環境資源報告成果查詢系統

化學迴圈程序處理廢塑膠之技術開發

中文摘要 本研究之主要目的在研發適用於處理廢塑膠之化學迴圈反應器,期能透過化學迴圈程序有效利用熱能、高轉化率等特性,研發低能耗、高效率的廢塑膠處理程序。化學迴圈程序技術主要有幾個關鍵技術,包括載氧體製備、載氧體輸送、反應器設計與參數最佳化等。而應用於固體燃料燃燒時,除了上述技術之外,亦需考慮固體燃料進料是否流暢。因此本研究將透過熱重分析系統、固定床反應器、機械強度測試來了解氧化鐵複合載氧體是否具有良好的特性可應用於化學迴圈程序。本團隊所開發之氧化鐵複合載氧體經過測試後發現具有良好的反應性及可迴圈性;除此之外,亦具有良好機械強度,可連續於化學迴圈反應系統中操作。本研究以聚氨酯(Polyurethane, PU)及聚丙烯(Polypropylene PP)塑膠顆粒作為處理對象,經由熱重分析、熱值分析後具有高熱焓值,可作為燃料使用。此外,PU及PP塑膠顆粒以固體燃料輸送系統在常溫下可穩定流暢地輸送PU及PP塑膠顆粒,並將測試後之參數用於設計處理廢塑膠之化學迴圈反應器。PU及PP塑膠顆粒在900°C下以CO2/O2作為氣化氣體進行空床氣化實驗,氣化後之組成主要為CO及H2,因此PU及PP塑膠顆粒在與載氧體進行燃燒前會先裂解、氣化為氣體燃料再與載氧體進燃燒反應。最後以本計劃所開發之移動床式化學迴圈反應器對PU及PP顆粒進行燃燒實驗,並找出最佳化的化學迴圈程序操作參數,以及透過長時間測試驗證反應器之可靠度。研究成果部分,本團隊開發之氧化鐵複合載氧體具有良好的反應性、可迴圈性及機械強度,並且以可以實際應用於塑膠顆粒燃燒實驗。在PU及PP塑膠顆粒之進料及裂解測試方面,藉由空床實驗及燃燒實驗找到適當操作條件,可完全燃燒進料之塑膠顆粒,並評估反應器處理之效能及經濟評估。在長時間連續燃燒實驗中,PU及PP塑膠顆粒可連續燃燒24小時,並且穩定維持100%的CO2產率。藉由連續操作實驗驗證本團隊開發的移動床反應系統對於塑膠顆粒燃燒的可靠度佳。
中文關鍵字 化學迴圈程序;廢塑膠;載氧體

基本資訊

專案計畫編號 EPA-101-U1U4-04-002 經費年度 101 計畫經費 1400 千元
專案開始日期 2012/02/29 專案結束日期 2012/11/30 專案主持人 顧洋
主辦單位 永續發展室(停用) 承辦人 林燕柔 執行單位 國立台灣科技大學育成中心

成果下載

類型 檔名 檔案大小 說明
期末報告 期末報告公開版.pdf 0MB

Development of Chemical Looping Process on Treatment of Waste Plastics

英文摘要 The chemical looping technology applying to waste plastics treatment was developed in this project. The advantages of high conversion of organic species and low energy consumption of chemical looping technology are benefit to treat waste plastics more efficiently. The key techniques including preparation of oxygen carrier, transportation of oxygen carriers between fuel and air reactors and optimal design for waste plastics treatment are essential for development of waste plastic combustion by chemical looping process. The Fe-based composite oxygen carrier was feasible for chemical looping process through preliminary tests by thermogravimetric analysis, fixed-bed reactor and mechanical strength prior to moving bed experiment. Polyurethane (PU) and polypropylene (PP) were used for solid fuels as well as treated plastics in this study. The enthalpies of PU and PP were quite high to employ as fuels for combustion. Besides, gasification of PU and PP particles with empty bed operation were conducted by using CO2/O2 as gasification reactants at 900°C. The components of gaseous fuels were mainly CO and H2. Therefore, PU and PP particles would be decomposed and gasified to be gaseous fuels prior to combustion with oxygen carriers. Finally, PU and PP particles were combusted by the moving bed reactor system developed in this project, and trying to find out the appropriate operation condition in terms of PU and PP combustion and long-term operation to verify the reliability of reactor system. The Fe-based composite oxygen carrier developed for moving bed reactor operation provided with well reactivity, recyclability and strong mechanical strength. The suitable gasification conditions of PU and PP particles were found by empty bed experiments, and applied to the combustion experiments in moving bed experiments. Complete combustion of PU and PP particles were achieved by combusted with Fe-based composite oxygen carrier in moving bed reactor. The combustion performance of moving bed reactor was evaluated for scaling up. Long-term operation for PU and PP particles combustion was last for 24 hours, and 100% of CO2 yield was stably reached.
英文關鍵字 chemical looping process;waste plastics;oxygen carrier