用済氷粒はホン・く−内の棚2.2より、
樋23を経て、ジェット部3に戻され循かん貴使用され
る。Since this invention has the above-mentioned configuration and is used for rF,
The fine ice particles that are continuously produced in large quantities are quickly sent to the particle size sorting cyclone d by the 111st jet pump, and only the ice particles of a size suitable for cleaning are further sent to the injection gun e. Harmful substances are removed from the surface of the metal object W, during which time the ice grains are difficult to melt, and in the second invention, the used ice grains are removed from the shelf 2.2 in the warehouse.
It passes through the gutter 23 and is returned to the jet section 3 for circulation and use.
又、第3番目の発明では、使用済氷粒、除去された肩書
物質、浴けた水はホン・;−を経て、フィルター肩書物
質除去装置に送られるので、除去された肩書物質及び洗
浄残有を含んだ水から、形の大きい洗浄残有は勿論、微
細な1害物質は完全に除去されるので公害問題をおこす
憂もなく、洗浄残有は除去廃棄される。又多量の使用済
氷粒も純水にかへられて、微氷粒製造用タンクaに送ら
れ、再び氷粒にfr−りかへられるので、経済的で且つ
公害のおそれのない、氷粒を噴射するクリー二/グ装置
を提供することが出来る。In addition, in the third invention, the used ice grains, the removed title substance, and the bathed water are sent to the filter title substance removal device through the filter, so that the removed title substance and the cleaning residue are Not only large-sized cleaning residues but also minute harmful substances are completely removed from the water containing the cleaning residues, so there is no concern about causing a pollution problem, and the cleaning residues are removed and disposed of. In addition, a large amount of used ice grains is also covered with pure water, sent to tank a for producing fine ice grains, and then recycled into ice grains again. It is possible to provide a cleaning device that sprays .
第1図は第1番目及び第2i目の発明に係る、氷粒を噴
射するり17−ニング装置の一実施例の一正面図、第2
図は第3番目の発明に係る、氷粒を噴射するクリーニン
グ装置の一実施例の正面図、第3図は微氷粒取出し装置
の一例の斜視図、第≠図は羽根車の一つの羽根の平面図
を夫々示し、AVi低温室、Bは加工室、aは掘氷粒製
造用タンク、bは微氷粒取出し移送装置、Cはジェット
ポンプ、dは粒径選別用サイクロン、eは噴射ガン、で
は加工室下部のホッパー、f、111ホツパーの下部室
、2は水固形物分゛離用サイクロン、hはフィルター、
1は第−次僧、jは第二次指、kは有害分質除去装置、
lは純水梨造装置、3はジェットポンプCのジェット部
を夫々示す。FIG. 1 is a front view of an embodiment of a gleaning device for injecting ice particles according to the first and second inventions;
The figure is a front view of an embodiment of a cleaning device that sprays ice particles according to the third invention, FIG. Showing the plan views of the AVi cold room, B is the processing room, a is the tank for producing ice particles, b is the ice particle extraction and transfer device, C is the jet pump, d is the cyclone for particle size selection, and e is the injection gun, the hopper at the bottom of the processing chamber, f, the lower chamber of the 111 hopper, 2 the cyclone for separating water and solids, h the filter,
1 is the first order finger, j is the second order finger, k is the harmful substance removing device,
1 indicates a pure water production device, and 3 indicates a jet section of a jet pump C, respectively.
Claims (3)
素の液面に微氷粒を浮遊させる微氷粒製造用タンクaと
、該タンクa中の浮遊微氷粒を取出して一定箇処に供給
する微氷粒取出し移送装置bと、前記微氷粒取出し移送
装置bより微氷粒を、−20℃以下の窒素ガスを作動用
気体とするジェットポンプcのジェット部3に受けて、
粒径選別用サイクロンdに該微氷粒を送るジェットポン
プcとを前記サイクロンdと共に設け、加工室Bの、−
20℃以下の圧搾窒素ガスを作動用気体とする噴射ガン
eに、前記サイクロンdで分離された噴射用氷粒を供給
するようにしたことを特徴とする氷粒を噴射するクリー
ニング装置(1) In a cold room A maintained at -15°C or lower, there is a tank a for producing ice particles that suspends ice particles on the liquid surface of liquefied nitrogen, and the floating ice particles in tank a are taken out. Fine ice grains are sent to a jet part 3 of a jet pump c whose operating gas is nitrogen gas at -20°C or less, from which the ice grains are sent to a certain point and are supplied to a certain location. receive,
A jet pump c for sending the fine ice particles to the particle size sorting cyclone d is provided together with the cyclone d, and the -
A cleaning device for injecting ice particles, characterized in that the ice particles for injection separated by the cyclone d are supplied to an injection gun e that uses compressed nitrogen gas of 20° C. or lower as a working gas.
素の液面に微氷粒を浮遊させる微氷粒製造用タンクaと
、該タンクa中の浮遊微氷粒を取出して一定箇処に供給
する微氷粒取出し移送装置bと、前記微氷粒取出し移送
装置より微氷粒を、−20℃以下の窒素ガスを作動用気
体とするジェットポンプcのジェット部3に受けて、粒
径選別用サイクロンdに該微氷粒を送るジェットポンプ
cとを前記サイクロンdと共に設け、少くとも−15℃
以下の低温に保持された隣の加工室Bの、圧搾窒素ガス
を作動気体とする噴射ガンeに前記サイクロンdで分離
された噴射用氷粒を供給するようにし、前記加工室Bの
下部のホッパーfよりは使用済氷粒の一部を前記ジェッ
トポンプcのジェット部3に戻すようにしたことを特徴
とする氷粒を噴射するクリーニング装置。(2) In a cold room A kept at -15°C or lower, there is a tank a for producing ice particles that suspends ice particles on the liquid surface of liquefied nitrogen, and a tank a for producing ice particles is taken out from the tank a. Fine ice grains are received by the ice grain removal and transfer device b that is supplied to a certain location and the jet portion 3 of a jet pump c that uses nitrogen gas at -20°C or less as the operating gas. A jet pump c for sending the fine ice particles to the particle size sorting cyclone d is provided together with the cyclone d, and the temperature is at least -15°C.
The ice grains for injection separated by the cyclone d are supplied to the injection gun e, which uses compressed nitrogen gas as a working gas, in the adjacent processing chamber B, which is maintained at a low temperature below. A cleaning device for jetting ice particles, characterized in that a part of the used ice particles is returned to the jet section 3 of the jet pump c from the hopper f.
素の液面に微氷粒を浮遊させる微氷粒製造用タンクaと
、該タンクa中の浮遊微氷粒を取出して一定箇処に供給
する微氷粒取出し移送装置bと、前記微氷粒取出し移送
装置より微氷粒を、−20℃以下の窒素ガスを作動用気
体とするジェットポンプcのジェット部3に受けて、粒
径選別用サイクロンdに該微氷粒を送るジェットポンプ
cとを前記サイクロンdと共に設け、加工室Bの、−2
0℃以下の圧搾窒素ガスを作動気体とする噴射ガンeに
前記サイクロンdで分離された噴射用氷粒を供給するよ
うにし、前記ホッパーfの下部室f_1に溜つた使用済
氷粒、融けた水、洗浄残査は水固形物分離用サイクロン
gを通して水と固形物とに分離し、大きい固形物は第一
次槽iに、固形物中洗浄残査及び水はフィルターhに夫
々送るようにし、前記洗浄残査以外の水は前記第一次槽
iと連通する第二次槽jに投入されるようにし、該第二
次槽jの水は次いで、有害分質除去装置kを経て純水製
造装置lに送るようにし、純水製造装置lにより作られ
た純水は前記微氷粒製造用タンクaに戻すようにしたこ
とを特徴とする氷粒を噴射するクリーニング装置。(3) In a cold room A kept at -15°C or lower, there is a tank a for producing ice particles in which micro ice particles are suspended on the liquid surface of liquefied nitrogen, and the floating micro ice particles in tank a are taken out. Fine ice grains are received by the ice grain removal and transfer device b that is supplied to a certain location and the jet portion 3 of a jet pump c that uses nitrogen gas at -20°C or less as the operating gas. A jet pump c for sending the fine ice particles to the particle size sorting cyclone d is installed together with the cyclone d, and -2
The ice particles for injection separated by the cyclone d are supplied to the injection gun e which uses compressed nitrogen gas of 0°C or less as the working gas, and the spent ice particles accumulated in the lower chamber f_1 of the hopper f are melted. Water and washing residue are separated into water and solids through a cyclone g for separating water and solids, and large solids are sent to the primary tank i, and washing residues and water in the solids are sent to a filter h. , water other than the cleaning residue is put into a secondary tank j communicating with the primary tank i, and the water in the secondary tank j is then purified through a harmful substance removal device k. A cleaning device for spraying ice grains, characterized in that the pure water produced by the water purification device I is sent to the water production device I, and the pure water produced by the water production device I is returned to the ice grain production tank a.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP25679185A JPS62120978A (en) | 1985-11-18 | 1985-11-18 | Cleaning device with spray of crushed ice |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP25679185A JPS62120978A (en) | 1985-11-18 | 1985-11-18 | Cleaning device with spray of crushed ice |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS62120978A true JPS62120978A (en) | 1987-06-02 |
Family
ID=17297490
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP25679185A Pending JPS62120978A (en) | 1985-11-18 | 1985-11-18 | Cleaning device with spray of crushed ice |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS62120978A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1991004449A1 (en) * | 1989-09-12 | 1991-04-04 | Ixtal Blast Technology Corp. | Apparatus for preparing, classifying and metering particle media |
US5357718A (en) * | 1992-10-19 | 1994-10-25 | Mitsubishi Denki Kabushiki Kaisha | Wafer rinsing apparatus |
US5367838A (en) * | 1992-06-01 | 1994-11-29 | Ice Blast International, Inc. | Particle blasting using crystalline ice |
EP1009959A1 (en) * | 1997-02-18 | 2000-06-21 | Inter Ice, Inc. | Ice blasting cleaning system and method of blasting |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6038624A (en) * | 1983-08-11 | 1985-02-28 | Tech Res & Dev Inst Of Japan Def Agency | Beam pattern measuring apparatus |
-
1985
- 1985-11-18 JP JP25679185A patent/JPS62120978A/en active Pending
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6038624A (en) * | 1983-08-11 | 1985-02-28 | Tech Res & Dev Inst Of Japan Def Agency | Beam pattern measuring apparatus |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1991004449A1 (en) * | 1989-09-12 | 1991-04-04 | Ixtal Blast Technology Corp. | Apparatus for preparing, classifying and metering particle media |
US5367838A (en) * | 1992-06-01 | 1994-11-29 | Ice Blast International, Inc. | Particle blasting using crystalline ice |
US5357718A (en) * | 1992-10-19 | 1994-10-25 | Mitsubishi Denki Kabushiki Kaisha | Wafer rinsing apparatus |
EP1009959A1 (en) * | 1997-02-18 | 2000-06-21 | Inter Ice, Inc. | Ice blasting cleaning system and method of blasting |
EP1009959A4 (en) * | 1997-02-18 | 2000-11-22 | Inter Ice Inc | Ice blasting cleaning system and method of blasting |
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