1) luqi fluid-bed furnace
鲁奇式沸腾炉
2) disperse fluidization
(沸腾炉)散式流化
3) fluidized-bed furnace
沸腾炉
1.
Application of fluidized-bed furnace in 100 kt/a S-NPK fertilizer plant;
沸腾炉在100kt/a S-NPK复混肥生产中的应用
4) fluidized bed roaster
沸腾炉
1.
Process design of fluidized bed roaster in Jiangtong-Wengfu's 400 kt/a pyrite-based sulphuric acid plant;
江铜-瓮福400 kt/a硫铁矿制酸装置沸腾炉的工艺设计
2.
Revamping of slag tapping and transportation system for sulphuric acid fluidized bed roaster;
硫铁矿制酸沸腾炉排渣系统改造
3.
Design of fluidized bed roaster of a 100 kt/a sulphuric acid plant;
100kt/a硫酸装置沸腾炉的设计
5) fluidized bed furnace
沸腾炉
1.
Conceiving of Fluidized Bed Furnace Reformed from 35T Spreader-Stoker Boiler;
我公司35t抛煤机炉改造沸腾炉之设想
2.
The current drying modification is on coal instead of diesel oil for fluidized bed furnace with high efficiency and low dust (GXDF), which results in annual more than 20 million RMB Yuan from cost saving of drying DAP, as well as stable appearance, colour and high class DAP product.
采用低飞灰沸腾炉(GXDF),以烟煤为燃料进行技改,介绍其工艺流程、工艺参数及煤代油后所取得的效果:年节约烘干DAP燃料成本2000多万元,DAP外观颜色基本无变化,各项指标均达到优等品要求。
3.
It is the key of the automatic ore feed control system for fluidized bed furnace in ore based acid plant to maintain good control of the dynamic balance between the air (O 2) intake and ore (FeS 2) feed of the fluidized bed furnace, the air/ore ratio, and to maintain a weak oxidizing atmosphere in the furnace.
控制好沸腾炉进风量 (O2 )和进矿量 (FeS2 )之间的动态平衡关系———风矿比 ,维持沸腾炉内呈弱氧化气氛 ,是矿制酸装置的沸腾炉给矿自动控制系统的关键问题。
6) Fluid-bed furnace
沸腾炉
1.
In accordance with the problem of high sulfur content in dust produced by 30?m 2 fluid-bed furnace of 40 kt/a sulfuric acid system,suggustion of mixing high zinc slag into zinc concentrate was put forward to recovery high zinc slay,reduce impurity of roasted ore and improve benefit.
根据 40kt/a硫酸系列的 30m2 沸腾炉产出焙尘含硫高的问题 ,提出了在入炉锌精矿原料中配入高锌渣的生产方案 ,回收高锌渣和减少焙烧矿杂质含量创造的效
2.
Due to a few blast caps of 30m 2 fluid-bed furnace,resulting in low feed rate of concentrates and bad result of desulfur,after increasing numbers of bast caps,wind power was raised,output and quality of sinters were obviously improuved.
30m2 沸腾炉风帽数量少 ,致使精矿投料量低、脱硫效果差 ,增加风帽数量后 ,风量加大 ,焙烧矿产量及质量均有了明显的变
补充资料：鲁奇煤气化炉
分子式：
CAS号：
性质：又称固定床加压煤气化炉(干法排渣)。煤气化炉的一种型式。气化炉是一直立圆筒，炉顶有加煤装置，底部有炉箅，气化炉上部设有分布兼搅拌破碎装置。气化剂(水蒸气和氧气)由炉底部通过炉箅进入炉内，与炉内的块煤进行气化反应，主要反应：2C+O2=2CO(放热)；C+H2O=CO+H2(吸热)。气化炉自热连续运行，制得的煤气由气化炉上部排出，其组成大致为：CO2 26.3％，CO23％，CH47.7％，H240％，N2+Ar2％，煤由炉顶加入，灰渣经炉箅排出，气化压力3.0MPa左右。该法一般用褐煤或部分无烟煤为原料，气化温度900～1000℃，生成气中含有较多的杂质(焦油、轻油、酚、氨、硫化物等)，需要处理。由于煤气中CH4含量较高，用作合成氨原料气时，需要在后工序进行处理。该炉型为鲁奇公司开发。
CAS号：
性质：又称固定床加压煤气化炉(干法排渣)。煤气化炉的一种型式。气化炉是一直立圆筒，炉顶有加煤装置，底部有炉箅，气化炉上部设有分布兼搅拌破碎装置。气化剂(水蒸气和氧气)由炉底部通过炉箅进入炉内，与炉内的块煤进行气化反应，主要反应：2C+O2=2CO(放热)；C+H2O=CO+H2(吸热)。气化炉自热连续运行，制得的煤气由气化炉上部排出，其组成大致为：CO2 26.3％，CO23％，CH47.7％，H240％，N2+Ar2％，煤由炉顶加入，灰渣经炉箅排出，气化压力3.0MPa左右。该法一般用褐煤或部分无烟煤为原料，气化温度900～1000℃，生成气中含有较多的杂质(焦油、轻油、酚、氨、硫化物等)，需要处理。由于煤气中CH4含量较高，用作合成氨原料气时，需要在后工序进行处理。该炉型为鲁奇公司开发。
说明：补充资料仅用于学习参考，请勿用于其它任何用途。
参考词条