Flowable liquid fertilizer containing suspended water insoluble nitrogen

Claim 2

A two stage process for preparing an aqueous dispersion of a urea-formaldehyde condensation product comprising: in a first stage, reacting together formaldehyde and urea in a molar ratio of formaldehyde to urea in the ratio from about 2.5 to 1 to about 4.7 to 1 in the presence of a condensation catalyst until the methanol tolerance is in the range from about 150% to about 800%, to form an intermediate reaction product, then in a second stage, reacting said intermediate reaction product with an additional amount of urea such that the overall molar ratio of urea to formaldehyde is in the range from 0.8 to 1 to about 1.7 to 1, at an acid pH and at an elevated temperature not above about 70° C., until the amount of water insoluble nitrogen present in the reaction mixture is in the range from about 15% to about 35% based on the total amount of nitrogen in the system.

Claim 3

The process of claim 1 wherein the pH throughout the first stage reaction is on the acid side.

Claim 4

The process of claim 2 wherein the molar ratio of formaldehyde to urea in the first stage reaction is in the range from about 3 to 1 to about 3.5 to 1.

Claim 5

The process of claim 1 wherein the pH during the first stage is initially alkaline so that the urea is methylolated, then acidic so that the reaction proceeds by condensation, with the elimination of water.

Claim 6

The process of claim 3 or 4 wherein the first stage reaction temperature is in the range from about 60° C. to reflux temperature.

Claim 7

The process of claim 5 wherein the intermediate reaction product produced by the first stage reaction has a methanol tolerance of about 260% or greater.

Claim 8

The process of claim 5 wherein the second stage reaction conditions are such that the water insoluble nitrogen content of the second stage reaction product is in the range from about 20% to about 30% by weight based on total available nitrogen in the second stage reaction product.

Claim 9

The process of claim 5 wherein the activity index of the second stage reaction product is in the range from about 50 to 95.

Claim 10

The process of claim 7 wherein the amount of total nitrogen in the second stage reaction product is in the range from about 15% to about 18% by weight based on the reaction product.

Claim 11

The process of claim 9 wherein the initial reactants of the second stage of the process include up to 5% by weight of dicyandiamide based on total solids in the second stage reaction mixture.

Claim 12

The process of claim 9 wherein up to 50% of the total amount of formaldehyde in the reaction product in the second stage of the process is derived from formaldehyde supplied to the second stage as a reactant, in the form of an aqueous solution at a concentration in the range from about 37% to about 55% by weight.

Claim 13

A two stage process for preparing an aqueous dispersion of a urea-formaldehyde condensation product comprising: in a first stage, reacting together formaldehyde and urea in a molar ratio of formaldehyde to urea in the ratio from about 2.5 to 1 to about 4.5 to 1 in the presence of an alkaline catalyst to methylolate the urea then reacting the material further at an acid pH until the methanol tolerance is in the range from about 150% to about 800%, to form an intermediate reaction product, then in a second stage, reacting said intermediate reaction product with an additional amount of urea such that the overall molar ratio of urea to formaldehyde is in the range from 0.8 to 1 to about 1.7 to 1, at an acid pH and at an elevated temperature not above about 70° C., until the amount of water insoluble nitrogen present in the reaction mixture is in the range from about 15% to about 35% based on the total amount of nitrogen in the system.

Claim 14

A two stage process for preparing an aqueous dispersion of a urea-formaldehyde condensation product comprising: in a first stage, reacting together formaldehyde and urea in a molar ratio of formaldehyde to urea in the ratio from about 2.5 to 1 to about 4.5 to 1 in the presence of an alkaline catalyst to methylolate the urea then reacting the material further at an acid pH until the methanol tolerance is in the range from about 150% to about 800%, to form an intermediate reaction product, then in a second stage, reacting said intermediate reaction product with an additional amount of urea such that the overall molar ratio of urea to formaldehyde is in the range from 0.8 to 1 to about 1.7 to 1, at an acid pH and at an elevated temperature not above about 70° C., until the amount of water insoluble nitrogen present in the reaction mixture is in the range from about 15% to about 35% based on the total amount of nitrogen in the system.

Claim 15

The process of claim 12 wherein the molar ratio of formaldehyde to urea in the first stage reaction is in the range from about 3 to 1 to about 3.5 to 1.

Claim 16

The process of claim 13 wherein the pH in the first stage acid reaction is in the range from 3.5 to 5.5.

Claim 17

The process of claim 14 wherein the first stage reaction temperature is in the range from about 60° C. to reflux temperature.

Claim 18

The process of claim 15 wherein the intermediate reaction product produced by the first stage reaction has a methanol tolerance of about 600%.

Claim 19

The process of claim 15 wherein the second stage reaction conditions are such that the water insoluble nitrogen content of the second stage reaction product is in the range from about 20% to about 30% by weight based on total available nitrogen in the second stage reaction product.

Claim 20

The process of claim 17 wherein the activity index of the second stage reaction product is in the range from about 50 to 95.

Claim 21

The process of claim 18 wherein the amount of total nitrogen in the second stage reaction product is in the range from about 15% to about 18% by weight based on the reaction product.

Claim 22

The process of claim 19 wherein the initial reactants of the second stage of the process include up to 5% by weight of dicyandiamide based on total solids in the second stage reaction mixture.

Claim 23

The process of claim 19 wherein up to 50% of the total amount of formaldehyde in the reaction product in the second stage of the process is derived from formaldehyde supplied to the second stage as a reactant, in the form of an aqueous solution at a concentration in the range from about 37% to about 55% by weight.

Claim 24

A two stage process for preparing an aqueous dispersion of a urea-formaldehyde condensation product comprising: in the first stage, reacting together formaldehyde and urea in a molar ratio of formaldehyde to urea in the range from about 3 to 1 to about 3.5 to 1, in the presence of an alkaline catalyst at an elevated temperature for a sufficient time to cause methylolation to occur, then continuing said reaction at an acid pH in the range from about pH 3.5 to about pH 5.5 at a temperature in the range from 60° C. to reflux, until the first stage reaction product exhibits a methanol tolerance in the range from about 500% to about 700%, then in the second stage, reacting the first stage reaction product with an additional amount of overall urea so that the urea to formaldehyde molar ratio is in the range from about 1.4 to 1 to about 1.7 to 1, at an acid pH and at an elevated temperature not above about 70° C., to achieve a level of water insoluble nitrogen in the second stage reaction product in the range from about 20% to about 30% by weight based on total nitrogen present, and an activity index in the range from about 65 to about 85, the total nitrogen content of the second stage final product being in the range from about 15% to about 18% by weight based on the total reaction product.

Claim 25

A two stage process for preparing an aqueous dispersion of a urea-formaldehyde condensation product comprising: in the first stage, reacting together formaldehyde and urea in a molar ratio of formaldehyde to urea in the range from about 3 to 1 to about 3.5 to 1, in the presence of an alkaline catalyst at an elevated temperature for a sufficient time to cause methylolation to occur, then continuing said reaction at an acid pH in the range from about pH 3.5 to about pH 5.5 at a temperature in the range from 60° C. to reflux, until the first stage reaction product exhibits a methanol tolerance in the range from about 500% to about 700%, then in the second stage, reacting the first stage reaction product with an additional amount of overall urea so that the urea to formaldehyde molar ratio is in the range from about 1.4 to 1 to about 1.7 to 1, at an acid pH and at an elevated temperature not above about 70° C., to achieve a level of water insoluble nitrogen in the second stage reaction product in the range from about 20% to about 30% by weight based on total nitrogen present, and an activity index in the range from about 65 to about 85, the total nitrogen content of the second stage final product being in the range from about 15% to about 18% by weight based on the total reaction product.

Claim 26

The process of claim 22 wherein the reactants for the second stage include dicyandiamide in an amount up to 5% by weight based on total solids present, dry basis.

Claim 27

The process of claim 22 wherein up to 50% of the formaldehyde supplied initially to the second stage as a reactant is supplied as an aqueous solution at a concentration in the range from about 37% to about 55%.

Claim 28

The process of claim 22 wherein the acid catalyzed reaction in the first stage is permitted to progress to the point where the methanol tolerance of the first stage reaction product is about 600%.

Claim 29

The process of claim 22 or 25 in which the reaction temperature in the second stage is not above 50° C.

Claim 30

The process of claim 22 or 25 wherein the second stage reaction product is formulated for fertilizer use by the addition of urea to adjust the total nitrogen content in the formulation to from about 17% to about 25% by weight based on the formulation.

Claim 31

The process of claim 27 wherein the formulation is adjusted in viscosity by the addition of a gum, so that the viscosity as measured on a Brookfield Viscometer Model LVF, spindle 2, at 30 rpm and 25° C., is in the range from about 150 cps to about 300 cps.

Claim 32

A product comprising the dispersion prepared by the process of claim 1, 4, 12, 16, 19 or 22.

Claim 33

An aqueous dispersion of a urea-formaldehyde condensation product having a molar ratio of urea to formaldehyde in the range from about 0.8 to 1 to about 1.7 to 1, in which at least 50% of the formaldehyde content of the product is supplied by a condensation product of urea and formaldehyde having a methanol tolerance in the range from about 150% to about 800%, and such that the condensation product is clear and will remain clear and substantially free from precipitated reaction material, upon storage for one year at room temperature, said dispersion being further characterized by having a viscosity in the range from about 150 cps to about 300 cps, as measured on a Brookfield Viscometer Model LVF, spindle 2, at 30 rpm and 25° C., which viscosity is stable at a temperature in the range from about 50° F. to 90° F. (10° C. to 32° C.) for at least four months when the nitrogen content of the product is in the range from about 17% to about 19% and at least two months when the total nitrogen content of the product is in the range from about 19% to about 25% by weight based on total product.

Claim 34

An aqueous dispersion of a urea-formaldehyde condensation product having a molar ratio of urea to formaldehyde in the range from about 0.8 to 1 to about 1.7 to 1, in which at least 50% of the formaldehyde content of the product is supplied by a condensation product of urea and formaldehyde having a methanol tolerance in the range from about 150% to about 800%, and such that the condensation product is clear and will remain clear and substantially free from precipitated reaction material, upon storage for one year at room temperature, said dispersion being further characterized by having a viscosity in the range from about 150 cps to about 300 cps, as measured on a Brookfield Viscometer Model LVF, spindle 2, at 30 rpm and 25° C., which viscosity is stable at a temperature in the range from about 50° F. to 90° F. (10° C. to 32° C.) for at least four months when the nitrogen content of the product is in the range from about 17% to about 19% and at least two months when the total nitrogen content of the product is in the range from about 19% to about 25% by weight based on total product.

Claim 35

An aqueous dispersion of a urea-formaldehyde condensation product having a molar ratio of urea to formaldehyde in the range from about 0.8 to 1 to about 1.7 to 1, in which at least 50% of the formaldehyde content of the product is supplied by a condensation product of urea and formaldehyde that has been alkaline methylolated and then acid reacted until the methanol tolerance is in the range from about 150% to about 800%, said dispersion being further characterized by having a viscosity in the range from about 150 cps to about 300 cps, as measured on a Brookfield Viscometer Model LVF, spindle 2, at 30 rpm and 25° C., which viscosity is stable at a temperature in the range from about 50° F. to 90° F. (10° C. to 32° C.) for at least four months when the nitrogen content of the product is in the range from about 17% to about 19% and at least two months when the total nitrogen content of the product is in the range from about 19% to about 25% by weight based on total product.

Claim 36

An aqueous dispersion of a urea-formaldehyde condensation product having a molar ratio of urea to formaldehyde in the range from about 0.8 to 1 to about 1.7 to 1, in which at least 50% of the formaldehyde content of the product is supplied by a condensation product of urea and formaldehyde that has been alkaline methylolated and then acid reacted until the methanol tolerance is in the range from about 150% to about 800%, said dispersion being further characterized by having a viscosity in the range from about 150 cps to about 300 cps, as measured on a Brookfield Viscometer Model LVF, spindle 2, at 30 rpm and 25° C., which viscosity is stable at a temperature in the range from about 50° F. to 90° F. (10° C. to 32° C.) for at least four months when the nitrogen content of the product is in the range from about 17% to about 19% and at least two months when the total nitrogen content of the product is in the range from about 19% to about 25% by weight based on total product.

Claim 37

The product of claim 31 which may contain, in reacted form therein, up to 5% by weight of total solids, dry basis, of dicyandiamide.