3000m~3/h排烟循环流化床脱硫工艺中试实验研究

介绍了采用真实烟气的 30 0 0m3 /h排烟循环流化床烟气脱硫工艺 (CFB FGD)及其中间试验装置 ,通过实验研究了钙硫摩尔比 (Ca/S)、近绝热饱和温度差 (ΔT)、烟气湿度、喷水量、入口SO2 浓度、浆液雾化质量、脱硫灰循环等对脱硫效果的影响。实验表明 ,CFB FGD工艺在停留时间小于 6s、烟气流速v =4— 6m/s、Ca/S =1.2、ΔT =10— 12℃时可实现高达 90 %的脱硫效率。     

蒸发二段真空度不稳定原因分析

对斯那姆尿素工艺二段蒸发真空度不稳定原因进行了较详细的分析，并提出相应的操作处理措施     

Breakthrough and Sulfate Conversion Analysis during Removal of Sulfur Dioxide by Calcium Oxide Sorbents

Sorption of sulfur dioxide (SO₂) was carried out on calcium‐based sorbents under dynamic conditions in a fixed bed. The experimental conditions were reaction temperature (700 to 1000°C), SO₂ concentration (1000‐10 000 ppm), sorbent particles size (1 to 2 mm) and the types of sorbents (hydroxide or carbonate). The sorption process was found to be effective at low concentration levels (less than 10 000 ppm) as the breakthrough time significantly decreased with increase in concentration. The maximum removal of SO₂ was observed at a reaction temperature of 950°C. The hydroxide‐based sorbents of relatively smaller particle size were found to exhibit superior sorption performance in terms of longer breakthrough time and higher sulfate conversion. A mathematical model developed, assuming a porous structure of the sorbent materials, attributed the low sulfation conversion during SO₂ sorption due to a pore diffusion mechanism.     

微波干法制备阳离子淀粉絮凝剂及其应用

以3—氯—2—羟丙基三甲基氯化铵为阳离子醚化剂，天然物质淀粉为原料，微波干法制得季铵型阳离子淀粉絮凝剂。通过正交试验，研究了各种因素对合成的影响，确定了最佳反应条件。结果表明：阳离子醚化剂与淀粉摩尔比0．35、NaOH与阳离子醚化剂摩尔比1．2、微波功率184W、辐射时间5min时，产物相对黏度为3．18，阳离子取代度为0．31。     

氨纶干法纺丝介质循环系统的设备和工艺介绍

介绍氨纶干法纺丝技术中纺丝介质 (SM )循环系统的主要设备 ,对循环风压力、风温度和风量控制进行了探讨。严格控制SM循环工艺参数 ,可减少并丝现象。     

智能混合控制器在转炉干法除尘中的应用

转炉干法除尘蒸发冷却器出口烟气温度大多数采用常规串级控制方式,但转炉冶炼前期控制效果并不理想.对转炉冶炼过程及蒸发冷却器出口烟气温度的控制难点进行研究,找出常规串级控制方式的缺点,并设计出一种智能混合控制器.采用智能模糊控制器和常规控制器并联的控制方式,对蒸发冷却器出口烟气温度进行控制,控制效果理想.实际应用表明,同常规串级控制器相比,智能混合控制器具有响应快、被控对象稳定等优点.     

中压分离器夹套部位接管组焊工艺

针对中压分离器夹套部位接管结构特点,分析了在制造过程中所面临的困难问题。介绍了为此而制定的特殊工艺方案以及方案的实施情况和结果。     

治理铬渣的两个关键

铬渣中存在的酸溶性六价铬是解毒效果能否持久的关键，而铬渣中游离氧化镁消化是利用铬渣作建筑材料时必须高度重视的问题，论述了湿法解毒、高温解毒和非熔融的综合利用法等方法，对铬盐行业的铬渣治理有指导作用。     

喷雾干燥塔结构对产品收率的影响

依据流体力学原理中颗粒沉降原理，对超细碳酸钙生产装置中压力式喷雾干燥塔的工艺参数进行了计算，并提出在干燥塔底增加一个文丘里装置的改造方案，降低了产品的落塔量，提高了干燥产品的收率；同时增加喷雾管道夹套冷却装置，避免了投料喷嘴容易堵塞、影响生产的现象，提高了干燥塔的生产能力。     

Investigation of CH4 Reforming with CO2 on Meso-Porous Al2O3-Supported Ni Catalyst

Meso-porous Al₂O₃-supported Ni catalysts exhibited the highest activity, stability and excellent coke-resistance ability for CH₄ reforming with CO₂ among several oxide-supported Ni catalysts (meso-porous Al₂O₃ (Yas1-2, Yas3-8), -Al₂O₃, -Al₂O₃, SiO₂, MgO, La₂O₃, CeO₂ and ZrO₂). The properties of deposited carbons depended on the properties of the supports, and on the meso-porous Al₂O₃-supported Ni catalyst, only the intermediate carbon of the reforming reaction formed. XRD and H₂-TPR analysis found that mainly spinel NiAl₂O₄ formed in meso-porous Al₂O₃ and -Al₂O₃-supported catalysts, while only NiO was detected in -Al₂O₃, SiO₂, CeO₂, La₂O₃ and ZrO₂ supports. The strong interaction between Ni and meso-porous Al₂O₃ improved the dispersion of Ni, retarded its sintering and improved the activated adsorption of CO₂. The coking reaction via CH₄ temperature-programed decomposition indicated that meso-porous Al₂O₃-supported Ni catalysts were less active for carbon formation by CH₄ decomposition than Ni/-Al₂O₃ and Ni/-Al₂O₃.