JPS6351194B2 - - Google Patents
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- Publication number
- JPS6351194B2 JPS6351194B2 JP54095381A JP9538179A JPS6351194B2 JP S6351194 B2 JPS6351194 B2 JP S6351194B2 JP 54095381 A JP54095381 A JP 54095381A JP 9538179 A JP9538179 A JP 9538179A JP S6351194 B2 JPS6351194 B2 JP S6351194B2
- Authority
- JP
- Japan
- Prior art keywords
- oil
- decomposition
- paint
- group
- gasification
- 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
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- Paints Or Removers (AREA)
- Application Of Or Painting With Fluid Materials (AREA)
Description
本発明は、料理用装置の庫内壁を被覆して、食
品等の汚れを触媒的に浄化される油分の分解能力
を有する被覆表面に関する。酸化触媒をガラスフ
リツト中へ分解させて形成した被覆表面は従来か
ら提案され、実用化されているが充分ではなかつ
た。
本発明者らは、料理用装置の庫内壁に形成され
る食品等による汚れを触媒的に浄化する為に用い
る触媒系に関して検討した結果、強力な酸化能力
を持つた酸化触媒は不適当で、食品による悪質な
汚れの中心をなす脂肪酸の熱分解を単に活性化す
る触媒で、酸化能力がほとんどないか、あつても
それが極めて弱い系統の触媒が極めて有効である
ことを見出し既に提案した。
これ等の触媒群はどちらかと言うと塩基性物質
が多く、触媒を分散させて表面を形成させるため
の結合剤としては、水ガラス系統の結合剤が用い
られていた。しかし、水ガラス系統の無機質塗料
の弱点は、水蒸気、炭酸ガス等の多い高温の雰囲
気下においては、塗膜中に残留するアルカリが反
応して、炭酸水素ナトリウムなどの白色の生成物
を生じることであつた。
この欠点は、塗装条件側の管理により十分に解
消出来る面はあるが、この様な管理ができ難い環
境条件、被塗装物形状においては、上記の問題は
実用上困難な問題を発生させていた。
本発明者らは、先の触媒系を分散坦持させる結
合剤として、リン酸、酸性金属リン酸塩などのリ
ン酸系の塗料に着目して被覆面の形成を種々検討
した。
酸性金属リン酸塩系の結合剤を用いる場合、塩
基性物質の多量の添加、とくにアルカリ土類金属
の添加は塗料の硬化(ゲル化)反応を起こし、塗
料の造膜性を低下させる欠点があるので、
(1) 周基律表1A族または2A族の酸化物。
(2) 式(MA)x(MB)y(O)zで表わされる化合
物。
但し、MA:1A族または2A族の元素。
MB:3B族または4B族の元素。
O:酸素
x,y,z:整数を示す。
から成る群から選んだ1種以上の触媒と、Ti,
Fe,Ni,Co,Cr,Agの酸化物の群から選んだ
1種以上の触媒とを共存させた場合に極めて優れ
た効果を発揮すると共に表面処理としても良好で
あることを見出した。
汚染する有機化合物の主成分は、脂肪酸で炭素
数が15〜22位のものであり、主として、パルミチ
ン酸、ステアリン酸、オレイン酸、リノール酸、
リノレイン酸などである。これ等は、加熱下で
は、タール化して黒色化して汚れとなるが、この
タール化反応のプロセスは下記の2種類が考えら
れる。1つは、過酸化物等の不完全酸化化合物の
中間体を経て重合するプロセスであり、もう1つ
は、熱分解して脱水素し、オレフインを経て重合
するプロセスである。
本発明は、従来の酸化触媒を用いて、調理によ
り生成した汚染有機化合物を燃焼、即ち完全酸化
しようというのではなく、油分などの汚れは、液
体または固体の状態で表面に存在しているから、
その部分でタール化したりすると好ましくないの
で、この油分を気体の状態に変化させて表面から
遊離させるものである。
そのための表面としては、油分そのものの蒸発
を有効に利用できる状態が望ましく、油分のガス
化に関しては、蒸発のみに頼つていては不十分で
ある。蒸発のみを活発に行なわせることからすれ
ば、平滑度の高い金属面では油もよく拡がり、蒸
発速度も極めて早くなるが、この場合にはタール
化が避けられない。表面を凹凸にして表面積を増
大させる場合には、一見蒸発速度が早そうに思わ
れるが、凹凸により油の拡散自体が阻害されるこ
とと、表面に3次元的に多孔性を設けた場合に
は、むしろその構造が邪魔になつて、蒸発速度は
フラツトな場合よりも遅くなる。したがつて、完
全な浄化を目的とすれば、油分のガス化に及ぼす
何等かの表面の質的な寄与が必要である。
以下本発明の一実施例をサラダ油についてのガ
ス化分解反応の場合について詳述する。
サラダ油を200〜300℃で分解した場合の生成ガ
スとしては、メタン、エチレン、エタン、一酸化
炭素、ホルムアルデヒドなどが発生していること
を同定したが、これ以外にもサラダ油自体に含ま
れる成分とは異なる分解炭化水素が、空気共存下
での熱分解においては生成しているのを分析し
た。
試験条件は、約2mgの化合物粉体に対してマイ
クロシリンジを用いて、1.0μのサラダ油を混合
させた条件下で密閉ガラス容器内において、300
℃で10分間分解させたのち、生成ガスをガスクロ
に導入して分析した。
分析条件としては、N2キヤリア(60ml/分)
を用い、F――D検出器でH2流量は60ml/分
空気流量は0.5/分となし、カラム条件として
は、3mmφ×3mのシリコンG,E,SE―30,
5%液相(シラマイトWを担体)を用いて、150
℃で5分間保持したのち、5℃/分の昇温速度で
250℃まで昇温分析を行なつて、分解生成ガスを
検出した。
以上の条件で、同定まではしていないが、、保
持時間、100,106,139,173(秒)の位置に分解
生成物を検出した。
代表的な材料についての検出ピークの面積の積
分結果(デジタルインテグレータを用いて積分し
た数値、即ち上記の4つの分解生成物の計数値の
総和)は表に示すとおりである。
この表よりサラダ油(大豆油)の空気共存下で
の分解において良好な触媒活性を示す金属酸化物
または化合物としては、周期律表の1族から4族
の金属の酸化物、なかでも1A族、2A族のアルカ
リ、アルカリ土類金属およびその酸化物が挙げら
れる。
更に優れた化合物としては、(MA)x(MB)y
(O)zの形で表わされる化合物で、MAが1A族、
または2A族の元素、MBが3B族、または4B族の
元素が良好であることが分る。なおOは酸素、
x,y,zは整数を示す。とくにMAがNa,K,
CaMgより成り、MBがC,Si,Alより成る化合
物を用いる時には最良であることが分る。
The present invention relates to a coating surface that coats the inner wall of a cooking device and has the ability to decompose oil to catalytically purify stains from foods and the like. A coating surface formed by decomposing an oxidation catalyst into glass frit has been proposed and put into practical use, but it has not been sufficient. The present inventors investigated the catalyst system used to catalytically purify food stains formed on the inner walls of cooking equipment, and found that oxidation catalysts with strong oxidation ability were unsuitable. We have already found and proposed that a catalyst that simply activates the thermal decomposition of fatty acids, which are the main cause of food stains, has little or very weak oxidizing ability and is extremely effective. Most of these catalysts are composed of basic substances, and a water glass-based binder has been used as a binder to disperse the catalyst and form a surface. However, the weakness of water glass-based inorganic paints is that in high-temperature atmospheres with a lot of water vapor and carbon dioxide, the alkali remaining in the paint film reacts and produces white products such as sodium bicarbonate. It was hot. Although this drawback can be fully resolved by controlling the coating conditions, the above problems can become difficult in practice due to environmental conditions and the shape of the object to be coated, where such control is difficult. . The present inventors have focused on phosphoric acid-based paints such as phosphoric acid and acidic metal phosphates as binders for dispersing and supporting the catalyst system, and have conducted various studies on the formation of coated surfaces. When using an acidic metal phosphate binder, the addition of large amounts of basic substances, especially alkaline earth metals, has the disadvantage of causing a curing (gelling) reaction of the paint and reducing the film-forming properties of the paint. (1) Oxides of Group 1A or Group 2A of the Peripheral Table. (2) A compound represented by the formula (MA) x (MB) y (O) z . However, MA: Group 1A or 2A element. MB: Group 3B or 4B element. O: Oxygen x, y, z: Indicates an integer. one or more catalysts selected from the group consisting of Ti,
It has been found that when coexisting with one or more catalysts selected from the group of oxides of Fe, Ni, Co, Cr, and Ag, an extremely excellent effect is exhibited and it is also good as a surface treatment. The main components of organic compounds that pollute are fatty acids with a carbon number of 15 to 22, mainly palmitic acid, stearic acid, oleic acid, linoleic acid,
Such as linoleic acid. When heated, these substances turn into tar, turn black, and become stains, but the following two types of processes can be considered for this tar reaction. One is a process of polymerization via an intermediate of an incompletely oxidized compound such as a peroxide, and the other is a process of thermal decomposition, dehydrogenation, and polymerization via an olefin. The present invention does not use a conventional oxidation catalyst to combust, that is, completely oxidize, the polluting organic compounds generated during cooking, but because dirt such as oil exists on the surface in a liquid or solid state. ,
Since it would be undesirable if that part were to turn into tar, this oil is changed into a gaseous state and released from the surface. For this purpose, it is desirable that the surface be in a state where the evaporation of the oil itself can be effectively utilized; however, relying only on evaporation is insufficient for the gasification of the oil. Considering that only evaporation is active, oil will spread well on a highly smooth metal surface and the evaporation rate will be extremely fast, but in this case tar formation is unavoidable. When increasing the surface area by making the surface uneven, it may seem that the evaporation rate is faster, but the unevenness itself inhibits the diffusion of oil, and if the surface is made three-dimensionally porous, Rather, its structure becomes a hindrance, and the evaporation rate is slower than in the flat case. Therefore, for the purpose of complete purification, some qualitative contribution of the surface to the gasification of oil is necessary. An embodiment of the present invention will be described in detail below regarding a gasification and decomposition reaction of salad oil. We identified that methane, ethylene, ethane, carbon monoxide, formaldehyde, etc. are generated as gases generated when salad oil is decomposed at 200 to 300℃, but there are also other components contained in the salad oil itself. analyzed that different decomposed hydrocarbons were produced during pyrolysis in the presence of air. The test conditions were as follows: Approximately 2mg of compound powder was mixed with 1.0μ of salad oil using a microsyringe, and 300mg of compound powder was mixed with 1.0μ of salad oil in a sealed glass container.
After decomposition at ℃ for 10 minutes, the generated gas was introduced into a gas chromatogram and analyzed. The analysis conditions are N2 carrier (60ml/min)
The H2 flow rate was 60 ml/min and the air flow rate was 0.5/min with the F--D detector.The column conditions were 3 mmφ x 3 m silicon G, E, SE-30,
150 using a 5% liquid phase (Silamite W as carrier)
After holding at ℃ for 5 minutes, increase temperature at 5℃/min.
Decomposition gas was detected by temperature raising analysis to 250℃. Under the above conditions, decomposition products were detected at retention times of 100, 106, 139, and 173 (seconds), although they were not identified. The results of integrating the areas of detected peaks for representative materials (values integrated using a digital integrator, ie, the sum of counts of the four decomposition products mentioned above) are shown in the table. From this table, metal oxides or compounds that exhibit good catalytic activity in the decomposition of salad oil (soybean oil) in the presence of air include oxides of metals from groups 1 to 4 of the periodic table, especially group 1A, Examples include Group 2A alkali and alkaline earth metals and their oxides. An even better compound is (MA) x (MB) y
A compound represented by (O) z , where MA is group 1A,
Or, it is found that elements of group 2A, MB of group 3B, or group 4B are good. Note that O is oxygen,
x, y, z represent integers. Especially when MA is Na, K,
It is found that it is best to use a compound consisting of CaMg and MB consisting of C, Si, and Al.
【表】
ガス化分解反応に用いる触媒としては、MnO2
やCuOは反応を妨害するため活性な形での使用は
避ける必要があり、また金属酸化物でも、Ti,
Fe,Ni,Co,Cr,Agなどの金属酸化物は、ガ
ス化分解の活性を示しており、とりわけFeの場
合には、優れた活性を持つている。
住友化学のリン酸塩系無機耐熱塗料「スミセラ
ムPタイプ」を結合剤として、先の触媒化合物を
これにブレンドして、塗料とし、これをアルミニ
ウム処理鋼板に塗布して、焼成したものについて
試験した。「スミサラムPタイプ」は、結合剤
(リン酸塩)の主剤と、反応性金属酸化物、充填
剤、顔料からなる硬化剤との2成分系であり、ボ
ールミルにより調合する構成を採つているが、こ
れにガス化分解反応に明らかな活性を示すガス化
分解触媒を加えると、結合剤は酸性であり、ガス
化分解触媒が塩基性化合物である時、或いはアル
カリ土類金属塩である時には、ガス化分解触媒
は、結合剤と反応して、塗料をゲル化させ好まし
くない。
先づ、塗料のみ10cm角、板厚0.4mmのアルミニ
ウム処理鋼板上に塗布し、(乾燥後の膜厚で約
100μに塗布)、焼付けは、100℃にて10分間乾燥
したのちに、200℃にて10分、最後に300℃にて30
分焼付けた。この塗膜は、良好な密着性と耐水
性、耐摩耗性、耐熱衝撃性、耐熱性、耐蒸気性、
耐薬品性などの特性を示したが油分の浄化性能
は、ほとんど見られなかつた。
なお、油分の浄化能力は下記の試験により評価
した。即ち、10cm角のテストピースを250℃の温
度に設定されたホツトプレート上に置き、1μ
のサラダ油を約50点分散させて、塗膜表面上に配
置し、油のシミ跡の変化を目視により追跡して評
価した。前述の塗料のみの場合には、この試験
で、テストピースのほぼ全面に、サラダ油の残渣
がこびりついた状態でタール化した。
次に、ガス化分解触媒の中で、最も能力の優れ
た触媒の1つであるケイ酸カルシウム5重量%添
加した。
この場合、結合剤は著しくゲル化したが、約10
%の水を加えて粘度調整をし、前述の塗装条件に
て塗布した。得られた塗布面は、クラツクの生成
が目立ち、テープ剥離による密着性式験をすると
1部がピンホール状に剥離し、密着性では不十分
な面はあつたが、他の物性はほぼ良好であり、油
の浄化能試験では約5分で、ほとんどシミ跡なく
浄化する良好な浄化性能を示した。アルミン酸石
灰の場合もほぼ同じ結果を示した。
次に、ガス化分解触媒の中で、塗料をゲル化す
る恐れのない触媒添加物として最も有効と思われ
る酸化鉄(Fe2O3)を10%添加して、同じ試験を
実施した。この場合には、ほとんど塗料のみと変
わらない良好な塗膜物性が得られた。浄化能試験
においても、2,3点の2mmφ程度のタール化の
跡は残つたが、一応の能力は得られた。
次に同じく、酸化鉄5%とアルミン酸石灰1%
とを添加した場合について同様の試験を実施し
た。
この場合、表面がざらざらとしている以外には
ほとんど塗料のみの場合と変わらない表面状態の
塗膜面が得られた。この塗膜面は、極めて優れた
表面物性を示し、塗料のみの場合と変わらなく、
むしろ耐衝撃性などは優れている特性を示した。
この塗膜面は特に著しい浄化性能を示し、シミ跡
は数分で消失し、同じ試験を7回繰返しても表面
にはタールの痕跡は残らなかつた。
この様な優れた効果が得られた原因として、両
触媒の相乗作用というよりは、むしろアルカリ土
類金属の若干の添加により塗料が部分的にゲル化
して、とくにその表面層において、触媒化合物が
結合剤と反応することなく表面層に露出する構造
が達成されたことによるものと思われる。
ガス化分解触媒の添加量としては、遷移金属の
酸化物の場合には5%以上、アルカリ土類金属塩
の場合には1%以下が良好で、とくに両者を併用
して用いる方法が最良である。
本発明の適用は一般の金属面、或いはセラミツ
ク面など、リン酸塩系結合剤が塗装可能な面へは
いづれも適用でき、また、もち論耐食性の向上を
配慮して下塗り塗装の上に重ねて塗装することも
可能であるし、膜厚を得たい場合には、本塗膜を
焼成後、何度も重ね塗りすることも可能である。
以上のように、本発明は食品等の汚れを容易に
浄化できる表面を形成する工業的価値の大なるも
のである。[Table] As a catalyst used for gasification decomposition reaction, MnO 2
It is necessary to avoid using Ti, CuO and CuO in an active form as they interfere with the reaction, and even metal oxides such as Ti,
Metal oxides such as Fe, Ni, Co, Cr, and Ag exhibit gasification and decomposition activity, and Fe in particular has excellent activity. Sumitomo Chemical's phosphate-based inorganic heat-resistant paint "Sumiceram P Type" was used as a binder, and the catalyst compound described above was blended with this to form a paint.The paint was applied to an aluminum-treated steel plate and then tested. . "Sumisaram P type" is a two-component system consisting of a main binder (phosphate) and a hardening agent consisting of reactive metal oxides, fillers, and pigments, and is formulated using a ball mill. , when a gasification decomposition catalyst showing obvious activity in the gasification decomposition reaction is added, when the binder is acidic and the gasification decomposition catalyst is a basic compound or an alkaline earth metal salt, The gasification decomposition catalyst reacts with the binder and causes the paint to gel, which is undesirable. First, the paint was applied onto a 10 cm square, 0.4 mm thick aluminum-treated steel plate (the film thickness after drying was approx.
After drying at 100℃ for 10 minutes, baking at 200℃ for 10 minutes, and finally at 300℃ for 30 minutes.
I baked it separately. This coating has good adhesion, water resistance, abrasion resistance, thermal shock resistance, heat resistance, steam resistance,
It showed properties such as chemical resistance, but almost no oil purification performance was observed. The oil purification ability was evaluated by the following test. That is, a 10 cm square test piece was placed on a hot plate set at a temperature of 250°C, and
Approximately 50 spots of salad oil were dispersed and placed on the coating surface, and changes in the oil stains were visually tracked and evaluated. In the case of using only the above-mentioned paint, in this test, the residue of salad oil was stuck to almost the entire surface of the test piece and turned into tar. Next, 5% by weight of calcium silicate, which is one of the most efficient catalysts among gasification and decomposition catalysts, was added. In this case, the binder gelled significantly, but ca.
% of water was added to adjust the viscosity, and the coating was applied under the above-mentioned coating conditions. The resulting coated surface had noticeable cracks, and when testing adhesion by peeling off the tape, some parts peeled off in the form of pinholes, and adhesion was insufficient on some surfaces, but other physical properties were generally good. In an oil purifying ability test, it showed good purifying performance, cleaning almost no stains in about 5 minutes. Almost the same results were obtained for lime aluminate. Next, the same test was conducted with the addition of 10% iron oxide (Fe 2 O 3 ), which is thought to be the most effective catalyst additive among gasification decomposition catalysts and does not cause the paint to gel. In this case, good physical properties of the coating film were obtained, which were almost the same as those obtained with paint alone. In the purification ability test, tarry traces of about 2 mmφ remained at a few points, but a certain level of ability was obtained. Next, similarly, 5% iron oxide and 1% lime aluminate.
A similar test was conducted for the case where . In this case, a coated film surface with almost the same surface condition as the case of paint alone was obtained, except that the surface was rough. This coating surface exhibits extremely excellent surface physical properties, and is no different from that of paint alone.
Rather, it showed excellent properties such as impact resistance.
This coated surface showed particularly remarkable cleaning performance; stains disappeared within a few minutes, and no trace of tar remained on the surface even after the same test was repeated seven times. The reason for this excellent effect is not the synergistic effect of both catalysts, but rather the addition of a small amount of alkaline earth metal causes the paint to partially gel, causing the catalytic compound to disintegrate, especially in its surface layer. This seems to be due to the fact that a structure was achieved that exposed the surface layer without reacting with the binder. The amount of gasification decomposition catalyst added is preferably 5% or more in the case of transition metal oxides and 1% or less in the case of alkaline earth metal salts, and it is especially best to use both in combination. be. The present invention can be applied to any surface that can be coated with a phosphate-based binder, such as general metal surfaces or ceramic surfaces, and can also be applied over an undercoat to improve corrosion resistance. It is also possible to apply the coating using the same method, or if a thicker film is desired, it is also possible to apply multiple coats after baking the main coating film. As described above, the present invention has great industrial value in that it forms a surface that can easily clean food stains and the like.
Claims (1)
1種以上の酸化物を5wt%〜50wt%とCaO,
Na2O,K2O,MgO,K2CO3,CaSiO3,
CaAl2O4,MgSiO3,BaSiO3,BaTiO3,
Li2SiO3,Na2CO3,Ca(OH)2の群から選んだ化
合物の1種以上を1wt%以下の配合にて、リン酸
塩結合剤中に分散させた油分の分解能力を有する
被覆表面。1 5wt% to 50wt% of one or more oxides selected from the group of Ti, Fe, Ni, Co, Cr, Ag and CaO,
Na 2 O, K 2 O, MgO, K 2 CO 3 , CaSiO 3 ,
CaAl 2 O 4 , MgSiO 3 , BaSiO 3 , BaTiO 3 ,
One or more compounds selected from the group of Li 2 SiO 3 , Na 2 CO 3 , and Ca(OH) 2 are dispersed in a phosphate binder at a concentration of 1 wt% or less and have the ability to decompose oil. coated surface.
Priority Applications (9)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9538179A JPS5620071A (en) | 1979-07-26 | 1979-07-26 | Coated surface with oil-decomposition ability |
| FR7925616A FR2439040A1 (en) | 1978-10-16 | 1979-10-15 | COATED SURFACES COMPRISING A BINDER CONTAINING ONE OR MORE OXIDES, CAPABLE OF DECOMPOSING OILS |
| GB7935663A GB2037271B (en) | 1978-10-16 | 1979-10-15 | Surface coatings capable of decomposing oil |
| SE7908515A SE7908515L (en) | 1978-10-16 | 1979-10-15 | COATED SURFACES |
| AU51776/79A AU530955B2 (en) | 1978-10-16 | 1979-10-15 | Coated surfaces capable of decomposing oils |
| CA000337728A CA1149363A (en) | 1978-10-16 | 1979-10-16 | Coated surfaces capable of decomposing oils |
| DE19792941768 DE2941768A1 (en) | 1978-10-16 | 1979-10-16 | OIL-DEGRADATING COMPOSITION AND SURFACES, ESPECIALLY OVEN INTERIORS COATED WITH THE COMPOSITION |
| US06/480,380 US4471027A (en) | 1978-02-13 | 1983-04-05 | Coated surfaces capable of decomposing oils |
| US06/586,144 US4515862A (en) | 1978-10-16 | 1984-03-05 | Coated surfaces capable of decomposing oils |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9538179A JPS5620071A (en) | 1979-07-26 | 1979-07-26 | Coated surface with oil-decomposition ability |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5620071A JPS5620071A (en) | 1981-02-25 |
| JPS6351194B2 true JPS6351194B2 (en) | 1988-10-13 |
Family
ID=14136059
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP9538179A Granted JPS5620071A (en) | 1978-02-13 | 1979-07-26 | Coated surface with oil-decomposition ability |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5620071A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0315696A (en) * | 1989-06-13 | 1991-01-24 | Nikkiso Co Ltd | Enclosed compressor |
-
1979
- 1979-07-26 JP JP9538179A patent/JPS5620071A/en active Granted
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0315696A (en) * | 1989-06-13 | 1991-01-24 | Nikkiso Co Ltd | Enclosed compressor |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5620071A (en) | 1981-02-25 |
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