化工学报
化工學報
화공학보
JOURNAL OF CHEMICAL INDUSY AND ENGINEERING (CHINA)
2015年
3期
1080-1087
,共8页
毛燕东%金亚丹%李克忠%毕继诚%李金来%辛峰
毛燕東%金亞丹%李剋忠%畢繼誠%李金來%辛峰
모연동%금아단%리극충%필계성%리금래%신봉
煤%气化%催化剂%烧结温度%压差法测定技术%压力%反应气氛%蒸汽
煤%氣化%催化劑%燒結溫度%壓差法測定技術%壓力%反應氣氛%蒸汽
매%기화%최화제%소결온도%압차법측정기술%압력%반응기분%증기
coal%gasification%catalyst%sintering temperature%pressure-drop technique%pressure%reaction atmosphere%water vapor
煤催化气化工艺中碱金属催化剂的引入加剧了气化炉的结渣,直接影响了流化床气化炉结渣的正常操作。煤灰的烧结特性是流化床气化炉结渣的主要影响因素之一,通过摸索工艺条件使煤气化在烧结温度以下运行,可有效避免流化床气化炉内出现结渣问题。利用压差法测定烧结温度,结合灰渣的 XRD 分析结果系统研究了钾基碱金属催化剂的添加量、操作压力、反应气氛对王家塔烟煤低温灰化煤灰烧结温度的影响。结果表明,碳酸钾催化剂的添加明显降低了煤的灰熔点及烧结温度。0.1~3.5 MPa下,烧结温度随压力增大而降低,而且压力对烧结温度的影响在高压区更为明显,具体影响规律与煤种灰成分及钾基碱金属催化剂的添加有关。空气、CO2氧化性气氛下的烧结温度较高,N2惰性气氛下次之,还原性气氛下较低,而蒸汽的加入显著降低了烧结温度。烧结温度的变化与不同气氛下铁离子存在状态及钾的存在形态密切相关。蒸汽气氛下,钾更多以 KOH 等低熔点化合物形态存在,而且含钾物相在蒸汽气氛下更容易同煤灰中的硅铝、铁钙等矿物质反应,生成低共融点化合物,致使灰熔点及烧结温度大幅下降。
煤催化氣化工藝中堿金屬催化劑的引入加劇瞭氣化爐的結渣,直接影響瞭流化床氣化爐結渣的正常操作。煤灰的燒結特性是流化床氣化爐結渣的主要影響因素之一,通過摸索工藝條件使煤氣化在燒結溫度以下運行,可有效避免流化床氣化爐內齣現結渣問題。利用壓差法測定燒結溫度,結閤灰渣的 XRD 分析結果繫統研究瞭鉀基堿金屬催化劑的添加量、操作壓力、反應氣氛對王傢塔煙煤低溫灰化煤灰燒結溫度的影響。結果錶明,碳痠鉀催化劑的添加明顯降低瞭煤的灰鎔點及燒結溫度。0.1~3.5 MPa下,燒結溫度隨壓力增大而降低,而且壓力對燒結溫度的影響在高壓區更為明顯,具體影響規律與煤種灰成分及鉀基堿金屬催化劑的添加有關。空氣、CO2氧化性氣氛下的燒結溫度較高,N2惰性氣氛下次之,還原性氣氛下較低,而蒸汽的加入顯著降低瞭燒結溫度。燒結溫度的變化與不同氣氛下鐵離子存在狀態及鉀的存在形態密切相關。蒸汽氣氛下,鉀更多以 KOH 等低鎔點化閤物形態存在,而且含鉀物相在蒸汽氣氛下更容易同煤灰中的硅鋁、鐵鈣等礦物質反應,生成低共融點化閤物,緻使灰鎔點及燒結溫度大幅下降。
매최화기화공예중감금속최화제적인입가극료기화로적결사,직접영향료류화상기화로결사적정상조작。매회적소결특성시류화상기화로결사적주요영향인소지일,통과모색공예조건사매기화재소결온도이하운행,가유효피면류화상기화로내출현결사문제。이용압차법측정소결온도,결합회사적 XRD 분석결과계통연구료갑기감금속최화제적첨가량、조작압력、반응기분대왕가탑연매저온회화매회소결온도적영향。결과표명,탄산갑최화제적첨가명현강저료매적회용점급소결온도。0.1~3.5 MPa하,소결온도수압력증대이강저,이차압력대소결온도적영향재고압구경위명현,구체영향규률여매충회성분급갑기감금속최화제적첨가유관。공기、CO2양화성기분하적소결온도교고,N2타성기분하차지,환원성기분하교저,이증기적가입현저강저료소결온도。소결온도적변화여불동기분하철리자존재상태급갑적존재형태밀절상관。증기기분하,갑경다이 KOH 등저용점화합물형태존재,이차함갑물상재증기기분하경용역동매회중적규려、철개등광물질반응,생성저공융점화합물,치사회용점급소결온도대폭하강。
Agglomeration in fluidized bed gasification system is considered as a primary operational problem, especially for catalytic coal gasification process because alkali catalyst worsens sintering and slagging. The optimal condition from the experiments will ensure the operation of coal gasification below sintering temperature and make the fluidized bed gasifier operate normally. In this paper a self-made pressurized pressure-drop measuring device combining analysis of X-ray diffractometer (XRD) analyzer were used to study the effects of alkali catalyst addition, operation pressure and reaction atmosphere on sintering temperature of Wangjiata bituminous coal from Inner Mongolia, China. Sintering temperatures declined markedly after adding potassium carbonate catalyst. Sintering temperatures decreased with increasing pressure in the range of 0.1—3.5 MPa, and a more obvious decrease could be observed in the interval of higher pressure. This effect could be related to coal ash composition and addition of alkali catalyst. Operation pressure influenced sintering temperatures by affecting reaction rate and mineral transformation in coal ash, as observed from XRD patterns. Sintering temperatures measured in the reducing reaction atmosphere were lower than those in inert and oxidizing atmospheres, which could be related to different existence forms of Fe ions and K. The addition of water vapor lowered sintering temperature significantly. The presence of water vapor led to formation of low melting point materials, such as KOH, and K-bearing materials were easier to react with minerals of coal ash to produce low temperature eutectics in water vapor atmosphere, thus lowering sintering temperature.