Integrated product by process for poly olefin production with reduced greenhouse gas emission

An amorphous poly alpha olefin (APAO) made with substantially zero CO2 emissions made by the process comprising the steps of:

• a. converting alkanes to ethylene, propylene, and 1-butene using renewable electric power in an oxidative-coupling of methane (OCM) plant comprising an ethylene plant, a 2-butene plant, a propylene plant, and a 1-butene plant, by the steps comprising:
• (i) providing an ethylene plant comprising an oxidation reactor and a first fractionation train and converting a natural gas and oxygen in the oxidation reactor to produce an oxidation reactor effluent comprising ethylene and passing the oxidation reactor effluent to the first fractionation train to recover a first ethylene stream, a second ethylene stream, and a third ethylene stream;
• (ii) providing a 2-butene plant comprising a dimerization unit and a second fractionation train and converting a portion of the first ethylene stream in the dimerization unit to produce a dimerization unit effluent comprising 2-butene and passing the dimerization unit effluent to the second fractionation train to recover a first 2-butene stream and a second 2-butene stream;
• (iii) providing a propylene plant comprising a metathesis reactor and a third fractionation train and converting a portion of the first 2-butene stream and a portion of the second ethylene stream in the metathesis reactor to produce a metathesis reactor effluent comprising propylene and passing the metathesis reactor effluent to the third fractionation train to recover the propylene;
• (iv) providing a 1-butene plant comprising a butene isomerization unit and a fourth fractionation train and converting a portion of the second 2-butene stream in the butene isomerization unit to produce a butene isomerization unit effluent comprising 1-butene and passing the butene isomerization unit effluent to the fourth fractionation train to recover the 1-butene;
• b. polymerizing any one of the 1-butene, propylene, or third ethylene stream in an APAO plant comprising boilers in which boiler stack gasses are produced, the polymerization comprising the simultaneous steps of:
• (i) applying a temperature of 130-175° F. to the 1-butene, the propylene or the third ethylene stream from the 1-butene plant, the propylene plant, or the ethylene plant, respectively;
• (ii) using renewable electric power to power the boilers while scrubbing at least one of the boiler stack gasses with a solvent to sequester carbon dioxide from the at least one of the boiler stack gasses;
• wherein the completion of steps (a.) and (b.) results in substantially zero CO2 emissions into the atmosphere and the formation of an amorphous poly alpha olefin.