US1839114A - Refining of petroleum oils - Google Patents
Refining of petroleum oils Download PDFInfo
- Publication number
- US1839114A US1839114A US74395A US7439525A US1839114A US 1839114 A US1839114 A US 1839114A US 74395 A US74395 A US 74395A US 7439525 A US7439525 A US 7439525A US 1839114 A US1839114 A US 1839114A
- Authority
- US
- United States
- Prior art keywords
- acid
- refining
- acids
- oil
- sulphur
- 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.)
- Expired - Lifetime
Links
- 239000003921 oil Substances 0.000 title description 15
- 238000007670 refining Methods 0.000 title description 14
- 239000003208 petroleum Substances 0.000 title description 5
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 17
- 150000007522 mineralic acids Chemical class 0.000 description 11
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 10
- 239000002253 acid Substances 0.000 description 10
- 150000007524 organic acids Chemical class 0.000 description 9
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 8
- 239000000203 mixture Substances 0.000 description 8
- 239000001117 sulphuric acid Substances 0.000 description 8
- 235000011149 sulphuric acid Nutrition 0.000 description 8
- 229960000583 acetic acid Drugs 0.000 description 6
- 239000003795 chemical substances by application Substances 0.000 description 6
- 230000005484 gravity Effects 0.000 description 6
- 235000011007 phosphoric acid Nutrition 0.000 description 6
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 5
- 150000007513 acids Chemical class 0.000 description 5
- 229940093915 gynecological organic acid Drugs 0.000 description 5
- 239000012263 liquid product Substances 0.000 description 5
- 238000000034 method Methods 0.000 description 5
- 229910017604 nitric acid Inorganic materials 0.000 description 5
- 235000005985 organic acids Nutrition 0.000 description 5
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 4
- 239000005864 Sulphur Substances 0.000 description 4
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 4
- 150000001875 compounds Chemical class 0.000 description 4
- 238000005336 cracking Methods 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- 239000004215 Carbon black (E152) Substances 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 229930195733 hydrocarbon Natural products 0.000 description 2
- 150000002430 hydrocarbons Chemical class 0.000 description 2
- 230000001590 oxidative effect Effects 0.000 description 2
- 238000005120 petroleum cracking Methods 0.000 description 2
- 238000004525 petroleum distillation Methods 0.000 description 2
- 101710083262 Ectin Proteins 0.000 description 1
- UEZVMMHDMIWARA-UHFFFAOYSA-N Metaphosphoric acid Chemical compound OP(=O)=O UEZVMMHDMIWARA-UHFFFAOYSA-N 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 238000010961 commercial manufacture process Methods 0.000 description 1
- XPPKVPWEQAFLFU-UHFFFAOYSA-N diphosphoric acid Chemical compound OP(O)(=O)OP(O)(O)=O XPPKVPWEQAFLFU-UHFFFAOYSA-N 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000012362 glacial acetic acid Substances 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 150000003016 phosphoric acids Chemical class 0.000 description 1
- 229940005657 pyrophosphoric acid Drugs 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
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
- C10G17/00—Refining of hydrocarbon oils in the absence of hydrogen, with acids, acid-forming compounds or acid-containing liquids, e.g. acid sludge
- C10G17/02—Refining of hydrocarbon oils in the absence of hydrogen, with acids, acid-forming compounds or acid-containing liquids, e.g. acid sludge with acids or acid-containing liquids, e.g. acid sludge
Definitions
- This invention relates to improvements in the refining of petroleum oils, and refers more particularly to the subjection of the lighter gravity liquid products produced in petroleum distillation and cracking to the action of various refining agents for the purpose of removing or converting objectionable color-forming, odor-forming, sulphur and analogous objectionable compounds.
- the essence of the present invention resides in the utilization, as a refining agent, of subtantially sulphur-free inorganic or organic acids, or a substantially stable combination of organic and inorganic acids as the sole refining agent, or in combination with any other suitable refining agent or any combination of refining agents to. accomplish the purpose above set forth.
- nitric acid nitric acid
- hydrochloric acid nitric acid
- orthophosphoric acid pyrophosphoric acid and metaphosphoric acid.
- These inorganic acids pointed out may be used alone or may be mixed with each other.
- one mixture of inorganic acids which has been found suitable for the purpose comprises a small proportion of nitric acid in one of the phosphoric acids.
- the present invention may be listed the f0 lowing: acetic (preferably glacial), chloracetic, citric, tartaric, and the like. These organic acids may be used alone or in combination with each other in suitable proportions, and the invention also contemplates that the organic acids may be mixed with the inorganic acids. As anillustrative example of the proportions in which these acids are mixed, phosphoric acid and be taken, as an example.
- the acetic acid in the mixture is always less than 50% by volume of the mixture, especially where the glacial acetic acid is used, for the reason that this acid is soluble in the oil and requires a larger proportion of phosphoric acid to reduce this solubility. This points acetic acid may.
- nitric acid for example, 5 to with phosphoric acid or with acetic acid.
- the percentage of nitric acid while not limited to the amount shown, must be kept as a smaller percentage relatively to the other acid in order to cut down its oxidizing properties, and thus obtain the benefits of the mixed acids.
- nitric acid to acetic acid or phosthe trade which are phoric acid strengthens them by adding some oxidizing value to these relatively weak acids-
- the present invention contemplates more particularly the refining of what are known as cracked distillates, and more particularly those cracked overhead products of end boiling point commercially satisfactory to produced directly from the cracking process.
- Steps in a process of refining the lighter gravity liquid products produced from the cracking of petroleum oil comprising subjecting the oil separately to the action of a substantially stable mixture of substantially sulphur-free organic and inorganic acids, and to the action of concentrated sulphuric acid to remove or convert objectionable compounds present in said lighter gravity liquid products.
- a step in a process of refining the lighter gravity liquid products obtained in the cracking of petroleum oil comprising subjecting said lighter gravity products to the action of a substantially stable mixture of substantially sulphur free organic and inorganic acids.
- a process for refining hydrocarbon oils which comprises treating the oil with concentrated sulphuric acid and with a mixture of substantially sulphur-free organic and inorganic acids having the property of reducing objectionable reaction between the sulphuric acid and the oil.
- a process for refining hydrocarbon oils which comprises treating the oil with concentrated sulphuric acid and with a mixture of phosphoric acid and acetic acid.
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Description
Patented Dec. 29, 1931 UNITED STATES PATENT OFFICE JACQUE C. MORRELL, OF CHICAGO, ILLINOIS, ASSIGNOB TO UNIVERSAL OIL PRODUCTS COMPANY, OF CHICAGO, ILLINOIS, A CORPORATION OF SOUTH DAKOTA BEFINING OF PETROLEUM OILS No Drawing. Application filed December 9, 1925,
This invention relates to improvements in the refining of petroleum oils, and refers more particularly to the subjection of the lighter gravity liquid products produced in petroleum distillation and cracking to the action of various refining agents for the purpose of removing or converting objectionable color-forming, odor-forming, sulphur and analogous objectionable compounds.
The essence of the present invention resides in the utilization, as a refining agent, of subtantially sulphur-free inorganic or organic acids, or a substantially stable combination of organic and inorganic acids as the sole refining agent, or in combination with any other suitable refining agent or any combination of refining agents to. accomplish the purpose above set forth.
I have discovered that when the lighter gravity liquid products produced in petroleum distillation and cracking are subjected to the action of concentrated sulphuric acid, for the purpose of refining and removing objectionable compounds, the strength of the concentrated acid produces an objectionable reaction, namely, the oxidation of compounds present, particularly in cracked distillates, reacting in such manner as to'leave in the refined oil substances which bring about an unstable condition in the oil with respect to color and odor.
To overcome this objection, various experiments were carried out, and I have discovered that it is possible to substitute for the concentrated sulphuric acid substantially sulphur-free inorganic or organic acids, either alone or in combination. Further, it' is possible to overcome the objections pointed out by preceding the treatment with concentrated sulphuric acid with the step of subj ectin the oil to the action of the substantially su phur-free acids above set forth.
It may be pointed out that it is the essence of the resent invention to use, essentially as .a refining agent, the substantially sulphurfree organic or. inorganic acids herein set out,
in combination with concentrated sulphuric acid, which. of course, includes the step of subjecting the oil first to the action of the substantially sulphur-free acids before de- Serial No. 74,395. Renewed November 10, 1980.
does not refer to the presence of small or accidental amounts of sulphur present in the materials from which the acid was made or introduced during the course of commercial manufacture, in other words, it does not refer to impurities which contain sulphur.
Among some of the inorganic acids contemplated for use in the present invention may be listed nitric acid, hydrochloric acid,
orthophosphoric acid, pyrophosphoric acid and metaphosphoric acid. These inorganic acids pointed out may be used alone or may be mixed with each other. For instance, one mixture of inorganic acids which has been found suitable for the purpose comprises a small proportion of nitric acid in one of the phosphoric acids.
Among the organic acids contemplated b the present invention may be listed the f0 lowing: acetic (preferably glacial), chloracetic, citric, tartaric, and the like. These organic acids may be used alone or in combination with each other in suitable proportions, and the invention also contemplates that the organic acids may be mixed with the inorganic acids. As anillustrative example of the proportions in which these acids are mixed, phosphoric acid and be taken, as an example. Preferably, the acetic acid in the mixture is always less than 50% by volume of the mixture, especially where the glacial acetic acid is used, for the reason that this acid is soluble in the oil and requires a larger proportion of phosphoric acid to reduce this solubility. This points acetic acid may.
out that the properties of these acids must be considered in their use. Another suitable mixture is the introduction ofa small percentage of nitric acid, for example, 5 to with phosphoric acid or with acetic acid. The percentage of nitric acid, while not limited to the amount shown, must be kept as a smaller percentage relatively to the other acid in order to cut down its oxidizing properties, and thus obtain the benefits of the mixed acids. On the other hand, the addition of nitric acid to acetic acid or phosthe trade which are phoric acid strengthens them by adding some oxidizing value to these relatively weak acids- The present invention contemplates more particularly the refining of what are known as cracked distillates, and more particularly those cracked overhead products of end boiling point commercially satisfactory to produced directly from the cracking process.
I claim as my invention:
1. Steps in a process of refining the lighter gravity liquid products produced from the cracking of petroleum oil, comprising subjecting the oil separately to the action of a substantially stable mixture of substantially sulphur-free organic and inorganic acids, and to the action of concentrated sulphuric acid to remove or convert objectionable compounds present in said lighter gravity liquid products. V
2. A step in a process of refining the lighter gravity liquid products obtained in the cracking of petroleum oil, comprising subjecting said lighter gravity products to the action of a substantially stable mixture of substantially sulphur free organic and inorganic acids.
3. A process for refining hydrocarbon oils which comprises treating the oil with concentrated sulphuric acid and with a mixture of substantially sulphur-free organic and inorganic acids having the property of reducing objectionable reaction between the sulphuric acid and the oil.
4. A process for refining hydrocarbon oils which comprises treating the oil with concentrated sulphuric acid and with a mixture of phosphoric acid and acetic acid.
JACQUE C. MORRELL.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US74395A US1839114A (en) | 1925-12-09 | 1925-12-09 | Refining of petroleum oils |
| US236377A US1853920A (en) | 1925-12-09 | 1927-11-28 | Refining of petroleum oils |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US74395A US1839114A (en) | 1925-12-09 | 1925-12-09 | Refining of petroleum oils |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1839114A true US1839114A (en) | 1931-12-29 |
Family
ID=22119325
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US74395A Expired - Lifetime US1839114A (en) | 1925-12-09 | 1925-12-09 | Refining of petroleum oils |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1839114A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2751331A (en) * | 1951-11-13 | 1956-06-19 | Texas Co | Process for selectively polymerizing diolefins |
-
1925
- 1925-12-09 US US74395A patent/US1839114A/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2751331A (en) * | 1951-11-13 | 1956-06-19 | Texas Co | Process for selectively polymerizing diolefins |
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