CN104229765B - A kind of production method preparing ammonium phosphate by-product Radix Paeoniae Rubra special fertilizer - Google Patents
A kind of production method preparing ammonium phosphate by-product Radix Paeoniae Rubra special fertilizer Download PDFInfo
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- 239000003337 fertilizer Substances 0.000 title claims abstract description 70
- 239000004254 Ammonium phosphate Substances 0.000 title claims abstract description 57
- 229910000148 ammonium phosphate Inorganic materials 0.000 title claims abstract description 57
- 235000019289 ammonium phosphates Nutrition 0.000 title claims abstract description 57
- MNNHAPBLZZVQHP-UHFFFAOYSA-N diammonium hydrogen phosphate Chemical compound [NH4+].[NH4+].OP([O-])([O-])=O MNNHAPBLZZVQHP-UHFFFAOYSA-N 0.000 title claims abstract description 57
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 18
- 239000006227 byproduct Substances 0.000 title claims abstract description 15
- 150000001875 compounds Chemical class 0.000 claims abstract description 52
- 239000000047 product Substances 0.000 claims abstract description 46
- 241000736199 Paeonia Species 0.000 claims abstract description 26
- 235000006484 Paeonia officinalis Nutrition 0.000 claims abstract description 26
- 238000002425 crystallisation Methods 0.000 claims abstract description 20
- 230000008025 crystallization Effects 0.000 claims abstract description 20
- 238000000034 method Methods 0.000 claims abstract description 13
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 claims description 51
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 42
- 239000013522 chelant Substances 0.000 claims description 28
- 238000001816 cooling Methods 0.000 claims description 27
- 229910052700 potassium Inorganic materials 0.000 claims description 27
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 claims description 26
- 239000011591 potassium Substances 0.000 claims description 26
- KCXVZYZYPLLWCC-UHFFFAOYSA-N EDTA Chemical compound OC(=O)CN(CC(O)=O)CCN(CC(O)=O)CC(O)=O KCXVZYZYPLLWCC-UHFFFAOYSA-N 0.000 claims description 25
- 229910000147 aluminium phosphate Inorganic materials 0.000 claims description 25
- 150000002500 ions Chemical class 0.000 claims description 25
- 238000003756 stirring Methods 0.000 claims description 25
- 239000002002 slurry Substances 0.000 claims description 24
- 229910052698 phosphorus Inorganic materials 0.000 claims description 23
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 claims description 22
- 229910052757 nitrogen Inorganic materials 0.000 claims description 22
- 239000011574 phosphorus Substances 0.000 claims description 22
- 238000006243 chemical reaction Methods 0.000 claims description 21
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 claims description 15
- 239000004202 carbamide Substances 0.000 claims description 15
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims description 14
- 239000011573 trace mineral Substances 0.000 claims description 13
- 235000013619 trace mineral Nutrition 0.000 claims description 13
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 12
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 claims description 9
- 239000000706 filtrate Substances 0.000 claims description 9
- 241000196324 Embryophyta Species 0.000 claims description 8
- WCUXLLCKKVVCTQ-UHFFFAOYSA-M Potassium chloride Chemical compound [Cl-].[K+] WCUXLLCKKVVCTQ-UHFFFAOYSA-M 0.000 claims description 6
- 125000004432 carbon atom Chemical group C* 0.000 claims description 6
- 229910052742 iron Inorganic materials 0.000 claims description 6
- 125000004430 oxygen atom Chemical group O* 0.000 claims description 6
- 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 claims description 5
- BHPQYMZQTOCNFJ-UHFFFAOYSA-N Calcium cation Chemical compound [Ca+2] BHPQYMZQTOCNFJ-UHFFFAOYSA-N 0.000 claims description 5
- JLVVSXFLKOJNIY-UHFFFAOYSA-N Magnesium ion Chemical compound [Mg+2] JLVVSXFLKOJNIY-UHFFFAOYSA-N 0.000 claims description 5
- BUGBHKTXTAQXES-UHFFFAOYSA-N Selenium Chemical compound [Se] BUGBHKTXTAQXES-UHFFFAOYSA-N 0.000 claims description 5
- PTFCDOFLOPIGGS-UHFFFAOYSA-N Zinc dication Chemical compound [Zn+2] PTFCDOFLOPIGGS-UHFFFAOYSA-N 0.000 claims description 5
- 229910021538 borax Inorganic materials 0.000 claims description 5
- 229910001424 calcium ion Inorganic materials 0.000 claims description 5
- 239000012065 filter cake Substances 0.000 claims description 5
- 238000010438 heat treatment Methods 0.000 claims description 5
- 239000004021 humic acid Substances 0.000 claims description 5
- 229910001425 magnesium ion Inorganic materials 0.000 claims description 5
- 239000000203 mixture Substances 0.000 claims description 5
- 229910052711 selenium Inorganic materials 0.000 claims description 5
- 239000011669 selenium Substances 0.000 claims description 5
- 239000004328 sodium tetraborate Substances 0.000 claims description 5
- 235000010339 sodium tetraborate Nutrition 0.000 claims description 5
- 229910052799 carbon Inorganic materials 0.000 claims description 4
- OTYBMLCTZGSZBG-UHFFFAOYSA-L potassium sulfate Chemical compound [K+].[K+].[O-]S([O-])(=O)=O OTYBMLCTZGSZBG-UHFFFAOYSA-L 0.000 claims description 4
- 229910052939 potassium sulfate Inorganic materials 0.000 claims description 4
- 235000011151 potassium sulphates Nutrition 0.000 claims description 4
- 239000001103 potassium chloride Substances 0.000 claims description 3
- 235000011164 potassium chloride Nutrition 0.000 claims description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 3
- 229910021529 ammonia Inorganic materials 0.000 claims description 2
- 235000011118 potassium hydroxide Nutrition 0.000 claims description 2
- WZLMXYBCAZZIRQ-UHFFFAOYSA-N [N].[P].[K] Chemical compound [N].[P].[K] WZLMXYBCAZZIRQ-UHFFFAOYSA-N 0.000 claims 1
- 238000002360 preparation method Methods 0.000 abstract description 16
- 235000015097 nutrients Nutrition 0.000 abstract description 9
- 239000002699 waste material Substances 0.000 abstract description 7
- 239000007788 liquid Substances 0.000 abstract description 6
- 239000002689 soil Substances 0.000 abstract description 5
- 239000000126 substance Substances 0.000 abstract description 5
- 238000005516 engineering process Methods 0.000 abstract description 4
- 238000004458 analytical method Methods 0.000 abstract description 3
- 238000005056 compaction Methods 0.000 abstract description 2
- 230000000295 complement effect Effects 0.000 abstract description 2
- 230000007613 environmental effect Effects 0.000 abstract description 2
- 235000006180 nutrition needs Nutrition 0.000 abstract description 2
- 235000021048 nutrient requirements Nutrition 0.000 abstract 1
- 239000000243 solution Substances 0.000 description 21
- 239000000843 powder Substances 0.000 description 13
- DZHMRSPXDUUJER-UHFFFAOYSA-N [amino(hydroxy)methylidene]azanium;dihydrogen phosphate Chemical compound NC(N)=O.OP(O)(O)=O DZHMRSPXDUUJER-UHFFFAOYSA-N 0.000 description 11
- 150000003839 salts Chemical class 0.000 description 9
- 230000000694 effects Effects 0.000 description 7
- 235000016709 nutrition Nutrition 0.000 description 6
- 238000010521 absorption reaction Methods 0.000 description 5
- 238000001035 drying Methods 0.000 description 5
- 210000003608 fece Anatomy 0.000 description 4
- 239000010871 livestock manure Substances 0.000 description 4
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- VYQNWZOUAUKGHI-UHFFFAOYSA-N monobenzone Chemical compound C1=CC(O)=CC=C1OCC1=CC=CC=C1 VYQNWZOUAUKGHI-UHFFFAOYSA-N 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 2
- 235000000832 Ayote Nutrition 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 235000009854 Cucurbita moschata Nutrition 0.000 description 2
- 240000001980 Cucurbita pepo Species 0.000 description 2
- 235000009804 Cucurbita pepo subsp pepo Nutrition 0.000 description 2
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 2
- 235000009811 Momordica charantia Nutrition 0.000 description 2
- 235000008331 Pinus X rigitaeda Nutrition 0.000 description 2
- 235000011613 Pinus brutia Nutrition 0.000 description 2
- 241000018646 Pinus brutia Species 0.000 description 2
- 244000078912 Trichosanthes cucumerina Species 0.000 description 2
- 235000008322 Trichosanthes cucumerina Nutrition 0.000 description 2
- 239000008280 blood Substances 0.000 description 2
- 210000004369 blood Anatomy 0.000 description 2
- 125000005521 carbonamide group Chemical group 0.000 description 2
- 239000013078 crystal Substances 0.000 description 2
- 241000411851 herbal medicine Species 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 244000144972 livestock Species 0.000 description 2
- 239000002609 medium Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 244000144977 poultry Species 0.000 description 2
- 235000015136 pumpkin Nutrition 0.000 description 2
- 239000010902 straw Substances 0.000 description 2
- VZGDMQKNWNREIO-UHFFFAOYSA-N tetrachloromethane Chemical compound ClC(Cl)(Cl)Cl VZGDMQKNWNREIO-UHFFFAOYSA-N 0.000 description 2
- PAWQVTBBRAZDMG-UHFFFAOYSA-N 2-(3-bromo-2-fluorophenyl)acetic acid Chemical compound OC(=O)CC1=CC=CC(Br)=C1F PAWQVTBBRAZDMG-UHFFFAOYSA-N 0.000 description 1
- KXGFMDJXCMQABM-UHFFFAOYSA-N 2-methoxy-6-methylphenol Chemical compound [CH]OC1=CC=CC([CH])=C1O KXGFMDJXCMQABM-UHFFFAOYSA-N 0.000 description 1
- ATRRKUHOCOJYRX-UHFFFAOYSA-N Ammonium bicarbonate Chemical compound [NH4+].OC([O-])=O ATRRKUHOCOJYRX-UHFFFAOYSA-N 0.000 description 1
- 241000675108 Citrus tangerina Species 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- 240000000691 Houttuynia cordata Species 0.000 description 1
- 235000013719 Houttuynia cordata Nutrition 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- 241001465754 Metazoa Species 0.000 description 1
- NBIIXXVUZAFLBC-UHFFFAOYSA-L Phosphate ion(2-) Chemical compound OP([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-L 0.000 description 1
- 241000218201 Ranunculaceae Species 0.000 description 1
- 240000001949 Taraxacum officinale Species 0.000 description 1
- 235000005187 Taraxacum officinale ssp. officinale Nutrition 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 239000001099 ammonium carbonate Substances 0.000 description 1
- 235000012501 ammonium carbonate Nutrition 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 150000001793 charged compounds Chemical class 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- NBIIXXVUZAFLBC-UHFFFAOYSA-M dihydrogenphosphate Chemical compound OP(O)([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-M 0.000 description 1
- 238000000855 fermentation Methods 0.000 description 1
- 230000004151 fermentation Effects 0.000 description 1
- 230000004720 fertilization Effects 0.000 description 1
- 239000012847 fine chemical Substances 0.000 description 1
- 238000009472 formulation Methods 0.000 description 1
- 230000000855 fungicidal effect Effects 0.000 description 1
- 239000000417 fungicide Substances 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- -1 hydrogen ions Chemical class 0.000 description 1
- 239000002917 insecticide Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 229910000402 monopotassium phosphate Inorganic materials 0.000 description 1
- 235000019796 monopotassium phosphate Nutrition 0.000 description 1
- 239000000618 nitrogen fertilizer Substances 0.000 description 1
- 235000021049 nutrient content Nutrition 0.000 description 1
- 230000002688 persistence Effects 0.000 description 1
- 239000005011 phenolic resin Substances 0.000 description 1
- 229920001568 phenolic resin Polymers 0.000 description 1
- 229940085991 phosphate ion Drugs 0.000 description 1
- PJNZPQUBCPKICU-UHFFFAOYSA-N phosphoric acid;potassium Chemical compound [K].OP(O)(O)=O PJNZPQUBCPKICU-UHFFFAOYSA-N 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 150000003112 potassium compounds Chemical class 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 238000003900 soil pollution Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- ZJHHPAUQMCHPRB-UHFFFAOYSA-N urea urea Chemical compound NC(N)=O.NC(N)=O ZJHHPAUQMCHPRB-UHFFFAOYSA-N 0.000 description 1
- 230000017260 vegetative to reproductive phase transition of meristem Effects 0.000 description 1
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- Fertilizers (AREA)
Abstract
本发明涉及化工技术领域,尤其是一种制备磷酸铵副产赤芍专用肥的生产方法,通过对赤芍生长过程的营养需求情况进行分析,并结合磷酸铵产品制备工艺中的缺点进行分析与了解,将赤芍专用化合态复合肥制备工艺与磷酸铵产品的制备工艺结合起来,使得两者的工艺进行互补,降低了磷酸铵产品制备工艺中的废液排放量,避免了深度结晶所带来的磷酸铵产品纯度较低的缺点,提高了磷酸铵产品的质量;通过对废液中的营养元素进行调节与搭配,使得制备出来的赤芍专用复合肥能够满足赤芍的营养需求,提高赤芍生长速度,改善赤芍产量和质量,降低了土壤板结率,提高了土地利用率,具有显著的环保价值和经济效益。The present invention relates to the field of chemical technology, in particular to a production method for preparing ammonium phosphate by-product Radix Paeoniae Rubra special fertilizer, by analyzing the nutrient requirements in the growth process of Radix Radix Radix Radix Paeoniae Rubra, combined with the shortcomings in the preparation process of ammonium phosphate products for analysis and analysis. We understand that the combination of the preparation process of red peony special compound fertilizer and the preparation process of ammonium phosphate products makes the two processes complement each other, reduces the waste liquid discharge in the preparation process of ammonium phosphate products, and avoids the deep crystallization. The shortcomings of the low purity of the ammonium phosphate products from the past have improved the quality of the ammonium phosphate products; by adjusting and matching the nutrient elements in the waste liquid, the prepared special compound fertilizer for red peony can meet the nutritional needs of red peony and improve the quality of the ammonium phosphate product. The growth rate of Radix Paeoniae Rubra improves the yield and quality of Radix Paeoniae Rubra, reduces the soil compaction rate, improves the land utilization rate, and has significant environmental protection value and economic benefits.
Description
技术领域technical field
本发明涉及化工技术领域,尤其是一种制备磷酸铵副产赤芍专用肥的生产方法。The invention relates to the technical field of chemical industry, in particular to a production method for preparing ammonium phosphate by-product red peony special fertilizer.
背景技术Background technique
赤芍,别名木赤芍、赤芍药、红赤芍、草赤芍,为毛茛科植物,多年生草本植物,具有清热凉血、散瘀止痛之功效。人们在栽培赤芍时,一般都是采用复合肥、尿素为主要肥料,效果较佳;但肥料中的营养成分却难以满足赤芍的需求,又因为大多数种植户对赤芍的生长规律和营养需求了解较少,并且所施肥料缺少一定的营养成分,根据木桶短板理论,在缺少某种营养元素时,也将会影响其他营养元素的吸收,进而造成赤芍的产量低,叶片枯萎、脱落、开花少、结果少,根部不发达,生长慢等问题;为此,有研究者对赤芍专用肥进行了研究,如专利号为201010156942.0的《一种赤芍中草药营养肥》提供了一种采用磷酸二氢钾、硫酸钾、杀虫剂、酚醛树脂、畜牧家禽粪便以及南瓜粉、苦瓜粉、松针粉等等多种中草药植物粉以及秸秆粉为原料,通过发酵打成块状营养肥,由此可见,现有技术中对于赤芍专用肥的制备还较为稀少,并且有的技术方案均是采用传统的化肥或者农家肥进行配合而成,而根据作物对氮磷钾肥的吸收情况来看,作物对氮肥的吸收率为20-46%、磷肥10-25%、钾肥是46-60%左右,这样就会导致大量的氮磷钾肥残留在土壤中,造成土壤的污染,因此,对于赤芍的栽培用肥急需要改进这种缺陷,使得赤芍专用肥能够满足赤芍需肥要求时,降低残留于土壤中的氮磷钾元素,提高赤芍专用复合肥的利用率。Radix Paeoniae Rubra, also known as Muchishao, Chishaoyao, Red Chishao, Cao Chishao, is a plant of Ranunculaceae, a perennial herb, which has the effects of clearing heat and cooling blood, dissipating blood stasis and relieving pain. When people cultivate Radix Paeoniae Rubra, they usually use compound fertilizer and urea as the main fertilizers, and the effect is better; but the nutrients in the fertilizers are difficult to meet the needs of Radix Paeoniae Rubra, and because most growers are concerned about the growth law of Radix Paeoniae Rubra and the There is little understanding of nutritional requirements, and the fertilizers applied lack certain nutrients. According to the theory of short boards of wooden barrels, when a certain nutrient element is lacking, it will also affect the absorption of other nutrient elements, resulting in low yield of Radix Paeoniae Rubra and leaves. Withering, falling off, less flowering, few results, underdeveloped roots, slow growth and other problems; for this reason, some researchers have studied the special fertilizer for red peony root, such as "A Kind of Red Peony Chinese Herbal Nutritional Fertilizer" with the patent number 201010156942.0. A kind of raw material is potassium dihydrogen phosphate, potassium sulfate, insecticide, phenolic resin, livestock and poultry manure, pumpkin powder, bitter gourd powder, pine needle powder and other Chinese herbal medicine plant powder and straw powder, which are made into lumps through fermentation. Nutritional fertilizer, it can be seen that the preparation of special fertilizer for red peony root is relatively rare in the prior art, and some technical solutions are all formed by using traditional chemical fertilizers or farmyard manure, and according to the absorption of nitrogen, phosphorus and potassium fertilizers by crops From the perspective of the situation, the absorption rate of nitrogen fertilizer by crops is 20-46%, phosphorus fertilizer is 10-25%, and potassium fertilizer is about 46-60%. This will cause a large amount of nitrogen, phosphorus and potassium fertilizers to remain in the soil, causing soil pollution. Therefore, For the cultivation of Radix Paeoniae Rubra, it is urgent to improve this defect, so that the special fertilizer for Radix Paeoniae Rubra can meet the fertilizer requirements of Radix Paeoniae Rubra, reduce the nitrogen, phosphorus and potassium elements remaining in the soil, and improve the utilization rate of the compound fertilizer for Radix Paeoniae Rubra.
同时,磷酸铵产品的制备工艺中,通常是采用湿法磷酸和热法磷酸中的一种,进行磷酸铵产品的制备的,这种工艺将会给磷酸铵产品的纯度造成影响,使得磷酸铵产品的纯度较低,为此需要对磷酸铵另外设计提纯工艺来进行磷酸铵产品的提纯,进而增大了磷酸铵产品的制备成本,于是,有人通过采用磷酸与尿素在低于80摄氏度下反应生成磷酸脲这种中间体,并再采用中间体作为原料与氨气反应,生成磷酸铵产品的,该工艺需要对磷酸铵产品进行降温循环结晶处理,但往往需要对磷酸铵产品进行深度结晶,才能够避免废液中大量的氮磷营养元素被排放到环境中,进而才能够避免资源的浪费,降低磷酸铵产品的生产成本,但是,由于深度结晶过程将会造成其他产品也被结晶而出,进而影响了磷酸铵产品的纯度。At the same time, in the preparation process of ammonium phosphate products, one of wet-process phosphoric acid and hot-process phosphoric acid is usually used to prepare ammonium phosphate products. This process will affect the purity of ammonium phosphate products, making ammonium phosphate The purity of the product is low. Therefore, it is necessary to design an additional purification process for ammonium phosphate to purify the ammonium phosphate product, thereby increasing the preparation cost of the ammonium phosphate product. Therefore, some people react by using phosphoric acid and urea at a temperature lower than 80 degrees Celsius. To produce an intermediate such as urea phosphate, and then use the intermediate as a raw material to react with ammonia gas to produce ammonium phosphate products. This process requires cooling and cyclic crystallization of ammonium phosphate products, but often requires deep crystallization of ammonium phosphate products. Only in this way can a large amount of nitrogen and phosphorus nutrients in the waste liquid be discharged into the environment, thereby avoiding the waste of resources and reducing the production cost of ammonium phosphate products. However, due to the deep crystallization process, other products will also be crystallized out. , thereby affecting the purity of the ammonium phosphate product.
为此,本研究者通过长期的努力研究与探索,将赤芍专用复合肥的制备工艺与磷酸铵的制备工艺结合起来,通过两者的优缺点进行互补,为磷酸铵产品的制备工艺和赤芍专用复合肥的制备工艺提供了一种新思路。For this reason, through long-term hard research and exploration, the researcher combined the preparation process of red peony special compound fertilizer with the preparation process of ammonium phosphate, and complemented each other through the advantages and disadvantages of the two, and provided the preparation process for ammonium phosphate products and red peony. The preparation process of special compound fertilizer for peony provides a new idea.
发明内容Contents of the invention
为了解决现有技术中存在的上述技术问题,本发明提供一种制备磷酸铵副产赤芍专用肥的生产方法,具有工艺简单,能够降低磷酸铵产品制备工艺中的废液排放量,提高磷酸铵产品的纯度,满足赤芍快速生长要求,提高赤芍品质等特征。In order to solve the above-mentioned technical problems in the prior art, the present invention provides a production method for preparing ammonium phosphate by-product Radix Paeoniae Rubra special fertilizer, which has the advantages of simple process, can reduce the discharge of waste liquid in the preparation process of ammonium phosphate products, and increase the production of phosphoric acid. The purity of the ammonium product meets the requirements of the rapid growth of Radix Paeoniae Rubra and improves the quality of Radix Radix Radix Paeoniae Alba.
具体是通过以下技术方案得以实现的:Specifically, it is achieved through the following technical solutions:
一种制备磷酸铵副产赤芍专用肥的生产方法,采用磷酸与尿素按照摩尔比为(1.5-1.8):1混合,在温度为90-110℃,搅拌反应1-2.5h,获得中间体料浆;再向中间体料浆中通入氨气,并控制反应温度为60-90℃,搅拌反应20-30min后,控制终点PH值为9.8-11.4,获得磷酸铵料浆;再将磷酸铵料浆置于循环降温结晶器中进行循环降温结晶处理,并对溶液中的氮磷元素进行检测分析和调整,使得溶液中氮磷元素成分的摩尔比为1.1:(1.1-1.7)后,停止结晶并过滤处理,滤饼为磷酸铵产品,向滤液中加入钾成分和中微量元素化合物,并调整溶液中氮磷钾元素成分的摩尔比为1.1:(1.1-1.7):(1.3-1.5)后,获得化合态复合肥初成品;再将化合态复合肥初成品置于烘干器中,采用升温速度为10℃/min升温至温度为60-70℃,干燥1.5-2.5h后,调整水分含量为1.5-2.5%,即可制得赤芍专用化合态复合肥。A production method for preparing ammonium phosphate by-product red peony root special fertilizer, using phosphoric acid and urea to mix according to the molar ratio of (1.5-1.8): 1, stirring and reacting for 1-2.5 hours at a temperature of 90-110°C to obtain an intermediate Slurry; then feed ammonia gas into the intermediate slurry, and control the reaction temperature to 60-90°C, stir and react for 20-30 minutes, and control the end point pH value to 9.8-11.4 to obtain ammonium phosphate slurry; then add phosphoric acid The ammonium slurry is placed in a circulating cooling crystallizer for circulating cooling crystallization treatment, and the nitrogen and phosphorus elements in the solution are detected, analyzed and adjusted so that the molar ratio of the nitrogen and phosphorus elements in the solution is 1.1: (1.1-1.7), Stop crystallization and filter treatment, the filter cake is an ammonium phosphate product, add potassium components and medium and trace element compounds to the filtrate, and adjust the mol ratio of the nitrogen, phosphorus and potassium element components in the solution to be 1.1: (1.1-1.7): (1.3-1.5 ), the primary product of compound fertilizer is obtained; then the primary product of compound fertilizer is placed in a dryer, and the temperature is raised to 60-70°C at a heating rate of 10°C/min, and after drying for 1.5-2.5h, By adjusting the water content to 1.5-2.5%, the compound fertilizer special for red peony root can be prepared.
所述的磷酸与尿素反应制备中间体料浆时,搅拌速度为180-200r/min。When the phosphoric acid and urea react to prepare the intermediate slurry, the stirring speed is 180-200r/min.
所述的通入氨气后进行搅拌反应20-30min时的搅拌速度为400-500r/min。The stirring speed is 400-500 r/min when the stirring reaction is carried out for 20-30 minutes after the ammonia gas is introduced.
所述的循环降温结晶器中进行循环降温结晶处理是将温度采用降温速度为5℃/min降温至≤30℃。The circulating cooling crystallization treatment in the circulating cooling crystallizer is to lower the temperature to ≤30 °C at a cooling rate of 5 °C/min.
所述的钾成分为氢氧化钾、硫酸钾、氯化钾中的一种。The potassium component is one of potassium hydroxide, potassium sulfate and potassium chloride.
所述的钾成分的浓度为30%。The concentration of the potassium component is 30%.
所述的中微量元素化合物为钙离子EDTA螯合物、铁离子EDTA螯合物、锌离子EDTA螯合物、硒离子EDTA螯合物、镁离子EDTA螯合物、硼砂、腐殖酸、草木灰的混合物。The middle and trace element compound is calcium ion EDTA chelate, iron ion EDTA chelate, zinc ion EDTA chelate, selenium ion EDTA chelate, magnesium ion EDTA chelate, borax, humic acid, plant ash mixture.
所述的中微量元素化合物的添加量为溶液总重量的16%左右。The added amount of the middle and trace element compound is about 16% of the total weight of the solution.
所述的化合态复合肥,其成分中含有以下氮磷钾化合态结构式:Described compound state compound fertilizer, its composition contains following nitrogen, phosphorus and potassium compound state structural formula:
其中,碳原子与氧原子之间的虚线表示C原子与O原子之间存在配位键。 Wherein, the dotted line between the carbon atom and the oxygen atom indicates that there is a coordination bond between the C atom and the O atom.
再添加钾成分和中微量元素化合物的时候,还可以添加发酵腐熟的畜牧家禽粪便、南瓜粉、苦瓜粉、秸秆粉、松针粉、鱼腥草粉、蒲公英粉、陈皮粉、灭菌灵、沼渣、沼液等有机或者无机物。When adding potassium components and trace element compounds, you can also add fermented and decomposed livestock and poultry manure, pumpkin powder, bitter gourd powder, straw powder, pine needle powder, Houttuynia cordata powder, dandelion powder, tangerine peel powder, fungicide, marsh Slag, biogas slurry and other organic or inorganic substances.
与现有技术相比,本发明的技术方案的技术效果体现在:Compared with the prior art, the technical effect of the technical solution of the present invention is reflected in:
1、通过对赤芍生长过程的营养需求情况进行分析,并结合磷酸铵产品制备工艺中的缺点进行分析与了解,将赤芍专用化合态复合肥制备工艺与磷酸铵产品的制备工艺结合起来,使得两者的工艺进行互补,降低了磷酸铵产品制备工艺中的废液排放量,避免了深度结晶所带来的磷酸铵产品纯度较低的缺点,提高了磷酸铵产品的质量。1. Through the analysis of the nutritional requirements in the growth process of Radix Paeoniae Rubra and the shortcomings in the preparation process of ammonium phosphate products, the preparation process of compound fertilizer for Radix Paeoniae Rubra and the preparation process of ammonium phosphate products are combined, The two processes complement each other, reduce the discharge of waste liquid in the ammonium phosphate product preparation process, avoid the disadvantage of low purity of the ammonium phosphate product caused by deep crystallization, and improve the quality of the ammonium phosphate product.
2、通过对废液中的营养元素进行调节与搭配,使得制备出来的赤芍专用复合肥能够满足赤芍的营养需求,提高赤芍生长速度,改善赤芍产量和质量,同时,避免因为营养元素搭配不当导致过多的残留元素在土壤中,降低了土壤板结率,提高了土地利用率,具有显著的环保价值和经济效益。2. By adjusting and matching the nutrient elements in the waste liquid, the prepared special compound fertilizer for red peony can meet the nutritional needs of red peony, increase the growth rate of red peony, improve the yield and quality of red peony, and at the same time, avoid the Improper matching of elements leads to excessive residual elements in the soil, which reduces the soil compaction rate and improves the land utilization rate, which has significant environmental protection value and economic benefits.
3、通过化合态复合肥生产工艺中技术参数,即就是温度、原料浓度以及配比的控制,使得磷酸与尿素反应后,生成磷酸脲产品,磷酸脲产品本身具有较强的酸性,而磷酸与尿素之间又是通过配位键的方式结合在一起形成的化合态复盐,也是传统技术中作为作物用肥,并且作物对该化合态复盐的吸收率比对尿素、碳酸铵、硝酸铵等一元、二元肥料吸收率均较优的一种化合态复合肥,然而,这种化合态复盐在磷酸存在的环境下,在80-250℃的温度下,会发生复杂的分解聚合反应,使得磷酸脲形成(H2PO4)-和(H2NCONH3)+两个离子,(H2NCONH3)+离子与磷酸接近,并在温度为80-160℃的环境下,形成中间离子和磷酸二氢根,并在C与O之间形成配位键,这种中间离子能够与对中元素化合物螯合形成多元素中间离子,进而能够继续与其他带负电荷的化合物或者离子形成螯合物,提高复盐中元素含量,进而能够调整该离子存在的复盐中的养分含量,同时,该螯合物又能够进行水解而被作物吸收,进而能够有效的长期为作物提供肥效,同时,结合对该离子存在的溶液中元素含量的测定,进而调整复盐形成时的各元素含量,烘干获得含有化合态复盐结构的复合肥,提高了赤芍专用肥的质量。3. Through the control of technical parameters in the production process of compound fertilizers, that is, temperature, raw material concentration and ratio control, after the reaction of phosphoric acid and urea, urea phosphate products are produced. Urea phosphate products themselves have strong acidity, while phosphoric acid and urea Urea is a compounded double salt formed by coordinating bonds, which is also used as a fertilizer for crops in traditional technology, and the absorption rate of the compounded double salt by crops is higher than that of urea, ammonium carbonate, and ammonium nitrate. It is a compound fertilizer with excellent absorption rate of mono- and binary fertilizers. However, in the presence of phosphoric acid, complex decomposition and polymerization reactions will occur at a temperature of 80-250°C. , so that urea phosphate forms (H 2 PO 4 )- and (H 2 NCONH 3 ) + two ions, (H 2 NCONH 3 ) + ions are close to phosphoric acid, and form at a temperature of 80-160°C The intermediate ion and dihydrogen phosphate form a coordination bond between C and O. This intermediate ion can chelate with the middle element compound to form a multi-element intermediate ion, which can then continue to interact with other negatively charged compounds or ions Form a chelate, increase the element content in the double salt, and then adjust the nutrient content in the double salt where the ion exists. At the same time, the chelate can be hydrolyzed and absorbed by the crops, which can effectively provide fertilizer for the crops for a long time At the same time, combined with the determination of the element content in the solution where the ion exists, the content of each element when the double salt is formed is adjusted, and the compound fertilizer containing the compound state double salt structure is obtained by drying, which improves the quality of the special fertilizer for red peony root.
具体实施方式detailed description
下面结合具体的实施方式来对本发明的技术方案做进一步的限定,但要求保护的范围不仅局限于所作的描述。The technical solutions of the present invention will be further limited below in conjunction with specific embodiments, but the scope of protection is not limited to the descriptions made.
原理说明:Principle description:
本发明通过对磷酸与碳酰胺反应的机理进行研究与探讨,并结合现有技术文献了解到,磷酸与碳酰胺反应生成磷酸脲,其分子式为:CO(NH2)2.H3PO4,在较高温度的环境下,磷酸中的H和O之间的化学键会断离,氢离子与尿素结合形成含有正电荷的离子态,使得磷酸脲形成一种正负电荷相吸引的离子复盐,其机理结构反应如下表达式:CO(NH2)2.H3PO4→(H2PO4)-.(H2NCONH3)+ The present invention studies and discusses the mechanism of the reaction between phosphoric acid and carbonamide, and combines the prior art literature to understand that phosphoric acid and carbonamide react to form urea phosphate, and its molecular formula is: CO(NH 2 ) 2 .H 3 PO 4 , In a higher temperature environment, the chemical bond between H and O in phosphoric acid will be broken, and hydrogen ions will combine with urea to form an ion state with a positive charge, making urea phosphate form an ion double salt that attracts positive and negative charges. , and its mechanism structure reaction is as follows: CO(NH 2 ) 2 .H 3 PO 4 →(H 2 PO 4 )-.(H 2 NCONH 3 ) +
进一步的,磷酸脲离子复盐在磷酸存在的环境下,其中的(H2NCONH3)+正离子与磷酸接近,形成C→O配位键的中间离子,即为(CO5PN2H8)+,进而使得磷酸脲中间体中含有大量的(H2PO4)-和(CO5PN2H8)+离子,在加入过量并且适量的铵根离子时,磷酸二氢根与铵根离子形成磷酸铵晶体被析出来,并通过检测分析滤液中的氮磷元素的含量,并按照赤芍的需求添加钾元素、镁元素、铁元素以及其他中微量元素,调整滤液中的营养结构,使得营养结构层满足赤芍的需求,再烘干即可制得含有N、P、K以及其他元素的赤芍专用化合态复合肥。Furthermore, in the presence of phosphoric acid in the presence of phosphoric acid, the (H 2 NCONH 3 ) + positive ion in the double salt of urea phosphate ion is close to phosphoric acid to form the intermediate ion of the C→O coordination bond, which is (CO 5 PN 2 H 8 ) + , so that the urea phosphate intermediate contains a large amount of (H 2 PO 4 )- and (CO 5 PN 2 H 8 ) + ions. Ions form ammonium phosphate crystals and are separated out, and the content of nitrogen and phosphorus elements in the filtrate is detected and analyzed, and potassium, magnesium, iron and other medium and trace elements are added according to the needs of red peony root to adjust the nutritional structure in the filtrate. Make the nutrient structure layer meet the requirement of Radix Paeoniae Rubra, and then dry to prepare the special chemical compound fertilizer for Radix Paeoniae Rubra containing N, P, K and other elements.
其具体的反应原理将通过以下反应结构式以及反应机理来进一步的说明:Its specific reaction principle will be further explained by the following reaction structural formula and reaction mechanism:
反应式一:Reaction formula one:
CO(NH2)2+H3PO4→CO(NH2)2.H3PO4 CO(NH 2 ) 2 +H 3 PO 4 →CO(NH 2 ) 2.H 3 PO 4
反应式二:Reaction two:
反应式三:Reaction three:
其中,碳原子与氧原子之间的虚线表示C原子与O原子之间存在配位键。Wherein, the dotted line between the carbon atom and the oxygen atom indicates that there is a coordination bond between the C atom and the O atom.
反应式四:Reaction four:
待结晶磷酸铵产品出来之后,再向滤液中添加钾元素、以及其他元素,则会与残留在滤液中的磷酸二氢根、磷酸氢根以及的中间离子进行反应,生成复盐形式的化合态赤芍专用复合肥。After the crystalline ammonium phosphate product comes out, potassium and other elements are added to the filtrate, which will react with the dihydrogen phosphate, hydrogen phosphate and other elements remaining in the filtrate. The intermediate ion is reacted to generate compound fertilizer special for red peony root in the form of double salt.
名词说明:Noun description:
磷酸脲(Ureaphosphate,UP),CAS号为4861-19-2,分子式为CH7N2O5P,可表示为CO(NH2)2·H3PO4:Ureaphosphate (UP), CAS No. 4861-19-2, molecular formula CH 7 N 2 O 5 P, can be expressed as CO(NH 2 ) 2 ·H 3 PO 4 :
是一种广泛应用于畜牧业、工业、农业等领域的精细化工产品,其固体为白色结晶或结晶性粉末,易溶于水和醇,不溶于醚类、甲苯及四氯化碳,水溶液呈酸性,熔融时开始分解放出二氧化碳和氨气。It is a fine chemical product widely used in animal husbandry, industry, agriculture and other fields. Its solid is white crystal or crystalline powder, soluble in water and alcohol, insoluble in ether, toluene and carbon tetrachloride, and its aqueous solution is It is acidic and starts to decompose when melting to release carbon dioxide and ammonia.
实施例:下面以具体的操作实施例来对本发明进行进一步阐述。Embodiment: The present invention will be further elaborated below with specific operation examples.
实施例1Example 1
一种制备磷酸铵副产赤芍专用肥的生产方法,采用磷酸与尿素按照摩尔比为1.5:1混合,在温度为90℃,搅拌反应1h,获得中间体料浆;再向中间体料浆中通入氨气,并控制反应温度为60℃,搅拌反应20min后,控制终点PH值为9.8,获得磷酸铵料浆;再将磷酸铵料浆置于循环降温结晶器中进行循环降温结晶处理,并对溶液中的氮磷元素进行检测分析和调整,使得溶液中氮磷元素成分的摩尔比为1.1:1.1后,停止结晶并过滤处理,滤饼为磷酸铵产品,向滤液中加入钾成分和中微量元素化合物,并调整溶液中氮磷钾元素成分的摩尔比为1.1:1.1:1.3后,获得化合态复合肥初成品;再将化合态复合肥初成品置于烘干器中,采用升温速度为10℃/min升温至温度为60℃,干燥1.5h后,调整水分含量为1.5%,即可制得赤芍专用化合态复合肥。A production method for preparing ammonium phosphate by-product Radix Paeoniae Rubra, which uses phosphoric acid and urea to mix at a molar ratio of 1.5:1, and stirs and reacts for 1 hour at a temperature of 90°C to obtain an intermediate slurry; Ammonia gas was passed into the medium, and the reaction temperature was controlled at 60°C. After stirring for 20 minutes, the pH value of the end point was controlled to be 9.8 to obtain ammonium phosphate slurry; then the ammonium phosphate slurry was placed in a circulating cooling crystallizer for circulating cooling crystallization treatment , and the nitrogen and phosphorus elements in the solution are detected, analyzed and adjusted so that the molar ratio of the nitrogen and phosphorus elements in the solution is 1.1:1.1, stop crystallization and filter, the filter cake is an ammonium phosphate product, and potassium components are added to the filtrate and medium and trace element compounds, and adjust the molar ratio of nitrogen, phosphorus, and potassium elements in the solution to 1.1:1.1:1.3 to obtain the first product of compound fertilizer; then place the first product of compound fertilizer in a dryer, and use The heating rate is 10°C/min, and the temperature is raised to 60°C. After drying for 1.5 hours, the moisture content is adjusted to 1.5%, and the special compound fertilizer for Radix Paeoniae Rubra can be obtained.
所述的磷酸与尿素反应制备中间体料浆时,搅拌速度为180r/min。When the phosphoric acid and urea react to prepare the intermediate slurry, the stirring speed is 180r/min.
所述的通入氨气后进行搅拌反应20min时的搅拌速度为400r/min。The stirring speed is 400 r/min when the stirring reaction is carried out for 20 minutes after the ammonia gas is introduced.
所述的循环降温结晶器中进行循环降温结晶处理是将温度采用降温速度为5℃/min降温至30℃。The circulating cooling crystallization process in the circulating cooling crystallizer is to lower the temperature to 30 °C at a cooling rate of 5 °C/min.
所述的钾成分为氢氧化钾。The potassium component is potassium hydroxide.
所述的钾成分的浓度为30%。The concentration of the potassium component is 30%.
所述的中微量元素化合物为0.6%钙离子EDTA螯合物、0.03%铁离子EDTA螯合物、0.05%锌离子EDTA螯合物、0.02%硒离子EDTA螯合物、0.04%镁离子EDTA螯合物、0.02%硼砂、4.3%腐殖酸、6.5%草木灰的混合物。The described trace element compound is 0.6% calcium ion EDTA chelate, 0.03% iron ion EDTA chelate, 0.05% zinc ion EDTA chelate, 0.02% selenium ion EDTA chelate, 0.04% magnesium ion EDTA chelate compound, 0.02% borax, 4.3% humic acid, 6.5% plant ash.
实施例2Example 2
一种制备磷酸铵副产赤芍专用肥的生产方法,采用磷酸与尿素按照摩尔比为1.8:1混合,在温度为110℃,搅拌反应2.5h,获得中间体料浆;再向中间体料浆中通入氨气,并控制反应温度为90℃,搅拌反应30min后,控制终点PH值为11.4,获得磷酸铵料浆;再将磷酸铵料浆置于循环降温结晶器中进行循环降温结晶处理,并对溶液中的氮磷元素进行检测分析和调整,使得溶液中氮磷元素成分的摩尔比为1.1:1.7后,停止结晶并过滤处理,滤饼为磷酸铵产品,向滤液中加入钾成分和中微量元素化合物,并调整溶液中氮磷钾元素成分的摩尔比为1.1:1.7:1.5后,获得化合态复合肥初成品;再将化合态复合肥初成品置于烘干器中,采用升温速度为10℃/min升温至温度为70℃,干燥2.5h后,调整水分含量为2.5%,即可制得赤芍专用化合态复合肥。A production method for preparing ammonium phosphate by-product Radix Paeoniae Rubra special fertilizer, using phosphoric acid and urea to mix according to the molar ratio of 1.8:1, stirring and reacting at a temperature of 110°C for 2.5 hours to obtain an intermediate slurry; Ammonia gas is introduced into the slurry, and the reaction temperature is controlled at 90°C. After stirring for 30 minutes, the pH value at the end point is controlled to be 11.4 to obtain ammonium phosphate slurry; then the ammonium phosphate slurry is placed in a circulating cooling crystallizer for circulating cooling crystallization treatment, and detect, analyze and adjust the nitrogen and phosphorus elements in the solution so that the molar ratio of the nitrogen and phosphorus elements in the solution is 1.1:1.7, then stop the crystallization and filter the treatment, the filter cake is an ammonium phosphate product, and add potassium to the filtrate Components and trace element compounds, and adjust the molar ratio of nitrogen, phosphorus and potassium elements in the solution to 1.1:1.7:1.5 to obtain the primary product of compound fertilizer; then place the primary product of compound fertilizer in the dryer, The temperature is raised to 70° C. at a heating rate of 10° C./min, and after drying for 2.5 hours, the moisture content is adjusted to 2.5 percent to obtain a special compound fertilizer for red peony root.
所述的磷酸与尿素反应制备中间体料浆时,搅拌速度为200r/min。When the phosphoric acid and urea react to prepare the intermediate slurry, the stirring speed is 200r/min.
所述的通入氨气后进行搅拌反应30min时的搅拌速度为500r/min。The stirring speed is 500 r/min when the stirring reaction is carried out for 30 minutes after the ammonia gas is introduced.
所述的循环降温结晶器中进行循环降温结晶处理是将温度采用降温速度为5℃/min降温至20℃。The circulating cooling crystallization treatment in the circulating cooling crystallizer is to lower the temperature to 20 °C at a cooling rate of 5 °C/min.
所述的钾成分为硫酸钾。The potassium component is potassium sulfate.
所述的钾成分的浓度为30%。The concentration of the potassium component is 30%.
所述的中微量元素化合物为0.2%钙离子EDTA螯合物、0.05%铁离子EDTA螯合物、0.03%锌离子EDTA螯合物、0.04%硒离子EDTA螯合物、0.01%镁离子EDTA螯合物、0.05%硼砂、3.7%腐殖酸、5.4%草木灰的混合物。The medium and trace element compound is 0.2% calcium ion EDTA chelate, 0.05% iron ion EDTA chelate, 0.03% zinc ion EDTA chelate, 0.04% selenium ion EDTA chelate, 0.01% magnesium ion EDTA chelate compound, 0.05% borax, 3.7% humic acid, 5.4% plant ash.
实施例3Example 3
一种制备磷酸铵副产赤芍专用肥的生产方法,采用磷酸与尿素按照摩尔比为1.65:1混合,在温度为100℃,搅拌反应2h,获得中间体料浆;再向中间体料浆中通入氨气,并控制反应温度为75℃,搅拌反应25min后,控制终点PH值为10.3,获得磷酸铵料浆;再将磷酸铵料浆置于循环降温结晶器中进行循环降温结晶处理,并对溶液中的氮磷元素进行检测分析和调整,使得溶液中氮磷元素成分的摩尔比为1.1:1.4后,停止结晶并过滤处理,滤饼为磷酸铵产品,向滤液中加入钾成分和中微量元素化合物,并调整溶液中氮磷钾元素成分的摩尔比为1.1:1.4:1.4后,获得化合态复合肥初成品;再将化合态复合肥初成品置于烘干器中,采用升温速度为10℃/min升温至温度为65℃,干燥2h后,调整水分含量为2%,即可制得赤芍专用化合态复合肥。A production method for preparing ammonium phosphate by-product red peony root special fertilizer, using phosphoric acid and urea to mix according to the molar ratio of 1.65:1, stirring and reacting for 2 hours at a temperature of 100°C to obtain an intermediate slurry; Ammonia gas was passed into the medium, and the reaction temperature was controlled at 75°C. After stirring for 25 minutes, the pH value of the end point was controlled to be 10.3 to obtain ammonium phosphate slurry; then the ammonium phosphate slurry was placed in a circulating cooling crystallizer for circulating cooling crystallization treatment , and detect, analyze and adjust the nitrogen and phosphorus elements in the solution, so that the molar ratio of the nitrogen and phosphorus elements in the solution is 1.1:1.4, stop the crystallization and filter, the filter cake is ammonium phosphate product, and add potassium to the filtrate and medium and trace element compounds, and adjust the molar ratio of nitrogen, phosphorus and potassium elements in the solution to 1.1:1.4:1.4 to obtain the first product of compound fertilizer; then place the first product of compound fertilizer in a dryer and use The heating rate is 10°C/min, and the temperature is raised to 65°C. After drying for 2 hours, the moisture content is adjusted to 2%, and the special compound fertilizer for red peony root can be prepared.
所述的磷酸与尿素反应制备中间体料浆时,搅拌速度为190r/min。When the phosphoric acid and urea react to prepare the intermediate slurry, the stirring speed is 190r/min.
所述的通入氨气后进行搅拌反应25min时的搅拌速度为450r/min。The stirring speed is 450 r/min when the stirring reaction is carried out for 25 minutes after the introduction of ammonia gas.
所述的循环降温结晶器中进行循环降温结晶处理是将温度采用降温速度为5℃/min降温至25℃。The circulating cooling crystallization treatment in the circulating cooling crystallizer is to lower the temperature to 25 °C at a cooling rate of 5 °C/min.
所述的钾成分为氯化钾。The potassium component is potassium chloride.
所述的钾成分的浓度为30%。The concentration of the potassium component is 30%.
所述的中微量元素化合物为0.3%钙离子EDTA螯合物、0.02%铁离子EDTA螯合物、0.02%锌离子EDTA螯合物、0.03%硒离子EDTA螯合物、0.06%镁离子EDTA螯合物、0.05%硼砂、2.6%腐殖酸、7.8%草木灰的混合物。The described trace element compound is 0.3% calcium ion EDTA chelate, 0.02% iron ion EDTA chelate, 0.02% zinc ion EDTA chelate, 0.03% selenium ion EDTA chelate, 0.06% magnesium ion EDTA chelate compound, 0.05% borax, 2.6% humic acid, 7.8% plant ash.
试验例:下面结合具体的实施例内容来对本发明的技术方案的技术效果以及产品特性做进一步的说明。Experimental example: the technical effect and product characteristics of the technical solution of the present invention will be further described in conjunction with specific examples below.
试验例本发明的赤芍专用化合态复合肥对赤芍生长态势的影响Test example The effect of the special compound fertilizer of Radix Paeoniae Rubra of the present invention on the growth situation of Radix Paeoniae Rubra
实验组:采用实施例1、实施例2、实施例3制得的赤芍专用复合肥按照传统赤芍种植技术进行赤芍种植,每亩添加本发明的复合肥160kg。Experimental group: the Paeoniae Rubra special compound fertilizer that adopts embodiment 1, embodiment 2, embodiment 3 to make is carried out Radix Paeoniae Rubra according to traditional planting technology of Radix Paeoniae Rubra, and adds 160kg of compound fertilizers of the present invention per mu.
对照组:采用专利号为201010156942.0的《一种赤芍中草药营养肥》按照传统赤芍种植技术进行赤芍种植,每亩添加营养肥160kg。Control group: "A Nutrient Fertilizer for Chinese Herbal Medicine of Radix Paeoniae Alba" with patent number 201010156942.0 was used to plant Radix Paeoniae Rubra according to the traditional planting technology of Radix Paeoniae Rubra, and 160 kg of nutritional fertilizer was added per mu.
注:以上实验组和对照组均采用有等量农家肥作为基肥。Note: The same amount of farmyard manure was used as base fertilizer in the above experimental group and control group.
从施肥10天后观察赤芍的生长态势情况,连续观察1个月,并记录如下表1所示:Observe the growth situation of Radix Paeoniae Rubra after 10 days of fertilization, observe continuously for 1 month, and record as shown in Table 1 below:
表1:Table 1:
由表中数据显示可以看出,本发明的赤芍专用肥能够快速提高赤芍的生长速度,肥效持续性较长。It can be seen from the data in the table that the special fertilizer for Radix Paeoniae Rubra of the present invention can rapidly increase the growth rate of Radix Radix Radix Radix Paeoniae Alba, and has a longer fertilizer effect persistence.
在此有必要指出的是,以上实施例和试验例仅限于对本发明的技术方案所能达到的技术效果做进一步的阐释和理解,不限于对本发明的技术方案的进一步限定,本领域技术人员在此基础上作出非突出实质性特征和非显著进步的改进,均属于本发明的保护范畴。It must be pointed out here that the above examples and test examples are limited to further explanation and understanding of the technical effects that the technical solution of the present invention can achieve, and are not limited to further limitations of the technical solution of the present invention. Improvements made on this basis without prominent substantive features and non-significant progress all belong to the protection category of the present invention.
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