US1798166A - Beta-naphthol pellet - Google Patents
Beta-naphthol pellet Download PDFInfo
- Publication number
- US1798166A US1798166A US178119A US17811927A US1798166A US 1798166 A US1798166 A US 1798166A US 178119 A US178119 A US 178119A US 17811927 A US17811927 A US 17811927A US 1798166 A US1798166 A US 1798166A
- Authority
- US
- United States
- Prior art keywords
- beta
- beta naphthol
- naphthol
- pellet
- pipe
- 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
- JWAZRIHNYRIHIV-UHFFFAOYSA-N 2-naphthol Chemical compound C1=CC=CC2=CC(O)=CC=C21 JWAZRIHNYRIHIV-UHFFFAOYSA-N 0.000 title 2
- 229950011260 betanaphthol Drugs 0.000 title 1
- 239000008188 pellet Substances 0.000 title 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C39/00—Compounds having at least one hydroxy or O-metal group bound to a carbon atom of a six-membered aromatic ring
- C07C39/12—Compounds having at least one hydroxy or O-metal group bound to a carbon atom of a six-membered aromatic ring polycyclic with no unsaturation outside the aromatic rings
- C07C39/14—Compounds having at least one hydroxy or O-metal group bound to a carbon atom of a six-membered aromatic ring polycyclic with no unsaturation outside the aromatic rings with at least one hydroxy group on a condensed ring system containing two rings
-
- 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
- Y10S159/00—Concentrating evaporators
- Y10S159/23—Cooling
Definitions
- My invention relates particularly to a process of spraying beta naphthol in such a manner as to secure certain advantages therefrom, and relates, also, to the sprayed beta naphthol produced therein.
- the ob ect of my invention is to provide a process for obtaining a new form of beta naphthol that is valuable commerclally.
- One of the purposes of my invention is to convert molten beta naphthol into a finely d1- vided spheroidal product which is substantially free from the tendency to agglomerate and cake, as, for example, when ground or flaked.
- a further object is to avoid deterioration of the beta naphthol which usually occurs when the latter is finely divided in the presence of air, b carrying out the process 1n an inert atmos ere. The deterioration of the beta naphtho is avoided thereby, both in the method of manufacture and in the sub sequent storage or transportation of the beta naphthol.
- Figure 1 is a vertical sectionof an apparatus which may be used in'accordance with my invention
- Figure 2 is an enlarged detail view showing the spraying machine contained therein.
- the liquid beta naphthol may be received in the liquid form from any suitable source of supply, such, for example, as the receiver of a still, whence it may be conveyed by a pipe 1 to a supply tank 2 provided with a'steam coil 3 for keeping the beta naphthol at the desired temperature to maintain the required fluidity.
- a valved pipe 4 is provided for drawing oil? the liquid beta naphthol from the tank 2 to a spraying device comprised ofa rapidly spinning bowl 5 driven by an electric motor 6 located in a compartment 7 provided at the top of a spraying chamber 8.
- the chamber 8 has a hopper-like conical bottom 9 leading to a valved discharge pipe 10 for delivering the spheroidal particles of beta naphthol to a cask 11, or any other type of receiver, for
- an inert gas such as carbon dioxide or nitrogen
- a supply pipe 12 connected to the bottom of the same and having therein a fan 13 supplied with compressed gas from a bottle 14 having a valve 15 at the top thereof and a pipe 16 leading to the inlet side of the fan 13.
- the heated gases pass up through the top of the chamber 8 through a filtering medium 17 of cloth of fine muslin, or other suitable medium, and thence outwardly through a pipe 18 to a cooler 19 having a series of vertically arranged tubes 20 therein around which there is passed a current of cooling water from a valved inlet pipe 21, and which is discharged through an overflow pipe 22.
- the cooled gases are then conveyed by a pipe 23 to the above mentioned fan 13 to be recirculated in the chamber 8.
- the liquid beta naphthol in the supply tank 2, and which is maintained as a liquid therein at a temperature of approximately 130 0., is supplied to the spraying device in which the rapidly spinning bowl 5 causes the molten beta naphthol to be thrown out by centrifugal force, in the form of a fine mist, the individual particles of which become chilled or solidified in a spheroidal shape while falling through in an atmosphere of inert gas in the chamber 8.
- the beta naphthol thus falls down in the hopper 9 in a fine granular form whence it may be discharged from time to time, as desired, or continuously, if desired, through the valved pipe 10 into the cask 11 or other receptacle.
- the inert gas in the chamber 8 becomes warm by contact with the betanaphthol, and is freed from any fine particles of beta naphthol by being passed through the filter 17 after which the gas is cooled down to a temperature preferably of 30 C. or lower. in the cooler 20, and is then recirculated by the fan 13 to the spraying chamber.
- An article of manufacture comprising beta naphthol in the form of finely'divided particles, substantially free from any tendency to agglomerate or cake, and which are substantially spheroidal in shape.
- An article of manufacture comprising beta naphthol in the form offinely divided particles having great resistance to deterioration due to formation in an inert gas, substantially free from any tendency to agglomerate or cake, and which are substantially spheriodal in shape.
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Description
March 31, 1931. c. E. MENSING BETA NAPHTHOL PELLET Filed March 24, 1927 351 abtomu w I Patented Mar. 31, 1931 UNITED STATES PATENT OFFICE CARL E. IENSING, OI BRIDGEWATEB TOWNSHIP, SOMERSET COUNTY, NEW JERSEY, ASSIGNOB, BY KESNE ASSIGNMENTS, TO THE CAI-CO CHEMICAL COMPANY, INC., A
CORPORATION OF DELAWARE IBETA-NAIPHTHOL PELLET Application filed March 24, 1927. Serial No. 178,119.
My invention relates particularly to a process of spraying beta naphthol in such a manner as to secure certain advantages therefrom, and relates, also, to the sprayed beta naphthol produced therein.
The ob ect of my invention is to provide a process for obtaining a new form of beta naphthol that is valuable commerclally. One of the purposes of my invention is to convert molten beta naphthol into a finely d1- vided spheroidal product which is substantially free from the tendency to agglomerate and cake, as, for example, when ground or flaked. A further object is to avoid deterioration of the beta naphthol which usually occurs when the latter is finely divided in the presence of air, b carrying out the process 1n an inert atmos ere. The deterioration of the beta naphtho is avoided thereby, both in the method of manufacture and in the sub sequent storage or transportation of the beta naphthol. When beta naphthol is exposed to the air there results a very decided oxidation, resulting in a darkening in color, and the higher the temperature at which the beta naphthol is exposed to the air the faster will be therate of deterioration due to oxidation. Therefore, in my process the oxidation, with the resultant darkening in color, is avoided.
Also, by discharging the product containing the inert gas into barrels, as hereinafter indicated, the voids therein will be filled with the inert atmosphere instead of air, thus avoiding the dar ening in color which would otherwise result. Again, by my process I lessen the hazards of dust explosion and resultant fire, which are common at present in the previous process of manufacturing powdered-or flaked beta naphthol. Another 1 portant object of my invention is to provi e a finely divided beta naphthol which will dissolve in solvents much more readily than in the case of previous finely divided beta naphthols obtained by other methods, in-
asmuch as in the product obtained by my While my invention is capable of being carried out in connection with many different types of apparatus I have shown only one type of apparatus for use therewith in the accompanying drawings, in which Figure 1 is a vertical sectionof an apparatus which may be used in'accordance with my invention; and v Figure 2 is an enlarged detail view showing the spraying machine contained therein.
In carrying out my invention, the liquid beta naphthol may be received in the liquid form from any suitable source of supply, such, for example, as the receiver of a still, whence it may be conveyed by a pipe 1 to a supply tank 2 provided with a'steam coil 3 for keeping the beta naphthol at the desired temperature to maintain the required fluidity. A valved pipe 4 is provided for drawing oil? the liquid beta naphthol from the tank 2 to a spraying device comprised ofa rapidly spinning bowl 5 driven by an electric motor 6 located in a compartment 7 provided at the top of a spraying chamber 8. The chamber 8 has a hopper-like conical bottom 9 leading to a valved discharge pipe 10 for delivering the spheroidal particles of beta naphthol to a cask 11, or any other type of receiver, for
shipment, storage, etc. Preferably an inert gas, such, for example, as carbon dioxide or nitrogen, is circulated upwardly through the chamber 8 from a supply pipe 12 connected to the bottom of the same and having therein a fan 13 supplied with compressed gas from a bottle 14 having a valve 15 at the top thereof and a pipe 16 leading to the inlet side of the fan 13. The heated gases pass up through the top of the chamber 8 through a filtering medium 17 of cloth of fine muslin, or other suitable medium, and thence outwardly through a pipe 18 to a cooler 19 having a series of vertically arranged tubes 20 therein around which there is passed a current of cooling water from a valved inlet pipe 21, and which is discharged through an overflow pipe 22. The cooled gases are then conveyed by a pipe 23 to the above mentioned fan 13 to be recirculated in the chamber 8.
In accordance with the operation of the process in said apparatus, the liquid beta naphthol in the supply tank 2, and which is maintained as a liquid therein at a temperature of approximately 130 0., is supplied to the spraying device in which the rapidly spinning bowl 5 causes the molten beta naphthol to be thrown out by centrifugal force, in the form of a fine mist, the individual particles of which become chilled or solidified in a spheroidal shape while falling through in an atmosphere of inert gas in the chamber 8. The beta naphthol thus falls down in the hopper 9 in a fine granular form whence it may be discharged from time to time, as desired, or continuously, if desired, through the valved pipe 10 into the cask 11 or other receptacle. The inert gas in the chamber 8 becomes warm by contact with the betanaphthol, and is freed from any fine particles of beta naphthol by being passed through the filter 17 after which the gas is cooled down to a temperature preferably of 30 C. or lower. in the cooler 20, and is then recirculated by the fan 13 to the spraying chamber.
While I have described my invention above in detail I wish it to be understood that many changes may be made therein without departing from the spirit of the same.
I claim:
1. An article of manufacture comprising beta naphthol in the form of finely'divided particles, substantially free from any tendency to agglomerate or cake, and which are substantially spheroidal in shape.
2. An article of manufacture comprising a very readilv soluble beta naphthol in the form of finely divided particles, substantially free from any tendency to agglomerate or cake, and which are substantially spheroidal in shape.
3. An article of manufacture comprising beta naphthol in the form offinely divided particles having great resistance to deterioration due to formation in an inert gas, substantially free from any tendency to agglomerate or cake, and which are substantially spheriodal in shape.
March, 1927.
CARL E. MENSING.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US178119A US1798166A (en) | 1927-03-24 | 1927-03-24 | Beta-naphthol pellet |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US178119A US1798166A (en) | 1927-03-24 | 1927-03-24 | Beta-naphthol pellet |
Publications (1)
Publication Number | Publication Date |
---|---|
US1798166A true US1798166A (en) | 1931-03-31 |
Family
ID=22651280
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US178119A Expired - Lifetime US1798166A (en) | 1927-03-24 | 1927-03-24 | Beta-naphthol pellet |
Country Status (1)
Country | Link |
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US (1) | US1798166A (en) |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2762700A (en) * | 1949-08-23 | 1956-09-11 | Richard J Brooks | Production of ferrous chloride and metallic iron powder |
US3058159A (en) * | 1958-12-29 | 1962-10-16 | Japan Reichhold Chemicals Inc | Method for producing a pearl-formed solid-state condensation-type resin |
US3280009A (en) * | 1959-07-13 | 1966-10-18 | Rheinpreussen Ag | Process and apparatus for spray evaporation |
US3549731A (en) * | 1967-05-09 | 1970-12-22 | Technion Res & Dev Foundation | Method for the production of resin particles |
US3676534A (en) * | 1969-09-26 | 1972-07-11 | Scott Anderson | Process relating to ultra-pure metal halide particles |
US3819310A (en) * | 1971-01-08 | 1974-06-25 | I Mavrovic | Apparatus for prilling urea |
US20040145069A1 (en) * | 2003-01-21 | 2004-07-29 | Low David Nicholson | Nozzle valve type spray dryer |
US20070045099A1 (en) * | 2005-09-01 | 2007-03-01 | Watervap, Llc | Method and system for seaparating solids from liquids |
US20070045100A1 (en) * | 2005-09-01 | 2007-03-01 | Watervap, Llc | Method and system for separating solids from liquids |
-
1927
- 1927-03-24 US US178119A patent/US1798166A/en not_active Expired - Lifetime
Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2762700A (en) * | 1949-08-23 | 1956-09-11 | Richard J Brooks | Production of ferrous chloride and metallic iron powder |
US3058159A (en) * | 1958-12-29 | 1962-10-16 | Japan Reichhold Chemicals Inc | Method for producing a pearl-formed solid-state condensation-type resin |
US3280009A (en) * | 1959-07-13 | 1966-10-18 | Rheinpreussen Ag | Process and apparatus for spray evaporation |
US3549731A (en) * | 1967-05-09 | 1970-12-22 | Technion Res & Dev Foundation | Method for the production of resin particles |
US3676534A (en) * | 1969-09-26 | 1972-07-11 | Scott Anderson | Process relating to ultra-pure metal halide particles |
US3819310A (en) * | 1971-01-08 | 1974-06-25 | I Mavrovic | Apparatus for prilling urea |
US20040145069A1 (en) * | 2003-01-21 | 2004-07-29 | Low David Nicholson | Nozzle valve type spray dryer |
US6820865B2 (en) * | 2003-01-21 | 2004-11-23 | David Nicholson Low | Nozzle valve type spray dryer |
US20070045099A1 (en) * | 2005-09-01 | 2007-03-01 | Watervap, Llc | Method and system for seaparating solids from liquids |
US20070045100A1 (en) * | 2005-09-01 | 2007-03-01 | Watervap, Llc | Method and system for separating solids from liquids |
US7357849B2 (en) * | 2005-09-01 | 2008-04-15 | Watervap, Llc | Method and system for separating solids from liquids |
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