JPS58909B2 - Defoaming method for slurry paint - Google Patents
Defoaming method for slurry paintInfo
- Publication number
- JPS58909B2 JPS58909B2 JP7990479A JP7990479A JPS58909B2 JP S58909 B2 JPS58909 B2 JP S58909B2 JP 7990479 A JP7990479 A JP 7990479A JP 7990479 A JP7990479 A JP 7990479A JP S58909 B2 JPS58909 B2 JP S58909B2
- Authority
- JP
- Japan
- Prior art keywords
- paint
- slurry
- defoaming
- spray gun
- slurry paint
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- 239000003973 paint Substances 0.000 title claims description 83
- 239000002002 slurry Substances 0.000 title claims description 30
- 238000000034 method Methods 0.000 title claims description 22
- 239000007921 spray Substances 0.000 claims description 20
- 239000002245 particle Substances 0.000 claims description 10
- 239000007788 liquid Substances 0.000 claims description 2
- 238000000576 coating method Methods 0.000 description 9
- 230000000052 comparative effect Effects 0.000 description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 8
- 238000000889 atomisation Methods 0.000 description 7
- 239000011248 coating agent Substances 0.000 description 7
- 239000000843 powder Substances 0.000 description 7
- 238000007872 degassing Methods 0.000 description 4
- 239000000428 dust Substances 0.000 description 4
- 239000007787 solid Substances 0.000 description 4
- 239000012530 fluid Substances 0.000 description 3
- 238000010899 nucleation Methods 0.000 description 3
- 239000003960 organic solvent Substances 0.000 description 3
- 239000011347 resin Substances 0.000 description 3
- 229920005989 resin Polymers 0.000 description 3
- 239000004925 Acrylic resin Substances 0.000 description 2
- 229920000178 Acrylic resin Polymers 0.000 description 2
- 239000012190 activator Substances 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 230000002542 deteriorative effect Effects 0.000 description 2
- 239000006260 foam Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000004094 surface-active agent Substances 0.000 description 2
- 229920001187 thermosetting polymer Polymers 0.000 description 2
- 206010024229 Leprosy Diseases 0.000 description 1
- 230000005856 abnormality Effects 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 239000002518 antifoaming agent Substances 0.000 description 1
- 239000000084 colloidal system Substances 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000000839 emulsion Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000004898 kneading Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
Landscapes
- Application Of Or Painting With Fluid Materials (AREA)
- Paints Or Removers (AREA)
Description
【発明の詳細な説明】
本発明はスラリー状塗料、すなわち水を媒体とし、これ
に平均粒子径約5〜50μの樹脂粉末を固形分濃度で約
20〜60重量%分散させた塗料の脱泡方法に関するも
のである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to defoaming of a slurry paint, that is, a paint in which water is used as a medium and resin powder with an average particle size of approximately 5 to 50 μm is dispersed in the solid content in an amount of approximately 20 to 60% by weight. It is about the method.
近年塗料業界において塗料の無公害化、省資源化が進め
られ塗料形態も従来の有機溶剤型塗料に代って水希釈型
塗料、粉体塗料の使用が増加してきている。In recent years, in the paint industry, efforts have been made to make paints pollution-free and resource-saving, and the use of water-dilutable paints and powder paints has been increasing in place of conventional organic solvent-based paints.
しかしながらこれら無公害、省資源型の塗料はその特注
上あるいは使用上の問題点を有していた。However, these non-polluting and resource-saving paints have had problems in customization and use.
例えば水希釈型塗料のうち水溶性塗料では固形分濃度を
高く出来ないため一度に厚膜塗装出来ず、またエマルジ
ョン塗料では界面活性剤を多量に使用するため塗膜の耐
水性、耐薬品性等が悪いという欠点があった。For example, among water-diluted paints, water-soluble paints cannot have a high solid content concentration, so thick films cannot be painted at once, and emulsion paints use a large amount of surfactant, so the water resistance and chemical resistance of the paint film are affected. The problem was that it was bad.
また粉体塗料では特別な塗装装置を必要とするので従来
の有機溶剤型塗料のようには適用範囲が広くなく、用途
がいちじるしく限定されるという欠点があった。Furthermore, since powder coatings require special coating equipment, they cannot be applied as widely as conventional organic solvent-based coatings, and have the disadvantage that their uses are severely limited.
最近無公害、省資源型の塗料として前記欠点を解決した
スラリー状塗料が開発されてきている。Recently, slurry paints have been developed as pollution-free and resource-saving paints that solve the above-mentioned drawbacks.
しかして、一般にスラリー状塗料は、高固形分濃度の塗
料であるので一度に厚膜塗装出来、また従来の有機溶剤
型塗料と同様な塗装装置が使用出来、さらに界面活性剤
等の量が少ないため耐水性、耐薬品性等の優れた塗膜が
形成出来るという利点を有している。Generally speaking, slurry paints have a high solid content concentration, so they can be coated in thick layers at one time, and can use the same coating equipment as conventional organic solvent-based paints, and they contain less amount of surfactants, etc. Therefore, it has the advantage that a coating film with excellent water resistance and chemical resistance can be formed.
しかしながらスラリー状塗料は前記のような利点を有し
ているが、塗料製造時に分散機、練合機を用いて樹脂粉
末を水中に分散させるため塗料中に多量の泡が発生し、
その泡を脱泡しないで使用した場合、貯蔵中に経時変化
し、樹脂粉末同志の凝集が起りやすくなりそのまま塗装
すると塗膜にブツが生じ平滑な塗面が得られないという
欠点を有していた。However, although slurry paints have the above-mentioned advantages, a large amount of bubbles are generated in the paint because the resin powder is dispersed in water using a dispersing machine and a kneading machine during paint production.
If the foam is used without defoaming, it will change over time during storage, and the resin powder will tend to aggregate with each other. If the foam is applied as it is, the paint film will become bumpy, making it impossible to obtain a smooth painted surface. Ta.
塗料の脱泡方法として従来消泡剤を添加する方法、真写
脱泡方法等が知られている。Conventionally known methods for defoaming paints include a method of adding an antifoaming agent, a photographic defoaming method, and the like.
ところで前者の方法では塗膜の耐食性等の低下の原因と
なり、また後者の方法では装置をバッチ式にせざるを得
ず、かつ脱泡を行なうと体積が増加するため設備を大き
くする必要があり、作業効率が悪いという欠点があった
。However, the former method causes a decrease in the corrosion resistance of the coating film, and the latter method requires a batch-type device, and degassing increases the volume, so the equipment needs to be larger. It had the disadvantage of poor work efficiency.
本発明は前記脱泡方法の欠点を解決した新規な方法に関
する。The present invention relates to a new method that overcomes the drawbacks of the defoaming methods described above.
更に詳しくは連続的にしかも塗料を変質させることなく
、脱泡可能なスラリー塗料の脱泡方法に関する。More specifically, the present invention relates to a method for defoaming slurry paint that can be defoamed continuously and without deteriorating the quality of the paint.
すなわち本発明は気泡を含むスラリー状塗料を、スプレ
ーガンよりスプレー乾燥しないように強く噴出し壁ある
いは邪魔板に衝突させ、次いで衝突した噴霧液体粒子を
捕集することを特徴とするスラリー状塗料の脱泡方法に
関する。That is, the present invention provides a slurry-like paint, which is characterized in that a slurry-like paint containing air bubbles is strongly jetted from a spray gun so as not to dry, and collides with a wall or a baffle plate, and then the collided sprayed liquid particles are collected. Concerning a defoaming method.
以下、図面を参照しながら本発明を説明する。The present invention will be described below with reference to the drawings.
第1図、第2図及び第3図は本発明に使用する代表的な
スラリー状塗料の脱泡装置である。FIGS. 1, 2, and 3 show typical defoaming equipment for slurry paint used in the present invention.
第1〜3図は気泡を含むスラリー状塗料を空気霧化タイ
プの二流体ノズルを有するスプレーガン1にてチャンバ
ー2中で噴射し、邪魔板3あるいはチャンバー2の側壁
あるいは底壁に衝突させ、脱泡したスラリー状塗料を流
れ落し、容器4で捕集する方式の脱泡装置である。1 to 3, a slurry-like paint containing air bubbles is injected into a chamber 2 by a spray gun 1 having an air atomization type two-fluid nozzle, and is caused to collide with a baffle plate 3 or a side wall or bottom wall of the chamber 2, This is a defoaming device in which defoamed slurry paint flows down and is collected in a container 4.
第1図は噴射したスラリー状塗料を邪魔板3に衝突させ
る方式であり、第2図及び第3図は噴射したスラリー状
塗料をそれぞれチャンバー2の底壁、側壁に衝突させる
方式である。FIG. 1 shows a method in which the sprayed slurry paint collides with a baffle plate 3, and FIGS. 2 and 3 show a method in which the sprayed slurry paint collides with the bottom wall and side wall of the chamber 2, respectively.
第1〜3図ではチャンバー2の底部に空気抜き口を備え
ているが場合により空気抜きとしてサイクロンを用いて
もよい。In FIGS. 1 to 3, an air vent is provided at the bottom of the chamber 2, but a cyclone may be used as the air vent in some cases.
また第1〜3図では噴射した塗料の捕集効率をあげるた
め、また水分の揮発によるスラリー状塗料の固形分濃度
変化を防止するためチャンバー2中で行なっているが、
第4図の如く必ずしもチャンバー中で行なう必要はない
。In addition, in Figures 1 to 3, the process is carried out in the chamber 2 in order to increase the collection efficiency of the sprayed paint and to prevent changes in the solid content concentration of the slurry paint due to volatilization of water.
It is not necessarily necessary to carry out the process in a chamber as shown in FIG.
第4図は気泡を含むスラリー状塗料槽5よりポンプによ
りスプレーガンに供給しく場合により槽5をスプレーガ
ンより高い位置に置き重力によりスプレーガンに供給し
てもよい)霧化用空気により気泡を含むスラリー状塗料
をスプレーガン1の先端で霧化させ邪魔板3に噴射させ
る方式%式%
本発明においてスラリー状塗料の噴射条件は脱泡効率及
び作業効率をよくするため、スプレーガンの塗料ノズル
ロ径約0.5〜4.0mm、特に好ましくは0.8〜3
mm;霧化空気圧約1〜7 kg/cm2特に好ましく
は2〜4kg/cm2;塗料噴出量約60〜10100
O/分;(霧化用空気容量)/(塗料噴出容量)比約1
00〜2000、特に好ましくは500〜1500が適
当であり、このような条件下でスラリー状塗料の噴霧平
均粒子径は20〜1000μとなり脱泡効率がよくなる
。In Figure 4, a slurry-like paint tank 5 containing air bubbles is supplied to the spray gun by a pump (in some cases, the tank 5 may be placed at a higher position than the spray gun and fed to the spray gun by gravity). Air bubbles are removed by atomizing air. In the present invention, the slurry paint is atomized at the tip of the spray gun 1 and sprayed onto the baffle plate 3. In the present invention, the conditions for spraying the slurry paint are as follows: Diameter of about 0.5 to 4.0 mm, particularly preferably 0.8 to 3
mm; atomization air pressure approximately 1 to 7 kg/cm2, particularly preferably 2 to 4 kg/cm2; paint ejection amount approximately 60 to 10,100
O/min; (atomizing air capacity)/(paint ejection capacity) ratio approximately 1
00 to 2,000, particularly preferably 500 to 1,500. Under such conditions, the average spray particle diameter of the slurry paint is 20 to 1,000 microns, which improves defoaming efficiency.
塗料ノズル口径は前記範囲より大きくなるとスラリー状
塗料の噴霧粒子が大きくなり脱泡効率が悪くなり、逆に
小さくなるとスラリー状塗料の吐出量が少なくなり作業
効率上好ましくない。If the diameter of the paint nozzle is larger than the above range, the sprayed particles of the slurry paint will be large and the defoaming efficiency will be poor, and if it is smaller, the amount of the slurry paint discharged will be reduced, which is unfavorable in terms of work efficiency.
また霧化空気圧は前記範囲より高くなるとスプレーダス
トが出来やすくなり、該ダストが捕集した塗料中でブツ
になり、塗膜に悪影響を及ぼし、逆に低くなるとスラリ
ー状塗料の微粒化が悪くなり、また脱泡効率が悪くなる
ため好ましくない。In addition, if the atomization air pressure is higher than the above range, spray dust is likely to be formed, and the dust becomes lumpy in the collected paint, which has a negative effect on the paint film.On the other hand, if the atomization air pressure is lower than the above range, the atomization of the slurry paint becomes worse. , which is also undesirable because the defoaming efficiency deteriorates.
また塗料噴出量は前記範囲より多くなると脱泡効率が悪
くなり、逆に少なくなると作業効率上好ましくない。Moreover, if the amount of paint ejected exceeds the above range, the defoaming efficiency will deteriorate, and if it decreases, it will be unfavorable in terms of work efficiency.
(霧化用空気容量)/(塗料噴出容量)比は、前記範囲
より大きくなるとスプレーダストが出来やすくなり、逆
に小さくなるとスラリー状塗料の微粒化が悪く噴霧粒子
が大きくなり、また脱泡効率が悪くなり好ましくない。When the ratio of (air capacity for atomization)/(paint ejection capacity) is larger than the above range, spray dust is likely to be formed, and conversely, when it is smaller, the atomization of the slurry paint becomes difficult and the spray particles become large, and the defoaming efficiency is increased. becomes worse, which is not desirable.
またスプレーガンのノズルと邪魔板あるいはチャンバー
壁との距離は50〜1000mm、特に好ましくは10
0〜300mmが適当である。Also, the distance between the nozzle of the spray gun and the baffle plate or chamber wall is 50 to 1000 mm, particularly preferably 10 mm.
0 to 300 mm is suitable.
距離が前記範囲より短くなると、ノズルにはね返りの塗
料が堆積し、それが乾きにより捕集塗料中に混入しブツ
の原因となり、一方長くなると水の飛散が犬になり、ド
ライスプレー気味になりダストとして捕集塗料中に混入
する問題があり、また脱泡効率も悪いため好ましくない
。If the distance is shorter than the above range, the splashed paint will accumulate on the nozzle, and when it dries, it will mix with the collected paint and cause spots. On the other hand, if the distance is longer, the water will scatter like a dry spray and cause dust. This is not preferable because there is a problem that it gets mixed into the collection paint and the defoaming efficiency is also poor.
本発明のスラリー状塗料の脱泡方法は、上記の如く連続
的に、しかも塗料を変質させることなく作業効率よく脱
泡することが出来る。As described above, the method for defoaming slurry paint of the present invention allows defoaming to be carried out continuously and efficiently without deteriorating the quality of the paint.
以下、本発明を実施例により更に詳細に説明する。Hereinafter, the present invention will be explained in more detail with reference to Examples.
実癩例1〜3及び比較例1〜3
熱硬化性アクリル樹脂粉体塗料(Vpet4000ホワ
イト−大日本塗料(株)製部品名)40重量部、活性剤
0.1重量部及び水40重量部をコロイドミルで分散し
、気泡を多く含むスラリー状塗料を調製した。Leprosy Examples 1 to 3 and Comparative Examples 1 to 3 40 parts by weight of thermosetting acrylic resin powder coating (Vpet4000 White - Part name manufactured by Dainippon Toyo Co., Ltd.), 0.1 part by weight of activator, and 40 parts by weight of water. was dispersed in a colloid mill to prepare a slurry paint containing many bubbles.
得られたスラリー状塗料の平均粒子径は15μ(コール
タ−カウンターにて測定)であった。The average particle diameter of the resulting slurry paint was 15 μm (measured with a Coulter counter).
このスラリー状塗料を第1図に示す装置にて塗料ノズル
口径15mmΦの二流体ノズルスプレーガンを使用して
第1表に示す条件下で脱泡処理した。This slurry paint was defoamed under the conditions shown in Table 1 using a two-fluid nozzle spray gun with a paint nozzle diameter of 15 mm in the apparatus shown in FIG.
脱泡処理した塗料の結果を第1表の下段に示す。The results for the defoamed paint are shown in the lower part of Table 1.
実強例4〜7及び比較例4〜5
熱硬化性アクリル樹脂粉体塗料(V pet 1370
ホワイト:大日本塗料C株)製部品名)40重量部、活
性剤0.1重量部及び水40重量部をボールミルで分散
し、気泡を多く含むスラリー状塗料を調製した。Actual strength examples 4 to 7 and comparative examples 4 to 5 Thermosetting acrylic resin powder coating (V pet 1370
White: manufactured by Dainippon Toyo C Co., Ltd. (part name) 40 parts by weight, 0.1 parts by weight of an activator, and 40 parts by weight of water were dispersed in a ball mill to prepare a slurry-like paint containing many bubbles.
得られたスラリー状塗料の平均粒子径は40μであった
。The average particle diameter of the obtained slurry paint was 40μ.
このスラリー状塗料を第1図に示す装置にて塗料ノズル
口径2.5mmΦ(但し比較例5のみ0.5mmΦにて
実施した。This slurry-like paint was applied using the apparatus shown in FIG. 1 with a paint nozzle diameter of 2.5 mmΦ (only Comparative Example 5 was used with a paint nozzle diameter of 0.5 mmΦ).
)の二流体ノズルスプレーガンを使用して第1表に示す
条件下で脱泡処理した。Degassing was carried out under the conditions shown in Table 1 using a two-fluid nozzle spray gun.
脱泡処理した塗料の結果を第1表の下段に示す。The results for the defoamed paint are shown in the lower part of Table 1.
第1表の結果より明らかの如く、本発明の方法に従って
実捲した実帷例1〜7は、良好なる脱泡処理出来たのに
対し、(霧化用空気容量)/(塗料噴出容量)比の小さ
い比較例1では脱泡率が悪く、脱泡処理後の塗料貯蔵安
定性も悪く、逆に比の大きい比較例4では脱泡処理後の
塗料にブッが多く発生するという結果が出た。As is clear from the results in Table 1, in Examples 1 to 7, which were rolled according to the method of the present invention, good defoaming treatment was achieved; Comparative Example 1, which had a small ratio, had a poor defoaming rate and poor storage stability of the paint after defoaming treatment, while Comparative Example 4, which had a high ratio, produced a lot of bubbles in the paint after defoaming treatment. Ta.
また邪魔板との距離を長くした比較例2では脱泡処理後
の塗料貯蔵安定性が悪く、逆に邪魔板との距離を短くし
た比較例3では脱泡処理後の塗料にブツが多く発生する
結果が出た。Furthermore, in Comparative Example 2, in which the distance to the baffle plate was long, the paint storage stability after degassing was poor, and on the contrary, in Comparative Example 3, in which the distance to the baffle plate was short, many particles appeared in the paint after degassing. I got the result.
また塗料ノズル口径の大きいスプレーガンを使用した比
較例5は脱泡処理後の塗料貯蔵安定性が悪い結果が出た
。Furthermore, in Comparative Example 5, in which a spray gun with a large paint nozzle diameter was used, the paint storage stability after defoaming treatment was poor.
脱泡率90%以上であると塗膜に悪影響を及ぼさない。A defoaming rate of 90% or more does not adversely affect the coating film.
注2)脱泡処理直後の捕集した塗料中のブツの発生◎:
ブツの発生なし、○:ブツが極くわずか発生、△:ブツ
が少し発生、×ブツが多量に発生
注3)脱泡処理し、捕集した塗料を35℃、1週間放置
◎:異常なし、○;極くわずかにシーディング、△:少
しシーディング、×ニジーディング大Note 2) Occurrence of particles in the collected paint immediately after defoaming treatment◎:
No lumps occur, ○: Very few lumps occur, △: A few lumps occur, × A large number of lumps occur Note 3) Defoaming treated and collected paint is left at 35℃ for 1 week ◎: No abnormality , ○: Very slight seeding, △: Slight seeding, × Large amount of seeding
第1図、第2図、第3図及び第4図は本発明に使用する
代表的なスラリー状塗料の脱泡装置の略図である。
1・・・・・・スプレーガン、2・・・・・・チャンバ
ー、3・・・・・・邪魔板、4・・・・・・捕集容器、
5・・・・・・スラリー状塗料槽。1, 2, 3, and 4 are schematic diagrams of a typical slurry paint defoaming device used in the present invention. 1... Spray gun, 2... Chamber, 3... Baffle plate, 4... Collection container,
5... Slurry paint tank.
Claims (1)
プレー乾燥しないように強く噴出し、壁あるいは邪魔板
に衝突させ、次いで衝突した噴霧液体粒子を捕集するこ
とを特徴とするスラリー状塗料の脱泡方法。 2 該スプレーガンの塗料ノズル口径が0.5〜4.0
mmである特許請求の範囲第1項記載のスラリー状塗料
の脱泡方法。 3 該スプレーガンの霧化空気圧が約1〜7kg/cm
2であり、塗料噴出量が約60〜1,000m1/分で
ある特許請求の範囲第1項または第2項記載のスラリー
状塗料の脱泡方法。 4 噴出を、霧化用空気容量/塗料噴出容量の比が約1
00〜2,000の条件下で行なう特許請求の範囲第1
項〜第3項記載のスラリー状塗料の脱泡方法。 5 スプレーガンと壁あるいは邪魔板との距離が約50
〜1,000mmであることを特徴とする特許請求の範
囲第1項〜第4項記載のスラリー状塗料の脱泡方法。[Claims] 1. A slurry-like paint containing air bubbles is strongly jetted from a spray gun so as not to dry, collides with a wall or a baffle plate, and then the collided sprayed liquid particles are collected. A method for defoaming slurry paint. 2 The paint nozzle diameter of the spray gun is 0.5 to 4.0.
2. The method for defoaming a slurry paint according to claim 1, wherein the diameter is 1 mm. 3 The atomizing air pressure of the spray gun is approximately 1 to 7 kg/cm.
2. The method for defoaming a slurry paint according to claim 1 or 2, wherein the amount of paint ejected is about 60 to 1,000 m1/min. 4 The jetting is controlled so that the ratio of atomizing air volume/paint jetting volume is approximately 1.
Claim 1 under the conditions of 00 to 2,000
A method for defoaming a slurry paint according to items 3 to 3. 5 The distance between the spray gun and the wall or baffle plate is approximately 50 mm.
5. A method for defoaming a slurry paint according to claims 1 to 4, characterized in that the thickness is 1,000 mm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7990479A JPS58909B2 (en) | 1979-06-25 | 1979-06-25 | Defoaming method for slurry paint |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7990479A JPS58909B2 (en) | 1979-06-25 | 1979-06-25 | Defoaming method for slurry paint |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS565164A JPS565164A (en) | 1981-01-20 |
| JPS58909B2 true JPS58909B2 (en) | 1983-01-08 |
Family
ID=13703262
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP7990479A Expired JPS58909B2 (en) | 1979-06-25 | 1979-06-25 | Defoaming method for slurry paint |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS58909B2 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS58107312U (en) * | 1982-01-18 | 1983-07-21 | 株式会社金久 | hand labeler |
| JPS58107311U (en) * | 1982-01-18 | 1983-07-21 | 株式会社金久 | hand labeler |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0711637U (en) * | 1993-08-02 | 1995-02-21 | 秀之 加藤 | Japanese-style room with floor columns |
| US5820955A (en) * | 1997-01-23 | 1998-10-13 | Brander; William M. | Absorbent container |
-
1979
- 1979-06-25 JP JP7990479A patent/JPS58909B2/en not_active Expired
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS58107312U (en) * | 1982-01-18 | 1983-07-21 | 株式会社金久 | hand labeler |
| JPS58107311U (en) * | 1982-01-18 | 1983-07-21 | 株式会社金久 | hand labeler |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS565164A (en) | 1981-01-20 |
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