US3647677A - Retardation of coke formation - Google Patents
Retardation of coke formation Download PDFInfo
- Publication number
- US3647677A US3647677A US832427A US3647677DA US3647677A US 3647677 A US3647677 A US 3647677A US 832427 A US832427 A US 832427A US 3647677D A US3647677D A US 3647677DA US 3647677 A US3647677 A US 3647677A
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- US
- United States
- Prior art keywords
- coke
- phosphorus
- oil
- formation
- retarder
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G75/00—Inhibiting corrosion or fouling in apparatus for treatment or conversion of hydrocarbon oils, in general
- C10G75/04—Inhibiting corrosion or fouling in apparatus for treatment or conversion of hydrocarbon oils, in general by addition of antifouling agents
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G7/00—Distillation of hydrocarbon oils
- C10G7/10—Inhibiting corrosion during distillation
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G9/00—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
- C10G9/14—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils in pipes or coils with or without auxiliary means, e.g. digesters, soaking drums, expansion means
- C10G9/16—Preventing or removing incrustation
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S585/00—Chemistry of hydrocarbon compounds
- Y10S585/949—Miscellaneous considerations
- Y10S585/95—Prevention or removal of corrosion or solid deposits
Definitions
- the present invention relates to a method for retarding the formation of coke in the high-temperature treatment of oils.
- coke may be significantly retarded in the high-temperature treatment of oils by incorporating into the oils a coke-retarding amount of a coke retarder selected from the group consisting of phosphorus, phosphorus compounds, and mixtures thereof.
- a coke retarder selected from the group consisting of phosphorus, phosphorus compounds, and mixtures thereof.
- the most preferred coke retarder in accordance with the present invention is elemental phosphorus, which may be used in the yellow, white, or red forms.
- elemental phosphorus which may be used in the yellow, white, or red forms.
- certain organic and inorganic phosphorus compounds have also been found to be effective.
- Phosphorus pentoxide and phosphorus pentasulfide have been found to be particularly effective inorganic compounds, while tributyl phosphine and triethyl thiophosphite are effective organic compounds.
- the phosphorus or phosphorus compound is introduced into the oil either during or prior to heating. It may be introduced directly in the form of a solid, liquid, vapor, or dispersion, or may be placed on a support such as alumina before introduction into the oil.
- Example 1 was repeated, except that 0.0044 gram (0.0088%) yellow phosphorus was employed. 2.27 grams of coke were obtained, demonstrating a 16% reduction in coke formation as compared with a similar run in the absence of phosphorus. As this example demonstrates, the use of elemental phosphorus is effective in the retardation of coke formation even at extremely low levels.
- Example 3 The procedure of Example 1 was repeated, except that 0.04 gram (0.08% red phosphorus was substituted for the yellow phosphorus. 2.18 grams of coke were obtained, showing a 19% reduction in coke formation as compared to a sample with no coke inhibitor.
- EXAMPLE 4 The following example was conducted in order to illustrate the deleterious effect of excess phosphorus. The procedure of Example 1 was repeated, except that 0.19 gram (0.4%) yellow phosphorus was incorporated into the crude oil. The experiment yielded 3.02 grams of coke as compared with 2.70 grams without any phosphorus additive. An identical run, in which red phosphorus was substituted for the yellow phosphorus, produced 3.59 grams of coke.
- EXAMPLE 5 A sample of sour crude oil was spiked with 0.05 VO(C H O' to represent a vanadium impurity often found in crude oils. Various inhibitors were added, and the amount of coke formed was measured. The results were shown in the following table.
- EXAMPLE 6 0.0023 gram (0.0046%) phosphorus pentasulfide was added to 50.4 grams of a domestic sour crude oil containing about p.p.m. nickel, 30 ppm. vanadium, and less than 1 p.p.rn. iron. The mixture was distilled and the coke formation measured in accordance with the procedure set forth in Example 1. 2.19 grams coke were yielded. This represents a 19% reduction in coke formation as compared to a similar test run on the same crude oil without any coke inhibitor.
- EXAMPLE 7 The procedure of Example 6 was repeated, except that only 0.0005 gram (0.001%) phosphorus pentasulfide was used. 2.28 grams of coke were obtained, showing a reduction in coke formation when the additive was used.
- a method for retarding the formation of coke comprising: incorporating into said oil a coke-retarding amount of a coke retarder selected from the group consisting of elemental phosphorus, phosphorus pentoxide, phosphorus pentasulfide, tributyl phosphine, triethyl thiophosphite, and mixtures thereof.
- a coke retarder selected from the group consisting of elemental phosphorus, phosphorus pentoxide, phosphorus pentasulfide, tributyl phosphine, triethyl thiophosphite, and mixtures thereof.
Abstract
THE FORMATION OF COKE IN HIGH-TEMPERATURE PETROLEUM TREATMENTS IS RETARDED BY ADDING TO THE OIL A COKE-RETARDING AMOUNT OF A COKE RETARDER SELECTED FROM THE GROUP CONSISTING OF ELEMENTAL PHOSPHOROUS AND COMPOUNDS THEREOF. VERY SMALL AMOUNTS OF THESE COKE RETARDERS ARE EFFECTIVE, WHILE THEY GENERALLY BECOME INEFFECTIVE ABOVE ABOUT 0.5%, BASED ON THE WEIGHT OF THE OIL.
Description
United States Patent 01 lice Patented Mar. 7, 1972 ABSTRACT OF THE DISCLOSURE The formation of coke in high-temperature petroleum treatments is retarded by adding to the oil a coke-retarding amount of a coke retarder selected from the group consisting of elemental phosphorus and compounds thereof. Very small amounts of these coke retarders are effective, while they generally become ineffective above about 0.5%, based on the weight of the oil.
The present invention relates to a method for retarding the formation of coke in the high-temperature treatment of oils.
The formation of coke in various high-temperature treatments of oils, particularly crude oils, has been a persistent problem. In processes such as visbreaking, catalytic cracking, and distillation, the coke that is formed has a tendency to inactivate catalysts and to clog the equipment, decreasing its efliciency of operation, and requiring periodic cleaning. The temperature at which coking becomes a problem depends upon a number of factors, particularly the characteristics of the oil being treated. As a general matter, such coke formation tends to become a problem at temperatures above about 700 F.
It has now been found that the formation of coke may be significantly retarded in the high-temperature treatment of oils by incorporating into the oils a coke-retarding amount of a coke retarder selected from the group consisting of phosphorus, phosphorus compounds, and mixtures thereof.
More particularly, it has been found that elemental phosphorus and a number of phosphorus compounds exhibit a coke retardation effect if employed Within the proper percentage range. These coke retarders have been found to be effective even at very low levels. Excellent coke retardation has been achieved, for example, with as little as 0.001% coke retarder incorporated into the oil. It is important, however, that excessive coke retarder not be employed, as excessive amounts have been found to actually accelerate rather than retard coke formation. The maximum amount of retarder that may be employed while still achieving coke retardation depends upon the nature of the oil being treated and upon the type of inhibitor being employed. As a general matter, more than about 0.5% inhibitor, based on the weight of the oil, will accelerate the production of coke, and is therefore undesirable. However, with many inhibitor-oil combinations, this coke acceleration will begin at a lower level. Therefore, the optimum proportion of inhibitor should be individually determined for each oil-inhibitor combination. It has also been found that, in coking operations, the addition of such coking retarders improves the quality of coke formed. An additional advantage of the method of the present invention is that it reduces the amount of dehydrogenation occurring during thermal processing. The coke retarders in accordance with the present invention have been found to be effective in the reduction of coke formation with oils which contain coke promoting metals such as vanadium, nickel, and the like.
The most preferred coke retarder in accordance with the present invention is elemental phosphorus, which may be used in the yellow, white, or red forms. However, certain organic and inorganic phosphorus compounds have also been found to be effective. Phosphorus pentoxide and phosphorus pentasulfide have been found to be particularly effective inorganic compounds, while tributyl phosphine and triethyl thiophosphite are effective organic compounds.
In carrying out the method of the present invention, the phosphorus or phosphorus compound is introduced into the oil either during or prior to heating. It may be introduced directly in the form of a solid, liquid, vapor, or dispersion, or may be placed on a support such as alumina before introduction into the oil.
The following examples are intended to illustrate the present invention, and should not be construed as limitative, the scope of the invention being determined by the appended claims.
EXAMPLE 1 Example 1 was repeated, except that 0.0044 gram (0.0088%) yellow phosphorus was employed. 2.27 grams of coke were obtained, demonstrating a 16% reduction in coke formation as compared with a similar run in the absence of phosphorus. As this example demonstrates, the use of elemental phosphorus is effective in the retardation of coke formation even at extremely low levels.
EXAMPLE 3 The procedure of Example 1 was repeated, except that 0.04 gram (0.08% red phosphorus was substituted for the yellow phosphorus. 2.18 grams of coke were obtained, showing a 19% reduction in coke formation as compared to a sample with no coke inhibitor.
EXAMPLE 4 The following example was conducted in order to illustrate the deleterious effect of excess phosphorus. The procedure of Example 1 was repeated, except that 0.19 gram (0.4%) yellow phosphorus was incorporated into the crude oil. The experiment yielded 3.02 grams of coke as compared with 2.70 grams without any phosphorus additive. An identical run, in which red phosphorus was substituted for the yellow phosphorus, produced 3.59 grams of coke.
EXAMPLE 5 A sample of sour crude oil was spiked with 0.05 VO(C H O' to represent a vanadium impurity often found in crude oils. Various inhibitors were added, and the amount of coke formed was measured. The results were shown in the following table.
Additive, Coke formed, wt. percent: wt. percent None 8.8 0.27% yellow phosphorus 5.8 0.13% tributyl phosphine 4.9
0.17% triethyl thiophosphite 5.3
As the above table demonstrates, significant reductions in coke formation are achieved by the addition of elemental phosphorus and phosphorus compounds.
EXAMPLE 6 0.0023 gram (0.0046%) phosphorus pentasulfide was added to 50.4 grams of a domestic sour crude oil containing about p.p.m. nickel, 30 ppm. vanadium, and less than 1 p.p.rn. iron. The mixture was distilled and the coke formation measured in accordance with the procedure set forth in Example 1. 2.19 grams coke were yielded. This represents a 19% reduction in coke formation as compared to a similar test run on the same crude oil without any coke inhibitor.
EXAMPLE 7 The procedure of Example 6 was repeated, except that only 0.0005 gram (0.001%) phosphorus pentasulfide was used. 2.28 grams of coke were obtained, showing a reduction in coke formation when the additive was used.
EXAMPLE 8 intended to cover in the appended claims all such modifications and variations as fall within the true spirit and scope of the invention.
We claim:
1. In the high-temperature treatment of oils, a method for retarding the formation of coke comprising: incorporating into said oil a coke-retarding amount of a coke retarder selected from the group consisting of elemental phosphorus, phosphorus pentoxide, phosphorus pentasulfide, tributyl phosphine, triethyl thiophosphite, and mixtures thereof.
2. The method as defined in claim 1 wherein said coke retarder is elemental phosphorus.
3. The method as defined in claim 1 wherein said coke retarder is phosphorus pentoxide.
4. The method as defined in claim 1 wherein said coke retarder is phosphorus pentasulfide.
5. The method as defined in claim 1 wherein said coke retarder is tributyl phosphine.
6. The method as defined in claim 1 wherein said coke retarder is triethyl thiophosphite.
References Cited UNITED STATES PATENTS 9/1970 Koszman 20848 \1/1971 Gillespie et al 20848 US. Cl. X.R.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US83242769A | 1969-06-11 | 1969-06-11 |
Publications (1)
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US3647677A true US3647677A (en) | 1972-03-07 |
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US832427A Expired - Lifetime US3647677A (en) | 1969-06-11 | 1969-06-11 | Retardation of coke formation |
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Cited By (26)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4024048A (en) * | 1975-01-07 | 1977-05-17 | Nalco Chemical Company | Organophosphorous antifoulants in hydrodesulfurization |
US4024049A (en) * | 1975-01-07 | 1977-05-17 | Nalco Chemical Company | Mono and di organophosphite esters as crude oil antifoulants |
US4024051A (en) * | 1975-01-07 | 1977-05-17 | Nalco Chemical Company | Using an antifoulant in a crude oil heating process |
DE2836853A1 (en) * | 1977-12-15 | 1979-06-21 | Nalco Chemical Co | METHOD FOR REDUCING POLLUTION IN AETHYLENE CRACK OVENS |
US4167471A (en) * | 1978-07-31 | 1979-09-11 | Phillips Petroleum Co. | Passivating metals on cracking catalysts |
US4419225A (en) * | 1983-03-30 | 1983-12-06 | Phillips Petroleum Company | Demetallization of heavy oils |
US4421638A (en) * | 1983-03-31 | 1983-12-20 | Phillips Petroleum Company | Demetallization of heavy oils |
US4444649A (en) * | 1982-11-15 | 1984-04-24 | Union Oil Company Of California | Antifoulant for high temperature hydrocarbon processing |
US4518484A (en) * | 1984-02-16 | 1985-05-21 | Phillips Petroleum Company | Metals removal with a light hydrocarbon and an organophosphorous compound |
EP0158968A2 (en) * | 1984-04-16 | 1985-10-23 | Phillips Petroleum Company | Antifoulants for thermal cracking processes |
US4552643A (en) * | 1985-01-22 | 1985-11-12 | Phillips Petroleum Company | Antifoulants for thermal cracking processes |
US4659452A (en) * | 1986-05-23 | 1987-04-21 | Phillips Petroleum | Multi-stage hydrofining process |
US4752374A (en) * | 1987-04-20 | 1988-06-21 | Betz Laboratories, Inc. | Process for minimizing fouling of processing equipment |
US4835332A (en) * | 1988-08-31 | 1989-05-30 | Nalco Chemical Company | Use of triphenylphosphine as an ethylene furnace antifoulant |
US4840720A (en) * | 1988-09-02 | 1989-06-20 | Betz Laboratories, Inc. | Process for minimizing fouling of processing equipment |
US4900426A (en) * | 1989-04-03 | 1990-02-13 | Nalco Chemical Company | Triphenylphosphine oxide as an ethylene furnace antifoulant |
EP0422991A1 (en) * | 1989-10-13 | 1991-04-17 | Total Raffinage Distribution S.A. | Hydrocarbon feed catalytic conversion process |
US5114436A (en) * | 1987-04-20 | 1992-05-19 | Betz Laboratories, Inc. | Process and composition for stabilized distillate fuel oils |
US5258113A (en) * | 1991-02-04 | 1993-11-02 | Mobil Oil Corporation | Process for reducing FCC transfer line coking |
WO1994006889A1 (en) * | 1992-09-15 | 1994-03-31 | Zalman Gandman | Process for obtaining lower olefins |
DE4405883C1 (en) * | 1994-02-21 | 1995-08-10 | Gerhard Prof Dr Zimmermann | Process for the preparation of thermally cracked products and application of the process for reducing the coking of heat exchange surfaces |
US5954943A (en) * | 1997-09-17 | 1999-09-21 | Nalco/Exxon Energy Chemicals, L.P. | Method of inhibiting coke deposition in pyrolysis furnaces |
US6344431B1 (en) * | 1991-12-30 | 2002-02-05 | Von Tapavicza Stephan | Use of selected inhibitors against the formation of solid organo-based incrustations from fluid hydrocarbon mixtures |
WO2002014581A1 (en) * | 2000-08-14 | 2002-02-21 | Ondeo Nalco Energy Services, L.P. | Phosphine coke inhibitors for edc-vcm furnaces |
US6706669B2 (en) | 2001-07-13 | 2004-03-16 | Exxonmobil Research And Engineering Company | Method for inhibiting corrosion using phosphorous acid |
US6852213B1 (en) | 1999-09-15 | 2005-02-08 | Nalco Energy Services | Phosphorus-sulfur based antifoulants |
-
1969
- 1969-06-11 US US832427A patent/US3647677A/en not_active Expired - Lifetime
Cited By (33)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4024048A (en) * | 1975-01-07 | 1977-05-17 | Nalco Chemical Company | Organophosphorous antifoulants in hydrodesulfurization |
US4024049A (en) * | 1975-01-07 | 1977-05-17 | Nalco Chemical Company | Mono and di organophosphite esters as crude oil antifoulants |
US4024051A (en) * | 1975-01-07 | 1977-05-17 | Nalco Chemical Company | Using an antifoulant in a crude oil heating process |
DE2836853A1 (en) * | 1977-12-15 | 1979-06-21 | Nalco Chemical Co | METHOD FOR REDUCING POLLUTION IN AETHYLENE CRACK OVENS |
US4167471A (en) * | 1978-07-31 | 1979-09-11 | Phillips Petroleum Co. | Passivating metals on cracking catalysts |
EP0007426B1 (en) * | 1978-07-31 | 1982-12-08 | Phillips Petroleum Company | Catalytic cracking process |
US4444649A (en) * | 1982-11-15 | 1984-04-24 | Union Oil Company Of California | Antifoulant for high temperature hydrocarbon processing |
US4419225A (en) * | 1983-03-30 | 1983-12-06 | Phillips Petroleum Company | Demetallization of heavy oils |
US4421638A (en) * | 1983-03-31 | 1983-12-20 | Phillips Petroleum Company | Demetallization of heavy oils |
US4518484A (en) * | 1984-02-16 | 1985-05-21 | Phillips Petroleum Company | Metals removal with a light hydrocarbon and an organophosphorous compound |
EP0158968A2 (en) * | 1984-04-16 | 1985-10-23 | Phillips Petroleum Company | Antifoulants for thermal cracking processes |
US4551227A (en) * | 1984-04-16 | 1985-11-05 | Phillips Petroleum Company | Antifoulants for thermal cracking processes |
EP0158968A3 (en) * | 1984-04-16 | 1986-09-10 | Phillips Petroleum Company | Antifoulants for thermal cracking processes |
US4552643A (en) * | 1985-01-22 | 1985-11-12 | Phillips Petroleum Company | Antifoulants for thermal cracking processes |
US4659452A (en) * | 1986-05-23 | 1987-04-21 | Phillips Petroleum | Multi-stage hydrofining process |
US5114436A (en) * | 1987-04-20 | 1992-05-19 | Betz Laboratories, Inc. | Process and composition for stabilized distillate fuel oils |
US4752374A (en) * | 1987-04-20 | 1988-06-21 | Betz Laboratories, Inc. | Process for minimizing fouling of processing equipment |
US4835332A (en) * | 1988-08-31 | 1989-05-30 | Nalco Chemical Company | Use of triphenylphosphine as an ethylene furnace antifoulant |
EP0357418A1 (en) * | 1988-08-31 | 1990-03-07 | Nalco Chemical Company | Use of triphenylphosphine as an ethylene furnace antifoulant |
US4840720A (en) * | 1988-09-02 | 1989-06-20 | Betz Laboratories, Inc. | Process for minimizing fouling of processing equipment |
US4900426A (en) * | 1989-04-03 | 1990-02-13 | Nalco Chemical Company | Triphenylphosphine oxide as an ethylene furnace antifoulant |
EP0422991A1 (en) * | 1989-10-13 | 1991-04-17 | Total Raffinage Distribution S.A. | Hydrocarbon feed catalytic conversion process |
FR2653133A1 (en) * | 1989-10-13 | 1991-04-19 | Total France | PROCESS FOR THE CATALYTIC CONVERSION OF A HYDROCARBON CHARGE |
US5213679A (en) * | 1989-10-13 | 1993-05-25 | Compagnie De Raffinage Et De Distribution Total France | Process for the catalytic conversion of a hydrocarbon feedstock |
US5258113A (en) * | 1991-02-04 | 1993-11-02 | Mobil Oil Corporation | Process for reducing FCC transfer line coking |
US6344431B1 (en) * | 1991-12-30 | 2002-02-05 | Von Tapavicza Stephan | Use of selected inhibitors against the formation of solid organo-based incrustations from fluid hydrocarbon mixtures |
WO1994006889A1 (en) * | 1992-09-15 | 1994-03-31 | Zalman Gandman | Process for obtaining lower olefins |
DE4405883C1 (en) * | 1994-02-21 | 1995-08-10 | Gerhard Prof Dr Zimmermann | Process for the preparation of thermally cracked products and application of the process for reducing the coking of heat exchange surfaces |
US5954943A (en) * | 1997-09-17 | 1999-09-21 | Nalco/Exxon Energy Chemicals, L.P. | Method of inhibiting coke deposition in pyrolysis furnaces |
US6852213B1 (en) | 1999-09-15 | 2005-02-08 | Nalco Energy Services | Phosphorus-sulfur based antifoulants |
WO2002014581A1 (en) * | 2000-08-14 | 2002-02-21 | Ondeo Nalco Energy Services, L.P. | Phosphine coke inhibitors for edc-vcm furnaces |
US6454995B1 (en) | 2000-08-14 | 2002-09-24 | Ondeo Nalco Energy Services, L.P. | Phosphine coke inhibitors for EDC-VCM furnaces |
US6706669B2 (en) | 2001-07-13 | 2004-03-16 | Exxonmobil Research And Engineering Company | Method for inhibiting corrosion using phosphorous acid |
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