Thermal cracking wax to normal alpha-olefins

Claim 1

The method of preparing n-alpha olefins containing 6-18 carbon atoms which comprises preheating and vaporizing a charge hydrocarbon wax stock to thermal cracking temperature; passing said charge hydrocarbon wax stock during said preheating and vaporizing operation through the intermediate temperature range of 625° F-800° F in a time less than about 8 seconds whereby the desired product contains a decreased porportion of paraffin impurities; thermally cracking said preheated charge wax stock in vapor phase at inlet temperatue of 600° F-800° F in the presence of steam at thermal cracking conditions thereby forming a product stream cracking effluent containing desired product n-alpha olefins containing 6-18 carbon atoms together with decreased proportion of paraffin impurities; withdrawing said product stream cracking effluent at 1050° F-1250° F; separating said desired product n-alpha olefins containing 6-18 carbon atoms from said product stream cracking effluent; and maintaining the Severity Value of said product stream cracking effluent during said separating less than about 66.5.

Claim 2

The method of preparing n-alpha olefins containing 6-18 carbon atoms which comprises preheating and vaporizing a charge hydrocarbon wax stock to thermal cracking temperature; passing said charge hydrocarbon wax stock during said preheating and vaporizing operation through the intermediate temperature range of 625° F-800° F in a time less than about 8 seconds whereby the desired product contains a decreased porportion of paraffin impurities; thermally cracking said preheated charge wax stock in vapor phase at inlet temperatue of 600° F-800° F in the presence of steam at thermal cracking conditions thereby forming a product stream cracking effluent containing desired product n-alpha olefins containing 6-18 carbon atoms together with decreased proportion of paraffin impurities; withdrawing said product stream cracking effluent at 1050° F-1250° F; separating said desired product n-alpha olefins containing 6-18 carbon atoms from said product stream cracking effluent; and maintaining the Severity Value of said product stream cracking effluent during said separating less than about 66.5.

Claim 5

The method of preparing n-alpha olefins containing 6-18 carbon atoms which comprises preheating and vaporizing a charge hydrocarbon wax stock to thermal cracking temperature; passing said charge wax stock during said preheating and vaporizing operation through the intermediate temperature range of 625° F-800° F in time less than about 8 seconds whereby the desired product contains a decreased proportion of paraffin impurities; thermally cracking said preheated charge wax stock in vapor phase, at inlet temperature of 600° F-800° F in the presence of steam at thermal cracking conditions thereby forming a product stream containing desired product n-alpha olefins containing 6-18 carbon atoms together with decreased proportion of paraffin impurities; withdrawing said product stream cracking effluent at 1050° F-1250° F; rectifying the thermally cracked wax stock thereby forming a n-alpha olefin containing rectified bottoms containing hydrocarbons having more than about 6 carbon atoms; distilling said n-alpha olefin containing rectified bottoms thereby forming as overhead, product n-alpha olefin stream containing hydrocarbons having 6-18 carbon atoms; and maintaining the overall Severity Value of said rectifying operation and said distilling operation less than about 66.5.

Claim 6

The method of preparing n-alpha olefins containing 6-18 carbon atoms which comprises preheating and vaporizing a charge hydrocarbon wax stock to thermal cracking temperature; passing said charge wax stock during said preheating and vaporizing operation through the intermediate temperature range of 625° F-800° F in time less than about 8 seconds whereby the desired product contains a decreased proportion of paraffin impurities; thermally cracking said preheated charge wax stock in vapor phase, at inlet temperature of 600° F-800° F in the presence of steam at thermal cracking conditions thereby forming a product stream containing desired product n-alpha olefins containing 6-18 carbon atoms together with decreased proportion of paraffin impurities; withdrawing said product stream cracking effluent at 1050° F-1250° F; rectifying the thermally cracked wax stock thereby forming a n-alpha olefin containing rectified bottoms containing hydrocarbons having more than about 6 carbon atoms; distilling said n-alpha olefin containing rectified bottoms thereby forming as overhead, product n-alpha olefin stream containing hydrocarbons having 6-18 carbon atoms; and maintaining the overall Severity Value of said rectifying operation and said distilling operation less than about 66.5.

Claim 11

The method of preparing n-alpha olefins containing 6-18 carbon atoms which comprises preheating and vaporizing a charge hydrocarbon wax stock to thermal cracking temperature; passing said charge wax stock during said preheating operation through the intermediate temperature range of 625° F-800° F in time less than about 5 seconds whereby the desired product contains a decreased proportion of paraffin impurities; thermally cracking said preheated charge wax stock in vapor phase, at inlet temperature of 600° F-800° F, in the presence of steam at thermal cracking conditions thereby forming a product stream containing desired product n-alpha olefins containing 6-18 carbon atoms together with decreased proportion of paraffin impurities; withdrawing said product stream cracking effluent at 1050° F-1250° F; rectifying the thermally cracked wax stock thereby forming a n-alpha olefin containing rectified bottoms containing hydrocarbons having more than about 6 carbon atoms; distilling said n-alpha olefin containing rectified bottoms thereby forming (i) as overhead a product n-alpha olefin stream containing hydrocarbons having 6-18 carbon atoms and (ii) as bottoms a stream containing hydrocarbons having more than about 20 carbon atoms; passing a portion of said distilling operation bottoms as quench liquid to the effluent of said cracking operation; fractionating a portion of said distilling operation bottoms thereby forming as overhead a wax condensate; recycling at least a portion of said wax condensate to the charge to said preheating operation; and maintaining the overall Severity Value in the column preheater, column sump, and column reboiler portions of said rectifying operation, said distilling operation and said fractionating operation less than about 66.5.

Claim 12

The method of preparing n-alpha olefins containing 6-18 carbon atoms which comprises preheating and vaporizing a charge hydrocarbon wax stock to thermal cracking temperature; passing said charge wax stock during said preheating operation through the intermediate temperature range of 625° F-800° F in time less than about 5 seconds whereby the desired product contains a decreased proportion of paraffin impurities; thermally cracking said preheated charge wax stock in vapor phase, at inlet temperature of 600° F-800° F, in the presence of steam at thermal cracking conditions thereby forming a product stream containing desired product n-alpha olefins containing 6-18 carbon atoms together with decreased proportion of paraffin impurities; withdrawing said product stream cracking effluent at 1050° F-1250° F; rectifying the thermally cracked wax stock thereby forming a n-alpha olefin containing rectified bottoms containing hydrocarbons having more than about 6 carbon atoms; distilling said n-alpha olefin containing rectified bottoms thereby forming (i) as overhead a product n-alpha olefin stream containing hydrocarbons having 6-18 carbon atoms and (ii) as bottoms a stream containing hydrocarbons having more than about 20 carbon atoms; passing a portion of said distilling operation bottoms as quench liquid to the effluent of said cracking operation; fractionating a portion of said distilling operation bottoms thereby forming as overhead a wax condensate; recycling at least a portion of said wax condensate to the charge to said preheating operation; and maintaining the overall Severity Value in the column preheater, column sump, and column reboiler portions of said rectifying operation, said distilling operation and said fractionating operation less than about 66.5.