CN105131968A - Alkaline soil conditioner and continuous steam-pressing device and method thereof - Google Patents
Alkaline soil conditioner and continuous steam-pressing device and method thereof Download PDFInfo
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- CN105131968A CN105131968A CN201510554293.2A CN201510554293A CN105131968A CN 105131968 A CN105131968 A CN 105131968A CN 201510554293 A CN201510554293 A CN 201510554293A CN 105131968 A CN105131968 A CN 105131968A
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- sulfate
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- 238000000034 method Methods 0.000 title claims abstract description 26
- 239000003516 soil conditioner Substances 0.000 title claims abstract description 23
- 239000002689 soil Substances 0.000 claims abstract description 83
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 claims abstract description 76
- CSNNHWWHGAXBCP-UHFFFAOYSA-L Magnesium sulfate Chemical compound [Mg+2].[O-][S+2]([O-])([O-])[O-] CSNNHWWHGAXBCP-UHFFFAOYSA-L 0.000 claims abstract description 58
- 239000002699 waste material Substances 0.000 claims abstract description 51
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid group Chemical group C(CC(O)(C(=O)O)CC(=O)O)(=O)O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 claims abstract description 49
- 239000005864 Sulphur Substances 0.000 claims abstract description 43
- HYBBIBNJHNGZAN-UHFFFAOYSA-N furfural Chemical group O=CC1=CC=CO1 HYBBIBNJHNGZAN-UHFFFAOYSA-N 0.000 claims abstract description 33
- 244000005700 microbiome Species 0.000 claims abstract description 33
- 229910052943 magnesium sulfate Inorganic materials 0.000 claims abstract description 29
- 235000019341 magnesium sulphate Nutrition 0.000 claims abstract description 29
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 18
- DIZPMCHEQGEION-UHFFFAOYSA-H aluminium sulfate (anhydrous) Chemical compound [Al+3].[Al+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O DIZPMCHEQGEION-UHFFFAOYSA-H 0.000 claims abstract description 17
- 239000004021 humic acid Substances 0.000 claims abstract description 17
- 239000000843 powder Substances 0.000 claims description 83
- 238000000855 fermentation Methods 0.000 claims description 78
- 230000004151 fermentation Effects 0.000 claims description 78
- 239000007788 liquid Substances 0.000 claims description 68
- 241000894006 Bacteria Species 0.000 claims description 60
- 238000007599 discharging Methods 0.000 claims description 43
- 239000000463 material Substances 0.000 claims description 42
- 241000194103 Bacillus pumilus Species 0.000 claims description 39
- 241000193417 Brevibacillus laterosporus Species 0.000 claims description 39
- 238000004519 manufacturing process Methods 0.000 claims description 34
- 241000193830 Bacillus <bacterium> Species 0.000 claims description 33
- 229910052717 sulfur Inorganic materials 0.000 claims description 33
- 239000011593 sulfur Substances 0.000 claims description 33
- SQQMAOCOWKFBNP-UHFFFAOYSA-L manganese(II) sulfate Chemical compound [Mn+2].[O-]S([O-])(=O)=O SQQMAOCOWKFBNP-UHFFFAOYSA-L 0.000 claims description 31
- 239000002364 soil amendment Substances 0.000 claims description 28
- 241001454747 Streptomyces aureus Species 0.000 claims description 27
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 claims description 27
- 229910021653 sulphate ion Inorganic materials 0.000 claims description 27
- 238000004659 sterilization and disinfection Methods 0.000 claims description 24
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 24
- RUTXIHLAWFEWGM-UHFFFAOYSA-H iron(3+) sulfate Chemical compound [Fe+3].[Fe+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O RUTXIHLAWFEWGM-UHFFFAOYSA-H 0.000 claims description 19
- 229910000360 iron(III) sulfate Inorganic materials 0.000 claims description 19
- 238000003756 stirring Methods 0.000 claims description 19
- 238000009423 ventilation Methods 0.000 claims description 19
- NWONKYPBYAMBJT-UHFFFAOYSA-L zinc sulfate Chemical compound [Zn+2].[O-]S([O-])(=O)=O NWONKYPBYAMBJT-UHFFFAOYSA-L 0.000 claims description 19
- 229960001763 zinc sulfate Drugs 0.000 claims description 19
- 229910000368 zinc sulfate Inorganic materials 0.000 claims description 19
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 claims description 18
- 244000046052 Phaseolus vulgaris Species 0.000 claims description 18
- 235000010627 Phaseolus vulgaris Nutrition 0.000 claims description 18
- 238000013019 agitation Methods 0.000 claims description 18
- 238000007605 air drying Methods 0.000 claims description 18
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 18
- 239000001110 calcium chloride Substances 0.000 claims description 18
- 229910001628 calcium chloride Inorganic materials 0.000 claims description 18
- 229940041514 candida albicans extract Drugs 0.000 claims description 18
- ZPWVASYFFYYZEW-UHFFFAOYSA-L dipotassium hydrogen phosphate Chemical compound [K+].[K+].OP([O-])([O-])=O ZPWVASYFFYYZEW-UHFFFAOYSA-L 0.000 claims description 18
- BNIILDVGGAEEIG-UHFFFAOYSA-L disodium hydrogen phosphate Chemical compound [Na+].[Na+].OP([O-])([O-])=O BNIILDVGGAEEIG-UHFFFAOYSA-L 0.000 claims description 18
- 229910000397 disodium phosphate Inorganic materials 0.000 claims description 18
- 235000019800 disodium phosphate Nutrition 0.000 claims description 18
- 238000005189 flocculation Methods 0.000 claims description 18
- 230000016615 flocculation Effects 0.000 claims description 18
- 238000011081 inoculation Methods 0.000 claims description 18
- 229910052760 oxygen Inorganic materials 0.000 claims description 18
- 239000001301 oxygen Substances 0.000 claims description 18
- 238000000926 separation method Methods 0.000 claims description 18
- 239000012138 yeast extract Substances 0.000 claims description 18
- YYRMJZQKEFZXMX-UHFFFAOYSA-L calcium bis(dihydrogenphosphate) Chemical compound [Ca+2].OP(O)([O-])=O.OP(O)([O-])=O YYRMJZQKEFZXMX-UHFFFAOYSA-L 0.000 claims description 16
- 229910000389 calcium phosphate Inorganic materials 0.000 claims description 16
- 230000000855 fungicidal effect Effects 0.000 claims description 16
- 239000000417 fungicide Substances 0.000 claims description 16
- 235000019691 monocalcium phosphate Nutrition 0.000 claims description 16
- PASHVRUKOFIRIK-UHFFFAOYSA-L calcium sulfate dihydrate Chemical compound O.O.[Ca+2].[O-]S([O-])(=O)=O PASHVRUKOFIRIK-UHFFFAOYSA-L 0.000 claims description 15
- 239000011505 plaster Substances 0.000 claims description 14
- 241001037822 Bacillus bacterium Species 0.000 claims description 12
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 claims description 12
- 235000007164 Oryza sativa Nutrition 0.000 claims description 12
- 239000001888 Peptone Substances 0.000 claims description 12
- 108010080698 Peptones Proteins 0.000 claims description 12
- 229920002472 Starch Polymers 0.000 claims description 12
- DPDMMXDBJGCCQC-UHFFFAOYSA-N [Na].[Cl] Chemical compound [Na].[Cl] DPDMMXDBJGCCQC-UHFFFAOYSA-N 0.000 claims description 12
- 239000008103 glucose Substances 0.000 claims description 12
- 235000019319 peptone Nutrition 0.000 claims description 12
- 239000004033 plastic Substances 0.000 claims description 12
- 229920003023 plastic Polymers 0.000 claims description 12
- 230000008569 process Effects 0.000 claims description 12
- 235000009566 rice Nutrition 0.000 claims description 12
- 210000000582 semen Anatomy 0.000 claims description 12
- 239000007787 solid Substances 0.000 claims description 12
- 235000019698 starch Nutrition 0.000 claims description 12
- 239000008107 starch Substances 0.000 claims description 12
- 238000010025 steaming Methods 0.000 claims description 12
- 235000015099 wheat brans Nutrition 0.000 claims description 12
- 239000000203 mixture Substances 0.000 claims description 10
- 239000002068 microbial inoculum Substances 0.000 claims description 8
- 238000002360 preparation method Methods 0.000 claims description 7
- 229920001817 Agar Polymers 0.000 claims description 6
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 claims description 6
- 244000068988 Glycine max Species 0.000 claims description 6
- 235000010469 Glycine max Nutrition 0.000 claims description 6
- 229910019142 PO4 Inorganic materials 0.000 claims description 6
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 claims description 6
- 240000004808 Saccharomyces cerevisiae Species 0.000 claims description 6
- 239000008272 agar Substances 0.000 claims description 6
- BFNBIHQBYMNNAN-UHFFFAOYSA-N ammonium sulfate Chemical compound N.N.OS(O)(=O)=O BFNBIHQBYMNNAN-UHFFFAOYSA-N 0.000 claims description 6
- 229910052921 ammonium sulfate Inorganic materials 0.000 claims description 6
- 235000011130 ammonium sulphate Nutrition 0.000 claims description 6
- 238000004458 analytical method Methods 0.000 claims description 6
- 230000002051 biphasic effect Effects 0.000 claims description 6
- 238000012364 cultivation method Methods 0.000 claims description 6
- 238000006385 ozonation reaction Methods 0.000 claims description 6
- 239000010452 phosphate Substances 0.000 claims description 6
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 claims description 6
- 239000011591 potassium Substances 0.000 claims description 6
- 229910052700 potassium Inorganic materials 0.000 claims description 6
- 239000001509 sodium citrate Substances 0.000 claims description 6
- 229910001220 stainless steel Inorganic materials 0.000 claims description 6
- 239000010935 stainless steel Substances 0.000 claims description 6
- 230000001954 sterilising effect Effects 0.000 claims description 6
- HRXKRNGNAMMEHJ-UHFFFAOYSA-K trisodium citrate Chemical compound [Na+].[Na+].[Na+].[O-]C(=O)CC(O)(CC([O-])=O)C([O-])=O HRXKRNGNAMMEHJ-UHFFFAOYSA-K 0.000 claims description 6
- 229940038773 trisodium citrate Drugs 0.000 claims description 6
- 239000010455 vermiculite Substances 0.000 claims description 6
- 235000019354 vermiculite Nutrition 0.000 claims description 6
- 229910052902 vermiculite Inorganic materials 0.000 claims description 6
- 241000233866 Fungi Species 0.000 claims description 5
- 239000002131 composite material Substances 0.000 claims description 5
- 238000010298 pulverizing process Methods 0.000 claims description 5
- 238000012545 processing Methods 0.000 claims description 4
- 230000035484 reaction time Effects 0.000 claims description 4
- 229920001661 Chitosan Polymers 0.000 claims description 3
- 240000007594 Oryza sativa Species 0.000 claims 4
- 201000010099 disease Diseases 0.000 abstract description 7
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 abstract description 7
- 230000003750 conditioning effect Effects 0.000 abstract description 4
- 230000008901 benefit Effects 0.000 abstract description 3
- 239000000126 substance Substances 0.000 abstract description 3
- QJZYHAIUNVAGQP-UHFFFAOYSA-N 3-nitrobicyclo[2.2.1]hept-5-ene-2,3-dicarboxylic acid Chemical compound C1C2C=CC1C(C(=O)O)C2(C(O)=O)[N+]([O-])=O QJZYHAIUNVAGQP-UHFFFAOYSA-N 0.000 abstract 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 abstract 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 abstract 1
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical class OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 abstract 1
- 229910052791 calcium Inorganic materials 0.000 abstract 1
- 239000011575 calcium Substances 0.000 abstract 1
- YYRMJZQKEFZXMX-UHFFFAOYSA-N calcium;phosphoric acid Chemical compound [Ca+2].OP(O)(O)=O.OP(O)(O)=O YYRMJZQKEFZXMX-UHFFFAOYSA-N 0.000 abstract 1
- 150000001875 compounds Chemical class 0.000 abstract 1
- 229910052602 gypsum Inorganic materials 0.000 abstract 1
- 239000010440 gypsum Substances 0.000 abstract 1
- 229910052749 magnesium Inorganic materials 0.000 abstract 1
- 239000011777 magnesium Substances 0.000 abstract 1
- 230000000813 microbial effect Effects 0.000 abstract 1
- 239000002426 superphosphate Substances 0.000 abstract 1
- MUBZPKHOEPUJKR-UHFFFAOYSA-N Oxalic acid Chemical compound OC(=O)C(O)=O MUBZPKHOEPUJKR-UHFFFAOYSA-N 0.000 description 24
- 240000008042 Zea mays Species 0.000 description 13
- 235000002017 Zea mays subsp mays Nutrition 0.000 description 13
- 241000196324 Embryophyta Species 0.000 description 9
- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 description 9
- 235000005822 corn Nutrition 0.000 description 9
- 241000209094 Oryza Species 0.000 description 8
- 230000000694 effects Effects 0.000 description 8
- 235000006408 oxalic acid Nutrition 0.000 description 8
- 239000003337 fertilizer Substances 0.000 description 6
- 239000011734 sodium Substances 0.000 description 6
- 235000016383 Zea mays subsp huehuetenangensis Nutrition 0.000 description 4
- 235000009973 maize Nutrition 0.000 description 4
- 239000000052 vinegar Substances 0.000 description 4
- 235000021419 vinegar Nutrition 0.000 description 4
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 3
- 241000607479 Yersinia pestis Species 0.000 description 3
- 238000013461 design Methods 0.000 description 3
- 238000009938 salting Methods 0.000 description 3
- 229930006000 Sucrose Natural products 0.000 description 2
- CZMRCDWAGMRECN-UGDNZRGBSA-N Sucrose Chemical compound O[C@H]1[C@H](O)[C@@H](CO)O[C@@]1(CO)O[C@@H]1[C@H](O)[C@@H](O)[C@H](O)[C@@H](CO)O1 CZMRCDWAGMRECN-UGDNZRGBSA-N 0.000 description 2
- 239000003513 alkali Substances 0.000 description 2
- 230000005540 biological transmission Effects 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 235000013681 dietary sucrose Nutrition 0.000 description 2
- 239000011790 ferrous sulphate Substances 0.000 description 2
- 235000003891 ferrous sulphate Nutrition 0.000 description 2
- 230000006872 improvement Effects 0.000 description 2
- BAUYGSIQEAFULO-UHFFFAOYSA-L iron(2+) sulfate (anhydrous) Chemical compound [Fe+2].[O-]S([O-])(=O)=O BAUYGSIQEAFULO-UHFFFAOYSA-L 0.000 description 2
- 229910000359 iron(II) sulfate Inorganic materials 0.000 description 2
- 229910000402 monopotassium phosphate Inorganic materials 0.000 description 2
- 235000019796 monopotassium phosphate Nutrition 0.000 description 2
- 235000015097 nutrients Nutrition 0.000 description 2
- PJNZPQUBCPKICU-UHFFFAOYSA-N phosphoric acid;potassium Chemical compound [K].OP(O)(O)=O PJNZPQUBCPKICU-UHFFFAOYSA-N 0.000 description 2
- 230000008439 repair process Effects 0.000 description 2
- 239000007921 spray Substances 0.000 description 2
- PRPINYUDVPFIRX-UHFFFAOYSA-N 1-naphthaleneacetic acid Chemical compound C1=CC=C2C(CC(=O)O)=CC=CC2=C1 PRPINYUDVPFIRX-UHFFFAOYSA-N 0.000 description 1
- 241000238631 Hexapoda Species 0.000 description 1
- 206010020880 Hypertrophy Diseases 0.000 description 1
- 235000008331 Pinus X rigitaeda Nutrition 0.000 description 1
- 235000011613 Pinus brutia Nutrition 0.000 description 1
- 241000018646 Pinus brutia Species 0.000 description 1
- FKNQFGJONOIPTF-UHFFFAOYSA-N Sodium cation Chemical compound [Na+] FKNQFGJONOIPTF-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 150000001447 alkali salts Chemical class 0.000 description 1
- 238000005282 brightening Methods 0.000 description 1
- ZFXVRMSLJDYJCH-UHFFFAOYSA-N calcium magnesium Chemical compound [Mg].[Ca] ZFXVRMSLJDYJCH-UHFFFAOYSA-N 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000005056 compaction Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 235000013312 flour Nutrition 0.000 description 1
- 230000009661 flower growth Effects 0.000 description 1
- 230000004927 fusion Effects 0.000 description 1
- 239000003292 glue Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000005556 hormone Substances 0.000 description 1
- 229940088597 hormone Drugs 0.000 description 1
- SEOVTRFCIGRIMH-UHFFFAOYSA-N indole-3-acetic acid Chemical compound C1=CC=C2C(CC(=O)O)=CNC2=C1 SEOVTRFCIGRIMH-UHFFFAOYSA-N 0.000 description 1
- JTEDVYBZBROSJT-UHFFFAOYSA-N indole-3-butyric acid Chemical compound C1=CC=C2C(CCCC(=O)O)=CNC2=C1 JTEDVYBZBROSJT-UHFFFAOYSA-N 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 238000002715 modification method Methods 0.000 description 1
- 239000000618 nitrogen fertilizer Substances 0.000 description 1
- 230000029553 photosynthesis Effects 0.000 description 1
- 238000010672 photosynthesis Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 230000000452 restraining effect Effects 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 229910001415 sodium ion Inorganic materials 0.000 description 1
- 208000024891 symptom Diseases 0.000 description 1
- 230000007306 turnover Effects 0.000 description 1
- 238000013022 venting Methods 0.000 description 1
Landscapes
- Fertilizers (AREA)
- Micro-Organisms Or Cultivation Processes Thereof (AREA)
Abstract
The invention belongs to the technical field of soil conditioning and repairing and particularly relates to alkaline soil conditioner and a continuous steam-pressing device and method thereof. The alkaline soil conditioner comprises, by weight, 15-30 parts of ardealite/desulfurized gypsum, 10-20 parts of citric acid residues, 3-10 parts of waste sulphur, 12-20 parts of superphosphate, 30-35 parts of furfural residues, 14-18 parts of magnesium sulfate, 6-10 parts of aluminum sulfate, 2-3 parts of sulfuric acid compounds and 15-30 parts of humic acid. According to the alkaline soil conditioner, surface soil alkaline substances can be neutralized, the Na+ and Cl-ion content of a soil plough layer can be reduced, the soil exchangeable calcium and magnesium content can be increased, and the soil structure can be improved. A compound microorganism microbial agent is adopted, alkalified soil can be effectively improved, the soil micro-ecological environment can be improved, and soil disease microorganisms can be killed. The alkaline soil conditioner can achieve the large-scale purpose, is free of the three-waste problem and suitable for being widely applied and popularized, and can generate great economic benefits.
Description
Technical field
The invention belongs to soil conditioning recovery technique field, be specifically related to a kind of alkaline soil amendment, also relate to continuous steaming pressure device and the method for above-mentioned amendment.
Background technology
Owing to using chemical fertilizer in a large number throughout the year, there is " red frost ", " white alkali " in the soil in many booths, this is the symptom of soil meta-alkalescence again and again.Salting of soil is the phenomenon that upper soll layer basic salt accumulates gradually, exchangeable sodium ion saturation percentage increases gradually.Will form saltings after soil alkalizes for a long time, saltings is not suitable for planting any crop, causes the reason of alkalization of soils mainly to use ammoniacal nitrogen fertilizer in a large number, causes soil pH value to rise.Eliminate alkalization of soils, generally adopt the alkalescence adding alkaline matter and come in sweetening of the soil in soil.To too alkaline soil, basic method is the alkalization degree lowering soil.
Modification method at present for alkaline soil generally has the following two kinds: one is organic improving method.Mix in soil exactly needle soil or broad-leaved native.Needle soil is that the needle of rotten pine tree, residual branch or sawdust retting form, alkaline, pH value 3.5-4, general alkaline soil mixes the needle soil of 1/5 or 1/6, the potted plant use of the most applicable basophilous flowers, broad-leaved soil is that the fallen leaves of various deciduous tree rot to form, pH value 4.5-5.5, the advantage of organic improving is multiple element contained after organic substance self rots, and is all that flower growth is necessary, and make loosing soil, ventilation property and water-permeable and water retention good.Two is inorganic improved methods.I.e. fusion 100 grams of-200 grams of sulfur flours in 1 cube of soil, sustainable 2 years-3 years of effectiveness.Suffer from the flowers and trees of yellows because of alkalization of soils, transplant in the alkaline soil of preparation, 10 days do not prick in new soil because of root, can not absorb nutrient, the most handy edible vinegar sprays the pros and cons of leaf.Like this by photosynthesis, the certain alkaline nutrient of leaf production is sent back to plant.If often spray edible vinegar (being watered 10 times), plant grew well can be made, leaf look dark green hypertrophy.Through frequentation basophilous flowers and trees blade face specking table sugar (being watered 50 times), also can make leaf surface brightening, flower is very large.And table sugar is a kind of hormone of taking root, its effect and naphthylacetic acid, indolebutyric acid and indolylacetic acid side by side, and use safer.
Inorganic improved method comprises again following mode:
Use SULPHUR POWDER: the seedbed of every square metre, mix 100-200 gram of SULPHUR POWDER, its alkaline validity period can maintain 2-3;
Use ferrous sulfate powder, every square metre applies 150 grams of ferrous sulfate powder, and Shi Houke reduces the pH value of 0.5-1 unit, and glue heavy soil for feature, consumption can increase by 1/3;
Water and execute vinegar liquid, a small amount of potted plant soil of family, if when its pH value is greater than 7, then available 150-200 vinegar liquid pouring doubly, within later 15-20 days, water once, efficiency is good;
Water and execute potassium dihydrogen phosphate, in alkaline soils, ferro element is easy to be fixed, and becoming can not utilization state, even if apply more iron, effect also can not be very desirable, therefore, can with 0.2% potassium dihydrogen phosphate or other alkaline fertilizer solution carry out drench soil, make soil be weakly alkaline, the ferro element in soil can be facilitated to be dissolved state, will root system of plant absorbing iron element to be conducive to.
Above-mentioned method after a long time use effect is unsatisfactory, easily causes soil compaction.
In addition, the existing steam pressure device of process soil conditioner generally comprises pressure measuring cylinder, and be positioned at the lid at pressure measuring cylinder two ends, when needing charging, open the lid of one end, material is put in pressure measuring cylinder, then steam pressure, during discharging, again to pressure measuring cylinder pressure release, because venting duration is longer, and can not continuous seepage in pressure leak process, cause inefficiency, especially for the material of long reaction time, have a strong impact on the normal operation of other operations, obvious reduction production efficiency, and the steam pressure device of above-mentioned discontinuous is interrupted pressure release due to it, it is complete that pressurization makes the pressure in steam pressure device substantially discharge, pressure loss is huge, efficiency of energy utilization is low, cost remains high.
Therefore, need for alkaline soil invention a kind of respond well, can in and alkali ion in topsoil soils, can effectively improve alkalify soil, reduce Na in soil plough horizon
+, Cl
-ion content, improves soil microenvironment, eliminates the alkaline soil amendment of soil disease microorganism.Also need improve for the steam pressure device and method of existing soil conditioner, make production process more continuous, enhance productivity.
Summary of the invention
In order to solve above-mentioned technical problem, the invention provides one and effectively can improve salinized soil, improving soil microenvironment, eliminate the alkaline soil amendment of soil disease microorganism.
Present invention also offers continuous steaming pressure device and the steam pressure method of above-mentioned alkaline soil amendment.
A kind of alkaline soil amendment, comprises the component of following portions by weight:
Citric acid waste 10-20
Sulfur waste sulphur 3-10
Phosphogypsum/desulfurated plaster 15-30
Calcium superphosphate 12-20
Furfural dregs 30-35
Magnesium sulfate 14-18
Tai-Ace S 150 6-10
Sulphate 2-3
Humic acids 15-30.
Above-mentioned sulphate is at least one in ferric sulfate, zinc sulfate, manganous sulfate.
Preferably, soil conditioner of the present invention comprises the component of following portions by weight:
Citric acid waste 12-15
Sulfur waste sulphur 3-6
Phosphogypsum/desulfurated plaster 20-25
Calcium superphosphate 15-17
Furfural dregs 30-35
Magnesium sulfate 16-17
Tai-Ace S 150 8-9
Sulphate 2-3
Humic acids 22-25;
Above-mentioned sulphate is at least one of ferric sulfate, zinc sulfate, manganous sulfate.
Preferred, alkaline soil amendment of the present invention comprises the component of following portions by weight:
Citric acid waste 14.13
Sulfur waste sulphur 4.56
Phosphogypsum/desulfurated plaster 22.38
Calcium superphosphate 16.05
Furfural dregs 32.45
Magnesium sulfate 16.48
Tai-Ace S 150 8.52
Sulphate 2.16
Humic acids 23.84;
Sulphate is mixture in ferric sulfate, zinc sulfate, manganous sulfate, and the ratio of weight and number of ferric sulfate, zinc sulfate, manganous sulfate is 1:1:1;
Sulfur waste sulphur is sulphur coated systems dedusting sulfur waste sulphur.
As a modification of the present invention, above-mentioned raw material combines with complex microbial inoculum by the present invention, and acting in conjunction is in alkaline soil, and the soil conditioner after improvement comprises the component of following portions by weight:
Citric acid waste 10-20
Sulfur waste sulphur 3-10
Phosphogypsum/desulfurated plaster 15-30
Calcium superphosphate 12-20
Furfural dregs 30-35
Magnesium sulfate 14-18
Tai-Ace S 150 6-10
Sulphate 2-3
Humic acids 15-30.
Complex micro organism fungicide 0.2-1
The composite fungus agent that complex micro organism fungicide is Alkaliphilic bacillus, bacillus laterosporus, bacillus pumilus, streptomyces aureus form; The weight ratio of described Alkaliphilic bacillus, bacillus laterosporus, bacillus pumilus, streptomyces aureus is 1 ~ 4:1 ~ 2:1 ~ 3:1 ~ 2;
Wherein Alkaliphilic bacillus 1 ~ 3 × 10
8cfu/g, bacillus laterosporus 0.5 ~ 2 × 10
8cfu/g, bacillus pumilus 0.5 ~ 1 × 10
8cfu/g, streptomyces aureus 0.5 ~ 1.5 × 10
8cfu/g.
Preferred, soil conditioner comprises the component of following portions by weight:
Citric acid waste 14.13
Sulfur waste sulphur 4.56
Phosphogypsum/desulfurated plaster 22.38
Calcium superphosphate 16.05
Furfural dregs 32.45
Magnesium sulfate 16.48
Tai-Ace S 150 8.52
Sulphate 2.16
Humic acids 23.84
Chitosan 1.25;
Sulphate is mixture in ferric sulfate, zinc sulfate, manganous sulfate, and the ratio of weight and number of ferric sulfate, zinc sulfate, manganous sulfate is 1:1:1;
Sulfur waste sulphur is sulphur coated systems dedusting sulfur waste sulphur;
The composite fungus agent that complex micro organism fungicide is Alkaliphilic bacillus, bacillus laterosporus, bacillus pumilus, streptomyces aureus form; The weight ratio of described Alkaliphilic bacillus, bacillus laterosporus, bacillus pumilus, streptomyces aureus is 3:2:2:1.5;
Wherein Alkaliphilic bacillus 1.8 × 10
8cfu/g, bacillus laterosporus 1.4 × 10
8cfu/g, bacillus pumilus 1.2 × 10
8cfu/g, streptomyces aureus 0.9 × 10
8cfu/g.
The preparation method of complex micro organism fungicide is as follows:
Prepared by Alkaliphilic bacillus: by Alkaliphilic bacillus strain inoculation to disinfection fermentation tank, fermention medium is: Semen Maydis powder 0.2-0.8%, extractum carnis 0.1-0.6%, bean cake powder 0.2-0.8%, Zulkovsky starch 0.1-0.4%, dipotassium hydrogen phosphate 0.02-0.08%, yeast extract 0.1-0.5%, Trisodium Citrate 0.05-0.15%, manganous sulfate 0.006-0.012%, pH7.5-7.9, fermentation condition: ventilation ratio is initiated with 0.8-1.2:0.5, culture temperature 35-40 DEG C, agitation revolution 100-200rpm, dissolved oxygen is not less than 30%, pH value is not less than 6.5, stir culture 6-8 hour, obtain fermented liquid, add Sodium phosphate dibasic and calcium chloride flocculation, rear employing filter press mode of having flocculated obtains bacterium mud, the 45-50 DEG C of forced air drying of bacterium mud is to water content 25-35%, put into pulverizer after cyclonic separation to pulverize, cross 30 mesh sieves and obtain Alkaliphilic bacillus bacterium powder, viable bacteria content 1 ~ 3 × 10 in Alkaliphilic bacillus bacterium powder
8cfu/g,
Bacillus laterosporus: by bacillus laterosporus strain inoculation to disinfection fermentation tank, fermention medium is: peptone 0.2-0.8%, yeast extract paste 0.01-0.06%, agar 0.2-0.8%, dregs of beans 0.1-0.4%, dipotassium hydrogen phosphate 0.02-0.08%, potassium primary phosphate 0.01-0.05%, magnesium sulfate 0.05-0.15%, manganous sulfate 0.006-0.012%, pH6.8-7.2, fermentation condition: ventilation ratio is initiated with 0.7-1.0:0.5, culture temperature 35-40 DEG C, agitation revolution 100-200rpm, dissolved oxygen is not less than 30%, pH value is not less than 6.5, stir culture 6-8 hour, obtain fermented liquid and add Sodium phosphate dibasic and calcium chloride flocculation, rear employing filter press mode of having flocculated obtains bacterium mud, the 45-50 DEG C of forced air drying of bacterium mud is to water content 25-35%, put into pulverizer after cyclonic separation to pulverize, cross 30 mesh sieves and obtain bacillus laterosporus bacterium powder,
Bacillus pumilus: by bacillus pumilus strain inoculation to disinfection fermentation tank, fermention medium is: starch 0.2-0.8%, yeast extract paste 0.01-0.06%, dregs of beans 0.2-0.8%, peptone 0.1-0.4%, dipotassium hydrogen phosphate 0.2-0.8%, glucose 0.1-0.5%, magnesium sulfate 0.05-0.15%, sodium-chlor 0.006-0.012%, pH6.8-7.2, fermentation condition: ventilation ratio is initiated with 0.8-1.2:0.5, culture temperature 35-40 DEG C, agitation revolution 100-200rpm, dissolved oxygen is not less than 30%, pH value is not less than 6.5, stir culture 6-8 hour, obtain fermented liquid and add Sodium phosphate dibasic and calcium chloride flocculation, rear employing filter press mode of having flocculated obtains bacterium mud, the 45-50 DEG C of forced air drying of bacterium mud is to water content 25-35%, put into pulverizer after cyclonic separation to pulverize, cross 30 mesh sieves and obtain bacillus pumilus bacterium powder,
Prepared by streptomyces aureus microbial inoculum: adopt liquid rotating solid biphasic cultivation method to cultivate, viride is carried out liquid fermenting, obtains liquid fermentation production, the substratum of described liquid fermenting is:
Glucose 0.01-0.06%, Semen Maydis powder 0.2-0.8%, yeast powder 0.1-0.4%, analysis for soybean powder 0.2-0.6%g,
Sodium-chlor 0.05-0.15%, KH2PO40.006-0.012%, ammonium sulfate 0.01-0.04%; Fermentation condition is: pH6.1-6.5,25-29 DEG C, passes into air and air flow is 9-11L/min, 0.02-0.04Mpa; Shaking culture 2-4 days, obtains liquid fermentation production;
By liquid fermentation production with expanded vermiculite be carrier carry out solid fermentation, specifically liquid fermentation production is mixed with rice bran and wheat bran, be placed in the stainless steel mesh screen through liming or ozonization, cover the plastics film of sterilization above, after being placed in 22-30 DEG C indoor cultivation 3-5 days, open plastics film, produce spore 3-5 days; Collect together with culture material, the moon dries in the air 5-7 days, puts into after pulverizer pulverizes, crosses 30 mesh sieves and obtain bacterium powder; The weight ratio of described liquid fermentation production and rice bran and wheat bran is 1:2:4;
Prepared by complex microorganism bacteria agent: the Alkaliphilic bacillus powder obtained in above-mentioned steps, bacillus laterosporus powder, bacillus pumilus, streptomyces aureus bacterium powder are mixed according to the ratio of 1 ~ 4:1 ~ 2:1 ~ 3:1 ~ 2, obtain complex microorganism bacteria agent.
Preferred, the preparation method of complex micro organism fungicide is as follows:
Prepared by Alkaliphilic bacillus: by Alkaliphilic bacillus strain inoculation to disinfection fermentation tank, fermention medium is: Semen Maydis powder 0.5%, extractum carnis 0.2%, bean cake powder 0.4%, Zulkovsky starch 0.2%, dipotassium hydrogen phosphate 0.03%, yeast extract 0.2%, Trisodium Citrate 0.08%, manganous sulfate 0.009%, pH7.8, fermentation condition: ventilation ratio is initiated with 2:1, culture temperature 37 DEG C, agitation revolution 150rpm, dissolved oxygen is not less than 30%, pH value is not less than 6.5, stir culture 7 hours, obtain fermented liquid, add Sodium phosphate dibasic and calcium chloride flocculation, rear employing filter press mode of having flocculated obtains bacterium mud, the 48 DEG C of forced air dryings of bacterium mud are to water content 30%, put into pulverizer after cyclonic separation to pulverize, cross 30 mesh sieves and obtain Alkaliphilic bacillus bacterium powder, viable bacteria content 2.5 × 10 in Alkaliphilic bacillus bacterium powder
8cfu/g,
Bacillus laterosporus: by bacillus laterosporus strain inoculation to disinfection fermentation tank, fermention medium is: peptone 0.5%, yeast extract paste 0.03%, agar 0.5%, dregs of beans 0.2%, dipotassium hydrogen phosphate 0.05%, potassium primary phosphate 0.04%, magnesium sulfate 0.09%, manganous sulfate 0.008%, pH7.0, fermentation condition: ventilation ratio is initiated with 9:5, culture temperature 37 DEG C, agitation revolution 150rpm, dissolved oxygen is not less than 30%, pH value is not less than 6.5, stir culture 7 hours, obtain fermented liquid and add Sodium phosphate dibasic and calcium chloride flocculation, rear employing filter press mode of having flocculated obtains bacterium mud, the 48 DEG C of forced air dryings of bacterium mud are to water content 30%, put into pulverizer after cyclonic separation to pulverize, cross 30 mesh sieves and obtain bacillus laterosporus bacterium powder,
Bacillus pumilus: by bacillus pumilus strain inoculation to disinfection fermentation tank, fermention medium is: starch 0.5%, yeast extract paste 0.03%, dregs of beans 0.5%, peptone 0.3%, dipotassium hydrogen phosphate 0.5%, glucose 0.3%, magnesium sulfate 0.09%, sodium-chlor 0.009%, pH6.9, fermentation condition: ventilation ratio is initiated with 1.1:0.5, culture temperature 37 DEG C, agitation revolution 150rpm, dissolved oxygen is not less than 30%, pH value is not less than 6.5, stir culture 7 hours, obtain fermented liquid and add Sodium phosphate dibasic and calcium chloride flocculation, rear employing filter press mode of having flocculated obtains bacterium mud, the 48 DEG C of forced air dryings of bacterium mud are to water content 32%, put into pulverizer after cyclonic separation to pulverize, cross 30 mesh sieves and obtain bacillus pumilus bacterium powder,
Prepared by streptomyces aureus microbial inoculum: adopt liquid rotating solid biphasic cultivation method to cultivate, viride is carried out liquid fermenting, obtain liquid fermentation production, the substratum of described liquid fermenting is: glucose 0.04%, Semen Maydis powder 0.5%, yeast powder 0.3%, analysis for soybean powder 0.4%g, sodium-chlor 0.08%, KH
2pO
40.009%, ammonium sulfate 0.02%; Fermentation condition is: pH6.3,27 DEG C, passes into air and air flow is 10L/min, 0.03Mpa; Shaking culture 3 days, obtains liquid fermentation production;
By liquid fermentation production with expanded vermiculite be carrier carry out solid fermentation, specifically liquid fermentation production is mixed with rice bran and wheat bran, be placed in the stainless steel mesh screen through liming or ozonization, cover the plastics film of sterilization above, be placed in the indoor cultivation of 25 DEG C after 4 days, open plastics film, produce spore 4 days; Collect together with culture material, the moon dries in the air 6 days, after putting into pulverizer pulverizing, crosses 30 mesh sieves and obtains bacterium powder; The weight ratio of described liquid fermentation production and rice bran and wheat bran is 1:2:4;
Prepared by complex microorganism bacteria agent: the Alkaliphilic bacillus powder obtained in above-mentioned steps, bacillus laterosporus powder, bacillus pumilus, streptomyces aureus bacterium powder are mixed according to the ratio of 3:2:2:1.5, obtain complex microorganism bacteria agent.
Continuous steaming pressure device of the present invention, the pressure supply unit comprising pressure measuring cylinder and be connected with pressure measuring cylinder, also comprises feeding warehouse and discharging bin, and the bottom of feeding warehouse is connected with one end of pressure measuring cylinder, and discharging bin is connected with the other end of pressure measuring cylinder; There is pusher pressure measuring cylinder inside; Multiple valve body is all had in feeding warehouse and discharging bin.
There are 4 valve bodies be arranged in order from top to bottom in feeding warehouse, feeding warehouse are divided into from bottom to up successively a, b, c, d, e five feed bin unit areas, have relief tube between d, e two feed bin unit, relief tube has check valve.
There are 4 valve bodies be arranged in order from top to bottom in discharging bin, discharging bin are divided into from top to bottom successively x, y, z, w, v five feed bin unit areas, have relief tube between w, v two feed bin unit, relief tube has check valve.
Pressure supply unit is vapour pipe, and vapour pipe can in spot distribution on pressure measuring cylinder, and vapour pipe also can be divided into multiple branch road and be connected with pressure measuring cylinder.
Pusher is auger.
Pressure measuring cylinder there is emergency pressure relief valve.
Pressure measuring cylinder and sea line are the pitch angle of 0.1-30 °, and pressure measuring cylinder is higher than the position of discharge port in the position near opening for feed, and namely pressure measuring cylinder vergence direction is downward-sloping gradually towards discharge port by opening for feed.
Feeding warehouse is vertical round shape, and feeding warehouse bottom is inverted truncated cone-shaped, and pressure measuring cylinder has opening for feed with feeding warehouse opposite position place;
Discharging bin is vertical round shape, and discharging bin top is truncated cone-shaped; Pressure measuring cylinder there is discharge port with discharging bin opposite position place.
Continuous steam pressure method of the present invention comprises following step:
First material is filled up pressure cylindrical shell and feeding warehouse, and close whole valve, in pressure measuring cylinder, high-pressure water vapor is injected by vapour pipe, in the cylindrical shell of pressure measuring cylinder, material starts timing after reaching working conditions, after reaching the reaction times, open a, between b valve body and x, two valve bodies between y valve body, auger simultaneously in trigger pressure cylinder cylindrical shell makes material in feeding warehouse a district unit slowly enter cylindrical shell, in feeding warehouse b district unit, material falls into the feed bin unit in a district simultaneously, material in the feed bin unit territory, x district of discharging bin is made to enter y district feed bin unit, material in pressure cylindrical shell enters the x district feed bin unit of discharging bin, after this end of processing, close a, between b and x, valve body between y, then feeding warehouse is step by step to material feeding in upper level feed bin unit and sealed material warehouse receipt is first, until top feed bin unit,
When e district, feeding warehouse top supplies of unit enters d district unit, now the d district unit of feeding warehouse is hole capital after selling all securities, and keep and the equal pressure of pressure measuring cylinder cylindrical shell, need first to carry out pressure release process to d district unit, operation is valve body and valve body closedown between c, d between d, e, air pressure is slowly leaked into e district unit by the check valve opened on relief tube, is opened by valve body between d, e and makes e district supplies of unit fall into d district unit, complete feeding warehouse fill process after pressure release.
In continuous steaming pressure device of the present invention, multiple valve body is all had in feeding warehouse and discharging bin, material adopts gravity condition freely falling body mode to carry between the multiple unit of feed bin, at feeding warehouse and discharging bin, multiple valve body is all set, realize the equipressure transmission of material in turnover feed bin, valve body in feed bin, in order to control the pressure equilibrium in feeding warehouse, discharging bin and pressure measuring cylinder, makes the pressurization in steam pressure process, steam pressure and pressure release carry out continuously.
Alkaline soil amendment of the present invention, can in and topsoil soils alkaline matter, reduce soil plough horizon Na
+, Cl
-ion content, improves soil exchangeable calcium-magnesium content, improves Soil structure, and present invention employs complex micro organism fungicide, can not only effectively improve alkalify soil, improve soil microenvironment, and can also eliminate soil disease microorganism.Alkaline soil amendment of the present invention can realize mass-producing and without three wastes problem, be suitable for large-scale popularization application, will produce huge economic benefit.
Continuous steaming pressure device provided by the present invention, owing to have employed the steam pressure device with feeding warehouse and discharging bin, in feeding warehouse and discharging bin, multiple valve body is set, to control the pressure equilibrium in feeding warehouse, discharging bin and pressure measuring cylinder, realize the continuous pressure in steam pressure process, steam pressure and pressure leak process, improve production efficiency and energy utilization rate.
Accompanying drawing explanation
Fig. 1 is the structural representation of the embodiment of the present invention 7;
Fig. 2 is the structural representation of the embodiment of the present invention 8;
In figure, 1-feeding warehouse, 2-valve body, 3-relief tube, 4-check valve, 5-pressure measuring cylinder, 6-emergency pressure relief valve, 7-discharging bin, 8-vapour pipe, 9-auger, 10-opening for feed, 11-discharge port.
Embodiment
Below in conjunction with the drawings and specific embodiments, the present invention is further described, so that those skilled in the art more understands the present invention, but does not limit the present invention with this.
Embodiment 1
Alkaline soil amendment comprises the component of following portions by weight:
Citric acid waste 14.13
Sulfur waste sulphur 4.56
Phosphogypsum/desulfurated plaster 22.38
Calcium superphosphate 16.05
Furfural dregs 32.45
Magnesium sulfate 16.48
Tai-Ace S 150 8.52
Sulphate 2.16
Humic acids 23.84;
Sulphate is mixture in ferric sulfate, zinc sulfate, manganous sulfate, and the ratio of weight and number of ferric sulfate, zinc sulfate, manganous sulfate is 1:1:1;
Sulfur waste sulphur is sulphur coated systems dedusting sulfur waste sulphur.
Select three pieces of soil properties identical and the ground of next-door neighbour, and the common feature on three pieces of ground is alkaline soils, pH value is about 8.7; These three pieces of ground are denoted as A, B, C respectively, use identical fertilizer, and the condition such as to hoe up weeds of watering is identical, the corn that varieties of plant is identical in A, B, C two pieces of ground.
Before maize planting, in A block ground, use soil conditioner of the present invention, use according to the amount on 50 kilograms, every mu of ground, measure soil acidity or alkalinity after 7 days, find that this plot pH value is reduced to 7.4 by 8.7, when detecting by the 30th day, pH value is about 7.6, and when detecting by the 100th day, pH value is about 7.8.Na in topsoil
+, Cl
-ion content reduces 25-34%, and the soil weight reduces 1.9-3.1g/cm
3, soil porosity increases 3.4-5.3%.
Before maize planting, use oxalic acid, measure soil acidity or alkalinity after 7 days in B block ground, find that this plot pH value is reduced to 7.5 by 8.7, when detecting by the 30th day, pH value is about 7.8, and when detecting by the 100th day, pH value is about 8.2.Na in topsoil
+, Cl
-ion is without noticeable change, and the soil weight reduces 0.3-0.8g/cm
3, soil porosity increases 0.7-1.1%.
C plot is blank, does not deal with soil, is only that other plantation is identical with A, B plot with fertilizer application condition;
When corn is ripe, compare the corn yield in two pieces of ground, result shows, the corn yield in A plot is 137% of B plot, is 179% of C plot.
As can be seen from above data, soil conditioner of the present invention, relative to common oxalic acid, to the conditioning repair of alkaline soil, improves the ability of Soil structure, all to be better than oxalic acid far away, and also will be far superior to for crop yield effect the soil using oxalic acid.
Embodiment 2
A kind of alkaline soil amendment, this alkaline soil amendment comprises the component of following portions by weight:
Citric acid waste 10
Sulfur waste sulphur 3
Phosphogypsum/desulfurated plaster 15
Calcium superphosphate 12
Furfural dregs 30
Magnesium sulfate 14
Tai-Ace S 150 6
Sulphate 2
Humic acids 15.
Sulphate is mixture in ferric sulfate, zinc sulfate, manganous sulfate, and the ratio of weight and number of ferric sulfate, zinc sulfate, manganous sulfate is 1:1:1;
Sulfur waste sulphur is sulphur coated systems dedusting sulfur waste sulphur.
Embodiment 3
A kind of alkaline soil amendment, this alkaline soil amendment comprises the component of following portions by weight:
Citric acid waste 20
Sulfur waste sulphur 10
Phosphogypsum/desulfurated plaster 30
Calcium superphosphate 20
Furfural dregs 35
Magnesium sulfate 18
Tai-Ace S 150 10
Sulphate 3
Humic acids 30.
Sulphate is mixture in ferric sulfate, zinc sulfate, manganous sulfate, and the ratio of weight and number of ferric sulfate, zinc sulfate, manganous sulfate is 1:1:1;
Sulfur waste sulphur is sulphur coated systems dedusting sulfur waste sulphur.
Embodiment 4
A kind of alkaline soil amendment, this alkaline soil amendment comprises the component of following portions by weight:
Citric acid waste 14.13
Sulfur waste sulphur 4.56
Phosphogypsum 22.38
Calcium superphosphate 16.05
Furfural dregs 32.45
Magnesium sulfate 16.48
Tai-Ace S 150 8.52
Sulphate 2.16
Humic acids 23.84
Chitosan 1.25;
Sulphate is mixture in ferric sulfate, zinc sulfate, manganous sulfate, and the ratio of weight and number of ferric sulfate, zinc sulfate, manganous sulfate is 1:1:1;
Sulfur waste sulphur is sulphur coated systems dedusting sulfur waste sulphur;
The composite fungus agent that complex micro organism fungicide is Alkaliphilic bacillus, bacillus laterosporus, bacillus pumilus, streptomyces aureus form; The weight ratio of described Alkaliphilic bacillus, bacillus laterosporus, bacillus pumilus, streptomyces aureus is 3:2:2:1.5;
Wherein Alkaliphilic bacillus 1.8 × 10
8cfu/g, bacillus laterosporus 1.4 × 10
8cfu/g, bacillus pumilus 1.2 × 10
8cfu/g, streptomyces aureus 0.9 × 10
8cfu/g.
Select three pieces of soil properties identical and the ground of next-door neighbour, and the common feature on three pieces of ground is alkaline soils, pH value is about 8.7; These three pieces of ground are denoted as A, B, C respectively, use identical fertilizer, and the condition such as to hoe up weeds of watering is identical, the corn that varieties of plant is identical in A, B, C two pieces of ground.
Before maize planting, in A block ground, use soil conditioner of the present invention, use according to the amount on 50 kilograms, every mu of ground, measure soil acidity or alkalinity after 7 days, find that this plot pH value is reduced to 7.2 by 8.7, when detecting by the 30th day, pH value is about 7.4, and when detecting by the 100th day, pH value is about 7.6.Na in topsoil
+, Cl
-ion content reduces 22-30%, and the soil weight reduces 1.7-2.9g/cm
3, soil porosity increases 3.1-5.0%.
Before maize planting, use oxalic acid, measure soil acidity or alkalinity after 7 days in B block ground, find that this plot pH value is reduced to 7.4 by 8.7, when detecting by the 30th day, pH value is about 7.6, and when detecting by the 100th day, pH value is about 8.3.Na in topsoil
+, Cl
-ion is without noticeable change, and the soil weight reduces 0.4-0.7g/cm
3, soil porosity increases 0.6-1.0%.C plot is blank, does not deal with soil, is only that other plantation is identical with A, B plot with fertilizer application condition;
When corn is ripe, compare the corn yield in two pieces of ground, result shows, the corn yield in A plot is 148% of B plot, is 197% of C plot.
As can be seen from above data, soil conditioner of the present invention, relative to common oxalic acid, to the conditioning repair of alkaline soil, improves the ability of Soil structure, oxalic acid to be better than far away, and also will be far superior to for crop yield effect the soil using oxalic acid.
The Corn diseases and insect pests in A plot is lower by 19.6% than the disease and pest incidence in B, C plot, 38.3%, visible, complex microbial inoculum of the present invention is repaired and the effect of improvement except playing acid soil, and also plays restraining effect to disease and pest.
Embodiment 5
A kind of alkaline soil amendment, this alkaline soil amendment comprises the component of following portions by weight:
Citric acid waste 10
Sulfur waste sulphur 3
Desulfurated plaster 15
Calcium superphosphate 12
Furfural dregs 30
Magnesium sulfate 14
Tai-Ace S 150 6
Sulphate 2
Humic acids 15
Complex micro organism fungicide 0.2
The preparation method of complex micro organism fungicide is as follows:
Prepared by Alkaliphilic bacillus: by Alkaliphilic bacillus strain inoculation to disinfection fermentation tank, fermention medium is: Semen Maydis powder 0.2%, extractum carnis 0.1%, bean cake powder 0.2%, Zulkovsky starch 0.1%, dipotassium hydrogen phosphate 0.02%, yeast extract 0.1%, Trisodium Citrate 0.05%, manganous sulfate 0.006%, pH7.5, fermentation condition: ventilation ratio is initiated with 8:5, culture temperature 35 DEG C, agitation revolution 100rpm, dissolved oxygen is not less than 30%, pH value is not less than 6.5, stir culture 6 hours, obtain fermented liquid, add Sodium phosphate dibasic and calcium chloride flocculation, rear employing filter press mode of having flocculated obtains bacterium mud, the 45 DEG C of forced air dryings of bacterium mud are to water content 25%, put into pulverizer after cyclonic separation to pulverize, cross 30 mesh sieves and obtain Alkaliphilic bacillus bacterium powder, viable bacteria content 1 × 10 in Alkaliphilic bacillus bacterium powder
8cfu/g,
Bacillus laterosporus: by bacillus laterosporus strain inoculation to disinfection fermentation tank, fermention medium is: peptone 0.2%, yeast extract paste 0.01%, agar 0.2%, dregs of beans 0.1%, dipotassium hydrogen phosphate 0.08%, potassium primary phosphate 0.01%, magnesium sulfate 0.05%, manganous sulfate 0.006%, pH6.8, fermentation condition: ventilation ratio is initiated with 7:5, culture temperature 35 DEG C, agitation revolution 100rpm, dissolved oxygen is not less than 30%, pH value is not less than 6.5, stir culture 6 hours, obtain fermented liquid and add Sodium phosphate dibasic and calcium chloride flocculation, rear employing filter press mode of having flocculated obtains bacterium mud, the 45 DEG C of forced air dryings of bacterium mud are to water content 25%, put into pulverizer after cyclonic separation to pulverize, cross 30 mesh sieves and obtain bacillus laterosporus bacterium powder,
Bacillus pumilus: by bacillus pumilus strain inoculation to disinfection fermentation tank, fermention medium is: starch 0.2%, yeast extract paste 0.01%, dregs of beans 0.2%, peptone 0.1%, dipotassium hydrogen phosphate 0.2%, glucose 0.1%, magnesium sulfate 0.05%, sodium-chlor 0.006%, pH6.8, fermentation condition: ventilation ratio is initiated with 8:5, culture temperature 35 DEG C, agitation revolution 100rpm, dissolved oxygen is not less than 30%, pH value is not less than 6.5, stir culture 6 hours, obtain fermented liquid and add Sodium phosphate dibasic and calcium chloride flocculation, rear employing filter press mode of having flocculated obtains bacterium mud, the 45 DEG C of forced air dryings of bacterium mud are to water content 25%, put into pulverizer after cyclonic separation to pulverize, cross 30 mesh sieves and obtain bacillus pumilus bacterium powder,
Prepared by streptomyces aureus microbial inoculum: adopt liquid rotating solid biphasic cultivation method to cultivate, viride is carried out liquid fermenting, obtains liquid fermentation production, the substratum of described liquid fermenting is:
Glucose 0.01%, Semen Maydis powder 0.2%, yeast powder 0.1%, analysis for soybean powder 0.2%g, sodium-chlor 0.05%, KH
2pO
40.006%, ammonium sulfate 0.01%; Fermentation condition is: pH6.1,25 DEG C, passes into air and air flow is 9L/min, 0.02Mpa; Shaking culture 2-4 days, obtains liquid fermentation production;
By liquid fermentation production with expanded vermiculite be carrier carry out solid fermentation, specifically liquid fermentation production is mixed with rice bran and wheat bran, be placed in the stainless steel mesh screen through liming or ozonization, cover the plastics film of sterilization above, be placed in the indoor cultivation of 22 DEG C after 3 days, open plastics film, produce spore 3 days; Collect together with culture material, the moon dries in the air 5 days, after putting into pulverizer pulverizing, crosses 30 mesh sieves and obtains bacterium powder; The weight ratio of described liquid fermentation production and rice bran and wheat bran is 1:2:4;
Prepared by complex microorganism bacteria agent: the Alkaliphilic bacillus powder obtained in above-mentioned steps, bacillus laterosporus powder, bacillus pumilus, streptomyces aureus bacterium powder are mixed according to the ratio of 1:1:1:1, obtain complex microorganism bacteria agent.
Embodiment 6
A kind of alkaline soil amendment, this alkaline soil amendment comprises the component of following portions by weight:
Citric acid waste 20
Sulfur waste sulphur 10
Phosphogypsum 30
Calcium superphosphate 20
Furfural dregs 35
Magnesium sulfate 18
Tai-Ace S 150 10
Sulphate 3
Humic acids 30
Complex micro organism fungicide 1
The preparation method of complex micro organism fungicide is as follows:
Prepared by Alkaliphilic bacillus: by Alkaliphilic bacillus strain inoculation to disinfection fermentation tank, fermention medium is: Semen Maydis powder 0.8%, extractum carnis 0.6%, bean cake powder 0.8%, Zulkovsky starch 0.4%, dipotassium hydrogen phosphate 0.08%, yeast extract 0.5%, Trisodium Citrate 0.15%, manganous sulfate 0.012%, pH7.9, fermentation condition: ventilation ratio is initiated with 1.2:0.5, culture temperature 40 DEG C, agitation revolution 200rpm, dissolved oxygen is not less than 30%, pH value is not less than 6.5, stir culture 8 hours, obtain fermented liquid, add Sodium phosphate dibasic and calcium chloride flocculation, rear employing filter press mode of having flocculated obtains bacterium mud, the 50 DEG C of forced air dryings of bacterium mud are to water content 35%, put into pulverizer after cyclonic separation to pulverize, cross 30 mesh sieves and obtain Alkaliphilic bacillus bacterium powder, viable bacteria content 3 × 10 in Alkaliphilic bacillus bacterium powder
8cfu/g,
Bacillus laterosporus: by bacillus laterosporus strain inoculation to disinfection fermentation tank, fermention medium is: peptone 0.8%, yeast extract paste 0.06%, agar 0.8%, dregs of beans 0.4%, dipotassium hydrogen phosphate 0.08%, potassium primary phosphate 0.05%, magnesium sulfate 0.15%, manganous sulfate 0.012%, pH7.2, fermentation condition: ventilation ratio is initiated with 2:1, culture temperature 40 DEG C, agitation revolution 200rpm, dissolved oxygen is not less than 30%, pH value is not less than 6.5, stir culture 8 hours, obtain fermented liquid and add Sodium phosphate dibasic and calcium chloride flocculation, rear employing filter press mode of having flocculated obtains bacterium mud, the 50 DEG C of forced air dryings of bacterium mud are to water content 35%, put into pulverizer after cyclonic separation to pulverize, cross 30 mesh sieves and obtain bacillus laterosporus bacterium powder,
Bacillus pumilus: by bacillus pumilus strain inoculation to disinfection fermentation tank, fermention medium is: starch 0.8%, yeast extract paste 0.06%, dregs of beans 0.8%, peptone 0.4%, dipotassium hydrogen phosphate 0.8%, glucose 0.5%, magnesium sulfate 0.15%, sodium-chlor 0.012%, pH7.2, fermentation condition: ventilation ratio is initiated with 1.2:0.5, culture temperature 40 DEG C, agitation revolution 200rpm, dissolved oxygen is not less than 30%, pH value is not less than 6.5, stir culture 8 hours, obtain fermented liquid and add Sodium phosphate dibasic and calcium chloride flocculation, rear employing filter press mode of having flocculated obtains bacterium mud, the 50 DEG C of forced air dryings of bacterium mud are to water content 35%, put into pulverizer after cyclonic separation to pulverize, cross 30 mesh sieves and obtain bacillus pumilus bacterium powder,
Prepared by streptomyces aureus microbial inoculum: adopt liquid rotating solid biphasic cultivation method to cultivate, viride is carried out liquid fermenting, obtains liquid fermentation production, the substratum of described liquid fermenting is:
Glucose 0.06%, Semen Maydis powder 0.8%, yeast powder 0.4%, analysis for soybean powder 0.6%g, sodium-chlor 0.15%, KH
2pO
40.012%, ammonium sulfate 0.04%; Fermentation condition is: pH6.5,29 DEG C, passes into air and air flow is 11L/min, 0.04Mpa; Shaking culture 4 days, obtains liquid fermentation production;
By liquid fermentation production with expanded vermiculite be carrier carry out solid fermentation, specifically liquid fermentation production is mixed with rice bran and wheat bran, be placed in the stainless steel mesh screen through liming or ozonization, cover the plastics film of sterilization above, be placed in the indoor cultivation of 30 DEG C after 5 days, open plastics film, produce spore 5 days; Collect together with culture material, the moon dries in the air 7 days, after putting into pulverizer pulverizing, crosses 30 mesh sieves and obtains bacterium powder; The weight ratio of described liquid fermentation production and rice bran and wheat bran is 1:2:4;
Prepared by complex microorganism bacteria agent: the Alkaliphilic bacillus powder obtained in above-mentioned steps, bacillus laterosporus powder, bacillus pumilus, streptomyces aureus bacterium powder are mixed according to the ratio of 4:2:3:2, obtain complex microorganism bacteria agent.
Embodiment 7
Continuous steaming pressure device of the present invention, comprise pressure measuring cylinder 5, also comprise the feeding warehouse 1 respectively in vertical tubular and discharging bin 7, feeding warehouse 1 bottom is inverted truncated cone-shaped, there is opening for feed 10 at pressure measuring cylinder 5 and feeding warehouse 1 opposite position place, and feeding warehouse 1 bottom is connected by opening for feed 10 with pressure measuring cylinder 5; Discharging bin 7 is vertical round shape, and discharging bin 7 top is truncated cone-shaped, and there is discharge port 11 at pressure measuring cylinder 5 and discharging bin 7 opposite position place, and discharging bin 7 top is connected by discharge port 11 with pressure measuring cylinder 5;
There is auger 9 pressure measuring cylinder 5 inside as pusher, constantly feeding warehouse 1 is released into the stirring of the material of pressure measuring cylinder 5, revolving pushing, improves the steam pressure efficiency of material.
Four valve bodies 2 are all had in feeding warehouse 1 and discharging bin 7,4 valve bodies be arranged in order from top to bottom 2 in feeding warehouse 1, valve body 2 can be sealed butterfly valve, feeding warehouse 1 is divided into from top to bottom successively e, d, c, b, a five feed bin unit areas, sealed butterfly valve can control e, d, c, b, a five feed bin unit areas close or conducting, d, e have relief tube between district, relief tube have check valve 4.When valve body 2 is closed, adjacent two feed unit are closed, and form independently seal cavity, when valve body 2 is opened, adjacent two feed unit are connected.No matter arrange how many feed bin unit, relief tube is all arranged between the adjacent feed bin unit in two, the top of feeding warehouse 1; In like manner, relief tube is also arranged between the adjacent feed bin unit in two, bottom of discharging bin 7;
There are 4 valve bodies be arranged in order from top to bottom 2 in discharging bin 7, discharging bin 7 are divided into from top to bottom successively x, y, z, w, v five feed bin unit areas.
Vapour pipe 8 is divided into multiple branch road and is connected with pressure measuring cylinder 5, provides pressure to pressure measuring cylinder 5.In the present embodiment, vapour pipe 8 is placed in the bottom of pressure measuring cylinder 5, and arranges along the axial direction due of pressure measuring cylinder 5; High pressure steam in such vapour pipe 8 is carried from top to bottom, connect larger with the contact surface of material, pressure, temperature transmission effect are better, simultaneously, the high pressure steam risen forms the uplift force to material, prevent the overweight shape to pressure measuring cylinder 5 of material from causing deformation effect, in addition, the high pressure steam of rising also can effectively prevent material from becoming block with the lower wall tubercle of pressure measuring cylinder 5.
Certain vapour pipe 8 also can design and be connected with pressure measuring cylinder 5 in other position, the top of such as pressure measuring cylinder 5 or side.
Pressure measuring cylinder 5 there is emergency pressure relief valve 6, so that emergency pressure relief is used.
Pressure measuring cylinder 5 and sea line are the pitch angle of about 8 °, and pressure measuring cylinder 5 is designed to oblique form, are that vergence direction is downward-sloping gradually towards discharge port 11 by opening for feed 10 in order to make pressure steam in pressure measuring cylinder 5 can better utilised.
The design of oblique pressure cylinder 5, is convenient to upwards, to the direction of opening for feed 10 condense carrying out adding the hot steam after heat exchange with material, can form the pressure towards discharge port 11 to material on the one hand, be convenient to discharging; On the other hand, the steam after being utilized also is with and is had surplus heat, and can carry out preheating being entered by pressure measuring cylinder 5 inner chamber feed unit to being about to the material entered in pressure measuring cylinder 5, improves the heat utilization efficiency of steam.
Continuous steaming pressure device of the present invention is when processing soil conditioner, first the soil conditioner in powder or fine particle shape after pulverization process is dropped into feeding warehouse, its operation logic is as follows: continuous steaming pressure device is when running for the first time, before logical steam first will in fine granularity or pulverous soil conditioner fill up pressure cylindrical shell 5 and feeding warehouse 1, and close whole valve 2, in pressure measuring cylinder 5, high-pressure water vapor is injected by vapour pipe 8, in the cylindrical shell of pressure measuring cylinder 5, material starts timing after reaching working conditions, after reaching the reaction times, open a, between b valve body and x, two valve bodies 2 between y valve body, auger 9 simultaneously in trigger pressure cylinder cylindrical shell makes material in feeding warehouse 1a district unit slowly enter cylindrical shell, in feeding warehouse 1b district unit, material falls into the feed bin unit in a district simultaneously, material in the feed bin unit territory, x district of discharging bin 7 is made to enter y district feed bin unit, material in pressure measuring cylinder 5 body enters the x district feed bin unit of discharging bin 7, after this end of processing, close a, between b and x, valve body 2 between y, then feeding warehouse 1 is step by step to material feeding in upper level feed bin unit and sealed material warehouse receipt is first, until top feed bin unit.
When e district, feeding warehouse 1 top supplies of unit enters d district unit, now the d district unit of feeding warehouse 1 is hole capital after selling all securities, and keep and the equal pressure of pressure measuring cylinder 5 cylindrical shell, need first to carry out pressure release process to d district unit, operation be between d, e valve body 2 and between c, d valve body 2 close, air pressure is slowly leaked into e district unit by 4 check valves opened on relief tube 6, is opened by valve body between d, e 2 and makes e district supplies of unit fall into d district unit, complete feeding warehouse 1 fill process after pressure release.
In certain the present invention, the feed bin unit of feeding warehouse 1 or discharging bin 7 might not be confined to 4, also can arrange multiple according to specific needs, as long as can realize the present invention.
Such as, in the present invention, feeding warehouse 1 is set to 5 feed bin unit, and discharging bin 7 only designs 3 feed bin unit, also drops within protection scope of the present invention as similar conversion.
Embodiment 8
Difference from Example 7 is, discharging bin is set to x, y, z three feed bin unit, its operation logic is with embodiment 7.
Claims (10)
1. an alkaline soil amendment, is characterized in that, described alkaline soil amendment comprises the component of following portions by weight:
Citric acid waste 10-20
Sulfur waste sulphur 3-10
Phosphogypsum/desulfurated plaster 15-30
Calcium superphosphate 12-20
Furfural dregs 30-35
Magnesium sulfate 14-18
Tai-Ace S 150 6-10
Sulphate 2-3
Humic acids 15-30.
2. a kind of alkaline soil amendment as claimed in claim 1, is characterized in that, described soil conditioner comprises the component of following portions by weight:
Citric acid waste 12-15
Sulfur waste sulphur 3-6
Phosphogypsum/desulfurated plaster 20-25
Calcium superphosphate 15-17
Furfural dregs 30-35
Magnesium sulfate 16-17
Tai-Ace S 150 8-9
Sulphate 2-3
Humic acids 22-25;
Above-mentioned sulphate is at least one of ferric sulfate, zinc sulfate, manganous sulfate.
3. a kind of alkaline soil amendment as claimed in claim 1, is characterized in that, described soil conditioner comprises the component of following portions by weight:
Citric acid waste 14.13
Sulfur waste sulphur 4.56
Phosphogypsum/desulfurated plaster 22.38
Calcium superphosphate 16.05
Furfural dregs 32.45
Magnesium sulfate 16.48
Tai-Ace S 150 8.52
Sulphate 2.16
Humic acids 23.84;
Described sulphate is mixture in ferric sulfate, zinc sulfate, manganous sulfate, and the ratio of weight and number of ferric sulfate, zinc sulfate, manganous sulfate is 1:1:1;
Described sulfur waste sulphur is sulphur coated systems dedusting sulfur waste sulphur.
4. a kind of alkaline soil amendment as claimed in claim 1, is characterized in that, described soil conditioner comprises the component of following portions by weight:
Citric acid waste 10-20
Sulfur waste sulphur 3-10
Phosphogypsum/desulfurated plaster 15-30
Calcium superphosphate 12-20
Furfural dregs 30-35
Magnesium sulfate 14-18
Tai-Ace S 150 6-10
Sulphate 2-3
Humic acids 15-30
Complex micro organism fungicide 0.2-1
The composite fungus agent that described complex micro organism fungicide is Alkaliphilic bacillus, bacillus laterosporus, bacillus pumilus, streptomyces aureus form; The weight ratio of described Alkaliphilic bacillus, bacillus laterosporus, bacillus pumilus, streptomyces aureus is 1 ~ 4:1 ~ 2:1 ~ 3:1 ~ 2;
Wherein Alkaliphilic bacillus 1 ~ 3 × 10
8cfu/g, bacillus laterosporus 0.5 ~ 2 × 10
8cfu/g, bacillus pumilus 0.5 ~ 1 × 10
8cfu/g, streptomyces aureus 0.5 ~ 1.5 × 10
8cfu/g.
5. a kind of alkaline soil amendment as claimed in claim 1, is characterized in that, described soil conditioner comprises the component of following portions by weight:
Citric acid waste 14.13
Sulfur waste sulphur 4.56
Phosphogypsum/desulfurated plaster 22.38
Calcium superphosphate 16.05
Furfural dregs 32.45
Magnesium sulfate 16.48
Tai-Ace S 150 8.52
Sulphate 2.16
Humic acids 23.84
Chitosan 1.25;
Described sulphate is mixture in ferric sulfate, zinc sulfate, manganous sulfate, and the ratio of weight and number of ferric sulfate, zinc sulfate, manganous sulfate is 1:1:1;
Described sulfur waste sulphur is sulphur coated systems dedusting sulfur waste sulphur;
The composite fungus agent that described complex micro organism fungicide is Alkaliphilic bacillus, bacillus laterosporus, bacillus pumilus, streptomyces aureus form; The weight ratio of described Alkaliphilic bacillus, bacillus laterosporus, bacillus pumilus, streptomyces aureus is 3:2:2:1.5;
Wherein Alkaliphilic bacillus 1.8 × 10
8cfu/g, bacillus laterosporus 1.4 × 10
8cfu/g, bacillus pumilus 1.2 × 10
8cfu/g, streptomyces aureus 0.9 × 10
8cfu/g.
6. a kind of alkaline soil amendment as claimed in claim 1, it is characterized in that, the preparation method of described complex micro organism fungicide is as follows:
Prepared by Alkaliphilic bacillus: by Alkaliphilic bacillus strain inoculation to disinfection fermentation tank, fermention medium is: Semen Maydis powder 0.2-0.8%, extractum carnis 0.1-0.6%, bean cake powder 0.2-0.8%, Zulkovsky starch 0.1-0.4%, dipotassium hydrogen phosphate 0.02-0.08%, yeast extract 0.1-0.5%, Trisodium Citrate 0.05-0.15%, manganous sulfate 0.006-0.012%, pH7.5-7.9, fermentation condition: ventilation ratio is initiated with 0.8-1.2:0.5, culture temperature 35-40 DEG C, agitation revolution 100-200rpm, dissolved oxygen is not less than 30%, pH value is not less than 6.5, stir culture 6-8 hour, obtain fermented liquid, add Sodium phosphate dibasic and calcium chloride flocculation, rear employing filter press mode of having flocculated obtains bacterium mud, the 45-50 DEG C of forced air drying of bacterium mud is to water content 25-35%, put into pulverizer after cyclonic separation to pulverize, cross 30 mesh sieves and obtain Alkaliphilic bacillus bacterium powder, viable bacteria content 1 ~ 3 × 10 in Alkaliphilic bacillus bacterium powder
8cfu/g,
Bacillus laterosporus: by bacillus laterosporus strain inoculation to disinfection fermentation tank, fermention medium is: peptone 0.2-0.8%, yeast extract paste 0.01-0.06%, agar 0.2-0.8%, dregs of beans 0.1-0.4%, dipotassium hydrogen phosphate 0.02-0.08%, potassium primary phosphate 0.01-0.05%, magnesium sulfate 0.05-0.15%, manganous sulfate 0.006-0.012%, pH6.8-7.2, fermentation condition: ventilation ratio is initiated with 0.7-1.0:0.5, culture temperature 35-40 DEG C, agitation revolution 100-200rpm, dissolved oxygen is not less than 30%, pH value is not less than 6.5, stir culture 6-8 hour, obtain fermented liquid and add Sodium phosphate dibasic and calcium chloride flocculation, rear employing filter press mode of having flocculated obtains bacterium mud, the 45-50 DEG C of forced air drying of bacterium mud is to water content 25-35%, put into pulverizer after cyclonic separation to pulverize, cross 30 mesh sieves and obtain bacillus laterosporus bacterium powder,
Bacillus pumilus: by bacillus pumilus strain inoculation to disinfection fermentation tank, fermention medium is: starch 0.2-0.8%, yeast extract paste 0.01-0.06%, dregs of beans 0.2-0.8%, peptone 0.1-0.4%, dipotassium hydrogen phosphate 0.2-0.8%, glucose 0.1-0.5%, magnesium sulfate 0.05-0.15%, sodium-chlor 0.006-0.012%, pH6.8-7.2, fermentation condition: ventilation ratio is initiated with 0.8-1.2:0.5, culture temperature 35-40 DEG C, agitation revolution 100-200rpm, dissolved oxygen is not less than 30%, pH value is not less than 6.5, stir culture 6-8 hour, obtain fermented liquid and add Sodium phosphate dibasic and calcium chloride flocculation, rear employing filter press mode of having flocculated obtains bacterium mud, the 45-50 DEG C of forced air drying of bacterium mud is to water content 25-35%, put into pulverizer after cyclonic separation to pulverize, cross 30 mesh sieves and obtain bacillus pumilus bacterium powder,
Prepared by streptomyces aureus microbial inoculum: adopt liquid rotating solid biphasic cultivation method to cultivate, viride is carried out liquid fermenting, obtains liquid fermentation production, the substratum of described liquid fermenting is:
Glucose 0.01-0.06%, Semen Maydis powder 0.2-0.8%, yeast powder 0.1-0.4%, analysis for soybean powder 0.2-0.6%g,
Sodium-chlor 0.05-0.15%, KH
2pO
40.006-0.012%, ammonium sulfate 0.01-0.04%; Fermentation condition is: pH6.1-6.5,25-29 DEG C, passes into air and air flow is 9-11L/min, 0.02-0.04Mpa; Shaking culture 2-4 days, obtains liquid fermentation production;
By liquid fermentation production with expanded vermiculite be carrier carry out solid fermentation, specifically liquid fermentation production is mixed with rice bran and wheat bran, be placed in the stainless steel mesh screen through liming or ozonization, cover the plastics film of sterilization above, after being placed in 22-30 DEG C indoor cultivation 3-5 days, open plastics film, produce spore 3-5 days; Collect together with culture material, the moon dries in the air 5-7 days, puts into after pulverizer pulverizes, crosses 30 mesh sieves and obtain bacterium powder; The weight ratio of described liquid fermentation production and rice bran and wheat bran is 1:2:4;
Prepared by complex microorganism bacteria agent: the Alkaliphilic bacillus powder obtained in above-mentioned steps, bacillus laterosporus powder, bacillus pumilus, streptomyces aureus bacterium powder are mixed according to the ratio of 1 ~ 4:1 ~ 2:1 ~ 3:1 ~ 2, obtain complex microorganism bacteria agent.
7. a kind of alkaline soil amendment as claimed in claim 6, it is characterized in that, the preparation method of described complex micro organism fungicide is as follows:
Prepared by Alkaliphilic bacillus: by Alkaliphilic bacillus strain inoculation to disinfection fermentation tank, fermention medium is: Semen Maydis powder 0.5%, extractum carnis 0.2%, bean cake powder 0.4%, Zulkovsky starch 0.2%, dipotassium hydrogen phosphate 0.03%, yeast extract 0.2%, Trisodium Citrate 0.08%, manganous sulfate 0.009%, pH7.8, fermentation condition: ventilation ratio is initiated with 2:1, culture temperature 37 DEG C, agitation revolution 150rpm, dissolved oxygen is not less than 30%, pH value is not less than 6.5, stir culture 7 hours, obtain fermented liquid, add Sodium phosphate dibasic and calcium chloride flocculation, rear employing filter press mode of having flocculated obtains bacterium mud, the 48 DEG C of forced air dryings of bacterium mud are to water content 30%, put into pulverizer after cyclonic separation to pulverize, cross 30 mesh sieves and obtain Alkaliphilic bacillus bacterium powder, viable bacteria content 2.5 × 10 in Alkaliphilic bacillus bacterium powder
8cfu/g,
Bacillus laterosporus: by bacillus laterosporus strain inoculation to disinfection fermentation tank, fermention medium is: peptone 0.5%, yeast extract paste 0.03%, agar 0.5%, dregs of beans 0.2%, dipotassium hydrogen phosphate 0.05%, potassium primary phosphate 0.04%, magnesium sulfate 0.09%, manganous sulfate 0.008%, pH7.0, fermentation condition: ventilation ratio is initiated with 9:5, culture temperature 37 DEG C, agitation revolution 150rpm, dissolved oxygen is not less than 30%, pH value is not less than 6.5, stir culture 7 hours, obtain fermented liquid and add Sodium phosphate dibasic and calcium chloride flocculation, rear employing filter press mode of having flocculated obtains bacterium mud, the 48 DEG C of forced air dryings of bacterium mud are to water content 30%, put into pulverizer after cyclonic separation to pulverize, cross 30 mesh sieves and obtain bacillus laterosporus bacterium powder,
Bacillus pumilus: by bacillus pumilus strain inoculation to disinfection fermentation tank, fermention medium is: starch 0.5%, yeast extract paste 0.03%, dregs of beans 0.5%, peptone 0.3%, dipotassium hydrogen phosphate 0.5%, glucose 0.3%, magnesium sulfate 0.09%, sodium-chlor 0.009%, pH6.9, fermentation condition: ventilation ratio is initiated with 1.1:0.5, culture temperature 37 DEG C, agitation revolution 150rpm, dissolved oxygen is not less than 30%, pH value is not less than 6.5, stir culture 7 hours, obtain fermented liquid and add Sodium phosphate dibasic and calcium chloride flocculation, rear employing filter press mode of having flocculated obtains bacterium mud, the 48 DEG C of forced air dryings of bacterium mud are to water content 32%, put into pulverizer after cyclonic separation to pulverize, cross 30 mesh sieves and obtain bacillus pumilus bacterium powder,
Prepared by streptomyces aureus microbial inoculum: adopt liquid rotating solid biphasic cultivation method to cultivate, viride is carried out liquid fermenting, obtain liquid fermentation production, the substratum of described liquid fermenting is: glucose 0.04%, Semen Maydis powder 0.5%, yeast powder 0.3%, analysis for soybean powder 0.4%g, sodium-chlor 0.08%, KH
2pO
40.009%, ammonium sulfate 0.02%; Fermentation condition is: pH6.3,27 DEG C, passes into air and air flow is 10L/min, 0.03Mpa; Shaking culture 3 days, obtains liquid fermentation production;
By liquid fermentation production with expanded vermiculite be carrier carry out solid fermentation, specifically liquid fermentation production is mixed with rice bran and wheat bran, be placed in the stainless steel mesh screen through liming or ozonization, cover the plastics film of sterilization above, be placed in the indoor cultivation of 25 DEG C after 4 days, open plastics film, produce spore 4 days; Collect together with culture material, the moon dries in the air 6 days, after putting into pulverizer pulverizing, crosses 30 mesh sieves and obtains bacterium powder; The weight ratio of described liquid fermentation production and rice bran and wheat bran is 1:2:4;
Prepared by complex microorganism bacteria agent: the Alkaliphilic bacillus powder obtained in above-mentioned steps, bacillus laterosporus powder, bacillus pumilus, streptomyces aureus bacterium powder are mixed according to the ratio of 3:2:2:1.5, obtain complex microorganism bacteria agent.
8. the continuous steaming pressure device of a kind of heavy soil soil conditioner as claimed in claim 1, the pressure supply unit comprising pressure measuring cylinder and be connected with pressure measuring cylinder, it is characterized in that, described steam pressure device also comprises feeding warehouse and discharging bin, the bottom of described feeding warehouse is connected with one end of pressure measuring cylinder, and described discharging bin is connected with the other end of pressure measuring cylinder; There is pusher described pressure measuring cylinder inside; Multiple valve body is all had in described feeding warehouse and discharging bin.
9. the continuous steaming pressure device of a kind of heavy soil soil conditioner as claimed in claim 8, is characterized in that,
There are 4 valve bodies be arranged in order from top to bottom in described feeding warehouse, feeding warehouse are divided into from bottom to up successively a, b, c, d, e five feed bin unit, have relief tube between described d, e two feed bin unit, described relief tube has check valve;
There are 4 valve bodies be arranged in order from top to bottom in described discharging bin, discharging bin are divided into from top to bottom successively x, y, z, w, v five regions, have relief tube between described w, v two feed bin unit, described relief tube has check valve;
Described pressure supply unit is vapour pipe;
Described pusher is auger;
Described pressure measuring cylinder there is emergency pressure relief valve;
Pressure measuring cylinder and sea line are the pitch angle of 0.1-30 °;
Described feeding warehouse is vertical round shape, and feeding warehouse bottom is inverted truncated cone-shaped, and described pressure measuring cylinder has opening for feed with feeding warehouse opposite position place;
Described discharging bin is vertical round shape, and discharging bin top is truncated cone-shaped; Described pressure measuring cylinder there is discharge port with discharging bin opposite position place.
10. utilize the continuous steaming pressure device according to any one of claim 8-9 to carry out a method for continuous steam pressure, comprise following step:
First material is filled up pressure cylindrical shell and feeding warehouse, and close whole valve, in pressure measuring cylinder, high-pressure water vapor is injected by vapour pipe, in the cylindrical shell of pressure measuring cylinder, material starts timing after reaching working conditions, after reaching the reaction times, open a, between b valve body and x, two valve bodies between y valve body, auger simultaneously in trigger pressure cylinder cylindrical shell makes material in feeding warehouse a district unit slowly enter cylindrical shell, in feeding warehouse b district unit, material falls into the feed bin unit in a district simultaneously, material in the feed bin unit territory, x district of discharging bin is made to enter y district feed bin unit, material in pressure cylindrical shell enters the x district feed bin unit of discharging bin, after this end of processing, close a, between b and x, valve body between y, then feeding warehouse is step by step to material feeding in upper level feed bin unit and sealed material warehouse receipt is first, until top feed bin unit,
When e district, feeding warehouse top supplies of unit enters d district unit, now the d district unit of feeding warehouse is hole capital after selling all securities, and keep and the equal pressure of pressure measuring cylinder cylindrical shell, first pressure release process is carried out to d district unit, operation is valve body 2 and valve body closedown between c, d between d, e, air pressure is slowly leaked into e district unit by the check valve opened on relief tube, is opened by valve body between d, e and makes e district supplies of unit fall into d district unit, complete feeding warehouse fill process after pressure release.
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