# US 4,395,903 A · Apparatus and method for determining the vapor pressure of heavy hydrocarbon mixtures

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- Number: US 4,395,903 A
- Document ID: US4395903A
- Status: Granted
- Kind: A
- Application number: 06/292,279
- Filed: 1981-08-12
- Granted: 1983-08-02
- Earliest claimed: 1981-08-12
- Assignees: Chevron Research Company
- Inventors: T. H. Gouw
- Web page: https://patentgrep.com/patent/US4395903A

## CPC

- G01N 25/14: by using distillation, extraction, sublimation, condensation, freezing, or crystallisation (G01N25/02 takes precedence)
- G01N 33/2823: {Raw oil, drilling fluid or polyphasic mixtures}
- G01N 7/16: by heating the material
- G01N: INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES (measuring or testing apparatus or processes other than immunoassay, involving enzymes or microorganisms C12M, C12Q)

## Abstract

A vapor pressure method and apparatus for accurately determining the vapor pressure of heavy crude oil and residual fractions is disclosed. A test sample of the crude or residuum is held in a constant temperature vessel from which vapors are continuously withdrawn and recycled into the crude or residuum until equilibrium is established. Once equilibrium is established a specimen of the vapors is extracted from the recycle line and analyzed by a gas chromatograph. Vapor pressure is calculated from the chromatographic analysis by known procedures.

## Claims

### Claim 1

Method for determining the vapor pressure of a heavy liquid hydrocarbon mixture comprising:
(a) maintaining the liquid hydrocarbon mixture at a substantially constant temperature in a closed vessel with a vapor space above the liquid;
(b) continuously withdrawing vapors from said vapor space;
(c) recycling the withdrawn vapors into the liquid hydrocarbon mixture below the liquid-vapor interface for a time sufficient to establish equilibrium between the liquid and vapor in the vessel;
(d) thereafter analyzing the composition of said withdrawn vapors by gas chromatography;
(e) calculating the partial pressures of the components of said vapors from the chromatographic analysis; and
(f) calculating the vapor pressure of the mixture by summing the partial pressures of the components.

### Claim 2 (depends on 1)

The method of claim 1 wherein a sample of the withdrawn recycling vapors is taken after step (c) and said sample is used for analysis of step (d).

### Claim 3 (depends on 1, 2)

The method of claim 1 or 2 wherein the vapors are heated after they are withdrawn from the vessel to prevent them from condensing during recycle and are cooled to said temperature substantially immediately before being introduced into the liquid hydrocarbon mixture

### Claim 4 (depends on 1)

The method of claim 1 wherein said time is at least about 10 minutes.

### Claim 5

Apparatus for determining the vapor pressure of a heavy liquid hydrocarbon mixture comprising in combination:
(a) a closed vessel in which the liquid hydrocarbon mixture is maintained with a vapor space above the liquid mixture;
(b) means for maintaining the temperature within the vessel substantially constant;
(c) a conduit for continuously withdrawing vapors from the vessel and recycling them back to the vessel at a location below the liquid-vapor interface, one end of the conduit opening into the vapor space and the other end opening into the liquid mixture;
(d) a pump connected into the conduit between said ends for providing the driving force for withdrawing the vapors from the vessel and recycling them back to the vessel;
(e) a vapor sampling means connected to the conduit between said ends for withdrawing a sample of the vapors from the lumen of the conduit once equilibrium has been established between the liquid and vapors within the vessel;
(f) sample analyzing means connected to the vapor sampling means for quantitatively analyzing the composition of the sample; and
(g) computer means connected to the sample analyzing means for calculating the partial pressures of the components of the composition from the analysis of the composition and summing the partial pressures to obtain the vapor pressure of the liquid hydrocarbon mixture.

### Claim 6 (depends on 5)

The apparatus of claim 5 wherein said means for maintaining the temperature within the vessel substantially constant is a substantially constant temperature liquid bath in which the vessel is immersed.

### Claim 7 (depends on 5)

The apparatus of claim 5 wherein the sample analyzing means is a gas chromatograph, capable of temperature programmed operation.

### Claim 8 (depends on 5)

The apparatus of claim 5 including heating means connected to the segment of said conduit proximate said one end for heating the withdrawn vapors to prevent them from condensing during recycle and wherein the segment of said conduit proximate said other end communicates with said temperature maintaining means whereby the vapors are cooled to substantially said temperature before they are introduced into the liquid hydrocarbon mixture within the vessel.