# US 2019/0169512 A1 · Method for determining asphaltene stability of a hydrocarbon-containing material > Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt - Number: US 2019/0169512 A1 - Document ID: US20190169512A1 - Status: Published application - Kind: A1 - Application number: 16/272,725 - Filed: 2019-02-11 - Published: 2019-06-06 - Earliest claimed: 2009-09-14 - Applicants: Chevron U.S.A. Inc. - Inventors: Estrella Rogel; Cesar Ovalles; Michael E. Moir - Web page: https://patentgrep.com/patent/US20190169512A1 ## CPC - C10G 75/00: Inhibiting corrosion or fouling in apparatus for treatment or conversion of hydrocarbon oils, in general (C10G7/10, C10G9/16 take precedence) - G06Q 99/00: Subject matter not provided for in other groups of this subclass - G01N 2030/8854: {involving hydrocarbons} - 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 - G06Q: INFORMATION AND COMMUNICATION TECHNOLOGY [ICT] SPECIALLY ADAPTED FOR ADMINISTRATIVE, COMMERCIAL, FINANCIAL, MANAGERIAL OR SUPERVISORY PURPOSES; SYSTEMS OR METHODS SPECIALLY ADAPTED FOR ADMINISTRATIVE, COMMERCIAL, FINANCIAL, MANAGERIAL OR SUPERVISORY PURPOSES, NOT OTHERWISE PROVIDED FOR - 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 method for determining asphaltene stability in a hydrocarbon-containing material having solvated asphaltenes therein is disclosed. The method involves the steps of: (a) precipitating an amount of the asphaltenes from a liquid sample of the hydrocarbon-containing material with an alkane mobile phase solvent in a column; (b) dissolving a first amount and a second amount of the precipitated asphaltenes by gradually and continuously changing the alkane mobile phase solvent to a final mobile phase solvent having a solubility parameter at least 1 MPa0.5 higher than the alkane mobile phase solvent; (c) monitoring the concentration of eluted fractions from the column; (d) creating a solubility profile of the dissolved asphaltenes in the hydrocarbon-containing material; and (e) determining one or more asphaltene stability parameters of the hydrocarbon-containing material. ## Claims ### Claim 1 A method for determining asphaltene stability in a hydrocarbon-containing material having solvated asphaltenes therein, the method comprising the steps of: (a) precipitating an amount of the asphaltenes from a liquid sample of the hydrocarbon containing material with at least one alkane mobile phase solvent in a column; (b) dissolving a first amount the precipitated asphaltenes by gradually and continuously adding to the column a final mobile phase solvent having a solubility parameter at least about 1 MPa0.5 higher than the at least one alkane mobile phase solvent, wherein the alkane mobile phase solvent changes from the alkane mobile phase solvent to the final mobile phase solvent during a period of about 5 minutes to about 120 minutes at a flowrate of about 1 mL/min to about 4 mL/min; (c) monitoring the concentration of each of the eluted fractions from the column; (d) generating a curve that represents the solubility parameter distribution of the asphaltene in the hydrocarbon containing material; and (e) determining one or more asphaltene stability parameters of the hydrocarbon containing material. ### Claim 2 (depends on 1) The method of claim 1, wherein the at least one alkane mobile phase solvent is selected from the group consisting of iso-octane, pentane, hexane, heptane and mixtures thereof. ### Claim 3 (depends on 1) The method of claim 1, wherein the first final mobile phase solvent is gradually and continuously added to the column at the injection point to sequentially change the alkane mobile phase solvent from 100% alkane mobile phase solvent to 100% final mobile phase solvent. ### Claim 4 (depends on 1) The method of claim 1, wherein the final mobile phase solvent is gradually and continuously added to the column at the injection point to sequentially change the alkane mobile phase solvent from 100% alkane mobile phase solvent to 100% final mobile phase solvent. ### Claim 5 (depends on 1) The method of claim 1, wherein the final mobile phase solvent is gradually and continuously added to the column at or upstream of the inlet of the column. ### Claim 6 (depends on 1) The method of claim 1, wherein the final mobile phase solvent is added to the column about 10 minutes after the liquid sample and alkane mobile phase are injected into the column. ### Claim 7 (depends on 1) The method of claim 1, further comprising monitoring the asphaltene concentration in the eluted fractions from the column after step (b) with a liquid chromatography detector which generates a signal proportional to the amount of each eluted fraction. ### Claim 8 (depends on 7) The method of claim 7, comprising calculating a percentage of each peak area for the first amount and the second amount of dissolved asphaltenes from the total peak areas, wherein the peak areas are derived from the signals. ### Claim 9 A method for determining asphaltene stability in a hydrocarbon-containing material having solvated asphaltenes therein, the method comprising the steps of: (a) precipitating an amount of the asphaltenes from a liquid sample of the hydrocarbon containing material with at least one alkane mobile phase solvent in a column; (b) dissolving a first amount and a second amount of the precipitated asphaltenes by (i) gradually and continuously adding to the column a first final mobile phase solvent having a solubility parameter at least about 1 MPa0.5 higher than the at least one alkane mobile phase solvent, at a rate of to dissolve a first amount of the precipitated asphaltenes; and (ii) gradually and continuously adding to the column a second final mobile phase solvent having a solubility parameter at least about 1 MPa0.5 higher than the first final mobile phase solvent to dissolve a second amount of the precipitated asphaltenes wherein the alkane mobile phase solvent changes from the alkane mobile phase solvent to the second final mobile phase solvent over a period of about 5 minutes to about 120 minutes at a flowrate of about 1 mL/min to about 4 mL/min. (c) monitoring the concentration of each of the eluted fractions from the column; (d) generating a curve that represents the solubility parameter distribution of the asphaltene in the hydrocarbon containing material; and (e) determining one or more asphaltene stability parameters of the hydrocarbon containing material. ### Claim 10 (depends on 9) The method of claim 9, wherein the first final mobile phase solvent is gradually and continuously added to the column at the injection point to sequentially change the alkane mobile phase solvent from 100% alkane mobile phase solvent to 100% first final mobile phase solvent. ### Claim 11 (depends on 9) The method of claim 9, wherein the first final mobile phase solvent is gradually and continuously added to the column at the injection point to sequentially change the first final mobile phase solvent from 100% first final mobile phase solvent to 100% final mobile phase solvent. ### Claim 12 (depends on 9) The method of claim 9, wherein the alkane mobile phase solvent is n-heptane, the first final mobile phase solvent is a blend of 90% dichloromethane and 10% methanol and the second final mobile phase solvent is methanol. ### Claim 13 (depends on 9) The method of claim 9, wherein the first final mobile phase solvent is added to the column 10 minutes after the liquid sample of the hydrocarbon containing material and the at least one alkane mobile phase solvent are added to the column. ### Claim 14 (depends on 9) The method of claim 9, wherein the second mobile phase solvent is added to the column 20 minutes after the at least first final mobile phase solvent is added to the column. ### Claim 15 (depends on 9) The method of claim 9, wherein the step of determining one or more asphaltene stability parameters comprises calculating an average solubility parameter of the second amount of dissolved asphaltenes. ### Claim 16 (depends on 9) The method of claim 9, wherein the average solubility parameter of the second amount of dissolved asphaltenes is calculated as a mean of a distribution corresponding to a peak or shoulder of the second amount of dissolved asphaltenes derived from the solubility profile. ### Claim 17 (depends on 9) The method of claim 9, wherein the step of determining one or more asphaltene stability parameters comprises calculating a ratio of peak, areas of the second amount of dissolved asphaltenes to the first amount of dissolved asphaltenes, wherein each of the peak areas are derived from the solubility profile. ### Claim 18 (depends on 9) The method of claim 9, wherein the step of determining one or more asphaltene stability parameters comprises calculating the overlapping area of the peak areas of the second amount of dissolved asphaltenes and the first amount of dissolved asphaltenes. ### Claim 19 (depends on 9) The method of claim 9, wherein the step of determining one or more asphaltene stability parameters comprises calculating an average solubility parameter of the second amount of dissolved asphaltenes. ### Claim 20 (depends on 9) The method of claim 9, wherein the average solubility parameter of the second amount of dissolved asphaltenes is calculated as a mean of a distribution corresponding to a peak or shoulder of the second amount of dissolved asphaltenes derived from the solubility profile. ### Claim 21 (depends on 9) The method of claim 9, wherein the step of determining one or more asphaltene stability parameters comprises calculating an overlapping area of peak areas of the second amount of dissolved asphaltenes and the first amount of dissolved asphaltenes, wherein each of the peak areas are derived from the solubility profile. ### Claim 22 (depends on 9) The method of claim 9, wherein the step of determining one or more asphaltene stability parameters comprises calculating ΔPS from an equation: ΔPS=t(75%)−t(25%) wherein t(75%) and t(25%) represent the time at which 75% and 25% of the asphaltene in the hydrocarbon-containing material have eluted. ### Claim 23 (depends on 9) The method of claim 9, further comprising selecting a second hydrocarbon containing material; repeating steps (a)-(e); and comparing the results with the first hydrocarbon containing material. ### Claim 24 A method for reducing fouling in one or more crude hydrocarbon refinery components, the method comprising the steps of: (a) selecting one or more hydrocarbon-containing feedstocks having a stable plurality of asphaltene components therein, wherein the selection of the one or more hydrocarbon-containing feedstocks comprises: (i) precipitating an amount of asphaltenes from a liquid sample of a hydrocarbon containing material with an alkane mobile phase solvent in a column; (ii) dissolving a first amount the precipitated asphaltenes by gradually and continuously adding to the column a final mobile phase solvent having a solubility parameter at least about 1 MPa0.5 higher than the at least one alkane mobile phase solvent, wherein the alkane mobile phase solvent changes from the alkane mobile phase solvent to the final mobile phase solvent during a period of about 5 minutes to about 120 minutes at a flowrate of about 1 mL/min to about 4 mL/min; (iii) monitoring the concentration of eluted fractions from the column; (iv) generating a curve that represents the solubility parameter distribution of the asphaltene in the hydrocarbon containing material; and (v) determining one or more asphaltene stability parameters of the hydrocarbon containing material; and (b) feeding the selected one or more hydrocarbon-containing feedstocks to the one or more crude hydrocarbon refinery components. ### Claim 25 (depends on 24) The method of claim 24, wherein the one or more crude hydrocarbon refinery components are selected from the group consisting of a heat exchanger, a furnace, a crude preheater, a coker preheater, a FCC slurry bottom, a debutanizer exchanger, a debutanizer tower, a feed/effluent exchanger, a furnace air preheater, a flare compressor component, a steam cracker, a steam reformer, a distillation column, a fractionation column, a scrubber, a reactor, a liquid-jacketed tank, a pipestill, a coker, a storage tank and a visbreaker. ### Claim 26 A system capable of experiencing fouling conditions associated with particulate or asphaltene fouling, the system comprising: (a) one or more crude hydrocarbon refinery components; and (b) one or more hydrocarbon-containing feedstocks having a stable plurality of asphaltene components therein and in fluid communication with the one or more crude hydrocarbon refinery components, wherein the one or more hydrocarbon-containing feedstocks are selected by a process comprising: (i) precipitating an amount of asphaltenes from a liquid sample of a hydrocarbon containing material with an alkane mobile phase solvent in a column; (ii) dissolving a first amount the precipitated asphaltenes by gradually and continuously adding to the column a final mobile phase solvent having a solubility parameter at least about 1 MPa0.5 higher than the at least one alkane mobile phase solvent, wherein the alkane mobile phase solvent changes from the alkane mobile phase solvent to the final mobile phase solvent during a period of about 5 minutes to about 120 minutes at a flowrate of about 1 mL/min to about 4 mL/min; (iii) monitoring the concentration of eluted fractions from the column; (iv) generating a curve that represents the solubility parameter distribution of the asphaltene in the hydrocarbon containing material; and (v) determining one or more asphaltene stability parameters of the hydrocarbon containing material. ### Claim 27 (depends on 26) The system of claim 26, wherein the one or more crude hydrocarbon refinery components are selected from the group consisting of a heat exchanger, a furnace, a crude preheater, a coker preheater, a FCC slurry bottom, a debutanizer exchanger, a debutanizer tower, a feed/effluent exchanger, a furnace air preheater, a flare compressor component, a steam cracker, a steam reformer, a distillation column, a fractionation column, a scrubber, a reactor, a liquid-jacketed tank, a pipestill, a coker, a storage tank and a visbreaker. ### Claim 28 A method for extending the activity of a supported or unsupported catalyst used in the reaction of one or more hydrocarbon-containing feedstocks, the method comprising the steps of: (a) selecting one or more hydrocarbon-containing feedstocks having a stable plurality of asphaltene components therein, wherein the selection of the one or more hydrocarbon-containing feedstocks comprises: (i) precipitating an amount of asphaltenes from a liquid sample of a hydrocarbon containing material with an alkane mobile phase solvent in a column; (ii) dissolving a first amount the precipitated asphaltenes by gradually and continuously adding to the column a final mobile phase solvent having a solubility parameter at least about 1 MPa0.5 higher than the at least one alkane mobile phase solvent, wherein the alkane mobile phase solvent changes from the alkane mobile phase solvent to the final mobile phase solvent during a period of about 5 minutes to about 120 minutes at a flowrate of about 1 mL/min to about 4 mL/min; (iii) monitoring the concentration of eluted fractions from tire column; (iv) generating a curve that represents the solubility parameter distribution of the asphaltene in the hydrocarbon containing material; and (v) determining one or more asphaltene stability parameters of the hydrocarbon containing material; and (b) contacting the selected one or more hydrocarbon-containing feedstocks with a supported or unsupported catalyst at a reaction temperature in a reaction zone. ### Claim 29 A method for determining asphaltene stability in a hydrocarbon-containing material having solvated asphaltenes therein, the method comprising the steps of: (a) precipitating an amount of the asphaltenes from a liquid sample of the hydrocarbon containing material with an alkane mobile phase solvent in a column; (b) dissolving a first amount the precipitated asphaltenes by gradually and continuously adding to the column a final mobile phase solvent having a solubility parameter at least about 1 MPa0.5 higher than the at least one alkane mobile phase solvent, wherein the alkane mobile phase solvent changes from the alkane mobile phase solvent to the final mobile phase solvent during a period of about 5 minutes to about 120 minutes at a flowrate of about 1 mL/min to about 4 mL/min; (c) monitoring the concentration of eluted fractions from the column; (d) generating a curve that represents the solubility parameter distribution of the asphaltene in the hydrocarbon containing material; and (e) determining one or more asphaltene stability parameters of the hydrocarbon containing material by calculating ΔPS from an equation: ΔPS=t(75%)−t(25%) wherein t(75%) and t(25%) represent the time at which 75% and 25% of the asphaltene in the hydrocarbon-containing material have eluted. ### Claim 30 A system, comprising: a plurality of components; and a processing device comprising at least one hardware processor, wherein the processing device is configured to operate the plurality of components to cause: (a) an amount of the asphaltenes to be precipitated from a liquid sample of the hydrocarbon containing material with at least one alkane mobile phase solvent in a column; (b) a first amount the precipitated asphaltenes to be dissolved by gradually and continuously adding to the column a final mobile phase solvent having a solubility parameter at least about 1 MPa0.5 higher than the at least one alkane mobile phase solvent, wherein the alkane mobile phase solvent changes from the alkane mobile phase solvent to the final mobile phase solvent during a period of about 5 minutes to about 120 minutes at a flowrate of about 1 mL/min to about 4 mL/min; (c) a concentration of each of the eluted fractions from the column to be monitired; (d) a curve that represents the solubility parameter distribution of the asphaltene in the hydrocarbon containing material to be generated; and (e) one or more asphaltene stability parameters of the hydrocarbon containing material to be determined.