〜，乙ί ί V 經濟部中央標準局負工消費合作社印策 Α7 ____Β7__ 五、發明説明（I ) 本申請案爲1 9 9 5年九月二十日所提出之美國專利 申請案第0 8 / 5 3 0，7 8 9號申請案之部分延續申請 發明背景 發明領域 本發明係相關於一種真空蒸餾裝置，尤其是相關於一 種不需使用真空泵或其他產生裝置而能夠產生真空之裝置 相關前技之說明 蒸餾過程在淨水以及其他液體的製造上已經被使用了 很長的一段時間。給水進入一煮沸或蒸發器中’而該給水 在其中蒸發。接著，蒸氣通過一冷卻室或是冷凝器，而該 蒸氣在其中冷凝以形成純水之微滴，該微滴通過而來到蒸 餾液出口。蒸餾是唯一能將包含於給水中之任何固體移除 之水淨化過程。 當蒸餾系統與其他淨化技術相較之時，在蒸餾系統中 有若干公認之缺點。第一就是所需用以將水煮沸爲蒸氣所 需的能量大量消耗，並接著將過度之熱量移除以彤成蒸餾 液β另一個實際上的缺點是當硬水在高沸點溫度下蒸餾時 所發生積垢之傾向。水之硬度反映了碳化鈣與硫酸鎂在給 水中所出現的量。在大規模蒸餾系統之狀況下，這些缺點 之若干解決方法已經被發展出來了。例如，能量之保存係 使用多階段蒸餾，其中蒸發之部分潛熱從一蒸餾階段回收 ，用以提供下一階段之熱量β 4 張尺度it用中國國家標皁（CNS ) Λ4規格（210X297公犛1 .I— ! I m ' n .ITi In m (請先閱讀背面之注意事項再填艿本頁) 經濟部中央標準局貝工消费合作社印繁 422716 7 Λ 7 Η7 五、發明説明（>) 另一此種解決方法是使用一蒸氣壓縮蒸餾裝置，該裝 置甚至可以降低大規模蒸餾系統所需的能量°在蒸氣壓縮 蒸餾中，水經由煮沸而蒸發，而所產生之蒸氣接著被壓縮 ，而此使得蒸氣之壓力並從而蒸氣的溫度都增加了。接著 ，此蒸氣被用以加熱煮沸器中的水’並且以一種可以回收 潛熱之方式。蒸氣壓縮蒸餾循環一旦開始之後’需要些微 之熱量，而所需要之能量僅爲提供蒸氣壓縮器本身。 在小規模蒸餾系統之狀況中，在每天1 0 0加侖或更 少的情況下，多階段蒸餾之資本成本以及蒸氣壓縮蒸餾不 充分的可靠性，使得這些選擇是無法接受的。因此’大多 數小規模蒸餾系統使用在大氣壓力下之簡單蒸鶴’其中在 大氣壓力下水之沸點爲華氏2 1 2度。因此’能量之消耗 與積垢是在小規模標準大氣蒸餾器中最主要的問題。 發明滴要 本發明克服了這些傳統蒸餾器中公認的缺點’尤其是 小規模標準大氣蒸餾器之缺點。在一觀點上：本發明之蒸 餾裝置爲一不需使用真空泵或其他產生裝置而能夠產生真 空之裝置，而在另一觀點上，本發明之蒸餾裝置將一般是 分離之蒸發器與冷凝器組合成一整合單元°這些創新的結 果是一個在低溫以分批過程而產生髙純度蒸餾水的系統’ 而其能量的消耗可以較標準大氣蒸餾方法低很多。同樣地 ，本發明中低溫蒸餾之另一優點是：來自一般存在於水中 之雜質的積垢可以消除。 本發明用於分批蒸餾一液體之裝置，其係包括一蒸發 5 、__ 本紙浪尺度適用中國國家標準《CNS ) A4坭格（2丨OX297公茇） ---------裝——,—訂------涑 (請先閱請背面之注意事項再填寫本頁) Λ227 1 β Α7 Η 7 五、發明说明（^) 器部分，該蒸發器部分具有一設有閥體之入口部分，其中 穿過該入口部分之一批處於第一大氣狀況下之液體被加入 蒸發器部分。一聚積部分接收蒸餾液，並且其係與該蒸發 器部分相通連。一加熱元件被安置在蒸發器部分，用於定 時間歇地蒸發該液體以形成第一與第二蒸氣。一具有閥體 之通氣口被設置，用以在加熱元件將該液體蒸發爲最初足 量之第一蒸氣，以使第一大氣狀況經由設有閥體之通氣孔 而從裝置淨化之後，封閉該裝置而使其與外界大氣隔離， 以形成一與大氣隔離之第二大氣狀況。一冷凝器被安置在 蒸發器部分與聚積部分之間，用於在一低於第一大氣狀況 壓力之壓力下冷凝一足量之第一蒸氣以形成一第三大氣狀 況，並且用於冷凝第二蒸氣以製造蒸餾液。裝置之較佳版 本更包括一自動控制機構（電子控制機構），該自動控制 機構與閥體、冷凝氣、以及加熱元件相通連，用於裝置之 定時操作。 _因此，本發明分批蒸餾裝置之主要目的與優點是不需 使用一機械式真空泵或其他產生裝置而能夠在裝置中產生 真空15 本發明之另一目的與優點是一種新穎的真空蒸餾過程 ，其係用於在低操作溫度下高純水之製造，並且使用較傳 統簡單蒸餾系統爲少之能量。 本發明之另一目的與優點是在煮沸器與冷凝器單元中 積垢之降低，其在本發明中係爲藉由一較低之沸點所達成 ，因此消除了除垢以及使用除垢化學藥品的必要。 I n 1 11 ; ~^衣 H —Ϊ- I li I —11IJ1 —i (#先聞讀背面之注意事項再瑱寫本頁) 經濟部中央標隼局負工消费合作社印製 本紙張尺度適用中國國家標準< CNS ) Λ4规格（2丨ΟΧ 29?公货） 7 A7 B7 經濟部智慧財產局貝工消費合作社印製 五、發明說明（If ) 本發明之另一目的與優點是由於裝置之低操作溫度而 使用較低成本之材料。 本發明之另一目的與優點是較低之沸點而使得裝置可 以較安全地控制與操作。 本發明之另一目的與優點是將一般爲分離之煮沸或蒸 發室以及冷凝功能組合爲單一容室0 本發明之另一目的與優點是一種使用一加強循環熱傳 裝置之創新方法，其中該熱傳裝置允許在煮沸器尺寸上之 大幅降低。 本發明之另一目的與優點是將本發明整合於標準冷凍 系統之設計中之容易性，其中冷凍器之冷凝器以及蒸發器 元件分別作爲蒸餾器之加熱與冷凝元件，而該二元件被整 合爲在蒸館裝置中一相同之元件。 本發明之另一目的與優點是當蒸氣被用以淨化裝置外 之空氣時’冷凝器碳精過濾器以及積聚器之殺菌能夠自動 地執行。 圖示簡單論曰彳 第一圖爲一習组技術中標準大氣蒸餾器之視圖； 第二圖爲本發明之裝置： 第三圖爲一具有預蒸發器部分之本發明裝置； 第四圖爲一具有預蒸發器部分之本發明裝置，其中該 蒸發器部分並未具有一加熱元件； 第五圖爲本發明之一實施例，其中第一容室並未完全 地分隔爲一預蒸發器部分以及一煮沸部分； 7 -----------I --I (請先閱讀背面之注意事項再填寫本頁) 本紙張尺度適用中國國家標準（CNS)A4規格（210x 297公釐) 經濟部中央樣隼局貝工消費合作社印'^ A7 B7 五、發明説明（f) 第六圖爲本發明之一實施例，其中第一容室包括兩個 加熱元件： 第七圖爲一具有預蒸發器部分以及一冷凍旋環系統之 本發明裝置： 第八圖爲本發明之一孤立分批處理蒸餾單元： 第九圖爲一孤立分批處理蒸餾單元之部分截面圖，其 係顯示了設計之不同元件： 第十圖爲一典型之標準家用冰箱的顯示圖，其係顯示 了分批處理水蒸餾單元之位置； 第十一圖爲一具有冷凍劑蒸發器之分批處理蒸餾單元 的部分截面圖，其係整合至一標準家用冰箱中： 第十二圖爲一並未具有冷凍劑蒸發器之分批處理蒸餾 單元的部分截面圖，其係整合至一標準家用冰箱中； 第十三圖依據本發明之真空蒸餾裝置之方塊圖，其係 顯示了電子控制機構之邏輯： 第十四圖爲電子控制機構操作之流程圖： 第十五圖爲電子控制機構之控制順序的圖表。 本發明之換作 所提出之分批處理蒸餾裝匱之基本定理爲：將一批水 或其他液體在蒸發器部份中煮沸，用以產生一第一蒸氣以 經由一具有閥體之通氣孔而淨化含有空氣之裝置。當裝置 被淨化時，該具有閥體之通氣孔是關閉的，將裝置封閉而 與大氣隔離。冷凝器被打開，接著蒸氣，例如水蒸氣，其 係與冷凝器相接觸而變成液體，從而將裝置中之壓力降低 8 ---------策------訂------朿 (請先閱讀背面之注意事項#填转本1) 本紙张尺度適用中國國家標隼（CNS ) Λ4^格（210X29^公处) 經濟部中央標率局工消费合作·社印製 “ Z 7 ' Q」 A7 ]?7 一— - _—.·-·—. 五、發明説明（么） 至一次大氣壓力，接著其允許在蒸發器部分之該批液體以 一較低溫度煮沸，而產生第二蒸氣。該第二蒸氣’例如水 蒸氣，其係接著被冷凝爲一蒸餾水或其他蒸餾液體之蒸餾 液。第一圖中所顯示的爲一標準大氣蒸餾器之結構、蒸餾 方法、以及操作。本發明之裝置則詳細地顯示在第二圖至 第六圖中。裝置之自動控制元件則顯示在第十^圖至第十 五圖中。而第七圖至第十二圖則顯示了裝置與〜用以加熱 及冷凝之冷凍系統合倂之情形° 標大氣蒸餾器 如第一圖中所顯示之一標準大氣蒸館器’其係爲蒸餾 之最簡單的形式，並且其係爲目前販售之佔有優勢的類型 。在一大氣壓下的水被加入煮沸器或蒸發器部分6 6中， 並且藉由加熱器1 4而加熱至華氏2 1 2度’而將水轉變 爲蒸氣，例如水蒸氣。該水蒸氣從蒸發器部分6 6經由一 連接管4 1而來到一冷凝器2 4或第二容室’並且接著藉 由在冷凝線圈2 4內部通過而冷凝’空氣經由〜風扇1 3 而吹過冷凝線圈之外部。在蒸餾器中之壓力爲〜大氣壓， 並且在整個蒸餾過程中均維持在一大氣壓之下。該水蒸氣 在冷凝器2 4中冷凝，用以形成蒸餾水微滴’該微滴落入 —第二容器或貯水池5 0中，其中該第二容器或貯水池5 0在水從蒸發器6 6被煮沸爲水蒸氣並且被當成蒸餾水之 蒸餾液而收集時，其係經由一通氣孔4 8而是對著大氣開 放的。蒸餾水接著藉著閥體5 2之打開而從貯水池移去。 一旦在煮沸器中之水下降至一規定之高度，則關閉該加熱 ______ 9 本紙ϋ度適用中關家標準（CNS )八4祕（21〇Χ297公兑) ' ~ ~ (請先鬩讀背而之注意事項再楨^-本頁) •裝· 、-=* 經濟部中央揉率局員工消资合作社印聚 Δ227 1 δΛ > Λ7 ^ Η7 五、發明说明（&) 將其冷凝爲蒸餾液。該冷凝器亦可以是在外部加有散熱片 之線圈，而風扇1 3將冷卻空氣吹過或拖至散熱片上（並 未顯示），並且來自第一容室之蒸氣在冷凝器管件之內表 面冷凝，並接著落至聚積部分4 0中。或者’該冷凝器2 4可以是一充滿有冷之氣體或液體之盤繞管件’其係位於 聚積部分4 0之中，而蒸氣與整個管件接觸並在冷凝線圈 之外部冷凝爲蒸餾液，而藉由滴落而傳送至聚積部分4 0 〇 本發明更包括一貯水池部分〔50)，如第二圖所示 。該貯水池部分（5 0)藉由一第二連接管件（4 6)而 被連接至聚積部分4 0。一具有閥體之通氣孔（4 4)被 安置在聚積部分4 0之外，而在一形式中’其係被安置在 聚積部分與貯水池部分之間的第二連接管件4 6上。在貯 水池部分所收集之蒸餾液可以爲了使用而藉由打開閥體5 2以移去。 可以淸楚看出的是，本發明之裝置與方法可以依據以 下階段而了解：注水、真空產生、蒸餾液製造、以及蒸餾 液排出。雖然該裝置可以經由手動方式而控制，該裝置與 方法較佳之形式包括$自動控制機構'，而在此所使用之 自動控制機構則係包括電子控制機構，此將在以下詳細說 明。其他自動控制機構包括與將在以下所敘述之電子控制 機構相組合的止回閥體。 蒸發器6 6以及冷凝2 4部分亦可以適用於一種可拆 卸、可封閉之連結，用以快速地將第一容室從該裝置上拆 ____π 本紙張尺反適用t國囷家標準（CNS ) Λ4規格（210X2i^i>$ ) ---------^--.----il------Φ (請先閲讀t·面之注意事項再填寫本頁) 經濟部智慧財產局員工消費合作社印製 1 多 4227 16、 ,〆'^_Β7_____ 五、發明說明（1 ) 除，並且可以快速地將第一容室可封閉地連結至該裝置。 注水 在操作中’在一大氣壓力之第一大蓮J犬況之下，蒸發 器部分6 6經由一具有閥體之進口璋3 6而將一批在往後 步驟中將要蒸發之液體6 4 (例如水）注入。蒸發器6 6 以及加熱元件14部分亦可以適用於一種可封閉之連結， 用以快速地拆除蒸發器6 6，並且可以快速地將蒸發器6 6可封閉地連結至該裝置。在裝置中所使用之典型可封閉 連結包括有一墊圏或〇形環組件，在操作期間其係合適地 封閉在裝置中的真空狀況，並且允許重複地封閉及開啓以 允許將液體充滿該裝置並且淸空該裝置中之蒸餾液。 直空產牛 加熱元件1 4被打開，並且液體6 4被轉換爲第一蒸 氣，例如水蒸氣，其係與裝置中的空氣相混合並輸送。蒸 氣/空氣混合氣接著被驅使，經由連接管件4 1而進入冷 凝器2 4中，而風扇1 3是位於關閉位置，亦即冷凝器之 冷卻功能是關閉的。蒸氣/空氣混合氣接著經由一在一第 一打開位置之具有閥體的可封閉通氣孔（4 4)而離開冷 凝室4 0。典型地，在真空產生階段，加熱元件1 4花了 幾分鐘的時間用以形成一最初足量之第一蒸氣，例如水蒸 氣，用以經由打開之具有閥體的通氣孔4 4而淨化裝置中 的第一大氣狀況°也就是說，裝置中大部分之空氣經由具 有閥體之可封閉通氣孔4 4而被驅離裝置之外’用以形成 蒸氣之一第二大氣狀況°蒸氣/空氣混合氣之—部份冷凝 12 本紙張尺度適用中國國家標準（CNS)A4規格（210 X 297公釐） I I-------I，裝 if —--^--訂--------線..· <請先閲讀f·面之注意事項再填寫本頁) 經濟部中央標隼局貝工消費合作社印架 42271® A7 _ ΙΪ7 五、發明説明（π ) 爲在貯水池部分5 0中之蒸餾液，並且空氣從貯水池部分 5 0頂端之空氣排出通氣孔（4 8)漏出。 在此點’真空產生接著藉由關閉具有閥髖之通氣孔4 4而達成’關上加熱器1 4並且打開風扇1 3，而較好是 藉由將在以下詳細敘述之自動控制機構所達成。藉由關閉 具有閥體之通氣孔4 4，第二大氣狀況被封閉而與外界大 氣隔離。藉由關上加熱器1 4並且打開風扇1 3，在第二 大氣狀況下之蒸氣，導致了一第二大氣壓力之降低，從而 創造出一個第三大氣狀況，而該第三大氣狀況爲裝置中之 —次大氣狀況或真空狀況，包括了在蒸發器6 6中所煮沸 水之上方的空間6 8。實際上，裝置之內壓已經被降低至 低於外界壓力，也就是降低內部壓力使其低於一大氣壓。 蒸餾液製浩 當裝置中之壓力下降時，在蒸發器部分6 6中液體之 沸點亦會下降，縱使蒸發器部分之加熱器已經被關上，液 體仍繼續煮沸而產生了一第二蒸氣。該蒸氣在冷凝器2 4 中被冷凝爲蒸餾液。當風扇1 3持續運轉時，蒸餾液持續 製造，並且最終達成一平衡狀態，其中真空增加而導致更 多之液體煮沸以產生一第二蒸氣’並且將熱量從蒸發器部 分6 6中之液體移去，直到實際上液體停止煮沸爲止。因 此，在蒸發器部分6 6中之加熱器1 4再一次被打開而處 於完全或部分之能量下’而剩下之液體6 4被加熱並且持 續煮沸，在一非常低之溫度（例如是大約華氏1 4 0度） 下產生一第二蒸氣，該第二蒸氣接著在冷凝器2 4中冷凝 13 ϋ n n n i n —13 m m I、1τI I n I n (¾先閱讀背而之注意亊項再"'寫本頁) 本紙张尺度適用中國國家棍準（CNS > Λ4现格（210X297公垃） 經濟部中央樣準局貝工消#合作社印裂 422716 五、發明説明（/ Μ ’而蒸餾液則收集於聚積部分4 〇中° ΜΜΜΜΆ —旦在蒸發器部分θ δ中之液體下降至一定的程度， 則加熱器1 4就被關上。接著，裝置中之真空藉由打開— 個或所有具有閥體之部分而破壞，亦即具有閥體可封閉進 口埠3 6或是蒸發器部分6 6之可拆卸可封閉連結3 7或 是具有閥體之通氣孔4 4。接著’被收集在聚積部分4 0 中之蒸餾液1 7經由閥體4 4而離開聚積部分4 ◦並且進 入貯水池部分5 0。接著’蒸餾液1 7爲了使用而經由— 閥體5 2移離貯水池部分5 0。 一批新的水則接著經由具有閥體之進口痺3 6或是可 拆卸可封閉連結3 7而被加入蒸發器部分6 6 ’並且重複 此等過程。 當本發明之裝置依據閥體、加熱元件、以及冷凝器之 定時操作（這可以經由手動方式所達成）時，可以了解到 裝置之較佳形式包括了用於閥體、加熱元件、以及冷凝器 之自動定時操作的自動控制機構（第十三圖至第十五圖） 〇 在此形式中，裝置之操作是在下面將敘述之自動控制 機構的控制之下。具有閥體之進口埠3 6、具有閥體之通 氣孔4 4、加熱元件1 4、以及風扇1 3是藉由電子控制 機構而在一定時的順序下自動地操作的，以達成在次大氣 壓力下分批蒸餾液體’而不需要一創造或維持真空之真空 泵或真空產生裝置的幫助。裝置之另一形式，具有閥體之 _ 14 本紙張尺度適用中囷國家標率（CNS ) Λ4«ί格U10X297公^ ' ---------裝------訂-------涑 (諳先閲讀背面之注意事項再填寫本頁) 經濟部中央搮準局貝工消费合作社印製 42271® Λ7 JJ7 五、發明説明（Iγ) 通氣孔4 4爲一單向（ο n e —wa y )機械閥，爲一般 所知之止回閥體，其係獨立於電子控制機構而操作，以使 得當冷凝器在第二大狀況下被打開時，在裝置中達成之次 大氣壓力導致止回閥關閉，而將裝置封閉以與外界大氣隔 離。 具有貯水池駔葙蒸發器;> 直空菡餾器 第三圖顯示了本發明之一實施例，其係包括有一預蒸 發器部分（7 0 )，該預蒸發器部分（7 0)作爲一預煮 沸器而操作。〜預蒸發器〃以及★預煮沸器Λ之詞可交換 地使用。除了一蒸發器部分6 6、一聚積部分4 0、以及 一貯水池部分5 0之外，本實施例亦包括有一預蒸發器部 分（7 0)，而該預蒸發器部分（7 0)之作用如同一預 煮沸器。同樣在此實施例中所揭露的是相關之閥體以及連 接管件。 開始時，在操作中，所有具有閥體之部分以及具有閥 體之通氣孔是關閉的。爲蒸發器部分之一具有閥體進口埠 的閥體（3 6 )是打開的。經由具有閥體進口埠3 6，該 蒸發部分6 6部分地充滿一批將被蒸餾之液體6 4。接著 ，具有閥體之進口埠3 6被關閉。 在—第一大氣狀況下，也就是在一大氣壓下，預煮沸 器部分7 0經由供應管件3 0而充滿來自蒸發器部分6 6 之液體，或經由供應管件8 .0而充滿來自聚積部分4 0之 液體，或者是經由供應管件8 4而充滿來自於貯水池部分 5 0之液體，或者，預煮沸器可以經由一具有閥體之管件 15 n m - n n n n n Γ __ . i m---ϋ n (郐先閱讀背面之注意事項再楨舄本頁)~, B ί V Indian policy of the Central Standards Bureau of the Ministry of Economic Affairs and Consumer Cooperatives A7 ____ Β7__ V. Description of the Invention (I) This application is US Patent Application No. 0, filed on September 20, 1995 / 5 3 0, 7 8 9 Partial continuation of the application. BACKGROUND OF THE INVENTION Field of the Invention The present invention relates to a vacuum distillation device, and particularly to a device capable of generating a vacuum without using a vacuum pump or other generating device. Technical description The distillation process has been used for a long time in the manufacture of purified water and other liquids. The feedwater enters a boiling or evaporator 'and the feedwater is evaporated therein. Then, the vapor passes through a cooling chamber or a condenser, and the vapor condenses therein to form droplets of pure water, and the droplets pass through to the outlet of the distillate. Distillation is the only water purification process that removes any solids contained in the feedwater. When distillation systems are compared with other purification technologies, there are several recognized disadvantages in distillation systems. The first is the large amount of energy required to boil water into steam, and then remove excess heat to form a distillate β. Another practical disadvantage is that when hard water is distilled at high boiling temperatures, The tendency to fouling. The hardness of the water reflects the amount of calcium carbide and magnesium sulfate present in the feedwater. In the context of large-scale distillation systems, several solutions to these disadvantages have been developed. For example, energy conservation uses multi-stage distillation, in which part of the latent heat of evaporation is recovered from one distillation stage to provide the heat of the next stage β 4 scale it uses the Chinese National Standard Soap (CNS) Λ4 specification (210X297) .I—! I m 'n .ITi In m (Please read the notes on the back before filling in this page) Central Standards Bureau, Ministry of Economic Affairs, Shellfish Consumer Cooperatives, India 422716 7 Λ 7 Η7 V. Description of the invention (>) Another such solution is to use a vapor compression distillation device, which can even reduce the energy required for large-scale distillation systems. In vapor compression distillation, water is evaporated by boiling, and the generated vapor is then compressed, and This increases the pressure of the vapor and thus the temperature of the vapor. This vapor is then used to heat the water in the boiler and in a way that latent heat can be recovered. Once the vapor compression distillation cycle has begun, 'a little heat is required, The energy required is only to provide the vapor compressor itself. In the case of small-scale distillation systems, at 100 gallons or less per day, multiple stages The capital cost of distillation and the inadequate reliability of vapor compression distillation make these options unacceptable. Therefore, 'most small-scale distillation systems use simple steaming cranes at atmospheric pressure', where the boiling point of water at atmospheric pressure is Fahrenheit 2 12 degrees. Therefore, 'energy consumption and fouling are the most important problems in small-scale standard atmospheric distillers. Invention of the invention The invention overcomes the recognized shortcomings of these traditional distillers', especially small-scale standard atmospheric distillers On the one hand, the distillation device of the present invention is a device capable of generating a vacuum without using a vacuum pump or other generating device. On the other hand, the distillation device of the present invention is generally a separate evaporator and The condenser is combined into an integrated unit. The result of these innovations is a system that produces distillate-purified distilled water at a low temperature in a batch process. And its energy consumption can be much lower than standard atmospheric distillation methods. Similarly, the low-temperature distillation Another advantage is that fouling from impurities normally present in water can be eliminated. The invention A device for batch distillation of a liquid, which includes an evaporation system. The paper scale is applicable to the Chinese national standard "CNS" A4 grid (2 丨 OX297). —Order ------ 涑 (Please read the notes on the back before filling this page) Λ227 1 β Α7 Η 7 V. Description of the invention (^) The evaporator part has a valve body. The inlet section, in which a batch of liquid in the first atmospheric condition passing through the inlet section is added to the evaporator section. An accumulation section receives the distillate and is connected to the evaporator section. A heating element is disposed in the evaporator section for periodically and intermittently evaporating the liquid to form first and second vapors. A vent with a valve body is provided to close the liquid after the heating element evaporates the liquid into a first sufficient amount of first vapor to purify the first atmospheric condition from the device through the vent provided with the valve body. The device is isolated from the outside atmosphere to form a second atmospheric condition that is isolated from the atmosphere. A condenser is disposed between the evaporator portion and the accumulation portion, for condensing a sufficient amount of the first vapor at a pressure lower than the pressure of the first atmospheric condition to form a third atmospheric condition, and for condensing the first Two vapors to make a distillate. The preferred version of the device further includes an automatic control mechanism (electronic control mechanism), which is connected to the valve body, the condensing gas, and the heating element for the timed operation of the device. _ Therefore, the main purpose and advantage of the batch distillation device of the present invention is to be able to generate a vacuum in the device without using a mechanical vacuum pump or other generating device. 15 Another object and advantage of the present invention is a novel vacuum distillation process. It is used for the manufacture of high-purity water at low operating temperatures and uses less energy than traditional simple distillation systems. Another object and advantage of the present invention is the reduction of scale in the boiler and condenser units, which is achieved in the present invention by a lower boiling point, thus eliminating descaling and the use of descaling chemicals Necessary. I n 1 11; ~ ^ 衣 H —Ϊ- I li I —11IJ1 —i (#Please read the notes on the back before writing this page) Printed on this paper. Applicable by the Central Bureau of Standards, Ministry of Economic Affairs and Consumer Cooperatives. China National Standard < CNS) Λ4 Specification (2 丨 〇 × 29? Public Goods) 7 A7 B7 Printed by Shelley Consumer Cooperatives, Bureau of Intellectual Property, Ministry of Economic Affairs V. Description of Invention (If) Another object and advantage of the present invention is due to the device Low operating temperatures and use lower cost materials. Another object and advantage of the present invention is that the lower boiling point makes the device safer to control and operate. Another object and advantage of the present invention is to combine a boiling or evaporation chamber and a condensing function that are generally separated into a single chamber. Another object and advantage of the present invention is an innovative method using an enhanced circulation heat transfer device, wherein the The heat transfer device allows a significant reduction in the size of the boiler. Another object and advantage of the present invention is the ease of integrating the present invention in the design of a standard refrigeration system, in which the condenser and evaporator elements of a freezer are used as heating and condensing elements of a distiller respectively, and the two elements are integrated It is an identical element in the steam room installation. Another object and advantage of the present invention is that when steam is used to purify the air outside the device, the sterilization of the condenser carbon filter and the accumulator can be performed automatically. The diagram is briefly described. The first picture is a view of a standard atmospheric distiller in a group of techniques. The second picture is a device of the invention. The third picture is a device of the invention with a pre-evaporator. The fourth picture is A device according to the invention with a pre-evaporator section, wherein the evaporator section does not have a heating element; the fifth figure is an embodiment of the invention, wherein the first chamber is not completely divided into a pre-evaporator section And a boiling part; 7 ----------- I --I (Please read the precautions on the back before filling this page) This paper size applies to China National Standard (CNS) A4 (210x 297) ^) Printed by the Central Laboratories of the Ministry of Economic Affairs, Shellfish Consumer Cooperatives' A7 B7 V. Description of the Invention (f) The sixth diagram is an embodiment of the invention, wherein the first chamber includes two heating elements: The seventh diagram is An apparatus of the present invention having a pre-evaporator section and a refrigerated ring system: FIG. 8 is an isolated batch processing distillation unit of the present invention: FIG. 9 is a partial cross-sectional view of an isolated batch processing distillation unit. Shows the different elements of the design: tenth Is a typical standard domestic refrigerator display, which shows the location of the batch process water distillation unit; Figure 11 is a partial cross-sectional view of a batch process distillation unit with a refrigerant evaporator, which is integrated into In a standard domestic refrigerator: FIG. 12 is a partial cross-sectional view of a batch processing distillation unit without a refrigerant evaporator, which is integrated into a standard domestic refrigerator; FIG. 13 is a vacuum distillation according to the present invention The block diagram of the device shows the logic of the electronic control mechanism: Figure 14 is a flowchart of the operation of the electronic control mechanism: Figure 15 is a chart of the control sequence of the electronic control mechanism. The basic theorem of batch processing distillation equipment proposed in the alternative of the present invention is: a batch of water or other liquid is boiled in the evaporator part to generate a first vapor to pass through a vent hole with a valve body And purify the device containing air. When the device is cleaned, the vent with valve body is closed, closing the device from the atmosphere. The condenser is opened, and then the vapor, such as water vapor, comes into contact with the condenser to become a liquid, thereby reducing the pressure in the device. ---- 朿 (Please read the precautions on the back # Fill in this book 1) This paper size applies to the Chinese national standard (CNS) Λ4 ^ grid (210X29 ^ public office) Central Standards Bureau, Ministry of Economic Affairs, Industrial and Consumer Cooperation · Community Print "Z 7 'Q" A7]? 7 I —-_ —. ····. V. Description of the invention (?) To the atmospheric pressure once, then it allows the batch of liquid in the evaporator section to a lower The temperature boils, and a second vapor is generated. The second vapor ', such as water vapor, is a distilled liquid which is then condensed into a distilled water or other distilled liquid. Shown in the first figure is the structure, distillation method, and operation of a standard atmospheric still. The device of the present invention is shown in detail in the second to sixth figures. The automatic control elements of the device are shown in Figs. 10-15. The seventh to twelfth pictures show the combination of the device and the refrigeration system for heating and condensation ° Standard atmospheric distillation device is one of the standard atmospheric distillation devices shown in the first figure, which is The simplest form of distillation, and it is the dominant type currently sold. Water at atmospheric pressure is added to the boiler or evaporator section 66, and is heated to 2 12 degrees Fahrenheit by a heater 14 to convert the water into steam, such as water vapor. The water vapor passes from the evaporator portion 66 to a condenser 24 or a second chamber through a connecting pipe 41 and then condenses by passing through the inside of the condensation coil 24 and the air is blown through the fan 1 3 Outside the condensation coil. The pressure in the still is ~ atmospheric, and it is maintained below one atmosphere throughout the distillation process. The water vapor is condensed in the condenser 24 to form droplets of distilled water. The droplets fall into a second container or reservoir 50, where the second container or reservoir 50 is removed from the evaporator 66 by the water. When boiled as water vapor and collected as a distillate of distilled water, it is open to the atmosphere through a vent hole 48. Distilled water is then removed from the reservoir by opening the valve body 52. Once the water in the boiler has dropped to a specified height, turn off the heating ______ 9 The degree of paper is applicable to CNS Standard 8 Secrets (21〇 × 297 KRW) '~ ~ (Please read first Note on the back again ^-this page) • Install ·,-= * Printed by the Consumers Cooperative of the Central Rubbing Bureau of the Ministry of Economy Δ227 1 δΛ > Λ7 ^ Η7 V. & Description of the invention Distillate. The condenser can also be a coil with a heat sink on the outside, and the fan 13 blows or drags cooling air onto the heat sink (not shown), and the vapor from the first chamber is on the inner surface of the condenser pipe. Condensed and then fell into the accumulation section 40. Or 'the condenser 24 may be a coiled pipe filled with cold gas or liquid', which is located in the accumulation portion 40, and the vapor contacts the entire pipe and condenses into a distillate outside the condensing coil. Conveyed by dripping to the accumulation section 400. The present invention further includes a reservoir section [50], as shown in the second figure. The reservoir portion (50) is connected to the accumulation portion 40 by a second connecting pipe (46). A vent hole (44) having a valve body is disposed outside the accumulation portion 40, and in one form, it is disposed on the second connection pipe 46 between the accumulation portion and the reservoir portion. The distillate collected in the tank portion can be removed by opening the valve body 52 for use. It can be clearly seen that the apparatus and method of the present invention can be understood in the following stages: water injection, vacuum generation, distillate production, and distillate discharge. Although the device can be controlled manually, the preferred form of the device and method includes a $ automatic control mechanism, and the automatic control mechanism used here includes an electronic control mechanism, which will be described in detail below. Other automatic control mechanisms include a check valve body combined with an electronic control mechanism to be described below. Evaporator 66 and condensation section 24 can also be applied to a detachable and closable connection to quickly remove the first container from the device. __Π This paper rule is not applicable to national standards (CNS) ) Λ4 specification (210X2i ^ i > $) --------- ^ --.---- il ------ Φ (Please read the precautions for t · face before filling out this page) Printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs, more than 4227 16, 〆 '^ _ Β7 _____ V. Description of the Invention (1) Except, and the first container can be hermetically connected to the device. Water injection in operation 'under the condition of the first large lotus J at an atmospheric pressure, the evaporator portion 6 6 passes through an inlet with a valve body 36 and a batch of liquid to be evaporated in the next step 6 4 (Such as water). The evaporator 66 and the heating element 14 can also be applied to a closable connection for quickly removing the evaporator 66, and the evaporator 66 can be quickly and hermetically connected to the device. A typical sealable connection used in a device includes a pad or o-ring assembly that is properly closed in the vacuum condition of the device during operation and allows repeated closure and opening to allow liquid to fill the device and Empty the distillate in the device. The direct air heating element 14 is turned on, and the liquid 64 is converted into a first vapor, such as water vapor, which is mixed with the air in the device and transported. The steam / air mixture is then driven into the condenser 24 through the connecting pipe 41, and the fan 13 is in the off position, that is, the cooling function of the condenser is turned off. The vapor / air mixture then leaves the condensation chamber 40 through a closable vent hole (44) with a valve body in a first open position. Typically, during the vacuum generation phase, the heating element 14 takes several minutes to form an initial sufficient amount of first vapor, such as water vapor, to purify the device through the open vent hole 4 4 with the valve body. The first atmospheric condition in the ° means that most of the air in the device is driven out of the device via the closable vent hole 4 4 having a valve body, which is used to form one of the second atmospheric conditions ° vapor / air Mixed gas—partially condensed 12 This paper size is in accordance with China National Standard (CNS) A4 (210 X 297 mm) I I --------- I, installed if --------- order --- ----- line .. < Please read the notes on f. Face before filling out this page) Ink stand 42271® A7 _ ΙΪ7, Shellfish Consumer Cooperative of Central Bureau of Standards of the Ministry of Economic Affairs 5. Description of the invention (π) is The distillate in the reservoir portion 50 and air leaked from the air exhaust vent (48) at the top of the reservoir portion 50. At this point, 'vacuum generation is then achieved by closing the vent hole 4 4 with a valve hip', and turning off the heater 14 and turning on the fan 13 is preferably achieved by an automatic control mechanism which will be described in detail below. By closing the vent hole 4 4 with the valve body, the second atmospheric condition is closed and isolated from the outside atmosphere. By turning off the heater 14 and turning on the fan 13, the vapor in the second atmospheric condition causes a reduction in a second atmospheric pressure, thereby creating a third atmospheric condition, which is in the device Sub-atmospheric or vacuum conditions include the space 68 above the boiling water in the evaporator 66. In fact, the internal pressure of the device has been reduced below the external pressure, that is, the internal pressure has been reduced to less than one atmosphere. When the pressure in the device decreases, the boiling point of the liquid in the evaporator section 66 will also decrease. Even if the heater of the evaporator section has been turned off, the liquid will continue to boil and a second vapor will be generated. This vapor is condensed into a distillate in the condenser 2 4. When the fan 13 continues to run, the distillate continues to be manufactured, and eventually reaches an equilibrium state, where the increase in vacuum causes more liquid to boil to produce a second vapor 'and transfers heat from the liquid in the evaporator section 66. Go until the liquid actually stops boiling. Therefore, the heater 14 in the evaporator section 6 6 is turned on again under full or partial energy 'and the remaining liquid 6 4 is heated and continuously boiled at a very low temperature (for example, about Fahrenheit (1 40 ° F) produces a second vapor, which is then condensed in condenser 24. 13 ϋ nnnin — 13 mm I, 1τI I n I n (¾Read the following and pay attention to the items before quoting ; 'Write this page) This paper size applies to the Chinese national standard (CNS > Λ4 is now (210X297)) Central Government Standards Bureau of the Ministry of Economic Affairs Bei Gong Xiao # Cooperative Newsletter 422716 5. Description of the invention (/ Μ' and distillation The liquid is collected in the accumulating section 40 ° ΜΜΜΜΜΆ— once the liquid in the evaporator section θ δ drops to a certain level, the heater 14 is turned off. Then, the vacuum in the device is turned on by one or all The part with the valve body is destroyed, that is, the valve body can close the inlet port 36 or the detachable and closable connection 3 7 of the evaporator part 6 6 or the vent hole 4 4 with the valve body. Then 'is collected in Distillate in accumulation part 4 0 1 7 passes through valve body 4 4 and leave the accumulation section 4 ◦ and enter the reservoir section 50 0. Then 'distillate 17 is passed through for use—the valve body 5 2 is removed from the reservoir section 50 0. A new batch of water is then passed through the inlet with the valve body. 3 6 or the detachable and closable connection 3 7 is added to the evaporator part 6 6 ′ and the process is repeated. When the device of the present invention operates according to the timing of the valve body, heating element, and condenser (this can be done manually (Achieved), it can be understood that the preferred form of the device includes an automatic control mechanism for the automatic timing operation of the valve body, heating element, and condenser (Figures 13 to 15). In this form The operation of the device is under the control of the automatic control mechanism which will be described below. The inlet port with the valve body 36, the vent hole with the valve body 4, 4, the heating element 1, 4, and the fan 13 are controlled electronically The mechanism operates automatically in a certain sequence to achieve batch distillation of liquids at sub-atmospheric pressure without the need for a vacuum pump or vacuum generating device to create or maintain a vacuum. Placed in another form, with a valve body _ 14 This paper size is applicable to the Chinese National Standard (CNS) Λ4 «ί 格 U10X297 公 ^ '--------- Installation ------ Order- ------ 涑 (谙 Please read the notes on the back before filling in this page) Printed by the Central Consumers' Bureau of the Ministry of Economic Affairs, Printed by the Shellfish Consumer Cooperative, 42271® Λ7 JJ7 V. Description of the invention (Iγ) Vent holes 4 4 is a single (Ο ne — wa y) mechanical valve is a generally known check valve body that operates independently of the electronic control mechanism so that when the condenser is opened in the second largest condition, it is achieved in the device The next atmospheric pressure caused the check valve to close and the device was closed to isolate it from the outside atmosphere. Tank storage evaporator; > Vertical air decanter The third figure shows an embodiment of the present invention, which includes a pre-evaporator section (70), the pre-evaporator section (70) as a Operate with pre-boiler. ~ The terms pre-evaporator 〃 and ★ pre-boiler Λ are used interchangeably. In addition to an evaporator section 66, an accumulation section 40, and a reservoir section 50, this embodiment also includes a pre-evaporator section (70), and the role of the pre-evaporator section (70) Like the same pre-boiler. Also disclosed in this embodiment are related valve bodies and connecting fittings. At the beginning, in operation, all parts with valve body and vent holes with valve body are closed. A valve body (36) with a valve body inlet for one of the evaporator sections is open. Via having a valve body inlet port 36, the evaporation section 66 is partially filled with a batch of liquid 64 to be distilled. Then, the inlet port 36 with the valve body is closed. In the first atmospheric condition, that is, at atmospheric pressure, the pre-boiler section 70 is filled with liquid from the evaporator section 66 through the supply pipe 30, or the supply section 8 is filled with the liquid from the accumulation section 4 The liquid of 0, or the liquid from the reservoir part 50, is filled through the supply pipe 84, or the preboiler can pass through a pipe with a valve body 15 nm-nnnnn Γ __. I m --- ϋ n ( (阅读 Read the precautions on the back before reading this page)
本紙掁尺度適用中國國家#準（CNS > Λ#兄格（210Χ297公釐） 經濟部中央標準局貝工消费合作社印策 …7'豸、221\S: A7 _____________一___ 五、發明説明（/Μ 8 2而充滿來自外部液體來源之液體。來自上述來源的水 注入預煮沸器中一預定之程度，並且適當之閥體2 9、7 8、8 6、或8 2是關閉的。 閥體7 6接著被打開，並接著在預煮沸器7 〇中之加 熱器1 4亦被打開，並且在預煮沸器中迅速地煮沸小量之 液態水7 2。在另一形式中，閥體7 6可以在整個過程中 是打開的。液體迅速地轉換至第一蒸氣或水蒸氣，其係經 由具有閥體之出口管件7 4而離開該預煮沸器7 0，而進 入蒸發器部分6 6之上方部分6 8，並且其與空氣相混合 ’接著經由連接管件4 1而離開蒸發器部分6 6，而進入 造型爲冷凝線圈之冷凝器2 4中。蒸氣/空氣混合氣通過 冷凝器2 4並且進入聚積部分4 0，並且與聚積部分4 0 中之空氣相混合，接著經由具有閥體之通氣孔4 4而由聚 積部分之底部離開，並且經由第二管件4 6而進入貯水池 部分5 0。 蒸氣在貯水池部分5 0中蒸餾液1 7下方表面冷凝， 並且從裝置淨化之空氣接著經由通氣孔（4 8)離開貯水 池部分5 0而進入外界空氣中。在幾分鐘之後，大部分之 空氣從裝置中被驅離，並且預煮沸器加熱器3 2被關閉， 而冷凝器風扇1 3則打開。具有閥體之通氣孔4 4以及閥 體7 6是關閉的，實際上封閉該裝置而與外界大氣隔離， 並且受限在裝置之中的第二大氣狀況下。或者，該閥體7 6可以是打開的，其係將包括在容置第二大氣狀況之裝置 區域的該預煮沸器。 16 ---------t-------IT------1 (¾先閱1ί背面之注意事項再填寫本頁) 本紙乐尺度適用中國國家標率（CNS ) Λ4规格（210X 297公釐） 422716 Λ7 H7 五、發明说明（) 在第二大氣狀況下，在封閉之裝置中與冷凝器2 4相 接觸之該蒸氣，例如水蒸氣，其係接著被冷卻並且變成蒸 餾液，例如水’創造了在裝置內部之一第三大氣狀況，其 中該第三大氣狀況爲次大氣或是真空狀況。一旦真空達到 大約2 5英吋汞柱，蒸發器部分6 6加熱器1 4被打開， 並且將主要煮沸器中的水加熱至華氏1 3 4度，在主要煮 沸器中的水煮沸而形成一第二蒸氣。轉變成水蒸氣之已煮 沸的水通過連接管件4 1而來到冷凝器2 4，其並且被冷 凝爲蒸餾液1 7 ’在真空下落入聚積部分4 0中。 經濟部中央標率局員工消費合作杜印裝 (請先閱讀背而之注意事項再填寫本頁) 一旦在蒸發部分6 6中的水達到一定的程度，加熱器 1 4被關閉’具有閥體之通氣孔4 4以及進口閥體3 6被 打開，破壞了真空（第三大氣狀況），而蒸餾液17經由 設在連接管件4 6上之閥體4 4而被收集在貯水池部分5 0中。尤其，進口閥體3 6或是可封閉連結3 7被打開以 破壞真空（第三大氣狀況）’並且具有閥體之通氣孔44 接著被打開，以使得在聚積部分4 0中之蒸餾液1 7流入 或漏入貯水池部分5 0。接著，蒸餾液1 7爲了使用而經 由一閥體5 2移離貯水池部分5 0。 將要蒸餾之一批新的水經由具有閥體之可封閉進口埠 3 6或是可拆卸可封閉連結3 7而進入蒸發器部分6 6， 並且該裝置預備好以重複此等過程。聚積部分4 〇之一特 點爲在底部有一小貯水池部分1 9，其係允許了一定量之 蒸餾液被收集用以隨後經由連接管件8 0而漏入預煮沸器 7 0中。 17 本紙張尺度適用中國國家標準（CNS)A4規格（210x 297公揞） 經濟部中央榡準局負工消費合作社印製 Λ7 H7 五、發明説明（/<) 將被了解的是此裝置之一較佳形式包括有自動控制機 構。在此形式中，裝置之操作是在一將在下面所敘述之自 動控制機構的控制之下β至少具有閥體之進口埠3 6、具 有閥體之通氣孔4 4、在蒸發器部分6 6之加熱元件1 4 、及/或風扇13是藉由自動控制機構而在一定時的順序 下自動地操作的，以達成在次大氣壓力下分批蒸餾液體， 而不需要一創造或維持真空之真空泵或真空產生裝置的幫 助。蒸發器6 6以及加熱元件1 4部分亦可以適用於一種 可拆卸可封閉之連結，用以快速地拆除蒸發器6 6，並且 可以快速地將蒸發器6 6可封閉地連結至該裝置。另一實 施例包括使用一如上所述之止回閥作爲閥體4 4。 第四圖顯示了裝置之另一形式，其係包括有一預蒸發 器部分7 0。此形式是相同於在第三圖中所敘述之裝置， 除了蒸發器元件並不具有一加熱元件之外。在真空產生階 段，預煮沸器7 0之加熱器3 2被打開至一高設定快速地 將預煮沸器中的水煮沸，並產生離開預煮沸器並經由閥體 4 4而淨化裝置4 2外空氣之蒸氣，如同之前所提及者。 一旦空氣從裝置被淨化以形成一第二大氣狀況’加熱 器被關閉而風扇1 3則被打開。可能是在電子控制機構的 控制之下之閥體4 4，或是可能爲一獨立於電子控制機構 而操作之機械式止回閥（單向閥）的閥體4 4 ’當水蒸氣 被冷凝並且真空產生時，該閥體4 4係爲自動地關閉的。 在一定的時間之後，加熱器3 2被切換至一較低動力 之設定，並且在次大氣（真空）狀況下於低於華氏2 1 2 .18 本紙張尺度適用中國國家標準（CNS ) Λ4規桔（210X297公犮） .~~, I I I -i «^1 、1T!J 1 » ! I (¾先閱讀背而之注意事項再填寫本頁) Λ7 422116 五、發明説明（/1) 度（例如華氏1 4 0度）之溫度煮沸在預煮沸器中的水， 並且閥體2 9被打開9或者，閥體2 9可以在整個過程中 均爲打開的。當水被煮沸並且進入冷凝器2 4中時，更多 的水藉由簡單之重力，經由管件3 0而從蒸發器6 6供入 預煮沸器中，並且持續此等程序。接著，一旦水落入預煮 沸器以及蒸發器部分至一定的程度，加熱器3 2傳感器關 閉。在此形式中蒸餾液之移除以及控制機構之使用，是相 同於先前第三圖中所敘述者。蒸發器6 6以及加熱元件1 4部分亦可以適用於一種可拆卸可封閉之連結3 7，用以 快速地拆除蒸發器6 6，並且可以快速地將蒸發器6 6可 封閉地連結至該裝置。 县有葙蒸發器部分以及可移動蒸發器部分之直空蒸餾器 在此實施例中，預煮沸器以及主要煮沸器被整合爲一 容器，而相似地*聚積器以及貯水池被組合爲另一容器， 如第五圖所示。第一容室6 9由一隔板7 1不完全地分隔 爲一較小之預煮沸部分以及一較大之主要煮沸容室6 6 〇 預煮沸部分7 0被定位在第一容室6 9之一側。一加熱元 件3 2被定位在預煮沸部分7 0之中間。預煮沸器7 0之 底部以一連接管件3 0而連接至主要煮沸器6 6之底部， 該管件3 0藉由重力而將主要煮沸器液體6 4供給至預煮 沸器液體7 2。該整合之預煮沸器/主要煮沸器第一容室 6 9於可封閉連接3 7處可分離地連接至冷凝器連接管件 4 1，並且可以其可以藉由一把手輕易地拆卸，並且從一 龍頭或從另一容器注入欲蒸餾之液體。接著，第一容室6 n Ϊ It I Γ -n n ; I n .., (评先閱讀t面之注意事項再读寫本頁) 經濟部中央樣準局員工消費合作社印策 本紙張尺度適用中國國家標準（CNS ) Μ現格（210 X 297公釐） 經濟部中央標準局®C工消费合作社印製 Λ7 Η 7 五、發明説明) 9被放回蒸餾器主體之適切位置。 同樣地，聚積器以及貯水池亦被整合爲一容器4 0 ( 第二容室），而具有一用以停止拆卸並且重新定位之適當 的把手（並未顯示）。組合之聚積器/貯水池亦爲可分離 地連接至冷凝器部分出口 2 5 〇容器4 0可以經由出口 4 7而淸空蒸餾液，該出口包括有一閥體4 4，並且接著被 重新定位在蒸餾器之主體上。一旦容器兩者（6 9以及4 0)被放置在其個別之適切位置上，在一側絞接（並未顯 示）之冷凝器2 4被降下並且以機械方式關閉在預煮沸器 /主要煮沸器3 7頂部以及在聚積器/貯水池容器2 5頂 部之氣密連接。 當預煮沸器加熱元件3 2被切換打開時，在預煮沸部 分中之液體7 2迅速地煮沸並且離開預煮沸部分之頂部， 並且進入主要煮沸器部分6 6而與預煮沸器7 0及主要煮 沸器部分6 6中的空氣相混合且淨化該空氣，並且由主要 煮沸器3 7頂部之出口埠3 7驅離，而該蒸氣/空氣混合 氣進入冷凝器管件4 1並接著進入冷凝器2 4 〇該蒸氣/ 空氣混合氣接著離開冷凝器2 4，並且經由在聚積器頂部 的埠2 5而進入了整合之聚積器/貯水池容器4 0中，通 過聚積器/貯水池容器4 0而經由在頂部之出口埠4 7之 單向閥體4 4而離開聚積器/貯水池容器4 0。當跟隨此 一路徑時，來自煮沸器之蒸氣淨化更多來自在蒸餾器內部 包圍部分之空氣，直到數分鐘後空氣之多數都被從該部分 移除^ . ____20 I I » I . ^ n ] ^懷 (iA先閱婧背而之注意事項存填寫本其) 本紙张尺度適用中國國家樣準（CNS ) Λ4規格（210X297公赀） 似”6 五、發明説明（β) Α7 Η7 Μ濟部中央標隼局員工消費合作社印製 本發明更進一歩的實施例被顯示在第六圖中。在此實 施例中’主要煮沸器6 6包括一單一容室，而在其底部具 有兩加熱元件1 4、3 2。聚積器與貯水池被組合爲一單 一容室4 0 ’如第六圖中所示。煮沸器6 6藉由一連接器 37可分離地連接至冷凝器進口41，並且可以輕易地藉 由一把手（並未顯示）而移除，並且從一龍頭或是從另一 容器注入欲蒸餾之液體。接著，煮沸器6 6被放回蒸餾器 主體之適切位置。 同樣地，聚積器以及貯水池亦被整合爲一容器4 0， 而具有一用以停止拆卸並且重新定位之適當的把手（並未 顯示）。組合之聚積器/貯水池亦爲可分離地連接至冷凝 器部分出口 2 5。貯水池可以經由可分離之出口埠4 7而 將蒸餾液淸空，其中該出口埠容置有閥體4 4，Μ且接著 被重新定位在蒸餾器之主體上。一旦容器4 0與6 6兩者 被放置在其個別之適切位置上，整合地連接並且在一側絞 接（並未顯示）之冷凝器2 4、風扇1 3、以及冷凝管4 1，其係被降下並且以機械方式關閉在預煮沸器/主要煮 沸器3 7頂部以及在聚積器/貯水池容器2 5頂部之氣密 連接。 當加熱元件1 4以及3 2兩者被打開時，在煮沸器6 6中之液體6 4迅速地煮沸，並且所產生之蒸氣相混並淨 化煮沸器6 6中的空氣，由煮沸器6 6頂部之出口埠3 7 離開，而該蒸氣/空氣混合氣通過冷凝器管件4 1並接著· 進入冷凝器2 4。該蒸氣/空氣混合氣通過並接著離開冷 21 (請先閱讀背面之注意事項再填鸿本頁)The standard of this paper is applicable to China National Standards (CNS > Λ # 哥格 (210 × 297 mm)) Printing policy of Shellfish Consumer Cooperatives, Central Standards Bureau of the Ministry of Economic Affairs ... Explanation (/ M 8 2 and filled with liquid from an external liquid source. Water from the above source is injected into the preboiler to a predetermined degree and the appropriate valve body 2 9, 7 8, 86, or 8 2 is closed The valve body 76 is then opened, and then the heater 14 in the pre-boiler 70 is also opened, and a small amount of liquid water 72 is quickly boiled in the pre-boiler. In another form, The valve body 76 can be opened throughout the process. The liquid quickly switches to the first vapor or water vapor, which leaves the pre-boiler 70 through the outlet pipe fitting 7 4 with the valve body and enters the evaporator section. The upper part 6 8 of 6 6 is mixed with the air, and then leaves the evaporator part 6 6 through the connecting pipe 41 and enters the condenser 2 4 shaped as a condensing coil. The vapor / air mixture passes through the condenser 2 4 and enter the accumulation part 4 0, and with the accumulation part The air in 40 is mixed, then exits from the bottom of the accumulation part through the vent hole 4 4 with the valve body, and enters the reservoir part 50 through the second pipe piece 46. The vapor is distilled in the reservoir part 50 The lower surface condenses, and the air purified from the device then exits the reservoir section 50 through the vent hole (48) and enters the outside air. After a few minutes, most of the air is driven away from the device and pre-boiler The heater 32 is turned off, and the condenser fan 13 is turned on. The vent holes 44 and the valve body 76 with the valve body are closed, and the device is actually closed to be isolated from the outside atmosphere, and is confined to the device. Under the second atmospheric condition. Alternatively, the valve body 76 may be open, which is to include the pre-boiler in the area of the device housing the second atmospheric condition. 16 --------- t ------- IT ------ 1 (¾Read the precautions on the back of 1ί before filling this page) The paper scale is applicable to China National Standards (CNS) Λ4 specifications (210X 297 mm) 422716 Λ7 H7 V. Description of the invention () In the second atmospheric condition, The vapor, such as water vapor, that is in contact with the condenser 24 is then cooled and turned into a distillate, such as water, which creates a third atmospheric condition inside the device, where the third atmospheric condition is secondary Atmospheric or vacuum conditions. Once the vacuum reaches approximately 25 inches of mercury, the evaporator section 66 heater 14 is turned on and the water in the main boiler is heated to 134 degrees Fahrenheit in the main boiler. The boiled water is boiled to form a second vapor. The boiled water that has been converted into water vapor passes through the connecting piece 41 to the condenser 2 4 and is condensed into a distillate 1 7 ′ which drops into the accumulation part 4 0 in a vacuum. in. The staff of the Central Standards Bureau of the Ministry of Economic Affairs's consumer cooperation Du printed equipment (please read the precautions before filling this page) Once the water in the evaporation part 6 6 reaches a certain level, the heater 1 4 is turned off 'has a valve body The vent hole 4 4 and the inlet valve body 36 are opened, breaking the vacuum (third atmospheric condition), and the distillate 17 is collected in the reservoir portion 50 through the valve body 4 4 provided on the connecting pipe piece 4 6. . In particular, the inlet valve body 36 or the closable connection 37 is opened to break the vacuum (third atmospheric condition) and the vent hole 44 having the valve body is then opened so that the distillate 1 in the accumulation portion 40 7 flows into or leaks into the reservoir section 50. Next, the distillate 17 is removed from the reservoir portion 50 through a valve body 52 for use. A new batch of water to be distilled enters the evaporator section 66 through a closable inlet port 36 with a valve body or a detachable closable connection 37, and the device is prepared to repeat these processes. One feature of the accumulation section 40 is a small reservoir section 19 at the bottom, which allows a certain amount of distillate to be collected for subsequent leakage into the pre-boiler 70 through the connecting pipe 80. 17 This paper size is in accordance with Chinese National Standard (CNS) A4 (210x 297 g). Printed by the Consumers' Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs Λ7 H7 V. Description of Invention (/ <) A preferred form includes an automatic control mechanism. In this form, the operation of the device is under the control of an automatic control mechanism which will be described below. Β has at least an inlet port of the valve body 3 6, a vent hole with a valve body 4 4, and an evaporator portion 6 6 The heating element 1 4 and / or the fan 13 are automatically operated in a certain sequence by an automatic control mechanism to achieve batch distillation of liquid at sub-atmospheric pressure without the need to create or maintain a vacuum. With the help of a vacuum pump or vacuum generator. The evaporator 66 and the heating element 14 can also be applied to a detachable and closable connection for quickly removing the evaporator 66, and the evaporator 66 can be quickly and hermetically connected to the device. Another embodiment includes using a check valve as described above as the valve body 44. The fourth figure shows another version of the device which includes a pre-evaporator section 70. This form is the same as the device described in the third figure, except that the evaporator element does not have a heating element. During the vacuum generation phase, the heater 32 of the preboiler 70 is turned on to a high setting to quickly boil the water in the preboiler, and leave the preboiler and pass through the valve body 4 4 to purify the device 4 2 outside. Vapor of air, as mentioned before. Once the air is purified from the device to form a second atmospheric condition, the heater is turned off and the fan 13 is turned on. It may be the valve body 4 4 under the control of the electronic control mechanism, or the valve body 4 4 may be a mechanical check valve (one-way valve) that operates independently of the electronic control mechanism. When the water vapor is condensed And when the vacuum is generated, the valve body 44 is automatically closed. After a certain period of time, the heater 32 is switched to a lower power setting, and it is lower than Fahrenheit 2 1 2 .18 under subatmospheric (vacuum) conditions. This paper standard applies the Chinese National Standard (CNS) Λ4 regulations Orange （210X297 公 犮）. ~~, III -i «^ 1, 1T! J 1»! I (¾Read the precautions before filling in this page) Λ7 422116 V. Description of the invention (/ 1) Degree ( For example, water boiled in a pre-boiler at a temperature of 140 degrees Fahrenheit, and the valve body 29 is opened 9 or the valve body 29 may be opened throughout the process. When the water is boiled and enters the condenser 24, more water is supplied from the evaporator 66 to the pre-boiler by simple gravity through the pipe 30, and this process is continued. Then, once the water falls into the pre-boiler and evaporator section to a certain extent, the heater 32 sensor is turned off. The removal of the distillate and the use of the control mechanism in this form are the same as those described in the previous third figure. The evaporator 66 and the heating element 14 can also be applied to a detachable and closable connection 3 7 for quickly removing the evaporator 6 6 and quickly closing the evaporator 6 6 to the device. . The prefective evaporator and the movable evaporator section of the vertical distillation still in this embodiment, the pre-boiler and the main boiler are integrated into one container, and similarly * the accumulator and the reservoir are combined into another container As shown in the fifth figure. The first compartment 69 is incompletely partitioned by a partition 7 1 into a smaller pre-boiled part and a larger main boiling part 6 6. The pre-boiled part 7 0 is positioned in the first compartment 6 9 One side. A heating element 32 is positioned in the middle of the pre-boiling portion 70. The bottom of the preboiler 70 is connected to the bottom of the main boiler 66 with a connecting pipe 30, which supplies the main boiler liquid 64 to the preboiler liquid 72 by gravity. The integrated pre-boiler / main boiler first compartment 6 9 is detachably connected to the condenser connection pipe 41 at the closable connection 37, and it can be easily disassembled by a handle and removed from a tap Or inject the liquid to be distilled from another container. Next, the first container room 6 n Ϊ It I Γ -nn; I n .., (Review the notes on t side before reading and writing this page) The Central Consumer Standards Bureau of the Ministry of Economic Affairs Employee Cooperative Co., Ltd. Printed paper This paper is applicable Chinese National Standard (CNS) M is now (210 X 297 mm) Printed by the Central Standards Bureau of the Ministry of Economic Affairs® C Industrial Consumer Cooperatives Λ7 Η 7 V. Description of the invention) 9 It is returned to the proper position of the main body of the still. Similarly, the accumulator and reservoir are integrated into a container 40 (second compartment), with a suitable handle (not shown) to stop disassembly and reposition. The combined accumulator / reservoir is also detachably connected to the condenser section outlet 2 5 0. The container 40 can be emptied of the distillate via the outlet 4 7 which includes a valve body 4 4 and is then repositioned for distillation On the body of the device. Once both containers (69 and 40) are placed in their respective appropriate positions, the condensers 2 4 spliced on one side (not shown) are lowered and mechanically closed in the pre-boiler / main boiling Airtight connection on top of accumulator 3 7 and on top of accumulator / reservoir container 2 5. When the pre-boiler heating element 32 is switched on, the liquid 72 in the pre-boiler section quickly boils and leaves the top of the pre-boiler section, and enters the main boiler section 66, and the pre-boiler 70 and the main The air in the boiler section 66 is mixed and purifies the air, and is driven away by the outlet port 37 on the top of the main boiler 37, and the vapor / air mixture enters the condenser pipe 41 and then enters the condenser 2. The steam / air mixture then leaves the condenser 24 and enters the integrated accumulator / reservoir container 40 through port 25 on the top of the accumulator, and passes through the accumulator / reservoir container 40 through The one-way valve body 44 of the top outlet port 47 leaves the accumulator / reservoir container 40. When following this path, the steam from the boiler purifies more of the air that surrounds the part inside the still, until a few minutes after the majority of the air is removed from the part ^. ____20 II »I. ^ N] ^ Huai (iA first read Jing's back and keep the notes) Please fill in this paper size China National Standard (CNS) Λ4 specification (210X297) 赀 Like "6 V. Description of invention (β) Α7 Η7 Μ central A further embodiment of the invention printed by the Standards Bureau employee consumer cooperative is shown in the sixth figure. In this embodiment, the 'primary boiler 6 6 includes a single chamber with two heating elements 1 at its bottom 4, 3 2. The accumulator and storage tank are combined into a single container 40 'as shown in the sixth figure. The boiler 66 is detachably connected to the condenser inlet 41 through a connector 37, and can be easily connected The ground is removed by a handle (not shown), and the liquid to be distilled is injected from a faucet or from another container. Then, the boiler 66 is returned to a proper position of the main body of the distillation. Similarly, the accumulator And the cistern is also integrated into A container 40, with an appropriate handle (not shown) to stop disassembly and reposition. The combined accumulator / reservoir is also detachably connected to the condenser section outlet 25. The reservoir can be separated by The outlet port 4 7 empties the distillate, wherein the outlet port contains the valve body 4 4M and is then repositioned on the main body of the still. Once both the containers 40 and 6 6 are placed on it In individual suitable locations, condenser 2 4, fan 1 3, and condenser tube 1 1 integratedly connected and twisted on one side (not shown) are lowered and mechanically closed in the preboiler / Airtight connection at the top of the main boiler 3 7 and at the top of the accumulator / reservoir container 2 5. When both the heating elements 1 4 and 3 2 are opened, the liquid 6 4 in the boiler 6 6 quickly boils, and The generated vapor mixes and purifies the air in the boiler 6 6 and exits from the outlet port 3 7 at the top of the boiler 6 6, and the vapor / air mixture passes through the condenser pipe 4 1 and then · enters the condenser 2 4 The vapor / air mixture passes Then leave the cold 21 (please read the Notes on the back of Hong reloading the page)
hL Γ - 本紙張尺度適用中國國家標準（CNS ) Λ4現格（2!〇><297公發） 五、發明説明（ Λ7 Ii7 經濟部中央標準局貝工消費合作社印製 凝器2 4 ’並且經由在聚積器2 5頂部的埠而進入了整合 之聚積器/貯水池容器4 0中，淨化來自容器4 0內部之 空氣，並且最後經由頂部之出口埠4 7的單向閥體4 4而 離開容器4 0。當跟隨此一路徑時，蒸氣淨化更多來自在 蒸餾器內部包圍部分之空氣，直到數分鐘後空氣之多數都 被從該蒸餾器部分移除。 一旦淨化步驟完成，煮沸器加熱元件3 2之一被關閉 ’加熱元件1 4仍是打開的，並且風扇1 3是打開的》當 蒸氣在冷凝器2 4中冷凝時，熱量被風扇1 3所帶走，在 貯水池容室4 0出口處之單向閥4 4關閉，封閉該蒸餾器 之內部空間並因此在蒸餾器內部形成一真空，並從而降低 了在煮沸器中的沸點。當更多的水蒸氣被冷凝時，沸點持 續降低，直到達到一大約爲華氏1 4 0度之最小沸點溫度 爲止。煮沸持續進行，直到煮沸器6 6中之液體6 4降至 由一感測器（並未顯示）所決定之一定程度爲止，並且加 熱元件1 4接著被關閉。一按鈕（並未顯示）被壓下，用 以破壞蒸餾器內部之真空，並接著冷凝器組件在其鉸接處 被旋開，破壞了如上所述在兩容室頂部之封閉的連接2 5 及3 7。接著，聚積器/貯水池容器4 0被移開，並且蒸 餾液1 7經由聚積器/貯水池容器進口埠4 7而被倒入另 一容器中。該預煮沸器/主要煮沸器容室6 6亦被移開， 並且注入欲蒸餾之新的液體，並且重複此等程序。 吾人所了解的是第五圖與第六圖中的實施例更包括在 蒸餾裝置與可移去第一及第二容室（第五圖中之4 0以及 22 {計先閲讀背面之注意事項再填耗本頁} •淨. -a rhL Γ-This paper size is applicable to Chinese National Standard (CNS) Λ4 is present (2! 〇 > < 297) 5 、 Explanation of the invention (Λ7 Ii7 Printed condenser by Shellfish Consumer Cooperative of Central Standards Bureau of Ministry of Economic Affairs 2 4 'And entered the integrated accumulator / reservoir container 40 through the port on the top of the accumulator 25, purifies the air from the inside of the container 40, and finally passes the one-way valve body 4 4 on the top outlet port 4 7 And leave the container 40. When following this path, the steam purifies more from the air surrounding the portion of the distiller, until most of the air is removed from the distiller after a few minutes. Once the purification step is complete, boil One of the heater heating elements 3 2 is turned off 'The heating element 14 is still on and the fan 13 is on. When the steam is condensed in the condenser 24, the heat is taken away by the fan 13 and is stored in the reservoir. The check valve 44 at the outlet of the chamber 40 is closed, closing the internal space of the distiller and thus creating a vacuum inside the distiller, and thereby reducing the boiling point in the boiler. When more water vapor is condensed , Boiling point continues Decrease until reaching a large minimum boiling point temperature of about 140 degrees Fahrenheit. Boiling continues until the liquid 6 4 in the boiler 6 6 reaches a certain level determined by a sensor (not shown) And the heating element 1 4 was then turned off. A button (not shown) was pressed to break the vacuum inside the still, and then the condenser assembly was unscrewed at its hinge, destroying the two The closed connections 2 5 and 37 at the top of the chamber. Next, the accumulator / reservoir container 40 is removed and the distillate 17 is poured into another container via the accumulator / reservoir container inlet port 47. The pre-boiler / main boiler chamber 66 is also removed, and a new liquid to be distilled is injected, and these procedures are repeated. What I understand is that the embodiments in the fifth and sixth figures further include In the distillation unit and the first and second chambers can be removed (40 and 22 in the fifth picture {count the precautions on the back before filling this page} • net. -Ar
I 本紙張尺度適用中國國家標隼（CNS ) Λ4現格（210 X 297公# ) Λ7 117 經濟部中央標率局βί工消费合作社印聚 五、發明説明（/) 69 :第六圖中之66以及40)之間電子連接，並且第 十三圖與第十四圖中所揭露之邏輯與控制元件包括有在此 所述之自動控制機構。 具有冷凍系統之直衣菡餾袈 第七圖說明了本發明真空蒸餾器與一冷凍系統相組合 之設計。此實施例合倂有上述之具有預蒸發器7 0以及貯 水池部分5 0的實施例（第三圖），其更包括有冷凍設備 ，其以一冷凍循環而達成在蒸發器部分6 6中該批水4 4 之加熱，以及在聚積部分4 0中蒸氣之冷凝。 在此實施例中，包含有一冷凍系統之冷凝線圏的加熱 元件1 4，其係將熱給予欲蒸餾之水，並且包括有冷凍系 統蒸發器之該冷凝部分2 4，其係將蒸氣之熱帶走，將其 在冷凝部分4 0中冷凝爲蒸餾液。第七圖顯示了蒸氣在冷 凍冷凝線圈2 4外部冷凝並且落入聚積部分4 0中。預煮 沸器7 0被用以製造一第一蒸氣水蒸氣，用以如同過去般 創造真空系統。然而，在使用一冷凍系統之實施例中，其 真空度較使用一風扇冷卻冷凝器之實施例高出相當多。一 2 9英吋汞柱之真空度可以達成，是因爲在冷凍蒸發器線 圈2 4中較低溫度的緣故。此相映於一在蒸發器部分6 6 中大約華氏7 6度的沸點溫度，使得水之加熱與煮沸較容 易達成，並且需要較少之能量。 在操作中，此過程是相同於在第三圖中所述者。次大 氣狀況或是真空是藉由在預煮沸器中使用一加熱器3 2將 水煮沸爲蒸氣，並且利用該蒸氣將空氣驅離該裝置所創造 23 本紙張尺度適用中國國家標準（CNS ) Λ4規格（210Χ29?公犮） ---------裝1Γ--；---訂---------泉 (請先閱讀背面之注意事項再球湾本頁) 經濟部中央標率局月工消費合作社印製 A22” 豸 Λ7 Η7 五、發明说明（yl) 出來的，接著’該裝置藉由關閉具有閥體之通氣孔4 4而 被封閉以與大氣相隔離=爲了避免冷凍系統之過熱’在真 空產生階段期間’連接聚積部分2 4與冷凍壓縮器1 0之 一管件2 8，其係在水6 4的沉浸之下通過蒸發器部分6 6。包括有冷凍冷凝線圈之加熱元件1 4 ’其係沉浸在蒸 發器部分6 6的水中’接著將蒸發器部分6 6中的水加熱 至至華氏7 6度而開始沸騰。 冷凍系統之一優點爲：由於其性能係數（C Ο Ρ，最 大至5.0)，當與一標準蒸餾系統相較時，煮沸—加侖水 之能量需求最多降至8 0 %。這是一很重要的能量節省， 尤其是在電力相當昂貴之區域。此能量之節省可以彌補冷 凍系統之額外資金消耗。該裝置冷凍形式之操作更詳細的 說明被包括在第六圖中。 洽浦循環蒸餾裝置 第八圖顯示了使用一冷凍循環之本發明的一較佳實施 例，其係將預煮沸器7 〇、蒸發器6 6、以及聚積部分4 0整合在一容室內。如第八圖所示之整合的容室（4 2 ) ，其係將一安置在該整合容室4 2底部之一蒸發器部分（ 6 6 )的水蒸發器加熱兀件（1 4 )、一安置有另一加熱 元件（3 2 )之預煮沸器或預蒸發器部分（7 0)、一蒸 氣冷凝器（2 4)、以及一聚積部份或蒸餾液收集器（4 0)合倂爲一整合裝置或單元。此實施例亦容置有一冷卻 器（2 0)以及一貯水池部分或蒸餾液貯水池〔5 0 )。 該整合之容室亦包括一具有閥體之進口埠（水進口閥）（ ______24_ 度i用^國國家標準{ CNS )八4规格{ 210X297公释) 裝 1» n n 银 (請先閱讀背面之注念事項再填荇本頁) -f-------- --------------- 經濟部中央榡隼局員工消费合作社印聚 pm - 五、發明説明（Ί 3 δ )’以及一蒸餾液排放閥（4 4 )與一排水閥（3 8 )3冷凍管線1 2、2 9、1 8、2 3通過整合容室之邊I This paper size is applicable to Chinese National Standards (CNS) Λ4 is now (210 X 297 public #) Λ7 117 Printed by the Central Standards Bureau of the Ministry of Economic Affairs βίconsumer cooperative Fifth, the description of the invention (/) 69: 66 and 40), and the logic and control elements disclosed in Figures 13 and 14 include the automatic control mechanism described herein. Straight garment distillation with a refrigeration system. Figure 7 illustrates the design of a combination of a vacuum still with a refrigeration system of the present invention. This embodiment combines the above-mentioned embodiment (the third figure) with a pre-evaporator 70 and a reservoir portion 50, which further includes a refrigeration device, which is achieved in a evaporator cycle by a refrigeration cycle. Heating of batch water 4 4 and condensation of steam in the accumulation part 40. In this embodiment, a heating element 14 including a condensation line of a refrigeration system is used to impart heat to the water to be distilled, and the condensation portion 2 4 of the refrigeration system evaporator is included, which is a tropical zone of vapor. Go and condense it into a distillate in the condensing section 40. The seventh figure shows that the vapor condenses outside the freezing condensation coil 24 and falls into the accumulation portion 40. The pre-boiler 70 is used to make a first vapor water vapor to create a vacuum system as in the past. However, in the embodiment using a refrigeration system, the degree of vacuum is considerably higher than the embodiment using a fan to cool the condenser. A vacuum of 29 inches of mercury can be achieved due to the lower temperature in the freezer coil 24. This phase is reflected in a boiling point temperature of about 76 degrees Fahrenheit in the evaporator section 6 6, which makes heating and boiling of water easier and requires less energy. In operation, this process is the same as described in the third figure. Sub-atmospheric conditions or vacuum are created by using a heater 32 in a pre-boiler to boil water into steam, and use the steam to drive the air away from the device. 23 The paper size applies Chinese National Standards (CNS) Λ4 Specifications (210 × 29? Male) --------- install 1Γ--; --- order --------- quan (please read the precautions on the back first, then the ball bay page) economy The Ministry of Standards and Standards Bureau printed A22 "月 Λ7 Η7 V. The description of the invention (yl), then 'The device is closed to isolate the atmosphere by closing the vent hole 4 4 with the valve body = In order to avoid overheating of the refrigeration system 'during the vacuum generation phase', the accumulation section 24 is connected to one of the refrigeration compressors 10's 28, which is passed through the evaporator section 66 under the immersion of water 64, including refrigeration. The heating element 1 4 of the condensing coil is immersed in the water of the evaporator section 66, and then the water in the evaporator section 66 is heated to 76 degrees Fahrenheit and begins to boil. One advantage of the refrigeration system is that because of its advantages Coefficient of performance (C Ο Ρ, up to 5.0), when compared with a standard distillation system At this time, the energy requirement of boiling-gallon water is reduced to 80% at most. This is a very important energy saving, especially in areas where electricity is quite expensive. This energy saving can make up for the extra capital consumption of the refrigeration system. The device freezes A more detailed description of the operation of the form is included in the sixth figure. The eighth figure of the Harper cycle distillation apparatus shows a preferred embodiment of the present invention using a refrigeration cycle, which uses a preboiler 70, an evaporator 6, 6, and the accumulation part 40 is integrated in a container. The integrated container (4 2) shown in the eighth figure is an evaporator part (6) which is arranged at the bottom of the integrated container 4 2 6) a water evaporator heating element (1 4), a pre-boiler or pre-evaporator section (70) with another heating element (32), a vapor condenser (24), and a The accumulation part or the distillate collector (40) is combined into an integrated device or unit. This embodiment also contains a cooler (20) and a reservoir part or distillate reservoir (50). The integrated The chamber also includes an inlet port with a valve body (water inlet Valve) (______24_ Degrees ^ National Standards {CNS) 8 4 specifications {210X297 public release) Packing 1 »nn silver (please read the notes on the back before filling out this page) -f ------ ---------------- Industry Consumer Cooperatives of the Central Government Bureau of the Ministry of Economic Affairs of the People's Republic of China pm-5. Description of the invention (Ί 3 δ) 'and a distillate drain valve (4 4) With a drain valve (3 8) 3 refrigeration line 1 2, 2 9, 1 8, 2 3 through the side of the integrated container
Bit 壁。 如下所述，本發明之閥體、冷凝器、加熱元件、以及 其他特殊元件’其皆在電子控制機構的控制之下，該電子 控制機構如同一自動控制系統般作用，用以打開加熱器、 製造蒸氣、淨化裝置、封閉裝置以與大氣隔離、關閉加熱 器、以及打開冷凝器以產生真空，並且持續蒸餾液之製造 ’以及排出或收集蒸餾液，此等程序將在以下藉由四個階 段：解：注水、真空產生、蒸餾液製造、以及蒸饉液排出 *而加以更詳細地說明。 由於本發明包括一分批過程，因此第一個步驟包括將 水注入蒸發器部分6 6 β爲了達到此一步驟，蒸餾液/空 氣出口閥（亦即具有閥體之通氣孔4 4)以及水進口閥（ 亦即具有閥體之進口埠3 6 )皆被打開，而排水閥3 8則 是關閉的。在預蒸發部分6 6中之加熱元件3 2是關閉的 。在一大氣壓下，裝置之蒸發器部分6 6經由該具有閥體 之進口埠3 6而充足地注入水，直到液體高度在加熱元件 上方爲止，接著，具有閥體之進口埠3 6被關閉β該系統 現在被加入第一大氣狀況下的水，相等於一大氣壓。 直空產牛 以下產生真空之裝置與方法在裝置中創造了一真空， 而不需使用真空泵或其他產生裝置，並且其係基於一簡單 25 ， 本紙張尺度適用中國國家標率（CNS )Λ4規格（2】0Χ 297公艎） ---------^.------it------^ (請先閱讀背而之注意事π 知寫本頁) 4221 Ί at B7 經濟部中央梯準局員工消費合作社印製 五、發明説明（γ 5 ) 之加熱裝置，該加熱裝置之操作如下：在水連續地從蒸發 器部分6 6經由連接管件3 0而供應至預蒸發部分7 0的 同時，打開安置在蒸發器部分6 6中之加熱元件3 2以產 生一第一蒸氣（例如水蒸氣）。在裝置包括有一冷凍系統 (第七圖至第十二圖）的形式下，經由加熱元件1 2所產 生之第一蒸氣水蒸氣，其亦將冷凍劑蒸發器2 4內部的冷 凍劑蒸氣加熱至一過熱狀態。爲了冷卻該過熱之冷凍劑， 沉浸在蒸發器部分6 6水中的熱交換器2 8將充足地降低 過熱之冷凍劑溫度，以允許真空循環繼續進行。 經由加熱元件3 2所產生之第一蒸氣，其係隨著最初 受限於裝置4 2之空氣*經由蒸餾液/空氣出口閥〔亦即 具有閥體之通氣孔）4 4、連接器管件4 6、以及蒸餾液 貯水槽5 0而被推出，其並且最後從蒸餾液貯水槽5 0頂 部之空氣排出通氣孔4 8排放出去。當一些冷蒸餾液出現 時，一些蒸氣將在蒸餾液貯水槽5 〇中被冷凝。 裝置4 2之內部被加襯以一絕綠襯裡，用以降低蒸氣 在其表面上的冷凝作用，其將使蒸氣停止而不會代替容室 的空氣。藉由加熱元件3 2所產生之水蒸氣將稀釋裝置4 2中的空氣直到數分鐘之後爲止，該裝置最後將幾乎完全 地充滿水蒸氣，而形成一第二大氣狀況β接著，蒸餾液/ 空氣出口閥（亦即具有閥體之通氣孔）4 4被關閉，並且 加熱元件3 2被關上。 由此觀點’裝置4 2中之壓力將相應於水蒸氣之溫度 。當冷凍機壓縮器1 〇被打開，並且冷凝器2 4將水蒸氣 _ 26 (婧先Μ讀背而之注意事項洱填寫本頁)Bit wall. As described below, the valve body, the condenser, the heating element, and other special elements of the present invention are all under the control of an electronic control mechanism, which functions like the same automatic control system to turn on the heater, Manufacture of vapors, purification devices, enclosures to isolate them from the atmosphere, turn off heaters, and open condensers to create vacuum, and continue the production of distillate, and drain or collect the distillate. These procedures will be followed in four stages : Solution: Water injection, vacuum generation, production of distilled liquid, and discharge of distilled liquid * will be explained in more detail. Since the present invention includes a batch process, the first step includes injecting water into the evaporator section 6 6 β. To achieve this step, the distillate / air outlet valve (ie, the vent hole 4 4 with the valve body) and water The inlet valve (that is, the inlet port 36 with a valve body) is opened, and the drain valve 38 is closed. The heating element 32 in the pre-evaporation section 66 is turned off. At atmospheric pressure, the evaporator portion 66 of the device is sufficiently filled with water through the inlet port 36 with the valve body until the liquid height is above the heating element, and then the inlet port 36 with the valve body is closed β The system is now added to water in the first atmospheric condition, which is equal to one atmosphere. The vacuum generating device and method for direct air production are to create a vacuum in the device without the use of a vacuum pump or other generating device, and it is based on a simple 25. This paper standard applies to China National Standard (CNS) Λ4 specifications (2) 0 × 297 public 艎) --------- ^ .------ it ------ ^ (Please read the precautions before knowing how to write this page) 4221 Ί at B7 Printed by the Consumer Cooperatives of the Central Ladder Bureau of the Ministry of Economic Affairs. 5. The heating device of the invention description (γ 5). The operation of the heating device is as follows: Water is continuously supplied from the evaporator section 6 6 to the connecting pipe 30. At the same time as the pre-evaporation section 70, the heating element 32 disposed in the evaporator section 66 is turned on to generate a first vapor (for example, water vapor). In the form that the device includes a refrigeration system (Figures 7 to 12), the first vapor water vapor generated by the heating element 12 also heats the refrigerant vapor inside the refrigerant evaporator 2 4 to An overheated state. To cool the superheated refrigerant, the heat exchanger 28 immersed in the water of the evaporator section 66 will sufficiently reduce the temperature of the superheated refrigerant to allow the vacuum cycle to continue. The first vapor generated by the heating element 32 is connected with the air initially restricted by the device 42 through the distillate / air outlet valve (ie, the vent hole with the valve body) 4 4. The connector pipe 4 6. The distillate storage tank 50 is pushed out, and it is finally discharged from the air exhaust vent 48 at the top of the distillate storage tank 50. When some cold distillate appears, some vapor will be condensed in the distillate storage tank 50. The inside of the device 42 is lined with an absolutely green lining to reduce the condensation of steam on its surface, which will stop the steam without replacing the air in the chamber. The water vapor generated by the heating element 32 will dilute the air in the device 4 2 until a few minutes later, the device will finally be almost completely filled with water vapor to form a second atmospheric condition β. Next, the distillate / air The outlet valve (ie, the vent hole with the valve body) 4 4 is closed, and the heating element 32 is closed. From this point of view, the pressure in the device 42 will correspond to the temperature of the water vapor. When the freezer compressor 10 is opened, and the condenser 2 4 will be water vapor _ 26 (Jingxian M read the back and note 洱 fill out this page)
I 本紙張尺度賴til财料（CNS) (21QX297公雄） 經濟部中央榡率局貝工消費合作、社印聚 Α7 Β7 五、發明説明f ) 冷卻爲水時，裝置4 2中水蒸氣之壓力將會隨著水蒸氣温 度而下降，從而在裝置操作期間達到了一爲次大氣或真空 狀況之第三大氣狀況。冷凍循環將產生一範圍介於2 7 -2 9英吋汞柱之間的真空裝況。而此甚至在進來的水並未 除氣的狀況下亦會發生。 蒸餾液製浩 蒸餾液製造之過程包括兩個如下所述之部分··（a) 水蒸發與冷凝劑冷凝；以及（b)水蒸氣冷凝與冷凝劑蒸 發。 水蒸發铤冷凝劑冷凝 在裝置包括有一冷凍系統的形式下，壓縮器1〇現在 被打開，而過熱之冷凍劑蒸氣被排出壓縮器10外。冷凍 劑過熱蒸氣行徑至安裝在蒸發器部分6 6之冷凍劑冷凝器 或加熱元件1 4之頂部。加熱元件之形式爲一管狀線圈， 其係從點1 2延伸至點1 8，並且是安置在蒸發器部分6 6中。冷凍劑冷凝器線圈14被分成兩個部分^線圈14 之上部被容置在覆蓋物1 6之圓柱狀部分內，而在線圈1 4之底部則被覆蓋以覆蓋物1 6之圓盤造型部分。在蒸發 器部分6 6的該批水在真空狀況下被冷凍劑所加熱β 水在冷凍劑冷凝器1 4之底部被預熱，並且持續加熱 至冷凍劑冷凝器1 4之上部。在水面高度1 — 2英吋下方 的水達到一過熱狀態，並且產生了一水蒸氣/水之混合物 。水蒸氣/水之混合物從覆蓋物1 6上部內突然冒出來， 並且衝撞蒸氣分離器3 4。 ___ 27 裝丨-----—訂------涑 (請先|«1讀背面之注意事項再填寫本頁> 紙張尺度適用ϊ{ϊ國囡豕棉球（CNS)Λ4規格（210χ297公¢ A7 H7 五、發明説明) 蒸氣經由蒸氣分離器3 4而上升至冷凝劑蒸發器/水 蒸氣冷凝器2 4，而同時水落下至覆蓋物1 6之外部。由 於蒸氣與液體密度之不同，在覆蓋物1 6之圓柱狀部分頂 部外的水被強迫向下，並接著在覆蓋物1 6之底部平板部 分下注入，並接著上升至覆蓋物1 6之圓柱狀部分內。此 增強了循環，熱傳裝置提升了在冷凍劑冷凝器1 4中水6 4與冷凍劑之間的對流熱傳。 當時，冷凍劑在蒸發器部份6 6中被水連續地冷凝。 低蒸氣比率之飽和冷凍劑接著行徑至冷卻器2 0，並且持 續地冷凝至一液體狀態。 7k菡氳冷凝/冷凝劑菡發 此時，冷凍劑經由冷凍劑壓力降低裝置22(例如膨 脹閥或毛細管）而流入冷凝劑蒸發器/水蒸氣冷凝器2 4 中。在擴張過程期間，液態冷凍劑溫度會顯著地下降。 經濟部中央標準局貝工消费合作社印» {饵先閱讀背面之注意事項再填寫本頁) 冷凍劑蒸發溫度爲了水而被選定在華氏3 2度以上， 用以防止凍結。在冷凝劑蒸發器/水蒸氣冷凝器2 4內的 冷凍劑，其係吸收來自蒸氣的能量，並且冷凝劑蒸發器/ 水蒸氣冷凝器2 4如同一蒸發管般作用以將冷凍劑在管子 內蒸發。 當時，水蒸氣釋放能量，其並且在冷凝劑蒸發器/水 蒸氣冷凝器2 4外被冷凝。冷凝液下落至蒸餾液收集器（ 亦即聚積部分）4 0。冷凍劑進入從點2 6延伸至壓縮器 1 0入口之熱交換器2 8。所有離開熱交換器之冷凍劑是 處於單相之蒸氣形式。 28 本紙乐尺度適用中國围家標準（CNS ) Λ4蚬格（210Χ297公烚） 經濟部中央橾準局貝工消资合作社印製 Λ7 Μ 7 五、發明説明wL-) 離開熱交換器2 8之冷凍劑，其通過吸入管路2 9而 到達壓縮器1 0。壓縮過程在此進行。高壓蒸氣接著通過 排出管路而到達冷凍劑冷凝器1 4，從而完成了蒸氣壓縮 冷凍循環。 以上之冷凍循環亦可以被一吸收式冷凍循環所代替。 吸收式冷凍循環是不同於蒸氣壓縮冷凍循環的，其係使用 熱能來代替機械能，用以產生一在完成冷凍循環所必須之 狀況改變。 冷凍循環之使用創造了一種效能提升，其中該效能即 爲由冷凍劑蒸發器2 4所釋放之能量除上輸入冷凍劑壓縮 器1 0之能量的比率，因此在與一簡單蒸餾系統相較之下 而產生了一相當之能量節省。 蒸餾水之製造是從上述水蒸餾循環持續而達成的，直 到在蒸發器部分6 6中液體之高度下降至一定高度爲止。 蒸餾液排出 分批蒸餾過程之下一個部分就是將蒸餾液17從收集 器或聚積部分4 0排出，並進入一外部的貯水池5 0。首 先，打開一允許空氣進入裝置並且破壞真空之進口閥3 6 。蒸餾液出口閥（具有閥體之通氣孔）4 4現在被打開， 並且蒸餾液經由重力而排出至蒸餾液貯水池5 0中。下一 個循環可以在此處開始。 第九圖顯示了本發明包含有冷凍循環之一孤立、商業 實施例。此實施例顯示了本發明一典型之商業形式，其在 蒸餾器容器4 2之下係具有壓縮器1 〇、冷卻器2 〇、蒸 29 ^衣-. . I: .· 、1T111 (¾先閱讀背面之注意事項再填寫本頁) 本紙張尺度適用中國固家標率（CNS )八4说格（210Χ 297公犮） 〜B：__ 五、發明說明) 餾液貯水池5 0 ’如第八圖所示。進口閥3 6穿過外殻4 之邊壁，而蒸餾液排放閥5 2亦是如此。一電源線1 1亦 穿過外殼4用以將電力供應至壓縮器1 0，並且供應至熱 交換器風扇2 1。上述之部件以及外殼皆爲固定地連接至 一支承底座6上。 憝合至一標進家用冰箱之蒸餾系統 第十圖顯示了本發明整合至一標準家用冰箱之典型實 施例的視圖。該視圖顯示了在一冰箱主體內包括有一蒸 餾器容器（4 2)、一蒸餾器貯水池5 0、一冷卻器2 0 、一壓縮器1 0、一電源線1 1。標準冷凍劑蒸發器（6 0)由本發明所分配並且用以冷卻冰箱之內部腔室。 將本發明整合至一家用冰箱之較佳實施例有兩個，將 在以下敘述。 具有冷凍劑蒸發器之水蒸餾裝置 第十一圖詳細地顯示了蒸餾單元之部分截面圖，其係 整合至一標準家用冰箱中並且包括兩相連之冷凍劑蒸發器 線圈，其中一線圈用於蒸餾器，而另一線圏則使用於冰箱 。除了附加之三個三向閥體5 4、與5 6，以及一 連接至冰箱蒸發器6 0之冷凍劑壓力降低_裝置5 8之外， 蒸餾單元之細節是相同於第六圖中所述者。 此系統是由兩個循環所購成的，其中之一循環爲水蒸 餾循環，而另一循環則是冷凍循環。水蒸餾循環已經在以 上之第八圖中敘述過了。冷凍循環是藉由三個三向閥體i 2、5 4、以及5 6所控制的。因此，離開壓縮器1 ◦至 30 本紙張尺度適用中國國家標準（CNS)A4規格（210 X 297公釐) (請先閱讀背面之注意事項再填寫本頁>I Paper size (CNS) (21QX297 male and male) The central government bureau of the Ministry of Economic Affairs, Shellfish Consumer Cooperative, Social Printing Poly A7 B7 V. Description of the invention f) When cooling to water, the pressure of water vapor in device 4 2 It will decrease with the temperature of the water vapour, thereby reaching a third atmospheric condition of a sub-atmospheric or vacuum condition during the operation of the device. The refrigeration cycle will produce a vacuum condition in the range of 27-29 inches of mercury. This can happen even when the incoming water is not degassed. Distillate production The process of distillate production includes two parts as described below: (a) water evaporation and condensation of the condensing agent; and (b) water vapor condensation and evaporation of the condensing agent. Water Evaporation and Condensate Condensation In the form of a unit including a refrigeration system, the compressor 10 is now opened, and the superheated refrigerant vapor is discharged out of the compressor 10. The refrigerant superheated vapor passes to the top of the refrigerant condenser or heating element 14 installed in the evaporator section 66. The heating element is in the form of a tubular coil which extends from point 12 to point 18 and is arranged in the evaporator section 66. The refrigerant condenser coil 14 is divided into two parts. The upper part of the coil 14 is accommodated in a cylindrical part of the cover 16 and the bottom of the coil 14 is covered with a disc shaped part of the cover 16 . The batch of water in the evaporator section 66 is heated by the refrigerant under vacuum. The β water is preheated at the bottom of the refrigerant condenser 14 and is continuously heated to the upper part of the refrigerant condenser 14. Water at a height of 1 to 2 inches below the surface reaches a superheated state and produces a water vapor / water mixture. The water vapor / water mixture suddenly emerged from the upper part of the cover 16 and collided with the vapor separator 34. ___ 27 Packing 丨 ------- Order ------ 涑 (please first | «1 read the precautions on the back before filling this page > paper size applies ϊ {ϊ 国 囡 豕 棉球 （CNS) Λ4 Specifications (210x297 male ¢ A7 H7 V. Description of the invention) The vapor rises to the condenser evaporator / water vapor condenser 2 4 through the vapor separator 34, and at the same time, the water falls to the outside of the cover 16 because of the vapor and liquid The difference in density is that the water outside the top of the cylindrical portion of the cover 16 is forced downward, and then is injected under the bottom plate portion of the cover 16 and then rises into the cylindrical portion of the cover 16. This enhances the circulation, and the heat transfer device improves the convective heat transfer between the water 64 and the refrigerant in the refrigerant condenser 14. At that time, the refrigerant was continuously condensed by the water in the evaporator portion 66. Low The saturated refrigerant with a vapor ratio then travels to the cooler 20, and continuously condenses to a liquid state. 7k 菡 氲 Condensation / Condensate burst At this time, the refrigerant passes through a refrigerant pressure reducing device 22 (such as an expansion valve or a capillary tube). ) Into the condenser evaporator / water vapor condenser 2 4. During the Zhang process, the temperature of the liquid refrigerant will drop significantly. Printed by the Central Bureau of Standards of the Ministry of Economic Affairs, Shelley Consumer Cooperatives »{Read the precautions on the back before filling this page) The evaporation temperature of the refrigerant is selected for Fahrenheit 3 2 Above degree to prevent freezing. The refrigerant in the condensate evaporator / water vapor condenser 24 absorbs energy from the vapor, and the condensate evaporator / water vapor condenser 24 acts as the same evaporation tube to place the refrigerant in the tube. evaporation. At that time, the water vapor released energy and it was condensed outside the condenser evaporator / water vapor condenser 24. The condensate drops to the distillate collector (ie the accumulation part) 40. The refrigerant enters a heat exchanger 28 extending from point 26 to the compressor 10 inlet. All refrigerant leaving the heat exchanger is in the form of a single-phase vapor. 28 The paper scale is applicable to the Chinese Enclosure Standard (CNS) Λ4 grid (210 × 297 gong) Printed by Λ7 Μ7 of the Central Government Bureau of Standards of the Ministry of Economic Affairs 工 7 Μ 7 5. Description of the invention wL-) Leave the heat exchanger 2 8 The refrigerant passes through the suction line 29 and reaches the compressor 10. The compression process takes place here. The high-pressure vapor then reaches the refrigerant condenser 14 through the discharge line, thereby completing the vapor compression refrigeration cycle. The above refrigeration cycle can also be replaced by an absorption refrigeration cycle. The absorption refrigeration cycle is different from the vapor compression refrigeration cycle. It uses thermal energy instead of mechanical energy to generate a change in conditions necessary to complete the refrigeration cycle. The use of the refrigeration cycle creates an efficiency improvement, where the efficiency is the ratio of the energy released by the refrigerant evaporator 24 divided by the energy input to the refrigerant compressor 10, so it is compared with a simple distillation system This resulted in a considerable energy savings. The production of distilled water is achieved from the continuation of the above-mentioned water distillation cycle, until the height of the liquid in the evaporator section 66 drops to a certain height. Distillate discharge The next part of the batch distillation process is to remove the distillate 17 from the collector or accumulation section 40 and enter an external storage tank 50. First, an inlet valve 36 is opened which allows air to enter the device and destroys the vacuum. The distillate outlet valve (with a vent hole of the valve body) 44 is now opened, and the distillate is discharged into the distillate reservoir 50 by gravity. The next cycle can begin here. The ninth figure shows an isolated, commercial embodiment of the invention including one of the refrigeration cycles. This embodiment shows a typical commercial form of the present invention, which has a compressor 10, a cooler 20, and a steamer 29 under the still vessel 4 2. I: .1, 1T111 (¾ 先Read the notes on the back and fill in this page again.) This paper scale is applicable to China Standards of Household Standards (CNS) 8 and 4 (210 × 297 cm) ~ B: __ V. Description of the invention) Distillate tank 5 0 'As the eighth As shown. The inlet valve 36 passes through the side wall of the casing 4, and so does the distillate discharge valve 52. A power cord 11 is also passed through the casing 4 to supply power to the compressor 10 and to the heat exchanger fan 21. The above-mentioned components and the housing are fixedly connected to a support base 6. Distillation system coupled to a standard domestic refrigerator. Figure 10 shows a view of a typical embodiment of the present invention integrated into a standard domestic refrigerator. This view shows that a main body of a refrigerator includes a distiller container (42), a distiller reservoir 50, a cooler 20, a compressor 10, and a power cord 11. A standard refrigerant evaporator (60) is dispensed by the present invention and is used to cool the internal cavity of the refrigerator. There are two preferred embodiments for integrating the present invention into a household refrigerator, which will be described below. Water Distillation Device with Refrigerant Evaporator Figure 11 shows in detail a partial cross-sectional view of the distillation unit, which is integrated into a standard domestic refrigerator and includes two connected refrigerant evaporator coils, one of which is used for distillation While the other cord is used in the refrigerator. The details of the distillation unit are the same as those described in the sixth figure, except for the three three-way valve bodies 5, 4, and 56, and a refrigerant pressure reduction device 608 connected to the evaporator 60 of the refrigerator. By. The system was purchased from two cycles, one of which was a water distillation cycle and the other was a refrigeration cycle. The water distillation cycle has been described in the eighth figure above. The refrigeration cycle is controlled by three three-way valve bodies i 2, 54 and 56. Therefore, leave the compressor 1 ◦ to 30 paper sizes applicable to Chinese National Standard (CNS) A4 specifications (210 X 297 mm) (Please read the precautions on the back before filling this page>
裝-----I 訂---------線 經濟部智慧財產局貝工消費合作社印製 經濟部中失標準扃貝工消費合作社印装 ，Ή β > .-^ Λ 7 Η 7 五、發明说明卜Ρ) 冷卻器2 Ο並經由冷凍劑壓力降低裝置5 8之冷凍劑’其 係進入了冰箱蒸發器6 0以完成冷凍循環。 不县有其內部洽凍劑蒸發器之水蒸齬奘置 第十二圖爲以上第十一圖中所敘述之蒸餾單元的部分 截面圖，除了不具有一內部冷凍劑蒸發器2 4 *冷凍劑壓 力降低裝置2 2、兩個三向閥體5 6與6 2、或是一熱交 換器2 8。冷凍劑現在進入該冰箱蒸發器6 0，而蒸餾器 容器4 2之頂部當其藉由來自冰箱蒸發器所供應之冷空氣 而在外表面所冷卻時，其係如同一蒸氣冷凝器般作用β此 蒸鱭單元亦被整合至一標準家用冰箱中，相同於以上第十 —圖中所示者。 在第二圖至第十五圖中所詳細敘述之緊密真空蒸餾系 統具有以下優點： 其容許能量消耗之減少低於（2 5 — 5 0 %) —標準 大氣蒸餾器。 1由於將通連之蒸發器部分與聚積部分合倂爲一容室， 並且藉由在水蒸發器中覆蓋物的使用所產生之增強對流， 真空蒸餾系統之尺寸降低了。 其使用一用以產生真空之裝置，但並未使用一真空泵 或產生裝置，因此允許了使用冷凍循環作爲一產生蒸氣之 加熱源。 當與簡單蒸餾系統相較時，其製造蒸餾水之能量消耗 降低了相當多。 加熱器真空產生裝置之使用降低了單元之整體尺寸。 31 本紙張尺度適用中國國家標準（CNS ) Λ4规格UIOX297公兑） [ 1 0. 1 I ί! (請先間讀背面之注意事項再填寫本頁) Α22Ί\^Packing ----- I Order --------- Printed by the Shell Property Consumer Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs, the standard of the Ministry of Economy 扃 Shellfish Consumer Cooperative, Ή β > .- ^ Λ 7 Η 7 V. Description of the invention (P) The cooler 2 0 and the refrigerant '5 through the refrigerant pressure reducing device 5 8 enters the refrigerator evaporator 60 to complete the refrigeration cycle. The county has its own internal refrigerant refrigerant evaporator. The twelfth figure is a partial cross-sectional view of the distillation unit described in the eleventh figure above, except that it does not have an internal refrigerant evaporator 2 4 * freezing Agent pressure reducing device 2 2, two three-way valve bodies 5 6 and 6 2, or a heat exchanger 28. The refrigerant now enters the refrigerator evaporator 60, and the top of the still vessel 4 2 acts as the same vapor condenser when it is cooled on the outer surface by cold air supplied from the refrigerator evaporator. Β This The steamed ravioli unit is also integrated into a standard domestic refrigerator, which is the same as the one shown in the tenth-picture above. The compact vacuum distillation system detailed in Figures 2 to 15 has the following advantages: It allows a reduction in energy consumption less than (25-50%)-a standard atmospheric still. 1 The size of the vacuum distillation system is reduced due to the combination of the connected evaporator section and the accumulating section into a single container and the enhanced convection generated by the use of the cover in the water evaporator. It uses a device for generating a vacuum, but does not use a vacuum pump or generating device, thus allowing the use of a refrigeration cycle as a heating source for generating steam. When compared to a simple distillation system, its energy consumption for producing distilled water is considerably reduced. The use of a heater vacuum generating device reduces the overall size of the unit. 31 This paper size applies to Chinese National Standard (CNS) Λ4 specification UIOX297. [1 0. 1 I ί! (Please read the precautions on the back before filling this page) Α22Ί \ ^
五、發明説明（) 由於較低之沸點，積垢的形戚降低了，従而消除了除 聒或是使用除垢化學藥品的必要。 該設計可以輕易地整合於傳統冰箱中，其中冰箱之冷 凝以及蒸發元件可以被整合爲在裝置中一相同之元件。 由於所使用之較低操作溫度，而允許使用較低成本之 材料。 由於真空所創造之較低沸點，而使得裝置可以較安全 地控制與操作。 自動控制機構之敘沭 吾人將了解的是此裝置之一較佳實施例係包含自動控制機 構。在此形式中，該裝置之操作是在將於以下所述之電子 控制機構的控制之下。至少具有閥體之進口埠3 6、具有 閥體之通氣孔4 4、加熱器3 2與1 4、風扇2 1、以及 壓縮器10是藉由電子控制機構而在一定時的順序下自動 地操作的’以達成在次大氣壓力下分批蒸餾液體，而不需 要一創造或維持真空之真空泵或真空產生裝置的幫助。 電子自動真荜菡餾裴 經濟部中央標準局負工消费合作社印裝 (請先閱讀背面之注意事項再填寫本頁) 本發明（第二圖至第十五圖）之較佳實施例更包括一 以用於自動真空蒸餾裝置之邏輯電路所實行之自動控制機 構（電子控制機構）。 真宠蒸餾器邏艟逛雷孑雷袼 根據本發明用於分批蒸餾液體並具有一預煮沸器7 〇 之自動真空蒸餾裝置，其電子控制邏輯電路的典型實施例 顯示在第十三圖中，以一簡化之方塊圖來說明邏輯電路的 _ 32 本紙乐尺度通用肀國囤尽樣準（CNS } M规格（21〇χ297公楚 6 A7 H7 五、發明説明（七。） 主要部件。一預煮沸器高水位感測器1 0 0檢査在預煮沸 器（預蒸發部分）中水之高水位，並且確定預煮沸器並未 滿溢。如果是這樣，該感測器關閉，並且一步進馬達1 2 8被定位以打開一閥體，用以避免水從裝置42(並未顯 示）之聚積部分4 0流入預煮沸器中。步進馬達亦爲微處 理器1 1 8所控制，其並且被只是以旋轉至四個預設的位 置，其中第一位置允許裝置中第三大氣狀況（真空狀況） 之破壞；第二位置關閉具有閥體之通氣孔，用以封閉裝置 以與外界大氣隔離，以允許真空之產生：第三位置允許蒸 餾水從聚積部分開口（並未顯示）而流入貯水池部分；第 四位置允許水從聚積部分流入預煮沸器中。 步進馬達控制閥體之位置，並且在注水、真空產生、 蒸餾液製造、以及蒸餾液排出階段之不同控制點上打開及 關閉這些閥體。同樣地，一低液面高度感測器1 〇 2被用 來檢査在預煮沸器中之水位，並且確定水位不會太低。如 果在預煮辨器中水位之高度低於感測器之高度，加熱元件 C並未顯示）則將有過熱而導致損壞之危險 如果是這樣 ’感測器1 0 2打開，並且預煮沸器加熱元件（並未顯示 )將不運作。同樣地’高水位感測器1 〇 4以及低水位感 測器106檢査在主要煮沸器（蒸發部分）（並未顯示） ，並且確保該水位是在兩水位之間以避免任何問題發生。 一主要煮沸器連接感測器1 〇 8被用來確保主要煮沸 器是正確地連接（亦即以一可封閉連接3 7或是可封閉閥 體3 6 )至本發明之裝置。如果此感測器保持打開，連接 _ - 33 裝 _ 訂 線 (請先閱讀背而之注意事項再功寫本頁) 經濟部中央標準局負工消費合作社印繁 本紙張尺度適用Τ國困本榡準（CNS ) Λ4規格（210Χ 297公泣} 把ML6 Β； 五、發明說明（今I) 主要煮沸器與該裝置之封閉（並未顯示）並未銜接，並且 在裝置中將不可能產生一真空狀況。V. Description of the invention () Due to the lower boiling point, the form of scale is reduced, which eliminates the need to remove 聒 or use descaling chemicals. This design can be easily integrated into a conventional refrigerator, in which the condensation and evaporation elements of the refrigerator can be integrated into an identical element in the device. Due to the lower operating temperatures used, lower cost materials are allowed. The lower boiling point created by the vacuum allows the device to be controlled and operated more safely. Description of the automatic control mechanism I will understand that a preferred embodiment of this device includes an automatic control mechanism. In this form, the device is operated under the control of an electronic control mechanism which will be described below. At least the inlet port 3 of the valve body 6, the vent hole 4 of the valve body 4, the heaters 3 2 and 1 4, the fan 21, and the compressor 10 are automatically controlled by the electronic control mechanism in a certain sequence It's operated to achieve batch distillation of liquids at sub-atmospheric pressure without the help of a vacuum pump or vacuum generating device that creates or maintains a vacuum. Electronic Automatic Distillation Printing by the Central Standards Bureau of the Ministry of Economic Affairs of the Offshore Consumer Cooperative (Please read the precautions on the back before filling out this page) The preferred embodiments of the present invention (Figures 2 to 15) include An automatic control mechanism (electronic control mechanism) implemented by a logic circuit for an automatic vacuum distillation apparatus. A true petit distillation apparatus is an automatic vacuum distillation apparatus for batch-distilling liquids and having a preboiler 70 according to the present invention. A typical embodiment of an electronic control logic circuit is shown in the thirteenth figure. A simplified block diagram is used to illustrate the logic circuit. 32 The paper scale is as accurate as the standard (CNS) M specification (21〇297297 Chu 6 A7 H7 V. Description of the invention (VII.) The main components. Preboiler high water level sensor 1 0 0 Check the high water level of the water in the preboiler (pre-evaporation section) and make sure that the preboiler is not full. If so, the sensor is turned off and a step The motor 1 2 8 is positioned to open a valve body to prevent water from flowing into the pre-boiler from the accumulation part 40 of the device 42 (not shown). The stepper motor is also controlled by the microprocessor 1 1 8 And it is only rotated to four preset positions. The first position allows the destruction of the third atmospheric condition (vacuum condition) in the device; the second position closes the vent hole with the valve body to close the device to the outside atmosphere. Isolation to allow The generation of air: the third position allows distilled water to flow from the accumulation part (not shown) and flow into the reservoir; the fourth position allows water to flow from the accumulation part into the pre-boiler. The stepper motor controls the position of the valve body, These valves are opened and closed at different control points in the vacuum generation, distillate manufacturing, and distillate discharge stages. Similarly, a low-level sensor 120 is used to check the water level in the pre-boiler, And make sure the water level is not too low. If the height of the water level in the pre-boiler is lower than the height of the sensor, the heating element C is not shown), there will be a risk of damage due to overheating. If so, 'Sensor 1 0 2 is turned on, and the pre-boiler heating element (not shown) will not work. Similarly, the 'high water level sensor 104 and low water level sensor 106 are checked at the main boiler (evaporation section) (not shown) ), And make sure that the water level is between the two water levels to avoid any problems. A main boiler connection sensor 10 is used to ensure that the main boiler is properly connected ( That is, a closable connection 3 7 or a closable valve body 3 6) to the device of the present invention. If the sensor remains open, connect the _-33 installation_ ordering line (please read the precautions on the back first and then work (Write this page) Printed by the Central Standards Bureau of the Ministry of Economic Affairs, Consumer Cooperatives, and printed on paper. The paper size is applicable to the National Standards (CNS) Λ4 specification (210 × 297). ML6 Β; 5. Description of the invention (now I) Mainly boiling The device is not connected to the enclosure (not shown) of the device and it will not be possible to create a vacuum condition in the device.
低通濾波器110、112、114、116被連接 至高與监水位控制感測器100、102、104、10 6 ' 1 0 8，其並且確保水位之攪動並不會使感測器弄錯 在錯誤之水位β反之，低通濾波器濾除水位感測信號之擾 動，並且感測器僅回應欲感測水位之主要數値》 I —微處理器丄丄_S_以電子方式處理來自該感測器1 0 0、102、104、106、10 8經由該濾波器1 1 〇、112、11 4、11 6之輸入信號，並且經由容置 在微處理器中唯讀記憶體丄_2JL之控制邏輯而理解該信號 之資訊β根據信號處理結果，一來自微處理器之輸出傳送 至一能發出聽得件之聲音的揚聲器1 2 2，警告使用者在 主要煮沸器注水之故障或錯誤（太滿或太空），或是在預 煮沸器中相似的狀況。另一信號被傳送至指示中繼以關閉 之預煮沸器加熱器繼電器1 2 4，並從而將電力供應予預 煮沸器加熱器3 2。來自微處理器一相似信號被傳送至主 要煮沸器加熱器1 4。同樣以一相似之方法，一信號被傳 送至電風扇1 3，導致該風扇在蒸餾循環中正確的時機打 開並且將空氣吹過冷凝器》 用於自動真空蒸餾器之雷子捽制器的流程圖 第十四圖顯示了用於本發明之典型電子控制器的流程 圖。由於絕緣並且在裝置中產生真空的需要，蒸餾過程基 本上爲一分批過程。此分批過程之控制順序如下所述：隨 34 本紙張尺度適用中國國家標準（CNS)A4規格（210 X 297公釐） (請先閱讀背面之注意事項再填窝本頁) • Λ^ϋιιιι^ί--I--— t^·· f 經濟部智慧財產局員工消費合作社印製 你·"·，‘__b7__ 五、發明說明 著蒸餾器之電源感測器之打開而開始了控制順序。接著， 控制器（並未顯示）檢查主要煮沸器連接感測器以及低/ 高液面高度感應器是否打開，如果沒有打開，即發出—警 告聲音1 3 5。如果所有的感測器104、106、10 8都打開了1 3 4，則控制器檢查預煮沸器高水位感測器 是否打開1 3 6。如果沒有，則步進馬達被定位至位置4 (1 3 8)’以允許水從聚積部分（並未顯示）流至預煮 沸器中》 如果超出特定之一段時間1 4 0，並且預煮沸器之水 位並未達到一高水位感測器，則發出一警告燈光或聲音丄 Α_2_以指示使用者檢查故障。 如果水位感測器1 0 0、1 0 2兩者皆打開，指示在 預煮沸器（並未顯示）中的水位處於正確範圍內，則步進 馬達（並未顯示）轉至位置3 ( 1 4 4)。爲了確定聚積 部份中的水藉由重力而流入貯水池（並未顯示），控制器 (並未顯示）檢查從電源感應器打開1 3 2之累積時間。 如果累積時間例如是超過兩分鐘，該預煮沸器加熱器 被打開1 4 6。接著，控制器連續第檢查預煮沸器低水位 感測器1 4 8，如果其仍然是打開的，則預煮沸器加熱器 繼續打開著。一旦預煮沸器低水位感測器1 0 2關閉，則 步進馬達轉至位置2 ( 1 5 0 )。在時間延遲之後1 5 2 ，預煮沸器加熱器被關閉1 5 4，風扇2 1被打開1 5 6 ，其係冷卻與冷凝器2 4相接觸之第一蒸氣，將水蒸氣轉 變成水2 1，並且開始在裝置中創造真空（第三大氣狀況 35 C請先間讀背面之注意事項再填寫本頁) •.裝--------訂---------線 ! 經濟部智慧財產局貝工消費合作社印製 本紙張尺度適用中國國家標準（CNS)A4規格（210 X 297公釐） 經濟部智慧財產局員工消費合作社印製 A7 B7 五、發明說明（A) )，其是被封閉以與外界大氣隔離的。在時間延遲一段時 間後1 5 8，在真空被降至一所希望之程度期間，主要煮 沸器（蒸發器部分）加熱器被打開1 6 0。 接著控制器檢查主要煮沸器低水位感測器1 0 6，並 且如果其係位於“打開”位置，（也就是意指在蒸發器部 份或主要煮沸器中仍有足量之水），主要煮沸器加熱器持 續煮沸水以形成第二蒸氣。一但控制器檢查並發現低水位 感測器1 6 6是關閉的，主要煮沸器加熱器1 4與風扇2 1被關閉1 6 2，並且步進馬達被轉至第一位置（1 6 4 )，在一段時間延遲166後，而破壞裝置中的真空狀況 。接著步進馬達被轉至位置3 ( 1 6 8)。當步進馬達位 於第三位置（1 6 8)時，收集在聚積部分（並未顯示） 之蒸餾水藉由重力而流入連接在聚積部分以下之貯水池部 分。此完成了該批之過程1 7 0。 第十五圖爲一用以操作裝置之控制次序的圖表。可以 淸楚看出的是本發明並非受限於第十五圖中之控制順序。 如同將可以被看出的，本發明用以分批蒸餾液體之裝 置可以使用於水以外的液體，包括甘醇、海水'鹽水、以 及酒精，但並非受限於此等液體。 因此，本發明代表性的實施例已經述及，熟於此技者 所必須注意的是，在此所揭露的僅爲示例，而其他可選擇 之改變及修正都落於本發明之觀點之中。因此，本發明並 未受限於在此說明之特定實施例，然僅由以下申請專利範 圍所界定。 36 本紙張尺度適用中國國家標準（CNS)A4規格（210 X 297公釐） (請先閱讀背面之注意事項再填寫本頁) -I ———— — — I— ^ i I---—II . 經濟部智慧財產局貝工消費合作社印製 4227 16, 五、發明說明) 圖式牛要元件符號說明 4 外殼 6 支承底座 8 冰箱主體 10 冷凍壓縮器 11 電源線 12 冷凍管線 13 風扇 14 加熱器/加熱線圈 16 覆蓋物 17 蒸餾液 18 冷凍管線 19 小貯水池部分 2 0 冷卻器 2 1 熱交換器風扇 2 2 冷凍劑壓力降低裝置 2 3 冷凍管線 2 4 冷凝器/冷凝線圏 2 5 聚積器-貯水池容器 2 6 點 2 8 管件 2 9 閥體 3 0 管件 3 2 預煮沸器加熱器 37 <請先閱讀背面之注意事項再填寫本頁) 裝------II 訂.---- 線 ！ 本纸張尺度適用中國國家標準（CNS)A4規格（210 X 297公釐） 422716 五、發明說明（〇 Α7 Β7 經濟部智慧財產局員工消費合作杜印製 3 4 蒸氣分離器 3 6 具有閥體之進口璋 3 7 可封閉連結 3 8 閥體 4 0 聚積部分/第二容器 4 1 第一管件/導管 4 2 裝置 4 3 絕緣襯裡 4 4 具有閥體之通氣孔 4 6 第二連接管件 4 7 出口 4 8 通氣孔 5 0 貯水池部分 5 2 閥體 5 4 三向閥體 5 6 三向閥體 5 8 冷凍劑壓力降低裝置 6 0 冰箱蒸發器 6 2 三向閥體 6 4 液體 6 6 蒸發器部分/第一容室 6 8 空間 6 9 第一容室 7 0 預蒸發器部分/預煮沸器部分 38 I ------訂·--------I <請先閱讀背面之注意事項再填寫本頁) 本紙張尺度適用中國國家標準（CNS)A4規格（210 X 297公釐） 4227fff 五、發明說明（W) 經濟部智慧財產局員工消費合作社印製 7 1 隔板 7 2 液態水 7 4 具有閥體之出口管件 7 6 閥體 7 8 閥體 8 0 供應管件 8 2 具有閥體之管件 8 4 供應管件 10 0 預煮沸器高水位感測器 10 2 低液面高度感測器 10 4 高水位感測器 10 6 低水位感測器 10 8 主要煮沸器連接感測器 110 低通濾波器 112 低通濾波器 114 低通濾波器 116 低通濾波器 118 微處理器 12 0 唯讀記憶體 12 2 揚聲器 12 4 預煮沸器加熱器繼電器 1 2 8 步進馬達 1 3 2 電源感應器 13 4 打開 39 裝-------—訂---------線 C請先閱讀背面之注意事項再填寫本頁) 本紙張尺度適用令國國家標準（CNS)A4規格（210 X 297公釐） 五、發明說明〉 13 5 13 6 13 8 14 0 14 2 14 4 14 6 14 8 15 0 15 2 1 5 4 15 6 15 8 16 0 16 2 16 6 16 8 1 7 0 422716 A7 執〆B7 警告聲音 打開 步進馬達之位置4 特定之一段時間 警告燈光或聲音 步進馬達之位置3 打開 預煮沸器低水位感測器 步進馬達之位置2 時間延遲 預煮沸器加熱器關閉 風扇打開 時間延遲一段時間 主要煮沸器打開 關閉 低水位感測器關閉 步進馬達之位置3 完成了該批之過程 *-------訂---------' (請先閱讀背面之注意事項再填寫本頁) 經濟部智慧財產局員工消費合作社印製 本紙張尺度適用中國國家標準（CNS)A4規格（210 X 297公釐）The low-pass filters 110, 112, 114, and 116 are connected to the high and supervised water level control sensors 100, 102, 104, and 10 6 '1 0 8 and ensure that the agitation of the water level does not cause the sensor to be mistaken. Wrong water level β Conversely, the low-pass filter removes the disturbance of the water level sensing signal, and the sensor only responds to the main number of the water level to be sensed. "I-Microprocessor 丄 丄 _S_ The sensors 1 0 0, 102, 104, 106, 10 8 pass through the input signals of the filters 1 1 0, 112, 11 4 and 116, and are stored in the microprocessor's read-only memory 丄 _2JL The control logic understands the information of the signal β. According to the signal processing result, an output from the microprocessor is transmitted to a speaker 1 2 2 that can hear the sound of the audible piece, alerting the user to the failure or error of water injection in the main boiler. (Too full or space), or similar conditions in a preboiler. Another signal is transmitted to the pre-boiler heater relay 1 2 4 which instructs the relay to be turned off, and thereby supplies power to the pre-boiler heater 32. A similar signal from the microprocessor is transmitted to the main boiler heater 14. Also in a similar way, a signal is transmitted to the electric fan 1 3, which causes the fan to turn on at the right time in the distillation cycle and blows air through the condenser. The process of a lightning trap for an automatic vacuum still Figure 14 shows a flowchart of a typical electronic controller used in the present invention. Due to the need for insulation and the creation of a vacuum in the unit, the distillation process is basically a batch process. The control sequence of this batch process is as follows: With 34 paper sizes, the Chinese National Standard (CNS) A4 specification (210 X 297 mm) applies (please read the precautions on the back before filling this page) • Λ ^ ϋιιιι ^ ί--I ---- t ^ ·· f Printed by the Consumer Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs " ·, '__b7__ 5. The invention explains that the power sensor of the still is turned on and the control sequence is started . Then, the controller (not shown) checks whether the main boiler connection sensor and the low / high liquid level sensor are turned on. If it is not turned on, a warning sound is issued 1 3 5. If all the sensors 104, 106, 108 are turned on 1 3 4, the controller checks whether the preboiler high water level sensor is turned on 1 3 6. If not, the stepper motor is positioned to position 4 (1 3 8) 'to allow water to flow from the accumulation section (not shown) to the pre-boiler.> If the specified time is exceeded 1 4 0 and the pre-boiler If the water level does not reach a high water level sensor, a warning light or sound 丄 Α_2_ is issued to instruct the user to check the fault. If both the water level sensors 1 0 0 and 1 0 2 are on, indicating that the water level in the pre-boiler (not shown) is in the correct range, the stepper motor (not shown) turns to position 3 (1 4 4). In order to determine that the water in the accumulation part flows into the reservoir by gravity (not shown), the controller (not shown) checks the accumulated time from when the power sensor is turned on 1 2 2. If the accumulated time is, for example, more than two minutes, the pre-boiler heater is turned on 1 4 6. Next, the controller continuously checks the pre-boiler low-water sensor 1 4 8 and if it is still on, the pre-boiler heater continues to be on. Once the pre-boiler low-water sensor 1 0 2 is turned off, the stepper motor is turned to position 2 (15 0). After a time delay of 15 2, the pre-boiler heater is turned off 1 5 4 and the fan 2 1 is turned on 1 5 6, which cools the first vapor in contact with the condenser 2 4 and converts the water vapor into water 2 1, and began to create a vacuum in the device (the third atmospheric condition 35 C, please read the precautions on the back before filling out this page) • .Install -------- Order --------- Online! Printed by Shelley Consumer Cooperative of Intellectual Property Bureau of the Ministry of Economics This paper is printed in accordance with Chinese National Standard (CNS) A4 (210 X 297 mm) Printed by the Consumer Cooperative of Intellectual Property Bureau of the Ministry of Economy A7 B7 )), Which is enclosed to be isolated from the outside atmosphere. After a time delay of 158, the main boiler (evaporator section) heater was turned on 160 while the vacuum was reduced to a desired level. The controller then checks the main boiler low water level sensor 106, and if it is in the "open" position (meaning that there is still sufficient water in the evaporator section or the main boiler), the main boiler The boiler heater continues to boil water to form a second vapor. Once the controller checks and finds that the low water level sensor 1 6 6 is turned off, the main boiler heater 1 4 and fan 2 1 are turned off 1 6 2 and the stepper motor is turned to the first position (1 6 4 ), After a delay of 166, the vacuum condition in the device is destroyed. The stepper motor is then turned to position 3 (1 6 8). When the stepping motor is in the third position (168), the distilled water collected in the accumulation portion (not shown) flows by gravity into the reservoir portion connected below the accumulation portion. This completes the batch process of 170. Figure 15 is a diagram of a control sequence for operating the device. It can be clearly seen that the present invention is not limited to the control sequence in the fifteenth figure. As will be seen, the apparatus for batch distillation of liquids of the present invention can be used with liquids other than water, including but not limited to glycols, seawater 'brines, and alcohols. Therefore, the representative embodiments of the present invention have been described. Those skilled in the art must pay attention to the fact that what is disclosed here is only an example, and other optional changes and modifications fall within the viewpoint of the present invention. . Therefore, the present invention is not limited to the specific embodiments described herein, but is only defined by the scope of the following patent applications. 36 This paper size applies to China National Standard (CNS) A4 (210 X 297 mm) (Please read the notes on the back before filling out this page) -I ———— — — I— ^ i I ---— II. Printed by Shelley Consumer Cooperative of Intellectual Property Bureau of the Ministry of Economic Affairs 4227 16, V. Description of the invention) Symbol description of the main components of the diagram 4 Housing 6 Support base 8 Refrigerator body 10 Freezer compressor 11 Power cord 12 Freezer line 13 Fan 14 Heating Cooler / heating coil 16 Cover 17 Distillate 18 Refrigeration line 19 Small reservoir section 2 0 Cooler 2 1 Heat exchanger fan 2 2 Refrigerant pressure reducing device 2 3 Refrigeration line 2 4 Condenser / condensation line 2 5 Accumulator -Reservoir container 2 6 points 2 8 Pipe fittings 2 9 Valve body 3 0 Pipe fittings 3 2 Pre-boiler heater 37 < Please read the precautions on the back before filling this page) Installation --- II order .-- -Line! This paper size is in accordance with China National Standard (CNS) A4 (210 X 297 mm) 422716 V. Description of the invention (〇Α7 Β7 DuPont printed by the staff of the Intellectual Property Bureau of the Ministry of Economy 3 4 Steam separator 3 6 Has a valve body Inlet 璋 3 7 Closeable connection 3 8 Valve body 4 0 Accumulation part / second container 4 1 First pipe fitting / conduit 4 2 Device 4 3 Insulating lining 4 4 Vent hole with valve body 4 6 Second connection pipe fitting 4 7 Outlet 4 8 Vent hole 5 0 Reservoir section 5 2 Valve body 5 4 Three-way valve body 5 6 Three-way valve body 5 8 Refrigerant pressure reducing device 6 0 Refrigerator evaporator 6 2 Three-way valve body 6 4 Liquid 6 6 Evaporator Part / First Container 6 8 Space 6 9 First Container 7 0 Pre-Evaporator / Pre-Boiler Section 38 I ------ Order · -------- I < Please read first Note on the back, please fill in this page again) This paper size is applicable to China National Standard (CNS) A4 (210 X 297 mm) 4227fff V. Description of the invention (W) Printed by the Intellectual Property Bureau of the Ministry of Economic Affairs and Consumer Cooperatives 7 1 Partition 7 2 Liquid water 7 4 Outlet fittings with valve body 7 6 Valve body 7 8 Valve 8 0 Supply fittings 8 2 Fittings with valve body 8 4 Supply fittings 10 0 Preboiler high water level sensor 10 2 Low liquid level sensor 10 4 High water level sensor 10 6 Low water level sensor 10 8 Main boiler connection sensor 110 Low-pass filter 112 Low-pass filter 114 Low-pass filter 116 Low-pass filter 118 Microprocessor 12 0 Read-only memory 12 2 Speaker 12 4 Pre-boiler heater relay 1 2 8 Stepper motor 1 3 2 Power sensor 13 4 Open 39 Install ------------ Order --------- Line C Please read the precautions on the back before filling in this page) Applicable national standard (CNS) A4 specification (210 X 297 mm) V. Description of invention> 13 5 13 6 13 8 14 0 14 2 14 4 14 6 14 8 15 0 15 2 1 5 4 15 6 15 8 16 0 16 2 16 6 16 8 1 7 0 422716 A7 execute B7 warning sound position of stepping motor 4 warning light or sound position of stepping motor for a certain period of time 3 open preboiler low water level sensor stepping motor Position 2 time delay preboiler heater off fan on time delay some time main Boiler is turned on and off. Low water level sensor is turned off. Stepping motor position is completed. 3 The batch process is completed. * ------- Order --------- '(Please read the precautions on the back first. (Fill in this page) Printed on the paper by the Consumers' Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs, the paper size applies to the Chinese National Standard (CNS) A4 (210 X 297 mm)