摘要:
This invention provides a method of manufacturing a hydrocarbon conversion catalyst by spray-drying a slurry containing alumina-magnesia and a crystalline alumonosilicate zeolite, which is chracterized in that the alumina-magnesia is treated with phosphrous containing solution before or after the slurry is subjected to a treatment of the spray-drying.
摘要翻译:本发明提供通过喷雾干燥含有氧化铝 - 氧化镁和结晶alumonosilicate沸石的浆料制造烃转化催化剂的方法,所有这一切都被chracterized DASS DER氧化铝 - 氧化镁与phosphrous浆料之前或之后包含溶液处理进行 处理喷雾干燥的。
摘要:
A process for the fluid catalytic cracking of a heavy fraction oil, which comprises the step of bringing the heavy fraction oil into contact with a catalyst containing an ultrastable Y-type zeolite, in a fluid catalytic cracking apparatus having a regenerating zone, a reaction zone, a separation zone and a stripping zone and under conditions that a reaction zone outlet temperature is in a range of 550 to 700°C, a catalyst/oil ratio is in a range of 15 to 100 wt/wt, and a difference between a regenerating zone catalyst concentration phase temperature (1) and the reaction zone outlet temperature (2) is in a range of 5 to 150°C. According to the fluid catalytic cracking process, an amount of dry gases generated by the thermal cracking of the heavy fraction oil can be lessened while a yield of light fraction olefins can be enhanced.
摘要:
A process for producing a fuel gas for fuel cells, which comprises treating a sulfur-containing hydrocarbon with a desulfurizing agent to reduce the sulfur content to 0.2ppm or less and bringing the treated hydrocarbon into contact with a steam reforming catalyst to provide a fuel gas mainly composed of hydrogen, characterized in that said desulfurizing agent comprises a copper-nickel alloy having a copper to nickel weight ratio of 95 : 5 to 5 : 95.
摘要:
A process for the fluid catalytic cracking of heavy fraction oils containing heavy metals such as Ni and V, which comprises withdrawing a portion of ferrite-containing catalyst particles circulating in a fluid catalytic cracking apparatus, separating the thus withdrawn catalyst particles into metals-richly deposited catalyst particles and metals-poorly deposited ones by using a magnetic separator and then returning the metals-poorly deposited catalyst particles, together with fresh ferrite-containing catalyst particles, into said cracking apparatus.