US2199564A - Hydrocarbon reactions - Google Patents
Hydrocarbon reactions Download PDFInfo
- Publication number
- US2199564A US2199564A US180572A US18057237A US2199564A US 2199564 A US2199564 A US 2199564A US 180572 A US180572 A US 180572A US 18057237 A US18057237 A US 18057237A US 2199564 A US2199564 A US 2199564A
- Authority
- US
- United States
- Prior art keywords
- sulfuric acid
- reactions
- derivatives
- hydrocarbons
- temperatures
- 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
- 229930195733 hydrocarbon Natural products 0.000 title description 12
- 150000002430 hydrocarbons Chemical class 0.000 title description 12
- 238000006243 chemical reaction Methods 0.000 title description 8
- 239000004215 Carbon black (E152) Substances 0.000 title description 6
- QAOWNCQODCNURD-UHFFFAOYSA-N sulfuric acid Substances OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 26
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 18
- 238000000034 method Methods 0.000 description 16
- PMPVIKIVABFJJI-UHFFFAOYSA-N Cyclobutane Chemical compound C1CCC1 PMPVIKIVABFJJI-UHFFFAOYSA-N 0.000 description 6
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 6
- 125000003118 aryl group Chemical group 0.000 description 6
- 125000004432 carbon atom Chemical group C* 0.000 description 6
- BDJAEZRIGNCQBZ-UHFFFAOYSA-N methylcyclobutane Chemical compound CC1CCC1 BDJAEZRIGNCQBZ-UHFFFAOYSA-N 0.000 description 6
- LVZWSLJZHVFIQJ-UHFFFAOYSA-N Cyclopropane Chemical compound C1CC1 LVZWSLJZHVFIQJ-UHFFFAOYSA-N 0.000 description 5
- 229950011148 cyclopropane Drugs 0.000 description 5
- 239000000203 mixture Substances 0.000 description 5
- 238000011282 treatment Methods 0.000 description 5
- 239000002253 acid Substances 0.000 description 4
- 125000000217 alkyl group Chemical group 0.000 description 4
- ODLMAHJVESYWTB-UHFFFAOYSA-N propylbenzene Chemical compound CCCC1=CC=CC=C1 ODLMAHJVESYWTB-UHFFFAOYSA-N 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 239000001117 sulphuric acid Substances 0.000 description 3
- 235000011149 sulphuric acid Nutrition 0.000 description 3
- PWATWSYOIIXYMA-UHFFFAOYSA-N Pentylbenzene Chemical class CCCCCC1=CC=CC=C1 PWATWSYOIIXYMA-UHFFFAOYSA-N 0.000 description 2
- 230000029936 alkylation Effects 0.000 description 2
- 238000005804 alkylation reaction Methods 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 239000003054 catalyst Substances 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 235000011121 sodium hydroxide Nutrition 0.000 description 2
- 230000002194 synthesizing effect Effects 0.000 description 2
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- 101100439251 Petunia hybrida CHI2 gene Proteins 0.000 description 1
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical class CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 1
- 239000003377 acid catalyst Substances 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 125000000484 butyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 description 1
- OCKPCBLVNKHBMX-UHFFFAOYSA-N butylbenzene Chemical compound CCCCC1=CC=CC=C1 OCKPCBLVNKHBMX-UHFFFAOYSA-N 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 239000003518 caustics Substances 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000006482 condensation reaction Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 125000000753 cycloalkyl group Chemical group 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000005194 fractionation Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000003502 gasoline Substances 0.000 description 1
- 229910052736 halogen Inorganic materials 0.000 description 1
- 125000005843 halogen group Chemical group 0.000 description 1
- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- 238000010907 mechanical stirring Methods 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 239000001294 propane Substances 0.000 description 1
- 125000001436 propyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])[H] 0.000 description 1
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 1
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 1
- 238000000197 pyrolysis Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000002407 reforming Methods 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 238000009877 rendering Methods 0.000 description 1
- 238000007363 ring formation reaction Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 238000006277 sulfonation reaction Methods 0.000 description 1
- 125000000383 tetramethylene group Chemical group [H]C([H])([*:1])C([H])([H])C([H])([H])C([H])([H])[*:2] 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2/00—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2527/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
- C07C2527/02—Sulfur, selenium or tellurium; Compounds thereof
- C07C2527/053—Sulfates or other compounds comprising the anion (SnO3n+1)2-
- C07C2527/054—Sulfuric acid or other acids with the formula H2Sn03n+1
Definitions
- This invention is more particularly related to reactions which occur between relatively stable cyclic hydrocarbons comprising benzol and its homologs and the members of the relatively unstable group of cycloparaflins having less than 5 carbon atoms in the ring.
- the invention is concerned with catalytic processes which enable the production of higher molecular weight alkylated derivatives of mono nuclear aromatics by the addition of alkyl groups through the agency of the designated unstable cycloparaffins.
- the invention comprises a process for the treatment of relatively stable hydrocarbons comprising benzol and its homologs with cycloparafiins containing 3 and 4 carbon atoms in the ring and comprising cyclopropane and cyclobutane to form alkylated derivatives of said stable hydrocarbons while utilizing relatively concentrated sulfuric acid catalysts, and relatively low temperature conditions.
- the cyclopropane and cyclobutane necessary for the process may be produced by the action of sodium on dihalogen derivatives of propane and n-butane respectively in which the halogen substitution is on the end carbon atoms.
- the reactions of this method of formation are shown in the following equations.
- tain degree of sulfonation of the aromatics may take place primarily, there is no particular disadvantage in this since the introduction of the cycloparaifins results in the alkylation of the aromatics with the regeneration of sulfuric acid for further use in the reactions.
- the operation may be modified by mixing the cycloparaflin and the aromatic with the proper proportion of sulfuric acid and maintaining the components of the mixture in intimate contact by mechanical stirring for a definite period of time with outside cooling to prevent undue temperature the.
- the acid and hydrocarbon layers are separated and the latter subjected to fractionation for the recovery of individual compounds or close cuts.
- operations may be conducted either in batch or continuous systerm.
- the alkylated products may be washed with caustic soda or other alkalis to remove traces of acids or acid products of the reactions and the spent acid catalyst may be treated by any necessary method to restore it to the condition fitting it for further service.
- the present process is particularly applicable to the treatment of the light distillate produced in the destructive distillation of coal and other hydrocarbonaceous material. It is also applicable to the treatment of analogous highly aromatic distillates produced by the intensive cracking of the heavier portions of petroleum to produce gasoline or by the reforming or secondary them with cyclopropane or cyclobutane are pre dominantly of a normal character as distinguished from similar derivatives made by using propylene and butylene.
- the mechanism of the reactions which lead to the formation of the normal alkyl derivatives is not known but it may be safely stated that the present process forms a definite means of producing such normal aromatic derivatives.
- the temperatures of operation are maintained at a. relatively low point so that ordinarily temperatures of above 30 C. are seldom utilized unless the aromatic or mixture of aromatics undergoing treatment is solid at these temperatures when more elevated temperatures may be used above their melting points and also if desired somewhat less reactive catalysts corresponding to the more dilute acid.
- Example I Into a solution of approximately 90 parts by weight of benzene and 45 parts by weight of 96% sulfuric acid maintained at a temperature of approximately 5 C., 18 parts by-weight of cyclopropane were passed at atmospheric pressure over a period of approximately 1 hour. The hydrocarbon layer was then separated and further treated by washing with'cold 96% sulfuric acid followed by water, dilute caustic, and a final water wash. A yield of normal propyl benzene boiling at 150 to 157 C. was obtained in an amount corresponding to approximately 35% of the theoretical.
- Emmple II A mixture of 30 parts by weight of methyl cyclobutane, 90 parts by weight of benzene and 90 parts by weight of 96% sulfuric acid was maintained at a temperature of approximately 4 C. for a period of 2% hours during which time the materials were vigorously agitated. After separation of the hydrocarbon layer, it was washed with cold 96% sulfuric acid, followed -by water, dilute caustic soda, and a final water wash. In this case a yield of approximately 30% of material corresponding in its properties to a mixture of amyl benzenes was separated.
- a process for producing alkvlated aromatics which comprises reacting an aromatic with a cycloparaflln of less than 5 carbon atoms in the ringin the presence of sulphuric acid and at a temperature of from -l to +30 C.
- a process for producing allwlated aromatics which comprises reacting an aromatic with a cycloparafiin of less than carbon atoms in the ring in the presence of sulphuric acid of above 85% concentration and. at a temperature of from l0 to +30 C.
- a process for producing normal propyl derivatives of aromatic hydrocarbons which comprises subjecting said hydrocarbons to the action of cyclo-propane at temperatures of the order of l() to +30 C. in the presence of sulfuric acid of over 85% concentration- 5.
- a process for producing normal butyl derivatives of aromatic hydrocarbons which comprises subjecting said hydrocarbons to the action of cyclo-butane at temperatures of the order of to +30 C. in the presence of sulfuric acid of over 35% concentration.
- a process for producing normal propyl benzene which comprises subjecting said benzene to the action of cycle-propane at temperatures of the order of 10 to +30 C. in the presence of sulfuric acid of over 85% concentration.
- a process for producing normal butyl benzene which comprises subjecting said benzene to the action of cyclo-butane at temperatures of the/ order of -10 to +3050. in the presence of sulfuric acid of over 85% concentration.
- a process for producing amyl benzenes which comprises subjecting benzene to the action of methyl cyclo-butane at temperatures of the order of -l0 to +30 C. in the presence of sulfuric acid of over 85% concentration.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Description
Patented May 7, 1940- UNITED STATES PATENT OFFICE HYDROOABBON REACTIONS No Drawing. Application December is, 1931, Serial No. 180,572
8 Claims.
This invention is more particularly related to reactions which occur between relatively stable cyclic hydrocarbons comprising benzol and its homologs and the members of the relatively unstable group of cycloparaflins having less than 5 carbon atoms in the ring.
More specifically the invention is concerned with catalytic processes which enable the production of higher molecular weight alkylated derivatives of mono nuclear aromatics by the addition of alkyl groups through the agency of the designated unstable cycloparaffins.
The art of synthesizing organic compounds and particularly those of a hydrocarbon character with which the present invention is concerned is important in view of the fact that special hydrocarbons in any one series may have peculiar characteristics rendering them suitable for use either as abasis for the development of useful derivatives or direct use in hydrocarbon mixtures such as, for example, those employed as fuels for internal combustion engines, lubricants etc. and the present invention is a contribution to the art of catalytically synthesizing such hydrocarbons.
In one specific embodiment the invention comprises a process for the treatment of relatively stable hydrocarbons comprising benzol and its homologs with cycloparafiins containing 3 and 4 carbon atoms in the ring and comprising cyclopropane and cyclobutane to form alkylated derivatives of said stable hydrocarbons while utilizing relatively concentrated sulfuric acid catalysts, and relatively low temperature conditions.
The aromatic hydrocarbons which may be alkylated by the low molecular weight cycloparafiins according to the present process comprise benzol as the simplest member of the series and any of its higher homologs which are still capable of adding more alkyl groups. This does not necessarily infer that all homologs are equally reactive or that all those containing unsubstituted ring hydrogen atoms are capable of further alkylation since the possibility of adding further alkyl groups is one determinable only by experiment.
The cyclopropane and cyclobutane necessary for the process may be produced by the action of sodium on dihalogen derivatives of propane and n-butane respectively in which the halogen substitution is on the end carbon atoms. The reactions of this method of formation are shown in the following equations.
CHIB! CHgBl' 0111.011, +2Na -2NaBr+- cmcmmomen, Other methods of manufacture may be employed involving various types of condensation and cyclization reactions although the above is generally the simplest and most practical. The principal properties of the two cycloparaflins are given below:
Compound 130111920 point, speigig giavity Cyclo ropane 35 Cyclo utane 11-12 0.7038
tain degree of sulfonation of the aromatics may take place primarily, there is no particular disadvantage in this since the introduction of the cycloparaifins results in the alkylation of the aromatics with the regeneration of sulfuric acid for further use in the reactions. In the case of cyclobutane and its alkylated derivatives such as methyl cyclobutane which may be normally liquid or readily liquefiable in the. preferred temperature range, the operation may be modified by mixing the cycloparaflin and the aromatic with the proper proportion of sulfuric acid and maintaining the components of the mixture in intimate contact by mechanical stirring for a definite period of time with outside cooling to prevent undue temperature the. After any of these treatments the acid and hydrocarbon layers are separated and the latter subjected to fractionation for the recovery of individual compounds or close cuts. Obviously operations may be conducted either in batch or continuous systerm. The alkylated products may be washed with caustic soda or other alkalis to remove traces of acids or acid products of the reactions and the spent acid catalyst may be treated by any necessary method to restore it to the condition fitting it for further service.
The present process is particularly applicable to the treatment of the light distillate produced in the destructive distillation of coal and other hydrocarbonaceous material. It is also applicable to the treatment of analogous highly aromatic distillates produced by the intensive cracking of the heavier portions of petroleum to produce gasoline or by the reforming or secondary them with cyclopropane or cyclobutane are pre dominantly of a normal character as distinguished from similar derivatives made by using propylene and butylene. The mechanism of the reactions which lead to the formation of the normal alkyl derivatives is not known but it may be safely stated that the present process forms a definite means of producing such normal aromatic derivatives.
The temperatures of operation are maintained at a. relatively low point so that ordinarily temperatures of above 30 C. are seldom utilized unless the aromatic or mixture of aromatics undergoing treatment is solid at these temperatures when more elevated temperatures may be used above their melting points and also if desired somewhat less reactive catalysts corresponding to the more dilute acid.
The following examples are given to indicate the type of reactions involvedin theprocess of thepresent invention although not with the intention of unduly limiting its proper scope.
Example I Into a solution of approximately 90 parts by weight of benzene and 45 parts by weight of 96% sulfuric acid maintained at a temperature of approximately 5 C., 18 parts by-weight of cyclopropane were passed at atmospheric pressure over a period of approximately 1 hour. The hydrocarbon layer was then separated and further treated by washing with'cold 96% sulfuric acid followed by water, dilute caustic, and a final water wash. A yield of normal propyl benzene boiling at 150 to 157 C. was obtained in an amount corresponding to approximately 35% of the theoretical.
Emmple II A mixture of 30 parts by weight of methyl cyclobutane, 90 parts by weight of benzene and 90 parts by weight of 96% sulfuric acid was maintained at a temperature of approximately 4 C. for a period of 2% hours during which time the materials were vigorously agitated. After separation of the hydrocarbon layer, it was washed with cold 96% sulfuric acid, followed -by water, dilute caustic soda, and a final water wash. In this case a yield of approximately 30% of material corresponding in its properties to a mixture of amyl benzenes was separated.
The nature of the present invention and. its practical possibilities are evident from the foregoing description and numerical data, neither of which however is intended to unduly limit its proper scope.
'cycloparafiln of less than 5 carbon atoms in the ring in the presence of sulphuric acid.
2. A process for producing alkvlated aromatics which comprises reacting an aromatic with a cycloparaflln of less than 5 carbon atoms in the ringin the presence of sulphuric acid and at a temperature of from -l to +30 C.
3. A process for producing allwlated aromatics which comprises reacting an aromatic with a cycloparafiin of less than carbon atoms in the ring in the presence of sulphuric acid of above 85% concentration and. at a temperature of from l0 to +30 C. v
4. A process for producing normal propyl derivatives of aromatic hydrocarbons which comprises subjecting said hydrocarbons to the action of cyclo-propane at temperatures of the order of l() to +30 C. in the presence of sulfuric acid of over 85% concentration- 5. A process for producing normal butyl derivatives of aromatic hydrocarbons which comprises subjecting said hydrocarbons to the action of cyclo-butane at temperatures of the order of to +30 C. in the presence of sulfuric acid of over 35% concentration.
6. A process for producing normal propyl benzene which comprises subjecting said benzene to the action of cycle-propane at temperatures of the order of 10 to +30 C. in the presence of sulfuric acid of over 85% concentration.
7. A process for producing normal butyl benzene which comprises subjecting said benzene to the action of cyclo-butane at temperatures of the/ order of -10 to +3050. in the presence of sulfuric acid of over 85% concentration.
8. A process for producing amyl benzenes which comprises subjecting benzene to the action of methyl cyclo-butane at temperatures of the order of -l0 to +30 C. in the presence of sulfuric acid of over 85% concentration.
' VLADIMIR N. .IPA'I'IEFF.
HERMAN PINES.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US180572A US2199564A (en) | 1937-12-18 | 1937-12-18 | Hydrocarbon reactions |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US180572A US2199564A (en) | 1937-12-18 | 1937-12-18 | Hydrocarbon reactions |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US2199564A true US2199564A (en) | 1940-05-07 |
Family
ID=22660942
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US180572A Expired - Lifetime US2199564A (en) | 1937-12-18 | 1937-12-18 | Hydrocarbon reactions |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US2199564A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2430660A (en) * | 1944-07-03 | 1947-11-11 | Phillips Petroleum Co | Production of alkenyl aromatics |
| US2695324A (en) * | 1952-05-16 | 1954-11-23 | California Research Corp | Hydrocarbon purification process |
-
1937
- 1937-12-18 US US180572A patent/US2199564A/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2430660A (en) * | 1944-07-03 | 1947-11-11 | Phillips Petroleum Co | Production of alkenyl aromatics |
| US2695324A (en) * | 1952-05-16 | 1954-11-23 | California Research Corp | Hydrocarbon purification process |
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