CN103833461A - Method for extraction of alga liquid fertilizer synergist by genetically engineered bacterium fermentation - Google Patents

Method for extraction of alga liquid fertilizer synergist by genetically engineered bacterium fermentation Download PDF

Info

Publication number
CN103833461A
CN103833461A CN201310616623.7A CN201310616623A CN103833461A CN 103833461 A CN103833461 A CN 103833461A CN 201310616623 A CN201310616623 A CN 201310616623A CN 103833461 A CN103833461 A CN 103833461A
Authority
CN
China
Prior art keywords
fermentation
marine alga
genetic engineering
alga
engineering bacterium
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN201310616623.7A
Other languages
Chinese (zh)
Inventor
王爱云
陈吉强
刘云
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
SHANDONG RUNYIN BIOCHEMICAL CO Ltd
Original Assignee
SHANDONG RUNYIN BIOCHEMICAL CO Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by SHANDONG RUNYIN BIOCHEMICAL CO Ltd filed Critical SHANDONG RUNYIN BIOCHEMICAL CO Ltd
Priority to CN201310616623.7A priority Critical patent/CN103833461A/en
Publication of CN103833461A publication Critical patent/CN103833461A/en
Pending legal-status Critical Current

Links

Images

Landscapes

  • Fertilizers (AREA)
  • Micro-Organisms Or Cultivation Processes Thereof (AREA)

Abstract

The invention discloses a method for extraction of an alga liquid fertilizer synergist by genetically engineered bacterium fermentation. The method comprises the following steps of by a molecular biological technology, extracting photosynthetic bacterium, lactobacillus and actinomycete genetic gene molecules which can decompose insoluble macromolecules of alga into soluble micromolecules, connecting the genetic gene molecules to saccharomycete cytoplasm so that a DNA genome is recombined, and carrying out the recombined DNA genome expression in escherichia coli cells to construct a genetically engineered bacterial strain. The method improves bioactivity of microorganisms and improves an alga large-molecule decomposition capability. The method utilizes a high-density fermentation technology, improves fermentation strength and shortens fermentation time. The method utilizes a micro-filtration membrane and ultrafilter membrane separation technology, completely retains biologically-active substances and nutrients of alga, forms a net-type fertilizer-carrying system from the alga extract and urea, delays urea decomposition, provides a plurality of nutrients for crops, promotes crop growth and realizes urea synergism.

Description

A kind of method of genetic engineering bacterium fermented extracted marine alga liquid fertilizer synergist
Technical field
The preparation method who the present invention relates to fertilizer synergist is directly involved in a kind of method of genetic engineering bacterium fermented extracted marine alga liquid fertilizer synergist.
Technical background
The general rate of fertilizer application of China's agricultural is large at present, and fertilizer efficiency utilization ratio is low, particularly taking urea as main utilization rate of nitrogen fertilizer is below 25%.A large amount of nitrogenous fertilizer decomposes volatilization or outflows with water and ecotope is polluted.Over nearly twenties years, agriculture and fertilizer expert has studied coating controlled-release fertilizer, inhibitor slow-release fertilizer, has added polypeptide fertilizer, has extended fertilizer efficiency period to suppressing urea decomposition, save fertilizer and play active effect, but ubiquity cost is high, the shortcoming such as few has additional nutrients.
Seaweed extracted liquor has greatly retained natural radioactivity component, contain a large amount of non-itrogenous organic substances, 40 several mineral materials and the VITAMIN such as incomparable abundant K, the Ca of land plant, Mg, Zn, I, contain especially Sargassum polysaccharides, alginic acid, highly unsaturated fatty acids and multiple natural phant growth regulator in marine alga, there is very high biological activity, the generation of nonspecific factor in can stimulating plant body, regulates Endogenous hormone balance.In urea, add seaweed extracted liquor, under the effect of hydrogen bond, Seaweed Extract and urea form the fertile body that carries of alpha-helix or macromolecule network structure, can not only delay the decomposition of urea, the more important thing is and provide multiple nutrient for farm crop, promote plant growth, therefore say that seaweed extracted liquor is current best area synergist.Once adopted chemical hydrolysis and flora heap fermentation method both at home and abroad.The activity of chemical hydrolysis havoc marine alga endogenous substance, nutritive ingredient loss is serious; Flora heap fermentation method fermentation time reached about 10 days, was difficult to realize suitability for industrialized production, sought the easily preparation method of the seaweed extracted liquor of row of a kind of high-efficient simple, was technical problem urgently to be resolved hurrily.
Summary of the invention
Object of the present invention is just to provide a kind of marine alga liquid extracting method of efficient, easy, complete reservation marine alga natural activity.
The object of the present invention is achieved like this: genetic engineering bacterium fermented extracted marine alga liquid fertilizer synergist production method step is as follows:
The structure of genetic engineering bacterium: selecting the fermentation of seaweed marine alga macromole of degrading is that micromolecular photosynthetic bacteria, milk-acid bacteria are donor, extract the gene group DNA in its cell, select yeast to extract its tenuigenin as carrier, connect recombinant plasmid dna genome, selection intestinal bacteria are host receptor, in recombinant plasmid dna gene insertion Bacillus coli cells, build genetic engineering bacterium.
The cultivation screening of genetic engineering bacterium: the engineering bacteria cell that builds gene is implanted in substratum and cultivated, and good bacterial strain continues to cultivate to filter out growth situation after every cultivation 12h, so cultivates five generations of screening, the excellent species filtering out.
Three grades of seed culture: the strain excellent filtering out is after culture medium culturing, and culture transferring is cultivated 8 hours culture transferrings to shaking table and cultivated 10h to 200L first class seed pot, then culture transferring is cultivated 12h to 1000L secondary seed tank.
Two-stage expands fermentation: to 10t ferment tank 16 hours, 10t tank fermented liquid is transplanted to the 20t fermentor tank employing flow feeding 30h that continuously ferments by 1000L seeding tank culture transferring.
Microfiltration membrane filtering solid impurity: fermented liquid is squeezed into microfiltration membrane separator filtering solid impurity with pump.
Ultra-filtration membrane filtering mycelia: the fermented liquid pump of removing solid impurity is squeezed into ultra-filtration membrane filtering mycelia.
Ion-exchange demineralization: the cleaner liquid of filtering mycelia is squeezed into ion-exchanger desalination with pump.
Negative pressure evaporation is concentrated: the marine alga liquid after desalination carries out the concentrated marine alga liquid that obtains of negative pressure evaporation.
A preferred embodiment of the invention: in three grades of seed culture, the configuration proportion of substratum is: pure water 800g/L, peptone 2.6g/L, yeast powder 2g/L, KH 2pO 32g/L, K 2hPO 31g/L, ZnSO 48H 2o 0.5g/L, MgSO 42g/L.
According to another kind of preferred implementation of the present invention: two-stage expands fermentation liquor formulation in fermentation and is: seaweed powder 200 order 25 mass parts, glucose 5 mass parts, inorganic salt 1 mass parts, beans matter albumen 2 mass parts, water 77 mass parts.45 DEG C of leavening temperatures, pH value is 6, dissolved oxygen ratio: 1:4.
Brief description of the drawings:
Accompanying drawing 1 shows the process flow diagram of the method for a kind of genetic engineering bacterium fermented extracted of the present invention marine alga liquid fertilizer synergist.
Embodiment
Accompanying drawing 1 shows the process flow sheet of the method for a kind of genetic engineering bacterium fermented extracted of the present invention marine alga liquid fertilizer synergist.Be described further below in conjunction with accompanying drawing.
The structure 1 of genetic engineering bacterium: selecting fermentation of seaweed can decompose the insoluble macromole of marine alga is the micromolecular photosynthetic bacteria of solubility, milk-acid bacteria, actinomycetes are as donor bacterium, the donor bacterium of selecting is cultivated respectively in substratum, from donor photosynthetic bacteria, milk-acid bacteria, in actinomycetes cell, obtain and there is the genetic molecule that decomposes marine alga characteristic, saccharomycetic tenuigenin is cut as carrier, by the photosynthetic bacteria obtaining, milk-acid bacteria gene combine with carrier, the gene group of restructuring is imported in colibacillary cell, gene are at expression in escherichia coli, so the new microorganism cells building is referred to as to genetic engineering bacterium.
The cultivation screening 2 of genetic engineering bacterium: prepare substratum: pure water 800g/L, peptone 2.6g/L, yeast powder 2g/L, KH 2pO 32g/L, K 2hPO 31g/L, ZnSO 48H 2o 0.5g/L, MgSO 42g/L, stirs, and then the genetic engineering bacterium of structure is implanted in substratum and is cultivated sampling after 24 hours, chooses the bacterial strain growing fine and continues to cultivate, and eliminates the weak bacterial strain of growing way, and so cultured continuously screened for five generations, finally selected strain excellent.
Three grades of seed culture 3: the strain excellent of selecting was implanted to shaking table culture medium culturing after 8 hours, culture transferring was to 200L seed tank culture 10 hours, culture transferring was to 1000L seed tank culture 12 hours again, 45 DEG C of three grades of culture temperature, pH value is 6, dissolved oxygen ratio: 1:4, when culture transferring, growth nursery stage is all in logarithmic phase.
Two-stage expands fermentation 4: the preparation of fermented liquid: seaweed powder 200 order 25 mass parts, glucose 5 mass parts, inorganic salt 1 mass parts, beans matter albumen 2 mass parts, water 77 mass parts.Fermented liquid is respectively charged in 10t, 20t fermentor tank, seed liquor culture transferring, to 10t fermentor tank, is fermented 16 hours, growth nursery stage is still in logarithmic phase, grain weight 150g/L, pours one grade fermemtation liquid into second order fermentation tank, takes flow feeding, fermented liquid concentration is remained on to 30%, grain weight keeps 150g/L, 45 DEG C of leavening temperatures, and pH value is 6, dissolved oxygen ratio: 1:4., fermentation time 30 hours.
Microfiltration membrane filtering solid impurity 5: fermented liquid pump is squeezed into microfiltration membrane separator with pump, fermented liquid one microfiltration membrane separator upper cover enters every film pipe clear liquid and after enrichment, discharges from purified liquor outlet in separator cylinder through fenestra, and solid impurity is discharged with the outlet of lower cover impurity.
Ultra-filtration membrane filtering thalline 6: the clear liquid of microfiltration membrane filtering is squeezed into ultra-filtration membrane separator with pump, liquid enters every ultrafiltration membrane pipe from upper cover, seaweed extracted liquor infiltration membranous wall is discharged from cleaner liquid outlet after enrichment in cylindrical shell, and macromole mycelia intercepts in pipe and discharges from the outlet of lower cover mycelia.
Ion-exchange demineralization 7: cleaner liquid is squeezed into the positively charged ions such as cation exchanger Ca, Mg, Na and is absorbed with pump, then is absorbed by negatively charged ion such as anion exchanger lactate, sulfate radicals, reaches the object of desalination.
Negative pressure evaporation concentrated 8: the cleaner liquid after desalination is squeezed into triple effect evaporation unit with pump, at negative pressure-0.99MPa, at 80 DEG C of temperature, the concentration of evaporation concentration to 90%, obtains seaweed extracted liquor.
Principal feature of the present invention is: the genetic engineering bacterium collection photosynthetic bacteria that the means of applied molecular biology build, milk-acid bacteria, actinomycetes, yeast fermentation energy in marine alga decomposes the insoluble macromolecular feature of marine alga in one, at expression in escherichia coli, greatly improve biological activity, strengthen the macromolecular ability of decomposition marine alga, adopt high cell density fermentation, improve ferment strength, shorten fermentation time, adopt microfiltration membrane and ultra-filtration membrane isolation technique, complete reservation biologically active substance and the nutritive substance in marine alga, make seaweed extracted liquor and urea be combined into network and carry fertile system, delay the decomposition of urea, and provide multiple nutrient for farm crop, promote the growth of farm crop, reach the object of urea synergy.

Claims (3)

1. a method for genetic engineering bacterium fermented extracted marine alga liquid fertilizer synergist, is characterized in that the step of the method is as follows:
The structure of genetic engineering bacterium: selecting the fermentation of seaweed marine alga macromole of degrading is that micromolecular photosynthetic bacteria, milk-acid bacteria are donor, extract the gene group DNA in its cell, select yeast to extract its tenuigenin as carrier, connect recombinant plasmid dna genome, selection intestinal bacteria are host receptor, in recombinant plasmid dna gene insertion Bacillus coli cells, construct genetic engineering bacterium;
The cultivation screening of genetic engineering bacterium: the genetically engineered mycetocyte of structure is implanted in substratum and cultivated, and good bacterial strain continues to cultivate to filter out growth situation after every cultivation 12h, so cultivates five generations of screening, the excellent species filtering out;
Three grades of seed culture: the strain excellent filtering out is after culture medium culturing, and culture transferring is cultivated 8 hours culture transferrings to shaking table and cultivated 10h to 200L first class seed pot, then culture transferring is cultivated 12h to 1000L secondary seed tank;
Two-stage expands fermentation: to 10t ferment tank 16 hours, 10t tank fermented liquid is transplanted to the 20t fermentor tank employing flow feeding 30h that continuously ferments by 1000L seeding tank culture transferring;
Microfiltration membrane filtering solid impurity: fermented liquid is squeezed into microfiltration membrane separator filtering solid impurity with pump;
Ultra-filtration membrane filtering mycelia: the fermented liquid pump of removing solid impurity is squeezed into ultra-filtration membrane filtering mycelia;
Ion-exchange demineralization: the cleaner liquid of filtering mycelia is squeezed into ion-exchanger desalination with pump;
Negative pressure evaporation is concentrated: the marine alga liquid after desalination carries out the concentrated marine alga liquid that obtains of negative pressure evaporation.
2. a kind of method of genetic engineering bacterium fermented extracted marine alga liquid fertilizer synergist according to claim 1, is characterized in that: the preparation of substratum in three grades of seed culture: pure water 800g/L, peptone 2.6g/L, yeast powder 2g/L, KH 2pO 32g/L, K 2hPO 31g/L, ZnSO 48H 2o 0.5g/L, MgSO 42g/L.
3. a kind of method of genetic engineering bacterium fermented extracted marine alga liquid fertilizer synergist according to claim 1, it is characterized in that: two-stage expands fermentation liquor formulation in fermentation and is: seaweed powder 200 order 25 mass parts, glucose 5 mass parts, inorganic salt 1 mass parts, beans matter albumen 2 mass parts, water 77 mass parts, 45 DEG C of leavening temperatures, pH value is 6, dissolved oxygen ratio: 1:4.
CN201310616623.7A 2013-11-29 2013-11-29 Method for extraction of alga liquid fertilizer synergist by genetically engineered bacterium fermentation Pending CN103833461A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201310616623.7A CN103833461A (en) 2013-11-29 2013-11-29 Method for extraction of alga liquid fertilizer synergist by genetically engineered bacterium fermentation

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201310616623.7A CN103833461A (en) 2013-11-29 2013-11-29 Method for extraction of alga liquid fertilizer synergist by genetically engineered bacterium fermentation

Publications (1)

Publication Number Publication Date
CN103833461A true CN103833461A (en) 2014-06-04

Family

ID=50797405

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201310616623.7A Pending CN103833461A (en) 2013-11-29 2013-11-29 Method for extraction of alga liquid fertilizer synergist by genetically engineered bacterium fermentation

Country Status (1)

Country Link
CN (1) CN103833461A (en)

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102173907A (en) * 2011-01-30 2011-09-07 山东金利丰生物科技股份有限公司 Preparation method of algae amino acid microbial fertilizer
CN102924134A (en) * 2012-11-26 2013-02-13 日照益康有机农业科技发展有限公司 Alga microorganism fertilizer agent and preparation method thereof
CN103012008A (en) * 2011-09-28 2013-04-03 上海中意农业科技发展有限公司 Formula for producing compound microbial fertilizer by use of algae and preparation method
CN103011916A (en) * 2012-12-14 2013-04-03 山东新超农业科技有限公司 Method for preparing organic bacteria liquid, organic bacteria liquid prepared by method and application of organic bacteria liquid
KR20130075511A (en) * 2011-12-27 2013-07-05 (주) 젠셀 Composition for promoting hair growth containing fermented extracts of herb mixture

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102173907A (en) * 2011-01-30 2011-09-07 山东金利丰生物科技股份有限公司 Preparation method of algae amino acid microbial fertilizer
CN103012008A (en) * 2011-09-28 2013-04-03 上海中意农业科技发展有限公司 Formula for producing compound microbial fertilizer by use of algae and preparation method
KR20130075511A (en) * 2011-12-27 2013-07-05 (주) 젠셀 Composition for promoting hair growth containing fermented extracts of herb mixture
CN102924134A (en) * 2012-11-26 2013-02-13 日照益康有机农业科技发展有限公司 Alga microorganism fertilizer agent and preparation method thereof
CN103011916A (en) * 2012-12-14 2013-04-03 山东新超农业科技有限公司 Method for preparing organic bacteria liquid, organic bacteria liquid prepared by method and application of organic bacteria liquid

Similar Documents

Publication Publication Date Title
CN107032886A (en) A kind of selenium-rich natural and multi-functional foliar fertilizer and preparation method thereof
CN102630490B (en) Artificial cultivation method for cordyceps militaris mycelium for increasing cordycepin content
CN101407761B (en) Liquid inocula composed of yeast fused strain, Geotrichum candidum Link and Rhizopus, and preparation and use thereof
CN104845896B (en) Produce the bacterial strain and method of Weilan gum
CN101984827B (en) Plant growth bacterial agent and preparation method thereof
CN103882080A (en) Effective method for preparing avermectin
CN104150977B (en) Preparation method and application of alga oligosaccharide biological fertilizer
CN102924136A (en) Process for utilizing abandoned feathers to produce special bio-organic fertilizer for bananas and product thereof
CN111394255B (en) Aspergillus buried and application thereof
CN111742778B (en) Lepista sordida strain and method for cultivating fruiting bodies by using liquid strain of Lepista sordida strain
CN103444441A (en) High-yield cultivation method of oyster mushrooms
CN102701801B (en) Method for producing biogas energy while preparing organic fertilizer or compound fertilizer by using inorganic fertilizer
CN101760437B (en) Bread yeast with high nucleic acid content and preparation method thereof
CN103833461A (en) Method for extraction of alga liquid fertilizer synergist by genetically engineered bacterium fermentation
CN102994427A (en) Bacillus mucilaginosus and preparation method of crude polysaccharide of bacillus mucilaginosus beneficial to growth of poultry
CN107963922A (en) A kind of preparation method of Enteromorpha ferment organic fertilizer
CN102711515B (en) Chlorella suspension for sea feed comprising extract of lotus leaf
CN104744152A (en) Method for manufacturing pleurotus geesteranus compost
CN103602599B (en) Electroporation conversion method for breeding high-temperature pleuratus ferulae
CN116042423A (en) Biogas slurry comprehensive utilization method
JPH05153852A (en) Cultivation of 'oohiratake' and 'hiratake' with medium composed mainly of squeezed cake of citrus fruit juice
CN107347815A (en) Utilize biological bacteria and the method for biological agent processing sulfurous method filter mud breeding earthworm
CN102154120A (en) Gossypol acetate degradation bacteria S1
CN106365792A (en) Polypeptide bio-compound organic fertilizer
CN104892048A (en) Production process of special organic fertilizer for watermelons

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
CB03 Change of inventor or designer information

Inventor after: Wang Zhiyong

Inventor after: Chen Zhenwei

Inventor after: Wang Aiyun

Inventor after: Chen Jiqiang

Inventor after: Liu Yun

Inventor before: Wang Aiyun

Inventor before: Chen Jiqiang

Inventor before: Liu Yun

COR Change of bibliographic data
WD01 Invention patent application deemed withdrawn after publication
WD01 Invention patent application deemed withdrawn after publication

Application publication date: 20140604