Oxygenate analysis and control by Raman spectroscopy

Claim 2

A process comprising: a) irradiating a sample of a liquid mixture consisting essentially of liquid hydrocarbons and comprising one or more oxygenated component to produce Raman scattered radiation emitted from the sample; b) collecting Raman scattered radiation emitted from the sample; c) dispersing or transforming the collected Raman scattered radiation from the sample into spectra with intensities corresponding to the concentration of components of the mixture; d) processing said spectra according to a regression model derived by multivariate analysis of Raman spectra, or a mathematical function of Raman spectra, of liquid mixtures containing known concentrations of one or more oxygenated hydrocarbons, to produce a control signal representative of the concentration of an oxygenated component in said mixture; e) controlling a process in response to said control signal.

Claim 3

A process according to claim 1 wherein said oxygenated hydrocarbon comprises methanol and wherein said collected Raman scattered radiation from the sample is measured in the range of frown about 2964-2814 and/or 1477-1014 nm.

Claim 4

A process according to claim 1 wherein said oxygenated hydrocarbon comprises 1-propanol and wherein said collected Raman scattered radiation from the sample is measured in the range of from about 2958-2858 and/or 1477-446 nm.

Claim 5

A process according to claim 1 whereto said oxygenated hydrocarbon comprises 2-propanol and whereto said collected Raman scattered radiation from the sample is measured in the range of from about 2995-2860 and/or 1473-800 nm.

Claim 6

A process according to claim 1 wherein said oxygenated hydrocarbon comprises 1-butanol and wherein said collected Raman scattered radiation from the sample is measured in the range of from about 2961-2859 and/or 1475-382 nm.

Claim 7

A process according to claim 1 whereto said oxygenated hydrocarbon comprises 2-butanol and wherein said collected Raman scattered radiation from the sample is measured in the range of from about 2990-2861 and/or 1477-481 nm.

Claim 8

A process according to claim 1 wherein said oxygenated hydrocarbon comprises isobutanol and wherein said collected Raman scattered radiation from the sample is measured in the range of from about 2995-2860 and/or 1473-800 nm.

Claim 9

A process according to claim 1 wherein said oxygenated hydrocarbon comprises tertiary butyl alcohol and wherein said collected Raman scattered radiation from the sample is measured in the range of from about 3000-2898 and/or 1470-320 nm.

Claim 10

A process according to 1 wherein said oxygenated hydrocarbon comprises tertiary amyl alcohol and wherein said collected Raman scattered radiation from the sample is measured in the range of from about 3000-2690 and/or 1470-320 nm.

Claim 11

A process according to 1 wherein said oxygenated hydrocarbon comprises tertiary amyl alcohol and wherein said collected Raman scattered radiation from the sample is measured in the range of from about 3000-2690 and/or 1470-320 nm.

Claim 12

A process according to claim 1 wherein said oxygenated hydrocarbon comprises methyl tertiary butyl ether (MTBE) and wherein said collected Raman scattered radiation from the sample is measured in the range of from about 3011-2791 and/or 892-466 nm.

Claim 13

A process according to claim 1 wherein said oxygenated hydrocarbon comprises ethyl tertiary butyl ether (ETBE) and wherein said collected Raman scattered radiation from the sample is measured in the range of from about 3011-2791 and/or 892-466 nm.

Claim 14

A process according to claim 1 wherein said oxygenated hydrocarbon comprises tertiary amyl methyl ether (TAME) and wherein said collected Raman scattered radiation from the sample is measured in the range of from about 3011-2791 and/or 892-466 nm.

Claim 15

A process according to claim 1 wherein said oxygenated hydrocarbon comprises diisopropyl ether (DIPE) and wherein said collected Raman scattered radiation from the sample is measured in the range of frown about 2995-2860 and/or 1473-800 nm.

Claim 16

A process comprising: a) irradiating a sample of a liquid mixture comprising as oxygenated component methanol, 1-propanol, 2-propanol, 1-butanol, 2-butanol, isobutanol, tertiary butanol, tertiary amyl alcohol, methyl tertiary butyl ether (MTBE), ethyl tertiary butyl ether (ETBE), tertiary amyl methyl ether (TAME), and/or diisopropyl ether (DIPE) to produce Raman scattered radiation emitted from the sample; b) collecting Raman scattered radiation emitted from the sample; c) dispersing or transforming the collected Raman scattered radiation from the sample into spectra with intensities corresponding to the concentration of said components; d) processing said spectra according to a regression model derived by multivariate analysis of Raman spectra, or derived from a mathematical function of Raman spectra, of liquid mixtures containing known concentrations of oxygenated hydrocarbons, to produce a control signal representative of the concentration of the oxygenated component in said mixture; e) controlling a process in response to said control signal.

Claim 17

A process comprising: a) irradiating a sample of a liquid mixture comprising as oxygenated component methanol, 1-propanol, 2-propanol, 1-butanol, 2-butanol, isobutanol, tertiary butanol, tertiary amyl alcohol, methyl tertiary butyl ether (MTBE), ethyl tertiary butyl ether (ETBE), tertiary amyl methyl ether (TAME), and/or diisopropyl ether (DIPE) to produce Raman scattered radiation emitted from the sample; b) collecting Raman scattered radiation emitted from the sample; c) dispersing or transforming the collected Raman scattered radiation from the sample into spectra with intensities corresponding to the concentration of said components; d) processing said spectra according to a regression model derived by multivariate analysis of Raman spectra, or derived from a mathematical function of Raman spectra, of liquid mixtures containing known concentrations of oxygenated hydrocarbons, to produce a control signal representative of the concentration of the oxygenated component in said mixture; e) controlling a process in response to said control signal.

Claim 18

The process of claim 14 wherein the liquid mixture is a hydrocarbon mixture.

Claim 19

The process of claim 14 wherein the sample is irradiated with near infrared radiation.

Claim 20

The process of claim 14 wherein the sample comprises methanol.

Claim 21

The process of claim 14 wherein the sample comprises 1-propanol.

Claim 22

The process of claim 14 wherein the sample comprises 2-propanol.

Claim 23

The process of claim 14 wherein the sample comprises 1-butanol.

Claim 24

The process of claim 14 wherein the sample comprises 2-butanol.

Claim 25

The process of claim 14 wherein the sample comprises isobutanol.

Claim 26

The process of claim 14 wherein the sample comprises tertiary butyl alcohol.

Claim 27

The process of claim 14 wherein the sample comprises tertiary amyl alcohol.

Claim 28

The process of claim 14 wherein said mixture comprises an alcohol.

Claim 29

A process according to claim 25 for determining the concentration of one or more alcohols or ethers in a liquid sample consisting essentially of hydrocarbons and said alcohols and/or said ethers, said process comprising: a) irradiating the liquid sample with radiation from a near infrared source to produce Raman scattered radiation emitted from said sample; b) collecting Raman scattered radiation emitted from the sample; c) transferring collected Raman scattered radiation and dispersing or transforming the collected Raman scattered radiation from the sample into spectra with intensities corresponding to the chemical composition of the components of said sample and concentrations of said components; d) processing said spectra according to a regression model derived by multivariate analysis of Raman spectra, or derived from a mathematical function of Raman spectra, of liquid mixtures containing known concentrations of alcohols and ethers, wherein the near infrared radiation source wavelength irradiating said sample is the same as, or correlated to, that employed in establishing said regression model; e) determining the concentration of at least one alcohol or ether present by processing the spectral intensities according to said model and producing a control signal representative of the concentration of an alcohol and/or ether in said mixture.

Claim 30

A process according to claim 26 wherein said determining of the concentration comprises emitting a signal indicative of said concentration and wherein said signal is transmitted to a means for controlling a process for producing a product comprising said alcohol or said ether.

Claim 31

A process according to claim 26 wherein the intensities corresponding to the chemical composition of components are determined at wave numbers comprising 3300-2250 and/or 1900-175 cm -1 .

Claim 32

The process of claim 14 wherein said mixture comprises an ether.

Claim 33

A process according to claim 14 wherein said multivariate analysis is accomplished by mathematical manipulation comprising neural network partial least squares (PLS), principal component regression (PCR), and/or multiple linear regression (MLR).

Claim 34

A process according to claim 14 wherein said regression model is derived by methods comprising Raman intensity differences and/or spectral subtraction.

Claim 35

A process according to claim 14 wherein said mixture comprises a synthetic fuel mixture.

Claim 36

A process according to claim 14 wherein said control signal is used in a feed-forward or a feed-back control apparatus.

Claim 37

A process according to claim 14 wherein said Raman scattered radiation is collected from regions comprising the fingerprint (FP) region or the CH stretching region.

Claim 38

A process according to claim 14 wherein transforming said collected Raman scattered radiation is by FT Raman.

Claim 39

A process comprising: a) irradiating a sample of a liquid mixture comprising hydrocarbons and further comprising as oxygenated hydrocarbon methanol, ethanol, 1-propanol, 2-propanol, 1-butanol, 2-butanol, isobutanol, tertiary butanol, tertiary amyl alcohol, methyl tertiary butyl ether (MTBE), ethyl tertiary butyl ether (ETBE), tertiary amyl methyl ether (TAME), and/or diisopropyl ether (DIPE) with near infrared radiation, producing Raman scattered radiation emitted from the sample; b) collecting Raman scattered radiation emitted from the sample; c) dispersing or transforming the collected Raman scattered radiation from the sample into spectra with intensities corresponding to the chemical composition of the components of the mixture of said sample and concentration of said components; d) processing said spectra according to a regression model derived by multivariate analysis of Raman spectra, or derived from a mathematical function of Raman spectra, of liquid mixtures containing known concentrations of oxygenated hydrocarbons, to produce a control signal representative of the concentration of oxygenated hydrocarbon in said mixture; e) controlling a process in response to said control signal.

Claim 40

A process comprising: a) irradiating a sample of a liquid mixture comprising hydrocarbons and further comprising as oxygenated hydrocarbon methanol, ethanol, 1-propanol, 2-propanol, 1-butanol, 2-butanol, isobutanol, tertiary butanol, tertiary amyl alcohol, methyl tertiary butyl ether (MTBE), ethyl tertiary butyl ether (ETBE), tertiary amyl methyl ether (TAME), and/or diisopropyl ether (DIPE) with near infrared radiation, producing Raman scattered radiation emitted from the sample; b) collecting Raman scattered radiation emitted from the sample; c) dispersing or transforming the collected Raman scattered radiation from the sample into spectra with intensities corresponding to the chemical composition of the components of the mixture of said sample and concentration of said components; d) processing said spectra according to a regression model derived by multivariate analysis of Raman spectra, or derived from a mathematical function of Raman spectra, of liquid mixtures containing known concentrations of oxygenated hydrocarbons, to produce a control signal representative of the concentration of oxygenated hydrocarbon in said mixture; e) controlling a process in response to said control signal.

Claim 41

The process of claim 36 wherein the liquid mixture is a hydrocarbon mixture.

Claim 44

An apparatus according to claim 38 wherein said control means comprises means for controlling the quantity of at least one component being delivered to a blending zone in which fuels are blended to produce a finished fuel blend having a preset desired concentration of at least one oxygenated hydrocarbon.