JP3071874B2 - Manufacturing method of purified lacquer - Google Patents
Manufacturing method of purified lacquerInfo
- Publication number
- JP3071874B2 JP3071874B2 JP3159628A JP15962891A JP3071874B2 JP 3071874 B2 JP3071874 B2 JP 3071874B2 JP 3159628 A JP3159628 A JP 3159628A JP 15962891 A JP15962891 A JP 15962891A JP 3071874 B2 JP3071874 B2 JP 3071874B2
- Authority
- JP
- Japan
- Prior art keywords
- lacquer
- rolls
- purified
- raw
- roll
- 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 - Fee Related
Links
- 239000004922 lacquer Substances 0.000 title claims description 117
- 238000004519 manufacturing process Methods 0.000 title claims description 15
- 239000000919 ceramic Substances 0.000 claims description 5
- 238000004898 kneading Methods 0.000 claims description 5
- 229910000831 Steel Inorganic materials 0.000 claims description 3
- 239000010959 steel Substances 0.000 claims description 3
- 239000004575 stone Substances 0.000 claims description 3
- 230000002093 peripheral effect Effects 0.000 claims description 2
- 239000002994 raw material Substances 0.000 description 13
- 239000011248 coating agent Substances 0.000 description 11
- 238000000576 coating method Methods 0.000 description 11
- 239000007788 liquid Substances 0.000 description 8
- 238000001035 drying Methods 0.000 description 7
- 238000007796 conventional method Methods 0.000 description 4
- 239000000047 product Substances 0.000 description 4
- 239000007787 solid Substances 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 230000014759 maintenance of location Effects 0.000 description 3
- 239000000428 dust Substances 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 238000007670 refining Methods 0.000 description 2
- 238000010998 test method Methods 0.000 description 2
- 206010053567 Coagulopathies Diseases 0.000 description 1
- 230000035602 clotting Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000006223 plastic coating Substances 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
Landscapes
- Compositions Of Macromolecular Compounds (AREA)
- Paints Or Removers (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は、漆器などの漆塗り製品
に用いる精製漆の製造方法に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing purified lacquer used for lacquered products such as lacquerware.
【0002】[0002]
【従来の技術】精製漆の品質は日本工業規格(K−59
50)に規定されており、当該規格に規定する品質を備
えた精製漆は、通常原料漆液又は生漆に所謂「なやし」
処理や「くろめ」処理を施すことにより製造されてい
る。即ち、先ず木製又はステンレス鋼製の桶内へ原料漆
液又は生漆を入れ、これを回転羽根で攪拌する(「なや
し」操作)。次に、攪拌した前記漆液を加熱して漆液内
の水分を除去し(「くろめ」操作)、最後に水分調整を
した漆液からごみ等の固形物を除去することにより、精
製漆を製造するものである。2. Description of the Related Art The quality of refined lacquer is based on Japanese Industrial Standards (K-59).
Purified lacquer having the quality stipulated in 50) and specified in the standard is commonly used as raw lacquer liquid or raw lacquer, so-called "Nayashi".
It is manufactured by subjecting it to processing or "clotting". That is, first, a raw lacquer liquid or raw lacquer is put into a wooden or stainless steel tub, and the raw lacquer is agitated by rotating blades ("Nayashi" operation). Next, the purified lacquer is heated by heating the stirred lacquer liquor to remove water in the lacquer liquor ("kurome" operation), and finally removing solids such as dust from the lacquer liquor having the adjusted water content. It is manufactured.
【0003】前記従来の精製漆の製造方法は極めて長い
歴史を有するものであり、優れた実用的効用を奏するも
のである。しかし、従来の精製漆の製造にも解決すべき
問題点が多く残されている。先ず第1の問題は、生漆等
の精製漆処理に要する時間の点である。即ち、従前の製
造方法は何れも所謂バッチ処理方式であり、且つ一回の
精製漆の製造に8〜10時間を必要とし、精製能率が極
めて悪いと云う難点がある。第2の問題は、漆塗膜の乾
燥に要する時間や漆塗膜の品質の点である。即ち、従来
の製法により製造した精製漆(透漆・黒漆)は一般的に
高粘度であるため、漆塗膜が硬化するまでに時間が掛か
り(例えば、20℃・80%RHの条件下で10〜12
時間を必要とする)、漆塗りの作業能率が著しく悪いう
え、形成された漆塗膜が透明性、耐光性及び耐候性(光
沢保持率)等の点で劣ると云う問題がある。[0003] The above-mentioned conventional method for producing purified lacquer has an extremely long history, and exhibits excellent practical utility. However, there are still many problems to be solved in the production of conventional purified lacquer. First, the first problem is the time required for processing the purified lacquer such as raw lacquer. That is, the conventional production methods are all so-called batch processing methods, and one production of purified lacquer requires 8 to 10 hours, and the purification efficiency is extremely poor. The second problem is the time required for drying the lacquer coating and the quality of the lacquer coating. That is, since the purified lacquer (translucent lacquer / black lacquer) manufactured by the conventional manufacturing method generally has a high viscosity, it takes time until the lacquer coating film is hardened (for example, at 20 ° C. and 80% RH). At 10-12
Time is required), the work efficiency of lacquering is extremely poor, and the formed lacquer coating film is inferior in terms of transparency, light resistance, weather resistance (gloss retention) and the like.
【0004】[0004]
【発明が解決しようとする課題】本発明は、従来のこの
種精製漆の製造方法に於ける上述の如き問題、即ち漆
の精製処理能率が低いこと、精製漆の粘度が高く、漆
塗膜の乾燥に長時間を必要とすること、形成された漆
塗膜の品質が比較的低いこと等の問題を解決せんとする
ものであり、低粘度で漆塗膜の乾燥時間が短く且つ高品
質の漆塗膜の形成を可能とした精製漆を、高能率で連続
的に、しかも安価に製造できるようにした精製漆の製造
方法を提供するものである。DISCLOSURE OF THE INVENTION The present invention relates to the above-mentioned problems in the conventional method for producing this type of purified lacquer, namely, the low lacquer refining efficiency, the high viscosity of the purified lacquer, To solve the problems such as the long time required for drying the lacquer film and the relatively low quality of the lacquer film formed. Low viscosity, short drying time of the lacquer film and high quality It is intended to provide a method for producing a purified lacquer which is capable of continuously and inexpensively producing a purified lacquer capable of forming a lacquer coating film.
【0005】[0005]
【課題を解決するための手段】本発明は、チルド、スチ
ール、セラミックス又は天然石を素材とする複数のロー
ル相互間若しくはプラスチックコーティングをした複数
のロール相互間で、原料漆又は生漆を連続的に混練する
ことを発明の基本構成とするものである。The present invention is to continuously knead raw lacquer or raw lacquer between a plurality of rolls made of chilled, steel, ceramics or natural stone or between a plurality of rolls coated with plastic. This is the basic configuration of the invention.
【0006】[0006]
【作用】原料漆液又は生漆は上方より低速回転側のロー
ル相互間へ供給される。供給された原料漆は、ロール外
表面に付着した状態で回転し、隣接するロール相互間で
混練されると共に、順次高速回転側のロール外表面へ付
着して行く。その間に原料漆液内の水分は蒸発等によっ
て除去され、且つ漆液そのものの練り込みが行なわれ
る。最外端のロール外表面へ付着した漆液はスクレーパ
ーによって掻き取られ、漆液内の固形物を除去した後、
精製漆として貯留されて行く。The lacquer liquid or raw lacquer is supplied from above to between the rolls on the low-speed rotation side. The supplied raw material lacquer rotates while adhering to the outer surface of the roll, is kneaded between the adjacent rolls, and sequentially adheres to the outer surface of the roll on the high-speed rotation side. During that time, the water in the raw material lacquer is removed by evaporation or the like, and the lacquer itself is kneaded. The lacquer liquid attached to the outermost roll outer surface is scraped off by a scraper, and after removing solids in the lacquer liquid,
It is stored as refined lacquer.
【0007】[0007]
【実施例】以下、図面に基づいて本発明の実施例を説明
する。図1は本発明の実施例の説明図であり、図に於い
てAは原料漆液又は生漆、1は原料タンク、2は漆液供
給口、3a・3b・3cは混練用ロール、4はスクレー
パ、5は機台、6は濾過器、7は精製漆タンク、Bは精
製漆である。Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 is an explanatory view of an embodiment of the present invention, in which A is a raw material lacquer or raw lacquer, 1 is a raw material tank, 2 is a lacquer liquid supply port, 3a, 3b and 3c are kneading rolls, 4 is A scraper, 5 is a machine stand, 6 is a filter, 7 is a purified lacquer tank, and B is a purified lacquer.
【0008】前記原料漆液Aはウルシの樹に傷をつけ、
にじみ出る樹液を採取した液であり、一般に荒味と呼ば
れているものである。また、生漆は、前記原料漆液をこ
して樹皮などの固形物を取り除いたものである。当該原
料漆液もしくは生漆Aとしては、日本産、中国産などの
他に種々のものがあるが、特に産地を限定されるもでは
ない。尚、本実施例に於いては於いては、中華人民共和
国の城口産の生漆Aが原料として使用されている。[0008] The raw material lacquer A damages the tree of sacrifice,
It is a liquid obtained by collecting the sap that oozes out, and is generally called rough taste. Raw lacquer is obtained by rubbing the raw material lacquer to remove solids such as bark. As the raw material lacquer or raw lacquer A, there are various types other than those from Japan, from China, and the like, but the place of production is not particularly limited. In this example, raw lacquer A from Shiroguchi in the People's Republic of China is used as a raw material.
【0009】前記混練用ロール3a・3b・3cはセラ
ミックを素材として形成されており、その外径は約50
mm、長さは200mmに選定されている。また、前記
各ロール3a・3b・3cは、水平面上に並列状に配設
され、機台5へ回動自在に支持されている。即ち、各ロ
ール3a・3b・3cは夫々隣接するロールが逆方向へ
回転するように、駆動装置(図示省略)により回転駆動
され、且つ各ロール相互間の間隙Gは間隙調整装置(図
示省略)により適宜寸法に調整されている。尚、前記各
ロール3a・3b・3cは、その回転周速度が原料供給
側から精製漆の取出し側へ向けて順次速くなるように回
転駆動されており、本実施例では第1ロール3aの回転
速度が80rpm、第2ロール3bの回転速度が200
rpm、第3ロール3cの回転速度が640rpmに夫
々設定されている。また、前記各ロール3a・3b・3
cの回転速度やロール間隙Gは、原料漆液Aの精製処理
量や原料漆液Aの粘度等によって適宜に調整され。The kneading rolls 3a, 3b, 3c are made of ceramic and have an outer diameter of about 50.
mm and length are selected to be 200 mm. The rolls 3a, 3b, and 3c are arranged in parallel on a horizontal plane, and are rotatably supported by the machine base 5. That is, each of the rolls 3a, 3b, and 3c is rotationally driven by a driving device (not shown) such that the adjacent rolls rotate in the opposite direction, and the gap G between the rolls is adjusted by a gap adjusting device (not shown). The size is adjusted as appropriate. The rolls 3a, 3b, and 3c are driven to rotate so that the circumferential speed of the rolls gradually increases from the raw material supply side to the refined lacquer take-out side. In the present embodiment, the rotation of the first roll 3a is performed. The speed is 80 rpm, and the rotation speed of the second roll 3b is 200
rpm and the rotation speed of the third roll 3c are set to 640 rpm, respectively. The rolls 3a, 3b, 3
The rotation speed c and the roll gap G are appropriately adjusted depending on the amount of the raw material lacquer A purified and the viscosity of the material lacquer A.
【0010】前記本実施例に於いては、混練用ロールと
してセラミックス製ロール3a・3b・3cを使用して
いるが、これに代えてチルド製ロールやスチール製ロー
ル、天然石製ロールを使用することも可能である。ま
た、所謂プラスチックコーティングを施したコーティン
グロールであってもよい。また、本実施例では外径50
mmのロールを使用しているが、ロールの外径は適宜に
選定可能である。例えば、外径250mmのロールを使
用した場合には、第1ロール3a、第2ロール3b、及
び第3ロール3cの回転数を夫々30rpm、60rp
m及び90rpmに選定している。更に、本実施例では
同外径の3本のロール3a・3b・3cを水平面上に並
列状に配列しているが、ロールの数は奇数本であれば何
本でもよい。また、各ロールの外径は夫々異なってもよ
く、この場合には、ロールの回転周速度が、下流側ほど
速くなるように各ロール回転数を制御する。更に、各ロ
ールは、軸心方向に見て彎曲状や三角状となるように配
列してもよく、ロール本数が増加した場合には彎曲状の
配列とする方が望ましい。In this embodiment, the ceramic rolls 3a, 3b and 3c are used as kneading rolls. Instead, chilled rolls, steel rolls and natural stone rolls are used. Is also possible. Further, a coating roll provided with a so-called plastic coating may be used. In this embodiment, the outer diameter is 50
Although a roll of mm is used, the outer diameter of the roll can be appropriately selected. For example, when a roll having an outer diameter of 250 mm is used, the rotation speeds of the first roll 3a, the second roll 3b, and the third roll 3c are set to 30 rpm and 60 rpm, respectively.
m and 90 rpm. Further, in this embodiment, three rolls 3a, 3b, 3c having the same outer diameter are arranged in parallel on a horizontal plane, but the number of rolls may be any number as long as it is an odd number. Further, the outer diameter of each roll may be different, and in this case, the rotation speed of each roll is controlled such that the rotational peripheral speed of the roll becomes higher toward the downstream side. Further, the rolls may be arranged so as to be curved or triangular when viewed in the axial direction. When the number of rolls increases, it is preferable to arrange the rolls in a curved shape.
【0011】原料漆液Aの精製に際しては、先ず各ロー
ル3a・3b・3cを夫々矢印方向へ所定の速度で回転
させる。次に、バルブ1aを開放し、原料タンク1から
適宜量の生漆Aを流出させ、供給口2から第1ロール3
aと第2ロール3bとの間隙Gの上方へ供給する。供給
された生漆Aは、各ロール3a・3b・3cの外表面へ
付着した状態下で隣接するロール相互間に於いて混練さ
れ、定常状態になれば、供給口2から供給された生漆A
にほぼ見合う量の精製漆B´が、スクレーパ4によって
第3ロール3cの外表面から連続的に除去され、濾過器
6上へ流下する。尚、供給された生漆Aは粘度が比較的
高いため、その全量がロール3a・3b・3cの各表面
へ付着した状態となり、機台5上へ滴下する漆は皆無と
なる。In purifying the raw material lacquer liquid A, first, each of the rolls 3a, 3b and 3c is rotated at a predetermined speed in the direction of the arrow. Next, the valve 1a is opened, an appropriate amount of raw lacquer A flows out of the raw material tank 1, and the first roll 3 is supplied from the supply port 2.
a above the gap G between the second roll 3b and the second roll 3b. The supplied raw lacquer A is kneaded between adjacent rolls while being attached to the outer surface of each of the rolls 3a, 3b, 3c, and when it reaches a steady state, the raw lacquer A supplied from the supply port 2 is supplied.
The purified lacquer B ′ in an amount corresponding to the above is continuously removed from the outer surface of the third roll 3 c by the scraper 4 and flows down onto the filter 6. In addition, since the supplied raw lacquer A has a relatively high viscosity, the entire amount thereof is in a state of being adhered to each surface of the rolls 3a, 3b, 3c, and there is no lacquer dripping onto the machine base 5.
【0012】濾過器6では、そのスクリーン6aによっ
て精製漆B´内のごみ等の固形物が除去され、最終製品
である精製漆Bが精製漆タンク7内へ貯留されて行く。
尚、前記濾過器6は、精製漆B´内のごみ等を連続的に
除去し得るものであれば、如何なる構造のものであって
もよいことは勿論である。In the filter 6, solids such as refuse in the purified lacquer B ′ are removed by the screen 6 a, and the purified lacquer B as a final product is stored in the purified lacquer tank 7.
The filter 6 may have any structure as long as it can continuously remove dust and the like in the purified lacquer B '.
【0013】前記実施例(生漆A・中華人民共和国の城
口産、ロール3・外径50mmφ、セラミック製、ロー
ル長さ・200mm、ロール回転数80rpm・200
rpm・640rpm)に於いては、生漆Aの供給量を
約0.3l/minとした場合に、水分含有量が2〜5
wt%の精製漆Bを約0.21l/minの割合で連続
的に取り出すことが出来る。即ち、約10lの精製漆B
を製造する場合には、本実施例では生漆Aの供給開始か
ら約10lの精製漆Bの取り出しまでに約10分間かか
り、且つロール等に付着した生漆Aの損失量は約1%と
なる。これに対して、従来の精製漆の製造方法によれ
ば、約10lの精製漆Bを得るのに約60分間かかり、
且つ桶等に付着した生漆Aの損失量は約5%となり、本
件発明に於いては、生漆Aの精製時間が大幅に短縮され
る。[0013] The above embodiment (raw lacquer A, from Shiroguchi, China, roll 3, outer diameter 50 mmφ, ceramic, roll length 200 mm, roll rotation speed 80 rpm 200
rpm / 640 rpm), when the supply amount of the raw lacquer A is about 0.3 l / min, the water content is 2 to 5
wt% of purified lacquer B can be continuously taken out at a rate of about 0.21 l / min. That is, about 10 l of purified lacquer B
In this embodiment, it takes about 10 minutes from the start of supply of the raw lacquer A to the removal of about 10 l of the purified lacquer B, and the loss amount of the raw lacquer A attached to the rolls and the like is about 1%. On the other hand, according to the conventional method for producing purified lacquer, it takes about 60 minutes to obtain about 10 l of purified lacquer B,
In addition, the loss amount of the raw lacquer A attached to the tub or the like is about 5%, and in the present invention, the purification time of the raw lacquer A is greatly reduced.
【0014】また、前記実施例により得られた精製漆B
と、従来方法により製造した精製漆との各種性能の比較
試験を行った。尚、試験試料には外径200mmの皿用
の木製生地を使用し、且つ下地仕上げや漆塗りは、両者
とも同じ条件としている。また、精製漆の性能比較試験
に於いて、下記の表1乃至表4は精製漆を所謂「黒漆」
とした場合を、表5精製漆を所謂「透漆」とした場合の
各性能を夫々示すものである。Further, the purified lacquer B obtained by the above embodiment
And a comparison test of various performances with a purified lacquer manufactured by a conventional method. The test sample used was a wooden cloth for a dish having an outer diameter of 200 mm, and the same conditions were used for the base finish and lacquering. In the performance comparison test of the purified lacquer, the following Tables 1 to 4 show that the purified lacquer is a so-called "black lacquer".
Table 5 shows each performance when the purified lacquer is a so-called "through lacquer".
【0015】表1は漆塗膜の乾燥時間の対比を示すもの
であり、漆塗膜の厚さ40μm(平均厚さ)、乾燥温度
20℃、PH75%の条件下に於ける対比である。Table 1 shows the comparison of the drying time of the lacquer coating film, under the conditions of a thickness of the lacquer coating film of 40 μm (average thickness), a drying temperature of 20 ° C. and a pH of 75%.
【0016】[0016]
【表1】 [Table 1]
【0017】表2は漆塗膜の硬度の立ち上がり(スオー
ドロッカー)を対比したものである。Table 2 compares the rise in hardness (sudlocker) of the lacquer coating film.
【0018】[0018]
【表2】 [Table 2]
【0019】表3は、漆塗膜の耐光性(光沢保持率)の
対比を示すものであり、JISK−5400に規定する
試験法により実施したものである。Table 3 shows a comparison of the light resistance (gloss retention) of the lacquer coating film, which was carried out according to a test method specified in JIS K-5400.
【0020】[0020]
【表3】 [Table 3]
【0021】表4は漆塗膜の耐候性(光沢保持率)の対
比を示すものであり、JISK−5400に規定する試
験法により実施したものである。Table 4 shows a comparison of the weather resistance (gloss retention) of the lacquer coating film, which was carried out according to a test method specified in JIS K-5400.
【0022】[0022]
【表4】 [Table 4]
【0023】表5は、精製漆Bを所謂「透漆」とした場
合の乾燥時間、粘度、光沢等の対比を示すものである。Table 5 shows a comparison of drying time, viscosity, gloss and the like when the purified lacquer B is so-called "lacquer lacquer".
【0024】[0024]
【表5】 [Table 5]
【0025】[0025]
【発明の効果】本発明では、複数本のロール相互間で原
料漆又は生漆を連続的に混練する構成としているため、
従来の製造方法に比較して漆の精製処理を短時間で行う
ことが出来、精製漆の製造コストの大幅な引下げが可能
となる。また、ロール相互間で原料漆又は生漆が均等に
且つ加圧下で混練されるため、従来の製造方法による精
製漆に比較して、精製漆の粘度が低下すると共に乾燥時
間が短縮され、更に耐光性や耐候性、透明性が大幅に向
上する。この様に、本発明で得られた精製漆は、その品
質が日本工業規格(JIS K−5950)の一級品に
適合する優秀な性能を有すると共に、製造コストの大幅
な引き下げによって安価となり、漆器などの漆塗り製品
の品質の向上、漆塗り作業の能率の向上及び製品コスト
の引き下げ等を図ることができる。According to the present invention, since raw lacquer or raw lacquer is continuously kneaded between a plurality of rolls,
The lacquer refining process can be performed in a shorter time as compared with the conventional production method, and the production cost of the purified lacquer can be significantly reduced. In addition, since the raw lacquer or raw lacquer is evenly kneaded under pressure between the rolls, the viscosity of the purified lacquer is reduced and the drying time is shortened, and the light resistance is further improved, as compared with the purified lacquer produced by the conventional production method. The properties, weather resistance and transparency are greatly improved. As described above, the purified lacquer obtained by the present invention has excellent performance conforming to the first grade of Japanese Industrial Standards (JIS K-5950), and is inexpensive due to a drastic reduction in manufacturing cost. It is possible to improve the quality of lacquered products such as lacquered products, improve the efficiency of lacquered work, reduce product costs, and the like.
【図1】本発明の実施例を示す説明図である。FIG. 1 is an explanatory diagram showing an embodiment of the present invention.
Aは原料漆液又は生漆、Bは精製漆、1は原料タンク、
2は漆液供給口、3は混練用ロール、4はスクレーパ、
5は機台、6は濾過器、7は精製漆タンク。A is a raw lacquer or raw lacquer, B is a purified lacquer, 1 is a raw material tank,
2 is a lacquer supply port, 3 is a kneading roll, 4 is a scraper,
5 is a machine stand, 6 is a filter, and 7 is a purified lacquer tank.
───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.7,DB名) C09F 1/02 C08L 93/00 C09D 193/00 ──────────────────────────────────────────────────続 き Continued on the front page (58) Field surveyed (Int. Cl. 7 , DB name) C09F 1/02 C08L 93/00 C09D 193/00
Claims (3)
然石を素材とする複数のロール相互間若しくはプラスチ
ックコーティングをした複数のロール相互間で、原料漆
又は生漆を連続的に混練することを特徴とする精製漆の
製造方法。1. Purified lacquer characterized by continuously kneading raw lacquer or raw lacquer between a plurality of rolls made of chilled, steel, ceramics or natural stone or between a plurality of rolls coated with plastic. Manufacturing method.
するロールを夫々逆方向へ且つ回転周速度が一方向から
他方向に向かって順次速くなるように回転駆動すると共
に、低速側のロール相互間へ上方より原料漆又は生漆を
連続的に供給し、高速側のロールの外表面より混練した
漆を連続的に掻き取るようにした請求項1に記載の精製
漆の製造方法。2. An odd number of rolls are arranged in parallel, and the adjacent rolls are rotationally driven in the opposite direction and the rotational peripheral speed is sequentially increased from one direction to the other direction. 2. The method for producing a purified lacquer according to claim 1, wherein raw lacquer or raw lacquer is continuously supplied from above to between the rolls, and the kneaded lacquer is continuously scraped off from the outer surface of the high-speed roll.
列して成る請求項2に記載の精製漆の製造方法。3. The method for producing a refined lacquer according to claim 2, wherein an odd number of rolls are arranged in parallel on a horizontal plane.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3159628A JP3071874B2 (en) | 1991-06-03 | 1991-06-03 | Manufacturing method of purified lacquer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3159628A JP3071874B2 (en) | 1991-06-03 | 1991-06-03 | Manufacturing method of purified lacquer |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH04359077A JPH04359077A (en) | 1992-12-11 |
| JP3071874B2 true JP3071874B2 (en) | 2000-07-31 |
Family
ID=15697876
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP3159628A Expired - Fee Related JP3071874B2 (en) | 1991-06-03 | 1991-06-03 | Manufacturing method of purified lacquer |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3071874B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2016000117A (en) * | 2014-06-12 | 2016-01-07 | 株式会社シナプス | Hair dehydration towel |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP7028483B2 (en) * | 2018-07-20 | 2022-03-02 | 有限会社橡 | Colored lacquer material and colored lacquer slit thread |
-
1991
- 1991-06-03 JP JP3159628A patent/JP3071874B2/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2016000117A (en) * | 2014-06-12 | 2016-01-07 | 株式会社シナプス | Hair dehydration towel |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH04359077A (en) | 1992-12-11 |
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