Slurry-phase skeletal iron catalyst process for synthesis gas conversion to hydrocarbons
View Patent ↗A continuous process is disclosed for the production of hydrocarbon liquids and wax by Fischer-Tropsch conversion of synthesis gas in contact with promoted skeletal iron catalyst particles in a slurry reactor. Wax product is readily separated from the skeletal iron catalyst in a catalyst settling drum and concentrated catalyst particles in wax slurry are recycled from the settling drum to the slurry reactor, while essentially solid-free wax is recovered as a product.
1. A continuous catalytic process for the conversion of synthesis gas into hydrocarbon liquids and wax, including the separation of wax from catalyst particles by gravity sedimentation, comprising:
contacting a feedstream comprising synthesis gas with a slurry of saturated hydrocarbon liquid arid skeletal iron catalyst particles in a reactor under conditions sufficient to convert the synthesis gas feedstream into by-product gases, light C 1 -C 4 hydrocarbon gases, C 5 + hydrocarbon liquids and hydrocarbon wax,
the skeletal iron catalyst particles having a skeletal structure formed by leaching a portion of metal from precursor particles;
separating the by-product gases, light hydrocarbon gases and C 5 + hydrocarbon liquids, excluding wax, as a reactor vapor overhead stream for separation and recovery of C 5 + hydrocarbon liquid products;
passing a reactor liquid slurry overflow stream rich in suspended skeletal iron catalyst particles and wax into a catalyst nettling drum through a reactor overflow line under conditions sufficient to separate catalyst particles and wax, wherein the skeletal iron catalyst particles in the overflow stream concentrate in a bottom portion of the drum by gravity sedimentation as a concentrated slurry of catalyst particles and hydrocarbon wax;
withdrawing a catalyst settling drum side-draw stream essentially free of catalyst particles from an upper portion or the drum and recovering wax product therefrom; and
passing a catalyst settling drum bottom stream rich in catalyst particles into a bottom portion of the reactor as a skeletal iron catalyst recycle stream.
2. The process of claim 1 , further comprising:
withdrawing a slip stream from the catalyst recycle stream as a spent catalyst purge stream; and
adding fresh catalyst to the reactor.
3. The process of claim 1 , further comprising:
treating said reactor liquid slurry overflow stream rich in suspended skeletal iron catalyst particles and wax in a hydroclone before passing the treated stream to the catalyst settling drum whereby the separation of catalyst particles and wax is augmented.
4. The process of claim 1 , wherein the reactor comprises a slurry bed reactor containing the skeletal iron catalyst particles.
5. The process of claim 4 , wherein the reactor conditions comprise a temperature of 230-280° C. a pressure of 1.7-5.5 MPa, and a space velocity of 1.0-5.0 NL/g-cat/hr.
6. The process of claim 1 , wherein the reactor further comprises internal cooling coils.
7. The reactor of claim 6 , wherein a liquid level in the reactor is maintained above the tap of the cooling coils by a liquid overflow line.
8. The process of claim 1 , further comprising:
recovering product wax from the catalyst settling drum side-draw stream by pumping the side-draw stream through a filter to remove trace spent catalyst;
passing the filtered stream to a wax product flash drum; and
recovering clear wax product from a bottom portion of the flash drum.
9. The process of claim 1 , wherein the catalyst settling drum side-draw stream contains less than 0.2 weight percent catalyst solids.
10. The process of claim 1 , wherein skeletal iron catalyst particles are recycled to the reactor from the bottom of the catalyst settling drum by pumping the recycle stream to a position in the reactor below reactor cooling coils.
11. The process of claim 1 , wherein the skeletal iron catalyst is an activated promoted catalyst.
12. The process of claim 11 , wherein the catalyst is activated by heating in contact with hydrogen gas and/or nitrogen.
13. The process of claim 1 , wherein the operating conditions of the catalyst settling drum comprise a temperature of 230-270° C., a pressure of 1.5-5.0 MPa Abs, and a residence time of 15-60 min.
14. The process of claim 1 , wherein 90-99 weight percent of the suspended catalyst particles in the reactor overflow stream settle in the bottom portion of the catalyst settling drum.
15. The process of claim 1 , wherein the syngas conversion comprises a once-through single pass operation.
16. The process of claim 1 , wherein the syngas conversion comprises a recycle mode operation wherein unconverted hydrogen gas and carbon monoxide are recycled to the syngas conversion reactor.
17. The process of claim 4 , wherein at least a portion of the skeletal iron catalyst particles in the slurry bed reactor have a particle size in a range of 20-200 microns.
18. The process of claim 1 , wherein the reactor comprises a fixed bed reactor containing the skeletal iron catalyst particles, wherein the at least a portion of the skeletal iron catalyst particles in the fixed bed reactor have a particle size in a range of 1000-10,000 microns.
19. A continuous catalytic process for the conversion of synthesis gas into hydrocarbon liquids and wax, comprising:
contacting synthesis gas with a slurry of hydrocarbon liquid and skeletal iron catalyst particles in a reactor under conditions sufficient to convert at least a portion of the synthesis gas into light C 1 -C 4 hydrocarbon gases, C 5 + hydrocarbon liquids, hydrocarbon wax, and optionally by-product gases,
the skeletal iron catalyst particles having a skeletal structure formed by leaching a portion of metal from precursor particles;
separating the light C 1 -C 4 hydrocarbon gases, C 5 + hydrocarbon liquids, and any by-product gases from the hydrocarbon wax as a reactor vapor overhead stream;
passing a reactor liquid slurry overflow stream containing suspended skeletal iron catalyst particles and hydrocarbon wax into a catalyst settling drum;
concentrating the skeletal iron catalyst particles in the liquid slurry overflow stream in a bottom portion of the catalyst settling drum by gravity sedimentation as a concentrated slurry of catalyst particles and hydrocarbon wax;
withdrawing a catalyst settling drum side-draw stream essentially free of catalyst particles from an upper portion of the catalyst settling drum and recovering hydrocarbon wax product therefrom; and
passing the concentrated slurry of catalyst particles and hydrocarbon wax into a bottom portion of the reactor as a skeletal iron catalyst recycle stream.
20. A continuous catalytic process for the conversion or synthesis gas into hydrocarbon liquids and wax, comprising:
forming synthesis gas comprised of carbon monoxide and hydrogen;
contacting the synthesis gas with a skeletal iron catalyst in a reactor under conditions sufficient to convert at least a portion of the synthesis gas into light C 1 -C 4 hydrocarbon gases, C 5 + hydrocarbon liquids, hydrocarbon wax, and optionally by-product gases,
the skeletal iron catalyst having a skeletal structure formed by leaching a portion of metal from precursor catalyst particles;
separating the light C 1 -C 4 hydrocarbon gases, C 5 + hydrocarbon liquids, and any by-product gases from the hydrocarbon wax as a reactor vapor overhead stream;
passing a reactor liquid slurry overflow stream containing suspended skeletal iron catalyst and hydrocarbon wax into a catalyst settling drum;
concentrating the skeletal iron catalyst in the liquid slurry overflow stream in a bottom portion of the catalyst settling drum by gravity sedimentation as a concentrated slurry of the skeletal iron catalyst and hydrocarbon wax;
withdrawing a catalyst settling drum side-draw stream essentially free of the skeletal iron catalyst from an upper portion of the catalyst settling drum and recovering hydrocarbon wax product therefrom; and
passing the concentrated slurry of the skeletal iron catalyst and hydrocarbon wax into a bottom portion of the reactor as a skeletal iron catalyst recycle stream.