# US 11,029,296 B2 · System and method for monitoring a reforming catalyst

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- Number: US 11,029,296 B2
- Document ID: US11029296B2
- Status: Granted
- Kind: B2
- Application number: 16/549,090
- Filed: 2019-08-23
- Published: 2019-12-12
- Granted: 2021-06-08
- Earliest claimed: 2017-11-07
- Assignees: Chevron Phillips Chemical Company LP
- Applicants: Chevron Phillips Chemical Company LP
- Inventors: Israel Garcia; Scott G. Morrison
- Web page: https://patentgrep.com/patent/US11029296B2

## CPC

- G01N 33/0047: {Organic compounds}
- C10G 69/00: Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process (C10G67/00 takes precedence)
- G01N 30/00: Investigating or analysing materials by separation into components using adsorption, absorption or similar phenomena or using ion-exchange, e.g. chromatography {or field flow fractionation} (G01N3/00, G01N5/00, G01N7/00, G01N9/00, G01N11/00, G01N13/00, G01N15/00, G01N17/00, G01N19/00, G01N21/00, G01N22/00, G01N23/00, G01N24/00, G01N25/00, G01N27/00, G01N29/00 take precedence)
- G01N 30/88: Integrated analysis systems specially adapted therefor, not covered by a single one of the groups G01N30/04 - G01N30/86
- G01N 33/005: {H2}
- G01N 33/0063: {using a threshold to release an alarm or displaying means}
- G01N 33/0067: {by measuring the rate of variation of the concentration}
- G06T 11/26: Drawing of charts or graphs
- C10G 2300/4031: Start up or shut down operations
- C10G 2400/30: Aromatics
- G01N 33/0068: {using a computer specifically programmed}
- G01N 2030/0095: {Separation specially adapted for use outside laboratory, e.g. field sampling, portable equipments}
- 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)
- C10G: CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION (cracking to hydrogen or synthesis gas C01B; cracking or pyrolysis of hydrocarbon gases to individual hydrocarbons or mixtures thereof of definite or specified constitution C07C; cracking to cokes C10B); RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- G06T: IMAGE DATA PROCESSING OR GENERATION, IN GENERAL

## Abstract

A method of monitoring catalytic performance of a catalyst used in a reforming process, comprising a) collecting gaseous component data from the reforming process; b) calculating a gaseous component ratio from the gaseous component data; and c) utilizing the gaseous component ratio to estimate an amount of catalytic activity remaining in the catalyst used in the reforming process, a number of days on stream remaining for the catalyst used in the reforming process, or both.

## Claims

### Claim 1

A method of modeling catalytic performance of a catalyst used in a reforming process, comprising:
a. constructing a two-coordinate graph containing a vertical axis for gaseous component ratio data and a horizontal axis for catalyst activity factor data;
b. obtaining a set of gaseous component ratio data and a set of catalyst activity factor data for the reforming process;
c. representing the set of gaseous component ratio data and the set of catalyst activity factor data upon the two-coordinate graph;
d. constructing a best-fit curve upon the two-coordinate graph, wherein the best-fit curve represents a graphical relationship of the set of gaseous component ratio data and the set of catalyst activity factor data;
e. assigning a catalyst activity end-of-run value and representing the catalyst activity end-of-run value as a vertical line upon the two-coordinate graph; and
f. determining a point of intersection of the best-fit curve with the vertical line and assigning a vertical axis value of the point of intersection as a gaseous component mole ratio end-of-run (M-EOR) value.

### Claim 2 (depends on 1)

A model prepared by the method of claim 1, wherein the model is a mathematical function representing the best-fit curve.

### Claim 3 (depends on 1)

The method of claim 1 wherein the gaseous component ratio data comprises a ratio of moles of hydrogen to moles of methane and wherein the gaseous component ratio data is obtained via gas chromatography.

### Claim 4 (depends on 3)

The method of claim 3 wherein the best-fit curve is constructed from gaseous component ratio data and catalyst activity factor data obtained from an ongoing reforming process, an equation, or historical reforming process data.

### Claim 5 (depends on 4)

The method of claim 4 wherein the graphical relationship of the best-fit curve is about linear and wherein the graphical relationship remains about linear during the reforming process.

### Claim 6

A method of modeling catalytic performance of a catalyst used in a reforming process, comprising:
a. constructing a two-coordinate graph containing a vertical axis for gaseous component ratio data and a horizontal axis for days-on-stream (DOS) data;
b. obtaining a set of gaseous component ratio data and a set of DOS data for the reforming process;
c. representing the set of gaseous component ratio data and the set of DOS data upon the two-coordinate graph; and
d. constructing a best-fit curve upon the two-coordinate graph, wherein the best-fit curve represents a graphical relationship of the set of gaseous component ratio data and the set of DOS data;
e. assigning a gaseous component ratio end-of-run value and representing the gaseous component ratio end-of-run value as a horizontal line upon the two-coordinate graph; and
f. determining a point of intersection of the best-fit curve with the horizontal line and assigning a horizontal axis value of the point of intersection as a DOS end-of-run (D-EOR) value.

### Claim 7 (depends on 6)

A model prepared by the method of claim 6, wherein the model is a mathematical function representing the best-fit curve.

### Claim 8 (depends on 6)

The method of claim 6 wherein the gaseous component ratio data comprises a ratio of moles of hydrogen to moles of methane wherein the gaseous component ratio end-of-run value comprises a mole ratio end-of-run (M-EOR) value and wherein the gaseous component ratio data is obtained via gas chromatography.

### Claim 9 (depends on 8)

The method of claim 8 wherein the best-fit curve is constructed from gaseous component ratio data and DOS data obtained from an ongoing reforming process, an equation, or historical reforming process data.

### Claim 10 (depends on 9)

The method of claim 9 wherein the graphical relationship of the best-fit curve is about linear and wherein the graphical relationship remains about linear during the reforming process.
