柿竹园多金属矿选矿废水处理试验研究

针对柿竹园多金属矿选矿废水量大、难沉降、pH值高、COD高等特点,研究了石灰沉降+ZJYH03氧化法、石灰沉降+漂白粉氧化法、石灰沉降+NaClO氧化法、聚合硫酸铁沉降+ZJYH03氧化法和石灰沉降+生物氧化法等废水处理工艺,并对比分析了各工艺的处理效果和药剂成本,结果表明: 聚合硫酸铁沉降+ZJYH03氧化法取得了较好的处理效果,该方法具有工艺简单、水质无色透明、药剂成本低等特点。     

利用纤维床生物反应器发酵生产链霉素

利用纤维床生物反应器(FBB)发酵生产链霉素,对发酵培养基氮源进行了优化,并与传统搅拌发酵进行了比较。结果表明,以可溶性有机氮源大豆蛋白胨作为发酵培养基氮源,并添加一定量蔗糖,可以完全替代黄豆粉,在1 LFBB中发酵96 h时链霉素效价达到5 567 U·mL~(-1)。在整个发酵过程中,所有菌体都被固定在纤维床反应器上,而发酵液保持澄清,这不仅有利于从无菌体的发酵液中进行产物的提取和纯化,也可以重复利用菌体生产次级代谢产物,从而缩短发酵周期,进一步提高链霉素在发酵过程中的体积生产率。     

Characterizations of friction welding joint interface for AISI 316

Because of heat amount is different from peripheral to central of friction welding interface, which is leaded to vary the characterizations along that interface. Current study, respectively, focused on the effect of different friction pressure on micro-structural and mechanical properties of that friction welding joint interface. Presently, these friction pressures are 110, 130, 150 and 170 MPa while kept all other conditions constant. The effects of different friction pressure on welding interface characterization were investigated by EDX, SEM, tensile, compression, impact and hardness tests. The tensile tests carried out on the standardized test piece with diameter 6 mm and 8 mm, thus, compression tests were extracted from the positions of 0°, 45° 90° with test specimen of 4 mm diameter and 6.5 mm length at weld center. Whereas, the impact test pieces were picked up in two positions, the first one is symmetrical, which it obtained to the respect of the rotation axis and the interface, on the other hand, the second one is non-symmetrical with the axis of rotation and symmetrical to the interface, for making the notch head coincide with the center of the welded joint, The obtained results showed that with reducing of friction pressure will present lack of bonding increasing from peripheral toward the welding center, which will responsible on reducing of the mechanical properties such as tensile, compression and impact strength.     

床温及SNCR脱硝对CFB锅炉NOx和N2O排放影响的试验研究

为了研究循环流化床（CFB）锅炉燃用无烟煤时床温及选择性非催化还原（SNCR）脱硝对于NO和N2O排放的影响，在1 MW CFB试验装置上开展了试验研究。结果表明:床温由880 ℃提高到970 ℃，NO排放质量浓度由119.5 mg/m3上升到226.0 mg/m3，N2O排放质量浓度由216.0 mg/m3降低到102.2 mg/m3；在氨氮摩尔比（NSR）为0~3.7之间，随着NSR的提高，脱硝效率从0上升到50.72%；进一步提高NSR到5.2，脱硝效率升至53.61%，增加较为缓慢；随着NSR从0提高到1.7，N2O排放质量浓度由84.3 mg/m3上升至118.3 mg/m3，增长较为缓慢；进一步提高NSR至2.0，N2O排放质量浓度上升至187.7 mg/m3，增长速度提高；继续提高NSR至5.2，N2O排放质量浓度上升至381.4 mg/m3；CFB锅炉采用以尿素为还原剂的SNCR脱硝工艺时，单纯通过加大NSR来提高脱硝效率不仅效果有限，过量喷入的还原剂会造成N2O排放量的显著提高。     

耦合膜分离的新型CO2低温捕集系统性能优化

CO₂捕集作为温室气体排放控制的有效手段已成为重要研究课题。作为新兴捕集技术之一，低温CO₂捕集因产品纯度高、无附加污染等优势受到关注。然而，该技术能耗和捕集率对于气体中CO₂浓度十分敏感，对于高CO₂浓度气体可获得较高的CO₂捕集率和较低能耗水平。基于此，本文提出了耦合膜分离的新型CO₂低温捕集系统，通过膜材料选择渗透性实现待捕集气体CO₂浓度主动调控，并在最优浓度下进行CO₂低温捕集。首先基于不同传统低温捕集系统特点，对比分析了不同耦合系统模式，从而确定了最优耦合系统结构。针对最优耦合系统进行了运行参数优化，并分别基于实现系统捕集能耗最低与捕集率最高的目标，获得了膜渗透侧CO₂浓度与进气CO₂浓度间的关系式，为该耦合系统中膜组件选型提供指导。研究表明，本文提出的耦合系统捕集能耗为1.92MJ/kgCO₂，相比于传统单一低温系统捕集能耗可降低16.5%。