Method of and apparatus for producing a foam-forming reaction mixture

Claim 1

A method of producing a foam-forming reaction mixture from at lest two liquid components which react with each other and which are continuously fed to a mixing zone where they are mixed together and wherein the volumetric flow of at least one component is measured continuously, comprising (A) dividing the flow of components from a storage container into a main stream and a subsidiary stream; (B) adjusting the subsidiary stream to the same working pressure as that of the main stream just before the main stream's introduction into a mixing zone; (C) measuring the volumetric flow of the subsidiary stream which passes through during a predetermined time interval; (D) determining the weight of mixture which has passed through during the same predetermined time interval; (E) determining the density of the component therefrom as the quotient of said weight and said volume; (F) measuring the volumetric flow of the main stream; and determining the mass flow of the main stream of the component as the product of the density of the component determined in step (E) and the volumetric flow of the main stream. (G) Comparing the determined value of the mass flow of the main stream with a predetermined desired value.

Claim 2

A method of producing a foam-forming reaction mixture from at lest two liquid components which react with each other and which are continuously fed to a mixing zone where they are mixed together and wherein the volumetric flow of at least one component is measured continuously, comprising (A) dividing the flow of components from a storage container into a main stream and a subsidiary stream; (B) adjusting the subsidiary stream to the same working pressure as that of the main stream just before the main stream's introduction into a mixing zone; (C) measuring the volumetric flow of the subsidiary stream which passes through during a predetermined time interval; (D) determining the weight of mixture which has passed through during the same predetermined time interval; (E) determining the density of the component therefrom as the quotient of said weight and said volume; (F) measuring the volumetric flow of the main stream; and determining the mass flow of the main stream of the component as the product of the density of the component determined in step (E) and the volumetric flow of the main stream. (G) Comparing the determined value of the mass flow of the main stream with a predetermined desired value.

Claim 3

An apparatus for producing a foam forming reaction mixture comprising storage containers for the reaction components; feed pipes which lead from the storage containers via metering pumps to a mixhead; a volumetric flow counter arranged in at least one feed pipe between the metering pump and the mixhead; a subsidiary pipe branched off upstream of said metering pump leading to a subsidiary pump; a volumetric flow counter downstream from said subsidiary pump; a throttle valve downstream from said volumetric flow counter; a changeover valve provided with two outlets arranged downstream from the throttle valve; a return pipe leading from one outlet of the changeover valve and a connecting pipe leading from the other outlet of the changeover valve to a weighing arrangement; a weighing arrangement comprising a measuring cylinder; pressure measuring instruments, one arranged in the feed pipe adjacent and downstream of the metering pump and one in the subsidiary pipe adjacent and downstream of the subsidiary pump; means for determining the density as the quotient of the weight measured in said weighing arrangement and the volume flow flowing through said volume at the flow counter which is downstream from said subsidiary pump; and, means for determining the mass flow as the product of the density determined by said density determining means and the volumetric flow flowing through said volumetric flow counter arranged in at least one feed pipe.

Claim 4

An apparatus for producing a foam forming reaction mixture comprising storage containers for the reaction components; feed pipes which lead from the storage containers via metering pumps to a mixhead; a volumetric flow counter arranged in at least one feed pipe between the metering pump and the mixhead; a subsidiary pipe branched off upstream of said metering pump leading to a subsidiary pump; a volumetric flow counter downstream from said subsidiary pump; a throttle valve downstream from said volumetric flow counter; a changeover valve provided with two outlets arranged downstream from the throttle valve; a return pipe leading from one outlet of the changeover valve and a connecting pipe leading from the other outlet of the changeover valve to a weighing arrangement; a weighing arrangement comprising a measuring cylinder; pressure measuring instruments, one arranged in the feed pipe adjacent and downstream of the metering pump and one in the subsidiary pipe adjacent and downstream of the subsidiary pump; means for determining the density as the quotient of the weight measured in said weighing arrangement and the volume flow flowing through said volume at the flow counter which is downstream from said subsidiary pump; and, means for determining the mass flow as the product of the density determined by said density determining means and the volumetric flow flowing through said volumetric flow counter arranged in at least one feed pipe.

Claim 7

An apparatus according to claims 2 or 3, wherein the weighing arrangement comprises a closed measuring cylinder with a rectangular perimeter which is confined from lateral movement by but can move vertically through a set of rollers; the measuring cylinder having inlet and outlet parts in the lower region for the subsidiary stream of the components and an air connection opening into the upper region; the upper region of air being separated from the lower region of liquid component by a plate floating on the liquid component.