CN101664141A - Comprehensive utilization and production process of kudzuvine root - Google Patents
Comprehensive utilization and production process of kudzuvine root Download PDFInfo
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- CN101664141A CN101664141A CN200910307109A CN200910307109A CN101664141A CN 101664141 A CN101664141 A CN 101664141A CN 200910307109 A CN200910307109 A CN 200910307109A CN 200910307109 A CN200910307109 A CN 200910307109A CN 101664141 A CN101664141 A CN 101664141A
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- defibrination
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- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims abstract description 152
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- 238000012545 processing Methods 0.000 claims abstract description 42
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- 241001330002 Bambuseae Species 0.000 claims description 11
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Images
Classifications
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
- Y02A40/10—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
- Y02A40/20—Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/40—Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse
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- Processing Of Solid Wastes (AREA)
- Fertilizers (AREA)
Abstract
The invention discloses a comprehensive utilization and production process of kudzuvine root, which is characterized by comprising the following steps: 1. cleaning; 2. healthy edibles and starch processing process; and 3. methane and manure production process. The flow production line reasonably combines the mature equipment and science, is equipped with an intelligent operation automatic controloperation system and a production automatic operation monitoring system, and has high degree of mechanization with the automation achieving more than 90 percent. The kudzuvine root is processed and produced with 100% utilization factor, is completely converted to full-price commodity through reclamation, replaces power sources, saves energy and reduces emission, saves resources, and has higher eco-environmental effect, thus achieving sustainable development by recycling.
Description
Technical field
The present invention relates to a kind of process of RADIX PUERARIAE processing.
Background technology
At present, the processing method that RADIX PUERARIAE is adopted substantially is with traditional prepared slices of Chinese crude drugs processing and the thick matter technology of producing food starch and bean vermicelli, and most of discarded having lost of the remaining material of processing and use back, a large amount of valency available resources that have have been wasted, the prepared slices of Chinese crude drugs are subjected to progressively eliminating of market simultaneously, starch is subjected to the restriction of like product, causes market plane narrow. and sales volume is few. and price is hanged down state.Trace sth. to its source and on the technical matters method, have technological deficiency:
1. the RADIX PUERARIAE prepared slices of Chinese crude drugs of prepared slices of Chinese crude drugs technology processing, in today of scientific and technological and economic development, Sui the consciousness requirement that the common people pursue health, the inherent medical substance of artificial growth RADIX PUERARIAE does not fundamentally reach former wild contained pharmaceutical quality, so plantation RADIX PUERARIAE medicine materical crude slice market is stagnated, economic worth is low. and profit is thin. and market prospects are secretly right.
2. RADIX PUERARIAE carries out processing and eating starch to the food starch process technology and bean vermicelli puts goods on the market to planting, and has reduced its due economic worth, causes market plane little, and sales volume is few. and price is low, does not produce its due society and economic benefits.
3. RADIX PUERARIAE is carried out the prepared slices of Chinese crude drugs and food starch and bean vermicelli processing, processing prepared slices of Chinese crude drugs consumption back resource abandons fully, and residue abandons substantially after the producing starch bean vermicelli, has wasted resource.
Summary of the invention
The technical problem to be solved in the present invention is, a kind of RADIX PUERARIAE comprehensive utilization manufacturing technique method is provided, this method is based on existing health food, biomass energy, resource recycling, ecological, environmental protective, in conjunction with the due practical value of RADIX PUERARIAE, can realize the recycling of RADIX PUERARIAE edible healthization, energy, resource, small investment, operating cost is low, environmental protection and energy saving, low to overcome the economic worth that RADIX PUERARIAE that prior art exists produces, deficiencies such as waste resource.
Technical scheme of the present invention is as follows: it comprises following process: the first, and cleaning process; The second, edible health product, starch process; The 3rd, biogas, fertilizer production process.
In cleaning process, RADIX PUERARIAE collect transport vehicle through count heavy pound meter heavy after, discharging is stored at the raw material depots, is transported to the manual sorting then and repaiies and select platform, flows to cleaning device after choosing and cleans through repairing; Discarded object after discarded object that pruning is selected and the cleaning flows to fecula preliminary treatment storehouse.
In cleaning process, water for cleaning flows to cleaning device by the water for cleaning circulatory pool, and the water after the cleaning flows to water for cleaning circulatory pool sedimentation and filtration again and recycles, and the external running water of water for cleaning circulatory pool is supplied with and replenished.
In edible product, starch process, give the dehydration of dehydration air-dry machine after RADIX PUERARIAE cleans and dispose, measure after taking off most RADIX PUERARIAE surface clean moisture, flow to the defibrination centrifuge after the metering and carry out defibrination of the mat woven of fine bamboo strips;
The solid that the defibrination centrifuge filters through the first time flows to for the second time, and the defibrination centrifuge carries out the defibrination second time;
For the first time defibrination and for the second time defibrination through the liquid of centrifugal filtration, pass through the pressure filtration of double-filtration pump (working pressure filter pump) respectively after, be conveyed into sterilization vacuum and low temperature fresh-keeping warehouse and deposit processing edible health product and deep processing;
The liquid that sterilization vacuum and low temperature fresh-keeping warehouse is deposited is through after measuring, it is synthetic to flow to the female reactor interpolation batching blending reaction of overflowing of batching, synthetic liquid flows to the vacuum-packed wire wrapping product of sterilization, the required heat energy of sterilization vacuum packet wiring is carried by the steam boiler connecting line and is supplied with, and the edible health product after the packing flows to warehouse for finished product and deposits sale;
Flow to the starch sedimentation separator through the solid of the defibrination centrifuge filtration second time and the solid of filtering through filter pump;
The starch that the starch sedimentation separator separates is conveyed into the starch dryer and dehydrates, the required heat energy of drying and dewatering connects hot water piping by steam boiler and carries supply, deviate from water and flow to the boiler injector, be conveyed into the starch stock after the starch drying and put sale and deep processing by the delivery pump connecting line;
The water that the starch sedimentation separator separates is conveyed into the cycling use of water pond, and circulation is supplied with the defibrination centrifuge and replenished water, and the concentration liquid that the starch sedimentation separator separates is conveyed into dry method biogas fermentation storehouse and wet method marsh-gas fermentation tank fermentation methane; The waste residue that the starch sedimentation separator separates is conveyed into the preliminary treatment of fermenting of fecula preliminary treatment storehouse, is conveyed into dry method biogas fermentation storehouse fermentation methane after the fermentation preliminary treatment.
In edible health product, starch process, defibrination of the mat woven of fine bamboo strips and for the second time during defibrination the insufficient section water yield by the supply of aquae destillata regulating reservoir, this aquae destillata by the boiler steam after pipeline connects cooling tower cooling conversion liquid state, flow to the aquae destillata regulating reservoir by the delivery pump connecting line, the water that separates after by starch sedimentation of some amount of makeup water flows to circulating water pool through the delivery pump connecting line again, is carried to replenish by the delivery pump connecting line again and gives defibrination of the mat woven of fine bamboo strips, defibrination use for the second time.
In biogas, fertilizer production process, the biogas of dry method biogas fermentation storehouse fermentation flows to biogas desulfurization knot screen impurity desulfurization, flow to biogas behind the impurity desulfurization and deposit the gas tank storage, flow to biogas purification devices purification process then, flow to the methane gas depots after the purification process and store, that this storing methane combustion gas flows to is automobile-used, domestic gas filling station and generating set;
The methane liquid of dry method biogas fermentation storehouse fermentation flows to wet method marsh-gas fermentation tank fermentation methane; Fermentation methane required heat energy in dry method biogas fermentation storehouse connects hot water piping by steam boiler and carries supply;
Biogas slag Shu send Give separator behind the fermentation methane of dry method biogas fermentation storehouse, oversize Shu send Give dry method biogas fermentation storehouse is fermentation methane once more, the processing of screenings Shu send Give ball mill, ball milling processing back Shu send Give batching blending tank adds the batching blending, the Shu send Give organic fertilizer granulation machine granulation of batching blending back, Shu send Give drying plant dehydrates after the granulation, flows to packing machine after the drying and packs, and is conveyed into agricultural high-efficiency organic fertilizer stock after the packing and puts sale;
The required heat energy of drying and dewatering connects hot water piping by steam boiler to be supplied with, and the water of deviating from flows to the boiler injector by the delivery pump connecting line;
Liquid behind the wet method marsh-gas fermentation tank fermentation methane flows to the crop foliage fertilizer process units and produces foliage fertilizer, and foliage fertilizer is conveyed into the stock and puts sale;
The biogas of wet method marsh-gas fermentation tank fermentation flows to biogas desulfurization knot screen impurity desulfurization by the delivery pump connecting line, with the biogas of dry method biogas fermentation storehouse fermentation disposal applications together.
In biogas, fertilizer production process, the unnecessary methane liquid of wet method marsh-gas fermentation tank fermentation methane flows to dry method biogas fermentation storehouse fermentation methane by the delivery pump connecting line, and the methane liquid that wet-fermentation and dry method fermentation are produced is regulated application mutually.
The above processing procedure disposes intellectualized operation autocontrol operation system and production automation monitoring operation system.
Through above production process, RADIX PUERARIAE is converted to commodity fully, economic benefit improves, and energy-saving and emission-reduction, alternative energy source economizes on resources, ecological, environmental protective, social benefit is good, yet has realized that RADIX PUERARIAE comes from from the purpose that returns edible healthization in nature, energy, resource, recycling ecological, environmental protective.The present invention has the RADIX PUERARIAE degree of depth product that obtains of processing of refining: edible health product, starch, methane combustion gas, leaves of plants leaven, high-quality and efficient agricultural fertilizer etc., fully represent the due society of RADIX PUERARIAE, environment, economic benefits, reached 100% recycling substantially.
Production-lines of the present invention adopt mature equipment and scientific and reasonable combination, dispose intellectualized operation autocontrol operation system and production automation monitoring operation system, the mechanization degree height, and automation reaches more than 90%.
The present invention has following significant effect:
1. RADIX PUERARIAE utilization rate 100% processing, resource is converted to the full price commodity completely, and resource reaches 100% substantially and returns in nature;
2. the integrated advanced design of production processing line, the combination configuration is novel.In practice operation, be verified: starch processing. the processing of edible health product. methane combustion gas processing. the processing of leaves of plants leaven. the recycling height of seriation ecological, environmental protective highly efficient regeneration such as high-quality and efficient agricultural fertilizer processing add the matter processing, have fully represented the due society of RADIX PUERARIAE. environment. economic benefits.
3. alternative energy source, energy-saving and emission-reduction economize on resources, and the recycling utilization sustainable development has the high ecological environmental effect.
Description of drawings
Fig. 1 is flow sheet equipment schematic diagram of the present invention, total figure; Because this system is huge, content is many, is subjected to the restriction of length (paper size), and some flow process is simplified, and has only provided processing equipment among the figure, carries not signal of kind equipment for connection commonly used.
Fig. 2 is a schematic flow sheet of the present invention, the process simplification figure of Fig. 1;
Fig. 3 is flow sheet equipment schematic diagram of the present invention, cleaning process schematic diagram;
Fig. 4 is flow sheet equipment schematic diagram of the present invention, edible health product, starch process schematic diagram;
Fig. 5 is flow sheet equipment schematic diagram of the present invention, biogas, fertilizer production process schematic diagram.
The specific embodiment
Embodiments of the invention:, be illustrated as follows to concrete implementing process ways and means in conjunction with the accompanying drawings according to process route of the present invention:
The present invention includes three processes, promptly the first, cleaning process; The second, edible health product, starch process; The 3rd, biogas, fertilizer production process.Total process is anticipated as shown in Figure 1 and Figure 2.
The first, cleaning process.As shown in Figure 3, RADIX PUERARIAE collect transport vehicle through count heavy pound meter heavy after, discharging is stored at the raw material depots, is transported to the manual sorting through belt type conveyer and repaiies and select platform, flows to cleaning device by belt type conveyer through repairing after choosing, and cleans.
Water for cleaning flows to cleaning device by the water for cleaning circulatory pool through the delivery pump connecting line, water after the cleaning flows to the water for cleaning circulatory pool by the delivery pump connecting line, sedimentation and filtration is given the cleaning device water for cleaning after the water pump connecting line is carried to supply water, and the external running water of water for cleaning circulatory pool is supplied with and replenished.
Discarded object after discarded object that pruning is selected and the cleaning flows to fecula preliminary treatment storehouse by belt type conveyer.
The second, edible health product, starch process.As shown in Figure 4, RADIX PUERARIAE cleans the back and flows to dehydration air-dry machine dehydration disposal by belt type conveyer, flow to the metering of electronics metering pound by belt type conveyer after taking off most RADIX PUERARIAE surface clean moisture, the metering back flows to defibrination of the defibrination centrifuge mat woven of fine bamboo strips by belt type conveyer.
The insufficient section water yield is supplied water to the defibrination centrifuge by aquae destillata regulating reservoir supply-water pump connecting line during defibrination of the mat woven of fine bamboo strips, aquae destillata by the boiler steam after pipeline connects cooling tower cooling conversion liquid state, flow to the aquae destillata regulating reservoir by the delivery pump connecting line, the water that separates after by starch sedimentation of some amount of makeup water flows to circulating water pool through the delivery pump connecting line again, is carried by the delivery pump connecting line and replenishes to defibrination water of the mat woven of fine bamboo strips.
The liquid of defibrination centrifugal filtration for the first time flows to filter pump by the delivery pump connecting line and carries out pressure filtration, is conveyed into sterilization vacuum and low temperature fresh-keeping warehouse through the liquid of twice pressure filtration and deposits processing edible health product and deep processing.
The solid that the defibrination centrifuge filters through the first time flows to the defibrination centrifuge defibrination second time for the second time by the belt type conveyer connection.
For the second time the insufficient section water yield is supplied water to the defibrination centrifuge second time by aquae destillata regulating reservoir supply-water pump connecting line during defibrination, aquae destillata by the boiler steam after pipeline connects cooling tower cooling conversion liquid state, flow to the aquae destillata regulating reservoir by the delivery pump connecting line, some amount of makeup water is divided after by starch sedimentation and is dried uply flowed to circulating water pool through the delivery pump connecting line again, is carried by the delivery pump connecting line and replenishes to secondary defibrination water.
The liquid of defibrination centrifugal filtration for the second time flows to filter pump by the delivery pump connecting line and carries out pressure filtration (filter pump among Fig. 3 is the pressure filtration pump), is conveyed into sterilization vacuum and low temperature fresh-keeping warehouse through the liquid of twice pressure filtration and deposits processing edible health product and deep processing.
After the liquid that sterilization vacuum and low temperature fresh-keeping warehouse is deposited is measured by delivery pump connecting line meter electronics, it is synthetic to flow to the female reactor interpolation batching blending reaction of overflowing of batching, synthetic liquid flows to the vacuum-packed wire wrapping product of sterilization by the delivery pump connecting line, the required heat energy of sterilization vacuum packet wiring is carried by the steam boiler connecting line and is supplied with, and the edible health product of packing is conveyed into the stock by the belt type conveyer connection and puts sale.
The solid that the defibrination centrifuge filters through the second time is conveyed into the starch sedimentation separator by the belt type conveyer connection, and the solid of filtering through the pressure filtration pump is conveyed into the starch sedimentation separator by the belt type conveyer connection.
The water that the starch sedimentation separator separates is conveyed into the cycling use of water pond by the delivery pump connecting line, circulation is supplied with the defibrination centrifuge and is replenished water, and the concentration liquid that the starch sedimentation separator separates is conveyed into dry method biogas fermentation storehouse and wet method marsh-gas fermentation tank fermentation methane by the delivery pump connecting line.
The starch that the starch sedimentation separator separates is conveyed into the starch dryer by the belt type conveyer connection and dehydrates, the required heat energy of drying and dewatering connects hot water piping by steam boiler and carries supply, deviate from water and flow to the boiler injector, be conveyed into starch stock list marketing and deep processing by the belt type conveyer connection after the starch drying by the delivery pump connecting line.
The slag that the starch sedimentation separator separates is connected by belt type conveyer and is conveyed into the preliminary treatment of fermenting of fecula preliminary treatment storehouse, is connected by belt type conveyer after the fermentation preliminary treatment to be conveyed into dry method biogas fermentation storehouse fermentation methane.
The 3rd, biogas, fertilizer production process.As shown in Figure 5, the biogas of dry method biogas fermentation storehouse fermentation flows to biogas desulfurization knot screen impurity desulfurization by the delivery pump connecting line, flow to biogas by the delivery pump connecting line behind the impurity desulfurization and deposit the gas tank storage, store gas and flow to biogas purification devices purification process by the delivery pump connecting line, flow to the methane gas depots by the delivery pump connecting line after the purification process and store, the storing methane combustion gas flows to automobile-used and civilian gas station and generating set by the delivery pump connecting line.
The methane liquid of dry method biogas fermentation storehouse fermentation flows to wet method marsh-gas fermentation tank fermentation methane by the delivery pump connecting line.Fermentation methane required heat energy in dry method biogas fermentation storehouse connects hot water piping by steam boiler and carries supply.
Biogas slag behind the fermentation methane of dry method biogas fermentation storehouse connects Shu send Give screening machine by belt type conveyer, and oversize connects Shu send Give dry method biogas fermentation storehouse fermentation methane once more by belt type conveyer.Screenings connects the processing of Shu send Give ball mill by belt type conveyer; ball milling processing back connects Shu send Give batching blending tank by belt type conveyer and adds the batching blending; batching blending back connects the granulation of Shu send Give organic fertilizer granulation machine by belt type conveyer; connecting Shu send Give dryer by belt type conveyer after the granulation dehydrates; flow to the baling line packing by the belt type conveyer connection after dry, the packing back is conveyed into agricultural high-efficiency organic fertilizer stock by the belt type conveyer connection and puts city's sale.
The required heat energy of drying and dewatering connects hot water piping by steam boiler and carries supply, and the water of deviating from flows to the boiler injector by the delivery pump connecting line.
The biogas of wet method marsh-gas fermentation tank fermentation flows to biogas desulfurization knot screen impurity desulfurization by the delivery pump connecting line, with the biogas of dry method biogas fermentation storehouse fermentation disposal applications together.
The unnecessary methane liquid of wet method marsh-gas fermentation tank fermentation methane flows to the biogas that ferments in dry method biogas fermentation storehouse by the delivery pump connecting line, and the methane liquid that wet-fermentation and dry method fermentation are produced is regulated application mutually.
Liquid behind the wet method marsh-gas fermentation tank fermentation methane flows to the crop foliage fertilizer process units by the delivery pump connecting line and produces foliage fertilizer, and foliage fertilizer is conveyed into inventory sale by the delivery pump connecting line.
Process of the present invention all adopts the equipment of prior art, and has disposed intellectualized operation autocontrol operation system and the production automation monitoring operation system that is suitable for that improve.
Be the process of manufacture of 100 tons of fresh RADIX PUERARIAEs below:
1. collect ecosystem plant fresh RADIX PUERARIAE by vehicles drive after counting heavy pound meter and weighing 100 tons, discharging is at the raw material depots, being transported to the manual sorting through belt type conveyer repaiies and selects platform, flow to cleaning device by belt type conveyer after choosing and clean through manually repairing, water for cleaning connects the water for cleaning circulatory pool through pipeline and carries supply, water after the cleaning flows to the water for cleaning circulatory pool cycle applications of sedimentation and filtration through the water pump connecting line, the external running water of water for cleaning circulatory pool is supplied with and is replenished, external running water is supplied with 10 tons of water, and the water for cleaning total amount is finished cleaning for 10 tons.The discarded object that discarded object that cleans and pruning are selected is transported to fecula preliminary treatment storehouse by belt type conveyer.
2. clean clean RADIX PUERARIAE and flow to the air-dry dehydration disposal of air blast by belt type conveyer, air-dry take off most RADIX PUERARIAE surface clean moisture after, flowing to the metering of electronics metering pound by belt type conveyer is 98.2 tons, and the metering back flows to defibrination of the defibrination centrifuge mat woven of fine bamboo strips by belt type conveyer.
Supply water 16 tons of aquae destillatas to the defibrination centrifuge by aquae destillata regulating reservoir supply-water pump connecting line during defibrination of the mat woven of fine bamboo strips, aquae destillata by the boiler steam after pipeline connects cooling tower cooling conversion liquid state, flow to the aquae destillata regulating reservoir by the delivery pump connecting line, supply with the defibrination centrifuge by the delivery pump connecting line.
The liquid of defibrination centrifugal filtration flows to pressure filtration pump filtration for the first time by the delivery pump connecting line for the first time, through the first time pressure filtration pump filtered liquid flow to pressure filtration pump for the second time by the delivery pump connecting line, through the second time pressure filtration pump filtered liquid be conveyed into sterilization vacuum and low temperature fresh-keeping warehouse by the delivery pump connecting line and deposit processing edible health product.
The slag that defibrination centrifuge defibrination filters through the first time flows to the defibrination centrifuge defibrination second time for the second time by the belt type conveyer connection.
Supply water 15 tons by aquae destillata regulating reservoir supply-water pump connecting line during defibrination for the second time and give defibrination centrifuge for the second time, aquae destillata by the boiler steam after pipeline connects cooling tower cooling conversion liquid state, flow to the aquae destillata regulating reservoir by the delivery pump connecting line, supply with the defibrination centrifuge by the delivery pump connecting line.
Defibrination centrifuge filtered liquid flows to pressure filtration pump for the first time by the delivery pump connecting line for the second time, through the first time pressure filtration pump filtered liquid flow to pressure filtration pump for the second time by the delivery pump connecting line, through the second time pressure filtration pump filtered liquid be conveyed into sterilization vacuum and low temperature fresh-keeping warehouse by the delivery pump connecting line and deposit processing edible health product.
3. sterilization vacuum and low temperature fresh-keeping warehouse is to adopt the vacuum machine to implement vacuum state in space, whole storage area, and the anion that adopts anion generator to produce under vacuum state is sterilized,, simultaneously full space, storage area adopts cryogenic temperature control fresh-keeping.
The liquid that leaves sterilization vacuum and low temperature fresh-keeping warehouse in is 65.38 tons by delivery pump connecting line electronics metering total amount and flows in the female reactor that overflows of batching, carry the interpolation batching by the metering of delivery pump connecting line meter electronics: ecosystem honey is concocted for 3.5 tons and is reacted synthetic, liquid after synthetic flows to the vacuum-packed wire wrapping product of sterilization by 68.88 tons of delivery pump connecting line meter electronics meterings, the required heat energy of sterilization vacuum packet wiring is carried by the steam boiler connecting line and is supplied with, and the ecosystem edible health product of packing is conveyed into the stock by the belt type conveyer connection and puts sale.
4. the solids that solids that the defibrination centrifuge filters and pressure filtration pump filter through the second time is connected by belt type conveyer and is conveyed into the starch sedimentation separator.
The water that separates behind the starch sedimentation is conveyed into the cycling use of water pond by the delivery pump connecting line, and circulation is supplied with the defibrination centrifuge and replenished water.
The concentration liquid that separates behind the starch sedimentation is conveyed into dry method biogas fermentation storehouse and wet method marsh-gas fermentation tank fermentation methane by the delivery pump connecting line.
Starch after starch sedimentation separates is conveyed into the starch dryer by the belt type conveyer connection and dehydrates, and it is that 15.1 tons of starch warehouse-ins are deposited list marketing that dried matter starch flows to electronics metering total amount by the belt type conveyer connection.
The required heat energy of drying machine drying dehydration connects hot water piping by steam boiler and carries supply, and deviate from water and flow to the boiler injector by the delivery pump connecting line,
Slag after starch sedimentation separates is conveyed into fecula preliminary treatment storehouse by the belt type conveyer connection and ferments 7 days time of preliminary treatment, is conveyed into dry method biogas fermentation storehouse fermentation methane by the belt type conveyer connection after the fermentation preliminary treatment.
5. after the fecula preliminary treatment in the box-like dry method biogas fermentation of the Shu send Jin Ru Group storehouse, close the sealing door, heat supply is heated and is fermented 35 days, sprays fermenting agent by built-in shower nozzle midway, and the biogas of fermenting and producing flows to the washing desulfurization by the pipeline gasing pump and takes off assorted device impurity desulfurization.
Adopt existing natural gas impurity desulfurization Processes and apparatus impurity desulfurization, flow to air accumulator by the pipeline gasing pump again, air accumulator gas storage flows to the biogas purification devices by the pipeline gasing pump and removes carbon dioxide, adopt lime absorption decarburization, it is 9.0 tons through electronics metering total amount that lime after the decarburization is converted into calcium bicarbonate, be used to produce the usefulness of coating, biogas after the decarburization is converted into 6750 cubes of the combustion gas (biogas that comprises wet method marsh-gas fermentation tank fermenting and producing) of content 98% above methane matter, processing is conveyed into the methane gas hold-up tank by gas transmission line after purifying, and flows to automobile-used gas station through gas transmission line again.
Biogas slag after the box-like dry method biogas fermentation of Group storehouse produces the biogas combustion gas divides selection by the defeated Give screen-dividing machine that send of belt type conveyer; oversize is by the box-like dry method biogas fermentation of belt type conveyer Shu send Hui Group storehouse secondary fermentation; screenings flows to the ball milling mechanical process by belt type conveyer; processing is handled the back and is conveyed into automatic gauge batching blending reactor (jar) by belt type conveyer; add 3.0 tons of reaction blendings of nitrogen phosphorus potassium comprehensive nutrient index reached GB and Peng Run soil; reaction blending back flows to the comminutor granulation by belt type conveyer; flow to dryer by belt type conveyer after the granulation; the oven dry back flows to packing machine by belt type conveyer, and metering 30.1 tons of water-soluble efficient agricultural compoiste fertilizers in packing back are conveyed into the stock by belt type conveyer and put sale.
Dry method biogas fermentation storehouse required heat energy when fermentation methane connects hot water piping by steam boiler and carries supply,
The required heat energy of fertilizer drying and dewatering connects hot water piping by steam boiler and carries supply, and the water of deviating from flows to the boiler injector by the delivery pump connecting line.
6. the biogas of wet method marsh-gas fermentation tank fermentation flows to biogas desulfurization knot screen impurity desulfurization by the delivery pump connecting line, with the biogas of dry method biogas fermentation storehouse fermentation disposal applications together.
The unnecessary methane liquid of wet method marsh-gas fermentation tank fermentation methane flows to the biogas that ferments in dry method biogas fermentation storehouse by the delivery pump connecting line, and the methane liquid that wet-fermentation and dry method fermentation are produced is regulated application mutually.
Liquid behind the wet method marsh-gas fermentation tank fermentation methane flows to the crop foliage fertilizer process units by the delivery pump connecting line and produces foliage fertilizer, and the foliage fertilizer process units is by filter. the blending agitator tank. and the concentration response still. delivery pump. pipe line Group becomes.Carry the liquid of marsh-gas fermentation tank fermentation to concentrate for the concentration response still by the delivery pump connecting line, prepare burden by flowing to the blending agitator tank after the filtration of delivery pump connecting line filter after concentrating: tobacco leaf tar carries out stir-concoction for 0.5 ton, and the blending back is put in storage by 5.2 tons of foliage fertilizers of delivery pump connecting line conveying and deposited sale.
Heat energy required when concentrating with the blending stirring is connected hot water piping conveying supply by steam boiler.
100 tons of fresh RADIX PUERARIAEs are through processing, and the output product has: 68.88 tons of liquid edible health product. 15.1 tons of starch. and 6750.0 cubes of methane combustion gas. 30.1 tons of agricultural fertilizers. 5.2 tons of agricultural organic foliar fertilizers. 9.0 tons of calcium bicarbonates.The product sample presentation detects and all reaches national standard or high-quality quality.Do not have solid-state during production operation. liquid state. gas is feared three waste discharge.
Claims (8)
1. a RADIX PUERARIAE fully utilizes manufacturing technique method, and it is characterized in that: it comprises following process: the first, and cleaning process; The second, edible health product, starch process; The 3rd, biogas, fertilizer production process.
2. RADIX PUERARIAE comprehensive utilization manufacturing technique method according to claim 1, it is characterized in that: in cleaning process, RADIX PUERARIAE collect transport vehicle through count heavy pound meter heavy after, discharging is stored at the raw material depots, be transported to the manual sorting then and repair and select platform, flow to cleaning device after choosing and clean through repairing; Discarded object after discarded object that pruning is selected and the cleaning flows to fecula preliminary treatment storehouse.
3. RADIX PUERARIAE comprehensive utilization manufacturing technique method according to claim 2, it is characterized in that: in cleaning process, water for cleaning flows to cleaning device by the water for cleaning circulatory pool, water after the cleaning flows to water for cleaning circulatory pool sedimentation and filtration again and recycles, and the external running water of water for cleaning circulatory pool is supplied with and replenished.
4. RADIX PUERARIAE comprehensive utilization manufacturing technique method according to claim 1, it is characterized in that: in edible product, starch process, giving the dehydration of dehydration air-dry machine after RADIX PUERARIAE cleans disposes, measure after taking off most RADIX PUERARIAE surface clean moisture, flow to the defibrination centrifuge after the metering and carry out defibrination of the mat woven of fine bamboo strips;
The solid that the defibrination centrifuge filters through the first time flows to for the second time, and the defibrination centrifuge carries out the defibrination second time;
For the first time defibrination and for the second time defibrination through the liquid of centrifugal filtration, pass through the pressure filtration of double-filtration pump respectively after, be conveyed into sterilization vacuum and low temperature fresh-keeping warehouse and deposit processing edible health product and deep processing;
The liquid that sterilization vacuum and low temperature fresh-keeping warehouse is deposited is through after measuring, it is synthetic to flow to the female reactor interpolation batching blending reaction of overflowing of batching, synthetic liquid flows to the vacuum-packed wire wrapping product of sterilization, the required heat energy of sterilization vacuum packet wiring is carried by the steam boiler connecting line and is supplied with, and the edible health product after the packing flows to warehouse for finished product and deposits sale;
Flow to the starch sedimentation separator through the solid of the defibrination centrifuge filtration second time and the solid of filtering through filter pump;
The starch that the starch sedimentation separator separates is conveyed into the starch dryer and dehydrates, the required heat energy of drying and dewatering connects hot water piping by steam boiler and carries supply, deviate from water and flow to the boiler injector, be conveyed into the starch stock after the starch drying and put sale and deep processing by the delivery pump connecting line;
The water that the starch sedimentation separator separates is conveyed into the cycling use of water pond, and circulation is supplied with the defibrination centrifuge and replenished water, and the concentration liquid that the starch sedimentation separator separates is conveyed into dry method biogas fermentation storehouse and wet method marsh-gas fermentation tank fermentation methane; The waste residue that the starch sedimentation separator separates is conveyed into the preliminary treatment of fermenting of fecula preliminary treatment storehouse, is conveyed into dry method biogas fermentation storehouse fermentation methane after the fermentation preliminary treatment.
5. RADIX PUERARIAE comprehensive utilization manufacturing technique method according to claim 4, it is characterized in that: at edible product, in the starch process, defibrination of the mat woven of fine bamboo strips and for the second time during defibrination the insufficient section water yield by the supply of aquae destillata regulating reservoir, this aquae destillata by the boiler steam after pipeline connects cooling tower cooling conversion liquid state, flow to the aquae destillata regulating reservoir by the delivery pump connecting line, the water that separates after by starch sedimentation of some amount of makeup water flows to circulating water pool through the delivery pump connecting line again, is carried by the delivery pump connecting line and replenishes to defibrination of the mat woven of fine bamboo strips, defibrination uses for the second time.
6. RADIX PUERARIAE comprehensive utilization manufacturing technique method according to claim 1, it is characterized in that: in biogas, fertilizer production process, the biogas of dry method biogas fermentation storehouse fermentation flows to biogas desulfurization knot screen impurity desulfurization, flow to biogas behind the impurity desulfurization and deposit the gas tank storage, flow to biogas purification devices purification process then, flow to the methane gas depots after the purification process and store, that this storing methane combustion gas flows to is automobile-used, domestic gas filling station and generating set;
The methane liquid of dry method biogas fermentation storehouse fermentation flows to wet method marsh-gas fermentation tank fermentation methane; Fermentation methane required heat energy in dry method biogas fermentation storehouse connects hot water piping by steam boiler and carries supply;
Biogas slag Shu send Give separator behind the fermentation methane of dry method biogas fermentation storehouse, oversize Shu send Give dry method biogas fermentation storehouse is fermentation methane once more, the processing of screenings Shu send Give ball mill, ball milling processing back Shu send Give batching blending tank adds the batching blending, the Shu send Give organic fertilizer granulation machine granulation of batching blending back, Shu send Give drying plant dehydrates after the granulation, flows to packing machine after the drying and packs, and is conveyed into agricultural high-efficiency organic fertilizer stock after the packing and puts sale;
The required heat energy of drying and dewatering connects hot water piping by steam boiler to be supplied with, and the water of deviating from flows to the boiler injector by the delivery pump connecting line;
Liquid behind the wet method marsh-gas fermentation tank fermentation methane flows to the crop foliage fertilizer process units and produces foliage fertilizer, and foliage fertilizer is conveyed into the stock and puts sale;
The biogas of wet method marsh-gas fermentation tank fermentation flows to biogas desulfurization knot screen impurity desulfurization by the delivery pump connecting line, with the biogas of dry method biogas fermentation storehouse fermentation disposal applications together.
7. RADIX PUERARIAE comprehensive utilization manufacturing technique method according to claim 6, it is characterized in that: in biogas, fertilizer production process, the unnecessary methane liquid of wet method marsh-gas fermentation tank fermentation methane flows to dry method biogas fermentation storehouse fermentation methane by the delivery pump connecting line, and the methane liquid that wet-fermentation and dry method fermentation are produced is regulated application mutually.
8. RADIX PUERARIAE comprehensive utilization manufacturing technique method according to claim 1, it is characterized in that: described processing procedure disposes intellectualized operation autocontrol operation system and production automation monitoring operation system.
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| CN2009103071099A CN101664141B (en) | 2009-09-17 | 2009-09-17 | Comprehensive utilization and production process of kudzuvine root |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102754680A (en) * | 2012-06-26 | 2012-10-31 | 李玉毕 | Storing and fresh-keeping method of fresh radix puerariae |
| CN104651218A (en) * | 2015-01-27 | 2015-05-27 | 深圳市海吉星环保有限责任公司 | Coupling utilization system and method of anaerobic fermentation of fruit and vegetable wastes and afterheat of bio-gas generator |
| CN107361331A (en) * | 2017-06-28 | 2017-11-21 | 防城港市防城区锦发种植专业合作社 | A kind of RADIX PUERARIAE method of comprehensive utilization |
| CN107410978A (en) * | 2017-06-28 | 2017-12-01 | 防城港市防城区锦发种植专业合作社 | A kind of method of Pachyrhizua angulatus comprehensive utilization |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1126761C (en) * | 2001-06-23 | 2003-11-05 | 湖南金健米业股份有限公司 | Industrial kudzu vine starch producing process |
| CN1331419C (en) * | 2004-11-04 | 2007-08-15 | 宋狄泉 | Process for preparing instant-dissolve kudzuvine root powder |
-
2009
- 2009-09-17 CN CN2009103071099A patent/CN101664141B/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102754680A (en) * | 2012-06-26 | 2012-10-31 | 李玉毕 | Storing and fresh-keeping method of fresh radix puerariae |
| CN104651218A (en) * | 2015-01-27 | 2015-05-27 | 深圳市海吉星环保有限责任公司 | Coupling utilization system and method of anaerobic fermentation of fruit and vegetable wastes and afterheat of bio-gas generator |
| CN107361331A (en) * | 2017-06-28 | 2017-11-21 | 防城港市防城区锦发种植专业合作社 | A kind of RADIX PUERARIAE method of comprehensive utilization |
| CN107410978A (en) * | 2017-06-28 | 2017-12-01 | 防城港市防城区锦发种植专业合作社 | A kind of method of Pachyrhizua angulatus comprehensive utilization |
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| CN101664141B (en) | 2012-07-11 |
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