摘要:
It is the objective of the present invention to provide a method for preparing a sintering resistant alkali-zeolite supported metal catalyst for catalytic methane oxidation that does not degrade by particle sintering and zeolite framework dealumination. This objective is achieved according to the present invention by a method for producing a precious metal/metal cation zeolite catalyst, hereinafter referred to as PM/MC-zeolite catalyst, for selective catalytic methane oxidation, comprising the steps of: a) treating a parent zeolite under desilication conditions in order to form mesopores (hereinafter referred to as nanocages) resulting in a desilicated zeolite; b) treating the desilicated zeolite in order to selectively extract extra-framework aluminum and surface framework aluminum, respectively, resulting in an acidic H-zeolite; c) loading the acidic H-zeolite with a precious metal compound by ion-exchange, impregnation or other technique and subsequent calcination resulting in an acidic PM/H-zeolite; d) neutralizing the strong acid sites of the PM/H-zeolite by a basic alkali metal salt or a base, and thus stabilize the precious metal within the nanocages of the zeolite. This method yields a hydrothermally stable sintering resistant methane oxidation catalyst. Both problems mentioned above are solved by the synthetic approach based on the removal of the acid sites of the parent PM/H-zeolite by post-exchanging it with an alkali cation, which resulted in capturing nano-sized PM particles within a zeolitic hierarchical structure and stabilization of the framework aluminum.
摘要:
A method of removing ventilation air methane (VAM) from ventilation air in coal mines using a chemical looping process to move metal or metal oxide particles between reactors such as a hydrogen generator (5) and a regenerator (7) to alternatively reduce and oxidise the particles such that VAM introduced into a combustor (6) provided with hydrogen from the hydrogen generator (5) can be processed in the regenerator (7) to produce air plus water plus carbon dioxide. Other variations involve the use of three reactors in the chemical looping process.
摘要:
A process engineering arrangement comprises a temperature swing adsorption apparatus (1) with at least one adsorber device (10), which is configured to adsorb at least one component of a process gas (G11), in an adsorption mode, and to release the at least one adsorbed component into a purge gas (G12) at a regeneration temperature, in a regeneration mode; a heating device (11), configured to heat the purge gas (G12) to at least the regeneration temperature; and a solar energy device (12) being configured to feed energy to the heating device (11) for operating the heating device (11).
摘要:
A hydrocarbons removal system and methods and uses thereof are described. The hydrocarbons removal system can comprise at least one sulfur trap and an oxidation catalyst.
摘要:
A method of forming the highly selective ultra-small pore amorphous adsorbent includes introducing an ion-exchange material to a sodium aluminosilicate zeolite such that an ion-exchanged zeolite forms, calcinating the ion-exchanged zeolite at a calcination temperature such that the ion-exchanged zeolite collapses and forms the decationized amorphous adsorbent, and introducing a back ion-exchange material to the decationized amorphous adsorbent such that the highly selective ultra-small pore amorphous adsorbent forms. The highly selective ultra-small pore amorphous adsorbent has a pore aperture size operable to permit carbon dioxide to adsorb into the amorphous adsorbent and operable to deny methane from adsorbing into the amorphous adsorbent.
摘要:
The present invention relates to a method for the oxidation of short-chain hydrocarbons, in particular methane. Said method uses a catalyst comprising a zeolite material which contains titanium and at least two noble metals. The invention also relates to the use of said catalyst for the oxidation of short-chain hydrocarbons, in particular methane, in exhaust gas streams.
摘要:
In a method for removing methane from feed gas having a methane concentration of 2 mole % or less, the feed gas is optionally mixed with make-up methane or air and passed through a heat exchanger to heat the gas to an oxidation reactor inlet temperature T1. The heated stream is passed to the reactor where the methane is oxidised. A gas stream including the products of the oxidation reaction are removed with the gas stream being at a reactor outlet temperature T2 higher than the inlet temperature T1. The gas stream is then passed through the heat exchanger against the reactor stream to recover heat from the gas stream removed in the reactor and to heat the reactor stream. The outlet temperature T2 is measured and the inlet temperature T1 is controlled by adjusting the relative amount of make-up methane and/or air added to the feed gas.
摘要:
Es wird eine Anlage (1) beschrieben, mit welcher aus Gasen, die einen hohen Inertgasanteil und einen geringen Methangasanteil aufweisen, Methangas entfernt werden kann. Sie besitzt hierzu eine Vorrichtung (2), die ein Außengehäuse (6) mit einem Einlass (3) für das zu reinigende Gas und einen Auslass (4) für das gereinigte Gas besitzt. Ein Wärmetauscher (8) wird von dem zu reinigenden Gas ein erstes Mal durchtreten und gelangt sodann in eine Katalysatorpackung (10), in welcher der Methangasanteil katalytisch unter Wärmeentwicklung entfernt wird. Das gereinigte Inertgas durchströmt nunmehr den Wärmetauscher (8) ein zweites Mal und steht dabei in Wärmeaustausch mit dem den Wärmetauscher (8) durchströmenden zu reinigenden Gas. Auf diese Weise lassen sich praktisch ohne Energieaufwand auch kleinste Methangasmengen aus Gasgemischen entfernen. Die entstehenden Reingase können einer weiteren Nutzung zugeführt werden.
摘要:
The present invention relates to a mixed-matrix composition comprising polymer having a fractional free volume of at least 0.1 and porous particles.