TW205572B - - Google Patents

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TW205572B
TW205572B TW081109386A TW81109386A TW205572B TW 205572 B TW205572 B TW 205572B TW 081109386 A TW081109386 A TW 081109386A TW 81109386 A TW81109386 A TW 81109386A TW 205572 B TW205572 B TW 205572B
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Taiwan
Prior art keywords
hydrogen
heat treatment
gas
furnace
pressure
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TW081109386A
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Chinese (zh)
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Mitsubishi Materials Corp
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Priority claimed from JP3339840A external-priority patent/JPH05149498A/en
Priority claimed from JP3337315A external-priority patent/JP2897500B2/en
Priority claimed from JP3347443A external-priority patent/JP2897502B2/en
Priority claimed from JP3347444A external-priority patent/JP2897503B2/en
Priority claimed from JP4004227A external-priority patent/JPH0673512A/en
Application filed by Mitsubishi Materials Corp filed Critical Mitsubishi Materials Corp
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Publication of TW205572B publication Critical patent/TW205572B/zh

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經濟部中央標準局貝工消費合作社印製 A6 Π557Γ_^_ 五、發明説明(3) 本發明係關於金屬材料之熱處理方法及裝置,尤關於 將氫氣吸收於金屬材料中,及將吸收於金p材料中之氬氣 放出,藉此變更金屬材料之組織而進行物理性調整,或金 靥材料之破碎之熱處理裝置。 習用技術中有一種進行金屬材料之物性調整等之方法 T · . . _ (例如將稀土類(R)-Fe-B条列合金之結晶粒予以細徹化而 提高其磁特性,或將Ti条列合金之組織予以粗大化而改善 疲勞強度及蠕變(creep)特性),該方法像在其一處理溫度 下將氫氣吸收於金屬材料後,再度放出該氫氣,藉此變更 金屬組織。圖1表示習用技術中之熱處理裝置。 圔1之熱處理裝置101中具有:收容金屬材料W並且將 該金屬材料W加熱至特定之處理溫度之熱處理爐102 ;經由 供氣通路103連結於該熱處理爐102並且儲存反應用氫氣之 氫氣銷瓶104;連結於熱處理爐102而吸引該熱處理爐102 内之氣體並且將之排出之排氣裝置105;及將被排出之氣 體燃燒處理而排出於大氣中之排氣處理裝置106。 該熱處理装置101在將金屬材料W搬入該熱處理爐102 内進行真空處理後,從氫氣銷瓶104中供給氫氣於熱處理 瀘102内,並且將熱處理爐102内之溫度保持於500¾〜 1000C,藉此將金屬材料W在氫氣之周圍環境内加熱至特 定溫度使其吸收氫氣,然後將熱處理爐102内之溫度保持 於該溫度,將熱處理爐102内之壓力降低至真空狀態,藉 此使金屬材料W將其吸收之氫氣放出。 從金屬材料W放出之氫氣經由排氣裝置105排氣,並且 本紙張尺度適用中國國家標準(CNS)甲4規格(210 X 297公釐) 3 〃請先閲讀背面之注意事項再填寫本頁)A6 Π557Γ _ ^ _ printed by Beigong Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs 5. Description of the invention (3) The present invention relates to a method and device for heat treatment of metal materials, in particular, to absorb hydrogen in metal materials and absorb gold. The argon gas in the material is released to change the structure of the metal material for physical adjustment, or a heat treatment device for the crushing of the gold material. There is a method for adjusting the physical properties of metal materials, etc. in the conventional technology. T _ (for example, the crystal grains of the rare earth (R) -Fe-B alloys are refined to improve their magnetic properties, or Ti The structure of the bar alloy is coarsened to improve fatigue strength and creep characteristics). This method is like absorbing hydrogen gas to a metal material at one of its processing temperatures and releasing the hydrogen gas again, thereby changing the metal structure. Fig. 1 shows a conventional heat treatment device. The heat treatment device 101 of No. 1 includes: a heat treatment furnace 102 that contains a metal material W and heats the metal material W to a specific processing temperature; a hydrogen pin bottle that is connected to the heat treatment furnace 102 via a gas supply path 103 and stores hydrogen for reaction 104; an exhaust device 105 connected to the heat treatment furnace 102 to attract the gas in the heat treatment furnace 102 and discharge it; and an exhaust treatment device 106 that burns the exhausted gas and discharges it into the atmosphere. After the metal material W is carried into the heat treatment furnace 102 for vacuum treatment, the heat treatment device 101 supplies hydrogen from the hydrogen pin 104 to the heat treatment lub 102, and maintains the temperature in the heat treatment furnace 102 at 500¾ ~ 1000C, thereby The metal material W is heated to a specific temperature in the surrounding environment of hydrogen to absorb hydrogen, and then the temperature in the heat treatment furnace 102 is maintained at this temperature, and the pressure in the heat treatment furnace 102 is reduced to a vacuum state, thereby making the metal material W Release the absorbed hydrogen. The hydrogen gas emitted from the metal material W is exhausted through the exhaust device 105, and this paper standard is applicable to the Chinese National Standard (CNS) A 4 specifications (210 X 297 mm) 3 〃 Please read the precautions on the back before filling this page)

A 裝. 訂. A6 B6 205572 五、發明説明(4 ) 在後段之排氣處理裝置106中燃燒後,被排出於裝置外。 該習用技術中,金屬材料之熱處理時便用之氫氣從氫 氣鋼瓶104供給於熱處理爐102後,經由排氣處理裝置106 排出於大氣中,故於每一次進行處理製程時必須重新供給 氫氣,結果氫氣消耗量變成非常大,而且為了儲存氫氣, 必須使用大容量氫氣鋼瓶1 0 4。 f上述問題之解決方法有例如將熱處理壚1 0 2排出之氫 氣送回供給側之氫氣鏑瓶104中之方式。 然而,這種方式仍然需要使用液化處理設備將氣化之 氫氣回復成液體,結果整値熱處理裝置變成大型化,處理 設備之設置成本提高,並非有效之解決方法。尤其在利用 許多熱處理爐進行熱處理時,必須在各熱處理爐上裝設氫 氣供給条統,結果使設備變成更大型化。 另外,將一度使用給熱處理之氫氣再度使用時,在熱 處理爐中進行處理時可能混入不纯物,對再度使用同時被 熱處理之金靥材料之待性發生不良影響。 本發明之主要目的為提供一種可解決上述習用技術之 問題之金屬材料之熱處理方法。 本發明之另一目的為提供一種可實施該熱處理方法之 裝置。 依照本發明之第1觀點,可提供一種金靥材料之熱處 理方法,該方法包括以下製程:將氫氣吸收於金屬材料之 氫氣吸收處理及從吸收氫氣之金靥材料中放出氫氣之氫氣 放出處理;及將金屬材料放出之·氫氣回收並將回收之氫氣 本紙張尺度適用中國國家標準(CNS)甲4規格(210 X 297公釐) --,-------------( 裝------訂^1·4 V請先閲讀背面之注意事項再塡寫本頁) 經濟部中央標準局貝工消費合作社印製 205572 A6 B6 _ 五、發明説明(5) 再度供給於該氫氣吸收放出製程中之氫氣回收製程。 在氫氣回收製程中,亦可將氫氣儲存'於氫氣吸收合金 中而且將儲存之氫氣放出;亦可反覆的進行包括將氫氣吸 收於金靥材料之氫氣吸收處理及從吸收氫氣之金属材料中 放出氫氣之氫氣放出處理之氫氣吸收放出製程。 在進行氬氣處理時,因為氫氣之吸收量與脱氫量大致 上為相等量,被回收之氫氣量與下次蓮轉時之氫氣量大致 相等,故幾乎不必重新供給氫氣,卽使因氫氣洩漏而有消 失,其消失量非常激小,只要補充該消失之氫氣量即可。 依照本發明之第2觀點,可提供一種金屬材料之熱處 理裝置,該裝置中包括:用來進行將氫氣吸收於金靥材料 中之氫氣吸收處理,及從吸收氫氣之金屬材料中放出氫氣 之氫氣放出處理之熱處理壚;及附設在熱處理爐上,用來 回收從熱處理爐中放出之氫氣並且將該氫氣再度供給於熱 處理爐之氫氣回收裝置。 該氫氣回收裝置亦可由氫氣吸收合金製成之氫氣儲存 裝置構成,亦可由用來進行將氫氣吸收於金屬材料中之氫 氣吸收處理,及從吸收氫氣之金屬材料中放出氫氣之氫氣 放出處理之第2熱處理爐構成。 氫氣吸收合金製儲存裝置可使用例如曰本特開昭55-126198號或美國專利第4270360號中掲示之氫氣吸收合金 儲存裝置。該裝置係由相距一定間隔平行的固定在密閉容 器内之2片多孔板,及設在該等2片多孔板外側分別與各多 孔板相距一間隔之加熱冷却部所構成,而在形成於多孔板 本紙張尺度適用中國國家標準(CNS)甲4規恪(210 X 297公坌) V請先閲讀背面之注意事項再塡寫本頁) 丨裝- 訂 年 經濟部中央標準局員工消費合作社印5衣 205572 a6 Ββ 五、發明説明(6) 存 , 儲後 。却 者冷 成或 而熱 金加 合部 存却 儲冷 氣熱 氫加 充將 填在 内氣 間氫 空之 之中 。 間金收 部合吸 却存被 冷儲或 熱氣出 加一氫¾ 與j於被 熱部爐 在内理 可及處 如力熱 例壓節 , 部諝 進内號 改其信 並測測 施檢檢 實來之 更用器 變置測 可設感 置上該 裝置據 理裝根 處存及 熱儲 , 之氣器 明氫測 發及感 本爐之 理度 處溫 之制 爐控 理之 處出 熱排 合爐 配理 此處 藉熱 , 從 度及 溫爐 或理 力處 壓熱 部於 内給 之供 置氣 裝氫 存將 儲 態 氣狀 。 氫理置 及處裝 氣力於 氬壓持 將之保 行制度 進控溫 在置之 正裝内 爐制置 理控裝 處由存 熱用儲 當利氣 , , 氫 中時將 置程置 裝製裝 之之制 構中控 結料度 種材溫 這屬及 有金置 具於裝 收制 吸控 溫成之 之構出 内使放 爐可氣 理 ,氫 處此之 熱如收 將 。吸 時力其 同壓將 , 定生 力待發 壓成金 定 壓 合 特加收 成且吸 壓而氣 減度氫 且溫之 並定置 ,持裝 度於存 溫持儲 定保氣 待度;氫 之被 中次 料依。 材氣理 屬氫處 金之收 於出吸 收放氣 吸中氬 氣置之 氫裝料 將存材 生儲 靥 發氣金 内氫行 燫從進 理當 , 處 ,後 熱後爐 在然理 且 。處 並象熱 , 現至 象收送 現吸輸 /請先閲讀背面之注意事項再填寫本頁) 經濟部中央標準局貝工消費合作社印製 之制 氣控 氫度 出溫 放及 中置 料裝 材制 屬控 金力 從壓 行之 進制 在控 爐置 理裝 處制 熱控 當 由 , 用 面利 方 , 一 時 程 製 定且 特而 成度 壓溫 減定 且待 並於 度持 溫保 定度 待溫 於之 持内 保置 度裝 溫存 之儲 内氣 爐氫 理將 處時 熱同 將 , 置力 裝壓 中 合 料收 材吸 屬氣 金氳 從之 生置 發装 内存 爐儲 理氣 處氫 熱在 在且 , 而 此 , 如.象 〇 現 力出 壓放 定之 待氣 成氫 壓出 加放 本紙張尺尽適用中國國家標準(CNS)甲4規格(210 X 297公釐) a6 B6 五、發明説明(7) 經濟部中央標準局員工消費合作社印製 I —--------------^--------裝------訂-----1.4------------------------ V諸先閲讀背面之注意事項再塡寫本頁) 被收間 之爐 裝給壓氣之從 設通並之 當吸至該吸 氣吸之 出理氣供之氫置或 可連 ,置 但氣通於氣 氫金爐 放處排之力及裝爐 亦相路裝 .,氫連給氫 之合理 中熱空爐壓爐氣理 ,互通存 理之置供行 出收處 爐將真理氣理排處 中置連儲 處用裝氣進 放吸熱 理置之處氫處空熱 置裝多氣 熱使存氫中 中氣與 處設中熱之熱真於 裝存許氫 行時儲將燫 料,_氣置 熱 ,置於中節節給 理儲之於 進理氣置理 材被裝 從上裝給爐調諏供 處氣路通 序處氫裝處 属次存 將路存供理但又制 熱氫迴連 順將將制熱 金依儲 於通儲置處不 ,控 之與閉的 之而置控個 從氣氣 可氣氣裝熱置度態 置爐用性 同理装述一 當氫氫 亦排氫存於裝溫狀 裝理通擇 相處換上另 。該在 ,之至儲給制部理 存處流選 述出轉用該 象 ,可 中置送氣供控内處 儲熱氣一 上放 ,利在 現後氣 置裝輸氫節述或之 。氣各氫之 照氣後且時 收置氫 裝存之從諝上力壚氣氫將成中 依氬中而同 吸裝, 理儲將氣來用壓理氫有 ,形路 亦成置 ,, 之存此 處氣而氫用利部處之具爐置通 中完裝中爐 氣儲如 熱氫引將置 ,内熱出在理設連 置爐存爐理 氫氣 。 述至吸在設置之合排 ,處間多 。裝理儲理處 生氫收 上送體且 ,裝置配爐外熱中許.置種處氣處熱 。 發至回。在輸氣並上節裝,理此多其等裝此熱氫熱値理 中送被環 氣之 ,路諝存作處 許在該換 値於他一處 金輸而循 氫内置通力儲動熱 置 ,將轉 一.收一其1:力收 本紙張尺度適用中國國家標準(CNS)甲4规格(210 X 297公釐) 7 205572 A6 B6 五、發明説明(8) 經濟部中央標準局員工消费合作社印製 v請先閲讀背面之注意事項再塡寫本頁) 態處的 t、 上中熱之内熱藉及 路氣爐輸置一因 t 丨力 熱 發各 狀熱行^路置各中及節 ,爐 通氫理置裝,。 Λ、、 壓 結多平 通裝於爐力調作理 氣之處裝製除S5置 連許爐 ί 氣存給理壓置動處 排内熱製精去 t、 了設 将 .熱可 之於理 £ 排儲供處部裝之熱 在路將精氣物卩途 間給處 之氣中熱内制置各 可通可氣氫純 W "中 爐供熱 h 中氫置各其控裝於 亦氣 ,氫過:不料?,路 . 亦 時 理氣多 / 置入裝於定以氣給 ,排構由通之材 ί 通 , 置 處氫許 „ 裝送存給測,排供 中於结經在ί 中屬 I 連 中 装 熱將使 存之儲供來號空氣 置通種作氣體金 纟之 多置可 h 儲將氣節用信真氫 裝流這動氫一氣對 1 路 許裝.且 氣而氫調據測及將 述將於之當一之其 氣迴 與存而Ϊ5氫體從來根檢度態 上置由置 ,氣止 彳閉 睡 氫 置儲, 至氣氣用,之溫狀 之設 α 裝此氫防 成用 裝氣出S3送之氫置置生之理 置側置氣因括可 —通 處 構 存氫排 i、 輸内將設裝産置處 裝游裝排。包, Ϊ 流 儲個爐 Μ 氣爐在上節所裝之 氣下製空中或時 I 氣 氣一理 t 氫理 ,通諝器存 Μ 排之精真置中氣 —氫 多 處 氣用處 之處置給力測儲理 。空置氣着裝氣氫 熱成 將利熱0出熱裝供壓感氣處出真裝氫隨存氫用 。2,形 有 ,可從 Μ 放各氣之之各氫熱排有氣之氣儲將使響第間 此即且 i 中引排中力之及各爐具排製氫氣可度影以爐 如 ,並 。Λ ί爐吸空爐壓度爐合處在空精之氫 ,再良若理 換爐轉Β理置真理氣溫理配熱 真以出至時於不 處 轉理蓮 處設之處氫部處此從 之予放送中此.生 熱 本紙張尺度適用中國國家標準(CNS)甲4規格(210 X 297公釐〉 8 205572 A6 B6 經濟部中丧標準局員工消費合作社印製 五、發明説明(9) 控制裝置,以便在各熱處理爐中進行氫氣吸收處理時將其 内部壓力昇壓並供給氫氣,而在各熱處理爐中進行氫氣放 出處理時將其内部壓力減壓並且排出氫氣。 這種结構之熱處理裝置中,若其中之一値熱處理嫌正 在進行將氫氣吸收於金屬材料中之製程時,該熱處理爐被 加熱至待定溫度後,由壓力控制裝置將氫氣供給於其内部 ,而且將内部壓力昇高至持定壓力,藉此在熱處理爐内發 生金屬材料之氫氣吸收現象而進行金屬材料之氫氣吸收處 理。當一値熱處理爐完成氫氣吸收處理而將該熱處理燫中 之處理轉換成氫氣放出處理後,由壓力控制裝置將該熱處 理内之氫氣吸收並排出,而且p着氫氣之排出將熱處理燫 内之壓力減壓。結果在熱處理爐内發生從金靥材料中放出 氫氣之放出現象而進行該金屬材料之氫氣放出處理。 一方面,如此在一個熱處理爐中進行氫氣放出處理時 ,經由連通路連結於該熱處理爐中之其他熱處理爐正在平 行於該處理進行將其内部加熱至特定溫度而進行氫氣吸收 處理之準備,在一値熱處理嫌完成氫氣放出處理之時刻或 平行於該處理,由壓力控制裝置將從一値熱處理爐吸引之 氫輸送至其他熱處理瀘中。因此對其他熱處理爐進行内部 壓力之昇壓操作及氫氣之填充操作而在其他熱處理爐中進 行氫氣吸收處理。 如上所述,依照本發明,在各熱處理爐間授受金屬材 料之熱處理時使用之氫氣,可抑制其放出於裝置外,而且 可使用一座熱處理爐所需要之氫氣量g行至少2座上熱處 本紙張尺度適用中國國家標準(CNS)甲4規格(210 X 297公釐) 〇 :請先閲讀背面之注意事項再埸寫本頁) 丨裝- 訂 r泉_ 205572 A6 B6 經濟部中央標準局負工消費合作杜印製 五、發明説明(10) 理爐之熱處理,不但可減少氫氣使用量,而且可避免裝置 之形狀增大。 亦可將熱處理爐互相連通而在各熱處理嫌間形成成氫 氣流通用閉迴路之連通路中途設置氫氣精製裝置。如此, 則將氫氣從一個熱處理爐送入其他熱處理爐時,可使該氫 氣通過氫氣精製裝置而將清淨之氫氣送入熱處理爐中。 以下參照圖式說明本發明之熱處理法及裝置。 圖2為表示本發明之概念之圔,亦即本發明第1實施例 之熱處理裝置之概略画。圖2中,1為用來進行氫氣處理之 熱處理爐。2為真空排氣裝置。3為濾器。4為氫氣吸收合 金儲存裝置。5, 6, 7為閥。8為管路。此等閥5, 6, 7可 防止被放出之已使用氫氣發生倒流,而且調節氫氣壓力及 流量。 真空排氣裝置2可根據其使用之進行氫氣處理之原料 而省略。圖3表示省略時之概略圖。圖3中,1為用來進行 氫氣處埋之熱處理爐。3為濾器。4為氫氣吸收合金儲存裝 置。5, 6, 7為閥。8為管路。此等閥5, 6, 7可防止被放 出之已使用過之氫氣發生倒流,而且調節氫氣之壓力及流 量。如此省略真空排氣裝置時,可利用與氫氣吸收合金儲 存裝置4之氫氣吸收壓之差進行在熱處理爐1内吸收氫氣之 原料之脱氫。換言之,若氫氣吸收合金儲存裝置4之氫氣 吸收力大於原料之氫氣吸收能力時,可利用氬氣吸收合金 儲存裝置4之氫氣吸收,使熱處理爐1内成為負壓,藉此可 進行熱處理爐1内之原料之脱氫。 本紙張尺度適用中國國家標準(CNS)甲4規格(210 X 297公货) .Λ V請先閲讀背面之注意事項再填寫本頁) 丨裝. .ΤΓ_ :.4. 20557 A6 B6 經濟部中央標準局工消费合作社印製 五、發明説明(11) 圖2及圖3中,將充滿氫氣之氫氣吸收合金儲存裝置4 之氫氣放出,同時開啓閥7將氫氣供給於熱處理爐1,在熱 處理爐1中實施將氫氣吸收於原料中後脱氫之氫氣處理, 將因為脱氫而放出之已使用過之氫氣經由管路8以真空排 氣装置2吸引,或直接以氫氣吸收合金儲存裝置4吸引。 經過脱氫從原料中放出之已使用過之氫氣中混合着從 原料等放出之氧,水分等徹量之不純氣體,灰塵等,故以 濾器3將不純氣髏,灰塵等去除而再度供給於氫氣吸收合 ,—._· — " ---------------------------------- '. 金儲存裝置4中。收存於氫氣吸收合金儲存裝置4内之氫氣 Ά.--. 吸收合金必須具有可充分吸收脱氫氣之容量。 依照習用技術,需要消耗大量之氫氣;但依照上述方 法,因為不必將使用過之氫氣放出於外部,故可有放的再 利用氫氣。即使消耗少童之氫氣,只要適當的補充消耗之 氫氣量即可。如上所述,本發明可有效的利用氫氣,安全 性高,操作亦簡單,其效果極大。 本發明可適用於合金之氫氣處理,但其應用範圍不限 定於合金之氫氣處理,亦可適用於需要使用氫氣之其他各 種熱處理。 以下參照實施例說明本發明之實施例。 [實驗例1 ] 將在電槳電弧(Plasma A「c)溶解爐中溶解縳造之鈸( Nd): 12.5 at% ,銘(Co): 11.6 at% ,硼(B): 6.0 at% ,錯(Zr): 0.1 at% ,鎵(Ga): 0.4 at% ,其餘為鐵(Fe) 所構成之成分組成之合金錠以1130t:之溫度在氬氣周圍環 本紙張尺度適用中國國家標準(CNS)甲4規格(210 X 297公釐) ·, ν請先閲讀背面之注意事項再填寫本頁) .装. .ST. --線-- A6 經濟部中央標準局男工消費合作社印製 B6_ 五、發明説明(1 2) 境中進行20小時之均化處理。 另一方面,如圖2所示,以管路8經由'閥5, 6, 7將熱 處理爐1,真空排氣裝置2,濾器3,及氫吸收合金儲裝置 4等連結,將經過均化處理之合金錠放入熱處理爐1内,將 氫氣吸收合金加熱至7010並從氫氣吸收合金儲存裝置4供 給氫氣而將熱處理瀘1内之壓力保持於1舾氣壓,將經過均 化處理之合金錠之溫度從室溫昇高至830它,在這種周圍 環境中將溫度保持於83010大約3 時,藉此吸收氫氣而進 行氫氣處理。 然後,開啓閥5,同時保持830t之溫度而關閉7停止 供給氫氣,以真空排氣裝置2排出氫氣處理爐1内之氫氣, 進行脱氫一直到IX lO^Torr以下,使排出之氫氣經過濾 *-— " 器3去除灰塵等後供給於氫氣吸收合金儲存裝置4中,將氫 氣吸收合金冷却至10t而再度儲存氫氣。 本實施例中使用之熱處理爐1僳使用具有外熱式 Kanthal線加熱器之真空管狀爐,在氫氣吸收合金儲存裝 ...I . ..一 -.-… * 置4内收存原子比為LaNU.7 A 1〇.3.组成之氫氣吸收合金, 而且使用氫氣儲存量為15Nm3之氫氣吸收合金儲存裝置。 再度儲存於氫氣吸收合金儲存装置4内之氫氣藉著將 收存於氫氣吸收合金儲存裝置4内之氫氣吸收合金加熱至 70t:而將儲存之氫氣再度排出並再度使用。反覆的進行這 種氫氣處理循環10次之結果,消失之氫氣量只有0.05Νιπ3 0 [習用例1 ] 12 Κ請先閲讀背面之注意ί項再填寫本頁) -裝. >ΤΓ. 7旅. 本紙張尺度適用十國國家標準(CNS)甲4規格(210 X 297公釐) 205572 A6 B6 Λ7 3 1 /—' 明 説 明 發 、 五 瀘 tn: 理 瓶處 銷氣 氣氫 氫與 用瓶 使銷 氣 氫 示 圖 未 該行 結進 連下 路件 管 條 以之 源同 給相 供L 氣 氫 為 作 例 驗 實 與 在 氣之 氫氣 次氫 10乎 驗 實 幾 1 例 驗 。 髮耗 實 .消 30氣 Nm氫 6 .6之 5 量 為大 量有 氣 , 氫中 之例 失用 消一習 果)在 结但 • » U Will οώ 列 處消 T 度壓 為溫冲 成在壓 組末水 將粉靜 金熱 合行A pack. Order. A6 B6 205572 5. Description of the invention (4) After being burned in the exhaust treatment device 106 in the rear stage, it is discharged outside the device. In this conventional technique, the hydrogen used in the heat treatment of the metal material is supplied from the hydrogen cylinder 104 to the heat treatment furnace 102, and then discharged into the atmosphere through the exhaust treatment device 106. Therefore, the hydrogen must be supplied again every time the treatment process is performed. The hydrogen consumption becomes very large, and in order to store hydrogen, a large-capacity hydrogen cylinder 104 must be used. f The solution to the above problem is, for example, a method of returning the hydrogen gas discharged from the heat treatment tank 102 to the hydrogen dysprosium bottle 104 on the supply side. However, this method still requires the use of liquefaction treatment equipment to restore the vaporized hydrogen gas to liquid. As a result, the overall heat treatment device becomes large, and the installation cost of the treatment equipment increases, which is not an effective solution. Especially when many heat treatment furnaces are used for heat treatment, it is necessary to install a hydrogen gas supply system on each heat treatment furnace, and as a result, the equipment becomes larger. In addition, when the hydrogen once used for heat treatment is reused, impurities may be mixed during the treatment in the heat treatment furnace, which adversely affects the treatability of the gold tantalum material that has been heat-treated at the same time. The main object of the present invention is to provide a heat treatment method for metal materials that can solve the problems of the above-mentioned conventional techniques. Another object of the present invention is to provide an apparatus that can implement the heat treatment method. According to the first aspect of the present invention, there can be provided a heat treatment method for gold-thorium materials. The method includes the following processes: hydrogen absorption treatment for absorbing hydrogen in metallic materials and hydrogen gas-releasing treatment for releasing hydrogen from the gold-thorax materials for hydrogen absorption; And release the metal materials · Hydrogen recovery and recovery of hydrogen. This paper standard applies to China National Standard (CNS) A 4 specifications (210 X 297 mm)-, ------------- (Installed ------ Order ^ 1 · 4 V, please read the precautions on the back before writing this page) Printed 205572 A6 B6 by the Beigong Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economy _ V. Invention Instructions (5) Again The hydrogen recovery process supplied to the hydrogen absorption and release process. In the hydrogen recovery process, hydrogen can also be stored in the hydrogen absorbing alloy and the stored hydrogen can be released; it can also be repeated to include hydrogen absorption treatment that absorbs hydrogen in the gold and gold material and releases from the metal material that absorbs hydrogen Hydrogen hydrogen release process hydrogen absorption process. During the argon treatment, the amount of hydrogen absorbed and the amount of dehydrogenation are approximately equal, and the amount of recovered hydrogen is approximately equal to the amount of hydrogen at the next lotus turn, so it is almost unnecessary to re-supply hydrogen. The leakage disappears, and the amount of disappearance is extremely small, as long as the amount of hydrogen gas that disappears is supplemented. According to the second aspect of the present invention, there can be provided a heat treatment apparatus for a metal material, the apparatus including: a hydrogen absorption process for absorbing hydrogen in a gold lute material and releasing hydrogen from the hydrogen-absorbing metal material The heat treatment lobe for release treatment; and attached to the heat treatment furnace for recovering the hydrogen gas released from the heat treatment furnace and supplying the hydrogen to the hydrogen recovery device of the heat treatment furnace again. The hydrogen recovery device may also be composed of a hydrogen storage device made of a hydrogen absorption alloy, and may also be composed of a hydrogen absorption process for absorbing hydrogen in a metal material and a hydrogen release process for releasing hydrogen from a metal material that absorbs hydrogen 2 Composition of heat treatment furnace. For the hydrogen absorbing alloy storage device, for example, the hydrogen absorbing alloy storage device shown in Japanese Patent Laid-Open No. 55-126198 or U.S. Patent No. 4270360 can be used. The device is composed of two porous plates fixed in parallel in a closed container at a certain interval, and a heating and cooling section provided on the outside of the two porous plates and separated from each porous plate by an interval, and formed in the porous The size of the paper on the board is in accordance with China National Standard (CNS) A4 (210 X 297). Please read the precautions on the back before writing this page) 丨 Installed-Printed by the Employee Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs 5 clothing 205572 a6 Ββ 5. Description of the invention (6) Store, after storage. However, if it is cold or the hot gold addition part is stored, the cold storage gas will be filled with hot hydrogen filling in the hydrogen space inside the air. At the same time, the Jinjin Department absorbed the cold storage or the hot gas was added and added a hydrogen ¾ and j in the heated part of the furnace as far as possible in the heat and pressure, such as the heat and pressure, the department changed its letter and measured the test The tester can be used to set the sensor, and the sensor can be installed on the device according to the reason for storage and heat storage. The gas generator can detect hydrogen and sense the temperature of the furnace. The heat exhausting furnace is arranged to borrow heat here, and the pressurized part of the autoclave is filled with hydrogen from the temperature and the furnace or the force, and the stored gas is stored in the state of storage. The hydrogen is placed and installed in the argon pressure to maintain the temperature control system. The temperature is controlled in the installed formal furnace. The control and installation place is used for heat storage and storage. When the hydrogen is in the middle, the process will be installed. In the manufacturing structure, the material temperature is controlled and the material is placed in the structure of the storage, absorption and temperature control, so that the furnace can be gasified, and the heat of hydrogen is like this. At the same pressure as suction, the vitality will be compressed into gold, the pressure will be fixed, and the special harvest will be combined with the suction pressure and the gas will be degraded and the temperature will be set at the same time. Was expected to follow. The material gas belongs to the place of hydrogen. The gold is collected from the gas, the gas is stored in the argon, and the hydrogen is charged. The raw materials are stored. The gas is produced. The hydrogen in the gas is processed properly. It is hot everywhere, and now it is inhaled until it is sent / received / please read the precautions on the back and then fill out this page.) The installation material is controlled by the power system, and the heat control is made at the furnace installation location. It is made with a square face, and it is formulated for a period of time and is specially tailored to the temperature and temperature. The temperature of the gas storage furnace in which the temperature is kept and the temperature is kept at the same time will be the same as the heat, and the material is collected and the material is collected and the gas is absorbed. The hydrogen heat is present in the gas management department, and, for example, as shown in the figure, the pressure is released and the gas is released until the hydrogen is released and the paper ruler is fully compliant with the Chinese National Standard (CNS) A 4 specifications (210 X 297 mm) a6 B6 V. Description of the invention (7) Printed by the Employee Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economy I —---------------- ^ -------- Installed ----- -Subscribe ----- 1.4 ------------------------ V Please read the precautions on the back and then write this page) The furnace is supplied with compressed gas When the hydrogen is supplied to the suction gas, the hydrogen supplied by the suction gas may be connected or connected, but the power of the gas is placed in the place of the gas hydrogen furnace and the furnace is installed in the same way. The hydrogen is reasonably hot Empty furnace pressure furnace gas structure, intercommunicating storage location for transportation and storage. Furnace will install the truth gas distribution center in the middle storage area with gas. The heat in the hydrogen gas and the heat in the middle of the heat is really stored when the hydrogen is stored, _ gas is placed in the heat, placed in the middle section for the storage, and the material is installed from the top. Furnace regulation and supply site, gas path, general order, hydrogen equipment, secondary storage, storage and management, but heating hydrogen back to Lian Shun, heating gold will be stored in the storage location, controlled and closed. The control of a gas-gas-gas-gas-heating furnace can be installed in the same way as when it is installed. When hydrogen and hydrogen are also discharged, the hydrogen is stored in a temperature-selective installation. It should be in the flow to the storage department of the storage department to describe the conversion of the image, the central gas supply can be used to control the internal storage of hot gas, and it can be used for hydrogen storage in the future gas installation. After the hydrogen gas is irradiated and the hydrogen is stored, the hydrogen gas will be stored in the same way as the argon, and the hydrogen will be compressed and stored in the argon. The hydrogen gas is stored here and the hydrogen is stored in the furnace at the right part of the furnace. During the installation, the furnace gas is stored as hot hydrogen, and the internal heat is released in the furnace. From the description to the suction arrangement, there are many places. Install and store the hydrogen at the storage place, and the device is equipped with heat outside the furnace. The gas is hot at the seeding point. Send back. In the case of gas transmission and installation, it is more reasonable to wait for the hot hydrogen to be sent to the ring gas in the heat, the Lushen storage office should be replaced by another gold in his place, and the hydrogen is built in. Hot set, it will be transferred to one. Receiving one: The paper size of the paper is applicable to the Chinese National Standard (CNS) A 4 specifications (210 X 297 mm) 7 205572 A6 B6 5. Invention description (8) Central Bureau of Standards, Ministry of Economic Affairs Printed by employee consumer cooperatives, please read the precautions on the back before writing this page) t at the state, the internal heat of the upper and middle heat and the road gas furnace transmission one reason t Set in the middle and section, the furnace is equipped with hydrogen. Λ 、、 The pressure knot is more flat and installed in the place where the furnace power is adjusted to the gas. It is installed in addition to the S5 and even the furnace. The gas is stored in the row of the heat and pressure. The heat is refined in the row. Disposal of the heat installed in the storage and supply department. In the road, the gas is supplied to the gas in the middle of the way. Each gas can be passed through. The hydrogen can be purified. Yu Yiqi, hydrogen too: Unexpected ?, Road. At the same time, there is a lot of gas / placed in the fixed gas supply, the row structure is made of through the material, the hydrogen is allowed to be placed ... As a result, the heat of the I company in the middle of the I will make the stored air supply the number of air, and it can be used as a gas. It can be used to store the gas section with genuine hydrogen hydrogen. This hydrogen gas can be installed on 1 way. Moreover, the gas-hydrogen control has been measured and will be described as the gas recovery and storage, and the Ϊ5 hydrogen body has been set up from the root state, the gas is closed and the hydrogen is stored, until the gas is used. The temperature setting is α. This hydrogen prevention gas is installed and the hydrogen sent by S3 is installed. The side gas can be installed. The hydrogen gas can be stored at the same place. .Package, Ϊ stream storage Furnace Μ gas furnace is used to make air or time under the gas installed in the previous section. The gas is conditioned for hydrogen, and the gas is stored in the arsenal to store the gas. The disposal of multiple hydrogen gas is useful for measuring storage. The vacant gas is filled with hydrogen and heated to generate heat from the heat 0 to the pressure-sensing gas. The hydrogen is stored with the hydrogen. 2. There are shapes, and each hydrogen can be released from the gas. The storage will make the first and second row and the middle row of the power and the hydrogen produced by each furnace can be affected by the furnace, and the furnace is located in the hydrogen of the air. If the temperature is good, the temperature will be matched with the heat so that the hydrogen will not be transferred to the location where the lotus is located. The hydrogen will be released here. The paper standard for heat generation is in accordance with Chinese national standards ( CNS) A4 specifications (210 X 297 mm) 8 205572 A6 B6 Printed by the employee consumer cooperative of the China National Funeral Standards Bureau of the Ministry of Economy 5. Description of the invention (9) The control device is used for hydrogen absorption treatment in each heat treatment furnace The internal pressure is boosted and hydrogen is supplied, while the hydrogen pressure is released in each heat treatment furnace to reduce the internal pressure and discharge the hydrogen In the heat treatment device of this structure, if one of the heat treatments is suspected to be in the process of absorbing hydrogen in the metal material, after the heat treatment furnace is heated to a predetermined temperature, the pressure control device supplies hydrogen to the inside, and Raise the internal pressure to a fixed pressure, whereby the hydrogen absorption of the metal material occurs in the heat treatment furnace to perform the hydrogen absorption treatment of the metal material. When the hydrogen absorption treatment is completed by the one heat treatment furnace, the treatment in the heat treatment is switched After the hydrogen gas is released, the hydrogen gas in the heat treatment is absorbed and discharged by the pressure control device, and the pressure in the heat treatment chamber is depressurized while the hydrogen gas is discharged. As a result, the phenomenon of hydrogen evolution from the gold-thorax material occurs in the heat treatment furnace, and the hydrogen evolution treatment of the metal material is performed. On the one hand, when hydrogen release treatment is performed in a heat treatment furnace in this way, other heat treatment furnaces connected to the heat treatment furnace through the communication path are preparing for hydrogen absorption treatment by heating the inside thereof to a specific temperature parallel to the treatment. When the heat treatment is deemed to be completed or parallel to the hydrogen release process, the pressure control device transports the hydrogen drawn from the one heat treatment furnace to other heat treatment lumens. Therefore, the pressure increase operation of the internal pressure and the filling operation of hydrogen are performed on the other heat treatment furnaces, and hydrogen absorption treatment is performed in the other heat treatment furnaces. As described above, according to the present invention, the hydrogen used in the heat treatment of the metal materials between the heat treatment furnaces can be prevented from being released from the device, and the amount of hydrogen required by one heat treatment furnace can be used for at least 2 hot places. The size of this paper is in accordance with Chinese National Standard (CNS) A4 specifications (210 X 297 mm) 〇: Please read the precautions on the back before writing this page) 丨 Installation-Order R Quan _ 205572 A6 B6 Central Bureau of Economic Standards Du-printing by negative labor consumption cooperation 5. Description of the invention (10) The heat treatment of the furnace not only reduces the amount of hydrogen used, but also avoids the increase in the shape of the device. It is also possible to connect the heat treatment furnaces to each other to form a hydrogen gas refining device in the middle of the communication path of a general closed loop forming a hydrogen gas flow between the heat treatment furnaces. In this way, when hydrogen gas is sent from one heat treatment furnace to another heat treatment furnace, the hydrogen gas can be passed through a hydrogen refining device to send clean hydrogen gas to the heat treatment furnace. The heat treatment method and apparatus of the present invention will be described below with reference to the drawings. Fig. 2 is a conceptual diagram showing the concept of the present invention, that is, a schematic drawing of the heat treatment apparatus according to the first embodiment of the present invention. In Fig. 2, 1 is a heat treatment furnace for hydrogen treatment. 2 is a vacuum exhaust device. 3 is the filter. 4 is hydrogen storage alloy storage device. 5, 6, 7 are valves. 8 is the pipeline. These valves 5, 6, 7 prevent backflow of used hydrogen that has been released and regulate the pressure and flow of hydrogen. The vacuum evacuation device 2 may be omitted according to the raw material used for hydrogen treatment. Fig. 3 shows a schematic diagram when omitted. In Fig. 3, 1 is a heat treatment furnace for hydrogen embedding. 3 is the filter. 4 is hydrogen storage alloy storage device. 5, 6, 7 are valves. 8 is the pipeline. These valves 5, 6, 7 prevent backflow of used hydrogen that has been discharged, and regulate the pressure and flow of hydrogen. When the vacuum evacuation device is omitted in this way, the dehydrogenation of the raw material for absorbing hydrogen in the heat treatment furnace 1 can be performed by using the difference in hydrogen absorption pressure from the hydrogen absorption alloy storage device 4. In other words, if the hydrogen absorption capacity of the hydrogen absorption alloy storage device 4 is greater than the hydrogen absorption capacity of the raw material, the hydrogen absorption of the argon absorption alloy storage device 4 can be used to make the heat treatment furnace 1 negative pressure, whereby the heat treatment furnace 1 can be performed Dehydrogenation of raw materials within. This paper scale is applicable to the Chinese National Standard (CNS) Grade A 4 (210 X 297 public goods). Λ V Please read the precautions on the back and then fill out this page) 丨 installation. ΤΓ_: .4. 20557 A6 B6 Central Ministry of Economic Affairs Printed by the Bureau of Standards, Industry and Consumers Co., Ltd. 5. Description of the invention (11) In FIGS. 2 and 3, the hydrogen filled hydrogen storage alloy storage device 4 is released, and at the same time the valve 7 is opened to supply hydrogen to the heat treatment furnace 1. 1. Hydrogen treatment of dehydrogenation after absorbing hydrogen in the raw material is carried out. The used hydrogen released due to dehydrogenation is sucked by the vacuum exhaust device 2 through the pipeline 8 or directly sucked by the hydrogen absorption alloy storage device 4 . The used hydrogen gas released from the raw material after dehydrogenation is mixed with oxygen, moisture and other impure gas and dust, etc., which are released from the raw material, so the impure gas and dust are removed by the filter 3 and supplied again. Hydrogen absorption, —._ · — " ---------------------------------- '. Gold storage device 4 in. Hydrogen stored in the hydrogen absorbing alloy storage device 4 The absorbing alloy must have a capacity to fully absorb the dehydrogenated hydrogen. According to the conventional technology, a large amount of hydrogen needs to be consumed; however, according to the above method, since it is not necessary to release the used hydrogen to the outside, the hydrogen can be reused. Even if young children are consumed, as long as the amount of hydrogen consumed is properly supplemented. As described above, the present invention can effectively use hydrogen, has high safety, and is simple to operate, and its effect is extremely great. The present invention can be applied to the hydrogen treatment of alloys, but its application range is not limited to the hydrogen treatment of alloys, and can also be applied to various other heat treatments that require the use of hydrogen. The embodiments of the present invention will be described below with reference to the embodiments. [Experimental example 1] The cymbals (Nd): 12.5 at%, Co (Co): 11.6 at%, boron (B): 6.0 at% will be dissolved in the electric propeller arc (Plasma A "c) dissolution furnace Error (Zr): 0.1 at%, gallium (Ga): 0.4 at%, the rest is composed of iron (Fe) composed of alloy ingots with a temperature of 1130t: around the argon gas. This paper standard is applicable to Chinese national standards ( CNS) A 4 specifications (210 X 297 mm) ·, ν Please read the precautions on the back before filling out this page). Installed .. ST. --Line-A6 Printed by the Male Workers' Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs B6_ V. Description of the invention (1 2) A 20-hour homogenization treatment is carried out in the environment. On the other hand, as shown in FIG. 2, the heat treatment furnace 1 is vacuum-exhausted by the pipeline 8 via the valves 5, 6, 7. 2, the filter 3, and the hydrogen absorption alloy storage device 4 are connected, the homogenized alloy ingot is placed in the heat treatment furnace 1, the hydrogen absorption alloy is heated to 7010 and hydrogen is supplied from the hydrogen absorption alloy storage device 4 to heat treatment The pressure in Lu 1 is maintained at 1 ℃, and the temperature of the homogenized alloy ingot is raised from room temperature to 830 it. In this surrounding environment, the temperature is maintained. At 83010, about 3 hours, hydrogen is absorbed by this to perform hydrogen treatment. Then, the valve 5 is opened while maintaining the temperature of 830t and 7 is closed to stop the supply of hydrogen, and the hydrogen in the hydrogen treatment furnace 1 is discharged by the vacuum exhaust device 2 for dehydration Hydrogen is below IX lO ^ Torr, the exhausted hydrogen gas is filtered *-" 3 to remove dust, etc., and then supplied to the hydrogen absorption alloy storage device 4, the hydrogen absorption alloy is cooled to 10t to store hydrogen again. The heat treatment furnace 1 used in the example uses a vacuum tubular furnace with an externally heated Kanthal wire heater, which is stored in a hydrogen absorption alloy ... I ......... 1 -.-... * The atomic ratio of storage in 4 is LaNU .7 A 10.3. Hydrogen absorbing alloys of composition, and using a hydrogen absorbing alloy storage device with a hydrogen storage capacity of 15 Nm3. Hydrogen stored again in the hydrogen absorbing alloy storage device 4 is stored by storing in the hydrogen absorbing alloy The hydrogen absorbing alloy in the device 4 is heated to 70t: the stored hydrogen is discharged again and used again. As a result of repeatedly performing this hydrogen treatment cycle 10 times, the amount of hydrogen disappeared is only 0.05Nι 3 0 [Practical example 1] 12 Κ Please read the notes on the back before filling in this page) -installation. ≫ ΤΓ. 7 brigades. This paper scale is applicable to the National Standards (CNS) A 4 specifications (210 X 297 Mm) 205572 A6 B6 Λ7 3 1 / — 'Explanatory notes, Wulu tn: The diagram of the bottle-selling gas hydrogen hydrogen and the bottle-selling bottle hydrogen gas hydrogen are not included in the trip. The source of the same supply phase L gas hydrogen is used as an example and the hydrogen gas in the gas is less than 10 cases. The consumption is 30%. The amount of 30 Nm of hydrogen is 6.6 of 5. The amount is a large amount of gas. The example of hydrogen is useless. The result is dissipated. At the end of the press, the hot water will be joined together

壓 氣 V .1 進 T 之 m&lt;時 W小 ο 3 12持 徑保 粒下 均件 平條 ,之 件 構 之 狀 形 定 持 作 製 置 裝 存 儲 金 爐合 理收 處吸 熱氣 氫 在 有 具 用 使 僳 爐1) 箱 α 空Mm 真3 之ao 器(L 熱為 加比 墨子 石原 式存 藏收 内中 4 氫, 合 之 收 成 a 吸 。 )..氣置 素氫裝 元之之 1 3 ] 土 a 同 稀5H相 等I1J1 d 為例 Μ量驗 Γ,存實 Ρ儲與 e,氣用 α氫使 用他 d使其 且 , Μ 6 卜 Ϊ, 並夕 但 ί δ金置 10合裝 5Α收存 4 吸儲 Νί氣金 &lt;請先閲讀背面之注意事項再填寫本頁) 裝· 為 内 4The compressed gas V .1 enters the T of the m &lt; hour W small ο 3 12 Holds a flat strip under the diameter and grain retention, and the shape of the piece is fixed for the system. The storage and storage gold furnace is reasonably received. The endothermic gas hydrogen is useful. Li furnace 1) Ao box with empty Mm true 3 (L heat is 4 hydrogen in the original storage of Gabi Mozi stone, and the combined harvest is a.) .. 1 of 1 ] Soil a is equal to dilute 5H and I1J1 d is an example of M measurement Γ, the actual storage of P and e, and the gas is used to make it use α hydrogen to make it, Μ 6 卜 Ϊ, at the same time but ί δ 金 置 10 combined 5Α Storing 4 absorbing and storing Νί 气 金 <Please read the precautions on the back before filling out this page)

爐 mn 理 處 置熱 装將 存 , 儲氣 金氫 合之 收中 吸其 氣出 氫放 將而 V 之Μ ^ 热壓 D氣 力阔 金 1 合於 收持 吸保 氣内 氫ί 之 訂. 環 Ϊ 5 圍 0〇 周至 氣高 氫昇 境 爐 m: 理 處 熱 入 放 將Furnace mn is handled and stored hot, the gas is stored in the hydrogenation of the gas, the gas is absorbed and the hydrogen is released, and the V Μ ^ hot pressure D gas power wide gold 1 is used to hold the hydrogen in the gas. Ϊ 5 around 0〇 to gas high hydrogen ascension furnace m: heat treatment

V 度 溫 之 件 構85 金於 合持 ♦ 1 T 保 之度 内溫 I將 下 境 環 圍 周 該 在 约 大 Ρ 經濟部中央標準局貝工消费合作社印製 將2S , 置 氣装 氫氣 收排 吸空 其真 使使 而後 時然 小 , 化為 相成 單空 ^真 以抽 予.内 織I 組 之 件 構 金 合 爐 m: 理 處 氣 氫 將 作The V temperature component is 85 gold and is held together. 1 T The internal temperature I will be around the border. The 2S will be printed at the Beigong Consumer Cooperative of the Central Standards Bureau of the Ministry of Economy. Exhaust and evacuate the air so that it becomes small, and it becomes a single air ^ truly to be pumped. The inner fabric of the group I is composed of the metal furnace m: the treatment of gas and hydrogen will be done

X 下 置 。裝 丨理氣 以 t 處排 0Γ氣空 4t氫真 0-之由 IL 化 相 + α 以 予 織 組 將 施 實 而 氬 脱 行 進 且 並 吸 2 於 含 除 去 3 器 濾 過 經 氣 氫 之 出 排 子 粒 徹 屬 金 之 引 吸 被置 之裝 中存 其儲 中 金 合 收 吸 氣 氫 至 送 輸 被 度 再 存 儲 氣 氫 將 而 V ο 1A 至 却 冷 金 合 收 吸 氣 氫 將 本紙張尺度適用中國國家標準(CNS)甲4規格(210 X 297公釐) 205572 A6 ___B6 _ _ 五、發明説明(1 4 ) 广請先閲讀背面之注意事項再填寫本頁) 於氫氣吸收合金儲存裝置4中。這種氫氣處理進行20次後, 消失之氫氣量為O.lNm3。 [習用例2] 使用氫氣鏑瓶(未圖式)作為氫氣供給源,以管路連結 該氫氣銅瓶與氫氣處理爐,在與實驗例2相同條件下進行 20次氫氣處理,結果消失之氫氣量為26.6Nm3。實驗例2中 幾乎無氫氣之消耗,但習用例中則大量的消耗氫氣。 [實驗例3 ] 本例中使用之合金為ZrCo合金。熱處理瀘1係使用具 有外熱式高純度磺化矽加熱器之真空箱爐,在氫氣吸收合 金儲存裝置4内收存原子比為(La0.7Mm0.3)Hi3.2Co0.5 Μη〇·7Α1〇.6(Μπ為La, Ce, Pr, Hd等稀土元素)組成之氫氣 吸收合金,並使用氫儲存量為15Nm3之氫氣吸收合金儲存 裝置。此時,省略真空排氣裝置,而使用以管路8連接閥 5與據器3而構成之圖3所不裝置。 經濟部中央標準局貝工消費合作社印製 將氫氣吸收合金儲存裝置4内之氫氣吸收合金加熱至 20〇υ使儲存於其中之氫氣放出,將熱處理嫿1内保持於6 氣壓之氫氣周圍環境,將放入熱處理燼1内之ZrCo合金之 溫度昇高至1501C,在該周圍環境中將溫度保持於150它大 約5小時而使其吸收氩氣後,將溫度降低至3010在301C之 溫度下保持2小時而進行氫氣化粉碎。 然後,將溫度昇高至200t:,從ZrCo合金中放出氫氣, 利用與’氫氣吸收合金儲存裝置4之氫氣壓力差將熱處理1 内抽真空使其成為lxl〇_1Torr hL下而進行脱氫。此時, 本紙張尺度適用中國國家標準(CNS)甲4規格(210 X 297公釐) i a A6 B6 205572 五、發明説明(15) (請先閲讀背面之注意事項再填寫本頁) 氫氣吸收合金儲存裝置4之氫氣吸收能力大於溫度2 00t時 之ZrCo合金之氫氣吸收能力許多,因而産‘生氫氣壓力差, 故可利用該氫氣壓力差進行熱處理爐1内之脱氫。 從熱處理爐1放出之氫氣經過濾器3披去除含於其中之 金屬撤粒子後,再度被輸送至氩氣吸收合金儲存裝置4中, 將氫氣吸收合金冷却至ίου而儲存於氫氣吸收合金儲存裝 置4中。這種氫氣處理進行20次後,消失之氫氣量為 0 . 2Nm3 〇 [習用例3 ] 使用氫氣鋼瓶(未圖示)作為氫氣供給源,以管路連結 該氫氣銷瓶與氫氣處理爐,在與實施例3相同之條件下進 行20次氫氣處理,結果消失之氫氣量為31.5Hm3。實驗例 2中幾乎無氫氣之消耗,但習用例中則消耗大量氫氣。 以下說明本發明之熱處理裝置之更具體實施例。 經濟部中央標準局R工消費合作社印製 圖4及圖5表示本發明第2實施例之金屬材料W之熱處理 裝置10。該熱處理裝置10包括:進行將氫氣吸收於金羼材 料V之氫氣吸收處理,及從吸收氫氣之金屬材料中放出氫 氣之氫氣放出處理之熱處理爐11;用來儲供給於熱處理爐 11及從熱處理爐11排出之氫氣之由氫氣吸收合金Μ製成之 氫氣儲存裝置12;分別設在熱處理鱸11及氫氣儲存裝置12 上,用來檢測其内部壓力及内部溫度之壓力感測器1 3及溫 度感測器1 4 ;根據各感測器1 3 , 1 4之檢測信號調節熱處理 爐11及氫氣儲存裝置12之内部壓力或溫度,藉此,配合熱 處理爐11之處理狀態將氫氣供給於熱處理爐11及從熱處理 本紙張尺度適用中國國家標準(CNS)甲4规格(210 X 297公釐) -,κ ^05572 A6 B6_ 五、發明説明(16) 爐排出之控制裝置15。 該熱處理爐11像使用真空容器内具有石墨,鎢絲,或 鉬等所構成之加熱器16之内熱式處理爐;或在真空容器外 具有Kanthal線,高純度磺化矽等之加熱器16之外熱式熱 處理爐。本實施例中係使用外熱式熱處理爐11。 此等外熱式及内熱式熱處理爐11可根據其處理對象之 金靥材料W之種類適當的變更。 如圖5所示,氫氣儲存裝置12包括:形成外殼之壓力 容器17;設在壓力容器17内,與其内周面相距一定間隔之 由熱傳導髏材料製成之傳熱容器18;設在傳熱容器18之中 央部之由多孔質體製成之支持管19;填充在形成於支持管 19與傳熱容器18之間之空間部内之氫氣吸收合金M;及包 圍在傳熱容器18周圍之加熱器20。 氫氣吸收合金Μ僳使用例如R-Ni条列合金(R為稀土元 素)。Ti-Fe-Mn条列合金,Ή-Μη条列合金等在常溫附近之 氫氣吸收率及放出率大之合金。 圖4中,於壓力容器17之壁部上設有貫穿該壁部而位 於支持管1 9内之連通管2 1 ;用來檢測壓力容器1 7之内部壓 力及内部溫度,亦即氫氣吸收合金Μ周圍之壓力及溫度之 壓力感測器1 3及溫度感測器1 4。 加熱器20連接於藉著控制供給於該加熱器20之電流而 控制其發熱量,以便調節壓力容器17内之溫度之溫度控制 裝置22。 連結於壓力容器17之連通管21之另一端連結於熱處理 16 r請先閲讀背面之注意事項再塡寫本頁) 丨裝- 訂· • I . 經濟部中央標準局員工消費合作社印制衣 本紙張尺度適用中國國家標準(CNS)甲4規格(210 X 297公釐) 205572 A6 經濟部中央標準局貝工消費合作杜印製 _B6_ 五、發明説明(17) 嫌11中使兩者成為連通,在其中途設有用來控制氫氣儲存 裝置12及熱處理爐11内之壓力之壓力控制'裝置23。 該壓力控制裝置23僳使用例如汽缸等具有可増減其容 積之結構而且不會與裝置外之氣體互相交換氣髏之結構, 例如汽缸,而且由控制裝置15選擇性的連通於熱處理爐11 與壓力容器17;並且將互相連通之該等容積放大而將熱處 理爐11或壓力容器17内之壓力減壓,吸引其内部之氫氣; 又減小容積而將壓力容器17内之壓力昇壓,並且將氫氣送 入其内部。 在熱處理爐11中設有與氫氣儲存裝置12相同之溫度控 制裝置22;各溫度控制裝置22連接於控制裝置15,而根據 控制裝置1 5所産生之控制信號控制供給於各加熱器1 6,2 0 之電流。 控制裝置15包括:中央處理電路(以下稱CPU)24;記、................... 億着該CPU24之動作程式之只讀記億器 &lt;以下稱R0M)25;記 億着熱處理爐11之控制程式之隨意存取記億器(以下稱RAM )26;經由匯流排母線連接於CPU24, R0M25,及RAM26而與 .一《—— 各壓力感測器1 3 ,溫度感測器1 4 ,溫度控制裝置2 2 ,及壓 力控制裝置23進行信號之授受之I/O介面27。 在壓力控制裝置23兩旁之連通管21上分別設有開閉閥 2 8 , 2 8 ;該等開閉閥2 8 , 2 8由控制裝置1 5分開的値別操作 而開閉,藉此將壓力控制裝置23選擇性的連通於熱處理爐 11或氫氣儲存裝置12。 本實施例中,作為熱處理對象之金屬材料W之組成如 17 (請先閲讀背面之注意事項再塡寫本頁) 丨裝. 訂. 本紙張尺度適用中國國家標準(CNS)甲4規格(210 X 297公釐) 2055*72 A6 B6 經濟部中央標準局员工消费合作社印製 五、發明説明(18) 下。 其中之一種金屬材料為R-Fe-B条列合’金(R為稀土元素 ),具有如下之组成: R:10 〜20at% B: 3 〜10 at% Fe:其餘及不能避免之不純物 視需要可添加如下之組成。 Co: 0.1 〜50 at% Μ ' 0.001〜5.0 a t % 但 Μ為 Al, Si, Ga, Ti, V, Cr, Zr, Nb, Mo, Hf, Ta, W, C, N中之一種或2種以上。 另一種金屬材料僳Ti条列合金之構造材料,有例如以 下之合金組成: 1) A1: 6 . 5 w t % , Sn: 1 . 4 vf t % , Zr: 1 w t % , Mo: 2.9 w t % , C r : 2 . 1 w t ^ , Fe: 1.7wt%,其餘為 Ti之合金。 2) A 1 : 6wt% , V: 4wt%,其餘為 Ti 之合金。 3) A1: 6 w t %, Sn: 2 w t % , Z r : 4 w t %, Mo: 2 w t % , 其餘為T i之合金。 4 ) V : 1 0 w t %,Fe: 2 w t % , Al: 3 w t % ,其餘為 Ti之 合金。 其他亦可使用於稀土 -Ni条列合金,Zr-Co条列合金等 氫氣吸收合金之活化處理,及粉末化處理。 以下利用實驗例4及5説明使用本實施例之裝置進行熱 處理時之具體例。 18 :請先閲讀背面之注意事項再填寫本頁) i裝_ 訂· .泉. 本紙張尺度適用中國國家標準(CNS)甲4規格(210 X 297公釐) 205572 A6 B6 五、發明説明(〗9 ) V請先閲讀背面之注意事項再填寫本頁) [實驗例4 ] 將表1中1〜4所示組成之R-Fe-B糸列合金在電漿電弧 溶解爐中溶解及鑄造後,在A「氣周圍環境中,11301, 20 小時之條件下進行均化處理。該金屬材料W具有粒徑120 ju m左右之粗大強磁性相。 將該金靥材料W放入熱處理爐11内,將熱處理燫11内 抽真空後,從控制裝置15將控制信號供給於兩個溫度控制 裝置22,開始加熱該熱處理爐11及氫氣儲存裝置12。 此時,溫度感測器1 4撿測出各熱處理爐1 1及氫氣儲存 裝置12之内部溫度,並將之反饋至控制裝置15,根據該反 饋信號補僂供給於各溫度控制裝置22之控制信號,藉此將 熱處理爐11之内部溫度保持於待定溫度(大約830C),並 將氫氣儲存裝置12之内部溫度保持於待定溫度(大約70Ό) 〇 然後,控制裝置1 5將驅動信號供給於氫氣儲存裝置1 2 側之開閉閥2 8 ,開啓該開閉閥2 8,藉此將氫氣儲存裝置1 2 連通於壓力控制裝置23。 經濟部中央標準局貝工消費合作社印製 此時,控制装置1 5將控制信號供給於壓力控制裝置2 3 ,以便吸收氫氣儲存裝置12之氫氣,藉此降低氫氣儲存裝 置12之壓力容器17内之壓力。 如此,從氫氣儲存裝置12内之氫氣吸收合金Μ中放出 氫氣,並且將氫氣吸引至壓力調節裝置23。 然後,控制裝置1 5將驅動信號供給於兩値開閉閥2 8 , 使開啓狀態之氫氣儲存裝置1 2側之開閉閥2 8關閉,另一開 本紙張尺度適用t國國家標準(CNS)甲4規格(210 X 297公釐) ,〇 A6 A6 205572 B6_ 五、發明説明(20) 閉閥28開啓,將壓力控制裝置23與熱處理爐11連通。 此時,控制裝置1 5將控制信號供給於' 壓力控制裝置2 3 ,將該壓力控制裝置23吸收之氫氣輸送至熱處理爐11,使 熱處理爐11之内部壓力上昇,並且將從氫氣儲存裝置12吸 引之氣氣輸送至熱處理爐11。 此時,熱處理瀘1 1之内部壓力已被壓力感測器1 3檢測 而反饋至控制裝置15,故根據該反饋信號調節開閉閥28之 開啓度,或控制壓力控制裝置23之動作量,藉此將熱處理 爐11内之氫氣壓力保持於大約latm。 如上所述完成氫氣供給後,控制裝置15將熱處理爐11 内之溫度調節成為大約830C,將該金靥材料在該溫度下 大約保持3小時,藉此將氫氣吸收於金屬材料W中。 然後,在將熱處理爐11内之溫度保持於830亡,並將 氫氣儲存裝置12之溫度保持於10亡之狀態下,控制裝置15 將驅動信號供給於熱處理爐1 1侧之開閉閥2 8 ,使該開閉閥 28開啓,並且將控制信號供給於壓力控制裝置23,使該壓 力控制裝置23將熱處理爐11内之氣體吸引。 如此,可降低熱處理瀘11内之壓力,使金屬材料放 出其所吸收之氫氣,並且將該氫氣吸收至壓力調節裝置23 ,藉此進行金羼材料W之脱氫。此時,熱處理爐11内之壓 力,係由壓力感測器13及控制裝置15所驅動而動作之壓力 控制裝置23所産生之動作量控制,被保持於lx lOMTorr 以下。 然後,控制装置15産生之驅動信號使熱處理爐11側之 本紙張尺度適用中國國家標準(CNS)甲4規格(210 X 297公釐) 9 Λ V請先閲讀背面之注意事項再填寫本頁) .裝, 訂_ 經濟部中央標準局员工消费合作社印製 205572 A6 B6 經濟部中央標準局興工消費合作社印製 五、發明説明(2 1) 開閉閥2 8關閉,使氫氣儲存裝置1 2側之開閉閥2 8開啓。此 後,由於壓力控制裝置23之動作,將壓方控制裝置23所吸 收之氫氣輸送至氫氣儲存裝置12之壓力容器17内。 此時,壓力容器17内之氫氣壓力隨着上述操作而昇高 ,因而將送入之氫氣由氫氣吸收合金Μ吸收並回收。 因此,進行上述處理後,各組成之Nd-Fe-B合金被粉 碎成400w m以下,而且在粉末内部具有由0.2〜0.4w m之 Nd2Fel4B之再結晶所構成之組織,並且具有所需之磁特性 Ο 如上所述,在本實施例之熱處理裝置10中,使用於金 靥材料W之熱處理之氫氣在氫氣儲存装置12與熱處理爐11 之間被授受,可抑制氫氣被放出於裝置外,故可顯著的減 少氫氣之使用量,而且不需要排氣處理用之設備,故可避 免裝置之形狀大型化,及防止設備費用之增加。 因為作為氫氣儲存裝置12使用之氫氣吸收合金Μ與習 用之容量相同氫氣網瓶比較,具有3倍至4倍之氫氣儲存能 力,故又可使裝置小型化。 表2中之左欐表示本實施例之熱處理裝置11中,將氫 氣儲存裝置12中之初期氫氣儲存量設定為35Nm3,對上述 各組成之金屬材料W進行1 0次處理後,測定氫氣減少量之 結果。 表2中之右橱僳為了比較而表示利用習用裝置對同樣 之各金屬材料W進行熱處理時之氫氣之減少量。 由表中之結果可知,依照本實施例,幾乎無氳氣之減 本紙張尺度適用中國國家標準(CNS)甲4規格(210 X 297公釐) V請先閲讀背面之注意事項再塡寫本頁) 丨裝· .11.X down. Install 丨 Riqi to discharge 0Γ gas at t, 4t hydrogen true 0- from the IL conversion phase + α to pre-weave the organization will be applied and argon de-traveling and suck 2 in the filter containing the filter 3 through the filtered hydrogen The gold is absorbed and stored in the installed equipment, and the stored gold is collected to absorb hydrogen until it is delivered to the temperature, and then the gas is stored. The V ο 1A to the cold gold is collected to absorb hydrogen. This paper standard is suitable for China. National Standard (CNS) A 4 specifications (210 X 297 mm) 205572 A6 ___B6 _ _ V. Description of the invention (1 4) Please read the precautions on the back before filling this page) in the hydrogen absorption alloy storage device 4. After this hydrogen treatment was performed 20 times, the amount of hydrogen disappeared was 0.1 Nm3. [Conventional Example 2] Using a hydrogen dysprosium bottle (not shown) as a hydrogen supply source, the hydrogen copper bottle and the hydrogen treatment furnace were connected by a pipeline, and hydrogen treatment was performed 20 times under the same conditions as in Experimental Example 2, and the resulting hydrogen gas disappeared. The amount is 26.6Nm3. In Experimental Example 2, there is almost no hydrogen consumption, but in the conventional example, a large amount of hydrogen is consumed. [Experimental Example 3] The alloy used in this example is ZrCo alloy. The heat treatment Lu 1 uses a vacuum box furnace with an external heat type high-purity sulfonated silicon heater, and the atomic ratio stored in the hydrogen absorbing alloy storage device 4 is (La0.7Mm0.3) Hi3.2Co0.5 Μη〇 · 7Α1 〇.6 (Mπ is La, Ce, Pr, Hd and other rare earth elements) composed of hydrogen absorption alloy, and the use of hydrogen storage capacity of 15Nm3 hydrogen storage alloy storage device. At this time, the vacuum evacuation device is omitted, and the device shown in FIG. 3, which is configured by connecting the valve 5 and the data device 3 with the pipeline 8, is used. Printed by the Beigong Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs, the hydrogen absorption alloy in the hydrogen absorption alloy storage device 4 is heated to 20 ° to release the hydrogen stored therein, and the heat treatment atmosphere 1 is maintained at a hydrogen atmosphere of 6 atmospheres. The temperature of the ZrCo alloy placed in the heat-treated ember 1 is increased to 1501C, and the temperature is maintained at 150 in the surrounding environment for about 5 hours to allow it to absorb argon gas, and the temperature is reduced to 3010 and maintained at a temperature of 301C Hydrogenation pulverization was carried out in 2 hours. Then, the temperature was raised to 200t: hydrogen gas was released from the ZrCo alloy, and the hydrogen pressure in the hydrogen storage alloy storage device 4 was used to evacuate the heat treatment 1 to lxl0_1 Torr hL for dehydrogenation. At this time, the paper scale is applicable to the Chinese National Standard (CNS) A4 specifications (210 X 297 mm) ia A6 B6 205572 5. Invention description (15) (please read the precautions on the back before filling this page) Hydrogen absorption alloy The hydrogen absorption capacity of the storage device 4 is greater than the hydrogen absorption capacity of the ZrCo alloy at a temperature of 200 t, so the hydrogen generation pressure difference is generated, so the hydrogen pressure difference can be used to perform dehydrogenation in the heat treatment furnace 1. After the hydrogen gas discharged from the heat treatment furnace 1 is removed by the filter 3 to remove the metal particles contained therein, it is transported to the argon absorption alloy storage device 4 again, and the hydrogen absorption alloy is cooled to ίου and stored in the hydrogen absorption alloy storage device 4 in. After this hydrogen treatment was performed 20 times, the amount of hydrogen disappeared was 0.2 Nm3. [Conventional Example 3] Using a hydrogen cylinder (not shown) as a hydrogen supply source, the hydrogen pin cylinder and the hydrogen treatment furnace were connected by a pipeline. The hydrogen treatment was performed 20 times under the same conditions as in Example 3, and as a result, the amount of hydrogen disappeared was 31.5 Hm3. In Experimental Example 2, there is almost no hydrogen consumption, but in the conventional example, a large amount of hydrogen is consumed. The following describes more specific embodiments of the heat treatment apparatus of the present invention. Printed by R Industry and Consumer Cooperative, Central Bureau of Standards, Ministry of Economic Affairs. Figures 4 and 5 show a heat treatment apparatus 10 for a metal material W according to a second embodiment of the present invention. The heat treatment apparatus 10 includes: a heat treatment furnace 11 that performs hydrogen absorption processing that absorbs hydrogen in the Jinge material V, and hydrogen release processing that releases hydrogen from the metal material that absorbs hydrogen; A hydrogen storage device 12 made of a hydrogen absorption alloy M for the hydrogen discharged from the furnace 11; respectively provided on the heat-treated perch 11 and the hydrogen storage device 12, a pressure sensor 13 and a temperature for detecting its internal pressure and internal temperature Sensor 14; adjust the internal pressure or temperature of the heat treatment furnace 11 and the hydrogen storage device 12 according to the detection signals of the sensors 1 3, 14 to thereby supply hydrogen to the heat treatment furnace in accordance with the processing state of the heat treatment furnace 11 11 and from the heat treatment of this paper, the standard of China National Standard (CNS) A 4 (210 X 297 mm)-, κ ^ 05572 A6 B6_ V. Description of the invention (16) Furnace discharge control device 15. The heat treatment furnace 11 uses an internal heat treatment furnace with a heater 16 composed of graphite, tungsten wire, or molybdenum in a vacuum container; or a heater 16 with a Kanthal line, high-purity sulfonated silicon, etc. outside the vacuum container External heat treatment furnace. In this embodiment, the external heat type heat treatment furnace 11 is used. These external heat type and internal heat type heat treatment furnaces 11 can be changed as appropriate according to the type of the metal material W to be processed. As shown in FIG. 5, the hydrogen storage device 12 includes: a pressure vessel 17 that forms an outer shell; a heat transfer vessel 18 made of a heat-conducting skull material disposed in the pressure vessel 17 at a certain distance from its inner circumferential surface; A support tube 19 made of a porous body in the central portion of the container 18; a hydrogen absorption alloy M filled in the space formed between the support tube 19 and the heat transfer container 18; and heating surrounding the heat transfer container 18器 20. As the hydrogen absorption alloy Msu, for example, R-Ni strip alloy (R is a rare earth element) is used. Ti-Fe-Mn bar alloys, Ή-Mη bar alloys, etc. have large hydrogen absorption rate and release rate near room temperature. In FIG. 4, a communication tube 21 is formed on the wall of the pressure vessel 17 and penetrates the wall and is located in the support tube 19; it is used to detect the internal pressure and internal temperature of the pressure vessel 17, that is, hydrogen absorption alloy Pressure sensors 1 3 and temperature sensors 14 for pressure and temperature around the M. The heater 20 is connected to a temperature control device 22 that controls the amount of heat generated by controlling the current supplied to the heater 20 so as to adjust the temperature in the pressure vessel 17. The other end of the connecting tube 21 connected to the pressure vessel 17 is connected to the heat treatment 16 r. Please read the precautions on the back before writing this page) 丨 Installation-Order · I. Printed copies of clothes by the Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs The paper scale is in accordance with Chinese National Standard (CNS) A4 specifications (210 X 297 mm). 205572 A6 Printed by Beigong Consumer Cooperation, Central Bureau of Standards, Ministry of Economic Affairs _B6_ V. Description of invention (17) In 11 cases, the two are connected In the middle, there is a pressure control device 23 for controlling the pressure in the hydrogen storage device 12 and the heat treatment furnace 11. The pressure control device 23 uses a structure such as a cylinder that can reduce its volume and does not exchange gas with the gas outside the device, such as a cylinder, and the control device 15 selectively communicates with the heat treatment furnace 11 and the pressure Container 17; and enlarge the interconnected volumes to reduce the pressure in the heat treatment furnace 11 or the pressure vessel 17 to reduce the pressure of the hydrogen inside; and reduce the volume to increase the pressure in the pressure vessel 17 and increase Hydrogen is fed into it. The heat treatment furnace 11 is provided with the same temperature control device 22 as the hydrogen storage device 12; each temperature control device 22 is connected to the control device 15, and the supply to each heater 16 is controlled according to the control signal generated by the control device 15; 2 0 current. The control device 15 includes: a central processing circuit (hereinafter referred to as a CPU) 24; a memory, a read-only memory device for the operation program of the CPU 24 ; Hereinafter referred to as R0M) 25; arbitrarily access the billions of memories (hereinafter referred to as RAM) 26 with the control program of the heat treatment furnace 11; connected to the CPU24, R0M25, and RAM26 via the bus bar. The pressure sensor 1 3, the temperature sensor 14, the temperature control device 2 2, and the pressure control device 23 perform an I / O interface 27 for signal transmission and reception. On the communication tubes 21 on both sides of the pressure control device 23, on-off valves 28, 28 are provided; these on-off valves 28, 28 are opened and closed by separate operations of the control device 15 to thereby control the pressure control device 23 is selectively connected to the heat treatment furnace 11 or the hydrogen storage device 12. In this embodiment, the composition of the metal material W as the heat treatment object is 17 (please read the precautions on the back before writing this page) 丨 Packed. Ordered. This paper scale is applicable to the Chinese National Standard (CNS) A 4 specifications (210 X 297 mm) 2055 * 72 A6 B6 Printed by the Employee Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs V. Invention Instructions (18). One of the metal materials is R-Fe-B series alloy (R is a rare earth element), which has the following composition: R: 10 ~ 20 at% B: 3 ~ 10 at% Fe: the rest and the impure physical vision that cannot be avoided If necessary, the following composition can be added. Co: 0.1 ~ 50 at% Μ '0.001 ~ 5.0 at% but Μ is one or two of Al, Si, Ga, Ti, V, Cr, Zr, Nb, Mo, Hf, Ta, W, C, N the above. Another metal material is the structural material of the Ti series alloy, which has the following alloy composition: 1) A1: 6.5 wt%, Sn: 1.4 vf t%, Zr: 1 wt%, Mo: 2.9 wt% , C r: 2.1 wt ^, Fe: 1.7 wt%, the rest is Ti alloy. 2) A 1: 6wt%, V: 4wt%, the rest is Ti alloy. 3) A1: 6 wt%, Sn: 2wt%, Zr: 4wt%, Mo: 2wt%, and the rest are Ti alloys. 4) V: 10 wt%, Fe: 2 wt%, Al: 3 wt%, and the rest are Ti alloys. Others can also be used for activation treatment and powdering treatment of hydrogen absorption alloys such as rare earth-Ni strip alloys, Zr-Co strip alloys. In the following, specific examples of heat treatment using the apparatus of this embodiment will be described using Experimental Examples 4 and 5. 18: Please read the precautions on the back before filling in this page) i 装 _ 定 ·. 泉. This paper scale is applicable to China National Standard (CNS) A 4 specifications (210 X 297 mm) 205572 A6 B6 V. Description of invention ( 〗 9) VPlease read the precautions on the back before filling in this page) [Experimental Example 4] Dissolve and cast the R-Fe-B Shito column alloy with the composition shown in Table 1 1 to 4 in the plasma arc dissolution furnace After that, homogenization treatment is carried out under the conditions of 11301 and 20 hours in the surrounding environment of the gas "A. The metal material W has a coarse ferromagnetic phase with a particle size of about 120 ju m. The gold tantalum material W is put into the heat treatment furnace 11 After evacuating the heat treatment chamber 11, the control device 15 supplies control signals to the two temperature control devices 22 to start heating the heat treatment furnace 11 and the hydrogen storage device 12. At this time, the temperature sensor 14 picks up The internal temperature of each heat treatment furnace 11 and hydrogen storage device 12 is output and fed back to the control device 15, and the control signal supplied to each temperature control device 22 is compensated according to the feedback signal, thereby the internal temperature of the heat treatment furnace 11 Maintain the temperature to be determined (about 830C), and put hydrogen The internal temperature of the storage device 12 is maintained at a predetermined temperature (about 70 °). Then, the control device 15 supplies the drive signal to the on-off valve 2 8 on the side of the hydrogen storage device 12 and opens the on-off valve 28 to store the hydrogen gas. The device 1 2 is connected to the pressure control device 23. Printed by the Beigong Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs At this time, the control device 15 supplies the control signal to the pressure control device 2 3 to absorb the hydrogen of the hydrogen storage device 12, thereby Reduce the pressure in the pressure vessel 17 of the hydrogen storage device 12. In this way, hydrogen is released from the hydrogen absorption alloy M in the hydrogen storage device 12, and the hydrogen is attracted to the pressure regulating device 23. Then, the control device 15 supplies the driving signal On the two-valve on-off valve 2 8, the on-off valve 2 8 on the 2 side of the open hydrogen storage device 12 is closed, and the other format of the paper is applicable to the national standard (CNS) A 4 specification (210 X 297 mm), 〇A6 A6 205572 B6_ V. Description of the invention (20) The valve 28 is opened, and the pressure control device 23 is connected to the heat treatment furnace 11. At this time, the control device 15 supplies the control signal to the pressure Control device 2 3, the hydrogen absorbed by the pressure control device 23 is sent to the heat treatment furnace 11, the internal pressure of the heat treatment furnace 11 is raised, and the gas gas sucked from the hydrogen storage device 12 is sent to the heat treatment furnace 11. At this time, the heat treatment The internal pressure of Lu 1 1 has been detected by the pressure sensor 13 and is fed back to the control device 15, so the opening degree of the on-off valve 28 is adjusted according to the feedback signal, or the operation amount of the pressure control device 23 is controlled, thereby the heat treatment furnace The hydrogen pressure in 11 is maintained at about latm. After the hydrogen supply is completed as described above, the control device 15 adjusts the temperature in the heat treatment furnace 11 to about 830C, and maintains the gold tantalum material at this temperature for about 3 hours, thereby absorbing hydrogen in the metal material W. Then, while maintaining the temperature in the heat treatment furnace 11 at 830, and maintaining the temperature of the hydrogen storage device 12 at 10, the control device 15 supplies a driving signal to the opening and closing valve 2 8 on the side of the heat treatment furnace 11, The on-off valve 28 is opened, and a control signal is supplied to the pressure control device 23 so that the pressure control device 23 sucks the gas in the heat treatment furnace 11. In this way, the pressure inside the heat treatment lube 11 can be reduced, the metal material can release the hydrogen it has absorbed, and the hydrogen can be absorbed into the pressure regulating device 23, thereby dehydrogenating the gold material W. At this time, the pressure in the heat treatment furnace 11 is controlled by the operation amount generated by the pressure control device 23 driven by the pressure sensor 13 and the control device 15 and operated, and is kept below lx lOMTorr. Then, the driving signal generated by the control device 15 makes the paper size on the side of the heat treatment furnace 11 applicable to the Chinese National Standard (CNS) A 4 specifications (210 X 297 mm) 9 Λ V Please read the precautions on the back before filling this page) .Installed and ordered _ Printed by the Ministry of Economic Affairs, Central Bureau of Standards, Employee Consumer Cooperative 205572 A6 B6 Printed by the Ministry of Economic Affairs, Central Bureau of Standards, Xinggong Consumer Co., Ltd. V. Description of the invention (2 1) The on-off valve 2 8 is closed, so that the hydrogen storage device 12 The on-off valve 28 is opened. Thereafter, due to the operation of the pressure control device 23, the hydrogen absorbed by the pressure control device 23 is sent to the pressure vessel 17 of the hydrogen storage device 12. At this time, the pressure of the hydrogen gas in the pressure vessel 17 increases with the above operation, so the fed hydrogen gas is absorbed and recovered by the hydrogen absorption alloy M. Therefore, after the above treatment, the Nd-Fe-B alloys of each composition are crushed to 400w m or less, and have a structure composed of recrystallized Nd2Fel4B of 0.2 ~ 0.4wm inside the powder, and have the required magnetic properties Ο As described above, in the heat treatment device 10 of this embodiment, the hydrogen used for the heat treatment of the gold material W is transferred between the hydrogen storage device 12 and the heat treatment furnace 11, and the hydrogen can be suppressed from being released outside the device. Significantly reduce the amount of hydrogen used, and do not require equipment for exhaust gas treatment, so it can avoid the large size of the device and prevent the increase in equipment costs. Since the hydrogen absorption alloy M used as the hydrogen storage device 12 has a hydrogen storage capacity of 3 to 4 times that of the conventional hydrogen mesh bottle with the same capacity, the device can be miniaturized. The left side in Table 2 indicates that in the heat treatment apparatus 11 of this embodiment, the initial hydrogen storage amount in the hydrogen storage device 12 is set to 35 Nm3, and the metal material W of each composition described above is treated 10 times, and then the hydrogen reduction is measured. Result. The right cabinet in Table 2 shows the amount of hydrogen reduction when the same metal materials W are heat-treated using conventional equipment for comparison. As can be seen from the results in the table, according to this embodiment, the paper standard of almost no gas reduction is applicable to the Chinese National Standard (CNS) A 4 specifications (210 X 297 mm) V. Please read the notes on the back before writing. Page) 丨 Install · 11.

-I I 經濟部中央樣準居员工消費合作社印製 205572 A6 _B6_ 五、發明説明(2 2) 少,其效果極大。 [實驗例5 ] ' 使用Ti合金作為金羼材料W。首先,在溫度750t!, 2000atm,及保持上述溫度及壓力3小時之條件下對具有表 3中之1, 2所示之組成,平均粒徑120Wm之Ti合金粉末進 行熱靜水壓冲壓,製作特定形狀之金屬材料W構件。 將該金屬材料W放置於具有内熱式石墨加熱器之熱處 理爐11内,將熱處理爐11内抽真空後,以控制裝置15驅動 熱處理裝置10之各構件,在與上述實施例相同之850t, latai之周圍環境下將氫氣吸收於金屬材料W中,然後在 850¾ , lx 10-4T〇rr之條件下進行該金羼材料W之脱氫處 理。 經過該熱處理後,産生具有粗大之ct+/3相之Ti合金 。這種組成之Ti合金其高循環疲勞強度及耐蟠變(c「eeP) 特性非常優異。 此時,熱處理所使用之氫氣亦在氫氣儲存裝置12與熱 處理爐11之間被授受,藉此可抑制氫氣洩漏至裝置外。 表4中之左橱表示利用初期狀態之氫氣儲存量為 35Νιη3之本實施例裝置對各Ti合金進行20次上述處理後測 定之氫氣減少量。表4中之右糊表示為了比較而利用習用 裝置對本實施例之各Ti合金進行熱處理時之氫氣減少量。 由表中之結果可知,本實施例中亦無氫氣之減少,與 習用裝置比較,有極明顯之改進。 圖6表示第2實施例之其他型式之第.3實施例。在以下 (請先閲讀背面之注意事項再填寫本頁)-I I Printed 205572 A6 _B6_ by the Central Prospective Resident Employee Consumer Cooperative of the Ministry of Economy V. The invention description (2 2) is few, and its effect is great. [Experimental Example 5] 'Ti alloy was used as the gold alloy material W. First, under the conditions of a temperature of 750t !, 2000atm, and maintaining the above temperature and pressure for 3 hours, the Ti alloy powder with the composition shown in Table 3, 1, 2 and an average particle size of 120Wm is hot hydrostatically pressed to produce A metal member W of a specific shape. The metal material W is placed in the heat treatment furnace 11 with an internal heating type graphite heater, after the inside of the heat treatment furnace 11 is evacuated, the components of the heat treatment device 10 are driven by the control device 15 at 850t, which is the same as the above embodiment. Hydrogen is absorbed in the metal material W in the surrounding environment of latai, and then the dehydrogenation treatment of the gold material W is performed under the conditions of 850¾, lx 10-4 Torr. After this heat treatment, a Ti alloy with a coarse ct + / 3 phase is produced. The Ti alloy of this composition has excellent high cycle fatigue strength and resistance to change (c "eeP). At this time, the hydrogen used in the heat treatment is also transferred between the hydrogen storage device 12 and the heat treatment furnace 11, whereby The leakage of hydrogen to the outside of the device is suppressed. The left cabinet in Table 4 indicates the amount of hydrogen reduction measured after performing the above-mentioned treatment on each Ti alloy 20 times using the device of the present example with a hydrogen storage capacity of 35Nιη3. The right paste in Table 4 It shows the amount of hydrogen reduction when using conventional equipment to heat treat each Ti alloy of this embodiment for comparison. From the results in the table, it can be seen that there is no reduction of hydrogen in this embodiment, which is a significant improvement compared to conventional equipment. Figure 6 shows the third embodiment of other types of the second embodiment. In the following (please read the precautions on the back before filling this page)

T .裝, 訂 本紙張尺度適用中國國家標準(CNS)甲4規格(210 X 297公藿) 22 A6 B6 205572 五、發明説明(23) 説明中,與第2實施例相同之部份以相同記號表示而省略 其說明。 . 本實施例中之金靥材料之熱處理裝置40包括:熱處理 爐11;由氫氣吸收合金Μ製成之氫氣儲存裝置12;將熱處 理爐11放出之氫氣翰送至氫氣儲存裝置12之排氣通路41; 將氫氣從氫氣儲存裝置12供給於熱處理爐11之供給通路42 ;設在排氣通路41中吸引熱處理爐11内之氣體而將之輸送 至氫氣儲存裝置12之真空排氣裝置43;設在供給通路42中 ,用來調節供給於熱處理爐11之氫氣壓力之壓力調節裝置 44;分別設在熱處理爐11及氫氣儲存裝置12之壓力感测器 1 3及溫度感測器1 4 ;及根據各感測器1 3 , 1 4之檢測信號調 節熱處理爐11及氫氣儲存裝置12之内部壓力或諝節内部溫 度,及調節真空排氣裝置43之動作,藉此配合熱處理爐11 之處理狀態控制供给於熱處理爐11之氫氣及從熱處理爐11 排出之氫氣之控制装置15。 真空排氣裝置43可使用真空泵,其前後設有開閉閥, 其吸引部連結於熱處理爐11 ,其排氣部連結於氫氣儲存裝 置12。形成於其間之排氣通路41保持氣密性。 壓力諝節裝置44具有開閉閥及減壓閥。平常係以開閉 閥闋閉供給通路42,切斷氫氣儲存裝置12與熱處理爐11之 連通狀態。若需要將氫氣供給於熱處理爐11時,係以減壓 閥將供給於熱處理燧11之氫氣壓力保持於latm以下。 本實施例中,利用供給通路42將氫氣鋼瓶45經由開閉 閥46連設於壓力調節裝置44與氫氣儲存裝置12之間,作為 本紙張尺度適用中國國家標準(CNS)甲4規格(210 X 297公釐) (請先閲讀背面之注意事項再塡寫本頁) .裝. 訂. 經濟部中央揉準局员工消费合作社印製 經濟部中央標準屬男工消费合作社印製 A6 B6 五、發明説明(2 4) 運轉初期之氫氣填充之用,或因洩漏而發生氫氣減少時之 補充之用。 ' 開閉閥46與真空排氣裝置43,壓力調節裝置44-起連 結於控制裝置15;利用控制裝置15所産生之控制信號控制 其動作。 本實施例之熱處理裝置40中之處理對象金靥材料W與 上述實施例中之金羼材料相同。 本實施例中,偽由真空排氣装置43進行氫氣儲存装置 12内之加壓。亦可如圖6所示,在真空排氣裝置43與氫氣 儲存裝置12之間設置加壓裝置47,利用該加壓裝置47使氫 氣儲存裝置12内之壓力更加昇高。此方式在增加儲存於氫 氣儲存裝置12内之氫氣量時非常有效。 以上各實施例中之各構件之形狀及結構,或處理條件 等皆僅為代表例,可根據使用之金屬材料組成,及設計要 求等變更實施。例如在以上各實施例中,熱處理時傜使用 氫氣,但亦可使用氫氣與惰性氣髏之混合氣體。此時可將 '—... 氫氣之分壓作為壓力控制之控制因素。 以下說明本實施例之熱處理裝置40之具體例。 [實驗例6 ] 熱處理裝置40中,在熱處理爐11内放置金屬材料W而 起動裝置後,由控制裝置15控制之各溫度控制裝置22使各 加熱器16, 20發熱,而由各溫度感測器14將熱處理爐11及 氫氣儲存裝置12内之溫度資訊反饋至控制裝置15,藉此可 將熱處理爐11及氫氣儲存裝置12之壓力容器17内之溫度保 本紙張尺度適用中國國家標準(CNS)甲4规格(210 X 297公釐) 〇 . &lt;請先閲讀背面之注意事項再塡寫本頁) -裝. 訂. 205572 A6 _B6_ 五、發明説明(2 5) (請先閲讀背面之注意事項再填寫本頁) 持於一定溫度。 因此,控制裝置15使壓力調節裝置44之開閉閥開啓, 氫氣在其壓力由於壓力諝節裝置44之減壓閥之作用而被保 持於latra之狀態下,從控制裝置15被供給於熱處理爐11。 由於以上操作,在熱處理爐11内發生將氫氣吸收於金 屬材料W中之吸收處理。 將氫氣吸收於金屬材料!ί中之吸收處理完畢後,控制 裝置15將壓力調節裝置44之開閉閥關閉,使真空排氣裝S 43動作,因而吸收熱處理嫿11内之氫氣而將之送入氫氣儲 存裝置12中。 如此,將熱處理瀘11内之壓力減壓而將氫氣儲存裝置 12内之壓力加壓,在熱處理爐11内發生氫氣之放出現象, 而在氫氣儲存裝置12之氫氣吸收合金Μ中發生氫氣吸收現 象。 結果,在熱處理爐11内發生金屬材料W之脱氫處理, 而將從金屬材料W放出之氫氣經由排出通路41回收至氫氣 儲存裝置12之氫氣吸收合金Μ中。 經濟部中央標準局员工消費合作社印製 若因反覆的進行熱處理,或因為在檢修等時將裝置開 放至大氣中而使氫氣量減少時,依照本實施例,係使開閉 閥46動作,將需要量之氫氣從氫氣銷瓶45補充至裝置中。 上述熱處理時之熱條件及壓力條件與以上所述實施例 大致相同,而經過熱處理後之金靥材料W之特性亦大致上 與以上實施例相同。 本實施例之熱處理中,熱處理時使用之氫氣亦在氫氣 25 本紙張尺度適用中國國家標準(CNS)甲4規格(210 X 297公釐) 205572 A6 B6 經濟部中央標準局貝工消費合作社印製 五、發明説明(2 6) 儲存裝置12與熱處理爐11之間被授受,可抑制其洩漏至裝 置外,故氫氣使用量非常少。 此外,本實施例中,因為將熱處理爐11内之氫氣直接 送入氫氣儲存裝置12中,故可同時進行熱處理爐11内之減 壓,氫氣儲存裝置12内之加壓,及將氫氣送入氫氣儲存裝 置12中之操作,藉此3簡化其操作条統。 又因為在供給通路42中設置壓力調節裝置44,故可高 精確度的控制從氫氣儲存裝置1 2供給於熱處理爐1 1之氫氣 之壓力,可進行穩定之熱處理。 以下參照圖7說明本發明之第4實施例之熱處理裝置。 圔中,50為本實施例之金屬材料W之熱處理裝置。該熱處 理裝置50包括:用來進行將氫氣吸收於金屬材料W中之氫 氣吸收處理,及従吸牧氫氣之金屬材料W中放出氫氣之氫 氣放出處理之許多座(本實施例中為2座)熱處理爐ll(lla, lib);將供給於該等熱處理爐ll(lla, lib)或從該等熱處 理爐中排出之氫氣儲存之由氫氣吸收合金Μ製成之氫氣儲 存裝置12;連通各熱處理爐ll(lla, Ub)與氫氣儲存裝置 12,在其間形成氫氣流通用閉迴路之許多連通路53(53a, 53b);將該等連通路53(53a, 53b)中之一選擇性的連通於 氣氣儲存裝置12之轉換裝置54;設在熱處理爐11及氫氣儲 存裝置1 2上,用來檢測其内部壓力及内部溫度之壓力感測 器1 3及溫度感測器1 4 ;根據各感測器1 3 , 1 4之檢測信號調 節熱處理爐11及氫氣儲存装置12之内部壓力或溫度,藉此 配合熱處理爐11之處理狀態將氫氣供給於熱處理爐11或從 V請先閲讀背面之注意事項再填寫本頁) -裝. 訂· ;泉. 本紙張尺度通用中國國家標準(CNS)甲4規格(210 X 297公釐) 26 A6 B6 五、發明説明(2 7) V'請先閲讀背面之注意ί項再填寫本頁) 熱處理爐11排出氫氣之控制裝置15。 各裝置之結構與以上所述實施例相睹,故省略其說明 。在連結於壓力容器17之連通管53之中途設有用來控制氫 氣儲存裝置12及熱處理爐11内之壓力之壓力控制裝置55。 該壓力控制裝置55經由轉換裝置54連接於兩個連通路53( 53a, 53b),而且由於該轉換装置54之作用,經由連通路 53(53a, 53b)選擇性的連通於各熱處理爐11或與各熱處理 爐11切斷連通;而經由設在連通路53之開閉閥56進行其與 氫氣儲存裝置12之連通及切斷。 壓力控制裝置55經由控制裝置15選擇性的連通於各熱 處理爐ll(Ua, lib)與壓力容器17;藉著將互相連通之構 件之容積放大而將各熱處理瀘ll(lla, lib)或壓力容器17 内之壓力減壓,吸收其内部之氫氣,又藉著減小其容積將 各熱處理爐lib)或壓力容器17内之壓力昇高,並 將氫氣送入其中。各熱處理爐ll(lla, lib)上設有與氫氣 儲存裝置12相同之溫度控制裝置22(22a, 22b)。該等溫度 控制裝置22(22a, 22b)連接於控制裝置15,而根據控制裝 置15所産生之控制信號,控制供給於各加熱器16, 20之電 經濟部中央揉準局员工消费合作社印製 流。 以下說明在具有上述結構之本實施例之熱處理裝置50 中進行金羼材料W之熱處理時之具髏例。 [實驗例7 ] 與實驗例4相同的製作具有表1至表4所示組成之R-Fe-B合金所構成之金屬材料W。將該金屬材料W放入一個熱處 本紙張尺度適用中國國家標準(CNS)甲4規格(210 X 297公釐) 27 205572 經濟部中央標準局员工消费合作社印製 明説 明發 '五 2 IX 置 裝 存 儲 氣 氫 及 a 1X 11爐 理 處 熱 該 熱 加 始 開 後 内 a 1X 1X燼 m: 理 部驅 11内將 嫌之15 理12置 處置裝 熱裝制 將存控 , 儲 , 持 保 約 大 持供 保號 度信 溫動 氣後開 氫然56 將 。閥 而度閉 , 溫開 度定該 溫待使 定之56 特 P 閥 之 7 閉 υ約開 5 &gt;大於 ;於給 轉間 5 , 5 時置 此裝 。制 55控 置力 裝壓 制與 控53 力路 壓通 於連 通各 連斷 2 J 1 切 置為 裝成 存持 。 儲保態 氣被狀 氫54之 將置通 ,裝連 啓換之 5 氫 置得 裝使 制 , 控低 力降 壓力 於壓 給之 供内 號17 信器 制容 控力 將 壓 15之 置12 裝置 制裝 控存 , 儲 後氣 然氫 將 供 號 信 33 驅 將 5 IX 置 裝 放制 S控 金 , 合後 收然 吸 〇 氣55 氫置 之裝 内 制 12控 置力 裝壓 存至 儲收 氣吸 氣 氫 該 將 並 氣 氫 出 V請先閱讀背面之注意事項再填寫本頁) 閉 其 使 6 5 閥 之 理 處 收 吸 氣 閉氩控 開行使 於進而 給通因 I3 此 藉 作 c,an^ 33 4 5 置 裝 換 轉 使 且並 置 裝 制 控 力 壓 與 a 11X 1X 燫 理 處熱 置 裝 制 控 力 壓 於 給 供 號 信 制 控 將 5 1X 置 裝 制 置 裝11 制爐 控理 力處 壓熱 爐 Bt 理 處 熱 至 出 送 氣 氫 之 收 吸 高 昇 力 壓 部 内 之 中 a 壚 理 處 熱 入 送 氣 氫 之 收 吸 键15 理置 處裝 熱制 , 控 時至 此饋 反 並 將 將12 此置 藉裝 ,存 la儲 I氣 氫 從 將 且 並 測 撿 3 IX 器 測 感 力 壓 被 力 壓 部 内 之 制 控 力 壓 制 控 號 信 饋 反 該 據 根 此 因 保 力 壓 氣 氫 之内 a 1A 1X爐 RE理 處 熱 將 可 此 藉 量 〇 作tm 動la 之約 55大 置於 裝持 後 給83 供約 氣大 氫為 成 成 完節 此調 如15約 置大 裝持 時 小 1 和和 1 屬靥 燫— — m: 理 處熱 金金 該於 將收 , 吸 P 氣 3 氫 將 此 藉 制保 控下 被度 度溫 溫該 之在 内料料 中 本紙張尺度適用中國國家標準(CNS)甲4規格(210 X 297公坌) 28 A6 B6 2055^2 五、發明説明(29) 然後,在將熱處理爐11a内之溫度保持於830C,將氫 氣儲存裝置12之溫度保持於1010之狀態下,將控制信號供 給於壓力控制裝置55,使該壓力控制裝置55吸引熱處理爐 1 1 a内之氣體。 如此減低熱處理爐11a内之壓力,藉此將吸收於金屬 材料W中之氫氣放出,並將該氫氣吸收至壓力控制裝置55, 藉此進行金靥材料W之脱氫。此時,熱處理爐1 1 a内之壓力 被壓力感測器13及控制裝置15所驅動而動作之壓力控制裝 置55之動作量所控制而被保持於1 X 10 μ Tor r hL下。 然後,控制裝置15所産生之驅動信號使轉換裝置54動 作,切斷壓力控制裝置55與一熱處理爐Ua間之連通,並 且開啓開閉閥5 6 ,然後,使壓力控制裝置5 5動作,藉此將 被壓力控制裝置55吸引之氫氣送入氫氣儲存裝置12之壓力 (請先閲讀背面之注意事項再填寫本頁) 丨裝, 訂_ 内 7 1Α 容 高 昇 而 作 操 述 上 着 隨 力金 壓 合 氣收 氫吸 之氣 内氫 17由 器氣 容氫 力之 壓入 , 送 時將 此而 因 收 回 並 收 吸 Μ 空 真 抽 内 -丨床_ 之 同 相 述 上 與 11用 爐利 理當 處 , 熱内 將lb 置I 裝 之 示 圖 未 用 f , 料 後材 然屬 金 將T. Packed, the size of the printed paper is in accordance with the Chinese National Standard (CNS) A 4 specifications (210 X 297 common patchouli) 22 A6 B6 205572 5. Description of the invention (23) In the description, the same parts as the second embodiment are the same Symbols are shown and their description is omitted. The heat treatment device 40 of the gold tantalum material in this embodiment includes: a heat treatment furnace 11; a hydrogen storage device 12 made of a hydrogen absorption alloy M; the hydrogen gas released from the heat treatment furnace 11 is sent to the exhaust path of the hydrogen storage device 12 41; supply hydrogen from the hydrogen storage device 12 to the supply path 42 of the heat treatment furnace 11; provided in the exhaust path 41 to suck the gas in the heat treatment furnace 11 and transport it to the vacuum exhaust device 43 of the hydrogen storage device 12; In the supply passage 42, a pressure adjusting device 44 for adjusting the pressure of the hydrogen gas supplied to the heat treatment furnace 11; a pressure sensor 13 and a temperature sensor 14 respectively provided in the heat treatment furnace 11 and the hydrogen storage device 12; and According to the detection signals of the sensors 1 3 and 14, the internal pressure or the internal temperature of the heat treatment furnace 11 and the hydrogen storage device 12 are adjusted, and the operation of the vacuum exhaust device 43 is adjusted to match the processing state of the heat treatment furnace 11 A control device 15 that controls the hydrogen gas supplied to the heat treatment furnace 11 and the hydrogen gas discharged from the heat treatment furnace 11. A vacuum pump can be used as the vacuum exhaust device 43, and opening and closing valves are provided at the front and rear, the suction part is connected to the heat treatment furnace 11, and the exhaust part is connected to the hydrogen storage device 12. The exhaust passage 41 formed therebetween maintains airtightness. The pressure unit 44 has an on-off valve and a pressure reducing valve. Normally, the supply passage 42 is closed by opening and closing the valve, and the communication state between the hydrogen storage device 12 and the heat treatment furnace 11 is cut off. When it is necessary to supply hydrogen gas to the heat treatment furnace 11, the pressure of the hydrogen gas supplied to the heat treatment flare 11 is kept below latm with a pressure reducing valve. In this embodiment, the supply cylinder 42 is used to connect the hydrogen cylinder 45 between the pressure regulator 44 and the hydrogen storage device 12 via the on-off valve 46. As the paper standard, the Chinese National Standard (CNS) A4 specification (210 X 297 Mm) (please read the precautions on the back before writing this page). Pack. Order. Printed by the Ministry of Economic Affairs Central Bureau of Labor and Employee's Consumer Cooperative Printed by the Central Ministry of Economics A6 B6. (2 4) It is used for hydrogen filling in the early stage of operation, or for supplementing when hydrogen is reduced due to leakage. The on-off valve 46 is connected to the vacuum exhaust device 43 and the pressure regulator 44 together with the control device 15; the control signal generated by the control device 15 controls its operation. The processing target gold tungsten material W in the heat treatment apparatus 40 of this embodiment is the same as the gold yoke material in the above embodiment. In this embodiment, the vacuum exhaust device 43 is used to pressurize the hydrogen storage device 12. As shown in FIG. 6, a pressurizing device 47 may be provided between the vacuum exhaust device 43 and the hydrogen storage device 12, and the pressure in the hydrogen storage device 12 may be further increased by the pressurizing device 47. This method is very effective in increasing the amount of hydrogen stored in the hydrogen storage device 12. The shape and structure of each member in the above embodiments, or processing conditions are only representative examples, and can be changed and implemented according to the composition of the metal material used, and design requirements. For example, in the above embodiments, hydrogen is used for heat treatment, but a mixed gas of hydrogen and inert gas can also be used. At this time, the partial pressure of hydrogen can be used as the control factor of pressure control. A specific example of the heat treatment apparatus 40 of this embodiment will be described below. [Experimental Example 6] In the heat treatment apparatus 40, after the metal material W was placed in the heat treatment furnace 11 and the apparatus was started, each temperature control device 22 controlled by the control device 15 caused the heaters 16, 20 to generate heat and sensed by each temperature The device 14 feeds back the temperature information in the heat treatment furnace 11 and the hydrogen storage device 12 to the control device 15, whereby the temperature guaranteed paper in the heat treatment furnace 11 and the hydrogen storage device 12 in the pressure vessel 17 can be applied to the Chinese National Standard (CNS) A 4 specifications (210 X 297 mm) 〇. &Lt; Please read the precautions on the back before writing this page)-Pack. Order. 205572 A6 _B6_ V. Description of invention (2 5) (Please read the precautions on the back first Please fill out this page again) Keep at a certain temperature. Therefore, the control device 15 opens the on-off valve of the pressure adjusting device 44, and the hydrogen gas is supplied from the control device 15 to the heat treatment furnace 11 in a state where the pressure of the hydrogen gas is maintained in the latra due to the action of the pressure reducing valve of the pressure yoke device 44 . Due to the above operation, the absorption process of absorbing hydrogen in the metal material W occurs in the heat treatment furnace 11. Absorb hydrogen in metallic materials! After the absorption process in ί is completed, the control device 15 closes the on-off valve of the pressure regulating device 44 to activate the vacuum exhaust device S 43, thereby absorbing the hydrogen in the heat treatment vessel 11 and sending it to the hydrogen storage device 12. In this way, the pressure in the heat treatment Lu 11 is decompressed and the pressure in the hydrogen storage device 12 is increased, and the phenomenon of hydrogen evolution occurs in the heat treatment furnace 11, and the hydrogen absorption phenomenon occurs in the hydrogen absorption alloy M of the hydrogen storage device 12. . As a result, the dehydrogenation treatment of the metal material W occurs in the heat treatment furnace 11, and the hydrogen gas discharged from the metal material W is recovered to the hydrogen absorption alloy M of the hydrogen storage device 12 through the exhaust passage 41. Printed by the Employee Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economy. If the heat treatment is repeated due to repeated heat treatment, or the amount of hydrogen is reduced by opening the device to the atmosphere during maintenance, etc., according to this embodiment, the opening and closing valve 46 will be required. The amount of hydrogen is replenished from the hydrogen pin bottle 45 into the device. The heat conditions and pressure conditions during the above heat treatment are substantially the same as those in the above-mentioned embodiment, and the characteristics of the gold-thorium material W after the heat treatment are also substantially the same as in the above-mentioned embodiment. In the heat treatment of this embodiment, the hydrogen used in the heat treatment is also hydrogen. The paper size is applicable to the Chinese National Standard (CNS) A 4 specifications (210 X 297 mm) 205572 A6 B6 Printed by Beigong Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs V. Description of the invention (26) The storage device 12 and the heat treatment furnace 11 are given and received, which can suppress the leakage to the outside of the device, so the amount of hydrogen used is very small. In addition, in this embodiment, since the hydrogen in the heat treatment furnace 11 is directly sent to the hydrogen storage device 12, the decompression in the heat treatment furnace 11, the pressurization in the hydrogen storage device 12, and the hydrogen can be sent simultaneously The operation in the hydrogen storage device 12 thereby simplifies its operation. Furthermore, since the pressure adjusting device 44 is provided in the supply path 42, the pressure of the hydrogen gas supplied from the hydrogen storage device 12 to the heat treatment furnace 11 can be controlled with high accuracy, and stable heat treatment can be performed. The heat treatment apparatus according to the fourth embodiment of the present invention will be described below with reference to FIG. In the meantime, 50 is the heat treatment device of the metal material W of this embodiment. The heat treatment device 50 includes: a plurality of seats (two seats in this embodiment) for performing hydrogen gas absorption treatment for absorbing hydrogen gas in the metal material W, and hydrogen gas release treatment for releasing hydrogen gas in the metal material W that absorbs hydrogen gas Heat treatment furnace ll (lla, lib); a hydrogen storage device 12 made of hydrogen absorbing alloy M that stores the hydrogen gas supplied to or discharged from the heat treatment furnace ll (lla, lib); connects each heat treatment The furnace 11 (lla, Ub) and the hydrogen storage device 12 form a plurality of communication paths 53 (53a, 53b) for a general closed loop of hydrogen flow therebetween; selectively connect one of these communication paths 53 (53a, 53b) The conversion device 54 in the gas storage device 12 is provided on the heat treatment furnace 11 and the hydrogen storage device 12 to detect the internal pressure and internal temperature of the pressure sensor 13 and the temperature sensor 14; according to each The detection signals of the sensors 1 3, 1 4 adjust the internal pressure or temperature of the heat treatment furnace 11 and the hydrogen storage device 12, thereby supplying hydrogen to the heat treatment furnace 11 or from the V (Notes to fill out this page)-installed. Order · Izumi. The paper size is in accordance with the Chinese National Standard (CNS) A 4 specifications (210 X 297 mm) 26 A6 B6 V. Description of invention (2 7) V 'Please read the notes on the back before filling this page ) A control device 15 for discharging hydrogen from the heat treatment furnace 11. The structure of each device is the same as that of the above-mentioned embodiment, so its description is omitted. A pressure control device 55 for controlling the pressure in the hydrogen gas storage device 12 and the heat treatment furnace 11 is provided in the middle of the communication pipe 53 connected to the pressure vessel 17. The pressure control device 55 is connected to the two communication paths 53 (53a, 53b) via the conversion device 54, and due to the function of the conversion device 54, selectively communicates with each heat treatment furnace 11 or via the communication path 53 (53a, 53b) The communication with each heat treatment furnace 11 is cut off; and the communication with the hydrogen storage device 12 is cut off through the on-off valve 56 provided in the communication path 53. The pressure control device 55 selectively communicates with each heat treatment furnace 11 (Ua, lib) and pressure vessel 17 via the control device 15; by enlarging the volume of the interconnected components, each heat treatment furnace 11 (lla, lib) or pressure The pressure in the container 17 is reduced to absorb the hydrogen inside, and the pressure in each heat treatment furnace 11b or the pressure container 17 is increased by reducing its volume, and the hydrogen is sent into it. Each heat treatment furnace 11 (lla, lib) is provided with the same temperature control device 22 (22a, 22b) as the hydrogen storage device 12. The temperature control devices 22 (22a, 22b) are connected to the control device 15, and according to the control signal generated by the control device 15, the electric power supplied to each heater 16, 20 is controlled and printed by the employee consumer cooperative of the Ministry of Economic Affairs flow. The following describes an example of a skeleton when heat treatment of the gold material W is performed in the heat treatment device 50 of the present embodiment having the above-mentioned structure. [Experimental Example 7] As in Experimental Example 4, a metal material W composed of an R-Fe-B alloy having the compositions shown in Tables 1 to 4 was produced. Put the metal material W in a hot place. The paper size is in accordance with the Chinese National Standard (CNS) A 4 specifications (210 X 297 mm) 27 205572 Printed instructions issued by the Employee Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs. Install the storage gas hydrogen and a 1X 11 furnace heat treatment after the heat starts to start a 1X 1X ember m: the management department drive 11 will be suspected 15 management 12 disposal disposal installed hot installation system will be stored and controlled, stored and guaranteed After holding the letter of approval, the letter about the temperature will start after the start of hydrogen. The valve is closed, and the temperature is set to the temperature to be set. The temperature of the valve is 56. The 7th of the valve is closed. The control 55 controls the installation pressure and the control 53 control circuit is connected to the connection and the connection is disconnected. 2 J 1 is set to be installed and stored. The storage and protection gas is turned on by the hydrogen 54, and the hydrogen is installed and replaced. The hydrogen is controlled by a low pressure drop. The pressure is controlled by the pressure. 12 devices are installed and stored. After storage, hydrogen will be supplied to the letter 33. 5 IX will be installed and the S control gold will be collected. After closing, the gas will be sucked in. 55 hydrogen will be installed. To store and collect hydrogen, get hydrogen out. Please read the precautions on the back before filling in this page.) Borrowed as c, an ^ 33 4 5 installation and conversion and juxtaposition installation control pressure and a 11X 1X heat treatment installation control pressure on the supply signal control will 5 1X installation control installation 11 Furnace control force pressure autoclave Bt heat treatment to the absorption of the outflowing hydrogen in the high-lift pressure part a a heat treatment area into the gas supply hydrogen absorption key 15 treatment location installed heating, time control so far The feedback will be used to install the 12th, and the hydrogen will be stored and stored in parallel. Pick up the 3 IX device to measure the pressure and control the pressure in the pressure control unit. The pressure control signal is fed back. This is based on the pressure of the pressure gas hydrogen. A 1A 1X furnace RE treatment heat will be able to use this amount to move tm. About 55 of la is placed to support the supply of gas and hydrogen to 83 after the installation is complete. This adjustment is as small as 15 when placed at the time of large installation. 1 and 1 belong to tiao sui-m: handle hot gold and gold Yu will receive, inhale P gas, 3 hydrogen, and use this system to ensure that the temperature is within the temperature of the material. This paper standard is applicable to the Chinese National Standard (CNS) A 4 specifications (210 X 297 public) 28 A6 B6 2055 ^ 2 V. Description of the invention (29) Then, while maintaining the temperature in the heat treatment furnace 11a at 830C and the temperature of the hydrogen storage device 12 at 1010, the control signal is supplied to the pressure control device 55 so that The pressure control device 55 attracts the gas in the heat treatment furnace 11a. In this way, the pressure in the heat treatment furnace 11a is reduced, whereby the hydrogen absorbed in the metal material W is released, and the hydrogen is absorbed into the pressure control device 55, thereby dehydrogenating the gold tantalum material W. At this time, the pressure in the heat treatment furnace 11a is controlled by the operation amount of the pressure control device 55 driven by the pressure sensor 13 and the control device 15 to be maintained at 1 X 10 µ Torr hL. Then, the drive signal generated by the control device 15 causes the conversion device 54 to operate, cuts off the communication between the pressure control device 55 and a heat treatment furnace Ua, and opens the on-off valve 56, and then, operates the pressure control device 55, thereby The pressure of the hydrogen that is attracted by the pressure control device 55 to the hydrogen storage device 12 (please read the precautions on the back and then fill out this page) 丨 Install, order _ 内 7 1Α Rong Gaosheng and follow the instructions on the gold pressure The hydrogen in the gas is absorbed by the combined gas, and the hydrogen 17 is pressed in by the gas capacity of the device. When sending it, it will be retracted and sucked. The vacuum is pumped into the inside.-The bed_ is the same as the 11 furnace. , The heat inside the lb set I installed diagram is not used f, the material is expected to be gold

爐 j 理 處 熱 該 入 搬 W 經濟部中央標準局员工消費合作社印製 氫熱 従 一 55DR 置將 裝 , 制作 控動 ] 4 力 5 壓置 , 裝 時換 度轉 溫得 定使 特 , 於氣 持氫 保收 度吸 JI 2 溫 1 内置 爐裝 將收 作吸 操氣 1 後 爐然 m: 理 處 置 裝 收 吸 氣 氫 於 通 i- 遶 入 送 氣 氫 之 中 其 將 作 33 始 開 5 5 置 裝 制 控 力 壓 收 爐吸 理氣 處氫 熱之 1 同 另相 b ixFurnace j Handle the heat and move it W The Ministry of Economic Affairs, Central Standards Bureau, Employee Consumer Cooperative Printed a 55DR Hydrogen Heater, install it, make the control] 4 force 5 pressure, change the temperature during installation and change the temperature must be special, good for gas Hold the hydrogen retention to absorb JI 2 temperature 1 The built-in furnace will be taken as the suction gas 1 After the furnace m: Dispose and collect the suction hydrogen in the pass i- around the supply hydrogen It will be 33 start 5 5 Install the system control pressure pressurizing furnace to absorb the hydrogen gas at the place where the heat is the same as the other phase b ix

In: 理 處 述 上 與 11 xi 進 内 b 1A i—A 瀘 ITT: 理 處 熱 一 另 該 在 本紙張尺度適用中國國家標準(CNS)甲4規格(210 X 297公釐) 29 A6 e&amp;^ia-^- 五、發明説明(3 q) {請先閲讀背面之注意事項再填寫本頁) 在另一熱處理爐lib中進行氫氣吸收處理之期間内, 熱處理爐11a中正在進行已完成熱處理之金屬材料W之冷却 ,搬出,或搬入新金屬材料W之操作。 反覆的進行以上操作,即可在各熱處理爐Ua, lib中 交替的進行金靥材料W之熱處理。 經過以上處理後,上述各組成之Na-Fe-B合金被粉碎 成400/im以下,而且在粉末内部具有由〇.2〜〇.4wm之 Nd2Fel4B之再結晶粒所構成之組織,並且具有所需之磁特 性。 如上所述,本實施例之熱處理裝置50中,將金靥材料 W之熱處理時使用之氫氣在氫氣儲存裝置12與各熱處理嫌 ll(lla, lib)之間授受,藉此可抑制放出於裝置外之氫氣 ,故可大幅度的減少氫氣使用量,而且不需要排氣處理用 設備,故可防止裝置形狀大型化及防止設備費之增加。 因為可將2座熱處理爐11錯開其處理循環蓮轉,藉此 將1座所需之氬氣交替的在各熱處理爐11中使用,因此, 卽使增設熱處理爐11時亦不會增加氫氣使用量,而且可防 止裝置之大型化。 經濟部中央標準局貝工消費合作社印製 此外,因為作為氫氣儲存裝置12使用之氬氣吸收合金 Μ與同容量之習用之氫氣鏑瓶比較,具有3倍至4倍之氫氣 儲存_力,故更可使裝置小型化。 表5中之左欄表示本實施例之熱處理裝置50中,將氫 氣儲存裝置12之初期氫氣儲存量設定為35Nra3,對具有上 述各組成之金屬材料W分別進行1 0 -大處理後,測定氫氣減 &quot;本紙張尺度適用中國國家標準(CNS)甲4規格(210 X 297公釐) ^ 205572 A6 B6_ 五、發明説明(3 Μ V'請先閲讀背面之注意事項再填寫本頁) 少量之結果。表5中之右橱表示為了比較而利用習用裝置 對同樣之各金羼材料w進行熱處理時之氫氣減少量之結果 〇 由表中可知,依照本實施例,幾乎無氫氣之減少,其 效果極大。 [實驗例8 ] 使用與實驗例5相同之Ti合金作為金屬材料W,在與實 驗例7相同之條件下進行該金靥材料W之脱氫處理。經過這 種處理之結果,製成具有粗大相之Ti合金。這種組 成之Ti合金具有優異之高循環疲勞強度及耐蠕變待性。此 時,熱處理所使用之氫氣亦在氫氣儲存裝置12與熱處理爐 11之間被授受,藉此防止氫氣洩漏至裝置外。 表6中之左稱表示利用初期狀態之氫氣儲存量為35Nm3 之本實施例之裝置對各種Ti合金分別進行20次處理後,測 定氫氣減少量之結果。表6中之右橱表示為了比較而利用 習用之裝置對本實施例之各種Ti合金進行熱處理時之氫氣 減少量。 由表中可知,本實施例中亦無氫氣之減少,與習用裝 置比較,有大幅度之改進。 經濟部中央標準局貝工消費合作杜印製 以下參照圖8說明本發明第5實施例之變更實施例之熱 處理裝置。以下說明中,與第4實施例相同之構件以相同 記號表示而省略其說明。 本實施例之金羼材料之熱處理裝置60包括:用來進行 將氫氣吸收於金屬材料W中之氫氣吸收處理,及從吸收氫 本紙張尺度適用中國國家標準(CNS)甲4規格(210 X 297公釐) A6 B6 2055^2 五、發明説明(3 2 ) 氣之金屬材料中放出氫氣之氫氣放出處理之許多熱處理爐 ll(lla, lib);用來儲存供給於熱處理爐’ll(lla, Ub)及 從熱處理嫌排出之氫氣之氫氣吸收合金Μ所構成之氫氣儲 存裝置12;連通各熱處理爐ll(lla, lib)與氫氣儲存裝置 12,而且將各熱處理爐(11a, 11b)放出之氩氣送入氫氣儲 存裝置12中之排氣通路61(61a, 61b);將氫氣從氫氣儲存 裝置12供給於各熱處理爐ll(lla, lib)中之供給通路62( 62a, 62b);連設於排氣通路61(61a, 61b)再吸收各熱處 理爐11 (11a, lib)中之氣體並將之送入氫氣儲存裝置12之 真空排氣裝置63;連設於供給通路62(62a, 62b)而調節供 給於各熱處理爐ll(lla, 11b)之氫氣壓力之壓力調節裝置 64;將許多排氣通路61(61a, 61b)及供給通路62(62a, 62b)中之一選擇性的連通於氫氣儲存装置12之轉換裝置65 ;分別設在各熱處理爐lib)及氫氣儲存裝置12, 用來檢測其内部壓力及内部溫度之壓力感测器1 3及溫度感 測器1 4 ;根據各感測器1 3 , 1 5所産生之檢測信號調節各熱 處理爐ll(lla, lib)及氫氣儲存裝置12之溫度及真空排氣 裝置63之動作,藉此配合各熱處理鱸ll(lla, lib)之處理 狀態將氫氣供給於各熱處理瀘ll(lla, lib)及從各熱處理 爐中排出之控制裝置15。 各真空排氣裝置63(63a, 63b)可使用例如真空泵,其 前後設有開閉閥。本實施例中,於各熱處理爐ll(lla, lib)上皆設有真空排氣裝置,其各吸引部連結於各熱處理 Mll(lla, lib),而排氣部經由轉換裝置65連接於氫氣儲 本紙張尺度適用中國國家標準(CNS)甲4規格(210 X 297公釐) C請先閲讀背面之注意事項再塡寫本頁) 丨裝. 訂. 經濟部中央樣準局员工消费合作社印製 32 Α6 Β6 ?05δ7: 五、發明説明(3 3) 存裝置12。形成於其間之排氣通路61保持氣密性。 本實施例中,於各熱處理爐ll(lla/llb)皆設有壓力 調節裝置6 4 ( 64a, 64b),而且分別設有開閉閥及減壓閥。 平常係由開閉閥關閉供給通路62而切斷氫氣儲存裝置12與 各熱處理鑪ll(lla, lib)之連通。若需要將氫氣供給於各 熱處理爐ll(lla, lib)時,傜利用減壓閥將供給於各熱處 理埔ll(lla, lib)之氫氣壓力保持於latm以下。圖8中, P為用來補償氫氣儲存裝置12内之壓力之追加壓力控制裝 置。 真空排氣裝置63,壓力調節裝置64不必每一座熱處理 爐11設置一個,可藉著增加轉換裝置65而兼用於許多座熱 處理爐1 1。 轉換裝置65包括:連結於設在每一熱處理爐11a, lib 之真空排氣裝置63a(63b)及壓力調節裝置64a(64b)之流路 轉換閥65a, 65b;及連結於該等流路轉換閥65a, 65b而將 之選擇性的連通於氫氣儲存裝置12之流路轉換閥65c所構 成,利·用該等流路轉換閥6 5 a,6 5 b,6 5 c之動作位置之組 合形成如下之4値糸統之氫氣流路: 經濟部中央標準局負工消費合作社印製 (i) 氫氣儲存裝置124流路轉換閥65c4流路轉換閥 65a —壓力調節裝置64a4熱處理鑪11a (ii) 熱處理瀘真空排氣裝置63a~&gt;流路轉換閥65a —流路轉換閥65c —氫氣儲存裝置12 (iii) 氫氣儲存装置12 —流路轉換閥65c —流路轉換閥 65b —壓力調節裝置64b4熱處理爐lib 本紙張尺度通用中國國家標準(CNS)甲4規格(210 X 297公釐) 33 A6 B6 經濟部中央標準局员工消費合作社印製 五、發明説明(34) (iv)熱處理爐llb~&gt;真空排氣裝置63b4流路轉換閥65 流路轉換閥65c4氫氣儲存裝置12 本實施例中,在流路轉換閥65c與氫氣儲存裝置12之 間經由開閉閥67裝設氫氣銷瓶66,以便在蓮轉初期填充氫 氣,或因洩漏等而減少氬氣時補充氫氣之用。 開閉閥67與真空排氣裝置63,壓力調節裝置64—起連 結於控制裝置15,而利用控制裝置15所産生之控制信號控 制其動作。 本實施例之熱處理裝置60中之處理對象金屬材料W與 上述實施例所述者相同。 本實施例之熱處理裝置S0中,將金属材料W收入熱處 理爐11a内而起動裝置後,由控制裝置15控制之各溫度控 制装置2 4使各加熱器1 6 , 2 0發熱,而且由各溫度感測器1 4 將各熱處理爐11及氫氣儲存装置12内之溫度資訊反饋至控 制裝置15,藉此將熱處理爐11及氫氣儲存裝置12之壓力容 器17内之溫度保持於特定溫度。 因此,各流路轉換閥65a, 65b, 65c被控制裝置驅動 而動作,形成(i)項所述之氫氣流路,將氫氣在由壓力調 節装置64a之減壓閥之作用保持其壓力於la tm以下之狀態 下,從氫氣儲存裝置12供給於熱處理瀘11a中。 由於以上操作,在熱處理爐11a内進行將氫氣吸收於 金屬材料W中之吸收處理。 將氫氣吸收於金靥材料中之吸收處理完畢之後,控 制裝置15使流路轉換閥65a動作,形成(ii)項所述之流路,71 /請先閱讀背面之注意事項再填寫本頁) •裝. 訂. 線. 本紙張尺度通用中國國家標準(CNS)甲4規格(210 X 297公坌) 經.濟部中央標準局貝工消費合作社印製 2055 竹 五、發明説明(3 5) 而且關閉壓力調節裝置64之開閉閥,並且使真空排氣裝置 63a動作,因而將熱處理爐lla内之氫氣吸收而將之送入氪 氣儲存裝置1 2中。 因此,將熱處理爐11a内之壓力降低,而將氫氣儲存 裝置12内加壓,在熱處理爐11内發生氫氣放出現象,在氣 氣儲存装置12之氫氣吸收合金Μ中發生氫氣之吸收現象。 結果,在熱處理爐11a内進行金屬材料W之脱氫處理, 並且使金屬材料W放出之氫氣經由排出通路61a被回收至氫 氣儲存裝置12之氫氣吸收合金Μ中。 以上之動作在兩座熱處理爐11a, lib中交替的進行, 而與上述實施例相同的,將儲存於單一之氫氣儲存裝置1 2 中之氬氣交替的在各熱處理瀘11a, lib中使用。 若因熱處理之反覆進行,或因檢修等而將裝置開放於 大氣中而使氫氣量減少時,本實施例中係使開閉閥67動作 而將所需量之氳氣從氫氣銷瓶66補充。 本實施例之熱處理時之熱條件及壓力條件等與上述實 施例大致相同,而經過熱處理後之金靥材料W之待性亦與 上述實施例大致相同。 本實施例之熱處理中,熱處理時使用之氳氣亦在氫氣 儲存裝置12與各熱處理爐ll(lla, lib)之間被授受而可抑 制洩漏至裝置外,故氫氣之使用量少,而且可由單一之氬 氣儲存裝置12供給一座熱處理燫所需之氫氣量使2座熱處 理瀘ll(lla, lib)蓮轉,因此可防止裝置之大型化。 本實施例中,因為將熱處理爐ll(lla, lib)内之氫氣 本紙張尺度適用中國國家標準(CNS)甲4規格(210 X 297公釐) Τΰ (請先閲讀背面之注意事項再塡寫本頁) -裝- 訂. 20诚2 A6 B6 經濟部中央標準局員工消費合作社印製 五、發明説明(3 6) 直接送入氫氣儲存裝置12中,故可同時進行熱處理嫌11内 之減壓,氫氣儲存裝置12内之加壓,及將氫氣送入氫氣儲 存裝置12中之動作,可簡化其操作条統。 又因為在供給通路62中設置壓力調節裝置64,故可非 常精確的控制從氫氣儲存裝置12供給於熱處理爐11中之氫 氣壓力,可進行穩定之熱處理。 上述實施例中,傜由真空排氣裝置63將氫氣儲存裝置 12内加壓。但亦可在真空排氣裝置63與氫氣儲存裝置12之 間設置加壓裝置,利用該加壓裝置將氫氣儲存裝置12内之 E力加以昇高。此方式在增加儲存於氫氣儲存裝置12内之 氫氣量時非常有效。 以上傺說明設置2座熱處理爐1 1之例。本發明不受其 限制,只要在熱處理爐11之製程循環不重叠之範圍内,則 可設置3座以上之熱處理爐11。 圖9表示本發明第6實施例之熱處理裝置70。該實施例 與圖6所示第3實施例不同之處僅為在排氣通路41上較真空 排氣裝置43更下游倒設置甩來精製流通於排氣通路41内之 氫氣之氫氣精製裝置76。因此,與圖6之實施例相同之部 份以相同記號表示而省略其說。 該熱處理裝置70之作用與圖6所示者大致相同,但隨 着真空排氣裝置43之動作,從熱處理燫11放出之氫氣經由 該氫氣精製裝置76被送入氫氣儲存裝置12之壓力容器17内 。因此,在通過氫氣精製裝置76之期間内將混入氫氣中或 包含氫氣之氣體中之不純物去除。依照本實施例,在氫氣 本紙張尺度適用中國國家標準(CNS)甲4規格(210 X 297公釐〉 ;請先閲讀背面之注意事項再填寫本頁) 丨装. *11. .,1線. A6 經濟部中央標準局貝工消费合作社印製 B6 五、發明説明(3 7) 被回收至氫氣儲存裝置之回收階段中,經由氫氣精製裝置 精製,故可防止再度使用氫氣時對金屬材'料tf之熱處理發 生不良影蜜。 圔10表示本發明第7實施例之熱處理裝置80。本實施 例與匾8所示第5實施例不同之處僅為在排氣路61(61a, 6 1 b )上較真空排氣發置6 3更下游側設置用來精製流動於排 氣通路61内之氫氣之氫氣精製裝置8 6 ( 8 6 a, 86b)。因此, 本例中與圖8所示實施例相同之部份以相同記號表示而省 略其說明。本裝置中,與上述實施例相同的,隨着真空排 氣裝置43之動作,從熱處理爐11放出之氫氣經由氫氣精製 裝置86被送入氫氣儲存裝置12之壓力容器17内,因此在通 過氫氣精製裝置86之期間内將混入氫氣中或包含氫氣之氣 髏中之不純物去除。 圖11表示使用熱處理燼作為氫氣回收裝置之本發明之 第8實施例。本實施例中之金屬材料之熱處理裝置210包括 :用來進行將氫氣吸收於金屬材料W中之氫氣吸收處理, 及從吸收氫氣之金屬材料W中放出氫氣之氫氣放出處理之 許多座(本實施例中為2座)熱處理爐A, B;連通熱處理爐 A與B而在各熱處理遽A與B間形成氫氣流通用閉迴路之連通 路211;設在連通路211之中途,在熱處理瀘A(B)進行氫氣 吸收處理時將其内部壓力昇高並且供給氫氣,而且在此等 熱處理爐A, B進行氫氣放出處理時將其内部壓力降低並且 排出氫氣之壓力控制裝置212。 本實施例中,各熱處理爐包括:在進行金靥材料W之 {請先閲讀背面之注意事項再填寫本頁) 裝- 訂 :4- 本紙張尺度適用中國國家標準(CNS)甲4規格(210 X 297公釐) 37 A6 B6 2055*^2 五、發明説明(3 8) 熱處理之前,先將之加熱之預熱室213;連通於該預熱213 以便進行金屬材料1/之氫氣吸收處理及氫氣放出處理之熱 處理室214;及連通於該熱處理室214以便將從熱處理室 214中送出之經過熱處理後之金羼材料W冷却之冷却室215 。各預熱室213,熱處理室214,及冷却室215可互相連通 及可予以屏蔽。與上述實施例相同的,各熱處理爐可使用 真空容器内具有由石墨,鎢或鉬等製成之加熱器之内熱式 處理爐,或真空容器外具有Kanthal或高純度磺化矽等加 熱器之外熱式處理爐。 連通路211將各熱處理爐A, B之熱處理室214連通,並 且在其中途設有壓力控制装置212,將兩個熱處理室214之 間氣密的連通,而在其間形成與大氣隔絶之氫氣之閉迴路 (請先閲讀背面之注意事項再填寫本頁) *ΤΓ- 造 構 之 積 容 其 減 增 可 有 具 2 2 置 裝 制 控 力 壓 與 且 可 如 例 造 構 之 體 氣 換 交 相 互 能 不 體 氣 之 部 外 置 裝 置 裝 κϋ $ 控 力 壓 之 IX 1Α 2 路 通 .1 遶 在 設 別 分 於 由 ο 等 缸 汽之 用 側 使兩 ,1線. 6 IX 2 0 ao 3a 開In: Dealing with the description and 11 xi into the b 1A i-A LuITT: Dealing with the heat should be in accordance with the Chinese National Standard (CNS) A 4 specifications (210 X 297 mm) 29 A6 e &amp; ^ ia-^-V. Description of the invention (3 q) {Please read the precautions on the back before filling in this page) During the hydrogen absorption treatment in another heat treatment furnace lib, the heat treatment in the heat treatment furnace 11a is being completed The operation of cooling the metal material W, moving it out, or moving it in a new metal material W. By repeatedly performing the above operations, the heat treatment of the gold tantalum material W can be alternately performed in each heat treatment furnace Ua, lib. After the above treatment, the Na-Fe-B alloy of the above composition is crushed to 400 / im or less, and has a structure composed of recrystallized particles of Nd2Fel4B of 0.2 ~ 0.4wm inside the powder, and has the Required magnetic properties. As described above, in the heat treatment device 50 of the present embodiment, the hydrogen gas used in the heat treatment of the gold tantalum material W is transferred between the hydrogen storage device 12 and each heat treatment material (lla, lib), thereby suppressing release from the device The external hydrogen can greatly reduce the amount of hydrogen used, and does not require exhaust treatment equipment, so it can prevent the device from becoming large in size and increasing the equipment cost. Because the two heat treatment furnaces 11 can be staggered in their treatment cycles, thereby using one of the required argon gas alternately in each heat treatment furnace 11, therefore, the addition of the heat treatment furnace 11 will not increase the use of hydrogen Quantity, and can prevent the device from becoming large. Printed by Beigong Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economy. In addition, because the argon absorption alloy M used as the hydrogen storage device 12 has a hydrogen storage capacity of 3 to 4 times compared with the conventional hydrogen dysprosium bottle of the same capacity, so The device can also be miniaturized. The left column in Table 5 shows that in the heat treatment device 50 of this embodiment, the initial hydrogen storage amount of the hydrogen storage device 12 is set to 35 Nra3, and the metal materials W having the above-mentioned compositions are subjected to 10-large treatments respectively, and then the hydrogen is measured. Minus &quot; This paper scale is applicable to the Chinese National Standard (CNS) A 4 specifications (210 X 297 mm) ^ 205572 A6 B6_ V. Invention description (3 Μ V'Please read the precautions on the back before filling this page) A small amount result. The right cabinet in Table 5 shows the results of the reduction in hydrogen when the same Jinjin materials w are heat-treated using conventional equipment for comparison. From the table, it can be seen that according to this embodiment, there is almost no reduction in hydrogen, and the effect is extremely great . [Experimental Example 8] The same Ti alloy as Experimental Example 5 was used as the metal material W, and the dehydrogenation treatment of the gold-solarium material W was performed under the same conditions as in Experimental Example 7. As a result of this treatment, a Ti alloy with a coarse phase is produced. The Ti alloy of this composition has excellent high cycle fatigue strength and creep resistance. At this time, the hydrogen used in the heat treatment is also transferred between the hydrogen storage device 12 and the heat treatment furnace 11, thereby preventing the hydrogen from leaking out of the device. The left-hand name in Table 6 shows the results of measuring the amount of hydrogen reduction after various treatments of Ti alloys were carried out 20 times with the apparatus of the present embodiment in which the hydrogen storage amount in the initial state was 35 Nm3. The right cabinet in Table 6 shows the amount of hydrogen reduction when various Ti alloys of this example were heat-treated using conventional equipment for comparison. As can be seen from the table, there is no reduction of hydrogen in this example, which is a significant improvement compared to conventional devices. Printed by Beigong Consumer Cooperation, Central Bureau of Standards, Ministry of Economic Affairs The following describes a heat treatment apparatus according to a modified embodiment of the fifth embodiment of the present invention with reference to FIG. 8. In the following description, the same components as in the fourth embodiment are denoted by the same symbols, and their descriptions are omitted. The heat treatment device 60 of the Jinjin material of this embodiment includes: a hydrogen absorption process for absorbing hydrogen in the metal material W, and the Chinese national standard (CNS) A4 specifications (210 X 297 Mm) A6 B6 2055 ^ 2 5. Description of the invention (3 2) Many heat treatment furnaces ll (lla, lib) for releasing hydrogen from the metal material of the gas; used to store and supply the heat treatment furnace'll (lla, Ub) and hydrogen storage device 12 composed of hydrogen absorption alloy M of hydrogen discharged from the heat treatment; connect each heat treatment furnace 11 (lla, lib) and hydrogen storage device 12, and release each heat treatment furnace (11a, 11b) Argon gas is fed into the exhaust passage 61 (61a, 61b) in the hydrogen storage device 12; the hydrogen is supplied from the hydrogen storage device 12 to the supply passage 62 (62a, 62b) in each heat treatment furnace 11 (lla, lib); The exhaust passage 61 (61a, 61b) re-absorbs the gas in each heat treatment furnace 11 (11a, lib) and sends it to the vacuum exhaust device 63 of the hydrogen storage device 12; connected to the supply passage 62 (62a, 62b) and adjust the hydrogen pressure supplied to each heat treatment furnace 11 (lla, 11b) Pressure regulator 64; one of the many exhaust passages 61 (61a, 61b) and supply passages 62 (62a, 62b) is selectively connected to the conversion device 65 of the hydrogen storage device 12; respectively provided in each heat treatment furnace lib) And hydrogen storage device 12, a pressure sensor 1 3 and a temperature sensor 1 4 for detecting its internal pressure and internal temperature; each heat treatment furnace is adjusted according to the detection signal generated by each sensor 1 3, 15 (lla, lib) and the temperature of the hydrogen storage device 12 and the operation of the vacuum exhaust device 63, thereby supplying hydrogen to each heat treatment Lull (lla, lib) and Control device 15 discharged from each heat treatment furnace. For each vacuum exhaust device 63 (63a, 63b), for example, a vacuum pump can be used, and opening and closing valves are provided at the front and back. In this embodiment, each heat treatment furnace ll (lla, lib) is provided with a vacuum exhaust device, each suction part is connected to each heat treatment Mll (lla, lib), and the exhaust part is connected to hydrogen through a conversion device 65 The size of the reserve paper is in accordance with the Chinese National Standard (CNS) Grade A (210 X 297 mm). C Please read the precautions on the back before writing this page) 丨 Installed. Ordered. Printed by the Employee Consumer Cooperative of the Central Bureau of Samples of the Ministry of Economic Affairs System 32 Α6 Β6? 05δ7: V. Description of the invention (3 3) Storage device 12. The exhaust passage 61 formed therebetween maintains airtightness. In this embodiment, each heat treatment furnace 11 (lla / llb) is provided with a pressure adjusting device 64 (64a, 64b), and is provided with an on-off valve and a pressure reducing valve, respectively. Normally, the supply path 62 is closed by an on-off valve to cut off the communication between the hydrogen storage device 12 and each heat treatment furnace 11 (lla, lib). If it is necessary to supply hydrogen to each heat treatment furnace 11 (lla, lib), Meng uses a pressure relief valve to keep the pressure of hydrogen supplied to each heat treatment furnace 11 (lla, lib) below latm. In FIG. 8, P is an additional pressure control device for compensating the pressure in the hydrogen storage device 12. The vacuum exhaust device 63 and the pressure adjusting device 64 do not need to be provided for each heat treatment furnace 11, and can be used for many heat treatment furnaces 11 by adding a conversion device 65. The switching device 65 includes: flow path switching valves 65a, 65b connected to a vacuum exhaust device 63a (63b) and a pressure regulating device 64a (64b) provided in each heat treatment furnace 11a, lib; and connected to these flow path switches The valves 65a, 65b are selectively connected to the flow path switching valve 65c of the hydrogen storage device 12, and the combination of the operating positions of these flow path switching valves 6 5 a, 6 5 b, 6 5 c The following 4 hydrogen flow paths are formed: Printed by the Consumer Labor Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs (i) Hydrogen storage device 124 flow path switching valve 65c4 flow path switching valve 65a — pressure regulator 64a4 heat treatment furnace 11a (ii ) Heat treatment Lu vacuum exhaust device 63a ~> flow path switching valve 65a-flow path switching valve 65c-hydrogen storage device 12 (iii) hydrogen storage device 12-flow path switching valve 65c-flow path switching valve 65b-pressure regulating device 64b4 Heat Treatment Furnace lib This paper scale is in accordance with the Chinese National Standard (CNS) A 4 specifications (210 X 297 mm) 33 A6 B6 Printed by the Employee Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs V. Invention Instructions (34) (iv) Heat Treatment Furnace llb ~ &gt; 63b4 flow path conversion of vacuum exhaust device 65 Flow path switching valve 65c4 Hydrogen storage device 12 In this embodiment, a hydrogen pin bottle 66 is installed between the flow path switching valve 65c and the hydrogen storage device 12 via an on-off valve 67, so as to fill the hydrogen at the initial stage of the lotus transfer, or due to leakage It is used to supplement hydrogen when reducing argon. The on-off valve 67 is connected to the control device 15 together with the vacuum exhaust device 63 and the pressure adjusting device 64, and its operation is controlled by the control signal generated by the control device 15. The metal material W to be processed in the heat treatment apparatus 60 of this embodiment is the same as that described in the above embodiment. In the heat treatment device S0 of this embodiment, after the metal material W is stored in the heat treatment furnace 11a and the device is started, each temperature control device 24 controlled by the control device 15 causes the heaters 16 and 20 to generate heat, and each temperature The sensor 14 feeds back the temperature information in each heat treatment furnace 11 and hydrogen storage device 12 to the control device 15, thereby maintaining the temperature in the pressure vessel 17 of the heat treatment furnace 11 and hydrogen storage device 12 at a specific temperature. Therefore, each of the flow path switching valves 65a, 65b, 65c is driven and operated by the control device to form the hydrogen flow path described in (i), and maintains the pressure of the hydrogen at la by the pressure reducing valve of the pressure adjusting device 64a In a state of tm or less, the hydrogen storage device 12 is supplied to the heat treatment lure 11a. Due to the above operations, the absorption process of absorbing hydrogen gas in the metal material W is performed in the heat treatment furnace 11a. After the absorption process of absorbing hydrogen in the gold material is completed, the control device 15 actuates the flow path switching valve 65a to form the flow path described in item (ii), 71 / please read the precautions on the back before filling this page) • Binding. Binding. Line. This paper scale is in accordance with the Chinese National Standard (CNS) A 4 specifications (210 X 297 gong). The Ministry of Economic Affairs, Central Standards Bureau, Beigong Consumer Cooperative Printed 2055 Bamboo Five, Invention Instructions (3 5) Furthermore, the on-off valve of the pressure regulator 64 is closed, and the vacuum exhaust device 63a is operated, so that the hydrogen in the heat treatment furnace 11a is absorbed and sent to the krypton gas storage device 12. Therefore, the pressure in the heat treatment furnace 11a is lowered, and the hydrogen storage device 12 is pressurized. Hydrogen evolution occurs in the heat treatment furnace 11, and a hydrogen absorption phenomenon occurs in the hydrogen absorption alloy M of the gas storage device 12. As a result, the dehydrogenation treatment of the metal material W is performed in the heat treatment furnace 11a, and the hydrogen gas released from the metal material W is recovered into the hydrogen absorption alloy M of the hydrogen gas storage device 12 through the discharge path 61a. The above operations are carried out alternately in the two heat treatment furnaces 11a, lib, and in the same way as the above embodiment, the argon gas stored in the single hydrogen storage device 12 is used alternately in each heat treatment Lu 11a, lib. If the heat treatment is repeated, or the device is opened to the atmosphere due to maintenance or the like to reduce the amount of hydrogen, in this embodiment, the on-off valve 67 is operated to supplement the required amount of radon gas from the hydrogen pin 66. The heat conditions and pressure conditions at the time of heat treatment in this embodiment are almost the same as those in the above-mentioned embodiment, and the hospitality of the gold tantalum material W after the heat treatment is also almost the same as in the above-mentioned embodiment. In the heat treatment of this embodiment, the radon gas used in the heat treatment is also conferred between the hydrogen storage device 12 and each heat treatment furnace 11 (lla, lib) to suppress leakage to the outside of the device, so the amount of hydrogen used is small, and the A single argon gas storage device 12 supplies the amount of hydrogen required for one heat treatment device to make two heat treatment devices (lla, lib) turn, thus preventing the device from becoming large. In this embodiment, because the hydrogen in the heat treatment furnace ll (lla, lib) is based on the paper standard of China National Standard (CNS) A 4 specifications (210 X 297 mm) Τΰ (please read the precautions on the back before writing This page) -Installation- Ordering. 20 Cheng 2 A6 B6 Printed by the Employee Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economy 5. Description of the invention (3 6) Directly sent to the hydrogen storage device 12, so the heat treatment can be reduced within 11 The pressure, the pressurization in the hydrogen storage device 12, and the action of sending hydrogen into the hydrogen storage device 12, can simplify the operating system. In addition, since the pressure adjusting device 64 is provided in the supply path 62, the pressure of the hydrogen gas supplied from the hydrogen storage device 12 into the heat treatment furnace 11 can be controlled very accurately, and stable heat treatment can be performed. In the above embodiment, the vacuum exhaust device 63 pressurizes the hydrogen storage device 12. However, a pressurizing device may be provided between the vacuum exhaust device 63 and the hydrogen storage device 12, and the E force in the hydrogen storage device 12 may be increased by the pressurizing device. This method is very effective in increasing the amount of hydrogen stored in the hydrogen storage device 12. The above description describes an example in which two heat treatment furnaces 11 are provided. The present invention is not limited thereto, as long as the process cycles of the heat treatment furnace 11 do not overlap, more than three heat treatment furnaces 11 may be provided. Fig. 9 shows a heat treatment apparatus 70 according to a sixth embodiment of the present invention. This embodiment differs from the third embodiment shown in FIG. 6 only in that a hydrogen refining device 76 is disposed on the exhaust passage 41 further downstream than the vacuum exhaust device 43 to refine hydrogen flowing in the exhaust passage 41 . Therefore, the same parts as those in the embodiment of Fig. 6 are denoted by the same symbols and their explanations are omitted. The function of the heat treatment device 70 is substantially the same as that shown in FIG. 6, but with the action of the vacuum exhaust device 43, the hydrogen gas released from the heat treatment device 11 is sent to the pressure vessel 17 of the hydrogen storage device 12 through the hydrogen purification device 76 Inside. Therefore, impurities that are mixed into the hydrogen gas or the hydrogen-containing gas are removed while passing through the hydrogen purification device 76. According to this embodiment, the Chinese National Standard (CNS) A4 specifications (210 X 297 mm) are applicable to the hydrogen paper standard; please read the precautions on the back before filling out this page) 丨 Install. * 1., 1 line . A6 Printed by the Beigong Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs. B. V. Description of the invention (3 7) Recovered in the recovery stage of the hydrogen storage device, refined by the hydrogen refining device, so it can prevent metal materials from being used again. Undesirable shadow honey occurs during the heat treatment of the material tf. The numeral 10 shows a heat treatment apparatus 80 according to the seventh embodiment of the present invention. This embodiment differs from the fifth embodiment shown in plaque 8 only in that the exhaust path 61 (61a, 6 1 b) is provided on the downstream side of the vacuum exhaust device 6 3 for refining the flow in the exhaust path Hydrogen refining device for hydrogen in 61 8 6 (8 6 a, 86b). Therefore, in this example, the same parts as those in the embodiment shown in FIG. 8 are indicated by the same symbols, and the description is omitted. In this device, as in the above embodiment, with the action of the vacuum exhaust device 43, the hydrogen gas discharged from the heat treatment furnace 11 is sent to the pressure vessel 17 of the hydrogen storage device 12 through the hydrogen refining device 86. During the period of the refining device 86, impurities contained in hydrogen gas or gas skeletons containing hydrogen gas are removed. Fig. 11 shows an eighth embodiment of the present invention using heat-treated ash as a hydrogen recovery device. The metal material heat treatment device 210 in this embodiment includes: a plurality of seats for performing hydrogen absorption processing for absorbing hydrogen in the metal material W, and hydrogen release processing for releasing hydrogen from the hydrogen-absorbing metal material W (this embodiment In the example, two) heat treatment furnaces A and B; a communication path 211 connecting the heat treatment furnaces A and B to form a general closed loop of hydrogen flow between each heat treatment A and B; provided in the middle of the communication path 211, in the heat treatment Lu A (B) A pressure control device 212 that raises the internal pressure of the hydrogen absorption process and supplies hydrogen, and reduces the internal pressure of the heat treatment furnaces A and B during the hydrogen release process and discharges the hydrogen. In this embodiment, each heat treatment furnace includes: Before performing the gold material W (please read the precautions on the back before filling out this page) Binding-Order: 4- This paper size is applicable to China National Standard (CNS) A4 specifications ( 210 X 297 mm) 37 A6 B6 2055 * ^ 2 5. Description of the invention (3 8) The preheating chamber 213 which is heated before heat treatment; connected to the preheating 213 for the hydrogen absorption treatment of metal material 1 / And hydrogen treatment chamber 214 for releasing hydrogen gas; and a cooling chamber 215 connected to the heat treatment chamber 214 so as to cool the heat-treated gold material W sent from the heat treatment chamber 214. The preheating chamber 213, the heat treatment chamber 214, and the cooling chamber 215 can communicate with each other and can be shielded. As in the above embodiments, each heat treatment furnace can use an internal heat treatment furnace with a heater made of graphite, tungsten or molybdenum in the vacuum container, or a heater such as Kanthal or high-purity sulfonated silicon outside the vacuum container Outside the heat treatment furnace. The communication path 211 connects the heat treatment chambers 214 of the heat treatment furnaces A and B, and a pressure control device 212 is provided in the middle of the two heat treatment chambers 214 to provide airtight communication between the two heat treatment chambers 214 and form a hydrogen gas isolated from the atmosphere Closed loop (please read the precautions on the back before filling in this page) * ΤΓ- The volume of the structure can be reduced by 2 2 installation control pressure and can be constructed as usual. The external device can be equipped with κϋ $ CONTROL PRESSURE IX 1Α 2 way through. 1 Winding on the side divided by ο equal cylinder steam use two, 1 line. 6 IX 2 0 ao 3a open

室 理 處 熱 之 B Α 室 爐理 理處 處熱 熱等 艏 此. 兩之 於通 通連 連被 的大 性龙 擇著 0 藉 用 一 作之 之中 經濟部中央標準局員工消費合作社印製 室 0t 理 處 熱 各 將 積 容 之 氣 氫 將 且 並 2 ,室 低理 減處 力熱 壓各 之將 内而 。 14小部 〜縮内 積其 容入 將吸 著氣 0 氫 ; 將 部並 内 , 其高 入昇 吸力 壓 之 内 IX 2 室 m: 理 處 熱 力示 壓圖 ,未 制由 控偽 之制 力控 壓作 部 動 内之 及17 度2 溫 δ 部21 内 之 行 進 序 順 及 力 壓 度 溫 之 定 設 先 預 照 依 置 裝 制 控 21等 置腦 各裝電 制徹 控之 閥 閉 開 各 及 本紙張尺度適用中國國家標準(CNS)甲4規格(210 X 297公釐) 38 A6 B6 2055^2 五、發明説明(39) 0 以下說明根據在具有上述結構之本實'施例之熱處理裝 置210中進行金鼷材料w之熱處理時之具體例,對具有上述 2種組成之金靥材料進行之2種實驗例。 [實驗例9 ] 使用具有表1〜表4所示組成之R-Fe-B合金作為熱處理 時使用之金屬材料W製作與實驗例1相同之材料。 將這種金靥材料W在具有外熱式Kanthal線加熱器之熱 處理燫A之預熱室213中,於真空狀態下予以預備加熱後, 並於真空狀態下於入熱處理室214内後,可將預熱室213與 熱處理室214氣密的屏蔽,開始進行熱處理室214之内部加 熱。 熱處理室2 1 4之内部溫度由其溫度感測器檢測而反饋 至控制裝置中,而根據該反饋信號將熱處理室214之内部 溫度保持於特定溫度(大約300t:)。 在蓮轉初期,從另外設置之未圖示之氫氣儲存裝置等 中將特定量之氫氣在特定壓力(大约latm)下送入熱處理爐 A之熱處理室214中。此時,熱處理爐A之熱處.理室214内之 内部壓力由壓力感測器檢測而反饋至控制裝置,根據該反 饋信號保持於上述壓力值。 如此完成氫氣供給後,由控制裝置熱處理爐A内之溫 度提舁至大約830它,將該金屬材料W在該溫度下大約保持 3小時,如此將氫氣吸收於金屬材料W中。 然後,在將熱處理爐Α内之溫度保持於830Ό之狀態下 本紙張尺度適用中國國家標準(CNS)甲4規格(210 X 297 :釐) „ 〇 {請先閲讀背面之注意事項再填寫本頁) -丨装— 訂 經濟部中央標準局負工消费合作社印製 A6 B6 經濟部中央標準局貝工消費合作社印製 五、發明説明(4〇 ) ,控制裝置將驅動信號供給於開閉閥216,使熱處理爐A之 熱處理室214連通,並且將驅動信號供給於壓力控制裝置 212而吸引熱處理燼A内之氣體。 如此,可將熱處理爐A内之壓力降低,而且將其内部 之氫吸收至壓力控制装置212,藉此,在熱處理爐A中將金 靥材料W所吸收之氫氣放出而進行金屬材料W之脱氫,而在 進行脫氫處理之後闊閉該開閉閥216,切斷熱處理爐A之熱 處理室214與壓力控制裝置212間之建通。 此時,熱處理燼A内之壓力由壓力感測器所産生之檢 測信號,及根據該檢測信號而由控制裝置控制之壓力控制 裝置212之動作量,保持於lxl〇-iTorr以下。 經過上述處理後,具有上述組成之Na-Fe-B合金被粉 碎成為400« m以下,而且在粉末内具有由0.2〜0.4w m之 Hd2Fel4B之再結晶粒所構成之組織,並且具有所需要之磁 待性。 當熱處理爐A中正在進行金屬材料W之氫氣放出處理之 同時,在熱處理燼B中將新金靥材料W予以預熱處理後將之 送入熱處理室214中,在熱處理室214中加熱至持定溫度, 成為可進行氫氣吸收處理之狀態。 因此,當控制裝置使開閉閥217開啓而使壓力控制裝 置212動作後,被該壓力控制裝置212吸引之氫氣在上述待 定壓力下披送入熱處理爐B之熱處理室214中,在熱處理燫 B中進行氫氣吸收處理。當該氫氣吸收處理完畢後,壓力 控制裝置212進行相反方向之動作,將送入熱處理瀘B中之 各紙張尺度適用中國國家標準(CNS)曱4规格(210 X 297公釐) &lt;請先閲讀背面之注意事項再填寫本頁) .装. .1T. -線. A6 ·〇5^2 _Β6_ 五、發明説明(4i 氫氣吸收而在熱處理爐Β中進行氫氣放出處理。 當熱處理爐Β完成金屬材料W之熱處理後,另一開閉閥 217關閉,切斷熱處理爐Β與壓力控制裝置212間之連通, 完成熱處理瀘Β中之金屬材料W之熱處理。 如上所述,在本實施例之熱處理裝置210中,將金羼 材料tf之熱處理時使用之氫氣在各熱處理爐A , Β之間經由 壓力調節裝置212予以授受,抑制氫氣放出於裝置外,故 可大幅度的減少氫氣使用量,而且不需要排氣處理設備, 故可避免裝置之形狀大型化及設備費之增加,而且在蓮轉 初期填充之1座熱處理爐用之氫氣量可供2座熱處理爐A, B運轉,故亦可防止裝置變成大型化。 將金屬材料W送入或送出各熱處理爐A, B時,例如在 送入或送出預熱室213及冷却室215與熱處理室214間時, 或在進行熱處理室214之真空排氣處理時,可能發生熱處 理時使用之氫氣洩漏至外部,反覆的進行熱處理之結果裝 置内之氫氣量減少之情事。但其減少量極少,即使其減少 量變成熱處理所需之量以下時,只需要補充該減少量即可 ,故氫氣儲存設備之容量亦不必太大。 本實施例之熱處理裝置210中,將初期之氫氣填充量 設定為35Hin3,對上述各組成之金靥材料W分別進行10次處 理後,測定其氫氣減少量,其結果與實驗例4相同。由該 結果可知,依照本實驗例,幾乎無氫氣之減少,其效果極 大。 [實驗例1 0 ] 本紙張尺度適用中國國家標準(CNS)甲4規格(210 X 297公釐) .. ,請先閲讀背面之注意事項再填寫本頁) .—裝- 訂 λ. 經濟部中央標準局S工消费合作社印製 五、發明説明(4 2) 例 驗 實 與 用 使 料 材 靥 , rfv w A 料爐 材理 屬 處 金熱 為之 作器 金熱 合加 T1墨 之石 同式 相熱 13 内 有 具 入 放 金 該 將 内 述於 上收 與吸 此氣 藉氫 , 將 件下 構境 各環 之圍 10周 2之 置m&lt; 裝at 0C ' - 理 處 ’ 熱 動 8 驅在 置的 裝同 制相 控例 用驗 利實B Α of the room management department, the heat of the furnace management department, and so on. The two are selected by the big dragons who are all in succession. The heat and gas will accumulate in the heat, and the heat pressure will be reduced within the room. 14 small parts ~ shrink it and accumulate it will be absorbed gas 0 hydrogen; will be part of the inside, which is higher than the suction pressure IX 2 Room m: handle the thermal pressure diagram, not controlled by the control of counterfeit control The operation in the press section and the temperature of 17 degrees 2 temperature δ The order of travel in the section 21 and the setting of the pressure and temperature are pre-charged according to the installation control 21 and the valve is installed in the brain and the electrical control is closed. And this paper scale is applicable to the Chinese National Standard (CNS) A 4 specifications (210 X 297 mm) 38 A6 B6 2055 ^ 2 V. Description of the invention (39) 0 The following description is based on the heat treatment in the "real-life" embodiment with the above structure As a specific example of the heat treatment of the gold-bearing material w in the device 210, two kinds of experimental examples were carried out on the gold-bearing material having the above two compositions. [Experimental Example 9] The R-Fe-B alloy having the composition shown in Table 1 to Table 4 was used as the metal material W used in the heat treatment to produce the same material as Experimental Example 1. After this kind of gold tantalum material W is pre-heated in the preheating chamber 213 of the heat treatment Supper A with an externally heated Kanthal wire heater under vacuum, and after entering the heat treatment chamber 214 under vacuum, it can be The preheating chamber 213 and the heat treatment chamber 214 are hermetically shielded, and heating of the inside of the heat treatment chamber 214 is started. The internal temperature of the heat treatment chamber 214 is detected by its temperature sensor and fed back to the control device, and the internal temperature of the heat treatment chamber 214 is maintained at a specific temperature (about 300t :) based on the feedback signal. In the early stage of the lotus turn, a specific amount of hydrogen gas is fed into the heat treatment chamber 214 of the heat treatment furnace A at a specific pressure (approximately latm) from a separately provided hydrogen storage device (not shown). At this time, the internal pressure in the heat treatment chamber A of the heat treatment furnace A is detected by the pressure sensor and fed back to the control device, and is maintained at the above-mentioned pressure value according to the feedback signal. After the hydrogen supply is completed in this way, the temperature in the heat treatment furnace A of the control device is raised to about 830, and the metal material W is maintained at this temperature for about 3 hours, thus absorbing hydrogen in the metal material W. Then, with the temperature in the heat treatment furnace A kept at 830Ό, this paper scale is applicable to the Chinese National Standard (CNS) A 4 specifications (210 X 297: PCT). ○ {Please read the precautions on the back before filling this page )-丨 installation- Ordered by the Ministry of Economic Affairs, Central Standards Bureau, Negative Work Consumer Cooperative to print A6 B6 Ministry of Economic Affairs, Central Standards Bureau, Beigong Consumer Cooperative Printed 5. Description of invention (4〇), the control device supplies the driving signal to the opening and closing valve 216, The heat treatment chamber 214 of the heat treatment furnace A is communicated, and the driving signal is supplied to the pressure control device 212 to attract the gas in the heat treatment ember A. In this way, the pressure in the heat treatment furnace A can be reduced and the hydrogen inside can be absorbed to the pressure The control device 212 releases the hydrogen absorbed by the gold tungsten material W in the heat treatment furnace A to dehydrogenate the metal material W, and after the dehydrogenation treatment, the opening and closing valve 216 is widely closed to cut off the heat treatment furnace A The connection between the heat treatment chamber 214 and the pressure control device 212. At this time, the pressure in the heat treatment ember A is detected by the pressure sensor, and based on the detection signal, the control device The operation amount of the pressure control device 212 to be controlled is kept below lxl〇-iTorr. After the above-mentioned treatment, the Na-Fe-B alloy with the above composition is crushed into 400 «m or less, and within the powder has from 0.2 to 0.4 The structure composed of recrystallized grains of Hd2Fel4B of wm, and has the required magnetism. While the hydrogen treatment of the metal material W is being performed in the heat treatment furnace A, the new gold material W will be given in the heat treatment ash B After the pre-heat treatment, it is sent to the heat treatment chamber 214 and heated to a fixed temperature in the heat treatment chamber 214 to become a state where hydrogen absorption treatment can be performed. Therefore, when the control device opens the on-off valve 217, the pressure control device 212 operates Then, the hydrogen absorbed by the pressure control device 212 is sent to the heat treatment chamber 214 of the heat treatment furnace B under the above-mentioned predetermined pressure, and hydrogen absorption treatment is performed in the heat treatment S. After the hydrogen absorption treatment is completed, the pressure control device 212 Carry out the action in the opposite direction, and apply the Chinese National Standard (CNS) # 4 specifications (210 X 297 mm) to each paper size fed into the heat treatment Lu B ; Please read the precautions on the back before filling in this page). Installation. .1T. -Line. A6 · 〇5 ^ 2 _Β6_ Fifth, the invention description (4i hydrogen absorption and hydrogen release treatment in the heat treatment furnace B. When heat treatment After the furnace B finishes the heat treatment of the metal material W, the other on-off valve 217 is closed to cut off the communication between the heat treatment furnace B and the pressure control device 212 to complete the heat treatment of the metal material W in the heat treatment Lu B. As described above, in this embodiment In the heat treatment device 210 of the example, the hydrogen used in the heat treatment of the gold tungsten material tf is given and received between the heat treatment furnaces A and B through the pressure adjustment device 212, which suppresses the release of hydrogen from the device, so the use of hydrogen can be greatly reduced It does not require exhaust gas treatment equipment, so it can avoid the enlargement of the shape of the device and the increase in equipment costs, and the amount of hydrogen used in the first heat treatment furnace filled at the initial stage of the lotus turn can be used for the operation of two heat treatment furnaces A and B. Therefore, it can also prevent the device from becoming larger. When the metal material W is fed into or out of each heat treatment furnace A, B, for example, when being fed into or out of the preheating chamber 213 and between the cooling chamber 215 and the heat treatment chamber 214, or when performing the vacuum exhaust treatment of the heat treatment chamber 214, Hydrogen used during heat treatment may leak to the outside, and the amount of hydrogen in the device may decrease as a result of repeated heat treatment. However, the amount of reduction is extremely small. Even if the amount of reduction becomes less than the amount required for heat treatment, it is only necessary to supplement the amount of reduction, so the capacity of the hydrogen storage device does not need to be too large. In the heat treatment apparatus 210 of this embodiment, the initial hydrogen filling amount was set to 35Hin3, and the gold-deposited material W of each composition described above was treated 10 times respectively, and then the hydrogen reduction amount was measured. The result was the same as in Experimental Example 4. From this result, it can be seen that according to this experimental example, there is almost no reduction in hydrogen gas, and the effect is extremely large. [Experimental example 10] This paper scale is applicable to the Chinese National Standard (CNS) A4 specifications (210 X 297 mm)... Please read the precautions on the back and then fill out this page.)-Binding-Order λ. Ministry of Economic Affairs Printed by the Central Bureau of Standards, S Industry and Consumer Cooperatives 5. Description of the invention (4 2) Examples of verification and use of materials, rfv w A The materials and furnace materials belong to the gold heat for the gold metal heat and T1 ink stone The same type of phase heat 13 contains the deposit and release of gold, which will be described in the upper collection and inhalation of this gas to borrow hydrogen, and the surroundings of the lower part of the ring are 10 weeks and 2 times. M &lt; Install at 0C '-treatment' heat The case of moving 8 drives with the same system phase control is verified by verification

V 中 料 材料 屬材 金靥V Medium-sized materials

之 W 金-7 進 下 件 條 之 Γ Γ ο T 4 - ο ii X 1 V ο 5 8 在 後 然 理 處 氫 脱 金 合 • 1 T 之 相 θ· + 極 性 待 變 蠕 耐 及 α 度 之強 大勞 粗疲 有琛 具循 成高 製其 , 金 後合 9Π *1 理 Τ 處之 述成 上組 過種 經這 。 有異 具優 A 爐 m: 理 處 熱 各 在 亦 氣 氫 之 用 使 所21 理置 處裝 熱制 , 控 時力 此壓 由 經 間 之 ΒW Jin-7 into the next article of Γ Γ ο T 4-ο ii X 1 V ο 5 8 in the subsequent treatment of hydrogen demetallization • 1 T phase θ + polarity to be changed creep resistance and α degree Powerful labor, exhaustion, fatigue, discipline, and discipline will lead him to a higher level, and Jin Houhe 9Π * 1 will be described in the previous group. There are different advantages. Furnace m: heat treatment is used for hydrogen gas. The heat treatment is installed at the 21st place, and the pressure is controlled by the time between the

,請先閲讀背面之注意事項再填寫本頁X .裝. 受 授 以 予 裝 至 漏 洩 氣 氫 制 抑 可 故 為 定 設 量 充 填 氣 氫 之 態 狀 期 初 之 置 裝 之 例 施 實 本 〇 將 LT 夕 置 各 對 置 裝 該 用 利 測可 後此 理由 處 〇 述同 上相 次果 2 結 行之 • 5 進 別 分 金 合 較 比 置 裝 用 例習 驗與 實, 與少 果減 結氣 , 氫 量無 少亦 減例 之施 氣實 氫本 其 , 定知 幅 大 有 具 訂. 經濟部中央標準局負工消費合作社印製 置 裝 fn: 理 處 熱 之 例 施 實 9 第 明 發 本 示 。表 善12第 改圖在 之 係 度 例 IK·- 夕 之 B A 爐 理 處 熱 座 2 之 例 施 實 8, Please read the precautions on the back before filling in this page X. Installation. It is granted to be installed until the leakage gas hydrogen is suppressed. Therefore, it is the example of the installation at the beginning of the state where a fixed amount of gas hydrogen is filled. LT Xizhi each installs the usage test, and the reasons for this can be described later. The same as above, the second time. The result is 2. The result is: 5. The scores are better than those of the installation use case. The amount of hydrogen can be reduced and the actual amount of hydrogen applied is reduced, and the scope of the determination is very specific. The Central Standards Bureau of the Ministry of Economic Affairs prints and installs the fn: the example of handling heat. Show. Table 12: Example of the first picture modification IK ·-Example of B A furnace processing hot seat 2

而 C 者 成 構 中 例 施 實 爐本 理 處 路 通 連 多 施 實 該 熱 座 1X 加 增 又 許 由 經 4 2 室 m: 理 處 熱 之 C A 爐 理 處 熱 各 路 通 遘 各 聯 串 置 裝 制 控 力 壓 之 同 相 例 施 實 述 上 與 有 設 途 中 之 閥 閉 開 對 1 及 本纸張尺度適用中國國家標準(CNS)甲4规格(210 X 297公釐) A6 205572 B6_ 五、發明説明(4 3) 216c),217 (217a , 217b , 217c) 〇 如此構成之熱處理裝置220中,藉著依次控制各壓力 控制裝置 212a, 212b, 212c,及開閉閥 216(216a, 216b, 216c), 217(217a, 217b,217c)之動作,將氫氣從熱處理 爐A送入熱處理爐B中,然後,從熱處理嫌B送入熱處理爐 C中,再從熱處理燼B送入熱處理爐C中,如此循環而在各 熱處理爐A, B, C中依次進行將氫氣吸收於金屬材料W之氫 氣吸收處理,及放出氫氣之氫氣放出處理。 在該熱處理裝置220中,熱處理時使用之氫氣亦只是 在各熱處理瀘A , B , C之間循環而極少洩漏至裝置外,故 可大幅度的減少氫氣使用量,而且若各熱處理爐A, B, C 之處理循環(搬入處理,預熱處理,氫氣吸收處理,氫氣 放出處理,冷却處理,及搬出處理)在時間上不會重叠, 即可使用1座熱處理爐所需要之氫氣量供給3座熱處理爐A, B, C運轉,故與3座熱處理爐A, B, C並聯獨立的蓮轉時比 較,可將裝置小型化。 圖13表示本發明之第10實施例。本實施例中之熱處理 裝置2 3 0像以2艏条统之連通路2 3 1, 23 2連通各熱處理爐A, B之熱處理室214,將各連通路231,232之中間連結於構成 第1實施例所示之壓力控制裝置212之真空排氣裝置233, 而且在各連通路231, 232中,於真空排氣裝置233之吸引 側設置開閉閥2 3 4 , 2 3 5。 具有上述構造之本實施例之熱處理裝置230中,其各 熱處理爐A, B之熱處理與第8實施例相同,只有兩座熱處 ,請先閲讀背面之注意事項再填寫本頁) -裝. ,ΤΓ· 經濟部中央標準局貝工消費合作社印製 本紙張尺度適用中國國家標準(CNS)甲4规格(210 X 297公釐) 43 20¾512 五、發明説明(44) 理爐A, B間之氫氣循環方法不同。 J 個 例 2 , 之 之態 言狀 換閉 關 為 後 理23 處置 收裝 吸.氣 氣排 氫空 成真 完在i設 理 處 熱 當 如 成 中 閥 閉 開 處 熱 與 另 入 送 之 將 而 收 23吸 聞1 ^DM ΒβΒ 閉氣 開之 之 間 Α 爐 爐理 理處 啓 開 置 裝 氣 排 空 真The C is configured in the middle of the example, the furnace is processed, and the road is used to implement more than 1X of the hot seat. The room is 2 2 m: the CA of the heat is processed, and the heat of the furnace is connected in series. The implementation of the same-phase example of installation control and pressure control is the same as that of the valve in the process of opening and closing and the paper size is applicable to the Chinese National Standard (CNS) A 4 specifications (210 X 297 mm) A6 205572 B6_ V. Description of the invention (43) 216c), 217 (217a, 217b, 217c). In the heat treatment device 220 thus constituted, by sequentially controlling the pressure control devices 212a, 212b, 212c, and the opening and closing valves 216 (216a, 216b, 216c), The action of 217 (217a, 217b, 217c) sends hydrogen from the heat treatment furnace A to the heat treatment furnace B, then from the heat treatment B to the heat treatment furnace C, and then from the heat treatment ember B to the heat treatment furnace C, so In the heat treatment furnaces A, B, and C, the hydrogen absorption process for absorbing hydrogen to the metal material W and the hydrogen release process for releasing hydrogen are performed in turn. In the heat treatment device 220, the hydrogen used in the heat treatment is only circulated between the heat treatment Lu A, B, C and rarely leaks out of the device, so the amount of hydrogen used can be greatly reduced, and if each heat treatment furnace A, The processing cycles of B and C (loading processing, preheating treatment, hydrogen absorption processing, hydrogen release processing, cooling processing, and removal processing) do not overlap in time, and the amount of hydrogen required for one heat treatment furnace can be used to supply 3 The heat treatment furnaces A, B, and C operate, so the device can be miniaturized compared with the three heat treatment furnaces A, B, and C in parallel with independent lotus rotation. Fig. 13 shows a tenth embodiment of the present invention. The heat treatment device 2 3 0 in this embodiment is connected to the heat treatment chamber 214 of each of the heat treatment furnaces A and B like the communication path 2 3 1, 23 2 of the system, connecting the middle of each communication path 231, 232 to the The vacuum exhaust device 233 of the pressure control device 212 shown in the first embodiment, and in each of the communication paths 231 and 232, on-off valves 2 3 4 and 2 3 5 are provided on the suction side of the vacuum exhaust device 233. In the heat treatment device 230 of this embodiment having the above structure, the heat treatment of each of the heat treatment furnaces A and B is the same as that of the eighth embodiment, and there are only two hot spots. Please read the precautions on the back and then fill out this page)-installed , TΓ · The paper standard printed by Beigong Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs is in accordance with the Chinese National Standard (CNS) A 4 specifications (210 X 297 mm) 43 20¾512 V. Description of invention (44) between furnace A and B The hydrogen circulation method is different. J case 2, the state of the situation is to change the retreat to Hou Li 23. Dispose, pack, and suck. The gas and hydrogen are exhausted, and the heat is completed in the i place. When the valve is closed, the heat is closed and the other is sent. Receive 23 suction smells 1 ^ DM ΒβΒ Between the closed gas and the open Α furnace and furnace management, open the gas and evacuate

内 A 作 動爐 3 I 3 理 rvi 處 熱Inside A operation furnace 3 I 3 Rvi heat

中 B 熱 將 此氣熱 , 如S他昇 少其上 減入力 處 , 熱量 將出 , 放 B 熱 爐在 理而 處因 室 ¾里½ X 理 23#處® 室33U氣 理Ϊ2ΜΜ I 置之 ί 處 β 行 裝 熱 U爐進 氣 之申理中 中排處Β Α空U嫌 熱 爐真 W 理 理由{I處 低 減 力 壓 之 内 送壓 氣部 氫内 之之 4 出 1 ΓΝ.1 放 mi一 理 處 中 Β 爐 m: 理 爐處 理熱 處之 熱測 入檢 送所 披器 , 測 時感 此力 壓 與 據壓 ^ 0 根内 由 4 傷 2 , 室 力理 壓處 氣熱 氳 之 之 β 2.值 置數 裝之 氣同 排相 空例 真施 之實 制述 控上 被與 而成 號制 信控 饋被 反而 之 , 關用 有作 力之 量 作 sh^ 之 閥 閉 開 之 下 態 狀 啓 開 將 後 然The B heat will heat the gas. If the heat rises less, the heat will come out, and the heat will come out. Put the B heat furnace in the room and place it in the room ¾ Li ½ X 理 23 # place ® room 33U gas management Ϊ2ΜΜ I set it ί The application of the hot air inlet of the hot U furnace at the middle row B Α The empty U suspected of the heat furnace is true W The reason {I at the low deceleration pressure within the pressure of the gas delivery part of the hydrogen 4 out 1 ΓΝ.1 Put mi At the center of the furnace m: the heat of the furnace treatment heat is measured into the inspection station, the pressure and the pressure are measured during the measurement ^ 0 by 4 wounds in the root 2, the beta of the gas heat at the room pressure 2. The value of the data set is the same as the phase of the air, and the actual implementation of the actual control system is controlled by the number control system. Instead, the valve with the effective amount of sh ^ is closed. The state will be followed

態 狀 閉 密 於 持 保 B 爐其 理啓 處開 熱 , 將後 而間 閉時 關之 34需 所 收 吸 氣 氫 過 經 置 裝 氣 th- 空 真 使21 且室 並理 , 處 35熱 32之 閥 β 閉爐 開理 他處 熱 收 吸爐 此理 藉處 , 熱 作入 動送 33之 將 而 氣 氫 之 内The state is sealed in the furnace B where the heat is kept, and the heat is turned off, and then the closed intake is closed 34. The required intake hydrogen is passed through the installation gas th-empty to make 21 and the room is treated, at 35 hot 32 The valve β closes the furnace and opens the other place. The heat absorbs the furnace. The reason is that the heat is fed into the general 33 and the gas is hydrogen.

之 A -----------------------裝------.ΤΓ^泉 (請先閲讀背面之注意ί項再填寫本頁) 中 經濟部中央標準局員工消費合作社印製 3t1 理 處 21出 室放 理氣 處氫 熱行 BE 理 處 中 Β 吸 爐氣 理氫 處行 熱進 在始 象開 現中 之A ]&lt;媒 同里 目理 . 處 述 上熱 上在 與且 根 後 作 操 述 上 行料 進材 的屬 覆金 反行 進 的 I 理 處 熱 之 A 爐 理 處 熱 各 在 可 述 上 與 亦 中 例 施 實 本 Βφκ 進 收 替 交 例 施 授只 被且 間而 瀘 , 理量 處用 熱使 値氣 兩氫 在少 只減 亦可 氣此 氫因 之 , 用外 使置 時裝 理至 處漏 熱洩 ,少 的極 同而 相受 本紙張尺度適用中國國家標準(CNS)甲4規格(210 X 297公釐) 2〇讲2 五、發明説明(4 5) 供 可 卽 氣 氫 之 用 使 爐 理 處 熱 座 大 太 必爐 不理 亦處 量熱 容當 之 , 置中 裝例 存施 儲實 氣本 要氫 需且A ----------------------- Installed -------- TΓ ^ 泉 (Please read the note on the back first and then fill in this page) Printed by the Ministry of Economy, Central Bureau of Standards, Employee and Consumer Cooperatives 3t1 Treatment Unit 21 out of the room Releasing gas department Hydrogen heating line BE processing department Β Suction furnace gas processing hydrogen processing line in the beginning of the image A] &lt; Limuli. The heat is described in the following and the root is used for the operation of the feed material. The material is reversed. Βφκ Introduce the replacement of the delivery of the teaching only by the time, the amount of heat used in the treatment place to reduce the value of the two hydrogen can only reduce the hydrogen can also be used for this hydrogen. The paper size is compatible with the Chinese National Standard (CNS) A 4 specifications (210 X 297 mm) 2〇 Lecture 2 V. Description of the invention (4 5) For the use of hydrogen gas to heat the furnace The large Taibei Furnace ignores and measures the heat capacity as well.

在 A 而 。 ,化 轉型 蓮大 爐置 理裝 處免 熱避- 座可 利 時 下 態 狀 出 放 氣 氫 氫 將 且 並爐 m: , 理 氣處 氫熱 收他 吸其 的之 制下 強態 IA狀 3 mt*- 處 妾' 收 從 &amp; 3 吸 23氣 置氫 裝入 氣送 排的 空制 真強 用氣 其 使 β 爐 ΠΕ 理 處 熱 行 進 的 強 且 而 時 同 可 此 0 昇 上 力 壓 部 内 0Ε 理 處 壓 昇 之 Β 爐 m: 理 處 熱 與 ΠΕ 理 處 壓 域» Ι-Ell 之移 丨氣 氫 之 間 者 兩 及 以 m: 理 處 各 行 進 的 速 迅 且 而 實 確 可 此 如 第 之 明 發 本 示 表 4 ΊΑ 圖 置 裝 氣 排 空 真 以 係 中In A and. , Transformation of the lotus furnace at the place where the heat is installed to avoid heat-the gas can be released in the next state, and the hydrogen will be combined with the furnace m: mt *-place concubine 'collection from &amp; 3 suction 23 gas and set hydrogen into the gas supply and exhaust of the empty system really strong gas, which makes the β furnace Π Ε heat treatment is strong and at the same time can be 0 liters of pressure In the department, the furnace of 0 Ε processing pressure rise m: the processing heat and the pressure range of ΠΕ processing »Ι-Ell shift between the gas and hydrogen and m: the speed of the processing of the processing and the actual speed of this As shown in the first issue, the table 4 ΊΑ is set to fill the gas and evacuate it.

Jan 置力 裝壓 理之 處側 熱氣 之排 例其 本在 〇 設 例及 施 , 實33 以造 中構 例餘 施其 實 , 10式 第方 代之 取12 以2 置 2’裝 1 -2 0 置控 裝力 制壓 控為 力作]0 3 一^ 壓33目 成2 ί — 置例 構 1 裝施 24氣實 置排10 裝空第 節真與 第置 與装 用氣 F th 作 S 之空 生真 産制 所控 例著 施藉 實傜 本例 施 實 第 〇 同 相 致 大 例 施 實 氣 氫 節 調 而 量. 作 nsu 之 之 爐 m: 理 處 熱 之 下 態 狀 理 處-1、 徽 本 吸 i 其 但 氣 為 氫 } 節 為力調 成壓其 即之行 亦内進 ( 4 1 14 力 2 2 壓 室 置 給理裝 供處節 之熱調 中 例 施 實 本 在 但 力 壓 用 利 以 傜 V請先閲讀背面之注意事項再填寫本頁) 丨裝. 訂_ 經濟部t央標準局貝工消費合作社印製 節理 調處 的出 確放 精氣 且氫 而為 細成 精而 常氣 非氫 力收 壓吸 給與 供節 之調 氣之 氫力 將 壓 可給 , 供 此該 如且 而 理 處 熱 保 確 可 故 立 獨 而 開 分 用 作 壓 減 之 爐 m: 理 處 〇 熱性 之定 態穩 狀之 圖第 之 第 明 發 本 示 表 較 bb 例 施 實 精 〇0氣 3 氣 置置 裝設 理上 處11 Λ/- 熱 之 例 施 實 路 通 逋 在 有 只 圖 與 裝 製 本紙張尺度適用中國國家標準(CNS)甲4規格(210 X 297公釐) 45 A6 B6 五、發明説明(46) 置313為其不同之處。匾16表示本發明之第13實施例之熱 處理裝置。與第10實施例比較,只有在連通路211上設置 氫氣精製裝置313為其不同之處。圖17為第14實施例之熱 處理裝置330,該實施例僳在圖14之第11實施例中附加氫 氣精製裝置313者。以上實施例中之氩氣精製裝置之作用 及效果與第6實施例及第7實施例相同,其說明從略。 ,請先閲讀背面之注意事项再填寫本頁) 經濟部中央標準局员工消費合作社印製 表 1 (at % ) \ Nd Co B Si A1 Zr Ga Fe 1 13.5 11.6 6.0 0.4 - - - 其餘 2 15.0 17.5 7.0 - 0.5 - - 其餘 3 12.5 17.5 6.5 - - 0.1 0.5 其餘 4 12.0 11.6 6.0 - - - 1.0 其餘 丨裝- 訂. ,^- 本紙張尺度適用中國國家標準(CNS)甲4規格(210 X 297公釐) 46 2t- 5 ύ ο 2 6 6 A B i 五、發明説明(47 ) 表 2 (Νπι3) 實施例 比較例 處理前 處理後 處理前 處理後 1 35.0 34.9 35.0 27.4 2 35.0 34.9 35.0 26.3 3 35.0 35.0 35.0 28.5 4 35.0 35.0 35.0 29.1 {請先Μ讀背面之注意事項再塡寫本頁) 丨裝. .ΤΓ. .線. 經濟部中央標準局员工消費合作社印製 表 3 (wt % )Jan placed the pressure on the side of the hot gas at the place where the arrangement of the hot air was originally set and implemented. Actually, the construction is based on the construction of Yu Shi. Actually, the 10th formula is taken as the 12th. Set up the control system and control the pressure control as a masterpiece] 0 3 1 ^ Press 33 mesh into 2 ί — Set example configuration 1 Pack 24 gas actual row 10 Pack empty section true and installed gas F th as S empty The actual production system is controlled by Shi Jiushi, this example is the 0th phase of the same phase, and the implementation of gas and hydrogen is regulated. The furnace for nsu m: handle the state under the heat -1, Huiben sucks i, but the gas is hydrogen} The knot is adjusted to the pressure, and the action is also advanced (4 1 14 force 2 2 The pressure chamber is placed for the management of the heat regulation of the section. To use Yiliu V, please read the precautions on the back and then fill out this page) 丨 Installed. Order _ The printing and jointing office of the Beigong Consumer Cooperative of the Ministry of Economy's Central Standards Bureau releases the gas and hydrogen to become fine. The normal gas is non-hydrogen pressure-reducing, and the hydrogen power supplying and supplying the regulating gas will be available, and the supply should be treated like this. Make sure that it can be used independently as a furnace for pressure reduction m: Treatment 〇 The thermal stability of the steady state diagram The first table of the figure shows that the table is more accurate than the bb example. Rationale 11 Λ /-An example of heat Shi Shilu Tongzhi applies the Chinese National Standard (CNS) A 4 specifications (210 X 297 mm) to the drawings and papers. 45 A6 B6 V. Invention description (46 ) Let 313 be its difference. The plaque 16 shows the heat treatment device of the thirteenth embodiment of the present invention. Compared with the tenth embodiment, the only difference is that the hydrogen purification device 313 is provided on the communication path 211. Fig. 17 is a heat treatment device 330 of the fourteenth embodiment. In this embodiment, a hydrogen gas refining device 313 is added to the eleventh embodiment of Fig. 14. The functions and effects of the argon gas refining apparatus in the above embodiments are the same as those in the sixth and seventh embodiments, and their explanations are omitted. , Please read the precautions on the back before filling in this page) Printed Form 1 (at%) \ Nd Co B Si A1 Zr Ga Fe 1 13.5 11.6 6.0 0.4---The rest 2 15.0 17.5 7.0-0.5--The rest 3 12.5 17.5 6.5--0.1 0.5 The rest 4 12.0 11.6 6.0---1.0 The rest 丨 Binding-Order., ^-This paper scale is applicable to China National Standard (CNS) A 4 specifications (210 X 297 ) 46 2t- 5 ύ ο 2 6 6 AB i V. Description of the invention (47) Table 2 (Νπι3) Examples Comparative Examples Before Treatment After Treatment After Treatment Before Treatment 1 35.0 34.9 35.0 27.4 2 35.0 34.9 35.0 26.3 3 35.0 35.0 35.0 28.5 4 35.0 35.0 35.0 29.1 (Please read the precautions on the back and then write this page) 丨 Installed ... ΤΓ.. 线. List printed by Employee Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs 3 (wt%)

本紙張尺度適用中國國家標準(CNS)甲4規格(210 X 297公釐) 2 S520The paper size is applicable to China National Standard (CNS) A4 specifications (210 X 297 mm) 2 S520

A 經濟部中央標準局負工消費合作社印製 五、發明説明(48) 表 4 (N m 3 ) \ 實施例 比較例 處理前 處理後 處理前 處理後 1 35.0 35.0 35.0 28.4 2 35.0 35.0 35.0 26.6 表5 (Nm3) \ 實施例 比 較 例 處理前 處理後 處理前 處理後 1 35.0 35.0 35.0 27.4 2 35.0 34.9 35.0 26.3 3 35.0 35.0 35.0 28.5 4 35.0 35.0 35.0 29.1 裝. 訂. ;請先閲讀背面之注意事項再填寫本頁) 本紙張尺度通用中國國家標準(CNS)甲4規格(210 X 297公釐) 48 五、發明説明(49) :請先閲讀背面之注意事項再填寫本頁) 表 6 ( N m 3 ) \ 實施例 比 較 例 處理前 處理後 處理前 處理後 1 35.0 35.0 35.0 28.4 2 35.0 34.9 35.0 26.6 圖式 画1為表示習用之金屬材料之熱處理裝置之概略圖; 圖2為本發明概略之說明圖,為本發明第1實施例之金 靥材料之熱處理裝置之方塊圖; 圖3為匾2之熱處理裝置之變更例之方塊圖; 圖4為本發明第2實施例之熱處理裝置之方塊圖; 絰濟部中央標準局員工消費合作社印製 圖5為表示圔4中熱處理装置之氫氣^儲存裝置之一部剖 斷透視圖; 圖6為本發明第3實施例之熱處理裝置之方塊圖; 圖7為本發明第4實施例之熱處理裝置之方塊圖; 圖8為本發明第5實施例之熱處理裝置之方塊圔; 圖9為本發明第6實施例之熱處理裝置之方塊圔; 圖10為將圖8中之第5菁施例變更之第7實施例之熱處 本紙張尺度適用中國國家標準(CNS)甲4規格(210 X 297公釐) 49A Printed by the Central Bureau of Standards of the Ministry of Economic Affairs of the Negative Work Consumer Cooperative V. Description of the invention (48) Table 4 (N m 3) \ Example Comparative Example Before Treatment After Treatment After Treatment Before Treatment 1 35.0 35.0 35.0 28.4 2 35.0 35.0 35.0 26.6 Table 5 (Nm3) \ Examples Comparative Examples Pre-treatment post-treatment post-treatment pre-treatment 1 35.0 35.0 35.0 27.4 2 35.0 34.9 35.0 26.3 3 35.0 35.0 35.0 28.5 4 35.0 35.0 35.0 29.1 Packing. Order. Please read the precautions on the back before (Fill in this page) The size of this paper is in accordance with the Chinese National Standard (CNS) A 4 specifications (210 X 297 mm) 48 5. Description of the invention (49): Please read the precautions on the back before filling out this page) Table 6 (N m 3) \ Comparative examples of the embodiment pre-treatment post-treatment post-treatment pre-treatment 1 35.0 35.0 35.0 28.4 2 35.0 34.9 35.0 26.6 drawing 1 is a schematic diagram showing a conventional metal material heat treatment device; FIG. 2 is a schematic description of the invention FIG. 3 is a block diagram of a heat treatment device for a gold-thorium material according to the first embodiment of the present invention; FIG. 3 is a block diagram of a modified example of a heat treatment device for a plaque 2; FIG. 4 is a block diagram of a heat treatment device according to a second embodiment of the present invention; printed by the Employee Consumer Cooperative of the Central Standards Bureau of the Ministry of Economy and Economics. FIG. 5 is a partially cut-away perspective view showing the hydrogen storage device of the heat treatment device in No. 4; FIG. 6 FIG. 7 is a block diagram of a heat treatment apparatus according to a fourth embodiment of the invention; FIG. 7 is a block diagram of a heat treatment apparatus according to a fourth embodiment of the invention; FIG. 8 is a block diagram of a heat treatment apparatus according to a fifth embodiment of the invention; Block 6 of the heat treatment apparatus of the sixth embodiment of the invention; FIG. 10 is the heat treatment of the seventh embodiment with the fifth embodiment of FIG. 8 changed. The paper scale is applicable to the Chinese National Standard (CNS) A 4 specification (210 X 297 mm) 49

A6 B6_ 五、發明説明(5Q) 理裝置之方塊圖; 圖11為本發明第8實施例之熱處理装置之方塊圖; 圖12為本發明第9實施例之熱處理裝置之方塊圖; 圖13為本發明第10實施例之熱處理裝置之方塊圖; 画14為本發明第11實施例之熱處理裝置之方塊圖; 圔15為將圖11之第8實施例變更之本發明第12實施例 之熱處理裝置之方塊圖; 圖16為將圖13之第10實施例變更之本發明第13實施例 之熱處理裝置之方塊圖; 圔17為圖14之第11實施例變更之本發明第14實施例之 熱處理裝置之方塊圔。 ί請先閲讀背面之注意事項再埸寫本頁) 訂. 經濟部中喪標準局员工消费合作社印製 本紙張尺度適用中國國家標準(CNS)甲4规格(210 X 297公釐)A6 B6_ V. Description of the invention (5Q) Block diagram of the processing device; FIG. 11 is a block diagram of the heat treatment device of the eighth embodiment of the invention; FIG. 12 is a block diagram of the heat treatment device of the ninth embodiment of the invention; Block diagram of the heat treatment apparatus of the tenth embodiment of the present invention; Drawing 14 is a block diagram of the heat treatment apparatus of the eleventh embodiment of the present invention; FIG. 15 is the heat treatment of the twelfth embodiment of the present invention, which changes the eighth embodiment of FIG. 11 Block diagram of the device; FIG. 16 is a block diagram of the heat treatment device of the thirteenth embodiment of the present invention modified from the tenth embodiment of FIG. 13; FIG. 17 is a fourteenth embodiment of the present invention modified from the eleventh embodiment of FIG. 14 The square of the heat treatment device. ί Please read the precautions on the back before writing this page). Ordered. Printed by the Employee Consumer Cooperative of the China Bureau of Standards and Economics of the Ministry of Economic Affairs. This paper scale is applicable to China National Standard (CNS) Grade 4 (210 X 297 mm)

Claims (1)

A7 B7 2〇55^__D7___ 六、,申請專利範圍 1. 一種金靥材料之熱處理方法,其特徽為包括:進行將 氫氣吸收於金屬材料中之氫氣吸收處·理,及從吸收氳 氣之金屬材料中放出氫氣之氫氣放出處理之製程;及 將從金羼材料中放出之氫氣回收,並將該回收之氫氣 再度供給於氫氣吸收及放出製程中之氫氣回收製程。 2. 如申請專利範圍第1項之方法,其中該氫氣回收製程 僳將氫氣儲存於氫氣吸收合金中,並且將儲存之氫氣 放出之製程。 3. 如申請專利範圍第1項之方法,其中該氫氣回收製程 係反覆的進行將氫氣吸收於金屬材料中之氫氣吸收處 理,及從吸收氫氣之金靥材料中放出氫氣之氫氣吸收 放出製程。 (請先《讀背面之注意Ϋ項再填寫本頁) 進吸處 來一從熱 用―及之 0C : ,理 括理處 包處出 為收放 激吸氣 待氣氬 其氫之 ,之氣 置中氫 裝料出 理材放 處屬中 熱金料 之於材 料收屬 材吸金 靥氣之 金氫氣 種將氫 一 行收 中氫 燼之 理中 處爐 熱理 從處 收熱 回於 來給 用供 , 度 上再 爐« 理氫 處將 熱且 在而 設 , 附氣 及氫 之 鑪出 理放 »濟部中央標準局Λ工消费合作杜印製 置 裝 收 回 氣 氫 該 中 其 置 裝 之 項 4 第 圍 〇 範 置,利 裝|專«:j JI 明 0 ~ Φ 氣S 5 置理 裝處 收收 回吸 。氣氣 置氫氫 裝該之 存中中 儲其料 氣 ,材 氫置屬 之裝金 成之於 構項收 所 4 吸 金第氣 合圍氫 收範將 吸利行 氣一專進 氫一請來 由^申用 係如傜 6 處 出 放 氣 氫 之 氣 氫 出 放 中 料 材 颶 金 之 氣 氫 收 吸 從第 及之 m: , 理 爐 m: 理 處 熱 本纸張尺度適用中國國家標準(CNS)甲4規格(210 X 297公釐) 5 1 經濟部中央櫺準居霣工消费合作杜印R 六、申請專利範圍 7. 如申請專利範圍第5項之裝置,其中又具有分別設在 熱處理爐及氫氣儲存裝置上,用來檢·测其内部壓力及 内部溫度之感測器,及根據感測器所産生之檢測信號 調節熱處理嫿及氫氣儲存裝置之内部壓力或溫度,藉 此配合熱處理爐之處理狀態將氫氣供給於熱處理爐中 或從熱處理爐中排出之控\制裝置。 8. 如申請專利範圍第7項之裝置,其中又具有:將熱處 〜一-——~---. 理爐放出之氫氣送入氫氣儲存裝置中之排氣通路;將 氫氣從氫氣儲存裝置供給於熱處理爐中之供給通路; 設在排氣通路上,吸收熱處理爐内之氣體而將之送入 氫氣儲存裝置中之真空排氣裝置;及設在供給通路上 用來調節供給於熱處理爐之氫氣壓力之壓力調節裝置 ,該控制裝置不但可調節内部壓力或内部溫度,而且 又可調節真空排氣裝置之動作,藉此控制供給於熱處 理爐及從其中排出之氫氣。 9. 如申請專利範圍第7項之裝置,其中又包括:分別具 有該等感測器之許多座熱處理爐;連通各熱處理爐與 氫氣儲存裝置,並在其間形成氫氣流通用閉迴路之許 多連通路;及將許多連通路中之一選擇性的連通於氫 氣儲存裝置之轉換裝置。 10.如申請專利範圍第9項之裝置,其中又包括:連通各 熱處理爐與氫氣儲存裝置,而且將各熱處理爐中放出 之氫氣送入氫氣儲存裝置中之排氣通路;將氫氣從氫 氣儲存裝置供給於各熱處理爐中之供給通路;連通於 (請先閲讀背面之注意事項再填寫本頁) .丨裝 訂 本紙張尺度適用中國國家標準(CNS)甲4規格(210 X 297公釐) 5 2 六、申請專利範園 A7 B7 C7 D7 綬濟部中央標準居β工消费合作社印製 氫 ,.節溫熱.'空氫 具與多氣 最間 ,昇出裝 置 置 入路調之各 真之 別壚許氫 通爐上力放制 裝 裝 送通力置於 在内 分一理之於 連/理路壓氣控 制--fj 之給壓装給 設路 :處路通 :處通部氫力 控 控 將供之存供 括通 活熱迴連 括熱連内行壓 力; 力 而於力儲氣 包氣 包各閉的 包各在其進之 壓j 壓 收-JS壓氣氫 又排 又通用性 又在設將在氣 該 該 吸連氣氫將 中於 中連通擇 中 ,及時爐氫 中 中 體及氫及此 其通 其;流選 其壚.,理理出 其 其&gt; 氣.,之爐藉。,流 ,爐氣一 ,理路處處排 , , 之置 中理,出置製 置 理氫之 置處通收熱且 置 置 内裝·爐處作排裝精 裝處成中 裝熱連吸各並 裝 装 嫌氣理熱動中之來 之熱形路 之 2 之氣當低 之 之 理排處節之爐項用 項座間通。項第路氫在降 項 項 處空熱調置理8,。11多其連置6與迴行而力1313 熱真各置裝處第側置第許在多裝第爐閉進,壓 第 。第 各之於装氣熱圍游裝圍之、許換圍理用在氣部 圍置圍 將中給制排各範下製範器置將轉範處通爐氫内 範裝範 ,置供控空從利之精利測裝及之利熱流理給其 利氣利 路装節該真及專置氣專感存;置專値氣處供將 專排專 通存調,及爐請裝氫請等儲路裝請 1 氫熱且時 請空請 氣儲來置 ,理申氣之申該氣通存申之成各並理。申真申 排氣用裝度處如排氣如有氫連儲如先形當高處;置如偽如 ! 一 ίII-----------叫--------裝------.玎-----Θ泉 (請先閲讀背面之注意事項再填寫本頁) 本纸張尺度適用中國國家標準(CNS)甲4规格(210 X 297公釐) 53 A7 B7 C7 D7 六、申請專利範团 傷由真空排氣裝置及設在其排氣側之壓力諝節裝置所 構成。 注 16. 如申請專利範圍第13項之裝置,其中又包括設在連通 路中途之氫氣精製裝置。 17. 如申請專利範讀第16項之裝置,其中該壓力控制裝置 係真空排氣裝置。 18. 如申請專利範圍第16項之裝置,其中該壓力控制裝置 係由真空排氣裝置及設在其排氣側之壓力調節裝置所 構成。 裝 19. 如申請專利範圍第18項之裝置,其中該氫氣精製裝置 傺設在真空排氣裝置舆壓力諝節裝置之間。 訂 經濟部中央標率局霣工消费合作社印製 本紙張尺度適用t國國家標準(CNS)甲4規格(210 X 297公釐)A7 B7 2〇55 ^ __ D7___ Sixth, the scope of patent application 1. A method of heat treatment of gold tantalum materials, its special emblem includes: the hydrogen absorption process of absorbing hydrogen in the metal material, and from the absorption of the gas The process of releasing hydrogen from the metal material; and recovering the hydrogen released from the Jinge material, and supplying the recovered hydrogen to the hydrogen recovery process in the hydrogen absorption and release process. 2. The method as claimed in item 1 of the patent scope, in which the hydrogen recovery process is a process of storing hydrogen in a hydrogen absorption alloy and releasing the stored hydrogen. 3. The method as described in item 1 of the patent application scope, in which the hydrogen recovery process is a hydrogen absorption process in which hydrogen is absorbed in a metal material repeatedly, and a hydrogen absorption release process in which hydrogen is released from the hydrogen-absorbent metal material. (Please read "Notes on the back" first and then fill in this page) Enter the suction part to use it from the heat-and the 0C:, the package is released for the absorption of argon and its hydrogen. The gas is placed in the hydrogen charge, and the material is placed in the middle heat gold material. The material is the material. The gold hydrogen gas species that absorbs gold and gas is the reason for the hydrogen in the row. The heat in the furnace is the heat from the place. For supply and use, re-furnace «The hydrogen management department will be hot and there, and the furnace with gas and hydrogen will be released» The Central Standard Bureau of the Ministry of Economic Affairs and Industry Consumer Cooperation Co., Ltd. Du Yin made the equipment to recover the gas and hydrogen. Items of installation 4 No. 0 Fan set, easy to install | Special «: j JI Ming 0 ~ Φ Gas S 5 Set the place to collect and suck. The gas is stored in hydrogen and hydrogen, and the material gas is stored in the storage. The material of the hydrogen is in the structure of the project. 4 The gold absorption gas and the hydrogen collection model will absorb the profit of the gas. The application system is the gas from which hydrogen gas is released from the 6th place in Yumeng. The hydrogen gas is released from the material Hurricane gas. The hydrogen absorption is from the first m:, the furnace m: the heat is processed. The paper size is applicable to the Chinese national standard (CNS ) A 4 specifications (210 X 297 mm) 5 1 The Ministry of Economic Affairs, Central Ministry of Housing and Urban Welfare Consumer Cooperation Du Yin R Six, the scope of patent application 7. Such as the application of the patent scope item 5, which also has a separate heat treatment On the furnace and hydrogen storage device, a sensor for detecting and measuring its internal pressure and internal temperature, and adjusting the internal pressure or temperature of the heat treatment device and hydrogen storage device according to the detection signal generated by the sensor, thereby cooperating with the heat treatment The processing state of the furnace is the control device that supplies hydrogen to the heat treatment furnace or is discharged from the heat treatment furnace. 8. The device as claimed in item 7 of the patent scope, which also includes: sending the hydrogen from the hot spot to the exhaust path of the hydrogen storage device; storing hydrogen from the hydrogen The device is supplied to the supply path in the heat treatment furnace; the vacuum exhaust device is provided on the exhaust path to absorb the gas in the heat treatment furnace and send it to the hydrogen storage device; and is provided on the supply path to adjust the supply to the heat treatment A pressure regulating device for the hydrogen pressure of the furnace. This control device can regulate not only the internal pressure or internal temperature, but also the action of the vacuum exhaust device, thereby controlling the hydrogen gas supplied to and discharged from the heat treatment furnace. 9. The device as claimed in item 7 of the patent scope, which also includes: a number of heat treatment furnaces with these sensors respectively; many heat treatment furnaces and hydrogen storage devices are connected, and there are many connections for forming a general closed loop of hydrogen flow between them Channel; and a conversion device that selectively connects one of the many communication paths to the hydrogen storage device. 10. The device as claimed in item 9 of the patent scope, which also includes: connecting each heat treatment furnace with a hydrogen storage device, and sending the hydrogen released from each heat treatment furnace into the exhaust path of the hydrogen storage device; storing hydrogen from the hydrogen The device is supplied to the supply channel in each heat treatment furnace; it is connected to (please read the precautions on the back before filling in this page). 丨 The size of the bound paper is applicable to the Chinese National Standard (CNS) A 4 specifications (210 X 297 mm) 5 2. Sixth, apply for a patent Fan Garden A7 B7 C7 D7. The central standard home of the Ministry of Economy and Economics. The β-consumer cooperative prints hydrogen. It saves temperature and heat. 'Empty hydrogen equipment and multi-gas are the most, and the lifting device is placed in various ways. The difference is that the hydrogen is put on the furnace and the force is put on the assembly and the delivery force is placed on the inside to separate the reason and the pressure control of the circuit-fj the pressure is installed to the road: the local road: the local power control Control the supply and supply of energy, including the return of heat and the internal pressure of the heat; the pressure of the closed gas bag of the gas storage bag is at its inlet pressure. It is assumed that the gas will be absorbed in the gas and the hydrogen will be in Optional communication in a timely manner in the body of the furnace and hydrogen, and this hydrogen which its pass; flow thereof selected from clay, which sort processing thereof &gt;.. Gas, by the furnace. , Flow, Furnace Gas One, Discharge Everywhere,, Place in the middle, put the place where the hydrogen is placed to collect heat and set the interior. Furnace place as a row of hardcover into the middle of the heat and even absorb each Furnace items that are presumed to be irritating, and that the heat from the heat path is arranged to be low are arranged in the section of the furnace, and the furnace is opened between the items. Item No. 1 hydrogen is placed in the air-conditioning system at the drop item. 11 Duoqi 6 and return and force 1313 hot Zhen each installation place on the first side of the first installation in the multi-furnishing furnace closed, press the first. The first one is to install the gas and heat the surroundings, and the Xuchang Governance is used in the gas surroundings. Control the air from the advantages of the precise measurement and installation of the positive heat flow to give it the advantage of the gas and the road, and the special gas is stored; the special gas is provided for the purpose of storing and adjusting the special exhaust gas, and the furnace is equipped with hydrogen Please wait for the storage road to install 1 hydrogen heat and please empty the gas storage to set up, and apply for the gas and store the gas separately. Shen Zhenshen's exhaust gas is installed at a place such as exhaust gas, if there is hydrogen and even storage is like a high place; it is like a false one! I ίII ----------- called -------- install ------. 玎 ----- Θ Spring (please read the precautions on the back before filling in this page) This paper scale is applicable to China National Standard (CNS) A 4 specifications (210 X 297 mm) 53 A7 B7 C7 D7 6. The patent application group injury consists of a vacuum exhaust device and a pressure unit installed on its exhaust side. Note 16. If the device under item 13 of the patent application scope includes a hydrogen refining device installed in the middle of the communication path. 17. For example, the device of patent application reading item 16, wherein the pressure control device is a vacuum exhaust device. 18. The device as claimed in item 16 of the patent scope, wherein the pressure control device is composed of a vacuum exhaust device and a pressure regulating device provided on the exhaust side thereof. Installation 19. The device as claimed in item 18 of the patent application, in which the hydrogen refining device is installed between the vacuum exhaust device and the pressure unit. Printed by the Central Engineering Bureau of the Ministry of Economic Affairs. Printed by the Engong Consumer Cooperative Society. This paper scale is applicable to the National Standard (CNS) A4 specification (210 X 297 mm)
TW081109386A 1991-11-28 1992-11-24 TW205572B (en)

Applications Claiming Priority (5)

Application Number Priority Date Filing Date Title
JP3339840A JPH05149498A (en) 1991-11-28 1991-11-28 Reuse of hydrogen used for hydrogen treatment
JP3337315A JP2897500B2 (en) 1991-12-19 1991-12-19 Heat treatment equipment for metallic materials
JP3347443A JP2897502B2 (en) 1991-12-27 1991-12-27 Heat treatment equipment for metallic materials
JP3347444A JP2897503B2 (en) 1991-12-27 1991-12-27 Heat treatment equipment for metallic materials
JP4004227A JPH0673512A (en) 1992-01-13 1992-01-13 Heat treatment apparatus for metallic material

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TW205572B true TW205572B (en) 1993-05-11

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