Computer-controlled bioreactor system for enzymatic synthesis of L-tryptophan

• US 5,629,202 A
• Filed: 06/06/1995
• Issued: 05/13/1997
• Est. Priority Date: 07/19/1994
• Status: Expired due to Term

• Current Assignee: Development Center for Biotechnology
• Original Assignee: Development Center for Biotechnology
• Inventors: Chan, Zen-Jen, Huang, Wuen-Hsian, Su, Chein-Shyong, Tsai, Hsin
• Primary Examiner(s): Beisner, William H.
• Application Number:
  US08/467,523
• Time in Patent Office: 707 Days
• Field of Search: 435/3, 435/4, 435/26, 435/108, 435/286.1, 435/286.5, 435/288.7, 435/289.1, 435/808, 435/286.7
• US Class Current: 435/286.5
• CPC Class Codes: C12M 41/48 Automatic or computerized control automatic analysis G01N35/00
• CPC Class Codes: C12P 13/22 Tryptophan; Tyrosine; Phenylalanine; 3,4-Dihydroxyphenylalanine

Abstract

Disclosed is an automatic computer-controlled bioreactor system for enzymatic synthesis of L-tryptophan which comprises a bioreactor linked to a computer equipped with an on-line indole assay device, in which the computer controls the feeding of indole, pyruvic acid and/or its salt and an ammonium salt into the bioreactor and feedback-controls the reaction in the bioreactor by indole concentration determined by the on-line indole assay device, wherein the feeding of indole and ammonium salt is controlled by a pre-defined profile that agrees with a tryptophanase activity profile and pyruvic acid and/or its salt is added at a predetermined time.

Claims

1. An computer-controlled bioreactor system for use in an enzymatic synthesis of L-tryptophan comprising:

a bioreactor;

a stirring means;

an indole storing means;

an ammonium salt storing means;

a pyruvic acid and/or pyruvate salt storing means;

an indole and ammonium salt feeding pump with an output means from said indole and ammonium salt storing means and input means to said bioreactor;

a pyruvic acid and/or pyruvate salt feeding pump with an output means from said pyruvic acid and/or pyruvate storing means and input means to said bioreactor;

a computer with data communication means to said stirring means, said pyruvic acid and/or pyruvate salt feeding pump and said indole and said ammonium salt feeding pump;

wherein said indole and ammonium salt feeding pump and pyruvic acid and/or pyruvate salt feeding pump are operatively linked with said computer;

wherein said indole and ammonium salt feeding pump and pyruvic acid and/or pyruvate salt feeding pump and said input means are capable of inputting said indole, said pyruvic acid or pyruvic salt and said ammonium salt into a reaction solution in said computer-controlled bioreactor;

wherein said computer and data communication means controls the input of said pyruvic acid or said pyruvic salt and said ammonium salt into said bioreactor by controlling said feeding pump and input means;

wherein said bioreactor stirring means mixes said indole with either the pyruvic acid or pyruvic salt and the ammonium salt in the presence of a tryptophanase;

wherein said computer controls the feeding rate of said indole to optimize said tryptophanase'"'"'s activity over time by calculating the input of said pyruvic acid or said pyruvic salt and said ammonium salt and the feeding rate of said indole according to a feeding rate of indole equation comprising;

space="preserve" listing-type="equation">F=5.51-5.44*10.sup.-2 T+2.79*10.sup.-4 T.sup.2 -7.05*10.sup.-7 T.sup.3 +7.0*10.sup.-10 T.sup.4,

wherein;

F is the feeding rate of indole (mmole/min/L),

T is the reaction time of enzymatic synthesis (min); and

wherein said computer controls the addition of pyruvic acid or pyruvic salt at a predetermined time.

2. The automatic computer-controlled bioreactor system of claim 1, further comprising:

wherein the biosynthesis efficiency is about 102 g/L of L-tryptophan in 3.5 hours of reaction.

8. The automatic computer-controlled bioreactor system of claim 1 or 3, further comprising:

wherein said tryptophanase is in a microorganism or a cell-free extract.

9. The automatic computer-controlled bioreactor system of claim 1 or 3, wherein said tryptophanase is produced by an E. coli microorganism.

10. The automatic computer-controlled bioreactor system of claim 9, wherein said E. coli microorganism is PGT 67/N 4830.

11. The automatic computer-controlled bioreactor system of claim 1 or 3, further comprising:

wherein an inosine is present as a precipitant for said L-tryptophan during said enzymatic synthesis.

12. The computer-controlled bioreactor system according to claim 1 or 3 wherein said ammonium salt is fed simultaneously with said indole.

13. The computer-controlled bioreactor system according to claim 1 or 3, further comprising:

wherein said pyruvic acid and/or pyruvate salt is added after about 40 to about 60 minutes of said enzymatic synthesis.

3. An computer-controlled bioreactor system for use in an enzymatic synthesis of L-tryptophan comprising:

a bioreactor;

a stirring means;

an indole storing means;

an ammonium salt storing means;

a pyruvic acid and/or pyruvate salt storing means;

an indole and ammonium salt feeding pump with an output means from said indole and ammonium salt storing means and an input means to said bioreactor;

a pyruvic acid and/or pyruvate salt feeding pump with an output means from said pyruvic acid and/or pyruvate storing means and an input means to said bioreactor;

an on-line indole assay device with an output means from said bioreactor and an input means to said on-line indole assay device;

a computer with data communication means to said stirring means, said pyruvic acid and/or pyruvate salt feeding pump and said indole and ammonium salt feeding pump, and said on-line indole assay device;

wherein said on-line indole assay device, said indole and ammonium salt feeding pump and said pyruvic acid and/or pyruvate salt feeding pump are operatively linked with said computer;

wherein said indole and ammonium salt feeding pump and pyruvic acid and/or pyruvate salt feeding pump and said input means are capable of inputting an indole, a pyruvic acid or a pyruvic salt and an ammonium salt into said reaction solution in said bioreactor;

wherein said computer and data communication means controls the input of said pyruvic acid or said pyruvic salt and said ammonium salt into said bioreactor by controlling said feeding pumps and said input means;

wherein said bioreactor stirring means mixes said indole with either the pyruvic acid or pyruvic salt and the ammonium salt in the presence of a tryptophanase;

wherein said on-line indole assay device comprises a photodetector capable of reading the optical density of a reaction solution sample obtained from said bioreactor by said output means from said bioreactor and said input means to said on-line indole assay device and wherein said on-line indole assay device reads the optical density of said reaction solution sample from said bioreactor;

wherein said on-line indole assay device is operatively linked to said computer and generates a feedback signal to said computer comprising the optical density of indole in a sample;

wherein said computer optimizes said tryptophanase'"'"'s activity by calculating the input of said pyruvic acid or said pyruvic salt and said ammonium salt and said feeding rate of indole by said input pumps by using said optical density of indole feedback signal according to a feedback signal output equation comprising;

space="preserve" listing-type="equation">S.sub.fb =S+3.492*O.sub.d -29.34*O.sub.d.sup.2 +0.0308,

wherein;

S_fb is a feedback signal output,

S is an original signal,

S=(F*6-33.167)/3.7257,

F is a feeding rate of indole (mmole/min/L), and

space="preserve" listing-type="equation">F=5.51-5.44*10.sup.-2 T+2.79*10.sup.-4 T.sup.2 -7.05*10.sup.-7 T.sup.3 +7.0*10.sup.-10 T.sup.4,

T is a reaction time of the enzymatic synthesis (min),

O_d is an optical density of indole; and

wherein said computer controls the addition of pyruvic acid or pyruvic salt at a predetermined time.

4. The automatic computer-controlled bioreactor system of claim 3 further comprising:

wherein said computer controls the feeding rate of indole into said reaction solution to optimize said tryptophanase'"'"'s activity by optimizing said feedback signal output S_fb according to a feedback signal output equation comprising;

space="preserve" listing-type="equation">S.sub.fb =0.002-8.76*10.sup.-2* T+4.49*T.sup.2 -11.35*T.sup.3 +11.27*10.sup.-10 *T.sup.4 +3.492*O.sub.d -29.34*O.sub.d.sup.2

wherein;

S_fb is the feedback signal output,

T is the reaction time of the enzymatic synthesis (min); and

O_d is the optical density of indole.

5. The automatic computer-controlled bioreactor system of claim 3 further comprising:

a Ehrlich'"'"'s reagent storage means with output means from said storage means and input means to said photodetector;

wherein said Ehrlich'"'"'s reagent input means inputs said Ehrlich'"'"'s reagent with said reaction solution sample in said photodetector;

wherein said photodetector uses said Ehrlich'"'"'s reagent in said reaction solution sample to obtain an optical density, O_d, reading;

wherein said photodetector outputs said optical density to said computer, which calculates the concentration of said indole in said reaction solution sample.

6. The automatic computer-controlled bioreactor system of claim 3 further comprising:

wherein said computer controls said pyruvic acid and/or pyruvic salt input pump to add additional pyruvic acid and/or pyruvic salt into said bioreactor reaction solution between about 40 to about 60 minutes after said enzymatic reaction is begun.

7. The automatic computer-controlled bioreactor system of claim 3, further comprising:

wherein the biosynthesis efficiency is about 108 g/L of L-tryptophan in 3.5 hours of reaction.