CN101497839B - 5-in-1 coal-contacting agent and preparation method thereof - Google Patents
5-in-1 coal-contacting agent and preparation method thereof Download PDFInfo
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- CN101497839B CN101497839B CN2008100574890A CN200810057489A CN101497839B CN 101497839 B CN101497839 B CN 101497839B CN 2008100574890 A CN2008100574890 A CN 2008100574890A CN 200810057489 A CN200810057489 A CN 200810057489A CN 101497839 B CN101497839 B CN 101497839B
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- magnesium
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- 238000002360 preparation method Methods 0.000 title claims abstract description 15
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 57
- 239000011777 magnesium Substances 0.000 claims abstract description 37
- XLOMVQKBTHCTTD-UHFFFAOYSA-N Zinc monoxide Chemical compound [Zn]=O XLOMVQKBTHCTTD-UHFFFAOYSA-N 0.000 claims abstract description 30
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 claims abstract description 20
- 229910052749 magnesium Inorganic materials 0.000 claims abstract description 20
- VKJKEPKFPUWCAS-UHFFFAOYSA-M potassium chlorate Chemical compound [K+].[O-]Cl(=O)=O VKJKEPKFPUWCAS-UHFFFAOYSA-M 0.000 claims abstract description 18
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 claims abstract description 17
- 239000012286 potassium permanganate Substances 0.000 claims abstract description 16
- 239000002994 raw material Substances 0.000 claims abstract description 16
- 239000011701 zinc Substances 0.000 claims abstract description 16
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 claims abstract description 14
- 229910052725 zinc Inorganic materials 0.000 claims abstract description 14
- 239000011787 zinc oxide Substances 0.000 claims abstract description 12
- 239000000920 calcium hydroxide Substances 0.000 claims abstract description 11
- 229910001861 calcium hydroxide Inorganic materials 0.000 claims abstract description 11
- 238000002156 mixing Methods 0.000 claims abstract description 9
- YYRMJZQKEFZXMX-UHFFFAOYSA-N calcium;phosphoric acid Chemical compound [Ca+2].OP(O)(O)=O.OP(O)(O)=O YYRMJZQKEFZXMX-UHFFFAOYSA-N 0.000 claims abstract 3
- 239000002426 superphosphate Substances 0.000 claims abstract 3
- 239000002245 particle Substances 0.000 claims description 12
- 238000010298 pulverizing process Methods 0.000 claims description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 claims description 4
- 235000008733 Citrus aurantifolia Nutrition 0.000 claims 2
- 235000011941 Tilia x europaea Nutrition 0.000 claims 2
- 239000004571 lime Substances 0.000 claims 2
- 239000003245 coal Substances 0.000 abstract description 67
- 238000002485 combustion reaction Methods 0.000 abstract description 56
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 abstract description 51
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 abstract description 33
- NUJOXMJBOLGQSY-UHFFFAOYSA-N manganese dioxide Chemical compound O=[Mn]=O NUJOXMJBOLGQSY-UHFFFAOYSA-N 0.000 abstract description 32
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 abstract description 28
- 229910002091 carbon monoxide Inorganic materials 0.000 abstract description 23
- 229910052815 sulfur oxide Inorganic materials 0.000 abstract description 14
- 239000003054 catalyst Substances 0.000 abstract description 13
- 239000000779 smoke Substances 0.000 abstract description 10
- 239000007800 oxidant agent Substances 0.000 abstract description 9
- 230000001590 oxidative effect Effects 0.000 abstract description 9
- 229910000389 calcium phosphate Inorganic materials 0.000 abstract description 8
- 229930195733 hydrocarbon Natural products 0.000 abstract description 8
- 235000019691 monocalcium phosphate Nutrition 0.000 abstract description 8
- 150000002430 hydrocarbons Chemical class 0.000 abstract description 7
- 238000000227 grinding Methods 0.000 abstract description 6
- XTQHKBHJIVJGKJ-UHFFFAOYSA-N sulfur monoxide Chemical class S=O XTQHKBHJIVJGKJ-UHFFFAOYSA-N 0.000 abstract description 6
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 34
- 239000000446 fuel Substances 0.000 description 30
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 20
- 229910052760 oxygen Inorganic materials 0.000 description 20
- 239000001301 oxygen Substances 0.000 description 20
- 238000006243 chemical reaction Methods 0.000 description 18
- 238000000034 method Methods 0.000 description 18
- 229910052742 iron Inorganic materials 0.000 description 13
- 238000006477 desulfuration reaction Methods 0.000 description 11
- 230000023556 desulfurization Effects 0.000 description 11
- 230000000694 effects Effects 0.000 description 11
- 239000000126 substance Substances 0.000 description 11
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 10
- 229910052799 carbon Inorganic materials 0.000 description 10
- 150000003254 radicals Chemical class 0.000 description 10
- 239000011575 calcium Substances 0.000 description 8
- 239000007789 gas Substances 0.000 description 8
- 239000000203 mixture Substances 0.000 description 8
- 238000007254 oxidation reaction Methods 0.000 description 8
- 229910019440 Mg(OH) Inorganic materials 0.000 description 7
- YYRMJZQKEFZXMX-UHFFFAOYSA-L calcium bis(dihydrogenphosphate) Chemical compound [Ca+2].OP(O)([O-])=O.OP(O)([O-])=O YYRMJZQKEFZXMX-UHFFFAOYSA-L 0.000 description 7
- 230000007613 environmental effect Effects 0.000 description 7
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 6
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 6
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 6
- 230000008901 benefit Effects 0.000 description 6
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 6
- 229910052717 sulfur Inorganic materials 0.000 description 6
- 239000011593 sulfur Substances 0.000 description 6
- JBQYATWDVHIOAR-UHFFFAOYSA-N tellanylidenegermanium Chemical compound [Te]=[Ge] JBQYATWDVHIOAR-UHFFFAOYSA-N 0.000 description 6
- 239000003546 flue gas Substances 0.000 description 5
- 230000003647 oxidation Effects 0.000 description 5
- 230000008569 process Effects 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- UJOBWOGCFQCDNV-UHFFFAOYSA-N 9H-carbazole Chemical compound C1=CC=C2C3=CC=CC=C3NC2=C1 UJOBWOGCFQCDNV-UHFFFAOYSA-N 0.000 description 4
- JUJWROOIHBZHMG-UHFFFAOYSA-N Pyridine Chemical compound C1=CC=NC=C1 JUJWROOIHBZHMG-UHFFFAOYSA-N 0.000 description 4
- SMWDFEZZVXVKRB-UHFFFAOYSA-N Quinoline Chemical compound N1=CC=CC2=CC=CC=C21 SMWDFEZZVXVKRB-UHFFFAOYSA-N 0.000 description 4
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 4
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 4
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 4
- 239000000428 dust Substances 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 4
- 239000001257 hydrogen Substances 0.000 description 4
- 229910052739 hydrogen Inorganic materials 0.000 description 4
- 229910052751 metal Inorganic materials 0.000 description 4
- 239000002184 metal Substances 0.000 description 4
- 230000009467 reduction Effects 0.000 description 4
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 3
- 239000000654 additive Substances 0.000 description 3
- 238000003915 air pollution Methods 0.000 description 3
- 150000002431 hydrogen Chemical class 0.000 description 3
- 239000012535 impurity Substances 0.000 description 3
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 3
- 229910052757 nitrogen Inorganic materials 0.000 description 3
- 238000003756 stirring Methods 0.000 description 3
- 238000012360 testing method Methods 0.000 description 3
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 2
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- 239000004215 Carbon black (E152) Substances 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 2
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 2
- 238000003916 acid precipitation Methods 0.000 description 2
- 230000002378 acidificating effect Effects 0.000 description 2
- 230000004913 activation Effects 0.000 description 2
- 238000004458 analytical method Methods 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 229910052791 calcium Inorganic materials 0.000 description 2
- BRPQOXSCLDDYGP-UHFFFAOYSA-N calcium oxide Chemical compound [O-2].[Ca+2] BRPQOXSCLDDYGP-UHFFFAOYSA-N 0.000 description 2
- 239000000292 calcium oxide Substances 0.000 description 2
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium oxide Inorganic materials [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 2
- 238000004364 calculation method Methods 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 230000005611 electricity Effects 0.000 description 2
- 239000003344 environmental pollutant Substances 0.000 description 2
- 239000002360 explosive Substances 0.000 description 2
- -1 hydrocarbon radicals Chemical class 0.000 description 2
- WPBNNNQJVZRUHP-UHFFFAOYSA-L manganese(2+);methyl n-[[2-(methoxycarbonylcarbamothioylamino)phenyl]carbamothioyl]carbamate;n-[2-(sulfidocarbothioylamino)ethyl]carbamodithioate Chemical compound [Mn+2].[S-]C(=S)NCCNC([S-])=S.COC(=O)NC(=S)NC1=CC=CC=C1NC(=S)NC(=O)OC WPBNNNQJVZRUHP-UHFFFAOYSA-L 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 150000002739 metals Chemical class 0.000 description 2
- 238000012544 monitoring process Methods 0.000 description 2
- 231100000719 pollutant Toxicity 0.000 description 2
- 239000011591 potassium Substances 0.000 description 2
- 229910052700 potassium Inorganic materials 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- UMJSCPRVCHMLSP-UHFFFAOYSA-N pyridine Natural products COC1=CC=CN=C1 UMJSCPRVCHMLSP-UHFFFAOYSA-N 0.000 description 2
- 235000017550 sodium carbonate Nutrition 0.000 description 2
- 229910000029 sodium carbonate Inorganic materials 0.000 description 2
- VWDWKYIASSYTQR-UHFFFAOYSA-N sodium nitrate Chemical compound [Na+].[O-][N+]([O-])=O VWDWKYIASSYTQR-UHFFFAOYSA-N 0.000 description 2
- 239000004071 soot Substances 0.000 description 2
- AKEJUJNQAAGONA-UHFFFAOYSA-N sulfur trioxide Chemical compound O=S(=O)=O AKEJUJNQAAGONA-UHFFFAOYSA-N 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- MGWGWNFMUOTEHG-UHFFFAOYSA-N 4-(3,5-dimethylphenyl)-1,3-thiazol-2-amine Chemical compound CC1=CC(C)=CC(C=2N=C(N)SC=2)=C1 MGWGWNFMUOTEHG-UHFFFAOYSA-N 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 1
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 1
- 239000002250 absorbent Substances 0.000 description 1
- 230000002745 absorbent Effects 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 239000003463 adsorbent Substances 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 208000006673 asthma Diseases 0.000 description 1
- 239000004067 bulking agent Substances 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- 150000001722 carbon compounds Chemical class 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 239000004568 cement Substances 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 231100000481 chemical toxicant Toxicity 0.000 description 1
- 150000001879 copper Chemical class 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 230000003009 desulfurizing effect Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000003487 electrochemical reaction Methods 0.000 description 1
- 230000005518 electrochemistry Effects 0.000 description 1
- 239000003623 enhancer Substances 0.000 description 1
- 230000003628 erosive effect Effects 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 230000005284 excitation Effects 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000002803 fossil fuel Substances 0.000 description 1
- 239000002816 fuel additive Substances 0.000 description 1
- 230000006870 function Effects 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 1
- UCNNJGDEJXIUCC-UHFFFAOYSA-L hydroxy(oxo)iron;iron Chemical compound [Fe].O[Fe]=O.O[Fe]=O UCNNJGDEJXIUCC-UHFFFAOYSA-L 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 239000002973 irritant agent Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 210000004072 lung Anatomy 0.000 description 1
- 229910001507 metal halide Inorganic materials 0.000 description 1
- 150000005309 metal halides Chemical class 0.000 description 1
- 229910017604 nitric acid Inorganic materials 0.000 description 1
- 150000004767 nitrides Chemical class 0.000 description 1
- 229910017464 nitrogen compound Inorganic materials 0.000 description 1
- 150000002830 nitrogen compounds Chemical class 0.000 description 1
- JCXJVPUVTGWSNB-UHFFFAOYSA-N nitrogen dioxide Inorganic materials O=[N]=O JCXJVPUVTGWSNB-UHFFFAOYSA-N 0.000 description 1
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 150000002897 organic nitrogen compounds Chemical class 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 230000008635 plant growth Effects 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 230000009993 protective function Effects 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
- 239000004317 sodium nitrate Substances 0.000 description 1
- 235000010344 sodium nitrate Nutrition 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 230000004936 stimulating effect Effects 0.000 description 1
- 239000011135 tin Substances 0.000 description 1
- 239000003440 toxic substance Substances 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
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- Catalysts (AREA)
Abstract
本发明提供一种5合1触煤剂及其制备方法,该触煤剂包括二氧化锰、氯酸钾、氢氧化钾、锌、氧化锌、氢氧化钙、过磷酸钙、镁;在上述原料中催化剂是二氧化锰,氧化剂是氯酸钾、高锰酸钾、氢氧化钾,固硫剂是锌、氧化锌、氢氧化钙、镁。制备方法是将各组份原料进行粉碎、研磨、混合,得到所述的5合1触煤剂成品。本发明的目的是要解决煤炭燃烧效率低下、燃烧污染严重、燃煤锅炉损耗的问题。本发明使煤炭燃烧效率提高15%-20%;本发明能有效去除煤炭在燃烧过程中产生的硫氧化物(SOx)33.3%,去除氮氧化物(NOx)20%-60%、去除一氧化碳(CO)及碳氢化合物(CxHr)50%-70%,去除烟尘50%-70%,而且能够防止燃煤锅炉的损耗。The present invention provides a 5-in-1 coal catalyzer and a preparation method thereof. The coal catalyzer comprises manganese dioxide, potassium chlorate, potassium hydroxide, zinc, zinc oxide, calcium hydroxide, superphosphate and magnesium; in the above raw materials, the catalyst is manganese dioxide, the oxidant is potassium chlorate, potassium permanganate and potassium hydroxide, and the sulfur-fixing agent is zinc, zinc oxide, calcium hydroxide and magnesium. The preparation method comprises crushing, grinding and mixing the raw materials of each component to obtain the 5-in-1 coal catalyzer finished product. The purpose of the present invention is to solve the problems of low coal combustion efficiency, serious combustion pollution and loss of coal-fired boilers. The present invention improves the coal combustion efficiency by 15%-20%; the present invention can effectively remove 33.3% of sulfur oxides (SOx) generated during the combustion of coal, remove 20%-60% of nitrogen oxides (NOx), remove 50%-70% of carbon monoxide (CO) and hydrocarbons (CxHr), remove 50%-70% of smoke, and can prevent the loss of coal-fired boilers.
Description
技术领域technical field
本发明属于燃煤添加剂领域,特别涉及一种包括催化剂、氧化剂和固硫剂的触煤剂,该触煤剂的制备方法包括以下步骤:粉碎、研磨、混合。The invention belongs to the field of coal-burning additives, and in particular relates to a coal-contacting agent comprising a catalyst, an oxidant and a sulfur-fixing agent. The preparation method of the coal-contacting agent comprises the following steps: crushing, grinding and mixing.
背景技术Background technique
我国是世界上产煤和烧煤最多的国家。煤是我国能源结构中第一能源。但是,材煤的燃烧利用中,普遍存在着两大问题:1.煤的燃烧不充分,不合理,耗煤大。热效率低,煤炭资源浪费严重;2.煤炭是一种不清洁的天然化石燃料,加之燃烧技术落后,致使煤在燃烧时产生大量烟尘、硫氧化物、一氧化碳等多种有害的气体和物质,污染大气。煤是由碳、氢、氧、氮、硫磷等多种元素组成的可燃的和不可燃的复杂物质,煤的燃烧是这些复杂化合物、混合物参与的复杂的物理、化学反应过程。以往,人们在利用煤炭获得热能时,只粗放地使其在空气中燃烧,不能合理、科学地利用,既造成煤炭资源的浪费,又严重污染大气环境。对此,我国在节煤降耗和减少燃煤有害排放方面做了大量开发工作,近年来开发了一些煤添加剂,如节煤晶、燃煤促进剂、助燃剂等。它们主要是以高锰酸盐、碳酸盐、氧化钙为助燃剂,以硝酸钠、铜盐、碳酸钠为除尘剂,以金属卤化物为膨松剂,以纯碱、氧化钙为脱硫剂,这些添加剂不仅其助燃、脱硫、除尘效果有待提高,而且用量大,对锅炉炉管无保护功能。my country is the country that produces and burns the most coal in the world. Coal is the primary energy source in my country's energy structure. However, in the combustion and utilization of coal, there are generally two major problems: 1. The combustion of coal is not sufficient, unreasonable, and consumes a lot of coal. Low thermal efficiency and serious waste of coal resources; 2. Coal is an unclean natural fossil fuel, coupled with backward combustion technology, resulting in a large amount of soot, sulfur oxides, carbon monoxide and other harmful gases and substances generated during coal combustion, polluting atmosphere. Coal is a combustible and non-combustible complex substance composed of carbon, hydrogen, oxygen, nitrogen, sulfur, phosphorus and other elements. The combustion of coal is a complex physical and chemical reaction process in which these complex compounds and mixtures participate. In the past, when people used coal to obtain heat energy, they only burned it extensively in the air, which could not be used rationally and scientifically, which not only caused a waste of coal resources, but also seriously polluted the atmospheric environment. In this regard, my country has done a lot of development work in saving coal and reducing harmful emissions from coal combustion. In recent years, some coal additives have been developed, such as coal-saving crystals, coal-burning accelerators, and combustion-supporting agents. They mainly use permanganate, carbonate, and calcium oxide as combustion aids, sodium nitrate, copper salt, and sodium carbonate as dust removers, metal halides as bulking agents, and soda ash and calcium oxide as desulfurizers. These additives not only need to improve their combustion-supporting, desulfurization, and dust-removing effects, but also have large dosages and have no protective function on boiler tubes.
中国专利ZL 03112961.7公开了一种包括灰色火山崖、碳酸钙、氯化钠、高锰酸钾等原料的高能节煤脱硫剂,用量为待燃煤总重量的5-6%。但是,其制造工艺复杂,节煤效果不明显,热稳定性差,其烟尘、CO、HC、SOx、NOx的脱除效果不明显,对锅炉炉体有一定腐蚀作用。Chinese patent ZL 03112961.7 discloses a high-energy and coal-saving desulfurizer comprising gray volcanic cliffs, calcium carbonate, sodium chloride, potassium permanganate and other raw materials, and the consumption is 5-6% of the total weight of coal to be burned. However, its manufacturing process is complicated, its coal-saving effect is not obvious, its thermal stability is poor, its removal effect of soot, CO, HC, SOx, and NOx is not obvious, and it has a certain corrosion effect on the boiler body.
本发明采用多种原料,提供一种新型5合1触煤剂,能够有效地节能减排,功效明显。The invention adopts a variety of raw materials to provide a novel 5-in-1 coal contact agent, which can effectively save energy and reduce emissions, and has obvious effects.
发明内容Contents of the invention
本发明提供一种5合1触煤剂及其制备方法,该触煤剂包括二氧化锰、氯酸钾、氢氧化钾、锌、氧化锌、氢氧化钙、过磷酸钙、镁;该方法将各组份原料进行粉碎、研磨、混合,得到所述的触煤剂成品。其目的是要解决煤炭燃烧效率低下、燃烧污染严重、燃煤锅炉损耗的问题。本发明技术能够产生省煤、省电、脱硫、减排、清炉之五大功效。The invention provides a 5-in-1 coal-contacting agent and a preparation method thereof. The coal-contacting agent comprises manganese dioxide, potassium chlorate, potassium hydroxide, zinc, zinc oxide, calcium hydroxide, calcium superphosphate, and magnesium; The component raw materials are pulverized, ground and mixed to obtain the finished coal-contacting agent. Its purpose is to solve the problems of low coal combustion efficiency, serious combustion pollution, and loss of coal-fired boilers. The technology of the invention can produce five major effects of coal saving, electricity saving, desulfurization, emission reduction and furnace cleaning.
本发明的技术方案是这样实现的:Technical scheme of the present invention is realized like this:
一种5合1触煤剂,其特征在于,包括下述重量份数配比的原料:A 5-in-1 coal-contacting agent is characterized in that it comprises the following raw materials in parts by weight:
二氧化锰 (MnO2) 2-3.5Manganese dioxide (MnO 2 ) 2-3.5
氯酸钾 (KClO3) 20-30Potassium chlorate (KClO 3 ) 20-30
高锰酸钾 (KMnO4) 6.5-10Potassium permanganate (KMnO 4 ) 6.5-10
氢氧化钾 (KOH) 10-15Potassium Hydroxide (KOH) 10-15
锌 (Zn) 15-20Zinc (Zn) 15-20
氧化锌 (ZnO) 5-10Zinc Oxide (ZnO) 5-10
氢氧化钙 (Ca(OH)2) 15-20Calcium Hydroxide (Ca(OH) 2 ) 15-20
过磷酸钙 (Ca(H2PO4)2) 15-20Calcium superphosphate (Ca(H 2 PO4) 2 ) 15-20
镁 (Mg) 5-10。Magnesium (Mg) 5-10.
所述的1千克的触煤剂中含有的化学成分为:钾185克,钙79克,锌72克,镁38克,锰32克,氧593克,杂质1克。The chemical composition contained in the 1 kg coal contact agent is: 185 grams of potassium, 79 grams of calcium, 72 grams of zinc, 38 grams of magnesium, 32 grams of manganese, 593 grams of oxygen, and 1 gram of impurities.
所述的触煤剂中,催化剂是二氧化锰,氧化剂是氯酸钾、高锰酸钾、氢氧化钾,固硫剂是锌、氧化锌、氢氧化钙、镁。In the described coal-contacting agent, the catalyst is manganese dioxide, the oxidant is potassium chlorate, potassium permanganate, potassium hydroxide, and the sulfur-fixing agent is zinc, zinc oxide, calcium hydroxide, and magnesium.
所述的触煤剂的制备方法,其特征在于,工艺步骤为:The preparation method of the described coal-contacting agent is characterized in that the process steps are:
A.粉碎:将所述的各组份原料按任意顺序,利用粉碎机分别进行单独粉碎;A. Pulverization: use a pulverizer to pulverize the raw materials of each component in any order;
B.研磨:将所述的粉碎后的各组份原料,利用碾碎机进行单独研磨,使其成为200目-300目的颗粒;B. Grinding: Grinding the pulverized raw materials of each component separately with a grinder to make it into 200-300 mesh particles;
C.混合:利用混合机将研磨后的所述的颗粒,按设定的比例均匀混合搅拌,即得成品。C. Mixing: Use a mixer to uniformly mix and stir the ground particles according to the set ratio to obtain the finished product.
所述的B步骤中,也可以利用研磨机进行单独研磨,使其成为200目-300目的颗粒。In the B step, it is also possible to use a grinder to grind separately to make it into 200 mesh-300 mesh particles.
本发明与已有技术相比具有如下优点:Compared with the prior art, the present invention has the following advantages:
1.本发明在煤炭燃烧过程中,使煤炭燃烧效率提高15%-20%。1. The present invention improves the coal combustion efficiency by 15%-20% during the coal combustion process.
2.本发明产生环保效益显著,能有效去除煤炭在燃烧过程中产生的硫氧化物(SOx)33.3%,去除氮氧化物(NOx)20%-60%、去除一氧化碳(CO)及碳氢化合物(CxHr)50%-70%,去除烟尘50%-70%,而且能够防止燃煤锅炉的损耗。2. The present invention has remarkable environmental protection benefits, and can effectively remove 33.3% of sulfur oxides (SOx) produced during coal combustion, 20%-60% of nitrogen oxides (NOx), and carbon monoxide (CO) and hydrocarbons (CxHr) 50%-70%, remove smoke and dust 50%-70%, and can prevent the loss of coal-fired boilers.
3.本发明产生了省煤、省电、脱硫、减排、清炉的5大功效,故称为“5合1触煤剂”。3. The present invention produces 5 major effects of coal saving, electricity saving, desulfurization, emission reduction, and furnace cleaning, so it is called "5 in 1 coal contact agent".
具体实施方式Detailed ways
实施例1:Example 1:
本实施例提供的所述的5合1触煤剂采用的配比如下:The proportioning that the described 5-in-1 coal-contacting agent provided by the present embodiment is adopted is as follows:
配制所述的触煤剂93.5kg-138.5kg,按重量份数配比包括下列组分:Prepare the described coal-contacting agent 93.5kg-138.5kg, comprising the following components in parts by weight:
二氧化锰 (MnO2) 2kg-3.5kgManganese dioxide (MnO 2 ) 2kg-3.5kg
氯酸钾 (KClO3) 20kg-30kgPotassium chlorate (KClO 3 ) 20kg-30kg
高锰酸钾 (KMnO4) 6.5kg-10kgPotassium permanganate (KMnO 4 ) 6.5kg-10kg
氢氧化钾 (KOH) 10kg-15kgPotassium Hydroxide (KOH) 10kg-15kg
锌 (Zn) 15kg-20kgZinc (Zn) 15kg-20kg
氧化锌 (ZnO) 5kg-10kgZinc Oxide (ZnO) 5kg-10kg
氢氧化钙 (Ca(OH)2) 15kg-20kgCalcium Hydroxide (Ca(OH) 2 ) 15kg-20kg
过磷酸钙 (Ca(H2PO4)2) 15kg-20kgCalcium superphosphate (Ca(H 2 PO4) 2 ) 15kg-20kg
镁 (Mg) 5kg-10kgMagnesium (Mg) 5kg-10kg
所述的触煤剂中,催化剂是二氧化锰,氧化剂是氯酸钾、高锰酸钾、氢氧化钾,固硫剂是锌、氧化锌、氢氧化钙、镁。In the described coal-contacting agent, the catalyst is manganese dioxide, the oxidant is potassium chlorate, potassium permanganate, potassium hydroxide, and the sulfur-fixing agent is zinc, zinc oxide, calcium hydroxide, and magnesium.
所述的触煤剂,其特征在于,所述的1千克的触煤剂中含有的化学成分为:钾185克,钙79克,锌72克,镁38克,锰32克,氧593克,杂质1克。The coal-contacting agent is characterized in that the chemical composition contained in 1 kg of the coal-contacting agent is: 185 grams of potassium, 79 grams of calcium, 72 grams of zinc, 38 grams of magnesium, 32 grams of manganese, and 593 grams of oxygen , 1 gram of impurity.
所述的触煤剂的制备方法,其特征在于,所述制备方法的工艺步骤为:The preparation method of the described coal contact agent is characterized in that the processing steps of the preparation method are:
A.粉碎:将上述的各组份原料按任意顺序,利用粉碎机分别进行单独粉碎;A. Pulverization: Use a pulverizer to pulverize the above-mentioned raw materials of each component in any order;
B.研磨:将上述的粉碎后的各组份原料,利用FT-150D型碾碎机进行单独研磨,使其成为200目-300目的颗粒;B. Grinding: Use the FT-150D type grinder to grind the above-mentioned raw materials of each component after pulverization to make them into 200-300 mesh particles;
C.混合:利用FT-2000KAS型卧式混合搅拌机将研磨后的所述的颗粒,按设定的比例均匀混合搅拌,即得成品。C. Mixing: Use FT-2000KAS horizontal mixing mixer to mix and stir the ground particles uniformly according to the set ratio to get the finished product.
所述的B步骤中,也可以利用研磨机进行单独研磨,使其成为200目-300目的颗粒。In the B step, it is also possible to use a grinder to grind separately to make it into 200 mesh-300 mesh particles.
本实施例的使用方法:The usage method of this embodiment:
方法1:将所述的触煤剂和煤炭按重量份数比2∶1000均匀撒在燃煤中。Method 1: Evenly sprinkle the coal-contacting agent and coal in the burning coal according to the weight ratio of 2:1000.
方法2:将所述的触煤剂和煤炭按重量份数比2∶1000混合均匀,并以人工或机械(如FT-2000KAS型卧式混合搅拌机)拌合,使用甚为简便。Method 2: Mix the coal-contacting agent and coal evenly at a weight ratio of 2:1000, and mix them manually or mechanically (such as FT-2000KAS horizontal mixing mixer), which is very easy to use.
本实施例所述的触煤剂适用于所有产地的粉煤、块煤,尤其以粉煤效果为佳;所述的块煤直径为3mm左右;新型的大锅炉大部分用粉煤,旧式的供热或工业锅炉用块煤。The coal contact agent described in this embodiment is suitable for pulverized coal and lump coal in all production areas, especially the effect of pulverized coal is good; the diameter of the lump coal is about 3mm; most of the new large boilers use pulverized coal, and the old type Lump coal for heating or industrial boilers.
本实施例产品安全可靠。根据天津市化学试剂研究所的分析报告,本实施例产品在低温下无法自燃,无酸性、刺激性,不会侵蚀锅炉、产生锅垢物,对锅炉无损伤;燃烧后无不良气体产生,未发现重金属等有毒化学成分;本实施例产品属普通货物,无易燃易爆性。The product of this embodiment is safe and reliable. According to the analysis report of Tianjin Chemical Reagent Research Institute, the product of this embodiment cannot spontaneously combust at low temperature, is non-acidic and irritating, will not corrode the boiler, produce boiler scale, and has no damage to the boiler; Toxic chemical components such as heavy metals were found; the product of this embodiment belongs to common goods, and is non-flammable and explosive.
本实施例助燃原理产生节能效益:The combustion-supporting principle of this embodiment produces energy-saving benefits:
在化学反应中,氧化反应为一个最普通且最重要的反应。氧化简单地说,即物质与氧发生作用而生成氧化物。燃烧则可说是最常见,也是最激烈的氧化反应。而凡在空气中或在有氧环境下能燃烧,同时产生光和热;可直接或间接利用以供给热能、动力或照明等用途的物质,可称之为燃料。Among chemical reactions, oxidation is one of the most common and important reactions. Oxidation simply means that a substance reacts with oxygen to form an oxide. Combustion is the most common and most intense oxidation reaction. Any substance that can burn in the air or in an aerobic environment to produce light and heat at the same time; and can be directly or indirectly used to provide heat, power or lighting can be called fuel.
燃料燃烧,若其可燃元素碳及氢完全氧化成CO2及H2O时。称之为完全燃烧。一般燃料的主要可燃成分为碳C、氢H2、一氧化碳CO及其他碳氢化合物CxHrOz。若其完全燃烧可以下列反应式表示:A fuel burns when its combustible elements carbon and hydrogen are completely oxidized to CO 2 and H 2 O. Call it complete combustion. The main combustible components of general fuel are carbon C, hydrogen H 2 , carbon monoxide CO and other hydrocarbons CxHrOz. If it burns completely, it can be represented by the following reaction formula:
C+O2→CO2 C+O 2 →CO 2
2HO2+O2→2HO2 2HO 2 +O 2 →2HO 2
2CO+O2→2CO2 2CO+O 2 →2CO 2
4CxHr+(4x+y)O2→4xCO2+2yH2O4CxHr+(4x+y)O 2 →4xCO 2 +2yH 2 O
4CxHrOz+(4x+y-2z)O2→4XCO2+2yH2O4CxHrOz+(4x+y-2z)O 2 →4XCO 2 +2yH 2 O
相反的,若燃料只部分燃烧或氧化不足时,称之为不完全燃烧。Conversely, if the fuel is only partially combusted or insufficiently oxidized, it is called incomplete combustion.
如碳不完全燃则生成一氧化碳:If the carbon is not completely combusted, carbon monoxide is formed:
2CO+O2→2CO2CO+O 2 →2CO
碳化合物若不完全燃烧,则常导致燃料的损失,降低燃烧的效率。为使燃料进行完全燃烧,须供给适量的空气与适当的温度环境。空气量过少,则不能完全燃烧。空气量过多则废气量增加,带走热量亦多,其结果使燃烧温度降低,同时造成污染。环境温度过高则浪费燃料,温度过低则不足使燃料完全燃烧。因此,完全燃烧可以充分发挥燃料的燃烧效率,并减少对空气的污染。依燃烧理论若燃料完全燃烧,理论上所需氧气或空气量,可由燃烧反应式求得。但实际空气时,无法使理论空气量与燃料中可燃成分完全燃烧,因此需供给过量的空气。实际空气量与理论空气量之比,称为过剩空气系数:If carbon compounds are not completely burned, it often leads to the loss of fuel and reduces the efficiency of combustion. In order to make the fuel burn completely, it is necessary to supply an appropriate amount of air and an appropriate temperature environment. If the amount of air is too small, complete combustion cannot be achieved. Too much air will increase the amount of exhaust gas and take away more heat. As a result, the combustion temperature will be lowered and pollution will be caused. If the ambient temperature is too high, fuel will be wasted, and if the temperature is too low, it will not be enough to completely burn the fuel. Therefore, complete combustion can give full play to the combustion efficiency of fuel and reduce air pollution. According to the combustion theory, if the fuel is completely combusted, the amount of oxygen or air required in theory can be obtained from the combustion reaction formula. However, in the case of actual air, it is impossible to completely combust the theoretical air volume and combustible components in the fuel, so an excessive amount of air needs to be supplied. The ratio of the actual air volume to the theoretical air volume is called the excess air coefficient:
m(过剩空气系数)=实际空气量/理论空气量m (excess air coefficient) = actual air volume / theoretical air volume
对已知燃料元素组成时所需氧量之计算:Calculation of oxygen required for known fuel element composition:
则理论需氧量(以NM3表示时)=22.4(C/12+H/4+S/32-O/32)(NM3/Kffuel)Theoretical oxygen demand (when expressed in NM 3 )=22.4(C/12+H/4+S/32-O/32)(NM 3 /Kffuel)
则理论需氧量(以Kg表示时)=32(C/12+H/4+S/32-O/32)(Kg/Kg fuel)Then the theoretical oxygen demand (expressed in Kg) = 32 (C/12+H/4+S/32-O/32) (Kg/Kg fuel)
所以理论空气量(Ao)为:So the theoretical air volume (Ao) is:
因为1Kg mole air=32×0.21+28×0.79=28.84KgBecause 1Kg mole air=32×0.21+28×0.79=28.84Kg
1Kg空气含氧量=0.21×32/2884=0.232Kg1Kg air oxygen content=0.21×32/2884=0.232Kg
所以理论空气量(Ao)为:So the theoretical air volume (Ao) is:
Ao=(C/12+H/4+S/32-O/32)×22.4/0.21Ao=(C/12+H/4+S/32-O/32)×22.4/0.21
=8.89C+2.67(H-O/8)+3.33S(NM3/Kf fuel)=8.89C+2.67(HO/8)+3.33S(NM 3 /Kf fuel)
Ao=(C/12+H/4+S/32-O/32)×32/0.232Ao=(C/12+H/4+S/32-O/32)×32/0.232
=11.49C+34.48(H-O/8)+4.30S(Kg/Kg Fuel)=11.49C+34.48(H-O/8)+4.30S(Kg/Kg Fuel)
其中C:燃料中碳之重量百分浓度,%Where C: weight percent concentration of carbon in fuel, %
H:燃料中碳之重量百分浓度,%H: weight percent concentration of carbon in fuel, %
S:燃料中碳之重量百分浓度,%S: weight percent concentration of carbon in fuel, %
O:燃料中碳之重量百分浓度,%O: weight percent concentration of carbon in fuel, %
由上述计算式,一吨燃煤若含碳量约60%,则理论需氧量为1500Kg,而所述的触煤剂中的主要成分如氯酸钾KClO3经二氧化锰MnO2催化,受热则分解释出氧O2:From the above calculation formula, if the carbon content of one ton of coal is about 60%, then the theoretical oxygen demand is 1500Kg, and the main component in the described coal-contacting agent is as potassium chlorate KClO catalyzed by manganese dioxide MnO , heated Decompose to release oxygen O 2 :
以所述的触煤剂:2Kg/1000Kg燃煤(Coal)之添加量。而其含氧成份约60%计,则可提供约1.2Kg之O2,即增加约0.12%之供氧量,以促进完全燃烧。燃煤炭完全燃烧的条件不仅是有足量的氧气,尚须其他条件的配合。有诸多专家学者研究化学反应的进行,常藉助触媒学,(或催化剂CATALYSTS)的效用,降低反应进行所须的活化能(Act-ivation Energy),以加速反应的进行。同时,在燃烧的反应中,加入适量的触媒,不但可以加速燃烧,同时亦加速放出热量,使不完全燃烧的物质减少。这类触媒,即所谓燃料添加剂。若以煤炭为燃料,即为煤炭触媒。燃烧反应的反应极为复杂,与燃料成分、燃烧环境及燃烧条件等变数与因素有关,基本的化学结构、自由基(Free radical)的生或与氧化反应有关的理论。The above-mentioned coal contact agent: 2Kg/1000Kg coal (Coal) addition. Based on its oxygen content of about 60%, it can provide about 1.2Kg of O 2 , that is, increase the oxygen supply by about 0.12%, so as to promote complete combustion. The condition for the complete combustion of coal is not only sufficient oxygen, but also the cooperation of other conditions. Many experts and scholars study the progress of chemical reactions, and often rely on the effectiveness of catalysis (or catalyst CATALYSTS) to reduce the activation energy (Activation Energy) required for the reaction to accelerate the reaction. At the same time, in the combustion reaction, adding an appropriate amount of catalyst can not only accelerate the combustion, but also accelerate the release of heat, reducing the incompletely combusted substances. Such catalysts are called fuel additives. If coal is used as fuel, it is a coal catalyst. Combustion reactions are extremely complex, and are related to variables and factors such as fuel composition, combustion environment, and combustion conditions. Basic chemical structures, free radicals, or theories related to oxidation reactions.
而在氧化反应的同时,分子状态的氧在相当高温度下,也可能因氧分子外围电子受激发(Excitation)而形成单电子性氧分子(Singlet Oxygen)。此单电子性氧分子的作用就如同自由基的作用一样,可与有机物中的氢原子结合形成新的自由基,而进行连续的反应,最后全部氧化生成二氧化碳与水蒸气:At the same time as the oxidation reaction, the oxygen in the molecular state may also form a single-electron oxygen molecule (Single Oxygen) due to the excitation of the peripheral electrons of the oxygen molecule at a relatively high temperature. This one-electron oxygen molecule acts like a free radical, it can combine with hydrogen atoms in organic matter to form new free radicals, and carry out continuous reactions, and finally all oxidize to generate carbon dioxide and water vapor:
2CnH2n+2+O’2→2CnH2n+1+H2O+[O]2CnH 2 n+2+O' 2 →2CnH 2 n+1+H 2 O+[O]
2CnH2n+1+O’2→2CnH2n+1+H2O+[O]2CnH 2 n+1+O' 2 →2CnH 2 n+1+H 2 O+[O]
由以上的基本反应,可以了解在燃烧过程及反应时,自由基的产生是一个必经的过程。同时,若在反应时增加自由基的产生,或加速自由基的形成,都可以提高燃烧的效。燃料增加剂的主要功用就是利用此原理,在催化过程中把能促使产生自由基的媒体加入燃烧环境中。使燃料在燃烧的过程中,加速产生自由基,而使达到完全燃烧的结果。如此不但燃料可以加速氧化,同时燃料所含的能量也可以尽量释出,获得最高的燃烧效率。From the above basic reactions, it can be understood that the generation of free radicals is a necessary process in the combustion process and reaction. At the same time, if the generation of free radicals is increased during the reaction, or the formation of free radicals is accelerated, the efficiency of combustion can be improved. The main function of the fuel enhancer is to use this principle to add media that can promote the generation of free radicals into the combustion environment during the catalytic process. During the combustion process of the fuel, the generation of free radicals is accelerated, so that the result of complete combustion can be achieved. In this way, not only the oxidation of the fuel can be accelerated, but also the energy contained in the fuel can be released as much as possible to obtain the highest combustion efficiency.
本实施例所述的触煤剂在增加煤炭燃烧过程中所需之自由基及加速自由基的形成上,成效斐然。经实际测试,燃烧效率约提高15%-20%,节煤率为5%-20%(依据锅炉的使用年龄及炉型而定)。The coal contacting agent described in this embodiment is effective in increasing the free radicals required in the coal combustion process and accelerating the formation of free radicals. According to the actual test, the combustion efficiency is increased by about 15%-20%, and the coal saving rate is 5%-20% (depending on the age and type of the boiler).
本实施例产生化学原理产生环保效益:The present embodiment produces chemical principle and produces environmental protection benefit:
本实施例能够产生积极的环保效益;齐齐哈尔市环境监测中心的环保监测分析说明,加入所述的触煤剂后,检测不合格的气体下降70%-91.5%而达到标准;检测合格的气体再下降33%,充分发挥环保效益。监测结果如下:The present embodiment can produce positive environmental benefits; the environmental monitoring analysis of Qiqihar City Environmental Monitoring Center shows that after adding the coal-contacting agent, the unqualified gas drops by 70%-91.5% and reaches the standard; Decrease 33%, give full play to the environmental benefits. The monitoring results are as follows:
1.硫氧化物(SOx)的去除1. Removal of sulfur oxides (SOx)
燃煤产生的最主要污染物为硫氧化物(SOx),而以目前国内燃煤锅炉烟气排放中SOx含量,除使用硫成份低于0.6%之燃煤外,大多无法达到国家排放标准(二氧化硫SO2排放标准为1200mg/M3),故需设置排烟脱硫(FGD,Flue Gas Desulfurization)来符合环保要求。再者,低硫煤成本较高。为了有效利用炭能资源并扩大煤源,燃煤过程中的除硫步骤势在必行。The most important pollutant produced by coal combustion is sulfur oxides (SOx), and the SOx content in the flue gas emissions of domestic coal-fired boilers, except for the use of coal with a sulfur content of less than 0.6%, most of them cannot meet the national emission standards ( The emission standard of sulfur dioxide (SO 2 ) is 1200mg/M 3 ), so FGD (Flue Gas Desulfurization) must be installed to meet environmental protection requirements. Furthermore, the cost of low-sulfur coal is higher. In order to effectively utilize carbon energy resources and expand coal sources, the sulfur removal step in the coal combustion process is imperative.
二氧化硫SO2是一种不燃烧不爆炸但具令人窒息的刺激性气体,其在空气中浓度为0.3-1.0ppm时,即能嗅出其味。若浓度超过3.0ppm,即会有使人感觉刺激痛苦的气味。在大气种,SO2经由光化学作用或触煤反应过程,可部分转为三氧化硫SO3或硫酸H2SO4、硫酸盐。从排烟中去除SO2的技术简称“排烟脱硫”。用于工业装置上排烟脱硫,应注意下列几个原因:Sulfur dioxide SO 2 is a non-flammable and non-explosive but suffocating irritating gas. When its concentration in the air is 0.3-1.0ppm, its smell can be smelled. If the concentration exceeds 3.0ppm, there will be a stimulating and painful smell. In atmospheric species, SO 2 can be partially transformed into sulfur trioxide SO 3 or sulfuric acid H 2 SO 4 and sulfate through photochemical action or coal-contact reaction process. The technology of removing SO2 from flue gas is called "flue gas desulfurization" for short. When used for flue gas desulfurization on industrial devices, the following reasons should be paid attention to:
A.排烟脱硫的工作原理及流程应简单,装置紧凑易于操作管理。A. The working principle and process of exhaust gas desulfurization should be simple, and the device should be compact and easy to operate and manage.
B.脱硫装置应具有较高的脱硫效率,能长期连续运转,经济效果好,节省人力,占地面积小。B. The desulfurization device should have high desulfurization efficiency, can operate continuously for a long time, has good economic effect, saves manpower, and occupies a small area.
C.脱硫过程中不产生二次污染物,回收产物应无二次污染公害。C. No secondary pollutants are produced during the desulfurization process, and the recovered products should have no secondary pollution hazards.
D.脱硫用的吸收剂与吸附剂价格便宜又易获得。D. Absorbents and adsorbents for desulfurization are cheap and easy to obtain.
E.在工作方法选择上应尽可能考虑到回收到有用的硫资源。E. The recovery of useful sulfur resources should be considered as much as possible in the selection of working methods.
所述的触煤剂以活性大之金属强氧化剂作为脱硫剂,其化学反应如下:The described coal-contacting agent uses a highly active metal strong oxidant as a desulfurizing agent, and its chemical reaction is as follows:
2KMnO4+5SO2+2H2O→K2SO4+2MnSO4+2H2SO4 2KMnO 4 +5SO 2 +2H 2 O→K 2 SO 4 +2MnSO 4 +2H 2 SO 4
2KMnO4+3H2SO4→K2SO4+2MnSO4+3H2O+5[O]2KMnO 4 +3H 2 SO 4 →K 2 SO 4 +2MnSO 4 +3H 2 O+5[O]
K2CO3+SO2→K2SO4+CO2 K 2 CO 3 +SO 2 →K 2 SO 4 +CO 2
MgO+H2O→Mg(OH)2 MgO+H 2 O→Mg(OH) 2
Mg(OH)2+SO2+5H2O→MgSO2·6H2OMg(OH) 2 +SO 2 +5H 2 O→MgSO 2 6H 2 O
Mg(OH)2+SO2→MgSO3·H2OMg(OH) 2 +SO 2 →MgSO 3 ·H 2 O
Mg(OH)2+SO26H2OH2O→Mg(HSO3)2 Mg(OH) 2 +SO 2 6H 2 OH 2 O→Mg(HSO 3 ) 2
Mg(OH)2+Mg(HSO3)2+10H2O→2MgSO3·6H2OMg(OH) 2 +Mg(HSO 3 ) 2 +10H 2 O→2MgSO 3 6H 2 O
2MgSO3+O2+7H2O→2MgSO3·7H2O2MgSO 3 +O 2 +7H 2 O→2MgSO 3 7H 2 O
ZnO+SO2→ZnSO3 ZnO+SO 2 →ZnSO 3
2Ca(H2PO4)2+2SO2+O22CaSO4P4O10+4H2O2Ca(H 2 PO 4 )2+2SO 2 +O 2 2CaSO 4 P 4 O 10 +4H 2 O
实际验证本发明对去除硫氧化物SOx 33.3%。It is actually verified that the present invention can remove 33.3% of sulfur oxides SOx.
2.氮氧化物(NOx)的去除2. Removal of nitrogen oxides (NOx)
NOx为一氧化氮NO及二氧化氮NO2的总称,其中95%为NO。其影响可:直接危害人体健康;妨碍植物生长;生成光化学氮化物,通称为烟雾(Smog是Smoke和Fog的总称),NOx在阳光照射下会与碳氢化合物作用生成臭氧O3为主的氧化物,O3会对呼吸器造成严重伤害,吸入Smog会刺激肺部及加剧哮喘;造成酸雨,NOx在大气中经过一连串的复杂反应,转化为硝酸。NOx is the general term for nitrogen monoxide NO and nitrogen dioxide NO 2 , of which 95% is NO. Its impact can: directly endanger human health; hinder plant growth; generate photochemical nitrogen compounds, commonly known as smog (Smog is the general name of Smoke and Fog), NOx will react with hydrocarbons under sunlight to generate ozone O 3- based oxidation O 3 will cause serious damage to the respirator, and inhalation of Smog will stimulate the lungs and aggravate asthma; cause acid rain, and NOx will be converted into nitric acid through a series of complex reactions in the atmosphere.
在燃烧过程中所产生的NOx主要有:A.热量NOx(Thermal NOx):空气中氮N2受热氧化成NOx;B.燃烧NOx(Fuel NOx):燃烧中有机氮化物转化成NOx;The NOx produced during the combustion process mainly includes: A. Thermal NOx (Thermal NOx): nitrogen N 2 in the air is heated and oxidized into NOx; B. Fuel NOx (Fuel NOx): organic nitrogen compounds are converted into NOx during combustion;
C.Prompt NOn:燃烧经系列反应生成碳氢自由基,经N2与O2化合后反应而生成NO2。C.Prompt NOn: Combustion generates hydrocarbon radicals through a series of reactions, and reacts with N 2 and O 2 to generate NO 2 .
以甲烷CH4为例说明如下:Take methane CH4 as an example to illustrate as follows:
CH4→CH3+HCH 4 →CH 3 +H
N2+CH3→NH2HCNN 2 +CH 3 →NH 2 HCN
HCN+H→CN+H2 HCN+H→CN+H 2
CN+O2→CO+NOCN+O 2 →CO+NO
NH2+O2→H2O+NONH 2 +O 2 →H 2 O+NO
燃煤所产生之NOx 80%是Fuel NOx,燃料中含氮化合物通常以咔唑(Carbazole)、吡啶(Pyridine,C5H5N)及喹啉(Quinoline)等形态存在。在燃烧时这些物质会分解或氧化为CN、NH、NH2等分子,然后再进一步氧化为NO2。80% of NOx produced by coal combustion is Fuel NOx. Nitrogenous compounds in fuel usually exist in the form of carbazole (Carbazole), pyridine (Pyridine, C 5 H 5 N) and quinoline (Quinoline). These substances will be decomposed or oxidized into CN, NH, NH 2 and other molecules during combustion, and then further oxidized into NO 2 .
燃烧后产生的废气可以用化学反应的方法,将NOx转化成无污染的氮气,所述的触煤剂同时以还原法及吸收法来去除NOx:The exhaust gas produced after combustion can be converted into non-polluting nitrogen by chemical reaction method, and the coal contacting agent is used to remove NOx by reduction method and absorption method at the same time:
2NO+2CO→N2+CO2 2NO+2CO→N 2 +CO 2
K2CO3+2NO2→KN2+KNO3+CO2 K2CO 3 +2NO 2 →KN 2 +KNO 3 +CO 2
2K(OH)+4NO→N2O+KNO2+H2O2K(OH)+4NO→N 2 O+KNO 2 +H 2 O
4K(OH)+6NO→N2O+4KNO2+H2O4K(OH)+6NO→N 2 O+4KNO 2 +H 2 O
SO2+NO2+H2O→H2SO4+NOSO 2 +NO 2 +H 2 O→H 2 SO 4 +NO
NO+NO2+H2SO4→H2SO4+NONO+NO 2 +H 2 SO 4 →H 2 SO 4 +NO
2NOHSO4+H2O→2H2SO4+(NO+NO2)2NOHSO 4 +H 2 O→2H 2 SO 4 +(NO+NO 2 )
3NO2H2O→2HNO3+NO3NO 2 H 2 O→2HNO 3 +NO
4NO+O2→4NO2 4NO+O 2 →4NO 2
Mg(OH)2+SO2→MgSO3+H2OMg(OH) 2 +SO 2 →MgSO 3 +H 2 O
Mg(OH)2+NO2+NO2→Mg(NO2)2+H2OMg(OH) 2 +NO 2 +NO 2 →Mg(NO 2 ) 2 +H 2 O
实际验证本发明可去除氮化物NOx达20%-60%。It is actually verified that the present invention can remove nitride NOx up to 20%-60%.
3.一氧化碳CO及碳氢化合物CxHr的去除3. Removal of carbon monoxide CO and hydrocarbon CxHr
所述的触煤剂以促进完全燃烧的方式减少一氧化碳及碳氢化合物的排放量。实际验证本发明可去除一氧化碳、碳氢化合物50%-70%。The coal contact agent reduces the emission of carbon monoxide and hydrocarbons by promoting complete combustion. It is actually verified that the present invention can remove 50%-70% of carbon monoxide and hydrocarbons.
4.烟尘的去除4. Removal of smoke and dust
日常生活中,最常碰到的空气污染问题,应该是黑烟。近年来由于燃烧技术的改良及空气污染防治设备的使用,工厂烟囱排放浓重黑烟的情形已不多见。然而在以含高硫成份煤或油为燃料的火力发电厂或水泥厂,烟囱口外常会有一种持续很久且高不透光率的白蓝色烟柱,其主要成分晟主要是微细硫酸盐粒子或凝结的硫酸气悬胶(Sulruric Acid Acrosol)。这些酸性物质,对空气品质有很大的不良影响,而且是造成酸雨及大气能见度降低的重要因素。所述的触煤剂以改善煤炭的燃烧状况以减少黑烟的排放量,并减少SOx的排放量以降低白烟的不透光度。经实际验证本发明去除烟尘50%-70%。In daily life, the most frequently encountered air pollution problem should be black smoke. In recent years, due to the improvement of combustion technology and the use of air pollution prevention and control equipment, it is rare for factory chimneys to emit thick black smoke. However, in thermal power plants or cement plants that use high-sulfur coal or oil as fuel, there is often a white-blue smoke column that lasts for a long time and has a high opacity outside the chimney mouth, and its main components are mainly fine sulfate particles or Condensed Sulfuric Acid Acrosol. These acidic substances have a great adverse effect on air quality, and are an important factor causing acid rain and reduced atmospheric visibility. The coal-contacting agent is used to improve the combustion state of coal to reduce the emission of black smoke, and to reduce the emission of SOx to reduce the opacity of white smoke. It has been verified that the present invention removes 50%-70% of smoke and dust.
5.防止燃煤锅炉的损耗5. Prevent loss of coal-fired boilers
铁共有在空气和湿气并在环境中,并在酸或与锡、铜等活性小的金属接触才会生锈。铁生锈是一种电化学的步骤,铁的表面有些部分能够从别的地方吸引电子,这是受了杂质、扭曲,或其他能改变铁活性的因素影响。如果电子从铁表面的一处移至另一边,则失去电子之处(氧化)成为阳极,得电子之处(还原)成为阴极,便形成了一个小规模的电池。阳极反应是铁变成+2价的铁离子Fe++,阴极反应为水H2O还原成氢氧根离子OH-和氢气H2。阳极的Fe++和阴极的OH-接触,则形成氢氧化铁(ii)Fe(OH)。再被空气氧化,成为氧化铁(iii)的水含物Fe2O3xH2O,这种红色的化合物就是我们所谓的锈。铁锈并不固著在铁表面,脱落后下屑的铁又会生锈,所以铁会不断地锈下去。Iron is in the air and moisture and in the environment, and will only rust when it is in contact with acid or tin, copper and other less active metals. Rusting of iron is an electrochemical process in which parts of the iron surface are able to attract electrons from elsewhere, due to impurities, distortion, or other factors that alter the activity of the iron. If electrons move from one side of the iron surface to the other, the place where electrons are lost (oxidized) becomes the anode, and the place where electrons are gained (reduced) becomes the cathode, forming a small-scale battery. The anode reaction is that iron becomes +2-valent iron ion Fe ++ , and the cathode reaction is the reduction of water H 2 O to hydroxide ion OH - and hydrogen H 2 . The Fe ++ of the anode contacts the OH - of the cathode, forming iron(ii)Fe(OH) hydroxide. It is then oxidized by air to become the hydrate Fe 2 O 3 xH 2 O of iron oxide (iii), and this red compound is what we call rust. Rust is not fixed on the iron surface, and the iron that has fallen off will rust again after falling off, so the iron will continue to rust.
2Fe→2Fe+++4e-(阳极)2Fe→2Fe ++ +4e - (anode)
2H2O+2e→2OH-+H2(阴极)2H 2 O+2e→2OH - +H 2 (cathode)
2Fe+++4OH-→2Fe(OH)2 2Fe ++ +4OH - → 2Fe(OH) 2
4Fe(OH)2+O2+2xH2O→2Fe2O3·xH2O+4H2O4Fe(OH) 2 +O 2 +2xH 2 O→2Fe 2 O 3 xH 2 O+4H 2 O
所述的触煤剂是以电化学原理,利用活性较大的金属如锌、镁与铁接触组合,使得铁在电化学反应中变作阴极,无法失去电子产生氧化生锈。The coal-contacting agent is based on the principle of electrochemistry, and uses highly active metals such as zinc and magnesium to contact and combine with iron, so that iron becomes a cathode in the electrochemical reaction, and cannot lose electrons to generate oxidation and rust.
Fe+++Zn→Fe+Zn++ Fe +++ Zn→Fe+Zn ++
Fe+++Mg→Fe+Mg++ Fe +++ Mg→Fe+Mg ++
且煤炭在高置释氧量下形成水煤气(Water Gas):一氧化碳CO+H。And coal forms water gas (Water Gas): carbon monoxide CO+H under high oxygen release.
C+H2O→CO+H2 C+ H2O →CO+ H2
其中CO为还原剂,可还原氧化铁为铁:Wherein CO is a reducing agent, which can reduce iron oxide to iron:
CO+FeO→Fe+CO2 CO+FeO→Fe+CO 2
所述的触煤剂是粉末固体粒状,非流质液体,不具有侵蚀、腐化、破坏性。不仅促进燃烧、减少不良气体之产生,对燃烧空间之金属传热体亦具有保护作用。The coal-contacting agent is in the form of powder, solid and granular, non-fluid liquid, and does not have erosion, corrosion and destructiveness. It not only promotes combustion and reduces the generation of bad gas, but also protects the metal heat transfer body in the combustion space.
实施例2:Example 2:
本实施例提供的所述的触煤剂采用的配比如下:The proportioning that the described coal-contacting agent that present embodiment provides adopts is as follows:
配制所述的触煤剂98.5kg,按重量份数配比包括下列组分:Prepare described coal-contacting agent 98.5kg, proportioning by weight comprises the following components:
二氧化锰 (MnO2) 2kgManganese dioxide (MnO 2 ) 2kg
氯酸钾 (KClO3) 20kgPotassium chlorate (KClO 3 ) 20kg
高锰酸钾 (KMnO4) 6.5kgPotassium permanganate (KMnO 4 ) 6.5kg
氢氧化钾 (KOH) 15kgPotassium Hydroxide (KOH) 15kg
锌 (Zn) 15kgZinc (Zn) 15kg
氧化锌 (ZnO) 5kgZinc Oxide (ZnO) 5kg
氢氧化钙 (Ca(OH)2) 15kgCalcium Hydroxide (Ca(OH) 2 ) 15kg
过磷酸钙 (Ca(H2PO4)2) 15kgCalcium superphosphate (Ca(H 2 PO4) 2 ) 15kg
镁 (Mg) 5kgMagnesium (Mg) 5kg
所述的触煤剂中,催化剂是二氧化锰,氧化剂是氯酸钾、高锰酸钾、氢氧化钾,固硫剂是锌、氧化锌、氢氧化钙、镁。In the described coal-contacting agent, the catalyst is manganese dioxide, the oxidant is potassium chlorate, potassium permanganate, potassium hydroxide, and the sulfur-fixing agent is zinc, zinc oxide, calcium hydroxide, and magnesium.
本实施例的制备方法和使用方法与实施例1相同。The preparation method and usage method of this embodiment are the same as that of embodiment 1.
实施例3:Example 3:
本实施例提供的所述的触煤剂采用的配比如下:The proportioning that the described coal-contacting agent that present embodiment provides adopts is as follows:
配制所述的触煤剂138.5kg,按重量份数配比包括下列组分:Prepare described coal-contacting agent 138.5kg, comprise the following components by weight proportioning:
二氧化锰 (MnO2) 3.5kgManganese dioxide (MnO 2 ) 3.5kg
氯酸钾 (KClO3) 30kgPotassium chlorate (KClO 3 ) 30kg
高锰酸钾 (KMnO4) 10kgPotassium permanganate (KMnO 4 ) 10kg
氢氧化钾 (KOH) 15kgPotassium Hydroxide (KOH) 15kg
锌 (Zn) 20kgZinc (Zn) 20kg
氧化锌 (ZnO) 10kgZinc Oxide (ZnO) 10kg
氢氧化钙 (Ca(OH)2) 20kgCalcium Hydroxide (Ca(OH) 2 ) 20kg
过磷酸钙 (Ca(H2PO4)2) 20kgCalcium superphosphate (Ca(H 2 PO4) 2 ) 20kg
镁 (Mg) 10kgMagnesium (Mg) 10kg
所述的触煤剂中,催化剂是二氧化锰,氧化剂是氯酸钾、高锰酸钾、氢氧化钾,固硫剂是锌、氧化锌、氢氧化钙、镁。In the described coal-contacting agent, the catalyst is manganese dioxide, the oxidant is potassium chlorate, potassium permanganate, potassium hydroxide, and the sulfur-fixing agent is zinc, zinc oxide, calcium hydroxide, and magnesium.
本实施例的制备方法和使用方法与实施例1相同。The preparation method and usage method of this embodiment are the same as that of embodiment 1.
实施例4:Example 4:
本实施例提供的所述的触煤剂采用的配比如下:The proportioning that the described coal-contacting agent that present embodiment provides adopts is as follows:
配制所述的触煤剂122.5kg,按重量份数配比包括下列组分:Prepare described coal contact agent 122.5kg, proportioning by weight comprises the following components:
二氧化锰 (MnO2) 3kgManganese dioxide (MnO 2 ) 3kg
氯酸钾 (KClO3) 30kgPotassium chlorate (KClO 3 ) 30kg
高锰酸钾 (KMnO4) 8.5kgPotassium permanganate (KMnO 4 ) 8.5kg
氢氧化钾 (KOH) 12.5kgPotassium Hydroxide (KOH) 12.5kg
锌 (Zn) 17.5kgZinc (Zn) 17.5kg
氧化锌 (ZnO) 8kgZinc Oxide (ZnO) 8kg
氢氧化钙 (Ca(OH)2) 18kgCalcium Hydroxide (Ca(OH) 2 ) 18kg
过磷酸钙 (Ca(H2PO4)2) 18kgCalcium superphosphate (Ca(H 2 PO4) 2 ) 18kg
镁 (Mg) 7kgMagnesium (Mg) 7kg
所述的触煤剂中,催化剂是二氧化锰,氧化剂是氯酸钾、高锰酸钾、氢氧化钾,固硫剂是锌、氧化锌、氢氧化钙、镁。In the described coal-contacting agent, the catalyst is manganese dioxide, the oxidant is potassium chlorate, potassium permanganate, potassium hydroxide, and the sulfur-fixing agent is zinc, zinc oxide, calcium hydroxide, and magnesium.
本实施例的制备方法和使用方法与实施例1相同。The preparation method and usage method of this embodiment are the same as that of embodiment 1.
实施例5:Example 5:
本实施例提供的所述的触煤剂采用的配比如下:The proportioning that the described coal-contacting agent that present embodiment provides adopts is as follows:
配制所述的触煤剂121.5kg,按重量份数配比包括下列组分:Prepare described coal contact agent 121.5kg, proportioning by weight comprises following component:
二氧化锰 (MnO2) 2.5kgManganese dioxide (MnO 2 ) 2.5kg
氯酸钾 (KClO3) 27kgPotassium chlorate (KClO 3 ) 27kg
高锰酸钾 (KMnO4) 9kgPotassium permanganate (KMnO 4 ) 9kg
氢氧化钾 (KOH) 14kgPotassium Hydroxide (KOH) 14kg
锌 (Zn) 19kgZinc (Zn) 19kg
氧化锌 (ZnO) 7.5kgZinc Oxide (ZnO) 7.5kg
氢氧化钙 (Ca(OH)2) 18kgCalcium Hydroxide (Ca(OH) 2 ) 18kg
过磷酸钙 (Ca(H2PO4)2) 16kgCalcium superphosphate (Ca(H 2 PO4) 2 ) 16kg
镁 (Mg) 8.5kgMagnesium (Mg) 8.5kg
所述的触煤剂中,催化剂是二氧化锰,氧化剂是氯酸钾、高锰酸钾、氢氧化钾,固硫剂是锌、氧化锌、氢氧化钙、镁。In the described coal-contacting agent, the catalyst is manganese dioxide, the oxidant is potassium chlorate, potassium permanganate, potassium hydroxide, and the sulfur-fixing agent is zinc, zinc oxide, calcium hydroxide, and magnesium.
本实施例的制备方法和使用方法与实施例1相同。The preparation method and usage method of this embodiment are the same as that of embodiment 1.
实施例6:Embodiment 6:
本实施例提供的各组分配比与实施例1相同,所述的触煤剂的制备方法,所述的制备方法的工艺步骤为:The distribution ratio of each component that present embodiment provides is identical with embodiment 1, and the preparation method of described coal-contacting agent, the processing step of described preparation method is:
A.粉碎:将上述的各组份原料按任意顺序,利用粉碎机分别进行单独粉碎;A. Pulverization: Use a pulverizer to pulverize the above-mentioned raw materials of each component in any order;
B.研磨:将上述的粉碎后的各组份原料,利用FT-150D型碾碎机进行单独研磨,使其成为200目-300目的颗粒;B. Grinding: Use the FT-150D type grinder to grind the above-mentioned raw materials of each component after pulverization to make them into 200-300 mesh particles;
C.混合:利用FT-2000KAS型卧式混合搅拌机,将研磨后的所述的颗粒,按设定的比例均匀混合搅拌,即得成品。C. Mixing: use the FT-2000KAS horizontal mixing mixer to mix and stir the ground particles uniformly according to the set ratio to obtain the finished product.
所述的B步骤中,也可以利用研磨机进行单独研磨,使其成为200目-300目的颗粒。In the B step, it is also possible to use a grinder to grind separately to make it into 200 mesh-300 mesh particles.
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