CN114426994A - D-psicose whole-cell synthesis method taking glycerol as substrate - Google Patents

D-psicose whole-cell synthesis method taking glycerol as substrate Download PDF

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CN114426994A
CN114426994A CN202210089073.7A CN202210089073A CN114426994A CN 114426994 A CN114426994 A CN 114426994A CN 202210089073 A CN202210089073 A CN 202210089073A CN 114426994 A CN114426994 A CN 114426994A
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psicose
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许敬亮
吕永坤
张辉
贾箐
熊文龙
阿拉牧
屈凌波
应汉杰
王诗元
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Abstract

The invention provides a whole-cell synthesis method of D-psicose, which converts glycerol into D-psicose in one pot and relates to the field of biochemical engineering. In order to avoid thermodynamic equilibrium in the isomerase pathway and to reduce the production cost of D-psicose by using expensive dihydroxyacetone phosphate and D-glyceraldehyde, the present invention constructs a complete conversion pathway from glycerol to D-psicose. The recombinant strain is used as a whole-cell catalyst, so that the glycerol is converted into the D-psicose in one pot. Compared with other similar methods, the method has the advantages that the reaction system has no intermediate product fructose (isomer of D-psicose) residue, and the product is single (only D-psicose is produced without by-product D-sorbose), so that the separation and purification are convenient; compared with an enzyme catalysis reaction system, the method omits a complicated enzyme purification process, has a simple production process and lower cost, and is suitable for large-scale production.

Description

D-psicose whole-cell synthesis method taking glycerol as substrate
Technical Field
The invention belongs to the field of biochemical engineering, and particularly relates to a D-psicose whole-cell synthesis method using glycerol as a substrate.
Background
D-Psicose (D-Psicose or D-Allulose) is a rare functional sugar, a small molecular weight monosaccharide naturally present in various types of food products, first found in sugarcane and beet molasses, murinus and wheat. The sugar degree of the D-psicose is 70% of that of the sucrose, and the calorie is only 0.3% of that of the sucrose, so that the D-psicose is called non-caloric sugar and is an ideal sugar substitute with ultralow calorie. D-psicose is Generally Recognized As Safe (GRAS) as approved by the U.S. food and drug administration. It has tremendous physiological benefits including blood glucose inhibitory properties, neuroprotective effects, active oxygen scavenging activity, anti-obesity effects, and the like. The D-psicose can also inhibit fat accumulation in abdominal cavity, and has strong active oxygen (ROS) scavenging ability and glutathione reducing ability. In addition, the D-psicose also has a neuroprotective effect, and has good protection and treatment effects on diseases such as neurodegeneration and atherosclerosis. Based on the functions, the D-psicose has important application value in the aspects of food processing, medical care and the like.
The chemical synthesis method of D-psicose is complicated in process and has certain limitations, and the chemical production process is relatively serious in pollution, so that breakthrough progress is not made. At present, two routes are mainly used for synthesizing D-psicose by a biotransformation method: (1) the technical route based on the ketose 3-epimerase, i.e. the enzyme cascade consisting of glucose isomerase and ketose 3-epimerase, converts glucose into fructose and D-psicose in succession. However, this pathway is a reversible reaction, and there is a thermodynamic equilibrium such that the substrate (glucose), the intermediate (fructose) and the product (D-psicose) coexist in the reaction system, and after the thermodynamic equilibrium is reached, the reaction is in a dynamic equilibrium. Since glucose, fructose and D-psicose are isomers of each other, this phenomenon makes separation and purification of the product very difficult. (2) Based on the aldolase route, it is now common to catalyze the condensation of dihydroxyacetone phosphate (DHAP) and D-glycerol aldehyde to D-psicose and D-sorbose using L-rhamnose-1-phosphate aldolase and fructose-1-phosphorylase. However, the product selectivity of the process is poor, and the product contains both D-psicose and D-sorbose. The two are isomers, and the existence of the byproduct D-sorbose brings great troubles to the separation and purification of the product. In addition, dihydroxyacetone phosphate and D-glyceraldehyde are expensive and unstable, so that large-scale in vitro synthesis is difficult. The invention constructs a whole-cell catalyst, can directly synthesize cheap glycerol into D-psicose, only contains D-psicose in the product, and has no byproduct D-sorbose. The invention has larger application potential in the fields of food and medicine.
Disclosure of Invention
In view of the above, the present invention aims to provide a method for synthesizing D-psicose using glycerol in whole cells, thereby realizing direct synthesis of D-psicose using glycerol as an inexpensive substrate without production of D-sorbose as a byproduct.
In order to achieve the above object, the present invention provides the following technical solutions:
the invention provides a method for synthesizing D-psicose by using glycerol whole cells, wherein the D-psicose synthesis method takes escherichia coli as a basal cell to construct a whole-cell catalyst to convert the glycerol into the D-psicose.
Optionally, the escherichia coli is escherichia coli BL21(DE 3).
Optionally, the whole-cell catalyst construction method comprises the following steps: the glycerol kinase-encoding gene (glpK, SEQ ID NO:6), the glycerol-3-phosphate dehydrogenase-encoding gene (glpD, SEQ ID NO:7), the L-fucoidan-1-phosphate aldolase-encoding gene (FucA, SEQ ID NO:8) and the fructose-1-phosphorylase-encoding gene (YqaB, SEQ ID NO:9) derived from Escherichia coli MG1655 and the sugar alcohol oxidase-encoding gene (AldO, SEQ ID NO:10) derived from Streptomyces coelicolor M145 were cloned between the BamHI and HindIII sites of the vector pET28a (PB) using a one-step cloning kit (Nanjing Nodezae Biotech Co., Ltd.) (primers, see Table 1), respectively. The above pathway genes were assembled as monocistrons by multiple rounds of ePathBricks assembly (specific method references: Xu, P., et al.,2012, ACS Synthetic Biology,1(7):256-266), to obtain recombinant plasmid pET28a (PB) N-KDABO (plasmid map is shown in FIG. 2). Wherein the expression of all pathway genes is controlled by a T7 promoter and a T7 terminator. The recombinant plasmid is transformed into escherichia coli BL21(DE3), and the recombinant escherichia coli BL21/KDABO is obtained. The recombinant strain can be used for preparing a whole-cell catalyst and synthesizing glycerol into D-psicose.
Alternatively, the conditions for converting glycerol into D-psicose using the recombinant strain BL21/KDABO described above were: culturing the recombinant E.coli to OD6000.6-0.8, IPTG was added to a final concentration of 0.05-0.5mM, and induction was carried out at 15-30 ℃ and 200rpm for 4-24 h. Centrifuging at 4 deg.C and 5000rpm to collect thallus, washing thallus with sterilized ultrapure water to remove culture medium, and resuspending thallus with 50mM phosphate buffer solution with pH of 6-8 to obtain resting cell which can be used as whole cell catalyst for subsequent reaction.
Optionally, the concentration of the substrate glycerol is 10-60 g/L.
Optionally, the conversion condition is 20-35 ℃ for 48 h.
Compared with the prior art, the invention has the following beneficial effects:
(1) the invention uses cheap raw material glycerol as a substrate instead of expensive dihydroxyacetone phosphate (DHAP) and D-glyceraldehyde, greatly reduces the production cost of D-psicose, and is suitable for large-scale production.
(2) The product only contains D-psicose, and does not contain D-sorbose as a byproduct, thereby being beneficial to separation and purification of the product.
(3) Compared with a ketose 3-epimerase approach, the method avoids the problems of thermodynamic equilibrium and the like, is expected to obtain higher conversion rate, has single product, and is convenient for subsequent separation and purification.
(4) Compared with enzyme catalysis, the whole-cell transformation avoids a series of problems such as complicated enzyme purification steps, cofactors and the like, has mild reaction conditions, and is more suitable for industrial production.
Drawings
FIG. 1 is a schematic diagram of the synthetic pathway for the conversion of glycerol to D-psicose. This pathway consists of glycerol kinase (glpK), glycerol-3-phosphate dehydrogenase (glpD), sugar alcohol oxidase (AldO), L-fucoidan-1-phosphate aldolase (FucA), and fructose-1-phosphorylase (YqaB).
FIG. 2 is a map of recombinant plasmid pET28a (PB) N-KDABO. The recombinant plasmid contains a glycerol kinase coding gene (glpK), a glycerol-3-phosphate dehydrogenase coding gene (glpD), an L-fucoidan-1-phosphate aldolase coding gene (FucA), a fructose-1-phosphorylase coding gene (YqaB) and a sugar alcohol oxidase coding gene (AldO), and the expressions of the genes are controlled by a T7 promoter and a T7 terminator and are connected in series in the form of monocistrons to form a conversion pathway from glycerol to D-psicose.
FIG. 3. ion chromatography analysis of whole cell transformed products. Glycerol is used as a substrate, and after the recombinant strain BL21/KDABO whole cell transformation, D-psicose is synthesized, and a by-product D-sorbose is not synthesized. Wherein, a recombinant strain BL21/KDABO containing a synthetic pathway from glycerol to D-psicose is an experimental group, and a strain BL21/pET28a (PB) N containing an empty plasmid pET28a (PB) N is a blank control.
FIG. 4 Whole cell catalyst preparation and transformation conditions optimization. (A) Concentration optimization of inducer IPTG, (B) induction temperature optimization, (C) induction time optimization, (D) reaction temperature optimization of conversion of glycerol to D-psicose, (E) pH optimization of conversion of glycerol to D-psicose, (F) initial concentration optimization of substrate glycerol.
FIG. 5 shows the D-psicose production with time under the optimum conditions. The optimal conditions are as follows: the concentration of an inducer IPTG is 0.05mM, the induction temperature is 20 ℃, the induction time is 12h, the reaction temperature is 25 ℃, the reaction pH is 7.5, and the initial concentration of a substrate is 40 g/L.
FIG. 6 shows the experimental production verification of D-psicose synthesis method at the fermenter level.
Detailed description of the preferred embodiment
The invention provides a D-psicose whole-cell synthesis method using glycerol as a substrate, and the D-psicose synthesis method can directly convert the glycerol into the D-psicose by constructing a recombinant escherichia coli engineering strain.
The method for synthesizing D-psicose using glycerol whole cells and the use thereof according to the present invention will be described in detail with reference to the following examples, which should not be construed as limiting the scope of the present invention.
Detailed Description
Example 1: recombinant escherichia coli whole cell method for converting glycerol into D-psicose
The glycerol kinase-encoding gene (glpK, SEQ ID NO:6), the glycerol-3-phosphate dehydrogenase-encoding gene (glpD, SEQ ID NO:7), the L-fucoidan-1-phosphate aldolase-encoding gene (FucA, SEQ ID NO:8) and the fructose-1-phosphorylase-encoding gene (YqaB, SEQ ID NO:9) derived from Escherichia coli MG1655 and the sugar alcohol oxidase-encoding gene (AldO, SEQ ID NO:10) derived from Streptomyces coelicolor M145 were cloned between the BamHI and HindIII sites of the vector pET28a (PB) using a one-step cloning kit (Nanjing Nodezaki Biotech Co., Ltd.) (the primers used are shown in Table 1), respectively. The recipient plasmid was digested with NheI/SalI, the donor plasmid was digested with AvrII/SalI, and the genes of the above-mentioned pathways were assembled as monocistrons by multiple rounds of ePathBricks (see: Xu, P., et al, 2012, ACS Synthetic Biology,1(7):256-266) to obtain recombinant plasmid pET28a (PB) N-KDABO (plasmid map is shown in FIG. 2). Wherein the expression of all pathway genes is controlled by a T7 promoter and a T7 terminator. The recombinant plasmid is transformed into escherichia coli BL21(DE3), and the recombinant escherichia coli BL21/KDABO is obtained. The recombinant strain can be used for preparing a whole-cell catalyst and synthesizing glycerol into D-psicose.
TABLE 1 primers used in the present invention
Figure BDA0003488404900000061
Recombinant E.coli BL21/KDABO was cultured overnight in LB medium at 37 ℃ and 200rpm, transferred to a 250mL Erlenmeyer flask containing 25mL fresh LB medium at an inoculum size of 2% (v/v), and cultured at 37 ℃ and 200rpm to log phase. Then, IPTG was added to the cells at a final concentration of 500. mu.M, and the cells were further cultured at 25 ℃ and 200rpm for 6 hours to express the gene in the D-psicose-synthesizing pathway of glycerol. Centrifuging at 4 deg.C and 5000rpm for 5min, collecting thallus, washing thallus with sterilized ultrapure water to remove culture medium, and then resuspending thallus with 50mM Phosphate Buffer Solution (PBS) with pH of 7.0 to obtain resting cell which can be used as whole cell catalyst for converting glycerol into D-psicose. Coli BL21/pET28a (PB) N with empty plasmid pET28a (PB) N was used as a blank control, and the other operating conditions were the same.
Glycerol was added to the above reaction system to a final concentration of 40g/L, and the reaction was carried out at 30 ℃ for 48 hours. The reaction supernatant was detected by ion chromatography.
The method for ion chromatography analysis of D-psicose and D-sorbose is as follows: the ion chromatography model is a Saimeifei ICS-6000 high-pressure ion chromatograph, the detector is an electrochemical detector, the chromatographic column model is PA-20, the mobile phase A is ultrapure water, the mobile phase B is 200mM NaOH aqueous solution, and gradient elution is carried out to obtain (B%): 0min 10%, 15min 10%, 15.1min 100%, 25min 100%, 25.1min 10%, 35min 10%, constant flow rate 0.5mL/min, sample size 25 μ L, and column oven and detector temperature both 30 ℃.
The ion chromatographic analysis result shows that the peak-off time of D-sorbose and D-psicose is 8.267min and 9.475min respectively.
The blank (E.coli BL21/pET28a (PB) N) synthesized neither D-psicose nor D-sorbose; the experimental group (recombinant E.coli BL21/KDABO) synthesized only D-psicose, but not D-sorbose (FIG. 3). The results indicate that the constructed whole-cell catalyst can convert glycerol into D-psicose without D-sorbose as a byproduct.
Example 2: whole-cell catalyst preparation and optimization of D-psicose synthesis conditions
In order to improve the yield and the conversion rate of the D-psicose, the invention further optimizes the conditions for preparing the whole-cell catalyst and the reaction conditions for synthesizing the D-psicose by converting glycerol.
The invention firstly optimizes the preparation process of the whole-cell catalyst: the concentration range of the inducer IPTG concentration is 0.001-0.5mM, the temperature range of the pathway gene induction expression is 15-30 ℃, and the time range of the pathway gene induction expression is 4-20 h. The results showed that the optimal concentration of the inducer IPTG was 0.05mM (FIG. 4A), the optimal induction temperature was 20 deg.C (FIG. 4B) and the optimal induction time was 12h (FIG. 4C). The invention optimizes the reaction condition of the conversion of the glycerol to the D-psicose: the temperature range of the reaction is 20-35 ℃, the pH range of the reaction is 6.0-8.0, and the initial concentration range of the substrate glycerol is 10-60 g/L. As a result, the optimum reaction temperature was 25 ℃ C (FIG. 4D), the optimum reaction pH was 7.5 (FIG. 4E), and the optimum initial substrate concentration was 40g/L (FIG. 4F).
Under the above-described optimum conditions, the present invention analyzed the change in the production amount of D-psicose with time. Under the condition, the yield of D-psicose reaches the maximum at 48h, namely 3.55 g/L.
Example 3: preparation of D-psicose by using fermentation tank to amplify reaction process
In order to verify the feasibility of the D-psicose synthesis method in the fermenter level pilot production, the reaction system was scaled up using a 5L fermenter according to the invention based on example 2. Activating recombinant Escherichia coli BL21/KDABO overnight, transferring into a fermentation tank containing 3L LB medium with an inoculum size of 2% (v/v), and culturing at 37 deg.C and 200rpm with ventilation of 4NI/min to OD6000.6-0.8. IPTG was added to a final concentration of 0.05mM,the induction was carried out at 20 ℃ and 200rpm for 12 hours at an aeration rate of 4NI/min to express the pathway gene. The cells were collected by centrifugation at 4 ℃ and 5000rpm for 15min, the cells were washed with sterilized ultrapure water to remove the medium, the cells were resuspended in a 50mM phosphate buffer solution having a pH of 7.5, and the medium was replaced with the phosphate buffer solution at a ratio of 1:1 to prepare a whole cell catalyst (resting cells). Glycerol was added to the reaction mixture to a final concentration of 50g/L, the reaction mixture was reacted at 25 ℃ and 200rpm with an aeration rate of 4NI/min, samples were taken at 12-hour intervals, and the D-psicose concentration was measured by ion chromatography. The results showed that the D-psicose yield reached 3.14g/L at 48h (FIG. 4). The result shows that the method constructed by the invention can be used for small-scale production on a fermentation tank and has larger application potential.
The foregoing is only an alternative embodiment of the present invention, and it should be noted that modifications and embellishments could be made by those skilled in the art without departing from the principle of the present invention, and these should be considered as the protection scope of the present invention.
Sequence listing
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Ile Ala Phe Pro Met Arg Phe Arg Leu Pro His Arg Pro His Leu Arg
85 90 95
Pro Ala Trp Met Ile Arg Ile Gly Leu Phe Met Tyr Asp His Leu Gly
100 105 110
Lys Arg Thr Ser Leu Pro Gly Ser Thr Gly Leu Arg Phe Gly Ala Asn
115 120 125
Ser Val Leu Lys Pro Glu Ile Lys Arg Gly Phe Glu Tyr Ser Asp Cys
130 135 140
Trp Val Asp Asp Ala Arg Leu Val Leu Ala Asn Ala Gln Met Val Val
145 150 155 160
Arg Lys Gly Gly Glu Val Leu Thr Arg Thr Arg Ala Thr Ser Ala Arg
165 170 175
Arg Glu Asn Gly Leu Trp Ile Val Glu Ala Glu Asp Ile Asp Thr Gly
180 185 190
Lys Lys Tyr Ser Trp Gln Ala Arg Gly Leu Val Asn Ala Thr Gly Pro
195 200 205
Trp Val Lys Gln Phe Phe Asp Asp Gly Met His Leu Pro Ser Pro Tyr
210 215 220
Gly Ile Arg Leu Ile Lys Gly Ser His Ile Val Val Pro Arg Val His
225 230 235 240
Thr Gln Lys Gln Ala Tyr Ile Leu Gln Asn Glu Asp Lys Arg Ile Val
245 250 255
Phe Val Ile Pro Trp Met Asp Glu Phe Ser Ile Ile Gly Thr Thr Asp
260 265 270
Val Glu Tyr Lys Gly Asp Pro Lys Ala Val Lys Ile Glu Glu Ser Glu
275 280 285
Ile Asn Tyr Leu Leu Asn Val Tyr Asn Thr His Phe Lys Lys Gln Leu
290 295 300
Ser Arg Asp Asp Ile Val Trp Thr Tyr Ser Gly Val Arg Pro Leu Cys
305 310 315 320
Asp Asp Glu Ser Asp Ser Pro Gln Ala Ile Thr Arg Asp Tyr Thr Leu
325 330 335
Asp Ile His Asp Glu Asn Gly Lys Ala Pro Leu Leu Ser Val Phe Gly
340 345 350
Gly Lys Leu Thr Thr Tyr Arg Lys Leu Ala Glu His Ala Leu Glu Lys
355 360 365
Leu Thr Pro Tyr Tyr Gln Gly Ile Gly Pro Ala Trp Thr Lys Glu Ser
370 375 380
Val Leu Pro Gly Gly Ala Ile Glu Gly Asp Arg Asp Asp Tyr Ala Ala
385 390 395 400
Arg Leu Arg Arg Arg Tyr Pro Phe Leu Thr Glu Ser Leu Ala Arg His
405 410 415
Tyr Ala Arg Thr Tyr Gly Ser Asn Ser Glu Leu Leu Leu Gly Asn Ala
420 425 430
Gly Thr Val Ser Asp Leu Gly Glu Asp Phe Gly His Glu Phe Tyr Glu
435 440 445
Ala Glu Leu Lys Tyr Leu Val Asp His Glu Trp Val Arg Arg Ala Asp
450 455 460
Asp Ala Leu Trp Arg Arg Thr Lys Gln Gly Met Trp Leu Asn Ala Asp
465 470 475 480
Gln Gln Ser Arg Val Ser Gln Trp Leu Val Glu Tyr Thr Gln Gln Arg
485 490 495
Leu Ser Leu Ala Ser
500
<210> 3
<211> 344
<212> PRT
<213> Streptomyces coelicolor
<400> 3
Met Glu Tyr Arg Ile Leu Gly Leu Ala Ala Glu Ala Ala Phe Phe Thr
1 5 10 15
Leu Leu Ser Val Pro Pro Leu Leu Leu Ser Leu Leu Gly Leu Leu Gly
20 25 30
Tyr Val Asp Ser Trp Ile Gly Ala Asp Thr Thr Glu Ser Leu Arg Asp
35 40 45
Asn Ile Leu Asp Ala Ser Arg Ala Val Leu Ser Glu Lys Gly Val Arg
50 55 60
Gln Ile Thr Glu Pro Ile Leu Asp Asp Val Met Lys Gly Gly Arg Pro
65 70 75 80
Asp Val Ile Ser Ile Gly Phe Leu Phe Ala Leu Trp Ser Gly Ser Arg
85 90 95
Ala Val Asn Val Phe Ile Asp Thr Ile Thr Val Met Tyr Gly Leu Asp
100 105 110
Gly Val Arg Gly Ile Val Arg Thr Arg Leu Met Ala Phe Leu Leu Phe
115 120 125
Ile Val Ala Leu Leu Ile Gly Ser Ile Ala Leu Pro Leu Met Val Ala
130 135 140
Gly Pro Asp Ala Val Val Arg Val Val Pro Trp Ser Thr Thr Val Val
145 150 155 160
Gln Val Leu Tyr Trp Pro Val Val Ile Ile Leu Ser Val Ala Phe Leu
165 170 175
Thr Thr Leu Tyr His Val Ser Val Pro Val Arg Ser Pro Trp Ile Glu
180 185 190
Asp Val Pro Gly Ala Leu Val Ala Leu Ala Met Trp Val Leu Gly Ser
195 200 205
Phe Leu Leu Arg Ile Tyr Leu Thr Ser Thr Val Glu Gly Pro Thr Ile
210 215 220
Tyr Gly Ser Leu Ala Ala Pro Val Ala Val Leu Leu Trp Ile Gly Val
225 230 235 240
Ser Ala Phe Ala Val Leu Val Gly Ala Ala Val Asn Ala Ala Ile Asp
245 250 255
Arg Val Trp Pro Ala Ala Ala Thr Ala Ala Ala Arg Glu Ala Asn Glu
260 265 270
Arg Leu Arg Gln Ala Gln Val Ala Glu Tyr Val Ala Arg Thr Thr Ala
275 280 285
Asn Gly Glu Gly Asp Pro Asp Met Pro Ser Glu Phe Pro Glu Arg Trp
290 295 300
Ser Arg Phe Leu Pro Pro Glu Asp Val Thr Ala Arg Leu Arg Thr Gln
305 310 315 320
Pro Lys Ser Ala Pro Pro Ala Asn His Thr His His Gln Lys His Asp
325 330 335
His Asn His Arg Asp Asp Ala Ser
340
<210> 4
<211> 215
<212> PRT
<213> Escherichia coli (Escherichia coli)
<400> 4
Met Glu Arg Asn Lys Leu Ala Arg Gln Ile Ile Asp Thr Cys Leu Glu
1 5 10 15
Met Thr Arg Leu Gly Leu Asn Gln Gly Thr Ala Gly Asn Val Ser Val
20 25 30
Arg Tyr Gln Asp Gly Met Leu Ile Thr Pro Thr Gly Ile Pro Tyr Glu
35 40 45
Lys Leu Thr Glu Ser His Ile Val Phe Ile Asp Gly Asn Gly Lys His
50 55 60
Glu Glu Gly Lys Leu Pro Ser Ser Glu Trp Arg Phe His Met Ala Ala
65 70 75 80
Tyr Gln Ser Arg Pro Asp Ala Asn Ala Val Val His Asn His Ala Val
85 90 95
His Cys Thr Ala Val Ser Ile Leu Asn Arg Ser Ile Pro Ala Ile His
100 105 110
Tyr Met Ile Ala Ala Ala Gly Gly Asn Ser Ile Pro Cys Ala Pro Tyr
115 120 125
Ala Thr Phe Gly Thr Arg Glu Leu Ser Glu His Val Ala Leu Ala Leu
130 135 140
Lys Asn Arg Lys Ala Thr Leu Leu Gln His His Gly Leu Ile Ala Cys
145 150 155 160
Glu Val Asn Leu Glu Lys Ala Leu Trp Leu Ala His Glu Val Glu Val
165 170 175
Leu Ala Gln Leu Tyr Leu Thr Thr Leu Ala Ile Thr Asp Pro Val Pro
180 185 190
Val Leu Ser Asp Glu Glu Ile Ala Val Val Leu Glu Lys Phe Lys Thr
195 200 205
Tyr Gly Leu Arg Ile Glu Glu
210 215
<210> 5
<211> 188
<212> PRT
<213> Escherichia coli (Escherichia coli)
<400> 5
Met Tyr Glu Arg Tyr Ala Gly Leu Ile Phe Asp Met Asp Gly Thr Ile
1 5 10 15
Leu Asp Thr Glu Pro Thr His Arg Lys Ala Trp Arg Glu Val Leu Gly
20 25 30
His Tyr Gly Leu Gln Tyr Asp Ile Gln Ala Met Ile Ala Leu Asn Gly
35 40 45
Ser Pro Thr Trp Arg Ile Ala Gln Ala Ile Ile Glu Leu Asn Gln Ala
50 55 60
Asp Leu Asp Pro His Ala Leu Ala Arg Glu Lys Thr Glu Ala Val Arg
65 70 75 80
Ser Met Leu Leu Asp Ser Val Glu Pro Leu Pro Leu Val Asp Val Val
85 90 95
Lys Ser Trp His Gly Arg Arg Pro Met Ala Val Gly Thr Gly Ser Glu
100 105 110
Ser Ala Ile Ala Glu Ala Leu Leu Ala His Leu Gly Leu Arg His Tyr
115 120 125
Phe Asp Ala Val Val Ala Ala Asp His Val Lys His His Lys Pro Ala
130 135 140
Pro Asp Thr Phe Leu Leu Cys Ala Gln Arg Met Gly Val Gln Pro Thr
145 150 155 160
Gln Cys Val Val Phe Glu Asp Ala Asp Phe Gly Ile Gln Ala Ala Arg
165 170 175
Ala Ala Gly Met Asp Ala Val Asp Val Arg Leu Leu
180 185
<210> 6
<211> 1509
<212> DNA
<213> Escherichia coli (Escherichia coli)
<400> 6
atgactgaaa aaaaatatat cgttgcgctc gaccagggca ccaccagctc ccgcgcggtc 60
gtaatggatc acgatgccaa tatcattagc gtgtcgcagc gcgaatttga gcaaatctac 120
ccaaaaccag gttgggtaga acacgaccca atggaaatct gggccaccca aagctccacg 180
ctggtagaag tgctggcgaa agccgatatc agttccgatc aaattgcagc tatcggtatt 240
acgaaccagc gtgaaaccac tattgtctgg gaaaaagaaa ccggcaagcc tatctataac 300
gccattgtct ggcagtgccg tcgtaccgca gaaatctgcg agcatttaaa acgtgacggt 360
ttagaagatt atatccgcag caataccggt ctggtgattg acccgtactt ttctggcacc 420
aaagtgaagt ggatcctcga ccatgtggaa ggctctcgcg agcgtgcacg tcgtggtgaa 480
ttgctgtttg gtacggttga tacgtggctt atctggaaaa tgactcaggg ccgtgtccat 540
gtgaccgatt acaccaacgc ctctcgtacc atgttgttca acatccatac cctggactgg 600
gacgacaaaa tgctggaagt gctggatatt ccgcgcgaga tgctgccaga agtgcgtcgt 660
tcttccgaag tatacggtca gactaacatt ggcggcaaag gcggcacgcg tattccaatc 720
tccgggatcg ccggtgacca gcaggccgcg ctgtttggtc agttgtgcgt gaaagaaggg 780
atggcgaaga acacctatgg cactggctgc tttatgctga tgaacactgg cgagaaagcg 840
gtgaaatcag aaaacggcct gctgaccacc atcgcctgcg gcccgactgg cgaagtgaac 900
tatgcgttgg aaggtgcggt gtttatggca ggcgcatcca ttcagtggct gcgcgatgaa 960
atgaagttga ttaacgacgc ctacgattcc gaatatttcg ccaccaaagt gcaaaacacc 1020
aatggtgtgt atgtggttcc ggcatttacc gggctgggtg cgccgtactg ggacccgtat 1080
gcgcgcgggg cgattttcgg tctgactcgt ggggtgaacg ctaaccacat tatacgcgcg 1140
acgctggagt ctattgctta tcagacgcgt gacgtgctgg aagcgatgca ggccgactct 1200
ggtatccgtc tgcacgccct gcgcgtggat ggtggcgcag tagcaaacaa tttcctgatg 1260
cagttccagt ccgatattct cggcacccgc gttgagcgcc cggaagtgcg cgaagtcacc 1320
gcattgggtg cggcctatct cgcaggcctg gcggttggct tctggcagaa cctcgacgag 1380
ctgcaagaga aagcggtgat tgagcgcgag ttccgtccag gcatcgaaac cactgagcgt 1440
aattaccgtt acgcaggctg gaaaaaagcg gttaaacgcg cgatggcgtg ggaagaacac 1500
gacgaataa 1509
<210> 7
<211> 1506
<212> DNA
<213> Escherichia coli (Escherichia coli)
<400> 7
atggaaacca aagatctgat tgtgataggg ggcggcatca atggtgctgg tatcgcggca 60
gacgccgctg gacgcggttt atccgtgctg atgctggagg cgcaggatct cgcttgcgcg 120
acctcttccg ccagttcaaa actcattcac ggtggcctgc gctaccttga gcactatgaa 180
ttccgcctgg tcagcgaggc gctggctgaa cgtgaagtgc tgctgaaaat ggccccgcat 240
atcgccttcc cgatgcgttt tcgcctgcca catcgtccgc atctgcgccc ggcgtggatg 300
attcgcattg gtctgtttat gtacgatcat ctgggtaaac gcaccagctt gccgggatca 360
actggtttgc gttttggcgc aaattcagtg ttaaaaccgg aaattaagcg cggattcgaa 420
tattctgact gttgggtaga cgacgcccgt ctggtactcg ccaacgccca gatggtggtg 480
cgtaaaggcg gcgaagtgct tactcggact cgcgccacct ctgctcgccg cgaaaacggc 540
ctgtggattg tggaagcgga agatatcgat accggcaaaa aatatagctg gcaagcgcgc 600
ggcttggtta acgccaccgg cccgtgggtg aaacagttct tcgacgacgg gatgcatctg 660
ccttcgcctt atggcattcg cctgatcaaa ggcagccata ttgtggtgcc gcgcgtgcat 720
acccagaagc aagcctacat tctgcaaaac gaagataaac gtattgtgtt cgtgatcccg 780
tggatggacg agttttccat catcggcact accgatgtcg agtacaaagg cgatccgaaa 840
gcggtgaaga ttgaagagag tgaaatcaat tacctgctga atgtgtataa cacgcacttt 900
aaaaagcagt taagccgtga cgatatcgtc tggacctact ccggtgtgcg tccgctgtgt 960
gatgatgagt ccgactcgcc gcaggctatt acccgtgatt acacccttga tattcatgat 1020
gaaaatggca aagcaccgct gctgtcggta ttcggcggta agctgaccac ctaccgaaaa 1080
ctggcggaac atgcgctgga aaaactaacg ccgtattatc agggtattgg cccggcatgg 1140
acgaaagaga gtgtgctacc gggtggcgcc attgaaggcg accgcgacga ttatgccgct 1200
cgcctgcgcc gccgctatcc gttcctgact gaatcgctgg cgcgtcatta cgctcgcact 1260
tacggcagca acagcgagct gctgctcggc aatgcgggaa cggtaagcga tctcggggaa 1320
gatttcggtc atgagttcta cgaagcggag ctgaaatacc tggtggatca cgaatgggtc 1380
cgccgcgccg acgacgccct gtggcgtcgc acaaaacaag gcatgtggct aaatgcggat 1440
caacaatctc gtgtgagtca gtggctggtg gagtatacgc agcagaggtt atcgctggcg 1500
tcgtaa 1506
<210> 8
<211> 648
<212> DNA
<213> Escherichia coli (Escherichia coli)
<400> 8
atggaacgaa ataaacttgc tcgtcagatt attgacactt gcctggaaat gacccgcctg 60
ggactgaacc aggggacagc ggggaacgtc agtgtacgtt atcaggatgg gatgctgatt 120
acgcctacag gcattccata tgaaaaactg acggagtcgc atattgtctt tattgatggc 180
aacggtaaac atgaggaagg aaagctcccc tcaagcgaat ggcgtttcca tatggcagcc 240
tatcaaagca gaccggatgc caacgcggtt gttcacaatc atgccgttca ttgcacggca 300
gtttccattc ttaaccgatc gatccccgct attcactaca tgattgcggc ggctggcggt 360
aattctattc cttgcgcgcc ttatgcgacc tttggaacac gcgaactttc tgaacatgtt 420
gcgctggctc tcaaaaatcg taaggcaact ttgttacaac atcatgggct tatcgcttgt 480
gaggtgaatc tggaaaaagc gttatggctg gcgcatgaag ttgaagtgct ggcgcaactt 540
tacctgacga ccctggcgat tacggacccg gtgccagtgc tgagcgatga agagattgcc 600
gtagtgctgg agaaattcaa aacctatggg ttacgaattg aagagtaa 648
<210> 9
<211> 567
<212> DNA
<213> Escherichia coli (Escherichia coli)
<400> 9
atgtacgagc gttatgcagg tttaattttt gatatggatg gcacaatcct ggatacggag 60
cctacgcacc gtaaagcgtg gcgcgaagta ttagggcact acggtcttca gtacgatatt 120
caggcgatga ttgcgcttaa tggatcgccc acctggcgta ttgctcaggc aattattgag 180
ctgaatcagg ccgatctcga cccgcatgcg ttagcgcgtg aaaaaacaga agcagtaaga 240
agtatgctgc tggatagcgt cgaaccgctt cctcttgttg atgtggtgaa aagttggcat 300
ggtcgtcgcc caatggctgt aggaacgggg agtgaaagcg ccatcgctga ggcattgctg 360
gcgcacctgg gattacgcca ttattttgac gccgtcgtcg ctgccgatca cgtcaaacac 420
cataaacccg cgccagacac atttttgttg tgcgcgcagc gtatgggcgt gcaaccgacg 480
cagtgtgtgg tctttgaaga tgccgatttc ggtattcagg cggcccgtgc agcaggcatg 540
gacgccgtgg atgttcgctt gctgtga 567
<210> 10
<211> 1035
<212> DNA
<213> Streptomyces coelicolor
<400> 10
atggagtacc gcatcctcgg cctggccgcc gaggccgcct tcttcaccct gctctcggtg 60
ccgcccctgc tgctgagcct cctcggtctg ctcggctacg tcgactcctg gatcggcgcc 120
gacaccaccg agagcctgcg cgacaacatc ctggacgcct cccgcgccgt gctctccgag 180
aagggcgtcc ggcagatcac cgagccgatc ctggacgacg tgatgaaggg cggccggccc 240
gacgtcatct ccatcggctt cctcttcgcc ctgtggtccg gatcccgcgc ggtgaacgtc 300
ttcatcgaca ccatcaccgt gatgtacggc ctcgacggcg tccggggcat cgtcaggacc 360
cgcctgatgg ccttcctcct cttcatcgtg gccctgctga tcgggtcgat cgcgctgccg 420
ctgatggtgg ccggaccgga cgccgtggtg cgggtcgtgc cctggtcgac gacggtcgta 480
caggtgctgt actggccggt cgtcatcatc ctctccgtgg ccttcctgac cacgctgtac 540
cacgtgtcgg tgcccgtgcg ctcgccgtgg atcgaggacg tccccggcgc gctggtcgcc 600
ctcgccatgt gggtgctggg cagcttcctg ctgcgcatct acctcaccag caccgtcgag 660
ggccccacca tctacggctc cctcgccgcg cccgtcgccg tgctgctgtg gatcggggtg 720
tccgcgttcg cggtgctcgt cggcgccgcg gtcaacgcgg ccatcgaccg ggtgtggccg 780
gccgccgcga ccgccgccgc ccgcgaggcc aacgagcggc tgcgccaggc ccaggtcgcc 840
gagtacgtgg cccgcacgac cgcgaacggc gagggcgacc ccgacatgcc ctccgagttc 900
cccgagcgct ggtcccgctt cctgcccccc gaggacgtca cggcccggct gcgcacccaa 960
ccgaagagcg cgcctcccgc gaaccacacc caccatcaaa agcacgacca caaccaccgc 1020
gacgacgcct cctga 1035
<210> 11
<211> 5371
<212> DNA
<213> Artificial sequence (Synthetic DNA)
<400> 11
atccggagtc gactcctcct ttcgctagca aaaaacccct caagacccgt ttagaggccc 60
caaggggtta tgctagttat tgctcagcgg tggcagcagc caactcagct tcctttacta 120
gtttgttagc agccggatct cagtggtggt ggtggtggtg ctcgagtgcg gccgcaagct 180
tgtagacgga gctcgaattc ggatccgcga cccatttgct gtccaccagt catgcttgcc 240
atatggctgc cgcgcggcac caggccgctg ctgtgatgat gatgatgatg gctgctgccc 300
atggtatatc tccttcttaa agttaaacaa aattatttct agaggggaat tgttatccgc 360
tcacaattcc cctatagtga gtcgtattaa tttcgcggga tcgagatctc gatcctctac 420
gccggacgca tcgtggccgg catcaccggc gcctaggtgc ggttgctggc gcctatatcg 480
ccgacatcac cgatggggaa gatcgggctc gccacttcgg gctcatgagc gcttgtttcg 540
gcgtgggtat ggtggcaggc cccgtggccg ggggactgtt gggcgccatc tccttgcatg 600
caccattcct tgcggcggcg gtgctcaacg gcctcaacct actactgggc tgcttcctaa 660
tgcaggagtc gcataaggga gagcgtcgag atcccggaca ccatcgaatg gcgcaaaacc 720
tttcgcggta tggcatgata gcgcccggaa gagagtcaat tcagggtggt gaatgtgaaa 780
ccagtaacgt tatacgatgt cgcagagtat gccggtgtct cttatcagac cgtttcccgc 840
gtggtgaacc aggccagcca cgtttctgcg aaaacgcggg aaaaagtgga agcggcgatg 900
gcggagctga attacattcc caaccgcgtg gcacaacaac tggcgggcaa acagtcgttg 960
ctgattggcg ttgccacctc cagtctggcc ctgcacgcgc cgtcgcaaat tgtcgcggcg 1020
attaaatctc gcgccgatca actgggtgcc agcgtggtgg tgtcgatggt agaacgaagc 1080
ggcgtcgaag cctgtaaagc ggcggtgcac aatcttctcg cgcaacgcgt cagtgggctg 1140
atcattaact atccgctgga tgaccaggat gccattgctg tggaagctgc ctgcactaat 1200
gttccggcgt tatttcttga tgtctctgac cagacaccca tcaacagtat tattttctcc 1260
catgaagacg gtacgcgact gggcgtggag catctggtcg cattgggtca ccagcaaatc 1320
gcgctgttag cgggcccatt aagttctgtc tcggcgcgtc tgcgtctggc tggctggcat 1380
aaatatctca ctcgcaatca aattcagccg atagcggaac gggaaggcga ctggagtgcc 1440
atgtccggtt ttcaacaaac catgcaaatg ctgaatgagg gcatcgttcc cactgcgatg 1500
ctggttgcca acgatcagat ggcgctgggc gcaatgcgcg ccattaccga gtccgggctg 1560
cgcgttggtg cggatatctc ggtagtggga tacgacgata ccgaagacag ctcatgttat 1620
atcccgccgt taaccaccat caaacaggat tttcgcctgc tggggcaaac cagcgtggac 1680
cgcttgctgc aactctctca gggccaggcg gtgaagggca atcagctgtt gcccgtctca 1740
ctggtgaaaa gaaaaaccac cctggcgccc aatacgcaaa ccgcctctcc ccgcgcgttg 1800
gccgattcat taatgcagct ggcacgacag gtttcccgac tggaaagcgg gcagtgagcg 1860
caacgcaatt aatgtaagtt agctcactca ttaggcaccg ggatctcgac cgatgccctt 1920
gagagccttc aacccagtca gctccttccg gtgggcgcgg ggcatgacta tcgtcgccgc 1980
acttatgact gtcttcttta tcatgcaact cgtaggacag gtgccggcag cgctctgggt 2040
cattttcggc gaggaccgct ttcgctggag cgcgacgatg atcggcctgt cgcttgcggt 2100
attcggaatc ttgcacgccc tcgctcaagc cttcgtcact ggtcccgcca ccaaacgttt 2160
cggcgagaag caggccatta tcgccggcat ggcggcccca cgggtgcgca tgatcgtgct 2220
cctgtcgttg aggacccggc taggctggcg gggttgcctt actggttagc agaatgaatc 2280
accgatacgc gagcgaacgt gaagcgactg ctgctgcaaa acgtctgcga cctgagcaac 2340
aacatgaatg gtcttcggtt tccgtgtttc gtaaagtctg gaaacgcgga agtcagcgcc 2400
ctgcaccatt atgttccgga tctgcatcgc aggatgctgc tggctaccct gtggaacacc 2460
tacatctgta ttaacgaagc gctggcattg accctgagtg atttttctct ggtcccgccg 2520
catccatacc gccagttgtt taccctcaca acgttccagt aaccgggcat gttcatcatc 2580
agtaacccgt atcgtgagca tcctctctcg tttcatcggt atcattaccc ccatgaacag 2640
aaatccccct tacacggagg catcagtgac caaacaggaa aaaaccgccc ttaacatggc 2700
ccgctttatc agaagccaga cattaacgct tctggagaaa ctcaacgagc tggacgcgga 2760
tgaacaggca gacatctgtg aatcgcttca cgaccacgct gatgagcttt accgcagctg 2820
cctcgcgcgt ttcggtgatg acggtgaaaa cctctgacac atgcagctcc cggagacggt 2880
cacagcttgt ctgtaagcgg atgccgggag cagacaagcc cgtcagggcg cgtcagcggg 2940
tgttggcggg tgtcggggcg cagccatgac ccagtcacgt agcgatagcg gagtgtatac 3000
tggcttaact atgcggcatc agagcagatt gtactgagag tgcaccatat atgcggtgtg 3060
aaataccgca cagatgcgta aggagaaaat accgcatcag gcgctcttcc gcttcctcgc 3120
tcactgactc gctgcgctcg gtcgttcggc tgcggcgagc ggtatcagct cactcaaagg 3180
cggtaatacg gttatccaca gaatcagggg ataacgcagg aaagaacatg tgagcaaaag 3240
gccagcaaaa ggccaggaac cgtaaaaagg ccgcgttgct ggcgtttttc cataggctcc 3300
gcccccctga cgagcatcac aaaaatcgac gctcaagtca gaggtggcga aacccgacag 3360
gactataaag ataccaggcg tttccccctg gaagctccct cgtgcgctct cctgttccga 3420
ccctgccgct taccggatac ctgtccgcct ttctcccttc gggaagcgtg gcgctttctc 3480
atagctcacg ctgtaggtat ctcagttcgg tgtaggtcgt tcgctccaag ctgggctgtg 3540
tgcacgaacc ccccgttcag cccgaccgct gcgccttatc cggtaactat cgtcttgagt 3600
ccaacccggt aagacacgac ttatcgccac tggcagcagc cactggtaac aggattagca 3660
gagcgaggta tgtaggcggt gctacagagt tcttgaagtg gtggcctaac tacggctaca 3720
ctagaaggac agtatttggt atctgcgctc tgctgaagcc agttaccttc ggaaaaagag 3780
ttggtagctc ttgatccggc aaacaaacca ccgctggtag cggtggtttt tttgtttgca 3840
agcagcagat tacgcgcaga aaaaaaggat ctcaagaaga tcctttgatc ttttctacgg 3900
ggtctgacgc tcagtggaac gaaaactcac gttaagggat tttggtcatg aacaataaaa 3960
ctgtctgctt acataaacag taatacaagg ggtgttatga gccatattca acgggaaacg 4020
tcttgctcta ggccgcgatt aaattccaac atggatgctg atttatatgg gtataaatgg 4080
gctcgcgata atgtcgggca atcaggtgcg acaatctatc gattgtatgg gaagcccgat 4140
gcgccagagt tgtttctgaa acatggcaaa ggtagcgttg ccaatgatgt tacagatgag 4200
atggtcagac taaactggct gacggaattt atgcctcttc cgaccatcaa gcattttatc 4260
cgtactcctg atgatgcatg gttactcacc actgcgatcc ccgggaaaac agcattccag 4320
gtattagaag aatatcctga ttcaggtgaa aatattgttg atgcgctggc agtgttcctg 4380
cgccggttgc attcgattcc tgtttgtaat tgtcctttta acagcgatcg cgtatttcgt 4440
ctcgctcagg cgcaatcacg aatgaataac ggtttggttg atgcgagtga ttttgatgac 4500
gagcgtaatg gctggcctgt tgaacaagtc tggaaagaaa tgcataaact tttgccattc 4560
tcaccggatt cagtcgtcac tcatggtgat ttctcacttg ataaccttat ttttgacgag 4620
gggaaattaa taggttgtat tgatgttgga cgagtcggaa tcgcagaccg ataccaggat 4680
cttgccatcc tatggaactg cctcggtgag ttttctcctt cattacagaa acggcttttt 4740
caaaaatatg gtattgataa tcctgatatg aataaattgc agtttcattt gatgctcgat 4800
gagtttttct aagaattaat tcatgagcgg atacatattt gaatgtattt agaaaaataa 4860
acaaataggg gttccgcgca catttccccg aaaagtgcca cctgaaattg taaacgttaa 4920
tattttgtta aaattcgcgt taaatttttg ttaaatcagc tcatttttta accaataggc 4980
cgaaatcggc aaaatccctt ataaatcaaa agaatagacc gagatagggt tgagtgttgt 5040
tccagtttgg aacaagagtc cactattaaa gaacgtggac tccaacgtca aagggcgaaa 5100
aaccgtctat cagggcgatg gcccactacg tgaaccatca ccctaatcaa gttttttggg 5160
gtcgaggtgc cgtaaagcac taaatcggaa ccctaaaggg agcccccgat ttagagcttg 5220
acggggaaag ccggcgaacg tggcgagaaa ggaagggaag aaagcgaaag gagcgggcgc 5280
tagggcgctg gcaagtgtag cggtcacgct gcgcgtaacc accacacccg ccgcgcttaa 5340
tgcgccgcta cagggcgcgt cccattcgcc a 5371

Claims (7)

1. A method for synthesizing D-psicose using glycerol whole cell is characterized in that glycerol is used as a substrate, and glycerol is converted into D-psicose using glycerol kinase (glpK, SEQ ID NO:1), glycerol-3-phosphate dehydrogenase (glpD, SEQ ID NO:2), sugar alcohol oxidase (AldO, SEQ ID NO:3), L-fucoidan-1-phosphate aldolase (FucA, SEQ ID NO:4) and fructose-1-phosphorylase (YqaB, SEQ ID NO:5) (the conversion pathway is shown in FIG. 1).
2. The transformation pathway of claim 1, wherein the glycerol kinase coding gene (glpK, SEQ ID NO:6), the glycerol-3-phosphate dehydrogenase coding gene (glpD, SEQ ID NO:7), the L-fucoidan-1-phosphate aldolase coding gene (FucA, SEQ ID NO:8) and the fructose-1-phosphorylase coding gene (YqaB, SEQ ID NO:9) are derived from Escherichia coli MG1655(Escherichia coli MG1655), and the sugar alcohol oxidase coding gene (AldO, SEQ ID NO:10) is derived from Streptomyces coelicolor M145(Streptomyces coelicolor M145).
3. The method for synthesizing D-psicose according to claim 1, wherein plasmid pET28a (PB) N (SEQ ID NO:11) is used as the expression vector of the transformation pathway, and recombinant plasmid pET28a (PB) N-KDABO (plasmid structure is shown in FIG. 2) containing all pathway genes is constructed.
4. According to the claim 1, claim 2 and claim 3, using Escherichia coli BL21(DE3) as expression host, and transforming the recombinant plasmid into Escherichia coli BL21(DE3) to obtain the engineering strain BL21/KDABO containing all pathway genes.
5. The method for the whole-cell synthesis of D-psicose according to claim 1 and the recombinant engineered strain according to claim 4, wherein the transformation conditions used are as follows: (1) culturing the recombinant engineering bacteria of the escherichia coli to OD in an LB culture medium600Adding isopropyl-beta-D-thiogalactoside (IPTG) with final concentration of 0.05-0.5mM, and inducing gene expression at 15-30 deg.C and 200rpm for 4-24 h; (2) centrifuging at 4 deg.C and 5000rpm to collect thallus, washing thallus with sterilized ultrapure water to remove culture medium, and resuspending thallus with 50mM Phosphate Buffer Solution (PBS) with pH of 6-8 to obtain resting cell; (3) adding glycerol with the final concentration of 10-60g/L as a substrate, and reacting for 48h at 20-35 ℃; (4) the yield of D-psicose was analyzed using ion chromatography.
6. According to claim 1 and claim 5, the optimum conditions of the present invention are: inducer IPTG concentration: 0.05mM, induction temperature: 20 ℃, induction time 12h, reaction temperature: reaction pH at 25 ℃: 7.5, substrate glycerol concentration: 40 g/L.
7. According to claim 1 and claim 6, the D-psicose whole-cell synthesis method according to the present invention produces not less than 3.54g/L of D-psicose under optimal conditions.
CN202210089073.7A 2022-01-25 2022-01-25 D-psicose whole-cell synthesis method taking glycerol as substrate Pending CN114426994A (en)

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Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104611249A (en) * 2014-11-17 2015-05-13 中国科学院天津工业生物技术研究所 Method for synthesis of D-psicose by aldolase whole cell
CN111172123A (en) * 2020-01-07 2020-05-19 江南大学 Production method of D-glyceraldehyde
CN111172215A (en) * 2020-01-07 2020-05-19 江南大学 Preparation method of D-type rare hexulose

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104611249A (en) * 2014-11-17 2015-05-13 中国科学院天津工业生物技术研究所 Method for synthesis of D-psicose by aldolase whole cell
CN111172123A (en) * 2020-01-07 2020-05-19 江南大学 Production method of D-glyceraldehyde
CN111172215A (en) * 2020-01-07 2020-05-19 江南大学 Preparation method of D-type rare hexulose

Non-Patent Citations (6)

* Cited by examiner, † Cited by third party
Title
PENG XU 等: "ePathBrick: A Synthetic Biology Platform for Engineering Metabolic Pathways in E. coli", 《ACS SYNTH. BIOL》 *
ZHOU CHEN 等: "Characterization of alditol oxidase from Streptomyces coelicolor and its application in the production of rare sugars", 《BIOORGANIC & MEDICINAL CHEMISTRY》 *
ZIJIE LI 等: "One-Pot Multienzyme Synthesis of Rare Ketoses from Glycerol", 《J. AGRIC. FOOD CHEM.》 *
ZIJIE LI 等: "Synthesis of D-Sorbose and D-Psicose by Recombinant Escherichia coli", 《JOURNAL OF CARBOHYDRATE CHEMISTRY》 *
陈洲: "基于DHAP依赖型醛缩酶以甘油为底物合成稀有己酮糖体系的构建", 《中国博士学位论文全文数据库工程科技Ⅰ辑》 *
高雅慧 等: "基于RhaD 醛缩酶的"一锅四酶法" 合成D-山梨糖和D-阿洛酮糖", 《食品工业科技》 *

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