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1)  DDS catalyst
DDS催化剂
1.
This article delineates the mechanism of DDS catalysts and the basic principle of the DDS solution desulfurization process,and discusses the process and applications of this wet method,and verifies the feasibility of this process.
论述了DDS催化剂的催化机理及DDS溶液脱硫基本原理,讨论了DDS生化湿法脱硫技术工艺流程及工业应用,验证了DDS生化湿法脱硫技术的可行性。
2.
The developing process was introduced for DDS de-sulfur technology from the of point of view of biochemistry, the constituent and action of DDS catalyst were analyzed, the basic principle was discussed for “gas de-sulfur method by catalysis of biochemical iron-alkali solution”, the problems to be noticed were indicated in the application process of DDS de-sulfur technolo.
从生物化学的角度介绍了DDS脱硫技术的研发过程 ,分析了DDS催化剂的组成和作用 ,论述了“生化铁—碱溶液催化法气体脱硫方法”的基本原理 ,指出了DDS脱硫技术在使用过程中应注意的问题。
3.
A new method has been developed for desulfurization and decarbonization of gases catalyzed by DDS catalyst.
介绍了DDS催化剂脱硫技术的理论基础和实验研究的方法与结果 ,并介绍了DDS催化剂脱硫技术在化肥厂半水煤气与变换气脱硫过程的工业应用 ,用于脱硫和脱碳 ,可将气体中总硫脱至 1mg/m3以下 ,二氧化碳含量降至 0 。
2)  Catalytic promotor DDS
催化助剂DDS
3)  DDS additives
DDS添加剂
1.
Since the prepressing property of low molar ratio urea formaldehyde resin was not suitable enough for veneer layingup during plywood production, the authors tried to improve it by adding DDS additives.
 针对现在胶合板用低摩尔比的脲醛树脂胶(UF)预压性能差的问题进行了研究,试验结果表明,用DDS添加剂和RN阳离子表面活性剂的组合能明显改善UF胶的预压性能。
4)  catalysis/catalyzer
催化/催化剂
5)  catalytic cracking catalyst
催化裂化催化剂
1.
The application of clay minerals in catalytic cracking catalysts is discussed in three aspects in this paper.
粘土矿物在催化裂化催化剂中的应用表现在三个方面 :(1)在无定形硅铝凝胶引入之前 ,活性白土的使用代表着一个历史阶段 ;(2 )层柱粘土的研究是目前国际上活跃的新型催化材料前沿课题之一 ,层柱蒙脱石的制备研究是当前最有吸引力的研究方向 ,铝多核羟基金属阳离子或有铝参与的多核羟基双金属阳离子柱化剂的研究制备是当前主要研究课题 ,并有从制备单一铝多核羟基聚合金属阳离子柱化剂向制备铝和其它元素的多核羟基聚合金属阳离子柱化剂的方向发展的趋势 ;(3)在寻求新催化剂载体中 ,伊 /蒙间层等矿物的层柱化显得尤为重要 ,用高岭土作催化裂化催化剂载体 ,在目前和将来的一段时间内仍将发挥重要作用 ,高岭土的成因、矿物成分、杂质含量、结构羟基的热稳定性以及物理性质等对催化特性均有影响 ,并有可能从中寻找到无活性载体。
2.
The mixture of zeolite REUSY and HL/HW composite zeolite with different contents of zeolite HW (IW/IL, the intensity ratio of XRD characteristic peaks for zeolite W and zeolite L, denoted as the content of zeolite HW in HL/HW composite zeolite) was used as the active component of catalytic cracking catalyst.
将不同HW沸石含量(以W及L沸石的XRD特定峰强度IW/IL值表示HW沸石在HL/HW复合沸石中的含量)的HL/HW复合沸石与REUSY沸石按相同比例复配后作为烃类催化裂化催化剂的活性组分,采用标准轻油微反方法对催化剂进行了活性评价(MAT),考察了不同HW含量的HL/HW复合沸石对催化剂活性、反应产物分布、汽油产品辛烷值及催化剂上积炭的影响。
6)  FCC catalyst
催化裂化催化剂
1.
Preparation of heavy metal resistant FCC catalyst;
抗重金属重油催化裂化催化剂的研制
2.
Performance evaluation of vanadium- tolerant FCC catalyst;
抗钒催化裂化催化剂的性能评价
3.
As an active component of fluid catalytic cracking(FCC) catalyst,the performance of Y zeolite catalysts after modification is reviewed,with the emphasis on the usage of FCC catalysts in desulfuration,enhancing the yield of diesel oil and propylene after a particular modification.
对催化裂化催化剂的活性组分Y型分子筛的脱铝改性及抗重金属污染改性方法和改性后的含Y型沸石的性能进行了详细介绍。
补充资料:Polymer of DDS,TPS,BD
CAS:61778-68-5
中文名称:1,12-十二烷二酸与对苯二甲酸和1,4-丁二醇的聚合物
英文名称:Polymer of DDS, TPS, BD;Polymer of DDS,TPS,BD
说明:补充资料仅用于学习参考,请勿用于其它任何用途。
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