Processes for producing low acid biomass-derived pyrolysis oils

a biomass-derived pyrolysis oil, low acid technology, applied in the direction of biofeedstock, liquid carbonaceous fuel, petroleum industry, etc., can solve the problems of limiting the utilization of biomass-derived pyrolysis oil as a biofuel, low energy density, corrosive, etc., and achieves low energy density and poor thermal stability of biomass-derived pyrolysis oil. , the effect of reducing the number of pyrolysis oil oxidation

Inactive Publication Date: 2012-01-26
UOP LLC
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

[0006]In an embodiment, by way of example only, a process for producing a low acid biomass-derived pyrolysis oil includes pre-treating a biomass-derived pyrolysis oil to form a treated acid-containing biomass-derived pyrolysis oil and esterifying the treated acid-containing biomass-derived pyrolysis oil in the presence of supercritical alcohol and a catalyst composition to form the low-acid biomass-derived pyrolysis oil, the catalyst composition comprising a material selected from the group consisting of an unsupported solid acid catalyst, an unsupported solid base catalyst, and a catalytic metal dispersed on a metal oxide support. The unsupported solid acid catalyst comprises a material selected from the group consisting of a molecular sieve and a Group V metal oxide. The molecular sieve comprises a material selected from the group consisting of zeolite and MCM 41. The unsupported solid base catalyst comprises a material selected from the group consisting of an alkaline earth metal exchanged molecular sieve, calcium oxide (CaO), magnesium oxide (MgO), and silicon oxide (SiO2). The catalytic metal comprises a metal selected from the group consisting of noble metals, non-noble metals, and combinations thereof the metal oxide support comprises a metal oxide selected from the group consisting of a Group IV metal oxide, a Group V metal oxide, a Group IIIA metal oxide, and combinations thereof.
[0007]In another embodiment, by way of example only, a process for producing a low acid biomass-derived pyrolysis oil includes pre-treating a biomass-derived pyrolysis oil to form a treated acid-containing biomass-derived pyrolysis oil, diluting the treated acid-containing biomass-derived pyrolysis oil with supercritical ethanol to form a solution including at least about 30% ethanol, by weight, and esterifying the treated acid-containing biomass-derived pyrolysis oil included in the solution in the presence of a catalyst composition and in the absence of gas in an upflow reactor to form the low-acid biomass-derived pyrolysis oil, wherein the catalyst composition comprises a noble metal support on a sulfated metal oxide.

Problems solved by technology

Although biomass-derived pyrolysis oil has great potential to replace up to 60% of transportation fuels and to reduce the dependency on conventional petroleum and its environmental impact, unprocessed biomass-derived pyrolysis oil is a complex, highly oxygenated organic liquid having properties that currently limit its utilization as a biofuel.
Specifically, unprocessed biomass-derived pyrolysis oil is generally thermally unstable and acidic (as measured by the total acid number (TAN)), making it corrosive, low in energy density, and susceptible to increased viscosity over time.
The low energy density and poor thermal stability of the biomass-derived pyrolysis oil is attributable in large part to oxygenated hydrocarbons in the oil, which undergo secondary reactions during storage.

Method used

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  • Processes for producing low acid biomass-derived pyrolysis oils
  • Processes for producing low acid biomass-derived pyrolysis oils
  • Processes for producing low acid biomass-derived pyrolysis oils

Examples

Experimental program
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Effect test

example 1

[0053]A pre-blended feed was prepared for use in several experiments, as will be discussed in further detail below. The pre-blended feed included about 50 weight percent (wt %) ethanol and about 50 wt % low water biomass-derived pyrolysis oil. The blended feed had a total acid number (TAN) of about 110.5, where 40.9 of the TAN was attributed to carboxylic acid and about 69.6 of the TAN was attributed to phenolic.

example 2

[0054]One hundred (100) grams of the pre-blended feed was added to an autoclave including 5.0 grams of 0.5% platinum on γ alumina. A head pressure of nitrogen about 2.75 MPa (400 psig) was added to the autoclave. The autoclave was then heated to a temperature in a range of about 255° C. The temperature was maintained for about 1.8 hours, and a maximum pressure of about 12.41 MPa (1800 psig) was achieved to provide supercritical conditions for the ethanol and to esterify the oil in the pre-blended feed. After the reaction, the pressure at room temperature was 4.13 MPa (600 psig). No solids were found in the autoclave, and about 10 grams of the liquid was converted to gas. The TAN of the esterified feed was about 65.62, where 25.24 of the TAN was attributed to carboxylic acid and 40.38 of the TAN was attributed to phenolic.

example 3

[0055]Ninety (90) grams of the pre-blended feed was added to an autoclave including 4.5 grams of about 70% to about 85% silicon oxide and about 15% to about 30% aluminum oxide. A head pressure of nitrogen in a range of about 2.75 MPa (400 psig) was added to the autoclave. The autoclave was then heated to a temperature in a range of about 255° C. The temperature was maintained for about 1.8 hours, and a maximum pressure of about 1800 psig was achieved to provide supercritical conditions for the ethanol and to esterify the oil in the pre-blended feed. After the reaction, the pressure at room temperature was 3.79 MPa (550 psig). No solids were found in the autoclave, and about 6% of the liquid was converted to gas. The TAN of the esterified feed was about 64.5, where 22.43 of the TAN was attributed to carboxylic acid and 42.06 of the TAN was attributed to phenolic.

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Abstract

Processes for producing a low acid biomass-derived pyrolysis oil are provided that include pre-treating a biomass-derived pyrolysis oil to form a treated acid-containing biomass-derived pyrolysis oil. The processes also include esterifying the treated acid-containing biomass-derived pyrolysis oil in the presence of supercritical alcohol and a catalyst composition to form the low-acid biomass-derived pyrolysis oil, the catalyst composition comprising a material selected from the group consisting of an unsupported solid acid catalyst, an unsupported solid base catalyst, and a catalytic metal dispersed on a metal oxide support.

Description

FIELD OF THE INVENTION[0001]The present invention generally relates to biofuels and processes for producing biofuels, and more particularly relates to low acid biomass-derived pyrolysis oils and processes for producing the same.DESCRIPTION OF RELATED ART[0002]Biomass-derived pyrolysis oil can be burned directly as fuel for certain boiler and furnace applications, and can also serve as a potential feedstock in the production of biofuels in petroleum refineries or in stand-alone process units. To form biomass-derived pyrolysis oil, solid carbonaceous biomass feedstock, i.e., “biomass”, such as wood waste, agricultural waste, etc., is initially rapidly heated to pyrolysis temperatures of about 300° C. to about 900° C. in the absence of air using a pyrolysis reactor. Under these conditions, solid products, liquid products, and gaseous pyrolysis products are produced. A condensable portion (vapors) of the gaseous pyrolysis products is condensed into biomass-derived pyrolysis oil.[0003]Al...

Claims

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Application Information

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Patent Type & Authority Applications(United States)
IPC IPC(8): C10L1/19
CPCC10L1/02Y02P30/20
Inventor TRAYNOR, THOMASBRANDVOLD, TIMOTHY A.
Owner UOP LLC
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