CN1583959A - Process for preparing biological diesel by repeseed fermenting method - Google Patents

Abstract

This invention has disclosed a kind of production technology of utilizing fermented legal system of the rape seed to fetch the biological diesel oil. Compared with diesel oil drawn the diesel oil made and is fetched in the petroleum, the burning that the biological diesel oil can not merely be more abundant, and the harmful gas dicharged in the air is much fewer. Ferment kinds of fungus, rape seed powder gone mouldy to stem from have, fermented course steady performance have, easy to control, it is high to transform the diesel oil rate, does not porph under the corresphonding save condition. This invention production technology is divided into five stages, raw materials pretreament, bacterial cultivation, neutralization, then wash dry fractional distillation, the production equipment used is like making oil equipment of one share, produce biological diesel oil have high economic benefits very, average each ton of rape seed can be made and fetched 245 kilograms of biological diesel oil, and will also produce 10% of the by products-glycerine and odder yeast during the process of producing biological firewood.

Description

Utilize the Semen Brassicae campestris fermentation method to produce the production technique of biofuel

Technical field:

The invention belongs to a kind of biochemical technology.Specifically from Semen Brassicae campestris, produce the Technology of biofuel by strain fermentation.And relate to the extraction and application of culture of strains and byproduct.

Technical background:

Along with development of modern industry, human energy-output ratio is more and more, can not the regenerated energy as natural oil, and along with the hardship of resource exhausts, it is for than being worse off, and the research renewable energy resources will be very promising technology to replace oil.Extracting ethanol now from grain is a kind of desirable direction, but its calorific value of ethanol petrol is low, and it is insufficient to burn, thereby extracts the morning that the diesel oil technology proposes by biochemical method in the vegetable oil material, but still unstable.

Summary of the invention:

The present invention seeks to disclose a kind of production technique of utilizing the Semen Brassicae campestris fermentation method to produce biofuel.Extract diesel oil in the diesel oil of producing and the oil and compare, biofuel can not only be burnt more fully, and is discharged into airborne obnoxious flavour and also wants much less.Fermentation kind of a bacterium derives from the Semen Brassicae campestris of going mouldy and separates and get, and stable performance in the fermenting process is easy to control, transforms diesel oil rate height, is not morphing under the preservation condition accordingly.

Preparation method of the present invention

1, pre-treatment of raw material: the pre-treatment of Semen Brassicae campestris: with Semen Brassicae campestris flush away earth, impurity elimination, the back is baked to jaundice with roaster with Semen Brassicae campestris, 110 ℃-115 ℃ of storing temperatures, time 2-2.5 minute, that the ground oil seeds that baked Semen Brassicae campestris is worn into about fineness 70 orders with pulverizer is standby

2, fermentation is not equipped with and the sterilization of sterile filtration system:

(1) pipeline fire bacterium;

Open valve and each pipeline valve of sterile filtration system of each input and output material pipeline, feed the steam of 0.15 MPa, each drain tap is closed in exhaust about 40 minutes, and the pipeline vapor pressure remains on 0.15 MPa, more than 30 minutes.

The sterilization of (2) sterile filtration system: throw into and respectively pass in and out valve, feed the steam of 0.15 MPa, allow each valve exhaust vapour more than 30 minutes, freezing air is got rid of sterilization, valve-off allows the vapor pressure of aseptic system the inside keep 0.15 MPa and 1 hour, starts air compressor then, open the total filter bottom blow-down valve, the cotton of strainer the inside is dried up; Help air and pass through, blow with air compressor machine approximately and got final product in 1.5 hours, close sewage draining valve, allow aseptic system keep the malleation of 0.01 MPa standby.

3. use culture of strains:

(1), nutrient solution preparation: pretreated canola 8%,, the corn steep liquor 0.15% of peptone 0.1%, 2 ten thousand unit, oral glucose powder 3%, the nitrogenous agricultural urea 0.2% more than 45, tap water 88.55%.

(2), equipment: biomicroscope, large vol rotary type bottle swingging machine, the triangular flask high-pressure sterilizing pot more than 5000 milliliters;

(3), concrete operations: even by using the material of measuring in the prescription to put into container for stirring, be sub-packed in then in 5000 milliliters the triangular flask, each bottled 500 milliliters, bottleneck is tightened with 6-8 layer gauze, place sterilization in the pressure kettle, when vapor pressure in the pot reaches 0.15 MPa, keep getting final product in 30 minutes, allow pressure kettle leave heating source and cool to zero naturally.Open pressure kettle and take out triangular flask, allow it cool to 28 ℃-30 ℃ naturally, then triangular flask is moved on on the Bechtop, open gauze, each triangular flask inserts test tube bacterium two rings, triangular flask is tied with gauze again, putting into bottle swingging machine cultivates, 30 ℃-31 ℃ of temperature, pH value 4.5-5, to contain 300,000,000-3.5 hundred million bacterium be qualified standby when the mattress bulk concentration reaches every milliliter of nutrient solution.

(4), the cultivation workshop section of one-level, second class inoculum

(4.1). the raw-material recipe ratio of first order seed: pretreated canola 10%, the corn steep liquor 0.25% of glucose powder 2%, 2 ten thousand unit, nitrogenous agricultural urea 0.35% more than 45%, peptone 0.15%, tap water 87.25%

Concrete operations, tap water in will filling a prescription is earlier put in the first class seed pot, and then add other materials successively, start stirrer and carry out reality jar sterilization by steam, vapor pressure reaches 0.15 MPa in jar, keep then cooling to 28 ℃ after one hour--30 ℃, under aseptic condition, the cultured big triangular flask bacterial classification of sterilisable chamber is joined in the first class seed pot with material sucking pipes, the bacterial classification consumption is 1.5% of a first class seed pot material, feeding sterile air then under the stirring that does not stop begins to cultivate, tank pressure is the 0.01-0.015 MPa, 30 ℃-31 ℃ of temperature are cultivated and were measured cell concentration in about 6 hours, and 3.5 hundred million-400,000,000 bacterium are qualified in the middle of every milliliter of seed culture fluid, pH value keeps between the 4.5-5 in whole culturing process, otherwise add acid, alkali is adjusted, and whole culturing process must not surpass 10 hours, and long bacterial classification of time is aging, be unfavorable for fermentation, the consumption of sterile air is that seed culture fluid per minute per ton is with 0.012-0.014 cube.

(4.2) second class inoculum is cultivated

Raw-material proportioning

Pretreated canola 14%, glucose powder 2%, 2 ten thousand unit corn steep liquor 0.3%, the agricultural urea 0.4% of nitrogen content more than 45%, peptone 0.2%, tap water 83%.

Concrete operations: earlier tap water is joined in the secondary seed jar by consumption, start stirrer, and then add other material in the proportioning successively, open the intensification of steam valve feeding steam simultaneously and carry out reality jar sterilization, when vapor pressure reaches 0.15 MPa, keep sterilization 1 hour, steam off then, make that temperature drops to 28 ℃-30 ℃ in the jar, then cultured primary seed solution is extracted in the secondary seed jar and cultivates, the consumption that first order seed is somebody's turn to do is that the 5%-6% of secondary seed solution is advisable, after finishing, feeding no mattress air cultivates under not stopping to stir, tank pressure is the 0.01-0.015 MPa, 30 ℃ of temperature--between 31 ℃ of pH value 4.5-5, the sterile air consumption is 0.012--0.014 cube of a seed culture fluid per minute per ton, cultivate about 6 hours and to measure cell concentration and should be every milliliter of seed culture fluid and contain 4.5 hundred million-500,000,000 bacterium, bud ratio is that 18%-22% is qualified, pH value keeps between the 4.5-5 in whole culturing process, otherwise with acid, alkali is adjusted, whole culturing process must not surpass 8 hours, otherwise bacterial classification is aging, the road fermentation of unfavorable back.

4. fermentation

(1), raw material ratio: pretreated canola 33%, 2 ten thousand unit corn steep liquor 0.4%, the urea 0.45% of nitrogen content more than 45%, peptone 0.1%, tap water 65%, glucose powder 1%.

(2), fermentation; Water in the proportioning is put in the fermentor tank, start stirrer, add other material in the proportioning more successively, feeding steam heats, real jar of sterilization, when the vapor pressure in the jar reaches 0.15 MPa, kept 1.5 hours, the middle stirring that does not stop, cool to 30 ℃-21 ℃ then, again cultured secondary seed solution is extracted into fermentor tank, consumption is the 10%-15% of fermented liquid, the back is adjusted between the pH value 4.5-5, close each feed valve, feeding sterile air ferments, fermentation initial stage sterile air consumption is a fermented liquid per minute 0.013-0.015 cubic meter per ton, temperature is controlled at 30 ℃-31 ℃ and is advisable, fermentation proceeds to and measures cell concentration and bud ratio about 8-10 hour, cell concentration should be and contained 1.5 hundred million-200,000,000 bacterium in every milliliter of fermented liquid this moment, bud ratio is 15%---18% is advisable, the consumption that at this moment should strengthen sterile air is a fermented liquid per minute gas consumption 0.015-0.017 cubic meter per ton, pH value is between the 4.5-5, ferment and measured bulk concentration and bud ratio by 20 hours, concentration should be every milliliter of fermented liquid and contains 300,000,000-3.5 hundred million bacterium, bud ratio should be 18%-22%, diesel oil content is that 5%-6% is normal, add the Glucose Liquid 1.5%-2% of the bacterium of having gone out simultaneously, sugar content 5%-6%, improve the vigor and the metabolic capacity of bacterial classification, add liquid glucose after 30 minutes, stop to ventilate and stop to stir about 4 hours, reduce pH value, pH value drops between the 4-4.2, at this moment start stirrer again, feed sterile air, the sterile air consumption is a fermented liquid per minute 0.015-0.017 cubic meter per ton, the middle running check microbial contamination situation of wanting, straight with biomicroscope alkali, ferment by 35-40 hour, diesel oil content should be 9%-9.5%, the pH value of this moment has been got back between the 4.5-5 again, this moment, fermentation entered end, the fermented liquid of fermentor tank is warmed to 70 ℃ ± 2 ℃, keep killing in 30 minutes fermentation diesel oil bacterial classification, otherwise can reduce diesel yield, whole fermentation process needs 35-45 hour.

5, neutralization

In the fermented liquid suction neutralization tank with above fermentor tank, under the stirring that does not stop, be warmed to 80 ℃-85 ℃, add content simultaneously and be the sodium hydroxide about 10% more than 90%, can be as solid sodium hydroxide with using again after 3 times of water-solubleization, this moment, the temperature with neutralization tank was raised to 95-98 ℃, under agitation kept 40 minutes, and then the pressure of neutralization tank adjusted to 0.12 MPa, kept 40-45 minute, purpose is to improve the rate of recovery of glycerine, and then the temperature of neutralization tank dropped to 75 ℃-80 ℃, with phosphoric acid pH value is dropped between the 4-4.2, kept 30 minutes. then at the lime powder that adds fermentation liquid measure 5%, under 75 ℃-80 ℃ situation, kept 40 minutes, the purpose that adds phosphoric acid and lime powder is that the temperature that remaining glucose in the fermented liquid generates after the easy elimination of gluconic acid calcium deposit neutralization tank is dropped to about 45 ℃, earlier with whizzer elimination thalline and impurity such as yeast slurry and rapeseed hull, and then with the more progressive elimination yeast of yeast whizzer, then with filtrate suction storage tank, again through 2 son further elimination residual impurity of ultra-fine filter very much, filtrate is extracted into separating tank staticly settles separation 10-12 hour, gas oil with the upper strata after time reaches sucks holding tank, lower floor is the glycerine sugar water, can send the evaporator tower evaporation, the diesel oil of holding tank is again through boiling water washing 3 times-4 times, the boiling water consumption is 3 times of oil, and then will wash good diesel oil and send into the fractionation of diesel oil dry fractionation device, obtained meeting the biofuel of national standard this moment, this diesel oil can reach the negative 20# of 0#-after measured, because of there is not wax in this fermentation diesel oil, plumbous, objectionable impuritiess such as ammonia, so but the convection drying fractionation is chemically examined qualified packing warehouse-in and is finished product.

6, byproduct---glycerin extraction

Glycerine is present in the water of separating tank lower floor, and industry claims sugar water, sugar water is delivered in the glycerine evaporator tower evaporated earlier, becomes raw glycerine when glycerol content reaches 75%--85%, and then reach the glycerine that meets national standard, i.e. saponification level glycerine after distillation.

7, fodder yeast

The yeast that leaches, yeast slurry, the rape shell again through washing, vacuum deodorization, go to hide, add the offal one yellow material of producing W-Gum, fermentation through fodder yeast can become qualified fodder yeast again, industries such as this product is applied to, breeds fish, shrimp, chicken, the fish meal of alternative after measured Denmark import, bone meal formula feed.

Embodiment:

Production technique of the present invention is divided into five stages, pre-treatment of raw material, spawn culture, neutralization, wash dry fractionation then, employed production unit is the same with one system oil equipment, the production biofuel has very high economic benefit, average Semen Brassicae campestris per ton can be produced 245 kilograms of biofuel, and also can produce 10% byproduct one glycerine and fodder yeast in the process of production biofuel.

The main production equipments of fermentation diesel oil:

1, the general fermentor tank of stirring-type; 2, sterile air filtering system; 3, I and II seeding tank; 4, diesel oil dry fractionation equipment; 5, byproduct one drier oil evaporation, distillation plant; 6, neutralization tank; 7, yeast whizzer; 8, fodder yeast fermentation equipment

Concrete operations are as follows:

1, pre-treatment of raw material workshop section: the pre-treatment of Semen Brassicae campestris: earlier Semen Brassicae campestris is used tap water flush away earth, impurity elimination, with rolling the skeleton symbol roaster Semen Brassicae campestris is baked to jaundice then, 110 ℃-115 ℃ of temperature, time 2-2.5 minute, this machinery is the discharging on one side of charging on one side, Semen Brassicae campestris is 2-2.5 minute in the residence time of machine the inside, and the meal of then will baked Semen Brassicae campestris wearing into about fineness 70 orders with pulverizer is standby, abbreviation: ground oil seeds.

2, fermentation is not equipped with the sterilization that reaches the sterile filtration system:

(1) pipeline fire bacterium; Carry out for guaranteeing to send out to separate smoothly, must earlier each pipeline be carried out steam sterilizing before the outer car, at first open valve and each pipeline valve of sterile filtration system of each input and output material pipeline, pass through the steam of 0.15 MPa then, allow steam and each pipeline valve UNICOM and exhaust vapour, exhaust is about 40 minutes, then each drain tap of Guaning, allow the interior vapor pressure of pipeline keep 0.15 MPa, keep to reach sterilising effect in 30 minutes.

The sterilization of (2) sterile filtration system: at first throw into and respectively pass in and out valve, pass through the steam of 0.15 MPa then, allow each valve exhaust vapour 30 minutes, be that freezing air is got rid of like this, help sterilization, close each drain tap then, allow the vapor pressure of aseptic system the inside keep 0.15 MPa 1 hour, start air compressor then, open the total filter bottom blow-down valve, can dry up the cotton of strainer the inside like this.Help air and pass through, blow with air compressor machine approximately and can reach standard in 1.5 hours, close sewage draining valve then, allow aseptic system keep the malleation of 0.01 MPa standby.

Two, use culture of strains workshop section:

1, raw material ratio: be called for short nutrient solution, pretreated Semen Brassicae campestris 8%, the corn steep liquor 0.15% of peptone 0.1%, 2 ten thousand unit, oral glucose powder 3%, the nitrogenous agricultural urea 0.2% more than 45, tap water 88.55%.

2, employed equipment: biomicroscope, large vol rotary type bottle swingging machine, 5000 milliliters of triangular flask high-pressure sterilizing pots

3, concrete operations: even by using the material of measuring in the prescription to put into container for stirring, be sub-packed in then in 5000 milliliters the triangular flask, each bottled 500 milliliters, bottleneck is tightened with 6-8 layer gauze, place sterilization in the pressure kettle, when vapor pressure in the pot reaches 0.15 MPa, keep getting final product in 30 minutes, allow pressure kettle leave heating source and cool to zero naturally.Open pressure kettle and take out triangular flask, allow it cool to 28 ℃-30 ℃ naturally, then triangular flask is moved on on the Bechtop, open gauze, each triangular flask inserts test tube bacterium two rings, triangular flask is tied with gauze again, putting into bottle swingging machine cultivates, 30 ℃-31 ℃ of temperature, pH value 4.5-5, to contain 300,000,000-3.5 hundred million bacterium be qualified standby when cell concentration reaches every milliliter of nutrient solution.

4, the cultivation workshop section of one-level, second class inoculum

1. the raw-material recipe ratio of first order seed: pretreated canola 10%, the corn steep liquor 0.25% of glucose powder 2%, 2 ten thousand unit, nitrogenous agricultural urea 0.35% more than 45%, peptone 0.15%, tap water 87.25%

Concrete operations, tap water in will filling a prescription is earlier put in the first class seed pot, and then add other materials successively, start stirrer and carry out reality jar sterilization by steam, vapor pressure reaches 0.15 MPa in jar, keep then cooling to 28 ℃ after one hour--30 ℃, under aseptic condition, the cultured big triangular flask bacterial classification of sterilisable chamber is joined in the first class seed pot with material sucking pipes, the bacterial classification consumption is 1.5% of a first class seed pot material, feeding sterile air then under the stirring that does not stop begins to cultivate, tank pressure is the 0.01-0.015 MPa, 30 ℃-31 ℃ of temperature are cultivated and were measured cell concentration in about 6 hours, and 3.5 hundred million-400,000,000 bacterium are qualified in the middle of every milliliter of seed culture fluid, pH value keeps between the 4.5-5 in whole culturing process, otherwise add acid, alkali is adjusted, and whole culturing process must not surpass 10 hours, and long bacterial classification of time is aging, be unfavorable for fermentation, the consumption of sterile air is that seed culture fluid per minute per ton is with 0.012-0.014 cube.

The I and II seed culture

1, raw-material proportioning

Pretreated canola 14%, the agricultural urea 0.4% of glucose powder 2%, 2 ten thousand unit corn steep liquor, 0.3% fluorine content more than 45%, peptone 0.2%.Tap water 83%.

2, concrete operations: earlier tap water is joined in the secondary seed jar by consumption, start stirrer, and then add other material in the proportioning successively, open the intensification of steam valve feeding steam simultaneously and carry out reality jar sterilization, when vapor pressure reaches 0.15 MPa, keep sterilization 1 hour, steam off then, make that temperature drops to 28 ℃-30 ℃ in the jar, then cultured primary seed solution is extracted in the secondary seed jar and cultivates, the consumption that first order seed is somebody's turn to do is that the 5%-6% of secondary seed solution is advisable, after finishing, feeding no mattress air cultivates under not stopping to stir, tank pressure is the 0.01-0.015 MPa, 30 ℃ of temperature--between 31 ℃ of pH value 4.5-5, the sterile air consumption is 0.012-0.014 cube of a seed culture fluid per minute per ton, cultivate about 6 hours and to measure cell concentration and should be every milliliter of seed culture fluid and contain 4.5 hundred million-500,000,000 bacterium, bud ratio is that 18%-22% is qualified, pH value keeps between the 4.5-5 in whole culturing process, otherwise with acid, alkali is adjusted, whole culturing process must not surpass 8 hours, otherwise bacterial classification is aging, the road fermentation of unfavorable back.

Three, fermentation workshop section

1, raw material ratio: pretreated canola 33%, 2 ten thousand unit corn steep liquor 0.4%, the urea 0.45% of nitrogen content more than 45%, peptone 0.1%, tap water 65%, glucose powder 1%.

2, fermentation; Earlier the tap water in the proportioning is put in the fermentor tank, start stirrer, add other material in the proportioning more successively, after finishing, feeding steam heats, real jar of sterilization, when the vapor pressure in the jar reaches 0.15 MPa, kept 1.5 hours, the middle stirring that does not stop, cool to 30 ℃-21 ℃ then, at this moment more cultured secondary seed solution is extracted into fermentor tank, consumption is the 10%-15% of fermented liquid, adding the back adjusts between the pH value 4.5-5, close each feed valve, feeding sterile air ferments, fermentation initial stage sterile air consumption is a fermented liquid per minute 0.013-0.015 cubic meter per ton, temperature is controlled at 30 ℃-31 ℃ and is advisable, fermentation proceeds to and measures cell concentration and bud ratio about 8-10 hour, cell concentration should be and contained 1.5 hundred million-200,000,000 mattresses in every milliliter of fermented liquid this moment, bud ratio is that 15%-18% is advisable, the consumption that at this moment should strengthen sterile air is a fermented liquid per minute gas consumption 0.015-0.017 cubic meter per ton, pH value is between the 4.5-5, ferment and measured mattress bulk concentration and bud ratio by 20 hours, concentration should be every milliliter of fermented liquid and contains 300,000,000-3.5 hundred million bacterium, bud ratio should be 18%-22%, diesel oil content is that 5%-6% is normal, add the Glucose Liquid 1.5%-2% of the bacterium of having gone out simultaneously, sugar content 5%-6%, purpose is to improve the vigor and the metabolic capacity of bacterial classification, add liquid glucose after 30 minutes, can stop to ventilate, stop stirrer, time is about 4 hours, purpose reduces pH value, pH value drops between the 4-4.2, at this moment start stirrer again, feed sterile air, the sterile air consumption is a fermented liquid per minute 0.015-0.017 cubic meter per ton, the middle running check microbial contamination situation of wanting, straight with biomicroscope alkali, ferment by 35-40 hour, diesel oil content should be 9%-9.5%, the pH value of this moment has been got back between the 4.5-5 again, this moment fermentation enters end, and the fermented liquid of fermentor tank is warmed to 70 ℃ 2 ℃, keeps killing in 30 minutes the diesel oil bacterial classification that ferments, otherwise can reduce diesel yield, whole fermentation process needs 35-45 hour.

Four, neutralization

Five, byproduct---extract glycerine and fodder yeast.

Claims (1)

1. production technique of utilizing the Semen Brassicae campestris fermentation method to produce biofuel; Preparation method of the present invention

(1), pre-treatment of raw material: the pre-treatment of Semen Brassicae campestris: with Semen Brassicae campestris flush away earth, impurity elimination, the back is baked to jaundice with roaster with Semen Brassicae campestris, 110 ℃-115 ℃ of storing temperatures, time 2-2.5 minute, that the ground oil seeds that baked Semen Brassicae campestris is worn into about fineness 70 orders with pulverizer is standby

(2), fermentation is not equipped with and the sterilization of sterile filtration system:

(2-1) pipeline fire bacterium;

Open valve and each pipeline valve of sterile filtration system of each input and output material pipeline, feed the steam of 0.15 MPa, each drain tap is closed in exhaust about 40 minutes, and the pipeline vapor pressure remains on 0.15 MPa, more than 30 minutes;

The sterilization of (2-2) sterile filtration system: throw into and respectively pass in and out valve, feed the steam of 0.15 MPa, allow each valve exhaust vapour more than 30 minutes, freezing air is got rid of sterilization, valve-off allows the vapor pressure of aseptic system the inside keep 0.15 MPa and 1 hour, starts air compressor then, open the total filter bottom blow-down valve, the cotton of strainer the inside is dried up; Help air and pass through, blow with air compressor machine approximately and got final product in 1.5 hours, close sewage draining valve, allow aseptic system keep the malleation of 0.01 MPa standby;

(3). use culture of strains:

(3-1), nutrient solution preparation: pretreated canola 8%,, the corn steep liquor 0.15% of peptone 0.1%, 2 ten thousand unit, oral glucose powder 3%, the nitrogenous agricultural urea 0.2% more than 45, tap water 88.55%;

(3-2), equipment: biomicroscope, large vol rotary type bottle swingging machine, the triangular flask high-pressure sterilizing pot more than 5000 milliliters;

(3-3), concrete operations: even by using the material of measuring in the prescription to put into container for stirring, be sub-packed in then in 5000 milliliters the triangular flask, each bottled 500 milliliters, bottleneck is tightened with 6-8 layer gauze, place sterilization in the pressure kettle, when vapor pressure in the pot reaches 0.15 MPa, keep getting final product in 30 minutes, allow pressure kettle leave heating source and cool to zero naturally; Open pressure kettle and take out triangular flask, allow it cool to 28 ℃-30 ℃ naturally, then triangular flask is moved on on the Bechtop, open gauze, each triangular flask inserts test tube bacterium two rings, triangular flask is tied with gauze again, putting into bottle swingging machine cultivates, 30 ℃-31 ℃ of temperature, pH value 4.5-5, to contain 300,000,000-3.5 hundred million bacterium be qualified standby when the mattress bulk concentration reaches every milliliter of nutrient solution;

(3-4), the cultivation workshop section of one-level, second class inoculum

(3-4.1). the raw-material recipe ratio of first order seed: pretreated canola 10%, the corn steep liquor 0.25% of glucose powder 2%, 2 ten thousand unit, nitrogenous agricultural urea 0.35% more than 45%, peptone 0.15%, tap water 87.25%

Concrete operations, tap water in will filling a prescription is earlier put in the first class seed pot, and then add other materials successively, start stirrer and carry out reality jar sterilization by steam, vapor pressure reaches 0.15 MPa in jar, keep cooling to after one hour 28 ℃-30 ℃ then, under aseptic condition, the cultured big triangular flask bacterial classification of sterilisable chamber is joined in the first class seed pot with material sucking pipes, the bacterial classification consumption is 1.5% of a first class seed pot material, feeding sterile air then under the stirring that does not stop begins to cultivate, tank pressure is the 0.01-0.015 MPa, 30 ℃-31 ℃ of temperature are cultivated and were measured cell concentration in about 6 hours, and 3.5 hundred million-400,000,000 bacterium are qualified in the middle of every milliliter of seed culture fluid, pH value keeps between the 4.5-5 in whole culturing process, otherwise add acid, alkali is adjusted, and whole culturing process must not surpass 10 hours, and long bacterial classification of time is aging, be unfavorable for fermentation, the consumption of sterile air is that seed culture fluid per minute per ton is with 0.012-0.014 cube;

(3-4.2) second class inoculum is cultivated

Raw-material proportioning

Pretreated canola 14%, glucose powder 2%, 2 ten thousand unit corn steep liquor 0.3%, the agricultural urea 0.4% of nitrogen content more than 45%, peptone 0.2%, tap water 83%;

Concrete operations: earlier tap water is joined in the secondary seed jar by consumption, start stirrer, and then add other material in the proportioning successively, open the intensification of steam valve feeding steam simultaneously and carry out reality jar sterilization, when vapor pressure reaches 0.15 MPa, keep sterilization 1 hour, steam off then, make that temperature drops to 28 ℃-30 ℃ in the jar, then cultured primary seed solution is extracted in the secondary seed jar and cultivates, the consumption that first order seed is somebody's turn to do is that the 5%-6% of secondary seed solution is advisable, after finishing, feeding no mattress air cultivates under not stopping to stir, tank pressure is the 0.01-0.015 MPa, between 30 ℃ of-31 ℃ of pH value 4.5-5 of temperature, the sterile air consumption is 0.012-0.014 cube of a seed culture fluid per minute per ton, cultivate about 6 hours and to measure cell concentration and should be every milliliter of seed culture fluid and contain 4.5 hundred million-500,000,000 bacterium, bud ratio is that 18%-22% is qualified, pH value keeps between the 4.5-5 in whole culturing process, otherwise with acid, alkali is adjusted, whole culturing process must not surpass 8 hours, otherwise bacterial classification is aging, the road fermentation of unfavorable back;

(4). fermentation

(4-1), raw material ratio: pretreated canola 33%, 2 ten thousand unit corn steep liquor 0.4%, the urea 0.45% of nitrogen content more than 45%, peptone 0.1%, tap water 65%, glucose powder 1%;

(4-2), fermentation; Water in the proportioning is put in the fermentor tank, start stirrer, add other material in the proportioning more successively, feeding steam heats, real jar of sterilization, when the vapor pressure in the jar reaches 0.15 MPa, kept 1.5 hours, the middle stirring that does not stop, cool to 30 ℃-21 ℃ then, again cultured secondary seed solution is extracted into fermentor tank, consumption is the 10%-15% of fermented liquid, the back is adjusted between the pH value 4.5-5, close each feed valve, feeding sterile air ferments, fermentation initial stage sterile air consumption is a fermented liquid per minute 0.013-0.015 cubic meter per ton, temperature is controlled at 30 ℃-31 ℃ and is advisable, fermentation proceeds to and measures cell concentration and bud ratio about 8-10 hour, cell concentration should be and contained 1.5 hundred million-200,000,000 bacterium in every milliliter of fermented liquid this moment, bud ratio is 15%---18% is advisable, the consumption that at this moment should strengthen sterile air is a fermented liquid per minute gas consumption 0.015-0.017 cubic meter per ton, pH value is between the 4.5-5, ferment and measured bulk concentration and bud ratio by 20 hours, concentration should be every milliliter of fermented liquid and contains 300,000,000-3.5 hundred million bacterium, bud ratio should be 18%-22%, diesel oil content is that 5%-6% is normal, add the Glucose Liquid 1.5%-2% of the bacterium of having gone out simultaneously, sugar content 5%-6%, improve the vigor and the metabolic capacity of bacterial classification, add liquid glucose after 30 minutes, stop to ventilate and stop to stir about 4 hours, reduce pH value, pH value drops between the 4-4.2, at this moment start stirrer again, feed sterile air, the sterile air consumption is a fermented liquid per minute 0.015-0.017 cubic meter per ton, the middle running check microbial contamination situation of wanting, straight with biomicroscope alkali, ferment by 35-40 hour, diesel oil content should be 9%-9.5%, the pH value of this moment has been got back between the 4.5-5 again, this moment, fermentation entered end, the fermented liquid of fermentor tank is warmed to 70 ℃ ± 2 ℃, keep killing in 30 minutes fermentation diesel oil bacterial classification, otherwise can reduce diesel yield, whole fermentation process needs 35-45 hour;

(5), neutralization

In the fermented liquid suction neutralization tank with above fermentor tank, under the stirring that does not stop, be warmed to 80 ℃-85 ℃, add content simultaneously and be the sodium hydroxide about 10% more than 90%, can be as solid sodium hydroxide with using again after 3 times of water-solubleization, this moment, the temperature with neutralization tank was raised to 95--98 ℃, under agitation kept 40 minutes, and then the pressure of neutralization tank adjusted to 0.12 MPa, kept 40-45 minute, purpose is to improve the rate of recovery of glycerine, and then the temperature of neutralization tank dropped to 75 ℃-80 ℃, with phosphoric acid pH value is dropped between the 4-4.2, kept 30 minutes. then at the lime powder that adds fermentation liquid measure 5%, under 75 ℃-80 ℃ situation, kept 40 minutes, the purpose that adds phosphoric acid and lime powder is that the temperature that remaining glucose in the fermented liquid generates after the easy elimination of gluconic acid calcium deposit neutralization tank is dropped to about 45 ℃, earlier with whizzer elimination thalline and impurity such as yeast slurry and rapeseed hull, and then with the more progressive elimination yeast of yeast whizzer, then with filtrate suction storage tank, again through 2 son further elimination residual impurity of ultra-fine filter very much, filtrate is extracted into separating tank staticly settles separation 10-12 hour, gas oil with the upper strata after time reaches sucks holding tank, lower floor is the glycerine sugar water, can send the evaporator tower evaporation, the diesel oil of holding tank is again through boiling water washing 3 times-4 times, the boiling water consumption is 3 times of oil, and then will wash good diesel oil and send into the fractionation of diesel oil dry fractionation device, obtained meeting the biofuel of national standard this moment, this diesel oil can reach the negative 20# of 0#-after measured, because of there is not wax in this fermentation diesel oil, plumbous, objectionable impuritiess such as ammonia, so but the convection drying fractionation is chemically examined qualified packing warehouse-in and is finished product;

(6), byproduct---glycerin extraction

Glycerine is present in the water of separating tank lower floor, and industry claims sugar water, sugar water is delivered in the glycerine evaporator tower evaporated earlier, becomes raw glycerine when glycerol content reaches 75%--85%, and then reach the glycerine that meets national standard, i.e. saponification level glycerine after distillation;

(7), fodder yeast extracts

The yeast that leaches, yeast slurry, the rape shell again through washing, vacuum deodorization, go to hide, add the offal one yellow material of producing W-Gum, fermentation through fodder yeast can become qualified fodder yeast again, industries such as this product is applied to, breeds fish, shrimp, chicken, the fish meal of alternative after measured Denmark import, bone meal formula feed.