Hydropyrolysis of biomass-containing feedstocks

Patent metadata

Field	Value
Publication number	US-10619105-B2
Application number	US-201715474245-A
Country	US
Kind code	B2
Filing date	Mar 30, 2017
Priority date	Jul 1, 2014
Publication date	Apr 14, 2020
Grant date	Apr 14, 2020

Abstract

Various techniques are disclosed for pretreating municipal solid waste (MSW) and other biomass-containing feedstocks that may be of a poorer quality and consequently more difficult, or even impossible, to convert to higher value liquid products (e.g., transportation fuels) using conventional processes. Such conventional processes may otherwise be satisfactory for the conversion of the biomass portion of the feedstock alone. The pretreatment of biomass-containing feedstocks may generally include steps carried out prior to a hydropyrolysis step and optionally further steps, in order to change one or more characteristics of the feedstock, rendering it more easily upgradable.

First claim

We claim:

1. A process for producing a higher value liquid product from an initial feedstock comprising the steps of:
a) removing a least a portion of plastic in the initial feedstock to provide a municipal solid waste (MSW) feedstock having a reduced plastic content relative to the initial feedstock; and
b) hydropyrolyzing the MSW feedstock in a hydropyrolysis reactor vessel containing hydrogen and a deoxygenating catalyst, producing a hydropyrolysis reactor output comprising at least one non-condensable gas, a partially deoxygenated hydropyrolysis product, and char particles,
wherein the MSW feedstock comprises one or more of (i) from about 5% to about 25% by weight polyethylene terephthalate, (ii) from about 5% to about 30% by weight high density polyethylene (iii) from about 1% to about 10% by weight polyvinyl chloride, (iv) from about 10% to about 35% by weight low density polyethylene, (v) from about 12% to about 40% by weight polypropylene, or (vi) from about 3% to about 15% by weight polystyrene.

2. The process of claim 1 , further comprising:
c) removing substantially all of the char particles from the hydropyrolysis reactor output to provide a purified hydropyrolysis reactor vapor stream having a reduced char content;
d) hydroconverting the purified hydropyrolysis reactor vapor stream in a hydroconversion reactor vessel in the presence of a hydroconversion catalyst, producing a hydroconversion reactor output; and
e) recovering a substantially fully deoxygenated hydrocarbon liquid and a gaseous mixture from the hydroconversion reactor output,
wherein the hydroconversion reactor output of step d) and the gaseous mixture of step e) include one or more contaminant gases generated from the hydrogenation of heteroatom-containing compounds in the MSW feedstock, the one or more contaminant gases selected from the group consisting of HCl, H 2 S, and NH 3 , the process further comprising:
f) removing at least a portion of the one or more contaminant gases from the hydroconversion reactor output of step d) or the gaseous mixture of step e).

3. The process of claim 2 , wherein the one or more contaminant gases includes HCl and step f) comprises contacting at least a portion of the reactor output of step d) or the gaseous mixture of step e) with a solid sorbent that adsorbs HCl.

4. The process of claim 1 , wherein the hydropyrolyzing step b) is operated with continuous, intermittent, or localized high agitation conditions that reduce the formation of agglomerates of particles of the deoxygenating catalyst.

5. The process of claim 4 , wherein the high agitation conditions include the continuous, intermittent, or localized use of a gas velocity that, in combination with the average particle size and particle size distribution of particles of the deoxygenating catalyst and agglomerates thereof in the hydropyrolysis reactor vessel, breaks formed agglomerates of particles of the deoxygenating catalyst.

6. The process of claim 5 , wherein the high agitation conditions include intermittent and localized use of a gas velocity that exceeds the overall superficial velocity of fluidizing gas in the hydropyrolysis reactor vessel.

7. The process of claim 1 , wherein said removing step (a) comprises providing, as at least a first fraction, the MSW feedstock, and further providing a second fraction having a content of plastic that is higher, compared to the content of plastic of the MSW feedstock.

8. The process of claim 7 , further comprising separately feeding the first and second fractions to the hydropyrolysis reactor vessel at separate locations.

9. The process of claim 8 , wherein the first fraction is fed to the hydropyrolysis reactor vessel through a cooled screw assembly, and wherein the second fraction is fed to the hydropyrolysis reactor vessel through a heated extruder.

10. The process of claim 1 , wherein the higher value liquid product comprises gasoline or diesel fuel boiling-range hydrocarbons.

11. A process for producing a higher value liquid product from an initial municipal solid waste (MSW) feedstock, comprising hydropyrolyzing a pretreated MSW feedstock in a hydropyrolysis reactor vessel containing hydrogen and a deoxygenating catalyst, producing a hydropyrolysis reactor output comprising at least one non-condensable gas, a partially deoxygenated hydropyrolysis product, and char particles,
wherein the pretreated MSW feedstock is obtained by removing at least a portion of plastic in the initial MSW feedstock to provide the pretreated MSW feedstock having a reduced plastic content relative to the initial MSW feedstock,
wherein the pretreated MSW feedstock comprises heteroatom-containing compounds including chloride-containing compounds, sulfur-containing compounds, and nitrogen-containing compounds, and
wherein the hydropyrolysis reactor output further comprises one or more contaminant gases generated from the hydrogenation of the heteroatom-containing compounds in the pretreated MSW feedstock, the one or more contaminant gases selected from the group consisting of HCl, H2S, and NH3.

12. The process of claim 11 , wherein the pretreated MSW feedstock comprises one or more of (i) from about 5% to about 25% by weight polyethylene terephthalate, (ii) from about 5% to about 30% by weight high density polyethylene (iii) from about 1% to about 10% by weight polyvinyl chloride, (iv) from about 10% to about 35% by weight low density polyethylene, (v) from about 12% to about 40% by weight polypropylene, or (vi) from about 3% to about 15% by weight polystyrene.

13. The process of claim 11 , further comprising:
removing substantially all of the char particles from the hydropyrolysis reactor output to provide a purified hydropyrolysis reactor vapor stream having a reduced char content;
hydroconverting the purified hydropyrolysis reactor vapor stream in a hydroconversion reactor vessel in the presence of a hydroconversion catalyst, producing a hydroconversion reactor output; and
recovering a substantially fully deoxygenated hydrocarbon liquid and a gaseous mixture from the hydroconversion reactor output,

wherein the hydroconversion reactor output and the gaseous mixture include the one or more contaminant gases, and further wherein the process comprises:
removing at least a portion of the one or more contaminant gases from the hydroconversion reactor output or the gaseous mixture.

14. The process of claim 13 , wherein the one or more contaminant gases includes HCl and wherein the step of removing at least a portion of the one or more contaminant gases comprises contacting at least a portion of the hydroconversion reactor output or the gaseous mixture with a solid sorbent that adsorbs HCl.

15. The process of claim 11 , wherein the hydropyrolyzing step is operated with continuous, intermittent, or localized high agitation conditions that reduce the formation of agglomerates of particles of the deoxygenating catalyst.

16. The process of claim 15 , wherein the high agitation conditions include the continuous, intermittent, or localized use of a gas velocity that, in combination with the average particle size and particle size distribution of particles of the deoxygenating catalyst and agglomerates thereof in the hydropyrolysis reactor vessel, breaks formed agglomerates of particles of the deoxygenating catalyst.

17. The process of claim 16 , wherein the high agitation conditions include intermittent and localized use of a gas velocity that exceeds the overall superficial velocity of fluidizing gas in the hydropyrolysis reactor vessel.

18. The process of claim

Assignees

• Gas Technology Inst

Inventors

• Felix Larry G
• Linck Martin B
• Marker Terry L
• Roberts Michael J

Classifications

• C10G3/42

  Catalytic treatment · CPC title

• C10G1/06

  by destructive hydrogenation · CPC title

• C10G3/52

  Hydrogen in a special composition or from a special source · CPC title

• C01B2203/062

  Hydrocarbon production, e.g. Fischer-Tropsch process · CPC title

• Y02P30/20

  using bio-feedstock · CPC title