CN108715736A - A kind of technique preparing medal polish cream coproduction acid - Google Patents
A kind of technique preparing medal polish cream coproduction acid Download PDFInfo
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- CN108715736A CN108715736A CN201810711211.4A CN201810711211A CN108715736A CN 108715736 A CN108715736 A CN 108715736A CN 201810711211 A CN201810711211 A CN 201810711211A CN 108715736 A CN108715736 A CN 108715736A
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- 239000002253 acid Substances 0.000 title claims abstract description 40
- 238000000034 method Methods 0.000 title claims description 18
- 239000006071 cream Substances 0.000 title 1
- 238000005498 polishing Methods 0.000 claims abstract description 76
- 229910052751 metal Inorganic materials 0.000 claims abstract description 66
- 239000002184 metal Substances 0.000 claims abstract description 66
- 238000004519 manufacturing process Methods 0.000 claims abstract description 57
- 239000000843 powder Substances 0.000 claims abstract description 38
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims abstract description 30
- PASHVRUKOFIRIK-UHFFFAOYSA-L calcium sulfate dihydrate Chemical compound O.O.[Ca+2].[O-]S([O-])(=O)=O PASHVRUKOFIRIK-UHFFFAOYSA-L 0.000 claims abstract description 30
- 239000010881 fly ash Substances 0.000 claims abstract description 28
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims abstract description 27
- 235000012054 meals Nutrition 0.000 claims abstract description 24
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 claims abstract description 19
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims abstract description 19
- 239000000463 material Substances 0.000 claims abstract description 18
- WRIDQFICGBMAFQ-UHFFFAOYSA-N (E)-8-Octadecenoic acid Natural products CCCCCCCCCC=CCCCCCCC(O)=O WRIDQFICGBMAFQ-UHFFFAOYSA-N 0.000 claims abstract description 15
- JLPULHDHAOZNQI-ZTIMHPMXSA-N 1-hexadecanoyl-2-(9Z,12Z-octadecadienoyl)-sn-glycero-3-phosphocholine Chemical compound CCCCCCCCCCCCCCCC(=O)OC[C@H](COP([O-])(=O)OCC[N+](C)(C)C)OC(=O)CCCCCCC\C=C/C\C=C/CCCCC JLPULHDHAOZNQI-ZTIMHPMXSA-N 0.000 claims abstract description 15
- LQJBNNIYVWPHFW-UHFFFAOYSA-N 20:1omega9c fatty acid Natural products CCCCCCCCCCC=CCCCCCCCC(O)=O LQJBNNIYVWPHFW-UHFFFAOYSA-N 0.000 claims abstract description 15
- QSBYPNXLFMSGKH-UHFFFAOYSA-N 9-Heptadecensaeure Natural products CCCCCCCC=CCCCCCCCC(O)=O QSBYPNXLFMSGKH-UHFFFAOYSA-N 0.000 claims abstract description 15
- 235000008733 Citrus aurantifolia Nutrition 0.000 claims abstract description 15
- 239000005642 Oleic acid Substances 0.000 claims abstract description 15
- ZQPPMHVWECSIRJ-UHFFFAOYSA-N Oleic acid Natural products CCCCCCCCC=CCCCCCCCC(O)=O ZQPPMHVWECSIRJ-UHFFFAOYSA-N 0.000 claims abstract description 15
- 239000002202 Polyethylene glycol Substances 0.000 claims abstract description 15
- 235000011941 Tilia x europaea Nutrition 0.000 claims abstract description 15
- WGLPBDUCMAPZCE-UHFFFAOYSA-N Trioxochromium Chemical compound O=[Cr](=O)=O WGLPBDUCMAPZCE-UHFFFAOYSA-N 0.000 claims abstract description 15
- 239000004203 carnauba wax Substances 0.000 claims abstract description 15
- 229910000423 chromium oxide Inorganic materials 0.000 claims abstract description 15
- 239000010433 feldspar Substances 0.000 claims abstract description 15
- QXJSBBXBKPUZAA-UHFFFAOYSA-N isooleic acid Natural products CCCCCCCC=CCCCCCCCCC(O)=O QXJSBBXBKPUZAA-UHFFFAOYSA-N 0.000 claims abstract description 15
- 239000004571 lime Substances 0.000 claims abstract description 15
- 239000003921 oil Substances 0.000 claims abstract description 15
- 235000019198 oils Nutrition 0.000 claims abstract description 15
- ZQPPMHVWECSIRJ-KTKRTIGZSA-N oleic acid Chemical compound CCCCCCCC\C=C/CCCCCCCC(O)=O ZQPPMHVWECSIRJ-KTKRTIGZSA-N 0.000 claims abstract description 15
- 239000004006 olive oil Substances 0.000 claims abstract description 15
- 235000008390 olive oil Nutrition 0.000 claims abstract description 15
- 239000012188 paraffin wax Substances 0.000 claims abstract description 15
- 229920001223 polyethylene glycol Polymers 0.000 claims abstract description 15
- 238000000926 separation method Methods 0.000 claims abstract description 15
- 229940083466 soybean lecithin Drugs 0.000 claims abstract description 15
- 238000002156 mixing Methods 0.000 claims abstract description 12
- 238000005188 flotation Methods 0.000 claims abstract description 11
- 239000000654 additive Substances 0.000 claims abstract description 9
- 235000019441 ethanol Nutrition 0.000 claims abstract description 8
- 238000000227 grinding Methods 0.000 claims abstract description 8
- 239000007788 liquid Substances 0.000 claims abstract description 8
- 239000003607 modifier Substances 0.000 claims abstract description 8
- 235000021313 oleic acid Nutrition 0.000 claims abstract description 8
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 18
- 239000002244 precipitate Substances 0.000 claims description 15
- 235000005340 Asparagus officinalis Nutrition 0.000 claims description 14
- 235000021355 Stearic acid Nutrition 0.000 claims description 14
- QIQXTHQIDYTFRH-UHFFFAOYSA-N octadecanoic acid Chemical compound CCCCCCCCCCCCCCCCCC(O)=O QIQXTHQIDYTFRH-UHFFFAOYSA-N 0.000 claims description 14
- OQCDKBAXFALNLD-UHFFFAOYSA-N octadecanoic acid Natural products CCCCCCCC(C)CCCCCCCCC(O)=O OQCDKBAXFALNLD-UHFFFAOYSA-N 0.000 claims description 14
- 239000008117 stearic acid Substances 0.000 claims description 14
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical group [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 claims description 12
- 239000007787 solid Substances 0.000 claims description 11
- 239000011734 sodium Substances 0.000 claims description 10
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 7
- 239000003245 coal Substances 0.000 claims description 7
- 229910052760 oxygen Inorganic materials 0.000 claims description 7
- 239000001301 oxygen Substances 0.000 claims description 7
- RHZUVFJBSILHOK-UHFFFAOYSA-N anthracen-1-ylmethanolate Chemical group C1=CC=C2C=C3C(C[O-])=CC=CC3=CC2=C1 RHZUVFJBSILHOK-UHFFFAOYSA-N 0.000 claims description 6
- 239000003830 anthracite Substances 0.000 claims description 6
- 229910000029 sodium carbonate Inorganic materials 0.000 claims description 6
- 235000011121 sodium hydroxide Nutrition 0.000 claims description 6
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 4
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 claims description 4
- 229910052799 carbon Inorganic materials 0.000 claims description 4
- 239000004927 clay Substances 0.000 claims description 4
- 229910052938 sodium sulfate Inorganic materials 0.000 claims description 4
- 235000011152 sodium sulphate Nutrition 0.000 claims description 4
- 230000000996 additive effect Effects 0.000 claims description 3
- 238000004090 dissolution Methods 0.000 claims description 3
- 238000010521 absorption reaction Methods 0.000 claims description 2
- 238000010304 firing Methods 0.000 claims description 2
- 238000010438 heat treatment Methods 0.000 claims description 2
- 235000017550 sodium carbonate Nutrition 0.000 claims description 2
- 238000003756 stirring Methods 0.000 claims description 2
- 244000003416 Asparagus officinalis Species 0.000 claims 2
- 239000003795 chemical substances by application Substances 0.000 claims 1
- 230000000694 effects Effects 0.000 abstract description 8
- 239000002699 waste material Substances 0.000 abstract description 4
- 239000002893 slag Substances 0.000 abstract description 3
- 150000003568 thioethers Chemical class 0.000 abstract description 2
- VBICKXHEKHSIBG-UHFFFAOYSA-N 1-monostearoylglycerol Chemical compound CCCCCCCCCCCCCCCCCC(=O)OCC(O)CO VBICKXHEKHSIBG-UHFFFAOYSA-N 0.000 abstract 1
- 235000002918 Fraxinus excelsior Nutrition 0.000 abstract 1
- DCXXMTOCNZCJGO-UHFFFAOYSA-N Glycerol trioctadecanoate Natural products CCCCCCCCCCCCCCCCCC(=O)OCC(OC(=O)CCCCCCCCCCCCCCCCC)COC(=O)CCCCCCCCCCCCCCCCC DCXXMTOCNZCJGO-UHFFFAOYSA-N 0.000 abstract 1
- 239000002956 ash Substances 0.000 abstract 1
- 239000000203 mixture Substances 0.000 description 13
- 241000234427 Asparagus Species 0.000 description 12
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 description 11
- GNTDGMZSJNCJKK-UHFFFAOYSA-N divanadium pentaoxide Chemical compound O=[V](=O)O[V](=O)=O GNTDGMZSJNCJKK-UHFFFAOYSA-N 0.000 description 10
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 8
- ANBBXQWFNXMHLD-UHFFFAOYSA-N aluminum;sodium;oxygen(2-) Chemical compound [O-2].[O-2].[Na+].[Al+3] ANBBXQWFNXMHLD-UHFFFAOYSA-N 0.000 description 7
- 229910001388 sodium aluminate Inorganic materials 0.000 description 7
- 239000002994 raw material Substances 0.000 description 6
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 5
- 238000006555 catalytic reaction Methods 0.000 description 5
- 239000003546 flue gas Substances 0.000 description 5
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 4
- 229910004298 SiO 2 Inorganic materials 0.000 description 4
- 229910018072 Al 2 O 3 Inorganic materials 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 2
- 229910052782 aluminium Inorganic materials 0.000 description 2
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 2
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 2
- 239000004566 building material Substances 0.000 description 2
- OSGAYBCDTDRGGQ-UHFFFAOYSA-L calcium sulfate Chemical group [Ca+2].[O-]S([O-])(=O)=O OSGAYBCDTDRGGQ-UHFFFAOYSA-L 0.000 description 2
- 238000005202 decontamination Methods 0.000 description 2
- 230000003588 decontaminative effect Effects 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 229910052976 metal sulfide Inorganic materials 0.000 description 2
- 239000002367 phosphate rock Substances 0.000 description 2
- KEAYESYHFKHZAL-UHFFFAOYSA-N Sodium Chemical compound [Na] KEAYESYHFKHZAL-UHFFFAOYSA-N 0.000 description 1
- 239000005864 Sulphur Substances 0.000 description 1
- AZDRQVAHHNSJOQ-UHFFFAOYSA-N alumane Chemical class [AlH3] AZDRQVAHHNSJOQ-UHFFFAOYSA-N 0.000 description 1
- 150000004645 aluminates Chemical class 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- WUKWITHWXAAZEY-UHFFFAOYSA-L calcium difluoride Chemical compound [F-].[F-].[Ca+2] WUKWITHWXAAZEY-UHFFFAOYSA-L 0.000 description 1
- 229910001634 calcium fluoride Inorganic materials 0.000 description 1
- JHLNERQLKQQLRZ-UHFFFAOYSA-N calcium silicate Chemical compound [Ca+2].[Ca+2].[O-][Si]([O-])([O-])[O-] JHLNERQLKQQLRZ-UHFFFAOYSA-N 0.000 description 1
- 229910052918 calcium silicate Inorganic materials 0.000 description 1
- 235000012241 calcium silicate Nutrition 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000001186 cumulative effect Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 238000002386 leaching Methods 0.000 description 1
- 238000005272 metallurgy Methods 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 238000010248 power generation Methods 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 150000004760 silicates Chemical class 0.000 description 1
- 239000002910 solid waste Substances 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 238000010301 surface-oxidation reaction Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09G—POLISHING COMPOSITIONS; SKI WAXES
- C09G1/00—Polishing compositions
- C09G1/02—Polishing compositions containing abrasives or grinding agents
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B17/00—Sulfur; Compounds thereof
- C01B17/69—Sulfur trioxide; Sulfuric acid
- C01B17/74—Preparation
- C01B17/76—Preparation by contact processes
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23F—NON-MECHANICAL REMOVAL OF METALLIC MATERIAL FROM SURFACE; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL; MULTI-STEP PROCESSES FOR SURFACE TREATMENT OF METALLIC MATERIAL INVOLVING AT LEAST ONE PROCESS PROVIDED FOR IN CLASS C23 AND AT LEAST ONE PROCESS COVERED BY SUBCLASS C21D OR C22F OR CLASS C25
- C23F3/00—Brightening metals by chemical means
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Inorganic Chemistry (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Abstract
本发明提供了一种制备金属抛光膏联产酸的工艺,包括如下步骤:将磷石膏、粉煤灰、添加剂和改性剂混合研磨制成生料,送入窑内焙烧得熟料;将熟料进行溶出,并进行固液分离;分离得到的溶液制备氧化铝;将制得的氧化铝与石灰、白泥、长石粉、氧化铬研磨混合得混合物料a,将混合物料a与硬脂酸、石蜡、棕榈蜡、乙醇、油酸、橄榄油、大豆磷脂、硬什油和聚乙二醇研磨混合,加热搅拌,冷却得金属抛光膏;将分离得到的残渣经浮选得硫化物;硫化物加工制得硫酸。本发明具有制备金属抛光膏和制酸成本低,废渣利用率高,采用氧化铝粉制备的金属抛光膏具有抛光效果好,完全去除表面污物、抛光的寿命长的优点,且制酸工艺简单。The invention provides a process for preparing metal polishing paste for co-production of acid, comprising the following steps: mixing and grinding phosphogypsum, fly ash, additives and modifiers to make raw meal, sending it into a kiln for roasting to obtain clinker; The clinker is dissolved, and solid-liquid separation is carried out; the separated solution is prepared into alumina; the prepared alumina is ground and mixed with lime, white mud, feldspar powder, and chromium oxide to obtain a mixed material a, and the mixed material a is mixed with stearin Acid, paraffin wax, palm wax, ethanol, oleic acid, olive oil, soybean lecithin, hard ashes oil and polyethylene glycol are ground and mixed, heated and stirred, and cooled to obtain a metal polishing paste; the separated residue is subjected to flotation to obtain sulfide; Sulfides are processed to produce sulfuric acid. The invention has the advantages of low cost for preparing metal polishing paste and acid production, high waste slag utilization rate, good polishing effect, complete removal of surface dirt and long polishing life, and simple acid production process. .
Description
技术领域technical field
本发明涉及一种制备金属抛光膏联产酸的工艺,属于冶金化工领域。The invention relates to a process for preparing metal polishing paste for co-production of acid, which belongs to the field of metallurgy and chemical industry.
背景技术Background technique
金属材料表面抛光助剂的研究得到了突飞猛进的发展。随着产品的不断更新,对这类金属材料表面抛光助剂的要求也越来越高,不仅具有金属表面去污、抛光、人工擦亮、去划痕、材料防腐作用,同时要求其安全无污染。现有的一种金属抛光膏具有处理后的表面氧化快效果好、抛光效果好、能实现去污,擦亮,护理等,同时工作效率高,但是在该金属抛光膏的生产中,由于金属抛光膏的加工原料中含有氧化铝,而现有氧化铝粉的制作工艺复杂、生产成本高,导致氧化铝粉价格贵,大大的增加了金属抛光膏的生产成本。The research on metal surface polishing aids has been developed by leaps and bounds. With the continuous update of products, the requirements for such metal surface polishing aids are getting higher and higher. It not only has the functions of metal surface decontamination, polishing, manual polishing, scratch removal, and material anticorrosion, but also requires it to be safe and non-toxic. Pollution. Existing a kind of metal polishing paste has the fast surface oxidation effect after treatment, good polishing effect, can realize decontamination, polish, care etc., work efficiency is high simultaneously, but in the production of this metal polishing paste, due to metal The processing raw material of the polishing paste contains alumina, but the production process of the existing alumina powder is complex and the production cost is high, resulting in high price of the alumina powder, which greatly increases the production cost of the metal polishing paste.
磷石膏是指在磷酸生产中用硫酸处理磷矿时产生的固体废渣,其主要成分为硫酸钙(CaSO4),其含量一般可达到70-90%左右。此外,磷石膏还含有多种杂质:未分解的磷矿,未洗涤干净的磷酸、氟化钙、铁、铝化合物、酸不溶物、有机质等。我国每年排放磷石膏约2000万吨,累计排量近亿吨。磷石膏在建材方面的利用率不到5%,大量磷石膏渣场占用土地,严重污染环境。Phosphogypsum refers to the solid waste generated when sulfuric acid is used to treat phosphate rock in the production of phosphoric acid. Its main component is calcium sulfate (CaSO 4 ), and its content can generally reach about 70-90%. In addition, phosphogypsum also contains a variety of impurities: undecomposed phosphate rock, unwashed phosphoric acid, calcium fluoride, iron, aluminum compounds, acid insoluble matter, organic matter, etc. my country emits about 20 million tons of phosphogypsum every year, with a cumulative discharge of nearly 100 million tons. The utilization rate of phosphogypsum in building materials is less than 5%, and a large number of phosphogypsum slag fields occupy land and seriously pollute the environment.
我国是个产煤大国,以煤炭为电力生产基本燃料。我国的能源工业稳步发展,发电能力年增长率为7.3%,电力工业的迅速发展,带来了粉煤灰排放量的急剧增加,燃煤热电厂每年所排放的粉煤灰总量逐年增加,1995年粉煤灰排放量达1.25亿吨,2000年约为1.5亿吨,到2010年将达到3亿吨,给我国的国民经济建设及生态环境造成巨大的压力。my country is a large coal-producing country, and coal is used as the basic fuel for electric power production. my country's energy industry has developed steadily, with an annual growth rate of 7.3% in power generation capacity. The rapid development of the power industry has brought about a sharp increase in the amount of fly ash discharged. The total amount of fly ash emitted by coal-fired thermal power plants has increased year by year. In 1995 The annual fly ash discharge amounted to 125 million tons, about 150 million tons in 2000, and will reach 300 million tons by 2010, which has caused enormous pressure on my country's national economic construction and ecological environment.
现目前,针对磷石膏和粉煤灰的综合利用的技术很少,基本上集中在建材和铺路等传统领域,这造成了磷石膏和粉煤灰中大量高价值成分的浪费,附加值非常低。而将磷石膏和粉煤灰综合利用来制金属抛光膏,同时联产酸的工艺,未见报道。At present, there are few technologies for the comprehensive utilization of phosphogypsum and fly ash, and they are basically concentrated in traditional fields such as building materials and paving, which results in the waste of a large number of high-value components in phosphogypsum and fly ash, and the added value is very low . However, the comprehensive utilization of phosphogypsum and fly ash to make metal polishing paste and the simultaneous production of acid have not been reported.
发明目的purpose of invention
本发明的目的在于,提供一种制备金属抛光膏联产酸的工艺。本发明具有制备金属抛光膏和制酸成本低,废渣利用率高,采用氧化铝粉制备的金属抛光膏具有抛光效果好,完全去除表面污物、抛光的寿命长的优点,且制酸工艺简单。The object of the present invention is to provide a process for preparing metal polishing paste with co-production of acid. The invention has the advantages of low cost for preparing metal polishing paste and acid production, high waste slag utilization rate, good polishing effect, complete removal of surface dirt and long polishing life, and simple acid production process. .
本发明的技术方案Technical scheme of the present invention
一种制备金属抛光膏联产酸的工艺,包括如下步骤:A kind of technique for preparing metal polishing paste co-production acid, comprises the steps:
A、将磷石膏、粉煤灰、添加剂和改性剂混合并研磨制成生料,送入窑内焙烧,制得熟料;A. Mix and grind phosphogypsum, fly ash, additives and modifiers to make raw meal, send it to the kiln for roasting, and make clinker;
B、将步骤A制得的熟料进行溶出,并进行固液分离;B, dissolving the clinker prepared in step A, and carrying out solid-liquid separation;
C、向步骤B分离得到的溶液中加入CO2至白色沉淀不再产生,然后将白色沉淀滤出后清洗烘干并灼烧,粉碎得氧化铝粉;C. Add CO to the solution separated in step B until the white precipitate is no longer produced, then filter the white precipitate, wash, dry and burn, and pulverize to obtain alumina powder;
D、将步骤C制得的氧化铝粉与石灰、白泥、长石粉、氧化铬研磨混合得混合物料a,将混合物料a与硬脂酸、石蜡、棕榈蜡、乙醇、油酸、橄榄油、大豆磷脂、硬什油和聚乙二醇研磨混合,加热搅拌,冷却得金属抛光膏;D. Grinding and mixing the alumina powder prepared in step C with lime, white mud, feldspar powder, and chromium oxide to obtain a mixed material a, and mixing the mixed material a with stearic acid, paraffin wax, palm wax, ethanol, oleic acid, olive oil , soybean lecithin, hard asparagus oil and polyethylene glycol are ground and mixed, heated and stirred, and cooled to obtain a metal polishing paste;
E、将步骤B分离得到的残渣经浮选,分离得硫化物;E, the residue obtained by step B separation is separated to obtain sulfide through flotation;
F、将步骤E分离出的硫化物置于30-50%的富氧环境下,在800-1200℃下焙烧3-5h,焙烧产生的烟气经五氧化二钒催化反应后,采用浓硫酸进行吸收,制得硫酸。F. Place the sulfide separated in step E in a 30-50% oxygen-enriched environment, and roast it at 800-1200°C for 3-5h. Absorption, producing sulfuric acid.
前述的制备金属抛光膏联产酸的工艺中,步骤A中,所述添加剂为碳酸钠、硫酸钠或烧碱;所述改性剂为无烟煤、碳或煤矸石。In the aforementioned process for preparing metal polishing paste for co-production of acid, in step A, the additive is sodium carbonate, sodium sulfate or caustic soda; the modifier is anthracite, carbon or gangue.
前述的制备金属抛光膏联产酸的工艺中,步骤A中,所述的生料中,磷石膏和粉煤灰按照1:0.6-2重量比的比例混合,添加剂添加比例按生料中所含Na2O和A12O3+Fe2O3总和的分子比为1:1添加,改性剂的混合比例为生料总重量的10-25%。In the aforementioned process for preparing metal polishing paste for co-production of acid, in step A, in the raw meal, phosphogypsum and fly ash are mixed according to the ratio of 1:0.6-2 by weight, and the additive addition ratio is as stated in the raw meal. The molecular ratio of the sum of Na 2 O and A1 2 O 3 +Fe 2 O 3 is 1:1, and the mixing ratio of the modifier is 10-25% of the total weight of the raw meal.
前述的制备金属抛光膏联产酸的工艺中,步骤A中,所述窑为工业回转窑、工业隧道窑或工业立窑。In the aforementioned process for preparing metal polishing paste for co-production of acid, in step A, the kiln is an industrial rotary kiln, an industrial tunnel kiln or an industrial shaft kiln.
前述的制备金属抛光膏联产酸的工艺中,步骤A中,是在温度1000-1350℃下焙烧时间1-2h。In the aforementioned process for preparing metal polishing paste for co-production of acid, in step A, the firing time is 1-2 hours at a temperature of 1000-1350°C.
前述的制备金属抛光膏联产酸的工艺中,步骤B中,所述熟料先水磨后溶出;溶出时的液固体积比为3-6:1。In the aforementioned process of preparing metal polishing paste for co-production of acid, in step B, the clinker is milled with water and then dissolved; the liquid-solid volume ratio during dissolution is 3-6:1.
前述的制备金属抛光膏联产酸的工艺中,所述溶出时的液固体积比为4-6:1。In the aforementioned process of preparing metal polishing paste for co-production of acid, the liquid-solid volume ratio during dissolution is 4-6:1.
前述的制备金属抛光膏联产酸的工艺中,步骤C中,所述灼烧是在温度900-1200℃下灼烧时间3-5h。In the aforementioned process of preparing metal polishing paste for co-production of acid, in step C, the burning is at a temperature of 900-1200° C. for 3-5 hours.
前述的制备金属抛光膏联产酸的工艺中,步骤D中,按重量份计,所述金属抛光膏包含氧化铝粉5-10份、硬脂酸15-20份、石蜡4-5份、棕榈蜡2-3份、石灰35-40份、乙醇15-20份、油酸3-5份、氧化铬2-3份、白泥6-8份、长石粉3-4份、橄榄油4-6份、大豆磷脂2-3份、硬什油2-4份和聚乙二醇7-9份。In the aforementioned process for preparing metal polishing paste for co-production of acid, in step D, by weight, the metal polishing paste comprises 5-10 parts of alumina powder, 15-20 parts of stearic acid, 4-5 parts of paraffin, 2-3 parts of palm wax, 35-40 parts of lime, 15-20 parts of ethanol, 3-5 parts of oleic acid, 2-3 parts of chromium oxide, 6-8 parts of white mud, 3-4 parts of feldspar powder, 4 parts of olive oil -6 parts, 2-3 parts of soybean lecithin, 2-4 parts of hard asparagus oil and 7-9 parts of polyethylene glycol.
前述的制备金属抛光膏联产酸的工艺中,步骤D中,所述加热搅拌是在温度为70-80℃下搅拌30-40min。In the aforementioned process of preparing metal polishing paste for co-production of acid, in step D, the heating and stirring is carried out at a temperature of 70-80° C. for 30-40 minutes.
本发明通过将磷石膏和粉煤灰反应、重组,使之成为有用物质。原理的总反应式为:The invention makes the phosphogypsum and fly ash react and reorganize into useful substances. The overall reaction formula of the principle is:
CaSO4(磷石膏)+ Na2O·SiO2·Al2O3(粉煤灰)→ Na2O·Al2O3 + CaO·SiO2↓ + [硫]CaSO 4 (phosphogypsum) + Na 2 O·SiO 2 ·Al 2 O 3 (fly ash) → Na 2 O·Al 2 O 3 + CaO·SiO 2 ↓ + [sulfur]
从该反应式可知,用磷石膏中的CaO与粉煤灰中的SiO2生成原硅酸钙( CaO·SiO2↓)后,得到可溶性极好的铝酸钠(Na2O·Al2O3)。反应式中的[硫],是指通过生料加添加剂和改性剂工艺,生成的金属硫化物;浸出熟料中的铝酸钠后,将得到的沉淀物浮选即可得到金属硫化物。It can be seen from the reaction formula that after CaO in phosphogypsum and SiO 2 in fly ash are used to generate calcium orthosilicate (CaO·SiO 2 ↓), sodium aluminate (Na 2 O·Al 2 O 3 ). [Sulphur] in the reaction formula refers to the metal sulfide generated by adding additives and modifiers to the raw meal; after leaching the sodium aluminate in the clinker, the obtained precipitate can be flotation to obtain the metal sulfide .
有益效果Beneficial effect
1、本发明通过利用磷石膏和粉煤灰作为原料,并加入添加剂和改性剂之后,在高温焙烧的工艺下得到主要含硅酸盐、铝酸盐和硫化物的熟料,而该铝酸盐的主要成分为铝酸钠,将铝酸钠水溶出后即可进行回收,而固体残渣浮选之后,得到硫化物,采用硫化物制备硫酸,1. The present invention uses phosphogypsum and fly ash as raw materials, and after adding additives and modifiers, obtains clinker mainly containing silicates, aluminates and sulfides under the high-temperature roasting process, and the aluminum The main component of acid salt is sodium aluminate, which can be recovered after dissolving sodium aluminate in water, and after flotation of solid residue, sulfide is obtained, and sulfuric acid is prepared by using sulfide.
通过回收的铝酸钠制备氧化铝,将氧化铝与其它原料制备金属抛光膏,由于整个工艺中主要以磷石膏和粉煤灰为原料,添加少量其他物质即可,因此,大大降低了制酸和金属抛光膏的成本投入。还大大增加了磷石膏和粉煤灰废渣的利用率,为缓解磷石膏和粉煤灰对环境的污染具有重要的贡献。Alumina is prepared from recovered sodium aluminate, and metal polishing paste is prepared from alumina and other raw materials. Since phosphogypsum and fly ash are mainly used as raw materials in the whole process, a small amount of other substances can be added. Therefore, the acid production is greatly reduced. And the cost input of metal polishing paste. It also greatly increases the utilization rate of phosphogypsum and fly ash waste residue, and makes an important contribution to alleviating the pollution of phosphogypsum and fly ash to the environment.
2、本发明通过的原料通过焙烧后,得到的成分分明,铝主要以铝酸钠形式存在,利用铝酸钠极易溶于水的特性,可简单快速的将其分离并用于制备氧化铝,将氧化铝与其它原料制备金属抛光膏,金属抛光膏具有抛光效果好,完全去除表面污物、抛光的寿命长的优点,且金属抛光膏成本低。2. After the raw materials passed in the present invention are roasted, the obtained components are distinct, and aluminum mainly exists in the form of sodium aluminate. Utilizing the characteristics that sodium aluminate is very soluble in water, it can be easily and quickly separated and used for the preparation of alumina. Aluminum oxide and other raw materials are used to prepare a metal polishing paste. The metal polishing paste has the advantages of good polishing effect, complete removal of surface dirt, long polishing life, and low cost of the metal polishing paste.
3、本发明将工艺中的固体残渣浮选之后,得到硫化物,采用硫化物制备硫酸,制酸的成本低,制酸工艺简单。3. The present invention obtains sulfide after flotation of the solid residue in the process, and uses the sulfide to prepare sulfuric acid. The cost of acid production is low and the acid production process is simple.
为进一步证明本发明的效果,发明人做了如下实验。In order to further prove the effect of the present invention, the inventors did the following experiments.
1、金属抛光膏的实验1. Experiment of metal polishing paste
发明人分别将以下五组实施例中的金属抛光膏对五块相同的金属表面进行抛光,当金属表面光泽明亮时,记录下抛光时间,并将抛光后金属自然放置20天,肉眼观察其抛光面,实验的结果如下:The inventor polished five identical metal surfaces with the metal polishing paste in the following five groups of examples, and recorded the polishing time when the metal surface was bright, and left the polished metal naturally for 20 days, and observed the polishing with naked eyes. On the other hand, the experimental results are as follows:
通过表1本发明金属抛光膏实验结果分析得到,本发明金属抛光膏抛光快、效果好、20天内不用进行二次抛光,所以本发明金属抛光膏具有抛光效果好,完全去除表面污物、抛光的寿命长的优点。Obtained by the analysis of the experimental results of the metal polishing paste of the present invention in Table 1, the metal polishing paste of the present invention has fast polishing, good effect, and does not need to carry out secondary polishing within 20 days, so the metal polishing paste of the present invention has a good polishing effect, completely removes surface dirt, and polishes The advantages of long life.
具体实施方式Detailed ways
下面结合实施例对本发明作进一步的说明,但并不作为对本发明限制的依据。The present invention will be further described below in conjunction with the examples, but not as a basis for limiting the present invention.
本发明的实施例Embodiments of the invention
实施例1:一种制备金属抛光膏联产酸的工艺,步骤如下:Embodiment 1: a kind of technique of preparing metal polishing paste co-production acid, the steps are as follows:
A、将磷石膏、粉煤灰、碳酸钠和无烟煤混合并研磨制成生料,送入工业回转窑内在温度1000℃下焙烧时间1.5h,制得熟料;其中,磷石膏和粉煤灰按照1:0.6重量比的比例混合,碳酸钠添加比例按生料中所含Na2O和A12O3+Fe2O3总和的分子比为1:1添加,无烟煤的混合比例为生料总重量的10%;A. Mix and grind phosphogypsum, fly ash, sodium carbonate and anthracite to make raw meal, send it to an industrial rotary kiln and roast it for 1.5 hours at a temperature of 1000°C to obtain clinker; among them, phosphogypsum and fly ash Mix according to the weight ratio of 1:0.6, add sodium carbonate according to the molecular ratio of the sum of Na 2 O and A1 2 O 3 +Fe 2 O 3 contained in the raw meal as 1:1, and add anthracite in the ratio of raw meal 10% of the total weight;
B、将步骤A制得的熟料以液固体积比为4:1进行水磨溶出,并进行固液分离;B, the clinker that step A is made is that 4:1 carries out water grinding stripping with liquid-solid volume ratio, and carries out solid-liquid separation;
C、将步骤B分离得到的残渣经浮选,分离得硫化物;C, the residue obtained by step B separation is separated to obtain sulfide through flotation;
D、将步骤C分离出的硫化物置于30%的富氧环境下,在800℃下焙烧5h,焙烧产生的烟气经五氧化二钒催化反应后,采用浓硫酸进行吸收,制得硫酸;D, place the sulfide isolated in step C under 30% oxygen-enriched environment, roast 5h at 800 DEG C, after the flue gas that roasting produces is through vanadium pentoxide catalytic reaction, adopt concentrated sulfuric acid to absorb, make sulfuric acid;
E、向步骤B分离得到的溶液中加入CO2至白色沉淀不再产生,然后将白色沉淀滤出后清洗烘干,在温度900℃下灼烧时间5h后粉碎得氧化铝粉;E. Add CO2 to the solution separated in step B until the white precipitate is no longer produced, then filter the white precipitate, wash and dry it, burn it at 900°C for 5 hours, and pulverize it to obtain alumina powder;
F、将步骤E制得的氧化铝粉与石灰、白泥、长石粉、氧化铬研磨混合得混合物料a,将混合物料a与硬脂酸、石蜡、棕榈蜡、乙醇、油酸、橄榄油、大豆磷脂、硬什油和聚乙二醇研磨混合,加热搅拌,加热搅拌是在温度为70℃下搅拌30min,冷却得金属抛光膏;其中按重量份计,所述金属抛光膏包含氧化铝粉5份、硬脂酸15份、石蜡4份、棕榈蜡2份、石灰35份、乙醇15份、油酸3份、氧化铬2份、白泥6份、长石粉3份、橄榄油4份、大豆磷脂2份、硬什油2份和聚乙二醇7份。F, grind and mix the aluminum oxide powder prepared in step E with lime, white mud, feldspar powder, and chromium oxide to obtain a mixed material a, mix the mixed material a with stearic acid, paraffin wax, palm wax, ethanol, oleic acid, olive oil , soybean lecithin, hard asparagus oil and polyethylene glycol are ground and mixed, heated and stirred, and the heated and stirred is stirred at a temperature of 70° C. for 30 minutes, and cooled to obtain a metal polishing paste; wherein the metal polishing paste contains aluminum oxide in parts by weight. 5 parts of powder, 15 parts of stearic acid, 4 parts of paraffin wax, 2 parts of palm wax, 35 parts of lime, 15 parts of ethanol, 3 parts of oleic acid, 2 parts of chromium oxide, 6 parts of white mud, 3 parts of feldspar powder, 4 parts of olive oil 2 parts, 2 parts of soybean lecithin, 2 parts of hard asparagus oil and 7 parts of polyethylene glycol.
实施例2:一种制备金属抛光膏联产酸的工艺,步骤如下:Embodiment 2: a kind of technique of preparing metal polishing paste co-production acid, the steps are as follows:
A、将磷石膏、粉煤灰、硫酸钠和碳混合并研磨制成生料,送入工业回转窑内在温度1200℃下焙烧时间2h,制得熟料;其中,磷石膏和粉煤灰按照1:1重量比的比例混合,烧碱添加比例按生料中所含Na2O和A12O3+Fe2O3总和的分子比为1:1.2添加,碳的混合比例为生料总重量的15%;A. Mix and grind phosphogypsum, fly ash, sodium sulfate and carbon to make raw meal, send it to an industrial rotary kiln and roast it for 2 hours at a temperature of 1200°C to obtain clinker; among them, phosphogypsum and fly ash are prepared according to 1:1 weight ratio, caustic soda is added according to the molecular ratio of the sum of Na 2 O and A1 2 O 3 +Fe 2 O 3 contained in the raw meal is 1:1.2, and the mixing ratio of carbon is the total weight of the raw meal 15% of
B、将步骤A制得的熟料以液固体积比为5:1进行水磨溶出,并进行固液分离;B, the clinker that step A is made is that 5:1 carries out water grinding stripping with liquid-solid volume ratio, and carries out solid-liquid separation;
C、将步骤B分离得到的残渣经浮选,分离得硫化物;C, the residue obtained by step B separation is separated to obtain sulfide through flotation;
D、将步骤C分离出的硫化物置于35%的富氧环境下,在900℃下焙烧4h,焙烧产生的烟气经五氧化二钒催化反应后,采用浓硫酸进行吸收,制得硫酸;D, place the sulfide isolated in step C under 35% oxygen-enriched environment, roast 4h at 900 DEG C, after the flue gas that roasting produces is through vanadium pentoxide catalytic reaction, adopt concentrated sulfuric acid to absorb, make sulfuric acid;
E、向步骤B分离得到的溶液中加入CO2至白色沉淀不再产生,然后将白色沉淀滤出后清洗烘干,在温度1000℃下灼烧时间4h后粉碎得氧化铝粉;E. Add CO2 to the solution separated in step B until the white precipitate no longer occurs, then filter out the white precipitate, wash and dry it, burn it at 1000°C for 4 hours, and then pulverize it to obtain alumina powder;
F、将步骤E制得的氧化铝粉与石灰、白泥、长石粉、氧化铬研磨混合得混合物料a,将混合物料a与硬脂酸、石蜡、棕榈蜡、乙醇、油酸、橄榄油、大豆磷脂、硬什油和聚乙二醇研磨混合,加热搅拌,加热搅拌是在温度为75℃下搅拌35min,冷却得金属抛光膏;其中按重量份计,所述金属抛光膏包含氧化铝粉7份、硬脂酸18份、石蜡4份、棕榈蜡3份、石灰36份、乙醇17份、油酸4份、氧化铬2份、白泥7份、长石粉3份、橄榄油5份、大豆磷脂3份、硬什油3份和聚乙二醇8份。F, grind and mix the aluminum oxide powder prepared in step E with lime, white mud, feldspar powder, and chromium oxide to obtain a mixed material a, mix the mixed material a with stearic acid, paraffin wax, palm wax, ethanol, oleic acid, olive oil , soybean lecithin, hard asparagus oil and polyethylene glycol are ground and mixed, heated and stirred, and the heated and stirred is stirred at a temperature of 75° C. for 35 minutes, and cooled to obtain a metal polishing paste; wherein the metal polishing paste contains aluminum oxide in parts by weight. 7 parts of powder, 18 parts of stearic acid, 4 parts of paraffin wax, 3 parts of palm wax, 36 parts of lime, 17 parts of ethanol, 4 parts of oleic acid, 2 parts of chromium oxide, 7 parts of white clay, 3 parts of feldspar powder, 5 parts of olive oil 3 parts, 3 parts of soybean lecithin, 3 parts of hard asparagus oil and 8 parts of polyethylene glycol.
实施例3:一种制备金属抛光膏联产酸的工艺,步骤如下:Embodiment 3: a kind of technique of preparing metal polishing paste co-production acid, the steps are as follows:
A、将磷石膏、粉煤灰、烧碱和煤矸石混合并研磨制成生料,送入工业回转窑内在温度1300℃下焙烧时间1.5h,制得熟料;其中,磷石膏和粉煤灰按照1:1.4重量比的比例混合,碳酸钠添加比例按生料中所含Na2O和A12O3+Fe2O3总和的分子比为1:1添加,煤矸石的混合比例为生料总重量的20%;A. Mix and grind phosphogypsum, fly ash, caustic soda and coal gangue to make raw meal, send it to an industrial rotary kiln and roast it at a temperature of 1300°C for 1.5 hours to obtain clinker; among them, phosphogypsum and fly ash Mix according to the weight ratio of 1:1.4, add sodium carbonate according to the molecular ratio of the sum of Na 2 O and A1 2 O 3 +Fe 2 O 3 contained in the raw meal as 1:1, and the mixing ratio of coal gangue is raw 20% of the total weight of the material;
B、将步骤A制得的熟料以液固体积比为6:1进行水磨溶出,并进行固液分离;B, the clinker that step A is made is that 6:1 carries out water grinding stripping with liquid-solid volume ratio, and carries out solid-liquid separation;
C、将步骤B分离得到的残渣经浮选,分离得硫化物;C, the residue obtained by step B separation is separated to obtain sulfide through flotation;
D、将步骤C分离出的硫化物置于45%的富氧环境下,在1000℃下焙烧3h,焙烧产生的烟气经五氧化二钒催化反应后,采用浓硫酸进行吸收,制得硫酸;D, place the sulfide isolated in step C under 45% oxygen-enriched environment, roast 3h at 1000 DEG C, after the flue gas that roasting produces is through vanadium pentoxide catalytic reaction, adopt concentrated sulfuric acid to absorb, make sulfuric acid;
E、向步骤B分离得到的溶液中加入CO2至白色沉淀不再产生,然后将白色沉淀滤出后清洗烘干,在温度1100℃下灼烧时间3h后粉碎得氧化铝粉;E. Add CO2 to the solution separated in step B until the white precipitate is no longer produced, then filter the white precipitate, wash and dry it, burn it at 1100°C for 3 hours, and pulverize it to obtain alumina powder;
F、将步骤E制得的氧化铝粉与石灰、白泥、长石粉、氧化铬研磨混合得混合物料a,将混合物料a与硬脂酸、石蜡、棕榈蜡、乙醇、油酸、橄榄油、大豆磷脂、硬什油和聚乙二醇研磨混合,加热搅拌,加热搅拌是在温度为80℃下搅拌40min,冷却得金属抛光膏;其中按重量份计,所述金属抛光膏包含氧化铝粉8份、硬脂酸19份、石蜡5份、棕榈蜡2份、石灰37份、乙醇18份、油酸3份、氧化铬3份、白泥8份、长石粉4份、橄榄油4份、大豆磷脂2份、硬什油4份和聚乙二醇8份。F, grind and mix the aluminum oxide powder prepared in step E with lime, white mud, feldspar powder, and chromium oxide to obtain a mixed material a, mix the mixed material a with stearic acid, paraffin wax, palm wax, ethanol, oleic acid, olive oil , soybean lecithin, hard asparagus oil and polyethylene glycol are ground and mixed, heated and stirred, and the heated and stirred is stirred at a temperature of 80° C. for 40 minutes, and cooled to obtain a metal polishing paste; wherein by weight, the metal polishing paste contains aluminum oxide 8 parts of powder, 19 parts of stearic acid, 5 parts of paraffin wax, 2 parts of palm wax, 37 parts of lime, 18 parts of ethanol, 3 parts of oleic acid, 3 parts of chromium oxide, 8 parts of white clay, 4 parts of feldspar powder, 4 parts of olive oil 2 parts of soybean lecithin, 4 parts of hard asparagus oil and 8 parts of polyethylene glycol.
实施例4:一种制备金属抛光膏联产酸的工艺,步骤如下:Embodiment 4: a kind of technique of preparing metal polishing paste co-production acid, the steps are as follows:
A、将磷石膏、粉煤灰、碳酸钠和煤矸石混合并研磨制成生料,送入工业回转窑内在温度1350℃下焙烧时间1h,制得熟料;其中,磷石膏和粉煤灰按照1:1.7重量比的比例混合,烧碱添加比例按生料中所含Na2O和A12O3+Fe2O3总和的分子比为1:1添加,煤矸石的混合比例为生料总重量的25%;A. Mix and grind phosphogypsum, fly ash, sodium carbonate and coal gangue to make raw meal, send it to an industrial rotary kiln and roast it at a temperature of 1350°C for 1 hour to make clinker; among them, phosphogypsum and fly ash Mix according to the weight ratio of 1:1.7, caustic soda is added according to the molecular ratio of the sum of Na 2 O and A1 2 O 3 +Fe 2 O 3 contained in the raw meal is 1:1, and the mixing ratio of coal gangue is raw meal 25% of the total weight;
B、将步骤A制得的熟料以液固体积比为5:1进行水磨溶出,并进行固液分离;B, the clinker that step A is made is that 5:1 carries out water grinding stripping with liquid-solid volume ratio, and carries out solid-liquid separation;
C、将步骤B分离得到的残渣经浮选,分离得硫化物;C, the residue obtained by step B separation is separated to obtain sulfide through flotation;
D、将步骤C分离出的硫化物置于45%的富氧环境下,在1200℃下焙烧3h,焙烧产生的烟气经五氧化二钒催化反应后,采用浓硫酸进行吸收,制得硫酸;D, place the sulfide isolated in step C under 45% oxygen-enriched environment, roast 3h at 1200 DEG C, after the flue gas that roasting produces is through vanadium pentoxide catalytic reaction, adopt concentrated sulfuric acid to absorb, make sulfuric acid;
E、向步骤B分离得到的溶液中加入CO2至白色沉淀不再产生,然后将白色沉淀滤出后清洗烘干,在温度1200℃下灼烧时间3h后粉碎得氧化铝粉;E. Add CO2 to the solution separated in step B until the white precipitate is no longer produced, then filter the white precipitate, wash and dry it, burn it at 1200°C for 3 hours, and pulverize it to obtain alumina powder;
F、将步骤E制得的氧化铝粉与石灰、白泥、长石粉、氧化铬研磨混合得混合物料a,将混合物料a与硬脂酸、石蜡、棕榈蜡、乙醇、油酸、橄榄油、大豆磷脂、硬什油和聚乙二醇研磨混合,加热搅拌,加热搅拌是在温度为75℃下搅拌35min,冷却得金属抛光膏;其中按重量份计,所述金属抛光膏包含氧化铝粉9份、硬脂酸16份、石蜡4份、棕榈蜡3份、石灰38份、乙醇19份、油酸4份、氧化铬2份、白泥7份、长石粉3份、橄榄油5份、大豆磷脂3份、硬什油3份和聚乙二醇7份。F, grind and mix the aluminum oxide powder prepared in step E with lime, white mud, feldspar powder, and chromium oxide to obtain a mixed material a, mix the mixed material a with stearic acid, paraffin wax, palm wax, ethanol, oleic acid, olive oil , soybean lecithin, hard asparagus oil and polyethylene glycol are ground and mixed, heated and stirred, and the heated and stirred is stirred at a temperature of 75° C. for 35 minutes, and cooled to obtain a metal polishing paste; wherein the metal polishing paste contains aluminum oxide in parts by weight. 9 parts of powder, 16 parts of stearic acid, 4 parts of paraffin wax, 3 parts of palm wax, 38 parts of lime, 19 parts of ethanol, 4 parts of oleic acid, 2 parts of chromium oxide, 7 parts of white clay, 3 parts of feldspar powder, 5 parts of olive oil 3 parts, 3 parts of soybean lecithin, 3 parts of hard asparagus oil and 7 parts of polyethylene glycol.
实施例5:一种制备金属抛光膏联产酸的工艺,步骤如下:Embodiment 5: a kind of technique of preparing metal polishing paste co-production acid, the steps are as follows:
A、将磷石膏、粉煤灰、硫酸钠和无烟煤混合并研磨制成生料,送入工业回转窑内在温度1200℃下焙烧时间2h,制得熟料;其中,磷石膏和粉煤灰按照1:2重量比的比例混合,烧碱添加比例按生料中所含Na2O和A12O3+Fe2O3总和的分子比为1:1添加,无烟煤的混合比例为生料总重量的20%;A. Mix and grind phosphogypsum, fly ash, sodium sulfate and anthracite to make raw meal, send it to an industrial rotary kiln and roast it at a temperature of 1200°C for 2 hours to obtain clinker; among them, phosphogypsum and fly ash according to Mix in a ratio of 1:2 by weight, caustic soda is added according to the molecular ratio of the sum of Na 2 O and A1 2 O 3 +Fe 2 O 3 contained in the raw meal as 1:1, and the mixing ratio of anthracite is the total weight of the raw meal 20% of
B、将步骤A制得的熟料以液固体积比为4:1进行水磨溶出,并进行固液分离;B, the clinker that step A is made is that 4:1 carries out water grinding stripping with liquid-solid volume ratio, and carries out solid-liquid separation;
C、将步骤B分离得到的残渣经浮选,分离得硫化物;C, the residue obtained by step B separation is separated to obtain sulfide through flotation;
D、将步骤C分离出的硫化物置于50%的富氧环境下,在1100℃下焙烧4h,焙烧产生的烟气经五氧化二钒催化反应后,采用浓硫酸进行吸收,制得硫酸;D, place the sulfide isolated in step C under 50% oxygen-enriched environment, roast 4h at 1100 DEG C, after the flue gas that roasting produces is through vanadium pentoxide catalytic reaction, adopt concentrated sulfuric acid to absorb, make sulfuric acid;
E、向步骤B分离得到的溶液中加入CO2至白色沉淀不再产生,然后将白色沉淀滤出后清洗烘干,在温度1200℃下灼烧时间5h后粉碎得氧化铝粉;E. Add CO2 to the solution separated in step B until the white precipitate no longer occurs, then filter out the white precipitate, wash and dry it, burn it at 1200°C for 5 hours, and pulverize it to obtain alumina powder;
F、将步骤E制得的氧化铝粉与石灰、白泥、长石粉、氧化铬研磨混合得混合物料a,将混合物料a与硬脂酸、石蜡、棕榈蜡、乙醇、油酸、橄榄油、大豆磷脂、硬什油和聚乙二醇研磨混合,加热搅拌,加热搅拌是在温度为80℃下搅拌40min,冷却得金属抛光膏;其中按重量份计,所述金属抛光膏包含氧化铝粉10份、硬脂酸20份、石蜡5份、棕榈蜡3份、石灰40份、乙醇20份、油酸5份、氧化铬3份、白泥8份、长石粉4份、橄榄油6份、大豆磷脂3份、硬什油4份和聚乙二醇9份。F, grind and mix the aluminum oxide powder prepared in step E with lime, white mud, feldspar powder, and chromium oxide to obtain a mixed material a, mix the mixed material a with stearic acid, paraffin wax, palm wax, ethanol, oleic acid, olive oil , soybean lecithin, hard asparagus oil and polyethylene glycol are ground and mixed, heated and stirred, and the heated and stirred is stirred at a temperature of 80° C. for 40 minutes, and cooled to obtain a metal polishing paste; wherein by weight, the metal polishing paste contains aluminum oxide 10 parts of powder, 20 parts of stearic acid, 5 parts of paraffin wax, 3 parts of palm wax, 40 parts of lime, 20 parts of ethanol, 5 parts of oleic acid, 3 parts of chromium oxide, 8 parts of white mud, 4 parts of feldspar powder, 6 parts of olive oil 3 parts of soybean lecithin, 4 parts of hard asparagus oil and 9 parts of polyethylene glycol.
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CN111647358A (en) * | 2020-07-09 | 2020-09-11 | 江苏安全技术职业学院 | Manufacturing process of polishing paste for mechanical polishing |
CN113234420A (en) * | 2021-06-22 | 2021-08-10 | 金顺浩研磨材料(南通)有限公司 | Polishing and grinding material and preparation method thereof |
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