Process for mitigating scale formation in tube reaction apparatus

Claim 2

A process for inhibiting scale formation in a continuous plug flow vertical tube waste reactor of the type in which liquid waste that contains scale-forming dissolved ions is injected into said reactor as an influent waste stream under heat and pressure to bring about a wet oxidation reaction within said liquid waste in a reaction zone in said reactor to break down said liquid waste into simpler components which are discharged from said reactor as an effluent waste stream, the process comprising adding a quantity of precipitating reagent to said liquid waste before said liquid waste enters said reaction zone and at a temperature significantly below the temperature of said reaction zone to form precipitates containing said ions which would otherwise accumulate as scale on the walls of said reactor.

Claim 3

The process for inhibiting scale formation recited in claim 1, wherein said precipitating reagent is a composition which forms precipitates with calcium, aluminum and magnesium ions and wherein said precipitates remain in suspension in said liquid waste.

Claim 4

The process for inhibiting scale formation recited in claim 1, wherein said quantity of precipitating reagent is at least equal to the quantity stoichiometrically required to bind all of said scale-forming ions in said liquid waste.

Claim 5

The process for inhibiting scale formation recited in claim 1, wherein said precipitating reagent is selected from the group consisting of phosphate ion producing compounds and oxalate ion producing compounds and combinations thereof.

Claim 6

The process for inhibiting scale formation recited in claim 1, wherein said precipitating reagent is selected from the group consisting of trisodium phosphate, a mixture of phosphoric acid and sodium hydroxide, and a mixture of oxalic acid and sodium hydroxide, and combinations thereof.

Claim 7

The process for inhibiting scale formation recited in claim 1, further comprising mixing said liquid waste after it is combined with said precipitating reagent to intimately contact said precipitating reagent with said scale-forming ions in said liquid waste.

Claim 8

The process for inhibiting scale formation recited in claim 6, wherein said mixing is achieved by adding said precipitating reagent to said liquid waste and bubbling a gaseous stream through said liquid waste to cause said precipitating reagent to be substantially uniformly distributed throughout said liquid waste.

Claim 9

The process for inhibiting scale formation recited in claim 7, wherein said gaseous stream includes a gas selected from the group consisting of air and oxygen.

Claim 10

The process for inhibiting scale formation recited in claim 1, wherein said precipitating reagent forms said precipitates with said ions when the temperature of said influent waste stream is less than that temperature at which said scale forms on said reactor walls.

Claim 11

A process for continuously inhibiting the growth of chemical scale on the walls of a continuous flow tube reactor of the type in which liquid waste is introduced as an influent waste stream to form a plug flow of liquid waste at elevated temperature and pressure to cause said liquid waste to react in a reaction zone to form more environmentally desirable components which are then carried out of said reactor as an effluent waste stream and wherein said liquid waste of said influent stream contains ions of calcium, aluminum and magnesium in solution, the process comprising the steps of: (a) analyzing said influent stream to determine the concentration of calcium, aluminum and magnesium present; (b) substantially continuously adding to said influent stream a precipitating reagent which forms precipitates with said calcium, aluminum and magnesium ions at a temperature below about 300° F. in a quantity substantially equal to the stoichiometric quantity required to bond all of the calcium, aluminum and magnesium determined in step (a) to be present in said influent waste stream; (c) analyzing said effluent stream to determine the concentration of calcium, aluminum and magnesium present; (d) comparing the concentration data obtained in step (a) with the concentration data obtained in step (c) (e) adjusting the quantity of precipitating reagent that is substantially continuously added to said influent waste stream and repeating steps (c), (d) and (e) until the concentration of calcium, aluminum, and magnesium in said effluent stream is substantially equal to the concentration of calcium, aluminum and magnesium in said influent stream.

Claim 12

A process for continuously inhibiting the growth of chemical scale on the walls of a continuous flow tube reactor of the type in which liquid waste is introduced as an influent waste stream to form a plug flow of liquid waste at elevated temperature and pressure to cause said liquid waste to react in a reaction zone to form more environmentally desirable components which are then carried out of said reactor as an effluent waste stream and wherein said liquid waste of said influent stream contains ions of calcium, aluminum and magnesium in solution, the process comprising the steps of: (a) analyzing said influent stream to determine the concentration of calcium, aluminum and magnesium present; (b) substantially continuously adding to said influent stream a precipitating reagent which forms precipitates with said calcium, aluminum and magnesium ions at a temperature below about 300° F. in a quantity substantially equal to the stoichiometric quantity required to bond all of the calcium, aluminum and magnesium determined in step (a) to be present in said influent waste stream; (c) analyzing said effluent stream to determine the concentration of calcium, aluminum and magnesium present; (d) comparing the concentration data obtained in step (a) with the concentration data obtained in step (c) (e) adjusting the quantity of precipitating reagent that is substantially continuously added to said influent waste stream and repeating steps (c), (d) and (e) until the concentration of calcium, aluminum, and magnesium in said effluent stream is substantially equal to the concentration of calcium, aluminum and magnesium in said influent stream.

Claim 13

The process recited in claim 10, wherein the quantity of precipitating reagent which is added to said influent waste stream is from about 100% to about 125% of the stoichiometric concentration required to bind all of the calcium present in said influent waste stream.

Claim 14

The process recited in claim 10, further comprising the step of mixing said influent waste stream between steps (b) and (c) to promote the reaction of said precipitating reagent with said calcium ions.

Claim 15

A process for the wet oxidation of liquid municipal waste in a vertical tube waste reactor of the type having a series of concentric reactor tubes partially buried vertically in the ground in which the formation of salt scale on the reactor walls is inhibited comprising adding a composition to said liquid municipal waste which binds scale-forming ions present in said waste before said waste undergoes wet oxidation in said vertical tube waste reactor.

Claim 16

A process for the wet oxidation of liquid municipal waste in a vertical tube waste reactor of the type having a series of concentric reactor tubes partially buried vertically in the ground in which the formation of salt scale on the reactor walls is inhibited comprising adding a composition to said liquid municipal waste which binds scale-forming ions present in said waste before said waste undergoes wet oxidation in said vertical tube waste reactor.

Claim 17

In a fluid waste treatment apparatus of the type in which fluid waste containing scale-forming ions enters a reaction zone where it is reacted with an oxidizing gas at an elevated temperature to produce a wet oxidation reaction to form a treated fluid waste, a process for inhibiting the formation of scale on the surfaces of the fluid waste treatment apparatus, the process comprising the steps of: (a) introducing the fluid waste into the fluid waste treatment apparatus as an influent fluid waste stream; (b) adding to the fluid waste a quantity of precipitating reagent sufficient to form substantially insoluble suspended precipitates with the scale-forming ions in the fluid waste before said fluid waste enters said reaction zone; (c) adding the oxidizing gas to the fluid waste to participate in the wet oxidation reaction; (d) flowing the influent fluid waste stream containing the precipitants and the oxidizing gas through the fluid waste treatment apparatus to the reaction zone; (e) reacting the fluid waste with the oxidizing gas in the reaction zone by increasing the temperature of the influent fluid waste stream in the reaction zone to produce the wet oxidation reaction; (f) removing the treated fluid waste containing the suspended precipitates from the fluid waste treatment apparatus as an effluent waste stream; whereby said scale-forming ions are bound as said insoluble precipitates by said precipitating reagent and are carried in suspension through said waste treatment apparatus so that said scale-forming ions cannot combine to form scale on the surfaces of said waste treatment apparatus.

Claim 18

In a fluid waste treatment apparatus of the type in which fluid waste containing scale-forming ions enters a reaction zone where it is reacted with an oxidizing gas at an elevated temperature to produce a wet oxidation reaction to form a treated fluid waste, a process for inhibiting the formation of scale on the surfaces of the fluid waste treatment apparatus, the process comprising the steps of: (a) introducing the fluid waste into the fluid waste treatment apparatus as an influent fluid waste stream; (b) adding to the fluid waste a quantity of precipitating reagent sufficient to form substantially insoluble suspended precipitates with the scale-forming ions in the fluid waste before said fluid waste enters said reaction zone; (c) adding the oxidizing gas to the fluid waste to participate in the wet oxidation reaction; (d) flowing the influent fluid waste stream containing the precipitants and the oxidizing gas through the fluid waste treatment apparatus to the reaction zone; (e) reacting the fluid waste with the oxidizing gas in the reaction zone by increasing the temperature of the influent fluid waste stream in the reaction zone to produce the wet oxidation reaction; (f) removing the treated fluid waste containing the suspended precipitates from the fluid waste treatment apparatus as an effluent waste stream; whereby said scale-forming ions are bound as said insoluble precipitates by said precipitating reagent and are carried in suspension through said waste treatment apparatus so that said scale-forming ions cannot combine to form scale on the surfaces of said waste treatment apparatus.

Claim 19

The process for inhibiting the formation of scale on the surfaces of a fluid waste treatment apparatus recited in claim 14, wherein said precipitating reagent added to said fluid waste in step (b) is selected from the group consisting of trisodium phosphate and sodium oxalate.

Claim 20

The process for inhibiting the formation of scale on the surfaces of a fluid waste treatment apparatus recited in claim 14, wherein said oxidizing gas is selected from the group consisting of oxygen and air.

Claim 21

The process for inhibiting the formation of scale on the surfaces of a fluid waste treatment apparatus recited in claim 14, further comprising the step of mixing said fluid waste containing said precipitating reagent following step (b) to intimately contact said precipitating reagent and said scale-forming ions to precipitate substantially all of said scale-forming ions.

Claim 22

The process for inhibiting the formation of scale on the surfaces of a fluid waste treatment apparatus recited in claim 14, wherein said oxidizing gas added in step (c) is bubbled as a gaseous stream into said fluid waste to intermix said oxidizing gas and said fluid waste.

Claim 23

The process for inhibiting the formation of scale on the surfaces of a fluid waste treatment apparatus recited in claim 14, wherein said reacting step (e) takes place when the temperature of said fluid waste is less than that temperature at which scale forms on said surfaces of said fluid waste treatment apparatus.