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Biorenewable naphtha

a biorenewable naphtha and biomass technology, applied in the direction of hydrocarbon preparation catalysts, hydrocarbon oil treatment products, fuels, etc., can solve the problems of reducing the efficiency of this process as a source of biorenewable naphtha, gasifiers with low reliability record, and f-t conversion capital costs

Inactive Publication Date: 2009-12-10
REG SYNTHETIC FUELS LLC
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

[0012]The present invention relates to a method for producing from a biorenewable feed stock a hydrocarbon naphtha composition useful for producing olefins, BTX aromatics, hydrogen, and also for direct use as gasoline blend stock and solvent. The biorenewable feed stock includes sources of glycerides (i.e. monoglycerides, diglycerides,

Problems solved by technology

One of the challenges facing transition to a green chemical industry is that the existing production facilities and infrastructure are designed around hydrocarbon feed stocks.
Although the process produces the desired hydrocarbon naphtha from a bio-renewable source, gasifiers suffer from a low reliability record.
Additionally, the capital costs associated with gasification and F-T conversion are known to be very high.
Furthermore, the need to recycle part of the naphtha to the gasifier further reduces the efficiency of this process as a source of bio-renewable naphtha.
Although these products are reported to have high octane rating and hence good gasoline blend stocks, they lack the desired properties as a chemical feed stock.

Method used

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Examples

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example 1

Hydrotreating of a Biorenewable Feed Stock

[0043]The present example demonstrates how naphtha was made from a renewable feedstock. A 100 cc isothermal tubular reactor was filled with 80 cc of a commercial NiMo catalyst and +70-100 mesh glass beads. The catalyst was sulfided with dimethyl disulfide. The sulfiding procedure included step-wise temperature increase to 650° F. After sulfiding, the reactor was cooled to 400° F.

[0044]Next a triglyceride / fatty acid feed was introduced to the isothermal reactor. The reactor was slowly heated to 650° F. to achieve full conversion of the triglyceride / fatty acid feed to n-paraffins. The reactor temperature was further increased to 700° F. to maintain good catalyst activity at 80 cc / hr feed rate (1 LHSV).

[0045]The hydrotreater performance with beef tallow as the triglyceride / fatty acid feed is summarized in Table 1. The yield of total products on feed basis exceeds 100% in part due to addition of hydrogen and also due to measurement errors associ...

example 2

Hydrocracking of Bio-Derived Heavy Hydrocarbons

[0047]The mainly C15-C18 n-paraffin composition obtained from hydrotreating bio-renewable feed stocks was used as feed for a hydrocracking pilot plant. These long chain hydrocarbons were derived via hydrotreating a biorenewable feed in a procedure similar to Example 1. The bio-renewable feed was a blend of chicken fat (45%), brown grease (19%), yellow grease (18%), floatation grease (9%), and miscellaneous waste animal fats from industrial food processing operations (9%). The hydrocracking pilot plant was a prototype of the embodiment of the present invention represented by FIG. 2.

[0048]The hydrocracker reactor system was loaded with 4.8 liters of a commercial hydrocracking catalyst. The catalyst was platinum-palladium on amorphous alumina / silica

[0049]The reactor was pressurized to 1,000 psig. After catalyst preconditioning, the temperature was increased again to achieve the desired level of hydrocracking to produce the biorenewable nap...

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Abstract

The present invention generally relates to a method for producing a naphtha product from a renewable feedstock. The method includes hydrotreating the renewable feedstock to produce a hydrotreating unit heavy fraction that includes n-paraffins, and hydrocracking the hydrotreating unit heavy fraction to produce a hydrocracking unit product that includes the naphtha product. The method also includes separating the naphtha fraction and optionally recycling the hydrocracking unit heavy fraction through the hydrocracking unit. The present invention also relates to a biorenewable naphtha product suitable for use as feed stock for steam crackers and catalytic reforming units, and for use as fuel, or fuel blend stock.

Description

STATEMENT REGARDING FEDERALLY SPONSORED RESEARCH OR DEVELOPMENT[0001]Not applicable.CROSS-REFERENCE TO RELATED APPLICATIONS[0002]Not applicable.FIELD OF THE INVENTION[0003]The present invention generally relates to a method for producing hydrocarbons from biomass. Specifically, the present invention relates to converting naturally occurring triglycerides and fatty acids to a composition including naphtha boiling range hydrocarbons. The present invention also relates to the resultant biorenewable naphtha product, whereby the naphtha is used as chemical feed stock, fuel, fuel blend stock, or solvent.BACKGROUND OF THE INVENTION[0004]The term “green chemistry” has been used to describe synthesis of chemicals from biorenewable feed stocks. It is considered a sustainable alternative to petroleum-based chemistry, and may mitigate the effect of high oil prices. One of the challenges facing transition to a green chemical industry is that the existing production facilities and infrastructure ...

Claims

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Application Information

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IPC IPC(8): C10L1/18C07C1/00
CPCC10G3/50C07C2529/072C10L1/06C10G3/46C10G3/54C10G2300/1014C10G2300/1018C10G2300/301C10G2300/308C10G2400/18C10G2300/4081C07C1/2078C07C4/06C07C5/22C07C2523/84C10G2400/02Y02P30/20
Inventor ABHARI, RAMINTOMLINSON, H. LYNNROTH, GARY
Owner REG SYNTHETIC FUELS LLC
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