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reformer for the catalytic cleavage of gaseous hydrocarbons.

机译:重整器,用于气态烃的催化裂解。

摘要

A reformer for catalytic cracking of gaseous hydrocarbons, in particular in the presence of water vapour, for obtaining a reconstituted gas, comprises a pressurized tank (1), a plurality of cracking tubes (2) parallel to one another in said tank, and a catalyst (PK). The heat convected through the tube walls and originating from a burning heating gas is transferred to the processing gas passing through the catalyst. In order to facilitate, on the one hand, the replacement of the catalyst, the heating gas (HG) is conveyed through the cracking tubes (2') and the catalyst (PK) is introduced into the pressurized tank (1) between the cracking tubes in the form of a loose material, and, on the other hand, in order to improve the support system for the cracking tubes, the tubes (2') are jointly supported with the catalyst (PK) vertically on a vault (5) made of ceramic material, provided with gas passages (5b) and defining a gas-collection space (9) for the reconstituted gas (PD). During use of the reformer as a primary reformer in a primary and secondary reformer installation, it is envisaged that in order to simplify said installation and improve thermal economy, the primary reformer (PR) and secondary reformer (SR) are arranged in a single pressurized tank (19) and that the reconstituted gas (PD) from the secondary reformer (SR) is fed to the primary reformer for the purpose of convection heating of the latter.
机译:一种用于气态烃的催化裂化,特别是在水蒸气存在下催化裂化的重整器,用于获得再生气体,该重整器包括加压罐(1),在所述罐中彼此平行的多个裂化管(2),以及催化剂(PK)。通过管壁对流并来自燃烧的加热气体的热被传递到通过催化剂的处理气体。为了一方面促进催化剂的更换,将加热气体(HG)通过裂化管(2')输送,并且将催化剂(PK)在裂化之间引入加压罐(1)中。另一方面,为了改进裂解管的支撑系统,管(2')与催化剂(PK)共同垂直支撑在金库(5)上由陶瓷制成的材料,具有气体通道(5b),并限定了用于再生气体(PD)的气体收集空间(9)。设想在将重整器用作初级和次级重整器装置中的初级重整器期间,为了简化所述安装并提高热经济性,将初级重整器(PR)和次级重整器(SR)布置在单个加压装置中。罐(19),并将来自二级重整器(SR)的再生气体(PD)进料到一级重整器中,以进行对流加热。

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