Looking for breakthrough ideas for innovation challenges? Try Patsnap Eureka!

Process for upgrading heavy hydrocarbon oils

a technology for upgrading hydrocarbons and hydrocarbon oils, which is applied in the direction of hydrocarbon oil refining, petroleum industry, liquid hydrocarbon mixture production, etc., can solve the problems of difficult to bring remote, heavy oil resources closer, and the infrastructure required for the handling, recovery and recycling of diluent could be expensiv

Inactive Publication Date: 2008-05-01
CHEVROU USA INC
View PDF26 Cites 79 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

"The present invention is about a way to upgrade heavy hydrocarbons by mixing them with heated water to form a mixture. This mixture is then reacted under supercritical water conditions without adding any extra hydrogen. The resulting product is a single-phase reaction product that can be separated into gas, effluent water, and upgraded hydrocarbon phases. The technical effect of this invention is the ability to upgrade heavy hydrocarbons to higher quality products without the need for additional hydrogen."

Problems solved by technology

Oil produced from a significant number of oil reserves around the world is simply too heavy to flow under ambient conditions.
This makes it challenging to bring remote, heavy oil resources closer to the markets.
1. The infrastructure required for the handling, recovery, and recycle of diluent could be expensive, especially over long distances. Diluent availability is another potential issue.
2. Hydrogen-addition processes such as hydrotreating or hydrocracking require significant investments in capital and infrastructure.
3. Hydrogen-addition processes also have high operating costs, since hydrogen production costs are highly sensitive to natural gas prices. Some remote heavy oil reserves may not even have access to sufficient quantities of low-cost natural gas to support a hydrogen plant. These hydrogen-addition processes also generally require expensive catalysts and resource intensive catalyst handling techniques, including catalyst regeneration.
4. In some cases, the refineries and / or upgrading facilities that are located closest to the production site may have neither the capacity nor the facilities to accept the heavy oil.
5. Coking is often used at refineries or upgrading facilities. Significant amounts of by-product solid coke are rejected during the coking process, leading to lower liquid hydrocarbon yield. In addition, the liquid products from a coking plant often need further hydrotreating. Further, the volume of the product from the coking process is significantly less than the volume of the feed crude oil.
It is well understood that solids in the system will pose significant challenges for reactor and process design.
Direct heating of oil feed may lead to over heating which in turn leads to more solid residue formation, lower desired product yield and lower product quality.

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • Process for upgrading heavy hydrocarbon oils
  • Process for upgrading heavy hydrocarbon oils
  • Process for upgrading heavy hydrocarbon oils

Examples

Experimental program
Comparison scheme
Effect test

example 1

Showing Typical Laboratory Process

[0042]FIG. 1 shows a process flow diagram for a laboratory unit for practicing some embodiments of the invention. Oil and supercritical water are contacted in a mixer prior to entering the reactor. The reactor is equipped with an inner tube for collecting the products (syncrude, excess water, and gas), and a bottom section where any metals or solids comprising a “dreg stream” of indeterminate properties or composition may accumulate. The shell-side of the reactor is kept isothermal during the reaction with a clamshell furnace and temperature controller. Preferred reactor residence times are 20-40 minutes, with preferred oil / water volume ratios on the order of 1:3. Preferred temperatures are around 374°-400° C. with the pressure at 3,200-4,000 psig. The reactor product stream leaves as a single phase, and is cooled and separated into gas, syncrude, and effluent water. The effluent water is recycled back to the reactor. Sulfur from the original feedst...

example 2

Properties of the Product Syncrude

[0044]A Hamaca crude oil was diluted with a diluent hydrocarbon at a ratio of 5:1 (20 vol % of diluent). The diluted Hamaca crude oil properties were measured before reacting it with the supercritical water process as referred to in Example 1 and FIG. 2. The properties of the crude were as follows: 12.8 API gravity at 60 / 60; 1329 CST viscosity @40° C.; 7.66 wt % C / H ratio; 13.04 wt % MCRT; 3.54 wt % sulfur; 0.56 wt % nitrogen; 3.05 mg KOH / gm acid number; 1.41 wt % water, 371 ppm Vanadium; and 86 ppm Nickel. The diluted Hamaca crude oil after the super critical water treatment was converted into a syncrude with the following properties: 24.1 API gravity at 60 / 60; 5.75 CST viscosity @40° C.; 7.40 wt % C / H ratio; 2.25 wt % MCRT; 2.83 wt % sulfur; 0.28 wt % nitrogen; 1.54 mg KOH / gm acid number; 0.96 wt % water; 24 ppm Vanadium; and 3 ppm Nickel Substantial reductions in metals and residues were observed, with simultaneous increase in the API gravity and...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

PUM

PropertyMeasurementUnit
temperatureaaaaaaaaaa
temperatureaaaaaaaaaa
temperatureaaaaaaaaaa
Login to View More

Abstract

A process using supercritical water to upgrade a heavy hydrocarbon feedstock into an upgraded hydrocarbon product or syncrude with highly desirable properties (low sulfur content, low metals content, lower density (higher API), lower viscosity lower, residuum content, etc.) is disclosed. The process does not require external supply of hydrogen nor does it use externally supplied catalysts. Improved methods of mixing the reactants are also disclosed.

Description

FIELD OF THE INVENTION[0001]The present invention relates to upgrading of heavy hydrocarbons such as whole heavy oil, bitumen, and the like using supercritical water.BACKGROUND OF THE INVENTION[0002]Oil produced from a significant number of oil reserves around the world is simply too heavy to flow under ambient conditions. This makes it challenging to bring remote, heavy oil resources closer to the markets. One typical example is the Hamaca field in Venezuela. In order to render such heavy oils flowable, one of the most common methods known in the art is to reduce the viscosity and density by mixing the heavy oil with a sufficient diluent. The diluent may be naphtha, or any other stream with a significantly higher API gravity (i.e., much lower density) than the heavy oil.[0003]For a case such as Hamaca, diluted crude oil is sent from the production wellhead via pipeline to an upgrading facility. Two key operations occur at the upgrading facility: (1) the diluent stream is recovered ...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

Application Information

Patent Timeline
no application Login to View More
Patent Type & Authority Applications(United States)
IPC IPC(8): C10G45/00C10G31/00
CPCC10G31/00C10G1/047
Inventor HE, ZUNQINGLI, LINLI, LIXIONGCHINN, DANIEL
Owner CHEVROU USA INC
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Patsnap Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Patsnap Eureka Blog
Learn More
PatSnap group products