JP2001009728A - Ice slurry surface working method and device therefor - Google Patents

Ice slurry surface working method and device therefor

Info

Publication number
JP2001009728A
JP2001009728A JP2000128122A JP2000128122A JP2001009728A JP 2001009728 A JP2001009728 A JP 2001009728A JP 2000128122 A JP2000128122 A JP 2000128122A JP 2000128122 A JP2000128122 A JP 2000128122A JP 2001009728 A JP2001009728 A JP 2001009728A
Authority
JP
Japan
Prior art keywords
ice
water
ice slurry
slurry
particles
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.)
Granted
Application number
JP2000128122A
Other languages
Japanese (ja)
Other versions
JP4236232B2 (en
Inventor
Shuji Fukano
修司 深野
Hiromichi Fukumoto
浩通 福本
Hisashi Kitagawa
恒 北川
明 ▲はい▼島
Akira Haijima
Naokatsu Kojima
直勝 小島
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.)
Fuji Seiki Machine Works Ltd
Mayekawa Manufacturing Co
Original Assignee
Fuji Seiki Machine Works Ltd
Mayekawa Manufacturing Co
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 Fuji Seiki Machine Works Ltd, Mayekawa Manufacturing Co filed Critical Fuji Seiki Machine Works Ltd
Priority to JP2000128122A priority Critical patent/JP4236232B2/en
Publication of JP2001009728A publication Critical patent/JP2001009728A/en
Application granted granted Critical
Publication of JP4236232B2 publication Critical patent/JP4236232B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Cleaning In General (AREA)
  • Other Air-Conditioning Systems (AREA)

Abstract

PROBLEM TO BE SOLVED: To work a surface without damaging a soft workpiece by turning supercooled water below a freezing point into supercooled ice grains obtained by a condition change by a vortex flowing water releasing means, and injecting ice slurry obtained by mixing the ice grains and cooling water at a prescribed ratio into the workpiece. SOLUTION: Supercooled water cooled below a freezing point by a supercooling part 12 of an supercooled water manufacturing part 10 falls on and collides with a crystallization plate 15 from a conduit 11a to instantly freeze as ice grains 29 to be successively supplied to an ice slurry storage tank 16. The ice grains 29 are mixed with chilled water 27 supplied from a cooling water supply device 20, cooling water is supplied so as to become the prescribed slurry concentration while turning on and off a solenoid valve 34 on the basis of a signal from a monitor 32 to be agitated and mixed by an agitating blade 18, and iced slurry 26 of the prescribed concentration is stored in the slurry storage tank 16. The ice slurry 26 is sent to an injection nozzle 22 from a carrying passage 19 to be accelerated by compressed gas supplied from a compressed gas supply pipe 36 to be injected toward a workpiece surface from the injection nozzle 22 to work the workpiece surface.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、スラリ化した氷粒
を高圧流体で吹き付け、微細加工ないし表面研磨等の機
械加工をする氷スラリを用いた液体ホーニング若しくは
液体ブラスト装置(以下氷スラリ表面加工装置という)
に係り、特に氷スラリを搬送路を介して表面加工部に導
き、該表面加工部内で噴射手段を介して該氷スラリを被
加工物に噴射してホーニング若しくはブラスト加工(表
面加工)を行う氷スラリ表面加工装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a liquid honing or liquid blasting apparatus (hereinafter referred to as ice slurry surface processing) using an ice slurry for spraying slurryed ice particles with a high-pressure fluid and performing machining such as fine processing or surface polishing. Device)
In particular, ice for conducting honing or blasting (surface processing) by guiding an ice slurry to a surface processing section via a transport path, and injecting the ice slurry to a workpiece through a jetting means in the surface processing section. The present invention relates to a slurry surface processing device.

【0002】[0002]

【従来の技術】従来より、砥粒若しくは粒状部材を液中
に懸濁してなる懸濁液を、流体圧を利用して高速度に加
速させて金属表面その他の加工物表面に吹き付ける液体
ブラスト若しくは液体ホーニング(以下両者を含めて液
体ホーニングという)は公知であり、かかる液体ホーニ
ング加工は、噴射材として研削砥粒、ガラスビーズ、植
物性粒子、合成樹脂粒子を使用して、機械加工後のバリ
取り形造品のバリ取り、微細加工、表面研削等の広範囲
の加工に使用されている。然し、前記従来技術では、被
加工部材の表面に噴射材が残留したり、ブラストによる
寸法変化や加工表面に損傷を与える恐れがある。そのた
め、これらの後処理で特に残留物の除去には多大の費用
と無駄な時間を浪費している状況である。
2. Description of the Related Art Conventionally, a liquid blast or a liquid blast, in which a suspension of abrasive grains or granular members in a liquid is accelerated to a high speed by using fluid pressure and sprayed onto a metal surface or other workpiece surface. Liquid honing (hereinafter referred to as liquid honing) is known. Such liquid honing is performed by using grinding abrasives, glass beads, vegetable particles, or synthetic resin particles as a blasting material, and then using a burr after machining. It is used for a wide range of processing such as deburring of molded products, fine processing and surface grinding. However, in the prior art, there is a risk that the blast material may remain on the surface of the workpiece, change in dimensions due to blasting, or damage the processing surface. For this reason, it is a situation in which a great deal of cost and wasteful time is wasted particularly in the removal of the residue in these post-treatments.

【0003】上記課題解決の一手段として、氷粒または
ドライアイス粒を使用し高圧気体で噴射するアイスブラ
スト加工方法が種々提案されている。例えば特開昭58
―102674号では、氷粒のみをエジェクタを利用し
て被処理面に噴射する技術が、又、特公平7−5741
において、冷媒蒸発ガスによる低温雰囲気による凍結粒
を噴射する技術が、又WO86/04536号にはドラ
イアイス粒子を用いたアイスブラスト技術が、夫々開示
されている。
As one means for solving the above-mentioned problems, various ice blasting methods have been proposed in which ice particles or dry ice particles are used and jetted with high-pressure gas. For example, JP-A-58
Japanese Patent Application Publication No. 10-26774 discloses a technique in which only ice particles are sprayed onto a surface to be processed using an ejector.
Discloses a technique for injecting frozen particles in a low-temperature atmosphere using refrigerant evaporating gas, and WO86 / 04536 discloses an ice blasting technique using dry ice particles.

【0004】しかしながら、上記方式はいずれも氷粒な
いしドライアイス粒のみを気流とともに噴射する構成の
ために、洗浄機能を伴わなう事が出来ず、このため噴射
により被加工部材より一旦離散した切削部材が再度付着
する問題や、吹き付けた氷粒が被加工部材の表面に累積
氷結凝集する問題、及び噴射材である氷粒やドライアイ
スが噴射部位までの搬送過程で管詰まりを起し安定した
噴射ノズルの運転が保障されない等の問題がある。
[0004] However, all of the above-mentioned methods have a structure in which only ice particles or dry ice particles are jetted together with an air flow, and thus cannot be accompanied by a washing function. The problem of re-attachment of members, the problem of ice particles sprayed to accumulate and freeze on the surface of the workpiece, and the fact that ice particles and dry ice, which are the blast material, cause clogging in the transport process to the blast site, resulting in a stable condition. There is a problem that the operation of the injection nozzle is not guaranteed.

【0005】そこで、上記問題点の解決のため、特開平
8−309660号公報において氷スラリを用いた液体
ホーニング(ブラスト)技術が開示されている。即ち、
上記提案は従来の液体ホーニングに見られた、被加工表
面に損傷を与えないようにするため氷を噴射材として使
用する点は前記アイスブラスト方法と同様であるが、本
従来技術では、加工後に後洗浄を必要としないように前
記氷粒に水を混合した氷スラリを用いて液体ホーニング
と同様な加工を行うものである。即ち本従来技術は、図
6に示すように、氷粒50と、貯液タンク53で冷却し
た冷却水52とを供給する撹拌混合装置55と、該撹拌
混合装置55で混合した氷スラリ51をポンプ54で高
圧噴射ノズル22まで導入し、前記高圧気体58で加速
噴射をしてブラストを行なうように構成したものであ
る。
In order to solve the above problem, Japanese Patent Application Laid-Open No. Hei 8-309660 discloses a liquid honing (blast) technique using ice slurry. That is,
The above proposal is similar to the above-mentioned ice blast method in that the conventional liquid honing uses ice as a blasting material in order to prevent damage to the surface to be processed. Processing similar to liquid honing is performed using an ice slurry in which water is mixed with the ice particles so that post-washing is not required. That is, in the prior art, as shown in FIG. 6, a stirring and mixing device 55 for supplying ice particles 50 and cooling water 52 cooled in a storage tank 53, and an ice slurry 51 mixed by the stirring and mixing device 55 are used. The high pressure gas is introduced to the high pressure injection nozzle 22 by the pump 54 and accelerated by the high pressure gas 58 to perform blasting.

【0006】そして、本従来技術では、図示しない氷塊
供給装置と供給された氷塊を破砕して所定粒度の氷粒5
0を製造するために設けた氷粒製造部57で所用粒度の
氷粒を適量用意するとともに、新水供給部17より貯液
タンク53に供給し付設してあるユニットクーラ56に
より適温の冷却水52を用意した後、上記用意された氷
粒50と冷却水52とをそれぞれ氷粒製造部57、貯液
タンク53より適量ずつ撹拌混合タンク55へ供給し
て、適度の濃度の氷スラリを撹拌混合により形成させ、
高圧噴射ノズル22までポンプ54を介して搬送してノ
ズル22よりスラリを噴射して表面加工を行う。なお、
上記貯液タンク53へは、液体ホーニング部21の排水
タンク22aより排水ポンプ22b、フィルタ22cを
介して噴射排水を回収するとともに新水供給部17より
新水を補充しボールタップ17aを介して所定水位に保
持するようにしている。
In the prior art, an ice block supply device (not shown) and a supplied ice block are crushed to form an ice block 5 having a predetermined particle size.
A suitable amount of ice particles having a required particle size is prepared by an ice particle producing section 57 provided for producing the water, and a cooling water of an appropriate temperature is supplied from a fresh water supply section 17 to a liquid storage tank 53 by a unit cooler 56 attached thereto. After preparing 52, the ice particles 50 and the cooling water 52 prepared above are supplied to the stirring and mixing tank 55 from the ice particle producing section 57 and the liquid storage tank 53, respectively, so that the ice slurry having an appropriate concentration is stirred. Formed by mixing,
The slurry is conveyed to the high-pressure jet nozzle 22 via the pump 54 and the slurry is jetted from the nozzle 22 to perform surface processing. In addition,
Into the liquid storage tank 53, the injection drainage is collected from the drainage tank 22a of the liquid honing unit 21 through the drainage pump 22b and the filter 22c, and fresh water is replenished from the fresh water supply unit 17 and the predetermined water level is supplied through the ball tap 17a. To keep it.

【0007】[0007]

【発明が解決しようとする課題】しかしながら上記従来
技術においても、下記のような課題を内蔵している。即
ち、前記従来技術では氷塊供給装置とともにこれを破砕
して所定粒度の氷粒を製造する氷粒製造部を必要とし設
備費がコスト高になる問題がある。また、氷塊を機械的
に破砕する構成の氷粒製造部では氷塊から粒径が一定の
氷粒を得ることは困難で、ブラスト能力が不安定となる
問題がある。更に上記従来技術においては、砕いた氷粒
と冷却ユニットで冷却された水を混合して適当濃度の氷
スラリを得るため、撹拌混合タンクの設置を必要とし、
そのような設備をしても、上記砕氷と前記チラーで冷や
した冷却水を別々に供給して撹拌するため、氷スラリの
濃度は不安定になり易い。
However, the above prior art also has the following problems. In other words, the conventional technique requires an ice block supply unit and an ice particle production unit for crushing the apparatus and producing ice particles having a predetermined particle size, which causes a problem that equipment cost is increased. In addition, in an ice particle production section configured to mechanically crush ice blocks, it is difficult to obtain ice particles having a constant particle size from the ice blocks, and there is a problem that blasting ability becomes unstable. Furthermore, in the above prior art, in order to obtain ice slurry of an appropriate concentration by mixing crushed ice particles and water cooled by a cooling unit, it is necessary to install a stirring and mixing tank,
Even with such equipment, since the crushed ice and the cooling water cooled by the chiller are separately supplied and stirred, the concentration of the ice slurry tends to be unstable.

【0008】本発明は上記課題解決のためになされたも
ので、氷粒を水と混合した氷スラリを被加工物に噴射し
て液体ホーニング若しくは液体ブラストと同様な加工を
行うに際し、粒度の一定した氷粒と一定した氷粒吐出量
により形成され濃度の安定した氷スラリを使用するよう
にして、ブラスト能力の安定化を図るとともに、別途撹
拌混合器の設置を必要とすることなく、コンパクトで低
コストの氷スラリ表面加工方法とその装置の提供を目的
とする。本発明の他の目的は、ダメージを受けやすい軟
質の被加工物に対してもダメージを与えることなく表面
加工を行うことができる氷スラリ表面加工方法とその装
置を提供することにある。
The present invention has been made in order to solve the above-mentioned problem, and when an ice slurry in which ice particles are mixed with water is sprayed onto a workpiece to perform processing similar to liquid honing or liquid blasting, a uniform particle size is obtained. The use of ice slurry with a stable concentration of ice particles and a constant volume of ice particles ejected ensures stable blasting capacity and is compact without the need for a separate stirring mixer. An object of the present invention is to provide a low-cost ice slurry surface processing method and an apparatus therefor. It is another object of the present invention to provide an ice slurry surface processing method and apparatus capable of performing surface processing without damaging a soft workpiece that is easily damaged.

【0009】[0009]

【課題を解決するための手段】かかる課題を解決するた
めに本発明は、氷粒を水と混合した氷スラリを被加工物
に噴射して液体ホーニング若しくは液体ブラストと同様
な加工を行う氷スラリ表面加工方法において、前記氷粒
が、氷点以下の過冷却水を渦流水解除手段による状態変
化により得られる過冷却氷粒であり、該氷粒と冷却水と
を所定割合で混合して得た氷スラリを被加工物に噴射す
る事を特徴とする。この場合前記過冷却水の温度を略−
2〜0℃に設定することにより、氷粒の粒径が略0.1
mm〜2mm、好ましくは0.1mm〜1mmの均一な
ものが製造でき好ましい。
SUMMARY OF THE INVENTION In order to solve the above-mentioned problems, the present invention provides an ice slurry in which ice slurry in which ice particles are mixed with water is sprayed onto a workpiece to perform processing similar to liquid honing or liquid blasting. In the surface processing method, the ice particles are supercooled ice particles obtained by changing the state of supercooled water having a temperature below the freezing point by vortex water releasing means, and the ice particles are obtained by mixing the ice particles and cooling water at a predetermined ratio. It is characterized by injecting ice slurry onto the workpiece. In this case, the temperature of the supercooled water is approximately-
By setting the temperature to 2 to 0 ° C., the particle size of the ice
It is preferable because a uniform product having a thickness of 2 mm to 2 mm, preferably 0.1 mm to 1 mm can be produced.

【0010】かかる発明によれば、機械的な破砕でなく
過冷却という衝突や撹拌という状態変化により均一粒径
の氷粒が形成できるために、粒度の一定した氷粒と一定
した氷粒吐出量により形成され濃度の安定した氷スラリ
を使用するようにして、ブラスト能力の安定化を図ると
ともに、別途撹拌混合器の設置を必要とすることなく、
コンパクトで低コストの氷スラリ表面加工装置を得るこ
とが出来る。即ち、本発明は、氷粒を水と混合した氷ス
ラリを噴射手段を介して被加工物に噴射して液体ホーニ
ング若しくは液体ブラストと同様な加工を行う氷スラリ
表面加工装置において、氷点以下の過冷却水を製造する
装置と、該過冷却水の状態変化により過冷却氷粒を得る
過冷却水解除手段とを具え、該過冷却水解除手段が、氷
粒と冷却水を混合してなる氷スラリ貯留槽上に位置して
いる事を特徴とする。
According to this invention, ice particles having a uniform particle size can be formed by a state change such as collision or agitation called supercooling rather than mechanical crushing. By using an ice slurry with a stable concentration formed by, and stabilizing the blasting capacity, without the need for the installation of a separate stirring mixer,
A compact and low-cost ice slurry surface processing apparatus can be obtained. That is, the present invention relates to an ice slurry surface processing apparatus which performs the same processing as liquid honing or liquid blasting by injecting an ice slurry in which ice particles are mixed with water into an object to be processed through an injection means, and using the same. An apparatus for producing cooling water, and supercooling water releasing means for obtaining supercooled ice particles by changing the state of the supercooling water, wherein the supercooling water releasing means mixes ice particles and cooling water to form ice. It is characterized by being located on a slurry storage tank.

【0011】この場合、前記過冷却水解除手段が、重力
エネルギを有する過冷却水の衝突により氷粒を製造する
衝突板、好ましくは断熱性若しくは表面が低摩擦性材か
らなる傾斜板で構成しても良く、又前記過冷却水解除手
段が、過冷却水を固体粒若しくは気泡粒との衝突により
氷粒を製造する水中解除部で構成しても良い。尚、前記
過冷却水解除手段は、断熱性若しくは低摩擦性の材料か
らなる傾斜板で構成することにより、生成した氷粒が傾
斜板に固着することなく、円滑に氷スラリ貯留槽に落下
する。
In this case, the supercooling water releasing means is constituted by a collision plate for producing ice particles by collision of the supercooling water having gravitational energy, preferably an inclined plate made of a heat insulating or low friction material. Alternatively, the supercooled water releasing means may be constituted by an underwater releasing section for producing ice particles by colliding the supercooled water with solid particles or air bubbles. The supercooled water releasing means is constituted by an inclined plate made of a heat-insulating or low-friction material, so that the generated ice particles fall smoothly into the ice slurry storage tank without being fixed to the inclined plate. .

【0012】又本発明は、前記被加工物に噴射される氷
スラリの氷粒と冷却水との混合比(氷スラリ濃度)調整
手段が、氷スラリ貯留槽と噴射手段間のスラリ搬送路上
に位置し、前記冷却水が氷スラリ貯留槽底部より導き入
れた氷点に近い冷却水である事を特徴とする。かかる発
明によれば、表面加工用の氷スラリの濃度が精度良く調
整できるとともに、その調整用の冷却水は氷スラリ貯留
槽底部より導き入れた氷点に近い冷却水であるために独
立した冷却水貯留槽が不要であり、且つ氷粒が溶けるこ
ともない。
Further, according to the present invention, the means for adjusting the mixing ratio (ice slurry concentration) between the ice particles of the ice slurry and the cooling water sprayed on the workpiece is provided on the slurry transport path between the ice slurry storage tank and the spraying means. And wherein the cooling water is cooling water near the freezing point introduced from the bottom of the ice slurry storage tank. According to this invention, the concentration of the ice slurry for surface processing can be adjusted with high accuracy, and the cooling water for the adjustment is a cooling water close to the freezing point introduced from the bottom of the ice slurry storage tank, so that independent cooling water is used. No storage tank is required, and the ice particles do not melt.

【0013】又前記氷スラリ貯留槽を循環する経路上
に、前記被加工物に噴射される氷スラリ濃度をモニタす
るモニタ手段が位置していれば、氷スラリ貯留槽内のス
ラリ濃度が一定化し、前記した調整手段が不要となる。
又本発明は、氷スラリ製造部で製造された氷スラリを、
氷スラリ搬送路を介して表面加工部に導き、該表面加工
部内で高圧流体で作動する噴射手段を介して被加工物に
噴射して表面加工を行う氷スラリ表面加工装置におい
て、前記氷スラリ製造部は、過冷却水の過冷却解除によ
り氷粒を形成する過冷却水製造部と、形成された氷粒の
供給を受け貯留冷水との撹拌混合により氷スラリを形成
する氷スラリ貯留槽と、氷スラリを噴射手段へ導く搬送
路の前段に設けた氷スラリ濃度調整部とより構成とした
ことを特徴とする。
[0013] If monitoring means for monitoring the concentration of the ice slurry sprayed on the workpiece is located on the path circulating in the ice slurry storage tank, the slurry concentration in the ice slurry storage tank is made constant. This eliminates the need for the adjusting means.
Also, the present invention provides an ice slurry manufactured by the ice slurry manufacturing section,
An ice slurry surface processing apparatus which guides a surface to a surface processing section via an ice slurry transport path and injects a workpiece through an injection means operated by a high-pressure fluid in the surface processing section to perform surface processing, The unit is a supercooled water producing unit that forms ice particles by releasing the supercooled water from the supercooled water, and an ice slurry storage tank that receives the formed ice particles and forms an ice slurry by stirring and mixing with the stored cold water, It is characterized by comprising an ice slurry concentration adjusting section provided at a preceding stage of a transport path for guiding the ice slurry to the injection means.

【0014】かかる発明によれば、前記した発明の効果
とともに、外部空気中で氷粒晶出板や水中解除器により
過冷却水より氷結状態の氷粒に状態変化させるようにし
たため、氷粒の大きさ及び氷粒の供給量は安定するとと
もに、氷スラリ貯留槽内の冷水量を常時所定量に制御す
ることにより、氷スラリの濃度を安定した状態に制御で
きるとともに、前記過冷却水製造部において過冷却水の
温度、流量の制御により氷粒の大きさ及び吐出量の適宜
規制可能のブラスト能力の安定したブラスト用氷スラリ
を得ることができる。又前記過冷却水製造部は、冷水よ
り過冷却水を形成する冷却器と、過冷却解除をする過冷
却水解除手段とを含み、前記冷却器の前段に冷水温度調
整部を設けるのがよい。
According to this invention, in addition to the effects of the above-mentioned invention, since the state of supercooled water is changed to frozen ice from the supercooled water by the ice crystallizing plate or the underwater canceller in the external air, The size and the supply amount of ice particles are stabilized, and the concentration of the ice slurry can be controlled in a stable state by constantly controlling the amount of cold water in the ice slurry storage tank to a predetermined amount. By controlling the temperature and the flow rate of the supercooled water, it is possible to obtain a blasting ice slurry having a stable blasting ability capable of appropriately controlling the size and discharge amount of ice particles. Further, the supercooled water producing unit includes a cooler that forms supercooled water from chilled water, and a supercooled water canceling unit that cancels supercooled water, and it is preferable to provide a chilled water temperature adjusting unit at a stage preceding the cooler. .

【0015】尚、前記過冷却水解除手段が、重力エネル
ギを有する過冷却水の衝突により氷粒を製造する衝突
板、好ましくは断熱性若しくは表面が低摩擦性材からな
る傾斜板で構成しても良く、又前記過冷却水解除手段
が、過冷却水を固体粒若しくは気泡粒との衝突により氷
粒を製造する水中解除部で構成しても良いことは前記し
たとおりである。上記構成により、前記過冷却水製造部
では、氷スラリ貯留槽に貯留されている冷水は過冷却水
製造部のブライン冷却器に導入され、好ましくは略−1
〜−2℃程度まで氷結することなく過冷却される。その
過冷却水は氷スラリ貯留槽上部に導入され、氷粒晶出板
との衝突の衝撃若しくは水中解除器による状態変化によ
り過冷却状態が解除され氷結し、氷粒となり氷スラリ貯
留槽内に落下し、氷スラリ貯留槽内では落下した前記氷
結状の氷粒と冷水が混合し、氷スラリが形成されるよう
にしてある。
The supercooling water releasing means is constituted by a collision plate for producing ice particles by collision of supercooling water having gravitational energy, preferably an inclined plate having a heat insulating or low friction material. As described above, the supercooled water releasing means may be constituted by an underwater releasing unit for producing ice particles by colliding the supercooled water with solid particles or air bubble particles. According to the above configuration, in the supercooled water production section, the cold water stored in the ice slurry storage tank is introduced into the brine cooler of the supercooled water production section, and preferably approximately -1.
It is supercooled without freezing to about -2 ° C. The supercooled water is introduced into the upper part of the ice slurry storage tank, and the supercooled state is released due to the impact of the collision with the ice crystallizing plate or the state change by the underwater release device, which freezes and becomes ice particles and enters the ice slurry storage tank. In the ice slurry storage tank that has fallen, the frozen ice particles that have fallen and the cold water are mixed to form an ice slurry.

【0016】そして、上記ブライン冷却器への冷水供給
路に冷水温度調節部を設け冷水がブライン冷却器内での
氷結を防止する構成にしてある。そして、ブライン冷却
器の使用により、負荷の変動に対応温度調整が可能で氷
粒の大きさ吐出量を適宜制御できる。なお、上記冷却器
には直膨型冷却器を使用してもよい。また、前記濃度調
整部は、搬送路前段において、氷スラリ貯留槽よりの高
濃度氷スラリに氷スラリ貯留槽の冷水を適量供給して濃
度調整する構成とするのがよいことは前記した通りであ
る。
A chilled water temperature control section is provided in a chilled water supply path to the brine cooler so that the chilled water is prevented from freezing in the brine cooler. By using the brine cooler, the temperature can be adjusted in response to the load fluctuation, and the size of the ice particles can be appropriately controlled. Note that a direct expansion type cooler may be used as the cooler. Further, as described above, it is preferable that the concentration adjusting section be configured to supply an appropriate amount of cold water of the ice slurry storage tank to the high-concentration ice slurry from the ice slurry storage tank and adjust the concentration in the front stage of the transport path. is there.

【0017】上記構成により、氷スラリ貯留槽において
撹拌安定した高濃度の氷スラリを高圧気体を介して噴射
ノズルまでの搬送過程の前段に氷濃度調整に氷スラリ貯
留槽の略一定の0℃に近い冷水を所用に応じて補給する
ようにしてあるため、従来の水をチラーで冷やした0℃
以上の水を別々に供給して撹拌する場合に比較し、高濃
度の氷スラリを氷スラリ貯留槽内で一定安定状態にし、
濃度をそれより下げる場合に殆ど0℃に近い冷水を補給
して安定した調整を可能にしている。前記氷スラリ貯留
槽は、表面加工部の噴射手段よりの排水を回収還流させ
冷水として使用する循環路を具えたことを特徴とする。
According to the above-mentioned structure, in the ice slurry storage tank, a high-concentration ice slurry which is stirred and stabilized is transferred to a substantially constant 0.degree. Because near cold water is supplied as required, conventional water is cooled with a chiller at 0 ° C.
Compared to the case where the above water is separately supplied and agitated, high-concentration ice slurry is kept in a stable state in the ice slurry storage tank,
When lowering the concentration, cold water near 0 ° C. is replenished to enable stable adjustment. The ice slurry storage tank is provided with a circulation path for collecting and recirculating waste water from the jetting means of the surface processing section and using it as cold water.

【0018】上記構成により、搬送路で搬送され噴射材
としてホーニング部の噴射手段より噴射された氷スラリ
の排水は、ホーニング部下部に設けられた排水回収タン
クより、沈澱物を除いた上澄み液をフィルタを介して氷
スラリ貯留槽へ還流再使用するようにしてある。前記搬
送路は、氷スラリ貯留槽と噴射手段とを結ぶ2重管搬送
路より構成し、該2重管の内管には氷スラリを重力落差
若しくは圧送により噴射手段まで搬送させ、外管には噴
射手段の排水を前記内管の外側に添い逆送させる正逆搬
送路構造としたことを特徴とする。かかる発明によれ
ば、氷スラリの導通路の外側に0℃に近い噴射手段の排
水が囲撓しているために、氷粒が溶けることなく、所定
スラリ濃度の搬送が可能である。
According to the above construction, the drainage of the ice slurry which is conveyed in the conveying path and jetted from the jetting means of the honing section as the jetting material is transferred from the drainage recovery tank provided at the lower part of the honing section to the supernatant liquid excluding the precipitate. It is designed to be recycled back to the ice slurry storage tank via the filter. The transfer path is constituted by a double pipe transfer path connecting the ice slurry storage tank and the injection means, and the inner pipe of the double pipe is used to transfer the ice slurry to the injection means by gravity head or pressure feed, and to the outer pipe. Is characterized in that it has a forward / reverse transport path structure in which the drainage of the injection means is sent to the outside of the inner pipe and fed backward. According to this invention, since the drainage of the injection means close to 0 ° C. is bent outside the ice slurry conduction path, it is possible to carry the predetermined slurry concentration without melting the ice particles.

【0019】[0019]

【発明の実施の形態】以下に図面を参照して本発明の実
施の形態を例示的に説明する。ただし、この実施の形態
に記載されている構造部品の寸法、材質、形状、相対位
置などは特に特定的な記載がない限りは、この発明の範
囲をそれのみに限定する趣旨ではなく、単なる説明例に
過ぎない。図1を参照しながら、この発明の第1実施形
態に係る氷スラリを用いた液体ホーニング装置の一実施
形態を説明する。図中10は過冷却水製造部であり、水
を過冷却状態に冷却する過冷却部(空冷コンデンシング
ユニット)12を具え、過冷却部12によって作られた
−2℃前後の過冷却水3は導管11aより氷粒晶出板1
5に落下衝突させ、0.1mm〜2mm、好ましくは
0.1mm〜1mmの氷粒29を晶出させる構成となっ
ている。
Embodiments of the present invention will be described below with reference to the accompanying drawings. However, the dimensions, materials, shapes, relative positions, and the like of the structural components described in this embodiment are not intended to limit the scope of the present invention thereto, unless otherwise specified. It is only an example. An embodiment of a liquid honing apparatus using an ice slurry according to a first embodiment of the present invention will be described with reference to FIG. In the figure, reference numeral 10 denotes a supercooling water producing unit, which comprises a supercooling unit (air cooling condensing unit) 12 for cooling water to a supercooled state, and a supercooling water 3 of about −2 ° C. produced by the supercooling unit 12. From the conduit 11a
5 and collide with it to crystallize ice particles 29 of 0.1 mm to 2 mm, preferably 0.1 mm to 1 mm.

【0020】氷粒晶出板15(製氷板)は断熱製板材の
表面にフッ素樹脂をコーティングした傾斜板で形成され
ており、該傾斜板はスラリ貯留槽16の上方に位置し、
該晶出板で晶出した氷粒29が氷スラリ貯留槽16へ導
かれる。なお、過冷却水とは氷点以下(約−1〜−2
℃)に冷却された氷結していない状態の水を言い、状態
変化が起こらない準安定状態を維持させて液相を保持し
ているが、何らかの衝撃を与えると瞬間的に氷結する性
質をもっている。一方、氷粒晶出板15(製氷板)の直
下に位置する氷スラリ貯留槽16の上方には、前記スラ
リ貯留槽16に温度制御された0℃に近い低温の冷水2
7を供給する冷却水供給装置20が設けられ、この冷却
水供給装置20から氷スラリ貯留槽16へ供給される冷
水27の量はモニタ32よりの信号に基づいてオンオフ
制御される電磁弁34によって調整されるようになって
いる。又、氷スラリ貯留槽16内にはモータ18aによ
って駆動される撹拌羽根18が内蔵せしめられており、
氷粒晶出板15によって晶出した氷粒29と冷却水供給
装置20から電磁弁34を介して供給された冷却水とを
撹拌して均一なスラリ濃度の氷スラリを作る様になって
いる。
The ice crystallizing plate 15 (ice making plate) is formed of an inclined plate obtained by coating a surface of a heat insulating plate with a fluororesin, and the inclined plate is located above a slurry storage tank 16.
The ice particles 29 crystallized by the crystallizing plate are guided to the ice slurry storage tank 16. The supercooled water is below freezing point (about -1 to -2).
℃) water that is not frozen and has a liquid phase that is maintained in a metastable state where no state change occurs, but has the property of freezing instantly when any impact is given . On the other hand, above the ice slurry storage tank 16 located immediately below the ice crystallizing plate 15 (ice making plate), the low-temperature cold water 2 near 0 ° C.
7 is provided, and the amount of cold water 27 supplied from the cooling water supply device 20 to the ice slurry storage tank 16 is controlled by an electromagnetic valve 34 that is turned on and off based on a signal from a monitor 32. It is being adjusted. Further, a stirring blade 18 driven by a motor 18a is built in the ice slurry storage tank 16,
The ice particles 29 crystallized by the ice particle crystallization plate 15 and the cooling water supplied from the cooling water supply device 20 via the electromagnetic valve 34 are stirred to produce an ice slurry having a uniform slurry concentration. .

【0021】又、図中32はスラリモニタであり、循環
経路35によりスラリポンプ33を介して氷スラリ貯留
槽16に接続されており、氷スラリ濃度を常時検出する
様になっている。氷スラリ濃度は、前記スラリモニタ3
2の検出結果に基づき冷却水供給装置20の電磁弁34
を適宜開閉し、氷スラリ貯留槽16へ流入する冷却水の
量を調整することによりブラストに必要な濃度設定値に
保持する様になっている。又、図中22は噴射ノズル
(ブラストガン)であり、スラリポンプ19aを介して
氷スラリ搬送路19によって氷スラリ貯留槽16から氷
スラリ26が圧送され、圧縮ガス供給管36によって供
給される圧縮ガスによって氷スラリを噴射する様になっ
ている。圧縮ガスとして通常は空気を用いる。なお、圧
縮ガス(エア)を使用せず、スラリポンプ19aの圧力
によって氷スラリを噴射ノズルより高速噴射するように
しても良い。
In the drawing, reference numeral 32 denotes a slurry monitor, which is connected to the ice slurry storage tank 16 via a slurry pump 33 via a circulation path 35 so as to constantly detect the ice slurry concentration. The ice slurry concentration was measured using the slurry monitor 3.
2 of the cooling water supply device 20 based on the detection result of
Is appropriately opened and closed, and the amount of cooling water flowing into the ice slurry storage tank 16 is adjusted to maintain the concentration set value required for blasting. In the drawing, reference numeral 22 denotes an injection nozzle (blast gun). The ice slurry 26 is pressure-fed from the ice slurry storage tank 16 by the ice slurry transport path 19 via a slurry pump 19a, and compressed by a compressed gas supply pipe 36. Ice slurry is sprayed by gas. Usually, air is used as the compressed gas. The ice slurry may be ejected at a high speed from the ejection nozzle by the pressure of the slurry pump 19a without using the compressed gas (air).

【0022】従って本実施形態によれば、過冷却水製造
部10の過冷却部12で氷点以下(本実施形態において
は約−2℃)に冷却された過冷却水は、導管11aから
晶出板15に落下衝突せしめられ、その衝撃によって瞬
間的に氷結して氷粒29となって、逐次氷スラリ貯留槽
16に供給される。なお、この氷粒29はIPF(製氷
率)が60%前後で安定しており、その粒径も0.1m
m〜2mm、好ましくは0.1mm〜1mm程度と極め
て均一である。そして晶出板15の傾斜面を利用して氷
スラリ貯留槽16に供給された氷粒29は冷却水供給装
置20から供給される温度制御された冷水27と混合さ
れるとともに、該冷却水はモニタ32よりの信号に基づ
いて電磁弁34をオンオフしながら所定濃度のスラリ濃
度になるように冷却水供給がなされ、更に撹拌羽根18
により撹拌混合されて予め設定された濃度の氷スラリ2
6がスラリ貯留槽16内に貯留される。
Therefore, according to the present embodiment, the supercooled water cooled to below the freezing point (about -2 ° C. in the present embodiment) in the supercooling section 12 of the supercooled water producing section 10 is crystallized from the conduit 11a. The plate 15 is caused to fall and collide with the plate 15, and is instantaneously frozen by the impact to form ice particles 29, which are sequentially supplied to the ice slurry storage tank 16. The ice particles 29 have a stable IPF (ice making ratio) of about 60%, and have a particle size of 0.1 m.
m to 2 mm, preferably about 0.1 mm to 1 mm. The ice particles 29 supplied to the ice slurry storage tank 16 by using the inclined surface of the crystallization plate 15 are mixed with the temperature-controlled cold water 27 supplied from the cooling water supply device 20, and the cooling water is Based on the signal from the monitor 32, the cooling water is supplied so as to have a predetermined slurry concentration while turning on and off the electromagnetic valve 34, and further, the stirring blade 18
Ice slurry of a predetermined concentration mixed with stirring
6 is stored in the slurry storage tank 16.

【0023】そして搬送路19より前記スラリは噴射ノ
ズル(ブラストガン)22に送られ、圧縮ガス供給管3
6から送られる圧縮ガスによって加速されてブラストガ
ン22から被加工物表面に向かって噴射され、被加工物
の表面加工に用いられる。従って本実施例においては、
氷スラリに用いられる氷粒はその粒径が0.1mm〜2
mm、好ましくは0.1mm〜1mm程度で均一性に富
んでおり、従来の氷スラリを用いた液体ホーニング装置
では被加工物表面にダメージを与えてしまう様な場合で
も、何ら問題なくブラスト作業の品質を向上させること
ができ、精密部品のバリ取りや洗浄などの作業に大いに
利用価値がある。又、従来の装置の様に固体状のブロッ
クアイスを削氷機でスライスするのではなく、過冷却水
から直接氷粒を作ってしまう為、製氷に要するエネルギ
ー効率は飛躍的に高く、省エネルギーの観点からも極め
てすぐれたものである。
Then, the slurry is sent to the injection nozzle (blast gun) 22 from the transport path 19 and is supplied to the compressed gas supply pipe 3.
It is accelerated by the compressed gas sent from 6 and sprayed from the blast gun 22 toward the surface of the workpiece to be used for surface processing of the workpiece. Therefore, in this embodiment,
Ice particles used for ice slurry have a particle size of 0.1 mm to 2 mm.
mm, preferably about 0.1 mm to 1 mm, which is rich in uniformity. In a conventional liquid honing device using an ice slurry, even if the surface of the workpiece is damaged, the blasting operation can be performed without any problem. It can improve the quality and is very useful for operations such as deburring and cleaning precision parts. In addition, instead of slicing solid block ice with an ice machine as in conventional equipment, ice particles are made directly from supercooled water, so the energy efficiency required for ice making is dramatically higher, and energy saving is achieved. It is extremely excellent from a viewpoint.

【0024】図2は、本発明の氷スラリ表面加工装置の
他の実施例の概略構成を示す図で、図3は図2の氷スラ
リの搬送路の好ましい形態を示す図である。なお、図1
に使用されている構成部品と同一機能を有する部品に対
しては同一符号を使用する。図2に見るように、本発明
の氷スラリ表面加工装置は、氷粒晶出板15を含みホー
ニングの噴射材に使用する氷粒を形成する過冷却水製造
部10と、過冷却水製造部により形成された氷粒と貯留
する冷水とにより氷スラリを形成する氷スラリ貯留槽1
6と、氷スラリ貯留槽16に貯留される冷水を過冷却水
製造部10へ再供給する冷水再供給路20dと、氷スラ
リ貯留槽16より氷スラリをホーニング用噴射ノズル2
2へ供給する搬送路19と、前記噴射ノズル22を高圧
気体で作動させるホーニング部(表面加工部)21とよ
り構成されている。
FIG. 2 is a view showing a schematic configuration of another embodiment of the ice slurry surface processing apparatus of the present invention, and FIG. 3 is a view showing a preferred form of the ice slurry transport path of FIG. FIG.
The same reference numerals are used for parts having the same functions as the constituent parts used in (1). As shown in FIG. 2, the ice slurry surface processing apparatus of the present invention includes a supercooled water producing section 10 including an ice grain crystallizing plate 15 and forming ice grains used for a horning blast material, and a supercooled water producing section. Slurry storage tank 1 that forms an ice slurry by the ice particles formed by the ice and the stored cold water
6, a cold water re-supply path 20d for re-supplying the cold water stored in the ice slurry storage tank 16 to the supercooled water production unit 10, and an injection nozzle 2 for honing the ice slurry from the ice slurry storage tank 16
2 and a honing unit (surface processing unit) 21 for operating the injection nozzle 22 with high-pressure gas.

【0025】上記過冷却水製造部10は、氷スラリ貯留
槽16より冷水再供給路20dを介して供給されたほぼ
0℃に近い冷水27より過冷却水を生成する冷却器11
と該冷却器11へ冷熱を供給する空冷コンデンシングユ
ニット12とを主構成とする。前記冷却器11はブライ
ンクーラで構成し蓄熱運転が可能で、ブラインの温度制
御と流量制御により、過冷却水の温度及び吐出量に対応
できるようにして、略−1.5℃の過冷却水を氷結せず
に準安定状態で得るようにしている。そして、氷スラリ
貯留槽16の直上空間に斜めに配置した氷粒晶出板15
上に導管11aを介して配置し、衝突の衝撃により過冷
却が解除され氷結して氷粒29を形成して氷スラリ貯留
槽16内に落下するようにしてある。
The supercooled water producing section 10 includes a cooler 11 for generating supercooled water from cold water 27 having a temperature of approximately 0 ° C. supplied from the ice slurry storage tank 16 via a cold water resupply path 20d.
And an air-cooling condensing unit 12 that supplies cold heat to the cooler 11. The cooler 11 is constituted by a brine cooler and can perform a heat storage operation. By controlling the temperature and the flow rate of the brine, the cooler 11 can cope with the temperature and the discharge amount of the supercooled water, and the supercooled water of approximately -1.5 ° C. Is obtained in a metastable state without freezing. The ice crystallizing plate 15 is disposed obliquely in the space directly above the ice slurry storage tank 16.
It is arranged above via a conduit 11 a, and the supercooling is released by the impact of the collision and freezes to form ice particles 29, which fall into the ice slurry storage tank 16.

【0026】なお、空冷コンデンシングユニット12
は、冷却器11の冷却媒体に2次冷媒のブラインを使用
し、該ブラインの冷却用に設けるようにした1次冷媒に
よる圧縮機、空冷凝縮器、受液槽、膨張部材、ブライン
冷却器等よりなる冷凍装置で、周知であるのでその説明
は省略する。なお、上記のようにブラインを2次冷媒と
して使用せず、前記1次冷媒を冷凍装置より直接前記冷
却器11に導入する直膨式冷却方式を使用してもよい。
コンデンシングユニット12については空冷コンデンシ
ングユニットを用いずに、水冷でもシステムが成り立つ
ので、特に大型化の場合は水冷のコンデンシングユニッ
トのほうが良い。
The air cooling condensing unit 12
Uses a secondary refrigerant brine as a cooling medium for the cooler 11, and uses a primary refrigerant compressor, an air-cooled condenser, a liquid receiving tank, an expansion member, a brine cooler, etc., which are provided for cooling the brine. The refrigerating apparatus is well known and will not be described. Instead of using the brine as the secondary refrigerant as described above, a direct expansion type cooling system in which the primary refrigerant is directly introduced into the cooler 11 from the refrigerating device may be used.
As for the condensing unit 12, a water-cooled condensing unit can be used without using an air-cooled condensing unit, so that a water-cooled condensing unit is particularly preferable for a large size.

【0027】また、前記冷却器11の手前の冷水再供給
路20dには予熱器13を設け、温水タンク14、ポン
プ14a、フィルタ20cを介して供給する冷水の温度
調整をして冷却器11内での氷結を防止するようにして
ある。予熱器13の熱源は本明細書中では温水である
が、検討の結果、熱源はコンデンシングユニットからの
ホットガス(高温ガス)を用いても良く、予熱器の熱源
を、温水、圧縮機からの高温ガス等、何れを用いても良
いことは明らかである。上記氷スラリ貯留槽16は、氷
粒晶出板15を含む過冷却水製造部10から導入される
氷粒29と、後記するホーニング部21よりポンプ22
b、フィルタ22cを介して還流される排水28の戻り
水とを撹拌用羽根18、モータ18aを介して撹拌し、
タンク内に安定した最高濃度を持つ氷スラリ26形成さ
せている。なお、前記排水28の氷スラリ貯留槽16内
への還流に際してはポンプ22bの圧送と噴射口を貯留
槽16の表面近くに設定し、氷粒29群に旋回流を発生
させ、前記撹拌効果を上げるようにしてある。
A preheater 13 is provided in the cold water re-supply passage 20d before the cooler 11, and the temperature of the cold water supplied through the hot water tank 14, the pump 14a and the filter 20c is adjusted, and the inside of the cooler 11 is adjusted. To prevent freezing. The heat source of the preheater 13 is hot water in the present specification, but as a result of examination, the heat source may be hot gas (high-temperature gas) from a condensing unit, and the heat source of the preheater may be hot water or a compressor. It is clear that any of the above-mentioned high-temperature gases may be used. The ice slurry storage tank 16 includes an ice particle 29 introduced from the supercooled water producing unit 10 including the ice particle crystallization plate 15 and a pump 22 from a honing unit 21 described later.
b, agitating the return water of the drainage 28 which is recirculated through the filter 22c via the stirring blade 18 and the motor 18a,
An ice slurry 26 having a stable maximum density is formed in the tank. When returning the drainage 28 into the ice slurry storage tank 16, the pump 22 b is pumped and the injection port is set near the surface of the storage tank 16 to generate a swirling flow in the group of ice particles 29 to reduce the stirring effect. I'm trying to raise it.

【0028】また、氷スラリ貯留槽16内へは新水供給
部17より随時新水の補給を可能とし、ボールタップ1
7aによりタンク内水位を一定に保持するようにしてあ
る。また氷スラリ貯留槽16の下部より前記冷水再供給
路20dを設けポンプ20a、フィルタ20cを介して
一定温度の略0℃に近い冷水27を予熱器13、冷却器
11へ導入するようにし、これにより安定した氷粒を得
ることができる。又上記氷スラリ貯留槽16の側壁より
氷スラリの最高濃度安定帯域に搬送路19を開口させ
て、ポンプ19aにより吸引される氷スラリが最高濃度
で安定してホーニング部21の噴射用ノズル22へ供給
されるように構成され、これにより圧縮ガス供給管36
から供給される圧縮空気等の高圧気体を介して被加工部
材表面に高濃度の氷スラリを高速噴射して所用の微細加
工ならびに洗浄を可能にしている。その際氷スラリは潜
熱を失って略0℃付近の低温排水28を形成して排水タ
ンク22aに貯留される。その上澄み排液を前記したよ
うにポンプ22b、フィルタ22cを介して氷スラリ貯
留槽16へ戻り水として還流するようにしてある。
Also, fresh water can be replenished into the ice slurry storage tank 16 from the fresh water supply unit 17 at any time.
7a keeps the water level in the tank constant. Further, the cold water re-supply path 20d is provided from the lower part of the ice slurry storage tank 16, and cold water 27 near a constant temperature of approximately 0 ° C. is introduced into the preheater 13 and the cooler 11 through the pump 20a and the filter 20c. Thus, more stable ice particles can be obtained. Further, the transport path 19 is opened from the side wall of the ice slurry storage tank 16 to the highest concentration stable zone of the ice slurry, and the ice slurry sucked by the pump 19a is stably supplied at the highest concentration to the injection nozzle 22 of the honing unit 21. The compressed gas supply pipe 36
High-density ice slurry is sprayed at high speed onto the surface of the workpiece through high-pressure gas such as compressed air supplied from the factory, thereby enabling required fine processing and cleaning. At this time, the ice slurry loses latent heat to form a low-temperature drainage 28 at approximately 0 ° C. and is stored in the drainage tank 22a. The supernatant liquid is returned to the ice slurry storage tank 16 via the pump 22b and the filter 22c as described above, and is returned as water.

【0029】なお、上記スラリ搬送路19の前段にスラ
リ濃度調整用の冷水取り入れ口20bを設け、取り入れ
た最高濃度の氷スラリに適量の略0℃に近い冷水を補給
をして適度の安定した濃度とし搬送過程における管路の
詰まり防止をしている。また、氷スラリ貯留槽16の前
記搬送路19への氷スラリ取り入れ口には氷粒の粒径分
布の一定化を図るために、所定メッシュの金網を設ける
ことが望ましい。
A cold water intake 20b for adjusting the slurry concentration is provided at the preceding stage of the slurry transport path 19, and a suitable amount of cold water close to 0 ° C. is replenished to the taken-in maximum concentration ice slurry to obtain a moderately stable water. The density is used to prevent clogging of the pipeline during the transport process. Further, it is desirable to provide a wire mesh having a predetermined mesh at the ice slurry intake port of the ice slurry storage tank 16 into the transport path 19 in order to stabilize the particle size distribution of the ice particles.

【0030】図3には、図1の氷スラリ搬送路の好まし
い実施例を示してある。本実施例は搬送路23を2重管
搬送システムで構成するようにしたもので、内管24と
外管25より構成し、ホーニング部21の噴射ノズル2
2に向け下向き傾斜管状に構成して、内管24に氷スラ
リを重力落差により流送できるようにし、外管25に前
記液体ホーニング部21の排水タンク22aに貯留され
た排水(戻り冷水)28をポンプ22b、フィルタ22
dを介して導入し、内管24の外側に沿いポンプアップ
により氷スラリ貯留槽16へ側へ圧送させて還流する構
成にしてある。この場合は、外管25を還流する排水2
8は前記ホーニングにより潜熱を失った低温水であるた
め、内管24の外壁は略0℃付近の低温を保ち、内管に
おける氷粒の詰まりを自動的に防止するとともに安定し
た氷スラリの状態を維持できる。
FIG. 3 shows a preferred embodiment of the ice slurry transport path of FIG. In the present embodiment, the transport path 23 is configured by a double pipe transport system, and is configured by an inner pipe 24 and an outer pipe 25, and the injection nozzle 2 of the honing unit 21.
2 is formed in a downwardly inclined tubular shape so that the ice slurry can be sent to the inner tube 24 by gravity drop, and the drainage (returned cold water) 28 stored in the drainage tank 22a of the liquid honing unit 21 is stored in the outer tube 25. The pump 22b, the filter 22
d, and is pumped up to the ice slurry storage tank 16 along the outside of the inner pipe 24 by pump-up and refluxed. In this case, the wastewater 2 flowing back through the outer pipe 25
8 is low-temperature water that has lost latent heat due to the honing, so that the outer wall of the inner tube 24 maintains a low temperature of about 0 ° C., automatically prevents clogging of ice particles in the inner tube, and maintains a stable ice slurry state. Can be maintained.

【0031】本発明の氷スラリ表面加工装置は上記構成
であるので、使用に際しては、予冷運転→製氷運転の過
程を経て液体ブラスト(液体ホーニング)運転に移行す
るのが好ましい。先ず上記予冷運転時には、氷スラリ貯
留槽16→冷却器11→氷スラリ貯留槽の水冷却用循環
路を形成させ、氷スラリ貯留槽16内に貯留する水を予
冷する。ついで製氷運転に移行するが、この場合は、氷
スラリ貯留槽16→予熱器13→冷却器11→氷粒晶出
板15→氷スラリ貯留槽の冷水循環路を形成させ、その
間に氷粒29を形成させ、氷スラリ貯留槽16内に安定
した濃度を持つ氷スラリ26旋回流層を形成させる。そ
の後、ついでブラスト運転に移行するが、この場合は、
下記に示す製氷運転とブラスト運転の並行運転をする。
Since the ice slurry surface processing apparatus of the present invention has the above-described configuration, it is preferable to shift to a liquid blasting (liquid honing) operation through a process of precooling operation → ice making operation when used. First, at the time of the precooling operation, the water cooling circulation path of the ice slurry storage tank 16 → the cooler 11 → the ice slurry storage tank is formed, and the water stored in the ice slurry storage tank 16 is precooled. Then, the operation shifts to the ice making operation. In this case, the ice slurry storage tank 16 → the preheater 13 → the cooler 11 → the ice crystallizing plate 15 → the cold water circulation path of the ice slurry storage tank is formed. Is formed, and an ice slurry 26 having a stable concentration is formed in the ice slurry storage tank 16. After that, it shifts to blast operation, but in this case,
The following ice making operation and blast operation are performed in parallel.

【0032】製氷運転においては、氷スラリ貯留槽16
→予熱器13→冷却器11→氷粒晶出板15→氷スラリ
貯留槽16の経路を冷却水が循環しながら製氷を行う。
氷スラリ貯留槽16内のスラリを用いるブラスト運転で
は、氷スラリ貯留槽→ホーニング部21→排水回収→氷
スラリ貯留槽16を循環しながらスラスト工程と冷水の
戻り工程が行われ、又氷スラリ貯留槽16には新水がレ
ベルセンサ(ボールタップ)17aに基づいて逐次補給
される。
In the ice making operation, the ice slurry storage tank 16
→ Preheating device 13 → Cooler 11 → Ice crystallizing plate 15 → Ice making while cooling water circulates through the path of ice slurry storage tank 16.
In the blast operation using the slurry in the ice slurry storage tank 16, the thrust step and the return step of the cold water are performed while circulating through the ice slurry storage tank → the honing unit 21 → the drainage recovery → the ice slurry storage tank 16. The tank 16 is successively replenished with fresh water based on a level sensor (ball tap) 17a.

【0033】従って、本実施形態によれば、被加工部材
の加工後の洗浄を噴射と同時に行なうことができ、氷ス
ラリの製造に際しては過冷却水の過冷却解除により行な
う構成にしてあるため、氷粒の大きさ、吐出量も随時ブ
ライン冷却器を使用して制御して、所用濃度の氷スラリ
を得ることができ、安定した氷スラリの使用によりブラ
スト能力の安定化を図ることができるとともに、イニシ
アルコストを低く抑えることができる。尚、前記実施形
態においては、前記過冷却水解除手段が、重力エネルギ
を有する過冷却水の衝突により氷粒を製造する衝突板に
より構成されているが、過冷却手段はこれのみに限定さ
れず、前記過冷却水を固体粒若しくはの気泡粒との衝突
により氷粒を製造する水中解除部で構成する事もでき
る。
Therefore, according to the present embodiment, the cleaning of the workpiece after processing can be performed simultaneously with the injection, and the production of the ice slurry is performed by releasing the supercooling water from the supercooling water. The size and discharge rate of ice particles can be controlled as needed using a brine cooler to obtain the required concentration of ice slurry, and the use of stable ice slurry can stabilize the blasting capacity. The initial cost can be kept low. In the above embodiment, the supercooling water releasing means is constituted by an impact plate for producing ice particles by collision of supercooling water having gravitational energy, but the supercooling means is not limited to this. Alternatively, the supercooled water may be constituted by an underwater release unit that produces ice particles by colliding with solid particles or air bubbles.

【0034】図4はかかる水中解除部を用いた本発明の
実施形態で、本発明の第3実施形態に係る氷スラリ表面
加工装置の詳細構成を示す。図5は図2の氷スラリ表面
加工装置に適用される過冷却水解除用の水中解除部を示
す。本発明の水中解除部40は、冷却器11より供給さ
れる過冷却水を、上部垂直導入通路42cより縦長漏斗
状の螺旋流生成容器42(水中解除部)に供給するとと
もに、該容器42の上側面に接線方向に設けた通路41
に、氷スラリ貯留槽16より供給される0℃前後の冷却
水を導入して、螺旋流Yを生成するとともに、該螺旋
流Yの導入とともに、氷スラリ貯留槽16より微小粒
の種氷を導入する。前記種氷の導入により容器42内で
過冷却水の状態変化(水中解除)が行われ、過冷却氷粒
が生成される。
FIG. 4 shows an embodiment of the present invention using such an underwater release unit, and shows a detailed configuration of an ice slurry surface processing apparatus according to a third embodiment of the present invention. FIG. 5 shows an underwater release unit for releasing supercooled water applied to the ice slurry surface processing apparatus of FIG. The underwater release unit 40 of the present invention supplies the supercooled water supplied from the cooler 11 to the vertically long funnel-shaped spiral flow generation container 42 (underwater release unit) from the upper vertical introduction passage 42c. A passage 41 provided tangentially on the upper surface
To, by introducing 0 ℃ before and after the cooling water supplied from the ice slurry reservoir 16, to generate a spiral flow Y 1, with the introduction of the helical flow Y 1, from the ice slurry reservoir 16 minute particle species Introduce ice. With the introduction of the seed ice, the state of the supercooled water is changed (released in water) in the container 42, and supercooled ice particles are generated.

【0035】そして容器内で、種氷と螺旋流Yと過冷
却水の垂直流Zの混合撹拌により過冷却解除が徐々に
伝播して氷スラリ貯留槽16直上位置にある出口42a
でIPF(氷/充填率)が高くなって過冷却氷/水が氷
スラリ貯留槽16に排出される。尚、前記種氷は水中解
除のきっかけを作るだけなので、解除後は入れない方が
よい。尚、容器内で過冷却水が充満していると、過冷却
水の流れに拘わらず、過冷却解除は上流側の冷却器11
側まで伝播していく。このため本発明では副流として渦
流を与え、容器42壁面付近の流速を上げている。渦流
は0℃程度のために、解除の伝搬が上流側の冷却器11
側まで伝播するのを容易に防ぐことが出来る。
[0035] Then in a vessel, the seed ice and helical flow Y 1 and over the cooling mixture stirred for vertical flow Z 1 of water supercooling release is gradually propagated in an ice slurry reservoir 16 just above the position outlet 42a
As a result, the IPF (ice / filling ratio) increases, and supercooled ice / water is discharged to the ice slurry storage tank 16. Since the seed ice only triggers release in water, it is better not to enter the seed ice after the release. When the supercooling water is filled in the container, the supercooling is released regardless of the flow of the supercooling water.
To the side. For this reason, in the present invention, a vortex is given as a sub-flow, and the flow velocity near the wall surface of the container 42 is increased. Since the vortex is about 0 ° C., the propagation of the release is caused by the upstream cooler 11.
Propagation to the side can be easily prevented.

【0036】かかる実施形態においても、氷スラリの製
造に際しては過冷却水の過冷却解除により行なう構成に
してあるため、氷粒の大きさ、吐出量も随時ブライン冷
却器を使用して制御して、所用濃度の氷スラリを得るこ
とができ、安定した氷スラリの使用によりブラスト能力
の安定化を図ることができるとともに、被加工部材の加
工後の洗浄を噴射と同時に行なうことができ、イニシア
ルコストを低く押さえることができる。
Also in this embodiment, since the production of the ice slurry is performed by canceling the supercooling of the supercooled water, the size and the discharge amount of the ice particles are controlled by using a brine cooler as needed. In addition, the required concentration of ice slurry can be obtained, the blast capacity can be stabilized by using a stable ice slurry, and the post-processing cleaning of the workpiece can be performed at the same time as the jetting, and the initial cost can be reduced. Can be kept low.

【0037】[0037]

【発明の効果】以上記載の如く本発明によれば、氷粒を
水と混合した氷スラリを被加工物に噴射して液体ホーニ
ング若しくは液体ブラストと同様な加工を行うに際し、
粒度の一定した氷粒と一定した氷粒吐出量により形成さ
れ濃度の安定した氷スラリを使用するようにして、ブラ
スト能力の安定化を図るとともに、別途撹拌混合器の設
置を必要とすることなく、コンパクトで低コストの氷ス
ラリ表面加工が可能となる。又本発明によれば、ダメー
ジを受けやすい軟質の被加工物に対してもダメージを与
えることなく表面加工を行うことができる。
As described above, according to the present invention, an ice slurry in which ice particles are mixed with water is sprayed on a workpiece to perform processing similar to liquid honing or liquid blasting.
By using ice slurry with a constant particle size and a constant ice particle discharge rate and a stable concentration, it is possible to stabilize the blasting capacity and without installing a separate stirring mixer. This enables compact and low-cost ice slurry surface processing. Further, according to the present invention, surface processing can be performed without damaging a soft workpiece that is easily damaged.

【図面の簡単な説明】[Brief description of the drawings]

【図1】 本発明の第1実施形態に係る氷スラリ表面加
工装置の概略構成図を示す。
FIG. 1 is a schematic configuration diagram of an ice slurry surface processing apparatus according to a first embodiment of the present invention.

【図2】 本発明の第2実施形態に係る氷スラリ表面加
工装置の詳細構成を示す。
FIG. 2 shows a detailed configuration of an ice slurry surface processing apparatus according to a second embodiment of the present invention.

【図3】 図2の氷スラリ表面加工装置に適用される氷
スラリ搬送路を示す。
FIG. 3 shows an ice slurry transport path applied to the ice slurry surface processing apparatus of FIG. 2;

【図4】 本発明の第3実施形態に係る氷スラリ表面加
工装置の詳細構成を示す。
FIG. 4 shows a detailed configuration of an ice slurry surface processing apparatus according to a third embodiment of the present invention.

【図5】 図2の氷スラリ表面加工装置に適用される過
冷却水解除用の水中解除部を示す。
FIG. 5 shows an underwater release section for supercooling water release applied to the ice slurry surface processing apparatus of FIG. 2;

【図6】 従来技術の氷スラリ表面加工装置の概略構成
を示す。
FIG. 6 shows a schematic configuration of a conventional ice slurry surface processing apparatus.

【符号の説明】[Explanation of symbols]

10 過冷却水製造部 15 氷粒晶出板 16 氷スラリ貯留槽 19 搬送路 21 ホーニング部 22 噴射ノズル 23 2重管搬送路 26 氷スラリ 27 冷水 29 氷粒 Reference Signs List 10 supercooled water production unit 15 ice crystallized plate 16 ice slurry storage tank 19 transport path 21 honing unit 22 injection nozzle 23 double pipe transport path 26 ice slurry 27 cold water 29 ice particles

─────────────────────────────────────────────────────
────────────────────────────────────────────────── ───

【手続補正書】[Procedure amendment]

【提出日】平成12年5月16日(2000.5.1
6)
[Submission date] May 16, 2000 (2000.5.1)
6)

【手続補正1】[Procedure amendment 1]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0003[Correction target item name] 0003

【補正方法】変更[Correction method] Change

【補正内容】[Correction contents]

【0003】上記課題解決の一手段として、氷粒または
ドライアイス粒を使用し高圧気体で噴射するアイスブラ
スト加工方法が種々提案されている。例えば特開昭58
―102674号では、氷粒のみをエジェクタを利用し
て被処理面に噴射する技術が、又、特公平7−574
において、冷媒蒸発ガスによる低温雰囲気による凍
結粒を噴射する技術が、又WO86/04536号には
ドライアイス粒子を用いたアイスブラスト技術が、夫々
開示されている。
As one means for solving the above-mentioned problems, various ice blasting methods have been proposed in which ice particles or dry ice particles are used and jetted with high-pressure gas. For example, JP-A-58
In No. -102674, the ice particles only by utilizing the ejector to inject the treated surface technology, also KOKOKU 7-574 7
No. 1 discloses a technique for injecting frozen particles in a low-temperature atmosphere using a refrigerant evaporating gas, and WO 86/04536 discloses an ice blast technique using dry ice particles.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) F25C 1/00 F25C 1/00 A (72)発明者 福本 浩通 東京都江東区牡丹2丁目13番1号 株式会 社前川製作所内 (72)発明者 北川 恒 東京都江東区牡丹2丁目13番1号 株式会 社前川製作所内 (72)発明者 ▲はい▼島 明 東京都江東区牡丹2丁目13番1号 株式会 社前川製作所内 (72)発明者 小島 直勝 静岡県駿東郡長泉町本宿663−4──────────────────────────────────────────────────の Continued on the front page (51) Int.Cl. 7 Identification symbol FI theme coat ゛ (Reference) F25C 1/00 F25C 1/00 A (72) Inventor Hiromichi Fukumoto 2-3-1 Botan, Koto-ku, Tokyo Inside the Maekawa Works Co., Ltd. (72) Inventor Hisashi Kitagawa 2-13-1, Botan, Koto-ku, Tokyo Inside the Maekawa Works Co., Ltd. (72) Inventor ▲ Yes ▼ Akira Akira 2-1-1 Botan, Koto-ku, Tokyo No. Inside the Maekawa Works (72) Inventor Naokatsu Kojima 663-4 Honjuku, Nagaizumi-cho, Sunto-gun, Shizuoka Prefecture

Claims (13)

【特許請求の範囲】[Claims] 【請求項1】 氷粒を水と混合した氷スラリを被加工物
に噴射して液体ホーニング若しくは液体ブラストと同様
な加工を行う氷スラリ表面加工方法において、 前記氷粒が、氷点以下の過冷却水を渦流水解除手段によ
る状態変化により得られる過冷却氷粒であり、該氷粒と
冷却水とを所定割合で混合して得た氷スラリを被加工物
に噴射する事を特徴とする氷スラリ表面加工方法。
1. An ice slurry surface processing method in which an ice slurry in which ice particles are mixed with water is sprayed onto a workpiece to perform processing similar to liquid honing or liquid blasting, wherein the ice particles are supercooled below a freezing point. Ice, which is supercooled ice particles obtained by changing the state of water by vortex water releasing means, and injecting an ice slurry obtained by mixing the ice particles and cooling water at a predetermined ratio onto a workpiece. Slurry surface processing method.
【請求項2】 前記過冷却水解除手段が、重力エネルギ
を有する過冷却水の衝突により氷粒を製造する衝突板、
若しくは過冷却水を固体粒若しくは気泡粒との衝突によ
り氷粒を製造する水中解除部である事を特徴とする請求
項1記載の氷スラリ表面加工方法。
2. A collision plate for producing ice particles by collision of supercooled water having gravitational energy,
2. The method according to claim 1, wherein the subcooling unit is an underwater release unit for producing ice particles by colliding supercooled water with solid particles or air bubbles.
【請求項3】 氷粒を水と混合した氷スラリを噴射手段
を介して被加工物に噴射して液体ホーニング若しくは液
体ブラストと同様な加工を行う氷スラリ表面加工装置に
おいて、 氷点以下の過冷却水を製造する装置と、該過冷却水の状
態変化により過冷却氷粒を得る過冷却水解除手段とを具
え、該過冷却水解除手段が、氷粒と冷却水を混合してな
る氷スラリ貯留槽上に位置している事を特徴とする氷ス
ラリ表面加工装置。
3. An ice slurry surface processing apparatus which performs processing similar to liquid honing or liquid blast by injecting an ice slurry in which ice particles are mixed with water into an object to be processed through an injection means, wherein supercooling below the freezing point is performed. An ice slurry comprising an apparatus for producing water and supercooled water releasing means for obtaining supercooled ice particles by changing the state of the supercooled water, wherein the supercooled water releasing means mixes ice particles and cooling water. An ice slurry surface processing device that is located on a storage tank.
【請求項4】 前記過冷却水解除手段が、重力エネルギ
を有する過冷却水の衝突により氷粒を製造する衝突板で
ある事を特徴とする請求項3記載の氷スラリ表面加工装
置。
4. The ice slurry surface processing apparatus according to claim 3, wherein said supercooling water releasing means is a collision plate for producing ice particles by collision of supercooling water having gravitational energy.
【請求項5】 前記過冷却水解除手段が、過冷却水を固
体粒若しくは気泡粒との衝突により氷粒を製造する水中
解除部である事を特徴とする請求項3記載の氷スラリ表
面加工装置。
5. The ice slurry surface processing according to claim 3, wherein said supercooled water releasing means is an underwater releasing section for producing ice particles by colliding the supercooled water with solid particles or air bubble particles. apparatus.
【請求項6】 前記被加工物に噴射される氷スラリの氷
粒と冷却水との混合比(氷スラリ濃度)調整手段が、氷
スラリ貯留槽と噴射手段間のスラリ搬送路上に位置し、
前記冷却水が氷スラリ貯留槽底部側より導き入れた氷点
に近い冷却水である事を特徴とする請求項3記載の氷ス
ラリ表面加工装置。
6. A means for adjusting a mixing ratio (ice slurry concentration) between ice particles of ice slurry and cooling water sprayed on the workpiece is located on a slurry transport path between the ice slurry storage tank and the spraying means,
4. The ice slurry surface processing apparatus according to claim 3, wherein the cooling water is cooling water near the freezing point introduced from the bottom of the ice slurry storage tank.
【請求項7】 前記氷スラリ貯留槽を循環する経路上
に、前記被加工物に噴射される氷スラリ濃度をモニタす
るモニタ手段が配置されている事を特徴とする請求項3
記載の氷スラリ表面加工装置。
7. A monitoring means for monitoring the concentration of ice slurry injected onto the workpiece on a path circulating in the ice slurry storage tank.
The described ice slurry surface processing apparatus.
【請求項8】 氷スラリ製造部で製造された氷スラリ
を、氷スラリ搬送路を介して表面加工部に導き、該表面
加工部内で高圧流体で作動する噴射手段を介して被加工
物に噴射して表面加工を行う氷スラリ表面加工装置にお
いて、 前記氷スラリ製造部は、過冷却水の過冷却解除により氷
粒を形成する過冷却水製造部と、形成された氷粒の供給
を受け貯留冷水との撹拌混合により氷スラリを形成する
氷スラリ貯留槽と、氷スラリを氷スラリ貯留槽より噴射
手段へ導く搬送路の前段に設けた氷スラリ濃度調整部と
より構成としたことを特徴とする氷スラリ表面加工装
置。
8. The ice slurry produced by the ice slurry production section is guided to a surface processing section via an ice slurry transport path, and is jetted to a workpiece through an injection means operated by a high-pressure fluid in the surface processing section. In the ice slurry surface processing apparatus for performing surface processing, the ice slurry manufacturing unit includes a supercooled water manufacturing unit that forms ice particles by releasing supercooling of supercooled water, and receives and stores the formed ice particles. It is characterized by comprising an ice slurry storage tank that forms an ice slurry by stirring and mixing with cold water, and an ice slurry concentration adjusting section provided at a front stage of a transport path that guides the ice slurry from the ice slurry storage tank to the injection means. Ice slurry surface processing equipment.
【請求項9】 前記過冷却水製造部は、冷水より過冷却
水を形成する冷却器と、過冷却解除をする過冷却水解除
手段とを含み、前記冷却器の前段に冷水温度調整部を設
けたことを特徴とする請求項8記載の氷スラリ表面加工
装置。
9. The supercooled water producing section includes a cooler for forming supercooled water from chilled water, and a supercooled water canceling means for canceling supercooled water, and includes a chilled water temperature adjusting section in front of the cooler. The ice slurry surface processing apparatus according to claim 8, wherein the apparatus is provided.
【請求項10】 前記濃度調整部は、搬送路前段におい
て、氷スラリ貯留槽よりの高濃度氷スラリに氷スラリ貯
留槽の冷水を適量供給して濃度調整する構成としたこと
を特徴とする請求項8記載の氷スラリ表面加工装置。
10. The concentration adjusting section is configured to supply an appropriate amount of cold water in an ice slurry storage tank to a high-concentration ice slurry from an ice slurry storage tank and adjust the concentration in a stage preceding the transport path. Item 10. An ice slurry surface processing apparatus according to item 8.
【請求項11】 前記氷スラリ貯留槽は、表面加工部の
噴射手段よりの排水を回収還流させ冷水として使用する
循環路を具えたことを特徴とする請求項8記載の氷スラ
リ表面加工装置。
11. The ice slurry surface processing apparatus according to claim 8, wherein the ice slurry storage tank has a circulation path for collecting and recirculating waste water from an injection means of the surface processing section and using the recovered water as cold water.
【請求項12】 前記搬送路は、氷スラリ貯留槽と噴射
手段とを結ぶ2重管搬送路より構成し、該2重管の内管
には氷スラリを重力落差若しくは圧送により噴射手段ま
で搬送させ、外管には噴射手段の排水を前記内管の外側
に添い逆送させる正逆搬送路構造としたことを特徴とす
る請求項8記載の氷スラリ表面加工装置。
12. The transporting path comprises a double pipe transporting path connecting the ice slurry storage tank and the injection means, and the ice slurry is transported to the injection means by gravity drop or pressure feeding to the inner pipe of the double pipe. 9. The ice slurry surface processing apparatus according to claim 8, wherein the outer pipe has a forward / reverse transport path structure in which the drainage of the injection means is supplied to the outer side of the inner pipe and fed back.
【請求項13】 前記過冷却水解除手段が、重力エネル
ギを有する過冷却水の衝突により氷粒を製造する衝突
板、若しくは過冷却水を固体粒若しくは気泡粒との衝突
により氷粒を製造する水中解除部で構成されていること
を特徴とする請求項9記載の氷スラリ表面加工装置。
13. The supercooling water releasing means produces an ice plate by colliding supercooled water having gravitational energy to produce ice particles, or colliding supercooled water with solid particles or air bubbles to produce ice particles. The ice slurry surface processing apparatus according to claim 9, comprising an underwater release section.
JP2000128122A 1999-04-28 2000-04-27 Ice slurry surface processing method and apparatus Expired - Fee Related JP4236232B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000128122A JP4236232B2 (en) 1999-04-28 2000-04-27 Ice slurry surface processing method and apparatus

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
JP11-122319 1999-04-28
JP12231999 1999-04-28
JP2000128122A JP4236232B2 (en) 1999-04-28 2000-04-27 Ice slurry surface processing method and apparatus

Publications (2)

Publication Number Publication Date
JP2001009728A true JP2001009728A (en) 2001-01-16
JP4236232B2 JP4236232B2 (en) 2009-03-11

Family

ID=26459469

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2000128122A Expired - Fee Related JP4236232B2 (en) 1999-04-28 2000-04-27 Ice slurry surface processing method and apparatus

Country Status (1)

Country Link
JP (1) JP4236232B2 (en)

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002239910A (en) * 2001-02-20 2002-08-28 Fuji Seiki Mach Works Ltd Liquid honing device
JP2002254313A (en) * 2001-02-28 2002-09-10 Fuji Seiki Mach Works Ltd Liquid honing method, and liquid honing device
WO2003031887A1 (en) * 2001-09-26 2003-04-17 The Kansai Electric Power Co., Inc. Method and system for making ice by underwater supercooling release and low temperature water supply system comprising it
JP2006071247A (en) * 2004-09-06 2006-03-16 Miyazaki Prefecture Method and device for making spherical ice particle
JP2007182918A (en) * 2006-01-05 2007-07-19 Mitsubishi Heavy Ind Ltd Hydrogen supply station
CN102042727A (en) * 2010-12-07 2011-05-04 河南科技大学 Fluid ice preparation method and device thereof
EP2065661A3 (en) * 2006-02-15 2012-04-04 LG Electronics Inc. Apparatus for supercooling and method of making slush through supercooling
CN104188922A (en) * 2014-08-12 2014-12-10 上海东富龙科技股份有限公司 Preparation method of nicotinylmethylamide freeze-dried powder injection preparation
CN108608338A (en) * 2018-05-23 2018-10-02 武汉大学 A kind of preceding mix grinding material jet flow generating apparatus
JP6482691B1 (en) * 2017-11-09 2019-03-13 チュン コー ジェームズ Production equipment for fine ice containing salt
KR102491251B1 (en) * 2021-10-27 2023-01-20 여경철 Blast device using water drop type ice ball

Cited By (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4564187B2 (en) * 2001-02-20 2010-10-20 株式会社不二精機製造所 Liquid honing equipment
JP2002239910A (en) * 2001-02-20 2002-08-28 Fuji Seiki Mach Works Ltd Liquid honing device
JP2002254313A (en) * 2001-02-28 2002-09-10 Fuji Seiki Mach Works Ltd Liquid honing method, and liquid honing device
WO2003031887A1 (en) * 2001-09-26 2003-04-17 The Kansai Electric Power Co., Inc. Method and system for making ice by underwater supercooling release and low temperature water supply system comprising it
KR100774604B1 (en) * 2001-09-26 2007-11-09 간사이 덴료쿠 가부시키가이샤 Method and system for making ice by underwater supercooling release and low temperature water supply system comprising it
JP2006071247A (en) * 2004-09-06 2006-03-16 Miyazaki Prefecture Method and device for making spherical ice particle
JP2007182918A (en) * 2006-01-05 2007-07-19 Mitsubishi Heavy Ind Ltd Hydrogen supply station
JP4563320B2 (en) * 2006-01-05 2010-10-13 三菱重工業株式会社 Hydrogen supply station
US8196424B2 (en) 2006-02-15 2012-06-12 Lg Electronics Inc. Apparatus for supercooling and method of making slush through supercooling
EP2065661A3 (en) * 2006-02-15 2012-04-04 LG Electronics Inc. Apparatus for supercooling and method of making slush through supercooling
CN102042727A (en) * 2010-12-07 2011-05-04 河南科技大学 Fluid ice preparation method and device thereof
CN102042727B (en) * 2010-12-07 2012-05-09 河南科技大学 Fluid ice preparation method and device thereof
CN104188922A (en) * 2014-08-12 2014-12-10 上海东富龙科技股份有限公司 Preparation method of nicotinylmethylamide freeze-dried powder injection preparation
JP6482691B1 (en) * 2017-11-09 2019-03-13 チュン コー ジェームズ Production equipment for fine ice containing salt
JP2019086273A (en) * 2017-11-09 2019-06-06 チュン コー ジェームズ Production device of fine ice containing salt content
CN108608338A (en) * 2018-05-23 2018-10-02 武汉大学 A kind of preceding mix grinding material jet flow generating apparatus
KR102491251B1 (en) * 2021-10-27 2023-01-20 여경철 Blast device using water drop type ice ball

Also Published As

Publication number Publication date
JP4236232B2 (en) 2009-03-11

Similar Documents

Publication Publication Date Title
US6328631B1 (en) Method and apparatus for surface processing using ice slurry
JP4236232B2 (en) Ice slurry surface processing method and apparatus
US7155930B2 (en) Apparatus for producing slush nitrogen and method for producing the same
JP3923662B2 (en) Granulation method and granulator used therefor
JP6128452B1 (en) Quick freezing method and quick freezing apparatus
JP2008068341A (en) Ice flake blasting apparatus
CN101522381B (en) Method and device for the production of chilled fresh concrete
JP2006000753A (en) Washing material production method, manufacturing apparatus of washing material, and washing system
WO2005075352A1 (en) Method and apparatus for producing slush nitrogen
KR20040054696A (en) Method and system for making ice by underwater supercooling release and low temperature water supply system comprising it
JP4507224B2 (en) Ice making device and ice making method by releasing subcooling in water
JP2002350017A (en) System for producing fluid ice
JP3996499B2 (en) Cleaning material manufacturing method, manufacturing apparatus therefor, and cleaning system using the same
JP5026869B2 (en) Cold energy utilization system, ice transport device, and cold energy utilization method
JPS62140767A (en) Shot blasting machining device by ice grains
JPS5855667A (en) Ice slurry manufacturing device and ice blast device utilizing said device and piping washer
JPH11153373A (en) Method and apparatus for removing stain
JPH0370928A (en) Ice heat accumulator
JP2005300002A (en) Sherbet ice manufacturing/storing/transport system, and ice storage chamber
JP2005009805A (en) Ice storage device
JP2004085181A (en) Ice heat storage device
KR20090020931A (en) Removing system aluminium burr
JPH03144235A (en) Submerged ice storing and thermal accumulating device with ice pieces and water mixing and transporting means
JP2001025968A (en) Liquid honing device using ice slurry
JP2007238826A (en) Method and apparatus for producing gas hydrate

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20060413

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20080612

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20080627

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20080826

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20080919

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20081117

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20081212

A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20081215

R150 Certificate of patent or registration of utility model

Free format text: JAPANESE INTERMEDIATE CODE: R150

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20111226

Year of fee payment: 3

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20111226

Year of fee payment: 3

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20121226

Year of fee payment: 4

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20121226

Year of fee payment: 4

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20131226

Year of fee payment: 5

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

LAPS Cancellation because of no payment of annual fees