Production method and production apparatus of particulate water absorbing agent containing water absorbent resin as main component

• US 20110021725A1
• Filed: 03/31/2009
• Published: 01/27/2011
• Est. Priority Date: 03/31/2008
• Status: Active Grant

• Current Assignee: Nippon Shokubai Company Limited
• Original Assignee: Nippon Shokubai Company Limited
• Inventors: Takaai, Toshihiro, Fujino, Shinichi, Dairoku, Yorimichi
• Granted Patent: US 8,420,752 B2
• Time in Patent Office: Days
• US Class Current: 526/64
• CPC Class Codes: A61L 15/60 Liquid-swellable gel-forming materials, e.g. super-absorbents
• CPC Class Codes: B01J 19/0086 Processes carried out with a view to control or to change the pH-value; Applications of buffer salts; Neutralisation reactions
• CPC Class Codes: B01J 2219/00006 Large-scale industrial plants
• CPC Class Codes: C07C 51/41 Preparation of salts of carboxylic acids C07C51/093 - C07C51/34 take precedence preparation of soap C11D
• CPC Class Codes: C07C 51/50 Use of additives, e.g. for stabilisation
• CPC Class Codes: C08F 2/10 Aqueous solvent
• CPC Class Codes: C08F 2/48 by ultraviolet or visible light
• CPC Class Codes: C08F 20/06 Acrylic acid; Methacrylic acid; Metal salts or ammonium salts thereof
• CPC Class Codes: C08F 220/06 Acrylic acid; Methacrylic acid; Metal salts or ammonium salts thereof
• CPC Class Codes: C08J 2333/02 Homopolymers or copolymers of acids; Metal or ammonium salts thereof
• CPC Class Codes: C08J 3/245 Differential crosslinking of one polymer with one crosslinking type, e.g. surface crosslinking
• CPC Class Codes: Y10T 137/4673 Plural tanks or compartments with parallel flow
• CPC Class Codes: Y10T 137/469 Sequentially filled and emptied [e.g., holding type]
• CPC Class Codes: Y10T 137/86187 Plural tanks or compartments connected for serial flow

Abstract

An apparatus (2) includes a neutralization tank (3), a pump (4), a heat exchanger (6), a line mixer (8), a polymerizer (10), a first pipe (12), a second pipe (14), a third pipe (16), a fourth pipe (18), and a fifth pipe (20). Continuously supplied into the neutralization tank (3) are a monomer aqueous solution and a basic aqueous solution, so as to prepare a mixture solution. The mixture solution is circulated through the first pipe (12), the pump (4), the second pipe (14), the heat exchanger (6), and the third pipe (16). The mixture solution is supplied to the polymerizer through the fourth pipe (18). The apparatus (2) satisfies a requirement that a value X is not more than 200, which value X is found according to the following expression: “X=(V/F)·A”, wherein V is a volume of the mixture solution present in a neutralization system, F is a flow volume of the mixture solution to be supplied to a polymerization system, and A is a contact area of the mixture solution present in the neutralization system with a device(s) and a pipe(s) constituting the neutralization system. With this arrangement, it is possible to provide a water absorbent resin having superior whiteness.

Claims

1. A method for producing a particulate water absorbing agent, said method comprising the steps of:

(a) circulating, in a neutralization system including a neutralization tank, a mixture solution containing an acid group-containing monomer and salt obtained by a neutralization reaction of the acid-containing monomer with a basic material;

(b) continuously supplying, to a polymerization system, a part of the mixture solution that is being circulated; and

(c) polymerizing a monomer component of the mixture solution in the polymerization system,

the method satisfying a requirement that a value X is not more than 200, the value X being found according to the following expression;

X=(V/F)·

A

wherein V (kg) is a volume of the mixture solution present in the neutralization system, F (kg/h) is a flow volume of the mixture solution to be supplied to the polymerization system, and A(m²) is a contact area of the mixture solution present in the neutralization system with a device(s) and a pipe(s) constituting the neutralization system.

2. The method as set forth in claim 1, wherein:

a residence time (V/F) of the mixture solution in the neutralization system is not more than 10 hours.

3. The method as set forth in claim 1, wherein:

the flow volume F is not less than 100 kg/h.

4. The method as set forth in claim 1, wherein the mixture solution in the neutralization tank has a monomer concentration of 30 mass % to 70 mass %.

5. The method as set forth in claim 1, further comprising, between the steps (b) and (c), the step of:

(d) adding a basic material to the mixture solution so as to increase a neutralization ratio of the mixture solution.

6. The method as set forth in claim 5, wherein the mixture solution has a neutralization ratio of 30 mol % to 90 mol % right after the step (d).

7. The method as set forth in claim 1, wherein the mixture solution in the neutralization system is circulated through the neutralization tank and a closed flow channel attached to the neutralization tank.

8. The method as set forth in claim 1, wherein:

the neutralization system includes the neutralization tank, a first loop, and a second loop;

the mixture solution in the neutralization tank is circulated through the first loop;

the mixture solution is drawn from the neutralization tank or the first loop into the second loop so that the mixture solution is carried through the second loop to a place closer to the polymerization system than to the first loop; and

the mixture solution then returns back through the second loop to the neutralization tank or the first loop.

10. The method as set forth in claim 1, wherein the acid group-containing monomer is acrylic acid and the acrylic acid contains a polymerization inhibitor by 1 ppm to 200 ppm.

11. The method as set forth in claim 1, wherein:

the acid group-containing monomer is acrylic acid;

the acrylic acid is purified by crystallization or distillation; and

the acrylic acid is then supplied to the neutralization system within 96 hours after the purification.

12. The method as set forth in claim 1, wherein:

the acid group-containing monomer is acrylic acid; and

the neutralization system is connected to a production facility of the acrylic acid via a pipe.

13. The method as set forth in claim 1, wherein the polymerization system carries out continuous kneader polymerization or continuous belt polymerization.

9. A method for producing a water absorbent resin, said method comprising the steps of:

(1) in a neutralization system including a neutralization tank, a first loop, and a second loop, circulating through the first loop a mixture solution which is present in the neutralization tank and which contains an acid group-containing monomer and salt obtained by a neutralization reaction of the acid group-containing monomer with a basic material;

(2) causing the mixture solution to be drawn from the neutralization tank or the first loop into the second loop so that the mixture solution is carried through the second loop to a place closer to a polymerization system than to the first loop, and then causing the mixture solution to return back through the second loop to the neutralization tank or the first loop; and

(3) continuously supplying the mixture solution from the neutralization system to the polymerization system.

18. The method as set forth in claim 9, wherein the acid group-containing monomer is acrylic acid and the acrylic acid contains a polymerization inhibitor by 1 ppm to 200 ppm.

19. The method as set forth in claim 9, wherein:

the acid group-containing monomer is acrylic acid;

the acrylic acid is purified by crystallization or distillation; and

the acrylic acid is then supplied to the neutralization system within 96 hours after the purification.

20. The method as set forth in claim 9, wherein:

the acid group-containing monomer is acrylic acid; and

the neutralization system is connected to a production facility of the acrylic acid via a pipe.

21. The method as set forth in claim 9, wherein the polymerization system carries out continuous kneader polymerization or continuous belt polymerization.

14. A production apparatus for producing a water absorbent resin, said production apparatus comprising:

a neutralization system;

a polymerization system; and

a pipe connecting the neutralization system to the polymerization system,

the neutralization system including;

a neutralization tank in which to store a mixture solution containing an acid group-containing monomer and salt obtained by a neutralization reaction of the acid group-containing monomer with a basic material;

a first loop for drawing the mixture solution from the neutralization tank and for returning the mixture solution back to the neutralization tank; and

a second loop for drawing the mixture solution from the neutralization tank or the first loop so that the mixture solution is carries through the second loop to a place closer to the polymerization system than to the first loop, and for retuning the mixture solution back to the neutralization tank or the first loop,

the mixture solution being continuously supplied from the neutralization system to the polymerization system via the pipe,

said production apparatus satisfying a requirement that a value X is not more than 200, the value X being found according to the following expression;

X=(V/F)·

A

wherein V (kg) is a volume of the mixture solution present in the neutralization system, F (kg/h) is a flow volume of the mixture solution to be supplied to the polymerization system, and A(m²) is a contact area of the mixture solution present in the neutralization system with a device(s) and a pipe(s) constituting the neutralization system.

15. The production apparatus as set forth in claim 14, wherein the acid group-containing monomer and a mixture solution of the basic material and water are continuously supplied to the first loop.

16. The production apparatus as set forth in claim 14, wherein:

a headspace in the neutralization tank has a volume of 50% to 90% with respect to a volume of the neutralization tank; and

the headspace is sealed with mixed gas of oxygen and inactive gas in which mixed gas an oxygen concentration is adjusted in advance.

17. The production apparatus as set forth in claim 14, wherein the neutralization system further includes a pipe that is connected to a production facility of the acid group-containing monomer.