Method for Cracking C_4 and preparing olefin by refinery C_4
A technology for refining carbon 4 and cracking carbon, which is applied in the field of producing ethylene and propylene, can solve the problems such as insufficient and effective utilization of carbon 4 resources, and achieve the effects of reducing production costs, increasing economic benefits and large economic benefits.
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[0040] Reference attached figure 1 The method of the present invention will be described.
[0041] Taking a 720,000-ton / year ethylene unit as an example, using the original unit, before adding C4 in the refinery, the raw material flow rate of naphtha used was 82575000kg / h (660,600 tons / year), and other cracking raw materials were 220000kg / h ( 1.76 million tons / year), 90,100kg / h ethylene (720,000 tons / year), 44,530kg / h propylene (356,000 tons / year), 16,240kg / h butadiene (130,000 tons / year), and 8,250kg / h isobutylene (66,000 tons / year).
[0042] After adopting the method of the present invention, add the naphtha of 76000kg / h (608,000 tons / year) and other cracking raw materials of 220000kg / h (1,760,000 tons / year) to enter the steam thermal cracking furnace, and the temperature produced after the cracking is Cracked gas at 820°C and pressure 0.15MPa is mixed with catalytic cracked gas from olefin catalytic cracking reactor and then enters the quenching system. The mixed cracked...
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