化工进展
化工進展
화공진전
CHEMICAL INDUSTRY AND ENGINEERING PROGRESS
2015年
1期
178-182
,共5页
时婷%王新刚%巫建锋%杨秀山%杨林%王辛龙
時婷%王新剛%巫建鋒%楊秀山%楊林%王辛龍
시정%왕신강%무건봉%양수산%양림%왕신룡
脱硫钙渣%二氧化硅%浸取%碳酸钙%制备
脫硫鈣渣%二氧化硅%浸取%碳痠鈣%製備
탈류개사%이양화규%침취%탄산개%제비
calcium phosphorus gypsum desulfurization slag%silica%leaching%calcium carbonate%preparation
为了有效利用磷石膏脱硫钙渣资源,以磷石膏脱硫钙渣为原料合成了球形轻质碳酸钙。本文首先利用XRD 和 SEM 等测试手段分析了磷石膏脱硫钙渣的主要组成是氧化钙,主要杂质为二氧化硅以及少量铁铝镁。在此基础上首次提出了氯化铵浸取磷石膏脱硫钙渣,而后碳化合成轻质碳酸钙的新工艺。探讨了浸取过程中氯化铵的添加量,水与钙渣的液固比(质量比),温度工艺参数对钙浸取率和硅脱除率的影响,确定了较优工艺条件为:氯化铵添加量为总固体质量的50%,水与钙渣的液固比为9∶1,温度为40℃。在该工艺条件下,钙的浸取率可达67.98%,硅的脱除率可达97.80%。对上述浸取液经碳化制备出的轻质碳酸钙,其纯度为97.90%,白度为94.2度,沉降体积为3.5mL/g,均符合《普通工业沉淀碳酸钙》(HG/T 2226—2010)标准对一等品指标要求,且主晶型为球文石型,表明了该工艺效果良好。
為瞭有效利用燐石膏脫硫鈣渣資源,以燐石膏脫硫鈣渣為原料閤成瞭毬形輕質碳痠鈣。本文首先利用XRD 和 SEM 等測試手段分析瞭燐石膏脫硫鈣渣的主要組成是氧化鈣,主要雜質為二氧化硅以及少量鐵鋁鎂。在此基礎上首次提齣瞭氯化銨浸取燐石膏脫硫鈣渣,而後碳化閤成輕質碳痠鈣的新工藝。探討瞭浸取過程中氯化銨的添加量,水與鈣渣的液固比(質量比),溫度工藝參數對鈣浸取率和硅脫除率的影響,確定瞭較優工藝條件為:氯化銨添加量為總固體質量的50%,水與鈣渣的液固比為9∶1,溫度為40℃。在該工藝條件下,鈣的浸取率可達67.98%,硅的脫除率可達97.80%。對上述浸取液經碳化製備齣的輕質碳痠鈣,其純度為97.90%,白度為94.2度,沉降體積為3.5mL/g,均符閤《普通工業沉澱碳痠鈣》(HG/T 2226—2010)標準對一等品指標要求,且主晶型為毬文石型,錶明瞭該工藝效果良好。
위료유효이용린석고탈류개사자원,이린석고탈류개사위원료합성료구형경질탄산개。본문수선이용XRD 화 SEM 등측시수단분석료린석고탈류개사적주요조성시양화개,주요잡질위이양화규이급소량철려미。재차기출상수차제출료록화안침취린석고탈류개사,이후탄화합성경질탄산개적신공예。탐토료침취과정중록화안적첨가량,수여개사적액고비(질량비),온도공예삼수대개침취솔화규탈제솔적영향,학정료교우공예조건위:록화안첨가량위총고체질량적50%,수여개사적액고비위9∶1,온도위40℃。재해공예조건하,개적침취솔가체67.98%,규적탈제솔가체97.80%。대상술침취액경탄화제비출적경질탄산개,기순도위97.90%,백도위94.2도,침강체적위3.5mL/g,균부합《보통공업침정탄산개》(HG/T 2226—2010)표준대일등품지표요구,차주정형위구문석형,표명료해공예효과량호。
To recycle desulfurization slag from phosphorous gypsum,spherical calcium carbonate was prepared from calcium-containing phosphorus gypsum desulfurization slag. The composition of raw materials were analyzed by XRD and SEM. The main substance was calcium oxide and the main impurity was silica. It also contained a small amount of iron,aluminum and magnesium. A new process leaching desulfurization slag by ammonium chloride and subsequent carbonization was firstly proposed. The affecting factors , such as amount of ammonium chloride , ratio of water and desulfurization slag(mass ratio),and temperature on the performance of leaching were investigated. The optimal conditions were: Amount of ammonium chloride 50% of the total weight of the solid, ratio of water and desulfurization slag 9∶1,temperature 40℃. Conversion of calcium was about 67.98% and removal of silica was 97.80% under the optimal conditions. The purity of the obtained calcium carbonate was 97.90%,sedimentation volume was 3.5mL/g and whiteness was 94.2, meeting the norm of first grade product in<General Industrial Precipitated Calcium Carbonate>(HG/T 2226—2010). Main polymorph of calcium carbonate crystals was vaterite.