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1)  self-propagating high-temperature synthesis
燃烧反应合成
1.
Al-Cu-based sound-absorbing materials by self-propagating high-temperature synthesis
燃烧反应合成Al-Cu基吸声材料
2)  combustion [英][kəm'bʌstʃən]  [美][kəm'bʌstʃən]
燃烧反应
1.
The Kinetic Study of PMMA Isothermal Combustion;
聚甲基丙烯酸甲酯等温燃烧反应的动力学研究
2.
The flame temperature of C_2H_2 combustion in NO was 3587 K by theoretical colculation, which was very near its actual temperature (3368 K).
1196n λ计算了乙炔在NO中燃烧反应的火焰温度,计算值为3587K,与实际温度3368K非常接近。
3)  combustion synthesis
燃烧反应
4)  combustion reaction
燃烧反应
1.
Mechanism of H_2 combustion reaction in N_2O;
H_2在N_2O内燃烧反应机理探讨
2.
Flame temperature of gas combustion reaction;
煤气燃烧反应的火焰温度
3.
The results showed that the main products of combustion reaction were TiB2 and MoB.
 采用燃烧反应工艺焊接了TiB2陶瓷与金属Mo,对中间反应层生成物进行了XRD物相分析,对焊接界面结合情况进行了电子探针分析。
5)  combustion synthesis
燃烧合成
1.
Densification factors of C_f/TiC-TiB_2 ceramic composites by combustion synthesis;
燃烧合成C_f/TiC-TiB_2陶瓷基复合材料的致密化因素探讨
2.
Effects of experimental parameters and mass-fractional of Al on combustion synthesis of Ti_3AlC_2;
实验参数和Al质量分数对燃烧合成Ti_3AlC_2的影响
3.
Effect of an external electric field on the combustion synthesis process of TiO_2-C-Al system;
电场对TiO_2-C-Al系燃烧合成过程的影响
6)  combustion reactivity
燃烧反应性
1.
By employing the method of thermogravimetric analysis and powder X-ray diffraction measured respectively were the combustion reactivity and structural changes of the semicoke of two low-rank bituminous coals and one type of anthracite during the process of pyrolysis at 400~1400 ℃.
用热天平(TGA)和粉末X射线衍射方法(XRD)分别测量了两种低变质程度烟煤和一种无烟煤的半焦在400~1 400℃热解过程中燃烧反应性及其结构的变化,探讨了低变质煤的反应性变化的原因。
2.
The combustion reactivity of chars from pyrolysis of Shenmu coal maceral concentrates under different pyrolysis temperature, heating rate and pressure were systematically investigated by using TGA.
近年来 ,对显微组分热解半焦燃烧反应性的研究已有报道[1~ 4 ] 。
3.
Taking the blended coal chars of anthracite and bituminous coal as examples,the physical and chemical properties and combustion reactivity of blended coal chars were investigated by micro-analysis method.
以无烟煤和烟煤的混煤焦为例,采用微观分析方法研究混煤焦的理化特性和燃烧反应性。
补充资料:催化燃烧反应器
分子式:
CAS号:

性质:实现催化燃烧反应过程的设备。反应器有固定床和流化床两类,目前工业上多采用固定床反应器。其主要优点:轴向返混少、反应速度较快,因而反应器体积小,催化剂用量少;气体在反应器内停留时间可严格控制,温度分布可适当调节,因而有利于提高转化率和选择性;催化剂磨损少;可在高温高压下操作。缺点是传热条件较差,不能用细粒催化剂,催化剂更换、再生较困难。根据催化剂床层,分布形式,反应器可分立式和卧式两种。根据换热要求和方式的不同,固定床反应器又可分为绝热式和换热式两类,用于废气净化反应器多数为绝热反应器。单段绝热反应器具有构造简单,气体分布均匀,空间利用率高等优点,但轴向浓度分布不均匀。为了能在一定程度上调节反应温度,可用多段反应器,段间进行热交换。

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