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1)  regasification in steam
水蒸气再气化
2)  steam gasification
水蒸气气化
1.
A novel hydrogen production in which Ca(OH)_2 is adopted as a CO_2 sorbent to increase H_2 yield in the process of hydrogen production from woody biomass by steam gasification was proposed.
提出一种新型的生物质水蒸气气化制氢方法。
2.
The characteristics of biomass oxygen rich-steam gasification in a fluidized bed for hydrogen rich gas production were tested.
以一个鼓泡流化床为反应器,对生物质富氧—水蒸气气化制取富氢燃气的特性进行了一系列的实验研究。
3)  catalytic gasification with steam
水蒸气催化气化
4)  steam activation
水蒸气活化
1.
Preparation of biomass activated carbon by steam activation
水蒸气活化制备生物质活性炭的实验研究
2.
Activated carbon was prepared from tobacco stem by steam activation.
以烟秆为原料,经炭化后用水蒸气活化制备活性炭。
3.
The technology conditions for preparation of active carbon from rice hull by steam activation and the factors influencing the activation were investigated.
研究了水蒸气活化法制备稻壳活性炭的工艺条件,探讨了炭化温度、活化温度、活化时间和水蒸气用量对活化效果的影响。
5)  water vapor activation
水蒸气活化
1.
In order to increase the desulphurization efficiency of the flue gas during the pulsed corona discharge process, and improve the effects that water & ammonia (NHa) on the desulphurization, water vapor activation with a corona discharges was proposed.
为了提高脉冲放电等离子体烟气的脱硫率,更好发挥水和氨在该过程中的作用,我们提出了电晕放电水蒸气活化提高脱硫率的方法。
6)  water vapor oxidation
水蒸气氧化
1.
The results show that the combined treatments can decrease the parabolic rate constant,effectively improve the property of water vapor oxidation resistance and be superior to deposited RE coating only.
在管式高温水蒸气氧化实验装置中 ,以 6 0 0℃脱氧水蒸气氧化 30 0h的试验条件评价其抗水蒸汽氧化性能 。
2.
The effects of grain size on water vapor oxidation resistance were discussed.
在自制的水蒸气氧化装置中,对两种具有不同金相组织的P91钢进行了水蒸气等温氧化试验,结果表明,氧化动力学曲线具有抛物线特征。
补充资料:水煤浆加压气化炉
分子式:
CAS号:

性质:又称德士古煤气化炉(Texaco type coal gasifier)。以水煤浆为原料进行气化的工业炉。气化炉为直立圆筒,内衬耐火砖。原料煤破碎至粒度小于l0mm后送人球磨机。煤粉与水、添加剂、助熔剂(视煤的灰熔点高低决定是否加助熔剂)在球磨机中磨制成含固量60%~70%的水煤浆,用泵送人气化炉烧嘴,与送人的氧气在烧嘴出口混合雾化进入温度为1500℃左右、压力为2~6MPa的气化炉进行气化反应。产生的煤气经下降管进入激冷室,被水激冷后,经文丘里洗涤管及煤气洗涤塔除尘,并被水蒸气饱和。该煤气经CO变换工序。出气化炉的高温煤气可以不用水激冷,改用废热锅炉回收热量(废锅流程),产生高压蒸汽。该法制得的煤气大致组成:CO45.2%,CO218.5%,H235.1%,CH40.1%。

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