CN104016505A - Method for preparing products by using maize straw and fresh sweet potato yellow serofluid - Google Patents

Method for preparing products by using maize straw and fresh sweet potato yellow serofluid Download PDF

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CN104016505A
CN104016505A CN201310061967.6A CN201310061967A CN104016505A CN 104016505 A CN104016505 A CN 104016505A CN 201310061967 A CN201310061967 A CN 201310061967A CN 104016505 A CN104016505 A CN 104016505A
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supernatant
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CN104016505B (en
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盛银河
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    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P60/00Technologies relating to agriculture, livestock or agroalimentary industries
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    • Y02P60/87Re-use of by-products of food processing for fodder production

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Abstract

The invention provides a method for preparing products by using maize straw and fresh sweet potato yellow serofluid. The method is characterized in that yellow serofluid generated when fresh sweet potato is used for preparing starch has the characteristics of strong water absorbing capacity and poor viscidity; when the yellow serofluid is pressurized by 0.1-0.23 Mpa in a closed container, the yellow serofluid is released into a precipitation separation pool to promote natural precipitation of the yellow serofluid and quick layering from water, the upper layer is represented by yellow serofluid supernatant 5UVA5a, and the obtained supernatant can reach the national discharge standard after being treated; the lower layer is represented by yellow serofluid subsidence liquid 5UVA5b, the separated yellow serofluid subsidence liquid 5UVA5b, maize straw powder and the like are mixed, treated and dried to obtain a product with the hardness of 1.8-3.2kg and ball particle diameter being 0.5-10mm. By the method, the technical problems that yellow serofluid and straw pollute the environment, the investment in an anaerobic reactor for alternative utilization is high, the equipment utilization rate is low, and the deep-processing of sweet potato and the comprehensive utilization of straws are seriously influenced are solved.

Description

Maize straw and fresh sweet potatoes (sweet potato) yellow seriflux is made the method for product
Technical field
The present invention relates to one and be applicable to Ipomoea batatas (formal name used at school: Ipomoea batatas), have another name called sweet potato, sweet potato, sweet potato, pachyrhizus, sweet potato, line sweet potato, sweet potato, golden potato, yam, Zhu's potato, pillow potato etc., particularly the Ipomoea batatas of starch producing (sweet potato) carries out starch isolation when 1~60 day left and right after results, and its starch productive rate is the highest.And utilizing new fresh sweet potatoes (sweet potato) in starch producing time institute water consumption to be: new fresh sweet potatoes (sweet potato) is 1: 3.5 with the ratio of water consumption, do not comprise clean that new fresh sweet potatoes (sweet potato) produces containing earth water, and 3 tons of new fresh sweet potatoes of per mu yield now (sweet potato), 1 ton of new fresh sweet potatoes of every processing (sweet potato) is just produced when starch can 3.5 tons of yellow serifluxes of output, and 3 tons of fresh sweet potatoes of processing (sweet potato) production starch hourly water consumption is 10.5 tons, the yellow seriflux producing is 10.5 tons.The yellow seriflux quantity that when the new fresh sweet potatoes of annual results (sweet potato), underground well water starch producing used produces is very big, its investment of yellow seriflux that adopts the new fresh sweet potatoes of anaerobism producer processing to produce is huge, with the pollution of digging pit or small-sized dam interception nature digestion method easily produces surrounding enviroment.
The harvest corn phase is first about 30 days of Ipomoea batatas (sweet potato) harvesting time, when harvest corn, produce a large amount of maize straws, part is used for direct returning to farmland or carries out feed ensiling and be pressed into sheet material and make stalk fuel and generating raw material and marsh gas raw materials, the method that the yellow seriflux that the maize straw of its remainder produces when carrying out seasoning or drying rear pulverizing with processing fresh Ipomoea batatas (sweet potato) production starch is produced spherical feed auxiliary material and spherical biology soil-moisture conservation fertilizer, relating to specifically one, to utilize yellow seriflux to have water-retaining capacity strong, the characteristic that viscosity is poor, discharge through pressurization, impel yellow seriflux to accelerate precipitated and separated in 5UVA precipitate and separate pond, be that yellow seriflux is layered as upper water 5A5a and represents, the yellow slurry of lower sediment thing represents with 5A5b, the water on upper strata represents with yellow slurry supernatant water liquid 5A5a, the Huang slurry of lower floor represents with yellow slurry sinking liquid 5A5b, first the Huang slurry supernatant water liquid 5A5a that isolates upper strata is pressurizeed to discharge in 5UVC precipitate and separate pond again and carry out natural sedimentation layering, the supernatant water liquid on upper strata represents with 5C5a, the Huang slurry sinking liquid of lower floor represents with 5C5b, supernatant water liquid 5C5a is sent in 5UVD precipitate and separate pond through adding water purification agent or adjusting pH value ON cycle pump and mix through natural sedimentation layering, the supernatant water liquid on upper strata represents with 5D5a, the precipitated liquid of lower floor represents with 5D5b, supernatant water liquid 5D5a is transported to and in 5UV E precipitate and separate pond, adds water purification agent polyacrylamide (aluminium iron polychloride, bodied ferric sulfate, polymerize aluminum chloride) and adjust pH value and mix with clean water or well water, precipitation is impelled the acceleration layering of 5E5a and 5E5b, upper strata represents with supernatant water liquid 5E5a, detecting magnitude of voltage through photo-sensor is 0.7~1.0v, detect through pH value controller, pH value 7.4~7.6, reach the water quality emission standard of national regulation.
The Huang slurry of lower floor represents with yellow slurry sinking liquid 5A5b; discharge the yellow slurry sinking liquid 5B5b of subnatant that postprecipitation layering extracts and represent with corn stalk powder straw powder such as () Ipomoea batatas straw powder, peanut straw powder, sweet sorghum stalk powders or improve the efficiency of granulating disc balling-up with melon rubber powder when Huang slurry sinking liquid 5A5b pressurizes again, then the method for a kind of spherolite feed auxiliary material of producing through mixing, fermentation, ball processed, oven dry.
The upper strata Huang slurry supernatant water liquid Huang slurry supernatant water liquid 5B5a that discharges acquisition through secondary pressurized represents, is 95~99%: 0.1~0.3 ‰: 0.1~0.5% through interpolation water purification agent (polyacrylamide, aluminium iron polychloride, bodied ferric sulfate, polymerize aluminum chloride etc.) and adjustment pH value material (milk of lime, sodium hydroxide etc.) through the supernatant liquor of pressurization release and the ratio of water purification agent and adjustment pH value material; Add through recycle pump and mix, after precipitation, isolated yellow slurry sinking liquid and corn stalk powder and bentonitic ratio are 80~50%: 20~50%: 0.1~0.3%; The method of a kind of spherolite biology soil-moisture conservation fertilizer of producing through mixing, fermentation, ball processed, oven dry.
Background technology
In the prior art, treatment process for the yellow seriflux that utilizes fresh sweet potatoes (sweet potato) to produce when the starch producing is: adopt anaerobism producer to process or extract yellow starch with whizzer or sheet frame pressing machine, its facility investment is large, plant factor only had about 30~60 days.And produce a large amount of maize straws period at harvesting corn, owing to catching up with kind of lower batch crops or direct returning to farmland or ensiling stalks feed and making straw board, stalk fuel, straw power generation etc. a difficult problem that mostly exists production and transport and producing apparatus high in cost of production.The present invention be utilize yellow seriflux that fresh sweet potatoes (sweet potato) produces in the time of starch producing through pressurization release, precipitation, isolated yellow slurry sinking liquid and corn stalk powder (sweet sorghum stalk powder, peanut straw powder, Ipomoea batatas (sweet potato) straw powder) through mixing, ferment, a kind of spherolite biology soil-moisture conservation fertilizer of producing of ball processed, oven dry and the method for spherolite feed auxiliary material.Wherein utilize yellow seriflux to there is water-retaining capacity strong, the characteristic that viscosity is poor, discharge, impel yellow seriflux in precipitate and separate pond, to accelerate layering through pressurization and realize separating of yellow slurry and water, isolated yellow slurry and corn stalk powder (sweet sorghum stalk powder, peanut straw powder and Ipomoea batatas straw powder) through mixing, the spherolite made of ball processed, oven dry, reached the standard of production granulated feed and fertilizer hardness.
Summary of the invention
Object of the present invention provides a kind of comprehensive utilization that utilizes " maize straw and fresh sweet potatoes yellow seriflux are manufactured the method for product " can solve stalk, the difficult problem of the yellow seriflux producing can solve again fresh sweet potatoes (sweet potato) starch producing time to environment just for existing weak point in above-mentioned prior art.The present invention is: the separation of solution yellow seriflux is that yellow seriflux accelerated yellow slurry afterwards through the pressure release of setting and water carries out natural sedimentation layering in precipitate and separate pond, upper strata is starched supernatant water liquid for Huang and is represented with 5a, lower floor starches sinking liquid for Huang and represents with 5b, isolate: 5A5a yellow slurry supernatant water liquid and the yellow slurry of 5A5b sinking liquid, and 5A5b yellow slurry sinking liquid and straw powder are through 14, 10 stalk mixing machines enter 15 after mixing, the 11 transparent photosynthetic ponds (plastics bag) that heat are carried out anaerobically fermenting be fermenting-ripening after being occurred sweet tart flavour and having strong wine flavour, temperature control is 18~43 DEG C, fermentation time is 1~7 day, use again 16, 12 granulating disc granulations and 17, 13 dry to producing 18, 14 granulated feed auxiliary materials, its produce 18, 14 granulated feed auxiliary material particle diameters are 0.5~10mm.And the yellow slurry of isolated 5A5a supernatant water liquid discharges through again pressurizeing and separates, adjust after pH value until add water purification agent, after precipitate and separate dilution, reach 299,5E5a state emission standard.
Object of the present invention can realize by following measures:
(1), pressurization releasing device be by: pressurized vessel (non-tower water supply pressurized vessel) control method is by the spacing water monitor in the upper limit and lower limit and the circulating pool that are set on twin contact tensimeter and the spacing water monitor in precipitate and separate pond, by the CPU on circuit card in the control of Photoelectric Detection controlling alarm case controlling setting numerical value that pressurized vessel discharges the upper limit on three contact force tables and the water level upper limit in lower limit and circulating pool with limit under water and precipitate and separate pond in the water level upper limit and water level lower limit, the Push And Release of determining the residual sea water pump in circulating pool be connected precipitate and separate pond in the Push And Release of electromagnetic valve realize the yellow seriflux in circulating pool flowed into the method discharging in precipitate and separate pond through electromagnetic valve exit when being pressurised into 0.1Mpa~0.23Mpa.
(2) U-shaped or V-type precipitate and separate pond is by the semi-underground type or the underground type concrete structure pond that produce the yellow seriflux settling tank volumetric quantity design-build of fresh sweet potatoes generation with reference to day, U and V represent that its function of shape of bottom, precipitate and separate pond is to be convenient to residual sea water pump clean the Huang slurry sinking liquid 5b suction of precipitation bottom, precipitate and separate pond represents with UV, represent totally 5 precipitate and separate ponds with 5, A represents the 1st precipitate and separate pond, B represents the 2nd precipitate and separate pond, C represents the 3rd precipitate and separate pond, D represents the 4th precipitate and separate pond, and E represents the 5th precipitate and separate pond.Yellow seriflux in settling tank discharges or adds water purification agent through pressurization and represents with 5a through the upper water of natural sedimentation layering, represent with yellow slurry supernatant liquor or with supernatant water liquid 5a, and yellow seriflux in settling tank discharges or adds water purification agent through pressurization and represents with 5b through lower floor's yellow slurry throw out of natural sedimentation layering, when yellow slurry supernatant liquor 5a in A precipitate and separate pond discharges or proceeds to 5A5a while processing in B settling tank and convert 5B5a.5b to through adding water purification agent processing through pressurization ... .5E5a.5b.And 5UVA, 5UVB, 5UVC, 5UVD, 5UVE precipitate and separate pond, 5a.5b in precipitate and separate pond is semi-underground type or the underground type concrete structure pond of yellow seriflux/cubic meter volumetric quantity design-build that while producing starch with reference to storage processing fresh Ipomoea batatas (sweet potato), produce every day, the tripping device of yellow slurry and water is installed in pond, be after yellow seriflux precipitated and separated, to be yellow slurry and water, and yellow slurry is yellow slurry sinking liquid 5A5b, water is yellow slurry supernatant water liquid 5A5a.And 5UVA precipitation detection separate tank 5a.5b integral part is: 47, it is by the plastics tubing such as PE and PVC that U-shaped supernatant liquor 5a detects tripping device, and diameter is 200~400mm, is highly: 1.5~3.6m, and the container of making, comprises 50, (16) spacing water monitor, 51, (14) (A) row's supernatant water pump, 49, (15d) connect 51, (14) (A) Connection Card of the flexible plastic tube of row's supernatant water pump, 48, (15) flexible plastic tube, 44, (15a) anti-water solenoid valve connects (p) floater shot with photo-sensor, 46, (15c) connect (p) point of fixity and 52 with the spacing water level of the floater shot of photo-sensor, (15e) be 51, (14) (A) the relief outlet composition of row's supernatant water liquid pump is respectively used to: 5UVA, 5UVB, 5UVC, 5UVD, 5UVE precipitation detects in separate tank and realizes with 47, U-shaped supernatant liquor 5a detects the import 45 of tripping device, (15b) enter supernatant liquor 5a from 52, (15e) be 51, (14) (A) relief outlet of row's supernatant water liquid pump is discharged the method that precipitates detection separate tank.The Huang slurry supernatant water liquid that 5UVA precipitation detects in separate tank represents with 5A5a, 5A5a from 52, (15e) relief outlet discharges to realize and separates.The Huang slurry supernatant liquor 5B5a that 5UVB precipitation detects in separate tank represents, 5B5a from 52, (15e) relief outlet discharges to realize and separates.The Huang slurry supernatant liquor 5C5a that 5UVC precipitation detects in separate tank represents, 5C5a from 52, (15e) relief outlet discharges the separation of the separation of supernatant 5C5a realizing.The Huang slurry supernatant liquor 5D5a that 5UVD precipitation detects in separate tank represents, 5D5a from 52, (15e) relief outlet discharges the separation that realizes supernatant liquor 5D5a.The Huang slurry supernatant liquor 5E5a that 5UV E precipitation detects in separate tank represents, 5E5a from 52, (15e) relief outlet discharges to realize and separates.
And the sinking liquid that precipitation detects in separate tank 5UVA, 5UVB, 5UVC, 5UVD, 5UVE is represented by 5A5b, 5B5b, 5C5b, 5D5b and 5E5b respectively, separator is by (4) (B) residual sea water pump and 54, (17) turbidity transducer, 59, (4a) residual sea water pump outlet and 57, (19) spacing water monitor 53,, and 57, (19) spacing water monitor 46, (15c) fixed position and 56, (15f) fluid inlet and sinking liquid 5b composition.And 68, (c) (8) be mix the circulation mixing pump that adds water purification agent and adjust pH value for, timing in 5UVD and 5UVE precipitate and separate pond mixes.
(3) electric control box is divided into: 6,4 Photoelectric Detection controlling alarm casees, 11,8 Photoelectric Detection controlling alarm casees, 22,15 Photoelectric Detection controlling alarm casees, 26,18 Photoelectric Detection controlling alarm casees, 29,59 Photoelectric Detection controlling alarm casees.
6,4 Photoelectric Detection controlling alarm case control functions are: 79,9. 1. 2. 5. 6. three contact force container controller pilot lamp, 77,7. waterproof electromagnetic valve pilot lamp of three contact switch of spacing water monitor pilot lamp, 76, three contact switch of photoelectricity turbidity transducer pilot lamp, 75, three contact switch of photoelectricity clear water sensor pilot lamp, 72, three contact switch of master switch pilot lamp, 71, three contact switch of single contact switch.
11, 8 Photoelectric Detection controlling alarm case control functions are: 79, single contact switch is master switch pilot lamp 9., three contact switch 71 are photoelectricity clear water sensor pilot lamp 1., 72, three contact switch are photoelectricity turbidity transducer pilot lamp 2., 73, three contact switch are PH controller pilot lamp 3., 74, three contact switch are temperature regulator pilot lamp 4., 75, three contact switch are spacing water monitor pilot lamp 5., three contact switch 76, 6. three contact force container controller pilot lamp, 77, three contact switch are waterproof electromagnetic valve pilot lamp 7., 78, three contact switch are timing mixed cycle pump control pilot lamp in pond 8..
22,15 Photoelectric Detection controlling alarm case control functions are: 79,9. 1. 2. 5. 6. 7. waterproof electromagnetic valve pilot lamp of twin contact pressurized vessel controller pilot lamp, 77, three contact switch of spacing water monitor pilot lamp, 76, three contact switch of photoelectricity turbidity transducer pilot lamp, 75, three contact switch of photoelectricity clear water sensor pilot lamp, 72, three contact switch of master switch pilot lamp, 71, three contact switch of single contact switch.
26, 18 Photoelectric Detection controlling alarm case control functions are: 79, single contact switch is master switch pilot lamp 9., 71, three contact switch are photoelectricity clear water sensor pilot lamp 1., 72, three contact switch are photoelectricity turbidity transducer pilot lamp 2., 73, three contact switch are PH controller pilot lamp 3., 74, three contact switch are temperature regulator pilot lamp 4., 75, three contact switch are spacing water monitor pilot lamp 5., 77, three contact switch are waterproof electromagnetic valve pilot lamp 7., 78, three contact switch are timing mixed cycle pump control pilot lamp in pond 8..
29, 59 Photoelectric Detection controlling alarm case control functions are: 79, single contact switch is master switch pilot lamp 9., 71, three contact switch are photoelectricity clear water sensor pilot lamp 1., 72, three contact switch are photoelectricity turbidity transducer pilot lamp 2., 73, three contact switch are PH controller pilot lamp 3., 74, three contact switch are temperature regulator pilot lamp 4., 75, three contact switch are spacing water monitor pilot lamp 5., 77, three contact switch are waterproof electromagnetic valve pilot lamp 7., 78, three contact switch are timing mixed cycle pump control pilot lamp in pond 8..
(4) Photoelectric Detection controlling alarm case span of control is:
At 5UVA, 5UVB, 5UVC, 5UVD, 5UVE precipitation detects the separation that realizes the supernatant water liquid 5A5a in 5UVA precipitation detection separate tank in separate tank, the separation that is supernatant liquor 5A5a be by the magnitude of voltage of the corresponding isolated sinking liquid of Photoelectric Detection controlling alarm case respectively by three corresponding contact switch 1. photoelectricity clear water sensor and three contact switch 3. the isolated magnitude of voltage of pH value controller and pH value be respectively: the magnitude of voltage that supernatant liquor 5A5a separates is 2.6~3.0, the magnitude of voltage that supernatant liquor 5B5a separates is 2.5~2.8, the magnitude of voltage of the separation of supernatant liquor 5C5a is 2.4~2.6, the magnitude of voltage of the separation of supernatant liquor 5D5a is 0.8~1.2PH7.7~8.5, the magnitude of voltage of the separation of supernatant liquor 5E5a is 0.7~1.0PH7.4~7.6.And the magnitude of voltage that precipitation detects the corresponding isolated sinking liquid of Photoelectric Detection controlling alarm case in separate tank 5UVA, 5UVB, 5UVC, 5UVD, 5UVE respectively by three corresponding contact switch 2. the isolated 5A5b sinking of photoelectricity turbidity transducer liquid magnitude of voltage is 4.5~5.0,5B5b sinking liquid magnitude of voltage is 4.5~5.0,5C5b sinking liquid magnitude of voltage is 4.5~5.0,5D5b sinking liquid magnitude of voltage be 4.5~5.0 and 5E5b magnitude of voltage be that sinking liquid magnitude of voltage is 4.5~5.0 to represent.
(5) indication range of utilizing " method that maize straw and fresh sweet potatoes yellow seriflux are made product " to control is: isolated sinking liquid magnitude of voltage 5A5b, 5B5b, 5C5b, 5D5b and 5E5b are 4.5~5.0.And isolated supernatant liquor magnitude of voltage is: 5A5a is 2.6~3.0,5B5a is 2.5~2.8,5C5a is 2.4~2.6,5D5a is 0.8~1.2PH7.7~8.5,5E5a0.7~1.0PH7.4~7.6.And non-tower water supply pressurized vessel relief pressure is 0.1~0.23Mpa ejection, its Main Function is, utilizes the relief pressure of 0.1~0.23Mpa to reach yellow seriflux and goes sticky object, accelerates the precipitate and separate of yellow slurry and water.And the mode of construction in precipitate and separate pond is underground type or semi-underground type, be shaped as U-shaped or V-type, width and height ratio are that to sink that the yellow slurry of liquid aspirates by residual sea water pump be that the Huang that 5b sinking liquid magnitude of voltage is 4.5~5.0 is starched to 1: 1.5~3.0 throw outs that are conducive to settling tank bottom completely.And tablets press is granulating disc.And utilize yellow slurry and guar-bean rubber powder and Ipomoea batatas stalk stalks such as () sweet sorghum, peanuts powder in 49~79.5%: the method for granulation feed auxiliary material is mixed, granulates, dried to 0.5~1.0%: 20~50% ratio, and its acquisition spherolite hardness is that 1.8~3.2kg, spherolite diameter are 0.5~10mm.
The supernatant liquor discharging through pressurization is through adding water purification agent (polyacrylamide, aluminium iron polychloride, bodied ferric sulfate, polymerize aluminum chloride etc.) and adjusting its supernatant liquor and water purification agent discharging through pressurization of pH value material (milk of lime, sodium hydroxide etc.) and the ratio of adjustment pH value material is: 95~99%: 0.1~0.4 ‰: 0.1~0.5% to add isolated supernatant liquor after recycle pump mixes, precipitates be 5a, and sinking liquid is 5b.
And the sinking liquid 5b that adjusts pH value through adding water purification agent presses than row with corn stalk powder and wilkinite: 52~75%: 23~48%: 0.2~0.5%; through mixing, fermentation, granulating disc granulation, oven dry granulation biology soil-moisture conservation fertilizer, it obtains spherolite hardness is 2.6~4.2kg.
And isolated supernatant liquor is 5a, through adjust with the dilution of clean water and well water pH value be 7.4~7.6 and magnitude of voltage discharge while reaching state specified standards while being 0.7~1.0v.
Brief description of the drawings
Fig. 1 is the vertical view (structural representation) of one embodiment of the present invention.
Fig. 2 (a) is the precipitate and separate control device sectional view (structural representation) of the settling tank in Fig. 1.
Fig. 2 (b) is the workflow demonstration figure of the control separation system of the Photoelectric Detection controlling alarm case of the precipitate and separate control device of the settling tank in control chart 1.
In Fig. 1: 1, 1 fresh sweet potatoes (sweet potato) starch producing precipitate and separate pond, 2, 2, fresh sweet potatoes (sweet potato) starch processing bean vermicelli, bean sheet jelly, 3, 3 isolated yellow seriflux circulating pool Isosorbide-5-Nitraes, 3A non-tower water supply pressurized vessel, 5, 5UVA precipitate and separate pond 5a.5b, 6, 4 Photoelectric Detection controlling alarm casees, 7, 5 yellow slurry sinking liquid 5A.5b circulating pools 2,8, 7 isolated yellow slurry sinking liquid 5A5b.5C5b circulating pools 3,9, 3B non-tower water supply pressurized vessel, 10, 5UVB settling tank separate tank 5a.5b, 11, 8 Photoelectric Detection warning separator boxs, 12, 9 yellow slurry sinking liquid straw bonding agent 5B5b circulating pools 4,13, 28 straw powder, 14, 10 straw powder mixers, 15, 11 transparent photosynthetic heating (plastics bag), 16, 12 granulating discs, 17, 13 dry, and 18, 14 granulated feed auxiliary materials, 19, 6 yellow slurry supernatant liquor 5A5a.5B5a circulating pools 5,20, 3C non-tower water supply pressurized vessel, 21, 5UVC precipitate and separate pond 5a.5b, 22, 15 Photoelectric Detection controlling alarm casees, 23, 16 yellow slurry supernatant water precipitated liquid 5C5b, 24, 17 supernatant water liquid 5C5a circulating pools 6,25, 5UVD supernatant water liquid adds water purification agent and adjusts pH value 5a.5b precipitate and separate pond, 26, 18 Photoelectric Detection separating controlling casees, 27, 5D5a supernatant water liquid circulating pool 7,28, 5UVE clear water liquid dilution pH value is adjusted 5a.5b turbidity and is detected separate tank, 29, 59 Photoelectric Detection separating controlling casees, 299, the discharge of 5E5a discharging standards, 30, 5E5b clear water dilution sinking liquid circulating pool 8,31, 20 supernatant sinking liquid straw bonding agent 5D5b circulating pools 9,32, 21 corn stalk powders, 33, 22 wilkinite tackiness agents, 34, 23 straw powder mixers, 35, 24 transparent photosynthetic pond (plastics bag), 36 of heating, granulating disc, 37, 26 dryers, 38, granular biological fertilizer.
Fig. 1 is that the upper strata yellow seriflux from 1,1 fresh sweet potatoes (sweet potato) starch producing precipitate and separate pond is isolated and entered in 3,3 isolated yellow seriflux circulating pools 1, and the process that enters 2,2 fresh sweet potatoes (sweet potato) starch and become through processing treatment bean vermicelli, bean sheet jelly product through the sinking liquid starch of the fresh sweet potatoes (sweet potato) of washing and precipitating, and the supernatant liquor water (yellow seriflux) producing in the time of the sinking liquid starch of the fresh sweet potatoes (sweet potato) of washing and precipitating to separate in entering 3,3 isolated yellow seriflux circulating pools 1 be yellow seriflux.When 3, in 3 isolated yellow seriflux circulating pools 1, yellow seriflux enters 4, in 3A non-tower water supply pressurized vessel, after discharging, pressurization enters 5, precipitate and separate is carried out in 5a.5b pond in 5UVA precipitate and separate pond, through 6, in 4 Photoelectric Detection controlling alarm casees 72, 2. photoelectricity sinking liquid sensor pilot lamp and three contact switch composition, detects and isolates the yellow slurry of 5A5b (the yellow sinking liquid of starching) and enter 7, in 5 yellow slurry sinking liquid 5A5b circulating pools 2, enter again 8, 7 isolated yellow slurry sinking liquid 5A5b, 5C5b circulating pool 3, then deliver into 9, 3B non-tower water supply pressurized vessel, discharges and flows into 10 through pressurization, 5UVB settling tank separate tank 5a.5b, after precipitated and separated by 11, in 8 Photoelectric Detection warning separator boxs 71, 1. photoelectricity supernatant liquor sensor pilot lamp and three contact switch composition, detect isolated 5B5a supernatant liquor through sensor and be transported to 19, in 6 yellow slurry supernatant liquor 5A5a.5B5a circulating pools 5, and through 71, 1. photoelectricity supernatant liquor sensor pilot lamp and three contact switch composition, the 5B5b detecting is transported to 12, in 9 yellow slurry sinking liquid straw bonding agent 5B5b circulating pools 4, and 13, 28 straw powder enter 14 simultaneously, in 10 straw powder mixers, mix, after mixing, enter again 15, in 11 transparent photosynthetic heating (plastics bag), ferment, after having fermented, then enter 16, 12 granulating discs carry out granulation, after granulation completes, carry out 17, 13 dry, and after having dried, obtain 18, 14 granulated feed auxiliary materials.
And enter 19, 6 yellow slurry supernatant liquor 5A5a, Huang slurry supernatant liquor 5A5a.5B5a circulating pool 5 in 5B5a circulating pool 5 is transported to 20, 3C non-tower water supply pressurized vessel is transported to 21 after pressurization discharges, in 5UVC precipitate and separate pond 5a.5b, carry out precipitated and separated, after layering through 22, in 15 Photoelectric Detection controlling alarm casees 72, 2. photoelectricity sinking liquid sensor pilot lamp and three contact switch composition, detect precipitated liquid 5C5b under isolated yellow slurry supernatant water through sensor and be conveyed into 23, in 16 yellow slurry supernatant water precipitated liquid 5C5b, be transported to again 7, in 5 yellow slurry sinking liquid 5A5b circulating pools 2.
And through 22, in 15 Photoelectric Detection controlling alarm casees 71, 1. the sensor of photoelectricity supernatant liquor sensor pilot lamp and three contact switch composition after testing isolated 24, in 17 supernatant water liquid 5C5a circulating pools 6, be transported to 25, 5UVD supernatant water liquid adds in water purification agent adjustment pH value 5a.5b precipitate and separate pond and adds water purification agent and add alkaline emulsion or liquid and open 78, 8. in pond, the recycle pump of timing mixed cycle pump control pilot lamp and three contact switch composition mixes, adjust the pH value of 5a.5b, impel the layering of 5a and 5b through precipitation, after layering through 26, in 18 Photoelectric Detection separating controlling casees 72, 2. the sensor of photoelectricity sinking liquid sensor pilot lamp and three contact switch composition detects that 5D5b supernatant water sinking liquid is transported to 31, in 20 supernatant liquor sinking liquid straw bonding agent 5D5b circulating pools 9.After layering through 26, in 18 Photoelectric Detection separating controlling casees 71, 1. the sensor that photoelectricity supernatant liquor sensor pilot lamp and three contact switch form after testing isolated 5D5a is transported to 27, in 5D5a supernatant water liquid circulating pool 7, be transported to again 28, 5UVE clear water liquid dilution pH value is adjusted 5a.5b turbidity and is detected in separate tank, again through 29, in 59 Photoelectric Detection separating controlling casees 73, 3. pH value controller pilot lamp and three contact switch composition and 78, 8. timing mixed cycle pump control pilot lamp and three contact switch composition in pond, sensor and the timer controlled mix, after mixing, impel layering, again through 29, in 59 Photoelectric Detection separating controlling casees 71, 1. the sensor that photoelectricity supernatant liquor sensor pilot lamp and three contact switch form after testing isolated 5E5a enters 299, after 5E5a discharging standards, discharge.
And 28, 5UVE clear water liquid dilution pH value is adjusted 5a.5b turbidity and is detected in separate tank, again through 29, in 59 Photoelectric Detection separating controlling casees 73, 3. pH value controller pilot lamp and three contact switch composition and 78, 8. in pond, sensor and the timer of timing mixed cycle pump control pilot lamp and three contact switch composition controls mix, mix postprecipitation and impel layering, through 72, 2. after the layering that the sensor of photoelectricity sinking liquid sensor pilot lamp and three contact switch composition detects, 5E5b is transported to 30, in 5E5b clear water dilution sinking liquid circulating pool 8, be transported to again 31, in 20 supernatant water sinking liquid straw bonding agent 5D5b circulating pools 9.
31,5D5b and 32,21 corn stalk powders and 33, the 22 wilkinite tackiness agents in 20 supernatant water sinking liquid straw bonding agent 5D5b circulating pools 9 are transported in 34,23 straw powder mixers and mix; after mixing, send into 35,24 transparent photosynthetic heating in pond (plastics bag) and carry out anaerobically fermenting; after having fermented, send into 36,25 granulating discs and carry out granulation; after granulation completes, send in 37,26 dryers and dry, after having dried, form 38,27 granular biological fertilizer.
Fig. 2 (a) is the precipitate and separate control device sectional view (structural representation) of the settling tank in Fig. 1.In Fig. 2 (a): 39, precipitation detects separate tank 5UVA, 40, precipitation detects separate tank 5UVB, 41, precipitation detects separate tank 5UVC, 42, precipitation detects separate tank 5UVD, 43, precipitation detects separate tank 5UVE, 44, (15a) anti-water solenoid valve, 45, (15b) the supernatant liquor water-in of connection 44 (15a) waterproof electromagnetic valve, 46, (15c) connect (p) connects the spacing water monitor of floater shot point of fixity with photoelectricity clear water liquid sensor, 47, U-shaped supernatant liquor 5a separation control device, 48, (15) water inlet flexible plastic tube, 49, (15d) connect 51, (14) (A) flexible plastic tube of row's supernatant water pump connect card, 50, (16) spacing water monitor control 51, (14) (A) Push And Release of row's supernatant liquor water pump, 51, (14) (A) row supernatant liquor water pump, 52, (15e) be 51, (14) (A) relief outlet of row's supernatant liquor water pump, 53, (4) (B) residual sea water pump, 54, 17 photoelectricity turbidity transducers, 555, (15t) upper limit point of fixity of spacing water monitor, 55, 8c timing mixed cycle pump, 56, (15f) enter the 5a.5b liquid that precipitate and separate pond need to separate, 555, (15t) upper limit point of fixity of spacing water monitor, 57, (19) spacing water monitor, 58, (9) pH value controller sensor, 59, (4a) sinking liquid 5b relief outlet, 60, (15h) electromagnetic valve, 61, 5A5a supernatant liquor, 62, 5B5a supernatant liquor, 63, 5C5a supernatant liquor, 64, 5D5a supernatant liquor, 65, 5E5a supernatant liquor, 66, 5A5b sinking liquid, 67, 5B5b sinking liquid, 68, 5C5b sinking liquid, 69, 5D5b sinking liquid, 70, 5E5b sinking liquid.
In Fig. 2 (a): be by 5UVA, 5UVB, 5UVC, 5UVD and 5 precipitations of 5UVE composition detect separate tank, and each detection precipitate and separate pond comprises 1 47, U-shaped supernatant liquor 5a separation control device, be: 47 in 5UVA, U-shaped supernatant liquor 5A.5a separation control device, in 5UVB 47, U-shaped supernatant liquor 5B5a separation control device, in 5UVC 47, U-shaped supernatant liquor 5C.5a separation control device, in 5UVD 47, in U-shaped supernatant liquor 5D5a separation control device and 5UVE 47, U-shaped supernatant liquor 5E5a separation control device, and 5 47, U-shaped supernatant liquor 5A5a, 5B5a, 5C5a, 5D5a and 5E5a separation control device are identical, and magnitude of voltage and the pH value of controlling locking are different, and 47, U-shaped supernatant liquor 5A5a, the magnitude of voltage of controlling locking is: 5A5a is 2.6~3.0, 5B5a is 2.5~2.8, 5C5a is 2.4~2.6, 5D5a is 0.8~1.2, for PH7.7~8.5, 5E5a is 0.7~1.0, PH7.4~7.6.
And by 5UVA, 5UVB, 5UVC, 5 precipitations of 5UVD and 5UVE composition detect separate tanks, and each precipitate and separate pond comprises that 1 by 53 (4) (B) residual sea water pumps, 54, 17 photoelectricity turbidity transducers, 555, (15t) upper limit point of fixity of spacing water monitor, 56, (15f) enter that precipitate and separate pond need to separate be 5a.5b liquid (5a represents supernatant water liquid, and 5b represents to sink liquid, represent herein by circulating pool enter precipitation detect in separate tank, need the mixing liquid that separates), 57, (19) spacing water monitor, 58, (9) pH value controller sensor, 59, (4a) sinking liquid 5b relief outlet, 60, (15h) electromagnetic valve, 66, 5A5b sinking liquid, 67, 5B5b sinking liquid, 68, 5C5b sinking liquid, 69, 5D5b sinking liquid and 70, the corresponding device of 5E5b sinking liquid composition, wherein detecting magnitude of voltage that locking separates and be identical is 4.1~5.0, and the precipitation of 5UVD and 5UVE composition detects in separate tank and respectively comprises that 1 is controlled locking 58, (9) pH value controller sensor and 55 timing mixed cycle pumps, and the precipitation of 5UVD composition detect in separate tank, lock 58, (9) pH value that pH value controller sensor locking separates is 7.7~8.5, and the precipitation of 5UVE composition detects that in separate tank, locking separates 58, (9) pH value of pH value controller sensor is 7.5~7.6, and carry out calculative determination according to the saturations of settling tank design and the flow of water pump/hour/cubic metre the cycling time of 55 timing mixed cycle pumps.
Fig. 2 (b) is the control separation system workflow demonstration figure of the Photoelectric Detection controlling alarm case of the precipitate and separate control device of the settling tank in control chart 1.
In Fig. 2 (b): 71, 1. photoelectricity supernatant liquor sensor pilot lamp and three contact switch composition, 72, 2. photoelectricity sinking liquid sensor pilot lamp and three contact switch composition, 73, 3. pH value controller pilot lamp and three contact switch composition, 74, 4. temperature regulator pilot lamp and three contact switch composition, 75, 5. spacing water monitor pilot lamp and three contact switch composition, 76, 6. three contact force container controller pilot lamp and three contact switch composition, 77, 7. waterproof electromagnetic valve pilot lamp and three contact switch composition, 78, 8. timing mixed cycle pump control pilot lamp and three contact switch composition in pond, 79, 9. master switch pilot lamp and single contact switch composition.
Embodiment
Embodiment mono-
Object of the present invention provide for existing weak point in above-mentioned prior art just a kind of utilize pressurization to discharge to accelerate yellow seriflux in precipitate and separate pond through natural sedimentation layering, upper strata is starched supernatant liquor for Huang and is represented with 5a, lower floor starches sinking liquid for Huang and represents with 5b, isolate: 5A5a yellow slurry supernatant water liquid and the yellow slurry of 5A5b sinking liquid, the method that the present invention utilizes 5A5b yellow slurry sinking liquid and sweet sorghum stalk powder to make granular fodder auxiliary material.As shown in Figure 1: when 1, in 1 fresh sweet potatoes (sweet potato) starch producing precipitate and separate pond, isolated yellow seriflux enters 3, in 3 isolated yellow seriflux circulating pools 1, by 6, 4 Photoelectric Detection controlling alarm case controls 3, residual sea water pump and spacing water monitor and 4 in 3 isolated yellow seriflux circulating pools 1, in twin contact tensimeter on 3A non-tower water supply pressurized vessel and 5UVA precipitate and separate pond 5a.5b 53, (4) (B) residual sea water pump, 54, 17 photoelectricity turbidity transducers, 57, (19) spacing water monitor, 60, (15h) electromagnetic valve, when 3, spacing water monitor in 3 isolated yellow seriflux circulating pools 1 is prescribed a time limit and 4 upper, when twin contact tensimeter on 3A non-tower water supply pressurized vessel reaches 0.23MPa and in 5UVA precipitate and separate pond 5a.5b 57, (19) spacing water monitor is prescribed a time limit lower, and 3, residual sea water pump in 3 isolated yellow seriflux circulating pools 1 quits work, and connects 60 in 5UVA precipitate and separate pond 5a.5b, (15h) electromagnetic valve is opened, and the yellow seriflux now discharging through pressurization is through 60, (15h) electromagnetic valve flows in 5UVA precipitate and separate pond and carries out 5a.5b precipitated and separated, when 6, 72 of 4 Photoelectric Detection controlling alarm casees, 2. photoelectricity sinking liquid sensor pilot lamp and three contact switch composition, 54 of control, when 17 photoelectricity turbidity transducer magnitudes of voltage reach 5.0v 53, (4) (B) residual sea water pump startup is transported to 7 the yellow slurry of 5A5b sinking liquid, in 5 yellow slurry sinking liquid 5A5b circulating pools 2, be transported to again 8, 7 isolated yellow slurry sinking liquid 5A5b, in 5C5b circulating pool 3.
By 11, 8 Photoelectric Detection warning separator box controls 8, 7 isolated yellow slurry sinking liquid 5A5b, the residual sea water pump in 5C5b circulating pool 3 and spacing water monitor and 9, in twin contact tensimeter on 3B non-tower water supply pressurized vessel and 5UVB precipitate and separate pond 5a.5b 53, (4) (B) residual sea water pump, 54, 17 photoelectricity turbidity transducers, 57, (19) spacing water monitor, 60, (15h) electromagnetic valve, when 8, 7 isolated yellow slurry sinking liquid 5A5b, the spacing water monitor in 5C5b circulating pool 3 is prescribed a time limit and 9 upper, when twin contact tensimeter on 3B non-tower water supply pressurized vessel reaches 0.23MPa and in 5UVB precipitate and separate pond 5a.5b 57, (19) spacing water monitor is prescribed a time limit lower, and 8, 7 isolated yellow slurry sinking liquid 5A5b, the residual sea water pump in 5C5b circulating pool 3 quits work, and connects 60 in 5UVB precipitate and separate pond 5a.5b, (15h) electromagnetic valve is opened, and the yellow seriflux now discharging through pressurization is through 60, (15h) electromagnetic valve flows in 5UVB precipitate and separate pond 5a.5b and carries out precipitated and separated, when 11, 72 of 8 Photoelectric Detection controlling alarm casees, 2. photoelectricity sinking liquid sensor pilot lamp and three contact switch composition, 54 of control, when 17 photoelectricity turbidity transducer magnitudes of voltage reach 5.0V 53, (4) (B) residual sea water pump startup is transported to 12 the yellow slurry of 5B5b sinking liquid, in 9 yellow slurry sinking liquid straw bonding agent 5B5b circulating pools 4.
12, Huang slurry sinking liquid straw bonding agent 5B5b and 13,28 sweet sorghum stalk powders in 9 yellow slurry sinking liquid straw bonding agent 5B5b circulating pools 4, add through mixing, granulate, drying and make spherolite feed auxiliary material in the ratio of 77: 23, it obtains spherolite hardness is the spherolite feed auxiliary material that 2.6kg, spherolite diameter are 0.6mm.
Embodiment bis-
As shown in Figure 1 when the magnitude of voltage of 24,17 supernatant water liquid 5C5a in 24,17 supernatant water liquid 5C5a circulating pools 6 is that 2.4~2.6v is transported to 25,5UVD supernatant water liquid adds water purification agent and adjusts in pH value 5a.5b precipitate and separate pond, enters 25,24,17 supernatant water liquid 5C5a in 5UVD precipitate and separate pond and water purification agent and the alkaline matter ratio of adjusting pH value classify as: 24,17 supernatant water liquid 5C5a inpuies are 96 cubic metres: water purification agent polyacrylamide 150kg dilution is that the liquid of 1 cubic metre and aluminium iron polychloride 150kg dilution are the liquid of 1 cubic metre: 3 cubic metres of milk of limes.
Through being transported to 25, 5UVD supernatant water liquid adds water purification agent and adjusts pH value 5a.5b precipitate and separate pond, in add water purification agent and add alkaline emulsion or liquid ON cycle pump, and with 78, 8. in pond, the recycle pump of timing mixed cycle pump control pilot lamp and three contact switch composition mixes, the pH value of adjusting 5a.5b is 7.9, reach the layering of 5a and 5b through precipitation, after layering through 26, 18 Photoelectric Detection separating controlling casees, in 72, 2. photoelectricity sinking liquid sensor pilot lamp and three contact switch composition, the magnitude of voltage of the 5D5b supernatant water sinking liquid that sensor detects is that 5.0v is transported to 31, in 20 supernatant liquor sinking liquid straw bonding agent 5D5b circulating pools 9.And after layering through 26, in 18 Photoelectric Detection separating controlling casees 71, 1. the sensor that photoelectricity supernatant liquor sensor pilot lamp and three contact switch form the after testing magnitude of voltage of isolated 5D5a is 0.9v, through 73, 3. after three contact pH value controllers are determined as 7.9, be transported to 27, in 5D5a supernatant water liquid circulating pool 7, then be transported to 28, 5UVE clear water liquid dilution pH value is adjusted 5a.5b turbidity and is detected in separate tank, then through 29, in 59 Photoelectric Detection separating controlling casees 73, 3. pH value controller pilot lamp and three contact switch composition and 78, 8. timing mixed cycle pump control pilot lamp and three contact switch composition in pond, sensor and the timer of control mix, mixing time is 2 hours, after mixing through natural sedimentation to layering, then through 29, in 59 Photoelectric Detection separating controlling casees 71, 1. photoelectricity supernatant liquor sensor pilot lamp separates when magnitude of voltage is 0.8v after testing with the sensor of three contact switch compositions, and isolated 5E5a measures the well water and 29 of sneaking into 5~10% by the cubic meter of 5E5a supernatant liquor water, in 59 Photoelectric Detection separating controlling casees 73, 3. the pH value of the sensor determination 5E5a supernatant liquor water of pH value controller pilot lamp and three contact switch composition is 7.5 to be transported to 52 after reaching discharging standards, 15e, 5E5a reaches discharging standards.
And 28, 5UVE clear water liquid dilution pH value is adjusted 5a.5b turbidity and is detected in separate tank, again through 29, in 59 Photoelectric Detection separating controlling casees 73, 3. pH value controller pilot lamp and three contact switch composition, with 78, 8. timing mixed cycle pump control pilot lamp and three contact switch composition in pond, sensor and the timer controlled mix, be mixed to layering, through 72, 2. the 5E5b after the layering that the sensor of photoelectricity sinking liquid sensor pilot lamp and three contact switch composition detects is transported to 30, in 5E5b clear water dilution sinking liquid circulating pool 8, be transported to again 31, in 20 supernatant liquor sinking liquid straw bonding agent 5D5b circulating pools 9.
31, the 5D5b sinking liquid and 32 of (it is 4.5~5.0v that supernatant liquor sinking liquid straw bonding agent 5D5b detects magnitude of voltage through photo-sensor) in 20 supernatant water sinking liquid straw bonding agent 5D5b circulating pools 9, 21 corn stalk powders and 33, the ratio of 22 wilkinite tackiness agents is 7.4 cubic metres: 2.55 tons: the slurry pipeline transport of 0.05 ton arrives, 34, in 23 straw powder mixers, mix, after mixing, send into 35, the 24 transparent photosynthetic ponds (plastics bag) that heat, in carry out anaerobically fermenting 2 days, leavening temperature is 40 DEG C, after having fermented, send into 36, 25 granulating discs, granulation, after completing, granulation sends into 37, 26 dryers, dry, after completing, oven dry forms 38, 27 granular biological soil moisture conservation fertilizer, its hardness is the spherolite biology soil-moisture conservation fertilizer of 4.0kg.

Claims (2)

1. a method of utilizing maize straw and fresh sweet potatoes (sweet potato) yellow seriflux to make product, it is characterized in that: it is strong that the yellow seriflux producing while adopting processing fresh Ipomoea batatas (sweet potato) starch has water-retaining capacity, the characteristic that viscosity is poor, through pressurize 0.1~0.23Mpa in airtight container time, discharge into the acceleration layering that impels yellow slurry and water in 5UVA settling tank, upper strata represents with yellow slurry supernatant water liquid 5UVA5a, detecting magnitude of voltage through photo-sensor is 2.6~3.0v, lower floor represents with yellow slurry sinking liquid 5UVA5b, detecting magnitude of voltage through photo-sensor is 4.5~5.0v, utilize yellow slurry sinking liquid 5UVA5b and corn stalk powder (sweet sorghum stalk powder, peanut straw powder, Ipomoea batatas straw powder) ratio is 80~50%: 20~50%, through mixing, anaerobically fermenting, disk pelletizing mechanism grain, dry and obtain a kind of spherolitic feed auxiliary material, the method one of the products such as biology soil-moisture conservation fertilizer, Huang slurry sinking liquid 5UVA5b discharges into the acceleration layering that impels yellow slurry and water in 5UVB settling tank through pressurize 0.1~0.23Mpa in airtight container time, upper strata represents with yellow slurry supernatant water 5UVB5a liquid, detecting magnitude of voltage through photo-sensor is 2.5~2.8v, lower floor represents with yellow slurry sinking liquid 5UVB5b, detecting magnitude of voltage through photo-sensor is 4.5~5.0v, utilize yellow slurry sinking liquid 5UVB5b and sweet sorghum stalk powder (corn stalk powder, peanut straw powder, Ipomoea batatas straw powder) and melon rubber powder ratio be 80~50%: 20~50%: 0.1~0.3%, through mixing, anaerobically fermenting, disk pelletizing mechanism grain, dry and obtain a kind of spherolitic feed auxiliary material, spherolite hardness is 1.8~3.2kg, spherolite diameter is the method two of 0.5~10mm product, supernatant water liquid 5UVC5a enters in 5UVD settling tank and represents with 5UVD5a.5b, add water purification agent polyacrylamide (aluminium iron polychloride, bodied ferric sulfate, polymerize aluminum chloride) and adjust milk of lime (sodium hydroxide for pH value, ammoniacal liquor) mix, precipitation is impelled the acceleration layering of 5UVD5a and 5UVD5b, upper strata represents with yellow slurry supernatant water liquid 5UVD5a, detecting magnitude of voltage through photo-sensor is 0.8~1.2v, detect through pH value controller, pH value 7.7~8.5, lower floor represents with yellow slurry sinking liquid 5UVD5b, detecting magnitude of voltage through photo-sensor is 4.5~5.0v, utilizing yellow slurry sinking liquid 5UVD5b and corn stalk powder and bentonite in powder ratio is 80~50%: 20~50%: 0.1~0.3%, through mixing, anaerobically fermenting, disk pelletizing mechanism grain, dry and obtain a kind of spherolitic biology soil-moisture conservation fertilizer, spherolite hardness is 1.8~3.2kg, spherolite diameter is the method three of 0.5~10mm product, supernatant water liquid 5UVD5a enters in 5UVE settling tank and represents with 5UVE5a.5b, add water purification agent polyacrylamide (aluminium iron polychloride, bodied ferric sulfate, polymerize aluminum chloride) and adjust pH value and (mix with clean water or well water, precipitation is impelled the acceleration layering of 5UVE5a and 5UVE5b, upper strata represents with yellow slurry supernatant water liquid 5UVE5a, detecting magnitude of voltage through photo-sensor is 0.7~1.0v, detect through pH value controller, pH value 7.4~7.6, reach the water quality emission standard of national regulation.
2. according to claim 1, a kind of method of utilizing maize straw and fresh sweet potatoes yellow seriflux to make product, it is characterized in that: the yellow seriflux producing when processing starch by using fresh sweet potatoes, in water pump is delivered to non-tower water supply pressurized vessel, when its control pressure 0.1~0.23Mpa, discharge, enter precipitate and separate pond, precipitation, separate, the mode of construction in precipitate and separate pond is underground type or semi-underground type, be shaped as U-shaped or V-type, width is 1: 1.5~3.0 with height ratio, 1 supernatant water liquid separating apparatus of being made by the plastics such as PE and PVC upper hose is installed in pond, diameter is 200~400mm, be highly 1.5~3.6m, 1 submersible pump is installed by 1 spacing water monitor control in device, the water-in of submersible pump is connected by flexible plastic tube, flexible plastic tube water inlet is connecting 1 waterproof electromagnetic valve, 1 the spacing water level bracing wire controller that is connected with 1 photoelectricity clear water liquid sensor and is being connected with 1 Aerated pipe stopper (ball), its principle of work is: when 49 in the settling tank of U or V-type, (15d) spacing line and P are with the sensor of floater shot and with 44, (15a) plastic hose of waterproof electromagnetic valve is connected, and 45, (15b) plastic hose water-in and P exceed 0.5~2cm with the transmitting of floater shot bottom with the photo-sensor level attitude of reception and are connected, making photo-sensor detect the CPU of the magnitude of voltage locking in electric control box processes, control the Push And Release of electromagnetic valve, to the water discharge that meets discharging standards, the waste water (yellow seriflux) that the method has produced while not only having solved maize straw and processing fresh Ipomoea batatas (sweet potato) production starch causes environmental pollution, and bio-feritlizer and the feed made can also produce great economic benefit and social effect.
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