AWAJI HARUO (JP)
SHIMOTO HIDESATO (JP)
SHARYOU MASAKI (JP)
JUJO PAPER CO LTD (JP)
| EP0374700A2 | 1990-06-27 | |||
| GB1189604A | 1970-04-29 |
| 1. | A process for hydrolysis of waterinsoluble ester in the presence of a lipase, characterized by the presence of a watersoluble polyelectrolyte. |
| 2. | A process according to Claim 1 , wherein the polyelectrolyte has 5 cationic groups, preferably tertiary or quaternary amine groups. |
| 3. | A process according to Claim 2, wherein the cationic polyelectrolyte is cationic starch or a copolymer of acrylamide with N(dimethyl aminomethyl) acrylamide, dimethylaminoethyl methacrylate ortrimethylaminoethyl methacrylate. |
| 4. | A process according to Claim 1 , wherein the polyelectrolyte has anionic 10 groups, preferably carboxyl groups. |
| 5. | A process according to Claim 4, wherein the anionic polyelectrolyte is a copolymer of acrylamide and acrylate. |
| 6. | A process according to any preceding claim, wherein the polyelectro¬ lyte is present in an amount of 21000 ppm, preferably 10200 ppm. |
| 7. | 15 7. A process according to any preceding claim, wherein the pH is in the range 37. |
| 8. | 5, preferably 47. |
| 9. | A process according to any preceding claim in the presence of a microbial lipase, preferably derived from a strain of Candida, Pseudomonas, Humicola, Chromobacterium or Aspergillus, and preferably at a lipase activity of 1 20 100 KLU/kg of dry matter. |
| 10. | A process according to any preceding claim for hydrolysis of esters in pitch during a pulping or papermaking process. |
| 11. | A process according to the preceding claim, whereby the cellulase activity is below 1000 EGU/kg. |
| 12. | 1 A method of increasing the rate of hydrolysis of waterinsoluble ester in the presence of a lipase by incorporation of a watersoluble polyelectrolyte. |
TECHNICAL FIELD
This invention relates to a process for hydrolysis of water-insoluble ester in the presence of a lipase, particularly to such a process for hydrolysis of pitch (resin) in pulp, and to a method of increasing the rate of hydrolysis of water- insoluble ester in the presence of a lipase by incorporation of a polyelectrolyte.
BACKGROUND ART
It is known that lipases can be used with advantage for efficient hydrolysis of water-insoluble esters, particularly triglycerides (e.g. JP-A 51 -080305, JP-A 58-126794, JP-A 59-210893, GB-A 2,176,480, WO 88/02775).
It is also known that some types of pulp made from wood have a high pitch content, e.g. various types of mechanical pulp. This can cause so-called pitch troubles in papermaking such as paper contamination or paper breaks. Pitch contains considerable amounts of triglycerides, more commonly known as fats, and other esters.
It is the object of this invention to provide an improved process for ester hydrolysis, applicable to hydrolysis of resin esters.
STATEMENT OF THE INVENTION
We have found that, surprisingly, addition of a water-soluble poly- electrolyte (i.e. an anionic or cationic polymer) significantly increases the hydrolysis rate of esters in the presence of lipases.
Various metal cations have been reported to affect lipase activity, and cationic surfactant has been reported inhibit lipase activity (Nishio et al., Agric. Biol. Chem., 51 (1), 181-186, 1987; C.E. Ibrahim et al., Agric. Biol. Chem., 51 (1), 37-45, 1987). The effect of polyelectrolytes on lipase activity has not been described. Accordingly, the invention provides a process for hydrolysis of water- insoluble ester in the presence of a lipase, characterized by the presence of a water- soluble polyelectrolyte. The invention also provides a method of increasing the rate of hydrolysis of water-insoluble ester in the presence of a lipase by incorporation of a water-soluble polyelectrolyte.
DETAILED DESCRIPTION OF THE INVENTION
Polyelectrolyte
The polyelectrolyte used in the invention may be any water-soluble polymer that contains functional groups which ionize in water. It may be cationic or anionic. A group of preferred anionics is anionic polyacrylamide, e.g. a copolymer of acrylamide and acrylate (such as sodium acrylate).
Some preferred cationic polymers are those contaning tertiary or quaternary amine groups. An example is cationic starch having diethylamino-ethyl groups or 2-hydroxy,2-(trimethylamino-methyl) ethyl groups attached to the hydroxyl group in the 6-position of the repeating glucose unit of the starch molecule. Another example is cationic polyacrylamide, e.g. a copolymer of acrylamide with N-(dimethyl-amino-methyl)-acrylamide, dimethyl-amino-ethyl methacrylate or trϊmethyl-amino-ethyl methacrylate. A further example is cationic polyamine such as quaternary polyamine and polyethyleneimine.
Use of the above-mentioned polyelectrolytes is particularly ad- vantageous in papermaking where these polymers may simultaneously act as fiocculants or retention aids.
The amount of polyelectrolyte is preferably 2-1000 ppm, preferably 10- 200 ppm in the reaction mixture, or 0.1-10 kg/ton of dry matter, particularly 0.3-3 kg/t.
Lipase For reasons of economy, microbial lipases are preferred. Examples of suitable enzymes are lipases derived from strains of Pseudomonas (especially Ps. cepacia, Ps. fluorescens, Ps. fragi and Ps. stutzeri), Candida (especially C. antarctica (e.g. lipase A or B, see WO 88/02775) and C. cylindracea), Humicola (especially H. brevispora, H. lanuginosa, H. brevis var. thermoidea and H. insolens), Chromobacterium (especially C. viscosum) and Aspergillus (especially A. niger). The amount of lipase will typically correspond to a lipase activity of 1 ,000-100,000 LU/kg dry matter or 50-5,000 LU/litre (LU = Lipase Unit, defined in WO 89/04361).
Ester hydrolysis process Typical process conditions are pH 3-7.5, particularly 4-7, a temperature from ambient to 80°C, particularly 30-60°C, and reaction times of 0.5-3 hours.
The process of the invention can be used for any lipase-catalyzed hydrolysis of water-insoluble esters, particularly triglycerides.
Thus, the process of the invention may be used for fat hydrolysis in the production of fatty acids, glycerides and/or glycerol from fat or oil. The ester may be a liquid at ambient temperature, such as soy bean oil and many other oils, or it may be a high melting fat, such as beef tallow.
Hydrolysis of resin esters
The process of the invention is particularly applicable to the hydrolysis of resin esters during a pulping or paper-making process, e.g. to avoid pitch troubles such as paper contamination, paper breaks or contamination of process equipment.
The process of the invention may be applied to any pitch-containing pulp, especially to pulps with a considerable content of triglycerides and other esters from pitch. Examples are pulps produced by mechanical pulping, alone or combined with a gentle chemical treatment, such as GW (Ground Wood), TMP (Thermo Mechanical Pulp) and CTMP (Chemical Thermo Mechanical Pulp).
Hydrolysis of esters in pitch according to the invention can be done in the pulping or stock preparation section, where addition of polyelectrolytes is particularly advantageous since it can also act as a retention or flocculation aid. The pulp typically has a consistency of 0.2-5% dry substance.
EXAMPLES
EXAMPLE 1
Red pine (Pinus radiata) ground wood pulp was treated with Humicola lipase in the presence of various polyelectrolytes. After the reaction the degree of triglyceride hydrolysis was determined by quantitative TLC using latroscan™. Conditions were: 4% pulp slurry, pH 4.5, temperature 40°C, agitation
300 rpm. The dosage of polyelectrolyte and enzyme is given below as ppm/DS. Results:
(*) : Determined by quantitative TLC; latroscan Method.
It is seen that all the anionic and cationic polymers tested increased the hydrolysis of triglyceride.
EΞXAMPLE 2
To verify the effect of polyelectrolytes on lipase activity another experiment was done, using two different cationic polymers. Conditions were: 4% pulp slurry, pH 4.5, temperature 40°C, 2 hours reaction time, agitation 300 rpm. Dosage of polyelectrolytes and enzyme are given below as ppm/DS.
(*) : Determined by quantitative TLC; latroscan Method.