动力工程学报
動力工程學報
동력공정학보
JOURNAL OF POWER ENGINEERING
2012年
11期
885-890
,共6页
陈鸿伟%索新良%陈龙%于伟峰%黄雪丽
陳鴻偉%索新良%陳龍%于偉峰%黃雪麗
진홍위%색신량%진룡%우위봉%황설려
复合催化剂%气化%催化强度%气化温度%催化剂前驱物%活化能
複閤催化劑%氣化%催化彊度%氣化溫度%催化劑前驅物%活化能
복합최화제%기화%최화강도%기화온도%최화제전구물%활화능
compound catalyst%gasification%catalytic intensity%gasification temperature%catalyst precur-sor%activation energy
在搭建的固定床实验台上对CaO和Fe(NO3)3复合催化锦界煤焦-CO2常压等温气化的反应特性进行了研究.结果表明:复合催化剂最佳质量添加比例为1%Ca、29/6Fe,且在最佳添加量下气化时间比原煤焦和单组分催化剂下的气化时间分别缩短了103rain和18rain,催化强度系数分别是原煤焦、单组分催化剂CaO和Fe(N03)3的5.71倍、1.65倍和2.04倍,气化温度降低了100K,气化温度降低程度介于单组分催化剂CaO和Fe(NO3)3之间;复合催化过程生成的部分Ca(NO3)2与CaO的活性不同,即Ca的催化强度与其前驱物的形式有一定关系;添加单组分催化剂的煤焦活化能与原煤焦的活化能基本相同,不同添加比例的复合催化剂的煤焦活化能增加的程度不同,且在最佳添加比例下增加程度最小,其值为15.4%.
在搭建的固定床實驗檯上對CaO和Fe(NO3)3複閤催化錦界煤焦-CO2常壓等溫氣化的反應特性進行瞭研究.結果錶明:複閤催化劑最佳質量添加比例為1%Ca、29/6Fe,且在最佳添加量下氣化時間比原煤焦和單組分催化劑下的氣化時間分彆縮短瞭103rain和18rain,催化彊度繫數分彆是原煤焦、單組分催化劑CaO和Fe(N03)3的5.71倍、1.65倍和2.04倍,氣化溫度降低瞭100K,氣化溫度降低程度介于單組分催化劑CaO和Fe(NO3)3之間;複閤催化過程生成的部分Ca(NO3)2與CaO的活性不同,即Ca的催化彊度與其前驅物的形式有一定關繫;添加單組分催化劑的煤焦活化能與原煤焦的活化能基本相同,不同添加比例的複閤催化劑的煤焦活化能增加的程度不同,且在最佳添加比例下增加程度最小,其值為15.4%.
재탑건적고정상실험태상대CaO화Fe(NO3)3복합최화금계매초-CO2상압등온기화적반응특성진행료연구.결과표명:복합최화제최가질량첨가비례위1%Ca、29/6Fe,차재최가첨가량하기화시간비원매초화단조분최화제하적기화시간분별축단료103rain화18rain,최화강도계수분별시원매초、단조분최화제CaO화Fe(N03)3적5.71배、1.65배화2.04배,기화온도강저료100K,기화온도강저정도개우단조분최화제CaO화Fe(NO3)3지간;복합최화과정생성적부분Ca(NO3)2여CaO적활성불동,즉Ca적최화강도여기전구물적형식유일정관계;첨가단조분최화제적매초활화능여원매초적활화능기본상동,불동첨가비례적복합최화제적매초활화능증가적정도불동,차재최가첨가비례하증가정도최소,기치위15.4%.
The gasification characteristics of Jinjie coal char with CO2 under compound catalytic action of CaO and Fe(NO3)a were studied under isothermal and ordinary pressure conditions on a fixedbed experi mental system. Results show that the optimal mass addition of compound catalyst is 1% Ca+2% Fe, in which case, the gasification time can be reduced by 103 min and 18 min respectively as compared with that of raw coal char and singlecomponent catalyst, and the catalytic intensity coefficient will be 5.71, 1.65 and 2.04 times of raw coal char, singlecomponent catalyst CaO and singlecomponent catalyst Fe(NOa )3, with a reduction of gasification temperature by 100 K, and a reduction of gasification temperature lying be tween singlecomponent catalysts CaO and Fe(NOa )3 ; the activity of partial Ca(NO3)2 produced under the compound catalytic action is different from that of CaO, that is, the catalytic intensity of Ca has a certain relationship with the form of its precursor; the activation energy of coal char with addition of singlecom ponent catalyst is basically the same as that of raw coal char. Addition proportions of compound catalyst influence the increase degree of activation energy of coal char, and the minimum increase degree 15.4% is to be obtained at the optimal addition proportion.