US1938116A - Process of removing odors from petroleum distillates - Google Patents
Process of removing odors from petroleum distillates Download PDFInfo
- Publication number
- US1938116A US1938116A US356302A US35630229A US1938116A US 1938116 A US1938116 A US 1938116A US 356302 A US356302 A US 356302A US 35630229 A US35630229 A US 35630229A US 1938116 A US1938116 A US 1938116A
- Authority
- US
- United States
- Prior art keywords
- distillate
- distillates
- odors
- materials
- petroleum distillates
- 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
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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
- C10G29/00—Refining of hydrocarbon oils, in the absence of hydrogen, with other chemicals
- C10G29/02—Non-metals
-
- 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
- C10G19/00—Refining hydrocarbon oils in the absence of hydrogen, by alkaline treatment
-
- 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
- C10G29/00—Refining of hydrocarbon oils, in the absence of hydrogen, with other chemicals
- C10G29/04—Metals, or metals deposited on a carrier
Definitions
- the objects of this invention are to provide a process of this kind in accordance with which the distillates of crude oils of the kind referred to may economically and effectively be treated to remove the objectionable odors therefrom; also 35 to provide a process of this kind in which the ingredients used to remove the objectionable odor from the distillates may be removed from the distillates without necessitating a re-dis-- tilling of the distillates; also to provide a process of this kind by means of which substances formed in the distillates as aresult of removing the odor producing ingredients can be removed by adsorption; also to improve processes of this kind in other respects hereinafter specified.
- the distillates having the objectionable odors are treated with materials which are relatively insoluble in the distillates, and which have the properties of combining with the sulphur compounds or other ingredient or ingredients of the distillates which cause these odors. These materials are mixed preferably in finely divided form with the distillate to be treated, and if necessary are kept in suspension in or intimate mixture with the distillate by agitation.
- the distillate may be re-distilled to separate the distillate from the materials used, or from the reaction products formed by the action of the material on the odor producing ingred ents.
- the material used for removing the odors from the distillate may be recovered therefrom by precipitation, centrifuging, filtration, or other means, so as to be available for v further treatment of distillates.
- the material added to the distillate is allowed to settle, so that it can be readily separated from the distillate and used 8,251,111,013 if desired, treated to remove sulphur compounds or other reaction products therefrom.
- the discolored distillate can then be quickly restored to a colorless state by mixing with, agitating with, or causing the distillate to flow through suitable 'adsorptive material, such for example, as fullers earth, silica gel, etc;, and the material w may, if desired, also be filtered in any suitable or desired manner.
- distillate is not discolored by the reaction, it may under some circumstances nevertheless be desirable to subject the same to an adsorbingagent to remove colorless reaction products in the distillate, which may have a detrimental effect on parts of engines or other apparatus or articles with which the distillate may contact.
- This treatment of the distillate is inexpensive and very effectively removes color and other reaction products therefrom, so that the resulting distillate is not only free from objectionable odors, but also colorless and free from any ingredients which might have a corrosive or other 1 injurious action on engines or other devices. If desired, it is, of course, possible to eflect a, separation of the added materials and reaction products from the distillate by re-distilling.
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)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Treatment Of Liquids With Adsorbents In General (AREA)
Description
Patented Dec. 5, 1933 Darren stares PROCESS OF REMOVING ODORS FROM PETROLEUM DISTILLATES William A. Smith, Hamtmgn. Y.
No Drawing. Application April 18, 1929 Serial No. 356,302
1 Claim. (Cl. 196-30) This invention relates to processes for removing odors from distillates of certain kinds of petroleums or crude oils.
Attempts have heretofore been made to re- 5 move odors from the distillates of certain kinds of crude oils which have objectionable odors, and which are known as skunk oils, such for example, as Lima, Venezuela, Mexican and other crude oils. In prior attemptsto remove the odors, various materials were added to the crude oil to act on the sulphur compounds in the oil during the distillation process, or vapors were subjected to the action of various 'materials but these processes either did not succeed in removing the objectionable odors, or, because of the fact that these materials could not be recovered from the residue, the processes were too expensive to be commercially feasible. These odors are generally believed to be due to the presence of certain sulphur compounds in the distillate, and these compounds are not removed by the means commonly employed for removing sulphur, 'nor are these compounds eliminated by the distillation process, as is sulphureted hydrogen. Because of lack of satisfactory methods for the removal of these odors, distillates from these crude oils are sold at prices lower than those of corresponding distillates of crude oils free from these odors.
' The objects of this invention are to provide a process of this kind in accordance with which the distillates of crude oils of the kind referred to may economically and effectively be treated to remove the objectionable odors therefrom; also 35 to provide a process of this kind in which the ingredients used to remove the objectionable odor from the distillates may be removed from the distillates without necessitating a re-dis-- tilling of the distillates; also to provide a process of this kind by means of which substances formed in the distillates as aresult of removing the odor producing ingredients can be removed by adsorption; also to improve processes of this kind in other respects hereinafter specified. In accordance with my invention the distillates having the objectionable odors are treated with materials which are relatively insoluble in the distillates, and which have the properties of combining with the sulphur compounds or other ingredient or ingredients of the distillates which cause these odors. These materials are mixed preferably in finely divided form with the distillate to be treated, and if necessary are kept in suspension in or intimate mixture with the distillate by agitation.
These materials upon reacting with the odor producing ingredients, cause either a discoloration of the distillate, or the production of substances in the distillate, which if left in the distillate, would be objected to by purchasers or Bil have a detrimental action on parts of engines or other apparatus or materials in connection With which the distillates may be used. 7
I have found that in carrying out my process,
these objectionable substances, whether or not i they cause discoloration of the distillate, can be readily removed by adsorption, filtration or both,
,or, if desired, the distillate may be re-distilled to separate the distillate from the materials used, or from the reaction products formed by the action of the material on the odor producing ingred ents. The material used for removing the odors from the distillate may be recovered therefrom by precipitation, centrifuging, filtration, or other means, so as to be available for v further treatment of distillates.
In carrying out my process, I have found that metallic cadmium or alloys thereof can be effectively employed for removing the objection- The material is 30 or without light, upon stopping the agitation, 5'.
the material added to the distillate is allowed to settle, so that it can be readily separated from the distillate and used 8,251,111,013 if desired, treated to remove sulphur compounds or other reaction products therefrom. The discolored distillate can then be quickly restored to a colorless state by mixing with, agitating with, or causing the distillate to flow through suitable 'adsorptive material, such for example, as fullers earth, silica gel, etc;, and the material w may, if desired, also be filtered in any suitable or desired manner. In case the distillate is not discolored by the reaction, it may under some circumstances nevertheless be desirable to subject the same to an adsorbingagent to remove colorless reaction products in the distillate, which may have a detrimental effect on parts of engines or other apparatus or articles with which the distillate may contact.
This treatment of the distillate is inexpensive and very effectively removes color and other reaction products therefrom, so that the resulting distillate is not only free from objectionable odors, but also colorless and free from any ingredients which might have a corrosive or other 1 injurious action on engines or other devices. If desired, it is, of course, possible to eflect a, separation of the added materials and reaction products from the distillate by re-distilling.
The process described can be used to advantage before the raw distillate has been subjected to the usual acid-lye-litharge treatment for the purpose of removingsulphur, or if desired, the
acid-lye-litharge treament may be employed after the distillate has been acted on as herein described, in which case the reaction products may be removed by the acid+lye=lithargetreatment so that no further treatment, such as' adsorption or re-distillation is necessary. It is, of
in liquid phase"tointimate mixture with metallic cadmium.
WILLIAM A. SMITH.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US356302A US1938116A (en) | 1929-04-18 | 1929-04-18 | Process of removing odors from petroleum distillates |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US356302A US1938116A (en) | 1929-04-18 | 1929-04-18 | Process of removing odors from petroleum distillates |
Publications (1)
Publication Number | Publication Date |
---|---|
US1938116A true US1938116A (en) | 1933-12-05 |
Family
ID=23400916
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US356302A Expired - Lifetime US1938116A (en) | 1929-04-18 | 1929-04-18 | Process of removing odors from petroleum distillates |
Country Status (1)
Country | Link |
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US (1) | US1938116A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2618586A (en) * | 1950-11-03 | 1952-11-18 | Wigton Abbott Corp | Process for desulfurizing petroleum products in the liquid phase |
US5894012A (en) * | 1993-08-19 | 1999-04-13 | Gilbert W. Denison | Method and system for recovering marketable end products from waste rubber |
-
1929
- 1929-04-18 US US356302A patent/US1938116A/en not_active Expired - Lifetime
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2618586A (en) * | 1950-11-03 | 1952-11-18 | Wigton Abbott Corp | Process for desulfurizing petroleum products in the liquid phase |
US5894012A (en) * | 1993-08-19 | 1999-04-13 | Gilbert W. Denison | Method and system for recovering marketable end products from waste rubber |
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