Catalysts for the dehydration of hydroxypropionic acid and its derivatives

• US 9,849,447 B2
• Filed: 08/29/2016
• Issued: 12/26/2017
• Est. Priority Date: 08/28/2015
• Status: Active Grant

• Current Assignee: The Procter & Gamble Company
• Original Assignee: The Procter & Gamble Company
• Inventors: Velasquez, Juan Esteban, Collias, Dimitris Ioannis, Godlewski, Jane Ellen
• Primary Examiner(s): Hailey, Patricia L
• Application Number:
  US15/249,712
• Publication Number:
  US 20170056863A1
• Time in Patent Office: 484 Days
• Field of Search: 502208-214
• CPC Class Codes: B01J 23/20 Vanadium, niobium or tantalum
• CPC Class Codes: B01J 27/16 containing oxygen , i.e. acids, anhydrides and their derivates with N, S, B or halogens without carriers or on carriers based on C, Si, Al or Zr; also salts of Si, Al and Zr
• CPC Class Codes: B01J 27/18 with metals other than Al or Zr
• CPC Class Codes: B01J 27/1806 with alkaline or alkaline earth metals
• CPC Class Codes: B01J 27/1811 with gallium, indium or thallium
• CPC Class Codes: B01J 27/1813 with germanium, tin or lead
• CPC Class Codes: B01J 27/186 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
• CPC Class Codes: B01J 27/187 with manganese, technetium or rhenium
• CPC Class Codes: B01J 27/188 with chromium, molybdenum, tungsten or polonium
• CPC Class Codes: B01J 27/195 with vanadium, niobium or tantalum
• CPC Class Codes: B01J 35/40 characterised by dimensions, e.g. grain size in a colloidal state B01J35/23; crystallite size B01J35/77
• CPC Class Codes: B01J 37/0036 Grinding
• CPC Class Codes: B01J 37/04 Mixing B01J37/0009, B01J37/0018 take precedence
• CPC Class Codes: B01J 37/08 Heat treatment B01J37/0009, B01J37/0018 take precedence
• CPC Class Codes: C07C 51/00 Preparation of carboxylic acids or their salts, halides or anhydrides of acids by hydrolysis of oils, fats or waxes C11C

Abstract

Hydroxypropionic acid, hydroxypropionic acid derivatives, or mixtures thereof are dehydrated using a catalyst and a method to produce bio-acrylic acid, acrylic acid derivatives, or mixtures thereof. A method to produce the dehydration catalyst is also provided.

Claims

1. A method of preparing a dehydration catalyst, comprising contacting a dehydration catalyst precursor mixture consisting essentially of one or more precursor phosphate salts under conditions including a water partial pressure and a temperature;

wherein said one or more precursor phosphate salts consist essentially of one or more monovalent cations, and one or more phosphate anions selected from the group represented by molecular formulae (IV) and (V);

[H₂P_yO_(3y+1)]^y−

 

 

(IV)

[PO₃]^z−

_z 

 

(V);

wherein y is any integer equal to or greater than 1 and z is any integer equal to or greater than 3;

wherein said one or more precursor phosphate salts are neutrally charged;

with a gas mixture comprising water vapor;

wherein the water partial pressure in said gas mixture is equal to or greater than the water partial pressure at the triple point of at least one of said one or more precursor phosphate salts;

wherein said contacting step between said dehydration catalyst precursor mixture and said gas mixture is performed at a temperature equal to or greater than the temperature at the triple point of at least one of said one or more precursor phosphate salts; and

wherein one or more amorphous phosphate salts are produced as a result of said one or more precursor phosphate salts being contacted with said water vapor.

2. The method of claim 1, wherein said one or more monovalent cations are selected from the group consisting of Na⁺, K⁺, Rb⁺, Cs⁺, and mixtures thereof.

3. The method of claim 1, wherein said water partial pressure is equal to or greater than about 4 bar;

and wherein said contacting step between said one or more precursor phosphate salts and said gas mixture is performed at a temperature equal to or greater than about 250°

C.

4. The method of claim 3, wherein the water partial pressure is between about 5 bar and about 35 bar.

5. The method of claim 3, wherein said temperature is between about 300°

C. and about 450°

C.

6. The method of claim 1, wherein said one or more phosphate anions are selected from the group represented by molecular formulae (IVa), (IVb), (IVc), (IVd), (Va), (Vb), (Vc) and mixtures thereof:

[H₂PO₄]⁻

 

 

(IVa)

[H₂P₂O₇]²⁻

 

 

(IVb)

[H₂P₃O₁₀]³⁻

 

 

(IVc)

[H₂P₄O₁₃]⁴⁻

 

 

(IVd)

[P₃O₉]³⁻

 

 

(Va)

[P₆O₁₈]⁶⁻

 

 

(Vb)

[PO₃]_nⁿ⁻

 

 

(Vc);

and wherein n is any integer equal to or greater than 3.

7. The method of claim 6, wherein said one or more precursor phosphate salts are selected from the group consisting of KH₂PO₄, (KPO₃)_n, any of their hydrated forms, and mixtures thereof.

8. The method of claim 1, wherein said contacting step is performed under a total pressure between about 4 bar and about 35 bar.

9. A method of claim 1, wherein said dehydration catalyst precursor mixture further comprises amorphous silicon oxide (SiO₂);

and wherein said amorphous silicon oxide is substantially chemically inert to said one or more precursor phosphate salts.

10. The method of claim 9, wherein the weight ratio between the total amount of said one or more precursor phosphate salts and the total amount of said silicon oxide in said dehydration catalyst precursor mixture is between about 1:

10 and about 4;

1.

11. A method of preparing a dehydration catalyst, comprising under conditions including a water partial pressure and a temperature, a dehydration catalyst precursor mixture consisting essentially of one or more precursor phosphate salts and one or more oxysalts;

wherein said one or more oxysalts are substantially chemically inert to said one or more precursor phosphate salts;

wherein said one or more precursor phosphate salts consist essentially of one or more monovalent cations, and one or more phosphate anions selected from the group represented by molecular formulae (IV) and (V);

[H₂P_yO_(3y+1)]^y−

 

 

(IV)

[PO₃]_z^z−

 

 

(V);

wherein y is any integer equal to or greater than 1 and z is any integer equal to or greater than 3;

wherein said one or more precursor phosphate salts are neutrally charged;

wherein said one or more oxysalts comprise one or more polyvalent cations, and one or more oxyanions selected from the group represented by molecular formulae (II) and (III);

[H<sub>(a−

2b)</sub>S_cO<sub>(4c−

b)</sub>]<sup>(2c−

a)−</sup>

 

 

(II)

[Ta_2dO_(5d+e)]^2e−

 

 

(III);

wherein a and b are positive integers or zero;

wherein c, d, and e are positive integers;

wherein (a−

2b) is equal to or greater than zero;

wherein (2c−

a) is greater than zero;

wherein said one or more oxysalts are neutrally charged;

with a gas mixture comprising water vapor;

wherein the water partial pressure in said gas mixture is equal to or greater than the water partial pressure at the triple point of at least one of said one or more precursor phosphate salts;

wherein said contacting step between said dehydration catalyst precursor mixture and said gas mixture is performed at a temperature equal to or greater than the temperature at the triple point of at least one of said one or more precursor phosphate salts; and

wherein one or more amorphous phosphate salts are produced as a result of said one or more precursor phosphate salts being contacted with said water vapor.

12. The method of claim 11, wherein said dehydration catalyst precursor mixture further comprises amorphous silicon oxide (SiO2);

and wherein said amorphous silicon oxide is substantially chemically inert to said one or more precursor phosphate salts.