化工进展
化工進展
화공진전
CHEMICAL INDUSTRY AND ENGINEERING PROGRESS
2012年
11期
2424-2428,2448
,共6页
张继军%栾金红%李霞%袁俊生
張繼軍%欒金紅%李霞%袁俊生
장계군%란금홍%리하%원준생
二氧化碳%脱钙率%脱镁率%海水温度%海水盐度
二氧化碳%脫鈣率%脫鎂率%海水溫度%海水鹽度
이양화탄%탈개솔%탈미솔%해수온도%해수염도
carbon dioxide%removal rate of calcium%removal rate of magnesium%temperature of seawater%salinity of seawater
对CO2法脱除海水中钙离子和镁离子进行研究,控制海水的pH值恒为8,考察温度、盐度对脱钙率和脱镁率的影响。结果表明,盐度35‰的海水,30~50℃时脱钙率由90%增长至95%,与此同时脱镁率由0增长至42%;脱钙率、脱镁率随温度升高而升高。在温度为30℃时,盐度35‰~105‰的海水脱钙率可由90%增长到97%,与此同时脱镁率由0增长到67%;脱钙率、脱镁率随盐度升高而升高。将得到的固体进行XRD检测可知,产物固相组成随温度、盐度的变化而变化。由此可知,海水盐度为35‰、pH值为8、温度为30℃是CO2法高效脱钙的最佳工艺条件。
對CO2法脫除海水中鈣離子和鎂離子進行研究,控製海水的pH值恆為8,攷察溫度、鹽度對脫鈣率和脫鎂率的影響。結果錶明,鹽度35‰的海水,30~50℃時脫鈣率由90%增長至95%,與此同時脫鎂率由0增長至42%;脫鈣率、脫鎂率隨溫度升高而升高。在溫度為30℃時,鹽度35‰~105‰的海水脫鈣率可由90%增長到97%,與此同時脫鎂率由0增長到67%;脫鈣率、脫鎂率隨鹽度升高而升高。將得到的固體進行XRD檢測可知,產物固相組成隨溫度、鹽度的變化而變化。由此可知,海水鹽度為35‰、pH值為8、溫度為30℃是CO2法高效脫鈣的最佳工藝條件。
대CO2법탈제해수중개리자화미리자진행연구,공제해수적pH치항위8,고찰온도、염도대탈개솔화탈미솔적영향。결과표명,염도35‰적해수,30~50℃시탈개솔유90%증장지95%,여차동시탈미솔유0증장지42%;탈개솔、탈미솔수온도승고이승고。재온도위30℃시,염도35‰~105‰적해수탈개솔가유90%증장도97%,여차동시탈미솔유0증장도67%;탈개솔、탈미솔수염도승고이승고。장득도적고체진행XRD검측가지,산물고상조성수온도、염도적변화이변화。유차가지,해수염도위35‰、pH치위8、온도위30℃시CO2법고효탈개적최가공예조건。
Precipitation of calcium and magnesium from seawater using CO2,the seawater of pH value in 8,the effects of the temperature and salinity were investigated in this research.When the salinity of seawater was 35‰,the removal rate of calcium increased from 90% to 95% when the temperature from 30 ℃ to 50 ℃.Meanwhile,the removal rate of magnesium was increased from 0 to 42%;the removal rate of calcium and magnesium also increased with the increasing temperature.When the temperature of seawater was 30 ℃,removal rate of calcium increased from 90% to 97% when salinity increased from 35‰ to 105‰.The removal rate of magnesium increased from 0 to 67%,the removal rate of calcium and magnesium increased with the increasing salinity as well.Solids precipitation was characterized using X-ray diffraction(XRD) analysis.The composition of precipitated solids varied with the changes in temperature and salinity.The optimum conditions of calcium removal from seawater under the experimental conditions in this paper were:temperature 30 ℃ and salinity 35‰.