TW200927282A - Deoxidizer - Google Patents
Deoxidizer Download PDFInfo
- Publication number
- TW200927282A TW200927282A TW97129427A TW97129427A TW200927282A TW 200927282 A TW200927282 A TW 200927282A TW 97129427 A TW97129427 A TW 97129427A TW 97129427 A TW97129427 A TW 97129427A TW 200927282 A TW200927282 A TW 200927282A
- Authority
- TW
- Taiwan
- Prior art keywords
- oxygen
- layer
- cerium oxide
- gas barrier
- trigonal
- Prior art date
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/06—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising oxides or hydroxides of metals not provided for in group B01J20/04
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
- B01J20/28014—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their form
- B01J20/28033—Membrane, sheet, cloth, pad, lamellar or mat
- B01J20/28035—Membrane, sheet, cloth, pad, lamellar or mat with more than one layer, e.g. laminates, separated sheets
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/30—Processes for preparing, regenerating, or reactivating
- B01J20/3007—Moulding, shaping or extruding
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/30—Processes for preparing, regenerating, or reactivating
- B01J20/3078—Thermal treatment, e.g. calcining or pyrolizing
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01F—COMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
- C01F17/00—Compounds of rare earth metals
- C01F17/20—Compounds containing only rare earth metals as the metal element
- C01F17/206—Compounds containing only rare earth metals as the metal element oxide or hydroxide being the only anion
- C01F17/224—Oxides or hydroxides of lanthanides
- C01F17/235—Cerium oxides or hydroxides
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2002/00—Crystal-structural characteristics
- C01P2002/50—Solid solutions
- C01P2002/52—Solid solutions containing elements as dopants
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Analytical Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Inorganic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Geology (AREA)
- Thermal Sciences (AREA)
- Physics & Mathematics (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
- Laminated Bodies (AREA)
- Gas Separation By Absorption (AREA)
Abstract
Description
200927282 九、發明說明: 【發明所屬之技術領域】 本發明係關於含有氧化鈽之去氧劑。又,树 使用該去氧劑之去氧體、去氧樹脂組合物及腔; 體。進而本發明係關於前述氧化鈽之製造方法。、積層 【先前技術】 近年來’對於食品安全性及品質維持之高要求, ❹ ❹ 2使包裝食品之食品用包裝體内部成為無氧狀態, ,品之氧化變質。具體而言,將吸收除去氣氛甲之氧之去 乳劑與食品-同放入密封於食品用包裝體内部除 用包裝體内部之殘留氧,使舍σ '、食口口 離。另,於不…! 裝體内部成為無氧狀 -食品用包裝體包裝,:::進前述去氧劑- 門尺乳遇入前述食品用包 部之同時,對透過前述食品用包裝體侵入内部之 藉由内含之去氧劑將之除去等。 量氧亦 作為除去氣氛中之氧之去氧 成者與由I㈣材料構w劑已知有由有機系材料構 …、機糸材料構成者。該等材料之 考慮,主要利用作為I機糸 本角度 氧劑,如下述化學式(;、)所」’、之鐵系去氧劑。該鐵系去 盘h Γ ,使鐵與氣氛中少量水分-門 ,、乳乳中之氧反應,藉此從氣氛中除去氧。 冋200927282 IX. DESCRIPTION OF THE INVENTION: TECHNICAL FIELD OF THE INVENTION The present invention relates to an oxygen scavenger containing cerium oxide. Further, the tree uses the oxygen scavenger, the deoxidizing resin composition, and the cavity. Further, the present invention relates to a method for producing the aforementioned cerium oxide. [Prior Art] In recent years, in order to meet the high requirements for food safety and quality maintenance, ❹ ❹ 2 has made the inside of the package for foods in packaged foods anaerobic, and the products are oxidized and deteriorated. Specifically, the de-emulsion which removes the oxygen of the atmosphere and the foodstuff are placed in the inside of the package for food, and the residual oxygen in the inside of the package is removed, so that the slag and the mouth are separated. Also, no... The inside of the package is an anaerobic-food package, and::: into the above-mentioned deoxidizer - the door-to-milk meets the food package, and the inside of the food package is invaded by the inside. The deoxidizer removes it and the like. The oxygen is also used as an oxygen scavenger for removing oxygen in the atmosphere and a material composed of an organic material and a material for the I (four) material. The consideration of these materials is mainly to use an oxygen-based deoxidizer as an oxygen generator such as the following chemical formula (;,). The iron is removed from the atmosphere, and the iron is reacted with a small amount of moisture in the atmosphere, the oxygen in the emulsion, thereby removing oxygen from the atmosphere.冋
Fe+1/2H2〇+3/4〇2〜Fe〇〇H ⑴ 仁,使用刖述先前之鐵系$胃& 題。 鐵系去氧劑之情形,具有下述問 (1)與氧反應時水分所堂 所需雖少但卻必要,故保存乾燥食 133482.doc 200927282 去氧劑之性能 :、電子零件及焊料粉等忌水製品之情形 就無法充分發揮。 (2) 食品與鐵系去氧劑一同包裝之製品+,進 金屬等異物混入之檢杳 有 於金屬檢—之睛形,該去氧劑中之鐵粉會反應 於金屬探測機’無法進行簡便之檢查。 (3) 曾發生因微波爐等之微波快速加熱而起火。Fe+1/2H2〇+3/4〇2~Fe〇〇H (1) Kernel, use the previous iron system $ stomach & In the case of an iron-based oxygen scavenger, the following problems are required: (1) The amount of water required for the reaction with oxygen is small but necessary, so the performance of the dry food 133482.doc 200927282 deoxidizer is preserved: electronic parts and solder powder If the situation of avoiding aquatic products is not enough, it will not be fully utilized. (2) The food packaged with the iron-based deoxidizer +, the incorporation of foreign matter such as metal into the metal is detected in the shape of the metal, the iron powder in the oxygenator will react to the metal detector 'cannot be carried out Easy check. (3) There was a fire caused by rapid microwave heating of a microwave oven or the like.
施為㈣去氧劑料之去氧劑,有人提出有經實 %理之無機氧化物、即具有氧缺陷之無機化合物 (參照專利文獻!至5)。同文獻中,作為具有氧缺陷之無機 氧化物,例示有二氧化欽、氧化鋅、氧化鈽。具有氧缺陷 之無機氧化物為氧化鈽之情形,該氧化鈽為螢石型之結晶 構造。該等無機氧化物’在與氧反應時無需存在水分此點 上’相對於鐵系去氧劑有利。但’該等無機氧化物之氧吸 收量’不及鐵系去氧劑。 專利文獻1:日本特開2005-104064號公報 專利文獻2:曰本特開20〇5· 105194號公報 專利文獻3:日本特開2005-105195號公報 專利文獻4 :日本特開2005-1051 99號公報 專利文獻5 :日本特開2005-105200號公報 【發明内容】 本發明係提供一種去氧劑,其特徵在於:含有具有三方 晶型之結晶構造、以Ce2〇3 χ(χ係〇以上、小於1之數)表示 之氧化鈽。 另’本發明係提供一種去氧體,其係於具有抗透氣度之 133482.doc 200927282 袋:包裝體内收容有前述去氧劑而成者。 另’本發明係提供_ 去氧劑與具有氧易透過性之樹脂脂組合物’其係含有前述 去:樹二發::提供—種去氧積層體薄膜,其係於由前述 壁性之氣體障壁層’ “一 卸槓層具有乳體障 易透過於該去氧層之另—面,積層具有氧 易透過性之氧易透過層而成。 本發明係提供—種氧化飾之製造方法,前述氧化 於八有二方晶型之結晶構造,並以%〇3办係〇以上小 之數)表示’該氧化鈽之製造方法包含: 將含氧錦鹽或其水合物在還原氣氛下以⑽代以上培燒 之步驟;或者 將以Ce〇2表示之氧化錦在還原氣氛下以12〇代以上培 之步驟。 【實施方式】 ❷ 以下對本發明基於其較佳實施形態進行說明。本發明之 去氧劑,作為其構成成分,係含有具有特定結晶構造之氧 化鈽而構成。具體而言’該氧化飾係具有三方晶型之結晶 構造、以Ce2〇3.x(x係〇以上、小於i之數)表示之物質。 另,在以下之說明中,為區別該氧化飾與先前所知之具有 螢石型結晶構造且具有氧缺陷之氧化飾,將之稱之為三方 晶型氧化鈽。 三方晶型氧化鈽具有如圖!所示之結晶構造。即,具有& 軸長、b轴長及c轴長均相同,且各軸之間之角度” β及丫 133482.doc -8 · 200927282As an oxygen scavenger of (4) an oxygen scavenger, it has been proposed to have an inorganic oxide, that is, an inorganic compound having an oxygen deficiency (see Patent Documents! to 5). In the same literature, as the inorganic oxide having oxygen deficiency, there are exemplified by dioxins, zinc oxide, and cerium oxide. The inorganic oxide having oxygen deficiency is cerium oxide, which is a fluorite-type crystal structure. These inorganic oxides are advantageously in contact with the oxygen-based oxygen scavengers in the absence of moisture in the reaction with oxygen. However, the oxygen absorption of these inorganic oxides is less than that of iron-based deoxidizers. Patent Document 1: JP-A-2005-104064 Patent Document 2: Japanese Patent Laid-Open Publication No. Hei. No. 2005-105195. Patent Document 3: JP-A-2005-105195 Patent Document 4: JP-A-2005-1051 99 SUMMARY OF THE INVENTION The present invention provides an oxygen scavenger comprising a crystal structure having a trigonal crystal form, and having a Ce2〇3 χ (χ 〇 〇 〇 〇 〇 〇 〇 〇 〇 〇 〇 〇 〇 〇 2005 2005 C C C C C C C C C C , less than 1) expressed by yttrium oxide. Further, the present invention provides an oxygen scavenger which is 133482.doc 200927282 bag having air permeability resistance: a package in which the aforementioned oxygen scavenger is contained. Further, the present invention provides a deoxidizing agent and a resinous resin composition having oxygen permeability, which comprises the foregoing: a second hair: a deoxidized laminate film provided by the aforementioned wall property "Gas barrier layer" "a barrier layer has a milk barrier that is easily transmitted through the other surface of the deoxidation layer, and is formed by an oxygen-permeable layer that has oxygen permeability. The present invention provides a method for producing an oxidation decoration. The oxidized crystal structure of the octagonal crystal form is represented by a number of 〇3 〇 办 ) ) ) ' ' ' ' ' 该 该 该 该 该 该 该 该 该 该 该 该 该 将 含 含 含 含 含 含 含The step of firing in (10) or more; or the step of cultivating the oxidized bromine represented by Ce 〇 2 in a reducing atmosphere in 12 以上 or more. EMBODIMENT Hereinafter, the present invention will be described based on preferred embodiments thereof. The oxygen scavenger of the present invention contains a cerium oxide having a specific crystal structure as a constituent component. Specifically, the oxidized metal has a crystal structure of a trigonal crystal structure, and has a Ce2〇3.x (x system or more). , less than the number of i) Further, in the following description, in order to distinguish the oxidized metal from the previously known oxidized crystal having a fluorite crystal structure and having oxygen deficiency, it is referred to as a trigonal cerium oxide. It has the crystal structure shown in Fig.!, that is, with & axis length, b-axis length and c-axis length are the same, and the angle between each axis" β and 丫 133482.doc -8 · 200927282
均相同並為非90度角之社曰μ A 度月之結晶構造。與之相 具有榮石型結晶構造之氧化飾,且古"十&前所知之 造。 、有如圖2所示之結晶構 如前所述,三方晶型氧化 之數彳矣-4 A 鈽以Ce2〇h(x係〇以上、小於i 之數)表不。式中,xg〇情 _ 滑形之二方晶型氧化錦,具有 如圖1所不之結晶構造。該 具有 價數A-僧 .Λ 形之二方日日型氧化鈽中鈽之 1買數為二價》〇以外之 心 圖1所- η之二方晶型氧化鈽,於 圖1所不之結晶構造中,氧 ^ .^ 听占位置中之幾處位置之惫士 為缺陷狀態。因此,該情 之氧成 數,對於-部分飾,因電冇補償型乳化鈽十鏵之價 外之數… 低於三價。即,X為。以 外之數之情形之三方晶型氧化 為二價<!伋僧# β π 系成為存在部分原子價 勹一價戈更低價數之鈽之異常原子價狀態。 二方晶型氧化鈽,其社罗φ 就越高。即,式氧缺陷越多’其氧吸收量 作,若… χ值越大,氧吸收量就越高。 ❹ 仕曰摄Λ 則不易穩定維持三方晶型之 、·口日日構造。從此觀點而言, 於1,紅从Α 别述式中之X值宜為大於0、小 、 較佳為大於〇、0.5以Τ'。#,π 理由A * 卜另,设x之上限值小於 一,X為1之情形下氧化鈽將盔法维捭-古a ^ 構造,而成為岩镑^^士曰 去維持二方曰曰型之結晶 收量。成為石鹽型之結晶構造,難以實現所希望之氧吸 陷Si氧化飾,藉由與氧接觸、將之吸收,首先氧缺 相對,先前所知之具有勞石二曰曰構…化飾。與之 化… 結晶構造且具有氧缺陷之氧 I7使吸收乳後其結晶構造亦無變化’式⑽2 y中作 133482.doc 200927282 為氧缺陷量之y值只在〇以上、小於〇·5之範圍内變動。因 如此之不同,三方晶型氧化鈽係具有遠超過具有螢石型結 晶構造之氧化鈽之理論界限的高氧吸收量。 。 二方晶型氧化鈽之氧吸收量,可藉由於該氧化鈽中添加 使乳吸收量增大之元素’使之置換固溶成為複合氧化物, 而進一步增大。添加元素,比如可從鎂(Mg)、鈣(Ca)、鳃 (Sr)鋇(Ba)、鑭(La)、鈮(Nb)、镨及釔所組成之群They are all the same and are non-90 degree angles of the 曰μ A degree of crystal structure. It is oxidized with a sapphire crystal structure, and it was made by the ancient "Ten & There is a crystal structure as shown in Fig. 2. As described above, the number 彳矣-4 A 钸 of the trigonal crystal oxidation is represented by Ce2〇h (x system 〇 or more, less than i). In the formula, xg 〇 _ sliding digonal crystal oxidized bromine, having a crystal structure as shown in Fig. 1. The number of the valence A-僧.Λ-shaped two-day type yttrium oxide 钸 钸 买 买 买 买 买 买 买 〇 〇 〇 〇 心 心 心 心 心 心 η η η η η η η η η η η η In the crystal structure, the oxygen is a defect state in a few places in the position. Therefore, the oxygen number of the situation, for the - part decoration, due to the price of the electric compensation type emulsification 钸 铧 ... ... ... ... ... ...... That is, X is. In addition, the trigonal crystal oxidation of the case is a divalent <!汲僧# β π system becomes an abnormal valence state in which a part of the valence valence is valence. The binary crystal yttrium oxide has a higher φ. That is, the more the oxygen deficiency is, the more the oxygen absorption amount is, and if the value is larger, the oxygen absorption amount is higher. ❹ 曰 曰 曰 不易 不易 不易 Λ Λ Λ Λ Λ Λ Λ Λ 曰 曰 不易 曰 曰 曰 曰 曰 曰From this point of view, the X value in 1, the red from Α is preferably greater than 0, small, preferably greater than 〇, and 0.5 Τ'. #,π Reason A * Bu Another, let x upper limit be less than one, X is 1 in the case of yttrium oxide will be the helmet method - ancient a ^ structure, and become the rock pound ^ ^ gentry to maintain the two sides The crystal yield of the 曰 type. When it is a crystal structure of a salt-salt type, it is difficult to achieve a desired oxygen-absorbing Si oxide, and it is contacted with oxygen and absorbed. First, oxygen deficiency is relatively high, and it has been previously known to have a stone structure. With the crystal structure and oxygen-deficient oxygen I7, there is no change in the crystal structure after absorption of milk. 'Formula (10) 2 y is used as 133482.doc 200927282 The y value of oxygen deficiency is only above 〇, less than 〇·5 Changes within the scope. Because of this difference, the trigonal cerium oxide system has a high oxygen absorption amount far exceeding the theoretical limit of cerium oxide having a fluorite-type crystal structure. . The oxygen absorption amount of the ternary crystal cerium oxide can be further increased by adding the element which increases the amount of emulsion absorption to the cerium oxide to form a composite oxide. Adding elements such as a group consisting of magnesium (Mg), calcium (Ca), strontium (Sr) strontium (Ba), strontium (La), strontium (Nb), strontium and barium
中選擇至少—種。該等元素中,添加從記⑺、㉝(Ca)及镨 ㈣所組成之群中選擇之至少一種,可顯著增大氧吸二 量’故特別適合。 别述元素之總添加量’從能穩定增大三方晶型氧化鈽之 氧吸收量之點來看,宜相對於鈽原子為1〜20 mol%。 先前所知之螢石㉟氧化鈽因具有高氧離子導電性,故其 活性非常高,氧吸收速度非常快。因Λ,使用螢石型氧化 筛之去氧劑,在等待與目標製品(比如乾燥食品或錠劑等) :同密封於包裝袋的期間就已吸收氧,從而降低去氧劑之 氧及收量。與之相對,三方晶型氧化鈽除具有氧吸收量高 之特徵之外’亦具有氧吸收速度相對較慢之特徵。氧吸收 速度較慢之理由係,=方a 一万日日型氧化鈽不具有氧離子導電 三方晶型氧化鈽之本發明之去氧劑,即使接觸大 逐漸氧化,故在等待與目標製品-同密封之時間設 疋上具有自由度。 曰=晶型氧化锦一般以粉末狀態使用。根據情形,三方 曰曰氧化鈽亦可以壓縮成形體等成形體之狀態使用。另, 133482.doc 200927282 三方晶型氧化鈽可藉由單獨使用其本身而構成本發明之去 氧劑。或,藉由將三方晶型氧化鈽與其他物質組合使用, 亦可構成本發明之去氧劑。作為其他物質,比如可列舉各 種除濕㈣。藉由與除㈣彳制,可構成具有除濕能之去 氧劑。與除濕劑併用之㈣,氧化飾相料氧化錦與除濕 劑之合計重量所占比例宜為5〇~99重量% ,尤其為6〇〜85重 量%。另-方面,除濕劑所占比例宜為卜咒重量%,尤其Choose at least one of them. Among these elements, at least one selected from the group consisting of (7), 33 (Ca), and 镨 (4) is added, and the amount of oxygen absorption can be remarkably increased, which is particularly suitable. The total addition amount of the elements described above is preferably from 1 to 20 mol% with respect to the ruthenium atom from the viewpoint of stably increasing the oxygen absorption amount of the trigonal iridium oxide. The fluorite 35 cerium oxide previously known has high oxygen ion conductivity, so its activity is very high and the oxygen absorption rate is very fast. Because of the use of fluorite-type oxidizing screen deoxidizer, while waiting for the target product (such as dry food or tablets, etc.): the oxygen is absorbed during the sealing of the packaging bag, thereby reducing the oxygen and oxygen of the oxygen scavenger the amount. In contrast, the trigonal cerium oxide has a feature that the oxygen absorption rate is relatively slow, in addition to the feature of high oxygen absorption. The reason why the oxygen absorption rate is slow is that the deoxidizer of the present invention does not have the oxygen ion-conducting trigonal crystal cerium oxide, and even if the contact is gradually oxidized, it is waiting for the target product - The time of the seal is set to have a degree of freedom.曰 = crystalline oxidized bromine is generally used in a powder state. Depending on the case, the trigonal antimony oxide can also be used in a state in which a molded body such as a molded body is compressed. Further, 133482.doc 200927282 Trigonal crystalline cerium oxide can constitute the deoxidizing agent of the present invention by using itself alone. Alternatively, the trioxane type cerium oxide may be used in combination with other substances to form the oxygen scavenger of the present invention. As other substances, for example, various dehumidifications (four) can be cited. By deuterium (4), a deoxidizing agent having dehumidifying energy can be constructed. In combination with the desiccant (4), the ratio of the total weight of the oxidized decorative material oxidized bromine to the dehumidifying agent is preferably from 5 〇 to 99% by weight, particularly from 6 〇 to 85 % by weight. On the other hand, the proportion of desiccant should be the weight of the curse, especially
為15〜40重量%。作為除濕劑,可使用無機系物質及有機 系物質之任—種。作為無機系除濕劑,可使m絲光彿 石、斜發沸石、毛衫等天料石,分子料合成沸石, 膨满土、蒙脫土等黏土系礦物,石夕膠、氧化銘、氧化妈、 具有吸濕性之鹽等。作為有機系除濕劑,可使用紙聚、含 有紙歡之紙、聚α,β不飽和㈣、聚α,ρ不飽和缓酸之離子 交聯物、乙婦-醋酸乙婦共聚物之部分/完全息化物、聚 醋酸乙烯醋之部分/完全4化物、纖維素系衍生物、聚亞 炫基氧化物衍生物、聚醋、聚酿胺等。前述除濕劑中,從 每單位重量之吸濕量大、低濕度下之吸濕力大、化學性穩 定、無發減毒性等安全性觀點考慮,特別宜使 礦物。 二方晶型氧化鈽以粉末狀態使用之情形,其粒徑可根據 :發明之去氧劑之劑型選擇恰當數值。比如本發明之去氧 劑收容於具有抗透氣度之袋狀包裝體(比如 1〇〜觸卿、)内之情形,從確保足夠的比表面積、確❹ 氧接觸之點來看,平均粒徑宜為〇 〇ι〜ι〇〇㈣、尤其為 133482.doc 200927282 0.0H μπ^。本發明之去氧劑與具有氧易透過性之樹脂構 成樹脂組合物形成薄膜形態之情形,氧化飾之粒徑宜為不 超過薄膜厚度之範圍。從該觀點考慮,氧化飾之平均粒徑 宜為0.01 20 μηι、尤其為〇〇1〜1〇㈣。本說明書中之平均 冑徑係藉由雷射繞射散射式粒度分布測定裝置進行測定。’ . 本發明之去氧劑’藉由將其收容於具有抗透氣度之袋狀 包裝體(比如抗透氣度1〇〜1〇〇〇〇〇秒)内,成為去氧體。該 形〜之去氧體’與比如乾燥食品或錠劑-同密封收容於包 裝材料Θ。作為構成包裝體之具有抗透氣度之材料,可列 舉由聚丙烯、聚丁二婦、聚甲基戊稀、熱可塑性彈性體、 聚對苯二甲酸乙二醇醋、石夕網樹脂、乙稀—醋酸乙稀共聚 物、聚異戊二烯、超低密度聚乙烯、低密度聚乙稀、中密 度聚乙烯、丙稀-乙烯共聚物、丙稀—乙稀無規聚合物、 乙烯·α烯烴共聚物等各種熱可塑性樹脂構成之薄膜經實施 穿孔者、紙或不織布或組合該等而成之積層體。此處之抗 Φ 透氣度,係根據JIS Ρ8117進行測定,表示100 mL空氣在 氣壓差l_23kPa下完全透過〇.〇〇〇642 m2面積所需時間。 本發明之去氧劑,亦可與具有氧易透過性之樹脂混練, 構成去氧樹脂組合物。該樹脂組合物,比如以顆粒狀形態 使用,作為各種樹脂成形體之原料。另,該樹脂組合物, 以由該顆粒狀所成形之各種樹脂成形體之形態、比如薄膜 形1、或盤开乂態進行使用。該樹脂組合物無論為何種形態, 從充刀展現去氧機能之觀點而言,該樹脂組合物中去氧劑 所占比例宜為1〇〜90重量%,尤其為2〇〜8〇重量%。另一方 133482.doc •】2- 200927282 面^從保持該樹脂組合物之強度及成形性之觀點而言,該 樹脂組合物中樹脂所占比例宜為10〜90重量%,尤其為 20〜80重量%。 ❹ ❹ 前述樹脂組合物以薄膜形態使用之情形,雖亦根據該薄 膜之具體用途,但該薄膜之厚度宜為^00㈣,尤其為 20 40 μηι。包括前述樹脂組合物為薄膜形態之情形,可於 該樹脂組合物中根據需要,除去氧劑及具有氧易透過性之 樹脂外,添加能使該樹脂組合物之特性提高之其他成分。 作為其他成分,比如可列舉用以將樹脂組合物著色成特定 顏色之顏料,及用以提高樹脂組合物強度之填料等。 前述薄膜可以由别述去氧樹脂組合物構成之單層狀態進 行使用。或者,亦可以具有前述去氧樹脂組合物所構成之 去氧層之多層構造之狀態進行使用。後者之情形,作為多 層構造之-例’可列舉於前述去氧樹脂組合物所構成之去 氧層之一面,積層具有氣體障壁性之氣體障壁層,且於該 去氧層之另-面’積層具有氧易透過性之氧易透過層二 氧積層體薄膜。前述去氧積層體薄膜係以如下方式使用, 即氣體障壁層向外(即大氣側),而氧易透過層向内(即欲去 氧之氣氛側)。氣體障壁層’至少具有對氧透過 性,宜亦具有對水分之阻障性。 前述去氧積層體簿腔;夕 ^ ^ ^ 瓶溥膜之一實施形態如圖3所示。同 示之去氧積層體薄膜1〇,且 具有由前述去氧樹脂組合物構成 之去氧層11。該去裊屉丨!# 氧層1之—面,設有與該去氧層11鄰接 之氣體障壁層12。另一方而 洲接 ’去氧層Π之另一面,設有與 133482.doc -13. 200927282 該去氧層11鄰接之氧易透過層13。此外,氣體障壁層12之 外側’設有與該氣體障壁層12鄰接之該氣體障壁層12之保 護層14。 圖3所示之去氧積層體薄膜1〇中之氣體障壁層12之材 料,可使用例如銘箔、聚乙稀醇、聚偏二氣乙稀塗佈延伸 尼龍(商品名)、對苯二甲酸一三曱基六亞曱基二胺縮聚 物、2,2 —雙(對胺基環己基)丙烷—己二酸共聚物、乙烯一 乙烯醇共聚物、聚氯乙烯、尼龍MXD(商品名)、尼龍6(商 品名)、尼龍6,6(商品名)等。 圖3所示之去氧積層體薄膜1〇中之氧易透過層13,係至 少可透過氧之層。三方晶型氧化鈽與除濕劑共同使用之情 形’氧易透過層13宜為可透過氧及水分之層。作為氧易透 過層13之材料,可使用比如不織布、聚乙烯(低密度聚乙 烯、超低密度聚乙烯等)、延伸聚丙烯(PP)、聚丙烯、乙烯 丙烯共聚物、乙烯丙烯橡膠、乙烯一丙烯酸乙酯共聚物 等。 作為圖3所示之去氧積層體薄膜1〇中之保護層14之材 料,可使用比如聚乙烯、聚丙烯、聚對苯二甲酸乙二醇酯 (PET)、聚醯胺等。 去氧積層體薄膜之另一實施形態如圖4所示。該圖所示 之積層體薄膜10',係於圖3所示之積層體薄膜上進一步增 加其他層者。具體而言,於去氧層;Π與氣體障壁層12之間 設置緩衝層15。另,於氣體障壁層12之外側,即氣體障壁 層12與保護層14之間,設置高度氣體障壁層16。 133482.doc 14 200927282 圖4所示之去氧積層體薄膜10,之緩衝層15,係對從薄膜 10’之外側所施加之物理性衝擊起緩衝作用之層。作為緩衝 層15之材料,可使用比如聚乙烯、聚丙烯等。 ❹It is 15 to 40% by weight. As the dehumidifying agent, any of an inorganic substance and an organic substance can be used. As an inorganic dehumidifying agent, it can be used as a mineral stone such as m-ray phos stone, clinoptilolite, sweater, etc., molecular material synthesis zeolite, bulk soil, montmorillonite and other clay minerals, Shi Xijiao, Oxidation Ming, oxidation mother , hygroscopic salts, etc. As the organic dehumidifying agent, paper poly, paper containing paper, poly-α, β-unsaturated (tetra), poly-α, ρ-unsaturated acid-exchanged ionic cross-linking material, and part of E-wife-acetate copolymer can be used. Completely compounded, partially/completely structured of polyvinyl acetate vinegar, cellulose-based derivatives, poly-sweet oxide derivatives, polyester, polyamine, and the like. Among the above-mentioned desiccant, it is particularly preferable to use minerals from the viewpoints of a large moisture absorption per unit weight, a large moisture absorption force under low humidity, chemical stability, and no toxicity reduction. When the digonal crystal cerium oxide is used in a powder state, the particle diameter may be selected according to the dosage form of the deoxidizing agent of the invention. For example, in the case where the oxygen scavenger of the present invention is contained in a bag-like package having a gas permeation resistance (for example, 1 〇 to touch,), the average particle diameter is obtained from the point of ensuring sufficient specific surface area and ensuring oxygen contact. It should be 〇〇ι ~ι〇〇 (4), especially 133482.doc 200927282 0.0H μπ^. In the case where the epoxy resin of the present invention and the resin composition having oxygen permeability form a film form, the particle diameter of the oxidized crystal is preferably not more than the thickness of the film. From this viewpoint, the average particle diameter of the oxidized decorative material is preferably 0.01 20 μηι, especially 〇〇1 to 1 〇 (4). The average diameter in the present specification is measured by a laser diffraction scattering type particle size distribution measuring apparatus. The deoxidizer of the present invention is an oxygen-removing body by being housed in a bag-like package having an air resistance (for example, air resistance of 1 〇 to 1 〇〇〇〇〇 second). The deoxidized body of the shape is sealed with the packaging material 与, such as a dried food or a lozenge. Examples of the material having air permeability resistance constituting the package include polypropylene, polybutan, polymethylpentene, thermoplastic elastomer, polyethylene terephthalate, and stone retort resin. Dilute-vinyl acetate copolymer, polyisoprene, ultra-low density polyethylene, low-density polyethylene, medium-density polyethylene, propylene-ethylene copolymer, propylene-ethylene random polymer, ethylene· A film made of various thermoplastic resins such as an α-olefin copolymer is subjected to a laminate of a perforator, paper, or nonwoven fabric or a combination thereof. The anti-Φ air permeability here is measured according to JIS Ρ 8117, and indicates the time required for 100 mL of air to completely pass through the area of 〇〇〇 〇〇〇 642 m 2 at a pressure difference of l_23 kPa. The oxygen scavenger of the present invention may be kneaded with a resin having oxygen permeability to constitute a deoxidizing resin composition. The resin composition is used in the form of pellets, for example, as a raw material of various resin molded bodies. Further, the resin composition is used in the form of various resin molded bodies formed in the form of pellets, for example, a film shape 1, or a disk-open state. Regardless of the form of the resin composition, the proportion of the oxygen scavenger in the resin composition is preferably from 1 to 90% by weight, particularly from 2 to 8 % by weight, from the viewpoint of exhibiting a degassing function. . The other party 133482.doc • 2 - 200927282 The ratio of the resin in the resin composition is preferably from 10 to 90% by weight, particularly from 20 to 80, from the viewpoint of maintaining the strength and formability of the resin composition. weight%. ❹ ❹ When the above resin composition is used in the form of a film, the thickness of the film is preferably 00 (four), especially 20 40 μm, depending on the specific use of the film. In the case where the resin composition is in the form of a film, other components which can improve the properties of the resin composition can be added to the resin composition as needed, in addition to the oxygen-removing agent and the oxygen-permeable resin. Examples of the other component include a pigment for coloring the resin composition into a specific color, and a filler for increasing the strength of the resin composition. The film may be used in a single layer state composed of a deoxidizing resin composition as described above. Alternatively, it may be used in a state of having a multilayer structure of an deoxidizing layer composed of the above-described deoxidizing resin composition. In the latter case, the example of the multilayer structure may be exemplified by one side of the deoxidizing layer composed of the above-described deoxidizing resin composition, a gas barrier layer having a gas barrier property, and another side of the deoxidizing layer. An oxygen permeation layer dioxide layer film having oxygen permeability is laminated. The foregoing oxygen-depleting laminate film is used in such a manner that the gas barrier layer is outward (i.e., on the atmospheric side) and the oxygen-permeable layer is inward (i.e., on the side of the atmosphere to be deoxidized). The gas barrier layer 'haves at least oxygen permeability and preferably has barrier properties against moisture. The foregoing deoxidized layered body cavity; one embodiment of the enamel film is shown in FIG. The deoxidized laminate film shown in the figure 1 has a deoxidizing layer 11 composed of the above-described deoxidizing resin composition. It’s time to go to the drawer! The surface of the oxygen layer 1 is provided with a gas barrier layer 12 adjacent to the deoxidizing layer 11. The other side is connected to the other side of the deoxidizing layer, and is provided with an oxygen-permeable layer 13 adjacent to the deoxidizing layer 11 of 133482.doc -13.200927282. Further, the outer side of the gas barrier layer 12 is provided with a protective layer 14 of the gas barrier layer 12 adjacent to the gas barrier layer 12. The material of the gas barrier layer 12 in the deoxidized laminate film 1 shown in FIG. 3 can be coated with a stretched nylon (trade name) or a terephthalic acid using, for example, a foil, a polyethylene glycol, a polyethylene terephthalate. Tris- decyl hexamethylenediamine polycondensate formic acid, 2,2-bis(p-aminocyclohexyl)propane-adipate copolymer, ethylene-vinyl alcohol copolymer, polyvinyl chloride, nylon MXD (trade name) ), nylon 6 (trade name), nylon 6,6 (trade name), and the like. The oxygen-permeable layer 13 in the deoxidized laminate film 1 shown in Fig. 3 is a layer which is at least permeable to oxygen. The trioxane type cerium oxide is preferably used in combination with a desiccant. The oxygen permeable layer 13 is preferably a layer which is permeable to oxygen and moisture. As the material of the oxygen-permeable layer 13, for example, non-woven fabric, polyethylene (low density polyethylene, ultra low density polyethylene, etc.), extended polypropylene (PP), polypropylene, ethylene propylene copolymer, ethylene propylene rubber, ethylene can be used. An ethyl acrylate copolymer or the like. As the material of the protective layer 14 in the deoxidized laminate film 1 shown in Fig. 3, for example, polyethylene, polypropylene, polyethylene terephthalate (PET), polyamide or the like can be used. Another embodiment of the deoxidized laminate film is shown in FIG. The laminate film 10' shown in the figure is further laminated on the laminate film shown in Fig. 3 to further increase the thickness of the laminate. Specifically, a buffer layer 15 is provided between the deionized layer and the gas barrier layer 12. Further, a gas barrier layer 16 is provided on the outer side of the gas barrier layer 12, that is, between the gas barrier layer 12 and the protective layer 14. 133482.doc 14 200927282 The deoxidized laminate film 10 shown in Fig. 4, the buffer layer 15 is a layer which buffers the physical impact applied from the outer side of the film 10'. As the material of the buffer layer 15, for example, polyethylene, polypropylene, or the like can be used. ❹
圖4所示之去氧積層體薄膜10,中之高度氣體障壁層16, 係與氣體障壁層12相比,阻隔氧透過之能力更高之層。作 為高度氣體障壁層16之材料,可使用比如以鋁箔為首之各 種金屬箱、以鋁為首之各種金屬之蒸鍍薄膜、各種氧化物 (二氧切、二氧化鈦、氧化錯、氧化銘)之蒸鑛薄膜等。 圖4所示之6層構造之去氧積層體薄膜1〇,,與圖3所示之 去氧積層體薄膜10相比,提升對從薄膜外側所施加之物理 性衝擊的緩衝作用。同時外部氣體之侵入更加困難。因 此14所示之去氧積層體薄膜1〇,,與圖㈣示之去氧積層 體薄膜10相比,附加價值更高。 下面’對本發明之純劑所使用之三方晶型氧化飾之較 佳製造方法進行說明。作為用於製造三方晶型氧化飾之原 :稱中係使用含氧鈽鹽或其水合物(以下,將該等 :稱為含氧飾鹽)。將該含氧鈽鹽在還原氣氛下進行终 燒,稭此可得到目標之三方晶型氧化鈽。 含氧鈽鹽,係由與师„)離子成對之陰離子含氧之 2所構成之鈽⑽化合物。作為含氧之陰離子,可使用 離子、硝酸離子、硫酸離子、氣氧化物離子等 =有該等含氧陰離子之飾化合物,可使用比 二六水合物、八水合物等)、㈣飾,、氮氧 133482.doc 15 200927282 :氧鈽鹽’#由將其在還原氣氛下、比如氫氣中培燒, 可传到三方晶型氧化鈽。該製造方法,因i階段之步驟即 I元成,故生產性極佳。對㈣燒,藉由適#調整其條 ’即可控制晶格中之氧缺陷之程度。作為錢條件比 如中進行2小時以上之料,可得到具有所希望之 乳:收量之三方晶型氧化鈽。1050t中則只fH、時以上 ❹The high-gas barrier layer 16 of the deoxidized laminate film 10 shown in Fig. 4 is a layer having a higher ability to block oxygen permeation than the gas barrier layer 12. As the material of the high gas barrier layer 16, various metal tanks such as aluminum foil, vapor-deposited films of various metals including aluminum, and various types of oxides (diox, titanium dioxide, oxidation, oxidation) can be used. Film and the like. The six-layer structure deoxidized laminate film 1 shown in Fig. 4 enhances the cushioning effect on the physical impact applied from the outside of the film as compared with the deoxidized laminate film 10 shown in Fig. 3. At the same time, the invasion of external gases is more difficult. Therefore, the deoxidized laminate film 1 shown in Fig. 14 has a higher added value than the deoxidized laminate film 10 shown in Fig. 4 . The following is a description of a preferred method for producing a trigonal crystal oxide used in the pure agent of the present invention. As a raw material for producing a trigonal crystal oxide: In the middle, an oxonium salt or a hydrate thereof is used (hereinafter, these are referred to as oxygen-containing salts). The oxonium salt is finally calcined under a reducing atmosphere to obtain a target trigonal cerium oxide. The oxonium salt is a compound of ruthenium (10) composed of an anion containing oxygen paired with the „) ion. As an anion containing oxygen, ions, nitrate ions, sulfate ions, gas oxide ions, etc. can be used. The oxyanion-containing compound can be used in a reducing atmosphere, such as hydrogen, using a ratio of dihexahydrate, octahydrate, etc., (iv), and nitrogen oxide 133482.doc 15 200927282: oxonium salt. In the middle of the burning, it can be transferred to the trigonal crystal yttrium oxide. The manufacturing method is excellent in productivity because the step of the i phase is I. Therefore, the (4) is burned, and the lattice can be controlled by adjusting the strip. The degree of oxygen deficiency in the middle. As a money condition, for example, a material having a desired amount of milk: a trigonal crystal of cerium oxide having a desired amount of milk is obtained. In the case of 1050 t, only fH or more is used.
燒可如此藉由提尚焙燒溫度而使焙燒時間縮短。不 過’提高培燒溫度’比如超過105(rc時,則作為培燒用之 爐之爐心管有必要使用氧化鋁等陶瓷系材料,因無法謂之 有利。使用陶瓷系材料之爐心管,在安全性及成本上都有 困難。相反地’即使進行在1050。〇以下之低溫培燒亦可得 到所希望之三方晶型氧化鈽之點,可說是本製造方法之優 點。在1050 C以下之焙燒,作為爐心管可使用安全且較便 宜之材料即不銹鋼製者。從進行1〇5〇它以下之低溫焙燒可 擴大所得之二方晶型氧化鈽之比表面積之點來看,亦為有 利。因比表面積越大,與氧之接觸面積越大,氧吸收速度 就越高。作為還原氣氛之具體例,使用氫氣氣氛之情形, 氣氛中之氫濃度宜為4體積%以上,尤其為8〇體積%以上。 使用一氧化碳氣氛之情形,氣氛中之一氧化碳濃度宜為4 體積%以上,尤其為80體積。/。以上。使用乙炔氣氛之情 形’氣氛中之乙炔濃度宜為2體積。/。以上,尤其為7〇體積0/。 以上。 於三方晶型氧化鈽中添加使氧吸收量增大之元素、使之 置換固溶之情形’將含氧鈽鹽與該元素之化合物(比如氧 133482.doc -16- 200927282 化物)混合,將該混合物 代替前述!階段之Μ ^還原培燒即可。 石型氧化鈽,再將:過先從含氧錦鹽暫且生成螢 三方晶型氧切。要rmrr錢步驟亦可得到 二= ㈣下培燒即可。作為培燒條件,比如以·C 培燒1小時以上即可。膝 屌 將由該燒得到之螢石型氧化鈽還 1階。燒’得到三方晶型氧化鈽。還原培燒之條件,比前述 焙燒方法之情形更為嚴格。具體而言,在氫濃产 宜為50體積%以上,士、甘法 牡風/辰度 ^ 尤其為90體積%以上之氫氣氣氛中進 仃比如120〇t 1小時以μ +地法 , 之纟。燒。即,在比前述1階段之焙 /之情形更焉溫之條件下進行還原培燒。由 可得到所要之三方晶型氧化飾。 魔 ❹ 含有由以上各方法所得之三方晶型氧化鈽之本發明之去 氧劑’比如將其置於氣氛中,吸收氣氛令之氧。因此,將 該去氧劑與食品等製品一同密封收容於包裝袋中,藉此可 二去包裝袋内之氧,可保持食品之鮮度等。此處所言之氣 氛係才曰保存例如食品、電子零件、醫藥品等商品時之一 般陡的生活環境氣氛。以石化燃料驅動之動力用引擎所排 出二氣等高溫及/或高壓之嚴酷氣氛,不包含於該生活 環兄氣氛中。關於生活環境氣氛之氣壓,包含從比如商品 包裝之減壓狀態(真空包裝等)至加壓狀態(殺菌處理之加壓 加熱殺菌或包装體之形狀維持用等)。關於溫度,包含從 50C(冷凍保存時)至18〇。(:(食品之殺菌處理)左右。另, 氣氛並不一定為空氣,亦可於氮氣等惰性氣體中進行沖 133482.doc 200927282 洗’使氧濃度下降β 另,將含有三方晶型氧化鈽之本發明之去氧劑投入以水 或水/谷液為首之液體中,可吸收液體中之溶存氧。 另,將含有三方晶型氧化鈽之本發明之去氧劑與大氣接 - 觸,可減少大氣中之氧濃度,藉此可得到高純度氮氣。具 • 豸而言,使用圖5所示之裝置,可得到高純度氮氣。該圖 所示之裝置20,具備壓縮大氣21之壓縮機22、除去大氣21 中之塵埃之過濾器23、中空線膜24、及去氧裝置28。中空 線膜24,係將使壓縮空氣中之氮成分與氧成分分離之中空 線成束捆扎而成。去氧裝置28,係將中空線臈24所分離出 之氮成分中所含微量氧除去之裝置。去氧裝置28中,填充 有本發明之去氧劑。 貯藏於壓縮機22之空氣槽中之壓縮空氣,藉由壓縮空氣 配管經由將壓縮空氣内之異物除去之預過濾器及微粒過濾 器等過濾器23,送入中空線膜。壓縮機22與過濾器23之 φ 間,亦可配設將壓縮空氣乾燥之乾燥機等乾燥機構。預過 濾器與微粒過濾器併用之情形,預過濾器宜除去壓縮空氣 内所存在之3 μ以上之大異物,微粒過濾器宜除去壓縮空 乳内所存在之0.01 μ以上之小異物。於微粒過濾器之下 •游,亦可配設具有除去壓縮空氣内之臭味之能力之活性碳 過濾器。 中空線膜24係聚酯製或聚烯烴製,由數千吸管狀之中空 線成束捆扎構成。藉由使壓縮空氣通過中空線之内部利 用各種氣體所固有之透過中空線膜速度之不同,使空氣中 133482.doc 18 200927282 含量最多之氮氣殘存。構成壓縮空氣之氣體透過中空線膜 之速度77為較快釋出之氣體與較慢釋出之氣體,殘存 氣體即為氮氣。特別是,中空線膜為以旨製之情形,水蒸 氣最易透過’緊跟其後為氫與氦,然後為-氧化碳,最後 為氧、風與氮最不易透過,#中作為最難透過之氣體之氣 被殘留。The calcination can be shortened by raising the calcination temperature. However, if the 'increasing the boiling temperature' is more than 105 (for rc, it is necessary to use a ceramic material such as alumina as the core tube of the furnace for cooking, which is not advantageous because of the use of the core material of the ceramic material. There are difficulties in safety and cost. Conversely, even if it is carried out at a low temperature of 1050 〇 below, the desired trigonal cerium oxide can be obtained, which is the advantage of this manufacturing method. At 1050 C In the following calcination, a stainless steel which is a safe and inexpensive material can be used as the core tube. From the point of performing the low-temperature calcination below 1〇5〇, the specific surface area of the obtained digonal crystal yttrium oxide can be enlarged. It is also advantageous. The larger the specific surface area, the larger the contact area with oxygen, and the higher the oxygen absorption rate. As a specific example of the reducing atmosphere, the hydrogen concentration in the atmosphere is preferably 4% by volume or more. In particular, in the case of a carbon monoxide atmosphere, the concentration of one of the carbon oxides in the atmosphere is preferably 4% by volume or more, especially 80% by volume or more. The concentration of acetylene in the medium is preferably 2 vol. / or more, especially 7 〇 volume 0 /. or more. Adding an element which increases the oxygen absorption amount to the trigonal cerium oxide, and replacing it with solid solution 'will contain The oxonium salt is mixed with a compound of the element (such as oxygen 133482.doc -16-200927282), and the mixture is replaced by the above-mentioned ! ^ reduction peening. Stone type cerium oxide, and then: Oxygen salt temporarily produces a trigonal crystal oxygen cut. To rmrr money step can also get two = (four) lower can be burned. As a burning condition, for example, it can be burned for more than 1 hour in C. The knee will be burned. The obtained fluorite-type cerium oxide is also in the first order. The crystallization of the fluorite-type cerium oxide is obtained. The conditions of the reduction sinter are more stringent than those of the above-mentioned baking method. Specifically, the concentration of hydrogen is preferably 50% by volume or more. ,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,, In the case of more temperate conditions, the reduction is carried out. Trigonal crystal oxide decoration. Konjac The oxygen scavenger of the present invention containing the trigonal crystal cerium oxide obtained by the above methods, such as placing it in an atmosphere, absorbing the atmosphere to make oxygen. Therefore, the deoxidizing agent is Products such as foods are sealed and contained in a packaging bag, so that the oxygen in the packaging bag can be removed, and the freshness of the food can be maintained. The atmosphere described here is such that foods, electronic parts, pharmaceuticals, and the like are stored. The atmosphere of the living environment is high. The reduced pressure state of the package (vacuum packaging, etc.) to the pressurized state (pressure sterilization of the sterilization treatment, shape maintenance of the package, etc.). Regarding the temperature, it ranges from 50C (when frozen) to 18〇. (: (sterilization of food)). In addition, the atmosphere is not necessarily air, and it can also be washed in an inert gas such as nitrogen. 133482.doc 200927282 Washing 'The oxygen concentration is decreased β. In addition, it will contain trigonal cerium oxide. The oxygen scavenger of the present invention is introduced into a liquid such as water or water/glutle solution, and can absorb dissolved oxygen in the liquid. Further, the oxygen scavenger of the present invention containing the trigonal cerium oxide can be contacted with the atmosphere. By reducing the concentration of oxygen in the atmosphere, high-purity nitrogen gas can be obtained. In the case of 豸, high-purity nitrogen gas can be obtained by using the apparatus shown in Fig. 5. The apparatus 20 shown in the figure has a compressor that compresses the atmosphere 21 22. The filter 23, the hollow wire film 24, and the deoxidizing device 28 for removing dust in the atmosphere 21. The hollow wire film 24 is formed by bundling hollow wires separating the nitrogen component and the oxygen component in the compressed air. The deaerator 28 is a device for removing a trace amount of oxygen contained in the nitrogen component separated by the hollow coil 24. The deoxidizing device 28 is filled with the oxygen scavenger of the present invention. Compressed air in, by compression The air pipe is sent to the hollow fiber membrane through a filter 23 such as a pre-filter and a particulate filter that removes foreign matter in the compressed air. Between φ of the compressor 22 and the filter 23, drying of the compressed air may be provided. Drying mechanism such as machine. When the pre-filter is used together with the particulate filter, the pre-filter should remove more than 3 μ of the foreign matter present in the compressed air. The particulate filter should remove 0.01 μ or more of the compressed empty milk. Small foreign matter. Under the particulate filter, it can also be equipped with an activated carbon filter with the ability to remove the odor in compressed air. Hollow wire film 24 is made of polyester or polyolefin, and is made up of thousands of suction tubes. The hollow wires are bundled and bundled, and the compressed air is passed through the inside of the hollow wire to utilize the difference in the speed of the hollow film passing through the various gases, so that the nitrogen in the air has the highest content of 133482.doc 18 200927282. The velocity 77 of the gas passing through the hollow wire membrane is a relatively quick release gas and a relatively slow release gas, and the residual gas is nitrogen. In particular, the hollow wire film is intended to be designed. , Most easily through water vapor 'immediately followed by hydrogen and helium, is then - carbon monoxide, oxygen and finally, the most easily through air and nitrogen, are used as the residual gas of the gas through the hardest in #.
壓縮空氣藉由通過中空線膜24而殘存之氮氣,經由氣體 配管後到達分歧部25。從該分歧部25分歧成二個配管系 統’其中-配管系統具有氮氣第】分歧管li與第^閉間 26另配s系統具有氮氣第2分歧管L2。於該第2分歧管 L2依次介裝有第2開閉閥27、去氧裝置28及氧滚度計3〇。 藉由打開第1開閉閥26,關閉第2開閉閥27,將達到約 95%〜".9%純度之氮從第1分歧管L1中釋出。藉由關閉糾 開閉閥26’打開第2開閉閥27,將達到約95%〜99·9%純度 之氮導入至去氧裝置28。然後,於去氧裝置28進而除: 氧’得到約99.9%以上高純度之氮氣。高純度氮氣之純度 由氧濃度計30監測。 本發明並不局限於前述實施形態。比如以前述之各方法 製造之三方晶型氧化鈽,根據還原焙燒之條件的不同,存 在由XRD測定可微弱觀㈣螢石型氧化鈽之繞科之: 形。即,有螢石型氧化㈣量混人三方晶型氧化飾之^ 形。但如此之微量#石型氧化鈽包含於三方晶型氧化 係為本發明所容許。 Τ [實施例] 133482.doc • 19- 200927282 以下,通過實施例對本發明進行進一步詳細說明。但本 發明之範圍並不局限於該實施例。 [實施例1] 將75 g碳酸氫敍溶解於5〇〇 ml水中,調製水溶液。邊授 拌該水溶液’邊滴下〇·1 Μ之硝酸鈽水溶液5〇〇 ml,進行 逆中和。將所生成之沈澱物用離子交換水進行2次洗淨過 濾,得到碳酸鈽八水合物。The compressed air passes through the gas pipe and reaches the branching portion 25 by the nitrogen gas remaining through the hollow wire film 24. From the branching portion 25, the two piping systems are divided into two. The piping system has a nitrogen gas. The branching pipe li and the second closing pipe 26 are provided with a nitrogen gas second branch pipe L2. The second opening and closing valve 27, the deaerator 28, and the oxygen ampometer 3 are sequentially placed in the second branch pipe L2. By opening the first opening and closing valve 26, the second opening and closing valve 27 is closed, and nitrogen having a purity of about 95% to < 9% is released from the first branch pipe L1. The second opening and closing valve 27 is opened by closing the closing valve 26', and nitrogen having a purity of about 95% to 99.9% is introduced into the deaerator 28. Then, in the deoxygenation unit 28, in addition to: oxygen, a high purity nitrogen gas of about 99.9% or more is obtained. The purity of the high purity nitrogen gas is monitored by an oxygen concentration meter 30. The present invention is not limited to the foregoing embodiment. For example, the trigonal cerium oxide produced by the above various methods has a weak view of the fluorite-type cerium oxide according to the conditions of the reduction calcination: (4). That is, there is a fluorite-type oxidized (four) amount mixed with a trigonal crystal oxide. However, such a trace amount of #石型钸 is contained in the trigonal form of oxidation as permitted by the present invention.实施 [Embodiment] 133482.doc • 19-200927282 Hereinafter, the present invention will be described in further detail by way of examples. However, the scope of the invention is not limited to the embodiment. [Example 1] 75 g of hydrogencarbonate was dissolved in 5 ml of water to prepare an aqueous solution. While admixing the aqueous solution, 5 〇〇 ml of a cerium nitrate aqueous solution of 〇·1 滴 was dropped to carry out reverse neutralization. The resulting precipitate was washed twice with ion-exchanged water to obtain cesium carbonate octahydrate.
將所得到之碳酸鈽八水合物8 1 · 5 7 g與後酸約3 g混合。 將該混合物進行還原處理(氫1〇〇%氣體下4〇〇 SCCM流 量)。處理溫度為l00(rc,處理時間為2小時。如此得到具 有三方晶型之結晶構造,且固溶妈,並以“〜表示之氧 化鈽。結晶構造由XRD測定決定。氧含量由後述氧吸收量 之測定逆算求得。三方晶型氧化铈之平均粒徑為2㈣。三 方:里氧化鈽中Ca含量係相對Ce原子為1〇 所得到 之三方晶型氧化鈽之SEM像如圖6所示。 [實施例2] 除作為還原培燒之條件,採用⑻代、工小時之條件以 ::與實施例1同樣而得到具有三方晶型之結晶構 ^ 以Ce2〇2.7表示之氣斗姑 D 乳化飾。三方晶型氧化鈽之平均粒徑 為 2 μιη。 [實施例3] 以實施例1所得到 ^ m u , 酸鈽八水合物與碳酸鈣之混合物 馮原料,將該混合物 時),得到固溶舞之乳下進行加熱處理(_°C、1小 錦。將該氧化鈽進行還原焙燒(氫 133482.doc -20- 200927282 100%氣體下400 SCCM流量 ,窗 一 1200 C、1小時)’得到具右 二方晶型之結晶構造、以c 〇 、The obtained cesium carbonate octahydrate 8 1 · 5 7 g was mixed with about 3 g of post-acid. The mixture was subjected to a reduction treatment (4 〇〇 SCCM flow under hydrogen 1% by gas). The treatment temperature is l00 (rc, the treatment time is 2 hours. Thus, a crystal structure having a trigonal crystal form is obtained, and the solid solution is used, and the yttrium oxide represented by "~" is determined. The crystal structure is determined by XRD measurement. The oxygen content is determined by oxygen absorption described later. The measurement of the amount is obtained by inverse calculation. The average particle size of the trigonal cerium oxide is 2 (four). The SEM image of the trigonal cerium oxide obtained by the three-party cerium oxide in the cerium oxide is 1 相对. [Example 2] In the same manner as in Example 1, except that the conditions of (8) generation and working hours were used, a crystal structure having a trigonal crystal form was obtained, and a gas cylinder represented by Ce2〇2.7 was obtained. The emulsion has a mean particle diameter of 2 μηη. [Example 3] The compound obtained in Example 1 is obtained by the mixture of the acid yttrium octahydrate and the calcium carbonate, and the mixture is obtained. Heat treatment under the emulsion of solid solution dance (_°C, 1 small brocade. The cerium oxide is reduced and calcined (hydrogen 133482.doc -20- 200927282 400 SCCM flow under 100% gas, window 1200 C, 1 hour) Obtaining a crystal structure having a right two-sided crystal form, 〇 ,
氧化鈽之平均粒徑為2〇μιη。 晶IThe average particle size of cerium oxide is 2 〇 μιη. Crystal I
[實施例4] 外除=原培燒之條件,採用幫、1小時之條件以 i餘與實施例3同樣而得到具有三方晶型之結㈣ 2以Ce2〇27表示之氧化铈。三方晶型氧化飾之平均粒徑 :”㈣所传到之三方晶型氧化鈽之sem像如圖7所 [比較例1] 以實施例1所得到之碳酸鈽為原料,將其在大氣下進行 …處理(6GG C、1小時)’得到氧化飾。將該氧化飾進行 還原培燒(氫職氣體下彻SCCM流量、1GG(rc、H、 時),得到具有螢石型之結晶構造、以CeOh66表示之氧化 飾°所得到之氧化鈽之平均粒徑為2μηι。 [評價1(氧吸收量)] ❹ 對實施例及比較例所得之氧化飾測定氧吸收量。其結 果’各實施例所得之氧化鈽之氧吸收量均為45,,相對 於此,比較例所得之氧化鈽之氧吸收量為34祕名。由該結 果可知,各實施例所得之三方晶型氧化鈽,與比較例所^ 之螢石型氧化鈽相比,氧吸收量格外高。 [評價2(氧吸收速度)] 對實施例所得之氧化㈣定氧吸收速度。其結果如圖8 所P由圖8所示之結果可知’實施例之氧化飾均可長時 間吸收氧。另’亦可知藉由適當調整還原培燒之條件,可 133482.doc •21 · 200927282 控制氧吸收速度。 [產業上之利用可能性][Example 4] Except for the conditions of the original calcination, a ruthenium oxide having a trigonal crystal form (4) 2 and a Ce2〇27 was obtained in the same manner as in Example 3 under the conditions of 1 hour. The average particle diameter of the trigonal crystal oxide: "(4) The sem image of the trigonal cerium oxide transmitted as shown in Fig. 7 [Comparative Example 1] The cerium carbonate obtained in Example 1 was used as a raw material, and it was placed under the atmosphere. The treatment was carried out (6 GG C, 1 hour) to obtain an oxidized decoration. The oxidized decoration was subjected to reduction peening (a flow rate of SCCM and a flow rate of 1GG (rc, H, H) in the hydrogen gas to obtain a crystal structure having a fluorite type. The average particle diameter of the cerium oxide obtained by the oxidation of the composition represented by CeOh66 was 2 μm. [Evaluation 1 (oxygen absorption amount)] 氧 The oxygen absorption amount of the oxidized articles obtained in the examples and the comparative examples was measured. The oxygen absorption amount of the obtained cerium oxide was 45, whereas the oxygen absorption amount of cerium oxide obtained in the comparative example was 34. The results show that the trigonal cerium oxide obtained in each example is compared with In the case of the fluorite-type cerium oxide of the example, the oxygen absorption amount is extremely high. [Evaluation 2 (oxygen absorption rate)] The oxidation (IV) oxygen absorption rate obtained in the examples is as shown in Fig. 8. As a result of the above, it can be seen that the oxidized articles of the examples can absorb oxygen for a long time. 'It is also known by appropriately adjusting the roasting reducing conditions, may be 133482.doc • 21 · 200927282 controlling oxygen absorption rate. [Possibility of industrial use]
如以上所詳述’根據本發明,可提供遠超過具有螢石型 結晶構造之先前氧化鈽之理論限界之具有高氧吸收量之新 型氧化鈽系去氧劑。其氧吸收量,在特定元素添加入氧化 鈽之情形還可進一步增大。另,本發明之去氧劑在金屬探 測機中無反應,將之與食品等一同包裝之製品,易於進行 金屬探測機之金屬等異物之混入檢查。此外,本發明之去 氧劑’不會因微波之照射而起火’故將之與食品等一同包 裝之製品可於微波爐等中安全地加熱。 【圖式簡單說明】 圖1係三方晶型氧化鈽之結晶構造示意圖。 圖2係螢石型氧化鈽之結晶構造示意圖。 圖3係顯示本發明之去氧積層體薄骐之一實施形態之模 式圖。As described in detail above, according to the present invention, a novel cerium oxide-based deoxidizing agent having a high oxygen absorption amount far exceeding the theoretical limit of the prior cerium oxide having a fluorite-type crystal structure can be provided. The amount of oxygen absorption can be further increased in the case where a specific element is added to cerium oxide. Further, the oxygen scavenger of the present invention does not react in the metal detector, and the product which is packaged together with the food or the like is easily subjected to the inspection of foreign matter such as metal of the metal detector. Further, the oxygen-removing agent of the present invention does not ignite due to the irradiation of microwaves, so that the product packaged together with food or the like can be safely heated in a microwave oven or the like. BRIEF DESCRIPTION OF THE DRAWINGS Fig. 1 is a schematic view showing the crystal structure of a trigonal cerium oxide. Fig. 2 is a schematic view showing the crystal structure of fluorite-type cerium oxide. Fig. 3 is a schematic view showing an embodiment of the deoxidized laminate of the present invention.
圖4係顯示本發明之去氧積層體薄膜 模式圖。 之另一實施形態之 圖5係顯示使用本發明之去氧劑之高純 模式圖。 < 圖6係實施例1所得到之三方 ^氧化鈽之SEM像。 圖7係實施例4所得到之三方 ^ , 氣化鈽之SEM像。 圖8係顯不各實施例所得到 = 速度之圖。 二方晶型氧化飾之氧吸收 【主要元件符號說明】 133482.doc -22. 200927282 ίο 10' 11 12 13 14 15 16 ❹ 21 22 23 24 25 26 27 28 ❿ 30 L1 ' L2 去氧積層體薄膜 去氧積層體薄膜 去氧層 氣體障壁層 氧易透過層 保護層 緩衝層 高度氣體障壁層 大氣 壓縮機 過濾器 中空線膜 分歧部 第1開閉閥 第2開閉閥 去氧裝置 氧濃度計 氮氣第1分歧管 氮氣第2分歧管 133482.doc -23-Fig. 4 is a view showing the mode of the deoxidized laminate film of the present invention. Fig. 5 of another embodiment shows a high-purity mode diagram using the oxygen scavenger of the present invention. < Figure 6 is an SEM image of the trigonal cerium oxide obtained in Example 1. Fig. 7 is a SEM image of the trigonal ^, vaporized enthalpy obtained in Example 4. Figure 8 is a graph showing the speed = obtained by the various embodiments. Oxygen absorption of binary crystal oxidation decoration [Main component symbol description] 133482.doc -22. 200927282 ίο 10' 11 12 13 14 15 16 ❹ 21 22 23 24 25 26 27 28 ❿ 30 L1 ' L2 deoxidized laminate film Oxygen buildup film deoxidation layer gas barrier layer oxygen permeation layer protective layer buffer layer height gas barrier layer atmospheric compressor filter hollow line membrane diverging part first opening and closing valve second opening and closing valve deaerator oxygen concentration meter nitrogen first Bifurcated tube nitrogen second branch tube 133482.doc -23-
Claims (1)
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2007203591 | 2007-08-03 |
Publications (2)
Publication Number | Publication Date |
---|---|
TW200927282A true TW200927282A (en) | 2009-07-01 |
TWI372656B TWI372656B (en) | 2012-09-21 |
Family
ID=40341253
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
TW97129427A TW200927282A (en) | 2007-08-03 | 2008-08-01 | Deoxidizer |
Country Status (3)
Country | Link |
---|---|
JP (1) | JP4339395B2 (en) |
TW (1) | TW200927282A (en) |
WO (1) | WO2009020019A1 (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
ES2434825B1 (en) * | 2012-06-11 | 2014-11-07 | Nanobiomatters Research & Development, S.L. | Cerium-based active materials with catalytic capacity and procedure for obtaining |
JP6576787B2 (en) * | 2015-10-20 | 2019-09-18 | 三井金属鉱業株式会社 | Oxygen scavenger and method for producing the same |
JP6876256B2 (en) * | 2017-12-05 | 2021-05-26 | トヨタ自動車株式会社 | Sulfide solid electrolyte secondary battery |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP4248986B2 (en) * | 2003-10-01 | 2009-04-02 | 凸版印刷株式会社 | Oxygen-absorbing laminate, package using the same, and content filling method using the same |
TW200730243A (en) * | 2005-12-15 | 2007-08-16 | Mitsui Mining & Smelting Co | Oxygen scavenger and method for producing the same |
JP5405744B2 (en) * | 2006-06-29 | 2014-02-05 | 三井金属鉱業株式会社 | Dehumidifying and oxygen scavenger |
-
2008
- 2008-07-30 WO PCT/JP2008/063636 patent/WO2009020019A1/en active Application Filing
- 2008-07-30 JP JP2008536234A patent/JP4339395B2/en not_active Expired - Fee Related
- 2008-08-01 TW TW97129427A patent/TW200927282A/en not_active IP Right Cessation
Also Published As
Publication number | Publication date |
---|---|
JPWO2009020019A1 (en) | 2010-11-04 |
JP4339395B2 (en) | 2009-10-07 |
WO2009020019A1 (en) | 2009-02-12 |
TWI372656B (en) | 2012-09-21 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
TWI429482B (en) | Dehumidifying deoxidizer | |
JP4001614B2 (en) | Oxygen scavenger and method for producing the same | |
WO2007069735A1 (en) | Oxygen scavenger and process for producing oxygen scavenger | |
JP4322311B2 (en) | Oxygen scavenger and method for producing oxygen scavenger | |
JP5464436B2 (en) | Oxygen absorbent, oxygen-absorbing resin composition, and oxygen-absorbing film | |
JP6185911B2 (en) | Oxygen generation / carbon dioxide absorbent package and method of transporting live fish and shellfish | |
JPWO2010004963A1 (en) | Oxygen scavenger | |
JPWO2017203912A1 (en) | Oxygen scavenger | |
TW200927282A (en) | Deoxidizer | |
KR20160107294A (en) | Oxygen-absorbing resin composition and oxygen-absorbing film | |
TWI474860B (en) | A dehumidification / deoxidation method, a deoxidizing package having a dehumidifying function, and a deoxidized film or deoxidizing resin composition | |
JP4260218B2 (en) | Oxygen scavenger and method for producing oxygen scavenger | |
CN101330971A (en) | Deoxidant and process for producing deoxidant | |
WO2004035477A1 (en) | Novel titanium oxide of lower order and method for preparation thereof | |
JP6576787B2 (en) | Oxygen scavenger and method for producing the same | |
JPWO2008133057A1 (en) | Production method of deoxidizing resin film | |
JP4185955B2 (en) | Oxygen scavenger and method for producing oxygen scavenger | |
JP2008308624A (en) | Oxygen-absorbing ink composition and laminate and method for producing oxygen-absorbing ink composition | |
JP2008173636A (en) | Oxygen scavenger and method for manufacturing oxygen scavenger | |
JP2020082624A (en) | Gas absorbing film | |
JP2016027939A (en) | Deoxidation agent, deoxidation package, deoxidation resin composition, deoxidation multilayer body, and manufacturing method of deoxidation agent | |
JP2023034210A (en) | Deoxidizer package and existence confirmation method of the same, and deoxidizer composition | |
JP2004010080A (en) | Package of zinc oxide particle |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
MM4A | Annulment or lapse of patent due to non-payment of fees |