Silica gel of improved properties and process of making same

Claim 2

In a process of producing silica gel, including the steps of precipitating a silicic acid-containing starting materials and acid reactant to first form an unstable silicic acid containing sol as an intermediate product, subsequently gelling the sol, washing the gel to remove the salts, and drying the gel, the improvements which comprise carrying out the precipitation process in two steps, wherein in the first step a first silicic acid-containing starting material with a silicon dioxide content between about 20% and about 32% by weight is introduced in such a fine distribution and at such a high discharge velocity into the acid reactant, while being subjected to high speed agitation, until a pH-value of the acid reactant between about 1.5 and about 1.8 is attained, that instantaneous reaction between the acid and the silicic acid containing starting material takes place without any precipitation of silicic acid, and wherein in the second precipitation step a second silicic acid-containing starting material having a silicon dioxide content between about 8% and about 14% by weight is introduced into the acid reactant until a pH-value of between about 2.6 and about 3.5 is attained, thereby producing a sol having a silicon dixoide content of about 14% to about 18% by weight, and carrying out the washing step by washing with a washing liquid of a pH between about 1.8 and about 12.0.

Claim 3

The process according to claim 1, in which the gelling step subsequent to the precipitation step includes the steps of simultaneous preliminary drying and gelling by conducting the sol in a thin layer through a conveyer belt drier.

Claim 4

The process according to claim 2, in which the belt of the conveyer belt drier comprises a plurality of mold elements for pre-shaping the gel into individual units of predetermined shape.

Claim 5

The process according to claim 3, in which a covering belt is assigned to said conveyer belt and both belts comprise elastic rubber or elastic plastic material, each conveyer belt having on its upper surface hemispherical recesses which are open at the top and each covering belt having hemispherical recesses at its lower surface which are open at the bottom, said recesses being of a diameter between about 15 mm. and about 28 mm.

Claim 6

The process according to claim 4, wherein said diameter is between about 22 mm and about 25 mm.

Claim 7

The process according to claim 2, in which the conveyer belt drier comprises lateral walls and transversely arranged ribs of plastic material, the conveyer belt of said conveyer belt drier comprising a chromium-nickel-steel belt, and wherein said washing and drying steps are carried out in a container, said container having an intermediate bottom with a bottom valve and being subdivided by said intermediate bottom into two container compartments, the upper compartment serving as washing container and the lower compartment as drier.

Claim 8

The process according to claim 1, wherein sai gelling step comprises gelling said sol in a plurality of hollow mold elements to form individual gel units of predetermined shape.

Claim 9

The process according to claim 7, wherein the shape of the mold elements is at least partly spherical.

Claim 10

The process according to claim 8, wherein the shape of the mold elements is spherical.

Claim 11

The process according to claim 8, wherein the shape of the mold elements is at least semi-spherical.

Claim 12

The process according to claim 1, wherein the acid reactant comprises sulfuric acid or hydrochloric acid.

Claim 13

The process according to claim 11, wherein the acid reactant comprises sulfuric acid containing between about 1% and about 5% sodium sulfate.

Claim 14

The process according to claim 11, wherein the acid reactant comprises hydrochloric acid containing between about 1% and about 5% sodium chloride.

Claim 15

The process of claim 1, wherein said steps of gelling and washing are carried out in a container having an intermediate bottom with a bottom valve, said container thus being subdivided into two container compartments, the upper compartment serving as gelling container while the lower compartment is constructed as washing and drying container.

Claim 16

The process according to claim 14, wherein said water glass solution is produced by reacting quartz sand with an at least 50% sodium hydroxide solution at a temperature between about 130° C. and about 180° C. and under a pressure between about 4 atm.gauge and about 12 atm.gauge.

Claim 17

The process according to claim 1, in which precipitation is effected batchwise in a precipitation container and further comprising maintaining the temperature of the reactants in the container below 20° C.

Claim 18

The process according to claim 16, wherein said cooling step comprises circulating the mixture of reactants through a cooling device.

Claim 19

The process of claim 1, in which the silicic acid containing starting material used for precipitation comprises a water glass solution having a ratio of sodium oxide to silicon dioxide between about 1.0:3.5 and about 1.0:5.0.

Claim 20

The process according to claim 1, wherein precipitation in the second precipitation step is continued only until the solution has attained a pH of about 3.0, and further comprising conducting a third precipitation step wherein there is introduced into the acid reactant a third silicic acid-containing starting material having a silicon dioxide content between about 5% and about 8% by weight.

Claim 21

The process according to claim 1, wherein precipitation is effected continuously in troughs arranged one after the other, in which the mixture of acid and silicic acid-containing starting materials during a first precipitation step remains in a first trough not longer than about 3 minutes and in the second precipitation step in a second trough for not more than about 2 minutes.

Claim 22

The process according to claim 1, in which removal of the salts by washing the gel is carried out with a washing liquid at an initial temperature of 15° C. which temperature is successively increased to a temperature of 50° C.

Claim 23

The process according to claim 1, wherein the first silicic acid-containing starting material is injected below the surface of the acid reactant.

Claim 24

The process according to claim 1, wherein the silicic acid-containing starting material is in each case a water glass solution.

Claim 25

The process according to claim 1, wherein the first silica acid-containing starting material contains about 32% by weight silicon dioxide and the acid reactant comprises a sulfuric acid solution having a sulfuric acid content of from about 10% to 12%.

Claim 26

The process according to claim 1, wherein the temperature of the acid reactant is maintained at a temperature below 20° C. during the precipitation step.

Claim 27

The process according to claim 1, wherein the washing step is carried out with a washing liquid having a pH between about 1.8 and 2.5.

Claim 28

The process according to claim 1, wherein the washing step is carried out with a washing liquid having a pH between about 2.5 and 3.5.

Claim 29

The process according to claim 1, wherein the washing step is carried out with a washing liquid having a pH between about 5 and 6.

Claim 30

The process according to claim 1, wherein the washing step is carried out with a washing liquid having a pH between about 7 and 8.

Claim 31

The process according to claim 1, wherein the washing step is carried out with a washing liquid having a pH between about 8 and 10.

Claim 32

The process according to claim 1, wherein the washing step is carried out with a washing liquid having a pH between about 10 and 12.

Claim 33

A process for producing silica gel, comprising the steps of: introducing a first water glass solution into an acid reactant in such a finely divided distribution and at such a velocity that instantaneous reaction between the water glass and acid takes place without any precipitation of silicic acid under agitation conditions of said acid reactant, said first water glass solution having a molar ratio of sodium oxide to silicon dioxide between about 1:3.5 and 1:5 and a silicon dioxide content of between about 20% and about 32% by weight, said introduction being continued until a pH value of the acid reactant between about 1.5 and about 1.8 is attained, the temperature of the acid reactant being maintained at a temperature less than about 20° C. during said introduction; after reaching the aforesaid pH value, introducing into said acid reactant a second water glass solution having a molar ratio of sodium oxide to silicon dioxide between about 1:3.5 and 1:5 and a silicon dioxide content of between about 8% and about 14% by weight until a pH value of the acid reactant between about 2.6 and about 3.5 is attained, whereby there is produced a sol having a silicon dioxide content of from about 14% to about 18% by weight; simultaneously gelling and pre-drying the sol; washing the pre-dried gel with a wash liquid having a pH value of between about 1.8 and about 12; and drying the washed gel with an atmosphere having a relative humidity of at least from about 80% to 90%.

Claim 34

A process for producing silica gel, comprising the steps of: introducing a first water glass solution into an acid reactant in such a finely divided distribution and at such a velocity that instantaneous reaction between the water glass and acid takes place without any precipitation of silicic acid under agitation conditions of said acid reactant, said first water glass solution having a molar ratio of sodium oxide to silicon dioxide between about 1:3.5 and 1:5 and a silicon dioxide content of between about 20% and about 32% by weight, said introduction being continued until a pH value of the acid reactant between about 1.5 and about 1.8 is attained, the temperature of the acid reactant being maintained at a temperature less than about 20° C. during said introduction; after reaching the aforesaid pH value, introducing into said acid reactant a second water glass solution having a molar ratio of sodium oxide to silicon dioxide between about 1:3.5 and 1:5 and a silicon dioxide content of between about 8% and about 14% by weight until a pH value of the acid reactant between about 2.6 and about 3.5 is attained, whereby there is produced a sol having a silicon dioxide content of from about 14% to about 18% by weight; simultaneously gelling and pre-drying the sol; washing the pre-dried gel with a wash liquid having a pH value of between about 1.8 and about 12; and drying the washed gel with an atmosphere having a relative humidity of at least from about 80% to 90%.

Claim 35

The process according to claim 32, wherein said simultaneous gelling and predrying step is carried out at a temperature of from about 50° C. to about 70° C.

Claim 36

The process according to claim 33, wherein said simultaneous gelling and predrying step is carried out until a water content of the gel of about 15% is attained.

Claim 37

The process according to claim 34, wherein said simultaneous gelling and predrying step is carried out by arranging the sol in layers of from about 500 mm to 1500 mm in thickness.

Claim 38

The process according to claim 35, wherein said drying step is carried out in a first stage with air at a temperature not initially exceeding about 60° C. and during the course of the first stage not exceeding about 80° C.

Claim 39

The process according to claim 36, wherein said drying step further comprises a second stage wherein air having a temperature between about 120° C. and 140° C. is employed.

Claim 40

The process according to claim 37, wherein in said washing step the wash liquid has a pH value of between about 7 and 11 and the temperature of the wash liquid is initially at least about 15° C. and is increased to a temperature of about 50° C.

Claim 41

Silica gel having a silicon dioxide content of between about 16% and about 24%, a pore diameter of between about 20 and about 25 Angstroem, a wetting heat of between about 32 and about 35 cal./g., a bulk weight between about 720 and about 770 g./cm. 3 , an adsorption temperature of up to about 100° C. and a desorption temperature of between about 150° C. and about 200° C.

Claim 42

Silica gel having a silicon dioxide content of between about 16% and about 24%, a pore diameter of between about 20 and about 25 Angstroem, a wetting heat of between about 32 and about 35 cal./g., a bulk weight between about 720 and about 770 g./cm. 3 , an adsorption temperature of up to about 100° C. and a desorption temperature of between about 150° C. and about 200° C.

Claim 43

The silica gel of claim 39, said gel being produced by the process of claim 26.

Claim 44

Silica gel having a silicon dioxide content between about 16% and about 24%, a pore diameter of between about 25 and 30 Angstroem, a wetting heat of between about 26 and about 30 cal./g., a bulk weight between about 680 and about 720 g./cm. 3 , an adsorption temperature of up to about 80° and a desorption temperature of between about 120° C. and about 150° C.

Claim 45

Silica gel having a silicon dioxide content between about 16% and about 24%, a pore diameter of between about 25 and 30 Angstroem, a wetting heat of between about 26 and about 30 cal./g., a bulk weight between about 680 and about 720 g./cm. 3 , an adsorption temperature of up to about 80° and a desorption temperature of between about 120° C. and about 150° C.

Claim 46

The silica gel of claim 41, said gel being produced by the process of claim 26.

Claim 47

Silica gel having a silicon dioxide content between about 16% and about 24%, a pore diameter of between about 30 and about 40 Angstroem, a wetting heat of between about 18 and about 22 cal./g., a bulk weight between about 560 and about 680 g./cm. 3 , an adsorption temperature of up to about 60° and a desorption temperature of between about 80° C. and about 100° C.

Claim 48

Silica gel having a silicon dioxide content between about 16% and about 24%, a pore diameter of between about 30 and about 40 Angstroem, a wetting heat of between about 18 and about 22 cal./g., a bulk weight between about 560 and about 680 g./cm. 3 , an adsorption temperature of up to about 60° and a desorption temperature of between about 80° C. and about 100° C.

Claim 49

The silica gel of claim 43, said gel being produced by the process of claim 28.

Claim 50

Silical gel having a silicon dioxide content between about 16% and about 24%, a pore diameter of between about 40 and about 50 Angstroem, a wetting heat of between about 15 and about 18 cal./g., a bulk weight between about 460 and about 520 g./cm. 3 , an adsorption temperature of up to about 40° and a desorption temperature of between about 50° C. and about 70° C.

Claim 51

Silical gel having a silicon dioxide content between about 16% and about 24%, a pore diameter of between about 40 and about 50 Angstroem, a wetting heat of between about 15 and about 18 cal./g., a bulk weight between about 460 and about 520 g./cm. 3 , an adsorption temperature of up to about 40° and a desorption temperature of between about 50° C. and about 70° C.

Claim 52

The silica gel of claim 45, said gel being produced by the process of claim 29.

Claim 53

Silica gel having a silicon dioxide content between about 16% and about 24%, a pore diameter of between about 50 and about 60 Angstroem, a wetting heat of between about 12 and about 15 cal./g., a bulk weight between about 300 and about 460 g./cm. 3 , an adsorption temperature of up to about 30° and a desorption temperature of between about 40° C. and about 60° C.

Claim 54

Silica gel having a silicon dioxide content between about 16% and about 24%, a pore diameter of between about 50 and about 60 Angstroem, a wetting heat of between about 12 and about 15 cal./g., a bulk weight between about 300 and about 460 g./cm. 3 , an adsorption temperature of up to about 30° and a desorption temperature of between about 40° C. and about 60° C.

Claim 55

The silica gel of claim 47, said gel being produced by the process of claim 30.

Claim 56

Silica gel having a silicon dioxide content between about 16% and about 24%, a pore diameter of between about 60 and about 70 Angstroem, a wetting heat of between about 10 and about 12 cal./g., a bulk weight between about 250 and about 350 g./cm. 3 , an adsorption temperature of up to about 20° and a desorption temperature of between about 30° C. and about 50° C.

Claim 57

Silica gel having a silicon dioxide content between about 16% and about 24%, a pore diameter of between about 60 and about 70 Angstroem, a wetting heat of between about 10 and about 12 cal./g., a bulk weight between about 250 and about 350 g./cm. 3 , an adsorption temperature of up to about 20° and a desorption temperature of between about 30° C. and about 50° C.

Claim 58

The silica gel of claim 49, said gel being produced by the process of claim 31.

Claim 59

The silica gel of claim 49, further characterized by the ability to adsorb up to 80% of its weight of water at a temperature between about 0° C. and about 20° C. and by a desorption effectiveness of from about 95% to about 98% at a temperature between about 50° C. and about 55° C.