200841358 九、發明說明： 【發明所屬之技術領域】 本發明為_種可_連加鮮取、H餾时、加熱濃縮及熱風 乾燥等程序，在封閉系統内將揮發之溶劑全部回收的自動切換溶 劑萃取光纜與電纜除膠設備及方法。 【先前技術】 • 習用溶劑清洗廢電線、電纜之回收方法，請參考中華民國專 鲁利公告號41備「含油脂廢電線、電纜之回收方法」（下稱習知 案1)，及專利公告號574〇79「溶劑更新方式連續萃取電境除膠的 方法」（下稱習知案2)。本發明與習知案比較，更具有下列之優 越性：200841358 IX. Description of the invention: [Technical field to which the invention pertains] The present invention is an automatic switching method for recovering all volatile solvents in a closed system, such as fresh extraction, fresh distillation, heating and concentration, and hot air drying. Solvent extraction cable and cable degreasing equipment and methods. [Prior Art] • For the method of recycling solvent-cleaning waste wires and cables, please refer to the Republic of China Lulu Bulletin No. 41 for “Recycling Methods for Waste Wires and Cables Containing Grease” (hereinafter referred to as Xizhi Case 1), and Patent Announcement No. 574〇79 “Method for continuous extraction of electroless gel removal by solvent renewal method” (hereinafter referred to as the conventional case 2). Compared with the conventional case, the present invention has the following advantages:
習知案1 重力分離 需另外設備， 轉移過程無法 避免溶劑揮發Convention 1 Gravity separation requires additional equipment, the transfer process cannot avoid solvent evaporation
污染控制 開放系統，無法 避免溶劑揮發 及制 量控 齊間 溶時 洗洗 清清 使後液動 複發溶自 洗β法度制 清用無濃控 Μ, 0 風設令 熱外由 另發C i無f細 _，容Μ 取燥、Γ系-皇萃乾備凝 風 熱 + 力 f在完鰣統 |程内嗜系一 ^過槽轉凝| 作取移冷 操萃需由 燥一無亦片 乾同 及 回 獨器時積緩溶量制 t儀排{4為量劑控 設m 1大作|^成間 1|^|以^啉制 潔貯制及槽槽τ清受 清立控間貯衝劑及不~ 重力分離 需另外設備，轉 移過程無法避免 溶劑揮發 除膠及乾燥操作 過程分開，需另 5免乾燥程序，轉 移過程無法避免 揮發 由冷凝效率控制 清潔溶劑迴流 量，不易直接控 制 5 200841358 是故，經由上述比較後，可知各該習知細缺點是溶劑清洗 及乾燥製料產生之射_，由於除觀麵财分開，在祥 移過程無法縣频概，尤其樹域加溫縣時往姆 成嚴重之二次污染，對操作人員及環境造成損害。 由此可見，上述習用物品仍有諸多缺失，實非良善之設計者， 而亟待加以改良。 • 本明人鑑於上述制溶鮮取或清洗製_衍生的各項 鬌缺點，乃亟思加以改良創新，經多年苦心孤言旨潛心研究，並設立 先導性實驗設備逐纽良，終於成功研發完縣件自動切換溶劑 萃取光纜與電纜除膠設備及方法。 ^ 【發明目的】 -/本發明之主要目的係在於提供-種錄自動切換操作之溶劑 萃取光鐵、電規除膠設備，在各階絲作時，均能保持溶劑及蒸 A不外洩，不會產生溶劑揮發之二次污染，達成製程無污染、合 _ 乎環保要求之綠色製程。 本發明之次要目的係在於提供一種自動切換乾燥製程，將熱 風引進萃取槽，無需將清洗後含溶劑之紐、魏移出槽外另行 乾燥由於在卒取與乾燥製程轉換間槽蓋無需打開，槽體始終保 持岔閉，因此不會造成溶劑逸出之二次污染。因為萃取槽兼具乾 、朵力此各]^^又操作時，揮發溶劑均由冷凝系統回收，達成溶劑 π全回收再利用，且不會產生溶劑揮發散逸之二次污染。 本發明之又一目的係在於提供一種獨立操作之清潔溶劑貯 6 200841358 槽，，收納識概清_，峨萃顿之兩倍2 以儀器控制溶劑進、排時間及 可 貯備多量溶劑，使加入溶劑量及1^#心作為緩衝槽， 制，亦可防止動態操作時多餘溶劑溢出。 數不又限 本發明之再-目的係在於提供 槽，承接含萃出賴之雜作之加熱遭縮蒸發 平扣驟之令液’經加熱及攪拌將溶劑 八 卒出璆體之溶液則留在槽内3 个^ , 夕-人/辰鈿後成為高濃度之膠髀冰 液’再由槽體底部閥門排出，另藉㈣膜芨淘^ % >體岭 出，產出回收之膠體。$猎由賴療發槽將殘存之溶劑蒸 本㈣之另—目⑽在於提供—種將加鮮取、 加熱濃縮及熱風乾燥等程序，經儀 u口收、 '能將原本充膠之廢光《及電㉝八::一完成之設備， 雜，均可納爾署之回=；；=錢/㈣線成分及膠 ♦網完全回收、完全無污==放%’_成⑽用之溶 零 【發明内容】 . 丨I、W目的，本發明所提供之自動切換溶鮮取光甓盘 魏除膠設備及方法，主要是^ 與 〜 一：貧化播+、人、t ^ /辰細槽、一瘵餾塔、 機二~处、—溶麵槽、—溶繼槽次冷凝11、一送風 /一 ”，、風加細等機構喊，_加鮮取、$_收、加埶 濃縮及熱風龄摒癸扣——、 “、、細又加熱 均4、卞序’經儀器控制逐步完成操作，各操作單元 女木 在各操作階段所產生之揮發溶劑均導入冷凝器，所 有之揮發溶劍抬人、红 ^回收再利用’藉溶劑反覆加溫清洗，可將含 7 200841358 油脂及防水膠之廢_、f觀全萃取轉，驗吹送可將 殘留溶劑完全雖，可以產岭燥除膠之回收絲、魏產品， 另一方面將含有溶出物之溶液驗，溶鑛氣冷翻收可得純淨 溶劑反覆賴，含糾物之溶液將溶齡全蒸發後可以產出回收 之防水膠，不會產生溶劑揮發之二次污染。本發日神連加熱萃取、 蒸鶴回收、加熱濃縮及熱風乾_料為—體，過程完全封閉， 各原料成分及仙之賴均完全败、達絲較全無污染物排The pollution control open system can not avoid the solvent volatilization and the volume control, the rinsing and washing, the clearing, the re-liquidification, the re-dissolution, the self-washing, the β-law system, the clearing control, the non-concentration control, the 0 wind setting No f fine _, Rong Μ Take dry, Γ - - - - - - - - - - - - - - - - - - - - 在 在 | | | | | | | | | | | | | | | | | | | | | | | | | | | | | | | | Also, when the film is dry and returning to the single device, the amount of the solution is reduced. The meter is controlled by the meter to control the m 1 large work |^ into the room 1|^| Control room storage agent and no ~ gravity separation requires additional equipment, the transfer process can not avoid the solvent evaporation and the drying process is separated, need another 5 dry process, the transfer process can not avoid the evaporation of the cleaning solvent to control the flow back of the cleaning solvent, not easy Direct control 5 200841358 is the reason. After the above comparison, it can be seen that each of the conventional shortcomings is the solvent generated by the solvent cleaning and the dry preparation. Because of the separation of the face and the money, the county frequency cannot be met in the process of moving, especially the tree domain. When heating the county, it will become a serious secondary pollution, causing damage to operators and the environment. . It can be seen that there are still many missing items in the above-mentioned household items, which are not good designers, but need to be improved. • In view of the shortcomings of the above-mentioned methods of making fresh or cleaned, the people of Mingming have been improving and innovating, and after years of painstaking research, they have set up pilot experimental equipment and successfully developed. The county equipment automatically switches solvent extraction cable and cable de-gluing equipment and methods. ^ [Object of the Invention] - / The main purpose of the present invention is to provide a solvent extraction light iron and electric gauge degumming equipment for automatic switching operation, and to maintain the solvent and steam A without leaking in each step of the wire. It will not produce secondary pollution of solvent volatilization, and achieve a green process with no pollution and environmental protection requirements. The secondary object of the present invention is to provide an automatic switching drying process for introducing hot air into the extraction tank without separately removing the solvent-containing nucleus and Wei from the tank after drying, since the tank cover does not need to be opened during the transition between the stroke and the drying process. The tank body remains closed at all times, so there is no secondary pollution of solvent escape. Because the extraction tank has both dry and vigorous force, the volatile solvent is recovered by the condensing system, and the solvent π is completely recovered and reused, and the secondary pollution of the solvent volatilization is not generated. Another object of the present invention is to provide an independently operated cleaning solvent storage 6 200841358 trough, which can be used to control the solvent in and out, and can store a large amount of solvent, so as to add The amount of solvent and 1^# core are used as a buffer tank to prevent excess solvent from overflowing during dynamic operation. The re-restriction of the present invention is to provide a trough, and to receive a solution containing the extraction and heating of the miscellaneous heating and evaporation, and to remove the solvent from the carcass by heating and stirring. In the tank, 3 ^, 夕-人/辰钿 become a high-concentration gelatin ice liquid' and then discharged from the bottom valve of the tank body, and borrowed (4) membrane 芨 ^ ^ % > body ridge out, producing recycled colloid . $ 猎 由 赖 赖 赖 赖 赖 赖 赖 赖 赖 赖 赖 赖 赖 赖 赖 赖 赖 赖 赖 赖 赖 赖 赖 赖 赖 赖 赖 赖 赖 赖 赖 赖 赖 赖 赖 赖 赖 赖 赖 赖 赖 赖 赖 赖 赖 赖 赖 赖 赖 赖 赖 赖 赖 赖 赖Light "and electricity 33 eight:: a completed equipment, miscellaneous, can be returned to the Naer Department =;; = money / (four) line components and glue ♦ net completely recovered, completely non-soil == put %'_ into (10) Dissolved zero [invention content]. 丨I, W purpose, the invention provides the automatic switching of the fresh-storing light-removing sputum disc de-geling equipment and method, mainly ^ and ~ one: depleted broadcast +, human, t ^ / Chen fine tank, a retort, machine 2 ~, - dissolve surface tank, - dissolve the tank secondary condensation 11, a supply of air / one", wind and fine and other institutions shout, _ fresh take, $ _ close , adding enthalpy and hot air age —— buckle -, ",, fine and heating are 4, 卞 sequence' is gradually completed by instrument control, the volatile solvent generated by each operating unit female wood in each operation stage is introduced into the condenser , all the volatile solution of the sword to lift people, red ^ recycling and reuse 'by solvent to reheat and clean, can contain 7 200841358 grease and waterproof rubber waste _, f view Full extraction, test blowing can be used to completely remove the residual solvent, can produce ridge dry degumming recovery silk, Wei products, on the other hand will contain the dissolution of the solution test, dissolved gas cold retraction can be obtained by pure solvent The solution containing the rectifying agent can completely produce the water-repellent rubber after the evaporation of the solution, and does not cause secondary pollution of the solvent volatilization. The hair of the Japanese god even heating extraction, steaming crane recycling, heating and concentration and hot air drying _ material for the body, the process is completely closed, the ingredients of each raw material and the sacred Lai are completely defeated, the wire is more completely free of pollutants
放0 【實施方式】 請參閱圖-所示’本發明所提供之自動切換溶劑萃取光繞與 電驗膠f聽’其主要包括有—萃取槽卜—濃縮槽2、一蒸顧塔 3、一濃縮槽主冷凝器4、一溶劑儲槽5、一溶劑儲槽次冷凝器6、 一送風機7、一熱風加熱器8 ;而其操作步驟為： 步驟1、將廢充膠（光）電纜裝置於多孔之網籃内，再置入萃 取槽1中，封閉槽蓋； 步驟2、將溶劑加入萃取槽1，淹沒廢充膠（光）電纜，以蒸氣 夾套將溶劑加熱至沸騰，進行溶解膠體作業。 步驟3、設定之萃取時間到達後打開槽底閥門將含膠之溶液經 由液體輸送管線排入濃縮槽2 ; 步驟4、加熱及攪拌濃縮槽2，將溶劑蒸發，溶劑蒸氣經蒸顧 塔3分離純化後經冷凝塔4冷凝成為液體，流入溶劑 貯槽5，重複使用；含萃出膠體之溶液則留在濃縮槽2 内濃縮累積。 8 200841358 々驟5、重複步驟2〜步驟*，以達成溶劑再生、重複萃取、洗 平（光）電缦之操作，洗出之膠體則逐次濃縮累積。 / 在萃取槽1中之廢充膠（光）魏㈣次萃取完成膠 體凊除後打開槽底閥門排除溶劑，再打開氣體閥門， 弓1進由送風機7產生，通過熱風加熱器8加熱之空氣， 將已洗較觀材料吹乾，完成乾燥作業，且將揮發 =氣經由蒸氣管_人冷凝ϋ 4巾时再_，乾燥 4間到達销嶋顺7、熱風加齡8以及氣體閥 門，打開槽蓋，產出乾燥脫膠之回收規線成分。 步驟7、f ttt熱蒸發濃縮後，溶出之膠體或油脂在濃縮槽 + —積’設定之萃較朗達後 處曰 Ϊ二f膠之溶液經由液體輸送管線排入另。薄： ^德槽，將溶劑完全蒸發後產域顧膠之回收 膠設t方i發換溶劑萃取域與電纜除 嶋峨趣=====等 ί作階段所產生之揮發溶劑均導人冷難，所有，在各 滅回收再翻，不會產生溶_發之二次 w劑均冷 為合乎環保要求之綠㈣程。本發明^達越程無污染、 =纜分離綱卿之_分及膠體，膠之廢光親 ^利料、統，所採狀萃取溶麻藉_^^^保署之回 用，達成全部成分回收再利用及製 王π回收再利 實際操作結果請參閱圖二至圖四求。 口一係為可實施之操 200841358 作條件例；圖三為〇· 4醜6·對充膠電缆以溶劑萃取除膠後產出 之電親成分重量百分比；圖四為充膠單模光纜以溶劑萃取除膠後 產出之光纜成分重量百分比。 【特點及功效】 本發明所提供之自動切換溶劑萃取光纜與電纜除膠設備及方 法’與其他習用技術相互比較時，更具備下列優點： 1 '本發明提供一種自動切換操作之萃取除膠製程，整個生產Putting 0 [Embodiment] Please refer to the figure--the automatic switching solvent extraction light-wound and electro-spectrum glue provided by the present invention, which mainly includes - extraction tank - concentration tank 2, a steaming tower 3, a concentration tank main condenser 4, a solvent storage tank 5, a solvent storage tank sub-condenser 6, a blower 7, a hot air heater 8; and the operation steps are as follows: Step 1, the waste filling (optical) cable The device is placed in a porous basket and then placed in the extraction tank 1 to close the tank cover; Step 2. The solvent is added to the extraction tank 1, the waste rubber (light) cable is flooded, and the solvent is heated to boiling with a steam jacket. Dissolve colloidal work. Step 3: After the set extraction time arrives, the valve at the bottom of the tank is opened, and the solution containing the glue is discharged into the concentration tank 2 through the liquid transfer line; Step 4, heating and stirring the concentration tank 2, the solvent is evaporated, and the solvent vapor is separated by steaming tower 3 After purification, it is condensed into a liquid through the condensation tower 4, flows into the solvent storage tank 5, and is reused; the solution containing the extracted colloid is left in the concentration tank 2 to be concentrated and accumulated. 8 200841358 Step 5. Repeat steps 2 to 4 to achieve solvent regeneration, repeated extraction, and washing (light) electrolysis. The washed gel is concentrated and accumulated. / Waste in the extraction tank 1 (light) Wei (four) extraction After the colloid removal, open the bottom valve to remove the solvent, then open the gas valve, the bow 1 is generated by the blower 7, and the air is heated by the hot air heater 8. Dry the washed material, complete the drying operation, and volatilize = gas through the steam tube _ human condensation ϋ 4 towels _, dry 4 to reach pin 嶋 7, hot air age 8 and gas valve, open The trough cover produces the recovery rule component of the dry degumming. Step 7. After fttt is concentrated by thermal evaporation, the dissolved colloid or oil is discharged into the other solution through the liquid transfer line after the concentration tank is set to be the same as the Ronda. Thin: ^德槽, the solvent is completely evaporated, the recovery of the rubber in the production area, the t-side, the solvent extraction domain and the cable, except for the fungus ===== Cold difficulty, all, in each of the recovery and recycling, will not produce dissolved _ hair of the second w agent is cold to meet the environmental requirements of the green (four) process. The invention has the advantages of non-polluting, non-contamination of the cable separation, and the colloid of the colloid, the waste light of the glue, the material, the system, the extraction of the extract, and the recycling of the _^^^ Please refer to Figure 2 to Figure 4 for the recovery and reuse of the components and the actual operation results of the King π recycling. The mouth is a conditional example of the implementable operation 200841358; the third figure is the weight percentage of the electric component obtained by solvent extraction and degumming of the rubberized cable; Figure 4 is the filled single mode optical cable. The percentage by weight of the cable component produced by solvent extraction and degumming. [Features and Efficacy] The automatic switching solvent extraction optical cable and cable de-gluing equipment and method provided by the present invention have the following advantages when compared with other conventional technologies: 1 'The present invention provides an extraction and de-gluing process for automatic switching operation , the entire production
過程無需將光纜、電纜原料移出槽外，在製程轉換間系統 始終保持封閉，因此不會造成溶劑逸出之二次污染。 本發明提供一種將加熱萃取、蒸餾回收、加熱濃縮及熱風 乾燥等程序，經儀器控制自動逐步完成之設備，各階段操 作時，揮發溶劑均由冷凝系統回收，達成溶劑完全回收再 利用，且因系統封閉，避免操作人員與溶劑及溶劑蒸汽接 觸’是符合勞工作業安全及環保法令要求之綠色製程。 上列詳細說明乃針對本發明之一可行實施例進行具體說明， 惟该實施例並_以_本發明之專利範圍，凡未脫離本發明技 藝精神所為之等效實施或變更，均應包含於本案之專利範圍中。 綜上所述，本案不僅於技術思想上確屬創新，並具備習用之 傳統方法解及之上财項魏，已充分符合新酿錢步性之 ^定發明專利要件，爰依法提出申請，懇請貴局核准本件發明 專利申請案，_發明，至感德便。 【圖式簡單說明】 200841358 请參閱以下有關本發明一較佳實施例之詳細說明及其附圖， 將可進-步瞭解本發明之技術内容及其目的功效；有關該實施例 之附圖為： 圖一為本發明自動切換溶劑萃取光纜與電纜除膠設備及方法 之構造圖； 圖二為該自動切換溶劑萃取光纜與電纜除膠設備及方法之可 實施操作條件例圖； 圖三為該自動切換溶劑萃取光纜與電纜除膠設備及方法對充 膠電繞以溶劑萃取除膠後產出之電纜成分重量百分比圖；以及 圖四為該自動切換溶劑萃取光纜與電纜除膠設備及方法對充 膠單模光纜以溶劑萃取除膠後產出之光纜成分重量百分比圖。 【主要元件符號說明】 1萃取槽(EX-01) 2濃縮槽(R-01): 3蒸餾塔 4濃縮槽主冷凝器 5溶劑儲槽(V-01) 6溶劑儲槽次冷凝器 7送風機 8熱風加熱器The process does not need to remove the cable and cable material out of the slot, and the system remains closed during the process change, so there is no secondary pollution of solvent escape. The invention provides a device which is automatically and gradually completed by means of instrument control, such as heating extraction, distillation recovery, heating concentration and hot air drying, and the volatile solvent is recovered by the condensing system during the operation of each stage, and the solvent is completely recovered and reused, and The system is closed to prevent operators from coming into contact with solvents and solvent vapors. It is a green process that meets the requirements of the Labor Safety and Environmental Protection Act. The above detailed description is intended to be illustrative of the preferred embodiments of the present invention, which are intended to be included in the scope of the present invention. The patent scope of this case. To sum up, this case is not only innovative in terms of technical thinking, but also has the traditional methods of using it and the above-mentioned financial items. It has fully met the requirements of the new invention of the money, and applied for it according to law. You have approved this invention patent application, _ invention, to the sense of virtue. [Brief Description of the Drawings] 200841358 Please refer to the following detailed description of a preferred embodiment of the present invention and the accompanying drawings, and the technical contents of the present invention and its functions will be further understood; FIG. 1 is a structural diagram of an apparatus and method for automatically switching solvent extraction optical cable and cable de-gluing according to the present invention; FIG. 2 is a diagram showing an operation condition of the automatic switching solvent extraction optical cable and cable de-gluing apparatus and method; Automatically switch solvent extraction cable and cable de-gluing equipment and method for charging the electric coil by solvent extraction and degumming to produce the weight percentage of the cable component; and Figure 4 is the automatic switching solvent extraction optical cable and cable de-gluing equipment and method A graph of the weight percentage of cable components produced by solvent extraction and degumming after filling a single-mode cable. [Main component symbol description] 1 Extraction tank (EX-01) 2 Concentration tank (R-01): 3 Distillation tower 4 Concentration tank Main condenser 5 Solvent storage tank (V-01) 6 Solvent storage tank Secondary condenser 7 blower 8 hot air heater