Process and apparatus for distributing cold ammonia

Claim 2

A process of distributing cold liquid ammonia substantially free of gaseous ammonia at substantially ambient or atmospheric pressure comprising (1) directing an initial stream of the liquid ammonia downward by gravity flow against a splash plate having a flat surface, the plane of the flat surface being positioned in a generally horizontal direction and at a substantially orthogonal direction relative to the axis of the initial ammonia stream, the stream making contact with the flat surface within an enclosed chamber and in a manner such that a flow of liquid is formed on the flat surface to achieve effective distribution when tilting the flat surface by up to about 10 degrees from the horizontal position while maintaining the direction of the axis of the stream relative to the plane of the flat surface substantially constant, and (2) passing the liquid ammonia from the flat surface to a plurality of outlets to thereby cause a division of the cold, liquid ammonia, wherein the axis of the initial stream of cold liquid ammonia is essentially vertical and wherein the length of the vertical stream is at least about 6 inches, and wherein the initial cold liquid ammonia stream is carried by a cylindrical conduit and the end of such conduit is in a plane essentially parallel to the plane of the flat surface and wherein the distance between the end of the cylindrical conduit and the flat surface is equal to between about 1/8 to about 1/2 of the average diameter of the cylindrical conduit.

Claim 3

Process as in claim 1 wherein the cold liquid ammonia is produced by (1) transferring ammonia from a pressure tank by means of a conduit to an expansion chamber where the pressurized ammonia is converted to a mixture of gaseous ammonia and cold liquid ammonia at substantially ambient or atmospheric pressure, and then (2) separating the gaseous ammonia and the cold liquid ammonia.

Claim 4

Process as in claim 2 wherein the initial stream of cold liquid ammonia has a flow rate between about 1 and about 15 gallons per minute.

Claim 5

Process as in claim 2 wherein the liquid ammonia from the outlets is passed through a plurality of spaced conduits attached to a field cultivator and applied in a spaced pattern to the soil.

Claim 6

Process as in claim 4 wherein the liquid ammonia applied to the soil is covered immediately after application to the soil with additional soil to prevent loss of the ammonia.

Claim 7

Process as in claim 4 wherein the separated gaseous ammonia is carried by a plurality of spaced conduits and applied below the surface of the soil.

Claim 8

In a process of applying cold, liquid ammonia substantially free of gaseous ammonia at substantially atmospheric pressure to the soil comprising (1) dividing an initial stream of the cold, liquid ammonia, the initial liquid stream being carried by gravity flow by an initial conduit, into a plurality of smaller streams which are carried by a plurality of secondary conduits which conduct the liquid ammonia to spaced positions along a field cultivator, (2) then applying the smaller streams of ammonia in a spaced pattern to the soil, and (3) then covering the ammonia which has been applied to the soil with additional soil to prevent loss of ammonia to the atmosphere, the improvement comprising dividing the initial stream of ammonia into the smaller streams by directing the initial stream downward against a substantially horizontal splash plate having a flat surface, the axis of the initial stream being substantially orthogonal to the plane of the flat surface and wherein the velocity of the liquid ammonia striking the flat surface, the distance between the end of the initial conduit closest to the flat surface and the flat surface, and the shape of the end of the conduit adjacent to the flat surface are regulated such that a controlled flow of liquid ammonia is formed on the flat surface such that a controlled division of liquid ammonia is accomplished even when the position of the flat surface is varied from the horizontal position, and wherein the average diameter of the initial conduit is between about 1/2 and about 2 inches and wherein the distance between the end of the initial conduit and the flat surface is between about 1/8 inch and about 1/2 inch and wherein the initial cold liquid ammonia stream is divided into smaller streams of substantially the same flow rate.

Claim 9

In a process of applying cold, liquid ammonia substantially free of gaseous ammonia at substantially atmospheric pressure to the soil comprising (1) dividing an initial stream of the cold, liquid ammonia, the initial liquid stream being carried by gravity flow by an initial conduit, into a plurality of smaller streams which are carried by a plurality of secondary conduits which conduct the liquid ammonia to spaced positions along a field cultivator, (2) then applying the smaller streams of ammonia in a spaced pattern to the soil, and (3) then covering the ammonia which has been applied to the soil with additional soil to prevent loss of ammonia to the atmosphere, the improvement comprising dividing the initial stream of ammonia into the smaller streams by directing the initial stream downward against a substantially horizontal splash plate having a flat surface, the axis of the initial stream being substantially orthogonal to the plane of the flat surface and wherein the velocity of the liquid ammonia striking the flat surface, the distance between the end of the initial conduit closest to the flat surface and the flat surface, and the shape of the end of the conduit adjacent to the flat surface are regulated such that a controlled flow of liquid ammonia is formed on the flat surface such that a controlled division of liquid ammonia is accomplished even when the position of the flat surface is varied from the horizontal position, and wherein the average diameter of the initial conduit is between about 1/2 and about 2 inches and wherein the distance between the end of the initial conduit and the flat surface is between about 1/8 inch and about 1/2 inch and wherein the initial cold liquid ammonia stream is divided into smaller streams of substantially the same flow rate.

Claim 10

Process as in claim 7 wherein the flow rate of the initial stream of cold liquid ammonia is varied between about 1 and about 15 gallons per minute while keeping the other parameters relatively constant.

Claim 11

Process as in claim 7 wherein the velocity of the initial stream is equivalent to that achieved from free fall of a distance of of least about 6 inches.

Claim 12

In a process of treating soil comprising (1) expanding a stream of pressurized liquid ammonia in an expansion chamber to form a mixture of cold liquid and cold gaseous ammonia, (2) separating the cold liquid ammonia and the cold gaseous ammonia to produce an initial gravity flow stream of cold liquid ammonia at substantially ambient or atmospheric pressure and a separate stream of cold gaseous ammonia at substantially ambient or atmospheric pressure, (3) dividing the initial cold liquid ammonia stream into a plurality of smaller separate streams, (4) applying these smaller separate stream to the soil in a spaced arrangement, and (5) then covering the liquid ammonia which has been applied to the soil with additional soil to prevent loss of ammonia into the atmosphere, the improvement comprising dividing the initial stream of cold liquid ammonia by (1) directing the initial stream downward through a substantially vertical enclosed conduit for a distance of at least about 6 inches such that substantially the entire initial stream contacts a flat surface of a splash plate and wherein the surface is in a substantially horizontal position and wherein the end of the enclosed conduit next to the flat surface is located sufficiently close to the surface and is of suitable configuration to force the liquid ammonia to form a liquid layer on the flat surface, which layer moves in a plurality of directions from the area where the liquid ammonia contacts the splash plate surface, and (2) directing the layer of liquid on the flat surface through a plurality of outlets to form said plurality of smaller streams, and wherein the flat surface and the end of the initial conduit adjacent to the flat surface are located in an enclosed chamber, and wherein the end of the conduit is in a plane essentially parallel to the plane of the flat surface and wherein the distance between the end of the conduit and the flat surface is between about 1/8 to about 1/2 of the average diameter of the conduit.

Claim 13

In a process of treating soil comprising (1) expanding a stream of pressurized liquid ammonia in an expansion chamber to form a mixture of cold liquid and cold gaseous ammonia, (2) separating the cold liquid ammonia and the cold gaseous ammonia to produce an initial gravity flow stream of cold liquid ammonia at substantially ambient or atmospheric pressure and a separate stream of cold gaseous ammonia at substantially ambient or atmospheric pressure, (3) dividing the initial cold liquid ammonia stream into a plurality of smaller separate streams, (4) applying these smaller separate stream to the soil in a spaced arrangement, and (5) then covering the liquid ammonia which has been applied to the soil with additional soil to prevent loss of ammonia into the atmosphere, the improvement comprising dividing the initial stream of cold liquid ammonia by (1) directing the initial stream downward through a substantially vertical enclosed conduit for a distance of at least about 6 inches such that substantially the entire initial stream contacts a flat surface of a splash plate and wherein the surface is in a substantially horizontal position and wherein the end of the enclosed conduit next to the flat surface is located sufficiently close to the surface and is of suitable configuration to force the liquid ammonia to form a liquid layer on the flat surface, which layer moves in a plurality of directions from the area where the liquid ammonia contacts the splash plate surface, and (2) directing the layer of liquid on the flat surface through a plurality of outlets to form said plurality of smaller streams, and wherein the flat surface and the end of the initial conduit adjacent to the flat surface are located in an enclosed chamber, and wherein the end of the conduit is in a plane essentially parallel to the plane of the flat surface and wherein the distance between the end of the conduit and the flat surface is between about 1/8 to about 1/2 of the average diameter of the conduit.

Claim 14

Process as in claim 10 wherein the axis of the initial conduit is positioned in a substantially orthogonal direction relative to the plane of the flat surface.

Claim 15

In a process of treating soil comprising (1) producing an initial gravity flow stream of cold liquid ammonia at substantially ambient or atmospheric pressure and a separate stream of cold gaseous ammonia at substantially ambient or atmospheric pressure by expanding pressurized liquid ammonia in an expansion chamber and then separating the liquid ammonia from the gaseous ammonia, (2) dividing the initial cold liquid ammonia stream into a plurality of separate streams, (3) applying this plurality of separate streams to the ground in a spaced arrangement, and (4) then covering the liquid ammonia which has been applied to the soil to prevent loss of ammonia to the atmosphere, the improvement wherein the initial stream of cold liquid ammonia is divided by directing the cold liquid ammonia downward by gravity flow through a substantially vertical initial conduit at least about 6 inches in length against a substantially horizontal flat surface to form a layer of liquid ammonia flowing in a plurality of directions into a plurality of conduits to form said plurality of smaller streams, and wherein the vertical initial conduit has an average diameter of between about 1/2 to about 2 inches and wherein the end of the vertical initial conduit lies in a plane substantially parallel to the flat surface and is spaced a distance of between about 1/8 inch and about 1/2 inch from the flat surface.

Claim 16

In a process of treating soil comprising (1) producing an initial gravity flow stream of cold liquid ammonia at substantially ambient or atmospheric pressure and a separate stream of cold gaseous ammonia at substantially ambient or atmospheric pressure by expanding pressurized liquid ammonia in an expansion chamber and then separating the liquid ammonia from the gaseous ammonia, (2) dividing the initial cold liquid ammonia stream into a plurality of separate streams, (3) applying this plurality of separate streams to the ground in a spaced arrangement, and (4) then covering the liquid ammonia which has been applied to the soil to prevent loss of ammonia to the atmosphere, the improvement wherein the initial stream of cold liquid ammonia is divided by directing the cold liquid ammonia downward by gravity flow through a substantially vertical initial conduit at least about 6 inches in length against a substantially horizontal flat surface to form a layer of liquid ammonia flowing in a plurality of directions into a plurality of conduits to form said plurality of smaller streams, and wherein the vertical initial conduit has an average diameter of between about 1/2 to about 2 inches and wherein the end of the vertical initial conduit lies in a plane substantially parallel to the flat surface and is spaced a distance of between about 1/8 inch and about 1/2 inch from the flat surface.

Claim 17

Process as in claim 12 wherein the axis of the initial conduit is positioned in a substantially orthogonal direction relative to the plane of the flat surface.

Claim 18

Process as in claim 13 wherein the vertical initial conduit has an average diameter of about 1 inch and wherein the end of the vertical conduit closest to the flat surface is spaced about 1/4 inch from the flat surface.

Claim 21

Apparatus as in claim 15 additionally comprising production means for the cold liquid ammonia, such production means comprising (1) means for transferring ammonia from a pressure tank by means of a conduit to an expansion chamber, (2) an expansion chamber where the pressurized ammonia is converted to a mixture of gaseous ammonia and cold liquid ammonia at substantially ambient or atmospheric pressure, and (3) means for separating the gaseous ammonia and the cold liquid ammonia.

Claim 22

Apparatus as in claim 16 wherein the means for directing an initial stream of cold liquid ammonia has the capacity for a flow rate between about 1 and about 15 gallons per minute.

Claim 23

Apparatus as in claim 16 wherein the outlets for the liquid ammonia are connected to a plurality of spaced conduits attached to a field cultivator for applying the liquid ammonia in a spaced pattern to the soil.

Claim 24

Apparatus as in claim 18 additionally comprising means for covering with additional soil the liquid ammonia applied to the soil immediately after such application to the soil to prevent loss of the ammonia.

Claim 25

Apparatus as in claim 18 additionally comprising a plurality of spaced conduit means for carrying the separate gaseous stream of ammonia, and means for applying the gaseous ammonia below the surface of the soil.

Claim 26

In an apparatus for applying cold liquid ammonia substantially free of gaseous ammonia at substantially atmospheric pressure to the soil comprising (1) means for dividing an initial stream of the cold liquid ammonia, comprising (a) means for carrying the initial liquid stream in a downward direction by gravity flow to a plurality of secondary conduit means which conduit the liquid ammonia as separate smaller streams to spaced positions along a field cultivator, (2) means for applying the smaller streams of ammonia in a spaced pattern to the soil, and (3) means for covering the ammonia which has been applied to the soil with additional soil to prevent loss of ammonia to the atmosphere, the improvement comprising means for dividing the initial stream of ammonia into the smaller streams comprising means for directing the initial stream against a substantially horizontal flat surface means, the axis of the initial stream being substantially orthogonal to the plane of the flat surface means and wherein the velocity of the liquid ammonia striking the flat surface, the distance between the end of the initial conduit means closest to the flat surface and the flat surface, and the shape of the end of the conduit adjacent to the flat surface are regulated such that a controlled flow of liquid ammonia may be formed on the flat surface such that a controlled division of liquid ammonia may be accomplished even when the position of the flat surface means is varied from the horizontal position, wherein the average diameter of the initial conduit means is about 1 inch and wherein the distance between the end of the initial conduit means and the flat surface is between about 1/8 inch and about 1/2 inch, and wherein the velocity of the initial stream is equivalent to that achieved from free fall of at least about 6 inches.

Claim 27

In an apparatus for applying cold liquid ammonia substantially free of gaseous ammonia at substantially atmospheric pressure to the soil comprising (1) means for dividing an initial stream of the cold liquid ammonia, comprising (a) means for carrying the initial liquid stream in a downward direction by gravity flow to a plurality of secondary conduit means which conduit the liquid ammonia as separate smaller streams to spaced positions along a field cultivator, (2) means for applying the smaller streams of ammonia in a spaced pattern to the soil, and (3) means for covering the ammonia which has been applied to the soil with additional soil to prevent loss of ammonia to the atmosphere, the improvement comprising means for dividing the initial stream of ammonia into the smaller streams comprising means for directing the initial stream against a substantially horizontal flat surface means, the axis of the initial stream being substantially orthogonal to the plane of the flat surface means and wherein the velocity of the liquid ammonia striking the flat surface, the distance between the end of the initial conduit means closest to the flat surface and the flat surface, and the shape of the end of the conduit adjacent to the flat surface are regulated such that a controlled flow of liquid ammonia may be formed on the flat surface such that a controlled division of liquid ammonia may be accomplished even when the position of the flat surface means is varied from the horizontal position, wherein the average diameter of the initial conduit means is about 1 inch and wherein the distance between the end of the initial conduit means and the flat surface is between about 1/8 inch and about 1/2 inch, and wherein the velocity of the initial stream is equivalent to that achieved from free fall of at least about 6 inches.

Claim 28

Apparatus as in claim 21 wherein the flow rate of the means for directing an initial stream of cold liquid ammonia has the capability of being varied between about 2 and about 15 gallons per minute while keeping the other parameters relatively constant.

Claim 29

In an apparatus for treating soil comprising (1) means for producing an initial stream of cold, gravity flow liquid ammonia at substantially ambient or atmospheric pressure and a separate stream of cold gaseous ammonia at substantially ambient or atmospheric pressure comprising means for expanding pressurized liquid ammonia in an expansion chamber and means for separating the liquid ammonia from the gaseous ammonia, (2) means for dividing the initial cold liquid ammonia stream into a plurality of separate streams, (3) means for applying the plurality of separate streams to the ground in a spaced arrangement, and (4) means for covering the liquid ammonia which has been applied to the soil to prevent loss of ammonia into the atmosphere, the improvement wherein the means for dividing the initial stream of cold liquid ammonia comprises means for directing the initial cold liquid ammonia stream downward by gravity flow through a substantially vertical initial conduit means at least about 6 inches in length against a substantially horizontal flat surface means to form a layer of liquid ammonia flowing in a plurality of directions into a plurality of conduit means to form said plurality of smaller streams, and wherein the vertical initial conduit means has an average diameter of between about 1/2 to about 2 inches and wherein the end of the vertical initial conduit lies in a plane substantially parallel to the flat surface and is spaced between about 1/8 inch and about 1/2 inch from the flat surface.

Claim 30

In an apparatus for treating soil comprising (1) means for producing an initial stream of cold, gravity flow liquid ammonia at substantially ambient or atmospheric pressure and a separate stream of cold gaseous ammonia at substantially ambient or atmospheric pressure comprising means for expanding pressurized liquid ammonia in an expansion chamber and means for separating the liquid ammonia from the gaseous ammonia, (2) means for dividing the initial cold liquid ammonia stream into a plurality of separate streams, (3) means for applying the plurality of separate streams to the ground in a spaced arrangement, and (4) means for covering the liquid ammonia which has been applied to the soil to prevent loss of ammonia into the atmosphere, the improvement wherein the means for dividing the initial stream of cold liquid ammonia comprises means for directing the initial cold liquid ammonia stream downward by gravity flow through a substantially vertical initial conduit means at least about 6 inches in length against a substantially horizontal flat surface means to form a layer of liquid ammonia flowing in a plurality of directions into a plurality of conduit means to form said plurality of smaller streams, and wherein the vertical initial conduit means has an average diameter of between about 1/2 to about 2 inches and wherein the end of the vertical initial conduit lies in a plane substantially parallel to the flat surface and is spaced between about 1/8 inch and about 1/2 inch from the flat surface.

Claim 31

Apparatus as in claim 23 wherein the axis of the initial conduit is positioned in a substantially orthogonal direction relative to the plane of the flat surface.

Claim 32

Apparatus as in claim 24 wherein the vertical initial conduit has an average diameter of about 1 inch and wherein the end of the vertical conduit closest to the flat surface is spaced about 1/4 inch from the flat surface.