大氮肥
大氮肥
대담비
LARGE SCALE NITROGENOUS FERTILIZER INDUSTRY
2012年
4期
217-221,239
,共6页
剩余污泥%气化%制氢%经济性
剩餘汙泥%氣化%製氫%經濟性
잉여오니%기화%제경%경제성
excess activated sludge%gasification%hydrogen production%economy
介绍污水处理厂剩余污泥与煤制成污泥煤浆进行气化制氢的方法和流程,分析其经济性和可靠性。研究发现,污泥煤浆气化出口合成气有效气约为80%,冷煤气效率约为72%,合成气产出率约为86%。污泥煤浆制氢能耗约为20.5GJ/1000m3H2,污泥添加量每增加5%,单位制氢能耗增加1.5%。采用污泥煤浆制氢,主要原料成本约920元/1000m3H2,且随着污泥添加量的增加,制氢成本下降。采用污泥制氢能处理到非常难于处理的废弃物,具有很好的经济效益和环境效益。
介紹汙水處理廠剩餘汙泥與煤製成汙泥煤漿進行氣化製氫的方法和流程,分析其經濟性和可靠性。研究髮現,汙泥煤漿氣化齣口閤成氣有效氣約為80%,冷煤氣效率約為72%,閤成氣產齣率約為86%。汙泥煤漿製氫能耗約為20.5GJ/1000m3H2,汙泥添加量每增加5%,單位製氫能耗增加1.5%。採用汙泥煤漿製氫,主要原料成本約920元/1000m3H2,且隨著汙泥添加量的增加,製氫成本下降。採用汙泥製氫能處理到非常難于處理的廢棄物,具有很好的經濟效益和環境效益。
개소오수처리엄잉여오니여매제성오니매장진행기화제경적방법화류정,분석기경제성화가고성。연구발현,오니매장기화출구합성기유효기약위80%,랭매기효솔약위72%,합성기산출솔약위86%。오니매장제경능모약위20.5GJ/1000m3H2,오니첨가량매증가5%,단위제경능모증가1.5%。채용오니매장제경,주요원료성본약920원/1000m3H2,차수착오니첨가량적증가,제경성본하강。채용오니제경능처리도비상난우처리적폐기물,구유흔호적경제효익화배경효익。
Both the method and the process flows for producing hydrogen through the gasification of sludge coal slurry made of excess activated sludge from sewage treatment plant and coal are introduced and the economy and reliability thereof analyzed. It has been found from the study that the effective gas at the outlet of sludge coal slurry gasifier amounts to approximately up to 80% ,the cold gas eiticiency is 12% and me syngas yield is 86%.The energy consumption in hydrogen production by sludge coal slurry gasification is 20.5 GJ/1 000 m3 H2.With each 5% increase of sludge addition, the energy consumption per unit hydrogen-making increases about 1.5%.For the hydrogen production by sludge coal slurry gasification,the cost of main raw materials is about RMB¥920.00/1 000 m3 H2 and with the increase of sludge addition, the cost decreases.Hydrogen-making by taking sludge may treat the wastes difficult to deal with in some other process and thus have good economic and environmental benefits.