US1000732A

US1000732A - Process of making nitric oxid.

Info

Publication number: US1000732A
Application number: US37853707A
Authority: US
Inventors: Friedrich Haeusser
Original assignee: Individual
Current assignee: Individual
Priority date: 1907-06-12
Filing date: 1907-06-12
Publication date: 1911-08-15
Anticipated expiration: 1928-08-15

Description

P. HAUSSBR.

PROCESS OF MAKING NITRIC OXID.

APPLICATION FILED JUNE 12. 1907 1,000,732. Patented Aug. 15, 1911.

UTO/f/VEY rnmnarcn riliussna, or xarsnnsnau'rnnn, cranium;

PROCESS OF MAKING NITRIC OXID.

Specification of Letters Patent. Patented Aug. '15, 1911.

Application flledJ'une 12, 1907. Serial No. 378,587.

To all whom it may concern:

Be it known that I, FRIEDRICH Hiiussnn, residing-at Kaiserslautern, in the Kingdom of Bavaria and German Empire, have invented new and useful Methods of Producing Oxid of Nitrogen by Means of Explosions, of which the following is a specification. This invention relates to a method for producing oxids of nitrogen by means of explosions from a mixture containing nitro en, oxygen and combustible gas or vapor.

he invention .is an improvement on and a further development of a method for production of oxids of nitrogen, which is patented to me by United States Letters Patent 961,350 of June 14, 1910. In the said Letters Patent a method is disclosed for producing oxidsof nitrogen by the explosive-combustion of a combustible gas mixture 'within the cylinder of a combustion engine, the mixture expanding within the engine after the explosion and acting thereby upon the piston.

It is an ob ect of-the present invention to simplify the method disclosed in said patent and to avoid certain disadvantages which were connected with the method described in said patent.

The operation of an engine which transinto mechanical enforms chemical energy ergy and which $1111 in practice. 7 p C' It is therefore an object of the invention to'produce "oxids of nitrogen by means of endently of a. process which explosions ind or the sake of mechanical is performed output; ower. 4

' Anot er'object is to use the heat of the exhaust gases' for concentrating the produced nitric acid or salts of nitric acid.

In my invention the gases aredischarged of a compressor, and the fresh charge is ignited in said chamber.. The ignition chamber referably is of suflicient size,.so that 5 the esired pressure therein before ignition is only obtained after several revolutions taneously produces oxids of nitrogen encounters many difliculties of the crank shaft of the compressor. By this means the number of explosions is considerably less than the number of revolutions of the compressor, so that the number of o erations of the exhaust valve in the ignition chamber, and consequently the wear and tear 'of said valve is reduced. The exhaust valve interposed between the cylinder'of the compressor and the ignition c amber serves only for the passage of the compressed gases before the same have reached the temperature of ignition.

The drawing shows by way of example diagrammatically devices for performing my method of producing oxid of nitrogen.

Figure 1 shows diagrammatically a longitudinal section through one device. Fig. 2 is a section on line AB of Fig. 1. Fig. 3 is a longitudinal section shown diagrammatically of a modified device. Fig. 4 is a diagrammatical view of a cam disk.

Piston 1 in the compressor cylinder 2 is actuated by the cran'k'3, a connecting rod being interposed between piston and crank. In its movement to the right in Fig. 1 the piston draws air or another mixture of oxygen and nitrogen by suction through conduit 4 into the cylinder 2, while a combustible preferably in gas or spray form is drawn'in through conduit 5 connected with a suitable supply, not shown. The admission of the oxygen-nitro 'en mixture is regulated by valve 7, \while tIle admissioh of the combustible is controlled by valve 6.

For the sake of better illustration valve 6 in Figs. 1 and 3 is shown to be disposed in one plane with valves 7, 8 and 14 although this showing does not agree with that of Fig. 2. It is to be understood however that this is only done for the sake of better illustration.

By the return stroke of the piston 1 to the left in Fig. 1, the mixture of air or nitrogen and oxygen with the combustible is conveyed through valve 8 into the explosion chamber 9. Valves 6, 7 and 8 are diagrammatically shown as sprin controlled valves. This operation is repeate until the gases in the explosion chamber 9 have reached a certain pressure. The mixture is then ex loded by means of an igniting device 10 an after having reached and maintained its maximum temperature for some time it is chilled rapidly to prevent decomposition of the.

nitric oxids formed during the explosion. The, maximum temperature should not be less than 1900 to 2000 degrees centigrade and it should remain at this point for some time. The chilling of the gases is effected by injecting into the explosion chambera suitable cooling means, for this purpose water air,

steam or such like maybe admitted from a valve 14 after'which operation chamber is filled with a new charge from the cyliner 2.

In the modification illustrated in Fig. 3 the chilling of the'gases is effected by conveying the same 'from'the chamber 9 through the exhaust valve 14 into a receptacle. 15 which is surrounded by cooling means.

. Whatever be the method for chilling the gases, care must be taken either by selecting a suitable amount of injection means or by selecting a suitable size of the cooling area of the receptacle 15 respectively that the temperature of the gases does not fall below' a temperature in which a decomposition of the nitric oxid might decrease the output. It is known that even at comparatively high temperatures, of about 1500 to 1600 degrees Centigrade, the decomposition takes place slowly. It is suflicient therefore to chill the gases to about this temperature. The gases are still very hot and therefore maybe used for purpose of concentration. The exhaust gases leaving the explosion chamber 9 in Fig. 1 or the cooling receptacle 15 in Fig. 3 respectively are conveyed through concentrating devices 16. Flowing through.these devices their temperature is lowered so far that the nitric oxid NO combines with the oxygen of the exhaust gases forming thereby dioxid of nitrogen NO,. From the concentrating device the exhaust gases flow through the absorption apparatus 17 in which the dioxid of nitrogen is washed out by means of water, forming thereby a diluted nitric acid in accordance with the equation cylinder 2. After the exhaust valve 14 has returned into closing position the compressor starts to operate in the way described above.

For the purpose of regulating the operation of the compressor in accordance with that of the valve 14 a cam shaft 19 is driven grees ,about 100 to 115 from the shaft, on which the crank 3 is mounted, a worm gear 18 serving for the transmission. A plurality of cam disks are mounted on the shaft 19 one only being shown, said disk 20 actuating the valves 6, 7 7 and-14 by means of levers or

links

21, 22

and 23. Springs secured to the valves serve for returning said valves automatically into closing position. The cam disks 20 on the shaft 19 are disposed-so that the valves 6 and 7 are opened during the suction stroke of the compressor and that they remain closed while the piston presses the gases from the cylinder 2 into the explosion cham-' ber 9. During the explosion of the gases in. 8 the chamber 9 and during the exhaust period of the same from said chamber, in which period valve 14 is opened, valve 6 remains closed. It is obvious therefore that during this period no fuel is conveyed into the cylinder 2. The valve 7 however remains open so that the piston may draw air into the cylinder 2 and mayexpel'the same therefrom through the air conduit 4. After the gases are discharged from the chamber 9 and after 9 valve 14 has returned to closing position valves 6 and 7 are actuated again as stated above.

The method described is more clearly explained by the following data, obtained from actual working on a basis of experiments in a laboratory. The explosion cham ber had a volume of 1.7 liters and was filled with a mixture of illuminating gas and air, said ingredients being present in the mixture in a ratio of'1:6.4. The pressure in the chamber amounted to 2.6 atmosphere. This pressure increased to'24.5' atmosphere after the ignition of the gases and the temperature of the explosion arose to about 1880 decentigrade. This temperature re-' mained approximately constant for about 1/10 of a second. After this period of constancy 60 cubic centimeters of water were in jected into the explosion chamber chillin 10 thereby the gases rapidly to a temperature of about 900 degrees'centigrade. The acid produced by these experiments was very weak as a large amount of injection medium was used. It contained about'3/10 gram .115 nitric acid to 100 grams water. One cubic meter of illuminating gas gave an output of grams nitric acid.

I claim:

1. A method for making nitric acid, which 130 consists in compressing a mixture of nitrogen, oxygen and a combustible into a separate ignition chamber, igniting the mixture therein,-allowing the temperature torise tothe point necessary for producing nitric oxid and allowing the temperature to remain until the nitric oxid is produced, suddenly causin the temperature to drop to a point slight y below the temperature at which the nitric oxid is decomposed, converting the nitric oxid into dilute nitric acid and concentratingthe same by the heat of said-exhaust gases.

2. A method for making nitric acid which consists in compressing a mixture of nitrogen, oxygen and a combustible, conveying the compressed mixture into an ignition chamber, igniting the mixture therein, allowing the temperature to rise to the point necessary for producing nitric oxid and allowing the temperature to remainuntil the nitric oxid is produced, suddenly causing the temperature to drop to a point below the temperature at which the nitric oxid is decomposed, converting the nitric oxid into dilute nitric acid and concentrating the same by the heat of said exhaust gases.

'3. A method for making nitric oxid, which consists in compressing a mixture of nitrogen, oxygen and a combustible conveying the compressed mixture into an ignition chamber, igniting the mixture therein, allowing the temperature to rise to the point necessary for producing nitric oxid and al- 2 lowing the temperature to remain untilthe nitric oxid is produced, suddenly causing the temperature to drop to a point below the temperature at which the nitric oxid is de composed and discharging the gases result ing from the ignition. 4. A method for making nitric oxid, which consists in compressing a mixture of nitrogen, oxygen and a combustible agent, forcing the compressed mixture into an ignition chamber until the mixture in said chamber is at a predetermined pressure, igniting the mixture, allowing the itiemperagure to rise to ahenwnntmecewyior n o ucing nitric oxid and allowing the tefmure tree- 0 main until the nitricoxid is produced, suddenly causing the temperature to drop to a point below the temperature at which the nitric oxid is decomposed and discharging the gases resulting from the ignition.

5. The process for produclng oxids of nitrogen by means of explosive combustion from a compressed mixture of nitrogen, oxygen, and a combustlble gas or vapor, consisting in first compressing the said mixture, then forcing the compressed mixture into an ignition chamber until a predetermined pressure has been attained therein,"

then exploding the mixture, maintaining the high temperature of explosion constant for a sufliciently long period to permit-the, formation of oxids of nitrogen, then passing.

the gaseous products of combustion into a cooled receptacle, thereby chilling the same and preventing decomposition of the oxids of the nitrogen, and finally causing the said products of combustion to pass through a concentrating apparatus for the purpose of chamber, igniting the mixture therein, al-

lowing the temperature to rise to the point necessary for producing nitric oxid and allowing the temperature to remain until the' nitric oxid is produced, conveying the gases resulting from the ignition, into a cooled vessel, to lower the temperature to a point below the temperature at which the nitric oxid is decomposed, and discharging the' gases.

In testimony whereof I have signed my name to this specification in the presence of two subscribing witnesses; a

FRIEDRICH HAUSSER. Witnesses:

WOLDEMAR HAUPT HENRY HAsrER;