High-yield production of fuels and petro- and oleo-chemical precursors from vegetable oils and other liquid feedstocks in a continuous-flow pyrolysis reactor with or without catalysts

Patent metadata

Field	Value
Publication number	US-10894920-B2
Application number	US-201916248240-A
Country	US
Kind code	B2
Filing date	Jan 15, 2019
Priority date	Aug 22, 2016
Publication date	Jan 19, 2021
Grant date	Jan 19, 2021

Abstract

Systems, methods, and materials for pyrolyzing vegetable oil feedstocks to obtain high yields of various products are described.

First claim

What is claimed is:

1. A pyrolysis system comprising:
a feedstock source;
an atomizer configured to receive feedstock from the feedstock source and deliver atomized droplets of the feedstock to a reactor in fluid communication with the atomizer,
wherein the reactor consists of a tube, optionally with one or more catalysts, defining an enclosure having a first end and a second end, and
wherein the atomizer is attached to the first end of the enclosure to introduce feedstock into the reactor and the reactor is configured to deliver pyrolysis products from the second end of the enclosure;
a first separation apparatus in fluid communication with the reactor such that pyrolysis products formed in the reactor are delivered from the second end of the enclosure to the first separation apparatus and,
a second separation apparatus in fluid communication with the first separation apparatus.

2. The pyrolysis system of claim 1 , wherein the atomizer is an ultrasonic atomizer.

3. The pyrolysis system of claim 1 , further including a pump configured to deliver feedstock from the feedstock source to the atomizer.

4. The pyrolysis system of claim 1 , wherein the feedstock source is configured to receive a quantity of feedstock that comprises vegetable oil, biooil, or biocrude.

5. The pyrolysis system of claim 4 , wherein the vegetable oil comprises soy bean oil, canola oil, corn oil, palm oil, palm kernel oil, mustard oil, grape seed oil, hazelnut oil, linseed oil, rice bran oil, sesame oil, safflower oil, carapa oil, guava oil, tall oil, camelina oil, babassu oil, pennycress oil, coconut oil, or mixtures thereof.

6. The pyrolysis system of claim 1 , wherein the pyrolysis system includes a temperature controller configured to regulate temperatures of the reactor ranging from about 400° C. to about 600° C.

7. The pyrolysis system of claim 1 , further including one or more added reactant sources configured to add one or more additional reactants to the reactor to allow vapor phase reactions with or without the presence of catalyst in the reactor.

8. The pyrolysis system of claim 7 , wherein the one or more additional reactants comprise ammonia, methanol, or hydrogen gas.

9. A pyrolysis system comprising:
a feedstock source;
an atomizer configured to receive feedstock from the feedstock source and deliver atomized droplets of the feedstock to a reactor in fluid communication with the atomizer,
wherein the reactor consists of a tube, optionally with one or more catalysts, defining an enclosure having a first end and a second end, and
wherein the atomizer is attached to the first end of the enclosure to introduce feedstock into the reactor and the reactor is configured to deliver pyrolysis products from the second end of the enclosure;
one or more added reactant sources configured to add one or more additional reactants to the reactor to allow vapor phase reactions with or without the presence of catalyst in the reactor;
a first separation apparatus in fluid communication with the reactor such that pyrolysis products formed in the reactor are delivered from the second end of the enclosure to the first separation apparatus; and,
wherein the reactor includes one or more catalysts selected from zeolites, metal oxides, solid acid catalysts, or solid base catalysts.

10. The pyrolysis system of claim 1 , further including a furnace wherein the reactor and/or feedstock is pre-heated before the atomized oil droplets are introduced into the reactor.

11. The pyrolysis system of claim 1 , wherein the reactor tube is stainless steel.

12. The pyrolysis system of claim 1 , wherein the reactor is disposed within a furnace.

13. The pyrolysis system of claim 1 , wherein the reactor is configured to be capable of being heated to, and maintaining, a temperature of up to 600° C. in the absence of oxygen.

Assignees

• Univ Toledo

Inventors

• Shirazi Yaser
• Viamajala Sridhar
• Varanasi Sasidhar

Classifications

• C10G2300/202

  Heteroatoms content, i.e. S, N, O, P · CPC title

• C11C1/00

  Preparation of fatty acids from fats, fatty oils, or waxes; Refining the fatty acids (recovery of fatty acids from waste materials C11B13/00) · CPC title

• Y02P30/20

  using bio-feedstock · CPC title

• C10G3/40 Primary

  Thermal non-catalytic treatment · CPC title

• C10G3/42

  Catalytic treatment · CPC title