化工进展
化工進展
화공진전
CHEMICAL INDUSTRY AND ENGINEERING PROGRESS
2012年
10期
2335-2340
,共6页
王晓扬%陈绍云%张永春%陈恒
王曉颺%陳紹雲%張永春%陳恆
왕효양%진소운%장영춘%진항
保碳脱硫%乙酸钠%氧化%再生%吸收剂
保碳脫硫%乙痠鈉%氧化%再生%吸收劑
보탄탈류%을산납%양화%재생%흡수제
carbon-keeping desulphurization%sodium acetate%oxidation%regeneration%absorbent
考察了用乙酸钠溶液选择性吸收二氧化碳中的二氧化硫,用碳酸钙再生使乙酸钠循环使用,并得到副产物石膏。该方法与已有的柠檬酸钠法相比,成本低,再生副反应少。实验主要分为吸收、氧化、再生三个步骤,静态分别考察不同因素对吸收率,氧化率以及再生过程的影响。结果表明:吸收过程中乙酸钠溶液的浓度为0.08mol/L时,对SO2的吸收效果较好,且低温更有利于吸收。氧化过程最佳条件为:催化剂硫酸锰浓度为0.03 mol/L,温度90℃,转速400 r/min,空气流量150 mL/min,pH=4.0。再生时控制碳酸钙加入量在0.7 g左右,且反应在90℃进行,有利于生成硫酸钙;再生5次,再生液吸收的穿透时间基本不变,饱和吸收量略有减小。
攷察瞭用乙痠鈉溶液選擇性吸收二氧化碳中的二氧化硫,用碳痠鈣再生使乙痠鈉循環使用,併得到副產物石膏。該方法與已有的檸檬痠鈉法相比,成本低,再生副反應少。實驗主要分為吸收、氧化、再生三箇步驟,靜態分彆攷察不同因素對吸收率,氧化率以及再生過程的影響。結果錶明:吸收過程中乙痠鈉溶液的濃度為0.08mol/L時,對SO2的吸收效果較好,且低溫更有利于吸收。氧化過程最佳條件為:催化劑硫痠錳濃度為0.03 mol/L,溫度90℃,轉速400 r/min,空氣流量150 mL/min,pH=4.0。再生時控製碳痠鈣加入量在0.7 g左右,且反應在90℃進行,有利于生成硫痠鈣;再生5次,再生液吸收的穿透時間基本不變,飽和吸收量略有減小。
고찰료용을산납용액선택성흡수이양화탄중적이양화류,용탄산개재생사을산납순배사용,병득도부산물석고。해방법여이유적저몽산납법상비,성본저,재생부반응소。실험주요분위흡수、양화、재생삼개보취,정태분별고찰불동인소대흡수솔,양화솔이급재생과정적영향。결과표명:흡수과정중을산납용액적농도위0.08mol/L시,대SO2적흡수효과교호,차저온경유리우흡수。양화과정최가조건위:최화제류산맹농도위0.03 mol/L,온도90℃,전속400 r/min,공기류량150 mL/min,pH=4.0。재생시공제탄산개가입량재0.7 g좌우,차반응재90℃진행,유리우생성류산개;재생5차,재생액흡수적천투시간기본불변,포화흡수량략유감소。
Selective desulfurization from carbon dioxide was investigated by absorption method using sodium acetate solution as the sbsorbent.The absorbent was regenerated by calcium carbonate with gypsum as the by-product.Compared to sodium citrate,desulfurization by sodium acetate would significantly reduce the cost and side reactions.This study was divided into three steps:absorption,oxidation,and regeneration.Effects of different factors on desulfurization efficiency,oxidation rate,and regeneration were investigated under static condition.Results indicated that the absorption ability of the absorbent(0.08 mol/L) was inversely propotional to the temperature.The optimal conditions for oxidation are as follows:catalyst of manganese sulfate 0.03 mol/L,rotational speed 400 r/min,airflow rate 150 mL/min,pH=4.0 and temperature 90 ℃.For the regeneration process,around 0.7 g calcium carbonate should be added to the absorbent and reacted at 90 ℃.After 5 times’ regeneartion,the breakthrough time of the regenerated absorbent was almost the same as fresh one;but the saturated absorption capacity decreased.