Medium and low temperature coal tar hydrorefining technology
A low-temperature coal tar and hydrotreating technology, applied in hydrotreating process, petroleum industry, refined hydrocarbon oil, etc., can solve the problems of cracking of aromatic hydrocarbons and affecting product income, etc.
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Examples
Embodiment 1
[0045] The catalyst was prepared by impregnation method, and the carrier was doped Co 2+ SAPO-5, Co 2+ The doping amount in SAPO-5 is controlled at 0.65% of the carrier mass. The active component molybdenum nitride MO 2 N, tungsten nitride W 2 N, molybdenum carbide Mo 2 The total content of C and tungsten carbide WC is 10% of the mass of the carrier, and their molar ratio is 1:0.4:0.3:0.8.
[0046] The catalyst is loaded into a fixed bed reactor, the reaction tube of the reactor is made of stainless steel with an inner diameter of 50mm, the catalyst bed is set to 3 layers, the temperature of the catalyst bed is measured by a UGU808 temperature control meter, and the raw material is medium and low temperature Coal tar was continuously transported by a double-plunger micropump manufactured by Beijing Satellite Manufacturing Plant. Hydrogen was supplied by a high-pressure gas cylinder and the flow rate was controlled by a Beijing Qixing Huachuang D07-11A / ZM gas mass flow mete...
Embodiment 2
[0051] The catalyst was prepared by impregnation method, and the carrier was doped Co 2+ SAPO-5, Co 2+ The doping amount in SAPO-5 is controlled at 0.7% of the carrier mass. The active component molybdenum nitride MO 2 N, tungsten nitride W 2 N, molybdenum carbide Mo 2 The total content of C and tungsten carbide WC is 10% of the mass of the carrier, and the molar ratio is 1:0.6:0.45):1.2.
[0052] All the other conditions are the same as in Example 1.
[0053] The final product was tested, the total sulfur content was reduced to 3ppm, and the loss rate of aromatics was less than 2%.
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More