High Nitrogen Renewable Feedstock Deoxygenation

Resolve Bottlenecks,
Find Innovative Solutions
Generate Solutions

Solution Overview

Problem

Renewable biological feedstocks high in nitrogen are challenging to process due to competing nitrogen conversion reactions during deoxygenation, making them more expensive and less commercially viable for producing diesel and jet fuel.

Innovation Solution

Increasing the hydrogen recycle gas rate in the deoxygenation zone, typically between 6000 to 9000 SCF/BBL, to effectively convert high nitrogen feedstocks into linear hydrocarbons, with subsequent isomerization to improve cold flow properties of the effluent.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Reliability

If conventional deoxygenation processes are used on high nitrogen feedstocks, then nitrogen conversion to ammonia competes with deoxygenation reaction, but processing cost increases and commercial value decreases

Engineering Contradiction:
Improvedeoxygenation efficiencyVSAvoidprocessing cost
Core Design Contradiction:
ReliabilityVSEase of manufacture

Solution Approach 1:

The patent changes key process parameters including increasing hydrogen partial pressure, optimizing temperature ranges (300-450°C), adjusting space velocity, and modifying catalyst composition (adding nitrogen-tolerant metals like Ru, Rh, or Ir to conventional catalysts). These parameter changes enable effective deoxygenation of high-nitrogen feedstocks without the competing ammonia formation that plagues conventional processes, thereby maintaining processing efficiency while reducing costs by enabling use of cheaper high-nitrogen feedstocks

Inventive Principle:
Principle #35Parameter changes

2Quantity of substance

If high nitrogen feedstocks are processed using conventional methods, then nitrogen conversion competes with deoxygenation, but commercial viability is reduced

Engineering Contradiction:
Improvefeedstock availabilityVSAvoidcommercial value
Core Design Contradiction:
Quantity of substanceVSAdaptability or versatility

Solution Approach 1:

The patent converts the harmful effect of nitrogen (which normally competes with deoxygenation and reduces efficiency) into a manageable parameter by using nitrogen-tolerant catalysts and optimized conditions. This allows the process to effectively handle high-nitrogen feedstocks like packer tallows, transforming what was previously a disadvantage into an opportunity to utilize abundant, cheaper feedstock sources that were previously unusable, thereby improving both feedstock availability and commercial value

Inventive Principle:
Principle #22Blessing in disguise (Convert harm into benefit)

Applied Scientific Principles

This section explains which scientific principles are used to turn an abstract innovation direction into a practical engineering solution.

Function Achieved in This Case

This approach allows for efficient conversion of high nitrogen feedstocks into hydrocarbons with reduced nitrogen content, improving processing efficiency and reducing costs, while enhancing fuel properties.

Implementation Method 1

deoxygenating a renewable feedstock in the presence of hydrogen in a deoxygenation zone comprising a catalyst

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 2

Organic nitrogen conversion to ammonia is a competing reaction to the necessary deoxygenation reaction

Methodology Applied
Scientific EffectChemical reaction: Chemical Bonding

Implementation Method 3

isomerizing the deoxygenated effluent in an isomerization zone comprising a catalyst and being operated under conditions to improve at least one cold flow property

Methodology Applied
Scientific EffectIsomerization: Catalysis

Data Source

PatentUS9637699B2Methods for processing nitrogen rich renewable feedstocks
Publication Date: 2017.05.02 UOP LLC
  • US9637699B2 patent drawing
  • US9637699B2 patent drawing

AI summary

Processes for producing a fuel from a renewable feedstock which may have more than 60 ppm nitrogen. The renewable feedstock is passed to a deoxygenation zone. A hydrogen stream, preferably formed from a recycled gas, is introduced into the deoxygenation zone at a relatively high rate. The hydrogen introduction may be between 3 to 5 times the rate of hydrogen consumption in the deoxygenation zone. The hydrogen introduction may also be between 6000 to 9000 SCF/BBL. A deoxygenated effluent, comprising less than 1 wppm nitrogen, may be isomerized and separated into one or more product hydrocarbon streams such as a diesel fuel or aviation fuel.